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    • 2. 发明申请
    • Removal of ultra- fine particles from a Fischer Tropsch stream
    • 从费 - 托流中除去超细颗粒
    • US20100256433A1
    • 2010-10-07
    • US12601722
    • 2008-05-27
    • Cyril David KnottenbeltPatrick Otto TaylorVernon Jeremay AdamsVolan Richard Nicholson
    • Cyril David KnottenbeltPatrick Otto TaylorVernon Jeremay AdamsVolan Richard Nicholson
    • C07C7/144
    • B01D61/142C10G2/30C10G2300/4081C10G2300/706
    • This invention relates to a process for the removal of catalyst particles from a hydrocarbon stream (14) derived from the reaction of synthesis gas (12) with a particulate Fischer Tropsch catalyst in a Fischer Tropsch reactor (10). The process includes a primary separation step (16) which makes use of a filter, wherein the filter has a pore size which is 70% to 95 of the average size of the particles of the Fischer Tropsch catalyst, thereby forming a primary filtered hydrocarbon stream (18) containing fine catalyst particles. The benefit of this selection of filter pore size is that it mitigates fines build-up on the filter of the primary separator. The primary filtered hydrocarbon stream(18) is then passed to a secondary separation step in a cross-flow filtration unit (20) which removes fine catalyst particles from the primary filtered hydrocarbon stream to provide a retenate (24) containing the catalyst fines, and permeate (22) containing a hydrocarbon product.
    • 本发明涉及一种从费 - 托反应器(10)中的合成气(12)与微量费 - 托催化剂反应的烃流(14)中除去催化剂颗粒的方法。 该方法包括使用过滤器的初级分离步骤(16),其中过滤器的孔径为费 - 托催化剂颗粒的平均尺寸的70%至95,从而形成初级过滤的烃流 (18)含有细小的催化剂颗粒。 这种过滤器孔径选择的好处是它可以减轻主分离器过滤器上的细粉。 然后将主要过滤的烃物流(18)通入交叉流过滤单元(20)中的二次分离步骤,其从初级过滤的烃流中除去细小的催化剂颗粒,从而提供含有催化剂细粉末的电极(24),以及 含有烃产物的渗透物(22)。
    • 6. 发明授权
    • Removal of ultra-fine particles from a Fischer Tropsch stream
    • 从费 - 托流中除去超细颗粒
    • US08344199B2
    • 2013-01-01
    • US12601722
    • 2008-05-27
    • Cyril David KnottenbeltPatrick Otto TaylorVernon Jeremay AdamsVolan Richard Nicholson
    • Cyril David KnottenbeltPatrick Otto TaylorVernon Jeremay AdamsVolan Richard Nicholson
    • C10G45/14
    • B01D61/142C10G2/30C10G2300/4081C10G2300/706
    • This invention relates to a process for the removal of catalyst particles from a hydrocarbon stream (14) derived from the reaction of synthesis gas (12) with a particulate Fischer Tropsch catalyst in a Fischer Tropsch reactor (10). The process includes a primary separation step (16) which makes use of a filter, wherein the filter has a pore size which is 70% to 95 of the average size of the particles of the Fischer Tropsch catalyst, thereby forming a primary filtered hydrocarbon stream (18) containing fine catalyst particles. The benefit of this selection of filter pore size is that it mitigates fines build-up on the filter of the primary separator. The primary filtered hydrocarbon stream (18) is then passed to a secondary separation step in a cross-flow filtration unit (20) which removes fine catalyst particles from the primary filtered hydrocarbon stream to provide a retenate (24) containing the catalyst fines, and permeate (22) containing a hydrocarbon product.
    • 本发明涉及一种从费 - 托反应器(10)中的合成气(12)与微量费 - 托催化剂反应的烃流(14)中除去催化剂颗粒的方法。 该方法包括使用过滤器的初级分离步骤(16),其中过滤器的孔径为费 - 托催化剂颗粒的平均尺寸的70%至95,从而形成初级过滤的烃流 (18)含有细小的催化剂颗粒。 这种过滤器孔径选择的好处是它可以减轻主分离器过滤器上的细粉。 然后将主要过滤的烃物流(18)通入交叉流过滤单元(20)中的二次分离步骤,其从初级过滤的烃流中除去细小的催化剂颗粒,从而提供含有催化剂细粉末的电极(24),以及 含有烃产物的渗透物(22)。