JPS633028B2 - - Google Patents
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- Publication number
- JPS633028B2 JPS633028B2 JP4041884A JP4041884A JPS633028B2 JP S633028 B2 JPS633028 B2 JP S633028B2 JP 4041884 A JP4041884 A JP 4041884A JP 4041884 A JP4041884 A JP 4041884A JP S633028 B2 JPS633028 B2 JP S633028B2
- Authority
- JP
- Japan
- Prior art keywords
- cleaned
- steam
- cylindrical body
- steam cleaning
- gas
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G5/00—Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents
- C23G5/02—Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents using organic solvents
- C23G5/04—Apparatus
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
【発明の詳細な説明】
本発明は蒸気洗浄方法に関し、特に金属などの
被洗浄物を有機溶剤等で蒸気洗浄した後の乾燥を
促進し、且つ乾燥後の被洗浄物に同伴して装置外
へ漏洩することによる有機溶剤の損失を防止する
に適した蒸気洗浄方法を提供するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a steam cleaning method, in particular, which accelerates the drying of objects to be cleaned, such as metals, after steam cleaning with an organic solvent, etc. The purpose of the present invention is to provide a steam cleaning method suitable for preventing loss of organic solvent due to leakage.
蒸気洗浄方法は、被洗浄物の洗浄と乾燥とを一
工程で行なうことができる点、及び被洗浄物が一
般に有機溶剤の蒸気中で乾燥されるため仕上り面
がきれいである点など数多くの特徴を有してお
り、ステンレス製品を始めとする種々の金属物品
の仕上げ工程として実施されている。従来、蒸気
洗浄に使用されている装置は、例えば上面が開放
された槽の底部に加熱器を設け、上面の開口部の
周囲にコンデンサーを設けた構造が一般的であ
る。しかしながら、かかる蒸気洗浄装置は単独あ
るいはスプレー洗浄など他の洗浄工程に接続して
被洗浄物の連続洗浄を行なう場合、多くの問題を
有している。即ち、上記装置において被洗浄物は
加熱器により蒸発した有機溶剤の蒸気が存在する
槽中で、該被洗浄物の表面に溶剤蒸気が凝縮する
ことによつて洗浄され、次いで被洗浄物の温度が
蒸気温度に達した時点点で乾燥されて槽より取り
出されるが、該被洗浄物が蒸気温度に達するまで
相当の時間を要する。そのため、被洗浄物が蒸気
洗浄装置の槽内でゆつくりと連続的に移動させ
て、該槽内で蒸気洗浄を行なう方法などが採用さ
れているが、処理スピードを大きくし難いという
問題を有していた。また、処理スピードを上げる
ために、蒸気洗浄装置の槽を被洗浄物の進行方向
に延長することによつて、蒸気と被洗浄物との接
触区間を伸ばすことも考えられるが、槽上面の開
口部における面積が増大するため、有機溶剤を含
む蒸気の漏洩量が増加するという問題を生じる。
また、上記した蒸気洗浄装置は槽内に被洗浄物を
出し入れするために、被洗浄物を移動させると共
に上下させる手段が必要であるため、被洗浄物の
移送機構が複雑化するという問題をも有する。 The steam cleaning method has many features, such as the ability to clean and dry the object to be cleaned in one step, and the fact that the object to be cleaned is generally dried in organic solvent vapor, resulting in a clean finished surface. It is used as a finishing process for various metal products including stainless steel products. Conventionally, devices used for steam cleaning generally have a structure in which, for example, a heater is provided at the bottom of a tank with an open top surface, and a condenser is provided around the opening in the top surface. However, such steam cleaning apparatuses have many problems when used alone or in conjunction with other cleaning processes such as spray cleaning for continuous cleaning of objects to be cleaned. That is, in the above-mentioned apparatus, the object to be cleaned is cleaned by condensing the solvent vapor on the surface of the object in a tank in which vapor of an organic solvent evaporated by a heater is present, and then the temperature of the object to be cleaned is increased. When the object reaches the steam temperature, it is dried and taken out from the tank, but it takes a considerable amount of time for the object to be cleaned to reach the steam temperature. For this reason, methods have been adopted in which the items to be cleaned are moved slowly and continuously in a tank of a steam cleaning device and steam cleaning is performed within the tank, but this method has the problem of making it difficult to increase the processing speed. Was. In addition, in order to increase the processing speed, it is possible to extend the contact area between the steam and the object by extending the tank of the steam cleaning equipment in the direction of movement of the object to be cleaned. Since the area of the part increases, a problem arises in that the amount of leakage of steam containing organic solvent increases.
