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    • 2. 发明授权
    • Two-stage separation process
    • 两阶段分离过程
    • US06190564B1
    • 2001-02-20
    • US09164557
    • 1998-10-01
    • Richard W. LehmannRussell G. Forbess
    • Richard W. LehmannRussell G. Forbess
    • C02F174
    • C02F11/086C02F1/74
    • A process is disclosed for producing an oxidized liquid effluent containing minimal dissolved gases therein, from a subcritical wet oxidation treatment system. The oxidation mixture exiting from the treatment system is separated into a first oxidized liquid effluent and a first gaseous phase as the mixture a first separator vessel operated at a relatively low superatmospheric pressure. Sufficient pressure is maintained in the first gaseous phase to provide the motive force for transport to further treatment or discharge. The first oxidized liquid effluent flows to a second separator vessel operated at essentially atmospheric pressure, where remaining dissolved gases separate from the first oxidized liquid effluent. The second gaseous phase is discharged and the second oxidized liquid effluent is suitable for storage or further treatment. Provision for adjusting the pH of the oxidized liquid effluent during the separation process is also disclosed.
    • 公开了一种从亚临界湿式氧化处理系统生产含有最少溶解气体的氧化液体流出物的方法。 从处理系统排出的氧化混合物被分离为第一氧化液体流出物和作为混合物的第一气相,第一分离器容器在相对低的超大气压力下操作。 在第一气相中保持足够的压力以提供用于运输以进一步处理或排放的动力。 第一氧化液体流出物流到在基本上大气压下操作的第二分离容器,其中剩余的溶解气体与第一氧化液体流出物分离。 排出第二气相,第二氧化液体流出物适于贮存或进一步处理。 还公开了在分离过程中调节氧化液体流出物的pH的规定。