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GENERAL53080
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Last modified
8/24/2016 8:38:45 PM
Creation date
11/23/2007 8:18:49 PM
Metadata
Fields
Template:
DRMS Permit Index
Permit No
M1980244
IBM Index Class Name
General Documents
Doc Date
4/16/1997
Doc Name
FAX COVER CRESSON PROJECT PERMIT M-80-244 STATUS OF LOW VOLUME SOLUTION COLLECTION SYSTEM FOR
From
CRIPPLE CREEK & VICTOR GOLD MINING CO
To
DMG
Media Type
D
Archive
No
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SFNT BY ~ X17-97 15 ~ 31 ; I NDFPFNDh7VCE M I N l~ ~ 303 832 8106 ~ # 6 <br />selection, discussed later, appeared to best represent the field measurements, If them are other imperfections at <br />higher elevazioae, they may be described by the more "standud' 2t 1 mm diameter. An czautple of the result of <br />many of the interim cottgnttations using the revisrd "initial' location and size, specifically the project:d head-flow <br />relationships for the St2.5 mm + 2f1 mm defect coafigurtttion acrd the St2.5 tom single imperfeaioa <br />ennftguration, ue provided as AuarR*~.:.r!c 6 and 7. <br />One of the variants of the configuration assumed a 6t3 mm diartteter imperfection az the third interval (rt 9257.5 <br />ft., between elevations 9255 [t. and 9260 tt.), and ao additional hrgterfectioae at higher elevations. This <br />wnliguration, the graph for which is provided as Attachmrnt 8, seems to represent a good fit to the field data. It <br />mould, CC&V believra. be used to check the LVSCS pump system for future capability. However, it would be <br />prc[narure to dtxtend entirely on this onnfiguration until higher pregnant solution heads have been measured. <br />Therefore, the 6t3 mm diameter iatperfectioa az elevation 9257.5 fee[ cane rerun with 2t1 mm diartterer <br />imperfections a[ higher elevations (one per sore, on the average), These probability curves of flow ventts head ace <br />presented in Attachment 9. This group of curves appears to represent the field data quite well. <br />in addition, a configurations with a 7±3.5 tom impertiution located in flu third interval (a[ 9257.5 ft) and 2 t 1 tam <br />imperfections at higher elevations, and with only the 713.5 mm iatperfectioa at the third interval were among the <br />wmbinatioru checked. The graphs for these two wnfigtuation are provided as Attachrttents 10 and 11. While these <br />graphs appear ro move the observed points to theoretical curves representing even ]ower probabilities than other, <br />they does not seem, as yet, to reflect the empirical curve itself. Therefore, these are only preseata:d, now, as <br />examples of the analyses performed. <br />In summary, the best fit to the current data base identified to date is the bt3 rnm sinpJe defect. However, in <br />rcxoguirion of the low pregnant solmion head oavrring ro date, CC&V hag selected the 6t3 mm + 2t1 tt~ <br />configura[ioa for itc cheek of pump design. <br />To reiterate what is likely obvious a[ this point, lhase computations ruing [he current LVSCS Phase II data have <br />been performs! to assess the adequacy of the excess pumping capadty of the LVSCS Phase II system. As the EPA <br />points out, if the drainage capacity ntezts or excewds the inflow rapacity, the system is acceptable. Once a good <br />representation of the deplnytoem of the imperfections has btxn developed, u has been accomplished with the resttJts <br />reported above, the flows that aright be anticipated [o develop as the pregtunt solution head ia.~reasnl may be better <br />estimatsl. For example, if flows expxted for the configtuaiioa of the 7 f 3.5 tom imperfection az dre third elevation <br />interval of the PLS, with no other imperfections, are examined, the flow raze az the 97.5 percent confda;. _ce intorval <br />and xt the tnazimum pregnant solution head of 50 fee[, would be 23 gallons per minute (gpm) (Attach~sunt 10). <br />To represent the eonfigttration that likely exists and to be conservative lry assutoing itnperfec[ions exist az higher <br />elevations, CCc$V selected Ilte configuration of the 6t3 nun imperfatioa at the sewad imerval elevazion with 2f 1 <br />rnm defects !Dental at higher elevations. The flow rate at the 50-foot head would be slightly less than 21 gpm <br />(Attachment 8). Of course, it is unlilnly that the ftd150 fool head would be reached, bocattse this is the maximum <br />height that mould be physically achieval within the desig»ated PLS of Phase II and it would involve excessive <br />inventory of gold in the fluid phase. <br />CC&V employs, at present, two pumps in each LVSCS. These ptarqu are installed in separate riser pumps located <br />relatively close to each other. They arc EPG Model TSP 3-9 (aka WSI)PT 3-9), electrically powered (lhp), <br />submersible units designed for side slope riser leacha[e removal. The pump curves ue attached (Auechmen[ l l). <br />The static head to be overoomc az the Phase I[ area is approximately 65 feet. Aewrding to tha pump curves <br />dccxibing these TSP3-9 ptunps, the capac:iry of wch of the pampa az heeds on the order of 100 feet is about 2't <br />gpm. As such, these pumps arc adtquate for presertt and projected pumping. <br />CCBcV has investigued othu pump arrangements that would locrnse the pumping eepseiry in tarots u dte flow <br />n[e should such additional putuping capacity be required. Far example, the same manutacttue can supply the TSP3 <br />model in other larger configurations that would increase the flow rete. Also available are TSPS and TSPB tnadela. <br />
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