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Ion exchange resin, condensate desalination tower and condensate purification device using this resin

机译:离子交换树脂,冷凝水脱盐塔和使用该树脂的冷凝水净化装置

摘要

PURPOSE:To reduce the size of the title purifier by controlling the content of divinylbenzene to have a determined value and adopting ion exchange resin having a large ion exchange capacity and exchange rate. CONSTITUTION:Since the cross-linking degree of ion exchange resins 6a, 6b is controlled by the adding amount of divinyl benzene, the ion exchange capacity per unit volume can be raised by increasing the cross-linking degree, and conversely, the difusion velocity and ion exchange rate can be raised by decreasing the cross-linking degree. The containing amount of divinyl benzene is set at ca. 8 weight % in the surface layer 7 and ca. 3 to 7 weight % in the middle part 8. Then, the condensate from a functional hollow yarn film filter 5 is supplied to a desalting tower 2 and impurity ions unremoved are exchanged by the ion exchange resins 6a, 6b. As the surface layer 7 has high cross-linking degree and large exchange capacity and dirt ions reaching the middle part 8 with low cross-linking degree are exchanged at a high defusion rate. Resultantly, the exchange rate of the resin 6a, 6b and exchange capacity as a whole increase.
机译:目的:通过控制二乙烯基苯的含量使其具有确定的值,并采用具有较大离子交换容量和交换速率的离子交换树脂,以减小标题纯化器的尺寸。组成:由于离子交换树脂6a,6b的交联度受二乙烯基苯的添加量控制,因此可以通过提高交联度来提高每单位体积的离子交换容量,反之,可以提高扩散速度和通过降低交联度可以提高离子交换速率。二乙烯基苯的含量设定为约1。在表面层7中约8重量%,并且中间部分8中的重量百分比为3至7重量%。然后,将来自功能性中空丝膜过滤器5的冷凝物供应至脱盐塔2,并且通过离子交换树脂6a,6b交换未除去的杂质离子。由于表面层7具有高的交联度和大的交换能力,并且以高的解吸率交换到达具有低的交联度的中间部分8的污垢离子。结果,树脂6a,6b的交换率和交换容量整体上增加。

著录项

  • 公开/公告号JP2892811B2

    专利类型

  • 公开/公告日1999-05-17

    原文格式PDF

  • 申请/专利权人 TOSHIBA KK;

    申请/专利号JP19900273373

  • 发明设计人 INAMI ICHIRO;

    申请日1990-10-15

  • 分类号G21F9/12;G21C19/307;G21F9/06;

  • 国家 JP

  • 入库时间 2022-08-22 02:31:32

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