Methanol plant and gasoline synthesis plant
US-2015376097-A1 · Dec 31, 2015 · US
US9790154B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9790154-B2 |
| Application number | US-201414769190-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 26, 2014 |
| Priority date | Mar 11, 2013 |
| Publication date | Oct 17, 2017 |
| Grant date | Oct 17, 2017 |
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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.
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The invention claimed is: 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.
Cross-Sectional Technologies · mapped topic
Energy recuperation; Heat pumps · CPC title
using waste heat from other processes · CPC title
Multiple effect distillation · CPC title
Cross-Sectional Technologies · mapped topic
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