In addition, the above-mentioned steam cleaning apparatus requires means for moving and raising and lowering the object to be cleaned in order to take it in and out of the tank, so it also has the problem of complicating the mechanism for transporting the object to be cleaned. have
本発明者等は、上記問題に鑑み検討した結果、
以上に示す新規な構造の蒸気洗浄装置を既に提案
している。即ち、両端が開口した筒状体に、被洗
浄物を移送する手段を設け、該筒状体の胴部に蒸
気供給手段を設けて有機溶剤の蒸気を供給すると
共に、その両端の開口部内壁にコンデンサーを設
けることにより、蒸気の漏洩量に影響なく、胴部
の長さ、即ち蒸気と被洗浄物との接触区間を延長
することができ、充分なラインスピードが確保で
きると共に、被洗浄物の移送ラインを平面化する
ことができ、移送機構の複雑さを解消した蒸気洗
浄装置である。該装置によれば前述の如き従来の
蒸気洗浄装置の有する問題は解決されるため、例
えば流し台のような複雑形状の大型被洗浄物を大
量に処理する場合に適する。 As a result of consideration in view of the above problems, the present inventors found that
A steam cleaning device with the novel structure described above has already been proposed. That is, a means for transporting the object to be cleaned is provided in a cylindrical body with openings at both ends, and a vapor supply means is provided in the body of the cylindrical body to supply vapor of an organic solvent. By installing a condenser in the pipe, it is possible to extend the length of the body, that is, the contact area between the steam and the object to be cleaned, without affecting the amount of steam leakage. This is a steam cleaning device that can flatten the transfer line and eliminate the complexity of the transfer mechanism. Since this apparatus solves the problems of the conventional steam cleaning apparatus as described above, it is suitable for processing large quantities of large objects to be cleaned with complex shapes, such as sinks, for example.
本発明者等は、上記した蒸気洗浄装置を用い
て、更に処理スピードを速め、且つ溶剤の回収率
を高める方法について検討した結果、本発明の蒸
気洗浄方法を提供するに至つたものである。 The present inventors have studied methods for further increasing the processing speed and increasing the solvent recovery rate using the above-mentioned steam cleaning apparatus, and as a result, have provided the steam cleaning method of the present invention.
即ち、本発明は両端が開口した筒状体で、一端
から他端に向けて被洗浄物が移送される手段を有
し、かつ該筒状体の胴部に蒸気洗浄部およびその
両端の開口部内壁に凝縮部を有する構造の蒸気洗
浄装置において被洗浄物を蒸気洗浄するにあた
り、筒状体内部における気体の少なくとも一部を
蒸気洗浄装置外へ抜き出し、蒸気回収装置を介し
て蒸気洗浄装置の凝縮部へ再循環することを特徴
とする蒸気洗浄方法である。 That is, the present invention provides a cylindrical body with both ends open, a means for transferring the object to be cleaned from one end to the other, and a steam cleaning section in the body of the cylindrical body and openings at both ends. When steam cleaning an object to be cleaned in a steam cleaning device that has a condensation section on the inner wall, at least a portion of the gas inside the cylindrical body is extracted to the outside of the steam cleaning device and transferred to the steam cleaning device via a steam recovery device. This is a steam cleaning method characterized by recirculation to the condensing section.
