CN101054234B - Upflow type anaerobic reactor - Google Patents
Upflow type anaerobic reactor Download PDFInfo
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- CN101054234B CN101054234B CN200710061817XA CN200710061817A CN101054234B CN 101054234 B CN101054234 B CN 101054234B CN 200710061817X A CN200710061817X A CN 200710061817XA CN 200710061817 A CN200710061817 A CN 200710061817A CN 101054234 B CN101054234 B CN 101054234B
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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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Abstract
The invention relates to an up flow type anaerobic reactor, which comprises a barrel of the reactor, a water distributor pipe arranged on the lower end of the barrel, a three phase separator composed of a cone diversion drum arranged on the upper end of the barrel and a gas hood arranged on the upper end of the cone diversion drum, a circular passage arranged between the lower end of the gas hoodwall and cone diversion drum wall, a circular passage arranged between the cone diversion drum and the upper wall of the barrel, a settling zone barrel arranged on the upper end of the reactor barrel, a drain trough arranged on top of the settling zone barrel, the combination of two circular passages can separate sludge with water, gas with water at different position, has good separating effect of gas, sludge, water, thereby avoiding the problem of return-sludge flow interfered by inlet flow because of mixed liquor ascent passage sharing one passage with return-sludge flow in a conventional three phase separator, the invention can keep liquid flow in settling zone steady, fluid state closing to laminar flow, has good solid-liquid separation effect.
Description
Technical field
The present invention relates to a kind of upflow type anaerobic reactor.
Background technology
Anaerobic Microbiological Treatment Technology is compared with traditional aerobe treatment technology, has the organic loading height, does not need a large amount of dilution waters; The purification efficiency height; The nutrition requirement is few; Do not need aeration, energy consumption is low, and working cost is low; Impact load and envrionment conditions have stronger adaptive faculty; Can produce biogas recycles as clean energy; Sludge yield is low, and the biological sludge of generation is easy to dehydration; Advantages such as reactor volume is little, and floor space is few.Be widely used in the processing of the middle and high concentration organic waste water of industries such as light industry, chemical industry, pharmacy, obtained effect preferably.That application is the most successful at present is upflow anaerobic sludge blanket reactor (UASB).
Waste water advances people's anaerobic reactor by water distributor at the bottom of by the pond, fully contacts with anaerobion at reaction zone waste water, produces the intensive biochemical reaction, and organism mainly is decomposed into biogas (CH by anerobe here
4, CO
2, H
2O etc.), produce a large amount of small biogas bubbles, bubble converges gradually in uphill process and increases and carry mud, water and rise together and enter triphase separator.Triphase separator (gas, solid, liquid separator) is made up of settling region and collection chamber (or claiming gas skirt), and the at first separated laggard people's collection chamber of gas (cover) is discharged reactor by the biogas pipe; Muddy water mixed solution after gas delivery enters the people settling region and carries out solid-liquid separation, and the waste water after the clarification is discharged reactor by effluent trough, and the anaerobic sludge that precipitates turns back to reaction zone by action of gravity by the seam that refluxes.The separation of above-mentioned mud, water, biogas can be finished by a triphase separator.
For high efficiency anaerobic reactor,, must in these devices, triphase separator be set in order to guarantee to keep the mud of q.s and good effluent quality in the anaerobic digestion device.And the quality of triphase separator separating effect directly has influence on separating of gas and mud and treat effluent in the device, thereby has influence on the success or failure of reactor operation.Therefore in DESIGN OF REACTOR, the design of triphase separator is a very crucial part.There is following problem in the bright domestic and international widely used anaerobic reactor of order:
Gas in gas, mud, the water mixed liquid enters the settling region, and promptly mud and water mixture are before entering the settling region, and gas does not separate removal effectively, owing to the solid, liquid separating effect is disturbed in gas leakage to the settling region.Precipitated isolating mud can not turn back to rapidly in the reactor, and can not keep has very high sludge concentration and long sludge age in the reactor.
Summary of the invention
Technical scheme to be solved by this invention provides a kind of separating effect that can improve anaerobic reactor biogas, mud, water mixed liquid, keep settling region liquid stream stable, keeping has very high sludge concentration and long sludge age in the reactor, improve the upflow type anaerobic reactor of volume of equipment utilization ratio.
