CN205953772U - Waste water recycling processing system of high -efficient desalination - Google Patents
Waste water recycling processing system of high -efficient desalination Download PDFInfo
- Publication number
- CN205953772U CN205953772U CN201620850946.1U CN201620850946U CN205953772U CN 205953772 U CN205953772 U CN 205953772U CN 201620850946 U CN201620850946 U CN 201620850946U CN 205953772 U CN205953772 U CN 205953772U
- Authority
- CN
- China
- Prior art keywords
- waste water
- mvpc
- processing system
- vaporizer
- treatment system
- 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.)
- Active
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a waste water recycling processing system of high -efficient desalination, include through consecutive physics pretreatment systems, biochemical reactions processing system, the deep purification processing system who connects of pipeline, deep purification processing system is including the consecutive MBR membrane bioreactor of priority, RO reverse osmosis water treatment ware and MVPC evaporimeter, high salt high concentration organic waste water elder generation carries on after the preliminary treatment through physics pretreatment systems, again after biochemical reactions processing system furthest gets rid of partial salinity and most organic matter, last waste water is handled through RO reverse osmosis water treatment ware and MVPC evaporimeter, system's desalination carries out, the dope is concentrated, control through leading system is handled, the inflow of ability effective control RO reverse osmosis water treatment ware and MVPC evaporimeter, alleviate the work load of RO reverse osmosis water treatment ware and MVPC evaporimeter, in order to reach the minimum mesh of working costs.
Description
Technical field
This utility model is related to Waste Water Treatment technical field, and the waste water recycling particularly to a kind of efficient desalination is processed
System.
Background technology
In recent years, the raising of the development with industrial and agricultural production and cities and towns living standards of the people, industrial wastewater, municipal sewage
Discharge capacity is increasing, the environmental pollution thus causing, and has badly influenced environmental ecology and human health, and especially high salt is high
The discharge of concentration organic wastewater.High salt high concentrated organic wastewater refers to that at least the high concentration containing 3.5% total dissolved solidss TDS has
Machine waste water, it is mainly derived from sea water and is applied to produce in the waste water of generation and industrial processes in industrial and agricultural production and life
High-salt wastewater.Except containing organic contamination beyond the region of objective existence, also containing substantial amounts of inorganic salt in high-salt wastewater, such as Cl-、SO4 2-、Na+、
Ca2+Plasma, the presence of these salt has obvious inhibitory action to conventional biological treatment.
For the intractable present situation of the industry high-concentration salt-containing wastewater such as current chemical industry, dyestuff, pharmacy, concentration of organic wastewater
Height, salt concentration is high, and pollutant component is complicated, and biodegradability is poor, and common process is difficult to break through high salinity for biochemical system
Suppression and toxic action, it is impossible to effective desalination, lead to system crash, run and there is a series of problem.
Utility model content
Technical problem to be solved in the utility model is to provide that a kind of suitability is wide, the efficient desalination of high treating effect
Waste water recycling treatment system.
By solving the technical scheme that above-mentioned technical problem is adopted:A kind of waste water recycling treatment system of efficient desalination, bag
Include and be sequentially connected the physics pretreatment system connecing, biochemical reaction processing system, advanced purification treatment system, described thing by pipeline
Reason pretreatment system includes regulating reservoir, flocculation basin and the tube settler being successively sequentially connected, described biochemical reaction processing system
Anaerobic pond, anoxic pond and the Aerobic Pond being sequentially connected including priority, described advanced purification treatment system includes successively being sequentially connected
MBR membrane bioreactor, RO anti-penetration wastewater disposal device and MVPC vaporizer, the wastewater effluent of described RO anti-penetration wastewater disposal device
Port is connected with the influent waste water port of MVPC vaporizer to reduce the capacity of wastewater entering MVPC vaporizer.
Further, the partial condensation water that described MVPC vaporizer produces is back to biochemical reaction processing system.
Further, it is additionally provided with accurate filter between described MBR membrane bioreactor and anti-penetration wastewater disposal device.
Further, it is additionally provided with pH regulator pond between described regulating reservoir and flocculation basin.
Beneficial effect:In the waste water recycling treatment system of this efficient desalination, high salt high concentrated organic wastewater first passes through physics
After pretreatment system carries out pretreatment, then remove part salinity to greatest extent through biochemical reaction processing system and major part is organic
After thing, last waste water is processed through RO anti-penetration wastewater disposal device and MVPC vaporizer, carries out system desalination, and dope concentrates, and passes through
The control process of front-end system, the inflow of energy effective control RO anti-penetration wastewater disposal device and MVPC vaporizer, mitigate RO reverse osmosis
Permeable processor and the workload of MVPC vaporizer, to reach the lowest coursing cost purpose.At this utility model waste water recycling
Reason system priority adopts materializing strategy, biochemical treatment and advanced treating tertiary treatment process, can be widely used in various types of
The process of high salt high-concentration waste water, capacity of resisting impact load is strong.
Brief description
With reference to the accompanying drawings and examples this utility model is described further;
Fig. 1 is the system diagram of this utility model embodiment.
Specific embodiment
With reference to Fig. 1, a kind of waste water recycling treatment system of efficient desalination of this utility model, it is sequentially connected including by pipeline
The physics pretreatment system 10 that connects, biochemical reaction processing system 20, advanced purification treatment system 30, physics pretreatment system 10 is wrapped
Include regulating reservoir 11, flocculation basin 12 and the tube settler 13 being successively sequentially connected, biochemical reaction processing system 20 include successively according to
Secondary connected anaerobic pond 21, anoxic pond 22 and Aerobic Pond 23, advanced purification treatment system 30 includes the MBR film being successively sequentially connected
Bioreactor 31, RO anti-penetration wastewater disposal device 32 and MVPC vaporizer 33, the wastewater effluent end of RO anti-penetration wastewater disposal device 32
Mouth is connected with the influent waste water port of MVPC vaporizer 33 to reduce the capacity of wastewater entering MVPC vaporizer 33.
Wherein, high salt high concentrated organic wastewater first passes through after physics pretreatment system 10 carries out pretreatment, then through biochemistry
After reaction treatment system 20 removes part salinity and most of Organic substance to greatest extent, last waste water is through RO anti-penetration wastewater disposal
Device 32 and MVPC vaporizer 33 are processed, and carry out system desalination, and dope concentrates, and by the control process of front-end system, can effectively control
RO anti-penetration wastewater disposal device 32 processed and the inflow of MVPC vaporizer 33, mitigate RO anti-penetration wastewater disposal device 32 and MVPC vaporizer
33 workload, to reach the lowest coursing cost purpose.
Preferably, the partial condensation water that MVPC vaporizer 33 produces is back to biochemical reaction processing system 20, Ke Yishi
When biochemical reaction processing system 20 in sewage salt content, strictly salinity is controlled in 8~10g/L, is prevented effectively from appearance
Biochemical system be destroyed, mud poisoning, microorganism deactivated the problems such as.
Preferably, being additionally provided with secondary filter between MBR membrane bioreactor 31 and RO anti-penetration wastewater disposal device 32
Device, wherein, enters accurate filter through the water that MBR membrane bioreactor 31 deals, removes waste water at accurate filter
In larger organic impurities and particulate matter, remove small organic impurities and dissolving at RO anti-penetration wastewater disposal device 32
Inorganic salts, finally pass through evaporation, salinity and the solidification of other pollutant are removed by crystallization, control system at MVPC vaporizer 33
Salinity is it is achieved that liquid zero-emission.
Wherein, it is additionally provided with pH regulator pond between regulating reservoir 11 and flocculation basin 12, dirty after pH regulator pond is processed
The pH value of water is between 9~10.
Above in conjunction with accompanying drawing, embodiment of the present utility model is explained in detail, but this utility model is not limited to
State embodiment, in the ken that described technical field those of ordinary skill possesses, can also be without departing from this practicality
On the premise of new objective, various changes can be made.
Claims (4)
1. a kind of waste water recycling treatment system of efficient desalination it is characterised in that:Including being sequentially connected the physics connecing by pipeline
Pretreatment system, biochemical reaction processing system, advanced purification treatment system, described physics pretreatment system includes successively phase successively
Regulating reservoir even, flocculation basin and tube settler, anaerobic pond that described biochemical reaction processing system includes successively being sequentially connected, lack
Oxygen pond and Aerobic Pond, described advanced purification treatment system includes MBR membrane bioreactor, the RO reverse osmosis water being successively sequentially connected
Processor and MVPC vaporizer, the wastewater effluent port of described RO anti-penetration wastewater disposal device and the influent waste water end of MVPC vaporizer
Mouth is connected to reduce the capacity of wastewater entering MVPC vaporizer.
2. efficient desalination according to claim 1 waste water recycling treatment system it is characterised in that:Described MVPC vaporizer
The partial condensation water producing is back to biochemical reaction processing system.
3. efficient desalination according to claim 1 waste water recycling treatment system it is characterised in that:In the life of described MBR film
It is additionally provided with accurate filter between thing reactor and anti-penetration wastewater disposal device.
