TT 184 Final

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    Tailings Storage and Heap Leaching in aCombined Facility A First for the MiningIndustry

    Thomas F. Kerr, P.E. Knight Pisold and Co., United States

    Michael G. Skurski, P.E. Newmont Mining Company, United States

    Peter D. Duryea, Ph.D., P.E. Knight Pisold and Co., United States

    ABSTRACT

    The La Quinua mill at the Yanacocha mine in Peru has a thickened tailings storage

    facility that is contained entirely within an active heap leach pad. In this respect, it isunique and unprecedented in the mining industry and provides the operator, Minera

    Yanacocha S.R.L. (MYRSL), with certain cost, land-use and closure efficiencies. The

    combined design requires that the leach ore embankments retaining the tailings

    provide the same high level of stability and security required of major tailings dams.

    Contrary to standard tailings dam construction, the leach ore in these embankments is

    placed in thick, uncompacted lifts so that they maintain adequate permeability for

    leaching. The resultant loose structure makes static and dynamic liquefaction a critical

    issue, and the key design principle for avoiding a liquefaction related failure is to keep

    the ore that is saturated or very near saturated when under leach well removed from

    the outer faces of the embankments and contained behind large unsaturated structural

    shells. Thus, the design and operational effort has become largely one of keeping

    these shells adequately drained and below fully saturated. The facility was

    successfully commissioned in early 2008 and its performance to date has met or

    exceeded all design objectives. The first phase of expansion, Phase 2, has been

    designed and will be developed by late 2009.

    Introduction

    The La Quinua tailings are produced at the back end of the counter current decantation

    (CCD) circuit associated with the mill. The tailings are thickened to a solids content of

    approximately 67 percent by weight in the last CCD stage before being disposed within

    the active La Quinua heap leach pad (HLP). The thickened tailings storage facility

    (TTSF) was commissioned in April 2008, and approximately 5.6 million dry metric

    tonnes (mdmt) of tailings have been placed in the facility during its first year of

    operation. The facility was originally designed to accommodate 45 mdmt of tailings

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    produced at a nominal rate of 5.0 mdmt per year over a nine year period but has

    flexibility to be expanded to over 50 mdmt. Studies are ongoing to confirm the

    necessity of this additional storage capacity.

    The TTSF is unique in that it is located within an active HLP and uses leach ore,

    strategically placed within specific lines and grades, to form the tailings embankments.

    The HLP has been in operation since 2001 and has been expanded in seven stages,

    generally in a north to south direction over the natural topography that rises upward to

    the south. Through the first quarter of 2009, approximately 390 mdmt of leach ore has

    been loaded onto the HLP, and at its final installed capacity it will contain over

    530 mdmt. The north to south development presented the opportunity for changing the

    loading plan in the latter stages to contain the tailings in the south side of the HLP after

    MYSRL made the decision to develop the La Quinua mill. Stages 5 and 6 of the HLP

    were re-configured by placing the ore into east and west zones thereby leaving a

    central area open that became the TTSF. The east and west zones now form the main

    tailings containment embankments. Containment on the north side is provided by the

    main body of the HLP developed in Stages 1 through 5, and containment on the south

    side is provided by the natural topography. A general plan of the TTSF and HLP is

    shown on Figure 1.

    Figure 1 - Plan of the La Quinua Operation and Thickened TailingsStorage Facility

    The TTSF will be developed in three phases. Phase 1, which is currently in operation,

    has leach ore embankments up to elevation 3612 meters (m), or to a maximum height

    of approximately 50 m, which provides storage for 10 mdmt of tailings. This amount of

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    storage will be used up in January 2010. Phase 2, which is now under development,

    will have embankments up to 3644 m and will increase the storage capacity to nearly

    29 mdmt. This capacity will be reached in January 2013. Phase 3 will be developed in

    2012 up to the final elevation of the TTSF, which is still to be determined depending on

    the required final tailings and leach ore capacities. The original design of the TTSF

    had a final elevation at 3660 m, but most likely the actual elevation will be between

    3665 and 3675 m, which will make the final maximum height of the embankments

    between 100 and 115 m.

