Device that comprises recycling to a separator a liquid effluent that is obtained from an absorber and is mixed with a feedstock
    1.
    发明授权
    Device that comprises recycling to a separator a liquid effluent that is obtained from an absorber and is mixed with a feedstock 有权
    包括将从吸收器获得并与原料混合的液体流出物再循环到分离器的装置

    公开(公告)号:US07132044B2

    公开(公告)日:2006-11-07

    申请号:US10071213

    申请日:2002-02-11

    IPC分类号: C10G5/00 B01D3/00

    CPC分类号: C10G5/06 C10G5/04 C10G70/041

    摘要: A device comprising at least one absorber, at least one cold separator from which is extracted a gaseous phase that feeds the absorber, at least one recycling to said cold separator of at least a portion of liquid effluent that is obtained from the absorber and which is mixed with the feedstock, at least one heat exchanger for cooling the mixture prior to the recycling, at least one conduit for recovering a light hydrocarbon-enriched liquid fraction obtained from the cold separator and at least one conduit for evacuating gases from the absorber, said device being useable for the treatment of a hydrogen-rich gas or for the recovery of a hydrocarbon-enriched liquid.

    摘要翻译: 一种装置,包括至少一个吸收器,至少一个冷分离器,从其中提取进料吸收器的气相,至少一个回收至所述冷分离器的至少一部分从吸收器获得的液体流出物, 与原料混合的至少一个热交换器,用于在再循环之前冷却混合物的至少一个热交换器,用于回收从冷分离器获得的轻烃富集的液体馏分的至少一个管道和用于从吸收器排出气体的至少一个管道, 装置可用于处理富氢气体或用于回收富含烃的液体。

    Apparatus for processing a product from catalytic reforming
    2.
    发明授权
    Apparatus for processing a product from catalytic reforming 失效
    用于处理来自催化重整的产物的装置

    公开(公告)号:US5597404A

    公开(公告)日:1997-01-28

    申请号:US466686

    申请日:1995-06-06

    CPC分类号: C10G35/04

    摘要: Apparatus for conducting an improved method of processing a catalytic reformate with an improved production of hydrogen. The apparatus comprises units for conducting a separation stage, absorption at 20.degree. to 60.degree. C. and at a pressure of at least 10 bars, purification of hydrogen over adsorbent beds and recycling of the residual gas obtained at purification.

    摘要翻译: 用于进行改进的氢气生产处理催化重整油的改进方法的装置。 该设备包括用于进行分离阶段的单元,在20℃至60℃的吸收和至少10巴的压力下,在吸附剂床上净化氢气并再循环净化时获得的残余气体。