JP4459479B2 - Mobile solvent regenerator - Google Patents

Mobile solvent regenerator Download PDF

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Publication number
JP4459479B2
JP4459479B2 JP2001175581A JP2001175581A JP4459479B2 JP 4459479 B2 JP4459479 B2 JP 4459479B2 JP 2001175581 A JP2001175581 A JP 2001175581A JP 2001175581 A JP2001175581 A JP 2001175581A JP 4459479 B2 JP4459479 B2 JP 4459479B2
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Japan
Prior art keywords
solvent
tank
regenerated
contaminated
regeneration
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JP2002362215A (en
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雄二 杉田
伸夫 篠原
博之 伊藤
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Chubu Electric Power Co Inc
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Chubu Electric Power Co Inc
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Description

【0001】
【発明の属する技術分野】
本発明は、汚れ成分が溶解している石油系溶剤等の汚染溶剤、例えば使用済みの洗浄用溶剤等をリサイクル使用できるように再生するための移動型の溶剤再生装置に関するものである。
【0002】
【従来の技術】
工場設備を石油系溶剤等の洗浄剤で洗浄することで、油等の汚れ成分によって汚染された溶剤が多量に発生する。従来からこうした洗浄用溶剤は大量に使用する事業所などでは、溶剤再生装置を設置しリサイクルすることも行われていたが、使用量が少量の場合や、工場、発電所等の洗浄剤を使用する事業所が各地に点在しているような場合には、各事業所毎に溶剤再生装置を据え付けていたのでは、全体として非常に多くの設備コストを要し、無駄が生じるものであった。このため多くは産業廃棄物として廃棄処理されていた。
【0003】
【発明が解決しようとする課題】
そこで本発明は、事業所毎に設備する必要がない移動型の溶剤再生装置を提供し、溶剤再生に要するコストや廃棄処理に要するコストを削減できるようにするとともに、使用済み溶剤のリサイクルを促進し、資源の有効活用を図ることを目的とするものである。
また、本発明は溶剤再生装置を移動するのに伴う可燃性溶剤の安全性を高め、かつ簡易な構成の移動型の溶剤再生装置を提供することを目的とするものである。
【0004】
【課題を解決するための手段】
そのために、本発明に係る移動型の溶剤再生装置は、汚れ成分が溶解した汚染溶剤を貯留する汚染溶剤タンクと、該汚染溶剤タンクから供給された汚染溶剤を加熱し蒸留する蒸留釜と、該蒸留釜で気化した溶剤を冷却水により冷却することで液化再生する復液器と、再生された溶剤を貯留する再生溶剤タンクとを移動車の荷室に搭載して稼働可能に配管するとともに、該蒸留釜、該復液器や該配管など装置内の溶剤の流通経路に溶剤再生後残留する溶剤の残留液を抜き取るための抜き取り手段と、該装置内の溶剤の流通経路を不活性ガスに置換するための不活性ガス供給手段を備えて成ることを特徴としている。
【0005】
該蒸留釜、該復液器や該配管など装置内の溶剤の流通経路に溶剤再生後に残留する溶剤の残留液を抜き取るための抜き取り手段と、該装置内の溶剤の流通経路を不活性ガスに置換するための不活性ガス供給手段を備えることによって、溶剤再生が終了した後において、蒸留釜、復液器、配管などの溶剤再生装置内に残留する溶剤の残留液は抜き取られるとともに、抜き取り後に残留する溶剤の可燃性ガスは安定な不活性ガスに置換される。
