CN201343476Y - Combined reclaimed water treatment system - Google Patents

Combined reclaimed water treatment system Download PDF

Info

Publication number
CN201343476Y
CN201343476Y CNU2008202251610U CN200820225161U CN201343476Y CN 201343476 Y CN201343476 Y CN 201343476Y CN U2008202251610 U CNU2008202251610 U CN U2008202251610U CN 200820225161 U CN200820225161 U CN 200820225161U CN 201343476 Y CN201343476 Y CN 201343476Y
Authority
CN
China
Prior art keywords
water
water treatment
treatment system
combined
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.)
Expired - Fee Related
Application number
CNU2008202251610U
Other languages
Chinese (zh)
Inventor
周继勇
刘晓华
孟祥岩
苏晓
王彦明
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.)
SHANDONG REACHEN ENVIRONMENTAL ENGINEERING Co Ltd
Original Assignee
SHANDONG REACHEN ENVIRONMENTAL ENGINEERING Co Ltd
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 SHANDONG REACHEN ENVIRONMENTAL ENGINEERING Co Ltd filed Critical SHANDONG REACHEN ENVIRONMENTAL ENGINEERING Co Ltd
Priority to CNU2008202251610U priority Critical patent/CN201343476Y/en
Application granted granted Critical
Publication of CN201343476Y publication Critical patent/CN201343476Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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

  • Physical Water Treatments (AREA)
  • Activated Sludge Processes (AREA)

Abstract

The utility model discloses a combined reclaimed water treatment system, which mainly relates to a reclaimed water treatment system combined with a membrane bio-reactor and an ultraviolet disinfection apparatus. The combined reclaimed water treatment system consists of a grid machine, a regulating tank, a submerged lift pump, a hair collector, a membrane module, an aerating blower, a self-sucking pump, an ultraviolet disinfection apparatus, a reclaimed water tank and a cleaning water tank. Sewage is treated by the membrane bio-reactor and then passes through the self-sucking pump, and the pressed water is sucked to the cleaning water tank after being treated by the ultraviolet disinfection apparatus arranged between the self-sucking pump and the conduit of the cleaning water tank. The combined reclaimed water treatment system has the advantages that the utility model is combined with the membrane bio-reactor and ultraviolet disinfection, the manufacturing cost is low, and the combined reclaimed water treatment system is suitable for popularization and application in a wide range.

