JP2535466B2 - Equipment for cleaning objects to be cleaned using flammable solvent - Google Patents
Equipment for cleaning objects to be cleaned using flammable solventInfo
- Publication number
- JP2535466B2 JP2535466B2 JP3298405A JP29840591A JP2535466B2 JP 2535466 B2 JP2535466 B2 JP 2535466B2 JP 3298405 A JP3298405 A JP 3298405A JP 29840591 A JP29840591 A JP 29840591A JP 2535466 B2 JP2535466 B2 JP 2535466B2
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- solvent
- tank
- steam
- cleaned
- 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
Links
Landscapes
- Cleaning By Liquid Or Steam (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Manufacturing Of Printed Wiring (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、電子部品、機械部品、
プリント基板等の可燃性溶剤を用いた被洗浄物の洗浄装
置に係るものである。BACKGROUND OF THE INVENTION The present invention relates to electronic parts, mechanical parts,
The present invention relates to a cleaning device for an object to be cleaned using a flammable solvent such as a printed circuit board.
【0002】[0002]
【従来の技術】従来、電子部品、機械部品、プリント基
板等の被洗浄物の洗浄には、特公平3ー49633号公
報、実開平1ー179784号公報、特開昭56ー11
5676号公報、特開昭54ー11396号公報及び特
開平3ー101881号公報記載の発明の如く、洗浄力
が優れていること、沸点が低く一液で液洗浄も蒸気洗浄
も行うことができることから、フッ素系有機溶剤や塩素
系有機溶剤が多用されて来た。2. Description of the Related Art Conventionally, for cleaning objects to be cleaned such as electronic parts, mechanical parts, and printed circuit boards, Japanese Examined Patent Publication No. 3-49633, Japanese Utility Model Laid-Open No. 179784, and Japanese Unexamined Patent Publication No. 56-11.
As in the inventions described in Japanese Patent No. 5676, Japanese Patent Application Laid-Open No. 54-11396 and Japanese Patent Application Laid-Open No. 3-101881, it has excellent cleaning power and has a low boiling point and can perform liquid cleaning and vapor cleaning with one liquid. Therefore, fluorine-based organic solvents and chlorine-based organic solvents have been frequently used.
【0003】[0003]
【発明が解決しようとする課題】しかし、フッ素系有機
溶剤や塩素系有機溶剤は、人体に悪影響を与えたり、オ
ゾン層を破壊したりするため使用が規制されるものとな
った。そこで、高沸点可燃性のシリコン系溶剤、炭化水
素系溶剤、親水性溶剤等を洗浄液として使用することが
考慮される。However, the use of fluorine-based organic solvents and chlorine-based organic solvents has been restricted because they adversely affect the human body and destroy the ozone layer. Therefore, it is considered to use a high boiling point flammable silicon solvent, a hydrocarbon solvent, a hydrophilic solvent or the like as the cleaning liquid.
【0004】しかしながら、これらの可燃性溶剤は沸点
が高く、蒸気温度も高いものとなるから、被洗浄物が熱
による変形、変質等を生じるものとなる。従って、現状
ではシリコン系溶剤、炭化水素系溶剤、親水性溶剤等を
蒸気洗浄用の溶剤として使用する事は困難なものであ
る。However, since these flammable solvents have high boiling points and high vapor temperatures, the objects to be cleaned are deformed and deteriorated by heat. Therefore, at present, it is difficult to use a silicon-based solvent, a hydrocarbon-based solvent, a hydrophilic solvent or the like as a solvent for steam cleaning.
【0005】また、可燃性高沸点溶剤を蒸気化すると、
高温蒸気となるため作業上危険であったり、高温化する
ために多くのエネルギーを必要とし、不経済となる欠点
を有している。When the flammable high boiling point solvent is vaporized,
Since it becomes high-temperature steam, it has a drawback in that it is dangerous in operation, and it requires a lot of energy to increase the temperature, which is uneconomical.
【0006】本発明は上述のごとき欠点を除去し、可燃
性高沸点のシリコン系溶剤、炭化水素系溶剤、親水性溶
剤等の高沸点溶剤を、常圧下に於けるよりも低い温度で
沸騰蒸発させ、蒸気洗浄用の溶剤として使用する事を可
能にする。また、被洗浄物の蒸気洗浄と乾燥工程の切り
替えを迅速に行い、効率の良い洗浄作業を可能にする。
また、高沸点の可燃性溶剤を用いて安全な蒸気洗浄を可
能にしようとするものである。The present invention eliminates the above-mentioned drawbacks and evaporates a high-boiling point solvent such as a flammable high-boiling point silicon-based solvent, a hydrocarbon-based solvent or a hydrophilic solvent at a temperature lower than that under normal pressure. And can be used as a solvent for steam cleaning. Further, the steam cleaning and the drying process of the object to be cleaned can be quickly switched to enable efficient cleaning work.
