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    Process for heating an ATR
    2.
    发明授权
    Process for heating an ATR 有权

    公开(公告)号：US10106405B2

    公开(公告)日：2018-10-23

    申请号：US15117002

    申请日：2015-04-08

    申请人： Haldor Topsøe A/S

    发明人： Per Juul Dahl ,  Thomas Sandahl Christensen

    IPC分类号： C01B3/38 ,  C01B3/36 ,  F27D99/00

    摘要： The present invention relates to a process for heating an ATR or POX comprising the steps of heating a process stream by at least one heating means, admitting the heated process stream to an ATR or POX reactor through a main burner, and heating the ATR or POX reactor to or above autoignition temperature of the process stream via the heated process stream.

    PROCESS FOR CONVERSION OF NATURAL GAS TO HYDROCARBON PRODUCTS AND A PLANT FOR CARRYING OUT THE PROCESS
    4.
    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

    申请人： Haldor Topsøe A/S

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

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

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

    摘要： 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.

    摘要翻译： 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。