CN204727858U - The pure biological flue gas equipment of a kind of marsh gas water elution - Google Patents
The pure biological flue gas equipment of a kind of marsh gas water elution Download PDFInfo
- Publication number
- CN204727858U CN204727858U CN201520342189.2U CN201520342189U CN204727858U CN 204727858 U CN204727858 U CN 204727858U CN 201520342189 U CN201520342189 U CN 201520342189U CN 204727858 U CN204727858 U CN 204727858U
- Authority
- CN
- China
- Prior art keywords
- tourie
- communicating pipe
- vacuum pump
- flue gas
- water elution
- 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.)
- Expired - Fee Related
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model proposes the pure biological flue gas equipment of a kind of marsh gas water elution, comprise tourie, tourie upper end is respectively arranged with vacuum pump and roots blower, roots blower is connected with tourie by reversing valve, vacuum pump is connected with described tourie by communicating pipe a, and the communicating pipe a be connected with described vacuum pump passes into the top of described tourie inside.Reversing valve is connected with described scavenging air receiver by communicating pipe b, and the communicating pipe b the other end be connected with described reversing valve is provided with aerator, and described aerator is arranged on the lower inside of described tourie.Biogas output channel is provided with above tourie.The utility model improves the level of automation of conventional pressure WATER-WASHING METHOD, reduce the energy consumption in carbon rejection process thus reduce cost, and working efficiency is high, good purification.
Description
Technical field
The utility model relates to a kind of equipment for purifying, refers to the pure biological flue gas equipment of a kind of marsh gas water elution especially.
Background technology
The main component of biogas is methane and carbon dioxide, and carbon dioxide content, greatly about 25% ~ 40%, seriously reduces the calorific value of biogas, thus limits the scope of application of biogas as renewable energy source.For improving calorific value and the utility value of biogas, we need to carry out carbonization treatment to biogas.Current marsh gas purifying carbonization treatment method mainly contains pressure swing adsorption process, chemiadsorption, pressure WATER-WASHING METHOD.Pressure swing adsorption process is the separating-purifying being realized gas by pressure change in time, and chemical absorption method is the purification & isolation spatially being realized gas by temperature variation, and pressure WATER-WASHING METHOD is the purification & isolation spatially being realized gas by the change of pressure.The most frequently used is pressure WATER-WASHING METHOD at present, and this method requires that level of automation is low, and facility investment is lower, and major equipment is Marsh gas compression machine and high-pressure hydraulic pump, and relative power consumption is comparatively large, is not too applicable to small-sized methane engineering.Therefore need a kind of energy consumption little, cost equipment low and applied widely solves the problems referred to above.The utility model provides a kind of Low investment, and the marsh gas water of less energy-consumption washes equipment for purifying, solves the problem.
Utility model content
The utility model proposes the pure biological flue gas equipment of a kind of marsh gas water elution, provide a kind of Low investment, the marsh gas water of less energy-consumption is washed equipment for purifying and is solved the problems referred to above.
The utility model is the pure biological flue gas equipment of a kind of marsh gas water elution,
Comprise tourie, described tourie upper end is respectively arranged with vacuum pump and roots blower,
Described vacuum pump is connected with described tourie by communicating pipe a, and described communicating pipe a passes into described tourie inner upper;
Described roots blower is connected with described tourie by communicating pipe b, and described communicating pipe b is provided with reversing valve.
As preferred technical scheme, the other end that described communicating pipe b passes into described tourie is provided with aerator, and described aerator is positioned at the lower inside of described tourie.
As preferred technical scheme, above described tourie, be provided with biogas output channel.
As preferred technical scheme, described roots blower adopts explosion-proof type roots blower.
As preferred technical scheme, described vacuum pump adopts water-ring vacuum pump.
Principle of work of the present utility model is the difference utilizing carbonic acid gas and methane solubleness in water, improves the methane concentration in gas product, then utilizes biogas different with the dividing potential drop of Carbon Dioxide in Air, realize the object of carbon dioxide separation.
During work, biogas is by entering the aerator bottom tourie after roots blower supercharging, form micro-bubble and enter tourie, bubble is in uphill process, carbonic acid gas dissolves gradually, thus improve the quality of biogas, along with time lapse, after the carbonic acid gas dissolved in water reaches finite concentration, carbon dioxide absorption reduced capability, in gas product, gas concentration lwevel rises gradually, at this moment entering of biogas is cut off, change vacuum pump into and suction vacuum operating is carried out to tourie, aerator communicating pipe b is by reversing valve and air communication simultaneously, because tourie internal pressure is low, air enters aerator through communicating pipe b and forms micro-bubble, fully contact with the carbon dioxide enriched aqueous solution, because pressure reduces, carbonic acid gas is parsed in a large number, when in water during gas concentration lwevel access expansion content, again pass into biogas, so repeatedly carry out.Can arrange that multiple devices recycle according to methane quantity and treatment time difference, to complete the continuity of methane purification.Vacuum pump inspiratory capacity is preferably 2 ~ 3 times for roots blower air quantity.Tourie height is preferably 5 ~ 10m, and select roots blower and the vacuum pump pump of convenient pressure according to tourie height, absorption tower water capacity is preferably 2 ~ 3 times of biogas treatment amount, and the bubble diameter of aerator gas explosion is preferably less than or equal to 2.5mm.
Owing to have employed technique scheme, the pure biological flue gas equipment of a kind of marsh gas water elution, utilizes the difference of carbonic acid gas and methane solubleness in water, improves the methane concentration in gas product, then utilize biogas different with the dividing potential drop of Carbon Dioxide in Air, realize the object of carbon dioxide separation.The utility model improves the level of automation of conventional pressure WATER-WASHING METHOD, reduce the energy consumption in carbon rejection process thus reduce cost, and working efficiency is high, good purification.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is a kind of marsh gas water elution pure biological flue gas device structure schematic diagram of the utility model embodiment;
In figure: 1-tourie; 2-aerator; 3-vacuum pump; 4-roots blower; 5-reversing valve; 6-communicating pipe b.
Embodiment
In order to further illustrate the utility model, be described below in conjunction with accompanying drawing:
Embodiment:
As shown in Figure 1, the utility model is the pure biological flue gas equipment of a kind of marsh gas water elution, comprise tourie 1, tourie 1 upper end is respectively arranged with water-ring vacuum pump 3 and explosion-proof type roots blower 4, explosion-proof type roots blower 4 is connected with tourie 1 by reversing valve 5, vacuum pump 3 is connected with tourie 1 by communicating pipe a, and the communicating pipe a be connected with vacuum pump 3 passes into the top of tourie 1 inside.Reversing valve 5 is connected with scavenging air receiver by communicating pipe b6, and the communicating pipe b6 the other end be connected with reversing valve 5 is provided with aerator 2, and aerator 2 is arranged on the lower inside of tourie 1.Biogas output channel is provided with above described tourie.
During work, the aerator 2 of biogas by entering bottom tourie 1 after roots blower 4 supercharging, form micro-bubble and enter tourie 1, bubble is in uphill process, carbonic acid gas dissolves gradually, thus improve the quality of biogas, along with time lapse, after the carbonic acid gas dissolved in water reaches finite concentration, carbon dioxide absorption reduced capability, in gas product, gas concentration lwevel rises gradually, at this moment entering of biogas is cut off, change vacuum pump 3 pairs of touries 1 into and carry out suction vacuum operating, aerator 2 communicating pipe b6 is by reversing valve 5 and air communication simultaneously, because tourie internal pressure is low, air enters aerator 2 through communicating pipe b6 and forms micro-bubble, fully contact with the carbon dioxide enriched aqueous solution, because pressure reduces, carbonic acid gas is parsed in a large number, when in water during gas concentration lwevel access expansion content, again pass into biogas, so repeatedly carry out.Can arrange that multiple devices recycle according to methane quantity and treatment time difference, to complete the continuity of methane purification.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. the pure biological flue gas equipment of marsh gas water elution, is characterized in that:
Comprise tourie, described tourie upper end is respectively arranged with vacuum pump and roots blower,
Described vacuum pump is connected with described tourie by communicating pipe a, and described communicating pipe a passes into described tourie inner upper;
Described roots blower is connected with described tourie by communicating pipe b, and described communicating pipe b is provided with reversing valve.
2. the pure biological flue gas equipment of a kind of marsh gas water elution as claimed in claim 1, is characterized in that:
The other end that described communicating pipe b passes into described tourie is provided with aerator, and described aerator is positioned at the lower inside of described tourie.
3. the pure biological flue gas equipment of a kind of marsh gas water elution as claimed in claim 2, is characterized in that:
Biogas output channel is provided with above described tourie.
4. the pure biological flue gas equipment of a kind of marsh gas water elution as claimed in claim 3, is characterized in that:
Described roots blower adopts explosion-proof type roots blower.
5. the pure biological flue gas equipment of a kind of marsh gas water elution as claimed in claim 4, is characterized in that:
Described vacuum pump adopts water-ring vacuum pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520342189.2U CN204727858U (en) | 2015-05-25 | 2015-05-25 | The pure biological flue gas equipment of a kind of marsh gas water elution |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520342189.2U CN204727858U (en) | 2015-05-25 | 2015-05-25 | The pure biological flue gas equipment of a kind of marsh gas water elution |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204727858U true CN204727858U (en) | 2015-10-28 |
Family
ID=54386222
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520342189.2U Expired - Fee Related CN204727858U (en) | 2015-05-25 | 2015-05-25 | The pure biological flue gas equipment of a kind of marsh gas water elution |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204727858U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861371A (en) * | 2017-03-22 | 2017-06-20 | 常熟理工学院 | A kind of biogas pressure-variable adsorption tower apparatus |
CN109628182A (en) * | 2018-11-28 | 2019-04-16 | 安徽天马环保装备有限公司 | A kind of biogas pressure washing method of purification and system |
-
2015
- 2015-05-25 CN CN201520342189.2U patent/CN204727858U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861371A (en) * | 2017-03-22 | 2017-06-20 | 常熟理工学院 | A kind of biogas pressure-variable adsorption tower apparatus |
CN109628182A (en) * | 2018-11-28 | 2019-04-16 | 安徽天马环保装备有限公司 | A kind of biogas pressure washing method of purification and system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110052123B (en) | Integrated device for removing carbon dioxide gas in gas | |
CN204727858U (en) | The pure biological flue gas equipment of a kind of marsh gas water elution | |
CN101724479B (en) | Method for pressure swing adsorption and concentration of methane | |
CN103031170A (en) | Production method for concentrating low-concentration gas to prepare LNG (liquefied natural gas) | |
CN202343087U (en) | Efficient waste gas neutralizing tower | |
CN106497620B (en) | Biogas purification and biogas slurry treatment system and method with biogas slurry as CO2 absorbent | |
CN204589317U (en) | Water electrolysis prepares pure hydrogen system | |
CN203212538U (en) | Methane separation and purification device | |
CN103113947A (en) | Methane separation and purification device and method thereof for purifying methane by absorbing CO2 through alkaline method | |
CN205024189U (en) | Decarbonization device of biological natural gas of marsh gas preparation | |
CN204111314U (en) | Small-sized three-tower structure molecular-sieve oxygen generator | |
CN203976745U (en) | Multitower series-parallel connection circulation amine absorption device | |
CN106119091A (en) | A kind of methane purification and canned system and technique | |
CN203525539U (en) | Decarbonization device for preparing biogas from methane | |
CN114917716A (en) | Spiral adsorption tower structure and process method for gas purification of biomass derived gas | |
CN210584487U (en) | Low-temperature methanol washing hydrogen sulfide treatment device | |
CN101104824A (en) | Method and device for producing synthetic natural gas from organic waste water | |
CN212383460U (en) | Treatment system for absorbing tail gas sulfur dioxide gas | |
CN204563876U (en) | A kind of device of carbon black tail gas gas separaion | |
CN201445894U (en) | Device capable of pressure swing absorption, decarbonization, pressure release and recovery | |
CN201295586Y (en) | Resource device for methane power generation gas | |
CN204411771U (en) | Tail acid gathering-device in isoleucine leaching process | |
CN205687915U (en) | A kind of methane purification and canned system | |
CN203976742U (en) | A kind of marsh gas purifying is processed compressed natural gas processed and is become skid to put | |
CN204395730U (en) | A kind of process system of flue gas combined desulfurization decarburization |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151028 Termination date: 20170525 |