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JP7141768B1 - Cleaning equipment for objects to be cleaned - Google Patents

Cleaning equipment for objects to be cleaned Download PDF

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JP7141768B1
JP7141768B1 JP2021117856A JP2021117856A JP7141768B1 JP 7141768 B1 JP7141768 B1 JP 7141768B1 JP 2021117856 A JP2021117856 A JP 2021117856A JP 2021117856 A JP2021117856 A JP 2021117856A JP 7141768 B1 JP7141768 B1 JP 7141768B1
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365mfc
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JP2023013565A (en
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正英 内野
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Japan Field Co Ltd
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Abstract

【課題】多大なコストをかけることなく、地球環境に配慮するとともに人体にも悪影響を及ぼしにくい洗浄を可能とする。【解決手段】沸点差が少ないHFC-365mfcとHFO-1233zd(z)とを、洗浄目的に応じた混合比にて混合した混合溶剤16を洗浄槽1内に収納し、この洗浄槽1内の混合溶剤16による被洗浄物15の液洗浄、及び/又は、当該混合溶剤を加熱して発生させた洗浄蒸気17による蒸気洗浄を行うとともに、この液洗浄及び/又は蒸気洗浄に使用した混合溶剤16を蒸留再生することにより、当該混合溶剤16を再利用可能とする。【選択図】図1Kind Code: A1 To enable cleaning that does not adversely affect the human body while giving consideration to the global environment without incurring a great deal of cost. SOLUTION: A mixed solvent 16 in which HFC-365mfc and HFO-1233zd(z) having a small boiling point difference are mixed at a mixing ratio according to the purpose of cleaning is contained in the cleaning tank 1, and Liquid cleaning of the object to be cleaned 15 with the mixed solvent 16 and/or steam cleaning with the cleaning steam 17 generated by heating the mixed solvent, and the mixed solvent 16 used for this liquid cleaning and/or steam cleaning By distilling and regenerating the mixed solvent 16, the mixed solvent 16 can be reused. [Selection drawing] Fig. 1

Description

本発明は、混合溶剤にて機械部品、電子部品、医療機器等の被洗浄物を洗浄するための洗浄装置に係るものである。 TECHNICAL FIELD The present invention relates to a cleaning apparatus for cleaning objects to be cleaned, such as mechanical parts, electronic parts, and medical equipment, with a mixed solvent.

特開2000-36478号公報 従来広く使われていたフッ素系溶剤のフロン113や塩素系溶剤の1.1.1.トリクロロエタンは、1995年、世界的にオゾン層破壊で全廃となった。その後、洗浄業界では安易に使用できる洗浄溶剤として、毒性の強いトリクロロエチレンやパークロロエチレン、塩化メチレン等が未だ使用されている。これらの洗浄溶剤は発がん性物質とも言われており人体に悪影響を及ぼすおそれがある。そして特許文献1に示す如く、HFCやHFEなどの洗浄溶剤が単独で、あるいは他の溶剤と混合して一般的に使用されている。CITATION LIST Patent Literature Patent Literature 1: Japanese Unexamined Patent Application Publication No. 2000-36478 SUMMARY OF THE INVENTION In 1995, the fluorine-based solvent Freon 113 and the chlorine-based solvent 1.1.1. Since then, highly toxic trichlorethylene, perchlorethylene, methylene chloride, and the like are still used as cleaning solvents that can be easily used in the cleaning industry. These cleaning solvents are said to be carcinogenic substances and may adversely affect the human body. As shown in Patent Document 1, cleaning solvents such as HFC and HFE are generally used alone or mixed with other solvents.

また洗浄業界では洗浄溶剤として石油系溶剤が多く使われているが、この石油系溶剤の沸点は170℃~220℃程度と高いものであるため、減圧しなければ蒸気洗浄が困難なものである。更に石油系溶剤は可燃性であって火災の危険性がある。そのため、石油系溶剤を洗浄溶剤として用いる場合には既存の洗浄装置では対応が困難となることから、専用の新たな設備投資が必要となる。従って、このような洗浄装置を取り扱う多くの中小企業にとっては、設備投資に多大な費用を投じる必要があるためコスト面などを考慮すると対応が困難なものとなっていた。 In the cleaning industry, petroleum-based solvents are often used as cleaning solvents, but since the boiling point of these petroleum-based solvents is as high as 170°C to 220°C, steam cleaning is difficult unless the pressure is reduced. . Furthermore, petroleum solvents are flammable and pose a fire hazard. Therefore, when a petroleum-based solvent is used as a cleaning solvent, it is difficult to deal with it with existing cleaning equipment, and new dedicated equipment investment is required. Therefore, for many small and medium-sized enterprises dealing with such cleaning equipment, it is necessary to invest a large amount of money in facility investment, and it has been difficult to deal with it in consideration of the cost aspect.

