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The gas turbine will be a General Electric Model LM5000 <br /> STSG high efficiency type. The LM5000 is a 3 shaft gas <br /> turbine with direct drive to the electric generator. The <br /> hot exhaust gases from the gas turbine will be ducted to a <br /> heat recovery steam generator. The electrical output of <br /> the gas turbine generator at average site conditions will <br /> be 46,950 W. <br /> The gas turbine mechanical accessories include a lube oil <br /> system, a fuel gas regulating system and a steam injection <br /> system. Projective devices including pressure and <br /> temperature gauges, vibration monitors, and fire detectors <br /> will be provided for safety alarm and shutdown functions. <br /> The electric generator will be direct coupled to the <br /> output shaft of the gas turbine. The generator will be a <br /> 3600 RPM, 13.0kV, 3 phase, 60 hertz , totally enclosed <br /> water--to--air cooled unit rated at 45,400 KVA at 0. 90 power <br /> factor. <br /> b. Heat Recovery Boiler <br /> The gas turbine will deliver 1 , 16 ,650 lb/hr exhaust gas <br /> at a temperature of 763"F to the heat recovery boiler <br /> during normal ambient temperature conditions (62"F) . The <br /> boiler will be a three pressure level , finned tube heat <br /> recovery type unit designed to produce a total of 129,000 <br /> pph of steam. High pressure_ superheated steam will be <br /> generated at 650 psig , 565"F; intermediate pressure <br /> superheated steam at 300 psig , 470"F; and low pressure <br /> saturated steam at approximately 25 psig. <br /> The high pressure steam will be injected into the gas <br /> turbine for emissions control and power augmentation. The <br /> intermediate pressure steam will be delivered to LOF and <br /> injected into the gas turbine for power augmentation. The <br /> low pressure steam will be used for deaeration, feedwater <br /> heating and supply to the chiller equipment. <br /> c. Selective Catalytic Reduction System <br /> A Selective Catalytic Reduction (SCR) System will be <br /> installed in the boiler to reduce Nitrous Oxide (NOx ) <br /> emissions. Ammonia will be injected into the gas stream <br /> which will react with the NOx in the presence of the <br /> catalyst to produce harmless nitrogen gas and water vapor. <br /> Any remaining NOx emitted to the atmosphere will be within <br /> the allowable limit=s established by the San Joaquin County <br /> Air Pollution Control District. By design, the ammonia <br /> slip is limited to 10 ppmvd , the TLV is 25 ppmvd. The <br /> ammonia storage area will be equipped with ammonia <br /> monitors which will alarm if a leak occurs. Also, there <br /> will be self-contained breathing equipment for personnel <br /> protection. <br />