Liquid-fuel synthesizing method and liquid-fuel synthesizing apparatus

Patent metadata

Field	Value
Publication number	US-9452405-B2
Application number	US-99820109-A
Country	US
Kind code	B2
Filing date	Sep 25, 2009
Priority date	Sep 30, 2008
Publication date	Sep 27, 2016
Grant date	Sep 27, 2016

Abstract

A liquid-fuel synthesizing method includes a synthesizing step of synthesizing liquid fuels by making a synthesis gas including a carbon monoxide gas and a hydrogen gas as the main components and a slurry having solid catalyst particles suspended in a liquid react with each other in a reactor, and a synthesis gas supply step of supplying the synthesis gas to the reactor from a plurality of supply devices provided in the reactor so as to have different heights.

First claim

The invention claimed is:

1. A liquid-fuel synthesizing apparatus comprising:
a reactor configured to synthesize liquid fuels using a Fischer-Tropsch synthesis reaction in which a synthesis gas including a carbon monoxide gas and a hydrogen gas as the main components and a slurry having solid catalyst particles suspended in a liquid react with each other in the reactor;
a plurality of supply devices which includes a first supply device provided at the bottom of the reactor and second supply devices each provided at the reactor at a height different from the first supply device, wherein the second supply devices are connected to the reactor at substantially equal intervals in a vertical direction,
a first flow line connected to a top of the reactor,
a vapor-liquid separator to which the first flow line is connected, and
a second flow line connected to the vapor-liquid separator and connected to only the first supply device among the supply devices, wherein
valves are respectively attached to the second supply devices so that a flow rate of the synthesis gas supplied from each of the second supply devices is individually adjusted via the valves,
the synthesis gas is supplied to the reactor from the first supply device and the second supply devices,
and wherein:
the plurality of supply devices is configured to supply the synthesis gas so that the gas superficial velocity in the reactor is within a range of 0.04 m/s to 0.3 m/s, and
each of the second supply devices are configured to supply the synthesis gas to the reactor at the same flow rate, the flow rate being determined by:
obtaining an amount of decrease of a gas superficial velocity in the slurry accompanying a reaction from the lower part to the upper part of the reactor, when the synthesis gas is supplied only from the first supply device; and
performing simulations or experiments to obtain the flow rate by which the amount of decrease of the gas superficial velocity can be compensated for and the gas superficial velocity within the reactor can be made uniform.

2. The liquid-fuel synthesizing apparatus according to claim 1 , wherein the plurality of supply devices is configured to supply the synthesis gas so that the gas superficial velocity in the reactor is within a range of 0.1 m/s to 0.2 m/s.

3. The liquid-fuel synthesizing apparatus according to claim 1 , wherein
each of the second supply devices has a plurality of supply ports provided on a cross-section of the reactor.

4. The liquid-fuel synthesizing apparatus according to claim 3 , wherein
each of the second supply devices includes: a trunk part provided so as to pass through a center of the reactor; and a plurality of internal tubes which is connected to the trunk part, is annularly formed concentrically with the reactor, and differs in diameter, and
the plurality of supply ports is formed in the plurality of internal tubes.

5. The liquid-fuel synthesizing apparatus according to claim 3 , wherein
each of the second supply devices includes: a trunk part provided so as to pass through a center of the reactor; and a plurality of branch parts which extends horizontally from the trunk part, and
the plurality of supply ports is formed in the plurality of branch parts.

6. The liquid-fuel synthesizing apparatus according to claim 1 , wherein
each of the second supply devices includes: a trunk part provided so as to pass through a center of the reactor and extend horizontally; and a plurality of branch parts extend horizontally from the trunk part so as to be perpendicular to the trunk part and be parallel to each other, and
a plurality of supply ports are formed in the plurality of branch parts.

Assignees

• Onishi Yasuhiro
• Hirama Akihiko
• Japan Oil Gas & Metals Jogmec
• Inpex Corp
• Jx Nippon Oil & Energy Corp
• Japan Petroleum Exploration Co Ltd
• Cosmo Oil Co Ltd
• Nippon Steel Eng Co Ltd

Inventors

• Onishi Yasuhiro
• Hirama Akihiko

Classifications

• B01J2208/003

  involving reactant slurries · CPC title

• B01J8/1827

  the fluidising gas being a reactant · CPC title

• B01J2208/00911

  Sparger-type feeding elements · CPC title

• C10G2/342

  with moving solid catalysts · CPC title

• B01J2208/00274

  involving reactant vapours · CPC title