上記の如き蒸気洗浄装置において蒸気洗浄後、
被洗浄物の乾燥(凝縮)速度を速めるためには、
単に該装置内の凝縮部へ外部より空気を吹き込む
方法によつても達成される。しかしながら、その
ような方法によれば、導入する外気のため筒状体
両端の開口部より漏洩する蒸気量が増大するた
め、気体の吸引手段、例えば圧縮機、送風機等に
容量の大きなものを用いなければならない問題が
ある。一方、蒸気洗浄装置の凝縮部で乾燥された
被洗浄物は筒状体の端部より製品として取り出さ
れるが、この際に該被洗浄物は凝縮部の雰囲気温
度に相当する蒸気を同伴する。したがつて、この
まま製品を蒸気洗浄装置外へ取り出した場合に
は、溶剤蒸気が大気中に漏洩すると共に溶剤の損
失を招く問題を生じる。上記問題を解決するため
の最も一般的な方法としては、蒸気洗浄装置にお
ける凝縮部の能力を大きくして凝縮速度を上げる
と共に、筒状の両端に吸引口を設け、蒸気回収装
置を介して、気体を大気中に排気する方法があ
る。ところが、該方法では溶剤を送風機等により
吸引する場合に、外気も混入するため、気体を吸
引する手段及び蒸気回収装置の大型化が避けられ
ない。更に、乾燥速度が遅い場合、被洗浄物の表
面に曇点を生じるため、製品の仕上りを損う結果
を招く問題もあつた。 After steam cleaning in the above steam cleaning equipment,
In order to speed up the drying (condensation) of the object to be cleaned,
This can also be achieved by simply blowing air into the condensing section of the device from the outside. However, according to such a method, the amount of steam leaking from the openings at both ends of the cylindrical body increases due to the introduced outside air, so it is necessary to use a large capacity gas suction means such as a compressor or blower. There is a problem that must be solved. On the other hand, the object to be cleaned that has been dried in the condensing section of the steam cleaning device is taken out as a product from the end of the cylindrical body, but at this time, the object to be cleaned is accompanied by steam corresponding to the atmospheric temperature of the condensing section. Therefore, if the product is taken out of the steam cleaning apparatus as it is, there will be a problem in that the solvent vapor will leak into the atmosphere and the solvent will be lost. The most common method to solve the above problem is to increase the capacity of the condensing section in the steam cleaning device to increase the condensation speed, and to provide suction ports at both ends of the cylindrical shape, and to use the steam through the steam recovery device. There is a method of exhausting the gas into the atmosphere. However, in this method, when the solvent is sucked by a blower or the like, outside air is mixed in, so it is inevitable that the means for sucking the gas and the vapor recovery device become larger. Furthermore, when the drying speed is slow, a cloud point is formed on the surface of the object to be cleaned, resulting in a problem that the finish of the product is impaired.
これに対して、本発明によれば凝縮部の気体の
一部を蒸気回収装置を介して自己循環させるた
め、装置の大型化の必要がなくなり、溶剤の回収
率を高めることが出来、さらに処理スピードも上
げることが出来る。 On the other hand, according to the present invention, a part of the gas in the condensing section is self-circulated via the vapor recovery device, so there is no need to increase the size of the device, the solvent recovery rate can be increased, and further processing is possible. You can also increase your speed.
本発明に用いる蒸気洗浄装置は、両端が開口し
た筒状体であり、該筒状体内に一端から他端に向
けて被洗浄物を移送する手段(以下、移送手段と
いう)があり、胴部に蒸気洗浄部を有し、且つ両
端の開口部内壁に凝縮部を有する構造であれば特
に制限されない。代表的1例として第1図にて詳
述する。 The steam cleaning device used in the present invention is a cylindrical body with both ends open, and there is a means (hereinafter referred to as a transfer means) for transferring the object to be cleaned from one end to the other end in the cylindrical body. There is no particular restriction as long as the structure has a steam cleaning section at the opening and a condensing section at the inner wall of the opening at both ends. A typical example will be explained in detail with reference to FIG.