    Overview of Design and Operations to Date

    The tailings are thickened in a high rate thickener acting as the final stage of the CCD

    circuit and then transported to the TTSF through one of two 1.5 kilometer (km) long, 12-

    inch-diameter, unlined, steel pipelines that are fed by one of two centrifugal pump

    trains. The tailings are deposited into the TTSF from multiple drop bars comprising 8-

    inch diameter high density polyethylene (HDPE) pipes located on approximately 50 m

    centers that extend down into the basin from 14-inch diameter HDPE distribution pipes

    running around the inside crest of the leach ore embankments. One distribution pipe is

    above the east side of the impoundment and a second one is above the north and west

    sides. The drop bars convey the slurry down onto the tailings beach to prevent it from

    eroding the faces of the embankments. This is important as the upper portions of

    these slopes are actively under leach. The drop bars are valve activated from off-takes

    on the distribution pipes to allow for controlled placement into the facility. The slurry

    discharges out of holes that are drilled by the operators along the top of each drop bar

    just ahead of the rising beach, and this leads to some dissipation of energy as the

    tailings slurry exits the drop bar onto the tailings beach. The tailings then flow at a

    relatively low velocity over the beach, which allows for liquid/solid separation. The

    points of active discharge are frequently rotated around the three sides of the TTSF to

    form a thin layered, drained and stable tailings deposit against the leach ore

    embankments.

    The beach is sloped into the south-central area of the facility so that surface water

    draining from the tailings and runoff from precipitation is displaced away from the

    embankments. A small surface water pond is maintained in the south-central area

    directly against a blanket underdrain that covers the lined base of the facility, which

    slopes down to a low point in the northwest corner. The underdrain comprises a layer

    of free draining gravel within which a network of perforated corrugated polyethylenetubing (CPT) pipes is installed, and this layer is covered with a geotextile to filter out the

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    tailings solids. The geotextile is covered with another layer of gravel and cobbles for

    erosion and ultraviolet protection of the geotextile.

    While the surface water pond is being progressively displaced upwards by the rising

    tailings, it is kept in continuous contact with the sloping underdrain, which removes the

    water from the facility. A series of decant towers has also been installed in the TTSF

    as a backup in the unlikely event that the hydraulic capacity of the underdrain is

    exceeded by an extreme event or if a portion of the underdrain becomes blinded off.

    To date, the decant towers have not been needed. The water removed by the

    underdrain and decant towers is conveyed into a pair of concrete encased outlet pipes

    that run under the northwest corner of the HLP to a downstream reclaim pond. From

    there, the water is recycled to the mill.

    Filling of the tailings basin is at an early stage. Initial deposition commenced from drop

    bars in the northwest corner, i.e., the lowest part of the basin, and as the deposit

    advanced upward and outward the adjacent drop bars on either side were

    progressively brought into use. The objective was to place new tailings over the

    existing deposit established from the last set of drop bars in order to avoid tailings

    slurry running over the underdrain. The initially placed tailings in the northwest corner

    were unable to achieve any appreciable liquid/solid separation or form a beach due to

    the small area available. To prevent large amounts of water from decanting into the

    leach ore embankments and potentially causing erosion of the ore and dilution of

    pregnant solution in the HLP, a geomembrane was installed on the face of the

    embankments in this corner. The geomembrane was extended up to elevation 3580

    m, and when the tailings deposit reached the top of the geomembrane, a sloping beach

    had been developed against the embankments that displaced the surface water pond

    away from them.

