CN207362015U - A kind of garbage percolation liquid treating system - Google Patents
A kind of garbage percolation liquid treating system Download PDFInfo
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- CN207362015U CN207362015U CN201721373152.1U CN201721373152U CN207362015U CN 207362015 U CN207362015 U CN 207362015U CN 201721373152 U CN201721373152 U CN 201721373152U CN 207362015 U CN207362015 U CN 207362015U
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- pipeline
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- 239000007788 liquid Substances 0.000 title claims abstract description 35
- 238000005325 percolation Methods 0.000 title claims abstract description 23
- 239000010802 sludge Substances 0.000 claims abstract description 91
- 239000010865 sewage Substances 0.000 claims abstract description 57
- 230000001105 regulatory effect Effects 0.000 claims abstract description 38
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000001556 precipitation Methods 0.000 claims abstract description 18
- 230000001112 coagulating effect Effects 0.000 claims abstract description 16
- 238000005189 flocculation Methods 0.000 claims abstract description 12
- 230000016615 flocculation Effects 0.000 claims abstract description 12
- 239000000320 mechanical mixture Substances 0.000 claims abstract description 12
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 9
- 230000001954 sterilising effect Effects 0.000 claims abstract description 8
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 2
- 238000004062 sedimentation Methods 0.000 claims 1
- 238000012545 processing Methods 0.000 description 16
- 239000000149 chemical water pollutant Substances 0.000 description 8
- 230000009471 action Effects 0.000 description 7
- 238000012958 reprocessing Methods 0.000 description 6
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000003900 soil pollution Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- -1 Afterwards Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
Abstract
It the utility model is related to a kind of garbage percolation liquid treating system, including grid, the first regulating reservoir, stripping tower, the second regulating reservoir, ABR ponds, SBR ponds, liquid storage tank, solution pool, paddle board formula mechanical mixture pond, perpendicular axis type machinery flocculation basin, vertical-flow coagulative precipitation tank, sludge concentration tank, activated carbon adsorber, sterilization pool, the first sewage pump, centrifugal fan, air blower, water sprayer, the first sludge lifting pump, the second sludge lifting pump, the 3rd sludge lifting pump, the 4th sludge lifting pump, the second sewage pump, the first dosing tank and the second dosing tank；The utility model flow is easy and effective, substantially increases sewage treating efficiency.
Description
Technical field
It the utility model is related to a kind of garbage percolation liquid treating system.
Background technology
Rubbish during stacking and landfill due to the biochemical degradation such as be compacted, ferment, while in precipitation and ground
A kind of liquid of the organic or inorganic composition of high concentration is generated under the seepage effect of lower water, we term it landfill leachate,
Also it is Leachate site.
CODcr, BOD5 concentration peak are compared with municipal sewage up to thousands of to tens of thousands of in landfill leachate, and concentration is high
Much, so percolate cannot be directly discharged into municipal sewage treatment pipeline without stringent processing, disposal, conventional
Garbage percolation liquid treating system flow is complicated, and sludge and sewage can not be distinguished effectively, so that wastewater treatment efficiency is not good enough, it is dirty
Mud can not be rapidly and thoroughly back in corresponding processing pond so that the circulation reprocessing of sludge is less efficient, finally have impact on
The disposal ability of landfill leachate, needs further improvement.
Utility model content
In view of the above-mentioned state of the art, the technical problem to be solved by the utility model is to provide a kind of letter of flow
Single effectively sludge and sewage can completely be distinguished and separate processing, substantially increase sewage treating efficiency, and sludge can be quick thorough
Bottom is back in corresponding processing pond, improves the garbage percolation liquid treating system of the circulation reprocessing efficiency of sludge.
