CN207973654U - A kind of initial stage garbage percolation liquid treating system - Google Patents
A kind of initial stage garbage percolation liquid treating system Download PDFInfo
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- CN207973654U CN207973654U CN201820997875.7U CN201820997875U CN207973654U CN 207973654 U CN207973654 U CN 207973654U CN 201820997875 U CN201820997875 U CN 201820997875U CN 207973654 U CN207973654 U CN 207973654U
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- 239000007788 liquid Substances 0.000 title claims abstract description 23
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 23
- 238000005325 percolation Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 230000000694 effects Effects 0.000 claims abstract description 12
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 claims abstract description 10
- 230000001105 regulatory effect Effects 0.000 claims abstract description 9
- 239000012528 membrane Substances 0.000 claims description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 9
- 239000003344 environmental pollutant Substances 0.000 claims description 6
- 244000005700 microbiome Species 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 231100000719 pollutant Toxicity 0.000 claims description 6
- 230000002550 fecal effect Effects 0.000 claims description 5
- 239000002033 PVDF binder Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 230000001228 trophic effect Effects 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 238000011026 diafiltration Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- 239000000149 chemical water pollutant Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000001728 nano-filtration Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 238000006396 nitration reaction Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 230000003373 anti-fouling effect Effects 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000037452 priming Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
A kind of initial stage garbage percolation liquid treating system includes mainly regulating reservoir, UASB equipment, A/O biochemistry pools, MBR equipment, NF equipment, upstriker wetland, downstriker wetland, photovoltaic generating system, control system, this system is worked by control system, the initial stage garbage percolation liquid treating system have the characteristics that high treating effect, save money, it is processed after water can reuse, this system can not only reduce the waste of water resource, moreover it is possible to realize recycling for water resource.
Description
Technical field
The utility model is related to be a kind of, ammonia nitrogen concentration lower landfill yard initial stage preferable for wastewater biodegradability
Garbage percolation liquid treating system.
Background technology
With the development of social economy and the raising of Living consumption, city, the yield of rural garbage are growing day by day, rubbish
Rubbish disposition becomes modern metropolitan cities a great problem, no matter is handled using that mode, can all there is landfill leachate generation, initial stage rubbish
The landfill leachate complicated component that landfill yard generates contains multiple pollutant, and relatively low ammonia nitrogen concentration is a kind of organic waste of high concentration
Water.It such as deals with improperly, environment will be caused seriously to pollute.The more biochemical process of method of processing landfill leachate, embrane method etc. at present,
But the water after it is processed cannot obtain preferable reuse.Again because of China's shortage of water resources, therefore it is treatment effect to study a kind of
It is good, save money but can the system of reuse be vital.
Utility model content
The technical problem to be solved by the present invention is to provide a kind of i.e. high treating effect, save money and can reuse
Initial stage garbage percolation liquid treating system.
Technical solution adopted by the utility model to solve its technical problems is：Initial stage garbage percolation liquid treating system, this
System is mainly including power supply system, the regulating reservoir for landfill leachate being adjusted water and water quality, the filter for obtaining filtering
Go out that liquid carries out the UASB equipment of Anaerobic Treatment, the percolate for successively obtaining UASB equipment anaerobism carries out biochemistry organics removal and
The A/O biochemistry pools of ammonia nitrogen and total nitrogen and by the percolate of biochemical treatment carry out oxygenolysis and solid-state separation MBR equipment,
And it is further filtered by the NF equipment for the percolate progress pollutant removal that oxygenolysis and solid-state detach, finally by percolate
Remove the upstriker wetland and downstriker wetland of pollutant, the regulating reservoir, UASB equipment, A/O biochemistry pools, MBR equipment, NF
Equipment, upstriker wetland, downstriker wetland are sequentially connected.
The NF equipment is connected with fecal suction truck, and the concentrate of NF equipment processing gained is back to fecal suction truck.
The MBR equipment includes membrane module and bioreactor.
The membrane module is PVDF materials.
The A/O biochemistry pools are connected with trophic system, for improving the activity of microorganism in biochemical treatment.
The A/O biochemistry pools and MBR equipment is respectively connected with air blower, and the air blower is for divulging information and supplying oxygen.
The NF equipment includes chemicals dosing plant, cartridge filter, high-pressure pump, NF membrane.
