JPH0975875A - Cleaning device for processed product - Google Patents

Cleaning device for processed product

Info

Publication number
JPH0975875A
JPH0975875A JP23029195A JP23029195A JPH0975875A JP H0975875 A JPH0975875 A JP H0975875A JP 23029195 A JP23029195 A JP 23029195A JP 23029195 A JP23029195 A JP 23029195A JP H0975875 A JPH0975875 A JP H0975875A
Authority
JP
Japan
Prior art keywords
oil
cleaning
cleaning liquid
filter
ultrafiltration membrane
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP23029195A
Other languages
Japanese (ja)
Inventor
Toshihide Fujii
敏秀 藤井
Mitsunobu Nomura
充延 野村
Masayuki Hosoda
将之 細田
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP23029195A priority Critical patent/JPH0975875A/en
Publication of JPH0975875A publication Critical patent/JPH0975875A/en
Pending legal-status Critical Current

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  • Cleaning By Liquid Or Steam (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a cleaning device for processed products for separating unnecessary solid matters, oil and the like contained in a cleaning fluid in a good manner. SOLUTION: In a cleaning device for processed products comprising a cleaning tank 11 filled with a cleaning fluid for processed products, a filter device 13 for separating solid matters from the fluid overflowing the cleaning tank 11 and an oil-water separation device 15 for separating oil from the cleaning fluid overflowing the cleaning tank 11, a bag filter is utilized as the filter device 13, and an ultrafiltration film device is utilized as the oil-water separation device 15.

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】本発明は、ブラウン管用の電
子銃部品などのように例えばプレス加工した加工部品を
洗浄する加工部品の洗浄装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for cleaning a processed part, such as an electron gun part for a cathode ray tube, which cleans, for example, a pressed processed part.

【0002】[0002]

【従来の技術】プレス加工などをした加工部品を洗浄す
る従来の加工部品の洗浄装置は、次のように構成されて
いる。
2. Description of the Related Art A conventional machined part cleaning apparatus for cleaning a machined part that has undergone press working is constructed as follows.

【0003】例えば、洗浄液が注入された洗浄槽におい
て加工部品が洗浄される構成になっている。そして、洗
浄槽からオーバフローした洗浄液はフィルタ装置に送ら
れる。フィルタ装置では、プレス磨耗によって発生した
金属粉などのような固形物のゴミが除去される。また、
固形物のゴミが除去された洗浄液は油水分離装置に送ら
れ、洗浄液に溶け込んでいる油が分離される。このよう
にしてゴミが除去され、また、油が分離された洗浄液は
再生洗浄液として洗浄槽に戻される。なお、油水分離装
置で分離された油は廃液として処分される。
For example, the processed parts are cleaned in a cleaning tank filled with a cleaning liquid. Then, the cleaning liquid overflowing from the cleaning tank is sent to the filter device. In the filter device, solid dust such as metal powder generated by press wear is removed. Also,
The cleaning liquid from which the solid dust has been removed is sent to the oil / water separation device, and the oil dissolved in the cleaning liquid is separated. Thus, the cleaning liquid from which dust has been removed and the oil has been separated is returned to the cleaning tank as a regenerated cleaning liquid. The oil separated by the oil / water separator is disposed of as a waste liquid.

【0004】[0004]

