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JPH0355193B2 - - Google Patents
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JPH0355193B2 - - Google Patents

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Publication number
JPH0355193B2
JPH0355193B2 JP28711186A JP28711186A JPH0355193B2 JP H0355193 B2 JPH0355193 B2 JP H0355193B2 JP 28711186 A JP28711186 A JP 28711186A JP 28711186 A JP28711186 A JP 28711186A JP H0355193 B2 JPH0355193 B2 JP H0355193B2
Authority
JP
Japan
Prior art keywords
solvent
heating
heating tube
steam cleaning
tube
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
Application number
JP28711186A
Other languages
Japanese (ja)
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JPS63141687A (en
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
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Priority to JP28711186A priority Critical patent/JPS63141687A/en
Publication of JPS63141687A publication Critical patent/JPS63141687A/en
Publication of JPH0355193B2 publication Critical patent/JPH0355193B2/ja
Granted legal-status Critical Current

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  • 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】 (産業上の利用分野) 本発明は、機械部品等の被洗浄物を蒸気洗浄槽
内で発生させた蒸発溶剤により洗浄するようにし
た蒸気洗浄装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a steam cleaning device that cleans objects to be cleaned, such as mechanical parts, with an evaporated solvent generated in a steam cleaning tank.

(従来の技術) 従来のこの種蒸気洗浄装置としては、蒸気洗浄
槽に収容した溶剤を直接加熱するようにしたもの
(以下「前者装置」という。)と、該溶剤の適量を
槽内外に亘つて循環させ、この循環溶剤を槽外に
おいて加熱するようにしたもの(以下「後者装
置」という。)とがある。
(Prior art) Conventional steam cleaning devices of this type include one that directly heats the solvent contained in a steam cleaning tank (hereinafter referred to as the "former device"), and one that directly heats the solvent contained in the steam cleaning tank (hereinafter referred to as the "former device"). There is a device in which the circulating solvent is heated outside the tank (hereinafter referred to as the "latter device").

すなわち、前者装置は、第2図に示す如く、蒸
気洗浄槽21の溶剤貯溜部21aに電気ヒータ等
の加熱器23を配設し、この加熱器23により槽
21内の溶剤22を直接加熱して、槽21上部の
洗浄部21b内を蒸発溶剤雰囲気に形成保持する
ように構成されている。また、冷却水を洗浄部2
1b内の冷却管24と槽21外の冷却塔25との
間で循環させることにより、洗浄部21b内を適
温に冷却維持することにしている。
That is, in the former device, as shown in FIG. 2, a heater 23 such as an electric heater is provided in the solvent reservoir 21a of the steam cleaning tank 21, and the solvent 22 in the tank 21 is directly heated by the heater 23. The cleaning section 21b in the upper part of the tank 21 is configured to form and maintain an evaporated solvent atmosphere. In addition, the cooling water is
By circulating between the cooling pipe 24 inside 1b and the cooling tower 25 outside the tank 21, the inside of the cleaning section 21b is kept cooled to an appropriate temperature.

また、後者装置は、第3図に示す如く、蒸気洗
浄槽31外に、冷媒が圧縮機34、凝縮器35、
膨張弁36、蒸発器37等を順次循環するヒート
ポンプ33を配設し、槽31の溶剤32の一部を
循環ポンプ38により溶剤貯溜部31aと凝縮器
35との間で循環させることによつて、その循環
溶剤を凝縮器35内において冷媒の凝縮潜熱によ
り加熱するように構成されている。また、冷却水
を蒸発器37と洗浄部31b内の冷却管39との
間で循環させることによつて、洗浄部31b内の
余剰部を回収して、その回収熱を蒸発器37にお
ける冷媒蒸発熱源として利用すると共に洗浄部3
1b内を適温に冷却維持するようにしている。
In addition, in the latter device, as shown in FIG.
By disposing a heat pump 33 that sequentially circulates through an expansion valve 36, an evaporator 37, etc., and circulating a part of the solvent 32 in the tank 31 between the solvent reservoir 31a and the condenser 35 using the circulation pump 38. , the circulating solvent is heated in the condenser 35 by the latent heat of condensation of the refrigerant. Further, by circulating the cooling water between the evaporator 37 and the cooling pipe 39 in the cleaning section 31b, the surplus inside the cleaning section 31b is recovered, and the recovered heat is used to evaporate the refrigerant in the evaporator 37. In addition to being used as a heat source, the cleaning section 3
The inside of 1b is kept cooled to an appropriate temperature.

而して、かかる蒸気洗浄装置にあつては、被洗
浄物を洗浄部21b,31bにもたらすと、溶剤
蒸気が被洗浄物の表面を凝縮、流下し、これによ
つて被洗浄物の表面に付着している油脂、切粉、
その他の不要物が洗い落されるのであり、一方、
洗浄後の凝縮溶剤は上記油脂等の不純物と共に貯
溜部21a,31aに回収されるのである。
In such a steam cleaning device, when the object to be cleaned is brought to the cleaning portions 21b and 31b, the solvent vapor condenses and flows down the surface of the object to be cleaned, thereby causing water to flow onto the surface of the object to be cleaned. Adhering oil and fat, chips,
Other unnecessary substances are washed away, while
The condensed solvent after washing is collected together with impurities such as the above-mentioned oils and fats into the reservoirs 21a and 31a.

(発明が解決しようとする問題点) しかしながら、前者装置の如く槽21内に加熱
器23を配設したものでは、槽21内の清掃や加
熱器23等の保守点検や修理等が極めて困難であ
り、実用性に劣る。
(Problems to be Solved by the Invention) However, in the former device in which the heater 23 is disposed inside the tank 21, it is extremely difficult to clean the inside of the tank 21 and to perform maintenance, inspection, and repair of the heater 23, etc. Yes, but less practical.

また、後者装置の如く溶剤を槽31外に循環さ
せるものでは、このような不都合はないが、その
反面、前記循環溶剤中の溶解物の析出や混入不純
物の付着による循環ポンプ38の故障並びにその
不安はこれを避け得べくもなく、安定した運転を
期待し得ない。
In addition, in the latter device which circulates the solvent outside the tank 31, there is no such inconvenience, but on the other hand, the circulation pump 38 may malfunction due to precipitation of dissolved substances in the circulating solvent or adhesion of mixed impurities. Anxiety cannot be avoided, and stable driving cannot be expected.

すなわち、後者装置にあつては、循環ポンプ3
8として、液漏れ防止を図る上から、マグネツト
を介して駆動する密閉型ポンプを用い、その回転
部と固定部との摺接部分の潤滑を、該摺接部分に
ポンプ吐出圧を利用して前記循環溶剤の一部を導
くことによつて行わしめているのが普通である。
一方、貯溜部31aには、上述した如く、洗浄後
の凝縮溶剤と共に被洗浄物から除去された不純物
が回収されることから、前記循環溶剤中には多量
の不純物が溶解、混入していることになる。した
がつて、かかる循環溶剤中の溶解物や混入不純物
の存在により、循環ポンプ38の潤滑用配管が詰
まつたり、前記摺接部分が焼き付いたりし易く、
更にポンプ羽根に付着物を生じてバランスが崩れ
る虞れがあり、ポンプ故障の原因となる。しか
も、溶剤32の沸点が低いため、ポンプ吸水圧が
低いとキヤビテーシヨンの原因ともなる。このよ
うに、後者装置では、循環ポンプ38の存在によ
り安定した運転を期待できない。
That is, in the case of the latter device, the circulation pump 3
8. In order to prevent liquid leakage, a closed type pump driven via a magnet is used, and the sliding part between the rotating part and the fixed part is lubricated by using the pump discharge pressure on the sliding part. This is usually done by directing a portion of the circulating solvent.
On the other hand, as described above, since the impurities removed from the object to be cleaned are collected together with the condensed solvent after cleaning, a large amount of impurities are dissolved and mixed in the circulating solvent. become. Therefore, due to the presence of dissolved substances and mixed impurities in the circulating solvent, the lubricating piping of the circulation pump 38 is likely to become clogged, and the sliding contact portions are likely to seize.
Furthermore, there is a risk that deposits may form on the pump blades, causing the balance to collapse, which may cause pump failure. Moreover, since the boiling point of the solvent 32 is low, cavitation may occur if the pump suction pressure is low. Thus, in the latter device, stable operation cannot be expected due to the presence of the circulation pump 38.

