JPH0741199B2 - Pressure washing device - Google Patents

Pressure washing device

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Publication number
JPH0741199B2
JPH0741199B2 JP4271371A JP27137192A JPH0741199B2 JP H0741199 B2 JPH0741199 B2 JP H0741199B2 JP 4271371 A JP4271371 A JP 4271371A JP 27137192 A JP27137192 A JP 27137192A JP H0741199 B2 JPH0741199 B2 JP H0741199B2
Authority
JP
Japan
Prior art keywords
pressure
cleaning liquid
cleaning
water
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP4271371A
Other languages
Japanese (ja)
Other versions
JPH06121962A (en
Inventor
野 裕 久 中
木 宏 和 鈴
Original Assignee
浜松熱処理工業株式会社
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 浜松熱処理工業株式会社 filed Critical 浜松熱処理工業株式会社
Priority to JP4271371A priority Critical patent/JPH0741199B2/en
Publication of JPH06121962A publication Critical patent/JPH06121962A/en
Publication of JPH0741199B2 publication Critical patent/JPH0741199B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、有形物(以下被洗浄
物)よりそれに付着した物体(以下付着物)を除去する
洗浄に関し、特に、これに限る意図ではないが、工具,
機械部品などの金属製品より、その加工,製造過程で付
着した油等を除去する洗浄に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to cleaning for removing an object (hereinafter referred to as an adhered matter) attached to a tangible object (hereinafter referred to as an object to be cleaned), and particularly, although not intended to be limited to this, a tool,
The present invention relates to cleaning for removing oil and the like attached to metal products such as machine parts during processing and manufacturing processes.

【0002】[0002]

【従来の技術】従来のこの種の洗浄には、フロン等の塩
素系有機溶剤あるいはカ性ソ−ダ水溶液等の水系洗浄剤
が用いられ、常圧又は減圧下で、溶剤あるいは洗浄剤は
必要に応じて加熱される。
2. Description of the Related Art For this type of conventional cleaning, a chlorine-based organic solvent such as CFC or an aqueous cleaning agent such as an aqueous solution of caustic soda is used, and the solvent or the cleaning agent is required under normal pressure or reduced pressure. Is heated accordingly.

【0003】[0003]

【発明が解決しようとする課題】溶剤は大気汚染の問題
がある。大気への溶剤の放散を防止するためには、洗浄
槽がある洗浄室から洗浄済の被洗浄物を乾燥室に移し、
該乾燥室から洗浄済の被洗浄物を出すと共に該乾燥室に
未洗浄の被洗浄物を入れて、乾燥室を閉じてから該室内
の未洗浄の被洗浄物を洗浄槽がある部屋に移して洗浄槽
に入れて、この洗浄を終えると洗浄済の被洗浄物を乾燥
室に移すという物体搬送と、乾燥室の気化溶剤を回収す
る工程が必要である。付帯設備が多くなるという問題
と、乾燥室に対する被洗浄物の出し入れにおいて気化溶
剤が大気に漏れるので完全な溶剤回収が無理である。
Solvents have a problem of air pollution. In order to prevent the release of the solvent into the atmosphere, move the cleaned object from the cleaning room with the cleaning tank to the drying room,
The cleaned object is put out from the drying chamber, the uncleaned object is put in the drying chamber, the drying chamber is closed, and the uncleaned object in the chamber is transferred to a room having a cleaning tank. It is necessary to carry out an object transfer of putting the cleaned object in a cleaning tank and transferring the cleaned object to the drying chamber when this cleaning is completed, and a step of collecting the vaporized solvent in the drying chamber. It is impossible to completely recover the solvent because the amount of auxiliary equipment increases and the vaporized solvent leaks to the atmosphere when the object to be cleaned is put in or taken out of the drying chamber.

【0004】水系洗浄剤を用いる洗浄では、大気汚染の
問題は実質上皆無で、洗浄剤の回収,再使用が比較的に
容易であるが、従来は洗浄性を高めるため、濃度3〜5
%のカ性ソ−ダ水溶液を洗浄液として用いるなど、かな
り高濃度の洗浄剤が使用されており、洗浄後に被洗浄物
の洗浄剤を水洗除去するのに多量の水と時間を要し、し
かも水洗後に水切り工程および乾燥工程を要する。すな
わち洗浄工程よりもむしろ後工程に、設備および処理時
間を多とする。水系洗浄剤による洗浄において従来から
設備や洗浄剤に改善が加えられてきたが、塩素系溶剤の
洗浄効果ならびに洗浄後に乾燥状態で取り出せる工程上
の利点については、水系洗浄剤による洗浄の課題として
残っている。
In the case of cleaning using a water-based cleaning agent, there is virtually no problem of air pollution, and it is relatively easy to recover and reuse the cleaning agent.
%, A very high concentration cleaning agent is used, such as an aqueous solution of caustic soda as a cleaning solution, and it requires a large amount of water and time to remove the cleaning agent from the object to be washed with water after cleaning. A draining process and a drying process are required after washing with water. That is, the equipment and processing time are increased in the subsequent process rather than the cleaning process. Although improvements have been made to equipment and cleaning agents for cleaning with water-based cleaning agents, the cleaning effect of chlorine-based solvents and the advantage of the process that can be taken out in a dry state after cleaning remain as issues for cleaning with water-based cleaning agents. ing.

【0005】本発明は、従来の水系洗浄における水の利
点を生かし、高い洗浄効果を得てしかも洗浄後処理を簡
単ないしは実質上不要とすることを目的とする。
An object of the present invention is to take advantage of water in conventional water-based cleaning, obtain a high cleaning effect, and make post-cleaning treatment simple or substantially unnecessary.

【0006】[0006]

【課題を解決するための手段】本発明の加圧式洗浄方法
では、加圧容器(1)内に被洗浄物(30)および水もしくは
水に水系洗浄剤を配合した洗浄液を入れて洗浄液を加熱
し、加圧容器内圧力を0.5Kg/cm2以上3Kg/cm2以下に、洗
浄液温度を加圧容器内圧では洗浄液が実質上気化しない
80℃〜130℃の温度に維持して、高温高圧洗浄液により
それに浸漬した被洗浄物の付着物を洗浄し、加圧容器
(1)内の洗浄液を、容器外に排出して容器外で冷却して
比重差により洗浄液より付着物を分離した後、加圧容器
(1)に再供給する。
According to the pressure type cleaning method of the present invention, the pressure vessel (1) is heated by heating the object to be cleaned (30) and water or a cleaning liquid containing water or an aqueous cleaning agent. and, a pressurized container pressure below 0.5 Kg / cm 2 or more 3 Kg / cm 2, is not substantially vaporized cleaning liquid to the washing liquid temperature in a pressurized vessel pressure
Keeping the temperature at 80 ℃ to 130 ℃, wash the deposits of the cleaning object immersed in it with the high temperature and high pressure cleaning liquid , and pressurize the container.
(1) Drain the cleaning solution inside the container and cool it outside the container.
After separating the deposits from the cleaning liquid due to the difference in specific gravity, pressurization container
Re-supplied to the (1).

