公开(公告)号：US09029429B2

公开(公告)日：2015-05-12

申请号：US14364367

申请日：2012-12-10

Applicant: Shell Oil Company

Inventor： Maarten Bracht ,  Martin Philipp Rohde

IPC: C07C27/06 ,  C07C1/04 ,  C01B3/36 ,  C01B3/38 ,  C10G2/00

CPC classification number: C07C1/04 ,  C01B3/36 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/062 ,  C01B2203/08 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/1671 ,  C01B2203/168 ,  C10G2/32 ,  C10K3/06 ,  Y02P20/52

Abstract: The present invention is directed to a process for the production of hydrocarbon product from two different hydrocarbonaceous feedstocks comprising the steps of preparing a feed syngas having a hydrogen/carbon monoxide [H2/CO] molar feed ratio suitable for Fischer-Tropsch synthesis, wherein the feed syngas is prepared by combining a first syngas having a H2/CO molar ratio below the molar feed ratio and a second syngas having a H2/CO molar ratio above the molar feed ratio; the first syngas is prepared from a liquid hydrocarbon comprising feedstock as the sole source of carbon in a first syngas manufacturing process comprising a non-catalytic partial oxidation step; the second syngas is prepared from a methane comprising feedstock as the sole source of carbon in a second syngas manufacturing process comprising a heat exchange reforming step and an auto-thermal reforming step; and the first and second syngas manufacturing processes are operated in parallel.

Abstract translation: 本发明涉及从两种不同的烃类原料生产烃产物的方法，包括以下步骤：制备具有适用于费 - 托合成的氢/一氧化碳[H 2 / CO]摩尔进料比的进料合成气，其中 通过将具有低于摩尔进料比的H 2 / CO摩尔比的第一合成气和H 2 / CO摩尔比高于摩尔进料比的第二合成气组合来制备进料合成气; 在包括非催化部分氧化步骤的第一合成气制备方法中，第一合成气由包含原料的液体烃制备为唯一的碳源， 在包括热交换重整步骤和自动热重整步骤的第二合成气制造方法中，第二合成气由包含原料的甲烷作为唯一的碳源制备， 并且第一和第二合成气制造工艺并行操作。

公开(公告)号：US20140350133A1

公开(公告)日：2014-11-27

申请号：US14364367

申请日：2012-12-10

Applicant: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. ,  SHELL OIL COMPANY

Inventor： Maarten Bracht ,  Martin Philipp Rohde

IPC: C07C1/04

CPC classification number: C07C1/04 ,  C01B3/36 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/062 ,  C01B2203/08 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/1671 ,  C01B2203/168 ,  C10G2/32 ,  C10K3/06 ,  Y02P20/52

Abstract: The present invention is directed to a process for the production of hydrocarbon product from two different hydrocarbonaceous feedstocks comprising the steps of preparing a feed syngas having a hydrogen/carbon monoxide [H2/CO] molar feed ratio suitable for Fischer-Tropsch synthesis, wherein the feed syngas is prepared by combining a first syngas having a H2/CO molar ratio below the molar feed ratio and a second syngas having a H2/CO molar ratio above the molar feed ratio; the first syngas is prepared from a liquid hydrocarbon comprising feedstock as the sole source of carbon in a first syngas manufacturing process comprising a non-catalytic partial oxidation step; the second syngas is prepared from a methane comprising feedstock as the sole source of carbon in a second syngas manufacturing process comprising a heat exchange reforming step and an auto-thermal reforming step; and the first and second syngas manufacturing processes are operated in parallel.

Abstract translation: 本发明涉及从两种不同的烃类原料生产烃产物的方法，包括以下步骤：制备具有适用于费 - 托合成的氢/一氧化碳[H 2 / CO]摩尔进料比的进料合成气，其中 通过将具有低于摩尔进料比的H 2 / CO摩尔比的第一合成气和H 2 / CO摩尔比高于摩尔进料比的第二合成气组合来制备进料合成气; 在包括非催化部分氧化步骤的第一合成气制备方法中，第一合成气由包含原料的液体烃制备为唯一的碳源， 在包括热交换重整步骤和自动热重整步骤的第二合成气制造方法中，第二合成气由包含原料的甲烷作为唯一的碳源制备， 并且第一和第二合成气制造工艺并行操作。