The present invention adopts following technical scheme:
The present invention includes reactor shell, be arranged on the reactor shell lower end the water distributor water pipe, be arranged on reactor shell upper end constitute triphase separator by taper guide shell and the gas hood that is arranged on taper guide shell upper end, be provided with circular channel one between the cover wall lower end of gas hood and the taper guide shell barrel, be provided with circular channel two between the last barrel of taper guide shell and reactor shell, the gas hood top is provided with the biogas vapor pipe, be provided with the settling region cylindrical shell in the upper end of reactor shell, the top of settling region cylindrical shell is provided with effluent trough.
The present invention is arranged between the settling region cylindrical shell of reactor shell upper end and the reactor shell and adopts tilting reflector to be connected.
The barrel of the present invention and the corresponding anaerobic reactor cylindrical shell of taper guide shell barrel lower end position is made of tilting reflector.
The wide-mouth of gas hood of the present invention and taper guide shell constitutes air chamber, and the gas hood top is provided with vapor pipe.
The wide-mouth of taper guide shell of the present invention is embedded in the gas hood.
Taper guide shell of the present invention and gas hood are by supporting the upper end that channel-section steel is fixedly installed on reactor shell.
Positively effect of the present invention is as follows:
Two circular channels of the present invention combine mud-water separation and gas-water separation are finished at different sites, the good separating effect of gas, mud, water, thus avoided in the traditional triphase separator mixing liquid rising passway and the mud shared passage mud water current that reflux that reflux to disturb bigger problem.
Adopt the present invention can keep settling region liquid stream stable, flow-shape makes it have the good solid-liquid separating effect near the laminar flow shape.
The circular wide-mouth on taper guide shell of the present invention top and cylindric gas hood constitute an air chamber and the bigger gas-liquid separation interface that volume is bigger, can effectively reduce the rate of release of biogas and the steam amount of carrying secretly of discharge reactor shell.
Adopt the gas in gas of the present invention, mud, the water mixed liquid can not enter the settling region cylindrical shell, be that mud and water mixture are before entering the settling region cylindrical shell, gas can separate removal effectively, avoids owing to the solid, liquid separating effect is disturbed in gas leakage to the settling region.
The present invention is arranged between the settling region cylindrical shell of reactor shell upper end and the reactor shell and adopts tilting reflector to be connected effective like this settling region volume that increased.Adopt the precipitated isolating mud of the present invention to turn back to rapidly in the reactor, very high sludge concentration and long sludge age are arranged in the reactor to keep.
North China pharmacy Kang Xin company limited sewage works adopts upflow type anaerobic reactor of the present invention, and 6100m is taken up an area of in 6,600,000 yuan of gross investments
2, adopt " anaerobic-aerobic " biochemical process to handle starch, vitamins B
12Composite waste has 500m
34 of upflow anaerobic sludge blanket reactors, 1000m
31 in aerobic aeration pond.The processing power of separate unit anaerobic reactor reaches 500m
3/ d, water inlet COD value average out to 10566mg/L, water outlet COD value average out to 992mg/L.Passed through the examination of State Environmental Protection Administration at present.
Langfang plum blossom monosodium glutamate company limited one factory's sewage works adopts upflow type anaerobic reactor of the present invention, and 5118m is taken up an area of in 5,700,000 yuan of gross investments
2, adopt " anaerobic-aerobic " treatment process, build GX-I type (500m
3) 4 of upflow anaerobic sludge blanket reactors, 3200m
31 in aerobic aeration pond.High concentrated organic wastewater at first adopts anaerobic reactor to handle, and the processing power of separate unit anaerobic reactor is 680m
3During/d, trimestral water inlet COD value average out to 5632mg/L, water outlet COD value average out to 327mg/L.Anaerobic reactor water outlet and lower concentration gourmet powder waste water mix the back and adopt the aerobic aeration pond to handle, and its processing power reaches 4500m
3/ d, water inlet COD value is 639mg/L, water outlet COD value is 146mg/L, has passed through the examination of Langfang City Environmental Protection Agency at present.
