IP Library › Granted Patent US 10,252,963
Granted Patent B2
US 10,252,963 · App. 15/519,003 · Granted Apr 9, 2019

Method for producing methanol and apparatus for producing methanol

Inventors: Yasuaki Kambe (Niigata, JP); Kohei Uchida (Niigata, JP); Hiroshi Watanabe (Niigata, JP); Daigo Hirakawa (Niigata, JP); Tatsuya Hasegawa (Tokyo, JP)
Assignee: MITSUBISHI GAS CHEMICAL COMPANY, INC.
C07C29/152B01J8/0492B01J8/0496B01J23/80B01J37/00B01J37/03C07C31/04B01J2208/00106B01J2208/00893C07B61/00Y02P20/52
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Quick Facts
Patent No.
US 10,252,963
App. No.
15/519,003
Granted
Apr 9, 2019
Kind
B2
Abstract

Synthesizing methanol from a synthesis gas and separating an unreacted gas from a reaction mixture obtained by passing through the synthesis step, the method including a synthesis loop having at least two synthesis steps and at least two separation steps; obtaining a first mixed gas by increasing through a circulator a pressure of a residual gas, obtained by removing a purge gas from the final unreacted gas separated from the final reaction mixture subsequent to the final synthesis step, and by mixing the residual gas with a fraction of a make-up gas; synthesizing methanol; separating a first unreacted gas from the first reaction mixture obtained in the synthesizing step; obtaining a second mixed gas by mixing the first unreacted gas and a fraction of the make-up gas; finally synthesizing methanol; and separating the final unreacted gas from the final reaction mixture obtained in the final synthesis step.

Claims (17)

1. A method for producing methanol comprising: synthesis steps of synthesizing methanol from a synthesis gas comprising hydrogen, carbon monoxide and carbon dioxide; and separation steps of separating an unreacted gas from a reaction mixture obtained by passing through one of the synthesis steps,

the method comprising a synthesis loop having at least two of the synthesis steps and at least two of the separation steps,

wherein the synthesis loop comprises: a first mixing step of obtaining a first mixed gas by increasing through a circulator a pressure of a residual gas, obtained by removing a purge gas from a final unreacted gas separated from a final reaction mixture in a final separation step subsequent to a final synthesis step, and by mixing the residual gas with 10 to 90 mol % of a make-up gas comprising hydrogen, carbon monoxide and carbon dioxide; a first synthesis step of synthesizing methanol from the first mixed gas; a first separation step of separating a first unreacted gas from a first reaction mixture obtained in the first synthesis step; a second mixing step of obtaining a second mixed gas by mixing the first unreacted gas and at least a fraction of 10 to 90 mol % of the make-up gas; the final synthesis step of finally synthesizing methanol; and the final separation step of separating the final unreacted gas from the final reaction mixture obtained in the final synthesis step, and

at least in the final synthesis step, a reaction temperature of a catalyst layer is controlled by indirect heat exchange with pressurized boiling water.

2. The method for producing methanol according to claim 1 , wherein at least one separation step of the at least two separation steps comprised in the synthesis loop is a step of separating with a gas-liquid separator a liquid comprising methanol, produced by cooling the gaseous reaction mixture.

3. The method for producing methanol according to claim 1 , wherein the first unreacted gas is mixed with 40 to 70 mol % of the make-up gas.

4. The method for producing methanol according to claim 1 , wherein in the first separation step, the first unreacted gas is obtained by separating 35 to 100 mol % of the methanol in the first reaction mixture.

5. The method for producing methanol according to claim 1 , wherein in the first separation step, the first unreacted gas is obtained by separating 75 to 96 mol % of the methanol in the first reaction mixture.

6. The method for producing methanol according to claim 1 , wherein a circulation ratio, which is a ratio of a molar flow rate of the residual gas obtained by removing the purge gas from the final unreacted gas to a molar flow rate of the make-up gas, is within a range from 0.6 to 2.0.

7. The method for producing methanol according to claim 6 , wherein the circulation ratio is within a range from 0.8 to 1.5.

8. The method for producing methanol according to claim 1 , wherein a temperature of the pressurized boiling water is within a range from 220° C. to 260° C.

9. The method for producing methanol according to claim 1 , wherein the final synthesis step is a step of synthesizing methanol from the second mixed gas, or a step of synthesizing methanol from a second unreacted gas or a third mixed gas obtained by mixing the second unreacted gas and a fraction of the make-up gas, the second unreacted gas being separated from a second reaction mixture obtained in the step of synthesizing methanol from the second mixed gas.

10. The method for producing methanol according to claim 1 , wherein the final synthesis step is a step of synthesizing methanol from the second mixed gas.

11. The method for producing methanol according to claim 1 , wherein a catalyst used in each of the synthesis steps comprises copper atoms and zinc atoms in an atomic ratio (copper/zinc) of 2.0 to 3.0, and further comprises aluminum atoms.

12. The method for producing methanol according to claim 1 , wherein a catalyst used in each of the synthesis steps comprises copper atoms and zinc atoms in an atomic ratio (copper/zinc) of 2.1 to 3.0, and further comprises alumina in a content of 3% to 20% by mass, and is prepared by a production method comprising: a step of producing a precipitate comprising copper and zinc by mixing an aqueous solution comprising copper, an aqueous solution comprising zinc and an alkali aqueous solution; a step of obtaining a mixture by mixing the precipitate and an alumina hydrate having a pseudo boehmite structure; and a step of molding the mixture so as for the density to be 2.0 to 3.0 g/mL.

13. The method for producing methanol according to claim 1 , wherein the proportion of the make-up gas to be mixed with the first unreacted gas is controlled according to a temperature of a reactor in the synthesis step.

14. The method for producing methanol according to claim 1 , wherein in each of all of the synthesis steps, a reaction temperature of a catalyst layer is controlled by indirect heat exchange with pressurized boiling water.

Assignments (2)
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE NAME PREVIOUSLY RECORDED AT REEL: 43001 FRAME: 0061. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Jan 23, 2019
From: KAMBE, YASUAKI; UCHIDA, KOHEI; WATANABE, HIROSHI; HIRAKAWA, DAIGO; HASEGAWA, TATSUYA
To: MITSUBISHI GAS CHEMICAL COMPANY, INC.
Reel/Frame 049510/0401 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 13, 2017
From: KAMBE, YASUAKI; UCHIDA, KOHEI; WATANABE, HIROSHI; HIRAKAWA, DAIGO; HASEGAWA, TATSUYA
To: MISUBISHI GAS CHEMICAL COMPANY, INC.
Reel/Frame 043001/0061 →
Priority Claims (1)
JP 2014-214081 · Oct 20, 2014 · national
Continuity (1)
Related Publication 20170240492A1 · Aug 24, 2017