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Page 28 <br /> filter and controls into a single package. In reality, many of the existing STEP systems fall somewhere in- <br /> between. Historically, the former has a poorer performance record. <br /> Each ma-te-ialahould-a-e-vatuatedlelative�o -g�vity�castancLreliability—For-example,.STEP—pumps-can-- — <br /> range from a $150 cast iron effluent pump that will provide 5 years of service up to a $500 multi-stage high head <br /> effluent pumps that should last more than 20 years. Effluent filters can range from less than 0.5 square feet of <br /> flow through area of 1/4" mesh up to filters with more than 20 square feet at 1/8"filtering size. Tanks can range <br /> from structurally unsound tanks that crack or collapse during installation and leak immediately to water-tight <br /> tanks with water-tight connections that can provide up to 50 years of anticipated life with proper installation. <br /> When substandard materials are utilized, either in new construction, or for replacement parts, an increase in <br /> 0&M costs is a certainty. A key component during construction is the inspection and/or replacement of the <br /> existing building sewer, the source of most of the inflow that can plague system performance. <br /> 0&M of on-site STEP systems is typically divided into two activities, reactive maintenance (RM)and <br /> preventative maintenance (PM). The protocol for on-site system maintenance varies greatly, even when <br /> comparing similar systems. <br /> Most systems have been operated with varied degrees of emphasis placed on PM activities,the frequency of <br /> which is dictated by the most sensitive components. Extremely aggressive PM programs have been able to <br /> reduce RM service calls to a point that they become relatively insignificant in the overall 0&M costs. <br /> Unfortunately an overly aggressive PM program can also result in higher overall 0&M costs when PM activities <br /> unnecessarily target components that have a significant level of reliability with less PM. <br /> A less known RM protocol is a run-to-fail approach,whereby maintenance is only performed when equipment <br /> fails. Essentially, the operator waits for an alarm. While this approach is fairly uncommon, it has some important <br /> implications. While daily 0&M costs (at least in the early years) may be extremely low, increasing frequency of <br /> major repairs and replacement activities will escalate as the system suffers from neglect.Additionally, public <br /> perception of a run-to-fail approach is generally poor because this approach may place the customer in a more <br /> responsible position of identifying system alarms and reporting them to the management entity. Most studies <br /> reveal that customers want as little responsibility as possible related to their systems. <br /> In practicality, the most cost-efficient STEP management approaches balance PM and RM to achieve the lowest <br /> overall cost for 0&M. The STEP systems that typically achieve the best overall 0&M cost tend to base them on <br /> the required PM cycles for each component. For example, most field experience indicates that tank <br /> accumulations measured every 3 years will allow the operators to determine the frequency of pumping required. <br /> Tank effluent screens are generally reported to need inspection and, if necessary, annual cleaning. The <br /> minimum frequency for pump and controls inspection is also about one year. Thus, a program can be designed <br /> to do the annually required tasks, and during those visits do the other less frequently required tasks at their <br /> required frequency. Thus, the least frequent operator visits would be annually, and would consist of inspecting <br /> the screens and the pump and controls. Other tasks would be added as necessary(e.g., tank accumulation <br /> checks every 3 years).As the records of high-quality STEP components are verified by unbiased experience, <br /> these minimum frequencies may increase.. <br /> One of most important components of STEP 0&M cost is tank pump-out intervals. Extended tank pump intervals <br /> can be achieved through the use of larger tanks and through the measurement of sludge and scum <br /> accumulation. In a managed STEP system,where tank inspections are executed as part of a PM program, <br /> pump-out intervals can be extended until they are functionally required. When a management program is in <br /> place, as is the case with centrally managed STEP system, pump-outs still provide earlier pump-out intervals for <br />