筒状体1は両端が開口しており、後述する移送
手段により被洗浄物が通過可能な断面積を有して
いるものであれば特に制限されない。例えば、形
状は円筒状、角筒状、馬蹄形状等が一般的であ
る。また、筒状体1の長さは、処理スピード、被
洗浄物の肉厚など熱容量を勘案して適宜決定すれ
ばよい。一般には、被洗浄物を筒状体内で蒸気温
度に昇温するのに必要な長さ以上とするのが好ま
しい。更に、筒状体1は、供給される有機溶剤の
蒸気が内壁面で冷却されて凝縮するのを防止する
ため、保温材で囲むか筒状体の材質に保温材料を
用いるか、場合によつては筒状体に加熱手段を設
けることが好ましい。特に筒状体壁面の温度は、
中央部或いは中央部よりやや入口側が最高温度と
なるように設計するのが好ましい。また、上記筒
状体1に存在する被洗浄物の移送手段2は、該筒
状体の一端(入口ともいう)から他端(出口とも
いう)に連続的被洗浄物3を移送することができ
る構造を有する公知の輸送機器が特に制限なく採
用される。 The cylindrical body 1 is open at both ends, and is not particularly limited as long as it has a cross-sectional area through which the object to be cleaned can pass by the transfer means described later. For example, the shape is generally cylindrical, prismatic, horseshoe, etc. Further, the length of the cylindrical body 1 may be appropriately determined in consideration of heat capacity such as processing speed and wall thickness of the object to be cleaned. Generally, it is preferable that the length be longer than the length necessary to raise the temperature of the object to be cleaned to the steam temperature within the cylindrical body. Furthermore, in order to prevent the supplied organic solvent vapor from being cooled and condensed on the inner wall surface, the cylindrical body 1 may be surrounded by a heat insulating material or may be made of a heat insulating material as the case may be. Therefore, it is preferable to provide a heating means in the cylindrical body. In particular, the temperature of the wall surface of the cylindrical body is
It is preferable to design so that the temperature is highest at the center or slightly closer to the inlet than the center. Further, the object to be cleaned transfer means 2 present in the cylindrical body 1 is capable of continuously transferring the object to be cleaned 3 from one end (also referred to as an inlet) to the other end (also referred to as an outlet) of the cylindrical body. Any known transportation device having a structure that can be used can be used without particular limitation.
従つて、該移送手段は、当該筒状体内部にのみ
独立して存在させる必要はなく、被洗浄物製造ラ
インの一部として筒状体内を貫通する構造であつ
てもよい。例えば、ベルトコンベア、ネツトコン
ベアー、コイルコンベアー、チエーンコンベアー
等のコンベアー類等が一般的であり、被洗浄物の
形状、大きさなどに合つた機器を適宜選ぶことが
できる。 Therefore, the transfer means does not need to be independently present only inside the cylindrical body, but may have a structure that penetrates through the cylindrical body as part of a production line for objects to be cleaned. For example, conveyors such as belt conveyors, net conveyors, coil conveyors, chain conveyors, etc. are common, and the equipment suitable for the shape and size of the object to be cleaned can be selected as appropriate.
