Laserfiche WebLink
STIG PROJECT -- EVALUATION OF WATER FOR INJECTION -- 28 March 1994 19 <br /> 15. Ball, J.W. and D.K. Nordstrom, WATEQ4F for calculating speciation of major, trace, and <br /> redox elements in natural waters: US Geol.Surv. Open-File Report 91-183, 1991, Menlo Park, <br /> California. <br /> 16. The crystal composition is complex, suggesting that growth would be difficult, except in <br /> (probably)limited circumstances.Additional references were sought,but not found in a cursory <br /> review of literature, suggesting an uncommon or rare occurrence. Computed equilibrium <br /> deposition potential exceeds 3 tons per month, but no deposition at all seems plausible also. If <br /> large accumulations of sludge do not develop during early operations then this variety of apatite <br /> may be disregarded. <br /> 17. Amorphous silica saturation is reached at 120 mg/kg at 77°F. Concentrations higher than <br /> that, risk deposition of silica on available surfaces. For the injection system, critical surfaces <br /> include the rock porosity near the wellbore. <br /> 18. For a concentration multiplier of 1.86 and concentration limit of 120 mg/kg, maximum <br /> input concentration would be 120/1.86=64.5 mg/kg.Statistics for measured concentrations are; <br /> avg = 59.5, std. dev = 11.2. The maximum tolerable input concentration (64.5 mg/kg) <br /> corresponds to +0.45 standard deviations above the average. Based on a Gaussian (normal) <br /> distribution, such a normally varying fluid would be injectable 67 percent of the "time". <br /> Irregularities of the silica concentration changes could cause doubt that the distribution <br /> is Gaussian. An alternative method to estimate statistical utility of injection/disposal can be <br /> based directly on the data. Using the values on which Figure 2 is based, and limiting the tally <br /> to different-day samples, 13 of 18 sampling days (72%) had silica <64.5 mg/kg. These two <br /> results are not statistically distinct. Nominally, injectability can be expected to be practical for <br /> about 2/3 of the time. <br /> 19.The procedure above disregards silica inhibitor (dispersant) that is planned for addition to <br /> the RO input fluid, specifically to stabilize silica there. Residuals of inhibitor may plausibly <br /> be present in the injectate mixture. Furthermore, it could appear practical to augment the <br /> inhibitor concentration for fluids which exceed the injectability index in order that they may <br /> be"safely" injected. However, at the present level of documentation, the stabilization actually <br /> imparted to the supersaturated silica concentrations is ambiguous for conditions in rocks near <br /> the wellbore. Until unambiguous support is developed, injection of supersaturated <br /> concentrations of silica into the well could be considered imprudent. <br /> 20. If chemically active fluid were in the well after closure, it could be displaced by pumping <br /> in two, or more, casing volumes of non-active fluid. Alternatively, plant operating conditions <br /> might be susceptible to modification yielding a smaller net concentration factor. This would <br /> require in-plant adjustments of rates involved with equation(2). The utility of this option has <br /> limits which deserve exploration prior to the need. <br /> DON MICHELS ASSOCIATES -Missoula,Montana USA <br />