JPH0651088B2 - Regeneration method of lubricating oil for vacuum pump - Google Patents

Regeneration method of lubricating oil for vacuum pump

Info

Publication number
JPH0651088B2
JPH0651088B2 JP63172879A JP17287988A JPH0651088B2 JP H0651088 B2 JPH0651088 B2 JP H0651088B2 JP 63172879 A JP63172879 A JP 63172879A JP 17287988 A JP17287988 A JP 17287988A JP H0651088 B2 JPH0651088 B2 JP H0651088B2
Authority
JP
Japan
Prior art keywords
oil
vacuum pump
lubricating oil
filter
fiber
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 - Fee Related
Application number
JP63172879A
Other languages
Japanese (ja)
Other versions
JPH0221914A (en
Inventor
義貴 斉藤
Original Assignee
義貴 斉藤
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 義貴 斉藤 filed Critical 義貴 斉藤
Priority to JP63172879A priority Critical patent/JPH0651088B2/en
Publication of JPH0221914A publication Critical patent/JPH0221914A/en
Publication of JPH0651088B2 publication Critical patent/JPH0651088B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Lubricants (AREA)
  • Filtering Materials (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、真空ポンプ用潤滑油の再生方法に関する。TECHNICAL FIELD The present invention relates to a method for regenerating a lubricating oil for a vacuum pump.

〔従来の技術〕[Conventional technology]

真空ポンプ、特に半導体製造装置に使用する真空ポンプ
は多量の腐食性ガスが混入し、多種のガスの反応生成物
が随伴し、一部は排気装置で処理されるが真空ポンプ油
に混合した部分は油を汚染劣化させる。このため、真空
ポンプの安定した作動のためにはこれらの夾雑物(酸、
酸化生成物、金属粉、ごみ等)を濾過し除去する必要が
ある。このための従来の技法には次の各種がある。
Vacuum pumps, especially those used in semiconductor manufacturing equipment, are mixed with a large amount of corrosive gas and are accompanied by reaction products of various gases, some of which are processed by an exhaust system but mixed with vacuum pump oil. Pollutes oil. Therefore, these impurities (acid,
It is necessary to remove oxidation products, metal powder, dust, etc.) by filtration. There are various conventional techniques for this.

1.フィルター方式(セルローズ,グラスファイバー,焼
結材等) 2.吸着剤フィルター方式(活性アルミナフィルター,活
性白土フィルター等) 3.静電濾過方式 4.組合せ方式 5.抽出分離方式(油中に水又は水溶液を添加して汚染物
質を水中に抽出し、比重差で分離) 1.フィルター方式 この方式にはプリーツ型フィルターとロールティッシュ
型フィルターとがあり、瀘材表面で夾雑物を除去する。
この形式のフィルターは固体夾雑物のみを除去し、濾過
精度は比較的低く、フィルター交換時に油の損失が多
い。
1. Filter method (cellulose, glass fiber, sintered material, etc.) 2. Adsorbent filter method (activated alumina filter, activated clay filter, etc.) 3. Electrostatic filtration method 4. Combination method 5. Extraction separation method (in oil) Contaminants are extracted into water by adding water or an aqueous solution and separated by the difference in specific gravity.) 1. Filter method This method has a pleated filter and a roll tissue type filter, and removes contaminants on the surface of the filter material.
This type of filter removes only solid contaminants, the filtration accuracy is relatively low, and there is a lot of oil loss when the filter is replaced.

