CN110028210A - A kind of technique suitable for UASB processing landfill leachate - Google Patents
A kind of technique suitable for UASB processing landfill leachate Download PDFInfo
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- CN110028210A CN110028210A CN201910463228.7A CN201910463228A CN110028210A CN 110028210 A CN110028210 A CN 110028210A CN 201910463228 A CN201910463228 A CN 201910463228A CN 110028210 A CN110028210 A CN 110028210A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/06—Contaminated groundwater or leachate
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/06—Controlling or monitoring parameters in water treatment pH
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/302—Nitrification and denitrification treatment
- C02F3/307—Nitrification and denitrification treatment characterised by direct conversion of nitrite to molecular nitrogen, e.g. by using the Anammox process
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Abstract
The invention discloses a kind of techniques suitable for UASB processing landfill leachate, specific embodiment is as follows: the landfill leachate that garbage loading embeading area generates is collected through collection conduit, then enter leachate equalization basin after grid separating solid impurities, conditioning tank water outlet flows into hydrolysis acidification pool, and hydrolysis acidification pool water outlet enters sieve pond and handled；The water outlet of sieve pond is promoted to UASB anaerobic reactor with pump, percolate enters two-stage A/O biochemical reaction tank after UASB anaerobic reactor Anaerobic Treatment, the percolate of biochemical treatment by elevator pump be lifted into ultrafiltration system, nanofiltration system and reverse osmosis membrane system handle reach discharge standard after reuse or discharge.Heating system is set when the present invention is in UASB anaerobic reactor, can be realized and heated automatically during anaerobic reaction, without heating to dosing chamber, saves cost.
Description
Technical field
The invention belongs to landfill leachate treatment fields, are related to a kind of technique suitable for UASB processing landfill leachate.
Background technique
Major way of the municipal solid waste sanitary landfill as house refuse final disposal, percolate treatment facility are
One of main indicator of domestic garbage was harmlessly treated, percolate whether up to standard is the emphasis examined.Consumer waste infiltration liquid is total
Body has high organic high-concentration ammonia-nitrogen, high chroma, high conductivity, salt content height, carbon-nitrogen ratio imbalance, difficult for biological degradation, pollution danger
The features such as evil is big, processing difficulty are high.
Due to the growth with the garbage loading embeading time, percolate will appear aging phenomenon, COD, BOD concentration in percolate
Decline, ammonia-nitrogen content raising, carbon, nitrogen are reduced than imbalance, biodegradability, are caused traditional biochemical treatment system that can not operate, are made
It is greatly reduced with the methane phase efficiency of UASB anaerobic reactor processing percolate, a series of problems, such as ammonia nitrogen removal effect is poor produces
It is raw, while grid+conditioning tank+hydrolysis acidification pool+pond dosing chamber+UASB anaerobic reactor+MBR+A/O is used in existing technology
+ disc tube reverse osmosis (dt-ro) film (DTRO)+disinfection process flow carries out the processing of percolate, needs to carry out water temperature tune in dosing chamber
Section increases operating cost；And since UASB reactor effluent quality index is still higher, it cannot directly enter MBR system, film
Bioreactor (MBR system) water inlet preferably meets COD and is less than the limit values such as 50mg/l less than 500mg/l, ammonia nitrogen, directly passes through MBR
The service life for reducing MBR system is be easy to cause after system processing, which is difficult to later refuse landfill diafiltration in 5 years
NH_3-N treating in liquid is up to standard；Biochemistry pool water outlet simultaneously is directly entered disc tube reverse osmosis (dt-ro) membranous system, makes disc tube reverse osmosis (dt-ro) film
System operating load is higher, Yi Fasheng fouling membrane, increases operating cost.
Summary of the invention
The purpose of the present invention is to provide a kind of techniques suitable for UASB processing landfill leachate, in UASB anaerobic reaction
Heating system is set when in device, can be realized and heated automatically during anaerobic reaction, heated without dosing chamber, is saved
Save cost, while in UASB anaerobic reactor treated sewage by Two-Stage Biochemical reaction tank removal organic matter and denitrogenation,
Cancel MBR technique in anaerobic reactor subsequent treatment process, also leachate quality can be made to reach subsequent using Two-Stage Biochemical system
Processing requirement, and the film cost and operating cost of MBR membrane processing method are all higher, investment and operation can be reduced by cancelling MBR technique
Cost.Water outlet flows into qualified discharge after ultrafiltration system, nanofiltration system and reverse osmosis membrane treatment system classification are handled after biochemical treatment,
Because the molecular size range of ultrafiltration, nanofiltration and reverse osmosis treatment successively decreases step by step, subsequent processing load can reduce using classification processing,
Extend the operation time limit of each membranous system, reduces operating cost.
