IP Library Granted Patent US 6,875,794
Granted Patent B2
US 6,875,794 · App. 10/197,519 · Granted Apr 5, 2005

Method of manufacturing methanol

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Quick Facts
Patent No.
US 6,875,794
App. No.
10/197,519
Granted
Apr 5, 2005
Kind
B2
Abstract

A method of manufacturing methanol comprising producing a synthesis gas containing hydrogen, carbon monoxide and carbon dioxide, allowing reaction of the synthesis gas to take place over a catalyst to produce a crude methanol, separating the crude methanol into unreacted gas and liquid crude methanol, and distilling the liquid crude methanol to separate it into refined methanol and waste water. Carbon dioxide in combustion exhaust gas to be discharged from a reformer is recovered, and that in feeding the carbon dioxide to the upstream side and/or the downstream side of the reformer, part of the unreacted gas is utilized as a purge gas, a portion of which being utilized as a fuel for a combustion device of the reformer, while the balance of the purge gas being utilized as a fuel for other heating sources and/or as an agent for desulfurizating raw gas.

Claims (16)

1. A method of manufacturing methanol comprising:

reacting hydrocarbons with water vapor in a reformer to produce a synthesis gas comprising hydrogen, carbon monoxide and carbon dioxide; allowing reaction of the synthesis gas to take place over a methanol-synthesizing catalyst to produce a crude methanol; cooling said crude methanol; separating said cooled crude methanol into unreacted gas and liquid crude methanol; and distilling said liquid crude methanol to separate it into refined methanol and waste water comprising low boiling point organic compounds and high boiling point organic compounds; and

wherein carbon dioxide in combustion exhaust gas to be discharged from said reformer is recovered in a carbon dioxide-recovering device, and that in feeding the carbon dioxide thus recovered to the upstream side and/or the downstream side of said reformer, a part of said unreacted gas is utilized as a purge gas, a portion of which being utilized as a fuel for a combustion device of said reformer, while the balance of said purge gas being utilized as a fuel for one or more other heating sources, and as an agent for desulfurizing raw gas, and wherein said unreacted gas comprises hydrogen.

2. The method of manufacturing methanol according to claim 1 , wherein at least one of said other heating sources is a boiler.

3. A method of manufacturing methanol comprising:

reacting hydrocarbons with water vapor in a reformer to produce a synthesis gas comprising hydrogen, carbon monoxide and carbon dioxide; allowing reaction of the synthesis gas to take place over a methanol-synthesizing catalyst to produce a crude methanol; cooling said crude methanol; separating said cooled crude methanol into unreacted gas and liquid crude methanol; and distilling said liquid crude methanol to separate it into refined methanol and waste water comprising low boiling point organic compounds and high boiling point organic compounds; and

wherein carbon dioxide in combustion exhaust gas to be discharged from the reformer is recovered in a carbon dioxide-recovering device, and that in feeding the carbon dioxide thus recovered to the upstream side and/or the downstream side of said reformer, part of said unreacted gas is used as a purge gas for enabling it to be utilized as a fuel for heating sources, except for a combustion device of said reformer, and as an agent for desulfurizing raw gas, and wherein said unreactive gas comprises hydrogen.

4. The method of manufacturing methanol according to claim 3 , wherein at least one of said other heating sources is a boiler.

5. The method of manufacturing methanol according to claim 1 , wherein said reformer is fueled by a hydrocarbon source.

6. The method of manufacturing methanol according to claim 5 , wherein the hydrocarbon source comprises natural gas.

7. The method of manufacturing methanol according to claim 3 , wherein said reformer is fueled by a hydrocarbon source.

8. The method of manufacturing methanol according to claim 7 , wherein the hydrocarbon source comprises natural gas.

9. The method of manufacturing methanol according to claim 1 , further comprising, setting a mixing molar ratio of methane to steam from 1:1.5 to 1:5 in a reaction tube of said reformer.

10. The method of manufacturing methanol according to claim 9 , further comprising, setting a mixing molar ratio of methane to carbon dioxide from 1:0.1 to 1:3 in a reaction tube of said reformer.

11. The method of manufacturing methanol according to claim 3 , further comprising, setting a mixing molar ratio of methane to steam from 1:1.5 to 1:5 in a reaction tube of said reformer.

12. The method of manufacturing methanol according to claim 11 , further comprising, setting a mixing molar ratio of methane to carbon dioxide from 1:0.1 to 1:3 in a reaction tube of said reformer.

Assignments (3)
CHANGE OF ADDRESS Recorded Sep 12, 2018
From: MITSUBISHI HEAVY INDUSTRIES, LTD.
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 047054/0625 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 12, 2018
From: MITSUBISHI HEAVY INDUSTRIES, LTD.
To: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
Reel/Frame 047054/0898 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 16, 2002
From: SEIKI, YOSHIO; IMAI, TETSUYA; KOBAYASHI, KAZUTO; OSORA, HIROYUKI; KUWADA, CHIE; MORITA, KAZUHIRO; MIYAMOTO, SHUICHI
To: MITSUBISHI HEAVY INDUSTRIES, LTD.; MITSUBISHI GAS CHEMICAL COMPANY, INC.
Reel/Frame 013393/0399 →