JP3485450B2 - Resource recovery landfill method - Google Patents
Resource recovery landfill methodInfo
- Publication number
- JP3485450B2 JP3485450B2 JP23529497A JP23529497A JP3485450B2 JP 3485450 B2 JP3485450 B2 JP 3485450B2 JP 23529497 A JP23529497 A JP 23529497A JP 23529497 A JP23529497 A JP 23529497A JP 3485450 B2 JP3485450 B2 JP 3485450B2
- Authority
- JP
- Japan
- Prior art keywords
- acid
- resource recovery
- water
- leachate
- treatment
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Processing Of Solid Wastes (AREA)
Description
【0001】[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、廃棄物
中の有価物を回収し、閉鎖期間の短縮を図る資源回収型
埋立処分方法を提供することを目的とする。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to landfill technology for final disposal sites for general waste, industrial waste, etc., and is a resource recovery type landfill disposal for recovering valuable materials in waste to shorten the closing period. The purpose is to provide a method.
【0002】[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
等により異なり、埋立地固有の特徴が見られる。たとえ
ば、浸出水中の有機性汚濁成分は埋立初期には高濃度で
あるが、経年的に減少し、数年後には生物分解可能な、
あるいは困難な有機物が残ってくる。また、焼却残渣や
不燃ごみを埋め立てる場合には、無機物が多いのでこれ
らに由来するSSや無機塩類が含まれることになる。ま
た、焼却残渣中や不燃ごみ中に生物分解が容易な有機物
が多い場合は、BOD,COD,T−N,NH4 +−N等
が比較的高濃度になる。2. Description of the Related Art The quantity of leachate at the final disposal site depends on the quality of landfill, weather conditions such as rainfall, landfill structure, size of landfill, size of catchment area, landfill period, elapsed time of landfill, etc. The characteristics peculiar to the landfill can be seen. For example, organic pollutants in leachate have high concentrations at the beginning of landfill, but they decrease over time and biodegradable after several years.
Or difficult organic matter remains. In addition, when landfilling incineration residues and non-combustible waste, since there are many inorganic substances, SS and inorganic salts derived from these are included. Also, if the incineration residue and often easy organic matter biodegradation noncombustible during garbage, BOD, COD, T-N , NH 4 + -N and the like is relatively high concentrations.
【0003】[0003]
【発明が解決しようとする課題】浸出水を処理する浸出
水処理施設は、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。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
する。The leachate treatment facility for treating leachate comprises a first coagulation sedimentation treatment facility, a biological treatment facility,
It is equipped with a second coagulation-sedimentation treatment facility, sand filtration treatment facility, activated carbon adsorption treatment facility, and the like. The first coagulation-sedimentation treatment equipment removes calcium in the raw water of the leachate to prevent scaling of pipes and pumps, and performs alkali coagulation-sedimentation treatment in combination with a calcium removing agent. The biological treatment equipment adopts the catalytic oxidation type cyclic denitrification method, which uses microorganisms on the surface of the packing material to decompose organic substances in the raw water and remove nitrogen components. The second coagulation-sedimentation treatment facility coagulates pollutants in biologically treated water by chemicals and removes them by gravity sedimentation, and performs weak acid coagulation-sedimentation treatment effective for removing COD and chromaticity components. The sand filtration equipment captures and removes fine suspended matter remaining in the coagulation-sedimentation-treated water with a filter medium composed of anthracite and silica sand. The activated carbon adsorption treatment device removes COD, chromaticity components, etc. due to the strong adsorption ability of activated carbon. Treated water is discharged after sterilization treatment.
【0004】上述した浸出水の処理においては、浸出中
の重金属や塩分等は無用な有害成分として処理している
が、重金属や塩分は本来において有価物であり、それら
を回収して資源化することが資源の再利用、有効活用の
観点において求められる。In the above-mentioned treatment of leachate, heavy metals and salts in the leachate are treated as useless harmful components, but heavy metals and salts are originally valuable materials and are recovered and recycled. Is required from the viewpoint of resource reuse and effective use.