そこで本願では上述の如き課題を解決しようとするものであって、多大なコストをかけることなく、地球環境に配慮するとともに人体にも悪影響を及ぼしにくい洗浄を可能にしようとするものである。 Therefore, the present invention is intended to solve the above-mentioned problems, and is intended to enable cleaning that does not adversely affect the human body while giving consideration to the global environment without incurring a great deal of cost.

来よりHFC-365mfc及びHFO-1233zd(z)は、それぞれ洗浄溶剤として広く知られている。しかし、HFC-365mfcは安価であるという利点はあるものの、地球温暖化係数が高い上に脱脂力が弱く用途が限られている。一方、HFO-1233zd(z)は地球温暖化係数が低く脱脂力は高いという利点はあるものの、現時点では量産されておらず価格が高いため単体で使用する場合にはコストが高くつくものである。そのため、HFC-365mfc単体、あるいはHFO-1233zd(z)単体での洗浄溶剤としての使用は上記のようなデメリットがあることから、一般的に使用することは困難となっていた。そこで本願発明者はHFC-365mfcとHFO-1233zd(z)との沸点差が小さい点に着目し、両者を混合した混合溶剤を開発するに至った。 HFC -365mfc and HFO-1233zd(z) are widely known as cleaning solvents. However, although HFC-365mfc has the advantage of being inexpensive, its use is limited due to its high global warming potential and weak degreasing power. On the other hand, although HFO-1233zd(z) has the advantages of low global warming potential and high degreasing power, it is not mass-produced at present and is expensive, so when used alone, the cost is high. . Therefore, it has been difficult to use HFC-365mfc alone or HFO-1233zd(z) alone as a cleaning solvent because of the disadvantages described above. Therefore, the inventors of the present application paid attention to the fact that the boiling point difference between HFC-365mfc and HFO-1233zd(z) was small, and came to develop a mixed solvent in which both are mixed.

即ち、HFC-365mfcの沸点が40.2℃、HFO-1233zd(z)の沸点が39℃と沸点差が小さい。一般的に、異なる二液を混合させた混合溶剤については従来より使用されているが、異なる二液を混合・加熱して蒸気を発生させた場合には、各液の沸点差によりどちらか一方が先に蒸発するものとなる。そのため、二液を混合・加熱した後の混合溶剤の混合割合が変化するという問題が生じていた。また、より沸点差の大きい二液の混合溶剤の再利用を試みた場合、各液において蒸発時間に著しい差が生じるため、沸点の高い溶剤は蒸気発生槽内に汚液とともに滞留するため再利用が困難なものとなっていた。 That is, HFC-365mfc has a boiling point of 40.2°C and HFO-1233zd(z) has a boiling point of 39°C. In general, a mixed solvent in which two different liquids are mixed has been conventionally used, but when two different liquids are mixed and heated to generate steam, one of them is will evaporate first. Therefore, there is a problem that the mixing ratio of the mixed solvent after the two liquids are mixed and heated changes. Also, when trying to reuse a two-liquid mixed solvent with a larger boiling point difference, there is a significant difference in the evaporation time of each liquid. was difficult.

方混合溶剤を構成する各液の沸点差が極めて少ない場合には、当該混合溶剤を沸点近傍まで加熱することによりほぼ同時に蒸気が発生するため、どちらか一方のみ蒸発するという事態が生じにくく、残留した混合溶剤の各液の混合比が大きく変化することはない。また当該混合溶剤による液洗浄あるいは蒸気洗浄後にこの混合溶剤を蒸留した場合には、ほぼ同時に蒸留再生を行うことができる。そのため、混合溶剤であるにもかかわらず、単体で使用した場合と同様の手順により混合溶剤を回収し再利用することが可能となり、当該混合溶剤の管理が容易となる。 On the other hand, if the difference in boiling points between the liquids that make up the mixed solvent is extremely small, heating the mixed solvent to near the boiling point will generate steam almost simultaneously, so it is unlikely that only one of them will evaporate. , the mixing ratio of each liquid in the remaining mixed solvent does not change significantly. Further, when the mixed solvent is distilled after liquid cleaning or vapor cleaning with the mixed solvent, distillation regeneration can be carried out almost simultaneously. Therefore, even though it is a mixed solvent, the mixed solvent can be recovered and reused by the same procedure as when used alone, and the mixed solvent can be easily managed.

