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Ameron Dualoy° Pipe Monitoring System <br /> 4.0 TEST RESULTS AND CALCULATIONS <br /> The results of this testing were used to determine if the operating conditions in <br /> an installed line are likely to produce a false alarm. The problem of a missed detection <br /> is much less likely as the test times for producing an alarm with a relatively small leak <br /> are short. Any leak of measurable rate will eventually produce an alarm, probably in <br /> less than one day, before any product is lost to the environment. If the measurements <br /> in level change in the reservoir are small under the test conditions, the probability of a <br /> false alarm is low. The test results for this evaluation are summarized in Table 1 listing <br /> all of the important parameters measured in this evaluation. <br /> Table 1. Summary of Test Results for 300 ft Pipeline Without Trapped Vapor. <br /> Parameter Worst Case Extrapolated <br /> Values for Test Results for <br /> Line 21 ft300 ft Line* <br /> Pressure chane (psi) 100 30 <br /> Level change due to pressure in/psi 0.00125 0.01786 <br /> Gross level change due to pressure (in) 0.125 0.54 <br /> Temperature change de F 68 30 <br /> Level change due to temperature in/de F)** 0.0148 0.2115 <br /> Gross level change due to temperature in 1.006 6.35 <br /> Minimumspacing of sensors in reservoir (in)*** 1.131 6.89 <br /> Alarmspacing — Service Factor of 1.5 in 1.70 10.34 <br /> Max Pipeline Length for this reservoirspacing ft21 300 <br /> *These values assume worst-case installed conditions. <br /> ** For worst-case temperature effects see Table 2. <br /> ***The minimum spacing includes both temperature and pressure effects operating in the same <br /> direction. The initial brine level is assumed to be near the midpoint of the sensor spacing. <br /> Primary Pipe Pressure Test <br /> Pressurization of the primary pipe produces a slight increase in the brine level. <br /> The results of the pressure test are provided in Figure D-1 in Appendix D. The trend is <br /> for the level to increase slightly as the pressure in the primary pipe is increased as was <br /> expected. The regression line for both tests gives a slope of 0.0002 inches per psi of <br /> pressure applied. The maximum observed range of level changes for the highest and <br /> lowest points were 0.125 for the first test and 0.095 inches for the second test. Using <br /> the worst-case conditions, the level change per psi is 0.00125 inches per psi for the 21 <br /> ft test line. <br /> If a linear extrapolation of the worst-case conditions (0.125 in/100 psi for a 21 ft <br /> pipeline) to a pressure of 30 psi in a pipe of 300 ft in length, the level increase would be <br /> expected to be approximately 0.54 inches, well below the change required to produce <br /> an alarm in a properly designed system. Since the pressure change of 100 psig is <br /> considerably larger than would normally be expected for a typical service station, the <br /> effects of pressure are minimal for the Ameron pipeline system. <br /> Page 7 of 12 <br />