CN108726819A - A kind of device of purification river black and odorous water - Google Patents

A kind of device of purification river black and odorous water Download PDF

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Publication number
CN108726819A
CN108726819A CN201810918146.2A CN201810918146A CN108726819A CN 108726819 A CN108726819 A CN 108726819A CN 201810918146 A CN201810918146 A CN 201810918146A CN 108726819 A CN108726819 A CN 108726819A
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CN
China
Prior art keywords
odorous water
river black
bucket
purification river
aeration
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Application number
CN201810918146.2A
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Chinese (zh)
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CN108726819B (en
Inventor
万娟娟
范德朋
黎伟杰
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Bi Wofeng Biotech Inc Of Foshan City
Shandong Biwo Feng Ecological Environment Co Ltd
Biwo Feng Engineering Co Ltd
Original Assignee
Bi Wofeng Biotech Inc Of Foshan City
Shandong Biwo Feng Ecological Environment Co Ltd
Biwo Feng Engineering Co Ltd
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Priority to CN201810918146.2A priority Critical patent/CN108726819B/en
Publication of CN108726819A publication Critical patent/CN108726819A/en
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Publication of CN108726819B publication Critical patent/CN108726819B/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/007Contaminated open waterways, rivers, lakes or ponds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/14NH3-N
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/16Total nitrogen (tkN-N)
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/02Odour removal or prevention of malodour
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/10Packings; Fillings; Grids
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Activated Sludge Processes (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Abstract

The present invention, which solves, invests big, the defect taken up a large area in showering technology in the prior art.A kind of device of purification river black and odorous water is provided, including vertical direction in a cavity, the cavity can fluid communication inhalant region, bio-reaction zone, settling zone, exhalant region, the inhalant region bottom is provided with bucket, the bucket bottom is connected with sludge pipe, and the bio-reaction zone is filled with filler and microorganism fungus kind.The technical program has the technical effect that:Can efficient degradation ammonia nitrogen, total nitrogen, low carbon compound, decompose larger molecular organics, investment is small, and floor space is small;By filled high polymer filler, microorganism fungus kind adhesion amount can be promoted, enhances degradation efficiency.