The purpose of the present invention can be achieved through the following technical solutions:
A kind of technique suitable for UASB processing landfill leachate, specific embodiment are as follows:
The first step, the landfill leachate that garbage loading embeading area generates are collected through collection conduit, then seep the rubbish after collection
Filtrate enters leachate equalization basin after the stainless steel fine fack separating solid impurities that conditioning tank entrance is arranged, and percolate exists
Homogeneous average is obtained in conditioning tank, guarantees system stability；
Second step, conditioning tank water outlet flow into hydrolysis acidification pool, and the hydrolysis acidification bacterium in hydrolysis acidification pool can be by long-chain high score
Sub- polymer hydrolysis acidification be the stronger small organic molecule alcohol of biodegradability or acid, can also be by partially not biochemical or biochemical
Weaker heterocycle type organic breaks ring and is degraded into biochemical organic molecule, improves dirty organic pollutants BOD5/CODCrValue,
Improve the biochemical of entire sewage；
Treated in second step percolate is entered sieve pond from hydrolysis acidification pool water outlet, examined in sieve pond by third step
PH value after surveying hydrolysis acidification, since refuse landfill diafiltration PH index in China's is generally in 6.51-8.25, after hydrolysis acidification
PH value can be down to 5.2, adjust pH value to 6.8-7.2 using sodium carbonate, and be allowed to meet methane phase in anaerobic reactor is suitable for
Condition；
Sieve pond water outlet pump in third step is promoted to UASB anaerobic reactor, the UASB anaerobic reactor by the 4th step
Bottom is equipped with heating system, and water distributor is placed in heating system, and the sewage after heating flows into pond body, passes through anaerobism ammonia oxygen in pond
Changing large amount of organic and generation in reaction directly removal sewage has the biogas for recycling and being worth, can after the collecting methane of generation
For the heating system of UASB anaerobic reactor bottom, operating cost is saved；
5th step, percolate enter two-stage A/O biochemical reaction tank after UASB anaerobic reactor Anaerobic Treatment, and percolate exists
Organic matter and denitrogenation are sufficiently removed in biochemistry pool, anaerobic reactor water outlet flows into level-one anoxic pond, after Aerobic biological process
Sewage, the ammonia nitrogen of wherein most is oxidized into nitrite (NO by nitration reaction2 -- N), nitrate (NO3 -- N),
Aerobic tank effluent recycling a part is to anoxic pond, in anaerobic condition, denitrifying bacterium using the nitrogen in nitrate as electron acceptor,
Nitrogen in nitrate is reduced into nitrogen (N by oxidation of organic compounds2), organic matter becomes carbon dioxide (CO2), to complete sewage
Remove organic matter and denitrification process；The sludge of the generation in biochemical reaction tank is discharged into sludge concentration tank simultaneously, de- by sludge
Water dispenser, which is handled, is down to 60% solid matter below to moisture content and is sent into refuse landfill landfill, supernatant be pumped into conditioning tank into
Row circular treatment；After garbage loading embeading field time was up to 5 years or more, ammonia-nitrogen content is increased, and content of organics reduces, and level-one is good
Oxygen pond effluent recycling a part makes to sieve pond into NO in the sewage of UASB anaerobic reactor2 --N/NH4 +- N close to 1.32,
The effective and thorough ammonia nitrogen for removing high ammonia-nitrogen wastewater can be had by sufficiently carrying out Anammox reaction；
6th step is lifted into ultrafiltration system by elevator pump by the percolate that the 5th step mesophytization is handled, in ultrafiltration
A kind of pressure activated film is utilized in system, colloid, particle and molecular weight phase in trap water under extraneous motive force (pressure) effect
To higher substance, and water and relatively small particles of solute penetrate UF membrane；It can be retained point by the screening of the micropore of film surface
The substance that son amount is 3x10000-1x10000, and it is greater than particle, the macromolecular of fenestra etc. since sieving actoion is trapped, thus
Most of colloidal silicon is removed, while can remove a large amount of organic matter etc.；
7th step, ultrafiltration system water outlet enter nanofiltration system, wherein nanofiltration (NF) between ultrafiltration and it is reverse osmosis between, section
Stay molecular weight in the range of 80-1000, aperture is several nanometers；
8th step, enters reverse osmosis membrane (RO) system after nanofiltration system, and the processing by RO system reaches discharge mark
Reuse or discharge after standard driven by pressure, will be in solution by means of the selective retention effect of semi-permeable membrane in counter-infiltration system
Solute is separated with solvent, and reverse osmosis film used is semi-permeable membrane, its micropore is smaller, diameter about 2nm, (or can only be had by water
Solvent), the substance of salt and other dissolutions cannot be passed through.It therefore can be by the inorganic ions, thin in raw water with reverse osmosis technology
The removal of the impurity such as bacterium, virus, organic matter and colloid, makes sewage qualified discharge.
