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changes of the air and the water states had to he computed. Fig. 13 shows coefficients of enhancement K vs. Re„ and vs. eA v, for different relative humidities of amhient air. A Figure 13. Coefficient Ke vs. ReA for different relative humidities of ambient air. Fig. lU shows ANu^ vs. Re^ and vs. v^ for different relative humidity of amhient air. Fig. 15 compares the actual heat exchanged in the dry and the wetted heat exchanger as a function of air velocity and Reynolds number for different relative humidities. The enthalpy changes experienced hy the air passing through the heat exchanger is in dicatedhytheAi^curve. Itshouldherecognizedthatinsome instances Ai^ reaches at some locations within the channel slightly largervaluesthanbetweeninletandexit. Thissituationwilloccur when condensation is present (not shown in Fig. 12 or Table l). The figure demonstrates clearly that a given heat load can he trans ferred to air flowing through the wetted condenser at a much lower velocitythanthroughthedryone. Thisisbeneficialinrespectto 200 400 600 800 1000 1200 1400 1600 1800 REYNOLDS NUMBER ReA 0 123456 789 10 AIR VELOCITY vA(m/sec) C-29PDF Image | Development of the Zinc-Chlorine Battery for Utility
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