JPS63232898A - Method and device for treating sludge containing organochlorine solvent - Google Patents

Method and device for treating sludge containing organochlorine solvent

Info

Publication number
JPS63232898A
JPS63232898A JP9321487A JP9321487A JPS63232898A JP S63232898 A JPS63232898 A JP S63232898A JP 9321487 A JP9321487 A JP 9321487A JP 9321487 A JP9321487 A JP 9321487A JP S63232898 A JPS63232898 A JP S63232898A
Authority
JP
Japan
Prior art keywords
sludge
extractor
vapor
solvent
perchlorethylene
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.)
Granted
Application number
JP9321487A
Other languages
Japanese (ja)
Other versions
JPH0355200B2 (en
Inventor
Nobuyuki Kanbara
暢幸 神原
Masatoki Matsuki
松木 政時
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.)
TSUNEISHI ZOSEN KK
Original Assignee
TSUNEISHI ZOSEN KK
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 TSUNEISHI ZOSEN KK filed Critical TSUNEISHI ZOSEN KK
Publication of JPS63232898A publication Critical patent/JPS63232898A/en
Publication of JPH0355200B2 publication Critical patent/JPH0355200B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently recover an organochlorine solvent in a short time by heating and agitating the sludge contg. the organochlorine solvent in an extractor, introducing the generated organochlorine solvent vapor into a cooler along with the steam introduced into the extractor and condensing the vapor. CONSTITUTION:The sludge contg. an organochlorine solvent such as perchloroethylene is heated and agitated in the extractor 2, the generated organochlorine solvent vapor is sent to the cooler 10 along with the steam introduced into the extractor 2, and the vapor is condensed. As a result, the organochlorine solvent is efficiently recovered in a short time, and can be reutilized. The sludge freed from the organochlorine solvent can be safely used for land reclamation, and the environmental pollution such as ground water pollution and air pollution can be obviated.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は、有機塩素系溶剤の再生に伴って発生する汚泥
、タンカーやタンクローリ−等の輸送装置の洗浄水から
溶剤を分離回収する際に発生ずる汚泥、更には貯蔵容器
等から゛発生する汚泥等から有機塩素系溶剤を回収する
汚泥の処理方法及び装置に関する。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention is directed to the treatment of sludge generated during the regeneration of organic chlorine solvents, which is generated when separating and recovering solvents from washing water of transport equipment such as tankers and tank trucks. The present invention relates to a sludge treatment method and apparatus for recovering organic chlorine solvents from the sludge generated, and further from the sludge generated from storage containers and the like.

〔従来技術〕[Prior art]

有機塩素系溶剤を含有する汚泥は従来産業廃棄物として
焼却され管理型埋立て地へ捨てられていたが、焼却炉の
腐食が著しく、かつ大気汚染を伴う等の欠点があった。
Conventionally, sludge containing organic chlorine solvents has been incinerated as industrial waste and disposed of in controlled landfills, but this has disadvantages such as severe corrosion in the incinerator and air pollution.

例えば、ドライクリーニングの溶剤として用いられるパ
ークロルエチレンは、クリーニング排出汚泥中に重量比
で約40〜50%含まれている。
For example, perchlorethylene, which is used as a solvent in dry cleaning, is contained in cleaning discharge sludge in an amount of about 40 to 50% by weight.

この汚泥は、従来産業廃棄物として焼却後管理型の埋立
て地へ捨てることになっているが、最近パークロルエチ
レンによる地下水汚染及びその発ガン性が問題となり、
クリーニング排出汚泥を回収し、安全に処理することか
にわかに問題となってきている。
Conventionally, this sludge has been disposed of as industrial waste in a controlled landfill after incineration, but recently, groundwater contamination by perchlorethylene and its carcinogenicity have become a problem.
Collecting and safely disposing of cleaning discharge sludge is rapidly becoming a problem.

汚泥中のパークロルエチレンを回収する方法としては、
蒸留法が知られており、第2図はバ−クロルエチレンを
含む汚泥からパークロルエチレンを蒸留する従来の装置
の概略図であり、汚泥加熱タンク21にパークロルエチ
レンを含む汚泥を入れ、加熱器22で加熱することによ
り発生したパークロルエチレン蒸気は冷却塔23に入り
、冷却管24で冷却され、液体となって排出管25から
取出されるようになっている。
As a method to recover perchlorethylene in sludge,
A distillation method is known, and FIG. 2 is a schematic diagram of a conventional apparatus for distilling perchlorethylene from sludge containing perchlorethylene. Sludge containing perchlorethylene is put into a sludge heating tank 21 and heated. Perchlorethylene vapor generated by heating in the vessel 22 enters a cooling tower 23, is cooled in a cooling pipe 24, becomes liquid, and is taken out from a discharge pipe 25.

