EP0944696B1 - Procede et installation de regeneration d'huiles lubrifiantes a hautes performances - Google Patents
Procede et installation de regeneration d'huiles lubrifiantes a hautes performances Download PDFInfo
- Publication number
- EP0944696B1 EP0944696B1 EP97950242A EP97950242A EP0944696B1 EP 0944696 B1 EP0944696 B1 EP 0944696B1 EP 97950242 A EP97950242 A EP 97950242A EP 97950242 A EP97950242 A EP 97950242A EP 0944696 B1 EP0944696 B1 EP 0944696B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- oil
- extraction
- waste oil
- strong base
- impurities
- 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
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Classifications
-
- 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
-
- 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
- C10M175/0016—Working-up used lubricants to recover useful products ; Cleaning with the use of chemical agents
Definitions
- the present invention relates to a method and a lubricating oil regeneration plant used with high performance.
- the object of the invention is therefore to propose such a process and the corresponding installation.
- a complementary addition of a strong base in aqueous solution due to 0.1 to 1% of pure bases by mass of lubricating oils is performed after step e).
- the amount of strong bases in aqueous solution can be between 0.5 to 3% of pure bases by mass used lubricating oils. This addition can be totally or partially cold or hot.
- the heating temperature of waste oils at regenerate between 120 and 250 ° C is a temperature at which the addition of the hot base is carried out in whole or in part.
- the used oils collected may have various origins. It can be, for example, oil engine, gear oil, hydraulic oil, turbine oil, etc.
- the regeneration process of the invention aims to eliminate light components, such as petrol, diesel and water, it allows also the elimination of degradation products from oil and additives but does not remove some components as heavy as the oils themselves and having different physical properties. he could be, for example, fuel oil elimination or treatment could not be obtained only by a complete refining process.
- Waste oil collected 1 having undergone with successful all of the tests come together in a tank 2.
- a base or a mixture of bases stored by elsewhere in a tank 4a is brought and mixed by means 5a to waste oils at temperature ambient between 10 and 40 ° C.
- Heating means 3 carry the oils taken from tank 2 and possibly mixed with the base, at a temperature between 120 and 250 ° C and preferably between 140 and 160 ° C.
- a base or a mixture of bases stored by elsewhere in a tank 4b is brought and mixed by means 5b to heated waste oils.
- an amount of pure bases between 0.5 and 3% by mass is added to waste oils.
- This rate as well as its distribution between the two cold and hot injection points, can be advantageously specified according to the quality of used oils and the nature of the base used.
- the base used is a strong base, preferably sodium or potassium hydroxide. We can also consider using a mixture of these bases.
- Waste oils brought to a temperature high, added with strong base, feed a water and oil extraction unit 6 light by triggering (flash).
- a water and oil extraction unit 6 light by triggering (flash).
- water evaporation is produced by expansion brutal mixing in a balloon.
- the diesel 9 is then discharged and the remaining mixture is led to a distillation column 10 allowing the fractionation of the mixture into sections lubricating base oils 11, 12 and separation of residue 15 where all the impurities are concentrated.
- Base oils can be separated at different levels depending on the number of cuts sought.
- the distillation column 10 is a column traditional vacuum which allows dissociation and the extraction of residues which are directed to a accumulation tank 14.
- the residues 15 are then removed and are likely to be used, for example, as tar or bitumen for road construction. They can also be used as fuel.
- the vacuum distillation column 10 is preferably associated with a depletion evaporator column bottom 13 to improve sound efficiency. Part of the energy needed to the rise in the temperature of used oils before the flash preferably comes from recovery of energy carried out on the cuts of base oils lubricants 11, 12 of the column outlet 10.
- Used oils are advantageously filtered during their recovery and when they leave the storage tank 2, so as to eliminate the solid particles they may contain.
- An additional basic solution is added made at lower proportions than additions initials, before the flash, the additional addition being in proportions of the order of 0.1 to 1% by mass of pure bases compared to oils used lubricants. It can be done in different points of the corresponding installation in each case has an embodiment.
- This process ensures better stability of regenerated base oils and fluidize the impurities, which allows a easier operation of the process.
- the oil temperature is then advantageously between 270 and 310 ° C.
- the additional basic addition is carried out under the same concentration conditions and than in the first embodiment, but after the extraction operation of diesel (stripping).
- a base stored in a tank 18 is brought and mixed by means 19 with oil stripped reheated directed towards the column of splitting.
- an evaporator 13 preferably thin-film, coupled to a vacuum column 10 eliminates most of the impurities.
- the oil obtained is then subjected to oxidation accelerated in a bin 22, before a quantity complementary to pure bases is added to it.
- a base stored in a tank 23b is brought and mixed with the oil by means of mixture 24.
- the oil is then fractionated in the column of distillation 20.
- the oil temperature when adding the base is advantageously between 200 and 300 ° C. for injection from reservoir 23b just before column 20 and is between 120 and 200 ° C for addition from a tank 23a directly in the oxidation tank 22.
- the evaporator 13 is advantageously a thin film evaporator. It is also possible to use several evaporators successively.
- the residues 21 of column 20 are, according to the efficiency of this column and the requirements imposed regenerated oils, either recirculated and injected at the entry in column 10, either routed to the storage of residues such as residues 15 from the distillation column 10 and the evaporator 13.
- sample 2 was obtained by a process according to the invention implemented according to one of Figures 2 and 3.
- Sample 3 was obtained by a process according to the invention implemented according to Figure 4. These samples are compared to sample 1 obtained with a single basic injection according to the prior art.
- samples 5 and 6 obtained according to the invention are to be compared with sample 4 obtained according to the prior art.
Landscapes
- 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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Lubricants (AREA)
Description
- l'adjonction complémentaire de bases fortes est réalisée au cours de l'étape d'extraction et de récupération de gasoil,
- l'adjonction complémentaire de bases fortes est réalisée postérieurement à l'étape d'extraction et de récupération de gasoil,
- après l'étape de déshydratation, d'extraction des hydrocarbures légers et du stripping du gasoil, l'huile strippée est débarrassée de ses impuretés (résidus) dans une colonne sous vide munie d'un système de rebouillage, puis soumise à une étape d'oxydation avant l'adjonction complémentaire de bases fortes, puis fractionnée,
- l'élimination des impuretés est obtenue par distillation sous vide assurant la séparation en huiles de bases lubrifiantes d'une part, et en un résidu concentrant toutes les impuretés d'autre part.
- la Figure 1 est une représentation schématique d'un procédé et d'une installation de régénération d'huiles lubrifiantes usagées de l'art antérieur ;
- la Figure 2 est une représentation schématique d'un procédé et d'une installation de régénération d'huiles lubrifiantes usagées dans un premier mode de réalisation de l'invention ;
- la Figure 3 est une représentation schématique d'un procédé et d'une installation de régénération d'huiles lubrifiantes usagées selon un deuxième mode de réalisation de l'invention ;
- la Figure 4 est une représentation schématique d'un procédé et d'une installation de régénération d'huiles lubrifiantes usagées selon un troisième mode de réalisation de l'invention.
- Le "Chlor test" permet de détecter la présence des chlorures. Un fil de cuivre trempé dans l'huile usagée est présenté à la flamme. Une flamme verdâtre indique la présence de chlorures.
- Le "Drop test" permet de détecter la présence de fuel. Une goutte d'huile est déposée sur un papier chromatographique. Une tache concentrique avec une auréole jaunâtre indique la présence de fuel.
- Le "Fat test" permet de détecter la présence des acides gras dans les huiles. On chauffe 2 ml d'huile usagée en présence d'une pastille de soude : lorsque l'huile se fige, après refroidissement, cela signifie que des acides gras sont présents.
- La détermination de la concentration en PCB (polychlorobiphényle). Ce test est réalisé et ses limites sont fixées en fonction de la réglementation en vigueur.
Claims (7)
- Procédé de régénération d'huiles lubrifiantes usagées ayant une faible teneur en fuel, acides gras et produits chlorés, dans lequel les huiles lubrifiantes usagées sont soumises aux étapes de traitement successives suivantes dans l'ordre:a) sélection des huiles usagées aptes au traitement satisfaisant les tests de régénérabilité;b) adjonction d'une première quantité d'une base forte en solution aqueuse;c) chauffage des huiles usagées à régénérer à une température comprise entre 120 et 250°C;d) adjonction d'une deuxième quantité de la base forte en solution aqueuse, la première et la deuxième quantités de base forte en solution aqueuse représentant ensemble de 0,5 à 3% de bases pures en masse d'huiles lubrifiantes usagées;e) déshydratation et extraction des hydrocarbures légers;f) extraction et récupération de gasoil (stripping);g) extraction et élimination des impuretés, l'élimination des impuretés étant obtenue par distillation sous vide assurant la séparation en huiles de bases lubrifiantes, d'une part, et en un résidu concentrant toutes les impuretés, d'autre part,
- Procédé de régénération selon la revendication 1,
caractérisé en ce que l'adjonction complémentaire de bases fortes est réalisée au cours de l'étape d'extraction et de récupération de gasoil. - Procédé de régénération selon la revendication 1,
caractérisé en ce que l'adjonction complémentaire de bases fortes est réalisée postérieurement à l'étape d'extraction et de récupération de gasoil. - Procédé de régénération selon la revendication 1,
caractérisé en ce que, après l'étape de déshydratation, d'extraction des hydrocarbures légers, et du stripping du gasoil, l'huile strippée est débarrassée de ses impuretés dans une colonne sous vide munie d'un système de rebouillage, puis soumise à une étape d'oxydation avant l'adjonction complémentaire de bases fortes, puis fractionnée. - Installation de régénération d'huiles usagées comportant:un réservoir (2) de stockage des huiles usagées,des moyens de chauffage (3) des huiles usagées,des moyens de stockage (4) d'une base forte,des moyens de mélange (5) de la base forte en une proportion déterminée aux huiles usagées,des moyens d'élimination des impuretés (10, 13, 14), les moyens de mélange (5) de la base forte aux huiles usagées et les moyens d'élimination des impuretés (10, 13, 14) une unité d'extraction de l'eau par détente (6) (flash) et une unité d'extraction du gasoil (8) (stripping) et les moyens d'extraction des impuretés (10, 13, 14) comportent une unité de distillation sous vide (10) associée à un évaporateur (13) d'épuisement de fond de colonne,
- Installation selon la revendication 5, caractérisée en ce qu'elle comporte un évaporateur (13) au moins placé après l'unité d'extraction du gasoil.
- Installation selon la revendication 6, caractérisée en ce que l'évaporateur (13) est à couches minces.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9615380 | 1996-12-13 | ||
FR9615380A FR2757175B1 (fr) | 1996-12-13 | 1996-12-13 | Procede et installation de regeneration d'huiles lubrifiantes a hautes performances |
PCT/FR1997/002224 WO1998026031A1 (fr) | 1996-12-13 | 1997-12-05 | Procede et installation de regeneration d'huiles lubrifiantes a hautes performances |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0944696A1 EP0944696A1 (fr) | 1999-09-29 |
EP0944696B1 true EP0944696B1 (fr) | 2001-04-04 |
Family
ID=9498674
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP97950242A Expired - Lifetime EP0944696B1 (fr) | 1996-12-13 | 1997-12-05 | Procede et installation de regeneration d'huiles lubrifiantes a hautes performances |
Country Status (23)
Country | Link |
---|---|
EP (1) | EP0944696B1 (fr) |
AR (1) | AR010353A1 (fr) |
AT (1) | ATE200302T1 (fr) |
AU (1) | AU5326998A (fr) |
BG (1) | BG64486B1 (fr) |
CA (1) | CA2274831C (fr) |
CZ (1) | CZ300297B6 (fr) |
DE (1) | DE69704500T2 (fr) |
DK (1) | DK0944696T3 (fr) |
DZ (1) | DZ2369A1 (fr) |
ES (1) | ES2156008T3 (fr) |
FR (1) | FR2757175B1 (fr) |
GR (1) | GR3036074T3 (fr) |
HK (1) | HK1022928A1 (fr) |
HU (1) | HU222544B1 (fr) |
MA (1) | MA24424A1 (fr) |
OA (1) | OA11060A (fr) |
PL (1) | PL186318B1 (fr) |
PT (1) | PT944696E (fr) |
RU (1) | RU2187544C2 (fr) |
TN (1) | TNSN97189A1 (fr) |
UA (1) | UA59382C2 (fr) |
WO (1) | WO1998026031A1 (fr) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6238551B1 (en) * | 1999-02-16 | 2001-05-29 | Miami University | Method of removing contaminants from petroleum distillates |
EP1559768B1 (fr) | 2002-07-15 | 2006-04-26 | Sener Grupo de Ingenier A, s.a. | Procede de regeneration d'huiles usees par extraction au moyen de dissolvants |
ES2199697B1 (es) | 2003-09-23 | 2005-02-01 | Sener Grupo De Ingenieria, S.A. | Procedimiento para regenerar aceites usados por desmetalizacion y destilacion. |
CN101104832B (zh) * | 2006-07-11 | 2012-04-25 | 北京百慧生化制药有限责任公司 | 废润滑油再炼制的方法及其设备 |
EP3078730A4 (fr) | 2013-11-08 | 2017-07-19 | Sener Ingenieria Y Sistemas, S.A. | Procédé pour augmenter le rendement en bases lubrifiantes lors de la régénération d'huiles usagées |
CN106906040B (zh) * | 2017-02-28 | 2020-01-10 | 中石化炼化工程(集团)股份有限公司 | 一种废润滑油的再生方法 |
CN107551657A (zh) * | 2017-10-18 | 2018-01-09 | 杭州正进能源技术有限公司 | 润滑油净化再生装置 |
TN2017000484A1 (fr) | 2017-11-20 | 2019-04-12 | Soc Tunisienne De Lubrifiants Sotulub | Amélioration du procédé de regénération des huiles usagées avec respect de différents aspects environnementaux. |
CN110628455A (zh) * | 2019-09-26 | 2019-12-31 | 南通市泓正再生资源有限公司 | 一种废矿物油再生回收处理系统 |
RU2713904C1 (ru) * | 2019-10-23 | 2020-02-11 | Акционерное общество "Интер РАО - Электрогенерация" | Способ регенерации использованных смазочных масел с высокими рабочими параметрами |
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 |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2818521A1 (de) * | 1978-04-27 | 1979-11-08 | Degussa | Verfahren zur wiederaufbereitung von gebrauchten schmieroelen (ii) |
IT1255534B (it) * | 1992-09-30 | 1995-11-09 | Processo di riraffinazione di oli usati | |
FR2703067B1 (fr) * | 1993-03-22 | 1995-08-04 | Sotulub | Procédé et installation de régénération d'huiles lubrifiantes. |
-
1996
- 1996-12-13 FR FR9615380A patent/FR2757175B1/fr not_active Expired - Fee Related
-
1997
- 1997-05-12 UA UA99063267A patent/UA59382C2/uk unknown
- 1997-11-24 TN TNTNSN97189A patent/TNSN97189A1/fr unknown
- 1997-12-05 ES ES97950242T patent/ES2156008T3/es not_active Expired - Lifetime
- 1997-12-05 DK DK97950242T patent/DK0944696T3/da active
- 1997-12-05 EP EP97950242A patent/EP0944696B1/fr not_active Expired - Lifetime
- 1997-12-05 PL PL97334068A patent/PL186318B1/pl unknown
- 1997-12-05 RU RU99115454/04A patent/RU2187544C2/ru active
- 1997-12-05 CA CA002274831A patent/CA2274831C/fr not_active Expired - Lifetime
- 1997-12-05 AU AU53269/98A patent/AU5326998A/en not_active Abandoned
- 1997-12-05 AT AT97950242T patent/ATE200302T1/de active
- 1997-12-05 PT PT97950242T patent/PT944696E/pt unknown
- 1997-12-05 HU HU0001433A patent/HU222544B1/hu active IP Right Grant
- 1997-12-05 CZ CZ0211899A patent/CZ300297B6/cs not_active IP Right Cessation
- 1997-12-05 WO PCT/FR1997/002224 patent/WO1998026031A1/fr active IP Right Grant
- 1997-12-05 DE DE69704500T patent/DE69704500T2/de not_active Expired - Lifetime
- 1997-12-10 DZ DZ970219A patent/DZ2369A1/fr active
- 1997-12-12 MA MA24900A patent/MA24424A1/fr unknown
- 1997-12-12 AR ARP970105867A patent/AR010353A1/es unknown
-
1999
- 1999-07-11 OA OA9900121A patent/OA11060A/fr unknown
- 1999-07-13 BG BG103577A patent/BG64486B1/bg unknown
-
2000
- 2000-03-29 HK HK00101925A patent/HK1022928A1/xx not_active IP Right Cessation
-
2001
- 2001-06-19 GR GR20010400918T patent/GR3036074T3/el unknown
Also Published As
Publication number | Publication date |
---|---|
WO1998026031A1 (fr) | 1998-06-18 |
HUP0001433A2 (hu) | 2000-08-28 |
DE69704500D1 (de) | 2001-05-10 |
DK0944696T3 (da) | 2001-05-14 |
PL186318B1 (pl) | 2003-12-31 |
ES2156008T3 (es) | 2001-06-01 |
DE69704500T2 (de) | 2002-03-28 |
MA24424A1 (fr) | 1998-07-01 |
HK1022928A1 (en) | 2000-08-25 |
GR3036074T3 (en) | 2001-09-28 |
CZ211899A3 (cs) | 2000-03-15 |
DZ2369A1 (fr) | 2002-12-28 |
FR2757175B1 (fr) | 1999-03-05 |
AU5326998A (en) | 1998-07-03 |
CA2274831A1 (fr) | 1998-06-18 |
HU222544B1 (hu) | 2003-08-28 |
HUP0001433A3 (en) | 2001-02-28 |
UA59382C2 (uk) | 2003-09-15 |
CZ300297B6 (cs) | 2009-04-15 |
CA2274831C (fr) | 2005-07-12 |
OA11060A (fr) | 2003-03-07 |
PL334068A1 (en) | 2000-01-31 |
EP0944696A1 (fr) | 1999-09-29 |
ATE200302T1 (de) | 2001-04-15 |
AR010353A1 (es) | 2000-06-07 |
BG103577A (en) | 2000-05-31 |
RU2187544C2 (ru) | 2002-08-20 |
FR2757175A1 (fr) | 1998-06-19 |
PT944696E (pt) | 2001-09-28 |
BG64486B1 (bg) | 2005-04-30 |
TNSN97189A1 (fr) | 1999-12-31 |
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