またHFC-365mfcとHFO-1233zd(z)との混合比を変化させることにより、使用目的に応じた混合溶剤を得ることができる。例えば、HFC-365mfcとHFO-1233zd(z)との混合比を変化させて脱脂力の強弱を調整したり、HFO-1233zd(z)の混合割合を多くすることにより環境への負荷を軽減したり、逆にHFC-365mfcの混合割合を多くすることにより価格を低廉なものにすることが可能となる。 By changing the mixing ratio of HFC-365mfc and HFO-1233zd(z), it is possible to obtain a mixed solvent suitable for the purpose of use. For example, the mixing ratio of HFC-365mfc and HFO-1233zd(z) can be changed to adjust the strength of the degreasing power, or the mixing ratio of HFO-1233zd(z) can be increased to reduce the burden on the environment. On the other hand, by increasing the mixing ratio of HFC-365mfc, the price can be lowered.

また、上記混合溶剤は、HFC-365mfcにHFO-1233zd(z)を加え、更にハイドロカーボンを溶解することにより洗浄力を向上可能としたものであっても良い。HFC-365mfc単体では石油系溶剤に溶解しにくいものであるが、このHFC-365mfcにHFO-1233zd(z)を添加することにより石油系溶剤にも溶解するものとなる。そしてこの混合溶剤に、更に石油系溶剤であるハイドロカーボンを溶解させることにより、脱脂洗浄力を効果的に高めることが以下の実験より明らかとなっている。 Further, the above-mentioned mixed solvent may be one in which HFO-1233zd(z) is added to HFC-365mfc and a hydrocarbon is further dissolved to improve detergency. HFC-365mfc alone is difficult to dissolve in petroleum solvents, but by adding HFO-1233zd(z) to this HFC-365mfc, it becomes soluble in petroleum solvents. The following experiment has revealed that the degreasing power can be effectively enhanced by further dissolving a hydrocarbon, which is a petroleum-based solvent, in this mixed solvent.

またハイドロカーボンは安価であるため、HFC-365mfcとHFO-1233zd(z)との混合液に添加することにより、低コストで脱脂洗浄力の優れた洗浄溶剤を得ることが可能となり、被洗浄物への適用範囲を拡大することができる。 In addition, since hydrocarbons are inexpensive, by adding them to the mixed solution of HFC-365mfc and HFO-1233zd(z), it is possible to obtain a low-cost cleaning solvent with excellent degreasing power. can expand the scope of application to

ここで、HFC-365mfcにHFO-1233zd(z)を加え、ハイドロカーボンを溶解した混合溶剤による被洗浄物からの油の除去能力を確認するため、以下の試験を行った。
試験1:混合溶剤の相溶性について
(HFC-365mfcとハイドロカーボンとの混合試験)
室温下でHFC-365mfc 150mlとハイドロカーボン150mlとを混合した場合、これら二液はほとんど溶け合わず、二層に分離した。
(HFC-365mfc、HFO-1233zd(z)、及びハイドロカーボンの混合試験)
室温下でHFC-365mfc 150ml、HFO-1233zd(z) 150ml、ハイドロカーボン50mlを混合した結果、各液が分離することなく溶けあって透明な混合溶剤を得ることができた。
Here, HFO-1233zd(z) was added to HFC-365mfc, and the following test was conducted in order to confirm the ability of the mixed solvent in which hydrocarbons were dissolved to remove oil from the object to be cleaned.
Test 1: Regarding compatibility of mixed solvents
(Mixing test of HFC-365mfc and hydrocarbon)
When 150 ml of HFC-365mfc and 150 ml of hydrocarbon were mixed at room temperature, the two liquids hardly dissolved and separated into two layers.
(HFC-365mfc, HFO-1233zd(z), and hydrocarbon mixture test)
150 ml of HFC-365mfc, 150 ml of HFO-1233zd(z) and 50 ml of hydrocarbon were mixed at room temperature.

試験2:混合溶剤による被洗浄物に付着した油の除去能力について
(被洗浄物)
50mm×50mmのSUS製の平板
(洗浄溶剤)
(a) HFC-365mfc
(b) HFO-1233zd(z)
(c) HFC-365mfcとHFO-1233zd(z)との混合比1:1の混合溶剤
(d) HFC-365mfcとHFO-1233zd(z)とハイドロカーボンとの混合比3:3:1の混合溶剤
(加工油)
レータス150(株式会社ジャパンエナジー製)
(試験方法)
1 室温下で被洗浄物を加工油浴に浸す。
2 加工油浴から被洗浄物を取り出して、油が滴下しなくなるまで油切りを行う。
3 油切りした被洗浄物を上記(a)~(d)の各洗浄溶剤に浸漬して3分間揺動洗浄を行う。
4 液切り乾燥を行う。
5 目視(肉眼)にて被洗浄物に加工油が残留しているかどうかを確認する。
Test 2: Ability to remove oil adhering to the object to be cleaned by mixed solvent (object to be cleaned)
50mm x 50mm SUS flat plate (cleaning solvent)
(a) HFC-365mfc
(b) HFO-1233zd(z)
(c) Mixed solvent of HFC-365mfc and HFO-1233zd(z) at a mixing ratio of 1:1
(d) Mixed solvent (processing oil) with a mixing ratio of 3:3:1 of HFC-365mfc, HFO-1233zd(z) and hydrocarbon
Latus 150 (manufactured by Japan Energy Co., Ltd.)
(Test method)
1 Immerse the object to be cleaned in a working oil bath at room temperature.
2 Remove the object to be cleaned from the processing oil bath and drain the oil until the oil stops dripping.
3. After draining the oil, the object to be cleaned is immersed in each of the above cleaning solvents (a) to (d) and rocked for 3 minutes.
4 Drain and dry.
5. Visually (with the naked eye) confirm whether or not processing oil remains on the object to be cleaned.

