JPH0570120B2 - - Google Patents
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- Publication number
- JPH0570120B2 JPH0570120B2 JP1697385A JP1697385A JPH0570120B2 JP H0570120 B2 JPH0570120 B2 JP H0570120B2 JP 1697385 A JP1697385 A JP 1697385A JP 1697385 A JP1697385 A JP 1697385A JP H0570120 B2 JPH0570120 B2 JP H0570120B2
- Authority
- JP
- Japan
- Prior art keywords
- solvent
- distiller
- dry cleaning
- tank
- water
- 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 - Lifetime
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Detergent Compositions (AREA)
- Cleaning By Liquid Or Steam (AREA)
Description
【発明の詳細な説明】
〔発明の属する技術分野〕
本発明は溶剤を用いて衣服等を洗濯するドライ
クリーニング設備に係り、特に原子力発電所内に
て着用された放射性物質の付着している衣服等を
洗濯するためのドライクリーニング設備に関す
る。[Detailed description of the invention] [Technical field to which the invention pertains] The present invention relates to dry cleaning equipment that uses a solvent to wash clothes, etc., and in particular, to dry cleaning equipment that uses a solvent to wash clothes, etc., and particularly clothes that are worn inside a nuclear power plant and have radioactive materials attached. Regarding dry cleaning equipment for washing clothes.
この発明はドライクリーニング機を複数基と蒸
留基を一基備え、原子力発電所内で着用する衣服
などを洗濯するドライクリーニング設備におい
て、蒸留器と溶剤タンクとの間に水分離機能を有
する溶剤受槽を設けることにより蒸留器を小型に
することができるものである。
This invention is a dry cleaning facility that is equipped with multiple dry cleaning machines and one distillation machine, and is used to wash clothes worn in nuclear power plants. By providing this, the distiller can be made smaller.
従来原子力発電所内で着用した衣服などは、水
洗いによつて洗濯されていたが、放射性物質を含
んだ洗濯廃液が多量に発生し、その設備が大規模
かつ複雑となるため最近は廃水量の少いドライク
リーニング法が導入される様になつた。
Traditionally, clothes worn inside nuclear power plants were washed with water, but as large amounts of laundry waste containing radioactive materials are generated and the equipment has become large and complex, the amount of waste water has recently been reduced. A new dry cleaning method was introduced.
第2図は、一般用ドライクリーニング設備の主
要な機器構成を示し、洗濯は次の様に行われる。
衣服などの被洗濯物を洗濯ドラム1に投入し、溶
剤タンク2に貯留されている溶剤をポンプ3によ
つてフイルタ4を通して洗濯ドラム1に移送す
る。洗浄は洗濯ドラムを回転しつつポンプおよび
フイルタからなる循環系によつて溶剤を連続的に
過しながら循環する。洗浄が終了すると溶剤を
溶剤タンクに戻した後、洗濯ドラムを高速で回転
し、遠心力によつて残留する溶剤を除去する。そ
の後漏れた被洗濯物をフアン5、リントフイルタ
6、凝縮器7、およびヒータ8からなる乾燥系で
乾燥し、被洗物から出る綿ごみはリントフイルタ
によつて除去され、溶剤蒸気は凝縮器によつて凝
縮され回収される。被洗物中の汚れは主としてフ
イルタによつて除去されるが、一部は溶剤中に残
留するために一定期間洗浄後溶剤は蒸留器9およ
び水分離器10からなる蒸留系によつて蒸留し精
製され水分を分離された溶剤は溶剤タンク2に戻
されて再使用される。 FIG. 2 shows the main equipment configuration of general dry cleaning equipment, and washing is performed as follows.
