CN203303844U - Flat membrane component for biological sewage treatment filtration - Google Patents

Flat membrane component for biological sewage treatment filtration Download PDF

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Publication number
CN203303844U
CN203303844U CN2013203892995U CN201320389299U CN203303844U CN 203303844 U CN203303844 U CN 203303844U CN 2013203892995 U CN2013203892995 U CN 2013203892995U CN 201320389299 U CN201320389299 U CN 201320389299U CN 203303844 U CN203303844 U CN 203303844U
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China
Prior art keywords
film assembly
plate film
communicated
membrane component
flat membrane
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Expired - Lifetime
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CN2013203892995U
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Chinese (zh)
Inventor
胡登燕
郑传勇
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SICHUAN GAOTONG ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
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SICHUAN GAOTONG ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
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Abstract

The utility model discloses a flat membrane component for biological sewage treatment filtration, which comprises a frame and a flat membrane component arranged in the frame; the flat membrane component comprises a membrane body; the membrane body is provided with an inner cavity channel for constituting the membrane body; and one end of the inner cavity channel is communicated with a water collection branch pipe through a flexible connecting pipe. The flat membrane component adopts an outer-inlet inner-suction filtration mode. Sewage enters the inside of the flat membrane component from the outside of the flat membrane component so as to be filtered, and clear water is sucked away from the inside of the flat membrane component in a suction mode. The frame is used for supporting the flat membrane component. The utility model can filter out 0.1 um particles, and has the advantages of favorable filtration effect and simple structure.

