EP1365005B1 - Verfahren zur Herstellung von Schmierölen - Google Patents

Verfahren zur Herstellung von Schmierölen Download PDF

Info

Publication number
EP1365005B1
EP1365005B1 EP03077527A EP03077527A EP1365005B1 EP 1365005 B1 EP1365005 B1 EP 1365005B1 EP 03077527 A EP03077527 A EP 03077527A EP 03077527 A EP03077527 A EP 03077527A EP 1365005 B1 EP1365005 B1 EP 1365005B1
Authority
EP
European Patent Office
Prior art keywords
range
process according
fischer
hydroisomerisation
molecular sieve
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
EP03077527A
Other languages
English (en)
French (fr)
Other versions
EP1365005A1 (de
Inventor
Jean-Marie Alexandre Bertaux
Gilbert Robert Bernard Germaine
Arend Hoek
Martinus Maria Petrus Janssen
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Priority to EP03077527A priority Critical patent/EP1365005B1/de
Publication of EP1365005A1 publication Critical patent/EP1365005A1/de
Application granted granted Critical
Publication of EP1365005B1 publication Critical patent/EP1365005B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • C10G67/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including solvent extraction as the refining step in the absence of hydrogen
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/043—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a change in the structural skeleton
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/10—Lubricating oil

Definitions

  • the present invention relates to a process for producing lubricating base oils from Fischer-Tropsch waxes, and in particular lubricating base oils having a viscosity index (VI) of at least 150.
  • VI viscosity index
  • the Fischer-Tropsch wax used as the feed in the working examples of EP-A-0,515,256 has a broad boiling range.
  • the difference between 90 %wt boiling point and 10 %wt boiling point is as high as 249 °C. This implies that a large variety of paraffinic molecules is present in said wax. Due to the presence of such large variety of different paraffinic molecules, it will be very difficult to meet the specifications as regards volatility when the base oils produced should be used as lubricating base oils.
  • a process for producing lubricating base oils having a VI of at least 130 from Fischer-Tropsch waxes, in which process the wax is first hydrotreated under severe conditions, then the hydrotreated wax is hydro-isomerised by contacting it with a fluorided Group VIII (noble) metal-on-alumina catalyst, subsequently the effluent from the hydro-isomerisation step is fractionated to produce a lubricating oil fraction and finally this lubricating oil fraction is dewaxed to produce the desired lubricating base oil. Unconverted wax recovered in the final dewaxing step may be recycled to the hydro-isomerisation step.
  • a fluorided Group VIII (noble) metal-on-alumina catalyst subsequently the effluent from the hydro-isomerisation step is fractionated to produce a lubricating oil fraction and finally this lubricating oil fraction is dewaxed to produce the desired lubricating base oil.
  • Unconverted wax recovered in the final dewaxing step may
  • the Fischer-Tropsch wax used should be a high boiling wax, since it is the intention to convert in the severe hydrotreating step that material present in the wax that has a boiling point above about 565 °C.
  • a Fischer-Tropsch wax is used which was obtained as the 370 °C+ fraction from the distillation of a Fischer-Tropsch synthesis product. Accordingly, the waxes used as the feedstocks are relatively high boiling waxes having a broad boiling range and a large heavy tail.
  • the fractionation after the hydroisomerisation step, or -if applied- after the hydrofinishing step should remove both the lightest fraction (boiling below 338 °C) and the heaviest fraction (boiling above 538 °C) from the hydroprocessed wax in order to obtain a final base oil product having acceptable volatility properties.
  • the wax used as the feed may be a synthetic wax from a Fischer-Tropsch process or could be a slack wax obtained from a dewaxing process. No specific demands are made upon the Fischer-Tropsch waxes to be useful as a feed in the process disclosed.
  • the Fischer-Tropsch wax used in Example 1 of US-A-5,059,299 is a high boiling wax having a relatively broad boiling range, which, as has already been stated above, results in the base oil product having unacceptable volatility properties.
  • the isomerisation catalyst used suitably comprises a hydrogenating component on a halogenated refractory oxide support.
  • the preferred catalyst is disclosed to be platinum on fluorided alumina.
  • the present invention aims to provide such improved process. More specifically, the present invention aims to provide a process for preparing base oils having a VI of at least 150 from a Fischer-Tropsch wax, which process involves a single hydroprocessing stage and a fractionation stage, wherein only the lighter components need to be removed from the hydroprocessed effluent. Furthermore, it is an object of the present invention to provide base oils having excellent properties, particularly in terms of VI and volatility, at commercially attractive yields.
  • the present invention relates to a process for the preparation of lubricating base oils having a VI of at least 150 from a Fischer-Tropsch wax feed, which process comprises the steps of:
  • the Fischer-Tropsch wax used as the feed for the present process is obtained via the well-known Fischer-Tropsch hydrocarbon synthesis process.
  • Fischer-Tropsch hydrocarbon synthesis involves the preparation of hydrocarbons from a mixture of carbon monoxide and hydrogen at elevated temperature and pressure in the presence of a suitable catalyst.
  • the Fischer-Tropsch catalyst normally is selective for preparing paraffinic molecules, mostly straight-chain paraffins, and the product from a Fischer-Tropsch synthesis reaction therefore usually is a mixture of a large variety of paraffinic molecules.
  • Those hydrocarbons that are gaseous or liquid at room temperature are recovered separately, for instance as fuel gas (C 5 -), solvent feedstocks and detergent feedstocks (up to C 17 ).
  • the more heavy paraffins (C 18 +) are recovered as one or more wax fractions, commonly referred to as Fischer-Tropsch wax(es) or synthetic wax(es).
  • Fischer-Tropsch wax(es) or synthetic wax(es) are useful as the feed, which meet the aforementioned requirements with respect to their boiling range and congealing point.
  • preferred Fischer-Tropsch wax feeds are those having a congealing point in the range of from 55 to 150 °C, preferably from 60 to 120 °C and/or such boiling range that the T 90 -T 10 is in the range of from 50 to 130 °C.
  • Those Fischer-Tropsch waxes melting below 100 °C suitably have a kinematic viscosity at 100 °C (Vk100) of at least 3 mm 2 /s, preferably between 3 and 12 mm 2 /s, more preferably between 4 and 10 mm 2 /s.
  • Fischer-Tropsch waxes melting above 100 °C suitably have a kinematic viscosity at a temperature T, which is 10 to 20 °C higher than their melting point, in the range of from 8 to 15 mm 2 /s, preferably from 9 to 14 mm 2 /s.
  • the hydroisomerisation catalyst used in step (a) may in principle be any catalyst known in the art to be suitable for isomerising paraffinic molecules.
  • suitable hydroisomerisation catalysts are those comprising a hydrogenation component supported on a refractory oxide carrier, such as amorphous silica-alumina, alumina, fluorided alumina, molecular sieves (zeolites) or mixtures of two or more of these.
  • a refractory oxide carrier such as amorphous silica-alumina, alumina, fluorided alumina, molecular sieves (zeolites) or mixtures of two or more of these.
  • One type of preferred catalysts to be applied in the hydroisomerisation step in accordance with the present invention are hydroisomerisation catalysts comprising platinum and/or palladium as the hydrogenation component.
  • a very much preferred hydroisomerisation catalyst comprises platinum and palladium supported on an amorphous silica-alumina (ASA) carrier.
  • the platinum and/or palladium is suitably present in an amount of from 0.1 to 5.0% by weight, more suitably from 0.2 to 2.0% by weight, calculated as element and based on total weight of carrier. If both present, the weight ratio of platinum to palladium (calculated as element) may vary within wide limits, but suitably is in the range of from 0.05 to 10, more suitably 0.1 to 5.
  • suitable noble metal on ASA catalysts are, for instance, disclosed in WO-A-94/10264 and EP-A-0,582,347.
  • Other suitable noble metal-based catalysts, such as platinum on a fluorided alumina carrier are disclosed in e.g. US-A-5,059,299 and WO-A-92/20759.
  • a second type of suitable hydroisomerisation catalysts are those comprising at least one Group VIB metal, preferably tungsten and/or molybdenum, and at least one non-noble Group VIII metal, preferably nickel and/or cobalt, as the hydrogenation component.
  • both metals are present as oxides, sulphides or a combination thereof.
  • the Group VIB metal is suitably present in an amount of from 1 to 35% by weight, more suitably from 5 to 30% by weight, calculated as element and based on total weight of catalyst.
  • the non-noble Group VIII metal is suitably present in an amount of from 1 to 25 %wt, preferably 2 to 15 %wt, calculated as element and based on total weight of carrier.
  • a hydroisomerisation catalyst of this type which has been found particularly suitable is a catalyst comprising nickel and tungsten supported on fluorided alumina.
  • a third class of suitable hydroisomerisation catalysts are those based on an intermediate pore size zeolitic material, suitably comprising at least one Group VIII metal component, preferably Pt and/or Pd, as the hydrogenation component.
  • Suitable zeolitic materials include ZSM-5, ZSM-22, ZSM-23, ZSM-35, SSZ-32, ferrierite, zeolite beta, mordenite and silica-alumino-phosphates, such as SAPO-11 and SAPO-31.
  • suitable hydroisomerisation catalysts are, for instance, described in WO-A-92/01657.
  • the conditions applied in step (a) are those known to be suitable in hydro-isomerisation operations.
  • the conditions then, involve operating temperatures in the range of from 275 to 450 °C, preferably 300 to 425 °C, a hydrogen partial pressure in the range of from 25 to 200 bar, a weight hourly space velocity (WHSV) in the range of from 0.1 to 10 kg/l/h, preferably 0.2 to 5 kg/l/h, and a gas rate in the range of from 100 to 5,000 Nl/kg, preferably 500 to 3,000 Nl/kg.
  • WHSV weight hourly space velocity
  • step (b) of the present process the hydroisomerised effluent from step (a) is separated into at least one lighter fraction and a heavy fraction.
  • the effective cutpoint of the heavy fraction is suitably in the range of from 325 to 450 °C and even more suitably is in the range of from 350 to 420 °C, particularly when the lubricating base oils to be obtained are to be used in engine oils.
  • the effective cutpoint of the heavy fraction is the temperature above which at least at least 85% by weight and preferably at least 90% by weight, of the hydrocarbons present in this heavy fraction has its boiling point.
  • This separation or fractionation can be achieved by techniques known in the art, such as atmospheric and vacuum distillation or vacuum flashing.
  • the heavy fraction obtained in step (b) is subsequently subjected to a catalytic dewaxing treatment in step (c) to arrive at the desired pour point.
  • suitable dewaxing catalysts for use in dewaxing step (c) are those catalysts based on a molecular sieve having pores with a diameter in the range of from 0.35 to 0.80 nm and containing covalently bound alumina moieties in its framework, which molecular sieve has been modified to reduce the mole percentage of alumina, suitably by a surface dealumination treatment.
  • This type of catalysts and dewaxing operations wherein such catalysts are used are disclosed in European patent application EP-A-832171.
  • a particularly suitable class of dewaxing catalysts comprise a hydrogenation component supported on surface deactivated molecular sieve and optionally a low acidity refractory oxide binder material.
  • the hydrogenation component may comprise at least one Group VIB metal component, for example one or more of tungsten, molybdenum and chromium and/or at least one Group VIII metal component, for example one or more of palladium, platinum, nickel and cobalt. It has been found particularly preferred for the purpose of the present invention to employ a hydrogenation component comprising platinum and/or palladium, suitably present in an amount of from 0.2 to 3.0% by weight as calculated as element and based on total weight of support, i.e. modified molecular sieve plus optional binder.
  • Suitable molecular sieves include MFI-type zeolites, such as ZSM-5 and silicalite, offretite, ferrierite, ZSM-35 and zeolites of the MTT-type, such as ZSM-23 and SSZ-32. Of these, the MTT-type zeolites, ferrierite, ZSM-5 and mixtures thereof are preferred for the purpose of the present invention. If present at all, suitable binder materials include low acidity refractory oxides such as silica, zirconia, titanium dioxide, germanium dioxide, boria and mixtures of two or more of these with silica being most preferred. The weight ratio of surface deactivated molecular sieve to binder may range from 10/90 to 100/0.
  • the lubricating base oils obtained by the process according to the present invention can be used in a variety of oils.
  • those lubricating base oils obtained from Fischer-Tropsch waxes having a T 90 between about 400 and 500 °C are very useful in electrical oils, transformer oils and refrigerator oils.
  • those base oils obtained from Fischer-Tropsch waxes having a T 90 above 450 °C, suitably between 450 and 575 °C, are very useful as lubricating base oils used for the more sophisticated lubricants required in, for instance, automotive engines.
  • a Fischer-Tropsch wax having the properties as listed in Table I was contacted with a fluorided NiW/alumina catalyst (5.0 %wt Ni, 23.1 %wt W, 4.6 %wt F, all based on total weight of carrier) at a temperature of 383 °C, a hydrogen partial pressure of 140 bar, a WHSV of 1 kg/l/h and a gas rate of 1,500 Nl/kg.
  • the effluent was fractionated and the 390 °C+ fraction (obtained at a yield of 87.8% by weight based on total effluent) was subsequently solvent dewaxed using MEK/toluene at -20 °C.
  • the resulting base oil had a VI of 165, a pour point of -15 °C, a kinematic viscosity at 100 °C (Vk100) of 4.95 mm 2 /s and a Noack volatility (as determined by CEC-L-40-T87) of 8.3% by weight.
  • Total yield of lubricating base oil amounted up to 41% by weight based on Fischer-Tropsch wax feed.
  • Example 2 The same Fischer-Tropsch wax as used in Example 1 was contacted with a PtPd/ASA (0.3 %wt Pt, 1 %wt Pd, ASA: silica/alumina molar ratio is 55/45) catalyst at a temperature of 332 °C, whilst the other conditions were the same as applied in Example 1.
  • the effluent was fractionated and the 390 °C+ fraction (obtained at a yield of 88.3% by weight based on total effluent) was subsequently solvent dewaxed using MEK/toluene at -20 °C.
  • the resulting base oil had a VI of 167, a pour point of -15 °C, a kinematic viscosity at 100 °C (Vk100) of 4.86 mm 2 /s and a Noack volatility of 7.4% by weight.
  • Total yield of lubricating base oil amounted up to 39% by weight based on Fischer-Tropsch wax feed.
  • Example 1 The procedure of Example 1 was repeated except that the 390 °C+ fraction obtained was catalytically dewaxed instead of solvent dewaxed.
  • Catalytic dewaxing was carried out by passing said 390 °C+ fraction over a dewaxing catalyst comprising 0.7% by weight of Pt on surface dealuminated ZSM-23 (surface dealumination carried out according to the method disclosed in U.S. Patent No. 5,157,191 using ammonium hexafluorosilicate) at a temperature of 310 °C, a hydrogen partial pressure of 40 bar, a WHSV of 1 kg/l/h and a gas rate of 693 Nl/kg.
  • a dewaxing catalyst comprising 0.7% by weight of Pt on surface dealuminated ZSM-23 (surface dealumination carried out according to the method disclosed in U.S. Patent No. 5,157,191 using ammonium hexafluorosilicate) at a temperature of 310 °C, a hydrogen
  • the resulting base oil had a VI of 151, a pour point of -27 °C, a kinematic viscosity at 100 °C (Vk100) of 4.96 mm 2 /s and a Noack volatility (as determined by CEC-L-40-T87) of 8.8% by weight.
  • Total yield of lubricating base oil amounted up to 62.4% by weight based on Fischer-Tropsch wax feed.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Lubricants (AREA)

Claims (12)