【0005】本発明は、上記した課題を解決するもので
あり、廃棄物から浸出水中に溶出する有価物を回収し、
埋立処分場の閉鎖期間の短縮を図る資源回収型埋立処分
方法を提供することを目的とする。The present invention is intended to solve the above-mentioned problems, and recovers valuable substances eluted from leachate from waste,
An object of the present invention is to provide a resource recovery type landfill disposal method for shortening the closing period of a landfill disposal site.
【0006】[0006]
【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、本発明の資源回収型埋立処分方法は、埋立処分場
から浸出する浸出水を脱塩処理し、脱塩処理において発
生する濃縮水をバイポーラ膜分離装置において分離処理
することにより、酸、アルカリを生成し、生成した酸を
埋立処分場の埋め立てた廃棄物に返送し、廃棄物を酸分
解して重金属を浸出水中に溶解し、廃棄物の性状を早期
に安定化するものである。In order to solve the above-mentioned problems, the resource recovery type landfill disposal method of the present invention desalinates the leachate leached from the landfill disposal site and concentrates it in the desalination process. By separating water with a bipolar membrane separator, acid and alkali are generated, the generated acid is returned to the landfill waste at the landfill disposal site, and the waste metal is decomposed by acid to dissolve the heavy metal in the leachate. , It stabilizes the properties of waste materials at an early stage.
【0007】バイポーラ膜分離装置において生成する
酸、アルカリを水処理におけるpH調整剤として利用す
るものである。脱塩処理において発生する濃縮水を電気
分解して次亜塩素酸ソーダを生成し、生成した次亜塩素
酸ソーダを水処理における消毒剤として利用するもので
ある。The acid and alkali produced in the bipolar membrane separator are used as a pH adjuster in water treatment. The concentrated water generated in the desalination treatment is electrolyzed to generate sodium hypochlorite, and the generated sodium hypochlorite is used as a disinfectant in water treatment.
【0008】脱塩処理において処理した処理水をごみ焼
却施設におけるガス冷却水として利用するものである。The treated water treated in the desalination treatment is used as gas cooling water in a refuse incineration facility.
【0009】[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は埋め
立てた廃棄物のごみ層2を覆土3で覆って埋立地を形成
しており、埋立地に降る雨水は覆土3、ごみ層2に浸透
し浸出水となって流出する。この浸出水は埋立地の最下
層に連通する集排水配水管路4を通って浸出水貯留槽5
に流入する。浸出水貯留槽5は浸出水を一時的に貯留す
るものであり、浸出水貯留槽5の浸出水はポンプ6を備
えた送水管路系7を通って有価物回収設備8に送る。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. In Fig. 1, the landfill disposal site 1 forms a landfill by covering the waste layer 2 of the landfilled waste with the cover soil 3, and the rainwater falling on the landfill penetrates the cover soil 3 and the waste layer 2 and becomes leachate. Outflow. This leachate passes through the drainage / drainage distribution pipe 4 communicating with the bottom layer of the landfill, and the leachate storage tank 5
Flow into. The leachate storage tank 5 temporarily stores leachate, and the leachate in the leachate storage tank 5 is sent to the valuable resource recovery facility 8 through a water supply pipe system 7 equipped with a pump 6.
【0010】有価物回収設備8は前処理工程と脱塩処理
工程とバイポーラ膜分離工程と電解処理工程を備えてい
る。前処理工程においては、浸出水中のカルシウムを沈
降分離9し、その分離水を膜分離型生物処理10してB
OD等を除去する。沈降分離9において沈殿したカルシ
ウムは汚泥脱水11し、カルシウム汚泥12を排ガス・
洗浄13や中和剤14として利用する。The valuable resource recovery facility 8 comprises a pretreatment step, a desalting step, a bipolar membrane separation step and an electrolytic treatment step. In the pretreatment step, calcium in the leachate is separated by sedimentation 9 and the separated water is subjected to a membrane separation type biological treatment 10 and B
Remove OD, etc. The calcium precipitated in the settling separation 9 is sludge dewatered 11 and the calcium sludge 12 is exhausted.
It is used as the cleaning 13 and the neutralizer 14.
【0011】脱塩処理工程においては、膜分離型生物処
理10の処理水を電気透析装置15において脱塩処理
し、脱塩処理した処理水をダイオキシン除去処理16す
る。この処理水は放流するか、ごみ焼却施設におけるガ
ス冷却水として利用する。In the desalination treatment step, the treated water of the membrane separation type biological treatment 10 is desalted in the electrodialyzer 15 and the desalted treated water is subjected to a dioxin removing treatment 16. This treated water should be discharged or used as gas cooling water in a refuse incineration facility.
【0012】バイポーラ膜分離工程においては、脱塩処
理において発生する濃縮水をバイポーラ膜分離装置17
において分離処理することにより、酸18、アルカリ1
9を生成する。生成した酸18は埋立処分場1の埋立地
に返送し、埋立地の廃棄物を酸分解して重金属を浸出水
中に溶解し、廃棄物の性状を早期に安定化する。このこ
とにより、埋立処分場1の供用の開始から閉鎖までに要
する閉鎖期間の短縮を図る。バイポーラ膜分離装置17
において生成する酸18、アルカリ19は、その双方を
水処理におけるph調整剤として利用することもでき
る。In the bipolar membrane separation step, the concentrated water generated in the desalting process is used as the bipolar membrane separation device 17
Acid 18, alkali 1 by separation treatment in
9 is generated. The generated acid 18 is returned to the landfill of the landfill disposal site 1, the waste of the landfill is decomposed by acid to dissolve the heavy metal in the leachate, and the properties of the waste are stabilized early. As a result, the closing period required from the start of the operation of the landfill disposal site 1 to the closing thereof will be shortened. Bipolar membrane separator 17
Both of the acid 18 and the alkali 19 produced in step 2 can be used as pH adjusters in water treatment.
【0013】脱塩処理において発生する濃縮水は、電気
分解20において次亜塩素酸ソーダ21となし、生成し
た次亜塩素酸ソーダ21は水処理における消毒剤として
利用する。The concentrated water generated in the desalting process is converted into sodium hypochlorite 21 in the electrolysis 20, and the generated sodium hypochlorite 21 is used as a disinfectant in the water treatment.
【0014】[0014]
【発明の効果】以上述べたように本発明によれば、脱塩
処理した浸出水の濃縮水からバイポーラ膜分離装置にお
いて酸、アルカリを生成し、生成した酸により廃棄物の
重金属を溶解することにより、廃棄物の性状を早期に安
定化することができ、酸、アルカリを水処理におけるp
H調整剤として利用でき、脱塩処理した濃縮水から電気
分解により次亜塩素酸ソーダを生成し、次亜塩素酸ソー
ダを水処理における消毒剤として利用でき、脱塩処理お
いて処理した処理水をごみ焼却施設におけるガス冷却水
として利用できるので、廃棄物から浸出水中に溶出する
有価物を回収し、埋立処分場の閉鎖期間の短縮を図るこ
とができる。As described above, according to the present invention, an acid and an alkali are produced in a bipolar membrane separation apparatus from concentrated water of desalted water, and the produced heavy acid dissolves heavy metals in waste. By doing so, the properties of the waste can be stabilized at an early stage, and acid and alkali can be added in water treatment.
It can be used as an H conditioner, can generate sodium hypochlorite by electrolysis from desalted concentrated water, and can use sodium hypochlorite as a disinfectant in water treatment. Treated water treated in desalination treatment. Since it can be used as gas cooling water in a refuse incineration facility, it is possible to collect valuable materials that are eluted from the waste into the leachate and shorten the closing period of the landfill disposal site.
