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(8tu/hl (Wl -2 6- 4- 106 8 2- 6 U / + ' PREFLASHER OUTLET PRESSURE [kPa (psiall 0a-4 0A 0 32 I 106 8- 2- 6- + DESIGN POINT -0 DATA (7/1181 18:OO) A D4TA (717181 16:OO) 4- 1o5 8 - - 0 DATA (7/8181 12:OO) PREDICTION LOCUS 41 2=6 1IIIII 1 2 46810' 2 I1I1III I1 2 146810' 2' 4(OF1 TEMPERATURE DIFFERENCE AT, Fig. 19. Condenser t e s t performance. direct-contact evaporator mode. preflash variation. 22.2 to7.8K(40to140F)at a heat load of-380kW(1.3x10' Btu/h) as increased brine throttling dropped preflasher outlet pressures from 361 to 309LPa (52to45psia). Theassociated data in Fig. 20show that lower preflasher outlet pressures brought vapor space temperatures closer to the corresponding pure isobatane saturation temperatures. The third period of direct-contact operation (October 1981) involved continued examination of condenser venting effects but with the addition of vapor sampling and composition analysis t o ascertain more accurately the amounts of contaminants present. Data from two sample rum, the e a r lier just before condenser venting began and the later after30min of venting, are presented in Figs. 21and22. Asnoted in earlier figures, 309 326 361 (451 (471 (521 ORNL-OWG 82-7000 E T 0PDF Image | Raft River Geothermal Test Site
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