本発明は、このような従来装置における問題を
すべて解決して、実用性に優れ且つ安定した運転
を行いうる蒸気洗浄装置を提供することを目的と
するものである。
It is an object of the present invention to provide a steam cleaning apparatus that is highly practical and capable of stable operation by solving all of the problems with conventional apparatuses.

(問題点を解決するための手段) 本発明の蒸気洗浄装置は、上記の目的を達成す
べく、特に、蒸気洗浄槽の外部に、上下端部を
夫々加熱溶剤吐出管及び被加熱溶剤導入管を介し
て蒸気洗浄層の溶剤貯溜部に連通接続した傾斜状
の溶剤加熱管を、該溶剤貯溜部の液面位置より下
方位に位置せしめて配設すると共に、前記溶剤加
熱管内の溶剤を加熱する溶剤加熱手段を設けたも
のである。
(Means for Solving the Problems) In order to achieve the above-mentioned object, the steam cleaning apparatus of the present invention is provided with a heated solvent discharge pipe and a heated solvent inlet pipe provided at the upper and lower ends of the steam cleaning tank, respectively. An inclined solvent heating tube is connected to the solvent storage section of the steam cleaning layer via the solvent storage section, and is positioned below the liquid level of the solvent storage section, and the solvent in the solvent heating tube is heated. The system is equipped with a solvent heating means.

(作用) 溶剤加熱管には、該管が溶剤貯溜部の液面位置
より下方位に位置されていることから、槽内の溶
剤が充満される。そして、この加熱管内の溶剤
(以下「管内溶剤」という。)が溶剤加熱手段によ
り加熱されると、管内溶剤の容積膨張によりそれ
自身に浮力が生じ、また管内溶剤にはその局部的
な沸騰により気泡が発生し、この気泡は、加熱管
が傾斜していることから、加熱管内を上昇してそ
の周りの液も巻き込んだ上昇流を形成し、管内溶
剤の身掛け上の比重が低下する。したがつて、加
熱昇温された管内溶剤は加熱溶剤吐出管から貯溜
部に吐出され、槽内の溶剤を加熱すると共に、比
重差による上昇に伴う減圧効果によつて膨張、蒸
発し、溶剤液面において多量の溶剤蒸気を発生す
る。また、これに伴つて、溶剤が貯溜部から被加
熱溶剤導入管を介して加熱管へと導入され、溶剤
が貯溜部と加熱管との間で循環せしめられること
になる。
(Function) Since the solvent heating tube is located below the liquid level of the solvent reservoir, it is filled with the solvent in the tank. When the solvent in the heating tube (hereinafter referred to as "solvent in the tube") is heated by the solvent heating means, buoyancy is generated due to the volume expansion of the solvent in the tube, and the solvent in the tube is locally boiled. Bubbles are generated, and since the heating tube is inclined, these bubbles rise inside the heating tube and form an upward flow that also involves the surrounding liquid, and the specific gravity of the solvent inside the tube decreases. Therefore, the heated solvent in the tube is discharged from the heated solvent discharge pipe to the storage section, heating the solvent in the tank, and expands and evaporates due to the depressurizing effect accompanying the rise due to the difference in specific gravity, and the solvent liquid Generates large amounts of solvent vapor on surfaces. Further, in conjunction with this, the solvent is introduced from the reservoir to the heating tube via the heated solvent introduction tube, and the solvent is circulated between the reservoir and the heating tube.

(実施例) 以下、本発明の構成を第1図に示す実施例に基
づいて具体的に説明する。
(Example) Hereinafter, the configuration of the present invention will be specifically explained based on the example shown in FIG.

第1図において、1は蒸気洗浄層で、下部には
所定の溶剤2を収容した溶剤貯溜部1a及びこれ
に連通する液面制御部1cが形成されており、溶
剤貯溜部1aの上部には被洗浄物の洗浄を行う洗
浄部1bが形成されている。液面制御部1cには
適宜の液面制御手段3が配設されていて、槽1内
の溶剤液面2aを所定の上限位置(実線位置)と
下限位置(鎖線位置)との範囲に維持しうるよう
になされている。この液面制御手段3は、例えば
第1図に示す如く、上限液位及び下限液位を各々
液位検出器4a,4bで検出し、これに基づいて
溶剤供給管5の弁5aを開閉制御するように構成
されている。
In FIG. 1, reference numeral 1 denotes a steam cleaning layer, at the bottom of which there is formed a solvent storage section 1a containing a predetermined solvent 2 and a liquid level control section 1c communicating with this, and at the top of the solvent storage section 1a. A cleaning section 1b is formed to clean the object to be cleaned. The liquid level control unit 1c is provided with an appropriate liquid level control means 3, which maintains the solvent liquid level 2a in the tank 1 within a predetermined upper limit position (solid line position) and lower limit position (dashed line position). It is made possible to do so. The liquid level control means 3 detects the upper limit liquid level and the lower limit liquid level with liquid level detectors 4a and 4b, respectively, as shown in FIG. 1, and controls the opening and closing of the valve 5a of the solvent supply pipe 5 based on this. is configured to do so.

そして、蒸気洗浄槽1の外部には、溶剤加熱管
6及び溶剤加熱手段7が配設されている。
A solvent heating pipe 6 and a solvent heating means 7 are disposed outside the steam cleaning tank 1.

この溶剤加熱管6は溶剤液面2a位置つまり前
記下限位置より下方位において傾斜状に配置され
ており、その上下端部を夫々加熱溶剤吐出管8及
び被加熱溶剤導入管9を介して前記溶剤貯溜部1
aに連通接続してある。したがつて、溶剤加熱管
6内には常時溶剤が充満されることになる。
The solvent heating tube 6 is arranged in an inclined manner at the solvent liquid level 2a position, that is, below the lower limit position, and its upper and lower ends are connected to the solvent through the heated solvent discharge tube 8 and the heated solvent introduction tube 9, respectively. Storage part 1
It is connected to a. Therefore, the solvent heating tube 6 is always filled with solvent.

ところで、加熱管6の傾斜角度θは、必要とす
る循環溶剤量が得られるように適宜に設定してお
く。すなわち、傾斜角度θを大きくすると浮力の
影響が大きくなり、循環溶剤量を増加させること
ができる。しかし、傾斜角度θを必要以上に大き
くすると、循環溶剤量は増大するものの、同時に
上昇溶剤の減圧沸騰も激しくなるため好ましくな
く、しかも液面2aを加熱管6の上方位に確保し
ておくために必要な溶剤量が多くなつて、設備上
好ましくない。したがつて、加熱管6の傾斜角度
θは、このような点を考慮して設定しておくこと
が望ましい。
Incidentally, the inclination angle θ of the heating tube 6 is appropriately set so as to obtain the required amount of circulating solvent. That is, when the inclination angle θ is increased, the influence of buoyancy becomes greater, and the amount of circulating solvent can be increased. However, if the inclination angle θ is made larger than necessary, the amount of circulating solvent will increase, but at the same time, the boiling under reduced pressure of the ascending solvent will also become more intense, which is undesirable. This increases the amount of solvent required, which is undesirable in terms of equipment. Therefore, it is desirable to set the inclination angle θ of the heating tube 6 in consideration of such points.

また、溶剤加熱手段7はヒートポンプでもつて
構成されている。このヒートポンプ7は、エンジ
ン等により駆動される圧縮機10から凝縮器1
1,膨張弁12,蒸発器13を経て圧縮器10に
至る冷媒の循環経路14を形成してなるユニツト
型のものである。
Further, the solvent heating means 7 is also constituted by a heat pump. This heat pump 7 connects a compressor 10 to a condenser 1 driven by an engine or the like.
1. It is of a unit type, forming a refrigerant circulation path 14 that passes through an expansion valve 12, an evaporator 13, and reaches a compressor 10.

前記凝縮器11は、前記溶剤加熱管6とこれを
囲繞する冷媒流動管15とからなる所謂傾斜型凝
縮器に構成されている。而して、この凝縮器11
内においては、圧縮機10を経た冷媒蒸気は冷媒
流動管15内をその上部の流入口15aから下部
の流出口15bへと流動する間に凝縮液化され、
一方、加熱管6内の溶剤つまり管内溶剤2′に上
記冷媒の凝縮潜熱、凝縮後の顕熱により加熱昇温
される。
The condenser 11 is configured as a so-called inclined condenser, which includes the solvent heating tube 6 and a refrigerant flow tube 15 surrounding the solvent heating tube 6. Therefore, this condenser 11
Inside, the refrigerant vapor that has passed through the compressor 10 is condensed and liquefied while flowing through the refrigerant flow pipe 15 from the upper inlet 15a to the lower outlet 15b.
On the other hand, the solvent in the heating tube 6, that is, the solvent 2' in the tube, is heated and heated by the latent heat of condensation of the refrigerant and the sensible heat after condensation.

また、前記蒸発器13には適宜の回収熱等の熱
源が投与されるが、こ実施例では、洗浄部1bで
の余剰熱を回収して、その回収熱を上記熱源とし
て又はその一部として利用している。すなわち、
前記洗浄部1b内に冷却管17を配設して、循環
ポンプ18により、冷却水を前記蒸発器13と冷
却管17との間で循環させて、循環経路14の冷
媒が蒸発器13内において洗浄部1bで回収した
熱により蒸発気化されると共に、冷却水が蒸発器
13で冷却されて冷却管17に循環されて、洗浄
部1b内を適温に冷却維持するように工夫してあ
る。
Further, a suitable heat source such as recovered heat is supplied to the evaporator 13, but in this embodiment, excess heat from the cleaning section 1b is recovered and the recovered heat is used as the heat source or as a part thereof. We are using. That is,
A cooling pipe 17 is disposed in the cleaning section 1b, and a circulation pump 18 circulates cooling water between the evaporator 13 and the cooling pipe 17, so that the refrigerant in the circulation path 14 is circulated within the evaporator 13. The cooling water is evaporated by the heat recovered in the cleaning section 1b, and the cooling water is cooled in the evaporator 13 and circulated through the cooling pipe 17, so that the inside of the cleaning section 1b is cooled and maintained at an appropriate temperature.

さらに、凝縮器11から膨張弁12に至る循環
経路14部分に、液化冷媒流出口15bの直下位
に配して受液器19を介設し、この受液器19に
より、冷媒凝縮液を冷媒流動管15からこれに滞
留させることなく速やかに流出させて貯溜させ、
もつて凝縮器11において冷媒の凝縮潜熱を充分
利用し得て、管内溶剤2′の加熱を効果的に行わ
しめると共に、冷媒蒸気の膨張弁12への浸入を
確実に防止するように工夫してある。
Furthermore, a liquid receiver 19 is interposed in the circulation path 14 from the condenser 11 to the expansion valve 12 directly below the liquefied refrigerant outlet 15b. It quickly flows out from the flow pipe 15 without being retained therein, and is stored therein.
The latent heat of condensation of the refrigerant can be fully utilized in the condenser 11 to effectively heat the solvent 2' in the pipe, and at the same time, it is devised to reliably prevent refrigerant vapor from entering the expansion valve 12. be.

なお、冷媒凝縮液の冷媒流動管15からの排出
が良好で且つ冷媒蒸気のシヨートパスがなく、し
かも凝縮器11での伝熱面積が充分に確保されて
いるときには、受液器19はこれを省略すること
ができることは勿論であり、また、冷媒循環経路
14には、前記した圧縮機10等の機器の他、必
要に応じてアキユムレータ、油分離器、ドライ
ヤ、フイルタ等を介設しておいても良いことは云
うまでもない。
Note that when the refrigerant condensate is well discharged from the refrigerant flow pipe 15, there is no short pass for refrigerant vapor, and a sufficient heat transfer area is secured in the condenser 11, the liquid receiver 19 is omitted. Of course, the refrigerant circulation path 14 may be equipped with an accumulator, an oil separator, a dryer, a filter, etc., as necessary, in addition to the above-mentioned equipment such as the compressor 10. Needless to say, it's a good thing.

