Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3778775B2 - Landfill stabilization methods - Google Patents
[go: Go Back, main page]

JP3778775B2 - Landfill stabilization methods - Google Patents

Landfill stabilization methods Download PDF

Info

Publication number
JP3778775B2
JP3778775B2 JP2000159282A JP2000159282A JP3778775B2 JP 3778775 B2 JP3778775 B2 JP 3778775B2 JP 2000159282 A JP2000159282 A JP 2000159282A JP 2000159282 A JP2000159282 A JP 2000159282A JP 3778775 B2 JP3778775 B2 JP 3778775B2
Authority
JP
Japan
Prior art keywords
washing
waste
landfill
water
cleaning
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
Application number
JP2000159282A
Other languages
Japanese (ja)
Other versions
JP2001334231A (en
Inventor
安雄 堀井
智彦 佐々木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP2000159282A priority Critical patent/JP3778775B2/en
Publication of JP2001334231A publication Critical patent/JP2001334231A/en
Application granted granted Critical
Publication of JP3778775B2 publication Critical patent/JP3778775B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Fire-Extinguishing Compositions (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、一般廃棄物や産業廃棄物等の最終処分場における埋立技術や、土壌汚染現場、不適正処分場、不法投棄現場等における回復技術に係り、処理に要する期間の短縮を図る埋立地の安定化方法に関する。
【0002】
【従来の技術】
従来の廃棄物埋立地は、堤体をなす貯留構造物によって周囲と遮断し、底部に遮水工および保護土(図示省略)を施工して雨水が浸出水として周囲の地中に漏出することを防止するとともに、浸出水を処理施設に導くための集廃水管を敷設している。集配水管は貯留構造物を貫通してポンプピットに連通しており、集配水管の開口にはゲートを設けている。ポンプピットには浸出水を排出する廃水ポンプを配置している。埋立構造は廃棄物と覆土が交互に層状を成している。
【0003】
埋立地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が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、塩類(Ca、Cl等)、重金属(Pb、Hg、Cd等)、ダイオキシン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。
【0004】
【発明が解決しようとする課題】
この埋立処分場の閉鎖は、処分場の全域における埋立が完了した後に、浸出水中の重金属、塩分等の有害成分の濃度が許容値以下に低下し、浸出水の水質が安定した時点で行なっている。
【0005】
したがって、埋立処分場の供用開始から閉鎖までに要する期間は長年月となり、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った。
【0006】
また、焼却残渣(飛灰、主灰)中のダイオキシン類の洗い出しは極めて少なく、埋立地内のダイオキシンポテンシャル(保有量)が高く、長期間にわたって埋立地のリスクが高くなるので、閉鎖までに要する期間が長くなる。
【0007】
本発明は上記した課題を解決するものであり、浸出水の水質を早期に安定化し、埋立の開始から閉鎖までの期間を短縮することができる埋立地の安定化方法を提供することを目的とする。
【0008】
【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、請求項1に係る本発明の安定化方法は、埋立地へ投入するに先立って廃棄物を前処理するものであって、細かく破砕した廃棄物を前段の機械洗浄工程において水で洗浄することにより廃棄物中の有機物、重金属、ダイオキシン類を洗浄液中に溶出させ、この洗浄廃水を分離除去工程で固液分離して得られる固形物と前段の機械洗浄工程における前段洗浄物とを後段の機械洗浄工程において有機溶媒で洗浄することにより廃棄物に残留するダイオキシン類を洗浄液中に溶出させ、後段の機械洗浄工程における後段洗浄物を前段の機械洗浄工程に再度投入して水で洗浄し、この機械洗浄後の最終洗浄物を埋立地へ投入し、分離除去工程の脱離液および後段の機械洗浄工程の洗浄廃水を埋立地の浸出水処理施設で水処理するものである。
【0011】
上記した構成により、廃棄物に含まれる塩類、重金属、ダイオキシン類の除去率が高まり、これらの有害物質が浸出水中に溶出することがなく、埋立処分場の供用開始から閉鎖までに要する期間を短縮することができる。
【0012】
【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、埋立廃棄物(又は搬入廃棄物)1は、都市ごみ焼却灰、産業廃棄物等の多種類の汚染物質を複合的に含むものであり、この埋立廃棄物1を埋立地へ投入するに先立って廃前処理する。
【0013】
埋立廃棄物1を破砕工程2において粒径30mm以下に細かく破砕し、破砕した廃棄物を機械洗浄工程3において水もしくは有機溶媒からなる洗浄液で洗浄する。機械洗浄工程3では、例えば機械式洗浄機の回転ドラム内に所定量の廃棄物と所定量の水もしくは有機溶媒を1:10の割合(容積比)で投入し、1回(20分程度)の洗浄作業において回転ドラムの回転によって廃棄物と洗浄液とを攪拌して洗浄作業を行う。この洗浄により廃棄物中の有機物(BOD、COD等)、重金属(Pb、Hg、Cd等)、ダイオキシン類を洗浄液中に溶出させ、1回の洗浄作業終了後に機械式洗浄機内の洗浄廃水(スラリー)を分離除去工程4に導く。この後、新たに水もしくは有機溶媒からなる洗浄液を機械式洗浄機の回転ドラム内に投入して洗浄作業を行い、この洗浄作業を4回以上行なう。全ての洗浄作業が終了した後に、機械式洗浄機に残った機械洗浄後の洗浄物を埋立地へ投入する。
【0014】
この洗浄によって得られる廃棄物の安定化指標は、最終回の洗浄作業後の洗浄廃水をろ過して得られるろ過水中の各成分量において以下のようになる。
EC(電気伝導率)≦1500μs/cm
Pb≦0.1ppm
DXN(ダイオキシン類)含有量≦10pg−TEQ/L
COD≦20ppm
分離除去工程4では、例えば沈降分離設備において洗浄廃水を沈降分離し、沈降した固形物を埋立地へ投入して埋立処分し、脱離液を埋立地の浸出水処理施設で水処理する。
【0015】
この構成により、廃棄物に含まれる塩類、重金属、ダイオキシン類を事前に除去するので、これらの有害物質が浸出水中に溶出することがなく、埋立処分場の供用開始から閉鎖までに要する期間を短縮することができる。
【0016】
図2は本発明の他の実施の形態を示すものである。図2において埋立廃棄物(又は搬入廃棄物)11は、都市ごみ焼却灰、産業廃棄物等の多種類の汚染物質を複合的に含むものであり、この埋立廃棄物11を埋立地へ投入するに先立って廃前処理する。
【0017】
埋立廃棄物11を破砕工程12において粒径30mm以下に細かく破砕し、破砕した廃棄物を前段の機械洗浄工程13において洗浄水で洗浄する。前段の機械洗浄工程13では、例えば機械式洗浄機の回転ドラム内に所定量の廃棄物と所定量の水を1:10の割合(容積比)で投入し、1回(20分程度)の洗浄作業において回転ドラムの回転によって廃棄物と洗浄液とを攪拌して洗浄作業を行う。この洗浄により廃棄物中の有機物(BOD、COD等)、重金属(Pb、Hg、Cd等)、ダイオキシン類を洗浄水中に溶出させ、1回の洗浄作業終了後に機械式洗浄機内の洗浄廃水(スラリー)を分離除去工程14に導く。この後、新たに洗浄水を機械式洗浄機の回転ドラム内に投入して洗浄作業を行い、この洗浄作業を4回以上行なう。
【0018】