このフィルター方式としては、特開昭56−7609号
公報および実開昭62−24904号公報のフィルター
が知られている。前者のフィルターは、外層部の一部が
親水性架橋重合体、残部がアクリロニトリル系重合体な
どの重合体で構成された水膨潤性繊維を含有する繊維集
合体を使用し、後者のフィルターは親水性基に置換した
アクリル系またはセルローズ系などの長繊維高吸水体か
ら構成されている。しかしながら、これらのフィルター
は油中の水分を除去することはできても、油中の酸性成
分を除去することはできず、真空ポンプの潤滑油の完全
な再生には使用ができない問題があった。
As this filter system, the filters disclosed in JP-A-56-7609 and JP-A-62-24904 are known. The former filter uses a fiber assembly containing a water-swellable fiber in which a part of the outer layer part is a hydrophilic cross-linked polymer and the rest is a polymer such as an acrylonitrile polymer, and the latter filter is hydrophilic. It is composed of a long-fiber highly water-absorbent material such as an acrylic or cellulose-based material substituted with a functional group. However, even though these filters can remove water in the oil, they cannot remove acidic components in the oil and thus cannot be used for complete regeneration of the lubricating oil of the vacuum pump. .

2.吸着剤フィルター方式 主として活性アルミナを使用するフィルタであり、濾過
性能を上げるために粉末を微細にすれば目詰まりを生じ
易い。酸の吸着量は充填量で定まるため吸着量を増加す
れば大型になる。フィルターが高価であり、フィルター
交換時に油の損失が多い。
2. Adsorbent filter method This is a filter that mainly uses activated alumina, and if the powder is made fine to improve the filtration performance, clogging is likely to occur. Since the adsorption amount of acid is determined by the filling amount, it becomes large when the adsorption amount is increased. The filter is expensive and there is a lot of oil loss when changing the filter.

3.静電濾過方式 対向極板間の静電気による捕集装置であり、静電気発生
のための装置が大型になる。電流の流れ易い条件下、即
ち酸価の高い油、水分の混入した油、高汚染油等は使用
できない。酸の除去機能がない。更に使用油量が多く、
濾過速度が遅い。
3. Electrostatic filtration method This is a device for collecting static electricity between the opposite electrode plates, and the device for generating static electricity becomes large. Conditions under which an electric current easily flows, that is, oil with a high acid value, oil mixed with water, highly contaminated oil, etc. cannot be used. There is no acid removal function. Furthermore, the amount of oil used is large,
The filtration rate is slow.

4.組合せ方式 A プリーツ型と活性アルミナフィルター プリーツ型フィルターで大きな夾雑物を除去し活性アル
ミナフィルターで小さい夾雑物の除去と酸の吸着を行な
う。
4. Combination method A Pleated filter and activated alumina filter Pleated filter is used to remove large contaminants, and activated alumina filter is used to remove small contaminants and acid adsorption.

使用油量が、フィルター交換時に油の損失が著しく多
い。更に大型になり高価になる。
The amount of oil used is extremely high when replacing the filter. It becomes larger and more expensive.

B 静電濾過と活性アルミナ吸着フィルター スペースの制約上活性アルミナの充填量が少なく、酸の
処理量が少なく、油の損失が多く、高価になる。
B Electrostatic Filtration and Activated Alumina Adsorption Filter Due to space restrictions, the amount of activated alumina filled is small, the amount of acid treated is small, and the loss of oil is large and the cost is high.

5.抽出分離方式 油中に水溶液等を添加して汚染物を抽出し、比重で分離
する。
5. Extraction separation method Add an aqueous solution to the oil to extract contaminants and separate them by specific gravity.

水溶性汚染物質には有効であるが、各種夾雑物の共存す
る場合は濾過精度が悪い。
It is effective for water-soluble contaminants, but filtration accuracy is poor when various contaminants coexist.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

このように従来による方法はいずれも真空ポンプの潤滑
油の再生に対し、問題を有しており、特に潤滑油に悪影
響を与える酸性成分の除去には不十分な方法となってい
た。
As described above, all of the conventional methods have a problem with respect to the regeneration of the lubricating oil of the vacuum pump, and in particular, they are insufficient methods for removing the acidic component that adversely affects the lubricating oil.

本発明は、上記事情を考慮してなされたものであり、真
空ポンプの潤滑油の再生に際し、酸性成分を効率良く除
去して、その長期の循環使用を可能とした再生方法を提
供することを目的とする。
The present invention has been made in consideration of the above circumstances, and provides a regeneration method capable of efficiently removing an acidic component during regeneration of a lubricating oil of a vacuum pump and enabling its long-term cyclic use. To aim.

