JPS64104B2 - - Google Patents

Info

Publication number
JPS64104B2
JPS64104B2 JP55036413A JP3641380A JPS64104B2 JP S64104 B2 JPS64104 B2 JP S64104B2 JP 55036413 A JP55036413 A JP 55036413A JP 3641380 A JP3641380 A JP 3641380A JP S64104 B2 JPS64104 B2 JP S64104B2
Authority
JP
Japan
Prior art keywords
oil
water
electric field
removal device
centrifugal separator
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
Application number
JP55036413A
Other languages
Japanese (ja)
Other versions
JPS56133054A (en
Inventor
Tooru Sasaki
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.)
Kleentek Industrial Co Ltd
Original Assignee
Kleentek Industrial Co Ltd
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 Kleentek Industrial Co Ltd filed Critical Kleentek Industrial Co Ltd
Priority to JP3641380A priority Critical patent/JPS56133054A/en
Publication of JPS56133054A publication Critical patent/JPS56133054A/en
Publication of JPS64104B2 publication Critical patent/JPS64104B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Electrostatic Separation (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、多量の水分や汚染物質を含んだ汚染
油の油処理方法に関するものである。 潤滑油や油圧作動油に汚染物が存在すると、機
械の故障や油洩れなどの種々の障害が発生するの
で、これらの油は高度に清浄化されていることが
望ましい。油の浄化方法としては、フイルタによ
る方法や遠心分離機による方法、静電浄油機によ
る方法などが知られているが、これらの方法はそ
れぞれ長所と欠点とを有している。すなわち、通
常のフイルタは微細な汚染粒子や水分を除去でき
ず、しかも目詰まりし易いという欠点を有してい
る。遠心分離機は比較的に大きい汚染粒子を除去
するのに適しているが、エマルジヨン化された水
分を完全に除去することが出来ず、また微細な汚
染粒子を除去できないという欠点を有している。
静電浄油機は、微細な汚染粒子でも除去できると
いう長所を有しているが、多量の水分が存在する
場合には油を浄化できないこと、及び油を高度に
清浄化しようとする場合には循環的に油を処理す
る必要があること等の欠点を有している。 本発明は、上記の考察に基づくものであつて、
多量の水分や汚染物質を含む汚染油を高度に正常
化できる油処理方法を提供することを目的として
いる。そしてそのため本発明の油処理方法は、電
界チヤージヤで油に電界を印加し、電界が印加さ
れた油を連通管を介して遠心分離機に送り、遠心
分離機で処理し、遠心分離機によつて処理された
油を連通管を介して吸水繊維を使用して水分を除
去する所の除水装置に送り、該除水装置で処理
し、該除水装置によつて処理された油を連通管を
介して静電浄油機に送り、静電浄油機で処理する
ことを特徴とするものである。以下、本発明を図
面を参照しつつ説明する。 第1図は本発明の油処理システムの1実施例を
示す図、第2図は遠心分離機における原液と処理
液との分離特性を示す図、第3図は電界を印加し
た場合における水の粒子の成長を説明する図であ
る。 第1図において、1は電界チヤージヤ、2は遠
心分離機、3は除水装置、4は静電浄油機、5は
連通管をそれぞれ示している。 本発明の油処理システムは、電界チヤージヤ
1、遠心分離機2、除水装置3、静電浄油機4お
よび装置間をつなぐ連通管5を有するものであ
る。 電界チヤージヤ1は、容槽と、容槽内に配置さ
れた複数の電極とを有しているものである。油を
容槽内に満し、対向する電極間に直流電圧又は交
流電圧を印加すると、油に電界が作用する。油に
電界が作用すると、油中の汚染粒子や水の粒子は
成長する。第3図イ,ロ,ハは、油中における水
の粒子の成長を示すものであつて、第3図イは1
分間電界を印加した場合における水の粒子を示
し、第3図ロは5分間電界を印加した場合におけ
る水の粒子を示し、第3図ハは30分間油に電界を
印加した場合における水の粒子をそれぞれ示して
いる。なお、第3図イ,ロ,ハは実物を100倍に
拡大した図である。遠心分離機2は、配管によつ
て電界チヤージヤ1と連通され、電界チヤージヤ
1から送られて来る油の中の汚染物および水分を
分離除去する。第2図は遠心分離機における原液
と処理液との分離特性を示すものである。第2図
において、Aは原液の分離特性、Bは1分間電界
を印加した油の分離特性、Cは5分間電界を印加
した油の分離特性、Dは30分間電界を印加した油
の分離特性をそれぞれ示している。第2図から判
るように、原液を遠心分離機で処理すると、処理
液の水分は1ないし1.5%位になるが、電界チヤ
ージヤで処理した後の油の場合には、処理液の水
分は0.5%(5000p.p.m)以下となる。 除水装置3は、容槽と、容槽内に配置された吸
水性の繊維の塊とを有しているものである。吸水
性の繊維としては、例えばアクリル繊維の心材の
表面にアクリル系の吸水性ゲルを塗布したものが
用いられる。下記の表は吸水装置の水分除去特性
を示すものである。
The present invention relates to a method for treating contaminated oil containing a large amount of water and contaminants. The presence of contaminants in lubricating oils and hydraulic fluids can cause various problems such as machine breakdowns and oil leaks, so it is desirable that these oils be highly purified. As methods for purifying oil, methods using filters, methods using centrifuges, methods using electrostatic oil purifiers, etc. are known, but each of these methods has advantages and disadvantages. In other words, ordinary filters have the drawback of not being able to remove fine contaminant particles and moisture, and moreover, being easily clogged. Although centrifugal separators are suitable for removing relatively large contaminant particles, they have the disadvantage that they cannot completely remove emulsified water and cannot remove fine contaminant particles. .
Electrostatic oil purifiers have the advantage of being able to remove even the smallest contaminant particles, but they cannot purify oil when a large amount of moisture is present, and they are difficult to clean when attempting to clean oil at a high level. has drawbacks such as the need to process the oil cyclically. The present invention is based on the above considerations, and includes:
