Hydrocarbon synthesis reaction apparatus

Patent metadata

Field	Value
Publication number	US-9688918-B2
Application number	US-201414778636-A
Country	US
Kind code	B2
Filing date	Mar 19, 2014
Priority date	Mar 26, 2013
Publication date	Jun 27, 2017
Grant date	Jun 27, 2017

Abstract

The hydrocarbon synthesis reaction apparatus according to the present invention includes a reaction vessel that brings a synthesis gas having carbon monoxide gas and hydrogen gas as main components into contact with a slurry having a solid catalyst suspended in a liquid hydrocarbon compound to synthesize a liquid hydrocarbon compound using a Fischer-Tropsch reaction; a filter that is provided within the reaction vessel and is configured to separate the liquid hydrocarbon compound from the catalyst; and a powdered catalyst particles-discharging device configured to discharge powdered catalyst particles in the solid catalyst in the slurry to the outside of the reaction vessel.

First claim

The invention claimed is:

1. A hydrocarbon synthesis reaction apparatus, comprising:
a reaction vessel configured to bring a synthesis gas having carbon monoxide gas and hydrogen gas as main components into contact with a slurry having a solid catalyst suspended in a liquid hydrocarbon compound to synthesize a liquid hydrocarbon compound using a Fischer-Tropsch reaction;
a filter that is installed inside the reaction vessel and is configured to separate the liquid hydrocarbon compound from the catalyst; and
a powdered catalyst particles-discharging device configured to discharge powdered catalyst particles in the solid catalyst in the slurry to the outside of the reaction vessel, wherein
the powdered catalyst particles-discharging device includes:
a first classifier configured to separate the powdered catalyst particles from the solid catalyst in the slurry, using a settling velocity difference of the particles in a liquid;
an outflow passage configured that the powdered catalyst particles separated in the first classifier flows to the outside of the first classifier together with the liquid hydrocarbon compound therethrough; and
a powdered catalyst particles separator that is provided in the outflow passage and is configured to trap the powdered catalyst particles.

2. The hydrocarbon synthesis reaction apparatus according to claim 1 , further comprising:
an outflow velocity adjuster configured to adjust the outflow velocity of the liquid hydrocarbon compound, including the powdered catalyst particles, in the outflow passage, wherein an upper portion of the first classifier is formed in the shape of a cone, and
wherein a plurality of slurry extraction nozzles arrayed in a height direction of the first classifier are provided inside the first classifier.

3. The hydrocarbon synthesis reaction apparatus according to claim 1 , wherein any one of a filtering system, a gravitational settling system, a cyclone system, a centrifugal separation system, and a magnetic separation system is adopted in the powdered catalyst particles separator.

4. The hydrocarbon synthesis reaction apparatus according to claim 1 , further comprising:
an agglomerated catalyst particles discharging device configured to discharge agglomerated catalyst particles in the solid catalysts in the slurry to the outside of the reaction vessel.

5. The hydrocarbon synthesis reaction apparatus according to claim 4 , wherein the agglomerated catalyst particles discharging device includes:
a second classifier configured to separate the agglomerated catalyst particles from the solid catalyst in the slurry, using a settling velocity difference of the particles in
a liquid; and
a discharging passage configured that the agglomerated catalyst particles separated in the second classifier are discharged to the outside of the second classifier therethrough.

6. The hydrocarbon synthesis reaction apparatus according to claim 5 , further comprising:
a supply rate adjustor configured to adjust the supply rate of the liquid hydrocarbon compound in a communication line that supplies the liquid hydrocarbon compound to the second classifier, wherein an upper portion of the second classifier is formed in the shape of a cone, and wherein the liquid hydrocarbon compound supplied to the second classifier is blown out upward inside the second classifier.

7. The hydrocarbon synthesis reaction apparatus according to claim 1 , wherein the reaction vessel is further provided with a catalyst particles feed device configured to feed new catalyst particles to the slurry in the reaction vessel.

Assignees

• Japan Oil Gas & Metals Jogmec
• Inpex Corp
• Jx Nippon Oil & Energy Corp
• Japan Petroleum Exploration Co Ltd
• Cosmo Oil Co Ltd
• Nippon Steel & Sumikin Eng Co
• Nippon Steel & Sumikin Eng Co

Inventors

• Murata Atsushi
• Yamada Eiichi
• Murahashi Kazuki
• Kato Yuzuru
• Onishi Yasuhiro

Classifications

• C10G2/32 Primary

  with the use of catalysts · CPC title

• C10G2/342

  with moving solid catalysts · CPC title

• C10G2/343 Primary

  according to the "moving-bed" method · CPC title

• C10G31/09 Primary

  by filtration · CPC title

• B01J2219/00006

  Large-scale industrial plants · CPC title