Technical solution is used by the utility model solves above-mentioned technical problem：A kind of garbage percolation liquid treating system,
It is mixed including grid, the first regulating reservoir, stripping tower, the second regulating reservoir, ABR ponds, SBR ponds, liquid storage tank, solution pool, paddle board formula machinery
Close pond, perpendicular axis type machinery flocculation basin, vertical-flow coagulative precipitation tank, sludge concentration tank, activated carbon adsorber, sterilization pool, first
Sewage pump, centrifugal fan, air blower, water sprayer, the first sludge lifting pump, the second sludge lifting pump, the 3rd sludge carry
Rise pump, the 4th sludge lifting pump, the second sewage pump, the first dosing tank and the second dosing tank, it is characterised in that the grid
It is connected by pipeline with the first regulating reservoir, first regulating reservoir is connected by pipeline with the first sewage pump, described
First sewage pump is connected by pipeline with stripping tower, and the bottom of the stripping tower is connected by pipeline with the second regulating reservoir
Connect, second regulating reservoir is connected by pipeline with ABR ponds, and the ABR ponds are connected by pipeline with SBR ponds, the SBR
Pond is connected by pipeline with paddle board formula mechanical mixture pond, and the paddle board formula mechanical mixture pond passes through pipeline and perpendicular axis type machinery
Flocculation basin is connected, and the perpendicular axis type machinery flocculation basin is connected by pipeline with vertical-flow coagulative precipitation tank, the perpendicular stream
Formula coagulative precipitation tank is connected by pipeline with the second sewage pump, and second sewage pump passes through pipeline and activated carbon
Adsorption tower is connected, and the bottom of the activated carbon adsorber is connected by pipeline with sterilization pool.
Preferably, the bottom of the stripping tower is also associated with centrifugal fan.
Preferably, the side in the SBR ponds is also associated with air blower.
Preferably, the bottom of second regulating reservoir is also associated with the second dosing tank.
Preferably, the bottom of first regulating reservoir is also associated with the first dosing tank.
Preferably, the side lower end in the ABR ponds is connected by pipeline with the 4th sludge lifting pump, the 4th sludge
Elevator pump is connected by pipeline with sludge concentration tank, and the side upper end of the sludge concentration tank passes through pipeline and the first regulating reservoir
It is connected.
Preferably, the bottom in the ABR ponds is connected by pipeline with the 3rd sludge lifting pump, the 3rd sludge lifting
Pump is connected by pipeline with sludge concentration tank.
Preferably, the side lower end in the SBR ponds is connected by pipeline with the first sludge lifting pump, first sludge
Elevator pump is connected by pipeline with sludge concentration tank.
Preferably, the side upper end of the vertical-flow coagulative precipitation tank is connected by pipeline with sludge concentration tank.
Preferably, the side upper end in the SBR ponds is connected by pipeline with water sprayer, and the water sprayer is located at paddle board formula
The upstream side in mechanical mixture pond, the water sprayer are also connected by pipeline with solution pool, and the solution pool passes through pipeline and storage
Liquid pool is connected.
Compared with prior art, the utility model has the advantage of：Rubbish is during stacking and landfill due to being compacted, sending out
The biochemical degradations such as ferment, while a kind of organic or nothing of high concentration is generated under the seepage effect of precipitation and underground water
The liquid of machine composition, we term it landfill leachate, is also Leachate site, CODcr, BOD5 concentration peak in landfill leachate
It is reachable thousands of to tens of thousands of, compared with municipal sewage, concentration is much higher, so percolate is not without stringent processing, disposal
Can be directly discharged into municipal sewage treatment pipeline, conventional garbage percolation liquid treating system flow is complicated, sludge and sewage without
Method is effectively distinguished, so that wastewater treatment efficiency is not good enough, sludge can not be rapidly and thoroughly back in corresponding processing pond, made
It is less efficient to obtain the circulation reprocessing of sludge, finally have impact on the disposal ability of garbage percolation liquid treating system；The utility model
Flow is easy and effective, and sludge and sewage can completely be distinguished and separate processing, substantially increase sewage treating efficiency, and sludge energy
Rapidly and thoroughly it is back in corresponding processing pond, improves the circulation reprocessing efficiency of sludge, ensure that at landfill leachate
The disposal ability of reason system, prevents from causing soil pollution.
Brief description of the drawings
Fig. 1 is the structure flow chart of the utility model.
Embodiment
As shown in Figure 1, a kind of garbage percolation liquid treating system, including grid 1, the first regulating reservoir 2, stripping tower 3, second are adjusted
Save pond 4, ABR ponds 5, SBR ponds 6, liquid storage tank 7, solution pool 8, paddle board formula mechanical mixture pond 9, perpendicular axis type machinery flocculation basin 10, perpendicular
Streaming coagulative precipitation tank 11, sludge concentration tank 12, activated carbon adsorber 13, sterilization pool 14, the first sewage pump 15, centrifugation are logical
Wind turbine 16, air blower 17, water sprayer 18, the first sludge lifting pump 19, the second sludge lifting pump 20, the 3rd sludge lifting pump 21,
4th sludge lifting pump 22, the second sewage pump 23, the first dosing tank 24 and the second dosing tank 25；Grid 1 by pipeline with
First regulating reservoir 2 is connected, and the first regulating reservoir 2 is connected by pipeline with the first sewage pump 15, the first sewage pump
15 are connected by pipeline with stripping tower 3, and the bottom of stripping tower 3 is connected by pipeline with the second regulating reservoir 4, the second regulating reservoir
4 are connected by pipeline with ABR ponds 5, and ABR ponds 5 are connected by pipeline with SBR ponds 6, and SBR ponds 6 pass through pipeline and paddle plated
Tool mixing pit 9 is connected, and paddle board formula mechanical mixture pond 9 is connected by pipeline with perpendicular axis type machinery flocculation basin 10, vertical axis
Formula machinery flocculation basin 10 is connected by pipeline with vertical-flow coagulative precipitation tank 11, vertical-flow coagulative precipitation tank 11 by pipeline with
Second sewage pump 23 is connected, and the second sewage pump 23 is connected by pipeline with activated carbon adsorber 13, activated carbon
The bottom of adsorption tower 13 is connected by pipeline with sterilization pool 14；The bottom of stripping tower 3 is also associated with centrifugal fan 16；SBR
The side in pond 6 is also associated with air blower 17；The bottom of second regulating reservoir 4 is also associated with the second dosing tank 25；First regulating reservoir 2
Bottom is also associated with the first dosing tank 24；The side lower end in ABR ponds 5 is connected by pipeline with the 4th sludge lifting pump 22, the
Four sludge lifting pumps 22 are connected by pipeline with sludge concentration tank 12, and the side upper end of sludge concentration tank 12 passes through pipeline and
One regulating reservoir 2 is connected；The bottom in ABR ponds 5 is connected by pipeline with the 3rd sludge lifting pump 21, the 3rd sludge lifting pump 21
It is connected by pipeline with sludge concentration tank 12；The side lower end in SBR ponds 6 is connected by pipeline with the first sludge lifting pump 19
Connect, the first sludge lifting pump 19 is connected by pipeline with sludge concentration tank 12；The side upper end of vertical-flow coagulative precipitation tank 11
It is connected by pipeline with sludge concentration tank 12, the side upper end in SBR ponds 6 is connected by pipeline with water sprayer 18, water sprayer
18 are located at the upstream side in paddle board formula mechanical mixture pond 9, and water sprayer 18 is also connected by pipeline with solution pool 8, and solution pool 8 passes through
Pipeline is connected with liquid storage tank 7；During processing, sewage is entered in the first regulating reservoir 2 after the preliminary filtering of grid 1, at this time,
Medicament is added in the first regulating reservoir 2 by the first dosing tank 24, and sewage reacts with medicament, with except insoluble matter in decontaminated water,
Afterwards, sewage enters the upper end of stripping tower 3 under the action of the first sewage pump 15 and successively oozes down, centrifugal fan 16
Air is blown into stripping tower 3 from the bottom up, so that the ammonia that sewage produces in stripping tower 3 be arranged from the top of stripping tower 3
Go out and collect, the sewage after processing is flowed into the second regulating reservoir 4 from 3 bottom of stripping tower；Second dosing tank 25 adds medicament
In the second regulating reservoir 4, sewage is further removed insoluble matter in the second regulating reservoir 4, on the second regulating reservoir 4
In ABR ponds 5 are flowed into, the organic substrate in sewage is gone the sewage of layer by being contacted with the microorganism in ABR ponds 5
Remove, the biogas produced in processing procedure is discharged and is collected from 5 bottom of ABR ponds, and the biosolids in sewage are by effectively