上記試験を行った結果、洗浄溶剤(a)HFC-365mfcについては油切り時に被洗浄物に付着していた加工油が残留しており加工油をほとんど溶解できないことが確認できた。また洗浄溶剤(b) HFO-1233zd(z)を用いた場合には、油切り時に被洗浄物に付着していた加工油が残留していなかった。また洗浄溶剤(c) HFC-365mfcとHFO-1233zd(z)との混合比1:1の混合溶剤を使用した場合には、油切り時に被洗浄物に付着していた加工油が部分的に残留していることが確認された。また洗浄溶剤(d) HFC-365mfcとHFO-1233zd(z)とハイドロカーボンとの混合比3:3:1の混合溶剤を用いた場合には、被洗浄物に付着していた加工油が残留していなかった。 As a result of the above test, it was confirmed that the cleaning solvent (a) HFC-365mfc could hardly dissolve the processing oil that had adhered to the object to be cleaned when the oil was removed. When the cleaning solvent (b) HFO-1233zd(z) was used, no processing oil remained on the object to be cleaned when the oil was removed. In addition, when using a mixed solvent (c) HFC-365mfc and HFO-1233zd(z) at a mixing ratio of 1:1, the processing oil that adhered to the object to be cleaned when the oil was removed was partially removed. confirmed to remain. Also, when using a mixed solvent (d) HFC-365mfc, HFO-1233zd(z) and hydrocarbon in a mixing ratio of 3:3:1, the processing oil adhering to the object to be cleaned remains. I didn't.

以上の結果より、HFC-365mfcにHFO-1233zd(z)を加え、更にハイドロカーボンを溶解することにより、被洗浄物に付着していた加工油を、HFC-365mfcとHFO-1233zd(z)との混合溶剤よりも更に効果的に溶解除去することができることが明らかとなった。そのため、プレス油やしぼり油のような粘性が高い汚れも容易に除去することができる混合溶剤を得ることが可能となる。 From the above results , by adding HFO-1233zd(z) to HFC-365mfc and further dissolving the hydrocarbon, the processing oil adhering to the object to be cleaned was It became clear that dissolution and removal can be performed more effectively than a mixed solvent with. Therefore, it is possible to obtain a mixed solvent that can easily remove highly viscous contaminants such as press oil and wringing oil.

また、上記混合溶剤は、HFC-365mfcよりもHFO-1233zd(z)の混合量を多くすることにより、HFO-1233zd(z)単体で使用した場合、HFC-365mfcとHFO-1233zd(z)とを同量とした場合、あるいはHFO-1233zd(z)よりもHFC-365mfcの混合量を多くした場合と比較して、地球温暖化率を低減可能となる。 In addition, by increasing the mixed amount of HFO-1233zd(z) than HFC-365mfc, the above mixed solvent can be used as HFC-365mfc and HFO-1233zd(z). The rate of global warming can be reduced compared to when the amount of HFC-365mfc is the same as that of HFO-1233zd(z), or when the amount of HFC-365mfc is greater than that of HFO-1233zd(z).

本願発明は、沸点差が少ないHFC-365mfcとHFO-1233zd(z)とを混合した混合溶剤を内部に収納するとともに、当該混合溶剤の洗浄蒸気を冷却するための冷却機構を開口部側に設け、被洗浄物の液洗浄、蒸気洗浄、及び/又は自熱乾燥を行う洗浄槽と、上記混合溶剤を収納するとともに、当該混合溶剤を加熱して洗浄蒸気を発生させる加熱機構を備え、当該洗浄蒸気を上記洗浄槽に移送するための移送管を設けた蒸気発生槽と、当該蒸気発生槽と上記洗浄槽との間に設けるとともに当該洗浄槽からの混合溶剤を蒸気発生槽内に回収可能とする回収管とを備えたものである。 In the present invention, a mixed solvent of HFC-365mfc and HFO-1233zd(z) with a small boiling point difference is stored inside, and a cooling mechanism for cooling the cleaning vapor of the mixed solvent is provided on the opening side. , a cleaning tank for liquid cleaning, steam cleaning, and/or autothermal drying of an object to be cleaned; A steam generation tank provided with a transfer pipe for transferring steam to the cleaning tank, and a steam generation tank provided between the steam generation tank and the cleaning tank and capable of recovering the mixed solvent from the cleaning tank into the steam generation tank. and a recovery tube.

本発明は上記の如く構成したものであって、HFC-365mfcの沸点が40.2℃、HFO-1233zd(z)が39℃と沸点差が小さいことから、当該混合溶剤を沸点近傍まで加熱することによりほぼ同時に蒸気が発生するため、どちらか一方のみ蒸発するという事態が生じにくく混合溶剤の各液の混合比が大きく変化しない。そのため混合溶剤の性質を一定に保つことができるため当該混合溶剤の管理が容易となり、特別な装置を必要とすることなく既存の装置を利用して洗浄作業を行うことができるため、洗浄コストを安価なものとすることが可能となる。 The present invention is configured as described above, and the boiling point of HFC-365mfc is 40.2°C, and the boiling point difference of HFO-1233zd(z) is 39°C. As a result, vapors are generated almost at the same time, so that the situation in which only one of the liquids evaporates is unlikely to occur, and the mixing ratio of each liquid in the mixed solvent does not change significantly. Therefore, the properties of the mixed solvent can be kept constant, making it easier to manage the mixed solvent, and cleaning can be performed using existing equipment without the need for special equipment, reducing cleaning costs. It is possible to make it inexpensive.

また本発明の混合溶剤による液洗浄あるいは上記洗浄後、再利用のためにこの混合溶剤を蒸留した場合にほぼ同時に蒸留再生ができるため、混合溶剤であるにもかかわらず、単体で使用した場合と同様の手順により蒸留再生液を回収することができることから、混合溶剤の再利用を単体の場合と同様に容易に行うことが可能となり、持続可能な社会への貢献に資するものである。 In addition, when this mixed solvent is distilled for reuse after liquid cleaning with the mixed solvent of the present invention or the above cleaning, distillation and regeneration can be performed almost at the same time. Since the distilled regenerated liquid can be recovered by the same procedure, the mixed solvent can be easily reused in the same way as the single solvent, which contributes to a sustainable society.

またHFC-365mfcとHFO-1233zd(z)との混合比を変化させることにより、使用目的に応じた混合溶剤を得ることができる。例えば、HFC-365mfcとHFO-1233zd(z)との混合比を変化させて脱脂力の強弱を調整したり、HFO-1233zd(z)の混合割合を多くすることにより環境への負荷を軽減したり、更にはHFC-365mfcの混合割合を多くすることにより混合溶剤を安価なものとすることが可能となる。 By changing the mixing ratio of HFC-365mfc and HFO-1233zd(z), it is possible to obtain a mixed solvent suitable for the purpose of use. For example, the mixing ratio of HFC-365mfc and HFO-1233zd(z) can be changed to adjust the strength of the degreasing power, or the mixing ratio of HFO-1233zd(z) can be increased to reduce the burden on the environment. Furthermore, by increasing the mixing ratio of HFC-365mfc, the mixed solvent can be made inexpensive.

本願発明を示す実施例1の概念図。BRIEF DESCRIPTION OF THE DRAWINGS The conceptual diagram of Example 1 which shows this invention.

本願発明の実施例1を図1に於いて説明すると、(1)は洗浄槽であって、この洗浄槽 (1)の開口部(2)付近には、本発明の冷却機構を構成する第1冷却管(3)を設けるとともに、底部側には、第2冷却管(4)を設けている。またこの洗浄槽(1)の隣には、図1に示す如く蒸気発生槽(5)を設けている。この蒸気発生槽(5)の開口部(6)側には、第3冷却管(7)を設けるとともに、底部側には本発明の加熱機構を構成するヒーター(8)及び温度センサー(10)を設けている。 Embodiment 1 of the present invention will be described with reference to FIG. A first cooling pipe (3) is provided, and a second cooling pipe (4) is provided on the bottom side. A steam generation tank (5) is provided next to the washing tank (1) as shown in FIG. A third cooling pipe (7) is provided on the opening (6) side of the steam generation tank (5), and a heater (8) and a temperature sensor (10) constituting the heating mechanism of the present invention are provided on the bottom side. is provided.