    Photo 2 - View to the west along thenorth side of the TTSF showing thetailings beach developed against theleach ore embankments

    Photo 1 - View to the west along thesouth side of the TTSF basin showingthe small surface water pond in thesouth-central area in contact with theunderdrain blanket layer on the linedbase of the facility

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    Photo 3 - View looking east showing

    that good liquid/solid separation isoccurring over the tailings beach andclear water is present in the surfacewater pond against the slopingunderdrain blanket

    Photo 4 - Close up view of clear water

    discharging from the outlet pipe from theTTSF underdrain

    The program of continuously rotating the active points of tailings deposition around the

    beach perimeter has been in use for approximately 6 months, and at the end of the first

    quarter of 2009, the top of the beach had reached elevation 3594 m. The average

    density of the deposit was approximately 1.53 tonnes per cubic meter (T/m 3), which is

    slightly in excess of the design value of 1.50 T/m 3. Modeling indicates the overall dry

    density of the deposit will progressively increase to 1.65 T/m 3 over the next few years

    as the rate of rise decreases. Figure 2 presents the filling curve for the TTSF, in terms

    of elevation versus dry tonnage of tailings deposited, based on the design densities. A

    few actual filling points are shown in the lower left hand corner, and as can be seen

    they are in good agreement with the design curve. The currently planned phases of

    expansion are depicted by the stepped line.

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    Figure 2 - TTSF Filling Curve and Staged Development Phases

    Vibrating wire piezometers were installed in the lower portion of the tailings deposit at a

    height of 2.5 m above the underdrain (on stands placed above the underdrain) and in

    the underdrain during Phase 1 construction. Figure 3 shows a timeline plot of the

    measured pore pressures in the tailings and in the underdrain.

    Figure 3 - TTSF Basin Piezometer Readings

    The piezometers in the underdrain (06, 08, 10 and 14) are registering pore pressures

    at near zero values, which indicates that the drain is operating at atmospheric pressure

    as designed. The piezometers in the lower tailings (07, 09, 11 and 15) are showing

    slightly higher pore pressures in the 1 to 3 m (of water) range but these values are wellbelow hydrostatic pressures thereby indicating that the tailings, while saturated, are

    well drained and consolidated and passing seepage flow downward to the underdrain.

    These results indicate that the seepage gradient into the underdrain is approximately

    1.5, and based on a coefficient of permeability of the lower tailings of 2.910 -5

    centimeters per second (cm/sec) from laboratory tests conducted during the design, the

    calculated rate of vertical drainage from the tailings into the underdrain is about 0.09

    cubic meters per second (m 3/sec) over the approximately 205,000 square meters (m 2)

    inundated by tailings at the time these measurements were taken. This represents a

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    fraction of the total flow discharging from the underdrain, the remainder being decanted

    water from the small surface water pond.

    Leach Ore Characteristics and Dynamic Stability of

    Embankments

    Leach Ore EmbankmentsCombining heap leach and tailings storage into a single facility changed the operating

    dynamics of what had previously been only a heap leach operation. Two key design

    challenges for the TTSF were that:

    The leach ore embankments would continue to be loaded and leached but this

    would now happen concurrently with tailings deposition, which provides certain

    interfacing, logistical and solution management issues, and

    The leach ore would be placed into the embankments in thick, uncompacted

    lifts (to enhance leaching), which is contrary to the fill placement in typical

    tailings dams, but despite this the embankments would still need to meet

    rigorous safety standards set by Newmont, Knight Piesold and the international

    mining community, particularly under earthquake loading.

    These challenges were met by: (1) configuring the embankments to have wide cross

    sections (to support ore loading and leaching) thus creating large structural shells that

    would remain unsaturated, (2) placing coarser and finer ores in selected locations to

    create zones in the embankments adapted from the heap design, (3) thickening the

    tailings to reduce the amount of water entering the TTSF, and (4) using a rotational

    tailings deposition method to build well drained and stable beaches against the

    embankments.

    Zones in the embankments that comprise coarser and finer ores are described below.

    Zones A and C with up to 15 percent fines that includes higher quality run-of-

    mine (ROM) ore is well drained and unsaturated even when under leach. Zone

    A is a coarse grained, 50-meter wide zone placed on the exposed ultimate

    downstream face of the embankment with minimum 50 percent gravel content;

    Zone C is placed a minimum of two 16-meter lifts thick at the base of the

    embankment over the leach pad.

