CN109761450A - It is adjusted with waste water, the comprehensive tower of precipitating and biogas pressure stabilization function - Google Patents
It is adjusted with waste water, the comprehensive tower of precipitating and biogas pressure stabilization function Download PDFInfo
- Publication number
- CN109761450A CN109761450A CN201910201057.0A CN201910201057A CN109761450A CN 109761450 A CN109761450 A CN 109761450A CN 201910201057 A CN201910201057 A CN 201910201057A CN 109761450 A CN109761450 A CN 109761450A
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- China
- Prior art keywords
- settling zone
- comprehensive tower
- biogas
- comprehensive
- precipitating
- Prior art date
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- 239000002351 wastewater Substances 0.000 title claims abstract description 20
- 230000006641 stabilisation Effects 0.000 title claims abstract description 17
- 238000011105 stabilization Methods 0.000 title claims abstract description 17
- 230000001376 precipitating effect Effects 0.000 title claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 230000001105 regulatory effect Effects 0.000 claims abstract description 34
- 230000007246 mechanism Effects 0.000 claims abstract description 9
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims abstract description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 5
- 238000003786 synthesis reaction Methods 0.000 claims description 5
- 239000011148 porous material Substances 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 abstract description 2
- 238000012545 processing Methods 0.000 description 5
- 239000013049 sediment Substances 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000010812 mixed waste Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 238000005067 remediation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Abstract
The invention discloses adjust, precipitate and the comprehensive tower of biogas pressure stabilization function with waste water, it includes comprehensive tower ontology, the comprehensive tower ontology includes the dish gas holder area separated up and down, adjusts settling zone, the settling zone that adjusts includes the settling zone extended from the middle part of the comprehensive tower ontology to bottom and is arranged in the regulatory region that the settling zone is circumferentially upper and is connected to the settling zone, is connected to the dish gas holder area through communicating pipe at the top of the regulatory region；The side of the regulatory region lower part is connected with raw water water inlet pipe, and the regulatory region lower part other side is connected with anaerobic reactor water inlet pipe to be connected to anaerobic reactor；The top of the settling zone is connected to anaerobic reactor outlet pipe, and the bottom of the settling zone is connected to the anaerobic reactor through mud return line；Dish gas holder area top is equipped with effluent weir, is equipped with Isobarically Control mechanism above the effluent weir, the dish gas holder area is communicated with biogas air inlet pipe and biogas escape pipe.Comprehensive tower provided by the invention, structure is simple, saves land occupation.
Description
Technical field
The present invention relates to technical field of waste water processing, in particular to a kind of to have waste water adjusting, precipitating and biogas pressure steady
Determine the comprehensive tower of function.
Background technique
Conventional high concentrated organic wastewater processing, general flow are that collecting-tank-conditioning tank-anaerobic reactor-medium sediment pool-is aerobic
Reactor-advanced treating, anaerobic reactor generate biogas and are collected into dish gas holder, subsequently into subsequent processing, utilize.It is useless
Water, biogas treatment long flow path, for structures mostly based on Reinforced Concrete Structure, processing structures are more, take up an area more, long construction period, subsequent
Land remediation of leaving the theatre is at high cost.
Summary of the invention
It is an object of the present invention to provide it is a kind of with waste water adjust, precipitating and biogas pressure stabilization function comprehensive tower, will adjust
Section pond, medium sediment pool and dish gas holder concentrate in a comprehensive tower, and it is big to solve the problems, such as that sewage treatment facility is taken up an area.
Based on the above issues, present invention provide the technical scheme that
It is adjusted with waste water, the comprehensive tower of precipitating and biogas pressure stabilization function comprising comprehensive tower ontology, the synthesis
Tower ontology includes the dish gas holder area separated up and down, adjusts settling zone, and the adjusting settling zone includes by the comprehensive tower ontology
The settling zone and be arranged in the regulatory region that the settling zone is circumferentially upper and is connected to the settling zone, institute that middle part extends to bottom
It states and is connected to the dish gas holder area through communicating pipe at the top of regulatory region；The side of the regulatory region lower part is connected with raw water water inlet
Pipe, the regulatory region lower part other side is connected with anaerobic reactor water inlet pipe to be connected to anaerobic reactor；The settling zone it is upper
Portion is connected to anaerobic reactor outlet pipe, and the bottom of the settling zone is connected to the anaerobic reactor through mud return line；Institute
Dish gas holder area top is stated equipped with effluent weir, the effluent weir top is equipped with Isobarically Control mechanism, the dish gas holder area connection
There are biogas air inlet pipe and biogas escape pipe.
