CN100509664C - Method for treating percolation liquid of water deficiency area garbage embedding field - Google Patents
Method for treating percolation liquid of water deficiency area garbage embedding field Download PDFInfo
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- CN100509664C CN100509664C CNB2007100555804A CN200710055580A CN100509664C CN 100509664 C CN100509664 C CN 100509664C CN B2007100555804 A CNB2007100555804 A CN B2007100555804A CN 200710055580 A CN200710055580 A CN 200710055580A CN 100509664 C CN100509664 C CN 100509664C
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
The invention discloses a disposing method of water deficiency area landfill waste site straining liquid belonging to high concentrate waste water disposing method, which comprises the following steps: installing balancing tank, ammonia blow-off, anaerobic treatment, aerobic treatment, materialized advanced treatment and recharge; possessing stronger placement, higher stability, lower capital expenditure and operating cost; realizing zero discharge of garbage straining liquid; controlling its pollution.
Description
Technical field
The present invention relates to a kind of treatment process of high-concentration sewage, specifically, adopt multi-stage biochemical to handle and recharge combination technique and carry out harmless treatment, can realize the zero release of percolate at the water-deficient area percolate from garbage filling field.
Background technology
Percolate is the high concentration organic sewage that rubbish produces in the landfill process, is mainly derived from the interior moisture of precipitation, organic matter degradation and rubbish itself.Be subjected to influence of various factors such as rubbish composition, quantity of precipitation, landfill yard structure, landfill time, the water yield of percolate changes greatly, water quality situation complexity.Have following characteristics:
(1) organic concentration height, the BOD in the percolate
5Reaching as high as several ten thousand mg/L with COD concentration, mainly is to produce in the acid fermentation stage, and pH reaches or a little less than 7, BOD
5With COD ratio be 0.5～0.6.
(2) heavy metal content height contains more than ten kind of metal ion in the percolate, wherein iron and zinc are higher in the acid fermentation stage, and the concentration of iron can reach about 2000mg/L, and zinc concentration can reach about 130mg/L.
(3) change of water quality is big, and the water quality of percolate depends on the make of landfill yard, the kind of rubbish, quality, quantity and the length at landfill age, and wherein the make of landfill yard is the main factor that influences percolate water quality.
(4) ammonia nitrogen concentration in the high percolate of nitrogen content increases along with the increase at garbage loading embeading age, can be up to about 2500mg/L.And when ammonia nitrogen concentration is too high, can influence microbic activity, reduce the effect of biological treatment.
(5) nutritive element is out of proportion, BOD in the general percolate
5/ P is mostly greater than 500, and the phosphoric rational proportion required with microorganism growth differs bigger.
(6) contain more hardly degraded organic substance.
Detect data presentation, contain 93 kinds of objectionable impuritiess in the percolate, 22 kinds of emphasis control lists that have been put into China and American National Environmental Protection Administration are wherein arranged, wherein a kind can be directly carcinogenic, 5 kinds can be brought out carcinogenic.Refuse landfill design, operation and management problem demanding prompt solution are effectively controlled and be treated as to percolate as a kind of concentration height, big, the difficult sewage of degrading of toxicity to it.
Domesticly according to investigations built refuse landfill and mostly adopt conventional sewage disposal technology to carry out percolate to handle poor effect.Therefore people constantly explore special treatment technology at percolate, and total development trend is the application of new and high technology in the water technology.As disclosing a kind of combination biological treatment in the CN1544356 patent document.The CN1478737A patent document discloses electrolytic oxidation+ceramic membrane biochemical treatment and separation+reverse-osmosis treated technology.Both at home and abroad to the achievement in research of refuse leachate treatment technology, mainly there is following several problem before making a general survey of:
(1) common process is difficult to adapt to high density, the difficult degradation characteristic of percolate, and treatment effect is difficult to guarantee;
(2) some COMBINED PROCESS route complexity, structures are more, and construction investment is big, the operational management difficulty;
(3) some special process equipment manufacturing cost height, operation energy consumption are big, and the processing cost height is applied difficulty;
In addition, China is vast in territory, and various places weather condition difference is big.The dry quantity of precipitation in the north and hinterland is little, and the generation of this area's percolate is lower.And do not specialize in and develop corresponding treatment technology as yet both at home and abroad at present at water-deficient area leachate quality, water yield characteristic expansion.