The object of the present invention is to provide an oil treatment method that can highly normalize contaminated oil containing large amounts of water and pollutants. Therefore, in the oil treatment method of the present invention, an electric field is applied to oil using an electric field charger, the oil to which the electric field has been applied is sent to a centrifugal separator through a communication pipe, and is processed by the centrifugal separator. The treated oil is sent via a communication pipe to a water removal device where water is removed using water-absorbing fibers, treated by the water removal device, and the oil treated by the water removal device is communicated. It is characterized by being sent to an electrostatic oil purifier via a pipe and processed by the electrostatic oil purifier. Hereinafter, the present invention will be explained with reference to the drawings. Fig. 1 is a diagram showing one embodiment of the oil treatment system of the present invention, Fig. 2 is a diagram showing the separation characteristics between the stock solution and the processing liquid in a centrifuge, and Fig. 3 is a diagram showing the separation characteristics of the stock solution and the processing solution in a centrifugal separator. FIG. 3 is a diagram illustrating the growth of particles. In FIG. 1, 1 is an electric field charger, 2 is a centrifugal separator, 3 is a water removal device, 4 is an electrostatic oil purifier, and 5 is a communication pipe. The oil treatment system of the present invention includes an electric field charger 1, a centrifugal separator 2, a water removal device 3, an electrostatic oil purifier 4, and a communication pipe 5 connecting the devices. The electric field charger 1 has a container and a plurality of electrodes arranged inside the container. When a tank is filled with oil and a DC or AC voltage is applied between opposing electrodes, an electric field acts on the oil. When an electric field acts on oil, contaminant particles and water particles in the oil grow. Figure 3 A, B, and C show the growth of water particles in oil, and Figure 3 A is 1.
Figure 3 (b) shows water particles when an electric field is applied for 5 minutes, and Figure 3 (c) shows water particles when an electric field is applied to oil for 30 minutes. are shown respectively. Note that Figure 3 A, B, and C are 100 times enlarged views of the actual product. The centrifugal separator 2 is connected to the electric field charger 1 through piping, and separates and removes contaminants and moisture from the oil sent from the electric field charger 1. FIG. 2 shows the separation characteristics between the stock solution and the treated solution in a centrifugal separator. In Figure 2, A is the separation characteristic of the undiluted solution, B is the separation characteristic of the oil with an electric field applied for 1 minute, C is the separation characteristic of the oil with the electric field applied for 5 minutes, and D is the separation characteristic of the oil with the electric field applied for 30 minutes. are shown respectively. As can be seen from Figure 2, when the undiluted solution is processed with a centrifuge, the water content of the processed liquid is about 1 to 1.5%, but when the oil is processed with an electric field charger, the water content of the processed liquid is 0.5%. % (5000p.pm) or less. The water removal device 3 has a container and a mass of water-absorbing fibers arranged in the container. As the water-absorbing fiber, for example, an acrylic fiber core material coated with an acrylic water-absorbing gel is used. The table below shows the moisture removal characteristics of the water absorption device.

