CN206645978U - A kind of garbage-compressing liquid processing device - Google Patents
A kind of garbage-compressing liquid processing device Download PDFInfo
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- CN206645978U CN206645978U CN201720407765.6U CN201720407765U CN206645978U CN 206645978 U CN206645978 U CN 206645978U CN 201720407765 U CN201720407765 U CN 201720407765U CN 206645978 U CN206645978 U CN 206645978U
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Abstract
It the utility model is related to environmental protection technical field; disclose a kind of garbage-compressing liquid processing device, including be sequentially connected by pipeline or irrigation canals and ditches and be provided with the collecting-tank of inlet and liquid outlet, the first coagulative precipitation tank, pH regulating reservoirs, anaerobic reactor, integrated bioreactor and the second coagulative precipitation tank.Garbage-compressing liquid processing device in the utility model handles garbage-compressing liquid using materializing strategy by the way of biochemical treatment is combined, most of suspended solid in garbage-compressing liquid is removed by the way of flocculation sediment first, reduce the content of the suspended solid and organic pollution in garbage-compressing liquid, reduce the load that organic matter is handled in subsequent reactions, reduce hydraulic detention time, reduce floor space, the medicament usage amount also significantly reduced simultaneously, so as to realize the cost-effective processing of garbage-compressing liquid in limited space.
Description
Technical field
Environmental protection technical field is the utility model is related to, more particularly to a kind of garbage-compressing liquid processing device.
Background technology
With being continuously increased for urban population, domestic waste is also being continuously increased, and generally at rubbish end processing away from
City farther out, at this moment needs to establish transporting compressed garbage and turned, rubbish is compressed, and reduces the volume of rubbish in order to transport.
And house refuse water content is larger, large amount of sewage can be produced in compression process, that is, forms garbage-compressing liquid.Garbage-compressing liquid belongs to
High concentrated organic wastewater, CODcr is up to 30000~50000mg/L, and BOD in waste water5It is relatively low, belong to difficult for biological degradation
Organic wastewater.Existing garbage-compressing liquid is directly directly handled using physico-chemical process and biochemical process more.Directly using physico-chemical process to rubbish
Rubbish compression liquid is handled, and reagent consumption amount certainly will be caused big, and power consumption cost is high, therefore causes overall operation cost high；Directly
Garbage-compressing liquid is handled using biochemical process, because pollutant concentration is high, then processing system needs the hydraulic retention grown very much
Time, system footprint area is caused to increase, and garbage compression transfer station is normally at downtown area, land used is at full stretch, leads
The technology is caused to be difficult to apply.
Utility model content
The purpose of this utility model is to provide a kind of garbage-compressing liquid processing device, to solve existing for above-mentioned prior art
Problem, while floor space is controlled, reagent cost is effectively controlled, the economy of garbage-compressing liquid is realized in limited space
Effective processing.
To achieve the above object, the utility model provides following scheme：
The utility model provides a kind of garbage-compressing liquid processing device, including be sequentially connected by pipeline or irrigation canals and ditches and it is equal
Collecting-tank, the first coagulative precipitation tank, pH regulating reservoirs, anaerobic reactor, the integral biological for being provided with inlet and liquid outlet are anti-
Answer device and the second coagulative precipitation tank.
Preferably, it is provided with grid at the inlet of the collecting-tank.
Preferably, heat cycles water tank, institute are connected with by pipeline between the pH regulating reservoirs and the anaerobic reactor
State and be provided with circulating-heating portion inside heat cycles water tank, the heat cycles water tank is provided with the inlet of heat cycles water tank first
With heat cycles water tank liquid outlet, the liquid outlet of the pH regulating reservoirs and the inlet of heat cycles water tank first pass through pipeline
Connection, the heat cycles water tank liquid outlet are connected with the inlet of the anaerobic reactor by pipeline, the anaerobic reaction
Device is provided with the liquid outlet of anaerobic reactor first, the liquid outlet of anaerobic reactor first and the integrated bioreactor
Inlet is connected by pipeline.
Preferably, the heat cycles water tank is provided with the inlet of heat cycles water tank second, on the anaerobic reactor
Provided with the liquid outlet of anaerobic reactor second, the liquid outlet of anaerobic reactor second and the inlet of heat cycles water tank second
Connected by pipeline.
