CN2420272Y - Integrated two phase anaerobe treatment reactor - Google Patents
Integrated two phase anaerobe treatment reactor Download PDFInfo
- Publication number
- CN2420272Y CN2420272Y CN00206243U CN00206243U CN2420272Y CN 2420272 Y CN2420272 Y CN 2420272Y CN 00206243 U CN00206243 U CN 00206243U CN 00206243 U CN00206243 U CN 00206243U CN 2420272 Y CN2420272 Y CN 2420272Y
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- phase
- reactor
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- integrated
- biological treatment
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to an integrated two-phase anaerobe treatment reactor. The space in the reactor can be organically divided into an acid producing phase biological treatment reaction zone, a two-phase anaerobic transition zone, a methane producing phase biological treatment reaction zone, a sludge-water separation zone, a gas-phase zone, etc. by using a plurality of groups of multiform sleeve barrels, and consequently, so the goal of the integration of two-phase anaerobe equipment can be realized. The integrated two-phase anaerobe treatment reactor has the advantages of simple management, simple operation, high treatment efficiency, small volume, small occupation of land and engineering cost reduction, which is especially suitable for the popularization and the application of high concentrated organic wastewater treating engineering of middle and small size.
Description
The utility model is a biological wastewater treatment technology.
Distinguishing features such as the diphasic anaerobic biological treatment is the treatment system of at present more advanced high-concentration organic industrial waste water, has the processing efficiency height, and is stable.But the equipment many (comprise and produce sour phase biological treatment reactor and produce methane biological treatment reactor mutually) that this technology is required, for medium and small waste water treatment engineering, because many, the operational administrative more complicated of device category, equipment thermosteresis are relatively large, cause processing efficiency to reduce, construction costs is higher.
On middle-size and small-size waste water treatment engineering, use all deficiencies that exist in view of existing diphasic anaerobic technique, the objective of the invention is to design a kind of integrated two-phase anaerobic biological treatment reactor, this reactor is fully to grasp product acid phase and producing under methane optimum process condition, ecological condition and the volume proportioning condition mutually, reasonable combination by process structure realizes the incorporate purpose of diphasic anaerobic equipment, thereby makes this reactor have distinguishing features such as simple to operate, that processing efficiency is high, construction costs is low.
According to design, the utility model structurally adopts the sleeve array configuration, adopt various forms of many group sleeves that the space in the reactor organically is divided into and produce sour phase reaction district, diphasic anaerobic zone of transition, produce methane phase reaction district, mud-water separation district, gas phase zone etc., thereby make this reactor have diphasic anaerobic biological treatment function.
In order to implement the present invention, provide the utility model most preferred embodiment below in conjunction with accompanying drawing.
Accompanying drawing 1 integrated diphasic anaerobic biological treatment reactor sectional view.
Accompanying drawing 2 integrated diphasic anaerobic biological treatment reactor 1-1 sectional views.
Shown in accompanying drawing 1, accompanying drawing 2, be the sour phase reaction of product district in the inner core 1 of integrated two-phase anaerobic biological treatment reactor, by the umbrella shape pod 4 that has airway 5 this district is divided into two portions up and down in this district, the bottom is for mixing reaction zone 19 fully, in be provided with water inlet pipe 7, jet agitator 8, the bottom is provided with blow-down pipe 9; Top is settling section 20; Be the diphasic anaerobic zone of transition between inner core 1 and the inner core 2; Be product methane phase reaction district between inner core 2 and the outer wall tube 3, by guide shell 10 this is divided into upper and lower two portions in this district, the bottom is for producing methane anaerobic reaction district 21, in filler 11 is housed, the bottom is provided with blow-down pipe 12 and shore pipe 13, top is muddy water depositing separation area 22, is provided with scum board 15, effluent trough 14 and rising pipe 16 in the district; The reactor upper end is a gas phase zone 6, and roof is provided with vapor pipe 17.For the ease of the inside reactor maintenance, on reactor outer wall tube 3, be provided with some access openings 18.
Implement the utility model, former water is entered through jet agitator 8 by water inlet pipe 7 and mixes reaction zone 19 fully, former water and bottom mud thorough mixing reaction under the powerful stirring action of jet agitator 8, the gas that is generated is collected after airway 5 enters in the gas phase zone 6 by umbrella pod 4.Reacted liter waterborne is walked around pod 4 and is entered Cheng Qing district, top 20, sedimentary mud is then collected by pod 4 and is back to bottom participation reaction, supernatant liquor then enters from the bottom through the diphasic anaerobic zone of transition between inner core 1, the inner core 2 and produces in the methane anaerobic reaction district 21 and the microbial film mixing and contacting reaction on mud and the filler 11, the methane gas that is produced is collected by guide shell 10 and is entered gas phase zone 6, and reacted water then rises and walks around guide shell 10 and enter mud-water separation settling region 22.The sedimentary mud of institute is collected to pass back into by guide shell 10 again and is produced methane anaerobic reaction district 21.Do not precipitate the scum silica frost that floats on the depositing separation area surface and then be retained in the surface by scum board 15, clear water then enters effluent trough 14, is discharged by rising pipe 16.And the collection and confinement of gases that diphasic anaerobic reaction is produced is in gas phase zone 6, discharged and is used by the vapor pipe 17 of roof.