【0007】本発明の加圧式洗浄装置は、注水口(6)お
よび排水口(7a,7c)を有する、被洗浄物(30)を収容する
加圧容器(1);被洗浄物(30)に付着していた付着物が含
まれる、水もしくは水に水系洗浄剤を配合した洗浄液よ
り、比重差により付着物を分離する付着物分離槽(12);
前記加圧容器(1)の排水口(7a,7c)から前記付着物分離槽
(12)に流れる洗浄液を冷却する冷却装置(25a,25c);前
記付着物分離槽(12)で付着物が分離された洗浄液を、前
記加圧容器(1)の注水口(6)に供給するポンプ(21);前記
加圧容器(1)内の洗浄液を加熱する加熱手段(4);加圧容
器(1)内の洗浄液の温度を検出する温度センサ(26);お
よび、加圧容器(1)内の圧力を検出する圧力センサ(1
0);を備える。
The pressure type washing apparatus of the present invention comprises a pressure vessel (1) for containing an article to be washed (30) having a water injection port (6) and a drain port (7a, 7c); An adherent separation tank (12) for separating adherents from water or a cleaning liquid containing a water-based cleaning agent containing the adherents adhered to, by the difference in specific gravity;
From the drainage port (7a, 7c) of the pressure vessel (1) to the deposit separation tank
Cooling device (25a, 25c) for cooling the cleaning liquid flowing to (12); supplying the cleaning liquid from which the adhered substances are separated in the adherent separated tank (12) to the water inlet (6) of the pressure vessel (1) Pump (21); heating means (4) for heating the cleaning liquid in the pressure vessel (1); temperature sensor (26) for detecting the temperature of the cleaning liquid in the pressure vessel (1); and pressure vessel (1) Pressure sensor (1
0);

【0008】なお、カッコ内の記号は、図面に示し後述
する実施例の対応要素に付したものである。
The symbols in parentheses are used for corresponding elements in the embodiments shown in the drawings and described later.

【0009】[0009]

【作用】本発明の加圧式洗浄方法での、0.5Kg/cm2以上3
Kg/cm2以下の圧力、該圧力では洗浄液が実質上気化しな
い80℃〜130℃の温度による、高温高圧の、水もしくは
水に水系洗浄剤を配合した洗浄液による洗浄では、被洗
浄物の表面の付着物の洗浄力が高い。例えば金属製品に
付着している油等は粘度が低下して流動化して被洗浄物
より離れて洗浄液中を上方に移動する。
[Function] In the pressure type cleaning method of the present invention, 0.5 Kg / cm 2 or more 3
The pressure of Kg / cm 2 or less, at a temperature of 80 ° C to 130 ° C at which the cleaning liquid does not substantially vaporize at the pressure, cleaning with a high-temperature high-pressure cleaning liquid containing water or a water-based cleaning agent in water, the surface of the object to be cleaned The cleaning power of adhered substances is high. For example, the oil or the like adhering to the metal product has a reduced viscosity and is fluidized and moves upward in the cleaning liquid away from the object to be cleaned.

【0010】一例として表1に、高温浸炭処理され焼入
油に投入された金属部品(機械部品)すなわち浸炭焼入
れ部品の焼入油の特性を示す。
As an example, Table 1 shows the characteristics of the quenching oil of a metal part (machine part), that is, a carburizing quenching part which has been subjected to a high temperature carburizing treatment and put into a quenching oil.

【0011】[0011]

【表1】 [Table 1]

【0012】例えば表1のグレ−ドBの焼入油は、それ
を40℃から100℃に昇温すると、動粘度が 438.1 cSt か
ら32.27 cSt に、1/10 以下に低下し、水の蒸気化温度
(100℃)あるいはそれ以上の温度では、焼入油の除
去が容易であることが分かる。
For example, in the case of grade B quenching oil in Table 1, when it is heated from 40 ° C. to 100 ° C., the kinematic viscosity drops from 438.1 cSt to 32.27 cSt, less than 1/10, and the vapor of water. It can be seen that the quenching oil can be easily removed at the temperature of conversion (100 ° C.) or higher.

【0013】表2に、水の蒸気圧特性を示す。表2中
の、網がけ領域が本発明の加圧式洗浄方法が適用される
領域である。
Table 2 shows the vapor pressure characteristics of water. The shaded area in Table 2 is the area to which the pressure-type cleaning method of the present invention is applied.

【0014】[0014]

【表2】 [Table 2]

【0015】本発明方法での圧力および温度の下限値
(圧力 0.5Kg,温度 80℃)は、油分を主とする付着物の
流動化をうながし、かつ洗浄液の蒸気化を実質上防止す
る下限条件であり、上限値(圧力 3.0Kg,温度 130℃)
は、加圧容器(1)の耐圧および加圧容器(1)に洗浄液を供
給するポンプ(21)の負荷(所要吐出圧)ならびに洗浄操業
の安全性から求めた上限条件である。表1には、40℃と
100℃の動粘度のみを示すが、下限温度80℃でも40℃に
対して粘度は大きく低下し、焼入油の除去が容易であ
る。この下限温度より温度を高くすることにより粘度が
更に低下し、焼入油の除去効果が更に高くなり、上限温
度130℃では除去効果がきわめて高くなる。
The lower limit values of pressure and temperature (pressure 0.5 Kg, temperature 80 ° C.) in the method of the present invention are the lower limit conditions for promoting fluidization of deposits mainly composed of oil and substantially preventing vaporization of the cleaning liquid. And the upper limit value (pressure 3.0 kg, temperature 130 ° C)
Is the upper limit condition obtained from the pressure resistance of the pressure vessel (1), the load (required discharge pressure) of the pump (21) that supplies the cleaning liquid to the pressure vessel (1), and the safety of the cleaning operation. Table 1 shows that
It shows only a kinematic viscosity of 100 ° C, but even at the lower limit temperature of 80 ° C, the viscosity drops significantly at 40 ° C, and quenching oil can be easily removed. When the temperature is higher than the lower limit temperature, the viscosity is further lowered, the quenching oil removing effect is further enhanced, and at the upper limit temperature 130 ° C., the removing effect is extremely high.

【0016】後述するように、本発明方法の上記領域
(圧力 0.5Kg,温度 80℃から圧力 3.0Kg,温度 130℃)
での高温高圧洗浄は水又は水に微量の水系洗浄剤を配合
した洗浄液で十分な洗浄効果をもたらす。洗浄液を水の
みとする場合あるいは水系洗浄剤を配合してもその残留
量が問題とならない程に微量である場合、洗浄後は、高
温状態となった被洗浄物の自体の熱で被洗浄物が乾燥す
るので、残留洗浄剤除去のための水洗や格別な乾燥工程
が不要である。
As will be described later, the above region of the method of the present invention (pressure 0.5 kg, temperature 80 ° C. to pressure 3.0 kg, temperature 130 ° C.)
The high-temperature and high-pressure cleaning described above brings about a sufficient cleaning effect with water or a cleaning liquid containing a small amount of an aqueous cleaning agent mixed with water. When the cleaning liquid is water only or when the residual amount is small enough to cause no problem even if an aqueous cleaning agent is mixed, after cleaning, the object to be cleaned is heated by the heat of the object to be cleaned itself. Since it is dried, there is no need for washing with water or a special drying step for removing the residual detergent.

【0017】水に水系洗浄剤を配合した洗浄液を用いる
場合でも、高温高圧による洗浄効果が高いので水系洗浄
剤の濃度は極く低く抑制することができ、洗浄後の洗浄
剤除去のための水洗は少量の水で短時間で済み簡単であ
ると共に、被洗浄物の温度低下が少いので乾燥工程は不
要もしくは簡単である。加えて、加圧容器(1)内の洗浄
液を、容器外に排出して容器外で冷却して比重差により
洗浄液より付着物を分離した後、加圧容器(1)に再供給
するので、洗浄液の消費が少く、洗浄廃棄物は実質上付
着物であって少量であるので、洗浄廃棄物の廃棄処理が
容易である。
Even when a cleaning liquid prepared by mixing an aqueous cleaning agent with water is used, the effect of cleaning by high temperature and high pressure is high, so that the concentration of the aqueous cleaning agent can be suppressed to an extremely low level, and the cleaning can be carried out for removing the cleaning agent after cleaning. Is simple and requires a small amount of water in a short time, and the temperature drop of the object to be cleaned is small, so a drying step is unnecessary or simple. In addition, cleaning inside the pressure vessel (1)
The liquid is discharged to the outside of the container and cooled outside the container, depending on the specific gravity difference.
After separating the deposits from the cleaning liquid, re-supply to the pressure vessel (1)
Consumes less cleaning liquid and virtually no cleaning waste
Since it is a kimono and it is a small amount, it is
It's easy.

【0018】本発明の加圧式洗浄装置によれば、ポンプ
(21)が、付着物分離槽(12)で付着物が分離された洗浄液
を加圧容器(1)の注水口(6)に供給し、加熱手段(4)が、
加圧容器(1)内の洗浄液を加熱する。加圧容器(1)の加圧
加熱された洗浄液に、被洗浄物の表面の付着物、特に高
温で水に溶け易い又は流動化し易い付着物、が溶け込み
又はまじり合う。付着物を含む洗浄液は、ポンプ(21)の
上記供給に伴ない加圧容器(1)の排水口(7a,7c)から付着
物分離槽(12)に流れるが、冷却装置(25a,25c)がこの洗
浄液を冷却する。この冷却により付着物は付着物分離槽
(12)において水から分離し易くなると共に、付着物分離
槽(12)での洗浄液の気化を防止することができる。
According to the pressure type cleaning apparatus of the present invention, the pump
(21) is supplied to the water inlet (6) of the pressure vessel (1) the cleaning liquid in which the adhered matter is separated in the adherent matter separation tank (12), the heating means (4),
The cleaning liquid in the pressure vessel (1) is heated. Deposits on the surface of the object to be cleaned, particularly deposits that are easily dissolved or fluidized in water at a high temperature, are dissolved or mixed with the cleaning liquid heated and pressurized in the pressure vessel (1). The cleaning liquid containing deposits flows from the discharge port (7a, 7c) of the pressure vessel (1) to the deposit separation tank (12) with the above supply of the pump (21), but the cooling device (25a, 25c). Cools this wash solution. Due to this cooling, the deposits will be removed from the deposit separation tank.
In (12), it becomes easy to separate from water, and vaporization of the cleaning liquid in the adhered substance separation tank (12) can be prevented.

【0019】温度センサ(26)の検出温度および圧力セン
サ(10)の検出圧に基づいて、加熱手段(4)による加熱量,
ポンプ(21)による洗浄液供給量等を制御することによ
り、加圧容器(1)内の洗浄液を付着物洗浄効果が高い高
温高圧に維持することができる。また、冷却装置(25a,2
5c)による、加圧容器(1)から付着物分離槽(12)に送られ
る洗浄液の冷却により、洗浄液の付着物は付着物分離槽
(12)において洗浄液から分離し易くなると共に、付着物
分離槽(12)での洗浄液の気化を防止することができる。
洗浄を終えると、加熱手段(4)による加熱を停止し、ポ
ンプ(21)および冷却装置(25a,25c)の駆動は継続して加
圧容器(1)内圧力が実質上大気圧となり、大気圧で洗浄
液が実質上蒸発しない値以下となったときに、加圧容器
(1)の上蓋(2)を開いて、被洗浄物を取り出しそして未洗
浄の被洗浄物を入れることにより、洗浄液の大気への逃
散は実質上ない。
Based on the temperature detected by the temperature sensor (26) and the pressure detected by the pressure sensor (10), the heating amount by the heating means (4),
By controlling the amount of the cleaning liquid supplied by the pump (21) and the like, the cleaning liquid in the pressure vessel (1) can be maintained at high temperature and high pressure, which has a high effect of cleaning adhered substances. In addition, the cooling device (25a, 2
By cleaning the cleaning liquid sent from the pressure vessel (1) to the deposit separation tank (12) by 5c), the deposit of the cleaning liquid is separated into the deposit separation tank.
In (12), it becomes easy to separate from the cleaning liquid, and vaporization of the cleaning liquid in the deposit separating tank (12) can be prevented.
When the cleaning is finished, the heating by the heating means (4) is stopped, the pump (21) and the cooling devices (25a, 25c) continue to be driven, and the pressure inside the pressure vessel (1) becomes substantially atmospheric pressure. Pressurized container when the cleaning liquid drops below a value at which it does not evaporate
By opening the upper lid (2) of (1), taking out the object to be cleaned and putting the uncleaned object to be cleaned, there is substantially no escape of the cleaning liquid to the atmosphere.

【0020】本発明の他の目的および特徴は、図面を参
照した以下の実施例の説明より明らかになろう。
Other objects and features of the present invention will become apparent from the following description of embodiments with reference to the drawings.

【0021】[0021]

【実施例】図1に、本発明を一態様で実施する洗浄装置
の主要部の構成を示す。この洗浄装置は、高温浸炭処理
され焼入油に投入された金属部品(機械部品)すなわち
浸炭焼入れ部品の、焼入油を洗浄除去するものである。
すなわち図1に示す洗浄装置は、表1に示す特性の、部
品に付着した焼入油を、主たる除去対象としている。
図1を参照する。加圧缶1は大略で本体3と上蓋2でな
り、本体3内のケ−ジ支台上に、浸炭焼入れ済の機械部
品を入れたケ−ジ30が載せられ、上蓋2はクラッチロ
ック8で本体3に気密に結合される。なお、図示しない
機構で、ロック8の解除,上蓋2の開放,本体3内から
のケ−ジ30の取出しおよびケ−ジ30の装入,上蓋2
の密閉およびロック8の施錠が自動的に行なわれる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows the structure of the main part of a cleaning apparatus for carrying out the present invention in one mode. This cleaning device cleans and removes the quenching oil of the metal parts (machine parts), that is, the carburizing and quenching parts that have been carburized at high temperature and put into the quenching oil.
That is, the cleaning apparatus shown in FIG. 1 mainly targets the quenching oil having the characteristics shown in Table 1 and attached to the component.
Please refer to FIG. The pressure can 1 is roughly composed of a main body 3 and an upper lid 2, a cage 30 containing carburized and quenched mechanical parts is placed on a cage abutment in the main body 3, and the upper lid 2 has a clutch lock 8 It is airtightly connected to the body 3. By a mechanism (not shown), the lock 8 is released, the upper lid 2 is opened, the cage 30 is taken out from the main body 3, and the cage 30 is loaded.
And the lock 8 is automatically locked.

【0022】本体3の上部位置には、2つの循環用排水
口7a,7b(図示せず)が相対向して開けられてお
り、これらの排水口に気密に結合したパイプを通して、
また電動弁23a,バイパス弁24aおよび電動弁23
a,バイパス弁24aを通して、本体3上部の洗浄液は
多管ク−ラ25aおよび25bに流れ、これらのク−ラ
25a,25bを通して油水分離槽12に排出される。
また、本体3の洗浄液は、本体3の下部位置の、水抜き
用排水口7cを通して、また電動弁23c,バイパス弁
24cおよび多管ク−ラ25cを通して、油水分離槽1
2に排出される。油水分離槽12には、上から下に下が
った仕切板19aおよび19cと下から上に立った仕切
板19bおよび19dがあり、加圧缶1から排出された
洗浄液はまず最右方の分離室(第1室)に入る。この分
離室で、洗浄液に含まれる、水より軽い物体すなわちケ
−ジ30に入れられた浸炭焼入れ済の機械部品の付着物
であった油分が上昇し水分が降下して、低比重の物体
(油)が上層となり、水分が下層となる。下層の油分が
少い洗浄液は仕切板19aの下方の通路を通って第2室
に流れる。この第2室でも油分が上昇し水分が降下し
て、低比重の物体(油)が上層となり、水分が下層とな
る。この第2室の上層の、油分が多い洗浄液は仕切板1
9bの上方の通路を通って第3室に流れる。この第3室
でも油分が上昇し水分が降下して、低比重の物体(油)
が上層となり、水分が下層となる。この第3室の下層
の、油分が少い洗浄液は仕切板19cの下方の通路を通
って第4室に流れる。この第4室でも油分が上昇し水分
が降下して、低比重の物体(油)が上層となり、水分が
下層となる。この第4室の上層の、油分が多い洗浄液は
仕切板19dの上方の通路を通って第5室に流れる。こ
の第5室でも油分が上昇し水分が降下して、低比重の物
体(油)が上層となり、水分が下層となる。この第5室
の下層の、油分が少い洗浄液はフィルタ20を通して電
動ポンプ21で吸引されて、逆止弁22を介して、本体
3下底の注水口6を通して本体3内に加圧注入される。
上述の油水分離槽12においては、加圧缶1から排出さ
れた洗浄液は、第1室から第5室に流れる間に水とそれ
より軽い油に分離し、油分の多くは第1室〜第5室に留
まり、上流側の室であるほど、上部層の油分が多い。そ
して最も油分が少い洗浄液がポンプ21で吸引されて加
圧缶1に加圧供給される。
At the upper position of the main body 3, two circulation drainage ports 7a, 7b (not shown) are opened facing each other, and a pipe airtightly connected to these drainage ports is used to
Further, the electric valve 23a, the bypass valve 24a and the electric valve 23
a, the cleaning liquid in the upper part of the main body 3 flows through the bypass valve 24a to the multi-tube coolers 25a and 25b, and is discharged to the oil / water separation tank 12 through these coolers 25a and 25b.
The cleaning liquid for the main body 3 passes through the drainage port 7c at the lower portion of the main body 3, and also through the motor-operated valve 23c, the bypass valve 24c and the multi-tube cooler 25c to separate the oil-water separation tank 1
It is discharged to 2. The oil / water separation tank 12 has partition plates 19a and 19c that are lowered from the top to the bottom and partition plates 19b and 19d that are standing from the bottom to the top, and the cleaning liquid discharged from the pressure can 1 is first in the rightmost separation chamber. Enter (Room 1). In this separation chamber, the object contained in the cleaning liquid, which is lighter than water, that is, the oil that was the deposit of the carburized and quenched machine parts in the cage 30 rises and the water content drops, so that the object of low specific gravity ( The oil is the upper layer and the water is the lower layer. The cleaning liquid containing less oil in the lower layer flows into the second chamber through the passage below the partition plate 19a. Also in this second chamber, the oil content rises and the water content falls, so that the object (oil) having a low specific gravity becomes the upper layer, and the water becomes the lower layer. The oily cleaning liquid in the upper layer of the second chamber is separated by the partition plate 1
It flows through the passage above 9b into the third chamber. Even in this third chamber, the oil content rises and the water content falls, and objects (oil) with low specific gravity
Is the upper layer, and water is the lower layer. The cleaning liquid containing less oil in the lower layer of the third chamber flows into the fourth chamber through the passage below the partition plate 19c. Also in this fourth chamber, the oil content rises and the water content falls, so that the object (oil) having a low specific gravity becomes the upper layer, and the water content becomes the lower layer. The oil-rich cleaning liquid in the upper layer of the fourth chamber flows into the fifth chamber through the passage above the partition plate 19d. Also in this fifth chamber, the oil content rises and the water content falls, so that an object (oil) having a low specific gravity becomes the upper layer, and the water becomes the lower layer. The cleaning liquid containing a small amount of oil in the lower layer of the fifth chamber is sucked by the electric pump 21 through the filter 20, and is pressurized and injected into the main body 3 through the check valve 22 and the water injection port 6 on the lower bottom of the main body 3. It
In the oil-water separation tank 12 described above, the cleaning liquid discharged from the pressurizing can 1 is separated into water and lighter oil while flowing from the first chamber to the fifth chamber, and most of the oil content is from the first chamber to the first chamber. It stays in 5 chambers, and the upstream chamber has more oil in the upper layer. Then, the cleaning liquid containing the least amount of oil is sucked by the pump 21 and supplied under pressure to the pressure can 1.

【0023】加圧缶1の本体3内には、ケ−ジ30を周
回するようにU字型の蒸気管4が装備されており、これ
らの蒸気管4に、図示しない流量調整弁を介して、加熱
媒体として高温蒸気が供給される。これにより加圧缶1
内の洗浄液が加熱される。加圧缶1の底部には電動撹拌
機5が装備されており、この撹拌スクリュ−が浸炭焼入
れ済の機械部品を入れたケ−ジ30の底面に水流を当て
る。これにより洗浄液は大略で、図1に一点鎖線細線で
示すル−プを描くように流れる。
A U-shaped steam pipe 4 is provided in the main body 3 of the pressurizing can 1 so as to circulate around the cage 30, and these steam pipes 4 are provided with a flow control valve (not shown). Then, high temperature steam is supplied as a heating medium. This enables pressure can 1
The cleaning liquid inside is heated. An electric stirrer 5 is provided at the bottom of the pressure can 1, and this stirring screw applies a water stream to the bottom surface of the cage 30 containing the carburized and quenched mechanical parts. As a result, the cleaning liquid flows in a rough manner and draws a loop indicated by a chain line in FIG.

【0024】加圧缶1には、その内部の洗浄液の温度を
検出する熱電対26および内部圧を検出する圧力計1
0、ならびに異常高圧放出用の安全弁(ブリ−フ弁)9
およびメンテ時排水用の排水弁11が備わっている。次
に、図1に示す洗浄装置の使用態様を説明する。
The pressure can 1 has a thermocouple 26 for detecting the temperature of the cleaning liquid therein and a pressure gauge 1 for detecting the internal pressure.
0, and safety valve for releasing abnormally high pressure (Brief valve) 9
And a drain valve 11 for maintenance drainage is provided. Next, a usage mode of the cleaning apparatus shown in FIG. 1 will be described.

【0025】1.連続循環モ−ド:加圧缶1に浸炭焼入
れ済の機械部品を入れたケ−ジ30を収納したとき洗浄
液面が排水口7aより高いレベルになるに十分な洗浄液
を加圧缶1に入れ、かつ油水分離槽12には、溢流口1
7に至る程度の洗浄液を入れておく。排水弁11,バイ
パス弁24a〜24c,排水弁16,18,排油弁13
および注水弁16はすべて閉じる。電動弁23a〜23
cも閉じる。
1. Continuous circulation mode: When the can 30 containing the carburized and quenched mechanical parts is stored in the pressure can 1, the pressure can 1 is filled with sufficient cleaning liquid so that the cleaning liquid level becomes higher than the drain port 7a. In addition, the oil-water separation tank 12 has an overflow port 1
The washing liquid up to 7 is added. Drain valve 11, bypass valves 24a to 24c, drain valves 16, 18, drain oil valve 13
And all the water injection valves 16 are closed. Motor operated valves 23a-23
Also close c.

【0026】A.機械部品を入れた1つのケ−ジ30を
本体3内に収納し上蓋2を気密に閉じ、クラッチロック
8で上蓋2をロックすると、蒸気管4への高温蒸気の供
給を開始し、撹拌機5を駆動し熱電対26の検出温度お
よび圧力計10の検出圧を監視し、検出温度が設定値以
上になると又は圧力計10の検出圧が設定値以上になる
と、多管ク−ラ25aおよび又は25bへの冷却水の供
給を開始し、電動弁23aおよび又は電動弁23bを開
き、ポンプ21を駆動する。そしてフィ−ドバック制御
により、熱電対26の検出温度が設定範囲となるよう
に、蒸気管4に供給する高温蒸気流量を調節し、圧力計
10の検出圧が設定範囲となるように、ポンプ21の駆
動速度を調節する。電動弁23aおよび又は23bの開
度および多管ク−ラ25aおよび又は25bに供給する
冷却水量は、油水分離槽12にク−ラから排出する洗浄
液が実質上蒸気化しないものに設定および調節する。
A. When one cage 30 containing mechanical parts is housed in the main body 3, the upper lid 2 is airtightly closed, and the upper lid 2 is locked by the clutch lock 8, the supply of high temperature steam to the steam pipe 4 is started, and the stirrer is started. 5 is monitored and the detection temperature of the thermocouple 26 and the detection pressure of the pressure gauge 10 are monitored. When the detection temperature exceeds a set value or the detection pressure of the pressure gauge 10 exceeds the set value, the multi-tube curler 25a and Alternatively, the supply of the cooling water to 25b is started, the electric valve 23a and / or the electric valve 23b is opened, and the pump 21 is driven. Then, by the feedback control, the flow rate of the high temperature steam supplied to the steam pipe 4 is adjusted so that the detected temperature of the thermocouple 26 is within the set range, and the pump 21 is adjusted so that the detected pressure of the pressure gauge 10 is within the set range. Adjust the drive speed of. The opening degree of the motor-operated valves 23a and / or 23b and the amount of cooling water supplied to the multi-tube coolers 25a and / or 25b are set and adjusted so that the cleaning liquid discharged from the coolers into the oil / water separation tank 12 is not substantially vaporized. .

【0027】B.熱電対26の検出温度が設定範囲にあ
り、しかも、圧力計10の検出圧が設定範囲にある状態
で設定時間が経過すると、ポンプ21の駆動速度を下
げ、蒸気管4への高温蒸気の供給を停止し、多管ク−ラ
25a〜25cすべてに冷却水を供給し、電動弁23a
〜23cを、油水分離槽12にク−ラを通して排出する
洗浄液が実質上蒸気化しない開度に開く。そして熱電対
26の検出温度および圧力計10の検出圧を監視し、そ
れらが、上蓋2を開いても加圧缶1内の洗浄液が実質上
蒸気化しないものになるのを待つ。
B. When the set temperature elapses while the detected temperature of the thermocouple 26 is within the set range and the detected pressure of the pressure gauge 10 is within the set range, the driving speed of the pump 21 is reduced to supply the high temperature steam to the steam pipe 4. Stop, supply cooling water to all the multi-tube coolers 25a to 25c, and operate the motor-operated valve 23a.
˜23c is opened to an opening such that the cleaning liquid discharged through the cooler into the oil / water separation tank 12 is not substantially vaporized. Then, the temperature detected by the thermocouple 26 and the pressure detected by the pressure gauge 10 are monitored, and they are waited until the cleaning liquid in the pressure can 1 is not substantially vaporized even when the upper lid 2 is opened.

【0028】C.熱電対26の検出温度および圧力計1
0の検出圧が、上蓋2を開いても加圧缶1内の洗浄液が
実質上蒸気化しないものになると、ポンプ21および撹
拌機5を停止し、電動弁23a〜23cを閉じ、多管ク
−ラ25a〜25cへの冷却水の供給を停止する。な
お、多管ク−ラ25a〜25cの冷却水供給は必ずしも
停止する必要はない。そしてクラッチロック8を解除
し、上蓋2を開いて、ケ−ジ30を取り出す。
C. Temperature detected by thermocouple 26 and pressure gauge 1
When the detected pressure of 0 is such that the cleaning liquid in the pressurizing can 1 is not substantially vaporized even when the upper lid 2 is opened, the pump 21 and the agitator 5 are stopped, the motor operated valves 23a to 23c are closed, and the multi-tube claw is closed. -Stop the supply of cooling water to the la 25a to 25c. The cooling water supply to the multi-tube coolers 25a to 25c does not necessarily have to be stopped. Then, the clutch lock 8 is released, the upper lid 2 is opened, and the cage 30 is taken out.

【0029】そして代りに、未洗浄の機械部品を入れた
1つのケ−ジ30を本体3内に収納する。以下上述の
A.〜C.を繰返す。油水分離槽12内の回収油分があ
る程度になると、排油弁14を開いて油水分離槽12の
第1室(最右室)の上層液を回収する。油水分離槽12
の液面レベルが下がると注水弁16を開いて水を補充
し、水系洗浄剤を用いるときには、補充水量に見合う水
系洗浄剤を槽12内に投入する。なお、洗浄液中の油分
濃度あるいは水系洗浄剤濃度を下げるときには、注水弁
16を開いて油水分離槽12に水を補充し排油弁14お
よび排水弁18を開いて槽12内の過剰洗浄液を回収す
る。また槽12内のスラッジ(泥状物)は排水弁16を
開いて回収する。
Instead, one cage 30 containing unwashed machine parts is housed in the main body 3. Hereinafter, the above A. ~ C. Repeat. When the amount of recovered oil in the oil / water separation tank 12 reaches a certain level, the oil discharge valve 14 is opened to recover the upper layer liquid of the first chamber (rightmost chamber) of the oil / water separation tank 12. Oil-water separation tank 12
When the liquid level decreases, the water injection valve 16 is opened to replenish the water, and when the water-based cleaning agent is used, the water-based cleaning agent corresponding to the amount of replenished water is put into the tank 12. When lowering the oil concentration or the water-based detergent concentration in the cleaning liquid, the water injection valve 16 is opened to replenish the oil / water separation tank 12 with water, and the drain valve 14 and the drain valve 18 are opened to recover the excess cleaning liquid in the tank 12. To do. The sludge (mud matter) in the tank 12 is collected by opening the drain valve 16.

【0030】以上に説明した連続循環モ−ドの操業の場
合には、洗浄液が油水分離槽12→加圧缶1→ク−ラ2
5a等→油水分離槽12と循環し、加圧缶1内で洗浄液
が加熱され被洗浄物に付着した油の粘度が大きく低下し
て(表1参照)流動化し、洗浄液に混じって加圧缶1か
ら出る。すなわち効率的な付着物洗浄が実現する。加圧
缶1から出た洗浄液がク−ラ25a等で冷却されるの
で、油水分離槽12で洗浄液の蒸気化が実質上なくしか
も洗浄液に混じった油の粘度が上昇し、油水分離が効率
的に実現する。油分の気化による大気への逃散を実質上
生じない。洗浄が終わり加圧缶1から出された被洗浄物
の温度は比較的に高く、そのまま放置することにより洗
浄液(水分)が被洗浄物より気化して逃げるので、水系
洗浄剤を用いない場合や、用いても微量で残留が問題な
い場合には、格別な乾燥工程を要しない。
In the operation of the continuous circulation mode described above, the cleaning liquid is an oil / water separation tank 12 → pressurized can 1 → curler 2.
5a, etc. → Circulates with the oil / water separation tank 12, the cleaning liquid is heated in the pressure can 1 and the viscosity of the oil adhering to the object to be cleaned is greatly reduced (see Table 1), fluidizes, and mixes with the cleaning liquid to pressurize the can. Get out of 1. That is, efficient cleaning of adhered substances is realized. Since the cleaning liquid discharged from the pressurizing can 1 is cooled by the cooler 25a or the like, the cleaning liquid is substantially not vaporized in the oil / water separation tank 12, and the viscosity of the oil mixed with the cleaning liquid is increased, so that the oil / water separation is efficient. Will be realized. Virtually no escape to the atmosphere due to oil vaporization. After cleaning, the temperature of the object to be cleaned discharged from the pressure can 1 is relatively high, and if left as it is, the cleaning liquid (water) vaporizes and escapes from the object to be cleaned. If a small amount remains even when used, no special drying step is required.

【0031】2.注入/排出切換えモ−ド:加圧缶1内
には洗浄液は実質上ないが、油水分離槽12には、溢流
口17に達する程度の洗浄液を入れておく。排水弁1
1,バイパス弁24a〜24c,排水弁16,18,排
油弁13および注水弁16はすべて閉じる。電動弁23
a〜23cも閉じる。
2. Injection / discharge switching mode: There is substantially no cleaning liquid in the pressurizing can 1, but the oil-water separation tank 12 contains a cleaning liquid that reaches the overflow port 17. Drain valve 1
1, the bypass valves 24a to 24c, the drain valves 16 and 18, the oil discharge valve 13 and the water injection valve 16 are all closed. Motorized valve 23
Also, a to 23c are closed.

【0032】a.機械部品を入れた1つのケ−ジ30を
本体3内に収納し上蓋2を気密に閉じ、クラッチロック
8で上蓋2をロックすると、ポンプ21を駆動して、排
水口7aのレベル(ケ−ジ30内部品はすべて洗浄液に
浸る)あるいはそれ以上のレベルまで、加圧缶1内に洗
浄液を供給する。そしてポンプ21を停止する。次に、
蒸気管4への高温蒸気の供給を開始し、撹拌機5を駆動
し熱電対26の検出温度および圧力計10の検出圧を監
視し、フィ−ドバック制御により、熱電対26の検出温
度が設定範囲となり圧力計10の検出圧が設定範囲とな
るように、蒸気管4に供給する高温蒸気流量を調節す
る。
A. When one cage 30 containing mechanical parts is housed in the main body 3 and the upper lid 2 is airtightly closed, and the upper lid 2 is locked by the clutch lock 8, the pump 21 is driven and the level of the drainage port 7a (case). The parts inside the container 30 are immersed in the cleaning liquid) or higher, and the cleaning liquid is supplied into the pressure can 1. Then, the pump 21 is stopped. next,
The supply of high temperature steam to the steam pipe 4 is started, the stirrer 5 is driven, the temperature detected by the thermocouple 26 and the pressure detected by the pressure gauge 10 are monitored, and the temperature detected by the thermocouple 26 is set by feedback control. The flow rate of the high temperature steam supplied to the steam pipe 4 is adjusted so that the pressure becomes a range and the detection pressure of the pressure gauge 10 becomes a set range.

【0033】b.熱電対26の検出温度が設定範囲にあ
り、しかも、圧力計10の検出圧が設定範囲にある状態
で設定時間が経過すると、撹拌機5を停止し、蒸気管4
への高温蒸気の供給を停止し、ク−ラ25aおよび25
bに冷却水を供給し電動弁23aおよび23bを、ク−
ラから油水分離槽12に排出される洗浄液が実質上蒸気
化しない開度に開く。そして圧力計10の圧力を監視し
て圧力が大気圧近くの設定圧に低下するとポンプ21を
低速駆動する。そして熱電対26の検出温度および圧力
計10の検出圧を監視して、圧力が該設定圧を越えない
範囲でポンプ21を加速し、熱電対26の検出温度が、
大気圧で洗浄液が実質上蒸気化しない温度になるとポン
プ21を停止し、多管ク−ラ25cに冷却水を供給し電
動弁23cを全開とする。
B. When the set temperature elapses while the detected temperature of the thermocouple 26 is within the set range and the detected pressure of the pressure gauge 10 is within the set range, the stirrer 5 is stopped and the steam pipe 4
To stop the supply of high temperature steam to the coolers 25a and 25a.
b to supply cooling water to the motor-operated valves 23a and 23b.
The cleaning liquid discharged from the tank to the oil / water separation tank 12 is opened to an opening that does not substantially vaporize. Then, the pressure of the pressure gauge 10 is monitored, and when the pressure drops to a set pressure near atmospheric pressure, the pump 21 is driven at a low speed. Then, the temperature detected by the thermocouple 26 and the pressure detected by the pressure gauge 10 are monitored, the pump 21 is accelerated within a range in which the pressure does not exceed the set pressure, and the temperature detected by the thermocouple 26 becomes
When the temperature reaches a temperature at which the cleaning liquid does not substantially vaporize under atmospheric pressure, the pump 21 is stopped, cooling water is supplied to the multi-tube cooler 25c, and the electric valve 23c is fully opened.

【0034】c.加圧缶1内の洗浄液面がケ−ジ30の
下底以下に下がったタイミングで、多管ク−ラ25a〜
25cへの冷却水の供給を停止し、電動弁23a〜23
cを閉じる。そしてクラッチロック8を解除し、上蓋2
を開いて、ケ−ジ30を取り出す。
C. When the level of the cleaning liquid in the pressure can 1 drops below the lower bottom of the cage 30, the multi-tube cooler 25a ...
Supply of cooling water to 25c is stopped, and motor operated valves 23a-23
Close c. Then, the clutch lock 8 is released, and the upper lid 2
Open and take out the cage 30.

【0035】そして代りに、未洗浄の機械部品を入れた
1つのケ−ジ30を本体3内に収納する。以下上述の
a.〜c.を繰返す。油水分離槽12内の回収油分があ
る程度になると、前記c.の段階で排油弁14を開いて
油水分離槽12の第1室(最右室)の上層液を回収す
る。油水分離槽12の液面レベルが下がると注水弁16
を開いて水を補充し、水系洗浄剤を用いるときには、補
充水量に見合う水系洗浄剤を槽12内に投入する。な
お、洗浄液中の油分濃度あるいは水系洗浄剤濃度を下げ
るときには、注水弁16を開いて油水分離槽12に水を
補充し排油弁14および排水弁18を開いて槽12内の
過剰洗浄液を回収する。また槽12内のスラッジ(泥状
物)は排水弁16を開いて回収する。
Instead, one cage 30 containing uncleaned mechanical parts is housed in the main body 3. The above a. ~ C. Repeat. When the amount of recovered oil in the oil / water separation tank 12 reaches a certain level, the c. At the stage of, the oil discharge valve 14 is opened to collect the upper layer liquid of the first chamber (rightmost chamber) of the oil / water separation tank 12. Water injection valve 16 when the liquid level in the oil / water separation tank 12 decreases
Is opened to replenish water, and when a water-based cleaning agent is used, the water-based cleaning agent corresponding to the amount of replenished water is put into the tank 12. When lowering the oil concentration or the water-based detergent concentration in the cleaning liquid, the water injection valve 16 is opened to replenish the oil / water separation tank 12 with water, and the drain valve 14 and the drain valve 18 are opened to recover the excess cleaning liquid in the tank 12. To do. The sludge (mud matter) in the tank 12 is collected by opening the drain valve 16.

【0036】以上に説明した注入/排出切換えモ−ドの
操業の場合には、加圧缶1に被洗浄物を入れると加圧缶
1に油水分離槽12の洗浄液が供給される。そして洗浄
液の循環は停止したまま加圧缶1内の洗浄液の所定条件
の加圧加熱が維持される。所定時間の加圧加熱が終わる
と、加熱を停止し、熱電対26の検出温度が大気圧で洗
浄液が実質上蒸気化しない温度になるまで、油水分離槽
12の洗浄液(低温)が加圧缶1に供給されこれに伴っ
て加圧缶1の洗浄液(高温)が排出される。この排出は
上部排水口7a,7bで行なわれるので、加圧缶1の、
洗浄に使用された液は、上層のもの(温度が高く、油分
が多い)から、ク−ラを介して油水分離槽12に排出さ
れる。熱電対26の検出温度が大気圧で洗浄液が実質上
蒸気化しない温度になると加圧缶1への洗浄液供給が停
止され、電動弁23cが開かれて、加圧缶1の洗浄液
が、下部位置の排水口7cを通して油水分離槽12に抜
かれる。 この注入/排出切換えモ−ドでも、加圧缶1
内で洗浄液が加熱され被洗浄物に付着した油の粘度が大
きく低下して(表1参照)流動化し洗浄液に混じって、
最終的には加圧缶1から出る。すなわち効率的な付着物
洗浄が実現する。加圧缶1から出た洗浄液がク−ラ25
a等で冷却されるので、油水分離槽12で洗浄液の蒸気
化が実質上なくしかも洗浄液に混じた油の粘度が上昇
し、油水分離が効率的に実現する。油分の気化による大
気への逃散を実質上生じない。洗浄が終わり加圧缶1か
ら出された被洗浄物の温度は比較的に高く、そのまま放
置することにより洗浄液(水分)が被洗浄物より気化し
て逃げるので、水系洗浄剤を用いない場合や、用いても
微量で残留が問題ない場合には、格別な乾燥工程を要し
ない。
In the operation of the injection / discharge switching mode described above, when the object to be cleaned is put into the pressure can 1, the cleaning liquid in the oil / water separation tank 12 is supplied to the pressure can 1. Then, while the circulation of the cleaning liquid is stopped, pressurization and heating of the cleaning liquid in the pressure can 1 under a predetermined condition are maintained. When the heating under pressure for a predetermined time is completed, the heating is stopped, and the cleaning liquid (low temperature) in the oil / water separation tank 12 is pressurized until the temperature detected by the thermocouple 26 reaches a temperature at which atmospheric pressure does not substantially vaporize the cleaning liquid. 1 and the cleaning liquid (high temperature) for the pressure can 1 is discharged accordingly. Since this discharge is performed at the upper drain ports 7a and 7b,
The liquid used for cleaning is discharged from the upper layer (having a high temperature and a large amount of oil) to the oil / water separation tank 12 via the cooler. When the temperature detected by the thermocouple 26 is atmospheric pressure and the temperature at which the cleaning liquid does not substantially vaporize, the supply of the cleaning liquid to the pressurizing can 1 is stopped, the electric valve 23c is opened, and the cleaning liquid in the pressurizing can 1 is at the lower position. Is drained to the oil / water separation tank 12 through the drainage port 7c. Even in this injection / discharge switching mode, the pressure can 1
When the cleaning liquid is heated inside, the viscosity of the oil adhering to the object to be cleaned greatly decreases (see Table 1) and fluidizes and mixes with the cleaning liquid,
Finally, the pressure can 1 exits. That is, efficient cleaning of adhered substances is realized. The cleaning liquid discharged from the pressure can 1 is cooler 25.
Since it is cooled by a or the like, the cleaning liquid is substantially not vaporized in the oil / water separation tank 12, the viscosity of the oil mixed in the cleaning liquid is increased, and the oil / water separation is efficiently realized. Virtually no escape to the atmosphere due to oil vaporization. After cleaning, the temperature of the object to be cleaned discharged from the pressure can 1 is relatively high, and if left as it is, the cleaning liquid (water) vaporizes and escapes from the object to be cleaned. If a small amount remains even when used, no special drying step is required.

【0037】なお、以上に説明した、加圧缶1への洗浄
液の充填,加圧加熱および加圧缶1よりの洗浄液の排出
は、同一被洗浄物に対して数回繰返して行ってもよい。
また、上述の連続循環モ−ドと注入/排出切換えモ−ド
を、同一被洗浄物に対して組合せて実行してもよい。
The filling of the cleaning liquid in the pressure can 1, the heating under pressure, and the discharge of the cleaning liquid from the pressure can 1 described above may be repeated several times for the same object to be cleaned. .
Further, the above-mentioned continuous circulation mode and injection / discharge switching mode may be combined for the same object to be cleaned.

【0038】次に上述の洗浄装置による洗浄効果を説明
する。洗浄液を水のみならびに0.1〜0.2%のカ性ソ−ダ
水溶液とし、洗浄温度(熱電対26による検出温度)を
90〜150℃として、上記a.での定常状態の加圧加熱を
20分間行なった結果、図2に黒丸で示す洗浄効果があ
った。圧力計10による検出圧は0.5〜3.0Kg/cm2であ
る。また、洗浄液を0.5〜0.8%のカ性ソ−ダ水溶液と
し、他は同一条件で洗浄を行なった結果を、図2に白丸
で示す。これらの結果より、洗浄液を水のみならびに0.
1〜0.2%のカ性ソ−ダ水溶液とした場合には、略110〜1
50℃で優れた洗浄効果があることが分かる。洗浄液を0.
5〜0.8%のカ性ソ−ダ水溶液とした場合には、80℃以上
で優れた洗浄効果があることが分かる。なお、上記A.
での定常状態の加圧加熱を20分間行なっても同様な、
もしくはそれ以上の効果が得られる。
Next, the cleaning effect of the above cleaning device will be described. As the cleaning liquid, only water and 0.1 to 0.2% aqueous solution of caustic soda are used, and the cleaning temperature (the temperature detected by the thermocouple 26) is set to
90 to 150 ° C., the above a. As a result of performing pressure heating in a steady state for 20 minutes, there was a cleaning effect shown by a black circle in FIG. The pressure detected by the pressure gauge 10 is 0.5 to 3.0 Kg / cm 2 . In addition, the results obtained by performing the washing under the same conditions except that the washing solution was a 0.5 to 0.8% aqueous solution of caustic soda are shown by white circles in FIG. Based on these results, the cleaning solution was water only and 0.
In the case of 1-0.2% aqueous solution of caustic soda, approximately 110-1
It can be seen that there is an excellent cleaning effect at 50 ° C. Wash solution to 0.
It can be seen that when the aqueous solution of caustic soda of 5 to 0.8% is used, an excellent cleaning effect is obtained at 80 ° C or higher. In addition, the above A.
Even if the steady-state pressure heating at 20 minutes is performed,
Or more effect can be obtained.

【0039】[0039]

【発明の効果】図3に従来の洗浄方法による洗浄効果
(白ブロック)と、上述の本発明の洗浄装置による洗浄
効果(斜線ブロック)とを示す。従来のアルカリ洗浄で
は濃度3〜5%のカ性ソ−ダ水溶液が用いられるが、本
発明によれば、低濃度で優れた洗浄効果が得られる。本
発明では、洗浄液が、水もしくは水に極少量の水系洗浄
剤を添加したものであるために、洗浄剤の濃度管理が楽
であり、管理の繁雑さ、コスト面でも改善される。加圧
容器(1)内の洗浄液を、容器外に排出して容器外で冷却
して比重差により洗浄液より付着物を分離した後、加圧
容器(1)に再供給するので、洗浄液の消費が少く、洗浄
廃棄物は実質上付着物であって少量であるので、洗浄廃
棄物の廃棄処理が容易である。
FIG. 3 shows the cleaning effect by the conventional cleaning method (white block) and the cleaning effect by the above-described cleaning apparatus of the present invention (shaded block). In the conventional alkaline cleaning, a caustic soda aqueous solution having a concentration of 3 to 5% is used, but according to the present invention, an excellent cleaning effect can be obtained at a low concentration. In the present invention, since the cleaning liquid is water or a very small amount of an aqueous cleaning agent added to water, it is easy to control the concentration of the cleaning agent, and management complexity and cost are also improved. Pressurization
The cleaning liquid in the container (1) is discharged outside the container and cooled outside the container.
After separating the adhering substances from the cleaning liquid by the difference in specific gravity, pressurize
As it is re-supplied to the container (1), the consumption of cleaning liquid is low and cleaning is possible.
Since the waste is practically a deposit and a small amount, it can be washed and discarded.
Disposal of waste is easy.

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

【図1】 本発明装置の一実施例を示すブロック図であ
る。
FIG. 1 is a block diagram showing an embodiment of a device of the present invention.

【図2】 図1に示す洗浄装置を用いた洗浄結果を示す
グラフである。
FIG. 2 is a graph showing cleaning results using the cleaning device shown in FIG.

【図3】 従来の洗浄方法による残留油分量分布と、図
1に示す洗浄装置を用いた洗浄による残留油分量分布を
示すグラフである。
FIG. 3 is a graph showing a distribution of residual oil content by a conventional cleaning method and a distribution of residual oil content by cleaning using the cleaning apparatus shown in FIG.

【符号の説明】[Explanation of symbols]

1:加圧缶(加圧容器) 2:上蓋 3:本体 4:蒸気管(加熱手
段) 5:撹拌機(撹拌手段) 6:注水口(注水
口) 7a,7c:排水口 8:クラッチロック 9:安全弁 10:圧力計(圧力
センサ) 11:排水弁 12:油水分離槽
(付着物分離槽) 13:排油口 14:排油弁 15:排水口 16:排水弁 17:溢流口 18:排水弁 19a〜19d:仕切板 20:フィルタ 21:ポンプ 22:逆止弁 23a〜23c:電動弁 24a〜24b:バ
イパス弁 25a〜25c:多管ク−ラ(冷却装置) 26:熱電対(温度センサ) 30:被洗浄物を入
れたケ−ジ
1: Pressurized can (pressurized container) 2: Upper lid 3: Main body 4: Steam pipe (heating means) 5: Stirrer (stirring means) 6: Water injection port (water injection port) 7a, 7c: Drain port 8: Clutch lock 9: Safety valve 10: Pressure gauge (pressure sensor) 11: Drain valve 12: Oil-water separation tank (sediment separation tank) 13: Oil drain port 14: Oil drain valve 15: Drain port 16: Drain valve 17: Overflow port 18 : Drain valve 19a to 19d: Partition plate 20: Filter 21: Pump 22: Check valve 23a to 23c: Electric valve 24a to 24b: Bypass valve 25a to 25c: Multi-tube cooler (cooling device) 26: Thermocouple ( Temperature sensor) 30: A cage containing an object to be cleaned

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】加圧容器内に被洗浄物および水もしくは水
に水系洗浄剤を配合した洗浄液を入れて洗浄液を加熱
し、加圧容器内圧力を0.5Kg/cm2以上3Kg/cm2以下に、洗
浄液温度を加圧容器内圧では洗浄液が実質上気化しない
80℃〜130℃の温度に維持して、高温高圧洗浄液により
それに浸漬した被洗浄物の付着物を洗浄し、加圧容器内
の洗浄液を、容器外に排出して容器外で冷却して比重差
により洗浄液より付着物を分離した後、加圧容器に再供
する加圧式洗浄方法。
1. A washload and the water or water putting a cleaning liquid formulated with an aqueous cleaning agent by heating the washing liquid in a pressurized vessel, the pressure vessel internal pressure 0.5 Kg / cm 2 or more 3 Kg / cm 2 or less In addition, the cleaning liquid temperature does not substantially evaporate when the pressure in the pressure vessel is increased.
Maintained at a temperature of 80 ° C. to 130 DEG ° C., washed deposits the cleaning object immersed in it by high temperature and high pressure cleaning liquid, pressurized container
Drain the cleaning liquid from outside the container and cool it outside the container to determine the difference in specific gravity.
After separating the adhered substances from the cleaning liquid by
Pressure cleaning method to supply .
【請求項2】注水口および排水口を有する、被洗浄物を
収容する加圧容器; 被洗浄物に付着していた付着物が含まれる、水もしくは
水に水系洗浄剤を配合した洗浄液より、比重差により付
着物を分離する付着物分離槽; 前記加圧容器の排水口から前記付着物分離槽に流れる洗
浄液を冷却する冷却装置; 前記付着物分離槽で付着物が分離された洗浄液を、前記
加圧容器の注水口に供給するポンプ; 前記加圧容器内の洗浄液を加熱する加熱手段; 加圧容器内の洗浄液の温度を検出する温度センサ;およ
び、 加圧容器内の圧力を検出する圧力センサ; を備える加圧式洗浄装置。
2. A pressurizing container having a water injection port and a drain port for accommodating an object to be cleaned; water containing an adhering material adhering to the object to be cleaned; An adherent separation tank for separating adherents by a difference in specific gravity; a cooling device for cooling the cleaning liquid flowing from the drainage port of the pressure vessel to the adherent separation tank; a cleaning liquid in which the adherents are separated in the adherent separation tank, A pump for supplying water to the water inlet of the pressurized container; a heating unit for heating the cleaning liquid in the pressurized container; a temperature sensor for detecting the temperature of the cleaning liquid in the pressurized container; and a pressure in the pressurized container. A pressure type cleaning device including a pressure sensor.
JP4271371A 1992-10-09 1992-10-09 Pressure washing device Expired - Lifetime JPH0741199B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4271371A JPH0741199B2 (en) 1992-10-09 1992-10-09 Pressure washing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4271371A JPH0741199B2 (en) 1992-10-09 1992-10-09 Pressure washing device

Publications (2)

Publication Number Publication Date
JPH06121962A JPH06121962A (en) 1994-05-06
JPH0741199B2 true JPH0741199B2 (en) 1995-05-10

Family

ID=17499142

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4271371A Expired - Lifetime JPH0741199B2 (en) 1992-10-09 1992-10-09 Pressure washing device

Country Status (1)

Country Link
JP (1) JPH0741199B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8616283B2 (en) * 2009-12-11 2013-12-31 E I Du Pont De Nemours And Company Process for treating water in heavy oil production using coated heat exchange units
JP5929294B2 (en) * 2012-02-21 2016-06-01 エコ・アース・エンジニアリング株式会社 Tantalum recovery method
CN108499967A (en) * 2018-05-25 2018-09-07 江苏亨通光纤科技有限公司 Optical fiber coating die cleaning device and clean method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02303584A (en) * 1989-05-15 1990-12-17 Furuno Electric Co Ltd Method and device for ultrasonic cleaning

Also Published As

Publication number Publication date
JPH06121962A (en) 1994-05-06

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