これにより溶剤再生後の移動時において、装置内は安定な不活性ガスで充填されて装置内に可燃性ガスが残ることなく、安全性を高めることができる。また、再生されるべき溶剤が、品種や汚染の状況が異なるなどこれまで処理した溶剤とは異種のものであるときに、前記抜き取り手段を用いることによって、これまでの残留液を回収でき、新たな再生時に異種溶剤の混入が防止でき、種々の品種の溶剤の再生に対応できる。
【0006】
また、再生溶剤タンクは、再生された溶剤の定量計量を構造的に可能とする構成となっていることを特徴としている。すなわち、再生溶剤タンクは、所定高さに連通口を有する仕切板によって互いに隣接する第1〜第Nの枡に仕切られ、再生された溶剤を第1の枡に流し込み、順次隣接する枡に該連通口を介して貯留させ、各枡に該連通口の高さで定まる再生溶剤の所定量が計量貯留されることを特徴としている。この構成により、各枡には連通口の高さで定まる所定量が貯留することとなり、防爆構造が必要とされるセンサ類を用いる複雑な測定回路装置を用いることなく、再生溶剤タンクの構造的な工夫によって定量計量を可能とし簡易な構成の移動型の溶剤再生装置とすることができる。
【0007】
また、本発明は上記溶剤再生装置において、蒸留釜、復液器や配管など装置内の溶剤の流通経路に残留する溶剤の残留液を抜き取るための抜き取り手段としてエゼクタ方式の吸引回収装置を具備したことを特徴としている。この吸引回収装置により、簡単な構成で迅速に溶剤の残留液をほぼ完全に回収できる。これにより、再生されるべき溶剤が、品種や汚染の状況が異なるなどこれまで処理した溶剤とは異種のものであるときにもその混入が無く溶剤再生が適切に行える。
【0008】
【発明の実施の形態】
次に図面に従い洗浄用溶剤の再生について本発明の実施の形態を説明する。本発明に係る移動型の洗浄用溶剤再生装置は、図1,図2に示したように、バン型トラックのような移動車1の荷室2内に再生装置本体6,冷却器7,不活性ガスタンク8、汚染溶剤タンク9、再生溶剤タンク10等を搭載している。
【0009】
汚染溶剤タンク9と再生溶剤タンク10は室内の一側壁寄りに設けられた棚の上下段に設けられている。汚染溶剤タンク9の上面にはストレーナ11が張設され、該ストレーナ上に置かれた汚染溶剤用一斗缶12から該汚染溶剤タンク9中に汚染溶剤を流し込み得るようにしている。
【0010】
再生溶剤タンク10は、再生された溶剤の定量計量を構造的に可能とするように構成されている。すなわち、再生溶剤タンクは、仕切板によって第1〜第Nの複数の枡に仕切られ、それぞれの枡の仕切板の所定高さの位置に連通口が設けられている。再生溶剤はタンクの第1の枡に流し込まれ、所定量すなわち仕切板の連通口の高さに達すると、この連通口を介して隣の第2の枡に流れ込み、順次第3〜第Nの枡に流れ込む。各枡に溜まった所定量の溶剤は枡の下部に設けられた取り出し口を介して取り出される。各枡の貯留量は、仕切板に設けられる連通口の高さを変えることにより調整される。
【0011】
このような溶剤の定量計量は、センサ等を用いることなく簡単な構造で計量を可能とするものである。また、このようなタンク内を連通口を有する仕切板で複数の枡に仕切る形式の定量計量手段は、溶剤に限らず種々の液体の定量計量に適用できるものである。
【0012】
本発明の実施の形態において、再生溶剤タンク10内は、仕切板3によって4つの枡4に仕切られ、該仕切板3の所定高さ部分に連通口5が開設され、該各枡4の下側に夫々蛇口13が設けられ、各枡毎に18リットルの再生溶剤が溜まり、18リットルを越すと連通口5を通って隣接する枡にその再生溶剤がオーバーフローするようにしている。このため各枡4中に、定量の再生溶剤が溜まり蛇口13を開けることでその再生溶剤を適宜、再生溶剤用一斗缶14に移し替えられるようにしている。
なお、荷室2内に設けられた作業スペース25には作業員が出入りし得るように荷室背面に扉26が設けられている。
【0013】
再生装置本体6は、図3に示したように、溶剤フィルタ15と、熱交換器16と、液位調整器17と、蒸留釜18と、オイルヒータ19と、廃液タンク20と、復液器21と、水分吸着器22とからなる。溶剤フィルタ15は配管30,バルブ31を介して汚染溶剤タンク9から流入してきた汚染溶剤を通過させることにより該溶剤中の微細なゴミを捕獲するものである。また、熱交換器16は、蒸留釜18で気化し排出された溶剤蒸気を通す導気管32が貫通状に設けられ、溶剤フィルタ15を通過してきた汚染溶剤を該溶剤蒸気の排熱により予熱するものである。
【0014】
