Invention Grant
- Patent Title: Hydrocarbon synthesis reaction apparatus, start-up process thereof, and hydrocarbon synthesis reaction system
- Patent Title (中): 烃合成反应装置,其启动过程和烃合成反应系统
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Application No.: US14006998Application Date: 2012-03-13
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Publication No.: US09434657B2Publication Date: 2016-09-06
- Inventor: Yasuhiro Onishi , Kazuhiko Tasaka , Tomoyuki Mikuriya
- Applicant: Yasuhiro Onishi , Kazuhiko Tasaka , Tomoyuki Mikuriya
- Applicant Address: JP Tokyo JP Tokyo JP Tokyo JP Tokyo JP Tokyo JP Tokyo
- Assignee: Japan Oil, Gas and Metals National Corporation,INPEX CORPORATION,JX Nippon Oil & Energy Corporation,Japan Petroleum Exploration Co., Ltd,COSMO OIL CO., LTD.,NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD
- Current Assignee: Japan Oil, Gas and Metals National Corporation,INPEX CORPORATION,JX Nippon Oil & Energy Corporation,Japan Petroleum Exploration Co., Ltd,COSMO OIL CO., LTD.,NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD
- Current Assignee Address: JP Tokyo JP Tokyo JP Tokyo JP Tokyo JP Tokyo JP Tokyo
- Agency: Panitch Schwarze Belisario & Nadel LLP
- Priority: JP2011-076649 20110330
- International Application: PCT/JP2012/056399 WO 20120313
- International Announcement: WO2012/132876 WO 20121004
- Main IPC: C07C1/00
- IPC: C07C1/00 ; C07C1/02 ; C07C1/04 ; C10G2/00 ; B01J8/00 ; B01J8/18 ; B01J8/20 ; B01J8/22 ; B01J19/00 ; B01J19/24

Abstract:
The hydrocarbon synthesis reaction apparatus is provided with a synthesis gas supply line in which a synthesis gas is compressed and supplied by a first compressor, a reactor configured to accommodate a catalyst slurry, a gas-liquid separator configured to separate an unreacted synthesis gas and hydrocarbons discharged from the reactor into a gas and a liquid, a first recycle line in which the unreacted synthesis gas after separation into a gas and a liquid is compressed and recycled into the reactor by a second compressor, and a second recycle line configured to recycle a residual unreacted synthesis gas after separation into a gas and a liquid into the inlet side of the first compressor at the time of start-up operation when the synthesis gas is gradually increased in the amount to be introduced.
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