JPH0655150A - Washing unit and washing apparatus using the same - Google Patents
Washing unit and washing apparatus using the sameInfo
- Publication number
- JPH0655150A JPH0655150A JP23316092A JP23316092A JPH0655150A JP H0655150 A JPH0655150 A JP H0655150A JP 23316092 A JP23316092 A JP 23316092A JP 23316092 A JP23316092 A JP 23316092A JP H0655150 A JPH0655150 A JP H0655150A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- hydrocarbon
- distiller
- boiling point
- 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.)
- Pending
Links
Landscapes
- Cleaning By Liquid Or Steam (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
(57)【要約】
【目的】 炭化水素系洗浄剤を全体的に入れ替えたりす
ることなく、炭化水素系洗浄剤を所定の洗浄効果を有す
る状態に保持し、連続して安定した洗浄を行うことが可
能であるとともに、種々の洗浄条件に対応した洗浄シス
テムを構築することが可能な洗浄ユニット及び該洗浄ユ
ニットを用いてなる洗浄装置を得る。
【構成】 本願発明の洗浄ユニットは、洗浄対象物を炭
化水素系洗浄剤により洗浄する洗浄槽1と、低沸点汚れ
成分及び高沸点汚れ成分を含む炭化水素系洗浄剤を蒸留
して、低沸点汚れ成分を蒸留分離する第1の蒸留器2
と、第1の蒸留器2において低沸点汚れ成分を蒸留分離
した炭化水素系洗浄剤を蒸留し、炭化水素系洗浄剤を蒸
留分離する第2の蒸留器3とを具備し、かつ、第2の蒸
留器3において分離した炭化水素系洗浄剤を洗浄槽1に
循環供給する。
(57) [Summary] [Purpose] To maintain a hydrocarbon-based cleaning agent in a state of having a predetermined cleaning effect and to perform continuous and stable cleaning without replacing the entire hydrocarbon-based cleaning agent. In addition to the above, a cleaning unit capable of constructing a cleaning system corresponding to various cleaning conditions and a cleaning apparatus using the cleaning unit are obtained. The cleaning unit of the present invention comprises a cleaning tank 1 for cleaning an object to be cleaned with a hydrocarbon-based cleaning agent, and a hydrocarbon-based cleaning agent containing a low-boiling point stain component and a high-boiling point stain component to distill a low-boiling point First distiller 2 for separating dirt components by distillation
And a second distiller 3 for distilling and separating the hydrocarbon-based detergent by distilling and separating the low-boiling-point contaminants in the first distiller 2, and the second distiller 3. The hydrocarbon-based cleaning agent separated in the distiller 3 is circulated and supplied to the cleaning tank 1.
Description
【0001】[0001]
【産業上の利用分野】本願発明は、電子部品、機械部品
など、種々の部品や製品の洗浄に用いられる洗浄装置に
関し、詳しくは、炭化水素系洗浄剤を用いて洗浄を行う
際に用いられる洗浄ユニット及び該洗浄ユニットを用い
てなる洗浄装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning device used for cleaning various parts and products such as electronic parts and mechanical parts, and more specifically, it is used when cleaning is performed using a hydrocarbon-based cleaning agent. The present invention relates to a cleaning unit and a cleaning device using the cleaning unit.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】従来、
電子部品や機械部品などを洗浄するための工業用洗浄剤
としては、フロン系洗浄剤や、トリクロロエタンなどの
塩素系溶剤が用いられてきた。しかし、これらの工業用
洗浄剤には、オゾン層の破壊や地下水の汚染、あるいは
作業環境の悪化などを引き起こすという問題点があり、
その使用が規制されつつある。2. Description of the Related Art Conventionally, the problems to be solved by the invention
Freon-based cleaning agents and chlorine-based solvents such as trichloroethane have been used as industrial cleaning agents for cleaning electronic components and mechanical components. However, these industrial cleaning agents have a problem that they cause destruction of the ozone layer, pollution of groundwater, or deterioration of working environment.
Its use is being regulated.
【0003】そのため、フロン系洗浄剤や、トリクロロ
エタンなどの塩素系溶剤以外の他の洗浄剤(例えば、炭
化水素系洗浄剤)を用いる方法が提案されているが、洗
浄剤が汚れてくると洗浄効果が低下するため、洗浄装置
内の洗浄剤を所定のピッチで更新する必要があり、洗浄
剤の入れ替えの際には洗浄装置を停止しなければなら
ず、効率が悪いという問題点がある。Therefore, a method using a CFC-based cleaning agent or a cleaning agent other than a chlorine-based solvent such as trichloroethane (for example, a hydrocarbon-based cleaning agent) has been proposed, but when the cleaning agent becomes dirty, cleaning is performed. Since the effect decreases, the cleaning agent in the cleaning device needs to be updated at a predetermined pitch, and the cleaning device must be stopped when the cleaning agent is replaced, which is a problem of inefficiency.
【0004】また、例えば、洗浄装置から抜き出した使
用済み洗浄剤を別の場所に設けた再生装置を用いて再生
し、これを再び洗浄装置に戻して再使用する場合、使用
済み洗浄剤の抜き出し、搬送、洗浄装置への張込みなど
の工程が必要となり、繁雑であるばかりでなく、コスト
の増大を招くという問題点がある。Further, for example, when the used cleaning agent extracted from the cleaning apparatus is regenerated by using a regenerating apparatus provided at another place and is returned to the cleaning apparatus for reuse, the used cleaning agent is extracted. However, there is a problem in that it is not only complicated, but also costs are increased, because steps such as transportation, and installation in a cleaning device are required.
【0005】一方、汚染した洗浄液を廃棄することはコ
スト面からみて不利になるばかりでなく資源の浪費とも
なり、好ましくない。On the other hand, it is not preferable to dispose of the contaminated cleaning liquid, not only in terms of cost but also in waste of resources.
【0006】本願発明は、上記問題点を解決するもので
あり、炭化水素系洗浄剤を全体的に入れ替えたりするこ
となく、炭化水素系洗浄剤を所定の洗浄効果を有する清
浄な状態に保持し、連続して安定した洗浄を行うことが
可能であるとともに、種々の洗浄条件に対応した洗浄シ
ステムを構築することが可能な洗浄ユニット及び該洗浄
ユニットを用いてなる洗浄装置を提供することを目的と
する。The present invention solves the above-mentioned problems, and keeps the hydrocarbon-based cleaning agent in a clean state having a predetermined cleaning effect without replacing the entire hydrocarbon-based cleaning agent. An object of the present invention is to provide a cleaning unit capable of continuously and stably cleaning and constructing a cleaning system corresponding to various cleaning conditions, and a cleaning apparatus using the cleaning unit. And
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に、本願発明の洗浄ユニットは、炭化水素系洗浄剤を用
いて洗浄対象物を洗浄する洗浄装置において、洗浄対象
物を炭化水素系洗浄剤により洗浄する洗浄槽と、洗浄工
程で混入した低沸点汚れ成分及び高沸点汚れ成分を含む
炭化水素系洗浄剤を蒸留して、低沸点汚れ成分を蒸留分
離する第1の蒸留器と、第1の蒸留器において低沸点汚
れ成分を蒸留分離した高沸点汚れ成分を含む炭化水素系
洗浄剤を蒸留し、炭化水素系洗浄剤を蒸留分離する第2
の蒸留器とを具備し、かつ、第2の蒸留器において分離
した炭化水素系洗浄剤を前記洗浄槽に循環供給するよう
にしたことを特徴とする。In order to achieve the above object, a cleaning unit of the present invention is a cleaning apparatus for cleaning an object to be cleaned using a hydrocarbon-based cleaning agent, and the object to be cleaned is hydrocarbon-based cleaning. A cleaning tank for cleaning with a cleaning agent, a first distiller for distilling and separating a low boiling point contaminant component by distilling a hydrocarbon cleaning agent containing a low boiling point contaminant component and a high boiling point contaminant component mixed in the cleaning step, In the first distiller, the hydrocarbon detergent containing the high-boiling-point stain component obtained by distilling off the low-boiling-point stain component is distilled, and the hydrocarbon-based detergent is distilled off.
And a hydrocarbon-based cleaning agent separated in the second distillation apparatus is circulated and supplied to the cleaning tank.
【0008】また、本願発明の洗浄装置は、上記の洗浄
ユニットを複数段直列に接続(配置)し、洗浄対象物を
順次後段の洗浄ユニットに送って多段洗浄するようにし
たことを特徴とする。Further, the cleaning apparatus of the present invention is characterized in that the above-mentioned cleaning units are connected (arranged) in a plurality of stages in series and the objects to be cleaned are sequentially sent to the subsequent cleaning unit for multi-stage cleaning. .
【0009】さらに、本願発明の洗浄装置は、上記の洗
浄装置に、さらに、前記各段の洗浄ユニットの第1及び
第2の蒸留器などの廃熱を利用する洗浄対象物の乾燥器
を併設したことを特徴とする。Further, in the cleaning apparatus of the present invention, the above-mentioned cleaning apparatus is further provided with a dryer for cleaning the objects to be cleaned utilizing waste heat such as the first and second distillers of the cleaning units at each stage. It is characterized by having done.
【0010】[0010]
【作用】本願発明の洗浄ユニットにおいては、洗浄対象
物が洗浄槽内で炭化水素系洗浄剤により洗浄される。一
方、洗浄槽内の炭化水素系洗浄剤は、第1の蒸留器にお
いて蒸留され、洗浄工程で混入した低沸点汚れ成分が蒸
留分離(除去)される。さらに、第1の蒸留器で低沸点
汚れ成分が除去された炭化水素系洗浄剤(高沸点汚れ成
分を含む)は、第2の蒸留器において蒸留され、炭化水
素系洗浄剤が溜分として分離回収され、洗浄槽に循環供
給される。なお、第2の蒸留器に残留する高沸点汚れ成
分は必要に応じて系外に排出される。In the cleaning unit of the present invention, the object to be cleaned is cleaned with the hydrocarbon-based cleaning agent in the cleaning tank. On the other hand, the hydrocarbon-based cleaning agent in the cleaning tank is distilled in the first distiller, and the low boiling point contaminant component mixed in the cleaning step is separated (removed) by distillation. Further, the hydrocarbon-based cleaning agent (including the high-boiling-point contaminant component) from which the low-boiling-point contaminant component has been removed in the first distiller is distilled in the second distiller, and the hydrocarbon-based detergent is separated as a fraction. It is collected and circulated and supplied to the cleaning tank. The high boiling point pollutant remaining in the second distiller is discharged out of the system as needed.
【0011】したがって、一つの洗浄ユニット内におい
て、炭化水素系洗浄剤中の低沸点(汚れ)成分及び高沸
点(汚れ)成分が分離、除去されるため、汚れた炭化水
素系洗浄剤を系外に抜き出して再生したりする必要がな
くなり、洗浄槽内の炭化水素系洗浄剤を常に所定の洗浄
能力を有する状態に保持して、洗浄対象物を確実に洗浄
することができるようになる。Therefore, the low boiling point (dirt) component and the high boiling point (dirt) component in the hydrocarbon type cleaning agent are separated and removed in one cleaning unit, so that the dirty hydrocarbon type cleaning agent is removed from the system. It is no longer necessary to extract and regenerate the cleaning object, and the hydrocarbon cleaning agent in the cleaning tank can always be kept in a state of having a predetermined cleaning ability to reliably clean the object to be cleaned.
【0012】また、本願発明の洗浄装置においては、洗
浄対象物が順次後段の洗浄ユニットに送られ、各段で洗
浄(多段洗浄)されるため、例えば、ひどい汚れを除去
する粗洗浄、次の中洗浄、さらには仕上げの精洗浄とい
うように、段階的に洗浄対象物を洗浄することが可能に
なる。したがって、洗浄対象物の状態や目標とする洗浄
の程度にあわせた条件で洗浄を行うことが可能になり、
洗浄効率を向上させることができる。Further, in the cleaning apparatus of the present invention, the object to be cleaned is sequentially sent to the subsequent cleaning unit and cleaned at each stage (multi-stage cleaning). Therefore, for example, rough cleaning for removing terrible dirt, It becomes possible to clean the object to be cleaned in stages, such as medium cleaning and further fine cleaning for finishing. Therefore, it becomes possible to perform cleaning under conditions that match the condition of the object to be cleaned and the target degree of cleaning.
The cleaning efficiency can be improved.
【0013】さらに、本願発明の洗浄装置においては、
上記各段の洗浄ユニットの第1及び第2の蒸留器などの
廃熱が、洗浄後の洗浄対象物を乾燥させるための乾燥器
において利用されるため、乾燥工程における熱エネルギ
ーの使用量を低減して洗浄装置全体としての省エネルギ
ーを図ることができる。Further, in the cleaning apparatus of the present invention,
Since the waste heat of the first and second distillers of the cleaning unit of each stage is used in the dryer for drying the object to be cleaned after cleaning, the amount of heat energy used in the drying process is reduced. As a result, it is possible to save energy in the cleaning device as a whole.
【0014】[0014]
【実施例】以下、本願発明の実施例を図に基づいて説明
する。図1は、本願発明の一実施例にかかる洗浄ユニッ
トを示す図である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a diagram showing a cleaning unit according to an embodiment of the present invention.
【0015】この実施例の洗浄ユニット20は、洗浄対
象物を炭化水素系洗浄剤により洗浄する洗浄槽1と、洗
浄工程で洗浄対象物に由来して混入した低沸点汚れ成分
及び高沸点汚れ成分を含む炭化水素系洗浄剤を蒸留して
低沸点汚れ成分を蒸留分離する第1の蒸留器2と、第1
の蒸留器2において低沸点汚れ成分を蒸留分離した高沸
点汚れ成分を含む炭化水素系洗浄剤を蒸留し、炭化水素
系洗浄剤を溜出させて分離する第2の蒸留器3とを備え
ている。The cleaning unit 20 of this embodiment comprises a cleaning tank 1 for cleaning an object to be cleaned with a hydrocarbon-based cleaning agent, and a low boiling point contaminant component and a high boiling point contaminant component mixed from the object to be cleaned in the cleaning step. A first distiller 2 for distilling and separating a low boiling point soil component by distilling a hydrocarbon-based detergent containing
And a second distiller 3 for distilling and separating the low-boiling-point stain component in the distiller 2 and distilling the hydrocarbon-containing detergent containing the high-boiling-point stain component, and distilling and separating the hydrocarbon-based detergent. There is.
【0016】洗浄槽1は、炭化水素系洗浄剤を所定の温
度に加熱するための加温ヒータ4、温度調節器11、蒸
散ガス冷却コイル7、炭化水素系洗浄剤仕切板16を有
する上部が開放された容器であり、炭化水素系洗浄剤の
温度調節、蒸散ガスの冷却、洗浄に用いられた炭化水素
系洗浄剤の仕切を行うことができる。The cleaning tank 1 has an upper portion having a heating heater 4 for heating a hydrocarbon-based cleaning agent to a predetermined temperature, a temperature controller 11, an evaporated gas cooling coil 7, and a hydrocarbon-based cleaning agent partition plate 16. It is an open container, and can control the temperature of the hydrocarbon-based cleaning agent, cool the evaporated gas, and partition the hydrocarbon-based cleaning agent used for cleaning.
【0017】また、第1の蒸留器2は、加温ヒータ5、
温度調節器12、炭化水素系洗浄剤の溢流板17、底部
から高沸点汚れ成分などを排出するための排出管31を
有した密閉常圧容器であり、洗浄槽1内の汚れた炭化水
素系洗浄剤を受け入れて洗浄槽1の液面を規制するとと
もに、洗浄工程において混入した低沸点汚れ成分を蒸留
分離することができるように構成されている。The first distiller 2 has a heating heater 5,
A sealed atmospheric pressure container having a temperature controller 12, a hydrocarbon-based detergent overflow plate 17, and a discharge pipe 31 for discharging high-boiling-point contaminants from the bottom. It is configured so as to receive the system cleaning agent to regulate the liquid level of the cleaning tank 1 and to distill and separate the low boiling point contaminant components mixed in in the cleaning step.
【0018】さらに、第2の蒸留器3は、加温ヒータ
6、温度警報調節器13、液面警報器14、蒸発ガス冷
却コイル8、再生液循環ライン18、高沸点汚れ成分を
系外に抜き出すための排出管32を備えた密閉常圧容器
であり、低沸点汚れ成分を分離する第1の蒸留器2より
溢流した高沸点汚れ成分を含む炭化水素系洗浄剤から、
炭化水素系洗浄剤を蒸留分離し、凝縮液(再生液)を再
生液循環ライン18を経て洗浄槽1に循環供給するとと
もに、高沸点汚れ成分をその底部に集め、例えば、温度
警報設定値、または、液面警報設定値において、内部の
高沸点汚れ成分(を含む汚れ液)を系外に排出し、また
は、炭化水素系洗浄剤貯槽10から新しい炭化水素系洗
浄剤を補給するように構成されている。Further, the second distiller 3 has a heating heater 6, a temperature alarm controller 13, a liquid level alarm device 14, an evaporative gas cooling coil 8, a regenerant liquid circulation line 18, and a high boiling point contaminant component outside the system. A closed atmospheric pressure vessel equipped with a discharge pipe 32 for withdrawing, from a hydrocarbon-based detergent containing a high boiling point contaminant component overflowing from the first distiller 2 for separating low boiling point contaminant components,
The hydrocarbon-based cleaning agent is separated by distillation, and the condensate (regeneration liquid) is circulated and supplied to the cleaning tank 1 through the regeneration liquid circulation line 18, and the high-boiling point contaminants are collected at the bottom thereof, for example, a temperature alarm set value, Alternatively, at the liquid level alarm set value, the internal high boiling point contaminant component (including the contaminant liquid) is discharged to the outside of the system, or a new hydrocarbon type detergent is replenished from the hydrocarbon type detergent storage tank 10. Has been done.
【0019】また、洗浄槽1の上部の蒸散ガス、第1の
蒸留器2の上部の蒸散ガス、第2の蒸留器3の上部の不
凝縮ガスは排気ブロワー9により系外に排出される。Further, the vaporized gas above the cleaning tank 1, the vaporized gas above the first distiller 2 and the non-condensed gas above the second distiller 3 are discharged outside the system by an exhaust blower 9.
【0020】さらに、第1の蒸留器2の蒸散ガス冷却コ
イル7、第2の蒸留器3の蒸発ガス冷却コイル8には、
冷却水が供給される。冷却水の供給は、凝縮液温度調節
器15により凝縮液が所定の温度になるように、調節供
給される。そして、第1の蒸留器の蒸散ガス冷却コイル
7、第2の蒸留器3の蒸発ガス冷却コイル8において熱
交換された冷却水(温排水)は、後述の乾燥器(21
a,21b)に送られ、廃熱回収された後排水される。Further, the evaporated gas cooling coil 7 of the first distiller 2 and the evaporated gas cooling coil 8 of the second distiller 3 are
Cooling water is supplied. The supply of the cooling water is adjusted and supplied by the condensate temperature controller 15 so that the condensate has a predetermined temperature. Then, the cooling water (warm waste water) that has undergone heat exchange in the evaporated gas cooling coil 7 of the first distiller and the evaporative gas cooling coil 8 of the second distiller 3 is dried by a dryer (21) described later.
a, 21b), waste heat is recovered, and then drained.
【0021】次に、上記のように構成された洗浄ユニッ
トの動作について説明を行う。Next, the operation of the cleaning unit configured as described above will be described.
【0022】まず、洗浄対象物を入れた、金網やパンチ
ングメタルなどの洗浄液が通過する材料からなる容器3
0が洗浄槽1内の炭化水素系洗浄剤中に浸漬され、洗浄
が行われる。このとき必要に応じて容器を揺動したり、
超音波振動を加えたりする。この洗浄工程において、洗
浄対象物に付着していた低沸点汚れ成分と高沸点汚れ成
分が炭化水素系洗浄剤中に移行する。低沸点汚れ成分と
高沸点汚れ成分が混入した炭化水素系洗浄剤は、第1の
蒸留器2に移行して加温ヒータ5により加熱され、低沸
点汚れ成分が蒸留分離される。なお、蒸散した低沸点汚
れ成分は蒸散ガス冷却コイル7を通過する冷却水と熱交
換した後、排気ブロワー9から系外に排出される。First, a container 3 containing a material to be cleaned and made of a material through which a cleaning liquid such as a wire mesh or punching metal passes.
0 is immersed in the hydrocarbon-based cleaning agent in the cleaning tank 1 for cleaning. At this time, rock the container as necessary,
Apply ultrasonic vibration. In this cleaning step, the low boiling point stain component and the high boiling point stain component adhering to the object to be cleaned are transferred into the hydrocarbon-based cleaning agent. The hydrocarbon detergent mixed with the low-boiling point stain component and the high-boiling point stain component moves to the first distiller 2 and is heated by the warming heater 5 to separate the low-boiling point stain component by distillation. The evaporated low-boiling-point contaminants exchange heat with the cooling water passing through the evaporated gas cooling coil 7, and are then discharged from the exhaust blower 9 to the outside of the system.
【0023】低沸点汚れ成分が除去された炭化水素系洗
浄剤(高沸点汚れ成分を含む)は、溢流板17を越えて
第2の蒸留器3に移行し、加温ヒータ6により加熱され
て、炭化水素系洗浄剤が蒸留分離される。そして、分離
された炭化水素系洗浄剤(再生液)は再生液循環ライン
18を経て洗浄槽1に循環供給される。また、第2の蒸
留器3の底部に溜まった高沸点汚れ成分は、例えば、温
度警報設定値などの所定の条件下において、排出管32
を経て系外に排出される。また、第2の蒸留器3の液面
が液面警報設定値以下になると、炭化水素系洗浄剤貯槽
10から新しい炭化水素系洗浄剤が補給される。なお、
図1において、33はベントラインである。The hydrocarbon cleaning agent (including the high boiling point contaminants) from which the low boiling point contaminants have been removed moves over the overflow plate 17 to the second distiller 3 and is heated by the heating heater 6. Thus, the hydrocarbon detergent is separated by distillation. Then, the separated hydrocarbon-based cleaning agent (regenerated liquid) is circulated and supplied to the cleaning tank 1 through the regenerated liquid circulation line 18. Further, the high-boiling-point contaminants accumulated at the bottom of the second distiller 3 are discharged from the discharge pipe 32 under a predetermined condition such as a temperature alarm set value.
Is discharged to the outside of the system. When the liquid level of the second distiller 3 becomes equal to or lower than the liquid level alarm set value, a new hydrocarbon-based cleaning agent is replenished from the hydrocarbon-based cleaning agent storage tank 10. In addition,
In FIG. 1, 33 is a vent line.
【0024】上述のように、この実施例の洗浄ユニット
20によれば、一つの洗浄ユニット内において、炭化水
素系洗浄剤中の低沸点(汚れ)成分及び高沸点(汚れ)
成分が分離、除去されるため、汚れた炭化水素系洗浄剤
を系外に抜き出して再生したりすることなく、洗浄槽内
の炭化水素系洗浄剤を常に所定の洗浄能力を有する状態
に保持して、洗浄対象物を確実に洗浄することができる
ようになる。As described above, according to the cleaning unit 20 of this embodiment, a low boiling point (dirt) component and a high boiling point (dirt) in the hydrocarbon-based cleaning agent are contained in one cleaning unit.
Since the components are separated and removed, the hydrocarbon cleaning agent in the cleaning tank is always kept in a state with a predetermined cleaning ability without extracting the dirty hydrocarbon cleaning agent out of the system for regeneration. Thus, the object to be cleaned can be surely cleaned.
【0025】また、図2は、上記の洗浄ユニット20を
用いて構成した本願発明の一実施例にかかる洗浄装置を
示す図である。この洗浄装置は、3つの洗浄ユニット2
0a,20b,20cと、2つの乾燥器21a,21b
を備えている。FIG. 2 is a diagram showing a cleaning apparatus according to an embodiment of the present invention, which is constructed by using the cleaning unit 20 described above. This cleaning device includes three cleaning units 2
0a, 20b, 20c and two dryers 21a, 21b
Is equipped with.
【0026】すなわち、この洗浄装置においては、粗洗
浄用の一段目の洗浄ユニット20aと、中洗浄用の2段
目の洗浄ユニット20bと、精洗浄用の3段目の洗浄ユ
ニット20cが直列に接続(配置)されている。また、
一段目の乾燥器21aと2段目の乾燥器21bも直列に
接続(配置)されている。That is, in this cleaning apparatus, the first-stage cleaning unit 20a for rough cleaning, the second-stage cleaning unit 20b for intermediate cleaning, and the third-stage cleaning unit 20c for precise cleaning are connected in series. Connected (placed). Also,
The first-stage dryer 21a and the second-stage dryer 21b are also connected (arranged) in series.
【0027】この乾燥器21a,21bは、それぞれ加
温コイル22a,22b及び乾燥ガス供給口23a,2
3bを有する開放器であり、上記各洗浄ユニット20
a,20b,20cを経て十分に洗浄された洗浄対象物
を通気乾燥するように構成されている。The dryers 21a and 21b are provided with heating coils 22a and 22b and dry gas supply ports 23a and 2 respectively.
The cleaning unit 20 is an opener having 3b.
The object to be cleaned that has been sufficiently cleaned via a, 20b, and 20c is configured to be air-dried.
【0028】この乾燥器21a,21bは、上記洗浄ユ
ニット20a,20b,20cの廃熱を利用するように
構成されており、第1の蒸留器2の蒸散ガス冷却コイル
7及び第2の蒸留器3の蒸発ガス冷却コイル8から排出
される温排水を乾燥器21a,21bの加温コイル22
a,22bに供給することにより、洗浄ユニット20
a,20b,20cの廃熱が乾燥器21a,21bにお
いて回収される。The dryers 21a and 21b are constructed so as to utilize the waste heat of the cleaning units 20a, 20b and 20c, and the evaporated gas cooling coil 7 of the first distiller 2 and the second distiller are used. The warm waste water discharged from the evaporative gas cooling coil 8 of No. 3 is heated by the heating coil 22 of the dryers 21a and 21b.
a, 22b to supply the cleaning unit 20
Waste heat of a, 20b, 20c is recovered in the dryers 21a, 21b.
【0029】なお、乾燥工程では、まず、洗浄後の洗浄
対象物が、1段目の乾燥器21aに入れられ、加温コイ
ル22aにより所定の温度に加熱しつつ、下部の乾燥ガ
ス供給口23aから乾燥ガス(通常は、空気が用いられ
るが、これに限られるものではない)を供給することに
より乾燥される。さらに、洗浄対象物は2段目の乾燥器
21bに移され、加温コイル22bにより所定の温度に
加熱しつつ、下部の乾燥ガス供給口23bから乾燥ガス
を供給することにより十分に乾燥される。こうして乾燥
された洗浄対象物は、部品や製品として回収され、その
用途に応じて次工程に送られる。In the drying step, first, the object to be cleaned after cleaning is put in the first-stage dryer 21a and heated to a predetermined temperature by the heating coil 22a, while the lower dry gas supply port 23a is provided. To provide drying gas (usually, but not limited to air). Further, the object to be cleaned is transferred to the second-stage dryer 21b, and is sufficiently dried by supplying the dry gas from the lower dry gas supply port 23b while being heated to a predetermined temperature by the heating coil 22b. . The object to be washed thus dried is collected as a part or a product and sent to the next step depending on its use.
【0030】上記実施例では、洗浄ユニットを3段に直
列接続(配置)した場合について説明したが、通常は、
2〜6段直列接続(配置)することにより、必要な洗浄
効率を得ることができる。但し、接続(配置)段数に特
別の制約はなく、洗浄対象物の用途、汚れの程度、後続
する処理工程の内容その他の条件を考慮して適当な段数
を選択することが可能である。In the above embodiment, the case where the cleaning units are connected in series (arranged) in three stages has been described.
The required cleaning efficiency can be obtained by connecting (arranging) two to six stages in series. However, there is no particular restriction on the number of connection (arrangement) stages, and it is possible to select an appropriate number of stages in consideration of the use of the object to be cleaned, the degree of contamination, the contents of subsequent processing steps, and other conditions.
【0031】また、上記実施例では、2つの乾燥器を直
列に接続(配置)した場合について説明したが、通常
は、1〜3段直列に接続(配置)することにより、洗浄
対象物を十分に乾燥することができる。但し、その段数
に特別の制約はなく、さらに多くの乾燥器を直列に配設
することも可能であり、また、乾燥器を並列に接続(配
置)することも可能である。In the above embodiment, the case where two dryers are connected (arranged) in series has been described, but normally, by connecting (arranging) 1 to 3 stages in series, the object to be cleaned can be sufficiently treated. Can be dried. However, the number of stages is not particularly limited, and more dryers can be arranged in series, and the dryers can be connected (arranged) in parallel.
【0032】なお、本願発明の洗浄装置において用いら
れる炭化水素系洗浄剤の種類には、特に制約はなく、種
々の炭化水素系洗浄剤を用いることが可能である。次
に、上記実施例にかかる洗浄装置を用いて行った洗浄実
験の結果を示す。There are no particular restrictions on the type of hydrocarbon-based cleaning agent used in the cleaning apparatus of the present invention, and various hydrocarbon-based cleaning agents can be used. Next, the results of a cleaning experiment conducted using the cleaning apparatus according to the above-mentioned example will be shown.
【0033】[実験例1]プレス加工したアルミニウム
製の精密部品を、長さ200mm×幅150mm×高さ10
0mmの角形のかごに充填し、炭化水素系洗浄剤としてエ
クソン社製,アクトレル(登録商標))を用いて、表1
に示すような条件の下で洗浄を行った。[Experimental Example 1] A precision part made of aluminum which has been press-worked has a length of 200 mm, a width of 150 mm and a height of 10.
It was filled in a 0 mm square cage and used as a hydrocarbon-based cleaner, Exxon Corp., ACTREL (registered trademark), and the results are shown in Table 1.
Washing was performed under the conditions shown in.
【0034】[0034]
【表1】 [Table 1]
【0035】洗浄された精密部品の脱脂率は99.99
%であった。The degreasing rate of the cleaned precision parts is 99.99.
%Met.
【0036】[実験例2]切削加工した鉄製部品を、直
径200mm×長さ150mmの円筒状のかごに充填し、炭
化水素系洗浄剤としてエクソン社製,アクトレル(登録
商標)を用いて、表2に示すような条件の下で洗浄を行
った。[Experimental Example 2] A machined iron part was filled in a cylindrical cage having a diameter of 200 mm and a length of 150 mm, and Acton (registered trademark) manufactured by Exxon Co. was used as a hydrocarbon cleaning agent. Washing was performed under the conditions shown in 2.
【0037】[0037]
【表2】 [Table 2]
【0038】洗浄された鉄製部品の脱脂率は99.97
%であった。The degreasing rate of the washed iron parts is 99.97.
%Met.
【0039】なお、上記実施例では、洗浄剤として炭化
水素系洗浄剤を用いた場合を例にとって説明したが、本
願発明の洗浄ユニット及び該洗浄ユニットを用いてなる
洗浄装置は、炭化水素系洗浄剤以外の他の有機系あるい
は無機系の洗浄剤を用いる場合にも適用することが可能
であり、その場合にも上記実施例と同様の効果を得るこ
とが可能である。In the above embodiments, the case where the hydrocarbon-based cleaning agent is used as the cleaning agent has been described as an example. However, the cleaning unit of the present invention and the cleaning device using the cleaning unit are not limited to hydrocarbon-based cleaning. It can be applied to the case of using an organic or inorganic cleaning agent other than the cleaning agent, and in that case, the same effect as that of the above-described embodiment can be obtained.
【0040】[0040]
【発明の効果】上述のように、本願発明の洗浄ユニット
は、洗浄対象物を炭化水素系洗浄剤により洗浄する洗浄
槽と、炭化水素系洗浄剤を蒸留して低沸点汚れ成分を蒸
留分離する第1の蒸留器と、第1の蒸留器において低沸
点汚れ成分を蒸留分離した高沸点汚れ成分を含む炭化水
素系洗浄剤を蒸留して、炭化水素系洗浄剤を蒸留分離す
る第2の蒸留器とを備え、かつ、第2の蒸留器において
分離した炭化水素系洗浄剤を前記洗浄槽に循環供給する
ようにしているので、一つの洗浄ユニット内において、
炭化水素系洗浄剤中の低沸点(汚れ)成分及び高沸点
(汚れ)成分を分離、除去し、汚れた炭化水素系洗浄剤
を系外に抜き出して再生したりする必要がなくなり、洗
浄槽内の炭化水素系洗浄剤を常に所定の洗浄能力を有す
る状態に保持して、洗浄対象物を確実に洗浄することが
可能になる。As described above, in the cleaning unit of the present invention, a cleaning tank for cleaning an object to be cleaned with a hydrocarbon-based cleaning agent and a hydrocarbon-based cleaning agent are distilled to separate low-boiling-point contaminants by distillation. A first distiller and a second distillation for distilling and separating the hydrocarbon detergent containing a high-boiling-point stain component obtained by distilling and separating the low-boiling-point stain component in the first distiller. Since the hydrocarbon-based cleaning agent separated in the second distiller is circulated and supplied to the cleaning tank, in one cleaning unit,
It is no longer necessary to separate and remove low-boiling point (dirt) components and high-boiling point (dirt) components in hydrocarbon-based cleaning agents and to remove dirty hydrocarbon-based cleaning agents from the system to regenerate them. It becomes possible to reliably clean the object to be cleaned by always keeping the hydrocarbon-based cleaning agent of (3) in a state having a predetermined cleaning ability.
【0041】また、本願発明の洗浄装置は、上記洗浄ユ
ニットを複数段直列に接続(配置)し、洗浄対象物を各
段の洗浄ユニットにおいて多段洗浄するようにしている
ので、洗浄対象物の状態や目標とする洗浄効率にあわせ
た条件で洗浄を行うことが可能になり、洗浄効果を向上
させることができる。Further, in the cleaning apparatus of the present invention, the cleaning units are connected (arranged) in a plurality of stages in series, and the cleaning target is subjected to multi-stage cleaning in the cleaning units of each stage. It becomes possible to perform cleaning under conditions that match the target cleaning efficiency and the cleaning effect can be improved.
【0042】さらに、上記各段の洗浄ユニットの第1及
び第2の蒸留器などの廃熱を利用した、洗浄後の洗浄対
象物を乾燥させるための乾燥器を併設した洗浄装置によ
れば、乾燥工程における熱エネルギーの使用量を低減し
て洗浄装置全体としての省エネルギーを図ることができ
る。Further, according to the cleaning apparatus, which uses the waste heat of the first and second distillers of the cleaning unit of each stage and has a dryer for drying the object to be cleaned after cleaning, It is possible to reduce the amount of heat energy used in the drying process and save energy in the cleaning device as a whole.
【図1】本願発明の一実施例にかかる洗浄ユニットを示
す図である。FIG. 1 is a diagram showing a cleaning unit according to an embodiment of the present invention.
【図2】本願発明の一実施例にかかる洗浄装置の概略構
成を示す図である。FIG. 2 is a diagram showing a schematic configuration of a cleaning apparatus according to an embodiment of the present invention.
1 洗浄槽 2 第1の蒸留器 3 第2の蒸留器 20(20a,20b,20c) 洗浄ユニット 21a,21b 乾燥器 30 洗浄対象物を収容す
る容器1 Cleaning Tank 2 First Distiller 3 Second Distiller 20 (20a, 20b, 20c) Cleaning Units 21a, 21b Dryer 30 Container for Accommodating Cleaning Object
───────────────────────────────────────────────────── フロントページの続き (72)発明者 斉藤 英司 兵庫県尼崎市杭瀬寺島2丁目1番2号 木 村化工機株式会社内 (72)発明者 秋田 浩司 兵庫県尼崎市杭瀬寺島2丁目1番2号 木 村化工機株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Eiji Saito 2-1, 2 Kisederajima, Amagasaki City, Hyogo Prefecture Kimura Kakoki Co., Ltd. (72) Koji Akita 2-1-2, Kisejijima, Amagasaki, Hyogo Kimura Kakoki Co., Ltd.
Claims (3)
洗浄する洗浄装置において、洗浄対象物を炭化水素系洗
浄剤により洗浄する洗浄槽と、洗浄工程で混入した低沸
点汚れ成分及び高沸点汚れ成分を含む炭化水素系洗浄剤
を蒸留して、低沸点汚れ成分を蒸留分離する第1の蒸留
器と、第1の蒸留器において低沸点汚れ成分を蒸留分離
した高沸点汚れ成分を含む炭化水素系洗浄剤を蒸留し、
炭化水素系洗浄剤を蒸留分離する第2の蒸留器とを具備
し、かつ、第2の蒸留器において分離した炭化水素系洗
浄剤を前記洗浄槽に循環供給するようにしたことを特徴
とする洗浄ユニット。1. A cleaning apparatus for cleaning an object to be cleaned using a hydrocarbon-based cleaning agent, a cleaning tank for cleaning the object to be cleaned with a hydrocarbon-based cleaning agent, and a low boiling point contaminant component and a high contaminant mixed in the cleaning step. A first distiller for distilling and separating a low boiling point stain component by distilling a hydrocarbon detergent containing a boiling point stain component, and a high boiling point stain component obtained by distilling and separating a low boiling point stain component in the first distiller. Distilling hydrocarbon cleaners,
A second distiller for distilling and separating a hydrocarbon-based cleaning agent is provided, and the hydrocarbon-based cleaning agent separated in the second distiller is circulated and supplied to the cleaning tank. Cleaning unit.
列に接続(配置)し、洗浄対象物を順次後段の洗浄ユニ
ットに送って多段洗浄するようにしたことを特徴とする
洗浄装置。2. A cleaning apparatus, wherein the cleaning units according to claim 1 are connected (arranged) in series in a plurality of stages, and the objects to be cleaned are sequentially sent to a cleaning unit in a subsequent stage for multi-stage cleaning.
記各段の洗浄ユニットの第1及び第2の蒸留器などの廃
熱を利用する洗浄対象物の乾燥器を併設したことを特徴
とする洗浄装置。3. The cleaning apparatus according to claim 2, further comprising a dryer for cleaning the object to be cleaned using waste heat such as the first and second distillers of the cleaning units of each stage. And cleaning equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23316092A JPH0655150A (en) | 1992-08-06 | 1992-08-06 | Washing unit and washing apparatus using the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23316092A JPH0655150A (en) | 1992-08-06 | 1992-08-06 | Washing unit and washing apparatus using the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0655150A true JPH0655150A (en) | 1994-03-01 |
Family
ID=16950664
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23316092A Pending JPH0655150A (en) | 1992-08-06 | 1992-08-06 | Washing unit and washing apparatus using the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0655150A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0356183A (en) * | 1989-07-25 | 1991-03-11 | Ebara Corp | Washing apparatus |
-
1992
- 1992-08-06 JP JP23316092A patent/JPH0655150A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0356183A (en) * | 1989-07-25 | 1991-03-11 | Ebara Corp | Washing apparatus |
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