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    Interpretation of the recovery/time curve and scale-up from column

    leach tests on a mixed oxide/sulfide copper ore

    Ronald J. RomanLeach, Inc.

    4741 N. Placita del Sol

    Tucson, AZ 85749

    Jose Hector Figueroa P. and Jorge Enrique Ruiz H.

    Mexicana de Cananea S.A. de C.V.

    Av. Juarez S/N

    Cananea, Sonora 84620

    Mexico

    Jorge Helleon G.Mexicana de Cobre, S.A. de C.V.

    Aptdo 20

    Nacozari, Sonora 84340

    Mexico

    Efrn Prez S.

    University of Sonora

    Dept. of Geology

    Hermosillo, Sonora 83000

    Mexico

    ABSTRACT

    The shrinking core model for coarse particle leaching has been generally accepted as

    describing the leaching of a copper oxide or sulfide ore. However, when a mixed

    oxide/sulfide ore is leached this model can not be used in its simple form because at least two

    and possibly three separate leaching processes are occurring simultaneously (dissolution of

    oxide copper minerals, secondary copper minerals and primarily copper minerals). It has been

    impossible to isolate their individual leaching curves from the recovery/time curve generatedby the column leach test. This paper describes a tests program carried out at the Groupo

    Mexico, Mexicana de Cobres La Caridad operation in which the individual recovery/time

    curves for the leaching of copper oxide mineral, secondary copper mineral and primary

    copper minerals were developed from standard column leach tests. Once the individual

    recovery/time curves were developed scale-up of the column leach test results to the

    commercial heap leaching operation is possible by using the shrinking core model.

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    INTRODUCTION

    A fifteen-year mine plan is being prepared by the staff at La Caridad. This mine plan

    will recognize and incorporate the leaching response of the individual ore blocks so the

    mining sequence can be based on the overall economics of the operation including the

    recovery of copper from the leach ore as well as the recovery of copper from the milled ore.

    This paper briefly describes part of the column leach test program that was undertaken at La

    Caridad and by the metallurgical staff at La Caridad with the assistance of Leach, Inc. The

    objective of this column leach program was to develop a correlation between the leachability

    of the ores from the La Caridad pit and the geologic and/or chemical characteristics of the

    individual ore blocks. The leachability of an ore is defined by the recovery/time curve

    generated by leaching the ore under plant conditions.

    The mine plan is made up of thousands of blocks that are contained within the pit

    limits. In order to determine if an individual block is to be considered waste, flotationfeed or heap leach feed the amount of copper which might be recovered from that block

    needs to be estimated. Normally, to obtain that estimate for the option of heap leaching a

    column leach test is required. With the column data in hand, the recovery/time curve for the

    commercial heap leaching operation is projected based on the shrinking core model (1,2).

    However, conducting thousands of column leach tests, one for each ore block, would be

    prohibitive from both the cost and the time required. An additional problem is that shrinking

    core models are based on the rate of movement of the interface between the leached shell and

    the unleached core of the ore particle. When the ore contains copper in more than one form

    (oxide, secondary sulfides and/or primary sulfides) then there exists more than one interface.

    It is therefore necessary to experimentally measure the rate of copper recovery for each of

    the forms of copper. No experimental technique is available to divide the experimentalrecovery/time curve from a column leach test into the individual recovery/time curves for the

    different copper components of an ore. The division of the overall recovery/time curve into

    its individual components is necessary if the shrinking core model is to be used to project the

    column leach test results to the commercial heap leach operation.

    It was a primary objective of this project to develop a technique to divide the

    experimentally determined recovery/time curve into individual recovery/time curves for each

    form of copper present in the ore and secondly to find an easily measured characteristic of

    an ore sample which correlates with the recovery/time curve under the commercial heap leach

    conditions. Because the copper produced from leaching the ore is recovered over several

    years, not only must the final recovery be estimated but the complete recovery/time curveneeds to be predicted so that the cash flow from the annual copper production from that ore

    block can be properly discounted when assigning a value to the ore block.