    Zone B with up to 20 percent fines forms the majority of the ore in theembankments in their middle elevations.

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    Zone D with up to 25 percent fines may be produced by mixing (on a truck by

    truck basis) higher fines content ore with lower fines content ore. This zone

    generally comprises the last two lifts placed on the heap and, while not part of

    the original design for the embankments, is being considered in current studies.

    Seepage and Stability AnalysesThe key design principle for stability is to keep saturated or near saturated areas of

    leach ore in the embankments well removed from the outer faces and contained behind

    the large structural shells. By keeping the leach ore in the shells well drained and less

    than fully saturated at all times, including when the embankments are under leach,

    liquefaction by static or dynamic loading will be prevented. Thus, the design effort

    became one of keeping these shells unsaturated. Finite element seepage modeling

    using the computer program SEEP/W (GEO-SLOPE, 2004a) was conducted to define

    the zones of potential saturation in the embankments.

    Available data with respect to the saturated hydraulic conductivity of the La Quinua ore

    were largely derived from testing a large number of samples in a previous study with

    samples selected to represent a substantial range of fines contents. During later

    analyses, conductivity versus depth relationships were developed from those

    laboratory data for the subset of samples that were considered to be representative of

    the ore types currently of interest (e.g., Zones A/C, Zone B, and Zone D). These

    relationships were further refined by calibrating the hydraulic/seepage model results

    against the observed field performance of the Stage 1 heap. In the seepage modeling

    presented later in this report, the TTSF embankments were subdivided into depth

    regions on 16-meter increments in accordance with the predominant lift thickness.

    Appropriate saturated hydraulic conductivities were then assigned to each depth range.

    Once a saturated conductivity was assigned to each portion of the relevant cross

    sections, it was also necessary to define the relationship between hydraulic

    conductivity (saturated and unsaturated) and soil suction for input into the variably

    saturated seepage model. The van Genuchten-Mualem formulation was adopted for

    analyses of the La Quinua facility, which requires definition of five curve fit parameters

    including: s (theta-s), r (theta-r), (alpha), n and m, where m=1-1/n. The previous

    laboratory testing program that generated the data on saturated hydraulic conductivity

    of the leach ore also included capillary moisture retention testing on most of the

    samples. Analyses of these data, once they had been corrected for the removal of

    oversize material, yielded the unsaturated flow parameters at two different test

    densities for the samples with a range of fines contents. Further evaluation of the data

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    resulted in the recommendations for modeling the Zones A/C, B and D materials. The

    resultant combination of saturated hydraulic conductivity and van Genuchten

    parameters define the required conductivity versus suction relationship for each

    material type and depth increment.

    A typical result of the seepage modeling is illustrated on Figure 4. The saturated zone

    is shown to be within the center of the embankment contained behind the wedge

    shaped structural shells. It is largely contained within the Zone B material while the

    Zone C material at the base of the embankment and the Zones A and B materials

    forming the outer shells are freely drained and unsaturated. This is consistent with the

    design objective. Figure 4 also shows flow vectors and contours of total head that

    define the flow regime through the maximum cross section of the west embankment

    (crest elevation 3660 m representing the original design) for the case where the full

    crest width of the embankment is under leach at the average maximum design solution

    application rate of 10 liters per hour per square meter (L/m 2/hr). The flow regime is

    shown to be is gravity dominated with flow lines largely vertically downward and little

    lateral spreading.

    Figure 4 - Seepage Analysis Resul ts - Crest Elevation 3660

    Limit equilibrium static and post-earthquake stability analyses of the embankments

    using SLOPE/W (GEO-SLOPE, 2004b) were then completed by importing the pore

    pressure data from the seepage files. The pore pressure data included the limits of the

    saturated and unsaturated ore together with the pore pressure values at each finiteelement node. Following this, dynamic stability analyses under the influence of the

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    maximum credible earthquake for the site, as established by a seismic risk

    assessment, were completed using the geomechanical finite difference-modeling

    program FLAC (Itasca, 2001). The initial step was to input density, modulus, strength

    and pore pressure values to determine the in-situ states of stress in the section under

    static loading conditions (self weight loads due to gravity alone). Material properties

    and a soil-liner interface strength relationship at the base were input from the results of

    extensive test work over several years on the HLP.