そして、当該蒸気発生槽(5)と洗浄槽(1)との間には、開閉弁(11)を備えた移送管(12)を設けており、両者を連通可能なものとしている。また当該移送管(12)の下方には、上記洗浄槽(1)と蒸気発生槽(5)との間に、洗浄槽(1)側から蒸気発生槽(5)の底部側に向かって下るように傾斜した回収管(13)が設けられており、当該回収管(13)を通じて洗浄槽(1)と蒸気発生槽(5)とが常時連通した状態となっている。 A transfer pipe (12) having an on-off valve (11) is provided between the steam generation tank (5) and the cleaning tank (1) so that the two can communicate with each other. In addition, below the transfer pipe (12), between the cleaning tank (1) and the steam generation tank (5), from the cleaning tank (1) toward the bottom side of the steam generation tank (5) A collection pipe (13) inclined as shown is provided, and the washing tank (1) and the steam generation tank (5) are in constant communication through the collection pipe (13).

そして上記の如く構成した被洗浄物(15)の洗浄装置を用いた洗浄方法について以下に説明する。まず、洗浄槽(1)内には、HFC-365mfcとHFO-1233zd(z)とを混合させて成る混合溶剤(16)を収納し、当該洗浄槽(1)内の第2冷却管(4)にてこの混合溶剤(16)を冷却しておく。ここで、HFC-365mfcの沸点が40.2℃、HFO-1233zd(z)が39℃と沸点差が小さいことから、当該混合溶剤(16)を沸点近傍まで加熱することによりほぼ同時に蒸気が発生する。そのため、どちらか一方のみ蒸発するという事態が生じにくく混合溶剤(16)の各液の混合比が大きく変化しないことから、混合溶剤(16)の性質を一定に保つことが可能となり当該混合溶剤(16)の管理が容易となる。 A cleaning method using the cleaning apparatus for the object to be cleaned (15) constructed as described above will be described below. First, in the cleaning tank (1), a mixed solvent (16) obtained by mixing HFC-365mfc and HFO-1233zd(z) is contained, and the second cooling pipe (4) in the cleaning tank (1) ) to cool the mixed solvent (16). Here, HFC-365mfc has a boiling point of 40.2°C and HFO-1233zd(z) has a boiling point difference of 39°C. do. Therefore, it is unlikely that only one of the liquids evaporates, and the mixing ratio of the liquids in the mixed solvent (16) does not change significantly. 16) can be easily managed.

尚、この各溶剤の混合比は、使用目的に応じて適宜変更することができる。例えば、HFC-365mfcとHFO-1233zd(z)との混合比を変化させて脱脂力の強弱を調整したり、HFO-1233zd(z)の混合割合を多くすることにより環境への負荷を軽減したり、更にはHFC-365mfcの混合割合を多くすることにより混合溶剤(16)を安価なものにしたりすることが可能となる。 The mixing ratio of each solvent can be appropriately changed according to the purpose of use. For example, the mixing ratio of HFC-365mfc and HFO-1233zd(z) can be changed to adjust the strength of the degreasing power, or the mixing ratio of HFO-1233zd(z) can be increased to reduce the burden on the environment. Further, by increasing the mixing ratio of HFC-365mfc, the mixed solvent (16) can be made inexpensive.

また、本実施例ではHFC-365mfcとHFO-1233zd(z)とを混合した混合溶剤(16)を用いているが、他の異なる実施例ではHFC-365mfcにHFO-1233zd(z)を加え、更に石油系溶剤であるハイドロカーボンを溶解させることにより、脱脂洗浄力を効果的に高めることも可能である。更にハイドロカーボンは安価であるため、HFC-365mfcとHFO-1233zd(z)との混合液に添加することにより、低コストで脱脂洗浄力の優れた洗浄溶剤を得ることが可能となり、被洗浄物(15)への適用範囲を拡大することができる。 In this example, the mixed solvent (16) in which HFC-365mfc and HFO-1233zd(z) are mixed is used. Further, by dissolving a hydrocarbon, which is a petroleum solvent, it is possible to effectively enhance the degreasing power. Furthermore, since hydrocarbons are inexpensive, by adding them to the mixture of HFC-365mfc and HFO-1233zd(z), it is possible to obtain a low-cost cleaning solvent with excellent degreasing and cleaning power. The scope of application to (15) can be expanded.

