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(0 UJ oc UJ X Q. 0) o S < UJ c 3 (0 m UJ cc a. TEMPERATURE IN °C Figure 36-8. Operating points for an auxiliary hydrate former to concentrate inert gases. Expected inlet pressure from the top of the store during charge is 1.5 atm, Cl^ partial pressure 1.485 atm with 1% C02. With coolant at 5°C, the minimum conceivable equilibrium temperature at the outlet would be 6°C, and the maximum would be 8°C. The associated partial pressures also are shown in Figure 36-8. The effect on the calculated CO^ concentration at these temperatures is given in Table 36-3 for a charge cycle with C0^ generated at 0.03% of the Cl^ rate. DISCUSSION Three of the. possible methods to remove inerts gas which were considered in pre liminary study offer promise for successful application to the load-leveling battery system. The methods are hydrate formation, thermal diffusion, and the electrowinning cell. 36-13PDF Image | Development of the Zinc-Chlorine Battery for Utility
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