【表】 この表から判るように、除水装置3を用いるこ
とにより、油中の水分を200p.p.m以下とするこ
とは容易である。 静電浄油機4は、容槽と、容槽内に形成された
正負の電極と、正負電極間に配置された集塵体と
を有し、電極間に油を流通させて、油中の汚染粒
子や水分を除去するものである。さきにも述べた
ように、静電浄油機は微細な汚染粒子をも除去で
きるものであつて、油中の汚染物を2mg/100ml
以下とすることが容易である。しかし、油中の水
分が500p.p.mより大きくなると、浄化性能が低
下するという欠点を有している。 次に本発明の操業例を説明する。いま、汚染粒
子が12mg/100ml、水分が50000p.p.mの油を2
/minの流量で電界チヤージヤ1に供給する。
電界チヤージヤ1から流出する油は遠心分離機2
に供給され、遠心分離機2で処理される。遠心分
離機2で処理された油の汚染物の量は6mg/100
mlであり、水分は1000p.p.mであつた。遠心分離
機2から流出する油は除水装置3を通過する。除
水装置3を通過した油の汚染物の量は5mg/100
mlであり、水分は200p.p.mであつた。除水装置
3を通過した油は静電浄油機4に供給され、静電
浄化処理される。静電浄油機4より流出する油の
汚染物の量は2mg/100mlであり、水分は1000p.
p.mであつた。この操業例から判るように、汚染
物の量が12mg/100ml、水分が50000p.p.mの油を
第1図の油処理システムの中を1回通過させるだ
けで、汚染物の量が2mg/100ml、水分が100p.p.
mの油が得られる。 以上の説明から明らかなように、本発明によれ
ば、多量の水分や汚染物質を含む汚染油を高度に
清浄化することが出来る。また、本発明の油処理
方法は、清浄化処理を効率的に行うことが出来る
と共に、火災の危険性が少なく安全性も高いと言
う効果をも有している。
[Table] As can be seen from this table, by using the water removal device 3, it is easy to reduce the water content in the oil to 200 p.pm or less. The electrostatic oil purifier 4 has a container, positive and negative electrodes formed in the container, and a dust collector disposed between the positive and negative electrodes, and circulates oil between the electrodes to remove water from the oil. It removes contaminant particles and moisture. As mentioned earlier, electrostatic oil purifiers are capable of removing even minute contaminant particles, and contaminants in oil can be removed by 2 mg/100 ml.
It is easy to do the following. However, when the water content in the oil exceeds 500 p.pm, it has the disadvantage that the purification performance decreases. Next, an example of operation of the present invention will be explained. Now, two pieces of oil with contaminant particles of 12 mg/100 ml and water content of 50,000 p.pm are
The electric field charger 1 is supplied with a flow rate of /min.
The oil flowing out from the electric field charger 1 is sent to the centrifuge 2.
and processed by centrifuge 2. The amount of contaminants in the oil processed by centrifuge 2 is 6mg/100
ml, and the water content was 1000 p.pm. Oil flowing out from the centrifuge 2 passes through a water removal device 3. The amount of contaminants in the oil that passed through water removal device 3 was 5mg/100
ml, and the water content was 200 p.pm. The oil that has passed through the water removal device 3 is supplied to an electrostatic oil purifier 4 where it is electrostatically purified. The amount of oil contaminants flowing out from the electrostatic oil purifier 4 is 2mg/100ml, and the water content is 1000p.
It was hot at pm. As can be seen from this operation example, by passing oil containing 12 mg/100 ml of contaminants and 50,000 ppm water through the oil treatment system shown in Figure 1 once, the amount of contaminants can be reduced to 2 mg/100 ml. , moisture is 100 p.p.
m of oil is obtained. As is clear from the above description, according to the present invention, contaminated oil containing a large amount of water and contaminants can be highly purified. Further, the oil treatment method of the present invention has the effect that cleaning treatment can be performed efficiently, and the risk of fire is low and safety is high.

