Page 219 - Lindens Handbook of Batteries
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ZINC-CARBON BATTERIES—LECLANCHÉ AND ZINC CHLORIDE CELL SYSTEMS       9.13

                                                      TABLE 9.3  Electrolyte Formulations*
                                                           Constituent    Weight %
                                                                Electrolyte I
                                                       NH Cl                26.0
                                                          4
                                                       ZnCl 2               8.8
                                                       H O                  65.2
                                                        2
                                                       Zinc-corrosion inhibitor  0.25–1.0
                                                                Electrolyte II
                                                       ZnCl 2              15–40
                                                       H O                 60–85
                                                        2
                                                       Zinc-corrosion inhibitor  0.02–1.0
                                                         *Electrolyte I based on Kozawa and Powers. 7
                                                         Electrolyte II based on Cahoon. 5





                    9.5.6  Corrosion Inhibitor
                                The classical zinc corrosion inhibitor has been mercuric or mercurous chloride, which forms an
                                amalgam with the zinc. Cadmium and lead, which reside in the zinc alloy, also provide zinc anode
                                corrosion  protection.  Other  materials  like  potassium  chromate  or  dichromate,  used  successfully
                                in the past, form oxide films on the zinc and protect via passivation. Surface-active organic com-
                                pounds, which coat the zinc, usually from solution, improve the wetting characteristic of the surface
                                unifying the potential. Inhibitors are usually introduced into the cell via the electrolyte or as part
                                of the coating on the paper separator. Zinc cans could be pretreated; however, this is ordinarily not
                                practical.
                                   Environmental concerns have generally eliminated the use of mercury and cadmium in these bat-
                                teries. These restrictions are posing problems for battery manufacturers in the areas of sealing, shelf
                                storage reliability, and leakage. This is critical for zinc chloride cells in that the lower pH electrolyte
                                can result in the formation of excessive hydrogen gas due to zinc dissolution. Certain classes of
                                materials considered for use to supplant mercury include gallium, indium, lead, tin, and bismuth,
                                either alloyed into the zinc or added to the electrolyte from their soluble salts. Other organic materi-
                                als, like glycols and silicates, offer protection alternatives. Additional restrictions on lead use, which
                                are already stringent, may also be imposed in the future.


                    9.5.7  Carbon Rod
                                The carbon rod used in round cells is inserted into the bobbin and performs the functions of current
                                collector. It also performs as a seal vent in systems without a positive venting seal. It is typically
                                made of compressed carbon, graphite, and binder, formed by extrusion, and cured by baking. It has,
                                by design, a very low electrical resistance. In Leclanché and zinc chloride cells with asphalt seals,
                                it provides a vent path for hydrogen and carbon dioxide gases that might build up in and above
                                the cathode during heavy discharge or elevated temperature storage. Raw carbon rods are initially
                                porous, but are treated with enough oils or waxes to prevent water loss (very harmful to cell shelf
                                life)  and  electrolyte  leakage. A  specific  level  of  porosity  is  maintained  to  allow  passage  of  the
                                evolved gases. Ideally, the treated carbon should pass internally evolved gases, but not pass oxygen
                                into the cell, which could add to zinc corrosion during storage. Typically this method of venting
                                gases is variable and less reliable then the use of venting seals. 4,6
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