CN204237619U - A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor - Google Patents
A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor Download PDFInfo
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- CN204237619U CN204237619U CN201420704286.7U CN201420704286U CN204237619U CN 204237619 U CN204237619 U CN 204237619U CN 201420704286 U CN201420704286 U CN 201420704286U CN 204237619 U CN204237619 U CN 204237619U
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- water
- water distributor
- anaerobic reactor
- return line
- organic wastewater
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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
A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor, comprise tank body, it is characterized in that tank base is provided with water distributor, water distributor upper end is provided with two-layer triphase separator, tank body outside top is provided with steam separator, described steam separator is provided with two groups of biogas-lift pipes, described two groups of biogas-lift pipes are connected on the venting port of tank interior two groups of triphase separators respectively, described steam separator is also provided with return line I, the other end of return line is connected to water distributor top water-in, described steam separator top is also provided with air shooter, described air shooter is provided with liquid packing, the utility model is by improving the structure of anaerobic reactor, the transformation efficiency of anaerobic reactor is improved, simultaneously efficient produced biogas to be reclaimed, increase the generation of anaerobic grain sludge, add the processing efficiency of high concentrated organic wastewater, and decrease running cost.
Description
Technical field
The utility model relates to a kind of energy-efficient high concentrated organic wastewater process anaerobic reactor, is specifically related to a kind of efficient, the rate of recovery is high, energy consumption is low a kind of high concentrated organic wastewater process anaerobic reactor.
Background technology
At present, biogas engineering is widelyd popularize as the environmental protection project of state key support, and provide policy to support, biogas engineering not only effectively can reduce the discharge of methane gas, methane conversion can also be become the gas of second stage employ, achieve second stage employ, namely decrease the generation of the Greenhouse effect attracted attention in the whole world, turn increase economic benefit.
Organic waste water is made to produce methane, anaerobic reactor must be needed, but existing anaerobic reactor unreasonable structure causes, lowly, cost of investment is greater than income sometimes, therefore causes enthusiasm not high for methane generation or transformation efficiency, trace it to its cause, namely because the unreasonable structure of anaerobic reactor causes, therefore, be necessary to improve anaerobic reactor.
Summary of the invention
In order to solve prior art problem, the utility model is by improving the structure of anaerobic reactor, the transformation efficiency of anaerobic reactor is improved, simultaneously efficient produced biogas to be reclaimed, increase the generation of anaerobic grain sludge, add the processing efficiency of high concentrated organic wastewater, and decrease running cost.
For achieving the above object, the present invention is by the following technical solutions: a kind of energy-efficient high concentrated organic wastewater process anaerobic reactor, comprise tank body, it is characterized in that tank base is provided with water distributor, water distributor upper end is provided with two-layer triphase separator, tank body outside top is provided with steam separator, described steam separator is provided with two groups of biogas-lift pipes, described two groups of biogas-lift pipes are connected on the venting port of tank interior two groups of triphase separators respectively, described steam separator is also provided with return line I, the other end of return line is connected to water distributor top water-in, described steam separator top is also provided with air shooter, described air shooter is provided with liquid packing.
Further, tank body is also provided with water inlet pipe and return line II, one end of described return line II is connected to the water outlet of triphase separator, the other end is connected on water inlet pipe, the other end of water inlet pipe is connected on the water-in of water distributor, the water inlet pipe between return line II and water distributor water-in is also provided with point water bag and a under meter.
Further, described water distributor is whirlwind-type water distributor.
Further, the water inlet pipe between water bag and water distributor is divided to be at least two.
Compared with prior art, the present invention has following beneficial effect: 1, by arranging two-layer triphase separator, the efficiency that biogas is produced improves greatly, sewage is after the process of the first layer triphase separator, sometimes transform still incomplete, therefore, increase second layer triphase separator and do further conversion processing, 2, by arranging return line I between steam separator and water distributor, biogas-lift pipe is set between steam separator and triphase separator, make between steam separator and water distributor, to produce elevation pressure reduction, now by after the water in steam separator is squeezed into water distributor, Water circulation hydrodynamics in water distributor is strengthened, thus increase the generation of anaerobic sludge particle, thus be that the generation of the first beneficial effect provides strong support, 3, by arranging return line II between triphase separator and water distributor, make the effluent cycle in triphase separator more thorough, thus increase methane content, 4, by making the water inlet pipe point between water bag and water distributor be more than two, therefore, this water inlet pipe and return tank I combine and produce Water circulation hydrodynamics, the beneficial effects such as to sum up after three beneficial effects, the utility model produces efficiently, running cost reduction.
Accompanying drawing explanation
For being described further the utility model, below in conjunction with the drawings and specific embodiments, technical scheme provided by the utility model is described further.
A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor structural representation of Fig. 1.
In figure, triphase separator 1, steam separator 2, biogas-lift pipe 3, return line I4, liquid packing 5, return line II6, point water bag 7, under meter 8, water distributor 9, water inlet pipe 10.
