SYSTEMS AND METHODS FOR SEPARATING HYDROCARBONS FROM WATER
    61.
    发明公开
    SYSTEMS AND METHODS FOR SEPARATING HYDROCARBONS FROM WATER 有权
    系统VERFAHREN ZUM TRENNEN VON KOHLENWASSERSTOFFEN VON WASSER

    公开(公告)号:EP2176517A4

    公开(公告)日:2012-08-15

    申请号:EP08781597

    申请日:2008-07-10

    申请人: MI LLC

    摘要: A system for separating hydrocarbons from water, the system including an inlet for receiving a fluid, the fluid including a water phase and a hydrocarbon phase, and a separation tank having a first partition and a second partition, wherein the first partition is configured to receive the fluid from the inlet. Furthermore, the system includes a first outlet configured to receive the water phase from the first partition, a second outlet configured to receive the hydrocarbon phase from the second partition, and a support structure configured to receive the water phase from the first outlet and the hydrocarbon phase from the second outlet. Also, a method of separating a fluid into a water phase and a hydrocarbon phase, the method including injecting the fluid containing the water phase and the hydrocarbon phase into a separation tank. The method further includes separating the water phase from the hydrocarbon phase, wherein the separating includes transmitting the fluid through a plurality of baffles, collecting the water phase, and collecting the hydrocarbon phase.

    摘要翻译: 一种用于从水中分离碳氢化合物的系统,所述系统包括用于接收流体的入口,所述流体包括水相和烃相,以及具有第一分隔和第二分隔的分离罐,其中所述第一分隔件构造成接收 来自入口的流体。 此外,该系统包括构造成从第一分隔件接收水相的第一出口,被配置为从第二分隔件接收烃相的第二出口和构造成从第一出口和烃接收水相的支撑结构 相位从第二个出口。 另外,将流体分离成水相和烃相的方法,该方法包括将含有水相和烃相的流体注入分离槽。 该方法还包括从烃相中分离水相,其中分离包括通过多个挡板传输流体,收集水相和收集烃相。

    FLÜSSIGKEITSFILTER UND FILTERSYSTEM
    65.
    发明公开
    FLÜSSIGKEITSFILTER UND FILTERSYSTEM 审中-公开
    液体过滤器和过滤系统

    公开(公告)号:EP2379197A1

    公开(公告)日:2011-10-26

    申请号:EP09768026.8

    申请日:2009-12-04

    申请人: Robert Bosch GmbH

    IPC分类号: B01D39/20 B01D63/06 B01D71/02

    摘要: The invention relates to a fluid filter, in particular for filtering water, comprising a plurality of inlet channels (2), a plurality of outlet channels (3) and filter walls (4) separating the inlet channels (2) from the outlet channels (3), wherein the inlet channels (2) are arranged parallel to the outlet channels (3), wherein the filter walls (4) have a plurality of pores through which the inlet channels (2) are connected to the outlet channels (3), wherein a cross-section area of all inlet channels (2) is larger than a cross-section area of all outlet channels (3), and a value of diameters of the pores of the filter walls (4) calculated by means of quicksilver porosimetry is a median d
    50 , lying between 0.01 to 0.5 μm, preferably between 0.03 to 0.2 μm, further preferably between 0.05 to 1.5 μm and most preferably equaling between 0.05 and 0.1 μm.