JP4197807B2 - Leachate load fluctuation mitigation method - Google Patents

Leachate load fluctuation mitigation method Download PDF

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Publication number
JP4197807B2
JP4197807B2 JP19380399A JP19380399A JP4197807B2 JP 4197807 B2 JP4197807 B2 JP 4197807B2 JP 19380399 A JP19380399 A JP 19380399A JP 19380399 A JP19380399 A JP 19380399A JP 4197807 B2 JP4197807 B2 JP 4197807B2
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Prior art keywords
leachate
waste
water
facility
treatment
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JP19380399A
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Japanese (ja)
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JP2001017996A (en
Inventor
正器 高比良
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Kubota Corp
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Kubota Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、一般廃棄物、産業廃棄物等の最終処分場における埋立技術に係り、浸出水負荷変動緩和方法に関する。
【0002】
【従来の技術】
最終処分場における浸出水の水量、水質は、埋立ごみ質、降雨量等の気象条件、埋立構造、埋立地の規模、集水面積の大小、埋立期間、ごみ埋立経過時間等により異なる。埋立処分場における浸出水は、埋立後に既に長い年月を経た既設埋立区画から出る浸出水も、埋立後の年月が短い新設埋立区画から出る浸出水も、廃棄物の存在しない未設埋立区画から出る浸出水をも一元的に集水し、その全量を同一工程において処理している。
【0003】
【発明が解決しようとする課題】
このために、浸出水処理施設における処理プラントの規模や処理能力は、処分場に降る全降水量を対象として設定する必要があり、しかも気象条件の変化による変動量をも考慮するために、浸出水を処理する浸出水処理施設の規模を算定する際にはどうしても能力に冗長な余裕のある施設にならざるを得なかった。
【0004】
しかし、浸出水は降雨量しだいで大きく変動するので、降雨量が少ないときには浸出水処理施設の運転稼動が連続的に停止する一方で、降雨量が集中する時期には汚濁負荷が大きくなって処理が追いつかず、浸出水を処分場に内部保留するような、両極端のケースが常態化している。
本発明は上記した課題を解決するものであり、浸出水処理施設における水処理負荷を平均化することができる浸出水負荷変動緩和方法を提供することを目的とする。
【0005】
【課題を解決するための手段】
上記の課題を解決するために、本発明の浸出水負荷変動緩和方法は、廃棄物を前処理して後に埋立処分場へ投入し、埋立処分場の浸出水を調整槽へ貯留し、前記前処理において廃棄物を一時的に洗浄設備に貯留し、洗浄設備において廃棄物を水洗して洗浄することにより汚濁質を洗浄排水とともに洗い出し、流れ出る汚水を汚水貯留槽に貯留し、汚水貯留槽から汚水を定量的に浸出水処理施設に供給し、調整槽から浸出水を適宜に浸出水処理施設に供給し、浸出水処理施設において汚水貯留槽から流入する汚濁質の多い汚水を定常的な基本水処理負荷として処理し、調整槽から流入する汚濁質の少ない浸出水を変動的な一時水処理負荷として処理するものである。
【0006】
上記した構成により、前処理として廃棄物を水洗いすることで埋立処分場に持ち込まれる汚濁量が少なくなり、浸出水中に含まれる汚濁質の絶対量が少なくなる。よって、降水量の変化によって浸出水の水量が変化しても、その汚濁量の変動量は小さなものとなり、浸出水が浸出水処理施設に与える一時水処理負荷の変動の影響は小さい。
【0007】
一方、前処理によって発生する汚水が降雨量に関係なく浸出水処理施設へ毎時に一定の水量および汚濁量で基本水処理負荷として流入するので、浸出水処理施設を一定レベルの稼動率で連続して運転することができる。
したがって、浸出水処理施設における水処理負荷は、基本水処理負荷と一時水処理負荷の和となり、変動幅が小さく平均化されたものとなる。
【0008】
前処理における洗浄水は浸出水処理施設の処理水を利用することもでき、調整槽に流入する浸出水を利用することもできる。
【0009】
【発明の実施の形態】
以下、本発明の実施形態を図面に基づいて説明する。図1において、埋立処分場1は集排水管2を有し、集排水管2は調整槽3に連通し、調整槽3が浸出水処理施設4に接続している。この浸出水処理施設4は、第1凝集沈殿処理設備、生物処理設備、第2凝集沈殿処理設備、砂ろ過処理設備、活性炭吸着処理設備などを備えている。
【0010】
第1凝集沈殿処理設備は、浸出水原水のカルシウムを除去して、配管・ポンプ類のスケーリングを防止するものであり、カルシウム除去剤を併用したアルカリ凝集沈殿処理を行なう。生物処理設備は、接触酸化型の循環脱窒法を採用しており、充填材表面の微生物を利用して、原水中の有機物の分解と窒素成分の除去を行なう。第2凝集沈殿処理設備は、生物処理水中の汚濁物質を薬品によって凝集させ、重力沈殿除去するものであり、CODや色度成分の除去に効果的な弱酸性凝集沈殿処理を行なう。砂ろ過処理設備は、凝集沈殿処理水中に残る微細な浮遊物質などを、アンスラサイトと珪砂によるろ材で捕捉し、除去する。活性炭吸着処理装置は、活性炭の強力な吸着能力によってCODや色度成分などを除去する。処理水は減菌処理の後に放流もしくは後述する洗浄水として循環利用する。
【0011】
埋立処分する廃棄物5としては、家庭から出る一般廃棄物、工場等から出る産業廃棄物、都市ごみ焼却施設から出る焼却残渣や不燃ごみがある。埋立処分場1に降る雨水は、覆土6の層、廃棄物5の層に浸透し、廃棄物5の有機性汚濁成分、SS、無機塩類等を含んで浸出水として流出し、集排水管2から調整槽3を通って浸出水処理施設4に流入する。
【0012】
埋立処分に際して廃棄物5は、前処理して後に埋立処分場へ投入する。前処理においては、廃棄物5を一時的に洗浄設備7に貯留し、洗浄設備7において廃棄物5に洗浄水をシャワーリングして水洗する。洗い出した廃棄物5の汚濁質は洗浄排水とともに汚水として汚水貯留槽8に貯留し、汚水貯留槽8から汚水をポンプ手段等により定量的に浸出水処理施設4に供給する。
【0013】
浸出水処理施設4においては、調整槽3から流入する汚濁質の少ない浸出水を変動的な一時水処理負荷として処理し、汚水貯留槽8から流入する汚濁質の多い汚水を定常的な基本水処理負荷として処理する。
前処理を行うことで埋立処分場1に持ち込まれる汚濁量が少なくなり、浸出水中に含まれる汚濁質の絶対量が少なくなるので、浸出水の汚濁量が変化しても、その変動量は小さなものとなり、浸出水が浸出水処理施設に与える影響は小さい。一方、前処理によって発生する汚水は降雨量に関係なく浸出水処理施設4へ毎時に一定の水量および汚濁量で流入するので、浸出水処理施設を一定レベルの稼動率で連続して運転することができる。したがって、浸出水処理施設4における水処理負荷は、基本水処理負荷と一時水処理負荷の和となり、変動幅が小さく平均化されたものとなる。洗浄水は浸出水処理施設4の処理水を利用することもでき、調整槽3に流入する浸出水を利用することもできる。
【0014】
【発明の効果】
以上述べたように本発明によれば、前処理することで降水量によって増減する浸出水の汚濁量の変動量が小さなものとなり、降雨量に関係なく汚水が浸出水処理施設へ毎時に一定の水量および汚濁量で基本水処理負荷として流入することになり、浸出水処理施設を一定レベルの稼動率で連続して運転することができ、基本水処理負荷と一時水処理負荷の和は、その変動幅が小さく平均化されたものとなり、浸出水処理施設における水負荷変動を緩和できる。
【図面の簡単な説明】
【図1】本発明の実施形態における埋立処分方法を示す摸式図である。
【符号の説明】
1 埋立処分場
2 集排水管
3 調整槽
4 浸出水処理施設
5 廃棄物
6 覆土
7 洗浄設備
8 汚水貯留槽
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a landfill technique at a final disposal site for general waste, industrial waste, and the like, and relates to a leachate load fluctuation mitigation method.
[0002]
[Prior art]
The amount and quality of leachate at the final disposal site vary depending on the meteorological conditions such as landfill waste quality, rainfall, etc., landfill structure, size of landfill, size of water collection area, landfill period, waste landfill elapsed time, etc. The leachate at the landfill site is the leachate from the existing landfill section that has already passed through the landfill, the leachate from the new landfill section that has been short after the landfill, and the unfilled landfill area where there is no waste. The leachate discharged from the water is also collected centrally, and the entire amount is treated in the same process.
[0003]
[Problems to be solved by the invention]
For this reason, the scale and capacity of the treatment plant in the leachate treatment facility must be set for the total amount of precipitation falling on the disposal site, and in order to take into account fluctuations due to changes in weather conditions, When calculating the scale of a leachate treatment facility that treats water, it was inevitable that the facility would have a redundant capacity.
[0004]
However, the leachate varies greatly depending on the amount of rainfall, so when the rainfall is low, the operation of the leachate treatment facility stops continuously, while the pollution load increases when the rainfall is concentrated. However, the extreme cases where the leachate cannot be caught and the leachate is retained inside the disposal site are becoming normal.
This invention solves an above-described subject, and it aims at providing the leachate load fluctuation | variation relaxation method which can average the water treatment load in a leachate treatment facility.
[0005]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, the leachate load fluctuation mitigation method of the present invention pretreats waste and then inputs it into a landfill site, stores leachate from the landfill site in a regulating tank, and In the treatment, waste is temporarily stored in the washing facility, and the waste is washed and washed in the washing facility to wash out the pollutant together with the washing waste water. The flowing waste water is stored in the waste water storage tank, and the waste water is stored in the waste water storage tank. Is quantitatively supplied to the leachate treatment facility, and the leachate is appropriately supplied from the adjustment tank to the leachate treatment facility. Treated as a treatment load, leachate with less pollutant flowing from the adjustment tank is treated as a variable temporary water treatment load.
[0006]
With the configuration described above, the amount of pollution brought into the landfill site is reduced by washing the waste as a pretreatment, and the absolute amount of pollutant contained in the leachate is reduced. Therefore, even if the amount of leachate changes due to changes in precipitation, the amount of change in the amount of pollution is small, and the influence of the change in temporary water treatment load that leachate has on the leachate treatment facility is small.
[0007]
On the other hand, sewage generated by pretreatment flows into the leachate treatment facility as a basic water treatment load at a constant amount of water and pollution every hour regardless of rainfall, so the leachate treatment facility is continuously operated at a certain level of operation rate. Can drive.
Therefore, the water treatment load in the leachate treatment facility is the sum of the basic water treatment load and the temporary water treatment load, and the fluctuation range is small and averaged.
[0008]
The washing water in the pretreatment can use the treatment water of the leachate treatment facility, and can also use the leachate flowing into the adjustment tank.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1, the landfill 1 has a drainage pipe 2, the drainage pipe 2 communicates with the adjustment tank 3, and the adjustment tank 3 is connected to the leachate treatment facility 4. The leachate treatment facility 4 includes a first coagulation sedimentation treatment facility, a biological treatment facility, a second coagulation sedimentation treatment facility, a sand filtration treatment facility, an activated carbon adsorption treatment facility, and the like.
[0010]