Preferably, the garbage-compressing liquid processing device also includes biogas container, the air inlet of the biogas container and institute
The exhaust outlet for stating anaerobic reactor is connected by pipeline.
Preferably, the garbage-compressing liquid processing device also includes circulating hot water feedway, the circulating hot water supply
Device includes biogas hot-water boiler and hot water circuit water tank, the combustion of the exhaust outlet of the biogas container and the biogas hot-water boiler
Air chamber connects；The hot water circuit water tank includes cold water portion and hot water portion, and the hot water portion is provided with hot water inlet and hot water goes out
Mouthful, the cold water portion is provided with cooling water inlet and cooling water outlet, the delivery port of the hot water inlet and the biogas hot-water boiler
It is connected, the hot water outlet connects with the water inlet in the circulating-heating portion, the cooling water inlet and the circulating-heating portion
Delivery port is connected, and the cooling water outlet is connected with the water inlet of the biogas hot-water boiler.
Preferably, the bottom of pond of first coagulative precipitation tank and second coagulative precipitation tank is equipped with sewage draining exit, described
Sewage draining exit is connected by pipeline with a sludge storage pool, is equipped with the pipeline that each sewage draining exit is connected with the sludge storage pool
One sludge pump, the sludge storage pool bottom are connected with a sludge dewatering equipment by pipeline.
Preferably, the leakage fluid dram of the sludge dewatering equipment is connected with a header tank, the header tank by pipeline with it is described
The water inlet connection of collecting-tank, the pipeline that the header tank is connected with the collecting-tank are provided with elevator pump.
Preferably, garbage-compressing liquid processing device also includes odor removal, and the air inlet of the odor removal is connected with one
House steward, the collecting-tank, first coagulative precipitation tank, the pH regulating reservoirs, the integrated bioreactor and described
Gas skirt is equipped with the top of two coagulative precipitation tanks, steam vent is equipped with the gas skirt, is all connected with each steam vent
There is a branch pipe, each branch pipe is connected with the house steward, and the house steward is provided with blower fan.
Preferably, the anaerobic reactor is EGSB reactors, the integrated A/O reactions of integrated bioreactor
Device.
The utility model achieves following technique effect relative to prior art：
Garbage-compressing liquid processing device in the utility model place by the way of biochemical treatment is combined using materializing strategy
Garbage-compressing liquid is managed, materializing strategy mode chooses flocculation reaction, and biochemical treatment mode is mutually tied using anaerobic reaction with aerobic reaction
The biochemical processing process of conjunction.Most of suspended solid in garbage-compressing liquid is removed by the way of flocculation sediment first, simultaneously
The organic pollution carried in suspended solid can be also removed in the lump, reduce the content of the suspended solid in garbage-compressing liquid, and
Most organic pollution is effectively cut down, meets requirement of the follow-up Anaerobic Treatment to suspended solid, reduces and locates in subsequent reactions
The load of organic matter is managed, while improves the treatment effeciency of subsequent reactions, improves the biodegradability of waste water, is reduced needed for subsequent reactions
Hydraulic detention time, reduce floor space, while also significantly reduce the medicine in the whole processing procedure of garbage-compressing liquid
Agent usage amount, so as to realize the cost-effective processing of garbage-compressing liquid in limited space.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
In the required accompanying drawing used be briefly described, it should be apparent that, drawings in the following description are only of the present utility model
Some embodiments, for those of ordinary skill in the art, without having to pay creative labor, can also basis
These accompanying drawings obtain other accompanying drawings.
Fig. 1 is the structural representation of the utility model garbage-compressing liquid processing device；
In figure：1- collecting-tanks, the coagulative precipitation tanks of 2- first, 3-pH regulating reservoirs, 4- heat cycles water tank, 5- hot water circuit water
Case, 6- biogas hot-water boiler, 7- biogas container, 8- anaerobic reactors, 9- integrated bioreactors, the coagulating sedimentation of 10- second
Pond, 11- odor removals, 12- blower fans, 13- sludge dewatering equipments, 14- header tanks, 15- sludge storage pools, 16- grids, 17- circulations add
Hot portion, the first inlet of 18- heat cycles water tank, 19- heat cycles water tanks liquid outlet, 20- anaerobic reactors inlet, 21-
The liquid outlet of anaerobic reactor first, the second inlet of 22- heat cycles water tank, the liquid outlet of 23- anaerobic reactors second, 24- heat
Water inlet, 25- hot water outlets, 26- cooling water inlets, 27- cooling water outlets.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
The purpose of this utility model is to provide a kind of garbage-compressing liquid processing device, to solve existing for above-mentioned prior art
Problem, while floor space is controlled, reagent cost is effectively controlled, the economy of garbage-compressing liquid is realized in limited space
Effective processing.
