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    Process and system for producing synthesis gas
    21.
    发明授权
    Process and system for producing synthesis gas 有权

    公开(公告)号：US11591214B2

    公开(公告)日：2023-02-28

    申请号：US16753427

    申请日：2018-11-15

    Applicant: HALDOR TOPSØE A/S

    Inventor： Peter Mølgaard Mortensen ,  Kim Aasberg-Petersen

    IPC: C01B3/38 ,  B01J19/00 ,  B01J19/24

    Abstract: A process for producing synthesis gas, the process including the steps of: a) in a reforming reactor, reacting a hydrocarbon feed stream together with an oxidant gas stream, thereby producing a first synthesis gas stream; b) providing a heated CO2 rich gas stream to an adiabatic post converter including a second catalyst active for catalyzing steam methane reforming, methanation and reverse water gas shift reactions; and c) in the adiabatic reforming post converter, letting at least a part of the first synthesis gas stream and the heated CO2 rich gas stream undergo steam methane reforming, methanation and reverse water gas shift reactions to thereby provide a product gas stream, the product gas stream being a synthesis gas stream. Also, a system for producing synthesis gas.

    PROCESS FOR CONVERSION OF NATURAL GAS TO HYDROCARBON PRODUCTS AND A PLANT FOR CARRYING OUT THE PROCESS
    25.
    发明申请
    PROCESS FOR CONVERSION OF NATURAL GAS TO HYDROCARBON PRODUCTS AND A PLANT FOR CARRYING OUT THE PROCESS 有权
    将天然气转化为烃类产品的过程和实施过程的工厂

    公开(公告)号：US20150152019A1

    公开(公告)日：2015-06-04

    申请号：US14556342

    申请日：2014-12-01

    Applicant: Haldor Topsøe A/S

    Inventor： Kristian Lindell ,  Thomas Sandahl Christensen ,  Michael Hultqvist ,  Kim Aasberg-Petersen

    IPC: C07C1/04 ,  B01J8/02 ,  B01J8/08 ,  B01J8/06

    CPC classification number: C07C1/041 ,  B01J8/02 ,  B01J8/065 ,  B01J8/08 ,  B01J2208/027 ,  C01B3/38 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0261 ,  C01B2203/0475 ,  C01B2203/062

    Abstract: A process for the conversion of natural gas to hydrocarbon products comprises the steps of (a) mixing natural gas with a small amount of hydrogen, (b) purifying the mixture from (a) in a feed purification section to obtain purified natural gas, (c) mixing the purified natural gas from (b) with steam to obtain the desired steam-to-carbon (S/C) ratio, (d) mixing the natural gas/steam mixture from (c) with the tail gas from the downstream Fischer-Tropsch synthesis or a part thereof in a syngas section and converting the mixture into a synthesis gas, (e) cooling the synthesis gas from (d) and condensing out the process water from it, (f) leading the dry synthesis gas from (e) to a carbon dioxide removal section, where the CO2 is removed from the synthesis gas, and (g) sending the CO2-deprived synthesis gas to the downstream Fischer-Tropsch synthesis unit as a make-up gas. The carbon dioxide removed from the syngas in step (f) is either vented or kept for other use without any part of it being recycled.

    Abstract translation: 将天然气转化为烃产物的方法包括以下步骤：（a）将天然气与少量的氢气混合，（b）在进料纯化段中纯化（a）的混合物以获得纯化天然气，（ c）将来自（b）的纯化天然气与蒸汽混合以获得所需的蒸汽 - 碳（S / C）比，（d）将来自（c）的天然气/蒸汽混合物与来自下游的尾气混合 费 - 托合成或其一部分在合成气部分中并将混合物转化为合成气，（e）从（d）冷却合成气并从其中冷凝出工艺水，（f）使干燥的合成气从 （e）到二氧化碳去除部分，其中CO 2从合成气中除去，和（g）将CO 2去除的合成气作为补充气体送入下游费 - 托合成装置。 在步骤（f）中从合成气中除去的二氧化碳被排出或保存用于其他用途，而没有任何部分被再循环。

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