CN205953772U - Waste water recycling processing system of high -efficient desalination - Google Patents

Waste water recycling processing system of high -efficient desalination Download PDF

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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
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China
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waste water
mvpc
processing system
vaporizer
treatment system
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CN201620850946.1U
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Chinese (zh)
Inventor
奚瑞锋
吴子锋
许桂贤
李柏易
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Guangdong Huanyuan Environmental Engineering Co Ltd
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Guangdong Huanyuan Environmental Engineering Co Ltd
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

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  • 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

A kind of waste water recycling treatment system of efficient desalination
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.
CN201620850946.1U 2016-08-08 2016-08-08 Waste water recycling processing system of high -efficient desalination Active CN205953772U (en)

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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

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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

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Cited By (6)

* Cited by examiner, † Cited by third party
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

Cited By (8)

* Cited by examiner, † Cited by third party
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

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