Items to be washed, such as clothes, are put into a washing drum 1, and the solvent stored in a solvent tank 2 is transferred to the washing drum 1 through a filter 4 by a pump 3. During washing, the washing drum is rotated and the solvent is continuously passed through a circulation system consisting of a pump and a filter. After washing is completed, the solvent is returned to the solvent tank, and the washing drum is rotated at high speed to remove residual solvent using centrifugal force. After that, the leaked items to be washed are dried in a drying system consisting of a fan 5, a lint filter 6, a condenser 7, and a heater 8. The cotton waste from the items to be washed is removed by the lint filter, and the solvent vapor is removed by the condenser. It is condensed and collected by Dirt in the object to be washed is mainly removed by a filter, but some of it remains in the solvent, so after washing for a certain period of time, the solvent is distilled by a distillation system consisting of a distiller 9 and a water separator 10. The purified solvent from which water has been separated is returned to the solvent tank 2 and reused.
小規模の洗濯をするドライクリーニング設備は
第2図の様に単基で使用されるが、原子力発電所
の様に被洗物の処理量が多く、ドライクリーニン
グ機が複数基からなる施設では、フイルタ冷却器
および蒸留機の様な補助設備を共用化すれば次の
様な面で有利となる。 Dry cleaning equipment for small-scale laundry is used as a single unit as shown in Figure 2, but in facilities such as nuclear power plants that handle a large amount of laundry and have multiple dry cleaning machines, If auxiliary equipment such as filter coolers and distillers are shared, it will be advantageous in the following aspects.
1 構成機器が少く、維持管理が容易になる。1. There are fewer components, making maintenance and management easier.
2 単基当りの所要スペースが少くなる。2. The space required per unit is reduced.
3 クリーニング設備の主要部分が小型となり、
機器間を接近できるので作業性が向上する。3 The main parts of the cleaning equipment have become smaller,
Work efficiency is improved because equipment can be brought closer together.
第3図は複数のドライクリーニング機に対し蒸
留器9を共用化した例である。洗濯工程は第2図
で説明したものと同様に行われ次の通りである。
各ドライクリーニング機で保有する溶剤は、蒸留
器9に集められ、蒸留した後、水分離器10を経
てポンプ12および配管13によつて各ドライク
リーニング機溶剤タンク2に分配される。蒸留に
供される溶剤中には、洗浄効果を高めるためのソ
ープや衣服から移行した水などが含まれ、また時
には水溶性汚れの洗浄効果を高めるために溶剤に
添加した水などが存在する。溶剤中にソープが存
在すると、蒸留時に発泡し易くまた水と溶剤の沸
点が著しく異なり、かつ溶剤の比重が水より大き
い場合(例フツソ系溶剤)には、蒸留器の槽内は
二相に分離し、上部に沸点の高い水層が形成され
るため突沸が起き易くなる。 FIG. 3 shows an example in which the distiller 9 is shared by a plurality of dry cleaning machines. The washing process is carried out in the same manner as described in FIG. 2 and is as follows.
The solvent held in each dry cleaning machine is collected in a distiller 9, distilled, and then distributed to each dry cleaning machine solvent tank 2 via a water separator 10 by a pump 12 and piping 13. The solvent used for distillation contains water migrated from soap and clothing to enhance the cleaning effect, and sometimes water is added to the solvent to enhance the cleaning effect of water-soluble stains. If soap is present in the solvent, it will easily foam during distillation, and if the boiling points of the water and solvent are significantly different and the specific gravity of the solvent is greater than that of water (e.g., a soft solvent), the inside of the distiller will be in two phases. It separates and forms an aqueous layer with a high boiling point at the top, making bumping more likely.
従つて蒸留器は、これらの異常現象に伴う事故
を防止するために、通常は蒸留器の水平方向の断
面積を大きくし、かつ直径を大きく設計しており
溶剤の最大収容容量の2倍程度の蒸留器を使用し
ている。蒸留に供される溶剤量は共用化によつて
大量となり蒸留器の単機容量も非常に大きなもの
となる。また放射性物質を含む溶剤を蒸留するた
めに、その製造にあたつては特別な品質管理が必
要で、かつ大型化に伴うコスト費上昇も大きく蒸
留器の小型化が大きな課題となつていた。 Therefore, in order to prevent accidents caused by these abnormal phenomena, distillers are usually designed with a large horizontal cross-sectional area and a large diameter, approximately twice the maximum capacity for solvent. distiller is used. The amount of solvent used for distillation increases due to shared use, and the capacity of a single distiller also becomes very large. In addition, since solvents containing radioactive substances are distilled, special quality control is required during production, and the cost increases as the size increases, making the miniaturization of distillers a major issue.
本発明は、原子力発電所用ドライクリーニング
設備の蒸留器の上記欠点を除去し、蒸留器を小型
化し維持、管理の容易なドライクリーニング設備
を提供することを目的とする。
An object of the present invention is to eliminate the above-mentioned drawbacks of the distiller of dry cleaning equipment for nuclear power plants, and to provide a dry cleaning equipment that has a smaller distiller and is easier to maintain and manage.
本発明によれば上記の目的は、ドライクリーニ
ング機を複数基と蒸留器を一基備えるドライクリ
ーニング設備の蒸留器と溶剤タンクとの間に水分
離機能を有する溶剤受槽を設け、使用済の溶剤を
溶剤受槽に受けて水と溶剤とに分離した後、溶剤
のみを前記蒸留器によつて蒸留するようにするこ
とによつて達成される。
According to the present invention, the above object is achieved by providing a solvent receiving tank having a water separation function between the distiller and the solvent tank of a dry cleaning equipment equipped with a plurality of dry cleaning machines and one distiller, and disposing of the used solvent. This is achieved by receiving the water in a solvent receiving tank and separating it into water and solvent, and then distilling only the solvent in the distiller.
本発明の実施例を第1図に基いて説明する。第
1図において、D1,D2,…、Drはドライクリー
ニング機を示し、夫々のドライクリーニング機
は、被洗物を投入し洗浄する洗濯ドラム1と洗浄
用溶剤を貯蔵する溶剤タンク2、溶剤を循環する
ポンプ3、溶剤中に移行した汚染物を除去するフ
イルム4からなる循環系と、乾燥に必要な熱風を
循環するフアン5、熱風中に含まれる綿くずなど
を除去するリントフイルタ6、被洗物中に残存し
熱風を作るヒーター8からなる熱風系と溶剤を共
通の蒸留器9を介して蒸留し水分離器10によつ
て溶剤の水分を分離する蒸留系と、3方弁として
なり循環系と蒸留系を切換える切換弁11、前記
蒸留器9と溶剤タンク2との間に共通の溶剤受槽
12とを備えている。
An embodiment of the present invention will be explained based on FIG. In Fig. 1, D 1 , D 2 , ..., Dr indicate dry cleaning machines, and each dry cleaning machine has a washing drum 1 into which items to be washed are loaded and washed, and a solvent tank 2 storing cleaning solvent. , a circulation system consisting of a pump 3 that circulates the solvent, a film 4 that removes contaminants transferred into the solvent, a fan 5 that circulates hot air necessary for drying, and a lint filter that removes cotton waste contained in the hot air. 6. A hot air system consisting of a heater 8 that remains in the object to be washed and generates hot air; a distillation system that distills the solvent through a common distiller 9 and separates water from the solvent by a water separator 10; It is provided with a switching valve 11 which acts as a valve and switches between a circulation system and a distillation system, and a common solvent receiving tank 12 between the distiller 9 and the solvent tank 2.
本発明によるドライクリーニング設備は被洗物
を洗浄した使用済溶剤は、溶剤受槽12に集めら
れ水分を分離され蒸留器9に入り蒸留される。蒸
留された溶剤はそれぞれの溶剤タンクにポンプ1
3および配管14によつて送られ再使用される。
また連続的に水分離を実施するには溶剤受槽12
と蒸留器9との間に小型の水分離器を設ければよ
い。 In the dry cleaning equipment according to the present invention, the used solvent used to clean the items to be washed is collected in a solvent receiving tank 12, water is separated from the solvent, and then the solvent is entered into a distiller 9 and distilled. The distilled solvent is pumped into each solvent tank.
3 and pipe 14 for reuse.
In addition, in order to perform water separation continuously, the solvent receiving tank 12
A small water separator may be provided between the distiller 9 and the distiller 9.