Beneficial effects of the present invention:
1, the present invention in UASB anaerobic reactor when heating system is set, can be realized during anaerobic reaction automatic
Heating, without heating to dosing chamber, saves cost.
2, the present invention cancels MBR technique after the processing of UASB anaerobic reactor, reduces investment and operating cost.It is directly over
Two-Stage Biochemical reaction tank removes organic matter and denitrogenation, also can reach subsequent processing requirement, final qualified discharge.
3, present invention water outlet after biochemical treatment flows into ultrafiltration system, nanofiltration system and reverse osmosis membrane treatment system, classification
Qualified discharge after processing.Because the molecular size range of ultrafiltration, nanofiltration and reverse osmosis treatment successively decreases step by step, can be subtracted using classification processing
Light subsequent processing load, extends the operation time limit of each membranous system, reduces operating cost.
4, the present invention will fill 5 years later percolate treating process parameter optimizations, by level-one aerobic tank effluent recycling one
Part to sieve pond makes into NO in the sewage of UASB anaerobic reactor2 --N/NH4 +- N meets Anammox close to 1.32
Optimum reaction condition, reaction equation NH4 ++NO2 -=N2+2H2O keeps the ammonia nitrogen removal of UASB anaerobic reactor high-efficient.It is raw
Change conversion zone removal organic matter and total nitrogen, then carry out ultrafiltration, nanofiltration and reverse osmosis membrane processing again, solves straight in the prior art
It connects biochemical reaction tank treated sewage through disc tube reverse osmosis (dt-ro) film process, keeps reverse osmosis membrane processing load higher, use
Service life short disadvantage.
Detailed description of the invention
In order to facilitate the understanding of those skilled in the art, the present invention will be further described below with reference to the drawings.
Fig. 1 is garbage leachate treatment process flow chart of the present invention.
Specific embodiment
A kind of technique suitable for UASB processing landfill leachate, as shown in Figure 1, specific embodiment is as follows:
The first step, the landfill leachate that garbage loading embeading area generates are collected through collection conduit, then seep the rubbish after collection
Filtrate enters leachate equalization basin after the stainless steel fine fack separating solid impurities that conditioning tank entrance is arranged, and percolate exists
Homogeneous average is obtained in conditioning tank, guarantees system stability；
Second step, conditioning tank water outlet flow into hydrolysis acidification pool, and the hydrolysis acidification bacterium in hydrolysis acidification pool can be by long-chain high score
Sub- polymer hydrolysis acidification be the stronger small organic molecule alcohol of biodegradability or acid, can also be by partially not biochemical or biochemical
Weaker heterocycle type organic breaks ring and is degraded into biochemical organic molecule, improves dirty organic pollutants BOD5/CODCrValue,
Improve the biochemical of entire sewage；
Treated in second step percolate is entered sieve pond from hydrolysis acidification pool water outlet, examined in sieve pond by third step
PH value after surveying hydrolysis acidification, since refuse landfill diafiltration PH index in China's is generally in 6.51-8.25, after hydrolysis acidification
PH value can be down to 5.2, adjust pH value to 6.8-7.2 using sodium carbonate, and be allowed to meet methane phase in anaerobic reactor is suitable for
Condition；
Sieve pond water outlet pump in third step is promoted to UASB anaerobic reactor, the UASB anaerobic reactor by the 4th step
Bottom is equipped with heating system, and water distributor is placed in heating system, and the sewage after heating flows into pond body, passes through anaerobism ammonia oxygen in pond
Changing large amount of organic and generation in reaction directly removal sewage has the biogas for recycling and being worth, can after the collecting methane of generation