Summary of the invention
The invention provides the treatment process of a kind of suitable water-deficient area percolate from garbage filling field.To solve the problem that treatment effect is bad, method is complicated, cost is high that exists in the percolate from garbage filling field processing of water-deficient area.The technical scheme that the present invention takes is: comprise the following steps:
One, equalizing tank is set: the waterpower adjustment pond that hydraulic detention time reaches 10d～20d is set;
Two, ammonia stripping: adopt the higher ammonia nitrogen of content in the cyclic aeration ammonia stripping jar treating refuse percolate; The waterpower recycle ratio is 5～4:1, and gas-water ratio is 500～900:1, and the stripping time is 0.5～1h; The stripping jar adopts gas---streaming waterborne, and water inlet and aeration gas are by the tank body bottom packing layer of upwards flowing through; The tank body middle part is a packing layer, fills high mass transfer ceramics filling, particle diameter 4～6mm.
Three, anaerobic treatment: adopt secondary upflow type anaerobic sewage sludge reactor (UASB), two-stage anaerobic stage waterpower total residence time 48h～60h, the I and II residence time, temperature of reactor was controlled at 20～40 ℃ than being 1:1 or 2:3, and the pH value stabilization is 7～8;
Four, aerobic treatment: adopt secondary efficient mass transfer filler contact oxidation method;
Wherein one-level contact oxidation technology residence time 6h～10h is provided with the medium-soft fibrous packing, gas-water ratio 10～15:1; Two-stage biological contact oxidation technology residence time 5h～8h is provided with floating stuffing, gas-water ratio 20～25:1.
Five, materialization advanced treatment: comprise coagulation, precipitation and filtration;
Coagulation adopts the jump partition plate reaction tank, adopts polyaluminium salts or polymeric ferric salt flocculation agent; Depositing technology adopts inclined-plate clarifying basin; Filtration process is a conventional rapid filter, and double-layer filter material is common quartz sand and hard coal.
Six, sludge treatment: aerobic system excess sludge and sludge from sedimentation tank enter sludge treating system, adopt plate and frame(type)filter press, and Yu Shui is back to equalizing tank, and dewatered sludge landfill is gone into waste layer;
Seven, recharge: adopt recharge system, comprise the sterilization pre-treatment, recharge, recharge system comprises: the pond, recharge pump, water-transmission line, shower nozzle.
Sterilization pre-treatment: pass through disinfection by chlorine dioxide; Kill virus and bacterium in the percolate on the one hand, can effectively alleviate on the other hand because of the bacterium algae multiplies the shower nozzle that recharges that causes and stop up.
Recharge: the number of times of batching is 4～7 times/d, hydraulic load 12～20L/m
2D, the COD 60～80g/m that loads
2D.
It is a kind of effective treatment process that processing is sprayed in the circulation of percolate, is mainly reflected in two aspects.The one, decrement, the spray of returning of percolate can be by evaporating or being absorbed by vegetation, and the treatment capacity outside the venue of minimizing percolate reduces the investment that percolate is handled.The 2nd, quicken the stabilization process.By recharging the water ratio that can improve waste layer, increase the humidity of rubbish, strengthen microbic activity in the rubbish, quicken methanogenic speed and organic decomposition, shorten the stabilization process of landfill waste.By reflux cycle, the BOD of percolate
5Can drop to 30～350mg/L and 70～500mg/L respectively with COD.
In addition, can also improve water-deficient area garbage loading embeading layer water ratio, quicken organic decomposition in the rubbish, shorten the stabilization process of landfill waste, make the stabilization process of former need 15 years～20 years foreshorten to 2 years～3 years by recharging.
Adopt the mode treating refuse percolate of circulated backfilling need consider the climate hydrologic condition, factors such as the number of times of batching, hydraulic load and COD load.Generally need determine, and the amount of recharging should improve along with the process of waste layer stabilization according to the test of landfill yard practical situation.The present invention determines that by testing optimum condition is: the number of times of batching is 4～7 times/d, hydraulic load 12～20L/m
2D, the COD 60～80g/m that loads
2D.The degradation efficiency of COD and BOD is reached respectively about 70% and 75%, and the percolate decrement also can reach more than 70%
The present invention compares with existing technology, pointed stronger, the advantage such as stability is higher, initial cost and operation cost are lower of this method.Especially along with the continuity of working time, the percolate decrement effect of recirculation process is progressively brought into play, finally can realize the zero release of percolate, controls its pollution.