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    PROCEDURE

    The column leach test program was divided into four parts:

    1. Determination of the reproducibility of the column leach test through duplicate tests,

    which were run at the La Caridad lab; and duplicate tests, one run at La Caridad and

    the other one run in the lab at Mountain States R & D International, Inc. (MSRDI)

    in Vail, Arizona.

    2. Determination of the change in the leachability of an ore resulting in changes in the

    operating parameters of the column leach test i.e. leach solution irrigation rate,

    column height, column diameter, leach solution chemistry, leach/rest cycle schedule,

    etc. This phase of the column test program was used to establish the procedure for

    the standard column leach test and to demonstrate that the leaching of the ore

    followed the shrinking core model of leaching.

    3. Determination of the leachability of ore samples from throughout the La Caridad

    deposit and analysis of the leachability in an attempt to correlate the leachability of an

    ore sample with geological and/or chemical parameters of the ore sample.

    4. Projection of the column leach test date to leachabilities for that ore sample when

    leached on the commercial heaps.

    This paper reports on the third part of this project: developing a correlation between

    the leaching recovery/time curve and the geologic and/or chemical characteristics of an ore

    sample.

    The La Caridad deposit has been divided into four zones based on both the geological

    and mineralogical characteristics of the rock. Ore samples for column leaching were collected

    from each of the four zones.

    In addition to this classification of the ore blocks, each ore block can be classified

    based on copper grade. Two classes based on copper grade were selected: Cu(total) equal

    to or greater than 0.15 percent and equal to or less than 0.30 percent, and Cu(total) greater

    than 0.30 percent.

    The most prevalent copper minerals in the La Caridad deposit are chalcocite, covelliteand chalcopyrite. In addition some oxide copper minerals as well as bornite are present.

    Because the responses of these minerals to leaching differ greatly, a third classification was

    established: the percentage of leachable copper. The leachable copper is defined as that

    copper contained in minerals solubilized by a five percent sulfuric acid solution or a ten

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    percent sodium cyanide solution (3). The fraction of the contained copper which is either acid

    soluble or cyanide soluble is called the Solubility Index or S.I. The other copper minerals,

    which by this definition are not leachable, are chalcopyrite and refractory mixed iron or

    manganese copper oxide minerals. Each ore block was then classified by its leachable

    copper content: less than 25 percent, equal to or greater than 25 percent but less than 50

    percent, equal to or greater than 50 percent but less than 75 percent and equal to or greater

    than 75 percent.

    In those column tests in which different ore samples were being evaluated for their

    leachability a standardized test procedure was used. The test procedure was designed to

    allow both the rate of copper solubilization and the ultimate copper recovery to be determined

    in as simple a test as possible. The standard test procedure was selected after running a

    preliminary group of 13 column leach tests in which the operating parameters were varied.

    Parameters varied included column height, column diameter, irrigation rate, cure procedure,

    rest cycle schedule and leach solution chemistry. In summary, the standardized test leaches

    a 90 kg ore sample crushed to -38 mm. for 90 days in a 152 mm diameter column 3.0 metersin height. A sample for a size/assay test is split from the ore sample and each size fraction is

    analyzed for acid soluble copper, cyanide soluble copper and total copper. The leach solution

    used in the column test is raffinate from the La Caridad heap leach circuit containing

    approximately 3.0 gpl total iron of which approximately 2.8 gpl is ferric iron. The free acid

    content of the leach solution is approximately 6 gpl. The column is irrigated at a rate of

    0.0034 lps/m and no rest or cure cycles are used.2

    Pregnant leach solution (PLS) samples are collected daily, their volumes determined

    and the solution assayed for ferrous iron, total iron, free acid and total copper. The ferric iron

    is calculated from the total iron and ferrous iron assay.

    REVIEW OF COLUMN DATA AND SIMULATION OF RESULTS

    The factors, which determine the recovery/time curve, can be divided into two groups:

    the operating parameters of the heap leach or column leach and the ore characteristics.

