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2019-12-13_REVISION - M1980244 (60)
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2019-12-13_REVISION - M1980244 (60)
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Last modified
1/7/2025 2:33:04 AM
Creation date
12/17/2019 8:34:53 AM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1980244
IBM Index Class Name
Revision
Doc Date
12/13/2019
Doc Name Note
Appendix 10 - 11
Doc Name
Request For Amendment To Permit
From
CC&V
To
DRMS
Type & Sequence
AM13
Email Name
TC1
MAC
BFB
ERR
JPL
Media Type
D
Archive
No
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ResponseSpill <br /> NEWMONT <br /> NORTH AWPICA <br /> Sustainability & External Relations <br /> 4.6 Process Solution Enhancement System(PSES) <br /> The PSES Plant is sized to treat the entire volume of process solution at CC&V in a two-stage process.The basic <br /> treatment steps consist of: <br /> • Combining the incoming pregnant solutions in a large tank/clarifier allowing solids precipitation to occur <br /> ahead of the existing gold recovery plant. <br /> • Recovering the nascent precipitates along with any carbon fines present in recovery plant effluent using a <br /> coagulation/sedimentation process. <br /> Clarified effluent from the treatment plant is returned to the Arequa Gulch Valley Leach Facility(VLF-1)through <br /> existing pumping/irrigation networks;solids are filter-pressed and bagged for transport and sale to a refiner to <br /> recover the contained gold associated with the fine carbon. Capture and sale of product solids prevents carbon <br /> from returning to the VLF-1 where it can rob gold from pregnant leach solutions. <br /> The system consists of three separate processes: (1)a Pregnant Solution (PS)Stabilization Process to equilibrate <br /> the chemistry of the pregnant solutions prior to the ADR-1 Plant; (2)a process solution enhancement system to <br /> remove solids from the barren solution before pumping it back to the VLF-1; and (3)a process to dewater the <br /> solids removed from the process solution. <br /> These processes are discussed in more detail below. <br /> Pregnant Solution Stabilization:The PSES process provides the reaction conditions needed to help stabilize the PS <br /> prior to the ADR-1.The PS from VLF-1 Phases 1, 2 and 5 flow to the PS Stabilization Tank.The PS from VLF-1 Phase <br /> 4 flows to the Enrichment Tank, but could be directed to the stabilization tank if desired.The PS Stabilization Tank <br /> provides time for the precipitation reactions to come to completion and settles some of the precipitated solids. <br /> These solids are re-circulated to enhance the precipitation process.The system has the ability to periodically feed <br /> soda ash to aid the precipitation.The PS pump station transfers the PS to the ADR-1. <br /> Barren Solution Enhancement:The system directs the Barren Solution (BS)from ADR-1 Plant Trains A, B, C, D and <br /> E to a CoMag process for suspended solids removal. CoMag uses chemical coagulation,flocculation and ballasted <br /> sedimentation to remove activated carbon fines, precipitates and other solids.The resulting enhanced barren(EB) <br /> solution increases the operating life of the drip emitters on the VLF-1.The EB solution pump station transfers the <br /> EB solution to the barren tank. <br /> Product Solids Recovery:An important benefit of the enhancement process is recovery of fine activated carbon <br /> solids from the BS.Additional gold recovery is expected from these solids as well. <br /> 4.6.1 Materials Storage/Secondary Containment <br /> Petroleum-based oils or fuels stored at the PSES Facility is limited to two electrical transformers, located outside <br /> on the northeast side of the building.The type and quantities of oil in these transformers is listed in Table 7. <br /> Occasionally small vehicles such as mine supervisor trucks and delivery trucks will be in the general vicinity of the <br /> PSES Plant.Such vehicles conceivably could have spills or tank ruptures nearby. <br /> Any spills will be contained inside of the PSES building itself, or within the VLF-1 lined system. Delivery trucks are <br /> staged on a concrete pad south of the plant.This unloading and storage area is protected by bollards to prevent <br /> accidental collisions between trucks and storage tanks. <br /> Any spills or releases of materials from the tanks/containers located outside of the PSE Plant would be contained <br /> by the liner and would report to the VLF-1. Spills or releases from the tanks inside the plant would be captured <br /> within the building itself. <br /> --- -------- _ ___---- _____ -----_.- __-- ----- ------__. ---- ------ __..--- <br /> Department THIS DOCUMENT IS UNCONTROLLED IN HARDCOPY FORMAT Doc Id:NA CCV-SER-PLAN- <br /> _..._... 1930_ — <br />
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