また蒸気発生槽(5)にも同様に、上記の如く洗浄槽(1)内に収納した混合溶剤(16)と同じ混合比の混合溶剤(16)を収納しておく。そして、当該蒸気発生槽(5)内の混合溶剤(16)をヒーター(8)にてHFC-365mfc及びHFO-1233zd(z)の沸点以上に加熱することによって、当該蒸気発生槽(5)内に混合溶剤(16)の洗浄蒸気(17)を発生させておく。尚、当該混合溶剤(16)の温度は温度センサー(10)により常時管理されている。 Similarly, the steam generation tank (5) contains a mixed solvent (16) having the same mixing ratio as the mixed solvent (16) contained in the cleaning tank (1) as described above. Then, by heating the mixed solvent (16) in the steam generation tank (5) with the heater (8) to the boiling point of HFC-365mfc and HFO-1233zd(z) or higher, the inside of the steam generation tank (5) The cleaning steam (17) of the mixed solvent (16) is generated in advance. The temperature of the mixed solvent (16) is constantly controlled by the temperature sensor (10).

上記の如く構成した洗浄装置を用いた被洗浄物(15)の洗浄方法について以下に説明する。まず、上記洗浄槽(1)内の混合溶剤(16)を第2冷却管(4)により冷却しておく。また上記移送管(12)の開閉弁(11)を閉止した状態で、蒸気発生槽(5)のヒーター(8)を作動させ、この蒸気発生槽(5)内の混合溶剤(16)をHFC-365mfcとHFO-1233zd(z)の沸点以上に加熱させて、当該混合溶剤(16)の洗浄蒸気(17)を予め発生させておく。 A method for cleaning the object to be cleaned (15) using the cleaning apparatus configured as described above will be described below. First, the mixed solvent (16) in the washing tank (1) is cooled by the second cooling pipe (4). In addition, with the on-off valve (11) of the transfer pipe (12) closed, the heater (8) of the steam generation tank (5) is operated to convert the mixed solvent (16) in the steam generation tank (5) into HFC. -365mfc and HFO-1233zd(z) are heated to above the boiling point to generate cleaning vapor (17) of the mixed solvent (16) in advance.

このような状態において、上記洗浄槽(1)の混合溶剤(16)中に被洗浄物(15)を浸漬し、液洗浄を行う。そして液洗浄が完了した後、当該被洗浄物(15)を図1に示す如く混合溶剤(16)の液面(14)よりも上方に配置する。そして、移送管(12)の開閉弁(11)を開放することにより、蒸気発生槽(5)内にて発生させた洗浄蒸気(17)を洗浄槽(1)内に移送させる。これにより、洗浄槽(1)内に流入した洗浄蒸気(17)が被洗浄物(15)に接触するものとなり、被洗浄物(15)の蒸気洗浄が行われる。そしてこの蒸気洗浄が終了した後、図1に示す如く被洗浄物(15)を洗浄槽(1)の開口部(2)付近の位置に移動させて、当該位置にて自熱乾燥を行うことにより、一連の洗浄作業が完了する。 In such a state, the object to be cleaned (15) is immersed in the mixed solvent (16) in the cleaning tank (1) for liquid cleaning. After the liquid cleaning is completed, the object to be cleaned (15) is placed above the liquid surface (14) of the mixed solvent (16) as shown in FIG. By opening the on-off valve (11) of the transfer pipe (12), the cleaning steam (17) generated in the steam generation tank (5) is transferred into the cleaning tank (1). As a result, the cleaning steam (17) flowing into the cleaning tank (1) comes into contact with the object to be cleaned (15), and the object to be cleaned (15) is steam cleaned. After completion of this steam cleaning, the object to be cleaned (15) is moved to a position near the opening (2) of the cleaning tank (1) as shown in FIG. 1, and autothermal drying is performed at that position. This completes a series of cleaning operations.

ここで、蒸気洗浄時に使用した洗浄槽(1)内の洗浄蒸気(17)は、当該洗浄槽(1)内に設けた第1冷却管(3)により蒸留液化されて洗浄槽(1)内の混合溶剤(16)中に回収される。また液洗浄時において、洗浄槽(1)内の混合溶剤(16)により被洗浄物(15)が冷却されるため、当該被洗浄物(15)に付着した洗浄蒸気(17)もこの冷却された被洗浄物(15)の表面にて凝縮液化され、当該被洗浄物(15)に付着していた汚れとともに混合溶剤(16)中に滴下し回収される。 Here, the cleaning steam (17) in the cleaning tank (1) used for steam cleaning is distilled and liquefied by the first cooling pipe (3) provided in the cleaning tank (1). is recovered in a mixed solvent (16) of During the liquid cleaning, the object to be cleaned (15) is cooled by the mixed solvent (16) in the cleaning tank (1), so the cleaning steam (17) adhering to the object to be cleaned (15) is also cooled. The condensate condenses on the surface of the object (15) to be cleaned, drops into the mixed solvent (16), and is collected together with the dirt adhering to the object (15).