上記のごとき従来の蒸留法では、ある程度まで蒸発する
と、それより内部がパークロルエチレンの沸点、即ち1
21.2℃まで温度があがらず、汚泥内部にパークロル
エチレンが残ってしまうという欠点があった。
In the conventional distillation method as described above, after evaporation reaches a certain point, the inside reaches the boiling point of perchlorethylene, that is, 1
There was a drawback that the temperature did not rise to 21.2°C and perchlorethylene remained inside the sludge.

〔発明の目的〕[Purpose of the invention]

本発明は前記従来の欠点を解消するためになされたもの
であり、汚泥中より有機塩素系溶剤を殆んど全量回収、
再利用を可能とし廃棄物による地下水汚染、大気汚染等
の公害防止を計ることを目的としたものである。
The present invention was made in order to eliminate the above-mentioned conventional drawbacks, and it is possible to recover almost the entire amount of organic chlorine solvent from sludge,
The purpose is to enable reuse and prevent pollution such as groundwater pollution and air pollution due to waste.

〔発明の構成〕[Structure of the invention]

上記の目的を達成するため、本発明は、有機塩素系溶剤
、例えばトリクロルエチレン、塩化メチレン、1−1−
11−リクロルエタン及びパークロルエチレン等を含有
する汚泥を、それらの有機塩素系溶剤の沸点以上に加熱
しながら攪拌し、汚泥中に液体で存在している汚泥をi
[I <粉砕することで、汚泥を有機塩素系溶剤を容易
に分離可能な状態にする。そして加熱、攪拌によって発
生した有機塩素系溶剤蒸気の大部分を回収する。密閉容
器内の空間及び汚泥本体内の空間に残留する有機塩素系
溶剤蒸気を、密閉容器内に水蒸気を供給し有機塩素系溶
剤蒸気と置換排出することによって、その殆んど全てを
回収再利用を可能とした。
In order to achieve the above object, the present invention uses organic chlorine solvents such as trichlorethylene, methylene chloride, 1-1-
Sludge containing 11-lichloroethane, perchlorethylene, etc. is stirred while being heated above the boiling point of the organic chlorine solvent, and the sludge existing in liquid form in the sludge is i.
[I <By pulverizing, the sludge is made into a state in which the organic chlorine solvent can be easily separated. Most of the organic chlorine solvent vapor generated by heating and stirring is then recovered. Almost all of the organic chlorine solvent vapor remaining in the space inside the sealed container and the space within the sludge body can be recovered and reused by supplying water vapor into the sealed container and discharging it to replace the organic chlorine solvent vapor. made possible.

〔実施例〕〔Example〕

以下図面を参照して本発明の方法及び装置を適用した実
施例を説明するが、第1図は本発明の一実施例における
パークロルエチレンに有汚泥処理装置の概略系統図であ
る。
Embodiments to which the method and apparatus of the present invention are applied will be described below with reference to the drawings. FIG. 1 is a schematic diagram of an apparatus for treating perchlorethylene with sludge in an embodiment of the present invention.

この装置は、内筒2A、外筒2Bからなる2重槽になっ
た抽出器2と、冷却器10に分かれており、抽出器2の
内筒2A中に設けた攪拌機9でパークロルエチレンを含
む汚泥を攪拌しながら外面よりの水蒸気Sによる加熱に
よりパークロルエチレンの沸点まで温度を上げてパーク
ロルエチレン蒸気とし、更に汚泥空間中、及び容器空間
中に存在するパークロルエチレン蒸気に置換水蒸気S′
を吹き込み、パークロルエチレン蒸気を全量冷却器10
に導き凝縮し、パークロルエチレンを回収し汚泥を処理
するものである。
This device is divided into an extractor 2, which is a double tank consisting of an inner cylinder 2A and an outer cylinder 2B, and a cooler 10. Perchlorethylene is produced by a stirrer 9 installed in the inner cylinder 2A of the extractor 2. While stirring the contained sludge, the temperature is raised to the boiling point of perchlorethylene by heating with water vapor S from the outside surface to produce perchlorethylene vapor, and the perchlorethylene vapor existing in the sludge space and the container space is replaced with water vapor S. ′
The perchlorethylene vapor is blown into the cooler 10.
This system collects perchlorethylene and treats the sludge.

