AN INTRODUCTION TO
CUT-OFF GRADE
ESTIMATION
SECOND EDITION
BY JEAN-MICHEL RENDU
BLENDING CONSTRAINTS WASTE BLOCK CAVING STOCKPILES
CLOSURE GRADE-TONNAGE PRICES MINE CUT-OFF LEACHING
UNDERGROUND NPV SOCIOECONOMIC METAL EQUIVALENT
OPEN PIT OPPORTUNITY POLYMETALLIC PROCESS PROFIT
RECLAMATION SELECTIVITY STOPES UTILITY NSR VARIABLE
RECOVERY NPV MILL CUT-OFF LEACHING BREAKEVEN STOCK
STOCKPILES CLOSURE POLYMETALLIC UNDERGROUND NPV
SOCIO-ECONOMIC METAL EQUIVALENT OPEN PIT OPPORTUNITY
POLYMETALLIC PROCESS PROFIT BLENDING CONSTRAINTS
WASTE BLOCK CAVING STOCKPILES CLOSURE GRADE-TONNAGE
PRICES MINE CUT-OFF LEACHING UNDERGROUND NPV SOCIO-
Published by the
Society for Mining,
Metallurgy & Exploration
GRADE
ESTIMATION
SECOND EDITION
AN INTRODUCTION TO
CUT-OFF
BY JEAN-MICHEL RENDU
!SME_COGrade2013_2ndED_TitlePg_L3.indd 1 11/21/13 2:15 PM
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ISBN: 978-0-87335-393-9
Ebook: 978-0-87335-394-6
Library of Congress Cataloging-in-Publication Data
Rendu, Jean-Michel, 1944- author.
An introduction to cut-off grade estimation / by Jean-Michel Rendu. -- Second edition.
pages cm
Includes bibliographical references and index.
ISBN 978-0-87335-393-9
1. Ores--Grading. 2. Ores--Sampling and estimation. I. Title.
TN560.R45 2014
622’.7--dc23
2013043932
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iii
Contents
PREFACE TO 2014 EDITION. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . vii
PREFACE TO 2008 EDITION. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . ix
Chapter 1 INTRODUCTION. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . . . 1
Chapter 2 GENERAL CONCEPTS. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . 5
Mathematical Formulation: Utility Function. . . . . . . . . . . . . . . 5
Cut-off Grade and Grade–Tonnage Relationship. . . . . . . . . . . 6
Direct Profit and Loss: Udir(x). . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . 8
Net Present Value: NPVi
. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . 10
Opportunity Costs and Benefits: Uopp(x). . . . . . . . . . . . . . . . . .å°“ 12
Other Costs and Benefits: Uoth(x). . . . . . . . . . . . . . . . . .å°“ . . . . . . 15
Cut-off Grade and Blending Strategy. . . . . . . . . . . . . . . . . .å°“ . . . 16
Chapter 3 BREAKEVEN CUT-OFF GRADE. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . 17
Cut-off Grade Between Ore and Waste. . . . . . . . . . . . . . . . . .å°“ . 17
Cut-off Grades in Open Pit Mines. . . . . . . . . . . . . . . . . .å°“ . . . . . . 20
Cut-off Grades in Underground Mines. . . . . . . . . . . . . . . . . .å°“ . 23
Cut-off Grade Between Two Processes. . . . . . . . . . . . . . . . . .å°“ . . 26
Cut-off Grade with Variable Recovery. . . . . . . . . . . . . . . . . .å°“ . . 28
Constant Tail Model of Variable Recovery. . . . . . . . . . . . . . . . 30
Breakeven Cut-off Grade and Polymetallic Deposits. . . . . . . 32
Opportunity Cost of Not Using the Optimum Cut-off
Grade. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . . . . . . 38
Cut-off Grade and Low-Grade Stockpiles. . . . . . . . . . . . . . . . . 40
Cut-off Grade and Optimization of Processing Plant
Operating Conditions. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . 44
Chapter 4 CAPACITY CONSTRAINTS AND OPPORTUNITY COSTS. . . 53
When Marginal Analysis No Longer Applies: A Gold
Leaching Operation. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . 53
Capacity Constraints and Increase in Cut-off Grade. . . . . . . 56
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iv Contents
Decreasing Cut-off Grade over Time: A Strategic
Objective. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . . . 61
Cut-off Grade Below Marginal Cut-off Grade. . . . . . . . . . . . . 63
Cut-off Grade Optimization with Opportunity Costs:
Practical Considerations. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . 66
Chapter 5 GEOLOGIC CONSTRAINTS AND OPPORTUNITY COSTS. . 69
Cut-off Grade When Processing Capacity Is Fixed. . . . . . . . . 69
Cut-off Grade When Mining Capacity Is Fixed. . . . . . . . . . . . 76
Cut-off Grade When Volume of Sales Is Fixed. . . . . . . . . . . . . 78
Releasing Capacity Constraints: A Base Metal Example. . . . 81
Chapter 6 CUT-OFF GRADE AND MINE PLANNING. . . . . . . . . . . . . . . . . .å°“ 87
Open Pit Mine: Economic Valuation of a Pushback. . . . . . . . 87
Underground Mine: Economic Valuation of a Stope. . . . . . . 89
Similarities Between Open Pit and Underground Mine
Planning. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . . . . 90
Block and Panel Caving. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . 91
Relationship Between Mine Selectivity, Deposit
Modeling, Ore Control, and Cut-off Grade. . . . . . . . . .98
Chapter 7 WHICH COSTS SHOULD BE INCLUDED IN CUT-OFF
GRADE CALCULATIONS?. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . 101
General Considerations. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . 101
How Specific Costs Influence Cut-off Grade
Calculations. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . 103
Other Costs and Benefits. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . 105
Chapter 8 BLENDING STRATEGY. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . 109
Blending Two Material Types. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . 110
Blending Three Material Types. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . 114
Blending to Maximize Tonnage. . . . . . . . . . . . . . . . . .å°“ . . . . . . . 118
Remarks Concerning an Increasingly Complex Blending
Problem. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . . . 120
Chapter 9 CLOSING REMARKS. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . 123
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Contents v
Appendix A Example 1. Net Present Value of Constant Cash Flow:
Proof of Formula. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . 127
Example 2. Net Present Value of Perpetuity Cash Flow:
Proof of Formula. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . 128
Example 3. Opportunity Cost of Mining a Peripheral
Deposit. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . . . 128
Example 4. Simplified Equation to Estimate Opportunity
Cost: Verification of First-Order Approximation. . . . 130
Example 5. Opportunity Cost of Not Using the Optimal
Cut-off Grade in a Copper Mine. . . . . . . . . . . . . . . . . .å°“ 131
Example 6. Stockpiling and Cut-off Determination in a
Copper Mine. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ 132
Example 7. Properties of Constant-Metric-Tons Curves
in Blending Diagrams. . . . . . . . . . . . . . . . . . . . . . . . . . . . .135
LIST OF SYMBOLS. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ 139
BIBLIOGRAPHY. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . 145
INDEX. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . 149
ABOUT THE AUTHOR. . . . . . . . . . . . . . . . . .å°“ . . . . . . . . . . . . . . . . 157
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
vi
DEDICATION
I am dedicating this book to my wife Karla and my two sons, Yannick and
Mikael. Life with a husband and father who spent too much time traveling to
remote mines all over the world, and then returned home to work long hours
in front of his computer, was not without challenges and disappointments. I am
grateful for their patience, understanding, and unquestioning love.
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vii
Preface to 2014 Edition
The first edition of An Introduction to Cut-off Grade Estimation was published
in 2008. Since then, many changes have occurred in the world economy.
Prices and costs have changed significantly. The commodity megatrend that
prevailed during the last decade changed management’s emphasis from cost
control to growth in production. But this trend reached its inevitable end in
2012, resulting in a return to a high priority being given to efficiency and cost
controls. The increasingly demanding political and socioeconomic environment has altered the way decisions are made.
Such changes should not alter the validity of a reference manual. However, the need to update An Introduction to Cut-off Grade Estimation became
apparent as a result of feedback received from those who read the first edition
and who attended cut-off grade courses I have given over the years. It became
apparent that the information was not always presented in a rational fashion.
Some fundamental concepts, such as those related to opportunity costs and
how those costs should be accounted for in decision making, needed clarification. The focus of the 2008 edition was on metal mining, and, over time,
many questions have been raised concerning application to industrial minerals, iron ore, and coal.
This new edition has attempted to take this feedback into account.
Chapters have been reorganized and their content clarified. The relationship
between optimization of net present value, capacity constraints, and opportunity cost is explained in greater detail. A new section has been added that
discusses blending strategies applicable to coal and iron ore mines, as well as in
an increasing number of metal mines. The objective was to make this new edition easier to read and of greater practical interest to practitioners operating
in a wider range of situations. In addition, the bibliography has been greatly
expanded. You, the readers, will decide whether the effort that went into this
new edition was justified.
Many individuals contributed to this edition. I am particularly grateful to
Professor Roussos Dimitrakopoulos of McGill University, Canada, who not
only reviewed and commented on early drafts of this book, but also gave me
the opportunity to give short courses on cut-off grade estimation at McGill
University and in Perth, Australia. The challenging questions raised by the
short-course attendees resulted in many of the changes made in this new
edition. I also thank Professor Joao Felipe Costa of Universidade Federal do
Rio Grande do Sul, Brazil, who also reviewed early drafts and helped correct
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
viii Preface to 2014 Edition
some of the errors I made. I also recognize Steven Hoerger and Fred Seymour
whom I have had the pleasure to work with for many years, and who contributed to the early development of ideas included in both the first and second
editions. I also thank the Society for Mining, Metallurgy & Exploration, who
accepted the manuscript, as well as Jane Olivier, manager of book publishing,
and Diane Serafin, senior editor, who made publication possible.
Bringing this book to successful publication required the effort of many
more individuals not listed here, but they know who they are and I am grateful to all of them. The responsibility for any errors, lapses, or absences of
clarity that may remain from the first edition or that I may have introduced in
the second edition is entirely mine.
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ix
Preface to 2008 Edition
This book started with a desire to understand how to answer an apparently
simple but actually complex question faced by all those responsible for the
development and operation of mines: How do we determine which cut-off
grade should be used to separate material that should be processed from that
which should be sent to the waste dump? The answer appears straightforward:
If it is profitable to process one metric ton of material, this ton should be
processed. But what is profitable? The cut-off grade has a direct bearing on the
tonnage of material mined, the tonnage and average grade of material processed, the size of the mining operation, and consequently capital costs, operating costs, environmental and socioeconomic impacts. Should we maximize
cash flow, net present value, the life of the mining operation, the return to
shareholders? How do we take into account economic, environmental, social,
political, ethical and moral values, objectives, and regulations?
Somewhat surprisingly, only one other book has been written exclusively
on the subject of cut-off grade estimation: The Economic Definition of Ore:
Cut-Off Grades in Theory and Practice by Ken Lane, published in 1988. Lane’s
book was and will remain the standard for mathematical formulation of
solutions to cut-off grade estimation when the objective is to maximize net
present value. Concepts first formulated by Lane were used as the foundation
of this book.
Considerable progress has been made in the last twenty years to improve
mine planning and optimize cut-off grades. Increasingly complex algorithms
have been developed, and better, easier to use computer programs have been
written to assist engineers and economists in analyzing mine plans, testing
the options, and improving production schedules. Computer programs have
become easier to use, but the assumptions made by those who write the programs are often lost to the end user. With this book I am hoping to bridge the
gap between theory and practice, the ivory tower and engineers in the field,
by describing the fundamental principles of cut-off grade estimation and providing concrete examples.
This book started as notes written during the last thirty years. Eventually these notes turned into an introductory short course. Each time I gave
the course, more and more questions were asked, concerning increasingly
complex situations, demanding more practical examples and challenging the
assumptions made. Each question resulted in corrections, additions, and more
chapters. I am extremely thankful to all those who helped me in this respect.
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x Preface to 2008 Edition
They include too many individuals over too many years to be listed here. They
know who they are and I would not have continued this work without their
probing and their interest in the subject. I am particularly grateful to Ernie
Bohnet who kept on motivating me when I doubted that I had a story to tell
or that there would be sufficient interest in continuing this effort to make it
worthwhile. It is because of Ernie that I completed this book. I also want to
thank the Society for Mining, Metallurgy & Exploration, and Jane Olivier,
who accepted the manuscript and brought it to publication in record time.
None of these people, of course, can be blamed for any errors or lapses that I
may have made and for which I am fully responsible.
My first book, An Introduction to Geostatistical Methods of Mineral Evaluation, was published in 1978 with the objective to clarify the already arcane
science of geostatistics. It is only fitting that An Introduction to Cut-Off Grade
Estimation be published, with similar objectives, in 2008, exactly thirty years
later.
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1
A cut-off grade is generally defined as the minimum amount of valuable product
or metal that one metric ton (i.e., 1,000 kg) of material must contain before this
material is sent to the processing plant. This definition is used to distinguish
material that should not be mined or should be wasted from that which should
be processed. In complex geological environments, impurities may have to be
considered to define the cut-off grade. Cut-off grades are also used to decide
the routing of mined material when two or more processes are available, such as
heap leaching and milling. Cut-off grades are used to decide whether material
should be stockpiled for future processing or processed immediately.
The need to separate material being mined according to its physical and
chemical properties before it is processed was well understood by historical
miners. In the year 1556, Georgius Agricola reminded the readers of De Re
Metallica that
Experienced miners, when they dig ore, sort the metalliferous material
from earth, stones, and solidified juices before it is taken from the shafts
and tunnels, and they put the valuable metal in trays and the waste into
buckets.… To smelt waste together with an ore involves a loss, for some
expenditure is thrown away, seeing that out of earth and stones only
empty and useless slags are melted out, and further, the solidified juices
also impede the smelting of the metals and cause loss.
Agricola thus pointed out that, for economic reasons, both chemical and
physical properties of material being mined must be taken into account,
including impurities and deleterious elements (solidified juices) before this
material is processed.
Cut-off grades are calculated by comparing costs and benefits. In simple geological and metallurgical environments, a single number, such as a
minimum metal content, is sufficient to define the cut-off grade. In more
complex situations, the quality of the material being processed, including the
Introduction
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2 CHAPTER ONE
amount of deleterious elements, must be taken into account. Sales contracts
may impose quality requirements that can only be satisfied by stockpiling and
blending material according to quality.
In most situations, costs and recoveries, and therefore cut-off grades, vary
with the geological characteristics of the material being mined. Grade is usually
the most important factor but may not be the only one. If material is sent to
a waste dump, the acid-generating potential of this material may have a direct
impact on costs related to environmental controls. Sulfide content may be a
critical—even overriding—factor for material sent to a roasting or flotation
plant. Clay content may have a deleterious effect on the recovery and throughput of a leaching plant. Phosphorous and silica grades must be considered in
selecting iron ore. Ash and sulfur content influence decisions in coal mines.
The cut-off grade defines the profitability of a mining operation as well as
the mine life. A high cut-off grade can be used to increase short-term profitability and the net present value (NPV) of a project, thus possibly enhancing
the benefit to shareholders and other financial stakeholders, including the
government and local communities. However, increasing the cut-off grade
is also likely to decrease the life of the mine. A shorter mine life can reduce
time-dependent opportunities such as those offered by price cycles. A shorter
mine life can also result in higher socioeconomic impact with reduced longterm employment and decreased benefits to employees and local communities.
Increased cut-off grades may be considered to reduce political risk by
ensuring a higher financial return over a shorter time period. The cut-off grade
may be increased when metal prices go up if this is needed to strengthen the
financial position of the company and reduce the risk of failure when metal
prices fall. Conversely, cut-off grades may be decreased during periods of high
prices to increase mine life and keep high-grade material available to maintain profitability when prices fall. Cut-off grades may also be constrained by
economic or technical performance criteria imposed by bank loans and other
financial institutions.
In some instances, a conscious decision might be made to increase the
mining capacity while keeping the processing capacity constant. This allows
an increase in cut-off grade. Some of the lower-grade material may be stockpiled for processing at a later date. Stockpiling may have a number of consequences—some positive (such as increased useful life of processing facilities)
and others negative (such as increased environmental risk and decreased
metallurgical recovery of stockpiled material).
Public reporting of reserves, which are dependent on the cut-off grade, is
subject to the rules and regulations of the various stock exchanges and other
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Introduction 3
regulatory agencies. A link exists between published reserves and generally
accepted accounting practices. Reserves enter into the calculation of capital
depreciation, company book value, unit cost of production, and taxes. A link
also exists between published reserves and the value that the financial market
gives to a mining company. For some commodities there is a fairly widely held
but arguably incorrect belief that this link is primarily a function of the magnitude of the reserves while quality is of lesser significance. Low cut-off grades
may be considered desirable by those calculating or publicly reporting reserves
if personal bonuses are a function of the magnitude of the published reserves.
As a result of these various links—some desirable, some not—there can be
a desire to maximize the published reserves by using the lowest technically,
financially, and legally defendable cut-off grade. However, one must always
keep in mind that reserves are published for the purpose of informing investors and other stakeholders, and that processes and controls should be put in
place to eliminate the influence of factors that could result in publication of
misleading estimates.
Both outsider and insider stakeholders have an interest in the cut-off
grade and the reserves deriving from it. Outsiders include shareholders,
financial institutions, local communities, environmentalists, regulators, governmental and nongovernmental agencies, suppliers, and contractors and
buyers of the product being sold. Insiders include company management and
employees. The board of directors represents the interests of the shareholders
and is often composed of both insiders and independent outsiders. Cut-off
grades are and should be primarily calculated taking into account only technical and economic constraints. However, the often-conflicting interests and
objectives of the many stakeholders must be understood and prioritized if the
best decision is to be made concerning cut-off grade determination.
The technical literature includes many publications on estimation and
optimization of cut-off grades. The most comprehensive reference is Kenneth F. Lane’s The Economic Definition of Ore: Cut-Off Grades in Theory and
Practice (Lane 1988). The objective most commonly accepted in cut-off grade
optimization studies is optimization of the NPV of future cash flows. To
reach this objective one must take into account space-related variables (such
as the geographic location of the deposit and its geological characteristics), as
well as time-related variables (including the order in which the material will
be mined and processed and the resulting cash flow). The time–space nature
of the problem is quite complex; consequently, so are the proposed mathematical solutions to cut-off grade optimization. The bibliography provides
detailed references to some of these solutions. This book attempts to explain
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4 CHAPTER ONE
basic concepts in a simple fashion, making them accessible to mine managers,
analysts, geologists, mining engineers, accountants, and other practitioners.
The book is divided into several chapters. General concepts are introduced in Chapter 2, including those of utility function, breakeven cut-off
grade, and opportunity cost. Each one of these concepts is then analyzed for
its application in increasingly complex situations, starting with Chapter 3 in
which estimation of breakeven cut-off grades is discussed. Examples are given
for how to separate ore from waste, choose between different processes, analyze polymetallic deposits, and develop stockpiling strategies.
The less intuitive but fundamental concept of opportunity cost is discussed in Chapters 4 and 5. Opportunity costs result from constraints that
are present in all mining operations. As shown in Chapter 4, ignoring capacity
constraints can result in underestimation of cut-off grades and the processing
of uneconomic material. Formulas are developed and examples given to illustrate the relationship between opportunity costs and cut-off grades. Opportunity costs decrease over time, and cut-off grades should decrease accordingly.
Constraints imposed by the geology of the deposit are discussed in Chapter 5.
Capacity constraints and geologic constraints must be taken into account
jointly to determine the applicable cut-off grade. This complex relationship is
illustrated by a number of examples.
Chapter 6 shows that while the same fundamental concepts can be used
to estimate cut-off grades in any situation, there are significant differences in
the application of these concepts to different mining methods. The costs that
should be included in cut-off grade calculations are further discussed in Chapter 7. Situations are considered in Chapter 8 where there is a need to stockpile
and blend material to satisfy constraints imposed by technical or marketing
requirements. New methods are introduced to optimize blending depending
on the objective to be reached.
Closing remarks can be found in Chapter 9, which is followed by Appendix A, a list of symbols, and a bibliography. Appendix A contains additional
examples and solutions to problems referenced in the main text of this book.
Measurements are usually given using the International System of Units
(SI), such as metric tons (t), grams (g), or meters (m). However, examples
are included that also make use of other units, such as ounces (oz) for gold or
pounds (lb) for copper, which are commonly used in specific industries.
One metric ton is equal to 1,000 kg (kilograms), or 2,205 lb. The word
“ounce” refers to a troy ounce of gold and is equal to 31.1035 g. The word
“short ton,” commonly used in the United States, is equal to 2,000 lb.
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5
2
Choosing a cut-off grade is equivalent to choosing the value of a geologically
defined parameter or set of parameters that will be used to decide whether one
metric ton (1 t) of material should be sent to one process or another.
MATHEMATICAL FORMULATION: UTILITY FUNCTION
Let x be the value of the parameter(s) that must be taken into account to
determine the destination to which the material should be sent. In simple
cases, a single parameter may be sufficient to define the destination such as
copper grade or gold grade. In other cases, a set of parameters may have to be
considered such as copper and gold grades, sulfide content, clay content, and
percentage of deleterious elements.
The value, or utility*, of sending one metric ton of material with parameter value (grade) x to destination 1 (process 1) is U1
(x). The utility of sending
the same material to destination 2 (process 2) is U2
(x). The destination that
should be chosen is that which results in the highest utility Umax(x). Figure 2-1
shows the relationship between Umax(x), U1
(x), and U2
(x). The cut-off grade
xc
is the value of x for which
U x U x 1 c 2 c () () =
If U2
(x) exceeds U1
(x) for x greater than xc
, then all material for which x is
greater than xc
should be sent to process 2. Figure 2-1 shows how the cut-off
* The term utility is used in decision theory to represent the satisfaction gained from
following a given course of action (Raiffa and Schlaifer 2000). This satisfaction is
a function of preferences and values specific to the decision maker. The utility of a
given cut-off grade strategy is a measure of the extent to which this strategy reaches
the mining company’s objectives.
General Concepts
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6 CHAPTER TWO
grade can be graphically determined by finding the intersection between
U1
(x) and U2
(x).
As indicated in the introduction, the choice of a cut-off grade is governed
primarily by financial objectives. However, the consequences of choosing a
given cut-off grade are complex and not all of a financial nature. When estimating cut-off grades, all controlling variables must be taken into account. To
facilitate this process, the utility U(x) of sending material of grade x to a given
process is expressed as the sum of three parts:
U x U x U x U x dir opp oth () () () () = + +
In this equation, Udir(x) represents the direct profit or loss that will be incurred
from handling one metric ton of material of grade x. Uopp(x) represents the
opportunity cost or benefit of changing the processing schedule by adding one
metric ton of grade x to the material flow. This opportunity cost only occurs
when there are constraints that limit how many tons can be processed at a
given time. Other factors, which must be taken into account in the calculation
of cut-off grades but may not be quantifiable, are represented by Uoth(x).
C U T- O F F G R A D E A N D G R A D E – TO N N A G E
RELATIONSHI P
The cut-off grade determines the tonnage and average grade of material
delivered to a given process and therefore the amount of product sold. In first
–40
–20
0
20
Grade x
40
60
0 2 4 6 8 10
Umax(x)
Cut-off Grade xc
U2
(x)
U1
(x)
Figure 2-1 Utility maximization and graphical determination of cut-off grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Utility U(x)
General Concepts 7
approximation, if T+c represents the tonnage and x+c symbolizes the average
grade of material above the cut-off grade xc
, the revenue from sales is equal to
T+c ∙ x+c ∙ r ∙ V where r is the proportion of valuable product recovered during
processing and V is the market value of the product sold. The cut-off grade
also determines the tonnage of material mined that will not be processed. Figure 2-2 shows the relationship among cut-off grade and tonnage and average
grade above cut-off grade. The curves on this graph are known as the grade–
tonnage curves. Grade–tonnage curves are used extensively throughout this
document to illustrate the impact that different cut-off grade strategies have
on the economics of a mining operation. Another relationship that is useful
in optimizing cut-off grades is shown in Figure 2-3. This figure shows the
quantity Q+c of valuable product contained in material above cut-off grade as
a function of the cut-off grade:
Q T + + c c = ⋅x +c
As an example, when considering a copper mine, the grade x, the cut-off
grade xc
, and the average grade above cut-off x+c are expressed in % Cu; the
tonnage T+c is expressed in metric tons; and the quantity Q+c is expressed in
metric tons or pounds of copper (1 t equals 2,205 lb). In a gold mine, the
grades are expressed in grams per metric ton (g/t) and the quantity of metal
in metric tons or ounces of gold (1 troy ounce equals 31.1035 g).
0
2
8
6
4
Cut-off Grade
10
12
0.0
1.0
4.0
3.0
2.0
5.0
6.0
0 0.5 1 2.5 2 1.5 3 3.5
Tonnage Above
Cut-off Grade
Average Grade Above
Cut-off Grade
x+c
T+c
xc
Figure 2-2 Example of grade–tonnage curve: tonnage and grade above cut-off grade
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Average Grade Above Cut-off Grade
8 CHAPTER TWO
DIRECT PROFIT AND LOSS: Udir( x )
Direct profits or losses associated with one metric ton of material, Udir(x), are
estimated by taking into account only costs and revenues that can be directly
assigned to mining this material, processing it, and selling the final product.
Breakeven cut-off grades are calculated taking into account only costs and revenues directly resulting from mining and processing (or wasting) one metric
ton of material at grade x. The impact, if any, on total tons mined, production
schedule, and cost per metric ton is ignored. The grade–tonnage relationship
is also ignored.
Mathematical Formulation
The direct profit or loss Udir(x) expected from processing one metric ton of
material of grade x is Uore(x) expressed as follows:
U x x r V R M P O ore o o o ( ) ( )= ⋅ ⋅ − ( )− + +
where
x = average grade
r = recovery, or proportion of valuable product recovered from
the mined material
V = value of one unit of valuable product
R = refining, transportation, cost of sales, and other costs
incurred per unit of valuable product
0
2
8
6
4
Cut-off Grade
10
12
0 0.5 1 2.5 2 1.5 3 3.5
Metal Content Above
Cut-off Grade
xc
Q+c
Figure 2-3 Quantity of valuable product contained above cut-off grade
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General Concepts 9
Mo
= mining cost per metric ton processed
Po
= processing cost per metric ton processed
Oo
= overhead cost per metric ton processed
If the valuable product is a concentrate, V is the value of one unit of
metal contained in the concentrate. For example, V can be the copper price
expressed in dollars per pound of copper, or the gold price expressed in dollars
per troy ounce of gold. r is the percentage of metal in concentrate that will be
paid for. R includes transportation and refining costs, and other deductions
and penalties to be deducted from V. When concentrate is sold to a smelter,
the applicable values of V, r, and R may be negotiated between seller and buyer
and specified in a smelter contract.
If the material is to be wasted, the value of Udir(x) is Uwaste(x), expressed
as follows:
U x M P O waste w w w ( ) = −( ) + +
Mw and Ow are mining and overhead costs, respectively, per metric ton of
waste. Pw is the cost of processing one metric ton of waste as may be needed
to avoid potential water contamination and acid generation, and to satisfy
other applicable regulatory and environmental requirements. The cut-off
grade between ore and waste is xc
such that Uore(xc
) = Uwaste(xc
). Solving this
equation gives the following result:
x M P O M P O r V R c o o o w w w [ ] ( ) ( ) ( ) = + + − + +
⋅ −
The cut-off grade between ore and waste is equal to the difference
between the cost of mining and processing ore and waste, (Mo
+ Po
+ Oo
) –
(Mw + Pw + Ow), divided by the value of one unit of metal contained in one
metric ton of material processed r ∙ (V – R).
Precious Metal Example
To illustrate how these formulas are used to calculate the cut-off grade, consider an open pit gold mining operation characterized as follows:
• For ore being processed: r = 90%, V = $1,400 per ounce of gold, R =
$25.00 per ounce, Mo
= $4.50 per metric ton mined and processed, Po
= $75.00 per metric ton processed, and Oo
= 20% of operating costs.
• For wasted material: Mw + Pw = $5.00, and Ow = 20% of operating
costs.
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10 CHAPTER TWO
The cut-off grade between ore and waste is calculated as follows:
[ ] [ ] ( ) ( ) = ⋅ + − ⋅ ⋅ −
= =
x 1.20 4.50 75.00 1.20 5.00 0.90 1,400 25
0.072 oz/t 2.25 g/t
c
NET PRESENT VALUE: NPVi
The optimal cut-off grade strategy is that which maximizes the enterprisespecific objective function. Such a function nearly always includes, but is not
limited to, net present value optimization. The net present value (NPVi
) of a
project is today’s cash equivalent of the cash flow that is expected to be generated by this project, assuming that money can be invested or borrowed at a
specified discount rate i (e.g., i = 10%).
Mathematical Formulation
If n is the life of a project measured in years, and the (positive or negative) cash
flow generated in year k is Ck
(k = 0, 1, 2, …, n–1), the net present value of the
project using the discount rate i is
∑
() () ()
( )
= + + + + + + +
= +
−
−
= −
NPV C C 1 i C 1 i C 1 i
NPV C 1 i
i 0 1 2
2
n 1
n 1
i k
k
k 0,n 1
Note that in this formula, and throughout this book, the first year (year 0) is
not discounted.
Example of NPV Calculation
Consider a project that is expected to generate the following cash flow over
seven years. The discount rate to be used is i = 15%. Yearly cash flows are in
millions of dollars.
C 200, 20, 100, 120, 100, 50, 20 k , k 0,6 = −{ } − =
The net present value is calculated in Table 2-1. The discounted cash flow
for a given year is equal to the undiscounted cash flow multiplied by the discount factor for this year. The total undiscounted cash flow is $170 million,
whereas the discounted cash flow—the project net present value—is $45.30
million.
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General Concepts 11
NPV of Constant and Perpetuity Cash Flows
In some situations a constant cash flow must be generated over a finite number of years to justify an investment such as sustaining capital. Some situations
also exist where constant yearly costs are expected to perpetuity, such as environmental remediation costs. Examples will be encountered throughout this
book. In such situations, simplifying formulas can be used to calculate net
present values.
If a project is expected to generate a constant cash flow C over n years, the
following equation can be used to calculate the net present value:
()() () ( ) = + + + + + + +
= − NPV C 111 i 1 1 i 1 1 i C g i,n i
2 n 1
where g(i,n) = [1 – (1 + i)–n] (1 + i)/i
If the cash flow is expected to be constant to perpetuity, the net present
value is
NPV C 1 i i i = + ( )
Proof of these formulas is given in Examples 1 and 2 in Appendix A for
constant cash flows and cash flows to perpetuity, respectively. Table 2-2 shows
how the net present value of a $1.00 constant cash flow varies depending of
the life of the project and the discount rate. For example, when calculated at
a 7% discount rate, the net present value of a yearly $1.00 cash flow over five
years has a net present value of $4.39. The same cash flow over an infinite
period has a net present value of $15.29.
Table 2-1 Calculation of net present value using a 15% discount rate
Year, k
Undiscounted
Cash Flow, millions, Ck
Discount Factor,
1/(1 + i)k
Discounted Cash Flow,
millions, Ck
/(1 + i)k
0 ($200.00) 1.0000 ($200.00)
1 $20.00 0.8696 $17.39
2 $100.00 0.7561 $75.61
3 $120.00 0.6575 $78.90
4 $100.00 0.5718 $57.18
5 $50.00 0.4972 $24.86
6 ($20.00) 0.4323 ($8.65)
Total $170.00 $45.30
undiscounted discounted
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12 CHAPTER TWO
OPPORTUNITY COSTS AND BENEFITS: U opp( x )
Ken Lane (1964, 1988) was first to demonstrate the importance of opportunity
costs in cut-off grade estimation. Opportunity cost is defined as the change in a
project net present value that results from changing the production schedule.
Capacity Constraints and Opportunity Cost
Consider a project for which the net present value of future cash flows NPVi
was calculated using the discount rate i. Assume that material was added
to the production schedule that was not included in the original schedule.
Also assume that there are production constraints, the implication being
that by adding new material, the originally planned production schedule is
postponed or slowed down. The net present value of the delayed production
schedule is NPV'i
, less than the original net present value NPVi
. By definition, the opportunity cost of changing the production schedule is equal to the
decrease in net present value, NPV'i
– NPVi
. Adding new material to the
production schedule is economically justified only if the net present value of
the cash flow generated by this new material exceeds the opportunity cost of
changing the original production schedule.
