首页> 外国专利> Purification and regeneration of a spent chemical nickel plating bath comprises a protonation stage and a demineralization stage involving removal of orthophosphite ions from the bath by using an ion-exchange membrane

Purification and regeneration of a spent chemical nickel plating bath comprises a protonation stage and a demineralization stage involving removal of orthophosphite ions from the bath by using an ion-exchange membrane

机译:用过的化学镍电镀液的纯化和再生包括质子化阶段和脱盐阶段,该阶段包括使用离子交换膜从镀液中去除正亚磷酸根离子

摘要

Purification and regeneration of a chemical nickel plating bath containing hypophosphite, orthophosphite and nickel ions and at least one dissociated weak acid involves a protonation stage, in which the pH of the bath is changed, and a demineralization stage, in which orthophosphite ions are removed from the bath by using an ion-exchange membrane at 15-50 deg C. The protonation stage can carried out by adding a strong acid, preferably HCl, directly to the bath, or by using an ion-exchange membrane which allows transfer of protons from an acidic solution to the spent chemical nickel plating bath. The demineralization stage is carried out at 15-50 deg C for 1-150 minutes. Preferably, the process comprises a third stage involving the addition of at least one nickel salt selected from nickel sulfate, nickel acetate, nickel carbonates, nickel fluoride, nickel sulfonate and nickel hypophosphite. Independent claims are given for: (a) application of the above process to a chemical nickel plating bath that also includes sulfate ions; and (b) an installation for regenerating a chemical nickel plating bath. The installation includes a first unit including: (1) insoluble cathode (C) and insoluble anode (A) (2) anode (9) and cathode (2) compartments containing electrolyte in direct contact with the anode (A) and cathode (C), respectively; (3) a side compartment separate from the cathode compartment (5) be an anion-exchange membrane (A56); and (4) a stack of at least one electrodialysis cell (7) for receiving the spent bath containing molecular weak acids and a compartment (8) for recovery of orthophosphite ions next to the electrodialysis cell (7). The electrodialysis cell (7) is defined on the cathode side by a cation exchange membrane (C67) and separated from the orthophosphite ion recovery compartment (8) by an anion exchange membrane (A78). The orthophosphite ion recovery compartment (8) is defined on the anode side by a cation exchange membrane (C89).
机译:包含次磷酸盐,正亚磷酸盐和镍离子以及至少一种离解的弱酸的化学镀镍浴的纯化和再生涉及质子化阶段(其中改变浴的pH值)和去矿物质阶段(其中从中移除正亚磷酸盐离子)可以通过在15-50摄氏度下使用离子交换膜对镀液进行处理。质子化阶段可以通过直接向镀液中添加强酸(最好是HCl)或使用允许质子从膜上转移的离子交换膜来进行。废化学镍镀液中的酸性溶液。脱盐阶段在15-50摄氏度下进行1-150分钟。优选地,该方法包括第三阶段,该第三阶段包括添加至少一种选自硫酸镍,乙酸镍,碳酸镍,氟化镍,磺酸镍和次磷酸镍的镍盐。具有以下独立权利要求:(a)将上述方法应用于还包含硫酸根离子的化学镀镍浴; (b)使化学镀镍浴再生的设备。该设备包括第一单元,该单元包括:(1)不溶性阴极(C)和不溶性阳极(A)(2)阳极(9)和阴极(2)隔室,其中包含与阳极(A)和阴极(C)直接接触的电解质), 分别; (3)与阴极室(5)分开的侧室是阴离子交换膜(A56)。 (4)至少一个电渗析池(7)的堆叠,该电渗析池(7)用于容纳含有分子弱酸的废液;和电渗析池(7)旁边的用于回收正亚磷酸根离子的隔室(8)。电渗析池(7)在阴极侧由阳离子交换膜(C67)限定,并通过阴离子交换膜(A78)与正亚磷酸根离子回收室(8)隔开。正磷酸根离子回收室(8)在阳极侧由阳离子交换膜(C89)限定。

著录项

  • 公开/公告号FR2798677A1

    专利类型

  • 公开/公告日2001-03-23

    原文格式PDF

  • 申请/专利权人 ETABLISSEMENTS A. RICHARD;

    申请/专利号FR19990012094

  • 发明设计人 RICHARD ANDRE;

    申请日1999-09-22

  • 分类号C23C18/36;C02F9/04;

  • 国家 FR

  • 入库时间 2022-08-22 01:07:51

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