CN203960014U - High-concentration waste water treatment integrated apparatus - Google Patents
High-concentration waste water treatment integrated apparatus Download PDFInfo
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- CN203960014U CN203960014U CN201420389463.7U CN201420389463U CN203960014U CN 203960014 U CN203960014 U CN 203960014U CN 201420389463 U CN201420389463 U CN 201420389463U CN 203960014 U CN203960014 U CN 203960014U
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- reactor
- pipe
- conservancy diversion
- water conservancy
- perforated pipe
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Abstract
A kind of high-concentration waste water treatment integrated apparatus, the water inlet pipe that reactor lower part connects is connected with the lower perforated pipe in reactor, it is material bed that the interior bottom of reactor is filled with anaerobion, above anaerobion is material bed, establish again perforated pipe on, upper perforated pipe is connected with the air intake pump one end outside reactor, and above upper perforated pipe, reaction zone is provided with water conservancy diversion membrane module, and reactor head is provided with taper vapor pipe, vapor pipe venting port connects the other end of air intake pump, and reactor top connects rising pipe 9.The reaction zone that the utility model is placed into anaerobic mud bed reactor by water conservancy diversion membrane module forms Novel built-in type anaerobic sludge bed apparatus, water conservancy diversion membrane module can force the gas that anaerobic digestion produces to pass through in its less passage, sewage sludge in passage is obtained than original much bigger aerodynamic force, do not increasing under the condition of hydraulic load, strengthen muddy water mass transfer, realize the self cleaning function of water conservancy diversion membrane module, thereby realize and be issued to high COD removal effect in high hydraulic load condition, and reducing film pollutes, improve membrane module service efficiency, reduce energy consumption.
Description
Technical field
The utility model relates to a kind of efficient industry high-concentration wastewater treatment equipment, relates in particular to for marine fishery processing industry, beer waste water corn processed waste water, alcohol distilled wastewater, malting effluent, the processing of the high concentrated organic wastewaters such as pharmacy waste water.
Background technology
Aspect sewage disposal, by membrane sepn and the biological treatment traditional treatment process such as active sludge that membrane bioreactor (MBR) technology that forms compares that combine, there is unrivaled huge advantage, for example the water quality of water outlet is good, water outlet can direct reuse, there is extremely high hydraulic load, floor space is also minimum simultaneously, and surplus sludge volume is few etc.And can solve thoroughly the microbes facing in micro-organism treatment process and along with water outlet, run off and caused process result degrades and effluent quality variation, it can be trapped in microorganism in reactor completely.Certainly favourable also have fraud, same shortcomings that have a lot of its development of restriction and application of anaerobism MBR.First be the total problem of MBR, the cost of film is high, and energy consumption is also relatively high, can produce film and pollute, and needs frequent cleaning and replacing, because film pollution can cause the minimizing of membrane flux, is that the minimizing of the saturating rate of water can have a strong impact on processing efficiency.Current anaerobism MBR mostly adopts external placed type (adopting external placed type to be because lack air bubbling in reactor, so need to carry out liquid circulation to improve pollution situation by water pump), thereby has caused power consumption relatively high.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of device for high concentration waste water treatment, can under relatively low upflow velocity, obtain high clearance, reduces film and pollutes, and improves film service efficiency.Improve on the one hand the life cycle of reactor, reduced operation and maintenance cost; Also reduce on the other hand floor space, saved energy consumption.
For solving the problems of the technologies described above, the utility model provides a kind of high-concentration waste water treatment integrated apparatus, it is characterized in that: the water inlet pipe that reactor lower part connects is connected with the lower perforated pipe in reactor, it is material bed that the interior bottom of reactor is filled with anaerobion, above anaerobion is material bed, establish again perforated pipe on, between the material bed and upper perforated pipe of anaerobion, outside position, connect a shore pipe, upper perforated pipe is connected with the air intake pump one end outside reactor, above upper perforated pipe, reaction zone is provided with water conservancy diversion membrane module, reactor head is provided with taper vapor pipe, vapor pipe venting port connects the other end of air intake pump, reactor top connects rising pipe 9.
Described perforated pipe is the perforation arm a vertical evenly connection level of perforated pipe circumferential apertures place.Described water conservancy diversion membrane module is dull and stereotyped water conservancy diversion film to be set or with setback plate water conservancy diversion film framework is tilted.
The reaction zone that the utility model is placed into anaerobic mud bed reactor by water conservancy diversion membrane module forms Novel built-in type anaerobic sludge bed apparatus, water conservancy diversion membrane module can force the gas that anaerobic digestion produces to pass through in its less passage, sewage sludge in passage is obtained than original much bigger aerodynamic force, do not increasing under the condition of hydraulic load, strengthen muddy water mass transfer, realize the self cleaning function of water conservancy diversion membrane module, thereby realize and be issued to high COD removal effect in high hydraulic load condition, and reducing film pollutes, improve membrane module service efficiency, reduce energy consumption.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is perforated pipe layout drawing;
Fig. 3 is same setback plate water conservancy diversion membrane module structure figure.
