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Raft River Geothermal Test Site

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Raft River Geothermal Test Site ( raft-river-geothermal-test-site )

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kd 2. WUIPMENT AND FACILITIES The test condenser was designed for and installed i n a geothermal prototype power plant of the binary-cycle type located i n south central Idaho. This section gives details of condenser design and fabrication, specifications of other primary components of the prototype power plant, and a description of the test site. 2.1 PrototvDe Power Plant The prototype power plant was built by Idaho National Engineering Laboratory (INEL) for the U.S. Department of Energy (DOE)t o investigate concepts that have the potential to enhance the commercial production of e l e c t r i c a l power from moderate temperature geothermal resources.' The modular nature of the plant allowed various components to be replaced by alternate components that perform equivalent functions but have unconve= tional or advanced design features. In this way, selected concepts could be tested in an operational environment that would, in many respects, re- semble a practical power plant situation without incurring full-scale costs. Designed for a nominal electrical-output of 60kWwith isobutane as the primary working fluid, the plant was first operated in April 1978. After checkout testing, baseline runs were conducted t o assess equipment capabilities i n October and November 1978. Some automatic controls were then added, and t r i a l continuous operation t e s t s were conducted i n Novem- ber 1978. After further modification for automatic control and shutdown under hazardous conditions, the plant operated i n automatic run mode from August 1979 to Janaary 1980.5 .Following system alterations, the original condenser was placed by an enhanced condenser (described i n Sect. 2.21, and a direct-c tact evaporator was installed i n parallel with the origi- nal surface evaporator in preparation for the tests (begun September 1980) reported here.',' The plant provided for continuous circulation of and interaction among the brine, cooling water, and isobutane streams. Major components of the plant (Fig. 1) included surface and direct-contact evaporators, t W /3

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