液位調整器17は蒸留釜18中の汚染溶剤の液位が一定となるようにシスターン40によって該蒸留釜に供給する汚染溶剤の量を自動調節するものである。蒸留釜18は内部に配管41が設けられ、またオイルヒータ19はそのタンク内に電熱ヒータ43を設けている。そして該電熱ヒータにより加熱したオイルをポンプ44により該配管41に循環させ、該蒸留釜18中の溶剤をその熱で気化させ、溶剤蒸気を前記導気管32を通して排出するものである。なお、ドレン栓66はオイルヒータ19のオイルを抜き取るためのものである。また、廃液タンク20は、この蒸留により該蒸留釜18中に残った廃液残査を貯留するもので、46は該廃液タンク中に配設された冷却水管である。
【0015】
また、復液器21には冷却水管50が配設され、熱交換器16を通過してきた溶剤蒸気を該冷却水管によりさらに冷却することにより液化再生させる。また、51は該復液器21の二次側に設けられたエゼクタ、52はチャッキバルブである。水分吸着器22中にはフィルタ53と冷却水管54が配設されている。そして該水分吸着器22中の溶剤をポンプ55によりエゼクタ51に循環させ、その循環する溶剤によって生じるエゼクタ効果により復液器21の液化した溶剤を水分吸着器22に導いている。そして、該水分吸着器22中から溶剤が配管56を通して前記再生溶剤タンク10に溢出し得るように構成される。
【0016】
なお、前記冷却水管46,50,54は一連のもので、前記冷却器7に配管57,58を介して連通され、該冷却器7によって冷却した冷水を水分吸着器22,復液器21,廃液タンク20の順に循環させている。また前記不活性ガスタンク8はバルブ59を開けることにより前記配管30に不活性ガス、たとえば窒素ガスを供給できるように設けられている。
【0017】
このため、設備洗浄等によって汚染された溶剤が発生した事業所にこの移動車を出張させ、その事業所から排出される汚染溶剤を入れた一斗缶12を汚染溶剤タンク9上に運んで、その汚染溶剤を汚染溶剤タンク9中に流し込む。汚染溶剤タンク9中に流し込まれた汚染溶剤は、溶剤フィルタ15,熱交換器16,液位調整器17を通って蒸留釜18に入り、オイルヒータ19により加熱されることで溶剤のみが気化し、その溶剤蒸気が導気管32を通して復液器21に導かれその冷却水管50により冷却されて液化し再生される。
【0018】
このようにして浄化再生された溶剤は、エゼクタ51によりさらに水分吸着器22中に吸引され水分が吸着された後、再生溶剤タンク10に流出する。再生溶剤タンク10に流出した再生溶剤は、連通口5をオーバーフローすることによって各枡4毎に18リットルずつ溜まる。このため、蛇口13を開けばレベル計、計量計などのセンサー類を設けることなく定量計量が可能となり、この再生溶剤用一斗缶に再生溶剤を確実に18リットルずつ移し替えることができる。
【0019】
こうして、溶剤再生を終えた後は、汚染溶剤タンク9及び再生溶剤タンク10内に残留する溶剤は拭き取りなどにより除去され、装置内の溶剤の残留液は、溶剤の流通経路である前記配管30に設けられたドレン栓60、液位調整器17に設けられたドレン栓61、復液器21に設けられたドレン栓62、水分吸着器22に設けられたドレン栓63、蒸留釜18に接続される廃液タンク20に設けられたドレン栓65、および配管56に設けられたドレン栓64を開けて、溶剤の残留液をとりだす。
【0020】
溶剤の残留液の抜き取り操作は、抜き取り手段としての上記各ドレン栓を開放し滴下する残留液を容器で回収することで行えるが、各ドレン栓に夫々エゼクタ方式の吸引回収装置を順に接続して抜き取り手段を構成し、各機器を含め溶剤流通経路内の残留液を該各ドレン栓60、61、62、63、64、65から排出させることが、簡易な構成で残留液を迅速にかつほぼ完全に排出させることができる点で好ましい。なお、各ドレン栓への吸引回収装置を順に接続することに代えて、各ドレン栓60〜65に個別に吸引回収装置を設けても良いし、各ドレン栓に共通して吸引回収装置を設けてもよい。
【0021】
エゼクタ方式の吸引回収装置とは、圧縮空気等による噴射エネルギーによるエゼクタ効果により残留液を回収するものをいい、その一例を図4に示す。
図4において、入り口弁68から圧縮空気等を超音速流でノズル69を介してエゼクタ本体70内に噴出させ、溶剤再生装置の各ドレン栓60〜65に接続されたエゼクタ本体70のドレン栓67より、随伴流として溶剤の残留液をエゼクタ本体70に吸引する。吸引された残留液と噴出流の混合液体は、残留溶剤回収筒71内に吐出し、吸引された溶剤の残留液は回収バルブ73より回収され、圧縮空気等は、出口バルブ72から排出される。
抜き取り手段は、このようなエゼクタ方式の吸引回収装置の他、各ドレン栓60〜65に吸引ブロアや真空ポンプを接続することにより構成してもよい。
【0022】
溶剤の残留液の回収の後、バルブ31を閉じ不活性ガスタンクのバルブ59を開け、不活性ガス例えば窒素ガスを配管30から溶剤フィルタ15,熱交換器16,液位調整器17、蒸留釜18に供給し、さらに導気管32、復液器21、および水分吸着器22、更には廃液タンク20および各配管など装置内の溶剤の流通経路となる配管及び機器に窒素ガスが行き渡るようにすることで、この流通経路中を窒素ガスによって満たすようにする。