【発明が解決しようとする課題】ところで、上記した構
成の加工部品の洗浄装置では、フィルタ装置として糸巻
きフィルタが使用されている。糸巻きフィルタは、多数
の孔が形成された芯に繊維または樹脂の細い糸を綾目状
に巻き付けた構造になっている。プレス加工部品の洗浄
装置に糸巻きフィルタを使用した場合、洗浄剤(界面活
性剤)や油に混ざり合った固形物のゴミがポンプの圧力
で押され、綾目状に巻かれた糸を広げるように作用し、
ゴミがすり抜けてしまう。このため、固形物が十分に除
去されない。このような場合、糸巻きフィルタの糸が広
がらないように、例えばポンプの圧力を下げることが考
えられる。しかし、ポンプの圧力を下げると洗浄液の流
れが弱くなり、フィルタとしての効果がなくなってしま
う。
By the way, in the apparatus for cleaning a processed component having the above-mentioned structure, a wound filter is used as a filter device. The thread winding filter has a structure in which a thin thread of fiber or resin is wound around a core in which a large number of holes are formed. When a thread winding filter is used in the washing device for pressed parts, solid dust mixed with detergent (surfactant) or oil is pushed by the pressure of the pump to spread the thread wound in a twill pattern. Acts on
Garbage slips through. Therefore, the solid matter is not sufficiently removed. In such a case, for example, the pressure of the pump may be lowered so that the yarn of the wound filter does not spread. However, if the pressure of the pump is lowered, the flow of the cleaning liquid becomes weak and the effect as a filter is lost.

【0005】また、油水分離装置としては、通常、樹脂
吸着方式が用いられる。樹脂吸着方式は、多数の米粒大
のポリプロピレンの集団の中に、油が混入した洗浄液を
通す構成で、ポリプロピレン粒に油を吸着させ洗浄液と
油を分離する方法である。この場合、洗浄液と油の分離
には、油と水の比重差を利用した、いわゆる比重分離方
式が採用される。
A resin adsorption system is usually used as the oil-water separator. The resin adsorption method is a method in which a cleaning liquid mixed with oil is passed through a large population of rice grain-sized polypropylene, and the oil is adsorbed to the polypropylene particles to separate the cleaning liquid and the oil. In this case, a so-called specific gravity separation method, which utilizes the difference in specific gravity of oil and water, is adopted for the separation of the cleaning liquid and the oil.

【0006】例えば、ポリプロピレン粒に吸着した油の
粒子は順次粗大化していく。そして、粗大化した油の粒
子が、最終的に、ポリプロピレン粒から分離し浮上する
ことになる。このような樹脂吸着方式は、分離する油と
洗浄液との間に大きな比重差が必要とされる。
For example, oil particles adsorbed on polypropylene particles are gradually coarsened. Then, the coarsened oil particles finally separate from the polypropylene particles and float. In such a resin adsorption method, a large difference in specific gravity is required between the oil to be separated and the cleaning liquid.

【0007】したがって、加工部品を洗浄する洗浄装置
の場合、油水分離装置として樹脂吸着方式を利用する
と、次のような問題がある。
Therefore, in the case of the cleaning device for cleaning the processed parts, if the resin adsorption method is used as the oil / water separating device, there are the following problems.

【0008】1)プレス加工の深絞りに使用される加工
油は極圧添加剤として塩素を含み、比重が1〜1.1と
洗浄液に近く、比重差を利用した分離が難しい。
1) The processing oil used for deep drawing in press working contains chlorine as an extreme pressure additive and has a specific gravity of 1 to 1.1, which is close to that of a cleaning liquid, and separation using the difference in specific gravity is difficult.

【0009】2)プレス強加工の際に表面に付着した潤
滑油膜はアルカリ洗浄剤のケン化作用だけでは取りきれ
ない。このため、可溶化作用のある界面活性剤を洗浄液
に含ませている。この場合、除去された油が界面活性剤
によって洗浄液に溶け込み、乳化し、エマルジョンとな
る。エマルジョンは洗浄液と油が一体化したものであ
り、樹脂吸着方式によって油を除去することが困難にな
る。
2) The lubricating oil film adhering to the surface during the press-hardening cannot be removed only by the saponification action of the alkaline detergent. Therefore, the cleaning liquid contains a surfactant having a solubilizing effect. In this case, the removed oil is dissolved in the cleaning liquid by the surfactant and emulsified to form an emulsion. Emulsion is a combination of cleaning liquid and oil, and it becomes difficult to remove oil by the resin adsorption method.