    Operating parameters include all those parameters that the plant operator can independently

    select or that are a result of one of the parameters under control of the operator. Particle

    size, lift height and irrigation rate fall into this group. In addition heap porosity (the

    percentage voids within the heap) is also in this group since it is determined by the particle

    size, heap height and the manner in which the heap was built. The second group (orecharacteristics) consists of parameters that the operator has no control over: ore specific

    gravity, porosity, mineralogy and copper mineralogy for example. The primary objective of

    this study was to determine a correlation between the ore characteristics (the second group

    of parameters) and the recovery/time curve. The relationship between the operating

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    parameters (the first group of parameters) and the recovery/time curve is based on the

    shrinking core model as described by LEACH (4), a software package for simulating a heap

    leach operation. All column tests were, therefore, run under conditions as close to identical

    as possible so that differences in their recovery/time curves would only result from differences

    in the ore characteristics of the individual ore samples use in each column.

    Analysis of the column leach test results revealed that the recovery/time curves of all

    of the ore samples could be described by three ratios: acid soluble copper to the total copper

    in the sample, cyanide soluble copper to the total copper in the sample and insoluble copper

    to the total copper in the sample.

    Table I summarizes the copper chemistry for all of the column tests run with the

    standard column test procedure. The recovery/time curves for a selected few of these tests

    are shown in Figure1 in which the recovery of total copper is plotted. In Figure 2 the same

    column tests are plotted showing the recovery of soluble copper. The copper recoveries in

    the tests were fitted by least squares regression analysis to an equation of the form:

    % Rec Cu(total) = A x S.I.(A.S.) + B x S.I.(CN sol.) +C x (Insol Cu) (1)t t t twhere:

    % Rec Cu(total) = Recovery of total copper at time t,tA , B and C = Constants, time variable,t t tS.I.(A.S.) = Ratio of acid soluble copper assay to total copper assay,

    S.I.(CN sol.) = Ratio of cyanide soluble copper assay to total copper assay,

    Insol Cu = Ratio of insoluble copper content to total copper assay.

    Equation 1 states that the copper recovery will be a function of the fraction acid

    soluble copper content, the fraction cyanide soluble copper content and the fraction insolublecopper content: the basic copper mineralogy of the ore. The equation also presumes that each

    of the three forms of copper present will leach independent of the amount of the other two

    forms of copper present and that all of the other characteristics of the ore will have no

    measurable effect on the recovery/time curve. Although this may be intuitively incorrect, if

    the variation in these other characteristics among the test samples is small then their effect on

    the recovery/time curve can be small or masked by the effect of the copper mineralogy. In

    addition any effect caused by these other characteristics will be indicated by the correlation

    coefficient of the regression equation.

    The results of the regression analysis are summarized in Table II. The constants, A,

    B and C can be interpreted as the recovery of the their respective copper component at thecorresponding times. Figure 3 shows the plots of the constants versus time.

    The adjusted correlation coefficient represents the amount of the change in

    recovery that is due to ore characteristics incorporated in equation 1. For example, at 20

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    Table I - Column leach test feed characteristics

    Column Zone % % % S.I. Acid S.I. Cyanide S.I. Cyanide S.I. TotalOre Cu(tot), Cu(A.S.), Cu(CN sol), S.I. Acid/