The first coagulation sedimentation treatment equipment removes calcium from the raw leachate water to prevent scaling of piping and pumps, and performs alkali coagulation sedimentation treatment using a calcium removal agent in combination. The biological treatment facility employs a catalytic oxidation type cyclic denitrification method, which uses microorganisms on the surface of the filler to decompose organic substances in raw water and remove nitrogen components. The second agglomeration and sedimentation treatment equipment agglomerates the pollutants in the biologically treated water with chemicals and removes gravity precipitates, and performs a weakly acidic agglomeration and precipitation treatment effective for removing COD and chromaticity components. The sand filtration facility captures and removes fine suspended solids remaining in the coagulated sediment treated water with a filter medium made of anthracite and quartz sand. The activated carbon adsorption treatment apparatus removes COD, chromaticity components, and the like by the strong adsorption ability of activated carbon. The treated water is discharged after the sterilization treatment or recycled as cleaning water described later.
[0011]
Waste 5 to be disposed of in landfill includes general waste from households, industrial waste from factories, incineration residues and incombustible waste from municipal waste incineration facilities. Rainwater that falls on the landfill site 1 penetrates the layer of the cover soil 6 and the layer of the waste 5 and flows out as leachate containing the organic pollutant components, SS, inorganic salts, etc. of the waste 5 and collects the drainage pipe 2 Then flows into the leachate treatment facility 4 through the adjustment tank 3.
[0012]
At the time of landfill disposal, the waste 5 is pretreated and then input to the landfill disposal site. In the pretreatment, the waste 5 is temporarily stored in the cleaning facility 7, and the cleaning water is showered in the cleaning facility 7 and washed with water. The pollutant of the washed out waste 5 is stored in the sewage storage tank 8 as sewage together with the cleaning waste water, and the sewage is quantitatively supplied from the sewage storage tank 8 to the leachate treatment facility 4 by a pump means or the like.
[0013]
In the leachate treatment facility 4, leachate with less pollutant flowing from the adjustment tank 3 is treated as a variable temporary water treatment load, and sewage with much pollutant flowing from the sewage storage tank 8 is treated as basic basic water. Process as processing load.
By performing pretreatment, the amount of pollution brought into the landfill site 1 is reduced, and the absolute amount of pollutant contained in the leachate is reduced. Therefore, even if the amount of leachate is changed, the amount of fluctuation is small. The leachate has little impact on the leachate treatment facility. On the other hand, since the sewage generated by the pretreatment flows into the leachate treatment facility 4 at a constant amount of water and pollution every hour regardless of rainfall, the leachate treatment facility should be operated continuously at a certain level of operation rate. Can do. Therefore, the water treatment load in the leachate treatment facility 4 is the sum of the basic water treatment load and the temporary water treatment load, and the fluctuation range is small and averaged. As the washing water, the treated water of the leachate treatment facility 4 can be used, and the leachate flowing into the adjustment tank 3 can also be used.
[0014]
【The invention's effect】
As described above, according to the present invention, the amount of change in the amount of leachate contamination that increases or decreases depending on the amount of precipitation is reduced by pretreatment, and the amount of sewage is fixed to the leachate treatment facility every hour regardless of the amount of rainfall. As the basic water treatment load flows in with the amount of water and pollution, the leachate treatment facility can be operated continuously at a certain level of operation rate, and the sum of the basic water treatment load and the temporary water treatment load is The fluctuation range is reduced and averaged, and fluctuations in water load at the leachate treatment facility can be mitigated.
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing a landfill disposal method in an embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Landfill disposal site 2 Drainage pipe 3 Adjustment tank 4 Leachate treatment facility 5 Waste 6 Covering soil 7 Cleaning equipment 8 Sewage storage tank