【0010】本発明は、上記した欠点を解決するもの
で、洗浄液に含まれる不要な固形物や油などを良好に分
離できる加工部品の洗浄装置を提供することを目的とす
る。
The present invention solves the above-mentioned drawbacks, and an object of the present invention is to provide a cleaning device for machined parts which can favorably separate unnecessary solids, oils and the like contained in the cleaning liquid.

【0011】[0011]

【課題を解決するための手段】本発明は、加工部品を洗
浄する洗浄液が注入された洗浄槽と、この洗浄槽からオ
ーバフローした洗浄液の中から固形物を分離するフィル
タ装置と、前記洗浄槽からオーバフローした洗浄液の中
から油を分離する油水分離装置とを具備した加工部品の
洗浄装置において、前記フィルタ装置としてバッグフィ
ルタを利用し、前記油水分離装置として限外ろ過膜装置
を利用している。
According to the present invention, there is provided a cleaning tank in which a cleaning liquid for cleaning a processed part is injected, a filter device for separating solids from the cleaning liquid overflowing from the cleaning tank, and the cleaning tank. In a cleaning device for a processed part, which includes an oil / water separator for separating oil from overflowed cleaning liquid, a bag filter is used as the filter device, and an ultrafiltration membrane device is used as the oil / water separator.

【0012】また、バッグフィルタが限外ろ過膜装置の
前段に位置している。
Further, the bag filter is located upstream of the ultrafiltration membrane device.

【0013】上記した構成によれば、固形物のゴミを分
離するフィルタ装置としてバッグフィルタを利用してい
る。バッグフィルタは多層構造であるため、流量が多い
状態でも、また圧力が高い状態でもゴミを保持する能力
が高く、ゴミの除去性能が向上する。
According to the above construction, the bag filter is used as the filter device for separating the solid dust. Since the bag filter has a multi-layered structure, it has a high ability to retain dust even when the flow rate is high and the pressure is high, and the dust removal performance is improved.

【0014】また、油水分離装置として限外ろ過膜装置
を利用している。限外ろ過膜装置は、水は通すが油や固
形分は通さない特殊な膜を使用している。この装置は、
油と洗浄液の比重差を利用する方式でないので、油と洗
浄液の分離性能が向上する。
An ultrafiltration membrane device is used as an oil / water separator. The ultrafiltration membrane device uses a special membrane that allows water to pass but not oil or solids. This device is
Since the method does not utilize the difference in specific gravity between the oil and the cleaning liquid, the separation performance between the oil and the cleaning liquid improves.

【0015】なお、限外ろ過膜装置は、油以外の固形分
例えばゴミなどを保持する機能を持っているが、ゴミな
どが付着すると寿命が短くなる。したがって、限外ろ過
膜装置をバッグフィルタの後に接続する構成にした方
が、限外ろ過膜装置の寿命を長くできる。
The ultrafiltration membrane device has a function of holding solids other than oil, such as dust, but if dust or the like adheres, the service life will be shortened. Therefore, the life of the ultrafiltration membrane device can be extended by connecting the ultrafiltration membrane device after the bag filter.

【0016】[0016]

【発明の実施の形態】本発明の実施の形態について図1
を参照して説明する。
BEST MODE FOR CARRYING OUT THE INVENTION FIG. 1 shows an embodiment of the present invention.
This will be described with reference to FIG.

【0017】11は洗浄槽で、加工部品を洗浄する洗浄
液が洗浄槽11内に注入されている。また、洗浄槽11
からオーバフローした洗浄液は中間貯蔵槽12に送られ
る。中間貯蔵槽12に送られた洗浄液はフィルタ装置1
3に通される。フィルタ装置13において、プレス磨耗
で発生した金属粉など固形物のゴミが除去される。固形
物のゴミが除去された洗浄液は、ポンプ14で油水分離
装置15に送られる。油水分離装置15では、洗浄液に
溶け込んでいる油が洗浄液から分離される。また、油が
分離された洗浄液は再生洗浄液として矢印Y1のように
洗浄槽11に戻される。なお、油水分離装置15で分離
された油は矢印Y2のように廃液として外部に送られ処
分される。
Reference numeral 11 is a cleaning tank, and a cleaning liquid for cleaning the processed parts is injected into the cleaning tank 11. Also, the cleaning tank 11
The cleaning liquid overflowing from is sent to the intermediate storage tank 12. The cleaning liquid sent to the intermediate storage tank 12 is the filter device 1
Passed through 3. In the filter device 13, solid dust such as metal powder generated by press wear is removed. The cleaning liquid from which the solid dust has been removed is sent to the oil / water separator 15 by the pump 14. In the oil / water separator 15, the oil dissolved in the cleaning liquid is separated from the cleaning liquid. Further, the cleaning liquid from which the oil has been separated is returned to the cleaning tank 11 as a regenerated cleaning liquid as indicated by an arrow Y1. The oil separated by the oil / water separator 15 is sent to the outside as a waste liquid for disposal as indicated by arrow Y2.

【0018】上記した構成の洗浄装置において、フィル
タ装置13としてバッグフィルタが利用されている。バ
ッグフィルタは、図2で示すように、全体は袋のような
構造をしており、袋を構成する材料は、例えば早期の目
詰まりを防ぐバイパス層21および洗浄液を内部に均一
に取り込むトランスポート層22、そして、外側のフィ
ルタ層23の3層構造になっている。そして、洗浄液は
上部の開口24から入り、袋を構成する各層21〜23
によって固形物のゴミが除去され、ゴミのない洗浄液が
外側に流れ出てくる。
A bag filter is used as the filter device 13 in the above-described cleaning device. As shown in FIG. 2, the bag filter has a bag-like structure as a whole, and the material forming the bag is, for example, a bypass layer 21 that prevents clogging at an early stage and a transport that uniformly takes in a cleaning liquid into the bag. The layer 22 and the outer filter layer 23 have a three-layer structure. Then, the cleaning liquid enters from the upper opening 24, and each layer 21 to 23 constituting the bag
By this, solid dust is removed, and the dust-free cleaning liquid flows out to the outside.

【0019】バッグフィルタは、他のフィルタ装置に比
較して、初期費用やランニング費用などコストの面や性
能の面で優れている。例えば、従来装置で使用された糸
巻きフィルタの場合、洗浄液中に残るゴミの量は100
mg/100ccであったが、バッグフィルタの場合、
50mg/100cc以下に低下している。
The bag filter is superior to other filter devices in terms of cost and performance such as initial cost and running cost. For example, in the case of the wound filter used in the conventional device, the amount of dust remaining in the cleaning liquid is 100
It was mg / 100cc, but in the case of a bag filter,
It has dropped to 50 mg / 100 cc or less.

【0020】また、油水分離装置として、限外ろ過膜装
置が採用されている。限外ろ過膜装置は、図3で示すよ
うに、コロジオン膜やゼラチン膜、セロファン膜などの
限外ろ過膜31で形成された通路中に洗浄液を通す構造
になっている。例えば洗浄液を白丸で、油を黒丸で示す
と、図の左側から洗浄液が入ってくる。このとき、油
(黒丸)は限外ろ過膜31を透過できずそのまま進み右
側に通り抜けていく。なお、洗浄液(白丸)は限外ろ過
膜31を透過する。このようにして油(黒丸)と洗浄液
(白丸)が分離されることになる。
An ultrafiltration membrane device is used as the oil / water separator. As shown in FIG. 3, the ultrafiltration membrane device has a structure in which a cleaning liquid is passed through a passage formed by an ultrafiltration membrane 31 such as a collodion membrane, a gelatin membrane, or a cellophane membrane. For example, if the cleaning liquid is indicated by a white circle and the oil is indicated by a black circle, the cleaning liquid enters from the left side of the figure. At this time, the oil (black circle) cannot pass through the ultrafiltration membrane 31 and proceeds as it is, passing through to the right. The cleaning liquid (white circle) passes through the ultrafiltration membrane 31. In this way, the oil (black circle) and the cleaning liquid (white circle) are separated.

【0021】限外ろ過膜装置を使用することによって、
エマルジョン化した洗浄廃液から油を容易に分離でき
た。例えば、図4に示すように洗浄液中の油分濃度(洗
浄液の劣化を示す指標の1つで、油重量/洗浄液重量
(%)で表される。)は0.9%以下になり、廃液量を
半減できた。図4の横軸は(日)で、縦軸は油分濃度
(%)である。また、測定期間をTで示している。
By using an ultrafiltration membrane device,
The oil could be easily separated from the emulsified cleaning waste liquid. For example, as shown in FIG. 4, the concentration of oil in the cleaning liquid (one of the indicators of deterioration of the cleaning liquid, represented by oil weight / cleaning liquid weight (%)) is 0.9% or less, and the amount of waste liquid Could be halved. The horizontal axis of FIG. 4 is (day), and the vertical axis is the oil concentration (%). The measurement period is indicated by T.

【0022】なお、限外ろ過膜方式でない電圧印加方
式、あるいは樹脂吸着方式と電圧印加方式を組み合わせ
た方式の場合は、エマルジョン化した洗浄廃液からの油
の分離が困難で、油分濃度の特性は図5に示すようにな
っている。図5も、横軸は日で、縦軸は油分濃度(%)
である。この場合、洗浄量の増加に伴い油分濃度(%)
は日毎に増加し、1.5%前後になっている。
In the case of a voltage application method that is not an ultrafiltration membrane method, or a method that combines a resin adsorption method and a voltage application method, it is difficult to separate oil from the emulsified cleaning waste liquid, and the characteristics of oil concentration are It is as shown in FIG. Also in FIG. 5, the horizontal axis is the day and the vertical axis is the oil concentration (%).
It is. In this case, the oil content (%) increases as the amount of washing increases.
Is increasing daily and is around 1.5%.

【0023】ここで、フィルタとして糸巻きフィルタ、
あるいはバッグフィルタを使用し、これらと限外ろ過膜
装置を組み合わせた場合の測定結果を表1に示す。
Here, as a filter, a spool filter,
Alternatively, Table 1 shows the measurement results when a bag filter is used and these are combined with an ultrafiltration membrane device.

【0024】 (表1) (組み合わせ) (膜洗浄)(液再生量) (寿命) 糸巻きフィルタと限外ろ過膜 2時間毎 10l/h 約3カ月 バッグフィルタと限外ろ過膜 7時間毎 25l/h 約1年間 膜洗浄は、限外ろ過膜装置の限外ろ過膜に不純物が付着
した際に行う洗浄のことで、バッグフィルタと限外ろ過
膜装置の組み合わせの方が、膜洗浄や液再生量、寿命そ
れぞれの面で優れている。
(Table 1) (Combination) (Membrane cleaning) (Liquid regeneration amount) (Life) Wound filter and ultrafiltration membrane every 2 hours 10 l / h 3 months Bag filter and ultrafiltration membrane every 7 hours 25 l / h Approximately 1 year Membrane cleaning is cleaning performed when impurities adhere to the ultrafiltration membrane of the ultrafiltration membrane device. The combination of the bag filter and the ultrafiltration membrane device is membrane cleaning or liquid regeneration. Excellent in both quantity and life.

【0025】糸巻きフィルタを用いた場合は、ゴミが素
通りするため、限外ろ過膜に付着する不純物が多くなり
洗浄頻度が高くなる。したがって液再生量も少なくな
る。また、限外ろ過膜に余分な負担をかけることになり
膜寿命も短くなっている。
When the wound filter is used, dust passes through the filter, so that the amount of impurities attached to the ultrafiltration membrane increases and the cleaning frequency increases. Therefore, the liquid regeneration amount also decreases. In addition, the extra life is shortened because an extra load is applied to the ultrafiltration membrane.

【0026】上記した図1の実施の形態では、バッグフ
ィルタを、中間貯蔵槽と油水分離装置との間に接続して
いる。しかし、バッグフィルタを洗浄槽に直接接続する
こともできる。なお、バッグフィルタを、中間貯蔵槽と
油水分離装置との間に接続し、さらに洗浄槽に接続すれ
ば、不純物の除去はより効果的に行える。
In the above-described embodiment of FIG. 1, the bag filter is connected between the intermediate storage tank and the oil / water separator. However, it is also possible to connect the bag filter directly to the cleaning bath. If the bag filter is connected between the intermediate storage tank and the oil / water separator and further connected to the cleaning tank, the impurities can be removed more effectively.

【0027】[0027]

【発明の効果】本発明によれば、洗浄液から不純物の除
去や油の分離が容易で、洗浄液の再生が効果的に行える
加工部品の洗浄装置を実現できる。
According to the present invention, it is possible to realize a cleaning device for machined parts, which can easily remove impurities and separate oil from the cleaning liquid and can effectively regenerate the cleaning liquid.

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

【図1】本発明の一つの実施形態を示す概略構成図であ
る。
FIG. 1 is a schematic configuration diagram showing one embodiment of the present invention.

【図2】本発明に使用されるバッグフィルタを示す図で
ある。
FIG. 2 is a view showing a bag filter used in the present invention.

【図3】本発明に使用される限外ろ過膜装置を説明する
図である。
FIG. 3 is a diagram illustrating an ultrafiltration membrane device used in the present invention.

【図4】本発明の特性を説明する図である。FIG. 4 is a diagram illustrating characteristics of the present invention.

【図5】従来例の特性を説明する図である。FIG. 5 is a diagram illustrating characteristics of a conventional example.

【符号の説明】[Explanation of symbols]

11…洗浄槽 12…中間貯蔵槽 13…フィルタ装置 14…ポンプ 15…油水分離装置 11 ... Washing tank 12 ... Intermediate storage tank 13 ... Filter device 14 ... Pump 15 ... Oil-water separation device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 加工部品を洗浄する洗浄液が注入された
洗浄槽と、この洗浄槽からオーバフローした洗浄液の中
から固形物を分離するフィルタ装置と、前記洗浄槽から
オーバフローした洗浄液の中から油を分離する油水分離
装置とを具備した加工部品の洗浄装置において、前記フ
ィルタ装置としてバッグフィルタを利用し、前記油水分
離装置として限外ろ過膜装置を利用したことを特徴とす
る加工部品の洗浄装置。
1. A cleaning tank into which a cleaning liquid for cleaning a processed part is injected, a filter device for separating solids from the cleaning liquid overflowing from the cleaning tank, and an oil from the cleaning liquid overflowing from the cleaning tank. An apparatus for cleaning processed parts, comprising: an oil-water separation device for separation; and a bag filter used as the filter device, and an ultrafiltration membrane device used as the oil-water separation device.
【請求項2】 バッグフィルタが限外ろ過膜装置の前段
に位置することを特徴とする請求項1記載の加工部品の
洗浄装置。
2. The apparatus for cleaning a processed part according to claim 1, wherein the bag filter is located in front of the ultrafiltration membrane device.
JP23029195A 1995-09-07 1995-09-07 Cleaning device for processed product Pending JPH0975875A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23029195A JPH0975875A (en) 1995-09-07 1995-09-07 Cleaning device for processed product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23029195A JPH0975875A (en) 1995-09-07 1995-09-07 Cleaning device for processed product

Publications (1)

Publication Number Publication Date
JPH0975875A true JPH0975875A (en) 1997-03-25

Family

ID=16905521

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23029195A Pending JPH0975875A (en) 1995-09-07 1995-09-07 Cleaning device for processed product

Country Status (1)

Country Link
JP (1) JPH0975875A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103551337A (en) * 2013-11-19 2014-02-05 安徽江淮汽车股份有限公司 Circulation filtration system and filtration method of mold cleaning fluid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103551337A (en) * 2013-11-19 2014-02-05 安徽江淮汽车股份有限公司 Circulation filtration system and filtration method of mold cleaning fluid

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