JPS6451120A - Refining method for hydrocarbon modified gas - Google Patents
Refining method for hydrocarbon modified gasInfo
- Publication number
- JPS6451120A JPS6451120A JP62208284A JP20828487A JPS6451120A JP S6451120 A JPS6451120 A JP S6451120A JP 62208284 A JP62208284 A JP 62208284A JP 20828487 A JP20828487 A JP 20828487A JP S6451120 A JPS6451120 A JP S6451120A
- Authority
- JP
- Japan
- Prior art keywords
- adsorption column
- gas
- adsorption
- pressure
- remove
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
PURPOSE:To remove CO2 efficiently from modified hydrocarbon gas by carrying out the adsorption process to adsorb and remove CO2 by feeding modified hydrocarbon gas to an adsorption column, the pressure equalizing process, exhausting process, the washing and cleaning process with refined gas, the pressure equalizing process and the pressuring process with refined gas in order one by one. CONSTITUTION:Starting gas 25 constituted of hydrocarbon modified gas is fed to an adsorption column A to adsorb and remove CO2 and the refined gas constituted of CH4 is flowed out and stored in a tank 41. Then, the adsorption column A is pressure equalized with an adsorption column C through valves 16, 5, 15 and 18, and the pressure of adsorption column A is reduced by a vacuum pump 51 to desorb CO2. Next, the adsorption column A is washed and cleaned in counter current by part of the refined gas exhausted out of the adsorption column B, and further pressure equalization is carried out between the adsorption column A and the adsorption column B. Lastly, part of the gas from an adsorption column C is introduced to the adsorption column A through valves 20, 5 and 16 and pressurized. Said respective processes are repeated in the adsorption columns A-C in order one by one.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62208284A JPH07165B2 (en) | 1987-08-24 | 1987-08-24 | Refining method of hydrocarbon reformed gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62208284A JPH07165B2 (en) | 1987-08-24 | 1987-08-24 | Refining method of hydrocarbon reformed gas |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6451120A true JPS6451120A (en) | 1989-02-27 |
JPH07165B2 JPH07165B2 (en) | 1995-01-11 |
Family
ID=16553696
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62208284A Expired - Lifetime JPH07165B2 (en) | 1987-08-24 | 1987-08-24 | Refining method of hydrocarbon reformed gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07165B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995026804A1 (en) * | 1994-04-05 | 1995-10-12 | Sumitomo Seika Chemicals Co., Ltd. | Method for removing carbon dioxide from mixed gas and alternative natural gas generating device using the method |
JP2003532519A (en) * | 2000-05-10 | 2003-11-05 | エアーセップ・コーポレーション | Multi-bed pressure swing adsorption method and apparatus |
JP2008296106A (en) * | 2007-05-30 | 2008-12-11 | Sumitomo Seika Chem Co Ltd | Refining method of mixed gas, and recycle system of mixed gas |
CN102921271A (en) * | 2012-11-07 | 2013-02-13 | 四川天一科技股份有限公司 | Improved process for recovering non-methane hydrocarbon in polyolefin tail gases by adsorption method |
JPWO2020255302A1 (en) * | 2019-06-19 | 2020-12-24 |
-
1987
- 1987-08-24 JP JP62208284A patent/JPH07165B2/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995026804A1 (en) * | 1994-04-05 | 1995-10-12 | Sumitomo Seika Chemicals Co., Ltd. | Method for removing carbon dioxide from mixed gas and alternative natural gas generating device using the method |
JP2003532519A (en) * | 2000-05-10 | 2003-11-05 | エアーセップ・コーポレーション | Multi-bed pressure swing adsorption method and apparatus |
JP2008296106A (en) * | 2007-05-30 | 2008-12-11 | Sumitomo Seika Chem Co Ltd | Refining method of mixed gas, and recycle system of mixed gas |
CN102921271A (en) * | 2012-11-07 | 2013-02-13 | 四川天一科技股份有限公司 | Improved process for recovering non-methane hydrocarbon in polyolefin tail gases by adsorption method |
JPWO2020255302A1 (en) * | 2019-06-19 | 2020-12-24 |
Also Published As
Publication number | Publication date |
---|---|
JPH07165B2 (en) | 1995-01-11 |
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Legal Events
Date | Code | Title | Description |
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R250 | Receipt of annual fees |
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