【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。FIG. 1 is a schematic diagram showing a landfill disposal method according to an embodiment of the present invention.
1 埋立処分場 5 浸出水貯留槽 8 有価物回収設備 15 電気透析装置 17 バイポーラ膜分離装置 1 landfill disposal site 5 Leachate storage tank 8 Valuable material recovery equipment 15 Electrodialysis device 17 Bipolar membrane separator
フロントページの続き (56)参考文献 特開 平4−78479(JP,A) 特開 平10−5714(JP,A) 特開 平5−277465(JP,A) (58)調査した分野(Int.Cl.7,DB名) B09B 1/00 - 5/00 Continuation of the front page (56) Reference JP-A-4-78479 (JP, A) JP-A-10-5714 (JP, A) JP-A-5-277465 (JP, A) (58) Fields investigated (Int .Cl. 7 , DB name) B09B 1/00-5/00
Claims (4)
理し、脱塩処理において発生する濃縮水をバイポーラ膜
分離装置において分離処理することにより、酸、アルカ
リを生成し、生成した酸を埋立処分場の埋め立てた廃棄
物に返送し、廃棄物を酸分解して重金属を浸出水中に溶
解し、廃棄物の性状を早期に安定化することを特徴とす
る資源回収型埋立処分方法。1. Leachate leached from a landfill site is desalted, and concentrated water generated in the desalination process is separated in a bipolar membrane separator to generate an acid and an alkali, and the generated acid is removed. A resource recovery type landfill disposal method characterized by returning the landfilled waste at a landfill disposal site, decomposing the acid with acid to dissolve heavy metals in the leachate, and stabilizing the properties of the waste at an early stage.
置において生成する酸、アルカリを、水処理におけるp
H調整剤として利用することを特徴とする資源回収型埋
立処分方法。2. The acid and alkali produced in the bipolar membrane separation apparatus according to claim 1 are added to p in water treatment.
A resource recovery type landfill disposal method characterized by being used as an H regulator.
生する濃縮水を、電気分解して次亜塩素酸ソーダを生成
し、生成した次亜塩素酸ソーダを水処理における消毒剤
として利用することを特徴とする資源回収型埋立処分方
法。3. The concentrated water generated in the desalting treatment according to claim 1 is electrolyzed to generate sodium hypochlorite, and the generated sodium hypochlorite is used as a disinfectant in water treatment. A resource recovery type landfill disposal method characterized by the above.
理した処理水を、ごみ焼却施設におけるガス冷却水とし
て利用することを特徴とする資源回収型埋立処分方法。4. A resource recovery type landfill disposal method, wherein the treated water treated in the desalination treatment according to claim 1 is used as gas cooling water in a refuse incineration facility.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23529497A JP3485450B2 (en) | 1997-09-01 | 1997-09-01 | Resource recovery landfill method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23529497A JP3485450B2 (en) | 1997-09-01 | 1997-09-01 | Resource recovery landfill method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1176970A JPH1176970A (en) | 1999-03-23 |
JP3485450B2 true JP3485450B2 (en) | 2004-01-13 |
Family
ID=16983992
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23529497A Expired - Fee Related JP3485450B2 (en) | 1997-09-01 | 1997-09-01 | Resource recovery landfill method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3485450B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100900305B1 (en) | 2007-07-31 | 2009-06-02 | 한양대학교 산학협력단 | Cover Design Device |
KR101284742B1 (en) * | 2011-03-15 | 2013-07-17 | 이명규 | A circular disposal method of landfill leachate and apparatus thereof |
JP5851789B2 (en) * | 2011-10-07 | 2016-02-03 | Dowaエコシステム株式会社 | Nitrogen treatment method for waste leachate |
-
1997
- 1997-09-01 JP JP23529497A patent/JP3485450B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH1176970A (en) | 1999-03-23 |
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