分離除去工程14では、例えば沈降分離設備において洗浄廃水を沈降分離し、脱離液を埋立地の浸出水処理施設で水処理する。分離除去工程14で沈降した固形物および前段の機械洗浄工程13における前段洗浄物を後段の機械洗浄工程15において有機溶媒で洗浄する。
【0019】
後段の機械洗浄工程15では、例えば機械式洗浄機の回転ドラム内に所定量の廃棄物と所定量の有機溶媒(濃度5%のメタノール)を1:10の割合(容積比)で投入し、30〜80℃(最適80℃)に加温し、1回(20分程度)の洗浄作業において回転ドラムの回転によって廃棄物と洗浄液とを攪拌して洗浄作業を行う。この洗浄作業によって廃棄物に残留するダイオキシン類を洗浄液中に溶出させ、洗浄廃水を埋立地の浸出水処理施設で水処理する。
【0020】
後段の機械洗浄工程15における後段洗浄物は前段の機械洗浄工程13において再び洗浄水で洗浄する。この前段の機械洗浄工程13では、例えば機械式洗浄機の回転ドラム内に所定量の廃棄物と所定量の水を1:10の割合(容積比)で投入し、1回(20分程度)の洗浄作業において回転ドラムの回転によって廃棄物と洗浄液とを攪拌して洗浄作業を行う。この機械洗浄後の最終洗浄物を埋立地へ投入する。
【0021】
この洗浄によって得られる廃棄物の安定化指標は、最終回の洗浄作業後の洗浄廃水をろ過して得られるろ過水中の各成分量において以下のようになる。
EC(電気伝導率)≦1500μs/cm
Pb≦0.1ppm
DXN(ダイオキシン類)含有量≦10ng−TEQ/g
つまり、DXN(ダイオキシン類)含有量が先の実施の形態のものに比して極微量となる。
【0022】
【発明の効果】
以上述べたように本発明によれば、埋立地へ投入するに先立って廃棄物を前処理し、廃棄物に含まれる塩類、重金属、ダイオキシン類を事前に除去するので、これらの有害物質が浸出水中に溶出することがなく、埋立処分場の供用開始から閉鎖までに要する期間を短縮することができる。
【図面の簡単な説明】
【図1】本発明の実施形態における処理方法を示すフローシートである。
【図2】本発明の他の実施形態における処理方法を示すフローシートである。
【符号の説明】
1 埋立廃棄物
2 破砕工程
3 機械洗浄工程
4 分離除去工程
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to landfill technology at final disposal sites such as general waste and industrial waste, and recovery technology at soil contamination sites, inappropriate disposal sites, illegal dumping sites, etc., and a landfill site that shortens the time required for processing It relates to the stabilization method.
[0002]
[Prior art]
The conventional waste landfill site is isolated from the surroundings by a storage structure that forms a levee body, and rainwater leaks into the surrounding ground as leachate by constructing a water barrier and protective soil (not shown) at the bottom. In addition, the collection and drainage pipes are installed to guide the leachate to the treatment facility. The collection and distribution pipe penetrates the storage structure and communicates with the pump pit, and a gate is provided at the opening of the collection and distribution pipe. The pump pit has a wastewater pump that discharges leachate. In the landfill structure, waste and soil cover are layered alternately.
[0003]
The amount of leachate in landfills depends on landfill quality, weather conditions such as rainfall, landfill structure, size of landfill, size of water collection area, landfill period, waste landfill elapsed time, etc. Is seen. For example, organic pollutants in leachate have a high concentration at the beginning of landfill, but decrease over time, and organic matter that is difficult to biodegrade remains after several years. In addition, when incineration residue or incombustible waste is landfilled, since there are many inorganic substances, SS, salts (Ca, Cl, etc.), heavy metals (Pb, Hg, Cd, etc.) and dioxins derived therefrom are included. In addition, when there are many organic substances that are easily biodegradable in incineration residues or incombustible waste, BOD, COD, TN, NH 4 + -N, etc. have a relatively high concentration.
[0004]
[Problems to be solved by the invention]
This landfill site is closed when landfill in the entire site has been completed and the concentration of harmful metals such as heavy metals and salt in the leachate has fallen below the permissible level and the quality of the leachate has stabilized. Yes.
[0005]
Therefore, it took many years for the landfill site to start and close, and the scale and capacity of the treatment plant in the leachate treatment facility had to be set for the total amount of precipitation falling on the landfill site.
[0006]
In addition, the amount of dioxins in incineration residue (fly ash, main ash) is extremely low, the dioxin potential in the landfill is high, and the risk of landfill is high over a long period of time. Becomes longer.
[0007]
This invention solves the above-mentioned subject, and aims at providing the stabilization method of the landfill which can stabilize the quality of leachate at an early stage, and can shorten the period from the start of landfill to closure. To do.
