公开(公告)号：EP3164206A1

公开(公告)日：2017-05-10

申请号：EP15736021.5

申请日：2015-07-01

申请人： Compact GTL plc

发明人： BONNER, Christopher William ,  DANNATT, Benjamin

IPC分类号： B01J19/00 ,  B01J19/24

CPC分类号： B01J15/005 ,  B01J19/0013 ,  B01J19/0093 ,  B01J19/249 ,  B01J2219/00058 ,  B01J2219/002 ,  B01J2219/00225 ,  B01J2219/00783 ,  B01J2219/00786 ,  B01J2219/00822 ,  B01J2219/00835 ,  B01J2219/0086 ,  B01J2219/00873 ,  B01J2219/00961 ,  B01J2219/0097 ,  B01J2219/00986 ,  B01J2219/2453 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2465 ,  B01J2219/2479 ,  B01J2219/2481 ,  B01J2219/2486 ,  B01J2219/2497 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0811 ,  C10G2/34

摘要： A catalytic reactor is provided comprising a plurality of first flow channels including a catalyst for a first reaction; a plurality of second flow channels arranged alternately with the first flow channels; adjacent first and second flow channels being separated by a divider plate (13a, 13b), and a distributed temperature sensor such as an optical fibre cable (19). The distributed temperature sensor may be located within the divider plate, or within one or 10 more of the flow channels.

摘要翻译： 一种催化反应器，包括：多个第一流动通道，包括用于第一反应的催化剂; 多个第二流动通道，与第一流动通道交替排列; 相邻的第一和第二流动通道由分隔板13分开; 以及分布式温度传感器19，该分布式温度传感器19设置在划分板和/或在一个或多个第一流动通道和/或一个或多个第二流动通道内。 分布式温度传感器可以是光缆，并且可以沿着通过分隔板的曲折路径，或者可以设置在第一或第二通道中的一个或多个内。 第一流动通道可以包括费 - 托催化剂，并且第二流动通道可以携带传热流体。 还公开了一种用于进行费 - 托合成的设备，其包含催化反应器。

公开(公告)号：EP2242571A2

公开(公告)日：2010-10-27

申请号：EP09710532.4

申请日：2009-02-10

申请人： Compact GTL PLC

发明人： BOWE, Michael Joseph ,  LEE-TUFFNELL, Clive Derek ,  PEAT, Robert

IPC分类号： B01J19/24 ,  C10G2/00

CPC分类号： B01J19/249 ,  B01J2219/0004 ,  B01J2219/00164 ,  B01J2219/00265 ,  B01J2219/2453 ,  B01J2219/2459 ,  B01J2219/2465 ,  B01J2219/247 ,  B01J2219/2479 ,  B01J2219/2497 ,  B01J2219/2498 ,  C10G2/31

摘要： A catalytic reaction module (10) for performing an endothermic reaction such as steam methane reforming, includes separate reactor blocks (12), each reactor block defining a multiplicity of first and second flow channels (15, 16) arranged alternately within the block to ensure thermal contact between the first and second flow channels. The reactor blocks (12a, 12b) may be arranged and connected for series flow of a combustible gas mixture in the first flow channels (15) and also of a gas mixture to undergo the endothermic reaction in the second flow channels (16). This enables the combustion process to be carried out in stages, with the option of cooling the combustion gases between stages, and introducing additional fuel and additional air.