Hydrocarbon synthesis reaction apparatus, start-up process thereof, and hydrocarbon synthesis reaction system

Patent metadata

Field	Value
Publication number	US-9434657-B2
Application number	US-201214006998-A
Country	US
Kind code	B2
Filing date	Mar 13, 2012
Priority date	Mar 30, 2011
Publication date	Sep 6, 2016
Grant date	Sep 6, 2016

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.

First claim

The invention claimed is:

1. A hydrocarbon synthesis reaction apparatus comprising:
a synthesis gas supply line in which a synthesis gas containing carbon monoxide gas and hydrogen gas as main components is sent by a synthesis gas sending device and the thus sent synthesis gas is compressed and supplied by a first compressor;
a reactor configured to accommodate a catalyst slurry prepared by suspending solid catalyst particles in a liquid to synthesize hydrocarbons by bringing the synthesis gas supplied from the synthesis gas supply line into contact with the 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;
an off-gas discharge line configured to discharge a portion of gas after separation by the gas-liquid separator as an off gas outside a system;
a first recycle line in which the unreacted synthesis gas after separation by the gas-liquid separator is compressed and recycled into the reactor by a second compressor; and
a second recycle line configured to recycle into the inlet side of the first compressor a residual unreacted synthesis gas to be introduced into the first recycle line, a part of the unreacted synthesis gas after separation by the gas-liquid separator, at the time of start-up operation when the synthesis gas to be introduced from the synthesis gas sending device to the reactor is introduced in a gradually increasing amount from a processing flow rate lower than the processing flow rate of the synthesis gas to be processed during operation at a rated flow rate to a processing flow rate of the synthesis gas during operation at a rated flow rate.

2. The hydrocarbon synthesis reaction apparatus according to claim 1 , wherein
the hydrocarbon synthesis reaction apparatus is provided with the first recycle line, and an inert gas flow line which is communicated with the inlet side of the first compressor from the gas-liquid separator, the first recycle line and the inlet gas flow line serve as an inert gas flow line in which a gas inside a system is replaced with an inert gas at the time of starting up the reactor and the catalyst slurry is also fluidized, and wherein
the inert gas flow line is also used as the second recycle line.

3. The hydrocarbon synthesis reaction apparatus according to claim 1 further comprising:
a converging and mixing unit which is installed at an upstream side at a site where the synthesis gas sent from the synthesis gas sending device is introduced into the inlet side of the first compressor and in which the unreacted synthesis gas from the second recycle line is converged and mixed with the synthesis gas sent from the synthesis gas sending device; and
a temperature controlling device configured to control a mixed gas mixed by the converging and mixing unit in such a manner that a temperature thereof is made at least equal to or higher than a temperature of the unreacted synthesis gas from the second recycle line.

4. A hydrocarbon synthesis reaction system for producing a liquid fuel base stock from a hydrocarbon feedstock, the hydrocarbon synthesis reaction system comprising:
the hydrocarbon synthesis reaction apparatus according to claim 1 ; and
a product fractionating unit configured to fractionate a liquid fuel base stock from hydrocarbons produced by the hydrocarbon synthesis reaction apparatus, wherein
the synthesis gas sending device is a synthesis gas production unit configured to reform the hydrocarbon feedstock to produce the synthesis gas and sends the synthesis gas to the synthesis gas supply line.

5. A start-up process of a hydrocarbon synthesis reaction apparatus described in claim 1 , the start-up process comprising:
a first step in which, prior to introduction of the synthesis gas into the reactor, an inert gas is introduced into the reactor in advance through the synthesis gas supply line, the first compressor and the second compressor are both operated at a rated flow rate to flow the inert gas via the first recycle line and the second recycle line, thereby, a gas inside a system is replaced with the inert gas, with the off gas discharged from the off-gas discharge line, and also the catalyst slurry is fluidized;
a second step in which the synthesis gas is introduced through the synthesis gas supply line, with the first compressor operated at a rated flow rate, into the reactor which is in a state that the catalyst slurry is fluidized by performing the first step at a flow rate lower than a processing flow rate during operation at a rated flow rate, an unreacted synthesis gas discharged from the reactor and separated by the gas-liquid separator is flowed via the first recycle line by operating the second compressor at a rated flow rate, and also a residual unreacted synthesis gas to be introduced into the first recycle line, a part of the unreacted synthesis gas after separation by the gas-liquid separator, is flowed via the second recycle line into the inlet side of the first compressor operated at a rated flow rate, thereby, the gas inside the system is replaced with the synthesis gas, with the off gas discharged from the off-gas discharge line, and the flow rate of supplying the synthesis gas from the synthesis gas supply line is also maintained at a constant flow rate lower than a processing flow rate during operation at a rated flow rate; and
a third step in which, at a stage that reaction becomes stable in the second step, the synthesis gas to be introduced into the reactor through the synthesis gas supply line is gradually increased in flow rate, while the unreacted synthesis gas to be flowed through the second recycle line is gradually decreased in flow rate, and the flow rate of the synthesis gas to be finally introduced into the reactor through the synthesis gas supply line is increased up to the processing flow rate of the synthesis gas which is processed during operation at a rated flow rate.

Assignees

• Onishi Yasuhiro
• Tasaka Kazuhiko
• Mikuriya Tomoyuki
• 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

Inventors

• Onishi Yasuhiro
• Tasaka Kazuhiko
• Mikuriya Tomoyuki

Classifications

• B01J2219/00202

  at the reactor outlet · CPC title

• B01J2208/00548

  Flow · CPC title

• C10G2/342

  with moving solid catalysts · CPC title

• B01J8/22

  gas being introduced into the liquid · CPC title

• B01J19/0033

  Optimalisation processes, i.e. processes with adaptive control systems (adaptive control systems per se G05B13/00) · CPC title