CN104071943B - Fibre bundle filtration membrane biological reaction apparatus - Google Patents

Fibre bundle filtration membrane biological reaction apparatus Download PDF

Info

Publication number
CN104071943B
CN104071943B CN201310103878.3A CN201310103878A CN104071943B CN 104071943 B CN104071943 B CN 104071943B CN 201310103878 A CN201310103878 A CN 201310103878A CN 104071943 B CN104071943 B CN 104071943B
Authority
CN
China
Prior art keywords
water
biological reaction
fibre bundle
outlet
automatic valve
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
Application number
CN201310103878.3A
Other languages
Chinese (zh)
Other versions
CN104071943A (en
Inventor
沈英立
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.)
Beijing first road water treatment New Technologies Inc
Original Assignee
沈英立
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 沈英立 filed Critical 沈英立
Priority to CN201310103878.3A priority Critical patent/CN104071943B/en
Publication of CN104071943A publication Critical patent/CN104071943A/en
Application granted granted Critical
Publication of CN104071943B publication Critical patent/CN104071943B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention discloses a kind of fibre bundle filtration membrane biological reaction apparatus, including biological reaction pool, this biological reaction pool includes water inlet, outlet, aeration opening, biological reaction pool has been covered with the antibacterial for degradation of organic substances, device also includes that, without constraint fiber bundle filter system, this nothing constraint fiber bundle filter system includes without constraint fiber bundle filter;The fibre bundle accumulation horizon that this nothing constraint fiber bundle filter includes in container, container in the lower porous plate of bottom, container, this fibre bundle accumulation horizon is made up of some free accumulation fibre bundle on this lower porous plate;The outlet of biological reaction pool connects this nothing constraint fiber bundle filter.Present configuration is simple, be readily cleaned, it is possible to decrease produce and maintenance cost.

Description

Fibre bundle filtration membrane biological reaction apparatus
Technical field
The present invention relates to a kind of membrane bioreactor, particularly relate to a kind of fibre bundle utilizing free accumulation and enter The membrane biological reaction apparatus that row filters.
Background technology
At sewage treatment area, the membrane bioreactor developed rapidly in recent years occupies very important Status.It possesses high organic matter degradation ability, and not only sludge discharge is few, and effluent quality is fine, can It is used directly as middle water, it is possible to be further utilized to prepare pure water.Existing membrane bioreactor is at it Water outlet is designed with one group of higher filter of filtering accuracy, and one is to improve the water quality after process, also It is to improve the density of flora in reactor, prevents reacting flora and run off with product water, reduce treatment effeciency.
Existing membrane bioreactor uses more filter have: hollow fiber membrane ultrafiltration device, and use The filter of filter plate composition, the work principle of filter of these filters is all that traditional embrane method filters, and traditional film Method filters and has the drawback that: structure is complicated, cost is high, dirt is cleaned relatively difficult after blocking up, fine for hollow Dimension ultrafilter, its operating fracture of wire and the problem of cleaning are more, and this just shortens the service life of filter, Add operation and the maintenance cost of membrane bioreactor.
Summary of the invention
In view of the foregoing, it is an object of the invention to provide a kind of fibre bundle filtration membrane biological reaction apparatus. It, by using the fibre bundle of free accumulation to filter, not only can ensure effluent quality, and simple in construction, It is readily cleaned and changes, and then production and maintenance cost can be reduced.
For achieving the above object, the present invention is by the following technical solutions:
A kind of fibre bundle filtration membrane biological reaction apparatus, including biological reaction pool, this biological reaction pool include into The mouth of a river, outlet, aeration opening, be covered with the antibacterial for degradation of organic substances in biological reaction pool, its feature Being, it also includes:
Without constraint fiber bundle filter system, this nothing constraint fiber bundle filter system includes without constraint fibre bundle Filter;This nothing constraint fiber bundle filter includes in container, container in the lower porous plate of bottom, container Fibre bundle accumulation horizon, this fibre bundle accumulation horizon is by some free accumulation fibre bundle structure on this lower porous plate Become;
The outlet of described biological reaction pool connects this nothing constraint fiber bundle filter.
Further:
Described nothing constraint fiber bundle filter is built in described biological reaction pool, described without constraint fibre bundle mistake Filter is provided with lower outlet, and this lower outlet keeps sealing to connect with the outlet of described biological reaction pool.
Described nothing constraint fiber bundle filter system also includes air water backwash import and the first automatic valve, this air water Backwash import connects by this first automatic valve and described container are internal.
Described air water backwash import is connected with described lower outlet by described first automatic valve.
Described nothing constraint fiber bundle filter system also includes finished product water pump, and described lower outlet is by this finished product Water pump connects with product water outlet.
Described nothing constraint fiber bundle filter system also includes the second automatic valve, and described lower outlet is by described Finished product water pump and this second automatic valve connect with described product water outlet.
Described nothing constraint fiber bundle filter system also includes the 3rd automatic valve, and described lower outlet is by described Finished product water pump and the 3rd automatic valve connect with flushing water recovery tube.
Described nothing constraint fiber bundle filter also includes being located at the upper barrier of described container internal upper part, upper porous Plate, is located at the lower barrier of bottom in described container.
Described nothing constraint fiber bundle filter is placed on described biological reaction pool, described without constraint fibre bundle filtration Device is provided with water inlet, and the outlet of described biological reaction pool keeps sealing to connect with water inlet on this.
Described fibre bundle has two kinds of versions, and the first is that the two ends of fibre bundle are broken into fast knot, fiber Shu Changdu determines according to described volume of a container size and filtered water stream amount, and the second is that the fiber of pencil is compiled Being made into the fabric of lamellar or bar shaped, its area and thickness determine according to described volume of a container size.
It is an advantage of the current invention that:
1, in the present invention, the fibre bundle without constraint fiber bundle filter use free accumulation of filtration enters Row filters, and not only filtering accuracy is good, and without mechanical part anchoring fiber bundle, only needs natural packing to exist On lower stop net and lower porous plate, simplify the structure of filter, reduce filter volume;
Without mechanically actuated when 2, carrying out backwash and regenerate, change and safeguard the extremely simple convenience of fibre bundle, And regeneration is very thorough, does not results in the blocking of filter, thus can improve filter efficiency and the fortune thereof of filter Reliability during row;
3, fibre bundle self has the longest life cycle, thus also can ensure device without frequent replacing Properly functioning;
4, simple in construction, be readily cleaned, without frequently changing fibre bundle, and then reduce production and safeguard Cost.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention is further detailed explanation.
Fig. 1 is the structural representation of the present invention.As it can be seen, the fibre bundle filtration membrane biological reaction of the present invention Device includes biological reaction pool 1 and without constraint fiber bundle filter system.Wherein, biological reaction pool 1 includes Water inlet 14, aeration opening 15 and outlet, be covered with the antibacterial for degradation of organic substances in biological reaction pool.
The nothing about bundle fiber being connected to biological reaction pool water outlet is included without constraint fiber bundle filter system Beam filter device 2, this nothing constraint fiber bundle filter 2 include the lower barrier of bottom in container 3, container 3, By the fibre bundle accumulation horizon 4 of some fibre bundle free accumulation on lower porous plate 5 and lower porous plate 5, Container 3 is provided with lower outlet 6.
Air water backwash import 7 and the first automatic valve 8, this air water is also included without constraint fiber bundle filter system Backwash import 7 is connected with lower outlet 6 by this first automatic valve 8.
Finished product water pump the 9, second automatic valve 10 and the 3rd automatic valve is also included without constraint fiber bundle filter system 11, lower outlet 6 is connected with product water outlet 12 by finished product water pump 9 and the second automatic valve 10;Under Outlet 6 is connected with flushing water recovery tube 13 by finished product water pump 9 and the 3rd automatic valve 11.
The work process of the fibre bundle filtration membrane biological reaction apparatus of the present invention is:
Pending sewage is entered biological reaction pool 1 by water inlet 14, and the air of outside press-in is via aeration opening 15 enter biological reaction pools 1, to maintain the normal breeding of antibacterial in biological reaction pool 1 and Organic substance in water Degraded;Now the first automatic valve 8 is closed, and finished product water pump 9 operates, and the second automatic valve 10 is opened, under go out Presenting negative pressure at the mouth of a river 6, the water in biological reaction pool 1 retrains the filtration of fiber bundle filter 2 through nothing, Discharge from product water outlet 12 after becoming clear water;
Along with water pollutant is in the gradually accumulation on fibre bundle accumulation horizon 4 surface, at product water outlet 12 The water yield is gradually reduced, and when dropping to certain value, fibre bundle filtration membrane biological reaction apparatus proceeds to recoil automatically Wash state.Under this state, finished product water pump 9 shuts down, and the second automatic valve 10 and the 3rd automatic valve 11 close Closing, and the first automatic valve 8 is opened, compressed air and backwashing water enter container 3 via air water backwash mouth 7 Bottom, and upwardly fibre bundle accumulation horizon 4 so that be separated from each other between each fibre bundle, and upwards rise Rising, stir, collide, dirt comes off from fibre bundle surface immediately;Meanwhile, aeration opening 15 enter Compressed air still continue, the water of container 3 periphery still in flowing and seethe state, therefore, from fiber The dirt major part come off on bundle all flow back into the water body of biological reaction pool 1 along with the backwashing water moved upward In;
In the final stage of backwash, in order to avoid dirt leaks into product water outlet, dirty in container 3 must be accelerated The mass rate of emission of thing, so that container internal cleaning is clean, this is accomplished by after backwash has carried out a period of time, By the water containing dirt of outflow at lower outlet 6 in flushing water recovery tube 13 is transmitted back to biological reaction pool 1. Now, as long as the first automatic valve 8 and the second automatic valve 10 being closed, open finished product water pump 9 and simultaneously Three automatic valves 11, so, under the swabbing action of finished product water pump 9, containing dirt in container 3 Flushing water can quickly discharge and return in biological reaction pool 1 via flushing water recovery tube 13;
After backwash terminates, being purified for filtering the fibre bundle of dirt, device comes back to filter dirt The normal operating conditions of water, without causing the blocking of filter, and can maintain antibacterial foot in biological reaction pool Enough density and normally breeding, to ensure the degraded of Organic substance in water.
It addition, in backwash process, for preventing the loss of fibre bundle, can arrange in container 3 internal upper part Barrier and upper porous plate 16, to stop that fibre bundle seethes in biological reaction pool 1;When fiber changed by needs During bundle accumulation horizon 4, as long as upper barrier and upper porous plate 16 are unloaded, the fibre bundle of free accumulation is taken Go out to be replaced, operate extremely simple.Separately longer in view of the life cycle of fibre bundle, thus without frequency Numerous replacing also can ensure the properly functioning of device and not blockage phenomenon.The fibre bundle used has two kinds Version, the first is that the two ends of fibre bundle are broken into fast knot, and fibre bundle length is according to the volume of container 3 Size and filtered water stream amount determine, the second is the fibrage slabbing pencil or the fabric of bar shaped, its Area and thickness determine according to the volume size of container 3.
According to the actual needs, the inside of biological reaction pool 1 can be arranged at without constraint fiber bundle filter 2, May also set up in the outside of biological reaction pool 1, as long as being connected to the water outlet of biological reaction pool 1, can be right Water after degraded carries out filtering.Specifically, if be built in biological anti-without constraint fiber bundle filter 2 Answer in pond 1, then need to ensure that lower outlet 6 seals with the outlet of biological reaction pool 1 and connect;If without constraint Fiber bundle filter 2 is placed on biological reaction pool 1, is provided with water inlet on without constraint fiber bundle filter 2, On this, water inlet seals with the outlet of biological reaction pool 1 and connects.
The fibre bundle filtration membrane biological reaction apparatus of the present invention, is the water outlet connection one in biological reaction pool Without constraint fiber bundle filter, this nothing constraint fiber bundle filter is equiped with by some fibre bundle free accumulation Fibre bundle accumulation horizon, filtered by this fibre bundle accumulation horizon, not only can reach good filtration Effect, and without mechanically actuated when cleaning, replacing, extremely simple.Present configuration is simple, be readily cleaned, Fibre bundle for filtering uses the cycle long, thus can reduce production and maintenance cost.
The above is presently preferred embodiments of the present invention and the know-why used thereof, for the skill of this area For art personnel, without departing from the spirit and scope of the present invention, any based on the technology of the present invention side Equivalent transformation on the basis of case, simple replacement etc. obviously change, belong to scope it In.

Claims (2)

1. the sewage treatment process of a fibre bundle filtration membrane biological reaction apparatus, it is characterised in that described reaction unit forms by biological reaction pool with without constraint fiber bundle filter system,
This biological reaction pool includes water inlet, outlet, aeration opening, has been covered with the antibacterial for degradation of organic substances in biological reaction pool,
This nothing constraint fiber bundle filter system is formed by without constraint fiber bundle filter, the first automatic valve, the second automatic valve, the 3rd automatic valve, finished product water pump, flushing water recovery tube, air water backwash import, product water outlet,
This nothing constraint fiber bundle filter is built in biological reaction pool, this nothing constraint fiber bundle filter includes the lower porous plate of bottom, upper barrier and the fibre bundle accumulation horizon in the lower barrier of bottom, container in upper porous plate, container of container internal upper part in container, container, this fibre bundle accumulation horizon is made up of some free accumulation fibre bundle on this lower porous plate, this nothing constraint fiber bundle filter is provided with lower outlet, and this lower outlet seals with the outlet of biological reaction pool and connects;
This lower outlet is through the first automatic valve and air water backwash inlet communication, and this lower outlet connects with product water outlet through finished product water pump, the second automatic valve, and this lower outlet connects with flushing water recovery tube through finished product water pump, the 3rd automatic valve;
Sewage is entered biological reaction pool by water inlet, compressed air enters biological reaction pool through aeration opening, first automatic valve is closed, finished product pump operation, second automatic valve is opened, presenting negative pressure at lower outlet, the water in biological reaction pool is through filtering without constraint fiber bundle filter, and the clear water after filtration is discharged by product water outlet;Along with water pollutant is in the gradually accumulation on fibre bundle accumulation horizon surface, the water yield at product water outlet is gradually reduced, when dropping to certain value, device proceeds to backwash state, finished product water pump shuts down, second automatic valve and the 3rd automatic valve are closed, first automatic valve is opened, compressed air and backwashing water enter the bottom of container through air water backwash mouth, upwardly fibre bundle accumulation horizon, is rinsed fibre bundle, simultaneously, compressed air enters biological reaction pool through aeration opening, and the dirt that fibre bundle comes off flow back in the water body of biological reaction pool with backwashing water;After backwash certain time, the first automatic valve and the second automatic valve are closed, and finished product water pump and the 3rd automatic valve are opened, and in container, the flushing water containing dirt returns in biological reaction pool through flushing water recovery tube.
2. the sewage treatment process of fibre bundle filtration membrane biological reaction apparatus as claimed in claim 1, it is characterized in that: described fibre bundle has two kinds of versions, the first is that the two ends of fibre bundle are broken into fast knot, fibre bundle length determines according to described volume of a container size and filtered water stream amount, the second is that the fibrage slabbing pencil or the fabric of bar shaped, its area and thickness determine according to described volume of a container size.
CN201310103878.3A 2013-03-28 2013-03-28 Fibre bundle filtration membrane biological reaction apparatus Active CN104071943B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310103878.3A CN104071943B (en) 2013-03-28 2013-03-28 Fibre bundle filtration membrane biological reaction apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310103878.3A CN104071943B (en) 2013-03-28 2013-03-28 Fibre bundle filtration membrane biological reaction apparatus

Publications (2)

Publication Number Publication Date
CN104071943A CN104071943A (en) 2014-10-01
CN104071943B true CN104071943B (en) 2016-09-14

Family

ID=51593604

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310103878.3A Active CN104071943B (en) 2013-03-28 2013-03-28 Fibre bundle filtration membrane biological reaction apparatus

Country Status (1)

Country Link
CN (1) CN104071943B (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1363526A (en) * 2001-12-14 2002-08-14 清华大学 Process and equipment for filtering liquid mixture of bioreactor by dynamic membrane
CN101074141A (en) * 2007-06-20 2007-11-21 大连春兴水处理科技发展有限公司 Process for regenerating, recovering and reutilizing low-concentration organic waste water
CN102050548A (en) * 2009-10-29 2011-05-11 中国石油化工股份有限公司 Treatment and reuse method of waste water in methanol-to-olefin process
CN102674539A (en) * 2012-05-09 2012-09-19 浙江清华长三角研究院 Nitrified sludge efficient enriching culture system based on membrane bioreactor and method
CN202666490U (en) * 2012-07-09 2013-01-16 沈英立 Unconstrained fiber bundle filter
CN203247171U (en) * 2013-03-28 2013-10-23 沈英立 Biological reaction device adopting fiber bundle filter membrane

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2535405Y (en) * 2002-04-22 2003-02-12 姚志明 Integrated sewage treatment apparatus by biological membrane method
CN103408127B (en) * 2008-05-20 2016-06-01 北京汉青天朗水处理科技有限公司 A kind of waste disposal plant
CN101704617A (en) * 2009-12-08 2010-05-12 大连善水德水务工程有限责任公司 Equipment for reclaiming and processing petrified enterprise sewage and process technology thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1363526A (en) * 2001-12-14 2002-08-14 清华大学 Process and equipment for filtering liquid mixture of bioreactor by dynamic membrane
CN101074141A (en) * 2007-06-20 2007-11-21 大连春兴水处理科技发展有限公司 Process for regenerating, recovering and reutilizing low-concentration organic waste water
CN102050548A (en) * 2009-10-29 2011-05-11 中国石油化工股份有限公司 Treatment and reuse method of waste water in methanol-to-olefin process
CN102674539A (en) * 2012-05-09 2012-09-19 浙江清华长三角研究院 Nitrified sludge efficient enriching culture system based on membrane bioreactor and method
CN202666490U (en) * 2012-07-09 2013-01-16 沈英立 Unconstrained fiber bundle filter
CN203247171U (en) * 2013-03-28 2013-10-23 沈英立 Biological reaction device adopting fiber bundle filter membrane

Also Published As

Publication number Publication date
CN104071943A (en) 2014-10-01

Similar Documents

Publication Publication Date Title
CN100531853C (en) Self-cleaning filtering system
CN102223933B (en) Water treatment methods
CN201283274Y (en) Automatic cleaning microfiltration membrane device
WO2010093026A1 (en) Filtering device and method of manufacturing same
CN106964256A (en) The curtain film sewage treatment system and method for a kind of continuously-running
CN208747776U (en) A kind of environmental protection household water filter
CN105060407B (en) A kind of filter membrane filter-core back-flushing cleaning device and back-flushing method
CN204017488U (en) Oil drop pot strainer is unloaded in oil field
CN101785972B (en) Water treatment system with bidirectional cleaning function
CN203075850U (en) Concentrated filter device
CN104071943B (en) Fibre bundle filtration membrane biological reaction apparatus
CN109336222A (en) Immersion gravity stream ceramic membrane microkinetic ultrafiltration system sewage disposal device and method
CN203108444U (en) Intelligent control system of ultrafiltration equipment
CN203247171U (en) Biological reaction device adopting fiber bundle filter membrane
CN204918271U (en) Drainage structure and multi -functional retaining station
KR100745121B1 (en) Filtering apparatus
KR101894277B1 (en) Water Treatment System for Underwater
CN111072171A (en) Filtering and purifying device for industrial wastewater treatment and using method
CN205699641U (en) Filter compressed air back-flushing device
CN205367995U (en) Underground water purification device
KR200191691Y1 (en) Automatic recleanable water purifier system with air drop
CN101622057A (en) Membrane filtration process and design
CN103055573A (en) Concentrated filtering device and cleaning method of filter elements
CN105060587A (en) Water filtering structure and multifunctional water storage station
CN214270464U (en) Reverse osmosis seawater desalination cartridge filter rinse-system that disinfects

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20180126

Address after: 102488 Beijing, Liangxiang, Fangshan District Triumph Street, Jianshe Road, No. 18

Patentee after: Beijing first road water treatment New Technologies Inc

Address before: 100075 room 3-3-901, Dongcheng District, Beijing

Patentee before: Shen Yingli

CP02 Change in the address of a patent holder
CP02 Change in the address of a patent holder

Address after: 301, floor 3, building 4, No. a 13, Jingsheng South 4th Street, Tongzhou District, Beijing

Patentee after: Beijing first road water treatment New Technologies Inc

Address before: 102488 Beijing, Liangxiang, Fangshan District Triumph Street, Jianshe Road, No. 18

Patentee before: Beijing first road water treatment New Technologies Inc