JP7120592B2 - Vacuum steam cleaning method - Google Patents

Vacuum steam cleaning method Download PDF

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JP7120592B2
JP7120592B2 JP2017241160A JP2017241160A JP7120592B2 JP 7120592 B2 JP7120592 B2 JP 7120592B2 JP 2017241160 A JP2017241160 A JP 2017241160A JP 2017241160 A JP2017241160 A JP 2017241160A JP 7120592 B2 JP7120592 B2 JP 7120592B2
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和彦 岡村
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株式会社クリンビー
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本発明は、被洗浄物に減圧下で洗浄剤の蒸気を接触させて真空蒸気洗浄を行う洗浄機に関する。更に詳しくは、真空蒸気洗浄時における蒸気発生・蒸留再生器に対する洗浄剤の供給・補給の制御を、使用する洗浄剤に応じて適切に行う真空蒸気洗浄方法に関する。 BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning machine that performs vacuum steam cleaning by contacting an object to be cleaned with vapor of a cleaning agent under reduced pressure. More particularly, the present invention relates to a vacuum steam cleaning method for appropriately controlling the supply and replenishment of cleaning agent to a steam generation/distillation regenerator during vacuum steam cleaning according to the cleaning agent used.

金属部品その他の被洗浄物の洗浄には、炭化水素系溶剤その他の溶剤からなる各種の洗浄剤の蒸気を所定の真空状態の下で被洗浄物に接触させる真空蒸気洗浄(減圧蒸気洗浄)が広く採用されている。真空蒸気洗浄は、被洗浄物が投入された密閉状態の真空蒸気洗浄槽を真空引きし、所定の真空状態(減圧状態)を維持しながら、蒸気発生・蒸留再生器から発生する洗浄剤の蒸気を真空蒸気洗浄槽に導入することによって行われる。 Vacuum steam cleaning (depressurized steam cleaning) is used to clean metal parts and other objects to be cleaned by contacting the object to be cleaned with vapors of various cleaning agents made of hydrocarbon solvents and other solvents under a predetermined vacuum condition. Widely adopted. In vacuum steam cleaning, vacuum is drawn from a sealed vacuum steam cleaning tank in which the object to be cleaned is placed, and while a predetermined vacuum state (reduced pressure state) is maintained, steam of the cleaning agent is generated from the steam generator/distillation regenerator. is introduced into the vacuum steam cleaning tank.

真空蒸気洗浄時には、蒸気発生・蒸留再生器に規定量の洗浄剤が貯留され、蒸気として失われる洗浄剤を逐次、補給して、所定量の蒸気発生状態が維持される。そのために、ボールタップ等を用いた液位調整器を介して洗浄剤を補給して、蒸気発生・蒸留再生器の洗浄剤の貯留量を一定に維持している。また、真空蒸気洗浄の終了後等において、蒸気発生・蒸留再生器の残留洗浄剤を排出する際には、液位調整器と蒸気発生・蒸留再生器の洗浄剤供給口との間に配置されている常開弁である煮詰めバルブを閉じて、残量洗浄剤を煮詰めて減容化した後に、外部に廃棄している。例えば、特許文献1には、液位調整機構を備えた真空洗浄・乾燥方法及び装置が開示され、特許文献2には液位調整器を備えた真空蒸留再生装置が開示されている。 During vacuum steam cleaning, a specified amount of cleaning agent is stored in the steam generation/distillation regenerator, and the cleaning agent lost as steam is sequentially replenished to maintain a specified amount of steam generation. For this reason, the cleaning agent is replenished through a liquid level adjuster using a ball tap or the like to maintain a constant amount of cleaning agent stored in the steam generator/distillation regenerator. In addition, when discharging the residual cleaning agent from the steam generation/distillation regenerator after vacuum steam cleaning is completed, the The boil-down valve, which is a normally open valve, is closed, and the residual detergent is boiled down to reduce the volume and then discarded outside. For example, Patent Document 1 discloses a vacuum cleaning/drying method and apparatus provided with a liquid level adjusting mechanism, and Patent Document 2 discloses a vacuum distillation regeneration apparatus provided with a liquid level adjuster.

特開平7-227581号公報JP-A-7-227581 特開平6-269604号公報JP-A-6-269604

ここで、真空蒸気洗浄に用いる洗浄剤としては各種のものが知られている。洗浄剤には、有機溶剤、例えばアルコール類と水を主成分とする非引火性洗浄剤として取り扱われるものがある。このような洗浄剤は水の含有率が、他の洗浄剤に比べて相対的に多い。 Various cleaning agents are known for use in vacuum steam cleaning. Some detergents are treated as non-flammable detergents containing organic solvents such as alcohols and water as main components. Such detergents have a relatively high water content compared to other detergents.

一般的に使用されている蒸気発生・蒸留再生器を用いて、水の含有量が多い洗浄剤による真空蒸気洗浄を行う場合には次のような弊害が発生する場合がある。蒸気発生・蒸留再生器において、水の含有量が多い洗浄剤を加熱して蒸気として発生する場合には、水の沸点の方が有機溶剤よりも低いので、水が先に蒸発する。減圧下では水の沸点が下がるので、洗浄剤に含まれている水が蒸発して無くなるまでは、蒸気発生・蒸留再生器内の温度が十分に高くならない。また、低温の水蒸気が供給される真空蒸気洗浄槽の側でも真空蒸気洗浄に適した温度まで内部温度が上昇しない。 When performing vacuum steam cleaning with a cleaning agent containing a large amount of water using a generally used steam generation/distillation regenerator, the following adverse effects may occur. In the steam generation/distillation regenerator, when a cleaning agent containing a large amount of water is heated to generate steam, the water evaporates first because the boiling point of water is lower than that of the organic solvent. Since the boiling point of water is lowered under reduced pressure, the temperature in the steam generation/distillation regenerator does not rise sufficiently until the water contained in the cleaning agent evaporates. In addition, even on the side of the vacuum steam cleaning tank to which low-temperature steam is supplied, the internal temperature does not rise to a temperature suitable for vacuum steam cleaning.

さらに、蒸気発生・蒸留再生器内の洗浄剤から水が蒸発すると、その分、洗浄剤の液位が低下するので、液位調整器が作用して、逐次、水の蒸発によって失われた量に対応する量の新たな洗浄剤が補給される。すなわち、蒸気発生・蒸留再生器内の洗浄剤から所定量の水が蒸発すると、水の含有量の多い洗浄剤が補給されてしまう。このため、水の含有量の多い洗浄剤を使用する場合には、有機溶剤の蒸発開始までに時間を要し、真空蒸気洗浄を効率良く行えない場合がある。 In addition, when water evaporates from the cleaning agent in the steam generation/distillation regenerator, the liquid level of the cleaning agent drops accordingly. A corresponding amount of fresh cleaning agent is replenished. That is, when a predetermined amount of water evaporates from the cleaning agent in the steam generation/distillation regenerator, the cleaning agent with a high water content is replenished. Therefore, when a cleaning agent containing a large amount of water is used, it takes time to start evaporating the organic solvent, and vacuum steam cleaning may not be performed efficiently.

本発明の目的は、このような点に鑑みて、水の含有量が相対的に多い洗浄剤を使用する場合でも被洗浄物の真空蒸気洗浄を効率良く行い得る真空蒸気洗浄方法を提案することにある。 SUMMARY OF THE INVENTION It is an object of the present invention to provide a vacuum steam cleaning method capable of efficiently vacuum steam cleaning an object to be cleaned even when using a cleaning agent having a relatively high water content. It is in.

本発明は、洗浄剤を、液位調整器および煮詰めバルブを介して、蒸気発生・蒸留再生器に供給し、前記蒸気発生・蒸留再生器から発生する前記洗浄剤の蒸気を用いて被洗浄物の真空蒸気洗浄を行い、前記煮詰めバルブを閉じて前記洗浄剤の供給を遮断して、前記蒸気発生・蒸留再生器の残留洗浄剤を、煮詰めて外部に排出する構成を備えた洗浄機による真空蒸気洗浄方法に関する。 In the present invention, a cleaning agent is supplied to a steam generator/distillation regenerator via a liquid level regulator and a boil-down valve, and the vapor of the cleaning agent generated from the steam generation/distillation regenerator is used to clean an object to be cleaned. vacuum steam cleaning, close the boil-down valve to cut off the supply of the cleaning agent, boil down the residual cleaning agent in the steam generator/distillation regenerator and discharge it to the outside. It relates to a steam cleaning method.

本発明による真空蒸気洗浄方法では、前記蒸気発生・蒸留再生器に対する前記洗浄剤の供給・補給を、次のように行う。まず、前記蒸気発生・蒸留再生器に、前記被洗浄物の前記真空蒸気洗浄に必要な規定量の前記洗浄剤を供給する。前記第1規定量の前記洗浄剤が前記蒸気発生・蒸留再生器に貯留された後に、前記煮詰めバルブを閉じる。前記被洗浄物の前記真空蒸気洗浄が行われる間においては、前記煮詰めバルブを閉じ状態に保持して、前記液位調整器による前記蒸気発生・蒸留再生器に対する前記洗浄剤の補給動作を行わないことを特徴としている。 In the vacuum steam cleaning method according to the present invention, the cleaning agent is supplied and replenished to the steam generation/distillation regenerator as follows. First, a specified amount of the cleaning agent necessary for the vacuum steam cleaning of the object to be cleaned is supplied to the steam generation/distillation regenerator. After the first prescribed amount of the cleaning agent is stored in the steam generation/distillation regenerator, the boil down valve is closed. While the vacuum steam cleaning of the object to be cleaned is being performed, the boil-down valve is kept closed, and the cleaning agent is not replenished to the steam generation/distillation regenerator by the liquid level adjuster. It is characterized by

真空蒸気洗浄においては、事前に、蒸気発生・蒸留再生器に規定量の洗浄剤が供給される。煮詰めバルブを閉じた状態で蒸気が発生し、液位調整器が作用しないので、蒸気発生中において蒸気発生・蒸留再生器に新たな洗浄剤が補給されることはない。したがって、水の含有量の多い洗浄剤を用いる場合には、最初の所定時間で水が蒸発して無くなり、その後は有機溶剤の蒸気が発生して真空蒸気洗浄槽に供給され始める。従来のように、繰り返し新たな洗浄剤が補給され、有機溶剤の蒸気の発生が開始されるまでに時間を要するという弊害を回避あるいは抑制できる。 In vacuum steam cleaning, a defined amount of cleaning agent is supplied in advance to the steam generation/distillation regenerator. Since steam is generated with the boil down valve closed and the level regulator is inactive, the steam generation/distillation regenerator is not replenished with fresh cleaning agent during steam generation. Therefore, when a cleaning agent containing a large amount of water is used, the water evaporates in the first predetermined period of time, after which organic solvent vapor is generated and begins to be supplied to the vacuum vapor cleaning tank. It is possible to avoid or suppress the problem that it takes a long time until the organic solvent vapor starts to be generated after repeated replenishment of a new cleaning agent as in the conventional art.

ここで、使用する洗浄剤の種類に応じて、蒸気発生・蒸留再生器に対する洗浄剤の供給・補給の形態を変えることも可能である。洗浄剤が、水の含有量が所定割合よりも多い第1洗浄剤、例えば、アルコール類と水を主成分とするノンハロゲン非引火性洗浄剤の場合には、上記のように事前に規定量の洗浄剤を蒸気発生・蒸留再生器に供給する第1制御モードを採用して、真空蒸気洗浄を行う。 Here, it is also possible to change the mode of supply and replenishment of the cleaning agent to the steam generation/distillation regenerator according to the type of cleaning agent used. When the cleaning agent is a first cleaning agent containing more water than a predetermined ratio, for example, a non-halogen non-flammable cleaning agent containing alcohol and water as main components, a predetermined amount of cleaning agent is added in advance as described above. Vacuum steam cleaning is performed using a first control mode of supplying cleaning agent to the steam generation/distillation regenerator.

洗浄剤が、水の含有量が上記の所定割合以下の第2洗浄剤の場合には、従来における場合と同様な第2制御モードにより、真空蒸気洗浄を行うことができる。第2制御モードでは、前記蒸気発生・蒸留再生器に、第1規定量よりも少ない第2規定量の前記洗浄剤を供給し、前記第2規定量の前記洗浄剤が前記蒸気発生・蒸留再生器に貯留された後は、前記煮詰めバルブを開状態に保持し、前記被洗浄物の前記真空蒸気洗浄が行われる間において、前記液位調整器による前記蒸気発生・蒸留再生器に対する前記洗浄剤の補給動作を行う。 When the cleaning agent is the second cleaning agent having a water content equal to or less than the above predetermined ratio, the vacuum steam cleaning can be performed by the second control mode as in the conventional case. In the second control mode, a second specified amount of the cleaning agent smaller than the first specified amount is supplied to the steam generation/distillation regenerator, and the second specified amount of the cleaning agent is supplied to the steam generation/distillation regeneration unit. After being stored in the vessel, the boiling down valve is kept open, and the cleaning agent to the steam generation/distillation regenerator by the liquid level adjuster while the vacuum steam cleaning of the object to be cleaned is being performed. perform the replenishment operation.

本発明を適用可能な真空洗浄機は、例えば、多槽式の真空蒸気洗浄乾燥機であり、前記被洗浄物に前記洗浄剤による粗洗浄を施す粗洗浄槽と、前記粗洗浄後の前記被洗浄物に、前記洗浄剤による仕上げ洗浄を施す仕上げ洗浄槽と、前記仕上げ洗浄後の前記被洗浄物に、前記真空蒸気洗浄および真空乾燥を施す真空蒸気洗浄乾燥槽とを有している。 A vacuum washer to which the present invention can be applied is, for example, a multi-tank vacuum steam washing/drying machine, and includes a rough washing tank for roughly washing the object to be washed with the cleaning agent, and the object to be washed after the rough washing. It has a finish cleaning tank for finishing cleaning with the cleaning agent to the cleaning object, and a vacuum steam cleaning and drying tank for performing the vacuum steam cleaning and vacuum drying on the cleaning object after the finish cleaning.

本発明は、1槽式の真空洗浄乾燥機にも同様に適用可能である。この場合の真空洗浄乾燥機では、その真空洗浄乾燥槽に粗洗浄用の前記洗浄剤を供給して、前記被洗浄物に粗洗浄を施し、前記真空蒸気洗浄乾燥槽から前記洗浄剤を回収する工程と、前記真空蒸気洗浄乾燥槽に仕上げ洗浄用の前記洗浄剤を供給して、前記粗洗浄後の前記被洗浄物に仕上げ洗浄を施し、前記真空蒸気洗浄乾燥槽から前記洗浄剤を回収する工程と、前記真空蒸気洗浄乾燥槽に、前記蒸気発生・蒸留再生器から前記蒸気を供給して、前記仕上げ洗浄後の前記被洗浄物に前記真空蒸気洗浄を施す工程と、前記真空蒸気洗浄乾燥槽を真空引きして、前記真空蒸気洗浄後の前記被洗浄物を真空乾燥する工程が行われる。 The present invention is similarly applicable to a one-tank vacuum washer-dryer. In the vacuum washing/drying machine in this case, the cleaning agent for rough cleaning is supplied to the vacuum washing/drying tank, the object to be cleaned is roughly washed, and the cleaning agent is recovered from the vacuum steam washing/drying tank. and supplying the cleaning agent for final cleaning to the vacuum steam cleaning and drying tank, subjecting the object to be cleaned after the rough cleaning to finish cleaning, and recovering the cleaning agent from the vacuum steam cleaning and drying tank. a step of supplying the steam from the steam generator/distillation regenerator to the vacuum steam cleaning and drying tank to apply the vacuum steam cleaning to the object to be cleaned after the finish cleaning; and the vacuum steam cleaning and drying. A step of vacuum-drying the object to be cleaned after the vacuum steam cleaning by evacuating the bath is performed.

本発明を適用した1槽式の真空蒸気洗浄乾燥機のシステム系統図である。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a system diagram of a one-tank vacuum steam washing and drying machine to which the present invention is applied; 本発明を適用した多槽式の真空蒸気洗浄乾燥機のシステム系統図である。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a system diagram of a multi-tank vacuum steam washing and drying machine to which the present invention is applied;

以下に、図面を参照して、本発明を適用した真空蒸気洗浄乾燥機の実施の形態を説明する。 EMBODIMENT OF THE INVENTION Below, with reference to drawings, embodiment of the vacuum steam washing dryer to which this invention is applied is described.

[実施の形態1]
図1は、本発明の実施形態1に係る1槽式の真空洗浄乾燥機のシステム系統図である。1槽式の真空洗浄乾燥機1は、密閉可能な真空洗浄乾燥槽2を備え、真空洗浄乾燥槽2の底には超音波発生部3が配置されている。真空洗浄乾燥槽2には、被洗浄物が洗浄カゴ4に入れた状態で投入される。真空洗浄乾燥槽2に投入された被洗浄物には、設定されたシーケンスに従って、所要電力および駆動用圧縮空気が供給される電装・圧空ボックス40に内蔵された洗浄機制御部41の制御の下で、真空粗洗浄工程、真空仕上げ洗浄工程、真空蒸気洗浄工程および真空乾燥工程が施される。洗浄機制御部41は、以下に述べるように、各部を駆動制御して、各工程を実行する。なお、熱媒油タンク42から細い破線で示す経路を介して熱媒油が循環して、加熱対象の各部を加熱する。また、外部の冷却水供給源43から太い破線で示す経路を介して冷却水が循環して、冷却対象の各部を冷却する。
[Embodiment 1]
FIG. 1 is a system diagram of a one-tank vacuum washing/drying machine according to Embodiment 1 of the present invention. A one-tank vacuum cleaning/drying machine 1 includes a vacuum cleaning/drying tank 2 that can be sealed, and an ultrasonic generator 3 is arranged at the bottom of the vacuum cleaning/drying tank 2 . An object to be cleaned is put in a cleaning basket 4 into the vacuum cleaning drying tank 2 . The objects to be cleaned placed in the vacuum cleaning drying tank 2 are supplied with the required electric power and driving compressed air according to a set sequence, under the control of a cleaning machine control unit 41 built in an electric/pneumatic box 40. , a vacuum rough cleaning step, a vacuum finish cleaning step, a vacuum steam cleaning step and a vacuum drying step are performed. The washing machine control section 41 drives and controls each section to perform each step as described below. Note that the heat medium oil circulates from the heat medium oil tank 42 through the path indicated by the thin dashed line to heat each part to be heated. In addition, cooling water circulates from an external cooling water supply source 43 through a path indicated by a thick dashed line to cool each part to be cooled.

真空粗洗浄工程では、真空洗浄乾燥槽2には、真空バッファタンク5の粗液タンク6から粗洗浄用の洗浄剤が供給管7を介して供給される。被洗浄物には、浸漬状態で真空超音波洗浄による粗洗浄が施される。真空洗浄乾燥槽2は、真空引き機構16によって所定の真空状態に保持される。粗洗浄後は、洗浄剤がフィルタ8を経由する回収管9を介して、粗液タンク6に回収される。 In the rough vacuum cleaning process, a cleaning agent for rough cleaning is supplied from the rough liquid tank 6 of the vacuum buffer tank 5 to the vacuum cleaning drying tank 2 through the supply pipe 7 . The object to be cleaned is subjected to rough cleaning by vacuum ultrasonic cleaning while being immersed. The vacuum washing/drying tank 2 is maintained in a predetermined vacuum state by the vacuum drawing mechanism 16 . After the rough cleaning, the cleaning agent is recovered in the crude liquid tank 6 through the recovery pipe 9 passing through the filter 8 .

次の真空仕上げ洗浄工程では、真空洗浄乾燥槽2には、真空バッファタンク5の仕上液タンク10から仕上げ洗浄用の洗浄剤が、供給管11を介して供給される。被洗浄物には、浸漬状態で真空超音波洗浄による仕上げ洗浄が施される。この場合も、真空洗浄乾燥槽2は、真空引き機構16によって所定の真空状態に保持される。仕上げ洗浄後は、洗浄剤がフィルタ12を経由する回収管13を介して、仕上液タンク10に回収される。仕上液タンク10には、リザーブタンク14から供給管15を介して、洗浄剤が補給される。 In the next vacuum finishing cleaning step, the cleaning agent for finishing cleaning is supplied from the finishing liquid tank 10 of the vacuum buffer tank 5 to the vacuum cleaning drying tank 2 through the supply pipe 11 . The object to be cleaned is subjected to final cleaning by vacuum ultrasonic cleaning while being immersed. Also in this case, the vacuum washing/drying tank 2 is kept in a predetermined vacuum state by the vacuum drawing mechanism 16 . After finishing cleaning, the cleaning agent is recovered in the finishing liquid tank 10 through the recovery pipe 13 passing through the filter 12 . The finishing liquid tank 10 is replenished with a cleaning agent from a reserve tank 14 through a supply pipe 15 .

洗浄剤の供給・回収は、真空洗浄乾燥槽2と各タンク6、10との間の高低差と、真空引き機構16による真空引きにより行われる。真空引き機構16は、液封式真空ポンプ17aとメカニカルブースターポンプ17bからなる2段構成となっている。洗浄剤の供給・回収時には、真空洗浄乾燥槽2、真空バッファタンク5は、それぞれ、真空引き配管18を介して、液封式真空ポンプ17aによる真空引きが行われ、ベントバルブ19、20による復圧が交互に行われる。 The supply and recovery of the cleaning agent are performed by the height difference between the vacuum cleaning/drying tank 2 and the tanks 6 and 10 and the vacuuming by the vacuuming mechanism 16 . The vacuuming mechanism 16 has a two-stage structure consisting of a liquid ring vacuum pump 17a and a mechanical booster pump 17b. At the time of supplying and recovering the cleaning agent, the vacuum cleaning/drying tank 2 and the vacuum buffer tank 5 are evacuated by a liquid ring vacuum pump 17a via a vacuum evacuation pipe 18, respectively, and are restored by vent valves 19 and 20. The pressure is alternated.

仕上げ洗浄工程の後は、真空蒸気洗浄工程が行われる。真空洗浄乾燥槽2は、真空引き機構16の液封式真空ポンプ17aによる1段の真空引きが行われ、所定の真空状態とされる。真空状態を維持しながら、真空洗浄乾燥槽2には、蒸気供給管22を介して、蒸気発生・蒸留再生器23から洗浄剤の蒸気が供給される。真空洗浄乾燥槽2内の被洗浄物に真空蒸気洗浄が施される。 After the finish cleaning process, a vacuum steam cleaning process is performed. The vacuum cleaning and drying tank 2 is evacuated in a first stage by the liquid ring vacuum pump 17a of the vacuuming mechanism 16 to a predetermined vacuum state. Vapor of the cleaning agent is supplied from the steam generator/distillation regenerator 23 to the vacuum cleaning/drying tank 2 through the steam supply pipe 22 while maintaining the vacuum state. The object to be cleaned in the vacuum cleaning/drying tank 2 is subjected to vacuum steam cleaning.

蒸気発生・蒸留再生器23には、供給管24を介して、真空バッファタンク5の粗液タンク6から洗浄剤が供給される。洗浄剤は、供給管24に取り付けたフィルタ25、液位調整器26および煮詰めバルブ27を順次に経由して、蒸気発生・蒸留再生器23の下端側に設けた供給口に供給される。蒸気発生・蒸留再生器23内には上下方向にヒーター23bが配置されている。蒸気発生・蒸留再生器23内において、液位調整器26によって規定された液位となるまで、洗浄剤が貯留される。洗浄剤は、ヒーター23bによって加熱されて蒸気となって、蒸気供給管22を介して、真空洗浄乾燥槽2に供給される。真空蒸気洗浄における蒸気発生・蒸留再生器23に対する洗浄剤の供給制御については後述する。 A cleaning agent is supplied from the crude liquid tank 6 of the vacuum buffer tank 5 to the steam generation/distillation regenerator 23 through a supply pipe 24 . The cleaning agent is supplied to the supply port provided at the lower end side of the steam generation/distillation regenerator 23 through the filter 25 attached to the supply pipe 24, the liquid level adjuster 26 and the boil-down valve 27 in sequence. A heater 23b is arranged vertically in the steam generation/distillation regenerator 23. As shown in FIG. The cleaning agent is stored in the steam generation/distillation regenerator 23 until the liquid level specified by the liquid level adjuster 26 is reached. The cleaning agent is heated by the heater 23 b to become steam, and is supplied to the vacuum cleaning/drying tank 2 through the steam supply pipe 22 . The supply control of the cleaning agent to the steam generation/distillation regenerator 23 in the vacuum steam cleaning will be described later.

蒸気発生・蒸留再生器23の下端部には排液口が配置されている。ここを介して、蒸気発生・蒸留再生器23の残存洗浄剤を、スラッジタンク28に排出可能である。スラッジタンク28に回収された廃液は、廃液管29を介して、外部の廃液ドラム缶30に回収され、産業廃棄物として処分される。 A drain port is arranged at the lower end of the steam generation/distillation regenerator 23 . Via this, residual cleaning agent in the steam generation/distillation regenerator 23 can be discharged to the sludge tank 28 . The waste liquid collected in the sludge tank 28 is collected in an external waste liquid drum 30 through a waste liquid pipe 29 and disposed of as industrial waste.

なお、蒸気発生・蒸留再生器23において蒸留再生される洗浄剤の蒸気は、凝縮器31を経由する配管32を介して凝縮されて、リザーブタンク14に回収される。あるいは、配管32、33を介して、真空バッファタンク35に回収される。 The vapor of the cleaning agent distilled and regenerated in the vapor generator/distillation regenerator 23 is condensed through a pipe 32 passing through a condenser 31 and recovered in the reserve tank 14 . Alternatively, it is collected in a vacuum buffer tank 35 via pipes 32 and 33 .

真空蒸気洗浄後は、真空洗浄乾燥槽2の液出しが行われる。真空蒸気洗浄時においては、真空洗浄乾燥槽2内で被洗浄物の表面等に付着して凝結した洗浄剤が、真空洗浄乾燥槽2の底に貯まる。洗浄剤は、回収管34を介して、真空バッファタンク35に回収される。真空バッファタンク35に回収された洗浄剤は、回収管35a、35b、フィルタ12を経由する回収管13を介して、粗液タンク6に回収可能である。 After the vacuum steam cleaning, the vacuum cleaning drying tank 2 is drained. At the time of vacuum steam cleaning, the cleaning agent adhered and condensed on the surface of the object to be cleaned in the vacuum cleaning and drying tank 2 accumulates at the bottom of the vacuum cleaning and drying tank 2 . The cleaning agent is recovered in a vacuum buffer tank 35 via a recovery pipe 34 . The cleaning agent collected in the vacuum buffer tank 35 can be collected in the crude liquid tank 6 via the collection pipes 35 a and 35 b and the collection pipe 13 passing through the filter 12 .

この後は、真空乾燥工程が行われる。真空洗浄乾燥槽2は、真空引き管21を介して、真空引き機構16によって2段の真空引きが行われ、所定の真空状態とされて被洗浄物が真空乾燥される。真空引き機構16の液封式真空ポンプ17aで真空引きされた洗浄剤の蒸気は、気液分離槽36で冷却されて凝縮回収される。回収された洗浄剤は、回収管37、35bおよびフィルタ12を経由する回収管13を介して、真空バッファタンク5の粗液タンク6に戻される。 After this, a vacuum drying process is performed. The vacuum cleaning/drying tank 2 is vacuumed in two stages by the vacuuming mechanism 16 through the vacuuming tube 21 to achieve a predetermined vacuum state, and the object to be cleaned is vacuum-dried. The vapor of the cleaning agent evacuated by the liquid ring vacuum pump 17a of the vacuuming mechanism 16 is cooled in the gas-liquid separation tank 36 and condensed and collected. The collected cleaning agent is returned to the crude liquid tank 6 of the vacuum buffer tank 5 via the collection pipes 37 , 35 b and the collection pipe 13 passing through the filter 12 .

(蒸気発生・蒸留再生器への洗浄剤の供給制御)
ここで、真空洗浄乾燥機1における真空蒸気洗浄工程においては、次のように、蒸気発生・蒸留再生器23に対する洗浄剤の供給が制御される。まず、本例では、洗浄剤として、アルコール類と水を主成分とするノンハロゲン非引火性洗浄剤を使用している。このような他の洗浄剤に比べて相対的に水の含有割合が多い洗浄剤としては、例えば、「ノンハロゲン非引火性洗浄剤 HAシリーズ」(東ソー株式会社製)がある。
(Supply control of cleaning agent to steam generator/distillation regenerator)
Here, in the vacuum steam cleaning step in the vacuum cleaning/drying machine 1, the supply of the cleaning agent to the steam generator/distillation regenerator 23 is controlled as follows. First, in this example, a non-halogen and non-flammable cleaning agent containing alcohol and water as main components is used as the cleaning agent. Examples of cleaning agents that contain relatively more water than other cleaning agents include "Non-Halogen Nonflammable Cleaning Agents HA Series" (manufactured by Tosoh Corporation).

真空蒸気洗浄工程では、真空バッファタンク5の粗液タンク6から、液位調整器26および煮詰めバルブ27を経由する供給管24を介して、洗浄剤を蒸気発生・蒸留再生器23に供給する。洗浄剤は、予め設定された規定量が蒸気発生・蒸留再生器23に貯留されるように供給される。液位調整器26によって規定量が設定される。 In the vacuum steam cleaning step, the cleaning agent is supplied from the crude liquid tank 6 of the vacuum buffer tank 5 to the steam generation/distillation regenerator 23 through the supply pipe 24 via the liquid level adjuster 26 and the boil-down valve 27 . The cleaning agent is supplied so that a predetermined amount is stored in the steam generation/distillation regenerator 23 . A specified amount is set by the liquid level adjuster 26 .

規定量の洗浄剤が蒸気発生・蒸留再生器23に貯留された後は、煮詰めバルブ27を閉じ、この状態で真空蒸気洗浄を行う。真空蒸気洗浄が行われる間は、煮詰めバルブ27が閉じ状態に保持されるので、液位調整器26は作用せず、蒸気発生・蒸留再生器23に対する洗浄剤の補給動作は行われない。 After a specified amount of cleaning agent is stored in the steam generation/distillation regenerator 23, the boiling down valve 27 is closed and vacuum steam cleaning is performed in this state. Since the boil-down valve 27 is kept closed while the vacuum steam cleaning is performed, the liquid level adjuster 26 does not operate and the cleaning agent replenishment operation to the steam generation/distillation regenerator 23 is not performed.

蒸気発生・蒸留再生器23においては、ヒーター23bによって貯留されている洗浄剤を加熱して蒸発させる。最初は、洗浄剤に含まれている沸点の低い水が蒸発し、しかる後に、洗浄剤に含まれている有機溶剤の蒸発が開始され、真空洗浄乾燥槽2において被洗浄物の真空蒸気洗浄が始まる。従来における一般的な真空蒸気洗浄工程においては、煮詰めバルブ27は常開弁であり、蒸気発生・蒸留再生器23に貯留されている洗浄剤の液位が蒸発により低下すると、液位調整器26が作用して、減った量に対応する新たな洗浄剤の補給動作が行われる。 In the steam generator/distillation regenerator 23, the heater 23b heats and evaporates the stored cleaning agent. At first, water with a low boiling point contained in the cleaning agent evaporates, after which the organic solvent contained in the cleaning agent begins to evaporate, and the object to be cleaned in the vacuum cleaning drying tank 2 is vacuum steam cleaned. begin. In the conventional general vacuum steam cleaning process, the boiling down valve 27 is a normally open valve, and when the liquid level of the cleaning agent stored in the steam generator/distillation regenerator 23 drops due to evaporation, the liquid level adjuster 26 acts to replenish new detergent corresponding to the reduced amount.

水の含有割合が比較的多い洗浄剤の場合には、補給された洗浄剤に含まれる水が蒸発する動作が繰り返されてしまい、有機溶剤の蒸気が発生して真空蒸気洗浄が実際に開始されるまでに時間を要する。本例では、煮詰めバルブ27を閉じ状態に保持するので、洗浄剤の補給動作が行われず、したがって、有機溶剤の蒸気の発生を早めることができ、効率良く、真空蒸気洗浄を行うことができる。 In the case of a cleaning agent containing a relatively large amount of water, the operation of evaporating the water contained in the replenished cleaning agent is repeated, generating vapor of the organic solvent and actually starting vacuum vapor cleaning. It takes time to In this example, since the boil-down valve 27 is kept closed, the cleaning agent is not replenished. Therefore, the generation of the organic solvent vapor can be accelerated, and the vacuum vapor cleaning can be efficiently performed.

また、本例では、最初に蒸気発生・蒸留再生器23に供給される洗浄剤の規定量を、液位調整器26によって洗浄剤を補給する場合に比べて、多めの量に設定する。これにより、真空蒸気洗浄に必要とされる蒸気を発生できる。 Also, in this example, the specified amount of cleaning agent initially supplied to the steam generation/distillation regenerator 23 is set to a larger amount than when the cleaning agent is replenished by the liquid level adjuster 26 . This allows the steam required for vacuum steam cleaning to be generated.

なお、蒸気発生・蒸留再生器23からの残量洗浄剤の廃棄時には、従来と同様に、煮詰めバルブ27を閉じて、残留洗浄剤を煮詰めて減容化して、スラッジタンク28に廃棄する。 When the residual cleaning agent from the steam generator/distillation regenerator 23 is discarded, the boil-down valve 27 is closed to boil down the residual cleaning agent to reduce its volume and discard it in the sludge tank 28, as in the conventional case.

(蒸気発生・蒸留再生器への洗浄剤の供給制御の別の例)
ここで、真空洗浄乾燥機1の真空蒸気洗浄工程において、従来と同様に、煮詰めバルブ27を開き状態に保持して、液位調整器26を作用させて、洗浄剤を補給して、蒸気発生・蒸留再生器23の液位を一定に保持する制御を採用できる。
(Another example of control of cleaning agent supply to steam generator/distillation regenerator)
Here, in the vacuum steam cleaning step of the vacuum cleaning and drying machine 1, the boil-down valve 27 is kept open as in the conventional case, and the liquid level adjuster 26 is operated to replenish the cleaning agent and generate steam. - A control that keeps the liquid level of the distillation regenerator 23 constant can be adopted.

例えば、水の含有割合が比較的少ない洗浄剤を使用する場合には、従来と同様な制御モートで洗浄剤の供給・補給制御を行う。この場合には、洗浄機制御部41には、蒸気発生・蒸留再生器23に対する洗浄剤の供給・補給のために、第1制御モードおよび第2制御モードが設定され、いずれか一方の制御モードを選択可能にする。 For example, when using a cleaning agent with a relatively low water content, the same control mode as in the prior art is used to control the supply and replenishment of the cleaning agent. In this case, the washing machine control section 41 is set with a first control mode and a second control mode for supplying and replenishing the washing agent to the steam generator/distillation regenerator 23, and either one of the control modes is set. be selectable.

水の含有割合が多い洗浄剤を使用する場合には、第1制御モードを選択する。第1制御モードは、上述の制御により行われる。水の含有割合が少ない洗浄剤を使用する場合には、第2制御モードを選択する。この場合には、蒸気発生・蒸留再生器23に所定の規定量の洗浄剤を供給する。規定量の洗浄剤が蒸気発生・蒸留再生器23に貯留された後も、煮詰めバルブ27を開状態に保持する。被洗浄物の真空蒸気洗浄が行われる間においては、液位調整器26が作用して、蒸気発生・蒸留再生器23に対する洗浄剤の補給動作が行われる。 The first control mode is selected when using a cleaning agent with a high water content. The first control mode is performed by the control described above. The second control mode is selected when using a cleaning agent with a low water content. In this case, a predetermined specified amount of cleaning agent is supplied to the steam generation/distillation regenerator 23 . Even after a specified amount of cleaning agent is stored in the steam generation/distillation regenerator 23, the boil down valve 27 is kept open. During the vacuum steam cleaning of the object to be cleaned, the liquid level adjuster 26 operates to replenish the cleaning agent to the steam generator/distillation regenerator 23 .

[実施の形態2]
図2は、本発明の実施の形態2に係る多槽式の真空洗浄乾燥機の一例のシステム系統図である。本実施の形態2の真空洗浄乾燥機50は、3槽式の真空洗浄乾燥機であり、被洗浄物に粗洗浄を施す粗洗浄槽である超音波発生部51aを備えた第1洗浄槽51と、粗洗浄後の被洗浄物に仕上げ洗浄を施す仕上げ洗浄槽である第2洗浄槽52と、仕上げ洗浄後の被洗浄物に真空蒸気洗浄および真空乾燥を施す真空蒸気洗浄乾燥槽53とを備えている。第1、第2洗浄槽51、52は共通の真空バッファタンク54内に配置されている。
[Embodiment 2]
FIG. 2 is a system diagram of an example of a multi-tank vacuum washing/drying machine according to Embodiment 2 of the present invention. The vacuum washing/drying machine 50 of Embodiment 2 is a three-tank type vacuum washing/drying machine, and includes a first washing tank 51 provided with an ultrasonic wave generator 51a, which is a rough washing tank for roughly washing an object to be cleaned. a second cleaning tank 52, which is a finishing washing tank, in which the objects to be cleaned after rough washing are subjected to finish washing; I have. The first and second cleaning tanks 51 and 52 are arranged in a common vacuum buffer tank 54 .

第1、第2洗浄槽51、52、および真空蒸気洗浄乾燥槽53には、被洗浄物が洗浄カゴ55に入れた状態で投入される。設定されたシーケンスに従って、洗浄カゴ55に入れた被洗浄物は、不図示の搬送機構によって、第1洗浄槽51に搬入されて超音波粗洗浄工程が施され、次に、第2洗浄槽52に搬入されて、仕上げ洗浄工程が施され、次に、真空蒸気洗浄乾燥槽53に投入されて、真空蒸気洗浄工程および真空乾燥工程が施される。所要電力および駆動用圧縮空気が供給される電装・圧空ボックス56に内蔵の洗浄機制御部57によって、各部が駆動制御されて、各工程が実行される。 The objects to be cleaned are placed in a cleaning basket 55 and put into the first and second cleaning tanks 51 and 52 and the vacuum steam cleaning/drying tank 53 . According to a set sequence, the objects to be cleaned placed in the cleaning basket 55 are carried into the first cleaning tank 51 by a transport mechanism (not shown), subjected to rough ultrasonic cleaning, and then subjected to the second cleaning tank 52. , subjected to a final cleaning process, and then put into a vacuum steam cleaning and drying tank 53 to undergo a vacuum steam cleaning process and a vacuum drying process. Each part is driven and controlled by a washing machine control part 57 built in an electric equipment/compressed air box 56 to which required electric power and driving compressed air are supplied, and each step is executed.

超音波粗洗浄工程では、第1洗浄槽51に貯留した粗洗浄用の洗浄剤に、被洗浄物が浸漬され、超音波洗浄による粗洗浄が施される。第1洗浄槽51から隣接のオーバーフロータンク60に流れ落ちた洗浄剤は、タンク61、循環ポンプ62、フィルタ63を経由する循環配管64を介して清浄化されて第1洗浄槽51に戻される。次の仕上げ洗浄工程では、第2洗浄槽52に貯留した仕上げ洗浄の洗浄剤に、被洗浄物が浸漬されて仕上げ洗浄が行われる。洗浄剤は、循環ポンプ65、フィルタ66を経由する循環配管67を介して清浄化されて第2洗浄槽52に戻される。また、リザーブタンク68から、給液ポンプ69を経由する給液管70を介して、洗浄剤が第2洗浄槽52に供給・補給される。第2洗浄槽52に供給された洗浄剤はオーバーフローして隣接の第1洗浄槽51に供給される。 In the ultrasonic rough cleaning process, the object to be cleaned is immersed in the cleaning agent for rough cleaning stored in the first cleaning tank 51 and subjected to rough cleaning by ultrasonic cleaning. The cleaning agent that has flowed down from the first cleaning tank 51 to the adjacent overflow tank 60 is cleaned through a circulation pipe 64 passing through the tank 61 , the circulation pump 62 and the filter 63 and returned to the first cleaning tank 51 . In the next finish cleaning step, the object to be cleaned is immersed in the cleaning agent for finish cleaning stored in the second cleaning tank 52 to perform finish cleaning. The cleaning agent is cleaned through a circulation pipe 67 passing through a circulation pump 65 and a filter 66 and returned to the second cleaning tank 52 . Further, the cleaning agent is supplied and replenished from the reserve tank 68 to the second cleaning tank 52 through the liquid supply pipe 70 that passes through the liquid supply pump 69 . The cleaning agent supplied to the second cleaning tank 52 overflows and is supplied to the adjacent first cleaning tank 51 .

仕上げ洗浄工程の後の真空蒸気洗浄工程は、真空蒸気洗浄乾燥槽53に被洗浄物が投入されて行われる。真空蒸気洗浄乾燥槽53は、真空引き配管71を介して、真空引き機構72による真空引きが行われ、所定の真空状態とされる。真空引き機構72は、液封式真空ポンプ73とメカニカルブースターポンプ74を備えている。真空蒸気洗浄工程では、液封式真空ポンプ73による一段の真空引きが行われ、所定の真空状態が維持される。この状態で、真空蒸気洗浄乾燥槽53には、蒸気供給管75を介して、蒸気発生・蒸留再生器76から洗浄剤の蒸気が供給される。真空蒸気洗浄乾燥槽53内の被洗浄物に真空蒸気洗浄が施される。 The vacuum steam cleaning process after the finish cleaning process is performed by putting the object to be cleaned into the vacuum steam cleaning/drying tank 53 . The vacuum steam cleaning/drying tank 53 is evacuated by a vacuuming mechanism 72 via a vacuuming pipe 71 to a predetermined vacuum state. The vacuuming mechanism 72 includes a liquid ring vacuum pump 73 and a mechanical booster pump 74 . In the vacuum steam cleaning step, the liquid ring vacuum pump 73 performs one-step vacuuming to maintain a predetermined vacuum state. In this state, the vapor of the cleaning agent is supplied from the vapor generator/distillation regenerator 76 to the vacuum vapor washing/drying tank 53 through the vapor supply pipe 75 . The object to be cleaned in the vacuum steam cleaning/drying tank 53 is subjected to vacuum steam cleaning.

蒸気発生・蒸留再生器76には、第1洗浄槽51の循環配管64から分岐する供給管77を介して、洗浄剤が供給される。洗浄剤は、供給管77に取り付けた液位調整器78および煮詰めバルブ79を順次に経由して、蒸気発生・蒸留再生器76の下端部に設けた供給口に供給される。蒸気発生・蒸留再生器76内には上下方向にヒーター76bが配置されている。蒸気発生・蒸留再生器76内において、液位調整器78によって規定された液位となるまで、洗浄剤が貯留される。洗浄剤は、ヒーター76bによって加熱されて蒸気となって、蒸気供給管75を介して、真空蒸気洗浄乾燥槽53に供給される。真空蒸気洗浄における蒸気発生・蒸留再生器76に対する洗浄剤の供給制御については後述する。 A cleaning agent is supplied to the steam generator/distillation regenerator 76 through a supply pipe 77 branching from the circulation pipe 64 of the first cleaning tank 51 . The cleaning agent is supplied to the supply port provided at the lower end of the steam generation/distillation regenerator 76 through a liquid level adjuster 78 attached to a supply pipe 77 and a boil-down valve 79 in sequence. A heater 76b is arranged vertically in the steam generation/distillation regenerator 76. As shown in FIG. Cleaning agent is stored in the steam generation/distillation regenerator 76 until the level defined by the level regulator 78 is achieved. The cleaning agent is heated by the heater 76 b to become steam, and is supplied to the vacuum steam cleaning/drying tank 53 through the steam supply pipe 75 . The supply control of the cleaning agent to the steam generation/distillation regenerator 76 in the vacuum steam cleaning will be described later.

蒸気発生・蒸留再生器76の下端部には排液口が配置され、ここを介して、蒸気発生・蒸留再生器76の残存洗浄剤を、スラッジタンク80に排出可能である。スラッジタンク80に回収された廃液は、廃液缶81に回収され、産業廃棄物として処分される。なお、蒸気発生・蒸留再生器23において蒸留再生された洗浄剤の蒸気は、凝縮器82を経由する配管83を介して凝縮されて、真空バッファタンク84に回収される。 A drain port is arranged at the lower end of the steam generation/distillation regenerator 76 , through which residual cleaning agent in the steam generation/distillation regenerator 76 can be discharged to the sludge tank 80 . The waste liquid collected in the sludge tank 80 is collected in a waste liquid can 81 and disposed of as industrial waste. The vapor of the cleaning agent distilled and regenerated in the vapor generation/distillation regenerator 23 is condensed through a pipe 83 passing through a condenser 82 and recovered in a vacuum buffer tank 84 .

真空蒸気洗浄後は、真空蒸気洗浄乾燥槽53の液出しが行われる。真空蒸気洗浄時においては、真空蒸気洗浄乾燥槽53内で被洗浄物の表面等に付着して凝結した洗浄剤が、真空蒸気洗浄乾燥槽53の底に貯まる。洗浄剤は、回収管85を介して、真空バッファタンク84に回収される。 After the vacuum steam cleaning, the vacuum steam cleaning drying tank 53 is drained. At the time of vacuum steam cleaning, the cleaning agent adhered and condensed on the surface of the object to be cleaned in the vacuum steam cleaning and drying tank 53 accumulates at the bottom of the vacuum steam cleaning and drying tank 53 . The cleaning agent is recovered in vacuum buffer tank 84 through recovery pipe 85 .

この後は、真空乾燥工程が行われる。真空蒸気洗浄乾燥槽53は、真空引き管86を介して、真空引き機構72によって2段の真空引きが行われ、所定の真空状態とされて被洗浄物が真空乾燥される。真空引き機構72の液封式真空ポンプ73で真空引きされた洗浄剤の蒸気は、気液分離槽87で冷却されて凝縮回収される。回収された洗浄剤は、回収管88および給液ポンプ69を経由する給液管70を介して、第2洗浄槽52に戻される。 After this, a vacuum drying process is performed. The vacuum steam cleaning/drying tank 53 is subjected to two stages of vacuuming by the vacuuming mechanism 72 through the vacuuming tube 86, and the object to be cleaned is vacuum-dried in a predetermined vacuum state. The vapor of the cleaning agent evacuated by the liquid ring vacuum pump 73 of the vacuuming mechanism 72 is cooled in the gas-liquid separation tank 87 and condensed and collected. The collected cleaning agent is returned to the second cleaning tank 52 via the recovery pipe 88 and the liquid supply pipe 70 that passes through the liquid supply pump 69 .

(蒸気発生・蒸留再生器への洗浄剤の供給制御)
本例の真空洗浄乾燥機50における真空蒸気洗浄工程において、次のように、蒸気発生・蒸留再生器76に対する洗浄剤の供給が制御される。洗浄剤として、アルコール類と水を主成分とするノンハロゲン非引火性洗浄剤を使用している。このような他の洗浄剤に比べて相対的に水の含有割合が多い洗浄剤としては、例えば、「ノンハロゲン非引火性洗浄剤 HAシリーズ」(東ソー株式会社製)がある。
(Supply control of cleaning agent to steam generator/distillation regenerator)
In the vacuum steam cleaning process in the vacuum cleaning/drying machine 50 of this embodiment, the supply of the cleaning agent to the steam generation/distillation regenerator 76 is controlled as follows. A non-halogen, non-flammable cleaning agent containing alcohol and water as the main components is used as the cleaning agent. Examples of cleaning agents that contain relatively more water than other cleaning agents include "Non-Halogen Nonflammable Cleaning Agents HA Series" (manufactured by Tosoh Corporation).

真空蒸気洗浄工程では、液位調整器78および煮詰めバルブ79を経由する供給管77を介して、洗浄剤が蒸気発生・蒸留再生器76に供給される。洗浄剤は、予め設定された規定量が蒸気発生・蒸留再生器76に貯留されるように供給される。液位調整器78によって規定量が設定される。規定量の洗浄剤が蒸気発生・蒸留再生器76に貯留された後は、煮詰めバルブ79を閉じ、この状態で真空蒸気洗浄を行う。真空蒸気洗浄が行われる間は、煮詰めバルブ79が閉じ状態に保持されるので、液位調整器78は作用せず、蒸気発生・蒸留再生器76に対する洗浄剤の補給動作は行われない。かかる制御により、実施の形態1の場合と同様に、効率良く、真空蒸気洗浄工程を実行できる。 In the vacuum steam cleaning process, the cleaning agent is supplied to the steam generation/distillation regenerator 76 via a supply line 77 via a liquid level regulator 78 and a boil down valve 79 . The cleaning agent is supplied so that a predetermined amount is stored in the steam generation/distillation regenerator 76 . A specified amount is set by the liquid level adjuster 78 . After a specified amount of cleaning agent is stored in the steam generation/distillation regenerator 76, the boiling down valve 79 is closed and vacuum steam cleaning is performed in this state. Since the boil-down valve 79 is kept closed while the vacuum steam cleaning is being performed, the liquid level adjuster 78 is inactive and the cleaning agent replenishment operation to the steam generation/distillation regenerator 76 is not performed. With such control, the vacuum steam cleaning process can be efficiently executed as in the case of the first embodiment.

また、本例においても、洗浄機制御部57に、蒸気発生・蒸留再生器76に対する洗浄剤の供給・補給を、第1制御モードおよび第2制御モードを設定し、いずれか一方の制御モードを選択可能にしておくことができる。第1制御モードは、上述した場合である。第2制御モードは、従来の場合のように、蒸気発生・蒸留再生器76に所定の規定量の洗浄剤を供給する。規定量の洗浄剤が蒸気発生・蒸留再生器76に貯留された後も、煮詰めバルブ79を開状態に保持する。被洗浄物の真空蒸気洗浄が行われる間においては、液位調整器78が作用して、蒸気発生・蒸留再生器76に対する洗浄剤の補給動作が行われる。 Also in this example, the first control mode and the second control mode are set in the washing machine control unit 57 for the supply and replenishment of the washing agent to the steam generation/distillation regenerator 76, and either one of the control modes is set. It can be left selectable. The first control mode is the case described above. The second control mode supplies a predetermined, prescribed amount of cleaning agent to the steam generation/distillation regenerator 76, as in the conventional case. Even after a specified amount of cleaning agent is stored in the steam generation/distillation regenerator 76, the boil down valve 79 is kept open. While the object to be cleaned is being vacuum steam cleaned, the liquid level adjuster 78 operates to replenish the cleaning agent to the steam generator/distillation regenerator 76 .

[その他の実施の形態]
なお、上記は、1槽式、3槽式の例であるが、本発明は、2槽式、あるいは4槽以上の多槽式の真空蒸気洗浄乾燥機に対しても、同様に適用可能である。
[Other embodiments]
Although the above is an example of a one-tank type and a three-tank type, the present invention can be similarly applied to a two-tank type or a multi-tank type vacuum steam washing/drying machine having four or more tanks. be.

1 真空洗浄乾燥機
2 真空洗浄乾燥槽
3 超音波発生部
4 洗浄カゴ
5 真空バッファタンク
6 粗液タンク
7 供給管
8 フィルタ
9 回収管
10 仕上液タンク
11 供給管
12 フィルタ
13 回収管
14 リザーブタンク
15 供給管
16 真空引き機構
17a 液封式真空ポンプ
17b メカニカルブースターポンプ
18 配管
19、20 ベントバルブ
21 真空引き管
22 蒸気供給管
23 蒸気発生・蒸留再生器
23b ヒーター
24 供給管
25 フィルタ
26 液位調整器
27 煮詰めバルブ
28 スラッジタンク
29 廃液管
30 廃液ドラム缶
31 凝縮器
32 配管
33 配管
34 回収管
35 真空バッファタンク
35a、35b 回収管
36 気液分離槽
37 回収管
40 電装・圧空ボックス
41 洗浄機制御部
42 熱媒油タンク
43 冷却水供給源
50 真空洗浄乾燥機
51 第1洗浄槽
51a 超音波発生部
52 第2洗浄槽
53 真空蒸気洗浄乾燥槽
54 真空バッファタンク
55 洗浄カゴ
56 電装・圧空ボックス
57 洗浄機制御部
60 オーバーフロータンク
61 タンク
62 循環ポンプ
63 フィルタ
64 循環配管
65 循環ポンプ
66 フィルタ
67 循環配管
68 リザーブタンク
69 給液ポンプ
70 給液管
71 配管
72 真空引き機構
73 液封式真空ポンプ
74 メカニカルブースターポンプ
75 蒸気供給管
76 蒸気発生・蒸留再生器
76b ヒーター
77 供給管
78 液位調整器
79 バルブ
80 スラッジタンク
81 廃液缶
82 凝縮器
83 配管
84 真空バッファタンク
85 回収管
86 真空引き管
87 気液分離槽
88 回収管
1 vacuum cleaning dryer 2 vacuum cleaning drying tank 3 ultrasonic generator 4 cleaning basket 5 vacuum buffer tank 6 crude liquid tank 7 supply pipe 8 filter 9 recovery pipe 10 finishing liquid tank 11 supply pipe 12 filter 13 recovery pipe 14 reserve tank 15 Supply pipe 16 Evacuation mechanism 17a Liquid ring vacuum pump 17b Mechanical booster pump 18 Pipes 19, 20 Vent valve 21 Evacuation pipe 22 Steam supply pipe 23 Steam generator/distillation regenerator 23b Heater 24 Supply pipe 25 Filter 26 Liquid level adjuster 27 Boil down valve 28 Sludge tank 29 Waste liquid pipe 30 Waste liquid drum 31 Condenser 32 Pipe 33 Pipe 34 Recovery pipe 35 Vacuum buffer tank 35 a, 35 b Recovery pipe 36 Gas-liquid separation tank 37 Recovery pipe 40 Electric equipment/compressed air box 41 Cleaning machine control unit 42 Heat medium oil tank 43 Cooling water supply source 50 Vacuum cleaning dryer 51 First cleaning tank 51a Ultrasonic generator 52 Second cleaning tank 53 Vacuum steam cleaning/drying tank 54 Vacuum buffer tank 55 Cleaning basket 56 Electrical/pneumatic box 57 Cleaning machine Control unit 60 overflow tank 61 tank 62 circulation pump 63 filter 64 circulation pipe 65 circulation pump 66 filter 67 circulation pipe 68 reserve tank 69 liquid supply pump 70 liquid supply pipe 71 pipe 72 evacuation mechanism 73 liquid ring vacuum pump 74 mechanical booster pump 75 steam supply pipe 76 steam generation/distillation regenerator 76b heater 77 supply pipe 78 liquid level adjuster 79 valve 80 sludge tank 81 waste liquid can 82 condenser 83 pipe 84 vacuum buffer tank 85 recovery pipe 86 evacuation pipe 87 gas-liquid separation tank 88 recovery tube

Claims (6)

洗浄剤を、液位調整器および煮詰めバルブを介して、蒸気発生・蒸留再生器に供給し、前記蒸気発生・蒸留再生器から発生する前記洗浄剤の蒸気を用いて被洗浄物の真空蒸気洗浄を行い、前記煮詰めバルブを閉じて前記洗浄剤の供給を遮断して、前記蒸気発生・蒸留再生器の残留洗浄剤を、煮詰めて外部に排出する洗浄機の真空蒸気洗浄方法であって、
前記蒸気発生・蒸留再生器に、前記被洗浄物の前記真空蒸気洗浄に必要な規定量の前記洗浄剤を供給し、
前記規定量の前記洗浄剤が前記蒸気発生・蒸留再生器に貯留された後に、前記煮詰めバルブを閉じ、
前記真空蒸気洗浄が行われる間において、前記煮詰めバルブを閉じ状態に保持して、前記液位調整器による前記蒸気発生・蒸留再生器に対する前記洗浄剤の補給動作を行わないことを特徴とする真空蒸気洗浄方法。
A cleaning agent is supplied to a steam generator/distillation regenerator through a liquid level regulator and a boil-down valve, and vacuum steam cleaning of an object to be cleaned is performed using the steam of the cleaning agent generated from the steam generation/distillation regenerator. and closing the boil-down valve to cut off the supply of the cleaning agent to boil down the residual cleaning agent in the steam generator/distillation regenerator and discharge it to the outside, comprising:
supplying a specified amount of the cleaning agent required for the vacuum steam cleaning of the object to be cleaned to the steam generation/distillation regenerator;
After the specified amount of the cleaning agent is stored in the steam generation/distillation regenerator, closing the boil-down valve,
The vacuum is characterized in that, while the vacuum steam cleaning is performed, the boil-down valve is kept closed, and the cleaning agent is not replenished to the steam generation/distillation regenerator by the liquid level adjuster. Steam cleaning method.
請求項1に記載の真空蒸気洗浄方法おいて、
前記洗浄剤として、アルコール類と水を主成分とするノンハロゲン非引火性洗浄剤を用いる真空蒸気洗浄方法。
The vacuum steam cleaning method of claim 1, wherein
A vacuum steam cleaning method using, as the cleaning agent, a non-halogen and non-flammable cleaning agent containing alcohol and water as main components.
洗浄剤を、液位調整器および煮詰めバルブを介して、蒸気発生・蒸留再生器に供給し、前記蒸気発生・蒸留再生器から発生する前記洗浄剤の蒸気を用いて被洗浄物の真空蒸気洗浄を行い、前記煮詰めバルブを閉じて前記洗浄剤の供給を遮断して、前記蒸気発生・蒸留再生器の残留洗浄剤を、煮詰めて外部に排出する洗浄機の真空蒸気洗浄方法であって、
前記蒸気発生・蒸留再生器に対する前記洗浄剤の供給・補給を、第1制御モードおよび第2制御モードのうちの一方の制御モードで行い、
前記第1制御モードは、
前記蒸気発生・蒸留再生器に、前記被洗浄物の前記真空蒸気洗浄に必要な第1規定量の前記洗浄剤を供給し、
前記第1規定量の前記洗浄剤が前記蒸気発生・蒸留再生器に貯留された後に、前記煮詰めバルブを閉じ、
前記被洗浄物の前記真空蒸気洗浄が行われる間において、前記煮詰めバルブを閉じ状態に保持して、前記液位調整器による前記蒸気発生・蒸留再生器に対する前記洗浄剤の補給動作を行わない制御であり、
前記第2制御モードは、
前記蒸気発生・蒸留再生器に、前記第1規定量よりも少ない第2規定量の前記洗浄剤を供給し、
前記第2規定量の前記洗浄剤が前記蒸気発生・蒸留再生器に貯留された後も、前記煮詰めバルブを開状態に保持し、前記被洗浄物の前記真空蒸気洗浄が行われる間において、前記液位調整器による前記蒸気発生・蒸留再生器に対する前記洗浄剤の補給動作を行う制御であることを特徴とする真空蒸気洗浄方法。
A cleaning agent is supplied to a steam generator/distillation regenerator through a liquid level regulator and a boil-down valve, and vacuum steam cleaning of an object to be cleaned is performed using the steam of the cleaning agent generated from the steam generation/distillation regenerator. and closing the boil-down valve to cut off the supply of the cleaning agent to boil down the residual cleaning agent in the steam generator/distillation regenerator and discharge it to the outside, comprising:
supplying and replenishing the cleaning agent to the steam generation/distillation regenerator in one of a first control mode and a second control mode;
The first control mode is
supplying a first specified amount of the cleaning agent required for the vacuum steam cleaning of the object to be cleaned to the steam generation/distillation regenerator;
After the first specified amount of the cleaning agent is stored in the steam generation/distillation regenerator, closing the boil-down valve;
While the vacuum steam cleaning of the object to be cleaned is being performed, control is performed such that the boiling down valve is kept closed and the cleaning agent is not replenished to the steam generation/distillation regenerator by the liquid level adjuster. and
The second control mode is
supplying a second specified amount of the cleaning agent, which is smaller than the first specified amount, to the steam generation/distillation regenerator;
Even after the second specified amount of the cleaning agent is stored in the steam generation/distillation regenerator, the boil-down valve is kept open, and during the vacuum steam cleaning of the object to be cleaned, the A vacuum steam cleaning method, characterized in that the cleaning agent is replenished to the steam generation/distillation regenerator by a liquid level regulator.
請求項3に記載の真空蒸気洗浄方法おいて、
前記洗浄剤が、水の含有量が所定割合よりも多い第1洗浄剤である場合には、前記第1制御モードを採用し、
前記洗浄剤が、水の含有量が前記所定割合以下の第2洗浄剤である場合には、前記第2制御モードを採用する真空蒸気洗浄方法。
A vacuum steam cleaning method according to claim 3, wherein
adopting the first control mode when the cleaning agent is a first cleaning agent containing more water than a predetermined ratio;
A vacuum steam cleaning method employing the second control mode when the cleaning agent is a second cleaning agent having a water content equal to or less than the predetermined ratio.
請求項1ないし4のうちのいずれか一つの項に記載の真空蒸気洗浄方法において、
前記洗浄機は多槽式の真空蒸気洗浄乾燥機であり、
前記被洗浄物に前記洗浄剤による粗洗浄を施す粗洗浄槽と、
前記粗洗浄後の前記被洗浄物に、前記洗浄剤による仕上げ洗浄を施す仕上げ洗浄槽と、
前記仕上げ洗浄後の前記被洗浄物に、前記真空蒸気洗浄および真空乾燥を施す真空蒸気洗浄乾燥槽と、
を有している真空蒸気洗浄方法。
A vacuum steam cleaning method according to any one of claims 1 to 4,
The washing machine is a multi-tank vacuum steam washing and drying machine,
a rough cleaning tank for roughly cleaning the object to be cleaned with the cleaning agent;
a finish cleaning tank for performing finish cleaning with the cleaning agent on the object to be cleaned after the rough cleaning;
a vacuum steam cleaning and drying tank for performing the vacuum steam cleaning and vacuum drying on the object to be cleaned after the finish cleaning;
A vacuum steam cleaning method comprising:
請求項1ないし4のうちのいずれか一つの項に記載の真空蒸気洗浄方法において、
前記洗浄機は1槽式の真空蒸気洗浄乾燥機であり、
前記真空蒸気洗浄乾燥機の真空蒸気洗浄乾燥槽に粗洗浄用の前記洗浄剤を供給して、前記被洗浄物に粗洗浄を施し、前記真空蒸気洗浄乾燥槽から前記洗浄剤を回収する工程と、
前記真空蒸気洗浄乾燥槽に仕上げ洗浄用の前記洗浄剤を供給して、前記粗洗浄後の前記被洗浄物に仕上げ洗浄を施し、前記真空蒸気洗浄乾燥槽から前記洗浄剤を回収する工程と、
前記真空蒸気洗浄乾燥槽に、前記蒸気発生・蒸留再生器から前記蒸気を供給して、前記仕上げ洗浄後の前記被洗浄物に前記真空蒸気洗浄を施す工程と、
前記真空蒸気洗浄乾燥槽を真空引きして、前記真空蒸気洗浄後の前記被洗浄物を真空乾燥する工程と、
を含む真空蒸気洗浄方法。
A vacuum steam cleaning method according to any one of claims 1 to 4,
The washing machine is a one-tank vacuum steam washing and drying machine,
a step of supplying the cleaning agent for rough cleaning to a vacuum steam cleaning and drying tank of the vacuum steam cleaning and drying machine, subjecting the object to be cleaned to rough cleaning, and recovering the cleaning agent from the vacuum steam cleaning and drying tank; ,
a step of supplying the cleaning agent for finish cleaning to the vacuum steam cleaning/drying tank, subjecting the object to be cleaned after the rough cleaning to finish cleaning, and recovering the cleaning agent from the vacuum steam cleaning/drying tank;
a step of supplying the steam from the steam generator/distillation regenerator to the vacuum steam cleaning/drying tank to subject the object to be cleaned after the finish cleaning to the vacuum steam cleaning;
a step of vacuum-drying the object to be cleaned after the vacuum steam cleaning by evacuating the vacuum steam cleaning and drying tank;
Vacuum steam cleaning method including.
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JP2000237706A (en) 1999-02-24 2000-09-05 Akuatekku:Kk Vacuum cleaning and drying method using single treating tank and device therefor
JP2006088109A (en) 2004-09-27 2006-04-06 Aqua Kagaku Kk Cleaning method and cleaning apparatus
JP2009028726A (en) 1993-08-30 2009-02-12 Tosei Electric Corp Vacuum distillation apparatus
JP2016049477A (en) 2014-08-29 2016-04-11 旭硝子株式会社 Washing and rinsing method

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JP2000237706A (en) 1999-02-24 2000-09-05 Akuatekku:Kk Vacuum cleaning and drying method using single treating tank and device therefor
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