To enable above-mentioned purpose of the present utility model, feature and advantage more obvious understandable, below in conjunction with the accompanying drawings and tool
Body embodiment is described in further detail to the utility model.
Embodiment one
The present embodiment provides a kind of garbage-compressing liquid processing device, as shown in figure 1, including passing through pipeline or irrigation canals and ditches phase successively
Collecting-tank 1 even, the first coagulative precipitation tank 2, pH regulating reservoirs 3, anaerobic reactor 8, the coagulation of integrated bioreactor 9 and second
Sedimentation basin 10, above-mentioned each reaction tank are provided with inlet and liquid outlet, have filled anaerobic sludge in anaerobic reactor 8, and one
Active sludge is filled in body bioreactor 9.
Garbage-compressing liquid processing device in the present embodiment is handled using materializing strategy by the way of biochemical treatment is combined
Garbage-compressing liquid, materializing strategy mode are chosen in the first coagulative precipitation tank 2 and the second coagulative precipitation tank 10 and carry out flocculation reaction,
Biochemical treatment mode uses the biochemical processing process that anaerobic reaction is combined with aerobic reaction.First by the way of flocculation sediment
Most of suspended solid in garbage-compressing liquid is removed, while the organic pollution carried in suspended solid can also be gone in the lump
Remove, reduce the content of the suspended solid in garbage-compressing liquid, and effectively cut down most organic pollution, meet follow-up anaerobism
The requirement to suspended solid is handled, reduces the load that organic matter is handled in subsequent reactions, while improves the processing effect of subsequent reactions
Rate, the biodegradability of waste water is improved, reduce the water conservancy residence time needed for subsequent reactions, reduce floor space, while also have
The medicament usage amount in the whole processing procedure of garbage-compressing liquid is reduced to effect, so as to realize garbage-compressing in limited space
The cost-effective processing of liquid.
During using the present apparatus, garbage-compressing liquid is emitted into collecting-tank 1 and is collected, the garbage-compressing liquid of collection is passed through
To the first coagulative precipitation tank 2, and flocculant is added into garbage-compressing liquid, the suspended solid for making to float on a liquid is gathered into
Group, form precipitation and be separated from water, so as to remove the most suspended solid in garbage-compressing liquid, while carried in suspended solid
Organic pollution can also be removed in the lump.Because garbage-compressing liquid is in acidity, pH value is relatively low, in order to which the anaerobism for ensureing follow-up is anti-
It should be preferably added to aerobic reaction normal operation, it is necessary to the pH value of liquid in pH regulating reservoirs 3 is adjusted into neutrality in the present embodiment
NaOH solution, the water outlet pH for making pH regulating reservoirs 3 are 6~9.PH value is regulated, garbage-compressing liquid continues to be passed through to anaerobic reactor 8
In, garbage-compressing liquid carries out metabolic response by anaerobic bacteria under anaerobic environment to pollutant, and most organic pollution reacts at last
Generate methane, CO2And water, so as to remove most organic pollution.Treatment sewage is passed through to integrated bioreactor 9
In after, can further remove the organic matter in sewage, NH3- N, TP (total phosphorus) etc., and the equipment of integrated bioreactor 9
Compact, floor space is small, the second coagulative precipitation tank 10 is connected after integrated bioreactor 9, to integrated bioreactor 9
Water outlet carries out flocculation reaction again, further reduces the content of suspended solid and organic matter, it is ensured that water outlet reaches discharge standard.
Grid 16 is preferably provided with the inlet of collecting-tank 1, can be to entering the rubbish pressure in collecting-tank 1 by grid 16
Contracting liquid is tentatively filtered, and removes the bulk rubbish etc. in garbage-compressing liquid.