また、前記筒状体1の胴部には蒸気洗浄部4、
蒸気供給手段(図示せず)からの蒸気供給口5が
存在する。蒸気供給手段は、筒状体内が蒸気洗浄
に必要な蒸気濃度を有するのに充分な量の蒸気を
供給できるものであれば、特に制限なく使用され
る。例えば、蒸気洗浄装置の近傍に蒸発器を設け
て、ここで蒸気を発生させ、該蒸気をノズルより
なる蒸気供給部5から供給する如くした方式(外
部供給方式)が、蒸気濃度のコントロールが容易
である。胴部が長い場合にもノズルの数を増やす
ことにより、全体に均一に蒸気を供給することも
好ましい。また、筒状体1の底面は、凝縮液の受
皿となるように構成され、必要に応じて凝縮液取
出口6に向け液が流れるよう傾斜をあたえる。凝
縮液は、取出口6から取り出され、凝縮液循環パ
イプにより蒸発器に循環する。勿論、蒸気供給手
段は上記のような外部供給方式に限定されるもの
ではなく、例えば、図には示されていないが、筒
状体の底部に液留めを形成し、該液留めに加熱器
を設けて有機溶剤を蒸発させることにより、蒸気
を供給する如くした方式も採用される。 Further, the body of the cylindrical body 1 includes a steam cleaning section 4,
There is a steam supply inlet 5 from steam supply means (not shown). The steam supply means may be used without particular limitation as long as it can supply a sufficient amount of steam to provide the steam concentration necessary for steam cleaning inside the cylindrical body. For example, a method (external supply method) in which an evaporator is provided near the steam cleaning device to generate steam and supply the steam from a steam supply section 5 consisting of a nozzle (external supply method) makes it easy to control the steam concentration. It is. Even when the body is long, it is preferable to increase the number of nozzles to uniformly supply steam to the entire body. Further, the bottom surface of the cylindrical body 1 is configured to serve as a condensate receiving tray, and is sloped as necessary so that the liquid flows toward the condensate outlet 6. The condensate is taken out from the outlet 6 and circulated to the evaporator via a condensate circulation pipe. Of course, the steam supply means is not limited to the external supply method as described above; for example, although not shown in the figure, a liquid reservoir is formed at the bottom of the cylindrical body, and a heater is attached to the liquid reservoir. A method is also adopted in which steam is supplied by providing a vaporizer to evaporate the organic solvent.
更に、上記装置には蒸気洗浄後の被洗浄物の乾
燥及び筒状体1内の蒸気が外部に漏洩するのを防
止するため、その両端の開口部の内壁にコンデン
サーとしての冷却手段7(及び7′)が設けられ
た凝縮部を有する。この際、コンデンサーの設置
態様として第1図では2組のコンデンサー群を一
系としたものが2系設けられた態様であるが、該
態様に特に限定されない。該冷却手段は、移送さ
れる被洗浄物に対して障害とならない構造であれ
ば、公知のコンデンサーなどが特に制限なく使用
される。例えば、蛇管式、プレート式等のコンデ
ンサーを筒状体1の両端開口部の近辺に付設する
のが一般的である。この場合、筒状体開口部の内
周全体に冷却面を形成させるのが効果的である
が、被洗浄物の出口側に付設する冷却手段7−b
(又は7′−b)にあつては上面で凝縮した液が被
洗浄物上に落下し、所謂曇点の生成の原因となる
ため、該凝縮液の落下を防止する手段を構じるこ
とが好ましい。例えば、筒状体1の出口付近の内
壁のうち上面に冷却面を存在させない態様、更に
は該上面を加熱する態様、上面に傾斜を持たせ、
凝縮液が該面に沿つて流れ筒状体の側壁に至るよ
うにする態様、被洗浄物の上方に傘を設ける態様
等の一つ又は二種以上を併用するのが好ましい。
これらのうち筒状体内壁の上面に冷却手段を存在
させない態様が、手軽で曇点の防止率も高いので
推奨される。 Furthermore, in order to dry the object to be cleaned after steam cleaning and to prevent the steam inside the cylindrical body 1 from leaking to the outside, the above apparatus is equipped with a cooling means 7 (and a condenser) on the inner wall of the opening at both ends. 7'). At this time, although the installation mode of the capacitors is shown in FIG. 1 as two systems in which two sets of capacitor groups are installed, the present invention is not particularly limited to this mode. As the cooling means, a known condenser or the like may be used without any particular restriction as long as it does not pose an obstacle to the transferred object to be cleaned. For example, it is common to attach a condenser of a flexible tube type, a plate type, etc. near the openings at both ends of the cylindrical body 1. In this case, it is effective to form a cooling surface on the entire inner periphery of the opening of the cylindrical body, but cooling means 7-b attached to the outlet side of the object to be cleaned
(or 7'-b), the liquid condensed on the top surface falls onto the object to be cleaned, causing the formation of a so-called cloud point, so a means must be provided to prevent the condensed liquid from falling. is preferred. For example, a mode in which a cooling surface is not present on the upper surface of the inner wall near the exit of the cylindrical body 1, a mode in which the upper surface is heated, a mode in which the upper surface is sloped,
It is preferable to use one or more of the following methods, such as a method in which the condensate flows along the surface and reaches the side wall of the cylindrical body, and a method in which an umbrella is provided above the object to be cleaned.