4. efficient desalination according to claim 1 and 2 waste water recycling treatment system it is characterised in that:In described regulation
It is additionally provided with pH regulator pond between pond and flocculation basin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620850946.1U CN205953772U (en) | 2016-08-08 | 2016-08-08 | Waste water recycling processing system of high -efficient desalination |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620850946.1U CN205953772U (en) | 2016-08-08 | 2016-08-08 | Waste water recycling processing system of high -efficient desalination |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205953772U true CN205953772U (en) | 2017-02-15 |
Family
ID=57974226
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620850946.1U Active CN205953772U (en) | 2016-08-08 | 2016-08-08 | Waste water recycling processing system of high -efficient desalination |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205953772U (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107162649A (en) * | 2017-05-27 | 2017-09-15 | 遵义盛林农业发展有限公司 | A kind of blueberry plantation irrigation water and its compound method |
CN107601744A (en) * | 2017-10-27 | 2018-01-19 | 长江勘测规划设计研究有限责任公司 | High-salt wastewater processing system and its method |
CN110590075A (en) * | 2019-10-10 | 2019-12-20 | 四川恒泰环境技术有限责任公司 | Pickle wastewater zero-discharge treatment process |
CN111003888A (en) * | 2019-12-24 | 2020-04-14 | 浙江筑原生态科技有限公司 | Treatment method of chemical wastewater of dead pigs |
CN112279450A (en) * | 2019-07-24 | 2021-01-29 | 上海清浥环保科技有限公司 | Zero-emission treatment process for high-salinity high-organic-matter wastewater |
CN114873857A (en) * | 2022-04-25 | 2022-08-09 | 倍杰特集团股份有限公司 | System and method for recycling and standard-reaching discharge of carbon dodecyl alcohol ester wastewater |
-
2016
- 2016-08-08 CN CN201620850946.1U patent/CN205953772U/en active Active
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107162649A (en) * | 2017-05-27 | 2017-09-15 | 遵义盛林农业发展有限公司 | A kind of blueberry plantation irrigation water and its compound method |
CN107601744A (en) * | 2017-10-27 | 2018-01-19 | 长江勘测规划设计研究有限责任公司 | High-salt wastewater processing system and its method |
CN107601744B (en) * | 2017-10-27 | 2024-02-06 | 长江勘测规划设计研究有限责任公司 | High-salt wastewater treatment system and method thereof |
CN112279450A (en) * | 2019-07-24 | 2021-01-29 | 上海清浥环保科技有限公司 | Zero-emission treatment process for high-salinity high-organic-matter wastewater |
CN110590075A (en) * | 2019-10-10 | 2019-12-20 | 四川恒泰环境技术有限责任公司 | Pickle wastewater zero-discharge treatment process |
CN111003888A (en) * | 2019-12-24 | 2020-04-14 | 浙江筑原生态科技有限公司 | Treatment method of chemical wastewater of dead pigs |
CN114873857A (en) * | 2022-04-25 | 2022-08-09 | 倍杰特集团股份有限公司 | System and method for recycling and standard-reaching discharge of carbon dodecyl alcohol ester wastewater |
CN114873857B (en) * | 2022-04-25 | 2023-02-07 | 倍杰特集团股份有限公司 | System and method for recycling and standard-reaching discharge of carbon dodecyl alcohol ester wastewater |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN205953772U (en) | Waste water recycling processing system of high -efficient desalination | |
CN103288309B (en) | Coal gasification wastewater zero-emission treatment method, and application thereof | |
CN102786183B (en) | Method for processing garbage leachate | |
CN101508514B (en) | Zero discharge recycle treatment method for garbage leachate | |
CN102786182B (en) | Device for processing landfill leachate | |
CN202322568U (en) | Deep treatment system of high-concentration percolate of integrated garbage treatment site | |
CN102120678B (en) | Sewage recycling device based on electrolysis and membrane biological reactor technology and method thereof | |
WO2010115319A1 (en) | Sewage treatment process and system | |
CN105481174A (en) | Wastewater treatment system in rubber and synthetic plastic industry | |
CN103663849A (en) | Method for treating papermaking wastewater based on combined process including integrated membrane technology and advanced oxidation technology | |
CN104649519A (en) | Sewage treatment device and method by combining bio-ferric process and anaerobic MBR method | |
CN104118973A (en) | Technique for processing reverse osmosis concentrated water | |
CN207062081U (en) | A kind of pharmaceutical wastewater processing system | |
CN209778571U (en) | Treatment system for leachate of household garbage landfill | |
CN104556528B (en) | A kind of integrated treatment process of clindamycin alkaline waste water | |
CN105060562A (en) | Deep treatment method of tannery wastewater | |
CN103896457B (en) | A kind of Fine Chemistry Wastewater treatment process | |
CN106517669B (en) | The positive osmosis treatment system of black smelly water A/O and treatment process | |
CN205974184U (en) | Processing system of landfill leachate embrane method concentrate | |
CN202610073U (en) | Processing apparatus of garbage percolating liquid | |
CN205035215U (en) | Landfill leachate treatment device | |
CN205368049U (en) | Sizing agent effluent treatment plant | |
CN209113686U (en) | A kind of combination unit handling hc effluent with high salt | |
CN107151082A (en) | The zero-discharge treatment system and its method of a kind of waste water containing DMF | |
CN106145555A (en) | A kind of efficient combination processing system for high NH4 source water |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |