CN100486681C - Outer installation type gas lift circulation membrane splitter - Google Patents
Outer installation type gas lift circulation membrane splitter Download PDFInfo
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- CN100486681C CN100486681C CNB2005100118466A CN200510011846A CN100486681C CN 100486681 C CN100486681 C CN 100486681C CN B2005100118466 A CNB2005100118466 A CN B2005100118466A CN 200510011846 A CN200510011846 A CN 200510011846A CN 100486681 C CN100486681 C CN 100486681C
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- clear water
- film silk
- encapsulating housing
- aerator
- tube connector
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- 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
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Abstract
An external separator with airlift cyclic membrane is composed of the membrane wires made of the organic hollow fiber membrane, the aerator under said membrane wires and consisting of air inlet tube, air cavity, and air distributing tube or chamber, the clean water collecting and flowing-out unit consisting of a clean water collecting cavity and a clean water discharging tube, and casing with top and bottom connecting tubes for connecting a biochemical reactor.
Description
Technical field
The present invention relates to environmental technology field, belong to the equipment that utilizes biochemical technology and membrane separation technique to dispose of sewage, particularly a kind of outer installation type gas lift circulation membrane splitter is installed on the membrane bioreactor, is used for the Separation of Solid and Liquid of active sludge intermixture.
Background technology
Membrane bioreactor is a kind of sewage disposal device that is combined by biochemical treatment unit and film separation unit.A subject matter of traditional activated sludge process is to rely on sludge settling to carry out mud-water separation, therefore need set up the sedimentation basin of large volume.If the sludge settling property variation will cause effluent quality poor.And owing to film can be trapped in solid and colloidal substance in the biochemical reactor, saved the construction of sedimentation basin, saved floor space, and make water outlet directly to enter surface water or be back to cooling water, the water of flushing the toilet, greening water, can be used as water for industrial use after further handling.The efficient crown_interception of film is trapped in the reactor microorganism fully, has realized separating fully of the reactor waterpower time of staying and sludge retention time.Can control hydraulic detention time and sludge retention time respectively like this, help breeding the growth of microorganism (as nitrifier or methanogen) slowly, prevent the Black Liquor with Efficient Bacteria in the reactor or the loss of dominant bacteria.Common some essential advanced treatment apparatus when membrane bioreactor does not need second pond and reuse, and can under very high sludge concentration, move, the sludge bulking phenomenon can not brought influence to its operation.Therefore it can have very high volumetric loading, and the more common activated sludge process of its floor space greatly reduces.Because the efficient crown_interception of film makes the macromolecular compound of difficult degradation that enough time of staying be arranged, therefore improved the degradation efficiency of hardly degraded organic substance greatly in biochemical reactor.The sludge loading of membrane bioreactor is low, causes its sludge yield low, and the excess sludge discharge amount is few.Therefore membrane bioreactor has broad application prospects.
In membrane bioreactor, membrane separation plant has two kinds of modes of emplacements.A kind of is that membrane separation device is placed on the biochemical reactor outside, utilizes circulating pump that mixed liquor is flowed fast on the film surface of membrane module, produces shearing force or turbulent flow thus and pollutes to alleviate film.In order to keep stable permeability rate, crossflow velocity is generally greater than 2m/s, and this just needs higher quantity of circulating water, causes higher unit to produce water consumption.Another kind is that membrane separation plant directly is immersed in the mixed liquor in the biochemical reactor, and the suction by vavuum pump or other types pump obtains filtered fluid.The cross-flow on film surface is produced by air agitation, aerator be arranged on membrane module under; Mixed liquor upwards flows with air-flow, produces shearing force on the film surface, and under the effect of shearing force, minimizing sludge suspension particle adheres to the film surface, allows water see through.
These two kinds of modes of emplacements respectively have its pluses and minuses.Membrane separation plant is placed on the mode that the biochemical reactor outside utilizes circulating pump circulation mixed liquor, and membrane flux is bigger, and the membrane module clean and maintenance is convenient, but the energy consumption height; And membrane separation plant is immersed in mode in the biochemical reactor mixed liquor, energy consumption is low, but because membrane module is submerged in the mixed liquor difficult clean and maintenance.
For the advantage of comprehensive these two kinds of modes of emplacements, overcome the defective of the two existence, external gas lift circulation membrane separation device is proposed.Membrane separation device is installed in the outside of biochemical reactor, but does not use circulating pump or suction pump, filter water outlet but utilize gravity head to drive.The air or oxygen that utilization blasts washes away the film surface, makes the swing of film silk, and circulates between membrane separation plant and biochemical reactor by the climbing power drive mixed liquor of gas in membrane separation plant.Membrane separation plant is installed in the outside of biochemical reactor, can simplifies the cleaning and the maintenance of membrane separation plant greatly.
Summary of the invention
The object of the present invention is to provide a kind of membrane bioreactor biochemical reaction zone outside that is positioned over, need not circulating pump returnedactivatedsludge mixed liquor, or the water outlet of suction pump suction filtration, and the membrane separation plant of energy on-line cleaning maintenance.
For achieving the above object, technical solution of the present invention provides a kind of outer installation type gas lift circulation membrane splitter, by the film silk, aerator, clear water is collected outlet unit, first tube connector, second tube connector and encapsulating housing are formed, wherein, encapsulating housing vertically is provided with, by cylindrical shell, flange constitutes, the cylindrical shell two ends are with flange seal, be connected with cleaning fluid on the upper flanges and add pipe, be connected with evacuated tube on the following end flanges, lower end, cylindrical shell side is connected to first tube connector, and the upper end is connected to second tube connector, adds pipe at cleaning fluid, evacuated tube, first tube connector and second tube connector are provided with valve; It is provided with aerator, clear water collector unit and film silk in the encapsulating housing inner chamber, aerator is made up of air cavity and air inlet pipe, and both communicate, air cavity is fixedly arranged on the inner chamber bottom, air inlet pipe one end is fixed on the air cavity, and the other end stretches out end flanges down downwards, and its periphery circle is connected with the lower end flange seal; The clear water collector unit is made up of clear water collecting chamber and clear water discharge pipe, and both communicate, and clear water discharge pipe one end is fixed on the clear water collecting chamber, and the other end stretches out outside the encapsulating housing, and its periphery circle is tightly connected with encapsulating housing; The film silk is the organic film of doughnut along the axial setting of encapsulating housing, is positioned at the top of aerator, is connected with the clear water collecting chamber;
Film silk upper end is fixed in the clear water collector unit that is located at its top, and film silk lower end is fixed in the aerator that is located at its bottom; Film silk, clear water collector unit and aerator are formed independently membrane separation assemblies, make film silk and encapsulating housing not affixed, and the clear water pipe is connected with the upper and lower end flange respectively by slip-knot with air inlet pipe.
Described outer installation type gas lift circulation membrane splitter, its described film silk, its lower end is connected in aerator air cavity upper surface, and its air cavity upper surface evenly is provided with a plurality of gas distribution tubes or distribution of gas hole, and this pipe or hole are positioned near the film silk outer peripheral edges;
The clear water collector unit, its clear water collecting chamber is fixedly arranged on encapsulating housing inner chamber top, is connected with film silk upper end, and the clear water discharge pipe stretches out outside the upper flanges, and shut film silk lower end, discharges clear water from the upper end through clear water collecting chamber and clear water discharge pipe.
Described outer installation type gas lift circulation membrane splitter, its described film silk, its upper end is fixedly arranged on encapsulating housing inner chamber upper bracket, the clear water collecting chamber of clear water collector unit is fixedly arranged on encapsulating housing inner chamber bottom, be connected with film silk lower end, outside the end flanges, shut film silk upper end under the clear water discharge pipe stretched out, and discharges clear water from the lower end through clear water collecting chamber and clear water discharge pipe;
The aerator air cavity places clear water collecting chamber top, and a plurality of gas distribution tubes or distribution of gas hole that its air cavity upper surface evenly is provided with are positioned near the film silk outer peripheral edges.
Described outer installation type gas lift circulation membrane splitter, its described clear water collector unit is two, its clear water collecting chamber is located at encapsulating housing inner chamber upper and lower part respectively, each is connected with film silk termination, two clear water discharge pipes stretch out respectively outside the upper and lower end flange, film silk open at both ends is discharged clear water from upper and lower end through two clear water collecting chambers and two clear water discharge pipes;
The aerator air cavity places down clear water collecting chamber top, and a plurality of gas distribution tubes or distribution of gas hole that its air cavity upper surface evenly is provided with are positioned near the film silk peripheral edge of bottom.
Described outer installation type gas lift circulation membrane splitter, its described film silk, its material are wherein a kind of of high molecular polymers such as polyethylene, polypropylene, polyvinyl chloride, Kynoar or polysulfones.
Described outer installation type gas lift circulation membrane splitter is installed in the outside of gas-lifting type biochemical reactor, is lower than mixed liquor liquid level certain altitude place, i.e. component film bioreactor sewage water treatment facility in the gas-lifting type biochemical reactor; It is the free end with first tube connector, link to each other with the sidewall mouth of biochemical reactor lower end by interface, the encapsulating housing inner chamber is communicated with the sidewall of biochemical reactor and the space between the central tube, free end with second tube connector, link to each other by the sidewall mouth of interface, the encapsulating housing inner chamber is communicated with the central tube of biochemical reactor with the biochemical reactor upper end.
Described outer installation type gas lift circulation membrane splitter, its described interface is removable connector, as flange, loose joint, hickey, cutting ferrule or pipe collar.
Described outer installation type gas lift circulation membrane splitter, its workflow is as follows: when from air inlet pipe when the aerator air cavity of external gas lift circulation membrane separation plant blasts air or oxygen, air or oxygen forms bubble by gas distribution tube or distribution of gas hole and moves upward along the film silk, wash away film silk surface, and cause the swing of film silk, make mud be difficult to attached to film silk surface; The air or oxygen mixed liquor concentrate of carrying under one's arms enters the central tube of membrane bioreactor biochemical reaction zone along second tube connector, and gas circulates along the central tube mixed liquor that drives inside and outside the central tube that rises;
City domestic sewage or industrial wastewater enter the biochemical reaction zone of membrane bioreactor through water inlet, fully mix with activated sludge, pollutant is decomposed and removes at biochemical reaction zone, simultaneously, partially mixed liquid enters described outer installation type gas lift circulation membrane splitter by first tube connector, with the liquid of water inlet equivalent under gravity head drives, filter continuous effluent through the film silk, clear water is collected the back by the clear water collecting chamber and is discharged outer installation type gas lift circulation membrane splitter by the clear water discharge pipe; Separated mud concentrate enters the central tube of biochemical reaction zone by second tube connector then under the rolling action of gas, circulation and so forth, and waste water is purified.
Described equipment, when needing cleaning film separation equipment, close the valve of first tube connector and second tube connector, the valve of opening evacuated tube is discharged the mixed liquor in the membrane separation plant, closes the valve of evacuated tube then, adds pipe by cleaning fluid and add clear water or chemical cleaning solution cleaning film silk in membrane separation plant, discharge cleaning fluid by evacuated tube then, close the valve of evacuated tube and cleaning fluid adding pipe, open the valve of two tube connectors, can normally move.
Described equipment when needing the film silk of repairing or sealing breakage, is closed the valve of two tube connectors, takes the interface of two tube connectors apart, pulls down membrane separation device.Take the flange at encapsulating housing two ends apart, can extract the film silk and safeguard.
Equipment of the present invention has following advantage:
1. membrane separation plant is installed in the outside of biochemical reactor, is communicated with biochemical reactor by tube connector, and valve and interface are set on tube connector, makes that the installation and removal of membrane separation plant are very easy, helps the maintenance and the cleaning of film.
2. when blasting the necessary air or oxygen of growth of microorganism toward biochemical reaction zone, gas at first concentrated area washes away film silk surface, makes that mud is difficult to reduce the film pollution in film silk surface attachment.Simultaneously because the carrying under one's arms effect of gas, the drive mixed liquor circulates between the interior outside of biochemical reactor central tube and biochemical reactor and membrane separation plant.Omit the mixed liquor circulating pump, reduced operation energy consumption.
3. membrane separation plant is installed in the outside of biochemical reactor, is communicated with biochemical reactor by tube connector, and valve and interface are set on tube connector, makes that the installation and removal of membrane separation plant are very easy, helps the maintenance and the cleaning of film.
Description of drawings
Fig. 1. the structural representation of clear water is discharged in the present device upper end;
Fig. 2. the structural representation of clear water is discharged in the present device lower end;
Fig. 3. the structural representation of clear water is discharged at the present device two ends;
Fig. 4. the assembling of present device and membrane bioreactor and schematic flow sheet.
The specific embodiment
A kind of outer installation type gas lift circulation membrane splitter is installed in the outside of gas-lifting type biochemical reactor, with its component film bioreactor sewage water treatment facility.
See Fig. 1, Fig. 2, Fig. 3, outer installation type gas lift circulation membrane splitter of the present invention, by film silk 11, aerator, clear water is collected outlet unit, first tube connector 4, second tube connector 6 and encapsulating housing 16 are formed, wherein, encapsulating housing 16 vertically is provided with, by cylindrical shell 5, flange constitutes, cylindrical shell 5 two ends are with flange seal, be connected with cleaning fluid on the upper flanges 7 and add pipe 9, be connected with evacuated tube 2 on the following end flanges 1, lower end, cylindrical shell 5 side is connected to first tube connector 4, and the upper end is connected to second tube connector 6, adds pipe 9 at cleaning fluid, evacuated tube 2, first tube connector 4 and second tube connector 6 are provided with valve 15; It is provided with aerator, clear water collector unit and film silk 11 in encapsulating housing 16 inner chambers, aerator is made up of air cavity 13 and air inlet pipe 3, both communicate, air cavity 13 is fixedly arranged on the inner chamber bottom, air inlet pipe 3 one ends are fixed on the air cavity 13, the other end stretches out end flanges 1 down downwards, and its periphery circle is tightly connected with following end flanges 1; The clear water collector unit is made up of clear water collecting chamber 10 and clear water discharge pipe 8, and both communicate, and clear water discharge pipe 8 one ends are fixed on the clear water collecting chamber 10, and the other end stretches out outside the encapsulating housing 16, and its periphery circle is tightly connected with encapsulating housing 16; Film silk 11 is the organic film of doughnut along the axial setting of encapsulating housing 16, is positioned at the top of aerator, communicates with clear water collecting chamber 10.
Its film silk 11 lower ends are connected in aerator air cavity 13 upper surfaces, and its air cavity 13 upper surfaces evenly are provided with a plurality of gas distribution tubes or distribution of gas hole 12, and this pipe or hole 12 are positioned near film silk 11 outer peripheral edges.
Clear water collector unit, its clear water collecting chamber 10 are fixedly arranged on encapsulating housing 16 inner chamber tops, are connected with film silk 11 upper ends, clear water discharge pipe 8 stretches out outside the upper flanges 7, shut film silk 11 lower ends, discharges clear water from the upper end through clear water collecting chamber 10 and clear water discharge pipe 8, as shown in Figure 1.
Its film silk 11, its upper end is fixedly arranged on encapsulating housing 16 inner chamber upper bracket 21, the clear water collecting chamber 10 of clear water collector unit is fixedly arranged on encapsulating housing 16 inner chamber bottoms, be connected with film silk 11 lower ends, clear water discharge pipe 8 stretches out outside the following end flanges 1, shut film silk 11 upper ends, discharges clear water from the lower end through clear water collecting chamber 10 and clear water discharge pipe 8;
The aerator air cavity places clear water collecting chamber 10 tops, and a plurality of gas distribution tubes or distribution of gas hole 12 that its air cavity 13 upper surfaces evenly are provided with are positioned near film silk 11 outer peripheral edges, as shown in Figure 2.
Outer installation type gas lift circulation membrane splitter of the present invention, its described clear water collector unit is two, its clear water collecting chamber 10a, 10b are located at encapsulating housing 16 inner chamber upper and lower parts respectively, each is connected with film silk 11 terminations, two clear water discharge pipe 8a, 8b stretch out respectively outside the upper and lower end flange 7,1, film silk 11 open at both ends are discharged clear water from upper and lower end through clear water collecting chamber 10a, 10b and clear water discharge pipe 8a, 8b;
Outer installation type gas lift circulation membrane splitter of the present invention is installed in the outside of gas-lifting type biochemical reactor, i.e. component film bioreactor sewage water treatment facility; It is the free end with first tube connector 4, link to each other with the sidewall mouth of biochemical reactor lower end by interface 14, encapsulating housing 16 inner chambers are communicated with the sidewall and the space between the central tube 20 of biochemical reactor, free end with second tube connector 6, link to each other by the sidewall mouth of interface 14, encapsulating housing 16 inner chambers are communicated with the central tube 19 of biochemical reactor with the biochemical reactor upper end.
Its interface 14 is removable connector, as flange, loose joint, hickey, cutting ferrule or pipe collar etc.
See Fig. 4, described gas-lifting type biochemical reactor 17 is a biochemical reaction zone, and one or more central tubes 19 are installed in the biochemical reaction zone, between central tube 19 and biochemical reaction zone 17 inwalls space 20 is arranged.Water in the central tube 19 is upward flow, and to stream, mixed liquor circulates inside and outside central tube 19 water outside the pipe for down.The upper portion side wall of biochemical reaction zone 17 has water inlet 18.
Described outer installation type gas lift circulation membrane splitter is a solid-liquid separating equipment, and the outside that is installed in biochemical reaction zone 17 is lower than mixed liquor liquid level certain altitude place.Outer installation type gas lift circulation membrane splitter is mainly collected outlet unit, first tube connector 4, second tube connector 6 and encapsulating housing 16 by film silk 11, aerator, clear water and is formed.Aerator is positioned at the lower end of film silk 11, is made up of air inlet pipe 3, air cavity 13 and gas distribution tube or distribution of gas hole 12.The clear water collector unit is made up of clear water collecting chamber 10 and clear water discharge pipe 8.The clear water collector unit can be installed in the upper end of film silk 11, also can be installed in the lower end of film silk 11, perhaps is installed in the two ends of film silk 11.First tube connector 4 is equipped with valve 15, one ends and is communicated with the lower end of encapsulating housing 16, and the other end is communicated with the sidewall of gas-lifting type biochemical reactor 17 and the space 20 between the central tube 19 by interface 14.Second tube connector 6 also is equipped with valve 15, one ends and is communicated with the upper end of encapsulating housing 16, and an end is communicated with the central tube 19 of gas-lifting type biochemical reactor 17 by interface 14.When air inlet pipe 3 blasts air or oxygen, because the castering action of gas makes that the mixed liquor in the biochemical reaction zone enters described outer installation type gas lift circulation membrane splitter by first tube connector 4.The bottom of film silk 11 is laid with gas distribution tube or distribution of gas hole 12, in order to wash away the film surface, the water outlet suction pump of the mixed liquor circulating pump of traditional detachable membrane bioreactor and integral type film biological reactor and the control module of water outlet are intermittently saved in mixed liquor continuous filtration water outlet under gravity head drives.Clear water flows out membrane separation plant by the clear water collector unit, and concentrate enters the central tube 19 of biochemical reactor 17, recirculated work by second tube connector 6.
When the flux of film silk 11 drops to when to a certain degree needing on-line cleaning, close the valve 15 of first tube connector 4 and second tube connector 6, the valve 15 of opening evacuated tube 2 is discharged the mixed liquor in the membrane separation plants, close the valve 15 of evacuated tube 2 then, add pipe 9 by cleaning fluid and in membrane separation plant, add clear water or chemical cleaning solution cleaning film silk 11, discharge cleaning fluid by evacuated tube 2 then, close the valve 15 of evacuated tube 2 and cleaning fluid adding pipe 9, open the valve 15 of two tube connectors 4,6, can normally move.
Need repairing when film silk 11 damages, when changing, close the valve 15 of two tube connectors 4,6, take two interfaces 14 apart, promptly can take off membrane separation plant.Take the flange 1,7 at encapsulating housing 16 two ends apart, can extract film silk 11 and safeguard.
Embodiment 1:
Outer installation type gas lift circulation membrane splitter is linked to each other by mode shown in Figure 4 with the gas-lifting type biochemical reactor, form the gas lift circulating gravity and go out to flow membrane bioreactor, the reactor dischargeable capacity is 80L.To contain COD is 200-600mg/L, and ammonia nitrogen is 50-100mg/L, and SS is that the sanitary sewage of 100-200mg/L enters membrane bioreactor by water inlet 18, and sludge concentration is 2000-5000mg/L, and water temperature is 10-30 ℃.The COD of water outlet is 20-60mg/L, ammonia nitrogen 0.5-15mg/L, and SS does not detect.
Embodiment 2:
Outer installation type gas lift circulation membrane splitter is linked to each other by mode shown in Figure 4 with the gas-lifting type biochemical reactor, form the gas lift circulating gravity and go out to flow membrane bioreactor, the reactor dischargeable capacity is 80L.To contain COD is 6000-18000mg/L, ammonia nitrogen is after the percolate elder generation of 1400-2000mg/L is the anaerobic filter processing of 63L through dischargeable capacity, enter membrane bioreactor by water inlet 18 again, sludge concentration is 4000-10000mg/L, and water temperature is 15-30 ℃.The COD of water outlet is 700-1000mg/L, ammonia nitrogen 6-25mg/L, and SS does not detect.Continuous filtration water outlet 90 days, film silk 11 flux maintain 5L/m
2More than the h.
Claims (3)
1, a kind of outer installation type gas lift circulation membrane splitter, collecting outlet unit, first tube connector, second tube connector and encapsulating housing by film silk, aerator, clear water forms, wherein, encapsulating housing vertically is provided with, constitute by cylindrical shell, flange, the cylindrical shell two ends are with flange seal, be connected with cleaning fluid on the upper flanges and add pipe, be connected with evacuated tube on the following end flanges, lower end, cylindrical shell side is connected to first tube connector, the upper end is connected to second tube connector, adds on pipe, evacuated tube, first tube connector and second tube connector at cleaning fluid to be provided with valve; It is characterized in that, in the encapsulating housing inner chamber, be provided with aerator, clear water collector unit and film silk, aerator is made up of air cavity and air inlet pipe, both communicate, air cavity is fixedly arranged on the inner chamber bottom, air inlet pipe one end is fixed on the air cavity, and the other end stretches out end flanges down downwards, and its periphery circle is connected with the lower end flange seal; The clear water collector unit is made up of clear water collecting chamber and clear water discharge pipe, and both communicate, and clear water discharge pipe one end is fixed on the clear water collecting chamber, and the other end stretches out outside the encapsulating housing, and its periphery circle is tightly connected with encapsulating housing; The film silk is the organic film of doughnut along the axial setting of encapsulating housing, is positioned at the top of aerator, communicates with the clear water collecting chamber;
Film silk upper end is fixed in the clear water collector unit that is located at its top, and film silk lower end is fixed in the aerator that is located at its bottom; Film silk, clear water collector unit and aerator are formed independently membrane separation assemblies, make film silk and encapsulating housing not affixed, and the clear water pipe is connected with the upper and lower end flange respectively by slip-knot with air inlet pipe.
2. outer installation type gas lift circulation membrane splitter as claimed in claim 1, it is characterized in that, described film silk, its lower end is connected in aerator air cavity upper surface, its air cavity upper surface evenly is provided with a plurality of gas distribution tubes or distribution of gas hole, and this pipe or hole are positioned near the film silk outer peripheral edges;
The clear water collector unit, its clear water collecting chamber is fixedly arranged on encapsulating housing inner chamber top, is connected with film silk upper end, and the clear water discharge pipe stretches out outside the upper flanges, and shut film silk lower end, discharges clear water from the upper end through clear water collecting chamber and clear water discharge pipe.
3. outer installation type gas lift circulation membrane splitter as claimed in claim 1, it is characterized in that, described clear water collector unit is two, its clear water collecting chamber is located at encapsulating housing inner chamber upper and lower part respectively, each is connected with film silk termination, two clear water discharge pipes stretch out respectively outside the upper and lower end flange, and film silk open at both ends is discharged clear water from upper and lower end through two clear water collecting chambers and two clear water discharge pipes;
The aerator air cavity places down clear water collecting chamber top, and a plurality of gas distribution tubes or distribution of gas hole that its air cavity upper surface evenly is provided with are positioned near the film silk peripheral edge of bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNB2005100118466A CN100486681C (en) | 2005-06-02 | 2005-06-02 | Outer installation type gas lift circulation membrane splitter |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100118466A CN100486681C (en) | 2005-06-02 | 2005-06-02 | Outer installation type gas lift circulation membrane splitter |
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| CN1872399A CN1872399A (en) | 2006-12-06 |
| CN100486681C true CN100486681C (en) | 2009-05-13 |
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| CNB2005100118466A Expired - Fee Related CN100486681C (en) | 2005-06-02 | 2005-06-02 | Outer installation type gas lift circulation membrane splitter |
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Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101422699B (en) * | 2008-12-02 | 2016-07-06 | 北京坎普尔环保技术有限公司 | Gas stripping internal circulation filter and filtering method of liquid film |
| CN102730816A (en) * | 2011-04-11 | 2012-10-17 | 金振忠 | Airlift external tubular membrane bioreactor purifier |
| CN103007754B (en) * | 2012-12-22 | 2016-05-18 | 郑州银科尔科技有限公司 | Multi phase state concurrent membrane separation device and technique |
| CN104174293A (en) * | 2014-08-27 | 2014-12-03 | 南京万德斯环保科技有限公司 | Device for relieving or preventing blockage of external tubular ultra-filtration membrane |
| CN106927560A (en) * | 2015-12-29 | 2017-07-07 | 乐金电子研发中心(上海)有限公司 | A kind of membrane aeration biomembrane reactor and its cleaning method |
| CN109847588A (en) * | 2019-01-15 | 2019-06-07 | 天津工业大学 | The method that multi-phase flow technology slows down gas-lifting type tubular type fouling membrane |
| CN110510732B (en) * | 2019-07-31 | 2023-03-21 | 中国航天员科研训练中心 | Composite membrane type biological reaction device |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5013331A (en) * | 1989-06-30 | 1991-05-07 | E. I. Du Pont De Nemours And Company | Permeator with selectable flow rates |
| JP2004181372A (en) * | 2002-12-04 | 2004-07-02 | Kubota Corp | Membrane module |
| CN1609015A (en) * | 2003-10-21 | 2005-04-27 | 中国科学院生态环境研究中心 | Sewage treating apparatus with baffling, aerating, boosting and gravitationally outflowing membrane bioreactor |
-
2005
- 2005-06-02 CN CNB2005100118466A patent/CN100486681C/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5013331A (en) * | 1989-06-30 | 1991-05-07 | E. I. Du Pont De Nemours And Company | Permeator with selectable flow rates |
| JP2004181372A (en) * | 2002-12-04 | 2004-07-02 | Kubota Corp | Membrane module |
| CN1609015A (en) * | 2003-10-21 | 2005-04-27 | 中国科学院生态环境研究中心 | Sewage treating apparatus with baffling, aerating, boosting and gravitationally outflowing membrane bioreactor |
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