Further, it is intended to enable safe steam cleaning by using a high boiling point combustible solvent.
【0007】[0007]
【課題を解決するための手段】本発明は上述のごとき課
題を解決するため、沸点100℃〜200℃の、シリコ
ン系溶剤、炭化水素系溶剤、親水性溶剤の1種または2
種以上を選択的に用いた高沸点溶剤を加熱する加熱機構
を設けるとともに凝縮器を介して減圧機構に接続し、内
部を連続的に減圧可能とする蒸気発生槽と、この蒸気発
生槽と制御弁を介して連通可能に形成するとともに凝縮
器を介して減圧機構に接続し、内部を連続的に減圧し得
る被洗浄物の洗浄槽とから成るものである。In order to solve the above-mentioned problems, the present invention uses one or two of a silicon-based solvent, a hydrocarbon-based solvent and a hydrophilic solvent having a boiling point of 100 to 200 ° C.
A steam generation tank that is equipped with a heating mechanism that heats a high boiling point solvent that selectively uses one or more species and that is connected to a decompression mechanism via a condenser to enable continuous decompression of the inside, and control with this steam generation tank The cleaning tank is formed so as to be able to communicate with each other through a valve, is connected to a decompression mechanism through a condenser, and is capable of continuously decompressing the inside of a cleaning tank for an object to be cleaned.
【0008】また、蒸気発生槽と被洗浄物の洗浄槽と
は、圧力調整弁を介して減圧機構に接続し、蒸気発生槽
内及び被洗浄物の洗浄槽内の圧力を任意に調整し得るも
のとしたものであっても良い。Further, the steam generating tank and the cleaning tank for cleaning the object to be cleaned can be connected to a pressure reducing mechanism via a pressure adjusting valve so that the pressures in the steam generating tank and the cleaning tank for the object to be cleaned can be adjusted arbitrarily. It may be a thing.
【0009】[0009]
【作用】本発明は上述のごとく構成したものであるか
ら、被洗浄物の洗浄にあたっては、被洗浄物の材質、被
洗浄物に付着した汚物等を考慮して沸点100℃〜20
0℃の、シリコン系溶剤、炭化水素系溶剤、親水性溶剤
の1種または2種以上を選択する。そして、この高沸点
溶剤により溶剤を連続的に減圧する減圧雰囲気内で蒸気
を発生させる。Since the present invention is configured as described above, in cleaning the object to be cleaned, the boiling point is 100 ° C. to 20 ° C. in consideration of the material of the object to be cleaned, the dirt attached to the object to be cleaned, and the like.
One kind or two kinds or more of a silicon-based solvent, a hydrocarbon-based solvent and a hydrophilic solvent at 0 ° C. is selected. Then, vapor is generated in a depressurized atmosphere in which the solvent is continuously depressurized by the high boiling point solvent.
【0010】また、本願明細書において、連続的に減圧
するとは、蒸気発生時から洗浄完了時まで絶え間無く減
圧機構を作動させることを意味せず、減圧雰囲気の減圧
状態を持続的に維持する事を意味するものである。そし
て、減圧機構は減圧状態に応じて断続作動させることも
可能である。Further, in the present specification, continuous depressurization does not mean that the depressurizing mechanism is continuously operated from the time when steam is generated to the time when cleaning is completed, but the depressurized state of the depressurized atmosphere is continuously maintained. Is meant. The decompression mechanism can also be operated intermittently according to the decompression state.
【0011】この蒸気は、連続的に減圧する減圧雰囲気
内で発生させるものであるから、常圧下で溶剤を沸騰し
て発生させる場合よりも低い温度で発生し、この低い蒸
気温度で被洗浄物の蒸気洗浄を行う事ができる。そのた
め、高温には耐えられない素材の被洗浄物であっても、
汚物除去に最適の溶剤を選択して、低い温度での蒸気洗
浄を行うことが可能となる。Since this vapor is generated in a decompressed atmosphere in which the pressure is continuously reduced, it is generated at a lower temperature than when it is generated by boiling a solvent under normal pressure. It can be used for steam cleaning. Therefore, even if the object to be cleaned is a material that cannot withstand high temperatures,
It is possible to select the optimum solvent for removing dirt and perform steam cleaning at a low temperature.
【0012】その結果、従来は浸漬洗浄、シャワー洗浄
等の液洗浄にしか使用できなかった、沸点100℃〜2
00℃の、シリコン系溶剤、炭化水素系溶剤、親水性溶
剤等の高沸点溶剤を、蒸気洗浄に使用することができ
る。そのため、フッ素系有機溶剤や塩素系有機溶剤を使
用することなく、環境に悪影響を及ぼすことのない蒸気
洗浄を可能とする。As a result, the boiling point of 100 ° C. to 2 ° C. has been conventionally usable only for liquid cleaning such as immersion cleaning and shower cleaning.
A high boiling point solvent such as a silicon-based solvent, a hydrocarbon-based solvent, or a hydrophilic solvent at 00 ° C. can be used for vapor cleaning. Therefore, it is possible to perform vapor cleaning without adversely affecting the environment without using a fluorine-based organic solvent or a chlorine-based organic solvent.
【0013】また、蒸気発生槽、洗浄槽等の内部が連続
的に減圧され、内部の空気が希薄なものとなるため、溶
剤に可燃性のものを選択しても、引火の危険を大幅に減
少することができるものである。Further, since the inside of the steam generation tank, cleaning tank, etc. is continuously decompressed and the air inside becomes lean, even if a flammable solvent is selected, there is a great risk of ignition. It can be reduced.
【0014】また、減圧雰囲気内の気圧を任意に設定し
得るものとすれば、減圧の度合いを変えて、種々の蒸気
温度を得ることにより、素材の異なる被洗浄物を1種類
の溶剤で行う事ができ、減圧の度合いを1つとした場合
に比較し、更に作業性を向上し、溶剤の種類を減らす事
ができるものである。Further, if the atmospheric pressure in the reduced pressure atmosphere can be arbitrarily set, the degree of the reduced pressure is changed to obtain various vapor temperatures so that the objects to be cleaned having different materials can be treated with one kind of solvent. It is possible to improve the workability and reduce the number of kinds of solvents as compared with the case where the degree of pressure reduction is set to one.
【0015】また、蒸気発生槽と洗浄槽とは制御弁を介
して接続しているから、蒸気洗浄の完了後被洗浄物の乾
燥を行う場合に、制御弁を閉止することにより洗浄槽に
溶剤蒸気の流入が無くなり、蒸気洗浄完了後に真空状態
を強くすることにより、沸点を更に低下させ真空乾燥を
無駄なく迅速に行うことができる。また、この真空乾燥
によって洗浄槽内の可燃性溶剤蒸気は排出され存在しな
いから、被洗浄物を取り出すために蓋体の開放を行って
も引火等の危険を生じることが無いものである。Further, since the steam generation tank and the cleaning tank are connected via a control valve, when the object to be cleaned is dried after completion of the steam cleaning, the control valve is closed to remove the solvent in the cleaning tank. By eliminating the inflow of steam and strengthening the vacuum state after the completion of steam cleaning, the boiling point can be further lowered and vacuum drying can be quickly performed without waste. Further, since the flammable solvent vapor in the cleaning tank is not discharged by the vacuum drying, there is no danger of ignition even if the lid is opened to take out the object to be cleaned.
【0016】また、可燃性溶剤に、沸点が100℃〜2
00℃の高沸点溶剤を用いているから、引火の危険が少
なく、消防法上の規制も受ける事が少なく、在庫管理が
容易となる。また、高沸点溶剤は在庫中に於ける自然の
蒸発消耗が少なくランニングコストを低くすることがで
きる。The boiling point of the flammable solvent is 100 ° C. to 2 ° C.
Since a high boiling point solvent of 00 ° C is used, the risk of ignition is low, the regulations under the Fire Service Law are low, and inventory management is easy. In addition, the high boiling point solvent has less natural evaporation and consumption in inventory, and the running cost can be reduced.
【0017】[0017]
【実施例】以下本発明の第1実施例を図1に於いて説明
すれば、(1)は蒸気発生槽で、沸点が100℃〜200
℃の可燃性高沸点溶剤(2)を加熱する加熱機構(3)を設
けて、蒸気発生部(4)としている。この加熱機構(3)は
可燃性高沸点溶剤(2)中に位置させた加熱コイル(5)内
に加熱スチームを導入して行う。この加熱スチームは、
供給源から電磁弁(6)、ニードルバルブ(7)を介して加
熱コイル(5)に導入し、この加熱コイル(5)を介して溶
剤(2)と熱交換を行った後、凝縮した水分を、スチーム
トラップ(8)を介して外部に排出する。また圧力計(1
0)による加熱スチームの圧力監視を行う。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described below with reference to FIG. 1. (1) is a steam generating tank having a boiling point of 100.degree.
A heating mechanism (3) for heating the flammable high-boiling point solvent (2) at ℃ is provided as a vapor generating part (4). This heating mechanism (3) is carried out by introducing heating steam into a heating coil (5) located in a flammable high boiling point solvent (2). This heating steam is
Water is introduced from the supply source to the heating coil (5) via the solenoid valve (6) and the needle valve (7), and after exchanging heat with the solvent (2) via the heating coil (5), condensed water Is discharged to the outside through the steam trap (8). In addition, pressure gauge (1
The pressure of the heating steam according to 0) is monitored.
【0018】また、電磁弁(6)は溶剤(2)のサーモコン
トローラー(11)と接続し、開閉弁操作を行う。また、
蒸気発生槽(1)内は、圧力計(12)、圧力スイッチ(1
3)等により常時内部圧力を監視し、万一、異常昇圧が
生じた場合には安全弁(14)を作動させて内部圧力を減
少する。Further, the solenoid valve (6) is connected to the thermo controller (11) for the solvent (2) to open / close the valve. Also,
Inside the steam generation tank (1), pressure gauge (12) and pressure switch (1
The internal pressure is constantly monitored by 3) or the like, and if an abnormal pressure rise occurs, the safety valve (14) is activated to reduce the internal pressure.
【0019】また、蒸気発生槽(1)は、上部方向に冷却
コイル(15)を巻き回して凝縮部(16)を形成してい
る。この冷却コイル(15)には、冷却水の導入管(17)
と排出管(18)を接続し、凝縮部(16)で凝縮した溶剤
を、水分分離器(20)で水分と分離した後、蒸気発生槽
(1)内に還流する。The steam generating tank (1) has a condenser (16) formed by winding a cooling coil (15) in the upper direction. This cooling coil (15) has a cooling water inlet pipe (17)
And the discharge pipe (18) are connected to each other, and the solvent condensed in the condenser (16) is separated from the water in the water separator (20), and then the steam generation tank.
Reflux into (1).
【0020】また蒸気発生槽(1)は、バキュームポン
プ、アスピレーター等の減圧機構(24)を接続し、内部
を連続的に減圧可能としている。この減圧機構(24)
は、圧力調整弁(25)を介して蒸気発生槽(1)に接続
し、蒸気発生槽(1)内の減圧度合いを任意に調整し得る
ものとしている。また、この蒸気発生槽(1)とは別個に
洗浄槽(38)を形成し、この洗浄槽(38)の内部で、被
洗浄物(21)の蒸気洗浄を行う。Further, the steam generation tank (1) is connected to a decompression mechanism (24) such as a vacuum pump or an aspirator so that the inside can be continuously depressurized. This decompression mechanism (24)
Is connected to the steam generation tank (1) via a pressure regulating valve (25), and the degree of pressure reduction in the steam generation tank (1) can be arbitrarily adjusted. Further, a cleaning tank (38) is formed separately from the steam generating tank (1), and the cleaning target (21) is cleaned with steam inside the cleaning tank (38).
【0021】この洗浄槽(38)は、蒸気供給管(42)及
び制御弁(43)を介して蒸気発生槽(1)と連通可能と
し、内部に蒸気洗浄部(22)を形成する。また、蒸気洗
浄部(22)の上部内面には冷却コイル(44)を巻き回し
て凝縮部(45)を設けている。また、この凝縮部(45)
の上部を蓋体(46)で開閉可能に密閉し、被洗浄物(2
1)の出入を可能としている。The cleaning tank (38) can communicate with the steam generating tank (1) through the steam supply pipe (42) and the control valve (43), and forms a steam cleaning section (22) inside. Further, a cooling coil (44) is wound around the inner surface of the upper portion of the steam cleaning section (22) to provide a condenser section (45). Also, this condensing part (45)
The upper part of the lid is closed with a lid (46) so that it can be opened and closed.
It is possible to go in and out of 1).
【0022】また、洗浄槽(38)は減圧機構(24)に接
続し、内部を連続的に減圧し得るものとする。この減圧
機構(24)と洗浄槽(38)との接続は、圧力調整弁(2
5)との間に開閉弁(47)を設けて行っている。Further, the cleaning tank (38) is connected to the pressure reducing mechanism (24) so that the inside can be continuously depressurized. The pressure reducing mechanism (24) and the cleaning tank (38) are connected to each other through the pressure regulating valve (2
An on-off valve (47) is provided between the above and 5).
【0023】また、蒸気発生槽(1)及び蒸気洗浄槽(3
8)内を減圧する過程で減圧機構(24)方向に吸引され
る洗浄蒸気は、凝縮器(26)によって凝縮液化する。こ
の凝縮器(26)は、内部に冷却水(27)を充填流動し、
この冷却水(27)内にバキュームパイプ(28)を浸漬す
ることにより、洗浄蒸気の凝縮液化を行う。また、この
バキュームパイプ(28)には、開閉弁(47)よりも圧力
調整弁(25)側に、蒸気発生槽(1)の凝縮部(16)に連
通する凝縮パイプ(49)を接続している。またこの凝縮
パイプ(49)には第6開閉弁(60)を配置している。Further, the steam generation tank (1) and the steam cleaning tank (3
The cleaning vapor sucked toward the decompression mechanism (24) in the process of decompressing the inside of (8) is condensed and liquefied by the condenser (26). This condenser (26) is filled with cooling water (27) to flow inside,
By immersing the vacuum pipe (28) in the cooling water (27), the cleaning vapor is condensed and liquefied. A condenser pipe (49) communicating with the condenser section (16) of the steam generation tank (1) is connected to the vacuum pipe (28) on the pressure regulating valve (25) side of the on-off valve (47). ing. Further, a sixth on-off valve (60) is arranged in this condensing pipe (49).