Claims (1)

廃棄物処分場において、前処理として一時的に廃棄物を洗浄設備に貯留して水洗し、廃棄物の保有する汚濁質を洗い出して流れ出る汚水を汚水貯留槽に貯留し、汚水貯留槽から汚水を定量的に浸出水処理施設に供給する一方で、前処理した廃棄物を埋立処分場へ投入し、埋立処分場の浸出水を調整槽へ貯留し、調整槽から浸出水を適宜に浸出水処理施設に供給し、浸出水処理施設において汚水貯留槽から流入する汚濁質の多い汚水を定常的な基本水処理負荷として処理し、調整槽から流入する汚濁質の少ない浸出水を変動的な一時水処理負荷として処理することを特徴とする浸出水負荷変動緩和方法。At the waste disposal site, the waste is temporarily stored in the washing facility and washed as a pretreatment, and the sewage flowing out after washing out the pollutants held in the waste is stored in the sewage storage tank, and the sewage is collected from the sewage storage tank. While supplying quantitatively to the leachate treatment facility, the pretreated waste is thrown into the landfill site, the leachate from the landfill site is stored in the adjustment tank, and the leachate is appropriately treated from the adjustment tank. The effluent with a large amount of pollutant that is supplied to the facility and flows from the sewage storage tank at the leachate treatment facility is treated as a regular basic water treatment load, and the leachate with a small amount of pollutant that flows from the adjustment tank is changed temporarily. A leachate load fluctuation mitigation method characterized by treating as a treatment load.
JP19380399A 1999-07-08 1999-07-08 Leachate load fluctuation mitigation method Expired - Lifetime JP4197807B2 (en)

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Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
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JP4197807B2 true JP4197807B2 (en) 2008-12-17

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015176697A1 (en) * 2014-05-17 2015-11-26 Hans Joachim Kahle Method and device for the treatment and use of bio-waste, residual waste and landfill material from domestic refuse landfills for biogas plants

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