    1 1 0.203 0.010 0.016 0.045 0.071 0.625 0.116

    2 1 0.211 0.015 0.016 0.064 0.068 0.938 0.131

    3 1 0.208 0.033 0.044 0.163 0.218 0.750 0.391

    4 1 0.240 0.033 0.097 0.138 0.406 0.340 0.544

    6 1 0.304 0.040 0.138 0.148 0.511 0.290 0.659

    7 1 0.268 0.028 0.037 0.111 0.147 0.757 0.258

    9 1 0.427 0.033 0.160 0.074 0.360 0.206 0.435

    11 1 0.419 0.062 0.282 0.145 0.660 0.220 0.806

    12 2 0.250 0.012 0.024 0.049 0.098 0.500 0.148

    12 2 0.212 0.015 0.031 0.063 0.130 0.484 0.193

    14 2 0.267 0.029 0.097 0.115 0.385 0.299 0.500

    15 2 0.337 0.035 0.054 0.114 0.175 0.648 0.289

    16 2 0.208 0.038 0.134 0.182 0.641 0.284 0.823

    17 2 0.291 0.076 0.159 0.251 0.525 0.478 0.776

    18 2 0.273 0.019 0.080 0.070 0.296 0.238 0.367

    19 2 0.353 0.020 0.015 0.053 0.040 1.333 0.093

    20 2 0.377 0.062 0.159 0.164 0.420 0.390 0.583

    21 2 0.384 0.083 0.204 0.230 0.565 0.407 0.795

    22 2 0.471 0.082 0.280 0.185 0.631 0.293 0.815

    23 3 0.198 0.016 0.012 0.083 0.062 1.333 0.145

    24 3 0.199 0.013 0.007 0.069 0.037 1.857 0.106

    25 3 0.199 0.025 0.021 0.126 0.106 1.190 0.231

    26 3 0.392 0.026 0.037 0.065 0.093 0.703 0.159

    27 3 0.693 0.222 0.327 0.301 0.444 0.679 0.745

    29 4 0.232 0.012 0.023 0.047 0.089 0.522 0.136

    30 4 0.218 0.018 0.015 0.085 0.071 1.200 0.156

    31 4 0.356 0.020 0.023 0.057 0.066 0.870 0.123

    32 4 0.286 0.026 0.027 0.086 0.090 0.963 0.176

    33 4 0.414 0.037 0.071 0.094 0.181 0.521 0.27534 4 0.587 0.076 0.296 0.144 0.546 0.264 0.690

    35 4 0.484 0.081 0.278 0.175 0.600 0.291 0.775

    36 4 0.475 0.106 0.210 0.234 0.464 0.505 0.698

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    0 20 40 60 80 100

    Leach time, days

    RecoveryCu(tot),

    %

    0

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    60

    70

    80

    90

    0 20 40 60 80 100Leach time, days

    RecoveryCu(Soluble),%

    6

    Figure 1 - Recovery of Total Copper for Selected Column Leach Tests

    Figure 2 - Recovery of Soluble Copper for Selected Column Leach Tests

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    0 20 40 60 80 100

    Time, days

    RegressionCoefficient

    (CuReco

    very,

    %)

    Cu(A.S.) Cu(CN sol)

    7

    Table II - Results of Regression Analysis

    Time, days A B C Correlation

    Adjusted

    Coefficient5 63.85 5.75 -2.37 0.818

    10 69.73 15.94 -2.65 0.859

    15 79.05 21.92 -2.90 0.869

    20 81.72 26.72 -2.62 0.871

    40 86.04 37.49 -1.41 0.885

    60 87.02 43.66 -0.36 0.886

    80 88.45 46.54 0.59 0.885

    Figure 3 - Regression Coefficients as a Function of Leach Time

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    days into leaching, equation 1 accounts for 87.1 percent of the change in recovery, the other

    12.9 percent must be attributed to factors not included in the equation. These would include

    experimental error, variations in operating parameters which were intended to be held

    constant in all tests (such as leach solution chemistry, irrigation rate, percent voids in the

    column, column height, particle size distribution, etc.) and differences in the leachability of

    the ore samples as a result of differences in the ore characteristics which effect the

    recovery/time curve, such as the ore porosity and reagent consumption.

    Table III contains measured recoveries and the calculated recoveries at selected times

    for column tests on 32 ore samples. The measured recoveries versus the calculated recoveries

    are plotted in Figure 4.

    The numerical values for the C term are interesting from both an academic point as

    well as a practical point. The negative value suggests that the chalcopyrite is initially acting

    as a preg robber. With increasing leach time this effect is reduced and the chalcopyrite then

    contributes to the copper produced by the column. This can be explained by the followingchemical reaction:

    CuFeS + Cu 2CuS + Fe (2)2+2 +2

    Initially the chalcopyrite reacts with copper in the leach solution, precipitating the

    copper as covellite and releasing iron into solution. As leaching progresses the covellite

    undergoes dissolution:

    CuS + 8Fe + 4H O Cu + SO +8Fe + 8H (3)+3 +2 = +2 +

    2 4

    and this second reaction releases more copper into solution than the first removes from

    solution. This reaction sequence is the typical A B C reaction where chalcopyrite is A,

    covellite is B and C represents solubilized copper. Consequently, the constant C is initially

    negative but eventually becomes positive.

