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2025-09-29_REVISION - M1980244 (4)
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2025-09-29_REVISION - M1980244 (4)
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Entry Properties
Last modified
10/1/2025 3:22:20 PM
Creation date
10/1/2025 3:06:09 PM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1980244
IBM Index Class Name
Revision
Doc Date
9/29/2025
Doc Name Note
2 VLF Expansion Design Report
Doc Name
Adequacy Review Response #2
From
CC&V
To
DRMS
Type & Sequence
AM14
Email Name
ERR
ZTT
Media Type
D
Archive
No
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Cripple Creek & Victor Gold Mine <br />Valley Leach Facility Expansions <br />Detailed Design for Permitting <br />NewFields Project No. 475.0106.064 <br />September 2025 <br /> <br /> <br /> <br />Page 15 <br />4.6. Solution Collection System <br />4.6.1. High-Volume Solution Collection System <br />A system of pipes called the High-Volume Solution Collection System (HVSCS) will collect and <br />direct process solution within the facility to either ADR2 or a PSSA. The HVSCS pipes, as shown <br />on Drawing A017, are located within the DCF directly above the geomembrane liner and consist <br />of secondary perforated CPe pipes varying in size from six (6) to twenty-eight (28) inches in <br />diameter and five (5) perforated twenty-four (24) inch and twenty-eight (28) inch diameter HDPE <br />primary header pipes. Pipe connection and spacing details can be referenced on Drawing A025. <br />As shown on Detail R on Drawing A025, two (2) feet of DCF cover shall be maintained on all <br />HVSCS pipes larger than 6 inches. <br />The smaller 4-inch diameter tertiary CPe collection pipes are spaced and arranged to direct flow <br />into secondary and primary header pipes that will direct flow to the PSSA. The piping system has <br />been sized to accommodate the maximum solution application flow rate of .0055 gallons per <br />minute (gpm) per square feet (ft2) with a factor of safety of 1.5. The calculations have accounted <br />for acceptable pipe deformations from being located beneath the loads of up to 800 feet of ore. <br />Additionally, the pipes were spaced to reduce the hydraulic head on the liner system to 2 feet or <br />less. Detailed calculations for the sizing of the various pipes can be referenced in Appendix D. <br />As the HVSCS pipes leave the VLF2 Phase 4 limits, the primary pipes will transition from <br />perforated to solid and routed to the 9550-foot bench located above ADR2. These pipes will <br />empty the process solution into a tank. Under normal operating conditions, the process solution <br />will then be routed directly to ADR2 where the minerals will be extracted from the solution and <br />recycled onto the VLF. However, in upset conditions when ADR2 cannot accept a solution, the <br />process solution will be directed to an infiltration gallery constructed on the 9550-foot bench. <br />The process solution within the VLF1 Phase 6 HVSCS will route flow to the VLF1 Phase 6 PSSA <br />area and into the Solution Recovery System (SRS), as discussed in Section 4.4.3. <br />4.6.2. VLF2 Phase 4 Infiltration Gallery <br />The Theis equation was used to evaluate single and total well field infiltration rates of the <br />infiltration gallery above ADR2. Numerical modeling to assess groundwater mounding was <br />performed in HYDRUS for a period of 24 hours. <br /> <br />The gallery consists of a series of fifty-four (54) gravity fed, 4-inch diameter, 0.100-inch slotted <br />PVC wells, spaced 38 feet perpendicular and 60 feet parallel to the bench. A blank section of PVC <br />pipe will extend down 30 feet from the land surface to the top of the screened interval, followed <br />by screen down to the elevation 50 feet above the liner. More information on the infiltration <br />gallery modelling can be found in Appendix C.
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