  1. Verfahren zur Herstellung von Schmiermittelgrundölen mit einem VI von wenigstens 150 aus einem Fischer-Tropsch-Wachs-Einsatzmaterial, welches Verfahren die folgenden Schritte umfaßt:
    (a) Inkontaktbringen des Fischer-Tropsch-Wachs-Einsatzmaterials mit einem Hydroisomerisationskatalysator unter Hydroisomerisationsbedingungen, umfassend Betriebstemperaturen von 275 bis 450 °C, einen Wasserstoffpartialdruck im Bereich von 25 bis 200 bar, eine gewichtsbezogene stündliche Raumgeschwindigkeit im Bereich von 0,1 bis 10 kg/l/h und einen Gasdurchsatz im Bereich von 100 bis 5000 Nl/kg,
    (b) Auftrennen des im Schritt (a) erhaltenen hydroisomerisierten Abstroms in wenigstens eine leichtere Fraktion und in eine schwere Fraktion und
    (c) katalytisches Entwachsen der schweren Fraktion in Gegenwart von Wasserstoff und von einem Entwachsungskatalysator zur Gewinnung des Grundöles, worin der Entwachsungskatalysator auf einem Molekularsieb mit Poren mit einem Durchmesser im Bereich von 0,35 bis 0,80 nm aufgebaut ist und in seinem Gitterwerk kovalent gebundene Aluminiumoxidrest enthält, welches Molekularsieb zur Verringerung des Molprozentsatzes an Aluminiumoxid modifiziert worden ist,
       und worin das Fischer-Tropsch-Wachs-Einsatzmaterial einen Erstarrungspunkt von wenigstens 50 °C aufweist und einen solchen Siedebereich hat, dass der Unterschied zwischen dem 90 Gew.%-Siedepunkt und dem 10 Gew.%-Siedepunkt (T90-T10) im Bereich von 40 bis 150 °C liegt.
  2. Verfahren nach Anspruch 1, worin T90-T10 im Bereich von 50 bis 130 °C liegt.
  3. Verfahren nach Anspruch 1 oder 2, worin das Fischer-Tropsch-Wachs-Einsatzmaterial einen Erstarrungspunkt im Bereich von 55 bis 150 °C, vorzugsweise von 60 bis 120 °C aufweist.
  4. Verfahren nach einem der vorstehenden Ansprüche, worin der Hydroisomerisationskatalysator eine auf einen Feuerfestoxidträger aufgebrachte Hydrierkomponente umfasst.
  5. Verfahren nach Anspruch 4, worin der Hydroisomerisationskatalysator Platin und/oder Palladium als die Hydrierkomponente umfasst.
  6. Verfahren nach Anspruch 5, worin der Hydroisomerisationskatalysator Platin und Palladium, aufgebracht auf einen amorphen Siliciumoxid-Aluminiumoxidträger, umfasst.
  7. Verfahren nach Anspruch 4, worin der Hydroisomerisationskatalysator wenigstens ein Gruppe VIB-Metall, vorzugsweise Wolfram, und wenigstens ein Gruppe VIII-Unedelmetall, vorzugsweise Nickel, als die Hydrierkomponente umfasst.
  8. Verfahren nach einem der vorstehenden Ansprüche, worin im Schritt (b) die schwere Fraktion bei einem effektiven Schnittpunkt im Bereich von 350 bis 420 °C erhalten wird.
  9. Verfahren nach einem der Ansprüche 1-8, worin der Entwachsungskatalysator einen Zeolith vom MFI-Typ, Offretit, Ferrierit oder MTT-Typ als Molekularsieb und ein Gruppe VIII-Metall umfasst.
  10. Verfahren nach Anspruch 9, worin der Entwachsungskatalysator einen Zeolith vom MTT-Typ als Molekularsieb umfasst.
  11. Verfahren nach einem der Ansprüche 9-10, worin das Gruppe VIII-Metall Platin und/oder Palladium ist, das in einer Menge von 0,2 bis 3,0 Gew.% zugegen ist.
  12. Verfahren nach einem der Ansprüche 1-11, worin das Molekularsieb des Entwachsungskatalysators zur Verringerung des Molprozentsatzes an Aluminiumoxid durch eine Oberflächendealuminierungsbehandlung modifiziert worden ist.
EP03077527A 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen Expired - Lifetime EP1365005B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP03077527A EP1365005B1 (de) 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
EP95402713 1995-11-28
EP95402713 1995-11-28
EP03077527A EP1365005B1 (de) 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen
EP19960203362 EP0776959B1 (de) 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
EP19960203362 Division EP0776959B1 (de) 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen

Publications (2)

Publication Number Publication Date
EP1365005A1 EP1365005A1 (de) 2003-11-26
EP1365005B1 true EP1365005B1 (de) 2005-10-19

Family

ID=26140596

Family Applications (2)

Application Number Title Priority Date Filing Date
EP19960203362 Expired - Lifetime EP0776959B1 (de) 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen
EP03077527A Expired - Lifetime EP1365005B1 (de) 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP19960203362 Expired - Lifetime EP0776959B1 (de) 1995-11-28 1996-11-28 Verfahren zur Herstellung von Schmierölen

Country Status (1)

Country Link
EP (2) EP0776959B1 (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105219427B (zh) * 2014-06-16 2017-08-25 中国石油化工股份有限公司 一种润滑油基础油的加工方法

Families Citing this family (251)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6090989A (en) * 1997-10-20 2000-07-18 Mobil Oil Corporation Isoparaffinic lube basestock compositions
ZA989528B (en) * 1997-12-03 2000-04-19 Schuemann Sasol S A Pty Ltd "Production of lubricant base oils".
WO1999032581A1 (en) * 1997-12-22 1999-07-01 Chevron U.S.A., Inc. Raffinate dewaxing process
JP2002503756A (ja) * 1998-02-13 2002-02-05 エクソンモービル リサーチ アンド エンジニアリング カンパニー 混合触媒系による潤滑油の製造
US6165949A (en) * 1998-09-04 2000-12-26 Exxon Research And Engineering Company Premium wear resistant lubricant
US6080301A (en) 1998-09-04 2000-06-27 Exxonmobil Research And Engineering Company Premium synthetic lubricant base stock having at least 95% non-cyclic isoparaffins
US6475960B1 (en) 1998-09-04 2002-11-05 Exxonmobil Research And Engineering Co. Premium synthetic lubricants
US6179994B1 (en) 1998-09-04 2001-01-30 Exxon Research And Engineering Company Isoparaffinic base stocks by dewaxing fischer-tropsch wax hydroisomerate over Pt/H-mordenite
US6332974B1 (en) 1998-09-11 2001-12-25 Exxon Research And Engineering Co. Wide-cut synthetic isoparaffinic lubricating oils
ES2190303B1 (es) 1999-04-29 2005-02-16 Institut Francais Du Petrole Procedimiento flexible de produccion de bases de aceites y destilados para una conversion-hidroisomerizacion sobre un catalizador ligeramente disperso seguida de un desparafinado catalitico.
FR2805543B1 (fr) * 2000-02-24 2003-09-05 Inst Francais Du Petrole Procede flexible de production de bases huiles et distillats moyens avec une conversion-hydroisomerisation suivie d'un deparaffinage catalytique
FR2792946B1 (fr) * 1999-04-29 2003-10-24 Inst Francais Du Petrole Procede de production de bases huiles et de distillats moyens a partir de charges hydrocarbonees par une conversion-hydroisomerisation sur un catalyseur faiblement disperse suivie d'un deparaffinage catalytique
FR2805542B1 (fr) * 2000-02-24 2003-09-05 Inst Francais Du Petrole Procede flexible de production de bases huiles et de distillats par une conversion-hydroisomerisation sur un catalyseur faiblement disperse suivie d'un deparaffinage catalytique
ES2185445B1 (es) * 1999-04-29 2004-08-16 Institut Francais Du Petrole Procedimiento flexible de produccion de bases de aceites y destilados medios con una conversion-hidroisomerizacion seguida de un desparafinado catalitico.
FR2792945B1 (fr) * 1999-04-29 2006-01-13 Inst Francais Du Petrole Procede de production de bases huiles et distillats moyens avec une conversion-hydroisomerisation suivie d'un deparaffinage catalytique
US7067049B1 (en) 2000-02-04 2006-06-27 Exxonmobil Oil Corporation Formulated lubricant oils containing high-performance base oils derived from highly paraffinic hydrocarbons
US6695965B1 (en) * 2000-04-04 2004-02-24 Exxonmobil Research And Engineering Company Process for adjusting the hardness of Fischer-Tropsch wax by blending
FR2812301B1 (fr) 2000-07-26 2003-04-04 Inst Francais Du Petrole Procede flexible de production de bases huiles et de distillats moyens a partir de charge contenant des heteroatomes
AU2005201627B2 (en) * 2000-11-08 2007-11-22 Chevron U.S.A. Inc. Manufacture of lubricants from Fischer-Tropsch syncrude
BR0115171A (pt) * 2000-11-08 2003-10-14 Chevron Usa Inc Processos para a fabricação de uma máteria-prima básica de lubrificantes e para receber um produto fischer-tropsch de gás natural convertido, e, método para a fabricação de produtos de hidrocarbonetos a partir de campos remotos de gás natural
US7670996B2 (en) 2001-02-13 2010-03-02 Shell Oil Company Lubricant composition having a base oil and one or more additives, wherein the base oil has been obtained from waxy paraffinic fischer-tropsch synthesized hydrocarbons
MY137259A (en) * 2001-03-05 2009-01-30 Shell Int Research Process to prepare a lubricating base oil and a gas oil.
AR032941A1 (es) 2001-03-05 2003-12-03 Shell Int Research Un procedimiento para preparar un aceite base lubricante y aceite base obtenido, con sus diversas utilizaciones
MY139353A (en) * 2001-03-05 2009-09-30 Shell Int Research Process to prepare a lubricating base oil and a gas oil
DE10126516A1 (de) 2001-05-30 2002-12-05 Schuemann Sasol Gmbh Verfahren zur Herstellung von mikrokristallinen Paraffinen
TWI277649B (en) 2001-06-07 2007-04-01 Shell Int Research Process to prepare a base oil from slack-wax
US6699385B2 (en) 2001-10-17 2004-03-02 Chevron U.S.A. Inc. Process for converting waxy feeds into low haze heavy base oil
US7285693B2 (en) 2002-02-25 2007-10-23 Shell Oil Company Process to prepare a catalytically dewaxed gas oil or gas oil blending component
EP1645615A1 (de) * 2002-03-05 2006-04-12 Shell Internationale Researchmaatschappij B.V. Ein medizinisches Weissöl enthaltende Schmierbasisölzusammensetzung
GB2402397B (en) * 2002-04-18 2005-05-11 Chevron Usa Inc Process for making lubricanting oils
GB2388842B (en) * 2002-04-18 2004-11-03 Chevron Usa Inc Process for making lubricating oils
DE10256431A1 (de) * 2002-05-31 2004-01-15 SCHÜMANN SASOL GmbH Mikrokristallines Paraffin, Verfahren zur Herstellung von mikrokristallinen Paraffine und Verwendung der mikrokristallinen Paraffine
EP1534801B1 (de) 2002-07-12 2006-01-25 Shell Internationale Researchmaatschappij B.V. Verfahren zur herstellung eines schweren und eines leichten schmier l-grund ls
AU2003255058A1 (en) 2002-07-18 2004-02-09 Shell Internationale Research Maatschappij B.V. Process to prepare a microcrystalline wax and a middle distillate fuel
DE60332242D1 (de) 2002-07-19 2010-06-02 Shell Int Research Zusammensetzung enthaltend epdm und paraffin ol
WO2004009738A1 (en) * 2002-07-19 2004-01-29 Shell Internationale Research Maatschappij B.V. Silicon rubber comprising an extender oil and process to prepare said extender oil
US6703353B1 (en) 2002-09-04 2004-03-09 Chevron U.S.A. Inc. Blending of low viscosity Fischer-Tropsch base oils to produce high quality lubricating base oils
US6951605B2 (en) 2002-10-08 2005-10-04 Exxonmobil Research And Engineering Company Method for making lube basestocks
US7077947B2 (en) 2002-10-08 2006-07-18 Exxonmobil Research And Engineering Company Process for preparing basestocks having high VI using oxygenated dewaxing catalyst
US7220350B2 (en) 2002-10-08 2007-05-22 Exxonmobil Research And Engineering Company Wax isomerate yield enhancement by oxygenate pretreatment of catalyst
US7704379B2 (en) 2002-10-08 2010-04-27 Exxonmobil Research And Engineering Company Dual catalyst system for hydroisomerization of Fischer-Tropsch wax and waxy raffinate
US20040129603A1 (en) * 2002-10-08 2004-07-08 Fyfe Kim Elizabeth High viscosity-index base stocks, base oils and lubricant compositions and methods for their production and use
US7282137B2 (en) * 2002-10-08 2007-10-16 Exxonmobil Research And Engineering Company Process for preparing basestocks having high VI
US7087152B2 (en) 2002-10-08 2006-08-08 Exxonmobil Research And Engineering Company Wax isomerate yield enhancement by oxygenate pretreatment of feed
US7125818B2 (en) 2002-10-08 2006-10-24 Exxonmobil Research & Engineering Co. Catalyst for wax isomerate yield enhancement by oxygenate pretreatment
US7144497B2 (en) 2002-11-20 2006-12-05 Chevron U.S.A. Inc. Blending of low viscosity Fischer-Tropsch base oils with conventional base oils to produce high quality lubricating base oils
CA2509369A1 (en) * 2002-12-09 2004-06-24 Shell Internationale Research Maatschappij B.V. Process for the preparation of a lubricant
US20040154958A1 (en) * 2002-12-11 2004-08-12 Alexander Albert Gordon Functional fluids having low brookfield viscosity using high viscosity-index base stocks, base oils and lubricant compositions, and methods for their production and use
US20040154957A1 (en) * 2002-12-11 2004-08-12 Keeney Angela J. High viscosity index wide-temperature functional fluid compositions and methods for their making and use
FR2851569B1 (fr) * 2003-02-21 2007-04-20 Inst Francais Du Petrole Procede d'hydrocraquage en deux etapes utilisant un catalyseur amorphe a base de platine et de palladium
US7198710B2 (en) * 2003-03-10 2007-04-03 Chevron U.S.A. Inc. Isomerization/dehazing process for base oils from Fischer-Tropsch wax
US6962651B2 (en) * 2003-03-10 2005-11-08 Chevron U.S.A. Inc. Method for producing a plurality of lubricant base oils from paraffinic feedstock
US7141157B2 (en) 2003-03-11 2006-11-28 Chevron U.S.A. Inc. Blending of low viscosity Fischer-Tropsch base oils and Fischer-Tropsch derived bottoms or bright stock
JP2006523598A (ja) 2003-04-15 2006-10-19 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 合成ガスの製造方法
EP1644465B1 (de) 2003-06-23 2010-03-17 Shell Internationale Researchmaatschappij B.V. Verfahren zur herstellung eines schmierbaseöls
US7727378B2 (en) 2003-07-04 2010-06-01 Shell Oil Company Process to prepare a Fischer-Tropsch product
WO2005005575A1 (en) 2003-07-04 2005-01-20 Shell Internationale Research Maatschappij B.V. Process to prepare a fischer-tropsch product
US7018525B2 (en) 2003-10-14 2006-03-28 Chevron U.S.A. Inc. Processes for producing lubricant base oils with optimized branching
US20050077208A1 (en) * 2003-10-14 2005-04-14 Miller Stephen J. Lubricant base oils with optimized branching
US8137531B2 (en) * 2003-11-05 2012-03-20 Chevron U.S.A. Inc. Integrated process for the production of lubricating base oils and liquid fuels from Fischer-Tropsch materials using split feed hydroprocessing
US7083713B2 (en) 2003-12-23 2006-08-01 Chevron U.S.A. Inc. Composition of lubricating base oil with high monocycloparaffins and low multicycloparaffins
US7195706B2 (en) 2003-12-23 2007-03-27 Chevron U.S.A. Inc. Finished lubricating comprising lubricating base oil with high monocycloparaffins and low multicycloparaffins
EP1550709A1 (de) * 2003-12-23 2005-07-06 Shell Internationale Researchmaatschappij B.V. Verfahren zum Herstellen eines trübungsfreien Grundöl
EP1548088A1 (de) 2003-12-23 2005-06-29 Shell Internationale Researchmaatschappij B.V. Verfahren zum Herstellen eines trübungsfreien Grundöls
US7763161B2 (en) 2003-12-23 2010-07-27 Chevron U.S.A. Inc. Process for making lubricating base oils with high ratio of monocycloparaffins to multicycloparaffins
US7282134B2 (en) 2003-12-23 2007-10-16 Chevron Usa, Inc. Process for manufacturing lubricating base oil with high monocycloparaffins and low multicycloparaffins
JP5053839B2 (ja) 2004-06-18 2012-10-24 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 潤滑油組成物
JP5133689B2 (ja) 2004-10-08 2013-01-30 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ フィッシャー・トロプシュ合成生成物からの低級オレフィンの製造方法
US7531083B2 (en) 2004-11-08 2009-05-12 Shell Oil Company Cycloalkane base oils, cycloalkane-base dielectric liquids made using cycloalkane base oils, and methods of making same
JP2008520786A (ja) 2004-11-18 2008-06-19 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 基油の製造方法
JP2008520787A (ja) 2004-11-18 2008-06-19 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ ガス油の製造方法
US7510674B2 (en) 2004-12-01 2009-03-31 Chevron U.S.A. Inc. Dielectric fluids and processes for making same
US7252753B2 (en) 2004-12-01 2007-08-07 Chevron U.S.A. Inc. Dielectric fluids and processes for making same
US7550415B2 (en) 2004-12-10 2009-06-23 Shell Oil Company Lubricating oil composition
US8076525B2 (en) 2004-12-20 2011-12-13 Shell Oil Company Gasoline cracking
EP1841839A1 (de) 2004-12-28 2007-10-10 Shell Internationale Research Maatschappij B.V. Verfahren zur herstellung eines grundöls aus einem produkt der fischer-tropsch-synthese
CN101090960B (zh) 2005-01-07 2010-10-27 新日本石油株式会社 润滑油基础油、内燃机用润滑油组合物和驱动传递装置用润滑油组合物
JP5180437B2 (ja) * 2005-01-07 2013-04-10 Ｊｘ日鉱日石エネルギー株式会社 潤滑油基油
JP6080489B2 (ja) * 2005-01-07 2017-02-15 Ｊｘエネルギー株式会社 潤滑油基油
JP2012180532A (ja) * 2005-02-02 2012-09-20 Jx Nippon Oil & Energy Corp 内燃機関用潤滑油組成物
JP5114006B2 (ja) * 2005-02-02 2013-01-09 Ｊｘ日鉱日石エネルギー株式会社 内燃機関用潤滑油組成物
JP5087224B2 (ja) * 2005-02-10 2012-12-05 Ｊｘ日鉱日石エネルギー株式会社 駆動伝達装置用潤滑油組成物
US7655605B2 (en) 2005-03-11 2010-02-02 Chevron U.S.A. Inc. Processes for producing extra light hydrocarbon liquids
EP1869146B1 (de) 2005-04-11 2011-03-02 Shell Internationale Research Maatschappij B.V. Verfahren zum mischen eines aus mineralien gewonnenen und eines aus der fischer-tropsch-synthese gewonnenen produkts an bord eines schiffs
US8070885B2 (en) 2005-05-19 2011-12-06 Shell Oil Company Quenching fluid
JP5517233B2 (ja) 2005-05-20 2014-06-11 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ フィッシャー・トロプシュ誘導ホワイトオイルを担体油として含有する組成物
US7851418B2 (en) 2005-06-03 2010-12-14 Exxonmobil Research And Engineering Company Ashless detergents and formulated lubricating oil containing same
AU2006260922A1 (en) 2005-06-23 2006-12-28 Shell Internationale Research Maatschappij B.V. Electrical oil formulation
US20070093398A1 (en) 2005-10-21 2007-04-26 Habeeb Jacob J Two-stroke lubricating oils
CA2643358A1 (en) 2006-02-21 2007-08-30 Shell Internationale Research Maatschappij B.V. Lubricating oil composition
EP1991639B1 (de) 2006-03-07 2015-04-22 Shell Internationale Research Maatschappij B.V. Verfahren zur herstellung eines fischer-tropsch-produkts
US8299005B2 (en) 2006-05-09 2012-10-30 Exxonmobil Research And Engineering Company Lubricating oil composition
US7863229B2 (en) 2006-06-23 2011-01-04 Exxonmobil Research And Engineering Company Lubricating compositions
RU2437830C2 (ru) 2006-07-11 2011-12-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Способ получения синтез-газа
US8747650B2 (en) 2006-12-21 2014-06-10 Chevron Oronite Technology B.V. Engine lubricant with enhanced thermal stability
JP5108318B2 (ja) 2007-02-01 2012-12-26 昭和シェル石油株式会社 新規な有機モリブデン化合物
JP5108315B2 (ja) 2007-02-01 2012-12-26 昭和シェル石油株式会社 有機モリブデン化合物よりなる摩擦調整剤およびそれを含む潤滑組成物
JP5108317B2 (ja) 2007-02-01 2012-12-26 昭和シェル石油株式会社 アルキルキサントゲン酸モリブデン、それよりなる摩擦調整剤およびそれを含む潤滑組成物
US20090062166A1 (en) 2007-08-28 2009-03-05 Chevron U.S.A. Inc. Slideway Lubricant Compositions, Methods of Making and Using Thereof
AU2008313698B2 (en) 2007-10-19 2012-04-19 Shell Internationale Research Maatschappij B.V. Functional fluids for internal combustion engines
EP2071008A1 (de) 2007-12-04 2009-06-17 Shell Internationale Researchmaatschappij B.V. Schmierzusammensetzung enthaltend ein Imidazolidinethion und ein Imidazolidon
CN101889069B (zh) 2007-12-07 2016-02-10 国际壳牌研究有限公司 基础油配制剂
US7956018B2 (en) 2007-12-10 2011-06-07 Chevron U.S.A. Inc. Lubricant composition
EP2075314A1 (de) 2007-12-11 2009-07-01 Shell Internationale Research Maatschappij B.V. Fettformulierungen
EP2072610A1 (de) 2007-12-11 2009-06-24 Shell Internationale Research Maatschappij B.V. Trägerölzusammensetzung
US8152869B2 (en) 2007-12-20 2012-04-10 Shell Oil Company Fuel compositions
WO2009080679A1 (en) * 2007-12-20 2009-07-02 Shell Internationale Research Maatschappij B.V. Process to prepare a gas oil and a base oil
JP2011508000A (ja) 2007-12-20 2011-03-10 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 燃料組成物
GB2455995B (en) * 2007-12-27 2012-09-26 Statoilhydro Asa A method of producing a lube oil from a Fischer-Tropsch wax
EP2078743A1 (de) 2008-01-10 2009-07-15 Shell Internationale Researchmaatschappij B.V. Kraftstoffzusammensetzung
AR070686A1 (es) 2008-01-16 2010-04-28 Shell Int Research Un metodo para preparar una composicion de lubricante
JP5517266B2 (ja) 2008-06-19 2014-06-11 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 潤滑グリース組成物
JP2011525563A (ja) 2008-06-24 2011-09-22 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ ポリ（ヒドロキシカルボン酸）アミドを含む潤滑組成物の使用法
EP2318485A1 (de) 2008-07-31 2011-05-11 Shell Oil Company Poly(hydroxycarbonsäure)-amidsalzderivat und schmiermittelzusammensetzung damit
EP2100946A1 (de) 2008-09-08 2009-09-16 Shell Internationale Researchmaatschappij B.V. Ölformulierungen
US20100162693A1 (en) 2008-12-31 2010-07-01 Michael Paul W Method of reducing torque ripple in hydraulic motors
JP5684147B2 (ja) 2009-01-28 2015-03-11 シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー 潤滑組成物
EP2186871A1 (de) 2009-02-11 2010-05-19 Shell Internationale Research Maatschappij B.V. Schmierzusammensetzung
EP2398872B1 (de) 2009-02-18 2013-11-13 Shell Internationale Research Maatschappij B.V. Verwendung einer schmiermittelzusammensetzung mit gtl-grundöl zur verringerung von kohlenwasserstoffemissionen
EP2248878A1 (de) 2009-05-01 2010-11-10 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
WO2010149706A1 (en) 2009-06-24 2010-12-29 Shell Internationale Research Maatschappij B.V. Lubricating composition
WO2010149712A1 (en) 2009-06-25 2010-12-29 Shell Internationale Research Maatschappij B.V. Lubricating composition
JP5667633B2 (ja) 2009-08-18 2015-02-12 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎｖｅｎｎｏｏｔｓｈａｐ 潤滑グリース組成物
EP2298855A1 (de) 2009-08-27 2011-03-23 Castrol Limited Verfahren zur Schmierung eines Dieselmotors mit einem Polyisobutylen enthaltenden Schmieröl
WO2011023766A1 (en) 2009-08-28 2011-03-03 Shell Internationale Research Maatschappij B.V. Process oil composition
US8349776B2 (en) 2009-09-29 2013-01-08 Chevron Oronite Company Llc Trunk piston engine lubricating oil compositions
CN102549125B (zh) 2009-10-09 2014-09-24 国际壳牌研究有限公司 润滑组合物
EP2159275A3 (de) 2009-10-14 2010-04-28 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
KR101950667B1 (ko) 2009-10-26 2019-02-21 쉘 인터내셔날 리써취 마트샤피지 비.브이. 윤활 조성물
EP2189515A1 (de) 2009-11-05 2010-05-26 Shell Internationale Research Maatschappij B.V. Funktionsflüssigkeitszusammensetzung
EP2186872A1 (de) 2009-12-16 2010-05-19 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
US20130000583A1 (en) 2009-12-24 2013-01-03 Adrian Philip Groves Liquid fuel compositions
BR112012016140A2 (pt) 2009-12-29 2016-05-31 Shell Int Research método para melhorar o desempenho do lubrificante de um motor de combustão interna, uso de uma composição de combustível líquido, e, composição de lubrificação
WO2011110551A1 (en) 2010-03-10 2011-09-15 Shell Internationale Research Maatschappij B.V. Method of reducing the toxicity of used lubricating compositions
KR20130016276A (ko) 2010-03-17 2013-02-14 쉘 인터내셔날 리써취 마트샤피지 비.브이. 윤활 조성물
EP2194114A3 (de) 2010-03-19 2010-10-27 Shell Internationale Research Maatschappij B.V. Composition de lubrification
CN102869755A (zh) 2010-05-03 2013-01-09 国际壳牌研究有限公司 用过的润滑组合物
EP2385097A1 (de) 2010-05-03 2011-11-09 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
JP5911857B2 (ja) 2010-07-05 2016-04-27 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎ Ｖｅｎｎｏｏｔｓｈａｐ グリース組成物の製造方法
WO2012017023A1 (en) 2010-08-03 2012-02-09 Shell Internationale Research Maatschappij B.V. Lubricating composition
EP2441818A1 (de) 2010-10-12 2012-04-18 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
US8455406B2 (en) 2010-10-28 2013-06-04 Chevron U.S.A. Inc. Compressor oils having improved oxidation resistance
EP2652096A1 (de) 2010-12-17 2013-10-23 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
CN103459572A (zh) 2011-04-05 2013-12-18 雪佛龙奥伦耐有限责任公司 低粘度船用气缸润滑油组合物
JP2014517097A (ja) 2011-05-05 2014-07-17 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ フィッシャー・トロプシュ誘導基油を含む潤滑油組成物
US20120304531A1 (en) 2011-05-30 2012-12-06 Shell Oil Company Liquid fuel compositions
EP2395068A1 (de) 2011-06-14 2011-12-14 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
US9206374B2 (en) 2011-12-16 2015-12-08 Chevron Oronite Sas Trunk piston engine lubricating oil compositions
US9593267B2 (en) 2011-12-20 2017-03-14 Shell Oil Company Adhesive compositions and methods of using the same
WO2013093103A1 (en) 2011-12-22 2013-06-27 Shell Internationale Research Maatschappij B.V. Lubricating composition
RU2014130105A (ru) 2011-12-22 2016-02-10 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Усовершенствования, касающиеся смазки компрессора высокого давления
EP2626405B1 (de) 2012-02-10 2015-05-27 Ab Nanol Technologies Oy Schmiermittelzusammensetzung
JP6266606B2 (ja) 2012-06-21 2018-01-24 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎ Ｖｅｎｎｏｏｔｓｈａｐ 重質フィッシャー・トロプシュ由来及びアルキル化芳香族基油を含む潤滑油組成物
EP2864459A1 (de) 2012-06-21 2015-04-29 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung
EP2867343A1 (de) 2012-06-28 2015-05-06 Shell Internationale Research Maatschappij B.V. Verfahren zur herstellung einer gasölfraktion und eines verbleibenden basisöls
CN104583380A (zh) 2012-08-01 2015-04-29 国际壳牌研究有限公司 电缆填充组合物
EP2695932A1 (de) 2012-08-08 2014-02-12 Ab Nanol Technologies Oy Schmierfettzusammensetzung
EP2746367A1 (de) 2012-12-18 2014-06-25 Shell Internationale Research Maatschappij B.V. Verfahren zur Herstellung von Basisöl und Gasöl
EP2816098A1 (de) 2013-06-18 2014-12-24 Shell Internationale Research Maatschappij B.V. Verwendung einer Schwefelverbindung zur Verbesserung der Oxidationsstabilität einer Schmierölzusammensetzung
EP2816097A1 (de) 2013-06-18 2014-12-24 Shell Internationale Research Maatschappij B.V. Schmierölzusammensetzung
MY173203A (en) 2013-10-31 2020-01-03 Shell Int Research Process for the conversion of a paraffinic feedstock
US10364403B2 (en) 2013-11-06 2019-07-30 Chevron Oronite Technology B.V. Marine diesel cylinder lubricant oil compositions
SG11201603378WA (en) 2013-11-06 2016-05-30 Chevron Oronite Technology Bv Marine diesel cylinder lubricant oil compositions
FR3013357B1 (fr) 2013-11-18 2016-09-16 Total Marketing Services Procede de production de fluides hydrocarbures a basse teneur en aromatiques
JP6829601B2 (ja) 2013-12-24 2021-02-10 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎ Ｖｅｎｎｏｏｔｓｈａｐ 潤滑組成物
EP3124505A4 (de) 2014-03-28 2017-12-06 Mitsui Chemicals, Inc. Ethylen/alpha-olefin-copolymer und schmieröl
US8968592B1 (en) 2014-04-10 2015-03-03 Soilworks, LLC Dust suppression composition and method of controlling dust
US9068106B1 (en) 2014-04-10 2015-06-30 Soilworks, LLC Dust suppression composition and method of controlling dust
WO2015172846A1 (en) 2014-05-16 2015-11-19 Ab Nanol Technologies Oy Additive composition for lubricants
US20170275555A1 (en) 2014-06-19 2017-09-28 Shell Oil Company Lubricating composition
WO2016032782A1 (en) 2014-08-27 2016-03-03 Shell Oil Company Methods for lubricating a diamond-like carbon coated surface, associated lubricating oil compositions and associated screening methods
WO2016039295A1 (ja) 2014-09-10 2016-03-17 三井化学株式会社 潤滑油組成物
JP6812345B2 (ja) 2014-11-04 2021-01-13 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎ Ｖｅｎｎｏｏｔｓｈａｐ 潤滑用組成物
MY188310A (en) 2014-11-12 2021-11-27 Shell Int Research Use of a fuel composition
JP6698660B2 (ja) 2014-12-17 2020-05-27 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎ Ｖｅｎｎｏｏｔｓｈａｐ 潤滑油組成物
EP3040404A1 (de) 2014-12-31 2016-07-06 Shell Internationale Research Maatschappij B.V. Verfahren zur Herstellung von NAPHTHA und Mitteldestillatfraktionen
RU2717349C2 (ru) 2015-02-06 2020-03-23 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Смазочная композиция
CN107207983B (zh) 2015-02-27 2022-11-18 国际壳牌研究有限公司 润滑组合物的用途
WO2016156328A1 (en) 2015-03-31 2016-10-06 Shell Internationale Research Maatschappij B.V. Use of a lubricating composition comprising a hindered amine light stabilizer for improved piston cleanliness in an internal combustion engine
WO2016166135A1 (en) 2015-04-15 2016-10-20 Shell Internationale Research Maatschappij B.V. Method for detecting the presence of hydrocarbons derived from methane in a mixture
WO2016184842A1 (en) 2015-05-18 2016-11-24 Shell Internationale Research Maatschappij B.V. Lubricating composition
EP3095842A1 (de) 2015-05-20 2016-11-23 Total Marketing Services Verfahren zur herstellung von biologisch abbaubaren kohlenwasserstoffflüssigkeiten auf basis von syngas
CN107849481B (zh) 2015-07-22 2021-09-03 雪佛龙奥伦耐技术有限责任公司 船用柴油机汽缸润滑油组合物
US9434881B1 (en) 2015-08-25 2016-09-06 Soilworks, LLC Synthetic fluids as compaction aids
US10808195B2 (en) 2015-09-22 2020-10-20 Shell Oil Company Fuel compositions
ES2815799T3 (es) 2015-11-30 2021-03-30 Shell Int Research Composición de combustible
EP3394216A1 (de) 2015-12-23 2018-10-31 Shell International Research Maatschappij B.V. Verfahren zur herstellung eines basisöls mit reduziertem trübungspunkt
CN109071736B (zh) 2016-05-13 2021-08-10 赢创运营有限公司 基于聚烯烃主链和甲基丙烯酸酯侧链的接枝共聚物
EP3497190B1 (de) 2016-08-15 2020-07-15 Evonik Operations GmbH Funktionelle polyalkyl (meth)-acrylate mit verbesserter entemulgierbarkeitsleistung
KR102303476B1 (ko) 2016-08-31 2021-09-24 에보니크 오퍼레이션즈 게엠베하 엔진 오일 배합물의 노아크 증발 손실을 개선시키기 위한 빗살형 중합체
EP3315586A1 (de) 2016-10-27 2018-05-02 Total Marketing Services Verwendung von biologisch abbaubaren kohlenwasserstoffflüssigkeiten als wärmeübertragungsmedien
EP3315592A1 (de) 2016-10-27 2018-05-02 Total Marketing Services Verwendung von biologisch abbaubaren kohlenwasserstoffflüssigkeiten als bohrflüssigkeiten
EP3315590A1 (de) 2016-10-27 2018-05-02 Total Marketing Services Verwendung von kohlenwasserstoffflüssigkeiten in elektrischen fahrzeugen
EP3336162A1 (de) 2016-12-16 2018-06-20 Shell International Research Maatschappij B.V. Schmiermittelzusammensetzung
KR102461593B1 (ko) 2016-12-19 2022-11-02 에보니크 오퍼레이션즈 게엠베하 분산제 빗살형 중합체를 포함하는 윤활 오일 조성물
MY192909A (en) 2016-12-23 2022-09-14 Shell Int Research Fischer-tropsch feedstock derived haze-free base oil fractions
US11078430B2 (en) 2016-12-23 2021-08-03 Shell Oil Company Haze-free base oils with high paraffinic content
EP3342842A1 (de) 2017-01-03 2018-07-04 Total Marketing Services Entwachsungs- und entaromatisierungsverfahren von kohlenwasserstoff in einem schlammreaktor
CN110072981B (zh) 2017-01-16 2022-02-25 三井化学株式会社 汽车齿轮用润滑油组合物
US20180305633A1 (en) 2017-04-19 2018-10-25 Shell Oil Company Lubricating compositions comprising a volatility reducing additive
EP3615641B1 (de) 2017-04-27 2022-04-13 Shell Internationale Research Maatschappij B.V. Verwendung eines dispersant in einer schmiermittelzusammensetzung
CN110914393A (zh) 2017-07-14 2020-03-24 赢创运营有限公司 包含酰亚胺官能度的梳形聚合物
EP3450527B1 (de) 2017-09-04 2020-12-02 Evonik Operations GmbH Neue viskositätsindexverbesserer mit definierten molekulargewichtsverteilungen
ES2801327T3 (es) 2017-12-13 2021-01-11 Evonik Operations Gmbh Mejorador del índice de viscosidad con resistencia al cizallamiento y solubilidad después del cizallamiento mejoradas
CN111630141B (zh) 2018-01-23 2022-07-19 赢创运营有限公司 聚合物-无机纳米粒子组合物、其制造方法和其作为润滑剂添加剂的用途
WO2019145287A1 (en) 2018-01-23 2019-08-01 Evonik Oil Additives Gmbh Polymeric-inorganic nanoparticle compositions, manufacturing process thereof and their use as lubricant additives
CN111655827B (zh) 2018-01-23 2022-07-26 赢创运营有限公司 聚合物-无机纳米粒子组合物、其制造方法和其作为润滑剂添加剂的用途
EP3784761B1 (de) 2018-04-26 2024-03-06 Shell Internationale Research Maatschappij B.V. Schmiermittelzusammensetzung und verwendung davon als rohrdichtmittel
WO2020007945A1 (en) 2018-07-05 2020-01-09 Shell Internationale Research Maatschappij B.V. Lubricating composition
CN112384599B (zh) 2018-07-13 2023-05-30 国际壳牌研究有限公司 润滑组合物
WO2020064619A1 (en) 2018-09-24 2020-04-02 Evonik Operations Gmbh Use of trialkoxysilane-based compounds for lubricants
EP3880773B1 (de) 2018-11-13 2022-07-06 Evonik Operations GmbH Statistische copolymere zur verwendung als grundöle oder schmierstoffadditive
WO2020126494A1 (en) 2018-12-19 2020-06-25 Evonik Operations Gmbh Use of associative triblockcopolymers as viscosity index improvers
WO2020126496A1 (en) 2018-12-19 2020-06-25 Evonik Operations Gmbh Viscosity index improvers based on block copolymers
BR102020004711A2 (pt) 2019-03-11 2021-01-19 Evonik Operations Gmbh copolímeros com base em polialquil(met)acrilato, composição aditiva, método de manutenção da kv100 em uma dada hths150, composição de óleo lubrificante
KR20210144769A (ko) 2019-03-20 2021-11-30 에보니크 오퍼레이션즈 게엠베하 연비, 분산력 및 침착 성능을 개선시키기 위한 폴리알킬(메트)아크릴레이트
EP3950902A4 (de) 2019-03-26 2022-08-10 Mitsui Chemicals, Inc. Schmierölzusammensetzung für fahrzeuggetriebeflüssigkeit und verfahren zur herstellung davon
EP3950897A4 (de) 2019-03-26 2022-08-10 Mitsui Chemicals, Inc. Schmierölzusammensetzung für kompressoröl und verfahren zu deren herstellung
KR20210139404A (ko) 2019-03-26 2021-11-22 미쓰이 가가쿠 가부시키가이샤 내연 기관용 윤활유 조성물 및 그의 제조 방법
EP3950898A4 (de) 2019-03-26 2022-08-10 Mitsui Chemicals, Inc. Schmierölzusammensetzung für kraftfahrzeuggetriebe und verfahren zu deren herstellung
CN113574149A (zh) 2019-03-26 2021-10-29 三井化学株式会社 内燃机用润滑油组合物及其制造方法
CN113574142A (zh) 2019-03-26 2021-10-29 三井化学株式会社 液压油用润滑油组合物及其制造方法
KR20210139407A (ko) 2019-03-26 2021-11-22 미쓰이 가가쿠 가부시키가이샤 그리스 조성물 및 그의 제조 방법
EP3950893B1 (de) 2019-03-26 2024-07-17 Mitsui Chemicals, Inc. Schmierölzusammensetzung für industriegetriebe und verfahren zu deren herstellung
EP3778839B1 (de) 2019-08-13 2021-08-04 Evonik Operations GmbH Viskositätsindexverbesserer mit verbesserter scherbeständigkeit
JP7408344B2 (ja) 2019-10-23 2024-01-05 シェルルブリカンツジャパン株式会社 潤滑油組成物
WO2021197974A1 (en) 2020-03-30 2021-10-07 Shell Internationale Research Maatschappij B.V. Managing thermal runaway
JP2023520456A (ja) 2020-03-30 2023-05-17 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 熱管理システム
CA3172828A1 (en) 2020-04-30 2021-11-04 Evonik Operations Gmbh Process for the preparation of dispersant polyalkyl (meth)acrylate polymers
KR20230004805A (ko) 2020-04-30 2023-01-06 에보니크 오퍼레이션즈 게엠베하 폴리알킬 (메트)아크릴레이트 중합체의 제조 방법
EP3907269B1 (de) 2020-05-05 2023-05-03 Evonik Operations GmbH Hydrierte lineare polydien copolymere als basisöle oder additive für schmierstoffzusammensetzungen
JP2023532931A (ja) 2020-07-03 2023-08-01 エボニック オペレーションズ ゲーエムベーハー 長鎖エポキシドから製造された親油性ポリエステルをベースとする高粘度ベースフルード
WO2022003087A1 (en) 2020-07-03 2022-01-06 Evonik Operations Gmbh High viscosity base fluids based on oil compatible polyesters
EP4208526A1 (de) 2020-09-01 2023-07-12 Shell Internationale Research Maatschappij B.V. Motorölzusammensetzung
JP2023544102A (ja) 2020-09-18 2023-10-20 エボニック オペレーションズ ゲーエムベーハー 潤滑剤添加剤としてグラフェン系材料を含む組成物
JP2023550390A (ja) 2020-11-18 2023-12-01 エボニック オペレーションズ ゲーエムベーハー 高粘度指数を有する圧縮機油
US20240043768A1 (en) 2020-12-18 2024-02-08 Evonik Operations Gmbh Process for preparing homo- and copolymers of alkyl (meth)acrylates with low residual monomer content
EP4060009B1 (de) 2021-03-19 2023-05-03 Evonik Operations GmbH Viskositätsindexverbesserer und schmierstoffzusammensetzung damit
ES2955513T3 (es) 2021-07-16 2023-12-04 Evonik Operations Gmbh Composición de aditivo de lubricante que contiene poli(metacrilatos de alquilo)
JPWO2023002947A1 (de) 2021-07-20 2023-01-26
WO2023099632A1 (en) 2021-12-03 2023-06-08 Evonik Operations Gmbh Boronic ester modified polyalkyl(meth)acrylate polymers
WO2023099630A1 (en) 2021-12-03 2023-06-08 Evonik Operations Gmbh Boronic ester modified polyalkyl(meth)acrylate polymers
WO2023099637A1 (en) 2021-12-03 2023-06-08 Totalenergies Onetech Lubricant compositions
WO2023099631A1 (en) 2021-12-03 2023-06-08 Evonik Operations Gmbh Boronic ester modified polyalkyl(meth)acrylate polymers
WO2023099634A1 (en) 2021-12-03 2023-06-08 Totalenergies Onetech Lubricant compositions
WO2023099635A1 (en) 2021-12-03 2023-06-08 Totalenergies Onetech Lubricant compositions
WO2023222677A1 (en) 2022-05-19 2023-11-23 Shell Internationale Research Maatschappij B.V. Thermal management system
WO2023247624A1 (en) 2022-06-22 2023-12-28 Shell Internationale Research Maatschappij B.V. A process to prepare kerosene
EP4381033A1 (de) 2022-08-08 2024-06-12 Evonik Operations GmbH Polyalkyl(meth)acrylat-basierte polymere mit verbesserten tieftemperatureigenschaften
EP4321602A1 (de) 2022-08-10 2024-02-14 Evonik Operations GmbH Schwefelfreie polyalkyl(meth)acrylat-copolymere als viskositätsindexverbesserer in schmiermitteln
WO2024120926A1 (en) 2022-12-07 2024-06-13 Evonik Operations Gmbh Sulfur-free dispersant polymers for industrial applications

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5059299A (en) * 1987-12-18 1991-10-22 Exxon Research And Engineering Company Method for isomerizing wax to lube base oils
US4943672A (en) * 1987-12-18 1990-07-24 Exxon Research And Engineering Company Process for the hydroisomerization of Fischer-Tropsch wax to produce lubricating oil (OP-3403)
AU640490B2 (en) * 1990-07-05 1993-08-26 Mobil Oil Corporation Production of high viscosity index lubricants
US5282958A (en) 1990-07-20 1994-02-01 Chevron Research And Technology Company Use of modified 5-7 a pore molecular sieves for isomerization of hydrocarbons
CA2047923C (en) * 1990-08-14 2002-11-19 Heather A. Boucher Hydrotreating heavy hydroisomerate fractionator bottoms to produce quality light oil upon subsequent refractionation
US5182248A (en) 1991-05-10 1993-01-26 Exxon Research And Engineering Company High porosity, high surface area isomerization catalyst
FR2676749B1 (fr) * 1991-05-21 1993-08-20 Inst Francais Du Petrole Procede d'hydroisomerisation de paraffines issues du procede fischer-tropsch a l'aide de catalyseurs a base de zeolithe h-y.
US5275719A (en) * 1992-06-08 1994-01-04 Mobil Oil Corporation Production of high viscosity index lubricants
IT1256084B (it) 1992-07-31 1995-11-27 Eniricerche Spa Catalizzatore per la idroisomerizzazione di normal-paraffine a catena lunga e procedimento per la sua preparazione
GB9222416D0 (en) 1992-10-26 1992-12-09 Ici Plc Hydrocarbons
EP0668342B1 (de) * 1994-02-08 1999-08-04 Shell Internationale Researchmaatschappij B.V. Verfahren zur Herstellung von Basisschmieröl

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105219427B (zh) * 2014-06-16 2017-08-25 中国石油化工股份有限公司 一种润滑油基础油的加工方法

Also Published As

Publication number Publication date
EP0776959B1 (de) 2004-10-06
EP1365005A1 (de) 2003-11-26
EP0776959A2 (de) 1997-06-04
EP0776959A3 (de) 1998-03-11

Similar Documents

Publication Publication Date Title
EP1365005B1 (de) Verfahren zur Herstellung von Schmierölen
CA2191290C (en) Process for producing lubricating base oils
AU755963B2 (en) Catalytic dewaxing process and catalyst composition
AU716734B2 (en) Process for the preparation of lubricating base oils
US20080045614A1 (en) Process to Make a Base Oil
JP5000296B2 (ja) フィッシャー・トロプシュ合成生成物から基油を製造する方法
JP2008525607A (ja) フィッシャー・トロプシュ合成生成物から基油を製造する方法
EP1720959B1 (de) Verfahren zur herstellung eines schmieröl-grundöls
JP2007526380A (ja) ２種以上の基油グレード及び中間蒸留物の連続的製造方法
EP1720961A1 (de) Verfahren zur herstellung von zwei oder mehr grundölqualitäten und mitteldestillaten
KR100426263B1 (ko) 윤활용 기재오일을 생성하는 방법
JP2008520786A (ja) 基油の製造方法
EP0744452B1 (de) Verfahren zur Herstellung von Basisschmierölen
EP2746367A1 (de) Verfahren zur Herstellung von Basisöl und Gasöl

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AC Divisional application: reference to earlier application

Ref document number: 0776959

Country of ref document: EP

Kind code of ref document: P

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): DE FR GB IT NL

17P Request for examination filed

Effective date: 20040322

17Q First examination report despatched

Effective date: 20040420

AKX Designation fees paid

Designated state(s): DE FR GB IT NL

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AC Divisional application: reference to earlier application

Ref document number: 0776959

Country of ref document: EP

Kind code of ref document: P

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): DE FR GB IT NL

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REF Corresponds to:

Ref document number: 69635320

Country of ref document: DE

Date of ref document: 20051124

Kind code of ref document: P

ET Fr: translation filed
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20060720

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20080919

Year of fee payment: 13

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20081127

Year of fee payment: 13

Ref country code: NL

Payment date: 20081127

Year of fee payment: 13

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20081010

Year of fee payment: 13

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20081022

Year of fee payment: 13

REG Reference to a national code

Ref country code: NL

Ref legal event code: V1

Effective date: 20100601

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20091128

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20100730

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20091130

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20100601

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20100601

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20091128

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20091128