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Pipeline and Reservoir Characteristics <br /> The evaluation testing was conducted in a pipeline with a capacity of 4.22 gallons <br /> with an inside diameter of 2.22 inches and a length of 21 ft. <br /> The pipeline construction material was ( ) steel (X) fiberglass ( ) flexible materials. <br /> The capacity of the liquid reservoir is approximately 0.56 gallons <br /> The dimensions of the reservoir are approximately 15 inches tall with a cross section <br /> surface area of approximately 8.66 square inches <br /> The liquid in the interstice was brine (30% CaC121. <br /> The sensor spacing used to measure the reservoir level alarms is 11.6 inches for a <br /> pipeline length of 300 ft. <br /> The sensor operating principle is can be any liquid that produces a <br /> signal change from the sensor. (e.g., float switches or optical switches) <br /> The approximate volume change to produce an alarm was 1,000 ml when the <br /> float is initially at the midpoint of the reservoir. <br /> The sensor(s) was previously evaluated (X) yes ( ) no. <br /> If so, reference the evaluation (see Appendix C) <br /> Pressure Test <br /> The tests were conducted with the primary line pressurized to 100 psi. <br /> The worst-case level change in the liquid reservoir was observed to 0.00125 inches <br /> per psi change in pressure from 0 psi to 100 psi. <br /> The liquid used to pressurize the primary pipe was water . <br /> Temperature Effects Without Trapped Vapor <br /> The nominal temperature of the hot product circulated through the line during the test <br /> was 100 deg F. <br /> The initial ambient temperature of the liquid in the interstice was 63 deg F. <br /> The final interstitial temperature was 100 deg F <br /> A total volume of 60 - 70 gallons passed through the line during the test. <br /> The temperature difference was 37 deg F. <br /> The level change in the reservoir was 0.28 inches. <br /> The level change was determined to be 0.0076 inches per deg F. <br /> The nominal temperature of the cold product circulated through the line during the test <br /> was 32 deg F. <br /> The initial temperature of the liquid in the interstice was 71 deg F. <br /> The final interstitial temperature was 37 deg F <br /> A total volume of 60 -70 gallons passed through the line during the test. <br /> The temperature difference was 34 deg F. <br /> The level change in the reservoir was 0.25 inches. <br /> The level change was determined to be 0.0073 inches per deg F. <br /> Liquid Filled Interstitial Monitoring—Results Forms Page 2 of 4 <br />