【0023】
このようにこの流通経路中を窒素ガス等の不活性ガスによって満たすことにより、溶剤の可燃性ガスが空気と混合して爆発するおそれがなくなり、溶剤再生を必要とする事業所から事業所へ安全に移動できるようになる。
なお、本実施の形態においては、洗浄用溶剤の再生について説明したが、本発明は、洗浄用溶剤に限らず、汚染された溶剤や再生可能な使用済の溶剤の再生に同様に適用できるものである。
【0024】
【発明の効果】
このように本発明に係る移動型の溶剤再生装置は、汚れ成分が溶解した汚染溶剤を貯留する汚染溶剤タンクと、該汚染溶剤タンクから供給された汚染溶剤を加熱し蒸留する蒸留釜と、該蒸留釜で気化した溶剤を冷却水により冷却することで液化再生する復液器と、再生された溶剤を貯留する再生溶剤タンクとを移動車の荷室に搭載して稼働可能に配管するとともに、該蒸留釜、該復液器や該配管など装置内の溶剤の流通経路に溶剤再生後残留する溶剤の残留液を抜き取るための手段と、該流通経路内を不活性ガスに置換するための不活性ガス供給手段を備えて構成されているので、溶剤再生装置の使用後において溶剤の流通経路は残留液が除去され、不活性ガスで置換することができ、不活性ガスで置換することにより溶剤の爆発のおそれなく安全に移動でき、工場、営業所、発電所等の溶剤再生の需要に低コストで産業廃棄物の削減に応じられるようにする有益な効果がある。
【0025】
また、再生溶剤タンクは定量計量を構造的に可能な構成となっており、レベル計、計量計などのセンサー類を設けることなく、簡易な構造の定量計量装置であるため、防爆仕様が不要であり低コストで故障の心配がなく、メンテナンスの必要がない。
【図面の簡単な説明】
【図1】本発明の実施の形態を示した移動車の縦断面図。
【図2】図1の移動車の水平断面平面図。
【図3】本発明の実施の形態を示した洗浄用溶剤再生装置の配管フロー図。
【図4】エゼクタ方式の吸引回収装置の模式図。
【符号の説明】
1 移動車
2 荷室
3 仕切板
4 枡
5 連通口
6 再生装置本体
7 冷却器
8 不活性ガスタンク
9 汚染溶剤タンク
10 再生溶剤タンク
15 溶剤フィルタ
16 熱交換器
17 液位調整器
18 蒸留釜
19 オイルヒータ
20 廃液タンク
21 復液器
22 水分吸着器
70 エゼクタ本体
71 残留溶剤回収筒
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a mobile solvent recycling apparatus for recycling a contaminated solvent such as a petroleum solvent in which a soil component is dissolved, for example, a used cleaning solvent so that it can be recycled.
[0002]
[Prior art]
By washing factory equipment with cleaning agents such as petroleum solvents, a large amount of solvent contaminated by dirt components such as oil is generated. Conventionally, in business establishments that use a large amount of such cleaning solvents, solvent recycling equipment has been installed and recycled. However, when the amount used is small, cleaning agents from factories and power plants are used. If there are many offices to be scattered around, installing a solvent recycling device at each office would require a large amount of equipment costs as a whole, resulting in waste. It was. For this reason, many were disposed of as industrial waste.