    This explanation of the role of chalcopyrite was supported by the observation that in

    some of the leach residues more covellite was found than could be accounted for by the

    covellite in the sample head plus the covellite produced from leaching half of the copper from

    the chalcocite. In addition, this reaction sequence is known to produce covellite during the

    alteration of primary copper deposits. There have been several reports of an induction

    period in leaching chalcopyrite ores similar to that suggested by the above sequence ofreactions. They have been attributed to an acclimatization period needed by the bacteria

    before taking part in the leaching process.

    The chalcopyrite eventually contributes to the production of copper from the heap.

    The column tests were not of sufficient duration to establish a recovery/time curve for the

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    Table III - Column leach test measured and calculated recovery

    Column

    Recovery, % (measured/calculated)

    5 days 10 days 20 days 40 days 60 days 80 days

    1 1.91/1.17 3.01/1.91 4.44/3.24 6.67/5.27 8.61/6.69 9.19/7.79

    2 1.50/2.39 2.21/3.21 4.05/4.73 6.76/6.79 8.68/8.18 9.24/9.26

    3 8.30/10.22 11.37/13.22 17.73/17.55 19.78/21.35 22.45/23.50 23.03/24.95

    4 9.55/10.07 14.93/14.89 20.58/20.93 25.24/26.45 28.60/29.57 29.89/31.37

    6 12.64/11.59 19.25/11.57 28.68/24.87 35.45/31.43 39.42/35.08 41.29/37.09

    7 6.17/6.18 7.45/8.12 9.80/11.06 12.87/14.02 14.15/15.81 15.39/17.10

    9 8.63/5.48 11.82/9.43 15.75/14.22 20.82/19.11 23.26/22.00 24.71/23.68

    11 17.73/12.61 28.23/20.14 41.76/29.00 50.25/36.98 55.80/41.40 58.42/43.69

    12 4.31/1.69 5.93/2.74 7.63/4.41 10.68/6.72 11.73/8.27 12.80/9.4312 6.89/2.86 8.58/4.33 10.40/6.52 13.83/9.17 15.15/10.88 17.04/12.11