In some embodiments wherein, the settling zone surrounded by conical baffled and guide shell arranged up and down and
At the conical baffled upper end is fixed on the comprehensive inner wall of tower, and the guide shell upper end is connected to described conical baffled
Lower end and lower end extend to the comprehensive tower bottom, and the guide shell is connected to the regulatory region.
In some embodiments wherein, anaerobic reactor outlet pipe one end be connected to the anaerobic reactor and
The other end extends to the settling zone top and forms water distribution pipeline section, and the water distribution pipeline section is fixed on described conical baffled through support rod
Upper and outer wall is equipped with several water distributing pores.
In some embodiments wherein, the Isobarically Control mechanism includes the air pressure being located above the effluent weir
Adjust cover, the automatic evacuation pipe for being connected to the dish gas holder area and the counterweight that air pressure adjustment cover lower end is set, institute
Air pressure adjustment cover is stated to be slidably matched with the comprehensive tower inner body wall.
In some embodiments wherein, the comprehensive tower inner body wall is equipped with several being arranged in a vertical direction
Guide rail, the outer wall of the air pressure adjustment cover are equipped with the guide wheel cooperated with the guide rail.
In some embodiments wherein, the counterweight is detachably arranged at air pressure adjustment cover lower end.
In some embodiments wherein, manual blow-down pipe is additionally provided on the air pressure adjustment cover.
In some embodiments wherein, the effluent weir is connected to through effluent weir collector pipe to be arranged in the comprehensive tower
Go out bucket on body outer wall, the bucket out is connected to aerobic reactor through comprehensive tower outlet pipe.
In some embodiments wherein, the regulatory region lower part is equipped with evacuated tube.
In some embodiments wherein, the lower part of the regulatory region is equipped with manhole.
Compared with prior art, the invention has the advantages that
1, using technical solution of the present invention, conditioning tank, medium sediment pool and dish gas holder are concentrated in a comprehensive tower, saved
Save occupied area；
2, the foul smell such as biogas generated using technical solution of the present invention, regulatory region and settling zone are collected in dish gas holder
Area reduces secondary pollution；
3, using technical solution of the present invention, traditional regulation pond is reduced, the foul smell collection device that medium sediment pool is separately provided, section
Investment-saving；
4, using technical solution of the present invention, the synthesis tower structure is simple, convenient for management.
Detailed description of the invention
In order to illustrate the technical solution of the embodiments of the present invention more clearly, required use in being described below to embodiment
Attached drawing be briefly described, drawings in the following description are only some embodiments of the invention, skill common for this field
For art personnel, without creative efforts, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is that there is the present invention waste water to adjust, precipitate and the structure of the comprehensive tower embodiment of biogas pressure stabilization function is shown
It is intended to；
Wherein:
1, comprehensive tower ontology；2, raw water water inlet pipe；3, evacuated tube；4, manhole；5, mud return line 6, anaerobic reactor into
Water pipe；7, temperature monitor；8, pH monitor；9, conical baffled；10, guide shell；11, anaerobic reactor outlet pipe；12, it supports
Bar；13, communicating pipe；14, partition；15, biogas air inlet pipe；16, biogas escape pipe；17, effluent weir；18, effluent weir collector pipe；
19, go out bucket；20, comprehensive tower outlet pipe；21, air pressure adjustment cover；22, counterweight；23, guide wheel；24, guide rail；25, automatic evacuation
Pipe；26, manual blow-down pipe；27, support frame；A, regulatory region；B, settling zone；C, dish gas holder area.