[0003]
[Problems to be solved by the invention]
Therefore, the present invention provides a mobile solvent recycling device that does not need to be installed at each office, and can reduce the cost required for solvent recycling and disposal, and promote the recycling of used solvents. The purpose is to make effective use of resources.
It is another object of the present invention to provide a mobile solvent regenerator having a simple structure that increases the safety of the combustible solvent that accompanies the movement of the solvent regenerator.
[0004]
[Means for Solving the Problems]
For this purpose , a mobile solvent regenerator according to the present invention includes a contaminated solvent tank that stores a contaminated solvent in which a soil component is dissolved, a distillation pot that heats and distills the contaminated solvent supplied from the contaminated solvent tank, and A condenser that liquefies and regenerates by cooling the solvent vaporized in the distillation kettle with cooling water and a regenerated solvent tank that stores the regenerated solvent are installed in the cargo compartment of a moving vehicle and are operatively piped. Extraction means for extracting the residual liquid of the solvent remaining after the regeneration of the solvent in the solvent flow path in the apparatus such as the distillation pot, the condenser and the pipe, and the solvent flow path in the apparatus as an inert gas It is characterized by comprising an inert gas supply means for replacement.
[0005]
Extraction means for extracting the residual liquid of the solvent remaining after the regeneration of the solvent in the flow path of the solvent in the apparatus such as the distillation pot, the condenser or the pipe, and the flow path of the solvent in the apparatus to an inert gas By providing an inert gas supply means for replacement, after the solvent regeneration is completed, the residual solvent remaining in the solvent regeneration device such as a distillation still, condenser, piping, etc. is withdrawn and after withdrawal The remaining solvent combustible gas is replaced with a stable inert gas.
Thereby, at the time of movement after solvent regeneration, the inside of the apparatus is filled with a stable inert gas, and the combustible gas does not remain in the apparatus, so that safety can be improved. In addition, when the solvent to be regenerated is a different type of solvent that has been treated so far, such as different varieties and contamination conditions, the previous residual liquid can be recovered by using the extraction means, and a new Thus, it is possible to prevent the mixing of different solvents during the regeneration, and to cope with the regeneration of various types of solvents.
[0006]
In addition, the recycled solvent tank is characterized by having a structure that enables quantitative measurement of the recycled solvent. That is, the regenerated solvent tank is partitioned into first to Nth ridges adjacent to each other by a partition plate having a communication port at a predetermined height, and the regenerated solvent is poured into the first basin and the A predetermined amount of the regenerated solvent determined by the height of the communication port is metered and stored in each basket. With this configuration, a predetermined amount determined by the height of the communication port is stored in each rod, and the structure of the recycled solvent tank can be obtained without using a complicated measurement circuit device that uses sensors that require an explosion-proof structure. By a simple device, quantitative measurement can be performed, and a mobile solvent regenerator having a simple configuration can be obtained.
[0007]
The present invention also includes an ejector-type suction recovery device as an extraction means for extracting a residual solvent solution remaining in a solvent flow path in the apparatus such as a distillation still, a condenser, or a pipe in the solvent regeneration apparatus. It is characterized by that. With this suction and recovery device, the solvent residual liquid can be recovered almost completely quickly with a simple configuration. As a result, even when the solvent to be regenerated is different from the solvent treated so far, such as different varieties and contamination conditions, the solvent can be regenerated appropriately without mixing.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
Next, an embodiment of the present invention will be described with respect to the regeneration of the cleaning solvent according to the drawings. As shown in FIG. 1 and FIG. 2, the mobile cleaning solvent regenerator according to the present invention has a regenerator main body 6, a cooler 7, An active gas tank 8, a contaminated solvent tank 9, a regenerated solvent tank 10 and the like are mounted.
[0009]
The contaminated solvent tank 9 and the regenerated solvent tank 10 are provided on the upper and lower stages of a shelf provided near one side wall of the room. A strainer 11 is stretched on the upper surface of the contaminated solvent tank 9 so that the contaminated solvent can be poured into the contaminated solvent tank 9 from a canister 12 for contaminated solvent placed on the strainer.
[0010]
The regenerated solvent tank 10 is configured so as to structurally enable the quantitative measurement of the regenerated solvent. In other words, the recycled solvent tank is partitioned into a plurality of first to Nth bowls by the partition plate, and a communication port is provided at a predetermined height position of the partition plate of each bowl. The regenerated solvent is poured into the first tank of the tank. When a predetermined amount, that is, the height of the communication port of the partition plate is reached, the recycled solvent flows into the adjacent second tank through the communication port. It flows into the cage. A predetermined amount of the solvent accumulated in each basket is taken out through a take-out port provided at the bottom of the bowl. The storage amount of each bag is adjusted by changing the height of the communication port provided in the partition plate.
[0011]
Such quantitative measurement of the solvent enables measurement with a simple structure without using a sensor or the like. Further, such a quantitative metering means of partitioning the inside of the tank into a plurality of baskets with a partition plate having a communication port is applicable not only to the solvent but also to the quantitative metering of various liquids.
[0012]
In the embodiment of the present invention, the regenerated solvent tank 10 is partitioned into four cages 4 by the partition plate 3, and a communication port 5 is opened at a predetermined height portion of the partition plate 3. A faucet 13 is provided on each side, and 18 liters of regenerated solvent is accumulated in each tub. After 18 liters, the regenerated solvent overflows to the adjacent tub through the communication port 5. For this reason, a fixed amount of regenerated solvent accumulates in each basket 4, and the regenerated solvent can be appropriately transferred to the regenerated solvent funnel 14 by opening the tap 13.
Note that a door 26 is provided on the rear surface of the luggage room so that workers can enter and leave the work space 25 provided in the luggage room 2.
[0013]
As shown in FIG. 3, the regenerator main body 6 includes a solvent filter 15, a heat exchanger 16, a liquid level adjuster 17, a distillation pot 18, an oil heater 19, a waste liquid tank 20, and a condenser. 21 and a moisture adsorber 22. The solvent filter 15 captures fine dust in the solvent by allowing the contaminated solvent flowing from the contaminated solvent tank 9 to pass through the pipe 30 and the valve 31. Further, the heat exchanger 16 is provided with an air guide pipe 32 through which the solvent vapor vaporized and discharged in the distillation pot 18 passes, and preheats the contaminated solvent that has passed through the solvent filter 15 by exhaust heat of the solvent vapor. Is.
[0014]
The liquid level adjuster 17 automatically adjusts the amount of the contaminated solvent supplied to the still with the cistern 40 so that the level of the contaminated solvent in the still 18 is constant. The distillation kettle 18 is provided with a pipe 41 inside, and the oil heater 19 is provided with an electric heater 43 in its tank. Then, the oil heated by the electric heater is circulated through the pipe 41 by the pump 44, the solvent in the distillation pot 18 is vaporized by the heat, and the solvent vapor is discharged through the air conduit 32. The drain plug 66 is for extracting oil from the oil heater 19. The waste liquid tank 20 stores the waste liquid residue remaining in the distillation still 18 by this distillation, and 46 is a cooling water pipe disposed in the waste liquid tank.
[0015]
Further, the condenser 21 is provided with a cooling water pipe 50, and the solvent vapor that has passed through the heat exchanger 16 is further cooled by the cooling water pipe to be liquefied and regenerated. Further, 51 is an ejector provided on the secondary side of the condenser 21, and 52 is a check valve. A filter 53 and a cooling water pipe 54 are disposed in the moisture adsorber 22. The solvent in the moisture adsorber 22 is circulated to the ejector 51 by the pump 55, and the liquefied solvent in the condenser 21 is guided to the moisture adsorber 22 by the ejector effect generated by the circulating solvent. The solvent is allowed to overflow from the moisture adsorber 22 to the regenerated solvent tank 10 through the pipe 56.
[0016]
The cooling water pipes 46, 50, 54 are a series, and are communicated with the cooler 7 via pipes 57, 58, and the cold water cooled by the cooler 7 is supplied to the moisture adsorber 22, the condenser 21, The waste liquid tank 20 is circulated in this order. The inert gas tank 8 is provided so that an inert gas such as nitrogen gas can be supplied to the pipe 30 by opening the valve 59.
[0017]
For this reason, this traveling vehicle is made a business trip to the establishment where the solvent polluted by the equipment washing or the like is generated, and the canister 12 containing the contaminated solvent discharged from the establishment is carried onto the contaminated solvent tank 9, The contaminated solvent is poured into the contaminated solvent tank 9. The contaminated solvent poured into the contaminated solvent tank 9 passes through the solvent filter 15, the heat exchanger 16, and the liquid level adjuster 17, enters the distillation pot 18, and is heated by the oil heater 19 so that only the solvent is vaporized. The solvent vapor is led to the condenser 21 through the air conduit 32 and cooled by the cooling water pipe 50 to be liquefied and regenerated.
