CN1495247A - Catalytic combusticon dehydrogenation process of mine gas for producing methyl alcohol - Google Patents
Catalytic combusticon dehydrogenation process of mine gas for producing methyl alcohol Download PDFInfo
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- CN1495247A CN1495247A CNA021136289A CN02113628A CN1495247A CN 1495247 A CN1495247 A CN 1495247A CN A021136289 A CNA021136289 A CN A021136289A CN 02113628 A CN02113628 A CN 02113628A CN 1495247 A CN1495247 A CN 1495247A
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- coal mine
- methyl alcohol
- catalyticcombustion
- catalyst
- mine gas
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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
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Abstract
The present invention discloses a catalytic combusion deoxidation process of coal mine gas for producing methyl alcohol. The methane being in the coal mine gas is concentrated, and can be used as raw material for producing methyl alcohol, before operation of methane concentration the coal mine gas can be undergone the process of catalytic combustion deoxidation treatment by using catalyst to make the oxygen concentration in the coal mine gas be less than 1%, then after the coal mine gas is undergone the processes of heat-recovery, cooling and water separation, it can be fed into the procedure of methane concentration treatment. The adoption of said invention can effectively remove oxygen from coal mine gas so as to ensure safety of methane concentration process.
Description
The invention belongs to basic organic chemical industry, especially adopting coal mine mash gas is the Technology field of raw material production methyl alcohol.
Develop rapidly along with China's chemical industry, the synthetic gas chemical products status in the national economy again is more and more important, as by synthetic gas or oxygenatedchemicalss such as the synthesizing glycol that sets out, ethanol, acetic acid such as the methyl alcohol of producing thus, formaldehyde, dme, and produce ethene, propylene or direct synthetic petroleum chemical products by synthetic gas.
The source of industrial synthetic gas is important to be had: Sweet natural gas (methane), heavy dross coal, by product etc., wherein with the Sweet natural gas for the feedstock production synthetic gas has less investment, scale is big, the feature of environmental protection good, cost is low advantage, this method has become one of main source of synthetic gas in the world.
Coal mine mash gas is the gas that is rich in methane, its utilization has suitable value, but because the content of methane is relatively low in the coal mine gas, the content of air is bigger, use relative difficult, cause a large amount of coal mine gas to fail for a long time well to be utilized, not only cause a large amount of wastings of resources, also caused the pollution of environment.
The method that the utilization key of coal mine mash gas is to locate a kind of economy is concentrated to methane wherein more than 90%, to this, Southwest Chemical Research and Design Institute has been invented transformation absorption (PSA) and has been put forward the technology of dense methane (Chinese patent bulletin CN85103557B), generally speaking, methane concentration in the coal mine gas must be brought up to more than 90%, and be concentrated in the process at methane, the oxygen level of discharging waste gas also is concentrated raising, owing to inevitably contain the methane gas of 5-15% in the waste gas, cause the composition of discharging waste gas to be in the scope that explosion gases is formed, therefore in gas exhaust duct, there is the danger of blast all the time, like this, further applying of this technology is restricted.
In view of the as above shortcoming of prior art, the objective of the invention is to design a kind of coal mine mash gas deoxidization technique, make it to overcome the above shortcoming of prior art, the possibility safe and effective, that eliminating is at low cost exploded.
The objective of the invention is to realize by following means.
Produce the catalyticcombustion deoxidization process of methyl alcohol with coal mine mash gas, methane in the coal mine mash gas is concentrated the raw material of back as methanol production, before the methane concentration operation, coal mine mash gas is carried out the catalyticcombustion deoxidation through catalyzer, make oxygen concn in the coal mine gas less than 1%, after recovery of heat-cooling-water sepn, enter methane concentration operation then again.
After adopting technology of the present invention,, got rid of the danger of blast in the concentration of carrying out just having reduced effectively before methane concentrates oxygen.Flow process of the present invention is simple, does not need to add in addition auxiliary material, though the burned consumption of part methane is arranged in deoxidation process, this part methane is converted into CO
2, CO and staying substantially in the methane product gas, loss only be a spot of hydrogen, and be raw material when generating methyl alcohol with methane, the hydrogen richness in the unstripped gas has generally all surpassed best ratio of carbon-hydrogen, promptly hydrogen richness was original just excessive.
Technological process flow process figure of the present invention as shown in Figure 1.
Coal mine mash gas is sent into catalytic burner by certain air speed after desulfurization, the catalyst combustion reaction temperature is 200-500 ℃, and reaction pressure is greater than normal pressure, and reaction velocity is 5000-10000h
-1Coal mine gas after the deoxidation is delivered to the PSA device and is carried out methane and concentrate after dedusting, cooling.Reactor adopts fixed-bed reactor, because the reaction heat of oxidizing reaction is bigger, liberated heat can produce steam output by waste heat boiler.
Embodiment 1
Unstripped gas is formed: CH
450%, N
240%, O
210%.Adopt calcium titanium type O composite metallic oxide catalyst, 450 ℃ of temperature of reaction, pressure is greater than normal pressure, air speed 10000h
-1Coal mine gas after the deoxidation is formed (percent by volume, butt):
CH
450%, N
244.4%, CO
24.9%, O
2Content is no more than 1%.
Oxygen removal rate＞90%.
Embodiment 2
Unstripped gas is formed with 1, adopts palladium (or platinum) catalyzer, 250 ℃ of temperature of reaction, and pressure is greater than normal pressure, air speed 5000h
-1Coal mine gas after the deoxidation consists of:
CH
449.5%, N
244%, CO
23.7%, CO1.8%, O
2Be no more than 1%.
Oxygen removal rate＞90%.
Coal mine gas after embodiment 1 and 2 deoxygenations is finished further concentrating of methane gas again in follow-up common process, the oxygen concentration in the discharging gas that is produced reduces greatly, is lower than the oxygen concn that detonates, thereby the safety that has guaranteed production is carried out.
Claims (5)
1, produces the catalyticcombustion deoxidization process of methyl alcohol with coal mine mash gas, methane in the coal mine mash gas is concentrated the raw material of back as methanol production, before the methane concentration operation, coal mine mash gas is carried out the catalyticcombustion deoxidation through catalyzer, make oxygen concn in the coal mine gas less than 1%, after recovery of heat-cooling-water sepn, enter methane concentration operation then again.
2, use the catalyticcombustion deoxidization process of coal mine mash gas according to the described production methyl alcohol of claim 1, it is characterized in that the catalyst combustion reaction temperature is 200-500 ℃, reaction pressure is greater than normal pressure, and reaction velocity is 5000-10000h
-1
3, use the catalyticcombustion deoxidization process of coal mine mash gas according to the described production methyl alcohol of claim 1, it is characterized in that described catalyzer can be noble metal catalyst, also can be non-metallic catalyst.
4, use the catalyticcombustion deoxidization process of coal mine mash gas according to the described production methyl alcohol of claim 1, it is characterized in that described noble metal catalyst is palladium catalyst or platinum catalyst.
5, use the catalyticcombustion deoxidization process of coal mine mash gas according to the described production methyl alcohol of claim 1, it is characterized in that described non-metallic catalyst is a calcium titanium type O composite metallic oxide catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021136289A CN1330739C (en) | 2002-04-18 | 2002-04-18 | Catalytic combusticon dehydrogenation process of mine gas for producing methyl alcohol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021136289A CN1330739C (en) | 2002-04-18 | 2002-04-18 | Catalytic combusticon dehydrogenation process of mine gas for producing methyl alcohol |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1495247A true CN1495247A (en) | 2004-05-12 |
| CN1330739C CN1330739C (en) | 2007-08-08 |
Family
ID=34231125
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021136289A Expired - Lifetime CN1330739C (en) | 2002-04-18 | 2002-04-18 | Catalytic combusticon dehydrogenation process of mine gas for producing methyl alcohol |
Country Status (1)
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| CN (1) | CN1330739C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101591579A (en) * | 2009-05-13 | 2009-12-02 | 赵昱 | Method for deoxidizing and concentrating mine gas |
| CN101139239B (en) * | 2007-09-06 | 2010-04-14 | 西南化工研究设计院 | Sulfur-resistant catalytic deoxidization process for methane-rich gas |
| CN101878285A (en) * | 2007-07-25 | 2010-11-03 | 大阪瓦斯株式会社 | System for processing combustible gas and method for processing combustible gas |
| WO2011009283A1 (en) * | 2009-07-23 | 2011-01-27 | 中国科学院大连化学物理研究所 | Catalyst for deoxidation of coalbed gas, preparation method and use thereof |
| CN101423783B (en) * | 2008-12-10 | 2011-10-26 | 西南化工研究设计院 | Mixture gas catalytic deoxidation process containing combustible gas |
| CN102433185A (en) * | 2010-09-29 | 2012-05-02 | 中国石油化工股份有限公司 | Catalytic deoxidation method for coalbed gas in coal mine area |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8803766D0 (en) * | 1988-02-18 | 1988-03-16 | Ici Plc | Methanol |
-
2002
- 2002-04-18 CN CNB021136289A patent/CN1330739C/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101878285A (en) * | 2007-07-25 | 2010-11-03 | 大阪瓦斯株式会社 | System for processing combustible gas and method for processing combustible gas |
| US8899968B2 (en) | 2007-07-25 | 2014-12-02 | Osaka Gas Co., Ltd. | Combustible gas processing system and combustible gas processing method |
| CN101139239B (en) * | 2007-09-06 | 2010-04-14 | 西南化工研究设计院 | Sulfur-resistant catalytic deoxidization process for methane-rich gas |
| CN101423783B (en) * | 2008-12-10 | 2011-10-26 | 西南化工研究设计院 | Mixture gas catalytic deoxidation process containing combustible gas |
| CN101591579A (en) * | 2009-05-13 | 2009-12-02 | 赵昱 | Method for deoxidizing and concentrating mine gas |
| CN101591579B (en) * | 2009-05-13 | 2014-08-06 | 赵昱 | Method for deoxidizing and concentrating mine gas |
| WO2011009283A1 (en) * | 2009-07-23 | 2011-01-27 | 中国科学院大连化学物理研究所 | Catalyst for deoxidation of coalbed gas, preparation method and use thereof |
| CN102433185A (en) * | 2010-09-29 | 2012-05-02 | 中国石油化工股份有限公司 | Catalytic deoxidation method for coalbed gas in coal mine area |
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| Publication number | Publication date |
|---|---|
| CN1330739C (en) | 2007-08-08 |
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Owner name: SOUTHWEST RESEARCH + DESIGN INSTITUTE OF CHEMICAL Free format text: FORMER NAME: SOUTHWEST RESEARCH + DESIGN INSTITUTE OF CHEMICAL INDUSTRY |
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Address after: 610255 box 445, South Airport Road, Sichuan, Chengdu, Chengdu Patentee after: Southwest Chemical Research & Design Institute Co., Ltd. Address before: 610255 box 445, South Airport Road, Sichuan, Chengdu, Chengdu Patentee before: Xinan Chemical Research & Design Inst. |
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Effective date of registration: 20191217 Address after: 611430 No.777, Xinghua 10th Road, dengshuang Town, Xinjin County, Chengdu City, Sichuan Province (Industrial Park) Patentee after: Haohua (Chengdu) Technology Co., Ltd. Address before: 610255 box 445, South Airport Road, Sichuan, Chengdu, Chengdu Patentee before: Southwest Chemical Research & Design Institute Co., Ltd. |
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Granted publication date: 20070808 |