It is trapped in ABR ponds 5 and forms sludge, the sludge under retaining is discharged under the action of the 4th sludge lifting pump 22 from 5 bottom of ABR ponds
Into sludge concentration tank 12, sludge concentration tank 12 will be input in the first regulating reservoir 2 again after sludge condensation；Similarly, under retaining
Sludge is still drained into sludge concentration tank 12 under the action of the 3rd sludge lifting pump 21 from 5 bottom of ABR ponds, sludge concentration tank
12 will be input in the first regulating reservoir 2 again after sludge condensation, and so allowing for sludge can rapidly and thoroughly discharge, and prevent from accumulating
It is more；Then, sewage is flowed into SBR ponds 6 from ABR ponds 5, meanwhile, air is blown into sewage by air blower 17 from the bottom up so that
Aerobic microbiological in sewage fully reacts, so as to carry out effective denitrification dephosphorization function to sewage.The dirt of the bottom in SBR ponds 6
Mud is discharged in sludge concentration tank 12 under the action of the first sludge lifting pump 19, and sludge concentration tank 12 will input again after sludge condensation
Into the first regulating reservoir 2；By the sewage in SBR ponds 6 under the action of water sprayer 18 with solution phase in liquid storage tank 7 and solution pool 8
Mix and be flowed into paddle board formula mechanical mixture pond 9, in paddle board formula mechanical mixture pond 9, sewage and liquid storage tank 7 and solution pool 8
In solution be further sufficiently mixed and be flowed into perpendicular axis type machinery flocculation basin 10, sewage is in perpendicular axis type machinery flocculation basin
10 are layered and are precipitated, and sewage is continuously introduced in vertical-flow coagulative precipitation tank 11 and is further precipitated and be layered, and are erected
The sludge of 11 bottom of streaming coagulative precipitation tank is drained into sludge concentration tank 12 under the action of the second sludge lifting pump 20, sludge
Concentration basin 12 will be input in the first regulating reservoir 2 again after sludge condensation；By the sewage of vertical-flow coagulative precipitation tank 11 second
The top of activated carbon adsorber 13 is entered under the action of sewage pump 23 and is adsorbed layer by layer from top to bottom, the dirt after absorption
Water is flowed out into sterilization pool 14 from the bottom of activated carbon adsorber 13, and sterilization pool 14 can be arranged after carrying out disinfection to sewage
Go out to outside, so as to complete the processing of percolate.
Rubbish during stacking and landfill due to the biochemical degradation such as be compacted, ferment, while in precipitation and ground
A kind of liquid of the organic or inorganic composition of high concentration is generated under the seepage effect of lower water, we term it landfill leachate,
Also it is Leachate site, CODcr, BOD5 concentration peak are compared, concentration with municipal sewage up to thousands of to tens of thousands of in landfill leachate
It is much higher, so percolate cannot be directly discharged into municipal sewage treatment pipeline without stringent processing, disposal, in the past
Garbage percolation liquid treating system flow it is complicated, sludge and sewage can not be distinguished effectively so that wastewater treatment efficiency is not good enough,
Sludge can not be rapidly and thoroughly back in corresponding processing pond so that the circulation reprocessing of sludge is less efficient, final to influence
The disposal ability of garbage percolation liquid treating system；The utility model flow is easy and effective, and sludge and sewage can be distinguished completely
And processing is separated, sewage treating efficiency is substantially increased, and sludge can be rapidly and thoroughly back in corresponding processing pond, improved
The circulation reprocessing efficiency of sludge, ensure that the disposal ability of garbage percolation liquid treating system, prevents from causing soil pollution.
Finally it should be noted that：Above example is only to illustrate the technical solution of the utility model, rather than its limitations；
Although the utility model is described in detail with reference to the foregoing embodiments, it will be understood by those of skill in the art that its according to
It can so modify to the technical solution described in foregoing embodiments, or which part technical characteristic is replaced on an equal basis
Change；And these modifications or replacement, the essence of appropriate technical solution is departed from various embodiments of the utility model technical solution
Spirit and scope.
