CN107285572A - A kind of biochemistry pool - Google Patents

A kind of biochemistry pool Download PDF

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Publication number
CN107285572A
CN107285572A CN201710662388.5A CN201710662388A CN107285572A CN 107285572 A CN107285572 A CN 107285572A CN 201710662388 A CN201710662388 A CN 201710662388A CN 107285572 A CN107285572 A CN 107285572A
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CN
China
Prior art keywords
room
biochemical
biochemistry pool
stainless steel
steel tube
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Granted
Application number
CN201710662388.5A
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Chinese (zh)
Other versions
CN107285572B (en
Inventor
胡家富
周凝
杜宇
蔡金燕
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Nanjing Hehai Environmental Research Institute Co Ltd
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Nanjing Hehai Environmental Research Institute Co Ltd
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Priority to CN201710662388.5A priority Critical patent/CN107285572B/en
Publication of CN107285572A publication Critical patent/CN107285572A/en
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Publication of CN107285572B publication Critical patent/CN107285572B/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • 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
    • C02F3/28Anaerobic digestion 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
    • C02F3/28Anaerobic digestion processes
    • C02F3/286Anaerobic digestion processes including two or more steps
    • 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
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/301Aerobic and anaerobic treatment in the same reactor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • 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)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

The invention discloses a kind of biochemistry pool, interconnected water inlet pipe, expansion chamber, Flow-rate adjustment room, dispatch tube, biochemical room, effuser are sequentially provided with biochemistry pool, biochemistry pool is additionally provided with back purge system, and back purge system includes wash tub pipe, developing room;Screen pack is provided with expansion chamber, biochemical room includes filler device, aerator, demister, filler device includes packing ring, stainless steel tube, fix bar, fix bar two ends are placed on the pool wall of biochemistry pool, packing ring is fixed with stainless steel tube, stainless steel tube is removably attachable in the fix bar;Stainless steel tube is that the wash tub pipe is installed in hollow-core construction, stainless steel tube, and water pipe is provided with spray head, and the spray head that stainless steel tube is provided with delivery port, water pipe is corresponding with delivery port position.The present invention have filler is easy to clean, be not susceptible to winding, it is agglomerating, fracture etc. phenomenon;The biochemistry pool advantage such as have biochemical effects good, simple to operate, practical.

Description

A kind of biochemistry pool
Technical field
The present invention relates to field of waste water treatment, specially a kind of biochemistry pool.
Background technology
Biochemistry pool provide time-program(me) sewage disposal, rather than the space program continuously provided sewage disposal.It is raw Change cell system and be not required to preliminary sedimentation tank, second pond and sludge recirculation system, preferable quiet heavy, good separating effect.It can be applied to chemical industry, stone Oil, electric power, steel, weaving, printing and dyeing, transport, storage, food brewing, fermentation, water process, desalinization etc..
Biochemistry pool is primarily configured as:Provided with water inlet pipe, expansion chamber, Flow-rate adjustment room, dispatch tube, biochemical room, stream in pond Outlet pipe.Operation principle is:Waste water is entered by air inlet pipe, is adjusted flow through settling the laggard inbound traffics regulation room of indoor settlement, is passed Send pipe to be sent to biochemical room, biochemical indoor carry out it is aerobic/anaerobic biochemical treatment, aeration, sedimentation, after foam removal, through effuser stream Go out biochemistry pool, complete the biochemical treatment of waste water.Filler that its mesophytization chamber interior is provided with, bottom are set provided with aerator, top There is demister, complete biochemical reaction.The top of filler is hung in fix bar using steel cable, bottom is not fixed, and vertical is arranged on It is biochemical indoor.