Specific embodiment
Above scheme is described further below in conjunction with specific embodiment.It should be understood that these embodiments are for illustrating
The present invention and be not limited to limit the scope of the invention.Implementation condition used in the examples can be done according to the condition of specific producer
Further adjustment, the implementation condition being not specified is usually the condition in routine experiment.
It is the process flow chart of the embodiment of the present invention referring to Fig. 1, provides a kind of with waste water adjusting, precipitating and biogas pressure
The comprehensive tower of power stabilization function, including comprehensive tower ontology 1, the comprehensive tower ontology 1 include the wet type gas separated up and down through partition 14
Cabinet area C, settling zone is adjusted, adjusting settling zone includes from 1 middle part of comprehensive tower ontology to the settling zone B of bottom extension and being arranged in
The regulatory region A being connected in settling zone B circumferential direction and with settling zone B, regulatory region A are connected to dish gas holder area C through communicating pipe 13.
It is connected with raw water water inlet pipe 2 in the side of the lower part regulatory region A, with the raw water for receiving collecting-tank to collect, adjusting is gone under A
The portion other side is connected with anaerobic reactor water inlet pipe 6 to be connected to anaerobic reactor, so that the sewage after regulating water quality, water be arranged
To anaerobic reactor.
The settling zone top B is connected to anaerobic reactor outlet pipe 11, to receive anaerobic reactor to be discharged, the settling zone bottom B
Anaerobic reactor is connected to through mud return line 5 with by sludge reflux to anaerobic reactor.
The dish gas holder area top C is equipped with effluent weir 17, and Isobarically Control mechanism, dish gas holder area are equipped with above effluent weir 17
C is communicated with biogas air inlet pipe 15 and biogas escape pipe 16, and the biogas that anaerobic reactor generates enters wet type through biogas air inlet pipe 16
Gas holder area C passes through the air pressure in Isobarically Control mechanism controls dish gas holder area C.
Wherein, for settling zone B by arranged up and down conical baffled 9 and guide shell 10 around forming, conical baffled 9 upper end is solid
It is scheduled on 1 inner wall of comprehensive tower ontology, 10 upper end of guide shell is connected to conical baffled 9 lower end and lower end extends to comprehensive tower bottom
Portion, guide shell 10 are connected to regulatory region A, and anaerobic reactor water outlet is consolidated through anaerobic reactor outlet pipe 11 into settling zone B
Liquid separation, sludge settling is in the settling zone bottom B, and sewage then enters regulatory region B and mixes with raw water, regulating water quality, water.
11 one end of anaerobic reactor outlet pipe is connected to anaerobic reactor and the other end extends to the settling zone top B and forms cloth
Water pipe section, water distribution pipeline section are fixed on conical baffled 9 through support rod 12, and the outer wall of water distribution pipeline section is equipped with several water distributing pores.
In this example, Isobarically Control mechanism includes the air pressure adjustment cover 21 for being located at 17 top of effluent weir, is connected to wet type gas
The automatic evacuation pipe 25 of cabinet area C and the counterweight 22 that 21 lower end of air pressure adjustment cover is set, air pressure adjustment cover 21 and comprehensive tower sheet
1 inner wall of body is slidably matched.Specifically, being equipped with several guide rails 24 being arranged in a vertical direction on 1 inner wall of comprehensive tower ontology, together
When the guide wheel 23 that cooperate with guide rail 24 is equipped on 21 outer wall of air pressure adjustment cover, guide rail 24 is through the fixation of support frame 27.The air pressure control
Mechanism processed controls the air pressure of dish gas holder area C through counterweight 22, is collected in the biogas of dish gas holder area C through biogas escape pipe 16
Into subsequent processing, with the fluctuation of biogas air inflow, air pressure adjustment cover 21 floats up and down along comprehensive tower, when air inflow continues greatly
When the gas output of biogas escape pipe 16, extra biogas is overflowed through automatic evacuation pipe 25.It can also be on air pressure adjustment cover 21
Equipped with manual blow-down pipe 26, in emergency circumstances for discharging biogas.