Among these, a mode in which no cooling means is provided on the upper surface of the inner wall of the cylindrical body is recommended because it is simple and has a high cloud point prevention rate.
本発明は、前述した蒸気洗浄装置を用いて被洗
浄物を蒸気洗浄後に乾燥するに際して、筒状体内
部の気体の少なくとも一部を装置外へ抜き出し、
蒸気回収装置を介して凝縮部へ再循環することを
特徴とするもので、その手段は特に制限されるも
のでない。例えば、第1図に示すように、筒状体
1内、好ましくは凝縮部7又は7′及び凝縮部近
辺の出口側における気体の一部を圧縮機又は送風
機8により吸引し、吸引した気体を蒸気回収装置
9に導入し、溶剤を分離除去した気体(一般に空
気)を蒸気洗浄装置の凝縮部に再循環する。蒸気
回収装置9により気液分離した後の溶剤は、配管
10を介して溶剤受皿11へ溜まる。この場合、
被洗浄物の乾燥速度を早めるために、必要に応じ
て溶剤を除去した気体を加熱して再循環するこ
と、或いは第1図に示す如く、凝縮部を2系列設
け、各々の系列に冷却手段を2組づつ設けると共
に、複数の吹込みノズル12,13により気体を
再循環させることが好ましい。後者の方法では
各々の凝縮部へ循環させる冷却水の種類を変える
(例えば、7−b及び7′−aに一般の安価な冷却
水を用い、7−a及び7′−bに冷水やブライン
を用いる)ことにより、冷却温度がコントロール
し易いことと共に、複数の吹込みノズルを用いて
気体を再循環させるために、例えば被洗浄物表面
に付着した溶剤の液滴(しずく)を飛ばす目的
と、被洗浄物表面の溶剤蒸気を溶剤の含まぬ気体
により置換する目的に分けて使用できるため、よ
り乾燥速度を速めることが出来る。 In the present invention, when drying an object to be cleaned after steam cleaning using the above-mentioned steam cleaning apparatus, at least a part of the gas inside the cylindrical body is extracted to the outside of the apparatus,
It is characterized by being recirculated to the condensing section via a vapor recovery device, and the means for doing so is not particularly limited. For example, as shown in FIG. 1, a part of the gas in the cylindrical body 1, preferably in the condensing section 7 or 7' and on the outlet side near the condensing section, is sucked by a compressor or blower 8, and the sucked gas is The gas (generally air) introduced into the steam recovery device 9 and separated from the solvent is recycled to the condensing section of the steam cleaning device. The solvent after being separated into gas and liquid by the vapor recovery device 9 is collected in a solvent receiving tray 11 via a pipe 10. in this case,
In order to speed up the drying rate of the object to be cleaned, it is possible to heat the gas from which the solvent has been removed and recirculate it as necessary, or, as shown in Figure 1, two series of condensing sections are provided and each series is equipped with a cooling means. It is preferable to provide two sets of each, and to recirculate the gas using a plurality of blowing nozzles 12 and 13. In the latter method, the type of cooling water that is circulated to each condensing section is changed (for example, using ordinary inexpensive cooling water for 7-b and 7'-a, and using cold water or brine for 7-a and 7'-b). In addition to making it easy to control the cooling temperature, multiple blow nozzles are used to recirculate the gas, which can be used to blow off solvent droplets that have adhered to the surface of the object to be cleaned. Since it can be used separately for the purpose of replacing the solvent vapor on the surface of the object to be cleaned with a gas that does not contain the solvent, the drying speed can be further increased.