    In the second stage of the dynamic analysis, the earthquake was applied by entering

    an appropriate acceleration time-history and incorporating a liquefaction triggering

    subroutine developed for use with FLAC at the University of British Columbia (Beatty

    and Byrne, 1999). In that subroutine, a real-time analysis is performed where

    triggering of liquefaction is evaluated in each finite difference zone by counting the

    number of cycles of shear stress experienced by that zone until a threshold number is

    reached. Strength and stiffness values are then re-assigned to the appropriate post-

    liquefied value at the moment of liquefaction. A conservative undrained shear strength

    (S u/p) ratio of 0.10 was selected to represent the strength of the liquefied leach ore.

    Experience dictates that this is a conservative (low) value for a material that contains

    significant gravel and sand percentages. Additionally, it was conservatively assumed

    that the unsaturated leach ore would be subject to cyclic softening under the design

    earthquake event, meaning that cyclic loading could generate positive pore pressures

    less than those necessary to fully liquefy the material but which still could result in a

    decrease in its shear strength. This was accounted for by reducing the friction angle of

    the softened material to two-thirds of its original value.

    Results of Dynamic AnalysesResults of the model showed the development of several shear bands that closely

    parallel the potential critical slip surfaces defined by limit equilibrium slope stability

    analyses (not reported in this paper). This close comparison between the two different

    models added confidence to the analyses. The shear bands are shown on Figure 5.

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    Figure 5 - Static Stress State of Dynamic Model Zones - Crest Elevation 3660

    Additional results from the FLAC analyses, consisting of contours of total deformation,are shown on Figure 6.

    Figure 6 - Post -Earthquake Deformations - Crest Elevation 3660

    The predicted permanent deformations at critical locations on the embankment,

    including along the underlying liner system and the crest, are small. Maximum

    permanent deformations along the liner are predicted to be on the order of 15

    centimeters, which should not result in significant damage to the liner or any loss of

    containment of process fluids or impounded tailings. Maximum vertical deformations

    on the crest of the facility are expected to be less that 25 centimeters, and the facility

    will have sufficient freeboard at all times to accommodate well in excess of this. The

    model shows that the unsaturated outer shells of the leach ore embankments provide

    sufficient strength and stiffness, even after strain softening, to confine the inner

    liquefied materials and keep the overall deformations to a minimum.

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    Post-earthquake static stability analyses were completed to estimate the limit

    equilibrium factor of safety of the embankment after the earthquake shaking ceases but

    with strain softened or liquefied zones remaining (i.e., before the excess pore

    pressures generated by the earthquake are dissipated). The results gave factors of

    safety in excess of 1.1, a generally accepted minimum, for all but two cases, which

    were in an area that will be buttressed by a downstream stage of the HLP (termed

    Stage 7). This stage was not modeled. The conclusion was that this stage needed to

    be raised to elevation 3548 meters before the leach ore embankments can be loaded

    to their ultimate height. Alternatively, this constraint can be described as a maximum

    seven-lift-differential between the crest of the TTSF embankment and the crest of the

    Stage 7 buttress during incremental loading of the HLP. Stage 7 of the HLP is

    currently under construction.

    Actual Leach Ore Placement

    In 2006, a sonic drill was purchased by MYSRL to aid in definition of fines content in

    the leach ore in the La Quinua pit and on the HLP. The purpose of this is to reduce the

    risk of placement of out of spec material within specific zones within the HLP and TTSF

    embankments. The drilling method was selected based on the requirement for

    continuous and maximum sample recovery. Previously this type of rig had been used

    successfully in geotechnical and process investigations of the original Stage 1 heap.

