CN101913697A - Natural reoxygenation biomembrane reaction device and water body in-situ remediation method thereof - Google Patents

Natural reoxygenation biomembrane reaction device and water body in-situ remediation method thereof Download PDF

Info

Publication number
CN101913697A
CN101913697A CN2010102118917A CN201010211891A CN101913697A CN 101913697 A CN101913697 A CN 101913697A CN 2010102118917 A CN2010102118917 A CN 2010102118917A CN 201010211891 A CN201010211891 A CN 201010211891A CN 101913697 A CN101913697 A CN 101913697A
Authority
CN
China
Prior art keywords
water
reaction unit
filler
support
ventilated membrane
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
Application number
CN2010102118917A
Other languages
Chinese (zh)
Inventor
郑先俊
李建平
刘增超
刘文辉
赵菁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xian Technological University
Original Assignee
Xian Technological University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Xian Technological University filed Critical Xian Technological University
Priority to CN2010102118917A priority Critical patent/CN101913697A/en
Publication of CN101913697A publication Critical patent/CN101913697A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

The invention discloses a natural reoxygenation biomembrane reaction device for the remediation of surface water and a water body in-situ remediation method thereof. The device comprises a reaction device bracket, a water-proof ventilated membrane, a filler, a counter weight and a connecting piece, wherein the reaction device bracket consists of a central bracket, a filler bracket and a protective bracket; the water-proof ventilated membrane is coated outside the central bracket; the filler is hung outside the water-proof ventilated membrane; and the bottom center of the reaction device is provided with the counter weight while the top center is provided with the connecting piece. The reaction device can be directly submerged in water, performs reoxygenation naturally while running, can effectively improve water quality and is suitable for repairing micro-polluted and slightly-polluted water bodies.

Description

Natural reaeration biomembrane reaction apparatus and water body in-situ restoration method thereof
Technical field
The present invention relates to a kind of technology of biological membrane and reaction unit thereof that the polluted surface water microorganism is repaired that be used for.
Background technology
Along with expanding economy, the direct or discharging that exceeds standard of many factory effluents and sanitary sewage causes the pollution of surface water.Cause that the topmost pollutent of water pollution is organism and nutritive substances such as nitrogen, phosphorus.Absorbed by the microbiological degradation in the water after can biochemical organism entering water body, the dissolved oxygen in the consume water.After nutritive substance such as nitrogen, phosphorus enters water body, can cause algal bloom.At night, respiration of algae and the Decomposition of dead algae will consume oxygen.After dissolved oxygen is reduced to a certain degree, will influence hydrobiological existence.After dissolved oxygen exhausted, water body will smelly blackening.Therefore, repair contaminated surface water, key is that Xiang Shuizhong provides oxygen, organism in the degradation water and nutritive substances such as nitrogen, phosphorus.
At present, mainly containing physics repairing method, chemical repairing method, biological restoration method and restoration of the ecosystem method aspect the polluted surface water body recovery technique.It is simple and be convenient to advantage such as application that biological restoration has low investment, high benefit, bookkeeping, and development potentiality is huge.The biopurification technology of domestic use mainly contains throws bacterium technology, technology of biological membrane and water reoxygenation aeration process.In recent years, people are incorporated into technology of biological membrane in the biological restoration of polluted surface water, have obtained significant effect.Biomembrance process is to make microorganism growth and breeding on carrier surface, by to the absorption of organic nutrient substance, oxygen to the diffusion of microbial film inside and the effects such as bio-oxidation that in film, taken place, pollutent is decomposed.It has the detergent power height, and certain nitrification function and characteristics such as the anti-water yield, variation water quality are arranged.
(patent No. is Chinese invention patent: ZL200310103050.4) disclose a kind of level rotary flow suspending carrier biofilm reactor and water body in-situ restoration method thereof.This biofilm reactor is made up of reactor body, water inlet feedway and helping air supply system, depth-width ratio is 0.5: 1~2.5: 1, set up flow apron at reactor four jiaos, its aerator is arranged in a side of reactor bottom, the water inlet feedway can be arranged with the reactor body branch, also can be processed into integral type, as the mud-water separation district, and the stacking volume that adds carrier granule accounts for 40~70% of reactor volume with flow apron and the formed groove of reactor one side upper wall surface.This biofilm reactor has Stability Analysis of Structures, convenient operation and control, organic pollutant and ammonia nitrogen removal frank than advantages such as height.But there is following deficiency in this reactor: 1. owing to be provided with into water feedway and helping air supply system, structure more complicated; 2. when mud reach mud-water separation district cumulative volume 1/3~1/2 the time need spoil disposal, bookkeeping relatively bothers; 3. need with water pump former water to be fed reactor, and need to use the air pump aeration, working cost is higher.
Summary of the invention
At the existing in prior technology deficiency, the purpose of this invention is to provide a kind of method and reaction unit that polluted surface water body original position is repaired that be used for, it does not need to be provided with water feed apparatus, does not need spoil disposal and aeration during operation yet.
The objective of the invention is to be achieved through the following technical solutions:
A kind of natural reaeration biomembrane reaction apparatus comprises reaction unit support, waterproof ventilated membrane, filler, counterweight and web member.The reaction unit support is made up of center bearing bracket, filler support and protective cradle.Coated outside waterproof ventilated membrane at center bearing bracket.At waterproof ventilated membrane outside hanging filler.Bottom centre at reaction unit is provided with counterweight, in the top center of reaction unit web member is set.
The present invention also provides a kind of method of utilizing above-mentioned reaction unit that water body in-situ is repaired, comprises the steps:
(1) arrange reaction unit: stay cord or support are set on the water surface, reaction unit is immersed in the water, be fixed on stay cord or the support by web member, the up-down adjustment web member makes the water surface apart from reaction unit top 5~10cm.
(2) biofilm: be under 10~30 ℃ the condition, generally about 1 month, to form active biological film in temperature at filling surface.If indigenous microorganism is less or also can adopt inoculation membrane formation start time for shortening reaction unit in the former water.
(3) operation: can repair water body efficiently, constantly after the biofilm success, but should regulate web member to prevent water and overflow in the air column or filler surfaces according to the variation of the water surface.
The present invention compared with prior art has following advantage and high-lighting effect: reaction unit of the present invention can directly be immersed in the water, does not have water-in and water-out and mud discharging device, and is simple in structure, invests low; This reaction unit does not need to use water pump and air pump, and noiseless during operation safeguards that simply working cost is low; This reaction unit can be reused, and does not need to change filler, can effectively improve water quality, is applicable to the water body reparation of little pollution, slight pollution.
Description of drawings
Fig. 1 is the longitudinal section synoptic diagram of natural reaeration biomembrane reaction apparatus provided by the invention.
Fig. 2 is that A among Fig. 1 is to view.
The longitudinal section synoptic diagram that Fig. 3 arranges for reaction unit.
Fig. 4 is that A among Fig. 3 is to view.
Among the figure, 1, center bearing bracket, 2, filler support, 3, protective cradle, 4, waterproof ventilated membrane, 5, filler, 6, counterweight, 7, web member, 8, stay cord.
Embodiment
For clearly demonstrating the technical characterstic of this programme,, and, this programme is set forth in conjunction with its accompanying drawing below by embodiment.
See figures.1.and.2, natural reaeration biomembrane reaction apparatus provided by the invention is made up of reaction unit support, waterproof ventilated membrane 4, filler 5, counterweight 6 and web member 7.The reaction unit support is made up of center bearing bracket 1, top and bottom filling support 2 and protective cradle 3.Top and bottom level at reaction unit are provided with filler support 2, and protective cradle 3 vertically is set around reaction unit.The top of center bearing bracket 1 is connected with the inner end of top filler support 2.Protective cradle 3 is connected with the outer end of top, bottom filling support 2.Coated outside waterproof ventilated membrane 4 at center bearing bracket 1.Hanging filler 5 in the space that waterproof ventilated membrane 4, protective cradle 3, top and bottom filling support 2 surround.In the bottom of reaction unit counterweight 6 is set, web member 7 is set at the top.
The each several part role is in the reaction unit: center bearing bracket 1 is used to support the hydraulic pressure that waterproof ventilated membrane 4 is born; filler support 2 is used for fixing, hanging filler 5, and protective cradle 3 is used for protecting filler 5 and the waterproof ventilated membrane 4 can be by the destructions such as floating matter of water.Waterproof ventilated membrane 4 can allow oxygen see through film and enter water body inside water resistance every in the film outside.Counterweight 6 makes the gravity of reaction unit be slightly larger than buoyancy, and even the reaction unit run-off the straight under the effect of gravity, still can be got back to the vertical position, can not turn on one's side below the centre of buoyancy in the position of center of gravity; Web member 7 is suspended on reaction unit on the stay cord or support that is arranged on the water surface, guarantees that reaction unit can be immersed in the water, and web member can up-down adjustment, to change the reaction unit buried degree of depth.
The principle of this reaction unit is: adopt the biology in situ reparation, reaction unit is immersed in the polluted water body, form the air column that gos deep into water body by center bearing bracket 1 and waterproof ventilated membrane 4, air column stretches out the water surface and atmosphere communicates, and oxygen sees through waterproof ventilated membrane and enters water body inside.The acting in conjunction of the water surface and waterproof ventilated membrane has formed the effect of stereo natural reoxygenation, has greatly improved transfer rate and the transmission capacity of oxygen in water.Original inhabitants in the water or microbe inoculation are adsorbed on the filler 5, and they utilize the oxygen katabolism organism in the water to obtain energy, and utilize nutritive substance synthetic cells such as nitrogen, phosphorus, are implemented in the growth and breeding on the filler, form microbial film.After microbial film forms, rely on absorption and biochemical action, water pollutant is removed.
With reference to Fig. 3 and Fig. 4, working process of the present invention is as follows: (1) arranges reaction unit: stay cord 8 or support are set on the water surface, reaction unit is immersed in the water, be fixed on stay cord 8 or the support by web member 7, up-down adjustment web member 7 makes the water surface apart from reaction unit top 5~10cm, and the spacing of stay cord 8 and reaction unit is by water quality situation and the decision of water body functions of use.(2) biofilm: be under 10~30 ℃ the condition, generally about 1 month, to form active biological film in temperature at filling surface.If indigenous microorganism is less or also can adopt inoculation membrane formation start time for shortening reaction unit in the former water.(3) operation: can repair water body efficiently, constantly after the biofilm success, but should regulate web member 7 to prevent water and overflow in the air column or filler 5 surfaces according to the variation of the water surface.
Reaction unit of the present invention can directly be immersed in the water, does not have water-in and water-out and mud discharging device, and is simple in structure, invests low; This reaction unit does not need to use water pump and air pump, and noiseless during operation safeguards that simply working cost is low; This reaction unit can be reused, and does not need to change filler, can effectively improve water quality, is applicable to the water body reparation of little pollution, slight pollution.

