CN108483659A - A kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant - Google Patents
A kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant Download PDFInfo
- Publication number
- CN108483659A CN108483659A CN201810611900.8A CN201810611900A CN108483659A CN 108483659 A CN108483659 A CN 108483659A CN 201810611900 A CN201810611900 A CN 201810611900A CN 108483659 A CN108483659 A CN 108483659A
- Authority
- CN
- China
- Prior art keywords
- folded plate
- reflux
- zone
- pump
- refluxing opening
- 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.)
- Pending
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 20
- 238000005728 strengthening Methods 0.000 title claims abstract description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 11
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 11
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 title claims abstract description 9
- 238000010992 reflux Methods 0.000 claims abstract description 81
- 239000012528 membrane Substances 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 230000003014 reinforcing effect Effects 0.000 claims abstract description 13
- 238000005276 aerator Methods 0.000 claims abstract description 7
- 238000005192 partition Methods 0.000 claims abstract description 7
- 239000000523 sample Substances 0.000 claims description 16
- 239000010802 sludge Substances 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 3
- -1 reflux pump Substances 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 8
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 5
- 239000011574 phosphorus Substances 0.000 abstract description 5
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 229920000388 Polyphosphate Polymers 0.000 description 2
- 229920000037 Polyproline Polymers 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000001205 polyphosphate Substances 0.000 description 2
- 235000011176 polyphosphates Nutrition 0.000 description 2
- 230000001154 acute effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/308—Biological phosphorus removal
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
Abstract
The present invention discloses a kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant, it is characterized by comprising folded plate reaction units, membrane biological reaction apparatus and PC control devices, the folded plate reaction unit includes folded plate reactor and reinforcing reflux, there is multigroup folded plate in folded plate reactor, folded plate reactor is separated into inversion A AO patterns by multigroup folded plate, there are intake pump and water inlet in anoxic zone front end, make partition wall with the public one block of folded plate of membrane biological reaction apparatus in anaerobic zone, the reinforcing reflux includes strengthening reflux line, strengthen refluxing opening and strengthens reflux pump, the membrane biological reaction apparatus includes membrane bioreactor, PH pops one's head in, DO pops one's head in, aerator and reflux.The configuration of the present invention is simple, technological process is simple and direct, operational management is convenient, floor space is small, operating cost is low, stability is high, and nitrogen, phosphorus in removal sewage is suitble to use.
Description
Technical field
The present invention relates to sewage plants and domestic sewage in rural areas tail water processing unit field, and it is de- to particularly belong to a kind of enhanced biological
Nitrogen dephosphorization folded plate reactor sewage-treatment plant.
Background technology
Sewage denitrification and dephosphorization is always the hot spot of water treatment field research, causes water quality anxious with nitrogen and phosphorus content in dampening is excessively high
Acute deterioration, frequent occurrence, water environment pollution and body eutrophication getting worse, China put into effect a variety of policies in succession, improve water
The discharge standard of body, current sewage disposal technology just gradually develop towards the direction of high efficiency, low energy consumption.
At this stage, anaerobic- anoxic- oxic (AAO) technique has been widely used in sewage disposal.But AAO
Sewage disposal mechanism has the following problems:1. since anaerobic zone is ranked forefront, the nitrate in returned sludge will produce not anaerobic zone
Profit influences;2. being located in the middle part of system in anoxic zone, denitrification occupy minus advantage in carbon source distribution, thus affects system
Denitrification effect;3. the suction phosphorus power that polyP bacteria is put aside in anaerobic zone is in anoxic section inefficient consumption;4. most microorganisms only pass through
Anoxic/aerobic alternate environment is gone through to generally require larger reflux ratio in order to reach higher denitrogenation dephosphorizing efficiency, cause to throw
The problems such as money and energy consumption are higher.Regarding to the issue above at a kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage of present invention offer
Manage device.
Invention content
The present invention provides a kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant, solves above-mentioned background technology
In the problem of mentioning.
The technical solution adopted by the present invention is as follows to achieve the above object:
A kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant, it is characterised in that react and fill including folded plate
It sets, membrane biological reaction apparatus and PC control devices, the folded plate reaction unit include folded plate reactor and reinforcing reflux, folding
Plate reactor has multigroup folded plate, multigroup folded plate that folded plate reactor is separated into inversion A AO patterns, and inversion A AO patterns are anoxic zone
In preceding anaerobic zone rear, there are intake pump and water inlet, anaerobic zone and the public one block of folded plate of membrane biological reaction apparatus in anoxic zone front end
Make partition wall, the reinforcing reflux includes strengthening reflux line, strengthening refluxing opening and strengthen reflux pump, strengthens refluxing opening peace
In anoxic zone and anaerobic zone, refluxing opening is strengthened in anoxic zone in succession respectively and reflux is strengthened in anaerobic zone at reinforcing reflux line both ends
Mouthful, strengthen reflux pump and be mounted on reinforcing reflux line, and intelligent unidirectionally pumped from anaerobic zone to anoxic zone is flowed, the film biology
Reaction unit includes membrane bioreactor, PH probes, DO probes, aerator and reflux, is had in membrane biological reaction apparatus
Membrane biological reaction apparatus is divided into aerobic zone and diaphragm area by deflector, deflector, and membrane bioreactor is mounted on diaphragm area, film life
Water outlet pump, outlet conduit and pressure gauge, PH probes are inserted into DO probes in aerobic zone object reactor in succession, and aerator gathers
Membrane biological reaction apparatus bottom, reflux can flow back nitrification liquid and sludge simultaneously, and reflux includes refluxing opening, reflux line
With reflux pump, wherein refluxing opening one is mounted in aerobic zone, another refluxing opening is mounted in anoxic zone, and reflux line is in succession
Refluxing opening in refluxing opening and anoxic zone, reflux pump are mounted on reflux line in aerobic zone, the PC control devices can regulate and control into
Water pump, PH probes, DO probes, reflux pump, water outlet pump and pressure gauge.
