CN201581030U - Garbage leachate treatment device - Google Patents
Garbage leachate treatment device Download PDFInfo
- Publication number
- CN201581030U CN201581030U CN2009202822999U CN200920282299U CN201581030U CN 201581030 U CN201581030 U CN 201581030U CN 2009202822999 U CN2009202822999 U CN 2009202822999U CN 200920282299 U CN200920282299 U CN 200920282299U CN 201581030 U CN201581030 U CN 201581030U
- Authority
- CN
- China
- Prior art keywords
- pipe
- casing body
- baffle
- deflection baffle
- ultra
- 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 - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000000945 filler Substances 0.000 claims abstract description 10
- 238000005276 aerator Methods 0.000 claims abstract description 7
- 239000012528 membrane Substances 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 11
- 230000000630 rising effect Effects 0.000 claims description 11
- 238000007789 sealing Methods 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 abstract description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000001651 autotrophic effect Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000001728 nano-filtration Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 239000010865 sewage Substances 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Disclosed is a garbage leachate treatment device. A water inlet pipe is arranged on one side of a casing body; the middle of the casing body is divided into two mutually communicated portions by a baffle plate and a lower deflection baffle plate; a plurality of equally spaced and mutually parallel upper deflection baffle plates are distributed and connected on the inner wall surface of the casing body through a closed portion; the top end and two sides of each upper deflection baffle plate are connected onto the inner wall of the casing body; lower plate sections of the upper deflection baffle plates are suspended and processed into folded plates; a plurality of equally spaced and perpendicular lower deflection baffle plates are connected onto the bottom inner wall of the casing body; fillers are arranged among the upper deflection baffle plates and the lower deflection baffle plates; a return pipe and a water outlet pipe which are mutually communicated are arranged at the bottom portion of the casing body; a biogas pipe is connected to the top portion of the casing body; an ultra-filtration film component is arranged on an opening portion of the upper portion of the casing body; a water outlet pipe with a water outlet pump is arranged on the upper edge of the ultra-filtration film component; an air pipe with an aerator is arranged on the lower edge of the ultra-filtration film component; and a stirrer is arranged on one side of the ultra-filtration film component. The treatment device is simple, compact, small in area occupation and low in treatment cost.
Description
Technical field
The utility model relates to a kind of water pollution control technical equipment, especially garbage filter liquid processing device.
Background technology
The processing of percolate is a unusual stubborn problem in landfill yard design, operation and the management always, is a difficult problem of generally acknowledging in the world.Garbage loading embeading is handled a kind of main mode that is still China's domestic rubbish disposal.Because the water quality and quantity of percolate changes greatly, ammonia-nitrogen content is high, organic pollutant content height and be difficult to problem such as biodegradable organic content height, cause the percolate treatment facility water outlet of the most of refuse landfill of China not reach emission request, can not be called sanitary filling field truly, at present comparatively general percolate treatment facility adopts (1) to adopt " biochemistry+materialization " technical finesse percolate, the biochemical treatment process can be degraded effectively, removal of pollutants, but is subjected to the not restriction of bio-degradable resistates existence.(2) directly adopt " high-pressure membrane separation " technical finesse percolate, the membrane sepn treating processes can be divided dried up and pollutent effectively, but because the membrane sepn processing can not be degraded, removal of pollutants, correspondingly can produce concentrated sewage more difficult in a large number, that dispose.(3) comprehensive " biochemistry+materialization+membrane sepn " technical finesse percolate that adopts, wherein, the biochemical treatment process can be degraded effectively, removal of pollutants, and the membrane sepn treating processes can be separated effectively and removed the not amounts of residual contamination do of bio-degradable, but also can produce condensed water.
Summary of the invention
In order to overcome the deficiencies in the prior art, the utility model provides a kind of novel garbage filter liquid processing device, adopts this device treating refuse percolate, simply, compactness is taken up an area of for a short time, and processing cost is low can to realize percolate low-cost processes and qualified discharge.
The technical scheme that its technical problem that solves the utility model adopts is: the garbage filter liquid processing device, one side is brought the housing of water pipe into, the centre has baffle plate to be divided into the two portions that communicate with following baffle, the part of sealing distribute to connect on the inner walls face a plurality of spacings identical and be parallel to each other on baffle, its top and both sides are connected on the inner walls, its lower plate section suspends and is processed into flap, and the flap bottom is towards rising pipe side, on inwall at the bottom of the housing, connect spacing and equate also vertical a plurality of baffle down, filler is arranged between the baffle up and down, the housing bottom influent side has return line to communicate with rising pipe, on one side case top is connected with the biogas pipe; Top is that open part has hyperfiltration membrane assembly, and there is the rising pipe of taking water pump and valve out of its top, and there is the blast main of band aerator in hyperfiltration membrane assembly bottom, and a side of hyperfiltration membrane assembly has agitator.