次に、第1図の回収装置によりパークロルエチレンを含
む汚泥からパークロルエチレンを回収する手順を説明す
ると、まず、水蒸気Sの止め弁6を開け、水蒸気Sを約
4 kg / cnlの圧力で内筒2Aと外筒2Bとの
間に供給し加熱する。
Next, to explain the procedure for recovering perchlorethylene from sludge containing perchlorethylene using the recovery device shown in Fig. 1, first, the stop valve 6 for steam S is opened, and the steam S is pumped at a pressure of about 4 kg/cnl. It is supplied between the inner cylinder 2A and the outer cylinder 2B and heated.

次に、抽出器2の蓋1を開け、抽出器2の2重槽の内筒
2A内にパークロルエチレンを含む汚泥を投入し、蓋1
を閉じて密閉する。
Next, open the lid 1 of the extractor 2, put the sludge containing perchlorethylene into the inner cylinder 2A of the double tank of the extractor 2, and
Close and seal.

次いで置換水蒸気供給弁16を開いて内筒2A内に置換
水蒸気を吹き込む。内筒2A内では、減速装置7付きの
モーター8を作動させることにより攪拌翼9が作動し、
汚泥を攪拌しながら周囲より加熱し、約121度でパー
クロルエチレン蒸気を発生し、置換水蒸気と共に冷却器
10に送られる。
Next, the displacement steam supply valve 16 is opened to blow displacement steam into the inner cylinder 2A. In the inner cylinder 2A, stirring blades 9 are operated by operating a motor 8 equipped with a speed reduction device 7.
While stirring the sludge, it is heated from the surroundings to generate perchlorethylene vapor at about 121 degrees, which is sent to the cooler 10 together with displacement steam.

冷却器10は冷却水Wcにて水冷されており、止め弁1
1を開けることにより作動し、冷却器lOで凝縮して液
化した水及びパークロルエチレンは、採取容器に回収さ
れる。
The cooler 10 is water-cooled with cooling water Wc, and the stop valve 1
1, and the water and perchlorethylene condensed and liquefied in the cooler IO are collected in a collection container.

なお、内筒2A、外筒2B間に供給された水蒸気Sはス
チームトラップ15を通り、ドレンDとなって排出され
る。
Note that the water vapor S supplied between the inner cylinder 2A and the outer cylinder 2B passes through the steam trap 15, becomes a drain D, and is discharged.

また、この2重槽になった抽出器2に蓋1を介して投入
されたパークロルエチレンを含む汚泥Mdは、処理され
た後、攪拌翼9により、処理汚泥Mcとして蓋19を取
外して排出され、パークロルエチレンを抽出した無機性
汚泥として管理型埋立て地等へ処分される。
In addition, the sludge Md containing perchlorethylene introduced into the double-tank extractor 2 through the lid 1 is treated and then discharged as treated sludge Mc by the stirring blades 9 by removing the lid 19. The sludge is then disposed of in a controlled landfill as inorganic sludge from which perchlorethylene has been extracted.

そこで、実際に実施した例として次にパークロルエチレ
ン含有汚泥についての処理した例を次に述べる。
Therefore, as an example of actual implementation, an example in which perchloroethylene-containing sludge was treated will be described next.

a、抽出容器の大きさ  内容積約25Ab、攪拌装置
 回転数  17.8R/M電動機  100Vx0.
2 KW C9汚泥投入量     約20A(20kg)d、投
入汚泥の性状(パーク含有率) 15.4%(重量比) e、加熱温度      149“C f、加熱水蒸気供給量(3,7kg/cn(G)5kg
/Hr g、置換水蒸気 ・  (大気圧) 0、2 kg/ Hr h、冷却水   〃  (15°C) 50A/Hr 1、処理時間 改正不要 j、処理した汚泥のパークロルエチレン含有量11■/
 kg 溶出試験濃度 0、036■/l このデータかられかるように、本発明方法で処理された
パークロルエチレン含有汚泥はllppmという極めて
少ない残量のパークロルエチレンが残るだけであること
がわかる。
a. Size of extraction container: Internal volume: approx. 25Ab, Stirring device: Rotation speed: 17.8R/M Electric motor: 100V x 0.
2 KW C9 sludge input amount: approx. 20A (20kg) d, properties of input sludge (park content) 15.4% (weight ratio) e, heating temperature 149"C f, heating steam supply amount (3.7kg/cn ( G) 5kg
/Hr g, displacement steam ・ (atmospheric pressure) 0.2 kg/Hr h, cooling water (15°C) 50A/Hr 1, treatment time No amendment requiredj, perchlorethylene content of treated sludge 11■/
kg elution test concentration 0.036 .mu./l As can be seen from this data, it can be seen that in the perchlorethylene-containing sludge treated by the method of the present invention, only an extremely small amount of residual perchlorethylene of 11 ppm remains.