Consider a mining operation in which, under current operating conditions, the processing plant capacity is fully utilized. If new material is added
to the original production schedule and given priority in the processing plant,
the material originally scheduled for processing will be delayed. The duration
t of this delay is the time needed to process the new material. The net present
value of the originally scheduled production will be reduced from NPVi
to
NPV'i
:
NPV ' NPV 1 i i i
t ( ) = +
Table 2-2 Calculation of net present value of a constant $1.00 cash flow over n years
Discount
Rate, i
Project Life (n years)
5 10 15 20 Infinity
NPVi
= g(i,n) NPVi
= (1 + i)/i
5% $4.55 $8.11 $10.90 $13.09 $21.00
7% $4.39 $7.52 $9.75 $11.34 $15.29
9% $4.24 $7.00 $8.79 $9.95 $12.11
11% $4.10 $6.54 $7.98 $8.84 $10.09
13% $3.97 $6.13 $7.30 $7.94 $8.69
15% $3.85 $5.77 $6.72 $7.20 $7.67
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General Concepts 13
The opportunity cost of postponing mining of the already scheduled
material is equal to the loss in NPV:
NPV ' NPV NPV 1 i 1 i i i
t ( ) − = + −
−
The new material should be mined or processed only if its net present
value exceeds the opportunity cost. An example is given in Example 3 in
Appendix A, which shows how to calculate the opportunity cost of mining a
peripheral deposit when this deposit is given priority over previously scheduled production.
Application to Cut-off Grade Estimation
The cut-off grade between two options is obtained by comparing the utility as
well as the advantages and disadvantages of choosing one option rather than
the other. The conclusions are valid only if all costs and benefits are taken into
account.
Opportunity costs or benefits, Uopp(x), may result from mining and processing one metric ton of material not previously scheduled for processing. No
opportunity cost is incurred if the mine, mill, refining facilities, and volume
of sales are not capacity constrained and if adding one more metric ton to the
process has no impact on previously expected cash flows. If there is a capacity constraint, the opportunity cost includes the cost of displacing material
already scheduled for processing and postponing treatment of this material.
Consider a project whose net present value of future cash flows NPVi
was calculated on the basis of currently planned production. According to the
current plan, there is no spare capacity in the processing plant. If one metric
ton of material is added to the capacity-constrained processing plant, treatment of the originally scheduled material is postponed by the time needed
to process the additional ton. Processing one metric ton of material takes t
units of time, where t is the inverse of the yearly plant capacity. Adding one new
metric ton of material not currently planned to be processed will decrease the
net present value of future cash flows from NPVi
to NPV'i
= NPVi
/ (1 + i)t
.
The difference, NPV'i
– NPVi
, is the opportunity cost of processing one more
metric ton of material:
U x NPV 1 i 1 opp i
t ( ) ( ) = + −
−
In this equation, the time t is very small, as it is equal to the inverse of the
yearly capacity of the constrained material flow. Calculus can be used to
demonstrate the following simplified formula for the opportunity cost:
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14 CHAPTER TWO
( ) = − ⋅ ⋅ U x i t NPV opp i
A comparison of the exact formula NPVi
[1 – (1 + i)–t] and its first-order
approximation i∙t∙NPVi
is given in Example 4 in Appendix A. This difference
is less than 10% for a discount rate i = 15%, and decreases for smaller discount
rates.
The discount rate i is expressed as a percentage per year; the time t is
expressed in years per unit of capacity-constrained material; the net present
value is expressed in dollars. The opportunity cost is therefore expressed in
dollars per unit of capacity-constrained material. The opportunity cost must
be added to the direct cost of the process that is capacity constrained.
If the mine is capacity constrained and a decision is made to mine an
additional metric ton of material that was not scheduled to be mined, t is the
time needed to mine this ton and the opportunity cost must be added to the
mining cost Mo
or Mw. If one new ton of ore is sent to a capacity-constrained
mill, t is the time needed to mill this metric ton, and the opportunity cost
must be added to the processing cost Po
. If the refining process is capacity
limited, t is the time needed to refine the concentrate produced from one
metric ton of material at grade x, and the opportunity cost must be added to
the refining cost R.
Application to an Underground Gold Mine
Consider an underground gold mine in which the net present value of future
cash flows is NPVi
= $800,000,000. This value was calculated using the
discount rate i = 15%. The mineshaft is capacity constrained, with a maximum haulage capacity of 1,500,000 t/yr. Consideration is given to mining
low-grade material on the periphery of high-grade stopes. This material was
not included in calculation of the above-mentioned net present value. The
time needed to mine and deliver one metric ton of material to the surface is
t = 1/1,500,000 year. The opportunity cost of adding one metric ton to the
production schedule is
U x 15% $800,000,000 1,500,000
$80.00 per metric ton of ore mined
opp ( )= − ⋅
= −
The following parameters apply to ore being processed:
r = 90%
V = $1,400 per ounce of gold recovered
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General Concepts 15
R = $20.00 per ounce of gold recovered
Mo
= $250.00 per metric ton mined
Po
= $85.00 per metric ton processed
Oo
= 20% of operating costs
If only direct costs and revenues are taken into account, the cut-off grade
between ore and waste is
[ ] [ ] ( ) ( ) = ⋅ + ⋅ −
= =
x 1.20 250.00 85.00 0.90 1,400.00 20.00
0.324 oz/t 10.07 g/t
c
Adding the $80.00 opportunity cost to the mining cost results in a 2 g/t
increase to the cut-off grade:
[ ] [ ] ( ) ( ) = ⋅ + + ⋅ −
= =
x 1.20 250.00 85.00 80.00 0.90 1,400.00 20.00
0.388 oz/t 12.07 g/t
c
At this stage of the mine life, low-grade peripheral material should be
mined only if it averages at least 12.07 g/t. When the mine approaches the
end of its life, the net present value of future cash flows will decrease toward
zero and so will the opportunity cost Uopp(x). The cut-off grade will then
decrease to reach the marginal cut-off grade, 10.07 g/t.
Multiple examples are given later that show how opportunity costs must
be taken into consideration depending on prevailing situations.
O T HER COSTS AND BENEFITS: U oth( x )
Cut-off grades play a critical role in defining tonnages mined and processed,
average grade of mill feed, and project economic feasibility. In addition to the
quantifiable financial impact that cut-off grade changes may have, other costs
and benefits must be taken into account, although their impacts are often not
easily quantifiable. Consideration must be given not only to changes in net
present value and cash flow—as measured by Udir(x) and Uopp(x)—but also
to all other impacts, Uoth(x), including those of an environmental, socioeconomic, ethical, or political nature.
Costs and benefits to all stakeholders must be evaluated, including shareholders, financial institutions, analysts, employees, customers, suppliers, local
communities, government, nongovernmental agencies, and future generations. Senior management must decide how to balance the needs, interests,
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16 CHAPTER TWO
and requirements of these stakeholders. Practical guidelines must be developed, including guidelines for cut-off grade determination, to ensure that
the projects are designed to reach the company’s often conflicting objectives.
Maximizing shareholder value is often quoted as a company’s primary objective. However, other objectives must be taken into account, which include
recognition of responsibilities toward all stakeholders.
CUT-OFF GRADE AND BLENDING STRATEGY
When determining cut-off grades, the situation most commonly encountered
is one where the decision whether a material type—defined by its physical
and chemical properties—should be mined and processed is made solely on
the basis of these properties. This does not take into account more complex
situations where blending of different material types is needed to obtain a
product that can be economically processed and sold. A material type may
have no economic value if considered on its own, but it is needed for blending
with other material to obtain an economically valuable product. For example,
in gold mines where refractory ore is treated by roasting, material with a high
sulfide content and low gold content may have no value if considered on its
own. Yet the calorific value of this material may be needed to economically
extract the gold contained in high-grade, low-sulfide ore.
Circumstances also occur where one material type does not satisfy constraints imposed by sales contracts, but blending with other material will
result in a product that exceeds contractual requirements. This can be the case
in a coal mining operation where one seam has a low calorific value and high
ash content and another seam has a high calorific value and low ash content.
By appropriately mixing the two products, it may be possible to increase the
tonnage of salable coal. Similarly, the product from one iron mine may not be
salable on its own, but a salable product may be obtained by blending with the
product of another mine that exceeds contractual requirements.
A typical situation happens where stockpiles are available with known
tonnages and geochemical properties. In which proportion should the stockpiles be blended to satisfy specified quality requirements? A similar situation
occurs when two or more mines are being designed whose products will have
to be blended before being processed or sold. What should be the mining rate
for each mine, and which cut-off grades should be applied to obtain a material
blend that maximizes profits? Different blending strategies are discussed in
this book.
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17
3
Minimum or breakeven cut-off grades are those that apply to situations where
only direct operating costs are taken into account. Capacity constraints are
ignored. Cash flows are not discounted. Opportunity costs are not taken into
consideration and neither are other consequences, financial or otherwise, that
changing the cut-off grade may have on mining and processing schedules and
cash flows.
CUT-OFF GRADE BETWEEN ORE AND WASTE
Consider material for which the decision has already been made that it will
be mined, so the remaining question is whether it should be sent to the processing plant or wasted.
Mathematical Formulation
Using notations introduced previously, the utility of mining and processing
one metric ton of ore-grade material, Uore(x), can be written as follows:
( ) ( )= ⋅ ⋅ − ( )− + + U x x r V R M P O ore o o o
where
x = average grade
r = proportion of valuable product recovered from the mined
material
V = value of one unit of valuable product
R = refining costs, defined as costs that are related to the unit of
valuable material produced
Mo
= mining cost per metric ton of ore
Po
= processing cost per metric ton of ore
Oo
= overhead cost per metric ton of ore
Breakeven
Cut-off Grade
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18 CHAPTER THREE
The utility of mining and wasting one metric ton of waste material, Uwaste(x),
can be written as follows:
( ) = −( ) + + U x M P O waste w w w
where
Mw = mining cost per metric ton of waste
Pw = processing cost per metric ton of waste, as may be needed to
avoid potential water contamination and acid generation
Ow = overhead cost per metric ton of waste
The minimum cut-off grade is the value xc
of x for which
[ ]
() ()
( ) ( ) ( )
=
= + + − + +
⋅ −
U x U x
x M P O M P O r V R
ore c waste c
c o o o w w w (EQ 3-1)
In this formula, the numerator represents the difference between mining,
processing, and overhead costs incurred when treating the material as ore and
those incurred when treating the same material as waste. In the denominator,
the metal recovery r must be that which applies to material of grade xc
, which
is not necessarily equal to the average recovery for all material sent to the
processing plant.
The relationship between utility functions and cut-off grade is graphically
represented in Figure 3-1.
Internal or Mill Cut-off Grade
If material must be mined, it should be processed if its grade is high enough to
pay for processing costs even if it does not pay for mining costs.
If the costs of mining and shipping material to the waste dump or to the
primary crusher are the same (Mo
= Mw) and there are no significant additional costs in processing waste (Pw = 0 and Ow = 0), this cut-off grade is only
a function of mill costs and recoveries and is independent of mining costs.
Equation 3-1 can be written as follows:
[ ] [ ] ( ) = + ⋅ − x P O r V R c o o (EQ 3-2)
This cut-off grade applies to material located within the limits of an open
pit mine or an underground stope. This material is internal to the current
mine plan and must be mined. The only question is whether it should be
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Breakeven Cut-off Grade 19
processed. For these reasons it is often called internal or mill cut-off grade.
In this formula the overhead cost Oo
is that which applies to processing only.
External or Mine Cut-off Grade Without Waste Stripping
If the option is to leave the material in the ground at no cost, it should be mined
only if its grade is high enough to pay for both mining and processing costs.
( )
( )
( ) ( )
=
= ⋅ ⋅ − − + +
U x 0
U x x r V R M P O
waste
ore o o o
The cut-off grade between ore and waste is
[ ] ( ) ( ) = + + ⋅ − x M P O r V R c o o o (EQ 3-3)
This cut-off grade includes the mining cost and is often referred to as the
external or mine cut-off grade*. The overhead cost Oo
is that which applies to
both mining and processing.
External or Mine Cut-off Grade with Waste Stripping
In the previous formula (Equation 3-3), the external or mine cut-off grade
applies to one metric ton of material of grade x that is exposed to the surface
* Other terms used in open pit mines include in-pit cut-off grade for material within
the pit limits (the internal or mill cut-off grade) and ex-pit cut-off grade for material not included in the pit limits (the external or mine cut-off grade).
U(x)
0
Uwaste(x) = –(Mw + Pw + Ow)
Uore(0) = –(Mo + Po + Oo)
Uore(x) = x·r·(V – R) – (Mo + Po + Oo)
Uore(xc
) = Uwaste(xc
)
xc
Figure 3-1 Relationship between utility functions and cut-off grade
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20 CHAPTER THREE
but had not been included in the mine plan; this material can be mined without waste stripping. This next example considers the case where some waste
stripping is needed. The strip ratio is defined as follows:
=s metric tons of waste per metric ton of ore
If this material is not mined, the utility is zero:
( ) = U x 0 waste
If the decision is made to mine the mineralized material, the utility is
( ) ( ) ( )= ⋅ ⋅ − ( )− + + − ⋅ + + U x x r V R M P O s M P O ore o o o w w w
The cut-off grade is
[ ] ( ) ( ) ( ) = + + + ⋅ + +
⋅ − x M P O s M P O r V R c o o o w w w (EQ 3-4)
CUT-OFF GRADES IN OPEN PIT MINES
The following example shows how to calculate mine and mill cut-off grades,
with and without waste stripping, in an open pit copper mine. The mine operating parameters are characterized as follows:
r = 86% (includes mill and smelter recovery)
V = $3.20 per pound of payable copper
R = $0.60 per pound of payable copper (includes freight,
smelting, and refining)
Mo
= $3.00 per metric ton of ore mined
Po
= $10.00 per metric ton of ore processed
Oo
= $1.70 per metric ton of ore processed
Mw = $3.30 per metric ton of waste mined
Pw = $0.50 per metric ton of waste mined (includes
environmental control and remediation)
Ow = $0.40 per metric ton of waste mined
The opportunity cost of classifying one metric ton of material as ore or
waste is as follows (1 t = 2,205 lb):
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Breakeven Cut-off Grade 21
( )
( )
( ) ( )
( ) ( )
( )
( )
= ⋅ ⋅ − − + +
= ⋅ ⋅ − ⋅ − + +
= −
= − + +
= − + +
= −
U x x r V R M P O
x 0.86 3.20 0.60 2,205 3.00 10.00 1.70
4,929x $14.70
U x M P O
3.30 0.50 0.40
$4.20
ore o o o
waste o o o
For material internal to the pit limits, the mill cut-off grade is
= − ( ) = x 14.70 4.20 4,929 0.21% Cu c (EQ 3-5)
For material external to the pit limits, the mine cut-off grade is
x = = 14.70 4,929 0.30% Cu c (EQ 3-6)
The cut-off grades calculated in Equations 3-5 and 3-6 could have been
obtained directly by substituting the appropriate values in Equations 3-1
and 3-3. The difference in cut-off grade, 0.09% Cu, represents the amount of
additional copper needed to pay for the cost of mining material that was not
scheduled to be mined. Figures 3-2 and 3-3 give graphical representations
of the utility functions used to calculate the mill and mine cut-off grades,
respectively.
In the previous calculations leading to Equation 3-6, the external or mine
cut-off grade is that which applies to one metric ton of material of grade x that
is exposed to the surface but had not been included in the mine plan. This
material can be mined without waste stripping. This next formula considers
the case where some waste stripping is needed to mine this material. The ore
to waste strip ratio is
s = 1.5 t of waste per metric ton of mineralized material
The utility of mining and processing the mineralized material is
( ) ( ) ( ) ( )
( ) ( )
( )
= ⋅ ⋅ − − + + − ⋅ + +
= ⋅ ⋅ − ⋅ − + +
− ⋅ + +
= −
U x x r V R M P O s M P O
x 0.86 3.20 0.60 2,205 3.00 10.00 1.70
1.5 3.30 0.50 0.40
4,929x $21.00
ore o o o w w w
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
22 CHAPTER THREE
The corresponding cut-off grade is
x = = 21.00 4,929 0.43%Cu c (EQ 3-7)
This cut-off grade could have been calculated directly by substituting the
appropriate values in Equation 3-4. Figure 3-4 gives a graphical representation
of the utility functions used to calculate the mine cut-off grade with a 1.5 strip
ratio.
–$20
–$10
–$15
$5
0
–$5
Cut-off Grade, % Cu
$10
$15
0.10% 0.20% 0.40% 0.30% 0.50%
Material Mined
and Wasted
Material Mined
and Processed
Cut-off Grade
0.21% Cu
Figure 3-2 Graphical estimation of internal (mill) cut-off grade
–$20
–$10
–$15
$5
0
–$5
Cut-off Grade, % Cu
$10
$15
0.10% 0.20% 0.40% 0.30% 0.50%
Material Not Mined
Material Mined
and Processed
Cut-off Grade
0.30% Cu
Uore(x)
Figure 3-3 Graphical estimation of external (mine) cut-off grade
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Breakeven Cut-off Grade 23
CUT-OFF GRADES IN UNDERGROUND MINES
General Considerations
Capacity constraints are common in underground mines. These may include
constraints imposed by ore body geometry, geotechnical conditions, shaft and
haulage capacities, ventilation requirements, mining method, size and type of
mining equipment, health and safety regulations, and other restrictions that
limit production from a stope, a mine section, or the mine as a whole. Furthermore, many decisions made in an underground mine are capital intensive and
take a significant amount of time to implement and result in positive cash flow.
In such an environment, capacity constraints have a significant effect on
the cut-off grades. Opportunity costs must be taken into account to quantify
how the project net present value is modified over time by changing cut-off
grade and mine plan. In this section, only undiscounted cash flows are taken
into account, without discounting. Opportunity costs will be discussed in
Chapter 4.
The minimum conditions that must be satisfied to justify development of
a new stope and how to determine the locations of stope boundaries, are two
aspects of underground mining that are discussed in the next sections (see
Figure 3-5).
Minimum Tonnage and Grade
A minimum grade is occasionally quoted when referring to the average grade
that a stope must exceed before it is considered for mining. Strictly speaking,
–$25
–$10
–$15
–$20
$5
0
–$5
Copper Grade, % Cu
$10
$15
0.10% 0.20% 0.40% 0.30% 0.50%
Material Not Mined
Material Mined
and Processed
Cut-off Grade
0.43% Cu Uore(x)
Figure 3-4 Graphical estimation of internal (mill) cut-off grade with strip ratio
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Utility, Profit per Metric Ton
24 CHAPTER THREE
this is not a cut-off grade but an average grade, which must be linked to a
tonnage. The minimum stope average grade depends on the size of the stope,
its location with respect to existing facilities, ease of access, geotechnical
conditions, and other stope-specific characteristics. This average grade is that
for which the cost of developing and mining the stope is expected to be less
than the profit made by processing the ore and selling the final product. This
calculation must be made on a discounted basis, taking all physical constraints
into account.
Optimization of Stope Size
When designing a stope, one must take into account the constraints imposed
by mining method and geotechnical conditions. One must also determine
whether lower-grade material located along the boundary of the stope should
be included in the stope. Such material should be mined only if the expected
value of the recoverable product it contains exceeds all incremental costs,
including mining, haulage, processing, backfilling, and other costs. The minimum cut-off grade that defines boundary material which should be mined
is the mine cut-off grade, and is estimated using a formula similar to that for
material at the bottom of an open pit mine (Equation 3-3):
[ ] ( ) ( ) = + + ⋅ − x M P O r V R c o o o
Mineralized Zone
Should we
extend the top
drift and make
the stope wider?
Proposed Accesses
and Stope
Boundaries
Existing Accesses
Figure 3-5 Estimation of average grade and cut-off grade in an underground mine
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Breakeven Cut-off Grade 25
As an example, consider an underground gold mine where the incremental mining cost is $120.00 per metric ton, the mill processing cost is $80.00
per metric ton, and the mining and processing overhead is $30.00 per metric
ton. The mill recovery is 90%. Given a gold price of $1,400 per ounce and a
sales cost of $80.00 per ounce, the minimum cut-off grade to be considered to
locate a stope boundary is (1 troy ounce = 31.1035 g)
[ ] [ ] ( ) = ⋅ + + ⋅ − = x 31.1035 120.00 80.00 30.00 0.90 1,400.00 80.00 6.02 g/t c
This cut-off grade is the lowest average grade that a stope increment must
have before it is considered for mining. Both planned and unplanned dilution
must be taken into account. The mining cost should include the incremental
development cost needed to make the stope wider. Opportunity costs such as
those imposed by haulage capacity constraint should be taken into account,
which will increase the cut-off grade. Opportunity costs will be discussed in
Chapter 4.
If low-grade material must be mined because it is located within a stope
or within other planned openings such as shafts, raises, drifts, crosscuts, and
so forth, a lower cut-off grade can be used to determine whether this material
should be wasted or processed. For such material, blasting and haulage costs
will be incurred whether the material is treated as ore or waste. Only incremental costs need be considered. The minimum cut-off grade is estimated
using the following general formula:
[ ] ( ) ( ) ( ) = + + − + +
⋅ − x M P O M P O r V R c o o o w w w
If ore and waste mining costs, including overhead, are the same (Mo
=
Mw) and waste processing costs are negligible (Pw = 0), this formula can be
written as follows:
[ ] ( ) ( ) = + ⋅ − x P O r V R c o o
The mill cut-off grade is recognized here (Equation 3-2). In this formula, the
overhead cost Oo
is that which applies to processing only. Applicable opportunity costs, which in this case are likely to be only those imposed by mill
capacity constraints, should also be taken into account, which will increase
the cut-off grade.
As an example, consider exploration drifts in an underground gold mine.
While mostly in waste, these drifts periodically encounter mineralized zones,
and the decision must be made whether this material should be wasted or
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
26 CHAPTER THREE
sent to the processing plant. Mining costs are Mo
= Mw = $350.00 per metric
ton, and mining overhead costs are Ow = $70.00 per metric ton, regardless of
whether the material is hauled to the waste dump or the mill. The milling cost
is Po
= $79.00 per metric ton, with a processing overhead cost of $12.00 per
metric ton. The total overhead cost per metric ton of ore, including mining
and processing, is Oo
= $70.00 + $12.00 = $82.00. The gold price is $1,450
per ounce, and the cost of sales is $90.00 per troy ounce. The mill recovery is
89%.
The minimum cut-off grade that should be used to send material to the
mill is
[ ]
[ ]
( )
( ) ( )
( ) ( )
= ⋅ + +
− +
⋅ −
= ⋅ + ⋅ −
=
x 31.1035
350.00 79.00 82.00
350.00 70.00
0.89 1,450.00 90.00
31.1035 79.00 12.00 0.89 1,450.00 90.00
2.34 g/t
c
CUT-OFF GRADE BETWEEN TWO PROCESSES
Mathematical Formulation
If two processes are available to treat the same material, cut-off grades must
be calculated to separate waste from ore being processed and to decide to
which one of the two processes the ore should be sent. How to decide whether
material should be processed or wasted was discussed previously. To decide
between two processes, the utility of sending material of grade x to process 1
must be compared with that of sending the same material to process 2. Mining costs, including haulage cost to the processing plant, may vary depending
on the process. Processing costs will be different and so will metallurgical
recoveries and overhead costs. If the product sold is a function of the process
being used, even the revenue per metric ton produced may differ. The cut-off
grade between two processes is calculated using the following formulas, where
subscripts refer to the process number:
( )
( )
() ()
( ) ( ) ( )
( )
( )
( ) ( )
( )
( )
= ⋅ ⋅ − − + +
= ⋅ ⋅ − − + +
=
= − + − + −
⋅ − − ⋅ −
U x x r V R M P O
U x x r V R M P O
U x U x
x M M P P O O r V R r V R
1 1 1 o1 o1 o1
2 2 2 o2 o2 o2
1 c 2 c
c o1 o2 o1 o2 o1 o2 1 1 2 2
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Breakeven Cut-off Grade 27
In this formula, the numerator is the difference between costs incurred if
one metric ton of material is sent to process 1 and costs incurred if the same
metric ton is sent to process 2. The denominator is the difference between
revenues resulting from sending one metric ton of material containing one
unit of valuable product (e.g., one ounce of contained gold or one pound of
contained copper) to process 1 and revenues resulting from sending the same
metric ton to process 2.
Precious Metal Example
Consider a gold mining operation from which material can be sent to either
of two processing facilities, a leach pad (process 1) or a mill (process 2). The
costs associated with this operation are as follows:
Mw = $3.00 mining cost per metric ton of waste
Pw = $0.80 processing cost per metric ton of waste
Ow = $0.40 overhead cost per metric ton of waste
Mo1 = $5.00 mining cost per metric ton of ore leached
Mo2 = $5.50 mining cost per metric ton of ore milled
Po1 = $9.00 processing cost per metric ton leached
Po2 = $35.00 processing cost per metric ton milled
Oo1 = $1.20 overhead cost per metric ton leached
Oo2 = $4.50 overhead cost per metric ton milled
r1
= 60% average leach recovery
r2
= 97% average mill recovery
V = $1,600 per ounce of gold sold
R1
= $50.00 per ounce of gold sold
R2
= $50.00 per ounce of gold sold
The utilities of sending one metric ton of material to the waste dump, the
leach pad, or the mill are calculated below. Dollars per ounce was converted to
dollars per gram (1 troy ounce = 31.1035 g) to obtain cut-off grades in grams
per metric ton.
( )
( )
( )
( )
( )
( )
( )
( )
= − + + = −
= ⋅ ⋅ − − + + = ⋅ −
= ⋅ ⋅ − − + + = ⋅ −
U x M P O $4.20
U x x r V R 31.1035 M P O $29.90 x $15.20
U x x r V R 31.1035 M P O $48.34 x $45.00
waste w w w
1 1 1 o1 o1 o1
2 2 2 o2 o2 o2
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28 CHAPTER THREE
These utility functions are plotted in Figure 3-6. The cut-off grades are
( ) ( )
( ) ( )
= −
=
= − −
=
Waste-leach cut-off 15.20 4.20 29.90
0.37 g/t
Leach-millcut-off 45.00 15.20 48.34 29.90
1.62 g/t
CUT-OFF GRADE WITH VARIABLE RECOVERY
Mathematical Formulation
In the previous examples, it was assumed that the recovery achieved in the
processing plant was a constant. For many processes and deposits, the recovery r is a function r(x) of the head grade x. The value of Uore(x) must then be
written as follows:
( ) () () = ⋅ ⋅ − ( )− + + U x x r x V R M P O ore o o o
The value of Uwaste(x) remains independent of x:
( ) = −( ) + + U x M P O waste w w w
($60)
$0
($20)
($40)
$20
Gold Grade, g/t
$40
$60
$80
0.5 1.5 1 2
Waste-Leach
Cut-off
Leach-Mill
Cut-off
Leach Utility
Waste Utility Mill Utility
Figure 3-6 Graphical estimation of cut-off grade between wasted, leached, and
milled material
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Breakeven Cut-off Grade 29
Calculating the cut-off grade requires finding the value of x such that Uore(x)
= Uwaste(x).
Nonlinear Recovery: A Precious Metal Example
Consider a gold mining operation from which material can be sent to either
of two processing facilities, a leach pad or a mill. Mining, processing, and
overhead costs are $4.20 for waste, $15.20 for leach, and $45.00 for mill. The
gold price is $1,600 per ounce from which must be deducted a $50.00-perounce sales cost. The maximum gold recoveries are 60% for leaching and 90%
for milling. Significantly lower recoveries are achieved for low-grade material.
Figure 3-7 shows the relationship between recoveries and grade, as determined from metallurgical testing and historical production statistics.
Figure 3-8 shows the profit per metric ton that will be made depending
on whether material of grade x is wasted (Uwaste(x) = –$4.20), sent to the
leach pad (U1
(x) = x ∙ r1
∙ $49.83 – $15.20), or processed in the mill (U2
(x) =
x ∙ r2
∙ $49.83 – $45.00). ($49.83 is the maximum value of one gram of gold
contained, assuming 100% recovery: (V – R)/32.1035). Figure 3-8 also shows
how the cut-off grade can be determined by graphical method. The relationship between the utility of leaching or milling material and the average grade
of this material is no longer linear. The optimal process for material of grade
x is that for which the utility is highest. The cut-off grades are the grades at
which the curves intersect. If a constant 60% recovery for leached material
and 90% recovery for milled material had been assumed, the waste-leach
0
10
20
30
40
50
60
70
80
90
100
Gold Grade, g/t
0 1 2 3 4 5 6 7 8
Mill Recovery
Leach Recovery
Figure 3-7 Relationship between recoveries and average grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Gold Recovery, %
30 CHAPTER THREE
cut-off would have been estimated at 0.38 g/t and the leach-mill cut-off at
1.99 g/t. When variable recoveries are taken into account, the cut-offs are
substantially higher, 1.16 g/t and 3.95 g/t respectively.
CONSTANT TAIL MODEL OF VARIABLE RECOVERY
Mathematical Formulation
A model often used to represent the relationship between plant recovery and
average grade of plant feed is the constant tail model. This model assumes
that a fixed amount of metal cannot be recovered, whatever the grade of the
material sent to the plant. If x is the average grade of one metric ton of material
and c is the fixed amount that cannot be recovered, the recoverable amount is
( ) ( ) ⋅ = ⋅ − x r x r x c c
where
x = average grade of material sent to process
r(x) = plant recovery if head grade is x
rc
= constant recovery after subtracting constant tail
c = constant tail
($100)
$0
($50)
$50
Gold Grade, g/t
$100
$150
$200
$250
1 2 3 4 5 6 7
Waste-Leach
Cut-off
Leach-Mill
Cut-off
Leach Utility
Mill Utility
Figure 3-8 Graphical estimation of cut-off grade between wasted, leached, and
milled material with variable recoveries
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Breakeven Cut-off Grade 31
The recovery function is as follows:
( )
( )
( )
< =
> = ⋅ −
If x c: r x 0
If x c: r x r 1 c x c
The cut-off grade is determined as follows:
[ ]
( )
( )
( )
( ) ( )
( )
() () ( )
( ) ( )
( )
= − + +
= ⋅ ⋅ − − + +
= ⋅ − ⋅ − − + +
= + + − + +
⋅ − +
U x M P O
U x x r x V R M P O
r x c V R M P O
x M P O M P O r V R c
waste w w w
ore o o o
c o o o
c o o o w w w c
If x'c
is the cut-off grade with constant recovery rc
, the cut-off grade with
constant tail is
x x c c = +' c
Constant Tail Model: A Precious Metal Example
Consider a gold mining operation where material is being milled. Mining,
processing, and overhead costs are $4.20 for waste and $45.00 for mill. The
gold price is $1,600 per ounce from which must be deducted a $50.00-perounce charge.
As a result of metallurgical tests, the mill recovery was determined to be
best represented using the constant tail model with parameters rc
= 90% and
c = 0.50 g/oz:
( ) ( )
( )
( )
< =
> = ⋅ − = ⋅ −
If x c: r x 0
If x c: r x r 1 c x 0.90 1 0.50 x c
The relationship between recovery r(x) and average grade x is shown in
Figure 3-9. The relationships between Uore(x) and Uwaste(x) and grade x are
calculated as follows:
( )
( )
( )
() () ( )
( ) ( )
= − + + = −
= ⋅ ⋅ − − + +
= ⋅ − ⋅ − −
= −
U x M P O 4.20
U x x r x V R M P O
0.90 x 0.50 1,600 50.00 31.1035 45.00
44.85x 67.43
waste w w w
ore o o o
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
32 CHAPTER THREE
These relationships are depicted in Figure 3-10. The cut-off grade between ore
and waste is xc
such that Uore(x) = Uwaste(x):
= − ( ) = x 67.43 4.20 44.85 1.41 g/t c
B R E A K E V E N C U T- O F F G R A D E A N D P O LY M E TA L L I C
DEPOSITS
Polymetallic deposits are defined as deposits that contain more than one metal
of economic value. The formulas that must be used to calculate the utility
of sending one metric ton of material to a given destination or process must
consider the contribution of each metal. The decision whether one metric ton
of material should be wasted or sent to the processing plant can no longer be
made on the basis of grade alone. Dollar values must be calculated for each
possible process, and the cut-off between ore and waste must be expressed in
dollar terms.