For the ease of adjusting the pressure of biogas escape pipe 16, counterweight 22 is detachably arranged under air pressure adjustment cover 21
Counterweight 22, is fixed on air pressure adjustment cover 21 by end for example, by using bolt, i.e. adjustable by the weight for adjusting counterweight 22
Air pressure.
Effluent weir 17, which is connected to be arranged on 1 outer wall of comprehensive tower ontology through effluent weir collector pipe 18, goes out bucket 19, should go out
Bucket 19 is connected to aerobic reactor through comprehensive tower outlet pipe 20, and comprehensive tower water outlet is drained into aerobic reactor and carries out aerobic place
Reason.
The lower part of regulatory region A is equipped with evacuated tube 3, to empty sewage in comprehensive tower.The lower part of regulatory region A is additionally provided with manhole
4, the maintenance to comprehensive tower internal unit.Lower part, the top of regulatory region A is respectively equipped with pH detector 8, temperature monitor 7, uses
To monitor water quality.
Collecting-tank raw water enters regulatory region A through raw water water inlet pipe 2 after pump is promoted, and anaerobic reactor water outlet flow to synthesis certainly
In the middle part of tower and enter settling zone B, completes to enter regulatory region A through guide shell 10 after being separated by solid-liquid separation, the water outlet of settling zone B and raw water are mixed
It closes, the sludge of regulating water quality, water, the settling zone bottom B is back to anaerobic reactor from mud return line 5 through sludge reflux pump
In, raw water and boosted pump from anaerobic reactor water inlet pipe of the mixed waste water of anaerobic effluent enter anaerobic reactor.Regulatory region A
The methane accumulation that anaerobic reaction generates is below conical baffled 9, by entering dish gas holder area C, comprehensive tower water outlet communicating pipe 13
Enter bucket 19 through effluent weir 17, effluent weir collector pipe 18, then enters aerobic reactor through comprehensive tower outlet pipe 20 and carry out
Aerobic Process for Treatment.The biogas that anaerobic reactor generates enters dish gas holder area C through biogas air inlet pipe, with the wave of biogas air inflow
Dynamic, air pressure adjustment cover 21 floats up and down, and when air inflow is persistently greater than the gas output of biogas escape pipe 16, biogas is through automatic evacuation pipe
25 discharges.
The above embodiments merely illustrate the technical concept and features of the present invention, and its object is to allow person skilled in the art
Member cans understand the content of the present invention and implement it accordingly, and it is not intended to limit the scope of the present invention.It is all according to the present invention
The equivalent transformation or modification that Spirit Essence is done, should be covered by the protection scope of the present invention.
Claims (10)
1. being adjusted with waste water, the comprehensive tower of precipitating and biogas pressure stabilization function, it is characterised in that: including comprehensive tower ontology
(1), the comprehensive tower ontology (1) includes the dish gas holder area (C) separated up and down, adjusts settling zone, adjusting settling zone packet
It includes the settling zone (B) extended from comprehensive tower ontology (1) middle part to bottom and is arranged in the settling zone (B) circumferential direction simultaneously
The regulatory region (A) being connected to the settling zone (B), regulatory region (A) top is with the dish gas holder area (C) through communicating pipe
(13) it is connected to；The side of regulatory region (A) lower part is connected with raw water water inlet pipe (2), and regulatory region (A) the lower part other side connects
Anaerobic reactor water inlet pipe (6) is connected to be connected to anaerobic reactor；The top of the settling zone (B) is connected to anaerobic reactor and goes out
The bottom of water pipe (11), the settling zone (B) is connected to the anaerobic reactor through mud return line (5)；The dish gas holder
The area top (C) is equipped with effluent weir (17), and Isobarically Control mechanism, the dish gas holder area (C) are equipped with above the effluent weir (17)
It is communicated with biogas air inlet pipe (15) and biogas escape pipe (16).