Description

Water treatment device in a kind of built-up type
Technical field
The utility model relates to a kind of middle water treatment system, is water treatment system in a kind of membrane bioreactor and the apparatus for ultraviolet disinfection bonded, belongs to water treatment field.
Background technology
China is the country of a shortage of water resources, and the human settlements water resources quantity is about 2200m 3, be about 1/4th of world average level.And China's water resource waste is serious, and water resource utilization efficiency is lower.Because the Industry Structure Industry Structure is unreasonable, the high water volume industry development is concentrated simultaneously, and production management level is low, and the water of productive use waste is serious; Thought of people is had less understanding, and lacks sense of crisis, and consciousness of saving water is poor, and city domestic water, domestic water wasting phenomenon are general; Lack overall control, violate the ecological rule development, the exploitation of predation formula, the utilization of waste formula, the management of chaotic formula occur; The repeating utilization factor of water is low, and relevant law, system are unsound, all is the reason that China's water resources crisis occurs.
Middle water reuse is the important channel that solves the city water resource crisis, also is the basic outlet of coordinating city water resource and water surrounding, and life sewage treatment and reuse can reduce can bring certain economic benefits to us again to phreatic exploitation.Middle water is meant various drainings after treatment, reaches the water quality standard of regulation, the undrinkable water that can use mixedly in scopes such as life, municipal administration, environment.Because its water-quality guideline is lower than the water quality standard of Drinking Water, but be higher than the water quality standard of the sewage that allows discharging, be between the two, so be called " middle water ".
Membrane bioreactor (Membrance Bio-Reactor is called for short MBR) technology is a kind of high-efficiency sewage treatment process that biological treatment combines and forms with membrane separation technique.Replace the second pond and the conventional filtration unit of traditional contact oxidation technology with membrane separation technique, the efficient solid-liquid separation capability of film makes effluent quality outstanding, and suspended substance and turbidity approach zero.
Membrane Bio-reactor Technology is a kind of new sewage treatment process that combines and form with ultrafiltration or micro-filtration technology and traditional activated sludge process, the mud-water separation process replaces the gravity settling of traditional technology with membrane sepn, no matter the settling property of solid particulate how, all can finish the mud-water separation process, and can avoid the biology of traditional activated sludge process to run off and cause the problem of thrashing.Membrane bioreactor is owing to almost completely hold back microorganism, but sludge retention time endless, so microbe population and kind are all very abundant in the reactor, system can move under high sludge concentration and low sludge loading, therefore degradation of organic substances is thorough, removes the effective of ammonia nitrogen, and effluent index is better than national standard and highly stable, surplus sludge volume is few, the simple and saving occupation of land of technology.
The ultraviolet radiation for sterilizing and disinfecting principle be utilize the ultraviolet ray of suitable wavelength in can the destroy microorganisms body cell DNA (thymus nucleic acid) or the molecular structure of RNA (Yeast Nucleic Acid), cause the growth cell death and (or) the reproducibility necrocytosis, reach the effect of sterilization and disinfection.Through test, the effective wavelength range of ultra-violet sterilization can be divided into four different wave bands: UVA (400~315nm), UVB (315~280nm), UVC (280~200nm) and vacuum ultraviolet ray (200~100nm).What can see through wherein that ozone layer and cloud layer arrive earth surface has only UVA and UVB part.With regard to sterilization speed, UVC is within the microorganism absorption peak scope, can within 1s, kill virus and bacterium by the dna structure by destroy microorganisms, and UVA and UVB are owing to be in outside the microorganism absorption peak scope, sterilization speed is very slow, often need a few hours just can play germicidal action, in the time, in fact this part belongs to invalid ultraviolet portion at the several seconds of actual engineering hydraulic retention (irradiation).Therefore, said ultraviolet disinfection in fact just is meant the UVC sterilization in the water supply and sewage work.The ultraviolet disinfection technology is based on the basis of modern anti-epidemiology, medical science and photodynamics, utilize high-level efficiency, high strength and long-life UVC wave band ultraviolet lighting water jets of particular design, various bacteriums, virus, parasite, algae and other pathogenic agent in the water are directly killed, reach the disinfectant purpose.
The middle water technology that adopts membrane bioreactor and ultraviolet radiation for sterilizing and disinfecting to combine combines advantage separately, and it is easier that equipment is installed, and treatment effect is stable, and working cost and first input expense are lower, have very strong practicality.
The utility model content
The utility model is according to the problem of above existence, adopt the knockdown middle water treatment device of membrane bioreactor and ultraviolet radiation for sterilizing and disinfecting, provide a kind of both efficient, but have the middle water technology of good sterilization effect and the cheap wide popularization and application of cost cost again.
Technical solutions of the utility model are made up of grid maker, equalizing tank, diving lift pump, hair collector, membrane module, Aeration fan, vacuum primingpump, apparatus for ultraviolet disinfection, middle pond, cleaning pond.
Sewage treatment process: sewage enters former water equalizing tank by drainage pipeline.Former water equalizing tank ingress is provided with grid maker, be used for tackling water greater than 3 millimeters particulate matter; Be provided with submersible pump in the former water equalizing tank, with sewage transport in reactor.The hair collector is set on pipeline, is used for tackling the hair of water; After sewage enters reaction tank, under the effect of aeration, water is formed in membrane bioreactor to circulate up and down, simultaneously under the filteration of the suction of vacuum primingpump and hollow-fibre membrane, make water see through hollow-fibre membrane, continue degraded in the bio-reactor, finish and large particulate matter is trapped in until degraded; For preventing the obstruction of hollow-fibre membrane surface, under the effect of aeration, the film silk is shaken fully, under the effect of mass force, the big material that floats over film silk surface is got rid of in the reactor, continue degraded; The water that comes out through vacuum primingpump directly enters middle pond, reuse in waterworks is transported to buildings again.On the pipeline between vacuum primingpump and the middle pond, ultraviolet sterilization apparatus is set, guarantees to handle back hygienic quality index and can satisfy reuse standard.
Bottom, described membrane biological reaction pond is provided with distribution device and blowdown apparatus, and the membrane bioreactor bottom air inlet connects gas blower.
The processing mode of membrane bioreactor combined uv, combine both advantages, effluent quality by membrane bioreactor is better, especially suspension content is lower, thereby make the ultraviolet penetration coefficient height of water, exposure intensity and the scope of UV-light in water is bigger, for follow-up disinfection by ultraviolet light has been carried out sufficient preparation.Simultaneously, apparatus for ultraviolet disinfection can become the sterilizing unit of enclosed ultraviolet radiation for sterilizing and disinfecting or open tunnel type according to water quality, water yield condition setting.
The utility model compared with prior art has following advantage:
1. membrane bioreactor adopts advanced hollow-fibre membrane one biological treatment process;
2. compare with traditional activated sludge process, save settling tank, device height is integrated, takes up an area of few; 3. the immersion membrane bioreactor assembly has unique screen shape structure, intermembranous difficult obstruction;
4. the used air of air purge film unites two into one with the required aeration of carrying out a biological disposal upon, and is energy-conservation obvious; 5. organic removal rate height, capacity of resisting impact load is strong, and water quality treatment is good, and stable effluent quality needs spoil disposal hardly;
6. ultraviolet sterilization apparatus has selectivity very flexibly, can select the ultraviolet sterilization apparatus of corresponding specification according to the size of the water yield.Can save cost.
7. the level of automation height is managed simple and convenient.
8. construction is simple, and equipment is installed easily.
9. the high efficiency of ultra-violet sterilization and broad spectrum have the very wide scope of application.
Description of drawings
The technical process interface chart that Fig. 1 the utility model is implemented.Grid maker (1), former water equalizing tank (2), diving lift pump (3), hair collection device (4), clean water tank (5), membrane biological reaction apparatus (6), self-priming water pump (7), aerating apparatus (8), ultraviolet sterilization apparatus (9) and middle pond (10).
Embodiment
In conjunction with the technical process interface chart that Fig. 1 the utility model is implemented the utility model enforcement optimal way is done following description.Should in water treatment system mainly by grid maker (1), former water equalizing tank (2), diving lift pump (3), hair collection device (4), clean water tank (5), membrane biological reaction apparatus (6), self-priming water pump (7), aerating apparatus (8), ultraviolet sterilization apparatus (9) and middle pond (10) are formed.Grid maker (1) is positioned at former water equalizing tank (2) internal upper part, diving lift pump (3) bottom in former water equalizing tank (2), diving lift pump (3) is connected with membrane biological reaction apparatus (6) by hair collection device (4), clean the upper end that water tank (5) is fixed on membrane biological reaction apparatus (6), membrane biological reaction apparatus (6) is connected with ultraviolet sterilization apparatus (9) by self-priming water pump (7), aerating apparatus (8) is positioned at the lower end of membrane biological reaction apparatus (6), and ultraviolet sterilization apparatus (9) is connected with middle pond (10).Sewage enters former water equalizing tank (2) after grid maker (1) is removed big particulate matter, regulate the water quality and the water yield.By diving lift pump (3) sewage is promoted to membrane bioreactor (6) then.Give membrane bioreactor (6) oxygen supply by aerating apparatus (8), through vacuum primingpump (7) sucking-off from membrane bioreactor (6), behind ultraviolet sterilization apparatus (9), send into middle pond, then according to the customer need reuse.