Heat cycles water tank 4, heat cycles water are preferably connected with by pipeline between pH regulating reservoirs 3 and anaerobic reactor 8
The inside of case 4 is provided with circulating-heating portion 17, and heat cycles water tank 4 is provided with the first inlet of heat cycles water tank 18 and heat cycles
Water tank liquid outlet 19, the liquid outlet of pH regulating reservoirs 3 and the first inlet of heat cycles water tank 18 of heat cycles water tank 4 pass through pipe
Road is connected, and heat cycles water tank liquid outlet 19 is connected with anaerobic reactor inlet 20 by pipeline, and heat cycles water tank goes out
The pipeline that liquid mouth 19 is connected with anaerobic reactor inlet 20 is provided with circulating pump, and anaerobic reactor 8 is provided with anaerobic reactor
First liquid outlet 21, the first liquid outlet of anaerobic reactor 21 are connected with the inlet of integrated bioreactor 9 by pipeline.
Heat cycles water tank 4 can be previously heated to necessarily to the garbage-compressing liquid that enter in anaerobic reactor 8
Temperature, garbage-compressing liquid is heated to 30~35 DEG C using heat cycles water tank 4 in the present embodiment, to ensure anaerobic reactor 8
In garbage-compressing liquid reaction temperature, so as to improve anaerobic reaction speed.
Heat cycles water tank 4 is provided with the second inlet of heat cycles water tank 22, and anaerobic reactor 8 is provided with anaerobic reaction
The second liquid outlet of device 23, the second liquid outlet of anaerobic reactor 23 are connected with the second inlet of heat cycles water tank 22 by pipeline.
The present embodiment is also insufficient to the pending garbage-compressing liquid in anaerobic reactor 8 and reaction using heat cycles water tank 4
Sewage carries out circulating-heating, is further ensured that the liquid in anaerobic reactor 8 is within the scope of stable temperature, maintains higher
Reaction rate, the treatment sewage that anaerobic reaction is finished, which continues to be passed through to integrated bioreactor 9, carries out subsequent reactions.
Garbage-compressing liquid processing device of the present utility model also preferably sets biogas container 7, the air inlet of biogas container 7
It is connected with the exhaust outlet of anaerobic reactor 8 by pipeline.The biogas container 7 that the present embodiment is set can be to producing in anaerobic reaction 8
Raw biogas is collected, and carries out secondary use, improves product utilization rate.
Garbage-compressing liquid processing device of the present utility model also preferably sets circulating hot water feedway, and circulating hot water supplies
Include biogas hot-water boiler 6 and hot water circuit water tank 5, the exhaust outlet of biogas container 7 and the combustion gas of biogas hot-water boiler 6 to device
Room connects；Hot water circuit water tank 5 includes cold water portion and hot water portion, and hot water portion is provided with hot water inlet 24 and hot water outlet 25, cold
Water portion is provided with cooling water inlet 26 and cooling water outlet 27, and hot water inlet 24 is connected with the delivery port of biogas hot-water boiler 6, and hot water goes out
Mouth 25 is connected with the water inlet in circulating-heating portion 17, and cooling water inlet 26 is connected with the delivery port in circulating-heating portion 17, cooling water outlet
27 are connected with the water inlet of biogas hot-water boiler 6.Cooling water inlet 26 and the delivery port of circulating-heating portion 17 are connected in the present embodiment
Pipeline and connection cooling water outlet 27 utilize anaerobic reactor 8 with being equipped with water pump on the pipeline of the water inlet of biogas hot-water boiler 6
Biogas caused by middle reaction provides the energy for the heat transfer medium in circulating-heating portion 17, heat cycles water tank 4 in the present embodiment
Heat transfer medium in circulating-heating portion 17 is water, and hot water circuit water tank 5 provides heat for the circulating-heating portion 17 of heat cycles water tank 4
Water, and cooling water circulating-heating portion 17 heated after garbage-compressing liquid is passed through to biogas hot-water boiler 6 and re-starts heating；Natural pond
Biogas in gas container 7, which is passed through into the fuel chamber of biogas hot-water boiler 6, to be burnt, and heat energy is produced, to from circulating-heating
The cooling water in portion 17 is heated.