そして、上記の如き洗浄蒸気(17)の液化回収により洗浄槽(1)内の混合溶剤(16)の液面(14)が上昇した場合には、この液面(14)が回収管(13)の連通口まで達した時点でオーバーフローして回収管(13)から蒸気発生槽(5)内に回収されるものとなる。 When the liquid level (14) of the mixed solvent (16) in the cleaning tank (1) rises due to the liquefaction recovery of the cleaning steam (17) as described above, the liquid level (14) rises to the recovery pipe (13). ), it overflows and is recovered from the recovery pipe (13) into the steam generation tank (5).

そして、上記の如く蒸気発生槽(5)内に回収された混合溶剤(16)は、再び加熱されて洗浄蒸気(17)となり、洗浄槽(1)に移送されて再び蒸気洗浄に使用されるものとなる。このように、本実施例では被洗浄物(15)の液洗浄及び/又は蒸気洗浄に使用した混合溶剤(16)を蒸留再生することが可能であるとともに、更にHFC-365mfcの沸点が40.2℃、HFO-1233zd(z)が39℃と沸点差が小さいことから、混合溶剤(16)であるにもかかわらず単体で使用した場合と同様の手順により蒸留再生液を回収することができるため、混合溶剤(16)の再利用を特別な装置を用いることなく単体の場合と同様に容易に洗浄作業を行うことができる。 Then, the mixed solvent (16) recovered in the steam generation tank (5) as described above is heated again to become cleaning steam (17), transferred to the cleaning tank (1), and used again for steam cleaning. become a thing. Thus, in this embodiment, the mixed solvent (16) used for liquid cleaning and/or steam cleaning of the object (15) to be cleaned can be recycled by distillation. Since the boiling point difference is small at 2°C and HFO-1233zd(z) at 39°C, it is possible to recover the distillate regenerated liquid by the same procedure as when using it alone, even though it is a mixed solvent (16). Therefore, the mixed solvent (16) can be reused and washed as easily as in the case of a single unit without using a special device.

1 洗浄槽
2 開口部
3 第1冷却管
5 蒸気発生槽
8 ヒーター
12 移送管
13 冷媒ガス
13 回収管
15 被洗浄物
16 混合溶剤
17 洗浄蒸気

REFERENCE SIGNS LIST 1 cleaning tank 2 opening 3 first cooling pipe 5 steam generation tank 8 heater 12 transfer pipe 13 refrigerant gas 13 recovery pipe 15 object to be cleaned 16 mixed solvent 17 cleaning steam

Claims (1)

沸点差が少ないHFC-365mfcとHFO-1233zd(z)とを混合した混合溶剤を内部に収納するとともに、当該混合溶剤の洗浄蒸気を冷却するための冷却機構を開口部側に設け、被洗浄物の液洗浄、蒸気洗浄、及び/又は自熱乾燥を行う洗浄槽と、上記混合溶剤を収納するとともに、当該混合溶剤を加熱して洗浄蒸気を発生させる加熱機構を備え、当該洗浄蒸気を上記洗浄槽に移送するための移送管を設けた蒸気発生槽と、当該蒸気発生槽と上記洗浄槽との間に設けるとともに当該洗浄槽からの混合溶剤を蒸気発生槽内に回収可能とする回収管とを備えたことを特徴とする被洗浄物の洗浄装置。 A mixed solvent of HFC-365mfc and HFO-1233zd(z) with a small boiling point difference is stored inside, and a cooling mechanism is provided on the opening side to cool the cleaning steam of the mixed solvent. a cleaning tank for performing liquid cleaning, steam cleaning, and/or autothermal drying; and a heating mechanism that stores the mixed solvent and heats the mixed solvent to generate cleaning steam. a steam generation tank provided with a transfer pipe for transferring to the tank; and a recovery pipe provided between the steam generation tank and the cleaning tank and capable of recovering the mixed solvent from the cleaning tank into the steam generation tank. A cleaning device for an object to be cleaned, comprising:
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Citations (2)

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Publication number Priority date Publication date Assignee Title
JP2016088963A (en) 2014-10-30 2016-05-23 セントラル硝子株式会社 Fluorine-containing olefin composition and cleaning method using the same
JP2020138166A (en) 2019-02-28 2020-09-03 セントラル硝子株式会社 Cleaning method using fluorine-containing organic solvent, preservation method of fluorine-containing organic solvent and recovery method

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JPH04244281A (en) * 1991-01-30 1992-09-01 Japan Field Kk Gas recovery apparatus
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* Cited by examiner, † Cited by third party
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JP2016088963A (en) 2014-10-30 2016-05-23 セントラル硝子株式会社 Fluorine-containing olefin composition and cleaning method using the same
JP2020138166A (en) 2019-02-28 2020-09-03 セントラル硝子株式会社 Cleaning method using fluorine-containing organic solvent, preservation method of fluorine-containing organic solvent and recovery method

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