General Considerations
Consider a metric ton of material that contains two valuable metals, copper
and gold. Let x1
and x2
be the copper and gold grades, respectively. The processing plant consists of crushing, grinding, and flotation circuits. A copper
concentrate is produced, which is sold to a smelter. The flotation plant recovery is r1
for copper and r2
for gold. Mining, processing, and overhead costs
0
10
20
30
40
50
60
70
80
90
100
Gold Grade, g/t
0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0
Asymptotic Recovery rc
Constant
Tail c Mill Recovery
Figure 3-9 Relationship between recovery and average grade with constant tail
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Gold Recovery, %
Breakeven Cut-off Grade 33
associated with one metric ton of material sent to the flotation plant are Mo
,
Po
, and Oo
, respectively. The corresponding costs per metric ton of waste are
Mw, Pw, and Ow. According to the smelter contract, the value received for sale
of the concentrate is p1
= 96.5% of the value of the copper contained in the
concentrate after deducting d1
, and p2
= 99% of the gold contained. Smelter
cost deductions are Cs
per metric ton of concentrate. The concentration ratio
K is the number of metric tons of material that must be processed to produce
one metric ton of concentrate. The cost of shipping one metric ton of concentrate to the smelter is Ct
. Metal prices are those quoted on the London Metal
Exchange, V1
and V2
for copper and gold, respectively. Hence the value of one
metric ton of material sent to the flotation plant:
( ) ( ) ( ) ( ) = − + −−− + + U x , x x r d p V x r p V C K C K M P O ore 1 2 1 1 1 1 1 2 2 2 2 s t o o o
If the same metric ton is sent to the waste dump, the corresponding costs are
= −( ) + + U M P O waste w w w
The material should be sent to the processing plant if
( ) > U x , x U ore 1 2 waste
($60)
$0
($20)
($40)
$20
Gold Grade, g/t
$40
$60
0.5 1.5 1.0 2.0 2.5 3.0 3.5
Constant Tail c
Waste-Mill
Cut-off
Waste Utility
Mill Utility
Figure 3-10 Graphical estimation of cut-off grade between wasted and milled
material with constant tail
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34 CHAPTER THREE
These formulas show that many factors enter into the calculation of the cutoff between ore and waste. Processing costs and recoveries are likely to be dependent not only on metal content but also on other geological characteristics such
as mineralogy, hardness, clay content, and degree of oxidation, which change
depending on the area of the deposit being mined. Smelter contracts heavily
penalize concentrates that are found to contain excessive amounts of specified
deleterious elements. All these factors must be taken into account when estimating the cut-off value applicable to one metric ton of mineralized material.
Because the value of one metric ton of material is a function of more
than one grade, it is no longer meaningful to talk about a “cut-off grade.” Historically, this multidimensional problem was reduced to a one-dimensional
problem by defining a “metal equivalent.” With the advance of computers and
the ease of use with which complex mathematical calculations can be made,
one now talks of cut-off values, which are expressed in dollar terms and require
calculation of a net smelter return. Net smelter return and metal equivalent
are discussed in the following sections.
Calculation of Cut-off Grades Using Net Smelter Return
For polymetallic deposits, the utility of sending one metric ton of material to
the smelter is best expressed in terms of net smelter return, or NSR. The net
smelter return is defined as the return from sales of concentrates, expressed in
dollars per metric ton of ore, excluding mining and processing costs.
Mathematical Formulation
In the previous copper-gold example, the net smelter return of one metric ton
of ore with copper grade x1
and gold grade x2
is
( ) ( ) ( ) = − + − − NSR x , x x r d p V x r p V C K C K 1 2 1 1 1 1 1 2 2 2 2 s t
The utility of sending this metric ton of ore to the processing plant is
( ) () () = − + + U x , x NSR x , x M P O ore 1 2 1 2 o o o
Using NSR values simplifies the calculation of cut-off grades. The NSR
cut-off between processing and wasting one metric ton of material is NSRc
,
obtained by setting Uore(x1
, x2
) equal to Uwaste:
( ) ( ) = + + − + + NSR M P O M P O c o o o w w w
In polymetallic deposits, cut-offs should not be expressed in terms of
minimum metal grade; they should be expressed in terms of minimum NSR.
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Breakeven Cut-off Grade 35
Calculation of NSR Cut-off: A Copper-Molybdenum Example
Consider a copper molybdenum mining operation. In this section, the subscript 1 refers to copper and subscript 2 refers to molybdenum. Hence x1
is
the copper grade and x2
is the molybdenum grade. The following parameters
characterize the operation:
r
1
= 89% copper flotation plant recovery
p1
= 96.5% copper smelting recovery
r2
= 61% molybdenum flotation plant recovery
p2
= 99% molybdenum roasting recovery
V1
= $1.20 value of one pound of copper sold
V2
= $6.50 value of one pound of molybdenum sold
R1
= $0.065 refining cost per pound of copper
K = 72 metric tons of ore must be processed to produce one
metric ton of concentrate
Cs
+ Ct
= $145 smelting and freight costs per metric ton of concentrate
R2
= $0.95 conversion, roasting, and freight costs per pound of
molybdenum
Mo
= $1.00 mining cost per metric ton of ore milled
Po1 = $3.00 mill processing cost per metric ton milled
Po2 = $0.15 incremental molybdenum processing cost per metric
ton milled
Oo
= $0.50 overhead cost per metric ton milled
Mw = $1.00 mining cost per metric ton wasted
Pw = $0.05 processing cost per metric ton wasted
Ow = $0.05 overhead cost per metric ton wasted
The NSR of one metric ton of material with average grade x1
, x2
is calculated as follows:
( )
( ) ( )
( )
( )
( )
= −
+ − − +
= ⋅ ⋅ − ⋅ ⋅
+ ⋅ ⋅ − ⋅ ⋅ −
= + −
NSR x , x x r p V R
x r p V R C C K
0.89 0.965 1.20 0.065 2,205 x
0.61 0.99 6.50 0.95 2,205 x 145.00 72
2,149x 7,390x 2.014
1 2 1 1 1 1 1
2 2 2 2 2 s t
1
2
1 2
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
36 CHAPTER THREE
Therefore, the NSR of one metric ton of ore averaging x1
= 0.45% Cu and x2
= 0.035% Mo is $10.24. For material that must be mined but can be either
wasted or processed, the cut-off NSR (mill or internal cut-off NSR) is NSRc
calculated as follows:
( ) ( ) ( )
( ) ( ) ( )
= + − + − + −
= + −+−+ −
=
NSR P P P O O M M
3.00 0.15 0.05 0.50 0.05 1.00 1.00
$3.55 per metric ton
c o1 o2 w o w o w
For material that need not be mined (mine or external cut-off NSR),
NSRc
is calculated as follows:
= + + +
= + + +
=
NSR P P O M
3.00 0.15 0.50 1.00
$4.65 per metric ton
c o1 o2 o o
The relationship between NSRc
, x1
, and x2
is shown in Figure 3-11.
Calculation and Reporting of Metal Equivalent
Before computers became widely used, it was common practice to talk about
polymetallic deposits in terms of metal equivalent. If one metric ton of material contains two metals, copper and molybdenum, with average grade x1
and
0.00
0.01
0.02
0.03
0.04
0.05
0.06
0.07
0.08
0.09
0.10
%Cu
0.0 0.05 0.10 0.15 0.20 0.25 0.30 0.35
Waste
Ore
NSR = $4.65
(Mine Cut-off)
NSR = $3.55
(Mill Cut-off)
Figure 3-11 Relationship between cut-off NSR and metal grades
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. %Mo
Breakeven Cut-off Grade 37
x2
respectively, the corresponding copper equivalent is defined as the copper
grade x1e that one metric ton must contain to produce the same revenue,
assuming no molybdenum.
The revenue generated by mining and processing one metric ton of
material with copper grade x1
and molybdenum grade x2
is NSR(x1
, x2
). The
revenue generated by mining and processing one metric ton of material with
copper grade x1e and no molybdenum is NSR(x1e, 0.0). The copper equivalent
is obtained by solving the following equation:
( ) = ( ) NSR x ,0.0 NSR x , x 1e 1 2
A molybdenum equivalent can be calculated instead of a copper equivalent. The molybdenum equivalent is the molybdenum grade x2e that satisfies
the following equation:
( ) = ( ) NSR 0.0, x NSR x , x 2e 1 2
In the previous copper-molybdenum example, the net smelter return was
expressed as follows:
( ) ( ) ( ) ( ) = − + − − + NSR x , x x r p V R x r p V R C C K 1 2 1 1 1 1 1 2 2 2 2 2 s t
Hence,
( ) ( ) ( ) = −−+ NSR x ,0.0 x r p V R C C K 1e 1e 1 1 1 1 s t
The copper equivalent is
( )() = + −
−
x x x r p V R r p V R 1e 1 2 2 2 2 2 1 1 1 1
Similarly, the molybdenum equivalent is
( )() = + −
−
x x x r p V R r p V R 2e 2 1 1 1 1 1 2 2 2 2
Using the information listed previously concerning prices, cost, and recoveries, the copper and molybdenum equivalents can be calculated as follows:
( )
( )
= + = +
= + = +
x x x 7,390 2,149 x 3.439x
x x x 2,149 7,390 x 0.291x
1e 1 2 1 2
2e 2 1 2 1
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
38 CHAPTER THREE
The copper equivalent of material averaging x1
= 0.45% Cu and x2
= 0.035%
Mo is 0.57% Cu-equivalent. The molybdenum equivalent of the same material is 0.166% Mo-equivalent.
In practice, because of the complexity of the formulas to be used to
correctly estimate the value of one metric ton of material, and because
equivalence changes with metal price, recoveries, and refining costs, grade
equivalence is rarely a useful tool in calculation of cut-off grades. Quoting the
amount of metal equivalent contained in a deposit is of little use to investors.
Publication of reserves in terms of metal equivalence is generally not accepted
by regulatory agencies unless additional disclosures are made, including publication of the average grade of each metal and explanation of the formula used
to calculate metal equivalence.
OPPORTUNITY COST OF NOT USING THE O P T I M U M
CUT-OFF GRADE
If the optimum cut-off grade is not used, material is sent to a destination
where the profit is less than could be made otherwise or the loss incurred is
greater than necessary. Figure 3-12 shows the opportunity cost incurred per
metric ton when a leach-mill cut-off grade of 3 g/t is used although the optimal cut-off grade is 4 g/t. The loss is represented by the difference between
the utility of the chosen process and that of the optimal process for the same
average grade. Figure 3-13 shows the opportunity cost incurred per metric ton
when a leach-mill cut-off grade of 5 g/t is used.
Mathematical Formulation
Let U1
(x) be the utility of leaching one metric ton of material of grade x and
U2
(x) be the utility of milling the same metric ton. These utilities can be written as follows (in these equations the cost of sales R is included in V, and the
overhead costs Oo
are included in Mo
, Po1, and Po2):
( )
( )
( )
( )
= ⋅ ⋅ − +
= ⋅ ⋅ − +
U x x r V M P
U x x r V M P
1 1 o o1
2 2 o o2
The optimal cut-off grade is
( ) ( ) = − −
x P P r r V c o1 o2 1 2
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Breakeven Cut-off Grade 39
–20
0
–10
10
20
30
40
Grade, g/t
1 2 3 4 5 6
Area of Opportunity Loss
If Cut-off = 3 g/t
Cut-off Actually Used
xs
= 3 g/t
Optimal Leach-Mill Cut-off
xc
= 4 g/t
Figure 3-12 Opportunity cost of using a cut-off grade lower than the optimal cutoff grade
–20
0
–10
10
20
30
40
Grade, g/t
1 2 3 4 5 6
Area of Opportunity Loss
If Cut-off = 5 g/t
Optimal Leach-Mill Cut-off
xc
= 4 g/t
Cut-off Actually Used
xs
= 5 g/t
Figure 3-13 Opportunity cost of using a cut-off grade higher than the optimal cutoff grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Utility, $/t Utility, $/t
40 CHAPTER THREE
Let xs
be the selected cut-off grade, which is lower than the optimal cutoff grade xc
(Figure 3-12). Material with grade x between xs
and xc
is being
milled but, ideally, should be leached. For each metric ton of grade x between
xs
and xc
, the opportunity cost is
( ) ( ) () () − = ⋅ − ⋅ − − U x U x x r r V P P 2 1 2 1 o2 o1
Integrating this formula from x = xs
to x = xc
we obtain the total opportunity
cost:
( ) ( )
( ) ( ) ( )
( ) = −
⋅ − ⋅
− −
⋅ −
total opportunity cost Q x Q x r r V
Tx Tx P P
s c 2 1
s c o2 o1
In this formula, T(xs
) – T(xc
) is the tonnage of material with average grade
between xs
and xc
, and Q(xs
) – Q(xc
) is the quantity of metal contained in this
material. One could avoid this opportunity cost by increasing the mill capacity by a tonnage amount equal to T(xs
) – T(xc
). Such an increase in capacity
is justified if the cost of such an increase is expected to be less than the total
opportunity cost.
Similar equations are applicable if xs
is higher than xc
and material that
should be milled is leached (Figure 3-13):
( ) ( )
( ) ( ) ( )
( ) = −
⋅ − ⋅
− −
⋅ −
total opportunity cost Q x Q x r r V
Tx Tx P P
c s 1 2
c s o1 o2
An example of how to estimate the opportunity cost is given in Example 5 in Appendix A.
CUT-OFF GRADE AND LOW-GRADE STOCKPILES
Consideration may be given to stockpiling low-grade material instead of wasting it if such material is not currently economic to process but metal prices
are expected to be higher at a later date. Stockpiling low-grade material may
also be considered when capacity constraints prevent current processing of
material that otherwise could be processed economically. To decide whether
material of grade x should be wasted or stockpiled, one must compare the
utility of wasting Uwaste(x) with that of stockpiling Ustp(x). The cut-off grade
between stockpile and waste is the value xc
of x for which U
stp(x) = Uwaste(x).
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Breakeven Cut-off Grade 41
The utility of wasting material of grade x is
( ) = −( ) + + U x M P O waste w w w
To calculate the utility of stockpiling, one must take into consideration
stockpiling costs, and the cost of retrieving material from the stockpile and
processing it at a later date. In addition, metallurgical recoveries of stockpiled
material may differ from those of freshly mined material, and the price of
the product sold may be different from that prevailing when the decision to
stockpile is made:
( )= −( ) + +
−
−
+
U x M P O
NPV(futurecosts of stockpile maintenance)
NPV(futurere-handling and processing costs)
NPV(futurerevenues from sales)
stp stp stp stp
where
M
stp = current mining costs per metric ton
delivered to the low-grade stockpile
P
stp = current costs of stockpiling material
that will be processed later, including
the cost per metric ton of extending the
stockpile area if required
O
stp = current overhead costs associated with
mining and stockpiling
NPV(future costs of
stockpile maintenance)
= net present value of yearly costs that
will be incurred to maintain stockpiled
material in an environmentally safe
fashion until it is processed
NPV(future re-handling
and processing costs)
= net present value of the one-time costs
that will be incurred when the material is retrieved from the stockpile and
processed
NPV(future revenues
from sales)
= net present value of revenues expected
from sales when processed material is
sold
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
42 CHAPTER THREE
At the time the product recovered from the stockpiles is sold, the revenues are x ∙ r
stp ∙ (Vstp
– R
stp), where rstp is the expected recovery at the time of
processing, Vstp is the dollar value of the product sold at the time it is sold, and
R
stp is the corresponding cost of sales per unit of product sold. The recovery
r
stp may be less or higher than that which would apply to the same material if
processed when mined. Sulfide material is likely to oxidize during stockpiling.
If a sulfide flotation process is to be used, oxidation will result in lower recovery. Conversely, if an oxide leach process is to be applied to material that was
not fully oxidized when mined, stockpiling may result in enhanced recovery.
There are obvious difficulties in using these formulas, the main one being
that future costs and revenues are difficult or impossible to estimate with
accuracy. Furthermore, because processing of stockpiled material is likely to
occur late in the mine life, the net present value of future revenues is likely to
be small compared with costs incurred at the time of mining and to maintain
the stockpile over time. For this reason, stockpiling low-grade material is often
a strategic decision that takes into account expectations of future increases
in metal prices, benefits associated with lengthening the mine life, and good
management of mineral resources. An example of how cut-off grades can be
estimated can be found in Example 6 in Appendix A.
Special Case: Low-Cost Stockpiles
The previous formulas are of a general nature and apply to stockpiles intended
to be processed in the foreseeable future that are located in specially prepared
areas. Some situations allow low-grade material to be stockpiled on top of
waste dumps with no additional cost. Such stockpiles may or may not be processed at a future date. The utility of stockpiling can then be written:
( )= −( ) + +
−
+
U x M P O
NPV(futurere-handling and processing costs)
NPV(futurerevenues from sales)
stp w w w
The cut-off grade between waste and stockpile is the value of x for which
NPV(futurerevenues from sales) = NPV(futurere-handling and processing costs)
Because sales and stockpile re-handling happen at the same time, discounting can be ignored and the cut-off grade is obtained by setting the
expected revenues from sales equal to the expected re-handling and processing
costs.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Breakeven Cut-off Grade 43
The expected revenues from sales are x ∙ rstp ∙ (Vstp
– R
stp). The cut-off grade
between waste and stockpile is
x = (expected re-handl
⋅ − ( )
ing and processing costs)
r V R c
stp stp stp
Net present values do not enter in this equation. If the assumptions concerning prices, costs, and recoveries that will prevail at the time of processing are
independent of time, the cut-off grade will also be independent of when the
stockpile is processed.
Special Case: High-Cost Waste Dumps
Other situations occur where the cost of maintaining mineralized waste
dumps is as high as that of stockpiling low-grade material for future processing. However, waste dumps must be maintained for life, whereas low-grade
stockpiles will be processed. If the expected life of the stockpile is n years and
C is the yearly cost of maintaining either the stockpile or the waste dump, the
net present value of maintenance costs is*
( ) ( )
( )
= + +
=
P C g i,n C 1 i i
P C g i,n
waste
stp
C g(i,n) is the net present value of a constant cash flow C over n years.
C (1 + i)/i is the net present value of a constant cash flow C to perpetuity. The
cut-off grade between waste and stockpile can be written as follows:
( )
( ) = − + x (expected re-handling a
⋅ −
nd processing costs) C 1 i i
r V R c
stp stp stp
If the assumptions concerning prices, costs, and recoveries that will prevail at
the time of processing are independent of time, the cut-off grade will also be
independent of when the stockpile is processed.
* It was shown earlier that the net present value of a constant cash-flow C over n
years is NPVi
= C g(i,n), where g(i,n) = [1 – (1 + i)–n] (1 + i)/i while the net
present value to perpetuity is C (1 + i)/i.
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44 CHAPTER THREE
C U T- O F F G R A D E A N D O P T I M I Z AT I O N O F
PROCESSING PLANT OPERATING CONDITIONS
In this section a method is developed to optimize a copper mining operation
where mining capacity is fixed, but the capacity of the processing plant can be
changed by changing grind size. Depending on the metallurgical properties of
the ore, using a coarser grind will increase plant throughput while reducing
cost per metric ton processed and decreasing recovery. Conversely, a finer
grind can decrease plant capacity, increase processing cost and recovery.
Mathematical Formulation
The following notations are used in this section:
r = processing plant recovery
V = value of copper contained in concentrate, after deduction for
smelter loss, freight, smelting, and refining costs
Po
= cost per metric ton of ore processed, including overhead
xc
= cut-off grade
T+c = tonnage above cut-off grade to be processed in one year
Q+c = quantity of copper to be processed in one year
x+c = average grade above cut-off grade
Since mining capacity and costs are fixed, the utility function that must
be optimized to estimate the economically optimal grind size is only a function of mill operations and can be written as follows:
() () () = ⋅ ⋅ − ⋅ + + + + + U T Q r T V T P T c c c c o c
where
U(T+c) = utility of running the plant at T+c capacity for one year
r(T+c) = processing plant recovery, if plant capacity is T+c
Po
(T+c) = cost per metric ton of ore processed, if plant capacity is T+c
Q+c is also a function of T+c. Both Q+c and T+c are functions of the cut-off
grade xc
. The optimal plant capacity is that for which U(T+c) reaches a maximum, and is calculated by setting the first derivative of U(T+c) equal to zero:
dU T dT 0
dQ dT r T V P T
Q dr T dT V T dP T dT
c c
c c c o c
c c c c o c c
( )
() ()
( ) ( )
=
= ⋅ ⋅ −
+ ⋅ ⋅ − ⋅
+ +
+ + + +
+ + + + + +
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Breakeven Cut-off Grade 45
If the tonnage processed is changed by a small amount dT+c because of a
small change in cut-off grade xc
, the amount of copper contained is increased
from Q+c = T+c ∙ x+c to Q+c + dQ+c = T+c ∙ x+c + dT+c ∙ xc
. Hence, dQ+c = dT+c
∙ xc
and the optimal plant capacity is T+c such that
() () () ( ) ⋅ ⋅ − + ⋅ ⋅ − ⋅ = + + + + + + + + x r T V P T Q dr T dT V T dP T dT 0 c c o c c c c c o c c
If the recovery r and the processing cost Po
were independent of T+c, this
equation would be easily solved for xc
:
()() [ ] = ⋅
= ⋅ + + x P T r T V P r V c o c c o
In such a situation, the applicable cut-off grade is the mill cut-off grade.
The term Q+c ∙ dr(T+c)/dT+c ∙ V represents the change in the value of the
product sold in one year, which results from the change in recovery. The term
T+c ∙ dPo
(T+c)/dT+c represents the change in operating cost per year, which
results from the change in processing cost per metric ton.
In this formulation of the problem, it was assumed that the value V of
the product sold is independent of the tonnage processed. This may not be
the case if the quality of the concentrate varies with tonnage processed and
head grade. It was also assumed that recovery is only a function of tonnage
processed and is independent of head grade. More complex equations would
apply if these assumptions could not be made.
Example: Optimization of Grinding Circuit in a Copper Mine
This example illustrates how plant capacity can be optimized when mine plans
are fixed; no major change can be made to the processing plant, but the plant
capacity can be increased by changing grind size. Mine production is fixed for
at least one year, and the tonnage, grade, and metal content of copper-bearing
material expected to be mined during this one-year period is as shown in
Table 3-1 and illustrated in Figures 3-14 and 3-15.
The ore is to be processed in a flotation plant. The mill was designed to
operate at the rate of 39.5 million metric tons per year with an average copper
recovery of 95%. Under these conditions, the mill operating costs are $5.24
per metric ton. When mine plans were finalized for the coming year, the
expected value of product sold was $1.00 per pound of copper in concentrate,
and the following mill cut-off grade was used for planning:
( ) = ⋅ ⋅ = x 5.24 0.95 1.00 2,205 0.25% Cu c
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
46 CHAPTER THREE
Table 3-1 Grade–tonnage relationship for the coming year of mining
Cut-off, % Cu
Tonnage,
million metric
tons
Average grade,
% Cu
Copper Content
thousand metric
tons Cu million lb Cu
0.15% 53.7 0.335% 180 397
0.16% 52.6 0.340% 179 395
0.17% 51.4 0.344% 177 390
0.18% 50.1 0.348% 174 384
0.19% 48.8 0.352% 172 378
0.20% 47.5 0.355% 168 372
0.21% 46.0 0.360% 165 365
0.22% 44.4 0.365% 162 357
0.23% 42.8 0.370% 159 349
0.24% 41.2 0.375% 155 341
0.25% 39.5 0.381% 150 332
0.26% 37.7 0.387% 146 322
0.27% 35.9 0.393% 141 311
0.28% 34.1 0.399% 136 300
0.29% 32.1 0.406% 131 288
0.30% 30.2 0.413% 125 275
0.31% 28.2 0.421% 119 262
25
35
30
40
45
55
50
60
0.32
0.36
0.34
0.38
0.40
0.42
0.44
Cut-off Grade, % Cu
0.12 0.16 0.20 0.24 0.28 0.32
Metric Tons of Material
Average Grade
Figure 3-14 Next year expected relationship between tonnage and grade above
cut-off grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Metric Tons of Material Above Cut-off, millions
Average Grade Above Cut-off, % Cu
Breakeven Cut-off Grade 47
As shown in Table 3-1, this cut-off grade implies that the mill feed will
be 39.5 million metric tons averaging 0.381% Cu and containing 332 million
pounds of copper. The value of the material sent to the mill, based on $1.00 per
pound of recoverable copper and excluding mining costs, was expected to be
() () () = ⋅ ⋅ − ⋅
= ⋅ ⋅ − ⋅
=
+ + + + + U T Q r T V T P T
332 0.95 1.00 39.5 5.24
$108 million
c c c c o c
Because of an unexpected increase in copper price, the mining company is
investigating whether short-term changes could be made to the mill feed and
throughput, which would result in increased utility. The copper price is now
expected to be $1.50 per pound of copper in concentrate instead of the $1.00
that was used for planning. The mine plan cannot be changed for at least one
year, and only changes in operating conditions can be made to the processing
plant. One option is to operate the mine and mill as planned while selling
the concentrate at the higher price. The value of the material sent to the mill,
excluding mining costs, would increase from $108 million to
( ) = ⋅ ⋅ − ⋅
=
+ U T 332 0.95 1.50 39.5 5.24
$266 million
c
100
120
140
160
180
200
0.32
0.36
0.34
0.38
0.40
0.42
0.44
Cut-off Grade, % Cu
0.12 0.16 0.20 0.24 0.28 0.32
Metric Tons of
Contained Copper
Average Grade
Figure 3-15 Next year expected relationship between metal content and grade
above cut-off grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Metric Tons of Copper Above Cut-off, thousands
Average Grade Above Cut-off, % Cu
48 CHAPTER THREE
Alternatively, one could consider a decrease in cut-off grade. At $1.50 per
pound of copper in concentrate, the minimum cut-off grade is
( ) = ⋅ ⋅ = x 5.24 0.95 1.50 2,205 0.17% Cu c
Table 3-1 shows that 51.4 million metric tons of ore would be mined
above this cut-off grade, averaging 0.344% Cu. Under current operating conditions, the mill can only process 39.5 million metric tons. The higher-grade
tons could be sent to the mill and the lower-grade tons could be stockpiled.
But such an approach is likely to increase short-term costs without increasing
revenues from concentrate sales. No advantage is taken of the higher copper
price.
Another option would consist of increasing mill throughput by increasing grind size. The result would be a decrease in operating cost per metric ton.
However, this is expected to result in a decrease in mill recovery. It has been
determined that the mill operating costs are 55% fixed costs and 45% inversely
proportional to the tonnage processed:
( ) = + + + P T 2.88 93.1 T o c c
This relationship between operating cost per metric ton and tonnage
processed per year is shown in Figure 3-16. The relationship between copper
recovery and mill throughput is shown in Figure 3-17. This relationship is
represented by the following equation:
() () = − + + + + + r T 0.000232 T 0.01362T 0.7729 c c
2
c
The function to be optimized is
() () () = ⋅ ⋅ − ⋅ + + + + + U T Q r T V T P T c c c c o c
In this equation, Q+c ∙ r(T+c) ∙ V represents the value of copper in concentrate,
and T+c ∙ Po
(T+c) represents the processing costs. The relationship between
U(T+c) and the cut-off grades (which defines T+c) is easily calculated using
Table 3-1 and the three preceding equations. The results are summarized
in Table 3-2 and shown in Figure 3-18. The highest return is $272 million,
$6 million higher than the $266 million calculated previously when plant
capacity was kept at 39.5 million metric tons per year. This highest return is
reached by increasing the plant capacity to approximately 44.4 million metric
tons per year.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Breakeven Cut-off Grade 49
4.00
5.00
4.50
5.50
6.00
6.50
Metric Tons Processed per Year, millions
25 30 35 40 45 50 55 60
Po
(T+c) = 2.88 + 93.1/T+c
Figure 3-16 Relationship between mill operating cost per metric ton and tonnage
processed per year
80
85
90
95
100
Metric Tons Processed per Year, millions
25 30 35 40 45 50 55 60
r(T+c) = –0.000232(T+c)2
+ 0.013624(T+c) + 0.7729
Figure 3-17 Relationship between copper recovery and tonnage processed per year
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Operating Cost per Metric Ton Processed, $ Copper Recovery, %
50 CHAPTER THREE
An alternative method of calculating the optimum processing rate consists of solving the following equation:
( ) = dU T d + + T 0.0 c c
which can be written as
() () () ( ) ⋅ ⋅ − + ⋅ ⋅ − ⋅ = + + + + + + + + x r T V P T Q dr T dT V T dP T dT 0.0 c c o c c c c c o c c
Table 3-2 Calculation of U(T+c) for various cut-off grades and corresponding
tonnages of mill feed T+c
V $/lb $1.50 $1.50 $1.50 $1.50 $1.50 $1.50
xc % Cu 0.20% 0.21% 0.22% 0.23% 0.24% 0.25%
T+c million
metric tons
47.5 46.0 44.4 42.8 41.2 39.5
x+c % Cu 0.355% 0.360% 0.365% 0.370% 0.375% 0.381%
Q+c million
pounds Cu
372 365 357 349 341 332
r(T+c) % 89.65% 90.86% 92.04% 93.09% 94.03% 94.90%
Po
(T+c) $/t $4.84 $4.90 $4.98 $5.06 $5.14 $5.24
Q+c · r(T+c) · V million $/yr $500 $497 $493 $487 $481 $473
–T+c · Po
(T+c) million $/yr ($230) ($226) ($221) ($216) ($212) ($207)
U(T+c) million $/yr $270 $271 $272 $271 $269 $266
200
220
240
260
280
300
Metric Tons Processed T+c, millions
25 30 35 40 45 50 55 60
U(T+c)
Figure 3-18 Relationship between utility U(T+c) and tonnage of mill feed T+c
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Utility of Processing T Metric Tons, $ million +c
Breakeven Cut-off Grade 51
In this equation, xc
∙ r(T+c) ∙ V – Po
(T+c) represents the change in value assuming
that recovery and costs remain constant; Q+c ∙ dr(T+c)/dT+c is attributable to the
change in recovery; –T+c ∙ dPo
(T+c)/dT+c is attributable to the change in costs.
The derivatives of Po
(T+c) and r(T+c) are easily calculated:
() ()
( )
= −
= − ⋅ +
+ + +
+ + +
dP T dT 93.1 T
dr T dT 0.000464 T 0.01362
o c c c
2
c c c
The relationship between dU(T+c)/dT+c and the cut-off grades is easily
calculated using Table 3-2 and the three preceding equations. The results are
summarized in Table 3-3 and plotted in Figure 3-19. The optimal return is
obtained if the tonnage of mill feed is set slightly less than 45 million metric
tons per year, the point where dU(T+c)/dT+c = 0.0 (Figure 3-19). Setting the
cut-off grade at 0.22% Cu will reach this objective, producing 44.4 million
Table 3-3 Calculation of dU(T+c)/dT+c for various cut-off grades and corresponding
tonnages of mill feed T+c
xc % Cu 0.20% 0.21% 0.22% 0.23% 0.24% 0.25%
xc
· r(T+c) · V – Po(T+c) $/t $1.09 $1.41 $1.72 $2.03 $2.32 $2.61
Q+c · dr(T+c)/dT+c · V $/t ($4.70) ($4.23) ($3.74) ($3.27) ($2.81) ($2.34)
–T+c · dPo
(T+c)/dT+c $/t $1.96 $2.02 $2.10 $2.18 $2.26 $2.36
dU(T+c)/dT+c $/t ($1.65) ($0.80) $0.08 $0.94 $1.77 $2.62
($2)
($4)
($6)
($8)
$4
$2
$-
$6
$8
Metric Tons Processed T+c, millions
30 35 40 45 50 55
dU(T+c)/dT+c
Figure 3-19 Relationship between incremental utility dU(T+c)/dT+c and tonnage of
mill feed T+c
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Change in Utility per Additional Metric Tons Processed
52 CHAPTER THREE
metric tons of mill feed (Table 3-2). The average mill head grade will be
0.365% Cu. Increasing the tonnage from 39.5 million metric tons to 44.4 million metric tons will be achieved by decreasing recovery from 95% to 92%.
This loss in recovery will be more than compensated by a decrease in operating
costs from $5.24 to $4.98 per metric ton.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
53
4
Capacity constraints have a direct influence on the cut-off grade. Opportunity costs are associated with each constraint, which implies that the cut-off
grade must be higher than the marginal cut-off grade, if the primary objective
is to maximize net present value. Decisions that are made without fully understanding the effects, direct and indirect, of changing cut-off grades can have
dire consequences. This was the case when very low marginal cut-off grades
were first introduced in low-grade gold leaching operations.
WHE N M A R G I N A L A N A LY S I S N O L O N G E R A P P L I E S :
A GOLD LEACHING OPERATION
In the 1990s, many gold mining companies significantly increased the tonnage
of material placed on their leach pads by lowering the cut-off grade. Marginal
analysis of leaching costs indicated that already low cut-off grades, often less
than 0.5 g/t, could be further reduced, sometimes down to 0.2 g/t. The expectation was that, with more ounces being placed on the leach pad, the amount
of gold recovered would increase on a monthly basis, as well as cumulatively
over time, while the cost per metric ton placed would decrease. The results
initially obtained were often disappointing. The tonnage of material added
by lowering the cut-off grade was large, resulting in a short-term decrease in
recovery, which in the worse cases meant a decrease in revenue instead of the
expected increase. In addition, the long-term impact of adding large tonnages
of very low-grade material to a leach pad was not fully understood. In some
cases, the result seemed to be a decrease in overall pad recovery, not only postponing short-term revenues but showing no increase in cumulative revenues
over the life of the project. On a discounted basis, the benefit of lowering the
cut-off grade was significantly less than expected, if not negative.