Claims (7)

1. a natural reaeration biomembrane reaction apparatus is characterized in that: comprise reaction unit support, waterproof ventilated membrane, filler, counterweight and web member.
2. according to right 1 desired natural reaeration biomembrane reaction apparatus; it is characterized in that: the reaction unit support is made up of center bearing bracket, filler support and protective cradle; top and bottom level at reaction unit are provided with filler support; protective cradle vertically is set around reaction unit; the top of center bearing bracket is connected with the inner end of top filler support, and protective cradle is connected with the outer end of top, bottom filling support.
3. according to right 1 desired natural reaeration biomembrane reaction apparatus, it is characterized in that: at the coated outside waterproof ventilated membrane of center bearing bracket.
4. according to right 1 desired natural reaeration biomembrane reaction apparatus, it is characterized in that: hanging filler in the space that waterproof ventilated membrane, top and bottom filling support, protective cradle surround.
5. according to right 1 desired natural reaeration biomembrane reaction apparatus, it is characterized in that: bottom centre is provided with counterweight at reaction unit.
6. according to right 1 desired natural reaeration biomembrane reaction apparatus, it is characterized in that: web member is set in the reaction unit top center.
7. one kind is utilized reaction unit as claimed in claim 1 that water body is carried out the method that original position is repaired, and it is characterized in that this method comprises the steps:
(1) arrange reaction unit: stay cord or support are set on the water surface, reaction unit is immersed in the water, be fixed on stay cord or the support by web member, the water surface is apart from reaction unit top 5~10cm.
(2) biofilm: be under 10~30 ℃ the condition, generally about 1 month, can finish biofilm in temperature.
(3) operation: can repair water body efficiently, constantly after the biofilm success, but should regulate web member to prevent water and overflow in the air column or filler surfaces according to the variation of the water surface.
CN2010102118917A 2010-06-28 2010-06-28 Natural reoxygenation biomembrane reaction device and water body in-situ remediation method thereof Pending CN101913697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010102118917A CN101913697A (en) 2010-06-28 2010-06-28 Natural reoxygenation biomembrane reaction device and water body in-situ remediation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010102118917A CN101913697A (en) 2010-06-28 2010-06-28 Natural reoxygenation biomembrane reaction device and water body in-situ remediation method thereof

