CN110357246A - A kind of sewage-treatment plant based on ceramic membrane - Google Patents

A kind of sewage-treatment plant based on ceramic membrane Download PDF

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Publication number
CN110357246A
CN110357246A CN201810296271.4A CN201810296271A CN110357246A CN 110357246 A CN110357246 A CN 110357246A CN 201810296271 A CN201810296271 A CN 201810296271A CN 110357246 A CN110357246 A CN 110357246A
Authority
CN
China
Prior art keywords
ceramic membrane
pipe
backwash
valve
water
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.)
Pending
Application number
CN201810296271.4A
Other languages
Chinese (zh)
Inventor
蒋发光
朱云鹏
张启伟
朱钵
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.)
Southwest Petroleum University
Original Assignee
Southwest Petroleum University
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 Southwest Petroleum University filed Critical Southwest Petroleum University
Priority to CN201810296271.4A priority Critical patent/CN110357246A/en
Publication of CN110357246A publication Critical patent/CN110357246A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08Flat membrane modules
    • 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
    • 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
    • C02F3/10Packings; Fillings; Grids
    • C02F3/102Permeable membranes
    • 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
    • B01D2321/04Backflushing
    • 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
    • B01D2321/18Use of gases
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/006Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/008Mobile apparatus and plants, e.g. mounted on a vehicle
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/03Pressure
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/40Liquid flow rate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • 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

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (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)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The present invention relates to a kind of aerobe flat ceramic film process waste plants, it is characterized in that being opened and closed using a production water pump by pressure change control valve, it is directly changed the working condition of ceramic membrane, other water pumps are replaced without closing, package unit, which can be arranged, to be mounted on moveable trolley.The present invention is mainly made of vehicle frame, production water pump, filter tank, clear water reserviors, flat ceramic membrane filtration module, ceramic membrane bracket, oxygen increasing pump, micropore aeration pipe, appendix etc..Compared to conventional panel ceramics membrane treatment appts, 1) working condition can be switched fast by including, without closing replacement water pump;2) package unit, which can be arranged, is mounted on moveable trolley, simplifies structure, saves space;3) structurally reasonable, practical, reduce cost.The method of the present invention can be used for common laboratory, the waste water after small-sized plant area's processing is biochemical.

Description

A kind of sewage-treatment plant based on ceramic membrane
Technical field
The present invention relates to a kind of technical fields with flat ceramic film process sewage, specially a kind of to be based on flat ceramic The sewage-treatment plant of film.
Background technique
Sewage in direct emission production and living, it will lead to the pollution of environment and the waste of water resource.How economy has The improvement effluent problem of effect is just particularly important, and is found efficient sewage disposal technology and is become and grinds to be very valuable Study carefully project.Flat ceramic membrane biological reaction apparatus is exactly the water process skill for combining biological treatment process and membrane separating process There is more significant advantage, technology to be applied to sewage treatment for art, opposite traditional biological processing technique, membrane technology Industry plays a significant role wherein.
From the point of view of domestic related flat ceramic film process sewage device development, country's mainstream membrane treatment appts are with life at present Based on object film, but biomembrane is easy to be contaminated in the long-term use, when being able to maintain that inside the plan normal membrane flux Between it is short, membrane module must be needed replacing if reaching target for a long time, increases whole investment and related operation cost. For Relative biological film, ceramic membrane can overcome the problems, such as major part existing for biomembrane.Ceramic membrane selection uses pottery Porcelain material is able to maintain long-term efficient and stable filtering, maintains the service life of normal membrane flux compared to for biomembrane It is significantly to improve.But because of the method that ceramic membrane system for handling still indiscriminately imitates biological film process at present, taken out using water pump is produced Water is rinsed using backwashing pump, and needing two water pumps is also two processes, and whole system needs to keep one to open one when working The working condition closed, and residual gas is had in pipe-line system, due to the brittleness of ceramic material itself, during backwash Ceramic membrane adversely affects, and influences the normal use of ceramic membrane.
In view of the above drawbacks, it is necessary to design a kind of sewage-treatment plant based on ceramic membrane.
Summary of the invention
The method that the present invention solves technical problem essentially consists in: being opened using a production water pump by pressure change control valve It closes, is directly changed the working condition of ceramic membrane, replace other water pumps without closing, simplify working forms;Package unit It can arrange and be mounted on moveable trolley, provide a kind of relatively reliable based on flat ceramic film sewage treatment device.
The technical scheme is that
A kind of sewage-treatment plant based on ceramic membrane comprising vehicle frame produces water pump, filter tank, clear water reserviors, plate pottery Porcelain membrane filtration module, ceramic membrane bracket, oxygen increasing pump, micropore aeration pipe, appendix, it is characterised in that: bottom of frame is rectangle frame Filter tank and clear water reserviors are arranged in frame structure, the left and right sides;Oxygen increasing pump is arranged on oxygen increasing pump workbench in centre, is connected by appendix Micropore aeration pipe is connect, setting produces water pump on producing pump working platform;The filter tank and clear water reserviors are reserved by quarter bend on vehicle frame Installation site is embedded in vehicle frame, and filter tank and clear water reserviors are equipped with exhaust-valve in same side;Ceramic membrane bracket is set in the middle part of the bottom of filter tank It which is provided with three micropore aeration pipes, flat ceramic membrane filtration module is embedded in the installation site reserved on ceramic membrane bracket;It is described Flat ceramic membrane filtration module, clear water reserviors produce between water pump through drainage-counter-flushing pipeline system connection, drainage-backwash Pipe-line system includes ceramic membrane instrumentation tubes, exhaust pipe, exhaust valve, positive pressure table, positive pressure table control valve, vacuum table, vacuum table It is control valve, water pressure sensing pipe, outlet valve, outlet pipe, backwash valve, backwash tube, flowmeter, flow detection pipe, trap, anti- Rinse inlet valve and backwash water inlet pipe composition.
Flat ceramic membrane filtration module is connect with ceramic membrane instrumentation tubes, ceramic membrane instrumentation tubes, exhaust pipe and water Detection pipe is pressed to connect by threeway, exhaust pipe is equipped with exhaust valve, and water pressure sensing pipe is equipped with positive pressure table and vacuum table leads to respectively It crosses positive pressure table control valve and vacuum table control valve is controlled;Water pressure sensing pipe, backwash tube and trap are connected by threeway, Backwash tube is equipped with backwash valve;Trap, backwash water inlet pipe and produce pump intake and be connected by threeway, backwash into Water pipe is equipped with backwash inlet valve, and the other end connects clear water reserviors side away from bottom of pond middle position;Flow detection pipe, backwash tube It is connected with outlet pipe by threeway, flow detection pipe is equipped with flowmeter, and outlet pipe is equipped with outlet valve.
Compared with prior art, the present invention has the beneficial effect that:
(1) present invention considers the characteristic of ceramic membrane, is opened using a production water pump by pressure change control valve It closes, is directly changed the working condition of ceramic membrane, replace other water pumps without closing, simplify working forms, improve whole The efficiency of a sewage-treatment plant.It has simplified in sewage disposal system, has recoiled using production water pump suction drainage, using backwashing pump Wash membrane module, traditional water treatment structure that two pumps machine opens and closes cycle operation respectively, frequently switches on.
(2) equipment production cost and operating cost are reduced present invention utilizes the pipeline structure singly pumped, easy maintenance, Working efficiency is higher than classic flat-plate ceramics film sewage treatment device, keeps a whole set of flat ceramic film sewage treatment device more easily single Memberization, modularization.
(3) package unit of the present invention, which can be arranged, is mounted on moveable trolley, is easy to use.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram one of the sewage-treatment plant based on ceramic membrane of the present invention.
Fig. 2 is drainage-counter-flushing pipeline system cross-sectional view in Fig. 1.
Fig. 3 is a kind of structural schematic diagram two of the sewage-treatment plant based on ceramic membrane of the present invention.
Fig. 4 is body frame structure for automotive schematic diagram of the invention.
In figure: 1. vehicle frames;2. castor;3. filter tank;4. ceramic membrane instrumentation tubes;5. exhaust pipe;6. exhaust valve;7. positive pressure Table;8. positive pressure table control valve;9. vacuum table;10. vacuum table control valve;11. water pressure sensing pipe;12. outlet valve;13. outlet pipe; 14. backwash valve;15. backwash tube;16. flowmeter;17. flow detection pipe;18. trap;19. backwashing inlet valve;20. Clear water reserviors;21. exhaust-valve;22. backwashing water inlet pipe;23. producing water pump;24. oxygen increasing pump;25. oxygen increasing pump workbench;26. producing Pump working platform;27. appendix;28. flat ceramic membrane filtration module;29. ceramic membrane bracket;30. micropore aeration pipe.
Specific embodiment
The present invention is not limited by following embodiments, can be determined according to the technique and scheme of the present invention with actual conditions Specific embodiment.Below with reference to Fig. 1~4 pair, the present invention is described below.The positional relationship of upper and lower, left and right etc. is foundation The layout direction of Figure of description 1 determines.
3 bottom of vehicle frame is rectangular frame structure, and filter tank 3 and clear water reserviors 20 are arranged in the left and right sides;Centre is in oxygenation pump work Oxygen increasing pump 24 is set on platform 25, micropore aeration pipe 30 is connected to the inner aeration in filter tank 3 by appendix 27, is put down producing pump working Setting produces water pump 23 on platform 26;The filter tank 3 and clear water reserviors 20 are embedded in vehicle frame 1 by the reserved installation site of quarter bend on vehicle frame 1 In;Setting ceramic membrane bracket 29 which is provided with three micropore aeration pipes 30, flat ceramic membrane filtration module in the middle part of 3 bottom of filter tank The installation site reserved on 28 insertion ceramic membrane brackets 29.Flat ceramic membrane filtration module 28, produces between water pump 23 clear water reserviors 20 By drainage-counter-flushing pipeline system connection, realizes and carry out drainage process and backwash process.
Drainage-counter-flushing pipeline system is specifically installed as flat ceramic membrane filtration module 28 and ceramic membrane instrumentation tubes 4 Connection, ceramic membrane instrumentation tubes 4, exhaust pipe 5 are connected with water pressure sensing pipe 11 by threeway, and exhaust pipe 5 is equipped with exhaust valve 6, water pressure sensing pipe 11 is equipped with positive pressure table 7 and vacuum table 9 and is carried out respectively by positive pressure table control valve 8 and vacuum table control valve 10 Control;Water pressure sensing pipe 11, backwash tube 15 are connected with trap 18 by threeway, and backwash tube 15 is equipped with backwash valve 14;Trap 18, backwash water inlet pipe 22 and production 23 water inlet of water pump are connected by threeway, and backwash water inlet pipe 22 is equipped with anti- Rinse inlet valve 19, the middle position of backwash 22 other end of water inlet pipe connection 20 side of clear water reserviors;Flow detection pipe 17, recoil It washes pipe 15 to connect with outlet pipe 13 by threeway, flow detection pipe 17 is equipped with flowmeter 16, and outlet pipe 13 is equipped with outlet valve 12。
The principle of the present invention is: will be by the waste water access filter tank 3 after biochemical treatment, sewage be have passed through by thick Filter, preliminary sedimentation, anaerobism, aerobic, materialization or other processing.The depth of water keeps 180mm~200mm to exceed ceramic membrane before drainage Filter assemblies 28, when drainage, need to open vacuum table control valve 10, trap 18 and outlet valve 12, close other all valves. The negative pressure that sewage is generated because producing 23 suction capacity of water pump, is sucked into ceramic membrane by flat ceramic membrane filtration module 28 and is worked Pipe 4 enters through water pressure sensing pipe 11 and trap 18 and produces water pump 23, enters outlet pipe 13 by flow detection pipe 17 later, 20 top of clear water reserviors flows into clear water reserviors 20.There is 80mm above diaphragm when the water surface drops to ceramic membrane filter assemblies 28 At~100mm, production water pump 23, which should stop working, avoids flat ceramic membrane filtration module 28 from exposing the surface.
9 pressure of vacuum table is stablized when normal table works tends towards stability in 0.025MPa~0.035MPa, production water flow, when 9 pressure of vacuum table carries out backwash when rising to 0.045MPa~0.055MPa.Need to open positive pressure table control valve 8 when backwash, Backwash valve 14 and backwash inlet valve 19, close other all valves.Clear water enters backwash water inlet pipe from clear water reserviors 20 22, which are produced water pump 23, flow detection pipe 17, backwash tube 15, water pressure sensing pipe 11, ceramic membrane instrumentation tubes 4, enters plate pottery Porcelain membrane filtration module 28, the dirt of flushing membrane on piece attachment.If corresponding situation can also be seriously added in blocking in clear water reserviors 20 Chemical agent carries out chemical cleaning.
Oxygen increasing pump 24 connects three micropore aeration pipes 30 on ceramic membrane bracket 29 by appendix 27, keeps exposing filter tank 3 Gas is that aerobic microbiological supplemental oxygen and auxiliary cleaning carry out cleaning flat ceramic membrane filtration module 28.
Exhaust pipe 5 and exhaust valve 6 be mainly used for sewage-treatment plant install for the first time or for a long time be not used after, work for the first time When exclude pipeline internal system gas.
Exhaust-valve 21 is mainly used for the spoil disposal of sewage-treatment plant, maintenance, sampling.
The present invention is not limited to above-mentioned specific embodiment, and those skilled in the art are from the above idea not By creative labor, the various transformation made are within the scope of the present invention.

Claims (2)

1. a kind of sewage-treatment plant based on ceramic membrane comprising vehicle frame (1), clear water reserviors (20), produces water at filter tank (3) Pump (23), flat ceramic membrane filtration module (28), ceramic membrane bracket (29), micropore aeration pipe (30), oxygen increasing pump (24), appendix (27), it is characterised in that: vehicle frame (1) bottom is rectangular frame structure, and filter tank (3) and clear water reserviors (20) are arranged in the left and right sides, in Between on oxygen increasing pump workbench (25) be arranged oxygen increasing pump (24), by appendix (27) connect micropore aeration pipe (30), producing Setting produces water pump (23) on pump working platform (26);The filter tank (3) and clear water reserviors (20) are reserved by quarter bend on vehicle frame (1) Installation site is embedded in vehicle frame (1), and filter tank (3) and clear water reserviors (20) are equipped with exhaust-valve (21) in same side;Filter tank (3) bottom Middle part setting ceramic membrane bracket (29) which is provided with three micropore aeration pipes (30), flat ceramic membrane filtration module (28) insertion pottery The installation site reserved on porcelain film bracket (29);The flat ceramic membrane filtration module (28), produces water pump (23) at clear water reserviors (20) Between by the connection of drainage-counter-flushing pipeline system, drainage-counter-flushing pipeline system include ceramic membrane instrumentation tubes (4), Exhaust pipe (5), exhaust valve (6), positive pressure table (7), positive pressure table control valve (8), vacuum table (9), vacuum table control valve (10), hydraulic pressure Detection pipe (11), outlet valve (12), outlet pipe (13), backwash valve (14), backwash tube (15), flowmeter (16), flow inspection Test tube (17), trap (18), backwash inlet valve (19) and backwash water inlet pipe (22) composition.
2. drainage as described in claim 1-counter-flushing pipeline system group becomes ceramic membrane filter assemblies (28) and plate is made pottery Porcelain film instrumentation tubes (4) connection, ceramic membrane instrumentation tubes (4), exhaust pipe (5) and water pressure sensing pipe (11) are connected by threeway, Exhaust pipe (5) is equipped with exhaust valve (6), and water pressure sensing pipe (11) is equipped with positive pressure table (7) and vacuum table (9) passes through positive pressure respectively Table control valve (8) and vacuum table control valve (10) are controlled;Water pressure sensing pipe (11), backwash tube (15) and trap (18) It is connected by threeway, backwash tube (15) is equipped with backwash valve (14);Trap (18), backwash water inlet pipe (22) He Chanshui It pumps (23) water inlet to be connected by threeway, backwash water inlet pipe (22) is equipped with backwash inlet valve (19), and other end connection is clear Pond (20) side is away from bottom of pond middle position;Flow detection pipe (17), backwash tube (15) and outlet pipe (13) lead to by three It connects, flow detection pipe (17) is equipped with flowmeter (16), and outlet pipe (13) is equipped with outlet valve (12).
CN201810296271.4A 2018-03-30 2018-03-30 A kind of sewage-treatment plant based on ceramic membrane Pending CN110357246A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810296271.4A CN110357246A (en) 2018-03-30 2018-03-30 A kind of sewage-treatment plant based on ceramic membrane

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Application Number Priority Date Filing Date Title
CN201810296271.4A CN110357246A (en) 2018-03-30 2018-03-30 A kind of sewage-treatment plant based on ceramic membrane

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CN110357246A true CN110357246A (en) 2019-10-22

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006281031A (en) * 2005-03-31 2006-10-19 Hitachi Plant Technologies Ltd Method of washing flat membrane element used for membrane filter device, and membrane filter device
CN103752175A (en) * 2014-01-22 2014-04-30 浙江卓锦工程技术有限公司 Immersed type on-line cleaning method and device for slab ceramic membrane
JP2015160181A (en) * 2014-02-28 2015-09-07 株式会社明電舎 Membrane module cleaning method
CN105417633A (en) * 2016-01-13 2016-03-23 烟台海德专用汽车有限公司 Sewage treatment system with integral ceramic membrane filters
CN206173081U (en) * 2016-10-28 2017-05-17 北京博鑫精陶环保科技有限公司 Little integrated equipment of dull and stereotyped ceramic membrane reuse of reclaimed water
CN107337326A (en) * 2017-09-06 2017-11-10 江西博鑫精陶环保科技有限公司 A kind of ceramic membrane aeration and pressure-fired ozone film reused water processing method and processing unit

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006281031A (en) * 2005-03-31 2006-10-19 Hitachi Plant Technologies Ltd Method of washing flat membrane element used for membrane filter device, and membrane filter device
CN103752175A (en) * 2014-01-22 2014-04-30 浙江卓锦工程技术有限公司 Immersed type on-line cleaning method and device for slab ceramic membrane
JP2015160181A (en) * 2014-02-28 2015-09-07 株式会社明電舎 Membrane module cleaning method
CN105417633A (en) * 2016-01-13 2016-03-23 烟台海德专用汽车有限公司 Sewage treatment system with integral ceramic membrane filters
CN206173081U (en) * 2016-10-28 2017-05-17 北京博鑫精陶环保科技有限公司 Little integrated equipment of dull and stereotyped ceramic membrane reuse of reclaimed water
CN107337326A (en) * 2017-09-06 2017-11-10 江西博鑫精陶环保科技有限公司 A kind of ceramic membrane aeration and pressure-fired ozone film reused water processing method and processing unit

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