Claims (2)

1. water treatment device in the built-up type, it is characterized in that by grid maker (1), former water equalizing tank (2), diving lift pump (3), hair collection device (4), clean water tank (5), membrane biological reaction apparatus (6), self-priming water pump (7), aerating apparatus (8), ultraviolet sterilization apparatus (9) and middle pond (10) are formed, grid maker (1) is positioned at former water equalizing tank (2) internal upper part, diving lift pump (3) bottom in former water equalizing tank (2), diving lift pump (3) is connected with membrane biological reaction apparatus (6) by hair collection device (4), clean the upper end that water tank (5) is fixed on membrane biological reaction apparatus (6), membrane biological reaction apparatus (6) is connected with ultraviolet sterilization apparatus (9) by self-priming water pump (7), aerating apparatus (8) is positioned at the lower end of membrane biological reaction apparatus (6), and ultraviolet sterilization apparatus (9) is connected with middle pond (10);
2. according to water treatment device in claims 1 described a kind of built-up type, it is characterized in that: described membrane bioreactor (6) gas collection is washed the required air of film and is united two into one with the required aeration of carrying out a biological disposal upon.
CNU2008202251610U 2008-12-11 2008-12-11 Combined reclaimed water treatment system Expired - Fee Related CN201343476Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008202251610U CN201343476Y (en) 2008-12-11 2008-12-11 Combined reclaimed water treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008202251610U CN201343476Y (en) 2008-12-11 2008-12-11 Combined reclaimed water treatment system

Publications (1)

Publication Number Publication Date
CN201343476Y true CN201343476Y (en) 2009-11-11

Family

ID=41275059

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008202251610U Expired - Fee Related CN201343476Y (en) 2008-12-11 2008-12-11 Combined reclaimed water treatment system

Country Status (1)

Country Link
CN (1) CN201343476Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103739152A (en) * 2013-11-15 2014-04-23 安徽省绿巨人环境技术有限公司 Community reclaimed water reuse system
EP3461344A3 (en) * 2014-06-24 2019-08-21 Krones Ag Tempering system with cleaning for process fluid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103739152A (en) * 2013-11-15 2014-04-23 安徽省绿巨人环境技术有限公司 Community reclaimed water reuse system
EP3461344A3 (en) * 2014-06-24 2019-08-21 Krones Ag Tempering system with cleaning for process fluid

Similar Documents

Publication Publication Date Title
CN101481194B (en) town domestic sewage treatment process
CN201587886U (en) Combined type MBR sewage treatment and reuse apparatus
CN101024534A (en) Biological electrochemical combined system for treating dye waste water and method thereof
CN104829056A (en) Integrated sewage treatment apparatus, and sewage treatment process flow using apparatus
CN110240367B (en) Sewage treatment system and method for synchronous and efficient removal of carbon, nitrogen and phosphorus
CN103359885A (en) Double-membrane wastewater biological treatment system
CN102557252A (en) Treating method of typical PPCPs (Pharmaceutical and Personal Care Products)
CN204675957U (en) Integrated sewage treating apparatus
CN208071545U (en) A kind of mine domestic wastewater processing unit
CN107751085A (en) A kind of circulating seawer cultivating system based on microalgae membrane bioreactor
CN101624253A (en) High efficient complex enzyme sewage treatment process and high efficient complex enzyme sewage treatment device
CN102101719A (en) Integral MBR sewage treating and recycling method and treatment device
CN210261453U (en) Recirculating aquaculture and tail water treatment integrated water treatment system
CN102515416A (en) Algae-removing and algae-collecting device for photocatalytic oxidation-biological floating bed
CN103936230A (en) Sewage treating method combining activated sludge process with bio-contact oxidation process
CN208362108U (en) System for circulating water aquaculture by using biofilter-artificial wetland
CN105668935A (en) Novel alga-active sludge coupling reactor and antibiotic removing method
CN201343476Y (en) Combined reclaimed water treatment system
CN205953758U (en) Novel alga - activated sludge coupled reaction ware
CN201406358Y (en) Combined reclaimed water treatment system
CN106082433A (en) Biological solid-carrying type film biological unit reactor
CN206014597U (en) A kind of sewage disposal system
CN208577510U (en) A kind of microkinetic combined film bioreactor
CN204607809U (en) Membrane biological reaction pond
CN109133523B (en) Forward osmosis membrane-based livestock and poultry breeding wastewater treatment device and treatment method

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20091111

Termination date: 20100111