MX172104B - IMPROVED OIL YIELDS FROM 5.6 TO 5.9 CST / 100 DEGREES C THROUGH WAX ISOMERIZATION USING BASIC TREATMENT GAS REGIMES - Google Patents

IMPROVED OIL YIELDS FROM 5.6 TO 5.9 CST / 100 DEGREES C THROUGH WAX ISOMERIZATION USING BASIC TREATMENT GAS REGIMES

Info

Publication number
MX172104B
MX172104B MX1423788A MX1423788A MX172104B MX 172104 B MX172104 B MX 172104B MX 1423788 A MX1423788 A MX 1423788A MX 1423788 A MX1423788 A MX 1423788A MX 172104 B MX172104 B MX 172104B
Authority
MX
Mexico
Prior art keywords
degrees
treatment gas
cst
wax
improved oil
Prior art date
Application number
MX1423788A
Other languages
Spanish (es)
Inventor
Heather Alexis Boucher
Original Assignee
Exxon Research Engineering Co
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 Exxon Research Engineering Co filed Critical Exxon Research Engineering Co
Publication of MX172104B publication Critical patent/MX172104B/en

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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Lubricants (AREA)

Abstract

La presente invención se refiere a un metodo para producir un rendimiento mejorado de aceite lubricante de la clase de viscosidad de 5.6 a 5.9 centistokes a 100 grados C, obtenido de la cera isomerizada, el metodo consiste de (1) isomerizar la cera a traves de un catalizador de isomerización bajo condiciones de temperatura, presión y velocidad espacial de isomerización típica, pero a un régimen de gas de tratamiento bajo dentro de la escala de 14.15 a 141.50 metros cúbicos normales por barril de H2 y (2) recuperar el aceite en la calidad de viscosidad de 5.6 a 5.9 centistokes a 100 grados C, del producto isomerizado producido de esta manera.The present invention relates to a method of producing an improved yield of lubricating oil of the viscosity class of 5.6 to 5.9 centistokes at 100 degrees C, obtained from the isomerized wax, the method consisting of (1) isomerizing the wax through an isomerization catalyst under typical isomerization temperature, pressure, and spatial velocity conditions, but at a low treatment gas rate within the range of 14.15 to 141.50 normal cubic meters per barrel of H2 and (2) recover oil in the viscosity grade of 5.6 to 5.9 centistokes at 100 degrees C, of the isomerized product produced in this way.

MX1423788A 1987-12-18 1988-12-16 IMPROVED OIL YIELDS FROM 5.6 TO 5.9 CST / 100 DEGREES C THROUGH WAX ISOMERIZATION USING BASIC TREATMENT GAS REGIMES MX172104B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US13499887A 1987-12-18 1987-12-18

Publications (1)

Publication Number Publication Date
MX172104B true MX172104B (en) 1993-12-03

Family

ID=22466035

Family Applications (1)

Application Number Title Priority Date Filing Date
MX1423788A MX172104B (en) 1987-12-18 1988-12-16 IMPROVED OIL YIELDS FROM 5.6 TO 5.9 CST / 100 DEGREES C THROUGH WAX ISOMERIZATION USING BASIC TREATMENT GAS REGIMES

Country Status (6)

Country Link
EP (1) EP0321304B1 (en)
JP (1) JPH01308491A (en)
AU (1) AU612214B2 (en)
DE (1) DE3881180T2 (en)
ES (1) ES2054834T3 (en)
MX (1) MX172104B (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7732386B2 (en) 2005-10-25 2010-06-08 Chevron U.S.A. Inc. Rust inhibitor for highly paraffinic lubricating base oil
WO2014139935A1 (en) 2013-03-11 2014-09-18 Basf Se The use of polyalkoxylates in lubricant compositions
US9708561B2 (en) 2013-05-14 2017-07-18 Basf Se Lubricating oil composition with enhanced energy efficiency
AU2014267528B2 (en) 2013-05-17 2017-05-18 Basf Se The use of polytetrahydrofuranes in lubricating oil compositions
KR102273229B1 (en) 2013-09-16 2021-07-05 바스프 에스이 Polyester and use of polyester in lubricants
CN105765042A (en) 2013-11-26 2016-07-13 巴斯夫欧洲公司 The use of polyalkylene glycol esters in lubricating oil compositions
ES2897930T3 (en) 2014-01-28 2022-03-03 Basf Se Use of alkoxylated polyethylene glycols in lubricating oil compositions
ES2620009T3 (en) 2014-04-22 2017-06-27 Basf Se Lubricating composition comprising an ester of a mixture of C17 alcohols
US10000720B2 (en) 2014-05-22 2018-06-19 Basf Se Lubricant compositions containing beta-glucans
WO2016138939A1 (en) 2015-03-03 2016-09-09 Basf Se Pib as high viscosity lubricant base stock
EP3277782A1 (en) 2015-03-30 2018-02-07 Basf Se Lubricants leading to better equipment cleanliness
EP3085757A1 (en) 2015-04-23 2016-10-26 Basf Se Stabilization of alkoxylated polytetrahydrofuranes with antioxidants
EP3293246A1 (en) 2016-09-13 2018-03-14 Basf Se Lubricant compositions containing diurea compounds
EP3315591A1 (en) 2016-10-28 2018-05-02 Basf Se Energy efficient lubricant compositions
WO2019110355A1 (en) 2017-12-04 2019-06-13 Basf Se Branched adipic acid based esters as novel base stocks and lubricants

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE627517A (en) * 1962-01-26
DE3479429D1 (en) * 1983-10-14 1989-09-21 Shell Int Research Hydrocarbon conversion processes and modified refractory oxides which can be used in such processes

Also Published As

Publication number Publication date
EP0321304A3 (en) 1989-08-30
EP0321304A2 (en) 1989-06-21
EP0321304B1 (en) 1993-05-19
DE3881180D1 (en) 1993-06-24
ES2054834T3 (en) 1994-08-16
DE3881180T2 (en) 1993-09-02
JPH01308491A (en) 1989-12-13
AU2696488A (en) 1989-06-22
AU612214B2 (en) 1991-07-04

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