    14 8.53/8.38 11.97/12.84 16.32/18.38 22.33/23 25.25/26.64 26.43/28.39

    15 5.93/6.58 7.48/8.83 10.50/12.11 13.23/15.35 14.33/17.29 15.14/18.63

    16 15.86/14.88 23.43/22.43 30.76/31.53 39.65/39.43 44.60/43.75 48.28/46.02

    17 22.00/18.50 29.15/25.26 37.26/33.93 45.44/40.94 48.46/44.66 50.50/46.74

    18 4.36/4.70 6.72/7.95 10.87/12.01 14.58/16.27 17.35/18.83 19.00/20.39

    19 0.74/1.46 1.38/1.92 2.90/3.01 4.66/4.76 5.83/6.01 6.69/7.06

    20 11.00/11.67 17.23/16.99 25.77/23.49 31.89/29.22 35.94/32.40 37.73/34.24

    21 11.28/17.44 18.31/24.50 27.85/33.35 35.04/40.68 39.97/44.61 42.09/46.75

    22 11.62/14.98 16.14/22.44 24.33/31.46 31.20/39.27 34.20/43.54 35.90/45.79

    23 4.00/3.62 4.89/4.51 7.52/6.20 9.42/8.26 10.60/9.62 11.83/10.73

    24 3.84/2.51 4.24/3.05 5.71/4.30 6.86/6.09 7.64/7.32 8.55/8.38

    25 6.66/6.81 8.00/8.40 11.45/11.07 13.96/13.68 15.59/15.26 17.26/16.48

    26 3.35/2.72 4.19/3.82 6.75/5.64 9.01/7.94 10.41/9.47 11.98/10.63

    27 26.58/21.18 31.76/27.40 40.17/35.80 46.80/42.19 50.02/45.49 51.58/47.44

    29 0.95/1.43 1.63/2.37 3.01/3.92 5.35/6.13 7.09/7.63 8.41/8.77

    30 3.37/3.86 4.44/4.85 5.70/6.66 8.11/8.82 9.31/10.22 10.69/11.35

    31 0.74/1.96 1.83/2.72 3.53/4.15 5.54/6.17 7.06/7.55 8.09/8.65

    32 2.47/4.08 3.18/5.27 4.10/7.30 6.75/9.63 7.85/11.14 8.80/12.30

    33 5.60/5.33 8.07/7.52 11.30/10.62 14.46/13.85 16.26/15.82 17.50/17.16

    34 8.59/11.59 13.99/17.92 20.21/25.54 26.29/32.42 29.34/36.26 31.00/38.33

    35 12.46/14.09 18.87/21.17 25.10/29.75 31.76/37.25 35.15/41.36 36.92/43.55

    36 15.46/16.89 23.84/22.90 33.21/30.72 40.59/37.09 44.52/40.49 48.81/42.45

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    Measured Cu(tot) Recovery, %

    CalculatedCu(tot)Rec

    overy,

    10

    Figure 4 - Comparison of measured and calculated Copper Recovery

    insoluble (chalcopyrite) copper fraction, however, the results of the standard copper

    mineralogical assay procedure indicated that the insoluble copper did leach under the typical

    column leach test conditions and data from the commercial heap indicates that some

    chalcopyrite is leached.

    Once the recovery/time curve under the base case test conditions is determined for any

    ore block, the recovery/time curve for the ore leached on the commercial heaps can beestimated based on the shrinking core model and a mass balance for the leach solution using

    the computer program LEACH. This is accomplished by dividing the copper in the ore into

    its acid soluble and cyanide soluble components, calculating the commercial heaps

    recovery/time curve for each of the two components independently then adding the recoveries

    for the two components together to obtain the recalculated recovery for the total ore. The

    contribution of the chalcopyrite to the total recovery was estimated to be one percent per year

    (i.e. 1 percent of the copper in the chalcopyrite would solubilized each year the ore was under

    leach).

    PROJECTION OF COMMERCIAL HEAP LEACHING RESULTS

    The high numerical values of the adjusted correlation coefficients for the regression

    equations imply that the recovery/time curves are almost completely and solely defined by the

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    copper mineralogy of the sample. Neither the ore zone from which the samples originated,

    the degree of alteration of the ore nor the grade of the ore appears to have any measurable

    influence on the recovery/time curve.

    Operating parameters (as opposed to ore characteristics) for the column tests were

    held constant. Particle size distributions, irrigation rates, column heights etc. were

    intentionally kept very nearly constant in all tests. The affect of changes in these parameters

    on the recovery/time curve can be calculated by the shrinking core model employed by the

    computer program LEACH.

    The constants generated by the regression analysis of the column test data physically

    represent the recoveries of the copper in each of the three copper mineral groups: the acid

    soluble fraction (copper oxides), the cyanide soluble fraction (secondary copper sulfides) and

    insoluble fraction (chalcopyrite). The overall copper recovery from a column leach test is

    found by taking a weighted average of these three curves. Given the recovery/time curves

    in Figure 3, the leachabilities based on the shrinking core model of the acid soluble andcyanide soluble fractions of the copper in the ore were calculated using the computer program

    LEACH. Once the leachabilities had been determined, the overall recovery/time curves

    were calculated for commercial heaps using the operating parameters of the commercial heaps

    and the computer program LEACH.

    Simulation of the commercial heap operation give the following results:

    The estimated recovery of the total contained copper in year 1 of leaching is:

    % Recovery Cu(total) = 91.1 x S.I.(A.S.) + 49.9 x S.I.(CN sol.) (3)

    The estimated recovery of the total contained copper in year 2 of leaching is:

    % Recovery Cu(total) = 8.9 x S.I.(A.S.) + 8.3 x S.I.(CN sol.) (4)

    The estimated recovery of the total contained copper in year 3 of leaching is:

    % Recovery Cu(total) = 5.0 x S.I.(CN sol.) (5)

    The estimated recovery of the total contained copper in year 4 of leaching is:

    % Recovery Cu(total) = 3.3 x S.I.(CN sol.) (6)

    The following points should be noted:

    ! All of the acid soluble copper is recovered in two years.

    ! The recoveries given are incremental recoveries: that is they are the

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    recovery for the year, not cumulative recoveries.

    ! The column test does not provide an estimate of the copper recovery from the

    insoluble copper (chalcopyrite). This has been assumed to be 1 percent of

    the copper in the chalcopyrite per year and was added to the above equations.

    ! The cumulative recovery for any number of years is found by summing the

    coefficients of the equations for all the years over which the cumulative

    recovery is desired.

    Core samples of the La Caridad deposit have been collected and assayed for acid

    soluble copper, cyanide soluble copper and total copper. A block model has been developed

    from the these core samples. Equations 3 to 6, together with an appropriate present value

    discount factor have been used to assign a value to each block for the copper that can be

    recovered by heap leaching. Because of the correlation that has been developed between the

    copper mineralogy and the copper recovery from heap leaching it is not necessary to run a

    column leach test on every core sample.

    CONCLUSIONS

    This study resulted in three observations. First, the variation in response to leaching

    of different La Caridad ore samples is primarily the result of variations in copper mineralogy

    of the different ore samples. While the ultimate copper recovery of each ore sample is a

    function of the percentage of the copper contained in the oxide and secondary sulfide

    minerals, the rate of leaching is primarily a function of the ratio of oxide to secondary sulfide

    minerals present. Other ore characteristics either have a minimal effect on the recovery/time

    curve or their effects have been masked by the copper mineralogy.

    Second, given a sufficient number of column leach tests the recovery/time curve can

    be separated into individual recovery/time curves for the three forms of copper present in the

    ore: oxide copper, secondary sulfide copper and primary sulfide copper. The recovery/time

    curve for the individual copper components of the ore can be scaled up to the commercial

    heap leaching operating parameters based on the shrinking core model. The projected overall

    recovery/time curve for the commercial heap leaching operation is found to be the weighted

    average of the recovery/time curves for these components. Once a sufficient number of

    column leach tests have been conducted it is possible to construct a recovery/time curve for

    any ore sample from the mineralogical assay of the sample: a column leach test is not needed.

    Third, chalcopyrite appears to act initially as a preg robber precipitating copper from

    the leach solution. This reaction converts the chalcopyrite to covellite, which eventually

    dissolves, contributing to the copper production from the ore.

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    ACKNOWLEDGMENTS

    The authors would like to acknowledge and thank the management of Mexicana de

    Cobra and Mexicana de Cananea for there support during this project and their permission

    to publish this paper. In addition we would like to thank the many other individuals at both

    La Caridad and Cananea who participated in the experimental program and in discussions on

    the column leach program and the plant operations.

    REFERENCES

    5. B.R. Benner and R.J. Roman, Determination of the Effective Diffusivity of H+ Ions

    in a Copper Ore, AIME Transactions, VOL 256, 1974, 103 - 105. (Also seehttp://members.aol.com/leachinc/PUBLICATIONS.html )

    6. R.J. Roman, B.R. Benner, and G.W. Benner, Diffusion Model for heap Leaching and

    Its Application to Scale-Up, AIME Transactions, Vol 256, 1974, 247 - 252 (Also

    see http://members.aol.com/leachinc/PUBLICATIONS.html )

    7. G.A. Parkison and R.B. Bhappu, The Sequential Copper Analysis Method

    geological, Mineralogical, and metallurgical Implications, paper presented at the

    SME Annual Meeting, Denver, CO, USA, 6-9 March 1995, Preprint No. 95-90

    (Also see http://members.aol.com/leachinc/CUMINERALS.html )

    8. R.J. Roman, A Software Package for Heap Leaching, Presented at the Second

    Canadian Conference on Computer Applications in the Mineral Industry, Vancouver,

    B.C., 1991. (Also see http://members.aol.com/leachinc/Software.html )