[0008]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the stabilization method of the present invention according to claim 1 pretreats waste before putting it into a landfill, and the waste that has been finely crushed is pre-machined. By washing with water in the washing process, organic substances, heavy metals and dioxins in the waste are eluted in the washing liquid, and the solid waste obtained by solid-liquid separation of this washing waste water in the separation and removal process and the mechanical washing process in the previous stage Dioxins remaining in the waste are eluted in the cleaning liquid by washing the pre-wash with the organic solvent in the post-machine wash process, and the post-wash in the post-machine wash process is re-injected into the pre-machine wash process. , washed with water, this after machine washing of the final wash was charged to the landfill, water treatment and cleaning waste water eluate and subsequent mechanical cleaning step of separating and removing step landfill leachate treatment facility It is intended to.
[0011]
With the above configuration, the removal rate of salts, heavy metals and dioxins contained in the waste is increased, and these harmful substances are not eluted in the leachate, reducing the time required from the start of operation to closure of the landfill site. can do.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1, landfill waste (or carry-in waste) 1 contains multiple types of pollutants such as municipal waste incineration ash and industrial waste, and this landfill waste 1 is thrown into the landfill. Prior to disposal, pre-treatment.
[0013]
The landfill waste 1 is finely crushed to a particle size of 30 mm or less in the crushing step 2, and the crushed waste is washed with a cleaning liquid composed of water or an organic solvent in the mechanical washing step 3. In the machine cleaning step 3, for example, a predetermined amount of waste and a predetermined amount of water or organic solvent are put in a ratio (volume ratio) of 1:10 into a rotating drum of a mechanical washer, and once (about 20 minutes). In this cleaning operation, the cleaning operation is performed by stirring the waste and the cleaning liquid by the rotation of the rotating drum. By this washing, organic substances (BOD, COD, etc.), heavy metals (Pb, Hg, Cd, etc.) and dioxins in the waste are eluted in the washing liquid, and the washing waste water (slurry) in the mechanical washing machine after one washing operation is completed. ) To the separation and removal step 4. Thereafter, a cleaning liquid composed of water or an organic solvent is newly put into the rotating drum of the mechanical cleaning machine to perform the cleaning operation, and this cleaning operation is performed four or more times. After all the cleaning operations are completed, the machine-cleaned items remaining in the mechanical washer are thrown into the landfill.
[0014]
The stabilization index of the waste obtained by this washing is as follows for each component amount in the filtered water obtained by filtering the washing waste water after the final washing operation.
EC (electrical conductivity) ≦ 1500 μs / cm
Pb ≦ 0.1ppm
DXN (Dioxins) Content ≦ 10pg-TEQ / L
COD ≦ 20ppm
In the separation / removal process 4, for example, the washing wastewater is settled and separated in a sedimentation separation facility, the settled solid matter is thrown into a landfill and disposed in landfill, and the desorbed liquid is water-treated in the leachate treatment facility in the landfill.
[0015]
This configuration removes salts, heavy metals, and dioxins contained in the waste in advance, so that these harmful substances do not elute into the leachate, shortening the time required from the start of operation to closure of the landfill site. can do.
[0016]
FIG. 2 shows another embodiment of the present invention. In FIG. 2, landfill waste (or carry-in waste) 11 contains multiple types of pollutants such as municipal waste incineration ash and industrial waste, and this landfill waste 11 is thrown into a landfill. Prior to waste disposal.