Compared with the prior art, beneficial effects of the present invention are as follows:
The present invention is combined by carrying out preferred design with PC control devices to folded plate reaction unit, membrane biological reaction apparatus,
At a kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant, with anoxic zone in the posterior inversion in preceding anaerobic zone
AAO patterns, the sewage disposal mechanism for solving AAO have the following problems:1. since anaerobic zone is ranked forefront, the nitrate in returned sludge
Adverse effect will produce to anaerobic zone;2. being located in the middle part of system in anoxic zone, denitrification occupy minus advantage in carbon source distribution,
Thus affect the denitrification effect of system;3. the suction phosphorus power that polyP bacteria is put aside in anaerobic zone is in anoxic section inefficient consumption;4. absolutely
Most of microorganism only undergoes anoxic/aerobic alternate environment and is generally required larger to reach higher denitrogenation dephosphorizing efficiency
Reflux ratio, cause investment and energy consumption it is higher the problems such as.The configuration of the present invention is simple, technological process is simple and direct, operational management is convenient, accounts for
Ground area is small, operating cost is low, stability is high, and nitrogen, phosphorus in removal sewage is suitble to use.
Description of the drawings
Fig. 1 is schematic structural view of the invention;
Digital corresponding component in figure:Chemicals dosing plant (1,2):Grug feeding jar (1), dosing pump (2);Partition board reactor (3~11);
Partition plate coagulation area (5), reaction zone (8), settling zone (11), settling section (7), water inlet (3), partition board (4), sludge bucket (9), water outlet
Mouth (6), sewage draining exit (10).
Specific implementation mode
Referring to attached drawing:A kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant, it is characterised in that including folding
Plate reaction unit (3,11), membrane biological reaction apparatus (4,5,8,9,10) and PC control devices (1), the folded plate reaction unit
(3,11) include folded plate reactor (3) has multigroup folded plate (13), multigroup folding with reflux (11), folded plate reactor (3) is strengthened
Folded plate reactor (3) is separated into inversion A AO patterns by plate (13), and inversion A AO patterns are that anoxic zone (2) exist in preceding anaerobic zone (12)
Afterwards, anoxic zone (2) front end has intake pump (14) and water inlet, anaerobic zone (12) public with membrane biological reaction apparatus (4,5,8,9,10)
Make partition wall with one piece of folded plate (13), the reinforcing reflux (11) includes strengthening reflux line (1103), strengthening refluxing opening
(1101) with reinforcing reflux pump (1102), strengthen refluxing opening (1101) and be mounted on anoxic zone (2) in anaerobic zone (12), strengthen back
Anoxic zone (2) strengthen refluxing opening (1101) and anaerobic zone (12) reinforcing refluxing opening in succession respectively at flow tube road (1103) both ends
(1101), strengthen reflux pump (1102) and be mounted on and strengthen on reflux line (1103), and it is intelligent unidirectionally from anaerobic zone (12) to
Anoxic zone (2) pump stream, the membrane biological reaction apparatus (4,5,8,9,10) include membrane bioreactor (8), PH probes (4), DO
It pops one's head in (5), aerator (9) and reflux (10), membrane biological reaction apparatus have deflector (15) in (4,5,8,9,10), lead
Membrane biological reaction apparatus (4,5,8,9,10) is divided into aerobic zone and diaphragm area by flowing plate (15), and membrane bioreactor (8) is mounted on
Diaphragm area, water outlet pump (7), outlet conduit and pressure gauge (6), PH probes (4) pop one's head in (5) to membrane bioreactor (8) with DO in succession
It is inserted into aerobic zone, aerator (9) gathers in membrane biological reaction apparatus (4,5,8,9,10) bottom, and reflux (10) can be same
Shi Huiliu nitrification liquids and sludge, reflux (10) include refluxing opening (1001), reflux line (1003) and reflux pump (1002),
Wherein refluxing opening (1001) one is mounted in aerobic zone, another refluxing opening (1001) is mounted in anoxic zone (2), return duct
Refluxing opening (1001) is mounted on refluxing opening (1001) in anoxic zone (2), reflux pump (1002) in aerobic zone in succession in road (1003)
On reflux line (1003), the PC control devices (1) can regulate and control intake pump (14), PH probes (4), DO probes (5), reflux pump
(1002), water outlet pump (7) and pressure gauge (6).
Claims (1)
1. a kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant, it is characterised in that including folded plate reaction unit,
Membrane biological reaction apparatus and PC control devices, the folded plate reaction unit include folded plate reactor and reinforcing reflux, folded plate
Reactor has multigroup folded plate, multigroup folded plate that folded plate reactor is separated into inversion A AO patterns, and inversion A AO patterns are that anoxic zone exists
Rear, anoxic zone front end has intake pump and water inlet, anaerobic zone to make with the public one block of folded plate of membrane biological reaction apparatus for preceding anaerobic zone
Partition wall, the reinforcing reflux include strengthening reflux line, strengthening refluxing opening and strengthen reflux pump, strengthen refluxing opening installation
In anoxic zone and anaerobic zone, refluxing opening is strengthened in anoxic zone in succession respectively and reflux is strengthened in anaerobic zone at reinforcing reflux line both ends
Mouthful, strengthen reflux pump and be mounted on reinforcing reflux line, and intelligent unidirectionally pumped from anaerobic zone to anoxic zone is flowed, the film biology
Reaction unit includes membrane bioreactor, PH probes, DO probes, aerator and reflux, is had in membrane biological reaction apparatus
Membrane biological reaction apparatus is divided into aerobic zone and diaphragm area by deflector, deflector, and membrane bioreactor is mounted on diaphragm area, film life
Water outlet pump, outlet conduit and pressure gauge, PH probes are inserted into DO probes in aerobic zone object reactor in succession, and aerator gathers
Membrane biological reaction apparatus bottom, reflux can flow back nitrification liquid and sludge simultaneously, and reflux includes refluxing opening, reflux line
With reflux pump, wherein refluxing opening one is mounted in aerobic zone, another refluxing opening is mounted in anoxic zone, and reflux line is in succession
Refluxing opening in refluxing opening and anoxic zone, reflux pump are mounted on reflux line in aerobic zone, the PC control devices can regulate and control into
Water pump, PH probes, DO probes, reflux pump, water outlet pump and pressure gauge.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810611900.8A CN108483659A (en) | 2018-06-14 | 2018-06-14 | A kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810611900.8A CN108483659A (en) | 2018-06-14 | 2018-06-14 | A kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant |
Publications (1)
Publication Number | Publication Date |
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CN108483659A true CN108483659A (en) | 2018-09-04 |
Family
ID=63342493
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201810611900.8A Pending CN108483659A (en) | 2018-06-14 | 2018-06-14 | A kind of strengthening biological carbon and phosphorous removal folded plate reactor sewage-treatment plant |
Country Status (1)
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111704315A (en) * | 2020-06-16 | 2020-09-25 | 沈阳环境科学研究院 | High-nitrogen high-concentration organic wastewater treatment system and method for realizing same |
CN112551828A (en) * | 2020-12-24 | 2021-03-26 | 华夏碧水环保科技有限公司 | Low-carbon-nitrogen-ratio rural domestic sewage treatment device and treatment process thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5480548A (en) * | 1993-12-28 | 1996-01-02 | Ch2M Hill, Inc. | Wastewater biological phosphorus removal process |
CN101092270A (en) * | 2007-06-08 | 2007-12-26 | 沈阳建筑大学 | Biological reactor of polygonal line flowing film |
CN107673557A (en) * | 2017-10-31 | 2018-02-09 | 安徽舜禹水务股份有限公司 | A kind of decentralized type sewage coupled processing method |
CN207608464U (en) * | 2017-11-20 | 2018-07-13 | 中国葛洲坝集团水务运营有限公司 | The device of inversion A AO+MBR integrated sewage disposals |
-
2018
- 2018-06-14 CN CN201810611900.8A patent/CN108483659A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5480548A (en) * | 1993-12-28 | 1996-01-02 | Ch2M Hill, Inc. | Wastewater biological phosphorus removal process |
CN101092270A (en) * | 2007-06-08 | 2007-12-26 | 沈阳建筑大学 | Biological reactor of polygonal line flowing film |
CN107673557A (en) * | 2017-10-31 | 2018-02-09 | 安徽舜禹水务股份有限公司 | A kind of decentralized type sewage coupled processing method |
CN207608464U (en) * | 2017-11-20 | 2018-07-13 | 中国葛洲坝集团水务运营有限公司 | The device of inversion A AO+MBR integrated sewage disposals |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111704315A (en) * | 2020-06-16 | 2020-09-25 | 沈阳环境科学研究院 | High-nitrogen high-concentration organic wastewater treatment system and method for realizing same |
CN112551828A (en) * | 2020-12-24 | 2021-03-26 | 华夏碧水环保科技有限公司 | Low-carbon-nitrogen-ratio rural domestic sewage treatment device and treatment process thereof |
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Application publication date: 20180904 |