Description of drawings:
Accompanying drawing is a preferred implementation process flow sheet of the present invention.
Embodiment
Embodiment 1
One, equalizing tank is set: the waterpower adjustment pond that hydraulic detention time reaches 10d is set.
Its effect is to regulate the water quality and the water yield that changes violent percolate, alleviates the impact to subsequent treatment process.Also can play preliminary settlement action except that alleviating, regulating the impact load, further protect the good operation of bulk treatment facility.
Two, ammonia stripping: adopt the higher ammonia nitrogen of content in the cyclic aeration ammonia stripping jar treating refuse percolate.The waterpower recycle ratio is 4:1, and gas-water ratio is 500:1, and the stripping time is 0.5h.The stripping jar adopts gas---streaming waterborne, and water inlet and aeration gas are by the tank body bottom packing layer of upwards flowing through.The tank body middle part is a packing layer, fills high mass transfer ceramics filling, particle diameter 4～6mm.
The ammonia nitrogen of high density is one of feature of percolate, and the ammonia nitrogen of high density has certain restraining effect to the treatment system of biology on the one hand, and C/N is than imbalance in the percolate because the ammonia nitrogen of high density causes for another side, and biological denitrificaion is difficult to carry out.Through stripping, ammonia nitrogen removal frank can reach about 75% in the percolate, has reduced the processing load of subsequent biological treatment technology.In addition, aeration stripping also can play certain preaeration effect, can reduce COD content in the percolate within the specific limits, and the step of going forward side by side is put in order sewage nutritive substance ratio, makes it more to help biological treatment.
Three, anaerobic treatment: anaerobic technique of the present invention adopts secondary upflow type anaerobic sewage sludge reactor (UASB), waste water evenly enters the UASB reactor from the bottom through water distributor, upwards flow, granule sludge (mud flco) is in suspended state under current that rise and bubble effect.Reactor lower part is the higher Sludge Bed of concentration, and top is the lower suspended sludge layer of concentration, and waste water contacts with anaerobic sludge, oxygenolysis organic pollutant under acid-producing bacteria group and the acting in conjunction of methane flora, and final fermentation forms methane.Top at reactor is provided with triphase separator, can outgas and make to pollute to precipitate to get back in the reactor.The COD load is higher in the UASB reactor, and sludge concentration is up to 100～500g/L in the reactor, so the COD clearance reaches 70%～90%.The UASB reactor produces biogas and can be used as resource utilization.
Two-stage anaerobic stage waterpower total residence time 48h, the I and II residence time also is that the I and II hydraulic detention time is 24h than for 1:1.Temperature of reactor is controlled at 20～40 ℃, and the pH value stabilization is 7～8.
Four, aerobic treatment: adopt secondary efficient mass transfer filler contact oxidation method.
Wherein one-level contact oxidation technology residence time 6h is provided with the medium-soft fibrous packing, as BR type semi soft packing, gas-water ratio 10:1; Two-stage biological contact oxidation technology residence time 5h is provided with floating stuffing, as SNP suspended biological filler, PF, gas-water ratio 20:1.
Five, materialization advanced treatment: this stage is an advanced treatment process, can effectively reduce Pollutant levels such as SS in the percolate.Comprise coagulation, precipitation and filtration process.
Coagulation process is the jump partition plate reaction tank, considers the characteristics of the high SS of percolate, adopts polyaluminium salts or polymeric ferric salt flocculation agent; Depositing technology adopts inclined-plate clarifying basin; Filtration process is a conventional rapid filter, and double-layer filter material is common quartz sand and hard coal.
Six, sludge treatment: aerobic system excess sludge and sludge from sedimentation tank enter sludge treating system, adopt plate and frame(type)filter press.Yu Shui is back to equalizing tank, and dewatered sludge landfill is gone into waste layer.
Seven, recharge: adopt recharge system, comprise the sterilization pre-treatment, recharge, recharge system comprises: the pond, recharge pump, water-transmission line, shower nozzle.