Adopt upflow type anaerobic reactor of the present invention, handle Hebei and protect the lemon citric acid production wastewater 870m of Group Co.,Ltd
3/ d, steady running is the result show: as system water inlet COD, BOD
5, when SS concentration is respectively 11584mg/L, 8100mg/L and 2360mg/L, handle back water outlet COD, BOD
5, SS is respectively 166mg/L, 34mg/L, 40mg/L, clearance reaches 98.6%, 99.6%, 98.3% respectively.The water quality of the total water port of enterprise is lower than " integrated wastewater discharge standard " (GB8978-96) table 2 primary standard value.Anaerobic reactor steady running load is 5.32kgCOD/m
3.d, the COD clearance is 95.9%, and biogas output is 3500m
3/ d.Anaerobism water outlet catalytic oxidation is handled, and the COD clearance is 54.9%.The separate unit reactor load improves operation result and shows: operating load can reach 13.4kg COD/m
3.d, the COD clearance is 92%.Passed through the examination of Baoding Environmental Protection Agency tissue at present.
Description of drawings
Accompanying drawing 1 is a UASB structure of reactor synoptic diagram in the prior art
Accompanying drawing 2 is structural representation of the present invention
Accompanying drawing 3 is for using sewage treatment technology process figure of the present invention
In the accompanying drawings: 1 water distributor water pipe, 2 reactor shells, 3 thermowell, 4 circular channels two, 5 settling region cylindrical shells, 6 circular channels one, 7 taper guide shells, 8 wide-mouths, 9 air chambers, 10 vapor pipes, 11 gas hoods, 12 effluent troughs, 13 rising pipes, 14 support channel-section steel, 15 reflectors, 16 stopple coupons, 17 manholes, 18 shore pipes, 19 grids, 20 equalizing tanks, 21 under meters, 22 interchanger, 23 water distributors, 24 water-sealed tanks, 25 surge tanks, 26 gas meters, 27 anaerobism settling tanks.
Embodiment
Use sewage treatment technology process of the present invention as shown in Figure 3, waste water enters equalizing tank 20 after grid 19 is removed bigger floating matter, suspended substance, carries out the water yield and regulates and the water quality equilibrium.Regulating back waste water enters in the anaerobic reactor cylindrical shell 2 of the present invention by water distributor 23 after under meter 21 and interchanger 22 preheatings, by the waterpower stirring of water inlet and the air-flow stirring action of biogas, waste water fully contacts with mud, and anaerobic bacteria flora is CH with organic matter degradation in the waste water
4And CO
2(biogas), the biogas that produces successively through going the user to use after water-sealed tank 24, surge tank 25 and gas meter 26 meterings; The anaerobism water outlet enters the next stage processing unit through anaerobism settling tank 27 post precipitations.
As shown in Figure 2, the present invention includes reactor shell 2, be arranged on the water distributor water pipe 1 of reactor shell 2 lower ends, what be arranged on reactor shell 2 upper ends constitutes triphase separator by taper guide shell 7 and the gas hood 11 that is arranged on taper guide shell 7 upper ends, be provided with circular channel 1 between the cover wall lower end of gas hood 11 and taper guide shell 7 barrels, be provided with circular channel 24 between the last barrel of taper guide shell 7 and reactor shell 2, gas hood 11 tops are provided with biogas vapor pipe 10, be provided with settling region cylindrical shell 5 in the upper end of reactor shell 2, the top of settling region cylindrical shell 5 is provided with effluent trough 12.Taper guide shell 7 and gas hood 11 are by supporting the upper end that channel-section steel 14 is fixedly installed on reactor shell 2.
The air-flow lift velocity that has higher ascending current speed and biogas to carry generation secretly owing to mixed solution in the reactor shell 2, make mud be difficult to realize separating with waste water, adopt the present invention, finish separating of biogas and mixing liquid in taper guide shell 7 inside, the circular wide-mouth 8 and the cylindric gas hood 11 on the guide shell of taper simultaneously 7 tops constitute an air chamber 9 and the bigger gas-liquid separation interface that volume is bigger, can effectively reduce the rate of release of biogas and the steam amount of carrying secretly of discharge reactor shell 2.
The circular channel one 6 of muddy water mixed solution of the present invention by forming between taper guide shell 7 and the gas hood 11, make and enter settling region cylindrical shell 5 and carry out mud-water separation, mud generation throwing out in the waste water, sedimentation under action of gravity, and return reaction zone along the skew wall of taper guide shell 7.For slowing down flow velocity and providing enough residence time for mud, the upper end of reactor shell 2 of the present invention specially extends out the settling region cylindrical shell, be arranged on and adopt tilting reflector 15 to be connected between the settling region cylindrical shell 5 of reactor shell 2 upper ends and the reactor shell 2, promptly the barrel with the corresponding anaerobic reactor cylindrical shell 2 of taper guide shell 7 barrel lower end positions is made of tilting reflector 15, effective like this settling region volume that increased.And bottom the settling region, make the structure similar to common vertical sedimentation basin, the gradient is beneficial to mud and returns reactor by the action of gravity landing about 50 °.
