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treatmentofthewatermightnothenecessary. Inadditiononlyup to1%ofthewatermassflowrateneedstohereplenished. The evaporative condenser can he huilt from hare tubes and still smaller than an unwetted device. Acknowledgments The work described was part of a study to optimize a refrigera tionsystemfora100MWHloadlevelingzinc-chloridebattery. The chlorine gas evolving during charging of the battery must be stored in form of a hydrate for safety reasons. The hydrate formation is exothermalandheatmustberemovedbymeansofaheatpump. The work was supported by Energy Development Associates, Madison Heights, Michigan under a contract PRF 0050-57 with Purdue Research Foundation. The funds granted made possible the whole investigation and is grate fullyacknowledged. TheauthorsalsoowegratitudetoMr.K.Lee,a graduate student who assisted to modify the computer programs for determination of enhancement of coefficient of performance. C-39PDF Image | Development of the Zinc-Chlorine Battery for Utility
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