EP0690903B2 - Procede et installation de regeneration d'huiles lubrifiantes - Google Patents

Procede et installation de regeneration d'huiles lubrifiantes Download PDF

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Publication number
EP0690903B2
EP0690903B2 EP94910446A EP94910446A EP0690903B2 EP 0690903 B2 EP0690903 B2 EP 0690903B2 EP 94910446 A EP94910446 A EP 94910446A EP 94910446 A EP94910446 A EP 94910446A EP 0690903 B2 EP0690903 B2 EP 0690903B2
Authority
EP
European Patent Office
Prior art keywords
oils
test
extraction
oil
sodium hydroxide
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
EP94910446A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0690903B1 (fr
EP0690903A1 (fr
Inventor
Med Hedi Merchaoui
Naceur Khalef
Abdelhafidh Jaafar
Achour Ouazzane
Med Ali Boufahja
Salah C/O Senda Sahraoui Meziou
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.)
TUNISIENNE DE LUBRIFIANTS-SOTULUB Ste
Original Assignee
TUNISIENNE DE LUBRIFIANTS-SOTULUB Ste
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
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Application filed by TUNISIENNE DE LUBRIFIANTS-SOTULUB Ste filed Critical TUNISIENNE DE LUBRIFIANTS-SOTULUB Ste
Publication of EP0690903A1 publication Critical patent/EP0690903A1/fr
Publication of EP0690903B1 publication Critical patent/EP0690903B1/fr
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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M175/00Working-up used lubricants to recover useful products ; Cleaning
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M175/00Working-up used lubricants to recover useful products ; Cleaning
    • C10M175/0016Working-up used lubricants to recover useful products ; Cleaning with the use of chemical agents
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M175/00Working-up used lubricants to recover useful products ; Cleaning
    • C10M175/0025Working-up used lubricants to recover useful products ; Cleaning by thermal processes

Definitions

  • the invention relates to a method and an installation for regenerating used lubricating oils.
  • Lubricating oils generally undergo modifications and alterations during their use, which implies their more or less frequent renewal.
  • oils After use, these oils generally contain solid residues, additives, combustion residues, etc ....
  • This installation includes two tanks, allowing two treatments, one with soda and the other with the ground, and two centrifuges, ensuring the separation, one of water and the other of used earth, of the oil to be treated.
  • the objective of the present invention is therefore the development of a process for the regeneration of lubricating oils little or non-polluting used and whose implementation can be done in good economic conditions.
  • the invention relates to a process for regenerating used lubricating oils comprising a step strong base treatment.
  • the method comprises the steps of successive object processing of claim 1.
  • the invention also relates to an installation for regenerating used oils allowing the implementation of the process mentioned above.
  • the vacuum distillation unit is associated with a column bottom exhaustion evaporator.
  • the used oils collected can have various origins, it can be for example engine oil, oil gears or hydraulic oil, turbine oil, etc.
  • the regeneration process of the invention essentially aims at the elimination of light components, such like gasoline, diesel and water, but cannot remove components as heavy as the oils themselves but having different physical properties. It could be, for example, fuel whose elimination or treatment could only be obtained by a complete refining process.
  • Chlor Test which makes it possible to detect the presence of chlorides.
  • a hardened copper wire in used oil is presented to the flame.
  • a greenish flame indicates the presence of chlorides.
  • the "Drop Test” detects the presence of fuel. A drop of oil is deposited on a chromatographic paper. A concentric spot with a yellowish halo indicates the presence of fuel.
  • the "Fat Test” detects the presence of fatty acids in oils. 2 ml of used oil is heated in presence of a soda tablet: when the oil freezes, after cooling, this means that fatty acids are present.
  • Preheating means 3 bring the oils taken from the tank 2 to a temperature between 140 and 160 ° C.
  • a base stored elsewhere in a tank 4 is supplied and mixed by means 5 with the used oils. preheated.
  • a quantity of pure base of between 1 and 3% by mass is added to the used oils.
  • This rate can advantageously be specified as a function of the quality of the used oils.
  • Water and light hydrocarbons are extracted and the remaining mixture is directed to a unit 8 for extracting diesel (stripping). This elimination is carried out by distillation in a column.
  • the gas oil 9 is then discharged and the remaining mixture is led to a distillation column 10 allowing the fractionation of the mixture into lubricating base oil sections and separation of the residue where all are concentrated the impurities.
  • Base oils can be separated at different levels depending on the number of cuts desired.
  • the distillation column 10 is a traditional vacuum column which allows the dissociation and the extraction of the residues, which are directed to an accumulation tank 14.
  • the residues 15 are then removed and are capable of being used, for example, as tar or bitumen for road construction. They can also be used as fuels.
  • the vacuum distillation column 10 is preferably associated with a bottom exhaustion evaporator. column 13 to improve its efficiency. Part of the energy required to raise the temperature used oils before the addition of the pure base preferably comes from the energy recovery carried out on the lubricating base oil sections 11, 12 of the column outlet 10.
  • the used oils are advantageously filtered during their recovery and when they leave the tank. storage 2, so as to eliminate the solid particles which they may contain.
  • the process and the installation of the invention therefore make it possible, from used oils, to obtain base oils of various reusable qualities, usable residues, water, light hydrocarbons and diesel.
  • This process provides a minimum recovery rate of 90%. This rate is the mass ratio of quantities of oils recovered by this industrial process, compared to that of oils recovered in the laboratory, in optimum conditions independent of any economic consideration.
  • the preferred embodiment uses the vacuum distillation column associated with an evaporator column bottom exhaustion. It is thus possible to obtain an oil cut recovery rate of excellent lubricant base, lower investment and operating costs compared to other processes known regeneration, to obtain regenerated oils as efficient as new base oils and to eliminate of these almost all metals.
  • the installation of the invention can be implemented easily under the best conditions of reliability.
  • Yield represents their yield (Mass ratio of the quantity recovered compared to the initial quantity of oil used to regenerate).
  • T.A.N. represents their acidity (acid number content).
  • VIS 40 ° C represents their viscosity at 40 ° C expressed in centistocks.
  • Color is expressed relative to standard reference colors. Plus the numeric value shown is weak, the better the color and appearance is a qualitative indication.
  • Ba represents barium, Ca calcium, Pb lead, Zn zinc, P phosphorus, Cr chromium, Fe iron and Si silicon.

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Lubricants (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Fats And Perfumes (AREA)
  • Blast Furnaces (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
EP94910446A 1993-03-22 1994-03-21 Procede et installation de regeneration d'huiles lubrifiantes Expired - Lifetime EP0690903B2 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR9303275 1993-03-22
FR9303275A FR2703067B1 (fr) 1993-03-22 1993-03-22 Procédé et installation de régénération d'huiles lubrifiantes.
PCT/FR1994/000308 WO1994021761A1 (fr) 1993-03-22 1994-03-21 Procede et installation de regeneration d'huiles lubrifiantes

Publications (3)

Publication Number Publication Date
EP0690903A1 EP0690903A1 (fr) 1996-01-10
EP0690903B1 EP0690903B1 (fr) 1998-11-18
EP0690903B2 true EP0690903B2 (fr) 2004-07-21

Family

ID=9445212

Family Applications (1)

Application Number Title Priority Date Filing Date
EP94910446A Expired - Lifetime EP0690903B2 (fr) 1993-03-22 1994-03-21 Procede et installation de regeneration d'huiles lubrifiantes

Country Status (19)

Country Link
EP (1) EP0690903B2 (es)
AT (1) ATE173490T1 (es)
AU (1) AU6285794A (es)
BG (1) BG63637B1 (es)
CA (1) CA2159006C (es)
CZ (1) CZ290614B6 (es)
DE (1) DE69414699T3 (es)
DK (1) DK0690903T4 (es)
DZ (1) DZ1762A1 (es)
ES (1) ES2124879T5 (es)
FR (1) FR2703067B1 (es)
HU (1) HU215167B (es)
MA (1) MA23144A1 (es)
OA (1) OA10185A (es)
PL (1) PL178021B1 (es)
RO (1) RO116092B1 (es)
RU (1) RU2107716C1 (es)
UA (1) UA39881C2 (es)
WO (1) WO1994021761A1 (es)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2757175B1 (fr) * 1996-12-13 1999-03-05 Tunisienne De Lubrifiants Sotu Procede et installation de regeneration d'huiles lubrifiantes a hautes performances
DE19727618A1 (de) * 1997-06-28 1999-01-07 Mann & Hummel Filter Verfahren zum Abscheiden von Verunreinigungen aus Kühlschmierstoffen
WO1999061566A2 (en) * 1998-05-28 1999-12-02 Interline Hydrocarbon, Inc. Method for obtaining base oil and removing contaminants and additives from used oil products
HU225697B1 (en) * 2001-11-20 2007-06-28 Jozsef Koszta Method for purifying of used oils
MXPA05000637A (es) 2002-07-15 2005-03-31 Sener Grupo De Ingenieria Sa Procedimiento para regenerar aceites usados por extraccion con disolventes.
ES2199697B1 (es) * 2003-09-23 2005-02-01 Sener Grupo De Ingenieria, S.A. Procedimiento para regenerar aceites usados por desmetalizacion y destilacion.
RU2266316C1 (ru) * 2004-09-03 2005-12-20 Общество с ограниченной ответственностью "Роса-1" (ООО "Роса-1") Способ регенерации масел
FR2961521B1 (fr) 2010-06-22 2013-07-12 Conception D Equipements Pour L Environnement Et L Ind Soc D Procede de purification d'une charge hydrocarbonee usagee
MX2016005893A (es) 2013-11-08 2016-08-17 Sener Ing & Sist Proceso para aumentar el rendimiento de bases lubricantes en la regeneracion de aceites usados.
CN110484345B (zh) * 2019-07-29 2021-12-17 四川绿艺华福石化科技有限公司 一种废润滑油再生方法
RU2712025C1 (ru) * 2019-10-23 2020-01-24 Акционерное общество "Интер РАО - Электрогенерация" Установка для регенерации использованных смазочных масел с высокими рабочими параметрами
RU2745628C1 (ru) * 2020-08-25 2021-03-29 Открытое акционерное общество "Всероссийский дважды ордена Трудового Красного Знамени теплотехнический научно-исследовательский институт" (ОАО "ВТИ") Установка для регенерации отработавших смазочных масел
RU2750729C1 (ru) * 2020-10-07 2021-07-01 Публичное акционерное общество "Нефтяная компания "Роснефть" (ПАО "НК "Роснефть") Способ регенерации отработанного триарилфосфатного огнестойкого турбинного масла
CN114225451A (zh) * 2021-12-23 2022-03-25 安徽国孚生态工程技术有限公司 一种废润滑油循环蓄热蒸馏装置及方法
CN114225452A (zh) * 2021-12-23 2022-03-25 安徽国孚生态工程技术有限公司 一种废润滑油四段蒸发回收方法
FR3137106A1 (fr) 2022-06-28 2023-12-29 Be Energy Système de traitement pour la décontamination et l’amélioration des propriétés d’huiles minérales usagées

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB243666A (en) * 1924-11-29 1926-10-21 Sharples Specialty Co Improved method of and apparatus for purifying oil
US1698257A (en) * 1926-05-05 1929-01-08 Laval Separator Co De Process of reclaiming used lubricating oil
US1919655A (en) * 1929-07-12 1933-07-25 Bocjl Corp Purification of oil
US3565791A (en) * 1968-12-12 1971-02-23 Kenneth Urquhart Method and apparatus for distiling oil and water mixtures
US3791965A (en) * 1972-04-07 1974-02-12 Petrocon Corp Process for re-refining used petroleum products
DE2818521A1 (de) * 1978-04-27 1979-11-08 Degussa Verfahren zur wiederaufbereitung von gebrauchten schmieroelen (ii)
US4256578A (en) * 1979-11-29 1981-03-17 Amsted Industries Incorporated Waste oil recovery process

Also Published As

Publication number Publication date
EP0690903B1 (fr) 1998-11-18
OA10185A (fr) 1996-12-18
HU9502763D0 (en) 1995-11-28
DE69414699D1 (de) 1998-12-24
FR2703067A1 (fr) 1994-09-30
CZ243395A3 (en) 1996-01-17
ES2124879T3 (es) 1999-02-16
PL178021B1 (pl) 2000-02-29
DE69414699T2 (de) 1999-05-27
WO1994021761A1 (fr) 1994-09-29
DK0690903T4 (da) 2004-11-22
PL310803A1 (en) 1996-01-08
UA39881C2 (uk) 2001-07-16
ES2124879T5 (es) 2005-02-16
CA2159006A1 (fr) 1994-09-29
CZ290614B6 (cs) 2002-09-11
DE69414699T3 (de) 2005-02-10
AU6285794A (en) 1994-10-11
HU215167B (hu) 1998-10-28
ATE173490T1 (de) 1998-12-15
DZ1762A1 (fr) 2002-02-17
RU2107716C1 (ru) 1998-03-27
EP0690903A1 (fr) 1996-01-10
DK0690903T3 (da) 1999-08-02
BG100012A (bg) 1996-11-29
HUT72015A (en) 1996-03-28
CA2159006C (fr) 2005-06-21
FR2703067B1 (fr) 1995-08-04
RO116092B1 (ro) 2000-10-30
MA23144A1 (fr) 1994-10-01
BG63637B1 (bg) 2002-07-31

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