IP Library Granted Patent US 9,790,154
Granted Patent B2
US 9,790,154 · App. 14/769,190 · Granted Oct 17, 2017

Methanol plant and gasoline synthesis plant

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Quick Facts
Patent No.
US 9,790,154
App. No.
14/769,190
Granted
Oct 17, 2017
Kind
B2
Abstract

Provided is a methanol plant that can obtain fresh water from sea water by using, in a seawater desalination device, the exhaust heat discharged in a step for producing methanol from natural gas. The methanol plant is provided with: a heat exchanger ( 4 ) that recovers into a thermal medium (for example, seawater) the exhaust heat discharged from a step for producing methanol from a feed stock (for example, natural gas); and a seawater desalinization device ( 6 ) that obtains freshwater from seawater using the exhaust heat recovered by means of the thermal medium.

Claims (20)

1. A methanol plant comprising:

a heat exchanger which makes exhaust heat that is discharged from a process of producing methanol from a feed stock be recovered to seawater; and

a seawater desalination device which obtains fresh water from the seawater by using the exhaust heat recovered from the seawater by the heat exchanger,

wherein a plurality of the heat exchangers is provided in a distillation process of the process of producing methanol in a flow direction of mixed gas after methanol synthesis,

wherein the mixed gas passes through the plurality of heat exchangers, and a temperature of the mixed gas decreases, and a wetness of the mixed gas increases as it flows toward a downstream side in the flow direction of the mixed gas, and

wherein heat exchange with the mixed gas having increased wetness is performed in the heat exchanger provided on a downstream side in the flow direction of the mixed gas.

2. The methanol plant according to claim 1 , wherein the exhaust heat has a temperature in a range of 100° C. to 200° C.

3. The methanol plant according to claim 2 , wherein the seawater desalination device obtains the fresh water by a multistage flash evaporation method using the exhaust heat.

4. The methanol plant according to claim 2 , wherein the methanol is produced by using vapor which is produced from the fresh water.

5. The methanol plant according to claim 2 , wherein the process is provided with a step of producing gasoline from the methanol.

6. The methanol plant according to claim 1 , wherein the seawater desalination device obtains the fresh water by a multistage flash evaporation method using the exhaust heat.

7. The methanol plant according to claim 6 , wherein the methanol is produced by using vapor which is produced from the fresh water.

8. The methanol plant according to claim 6 , wherein the process is provided with a step of producing gasoline from the methanol.

9. The methanol plant according to claim 1 , wherein the methanol is produced by using vapor which is produced from the fresh water.

10. The methanol plant according to claim 9 , wherein the process is provided with a step of producing gasoline from the methanol.

11. The methanol plant according to claim 1 , wherein the process is provided with a step of producing gasoline from the methanol.

12. A gasoline synthesis plant comprising:

a methanol plant which produces methanol from a feed stock;

a heat exchanger which makes exhaust heat that is discharged from a process of producing gasoline from the methanol be recovered to seawater; and

a seawater desalination device which obtains fresh water from the seawater by using the exhaust heat recovered by the seawater.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 18, 2018
From: MITSUBISHI HEAVY INDUSTRIES, LTD.
To: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
Reel/Frame 046581/0430 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 20, 2015
From: IIJIMA, MASAKI; HIRAYAMA, HARUAKI
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 036381/0833 →