Publications (1)

Publication Number Publication Date
CN101913697A true CN101913697A (en) 2010-12-15

Family

ID=43321381

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010102118917A Pending CN101913697A (en) 2010-06-28 2010-06-28 Natural reoxygenation biomembrane reaction device and water body in-situ remediation method thereof

Country Status (1)

Country Link
CN (1) CN101913697A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102583778A (en) * 2012-03-04 2012-07-18 北京博汇特环保科技有限公司 Aeration-forced river channel purification plant
CN104150582A (en) * 2014-08-19 2014-11-19 中国建筑设计研究院 Modularized energy-saving spatial formula sewage treatment device and system thereof used for multi-floor buildings
CN104402112A (en) * 2014-11-10 2015-03-11 温州医科大学 Material-filled cylinder for water in-situ purification and construction method thereof
CN104496010A (en) * 2014-11-30 2015-04-08 陈伟群 Bionic filler fixing device
CN107381797A (en) * 2017-09-11 2017-11-24 林朝辉 A kind of sewage purification oxidation pool structure
CN107986457A (en) * 2018-01-10 2018-05-04 河海大学 A kind of differential suspension formula water body in-situ dirty device only
CN110482710A (en) * 2019-05-30 2019-11-22 江苏滤盾膜科技有限公司 A kind of sewage treatment microbial film coupling carrier
CN112125413A (en) * 2020-09-02 2020-12-25 浙江万里学院 Portable underwater deep aerator with denitrification and dephosphorization functions
CN113716800A (en) * 2021-08-30 2021-11-30 长沙工研院环保有限公司 Unpowered biofiltration reactor

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR950003545B1 (en) * 1992-01-09 1995-04-14 주식회사 화랑환경 Treatment method and apparatus for waste water containning sugar
CN1562772A (en) * 2004-04-08 2005-01-12 上海交通大学 Ventilation and reaeration system with no power for treating land of sewage
CN1654356A (en) * 2004-12-30 2005-08-17 西安建筑科技大学 Reinforced biological contacting oxidation water correction apparatus
CN1654361A (en) * 2005-01-13 2005-08-17 河海大学 Method for purifying polluted river water on original position by floating bed plants and biologic membrane composite technique
CN1931742A (en) * 2006-08-28 2007-03-21 王宝贞 In-site comprehensive polluted-water purifying process
CN1931743A (en) * 2006-09-22 2007-03-21 东南大学 Integral sputtering-oxygenating-biofiltering waste water purifying apparatus and process
CN101372376A (en) * 2008-10-09 2009-02-25 环境保护部华南环境科学研究所 Combined type blast aeration system

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR950003545B1 (en) * 1992-01-09 1995-04-14 주식회사 화랑환경 Treatment method and apparatus for waste water containning sugar
CN1562772A (en) * 2004-04-08 2005-01-12 上海交通大学 Ventilation and reaeration system with no power for treating land of sewage
CN1654356A (en) * 2004-12-30 2005-08-17 西安建筑科技大学 Reinforced biological contacting oxidation water correction apparatus
CN1654361A (en) * 2005-01-13 2005-08-17 河海大学 Method for purifying polluted river water on original position by floating bed plants and biologic membrane composite technique
CN1931742A (en) * 2006-08-28 2007-03-21 王宝贞 In-site comprehensive polluted-water purifying process
CN1931743A (en) * 2006-09-22 2007-03-21 东南大学 Integral sputtering-oxygenating-biofiltering waste water purifying apparatus and process
CN101372376A (en) * 2008-10-09 2009-02-25 环境保护部华南环境科学研究所 Combined type blast aeration system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
王立立等: "悬浮式生物膜法处理河涌水挂膜实验", 《暨南大学学报(自然科学版)》, vol. 29, no. 1, 28 February 2008 (2008-02-28) *

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102583778A (en) * 2012-03-04 2012-07-18 北京博汇特环保科技有限公司 Aeration-forced river channel purification plant
CN104150582A (en) * 2014-08-19 2014-11-19 中国建筑设计研究院 Modularized energy-saving spatial formula sewage treatment device and system thereof used for multi-floor buildings
CN104150582B (en) * 2014-08-19 2016-04-27 中国建筑设计院有限公司 The energy-conservation three-dimensional waste disposal plant of modularization for many floors building and system
CN104402112A (en) * 2014-11-10 2015-03-11 温州医科大学 Material-filled cylinder for water in-situ purification and construction method thereof
CN104496010A (en) * 2014-11-30 2015-04-08 陈伟群 Bionic filler fixing device
CN107381797A (en) * 2017-09-11 2017-11-24 林朝辉 A kind of sewage purification oxidation pool structure
CN107986457A (en) * 2018-01-10 2018-05-04 河海大学 A kind of differential suspension formula water body in-situ dirty device only
CN107986457B (en) * 2018-01-10 2021-05-28 河海大学 Layered suspension type water body in-situ sewage purification device
CN110482710A (en) * 2019-05-30 2019-11-22 江苏滤盾膜科技有限公司 A kind of sewage treatment microbial film coupling carrier
CN112125413A (en) * 2020-09-02 2020-12-25 浙江万里学院 Portable underwater deep aerator with denitrification and dephosphorization functions
CN112125413B (en) * 2020-09-02 2022-11-01 浙江万里学院 Portable underwater deep aerator with denitrification and dephosphorization functions
CN113716800A (en) * 2021-08-30 2021-11-30 长沙工研院环保有限公司 Unpowered biofiltration reactor

Similar Documents

Publication Publication Date Title
CN101913697A (en) Natural reoxygenation biomembrane reaction device and water body in-situ remediation method thereof
CN102863081B (en) Three-dimensional ecological deodorization dephosphorization denitrification method as well as device and application
CN100415662C (en) System and process for sawage treating with baffling wet land filtering tank and rateral underflow wet land bed
CN102849844B (en) Coupling bioreactor and method for simultaneously purifying malodorous gas and waste water by using same
CN205241356U (en) Ecological chinampa water treatment facilities of solar energy combined type
CN204324990U (en) Be applicable to the multi-stage biological filter tank-ecological pond purification system into lake landscape water body
WO2008130885A3 (en) Membrane supported biofilm apparatus and process
CN103241907B (en) Method and device for treating organic oil-containing wastewater
CN102249400B (en) Device for ecologically restoring natural water body in situ
CN204474503U (en) A kind of country sewage drips the ecological canal treatment system of filter
CN104528939B (en) Multimedium bacteria bed repairs the device and method of polluted source
CN101830568A (en) Functional biological fixation in-situ remediation method for underground water polluted by nitrogen
CN1631817A (en) Integrated anaerobic-wetland wastewater treatment apparatus and method therefor
KR101167599B1 (en) The biological nutrient removal efficiency of nitrogen and phosphorous apparatus filled porous media
JP5802141B2 (en) Method and apparatus for treating 1,4-dioxane-containing wastewater
CN205740504U (en) A kind of integrated sewage treating apparatus based on bamboo fibre filler
CN205035137U (en) Point source sewage treatment plant
CN111995193A (en) Integrated intelligent device and method for advanced treatment of medical wastewater
CN204737774U (en) Biological carrier of box with a net formula and immobilized microbe device of disposing of sewage
CN110467265A (en) A kind of comprehensive reactor of waste water ecological control
CN204058050U (en) A kind of BAF processing rainwater
CN208200655U (en) A kind of breeding wastewater ecological management system
CN109879536A (en) A kind of domestic sewage in rural areas purification system and purification method
CN115466014A (en) Ecological floating bed, solar aerator, and domestic sewage purification device and method
CN105314730A (en) Automatic water treatment biochemical reactor for sewage riverway

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
DD01 Delivery of document by public notice

Addressee: Zheng Xianjun

Document name: Notification of Publication of the Application for Invention

Addressee: Head of the Intellectual Property Department of Xi'an Technological University

Document name: Notification of Passing Preliminary Examination of the Application for Invention

C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
DD01 Delivery of document by public notice

Addressee: Zheng Xianjun

Document name: the First Notification of an Office Action

DD01 Delivery of document by public notice
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20101215

DD01 Delivery of document by public notice

Addressee: Zheng Xianjun

Document name: Notification that Application Deemed to be Withdrawn