APPARATUS AND METHOD FOR CONDUCTING A FISCHER-TROPSCH SYNTHESIS REACTION
    72.
    发明授权
    APPARATUS AND METHOD FOR CONDUCTING A FISCHER-TROPSCH SYNTHESIS REACTION 有权
    用于引导费歇氏 - 合成反应合成反应的装置和方法

    公开(公告)号:EP2561044B1

    公开(公告)日:2018-02-21

    申请号:EP11718468.9

    申请日:2011-04-18

    申请人: GTL. F1 AG

    发明人: HANSEN, Roger

    IPC分类号: C10G2/00 C07C1/04 C10G5/06

    摘要: In order to avoid fouling (precipitation of solid matter on cold surfaces) in heat-exchangers down-stream of the gas outlet of a Fischer-Tropsch reactor, the reactor gas stream containing hydrocarbon products that are solid at lower temperatures is fed into a liquid wash tank. Condensation of heavy oil in the liquid wash tank is effected by feeding an evaporable light oil into the liquid wash tank. Heavy oil is recovered as a bottom product from the liquid wash tank while a gaseous product is taken out of the liquid wash tank as the top product. The light oil is obtained from the wash tank top product.

    HYDROCARBON GAS PROCESSING
    74.
    发明公开
    HYDROCARBON GAS PROCESSING 审中-公开
    BEHANDLUNG冯KOHLENWASSERSTOFFGAS

    公开(公告)号:EP3044528A1

    公开(公告)日:2016-07-20

    申请号:EP14843550.6

    申请日:2014-08-18

    IPC分类号: F25J3/02 F25J3/08

    摘要: A process and an apparatus are disclosed for a compact processing assembly to remove C5 and heavier hydrocarbon components from a hydrocarbon gas stream. The hydrocarbon gas stream is expanded to lower pressure and supplied to the processing assembly between an absorbing means and a mass transfer means. A distillation vapor stream is collected from the upper region of the absorbing means and cooled in a first heat and mass transfer means inside the processing assembly to partially condense it, forming a residual vapor stream and a condensed stream. The condensed stream is supplied to the absorbing means at its top feed point. A distillation liquid stream is collected from the lower region of the mass transfer means and directed into a second heat and mass transfer means inside the processing assembly to heat it and strip out its volatile components.

    摘要翻译: 公开了一种用于紧凑加工组件以从烃气流中除去C5和较重烃组分的方法和装置。 将烃气流膨胀到较低的压力,并在吸收装置和传质装置之间提供给处理组件。 蒸馏蒸气流从吸收装置的上部区域收集,并在处理组件内部的第一热传质装置中冷却,以使其部分冷凝,形成残余蒸气流和冷凝流。 冷凝的流在其顶部进料点处供应到吸收装置。 蒸馏液流从质量传递装置的下部区域收集并且被引导到处理组件内部的第二打浆和传质装置中,以加热它并剥离其挥发性组分。

    SYSTEM AND METHOD FOR SIDESTREAM MIXING
    75.
    发明公开
    SYSTEM AND METHOD FOR SIDESTREAM MIXING 有权
    系统和方法的电力MIX PAGE

    公开(公告)号:EP2969157A1

    公开(公告)日:2016-01-20

    申请号:EP14774106.0

    申请日:2014-03-11

    IPC分类号: B01F5/00 C10G31/00

    摘要: Systems and methods are provided for sidestream mixing. The system may include a first junction formed from a plurality of conduits. The plurality of conduits may include a first conduit fluidly coupled to a compressor, the first conduit forming a first conduit diameter and configured to flow therethrough a first process fluid stream of a plurality of process fluid streams. The plurality of conduits may also include a second conduit fluidly coupled to the first conduit and the compressor, and configured to flow therethrough a second process fluid stream of the plurality of process fluid streams. The first junction may be disposed a first distance at least three times the first conduit diameter upstream of the compressor, such that the first process fluid stream and the second process fluid stream are mixed and form a first combined process fluid stream prior to being fed into and pressurized in the compressor.

    OIL WELL PRODUCT TREATMENT
    78.
    发明公开
    OIL WELL PRODUCT TREATMENT 审中-公开
    石油钻探产品处理

    公开(公告)号:EP2782979A1

    公开(公告)日:2014-10-01

    申请号:EP12795594.6

    申请日:2012-11-15

    摘要: A plant for treating fluid products obtained from an oil well, to produce a hydrocarbon product, comprises a series of separators at progressively lower pressures, to which the fluid products are supplied in succession. A high pressure gas phase is obtained from the separator and is supplied to a flow restrictor so as to undergo cooling through the Joule Thomson effect, and then passed to a NGL separator to produce a natural gas liquid stream and a gaseous natural gas stream. The natural gas stream is then processed chemically, using a synthesis gas production unit, and a Fischer-Tropsch synthesis unit to produce a synthetic crude oil. The synthetic crude oil is supplied to one of the separators, and the natural gas liquid stream is supplied to another of the separators; the pressure in the one separator is greater than the pressure in the other separator.