Advantageous effect：The initial stage garbage percolation liquid treating system have high treating effect, save money, it is processed after water
Can reuse the characteristics of, this system can not only reduce the waste of water resource, moreover it is possible to realize recycling for water resource.
Description of the drawings
Fig. 1 is initial stage garbage percolation liquid treating system flow chart.
Specific implementation mode
It is proposed a kind of high treating effect in conjunction with attached drawing this patent, save money but can reuse initial stage landfill leachate treatment
System.
This system mainly include regulating reservoir, UASB equipment, A/O biochemistry pools, MBR equipment, NF equipment, upstriker wetland, under
Line wetland, photovoltaic generating system, control system, this system are worked by control system.
The landfill leachate at initial stage is entered regulating reservoir, regulating pondage by newly-built refuse landfill by catheter collection gravity flow
It is promoted in UASB equipment processing systems by elevator pump with after water quality, since the COD and SS of initial stage landfill leachate are higher,
Therefore it can effectively be degraded most organic matter and SS by Anaerobic Treatment, reduce follow-up nitrification, denitrification and MBR equipment
Energy consumption.The organic nitrogen of part is converted into inorganic nitrogen in anaerobic processes, and corresponding NH3-N concentration will increase, but due to subsequently adopting
Ammonia nitrogen can be converted into nitrogen removal using the method for biology completely with nitration denitrification technique.The water outlet of UASB equipment flows into certainly
Enter nitration denitrification pond, biochemical organics removal and ammonia nitrogen and total nitrogen；Enter MBR equipment system through nitrifying biochemical treatment water outlet gravity flow
System, membrane bioreactor（MBR）It is mainly made of membrane module and bioreactor two parts, a large amount of microorganism（Activated sludge）
It is come into full contact with matrix in bioreactor, by oxygenolysis progress metabolism to maintain own growth, breeding,
Make organic pollutant degradation simultaneously.Membrane module carries out solid-liquid by the effects that mechanical grading, retention to waste water and mud mixed liquid
Separation, macromolecular substances etc. return to bioreactor after being concentrated, so as to avoid the loss of microorganism.Membrane module is equivalent to biography
The secondary settling tank for technique of uniting, but overcome many disadvantages of traditional secondary settling tank.The water outlet of MBR equipment is pumped into water tank by self priming pump, then
Enter NF equipment i.e. nanofiltration system through booster pump, most COD, BOD, NH3-N, TN, SS, a huge sum of money are removed by nanofiltration system
Belong to, the pollutants such as Escherichia coli and coloration, the concentrate of nanofiltration system is transported to landfill area landfill by fecal suction truck, is discharged from flowing into
In line and downstriker wetland, wetland selects five layers of complex media, and it is 90cm to lay height, by the further mistake of PKA wetlands
The pollutants such as remaining organic matter, nitrogen, phosphorus, pathogen in water removal are filtered off, final outflow water is made to rinse, flush the toilet or irrigate as road
Deng use.The form that all power supply system electricity consumptions are all made of photovoltaic generation wherein in whole system and city is electrically coupled eliminates partially
Remote area is difficult to the obstacle being powered.
A/O biochemistry pools and MBR equipment described in this system are respectively connected with air blower, the effect of air blower：First, to life
Change aerobic bacteria and increase oxygen, ensures their living environments, reach the needs of sewage disposal；Second is that ventilation, since sewage disposal is more
Number all uses biochemical reaction, will produce some biogas and other decomposition gases, and the smell is awful simultaneously with certain danger,
In order to ensure safety and improve environment, site environment is aerated.
This system to initial stage landfill leachate in biochemical treatment, by adding the nutrient solution in trophic system in biochemistry pool
Activity to improve microorganism is improved to the removal rate of COD, ammonia nitrogen, COD, ammonia nitrogen removal rate be 80-90% or so, water outlet is full
Sufficient film process inflow requirement.The form of MBR equipment includes a variety of configurations such as immersion, flat, and membrane module uses PVDF materials,
Microbial cells are detached by efficient MBR membrane modules from water outlet, it is ensured that are more than 0.02 μm of particulate matter, microorganism and and COD
Relevant suspended matter is safely trapped in system, and sludge concentration is maintained by the continuous recycle stream of aeration of cross-current type.MBR
Device program stops after running 10-20min after starting with certain flow supply purging pocket, and self-priming pump operation is after 2-3 minutes
Stopping restarts again, continuous circular flow.Nanofiltration system includes chemicals dosing plant, cartridge filter, high-pressure pump, NF membrane etc.,
Using the principle of modularized design Automatic Control, system, by the switching of different valves, starts " anti-after running a period of time
The program of flushing-gas flushing-flushing-operation ", the not outer row of system concentrated water in normal operation, only opens " backwash-in system
There is partial concentration waste water to be back to regulating reservoir when gas flushing-just flushing " program to be handled again, NF membrane has higher through speed
Degree, desalting performance is strong, mechanical strength is good, the high feature of antifouling property.The side that PKA wetlands are combined using upstriker and downstriker
Formula, it is overpunching water distribution that medium, which uses five layers of complex media, pipe arrangement, and the operation logic that underpunch is catchmented goes out nanofiltration
Water is further filtered, wherein to the removal rate 80-90% of COD, ammonia nitrogen.
The initial stage garbage percolation liquid treating system have high treating effect, save money, it is processed after water can reuse
Feature, this system can not only reduce the waste of water resource, moreover it is possible to realize recycling for water resource.
Claims (8)
1. a kind of initial stage garbage percolation liquid treating system, it is characterised in that：This system includes mainly power supply system, to garbage filter
Liquid is adjusted the regulating reservoir of water and water quality, the filter liquor of filtering acquisition is carried out to the UASB equipment of Anaerobic Treatment, successively
The percolate that UASB equipment anaerobism is obtained carry out biochemical organics removal and ammonia nitrogen and total nitrogen A/O biochemistry pools and will be biochemical
The diafiltration that processed percolate carries out the MBR equipment of oxygenolysis and solid-state separation and detaches oxygenolysis and solid-state
Liquid carries out the NF equipment of pollutant removal, percolate is finally further filtered off to the upstriker wetland and downstriker of depollution object
Wetland, the regulating reservoir, UASB equipment, A/O biochemistry pools, MBR equipment, NF equipment, upstriker wetland, downstriker wetland are successively
Connection.
2. a kind of initial stage garbage percolation liquid treating system according to claim 1, it is characterised in that：The NF equipment connects
It is connected to fecal suction truck, the concentrate of NF equipment processing gained is back to fecal suction truck.
3. a kind of initial stage garbage percolation liquid treating system according to claim 1, it is characterised in that：The MBR equipment
Including membrane module and bioreactor.
4. a kind of initial stage garbage percolation liquid treating system according to claim 3, it is characterised in that：The membrane module is
PVDF materials.
5. a kind of initial stage garbage percolation liquid treating system according to claim 1, it is characterised in that：The A/O is biochemical
Pond is connected with trophic system, for improving the activity of microorganism in biochemical treatment.
6. a kind of initial stage garbage percolation liquid treating system according to claim 1, it is characterised in that：The A/O is biochemical
Pond and MBR equipment are respectively connected with air blower, and the air blower is for divulging information and supplying oxygen.
7. a kind of initial stage garbage percolation liquid treating system according to claim 1, it is characterised in that：The NF equipment packets
Include chemicals dosing plant, cartridge filter, high-pressure pump, NF membrane.
8. a kind of initial stage garbage percolation liquid treating system according to claim 1, it is characterised in that：The power supply system
The form that electricity consumption is all made of photovoltaic generation and city is electrically coupled.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201820997875.7U CN207973654U (en) | 2018-06-27 | 2018-06-27 | A kind of initial stage garbage percolation liquid treating system |
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| CN201820997875.7U CN207973654U (en) | 2018-06-27 | 2018-06-27 | A kind of initial stage garbage percolation liquid treating system |
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| CN207973654U true CN207973654U (en) | 2018-10-16 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110772962A (en) * | 2019-11-29 | 2020-02-11 | 北京京城环保股份有限公司 | Method for denitration of waste incineration flue gas by ammonia in waste leachate |
-
2018
- 2018-06-27 CN CN201820997875.7U patent/CN207973654U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110772962A (en) * | 2019-11-29 | 2020-02-11 | 北京京城环保股份有限公司 | Method for denitration of waste incineration flue gas by ammonia in waste leachate |
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