首页> 外国专利> Method for processing drinking water, brine or filling water for bathing by removing halide ions such as iodide, bromide or chlorine ion, comprises oxidative halogenation of an organic compound added to water at an anode

Method for processing drinking water, brine or filling water for bathing by removing halide ions such as iodide, bromide or chlorine ion, comprises oxidative halogenation of an organic compound added to water at an anode

机译:通过去除卤离子如碘离子,溴离子或氯离子来处理饮用水,盐水或填充沐浴水的方法,该方法包括在阳极处添加至水中的有机化合物的氧化卤化

摘要

The method comprises oxidative halogenating an organic compound added to water at an anode (A1, A2, A3), separating the halogenated organic compound from the water by a separation process, converting XO 3-ions remaining in the water to the corresponding halide ion at a cathode (K1, K2, K3) connected with the anode over a power source (S) and repeating the process steps up to a predetermined concentration limit value for X -or XO 3-ions. A grafite anode, diamond coated anode or platinum anode is used as the anode. The water to be purified is subjected with a catalyst (2). The method comprises oxidative halogenating an organic compound added to water at an anode (A1, A2, A3), separating the halogenated organic compound from the water by a separation process, converting XO 3-ions remaining in the water to the corresponding halide ion at a cathode (K1, K2, K3) connected with the anode over a power source (S) and repeating the process steps up to a predetermined concentration limit value for X -or XO 3-ions. A graphite anode, diamond coated anode or platinum anode is used as the anode. The water to be purified is subjected with a catalyst (2) after the conversion and optionally before the oxidative halogenation or during the separation. A reducing agent is added to the water to be purified after the conversion and halogentaion. The pH of water is adjusted to 9.5-10.5. The separation process is filtration and/or stripping process. An active coal filter or anthracite filter is used for separating the halogenated organic compound. The concentration limit value for XO 3-ion is = 10 mu g/l. The water is circulated for repeating the process and the process is carried out as batch or continuous process. An independent claim is included for a device for processing drinking water, brine or filling water for bathing.
机译:该方法包括在阳极(A1,A2,A3)上氧化卤化添加到水中的有机化合物,通过分离工艺从水中分离卤化有机化合物,将残留在水中的XO 3->离子转化为相应的卤离子。在电源(S)上与阳极连接的阴极(K1,K2,K3)上,重复上述步骤,直至达到X-或XO 3--离子的预定浓度极限值。嫁接阳极,金刚石涂覆阳极或铂阳极用作阳极。待净化的水用催化剂(2)处理。该方法包括在阳极(A1,A2,A3)上氧化卤化添加到水中的有机化合物,通过分离工艺从水中分离卤化有机化合物,将残留在水中的XO 3->离子转化为相应的卤离子。在电源(S)上与阳极连接的阴极(K1,K2,K3)上,重复上述步骤,直至达到X-或XO 3--离子的预定浓度极限值。石墨阳极,金刚石涂覆的阳极或铂阳极用作阳极。在转化之后并且任选在氧化卤化之前或在分离期间,将要纯化的水用催化剂(2)处理。在转化和卤化之后,将还原剂添加到待纯化的水中。将水的pH调节至9.5-10.5。分离过程是过滤和/或汽提过程。活性煤过滤器或无烟煤过滤器用于分离卤代有机化合物。 XO 3->离子的浓度极限值为= 10μg / l。使水循环以重复该过程,并且该过程以间歇或连续过程进行。包括用于处理饮用水,盐水或沐浴水的设备的独立权利要求。

著录项

  • 公开/公告号DE102008041164A1

    专利类型

  • 公开/公告日2010-02-25

    原文格式PDF

  • 申请/专利权人 WERTHMANN CHRISTINE;

    申请/专利号DE20081041164

  • 发明设计人 WERTHMANN CHRISTINE;

    申请日2008-08-11

  • 分类号C02F9/06;C02F1/461;C02F1/58;C02F1/70;

  • 国家 DE

  • 入库时间 2022-08-21 18:28:49

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