[0017]
The landfill waste 11 is finely crushed to a particle size of 30 mm or less in the crushing step 12, and the crushed waste is washed with washing water in the preceding machine washing step 13. In the machine cleaning step 13 in the previous stage, for example, a predetermined amount of waste and a predetermined amount of water are introduced into a rotating drum of a mechanical washer at a ratio (volume ratio) of 1:10 once (about 20 minutes). In the cleaning operation, the cleaning operation is performed by stirring the waste and the cleaning liquid by the rotation of the rotating drum. By this washing, organic substances (BOD, COD, etc.), heavy metals (Pb, Hg, Cd, etc.) and dioxins in the waste are eluted in the washing water, and the washing waste water (slurry in the mechanical washing machine) after the completion of one washing operation. ) To the separation and removal step 14. After that, cleaning water is newly added into the rotating drum of the mechanical cleaning machine to perform cleaning work, and this cleaning work is performed four or more times.
[0018]
In the separation / removal step 14, for example, the washing wastewater is settled and separated in a sedimentation separation facility, and the desorbed liquid is treated with water in a leachate treatment facility in a landfill. The solid matter settled in the separation / removal step 14 and the pre-washed product in the pre-machine wash step 13 are washed with an organic solvent in the post-machine wash step 15.
[0019]
In the subsequent mechanical cleaning step 15, for example, a predetermined amount of waste and a predetermined amount of organic solvent (concentration of 5% methanol) are charged in a ratio (volume ratio) of 1:10 into a rotating drum of a mechanical cleaning machine, Heating is performed at 30 to 80 ° C. (optimum 80 ° C.), and the cleaning operation is performed by stirring the waste and the cleaning liquid by rotating the rotating drum in one cleaning operation (about 20 minutes). Dioxins remaining in the waste are eluted in the cleaning liquid by this cleaning operation, and the cleaning wastewater is treated with the leachate treatment facility in the landfill.
[0020]
The post-cleaning material in the post-machine washing step 15 is washed again with washing water in the pre-machine wash step 13. In the machine cleaning step 13 in the preceding stage, for example, a predetermined amount of waste and a predetermined amount of water are put into a rotating drum of a mechanical washer at a ratio (volume ratio) of 1:10 once (about 20 minutes). In this cleaning operation, the cleaning operation is performed by stirring the waste and the cleaning liquid by the rotation of the rotating drum. The final washed product after machine washing is thrown into the landfill.
[0021]
The stabilization index of the waste obtained by this washing is as follows for each component amount in the filtered water obtained by filtering the washing waste water after the final washing operation.
EC (electrical conductivity) ≦ 1500 μs / cm
Pb ≦ 0.1ppm
DXN (dioxins) content ≦ 10 ng-TEQ / g
That is, the DXN (dioxins) content is extremely small compared to the previous embodiment.
[0022]
【The invention's effect】
As described above, according to the present invention, waste is pretreated before being put into a landfill, and salts, heavy metals and dioxins contained in the waste are removed in advance. It does not elute in water, and the time required from the start of operation of the landfill site to closure can be shortened.
[Brief description of the drawings]
FIG. 1 is a flow sheet showing a processing method in an embodiment of the present invention.
FIG. 2 is a flow sheet showing a processing method in another embodiment of the present invention.
[Explanation of symbols]
1 Landfill waste 2 Crushing process 3 Machine washing process 4 Separation and removal process