Description

A kind of device of purification river black and odorous water
Technical field
The present invention relates to sewage disposal environmental protection equipment, especially a kind of collection bioreactor and it is deposited in integrated efficient Handle the environmental protecting device of black and odorous water.
Background technology
The urban river component part important as urban ecological system has supply water source, provides greenery patches, improves ring The functions such as border, communications and transportation, culture and education and tourist recreation are of great significance to the ecological construction in city.
Whole nation water pollution phenomenon is on the rise at present, and water quality is worsening.There are 1200 a plurality of rivers of monitoring in the whole nation There are 850 by different degrees of pollution, and has the tendency that constantly aggravating.In seven big water systems, be not suitable for doing drinking water source Section up to 40%, the more flourishing cities and towns section pollution of industry protrudes, and drinking water source is done in 78% unsuitable in the section of city.River The contamination index in road is the self-purification capacity that the organic matters such as ammonia nitrogen, five-day BOD are more than river.
When the organic pollution in water body when there are a lot, pollutant just decomposes under microbial action, when molten in water body When solving oxygen less than 0.2mg/L, water body is just converted into anaerobic environment, and water body can only carry out slowly coming in the way of anaerobic fermentation The reaction of degradation of contaminant to generate a large amount of hydrogen sulfide, ammonia, and generates the sludge of black.
Water ecology, which is repaired, in the prior art mainly uses in-situ immobilization and showering technology.The in-situ immobilization time is long, Slowly effect;Although showering technology can reach preferable effect, investment is big, takes up a large area.
Invention content
The present invention provides a kind of device of purification river black and odorous water, big to solve to invest in existing showering technology, The defect taken up a large area.In order to solve the above technical problems, the present invention is achieved by the following scheme:
A kind of device of purification river black and odorous water, including vertical direction can fluid communication in a cavity, the cavity Inhalant region, bio-reaction zone, settling zone, exhalant region, the inhalant region bottom are provided with bucket, and the bucket bottom is connected with row Mud pipe, the bio-reaction zone are filled with filler and microorganism fungus kind.
Preferably, the filler is polyurethane, and the specific surface area of the polyurethane is 3.5 × 105m2/m3
Preferably, the filling rate of the filler is 10% -30%.
Preferably, the microorganism fungus kind is bacillus and/or saccharomycete and/or enzyme.
Preferably, the inhalant region center is provided with water inlet module, the water inlet module include water inlet pipe and with it is described into The central tube of water pipe connection, the central tube are cylindrical shape, are open to the bucket direction.
Preferably, the water inlet module further includes flow apron, and the flow apron is arranged in the central tube and bucket Between.
Preferably, the flow apron is coniform, and bottom surface is towards bucket side.
Preferably, it is provided with aeration module at the top of the inhalant region, the aeration module includes aeration plate and in the exposure Equally distributed aeration opening on gas disk, the aeration opening are aerated to the bio-reaction zone direction.
Preferably, the aeration control is in gas-water ratio A ∈【3:1,10:1】.
Preferably, the settling zone is sloping plate deposition district, using the inclined tube or inclined plate of pp materials.
Preferably, the inhalant region, bio-reaction zone, settling zone, exhalant region are isolated by partition board, and the partition board carries air guide Hole.
Optionally, the inhalant region, bio-reaction zone, settling zone, exhalant region are isolated by filter.
Preferably, the spoil disposal nozzle is provided with valve switch.
Preferably, the exhalant region is provided with effluent weir, and water outlet is provided in the effluent weir.
Preferably, the inhalant region, bio-reaction zone are provided with manhole.
Compared with prior art, technical solution provided by the invention, the technique effect or advantage having are:
1, using bio-reaction zone, can efficient degradation ammonia nitrogen, total nitrogen, low carbon compound, decompose larger molecular organics, investment It is small, and floor space is small.
2, by filled high polymer filler, microorganism fungus kind adhesion amount can be promoted, enhances degradation efficiency.
Description of the drawings
Fig. 1 is the three-dimensional structure diagram of present invention purification river black and odorous water device;
Fig. 2 is present invention purification river black and odorous water device along line A-A diagrammatic cross-section;
Specific implementation mode
In order to better understand the above technical scheme, being carried out to above-mentioned technical proposal below in conjunction with Figure of description detailed Explanation.
As depicted in figs. 1 and 2, the device of a kind of purification river black and odorous water, an including cavity 1, in the cavity 1 Vertically can fluid communication inhalant region 2, bio-reaction zone 3, settling zone 4, exhalant region 5, the inhalant region 2, biology are anti- Area 3, settling zone 4, exhalant region 5 is answered to be isolated respectively by first partition 17, second partition 18, third partition board 19, the first partition 17, second partition 18, third partition board 19 carry gas port, and the partition board can be substituted by filter.
2 bottom of the inhalant region is provided with bucket 6, and 6 bottom of the bucket is connected with sludge pipe 7, is set on the sludge pipe 7 It is equipped with valve switch (do not illustrate and in figure).2 center of the inhalant region is provided with water inlet module 10, and the water inlet module 10 is wrapped Water inlet pipe 11 and the central tube being connect with the water inlet pipe 11 12 are included, the central tube 12 is cylindrical shape, to 6 direction of the bucket Opening.The water inlet module 10 further includes flow apron 13, the setting of the flow apron 13 the central tube 12 and bucket 6 it Between, to be coniform, bottom surface is towards 6 side of bucket.The central tube 12 coordinates with the deflector 13, and the sewage of inflow is uniform It is distributed to the inhalant region 2.2 top of the inhalant region is provided with aeration module 14, and the aeration module 14 includes aeration plate 15 And in 15 equally distributed aeration opening 16 of the aeration plate, the aeration opening 16 is aerated to 3 direction of the bio-reaction zone.
Filler 8 and microorganism fungus kind (not illustrating in figure) are filled in the bio-reaction zone 3, the filler 8 is poly- ammonia The specific surface area of ester, the polyurethane is 3.5 × 105m2/m3, using the polyurethane of the specific surface area, microorganism can be improved Adhesive rate.The filling rate of the filler 8 is 10% -30%, and filler 8 in equipment can be made to be in the state of flowing, sewage with fill out Microorganism on material 8 can realize that cross-flow, a variety of ways of contact such as fair current make the polluter in sewage fully be connect with microorganism It touches.Aeration control is in gas-water ratio between 3:1—10:, it can be achieved that have formed sample, anoxic, anaerobism three-phase in filler 8 net between 1 Change system.It is demonstrated experimentally that if gas-water ratio is too small, the easy anaerobism of equipment, while filler 8 is not easy to form flow regime;Gas-water ratio mistake Height, the microbial aggregate being made of filler 8 and microorganism fungus kind are easy to be broken up, and system impact resistance weakens, while It is unfavorable for forming aerobic-anaerobic-anaerobism three-phase purification system in filler 8.The microorganism fungus kind is bacillus and/or ferment Female bacterium and/or enzyme.After above-mentioned strain, the outlet effect of the equipment can reach:Transparency>25cm, ammonia nitrogen≤8mg/L (when influent ammonia nitrogen is more than 30mg/L, it is 70%) dissolved oxygen >=2.0mg/L, oxidation-reduction potential that water outlet ammonia nitrogen, which removes,> 50mV。
The settling zone 4 is sloping plate deposition district, using the inclined tube or inclined plate of pp materials.
The exhalant region 5 is provided with effluent weir 20, and water outlet 21 is provided in the effluent weir 20.For the ease of observation institute It states the inhalant region 2 of equipment, situation in bio-reaction zone 3, be respectively arranged on the inhalant region 2,3 outer wall of bio-reaction zone One manhole 22 and the second manhole 23.
The course of work of above equipment is:Sewage enters central tube 12 by water inlet pipe 11 and carries out water distribution, the central tube 12 coordinate with the deflector 13, realize sewage uniform mixed distribution in the inhalant region 2, flow is in the aeration module 14 Under the action of flow up, the microbial aggregate being made of filler 8 and microorganism fungus kind due to gravity effect, to flowing down Dynamic, such type of flow can be such that microorganism is come into full contact in bio-reaction zone 3 with the polluter in sewage.
The aeration opening 16 is aerated to 3 direction of the bio-reaction zone, oxygen is transported to bio-reaction zone 3, in biology Aerobic, anoxic is formd in the filler 8 of reaction zone, (filler is followed successively by aerobic, anoxic by outside, detests inward at three interfaces of anaerobism Oxygen), the effects that microorganism carries out aerobic nitrifications at three interfaces, anoxic denitrification, is by the organic matter removal in black and odorous water.
Sewage enters settling zone 4 with air-flow, by sloping plate deposition, carries out mud-water separation, clear water passes through in effluent weir 20 Water outlet 21 be discharged.Sludge is constantly fused to the sludge bulking of bigger under the collision of inclined plate, when sludge bulking dead weight is more than flow It when entrusting power, falls down, inhalant region 2 is entered by settling zone 4, bio-reaction zone 3, finally the precipitation in the bucket 6, leads to Cross the discharge of the sludge pipe 7.

