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6II i 4 2 ;0U 4 (3 106 - ORNL-DWG 824996 ETD II 29 r 8 6 4 2 noted earlier, these predictions are based on (1) laboratory dataZ for R-600a condensing outside tube -E(Appendix B) and (2) the Dittus-Boel ter forced-convection correlation' fluid contaminants. Water property values for viscosity, specific heat, and thermal conductivity were taken from Ref. 11, and those for density were taken from Ref. 12. Three distinct periods were devoted to tests in the surface evapora- tor mode: SeptemberOctober 1980, December 1980, and March 1981. The f i r s t period was intended t o be a shakedown sequence t o map out operating ranges of heat load and water flow for the modified prototype + DESIGN LOCUS: WATER FLOW = 1.893 X m3/s (300 gpm) WATER INLET TEMPERATURE = 297.039 K (75OF) DESIGN POINT: HEAT LOAD = 5.86 x 105 w I 1 (2.00X lo6Btu/h) 2 A 6810' 2 (K) IIIIIIIII 2 46810' 2 4(OF) TEMPERATURE DIFFERENCE AT,,,, Fig. 10. Condenser design performance locus. with no allowance for fouling or working-PDF Image | Raft River Geothermal Test Site
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