Production of sodium bicarbonate by reversion of NaHC03-containing double salt
    1.
    发明公开
    Production of sodium bicarbonate by reversion of NaHC03-containing double salt 失效
    一种用于通过的NaHCO 3的含有复盐的转化生产碳酸氢钠处理。

    公开(公告)号:EP0135323A2

    公开(公告)日:1985-03-27

    申请号:EP84305201.0

    申请日:1984-07-31

    申请人: FMC Corporation

    IPC分类号: C01D7/14

    CPC分类号: C01D7/10

    摘要: Sodium bicarbonate is produced by introducing solid sodium sesquicarbonate and/or Wegscheider's salt into a reversion slurry, saturated with respect to bicarbonate and containing at least 10 wt. % solids, to effect rapid and complete conversion of the feed solids to crystalline sodium bicarbonate which is recovered from the slurry. Carbon dioxide is introduced into the reversion liquor to maintain its composition at a relatively constant value, preferably in a region of the Na 2 C0 3 -NaHC0 3- H 2 0 phase diagram that minimizes the equilibrium partial pressure of CO 2 vapor above such liquor.

    摘要翻译: 碳酸氢钠通过引入固体倍半碳酸钠和/或Wegscheider的盐成反转浆液,相对于饱和碳酸氢盐和含有至少10%(重量)生产的。固体,以实现进料固体的快速和完全转化为结晶碳酸氢钠所有这些是 从浆料中回收。 二氧化碳被引入到返液维持其组合物在相对恒定的数值,最好是在碳酸钠 - 碳酸氢钠-H2O相图的区域做最小化CO2蒸气的上述寻求酒的平衡分压。

    Production of sodium bicarbonate by reversion of NaHC03-containing double salt
    2.
    发明公开
    Production of sodium bicarbonate by reversion of NaHC03-containing double salt 失效
    通过还原含有NAHC03的双盐生产二硼酸钠

    公开(公告)号:EP0135323A3

    公开(公告)日:1986-06-04

    申请号:EP84305201

    申请日:1984-07-31

    申请人: FMC Corporation

    IPC分类号: C01D07/14

    CPC分类号: C01D7/10

    摘要: Sodium bicarbonate is produced by introducing solid sodium sesquicarbonate and/or Wegscheider's salt into a reversion slurry, saturated with respect to bicarbonate and containing at least 10 wt. % solids, to effect rapid and complete conversion of the feed solids to crystalline sodium bicarbonate which is recovered from the slurry. Carbon dioxide is introduced into the reversion liquor to maintain its composition at a relatively constant value, preferably in a region of the Na 2 C0 3 -NaHC0 3- H 2 0 phase diagram that minimizes the equilibrium partial pressure of CO 2 vapor above such liquor.