Continuous ion exchange process and apparatus
    1.
    发明授权
    Continuous ion exchange process and apparatus 失效
    连续离子交换过程和设备

    公开(公告)号:US3879287A

    公开(公告)日:1975-04-22

    申请号:US30258972

    申请日:1972-10-31

    Inventor: PORTER ROBERT R

    CPC classification number: B01J47/11

    Abstract: A solution to be treated by ion exchange is continuously introduced into the bottom of the first of a series of ion exchange vessels containing respective adsorption columns of an appropriate, particulate, ion exchange material, and is passed successively through the subsequent ion exchange vessels of the series, so that such solution flows continuously upwardly through each adsorption column, thence to the bottom of the next column, and is finally discharged from the last column of the series as fully treated solution. The loaded adsorption column is removed from the first vessel of the series, usually to eluting means for regeneration, and the other adsorption columns are transferred from vessel to vessel up the line, the adsorption column of the last vessel of the series being replaced by substantially unloaded ion exchange material, usually eluted material from the adsorption column of the first vessel of the series. The cycle is repeated continuously throughout any given period of operation of the method. The eluting means preferably comprises one or more conventional fixed bed ion exchange vessels, with or without a holding vessel in advance thereof, and there is preferably an excess of ion exchange material at this stage so that, in conjunction with such vessel or vessels, there is a metering of ion exchange material circulating batchwise through the system countercurrent to the solution.

    Abstract translation: 通过离子交换处理的溶液被连续地引入到包含合适的颗粒状离子交换材料的各个吸附塔的一系列离子交换容器的第一个的底部,并连续地通过随后的离子交换容器 使得这样的溶液连续向上流过每个吸附柱,然后从下一个塔的底部流出,最后作为完全处理的溶液从串联的最后一个塔排出。 将负载的吸附塔从该系列的第一容器中取出,通常用于洗脱用于再生的装置,并且其它吸附塔从容器中转移到容器上,该系列的最后一个容器的吸附塔被基本上 未加载的离子交换材料,通常是从该系列的第一容器的吸附塔洗脱的物质。 在该方法的任何给定的操作周期内连续重复循环。 洗脱装置优选地包括一个或多个常规的固定床离子交换容器,其中有或没有预先存放容器,并且在该阶段优选地存在过量的离子交换材料,使得与这样的容器或容器结合在一起 是通过与溶液逆流的系统分批循环的离子交换材料的计量。

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