Embodiment
As shown in Figure 1, a kind of energy-efficient high concentrated organic wastewater process anaerobic reactor, comprise tank body, it is characterized in that tank base is provided with water distributor 9, water distributor 9 upper end is provided with two-layer triphase separator 1, tank body outside top is provided with steam separator 2, described steam separator 2 is provided with two groups of biogas-lift pipes 3, described two groups of biogas-lift pipes 3 are connected on the venting port of tank interior two groups of triphase separators 1 respectively, described steam separator 2 is also provided with return line I4, the other end of return line I4 is connected to water distributor 9 top water-in, described steam separator 2 top is also provided with air shooter, described air shooter is provided with liquid packing 5.
Further, tank body is also provided with water inlet pipe and return line II6, one end of described return line II6 is connected to the water outlet of triphase separator 1, the other end is connected on water inlet pipe 10, the other end of water inlet pipe 10 is connected on the water-in of water distributor 9, and the water inlet pipe 10 between return line II6 and water distributor 9 water-in is also provided with point water bag 7 and under meter 8.
Further, described water distributor 9 is whirlwind-type water distributor.
Further, the water inlet pipe 10 between water bag 7 and water distributor 9 is divided to be at least two.
Obviously; above-mentioned embodiment is only better embodiment of the present utility model; the apparent technical scheme that can obtain except the utility model embodiment of those skilled in the art, therefore any simple modifications on the utility model basis all belongs to protection domain of the present utility model.
Claims (4)
1. an energy-efficient high concentrated organic wastewater process anaerobic reactor, comprise tank body, it is characterized in that tank base is provided with water distributor, water distributor upper end is provided with two-layer triphase separator, tank body outside top is provided with steam separator, described steam separator is provided with two groups of biogas-lift pipes, described two groups of biogas-lift pipes are connected on the venting port of tank interior two groups of triphase separators respectively, described steam separator is also provided with return line I, the other end of return line is connected to water distributor top water-in, described steam separator top is also provided with air shooter, described air shooter is provided with liquid packing.
2. one according to claim 1 energy-efficient high concentrated organic wastewater process anaerobic reactor, it is characterized in that tank body being also provided with water inlet pipe and return line II, one end of described return line II is connected to the water outlet of triphase separator, the other end is connected on water inlet pipe, the other end of water inlet pipe is connected on the water-in of water distributor, the water inlet pipe between return line II and water distributor water-in is also provided with point water bag and a under meter.
3. one according to claim 1 energy-efficient high concentrated organic wastewater process anaerobic reactor, is characterized in that described water distributor is whirlwind-type water distributor.
4. one according to claim 1 energy-efficient high concentrated organic wastewater process anaerobic reactor, is characterized in that the water inlet pipe point between water bag and water distributor is at least two.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420704286.7U CN204237619U (en) | 2014-11-21 | 2014-11-21 | A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420704286.7U CN204237619U (en) | 2014-11-21 | 2014-11-21 | A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor |
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| CN204237619U true CN204237619U (en) | 2015-04-01 |
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| CN201420704286.7U Expired - Fee Related CN204237619U (en) | 2014-11-21 | 2014-11-21 | A kind of energy-efficient high concentrated organic wastewater process anaerobic reactor |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105110563A (en) * | 2015-08-31 | 2015-12-02 | 南京大学 | Two-phase double-circulation anaerobic device for treating sulfate organic wastewater and treating method |
| CN106495411A (en) * | 2016-12-09 | 2017-03-15 | 南京大善环境科技有限公司 | Wastewater treatment ICBB technique and device in Ginkgo Biloba Extract extraction process |
| CN110316819A (en) * | 2019-06-21 | 2019-10-11 | 广西博世科环保科技股份有限公司 | A kind of high concentrated organic wastewater treatment reactor |
| CN111439833A (en) * | 2020-05-06 | 2020-07-24 | 山东双融环保工程有限公司 | Multilayer automatic internal circulation SRIC anaerobic reactor |
-
2014
- 2014-11-21 CN CN201420704286.7U patent/CN204237619U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105110563A (en) * | 2015-08-31 | 2015-12-02 | 南京大学 | Two-phase double-circulation anaerobic device for treating sulfate organic wastewater and treating method |
| CN106495411A (en) * | 2016-12-09 | 2017-03-15 | 南京大善环境科技有限公司 | Wastewater treatment ICBB technique and device in Ginkgo Biloba Extract extraction process |
| CN106495411B (en) * | 2016-12-09 | 2019-10-22 | 南京大善环境科技有限公司 | Wastewater treatment ICBB technique and device in ginkgo biloba p.e extraction process |
| CN110316819A (en) * | 2019-06-21 | 2019-10-11 | 广西博世科环保科技股份有限公司 | A kind of high concentrated organic wastewater treatment reactor |
| WO2020252819A1 (en) * | 2019-06-21 | 2020-12-24 | 广西博世科环保科技股份有限公司 | High-concentration organic wastewater treatment reactor |
| CN111439833A (en) * | 2020-05-06 | 2020-07-24 | 山东双融环保工程有限公司 | Multilayer automatic internal circulation SRIC anaerobic reactor |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: Industrial Road Licheng District, Ji'nan city of Shandong province 250000 No. 88 East International Plaza Building 4, room 2303 Patentee after: Shandong Shuang Rong Environmental Protection Engineering Co.,Ltd. Address before: Room 206, No. 173, industrial North Road, Ji'nan City, Shandong, Shandong Patentee before: Jinan Shuangrong Environmental Protection Engineering Co.,Ltd. |
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| 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: 20150401 Termination date: 20211121 |