CN2910906Y - Union equipment for treating wastewater contg. difficult degradation substances combined membrane biological reactor and reverse osmosis - Google Patents

Union equipment for treating wastewater contg. difficult degradation substances combined membrane biological reactor and reverse osmosis Download PDF

Info

Publication number
CN2910906Y
CN2910906Y CNU2005200453421U CN200520045342U CN2910906Y CN 2910906 Y CN2910906 Y CN 2910906Y CN U2005200453421 U CNU2005200453421 U CN U2005200453421U CN 200520045342 U CN200520045342 U CN 200520045342U CN 2910906 Y CN2910906 Y CN 2910906Y
Authority
CN
China
Prior art keywords
water
penetration
treatment
mbr membrane
water tank
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
CNU2005200453421U
Other languages
Chinese (zh)
Inventor
丁桓如
王罗春
闻人勤
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.)
Shanghai University of Electric Power
Original Assignee
Shanghai University of Electric Power
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 Shanghai University of Electric Power filed Critical Shanghai University of Electric Power
Priority to CNU2005200453421U priority Critical patent/CN2910906Y/en
Application granted granted Critical
Publication of CN2910906Y publication Critical patent/CN2910906Y/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

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model discloses a membrane bioreactor-anti-penetration combination device for treating refractory degradation industrial wastewater. The characters are that the device consists of a water tank which is for introducing awaiting treatment wastewater in which is arranged with a MBR membrane, a water tank for storing MBR membrane effluent, a MBRM water out pump with high suction height which is arranged between the two water tanks, an anti-penetration treatment device(RO) which is arranged with a water inlet and two water outlets, a RO intake pump which is arranged between the water tank for storing MBR membrane effluent and the water inlet of the anti-penetration treatment device (RO) . One water outlet of the RO intake pump connects with the water tank for storing MBR membrane effluent by pipe, and the other water outlet exhausts and reuses the water after treatment. The device uses both anti-penetration (RO) and MBR membrane. By using excellent characteristics of the MBR membrane the wastewater after treatment which reaches the requirement of anti-penetration is transported to anti-penetration, which can make COD reduced, suspension matter of anti-penetration effluent and COD, etc, meet the standard of emission, even meet the standard of high quality reuse water.

Description

Handle the membrane bioreactor-reverse osmosis combined apparatus of indegradable industrial effluent
Technical field
The utility model relates to a kind of wastewater treatment equipment, particularly a kind of membrane bioreactor-reverse osmosis combined apparatus of handling indegradable industrial effluent.
Background technology
Industrial have much be difficult to biodegradable waste water, as water treatment intermediate ion exchange resin regenerative wastewater, the citric acid wastewater of boiler acid pickling discharging, EDTA Cleaning Wastewater etc.These trade effluents do not have the good treatment method at present as yet, are difficult to be degraded with bioremediation yet.MBR is the abbreviation of membrane bioreactor, and it is that MBR film with special use is placed in the wastewater disposal basin of biological treatment, with the organic oxidation in the water, improves biological treatment effect by the face high-concentration activated sludge, improves waste water treatment efficiency greatly.And to some trade effluent of difficult for biological degradation, owing to can not form active sludge, the MBR technology is difficult to use.
Summary of the invention
The purpose of this utility model is in order to make the MBR technology use the processing of some trade effluent of difficult for biological degradation, a kind of membrane bioreactor-reverse osmosis (RO) combined apparatus of handling indegradable industrial effluent to be provided.
The technical solution of the utility model is: a kind of membrane bioreactor-reverse osmosis combined apparatus of handling indegradable industrial effluent is characterized in that it comprises that is introduced a pending waste water, and is placed with the water tank of MBR film in waste water; One for storing the water tank of MBR film water outlet; One places the MBRM of the high suction lift between two water tanks to go out water pump; One is equipped with a water-in and two water outlet reverse-osmosis treated devices (RO), be equipped with a RO intake pump between the water tank of its water-in and the water outlet of storage MBR film, the one water outlet is connected with the water tank of storing the water outlet of MBR film by pipeline, another water outlet discharging or reuse water after treatment.
Because this device is with MBR film and reverse osmosis (RO) coupling, utilize the good characteristic of MBR film itself, send into reverse osmosis after wastewater treatment reached the reverse osmosis requirement, this reduces COD, indexs such as the suspended substance of reverse osmosis water outlet, COD reach emission standard, even can reach fine reuse water standard.
Description of drawings
Fig. 1 is the utility model structure principle chart;
Fig. 2 handles ion exchange regenerant waste water schematic diagram for the utility model;
Fig. 3 handles lemon pickling waste waters schematic diagram for the utility model.
Embodiment
By shown in Figure 1, a kind of membrane bioreactor-reverse osmosis combined apparatus of handling indegradable industrial effluent is called for short the MBRM-RO treatment unit, is characterized in, it comprises that is introduced a pending waste water, and is placed with the water tank 1 of MBR film 2 in waste water; One for storing the water tank 4 of MBR film water outlet; One places the MBRM of the high suction lift between two water tanks to go out water pump 3; One is equipped with a water-in and two water outlet reverse-osmosis treated devices (RO) 6, be equipped with a RO intake pump 5 between the water tank of its water-in and the water outlet of storage MBR film, the one water outlet is connected with the water tank 4 of storing the water outlet of MBR film by pipeline 7, another water outlet discharging or reuse water after treatment.
This device can be placed on automobile or other running gears, and automobile or running gear can directly move to treatment unit the scene of processing, handle, and is applicable to handle non-recurrent waste water.This device also can be installed on pending place, waste water water source, is applicable to handle regular waste water.
What Fig. 2 was represented is that the utility model is handled ion exchange regenerant waste water schematic diagram, be connected with MBRM-RO treatment unit 10 by pump 9 by contain ion exchange regenerant wastewater disposal basin 8, one outlet, 11 discharging and the reuse water after treatment of MBRM-RO treatment unit, in the wastewater disposal basin that turns back to the front of another outlet, before advancing the processing of MBRM-RO treatment unit, ion exchange regenerant waste water need add acid and add alkali, makes PH be transferred to neutrality.Water quality after treatment: SS ≈ 0, COD<100mg/L.Through circular treatment, a small amount of waste water after concentrating is burned or other modes are handled.
What Fig. 3 was represented is that the utility model is handled lemon pickling waste waters schematic diagram, the waste water of lemon pickling wastewater disposal basin 12 after lime precipitation is handled to another wastewater disposal basin 13, add acid again and be adjusted to neutrality, enter MBRM-RO treatment unit 15 by pump 14, one outlet, 16 discharging and the reuse water after treatment of MBRM-RO treatment unit are in the wastewater disposal basin that turns back to the front of another outlet.Water quality after treatment: SS ≈ 0, COD<100mg/L.
MBR film and reverse osmosis (RO) coupling and MBR film and reverse osmosis (RO) be the application characteristic comparison sheet separately:
Characteristic The problem that occurs when in the high organic industrial sewage of difficult degradation, using separately Role when MBR and RO coupling (handling the high organic industrial sewage of difficult degradation)
MBR 1. use with biological treatment, can form one deck high-concentration activated sludge at face, strengthen biochemical action.2. membrane pore size is little, and filtration again guarantees out that water suspension is low.3. the film contamination resistance is strong. Can not reach and reduce organic purpose in the water, can not form active sludge. Utilize its contamination resistance strong, the aperture is little, strainability is good, go out the low characteristic of water suspension, guarantee that the RO influent quality is good, RO can use for a long time.
RO 1. fenestra is very little, and is strong to separating substances ability in the water.2. film easily pollutes, and influent quality is required high. Film is very fast blocked, can't use. Utilize RO membrane sepn ability strong, when having MBR to guarantee its influent quality, give full play to the RO separation performance, remove organism in the water, guarantee that water outlet reaches emission standard.

Claims (1)

1, a kind of membrane bioreactor-reverse osmosis combined apparatus of handling indegradable industrial effluent is characterized in that, it comprises that is introduced a pending waste water, and is placed with the water tank (1) of membrane bioreactor with film (2) in waste water; One is the water tank (4) of storage film bio-reactor with the film water outlet; A membrane bioreactor film that places the high suction lift between two water tanks is with going out water pump (30); One is equipped with a water-in and two water outlet reverse-osmosis treated devices (6), be equipped with a feed water by reverse osmosis pump (5) between its water-in and the water tank of storage film bio-reactor with the film water outlet, the one water outlet is connected with the water tank (4) of storage film bio-reactor with the film water outlet by pipeline (7), another water outlet discharging or reuse water after treatment.
CNU2005200453421U 2005-09-28 2005-09-28 Union equipment for treating wastewater contg. difficult degradation substances combined membrane biological reactor and reverse osmosis Expired - Fee Related CN2910906Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2005200453421U CN2910906Y (en) 2005-09-28 2005-09-28 Union equipment for treating wastewater contg. difficult degradation substances combined membrane biological reactor and reverse osmosis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2005200453421U CN2910906Y (en) 2005-09-28 2005-09-28 Union equipment for treating wastewater contg. difficult degradation substances combined membrane biological reactor and reverse osmosis

Publications (1)

Publication Number Publication Date
CN2910906Y true CN2910906Y (en) 2007-06-13

Family

ID=38132765

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2005200453421U Expired - Fee Related CN2910906Y (en) 2005-09-28 2005-09-28 Union equipment for treating wastewater contg. difficult degradation substances combined membrane biological reactor and reverse osmosis

Country Status (1)

Country Link
CN (1) CN2910906Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010037156A1 (en) * 2008-09-30 2010-04-08 Central Gippsland Region Water Corporation Process and plant for treating a water stream
US11072550B2 (en) 2016-01-07 2021-07-27 Central Gippsland Region Water Corporation Membrane separation process

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010037156A1 (en) * 2008-09-30 2010-04-08 Central Gippsland Region Water Corporation Process and plant for treating a water stream
AU2008261116B2 (en) * 2008-09-30 2013-02-07 Central Gippsland Region Water Corporation Process and plant for treating a water stream
US8741143B2 (en) 2008-09-30 2014-06-03 Central Gippsland Region Water Corporation Process and plant for treating a water stream
US11072550B2 (en) 2016-01-07 2021-07-27 Central Gippsland Region Water Corporation Membrane separation process

Similar Documents

Publication Publication Date Title
CN103288309B (en) Coal gasification wastewater zero-emission treatment method, and application thereof
CN101851046B (en) Device for deep treatment and complete recovery of coking wastewater and application method thereof
CN101209886B (en) Advanced treatment recycling technique of urban sewage
CN101891354B (en) Process for treating cold rolling wastewater through ozone reaction and activated carbon filtration
CN102616962A (en) Deep stage treatment method for industrial wastewater
CN1772649A (en) Combined membrane bioreactor-reverse osmosis unit for treating non-degradable industrial effluent
CN101781048B (en) Low ammonia nitrogen waste water treatment and recycling method
CN205045948U (en) Petrochemical is efficient handling of discharging equipment for sewage
CN109607965A (en) A kind of system and method for sewage treatment plant tail water advanced nitrogen dephosphorization
CN114940561A (en) Oil sludge treatment waste liquid treatment system
CN104710077A (en) Treatment system and treatment method of synthetic rubber wastewater
CN107176679A (en) The aerobic membrane module processing method of anaerobic/anoxic
CN2910906Y (en) Union equipment for treating wastewater contg. difficult degradation substances combined membrane biological reactor and reverse osmosis
CN101514046A (en) Treatment process for manganese-containing organic wastewater membrane bioreactor
CN104787967A (en) Treatment device for slightly-polluted surface water and application thereof
CN104909517A (en) Industrial production wastewater advanced treatment device
CN105174606B (en) A kind of membrane technology medical waste water with disinfection by ultraviolet light processes device
CN204661392U (en) The forward osmosis membrane bioreactor of process Lake Water
CN207552128U (en) A kind of device of integrated membrane process hydridization removal low concentration selenium-containing wastewater
CN209740890U (en) Cutting fluid integration processing apparatus
CN103253836B (en) A kind of percolate deep purifying treatment unit and method
CN213623758U (en) Industrial wastewater treatment device
CN105000714A (en) Coagulation treatment and membrane separation combined waste water treatment system and application thereof
CN107759024A (en) A kind of integrated membrane process hydridization removes the method and device of low concentration selenium-containing wastewater
CN211035625U (en) Sewage split flow-separation treatment assembly

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: 20070613

Termination date: 20100928