To illustrate this point, consider a gold mining operation where the
total tonnage of ore and waste material scheduled to be mined in the coming year was 10 million metric tons. This material was characterized by the
Capacity Constraints
and Opportunity Costs
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54 CHAPTER FOUR
grade–tonnage curve shown in Figure 4-1. Initially, the cut-off grade was set
at 0.50 g/t, which corresponded to 6.59 million metric tons of leach-grade
material averaging 1.36 g/t and containing 288,000 oz of gold. The leach
recovery was expected to be 65%, resulting in the production of 187,000 oz
in the coming year.
A review of the previous year’s operating costs showed that the cut-off
grade could be lowered to 0.40 g/t if the recovery could be maintained at
65%. Laboratory tests confirmed that recovery was independent of grade,
and the decision was made to lower the cut-off grade and add the lower-grade
material to the pad.
After two months of operation, managers realized that the gold production target for the year was not going to be met. If nothing changed, the
amount of gold sold was going to be less than expected before the cut-off
grade was decreased. Management immediately requested a review of the
situation. The results of this review were as follows:
• Metallurgical tests confirmed no decrease in recovery for lower-grade
material.
• Metallurgical tests and review of past operational conditions showed
that the amount of gold recovered was an increasing function of the
solution ratio, defined as the metric tons of cyanide solution used
per metric ton of material placed on the pad. This relationship was as
illustrated in Figure 4-2.
3
4
5
6
7
10
9
8
1.0
1.4
1.2
1.6
1.8
2.0
Cut-off Grade, g/t
0.2 0.3 0.4 0.5 0.6 0.7 0.8
Tonnage 7.51
Tonnage 6.59
Cut-off 0.4 Cut-off 0.5
Average Grade 1.25
Average
Grade 1.36
Figure 4-1 Estimation of tonnage and grade above cut-off grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Metric Tons Above Cut-off Grade, millions
Average Grade Above Cut-off Grade
Capacity Constraints and Opportunity Costs 55
• Provided that a four-month leaching cycle was adhered to, the original solution ratio was 1:1, as needed to reach 65% recovery.
• Lowering the cut-off grade to 0.40 g/t increased the tonnage to
be placed on the pad from 6.59 to 7.51 million metric tons and
decreased the average grade from 1.36 to 1.25 g/t (Figure 4-1). The
ounces placed increased from 288,000 to 302,000 oz, a 5% increase.
• Because no change was made to the amount of solution placed on the
pad, the increase in tonnage from 6.59 to 7.51 million metric tons
resulted in a decrease in solution ratio from 1.0 to 0.88. The expected
recovery should have been 61% instead of 65% (Figure 4-2).
• This 6% decrease in recovery exceeds the expected 5% increase in
ounces placed on the pad. The total metal recovered during the year
should have been expected to decrease from 187,000 to 184,000 oz.
Ignoring the relationship between leach recovery and solution ratio was
equivalent to ignoring a capacity constraint. The corresponding opportunity
cost was ignored, and consequently the cut-off grade was underestimated.
Lowering the cut-off grade to 0.40 g/t might have been justified if a costeffective method of increasing the recovery had been put in place. One option
was to increase the volume of fresh solution placed on the pad, which would
require changes in pond size, pipes, pumps, and the capacity of the carbon
columns or Merrill-Crowe plant used to process the solution. Another option
45
50
55
60
65
70
Solution Ratio
0.60 0.70 0.80 0.90 1.00 1.10
Recovery 65%
Recovery 61%
Ratio 0.88 Ratio 1.0
Figure 4-2 Relationship between leach recovery and solution ratio
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Leach Recovery, %
56 CHAPTER FOUR
was to recycle the pregnant solution on the pad, which would increase the
solution-to-ore ratio without incurring some of the high costs associated
with the first option. All changes to the leach plant had to take into account
constraints imposed by operating permits and other conditions (technical,
environmental, or legal) that would limit the options available to solve the
problem.
Assume that, for environmental and permitting reasons, the size of the
leach plant could not be increased. Which approach should have been used to
determine the optimal cut-off grade? Taking into account the low operating
costs, this optimal cut-off grade was likely to be less than 0.5 g/t (which was
determined on the basis of higher costs) but more than 0.4 g/t (which used
the lower costs but ignored the operating constraint). An iterative approach
could be used that consists of decreasing the cut-off grade by small successive
increments and fully assessing the economic consequences until no further
decrease is justified.
1. Assume that the cut-off grade is lowered from the current 0.50 g/t
to 0.48 g/t.
2. Estimate the increase in tonnage and ounces that will be placed on
the pad as a result of the lower cut-off grade.
3. Calculate the corresponding decrease in solution ratio and leach
recovery.
4. Calculate the resulting change in total gold recovered, taking into
account the increase in gold placed and decrease in recovery.
5. Compare the change in expected gold sold with the corresponding
change in cost of operation. Differences between the cost of wasting
material and placing it on the pad should be taken into account.
6. If the change in revenue from sales exceeds the change in costs, the
cut-off grade can be reduced to 0.48 g/t. The analysis should then be
repeated assuming a lower 0.46 g/t cut-off. The optimum cut-off is
that for which the change in revenue is equal to the change in cost.
C A PA C I T Y C O N S T R A I N T S A N D I N C R E A S E I N C U T- O F F
GRADE
All mining operations are subject to capacity constraints. These constraints
can be in the mine itself, in the processing plant, in the refinery, or in the volume of material that can be sold. A consequence is that if additional material
is added to the currently expected production, this material will postpone
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Capacity Constraints and Opportunity Costs 57
mining, processing, refining, or sale of this production. The net present value
of the currently expected cash flow will be decreased. This decrease, which is
by definition the opportunity cost of adding the new material, must be taken
into account when calculating cut-off grades.
Mathematical Formulation
The mathematical equations that are used to determine opportunity costs
were discussed in chapter 2. They can be summarized as follows. NPVi
is the
net present value of the currently expected cash flow, and t is the time by
which this cash flow will be delayed by adding new material to the production
schedule. The opportunity cost of adding this material is
( ) ( ) = + −
−
U x NPV 1 i 1 opp i
t
The cut-off grade is estimated by comparing the cost of adding one additional metric ton of material to the production schedule, with the value of the
product recoverable from this material. A new metric ton added to the production schedule must pay for all direct costs associated with this ton, and for
the opportunity cost. When t is a very small fraction of one year, as is the case
when only one metric ton of material is being considered, the opportunity
cost is estimated as follows:
( ) = − ⋅ ⋅ U x i t NPV opp i
The time t that is needed to mine, process, or sell one unit of material
is equal to the inverse of the constrained capacity. If the constraint is in the
mine, the capacity is measured in metric tons mined per year, t is the time
needed to mine one metric ton of material, and the opportunity cost is measured in dollars per metric ton mined. This cost must be added to the mining
costs Mo
and Mw. If the constraint is in the mill, t is the time needed to process one metric ton of material, and the opportunity cost must be added to
the processing cost Po
. If the constraint is in the refining capacity—which in
the case of a copper mine is expressed in pounds of copper per year—t is the
time needed to refine one pound of copper, and the opportunity cost must be
added to the refining cost R.
The following equations, defined previously, will also be used in this
section:
Utility of mining 1 t of ore: Uore(x) = x ∙ r ∙ (V – R) – (Mo
+ Po
+ Oo
)
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
58 CHAPTER FOUR
Utility of mining 1 t of waste: Uwaste(x) = –(Mw + Pw + Ow)
Mine cut-off grade: xc
= [(Mo
+ Po
+ Oo
) – (Mw + Pw+ Ow)] / [r ∙ (V – R)]
Mill cut-off grade: xc
= (Mo
+ Po
+ Oo
) / [r ∙ (V – R)]
Cut-off Grade in a Capacity-Constrained Copper Mine
In this section, a copper mine example is used to illustrate the relationship
between capacity constraints, opportunity cost, and cut-off grade. A preliminary feasibility study was completed, which included specific assumptions
concerning the mine, mill, and refinery capacities. The results of the feasibility
study are summarized in Tables 4-1 and 4-2.
Results of Project Feasibility Study
The project is characterized by a set of operational parameters, both technical
and financial, that are summarized in Table 4-1. These parameters are used to
calculate a yearly cash flow, C = $115.68 million, which is assumed to be constant over the ten-year life of the project. Cash flow calculation and project
net present value are summarized in Table 4-2. Given a constant cash flow per
year over ten years (n = 10), and a discount rate of 12% (i = 12%), the project
net present value can be calculated using this formula:
( ) () () = = − +
⋅ + = − NPV C g i,n C 1 1i 1i i 6.328 C i
n
The project net present value is $732.06 million.
Breakeven Cut-off Grades
Assuming no capacity constraint, the utility of sending one metric ton of
material of grade x to the process plant is
( ) ( ) ( ) = ⋅ ⋅ − − + + = − U x x 0.84 2.95 0.75 4.50 9.00 2.20 1.848x 15.70 ore
If one metric ton is sent to the waste dump, the utility is
( ) = −( ) + + = − U x 4.00 0.80 0.65 5.45 waste
The mine and mill breakeven cut-off grades are calculated as follows:
Mine breakeven cut-off grade: xc
= 15.70/(1.848 ∙ 2,205) = 0.385% Cu
Mill breakeven cut-off grade: xc
= (15.70 – 5.45)/(1.848 ∙ 2,205) = 0.252% Cu
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Capacity Constraints and Opportunity Costs 59
Cut-off Grades with Mill Capacity Constraint
If the mill capacity is limited to 50 million metric tons of ore per year, adding
one new metric ton of material to the mill feed will postpone the currently
expected cash flow by t years, where t is the inverse of the mill capacity. The
corresponding opportunity cost is
Uopp(x) = –i∙t∙NPVi
= –0.12 ∙ 732,060,000/50,000,000
= –$1.76 per metric ton processed
The mine and mill cut-off grades are calculated adding this cost to the
processing cost:
Mine cut-off grade: xc
= (15.70 + 1.76)/(1.848 ∙ 2,205) = 0.428% Cu
Mill cut-off grade: xc
= (15.70 + 1.76 – 5.45)/(1.848 ∙ 2,205)
= 0.295% Cu
Table 4-1 Copper mine operating and financial assumptions
General operating conditions
Mine capacity 72,000,000 metric tons mined per year
Mill capacity (flotation) 50,000,000 metric tons processed per year
Refining capacity 480,000,000 pounds of copper refined per year
Average grade 0.52% Cu average grade of ore processed
Fixed costs (unallocated) $100,000,000 $/yr
Variable costs
Mw $4.00 $/waste metric ton mined
Pw $0.80 $/waste metric ton mined
Ow $0.65 $/waste metric ton mined
Mo $4.50 $/ore metric ton mined
Po $9.00 $/ore metric ton mined
Oo $2.20 $/ore metric ton mined
Average grade, recovery, and revenue per pound of copper
x 0.55% Cu average grade of ore mined
r 84% copper recovery (flotation and smelter)
V $2.95 copper price per pound of recovered copper
R $0.75 freight and smelting cost per pound of
recovered copper
Discount rate and mine life
i 12% discount rate
n 10 mine life (years)
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
60 CHAPTER FOUR
To compensate for the mill opportunity cost, both the mine and mill cut-off
grades must be increased by 0.043% Cu.
Cut-Off Grades with Mine Capacity Constraint
If the mine capacity is limited to 72 million metric tons of ore per year, mining one new metric ton of material that was not scheduled to be mined will
postpone the currently expected cash flow by t years, where t is the inverse of
the mine capacity. The corresponding opportunity cost is
Uopp(x) = –i∙t∙NPVi
= –0.12 ∙ 732,060,000/72,000,000
= –$1.22 per metric ton mined
The mine and mill cut-off grades are calculated adding this cost to the
mining cost:
Table 4-2 Yearly cash flow and net present value of copper project
Yearly cash flow
Metric tons mined 72 million metric tons per year
Metric tons ore 50 million metric tons per year
Metric tons waste 22 million metric tons per year
Cost per metric ton ore $15.70 $/t mined and processed
Cost per metric ton waste $5.45 $/t mined and wasted
Cost per year ore $785.00 million $/yr
Cost per year waste $119.90 million $/yr
Total operating cost $904.90 million $/yr
Fixed cost per year $100.00 million $/yr
Total cost per year $1,004.90 million $/yr
Ore grade 0.55% Cu
Copper contained 606.38 million lb Cu/yr
Copper recovered 509.36 million lb Cu/yr
Revenue per pound sold $2.20 $/lb
Revenue from sales $1,120.58 million $/yr
Net cash flow $115.68 million $/yr (C)
Net present value
Discount rate 12% %/yr (i)
Mine life 10 years (n)
NPV factor g(i,n) 6.328 g(i,n) = [1 – (1 + i)–n] · (1 + i)/i
Net present value $732.06 NPVi
= C g(i,n)
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Capacity Constraints and Opportunity Costs 61
Mine cut-off grade: xc
= (15.70 + 1.22)/(1.848 ∙ 2,205) = 0.415% Cu
Mill cut-off grade: xc
= [(15.70 + 1.22) – (5.45 + 1.22)]/(1.848 ∙ 2,205)
= 0.252% Cu
The mill breakeven cut-off grade is equal to the marginal cut-off grade.
The reason is that the cost of processing one metric ton of material after it has
been mined is independent of the mining cost.
Cut-off Grades with Refinery Capacity Constraint
If the refinery has a limited capacity of 500 million pounds of copper per
year, adding one more pound of copper will postpone the currently expected
copper production by t years, where t is the inverse of the refinery capacity.
The corresponding opportunity cost is
Uopp(x) = –i∙t∙NPVi
= –0.12 ∙ 732,060,000/500,000,000
= –$0.176 per pound refined
The mine and mill cut-off grades are calculated adding this cost to the
cost per pound:
Mine cut-off grade: xc
= 15.70/[0.84 ∙ (2.95 – 0.75 – 0.176) ∙ 2,205]
= 0.419% Cu
Mill cut-off grade: xc
= (15.70 – 5.45)/[0.84 ∙ (2.95 – 0.75 – 0.176) ∙ 2,205]
= 0.273% Cu
To compensate for the refinery opportunity cost, the mine and mill cut-off
grades must both be increased by the same percentage: (2.95 – 0.75)/(2.95 –
0.75 – 0.176) = 8.7%.
D E C R E A S I N G C U T- O F F G R A D E O V E R T I M E :
A STRATEGIC OBJECTIVE
In most situations, the expected net present value of future cash flows
decreases over time. When the project approaches the end of its life, little
material remains to be mined and the net present value of future cash flows
approaches zero, or it may become negative as reclamation costs exceed generated cash flows.
Consider the copper mine described previously. The yearly cash flow was
expected to be constant at $115,680,000 per year. Table 4-3 shows how the
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
62 CHAPTER FOUR
net present value of future cash flows should be calculated for the first three
years of the mine life. In year 0, this NPV is $732.05 million; in year 1, it is
$690.34 million; in year 2, it is $643.62 million. In year 9, the last year of
operation, the NPV is equal to a one-year undiscounted cash flow, $115.68
million. In year 10, there is no production and the cash flow is zero. Figure 4-3
shows the relationship between the NPV of future cash flows and the year
when this NPV is calculated.
As the NPV of future cash flows decreases, the opportunity cost decreases
and so does the cut-off grade. The relationships between NPVi
, the opportunity cost i∙t∙NPVi
, and the mill and mine cut-off grades are calculated in
Table 4-4. The capacity constraints are assumed to be the same throughout
the mine life:
• Mill capacity: 50 million metric tons processed per year
• Mine capacity: 72 million metric tons mined per year
• Refinery capacity: 500 million lb of copper per year
The cut-off grades are estimated using the equations developed earlier:
• If the mill is capacity constrained, t = 1/50,000,000 yr/t and
Mine cut-off grade: xc
= (15.70 + i∙t∙NPVi
)/(1.848 ∙ 2,205)
Mill cut-off grade: xc
= (15.70 + i∙t∙NPVi
– 5.45)/(1.848 ∙ 2,205)
Table 4-3 Calculation of remaining net present value in years 0 to 3
Project
Year
Year when remaining NPVi
is calculated (i = 12%)
0 1 2 3
Remaining
Cash Flow
Discount
Factor
Remaining
Cash Flow
Discount
Factor
Remaining
Cash Flow
Discount
Factor
Remaining
Cash Flow
Discount
Factor
0 115.68 1.000
1 115.68 0.893 115.68 1.000
2 115.68 0.797 115.68 0.893 115.68 1.000
3 115.68 0.712 115.68 0.797 115.68 0.893 115.68 1.000
4 115.68 0.636 115.68 0.712 115.68 0.797 115.68 0.893
5 115.68 0.567 115.68 0.636 115.68 0.712 115.68 0.797
6 115.68 0.507 115.68 0.567 115.68 0.636 115.68 0.712
7 115.68 0.452 115.68 0.507 115.68 0.567 115.68 0.636
8 115.68 0.404 115.68 0.452 115.68 0.507 115.68 0.567
9 115.68 0.361 115.68 0.404 115.68 0.452 115.68 0.507
10 0 0 0 0
NPVi $732.05 $690.34 $643.62 $591.29
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Capacity Constraints and Opportunity Costs 63
• If the mine is capacity constrained, t = 1/72,000,000 yr/t and
Mine cut-off grade: xc
= (15.70 + i∙t∙NPVi
)/(1.848 ∙ 2,205)
Mill cut-off grade: xc
= (15.70 – 5.45)/(1.848 ∙ 2,205)
• If the smelter is capacity constrained, t = 1/500,000,000 yr/lb and
Mine cut-off grade:
xc
= 15.70/[0.84 ∙ (2.95 – 0.75 – i∙t∙NPVi
) ∙ 2,205]
Mill cut-off grade:
xc
= (15.70 – 5.45)/[0.84 ∙ (2.95 – 0.75 – i∙t∙NPVi
) ∙ 2,205]
Figure 4-4 shows how the mine cut-off grade changes in function of the
year when it is calculated, depending on whether constraints are on mine,
mill, or refinery capacity. Figure 4-5 shows the same information for the mill
cut-off grade. In this example, the mill capacity constraint is that which has
the highest cost, as measured by the amount of copper needed to maintain the
project net present value.
CUT-OFF GRADE BELOW MARGINAL CUT-OFF GRADE
Situations arise when it is justified to use a cut-off grade below the marginal
cut-off grade. At the end of the mine life, the net present value of future
cash flows may be negative, when reclamation costs are exceeding expected
0
700
600
500
400
300
200
100
800
Project Year When NPV Is Calculated
0 1 2 3 4 5 6 7 8 9 10
Figure 4-3 Relationship between NPV of future cash flow and year when NPV is
calculated
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. NPV of Future Cash Flow, $
64 CHAPTER FOUR
revenues from operations. The opportunity cost changes sign from negative to
positive: postponing expenditures increases the remaining project net present
value. A cut-off grade below the marginal cut-off grade may be justified, provided the loss incurred in mining and processing this material is less than the
benefit of postponing reclamation expenditures.
At the end of the mine life, if CR is the expected reclamation cost, the
net present value of this cost is –CR. If reclamation is postponed by one year,
this net present value is increased from –CR to –CR/(1 + i). The opportunity
cost is
[ ] () () − + = + C 1 1 1 i C i 1 i R R
The cut-off grade that can be used to postpone reclamation by one year
can be below the marginal cut-off grade. The only requirement is that the cash
flow C generated by mining low-grade material during the last year, added to
the corresponding opportunity, is positive:
( )
( )
+ + >
> − +
C C i 1 i 0
C C i 1 i
R
R
The cash flow C can be negative. If the cost of reclamation is $15 million and
i = 10%, the maximum loss that can be justified to postpone reclamation by
one year is 15 ∙ (0.1/1.1) = $1.36 million.
Table 4-4 Calculation of opportunity cost and cut-off grade per year
Capacity
Constraint
Mill Constraint, 50 million
metric tons processed
Mine Constraint, 72 million
metric tons mined
Refinery Constraint,
500 million lb copper
Year
NPVi
, $
million
Opportunity
Cost, $
Cut-off
Grade, % Cu Opportunity
Cost, $
Cut-off
Grade, % Cu Opportunity
Cost, $
Cut-off
Grade, % Cu
Mine Mill Mine Mill Mine Mill
0 732 1.76 0.43% 0.29% 1.22 0.42% 0.25% 0.18 0.42% 0.27%
1 690 1.66 0.43% 0.29% 1.15 0.41% 0.25% 0.17 0.42% 0.27%
2 644 1.54 0.42% 0.29% 1.07 0.41% 0.25% 0.15 0.41% 0.27%
3 591 1.42 0.42% 0.29% 0.99 0.41% 0.25% 0.14 0.41% 0.27%
4 533 1.28 0.42% 0.28% 0.89 0.41% 0.25% 0.13 0.41% 0.27%
5 467 1.12 0.41% 0.28% 0.78 0.40% 0.25% 0.11 0.41% 0.27%
6 394 0.94 0.41% 0.27% 0.66 0.40% 0.25% 0.09 0.40% 0.26%
7 311 0.75 0.40% 0.27% 0.52 0.40% 0.25% 0.07 0.40% 0.26%
8 219 0.53 0.40% 0.26% 0.36 0.39% 0.25% 0.05 0.39% 0.26%
9 116 0.28 0.39% 0.26% 0.19 0.39% 0.25% 0.03 0.39% 0.25%
10 0 0.00 0.39% 0.25% 0.00 0.39% 0.25% 0.00 0.39% 0.25%
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Capacity Constraints and Opportunity Costs 65
Postponing reclamation costs is justified if maximizing net present value
is the only objective. Other financial, legal, environmental, and socioeconomic factors may be taken into account that will influence the decision
when to close the mine. Other circumstances occur where using a cut-off
grade below the marginal cut-off grade is justified. This may be the case when
the tonnage of material exceeding the marginal cut-off grade is less than the
0.38
0.43
0.42
0.41
0.40
0.39
Project Year
0 1 2 3 4 5 6 7 8 9 10
No Constraint
Mine Constraint
Mill Constraint
Refinery Constraint
Figure 4-4 Relationship between mine cut-off grade and project year
0.24
0.30
0.29
0.28
0.27
0.25
0.26
Project Year
0 1 2 3 4 5 6 7 8 9 10
No Constraint
Mine Constraint
Mill Constraint
Refinery Constraint
Figure 4-5 Relationship between mill cut-off grade and project year
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Mine Cut-off Grade, % Mill Cut-off Grade, %
66 CHAPTER FOUR
plant capacity. Several options must then be considered, which have different
technical and financial consequences:
• Run the plant below capacity. This will increase the cost per metric
ton processed. In some circumstances, higher recovery is achievable
when reducing the mill throughput. How to optimize plant capacity
was discussed previously.
• Run the plant as a batch plant, with periodic shutdowns. The cost of
shutdowns must be considered to optimize cut-off grade.
• Run the plant at capacity using a cut-off grade below the marginal
cut-off grade. If the tonnage needed to fill the plant is relatively small,
this option is likely to be the best one.
CUT-OFF GRADE OPTIMIZATION WITH O P P O R T U N I T Y
COSTS: PRACTICAL CONSIDERATIONS
The formula Uopp(x) = –i∙t∙NPVi
is useful to determine whether cut-off grades
and net present value have been optimized. The cut-off grade calculated using
opportunity costs must be compared with that currently used in the mine
plan. If the former is higher than the latter, consideration should be given to
increasing the cut-off grade. This may be possible by increasing mine capacity
or changing plant capacity. Conversely, if the planned cut-off grade is lower
than the cut-off grade calculated using the opportunity cost, indications are
that facilities might have been overdesigned. Constraints imposed by the
geology of the deposit have a major influence on the determination of cut-off
grades and optimum mine and mill capacities. This influence will be discussed
in Chapter 5.
Cut-off grades calculated from cash flows that have not been optimized
are also not optimal. An iterative approach must be used to maximize the
net present value. For example, one could first calculate a cash flow using a
fixed cut-off grade such as the marginal cut-off grade. From this cash flow,
cut-off grades could be reestimated using opportunity costs. But new cut-off
grades imply new mine plans, new cash flows, and therefore new opportunity
costs, which must be used to, once again, reestimate the cut-off grades. This
lengthy process must be repeated until the net present value is optimized.
Fortunately, algorithms have been developed and continue to be improved
to facilitate simultaneous optimization of mine plans, production schedules,
and material allocation, with implied optimization of cut-off grade strategies
(see bibliography). Computer programs are available that render complex
theoretical solutions accessible to mining engineers and other practitioners.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Capacity Constraints and Opportunity Costs 67
While solutions applicable to open pit environments are more advanced,
underground mines are given increasing attention.
Before changing the cut-off grade, all costs and benefits likely to result
from this change must be carefully examined. Complex relationships occur
between the space-dependent (and sometimes time-dependent) geological
and geotechnical properties of the deposit, the time-dependent economic
variables (capital and operating costs, metal prices, environmental and socioeconomic impact), and technical constraints, which, to some extent, can be
controlled (mining and processing methods, operational capacity). These
factors must all be taken into account to optimize cut-off grades, yearly
production, and cash flows. No simple solutions exist for this complex multidimensional optimization problem.
Cut-off grades that were estimated to be optimal at the time the original
mine plan was developed must be continuously reexamined. Current and
expected costs and prices, mine and mill performance, and environmental
and socioeconomic conditions will change over time, resulting in changes in
future cash flow and opportunity costs. Maximizing net present value tends
to give no value to actions where consequences will only be felt at the end
of the mine life. For example, actions may have to be taken throughout the
life of a project to minimize future costs of reclamation and environmental
compliance. The cost of these actions may be significant from a net present
value point of view, but the resulting savings, which will be incurred at the
end of the mine life, may have no impact on the net present value. Similarly,
stockpiling low-grade material may increase costs throughout the mine life,
but revenues resulting from processing these stockpiles will only be realized
at the end of the mine life. Maximizing net present value should never be the
sole guide to decision making.
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Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
69
5
As mentioned previously, constraints imposed by the geology of the deposit
play a critical role in defining the optimal cut-off grade. The tonnage and
grade of material that can be made available for processing is continuously
changing during the life of the mine. The influence of geologic constraints is
analyzed in conjunction with other constraints such as those on mine or mill
capacity, and on volume of sales.
CUT-OFF GRADE WHE N P R O C E S S I N G C A PA C I T Y
IS FIXE D
Ideally, a new mine should be designed such that mining capacity and processing capacity are perfectly balanced and the planned cut-off grades are optimum given the expected cash flow. In practice, this situation occurs only on
paper, when the project is designed. As soon as operations start, imbalances
invariably appear. The actual processing plant capacity exceeds or falls below
that expected. The mining capacity is higher or lower than planned. Mine and
mill capacities are no longer balanced, new constraints appear, and the cutoff grade must be changed accordingly. The cut-off grade must also take into
account differences between expected and actual costs, productivities, recoveries, and market value of product sold. When a new project is designed, mine
and mill capacities and corresponding cut-off grades are chosen primarily to
optimize financial objectives. Once mine and mill facilities are built, physical
constraints become the main drivers and studies must be completed to determine whether removing these constraints is financially justified.
Relationship Between Mine Capacity and Cut-off Grade
In this section, it will be assumed that the capacity of the processing plant is
fixed and cannot be changed. The only change that can be made is to the mining capacity. What is the impact of a change in mining capacity on the cut-off
grade and the grade of the material sent to the plant?
Geologic Constraints
and Opportunity Costs
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70 CHAPTER FIVE
• Consider an increase in mining capacity, defined as tonnage mined
per year.
• This increase requires an increase in mining capital cost, and is likely
to result in an increase in total mine operating costs per year. However, it is also likely to result in decreased mining and overhead costs
per metric ton mined.
• Given that the processing capacity is fixed, the cut-off grade must be
increased to keep the tonnage sent to the mill constant. The average
grade of mill feed will increase and so will the quantity of product
sold.
• The mine life will decrease.
• In some instances, the lower-grade material, which is not processed,
will be stockpiled. Stockpiling of low-grade material was discussed
previously.
To decide whether an increase in mining capacity is justified, the expected
net impact on the utility of the project must be assessed, taking into account
the following factors:
• Increased capital cost of new mining capacity
• Decreased mine unit operating cost
• Increased plant head grade and increased metal sales per year
• Loss of low-grade material or delayed processing of some of this
material
• Reduced mine life and resulting socioeconomic and political impact
• Reduced project life and decreased political risk, if applicable
• Change in environmental impact
A simple example follows. Consider a mining operation in which the
plant was designed to process an average of 250,000 metric tons per month, or
3 million metric tons per year. The grade–tonnage relationship corresponding
to the mineralized material expected to be mined during the coming year is
shown in Figure 5-1. At the current mining capacity, the 3 million metric ton
plant capacity is consistent with a cut-off grade of 0.74 g/t and a mill feed
average grade of 1.56 g/t.
Consideration is being given to increasing the mining capacity by 50%,
and the impact such a change would have on the coming year is being investigated. If the mining capacity is increased by 50%, the material currently scheduled to be mined in one year will be mined in eight months. Since the mill
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Geologic Constraints and Opportunity Costs 71
can process only 250,000 metric tons a month, it will only consume 2 million
metric tons during this eight-month period. This tonnage corresponds to a
cut-off grade of 1.03 g/t and an average mill feed head grade of 1.90 g/t (Figure 5-1). Consideration should be given to stockpiling the material between
1.03 g/t and a cut-off grade somewhat higher than 0.74 g/t. This material
should be considered for re-handling and processing at a later date.
The proposed 50% increase in mining capacity may or may not be
optimal. To be economically justified, an increase in mining capacity must
take into account financial, technical, environmental, permitting, and other
constraints imposed by deposit size and shape, mining method, size of equipment, safety and environmental regulations, and other parameters. Depending on the limitations imposed by these constraints, an iterative approach is
best suited to mining capacity optimization. Such an approach can consist of
the following steps:
1. Assume a 1 million metric ton increase in mining capacity (or some
other increase that is technically achievable).
2. Calculate the resulting decrease in mine life.
3. Estimate the increase in cut-off grade and resulting higher mill head
grade that is consistent with the increase in mining capacity and fixed
processing capacity.
4. Estimate the increase in mine capital and yearly operating costs
needed to increase the mining capacity. Calculate the corresponding
0
4
3
2
1
5
6
1.0
1.4
1.2
1.6
1.8
2.0
2.2
2.4
Cut-off Grade
0.5 0.6 0.7 0.8 0.9 1.0 1.1 1.2
Tonnage Above
Cut-off Grade
Average Grade Above
Cut-off Grade
Average 1.90
Average 1.56
Cut-off 1.03 Cut-off 0.74
Tonnage 3.0
Tonnage 2.0
Figure 5-1 Estimation of cut-off grade assuming fixed processing capacity
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Tonnage Above Cut-off Grade
Average Grade Above Cut-off Grade
72 CHAPTER FIVE
discounted incremental mining costs (DIMC) for the remaining life
of the project.
5. Estimate the increase in mill production per year (units of product
sold) and calculate the corresponding discounted incremental revenues (DIR).
6. If low-grade material is to be stockpiled, the net present value of this
material should also be taken into account.
7. If the DIR exceed the DIMC, this analysis should be repeated assuming an additional 1-million-metric-ton increase in mining capacity.
8. The optimal mining capacity is that for which DIR equals DIMC.
In this previous discussion, it was assumed that the increase in mine
capacity could be achieved without changing mine selectivity. The grade–
tonnage curve did not change. The volumes being mined remained the
same, but these volumes were mined faster. This situation will occur if more
equipment of the same size is added to an open pit mine with no change to
the pit design, or if more stopes are put in production simultaneously without changing the underground mining method or the stope design. Some
situations occur where the assumptions of constant grade–tonnage curve
cannot be made. In open pit mines, larger trucks and loading equipment,
increased bench height, and wider spacing between blast holes can be used
to increase capacity. The result is a decrease in selectivity, resulting in a new
grade–tonnage curve. Similarly, underground production can be increased by
using a different mining method, which may result in lower selectivity joined
with significantly lower costs per metric ton. The impact of selectivity on the
grade–tonnage curve, the cut-off grade, and the mill feed average grade will
be discussed at the end of Chapter 6. Increasing the mining capacity will not
necessarily result in a higher head grade if this increase is realized by significantly decreasing mine selectivity.
Using Opportunity Cost as a Guide to Mine Capacity Optimization
The approach to mine capacity optimization previously described can be
extremely time-consuming. An alternative approach is presented here, which
can be used to rapidly converge toward the desired solution, provided there is
little variability in the geologic properties of the deposit being mined.
Consider an open pit gold mine operating under the following conditions:
• Total tonnage mined: T1
= 4.5 million t/yr
• Waste mined: Tw1 = 1.5 million t/yr
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Geologic Constraints and Opportunity Costs 73
• Ore mined and processed: T+c1 = 3.0 million t/yr
• Cut-off grade: xc1 = 0.74 g/t
• Average grade above cut-off: x+c1 = 1.56 g/t
Costs associated with waste material:
• Mw = $3.50 per metric ton of waste
• Pw = $0 per metric ton of waste
• Ow = $0.88 per metric ton of waste
Costs associated with processed material:
• Mo
= $3.20 per metric ton of ore
• Po
= $15.00 per metric ton of ore
• Oo
= $4.55 per metric ton of ore
• Plant recovery: r = 87%
• Gold price: V = $1,400 per ounce of gold (1 troy ounce = 31.1035 g)
• Cost of sales: R = $50 per ounce of gold
The grade–tonnage curves representing one year of production are shown
in Figure 5-2. The marginal cut-off grades are as follows:
Mill marginal
cut-off grade:
[ ] ( ) ( ) ( ) = + + − + +
−
=
x M P O M P O r V R 31.1035
0.49 g/t
c o o o w w w
Mine marginal
cut-off grade:
[ ] ( ) ( ) = + + −
=
x M P O r V R 31.1035
0.60 g/t
c o o o
These marginal cut-off grades are significantly lower than the 0.74 g/t
cut-off grade used in the current operation. The difference reflects constraints
imposed by the plant’s capacity.
The total tonnage available for mining is 22.5 million metric tons. The
deposit will be mined out during the five-year life of the mine. Because of low
variability in the deposit geology, the yearly cash flow (YCF) is expected to
be constant over a five-year mine life. This cash flow is estimated as follows:
( ) ( ) ( ) = − − + + − + +
=
+ + + YCF T x r V R T M P O T M P O
$102 million per year
1 c1 c1 c1 o o o w1 w w w
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
74 CHAPTER FIVE
The net present value of this cash flow, calculated at a discount rate
i = 10%, and a five-year mine life is NPVi1 = $425 million. The opportunity
cost of the mill capacity constraint is i∙t∙NPVi1 = 0.10 ∙ 425/4.5 = $9.44 per
metric ton processed, which is equivalent to 9.44 ∙ 31.1035/[0.87 ∙ (1,400 –
50)] = 0.25 g/t. When taking the opportunity cost into consideration, the
mill cut-off grade is raised from 0.49 g/t to 0.74 g/t, which happens to be the
cut-off grade used in the current mine plan.
Consideration is being given to increasing mine capacity by 25%, from
4.5 to 5.625 million metric tons a year, thus reducing the mine life from five
to four years. The mill capacity remains the same, at 3 million metric tons a
year. The amount of waste material is increased from 1.5 million metric tons
to 2.625 million metric tons, calculated as follows:
• Total tonnage mined: T2
= 5.625 million t/yr
• Ore mined and processed: T+c2 = 3.0 million t/yr
• Waste mined: Tw2 = 2.625 million t/yr
The tonnage-grade curves that represent current (4.5 million metric tons)
and proposed (5.625 million metric tons) yearly production are shown in Figure 5-3. The proposed tonnage curve is obtained by multiplying the current
one by 1.25. The proposed grade curve is identical to the current one. From
these curves, one gets the cut-off grade to be used to fill the plant, and the
average grade above cut-off grade is as follows:
• Cut-off grade: xc2 = 0.90 g/t
1
4
4.5
3
3.5
2.5
2
1.5
5
1.2
1.5
1.4
1.3
1.6
1.7
1.8
1.9
2.0
2.1
Cut-off Grade
0.6 0.65 0.7 0.75 0.8 0.85 0.9 0.95 1 1.05 1.1
Tonnage Above
Cut-off Grade
Average Grade Above
Cut-off Grade
Average Grade 1.56 g/t
Cut-off Grade 0.74 g/t
3 Million
Metric Tons
Figure 5-2 Grade–tonnage curves for material mined in one year at 4.5 t/yr
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Tonnage Above Cut-off Grade
Average Grade Above Cut-off Grade
Geologic Constraints and Opportunity Costs 75
• Average grade above cut-off: x+c2 = 1.75 g/t
Assuming that the costs per metric ton remain the same, the proposed
yearly cash flow is estimated at
( ) ( ) ( ) = − − + + − + +
=
+ + + YCF T x r V R T M P O T M P O
$119 million per year
2 c2 c2 c2 o o o w 2 w w w
As a result of a higher head grade, this yearly cash flow is significantly
higher than the $102 million currently expected. The net present value of this
cash flow, calculated at a discount rate i =10% and a reduced life of four years
is NPVi2 = $415 million. This net present value is less than the $425 million
estimated at the current mining rate. The reason is that the life of the project
has been reduced from five years to four. The difference in net present value
would be even more significant if, as it should be, the cost of expanding the
mine capacity was taken into account. This cost would occur in year 0 and
would not be discounted.
The marginal cut-off grades are significantly lower than the cut-off grades
used to fill the plant. This is more so when the mine capacity is increased.
The net present value of both scenarios would be significantly improved
if low-grade material was stockpiled and processed at the end of the mine
life, after mining is completed and the higher-grade material has been processed. More low-grade material is available for stockpiling when the mine
1
4
4.5
3
3.5
2.5
2
1.5
5
1.2
1.5
1.4
1.3
1.6
1.7
1.8
1.9
2.0
2.1
Cut-off Grade
0.6 0.65 0.7 0.75 0.8 0.85 0.9 0.95 1 1.05 1.1
Tonnage Above
Cut-off Grade with
25% Increase in
Mine Capacity
Average Grade Above
Cut-off Grade
New Average
Grade 1.75 g/t
Current Average
Grade 1.56 g/t
New Cut-off
Grade 0.90 g/t
Current Cut-off
Grade 0.74 g/t
3 Million
Metric Tons
Processed
3.75 Million
Current Tonnage Above
Cut-off Grade
Figure 5-3 Current and proposed grade–tonnage curves for material mined in one
year
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Average Grade Above Cut-off Grade
76 CHAPTER FIVE
capacity is increased, and stockpiling will have a greater economic impact in
this situation.
Alternative mine plans should be considered, all of which should include
a stockpiling option. One alternative is to lower the mine capacity and therefore the mill head grade, thus increasing the mine life but decreasing the
yearly cash flow. Another option, if feasible, would consist of increasing the
mill capacity. The optimal solution is likely to be that where declining cut-off
grades are used, starting with 0.74 g/t during the current year and reaching
0.49 g/t at the end of the mine life.
CUT-OFF GRADE WHEN MINING CAPACITY IS FIXE D
In the previous analysis, a fixed processing capacity was assumed to be the case.
Now consider the situation where the mining capacity is fixed but an increase
in plant capacity is being proposed. A lower cut-off grade is needed to balance
the mining capacity with the plant capacity. Increasing the mill capacity has
the following impacts:
• The tonnage processed per year is increased.
• The tonnage mined is not changed. The cut-off grade must be
decreased to keep the processing plant full.
• The average grade of material sent to the mill decreases, but the metal
content of this material increases.
• More metal is recovered, resulting in higher revenues from sales.
• The capital cost of plant expansion must be taken into account.
• The plant operating costs are likely to increase per unit of time (cost
per year) but should decrease per unit of production (cost per metric
ton processed).
The optimal plant capacity is that which maximizes the total utility of the
project, taking into account financial impact (increased capital cost, decreased
unit operating cost, increased revenue from sales), as well as socioeconomic,
environmental, political, and other impacts.
For example, consider a mining operation in which the plant was
designed to process an average of 250,000 metric tons per month, or 3 million
metric tons per year. The grade–tonnage relationship corresponding to the
mineralized material expected to be mined at the current capacity is shown
in Figure 5-4. At the current mining capacity, this plant capacity is consistent
with a cut-off grade of 0.74 g/t, corresponding to a mill feed average grade of
1.56 g/t.
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Geologic Constraints and Opportunity Costs 77
Management is considering increasing the size of the processing plant by
20% and investigating the impact that such a change would have on the coming year. If the processing capacity is increased by 20% and the mining capacity is kept constant, the cut-off grade must be decreased to 0.61 g/t to supply
3.6 million metric tons to the mill (Figure 5-4), and the average grade of mill
feed will decrease to 1.41 g/t. The gold content of the material processed will
increase from 2.51 million oz to 2.73 million oz. This cut-off grade calculation only takes into account capacity constraints and is independent of the
economics of the project. The increase in plant capacity must be justified not
only by the increase in material processed, but also taking into account capital
cost requirements, possible changes (increase or decrease) in recovery, a likely
decrease in operating costs, and all other direct and indirect costs and benefits.
The proposed 20% increase in processing capacity may or may not be
optimal. To be economically justified, an increase in plant capacity must take
into account financial, technical, environmental, permitting, and other constraints imposed by the size of the available processing equipment, limitations
on tailings dam expansion, maximum permitted dust emission, and other
parameters. Depending on the limitations imposed by these constraints, an
iterative approach is best suited to plant capacity optimization. This approach
can consist of the following steps:
1. Assume a 1-million-metric-ton increase in processing capacity (or
some other increase that is technically achievable).
0
4
3
2
1
6
5
1.0
1.4
1.2
1.6
1.8
2.0
2.2
2.4
Cut-off Grade
0.5 0.6 0.7 0.8 0.9 1 1.1 1.2
Tonnage 3.6
Tonnage 3.0
Cut-off 0.61 Cut-off 0.74
Average 1.56
Average Grade 1.41
Figure 5-4 Estimation of cut-off grade assuming fixed mining capacity
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Tonnage Above Cut-off Grade
Average Grade Above Cut-off Grade
78 CHAPTER FIVE
2. Estimate the decrease in cut-off grade and resulting lower mill head
grade that is consistent with the fixed mining capacity and higher
processing capacity.
3. Estimate the increase in mill capital and yearly operating costs needed
to increase the processing capacity. Calculate the corresponding discounted incremental processing cost (DIPC) for the remaining life
of the project.
4. Estimate the increase in mill production per year (units of product
sold) and calculate the corresponding discounted incremental revenue (DIR).
5. If DIR exceeds DIPC, this analysis should be repeated, assuming an
additional 1-million-metric-ton increase in processing capacity.
6. The optimal processing capacity is that for which DIR equals DIPC.
CUT-OFF GRADE WHEN VOLUME OF SALES IS FIXE D
In this analysis, it is assumed that the volume of sales is fixed. This may be
because all products are sold under contracts that specify the volume that will
be bought on a yearly basis. Perhaps the market is small and the amount of
product that can be sold is limited. Or it might be that management specifies
the amount to be produced from a given operation for reasons external to the
operation under consideration.
Fixed Sales with No Mining or Processing Constraint
In this example it is assumed that the recovery achieved in the processing
plant is independent of tonnage processed and plant head grade. In such a
situation, requiring a fixed volume of sales is equivalent to requiring a fixed
quantity of metal (or other salable product) delivered by the mine to the
processing plant. This quantity Q+c is equal to the tonnage delivered T+c multiplied by the average grade of plant feed x+c:
+ + = ⋅ + Q T c c x c
Consider a gold mining operation that has been requested to supply 4 t of
gold (130,000 oz) to the processing plant over a one-year period (Q+c = 4.0 t
of gold). Consider three scenarios:
1. There is no constraint on either mine or plant capacity. This is usually
the case only during the feasibility study.
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Geologic Constraints and Opportunity Costs 79
2. The mine capacity is fixed, but the plant capacity is not.
3. The plant capacity is fixed, but the mine capacity is not.
If neither the mine nor the processing plant is capacity constrained, the
number of possible cut-off grades is theoretically infinite. A high cut-off grade
will result in a high average grade above cut-off grade x+c. The higher the cutoff grade, the lower the capacity T+c of the processing plant that is needed to
keep sales at the required level. But in the case of an open pit mine, a higher
cut-off grade will require mining more metric tons per year. In the case of
an underground mine, smaller stopes may have to be designed to eliminate
peripheral low-grade material, and low-grade stopes may have to be rejected.
When neither mine nor plant capacity is fixed, cut-off grade optimization requires analysis of several feasible solutions: low cut-off grade and large
plant size or high cut-off grade and smaller plant size. Technical constraints,
including constraints imposed by the geology of the deposit, will reduce the
number of feasible options. Higher cut-off grades will result in lower capital
costs for the plant and likely higher operating costs, while the impact on mine
capital and operating costs will be a function of the geological properties of
the deposit and the applicable mining methods. Cut-off grade optimization
requires estimation of capital and operating costs and cash flow analysis for
each feasible solution.
Fixed Sales and Fixed Processing Rate with No Mining Constraint
Cut-off grade determination becomes easier if, in addition to the constraint
on the amount of metal processed, one adds a constraint on either plant or
mine capacity. First assume that the plant capacity, defined as tonnage processed per year, is fixed. With both tonnage processed T+c and metal content
Q+c being fixed, the plant head grade x+c is calculated as follows:
= + + + x Q T c c c
If it is known what material can be mined in the coming months, one can
determine the cut-off grade needed to reach the necessary average grade and
the mining rate needed to reach the necessary tonnage of mill feed T+c.
Consider the gold mine that was asked to supply 4 t of gold to the processing plant during the coming year. In addition, assume that the capacity of
the processing plant is fixed at 2 million t/yr. To satisfy these constraints, the
head grade must be
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80 CHAPTER FIVE
( ) ( )
=
=
=
+ + + x Q T
4,000,000 g/yr 2,000,000 t/yr
2.00 g/t
c c c
A preliminary mine plan was developed during which 6 million metric
tons of material, both ore and waste, would be mined. The corresponding
grade–tonnage relationship is shown in Figure 5-5. From this relationship,
one determines that the cut-off grade needed to get an average grade of 2.0 g/t
is 1.12 g/t. There are only 1.78 million metric tons of mill feed above cut-off
grade in this preliminary mine plan. Since the mill capacity is 2 million t/yr,
this material will be processed in 10.7 months, calculated as follows:
( ) ( ) ( ) 12 months/yr 1⋅ = .78 million metrictons 2.0 million t/yr 10.7 months
Six million metric tons are scheduled to be mined in this preliminary
mine plan. To mine this tonnage in 10.7 months, the mining rate must be
6.0/10.7 = 560,000 t/month or 6.7 million t/yr.
In conclusion, for the mine to send 4 t of gold per year to a plant that has
a capacity of 2 million t/yr, a total of 6.7 million metric tons must be mined
every year and a cut-off grade of 1.12 g/t must be used. The plant head grade
will be 2.0 g/t.
0
4
3
2
1
6
5
1.0
1.4
1.2
1.6
1.8
2.0
2.2
2.4
Cut-off Grade
0.5 0.6 0.7 0.8 0.9 1 1.1 1.2
Average Grade 2.00
Cut-off 1.12
Tonnage 1.78
Figure 5-5 Estimation of cut-off grade and tonnage given an average grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Tonnage Above Cut-off Grade
Average Grade Above Cut-off Grade
Geologic Constraints and Opportunity Costs 81
Fixed Sales and Fixed Mining Rate with No Processing Constraint
Now consider the case where the mine capacity is constrained at 6 million t/yr
and the metal content of the material to be sent to the mill is set at 4 t of gold
per year. A yearly mine plan was developed in which 6 million metric tons are
to be mined. The corresponding grade–tonnage relationship is shown in Figure 5-5. From the values of T+c and x+c shown in this figure, one can calculate
the metal content of material above cut-off grade Q+c = T+c ∙ x+c and plot this
metal content as a function of cut-off grade x (Figure 5-6).
Figure 5-6 shows the relationship between cut-off grade and quantity of
metal above cut-off grade, as scheduled to be mined in the current mine plan.
Because the quantity of metal to be processed is Q+c = 4.0 t of gold, the cutoff grade must be 0.97 g/t. The tonnage and average grade of material above
this cut-off grade can be determined using the grade–tonnage relationship
(Figure 5-7):
=
=
+
+
T 2.20 million metrictons
x 1.82 g/t
c
c
Given that 6 million metric tons of material are scheduled to be mined
in the coming year and that the mine must send 4 t of gold to the processing
plant, a cut-off grade of 0.97 g/t must be used, resulting in 2.20 million metric
tons of material being sent to the processing plant, averaging 1.82 g/t. This can
only be achieved if the plant capacity is at least 2.20 million t/yr.
R E L E A S I N G C A PA C I T Y C O N S T R A I N T S : A B A S E M E TA L
EXAMPLE
The previous analyses have shown the sometimes deterministic effect that
geologic constraints imposed by nature, combined with capacity constraints,
have on cut-off grades. In this section, an example is given for how to determine the economic feasibility of releasing capacity constraints under defined
geologic conditions.
Consider a copper mining and processing operation. Mine and mill
capacities are 79 million metric tons and 39.5 million t/yr, respectively. The
copper resources included in that part of the deposit scheduled to be mined
in the coming year are listed in Table 5-1. The cut-off grade for mill feed is
0.25% Cu. The reserves to be mined and processed in the coming year are 39.5
million metric tons averaging 0.381% Cu and containing 150,000 metric tons
of copper (332 million lb of copper).
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82 CHAPTER FIVE
Management wishes to assess the sensitivity of the project to changes in
mine, mill, or smelter capacity. Four cases are to be considered:
• Case 1: Assume that the mine capacity is increased by 10%, from
79 to 86.9 million metric tons, but the mill capacity remains fixed
at 39.5 million t/yr. The 79 million metric tons that were scheduled
to be mined in one year, including the resources shown in Table 5-1,
2.0
5.5
5.0
4.5
4.0
3.5
3.0
2.5
6.0
Cut-off Grade
0.5 1 0.9 0.8 0.7 0.6 1.1 1.2
Metal Content 4.0
Cut-off 0.97
Figure 5-6 Estimation of cut-off grade given the required metal content of mine feed
0
4
3
2
1
6
5
1.0
1.4
1.2
1.6
1.8
2.0
2.2
2.4
Cut-off Grade
0.5 0.6 0.7 0.8 0.9 1 1.1 1.2
Average
Grade 1.82
Cut-off 0.97
Tonnage 2.20
Figure 5-7 Estimation of tonnage and average grade above cut-off grade
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Metal Content Above Cut-off Grade Tonnage Above Cut-off Grade
Average Grade Above Cut-off Grade
Geologic Constraints and Opportunity Costs 83
will be mined in 1/1.1 = 0.91 years (10.9 months). During this
period, the mill can only process 35.9 million metric tons. From
Table 5-1, one sees that to send only 35.9 million metric tons to the
processing plant, the cut-off grade must be increased to 0.27% Cu.
The mill head grade will be 0.393% Cu. Assuming that the same average grade can be maintained over one year, 39.5 million metric tons
of ore will be processed at an average grade 0.393% Cu, containing
155,000 t of copper.
• Case 2: Assume that the capacity of the flotation plant is increased
by 10%, from 39.5 to 43.5 million metric tons, but the mine capacity is unchanged at 79 million t/yr. The resources available to feed
the mill in one year remain as shown on Table 5-1. To supply 43.5
million metric tons to the mill, the cut-off grade must be lowered to
0.225% Cu. The mill head grade will average 0.367% Cu, resulting in
160,000 t of copper being processed.
Table 5-1 Copper resources contained in material scheduled to be mined
Cut-off
Grade,
% Cu
Minable
Tonnage, million
metric tons
Minable Grade,
% Cu
Minable Copper Content
thousand
metric tons Cu million lb Cu
0.15% 53.7 0.335% 180 397
0.16% 52.6 0.340% 179 395
0.17% 51.4 0.344% 177 390
0.18% 50.1 0.348% 174 384
0.19% 48.8 0.352% 172 378
0.20% 47.5 0.355% 168 372
0.21% 46.0 0.360% 165 365
0.22% 44.4 0.365% 162 357
0.23% 42.8 0.370% 159 349
0.24% 41.2 0.375% 155 341
0.25% 39.5 0.381% 150 332
0.26% 37.7 0.387% 146 322
0.27% 35.9 0.393% 141 311
0.28% 34.1 0.399% 136 300
0.29% 32.1 0.406% 131 288
0.30% 30.2 0.413% 125 275
0.31% 28.2 0.421% 119 262
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84 CHAPTER FIVE
Table 5-2 Cut-off grades, and mine and mill capacities required to satisfy specific
capacity requirements
Cut-off
Grade,
% Cu
Tonnage
Milled,
million
metric
tons
Average
Grade,
% Cu
Copper Content Tonnage
Mined,
million
metric
tons
thousand
metric
tons Cu
million lb
Cu
Base Case
Values 0.250% 39.5 0.381% 150 332 79.0
Case 1: Increase mining rate by 10%. Keep processing rate at same level.
Values 0.270% 39.5 0.393% 155 342 86.9
Difference
from base
case
8% 0% 3% 3% 3% 10%
Case 2: Increase processing rate by 10%. Keep mining rate at same level.
Values 0.225% 43.5 0.367% 160 352 79.0
Difference
from base
case
–10% 10% –4% 6% 6% 0%
Case 3: Increase copper produced by 10%. Keep mining rate at same level.
Values 0.210% 46.0 0.360% 165 365 79.0
Difference
from base
case
–16% 16% –6% 10% 10% 0%
Case 4: Increase copper produced by 10%. Keep milling rate at same level.
Values 0.305% 39.5 0.418% 165 364 107
Difference
from base
case
22% 0% 10% 10% 10% 36%
• Case 3: Management wishes to determine under which conditions
10% more copper could be sent to the processing plant if mine capacity remains fixed at 79 million metric tons. The copper content of
processed material must increase from 150,000 to 165,000 t. From
Table 5-1 it can be seen that the cut-off grade must be decreased to
0.21% Cu, resulting in 46.0 million metric tons of ore being sent to
the mill, averaging 0.360% Cu. If the mining rate is not changed, a
10% increase in copper processed can only be achieved by decreasing
the average grade by 6% and increasing the tonnage milled by 16%.
• Case 4: Management wishes to determine under which conditions
10% more copper could be sent to the processing plant if mill
capacity remains fixed at 39.5 million metric tons. To increase the
copper content of mill feed from 150,000 to 165,000 t, the mill head
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Geologic Constraints and Opportunity Costs 85
grade must be increased from 0.381% Cu to 165,000/39,500,000 =
0.418% Cu. Table 5-1 shows that, to reach this average grade, it is
necessary to use a cut-off grade of 0.305% Cu. There are only 29.2
million metric tons above this cut-off grade. Given the mill capacity
of 39.5 million metric tons, this ore will be consumed in 29.2/39.5 =
0.74 year (8.88 months). The mining rate must therefore be increased
from 79 million t/yr to 79/0.74 = 107 million t/yr. If the processing
rate is not changed, a 10% increase in copper processed can only be
reached by increasing the average grade by 10% and increasing the
tonnage mined by 36%.
The results are summarized in Table 5-2. Each case is compared with the base
case, in which 79 million metric tons are mined and 39.5 million metric tons
are processed.
This simple example shows procedures that can be used to calculate
cut-off grades taking into account geologic constraints (as summarized in
Table 5-1) and technical constraints, including mine, mill, or production
capacities. No attempt was made to assess whether the proposed solutions
were economically feasible or justified. To do so would require completing
this analysis not only over one year (as done in this example) but for the life of
the mine. Implementing any of the mining and processing plans summarized
in Table 5-2 would require additional capital expenditures; would change
operating costs; might shorten the mine life (cases 1 and 4); could justify
stockpiling of low-grade material (case 4); and might require other operational changes. All these changes would result in changes in cash flow, which
would have to be quantified to decide on the best option.
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Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
87
6
While there are obvious differences, there are also many similarities between
questions that must be answered when designing open pit and underground
mines. These similarities are illustrated in the examples that follow. Different
mining methods are considered, including open pit, selective underground,
and block and panel caving.
O P E N P I T M I N E : E C O N O M I C VA L U AT I O N O F A
PUSHBACK
In this section, a situation is analyzed where a pushback is considered to be
added to an open pit mine. To make this decision and optimize the cut-off
grade, two mine plans should be considered:
1. The first plan assumes that the pushback is not mined. The net present value of future cash flows is NPVi1.
2. The second plan assumes that the pushback is mined. The cash flow
generated by this plan can be divided in two parts: the cash flow corresponding to the material originally scheduled to be mined and the
cash flow generated by the pushback.
Under the second mine plan, the net present value of the material that
was initially scheduled to be mined is likely to decrease from NPVi1 to NPVi2.
The pushback net present value is NPV'i
. The net present value of the second
mine plan is NPVi2 + NPV'i
. The pushback should be mined only if NPV'i
exceeds the difference NPVi1 – NPVi2:
NPV ' > − NPV NPV i i1 i2
The difference NPVi1 – NPVi2 represents the opportunity cost of mining
the pushback. The pushback should only be mined if its net present value
NPV'i is not only positive but also exceeds the opportunity cost. The reason
why there is an opportunity cost to adding a pushback to an existing mine
Cut-off Grade
and Mine Planning
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88 CHAPTER SIX
plan is because there are capacity constraints. Mine capacity, mill capacity, or
volume of sales is constrained. These capacities must be shared between the
material originally scheduled to be mined and the new material coming from
the pushback. To release the capacities that are required to mine the pushback, the following changes might be considered:
• Reduce the rate at which the original material is being mined, and
allocate the spare mining capacity to the pushback.
• Increase the cut-off grade of direct mill feed to release mill capacity
for material coming from the pushback.
• Delay processing of lower-grade material by stockpiling it.
These actions will decrease the net present value from NPVi1 to NPVi2.
Alternatively, additional capital could be invested, including that needed to
increase the mine or mill capacity. This capital cost reduces the net present
value NPV'i
of the pushback.
The net present value NPV'i
of the pushback is calculated from the value
of each block included in the pushback and can be expressed as follows:
NPV'i
= – I + Σ Ujk / (1 + i)k
I = capital cost needed to mine and process the pushback
Ujk = utility of mining block j in year k
i = discount rate
Ujk = Ujk,dir + Ujk,opp + Ujk,oth where
Ujk,dir = direct utility of mining block j in year k
Ujk,opp = opportunity cost of mining block j in year k
Ujk,oth = other utility of mining block j in year k
If there is no capacity constraint, all blocks that will generate a positive
cash flow when processed (Ujk,dir > 0) should be processed when mined. The
cut-off grade is independent of when the block is mined. The pushback can
be mined without changing when, or whether, other material is being mined
outside the pushback. The net present value of the material that was originally
scheduled to be mined remains unchanged, NPVi2 = NPVi1. The pushback’s
mining schedule is only a function of the sequence to be followed to mine the
pushback and is independent of any other mining activity that may be taking
place. The decision to mine the pushback is only a function of whether or not
its net present value NPV'i
is positive.
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Cut-off Grade and Mine Planning 89
However, optimization of mine and mill operations implies balancing
capital and operating costs, which invariably results in capacity constraints
and nonzero opportunity costs: Ujk,opp > 0. Nonzero opportunity costs result
in time delays, higher cut-off grades, fewer blocks being processed, and,
therefore, lower pushback net present value. A pushback for which NPV'i
is
positive if capacity constraints are ignored may have a negative NPV'i
if these
constraints are taken into account. Ignoring capacity constraints may result in
mining pushbacks that should not be mined and designing a pit that is larger
than it should be.
There are two dependent sets of constraints to be taken into account
when evaluating a pushback: constraints that apply if the pushback is mined
as a stand-alone operation and constraints that result from having to share
capacity with the material originally scheduled to be mined. Considering a
pushback as a stand-alone operation is rarely, if ever, a reasonable assumption.
It may be possible to dedicate mining equipment entirely to the pushback.
This capital cost must be included in NPV'i
and in cut-off grade optimization.
Even under these circumstances, mine schedules and cut-off grades must take
into account process capacity constraints. The plant is at least in part utilized
by material previously scheduled to be mined, and taking this capacity constraint into account will reduce the value of the pushback.
When more constraints are added to the pushback, its value NPV'i
decreases. Releasing these constraints can be achieved by assigning capacity
to the pushback that was previously utilized elsewhere. However, this will
increase the constraints on the material originally scheduled to be mined
and increase the opportunity cost NPVi1 – NPVi2. The optimal capacity
assignment is that where further change will result in a decrease in NPVi2 that
exceeds the increase in NPV'i
. Finding this optimum can be time-consuming
and may require use of specialized open pit mine-design software.
U N D E R G R O U N D M I N E : E C O N O M I C VA L U AT I O N O F A
STOPE
Situations similar to those previously described in open pit mines are also
encountered in underground mines. A stope should be mined if the net
present value of generated cash flow is positive. All costs and benefits must
be taken into account, as well as when these costs and benefits are realized.
This includes the cost of stope development (such as access drifts and crosscuts); the cost of waste mining, stockpiling, and re-handling; the cost of ore
mining, stockpiling, re-handling, and processing; and all costs allocated to
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90 CHAPTER SIX
low-grade stockpiles, if any. Revenues include those incurred from processing
ore directly sent to the mill, as well as those realized at a later date from lowgrade stockpiles.
If there is no capacity constraint, all material that can generate a positive
cash flow, if processed when mined, will be processed. But project optimization invariably results in capacity constraints, such as those imposed by shaft
and drift haulage capacity, ventilation, maximum speed of development, or
mining method. These constraints result in nonzero opportunity costs and
higher cut-off grades. When capacity constraints are taken into account, the
size of some stopes is likely to be reduced, and some stopes will no longer be
considered economically minable.
Shifting capacity from other parts of the mine can be used to release
constraints on the stope and increase the stope net present value (NPV'i).
For example, one may assign shaft capacity to material produced by the new
stope by slowing down mining from other stopes. However, more constraints
will result, which apply to material previously scheduled to be mined. If
NPVi1 was the net present value of this material before the new stope was
taken into account, and NPVi2 its net present value when the new constraints
are imposed, NPVi2 is less than NPVi1. The difference NPVi1 –NPVi2 is the
opportunity cost of mining the new stope. Adding the new stope to the production schedule is justified only if
NPV ' > − NPV NPV i i1 i2
When more constraints are added to a stope, its value NPV'i
decreases.
Releasing these constraints can be achieved by assigning capacity to the
stope that was previously utilized elsewhere. However, this will increase the
constraints on the material originally scheduled to be mined and increase
the opportunity cost NPVi1 – NPVi2. The optimal capacity assignment is
that where further change will result in a decrease in NPVi2 that exceeds the
increase in NPV'i
. Finding this optimum can be time-consuming and may
require use of specialized underground mining software.
S I M I L A R I T I E S B E T W E E N O P E N P I T A N D
UNDERGROUND MINE PLANNING
As shown in the previous discussions, there are many similarities between
questions concerning open pit and underground mines, and the approach that
must be followed to answer these questions. Here are some of these questions:
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Cut-off Grade and Mine Planning 91
• How do capacity constraints influence cut-off grade and cash flow?
• Which cut-off grade should be used to separate waste material, stockpiled material, and material sent to the processing plant?
• Should a pushback be mined in an open pit mine or a stope be mined
in an underground mine?
• Should low-grade material at the bottom of a pushback or surrounding a stope be mined or left in the ground?
• If low-grade material must be mined, should it be wasted, stockpiled,
or processed?
• How should the time difference between mining, stockpiling, processing, and selling material be taken into account in designing open
pit and underground mines?
BLOCK AND PANEL CAVING
When a block or panel caving mining method is used, estimation of cut-off
grades must take into account the limited flexibility that operators have in
controlling the grade of material pulled. Cut-off grades are used to determine
the location and size of a block or panel, and to decide when pulling material
from a drawpoint should be stopped. Cut-off grades are not likely to play a
significant role, if any, when waste or low-grade material is encountered in the
block.
Constraints Imposed by Block and Panel Caving
Many factors must be taken into account when designing a block in addition
to the geotechnical properties of the deposit and the continuity of mineralization. Ideally, blocks are located in relatively high-grade areas that can be
mined without significant internal or external waste dilution, the drawpoints
and production levels are located in lower-grade or waste areas, and the block
boundaries are located near lower-grade or waste zones. Internal and external
waste or low-grade dilution will occur, which must be taken into account
when locating blocks and drawpoints. When ore is drawn, waste is mixed
with higher-grade material, thus eliminating the opportunity to mine waste
selectively.
The rate at which material is pulled from drawpoints should match the
natural rate of caving. The material should be drawn in a uniform fashion
across drawpoints. Production cannot be stopped in one drawpoint without affecting surrounding drawpoints. If a drawpoint containing waste is
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92 CHAPTER SIX
surrounded by other high-grade drawpoints, mining waste cannot be stopped.
However, if the waste drawpoint is located on the periphery of the block
being mined, this drawpoint can be stopped. Production is stopped when
waste indicates that the entire ore column has been pulled.
Productivity is dependent on a high rate of production, which is not
conducive to selective mining of ore and waste material. The capital cost of
underground and surface infrastructure needed to handle waste separately
from ore-grade material is likely to be high. Attempting selective mining is
likely to increase the mine operating costs. For these reasons, some block caving operations have chosen to send all material mined to the processing plant,
whatever the grade.
Marginal Cut-off Grade and Drawpoint Management
Once a block has been developed and the infrastructure is in place (including
drifts, haulage facilities, drawpoints, ventilation, etc.), the utility of mining
and processing one metric ton of material is
( ) ( ) = ⋅ ⋅ − ( )− + + U x x r V R M P O dir o o o
where
x = average grade
r = recovery, or proportion of salable product recovered from
the mined material
V = value of one unit of salable product
R = refining, transportation, and other costs of sales that are
expressed in dollars per unit of salable product
Mo
= mining cost per metric ton processed
Po
= processing cost per metric ton processed
Oo
= overhead cost per metric ton processed
The minimum grade that can be mined and processed at a profit is xc1
such that Udir(xc1) = 0:
[ ] [ ] ( ) = + + ⋅ − x M P O r V R c1 o o o
This cut-off grade should be used to decide whether production from a drawpoint should be stopped because of excessive lateral dilution or because the
entire ore column has been mined.
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Cut-off Grade and Mine Planning 93
Marginal Cut-off Grade and Block Design
Incremental analysis must be used to determine the optimal size and location
of a block. To decide whether a new row of drawpoints should be added along
the periphery of a block, one must first estimate the tonnage T and average
grade x of the material that will be pulled from these drawpoints, taking dilution into account. If one considers only operating costs and ignores the capital
and opportunity cost of adding one row of drawpoints, this row should be
added if the average grade x exceeds the cut-off grade xc1 calculated previously.
If the average grade of the last row of drawpoints is equal to xc1, the
cash flow generated from these drawpoints will not justify the capital cost
of developing them. In addition, development of a larger block by addition
of peripheral drawpoints will delay production from what could have been a
smaller block. The cut-off grade applicable to the last row of drawpoints must
take into account capital and opportunity costs.
Influence of Capital Cost and Discount Rate
Additional capital expenditures are needed to develop one more row of
drawpoints. This capital cost I must be recovered from profits generated by
the drawpoints. On an undiscounted basis, the profit made from mining and
processing T metric tons of material with average grade x is T ∙ [x ∙ r ∙ (V – R)
– (Mo
+ Po
+ Oo
)]. This profit must be greater than or equal to the capital cost
I. The cut-off grade applicable to this last row of drawpoints is determined by
adding the capital cost per metric ton I/T to the operating costs M, P, and O:
[ ] [ ] ( ) = + + + ⋅ − x M P O I T r V R c2 o o o
where
I = capital cost incurred to develop a new row of drawpoints
T = tonnage to be mined from the new row of drawpoints
The requirement of a minimum rate of return should be taken into
account in calculating the cut-off grade. The following additional notations
are used:
i = minimum rate of return (discount rate)
n = number of years during which material will be pulled from
the new drawpoints
Then make the simplifying assumption that the tonnage mined and corresponding average grade will be the same every year, T/n and x, respectively.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
94 CHAPTER SIX
The yearly cash flow YCF expected to be generated from the new drawpoints
is
( ) ( ) ( ) = ⋅ ⋅ ⋅ − − + +
YCF T n x r V R Mo o P Oo
The net present value of this cash flow (NPV'i
) is calculated as follows*:
()() () ( ) = ⋅ + ++ + + + +
= − NPV ' YCF 1 1 1 i 1 1 i 1 1 i YCF g i,n i
2 n 1
where g(i,n) = [1– (1 + i)–n] (1 + i)/i.
The minimum cut-off grade applicable to the new row of drawpoints is
xc3 such that the net present value of generated cash flows NPV'i
is equal to
the capital investment I:
[ ]
( )
( )
( )
( )
( ) ( )
( ) ( )
=
⋅ ⋅ ⋅ − − + +
⋅ =
= + + + ⋅
⋅ −
NPV ' I
T n x r V R M P O g i,n I
x M P O n g i,n I T r V R
i
c3 o o o
c3 o o o
Opportunity Cost
In addition to increasing capital costs, increasing the size of a block can delay
production that could be pulled from a smaller block. Assume that a small,
presumably high-grade block has been designed and that a production schedule has been developed accordingly. The net present value NPVi
of future
cash flows expected to be generated from mining this block was calculated
using the discount rate i. If t is the time by which production from the smaller
block will be delayed to allow development of one more row of drawpoints,
the corresponding opportunity cost is
( )= − ⋅ ⋅ U x t i NPV opp i
This opportunity cost represents a decrease in net present value, which must
be added to the capital cost of adding the new drawpoints. Taking this cost
into account, the cut-off grade is as follows:
* The notation NPV'i
is used to make the distinction between the net present
value of previously scheduled operations, NPVi
, and the net present value of the
proposed additional row of drawpoints, NPV'i
. The first year of production is not
discounted.
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Cut-off Grade and Mine Planning 95
[ ] ( ) ( ) ( ) = + + + ⋅ + ⋅ ⋅
⋅ − x M P O n g i,n I t i NPV T r V R c4 o o o i
where
Mo
= mining cost per metric ton processed
Po
= processing cost per metric ton processed
Oo
= overhead cost per metric ton processed
g(i,n) = [1 – (1 + i)–n] (1 + i)/i
n = number of years during which material will be pulled from
the new row of drawpoints
i = minimum rate of return (discount rate)
I = capital cost incurred to develop the new row of drawpoints
t = time by which previously scheduled production will be
delayed
NPVi
= net present value of previously scheduled production
T = tonnage to be mined from the new row of drawpoints
r = recovery, or proportion of salable product recovered from
the mined material
V = value of one unit of salable product
R = refining, transportation, and other costs of sales that are
expressed in dollar per unit of salable product
Example: Block Caving Copper Mine Operation
Consider a copper mine that is exploited by the block caving method. The
deposit is scheduled to be mined using macroblocks 150 m high. The drawpoints are located on a 20-m grid. The current operating conditions are as
follows:
• Direct mining cost: $9.00 per metric ton of ore
• Processing cost: $7.00 per metric ton of ore
• General and administrative cost: $1.60 per metric ton of ore
• Freight, smelting, and refining: $0.50 per pound of payable copper
The mill recovery is 87% and the smelter recovery is 96%, including transportation losses. The long-term copper price is assumed to be $2.30 per pound
of payable copper (1 t = 2,205 lb).
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96 CHAPTER SIX
Using the above notations, this can be written as follows:
Mo
= $9.00
Po
= $7.00
Oo
= $1.60
V = $2.30
R = $0.50
r = 0.87 ∙ 0.96 = 83.52%
The marginal cut-off grade for an existing drawpoint is
[ ] [ ] ( ) = + + ⋅ − ⋅ = x 9.00 7.00 1.60 83.52 2.30 0.50 2,205 0.53% Cu c1
The cost of developing a new drawpoint, including access and other
development costs, is I = $240,000. The specific gravity of the ore is 2.5 t/m3
,
and the average tonnage contained in one column is T = 20 ∙ 20 ∙ 150 ∙ 2.5 =
150,000 t. On an undiscounted per-metric-ton basis, the cost of drawpoint
development is
I T = = $240,000 150,000 $1.60 per metric ton
The amount of copper needed to recover this cost is
[ ] ( ) − = ⋅ − ⋅ = x x $1.60 83.52 2.30 0.50 2,205 0.05% Cu c2 c1
The cut-off grade to be used to pay for operating costs and undiscounted capital cost per metric ton is
= + = x 0.53 0.05 0.58% Cu c2
The life of a macroblock is estimated at n = 10 years. An i = 15% rate of
return is expected for all investments. The capital recovery needed per metric
ton to obtain this rate of return is n/g(i,n) ∙ (I/T):
( ) ( )
( ) ( )( )
( )
= − +
⋅ + =
⋅ = ⋅ =
− g i,n 1 1 0.15 1 0.15 0.15 5.772
n g i,n I T 10 5.77 1.60 $2.77 per metric ton
10
The amount of copper needed to recover this cost is
[ ] ( ) − = ⋅ − ⋅ = x x $2.77 83.52 2.30 0.50 2,205 0.08% Cu c3 c1
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Cut-off Grade and Mine Planning 97
The cut-off grade to be used to pay for operating costs and discounted capital
cost per metric ton is
=+= x 0.53 0.08 0.61% Cu c3
The macroblock under consideration is scheduled to go into production
immediately. As designed, the macroblock is composed of 15 columns for a
total tonnage of 15 ∙ 150,000 = 2,250,000 t. The average grade of this material
is 2.00% Cu, and the total value of the ore contained is
[ ] ( ) ( ) ⋅ ⋅ ⋅ − ⋅ − + + = 2,250,000 0.02 0.8352 2.30 0.5 2,205 9.00 7.00 1.60 $109,570,896
Assuming a uniform cash flow per year over ten years, the net present value
of this cash flow is
( ) ( ) = ⋅ = ⋅ = NPV 109,570,896 10 g i,n 10,957,090 5,772 $63,269,762 i
Consideration is being given to adding one more drawpoint to the macroblock. The time needed to develop this drawpoint is estimated at 12 days.
This will delay copper production from the macroblock by 12 days at an
opportunity cost:
( ) ⋅ ⋅ = ⋅ ⋅ = t i NPV 12 365 0.015 63,269,762 $311,867 i
This cost is incurred today but must be recovered over the life of the project. It
must be added to the capital cost I. To ensure a 15% rate of return, the amount
needed per year is
( ) ( ) ( )⋅ = ⋅ = n g i,n 311,867 T 10 5.77 2.08 $3.60 per metric ton
The amount of copper needed to recover this cost is
[ ] ( ) − = ⋅ − ⋅ = x x $3.60 83.52 2.30 0.50 2,205 0.11% Cu c4 c3
The cut-off grade to be used to pay for operating costs, discounted capital
cost per metric ton, and discounted opportunity cost is
=+= x 0.61 0.11 0.72% Cu c4
This cut-off grade is significantly higher than the marginal cut-off grade
xc1 = 0.53% Cu. If a lower discount rate was acceptable, such as i = 6% instead
of 15%, the cut-off grade would be reduced to xc4 = 0.64% Cu. To fully take
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98 CHAPTER SIX
into account all costs and benefits associated with adding one more drawpoint
to an existing macroblock, one should also look at consequences other than
those considered here. These may include the opportunity cost of delaying
production from other parts of the operation, lowering the head grade, and
increasing the mine life.
RELATIONS HI P B E T W E E N M I N E S E L E C T I V I T Y, D E P O S I T
MODELING, ORE CONTROL, AND CUT-OFF GRADE
In the previous examples, it was assumed that the grade–tonnage relationship
which characterizes the deposit is independent of the mining capacity. However, in many instances, changes in mining capacity are accompanied by changes
in mining method, size of mining equipment, bench height, stope dimensions,
drill hole spacing, ore control method, and other parameters that determine
mine selectivity and the shape of the grade–tonnage curve. These changes must
be taken into account in establishing the likely effect that changes in mining
capacity and cut-off grade will have on mill feed and reserves.
As an example, consider a gold deposit for which the total resources
above a zero cut-off grade are calculated at 20 million metric tons averaging
10 g/t. The geology of the deposit is such that either open pit or underground
mining methods can be used. Figures 6-1 and 6-2 both show the grade–
tonnage relationships corresponding to the open pit and underground mining
methods.
The open pit cut-off grade was estimated at 3.0 g/t. The amount of material that could be mined above this cut-off grade was 15.2 million metric tons,
averaging 12.6 g/t and containing 6.1 million oz (solid lines in Figure 6-1). If
the high-selectivity model had been used to evaluate the open pit option, the
reserves would have been erroneously estimated at 11.1 million metric tons,
averaging 16.9 g/t and containing 6.0 million oz (dotted lines in Figure 6-1).
The underground cut-off grade was estimated at 7.0 g/t. The amount
of material that could be mined above this cut-off grade was 6.5 million
metric tons, averaging 25.6 g/t and containing 5.3 million oz (solid lines
in Figure 6-2). If the low-selectivity model had been used to determine the
feasibility of the underground mining method, the reserves would have been
erroneously estimated at 8.9 million metric tons, averaging 18.2 g/t and containing 5.2 million oz (dotted lines in Figure 6-2).
The errors made when using the open pit model to evaluate the underground resources or the underground model to evaluate the open pit resources
are summarized in Table 6-1. Although this table represents an extreme case, it
clearly shows that changes in both mining method and cut-off grade must be
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Cut-off Grade and Mine Planning 99
evaluated jointly. Appropriate deposit models must be used, which reflect the
conditions that are expected to prevail when these changes are made. When
assessing the impact that changes in mining capacity may have on mill head
grades, one must take into account not only changes in cut-off grades but also
changes in the grade–tonnage curve. The grade–tonnage curve will remain
4
12
10
8
6
20
14
16
18
5
30
25
20
15
10
35
Cut-off Grade
1 2 3 4 5 6 7 8 9
Tonnage 15.2
Tonnage 11.1
Cut-off 3.0
Average Grade 16.9
Average Grade 12.6
Figure 6-1 Application of open pit low-selectivity cut-off grade to low- and
high-selectivity models (solid lines show the low-selectivity model; dotted lines
show the high-selectivity model)
4
12
10
8
6
20
14
16
18
5
30
25
20
15
10
35
Cut-off Grade
1 2 3 4 5 6 7 8 9
Tonnage 8.9
Tonnage 6.5 Cut-off 7.0
Average Grade 25.6
Average
Grade 18.2
Figure 6-2 Application of the underground high-selectivity cut-off grade to highand low-selectivity models (solid lines show the high-selectivity model; dotted
lines show the low-selectivity model)
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Tonnage Above Cut-off Grade
Average Grade Above Cut-off Grade
Tonnage Above Cut-off Grade
Average Grade Above Cut-off Grade
100 CHAPTER SIX
the same only if no change is made to mining method, ore control practices,
and size of mining equipment.
A computer-generated deposit model is the foundation on which mine
plans are developed, cut-off grades are optimized, and the tonnage and average
grade of material processed are determined. For the results of a feasibility study
to be meaningful, the deposit model must reflect the geological properties of
the deposit. In addition, the relationship between cut-off grade, tonnage, and
average grade above cut-off grade, which is implied by the deposit model, must
be the same as that which will be realized when the deposit is mined.
The deposit model must be developed taking into account the mining
method that will be used and how selective this method will be. Different
models are usually needed for open pit and underground mines, for bulk
mining and selective mining, for block caving and cut-and-fill. Selectivity
is a function not only of the geology of the deposit and the mining method
but also of bench height and blast hole spacing, stope design, type and size of
mining equipment, and ore control method. The significance of these factors
must be assessed when developing the deposit model.
It is not sufficient to make realistic selectivity assumptions when developing the deposit model and optimizing the cut-off grade. These assumptions
must be respected when the deposit is being mined. Otherwise, the tonnage
and average grade of material mined and processed will differ from that estimated when the project feasibility study was completed. In practice, changes
will occur during the life of the mine, which will change selectivity. Such
changes may include changing mining method, using smaller or higher bench
heights, designing larger or smaller stopes, changing the equipment size, and
modifying ore control practices. Whenever such changes are made, one must
question whether they will change the grade–tonnage curve sufficiently to
require development of a new deposit model.
Table 6-1 Influence of deposit model and cut-off grade on estimated mineral
resources
Deposit Model
Open Pit Mine Cut-off, 3.0 g/t Underground Mine Cut-off, 7.0 g/t
Metric
Tons,
millions
Grade,
g/t
Ounces,
millions
Metric
Tons,
millions
Grade,
g/t
Ounces,
millions
High selectivity 11.1 16.9 6.0 6.5 25.6 5.3
Low selectivity 15.2 12.6 6.1 8.9 18.2 5.2
Correct model 15.2 12.6 6.1 6.5 25.6 5.3
Error if correct
model not used
–27% 34% –2% 36% –29% –3%
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101
7
Mining engineers face a significant challenge when determining which costs
should be included in a cut-off grade calculation. Collaboration between
engineers and accountants is necessary to ensure that meaningful numbers are
used and that all applicable costs are included. In this chapter, some general
principles concerning costs and how they should be treated in the estimation
of cut-off grades are discussed, which are illustrated by specific examples.
GENERAL CONSIDERATIONS
Costs can be divided between fixed and variable. Fixed costs are expenses for
which the total does not change in proportion to the level of activity within the
relevant time period or scale of production. By contrast, variable costs change
in relation to the level of activity. In cut-off grade calculations, costs incurred
when drilling, sampling, blasting, loading, crushing, and grinding the ore as
well as during flotation, concentrate drying, filtering and shipping, smelting
and refining, and so forth, are usually considered variable costs. These costs
are directly related to the production capacity. Initial capital expenditures,
equipment depreciation, general administration, property taxes, marketing,
public relations, government relations, and so on, are considered fixed costs.
To the extent that fixed and variable costs are properly defined, cut-off grade
optimization requirements only take variable costs into consideration.
It is important to realize that fixed costs are fixed only within a certain
range of activity or over a certain period of time. If significant changes are
made to the cut-off grade that require expansion of a leach pad or tailings
dam, costs related to such expansions can no longer be considered fixed. If the
life of mine is extended or shortened beyond the current expected life, general
and administrative (G&A) costs will change. These changes should be taken
into account in the cut-off grade calculation by allocating their cost to that
part of the operation (mine, mill, leach plant, concentrator, smelter, refinery,
etc.) that drives the change.
Which Costs Should Be
Included in Cut-off Grade
Calculations?
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102 CHAPTER SEVEN
Sunk costs are expenses that were incurred in the past and do not change
with the level of activity. Once a mine is in full production, the costs incurred
for pre-stripping, shaft sinking, plant construction, and original infrastructure
are sunk. Such costs are not taken into account when deciding whether the
cut-off grade should be changed. However, during a project feasibility study,
all costs, including the initial capital cost, have an influence on the cut-off
grade. The cut-off grade determines the tonnage, grade, and location of material available for processing, which in turn drive mine and plant size, capital
and operating costs, and financial performance. Conversely, operating costs
are a critical input in the determination of the minimum cut-off grade. Different cut-off grade profiles, including cut-off grades that decrease over time,
will require different mine plans and capital costs, and will result in better or
worse financial performance. An iterative process must be used to determine
the combination of cut-off grades, size of operation, and resulting capital and
operating costs that will best satisfy the company’s objectives.
Balancing initial and sustaining capital costs, operating costs, and cutoff grades is a critical part of a project feasibility study. If all assumptions
made during the feasibility study, including those related to the geology of
the deposit, the production capacity, the cost of operations, and the value of
the product sold, remained true during the entire life of the mine, the cut-off
grades would remain as planned. No cut-off grade change could be justified
since plans were optimized and changes would reduce the value of the project. Decreasing the cut-off grade would require that additional lower-grade
material be processed, which could not be achieved without either increasing
the size of the plant or decreasing the net present value of future cash flows.
Conversely, increasing the cut-off grade above that planned would result in
underutilization of available capacity.
In practice, operating conditions differ from those assumed during the
feasibility study, the geological properties of the deposit differ from those
initially expected, capacities are either not reached or exceeded, mine and mill
are no longer balanced, costs and the value of products sold are better or worse
than expected, and cut-off grades must be continuously reestimated.
A company’s financial objectives are likely to include expectation of a
minimum return on investment, which cut-off grade calculations must take
into account. If the time needed to mine one metric ton of material, process
it, recover a salable product, and get a return from the sale of this product
exceeds one year, costs and revenues should be discounted at the companyspecified rate. While sunk costs do not influence cut-off grades, the cost of
future sustaining capital expenditures must be included in the cut-off grade
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Which Costs Should Be Included in Cut-off Grade Calculations? 103
calculation to ensure that all material processed covers the capital invested,
including a specified minimum return on investment.
HO W S P E C I F I C C O S T S I N F L U E N C E C U T- O F F G R A D E
CALCULATIONS
A few examples follow that illustrate how specific costs influence the cut-off
grade. It is assumed that the mining company expects a minimum 15% return
(i = 15%) on all investments:
• Stockpiling of low-grade material. This was discussed previously. The
decision to stockpile material is more often than not a strategic decision rather than a decision based solely on expected cash flows and
net present value.
• Leaching operation. In leaching operations, capital and operating
costs, metal recovery, and metal sales occur over several years, and
the cut-off grade might have to be determined using discounted cash
flows. Consider a gold leaching operation with a five-year leach cycle.
The total gold recovery is expected to reach 60%. Recovery and cost
per year are given in Table 7-1. The waste-leach cut-off grade is to be
estimated using a gold price V = $1,150 per ounce, a cost of sales of
$50 per ounce, and a discount rate of 15%. The expected yearly revenue per ounce of gold contained in the material being leached is r (V
– R), where r varies from year to year. This revenue is shown in Table
7-1, column 4. The last three columns in Table 7-1 show the discount
factor 1/(1 + i), the discounted cost per metric ton, and the discounted revenue per ounce contained. The cut-off grade is calculated
as the ratio of total costs over total revenues per ounce. If cash flows
are not discounted, this cut-off grade is 0.47 g/t. To obtain a 15%
return on investment the cut-off grade must be increased to 0.52 g/t.
• Sustaining capital. Sustaining capital is capital expenditures that
must be incurred on a periodic basis to maintain production at the
current level. For example, new trucks may have to be bought every
eight years, leach pad expansions may be needed every four years,
tails dam lifts may be added every seven years. Let I be the total cost
of this investment and n its expected useful life in years. The cut-off
grade should be high enough to ensure a minimum return on investment (i = 15%). This is achieved by including the cost of capital in
the cut-off grade calculation. Let CI
be the cost per year that must be
recognized to recover the investment I over n years at the specified
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104 CHAPTER SEVEN
discount rate i. The net present value of this constant cost is CI
g(i,n),
where g(i,n) = [1 – (1 + i)–n] ∙ (1 + i)/i. This cost must satisfy the
following equation:
( ) = C g i,n I I
Therefore, the cost per year that should be included in the cut-off
grade calculation is
= ( ) C I g i,n I
If i = 15% and n = 8, the cost of capital is CI
= 0.19 I per year. If
no minimum return on investment was specified, the cost of capital
would be CI
= I/n = 0.13 I per year. In the cut-off grade calculation,
costs per year must be converted to costs per unit of production.
These costs must be added to mining costs if the sustaining capital is
for mining equipment, to leaching costs if it is for leach pad expansion, and to milling costs if it is for a tailings dam. Incremental capital
expenditures, which are optional and must be justified by a feasibility
study, should not be considered as sustaining capital.
• Incremental capital expenditures. Such expenditures may be required
to maintain production beyond the planned life or to reach a higher
level of production. The cost of these incremental capital expenditures must be taken into account in deciding whether the life should
be extended or production should be increased. Different cut-off
grade strategies should be considered. Once the decision is made to
Table 7-1 Calculation of cut-off grade in a gold leach operation
Year Recovery
Undiscounted Discounted
Cost per
Metric Ton
Revenue
per Ounce
Contained
Discount
Factor
Cost per
Metric Ton
Revenue
per Ounce
Contained
0 15% $6.00 $165 1.00 $6.00 $165
1 15% $1.00 $165 0.87 $0.87 $143
2 12% $1.00 $132 0.76 $0.76 $100
3 10% $1.00 $110 0.66 $0.66 $72
4 8% $1.00 $88 0.57 $0.57 $50
Total 60% $10.00 $660 — $8.85 $531
Cut-off
grade
oz/t — 0.0152 — — 0.0167
g/t — 0.47 — — 0.52
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Which Costs Should Be Included in Cut-off Grade Calculations? 105
make the investment, incremental capital expenditures are sunk, and
only remaining capacity constraints should influence cut-off grade
decisions.
• Closure and reclamation costs. At the end of a mine life, one-time closure costs are incurred. These costs, CR, decrease the net present value
of a project’s future cash flow and therefore the opportunity cost
i∙t∙NPVi
. At the beginning of the mine life, the influence of closure
costs on net present value is small, but it increases when the project
matures. It was shown previously that if closure can be postponed by
one year by mining low-grade material, the corresponding cash flow
C could be negative. The only constraint is that C > –CR i/(1 + i).
• Cost to perpetuity. In some circumstances (e.g., if a water treatment
plant must operate forever after closing a mining operation), a
project generates a constant negative cash flow to perpetuity. It was
shown previously that if C is a yearly cash flow to perpetuity, the net
present value of this cash flow is NPVi
= C(1 + i)/i. This net present
value is constant over time and can be considered as a fixed cost that
does not influence the cut-off grade. However, this cost decreases the
net present value of the project and should be taken into consideration when completing a feasibility study.
• Overhead costs. G&A and other overhead costs must also be divided
between fixed and variable costs. Variable G&A costs must be
included in all cut-off grade calculations. Fixed G&A costs, usually
expressed on a per-year basis, must be included if the change in cutoff grade will change the mine life. This will be the case whenever one
of the processes is capacity constrained. The fixed part of overhead
costs can no longer be considered as fixed because lowering the cutoff grade will require extending the mine life. These costs must be
expressed on a per-unit-of-production basis (by dividing costs per year
by production per year) and added to the unit cost of the capacityconstrained process.
O T HER COSTS AND BENEFITS
Cut-off grades play a critical role in defining tonnages mined and processed,
average grade of mill feed, life of mine, cash flows, and all major characteristics
of a mining operation. In addition to the economically quantifiable financial
impact that cut-off grade changes may have, other costs and benefits must
be taken into account even though their impact is not easily quantifiable.
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106 CHAPTER SEVEN
Consideration must be given not only to changes in cash flow and net present
value—as measured by Udir(x) and Uopp(x)—but also to all other impacts,
Uoth(x), including those of an environmental, socioeconomic, ethical, or political nature. Costs and benefits to all stakeholders must be evaluated. For most
mining operations, the following stakeholders must be taken into account:
• Shareholders, who supply the capital needed for the operation and
expect a return on their investment
• Banks, who contribute to the supply of financial resources the mining company needs to operate or expand
• Analysts, who advise the investing community
• Employees and their families
• Users of the final product sold by the mining operation, whether it
is coal, gold, copper concentrate, iron ore, processed metal, or industrial minerals
• Suppliers, from whom the mining operation purchases equipment,
energy, consumables, supplies, services, or expertise
• Local communities, including neighbors of the mining operation
• The local, regional, federal, or country governments, who are responsible for the welfare of their citizens and benefit from the taxes levied
from the mining company. These governments must plan for new
infrastructure, roads, health, education, and entertainment; increases
in traffic, crime, and prostitution; and higher demand for water,
food, and housing. They also have a fiduciary duty to ensure appropriate exploitation of national resources.
• Future generations, which will live with the long-term impact, good
or bad, of the mining operation
• Nongovernmental organizations whose mission, self-appointed or
otherwise, is to defend the interests of some of the above stakeholders
Senior management decides how to balance the needs, interests, and
requirements of the different stakeholders. Those in charge of mine planning
must be given practical guidelines for cut-off grade determination to ensure
that the projects are designed to reach the company’s objectives. Maximizing
shareholder value (including minimizing shareholder liability) is often quoted
as a company’s primary objective. However, a company’s objectives must
include recognition of responsibilities toward all stakeholders, not only the
shareholders.
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Which Costs Should Be Included in Cut-off Grade Calculations? 107
Higher cut-off grades may increase short-term profitability and enhance
return to shareholders and other financial stakeholders. Higher cut-off grades
may shorten the payback period, thus reducing political risk of creeping or
outright nationalization. But reduced mine life reduces time-dependent
opportunities, such as those offered by price cycles. Conversely, lower cut-off
grades may increase project life with longer economic benefit to all stakeholders, including shareholders, employees, local communities, and government.
Longer mine life may result in more stable employment, less socioeconomic
disruption to local communities, and more stable tax revenues to government.
Lower cut-off grades imply fuller consumption of mineral resources, which
may present political advantages or may be required by law. All stakeholders
may have to choose between higher financial returns over shorter time periods
or lower returns over longer time periods. Using high but decreasing cut-off
grades early in the mine life and stockpiling low-grade material for later processing can help balance financial returns and mine life.
One method of optimizing cut-off grades while taking into account
unquantifiable costs and benefits consists of evaluating the project under a
variety of constraints imposed on discount rate, mine or mill capacity, volume
of sales, capital or operating costs, and so forth. Changes in the opportunity
cost of imposing these constraints, Uopp(x), are compared with the corresponding changes in other costs, Uoth(x). The optimal cut-off grade is that for
which the marginal (and quantifiable) increase in opportunity cost is equal to
the corresponding marginal (but subjective) decrease in other costs.
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Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
109
8
In an increasingly complex environment, blending strategies may be critical
in maximizing the profitability of an operation or set of operations. For
example, a metallurgical process may require that the chemical properties of
the mill feed fall within specific ranges. Sales contracts may impose limits on
the quality of the product being sold and the contaminants it contains. Environmental regulations may impose constraints on the mill feed, as needed for
environmental emission control.
In a gold mine where refractory ore is treated by roasting, there might be
different parts of the deposit with different geochemical properties. Material
with high sulfide content and low gold content may have no economic value if
considered on its own. Conversely, processing material with high gold content
and low sulfur content may be problematic. However, adding the calorific
value of the high-sulfide material to the gold value of the high-gold material
may result in a highly profitable operation.
In a coal mining operation, one seam may have a low calorific value and
high ash content, and another seam a high calorific value and low ash content.
By appropriately mixing the two products, it may be possible to increase the
tonnage of salable coal that satisfies contractual agreements on both sulfur
grade and calorific value. Similarly, the product from one iron mine may have
no economic value if considered on its own, but a salable product may be
obtained by blending it with iron ore from another mine that exceeds contractual requirements.
Blending strategies applicable in relatively simple situations, such as when
there are only two or three stockpiles, are discussed in this chapter. The objective is to give the reader a high-level understanding of the strategic aspect of
stockpiling and blending. Although practitioners are likely to encounter more
complex situations, the solution to such problems falls outside the scope of
this book.
Blending Strategy
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110 CHAPTER EIGHT
BLENDING TWO MATERIAL TYPES
Consider a gold roasting operation that has access to two sources of concentrate, a 20,000 t high-sulfide, low-gold stockpile (concentrate 1) and a
40,000 t low-sulfide, high-grade stockpile (concentrate 2). The concentrate
properties are summarized in Table 8-1. Table 8-2 shows that 82% of the gold
is in concentrate 2. The following notations are used:
Ti
= tonnage of concentrate i, i = 1,2
x1i = sulfur grade of concentrate i, i = 1,2
x2i = gold grade of concentrate i, i = 1,2
To
= tonnage of roaster feed
x1o = sulfur grade of roaster feed
x2o = gold grade of roaster feed
pi
= proportion of concentrate i in roaster feed, i = 1,2
t
i
= tonnage of concentrate i in roaster feed, i = 1,2
Blending to Maximize Gold Grade in Roaster Feed
To satisfy fuel requirements, the roaster needs feed averaging at least 1.5%
sulfur. An objective could be to maximize the blended gold grade while satisfying the sulfur requirements. Figure 8-1, called a blending diagram, shows
the relationship between sulfur grade and gold grade for the two concentrates
and all possible concentrate blends. Potential roaster feeds are represented by
Table 8-1 Properties of concentrates available for blending
Material Source
Index
i
Tonnage, Kt
Ti
Grade Metal Content
Sulfur, %
x1i
Gold, g/t
x2i
Sulfur, Kt
Ti
x1i
Gold, kg
T2
x2i
Concentrate 1 1 20 3.50 40 0.70 800
Concentrate 2 2 40 1.20 90 0.48 3,600
Total — 60 1.97 73.3 1.18 4,400
Table 8-2 Percentage of available tonnage and metal content in each concentrate
Material Source
Index
i Tonnage, %
Metal Content
Sulfur, % Gold, %
Concentrate 1 1 33 59 18
Concentrate 2 2 67 41 82
Total — 100 100 100
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Blending Strategy 111
a point on the diagram: concentrate 1 is at point A, and concentrate 2 is at
point B. The only feasible grades that can be obtained by blending concentrates 1 and 2 are those along the line AB. If only blends that contain more
than 1.5% sulfur are acceptable, the blend that maximizes the gold grade is
that which exactly satisfies the sulfur constraint; it is represented by point C
on the blending diagram.