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

第1図は本発明の油処理システムの1実施例を
示す図、第2図は遠心分離機における原液と処理
液との分離特性を示す図、第3図は電界を印加し
た場合における水の粒子の成長を説明する図であ
る。 1……電界チヤージヤ、2……遠心分離機、3
……除水装置、4……静電浄油機、5……連通
管。
Fig. 1 is a diagram showing an embodiment of the oil treatment system of the present invention, Fig. 2 is a diagram showing the separation characteristics between the stock solution and the processing liquid in a centrifugal separator, and Fig. 3 is a diagram showing the separation characteristics of the undiluted solution and the processing solution in a centrifugal separator. FIG. 3 is a diagram illustrating the growth of particles. 1...Electric field charger, 2...Centrifugal separator, 3
...Water removal device, 4...Electrostatic oil purifier, 5...Communication pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 電界チヤージヤで油に電界を印加し、電界が
印加された油を連通管を介して遠心分離機に送
り、遠心分離機で処理し、遠心分離機によつて処
理された油を連通管を介して吸水繊維を使用して
水分を除去する所の除水装置に送り、該除水装置
で処理し、該除水装置によつて処理された油を連
通管を介して静電浄油機に送り、静電浄油機で処
理することを特徴とする油処理方法。
1 Apply an electric field to the oil using an electric field charger, send the oil to which the electric field has been applied to the centrifugal separator via the communicating tube, process it in the centrifugal separator, and send the oil treated by the centrifuge through the communicating tube. The oil is sent to a water removal device where water is removed using water-absorbing fibers, and treated by the water removal device.The oil treated by the water removal device is sent to an electrostatic oil purifier through a communication pipe. An oil processing method characterized by sending the oil to a tank and treating it with an electrostatic oil purifier.
JP3641380A 1980-03-22 1980-03-22 Oil treating system Granted JPS56133054A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3641380A JPS56133054A (en) 1980-03-22 1980-03-22 Oil treating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3641380A JPS56133054A (en) 1980-03-22 1980-03-22 Oil treating system

Publications (2)

Publication Number Publication Date
JPS56133054A JPS56133054A (en) 1981-10-17
JPS64104B2 true JPS64104B2 (en) 1989-01-05

Family

ID=12469134

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3641380A Granted JPS56133054A (en) 1980-03-22 1980-03-22 Oil treating system

Country Status (1)

Country Link
JP (1) JPS56133054A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61287984A (en) * 1985-06-14 1986-12-18 Mitsubishi Kakoki Kaisha Ltd Method and device for cleaning heavy oil containing catalyst
JPH0450902Y2 (en) * 1987-07-03 1992-12-01
JP6460530B2 (en) * 2015-04-28 2019-01-30 株式会社ゼオテック Oil regeneration method and apparatus

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4917567A (en) * 1972-06-12 1974-02-16
JPS52148870A (en) * 1976-03-09 1977-12-10 Koushiyou Kk Pressureefiltrating spiral electrode electric emulsion separator dust collector

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4917567A (en) * 1972-06-12 1974-02-16
JPS52148870A (en) * 1976-03-09 1977-12-10 Koushiyou Kk Pressureefiltrating spiral electrode electric emulsion separator dust collector

Also Published As

Publication number Publication date
JPS56133054A (en) 1981-10-17

Similar Documents

Publication Publication Date Title
JP3530209B2 (en) Method and apparatus for treating suspended sewage containing dissolved contaminants
US4865742A (en) Method of treating polluted oil-in-water emulsions or microemulsions
ATE127097T1 (en) DEVICE AND METHOD FOR PURIFYING HYDROGEN FLUORIDE.
CA3005192A1 (en) Standardized oilfield water treatment device and process using physical method
KR890005261B1 (en) A liquid filtering device
JPS64104B2 (en)
Kessick et al. Electrophoretic mobilities of virus adsorbing filter materials
KR100349823B1 (en) Oil refining method
JPH10216721A (en) Ultrapure water producing device
JP2001170656A (en) Process for removing solid particulate, more particularly silica and/or alumina particulate from waste water
CN212700868U (en) Lubricating oil purification and detection equipment
CN209302420U (en) A kind of heat-treatment quenching oil groove fume purifying set composite
CA1073365A (en) Process and apparatus for removal of ash from waste water treatment system
JPS63147506A (en) Method for cleaning hollow yarn membrane filter
KR830007438A (en) Wastewater Treatment Method
JP3947663B2 (en) Chelate regenerator
JP6460530B2 (en) Oil regeneration method and apparatus
WO1982004202A1 (en) Oil treating apparatus
WO2001030707A1 (en) Device and method for treating dental waste streams
RU2029733C1 (en) Sewage water cleaning method
JPS6230505A (en) Filter apparatus
RU2116258C1 (en) Method and installation for removing petroleum products from water
SU836075A1 (en) Method of oil dehydration and desalinization
RU14209U1 (en) WATER TREATMENT PLANT
SU994421A1 (en) Method for purifying water