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{Vert EIk .Nine <br />The discharge water was then mixed with the North Fork Upper water and compared to the suspect <br />levels (Table 66). A11 of the mixed concentrations were well below the respective suspect levels. <br />In addition. the mired concenhations were consisrent with the downstream North Fork water <br />quality, thereby- confirming the methodology. There were several metals that sere not sampled for <br />in the discharge water. Since none of the metals was detected in the upstream or downstream North <br />Fork samples, the concentration of the metals in the dischazge water, if present, was determined to <br />be very loco. Fttrdtermare, the detection levels in the downstream sample were all well below the <br />respective suspect levels. <br />NNE performed the same evaluation using a discharge rate of 2.0 cfs for the l~1\VT'F. This rate is <br />considered to be the maximum rate that could be sustained Cor significant periods of time. Table 66 <br />presen[s the results oC[his mixing zone ana[;5is. All of the mixed concentratiots are below the <br />respective suspect levels for this scenario as well. \Vhile these analyses were performed <br />considering short-term potential impacts, the evaluation could also be considered aworst-case <br />scenario for long-[elm eftects. Based on this evaluation; the discharge of mine water to the North <br />Fork will not adversely affect the use of the water by downstream agricultttral users. <br />1VWE has reviewed the salinity (I'DS) loading anah•sis in the 2001 Cumulative Hydrologic <br />Impacts Analysis (CI-IIA) for the North Fork in the contest of 14fCC's 1996 discharges. In <br />the CHIA, CDMG calculated the cumulative TDS (salinity) loading to the North Fork from <br />coal mines located in the north Fork valley. The assumptions used for diCC's contribution <br />were a discharge rate of 5,520 gpm (12.3 cfs) and a TDS concentration of 2,500 mglL. <br />W\V~ has updated the evaluation of the salinity loading based on the TDS concentrations and <br />flow rates shown in Table 66. Using the TDS concentration of 3;200 nr~/L and aflow- rate of <br />400 gpm (0.89 cfs), the salinity loading to the \orth Fork is 2,300 tons per year. Urine the <br />maximum sustained flow- rate of 900 gpm (2.0 cfs); the salinity- loading to the North Fork is <br />6,300 tons per }-ear. Both loading rates are well below the value assumed in the CPIIA for \Vest <br />Elk i4line. <br />The sewage collected from the site will be domestic in nature and will consist of soluble B.O.D., <br />volatile suspended solids, and inert solids, which will 6e treated using biological organisms to <br />aerobically stabilize the waste. Since biological treatment will be ttsed, with no chemical treatment <br />required, there should be no secondary by-products ufiich would not be similar to those existing in <br />the North Fork of the Gunnison. <br />The effluent from the treatment unit has the following characteristics: <br />Soluble B.O.D. 1 b mg1L <br />Suspended Solids B.O.D. 14 m <br /> 30 mg/[: <br />Suspended Solids 30 mef L. <br />Ammonia (NH}) 1.0 mg/L <br />Nitrate (NO3) 29 mgrl, <br />Combined Chlorine Residual 0.1 mg/L <br />Fecal Colifonns 10,000/100m1 <br />1.0670 Rnkt0lunt:005 PRIG; Rev. IfnrcA?006 <br />