CN207210188U - A kind of garbage penetrating fluid processing system - Google Patents
A kind of garbage penetrating fluid processing system Download PDFInfo
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- CN207210188U CN207210188U CN201621445844.8U CN201621445844U CN207210188U CN 207210188 U CN207210188 U CN 207210188U CN 201621445844 U CN201621445844 U CN 201621445844U CN 207210188 U CN207210188 U CN 207210188U
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- pipeline
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- filtering ponds
- pond
- biochemistry pool
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Abstract
The utility model discloses a kind of garbage penetrating fluid processing system, including the first filtering ponds, sedimentation basin, pH value regulating reservoir, biochemistry pool, anaerobic pond, denitrification pond, nitrification tank, the second filtering ponds, sludge concentration tank, detection cell, clear water reserviors.The utility model utilizes rational pre-treatment, goes the removal of impurity, improves penetrating fluid biodegradability, physical-chemical process and biochemical process are rationally make use of, removes ammonia nitrogen and hardly degraded organic substance, the complementary advantage of each method can be played, high treating effect, energy qualified discharge, cost are low.
Description
【Technical field】
The utility model belongs to sewage disposal system technical field, more particularly to a kind of garbage penetrating fluid processing system.
【Background technology】
Contain very more polluters in city life garbage landfill penetrating fluid (hereinafter referred to as " penetrating fluid "), and
It is dense, and these groups of contaminants are closely related into factors such as the environmental condition with concentration and landfill yard, the landfill time limits, its
Greatly and complicated component, biodegradability is poor for water quality and quantity change, turns into grave danger of environment, percolate without processing completely
It is discharged into rivers and lakes, organic pollution therein, inorganic pollution can be contaminated aquatile and crops, and pass through food
Thing chain and ecological environment produce harm to health.Current refuse leachate processing equipment, to organic matter, nitrogen, phosphorus and again
The filtering of metal, decomposition efficiency be not high, and the water quality of filtering is unstable, it is difficult to meets《Consumer waste filling and embedding contamination control standard》
The discharge standard of (GB 16889-2008).Patent No. ZL201220110944.0 Chinese patent was on November 21st, 2012
A kind of device for treatment of garbage penetrant is disclosed, two kinds of processing modes of MBR and DTRO can be combined to enter percolate
The water outlet of row processing, the treatment in situ, raising of achievable refuse leachate to the removal ability of ammonia nitrogen and organic matter, processing can
National grade one discharge standard is stably reached, but this installation cost is too high, it is therefore desirable to which group is optimized to each handling process
Close, so as to realize the efficiency of whole system, make discharged wastewater met the national standard.
【Utility model content】
The utility model provides a kind of garbage penetrating fluid processing system, to solve existing infiltration liquid processing device in the presence of scarce
The problems such as refuse leachate cost is high is fallen into or handles, the utility model utilizes rational pre-treatment, goes the removal of impurity, improves penetrating fluid
Biodegradability, physical-chemical process and biochemical process are rationally make use of, remove ammonia nitrogen and hardly degraded organic substance, the mutual of each method can be played
The advantage of benefit, high treating effect, energy qualified discharge, cost are low.
To solve above technical problem, the utility model provides following technical scheme：
A kind of garbage penetrating fluid processing system, including the first filtering ponds, sedimentation basin, pH value regulating reservoir, biochemistry pool, anaerobism
Pond, denitrification pond, nitrification tank, the second filtering ponds, sludge concentration tank, detection cell, clear water reserviors, the first filtering ponds side pass through
Pipeline is connected with the sedimentation basin；The sedimentation basin opposite side is connected by pipeline with the pH value regulating reservoir；The pH value is adjusted
Section pond opposite side is connected by pipeline with the biochemistry pool；The biochemistry pool opposite side is connected by pipeline with the anaerobic pond；
The anaerobic pond opposite side is connected by pipeline with the denitrification pond；Denitrification pond opposite side passes through pipeline and the nitre
Change pond to be connected；The nitrification tank opposite side is connected by pipeline with second filtering ponds；The second filtering ponds opposite side leads to
Piping is connected with the sludge concentration tank；The sludge concentration tank opposite side is connected by pipeline with the detection cell；It is described
Detection cell opposite side is connected by pipeline with the clear water reserviors.
Further, first filtering ponds are provided with the first filtering ponds water inlet pipe, and grid are provided with first filtering ponds
Net, the grid gap length of the aperture plate is 0.01-1cm.
Further, separation filter plate is provided with the sedimentation basin, temperature device, the temperature dress are provided with the sedimentation basin
Put and maintain temperature at 22-30 DEG C.
Further, the biochemistry pool is provided with biochemistry pool air inlet pipe, aeration tube, observation panel, and the biochemistry pool air inlet pipe is set
On the biochemistry pool, the aeration tube is located at the biochemistry pool bottom, and the observation panel is located at the top of the biochemistry pool.
Further, the clear water reserviors are provided with clear water reserviors outlet pipe.
The utility model has following effects：
(1) rational pre-treatment is utilized, goes the removal of impurity, penetrating fluid biodegradability is improved, rationally make use of physical-chemical process
And biochemical process, ammonia nitrogen and hardly degraded organic substance are removed, the complementary advantage of each method can be played, high treating effect can row up to standard
Put, cost is low；
(2) relief liquor of each device can flow back reprocessing, reduce in processing procedure two caused by caused pollutant again
Secondary pollution.
【Brief description of the drawings】
Fig. 1 is the utility model garbage penetrating fluid processing system structural representation,
In figure, 1 is the first filtering ponds, and 1-1 is the first filtering ponds water inlet pipe, and 2 be sedimentation basin, and 3 be pH value regulating reservoir, and 4 are
Biochemistry pool, 41 be biochemistry pool air inlet pipe, and 42 be aeration tube, and 43 be observation panel, and 5 be anaerobic pond, and 6 be denitrification pond, and 7 be nitrification
Pond, 8 be the second filtering ponds, and 9 be sludge concentration tank, and 10 be detection cell, and 11 be clear water reserviors, and 111 be clear water reserviors outlet pipe.
【Embodiment】
The utility model content is described in detail with reference to such as Fig. 1.
Embodiment 1
A kind of garbage penetrating fluid processing system, including the first filtering ponds 1, sedimentation basin 2, pH value regulating reservoir 3, biochemistry pool 4, detest
Oxygen pond 5, denitrification pond 6, nitrification tank 7, the second filtering ponds 8, sludge concentration tank 9, detection cell 10, clear water reserviors 11, first mistake
The side of filter tank 1 is connected by pipeline with the sedimentation basin 2；First filtering ponds 1 are provided with the first filtering ponds water inlet pipe 1-1,
Aperture plate is provided with first filtering ponds 1, the grid gap length of the aperture plate is 0.05cm；The opposite side of sedimentation basin 2 leads to
Piping is connected with the pH value regulating reservoir 3；Separation filter plate is provided with the sedimentation basin 2, being provided with temperature in the sedimentation basin 2 fills
Put, the temperature device maintains temperature at 26 DEG C；The opposite side of pH value regulating reservoir 3 is connected by pipeline with the biochemistry pool 4；
The biochemistry pool 4 is provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, and the biochemistry pool air inlet pipe 41 is located at the life
Change on pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；It is described
The opposite side of biochemistry pool 4 is connected by pipeline with the anaerobic pond 5；The opposite side of anaerobic pond 5 passes through pipeline and the denitrification
Pond 6 is connected；The opposite side of denitrification pond 6 is connected by pipeline with the nitrification tank 7；The opposite side of nitrification tank 7 passes through pipe
Road is connected with second filtering ponds 8；The opposite side of second filtering ponds 8 is connected by pipeline with the sludge concentration tank 9；Institute
The opposite side of sludge concentration tank 9 is stated by pipeline with the detection cell 10 to be connected；The opposite side of detection cell 10 passes through pipeline and institute
Clear water reserviors 11 are stated to be connected；The clear water reserviors 11 are provided with clear water reserviors outlet pipe 111.
Embodiment 2
A kind of garbage penetrating fluid processing system, including the first filtering ponds 1, sedimentation basin 2, pH value regulating reservoir 3, biochemistry pool 4, detest
Oxygen pond 5, denitrification pond 6, nitrification tank 7, the second filtering ponds 8, sludge concentration tank 9, detection cell 10, clear water reserviors 11, first mistake
The side of filter tank 1 is connected by pipeline with the sedimentation basin 2；First filtering ponds 1 are provided with the first filtering ponds water inlet pipe 1-1,
Aperture plate is provided with first filtering ponds 1, the grid gap length of the aperture plate is 0.01cm；The opposite side of sedimentation basin 2 leads to
Piping is connected with the pH value regulating reservoir 3；Separation filter plate is provided with the sedimentation basin 2, being provided with temperature in the sedimentation basin 2 fills
Put, the temperature device maintains temperature at 22 DEG C；The opposite side of pH value regulating reservoir 3 is connected by pipeline with the biochemistry pool 4；
The biochemistry pool 4 is provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, and the biochemistry pool air inlet pipe 41 is located at the life
Change on pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；It is described
The opposite side of biochemistry pool 4 is connected by pipeline with the anaerobic pond 5；The opposite side of anaerobic pond 5 passes through pipeline and the denitrification
Pond 6 is connected；The opposite side of denitrification pond 6 is connected by pipeline with the nitrification tank 7；The opposite side of nitrification tank 7 passes through pipe
Road is connected with second filtering ponds 8；The opposite side of second filtering ponds 8 is connected by pipeline with the sludge concentration tank 9；Institute
The opposite side of sludge concentration tank 9 is stated by pipeline with the detection cell 10 to be connected；The opposite side of detection cell 10 passes through pipeline and institute
Clear water reserviors 11 are stated to be connected；The clear water reserviors 11 are provided with clear water reserviors outlet pipe 111.
