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JP2001181874A - Degreasing and cleaning method and cleaner - Google Patents

Degreasing and cleaning method and cleaner

Info

Publication number
JP2001181874A
JP2001181874A JP36091599A JP36091599A JP2001181874A JP 2001181874 A JP2001181874 A JP 2001181874A JP 36091599 A JP36091599 A JP 36091599A JP 36091599 A JP36091599 A JP 36091599A JP 2001181874 A JP2001181874 A JP 2001181874A
Authority
JP
Japan
Prior art keywords
hydrocarbon
cleaning
tank
cleaning tank
based solvent
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.)
Granted
Application number
JP36091599A
Other languages
Japanese (ja)
Other versions
JP4328436B2 (en
Inventor
Kenichi Yamaoka
憲一 山岡
Yoshio Matsuda
淑男 松田
Tsutomu Ota
努 太田
Hiroyasu Murata
裕康 村田
Nobuyuki Yamaji
信幸 山地
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sansha Electric Manufacturing Co Ltd
Mitsubishi Electric Corp
Original Assignee
Sansha Electric Manufacturing Co Ltd
Mitsubishi Electric Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sansha Electric Manufacturing Co Ltd, Mitsubishi Electric Corp filed Critical Sansha Electric Manufacturing Co Ltd
Priority to JP36091599A priority Critical patent/JP4328436B2/en
Publication of JP2001181874A publication Critical patent/JP2001181874A/en
Application granted granted Critical
Publication of JP4328436B2 publication Critical patent/JP4328436B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Cleaning By Liquid Or Steam (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain the degreasing and cleaning method and cleaner by which a material deposited with a water-soluble oil, a nonaqueous oil, etc., to be cleaned is surely cleaned, and the plating film and coating film excellent in appearance, corrosion resistance and adhesion are provided as the degreasing and cleaning method and cleaner for cleaning the material with a hydrocarbonic solvent contained in a single hydrocarbonic cleaning tank of one-tank structure. SOLUTION: A material to be cleaned is dipped in the hydrocarbonic solvent contained in a hydrocarbonic cleaning tank of one-tank structure in the first stage, and the material dipped in the solvent is dipped in an acidic solution in the second stage so as to clean the material.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、水溶性油及び非
水系油などが付着したアルミニウム合金等の被処理物に
おける表面周辺に対して、所要の機能を賦与するために
おこなわれる、めっきや塗装のための脱脂洗浄方法およ
びその洗浄装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to plating and coating performed on a surface of an object to be treated such as an aluminum alloy to which a water-soluble oil or a non-aqueous oil has been adhered so as to impart a required function. The present invention relates to a degreasing cleaning method and a cleaning device therefor.

【0002】[0002]

【従来の技術】一般に、めっきや塗装を行なうための被
処理物の表面には、水溶性油及び非水系油などの付着物
が存在するため、めっきや塗装を行う前の前処理として
脱脂洗浄処理を行う必要がある。この種の洗浄処理にお
いては、トリクロロエチレン等の塩素系有機溶剤を洗浄
溶剤に用いた脱脂洗浄が従来広く行なわれていた。しか
しながら、この洗浄溶剤は環境に対して悪影響を及ぼす
可能性のある有害な物質を含んでおり、洗浄液が地下に
浸透して土壌や地下水などを汚染しないように、あるい
は空気中に拡散して大気を汚染しないように慎重に管理
して洗浄処理を行う必要があり、また環境問題の観点か
らも使用の廃止が望まれていた。
2. Description of the Related Art In general, since there is a deposit such as a water-soluble oil and a non-aqueous oil on the surface of an object to be plated or painted, degreasing and cleaning are performed as a pretreatment before plating and painting. Processing needs to be performed. In this type of cleaning treatment, degreasing cleaning using a chlorine-based organic solvent such as trichloroethylene as a cleaning solvent has been widely performed. However, this cleaning solvent contains harmful substances that may have an adverse effect on the environment, so that the cleaning liquid does not penetrate into the ground and contaminate soil or groundwater, or diffuse into the air to remove air. It is necessary to carry out the cleaning treatment with careful management so as not to contaminate it, and it has been desired to abolish the use from the viewpoint of environmental problems.

【0003】このために、近年この種の洗浄処理では、
トリクロロエチレン等の塩素系有機溶剤に代わる脱脂洗
浄溶剤として、例えばパラフィン系の炭化水素(例えば
組成式C12.224.4)のような炭化水素系溶剤が用いら
れている。この溶剤を用いた脱脂洗浄処理では、先ず水
溶性油中に存在する防腐剤や界面活性剤等の水溶性成分
を水溶性洗浄剤で取り除き、次いで炭化水素系溶剤によ
って水分を除去した後、最後に水溶性油に含まれる油分
と非水系の油分を除去する方法が採られていた。
[0003] For this reason, in recent years, this type of cleaning process has
As degreasing solvent in place of chlorinated organic solvents trichlorethylene, for example, hydrocarbon solvents such as paraffinic hydrocarbons (e.g. formula C 12.2 H 24.4) is used. In the degreasing cleaning treatment using this solvent, first, water-soluble components such as preservatives and surfactants present in the water-soluble oil are removed with a water-soluble cleaning agent, and then water is removed with a hydrocarbon-based solvent. A method for removing oil contained in water-soluble oil and non-aqueous oil has been adopted.

【0004】図5は、炭化水素系溶剤を用いた従来のア
ルミニウム合金に対する洗浄処理からめっき処理までの
表面処理における概略工程を示す図である。図5におい
て、油分を除去する洗浄装置1bでは、水溶性洗浄剤を
満たした第一の洗浄槽2で被処理物の表面に存在する水
溶性成分の防腐剤や界面活性剤等を除去し、炭化水素系
溶剤を満たした第二の洗浄槽3で被処理物の表面に残る
水分を除去し、炭化水素系溶剤を満たした第三の洗浄槽
4で油分を除去する。次に、油分を除去した被処理物
は、常法によるアルカリ脱脂槽5で動植物油を除去さ
れ、水洗を経て酸洗い槽6で被処理物の表面が活性化さ
れ、さらに水洗を経てめっき槽7でめっき処理される。
FIG. 5 is a view showing a schematic process in a surface treatment from a cleaning treatment to a plating treatment for a conventional aluminum alloy using a hydrocarbon-based solvent. In FIG. 5, in a cleaning device 1 b for removing oil, a preservative, a surfactant, and the like of a water-soluble component present on the surface of the processing object are removed in a first cleaning tank 2 filled with a water-soluble cleaning agent. Moisture remaining on the surface of the object is removed in the second cleaning tank 3 filled with the hydrocarbon solvent, and oil is removed in the third cleaning tank 4 filled with the hydrocarbon solvent. Next, the object to be treated from which the oil has been removed is subjected to removal of animal and vegetable oils in an alkaline degreasing tank 5 by a conventional method, washed with water, activated in a pickling tank 6, and further washed with water to form a plating tank. 7 is plated.

【0005】[0005]

【発明が解決しようとする課題】上記のように従来の洗
浄装置1bは、水溶性洗浄剤を満たした第一の洗浄槽
2、炭化水素系溶剤を満たした第二の洗浄槽3及び第三
の洗浄槽4とで構成された三槽から成る脱脂洗浄槽を備
え、第二の洗浄槽3と第三の洗浄槽4に炭化水素系溶剤
を要するため、洗浄装置1bを設置するスペースや消防
法による保管容量に関する制限規定の関係上、1槽当り
の容量が小さくなり、したがって被処理物の対象品も寸
法上の制限を受けざるを得なかった。
As described above, the conventional cleaning apparatus 1b comprises a first cleaning tank 2 filled with a water-soluble cleaning agent, a second cleaning tank 3 filled with a hydrocarbon-based solvent, and a third cleaning tank 3 filled with a hydrocarbon solvent. And a third cleaning tank 4 comprising a degreasing cleaning tank, and a second cleaning tank 3 and a third cleaning tank 4 requiring a hydrocarbon-based solvent. Due to the restrictions on the storage capacity by the law, the capacity per tank is reduced, so that the object to be processed must be limited in size.

【0006】一方、被処理物の寸法上の制限を避けるた
めに炭化水素系溶剤を満たした槽を1槽化した場合、例
えばアルミニウム合金を炭化水素系溶剤で洗浄した後
に、アルカリ脱脂槽5で常法によるアルカリ脱脂を行な
い、水洗を経て酸洗い槽6で酸洗いし、水洗を経てめっ
き槽7でめっきを行うときに、水溶性油の成分である防
腐剤や界面活性剤がアルカリ脱脂槽5及び酸洗い槽6で
除去出来ず、その結果外観を損なったり、耐蝕性や密着
性の劣っためっきとなるなどの欠陥が生じた。
On the other hand, when the tank filled with the hydrocarbon-based solvent is made into one tank in order to avoid the restriction on the size of the object to be treated, for example, after the aluminum alloy is washed with the hydrocarbon-based solvent, the aluminum degreasing tank 5 is used. When performing alkali degreasing by a conventional method, washing with water and pickling in the pickling tank 6, and performing plating in the plating tank 7 after washing with water, the preservative or surfactant which is a component of the water-soluble oil is removed from the alkali degreasing tank. 5 and the pickling tank 6 could not be removed, resulting in defects such as impaired appearance and plating with poor corrosion resistance and adhesion.

【0007】この発明は、かかる問題を解決するために
成されたものであり、水溶性油、非水系油がなどが付着
した被処理物について脱脂が確実に行なわれ、外観や耐
蝕性、密着性に優れためっき膜及び塗膜を提供する、脱
脂洗浄方法および洗浄装置を得ることを目的としたもの
である。
SUMMARY OF THE INVENTION The present invention has been made to solve such a problem. The object to be treated to which a water-soluble oil or a non-aqueous oil has adhered is surely degreased, and its appearance, corrosion resistance, and adhesion are improved. It is an object of the present invention to obtain a degreasing cleaning method and a cleaning apparatus which provide a plating film and a coating film having excellent properties.

【0008】また、この発明は、炭化水素系溶剤によっ
て油を除去する洗浄槽の大型化と、十分な安全性の確保
を図り、被処理物の寸法上の制限を緩和して脱脂を行な
うとともに脱脂洗浄後の乾燥を短時間で行うことを目的
とするものである。
Further, the present invention increases the size of a cleaning tank for removing oil with a hydrocarbon-based solvent, secures sufficient safety, relaxes the dimensional restrictions on the object to be treated, and performs degreasing. It is intended to perform drying after degreasing and washing in a short time.

【0009】[0009]

【課題を解決するための手段】第1の発明による脱脂洗
浄方法は、水溶性油及び非水系油などが付着した被洗浄
物を炭化水素系溶剤に浸漬して脱脂した後、酸性溶液で
水溶性油の成分を除去するものである。
According to a first aspect of the present invention, there is provided a degreasing cleaning method according to the first aspect of the present invention, wherein an object to be cleaned to which a water-soluble oil or a non-aqueous oil is adhered is immersed in a hydrocarbon solvent to degrease the material, and then the aqueous solution is acidified. It removes the components of the essential oil.

【0010】また、第2の発明による脱脂洗浄方法は、
水溶性油及び非水系油などが付着した被洗浄物を炭化水
素系溶剤に浸漬して脱脂した後、動植物油を除去するた
めのアルカリ脱脂を得ることなく酸性溶液に浸漬するこ
とによって水溶性油の成分を除去し、しかるべき後に動
植物油を除去するアルカリ脱脂と被洗浄物を化学的に活
性化する酸洗いを行なうものである。
[0010] The degreasing and cleaning method according to the second invention comprises:
After the object to be cleaned to which the water-soluble oil and the non-aqueous oil are adhered is immersed in a hydrocarbon-based solvent to degrease it, and then immersed in an acidic solution without obtaining an alkaline degrease for removing animal and vegetable oils. And then, after appropriate time, alkali degreasing to remove animal and vegetable oils and pickling to chemically activate the object to be cleaned.

【0011】また、第3の発明による脱脂洗浄方法は、
上記酸性溶液が、0.267モル乃至2.670モルの
硫酸と0.56モル以下のアルミニウムを成分とする洗
浄液から成るものである。
Further, the degreasing and cleaning method according to the third invention is characterized in that:
The acidic solution comprises a washing solution containing 0.267 mol to 2.670 mol of sulfuric acid and 0.56 mol or less of aluminum.

【0012】また、第4の発明による脱脂洗浄方法は、
上記酸性溶液が、0.206モル乃至0.412モルの
硝酸と0.05モル乃至0.10モルのフッ酸と0.1
5モル乃至0.30モルの塩化第二鉄を成分とする洗浄
液から成るものである。
Further, the degreasing and cleaning method according to the fourth invention comprises:
The acidic solution is prepared by mixing 0.206 mol to 0.412 mol of nitric acid, 0.05 mol to 0.10 mol of hydrofluoric acid and 0.1 mol.
It consists of a cleaning solution containing 5 to 0.30 mol of ferric chloride.

【0013】また、第5の発明による脱脂洗浄方法は、
5.03乃至6.70モルの硝酸と、3.35乃至4.
46モルの硫酸と、0.18乃至0.37モルのりん酸
と、1.58乃至2.10モルの酸性弗化アンモニウム
とを成分とする洗浄液から成るものである。
Further, the degreasing and cleaning method according to the fifth invention is characterized in that:
5.03 to 6.70 mol of nitric acid and 3.35 to 4.
The cleaning solution comprises 46 mol of sulfuric acid, 0.18 to 0.37 mol of phosphoric acid, and 1.58 to 2.10 mol of ammonium acid fluoride.

【0014】また、第6の発明による脱脂洗浄方法は、
被洗浄物を炭化水素系溶剤に浸漬する第1の工程と、上
記炭化水素系溶剤に浸漬された被洗浄物を酸性溶液に浸
漬する第2の工程と、上記酸性溶液に浸漬された被洗浄
物をアルカリ脱脂する第3の工程と、上記アルカリ脱脂
された被洗浄物を化学的に活性化する酸洗いを行う第4
の工程とを備えたものである。
Further, the degreasing and cleaning method according to the sixth invention is characterized in that:
A first step of immersing the object to be cleaned in a hydrocarbon-based solvent; a second step of immersing the object to be cleaned immersed in the hydrocarbon-based solvent in an acidic solution; A third step of alkali-degreasing the object, and a fourth step of pickling for chemically activating the alkali-degreased object to be cleaned.
And the steps of

【0015】また、第7の発明による脱脂洗浄方法は、
上記第4の工程として、上記第3の工程でアルカリ脱脂
された被洗浄物を後工程でめっきもしくは塗装するため
の酸洗いを行うものである。
Further, the degreasing and cleaning method according to the seventh invention is characterized in that:
In the fourth step, the object to be cleaned, which has been alkali-degreased in the third step, is subjected to pickling for plating or painting in a subsequent step.

【0016】また、第8の発明による脱脂洗浄方法は、
気密形成可能な炭化水素洗浄槽に水溶性油及び非水系油
等が付着した被洗浄物を収容し内部を気密形成する準備
工程と、上記炭化水素洗浄槽に設けた複数のノズルから
炭化水素系溶剤をシャワー水として供給し上記被洗浄物
をシャワー洗浄するとともに、上記炭化水素洗浄槽に上
記炭化水素系溶剤を溜める第1のシャワー洗浄工程と、
上記シャワー水を継続して供給させて溜められた炭化水
素系溶剤を攪拌させるとともに、上記被洗浄物から取り
出された水溶性油及び非水系油を上記炭化水素系溶剤と
ともに回収する第2のシャワー洗浄工程とを備えたもの
である。
Further, the degreasing method according to the eighth invention is characterized in that:
A preparatory step of storing an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like is attached in a hydrocarbon cleaning tank capable of forming airtight, and forming an airtight inside; A first shower cleaning step of supplying the solvent as shower water and shower-cleaning the object to be cleaned, and storing the hydrocarbon-based solvent in the hydrocarbon cleaning tank;
A second shower for continuously supplying the shower water to stir the accumulated hydrocarbon solvent and recovering the water-soluble oil and the non-aqueous oil taken out from the object to be cleaned together with the hydrocarbon solvent; And a washing step.

【0017】また、第9の発明による脱脂洗浄方法は、
気密形成可能な炭化水素洗浄槽に水溶性油及び非水系油
等が付着した被洗浄物を収容し内部を気密形成する準備
工程と、上記炭化水素洗浄槽に設けた複数のノズルから
炭化水素系溶剤をシャワー水として供給し上記被洗浄物
をシャワー洗浄するとともに、上記炭化水素洗浄槽に上
記炭化水素系溶剤を溜める第1のシャワー洗浄工程と、
上記第1のシャワー洗浄工程終了後上記炭化水素洗浄槽
に大量且つ高速に上記炭化水素系溶剤を供給し噴流水を
発生させるとともに回収し、上記炭化水素系溶剤を循環
させる噴流水循環工程とを備えたものである
Further, the degreasing and cleaning method according to the ninth invention is characterized in that:
A preparatory step of storing an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like is attached in a hydrocarbon cleaning tank capable of forming airtight, and forming an airtight inside; A first shower cleaning step of supplying the solvent as shower water and shower-cleaning the object to be cleaned, and storing the hydrocarbon-based solvent in the hydrocarbon cleaning tank;
A jet water circulating step of supplying the hydrocarbon solvent in a large amount and at a high speed to the hydrocarbon washing tank after the first shower washing step, generating and collecting jet water, and circulating the hydrocarbon solvent. Is

【0018】また、第10の発明による脱脂洗浄方法
は、気密形成可能な炭化水素洗浄槽に水溶性油及び非水
系油等が付着した被洗浄物を収容し内部を気密形成する
準備工程と、上記炭化水素洗浄槽に設けた複数のノズル
から炭化水素系溶剤をシャワー水として供給し上記被洗
浄物をシャワー洗浄する第1のシャワー洗浄工程と、上
記第1のシャワー洗浄工程終了後上記炭化水素系溶剤を
回収する第1の回収工程と、上記第1の回収工程終了後
清浄な炭化水素系溶剤を被洗浄物に供給しリンスするリ
ンス工程と、上記リンス工程終了後リンス後の上記炭化
水素系溶剤を回収する第2の回収工程と、上記第2の回
収工程終了後上記炭化水素洗浄槽に加熱した窒素ガスを
供給して、上記炭化水素洗浄槽内を窒素ガスに置換する
第1の窒素ガス置換工程と、上記第1の窒素ガス置換工
程終了後上記炭化水素洗浄槽を減圧する減圧乾燥工程と
を備えたものである。
[0018] The degreasing method according to the tenth aspect of the present invention includes a preparatory step of accommodating an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered in an airtightly formed hydrocarbon cleaning tank, and forming an airtight inside. A first shower cleaning step of supplying a hydrocarbon-based solvent as shower water from a plurality of nozzles provided in the hydrocarbon cleaning tank to shower-clean the object to be cleaned, and the hydrocarbon after completion of the first shower cleaning step A first recovery step of recovering a system solvent, a rinsing step of supplying a clean hydrocarbon-based solvent to the object to be cleaned after the first recovery step, and rinsing the hydrocarbon after the completion of the rinsing step A second recovery step of recovering the system solvent, and a first step of supplying heated nitrogen gas to the hydrocarbon cleaning tank after completion of the second recovery step to replace the inside of the hydrocarbon cleaning tank with nitrogen gas. Nitrogen gas replacement Extent and is obtained by a vacuum drying process for reducing the pressure of said first nitrogen-gas replacement step after completion of the hydrocarbon cleaning tank.