Claims (10)

1. it is a kind of purification river black and odorous water device, including in a cavity, the cavity vertical direction can fluid communication into Pool, bio-reaction zone, settling zone, exhalant region, the inhalant region bottom are provided with bucket, and the bucket bottom is connected with spoil disposal Pipe, the bio-reaction zone are filled with filler and microorganism fungus kind.
2. a kind of device of purification river black and odorous water described in claim 1, it is characterised in that the filler is polyurethane, institute The specific surface area for stating polyurethane is 3.5 × 105m2/m3
3. a kind of device of purification river black and odorous water described in claim 1, it is characterised in that the filling rate of the filler is 10% -30%.
4. a kind of device of purification river black and odorous water described in claim 1, it is characterised in that the microorganism fungus kind is bud Spore bacillus and/or saccharomycete and/or enzyme.
5. a kind of device of purification river black and odorous water described in claim 1, it is characterised in that the inhalant region center setting There is a water inlet module, the water inlet module includes water inlet pipe and the central tube that is connect with the water inlet pipe, and the central tube is cylinder Shape is open to the bucket direction.
6. a kind of device of purification river black and odorous water described in claim 5, it is characterised in that the water inlet module further includes Flow apron, the flow apron are arranged between the central tube and bucket, and the flow apron is coniform, bottom surface direction Bucket side.
7. a kind of device of purification river black and odorous water described in claim 6, it is characterised in that the aeration control is in gas Water ratio A ∈ [3:1,10:1].
8. a kind of device of purification river black and odorous water described in claim 1, it is characterised in that setting at the top of the inhalant region There is an aeration module, the aeration opening that the aeration module includes aeration plate and connect with the aeration plate, the aeration opening is to described Bio-reaction zone direction is aerated.
9. a kind of device of purification river black and odorous water described in claim 1, it is characterised in that the inhalant region, biological respinse Area, settling zone, exhalant region are isolated by partition board, and the partition board carries gas port.
10. a kind of device of purification river black and odorous water described in claim 1, it is characterised in that the exhalant region is provided with out Mill weir is provided with water outlet in the effluent weir.
CN201810918146.2A 2018-08-13 2018-08-13 Device for purifying black and odorous water body of river channel Active CN108726819B (en)