[0018]
The solvent purified and regenerated in this way is further sucked into the moisture adsorber 22 by the ejector 51 to adsorb moisture, and then flows out into the regeneration solvent tank 10. The regenerated solvent that has flowed into the regenerated solvent tank 10 overflows the communication port 5 and accumulates 18 liters for each basket 4. For this reason, if the faucet 13 is opened, quantitative measurement can be performed without providing sensors such as a level meter and a meter, and the regenerated solvent can be reliably transferred to the regenerated solvent funnel 18 liters at a time.
[0019]
Thus, after the solvent regeneration is completed, the solvent remaining in the contaminated solvent tank 9 and the regeneration solvent tank 10 is removed by wiping or the like, and the solvent residual liquid in the apparatus is put into the pipe 30 which is a solvent flow path. It is connected to the drain plug 60 provided, the drain plug 61 provided in the liquid level adjuster 17, the drain plug 62 provided in the condenser 21, the drain plug 63 provided in the moisture adsorber 22, and the distillation pot 18. The drain plug 65 provided in the waste liquid tank 20 and the drain plug 64 provided in the pipe 56 are opened, and the solvent residual liquid is taken out.
[0020]
The residual solvent can be drained by opening the drain plugs as the draining means and collecting the residual liquid to be dropped in a container. Ejector-type suction and recovery devices are connected to the drain stoppers in order. It constitutes a drawing means, and the residual liquid in the solvent flow path including each device can be discharged from each drain plug 60, 61, 62, 63, 64, 65. This is preferable in that it can be completely discharged. Instead of connecting the suction recovery devices to each drain plug in order, a suction recovery device may be provided for each drain plug 60 to 65, or a suction recovery device is provided in common for each drain plug. May be.
[0021]
An ejector-type suction recovery device refers to a device that recovers a residual liquid by an ejector effect caused by jet energy such as compressed air, and an example thereof is shown in FIG.
In FIG. 4, compressed air or the like is jetted from an inlet valve 68 into the ejector body 70 through a nozzle 69 in a supersonic flow, and drain plugs 67 of the ejector body 70 connected to the drain plugs 60 to 65 of the solvent regeneration device. Thus, the residual solvent is sucked into the ejector body 70 as an accompanying flow. The sucked residual liquid and the mixed liquid of the jet flow are discharged into the residual solvent recovery cylinder 71, the residual solvent liquid sucked is recovered from the recovery valve 73, and the compressed air and the like are discharged from the outlet valve 72. .
The extraction means may be constituted by connecting a suction blower or a vacuum pump to each drain plug 60 to 65 in addition to such an ejector type suction recovery device.
[0022]
After collecting the residual solvent, the valve 31 is closed and the valve 59 of the inert gas tank is opened. An inert gas such as nitrogen gas is supplied from the pipe 30 to the solvent filter 15, heat exchanger 16, liquid level adjuster 17, and still 18. In addition, the nitrogen gas is allowed to reach the pipes and equipment that serve as a flow path for the solvent in the apparatus, such as the conduit 32, the condenser 21, and the moisture adsorber 22, and the waste liquid tank 20 and each pipe. Then, the distribution channel is filled with nitrogen gas.
[0023]
By filling this distribution channel with inert gas such as nitrogen gas in this way, there is no risk of the solvent flammable gas mixing with the air and exploding, and it is safe from establishment to establishment that requires solvent regeneration. Will be able to move to.
In this embodiment, the regeneration of the cleaning solvent has been described. However, the present invention is not limited to the cleaning solvent, but can be similarly applied to the regeneration of a contaminated solvent or a reusable used solvent. It is.
