JPS57122025A - Utilizing method of surplus gas - Google Patents

Utilizing method of surplus gas

Info

Publication number
JPS57122025A
JPS57122025A JP840881A JP840881A JPS57122025A JP S57122025 A JPS57122025 A JP S57122025A JP 840881 A JP840881 A JP 840881A JP 840881 A JP840881 A JP 840881A JP S57122025 A JPS57122025 A JP S57122025A
Authority
JP
Japan
Prior art keywords
gas
methanol
surplus
give
demand
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.)
Pending
Application number
JP840881A
Other languages
Japanese (ja)
Inventor
Kiyota Iwaki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP840881A priority Critical patent/JPS57122025A/en
Publication of JPS57122025A publication Critical patent/JPS57122025A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To adjust the supply and demand of a surplus gas advantageously, by adjusting components in the surplus gas formed as by-product in an iron mill, etc. to a specific volume ratio H2/CO, methanizing the adjusted gas, partially oxidizing the methanized gas to give methanol gas, cooling the gas to ordinary temperature, and easily liquefying and storing the surplus gas.
CONSTITUTION: A coke oven gas (COG) 1 formed as a by-product in an iron mill, etc. is mixed with a converter gas (LDG) 2 in a gas mixer 9 to adjust the volume ratio between H2 and CO to ≥3. The adjusted mixture is then passed through a methanizing reaction column 10 to give a gas rich in methane. The gas is then dehdrated in a dehydrating column 11 and decarbonated in a decarbonating column 12 Oxygen or air 14 is added to the decarbonated gas in an amount of the upper explosion limit or above, and the gas is partially oxidized in the presence of a chromium oxide as a catalyst in a methanol reaction colum 13 to afford the methanol gas. The resultant methanol gas is then cooled to ordinary temperature in an indirect cooler 15 to give liquid methanol 17. According to the method, methanol is obtained by the partial oxidation of the methane at a relatively low pressure, and the surplus gas can be easily liquefied and stored. Thus, the mthanol is useful for adjusting the supply and demand of the surplus gas in the season of low electric power demand.
COPYRIGHT: (C)1982,JPO&Japio
JP840881A 1981-01-22 1981-01-22 Utilizing method of surplus gas Pending JPS57122025A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP840881A JPS57122025A (en) 1981-01-22 1981-01-22 Utilizing method of surplus gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP840881A JPS57122025A (en) 1981-01-22 1981-01-22 Utilizing method of surplus gas

Publications (1)

Publication Number Publication Date
JPS57122025A true JPS57122025A (en) 1982-07-29

Family

ID=11692323

Family Applications (1)

Application Number Title Priority Date Filing Date
JP840881A Pending JPS57122025A (en) 1981-01-22 1981-01-22 Utilizing method of surplus gas

Country Status (1)

Country Link
JP (1) JPS57122025A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0200880A2 (en) * 1985-04-27 1986-11-12 Ruhrkohle Aktiengesellschaft Process for the preparation of chemical raw materials
DE3805397A1 (en) * 1988-02-20 1989-08-24 Ruhrkohle Ag Process for producing fuel methanol (motor fuel) from coke oven gas and metallurgical plant gas
WO2010136313A1 (en) * 2009-05-25 2010-12-02 Uhde Gmbh Syngas production method
CN103423589A (en) * 2013-08-27 2013-12-04 唐山中润煤化工有限公司 Liquid oxygen vaporizing system for technology of preparing methanol with coke oven gas and technology

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0200880A2 (en) * 1985-04-27 1986-11-12 Ruhrkohle Aktiengesellschaft Process for the preparation of chemical raw materials
DE3805397A1 (en) * 1988-02-20 1989-08-24 Ruhrkohle Ag Process for producing fuel methanol (motor fuel) from coke oven gas and metallurgical plant gas
WO2010136313A1 (en) * 2009-05-25 2010-12-02 Uhde Gmbh Syngas production method
US8617423B2 (en) 2009-05-25 2013-12-31 Thyssenkrupp Uhde Gmbh Syngas production method
CN103423589A (en) * 2013-08-27 2013-12-04 唐山中润煤化工有限公司 Liquid oxygen vaporizing system for technology of preparing methanol with coke oven gas and technology

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