【0024】この凝縮液化した溶剤は、電磁弁(30)を
介して減圧機構(24)で吸引し、溶剤槽(31)に貯留す
るとともに還流用電磁弁(29)を設けたオーバーフロー
管(32)を介して蒸気発生槽(1)の蒸気発生部(4)に還
流している。また、この溶剤槽(31)は溶剤(2)の上部
に空間部(33)を設け、この空間部(33)に排気管(3
4)を挿入している。The condensed and liquefied solvent is sucked by the pressure reducing mechanism (24) through the electromagnetic valve (30) and stored in the solvent tank (31) and the overflow pipe (32) provided with the reflux electromagnetic valve (29). ) To the steam generating section (4) of the steam generating tank (1). Further, the solvent tank (31) is provided with a space (33) above the solvent (2), and the exhaust pipe (3) is provided in the space (33).
4) is inserted.
【0025】上述のごとく構成したものに於いて、被洗
浄物(21)の蒸気洗浄を行うには、まず第6開閉弁(6
0)を開弁し蒸気発生槽(1)を減圧して蒸気を発生させ
た後、開閉弁(47)を開弁して洗浄槽(38)の内部を減
圧する。そして、洗浄槽(38)の内部を蒸気発生槽(1)
と略同一の気圧とした時に、制御弁(43)を開弁し洗浄
槽(38)の蒸気洗浄部(22)に、蒸気発生槽(1)の洗浄
蒸気を導入し、被洗浄物(21)の蒸気洗浄を行う。この
場合に、第6開閉弁(60)を開弁したままでも良いが、
これを閉止すれば洗浄槽(38)の減圧効率を更に良いも
のとする事ができる。In the above structure, in order to perform the steam cleaning of the object to be cleaned (21), first, the sixth on-off valve (6
0) is opened to depressurize the steam generation tank (1) to generate steam, and then the on-off valve (47) is opened to depressurize the inside of the cleaning tank (38). Then, inside the cleaning tank (38), the steam generation tank (1)
When the atmospheric pressure is about the same as the above, the control valve (43) is opened and the cleaning steam of the steam generating tank (1) is introduced into the steam cleaning section (22) of the cleaning tank (38) to clean the object to be cleaned (21). ) Perform steam cleaning. In this case, the sixth on-off valve (60) may be left open,
If this is closed, the decompression efficiency of the cleaning tank (38) can be further improved.
【0026】このように、蒸気発生槽(1)及び洗浄槽
(38)内を連続的に減圧して洗浄蒸気を発生するため、
可燃性高沸点溶剤(2)の沸点を常圧よりも低くすること
ができる。その結果、従来は行うことができなかった、
シリコン系溶剤、炭化水素系溶剤、親水性溶剤等の可燃
性高沸点溶剤を洗浄液として使用することが可能とな
る。そして、前述したごとく、高温には耐えられない素
材の被洗浄物(21)であっても、上記の溶剤を選択して
低い温度での蒸気洗浄を行うことが可能となる。As described above, the steam generation tank (1) and the cleaning tank
Since the pressure inside (38) is continuously reduced to generate cleaning vapor,
The boiling point of the flammable high boiling point solvent (2) can be made lower than atmospheric pressure. As a result, it could not be done in the past,
It becomes possible to use a flammable high-boiling point solvent such as a silicon-based solvent, a hydrocarbon-based solvent, or a hydrophilic solvent as the cleaning liquid. Then, as described above, even if the material to be cleaned (21) that cannot withstand high temperature is selected, the solvent can be selected to perform steam cleaning at low temperature.
【0027】また、蒸気洗浄部(22)内の気圧を任意に
設定できるから、減圧の度合いを変えて、種々の蒸気温
度を得ることにより、素材の異なる被洗浄物(21)を1
種類の溶剤(2)で、浸漬洗浄から蒸気洗浄まで行う事が
できる。Further, since the atmospheric pressure in the steam cleaning section (22) can be arbitrarily set, the degree of pressure reduction can be changed to obtain various steam temperatures, so that the objects to be cleaned (21) of different materials can be
Dipping and steam cleaning can be performed with the same type of solvent (2).
【0028】次ぎに、蒸気洗浄の完了した被洗浄物(2
1)を乾燥するには制御弁(43)を閉止して洗浄槽(3
8)への蒸気の供給を停止する。この蒸気の供給停止に
より、減圧機構(24)により連続的に減圧している洗浄
槽(38)内は、急速に残留蒸気が排除されるとともに減
圧度合いを強くすることにより、減圧雰囲気内の沸点が
蒸気洗浄時よりも下がるから、迅速な乾燥を可能とす
る。また、乾燥完了後に蓋体(46)を開放して被洗浄物
(21)を取り出す場合にも、可燃性蒸気は洗浄槽(38)
内に存在しないから、引火の危険が無く安全な作業を行
うことができる。Next, the cleaning object (2
To dry 1), close control valve (43) and wash tank (3
Stop the supply of steam to 8). By stopping the supply of the steam, the residual pressure of the cleaning tank (38), which is continuously decompressed by the decompression mechanism (24), is rapidly eliminated, and the degree of decompression is strengthened, so that the boiling point in the decompression atmosphere Is lower than that during steam cleaning, enabling quick drying. Also, after the drying is completed, the lid (46) is opened to clean the object to be cleaned.
Even when taking out (21), the combustible vapor is washed in the washing tank (38).
Since it does not exist inside, there is no danger of ignition and safe work can be performed.
【0029】また、高沸点溶剤(2)の蒸留再生を行うに
は、制御弁(43)、開閉弁(47)を閉止し、第6開閉弁
(60)を開放して高沸点溶剤(2)を加熱すれば、溶剤蒸
気は第6開閉弁(60)、バキュームパイプ(28)を介し
て凝縮器(26)に導かれ凝縮することができる。この凝
縮液は、溶剤槽(31)に溜められ、必要に応じて蒸気発
生槽(1)に導入する。In order to carry out the distillation regeneration of the high boiling point solvent (2), the control valve (43) and the on-off valve (47) are closed, and the sixth on-off valve is closed.
When the high boiling point solvent (2) is heated by opening (60), the solvent vapor can be guided to the condenser (26) through the sixth opening / closing valve (60) and the vacuum pipe (28) and condensed. . This condensate is stored in the solvent tank (31) and, if necessary, introduced into the steam generation tank (1).
【0030】[0030]
【発明の効果】本発明は上述のごとく構成したものであ
るから、環境、人体等に悪影響を及ぼすフッ素系有機溶
剤や塩素系有機溶剤を用いずに、環境、人体等に影響の
少ない、沸点100℃〜200℃の、シリコン系溶剤、
炭化水素系溶剤、親水性溶剤等の高沸点溶剤を用いなが
ら、低い蒸気温度で被洗浄物の蒸気洗浄を行う事がで
き、耐熱性の低い素材の被洗浄物の蒸気洗浄が可能とな
る。EFFECTS OF THE INVENTION Since the present invention is configured as described above, it has a small boiling point that does not affect the environment or human body without using a fluorine-based organic solvent or chlorine-based organic solvent that adversely affects the environment or human body. Silicon-based solvent at 100 ° C to 200 ° C,
While using a high boiling point solvent such as a hydrocarbon solvent or a hydrophilic solvent, it is possible to perform the vapor cleaning of the object to be cleaned at a low vapor temperature, and it is possible to perform the vapor cleaning of the object to be cleaned of a material having low heat resistance.
【0031】その結果、耐熱性の低い被洗浄物でも、1
種類の溶剤で洗浄が可能となり、洗浄作業の手数を大幅
に減少できる。また、溶剤の在庫を少なくし経済的であ
ると共に多種類の溶剤を在庫とする事から生じる、火災
等の危険を防止できる。As a result, even if the object to be cleaned has low heat resistance,
Cleaning can be performed with different types of solvents, and the number of cleaning operations can be greatly reduced. In addition, the inventory of the solvent is reduced, which is economical, and the risk of fire or the like caused by inventorying many kinds of solvents can be prevented.
【0032】また、溶剤に、沸点が100℃〜200℃
の高沸点溶剤を用いるから、引火の危険が少なく、消防
法上の規制も受ける事が少ないとともに、高沸点溶剤は
在庫中に於ける自然の蒸発消耗が少なくランニングコス
トを低くすることができ、在庫管理も容易となる。The solvent has a boiling point of 100 ° C. to 200 ° C.
Since it uses a high boiling point solvent, it is less likely to catch fire and is less subject to regulations under the Fire Service Act, and the high boiling point solvent has less natural evaporation and consumption in inventory and can reduce running costs, Inventory management becomes easy.
【0033】また、蒸気発生槽、洗浄槽等の内部が連続
的に減圧され、内部の空気が希薄なものとなるため、溶
剤に可燃性のものを選択しても、引火の危険を大幅に減
少することができ、安全な洗浄作業を可能とする。Further, since the inside of the steam generating tank, the cleaning tank, etc. is continuously decompressed and the air inside becomes lean, even if a flammable solvent is selected, the risk of ignition is greatly increased. It is possible to reduce the number, and it enables safe cleaning work.