Embodiment
With reference to Fig. 1, the long the ratio of width to height 1:1 of this reactor 10 design: 6, effective high 180cm, protect high 20cm, long * wide, useful volume, the water inlet pipe 1 that reactor lower part connects is connected with the lower perforated pipe 2 in reactor, in reactor, bottom is filled with anaerobion material bed 3, above anaerobion is material bed, establish again perforated pipe 5 on, between the material bed and upper perforated pipe of anaerobion, outside position, connect a shore pipe 4, upper perforated pipe is connected with air intake pump 6 one end outside reactor, on upper perforated pipe, identity distance reactor bottom 100cm works the dull and stereotyped water conservancy diversion membrane modules 7 of arranging inclination 60 degree, arrange altogether 4 water conservancy diversion moulds 701, water conservancy diversion membrane module model is: length is 25cm, width is 25cm, 60 degree that tilt are placed in organic glass frame 702, reactor head is provided with taper vapor pipe 8, vapor pipe venting port connects the other end of air intake pump 6, reactor top connects rising pipe 9.
With reference to Fig. 2, upper and lower perforated pipe is all the perforation arm 12 of even connection level on vertical perforated pipe 11 circumference, and reactor water inlet pipe is connected with vertical perforated pipe 11.
With reference to Fig. 3, with setback plate water conservancy diversion membrane module, be, at organic glass frame 702 medium dip 60 degree, same setback plate water conservancy diversion film 703 is set, then put into reactor reaction zone.
During work, processed sewage enters reactor water distribution system perforated pipe 2 by water inlet pipe 1, then processed sewage evenly enters material bed 3 reaction zones of anaerobion by eyelet, muddy water mixed solution in reaction zone and the biogas producing due to microbiological anaerobic digestion upwards flow, biogas rises, enter in the passage of perforated pipe 5, biogas is by after water conservancy diversion membrane module 7, gas continues to rise, portion gas is got rid of by top vapor pipe 8, also can portion gas be entered in the passage of upper perforated pipe 5 by air pump 6, to add the upflow velocity of atmospheric, then play the effect of air purge membrane module.Be in the mud of reaction zone 3, the good mud of part settling property can fall back in Sludge Bed by nature, and the water after processing is discharged through rising pipe 9.
Claims (4)
1. a high-concentration waste water treatment integrated apparatus, it is characterized in that: the water inlet pipe that reactor lower part connects is connected with the lower perforated pipe in reactor, it is material bed that the interior bottom of reactor is filled with anaerobion, above anaerobion is material bed, establish again perforated pipe on, between the material bed and upper perforated pipe of anaerobion, outside position, connect a shore pipe, upper perforated pipe is connected with the air intake pump one end outside reactor, above upper perforated pipe, reaction zone is provided with water conservancy diversion membrane module, reactor head is provided with taper vapor pipe, vapor pipe venting port connects the other end of air intake pump, reactor top connects rising pipe.
2. high-concentration waste water treatment integrated apparatus according to claim 1, is characterized in that: described upper and lower perforated pipe is all the perforation arm a vertical evenly connection level of perforated pipe circumferential apertures place.
3. according to the high-concentration waste water treatment integrated apparatus described in claim 1 or 2, it is characterized in that: described water conservancy diversion membrane module is dull and stereotyped water conservancy diversion film to be set or with setback plate water conservancy diversion film framework is tilted.
4. high-concentration waste water treatment integrated apparatus according to claim 3, is characterized in that: water conservancy diversion film inclination 60 degree of water conservancy diversion membrane module are arranged in organic glass frame.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420389463.7U CN203960014U (en) | 2014-07-15 | 2014-07-15 | High-concentration waste water treatment integrated apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420389463.7U CN203960014U (en) | 2014-07-15 | 2014-07-15 | High-concentration waste water treatment integrated apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203960014U true CN203960014U (en) | 2014-11-26 |
Family
ID=51920623
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420389463.7U Expired - Fee Related CN203960014U (en) | 2014-07-15 | 2014-07-15 | High-concentration waste water treatment integrated apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203960014U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105502653A (en) * | 2016-01-28 | 2016-04-20 | 中国科学技术大学 | Anaerobic biological membrane-membrane bioreactor and sewage treatment method |
-
2014
- 2014-07-15 CN CN201420389463.7U patent/CN203960014U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105502653A (en) * | 2016-01-28 | 2016-04-20 | 中国科学技术大学 | Anaerobic biological membrane-membrane bioreactor and sewage treatment method |
| CN105502653B (en) * | 2016-01-28 | 2018-05-29 | 中国科学技术大学 | A kind of anaerobic organism film-membrane bioreactor and sewage water treatment method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170106 Address after: 130013 Jilin province Changchun Tongxin Village District City Garden III District 14 Building Room 102 garage Patentee after: Changchun Kelong Environmental Consulting Co., Ltd. Address before: 315012 Ningbo Airport Road, Zhejiang, No. 1988 Patentee before: Zhejiang Business Technology Institute |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141126 Termination date: 20210715 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |