Method for producing synthesis gas

Patent metadata

Field	Value
Publication number	US-9056772-B2
Application number	US-201113581026-A
Country	US
Kind code	B2
Filing date	Feb 21, 2011
Priority date	Mar 2, 2010
Publication date	Jun 16, 2015
Grant date	Jun 16, 2015

Abstract

It is avoided that the sulfur compounds originating from the castable is mixed into produced synthesis gas, the mixed sulfur compounds are separated and collected with carbon dioxide, the collected carbon dioxide is recycled as raw material gas and then the sulfur compounds is directly supplied to the reformer to consequently degrade the reforming catalyst in the reformer by sulfur poisoning. The carbon dioxide separated and collected in the carbon dioxide removal step is introduced into the desulfurization apparatus of the desulfurization step or the sulfur compounds adsorption apparatus before being recycled to the reformer to remove the sulfur compounds.

First claim

The invention claimed is:

1. A method for producing synthesis gas comprising a desulfurization step of desulfurizing sulfur compounds in natural gas by means of a desulfurization apparatus; a synthesis gas production step for producing synthesis gas by way of a reforming reaction of gas containing desulfurized natural gas, steam and carbon dioxide; and a carbon dioxide removal step for separating and collecting separated and collected gas containing carbon dioxide as main component from the produced synthesis gas, the method further comprising a step of recycling the separated and collected gas for the synthesis gas production step,
wherein the desulfurization step is constituted of two steps including a first step of hydrogenating the sulfur compounds contained in natural gas and a second step of adsorbing the sulfur compounds hydrogenated in the first step by means of a desulfurizing agent, and
wherein said separated and collected gas is introduced into the natural gas after the first step and before the second step.

2. The method according to claim 1 , characterized in that a main component of the desulfurizing agent employed in the desulfurization apparatus is zinc oxide.

3. The method according to claim 1 , characterized in that a concentration of sulfur compounds contained in the gas introduced into the synthesis gas production step is less than 10 vol-ppb in terms of sulfur atoms.

4. The method according to claim 1 , characterized in that said separated and collected gas shows a temperature range from 300 to 400° C., a pressure range from 2.1 to 2.7 MPaG and a GHSV range from 1,000 to 2,000 h −1 at the time of being introduced into the desulfurization apparatus.

5. The method according to claim 1 , characterized in that the gas introduced into the synthesis gas production step shows an H 2 O/C mol ratio of larger than 0 and less than 3.0 and a CO 2 /C mol ratio of larger than 0 and less than 1.0.

6. A method for producing synthetic hydrocarbons from natural gas, characterized in that synthesis gas produced by the method according to claim 1 is subjected to a Fischer-Tropsch reaction, Fischer-Tropsch oil is produced by separating a gaseous product from the Fischer-Tropsch reaction product, and light hydrocarbon gas and kerosene and gas oil that is the final product are separated from each other by distilling a hydrogenation product obtained by hydroprocessing the Fischer-Tropsch oil.

7. A method for producing synthesis gas comprising a desulfurization step for desulfurizing sulfur compounds in natural gas; a synthesis gas production step for producing synthesis gas by way of a reforming reaction of gas containing desulfurized natural gas, steam and carbon dioxide; and a carbon dioxide removal step for separating and collecting separated and collected gas containing carbon dioxide as main component from the produced synthesis gas, the method further comprising a step for recycling said separated and collected gas for the synthesis gas production step,
wherein said separated and collected gas is introduced into an adsorption apparatus to remove sulfur compounds from said separated and collected gas and subsequently recycled for the synthesis gas production step, and
wherein the adsorption apparatus is provided separately from the desulfurization step.

8. The method according to claim 7 , characterized in that the adsorption apparatus employs active carbon or zeolite as adsorbent.

9. The method according to claim 7 , characterized in that a concentration of the sulfur compounds contained in the gas recycled for the synthesis gas production step is less than 10 vol-ppb in terms of sulfur atoms.

10. The method according to claim 7 , characterized in that an operating conditions of the adsorption apparatus is that a temperature range is room temperature to 50° C., a pressure range is 0.0 to 0.3 MPaG and a GHSV range is 1,000 to 3,000 h −1 .

11. The method according to claim 7 , characterized in that the gas introduced into the synthesis gas production step shows an H 2 O/C mol ratio of larger than 0 and less than 3.0 and a CO 2 /C mol ratio of larger than 0 and less than 1.0.

12. A method for producing synthetic hydrocarbons from natural gas, characterized in that synthesis gas produced by the method according to claim 7 is subjected to a Fischer-Tropsch reaction, Fischer-Tropsch oil is produced by separating a gaseous product from the Fischer-Tropsch reaction product, and light hydrocarbon gas and kerosene and gas oil that is the final products are separated from each other by distilling a hydrogenation product obtained by hydroprocessing the Fischer-Tropsch oil.

Assignees

• Hodoshima Shinya
• Yagi Fuyuki
• Wakamatsu Shuhei
• Kawazuishi Kenichi
• Japan Oil Gas & Metals Jogmec
• Inpex Corp
• Jx Nippon Oil & Energy Corp
• Japan Petroleum Exploration Co
• Cosmo Oil Co Ltd
• Nippon Steel Eng Co Ltd
• Chiyoda Corp

Inventors

• Hodoshima Shinya
• Yagi Fuyuki
• Wakamatsu Shuhei
• Kawazuishi Kenichi

Classifications

• C01B3/384 Primary

  with external heating of the catalyst · CPC title

• C01B3/48

  followed by reaction of water vapour with carbon monoxide · CPC title

• C01B2203/0238

  the reforming step being a carbon dioxide reforming step · CPC title

• C01B2203/0415

  Purification by absorption in liquids · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title