【0034】また、蒸気発生槽と洗浄槽とは制御弁を介
して接続しているから、蒸気洗浄の完了後被洗浄物の乾
燥を行う場合に、制御弁を閉止することにより洗浄槽に
溶剤蒸気の流入が無くなるとともに蒸気洗浄時よりも真
空度を高めて沸点を低下することにより、真空乾燥を無
駄なく迅速に行うことができる。また、この真空乾燥に
よって洗浄槽内の可燃性溶剤蒸気は排出され存在しない
から、被洗浄物を取り出すために蓋体の開放を行っても
引火等の危険を生じることが無いものである。Further, since the steam generation tank and the cleaning tank are connected via the control valve, when the object to be cleaned is dried after completion of the steam cleaning, the control valve is closed to remove the solvent in the cleaning tank. By eliminating the inflow of steam and increasing the degree of vacuum and lowering the boiling point as compared with the time of steam cleaning, vacuum drying can be performed quickly without waste. Further, since the flammable solvent vapor in the cleaning tank is not discharged by the vacuum drying, there is no danger of ignition even if the lid is opened to take out the object to be cleaned.
【0035】また、減圧雰囲気内の気圧を任意に設定し
得るものとすれば、減圧の度合いを変えて、種々の蒸気
温度を得ることにより、素材の異なる被洗浄物を1種類
の溶剤で、浸漬洗浄から蒸気洗浄まで、または蒸気洗浄
のみを、行う事ができ、減圧の度合いを1つとした場合
に比較し、更に作業性を向上し、溶剤の種類を減らす事
ができるものである。Further, if the atmospheric pressure in the depressurized atmosphere can be arbitrarily set, the degree of depressurization is changed to obtain various vapor temperatures, so that the objects to be cleaned having different materials can be treated with one solvent, From the immersion cleaning to the steam cleaning, or only the steam cleaning can be performed, and the workability can be further improved and the kinds of the solvent can be reduced as compared with the case where the degree of pressure reduction is one.
【0036】また、蒸気洗浄を行わない場合は、複数の
弁の開閉を行うことにより、容易に蒸留再生器として使
用することができるから、装置の多目的な使用を可能と
し経済的で廉価な装置とすることができる。Further, when steam cleaning is not carried out, it can be easily used as a distillation regenerator by opening and closing a plurality of valves, so that the apparatus can be used for multiple purposes and is economical and inexpensive. Can be
【図1】第1実施例を示す概略断面図である。FIG. 1 is a schematic cross-sectional view showing a first embodiment.
1 蒸気発生槽 2 溶剤 3 加熱機構 21 被洗浄物 22 蒸気洗浄部 24 減圧機構 25 圧力調整弁 26 凝縮器 38 洗浄槽 43 制御弁 1 Steam Generation Tank 2 Solvent 3 Heating Mechanism 21 Object to be Washed 22 Steam Cleaning Section 24 Pressure Reduction Mechanism 25 Pressure Adjustment Valve 26 Condenser 38 Cleaning Tank 43 Control Valve
フロントページの続き (56)参考文献 特開 昭56−115676(JP,A) 特開 昭54−113965(JP,A) 特開 平3−101881(JP,A) 特開 平3−140485(JP,A) 特開 平3−293072(JP,A) 特開 平2−198678(JP,A) 特開 平2−83074(JP,A) 特開 昭60−55611(JP,A) 特開 昭59−10379(JP,A) 実開 平1−179784(JP,U) 実開 平1−163486(JP,U) 実開 昭63−193588(JP,U) 特公 平3−49633(JP,B2) 特公 平1−46162(JP,B2) 特公 昭50−16589(JP,B2) 特公 平6−11435(JP,B2)Continuation of front page (56) Reference JP-A-56-115676 (JP, A) JP-A-54-113965 (JP, A) JP-A-3-101881 (JP, A) JP-A-3-140485 (JP , A) JP 3-293072 (JP, A) JP 2-198678 (JP, A) JP 2-83074 (JP, A) JP 60-55611 (JP, A) JP 59-10379 (JP, A) Actually open 1-179784 (JP, U) Actually open 1-163486 (JP, U) Actually open 63-193588 (JP, U) JP-B 3-49633 (JP, B2) Japanese Patent Publication 1-46162 (JP, B2) Japanese Patent Publication 50-16589 (JP, B2) Japanese Publication 6-11435 (JP, B2)
Claims (2)
溶剤、炭化水素系溶剤、親水性溶剤の1種または2種以
上を選択的に用いた高沸点溶剤を加熱する加熱機構を設
けるとともに凝縮器を介して減圧機構に接続し、内部を
連続的に減圧可能とする蒸気発生槽と、この蒸気発生槽
と制御弁を介して連通可能に形成するとともに凝縮器を
介して減圧機構に接続し、内部を連続的に減圧し得る被
洗浄物の洗浄槽とから成ることを特徴とする可燃性溶剤
を用いた被洗浄物の洗浄装置。1. A heating mechanism for heating a high boiling point solvent having a boiling point of 100 ° C. to 200 ° C., which is a selective use of one or more of a silicon-based solvent, a hydrocarbon-based solvent and a hydrophilic solvent, and is condensed. It is connected to a pressure reducing mechanism via a condenser, and a steam generating tank that can continuously reduce the pressure inside is formed so that it can communicate with this steam generating tank via a control valve, and it is connected to a pressure reducing mechanism via a condenser. And a cleaning tank for cleaning an object to be continuously depressurized, the apparatus for cleaning an object using a flammable solvent.