溶剤受槽12の構造は、上部に高さの異なる取
出口を2ケ所備え槽に集められた水と溶剤との混
合液を、水と溶剤との比重の違いにより比重の軽
い水が上方に比重の重い溶剤が下方にたまること
を利用して、槽の上側の取出口から水を取出し、
槽の下側の取出口から溶剤を取出すようにしたも
のである。 The structure of the solvent receiving tank 12 has two outlet ports at different heights at the top, and the mixed liquid of water and solvent collected in the tank is drained upward due to the difference in specific gravity between the water and the solvent. Taking advantage of the fact that the heavy solvent accumulates below, take out the water from the outlet at the top of the tank.
The solvent is taken out from the outlet at the bottom of the tank.
本発明は、複数基のドライクリーニング機に共
通する蒸留受槽および蒸留器を用いて汚染された
溶剤を蒸留精製し再使用するドライクリーニング
装置について説明したが、エマルジヨン型ドライ
クリーニング装置の場合には単機でも応用可能で
ある。
The present invention has described a dry cleaning device that distills and purifies contaminated solvent and reuses it using a distillation tank and a distillation device common to multiple dry cleaning machines, but in the case of an emulsion type dry cleaning device, a single machine However, it is applicable.
エマルジヨン型ドライクリーニング装置は、ド
ライクリーニングのもつ水溶性汚れが洗浄できな
い欠点を補うために溶剤中に5〜20%の水を添加
して被洗物を洗濯する方法である。機器構成は、
第3図に示すものと同じであるが溶剤中に多量の
水を含むために突沸を起し易く、蒸留器を小型化
することが難しく蒸留器の容量は最大収容容量の
2倍程度となつている。 Emulsion type dry cleaning equipment is a method of washing items by adding 5 to 20% water to a solvent in order to compensate for the disadvantage of dry cleaning in that water-soluble stains cannot be removed. The equipment configuration is
It is the same as the one shown in Figure 3, but since the solvent contains a large amount of water, bumping is likely to occur, making it difficult to downsize the distiller, and the distiller's capacity is approximately twice the maximum storage capacity. ing.
本発明をエマルジヨン型ドライクリーニングに
適用した場合、第3図のポンプ3と蒸留器9との
間に水分離機能を備えた溶剤受槽を設ければよ
く、蒸留器と溶剤受槽の容量をあわせても従来の
蒸留器よりも小さくでき小型化が可能である。こ
の場合ドライクリーニング機にくらべて、溶剤中
に存在する水量は非常に多く突沸の危険は大きい
が溶剤受槽を備えることにより危険性を除去でき
る。 When the present invention is applied to emulsion-type dry cleaning, a solvent receiving tank with a water separation function may be provided between the pump 3 and the distiller 9 shown in Fig. 3, and the combined capacity of the distiller and the solvent receiving tank may be It can also be made smaller than conventional distillers. In this case, compared to a dry cleaning machine, the amount of water present in the solvent is much larger and there is a greater risk of bumping, but this risk can be eliminated by providing a solvent receiving tank.
本発明によれば、各ドライクリーニング機と蒸
留機との間に水分離機能を備えた溶剤受槽を設け
たことにより、
1 発泡や突沸の危険のない小型蒸留器とするこ
とができる。
According to the present invention, by providing a solvent receiving tank with a water separation function between each dry cleaning machine and the distillation machine, it is possible to provide a small-sized distillation machine without the risk of foaming or bumping.
2 小型蒸留であるため、無駄な空間が非常に少
くなり、熱効率もよく省エネルギ化が計れる。2. Because it is a small-sized distillation, there is very little wasted space, and the thermal efficiency is high, resulting in energy savings.
3 従来の蒸留器は発泡、突沸などの影響をなく
すために、最大収容容量に対し2倍程度の容量
を占めていたが、溶剤受槽の容量は最大収容容
量と等しくてよく、蒸留器も蒸留能力に見合つ
た程度でよいために、両者をあわせても従来の
蒸留器より小型とすることができスペースを狭
くできる。3 Conventional distillers have a capacity that is approximately twice the maximum capacity in order to eliminate the effects of foaming, bumping, etc. However, the capacity of the solvent receiving tank can be equal to the maximum capacity, and the distiller can also be used for distillation. Since the distiller only needs to be of a size commensurate with its capacity, the distiller can be made smaller than the conventional distiller even if both are combined, and the space can be narrowed down.