    Leach ore placed into the early stages of the HLP before implementation of the

    zonation described previously would have been classed as Zone B, comprising typical

    La Quinua leach ore. Later, Zones A and C, and Zone D represented selective mining,

    blending and placement of cleaner and dirtier material, respectively. Review of

    leach ore placement data from the sonic rig indicated that there was not adequate

    differentiation in the fines contents of the various zones in the TTSF embankments,

    e.g., much of the material placed resembled Zone B. It is expected that more intensive

    use of the sonic drill as described above, coupled with improvements in ore control

    protocols, should improve compliance with the zone characteristics during future ore

    placement.

    It must be noted that the stability of the HLP and TTSF embankments are strongly

    influenced by the zones of saturation and pore pressures within the leach ore.

    Monitoring of water levels and positive and negative pressure heads within the

    embankments during operations will provide critical feedback with respect to theperformance of these structures relative to that which was predicted (i.e., maintenance

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    of an adequate factor of safety against slope failure). While some analyses of the HLP

    and/or TTSF indicated that a reduced leach application rate may be required when fully

    loaded, actual operational control will be based on the observed pore pressures and

    saturated zones within the embankments. Higher leach application rates and/or the

    inadvertent inclusion of higher fines content materials may be acceptable as long as

    the threshold levels are not exceeded. Because of the importance of controlling the

    process solution level and maintaining structural shells at a sufficiently low degree of

    saturation, future efforts will include an emphasis on expansion of the number and

    types of instruments within the HLP and TTSF embankments. These may comprise

    instruments capable of measuring soil suction as well as pressure head to assess

    moisture content (and hence the degree of saturation) via the moisture characteristic

    curves already defined for the various leach ore types/embankment zones.

    Conclusions

    The La Quinua TTSF is unique in that it is located within the La Quinua HLP and uses

    heap leach ore, strategically placed within specific lines and grades, to form the

    containing embankments. Contrary to standard tailings dam practices these

    embankments have been built with leach ore placed in thick, uncompacted lifts and are

    subject to leach solution being applied to, and percolating through, them. The loose

    structure makes static and dynamic liquefaction potentially a critical issue, and the key

    design principle for avoiding a liquefaction related failure is to keep the saturated or

    near saturated zones well contained in the embankments behind large structural shells

    that are unsaturated at all times. Dynamic analyses have shown that while the

    potential for liquefaction or strain softening of some saturated or near saturated zones

    in the embankments is predicted under to occur under the maximum credible

    earthquake, the predicted deformations would be minimal. Post-earthquake stability

    analyses using cyclic strain softened and liquefied strengths also showed that

    adequate stability will be maintained. These findings will be confirmed with a

    comprehensive geotechnical investigation and follow-up slope stability and dynamic

    deformation analyses of the actual materials placed in the TTSF and in the unlikely

    event that this indicates conditions markedly different from those discussed herein, the

    achievement of non-liquefiable conditions in the structural shell zones of the leach ore

    embankments will be established by controlling the leach solution application rate and

    verifying with pore pressure and soil suction monitoring.

    The advantages of this combined tailings and heap leach facility for its owner were: (1)reduced capital construction costs, (2) reduced projected operating cost, and (3) ability

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    to meet a 2008 schedule commissioning. While other tailings depositional techniques

    and locations were studied, designing and constructing the tailings impoundment within

    the HLP proved to be a truly innovative step, which in part defined MYSRLs La Quinua

    mill projects success.

    ReferencesBeatty, M.H. and P.M. Byrne, 1999, A Synthesized Approach for Modeling Liquefaction

    and Displacements, Proceedings of the International FLAC Symposium on

    Numerical Modeling in Geomechanics , A.A. Balkema Publishers.

    GEO-SLOPE, 2004a, SEEP/W Version 5.20 , GEO-SLOPE International Ltd., Calgary,

    Alberta.

    GEO-SLOPE, 2004b, SLOPE/W Version 5.20 , GEO-SLOPE International Ltd., Calgary,

    Alberta.

    Itasca, 2001, FLAC Version 4.00 - Users Manual , Itasca Consulting Group Inc.

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