力調整弁を介して減圧機構に接続し、蒸気発生槽内及び
被洗浄物の洗浄槽内の圧力を任意に調整し得るものとし
た事を特徴とする請求項1記載の可燃性溶剤を用いた被
洗浄物の洗浄装置。2. The steam generating tank and the cleaning tank for cleaning the object to be cleaned are connected to a pressure reducing mechanism via a pressure adjusting valve, and the pressures inside the steam generating tank and the cleaning tank for cleaning the object to be cleaned can be arbitrarily adjusted. The cleaning device for an object to be cleaned using the flammable solvent according to claim 1, wherein
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3298405A JP2535466B2 (en) | 1991-10-17 | 1991-10-17 | Equipment for cleaning objects to be cleaned using flammable solvent |
| TW81110340A TW204306B (en) | 1991-10-17 | 1992-12-24 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3298405A JP2535466B2 (en) | 1991-10-17 | 1991-10-17 | Equipment for cleaning objects to be cleaned using flammable solvent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05123658A JPH05123658A (en) | 1993-05-21 |
| JP2535466B2 true JP2535466B2 (en) | 1996-09-18 |
Family
ID=17859286
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3298405A Expired - Lifetime JP2535466B2 (en) | 1991-10-17 | 1991-10-17 | Equipment for cleaning objects to be cleaned using flammable solvent |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP2535466B2 (en) |
| TW (1) | TW204306B (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0754179A (en) * | 1993-08-06 | 1995-02-28 | Kimura Chem Plants Co Ltd | Washing / drying device |
| JPH07171301A (en) * | 1993-12-08 | 1995-07-11 | Japan Field Kk | Distillation regeneration device and steam cleaning device using this distillation regeneration device |
| JPH07185202A (en) * | 1993-12-28 | 1995-07-25 | Japan Field Kk | Distillation regeneration device and cleaning device using this distillation regeneration device |
| JP3634718B2 (en) * | 1996-07-25 | 2005-03-30 | アクア化学株式会社 | Cleaning device |
| JP3096241B2 (en) * | 1996-07-25 | 2000-10-10 | アクア化学株式会社 | Cleaning equipment |
| JP4225985B2 (en) * | 2005-06-01 | 2009-02-18 | ジャパン・フィールド株式会社 | Method and apparatus for cleaning object to be cleaned |
| JP6306257B1 (en) * | 2017-09-20 | 2018-04-04 | 正英 内野 | Cleaning method for removing contaminated grease from objects to be cleaned with grease |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54113965A (en) * | 1978-02-27 | 1979-09-05 | Paakaa Netsushiyori Kougiyou K | Solvent washing method and its device |
| JPS54154166A (en) * | 1978-05-26 | 1979-12-05 | Nippon Kakouki Kougiyou Kk | Solvent vapor dispersion preventive method in washer for organic solvent |
| JPS56115676A (en) * | 1980-02-15 | 1981-09-10 | Paakaa Netsushiyori Kogyo Kk | Solvent washing method and its device |
| JPS62169420A (en) * | 1986-01-22 | 1987-07-25 | Hitachi Tokyo Electron Co Ltd | Surface treatment method and device |
| JPH0767552B2 (en) * | 1986-05-29 | 1995-07-26 | 株式会社日立製作所 | Cleaning equipment |
| JPS6373934U (en) * | 1986-10-31 | 1988-05-17 | ||
| JPH0529113Y2 (en) * | 1987-05-29 | 1993-07-26 | ||
| JP2562036B2 (en) * | 1987-09-21 | 1996-12-11 | 日本石油化学株式会社 | Dry soap |
| JPH01179784U (en) * | 1988-06-03 | 1989-12-25 | ||
| JP2582627B2 (en) * | 1988-08-25 | 1997-02-19 | 株式会社トクヤマ | Cleaning method and apparatus |
| JPH0389985A (en) * | 1989-05-29 | 1991-04-15 | Japan Fuirudo Kk | Method and apparatus for washing object to be washed |
| JP2795415B2 (en) * | 1989-07-14 | 1998-09-10 | 株式会社シマノ | Fishing rod |
| JPH0611435B2 (en) * | 1989-09-18 | 1994-02-16 | 山崎化学工業株式会社 | Vacuum cleaning device |
| JPH03152545A (en) * | 1989-11-09 | 1991-06-28 | Minolta Camera Co Ltd | Production of photosensitive body |
-
1991
- 1991-10-17 JP JP3298405A patent/JP2535466B2/en not_active Expired - Lifetime
-
1992
- 1992-12-24 TW TW81110340A patent/TW204306B/zh active
Also Published As
| Publication number | Publication date |
|---|---|
| TW204306B (en) | 1993-04-21 |
| JPH05123658A (en) | 1993-05-21 |
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