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2 andliquidpressuresof6.9and13.8k/m (1and2psig). The controller set point was adjusted by means of the valve seat position toread6.22+0.7kN/m (25+3inchesofwater). Differentialpressure wasmeasuredwithaMagnehelicgage(0-50inchesofwater). Liquid pressurewasmeasuredwitha0-15psiggage. Flowratewasmeasured with a Brooks rotameter. DataRecordngRequirements. Entriesweremadeinalogbookof/P at each flow rate and pressure. Values and Tolerances. Differential pressure was required to be 6.22 + 0.7 kN/m2 (25 + 3 inches of water). Results. Themeasuredsetpointsforthe/APcontrollerswerethe following: 1. 2. 3. 4. 02 kN/m2 (in. H2 0) 5.97 - 6.72 (24.0 - 27.0) 6.10 - 6.72 (24.5 - 27.0) 5.97 - 6.85 (24.0 - 27.5) 5.97 - 6.72 (24.0 - 27.0) H2 kN/m (in. H2 0) 6.o5 - 6.85 (24.3 - 27.5) 6.10 - 6.85 (24.5 - 27.5) 6.10 - 6.97 (24.5 - 28.0) 6.10 - 6.85 (24.5 - 27.5) External Leakage. Conditions. Inletliquidandgasportsweremanifolded,exitgas port was sealed and the unit was submerged in water with 34.5 kN/m2 (5psig)N pressureonthemanifold. 2 Data Recording Requirements. Log book entry; pass or fail. No data sheet. Results.AlloftheAPcontrollerspassedthistest. 3.2.3 WaterFeedController Conditions. The water feed controller was installed in a bench reservoir containingwater. EndtoendsignaloutputvsH20headininches, control band, hysteresis, level safeties, and timing circuits were monitored. 46PDF Image | WATER ELECTROLYSIS SYSTEM REFURBISHMENT
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