このように構成された蒸気洗浄装置にあつて
は、管内溶剤2′は、凝縮器11内で冷媒の凝縮
潜熱及びその一部の凝縮後の顕熱により加熱昇温
され、その結果生じる管内溶剤2′の容積膨張に
よる浮力と局所的な沸騰による気泡とにより、溶
剤加熱管6の上下部分間に差圧を生じ、管内溶剤
2′が上方に流動し、昇温溶剤が吐出管8から貯
溜部1aに吐出され、貯溜部1aの溶剤2を加熱
すると共に、比重差による上昇流に伴う減圧で膨
張蒸発し、表面において多量の蒸気を発生する。
また、これに伴つて、貯溜部1aの溶剤2が導入
管9から加熱管6へと導入され、溶剤2が貯溜部
1a・凝縮器11間で循環されると共に凝縮器1
1によつて繰り返し加熱され、洗浄部1b内を溶
剤蒸気雰囲気に保持する。
In the steam cleaning device configured in this way, the pipe solvent 2' is heated in the condenser 11 by the latent heat of condensation of the refrigerant and the sensible heat after condensing a part of the refrigerant, and the resulting pipe solvent Due to the buoyancy caused by the volumetric expansion of 2' and the bubbles caused by local boiling, a pressure difference is created between the upper and lower parts of the solvent heating tube 6, the solvent 2' in the tube flows upward, and the heated solvent is discharged from the discharge tube 8 into the reservoir. The solvent 2 is discharged into the storage section 1a, heats the solvent 2 in the storage section 1a, expands and evaporates due to the reduced pressure caused by the upward flow due to the difference in specific gravity, and generates a large amount of steam on the surface.
Along with this, the solvent 2 in the storage section 1a is introduced from the introduction pipe 9 to the heating tube 6, and the solvent 2 is circulated between the storage section 1a and the condenser 11.
1 to maintain the inside of the cleaning section 1b in a solvent vapor atmosphere.

ところで、溶剤2に不純物が溶解、混入してい
る場合、溶剤2を蒸発させると、蒸発部分におい
て含有不純物が析出したり、蒸発部近傍の部材に
付着したりする。このため、管内溶剤2′の加熱
に際しては、管内溶剤2′が完全に蒸発して加熱
管6内に液が存在しなくなる所謂ドライアウト状
態や加熱管6内に液があるにも拘らず伝熱面上に
おいて局所的に大きな気泡が生じる所謂バーンア
ウト状態となるのを避ける必要がある。かかる現
象が生じる原因としては、蒸気洗浄槽内の保有
溶剤量が極めて少なく、常時、加熱管6内に液面
が存在すること、加熱管6の伝熱温度が非常に
高く、伝熱面上で激しく沸騰していること、加
熱管6内の溶剤循環量が加熱熱量に比して少ない
ことが考えられる。
By the way, when impurities are dissolved or mixed in the solvent 2, when the solvent 2 is evaporated, the contained impurities may precipitate in the evaporation part or adhere to members near the evaporation part. For this reason, when heating the solvent 2' in the tube, there is a so-called dry-out state in which the solvent 2' in the tube completely evaporates and no liquid is present in the heating tube 6, or there is a situation where no liquid is present in the heating tube 6, but no liquid is transmitted. It is necessary to avoid a so-called burnout condition in which large bubbles locally form on the hot surface. The reasons why this phenomenon occurs are that the amount of solvent retained in the steam cleaning tank is extremely small and a liquid level always exists in the heating tube 6, and that the heat transfer temperature of the heating tube 6 is extremely high, causing a drop on the heat transfer surface. It is thought that the solvent is boiling violently and that the amount of solvent circulating in the heating tube 6 is small compared to the amount of heating heat.

しかし、上記した蒸気洗浄装置では、前記〜
の原因をすべて排除すべく工夫されており、し
たがつて上記した不都合はこれが全く生じないの
である。
However, in the above-mentioned steam cleaning apparatus, the above-mentioned ~
It has been devised to eliminate all causes of this, and therefore the above-mentioned inconveniences do not occur at all.

