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.bpr x 2.1.6 Turbine/aenerator The turbine was an axial flow unit fabricated specifically for the plant by Barber-Nichols Engineering Company. Its rated gross output was 79.8 kW a t 2.158-MPa (313-psia) inlet pressure, 0.365-MPa (53-psis) outlet pressure, and 1.64 kg/s (1.30 x lo4 lbm/h) saturated (inlet) isobutane flow driving the induction motor/generator through a gearbox (Model EGG- 501lGB). The associated electrical/mechanical energy conversion unit was a 100-hp Marathon Electric motor/generator (explosion proof, fan cooled, 3 phase, 60 Hz, 3560 rpm, 230/460 V, and 230/115 A). 2.1.7 Vent condenser The vent condenser was an American Precision Industries (Basco Divi- sion) shell-and-tube heat exchanger connected to the vent line leading from the condenser. The single-pass Type 500 unit used for these tests had an Admiralty tube bundle with an outside area of 2.14 ma (23 ft2). Cooling-water flow was on the tube side [about 1.26 x mr/s (20 gpm)] and working-fluid flow was on the shell side. The purpose of the vent condenser was to remove as much isobutane as possible from the condenser vent stream and to return it as liquid to the samp section of the con- denser shell. 2.1.8 Coolina tower A Marley mechanical-draf t cross-flow cooling tower (Serial 13-1-600) was used to reject heat from the circulating cooling water to the ambient air. The tower fan was powered by a 5-hp motor (3 phase, 60Hz,1740 rpm, 220/440 V, and 13.7/6.85 A). The tower samp was f i t t e d with a Johnston vertical turbine pump driven 30-hp General Electric motor (3 phase, 60 Hz, 1750 rpm, 230/460 V, and 77/38.5 A) t o provide the cooling-water flow required for plant operation. Local shallow wells supplied makeup water as required. 2.2 Vertical-Fluted-Tube Condenser The design for the vertical-fluted-tube condenser (Fig. 2) was based onearlier ORNL concepts and experiments but modified to satisfy con- straints imposed by IN= for operation of the prototype power plant. 8 ? U- 7PDF Image | Raft River Geothermal Test Site
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