It is circular channel 24 that the present invention forms mud backflow seam by settling region reflector 15 and taper guide shell 7.According to fluid mechanics principle, the open area of circular channel 24 is little more a lot of than circular channel one 6 open area, and its resistance is bigger, and waste water mainly one 6 flows out from the circular channel, and the bigger mud of settling velocity could be from the circular channel 24 flows back to reactor shell 2; And less flco is just eluriated discharge reactor shell 2 by waterpower, helps the formation of granule sludge.
The design of circular channel 24 of the present invention is most important, combines with circular channel 1 mud-water separation and gas-water separation are finished at different sites, the good separating effect of gas, mud, water.Thereby avoided in the traditional triphase separator a mixing liquid rising passway and mud shared passage (as shown in Figure 1) the mud water current that reflux that reflux to disturb bigger problem.
As shown in Figure 2, the diameter of reactor shell 2 of the present invention is a 3-13 rice, the diameter of taper guide shell wide-mouth 8 is a 2-9 rice, constituting taper guide shell 7 swash plate angle [alpha] is 45 °-60 °, the angle beta of reflector 15 is 45 °-60 °, the diameter of cylindric gas hood 11 is a 2.5-10 rice, and the width of circular channel 1 is a 0.15-0.5 rice, and the width of circular channel 24 is a 0.03-0.2 rice.The diameter of vapor pipe 10 is a 0.08-0.4 rice.
Embodiment 1: structure of the present invention as mentioned above, wherein the diameter of reactor shell 2 is 3 meters, the diameter of taper guide shell wide-mouth 8 is 2 meters, constituting taper guide shell 7 swash plate angle [alpha] is 45 °, the angle beta of reflector 15 is 45 °, the diameter of cylindric gas hood 11 is 2.5 meters, and the width of circular channel 1 is 0.25 meter, and the width of circular channel 24 is 0.03 meter.The diameter of vapor pipe 10 is 0.08 meter.
Embodiment 2: structure of the present invention as mentioned above, wherein the diameter of reactor shell 2 is 13 meters, the diameter of taper guide shell wide-mouth 8 is 9 meters, constituting taper guide shell 7 swash plate angle [alpha] is 60 °, the angle beta of reflector 15 is 60 °, the diameter of cylindric gas hood 11 is 10 meters, and the width of circular channel 1 is 0.5 meter, and the width of circular channel 24 is 0.2 meter.The diameter of vapor pipe 10 is 0.4 meter.
Embodiment 3: structure of the present invention as mentioned above, wherein the diameter of reactor shell 2 is 6 meters, the diameter of taper guide shell wide-mouth 8 is 4.8 meters, constituting taper guide shell 7 swash plate angle [alpha] is 50 °, the angle beta of reflector 15 is 50 °, the diameter of cylindric gas hood 11 is 5.1 meters, and the width of circular channel 1 is 0.15 meter, and the width of circular channel 24 is 0.1 meter.The diameter of vapor pipe 10 is 0.2 meter.
Claims (5)
1. upflow type anaerobic reactor, it is characterized in that it comprises reactor shell (2), be arranged on the water distributor water pipe (1) of reactor shell (2) lower end, what be arranged on reactor shell (2) upper end constitutes triphase separator by taper guide shell (7) and the gas hood (11) that is arranged on taper guide shell (7) upper end, be provided with circular channel one (6) between the cover wall lower end of gas hood (11) and taper guide shell (7) barrel, be provided with circular channel two (4) between the last barrel of taper guide shell (7) and reactor shell (2), gas hood (11) top is provided with biogas vapor pipe (10), be provided with settling region cylindrical shell (5) in the upper end of reactor shell (2), the top of settling region cylindrical shell (5) is provided with effluent trough (12), is arranged on that the tilting reflector (15) of employing is connected between the settling region cylindrical shell (5) of reactor shell (2) upper end and the reactor shell (2).
