CN107998895A - A kind of plate membrane on-line cleaning device and its cleaning method - Google Patents

A kind of plate membrane on-line cleaning device and its cleaning method Download PDF

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Publication number
CN107998895A
CN107998895A CN201810078827.2A CN201810078827A CN107998895A CN 107998895 A CN107998895 A CN 107998895A CN 201810078827 A CN201810078827 A CN 201810078827A CN 107998895 A CN107998895 A CN 107998895A
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China
Prior art keywords
cleaning
plate membrane
cannula
drug
feed pipe
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Application number
CN201810078827.2A
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Chinese (zh)
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CN107998895B (en
Inventor
杨柳
王长鹏
李鹏
杨波
庞新生
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Henan New Investment Environmental Protection Polytron Technologies Inc
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Henan New Investment Environmental Protection Polytron Technologies Inc
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/16Use of chemical agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters
    • 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

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention belongs to plate membrane cleaning technique field, and in particular to a kind of plate membrane on-line cleaning device and its cleaning method.The plate membrane on-line cleaning device includes connected drug-feeding tube and chemical feed pipe, the exit of drug-feeding tube is equipped with atomizer, cannula cleaning is housed by bearing holder (housing, cover) outside chemical feed pipe, chemical feed pipe is equipped with duct, cannula cleaning is equipped with perforate, and opening direction is along cannula cleaning tube wall tangential direction.The cleaning performance of the plate membrane on-line cleaning device of the present invention is good, and easy to use, operating cost saving, has a vast market prospect.

Description

A kind of plate membrane on-line cleaning device and its cleaning method
Technical field
The invention belongs to plate membrane cleaning technique field, and in particular to a kind of plate membrane on-line cleaning device and its cleaning side Method.
Background technology
Membrane bioreactor(MBR)Be gradually rise in recent years it is a kind of in advanced treatment of wastewater technology, because it is with work The many merits such as skill flow is short, high treating effect, floor space is few, microorganism concn is high, are in quick in Practical Project Developing stage.Certainly, MBR is while with many merits, it may have it is certain the shortcomings that:2. 1. fouling membrane than is comparatively fast invested into This is higher.Especially membrane pollution problem, has become a urgent problem to be solved for limiting the popularization of its Rapid Popularization.
Fouling membrane refers to film in filter process, and physics occurs for the particulate, colloidal particle or solute transportation and film in water Adsorbed caused by chemical action or mechanism in film surface or fenestra, deposit and cause membrane aperture to diminish or blocks etc. work With the phenomenon for making film generation permeation flux change with stalling characteristic.For fouling membrane, the structure of film in itself does not occur Change, as long as can just make the performance recovery of film or part return to original state by appropriate cleaning.Therefore, for film Membrane reactor is cleaned in pollution problem, extend the service life of membrane module just become membrane reactor research hot spot ask Topic.
The cleaning way of membrane bioreactor mainly has two kinds at present:On-line cleaning and offline cleaning.It is either online clear Wash or offline cleaning, MBR module are all not normally functioning, the water yield of whole system declines.
A kind of self-cleaning MBR flat sheet membrane module and its cleaning were once disclosed in Chinese patent application 201310314883.9 Method, the membrane module are that plate membrane is fixed in special frame to be made, and add charger to carry out film in frame Gas flushing.The self-cleaning MBR flat sheet membrane module and its cleaning method realize MBR membrane modules self-cleaning in the process of running, pole The earth improves its resistant to pollution ability, but still remains problems with:
1st, chemical is sprayed using orientation, and clean range is limited, and medicament wastes serious;
2nd, purged using gas, power consumption is high, energy waste;
3rd, gas purging deposits the defects of intensity is low, and general effect is poor.
The content of the invention
It is an object of the invention to provide a kind of good, easy to use, operating cost saving the plate membrane of cleaning performance is online Cleaning device and its cleaning method.
To solve above technical problem, the present invention uses following technical scheme:
A kind of plate membrane on-line cleaning device, it is characterised in that including connected drug-feeding tube and chemical feed pipe, the exit of drug-feeding tube Equipped with atomizer, cannula cleaning is equipped with by bearing holder (housing, cover) outside chemical feed pipe, chemical feed pipe is equipped with duct, and cannula cleaning is equipped with Perforate, opening direction are along cannula cleaning tube wall tangential direction.
The drug-feeding tube is formed by connecting You Transverse pipes and vertical tube, and the side of vertical tube is equipped with track, the outer wall of vertical tube equipped with The sliding block of track adaptation.
The outside diameter of the cannula cleaning is less than the spacing of plate membrane, is slightly less than 1-2cm, the length and plate membrane of cannula cleaning Be of same size.
The drug-feeding tube is equipped with booster pump, and drug-feeding tube is flexible duct.
A diameter of 0.1-1mm in duct on the chemical feed pipe.
The atomizer is refraction type atomizer.
The cannula cleaning is lined with the steel-plastics composite pipe of polytetrafluoroethylene ethylene layer for internal layer.
The method cleaned using plate membrane on-line cleaning device to plate membrane, cleaning method step are as follows:1), will be clear Casing is washed to be placed in inside plate membrane;2), the import of drug-feeding tube is connected with equipped with the dosing tank of cleaning agent, cleaning agent is through booster pump Entering atomizer after pressurization to be atomized, the cleaning agent after atomization enters chemical feed pipe and enters cannula cleaning by the duct of chemical feed pipe, Sprayed by the perforate on cannula cleaning, rotate cannula cleaning, the medicament of ejection cleans plate membrane;3), cleaning During, control slide block is moved up and down along track(It is 10-30cm/min to move up and down speed), full side is carried out to plate membrane inside Position cleaning.
The pressure of atomizer is 0.2MPa, flow 50L/h, controls the pressure and flow of atomizer, is to make Cleaning agent is sprayed with suitable state, cannula cleaning rotating speed caused by avoiding hypertonia, flow excessive it is too fast and to plate membrane Damage, also avoid not caused enough the cleaning performance of cleaning pressure of cleaning agent caused by pressure is too low, flow is too small poor.
It is 10-30cm/min to control operating rate control of the cannula cleaning inside plate membrane, this is because speed is too high When, cleaning is difficult to totally thoroughly, and when speed is too low, cleaning efficiency is low and wastes cleaning agent,
Drug-feeding tube is flexible duct, its material is polyesters.
Cannula cleaning is steel-plastics composite pipe, its internal layer is lined with polytetrafluoroethylene ethylene layer.
The beneficial effects of the present invention are:
1)Cleaning performance is good.The cannula cleaning of on-line cleaning device of the present invention is arranged on outside chemical feed pipe by bearing mode, because This can rotate cannula cleaning when being sprayed by the Application of spray chemical cleaning technology for evaporating agent that cannula cleaning sprays through tangential perforate, while dosing Pipe and cannula cleaning can be run up and down along track, so that cannula cleaning can be inside plate membrane after being placed in plate membrane inside Operation up and down, since the chemical that rotation sprays is comprehensive to plate membrane progress, is cleaned without dead angle, clean range is wider, Effect is more preferable.
2)It is easy to use, it is stable.On-line cleaning device using the present invention carries out plate membrane on-line cleaning, cleaning Process can cover the Life cycle of plate film assembly.Using apparatus of the present invention in the cleaning process to plate membrane, it is not necessary to Plate membrane is stopped intaking, does not influence the production water and treatment effeciency of MBR processing systems.
3)Operating cost is low.Cleaning agent passes through atomizer to on-line cleaning device of the present invention in use Atomization process, makes cleaning agent enter chemical feed pipe and cannula cleaning in spray pattern, and final spray pattern, which sprays, is cleaned, can be The usage amount of cleaning agent is reduced on the premise of reaching same cleaning performance, saves reagent cost.
Brief description of the drawings
Fig. 1 is the structure diagram of the plate membrane on-line cleaning device of the present invention.
Fig. 2 is the chemical feed pipe of plate membrane on-line cleaning device of the present invention and the structure diagram of cannula cleaning.
Fig. 3 is the chemical feed pipe of plate membrane on-line cleaning device of the present invention and the sectional view of cannula cleaning.
Embodiment
The present invention is described in detail with reference to embodiments:
Plate membrane on-line cleaning device as shown in Figure 1, including drug-feeding tube 3 and chemical feed pipe 6,3 You Transverse pipes 31 of drug-feeding tube and vertical tube 32 are formed by connecting, and transverse tube 31 is equipped with booster pump 2, the side of vertical tube 32 is equipped with track 9, and the outer wall of vertical tube 32 is equipped with and rail The sliding block 8 that road 9 is adapted to;The vertical tube 32 of drug-feeding tube 3 links together with chemical feed pipe 6, and 32 exit of vertical tube of drug-feeding tube 3 is equipped with folding Penetrate formula atomizer 5;Cannula cleaning 7 is set with by bearing 4 outside chemical feed pipe 6, as shown in Fig. 2, chemical feed pipe 6 is equipped with diameter The duct of 0.1-1mm, cannula cleaning 7 are equipped with perforate, and opening direction is along 7 tube wall tangential direction of cannula cleaning.
Specifically, the outside diameter of cannula cleaning 7 is less than the spacing of plate membrane, is slightly less than 1-2cm, the length of cannula cleaning 7 with Plate membrane is of same size, and the material of drug-feeding tube 3 is the flexible duct of polyesters;The material of cannula cleaning 7 is Copper-plastic Composite Pipe, Polytetrafluoroethylene ethylene layer is lined with inner wall.
The sliding block 8 of the present invention can use the mechanism or telescopic of walking about of stylus printer when being run along track about 9 Connecting tube, or hydraulic gear is set.
When plate membrane on-line cleaning device using the present invention cleans plate membrane, cleaning method is as follows:1), will be clear Casing 7 is washed to be placed in inside plate membrane;2), the import of 3 Transverse pipes 31 of drug-feeding tube is connected with equipped with the dosing tank 1 of cleaning agent, clean Agent is atomized after the pressurization of booster pump 2 into refraction type atomizer 5, and the cleaning agent after atomization enters chemical feed pipe 6 and by chemical feed pipe 6 Duct enter cannula cleaning 7, by cannula cleaning 7 perforate spray, rotate cannula cleaning 7, the medicament pair of ejection Plate membrane is cleaned;3), in cleaning process, 10 control slide block 8 of electric control part is along track 9 with the speed of 10-30cm/min Lower movement, so as to drive cannula cleaning 7 to move up and down inside plate membrane, the cleaning agent sprayed by cannula cleaning 7 is to plate membrane Inside carries out comprehensive cleaning.
During use, the pressure for controlling refraction type atomizer 5 is 0.2MPa, and flow 50L/h, makes cleaning agent with most Good pressure and flow spray, and neither damage plate membrane can be realized most preferably in the state of cleaning agent dosage minimum again at this time Cleaning performance.The operating rate of control slide block 8, operating rate of the cannula cleaning 7 inside plate membrane is moderate at this time.

Claims (9)

1. a kind of plate membrane on-line cleaning device, it is characterised in that including connected drug-feeding tube and chemical feed pipe, the outlet of drug-feeding tube Place is equipped with atomizer, cannula cleaning is housed by bearing holder (housing, cover) outside chemical feed pipe, chemical feed pipe is equipped with duct, is set on cannula cleaning There is perforate, opening direction is along cannula cleaning tube wall tangential direction.
2. plate membrane on-line cleaning device as claimed in claim 1, it is characterised in that the drug-feeding tube You Transverse pipes and vertical tube connect Connect and form, the side of vertical tube is equipped with track, and the outer wall of vertical tube is equipped with the sliding block being adapted to track.
3. plate membrane on-line cleaning device as claimed in claim 1 or 2, it is characterised in that the outside diameter of the cannula cleaning is small In the spacing of plate membrane, the length of cannula cleaning and being of same size for plate membrane.
4. plate membrane on-line cleaning device as claimed in claim 1 or 2, it is characterised in that the drug-feeding tube is equipped with supercharging Pump, drug-feeding tube is flexible duct.
5. plate membrane on-line cleaning device as claimed in claim 1 or 2, it is characterised in that duct is straight on the chemical feed pipe Footpath is 0.1-1mm.
6. plate membrane on-line cleaning device as claimed in claim 1 or 2, it is characterised in that the atomizer is refraction type Atomizer.
7. plate membrane on-line cleaning device as claimed in claim 1 or 2, it is characterised in that the cannula cleaning serves as a contrast for internal layer There is the steel-plastics composite pipe of polytetrafluoroethylene ethylene layer.
8. a kind of method cleaned using any one of the claim 1-7 plate membrane on-line cleaning devices to plate membrane, It is characterized in that, cleaning method is as follows:1), cannula cleaning is placed in inside plate membrane;2), by the import of drug-feeding tube with equipped with clear The dosing tank connection of lotion, cleaning agent enter atomizer after booster pump pressurizes and are atomized, and the cleaning agent after atomization enters dosing Manage and cannula cleaning is entered by the duct of chemical feed pipe, sprayed by the perforate on cannula cleaning, rotate cannula cleaning, spray Medicament plate membrane is cleaned;3), in cleaning process, control slide block is moved up and down along track, and plate membrane inside is carried out Comprehensive cleaning.
9. cleaning method as claimed in claim 8, it is characterised in that:The pressure of atomizer is 0.2MPa, flow 50L/ h。
CN201810078827.2A 2017-06-30 2018-01-26 Online cleaning device and cleaning method for flat film Active CN107998895B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN2017105201725 2017-06-30
CN201710520172.5A CN107224880A (en) 2017-06-30 2017-06-30 A kind of Flat Membrane on-line cleaning device and its cleaning method

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CN107998895A true CN107998895A (en) 2018-05-08
CN107998895B CN107998895B (en) 2024-07-02

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CN201710520172.5A Pending CN107224880A (en) 2017-06-30 2017-06-30 A kind of Flat Membrane on-line cleaning device and its cleaning method
CN201810078827.2A Active CN107998895B (en) 2017-06-30 2018-01-26 Online cleaning device and cleaning method for flat film
CN201820136359.5U Active CN208449072U (en) 2017-06-30 2018-01-26 A kind of plate membrane on-line cleaning device

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107224880A (en) * 2017-06-30 2017-10-03 河南新投环保科技股份有限公司 A kind of Flat Membrane on-line cleaning device and its cleaning method
CN108579445B (en) * 2018-04-08 2020-08-04 湖南烁普新材料有限公司 Porous membrane diluent extraction device, extraction method and porous membrane preparation method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004056458A2 (en) * 2002-12-19 2004-07-08 Hydranautics Methods for cleaning and maintaining membrane surface during filtration
CN102423640A (en) * 2011-10-18 2012-04-25 华北电力大学 Integrated membrane module including on-line ultrasonic monitoring and cleaning
CN104944571A (en) * 2015-06-16 2015-09-30 南京中材水务股份有限公司 Impulse type flushing device for flat membrane bioreactor and flushing method thereof
CN105692873A (en) * 2014-11-27 2016-06-22 同济大学 On-line cleaning equipment of membrane bioreactor and method thereof
CN206262501U (en) * 2016-12-14 2017-06-20 洛阳中超新材料股份有限公司 A kind of autoclave cleaning device
CN208449072U (en) * 2017-06-30 2019-02-01 河南新投环保科技股份有限公司 A kind of plate membrane on-line cleaning device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004056458A2 (en) * 2002-12-19 2004-07-08 Hydranautics Methods for cleaning and maintaining membrane surface during filtration
CN102423640A (en) * 2011-10-18 2012-04-25 华北电力大学 Integrated membrane module including on-line ultrasonic monitoring and cleaning
CN105692873A (en) * 2014-11-27 2016-06-22 同济大学 On-line cleaning equipment of membrane bioreactor and method thereof
CN104944571A (en) * 2015-06-16 2015-09-30 南京中材水务股份有限公司 Impulse type flushing device for flat membrane bioreactor and flushing method thereof
CN206262501U (en) * 2016-12-14 2017-06-20 洛阳中超新材料股份有限公司 A kind of autoclave cleaning device
CN208449072U (en) * 2017-06-30 2019-02-01 河南新投环保科技股份有限公司 A kind of plate membrane on-line cleaning device

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CN208449072U (en) 2019-02-01
CN107224880A (en) 2017-10-03
CN107998895B (en) 2024-07-02

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