CN202030613U - Water pressure type recycled water recycling device - Google Patents
Water pressure type recycled water recycling device Download PDFInfo
- Publication number
- CN202030613U CN202030613U CN2011200842919U CN201120084291U CN202030613U CN 202030613 U CN202030613 U CN 202030613U CN 2011200842919 U CN2011200842919 U CN 2011200842919U CN 201120084291 U CN201120084291 U CN 201120084291U CN 202030613 U CN202030613 U CN 202030613U
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- CN
- China
- Prior art keywords
- water
- tank
- pond
- pipeline
- hydraulic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 75
- 238000004064 recycling Methods 0.000 title abstract description 15
- 239000012528 membrane Substances 0.000 claims abstract description 35
- 238000011010 flushing procedure Methods 0.000 claims abstract description 20
- 239000010865 sewage Substances 0.000 claims abstract description 10
- 238000005273 aeration Methods 0.000 claims abstract description 9
- 239000010802 sludge Substances 0.000 claims abstract description 8
- 239000002033 PVDF binder Substances 0.000 claims abstract description 5
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims abstract description 5
- 230000001105 regulatory effect Effects 0.000 claims abstract 6
- 238000004140 cleaning Methods 0.000 claims description 15
- 239000003973 paint Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 4
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 238000005260 corrosion Methods 0.000 claims 1
- 238000005488 sandblasting Methods 0.000 claims 1
- 230000008929 regeneration Effects 0.000 abstract description 2
- 238000011069 regeneration method Methods 0.000 abstract description 2
- 239000010842 industrial wastewater Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 4
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 230000009189 diving Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005457 optimization Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 230000003245 working effect Effects 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000013043 chemical agent Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002990 reinforced plastic Substances 0.000 description 2
- 239000000741 silica gel Substances 0.000 description 2
- 229910002027 silica gel Inorganic materials 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002550 fecal effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000247 postprecipitation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
Images
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型公开了一种水压式中水回用装置，包括集污池、通过管道与所述集污池相连的调节池、通过管道与所述调节池另一端相连的二次水处理池以及与所述二次水处理池相连的回用水箱和污泥池，所述调节池中装有潜水推流器，所述二次水处理池中浸有MBR膜反应器，所述MBR膜反应器中的膜为PVDF平板膜，所述二次水处理池内设有水压冲洗装置，所述水压循环冲洗装置包括水压冲洗管道和安装在所述水压冲洗管道下面的曝气管，所述曝气管外端连有风机。本实用新型具有较强的实用性和广阔的市场前景，作为生活污水及工业废水处理再生装置，提高水资源的利用率，减少对清洁水资源的消耗。
The utility model discloses a water pressure type reclaimed water reuse device, which comprises a sewage collecting pool, a regulating pool connected with the sewage collecting pool through a pipeline, and a secondary water treatment pool connected with the other end of the regulating pool through a pipeline And the recycling water tank and the sludge tank connected with the secondary water treatment tank, the submerged flow booster is installed in the regulating tank, the MBR membrane reactor is immersed in the secondary water treatment tank, and the MBR membrane The membrane in the reactor is a PVDF flat membrane, and a hydraulic flushing device is provided in the secondary water treatment tank, and the hydraulic circulation flushing device includes a hydraulic flushing pipeline and an aeration tube installed under the hydraulic flushing pipeline , the outer end of the aeration pipe is connected with a fan. The utility model has strong practicability and broad market prospects. As a treatment and regeneration device for domestic sewage and industrial wastewater, the utility model improves the utilization rate of water resources and reduces the consumption of clean water resources.
Description
Technical field
The utility model relates to environment-protection wastewater regeneration industry, is specifically related to water recycling device in a kind of hydraulic type.
Background technology
Conventional producing, contain in the sanitary sewage organism, suspended substance, bacterium, metal ion, salt grades, above-mentioned pollutent is handled by conventional physico-chemical processes and traditional biological method can't be able to effective removal, water outlet after the processing can't be as effective water resources recycle, pollutent indexs such as COD, BOD, SS, TP, colibacillus of excrement do not reach the requirement among " city miscellaneous water water quality standard " GB/T18920-2002, directly carry out reuse and may bring secondary pollution.
Water recycling device in the membrane bioreactor (MBR) is to adopt the reclamation set of hollow-fibre membrane as carrier mostly at present, the low 20L/m that reaches as high as of the system membranes flux of tubular fibre curtain type membrane
2.h; What adopt when suction pump suction waste water is that pressurized air comes the film surface is washed, and energy consumption is than higher, steam-water ratio 24: 1, and the power of fan of required configuration is big; Film is short work-ing life, and film fracture of wire phenomenon is serious, and 2-3 need change once, and film replacement charge height is uneconomical; The film surface cleaning is not thorough, and system needs tackle gear when cleaning membrane module is proposed to put into cleaning agent from water, and operation is difficulty quite.
The utility model content
The utility model purpose: the utility model provides a kind of water recycling device in the film hydraulic type in work-ing life that cuts down the consumption of energy, prolongs in order to solve the deficiencies in the prior art.
The technical solution adopted in the utility model: water recycling device in a kind of hydraulic type, comprise the dirty pond of collection, the equalizing tank that links to each other with the dirty pond of described collection by pipeline, secondary water treating pond that links to each other with the described equalizing tank the other end by pipeline and reuse water tank and the sludge sump that links to each other with described secondary water treating pond, the diving impeller is housed in the described equalizing tank, on the pipeline between described secondary water treating pond and the equalizing tank lift pump and y-type filter are housed, be soaked with the MBR membrane reactor in the described secondary water treating pond, film in the described MBR membrane reactor is the PVDF flat sheet membrane, chemically-cleaning device is equipped with in described secondary water treating pond outside, described chemically-cleaning device links to each other with described MBR membrane reactor by header, be provided with hydraulic pressure circulation flushing device in the described secondary water treating pond, described hydraulic pressure circulation flushing device comprises that the hydraulic pressure flushing pipe is installed in the aeration tube below the described hydraulic pressure flushing pipe, and described aeration tube outer end is connected with blower fan.
Adopt the PVDF flat sheet membrane as the film main part, membrane flux can reach 30L/m
2.h; The use of hydraulic pressure flushing arrangement cuts down the consumption of energy, and steam-water ratio was reduced to 10: 1.
As optimization, between described chemically-cleaning device and the described MBR membrane reactor electrically operated valve is housed, can realize on-line cleaning.
As optimization, water recycling device is provided with the equipment room that the Q235-A carbon steel material is made outward in the described hydraulic type, described equipment room inwall is the steel plate that three cloth, four oily reinforced plastics are made, be brushed with twice rust-inhibiting paint and twice finish paint after the derusting by sandblast of described equipment room outer wall, integration apparatus is stable, energy consumption is low, long service life.
As optimization, the water recycling device system is by the industrial computer intelligent control in the described hydraulic type.
Beneficial effect: the hydraulic pressure that the utility model produces by inlet water lifting pumps, penetrate water by the hydraulic pressure flushing pipe film surface is cleaned, when normally moving, system the film surface is thoroughly cleaned by the circulation of membrane reactor inside water pressure.Air by spray hydraulic pressure circulation and bottom forms disorderly turbulent flow on the film surface, and decelerating membrane pollution prolongs cycle of matting film, reduces the destructiveness of chemical agent to film, in the work-ing life of prolongation film, the longlyest reaches 6 years; Flat sheet membrane can be easy to find from this sheet film water outlet silica gel strip after damaging, and tightens silica gel strip, can easily standby flat sheet membrane be changed, and the assurance system normally moves.
Description of drawings
Fig. 1 is a water recycling device process flow sheet in the hydraulic type;
Fig. 2 is a water recycling device structural representation in the hydraulic type.
Embodiment
The utility model is described in further detail below in conjunction with embodiment:
As Fig. 1, shown in 2, water recycling device in a kind of hydraulic type, comprise the dirty pond 1 of collection, the equalizing tank 2 that links to each other by the dirty pond 1 of pipeline and described collection, secondary water treating pond 3 that links to each other with described equalizing tank 2 the other ends by pipeline and reuse water tank 4 and the sludge sump 5 that links to each other with described secondary water treating pond 3, diving impeller 6 is housed in the described equalizing tank 2, on the pipeline between described secondary water treating pond 3 and the equalizing tank 2 lift pump 7 and y-type filter are housed, be soaked with MBR membrane reactor 8 in the described secondary water treating pond 3, film in the described MBR membrane reactor 8 is the PVDF flat sheet membrane, chemically-cleaning device 9 is equipped with in described secondary water treating pond 3 outsides, described chemically-cleaning device 9 links to each other with described MBR membrane reactor 8 by header 10, be provided with hydraulic pressure circulation flushing device in the described secondary water treating pond 3, described hydraulic pressure flushing arrangement comprises hydraulic pressure flushing pipe 11 and is installed in aeration tube 12 below the described hydraulic pressure flushing pipe 11 that described aeration tube 12 outer ends are connected with blower fan 13.
Between described chemically-cleaning device 9 and the described MBR membrane reactor 8 electrically operated valve 14 is housed.
Water recycling device is provided with the equipment room 15 that the Q235-A carbon steel material is made outward in the described hydraulic type, described equipment room 15 inwalls are the steel plate that three cloth, four oily reinforced plastics are made, be brushed with twice rust-inhibiting paint and twice finish paint after the described equipment room 15 outer wall derusting by sandblast, the water recycling device system is by the industrial computer intelligent control in the described hydraulic type.
Principle of work: in hydraulic type in the water recycling device process system, the waste water that collects in the dirty pond is removed the bulk foreign material through grid earlier before flowing into equalizing tank, protects equipment such as follow-up water pump not blocked.Equalizing tank has the long residence time, can suitably inoculate the oxygen activity mud of holding concurrently, and the double hydrolytic tank of doing uses, and sewage thorough mixing under the effect of diving impeller is even, under the effect of the oxygen bacterium of holding concurrently organic difficult degradation macromolecular substance is hydrolyzed into small organic molecule.Sewage again by water pump lifting to the MBR reactor, y-type filter filtering finely ground particles is set in the pipeline.
Equalizing tank sewage is delivered to the hydraulic pressure flushing pipe by lift pump, the pressurized air thorough mixing that High-Pressure Water that lift pump produces and blower fan are carried, form turbulent flow, membrane module draws water by the procedure auto-control suction pump, active sludge is blocked on the film surface, flat sheet membrane has had hydraulic pressure to clean and the cleaning of blower fan aeration, and cleaning is recovered on the film surface faster.Clear water after the suction drains into the reuse water tank.Enter for operation blower fan, the lift pump of keeping system and normally open when equalizing tank is anhydrous, electrically operated valve switches to the internal recycle state, and the carbonated drink turbulent flow that same parameter hydraulic pressure combines with pressurized air is implemented cleaning to the film surface.
Active sludge is constantly bred in MBR reactor for treatment process, discharges mud automatically to sludge sump by the water quality in-line meter, and from flowing into equalizing tank, regularly extract out by fecal suction truck by mud through the post precipitation supernatant liquor for mud in the sludge sump.When flat sheet membrane surface slight pollution, transmit signal by suction pump suction inlet vacuum pressure transmitter pressure to intelligence controlling device, send instruction and close suction pump, start automatic flushing device, adopt clear water to clean flat sheet membrane and can recover normal use; Clean final vacuum pressure registration can't reduce the time when water is counter, start chemical agent automatically and clean, carry out matting with citric acid, clorox respectively, scavenging solution enters equalizing tank by suction pump, clean finish after system recovery move.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200842919U CN202030613U (en) | 2011-03-25 | 2011-03-25 | Water pressure type recycled water recycling device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200842919U CN202030613U (en) | 2011-03-25 | 2011-03-25 | Water pressure type recycled water recycling device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202030613U true CN202030613U (en) | 2011-11-09 |
Family
ID=44892919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200842919U Expired - Lifetime CN202030613U (en) | 2011-03-25 | 2011-03-25 | Water pressure type recycled water recycling device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202030613U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102173544A (en) * | 2011-03-25 | 2011-09-07 | 南通京源水工自动化设备有限公司 | Hydraulic reclaimed water recycling device |
| CN102674577A (en) * | 2012-04-25 | 2012-09-19 | 江苏清涵环保科技有限公司 | Full-automatic energy-saving reclaimed water recycling device |
-
2011
- 2011-03-25 CN CN2011200842919U patent/CN202030613U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102173544A (en) * | 2011-03-25 | 2011-09-07 | 南通京源水工自动化设备有限公司 | Hydraulic reclaimed water recycling device |
| CN102173544B (en) * | 2011-03-25 | 2013-02-13 | 南通京源水工自动化设备有限公司 | Hydraulic reclaimed water recycling device |
| CN102674577A (en) * | 2012-04-25 | 2012-09-19 | 江苏清涵环保科技有限公司 | Full-automatic energy-saving reclaimed water recycling device |
| CN102674577B (en) * | 2012-04-25 | 2013-10-23 | 江苏清涵环保科技有限公司 | Full-automatic energy-saving reclaimed water recycling device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20111109 Effective date of abandoning: 20130306 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20111109 Effective date of abandoning: 20130306 |
|
| RGAV | Abandon patent right to avoid regrant |