ところが、従来の単なる加熱攪拌乾燥の場合、処理容器
内の空間及び汚泥本体内の空間に残留する有機塩素系溶
剤が凝縮し再汚染するために、1.000ppm以下に
は処理することが不可能であるのが実情である。
However, in the case of conventional simple heating and stirring drying, it is impossible to reduce the concentration to 1.000 ppm or less because the organic chlorine solvent remaining in the space inside the processing container and the space within the sludge body condenses and re-contaminates the sludge. The reality is that.

なお、トリクロロエタン、トリクロロエチレン、塩化メ
チレン等沸点の低い溶剤を含有する汚泥を本装置で処理
する場合は、加熱蒸気の供給量を制限することによって
処理温度を制御する。
When treating sludge containing a solvent with a low boiling point, such as trichloroethane, trichlorethylene, or methylene chloride, with this apparatus, the treatment temperature is controlled by limiting the amount of heated steam supplied.

〔発明の効果〕〔Effect of the invention〕

以上に説明したように、本発明の汚泥処理方法において
は、加熱する抽出器内に攪拌翼をつけることにより、汚
泥全てをむらなく攪拌し、発生した有機塩素系溶剤蒸気
は水蒸気と置換されるので、汚泥中の有機塩素系溶剤を
殆んど抽出でき、その処理汚泥を有機塩素系溶剤を抽出
した無機性汚泥として埋立て地へ埋めるので、より安全
な埋立てが可能となり、加えて従来のような焼却処理も
不必要なため、焼却時に発生する有毒ガスも出ないため
、大気汚染等公害防止にもなる等多大な効果がある。
As explained above, in the sludge treatment method of the present invention, all the sludge is evenly stirred by installing a stirring blade in the heated extractor, and the generated organic chlorine solvent vapor is replaced with water vapor. Therefore, most of the organic chlorine solvents in the sludge can be extracted, and the treated sludge is buried in the landfill as inorganic sludge from which the organic chlorine solvents have been extracted, making safer landfilling possible. Since there is no need for incineration, no toxic gas is emitted during incineration, which has great effects such as preventing air pollution and other pollution.

また、有機塩素系溶剤を含んだ汚泥を攪拌しながら直接
加熱し、かつ置換水蒸気を吹き込むため、短時間で効率
よく有機塩素系溶剤を回収して再利用が可能となるので
、より確実な汚泥の無害化ができると共に、経済的であ
る。
In addition, since the sludge containing organochlorine solvents is directly heated while stirring and displacement steam is blown into the sludge, the organochlorine solvents can be efficiently recovered and reused in a short period of time, making the sludge more reliable. It is economical as well as making it harmless.

更に、本発明で特に水蒸気を抽出器内に導入したのは、
これにより有機塩素系溶剤蒸気を抽出器内から外に排出
する効果を有すると共に、有機塩素系溶剤蒸気を薄める
ことによって抽出器以降の設備の有機塩素系溶剤による
腐食を防止し、かつ有機塩素系溶剤蒸気の完全排出の後
に水蒸気によってきれいに有機塩素系溶剤の付着分を除
去することができ、更に抽出器内に水蒸気が残留しても
無害であるという効果を有するからである。
Furthermore, in the present invention, water vapor is introduced into the extractor because
This has the effect of discharging organochlorine solvent vapor from inside the extractor to the outside, and by diluting the organochlorine solvent vapor, it prevents corrosion of equipment after the extractor due to organochlorine solvents. This is because, after the solvent vapor is completely discharged, the adhering portion of the organic chlorine solvent can be cleanly removed by the water vapor, and even if the water vapor remains in the extractor, it is harmless.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例における有機塩素系溶剤含有
汚泥の処理装置の概略系統図であり、また第2図は有機
塩素系溶剤を含む汚泥から有機塩素系溶剤を蒸留する従
来の装置の概略図である。 2・・・抽出器、9・・・攪拌機、10・・・冷却器、
S・・・水蒸気、S′・・・置換水蒸気。
FIG. 1 is a schematic system diagram of an apparatus for treating sludge containing organochlorine solvents in an embodiment of the present invention, and FIG. 2 shows a conventional apparatus for distilling organochlorine solvents from sludge containing organochlorine solvents. FIG. 2...Extractor, 9...Agitator, 10...Cooler,
S... water vapor, S'... displacement water vapor.

