Process for sugar beet juice clarification
    2.
    发明授权
    Process for sugar beet juice clarification 失效
    甜菜汁澄清方法

    公开(公告)号:US6051075A

    公开(公告)日:2000-04-18

    申请号:US751044

    申请日:1996-11-15

    CPC classification number: C13B20/16 C13B20/005

    Abstract: Diffusion juice of a sugar plant is heated under stable sucrose conditions, notably alkaline pH, and held above 70.degree. C. for sufficient duration to effect significant agglomeration. The agglomerated particulates are removed by phase separation procedures, leaving a clarified juice containing a very low, typically 0.1-0.5 volume percent, solids load.

    Abstract translation: 糖厂的扩散汁在稳定的蔗糖条件下,特别是碱性pH下加热,并保持在70℃以上足够的持续时间以显着凝聚。 通过相分离程序除去附聚的颗粒,留下含有非常低的,通常为0.1-0.5体积%的固体负载的澄清的果汁。

    Regenerant reuse
    3.
    发明申请
    Regenerant reuse 失效
    再生再利用

    公开(公告)号:US20050051491A1

    公开(公告)日:2005-03-10

    申请号:US10841936

    申请日:2004-05-07

    Abstract: The invention provides a method for recycling the waste regenerant from softeners. The method includes passing a high concentration of monovalent ionic halide salt through a resin bed. The high monovalent cation concentration causes the divalent cations on the resin to be exchanged with the monovalent cations by osmotic forces. The regenerant is then treated to precipitate the divalent cations and replace them with monovalent cations.

    Abstract translation: 本发明提供了一种从软化剂再循环废旧再生剂的方法。 该方法包括使高浓度的一价离子卤化物盐通过树脂床。 高一价阳离子浓度导致树脂上的二价阳离子通过渗透力与一价阳离子交换。 然后处理再生剂以沉淀二价阳离子并用一价阳离子代替它们。

    Ion exchange process
    4.
    发明授权
    Ion exchange process 有权
    离子交换过程

    公开(公告)号:US07846338B2

    公开(公告)日:2010-12-07

    申请号:US11986616

    申请日:2007-11-21

    CPC classification number: C02F1/42 B01J39/05 B01J39/07 B01J49/53 C02F2001/425

    Abstract: A method is described that relates to reducing amounts of regenerant waste or increasing the concentration of regenerant waste from ion exchange processes. A method is described that may allow a batch ion exchange process to compete on these factors with continuous or simulated continuous ion exchange processes, and/or to improve the efficiency in operation continuous or simulated continuous ion exchange processes. A specific application addressed is the treatment of water in the Coal Bed Methane Process.

    Abstract translation: 描述了一种减少再生废物量或从离子交换过程增加再生废物浓度的方法。 描述了可以允许批次离子交换过程利用连续或模拟的连续离子交换过程在这些因素上竞争和/或提高连续或模拟连续离子交换过程的操作效率的方法。 一个具体的应用是煤层气过程中的水处理。

    Ion exchange process
    7.
    发明申请
    Ion exchange process 有权
    离子交换过程

    公开(公告)号:US20080156732A1

    公开(公告)日:2008-07-03

    申请号:US11986616

    申请日:2007-11-21

    CPC classification number: C02F1/42 B01J39/05 B01J39/07 B01J49/53 C02F2001/425

    Abstract: A method is described that relates to reducing amounts of regenerant waste or increasing the concentration of regenerant waste from ion exchange processes. A method is described that may allow a batch ion exchange process to compete on these factors with continuous or simulated continuous ion exchange processes, and/or to improve the efficiency in operation continuous or simulated continuous ion exchange processes. A specific application addressed is the treatment of water in the Coal Bed Methane Process.

    Abstract translation: 描述了一种减少再生废物量或从离子交换过程增加再生废物浓度的方法。 描述了可以允许批次离子交换过程利用连续或模拟的连续离子交换过程在这些因素上竞争和/或提高连续或模拟连续离子交换过程的操作效率的方法。 一个具体的应用是煤层气过程中的水处理。

    Regenerant reuse
    8.
    发明授权
    Regenerant reuse 失效
    再生再利用

    公开(公告)号:US07157005B2

    公开(公告)日:2007-01-02

    申请号:US10841936

    申请日:2004-05-07

    Abstract: The invention provides a method for recycling the waste regenerant from softeners. The method includes passing a high concentration of monovalent ionic halide salt through a resin bed. The high monovalent cation concentration causes the divalent cations on the resin to be exchanged with the monovalent cations by osmotic forces. The regenerant is then treated to precipitate the divalent cations and replace them with monovalent cations.

    Abstract translation: 本发明提供了一种从软化剂再循环废旧再生剂的方法。 该方法包括使高浓度的一价离子卤化物盐通过树脂床。 高一价阳离子浓度导致树脂上的二价阳离子通过渗透力与一价阳离子交换。 然后处理再生剂以沉淀二价阳离子并用一价阳离子代替它们。

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