Claims (1)

埋立地へ投入するに先立って廃棄物を前処理するものであって、細かく破砕した廃棄物を前段の機械洗浄工程において水で洗浄することにより廃棄物中の有機物、重金属、ダイオキシン類を洗浄液中に溶出させ、この洗浄廃水を分離除去工程で固液分離して得られる固形物と前段の機械洗浄工程における前段洗浄物とを後段の機械洗浄工程において有機溶媒で洗浄することにより廃棄物に残留するダイオキシン類を洗浄液中に溶出させ、後段の機械洗浄工程における後段洗浄物を前段の機械洗浄工程に再度投入して水で洗浄し、この機械洗浄後の最終洗浄物を埋立地へ投入し、分離除去工程の脱離液および後段の機械洗浄工程の洗浄廃水を埋立地の浸出水処理施設で水処理することを特徴とする埋立地の安定化方法。 Waste is pretreated before being put into the landfill, and finely crushed waste is washed with water in the previous mechanical washing process to remove organic matter, heavy metals, and dioxins in the washing solution. The solid waste obtained by solid-liquid separation in the separation and removal process and the pre-wash in the previous mechanical washing process are washed with an organic solvent in the post-mechanical washing process to remain in the waste. Dioxins to be eluted in the cleaning liquid, the latter-stage washing product in the latter-stage machine washing step is again put into the former-stage machine washing step and washed with water, and the final washing item after this machine washing is thrown into the landfill. A landfill stabilization method characterized in that the desorbed liquid in the separation and removal process and the washing wastewater in the subsequent mechanical washing process are treated with a leachate treatment facility at the landfill.
JP2000159282A 2000-05-30 2000-05-30 Landfill stabilization methods Expired - Fee Related JP3778775B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000159282A JP3778775B2 (en) 2000-05-30 2000-05-30 Landfill stabilization methods