2. the comprehensive tower according to claim 1 with waste water adjusting, precipitating and biogas pressure stabilization function, feature exist
In: the settling zone (B) is surrounded by conical baffled (9) arranged up and down and guide shell (10) and is formed, conical baffled (9)
Upper end is fixed on comprehensive tower ontology (1) inner wall, and guide shell (10) upper end is connected to conical baffled (9) lower end
And lower end extends to the comprehensive tower bottom, the guide shell (10) is connected to the regulatory region (A).
3. the comprehensive tower according to claim 2 with waste water adjusting, precipitating and biogas pressure stabilization function, feature exist
In: described anaerobic reactor outlet pipe (11) one end is connected to the anaerobic reactor and the other end extends to the settling zone
(B) water distribution pipeline section is formed at top, and the water distribution pipeline section is fixed on conical baffled (9) through support rod (12) and outer wall is equipped with
Several water distributing pores.
4. the comprehensive tower according to claim 1 with waste water adjusting, precipitating and biogas pressure stabilization function, feature exist
In: the Isobarically Control mechanism include be located at air pressure adjustment cover (21) above the effluent weir (17), be connected to it is described wet
Counterweight (22) of the automatic evacuation pipe (25) and setting in formula gas holder area (C) in air pressure adjustment cover (21) lower end, the gas
Pressure adjusts cover (21) and is slidably matched with comprehensive tower ontology (1) inner wall.
5. the comprehensive tower according to claim 4 with waste water adjusting, precipitating and biogas pressure stabilization function, feature exist
In: comprehensive tower ontology (1) inner wall is equipped with several guide rails (24) being arranged in a vertical direction, the air pressure adjustment cover
(21) outer wall is equipped with the guide wheel (23) cooperated with the guide rail (24).
6. the comprehensive tower according to claim 4 with waste water adjusting, precipitating and biogas pressure stabilization function, feature exist
In: the counterweight (22) is detachably arranged at air pressure adjustment cover (21) lower end.
7. the comprehensive tower according to claim 4 with waste water adjusting, precipitating and biogas pressure stabilization function, feature exist
In: manual blow-down pipe (26) are additionally provided on the air pressure adjustment cover (21).
8. according to claim 1 to the synthesis described in 7 any one with waste water adjusting, precipitating and biogas pressure stabilization function
Tower, it is characterised in that: the effluent weir (17) through effluent weir collector pipe (18) be connected to setting the comprehensive tower ontology (1) outside
Go out bucket (19) on wall, bucket (19) out are connected to aerobic reactor through comprehensive tower outlet pipe (20).
9. according to claim 1 to the synthesis described in 7 any one with waste water adjusting, precipitating and biogas pressure stabilization function
Tower, it is characterised in that: the regulatory region lower part (A) is equipped with evacuated tube (3).
10. according to claim 1 to described in 7 any one with waste water adjust, precipitating and biogas pressure stabilization function it is comprehensive
Close tower, it is characterised in that: the lower part of the regulatory region (A) is equipped with manhole (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910201057.0A CN109761450B (en) | 2019-03-15 | 2019-03-15 | Comprehensive tower with wastewater regulation, precipitation and biogas pressure stabilization functions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910201057.0A CN109761450B (en) | 2019-03-15 | 2019-03-15 | Comprehensive tower with wastewater regulation, precipitation and biogas pressure stabilization functions |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109761450A true CN109761450A (en) | 2019-05-17 |
| CN109761450B CN109761450B (en) | 2024-01-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910201057.0A Active CN109761450B (en) | 2019-03-15 | 2019-03-15 | Comprehensive tower with wastewater regulation, precipitation and biogas pressure stabilization functions |
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| Country | Link |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113912180A (en) * | 2021-11-01 | 2022-01-11 | 上海心缘环境工程有限公司 | Self-lifting three-phase separator and floating gas holder integrated device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113912180A (en) * | 2021-11-01 | 2022-01-11 | 上海心缘环境工程有限公司 | Self-lifting three-phase separator and floating gas holder integrated device |
| CN113912180B (en) * | 2021-11-01 | 2023-07-18 | 上海心缘环境工程有限公司 | Self-elevating three-phase separator and floating gas holder integrated device |
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| Publication number | Publication date |
|---|---|
| CN109761450B (en) | 2024-01-30 |
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