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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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TERMINAL BUS CONNECTION ELECTROLYTE | INLET TEFLON, BODY TEFLON FRAME ELECTRODE/BUS ASSEMBLY Figure 28-3. Demountable electrode assembly. Two identical units are employed. Note that electrode/bus assembly is easily weighed. Proposed Experimental Approach A two-level factorial approach in three variables as detailed in Table 28-3 will be employed. The third "paired" variable is admittedly a concession to the use of a chlorine-chlorine cell, and reflects the pH and chloride-concentration swing associated with battery operation. Temperature and current density levels specified should ensure a 10-20 fold range in corrosion. When obtained as a function of electrolyte swing, the data generated should allow definitive judgements as to any limitations which may exist and, in addition, provide direction as to any required corrective measures which must be undertaken. 28-10

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