[0024]
【The invention's effect】
As described above, the mobile solvent regenerator according to the present invention includes a contaminated solvent tank that stores a contaminated solvent in which a contaminated component is dissolved, a distillation pot that heats and distills the contaminated solvent supplied from the contaminated solvent tank, and A condenser that liquefies and regenerates by cooling the solvent vaporized in the distillation kettle with cooling water and a regenerated solvent tank that stores the regenerated solvent are installed in the cargo compartment of a moving vehicle and are operatively piped. Means for extracting the residual liquid of the solvent remaining after the regeneration of the solvent in the flow path of the solvent in the apparatus such as the distillation pot, the condenser or the pipe, and an inert gas for substituting the inert flow in the flow path. Since it comprises an active gas supply means, after use of the solvent regeneration device, the solvent flow path can be replaced with an inert gas after the residual liquid is removed, and the solvent can be replaced by an inert gas. May explode Safely can be moved, factories, sales offices, there is a beneficial effect to ensure that is depending on the reduction of industrial waste at a low cost to the demand for solvent regeneration, such as power plants.
[0025]
In addition, the recycled solvent tank has a structure that can quantitatively measure, and it is a quantitative measuring device with a simple structure without the need for sensors such as level meters and metering meters. There is no low cost, no worry of failure, and no maintenance is required.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of a mobile vehicle showing an embodiment of the present invention.
FIG. 2 is a horizontal sectional plan view of the mobile vehicle of FIG.
FIG. 3 is a piping flow diagram of a cleaning solvent regenerator showing an embodiment of the present invention.
FIG. 4 is a schematic diagram of an ejector-type suction recovery device.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Mobile vehicle 2 Cargo compartment 3 Partition plate 4 枡 5 Communication port 6 Regenerator main body 7 Cooler 8 Inert gas tank 9 Contaminated solvent tank 10 Regenerated solvent tank 15 Solvent filter 16 Heat exchanger 17 Liquid level adjuster 18 Distilling pot 19 Oil Heater 20 Waste liquid tank 21 Condenser 22 Moisture adsorber 70 Ejector body 71 Residual solvent recovery cylinder

Claims (2)

汚れ成分が溶解した汚染溶剤を貯留する汚染溶剤タンクと、
該汚染溶剤タンクから供給された汚染溶剤を加熱し蒸留する蒸留釜と、
該蒸留釜で気化した溶剤を冷却水により冷却することで液化再生する復液器と、
再生された溶剤を貯留する再生溶剤タンクとを移動車の荷室に搭載して稼働可能に配管するとともに、該蒸留釜、該復液器や該配管など装置内の溶剤の流通経路に溶剤再生後残留する溶剤の残留液を抜き取るための抜き取り手段と、
該装置内の溶剤の流通経路を不活性ガスに置換するための不活性ガス供給手段を備え、
前記再生溶剤タンクは、所定高さに連通口を有する仕切板によって互いに隣接する第1〜第Nの枡に仕切られ、再生された溶剤を第1の枡に流し込み、順次隣接する枡に該連通口を介して貯留させ、各枡に該連通口の高さで定まる再生溶剤の所定量が計量貯留されることを特徴とする移動型の溶剤再生装置。
A contaminated solvent tank for storing a contaminated solvent in which dirt components are dissolved;
A distillation still for heating and distilling the contaminated solvent supplied from the contaminated solvent tank;
A condenser that liquefies and regenerates the solvent vaporized in the distillation kettle by cooling with cooling water;
A regenerated solvent tank for storing regenerated solvent is installed in the cargo compartment of a moving vehicle and operatively piped, and the solvent is regenerated in the solvent flow path in the apparatus such as the distillation tank, the condenser and the pipe. Extraction means for extracting residual liquid of the solvent remaining after,
An inert gas supply means for replacing the flow path of the solvent in the apparatus with an inert gas;
The regenerated solvent tank is partitioned into first to Nth ridges adjacent to each other by a partition plate having a communication port at a predetermined height, and the regenerated solvent is poured into the first tub and sequentially communicated with the adjacent tubs. A mobile solvent regeneration apparatus characterized in that a predetermined amount of a regeneration solvent which is stored through a mouth and determined by the height of the communication port is measured and stored in each basket .
蒸留釜、復液器や配管など装置内の溶剤流通経路に溶剤再生後残留する溶剤の残留液を抜き取るための抜き取り手段としてエゼクタ方式の吸引回収装置を具備した請求項1に記載の移動型の溶剤再生装置。  The movable type of claim 1, comprising an ejector-type suction recovery device as extraction means for extracting residual solvent remaining after solvent regeneration in a solvent flow path in the apparatus such as a distillation pot, condenser or piping. Solvent regenerator.
JP2001175581A 2001-06-11 2001-06-11 Mobile solvent regenerator Expired - Lifetime JP4459479B2 (en)

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