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Development of the Zinc-Chlorine Battery for Utility

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Development of the Zinc-Chlorine Battery for Utility ( development-zinc-chlorine-battery-utility )

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Cl2 SUPPLY TEMPERATURE CONTROLLED WATER BATH VENT TO HOOD CELL THERMOMETER FLOW METER ELECTROLYTE PUMP Figure 35-2. Schematic diagram of system for running the chlorine electrode test cell. Electrolyte is maintained at 30°C. The porous graphite materials being evaluated were activated electrolytically as described in the preceding section. All materials were activated and cycled until leveling of performance with further electrolytic activation was observed. Data reported were thereby obtained with "fully" activated electrodes. The reservoir height of the water-permeability test system shown in Figure 35-3 was dictated by the pressure necessary to flow through the entire height of the most porous electrode material. A sealant was used to ensure a proper hydraulic seal. Eight hundred milliliters of water were flowed through each electrode, the timerequiredbeingdependentonthepermeabilityofeachsample. Ambienttemp­ erature was 'v22°C. Electrode thickness for each was 0.080” (0.20cm). 35-4

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