Claims (1)

【特許請求の範囲】 1、有機塩素系溶剤を含む汚泥を抽出器内で加熱攪拌し
、発生した有機塩素系溶剤蒸気を、抽出器内に導入した
水蒸気と共に冷却器に送って凝縮させて有機塩素系溶剤
を回収する有機塩素系溶剤を含有する汚泥の処理方法。 2、有機塩素系溶剤を含む汚泥を加熱攪拌する抽出器と
、該抽出器内に水蒸気を供給する水蒸気供給装置と、有
機塩素系溶剤蒸気及び水蒸気を凝縮する冷却器からなる
有機塩素系溶剤を含有する汚泥の処理装置。
[Claims] 1. Sludge containing an organic chlorine solvent is heated and stirred in an extractor, and the generated organic chlorine solvent vapor is sent to a cooler together with the water vapor introduced into the extractor and condensed. A method for treating sludge containing organic chlorine solvents that recovers chlorine solvents. 2. An extractor that heats and stirs sludge containing an organic chlorine solvent, a steam supply device that supplies water vapor into the extractor, and a cooler that condenses the organic chlorine solvent vapor and water vapor. Treatment equipment for the sludge it contains.
JP9321487A 1986-11-26 1987-04-17 Method and device for treating sludge containing organochlorine solvent Granted JPS63232898A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP61-279674 1986-11-26
JP27967486 1986-11-26

Publications (2)

Publication Number Publication Date
JPS63232898A true JPS63232898A (en) 1988-09-28
JPH0355200B2 JPH0355200B2 (en) 1991-08-22

Family

ID=17614284

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9321487A Granted JPS63232898A (en) 1986-11-26 1987-04-17 Method and device for treating sludge containing organochlorine solvent

Country Status (1)

Country Link
JP (1) JPS63232898A (en)

Also Published As

Publication number Publication date
JPH0355200B2 (en) 1991-08-22

Similar Documents

Publication Publication Date Title
US4715965A (en) Method for separating and recovering volatilizable contaminants from soil
CA1337481C (en) Process and apparatus for separating organic contaminants from contaminated inert materials
US5253597A (en) Process for separating organic contaminants from contaminated soils and sludges
US5756871A (en) Treating method for converting wastes into resources and its equipment
US4993873A (en) Process for treating contaminated earth
JP2003112160A (en) Polluted soil cleaning apparatus
US5811607A (en) Composite shingle particle salvage system
JPH02502395A (en) Waste treatment equipment and method
EP0502882B1 (en) Method and apparatus for cleaning drill cuttings
EP0285231A1 (en) Method and apparatus for treating mixed organic and inorganic wastes
GB2301112A (en) Recovering useful products from waste material
US5896876A (en) Method and apparatus for decontamination of poly chlorinated biphenyl contaminated soil
US6423151B1 (en) Removal of toxic contaminants from porous material
EP0588865B1 (en) Cleaning hydrocarbon contaminated material
CA3006811C (en) Wet dryer for diluent recovery
US4975195A (en) Apparatus and method for processing trap wastes and the like
JPS63232898A (en) Method and device for treating sludge containing organochlorine solvent
FI97281C (en) Method of purifying a contaminated soil material and plant for use in the method
US5922277A (en) Recycling system for hazardous waste disposal
JP2003300058A (en) Soil treating method
JP3618685B2 (en) Method and apparatus for treating organochlorine compounds in soil, solids and fly ash
JPH09155326A (en) Method for processing waste containing chlorine
US5804434A (en) Process for removing solvent from soil and debris
Trowbridge et al. Refinery sludge treatment/hazardous waste minimization via dehydration and solvent extraction
JP3692325B2 (en) Soil purification equipment