There is problems with use in existing biochemistry pool:1st, filler is needed in periodic cleaning, but existing design The cleaning of filler is cumbersome, and obviously filler is easily washed out using directly being rinsed with high-pressure hydraulic pump, and it is aobvious that filler is removed into cleaning Right hell to pay;2nd, when waste water is sent to biochemical room by dispatch tube, under hydraulic blow, biochemical indoor pencil filler may occur The phenomenon such as fibre bundle winding, agglomerating, fracture, suitably can reduce hydraulic load and aeration intensity to solve, and change fracture in time Steel cable, reduce water conservancy negative pressure and aeration intensity and although solve problem, but cause the decreased influent flow of waste water, operating time Increase.
The content of the invention
To solve the above problems, the invention discloses a kind of biochemistry pool.
In order to reach object above, the present invention provides following technical scheme:
Interconnected water inlet pipe, expansion chamber, Flow-rate adjustment room, dispatch tube, biochemistry are sequentially provided with a kind of biochemistry pool, biochemistry pool Room, effuser, the biochemistry pool are additionally provided with back purge system, and the back purge system includes wash tub pipe, connection wash tub pipe Developing room;Screen pack, the exposure that the biochemical room includes the internal filler device being provided with, bottom is provided with are provided with the expansion chamber The demister that device of air, top are provided with, the filler device includes packing ring, stainless steel tube, fix bar, the fix bar two ends It is placed on the pool wall of biochemistry pool, packing ring is fixed with the stainless steel tube, the stainless steel tube is removably attachable to In the fix bar;The stainless steel tube is to be installed in hollow-core construction, the stainless steel tube on the wash tub pipe, the water pipe Provided with spray head, the spray head that the stainless steel tube is provided with delivery port, water pipe is corresponding with delivery port position.
Further, the biochemistry pool is sequentially connected in series the biochemical room being connected including at least two, and each biochemistry room is equal Dispatch tube, effuser are connected, and provided with control valve on dispatch tube.Biochemical room is divided into be connected in series one by one small Biochemical room, achievable waste water passes sequentially through each biochemical room, realizes series connection biochemical treatment, can also be closed according to actual wastewater flow rate The control valve of the dispatch tube of preceding biochemical room connection is set, the size for reducing biochemistry pool is realized, it is rational to carry out at biochemistry Reason, and the preceding biochemistry pool of set location is cleared up, cleaning is realized in the case where that need not stop operation.
Further, the biochemical room be aerobic biochemical room, anaerobic biological room wherein one in or two kinds.
Further, the biochemistry pool includes two anaerobic biological rooms, the four aerobic biochemical rooms being sequentially connected.
Further, the bottom of the biochemical room is provided with settling tank.The precipitum that biochemical room is produced can directly be settled, kept away Exempt from precipitum and enter effuser.
Further, the water inlet end of the biochemical room, which is provided with pretreatment chamber, the pretreatment chamber, is provided with pre- filler, described The water side of pretreatment chamber is provided with out the network of rivers, it is described go out the network of rivers be fenestral fabric.
The operation principle of the present invention:After waste water enters from water inlet pipe, first in sedimentation indoor settlement, the waste water after sedimentation enters Inbound traffics reconcile room, and regulation enters the flow of the waste water of biochemical room, and waste water is sent in biochemistry pool from dispatch tube, in biochemistry pool Carry out after biochemical treatment, from effuser outflow.Screen pack is provided with the side of expansion chamber, screen pack may filter that tiny particle Thing, optimizes the effect of sedimentation;Waste water is sent to the pretreatment chamber of biochemical room after filtering by dispatch tube, is provided with pretreatment chamber Filler in pre- filler, pretreatment chamber can monitor biochemical status, be also convenient for debugging, can also be pulled out this condiment in routine use The water surface checks the upgrowth situation of biochemical film, and the water side of pretreatment chamber is provided with out the network of rivers, can avoid water outlet pressure excessive to biochemical room The filler of front end is impacted, and goes out the network of rivers equivalent to water distributing plate, be uniformly distributed pretreatment chamber water side goes out water state;Then Into pretreatment chamber, biochemical reaction can in advance be judged in pretreatment chamber, demister can remove the white of biochemical reaction generation Foam, aerator aeration, filler device can form biochemical film and carry out biochemical reaction, wherein be inside the stainless steel tube of filler device Hollow-core construction, is carried out again in hollow interior installation flusher to filler device, must be to filler after a period of time due to using Device is rinsed, and otherwise influences biochemical effects and speed, and the flusher flushing speed that the present invention is improved is fast, effect is good and saves Shi Shengli, reduces labor intensity, and automated development can be achieved.Stainless steel tube and water pipe play good fixation, can avoid Winding between filler, agglomerating phenomenon.
In summary, it is an advantage of the invention that:1st, filler is easy to clean, simple to operate, time saving and energy saving;And survivable fill out Material;2nd, biochemical indoor pencil filler is not susceptible to the phenomenon such as winding, agglomerating, fracture, while not influenceing the normal life of biochemical room Change reaction;3rd, the biochemistry pool disclosed by the invention advantage such as have biochemical effects good, simple to operate, practical.
Brief description of the drawings
Fig. 1, the present invention structural representation;
Fig. 2, the internal structure schematic diagram of the biochemical room of the embodiment of the present invention 1;
Fig. 3, the present invention wastewater treatment process block diagram;
The biochemical cell structure figure of the first situation 6 of Fig. 4, the embodiment of the present invention 2;
Fig. 5, the embodiment of the present invention 2 biochemical cell structure figure of second of situation 6.
Wherein:Water inlet pipe 1, expansion chamber 2, Flow-rate adjustment room 3, dispatch tube 4, control valve 41, biochemical room 5, the first anaerobism Biochemical room 501, the second anaerobic biological room 502, the 3rd aerobic biochemical room 503, the 4th aerobic biochemical room 504, the 5th aerobic biochemical Room 505, the 6th aerobic biochemical room 506, filler device 51, packing ring 511, stainless steel tube 512, fix bar 513, aerator 52nd, demister 53, effuser 6, screen pack 21, pretreatment chamber 7, pre- filler 71, go out the network of rivers 72, back purge system 8, wash tub pipe 81st, developing room 82, spray head 83.
Embodiment
With reference to the accompanying drawings and detailed description, the present invention is furture elucidated, it should be understood that following embodiments are only For illustrating the present invention rather than limitation the scope of the present invention.
As shown in Figure 1, Figure 2, Figure 3 shows, interconnected water inlet pipe 1, expansion chamber are sequentially provided with a kind of biochemistry pool, biochemistry pool 2nd, screen pack 21 is provided with Flow-rate adjustment room 3, dispatch tube 4, biochemical room 5, effuser 6, expansion chamber, the water inlet end of biochemical room is provided with Pre- filler 71 is provided with pretreatment chamber 7, pretreatment chamber, the water side of pretreatment chamber is provided with out the network of rivers 72, it is latticed to go out the network of rivers Structure, goes out network of rivers side and is provided with biochemical room, the aerator that biochemical room includes the internal filler device 51 being provided with, bottom is provided with 52nd, the demister 53 that top is provided with, filler device includes packing ring 511, stainless steel tube 512, fix bar 513, fix bar two ends It is placed on the pool wall of biochemistry pool, packing ring is fixed with stainless steel tube, stainless steel tube is removably attachable in fix bar.
Biochemistry pool is additionally provided with back purge system 8, and back purge system includes wash tub pipe 81, connects the developing room of wash tub pipe 82;Stainless steel tube is that the wash tub pipe is installed in hollow-core construction, stainless steel tube, and water pipe is provided with spray head 83, stainless steel tube The spray head being provided with delivery port, water pipe is corresponding with delivery port position.Realized by the wash tub pipe of back purge system to filler Backwash.In concrete operations, packing ring is arranged on stainless steel tube in string-like, and is set out between not having two packing rings The mouth of a river.The quantity of spray head can voluntarily be set according to actual needs.
In the present embodiment, to facilitate installation, the water pipe of flusher includes the supervisor of a connection developing room, supervisor Upper each branch pipe of connection, branch pipe is arranged in steel pipe endlessly.
Meanwhile, back purge system can be used to add medicine.Medicine needed for being added in developing room, is directly filled by backwashing Put and be ejected into biochemical interior.
The material of packing ring can select ceramic material commonly used in the prior art, metal material, plastic material etc..Anaerobism/ Aerobic bacteria can form biochemical film on packing ring.
Stainless steel tube is removably attachable in fix bar, the concrete mode used in the present embodiment for:In steel endlessly The top of pipe is provided with steel wire rope, and wire rope rope is in fix bar;Certainly, in other embodiments, more firm side can be used Formula, such as sets buckle respectively on stainless steel tube and fix bar, using snapping connection;Certainly, other prior arts can also be used In common technology means implement.
In the present embodiment, the bottom of biochemical room is provided with settling tank.The precipitum that biochemical room is produced can directly be settled, kept away Exempt from precipitum and enter effuser.
Embodiment 2
Biochemical room is divided into 6 and is sequentially connected in series the biochemical room being connected in the present embodiment, and each biochemistry room side is all connected with passing Pipe, effuser are sent, and provided with control valve 41 on dispatch tube.6 biochemical rooms are followed successively by the life of the first anaerobism in the present embodiment Change room 501, the second anaerobic biological room 502, the 3rd aerobic biochemical room 503, the 4th aerobic biochemical room 504, the 5th aerobic biochemical room 505th, the 6th aerobic biochemical room 506.Remaining structure is same as Example 1.Because biochemical room is arranged in series 6, therefore in order to save About cost is only in the first biochemical room connection and process chamber.Therefore the frequency of use highest of the biochemical room in strange land.
Biochemical room is divided into the small biochemical room being connected in series one by one, achievable waste water passes sequentially through each biochemical room, Series connection biochemical treatment is realized, the control for the dispatch tube that preceding biochemical room connection is set according to actual wastewater flow rate, can be also closed Valve, realizes the size for reducing biochemistry pool, reasonably carries out biochemical treatment, and clears up the preceding biochemistry pool of set location, not Need to realize cleaning in the case of stopping operation.
If wastewater treatment capacity is less, it is not necessary to which so big biochemical room processing is alternative to carry out biochemical treatment.
Arrow represents the flow direction of waste water in a kind of biochemical cell structure figure of 6 of biochemistry pool as shown in Figure 4, figure.The A kind of situation, when low to the demand of anaerobic biochemical treatment:The first anaerobic biological room can be closed, it is the 3rd aerobic biochemical room, the 4th good Oxygen biochemistry room, the 5th aerobic biochemical room, the control valve of transmission official's pipe of the 6th aerobic biochemical room, open the second anaerobic biological room Dispatch tube control valve, waste water directly from the second anaerobic biological room enter, because each biochemical room is connected, waste water is follow-up Biochemical treatment is carried out into the three, the four, the five, the 6th aerobic biochemical rooms, the first anaerobic biological room is vacated;On the one hand it is this to set The working strength of biochemical room can be reduced by putting, the service life of the biochemical room of extension;On the other hand it can realize to the first anaerobism simultaneously The cleaning of biochemical room.The control valve of the second anaerobic biological room is similarly optionally closed, is realized to the second anaerobic biological room Cleaning.
Arrow represents the flowing of waste water in the biochemical cell structure figure of 6 of biochemistry pool in another case as shown in Figure 5, figure Direction.Second of situation:When anaerobic biochemical treatment need not be carried out, the first anaerobic biological room, the second anaerobic biological can be closed The control valve of room, and the selective control valve for opening aerobic biochemical room, in the present embodiment, it is aerobic that selection opens the 4th The control valve of biochemical room, closes the 3rd aerobic biochemical room, the 5th aerobic biochemical room, the control valve of the 6th aerobic biochemical room, Realize that waste water directly enters from the 4th aerobic biochemical room, waste water subsequently enters into the 5th aerobic biochemical room, the 6th aerobic biochemical room Row biochemical reaction;Now realize the cleaning to the 3rd aerobic biochemical room;Similarly, it can be achieved to the four, the 5th aerobic biochemical rooms Cleaning.Because the 6th aerobic biochemical room is located at end, the frequency relative reduction of cleaning can only stop doing business clear when having to cleaning Wash.
Certainly according to actual needs, biochemical room be aerobic biochemical room, anaerobic biological room wherein one in or two kinds.And number Can voluntarily it be set with biochemical room species.
Technological means disclosed in the present invention program is not limited only to the technological means disclosed in above-mentioned embodiment, in addition to Constituted technical scheme is combined by above technical characteristic.It should be pointed out that for those skilled in the art For, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications are also considered as Protection scope of the present invention.

Claims (6)

1. interconnected water inlet pipe, expansion chamber, Flow-rate adjustment room, dispatch tube, life are sequentially provided with a kind of biochemistry pool, biochemistry pool Change room, effuser, it is characterised in that:The biochemistry pool is additionally provided with back purge system, the back purge system include wash tub pipe, Connect the developing room of wash tub pipe;Screen pack is provided with the expansion chamber, the biochemical room includes internal provided with filler device, bottom The demister that aerator that portion is provided with, top are provided with, the filler device includes packing ring, stainless steel tube, fix bar, described Fix bar two ends are placed on the pool wall of biochemistry pool, and packing ring is fixed with the stainless steel tube, and the stainless steel tube is removable That unloads is connected in the fix bar;The stainless steel tube is that the wash tub pipe is installed in hollow-core construction, the stainless steel tube, The water pipe is provided with spray head, and the spray head that the stainless steel tube is provided with delivery port, water pipe is corresponding with delivery port position.
2. a kind of biochemistry pool as claimed in claim 1, it is characterised in that:The biochemistry pool is sequentially connected in series phase including at least two Lead to the biochemical room connect, each biochemistry room is all connected with dispatch tube, effuser, and provided with control valve on dispatch tube.
3. a kind of biochemistry pool as claimed in claim 2, it is characterised in that:The biochemical room is aerobic biochemical room, anaerobic biological In wherein the one of room or two kinds.
4. a kind of biochemistry pool as claimed in claim 3, it is characterised in that:The biochemistry pool includes two anaerobism being sequentially connected Biochemical room, four aerobic biochemical rooms.
5. a kind of biochemistry pool as claimed in claim 1, it is characterised in that:The bottom of the biochemical room is provided with settling tank.
6. a kind of biochemistry pool as claimed in claim 1, it is characterised in that:The water inlet end of the biochemical room is provided with pretreatment chamber, Be provided with pre- filler in the pretreatment chamber, the water side of the pretreatment chamber is provided with out the network of rivers, it is described go out the network of rivers be latticed knot Structure.
CN201710662388.5A 2017-08-04 2017-08-04 Biochemical pool Active CN107285572B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115108634A (en) * 2022-06-09 2022-09-27 同济大学建筑设计研究院(集团)有限公司 Multi-mode self-adaptive mutual operation biochemical system and method based on computer vision high-efficiency energy conservation

Citations (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101496972A (en) * 2009-01-14 2009-08-05 卢普伦 Novel rotor type fibre filtering material