The bottom of pond of first coagulative precipitation tank 2 and the second coagulative precipitation tank 10 is equipped with sewage draining exit, and sewage draining exit passes through pipeline
It is connected with a sludge storage pool 15, a sludge pump, sludge storage pool 15 is equipped with the pipeline that each sewage draining exit is connected with sludge storage pool 15
Bottom is connected with a sludge dewatering equipment 13 by pipeline.Rubbish pressure in first coagulative precipitation tank 2 and the second coagulative precipitation tank 10
The sediment that suspended solid in contracting liquid is gathered into is discharged into sludge storage pool 15 by sludge pump, and sludge storage pool 15 will be collected into
Suspended solid sediment, which is discharged into sludge dewatering equipment 13, carries out dewater treatment, and the sludge obtained after dehydration is transported to garbage loading embeading
Field landfill.
The leakage fluid dram of sludge dewatering equipment 13 is connected with a header tank 14, the water inlet that header tank 14 passes through pipeline and collecting-tank 1
Mouthful connection, the pipeline that header tank 14 is connected with collecting-tank 1 are provided with elevator pump, caused dirt in the dehydration of sludge dewatering equipment 13
Water continues to be passed through to collecting-tank 1 by elevator pump carries out further purified treatment.
Garbage-compressing liquid processing device of the present utility model also preferably sets odor removal 11, the air inlet of odor removal 11
Mouth is connected with a house steward, collecting-tank 1, the first coagulative precipitation tank 2, pH regulating reservoirs 3, the coagulation of integrated bioreactor 9 and second
The top of sedimentation basin 10 is equipped with gas skirt, and steam vent is equipped with gas skirt, is respectively connected with a branch pipe on each steam vent, each
House steward Guan Junyu connects, and house steward is provided with blower fan 12.Due to collecting-tank 1, the first coagulative precipitation tank 2, pH regulating reservoirs 3, integration
The coagulative precipitation tank 10 of bioreactor 9 and second can produce foul smell during garbage-compressing liquid is handled, foul smell it is main into
It is divided into H2S and NH3, being directly discharged into air to pollute, the present embodiment set odor removal 11 can be to garbage-compressing liquid at
Caused gas carries out deodorizing process during reason, removes in gas and includes H2S and NH3Foul smell, the gas after processing discharges again
Into air, the pollution of environment is avoided, the deodorization mode of odor removal 11 can select chemical washing deodorization or biological deodorizing.
The anaerobic reactor 8 of the present embodiment is preferably EGSB reactors, i.e. CGSB, and EGSB reacts
Device processing load is high, and floor space is small, and power consumption is low, and has biogas generation, caused biogas can be used for into biogas heat simultaneously
Homogeneous solution-type reactor 6 heats the treatment sewage in anaerobic reactor 8 after burning, improve the temperature of anaerobic reaction, further improve anaerobism
The efficiency of reaction.Integrated bioreactor 9 is preferably integrated A/O reactors, using the A/O (anoxics/good of activated sludge
Oxygen) reaction process, anoxic and aerobic and mud-water separation are formed into integrated equipment for wastewater treatment, remove CODcr, NH in waste water3-
N, TP etc., make facility compact, and floor space reduces.
Apply specific case in the utility model to be set forth principle of the present utility model and embodiment, the above
The explanation of embodiment is only intended to help and understands method and its core concept of the present utility model；Meanwhile for the one of this area
As technical staff, according to thought of the present utility model, there will be changes in specific embodiments and applications.To sum up
Described, this specification content should not be construed as to limitation of the present utility model.
Claims (10)
- A kind of 1. garbage-compressing liquid processing device, it is characterised in that：Including being sequentially connected by pipeline or irrigation canals and ditches and be respectively provided with There are collecting-tank, the first coagulative precipitation tank, pH regulating reservoirs, anaerobic reactor, the integrated bioreactor of inlet and liquid outlet With the second coagulative precipitation tank.
- 2. garbage-compressing liquid processing device according to claim 1, it is characterised in that：Set at the inlet of the collecting-tank It is equipped with grid.