If p1
is the percentage of concentrate 1 in the blend, and p2
the percentage of concentrate 2, the optimal blend is obtained by solving the following
equations:
+ =
+ =
p x p x 1.5%
p p 1
1 11 2 12
1 2
The concentrates should be fed to the roaster in the following proportions:
( ) ( ) =− −=
= − =
p 1.5% 1.2% 3.5% 1.2% 13%
p 1 13% 87%
1
2
Note that p1
and p2
are equal to the ratio of the line segments on the blending
diagram: p1
= CB/AB and p2
= AC/AB. After blending, the gold and sulfur
grades of the concentrate delivered to the roaster are
= + =
= + =
x p x p x 1.5% sulfur
x p x p x 83.5 g/t
10 1 11 2 21
20 1 21 2 22
20
30
40
50
60
70
80
90
100
Sulfur Grade, %
0 0.50 1.00 1.50 2.00 2.50 3.00 3.50 4.00
B
A
C Concentrate 2
Selected Blend
Feasible Blends
Concentrate 1
Not Acceptable Acceptable
Figure 8-1 Feasible blends for two concentrate stockpiles
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Gold Grade, g/t
112 CHAPTER EIGHT
The total tonnage of material sent to the roaster is To
, composed of t1
metric tons of concentrate 1 and t2
metric tons of concentrate 2, which must
satisfy the following equations:
= +
=
=
T t t
t T p
t T p
o 1 2
1 o 1
2 o 2
Neither t1
nor t2
can exceed the total tonnages, T1
and T2
, available in each
stockpile. Therefore, the maximum value of To
is the smallest value of Ti
/pi
.
( )
= =
= =
= =
= ⋅ =
= ⋅ =
T p 20 0.13 154 thousand metrictons
T p 40 0.87 46 thousand metrictons
T minimum 154, 46 46 thousand metric tons
t 13% 46 6 thousand metric tons
t 87% 46 40 thousand metrictons
1 1
2 2
o
1
2
The gold content of the roaster feed is
+ = ⋅ + ⋅ = t x t x 6 40 40 90 3,840 kg, or 123 thousand ounces of gold 1 11 2 21
Blending to Maximize Gold Content in Roaster Feed
In the previous example, the objective was to maximize the gold grade in the
roaster feed while maintaining a sulfur grade not less than 1.5%. This resulted
in 13% of stockpile 1 and 87% of stockpile 2 containing 3,840 kg of gold being
sent to the roaster. This example considers the economically more meaningful
objective of maximizing the amount of gold sent to the roaster while still satisfying the requirement that the sulfur content be not less than 1.5%.
The gold and sulfur contents vary with the proportion of each stockpile
sent to the roaster. Using the following formula, one can calculate the maximum tonnage To
of material sent to the roaster for different proportions p1
of concentrate 1:
= ( ) T minimum T p ,T p o 1 1 2 2
where p1
and p2
must be positive and their sum must be such that p1
+ p2
= 1.
Once the tonnage To
has been calculated for a given p1
, it is possible to deduce
the tonnages t1
and t2
of each stockpile sent to the roaster:
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Blending Strategy 113
=
=
t T p
t T p
1 o 1
2 o 2
Total tonnages and tonnages originating from each stockpile are plotted
in Figure 8-2. The sulfur and gold average grades of the blended material are
obtained using the following equations (Figure 8-3):
( )
( )
= + −
= + −
x p x 1 p x
x p x 1 p x
10 1 11 1 21
20 1 21 1 22
The corresponding sulfur and gold contents, To
x10 and To
x2o, respectively,
are shown in Figure 8-4. The blend that maximizes the gold content is composed of 33% concentrate 1 and 67% concentrate 2. This results in 60,000 t
of material being sent to the roaster, averaging 1.97% sulfur and 73.3 g/t gold
and containing 4,400 kg of gold. Figure 8-4 shows that when the proportion
of concentrate 1 decreases below 33%, the decrease in gold content is slow
while the decrease in sulfur content is very sharp. These trends are reversed
above 33%. An understanding of these relationships is fundamental if optimal blends are to be achieved under different cost, recovery, geochemical, or
operational conditions.
0
10
20
30
40
50
60
70
Percentage of Concentrate 1 in Blend, %
0 10 20 30 40 50 60 70 80 90 100
Blend with Maximum Tonnage
Total Metric Tons
Concentrate 1
Concentrate 2
Figure 8-2 Feasible tonnage of blended material, as a function of the percentage
p1
of stockpile 1
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Metric Tons, thousands
114 CHAPTER EIGHT
BLENDING T HREE MATERIAL TYPES
In the previous example, the case was considered where only two stockpiles
were available for blending. Now consider three stockpiles. Each stockpile
is characterized by its tonnage and two grades, as shown on Table 8-3. If all
stockpiles were blended to get a single product, the result would be seven
0.0
0.6
0.4
0.2
1.4
0.8
1.0
1.2
0
500
1,000
1,500
2,000
2,500
3,000
3,500
4,000
4,500
5,000
Percentage of Concentrate 1 in Blend, %
0 10 20 30 40 50 60 70 80 90 100
Blend with Maximum Tonnage
Sulfur Content
Gold Content
Figure 8-4 Metal content of blended material, as a function of the percentage p1
of
stockpile 1
0.5
2.0
1.5
1.0
4.0
2.5
3.0
3.5
30
90
80
70
60
40
50
100
Percentage of Concentrate 1 in Blend, %
0 10 20 30 40 50 60 70 80 90 100
Blend with Maximum Tonnage
Sulfur Grade Gold Grade
Figure 8-3 Average grade of blended material, as a function of the percentage p1
of stockpile 1
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Sulfur Content, Kt
Gold Content, kg
Sulfur Grade, %
Gold Grade, g/t
Blending Strategy 115
thousand metric tons of material with grade 1 equal to 1.03 and grade 2 equal
to 12.3. To get this result, the stockpiles would have to be blended in the following proportions (Table 8-4): 29% from stockpile 1, 14% from stockpile 2,
and 57% from stockpile 3.
The blending diagram in Figure 8-5 shows the relationship between
grade 1 and grade 2 for the three stockpiles. The three points, A, B, and C,
represent the stockpiles. The only grade combinations that can be obtained by
blending the three stockpiles are those located within the boundaries of the
triangle ABC, defined as the feasible blends domain.
Blending to Reach Specific Grades
Consider the case where a blend needs to be obtained with specific grades: x10
for grade 1 and x20 for grade 2. To obtain these grades, the stockpiles much be
blended in the following proportions, p1
, p2
, and p3
, such that
+ + =
+ + =
+ + =
p x p x p x x
p x p x p x x
p pp1
1 11 2 12 3 13 10
1 21 2 22 3 23 20
1 2 3
In addition, p1
, p2
, and p3
must be positive, a condition that will be satisfied if
the point with coordinates x10, x20 falls within the ABC triangle in Figure 8-5.
The solution to these equations is easily calculated:
Table 8-3 Stockpiles available for blending
Stockpile Index i
Stockpile
Tonnage,
Ti
Stockpile
Grade 1,
x1i
Stockpile
Grade 2,
x2i
Contained
Metal 1,
Ti
x1i
Contained
Metal 2,
Ti
x2i
1 1 2,000 1.00 7.0 2,000 14,000
2 2 1,000 2.00 12.0 2,000 12,000
3 3 4,000 0.80 15.0 3,200 60,000
Total 7,000 1.03 12.3 7,200 86,000
Table 8-4 Percentage of available tonnage and metal content in each stockpile
Stockpile Index i Tonnage, % Metal 1, % Metal 2, %
1 1 29 28 16
2 2 14 28 14
3 3 57 44 70
Total 100 100 100
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116 CHAPTER EIGHT
( )( )( )( )
( )( ) ( )( )
( )( ) ( )( )
( )( ) ( )( )
=
= − − − − −
= − − − − −
=
= − − − − −
= − − − − −
= − −
p A B
A x x x x x x x x
B x x x x x x x x
p A B
A x x x x x x x x
B x x x x x x x x
p 1 p p
1 1 1
1 10 13 22 23 20 23 12 13
1 11 13 22 23 21 23 12 13
2 2 2
2 10 13 21 23 20 23 11 13
2 12 13 21 23 22 23 11 13
3 1 2
For example, if x10 = 1.20 and x20 = 11.0, then p1
= 40.0%, p2
= 26.7%, and
p3
= 33.3%. Knowing these proportions, one needs to calculate the maximum
tonnage of blended material that can be produced and the tonnage of each
stockpile that will be used (and therefore the tonnage that will remain in
stockpiles) to reach this blended tonnage.
The maximum tonnage of blended material is T0
made of t1
metric tons
of stockpile 1, t2
metric tons of stockpile 2, and t3
metric tons of stockpile 3:
= + + T t 0 1 t t 2 3
6
7
8
9
10
11
12
13
14
15
16
Grade 1
0.7 0.8 0.9 1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1
C
A
B
Stockpile 3: Tonnage = 4,000,
Grade 1 = 0.8, Grade 2 = 15
Stockpile 1: Tonnage = 2,000,
Grade 1 = 1, Grade 2 = 7
Total: Tonnage = 7,000,
Grade 1 = 1.03, Grade 2 = 12.3
Stockpile 2:
Tonnage = 1,000,
Grade 1 = 2,
Grade 2 = 12
Figure 8-5 Feasible blends domain for three stockpiles
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. Grade 2
Blending Strategy 117
The tonnage ti
that can be taken from stockpile i cannot exceed the total
tonnage Ti
of material in stockpile i. Using the previous example, the maximum value of T0
is the smallest of
= =
= =
= =
T p 2,000 40.0% 5,000 t
T p 1,000 26.7% 3,750 t
T p 4,000 33.3% 12,000 t
1 1
2 2
3 3
Therefore, T0
= 3,750 t. The material consumed and that remaining in stockpiles is summarized in Table 8-5. Stockpile 2 was entirely consumed, but
3,250 t remain in stockpile, of which 500 t are in stockpile 1 and 2,750 t in
stockpile 3.
Using Linear Algebra to Determine Stockpile Blends
The following equations were used to determine how three stockpiles should
be blended to obtain specific average grades:
+ + =
+ + =
+ + =
p x p x p x x
p x p x p x x
p pp1
1 11 2 12 3 13 10
1 21 2 22 3 23 20
1 2 3
These equations can be written using matrix notations:
Table 8-5 Material blended and processed, and material remaining in stockpile
Material
Type Index i
Tonnage, t
Ti
Percentage,
pi
Grade 1,
x1i
Grade 2,
x2i
Material blended and processed
Stockpile 1 1 1,500 40.00% 1.0 7.0
Stockpile 2 2 1,000 26.67% 2.0 12.0
Stockpile 3 3 1,250 33.33% 0.8 15.0
Total 0 3,750 100.00% 1.2 11.0
Material remaining in stockpiles
Stockpile 1 1 500 — — —
Stockpile 2 2 0 3.10% 2.0 12.0
Stockpile 3 3 2,750 96.90% 0.8 15.0
Total 0 3,250 100.00% 0.8 14.9
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
118 CHAPTER EIGHT
=
x x x
x x x
1 1 1
p
p
p
x
x
1
11 12 13
21 22 23
1
2
3
10
20
If X is the stockpile grade matrix, p the proportion vector, and x0
the
target grade vector, the proportions p are calculated as follows:
=
= −−
Xp x
p X x
0
1
0
The vector p is calculated by multiplying the inverse of the matrix X with the
vector x0
. Using the previous numerical example*:
=
=
− −
−
− −
=
p −
p
p
1.0 2.0 0.8
7 1
1 1
2 1
1
5
1.2
11
1
0.333 0.133 2.267
0.889 0.022 1.044
0.556 0.111 0.222
1.2
11
1
40.0%
26.7%
33.3%
1
2
3
1
These equations do not guarantee that the proportions pi are all between 0
and 1. Indeed if, in the blending diagram, the point defined by the vector x0
is outside the ABC feasible area, proportions greater than 1 and less than 0
will be calculated.
BLENDING TO MAXIMIZE TONNAGE
There are circumstances where the objective is to maximize the tonnage of
blended material subject to specified grade constraints. The tonnages that can
be obtained by blending are those that correspond to points falling within the
* The matrix inversion was performed using the Microsoft Excel function
MINVERSE.
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Blending Strategy 119
ABC feasible domain shown in Figure 8-5. To understand the relationship
between grade constraints and tonnages, one must understand how tonnages
vary within the feasible domain. Using the method previously described,
the tonnage To
can be calculated for all points within the feasible domain.
The results are shown in Figure 8-6. One obtains a two-dimensional grade–
tonnage surface, akin to the more familiar one-dimensional grade–tonnage
curve. The constant-tonnage curves, defined as Iso-T lines, are composed of
line segments that are parallel to the sides of the ABC triangle. This property
of the Iso-T lines is explained in Example 7 in Appendix A.
Blending to Maximize Metal Content
There are circumstances, such as the one presented in the two-stockpiles
example, where the objective is to maximize the metal content of the blended
material, subject to specific grade constraints. For example, the objective
might be to maximize the gold content, subject to the sulfur grade being
within specified limits. Optimizing metal content requires understanding
how this content varies within the feasible domain of blended material.
Using the same example as previously mentioned, the metal content Q20 =
To
x20 was calculated for all points within the feasible domain, and the results
were contoured as shown in Figure 8-7. A surface is obtained that represents
the relationship between gold content and both sulfur and gold grades. This
6
7
8
9
10
11
12
13
14
15
16
Grade 1 of Blended Material
0.7 0.8 0.9 1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1
4,000
2,000
7,000 1,000
Figure 8-6 Grade–tonnage relationship and constant tonnage (Iso-T) lines of
blended material
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
5,000
6,000
Grade 2 of Blended Material
2,000
3,000
2,500
1,500
2,500
3,000
4,000
5,000
120 CHAPTER EIGHT
relationship can be represented by contour lines, defined as Iso-Q lines, along
which the gold quantity is constant. These lines are composed of segments
that are no longer parallel to the sides of the ABC triangle.
Blending to Satisfy Ratio Constraints
Some circumstances occur where the constraints are on variables, such as
ratios, that cannot be averaged between stockpiles. For example, in a nickel
laterite operation, there might be a requirement on the silica-to-magnesia
ratio. The ratio of a blended product is not equal to the weighted average of
the individual stockpile ratios. Using the same example as above, one can calculate the ratio between the two grades (grade 2 divided by grade 1) and plot
it as shown in Figure 8-8. The optimal blend might be that which maximizes
one of the variables while maintaining the ratio between two other variables
within specified boundaries.
REMARKS CONCERNING AN INCREASINGLY COMPLEX
BLENDING PROBLEM
The methods described previously can be used to optimize blending of any
number of stockpiles when the difference between the number of stockpiles
and the number of grade or quality constraints is exactly equal to 1. It was
6
7
8
9
10
11
12
13
14
15
16
Grade 1 of Blended Material
0.7 0.8 0.9 1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1
60,000
86,000
14,000
12,000
Figure 8-7 Grade–metal content relationship and constant metal content (Iso-Q)
lines of blended material (metal 1)
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
70,000
15,000
20,000
30,000
Grade 2 of Blended Material
60,000
50,000
40,000
30,000
20,000
Blending Strategy 121
also assumed that the objective function was to maximize tonnage or metal
content, subject to specified constraints on grade or quality. When these conditions are not satisfied, defining an optimal blending strategy can become
increasingly complex, and mathematical programming methodologies have
to be considered, which fall outside the scope of this book (see bibliography).
In the previous examples, it was assumed that the stockpiles already
existed. A similar situation would be that where consideration is given to
blending production from mines with fixed yearly production, such that tonnage, grade, and quality of material available for blending are known. In such
situations, the feasible domain is fully defined by the tonnages and grades/
qualities available from the stockpiles or from the different mines. When
considering new mines that are not yet operating, a stockpiling strategy needs
to be developed to optimize the feasibility of the project. Depending on the
geological properties of the deposit, a number of stockpiling options are likely
to be feasible, each stockpile being defined by both upper and lower cut-off
grades. Depending on deposit geology, mine schedule, and cut-off grades,
there is likely to be a very large number of feasible stockpile options. On the
blending diagram, the feasible domain defined by the stockpiles must contain
the target point where the requirements imposed on the blended product
are satisfied. In addition, the stockpiles should be such that when blended in
6
7
8
9
10
11
12
13
14
15
16
Grade 1 of Blended Material
0.7 0.8 0.9 1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1
y/x = 18.75
y/x = 7
y/x = 6
Figure 8-8 Grade–metal ratio relationship and constant ratio (Iso-R) lines of
blended material
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
y/x = 8
y/x = 10
y/x = 12
y/x = 14
Grade 2 of Blended Material
122 CHAPTER EIGHT
the required proportions, they are consumed in their entirety. Solving this
problem, known as the inverse blending problem, can be extremely complex.
A number of mine planning optimization tools have been developed to assist
engineers in developing stockpiling and corresponding cut-off grade strategies that maximize specified objective functions during the life of a mining
operation.
The previous examples also assume a deterministic environment, where
the stockpile properties are known and constant throughout the life of the
stockpile. In practice, there is always uncertainty concerning stockpile properties. A blending solution that is optimal under deterministic assumptions
is not likely to be acceptable in the presence of uncertainty. A small variation
in stockpile properties may result in a blended product that does not satisfy
specified requirements. In such situations, the multivariate distributions
of the properties of the different sources of material must be considered to
develop a stockpiling and blending strategy that is flexible and can adapt to
change. This strategy might be quite different from the deterministic solution.
The complexity of the blending problem also increases significantly when
constraints are on variables that cannot be averaged, such as ratios between
two grades. Considerable research is dedicated to finding solutions to these
complex situations. Development of appropriate algorithms and related computer programs is aimed at bringing practical solutions to practitioners (see
the bibliography).
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123
9
The cut-off grade determines the tonnage and average grade of material processed and is critical in the determination of the economic feasibility of a project. All consequences of choosing a cut-off grade must be taken into account,
including technical, economic, legal, environmental, social, and political as
illustrated by the following fundamental equation:
() () () () = + + U x U x U x U x dir opp oth
This equation represents the utility of sending material of grade x to a given
destination. The optimal cut-off grade between two options is that where the
utility U1
(x) of one option is equal to the utility U2
(x) of the other option.
Udir(x) represents direct revenues and costs. If only this term is taken into
account, the cut-off grade between two options is
( ) ( ) ( )( ) = + + − + +
− −
x M P O M P O r r V R c 1 1 1 2 2 2 1 2
Uopp(x) represents the opportunity cost of mining or processing material
that was not scheduled to be mined or processed, and there are operating
constraints. This cost is proportional to the net present value of future cash
flows, and inversely proportional to the size of the constraints imposed on
production:
( ) = − ⋅ ⋅ U x t i NPV opp i
Because the net present value of future cash flows decreases over time,
optimization of project economics is usually best achieved with high cut-off
grades at the beginning of the mine life and lower cut-off grades at the end.
Uoth(x) represents other costs that must be taken into account that are
often not quantifiable in dollar terms. These costs can be highly significant
Closing Remarks
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124 CHAPTER NINE
and imply that net present value is typically not the only objective to be considered when optimizing cut-off grades.
Cut-off grade optimization is an iterative process. When planning a new
mining operation, a cut-off grade profile must be chosen to define operating
conditions, including mining rate, processing rate, volume of sales, capital
and operating costs, cash flow, and net present value. Because the optimal
cut-off grade is a function of operating costs and net present value, the first
mine plan is not likely to be optimal. Once a cash flow has been determined
under a specific set of assumptions—including assumptions related to cut-off
grades—the underlying cut-off grade strategy must be reevaluated. The sensitivity of the project economics must be analyzed as a function of changes in
cut-off grades.
As a feasibility study progresses over time, the properties of the deposit
are better understood as a result of additional drilling and improved modeling; mining and processing methods are better defined; constraints on
production are quantified; capital and operating costs are refined; and socioeconomic, environmental, and other costs are better understood. All these
changes should be taken into account when determining the cut-off grade.
The determination of cut-off grades must also consider all future costs.
During the feasibility study, these costs include the capital costs of building
the site. When the mine and mill are operating, these costs are sunk and
should no longer be taken into consideration. The cut-off grade strategy that
optimizes net present value is independent of sunk costs. During the feasibility study there are no capacity constraints, but capital expenditures are taken
into account to optimize cut-off grades. When the mine is operating, sunk
costs should no longer be taken into account to optimize cut-off grades. However, there are capacity constraints, which are the results of decisions made
during the feasibility study. If the estimates made during the feasibility study,
including those related to mine and mill capacities, hold true when the mine
is in operation, the optimal cut-off grade strategy remains unchanged. This
strategy is the same at the end of the feasibility study when capital costs are
taken into account to optimize the size of the facilities, and during operations
when capacity constraints are imposed by the built facilities.
But operating conditions are never identical to those assumed during the
feasibility study. These conditions change continuously:
• The actual mine and mill capacities differ from those which were
expected before construction.
• The mill recovery and optimal operating conditions are different
from planned.
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Closing Remarks 125
• The deposit properties differ from those in the model that was used
during the feasibility study.
• Costs are different from expected.
• Prices of products sold are different.
Consequently, cut-off grades should be continuously reviewed and changed
as conditions demand.
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Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
127
EXA M P L E 1 . N E T P R E S E N T VA L U E O F C O N S TA N T
CASH FLOW: PROOF OF FORMULA
Problem Statement
If a project is expected to generate a constant cash flow C over n years (Ck
=
C for k = 0, 1, …, n – 1), the net present value of this cash flow is
()() () = + + + + + + +
− NPV C 1 1 1 i 1 1 i 1 1 i i
2 n 1
Show that
()() () ( ) + ++ + + + + = − 1 1 1 i 1 1 i 1 1 i g i,n 2 n 1
where g(i,n) = [1 – (1 + i)–n] ∙ (1 + i)/i.
Solution
Define a = 1/(1 + i). Then
1 1 1 i 1 1 i 1 1 i 1 a a a a a 2 n 1 2 3 n 2 n 1 + ++ + ()() () + + + = + + +++ + ( ) ( ) − − −
If the right-hand side of this equation is multiplied by (1 – a), the following
result is obtained:
( ) + + +++ +
⋅ − = − ( ) ( ) − − 1 a a a a a 1 a 1 a 2 3 n 2 n 1 n
Therefore,
( ) ( ) + + +++ + = − − ( ) ( ) − − 1 a a a a a 1 a 1 a 2 3 n 2 n 1 n
Given that a = 1/(1 + i), this equation can be written as follows:
()() () () ( ) + ++ + + + + = − +
⋅ + − − 1 1 1 i 1 1 i 1 1 i 1 1 i 1 i i 2 n 1 n
Appendix A
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128 APPENDIX A
EXA M P L E 2 . N E T P R E S E N T VA L U E O F P E R P E T U I T Y
CASH FLOW: PROOF OF FORMULA
Problem Statement
Show that if a project is expected to generate a constant cash flow C to perpetuity, its net present value is NPVi
= C (1 + i)/i.
Solution
A proof was given previously that if a project generates a constant cash flow C
for n years, its net present value is NPVi
= C g(i,n), where
( ) ( ) ( ) = − +
⋅ + − g i,n 1 1 i 1 i i n
If n goes to infinity, then (1 + i)n
goes to infinity and (1 + i)–n goes to zero.
The limit of g(i,n) is
( )= + ( ) g i,n 1 i i
EXA M P L E 3 . O P P O R T U N I T Y C O S T O F M I N I N G A
PERIPHERAL DEPOSIT
Problem Statement
Consider the open pit mine shown in Figure A-1. Two parts of the deposit
remain to be mined:
1. A “main pit” that requires mining low-grade and waste material for
two years, followed by eight years of mining higher-grade material.
The cash flow generated during the first two years is expected to be
negative at $45 million per year. During the next eight years, a positive cash flow will be generated equal to $250 million per year.
2. A “mini-pit” that can be mined in one year and is expected to generate a positive cash flow of $90 million.
Under current conditions, the main pit can only be mined if the minipit area can be used as a waste dump. This leaves two options: Mine only the
main pit and condemn the mini-pit (option 1); or mine the mini-pit first followed by the main pit (option 2). Assuming a 15% discount rate, what is the
opportunity cost of mining the mini-pit first? Which one of the two options
would you recommend? If there were other locations where waste could be
dumped, a third option would be to mine the main pit first and the mini-pit
last (option 3). Which option would you recommend?
Repeat this analysis using a 5% discount rate.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Appendix A 129
Solution
The net present values of each option are calculated in Table A-1. To show the
influence that each pit has on the other, the expected main pit and mini-pit
undiscounted cash flows are shown separately. The discount factors 1/(1 + i)k–1
have been calculated for each year k using a discount rate i = 15%. The net
present value of each option is the sum of the product of undiscounted yearly
cash flows with a discount factor. Under option 1, only the main pit is mined
with net present value NPVi
= $891 million. Under option 2, mining the
main pit is postponed by one year. The main pit net present value is decreased
to NPV'i
= $775 million. The opportunity cost of mining the mini-pit first is
$891 – $775 = $116 million. The net present value of the mini-pit is only $90
million, not enough to pay for the opportunity cost. The NPV of option 2 is
$865 million, less than that of option 1. If the choice is between options 1 and
2, option 1 is that which should be chosen. Under option 3, the net present
value of the mini-pit is $22 million, and the total net present value is $913
million. If feasible, option 3 is the best choice.
If a 5% discount rate is used, the results are as shown in Table A-2. The
opportunity cost of mining the mini-pit first (option 2) is $69 million. The
mini-pit’s net present value is $90 million. Option 2 is better than option 1.
However, option 3 is still the best option.
Mini-Pit
Mining: 1 year
Cash Flow: $90 million/yr
Main Pit - Phase 2
Mining: 8 years
Cash Flow: $250 million/yr
Main Pit - Phase 1
Mining: 2 years
Negative Cash Flow: $45 million/yr
Figure A-1 Schematic representation of main pit and mini-pit
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130 APPENDIX A
EXA M P L E 4 . S I M P L I F I E D E Q U AT I O N TO E S T I M AT E
OPPORTUNITY C O S T: V E R I F I C AT I O N O F F I R S T- O R D E R
APPROXIMATION
Problem Statement
Show that for small values of t, the difference between the exact formula [1 –
(1 + i)–t] NPVi
and its first-order approximation i ∙ t ∙ NPVi
is less than 10%.
Compare the two formulas for t varying from zero to two hundredths of a
year (approximately one week) and i = 15%.
Solution
Figure A-2 shows the relationship between 1 – (1 + i)–t and i ∙ t as a dotted
line. The maximum value of i ∙ t is 0.02 ∙ 15% = 0.003. The discount factor
Table A-1 Cash flow and net present value of options 1 to 3 (discount rate i = 15%)
Year k
Discount
Factor
1/(1 + i)k
Option 1 Option 2 Option 3
Main Pit Mini-Pit Main Pit Mini-Pit Main Pit Mini-Pit
0 1.000 ($45) — $90 ($45) —
1 0.870 ($45) — ($45) — ($45) —
2 0.756 $250 — ($45) — $250 —
3 0.658 $250 — $250 — $250 —
4 0.572 $250 — $250 — $250 —
5 0.497 $250 — $250 — $250 —
6 0.432 $250 — $250 — $250 —
7 0.376 $250 — $250 — $250 —
8 0.327 $250 — $250 — $250 —
9 0.284 $250 — $250 — $250 —
10 0.247 — — $250 — $90
Net present value per pit $891 $0 $775 $90 $891 $22
Opportunity cost $0 — ($116) — $0 —
Total net present value $891 $865 $913
Table A-2 Cash flow and net present value of options 1 to 3 (discount rate i = 5%)
Option 1 Option 2 Option 3
Main Pit Mini-Pit Main Pit Mini-Pit Main Pit Mini-Pit
Net present value per pit $1,451 $0 $1,382 $90 $1,451 $55
Opportunity cost $0 — ($69) — $0 —
Total net present value $1,451 $1,472 $1,506
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Appendix A 131
calculated using the first-order approximation, i ∙ t, is less than 10% higher
than that using the exact equation, 1 – (1 + i)–t. This difference decreases for
smaller values of i.
EXAMPLE 5. OPPORTUNITY COST OF NOT USING T HE
OPTIMAL CUT-OFF GRADE IN A COPPER MINE
Problem Statement
Consider a copper mine in which the material can be either leached (process 1) or sent to a flotation plant (process 2). The relevant operating conditions are summarized as follows:
Leach recovery: r
1
= 57%
Mill recovery: r2
= 89%
Leach processing cost: P01 = $2.50 per metric ton leached
(including overhead)
Mill processing cost: P02 = $29.00 per metric ton milled
(including overhead)
Copper price: V = $2.50 per pound of salable copper
(after cost of sales)
Demonstrate that the cut-off grade xc
between leach and mill is 1.50% Cu.
0.0000
0.0030
0.0025
0.0020
0.0015
0.0010
0.0005
x = 1 – 1/(1 + i)t
0.000 0.0005 0.0010 0.0015 0.0020 0.0025 0.0030
i = 15%
y = x
y = 1.10x
Figure A-2 Comparison of 1 – (1 + i)–t and i · t for i = 15% and t less than 0.02 years
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved. y = i·t
132 APPENDIX A
The mill capacity is such that it can only accept material exceeding xs
=
1.60% Cu. The tonnage and metal content of material above the two cut-off
grades are as follows:
Above xc
= 1.50% Cu: 10.842 million metric tons containing
588.84 million lb of copper
Above xs
= 1.60% Cu: 9.606 million metric tons containing
546.59 million lb of copper
What is the opportunity cost of sending material averaging between xc
and xs
to the leach pad instead of the mill?
Solution
The cut-off grade between mill and leach is
[ ]
( ) ( )
( ) ( )
= − −
= − − ⋅ ⋅ =
x P P r r V
x 29.00 2.50 89% 87% 2.5 2,205 1.50% Cu
c o1 o2 1 2
c
A change in cut-off grade from xc
= 1.50% Cu to xs
= 1.60% Cu results
in moving 1.236 million metric tons containing 42.25 million lb of copper
from the mill to the leach pad. The result is a savings in processing costs and
a loss of revenue:
Cost savings: [T(xs
) – T(xc
)] ∙ (Po2 – Po1) = 1.236 ∙ (29.00 – 2.50)
= $32.75 million
Revenue loss: [Q(xs
) – Q(xc
)] ∙ (r2
– r1
) ∙ V = 42.25 ∙ (89% – 57%) ∙ 2.5
= $33.80 million
Total opportunity cost = 33.80 – 32.75 = $1.05 million
For the mill to accept all material above 1.50% Cu, its capacity would
have to be increased by 13%. Such an increase would be justified only if it
could be achieved for less than $1.05 million.
EXA M P L E 6 . S TO C K P I L I N G A N D C U T- O F F
DETERMINATION IN A COPPER MINE
Problem Statement
Consider an open pit copper mine in which material can be sent to a flotation
plant, a stockpile, or a waste dump. The parameters that apply to each option
are listed in Table A-3. You are asked to do the following:
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Appendix A 133
• Calculate and plot the utility of each option as a function of the
copper grade.
• Calculate the cut-off grade between waste, stockpile, and mill. Interpret the results.
• Which cut-off grades would apply to the stockpile if the mill capacity
is such that only material exceeding 0.35% Cu can be processed?
Solution
Table A-4 shows the mining and processing costs per year for waste dump,
direct mill, and stockpile options. In this table, the $0.10 yearly cost per ton of
material stockpiled applies to years 1 to 4, whereas the $1.00 cost of retrieving
one ton of material from stockpile is only incurred in year 4. The $0.05 yearly
Table A-3 Copper mine operating parameters
Milled material
Mo $1.90 Mining cost per metric ton of ore mined and shipped to the mill,
including mine overhead
Po $10.00 Processing cost per metric ton of ore, including process overhead
r 86% Copper recovery for fresh material
Wasted material
Mw $2.00 Mining cost per metric ton of waste mined and placed on waste dump,
including mine overhead
Pw $0.05 Yearly cost per metric ton of waste dumped, including stockpile
maintenance and water treatment plant operating cost
Stockpiled material
Mstp1 $2.50 Mining cost per metric ton of material mined and stockpiled, including
overhead and capital cost per metric ton for pad preparation
Pstp $0.10 Yearly cost per metric ton of material stockpiled, including stockpile
maintenance and water treatment plant operating cost
Mstp2 $1.00 Cost per metric ton to retrieve material from stockpile and ship it to the
mill, including environmental remediation and overhead
dr –3% Loss of recovery due to oxidation during life of stockpile
Life of mine
n 5 Life of stockpile in years, including year 0 when ore is mined and year 4
when stockpile is processed
Value of recovered copper
V $3.00 Value of one pound of copper recovered, net of shipping and smelting
costs, and other costs of sale
Discount rate
i 10% Discount rate per year
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134 APPENDIX A
Table A-5 Undiscounted and discounted costs per metric ton mined, and
revenues per pound processed
Year
Total Cost per Metric Ton
Dollar per Pound
of Cu Contained Discount
Factor,
Waste Mill Stockpile Waste Mill Stockpile 1/(1 + i)n
0 ($2.00) ($11.90) ($2.50) — $2.58 — 1.000
1 ($0.05) — ($0.10) — — — 0.909
2 ($0.05) — ($0.10) — — — 0.826
3 ($0.05) — ($0.10) — — — 0.751
4 To infinity — ($11.10) — — $2.49 0.683
Total
Undiscounted Undiscounted
($7.00) ($11.90) ($13.90) $0.00 $2.58 $2.49
Discounted Discounted
($2.55) ($11.90) ($10.33) $0.00 $2.58 $1.70
cost per metric ton of waste applies to perpetuity. Table A-5 shows the total
cost (mining plus processing) per year for the three processes, and the corresponding value per pound contained in material processed. For direct mill
feed, the value per pound is r V = 86% ∙ $3.00 = $2.58, which is recovered in
year 0. For material stockpiled, this value is (r + dr) V = (86% – 3%) ∙ $3.00
= $2.49 per pound, which is recovered in year 4.
Also shown in Table A-5 are cumulative costs per metric ton and value
per pound, both discounted and undiscounted, for as long as the material
under consideration carries costs (to perpetuity for waste, five years for stockpiled material, one year for direct mill feed). For stockpiled material, the
undiscounted value is based on the assumption that the $0.05 yearly cost will
apply to 100 years, starting in year 1. The discounted value of the $0.05 cost
to perpetuity is $0.05 ∙ (1 + i)/i = 11 ∙ $0.05 = $0.55.
Table A-4 Mining and processing costs per year for material wasted, milled,
and stockpiled
Year
Mining Cost per Metric Ton Processing Cost per Metric Ton
Waste Mill Stockpile Waste Mill Stockpile
0 ($2.00) ($1.90) ($2.50) — ($10.00) —
1 ($0.05) — ($0.10) — — —
2 ($0.05) — ($0.10) — — —
3 ($0.05) — ($0.10) — — —
4 To infinity — ($1.10) — — ($10.00)
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Appendix A 135
The utility of sending one metric ton of material to a given process is
equal to the net present value of the cash flow generated by this ton. For example, if one metric ton of material of grade x is sent to the stockpile, the net
present value of this decision is NPVstp = –$10.33 + $1.70 ∙ 2,205 ∙ x, where x
is expressed in % Cu and 2,205 is the number of pounds per metric ton. The
three net present values can be written as follows:
For waste: Uwaste(x) = –$2.55
For direct feed: Uore(x) = –$11.90 + 2.58 ∙ 2,205 ∙ x
For stockpile: U
stp(x) = –$10.33 + 1.70 ∙ 2,205 ∙ x
These lines are plotted in Figure A-3. The cut-off grades between two processes are defined by the point of intersection of the lines corresponding to
these processes:
Waste-mill cut-off grade: ( )
( ) = −
⋅ = x 11.90 2.55
2.58 2,205
0.16% Cu c
Waste-stockpile cut-off grade: ( )
( ) = −
⋅ = x 10.33 2.55
1.70 2,205
0.21% Cu c
Mill-stockpile cut-off grade:
[ ]
( )
( ) = −
− ⋅ = x 11.90 10.33
2.58 1.70 2,205
0.08% Cu c
As one would expect, if there is no mill capacity constraint, the best decision is to waste all material below 0.16% Cu and to send material above 0.16%
Cu directly to the mill. However, if the mill capacity is such that only material
above 0.35% Cu can be processed, all material between 0.21% Cu and 0.35%
Cu should be stockpiled and processed at a later date (Figure A-4).
EXA M P L E 7 . P R O P E R T I E S O F C O N S TA N T- M E T R I C - TO N S
CURVES IN BLENDING DIAGRAMS
Problem Statement
Figure A-5 shows the relationship between three stockpiles, i = 1,3. The tonnage of material in stockpile i is Ti
with grade x1i and x2i. The first grade, x1
,
is plotted on the horizontal axis, while the second grade, x2
, is plotted along
the vertical axis. The stockpiles are represented by the points A, B, and C.
The objective is to blend the three stockpiles to obtain a product of grade
x10, x20. The proportions in which the stockpiles are blended is pi
, i = 1,3. The
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136 APPENDIX A
(15)
15
10
5
0
(5)
(10)
Grade, % Cu
0.10 0.20 0.30
Waste-Mill
Cut-off: 0.16% Cu
Waste-Stockpile
Cut-off: 0.21% Cu
Figure A-3 Net present value of three options: best option with no mill capacity
constraint
(15)
15
10
5
0
(5)
(10)
Grade, % Cu
0.10 0.20 0.30
Mill Capacity
Cut-off: 0.35% Cu
Waste-Stockpile
Cut-off: 0.21% Cu
Figure A-4 Net present value of three options: best option with mill capacity
constraint
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Stockpile
Mill
Profit, $/t Profit, $/t
Appendix A 137
maximum tonnage of blended material is T0
. It was shown in chapter 8 that
T0
is equal to the smallest value of the ratios Ti
/pi
.
Show that, on graphs such as Figure A-5, the shapes that define blends
with the same maximum tonnage (Iso-T shapes, on which T0
is a constant) are
made of line segments parallel to the lines AB, AC, or AD.
Solution
For the tonnages T0
to be constant, the proportion pi applicable to one of the
stockpiles must remain constant so that the ratio Ti
/pi
remains constant. If
a line is drawn from A (stockpile 1), which intersects an Iso-T line in D and
the line BC in E, the proportion p1
is equal to the ratio DE/AE (Figure A-5).
If another line AE' is drawn, which intersects the same Iso-T line in D', the
proportion p'1
is equal to the ratio D'E'/AE'. If stockpile 1 is that which limits the maximum tonnage T0
, the proportions p1
and p'1
must be equal. The
ratios DE/AE and DE'/AE' are equal only if the Iso-T line DD' is parallel to
the line BC.
6
7
8
9
10
11
12
13
14
15
16
Grade 1 of Blended Material
0.7 0.8 0.9 1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 2.0 2.1
C
E'
D'
D
E
A
B
Figure A-5 Relationship between stockpile properties and lines with constant
tonnage
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Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
139
Symbol Description
C constant yearly cash flow
c constant tail in recovery function
CI revenues required every year during n years to get a return on
investment i on a capital investment I: CI
= I / g(i,n)
Ck cash flow generated by a project in year k, k = 0, 1, 2, …, n
CR expected end-of-life reclamation costs
Cs smelter costs per metric ton of concentrate
Ct cost of shipping one metric ton of concentrate to the smelter
d1 metal grade deducted from recovered grade in calculation of
smelter payment for metal 1
DIMC discounted incremental mining costs
DIPC discounted incremental processing costs
DIR discounted incremental revenues
dPo
(T+c)/dT+c first-order derivative of Po
(T+c) with respect to T+c
dQ+c/dT+c first-order derivative of Q+c with respect to T+c
dr(T+c)/dT+c first-order derivative of r(T+c) with respect to T+c
dU(T+c)/dT+c first-order derivative of U(T+c) with respect to T+c
g(i,n) = [1 − 1/(1 + i)n
](1 + i)/i
I capital cost invested
i minimum rate of return (discount rate)
K concentration ratio defined as number of metric tons of
material that must be processed to produce one metric ton of
concentrate
M mining cost per metric ton processed
Mo mining cost per metric ton of ore
List of Symbols
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140 LIST OF SYMBOLS
Symbol Description
Mo1 value of Mo
for process 1
Mo2 value of Mo
for process 2
Mstp current mining costs per metric ton delivered to low-grade
stockpile
Mw mining cost per metric ton of waste
n number of years
NPV net present value
NPVi net present value of future cash flows, calculated using the
discount rate i
NSR(x1
, x2
) net smelter return, defined as returns from selling concentrate
produced from one metric ton of ore with average grades x1
, x2
,
less smelting charges
NSRc NSR cut-off between processing and wasting one metric ton of
material
Oo overhead cost per metric ton of ore
Oo1 value of Oo
for process 1
Oo2 value of Oo
for process 2
Ostp current overhead costs associated with mining and stockpiling
one metric ton of low-grade material
Ow overhead cost per metric ton of waste
p1 proportion of metal 1 contained in concentrate that is paid for
by smelter
p2 proportion of metal 2 contained in concentrate that is paid for
by smelter
pi in Chapter 8, proportion of stockpile or concentrate i in
blended material
Po processing cost per metric ton of ore
Po
(T+c) processing cost per metric ton of ore processed, if plant capacity
is T+c
Po1 processing cost for process 1
Po2 processing cost for process 2
Pstp net present value of future costs of stockpiling material that will
be processed later
Pw processing cost per metric ton of waste
Pwaste net present value of future costs of wasting material
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
List of Symbols 141
Symbol Description
Q(x) quantity of metal in material whose grade is greater than x
Q+c quantity of metal contained in material above cut-off grade
xc
: Q+c = T+c ∙ x+c
R refining, transportation, and cost of sales per unit of product
sold
r recovery, or proportion of valuable product recovered from the
mined material
r(T+c) processing plant recovery, if plant capacity is T+c
r(x) process recovery for material of average grade x
R1 value of R for process 1
R2 value of R for process 2
r1 value of r for process 1
r2 value of r for process 2
rc constant recovery after subtracting constant tail c
Rstp refining, transportation, and cost of sales per unit of product
sold from stockpile at the time product is sold
rstp recovery expected at the time stockpiled material is processed
s stripping ratio, defined as tons of waste per tons of ore
T tonnage of ore and waste to be mined
t time, measured in years
T+c tonnage above cut-off grade
Ti tonnage of material in stockpile or concentrate i
t
i tonnage of stockpile or concentrate i in blended material
To tonnage of material in blended material
Tw tonnage of waste to be mined
U(T+c) utility of running the plant at T+c capacity for one year
U(x) utility of sending one metric ton of material of grade x to a
given process: U(x) = Udir(x) + Uopp(x) + Uoth(x)
U1
(x) utility of sending one metric ton of material of grade x to
process 1
U2
(x) utility of sending one metric ton of material of grade x to
process 2
Udir(x) direct utility (profit or loss) of processing one metric ton of
material of grade x
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142 LIST OF SYMBOLS
Symbol Description
Ujk utility of mining block j in year k
Ujk,dir direct utility of mining block j in year k
Ujk,opp opportunity cost of mining block j in year k
Ujk,oth other utility of mining block j in year k
Umax(x) maximum utility resulting from sending material of grade x to
either of two processes
Uopp(x) opportunity cost or benefit of changing the processing schedule
by adding one metric ton of grade x to the material flow
Uore(x) utility of mining and processing one metric ton of material of
grade x
Uore(x1
, x2
) utility of sending one metric ton of material with metal grades
x1
, x2
to the processing plant
Uoth(x) utility of other factors that must be taken into account in the
calculation of cut-off grades
Ustp(x) utility of stockpiling material of grade x
Uwaste(x) utility of mining and wasting one metric ton of material of
grade x
V value of one unit of valuable product
V1 value of one unit of product 1, such as one pound of copper
V2 value of one unit of product 2, such as one ounce of gold
Vstp dollar value of the product recovered from stockpile at the time
product is sold
x average grade
x+c average grade above cut-off grade xc
x1e grade equivalent expressed in terms of metal 1
x2e grade equivalent expressed in terms of metal 2
x1i average grade of metal 1 in stockpile or concentrate i
x2i average grade of metal 2 in stockpile or concentrate i
xc cut-off grade
xc1 cut-off grade 1, taking only operating costs into account
xc2 cut-off grade 2, taking into account operating costs and
undiscounted capital cost per metric ton
xc3 cut-off grade 3, taking into account operating costs and
discounted capital cost per metric ton
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List of Symbols 143
Symbol Description
xc4 cut-off grade 4, taking into account operating costs, discounted
capital cost per metric ton, and opportunity costs
xs selected cut-off grade
YCF yearly cash flow
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Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
145
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Dimitrakopoulos, R. 2011. Stochastic optimization for strategic mine planning: A
decade of developments. J. Min. Sci. 84(2):138–150.
Duckworth, I., Casten, T., and Rakidjan, M. 2012. Overview of Freeport-McMoran’s
proposed DMLZ mine at Grasberg. Min. Eng. 62(8):20–26.
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APCOM Symposium. Wollongong, Australia: The Australasian Institute of Mining and Metallurgy. September 2011. pp. 371–380.
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149
Note: f. indicates figure; n. indicates (foot)note; t. indicates table.
Agricola, Georgius, on separation, 1
Blending, 109
coal of different characteristics, 109
complex cases (inverse blending
problem), 120–122
gold of different characteristics, 109,
110–113, 110t., 111f., 113f.,
114f.
iron of different characteristics, 109
linear algebra in determining
stockpile blends, 117–118
to maximize gold content, 110t.,
112–113, 113f., 114f.
to maximize gold grade, 110–112,
110t., 111f.
to maximize metal content, 119–120,
120f.
to maximize tonnage, 116f., 118–120,
119f., 120f., 121f.
to reach specific grades, 115–117,
115t., 116f., 117t.
to satisfy ratio constraints, 120, 121f.
strategy, 16
three material types, 114–118, 115t.,
116f., 117t.
two material types, 110–114, 110t.,
111f., 113f., 114f.
See also Stockpiles and stockpiling
Block caving
and capital cost, 93
constraints imposed by, 91–92
and cut-off grades, 91
economic valuation example (copper
mine), 95–98
marginal cut-off grade and block
design, 93
marginal cut-off grade and drawpoint
management, 92
and minimum rate of return, 93, 95,
96, 97
opportunity cost, 94–95
and yearly cash flow, 94
Breakeven cut-off grade, 8, 17
without capacity constraints (copper
mine), 58
and polymetallic deposits, 32–38
Capacity constraints, 124
and decreasing cut-off grade and NPV
over time (copper mine), 61–63,
62t., 63f., 64t., 65f.
and increased cut-off grade (copper
mine example), 56–61, 59t., 60t.
and opportunity cost, 12–14, 53
and opportunity cost with lowered
cut-off grade (gold leaching),
53–56, 54f., 55f.
Index
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150 INDEX
and pushback mining, 88-89
underground mines, 23
See also Mill capacity
Capital costs, 101, 102
constraints on, and changes in
opportunity cost, 107
Cash flow
constant over n years, 11, 12t., 127
constant to perpetuity, 11, 12t., 128
See also Net present value; Yearly cash
flow
Closure and reclamation costs, 105
Coal, 109
Concentrates, 9
Constant metal content lines. See Iso-Q
lines
Constant ratio lines. See Iso-R lines
Constant tail model, 30–31
precious metal example, 31–32, 32f.,
33f.
Constant-tonnage curves. See Iso-T lines
Copper
block caving and opportunity cost,
95–98
breakeven cut-off grade without
capacity constraints, 58
capacity constraints and decreasing
cut-off grade and NPV over time,
61–63, 62t., 63f., 64t., 65f.
capacity constraints and increased
cut-off grade, 56–61, 59t., 60t.
grinding circuit optimization, 44–52,
46f., 46t., 47f., 49f., 50f., 50t.,
51f., 51t.
mine and mill cut-off grades in open
pit mines, 20–22, 22f., 23f.
opportunity cost and cut-off grades
with mill capacity constraint,
59–60
opportunity cost and cut-off grades
with mine capacity constraint,
60–61
opportunity cost and cut-off grades
with refinery capacity constraint,
61
opportunity cost of not using optimal
cut-off grade, 131–132
releasing capacity constraints, 81–85,
83t., 84t.
stockpiling and cut-off determination,
132–135, 133t., 134t.
See also under Polymetallic deposits
Costs
capital, 101, 102, 107, 124
closure and reclamation, 105
and cut-off grade, 101–105
fixed, 101
future, 124
incremental capital expenditures,
104–105
leaching operation, 103, 104t.
and minimum return on investment,
102–103
operating, 102, 107
other (environmental, political, etc.),
15–16
overhead, 105
to perpetuity, 105
and stakeholders, 105–107
of stockpiling of low-grade material,
103
sunk, 102, 124
sustaining capital, 103–104
variable, 101
Cut-off grades
below marginal cut-off grade, 63–66
between ore and waste, 9, 17–18
and blending strategy, 16
breakeven calculations, 8, 17
and closure and reclamation costs,
105
and costs and benefits, 1–2, 12–16
decreasing, and NPV decrease over
time (copper mine), 61–63, 62t.,
63f., 64t., 65f.
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Index 151
defined, 1, 5
and fixed mine capacity, 76–78, 77f.
and fixed processing capacity, 69–76,
71f., 74f., 75f.
and fixed sales volume, 78–81, 80f., 82f.
fundamental equation, 6, 123–124
and grade-tonnage relationship, 6–7,
7f., 8f.
and grinding circuit optimization,
44–52
and increased mining capacity with
constant processing capacity, 2
and incremental capital expenditures,
104–105
and leaching operation costs, 103, 104t.
and low-grade stockpiles, 40–43, 103
and net present value, 2, 3, 10
and opportunity cost, 13–14, 38–40,
39f.
optimization as iterative process, 124
optimization with opportunity costs,
66–67
and overhead costs, 105
and price fluctutations, 2
and profitability, 2
and published reserves, 2–3
purposes of, 1
and stakeholders’ interests, 3
and sustaining capital, 103–104
and time-space considerations, 3
and utility functions, 17–18, 19f.
See also Breakeven cut-off grade;
Mine (external) cut-off grade;
Mill (internal) cut-off grade;
Process comparison cut-off
grade; Variable recovery cut-off
grade
Cut-off values, 34
De Re Metallica, 1
Direct profit or loss, 8–9
precious metal example, 9–10
Discount rate. See Minimum rate of
return
Discounted incremental mining costs
(DIMC), 71–72
Discounted incremental processing cost
(DIPC), 78
Discounted incremental revenues
(DIR), 72, 78
The Economic Definition of Ore: Cut-Off
Grades in Theory and Practice, 3
Ex-pit cut-off grade. See Mine (external)
cut-off grade
External cut-off grade. See Mine
(external) cut-off grade
Fixed sales volume
and fixed mining rate with no
processing constraint, 81, 82f.
and fixed processing rate with no
mining constraint, 79–81, 80f.
with no mining or processing
constraint, 78–79
Gangue, negative effects of, 2
Geologic constraints, 66, 67
and assessment of releasing capacity
constraints, 81–85, 83t., 84t.
See also Mine capacity
Gold
capacity constraints and opportunity
cost with lowered cut-off grade,
53–56, 54f., 55f.
and constant tail model, 30–32, 32f.,
33f.
cut-off grade and specific costs,
103–104, 104t.
cut-off grade between two processes,
26–28, 28f.
cut-off grade in plant capacity
optimization, 76–78, 77f.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
152 INDEX
cut-off grade with fixed sales and no
mining or processing constraint,
78–79
cut-off grade with fixed sales, fixed
mining rate, and no processing
constraint, 81, 82f.
cut-off grade with fixed sales, fixed
processing rate, and no mining
constraint, 79–80, 80f.
cut-off grade with variable recovery,
28–30, 29f., 30f.
of different characteristics, blending,
109, 110–113, 110t., 111f.,
113f., 114f., 119–120, 120f.
mine selectivity, deposit modeling,
ore control, and cut-off grade,
98–100, 99f., 100t.
opportunity cost in mine capacity
optimization, 72–76, 74f., 75f.
opportunity cost of increased
tonnage, 14–15
optimization of stope size, 24–26
use for high-sulfide, low-gold ore, 16
See also under Polymetallic deposits
Grade-tonnage relationship, 6–7, 7f., 8f.
and constant metal content (Iso-Q)
lines, 119–120, 120f.
and constant-tonnage curves (Iso-T
lines), 119, 119f., 135–137, 137f.
Grinding circuit optimization, 44
advantages of finer and coarser grinds,
44
copper mine example, 45–52, 46f.,
46t., 47f., 49f., 50f., 50t., 51f., 51t.
and expected grade-tonnage
relationship, 45–48, 46f., 46t.,
47f.
formula, 44–45
and incremental utility–tonnage
relationship, 50–52, 51f., 51t.
and operating cost–tonnage
relationship, 48, 49f., 50f., 50t.
In-pit cut-off grade. See Mill (internal)
cut-off grade
Incremental capital expenditures,
104–105
Internal cut-off grade. See Mill
(internal) cut-off grade
Inverse blending problem, 120–122
Iron, 109
Iso-Q lines, 119–120, 120f.
Iso-R lines, 120, 121f.
Iso-T lines, 119, 119f., 135–137, 137f.
Lane, F., 3
Leaching operation costs, 103, 104t.
Marginal cut-off grades, 73
cut-off grade below, 63–66
Metal equivalent, 34
and NSR (calculation and reporting),
36–38
Mill capacity
constraints on, and changes in
opportunity cost, 107
fixed, and fixed sales volume with no
mining constraint, 79–81, 80f.
fixed, with increased mine capacity,
81–83, 83t., 84t.
fixed, with increased mineral content,
81–82, 83t., 84–85, 84t.
increased, with fixed mine capacity,
81–82, 83, 83t., 84t.
and mine capacity, imbalances in, 69
unconstrained, and fixed sales volume,
78–79, 81, 82f.
Mill (internal) cut-off grade, 18–19, 45
open pit mines, 21–22, 22f., 23f.
underground mines, 25–26
Mine capacity
assessing whether increase is justified,
70–72, 71f.
changes in, and effect on cut-off
grade, 69–72
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Index 153
with constant grade-tonnage curve,
70–72, 71f.
without constant grade-tonnage
curve, 72
constraints on, and changes in
opportunity cost, 107
and cut-off grade (copper mine),
60–61
fixed, and cut-off grade, 76–78, 77f.
fixed, with increased mill capacity,
81–82, 83, 83t., 84t.
fixed, with increased mineral content,
81–82, 83t., 84, 84t.
grade-tonnage curves, current and
proposed, 73–75, 74f., 75f.
increased, with fixed mill capacity,
81–83, 83t., 84t.
and mill capacity, imbalances in, 69
open pit and underground methods
compared for same deposit,
98–100, 99f., 100t.
opportunity cost in optimization of,
72–76, 74f., 75f.
unconstrained, and fixed sales volume,
78–81, 80f.
Mine (external) cut-off grade
with waste stripping, 19–20
without waste stripping, 19
Mine planning
and block and panel caving, 91–98
open pit and underground methods
compared for same deposit,
98–100, 99f., 100t.
pushback mining valuation for open
pit mine, 87–89
and similarities between underground
and open pit mines, 90–91
stope mining valuation for
underground mine, 89–90
Mines. See Mine (external) cut-off grade;
Open pit mines; Stockpiles and
stockpiling; Underground mines
Minimum rate of return
and block and panel caving, 93, 95,
96, 97
constraints on, and changes in
opportunity cost, 107
Minimum return on investment,
102–103
Molybdenum. See under Polymetallic
deposits
Net present value (NPV), 2, 3, 10, 74
calculation example, 10, 11t.
and constant cash flow over n years,
11, 12t., 127
and constant cash flow to perpetuity,
11, 12t., 128
and cut-off grade optimization,
66–67
in economic valuation of pushback,
87–89
in economic valuation of stopes,
89–90
formula, 10, 127
and opportunity cost, 12–14, 56–57
Net smelter return (NSR), 34
cut-off example (coppermolybdenum), 35–36, 36f.
and cut-off grade (formula), 34
and metal equivalent, 36–38
Open pit mines
cut-off grades in, 20–22
mill cut-off grade, 21, 22f.
mill cut-off grade with strip ratio,
21–22, 23f.
mine cut-off grade, 21, 22f.
and pushback, NPV in consideration
of, 87–89
and underground method, compared
for same deposit, 98–100, 99f.,
100t.
and underground mines, similarities
in planning for, 90–91
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154 INDEX
Operating conditions, 124–125. See also
Processing plant operations
Operating costs, 102
and benefits, 12–15
constraints on, and changes in
opportunity cost, 107
Opportunity costs
and capacity constraints, 12–14,
128–129, 129f., 130t.
and capacity constraints with lowered
cut-off grade (gold leaching
example), 53–56, 54f., 55f.
and cut-off grade below marginal cutoff grade, 63–66
in cut-off grade estimation, 13–14, 107
in cut-off grade optimization, 66–67
and cut-off grades with mill capacity
constraint (copper mine), 59–60
and cut-off grades with mine capacity
constraint (copper mine), 60–61
and cut-off grades with refinery
capacity constraint (copper
mine), 61
and decreasing cut-off grade over time
(copper mine), 61–63, 62t., 63f.,
64t., 65f.
defined, 12, 56–57
in mine capacity optimization,
72–76, 74f., 75f.
and net present value, 12–14, 56–57
of not using optimum cut-off grade,
38–40, 39f., 131–132
and peripheral deposit, 12–13,
128–129, 129f., 130t.
in pushback mining, 87–88
simplified equation to estimate,
130–131, 131f.
underground gold mine example,
14–15
Overhead costs, 105
Panel caving
and capital cost, 93
constraints imposed by, 91–92
and cut-off grades, 91
economic valuation example (copper
mine), 95–98
marginal cut-off grade and block
design, 93
marginal cut-off grade and drawpoint
management, 92
and minimum rate of return, 93, 95,
96, 97
opportunity cost, 94–95
and yearly cash flow, 94
Polymetallic deposits
breakeven cut-off grades, 32–38
copper-gold, 32–34
copper-gold, and net smelter return
(NSR), 34
copper-molybdenum, and net smelter
return, 35–38
and cut-off values, 34
defined, 32
and metal equivalent, 34
metal equivalent calculation and
reporting, 36–38
NSR cut-off calculation, 34–36, 36f.
Process comparison cut-off grade
in choosing between two processes,
26–27
precious metal example, 27–28, 28f.
Processing plant operations. See
Blending strategy; Grinding circuit
optimization; Mill (internal)
cut-off grade; Process comparison
cut-off grade; Stockpiles and
stockpiling
Pushbacks, 91
economic valuation of, 87–89
Reserves, published, 2–3
Stakeholders’ interests
and costs, 105–107
and cut-off grade, 3
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
Index 155
Stockpiles and stockpiling, 1, 2, 3, 16
and cut-off estimation, 40–42,
132–135, 133t., 134t., 136f.
and high-cost waste dumps, 43
and low-cost stockpiles, 42–43
low-grade, and cut-off grades, 40–43,
103
vs. wasting, 40–41
See also Blending
Stopes, 91
economic valuation of, 89–90
minimum average grade, 23–24, 24f.
size optimization, 24–26
Sunk costs, 102
Sustaining capital, 103–104
Symbols, list of, 139–143
Underground mines
and capacity constraints, 23
cut-off grades in, 23–26
estimation of average and cut-off
grades in, 23, 24f.
mill cut-off grade, 25–26
mine cut-off grade, 24–25
minimum average stope grade, 23–24,
24f.
and open pit method, compared for
same deposit, 98–100, 99f., 100t.
and open pit mines, similarities in
planning for, 90–91
and opportunity costs, 23
stope size optimization, 24–26
stopes, economic valuation of, 89–90
Utility, defined, 5n.
Utility functions, 5–6, 6f.
and cut-off grade, 17–18, 19f.
fundamental equation, 6, 123–124
Udir, 6, 8–10, 123
Uopp, 6, 12–15, 123
Uoth, 6, 15–16, 123–124
Variable costs, 101
Variable recovery cut-off grade, 28–29
constant tail model, 30–32, 32f., 33f.
precious metal example, 29–30, 29f.,
30f.
Yearly cash flow (YCF), 73–74, 75
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Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
157
About the Author
Jean-Michel ( J.M.) Rendu is an independent mining consultant with forty
years of experience in the mining industry. He is recognized worldwide as
an expert in the estimation and public reporting of mineral resources and
mineral reserves, geostatistics, and mine planning. In his former position as
vice president of resources and mine planning with Newmont Mining Corporation for seventeen years, he was responsible for the management of all
Newmont mining engineering activities, including project reviews, staffing
and support of corporate and mine-site mining groups, estimation and public
reporting of mineral resources and mineral reserves, mine planning, and ore
control. J.M.’s consulting activities gave him the opportunity to work on all
continents except Antarctica.
J.M. has authored more than fifty technical papers on deposit modeling, mine planning, methods and guidelines for estimation of resources and
reserves, U.S. and international regulatory requirements for public reporting,
and geostatistical theory and practice. He is also the author of An Introduction to Geostatistical Methods of Mineral Evaluation, a South African Institute
of Mining and Metallurgy Monograph Series publication, first published in
1978 (second edition 1981).
During his professional career, J.M. was assistant professor at the University of Wisconsin–Madison, honorary professor at the University of
Queensland, adjunct associate professor at the Colorado School of Mines,
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158 ABOUT THE AUTHOR
invited lecturer at École Polytechnique and McGill University in Montreal,
and external lecturer at the University of Witwatersrand in South Africa.
J.M. has taught short courses on estimation and public reporting of mineral
resources and mineral reserves, cut-off grade calculation, and geostatistical
theory and practice.
In addition to being a Founding Registered Member of the Society for
Mining, Metallurgy, and Exploration, Inc. (SME), J.M. served as SME Board
member and chairman of SME’s Mining and Exploration (M&E) Division,
Ethics Committee, and Resources and Reserves Committee. He was a founding member and U.S. representative of the Committee for Mineral Reserves
International Reporting Standards (CRIRSCO). He is a Fellow of both the
Australasian Institute of Mining and Metallurgy and the South African Institute of Mining and Metallurgy.
J.M. was a recipient of the Henry Krumb Lecturer Award in 1992; the
Presidential Award in 1992 and 2004; the Daniel C. Jackling Award in 1994;
the M&E Division Distinguished Service Award and the AIME Mineral
Economics Award in 2008; the SME Distinguished Member Award and the
American Mining Hall of Fame Medal of Merit Award in 2009. J.M. is an
elected member of the U.S. National Academy of Engineering.
Copyright © 2013 Society for Mining, Metallurgy, and Exploration, Inc. All rights reserved.
GRADE
ESTIMATION
SECOND EDITION
AN INTRODUCTION TO
CUT-OFF
AN INTRODUCTION TO
CUT-OFF GRADEESTIMATION
BY JEAN-MICHEL RENDU
BLENDING CONSTRAINTS WASTE BLOCK CAVING STOCKPILES
CLOSURE GRADE-TONNAGE PRICES MINE CUT-OFF LEACHING
UNDERGROUND NPV SOCIOECONOMIC METAL EQUIVALENT
OPEN PIT OPPORTUNITY POLYMETALLIC PROCESS PROFIT
RECLAMATION SELECTIVITY STOPES UTILITY NSR VARIABLE
RECOVERY NPV MILL CUT-OFF LEACHING BREAKEVEN STOCK
STOCKPILES CLOSURE POLYMETALLIC UNDERGROUND NPV
SOCIO-ECONOMIC METAL EQUIVALENT OPEN PIT OPPORTUNITY
POLYMETALLIC PROCESS PROFIT BLENDING CONSTRAINTS
WASTE BLOCK CAVING STOCKPILES CLOSURE GRADE-TONNAGE
PRICES MINE CUT-OFF LEACHING UNDERGROUND NPV SOCIOAn Introduction to Cut-off Grade Estimation examines one of
the most important calculations in the mining industry. Cut-off
grades are essential to determining the economic feasibility and
mine life of a project. Profitability and socioeconomic impact of
mining operations are influenced by the choice of cut-off grades.
Cut-off grades play a key role in estimating mineral reserves
that can be publicly reported.
This new edition is easier to read and of greater practical interest to
practitioners. The relationship between optimization of net present
value, capacity constraints, and opportunity cost is explained in
greater detail. A new section discusses blending strategies, which
play a critical role in an increasing number of mining operations.
Author Jean-Michel Rendu, an internationally recognized expert
in the management, estimation, and public reporting of mineral
resources, provides practical insights. As a manager in major mining
companies, a consultant, and an educator, Rendu has acquired
considerable experience in all aspects of mining engineering,
experience that was incorporated into this publication.
The Society for Mining, Metallurgy & Exploration (SME),
advances the worldwide mining and minerals community
through information exchange and professional development.
SME is the world’s largest association of mining and
minerals professionals.
SECOND EDITION
BY JEAN-MICHEL RENDU
!SME_COGrade2013_2ndED_FullCV_F5.indd 1 12/26/13 8:21 AM AN INTRODUCTION TO CUT-OFF GRADE ESTIMATION SECOND EDITION RENDU