4 放射性物質で汚染され易い機器は蒸留器であ
り、その小型化によつて汚染面積が縮少し維持
管が容易となる。4. Equipment that is easily contaminated with radioactive materials is the distiller, and its miniaturization reduces the contaminated area and makes maintenance pipes easier.
以上のとおり共通の溶剤受槽を設けることによ
つてスペースを縮少し運転維持管理の合理化を計
ることができる。 As described above, by providing a common solvent receiving tank, space can be reduced and operation and maintenance can be streamlined.
第1図は本発明の実施例による原子力発電所用
のドライクリーニング設備の系統図、第2図は従
来のドライクリーニング機の系統図、第3図は従
来の原子力発電所用ドライクリーニング設備の系
統図である。
1……洗濯ドラム、2……溶剤タンク、3……
ポンプ、4……フイルタ、5……フアン、6……
リントフイルタ、7……凝縮器、8……ヒータ、
9……蒸留器、10……水分離器、11……切換
弁、12……溶剤受槽、13……ポンプ、14…
…配管。
Figure 1 is a system diagram of dry cleaning equipment for nuclear power plants according to an embodiment of the present invention, Figure 2 is a system diagram of a conventional dry cleaning machine, and Figure 3 is a system diagram of conventional dry cleaning equipment for nuclear power plants. be. 1...Washing drum, 2...Solvent tank, 3...
Pump, 4... Filter, 5... Fan, 6...
Lint filter, 7... Condenser, 8... Heater,
9... distiller, 10... water separator, 11... switching valve, 12... solvent receiver tank, 13... pump, 14...
…Piping.
Claims (1)
洗濯ドラムに溶剤を溶剤タンクから循環供給する
循環系と、前記洗濯ドラムに熱風を循環しながら
洗濯された被洗物を乾燥する乾燥系とからなるド
ライクリーニング機を複数基設置するとともに、
使用済の溶剤を蒸留する蒸留器を一基備えるドラ
イクリーニング設備において、前記蒸留器と溶剤
タンクとの間に水分離機能を有する溶剤受槽を設
け、使用済の溶剤を前記溶剤受槽に受けて水と溶
剤とに分離した後、溶剤のみを前記蒸留器によつ
て蒸留するようにしたことを特徴とする原子力発
電所用ドライクリーニング設備。1. A washing drum that rotates with items to be washed, a circulation system that circulates and supplies solvent from a solvent tank to the washing drum, and a drying system that dries the washed items while circulating hot air through the washing drum. In addition to installing multiple dry cleaning machines consisting of
In a dry cleaning facility equipped with one distiller for distilling used solvent, a solvent receiving tank having a water separation function is provided between the distiller and the solvent tank, and the used solvent is received in the solvent receiving tank and water is removed. 1. A dry cleaning equipment for a nuclear power plant, characterized in that, after separating into a solvent and a solvent, only the solvent is distilled by the distiller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1697385A JPS61176896A (en) | 1985-01-31 | 1985-01-31 | Dry cleaning facility for nuclear power plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1697385A JPS61176896A (en) | 1985-01-31 | 1985-01-31 | Dry cleaning facility for nuclear power plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61176896A JPS61176896A (en) | 1986-08-08 |
| JPH0570120B2 true JPH0570120B2 (en) | 1993-10-04 |
Family
ID=11931013
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1697385A Granted JPS61176896A (en) | 1985-01-31 | 1985-01-31 | Dry cleaning facility for nuclear power plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61176896A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4423958A1 (en) * | 1994-07-07 | 1996-01-11 | Trw Repa Gmbh | Belt retractor |
-
1985
- 1985-01-31 JP JP1697385A patent/JPS61176896A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61176896A (en) | 1986-08-08 |
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