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000159282A JP3778775B2 (en) 2000-05-30 2000-05-30 Landfill stabilization methods

Publications (2)

Publication Number Publication Date
JP2001334231A JP2001334231A (en) 2001-12-04
JP3778775B2 true JP3778775B2 (en) 2006-05-24

Family

ID=18663623

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000159282A Expired - Fee Related JP3778775B2 (en) 2000-05-30 2000-05-30 Landfill stabilization methods

Country Status (1)

Country Link
JP (1) JP3778775B2 (en)

Also Published As

Publication number Publication date
JP2001334231A (en) 2001-12-04

Similar Documents

Publication Publication Date Title
CN104889149B (en) Ectopic classification leaching repair complete process of arsenic and heavy metal contaminated soil
CN102745872B (en) Treatment method and device for riverway and lake heavy metal pollution bottom sludge
CN112371714A (en) Remediation method for treating contaminated site soil
US6123483A (en) Method and apparatus for decontaminating soil and mud polluted with hazardous waste and petroleum products
CN204620627U (en) A kind of soil heterotopic elution circuit
JP4464075B2 (en) Purification method for contaminated soil
JPH06114294A (en) Method and device for treatment of muddy water or sand and soil-containing material
JP3778775B2 (en) Landfill stabilization methods
CN105967496B (en) A kind of harmless treatment method of high-salt sludge
JP2004358347A5 (en)
JP3439636B2 (en) Early stable landfill method
CN102020403A (en) Sludge purification treatment method and device
JP2007069185A (en) Inorganic cleaning method
JP3664399B2 (en) Organic wastewater and sludge treatment method and treatment equipment
KR200422043Y1 (en) Sludge Removal and Sewage Treatment System of Dredged Soil
CN213113013U (en) Canal bottom mud treatment device
JP2000061421A (en) Waste treatment method
JP3683202B2 (en) Wastewater treatment equipment
JP4436953B2 (en) Waste disposal method
CN121060926B (en) Coupling method for cleaning waste plastics and recycling humus soil by utilizing landfill leachate
JP3916524B2 (en) Waste cleaning equipment
JP3145025B2 (en) Method and apparatus for treating radioactive waste liquid containing surfactant
JP4409083B2 (en) Waste final disposal site
JP2002059106A (en) Incineration ash disposal method and final waste disposal site
KR20080042268A (en) River sludge treatment system and method

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040427

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20051108

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20051228

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060131

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060228

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees