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STIG PROJECT -- EVALUATION OF WATER FOR INJECTION -- 28 March 1994 15 <br /> ;600 gpm going to WSWPCF. When silica concentrations are not favorable, all the discharge from <br /> the waste receiver tank must be directed to WSWPCF. This section describes how silica <br /> concentrations may be monitored to control acceptable splitting of the waste stream. <br /> Timing Aspects <br /> Less than 5 mg/kg separate the average concentration (59.5 mg/kg) from the critical <br /> concentration(64.5 mg/kg).Figure 2A shows that silica concentrations can shift at least as quickly <br /> as 1 mg/kg per hour for a few tens of hours. When monitoring silica concentrations, a component <br /> of time will be involved with obtaining an analytical result for water currently in the process <br /> stream. In practice, a trend cannot be identified with fewer than three sequential samples, and <br /> verification could require a fourth and plausibly a fifth sample.Subsequent increments of time will <br /> be required to review the data in order to make a decision about changing the split of discharged <br /> waste. <br /> Once the well is closed, stagnant, supersaturated fluid could deposit minerals in sensitive <br /> porosity near the wellbore. The resting time after closure will favor deposition of a tiny increment <br /> of mineral as the chemical aspects approach equilibrium. There may be other practical <br /> altenatives20, but over the life of the project, many occasions of closure, each with an <br /> individually tiny effect, could have a significant cumulative effect. Accordingly a good effort <br /> should be made to respond quickly enough to a rising silica concentration that even these small <br /> increments of deposition are avoided. Of course, responding too soon carries a statistical risk that <br /> a projected rise in silica concentration does not actually reach the critical level, resulting in loss <br /> of advantage that injection is intended to give. Too slow a response risks mineral deposition in <br /> rock porosity near the wellbore. <br /> Monitoring and Data Review <br /> The description above appears to require a capability to respond within a small number of <br /> hours. Two, or so, could be a reasonable target. This could be met by continuous, or semi- <br /> continuous analysis of silica in selected parts of the in-plant flow system. Two silica monitoring <br /> locations are indicated in Figure 1. Automated sampling frequency of three per hour, or faster, <br /> would be satisfactory. An automated method of reviewing results should be considered because <br /> substantial periods of time will pass in which no symptom of risk would be apparent. The <br /> automated data review system should respond both to near-critical concentrations and to high rates <br /> of change of concentration. <br /> Location of silica monitor #1 is indicated (Figure 1) on the discharge of the ultrafilter. <br /> This is considered superior to upstream alternatives for analytical reasons.Silica in WSWPCF water <br /> may not be entirely monomeric, but it is the monomeric form that is of concern with calculated <br /> saturations. Ultrafiltration will probably remove most of the extraneous varieties, providing for <br /> a more reliable analytical result from the sampler. <br /> Locating the sampler at an alternative,downstream location,such as the RO waste streams, <br /> reduce the practical response time for the system. Also, a concentration measured there must be <br /> compensated by the current RO concentration factor before it could be reliably applied to other <br /> units.Associated error or uncertainty would propagate unfavorably in the arithmetic of assessment. <br /> To use the monitoring results,combine them with a multiplier(m*) derived from equation <br /> DON MICHELS ASSOCIATES -Missoula,Montana USA <br />