- 3. garbage-compressing liquid processing device according to claim 1, it is characterised in that：The pH regulating reservoirs and the anaerobism Heat cycles water tank is connected with by pipeline between reactor, circulating-heating portion is provided with inside the heat cycles water tank, it is described Heat cycles water tank is provided with the inlet of heat cycles water tank first and heat cycles water tank liquid outlet, the pH regulating reservoirs go out Liquid mouth is connected with the inlet of heat cycles water tank first by pipeline, the heat cycles water tank liquid outlet and the anaerobism The inlet of reactor is connected by pipeline, and the anaerobic reactor is provided with the liquid outlet of anaerobic reactor first, the anaerobism The liquid outlet of reactor first is connected with the inlet of the integrated bioreactor by pipeline.
- 4. garbage-compressing liquid processing device according to claim 3, it is characterised in that：The heat cycles water tank is provided with The inlet of heat cycles water tank second, the anaerobic reactor are provided with the liquid outlet of anaerobic reactor second, the anaerobic reaction The liquid outlet of device second is connected with the inlet of heat cycles water tank second by pipeline.
- 5. garbage-compressing liquid processing device according to claim 4, it is characterised in that：The garbage-compressing liquid processing device Also include biogas container, the air inlet of the biogas container is connected with the exhaust outlet of the anaerobic reactor by pipeline.
- 6. garbage-compressing liquid processing device according to claim 5, it is characterised in that：The garbage-compressing liquid processing device Also include circulating hot water feedway, the circulating hot water feedway includes biogas hot-water boiler and hot water circuit water tank, institute The exhaust outlet for stating biogas container is connected with the fuel chamber of the biogas hot-water boiler；The hot water circuit water tank include cold water portion and Hot water portion, the hot water portion are provided with hot water inlet and hot water outlet, and the cold water portion is provided with cooling water inlet and cooling water outlet, The hot water inlet is connected with the delivery port of the biogas hot-water boiler, the water inlet in the hot water outlet and the circulating-heating portion Mouth connection, the cooling water inlet are connected with the delivery port in the circulating-heating portion, the cooling water outlet and the biogas water bath The water inlet connection of stove.
- 7. garbage-compressing liquid processing device according to claim 1, it is characterised in that：First coagulative precipitation tank and institute The bottom of pond for stating the second coagulative precipitation tank is equipped with sewage draining exit, and the sewage draining exit is connected by pipeline with a sludge storage pool, each institute State and a sludge pump is equipped with the pipeline that sewage draining exit is connected with the sludge storage pool, the sludge storage pool bottom is connected by pipeline There is a sludge dewatering equipment.
- 8. garbage-compressing liquid processing device according to claim 7, it is characterised in that：The leakage fluid dram of the sludge dewatering equipment A header tank is connected with, the header tank is connected by pipeline with the water inlet of the collecting-tank, the header tank and the collection The pipeline of pond connection is provided with elevator pump.
- 9. garbage-compressing liquid processing device according to claim 1, it is characterised in that：Garbage-compressing liquid processing device also wraps Odor removal is included, the air inlet of the odor removal is connected with a house steward, the collecting-tank, first coagulative precipitation tank, institute State and be equipped with gas skirt, the collection at the top of pH regulating reservoirs, the integrated bioreactor and second coagulative precipitation tank Steam vent is equipped with gas hood, a branch pipe is respectively connected with each steam vent, each branch pipe is connected with the house steward, institute State house steward and be provided with blower fan.
- 10. garbage-compressing liquid processing device according to claim 1, it is characterised in that：The anaerobic reactor is EGSB Reactor, the integrated A/O reactors of integrated bioreactor.
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| CN201720407765.6U CN206645978U (en) | 2017-04-18 | 2017-04-18 | A kind of garbage-compressing liquid processing device |
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| CN201720407765.6U CN206645978U (en) | 2017-04-18 | 2017-04-18 | A kind of garbage-compressing liquid processing device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109942151A (en) * | 2019-03-29 | 2019-06-28 | 崔潇月 | A method of effectively removing ammonia in landfill leachate |
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2017
- 2017-04-18 CN CN201720407765.6U patent/CN206645978U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109942151A (en) * | 2019-03-29 | 2019-06-28 | 崔潇月 | A method of effectively removing ammonia in landfill leachate |
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