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RECOVERY OF CYANIDE FROM WASTE WATERS BY AN ION EXCHANGE PROCESS

机译:离子交换法从废水中回收氰化物。

摘要

ROGERS, BERESKIN & PARRInventor: Carla C. FreyW. Ronald HatchMargaret K. WitteTitle: RECOVERY OF CYANIDE FROM WASTEWATERS BY AN ION EXCHANGE PROCESSABSTRACT OF THE DISCLOSUREA process is described for the substantially completerecovery of cyanide reagent and metal forming water solublemetal-cyanide complexes contained in mill effluents andwaste waters. The process is comprised of a loading cyclewherein the metal-cyanide complexes are adsorbed onto abasic ion exchange resin and the free cyanide containingcolumn effluent is returned to the mill. The metal ions,which are usually mostly copper, nickel and zinc, and thecomplexing cyanide are eluted in the subsequent regenerantcycle by an acid solution having controlled pH and controlledredox potential, the latter being measured against thesaturated calomel electrode. The preferred oxidant tocontrol the redox potential of the regenerant solution ishydrogen peroxide. The generated hydrogen cyanide is spargedwith air, or removed by subatmospheric pressure from theregenerant solution, and dissolved in an alkaline scrubbersolution for reuse. The metal ions are recovered from ableed solution.
机译:罗杰斯,贝尔斯金和帕尔发明人:Carla C. Frey罗纳德·哈奇玛格丽特·维特标题:从废料中回收氰化物离子交换法披露摘要描述了基本完成的过程氰化物试剂和金属形成水溶性的回收工厂废水和废水中所含的金属氰化物络合物浪费水。该过程包括一个加载周期其中金属氰化物络合物被吸附到碱性离子交换树脂和游离氰柱流出物返回到磨机。金属离子通常主要是铜,镍和锌,络合氰化物在随后的再生剂中洗脱通过控制pH值和控制pH值的酸性溶液循环氧化还原电势,后者是根据饱和甘汞电极。首选氧化剂控制再生溶液的氧化还原电位是过氧化氢。喷射产生的氰化氢空气,或通过低于大气压从再生溶液,并溶于碱性洗涤塔重用的解决方案。金属离子从排液。

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