Sterilization pre-treatment: pass through disinfection by chlorine dioxide; Kill virus and bacterium in the percolate on the one hand, can effectively alleviate on the other hand because of the bacterium algae multiplies the shower nozzle that recharges that causes and stop up.
Recharge: the number of times of batching is 4～7 times/d, hydraulic load 12～20L/m
2D, the COD 60～80g/m that loads
2D.
Kill virus and bacterium in the percolate on the one hand by disinfection by chlorine dioxide, can effectively alleviate on the other hand because of the bacterium algae multiplies the shower nozzle that recharges that causes and stop up.
It is a kind of effective treatment process that processing is sprayed in the circulation of percolate, is mainly reflected in two aspects.The one, decrement, the spray of returning of percolate can be by evaporating or being absorbed by vegetation, and the treatment capacity outside the venue of minimizing percolate reduces the investment that percolate is handled.The 2nd, quicken the stabilization process.By recharging the water ratio that can improve waste layer, increase the humidity of rubbish, strengthen microbic activity in the rubbish, quicken methanogenic speed and organic decomposition, shorten the stabilization process of landfill waste.By reflux cycle, the BOD of percolate
5Can drop to 30～350mg/L and 70～500mg/L respectively with COD.
In addition, can also improve water-deficient area garbage loading embeading layer water ratio, quicken organic decomposition in the rubbish, shorten the stabilization process (making the stabilization process of former need 15 years～20 years foreshorten to 2 years～3 years) of landfill waste by recharging.
Adopt the mode treating refuse percolate of circulated backfilling need consider the climate hydrologic condition, factors such as the number of times of batching, hydraulic load and COD load.Generally need determine, and the amount of recharging should improve along with the process of waste layer stabilization according to the test of landfill yard practical situation.The present invention determines that by testing optimum condition is: the number of times of batching is 4～7 times/d, hydraulic load 12～20L/m
2.d, COD load 60～80g/m
2D.The degradation efficiency of COD and BOD is reached respectively about 70% and 75%, and the percolate decrement also can reach more than 70%.
Embodiment 2
One, equalizing tank is set: the waterpower adjustment pond is the underground type skeleton construction, hydraulic detention time 18d.
Two, ammonia stripping: adopt the higher ammonia nitrogen of content in the cyclic aeration ammonia stripping jar treating refuse percolate.Recycle ratio is 5:1, and gas-water ratio is 700:1, and the stripping time is 45min.The stripping jar adopts gas---streaming waterborne, and water inlet and aeration gas are by the tank body bottom packing layer of upwards flowing through.The tank body middle part is a packing layer, fills high mass transfer ceramics filling, particle diameter 4～6mm.
Three, anaerobic treatment: anaerobic technique of the present invention adopts secondary upflow type anaerobic sewage sludge reactor (UASB).
Two-stage anaerobic stage waterpower total residence time 60h, the I and II residence time also is that the I and II hydraulic detention time is respectively 24h and 36h than for 2:3.Temperature of reactor is controlled at 20～40 ℃, and the pH value stabilization is 7～8.
Four, aerobic treatment: adopt secondary efficient mass transfer filler contact oxidation method.
Wherein one-level contact oxidation technology residence time 8h is provided with medium-soft fibrous packing gas-water ratio 12:1; Two-stage biological contact oxidation technology residence time 6h is provided with floating stuffing, as SNP suspended biological filler, PF, gas-water ratio 20:1.
Five, materialization advanced treatment process: this stage is an advanced treatment process, can effectively reduce Pollutant levels such as SS in the percolate.Comprise coagulation, precipitation and filtration process.
Coagulation process is the jump partition plate reaction tank, considers the characteristics of the high SS of percolate, adopts polyaluminium salts or polymeric ferric salt flocculation agent; Depositing technology adopts inclined-plate clarifying basin; Filtration process is a conventional rapid filter, and double-layer filter material is common quartz sand and hard coal.
Six, sludge treatment: aerobic system excess sludge and sludge from sedimentation tank enter sludge treating system, adopt plate and frame(type)filter press.Yu Shui is back to equalizing tank, and dewatered sludge landfill is gone into waste layer.
Seven, recharge: adopt recharge system, comprise the sterilization pre-treatment, recharge, recharge system comprises: the pond, recharge pump, water-transmission line, shower nozzle.