〔課題を解決するための手段および作用〕[Means and Actions for Solving the Problems]

本発明の再生方法は、含水率0.1〜30%の範囲内で
含水させたアクリル系吸水性繊維を含む濾過エレメント
に真空ポンプ内の潤滑油を循環供給して、潤滑油内の酸
性成分を除去することを特徴とする。
In the regeneration method of the present invention, the lubricating oil in the vacuum pump is circulated and supplied to the filtration element containing the acrylic water-absorbent fiber which is hydrated in the water content range of 0.1 to 30% to obtain the acidic component in the lubricating oil. Is removed.

含水したアクリル系吸水性繊維を備えた濾過エレメント
は構成繊維の表面に水分層を有しており、この表面の水
分層が真空ポンプの潤滑油内に混在する酸性成分を除去
するように作用する。すなわち、含水によって繊維表層
部に形成された水分層は、繊維内部に存在する酸置換基
を活性化すると共に、水分層に接触した酸性物質を強力
に捕捉する機能を備え、これにより初期酸中和効率を高
めるためである。従って、濾過エレメントに真空ポンプ
内の潤滑油を循環供給することにより、潤滑油内の酸性
成分が徐々に除去され、最終的な潤滑油の再生を効率良
く行なうことができる。
The filtration element including the water-containing acrylic water-absorbent fiber has a moisture layer on the surface of the constituent fibers, and the moisture layer on this surface acts to remove the acidic components mixed in the lubricating oil of the vacuum pump. . That is, the water layer formed on the surface layer of the fiber by hydration activates the acid substituents present inside the fiber and has a function of strongly capturing the acidic substance in contact with the water layer, whereby the initial acid This is to increase the sum efficiency. Therefore, by circulatingly supplying the lubricating oil in the vacuum pump to the filter element, the acidic components in the lubricating oil are gradually removed, and the final regeneration of the lubricating oil can be efficiently performed.

このような、酸性成分除去機能を有する含水率の範囲
は、0.1〜30%より好ましくは3〜15%である。
含水率が0.1%以下では酸性成分除去機能が十分でな
く、また含水率が30%以上ではアクリル系繊維の繊維
弾性が喪失して、濾過エレメントとしての形状維持がで
きなくなるためである。
The range of the water content having the acidic component removing function is 0.1 to 30%, preferably 3 to 15%.
When the water content is 0.1% or less, the acidic component removing function is not sufficient, and when the water content is 30% or more, the fiber elasticity of the acrylic fiber is lost and the shape of the filtration element cannot be maintained.

〔実施例〕〔Example〕

本発明を例示とした実施例並びに図面について説明す
る。
Examples and drawings illustrating the present invention will be described.

図は本発明の方法を密閉循環式濾過装置に適用した例を
示す。真空ポンプ10は吸気口12と排気口14とを有
し、吸気口12を所要の機器に接続する。潤滑油回路は
ドレン口16からポンプ20,濾過装置22を経て給油
口18に接続する回路32を形成する。濾過装置22の
フィルター槽24に底入口26から油を導入し、油は上
昇して環状のフィルターエレメント28内を通り、底出
口30から給油口18に戻る。
The figure shows an example in which the method of the present invention is applied to a closed circulation type filtration device. The vacuum pump 10 has an intake port 12 and an exhaust port 14, and connects the intake port 12 to a required device. The lubricating oil circuit forms a circuit 32 connecting from the drain port 16 to the oil supply port 18 via the pump 20 and the filtering device 22. Oil is introduced into the filter tank 24 of the filtering device 22 from the bottom inlet 26, the oil rises, passes through the annular filter element 28, and returns from the bottom outlet 30 to the oil supply port 18.

上述の構成に好適なフィルターエレメント28の実施の
例は下記の通りである。
An example of an implementation of the filter element 28 suitable for the above construction is as follows.