Embodiment 3
A kind of garbage penetrating fluid processing system, including the first filtering ponds 1, sedimentation basin 2, pH value regulating reservoir 3, biochemistry pool 4, detest
Oxygen pond 5, denitrification pond 6, nitrification tank 7, the second filtering ponds 8, sludge concentration tank 9, detection cell 10, clear water reserviors 11, first mistake
The side of filter tank 1 is connected by pipeline with the sedimentation basin 2；First filtering ponds 1 are provided with the first filtering ponds water inlet pipe 1-1,
Aperture plate is provided with first filtering ponds 1, the grid gap length of the aperture plate is 1cm；The opposite side of sedimentation basin 2 passes through pipe
Road is connected with the pH value regulating reservoir 3；Separation filter plate is provided with the sedimentation basin 2, temperature device is provided with the sedimentation basin 2,
The temperature device maintains temperature at 30 DEG C；The opposite side of pH value regulating reservoir 3 is connected by pipeline with the biochemistry pool 4；Institute
State biochemistry pool 4 and be located at the biochemistry provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, the biochemistry pool air inlet pipe 41
On pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；The life
Change the opposite side of pond 4 by pipeline with the anaerobic pond 5 to be connected；The opposite side of anaerobic pond 5 passes through pipeline and the denitrification pond
6 are connected；The opposite side of denitrification pond 6 is connected by pipeline with the nitrification tank 7；The opposite side of nitrification tank 7 passes through pipeline
It is connected with second filtering ponds 8；The opposite side of second filtering ponds 8 is connected by pipeline with the sludge concentration tank 9；It is described
The opposite side of sludge concentration tank 9 is connected by pipeline with the detection cell 10；The opposite side of detection cell 10 by pipeline with it is described
Clear water reserviors 11 are connected；The clear water reserviors 11 are provided with clear water reserviors outlet pipe 111.
Embodiment 4
A kind of garbage penetrating fluid processing system, including the first filtering ponds 1, sedimentation basin 2, pH value regulating reservoir 3, biochemistry pool 4, detest
Oxygen pond 5, denitrification pond 6, nitrification tank 7, the second filtering ponds 8, sludge concentration tank 9, detection cell 10, clear water reserviors 11, first mistake
The side of filter tank 1 is connected by pipeline with the sedimentation basin 2；First filtering ponds 1 are provided with the first filtering ponds water inlet pipe 1-1,
Aperture plate is provided with first filtering ponds 1, the grid gap length of the aperture plate is 0.04cm；The opposite side of sedimentation basin 2 leads to
Piping is connected with the pH value regulating reservoir 3；Separation filter plate is provided with the sedimentation basin 2, being provided with temperature in the sedimentation basin 2 fills
Put, the temperature device maintains temperature at 24 DEG C；The opposite side of pH value regulating reservoir 3 is connected by pipeline with the biochemistry pool 4；
The biochemistry pool 4 is provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, and the biochemistry pool air inlet pipe 41 is located at the life
Change on pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；It is described
The opposite side of biochemistry pool 4 is connected by pipeline with the anaerobic pond 5；The opposite side of anaerobic pond 5 passes through pipeline and the denitrification
Pond 6 is connected；The opposite side of denitrification pond 6 is connected by pipeline with the nitrification tank 7；The opposite side of nitrification tank 7 passes through pipe
Road is connected with second filtering ponds 8；The opposite side of second filtering ponds 8 is connected by pipeline with the sludge concentration tank 9；Institute
The opposite side of sludge concentration tank 9 is stated by pipeline with the detection cell 10 to be connected；The opposite side of detection cell 10 passes through pipeline and institute
Clear water reserviors 11 are stated to be connected；The clear water reserviors 11 are provided with clear water reserviors outlet pipe 111.
Embodiment 5
A kind of garbage penetrating fluid processing system, including the first filtering ponds 1, sedimentation basin 2, pH value regulating reservoir 3, biochemistry pool 4, detest
Oxygen pond 5, denitrification pond 6, nitrification tank 7, the second filtering ponds 8, sludge concentration tank 9, detection cell 10, clear water reserviors 11, first mistake
The side of filter tank 1 is connected by pipeline with the sedimentation basin 2；First filtering ponds 1 are provided with the first filtering ponds water inlet pipe 1-1,
Aperture plate is provided with first filtering ponds 1, the grid gap length of the aperture plate is 0.08cm；The opposite side of sedimentation basin 2 leads to
Piping is connected with the pH value regulating reservoir 3；Separation filter plate is provided with the sedimentation basin 2, being provided with temperature in the sedimentation basin 2 fills
Put, the temperature device maintains temperature at 28 DEG C；The opposite side of pH value regulating reservoir 3 is connected by pipeline with the biochemistry pool 4；
The biochemistry pool 4 is provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, and the biochemistry pool air inlet pipe 41 is located at the life
Change on pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；It is described
The opposite side of biochemistry pool 4 is connected by pipeline with the anaerobic pond 5；The opposite side of anaerobic pond 5 passes through pipeline and the denitrification
Pond 6 is connected；The opposite side of denitrification pond 6 is connected by pipeline with the nitrification tank 7；The opposite side of nitrification tank 7 passes through pipe
Road is connected with second filtering ponds 8；The opposite side of second filtering ponds 8 is connected by pipeline with the sludge concentration tank 9；Institute
The opposite side of sludge concentration tank 9 is stated by pipeline with the detection cell 10 to be connected；The opposite side of detection cell 10 passes through pipeline and institute
Clear water reserviors 11 are stated to be connected；The clear water reserviors 11 are provided with clear water reserviors outlet pipe 111.
Above content is to combine specific preferred embodiment further detailed description of the utility model, it is impossible to
Assert that specific implementation of the present utility model is confined to these explanations.For the ordinary skill of the utility model art
For personnel, without departing from the concept of the premise utility, some simple deduction or replace can also be made, should all be regarded
To belong to the scope of patent protection that the utility model is determined by the claims submitted.
Claims (5)
1. a kind of garbage penetrating fluid processing system, including the first filtering ponds (1), sedimentation basin (2), pH value regulating reservoir (3), biochemistry pool
(4), anaerobic pond (5), denitrification pond (6), nitrification tank (7), the second filtering ponds (8), sludge concentration tank (9), detection cell (10), clear
Pond (11), it is characterised in that：First filtering ponds (1) side is connected by pipeline with the sedimentation basin (2)；The precipitation
Pond (2) opposite side is connected by pipeline with the pH value regulating reservoir (3)；PH value regulating reservoir (3) opposite side by pipeline with
The biochemistry pool (4) is connected；Biochemistry pool (4) opposite side is connected by pipeline with the anaerobic pond (5)；The anaerobic pond
(5) opposite side is connected by pipeline with the denitrification pond (6)；Denitrification pond (6) opposite side passes through pipeline and the nitre
Change pond (7) to be connected；Nitrification tank (7) opposite side is connected by pipeline with second filtering ponds (8)；Second filtering ponds
(8) opposite side is connected by pipeline with the sludge concentration tank (9)；Sludge concentration tank (9) opposite side passes through pipeline and institute
Detection cell (10) is stated to be connected；Detection cell (10) opposite side is connected by pipeline with the clear water reserviors (11).
2. garbage penetrating fluid processing system according to claim 1, it is characterised in that：Set on first filtering ponds (1)
There is the first filtering ponds water inlet pipe (1-1), be provided with aperture plate in first filtering ponds (1), the grid gap length of the aperture plate is
0.01-1cm。
3. garbage penetrating fluid processing system according to claim 1, it is characterised in that：It is provided with and divides in the sedimentation basin (2)
From filter plate, temperature device is provided with the sedimentation basin (2), the temperature device maintains temperature at 22-30 DEG C.
4. garbage penetrating fluid processing system according to claim 1, it is characterised in that：The biochemistry pool (4) is provided with biochemistry
Pond air inlet pipe (41), aeration tube (42), observation panel (43), the biochemistry pool air inlet pipe (41) are located on the biochemistry pool (4), institute
State aeration tube (42) and be located at the biochemistry pool (4) bottom, the observation panel (43) is located at the top of the biochemistry pool (4).
5. garbage penetrating fluid processing system according to claim 1, it is characterised in that：The clear water reserviors (11) are provided with clear
Pond outlet pipe (111).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621445844.8U CN207210188U (en) | 2016-12-27 | 2016-12-27 | A kind of garbage penetrating fluid processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621445844.8U CN207210188U (en) | 2016-12-27 | 2016-12-27 | A kind of garbage penetrating fluid processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207210188U true CN207210188U (en) | 2018-04-10 |
Family
ID=61810105
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621445844.8U Expired - Fee Related CN207210188U (en) | 2016-12-27 | 2016-12-27 | A kind of garbage penetrating fluid processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207210188U (en) |
-
2016
- 2016-12-27 CN CN201621445844.8U patent/CN207210188U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180410 Termination date: 20191227 |