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CN108726819B CN108726819B (en) 2024-03-26

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111908714A (en) * 2020-07-16 2020-11-10 上海环境绿色生态修复科技有限公司 Cruising type river water purification system on water surface
CN112624489A (en) * 2019-10-08 2021-04-09 天津科技大学 Purify ecological dam device in black and odorous river course

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004041981A (en) * 2002-07-15 2004-02-12 Mitsubishi Heavy Ind Ltd Organic waste water treatment method and its system
CA2583752A1 (en) * 2004-10-12 2006-04-20 Biocast Systems, Inc. Integrated multi-zone wastewater treatment system and method
CN104671617A (en) * 2015-03-12 2015-06-03 大连交通大学 Integrated treatment equipment for mixed waste cutting fluid and domestic sewage
CN204625325U (en) * 2015-03-16 2015-09-09 广西迦姆农业生物技术有限公司 A kind of microorganism sewage purifying device
CN204999692U (en) * 2015-09-24 2016-01-27 杭州师范大学 Fall STREAMING and mix packing layer anaerobic ammonium oxidation bioreactor
CN205740469U (en) * 2016-06-07 2016-11-30 华北电力大学(保定) A kind of double-circulating fluid bed Fenton reactor
CN205803261U (en) * 2016-07-02 2016-12-14 武汉森泰环保股份有限公司 A kind of reaction precipitation integrated aerobic fluid bed
CN106315844A (en) * 2016-09-27 2017-01-11 华南理工大学 ANAMMOX reactor and starting method thereof by inoculating mixed sludge
CN208776531U (en) * 2018-08-13 2019-04-23 碧沃丰工程有限公司 A kind of device purifying river black and odorous water

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004041981A (en) * 2002-07-15 2004-02-12 Mitsubishi Heavy Ind Ltd Organic waste water treatment method and its system
CA2583752A1 (en) * 2004-10-12 2006-04-20 Biocast Systems, Inc. Integrated multi-zone wastewater treatment system and method
CN104671617A (en) * 2015-03-12 2015-06-03 大连交通大学 Integrated treatment equipment for mixed waste cutting fluid and domestic sewage
CN204625325U (en) * 2015-03-16 2015-09-09 广西迦姆农业生物技术有限公司 A kind of microorganism sewage purifying device
CN204999692U (en) * 2015-09-24 2016-01-27 杭州师范大学 Fall STREAMING and mix packing layer anaerobic ammonium oxidation bioreactor
CN205740469U (en) * 2016-06-07 2016-11-30 华北电力大学(保定) A kind of double-circulating fluid bed Fenton reactor
CN205803261U (en) * 2016-07-02 2016-12-14 武汉森泰环保股份有限公司 A kind of reaction precipitation integrated aerobic fluid bed
CN106315844A (en) * 2016-09-27 2017-01-11 华南理工大学 ANAMMOX reactor and starting method thereof by inoculating mixed sludge
CN208776531U (en) * 2018-08-13 2019-04-23 碧沃丰工程有限公司 A kind of device purifying river black and odorous water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112624489A (en) * 2019-10-08 2021-04-09 天津科技大学 Purify ecological dam device in black and odorous river course
CN111908714A (en) * 2020-07-16 2020-11-10 上海环境绿色生态修复科技有限公司 Cruising type river water purification system on water surface

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