上記の蒸気回収装置9としては、周知の種々の
方法、例えばコンデンサーにより気液分離する方
法や活性炭等の吸着剤を用いる吸着方法等が利用
出来るが、気体の循環装置として圧縮機を用い、
気体を加圧する場合には、水等の安価な冷却源を
用いて、比較的小型のコンデンサーにより、効率
良く溶剤蒸気を凝縮分離することが可能であるた
め好ましい。 As the above-mentioned vapor recovery device 9, various well-known methods can be used, such as a method of separating gas and liquid using a condenser, an adsorption method using an adsorbent such as activated carbon, etc., but using a compressor as a gas circulation device,
When pressurizing the gas, it is preferable because it is possible to efficiently condense and separate the solvent vapor using a relatively small condenser using an inexpensive cooling source such as water.
筒状体内部の気体を装置外へ抜き出す手段8に
用いる送風機、圧縮機等の種類(型式)、能力等
については、筒状体1の容積、被洗浄物の形状及
び処理量等により適宜選定される。この際、送風
機8等に接続する吸引口14の位置は、筒状体1
の端部に近いと、外気の吸引の影響が大きく、送
風機の容量を大きくする必要が生じるため、該吸
引口14は凝縮部又は凝縮部出口側近傍に付設す
ることが好ましい。 The type (model), capacity, etc. of the blower, compressor, etc. used for the means 8 for extracting the gas inside the cylindrical body to the outside of the apparatus are appropriately selected depending on the volume of the cylindrical body 1, the shape of the object to be cleaned, the processing amount, etc. be done. At this time, the position of the suction port 14 connected to the blower 8 etc.
The suction port 14 is preferably attached to the condensing section or near the outlet of the condensing section, since the suction port 14 has a large influence on the suction of outside air and requires a large capacity of the blower.
その他、本発明における洗浄液は、従来蒸気洗
浄剤として使用されている易揮発性の液体、例え
ばエーテル、アルコール、メチレンクロライド、
ジクロルエタン、トリクロルエタン、パークロル
エチレンなどの有機溶剤、特に塩素化炭化水素類
が好適に用いられるが、その他水などであつても
よい。 In addition, the cleaning liquid in the present invention may include readily volatile liquids conventionally used as steam cleaning agents, such as ether, alcohol, methylene chloride,
Organic solvents such as dichloroethane, trichloroethane, and perchlorethylene, particularly chlorinated hydrocarbons, are preferably used, but other solvents such as water may also be used.
本発明の装置は、金属加工品を始めとする各種
物品の蒸気洗浄に好適に使用される。例えば、金
属加工品としては金属板、金属板加工品;金属性
のネジ、ボルト、ナツトなどの金属部品等が挙げ
られる。 The apparatus of the present invention is suitably used for steam cleaning of various articles including metal workpieces. For example, metal products include metal plates, metal plate products, and metal parts such as metal screws, bolts, and nuts.
本発明の1例として、比較的沸点の高い溶剤、
例えばトリクロルエタンやパークロルエチレン等
を使用する場合、気体の再循環なしで凝縮部のみ
で乾燥させると、乾燥に数10秒乃至数分を要し、
乾燥速度が小さいため、被洗浄物表面へ曇点が生
ずる。これを防止するためには、凝縮部の容積を
大きく(長く)する必要がある。一方、気体を適
量(必要に応じて加熱して)、被洗浄物に吹き付
けると数秒程度で乾燥可能で、上記したような装
置の過大化や曇点発生といつた問題を防止出来
る。吹き込み空気量は、被洗浄物の形状等により
適宜選定されるが、本方法は溶剤蒸気と気体との
置換をも兼ねるため、凹部を有する(蒸気滞留部
を有する)被洗浄物の場合は、その滞留部容積の
3〜5倍の量を導入すれば良い。 As an example of the present invention, a relatively high boiling point solvent,
For example, when using trichloroethane, perchlorethylene, etc., drying only in the condensing section without gas recirculation takes several tens of seconds to several minutes.