Claims (10)
1. a kind of garbage percolation liquid treating system, including grid, the first regulating reservoir, stripping tower, the second regulating reservoir, ABR ponds, SBR
Pond, liquid storage tank, solution pool, paddle board formula mechanical mixture pond, perpendicular axis type machinery flocculation basin, vertical-flow coagulative precipitation tank, sludge are dense
Contracting pond, activated carbon adsorber, sterilization pool, the first sewage pump, centrifugal fan, air blower, water sprayer, the first sludge lifting
Pump, the second sludge lifting pump, the 3rd sludge lifting pump, the 4th sludge lifting pump, the second sewage pump, the first dosing tank and
Two dosing tanks, it is characterised in that the grid is connected by pipeline with the first regulating reservoir, and first regulating reservoir passes through pipeline
It is connected with the first sewage pump, first sewage pump is connected by pipeline with stripping tower, the stripping tower
Bottom is connected by pipeline with the second regulating reservoir, and second regulating reservoir is connected by pipeline with ABR ponds, the ABR ponds
It is connected by pipeline with SBR ponds, the SBR ponds are connected by pipeline with paddle board formula mechanical mixture pond, the paddle plated
Tool mixing pit is connected by pipeline with perpendicular axis type machinery flocculation basin, and the perpendicular axis type machinery flocculation basin is by pipeline with erecting
Streaming coagulative precipitation tank is connected, and the vertical-flow coagulative precipitation tank is connected by pipeline with the second sewage pump, described
Second sewage pump is connected by pipeline with activated carbon adsorber, and the bottom of the activated carbon adsorber is by pipeline with disappearing
Malicious pond is connected.
2. a kind of garbage percolation liquid treating system according to claim 1, it is characterised in that the bottom of the stripping tower is also
It is connected with centrifugal fan.
3. a kind of garbage percolation liquid treating system according to claim 1, it is characterised in that the side in the SBR ponds is also
It is connected with air blower.
A kind of 4. garbage percolation liquid treating system according to claim 1, it is characterised in that the bottom of second regulating reservoir
Portion is also associated with the second dosing tank.
A kind of 5. garbage percolation liquid treating system according to claim 1, it is characterised in that the bottom of first regulating reservoir
Portion is also associated with the first dosing tank.
6. a kind of garbage percolation liquid treating system according to claim 1, it is characterised in that under the side in the ABR ponds
End is connected by pipeline with the 4th sludge lifting pump, and the 4th sludge lifting pump is connected by pipeline with sludge concentration tank
Connect, the side upper end of the sludge concentration tank is connected by pipeline with the first regulating reservoir.
7. a kind of garbage percolation liquid treating system according to claim 1, it is characterised in that the bottom in the ABR ponds leads to
Piping is connected with the 3rd sludge lifting pump, and the 3rd sludge lifting pump is connected by pipeline with sludge concentration tank.
8. a kind of garbage percolation liquid treating system according to claim 1, it is characterised in that under the side in the SBR ponds
End is connected by pipeline with the first sludge lifting pump, and first sludge lifting pump is connected by pipeline with sludge concentration tank
Connect.
A kind of 9. garbage percolation liquid treating system according to claim 1, it is characterised in that the vertical-flow coagulating sedimentation
The side upper end in pond is connected by pipeline with sludge concentration tank.
10. a kind of garbage percolation liquid treating system according to claim 1, it is characterised in that on the side in the SBR ponds
End is connected by pipeline with water sprayer, and the water sprayer is located at the upstream side in paddle board formula mechanical mixture pond, and the water sprayer is also
It is connected by pipeline with solution pool, the solution pool is connected by pipeline with liquid storage tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721373152.1U CN207362015U (en) | 2017-10-24 | 2017-10-24 | A kind of garbage percolation liquid treating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721373152.1U CN207362015U (en) | 2017-10-24 | 2017-10-24 | A kind of garbage percolation liquid treating system |
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| Publication Number | Publication Date |
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| CN207362015U true CN207362015U (en) | 2018-05-15 |
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| CN201721373152.1U Expired - Fee Related CN207362015U (en) | 2017-10-24 | 2017-10-24 | A kind of garbage percolation liquid treating system |
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| Country | Link |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109179918A (en) * | 2018-11-19 | 2019-01-11 | 中朗德水务环境科技有限公司 | A kind of biochemical processing method for refuse landfill landfill leachate |
-
2017
- 2017-10-24 CN CN201721373152.1U patent/CN207362015U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109179918A (en) * | 2018-11-19 | 2019-01-11 | 中朗德水务环境科技有限公司 | A kind of biochemical processing method for refuse landfill landfill leachate |
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| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180515 |
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| CF01 | Termination of patent right due to non-payment of annual fee |