For the heating system of UASB anaerobic reactor bottom, operating cost is saved；
5th step, percolate enter two-stage A/O biochemical reaction tank after UASB anaerobic reactor Anaerobic Treatment, and percolate exists
Organic matter and denitrogenation are sufficiently removed in biochemistry pool, anaerobic reactor water outlet flows into level-one anoxic pond, after Aerobic biological process
Sewage, the ammonia nitrogen of wherein most is oxidized into nitrite (NO by nitration reaction2 -- N), nitrate (NO3 -- N),
Aerobic tank effluent recycling a part is to anoxic pond, in anaerobic condition, denitrifying bacterium using the nitrogen in nitrate as electron acceptor,
Nitrogen in nitrate is reduced into nitrogen (N by oxidation of organic compounds2), organic matter becomes carbon dioxide (CO2), to complete sewage
Remove organic matter and denitrification process；The sludge of the generation in biochemical reaction tank is discharged into sludge concentration tank simultaneously, de- by sludge
Water dispenser, which is handled, is down to 60% solid matter below to moisture content and is sent into refuse landfill landfill, supernatant be pumped into conditioning tank into
Row circular treatment；After garbage loading embeading field time was up to 5 years or more, ammonia-nitrogen content is increased, and content of organics reduces, and level-one is good
Oxygen pond effluent recycling a part makes to sieve pond into NO in the sewage of UASB anaerobic reactor2 --N/NH4 +- N close to 1.32,
The effective and thorough ammonia nitrogen for removing high ammonia-nitrogen wastewater can be had by sufficiently carrying out Anammox reaction；
6th step is lifted into ultrafiltration system by elevator pump by the percolate that the 5th step mesophytization is handled, in ultrafiltration
A kind of pressure activated film is utilized in system, colloid, particle and molecular weight phase in trap water under extraneous motive force (pressure) effect
To higher substance, and water and relatively small particles of solute penetrate UF membrane；It can be retained point by the screening of the micropore of film surface
The substance that son amount is 3x10000-1x10000, and it is greater than particle, the macromolecular of fenestra etc. since sieving actoion is trapped, thus
Most of colloidal silicon is removed, while can remove a large amount of organic matter etc.；
7th step, ultrafiltration system water outlet enter nanofiltration system, wherein nanofiltration (NF) between ultrafiltration and it is reverse osmosis between, section
Stay molecular weight in the range of 80-1000, aperture is several nanometers；
8th step, enters reverse osmosis membrane (RO) system after nanofiltration system, and the processing by RO system reaches discharge mark
Reuse or discharge after standard driven by pressure, will be in solution by means of the selective retention effect of semi-permeable membrane in counter-infiltration system
Solute is separated with solvent, and reverse osmosis film used is semi-permeable membrane, its micropore is smaller, diameter about 2nm, (or can only be had by water
Solvent), the substance of salt and other dissolutions cannot be passed through.It therefore can be by the inorganic ions, thin in raw water with reverse osmosis technology
The removal of the impurity such as bacterium, virus, organic matter and colloid, makes sewage qualified discharge.
Present invention disclosed above preferred embodiment is only intended to help to illustrate the present invention.There is no detailed for preferred embodiment
All details are described, are not limited the invention to the specific embodiments described.Obviously, according to the content of this specification,
It can make many modifications and variations.These embodiments are chosen and specifically described to this specification, is in order to better explain the present invention
Principle and practical application, so that skilled artisan be enable to better understand and utilize the present invention.The present invention is only
It is limited by claims and its full scope and equivalent.
Claims (4)
1. a kind of technique suitable for UASB processing landfill leachate, which is characterized in that specific embodiment is as follows:
The first step, the landfill leachate that garbage loading embeading area generates is collected through collection conduit, then by the landfill leachate after collection
Enter leachate equalization basin after the stainless steel fine fack separating solid impurities of conditioning tank entrance setting, percolate is being adjusted
Homogeneous average is obtained in pond；
Second step, conditioning tank water outlet flow into hydrolysis acidification pool, and long chain macromolecule polymerize by the hydrolysis acidification bacterium in hydrolysis acidification pool
Object hydrolysis acidification is the stronger small organic molecule alcohol of biodegradability or acid, also can will be partially not biochemical or weaker biochemical miscellaneous
Ring type organic breaks ring and is degraded into biochemical organic molecule, improves dirty organic pollutants BOD5/CODCrValue；
Treated in second step percolate is entered sieve pond from hydrolysis acidification pool water outlet and handled by third step；
Sieve pond water outlet pump in third step is promoted to UASB anaerobic reactor, the UASB anaerobic reactor bottom by the 4th step
Equipped with heating system, water distributor is placed in heating system, and the sewage after heating flows into pond body, anti-by Anammox in pond
Large amount of organic in sewage should directly be removed and generate the biogas with recycling value, be used for after the collecting methane of generation
The heating system of UASB anaerobic reactor bottom；
5th step, percolate enter two-stage A/O biochemical reaction tank after UASB anaerobic reactor Anaerobic Treatment, and percolate is in biochemistry
Organic matter and denitrogenation are sufficiently removed in pond；
6th step is lifted into ultrafiltration system by elevator pump by the percolate that the 5th step mesophytization is handled, in ultrafiltration system
It is middle to utilize pressure activated film, colloid in trap water, particle and the relatively high substance of molecular weight under pressure, and water and phase
UF membrane is penetrated to lesser particles of solute；
7th step, ultrafiltration system water outlet enter nanofiltration system, and the particle to molecular weight in 80-1000 is filtered；
8th step, sewage enter reverse osmosis membrane system after nanofiltration system is handled, reach by the processing of reverse osmosis membrane system
Reuse or discharge after discharge standard.
2. a kind of technique suitable for UASB processing landfill leachate according to claim 1, which is characterized in that third step
In pH value after the real-time detection hydrolysis acidification of sieve pond, while adjusting pH value to 6.8-7.2 using sodium carbonate, be allowed to meet and detest
The suitable condition of methane phase in oxygen reactor.
3. a kind of technique suitable for UASB processing landfill leachate according to claim 1, which is characterized in that the 5th step
The sludge of generation in mesophytization reaction tank is discharged into sludge concentration tank, is handled by sludge dewatering equipment to moisture content and is down to 60%
Solid matter below is sent into refuse landfill landfill, and supernatant, which is pumped into conditioning tank, carries out circular treatment.
4. a kind of technique suitable for UASB processing landfill leachate according to claim 1, which is characterized in that the 5th step
In after garbage loading embeading field time was up to 5 years or more, ammonia-nitrogen content increases, and content of organics reduces, and level-one aerobic tank is discharged back
Stream a part makes the sewage into UASB anaerobic reactor sufficiently carry out Anammox reaction to sieve pond, can be effective
Thoroughly remove the ammonia nitrogen of high ammonia-nitrogen wastewater.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110482780A (en) * | 2019-07-19 | 2019-11-22 | 南宁师范大学 | It is a kind of based on micro- aerobic domestic waste transfer station Leachate site advanced treatment process |
| CN110577333A (en) * | 2019-09-26 | 2019-12-17 | 南昌首创环保能源有限公司 | Novel process for treating percolate |
| CN111689646A (en) * | 2020-06-03 | 2020-09-22 | 浦华环保有限公司 | Treatment process of leachate of waste incineration plant |
| CN113480084A (en) * | 2021-05-31 | 2021-10-08 | 国能朗新明环保科技有限公司 | Standard treatment method and system for high-ammonia-nitrogen and low-carbon-nitrogen ratio sludge drying liquid |
| CN113636715A (en) * | 2021-07-16 | 2021-11-12 | 国能龙源环保南京有限公司 | Integrated wastewater treatment system with front-end organic degradation |
| CN114702134A (en) * | 2022-04-02 | 2022-07-05 | 安徽世绿环保科技有限公司 | Multistage AO sewage treatment plant of segmentation water inflow |
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| CN110482780A (en) * | 2019-07-19 | 2019-11-22 | 南宁师范大学 | It is a kind of based on micro- aerobic domestic waste transfer station Leachate site advanced treatment process |
| CN110577333A (en) * | 2019-09-26 | 2019-12-17 | 南昌首创环保能源有限公司 | Novel process for treating percolate |
| CN111689646A (en) * | 2020-06-03 | 2020-09-22 | 浦华环保有限公司 | Treatment process of leachate of waste incineration plant |
| CN113480084A (en) * | 2021-05-31 | 2021-10-08 | 国能朗新明环保科技有限公司 | Standard treatment method and system for high-ammonia-nitrogen and low-carbon-nitrogen ratio sludge drying liquid |
| CN113636715A (en) * | 2021-07-16 | 2021-11-12 | 国能龙源环保南京有限公司 | Integrated wastewater treatment system with front-end organic degradation |
| CN114702134A (en) * | 2022-04-02 | 2022-07-05 | 安徽世绿环保科技有限公司 | Multistage AO sewage treatment plant of segmentation water inflow |
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