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• • Figure 2 <br /> The following steps should be taken on a regular basis <br /> to reduce the use of oversized motors: Maximum RI Concentrations Overestimate <br /> Actual Concentrations During P&T <br /> • inventory all pumps,blowers,and air <br /> compressors Maz. Rlco ncenira tion <br /> 6 <br /> • note their power requirements (in horsepower) <br /> • to <br /> use their manuals and O&M data to compare a le n a e e influent <br /> � y rfrom ealm ant plant om <br /> their specifications to the actual task E extra clip n w e Its <br /> w <br /> a <br /> • conduct a cost-benefit analysis of replacing y 2 <br /> oversized equipment with new equipment or <br /> installing a variable speed drive that will allow <br /> an operator to control its power usage 0 <br /> RI Design & 0&M O&M O&M <br /> • replace equipment that demonstrate significant In a Is Ila do n Yr. 1 Yr. 3 Yr. 5 <br /> cost savings (i.e., can pay off cost of rim a (ye a rs I <br /> replacement in a few years) The concentration of PCE is measured during the <br /> remedial investigation and then during O&M. Due to <br /> In general, assuming 75%motor efficiency and pumping and the blending of water from different <br /> extraction wells and overall mass reduction in ground <br /> $0.10/kilowatt-hour(kWh), water,the influent concentration to the treatment plant <br /> during O&M is often much lower than the maximum RI <br /> 1 horsepower = $70/month concentration observed in the aquifer. <br /> The cost savings of replacing a large blower for a <br /> smaller, more efficient one is shown in Example 3. determine if components are oversized. As shown in <br /> Example 4,conducting a cost-benefit analyses will <br /> help determine if it is cost-effective to eliminate or <br /> Example 3 replace oversized components. <br /> Savings from Replacing a 50-hp Blower with a <br /> 15-hp Blower Example 4 <br /> 50 hp x $70/month/hp $3,500/month Evaluating Over-design of Treatment for Air <br /> 15 hp x S70/month/hp — $1,050/month Stripper Offgas <br /> Savings $2,450/month Operational Parameters <br /> 36 lbs of VOCs per day in plant influent <br /> Payoff time: Less than one year assuming a capital 0 lbs of VOCs per day in plant effluent <br /> cost of$25,000 to replace the blower. 36 lbs of VOCs per day in air stripper offgas <br /> Off.-as Treatment(Thermal Oxidizer)Parameters <br /> designed for 160 lbs of VOCs per hour <br /> Over-designed Treatment Components requires$22,000/month for natural gas <br /> requires$3,000/month for electricity <br /> Individual components of the treatment system may be <br /> Solution: Replace thermal oxidizer with an onsite <br /> over-designed with respect to the operational <br /> parameters of the system, such as pumping rate or carbon regeneration system. <br /> influent concentration. Figure 2 illustrates why some designed for over 50 lbs of VOCs per day <br /> systems may be over-designed. capital costs for implementation: $370,000 <br /> utility costs of$2,000 per month <br /> estimated annual cost savings: $276,000 per year <br /> Comparing design parameters and actual parameters for <br /> a treatment system and its components will help <br /> 13 <br />