2. a kind of upflow type anaerobic reactor according to claim 1 is characterized in that being made of tilting reflector (15) with the barrel of taper guide shell (7) the corresponding anaerobic reactor cylindrical shell of barrel lower end position (2).
3. a kind of upflow type anaerobic reactor according to claim 1 and 2 is characterized in that the wide-mouth (8) of gas hood (11) and taper guide shell (7) constitutes air chamber (9), and gas hood (11) top is provided with vapor pipe (10).
4. a kind of upflow type anaerobic reactor according to claim 1 and 2 is characterized in that the wide-mouth (8) of taper guide shell (7) is embedded in the gas hood (11).
5. a kind of upflow type anaerobic reactor according to claim 1 and 2 is characterized in that taper guide shell (7) and gas hood (11) are by supporting the upper end that channel-section steel (14) is fixedly installed on reactor shell (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200710061817XA CN101054234B (en) | 2007-04-28 | 2007-04-28 | Upflow type anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200710061817XA CN101054234B (en) | 2007-04-28 | 2007-04-28 | Upflow type anaerobic reactor |
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| CN101054234A CN101054234A (en) | 2007-10-17 |
| CN101054234B true CN101054234B (en) | 2010-07-07 |
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| CN200710061817XA Active CN101054234B (en) | 2007-04-28 | 2007-04-28 | Upflow type anaerobic reactor |
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Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010113B (en) * | 2010-10-27 | 2013-01-16 | 山东建筑大学 | Anaerobic solid reactor |
| CN102583733A (en) * | 2012-03-28 | 2012-07-18 | 南京中衡元环保设备有限公司 | Anaerobic denitration fluidized bed reactor |
| GB2551344B (en) * | 2016-06-13 | 2022-01-19 | Woxford Environmental Tech Uk Ltd | Anaerobic reactor |
| CN106145316A (en) * | 2016-08-12 | 2016-11-23 | 深圳市清研环境科技有限公司 | Aerobic three-phase separator with mozzle and the application process in sewage disposal thereof |
| CN107162182A (en) * | 2017-05-15 | 2017-09-15 | 杜普利 | A kind of waste water solid separation equipment and its separation method |
| CN111392874B (en) * | 2019-09-12 | 2022-05-06 | 浙江海洋大学 | High ammonia nitrogen autotrophic nitrogen removal device |
| CN115043550B (en) * | 2022-06-24 | 2023-06-20 | 苏州城投环境科技发展有限公司 | Environment-friendly sewage treatment device and treatment method thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1174815A (en) * | 1997-04-26 | 1998-03-04 | 张振家 | High-effect anaerobic treatment device for waste water and method thereof |
| CN2647845Y (en) * | 2003-10-20 | 2004-10-13 | 四川大学 | Coking waste water disposal device |
| CN2682070Y (en) * | 2003-08-06 | 2005-03-02 | 华特科技（四川）环境工程有限公司 | Anaerobic microbiological stationary reactor |
-
2007
- 2007-04-28 CN CN200710061817XA patent/CN101054234B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1174815A (en) * | 1997-04-26 | 1998-03-04 | 张振家 | High-effect anaerobic treatment device for waste water and method thereof |
| CN2682070Y (en) * | 2003-08-06 | 2005-03-02 | 华特科技（四川）环境工程有限公司 | Anaerobic microbiological stationary reactor |
| CN2647845Y (en) * | 2003-10-20 | 2004-10-13 | 四川大学 | Coking waste water disposal device |
Non-Patent Citations (1)
| Title |
|---|
| JP特开2006-51490A 2006.02.23 |
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Application publication date: 20071017 Assignee: Walker Environment Technology (Shenzhen) Co., Ltd. Assignor: Hebei University of Science and Technology Contract record no.: 2017310000046 Denomination of invention: Upflow type anaerobic reactor Granted publication date: 20100707 License type: Exclusive License Record date: 20170825 |
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Effective date of registration: 20180507 Address after: 518062 Shenzhen, Guangdong, Shenzhen, Nanshan District, Guangdong Province Road 1003, Shenzhen road software base 4 blocks 604 rooms Patentee after: Walker Environment Technology (Shenzhen) Co., Ltd. Address before: 050018 School of environmental engineering, Hebei University Of Science and Technology, 70 Yuhua East Road, Shijiazhuang, Hebei Patentee before: Hebei University of Science and Technology |
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