Because the utility model has been realized the incorporate purpose of diphasic anaerobic biological treating equipment, make not only that equipment operation management is simple, processing efficiency is high, and because equipment volume is little, it is little to take up an area of, thereby whole construction costs is obviously reduced, very help the promotion and application of middle-size and small-size high concentrated organic wastewater engineering.
Claims (6)
1. integrated two-phase anaerobic biological treatment reactor, it is characterized in that, this reactor is telescopic unitized construction, space in the reactor organically is divided into the zone of difference in functionality by multi-form sleeve, wherein be the sour phase reaction of product district in the inner core 1, by umbrella shape pod 4 this is divided into two portions up and down in this district, the bottom is for mixing reaction zone 19 fully, and top is settling section 20; Be the diphasic anaerobic zone of transition between inner core 1 and the inner core 2; For producing methane phase reaction district, by guide shell 10 this is divided into upper and lower two portions in this district between inner core 2 and the outer wall tube 3, the bottom is for producing methane anaerobic reaction district 21, and top is muddy water depositing separation area 22; The reactor upper end is a gas phase zone 6.
2. integrated two-phase anaerobic biological treatment reactor as claimed in claim 1 is characterized in that mixing fully in umbrella shape pod 4 bottoms and is provided with water inlet pipe 7 and jet agitator 8 in the reaction zone 19, and the bottom is provided with blow-down pipe 9.
3. as claim 1,2 described integrated two-phase anaerobic biological treatment reactors, it is characterized in that the said airway 5 that on umbrella shape pod 4, has.
4. integrated two-phase anaerobic biological treatment reactor as claimed in claim 1 is characterized in that in the product methane anaerobic reaction district, said guide shell 10 bottoms 21 filler 11 bottoms being housed is provided with blow-down pipe 12 and shore pipe 13.
5. as claim 1,4 described integrated two-phase anaerobic biological treatment reactors, it is characterized in that being provided with scum board 15, effluent trough 14 and rising pipe 16 in the mud-water separation district, said guide shell 10 top 22.
6. integrated two-phase anaerobic biological treatment reactor as claimed in claim 1 is characterized in that the roof of said gas phase zone 6 is provided with vapor pipe 17.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN00206243U CN2420272Y (en) | 2000-03-11 | 2000-03-11 | Integrated two phase anaerobe treatment reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN00206243U CN2420272Y (en) | 2000-03-11 | 2000-03-11 | Integrated two phase anaerobe treatment reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2420272Y true CN2420272Y (en) | 2001-02-21 |
Family
ID=33574229
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN00206243U Expired - Fee Related CN2420272Y (en) | 2000-03-11 | 2000-03-11 | Integrated two phase anaerobe treatment reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2420272Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102115258A (en) * | 2011-04-08 | 2011-07-06 | 中国人民解放军后勤工程学院 | Two-phase integrated anaerobic reactor |
| CN102153196A (en) * | 2011-04-08 | 2011-08-17 | 中国人民解放军后勤工程学院 | Heating type integrated sewage treatment device |
| CN103086505A (en) * | 2013-01-28 | 2013-05-08 | 苏州科技学院 | Device and method for strengthening impact resisting load of anaerobic treatment wastewater |
| CN103253765A (en) * | 2006-11-27 | 2013-08-21 | Dvo公司 | Method and apparatus for anaerobic digestion of organic liquid waste stream |
| CN108726828A (en) * | 2018-08-15 | 2018-11-02 | 四川达沃斯生态环保科技股份有限公司 | A kind of organic matter anaerobic reactor |
-
2000
- 2000-03-11 CN CN00206243U patent/CN2420272Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103253765A (en) * | 2006-11-27 | 2013-08-21 | Dvo公司 | Method and apparatus for anaerobic digestion of organic liquid waste stream |
| CN102115258A (en) * | 2011-04-08 | 2011-07-06 | 中国人民解放军后勤工程学院 | Two-phase integrated anaerobic reactor |
| CN102153196A (en) * | 2011-04-08 | 2011-08-17 | 中国人民解放军后勤工程学院 | Heating type integrated sewage treatment device |
| CN102153196B (en) * | 2011-04-08 | 2012-07-25 | 中国人民解放军后勤工程学院 | Heating type integrated sewage treatment device |
| CN103086505A (en) * | 2013-01-28 | 2013-05-08 | 苏州科技学院 | Device and method for strengthening impact resisting load of anaerobic treatment wastewater |
| CN103086505B (en) * | 2013-01-28 | 2014-10-08 | 苏州科技学院 | Device and method for strengthening impact resisting load of anaerobic treatment wastewater |
| CN108726828A (en) * | 2018-08-15 | 2018-11-02 | 四川达沃斯生态环保科技股份有限公司 | A kind of organic matter anaerobic reactor |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |