KR960017829A - Industrial Waste Oil Recycling Method and Device - Google Patents

Industrial Waste Oil Recycling Method and Device Download PDF

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Publication number
KR960017829A
KR960017829A KR1019940030888A KR19940030888A KR960017829A KR 960017829 A KR960017829 A KR 960017829A KR 1019940030888 A KR1019940030888 A KR 1019940030888A KR 19940030888 A KR19940030888 A KR 19940030888A KR 960017829 A KR960017829 A KR 960017829A
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South Korea
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electrode plate
waste oil
tank
vacuum
layer
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KR1019940030888A
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Korean (ko)
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KR0138026B1 (en
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구경회
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구경회
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Publication of KR0138026B1 publication Critical patent/KR0138026B1/en

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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M175/00—Working-up used lubricants to recover useful products ; Cleaning
    • C10M175/0066—Use of electrical and magnetical means
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1003—Waste materials
    • C10G2300/1007—Used oils
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
    • C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00—Distillation of hydrocarbon oils
    • C10G7/003—Distillation of hydrocarbon oils distillation of lubricating oils

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Electrostatic Separation (AREA)

Abstract

1. 청구범위에 기재된 발명이 속한 기술분야1. TECHNICAL FIELD OF THE INVENTION

산업용 폐오일 재생방법 및 장치Industrial Waste Oil Recycling Method and Device

2. 발명의 해결하려고 하는 기술적 과제2. Technical problem to be solved

본 발명은 진공 및 쿨롱 (COULOMB) 법칙의 전기력을 이용하여 진공내에서의 유체는 비등점이 강하되므로 상온에서 증류되는 성질을 이용 진공도를 유지하는 용기에 폐오일을 유입시키어 오일속의 수분, 수지성물질, 산화물, 가스등을 제거한 후 초고전압이 흐르는 용기내로 오일을 통과시켜주어서 5미크론 이상의 입자뿐아니라, 종래의 기술로는 제거할수 없었던 1미크론 이하 0.05 미크론 (표면에 대전될 수 있는 입자의 한계사이즈)크기의 입자까지 제거하여 오폐일의 재생 및 재활용이 가능토록한 것임.The present invention uses the electric force of the vacuum and the Coulomb law, the fluid in the vacuum is lowered the boiling point, so the waste oil is introduced into the container to maintain the degree of vacuum using the property of distillation at room temperature, water, resinous material in the oil After removing the oxides, gases, etc., the oil is passed through a container with ultra high voltage to not only particles of 5 microns or more, but also 0.05 microns or less, which cannot be removed by conventional techniques (limit size of particles that can be charged on the surface). By removing the particles of size, it is possible to recycle and recycle the waste days.

3. 발명의 해결방법의 요지3. Summary of Solution to Invention

오일흡입펌프(1)로 가열된 폐오일을 흡입 이송하여 진공탱크(3)내의 노즐(3)을 통해 스프레이시켜 증류층(12)을 거치는 동안 폐오일 내의 유동성오염 물질이 증류되어 진공탱크(2) 상단에 모여지면 진공펌프(2)에 의해 외부로 배출하는 과정에서 배출 가스는 공기응축기(4)로 냉각시켜 응축한후 배출탱크(5)에 저장하고, 일정량이 모이면 배출밸브를 통해 드레인 시키어서 폐수처리 설비로 이동시키고, 다음 응축되지 않는 가스는 진공펌프(6)로 대기중으로 1차처리 배출시키는 공정과 증류층(12)을 통과한 폐오일을 진공탱크(2) 하단 내부에 저장되고 일정량이 차게되면, 펌프(7)에 의하여 직규고전압이 인가된 탱크(8)내로 투입시키어 직류고전압발생장치(11)에 의하여 +전극판(9)과 -전극판(9a)은 높은 전위차를 갖게 되어 코로나방전층(10)을 형성하게되며, 폐오일이 코로나방진층(10)을 통과하는 동안 폐오일 내의 오염물질은 각기 고유의 성질에 따라 표면에 +,-로 대전되어 전극판에 이동 흡착 제거되는 2차처리공정으로 처리된 것임.The waste oil heated by the oil suction pump 1 is suctioned and sprayed and sprayed through the nozzle 3 in the vacuum tank 3 to pass through the distillation layer 12. ) When collected at the top, the exhaust gas is discharged to the outside by the vacuum pump (2), cooled by the air condenser (4), condensed and stored in the discharge tank (5). To the wastewater treatment plant, and the non-condensed gas is first discharged into the atmosphere by the vacuum pump (6) and the waste oil passing through the distillation layer (12) is stored inside the bottom of the vacuum tank (2). When a certain amount becomes cold, the positive electrode plate 9 and the negative electrode plate 9a are introduced into the tank 8 to which the high voltage is applied by the pump 7 so that the positive electrode plate 9 and the negative electrode plate 9a have a high potential difference. To form a corona discharge layer 10, waste waste The contaminants in waste oil while passing through the corona dustproof layer 10 is, respectively, depending on the specific nature +, the surface will be charged to the process as a secondary processing step that removes the moving electrode plate absorption.

4. 발명의 중요한 용도4. Important uses of the invention

산업용 폐오일 재생방법 및 장치Industrial Waste Oil Recycling Method and Device

Description

산업용 폐오일 재생방법 및 장치Industrial Waste Oil Recycling Method and Device

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음As this is a public information case, the full text was not included.

제1도는 본 발명의 계통도1 is a schematic diagram of the present invention.

제2도는 본 발명의 중류층을 형성한 부분사시도2 is a partial perspective view of the middle class of the present invention.

Claims (4)

오일흡입펌프(1)로 가열된 폐오일을 흡입 이송하여 진공탱크(3)내의 노즐(3)을 통해 스프레이시켜 증류층(12)을 거치는 동안 폐오일 내의 유동성오염 물질이 증류되어 진공탱크(2) 상단에 모여지면 진공펌프(2)에 의해 외부로 배출하는 과정에서 배출 가스는 공기응축기(4)로 냉각시켜 응축한후 배출탱크(5)에 저장하고, 일정량이 모이면 배출밸브를 통해 드레인 시키어서 폐수처리 설비로 이동시키고, 다음 응축되지 않는 가스는 진공펌프(6)로 대기중으로 1차처리 배출시키는 공정과 증류층(12)을 통과한 폐오일을 진공탱크(2) 하단 내부에 저장되고 일정량이 차게되면, 펌프(7)에 의하여 직규고전압이 인가된 탱크(8)내로 투입시키어 직류고전압발생장치(11)에 의하여 +전극판(9)과 -전극판(9a)은 높은 전위차를 갖게 되어 코로나방전층(10)을 형성하게되며, 폐오일이 코로나방진층(10)을 통과하는 동안 폐오일 내의 오염물질은 각기 고유의 성질에 따라 표면에 +,-로 대전되어 전극판에 이동 흡착 제거되는 2차처리 공정으로된 산업용 폐오일 재생방법.The waste oil heated by the oil suction pump 1 is suctioned and sprayed and sprayed through the nozzle 3 in the vacuum tank 3 to pass through the distillation layer 12. ) When collected at the top, the exhaust gas is discharged to the outside by the vacuum pump (2), cooled by the air condenser (4), condensed and stored in the discharge tank (5). To the wastewater treatment plant, and the non-condensed gas is first discharged into the atmosphere by the vacuum pump (6) and the waste oil passing through the distillation layer (12) is stored inside the bottom of the vacuum tank (2). When a certain amount becomes cold, the positive electrode plate 9 and the negative electrode plate 9a are introduced into the tank 8 to which the high voltage is applied by the pump 7 so that the positive electrode plate 9 and the negative electrode plate 9a have a high potential difference. To form a corona discharge layer 10, waste waste The corona contaminants in the waste oil while passing through the dust-proof layer 10, respectively, depending on the specific nature +, the surface is charged to the to the secondary treatment process is removed movement adsorbed to the electrode plate of industrial waste oil recycling method. 증류층(12)을 가진 진공탱크(2) 상단측면에 오일흡입펌프(1)를 통해 흡입되는 노즐(3)을 결합하며 상단에는 공기응축기(4)와 배출탱크(5)를 파이프로 연결시키며, 배출탱크(5)에는 진공펌프(6)를 결합하며, 진공탱크(2) 하단측면에는 직류고전압발생장치(11)와 연결된 +전극판(9)과 -전극판(9a)을 설치한 탱크(8)사이에 폐오일 공급펌프(7)를 설치하여 폐오일이 공급되게 함을 특징으로한 산업용 폐오일 재생장치.Coupling the nozzle (3) suctioned through the oil suction pump (1) to the upper side of the vacuum tank (2) having a distillation layer (12) and connects the air condenser (4) and the discharge tank (5) by a pipe , The vacuum tank (6) is coupled to the discharge tank (5), the lower side of the vacuum tank (2) tank having a + electrode plate (9) and-electrode plate (9a) connected to the DC high voltage generator (11) Waste oil supply pump (7) installed between the (8) industrial waste oil recycling apparatus characterized in that the waste oil is supplied. 제2항에 있어서, 증류층(12)을 다수의 구멍(12b)을 뚫은 증류파이프(12a)를 일정길이로 하여서, 상기의 다수의 구멍(12b)이 지그재그 형상이 되게 증류파이프(12a)를 수직상으로 배열조립하여서 됨을 특징으로한 산업용 폐오일 재생장치.3. The distillation pipe (12a) according to claim 2, wherein the distillation pipe (12a) having the distillation layer (12) having a plurality of holes (12b) is a predetermined length, and the distillation pipe (12a) is zigzag-shaped. Industrial waste oil recycling apparatus, characterized in that the vertically arranged assembling. 제2항에 있어서, 탱크(8)내부의 상, 하단에 - 전극판(9a)을 설치하며, 중앙에 +전극판(9)을 설치하여 직류고전압발생장치(11)에 연결시켜 전류공급시 코로나방전층(10)을 형성되게함을 특징으로한 산업용 폐오일 재생장치.According to claim 2, the upper and lower ends of the tank (8)-the electrode plate (9a) is installed, the + electrode plate (9) in the center is connected to the DC high voltage generator (11) when supplying current Industrial waste oil recycling apparatus, characterized in that to form a corona discharge layer (10). ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019940030888A 1994-11-23 1994-11-23 Process and apparatus for refinery of industrial waste oil KR0138026B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019940030888A KR0138026B1 (en) 1994-11-23 1994-11-23 Process and apparatus for refinery of industrial waste oil

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Application Number Priority Date Filing Date Title
KR1019940030888A KR0138026B1 (en) 1994-11-23 1994-11-23 Process and apparatus for refinery of industrial waste oil

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KR960017829A true KR960017829A (en) 1996-06-17
KR0138026B1 KR0138026B1 (en) 1998-04-28

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100837093B1 (en) * 2008-02-15 2008-06-12 동우이엔이주식회사 Oil recycling system
KR100964709B1 (en) * 2007-12-10 2010-06-21 동우전기공업(주) Purification system of waste oil and method thereof
KR20170005907A (en) 2015-06-29 2017-01-17 한국화학연구원 Recycling Method for perfluoropolyethers high vaccum pump oil and its apparatus

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100880387B1 (en) * 2007-02-15 2009-01-30 신대한정유산업(주) Ion refining oil manufacturing system using an resonance device and refining method of waste oil using the system
KR100863154B1 (en) * 2008-04-18 2008-10-13 주식회사 삼영필텍 Mobile purification system of waste oil

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100964709B1 (en) * 2007-12-10 2010-06-21 동우전기공업(주) Purification system of waste oil and method thereof
KR100837093B1 (en) * 2008-02-15 2008-06-12 동우이엔이주식회사 Oil recycling system
KR20170005907A (en) 2015-06-29 2017-01-17 한국화학연구원 Recycling Method for perfluoropolyethers high vaccum pump oil and its apparatus

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Publication number Publication date
KR0138026B1 (en) 1998-04-28

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