CN101514051A (en) * 2009-03-27 2009-08-26 哈尔滨工业大学 Self-demoulding biologic-carrier internal circulation filtering technology and a device thereof
CN101597131A (en) * 2009-06-05 2009-12-09 浙江旺能环保股份有限公司 A kind of rubbish leachate treatment method and treatment unit
CN101638264A (en) * 2009-08-27 2010-02-03 同济大学 Sponge anti-clogging strengthening compound flow constructed wetland domestic sewage treatment device
KR20100031969A (en) * 2008-09-17 2010-03-25 주식회사 동인엔지니어링 A compact wastewater treatment using carrier plate
EP2213363A1 (en) * 2008-12-22 2010-08-04 Seccua GmbH Deutschland Filtration device
CN102086058A (en) * 2010-11-17 2011-06-08 安徽工业大学 Loofah sponge filler used in slightly polluted source water biological pretreatment and pretreatment method
CN102101744A (en) * 2011-01-11 2011-06-22 山东省农业科学院农业资源与环境研究所 Biogas slurry treatment system for use in biogas project
CN102531272A (en) * 2010-12-31 2012-07-04 苏州嘉净环保科技股份有限公司 Integrated device for treating decentralized domestic sewage
CN102815838A (en) * 2012-08-13 2012-12-12 上海川鼎国际贸易有限公司 Printing fountain solution filtration recycling and zero discharging system, and technology process thereof
CN102826652A (en) * 2012-01-13 2012-12-19 北京海思清膜科技有限公司 Inner-aeration hollow fiber film carrier module and its application method
US20130153493A1 (en) * 2010-08-13 2013-06-20 University Of Regina Moving bed membrane bioreactor
CN203238125U (en) * 2013-05-16 2013-10-16 四川建筑职业技术学院 Sewage treatment micro-flocculation deep filtration device
CN203307116U (en) * 2013-05-27 2013-11-27 广州华浩能源环保集团有限公司 Easily-replaced combined packing device for treating sewage
CN103992004A (en) * 2014-04-23 2014-08-20 北京城市排水集团有限责任公司 Rural sewage advanced treatment and biochemical filtration integration device and running method thereof
CN104129887A (en) * 2014-07-15 2014-11-05 兰仰光 Reclaimed water recycling system based on membrane bioreactor
CN104150585A (en) * 2014-07-28 2014-11-19 浙江大学 Denitrification and algae removal-enhanced raw water biomembrane pretreatment technology device and method
CN104609673A (en) * 2015-02-03 2015-05-13 厦门科林尔环保科技有限公司 Non-antibiotic pharmaceutical wastewater treatment process
CN104628228A (en) * 2015-02-03 2015-05-20 新疆德安环保工程有限公司 Modular sewage treatment and reclamation method and device
CN204342600U (en) * 2014-11-25 2015-05-20 浙江大学 One is suitable for high turbidity raw sewage pretreated combined bio film reaction device
CN104692586A (en) * 2013-12-10 2015-06-10 江西省三余环保节能科技有限公司 Breeding sewage treatment equipment
CN205222786U (en) * 2015-11-06 2016-05-11 浙江大湖环境科技有限公司 Trickling filter layering recoil aeration equipment
CN206051809U (en) * 2016-09-29 2017-03-29 四川建筑职业技术学院 A kind of sewage treatment biofilter with adjustable density fillers
CN206173163U (en) * 2016-07-08 2017-05-17 广东沪利环境科技发展有限公司 Wastewater treatment device
CN206188568U (en) * 2016-08-25 2017-05-24 南通科技职业学院 Livestock and poultry breeding wastewater processing apparatus
CN106865790A (en) * 2017-05-02 2017-06-20 广东工业大学 A kind of sewage disposal device
CN207294503U (en) * 2017-08-04 2018-05-01 南京河海环境研究院有限公司 A kind of biochemistry pool
CN211620045U (en) * 2019-11-15 2020-10-02 江苏裕创环境科技有限公司 Novel hydrolysis acidification pool

Patent Citations (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20100031969A (en) * 2008-09-17 2010-03-25 주식회사 동인엔지니어링 A compact wastewater treatment using carrier plate
EP2213363A1 (en) * 2008-12-22 2010-08-04 Seccua GmbH Deutschland Filtration device
CN101496972A (en) * 2009-01-14 2009-08-05 卢普伦 Novel rotor type fibre filtering material
CN101514051A (en) * 2009-03-27 2009-08-26 哈尔滨工业大学 Self-demoulding biologic-carrier internal circulation filtering technology and a device thereof
CN101597131A (en) * 2009-06-05 2009-12-09 浙江旺能环保股份有限公司 A kind of rubbish leachate treatment method and treatment unit
CN101638264A (en) * 2009-08-27 2010-02-03 同济大学 Sponge anti-clogging strengthening compound flow constructed wetland domestic sewage treatment device
US20130153493A1 (en) * 2010-08-13 2013-06-20 University Of Regina Moving bed membrane bioreactor
CN102086058A (en) * 2010-11-17 2011-06-08 安徽工业大学 Loofah sponge filler used in slightly polluted source water biological pretreatment and pretreatment method
CN102531272A (en) * 2010-12-31 2012-07-04 苏州嘉净环保科技股份有限公司 Integrated device for treating decentralized domestic sewage
CN102101744A (en) * 2011-01-11 2011-06-22 山东省农业科学院农业资源与环境研究所 Biogas slurry treatment system for use in biogas project
CN102826652A (en) * 2012-01-13 2012-12-19 北京海思清膜科技有限公司 Inner-aeration hollow fiber film carrier module and its application method
CN102815838A (en) * 2012-08-13 2012-12-12 上海川鼎国际贸易有限公司 Printing fountain solution filtration recycling and zero discharging system, and technology process thereof
CN203238125U (en) * 2013-05-16 2013-10-16 四川建筑职业技术学院 Sewage treatment micro-flocculation deep filtration device
CN203307116U (en) * 2013-05-27 2013-11-27 广州华浩能源环保集团有限公司 Easily-replaced combined packing device for treating sewage
CN104692586A (en) * 2013-12-10 2015-06-10 江西省三余环保节能科技有限公司 Breeding sewage treatment equipment
CN103992004A (en) * 2014-04-23 2014-08-20 北京城市排水集团有限责任公司 Rural sewage advanced treatment and biochemical filtration integration device and running method thereof
CN104129887A (en) * 2014-07-15 2014-11-05 兰仰光 Reclaimed water recycling system based on membrane bioreactor
CN104150585A (en) * 2014-07-28 2014-11-19 浙江大学 Denitrification and algae removal-enhanced raw water biomembrane pretreatment technology device and method
CN204342600U (en) * 2014-11-25 2015-05-20 浙江大学 One is suitable for high turbidity raw sewage pretreated combined bio film reaction device
CN104609673A (en) * 2015-02-03 2015-05-13 厦门科林尔环保科技有限公司 Non-antibiotic pharmaceutical wastewater treatment process
CN104628228A (en) * 2015-02-03 2015-05-20 新疆德安环保工程有限公司 Modular sewage treatment and reclamation method and device
CN205222786U (en) * 2015-11-06 2016-05-11 浙江大湖环境科技有限公司 Trickling filter layering recoil aeration equipment
CN206173163U (en) * 2016-07-08 2017-05-17 广东沪利环境科技发展有限公司 Wastewater treatment device
CN206188568U (en) * 2016-08-25 2017-05-24 南通科技职业学院 Livestock and poultry breeding wastewater processing apparatus
CN206051809U (en) * 2016-09-29 2017-03-29 四川建筑职业技术学院 A kind of sewage treatment biofilter with adjustable density fillers
CN106865790A (en) * 2017-05-02 2017-06-20 广东工业大学 A kind of sewage disposal device
CN207294503U (en) * 2017-08-04 2018-05-01 南京河海环境研究院有限公司 A kind of biochemistry pool
CN211620045U (en) * 2019-11-15 2020-10-02 江苏裕创环境科技有限公司 Novel hydrolysis acidification pool

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
邵振鲁;邢伟彬;庞林茂;: "快滤池常用两种配水系统的比较与探讨", 甘肃科技纵横, no. 09 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115108634A (en) * 2022-06-09 2022-09-27 同济大学建筑设计研究院(集团)有限公司 Multi-mode self-adaptive mutual operation biochemical system and method based on computer vision high-efficiency energy conservation
CN115108634B (en) * 2022-06-09 2023-09-26 同济大学建筑设计研究院(集团)有限公司 Multi-mode self-adaptive inter-camping system and method based on computer vision and high efficiency and energy conservation

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