【0019】また、第11の発明による脱脂洗浄方法
は、気密形成可能な炭化水素洗浄槽に水溶性油及び非水
系油等が付着した被洗浄物を収容し内部を気密形成する
準備工程と、上記炭化水素洗浄槽に設けた複数のノズル
から炭化水素系溶剤をシャワー水として供給し上記被洗
浄物をシャワー洗浄するとともに、上記炭化水素洗浄槽
に上記炭化水素系溶剤を溜める第1のシャワー洗浄工程
と、上記第1のシャワー洗浄工程終了後上記炭化水素洗
浄槽に大量且つ高速に上記炭化水素系溶剤を供給し噴流
水を発生させるとともに回収し、上記炭化水素系溶剤を
循環させる噴流水循環工程と、上記噴流水循環工程終了
後上記炭化水素系溶剤を回収する第1の回収工程と、上
記第1の回収工程終了後清浄な炭化水素系溶剤を被洗浄
物に供給しリンスするリンス工程と、上記リンス工程終
了後上記リンス後の炭化水素系溶剤を回収する第2の回
収工程と、上記第2の回収工程終了後上記炭化水素洗浄
槽に加熱した窒素ガスを供給して、上記炭化水素洗浄槽
内を窒素ガスに置換する第1の窒素ガス置換工程と、上
記第1の窒素ガス置換工程終了後上記炭化水素洗浄槽を
減圧する減圧乾燥工程とを備えたものである。
[0019] The degreasing method according to the eleventh aspect of the present invention includes a preparatory step of accommodating an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered in an airtightly formed hydrocarbon cleaning tank, and forming an airtight inside. First shower cleaning in which the hydrocarbon-based solvent is supplied as shower water from a plurality of nozzles provided in the hydrocarbon cleaning tank to shower-clean the object to be cleaned, and the hydrocarbon-based solvent is stored in the hydrocarbon cleaning tank. And a jet water circulating step of supplying the hydrocarbon solvent in a large amount and at a high speed to the hydrocarbon cleaning tank after the first shower cleaning step, generating and collecting jet water, and circulating the hydrocarbon solvent. And a first recovery step of recovering the hydrocarbon-based solvent after completion of the jet water circulation step, and supplying a clean hydrocarbon-based solvent to the object to be cleaned after completion of the first recovery step, and rinsing the same. A rinsing step, a second recovery step of recovering the hydrocarbon solvent after rinsing after the rinsing step, and supplying heated nitrogen gas to the hydrocarbon cleaning tank after the second recovery step. The method includes a first nitrogen gas replacement step of replacing the inside of the hydrocarbon cleaning tank with nitrogen gas, and a reduced pressure drying step of reducing the pressure of the hydrocarbon cleaning tank after the first nitrogen gas replacement step.

【0020】また、第12の発明による脱脂洗浄方法
は、上記窒素ガス置換工程終了後に、上記炭化水素洗浄
槽内にエアーを供給し、窒素ガスからエアーに置換する
第1の混合置換工程を備えたものである。
Further, the degrease cleaning method according to the twelfth invention comprises a first mixed replacement step of supplying air into the hydrocarbon cleaning tank and replacing the nitrogen gas with air after the completion of the nitrogen gas replacement step. It is a thing.

【0021】また、第13の発明による脱脂洗浄方法
は、上記減圧乾燥工程終了後に、上記炭化水素洗浄槽に
加熱した窒素ガスを供給して、上記炭化水素洗浄槽内を
窒素ガスに置換する第2の窒素ガス置換工程と、上記炭
化水素洗浄槽内にエアーを供給し、窒素ガスからエアー
に置換する第2の混合置換工程を備えたものである。
In a thirteenth aspect of the present invention, in the degreasing cleaning method according to the thirteenth aspect, after the reduced pressure drying step is completed, heated nitrogen gas is supplied to the hydrocarbon cleaning tank to replace the inside of the hydrocarbon cleaning tank with nitrogen gas. A nitrogen gas replacement step, and a second mixed replacement step of supplying air into the hydrocarbon cleaning tank and replacing the nitrogen gas with air.

【0022】また、第14の発明による洗浄装置は、水
溶性油及び非水系油などが付着した被洗浄物を炭化水素
系溶剤によって脱脂洗浄する洗浄装置において、炭化水
素系溶剤を注入するための1槽から成る炭化水素洗浄槽
と、水溶性油の成分を除去する酸性溶液を注入するため
の酸洗い槽とを備えたものである。
A cleaning apparatus according to a fourteenth aspect of the present invention is a cleaning apparatus for degrease-cleaning an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered, using a hydrocarbon-based solvent. It is provided with a hydrocarbon washing tank consisting of one tank and an acid washing tank for injecting an acidic solution for removing components of the water-soluble oil.

【0023】また、第15の発明による洗浄装置は、水
溶性油及び非水系油などが付着した被洗浄物を炭化水素
系溶剤によって脱脂洗浄する洗浄装置において、炭化水
素系溶剤を注入するための1槽から成る炭化水素洗浄槽
と、上記炭化水素洗浄槽で洗浄される被洗浄物を、上記
炭化水素洗浄槽から酸性溶液を注入するための酸洗い槽
へ向かう搬送経路へ搬送するための移送手段とを備えた
ものである。
A cleaning apparatus according to a fifteenth aspect of the present invention is a cleaning apparatus for degrease-cleaning an object to be cleaned to which a water-soluble oil and a non-aqueous oil are attached with a hydrocarbon solvent. A hydrocarbon cleaning tank composed of one tank, and a transfer for transferring an object to be cleaned in the hydrocarbon cleaning tank to a transport path from the hydrocarbon cleaning tank to an acid cleaning tank for injecting an acidic solution. Means.

【0024】また、第16の発明による洗浄装置は、上
面に開口部を有する槽とこの槽の開口部を塞ぐあるいは
開くための開閉自在な蓋とを有し、この槽に水溶性油及
び非水系油等が付着した被洗浄物を収容し炭化水素系溶
剤による洗浄を行う気密形成可能な炭化水素洗浄槽であ
って、上記蓋の下面に互いに離間して配置され炭化水素
系溶剤を噴出する複数のノズルと、上記それぞれのノズ
ルから噴出された炭化水素系溶剤が重なりを有する高さ
の近傍に設けられ、上記炭化水素系溶剤を槽内から排出
する排水口とを有した炭化水素洗浄槽を備えたものであ
る。
A cleaning apparatus according to a sixteenth aspect of the present invention has a tank having an opening on an upper surface and an openable / closable lid for closing or opening the opening of the tank. An airtightly formed hydrocarbon cleaning tank that accommodates an object to be cleaned to which water-based oil or the like has adhered and performs cleaning with a hydrocarbon-based solvent, which is disposed separately from the lower surface of the lid and ejects the hydrocarbon-based solvent. A plurality of nozzles and a hydrocarbon cleaning tank provided near a height at which the hydrocarbon solvents ejected from the respective nozzles have an overlap, and a drain port for discharging the hydrocarbon solvents from the tank; It is provided with.

【0025】また、第17の発明による洗浄装置は、第
1の開口部とこの開口部を開閉するための第1の開閉手
段を有し、水溶性油及び非水系油等が付着した被洗浄物
を収容し炭化水素系溶剤による洗浄を行う気密形成可能
な炭化水素洗浄槽と、上記炭化水素洗浄槽から洗浄後の
炭化水素系溶剤を回収する排液回収手段と、上記炭化水
素洗浄槽内のガス又は水分を外部に排気する第1の排気
手段とを備え、上記炭化水素洗浄槽は、第2の開口部、
この開口部を開閉するための第2の開閉手段、および内
部の空気を上記外部に排出する第2の排気手段とを有し
て気密形成可能なコテージ内に収容されるように設置さ
れるものである。
A cleaning apparatus according to a seventeenth aspect of the present invention has a first opening and first opening / closing means for opening and closing the opening, and a cleaning target to which water-soluble oil, non-aqueous oil, or the like adheres. A hydrocarbon-cleaning tank capable of forming a gas-tight chamber for containing a substance and cleaning with a hydrocarbon-based solvent, a drainage recovery means for recovering the hydrocarbon-based solvent after cleaning from the hydrocarbon-cleaning tank, and A first exhaust unit that exhausts the gas or moisture of the gas to the outside, wherein the hydrocarbon cleaning tank has a second opening,
A second opening / closing means for opening / closing the opening, and a second exhaust means for exhausting the internal air to the outside; It is.

【0026】また、第18の発明による洗浄装置は、水
溶性油及び非水系油等が付着した被洗浄物を収容し炭化
水素系溶剤による洗浄と乾燥を行う気密形成可能な炭化
水素洗浄槽と、上記炭化水素系溶剤を収容するリザーブ
タンクと、上記炭化水素系溶剤を蒸留再生させた清浄な
炭化水素系溶剤を収容するリンス液タンクと、上記リザ
ーブタンク内の上記炭化水素系溶剤を取り入れ、上記炭
化水素洗浄槽に供給する洗浄用ポンプと、上記リンス液
タンク内の上記清浄な炭化水素系溶剤を取り入れ、上記
炭化水素洗浄槽に供給するリンス液用ポンプとが、気密
形成可能なコテージにより収容されているものである。
A cleaning apparatus according to an eighteenth aspect of the present invention includes a hydrocarbon cleaning tank capable of containing an object to be cleaned to which a water-soluble oil, a non-aqueous oil, or the like has adhered, and performing an airtight hydrocarbon cleaning tank for cleaning and drying with a hydrocarbon solvent. A reservoir tank containing the hydrocarbon solvent, a rinse liquid tank containing a clean hydrocarbon solvent obtained by distilling and regenerating the hydrocarbon solvent, and incorporating the hydrocarbon solvent in the reserve tank; A cleaning pump to be supplied to the hydrocarbon cleaning tank, and a rinse liquid pump that takes in the clean hydrocarbon solvent in the rinsing liquid tank and supplies the hydrocarbon cleaning tank to the rinsing liquid tank, according to a cottage that can be airtightly formed. It is housed.

【0027】また、第19の発明による洗浄装置は、水
溶性油及び非水系油等が付着した被洗浄物を収容し炭化
水素系溶剤による洗浄と乾燥を行う気密形成可能な炭化
水素洗浄槽と、上記炭化水素洗浄槽から洗浄後の炭化水
素系溶剤を回収する排液回収手段と、上記炭化水素洗浄
槽内のガス又は水分を外部に排出する真空ポンプと、窒
素ガスを発生させる窒素ガス発生装置と、上記窒素ガス
を上記炭化水素洗浄槽に供給し窒素ガスに置換する置換
乾燥系と、上記窒素ガス置換終了後に、上記炭化水素洗
浄槽内にエアーを供給し、窒素ガスからエアーに置換す
る混合置換系とを備えたものである。
A cleaning apparatus according to a nineteenth aspect of the present invention includes a hydrocarbon-cleaning tank capable of holding an object to be cleaned to which a water-soluble oil and a non-aqueous oil or the like has adhered and capable of cleaning and drying with a hydrocarbon-based solvent and drying. A drain recovery means for recovering the hydrocarbon solvent after cleaning from the hydrocarbon cleaning tank, a vacuum pump for discharging gas or moisture in the hydrocarbon cleaning tank to the outside, and a nitrogen gas generation for generating nitrogen gas An apparatus, a replacement drying system for supplying the nitrogen gas to the hydrocarbon cleaning tank and replacing it with nitrogen gas, and after the completion of the nitrogen gas replacement, supplying air into the hydrocarbon cleaning tank and replacing the nitrogen gas with air. And a mixed substitution system.

【0028】また、第20の発明による洗浄装置は、水
溶性油及び非水系油等が付着した被洗浄物を収容し炭化
水素系溶剤による洗浄と乾燥を行う気密形成可能な炭化
水素洗浄槽と、上記炭化水素系溶剤を収容するリザーブ
タンクと、上記炭化水素系溶剤を蒸留再生させた清浄な
炭化水素系溶剤を収容するリンス液タンクと、上記リザ
ーブタンク内の上記炭化水素系溶剤を取り入れ、上記炭
化水素洗浄槽に供給する洗浄用ポンプと、上記リンス液
タンク内の上記清浄な炭化水素系溶剤を取り入れ、上記
炭化水素洗浄槽に供給するリンス液用ポンプと、上記炭
化水素洗浄槽内のガス又は水分を外部に排出する真空ポ
ンプと、窒素ガスを発生させる窒素ガス発生装置と、上
記窒素ガスを上記炭化水素洗浄槽に供給し窒素ガスに置
換する置換乾燥系とを備えたものである。
A cleaning apparatus according to a twentieth aspect of the present invention comprises an airtight hydrocarbon cleaning tank for containing an object to be cleaned to which a water-soluble oil, a non-aqueous oil, or the like is attached, and performing cleaning and drying with a hydrocarbon solvent. A reservoir tank containing the hydrocarbon solvent, a rinse liquid tank containing a clean hydrocarbon solvent obtained by distilling and regenerating the hydrocarbon solvent, and incorporating the hydrocarbon solvent in the reserve tank; A cleaning pump for supplying to the hydrocarbon cleaning tank, a rinsing liquid pump for supplying the clean hydrocarbon-based solvent in the rinsing liquid tank, and supplying the rinsing liquid to the hydrocarbon cleaning tank, A vacuum pump for discharging gas or moisture to the outside, a nitrogen gas generator for generating nitrogen gas, and a replacement drying system for supplying the nitrogen gas to the hydrocarbon cleaning tank and replacing it with nitrogen gas It is those with a.

【0029】また、第21の発明による洗浄装置は、上
記置換乾燥系に水分とガスとを分離させ乾燥させる乾燥
器と、ガスを加熱する加熱器とを備えたものである。
A cleaning apparatus according to a twenty-first aspect of the present invention is provided with a dryer for separating and drying water and gas from the replacement drying system, and a heater for heating gas.

【0030】また、第22の発明による洗浄装置は、上
記洗浄用ポンプから上記炭化水素洗浄槽に設けられた複
数のノズルに上記炭化水素系溶剤を送出し、上記ノズル
からシャワー水を供給するシャワー水供給機構と、上記
洗浄用ポンプから上記炭化水素洗浄槽に大量かつ高速に
上記炭化水素系溶剤を供給する噴流水供給機構と、上記
シャワー水供給機構と上記噴流水供給機構とを切換指令
する切換指令装置とを備えたものである。
The cleaning apparatus according to a twenty-second aspect of the present invention is a shower wherein the hydrocarbon-based solvent is sent from the cleaning pump to a plurality of nozzles provided in the hydrocarbon cleaning tank, and shower water is supplied from the nozzles. A water supply mechanism, a jet water supply mechanism for supplying the hydrocarbon solvent from the cleaning pump to the hydrocarbon cleaning tank in a large amount and at a high speed, and a command to switch between the shower water supply mechanism and the jet water supply mechanism. And a switching command device.

【0031】また、第23の発明による洗浄装置は、上
記炭化水素洗浄槽が、開口する上部と、側部から内部に
向かって下がる勾配を有し、その中央部が下に深淵をな
す底部とを有する洗浄部と、上記洗浄部の開口を覆いふ
さぐ蓋とを有し気密状態を形成可能な洗浄槽であり、両
側に伸張し、中央部が深淵をなして上記炭化水素洗浄槽
に収容されるバスケットとの組合せを備えたものであ
る。
Further, in the cleaning apparatus according to the twenty-third aspect, the hydrocarbon cleaning tank has an opening at the top and a slope descending from the side toward the inside, and the bottom has a deep bottom at the center. A washing tank having a washing section having a lid and a cover covering the opening of the washing section, and capable of forming an airtight state.The washing tank extends on both sides, and the central part forms a deep abundance and is accommodated in the hydrocarbon washing tank. It is provided with a combination with a basket.

【0032】さらにまた、第24の発明による洗浄装置
は、水溶性油及び非水系油等が付着した被洗浄物を収容
し炭化水素系溶剤による洗浄と乾燥を行う気密形成可能
な炭化水素洗浄槽と、上記炭化水素系溶剤を収容するリ
ザーブタンクと、上記リザーブタンク内の上記炭化水素
系溶剤を取り入れ、上記炭化水素洗浄槽に供給する洗浄
用ポンプと、上記リザーブタンク内の炭化水素系溶剤が
所定の液面レベルより低下したとき上記洗浄用ポンプの
動作の停止指令を行う液面プロテクタとを備えたもので
ある。
Furthermore, the cleaning apparatus according to the twenty-fourth aspect of the present invention is a hydrocarbon cleaning tank capable of holding an object to be cleaned to which a water-soluble oil or a non-aqueous oil or the like has adhered and performing an airtight formation and cleaning and drying with a hydrocarbon solvent. And, a reservoir tank containing the hydrocarbon solvent, a washing pump that takes in the hydrocarbon solvent in the reserve tank and supplies it to the hydrocarbon washing tank, and a hydrocarbon solvent in the reserve tank. A liquid level protector for issuing a command to stop the operation of the cleaning pump when the liquid level falls below a predetermined liquid level.

【0033】[0033]

【発明の実施の形態】実施の形態1.図1は、この発明
の実施の形態1による各処理槽およびその表面処理工程
を示すものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiment 1 FIG. 1 shows each processing tank according to Embodiment 1 of the present invention and surface treatment steps thereof.

【0034】図1において、1aは炭化水素系溶剤が注
入され、概略寸法が例えば長さ3500mm×幅800
mm×深さ700mmのように、消防法で規制される最
大容量を満足する大きさ(容量2000リットル未満)
を有した1槽構造の炭化水素洗浄槽を示し、この槽では
炭化水素系溶剤によって、例えばアルミニウム合金のよ
うな被処理物を脱脂する洗浄工程を行い、水溶性油に含
まれる油及び非水系油を除去する。
In FIG. 1, reference numeral 1a denotes a hydrocarbon-based solvent injected, and its approximate dimensions are, for example, 3500 mm in length × 800 in width.
A size that satisfies the maximum capacity regulated by the Fire Service Law, such as mm x 700 mm (capacity less than 2000 liters)
1 shows a hydrocarbon cleaning tank having a single tank structure, in which a cleaning step of degreased an object to be processed such as an aluminum alloy with a hydrocarbon-based solvent is performed. Remove the oil.

【0035】次に、0.267モル乃至2.670モル
の硫酸と0.56モル以下のアルミニウムとを成分とす
る酸洗液、又は0.206モル乃至0.412モルの硝
酸と0.05モル乃至0.10モルのフッ酸と0.15
モル乃至0.30モルの塩化第二鉄とを成分とする酸洗
液、又は5.03乃至6.70モルの硝酸と3.35乃
至4.46モルの硫酸と0.18乃至0.37モルのり
ん酸と1.58乃至2.10モルの酸性弗化アンモニウ
ムとを成分とする酸洗液を内含した酸洗い槽6で被処理
物を洗浄することによって、水溶性油中の防腐剤や界面
活性剤等の水溶性成分を除去する。なお、この酸洗液の
濃度については、ここで規定した範囲外のモル数を用い
た場合に水溶性成分の除去効果が低減し、この後工程で
めっき処理を行う際に耐食性や密着性の劣っためっきに
なり得る。
Next, a pickling solution containing 0.267 mol to 2.670 mol of sulfuric acid and 0.56 mol or less of aluminum, or 0.206 mol to 0.412 mol of nitric acid and 0.05 mol Mol to 0.10 mol of hydrofluoric acid and 0.15 mol
A pickling solution containing mol to 0.30 mol of ferric chloride, or 5.03 to 6.70 mol of nitric acid, 3.35 to 4.46 mol of sulfuric acid and 0.18 to 0.37 The object to be treated is washed in a pickling tank 6 containing a pickling solution containing mol phosphoric acid and 1.58 to 2.10 mol of ammonium ammonium fluoride as components. Removes water-soluble components such as agents and surfactants. Regarding the concentration of the pickling solution, when a mole number outside the range specified here is used, the effect of removing the water-soluble component is reduced, and when performing plating treatment in the subsequent step, corrosion resistance and adhesion Poor plating can result.

【0036】以上のように洗浄処理することにより、水
溶性油中の防腐剤や界面活性剤等の水溶性成分の除去に
優れた効果を発揮し、従来は3槽で行っていた水溶性洗
剤(第一の洗浄槽2に内含)と炭化水素系溶剤(第二、
第三の洗浄槽3、4に内含)による脱脂洗浄処理を、炭
化水素系溶剤を内含する1槽の洗浄槽(炭化水素洗浄槽
1a)と酸洗い槽6で行うことができ、洗浄工程がより
短縮される。また、洗浄装置を1槽の炭化水素洗浄槽1
aと酸洗い槽6とで構成することによって、洗浄装置の
大型化を図ることが可能となり、したがって、例えば炭
化水素洗浄槽1a内に目一杯入るような大物の被処理物
の洗浄や、一般の小物被処理物の大量洗浄が可能とな
り、洗浄作業のコスト低減につながる。なお、この洗浄
装置では、被洗浄物としてアルミニウム合金以外の合金
の洗浄を行っても良い。また、炭化水素洗浄槽1aの最
大容量が、消防法で規定されている最大容量を満足する
大きさであれば、上述した槽の寸法以外の大きさであっ
ても良く、被洗浄物の最大寸法や形状、あるいは炭化水
素洗浄槽1a内で被洗浄物を納めるバスケットの大きさ
などに合わせて槽の寸法をきめれば良い。さらに、炭化
水素洗浄槽1aと酸洗い槽6は、被洗浄物を炭化水素洗
浄槽1aから酸洗い槽6へ移送する作業効率を著しく妨
げない範囲において、離間した異なるスペースに分離し
て配置しても良い。この場合、炭化水素洗浄槽1aから
酸洗い槽6への移送手段として、炭化水素洗浄槽1a中
の被洗浄物を吊り上げて引き出し、酸洗い槽6近辺ある
いはその搬送経路上に向けて搬送するためにクレーンの
ような搬送装置を備えるのが、移送効率をあげる点で望
ましい。
By performing the washing treatment as described above, an excellent effect of removing water-soluble components such as a preservative and a surfactant in the water-soluble oil is exhibited, and the water-soluble detergent conventionally used in three tanks is used. (Included in the first cleaning tank 2) and a hydrocarbon solvent (second,
The degreasing cleaning process using the third cleaning tanks 3 and 4) can be performed in one cleaning tank (hydrocarbon cleaning tank 1a) and a pickling tank 6 containing a hydrocarbon solvent. The process is further shortened. Further, the cleaning device is a single hydrocarbon cleaning tank 1.
a and the pickling tank 6, it is possible to increase the size of the cleaning apparatus. Therefore, for example, cleaning of a large object to be fully covered in the hydrocarbon cleaning tank 1a, It is possible to wash a large amount of small objects to be processed, which leads to a reduction in the cost of the washing operation. In this cleaning apparatus, an object other than an aluminum alloy may be cleaned as an object to be cleaned. Further, as long as the maximum capacity of the hydrocarbon cleaning tank 1a satisfies the maximum capacity specified by the Fire Service Act, the hydrocarbon cleaning tank 1a may have a size other than the dimensions of the tank described above. The size of the tank may be determined according to the size and shape, or the size of the basket for storing the object to be cleaned in the hydrocarbon cleaning tank 1a. Further, the hydrocarbon washing tank 1a and the pickling tank 6 are separately arranged in different spaces which do not significantly impede the work efficiency of transferring the object to be washed from the hydrocarbon washing tank 1a to the pickling tank 6. May be. In this case, as a means for transferring from the hydrocarbon washing tank 1a to the pickling tank 6, the object to be washed in the hydrocarbon washing tank 1a is lifted and pulled out, and is conveyed to the vicinity of the pickling tank 6 or to the conveying route thereof. It is desirable to provide a transfer device such as a crane in order to increase transfer efficiency.

【0037】実施の形態2.この実施の形態では、図1
に示す炭化水素洗浄槽1aにおいて油分を除去し、酸洗
い液槽6で水溶性油中の防腐剤や界面活性剤等の水溶性
成分を除去して水洗を経た後に、この実施の形態では酸
洗い槽6近辺に配置されるめっき槽にてめっき処理を行
う。
Embodiment 2 In this embodiment, FIG.
After the oil content is removed in the hydrocarbon washing tank 1a shown in (1) and the water-soluble components such as preservatives and surfactants in the water-soluble oil are removed in the pickling liquid tank 6, and the water is washed, the acid is removed in this embodiment. Plating is performed in a plating tank arranged near the washing tank 6.

【0038】このめっき処理では、まず常法によるアル
カリ脱脂液槽5で動植物油を除去し水洗を行った後、実
施の形態1で示した酸洗い液槽6を再び用いて酸洗いを
行い被処理物を活性化し、水洗を経てめっき液槽7でめ
っき処理を行う。
In this plating treatment, animal and vegetable oils are first removed in a conventional alkaline degreasing solution tank 5 and washed with water, and then pickling is performed again using the pickling solution tank 6 described in the first embodiment. The treated material is activated, and after the washing, plating treatment is performed in the plating solution tank 7.

【0039】図2において、25mm×100mm×1
mmの厚さを有する、6061材、5052材などのア
ルミニウム合金片に水溶性油を塗布し、所定時間放置後
に水溶性油の塗布されたアルミニウム合金片を炭化水素
洗浄槽1aにて洗浄後、めっき処理した場合の、従来の
手法(従来法A)とこの実施の形態による手法(本方法
B)とのめっきの出来栄えを比較した結果を示す。ここ
において、水溶性油中の防腐剤や界面活性剤等の水溶性
成分の除去度合いに応じて、めっきの出来栄えが異なっ
てくる。図において、従来法Aでは、5つのアルミニウ
ム合金片をそれぞれ6h,12h,24h,48h,9
6hの各時間放置後、各時間放置されたアルミニウム合
金片をそれぞれ炭化水素洗浄槽1aにて洗浄し、アルカ
リ脱脂槽5でアルカリ脱脂を行った後に、酸洗い槽6に
て活性化のための酸洗いをしてから、めっき槽7にてア
ルミニウム化学皮膜処理または無電解ニッケルめっきを
行った。また、本方法Bでは、5つのアルミニウム合金
片をそれぞれ6h,12h,24h,48h,96hの
各時間放置後、各時間放置されたアルミニウム合金片を
それぞれ炭化水素洗浄槽1aにて洗浄し、0.267モ
ル乃至2.670モルの硫酸と0.56モル以下のアル
ミニウムとを成分とする酸洗液、又は0.206モル乃
至0.412モルの硝酸と0.05モル乃至0.10モ
ルのフッ酸と0.15モル乃至0.30モルの塩化第二
鉄とを成分とする酸洗液、又は1.33モル乃至13.
3モルの硝酸もしくは5.03乃至6.70モルの硝酸
と3.35乃至4.46モルの硫酸と0.18乃至0.
37モルのりん酸と1.58乃至2.10モルの酸性弗
化アンモニウムとを成分とする酸洗液の含有された酸洗
い槽6にて洗浄する。その後、このアルミニウム合金片
をアルカリ脱脂槽5でアルカリ脱脂を行い、再び酸洗い
槽6に入れて活性化のためにの酸洗いをしてから、めっ
き槽7にてアルミニウム化学皮膜処理または無電解ニッ
ケルめっきを行った。これによれば、本方法Bのよう
に、炭化水素系溶剤で洗浄後、アルカリ洗浄の前に上記
成分の酸洗液で洗浄を行なうことにより、アルミニウム
合金への化学皮膜処理後に膜の外観が優れ、かつ耐蝕性
が向上し、無電解ニッケルにおいても膜の密着性が向上
すると言う優れた効果を得られることが判る。またこの
結果により、本方法Bを採用することによって水溶性油
中の防腐剤や界面活性剤等の水溶性成分が十分に除去さ
れることが判る。
In FIG. 2, 25 mm × 100 mm × 1
water-soluble oil is applied to aluminum alloy pieces such as 6061 material and 5052 material having a thickness of 5 mm, and after leaving for a predetermined time, the aluminum alloy pieces coated with the water-soluble oil are washed in a hydrocarbon washing tank 1a. The results of comparison of plating performance between the conventional method (conventional method A) and the method according to this embodiment (this method B) when plating is performed are shown. Here, the quality of plating varies depending on the degree of removal of water-soluble components such as a preservative and a surfactant in the water-soluble oil. In the figure, in the conventional method A, five aluminum alloy pieces are respectively attached to 6h, 12h, 24h, 48h, 9
After leaving for 6 hours, the aluminum alloy pieces left for each time are washed in a hydrocarbon washing tank 1a, alkali degreasing is performed in an alkali degreasing tank 5, and then activated in an acid washing tank 6. After pickling, aluminum plating or electroless nickel plating was performed in the plating tank 7. Further, in the method B, after leaving the five aluminum alloy pieces for 6 h, 12 h, 24 h, 48 h, and 96 h, respectively, the aluminum alloy pieces left for each time are washed in the hydrocarbon washing tank 1 a, respectively. A pickling solution containing sulfuric acid of 0.267 mol to 2.670 mol and aluminum of 0.56 mol or less, or 0.206 mol to 0.412 mol of nitric acid and 0.05 mol to 0.10 mol of Pickling solution containing hydrofluoric acid and 0.15 mol to 0.30 mol of ferric chloride, or 1.33 mol to 13.
3 mol of nitric acid or 5.03 to 6.70 mol of nitric acid, 3.35 to 4.46 mol of sulfuric acid and 0.18 to 0.1 mol.
Washing is carried out in a pickling bath 6 containing a pickling solution containing 37 mol of phosphoric acid and 1.58 to 2.10 mol of ammonium fluoride. Thereafter, the aluminum alloy pieces are subjected to alkali degreasing in an alkali degreasing tank 5 and again put into a pickling tank 6 to be pickled for activation, and then subjected to an aluminum chemical film treatment or electroless plating in a plating tank 7. Nickel plating was performed. According to this, as in the present method B, after cleaning with a hydrocarbon-based solvent, and before cleaning with an alkali, cleaning with an acid pickling solution of the above-described component is performed, so that the appearance of the film after the chemical coating treatment on the aluminum alloy is improved. It can be seen that the excellent effect of improving the corrosion resistance and improving the adhesiveness of the film even with electroless nickel can be obtained. Further, from the results, it can be understood that the water-soluble components such as the preservative and the surfactant in the water-soluble oil are sufficiently removed by employing the method B.

【0040】以上のように、実施の形態2による炭化水
素洗浄槽1aおよび酸洗い槽6での洗浄処理後に、この
めっき処理を行うことにより、従来の炭化水素系溶剤に
よる脱脂洗浄処理後のめっき処理と比べて、外観に優
れ、耐蝕性、密着性に優れためっき膜や塗膜を得る事が
出来る。また、このめっきの前処理として酸洗いを行う
酸洗い槽6を、脱脂洗浄処理とめっき処理の両方に兼用
することによって、洗浄装置およびめっき処理のための
設備が簡潔になる。
As described above, by performing the plating treatment after the cleaning treatment in the hydrocarbon washing tank 1a and the pickling tank 6 according to the second embodiment, the plating after the conventional degreasing treatment with a hydrocarbon solvent is performed. Compared with the treatment, it is possible to obtain a plating film or a coating film which is excellent in appearance, corrosion resistance and adhesion. Further, by using the pickling tank 6 for pickling as a pre-treatment of the plating for both the degreasing and the plating and the plating, the cleaning device and the equipment for the plating are simplified.

【0041】なおこのめっき処理では、酸洗い槽6以外
の、所定の酸洗液が内含された他の酸洗い槽を使って活
性化のための酸洗いを行っても良いことは言うまでもな
い。また、めっき処理の工程においては、めっきの代わ
りに塗装処理を行っても良い。
In this plating treatment, it goes without saying that pickling for activation may be performed using another pickling tank containing a predetermined pickling solution other than the pickling tank 6. . In the plating process, a coating process may be performed instead of plating.

【0042】実施の形態3.つぎに、図1に示す炭化水
素洗浄槽1aを用いた洗浄装置の具体的な実施の形態を
図3により説明する。図において10は炭化水素洗浄槽
であり、これは図1の炭化水素洗浄槽1aに当たる。炭
化水素洗浄槽10は、上部が開口する洗浄部10aと、
洗浄部10aの開口を覆いふさぐ開閉可能な蓋10bに
より構成されている。洗浄部10aは、側部10cと、
側部10cの下部から内部に向かって2〜10度の角度
で下がる勾配を有する第1の底部10dと、この第1の
底部10dの中央が下に深淵を成す第2の底部10eと
を有し全体が逆凸型の構造となっており、上述したよう
に概略寸法が例えば長さ3500mm×幅800mm×
深さ700mmのように、消防法で規制される最大容量
を満足する大きさ(容量2000リットル未満)を有し
ている。
Embodiment 3 Next, a specific embodiment of the cleaning apparatus using the hydrocarbon cleaning tank 1a shown in FIG. 1 will be described with reference to FIG. In the figure, reference numeral 10 denotes a hydrocarbon cleaning tank, which corresponds to the hydrocarbon cleaning tank 1a in FIG. The hydrocarbon cleaning tank 10 includes a cleaning unit 10a having an open top,
The opening and closing cover 10b covers the opening of the cleaning unit 10a. The cleaning unit 10a includes a side unit 10c,
It has a first bottom portion 10d having a gradient that is inclined downward from the lower portion of the side portion 10c at an angle of 2 to 10 degrees, and a second bottom portion 10e having a deep bottom at the center of the first bottom portion 10d. The whole has an inverted convex structure, and as described above, the approximate dimensions are, for example, length 3500 mm × width 800 mm ×
It has a size (capacity less than 2000 liters) that satisfies the maximum capacity regulated by the Fire Service Law, such as a depth of 700 mm.

【0043】12は洗浄部10aに収容される大きさを
有するバスケットであり、このバスケット12内に図示
しない水溶性油及び非水系油等が付着した被洗浄物が収
容される。このバスケット12は、大型の被洗浄物を収
容して第2の底部10eを跨ぎ、第1の底部10dにの
み置かれて洗浄するためのものや、小物の被洗浄物を収
容して第2の底部10eに置かれて洗浄するためのもの
や、下部の中央が窪みこの窪みに小物の被洗浄物を収容
し、上部が両端に伸びこの上部に大型の被洗浄物を収容
して洗浄するものであってもよい。
Reference numeral 12 denotes a basket having a size to be accommodated in the washing section 10a, and an object to be washed to which water-soluble oil and non-aqueous oil (not shown) are attached is accommodated in the basket 12. The basket 12 accommodates a large object to be washed, straddles the second bottom portion 10e, and is placed only on the first bottom portion 10d for washing. Alternatively, the basket 12 accommodates a small object to be washed. The bottom portion 10e is used for cleaning, and the center of the lower portion is depressed to accommodate a small object to be cleaned in the depression, and the upper portion extends to both ends to accommodate a large object to be cleaned in the upper portion. It may be something.

【0044】14はリザーブタンクで、炭化水素系溶剤
15を収容し、後述するように炭化水素系溶剤15が容
易に送出されるために、外部と通気可能な小さな通気孔
を有し大気圧を受けている。この通気孔は屋外に連通さ
れ、洗浄装置が停止しているときには屋外とも遮蔽され
ていることが安全上望ましい。リザーブタンク14の一
部には、他の部分の炭化水素系溶剤より清浄な炭化水素
系溶剤15aを収容するリンス液タンク14aが設けら
れている。リンス液タンク14aはリザーブタンク14
の底部近傍が水平方向に伸び、その先端が高さhの段差
14bを有しており、その段差14bの外側壁面とリザ
ーブタンク14の側壁面との間に小容量の液面検出部1
4cを有している。24は蒸留器で、リザーブタンク1
4内の下部の炭化水素系溶剤15がバルブ40fを介し
て取り入れられ、加熱蒸留後冷却されて清浄な炭化水素
系溶剤15aとして再生され、リンス液タンク14aに
回収される。清浄な炭化水素系溶剤15aがリンス液タ
ンク14aの容量より多くなると、オーバフローしてリ
ザーブタンク14内に収容され、炭化水素系溶剤15が
徐々に清浄化されていく。なお、上記リンス液タンク1
4aはリザーブタンク14内に設けられているが、リザ
ーブタンク14と分割されていても良い。
Reference numeral 14 denotes a reserve tank which contains a hydrocarbon-based solvent 15 and has a small vent hole through which the hydrocarbon-based solvent 15 can be vented to the outside, as described later, to reduce the atmospheric pressure. is recieving. It is desirable from the viewpoint of safety that the ventilation hole communicates with the outside and is shielded from the outside when the cleaning device is stopped. A part of the reserve tank 14 is provided with a rinsing liquid tank 14a that stores a hydrocarbon-based solvent 15a that is cleaner than other parts of the hydrocarbon-based solvent. Rinse liquid tank 14a is reserved tank 14
Has a step 14b having a height h at its tip, and a small-capacity liquid level detector 1 between the outer wall surface of the step 14b and the side wall surface of the reserve tank 14.
4c. Reference numeral 24 denotes a distiller and reserve tank 1
The lower hydrocarbon-based solvent 15 in 4 is taken in via the valve 40f, cooled after heating and distillation, regenerated as a clean hydrocarbon-based solvent 15a, and collected in the rinsing liquid tank 14a. When the clean hydrocarbon solvent 15a becomes larger than the capacity of the rinsing liquid tank 14a, it overflows and is stored in the reserve tank 14, and the hydrocarbon solvent 15 is gradually purified. The rinsing liquid tank 1
4 a is provided in the reserve tank 14, but may be divided from the reserve tank 14.

【0045】上記炭化水素洗浄槽10の第2の底部10
eには排水管42aが設けられバルブ40aを介してリ
ザーブタンク14に接続され、炭化水素洗浄槽10にあ
る洗浄液の炭化水素系溶剤がリザーブタンク14に戻さ
れる。
The second bottom 10 of the hydrocarbon washing tank 10
A drain pipe 42a is provided at e and is connected to the reserve tank 14 via the valve 40a. The hydrocarbon solvent of the cleaning liquid in the hydrocarbon cleaning tank 10 is returned to the reserve tank 14.

【0046】上記炭化水素洗浄槽10には、蓋10bの
内側に複数のノズル22a1、22a2が設けられ、側
部10cに複数のノズル22bが設けられ、第1の底部
10dに複数のノズル22cが設けられ、第2の底部1
0eに複数のノズル22dが設けられている。16は洗
浄用ポンプで、液面検出部14cに設けられた液面レベ
ル検出器44より下側のリザーブタンク14の下部から
炭化水素系溶剤15が取り入れられ、バルブ40b、バ
ルブ40c、シャワー水供給管42bを介して、ノズル
22a1、22a2、ノズル22b、ノズル22c、ノ
ズル22dに送出され、ノズル22a1、22a2、ノ
ズル22b、ノズル22c、ノズル22dから炭化水素
系溶剤がシヤワー水として炭化水素洗浄槽10に送り込
まれる。特に、蓋10bに設けられた複数のノズル22
a1、22a2から送り出されるシャワー水は60〜1
50度の角度を有して噴出され、隣り合うノズルから送
出されたシャワー水がバスケット12までに重なり合
い、洗浄液の炭化水素系溶剤がバスケット12内の被洗
浄物に必ず当たる構造となっている。
In the hydrocarbon washing tank 10, a plurality of nozzles 22a1 and 22a2 are provided inside the lid 10b, a plurality of nozzles 22b are provided on the side 10c, and a plurality of nozzles 22c are provided on the first bottom 10d. Provided, second bottom 1
A plurality of nozzles 22d are provided at 0e. Reference numeral 16 denotes a cleaning pump which takes in the hydrocarbon-based solvent 15 from the lower part of the reserve tank 14 below the liquid level detector 44 provided in the liquid level detector 14c, and supplies a valve 40b, a valve 40c, and a shower water supply. The hydrocarbon-based solvent is sent out to the nozzles 22a1, 22a2, 22b, 22c, and 22d through the pipe 42b, and the hydrocarbon-based solvent is converted into shower water from the nozzles 22a1, 22a2, 22b, 22c, and 22d as shower water. Sent to. In particular, the plurality of nozzles 22 provided on the lid 10b
shower water sent out from a1, 22a2 is 60-1
Shower water ejected at an angle of 50 degrees and sent out from an adjacent nozzle overlaps with the basket 12 so that the hydrocarbon-based solvent of the washing liquid always hits the object to be washed in the basket 12.

【0047】40dはバルブ40cと並列に設けられた
バルブで、洗浄用ポンプ16から送出された炭化水素系
溶剤がバルブ40d、噴流水供給管42cから噴流水と
して炭化水素洗浄槽10の第2の底部10eに供給され
る。この噴流水はシャワー水よりも流量が多く高速で供
給される。第2の底部10eは洗浄部10aの上部より
も小容量のため、供給される炭化水素系溶剤が第2の底
部10eの側壁面に当たり回転して上部に盛り上がるよ
うに供給される。
Numeral 40d is a valve provided in parallel with the valve 40c. The hydrocarbon solvent sent from the cleaning pump 16 receives the valve 40d and the second water of the hydrocarbon cleaning tank 10 as the jet water from the jet water supply pipe 42c. It is supplied to the bottom 10e. The jet water has a larger flow rate than the shower water and is supplied at a high speed. Since the second bottom portion 10e has a smaller capacity than the upper portion of the cleaning section 10a, the supplied hydrocarbon-based solvent rotates against the side wall surface of the second bottom portion 10e and is supplied so as to rise to the upper portion.

【0048】18はリンス液用ポンプで、リンス液タン
ク14aの下部から清浄な炭化水素系溶剤15aが取り
入れられバルブ40eを介して送出される。そして、バ
ルブ40eを介して送出された炭化水素系溶剤は、上述
のバルブ40cを介して炭化水素洗浄槽10に清浄なシ
ャワー水として供給される。
Reference numeral 18 denotes a rinsing liquid pump. A clean hydrocarbon solvent 15a is taken in from the lower part of the rinsing liquid tank 14a and is sent out via a valve 40e. Then, the hydrocarbon-based solvent sent out via the valve 40e is supplied to the hydrocarbon washing tank 10 as clean shower water via the above-described valve 40c.

【0049】20は洗浄用ポンプ16から送り出される
炭化水素系溶剤の流量をシャワー水用と噴流水用に切換
指令する流量切換指令装置である。
Reference numeral 20 denotes a flow rate switching command device for switching the flow rate of the hydrocarbon solvent sent from the cleaning pump 16 between shower water and jet water.

【0050】42dは排水排気管で、シャワー水及び噴
流水が供給されたとき、炭化水素洗浄槽10の洗浄部1
0aの上部、例えば炭化水素系溶剤が炭化水素洗浄槽1
0に、例えば1400リットル程度溜められてバスケッ
ト12の上部が水没する前後で、炭化水素洗浄槽10か
らオーバフローする高さにあり、炭化水素系溶剤が排水
排気管42d、バルブ40gを介してリザーブタンク1
4に回収される。
Reference numeral 42d denotes a drainage exhaust pipe, which is provided with a washing section 1 of the hydrocarbon washing tank 10 when shower water and jet water are supplied.
0a, for example, the hydrocarbon solvent is in the hydrocarbon cleaning tank 1
0, for example, about 1400 liters, and before and after the upper part of the basket 12 is submerged, at a height at which it overflows from the hydrocarbon washing tank 10, and the hydrocarbon-based solvent is reserved through the drainage exhaust pipe 42d and the valve 40g. 1
Collected in 4.

【0051】28は真空ポンプで、炭化水素洗浄槽10
内部の炭化水素系溶剤のガス、エアー又は後述する窒素
ガスを上記排水排気管42d、バルブ40hを介して外
部に排気する。26は乾燥器で炭化水素洗浄槽10から
排水排気管42d、バルブ40hを介して取り入れられ
た水分を含むガスを、水分とガスを分離させ乾燥させる
ものであり、その一部は真空ポンプから外部に排気され
る。34は窒素ガス発生器で、窒素ガス発生器34から
送出された窒素ガスがバルブ40i、バルブ40hを介
して乾燥器26に取り込まれる。30はファンで乾燥器
26から送出されたガスを吸入し、加熱器32に送出さ
せる。加熱器32に送出されたガス又はエアーが加熱器
32により加熱され、バルブ40j、窒素ガス供給管4
2eを介して炭化水素洗浄槽10に供給される。
Reference numeral 28 denotes a vacuum pump,
The gas of the internal hydrocarbon solvent, air or nitrogen gas described later is exhausted to the outside via the drainage exhaust pipe 42d and the valve 40h. Reference numeral 26 denotes a dryer for separating and drying the gas containing water taken from the hydrocarbon cleaning tank 10 through the drainage exhaust pipe 42d and the valve 40h, and separating a part of the gas from the gas from the vacuum pump. Exhausted. Reference numeral 34 denotes a nitrogen gas generator, and the nitrogen gas sent from the nitrogen gas generator 34 is taken into the dryer 26 via the valves 40i and 40h. Numeral 30 denotes a fan for inhaling gas sent from the dryer 26 and sending it to the heater 32. The gas or air sent to the heater 32 is heated by the heater 32, and the valve 40j, the nitrogen gas supply pipe 4
It is supplied to the hydrocarbon cleaning tank 10 via 2e.

【0052】なお、46は液面プロテクタで、リザーブ
タンク14から炭化水素洗浄槽10に送られる炭化水素
系溶剤15の量が、排水排気管42dからリザーブタン
ク14に回収される量より多くなり、リザーブタンク1
4内の炭化水素系溶剤15が液面検出部14cに設けら
れた液面レベル検出器44より下側になると、洗浄用ポ
ンプ16及び蒸留器24の動作の停止を指令する。これ
により、洗浄用ポンプ16及び蒸留器24が無負荷運転
をすることがなく、焼損することがない。
Reference numeral 46 denotes a liquid level protector, in which the amount of the hydrocarbon solvent 15 sent from the reserve tank 14 to the hydrocarbon cleaning tank 10 is larger than the amount recovered in the reserve tank 14 from the drainage pipe 42d. Reserve tank 1
When the hydrocarbon solvent 15 in 4 is below the liquid level detector 44 provided in the liquid level detector 14c, a command is issued to stop the operation of the cleaning pump 16 and the distiller 24. Thereby, the washing pump 16 and the distiller 24 do not perform a no-load operation, and do not burn.

【0053】また、36は第2の底部10eに設けられ
た超音波振動子で、炭化水素洗浄槽10に炭化水素系溶
剤が溜まった後、超音波発振器38からの電気エネルギ
ーによって超音波振動させられて、被洗浄物の洗浄効果
を高めるために設けられている。この超音波振動子36
は図3では第2の底部10eの底に配置されているが、
第2の底部10eの側部に配置されてもよい。また、4
0kは外部のエアーを取り入れるバルブである。
Reference numeral 36 denotes an ultrasonic vibrator provided on the second bottom portion 10e. After the hydrocarbon solvent is accumulated in the hydrocarbon cleaning tank 10, the ultrasonic vibrator is ultrasonically vibrated by electric energy from an ultrasonic oscillator 38. It is provided to enhance the cleaning effect of the object to be cleaned. This ultrasonic vibrator 36
Is located at the bottom of the second bottom part 10e in FIG. 3,
It may be arranged on the side of the second bottom 10e. Also, 4
0k is a valve for taking in external air.

【0054】バルブ40a〜k、洗浄用ポンプ16、リ
ンス液用ポンプ18、真空ポンプ28、ファン30、窒
素ガス発生器34,超音波発振器38への動作指令及び
停止指令は、図示しない制御装置、例えばCPUを用い
たプログラマブルコントローラ等によって行われる。
Operation commands and stop commands to the valves 40a to k, the cleaning pump 16, the rinsing liquid pump 18, the vacuum pump 28, the fan 30, the nitrogen gas generator 34, and the ultrasonic oscillator 38 are transmitted to a control unit (not shown). For example, it is performed by a programmable controller using a CPU.

【0055】そして、炭化水素洗浄槽10、リザーブタ
ンク14、リンス液タンク14a、液面検出部14c、
洗浄用ポンプ16、リンス液用ポンプ18,蒸留器2
4、乾燥器26、真空ポンプ28、ファン30、加熱器
32、窒素ガス発生器34、超音波振動子36、液面プ
ロテクタ46及びバルブ40a〜kを含めた洗浄装置
は、掘られたピット内に収容され、全体が気密構成可能
なコテージ48により囲まれている。このコテージ48
の上部近傍にはダクト50が設けられ、コテージ内のガ
ス及びエアーがダクト50から屋外に排出される。ま
た、コテージ48には開口部が有って通常は開閉可能な
扉48bで塞がれており、図4に示す乾燥期間Eが終了
し、炭化水素洗浄槽10の蓋10bが開いてから所定時
間経過した後、この扉48bが(図3の矢印方向に移動
して)開いて、この開口部を通じて炭化水素洗浄槽10
からバスケット12が取り出される。これによって、乾
燥期間Eにおける排気工程の異常や炭化水素洗浄槽内の
残留ガスなどにより、炭化水素系溶剤の気化したガスが
コテージ内に漏れても、コテージ内のガス及びエアーが
屋外に排出されるので、炭化水素系溶剤がコテージ外
の、例えば洗浄装置を設置した建物内に漏れて床面付近
に滞留するようなことはない。なお、このコテージ48
は、ダクト50からの排気によって内部を負圧にし、コ
テージ内に漏れたガスを排出可能な程度に気密すれば良
い。
Then, the hydrocarbon cleaning tank 10, the reserve tank 14, the rinsing liquid tank 14a, the liquid level detecting section 14c,
Cleaning pump 16, Rinse liquid pump 18, Distiller 2
4. The cleaning device including the dryer 26, the vacuum pump 28, the fan 30, the heater 32, the nitrogen gas generator 34, the ultrasonic oscillator 36, the liquid level protector 46, and the valves 40a to 40k And the whole is surrounded by a cottage 48 that can be airtightly constructed. This cottage 48
A duct 50 is provided near the upper part of the cottage, and gas and air in the cottage are discharged from the duct 50 to the outside. The cottage 48 has an opening and is normally closed by a door 48b which can be opened and closed, and a predetermined period after the drying period E shown in FIG. 4 ends and the lid 10b of the hydrocarbon cleaning tank 10 is opened. After a lapse of time, the door 48b is opened (moved in the direction of the arrow in FIG. 3), and the hydrocarbon cleaning tank 10 is opened through the opening.
Is taken out of the basket 12. With this, even if the vaporized gas of the hydrocarbon-based solvent leaks into the cottage due to abnormality in the exhaust process during the drying period E or residual gas in the hydrocarbon cleaning tank, the gas and air in the cottage are discharged to the outside. Therefore, there is no possibility that the hydrocarbon-based solvent leaks out of the cottage, for example, into a building where the cleaning device is installed, and stays near the floor. This cottage 48
In this case, the inside of the cottage may be made negative pressure by exhausting air from the duct 50, and the gas leaking into the cottage may be airtight enough to be exhausted.

【0056】上記洗浄装置を図4に示すタイムチャート
を用いてその動作を説明する。図4において、期間Cは
洗浄前の準備期間を、期間Dは洗浄期間を、また、期間
Eは乾燥期間を示す。図4(a)〜(k)はそれぞれバ
ルブ40a〜kの動作を示し、また、0ラインの期間は
バルブが閉じた状態を示し、0ラインより上の期間はバ
ルブが開いた状態を示している。また、同図(l)〜
(p)はそれぞれ洗浄用ポンプ16,リンス液用ポンプ
18、真空ポンプ28、ファン30,窒素ガス発生器3
4の各装置の動作で0ラインの期間は当該装置が停止し
ている状態を示し、0ラインより上の期間は当該装置が
動作している状態を示している。
The operation of the above cleaning apparatus will be described with reference to a time chart shown in FIG. In FIG. 4, a period C indicates a preparation period before cleaning, a period D indicates a cleaning period, and a period E indicates a drying period. 4 (a) to 4 (k) show the operation of the valves 40a to 40k, respectively, and show the state where the valve is closed during the period of the 0 line, and show the state where the valve is open during the period above the 0 line. I have. In addition, FIG.
(P) shows a cleaning pump 16, a rinsing liquid pump 18, a vacuum pump 28, a fan 30, and a nitrogen gas generator 3 respectively.
In the operation of each device of No. 4, the period of line 0 indicates that the device is stopped, and the period above line 0 indicates that the device is operating.

【0057】今、準備期間Cの時刻t0より前の期間は
全てのバルブ40a〜kが閉塞されており、炭化水素洗
浄槽10の蓋10bが開かれ、コテージ48の扉48b
が開かれて被洗浄物を収容したバスケット12が洗浄部
10a内に収容された後、蓋10bおよび扉48bが閉
じられ炭化水素洗浄槽10は気密状態となる。
Now, before the time t0 of the preparation period C, all the valves 40a to 40k are closed, the lid 10b of the hydrocarbon cleaning tank 10 is opened, and the door 48b of the cottage 48 is opened.
Is opened and the basket 12 accommodating the object to be washed is accommodated in the washing section 10a, the lid 10b and the door 48b are closed, and the hydrocarbon washing tank 10 is in an airtight state.

【0058】いま、準備期間中の時刻t0で、バルブ4
0a、40f、40h、40i、40jはそれぞれ図4
(a)、(f)、(h)、(i)、(j)に示すように
開放され、バルブ40b、40c、40d、40e、4
0g、40kはそれぞれ図4(b)、(c)、(d)、
(e)、(g)、(k)に示すように閉塞を継続してい
る。もし、炭化水素洗浄槽10に炭化水素系溶剤が残っ
ているときはバルブ40aを介してリザーブタンクに回
収される。
Now, at time t0 during the preparation period, the valve 4
0a, 40f, 40h, 40i, and 40j are respectively shown in FIG.
Opened as shown in (a), (f), (h), (i), (j), valves 40b, 40c, 40d, 40e, 4
0g and 40k correspond to FIGS. 4 (b), (c), (d),
The blockage is continued as shown in (e), (g), and (k). If the hydrocarbon solvent remains in the hydrocarbon cleaning tank 10, it is collected in the reserve tank via the valve 40a.

【0059】さらに、時刻t0で真空ポンプ28,ファ
ン30、窒素ガス発生器34をそれぞれ図4(n)、
(o)、(p)に示すように動作させると、炭化水素洗
浄槽10内の炭化水素系溶剤のガス及びエアーが排水排
気管42d、バルブ40hから取り出されるとともに、
窒素ガス発生器34から送り出された窒素ガスが、バル
ブ40hを介して乾燥器26に取り込まれる。乾燥器2
6から送出されて乾燥したガス及びエアーの一部は、真
空ポンプ28を介して外部に排出される。乾燥器26か
ら送出されて乾燥したガス及びエアーの他の一部は、フ
ァン30を介して加熱器32に送り込まれて加熱され
る。加熱器32により加熱されたガス及びエアーはバル
ブ40j、窒素ガス供給管42eを介して炭化水素洗浄
槽10内に供給され、窒素ガス及びエアーが循環して炭
化水素洗浄槽10内がエアーから窒素ガスに置換されて
いく。
Further, at time t0, the vacuum pump 28, the fan 30, and the nitrogen gas generator 34 are connected to each other as shown in FIG.
When operated as shown in (o) and (p), gas and air of the hydrocarbon solvent in the hydrocarbon cleaning tank 10 are taken out from the drainage exhaust pipe 42d and the valve 40h,
The nitrogen gas sent from the nitrogen gas generator 34 is taken into the dryer 26 via the valve 40h. Dryer 2
A part of the dried gas and air sent out from 6 is discharged to the outside via a vacuum pump 28. Another part of the dried gas and air sent from the dryer 26 is sent to the heater 32 via the fan 30 to be heated. The gas and air heated by the heater 32 are supplied into the hydrocarbon cleaning tank 10 through a valve 40j and a nitrogen gas supply pipe 42e, and the nitrogen gas and air circulate, and the hydrocarbon cleaning tank 10 changes from air to nitrogen. It is replaced by gas.

【0060】そして、炭化水素洗浄槽10内の窒素ガス
が所定量になる時刻t1において真空ポンプ28,ファ
ン30、窒素ガス発生器34をそれぞれ図4(n)、
(o)、(p)に示すように停止させ、バルブ40a、
40h、40i、40jをそれぞれ図4(a)、
(h)、(i)、(j)に示すように閉塞させて、洗浄
期間Dへの待機状態となる。
Then, at time t1 when the nitrogen gas in the hydrocarbon cleaning tank 10 reaches a predetermined amount, the vacuum pump 28, the fan 30, and the nitrogen gas generator 34 are respectively turned on as shown in FIG.
(O), stop as shown in (p), valve 40a,
40h, 40i, and 40j are respectively shown in FIG.
It is closed as shown in (h), (i), and (j), and enters a standby state for the cleaning period D.

【0061】時刻t0からの準備期間Cを終えて時刻t
2になると、バルブ40b、40c、40gがそれぞれ
図4(b)、(c)、(g)に示すように開放され、洗
浄用ポンプ16は図4(l)に示すように動作を開始す
る。洗浄用ポンプ16が動作を開始すると、リザーブタ
ンク14の炭化水素系溶剤15は洗浄用ポンプ16に取
り込まれ、洗浄用ポンプ16から送出される。送出され
た炭化水素系溶剤は、バルブ40b、バルブ40c、シ
ャワー水供給管42bを介してノズル22a1、22a
2、22b、22c、22dから炭化水素洗浄槽10送
出されてバスケット12に収容されている被洗浄物を第
1のシャワー洗浄するとともに、炭化水素洗浄槽10内
に炭化水素系溶剤を溜めていく。
At the end of preparation period C from time t0, at time t
When the pressure becomes 2, the valves 40b, 40c, and 40g are opened as shown in FIGS. 4B, 4C, and 4G, respectively, and the cleaning pump 16 starts operating as shown in FIG. . When the cleaning pump 16 starts operating, the hydrocarbon solvent 15 in the reserve tank 14 is taken into the cleaning pump 16 and sent out from the cleaning pump 16. The hydrocarbon solvent that has been sent out passes through the nozzles 22a1, 22a via the valve 40b, the valve 40c, and the shower water supply pipe 42b.
The object to be cleaned which is sent out from the hydrocarbon cleaning tank 10 from the tanks 2, 22 b, 22 c, and 22 d and stored in the basket 12 is subjected to the first shower cleaning, and the hydrocarbon solvent is accumulated in the hydrocarbon cleaning tank 10. .

【0062】被洗浄物が炭化水素系溶剤に水没しても、
ノズル22a1、22a2に加えてノズル22b、22
c、22dから炭化水素系溶剤がシャワー水として供給
されるため、炭化水素洗浄槽10内に溜められた炭化水
素系溶剤は攪拌されて、被洗浄物は洗浄される。そし
て、被洗浄物に付着した水溶性油又は非水系油は炭化水
素系溶剤内に取り出され排水排気管42d、バルブ40
gを介してリザーブタンク14に回収される。第1のシ
ャワー洗浄と、シャワー水による炭化水素系溶剤の攪拌
と洗浄後の回収を行なう第2のシャワー洗浄は小物の被
洗浄物の洗浄に適する。なお、炭化水素洗浄槽10内に
溜められた炭化水素系溶剤を抜くために、バルブ40a
を開放する場合にもノズル22a1、22a2から炭化
水素系溶剤をシャワー水として送り込み、シャワー洗浄
をしてもよい。
Even if the object to be cleaned is submerged in a hydrocarbon solvent,
In addition to the nozzles 22a1, 22a2, the nozzles 22b, 22
Since the hydrocarbon-based solvent is supplied as shower water from c and 22d, the hydrocarbon-based solvent stored in the hydrocarbon cleaning tank 10 is stirred, and the object to be cleaned is cleaned. Then, the water-soluble oil or the non-aqueous oil attached to the object to be cleaned is taken out into the hydrocarbon-based solvent, and the drainage exhaust pipe 42d and the valve 40
g and is collected in the reserve tank 14. The first shower cleaning and the second shower cleaning in which a hydrocarbon-based solvent is stirred with shower water and recovered after the cleaning are suitable for cleaning small objects to be cleaned. In order to remove the hydrocarbon solvent stored in the hydrocarbon cleaning tank 10, the valve 40a
May be opened, the hydrocarbon solvent may be sent from the nozzles 22a1 and 22a2 as shower water to perform shower cleaning.

【0063】上記時刻t2からの第1のシャワー洗浄工
程で炭化水素洗浄槽10に炭化水素系溶剤が所定量溜ま
った時刻t3において、バルブ40cを図4(c)に示
すように閉塞し、バルブ40hを図4(h)に示すよう
に開放する。同時に、真空ポンプ28を図4(n)に示
すように動作させて、シャワー洗浄時に発生した炭化水
素洗浄槽10内及び炭化水素系溶剤中の泡を除く。
At time t3 when a predetermined amount of the hydrocarbon solvent has accumulated in the hydrocarbon cleaning tank 10 in the first shower cleaning step from time t2, the valve 40c is closed as shown in FIG. 40h is opened as shown in FIG. At the same time, the vacuum pump 28 is operated as shown in FIG. 4 (n) to remove bubbles generated in the hydrocarbon cleaning tank 10 and in the hydrocarbon solvent during the shower cleaning.

【0064】なお、泡を除いた後、超音波振動子36を
動作させると、炭化水素系溶剤の洗浄と超音波のキャビ
テーションにより洗浄効果が高められる。
When the ultrasonic vibrator 36 is operated after removing the bubbles, the cleaning effect is enhanced by the cleaning of the hydrocarbon solvent and the cavitation of the ultrasonic wave.

【0065】上記超音波照射による洗浄後、時刻t4に
おいてバルブ40dを図4(d)に示すように開放し
て、さらに流量切換指令装置20により洗浄用ポンプ1
6から送出される炭化水素系溶剤を大量且つ高速にする
と、炭化水素系溶剤は洗浄用ポンプ16、バルブ40
b、バルブ40d、噴流水供給管42cを介して炭化水
素洗浄槽10に送り込まれる。炭化水素洗浄槽10に送
り込まれた炭化水素系溶剤は、小容量の第2の底部10
eから第1の底部10dまで盛り上がり噴流水となって
バスケット12内に収容されている大型の被洗浄物を洗
浄する。洗浄後の炭化水素系溶剤は排水排気管42dか
らオーバフローし、バルブ40gを介してリザーブタン
ク14に回収される。そして、炭化水素系溶剤は洗浄用
ポンプ16、バルブ40b、バルブ40d、噴流水供給
管42c、炭化水素洗浄槽10、排水排気管42d、バ
ルブ40g、リザーブタンク14の経路を循環し、大型
の被洗浄物を炭化水素系溶剤により循環洗浄する。な
お、この噴流水により洗浄する場合、リザーブタンク1
4内のエアーが噴流水とともに炭化水素洗浄槽10に送
り込まれるため、バルブ40h、40i、40jを図4
(h)、(i)、(j)に示すように開放し、さらに真
空ポンプ28、ファン30、窒素ガス発生器34を図4
(n)、(o)、(p)に示すように動作させて、炭化
水素洗浄槽10内を排気と窒素ガスに置換することが、
安全上望ましい。
After the cleaning by the ultrasonic irradiation, at time t4, the valve 40d is opened as shown in FIG.
When a large amount and high speed of the hydrocarbon-based solvent sent out from the pump 6 are used, the hydrocarbon-based solvent is supplied to the cleaning pump 16 and the valve 40.
b, the valve 40d and the jet water supply pipe 42c are fed into the hydrocarbon cleaning tank 10. The hydrocarbon-based solvent fed into the hydrocarbon cleaning tank 10 contains a small volume of the second bottom 10.
e, and rises from the first bottom portion 10d to become jet water to wash a large object to be washed accommodated in the basket 12. The washed hydrocarbon-based solvent overflows from the drainage exhaust pipe 42d and is collected in the reserve tank 14 via the valve 40g. Then, the hydrocarbon solvent circulates through the paths of the cleaning pump 16, the valve 40b, the valve 40d, the jet water supply pipe 42c, the hydrocarbon cleaning tank 10, the drainage exhaust pipe 42d, the valve 40g, and the reserve tank 14, thereby forming a large-sized tank. The washing is circulated and washed with a hydrocarbon solvent. When washing with the jet water, the reserve tank 1
4 is sent to the hydrocarbon washing tank 10 together with the jet water, the valves 40h, 40i, and 40j are set in FIG.
(H), (i) and (j) are opened, and the vacuum pump 28, the fan 30, and the nitrogen gas generator 34 are connected as shown in FIG.
By operating as shown in (n), (o) and (p), the inside of the hydrocarbon cleaning tank 10 is replaced with exhaust gas and nitrogen gas.
Desirable for safety.

【0066】時刻t4からの噴流水循環工程による噴流
洗浄終えた時刻t5になると、バルブ40h、40i、
40jを図4(h)、(i)、(j)に示すように閉塞
し、さらに洗浄用ポンプ16、真空ポンプ28、ファン
30、窒素ガス発生器34を図4(l)、(n)、
(o)、(p)に示すように動作を停止させるととも
に、噴流洗浄時に閉塞していたバルブ40aを図4
(a)に示すように開放し、さらに、バルブ40b及び
バルブ40dを図4(b)及び(d)に示すように閉塞
させる。これにより炭化水素洗浄槽10の炭化水素系溶
剤は開放されたバルブ40aを介してリザーブタンク1
4に回収される。
At time t5 when the jet cleaning by the jet water circulation process from time t4 is completed, the valves 40h, 40i,
40j is closed as shown in FIGS. 4 (h), (i) and (j), and the cleaning pump 16, the vacuum pump 28, the fan 30, and the nitrogen gas generator 34 are closed as shown in FIGS. 4 (l) and 4 (n). ,
As shown in FIGS. 4 (o) and 4 (p), the operation is stopped, and the valve 40a closed at the time of jet cleaning is moved to FIG.
4A, the valve 40b and the valve 40d are closed as shown in FIGS. 4B and 4D. As a result, the hydrocarbon solvent in the hydrocarbon cleaning tank 10 is supplied to the reserve tank 1 through the opened valve 40a.
Collected in 4.

【0067】時刻t5からの第1の回収工程を終えて時
刻t6になると、バルブ40c、40eが図4(c)、
(e)に示すように開放され、リンス液用ポンプ18が
図4(m)に示すように動作を開始する。リンス液用ポ
ンプ18が動作を開始すると、リンス液タンク14aの
下部から清浄なリンス用の炭化水素系溶剤15aが取り
込まれ送出される。リンス液用ポンプ18により送出さ
れた清浄な炭化水素系溶剤は、バルブ40e、バルブ4
0c、シャワー水供給管42bを介してノズル22a
1、22a2、22b、22c、22dから炭化水素洗
浄槽10送出されてバスケット12に収容されている被
洗浄物をシャワーリンスする。リンス後の炭化水素系溶
剤はバルブ40aを介してリザーブタンク14に回収さ
れる。
At the time t6 after the first recovery step from the time t5, the valves 40c and 40e are switched to the state shown in FIG.
It is opened as shown in (e), and the rinsing liquid pump 18 starts operating as shown in FIG. 4 (m). When the rinsing liquid pump 18 starts operating, a clean hydrocarbon solvent 15a for rinsing is taken in from the lower part of the rinsing liquid tank 14a and sent out. The clean hydrocarbon-based solvent delivered by the rinsing liquid pump 18 is supplied to the valve 40e and the valve 4e.
0c, the nozzle 22a through the shower water supply pipe 42b
The objects to be cleaned which are sent out of the hydrocarbon cleaning tank 10 from the baskets 12, 22 a 2, 22 b, 22 c and 22 d and stored in the basket 12 are shower-rinsed. The hydrocarbon solvent after rinsing is collected in the reserve tank 14 via the valve 40a.

【0068】時刻t6からのリンス工程を終えて時刻t
7になるとバルブ40c、バルブ40eがそれぞれ図4
(c)、(e)に示すように閉塞されとともに、リンス
液用ポンプ18が図4(m)に示すように動作を停止す
る。これにより、炭化水素洗浄槽10に残ったリンス後
の炭化水素系溶剤は第2の底部10eから排水管42
a、バルブ40aを介してリザーブタンク14に回収さ
れて時刻t2から始まった洗浄期間Dは終了する。
After the rinsing step from time t6 is completed, time t
7, the valve 40c and the valve 40e are respectively shown in FIG.
As shown in FIGS. 4C and 4E, the rinsing liquid pump 18 stops operating as shown in FIG. As a result, the hydrocarbon solvent after rinsing remaining in the hydrocarbon cleaning tank 10 is discharged from the second bottom portion 10e to the drain pipe 42.
a, the cleaning period D collected from the reserve tank 14 via the valve 40a and started at time t2 ends.

【0069】時刻t7からの第2の回収工程を終えて時
刻t8になると、バルブ40a、バルブ40gはそれぞ
れ図4(a)、(g)に示すように閉塞され、バルブ4
0h、バルブ40i、バルブ40jがそれぞれ図4
(h)、(i)、(j)に示すように開放される。同時
に、真空ポンプ28,ファン30、窒素ガス発生器34
をそれぞれ図4(n)、(o)、(p)に示すように動
作させると、炭化水素洗浄槽10内の炭化水素系溶剤の
ガスが排水排気管42d、バルブ40hから取り出され
乾燥器26に取り込まれるとともに、窒素ガス発生器3
4から送り出された窒素ガスが、バルブ40i、40h
から乾燥器26に取り込まれる。
At time t8 after the completion of the second recovery step from time t7, the valves 40a and 40g are closed as shown in FIGS.
0h, valve 40i, and valve 40j are respectively shown in FIG.
It is opened as shown in (h), (i) and (j). At the same time, vacuum pump 28, fan 30, nitrogen gas generator 34
Are operated as shown in FIGS. 4 (n), (o) and (p), respectively, the gas of the hydrocarbon solvent in the hydrocarbon washing tank 10 is taken out from the drainage exhaust pipe 42d and the valve 40h and is dried. And the nitrogen gas generator 3
4, the nitrogen gas sent out from the valves 40i, 40h
From the dryer 26.

【0070】乾燥器26から送出された乾燥したガスの
一部は、真空ポンプ28により外部に排出される。乾燥
器26から送出された乾燥したガスの他の一部は、ファ
ン30を介して加熱器32に送り込まれて加熱される。
加熱器32により加熱されたガスはバルブ40j、窒素
ガス供給管42eを介して炭化水素洗浄槽10内に供給
され、窒素ガスが循環して炭化水素洗浄槽10内が炭化
水素系溶剤のガスから窒素ガスに置換されていく。この
窒素ガスは水分が乾燥器26により分離されているた
め、炭化水素洗浄槽10内の水分も減少し、被洗浄物も
乾燥されていく。
A part of the dried gas sent from the dryer 26 is discharged to the outside by the vacuum pump 28. Another part of the dried gas sent from the dryer 26 is sent to the heater 32 via the fan 30 and is heated.
The gas heated by the heater 32 is supplied into the hydrocarbon cleaning tank 10 via the valve 40j and the nitrogen gas supply pipe 42e, and the nitrogen gas is circulated so that the inside of the hydrocarbon cleaning tank 10 is separated from the hydrocarbon solvent gas. It is replaced by nitrogen gas. Since the moisture of the nitrogen gas is separated by the dryer 26, the moisture in the hydrocarbon cleaning tank 10 also decreases, and the object to be cleaned is also dried.

【0071】時刻t9になるとバルブ40kを図4
(k)に示すように開放し、窒素ガスとともに外部のエ
アーが乾燥器28、ファン30、加熱器32、バルブ4
0j、窒素ガス供給管42eを介して炭化水素洗浄槽1
0内に送り込まれる。加熱器32により加熱された窒素
ガスとエアーの混合ガスにより被洗浄物が加熱乾燥され
る。
At time t9, the valve 40k is set to the position shown in FIG.
As shown in (k), the air is opened together with the nitrogen gas and the external air is supplied to the dryer 28, the fan 30, the heater 32, and the valve 4.
0j, hydrocarbon cleaning tank 1 via nitrogen gas supply pipe 42e
It is sent within 0. The object to be cleaned is heated and dried by the mixed gas of the nitrogen gas and the air heated by the heater 32.

【0072】時刻t10になるとバルブ40i、40j
をそれぞれ図4(i)、(j)に示すように閉塞し、窒
素ガス発生器34を図4(p)に示すようにその動作を
停止させる。炭化水素洗浄槽10内には加熱されたエア
ーが送り込まれて、被洗浄物が加熱乾燥される。
At time t10, the valves 40i, 40j
Are closed as shown in FIGS. 4 (i) and 4 (j), respectively, and the operation of the nitrogen gas generator 34 is stopped as shown in FIG. 4 (p). Heated air is sent into the hydrocarbon cleaning tank 10, and the object to be cleaned is heated and dried.

【0073】時刻t8からの第1の置換乾燥工程を終え
て時刻t11になるとバルブ40kを図4(k)に示す
ように閉塞させ、ファン30を図4(o)に示すように
停止させる。これにより、炭化水素洗浄槽10内のエア
ーは排水排気管42d、バルブ40h、乾燥器26、真
空ポンプ28を介して全て外部に排出され、炭化水素洗
浄槽10内は減圧していく。減圧が大気圧より更に進む
と炭化水素洗浄槽10内の水分は気化し、真空ポンプ2
8を介して全て外部に排出されて、被洗浄物は乾燥され
減圧乾燥による減圧乾燥工程が進む。
At the time t11 after the completion of the first replacement drying step from the time t8, the valve 40k is closed as shown in FIG. 4 (k), and the fan 30 is stopped as shown in FIG. 4 (o). Thereby, all the air in the hydrocarbon cleaning tank 10 is discharged to the outside via the drainage exhaust pipe 42d, the valve 40h, the dryer 26, and the vacuum pump 28, and the pressure in the hydrocarbon cleaning tank 10 is reduced. When the decompression proceeds further than the atmospheric pressure, the water in the hydrocarbon cleaning tank 10 evaporates, and the vacuum pump 2
The material to be cleaned is all discharged to the outside via the drying unit 8, and the object to be washed is dried, and a reduced pressure drying step by reduced pressure drying proceeds.

【0074】時刻t11からの減圧乾燥工程を終えたと
き、炭化水素洗浄槽10内は0度程度の低温になってお
り、この状態で減圧から復圧した場合、炭化水素洗浄槽
10の蓋10bに水滴が発生することがある。このた
め、時刻t12においてバルブ40j、40kをそれぞ
れ図4(j)、(k)に示すように開放させ、同時に、
ファン30を図4(o)に示すように動作させると、炭
化水素洗浄槽10外のエアーがファン30、加熱器3
2、バルブ40j、窒素ガス供給管42eを介して炭化
水素洗浄槽10に供給される。加熱器32により加熱さ
れたエアーにより炭化水素洗浄槽10内の水分が除かれ
ていく。
At the end of the reduced pressure drying step from time t11, the inside of the hydrocarbon cleaning tank 10 is at a low temperature of about 0 ° C. When the pressure is restored from the reduced pressure in this state, the lid 10b of the hydrocarbon cleaning tank 10 In some cases, water droplets may be generated. Therefore, at time t12, the valves 40j and 40k are opened as shown in FIGS. 4 (j) and 4 (k), respectively.
When the fan 30 is operated as shown in FIG. 4 (o), the air outside the hydrocarbon cleaning tank 10 is
2. It is supplied to the hydrocarbon cleaning tank 10 via a valve 40j and a nitrogen gas supply pipe 42e. The water in the hydrocarbon cleaning tank 10 is removed by the air heated by the heater 32.

【0075】そして、時刻t13になると、バルブ40
kを図4(k)に示すように閉塞させ、バルブ40iを
図4(i)に示すように開放させる。同時に、窒素ガス
発生器34を図4(p)に示すように動作させると、炭
化水素洗浄槽10内に窒素ガス発生器34からの窒素ガ
スが取り込まれる。この窒素ガスは乾燥器26により加
熱され炭化水素洗浄槽10を加熱し水分をさらに取り除
く。
At time t13, the valve 40
k is closed as shown in FIG. 4 (k), and the valve 40i is opened as shown in FIG. 4 (i). At the same time, when the nitrogen gas generator 34 is operated as shown in FIG. 4 (p), the nitrogen gas from the nitrogen gas generator 34 is taken into the hydrocarbon cleaning tank 10. The nitrogen gas is heated by the dryer 26 to heat the hydrocarbon cleaning tank 10 to further remove water.

【0076】時刻t14になると、バルブ40kを図4
(k)に示すように開放させる。これにより窒素ガスと
ともに外部のエアーが再度乾燥器28、ファン30、加
熱器32、バルブ40j、窒素ガス供給管42eを介し
て炭化水素洗浄槽10内に送り込まれる。加熱器32に
より加熱された窒素ガスとエアーの混合ガスにより炭化
水素洗浄槽10が加熱されて水分をさらに取り除かれ
る。
At time t14, the valve 40k is set to the position shown in FIG.
Release as shown in (k). Thereby, the external air is again sent into the hydrocarbon cleaning tank 10 through the dryer 28, the fan 30, the heater 32, the valve 40j, and the nitrogen gas supply pipe 42e together with the nitrogen gas. The hydrocarbon cleaning tank 10 is heated by the mixed gas of nitrogen gas and air heated by the heater 32 to further remove moisture.

【0077】時刻t15になるとバルブ40i、40j
をそれぞれ図4(i)、(j)に示すように閉塞し、窒
素ガス発生器34を図4(p)に示すようにその動作を
停止させる。これにより炭化水素洗浄槽10内には加熱
されたエアーのみが送り込まれて、炭化水素洗浄槽10
が加熱され水分が除かれる。このとき、炭化水素洗浄槽
10の蓋10bを少し開けて、炭化水素洗浄槽10外の
を炭化水素洗浄槽10内に入れて、炭化水素洗浄槽10
内を復圧していく。
At time t15, the valves 40i, 40j
Are closed as shown in FIGS. 4 (i) and 4 (j), respectively, and the operation of the nitrogen gas generator 34 is stopped as shown in FIG. 4 (p). As a result, only heated air is sent into the hydrocarbon cleaning tank 10 and the hydrocarbon cleaning tank 10 is heated.
Is heated to remove moisture. At this time, the lid 10b of the hydrocarbon cleaning tank 10 is slightly opened, and the outside of the hydrocarbon cleaning tank 10 is put into the hydrocarbon cleaning tank 10, and the hydrocarbon cleaning tank 10 is opened.
The pressure inside is restored.

【0078】時刻t16になり炭化水素洗浄槽10内が
完全に復圧するとバルブ40h、40kを図4(h)、
(k)に示すように閉塞し、真空ポンプ28、ファン3
0を図4(n)、(o)に示すように動作を停止させ、
時刻t8から始まった乾燥期間Eは終了する。同時に、
蒸留器24を停止させる。そして、炭化水素洗浄槽10
の蓋10bが開かれ、さらに所定時間経過後に扉48b
が開いて、被洗浄物を収容したバスケット12が取り出
される。
At time t16, when the pressure inside the hydrocarbon cleaning tank 10 is completely restored, the valves 40h and 40k are switched to the state shown in FIG.
As shown in (k), the vacuum pump 28 and the fan 3 are closed.
0 is stopped as shown in FIGS. 4 (n) and 4 (o),
The drying period E started from time t8 ends. at the same time,
The still 24 is stopped. And the hydrocarbon washing tank 10
Is opened, and after a predetermined time has passed, the door 48b is opened.
Opens, and the basket 12 containing the object to be cleaned is taken out.

【0079】上記洗浄装置では、従来炭化水素系溶剤を
含む炭化水素洗浄槽として2槽又は3槽のものを使用し
ていたが、これを1槽の炭化水素洗浄槽で、洗浄と乾燥
を行うことができ、可燃性の炭化水素系溶剤を少なくす
ることができる。これにより、洗浄装置を大型にするこ
とができ、それに伴い大型の被洗浄物を洗浄することが
できる。また、洗浄された被洗浄物が清浄な炭化水素系
溶剤によりリンスされ、リンス後の炭化水素系溶剤が回
収された後、炭化水素洗浄槽内の水分を含んだ炭化水素
系溶剤のガスが窒素ガスに置換されるので水分が除かれ
乾燥を早めることができるとともに、可燃の危険性を除
くことができる。また、炭化水素系溶剤のガスが窒素ガ
スに置換した後、さらに、炭化水素洗浄槽10内をエア
ーに置換することにより、洗浄後の乾燥工程に要する窒
素ガスの量を低減することができる。さらに、真空ポン
プで炭化水素洗浄槽を減圧することにより、炭化水素洗
浄槽内の水分が気化し外部に排出されるので、短時間で
乾燥することができる。
In the above-described cleaning apparatus, two or three hydrocarbon cleaning tanks containing a hydrocarbon-based solvent have conventionally been used, but the cleaning and drying are performed in a single hydrocarbon cleaning tank. Flammable hydrocarbon solvents can be reduced. Thus, the size of the cleaning device can be increased, and accordingly, a large object to be cleaned can be cleaned. Further, the cleaned object to be cleaned is rinsed with a clean hydrocarbon-based solvent, and after the rinsed hydrocarbon-based solvent is recovered, the hydrocarbon-based solvent gas containing water in the hydrocarbon cleaning tank is flushed with nitrogen. Since it is replaced by gas, moisture can be removed and drying can be accelerated, and the danger of flammability can be eliminated. Further, after the hydrocarbon solvent gas is replaced with nitrogen gas, the inside of the hydrocarbon cleaning tank 10 is further replaced with air, whereby the amount of nitrogen gas required for the drying step after cleaning can be reduced. Furthermore, by decompressing the hydrocarbon cleaning tank with a vacuum pump, moisture in the hydrocarbon cleaning tank is vaporized and discharged to the outside, so that drying can be performed in a short time.

【0080】上記実施の形態ではシャワー洗浄後に超音
波照射による洗浄し、超音波洗浄の後に、噴流水により
洗浄する場合について説明したが、被洗浄物が小物の場
合、バルブ40aを閉塞することなくシャワー洗浄を行
い、洗浄を終えることもでき、また、シャワー洗浄後に
超音波照射して超音波洗浄後に全洗浄を終える場合も選
択できる。さらに、被洗浄物が大型の場合、超音波洗浄
を除きシャワー洗浄後に噴流水洗浄する洗浄の場合も選
択できる。
In the above-described embodiment, the case of cleaning by ultrasonic irradiation after shower cleaning, and cleaning by jet water after ultrasonic cleaning has been described. However, when the object to be cleaned is a small object, the valve 40a is not closed. It is also possible to perform shower cleaning and finish the cleaning, or to select a case where ultrasonic cleaning is performed after the shower cleaning and the entire cleaning is completed after the ultrasonic cleaning. Further, when the object to be cleaned is large, a cleaning method of jet water cleaning after shower cleaning except ultrasonic cleaning can be selected.

【0081】[0081]

【発明の効果】この発明によれば,以下に記載するよう
な効果を奏する。
According to the present invention, the following effects can be obtained.

【0082】第1から第6、および第14、15の発明
によれば、従来の炭化水素系溶剤の洗浄槽を構成する水
溶性成分除去槽が不要となり、更には炭化水素系溶剤に
よる水切り槽が不要になるので、洗浄工程が短縮される
と同時に、炭化水素系溶剤の内含槽も2槽から1槽にな
るため、洗浄装置を大型化でき、より大きな被洗浄物や
大量の小物の洗浄を行なうことが可能となる。
According to the first to sixth and fourteenth and fifteenth inventions, the conventional water-soluble component removing tank constituting the washing tank for the hydrocarbon solvent becomes unnecessary, and further, the drainage tank using the hydrocarbon solvent is used. Since the cleaning process is shortened, the cleaning process is shortened, and at the same time, the number of the tanks containing the hydrocarbon solvent is reduced from two to one. Cleaning can be performed.

【0083】また、第7の発明によれば、従来の炭化水
素系溶剤による脱脂洗浄処理後のめっき処理と比べて、
外観に優れ、耐蝕性、密着性に優れためっき膜や塗膜を
得る事が出来る。また、このめっきの前処理として酸洗
いを行う酸洗い槽を、脱脂洗浄処理とめっき処理の両方
に兼用することによって、洗浄装置およびめっき処理の
ための設備が簡潔になる。
Further, according to the seventh invention, compared with the conventional plating treatment after degreasing and cleaning treatment with a hydrocarbon solvent,
It is possible to obtain plating films and coatings which are excellent in appearance, corrosion resistance and adhesion. Further, by using the pickling tank for pickling as a pre-treatment of the plating for both the degreasing cleaning and the plating, the cleaning device and the equipment for the plating are simplified.

【0084】また、第8の発明によれば、被洗浄物を収
容し気密形成された炭化水素洗浄槽に炭化水素系溶剤を
シャワー水として供給し、被洗浄物を洗浄させるととも
に、炭化水素系溶剤を炭化水素洗浄槽に溜め、この後シ
ャワー水を継続して供給させて溜められた炭化水素系溶
剤を攪拌させることにより、小物又は大型の被洗浄物に
付着した水溶性油及び非水系油等を高速かつ確実に除去
させることができる。また、洗浄を行う炭化水素洗浄槽
は1槽で行われるので、可燃性の炭化水素系溶剤を少な
くすることができる。
According to the eighth aspect of the present invention, a hydrocarbon-based solvent is supplied as shower water to an air-tightly formed hydrocarbon cleaning tank that accommodates an object to be cleaned, and cleans the object to be cleaned and the hydrocarbon-based solvent. The solvent is stored in the hydrocarbon cleaning tank, and then the shower water is continuously supplied to stir the stored hydrocarbon-based solvent, so that the water-soluble oil and the non-aqueous oil adhered to the small or large object to be cleaned. Etc. can be removed quickly and reliably. In addition, since the washing is performed in one hydrocarbon washing tank, the amount of flammable hydrocarbon solvents can be reduced.

【0085】また、第9の発明によれば、被洗浄物を収
容し気密形成された炭化水素洗浄槽に炭化水素系溶剤を
シャワー水として供給し、被洗浄物を洗浄させるととも
に、炭化水素系溶剤を炭化水素洗浄槽に溜めることによ
り、この後大量且つ高速に上記炭化水素系溶剤を供給す
ると、炭化水素洗浄槽内に噴流水が発生し、特に大型の
被洗浄物に付着した水溶性油及び非水系油等が高速かつ
確実に除去されることができる。また、洗浄を行う炭化
水素洗浄槽は1槽で行われるので、可燃性の炭化水素系
溶剤を少なくすることができる。
According to the ninth aspect of the present invention, the hydrocarbon-based solvent is supplied as shower water to the hydrocarbon-cleaning tank containing the object to be cleaned and formed airtight, thereby cleaning the object to be cleaned and the hydrocarbon-based solvent. By storing the solvent in the hydrocarbon cleaning tank, and then supplying the above-mentioned hydrocarbon-based solvent in a large amount and at a high speed, a jet of water is generated in the hydrocarbon cleaning tank, and especially the water-soluble oil adhered to a large cleaning object. And non-aqueous oil and the like can be rapidly and reliably removed. In addition, since the washing is performed in one hydrocarbon washing tank, the amount of flammable hydrocarbon solvents can be reduced.

【0086】また、第10の発明によれば、被洗浄物を
収容し気密形成された炭化水素洗浄槽に炭化水素系溶剤
をシャワー水として供給すると、小容量の炭化水素系溶
剤で被洗浄物に付着した水溶性油及び非水系油等が確実
に除去され、また、洗浄された被洗浄物が清浄な炭化水
素系溶剤によりリンスされ、そのリンス後の炭化水素系
溶剤が回収された後、炭化水素洗浄槽内の水分を含んだ
炭化水素系溶剤のガスが加熱された窒素ガスに置換され
て、水分が除かれ乾燥を早めることができるとともに、
可燃の危険性を除くことができる。さらに、炭化水素洗
浄槽を減圧することにより、炭化水素洗浄槽内の水分が
気化し外部に排出されるので、短時間で乾燥することが
できる。
According to the tenth aspect of the present invention, when the hydrocarbon-based solvent is supplied as shower water to the air-tightly formed hydrocarbon cleaning tank that accommodates the object to be cleaned, the object to be cleaned is reduced with a small volume of the hydrocarbon-based solvent. After the water-soluble oil and non-aqueous oil adhered to the surface are securely removed, the washed object to be washed is rinsed with a clean hydrocarbon solvent, and after the rinsed hydrocarbon solvent is recovered, The gas of the hydrocarbon-based solvent containing water in the hydrocarbon cleaning tank is replaced by heated nitrogen gas, and the water is removed and drying can be accelerated.
The risk of flammability can be eliminated. Furthermore, since the water in the hydrocarbon cleaning tank is vaporized and discharged to the outside by reducing the pressure in the hydrocarbon cleaning tank, drying can be performed in a short time.

【0087】また、第11の発明によれば、被洗浄物を
収容し気密形成された炭化水素洗浄槽に炭化水素系溶剤
をシャワー水として供給すると、被洗浄物が洗浄される
とともに、炭化水素系溶剤が炭化水素洗浄槽に溜めら
れ、この後大量且つ高速に上記炭化水素系溶剤を供給す
ると、炭化水素洗浄槽内に噴流水が発生し、大型の被洗
浄物に付着した水溶性油及び非水系油等を高速かつ確実
に除去する。また、洗浄を行う炭化水素洗浄槽は1槽で
行われるので、可燃性の炭化水素系溶剤を少なくするこ
とができる。そして、洗浄された被洗浄物が清浄な炭化
水素系溶剤によりリンスされ、そのリンス後の炭化水素
系溶剤が回収された後、炭化水素洗浄槽内の水分を含ん
だ炭化水素系溶剤のガスが加熱した窒素ガスに置換され
て、水分が除かれ乾燥を早めることができるとともに、
可燃の危険性を除くことができる。さらに、炭化水素洗
浄槽を減圧することにより、炭化水素洗浄槽内の水分が
気化し外部に排出されるので、短時間で乾燥することが
できる。
According to the eleventh aspect of the present invention, when the hydrocarbon-based solvent is supplied as shower water to the hydrocarbon-cleaning tank containing the article to be cleaned and formed airtight, the article to be cleaned is washed and the hydrocarbon is added. When the system solvent is accumulated in the hydrocarbon cleaning tank, and then the large amount and high speed supply of the hydrocarbon solvent is performed, jet water is generated in the hydrocarbon cleaning tank, and the water-soluble oil and High speed and reliable removal of non-aqueous oil. In addition, since the washing is performed in one hydrocarbon washing tank, the amount of flammable hydrocarbon solvents can be reduced. Then, the cleaned object to be cleaned is rinsed with a clean hydrocarbon-based solvent, and after the rinsed hydrocarbon-based solvent is recovered, the gas of the hydrocarbon-based solvent containing water in the hydrocarbon cleaning tank is removed. Replaced by heated nitrogen gas, moisture is removed and drying can be accelerated,
The risk of flammability can be eliminated. Furthermore, since the water in the hydrocarbon cleaning tank is vaporized and discharged to the outside by reducing the pressure in the hydrocarbon cleaning tank, drying can be performed in a short time.

【0088】また、第12の発明によれば、供給する窒
素ガスにより安全性を確保するとともに、その窒素ガス
も最小限の量で乾燥を行うことができる。
According to the twelfth aspect, the safety can be ensured by the supplied nitrogen gas, and the nitrogen gas can be dried with a minimum amount.

【0089】また、第13の発明によれば、減圧乾燥時
に冷却されてできる水滴を加熱された窒素ガスにより安
全に乾燥させるとともに、その窒素ガスも最小限の量で
乾燥を行うことができる。さらに、炭化水素洗浄槽を確
実に復圧させることができる。
Further, according to the thirteenth aspect, it is possible to safely dry water droplets formed by cooling at the time of drying under reduced pressure with heated nitrogen gas, and to dry the nitrogen gas with a minimum amount. Further, the pressure of the hydrocarbon cleaning tank can be reliably restored.

【0090】また、第16の発明によれば、被洗浄物を
収容し気密形成された炭化水素洗浄槽内の上部から炭化
水素系溶剤を噴出させ、その噴流を被洗浄物に当てて洗
浄を行うことにより、被洗浄物に付着していた水溶性油
及び非水系油等を、炭化水素洗浄槽に溜まった炭化水素
系溶剤とともに確実に排水することができる。
Further, according to the sixteenth aspect, the hydrocarbon-based solvent is ejected from the upper portion of the airtightly formed hydrocarbon washing tank containing the article to be washed, and the jet is applied to the article to be washed. By doing so, the water-soluble oil, non-aqueous oil and the like adhering to the object to be cleaned can be reliably drained together with the hydrocarbon-based solvent accumulated in the hydrocarbon cleaning tank.

【0091】また、第17、18の発明によれば、気密
形成された1槽の炭化水素洗浄槽が気密構成可能なコテ
ージに収容されているため、もし炭化水素洗浄槽から炭
化水素系溶剤が漏れてもコテージ内に収容され、屋外に
排出されるので、安全性が十分確保されるとともに衛生
上良い。
According to the seventeenth and eighteenth aspects of the present invention, since the one airtightly formed hydrocarbon cleaning tank is housed in a cottage that can be airtightly constructed, the hydrocarbon solvent is removed from the hydrocarbon cleaning tank. Even if it leaks, it is housed in the cottage and discharged outside, ensuring sufficient safety and good hygiene.

【0092】また、第19の発明によれば、窒素ガスを
最小限の量で乾燥を行うことができ、炭化水素洗浄槽を
確実に復圧させることができる。
Further, according to the nineteenth aspect, the nitrogen gas can be dried with a minimum amount, and the pressure in the hydrocarbon cleaning tank can be reliably restored.

【0093】また、第20の発明によれば、被洗浄物を
収容し気密形成された1槽の炭化水素洗浄槽で、洗浄用
ポンプにより供給される炭化水素系溶剤により被洗浄物
が洗浄され、リンス液用ポンプにより供給される清浄な
炭化水素系溶剤により被洗浄物がリンスされる。さら
に、真空ポンプと炭化水素洗浄槽に窒素ガスを供給し置
換する置換乾燥系とにより洗浄後の被洗浄物を乾燥させ
ることができる。このため、可燃性の炭化水素系溶剤を
少なくすることができる。また、洗浄された被洗浄物を
リンスした清浄な炭化水素系溶剤が回収された後、炭化
水素洗浄槽内の水分を含んだ炭化水素系溶剤のガスを窒
素ガスに置換されて、水分が除かれ乾燥を早めることが
できるとともに、可燃の危険性を除くことができる。さ
らに、真空ポンプで炭化水素洗浄槽を減圧することによ
り、炭化水素洗浄槽内の水分が気化し外部に排出される
ので、短時間で乾燥することができる。
According to the twentieth aspect, the object to be cleaned is cleaned by the hydrocarbon-based solvent supplied by the cleaning pump in the one air-tight hydrocarbon cleaning tank containing the object to be cleaned. The object to be cleaned is rinsed by the clean hydrocarbon solvent supplied by the rinsing liquid pump. Furthermore, the object to be cleaned after the cleaning can be dried by the vacuum pump and the replacement drying system that supplies and replaces the nitrogen gas to the hydrocarbon cleaning tank. Therefore, the amount of flammable hydrocarbon solvents can be reduced. After the clean hydrocarbon-based solvent obtained by rinsing the cleaned object to be cleaned is recovered, the gas of the hydrocarbon-based solvent containing water in the hydrocarbon cleaning tank is replaced with nitrogen gas to remove water. He can dry faster and eliminate the danger of flammability. Furthermore, by decompressing the hydrocarbon cleaning tank with a vacuum pump, moisture in the hydrocarbon cleaning tank is vaporized and discharged to the outside, so that drying can be performed in a short time.

【0094】また、第21の発明によれば、洗浄後の炭
化水素洗浄槽内の水分を加熱して水分の気化を促進する
ことができ、短時間で乾燥することができる。
Further, according to the twenty-first aspect, the water in the hydrocarbon cleaning tank after cleaning can be heated to promote the vaporization of the water, and can be dried in a short time.

【0095】また、第22の発明によれば、シャワー水
供給機構と噴流水供給機構とを切換することにより小物
の被洗浄物を大量に洗浄することができ、また大型の被
洗浄物をも洗浄することができる。
Further, according to the twenty-second aspect, by switching between the shower water supply mechanism and the jet water supply mechanism, a large amount of small objects to be cleaned can be cleaned, and a large object to be cleaned can be cleaned. Can be washed.

【0096】また、第23の発明によれば、バスケット
には小物の被洗浄物を大量に収容でき、さらに大型の被
洗浄物も収容できる。また、小物又は大型の被洗浄物を
選択して洗浄と乾燥ができ、更に小物の被洗浄物と大型
の被洗浄物とを同時に洗浄と乾燥を行うことができる。
According to the twenty-third aspect, the basket can store a large amount of small objects to be cleaned, and can also store a large object to be cleaned. In addition, cleaning and drying can be performed by selecting a small object or a large object to be cleaned, and the small object to be cleaned and the large object to be cleaned can be simultaneously cleaned and dried.

【0097】さらにまた、第24の発明によれば、リザ
ーブタンクから炭化水素洗浄槽10に送られる炭化水素
系溶剤の量が多くなり、リザーブタンク内の炭化水素系
溶剤が低下しても、液面プロテクタが動作して、洗浄用
ポンプの動作の停止を指令する。これにより、洗浄用ポ
ンプが無負荷運転をすることがなく、焼損することがな
い。
Further, according to the twenty-fourth aspect, the amount of the hydrocarbon-based solvent sent from the reserve tank to the hydrocarbon cleaning tank 10 increases, and even if the amount of the hydrocarbon-based solvent in the reserve tank decreases, the amount of the solvent increases. The surface protector operates to instruct the cleaning pump to stop operating. Thus, the cleaning pump does not perform a no-load operation and does not burn.

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

【図1】 この発明の実施の形態1および2による表面
処理工程図である。
FIG. 1 is a surface treatment process diagram according to Embodiments 1 and 2 of the present invention.

【図2】 この発明の実施の形態2による表面処理工程
を行った場合のめっきの出来栄えを示す図である。
FIG. 2 is a diagram showing a result of plating when a surface treatment step according to a second embodiment of the present invention is performed.

【図3】 この発明の実施の形態3による洗浄装置の概
略構成図である。
FIG. 3 is a schematic configuration diagram of a cleaning device according to a third embodiment of the present invention.

【図4】 図3の洗浄装置における各部のタイムチャー
ト図である。
FIG. 4 is a time chart of each part in the cleaning apparatus of FIG. 3;

【図5】 従来の炭化水素を使った表面処理工程図であ
る。
FIG. 5 is a process diagram of a conventional surface treatment using a hydrocarbon.

【符号の説明】[Explanation of symbols]

1a 炭化水素洗浄槽 1b 洗浄装置 2 第一の洗浄槽 3 第二の洗浄槽 4 第三の洗浄槽 5 アルカリ脱脂槽 6 酸洗い槽 7 めっき槽 10 炭化水素洗浄槽 10a 洗浄部 10b 蓋 10d 第1の底部 10e 第2の底部 12 バスケット 14 リザーブタンク 14a リンス液タンク 14b 段差 14c 液面検出部 15 炭化水素系溶剤 15a 清浄な炭化水素系溶剤 16 洗浄用ポンプ 18 リンス液用ポンプ 20 流量切換指令装置 22a1、22a2、22b、22c、22d ノズル 24 蒸留器 26 乾燥器 28 真空ポンプ 30 ファン 32 加熱器 34 窒素ガス発生器 36 超音波振動子 40a、40b、40c、40d、40e、40f、4
0g、40h、40i 、40j、40k バルブ 42a 排水管 42b シャワー水供給管 42c 噴流水供給管 42d 排水排気管 42e 窒素ガス供給管 44 液面レベル検出器 46 液面プロテクタ 48 コテージ 48b 扉 50 ダクト
1a hydrocarbon washing tank 1b washing device 2 first washing tank 3 second washing tank 4 third washing tank 5 alkali degreasing tank 6 pickling tank 7 plating tank 10 hydrocarbon washing tank 10a washing unit 10b lid 10d first 10e Second bottom 12 Basket 14 Reserve tank 14a Rinse liquid tank 14b Step 14c Liquid level detector 15 Hydrocarbon solvent 15a Clean hydrocarbon solvent 16 Cleaning pump 18 Rinse liquid pump 20 Flow rate switching command device 22a1 , 22a2, 22b, 22c, 22d Nozzle 24 Distiller 26 Dryer 28 Vacuum pump 30 Fan 32 Heater 34 Nitrogen gas generator 36 Ultrasonic transducer 40a, 40b, 40c, 40d, 40e, 40f, 4f
0g, 40h, 40i, 40j, 40k Valve 42a Drain pipe 42b Shower water supply pipe 42c Jet water supply pipe 42d Drain discharge exhaust pipe 42e Nitrogen gas supply pipe 44 Liquid level detector 46 Liquid level protector 48 Cottage 48b Door 50 duct

───────────────────────────────────────────────────── フロントページの続き (72)発明者 松田 淑男 東京都千代田区丸の内二丁目2番3号 三 菱電機株式会社内 (72)発明者 太田 努 東京都千代田区丸の内二丁目2番3号 三 菱電機株式会社内 (72)発明者 村田 裕康 大阪府大阪市東淀川区西淡路3丁目1番56 号 株式会社三社電機製作所内 (72)発明者 山地 信幸 大阪府大阪市東淀川区西淡路3丁目1番56 号 株式会社三社電機製作所内 Fターム(参考) 3B201 AA46 AB01 BB05 BB23 BB82 BB85 BB95 BB96 CB15 CC01 CC12 CD11 CD42 CD43 4K053 PA10 QA04 RA15 RA16 RA17 RA18 RA25 RA29 RA32 SA04 SA06 SA08 SA18 TA12 TA16 TA17 XA11 XA24 XA28  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yoshio Matsuda 2-3-2 Marunouchi, Chiyoda-ku, Tokyo Within Mitsubishi Electric Corporation (72) Inventor Tsutomu Ota 2-3-2 Marunouchi, Chiyoda-ku, Tokyo Inside Ryo Denki Co., Ltd. (72) Inventor Hiroyasu Murata 3-1-156 Nishi-Awaji, Higashi-Yodogawa-ku, Osaka-shi, Osaka Inside Sansha Electric Manufacturing Co., Ltd. No. 1-56 F-term in Sansha Electric Manufacturing Co., Ltd. (reference) 3B201 AA46 AB01 BB05 BB23 BB82 BB85 BB95 BB96 CB15 CC01 CC12 CD11 CD42 CD43 4K053 PA10 QA04 RA15 RA16 RA17 RA18 RA25 RA29 RA32 SA04 SA06 SA08 SA18 TA12 TA16 TA17 XA XA28

Claims (24)

【特許請求の範囲】[Claims] 【請求項1】 水溶性油及び非水系油などが付着した被
洗浄物を炭化水素系溶剤に浸漬して脱脂した後、酸性溶
液で水溶性油の成分を除去する脱脂洗浄方法。
1. A degreasing cleaning method in which an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered is immersed in a hydrocarbon solvent to degrease, and then a component of the water-soluble oil is removed with an acidic solution.
【請求項2】 水溶性油及び非水系油などが付着した被
洗浄物を炭化水素系溶剤に浸漬して脱脂した後、動植物
油を除去するためのアルカリ脱脂を得ることなく酸性溶
液に浸漬することによって水溶性油の成分を除去し、し
かるべき後に動植物油を除去するアルカリ脱脂と被洗浄
物を化学的に活性化する酸洗いを行なう脱脂洗浄方法。
2. An object to be washed to which a water-soluble oil or a non-aqueous oil is adhered is immersed in a hydrocarbon solvent to degrease it, and then immersed in an acidic solution without obtaining alkaline degreasing for removing animal and vegetable oils. A degreasing method in which the components of the water-soluble oil are removed by an appropriate method, followed by alkaline degreasing for removing animal and vegetable oils and acid pickling for chemically activating the object to be cleaned.
【請求項3】 上記酸性溶液は、0.267モル乃至
2.670モルの硫酸と0.56モル以下のアルミニウ
ムを成分とする洗浄液から成ることを特徴とする請求項
1もしくは2に記載の脱脂洗浄方法。
3. The degreasing method according to claim 1, wherein the acidic solution comprises a cleaning liquid containing 0.267 mol to 2.670 mol of sulfuric acid and 0.56 mol or less of aluminum. Cleaning method.
【請求項4】 上記酸性溶液は、0.206モル乃至
0.412モルの硝酸と0.05モル乃至0.10モル
のフッ酸と0.15モル乃至0.30モルの塩化第二鉄
を成分とする洗浄液から成ることを特徴とする請求項1
もしくは2に記載の脱脂洗浄方法。
4. The acidic solution comprises 0.206 mol to 0.412 mol of nitric acid, 0.05 mol to 0.10 mol of hydrofluoric acid and 0.15 mol to 0.30 mol of ferric chloride. 2. A cleaning liquid as a component.
Or the degreasing method according to 2.
【請求項5】 上記酸性溶液は、5.03乃至6.70
モルの硝酸と、3.35乃至4.46モルの硫酸と、
0.18乃至0.37モルのりん酸と、1.58乃至
2.10モルの酸性弗化アンモニウムとを成分とする洗
浄液から成ることを特徴とする請求項1もしくは2に記
載の脱脂洗浄方法。
5. The method according to claim 1, wherein the acidic solution is in a range of 5.03 to 6.70.
Moles of nitric acid, 3.35 to 4.46 moles of sulfuric acid,
3. A degreasing cleaning method according to claim 1, comprising a cleaning solution containing 0.18 to 0.37 mol of phosphoric acid and 1.58 to 2.10 mol of ammonium acid fluoride. .
【請求項6】 被洗浄物を炭化水素系溶剤に浸漬する第
1の工程と、上記炭化水素系溶剤に浸漬された被洗浄物
を酸性溶液に浸漬する第2の工程と、上記酸性溶液に浸
漬された被洗浄物をアルカリ脱脂する第3の工程と、上
記アルカリ脱脂された被洗浄物を化学的に活性化する酸
洗いを行う第4の工程とを備えた脱脂洗浄方法。
6. A first step of immersing the object to be cleaned in a hydrocarbon solvent, a second step of immersing the object to be cleaned immersed in the hydrocarbon solvent in an acidic solution, A degreasing / cleaning method comprising a third step of alkali-degreasing the immersed object to be cleaned and a fourth step of pickling to chemically activate the alkali-degreased object to be cleaned.
【請求項7】 上記第4の工程は、上記第3の工程でア
ルカリ脱脂された被洗浄物を後工程でめっきもしくは塗
装するための酸洗いを行うことを特徴とする請求項6記
載の脱脂洗浄方法。
7. The degreasing method according to claim 6, wherein in the fourth step, the object to be cleaned which has been alkali-degreased in the third step is subjected to pickling for plating or painting in a subsequent step. Cleaning method.
【請求項8】 気密形成可能な炭化水素洗浄槽に水溶性
油及び非水系油等が付着した被洗浄物を収容し内部を気
密形成する準備工程と、上記炭化水素洗浄槽に設けた複
数のノズルから炭化水素系溶剤をシャワー水として供給
し上記被洗浄物をシャワー洗浄するとともに、上記炭化
水素洗浄槽に上記炭化水素系溶剤を溜める第1のシャワ
ー洗浄工程と、上記シャワー水を継続して供給させて溜
められた炭化水素系溶剤を攪拌させるとともに、上記被
洗浄物から取り出された水溶性油及び非水系油を上記炭
化水素系溶剤とともに回収する第2のシャワー洗浄工程
とを備えた脱脂洗浄方法。
8. A preparatory step for storing an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like is attached in a hydrocarbon cleaning tank capable of forming an airtight state and forming the inside airtight, and a plurality of steps provided in the hydrocarbon cleaning tank. A first shower cleaning step of supplying the hydrocarbon-based solvent as shower water from the nozzle to shower-clean the object to be cleaned and storing the hydrocarbon-based solvent in the hydrocarbon cleaning tank, and continuing the shower water. A second shower cleaning step of agitating the supplied hydrocarbon-based solvent and collecting the water-soluble oil and the non-aqueous oil removed from the object to be cleaned together with the hydrocarbon-based solvent. Cleaning method.
【請求項9】 気密形成可能な炭化水素洗浄槽に水溶性
油及び非水系油等が付着した被洗浄物を収容し内部を気
密形成する準備工程と、上記炭化水素洗浄槽に設けた複
数のノズルから炭化水素系溶剤をシャワー水として供給
し上記被洗浄物をシャワー洗浄するとともに、上記炭化
水素洗浄槽に上記炭化水素系溶剤を溜める第1のシャワ
ー洗浄工程と、上記第1のシャワー洗浄工程終了後上記
炭化水素洗浄槽に大量且つ高速に上記炭化水素系溶剤を
供給し噴流水を発生させるとともに回収し、上記炭化水
素系溶剤を循環させる噴流水循環工程とを備えた脱脂洗
浄方法。
9. A preparatory step for accommodating a cleaning object to which a water-soluble oil, a non-aqueous oil or the like has adhered in a hydrocarbon cleaning tank capable of forming an airtight state, and forming the inside of the hydrocarbon cleaning tank airtight; A first shower cleaning step of supplying the hydrocarbon-based solvent as shower water from a nozzle to shower-clean the object to be cleaned and storing the hydrocarbon-based solvent in the hydrocarbon cleaning tank; and a first shower cleaning step. A dewatering / cleaning method comprising: supplying a large amount of the hydrocarbon-based solvent to the hydrocarbon-cleaning tank at a high speed after completion; generating and collecting jet water; and circulating the hydrocarbon-based solvent.
【請求項10】 気密形成可能な炭化水素洗浄槽に水溶
性油及び非水系油等が付着した被洗浄物を収容し内部を
気密形成する準備工程と、上記炭化水素洗浄槽に設けた
複数のノズルから炭化水素系溶剤をシャワー水として供
給し上記被洗浄物をシャワー洗浄する第1のシャワー洗
浄工程と、上記第1のシャワー洗浄工程終了後上記炭化
水素系溶剤を回収する第1の回収工程と、上記第1の回
収工程終了後清浄な炭化水素系溶剤を被洗浄物に供給し
リンスするリンス工程と、上記リンス工程終了後リンス
後の上記炭化水素系溶剤を回収する第2の回収工程と、
上記第2の回収工程終了後上記炭化水素洗浄槽に加熱し
た窒素ガスを供給して、上記炭化水素洗浄槽内を窒素ガ
スに置換する第1の窒素ガス置換工程と、上記第1の窒
素ガス置換工程終了後上記炭化水素洗浄槽を減圧する減
圧乾燥工程とを備えた脱脂洗浄方法。
10. A preparatory step for accommodating an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered in a hydrocarbon cleaning tank capable of forming an airtight state, and forming an airtight inside, and a plurality of steps provided in said hydrocarbon cleaning tank. A first shower cleaning step of supplying a hydrocarbon-based solvent as shower water from a nozzle to shower-clean the object to be cleaned, and a first recovery step of recovering the hydrocarbon-based solvent after the first shower cleaning step is completed A rinsing step of supplying and rinsing a clean hydrocarbon-based solvent to the object to be cleaned after completion of the first recovery step, and a second recovery step of recovering the hydrocarbon-based solvent after rinsing after completion of the rinsing step When,
After the completion of the second recovery step, a heated nitrogen gas is supplied to the hydrocarbon cleaning tank to replace the inside of the hydrocarbon cleaning tank with nitrogen gas. A depressurizing and drying step of depressurizing the hydrocarbon cleaning tank after the replacement step.
【請求項11】 気密形成可能な炭化水素洗浄槽に水溶
性油及び非水系油等が付着した被洗浄物を収容し内部を
気密形成する準備工程と、上記炭化水素洗浄槽に設けた
複数のノズルから炭化水素系溶剤をシャワー水として供
給し上記被洗浄物をシャワー洗浄するとともに、上記炭
化水素洗浄槽に上記炭化水素系溶剤を溜める第1のシャ
ワー洗浄工程と、上記第1のシャワー洗浄工程終了後上
記炭化水素洗浄槽に大量且つ高速に上記炭化水素系溶剤
を供給し噴流水を発生させるとともに回収し、上記炭化
水素系溶剤を循環させる噴流水循環工程と、上記噴流水
循環工程終了後上記炭化水素系溶剤を回収する第1の回
収工程と、上記第1の回収工程終了後清浄な炭化水素系
溶剤を被洗浄物に供給しリンスするリンス工程と、上記
リンス工程終了後上記リンス後の炭化水素系溶剤を回収
する第2の回収工程と、上記第2の回収工程終了後上記
炭化水素洗浄槽に加熱した窒素ガスを供給して、上記炭
化水素洗浄槽内を窒素ガスに置換する第1の窒素ガス置
換工程と、上記第1の窒素ガス置換工程終了後上記炭化
水素洗浄槽を減圧する減圧乾燥工程とを備えた脱脂洗浄
方法。
11. A preparatory step for accommodating a cleaning object to which a water-soluble oil, a non-aqueous oil or the like has adhered in a hydrocarbon cleaning tank capable of forming an airtight state, and forming an airtight inside, and a plurality of cleaning steps provided in said hydrocarbon cleaning tank. A first shower cleaning step of supplying the hydrocarbon-based solvent as shower water from a nozzle to shower-clean the object to be cleaned and storing the hydrocarbon-based solvent in the hydrocarbon cleaning tank; and a first shower cleaning step. After the completion, a large amount and high speed of the hydrocarbon solvent is supplied to the hydrocarbon washing tank to generate and collect jet water, and the jet water circulation step of circulating the hydrocarbon solvent; A first recovery step of recovering the hydrogen-based solvent, a rinsing step of supplying a clean hydrocarbon-based solvent to the object to be cleaned after the first recovery step and rinsing the same; A second recovery step of recovering the hydrocarbon solvent after the rinsing, and supplying a heated nitrogen gas to the hydrocarbon cleaning tank after completion of the second recovery step so that nitrogen gas is supplied into the hydrocarbon cleaning tank. A degreasing cleaning method comprising: a first nitrogen gas replacement step of replacing the pressure with a nitrogen gas; and a reduced-pressure drying step of reducing the pressure of the hydrocarbon cleaning tank after the completion of the first nitrogen gas replacement step.
【請求項12】 上記窒素ガス置換工程終了後に、上記
炭化水素洗浄槽内にエアーを供給し、窒素ガスからエア
ーに置換する第1の混合置換工程を備えたことを特徴と
する請求項10もしくは11記載の脱脂洗浄方法。
12. The method according to claim 10, further comprising a first mixing and replacing step of supplying air into the hydrocarbon cleaning tank and replacing the nitrogen gas with air after the nitrogen gas replacing step. 12. The degreasing cleaning method according to 11.
【請求項13】 上記減圧乾燥工程終了後に、上記炭化
水素洗浄槽に加熱した窒素ガスを供給して、上記炭化水
素洗浄槽内を窒素ガスに置換する第2の窒素ガス置換工
程と、上記炭化水素洗浄槽内にエアーを供給し、窒素ガ
スからエアーに置換する第2の混合置換工程を備えたこ
とを特徴とする請求項10ないし12記載の脱脂洗浄方
法。
13. A second nitrogen gas replacement step of supplying heated nitrogen gas to the hydrocarbon cleaning tank to replace the inside of the hydrocarbon cleaning tank with nitrogen gas after the completion of the reduced pressure drying step. 13. The degreasing cleaning method according to claim 10, further comprising a second mixing and replacing step of supplying air into the hydrogen cleaning tank and replacing the nitrogen gas with air.
【請求項14】 水溶性油及び非水系油などが付着した
被洗浄物を炭化水素系溶剤によって脱脂洗浄する洗浄装
置において、炭化水素系溶剤を注入するための1槽から
成る炭化水素洗浄槽と、水溶性油の成分を除去する酸性
溶液を注入するための酸洗い槽とを備えた洗浄装置。
14. A cleaning apparatus for degreasing and cleaning an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered with a hydrocarbon-based solvent, comprising a hydrocarbon-cleaning tank for injecting a hydrocarbon-based solvent. A washing device including a pickling tank for injecting an acidic solution for removing components of a water-soluble oil.
【請求項15】 水溶性油及び非水系油などが付着した
被洗浄物を炭化水素系溶剤によって脱脂洗浄する洗浄装
置において、炭化水素系溶剤を注入するための1槽から
成る炭化水素洗浄槽と、上記炭化水素洗浄槽で洗浄され
る被洗浄物を、上記炭化水素洗浄槽から酸性溶液を注入
するための酸洗い槽へ向かう搬送経路へ搬送するための
移送手段とを備えた洗浄装置。
15. A cleaning apparatus for degreasing and cleaning an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered with a hydrocarbon-based solvent, comprising a hydrocarbon-cleaning tank for injecting a hydrocarbon-based solvent. A transfer device for transferring an object to be cleaned in the hydrocarbon cleaning tank to a transport path from the hydrocarbon cleaning tank to an acid cleaning tank for injecting an acidic solution.
【請求項16】 上面に開口部を有する槽とこの槽の開
口部を塞ぐあるいは開くための開閉自在な蓋とを有し、
この槽に水溶性油及び非水系油等が付着した被洗浄物を
収容し炭化水素系溶剤による洗浄を行う気密形成可能な
炭化水素洗浄槽であって、上記蓋の下面に互いに離間し
て配置され炭化水素系溶剤を噴出する複数のノズルと、
上記それぞれのノズルから噴出された炭化水素系溶剤が
重なりを有する高さの近傍に設けられ、上記炭化水素系
溶剤を槽内から排出する排水口とを有した炭化水素洗浄
槽を備えた洗浄装置。
16. A tank having an opening on the upper surface and an openable / closable lid for closing or opening the opening of the tank,
An air-tightly formed hydrocarbon cleaning tank for storing an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered, and performing cleaning with a hydrocarbon-based solvent. A plurality of nozzles that eject a hydrocarbon solvent,
A cleaning device comprising a hydrocarbon cleaning tank provided near a height at which the hydrocarbon solvents ejected from the respective nozzles have an overlap, and having a drain port for discharging the hydrocarbon solvents from the tank. .
【請求項17】 第1の開口部とこの開口部を開閉する
ための第1の開閉手段を有し、水溶性油及び非水系油等
が付着した被洗浄物を収容し炭化水素系溶剤による洗浄
を行う気密形成可能な炭化水素洗浄槽と、上記炭化水素
洗浄槽から洗浄後の炭化水素系溶剤を回収する排液回収
手段と、上記炭化水素洗浄槽内のガス又は水分を外部に
排気する第1の排気手段とを備え、上記炭化水素洗浄槽
は、第2の開口部、この開口部を開閉するための第2の
開閉手段、および内部の空気を上記外部に排出する第2
の排気手段とを有して気密形成可能なコテージ内に収容
されるように設置されることを特徴とする洗浄装置。
17. A cleaning device having a first opening and first opening / closing means for opening and closing the opening, containing an object to be cleaned to which a water-soluble oil, a non-aqueous oil, or the like is attached, and comprising a hydrocarbon-based solvent. An airtight hydrocarbon cleaning tank for cleaning, a drainage recovery means for recovering the hydrocarbon solvent after cleaning from the hydrocarbon cleaning tank, and exhausting gas or moisture in the hydrocarbon cleaning tank to the outside. A first exhaust unit, wherein the hydrocarbon cleaning tank has a second opening, a second opening / closing unit for opening / closing the opening, and a second opening / discharging unit for discharging internal air to the outside.
A cleaning device, which is installed so as to be housed in a cottage that can be formed airtight with the exhaust means.
【請求項18】 水溶性油及び非水系油等が付着した被
洗浄物を収容し炭化水素系溶剤による洗浄と乾燥を行う
気密形成可能な炭化水素洗浄槽と、上記炭化水素系溶剤
を収容するリザーブタンクと、上記炭化水素系溶剤を蒸
留再生させた清浄な炭化水素系溶剤を収容するリンス液
タンクと、上記リザーブタンク内の上記炭化水素系溶剤
を取り入れ、上記炭化水素洗浄槽に供給する洗浄用ポン
プと、上記リンス液タンク内の上記清浄な炭化水素系溶
剤を取り入れ、上記炭化水素洗浄槽に供給するリンス液
用ポンプとが、気密形成可能なコテージにより収容され
ている洗浄装置。
18. A hydrocarbon-cleaning tank capable of containing an object to be cleaned to which a water-soluble oil, a non-aqueous oil or the like has adhered, and being capable of forming an airtight seal for washing and drying with a hydrocarbon-based solvent, and containing the hydrocarbon-based solvent. A cleaning tank that contains a reserve tank, a rinsing liquid tank containing a clean hydrocarbon-based solvent obtained by distilling and regenerating the hydrocarbon-based solvent, and supplying the hydrocarbon-based solvent in the reserve tank to the hydrocarbon-cleaning tank. A cleaning device in which a rinsing liquid pump and a rinsing liquid pump that takes in the clean hydrocarbon-based solvent in the rinsing liquid tank and supplies the rinsing liquid to the hydrocarbon cleaning tank are housed in a cottage that can be airtightly formed.
【請求項19】 水溶性油及び非水系油等が付着した被
洗浄物を収容し炭化水素系溶剤による洗浄と乾燥を行う
気密形成可能な炭化水素洗浄槽と、上記炭化水素洗浄槽
から洗浄後の炭化水素系溶剤を回収する排液回収手段
と、上記炭化水素洗浄槽内のガス又は水分を外部に排出
する真空ポンプと、窒素ガスを発生させる窒素ガス発生
装置と、上記窒素ガスを上記炭化水素洗浄槽に供給し窒
素ガスに置換する置換乾燥系と、上記窒素ガス置換終了
後に、上記炭化水素洗浄槽内にエアーを供給し、窒素ガ
スからエアーに置換する混合置換系とを備えた洗浄装
置。
19. A hydrocarbon-cleaning tank capable of containing an object to be cleaned to which a water-soluble oil, a non-aqueous oil, or the like is attached, and being cleaned and dried with a hydrocarbon-based solvent, and after cleaning from the hydrocarbon-cleaning tank. Wastewater collecting means for collecting the hydrocarbon solvent, a vacuum pump for discharging gas or moisture in the hydrocarbon washing tank to the outside, a nitrogen gas generator for generating nitrogen gas, and A cleaning system including a replacement drying system that supplies a hydrogen cleaning tank and replaces with nitrogen gas, and a mixed replacement system that supplies air into the hydrocarbon cleaning tank and replaces nitrogen gas with air after completion of the nitrogen gas replacement. apparatus.
【請求項20】 水溶性油及び非水系油等が付着した被
洗浄物を収容し炭化水素系溶剤による洗浄と乾燥を行う
気密形成可能な炭化水素洗浄槽と、上記炭化水素系溶剤
を収容するリザーブタンクと、上記炭化水素系溶剤を蒸
留再生させた清浄な炭化水素系溶剤を収容するリンス液
タンクと、上記リザーブタンク内の上記炭化水素系溶剤
を取り入れ、上記炭化水素洗浄槽に供給する洗浄用ポン
プと、上記リンス液タンク内の上記清浄な炭化水素系溶
剤を取り入れ、上記炭化水素洗浄槽に供給するリンス液
用ポンプと、上記炭化水素洗浄槽内のガス又は水分を外
部に排出する真空ポンプと、窒素ガスを発生させる窒素
ガス発生装置と、上記窒素ガスを上記炭化水素洗浄槽に
供給し窒素ガスに置換する置換乾燥系とを備えた洗浄装
置。
20. An air-tightly formed hydrocarbon cleaning tank for containing an object to be washed to which a water-soluble oil, a non-aqueous oil or the like is attached, and for washing and drying with a hydrocarbon solvent, and containing the hydrocarbon solvent. A cleaning tank that contains a reserve tank, a rinsing liquid tank containing a clean hydrocarbon-based solvent obtained by distilling and regenerating the hydrocarbon-based solvent, and supplying the hydrocarbon-based solvent in the reserve tank to the hydrocarbon-cleaning tank. Pump, a rinsing liquid pump that takes in the clean hydrocarbon solvent in the rinsing liquid tank and supplies it to the hydrocarbon cleaning tank, and a vacuum that discharges gas or moisture in the hydrocarbon cleaning tank to the outside. A cleaning apparatus comprising: a pump; a nitrogen gas generator for generating nitrogen gas; and a replacement drying system for supplying the nitrogen gas to the hydrocarbon cleaning tank and replacing the hydrocarbon gas with nitrogen gas.
【請求項21】 上記置換乾燥系に水分とガスとを分離
させ乾燥させる乾燥器と、ガスを加熱する加熱器とを備
えたことを特徴とする請求項20記載の洗浄装置。
21. The cleaning apparatus according to claim 20, wherein the replacement drying system includes a dryer for separating and drying moisture and gas, and a heater for heating the gas.
【請求項22】 上記洗浄用ポンプから上記炭化水素洗
浄槽に設けられた複数のノズルに上記炭化水素系溶剤を
送出し、上記ノズルからシャワー水を供給するシャワー
水供給機構と、上記洗浄用ポンプから上記炭化水素洗浄
槽に大量かつ高速に上記炭化水素系溶剤を供給する噴流
水供給機構と、上記シャワー水供給機構と上記噴流水供
給機構とを切換指令する切換指令装置とを備えたことを
特徴とする請求項20記載の洗浄装置。
22. A shower water supply mechanism for sending the hydrocarbon-based solvent from the washing pump to a plurality of nozzles provided in the hydrocarbon washing tank and supplying shower water from the nozzles, and the washing pump. A jet water supply mechanism for supplying the hydrocarbon-based solvent to the hydrocarbon cleaning tank in a large amount and at a high speed, and a switching command device for switching between the shower water supply mechanism and the jet water supply mechanism. The cleaning device according to claim 20, wherein
【請求項23】 上記炭化水素洗浄槽が、開口する上部
と、側部から内部に向かって下がる勾配を有し、その中
央部が下に深淵をなす底部とを有する洗浄部と、上記洗
浄部の開口を覆いふさぐ蓋とを有し気密状態を形成可能
な洗浄槽であり、両側に伸張し、中央部が深淵をなし上
記炭化水素洗浄槽に収容されるバスケットとの組合せを
備えたことを特徴とする請求項20記載の洗浄装置。
23. A cleaning section, wherein the hydrocarbon cleaning tank has an opening at the top, a slope having a slope descending from the side to the inside, and a bottom having a deep bottom at the center thereof; A washing tank capable of forming an airtight state having a lid that covers and closes the opening of the washing tank, which is extended to both sides, and has a combination with a basket formed in the hydrocarbon washing tank with a central part forming an abyss. The cleaning device according to claim 20, wherein
【請求項24】 水溶性油及び非水系油等が付着した被
洗浄物を収容し炭化水素系溶剤による洗浄と乾燥を行う
気密形成可能な炭化水素洗浄槽と、上記炭化水素系溶剤
を収容するリザーブタンクと、上記リザーブタンク内の
上記炭化水素系溶剤を取り入れ、上記炭化水素洗浄槽に
供給する洗浄用ポンプと、上記リザーブタンク内の炭化
水素系溶剤が所定の液面レベルより低下したとき上記洗
浄用ポンプの動作の停止指令を行う液面プロテクタとを
備えた洗浄装置。
24. An air-tightly formed hydrocarbon washing tank for containing an object to be washed to which a water-soluble oil, a non-aqueous oil or the like is attached, and for washing and drying with a hydrocarbon solvent, and for accommodating the hydrocarbon solvent. A reservoir, and a cleaning pump that takes in the hydrocarbon-based solvent in the reserve tank and supplies the hydrocarbon-based cleaning tank with the cleaning pump, and that the hydrocarbon-based solvent in the reserve tank drops below a predetermined liquid level. A cleaning device comprising: a liquid level protector that issues a command to stop the operation of the cleaning pump.
JP36091599A 1999-12-20 1999-12-20 Degreasing and cleaning method and cleaning apparatus Expired - Lifetime JP4328436B2 (en)

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JP2006253517A (en) * 2005-03-14 2006-09-21 Dainippon Screen Mfg Co Ltd Reduced-pressure dryer
JP2008272114A (en) * 2007-04-26 2008-11-13 Olympus Medical Systems Corp Endoscope cleaning disinfection device
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