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    • 2. 发明授权
    • Electrochemical process for producing hydrosulfite solutions
    • 生产连二亚硫酸盐溶液的电化学工艺
    • US4992147A
    • 1991-02-12
    • US190630
    • 1988-05-05
    • Roger E. Bolick, IIDavid W. CawlfieldJimmy M. French
    • Roger E. Bolick, IIDavid W. CawlfieldJimmy M. French
    • C25B1/14
    • C25B1/14
    • A process for electrolyzing an aqueous catholyte solution comprising an alkali meal bisulfite to produce an alkali metal hydrosulfite in an electrolytic membrane cell having a cation exchange membrane separating a cathode compartment from an anode compartment, a porous cathode having a face adjacent the membrane, a back opposite, and a porous structure conjoining the face and the back, and a cathode-membrane gap between the porous cathode and the cation exchange membrane. The process comprises directing at least 50 percent of the volume of the aqueous alkali metal bisulfite catholyte through the porous cathode and transverse to the face and back of the cathode, the porous cathode having a ratio of total surface area to the projected surface area of at least about 30:1.High purity solutions of alkali metal hydrosulfites, such as sodium hydrosulfite having concentrations of at least 120 grams per liter, are produced at current densities in the range of 1.0 to 4.5 KA/m.sup.2 and at reduced cell voltages. The thiosulfate impurity concentration is from 0 to about 10 percent by weight of the hydrosulfite.
    • 电解含碱金属亚硫酸氢盐的含水阴极电解液的方法,在具有将阳极室与阳极室隔离的阳离子交换膜的电解膜电池中制造碱金属连二亚硫酸盐,具有邻近膜的表面的多孔阴极,背面 和与表面和背面结合的多孔结构以及多孔阴极和阳离子交换膜之间的阴极 - 膜间隙。 该方法包括将至少50%的碱金属亚硫酸氢盐水溶液的体积引导通过多孔阴极并横向于阴极的表面和背面,多孔阴极具有总表面积与投影表面积的比值 至少约30:1。 碱性金属连二亚硫酸盐的高纯度溶液,例如浓度为至少120克/升的连二亚硫酸钠,以1.0-4.5KA / m 2的电流密度和电池电压降低产生。 硫代硫酸盐杂质浓度为连二亚硫酸盐的0至约10重量%。