Catalytic process
Abstract
Fischer-Tropsch synthesis is performed using a compact catalytic reactor unit (10) defining channels in which is a gas-permeable catalyst structure (16), the channels extending between headers (18). The synthesis occurs in at least two stages, as the reactor unit provides at least two successive channels (14, 14a) for the Fischer-Tropsch synthesis connected by a header, the gas flow velocity through the first channel being sufficiently high that no more than 65% of the carbon monoxide undergoes conversion. The gases are cooled (25) in the header between the two stages, so as to condense water vapour, and then pass through the second channel at a sufficiently high gas flow velocity that no more than 65% of the remaining carbon monoxide undergoes conversion. This lowers the partial pressure of water vapour and so suppresses oxidation of the catalyst.
Term
Term ended
Projected expiry passed 27 November 2023, 2.8 years ago.
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69 members in 20 offices
Priority claims2
| Document | Office | Kind | Date |
|---|---|---|---|
| 0205443 | United Kingdom | W | |
| 0314790 | United Kingdom | A |
Members69
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| GB0204677D0 | United Kingdom | D0 | |
| WO03048034A1 | World Intellectual Property Organization (WIPO) | A1 | |
| WO03048035A1 | World Intellectual Property Organization (WIPO) | A1 | |
| TW200300703A | Taiwan Province of China | A | |
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| TW200301160A | Taiwan Province of China | A | |
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| NO20033454D0 | Norway | D0 | |
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| BR0206966A | Brazil | A | |
| TW590798B | Taiwan Province of China | B | |
| CA2505614A1 | Canada | A1 | |
| WO2004050799A1 | World Intellectual Property Organization (WIPO) | A1 | |
| TW592832B | Taiwan Province of China | B | |
| AU2003285558A1 | Australia | A1 | |
| GB0412152D0 | United Kingdom | D0 | |
| EP1451098A1 | European Patent Office (EPO) | A1 | |
| NO20042280L | Norway | L | |
| GB2399516A | United Kingdom | A | |
| TW200420342A | Taiwan Province of China | A | |
| BR0214693A | Brazil | A | |
| US2005054737A1 | United States of America | A1 | |
| GB2399516B | United Kingdom | B | |
| AP2005003315A0 | African Regional Intellectual Property Organization (ARIPO) | A0 | |
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| US2005171217A1 | United States of America | A1 | |
| MXPA05005870A | Mexico | A | |
| KR20050085124A | Republic of Korea | A | |
| EP1567616A1 | European Patent Office (EPO) | A1 | |
| NO20053244L | Norway | L | |
| BR0316828A | Brazil | A | |
| CN1720316A | China | A | |
| RU2005120773A | Russian Federation | A | |
| US2006041029A1 | United States of America | A1 | |
| JP2006508234A | Japan | A | |
| US7087651B2 | United States of America | B2 | |
| EP1567616B1 | European Patent Office (EPO) | B1 | |
| AT337385T | Austria | T | |
| ATE337385T1This record | Austria | T1 | |
| DE60307885D1 | Germany | D1 | |
| DK1567616T3 | Denmark | T3 | |
| OA12965A | African Intellectual Property Organization (OAPI) | A | |
| DE60307885T2 | Germany | T2 | |
| AU2002365663B2 | Australia | B2 | |
| MY129719A | Malaysia | A | |
| US7217741B2 | United States of America | B2 | |
| TWI281877B | Taiwan Province of China | B | |
| MY131482A | Malaysia | A | |
| RU2310677C2 | Russian Federation | C2 | |
| MY135490A | Malaysia | A | |
| US2008194712A1 | United States of America | A1 | |
| AU2003285558B2 | Australia | B2 | |
| CN100548942C | China | C | |
| JP4446388B2 | Japan | B2 | |
| EP1567616B2 | European Patent Office (EPO) | B2 | |
| DE60307885T3 | Germany | T3 | |
| KR101053040B1 | Republic of Korea | B1 | |
| US8021633B2 | United States of America | B2 | |
| US2012058028A1 | United States of America | A1 | |
| CA2505614C | Canada | C | |
| BR0216052B1 | Brazil | B1 | |
| BRPI0216052B1 | Brazil | B1 | |
| BR0316828B1 | Brazil | B1 | |
| NO333822B1 | Norway | B1 | |
| US8753589B2 | United States of America | B2 | |
| US2014234168A1 | United States of America | A1 | |
| DK1567616T4 | Denmark | T4 |
Numbers
- Application
- 3778556
Titles2
- English
- CATALYTIC REACTOR AND PROCESS
- German
- KATALYTISCHER REAKTOR UND VERFAHREN
Classification
- CPC, 9
- C10G2/341
- B01J19/24
- B01J19/249
- B01J19/2495
- B01J2219/2465
- B01J2219/247
- B01J2219/2477
- C10G2/00
- C07C1/04
- IPC, 2
- B01J19 24
- C10G2 00