Because the drying speed is slow, cloud points occur on the surface of the object to be cleaned. In order to prevent this, it is necessary to increase (lengthen) the volume of the condensing section. On the other hand, if an appropriate amount of gas (heated if necessary) is sprayed onto the object to be cleaned, it can be dried in about a few seconds, and problems such as overscaling of the device and occurrence of clouding points as described above can be prevented. The amount of blown air is appropriately selected depending on the shape of the object to be cleaned, etc., but since this method also replaces solvent vapor with gas, in the case of an object to be cleaned that has a concave portion (has a vapor retention area), It is sufficient to introduce an amount 3 to 5 times the volume of the retention section.
第1図は本発明に用いる蒸気洗浄装置の代表的
1例を示す断面図である。図中1は筒状体、2は
移送手段、3は被洗浄物、4は蒸気洗浄部、5は
蒸気供給部、6は凝縮液取出口、7及び7′は凝
縮部(7−a,7−b及び7′−a,7′−bは冷
却手段)、8は圧縮機又は送風機、9は蒸気回収
装置、10は配管、11は溶済受皿、12及び1
3は気体吹込みノズル、14は吸引口である。
FIG. 1 is a sectional view showing a typical example of a steam cleaning device used in the present invention. In the figure, 1 is a cylindrical body, 2 is a transfer means, 3 is an object to be cleaned, 4 is a steam cleaning section, 5 is a steam supply section, 6 is a condensate outlet, 7 and 7' are condensation sections (7-a, 7-b, 7'-a, 7'-b are cooling means), 8 is a compressor or blower, 9 is a steam recovery device, 10 is piping, 11 is a melted saucer, 12 and 1
3 is a gas blowing nozzle, and 14 is a suction port.
Claims (1)
て被洗浄物が移送される手段を有し、かつ該筒状
体の胴部に蒸気洗浄部を、その両端の開口部内壁
に凝縮部を有する構造の蒸気洗浄装置において被
洗浄物を蒸気洗浄するにあたり、筒状体内部にお
ける気体の少なくとも一部を蒸気洗浄装置外へ抜
き出し、蒸気回収装置を介して蒸気洗浄装置の凝
縮部へ再循環することを特徴とする蒸気洗浄方
法。1 A cylindrical body with both ends open and a means for transferring the object to be cleaned from one end to the other, and a steam cleaning part in the body of the cylindrical body, and a steam cleaning part in the inner wall of the opening at both ends. When steam cleaning an object to be cleaned in a steam cleaning device having a structure with A steam cleaning method characterized by circulation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4041884A JPS60187685A (en) | 1984-03-05 | 1984-03-05 | Steam cleaning method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4041884A JPS60187685A (en) | 1984-03-05 | 1984-03-05 | Steam cleaning method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60187685A JPS60187685A (en) | 1985-09-25 |
| JPS633028B2 true JPS633028B2 (en) | 1988-01-21 |
Family
ID=12580107
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4041884A Granted JPS60187685A (en) | 1984-03-05 | 1984-03-05 | Steam cleaning method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60187685A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR102115432B1 (en) * | 2018-08-31 | 2020-05-26 | 한국항공우주연구원 | Corrosion preventing method using preventing corrosion apparatus for cooling channel of blower for satellite thermal vacuum test chamber |
-
1984
- 1984-03-05 JP JP4041884A patent/JPS60187685A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60187685A (en) | 1985-09-25 |
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