Sterilization pre-treatment: pass through disinfection by chlorine dioxide; Kill virus and bacterium in the percolate on the one hand, can effectively alleviate on the other hand because of the bacterium algae multiplies the shower nozzle that recharges that causes and stop up.
Recharge: the number of times of batching is 4～7 times/d, hydraulic load 12～20L/m
2D, the COD 60～80g/m that loads
2D.
Embodiment 3
One, equalizing tank is set: the waterpower adjustment pond is the underground type skeleton construction, hydraulic detention time 20d.
Two, ammonia stripping: adopt the higher ammonia nitrogen of content in the cyclic aeration ammonia stripping jar treating refuse percolate.Recycle ratio is 5:1, and gas-water ratio is 900:1, and the stripping time is 1h.The stripping jar adopts gas---streaming waterborne, and water inlet and aeration gas are by the tank body bottom packing layer of upwards flowing through.The tank body middle part is a packing layer, fills high mass transfer ceramics filling, particle diameter 4～6mm.
Three, anaerobic treatment: anaerobic technique of the present invention adopts secondary upflow type anaerobic sewage sludge reactor (UASB).
Two-stage anaerobic stage waterpower total residence time 60h, the I and II residence time also is that the I and II hydraulic detention time is respectively 24h and 36h than for 2:3.Temperature of reactor is controlled at 20～40 ℃, and the pH value stabilization is 7～8.
Four, aerobic treatment: adopt secondary efficient mass transfer filler contact oxidation method.
Wherein one-level contact oxidation technology residence time 10h is provided with medium-soft fibrous packing gas-water ratio 15:1; Two-stage biological contact oxidation technology residence time 8h is provided with floating stuffing (as SNP suspended biological filler, PF), gas-water ratio 25:1.
Five, materialization advanced treatment process: this stage is an advanced treatment process, can effectively reduce Pollutant levels such as SS in the percolate.Comprise coagulation, precipitation and filtration process.
Coagulation process is the jump partition plate reaction tank, considers the characteristics of the high SS of percolate, adopts polyaluminium salts or polymeric ferric salt flocculation agent; Depositing technology adopts inclined-plate clarifying basin; Filtration process is a conventional rapid filter, and double-layer filter material is common quartz sand and hard coal.
Six, sludge treatment: aerobic system excess sludge and sludge from sedimentation tank enter sludge treating system, adopt plate and frame(type)filter press.Yu Shui is back to equalizing tank, and dewatered sludge landfill is gone into waste layer.
Seven, recharge: adopt recharge system, comprise the sterilization pre-treatment, recharge, recharge system comprises: the pond, recharge pump, water-transmission line, shower nozzle.
Sterilization pre-treatment: pass through disinfection by chlorine dioxide; Kill virus and bacterium in the percolate on the one hand, can effectively alleviate on the other hand because of the bacterium algae multiplies the shower nozzle that recharges that causes and stop up.
Recharge: the number of times of batching is 4～7 times/d, hydraulic load 12～20L/m
2D, the COD 60～80g/m that loads
2.d.
Claims (1)
1, the treatment process of a kind of suitable water-deficient area percolate from garbage filling field comprises the following steps:
One, equalizing tank is set: the waterpower adjustment pond that hydraulic detention time reaches 10d～20d is set, percolate from garbage filling field is entered in this equalizing tank;
Two, ammonia stripping: the percolate from garbage filling field in the equalizing tank is risen in the cyclic aeration ammonia stripping jar, adopt the ammonia nitrogen in this cyclic aeration ammonia stripping jar treating refuse percolate; The waterpower recycle ratio is 5～4:1, and gas-water ratio is 500～900:1, and the stripping time is 0.5～1h; The stripping jar adopts gas-streaming waterborne, and water inlet and aeration gas are by the tank body bottom packing layer of upwards flowing through; The tank body middle part is a packing layer, fills ceramics filling, particle diameter 4～6mm;
Three, anaerobic treatment: adopt secondary upflow type anaerobic sewage sludge reactor (UASB), to flow into through the percolate from garbage filling field behind the ammonia stripping in this secondary upflow type anaerobic sewage sludge reactor, two-stage anaerobic stage waterpower total residence time 48h～60h, I and II residence time ratio is 1: 1 or 2: 3, temperature of reactor is controlled at 20～40 ℃, and the pH value stabilization is 7～8;
Four, aerobic treatment: adopt secondary mass transfer filler contact oxidation method, the percolate from garbage filling field through anaerobic treatment is flowed in the aerobic treatment device;
Wherein one-level catalytic oxidation residence time 6h～10h is provided with the medium-soft fibrous packing, gas-water ratio 10～15:1; Two-stage biological contact oxidation residence time 5h～8h is provided with floating stuffing, gas-water ratio 20～25:1;
Five, materialization advanced treatment: the percolate from garbage filling field through aerobic treatment is flowed in the materialization advanced treatment pond, comprise coagulation, precipitation and filtration;
Coagulation adopts the jump partition plate reaction tank, adopts polyaluminium salts or polymeric ferric salt flocculation agent; Depositing technology adopts inclined-plate clarifying basin; Filtration process is a conventional rapid filter, and double-layer filter material is common quartz sand and hard coal;
Six, sludge treatment: excess sludge and sludge from sedimentation tank enter sludge treating system in the aerobic treatment, adopt plate and frame(type)filter press, and Yu Shui is back to equalizing tank, and dewatered sludge landfill is gone into waste layer;
Seven, recharge: adopt recharge system, this recharge system comprises: the pond, recharge pump, water-transmission line, shower nozzle; Make percolate from garbage filling field flow into this recharge system, the pre-treatment that carries out disinfection, recharge through the materialization advanced treatment:
Sterilization pre-treatment: pass through disinfection by chlorine dioxide;
Recharge: the number of times of batching is 4～7 times/d, hydraulic load 12～20L/m
2D, the COD 60～80g/m that loads
2D.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101302068B (en) * | 2008-07-04 | 2010-06-02 | 四川省环境保护科学研究院 | Multi-stage refluxing load control biological process and matched facilities |
| CN101318740B (en) * | 2008-07-18 | 2011-06-08 | 黄主榕 | Garbage leachate processing technique |
| CN101804411A (en) * | 2010-03-02 | 2010-08-18 | 华东师范大学 | Method for controlling obnoxious gas of urban refuse landfill |
| EP2418176A1 (en) * | 2010-08-12 | 2012-02-15 | Basf Se | Method for purifying waste water resulting from the processing of raw mononitrobenzol |
| CN102329057B (en) * | 2011-09-09 | 2013-02-13 | 杭州江南科学研究院有限公司 | Method for treating high concentration ammonia nitrogen landfill leachate |
| CN102701540A (en) * | 2012-06-28 | 2012-10-03 | 苏州科博思流体科技有限公司 | High-efficiency domestic sewage treatment device |
| CN102897972B (en) * | 2012-09-27 | 2013-09-11 | 崇明县绿化和市容管理局 | Domestic waste landfill site leachate zero-discharge system and treatment method |
| CN103553244B (en) * | 2013-11-15 | 2014-08-13 | 武汉理工大学 | Method for purifying refuse leachate by coupling inorganic gradient adsorption with organic flocculation |
| CN103663833A (en) * | 2013-12-03 | 2014-03-26 | 北京市环境保护科学研究院 | Treatment method and device for fluidizing and stripping high ammonia and nitrogen waste water |
| CN104722562B (en) * | 2015-03-13 | 2016-10-05 | 西南交通大学 | The control technique of aerobe reactor landfill yard |
| CN105819626A (en) * | 2016-05-09 | 2016-08-03 | 杭州鼎隆环保科技有限公司 | Combined customized sewage disposal system |
| CN105836974B (en) * | 2016-05-24 | 2019-07-16 | 华南理工大学 | A kind of garbage leachate treatment device and method |
| CN106365376A (en) * | 2016-08-30 | 2017-02-01 | 宜兴市中发水处理环保设备有限公司 | Treating system applied to garbage leachate |
| CN110282828A (en) * | 2019-07-02 | 2019-09-27 | 安徽伊尔思环境科技有限公司 | A kind of garbage loading embeading infiltration liquid processing method |
| CN115353254A (en) * | 2022-07-29 | 2022-11-18 | 上海同济建设科技股份有限公司 | Carbon emission reduction process and device for leachate treatment system |
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