形状,外径180mm,高さ115mmのドーナツ型 繊維充填率5−50% 繊維含水率0.1−30% 繊維の種類 アクリル系吸水性繊維 他の繊維,不織布,綿状エレメント,糸巻き状エレメン
ト等を混入して得る。
Shape, outer diameter 180mm, height 115mm, donut type Fiber filling rate 5-50% Fiber moisture content 0.1-30% Fiber type Acrylic water-absorbent fiber Other fiber, non-woven fabric, cotton element, wound element, etc. And get it.

ポンプ 加圧型油循環ポンプ (0.1-15 lt/min) 図示の構成は真空ポンプを直結した連続循環密閉式濾過
装置であるが、回路にバイパスを形成し又は真空ポンプ
のタンクから油を供給させ、濾過装置はこのタンク又は
別のタンクの使用済み潤滑油の再生を行なうこともでき
ることは勿論である。
Pump Pressurized oil circulation pump (0.1-15 lt / min) Although the configuration shown is a continuous circulation closed filtration device directly connected to a vacuum pump, it forms a bypass in the circuit or supplies oil from the tank of the vacuum pump. It goes without saying that the filtering device can also recycle the used lubricating oil in this tank or another tank.

本発明の図示の濾過装置の実施の例を塩素系ドライエッ
チング工程における真空ポンプ油の再生例として以下に
示す。
An example of implementation of the illustrated filtration device of the present invention will be shown below as an example of regeneration of vacuum pump oil in a chlorine-based dry etching process.

再生処理条件 オイル 弗素系合成油(BARRIERTA J25 ) 処理油量 10 lt 循環ポンプ流量 1.3 lt/min フィルタ槽容量 3.5 lt 処理温度 常温 エレメント 180 φ X 115mm 繊維充填率 20% 繊維含水率 10% 分析結果 処理前の分析値 重量汚染度 106 mg/100ml 強酸価 150 mg/l 処理後の分析値 処理時間 hr 0 1 2 3 重量汚染度mg/100ml 106 13 1.2 0 強酸価 mg/l 105 22 1.8 0 弗素系ドライエッチング工程における連続使用の実施の
例を他の既知の濾過方式と同様の条件で使用した例を以
下の表1に示す。
Regeneration treatment condition Oil Fluorine-based synthetic oil (BARRIERTA J25) Treatment oil amount 10 lt Circulation pump flow rate 1.3 lt / min Filter tank capacity 3.5 lt Treatment temperature Normal temperature element 180 φ X 115mm Fiber filling rate 20% Fiber moisture content 10% Analysis result treatment Previous analysis value Weight pollution degree 106 mg / 100 ml Strong acid value 150 mg / l Analysis value after treatment Treatment time hr 0 1 2 3 Weight pollution degree mg / 100 ml 106 13 1.2 0 Strong acid value mg / l 105 22 1.8 0 Fluorine-based Table 1 below shows an example of continuous use in the dry etching step, which is used under the same conditions as other known filtration methods.

使用条件 使用油 松村石油研究所 MR-200 粘度 73.6 cst/40 ゜ 全酸価 0 重量汚染度 0 真空ポンプ 日本真空技研 D-950 使用雰囲気ガス フロン 従来の処理方式に比較して、粘度、全酸価、汚染度を長
期間に亘って維持制御することが可能となった。
Usage conditions Oil used Matsumura Oil Research Institute MR-200 Viscosity 73.6 cst / 40 ° Total acid value 0 Weight pollution degree 0 Vacuum pump Japan Vacuum Giken D-950 Working atmosphere gas Freon Compared with conventional treatment methods, viscosity and total acid It has become possible to maintain and control the price and pollution level over a long period of time.

表2は真空ポンプ(D-950,日本真空技術(株)製)の潤
滑油として、弗素系合成油10を使用し、この潤滑油
を各含水率をアクリル系吸水性繊維を有した濾過エレメ
ントに循環供給した場合の結果を示す。同表から含水率
0.1〜30%、好ましくは3〜15%の範囲におい
て、良好な酸性成分除去を有していることが判る。
Table 2 shows that a fluorine-based synthetic oil 10 is used as a lubricating oil for a vacuum pump (D-950, manufactured by Nippon Vacuum Technology Co., Ltd.). The results are shown in the case of circulating supply. It can be seen from the table that the water content of 0.1 to 30%, preferably 3 to 15%, is sufficient to remove acidic components.

〔発明の効果〕 1.酸の除去 本発明によるアクリル系吸水性繊維フィルタエレメント
は0.1−30%含水させることにより、油中の酸が水に
置換し、酸化の上昇を制御し、中和効果を生ずる。従っ
て、真空ポンプの潤滑油を循環供給することにより、酸
性成分を確実に除去することができる。
[Effects of the Invention] 1. Removal of Acid The acrylic water-absorbent fiber filter element according to the present invention contains 0.1-30% of water so that the acid in the oil is replaced by water to control the increase in oxidation. Produces a sum effect. Therefore, by circulating and supplying the lubricating oil of the vacuum pump, the acidic component can be reliably removed.

2.夾雑物及び反応生成物の除去 繊維表面に夾雑物が付着し、順次堆積して夾雑物を処理
除去する。
2. Removal of contaminants and reaction products Contaminants adhere to the fiber surface and are sequentially deposited to remove contaminants by processing.

3.酸と夾雑物が共存している場合の除去 繊維表面に夾雑物が付着し、酸は水分層に置換されて除
去される。
3. Removal when acid and contaminants coexist The contaminants adhere to the fiber surface, and the acid is replaced by the water layer and removed.

4.使用条件に対する適応性 本発明のフィルターエレメントは密度調整、含水率調
整、各種形状の加工が容易であり、各種の使用条件に容
易に適合できる。
4. Adaptability to usage conditions The filter element of the present invention is easy to adjust density, moisture content, and be processed into various shapes, and can be easily adapted to various usage conditions.

即ち、夾雑物生成物の混入の多い場合は密度を小とす
る。酸の混入の多い場合は含水率を大きくする。この作
業はフィルターエレメントの調整、充填に際して容易に
行なうことができる。
That is, the density is set low when a large amount of contaminant products is mixed. Increase the water content if there is a large amount of acid. This operation can be easily performed when adjusting and filling the filter element.

また、本発明の含水したアクリル系吸水性繊維は、その
含水により繊維の表面が活性化されており、強力な吸着
力を有している。このため繊維密度がラフであっても、
酸や夾雑物、その他の有害物質を除去することができ、
目詰まりも長じることなく、長期間使用することができ
る。そして、これら有害物質の除去により真空ポンプの
潤滑油の再生を確実に行なうことができる。
In addition, the water-containing acrylic water-absorbent fiber of the present invention has a strong adsorption power because the surface of the fiber is activated by the water content. Therefore, even if the fiber density is rough,
Can remove acids, contaminants and other harmful substances,
It can be used for a long time without long clogging. Then, by removing these harmful substances, it is possible to surely regenerate the lubricating oil of the vacuum pump.

本発明の濾過装置の使用によって、真空ポンプの使用済
み油を所要の規格に再生でき、半導体製造に際して著し
く有効である。
By using the filtration device of the present invention, the used oil of the vacuum pump can be regenerated to the required standard, which is remarkably effective in semiconductor manufacturing.

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

図は本発明による真空ポンプ潤滑油の再生方法の一例を
示す図である。 10……真空ポンプ 12……吸気口 14……排気口 16……ドレン口 18……給油口 20……循環ポンプ 22……濾過装置 24……フィルター槽 28……フィルターエレメント
The figure is a diagram showing an example of a method for regenerating a vacuum pump lubricating oil according to the present invention. 10 ... Vacuum pump 12 ... Intake port 14 ... Exhaust port 16 ... Drain port 18 ... Oil supply port 20 ... Circulation pump 22 ... Filtration device 24 ... Filter tank 28 ... Filter element

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】含水率0.1〜30%の範囲内で含水させ
たアクリル系吸水性繊維を含む濾過エレメントに真空ポ
ンプ内の潤滑油を循環供給して、潤滑油内の酸性成分を
除去することを特徴とする真空ポンプ用潤滑油の再生方
法。
1. A lubricating oil in a vacuum pump is circulated and supplied to a filter element containing an acrylic water-absorbent fiber which has a water content of 0.1 to 30% to remove an acidic component in the lubricating oil. A method for regenerating a lubricating oil for a vacuum pump, comprising:
JP63172879A 1988-07-12 1988-07-12 Regeneration method of lubricating oil for vacuum pump Expired - Fee Related JPH0651088B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63172879A JPH0651088B2 (en) 1988-07-12 1988-07-12 Regeneration method of lubricating oil for vacuum pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63172879A JPH0651088B2 (en) 1988-07-12 1988-07-12 Regeneration method of lubricating oil for vacuum pump

Publications (2)

Publication Number Publication Date
JPH0221914A JPH0221914A (en) 1990-01-24
JPH0651088B2 true JPH0651088B2 (en) 1994-07-06

Family

ID=15950004

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63172879A Expired - Fee Related JPH0651088B2 (en) 1988-07-12 1988-07-12 Regeneration method of lubricating oil for vacuum pump

Country Status (1)

Country Link
JP (1) JPH0651088B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002188589A (en) 2000-12-21 2002-07-05 Canon Inc Vacuum exhaust device and method therefor
DE10349741A1 (en) * 2003-10-23 2005-06-02 Ebro Electronic Gmbh & Co. Kg Method for measuring fats or oils and corresponding filtering device and measuring device
CN101954206B (en) * 2010-08-26 2014-03-05 常州亿晶光电科技有限公司 Liquid lubricating oil filtering device

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS567609A (en) * 1979-06-29 1981-01-26 Japan Exlan Co Ltd Dewatering filter for liquids
JPH0227842Y2 (en) * 1985-07-31 1990-07-26

Also Published As

Publication number Publication date
JPH0221914A (en) 1990-01-24

Similar Documents

Publication Publication Date Title
CN105329976B (en) The method for adsorbing perfluorochemical in simultaneously degradation water
DE602004031035D1 (en) LIQUID FILTRATION APPARATUS AND METHOD WITH SUPER-SWIMMING FILTRATION PARTICLES
WO2002070105A3 (en) Filtration media of porous inorganic particles
WO2013191272A1 (en) Water treatment system
CN106630003A (en) Oily wastewater treatment device and method
JP2947314B2 (en) Adsorption and reaction equipment
JPH0651088B2 (en) Regeneration method of lubricating oil for vacuum pump
CN205774345U (en) A kind of electrostatic and coalescence oil filter device
CS269985B2 (en) Method of perfluorpolyether oils cleaning
CN206590968U (en) Cutting fluid waste liquid decontamination cycle water saving fixtures
RU2429043C1 (en) Filter device (versions)
CN206886722U (en) A kind of absorbent charcoal adsorber with regenerative system
JPH0131401B2 (en)
CN201625490U (en) Exhaust gas purifying device
CN211688683U (en) Wastewater treatment system for production workshop
CN208194047U (en) A kind of fume gases cleaning equipment
CN112044213A (en) Water elution device for oil-containing waste gas
JP2020089852A (en) Regeneration method and regeneration device of filtration membrane, and filtration method and filtration device of oil-containing wastewater
JP2003340215A (en) Apparatus for removing impurities from coating pretreatment liquid
JP2001517142A (en) Method and apparatus for purifying a liquid containing impurities
RU2282489C2 (en) Cleaning of filter on base of hollow fibers at frontal mode of operation
CN220642844U (en) Dichloromethane waste water treatment system
JPH0128806Y2 (en)
CN105435572A (en) Air purifier
RU202824U1 (en) Hydrocyclone

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080706

Year of fee payment: 14

LAPS Cancellation because of no payment of annual fees