すなわち、液面制御手段3により蒸気洗浄槽1
の溶剤液面2aを制御し、常に加熱管6内に溶剤
2′が充満するようにして、前記の原因を排除
している。また、溶剤加熱手段をヒートポンプ7
でもつて構成して、凝縮温度を任意に設定可能な
冷媒の凝縮熱を溶剤加熱源として用い、加熱管6
の伝熱表面温度を適温に保ちうるようにして、前
記の原因を排除している。しかも、このように
管内溶剤2′を最適温度で加熱することから、溶
剤劣化の問題も生じない。さらに、傾斜型凝縮器
11ないし加熱管の傾斜角度θを調整することに
よつて、循環溶剤量の調整を行うことができるよ
うにして、前記の原因を排除している。
That is, the steam cleaning tank 1 is controlled by the liquid level control means 3.
The above-mentioned cause is eliminated by controlling the solvent liquid level 2a so that the heating tube 6 is always filled with the solvent 2'. In addition, the solvent heating means is a heat pump 7.
The heating tube 6
The above-mentioned causes are eliminated by keeping the heat transfer surface temperature at an appropriate temperature. Moreover, since the solvent 2' in the tube is heated at the optimum temperature in this manner, the problem of solvent deterioration does not occur. Further, by adjusting the inclination angle θ of the inclined condenser 11 or the heating tube, the amount of circulating solvent can be adjusted, thereby eliminating the above-mentioned cause.

なお、上記実施例においては、溶剤加熱手段と
してヒートポンプ7を用いて、その凝縮器11
を、溶剤加熱管6とこれを囲繞する冷媒流動管1
5とからなる傾斜型凝縮器に構成したが、溶剤加
熱手段としては、例えば、溶剤加熱管6内の溶剤
2′と該加熱管6の外周囲繞領域に導いた温水、
蒸気、熱媒体油等の加熱流体とを熱交換させるよ
うにするとか、或は溶剤加熱管6に電気ヒータ等
の加熱器を付設して、これによつて管内溶剤2′
を直接加熱するようにしても良い。また、加熱管
6は複数本設置するようにしても良い。
In the above embodiment, the heat pump 7 is used as the solvent heating means, and the condenser 11 of the heat pump 7 is used as the solvent heating means.
, a solvent heating pipe 6 and a refrigerant flow pipe 1 surrounding it.
5, the solvent heating means includes, for example, the solvent 2' in the solvent heating tube 6 and the hot water introduced into the outer peripheral area of the heating tube 6.
The solvent 2' in the pipe may be heated by exchanging heat with a heating fluid such as steam or heat transfer oil, or by attaching a heater such as an electric heater to the solvent heating pipe 6.
may be heated directly. Further, a plurality of heating tubes 6 may be installed.

(発明の効果) 以上の説明から明らかなように、本発明の蒸気
洗浄装置にあつては、前者装置の如く蒸気洗浄槽
内に加熱器を設けないから、蒸気洗浄槽内の清掃
等が容易に行うことができ、実用性に富み且つ既
存の装置をも容易に改造することができる。
(Effects of the Invention) As is clear from the above explanation, in the steam cleaning device of the present invention, unlike the former device, a heater is not provided in the steam cleaning tank, so cleaning the inside of the steam cleaning tank is easy. It is very practical, and existing equipment can be easily modified.

しかも、謂わばエアリフトポンプの原理を応用
して、溶剤を循環させるようにしたものであるか
ら、後者装置のような循環ポンプを必要とせず、
安定した運転を行うことができる。特に、前記実
施例の如く、溶剤加熱手段としてヒートポンプを
使用することによつて、溶剤劣化を確実に防止で
きると共に、循環ポンプを使用しないこととも相
俟つて大幅な省エネルギ化を図ることができる。
Moreover, since the solvent is circulated by applying the principle of an air lift pump, there is no need for a circulation pump like the latter device.
Stable operation is possible. In particular, by using a heat pump as the solvent heating means as in the above embodiment, it is possible to reliably prevent solvent deterioration, and in combination with not using a circulation pump, significant energy savings can be achieved. .

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

第1図は本発明に係る蒸気洗浄装置の一実施例
を示した縦断側面図であり、第2図及び第3図は
夫々従来の蒸気洗浄装置を示した縦断側面図であ
る。 1……蒸気洗浄槽、1a……溶剤貯溜部、1b
……洗浄部、2……溶剤、2′……管内溶剤(溶
剤加熱管内の溶剤)、2a……溶剤液面、6……
溶剤加熱管、7……ヒートポンプ(溶剤加熱手
段)、8……加熱溶剤吐出管、9……被加熱溶剤
導入管、11……凝縮器、15……冷媒流動管。
FIG. 1 is a longitudinal sectional side view showing one embodiment of a steam cleaning apparatus according to the present invention, and FIGS. 2 and 3 are longitudinal sectional side views showing conventional steam cleaning apparatuses, respectively. 1...Steam cleaning tank, 1a...Solvent reservoir, 1b
...Cleaning section, 2...Solvent, 2'...Solvent in the tube (solvent in the solvent heating tube), 2a...Solvent liquid level, 6...
Solvent heating pipe, 7... Heat pump (solvent heating means), 8... Heated solvent discharge pipe, 9... Heated solvent introduction pipe, 11... Condenser, 15... Refrigerant flow pipe.

Claims (1)

【特許請求の範囲】 1 蒸気洗浄槽の外部に、上下端部を夫々加熱溶
剤吐出管及び被加熱溶剤導入管を介して蒸気洗浄
槽の溶剤貯溜部に連通接続した傾斜状の溶剤加熱
管を、該溶剤貯溜部の液面位置より下方位に位置
せしめて配設すると共に、前記溶剤加熱管内の溶
剤を加熱する溶剤加熱手段を設けたことを特徴と
する蒸気洗浄装置。 2 前記溶剤加熱手段がヒートポンプであり、こ
のヒートポンプの凝縮器が、前記溶剤加熱管とこ
れを囲繞する冷媒流動管とからなることを特徴と
する、特許請求の範囲第1項に記載する蒸気洗浄
装置。 3 前記溶剤加熱手段が、前記溶剤加熱管内の溶
剤と該加熱管の外周囲繞領域に導いた温水、蒸
気、熱媒体油等の加熱流体とを熱交換させるよう
に構成されたものであることを特徴とする、特許
請求の範囲第1項に記載する蒸気洗浄装置。
[Scope of Claims] 1. Outside the steam cleaning tank, there is provided an inclined solvent heating pipe whose upper and lower ends are connected to the solvent reservoir of the steam cleaning tank through a heated solvent discharge pipe and a heated solvent introduction pipe, respectively. 2. A steam cleaning device, comprising: a solvent heating means disposed below the liquid level of the solvent reservoir and heating the solvent in the solvent heating tube. 2. Steam cleaning according to claim 1, wherein the solvent heating means is a heat pump, and the condenser of the heat pump is composed of the solvent heating tube and a refrigerant flow tube surrounding the solvent heating tube. Device. 3. The solvent heating means is configured to exchange heat between the solvent in the solvent heating tube and a heating fluid such as hot water, steam, or heat medium oil led to the outer peripheral area of the heating tube. A steam cleaning device according to claim 1, characterized in that:
JP28711186A 1986-12-02 1986-12-02 Steam washer Granted JPS63141687A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28711186A JPS63141687A (en) 1986-12-02 1986-12-02 Steam washer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28711186A JPS63141687A (en) 1986-12-02 1986-12-02 Steam washer

Publications (2)

Publication Number Publication Date
JPS63141687A JPS63141687A (en) 1988-06-14
JPH0355193B2 true JPH0355193B2 (en) 1991-08-22

Family

ID=17713201

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28711186A Granted JPS63141687A (en) 1986-12-02 1986-12-02 Steam washer

Country Status (1)

Country Link
JP (1) JPS63141687A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6057832B2 (en) * 2013-05-07 2017-01-11 東洋ゴム工業株式会社 Tire cleaning method and tire cleaning apparatus for cleaning tire surface
JP2015020108A (en) * 2013-07-18 2015-02-02 株式会社Ihi Vacuum cleaning device

Also Published As

Publication number Publication date
JPS63141687A (en) 1988-06-14

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