The garbage filter liquid processing device is spaced apart two parts that communicate in the housing, Yi Bian anaerobic reactor baffle is up and down arranged, this part is formed the anaerobic baffled reactor with several compartments.Each upper compartment at anaerobic baffled reactor is provided with the water treatment filler, can select elastic filler, combined stuffing, soft-filler etc., makes attached biological film on the filler.The two portions that communicate can flow automatically and enter.Hyperfiltration membrane assembly is set in the other side, the blast main of aerator is installed below it.This part is called the one-step autotrophic nitrogen removal membrane bioreactor.Can realize one-step autotrophic nitrogen removal.
The ultra-filtration membrane junctional membrane goes out water pump.Sewage is under suction function in the one-step autotrophic nitrogen removal membrane bioreactor, and by ultrafiltration membrance filter, tunicle goes out water pump and extracts out.A film water outlet part flow to nanofiltration equipment, a part by return line flow to the anaerobic reactor feed-water end.
Film goes out water pump and connects nanofiltration equipment.The ultrafiltration water outlet enters nanofiltration system and carries out depth type filtration, realizes qualified discharge.This equipment also can adopt reverse osmosis system that advanced treatment is carried out in the ultra-filtration membrane water outlet, can realize same effect.
The beneficial effects of the utility model are, this device is simple, and compactness is taken up an area of for a short time, and processing cost is lower, has realized saving energy and reduce the cost, and has wide market application prospect.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is the front view of garbage filter liquid processing device.
Fig. 1 is the vertical view of garbage filter liquid processing device.
1. housings among the figure, 2. filler, 3. biogas pipe, 4. baffle plate 5. goes out water pump, 6. rising pipe, 7. valve, 8. return line, 9. agitator, 10. aerator, 11. blast mains, 12. hyperfiltration membrane assemblies, 13. times baffles, baffle on 14., 15. water inlet pipes.
Embodiment
At Fig. 1, in 2, the garbage filter liquid processing device, one side is brought the housing (1) of water pipe (15) into, the centre has baffle plate (4) to be divided into the two portions that communicate with following baffle (13), the part of sealing distribute to connect on the inner walls face 2 spacings identical and be parallel to each other on baffle (14), its top and both sides are connected on the inner walls, its lower plate section suspends and is processed into flap, and the flap bottom is towards rising pipe side, connecting spacing on inwall at the bottom of the housing equates and vertical 3 following baffles, filler (2) is arranged between the baffle up and down, and the housing bottom influent side has return line (8) to communicate with rising pipe, on one side case top is connected with biogas pipe (3); Top is that open part has hyperfiltration membrane assembly (12), and there is the rising pipe (6) of taking water pump (5) and valve (7) out of its top, and there is the blast main (11) of band aerator (10) in hyperfiltration membrane assembly bottom, and a side of hyperfiltration membrane assembly has agitator (9).
Claims (3)
1. garbage filter liquid processing device, by housing, filler, the biogas pipe, baffle plate, go out water pump, rising pipe, valve, return line, agitator, aerator, blast main, hyperfiltration membrane assembly, following baffle, last baffle, water inlet pipe is formed, it is characterized in that: a side is brought the housing (1) of water pipe (15) into, the centre has baffle plate (4) to be divided into the two portions that communicate with following baffle (13), the part of sealing distribute to connect on the inner walls face a plurality of spacings identical and be parallel to each other on baffle (14), its top and both sides are connected on the inner walls, its lower plate section suspends and is processed into flap, and the flap bottom is towards rising pipe side, on inwall at the bottom of the housing, connect vertical a plurality of baffles down that spacing equates, filler (2) is arranged between last baffle and the following baffle; Top is that open part has hyperfiltration membrane assembly (12), and there is the rising pipe (6) of taking water pump (5) and valve (7) out of its top, and there is the blast main (11) of band aerator (10) in hyperfiltration membrane assembly bottom, and a side of hyperfiltration membrane assembly has agitator (9).
2. garbage filter liquid processing device according to claim 1 is characterized in that: on one side case top is connected with biogas pipe (3).
3. garbage filter liquid processing device according to claim 1 is characterized in that: the housing bottom influent side has return line (8) to communicate with rising pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202822999U CN201581030U (en) | 2009-11-29 | 2009-11-29 | Garbage leachate treatment device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202822999U CN201581030U (en) | 2009-11-29 | 2009-11-29 | Garbage leachate treatment device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201581030U true CN201581030U (en) | 2010-09-15 |
Family
ID=42723027
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2009202822999U Expired - Fee Related CN201581030U (en) | 2009-11-29 | 2009-11-29 | Garbage leachate treatment device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201581030U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2505515A (en) * | 2012-09-04 | 2014-03-05 | Integrated Effluent Solutions Ltd | Treatment of contaminated effluent |
CN103922473A (en) * | 2014-04-22 | 2014-07-16 | 昆明金泽实业有限公司 | Anaerobic and aerobiotic circular integration waste water treatment device with low energy consumption |
CN104692524A (en) * | 2014-10-21 | 2015-06-10 | 深圳市百斯特环保工程有限公司 | Anaerobic baffled reactor and leachate anaerobic treatment method |
CN106186512A (en) * | 2016-07-07 | 2016-12-07 | 北京城市排水集团有限责任公司 | A kind of sewage-treatment plant and processing method thereof |
-
2009
- 2009-11-29 CN CN2009202822999U patent/CN201581030U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2505515A (en) * | 2012-09-04 | 2014-03-05 | Integrated Effluent Solutions Ltd | Treatment of contaminated effluent |
CN103922473A (en) * | 2014-04-22 | 2014-07-16 | 昆明金泽实业有限公司 | Anaerobic and aerobiotic circular integration waste water treatment device with low energy consumption |
CN103922473B (en) * | 2014-04-22 | 2015-09-23 | 昆明金泽实业有限公司 | A kind of anaerobism of less energy-consumption and aerobic circular integration wastewater treatment equipment |
CN104692524A (en) * | 2014-10-21 | 2015-06-10 | 深圳市百斯特环保工程有限公司 | Anaerobic baffled reactor and leachate anaerobic treatment method |
CN106186512A (en) * | 2016-07-07 | 2016-12-07 | 北京城市排水集团有限责任公司 | A kind of sewage-treatment plant and processing method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202849154U (en) | Novel anaerobic membrane bioreactor for treating high-sulfate organic wastewater | |
CN201581030U (en) | Garbage leachate treatment device | |
CN105347475B (en) | A kind of symmetrical built-in anaerobic membrane bioreactor | |
CN215161380U (en) | External anaerobic MBR device | |
CN106277593B (en) | An integrated domestic sewage treatment system | |
CN202849204U (en) | Mmultistage sewage treatment device utilizing microbial technology | |
CN201648106U (en) | Coking wastewater flat-plate MBR treatment equipment | |
CN205061738U (en) | Clarifier is adsorbed with fixed attention to high -efficient mixing | |
CN205061814U (en) | Domestic sewage purification treatment facility | |
CN103241834A (en) | Pulse internal circulation anaerobic reactor | |
CN213680283U (en) | Novel high-efficient biological integration sewage treatment device | |
CN102260023B (en) | Apparatus for treating domestic sewage by utilizing anaerobic expanded granular sludge bed | |
CN106277592B (en) | Double-membrane self-circulation sewage treatment system | |
CN204752312U (en) | Up -flow anaerobic sludge blanket filtering pond | |
CN214693752U (en) | Integrated sewage treatment equipment | |
CN210974071U (en) | Water seal device of anaerobic tank | |
CN210065289U (en) | Integrated medical wastewater treatment device | |
CN102992550B (en) | Mudpack coupled duplex integrated high rate anaerobic reactor and application thereof | |
CN108328869B (en) | Anaerobic membrane bioreactor and wastewater treatment system | |
CN206052010U (en) | A kind of multistage collection scum silica frost organic garbage methane installation for fermenting | |
CN204981519U (en) | Sewage treatment inner loop MBR membrane bioreactor | |
CN205382072U (en) | High -efficiency biological membrane integration sewage treatment system | |
CN211847599U (en) | Movable land industrial sewage treatment machine | |
CN214528590U (en) | Denitrification device for municipal sewage treatment | |
CN205061644U (en) | Save reinforceing of medicament and thoughtlessly congeal clarifier |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100915 Termination date: 20121129 |