Description

A kind of for Sewage Biological Treatment filtration plate film assembly
Technical field
The utility model relates to a kind of for Sewage Biological Treatment filtration plate film assembly, belongs to the environment protection sewage processing technology field.
Background technology
Current sewage disposal technology basic forming, but the Eutrophication of the water body that nitrogen phosphorus excessive emissions causes, still that water pollutes the significant problem existed, sewage disposal no longer only be take and is removed organic matter (COD etc.) and be purpose, but should remove organic matter denitrogenation dephosphorizing again, reduce the water body Eutrophication, traditional Biological Nitrogen Removal Processe, comprise A/0, improvement A/0, the techniques such as oxidation ditch, though generally have Nitrogen/Phosphorus Removal, but reactor is many, complex process, energy consumption is high, in order to obtain simultaneously Nitrogen/Phosphorus Removal preferably, need to increase sludge reflux or additional carbon, not only increased the process operation expense, and produced a large amount of excess sludges.The denitrification nitrogen and phosphorus removal technology is existing certain development in recent years, it usings the electron acceptor of nitrate anion while replacing oxygen as dephosphorization, by Denitrifying Phosphate Accumulating Organisms, denitrogenation and dephosphorization process are united two into one, can overcome the contradiction between the traditional handicraft denitrogenation dephosphorizing, reduce aeration rate, the reduce mud discharge capacity, be the denitrification dephosphorization technique of energy-efficient and sustainable development, and this is focus and the inexorable trend of current municipal sewage denitrification dephosphorization technique research.About the denitrification nitrogen and phosphorus removal technology, a lot of research is also arranged now, although method can both obtain treatment effect preferably greatly at present, but in technique, ubiquity will carry out precipitate and separate to Denitrifying Phosphate Accumulating Organisms with a plurality of sedimentation basins, exist reactor many, many weak points such as step is many, and the reactor dischargeable capacity is little, and efficiency is low, be awkward.And present stage also lacks the device for biofiltration, therefore study a kind of biological membrane assembly that can filter more than 0.1um imperative.
The utility model content
The purpose of this utility model is to provide a kind of and filters plate film assembly for Sewage Biological Treatment, but other particle of 0.1um level, and purification filtering is respond well, simple in structure.
The purpose of this utility model is achieved through the following technical solutions: a kind of for Sewage Biological Treatment filtration plate film assembly, comprise framework and be arranged on the plate film assembly in framework, plate film assembly comprises film body, film body has the bore passages that forms film body, and bore passages one end is communicated with by connecting flexible pipe the arm that catchments.The filter type of plate film assembly is: advance internal-suction type outward and filter.Namely from the outside of plate film assembly, enter the inside of plate film assembly, form and filter, adopt Smoking regime, take the clear water of plate film assembly inside away.Framework is for the support plate membrane module.
Plate film assembly is the earthenware slab membrane module.The earthenware slab membrane module is provided with the aperture of 0.1um, the catching probability and can reach more than 95% of its 0.1um particle.Use the PH scope to be 2-12, serviceability temperature can reach 80 degrees centigrade.
The arm that catchments is communicated with water header.Water after the water header exhaust filtering.
Bore passages is communicated with scavenge pipe and aeration tube away from an end that connects flexible pipe, between aeration tube and bore passages, is provided with loose gas blowout head.Scavenge pipe and aeration tube form back purge system, and one is dropped into gas, one and passes into flushing water.
The plate film assembly lower end is provided with the bottom water leg, and bore passages is communicated with the bottom water leg, and scavenge pipe is communicated with the bottom water leg, and aeration tube extends into the bottom water leg, and loose gas blowout head is communicated with the end that aeration tube extends into the bottom water leg.
The plate film assembly upper end is provided with the upper-part centralized tank, and water header is communicated with the upper-part centralized tank by connecting flexible pipe successively.
Framework is provided with the axis brace parallel with the plate film assembly surface.Brace increases the support degree of framework.
In sum, the utlity model has following advantage: but other particle of 0.1um level, and purification filtering is respond well, simple in structure.
The accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of plate film assembly.
Fig. 3 is the tangent plane schematic diagram of Fig. 2 AA direction.
In accompanying drawing, the corresponding name of Reference numeral is called: 1, water header, 2, the arm that catchments, 3, plate film assembly, 4, connect flexible pipe, 5, brace, 6, framework, 7, scavenge pipe, 8, aeration tube, 9, loose gas blowout head, 301, membrane module is installed and is supported, 302, upper-part centralized tank, 303, delivery port, 304, the bottom water leg, 305, Butterworth Hatch, 306, bore passages.
The specific embodiment
The utility model is described in further detail below in conjunction with embodiment and accompanying drawing, but embodiment of the present utility model is not limited to this.
Embodiment:
As shown in Figure 1 to Figure 3,
A kind of for Sewage Biological Treatment filtration plate film assembly, comprise framework 6 and be arranged on the plate film assembly 3 in framework, plate film assembly 3 comprises film body, and film body has the bore passages 306 that forms film body, and bore passages 306 1 ends are communicated with by connecting flexible pipe 4 arm 2 that catchments.The filter type of plate film assembly 3 is: advance internal-suction type outward and filter.Namely from the outside of plate film assembly 3, enter the inside of plate film assembly 3, form and filter, adopt Smoking regime, take the clear water of plate film assembly 3 inside away.Framework is for support plate membrane module 3.
Plate film assembly 3 is the earthenware slab membrane module.The earthenware slab membrane module is provided with the aperture of 0.1um, the catching probability and can reach more than 95% of its 0.1um particle.Use the PH scope to be 2-12, serviceability temperature can reach 80 degrees centigrade.
The arm 2 that catchments is communicated with water header 1.Water after water header 1 exhaust filtering.
Bore passages 306 is communicated with scavenge pipe 7 and aeration tube 8 away from an end that connects flexible pipe 4, between aeration tube 8 and bore passages 306, is provided with the gas blowout 9 of faling apart.Scavenge pipe 7 and aeration tube 8 forms back purge systems, and one is dropped into gas, one and passes into flushing water.
Plate film assembly 3 lower ends are provided with bottom water leg 304, bore passages 306 is communicated with bottom water leg 304, scavenge pipe 7 is communicated with bottom water leg 304, and aeration tube 8 extends into bottom water leg 304, and loose gas blowout 9 is communicated with the end that aeration tube 8 extends into bottom water leg 304.
Plate film assembly 3 upper ends are provided with upper-part centralized tank 302, and water header 1 is communicated with upper-part centralized tank 302 by connecting flexible pipe 4 successively.
Framework is provided with the axis brace 5 parallel with the plate film assembly surface.Brace 5 increases the support degree of framework.
Concrete, in framework 6, set up the plate film assembly 3 of 50-100 sheet, upper-part centralized tank 302 is communicated with bore passages 306, when plate film assembly 3 through after filtering, in bore passages 306, be full of clear water, after clear water meets water level, arrive upper-part centralized tank 302, with the delivery port 303 of upper-part centralized tank 302, be communicated with the discharge clear water by connecting flexible pipe 4.
While carrying out backwash, bottom water leg 304 connects scavenge pipes 7 by Butterworth Hatch 305, passes into backwashing water by scavenge pipe 7, by loose gas blowout 9, passes into gas for bottom water leg 304 with aeration tube 8 simultaneously and carries out Air Exposure, reach the purpose of backwash with this.
Water after this structure purifies, in its water outlet, to be less than 10, TSS content be that 0, TOC content is 5.2mg/L to the coli-group number, BOD content is 2mg/L, COD CrContent is 11mg/L, COD MnContent is 5mg/L, and T-N content is 7.3mg/L, and T-P content is 1.4mg/L; And in its former water, the coli-group number is less than countlessly, TSS content is 145, and TOC content is 22.3mg/L, and BOD content is 198mg/L, COD CrContent is 311mg/L, COD MnContent is 106mg/L, and T-N content is 23.1mg/L, and T-P content is 2.5mg/L.
Its operational mode is: in every ten minutes, 9.5 minutes is filtration time.0.5 minute be backwashing time.
As mentioned above, can well realize the utility model.

Claims (7)

1. one kind is filtered plate film assembly for Sewage Biological Treatment, it is characterized in that: comprise framework (6) and be arranged on the plate film assembly (3) in framework, plate film assembly (3) comprises film body, film body has the bore passages (306) that forms film body, and bore passages (306) one ends are communicated with the arm that catchments (2) by connecting flexible pipe (4).
2. according to claim 1 a kind of for Sewage Biological Treatment filtration plate film assembly, it is characterized in that: plate film assembly (3) is the earthenware slab membrane module.
3. according to claim 1 a kind of for Sewage Biological Treatment filtration plate film assembly, it is characterized in that: the arm that catchments (2) is communicated with water header (1).
4. according to claim 1 a kind of for Sewage Biological Treatment filtration plate film assembly, it is characterized in that: bore passages (306) is communicated with scavenge pipe (7) and aeration tube (8) away from an end that connects flexible pipe (4), between aeration tube (8) and bore passages (306), is provided with loose gas blowout head (9).
5. according to claim 4 a kind of for Sewage Biological Treatment filtration plate film assembly, it is characterized in that: plate film assembly (3) lower end is provided with bottom water leg (304), bore passages (306) is communicated with bottom water leg (304), scavenge pipe (7) is communicated with bottom water leg (304), aeration tube (8) extends into bottom water leg (304), and loose gas blowout head (9) is communicated with the end that aeration tube (8) extends into bottom water leg (304).
6. described a kind of for Sewage Biological Treatment filtration plate film assembly according to any one in claim 1-5, it is characterized in that: plate film assembly (3) upper end is provided with upper-part centralized tank (302), and water header (1) is communicated with upper-part centralized tank (302) by connecting flexible pipe (4) successively.
7. described a kind of for Sewage Biological Treatment filtration plate film assembly according to any one in claim 1-5, it is characterized in that: framework is provided with the axis brace (5) parallel with the plate film assembly surface.
CN2013203892995U 2013-07-02 2013-07-02 Flat membrane component for biological sewage treatment filtration Expired - Lifetime CN203303844U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
CN2013203892995U CN203303844U (en) 2013-07-02 2013-07-02 Flat membrane component for biological sewage treatment filtration

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104891655A (en) * 2015-06-02 2015-09-09 中国科学院生态环境研究中心 Device and method for treating high ammonia nitrogen wastewater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104891655A (en) * 2015-06-02 2015-09-09 中国科学院生态环境研究中心 Device and method for treating high ammonia nitrogen wastewater

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Granted publication date: 20131127