EP0321307A2 - Verfahren zur Isomerisierung von Wachs zu Schmierbasisölen - Google Patents

Verfahren zur Isomerisierung von Wachs zu Schmierbasisölen Download PDF

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Publication number
EP0321307A2
EP0321307A2 EP88311989A EP88311989A EP0321307A2 EP 0321307 A2 EP0321307 A2 EP 0321307A2 EP 88311989 A EP88311989 A EP 88311989A EP 88311989 A EP88311989 A EP 88311989A EP 0321307 A2 EP0321307 A2 EP 0321307A2
Authority
EP
European Patent Office
Prior art keywords
wax
oil
catalyst
isomerization
fraction
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.)
Granted
Application number
EP88311989A
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English (en)
French (fr)
Other versions
EP0321307A3 (en
EP0321307B1 (de
Inventor
Biddanda Umesh Achia
James David Bell
Ian Alfred Cody
William Augusta Wachter
Theodore Harvey West
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ExxonMobil Technology and Engineering Co
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Exxon Research and Engineering Co
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Publication date
Application filed by Exxon Research and Engineering Co filed Critical Exxon Research and Engineering Co
Publication of EP0321307A2 publication Critical patent/EP0321307A2/de
Publication of EP0321307A3 publication Critical patent/EP0321307A3/en
Application granted granted Critical
Publication of EP0321307B1 publication Critical patent/EP0321307B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • 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

Definitions

  • Another preferred catalyst is a catalyst prepared by a process involving depositing a hydrogenation metal on an alumina or material containing alumina support, calcining said metal loaded support typically at between 350 to 500°C, preferably about 450 to 500°C for about 1 to 5 hrs, preferably about 1 to 3 hrs and fluoriding said metal loaded support using a high pH fluorine source solution to a bulk fluorine level of about 8 wt% or less (e.g., 2 to 8 wt%), preferably about 7 wt% or less, said high pH source solution being at a pH of 3.5 to 4.5 and preferably being a mixture of NH4F and HF followed by rapid drying/heating in a thin bed or rotary kiln to insure thorough even heating in air, oxygen containing atmosphere or an inert atmosphere to a temperature between about 350 to 450°C in about 3 hours or less, preferably 375 to 400°C and holding at the final temperature, if necessary, for a time suffi­cient to reduce
  • catalysts prepared using solutions of pH 3.5 or less are not heated first, then it is preferred that they be subsequently activated at more severe conditions, i.e. for longer times and/or at higher temperatures. On the other hand, if they are heated first, then moderate activation procedures similar to those employed with catalysts made from the higher pH solution treatment will suffice.
  • the sized material will range in size between about 1/64 to 1/32 inch in size.
  • the total liquid product (TLP) from the isomerization unit can be advantageously treated in a second stage at mild conditions using the isomerization catalyst or simply noble Group VIII on refractory metal oxide catalyst to reduce PNA and other contaminants in the isomerate and thus yield an oil of improved day­light stability.
  • the sample of Catalyst 2 as charged to the 3600 cc unit was activated as follows: at 300 psi H2 at 11 SCF H2/hour per pound of catalyst, heat from room temperature to 100°C at 10°C/hour; hold at 100°C for 24 hours; heat from 100°C to 250°C at 10°C per hour; hold at 250°C for 15 hours; then at 22 SCF H2/hour per pound of catalyst, heat from 250 to 400°C in 31 hours; hold at 400°C for 3 hours.
  • Catalyst 5 was prepared by meshing the dried/heated form of Catalyst 5 to a particle size of 1/30" (14/35 mesh). After meshing to a particle size of 1/30" (14/35 mesh), Catalyst 6 was activated in flowing hydrogen by heating from room temperature to 100°C over a 2 hour period, holding at 100°C for 1 hour, heating from 100 to 450°C over a 3 hour period, holding at 450°C for 1 hour. Activation pressure was 50 PSI.
EP88311989A 1987-12-18 1988-12-16 Verfahren zur Isomerisierung von Wachs zu Schmierbasisölen Expired - Lifetime EP0321307B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US13515087A 1987-12-18 1987-12-18
US135150 1993-10-12

Publications (3)

Publication Number Publication Date
EP0321307A2 true EP0321307A2 (de) 1989-06-21
EP0321307A3 EP0321307A3 (en) 1989-08-30
EP0321307B1 EP0321307B1 (de) 1993-04-21

Family

ID=22466775

Family Applications (1)

Application Number Title Priority Date Filing Date
EP88311989A Expired - Lifetime EP0321307B1 (de) 1987-12-18 1988-12-16 Verfahren zur Isomerisierung von Wachs zu Schmierbasisölen

Country Status (7)

Country Link
EP (1) EP0321307B1 (de)
JP (1) JP2607284B2 (de)
AU (1) AU610312B2 (de)
CA (1) CA1333057C (de)
DE (1) DE3880455T2 (de)
ES (1) ES2054835T3 (de)
MX (1) MX169698B (de)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0491536A1 (de) * 1990-12-19 1992-06-24 Exxon Research And Engineering Company Wachsisomer mit einem reduzierten Stockpunkt
US5275719A (en) * 1992-06-08 1994-01-04 Mobil Oil Corporation Production of high viscosity index lubricants
EP0620264A2 (de) * 1993-04-14 1994-10-19 BP Chemicals Limited Schmieröle
WO1995007960A1 (en) * 1993-09-13 1995-03-23 Exxon Research And Engineering Company Additive concentrate for use with gasolines
FR2718146A1 (fr) * 1994-04-01 1995-10-06 Inst Francais Du Petrole Procédé de production d'huiles à partir de coupes lourdes en deux étapes comprenant un hydrotraitement suivi d'une hydroisomérisation.
FR2718145A1 (fr) * 1994-04-01 1995-10-06 Inst Francais Du Petrole Procédé de traitement avec hydroisomérisation de charges issues du procédé fischer-tropsch.
WO1997021788A1 (en) * 1995-12-08 1997-06-19 Exxon Research And Engineering Company Biodegradable high performance hydrocarbon base oils
US6103101A (en) * 1993-10-01 2000-08-15 Petroleo Brasileiro S.A.-Petrobras Process for producing lube base oils of high viscosity index and diesel oil of high cetaned number
EP1054942A1 (de) * 1998-02-13 2000-11-29 ExxonMobil Research and Engineering Company Herstellung von schmierölen mit einem katalysatorverbundsystem
EP1062305A1 (de) * 1998-02-13 2000-12-27 ExxonMobil Research and Engineering Company Basisöl mit niedriger viskosität für schmiermittel
AU730150B2 (en) * 1997-10-09 2001-03-01 Agip Petroli S.P.A. Process for the hydroisomerization of long-chain N-paraffins and catalyst suitable for the purpose
US6420618B1 (en) 1998-09-04 2002-07-16 Exxonmobil Research And Engineering Company Premium synthetic lubricant base stock (Law734) having at least 95% noncyclic isoparaffins
US6475960B1 (en) 1998-09-04 2002-11-05 Exxonmobil Research And Engineering Co. Premium synthetic lubricants
EP1559769A1 (de) * 2003-12-19 2005-08-03 Shell Internationale Researchmaatschappij B.V. Verfahren zur Herstellung von Basisölen mit unterschiedlichen Viskositätsindizes
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
US7198710B2 (en) 2003-03-10 2007-04-03 Chevron U.S.A. Inc. Isomerization/dehazing process for base oils from Fischer-Tropsch wax

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MY139353A (en) * 2001-03-05 2009-09-30 Shell Int Research Process to prepare a lubricating base oil and a gas oil
WO2006136590A2 (en) * 2005-06-23 2006-12-28 Shell Internationale Research Maatschappij B.V. Process to reduce the pour point of a waxy paraffinic feedstock

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE627517A (de) * 1962-01-26
US2668866A (en) * 1951-08-14 1954-02-09 Shell Dev Isomerization of paraffin wax
FR1457131A (fr) * 1964-12-08 1966-10-28 Shell Int Research Procédé de production d'huiles lubrifiantes ou de constituants d'huiles lubrifiantes

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2668866A (en) * 1951-08-14 1954-02-09 Shell Dev Isomerization of paraffin wax
BE627517A (de) * 1962-01-26
FR1457131A (fr) * 1964-12-08 1966-10-28 Shell Int Research Procédé de production d'huiles lubrifiantes ou de constituants d'huiles lubrifiantes

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0491536A1 (de) * 1990-12-19 1992-06-24 Exxon Research And Engineering Company Wachsisomer mit einem reduzierten Stockpunkt
US5149452A (en) * 1990-12-19 1992-09-22 Exxon Research And Engineering Company Wax isomerate having a reduced pour point
US5275719A (en) * 1992-06-08 1994-01-04 Mobil Oil Corporation Production of high viscosity index lubricants
EP0620264A2 (de) * 1993-04-14 1994-10-19 BP Chemicals Limited Schmieröle
EP0620264A3 (de) * 1993-04-14 1995-02-08 Bp Chem Int Ltd Schmieröle.
WO1995007960A1 (en) * 1993-09-13 1995-03-23 Exxon Research And Engineering Company Additive concentrate for use with gasolines
US5720782A (en) * 1993-09-13 1998-02-24 Exxon Research And Engineering Company Additive concentrate for use with gasolines
US6103101A (en) * 1993-10-01 2000-08-15 Petroleo Brasileiro S.A.-Petrobras Process for producing lube base oils of high viscosity index and diesel oil of high cetaned number
FR2718146A1 (fr) * 1994-04-01 1995-10-06 Inst Francais Du Petrole Procédé de production d'huiles à partir de coupes lourdes en deux étapes comprenant un hydrotraitement suivi d'une hydroisomérisation.
FR2718145A1 (fr) * 1994-04-01 1995-10-06 Inst Francais Du Petrole Procédé de traitement avec hydroisomérisation de charges issues du procédé fischer-tropsch.
WO1995027020A1 (fr) * 1994-04-01 1995-10-12 Institut Français Du Petrole Procede de traitement avec hydroisomerisation de charges issues du procede fischer-tropsch
US5834522A (en) * 1994-04-01 1998-11-10 Institut Francais Du Petrole Hydroisomerization treatment process for feeds from the fisher-tropsch process
US6096940A (en) * 1995-12-08 2000-08-01 Exxon Research And Engineering Company Biodegradable high performance hydrocarbon base oils
WO1997021788A1 (en) * 1995-12-08 1997-06-19 Exxon Research And Engineering Company Biodegradable high performance hydrocarbon base oils
EP1389635A1 (de) * 1995-12-08 2004-02-18 ExxonMobil Research and Engineering Company Bioabbaubare Hochleistungskohlenwasserstoffbasisöle
US6506297B1 (en) 1995-12-08 2003-01-14 Exxonmobile Research And Engineering Company Biodegradable high performance hydrocarbon base oils
AU730150B2 (en) * 1997-10-09 2001-03-01 Agip Petroli S.P.A. Process for the hydroisomerization of long-chain N-paraffins and catalyst suitable for the purpose
EP1062305A1 (de) * 1998-02-13 2000-12-27 ExxonMobil Research and Engineering Company Basisöl mit niedriger viskosität für schmiermittel
EP1054942A1 (de) * 1998-02-13 2000-11-29 ExxonMobil Research and Engineering Company Herstellung von schmierölen mit einem katalysatorverbundsystem
EP1062305A4 (de) * 1998-02-13 2005-03-09 Exxonmobil Res & Eng Co Basisöl mit niedriger viskosität für schmiermittel
EP1054942A4 (de) * 1998-02-13 2006-07-26 Exxonmobil Res & Eng Co Herstellung von schmierölen mit einem katalysatorverbundsystem
US6420618B1 (en) 1998-09-04 2002-07-16 Exxonmobil Research And Engineering Company Premium synthetic lubricant base stock (Law734) having at least 95% noncyclic isoparaffins
US6475960B1 (en) 1998-09-04 2002-11-05 Exxonmobil Research And Engineering Co. Premium synthetic lubricants
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
US7198710B2 (en) 2003-03-10 2007-04-03 Chevron U.S.A. Inc. Isomerization/dehazing process for base oils from Fischer-Tropsch wax
NL1025687C2 (nl) * 2003-03-10 2010-05-18 Chevron Usa Inc Werkwijze voor het produceren van een veelheid van smeermiddelbasisoliën uit een paraffinische voeding.
EP1559769A1 (de) * 2003-12-19 2005-08-03 Shell Internationale Researchmaatschappij B.V. Verfahren zur Herstellung von Basisölen mit unterschiedlichen Viskositätsindizes

Also Published As

Publication number Publication date
AU610312B2 (en) 1991-05-16
AU2694088A (en) 1989-06-22
DE3880455D1 (de) 1993-05-27
DE3880455T2 (de) 1993-09-16
ES2054835T3 (es) 1994-08-16
EP0321307A3 (en) 1989-08-30
CA1333057C (en) 1994-11-15
JP2607284B2 (ja) 1997-05-07
EP0321307B1 (de) 1993-04-21
JPH01301788A (ja) 1989-12-05
MX169698B (es) 1993-07-19

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