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NO962940L - Method of hydroisomerization - Google Patents

Method of hydroisomerization

Info

Publication number
NO962940L
NO962940L NO962940A NO962940A NO962940L NO 962940 L NO962940 L NO 962940L NO 962940 A NO962940 A NO 962940A NO 962940 A NO962940 A NO 962940A NO 962940 L NO962940 L NO 962940L
Authority
NO
Norway
Prior art keywords
metal
group
hydrogen
weight
feed
Prior art date
Application number
NO962940A
Other languages
Norwegian (no)
Other versions
NO962940D0 (en
Inventor
Stephen Mark Davis
Jack Wayne Johnson
Charles John Mart
Daniel Francis Ryan
Robert Jay Wittenbrink
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 NO962940D0 publication Critical patent/NO962940D0/en
Publication of NO962940L publication Critical patent/NO962940L/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
    • C10G45/66—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 with moving solid particles

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)

Abstract

Oppfinnelsen vedrører en hydroisomeriseringsfrem- gangsmåte for omdannelse av en C5+ parafininn- mating, spesielt en Fischer-Tropsch voks og hydro- gen til midtdestillater ved at innmatingen og hy- drogen bringes i kontakt, under hydroisomerise- rings-reaksjonsbetingelser, med en katalysator omfattende et gruppe IB metall, et gruppe VIB me- tall, et gruppe VIII metall, eller blandinger av to eller flere av disse metaller, båret på silika- aluminiumoksyd oppslemmet i en parafinvæske. Kata- lysatorpartiklene er tilstede i oppslemmingen i en konsentrasjon større enn 10 vekt%, fortrinnsvis større enn 25 vekt%, og den midlere diameter av partiklene ligger i området 30-150 /mi, fortrinn- svis 40-60 /ui.The invention relates to a hydroisomerization process for converting a C5 + paraffin feed, in particular a Fischer-Tropsch wax and the hydrogen to center distillates by contacting the feed and the hydrogen, under hydroisomerization reaction conditions, with a catalyst comprising a group IB metal, a group VIB metal, a group VIII metal, or mixtures of two or more of these metals, carried on silica alum suspended in a paraffin liquid. The catalyst particles are present in the slurry at a concentration greater than 10% by weight, preferably greater than 25% by weight, and the average diameter of the particles is in the range of 30-150 µm, preferably 40-60 µl.

NO962940A 1995-07-14 1996-07-12 Method of hydroisomerization NO962940L (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US50233695A 1995-07-14 1995-07-14

Publications (2)

Publication Number Publication Date
NO962940D0 NO962940D0 (en) 1996-07-12
NO962940L true NO962940L (en) 1997-01-15

Family

ID=23997362

Family Applications (1)

Application Number Title Priority Date Filing Date
NO962940A NO962940L (en) 1995-07-14 1996-07-12 Method of hydroisomerization

Country Status (8)

Country Link
EP (1) EP0753563B1 (en)
JP (1) JP3860863B2 (en)
AU (1) AU702829B2 (en)
CA (1) CA2179093A1 (en)
DE (1) DE69604978T2 (en)
MY (1) MY115196A (en)
NO (1) NO962940L (en)
SG (1) SG67953A1 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6296757B1 (en) 1995-10-17 2001-10-02 Exxon Research And Engineering Company Synthetic diesel fuel and process for its production
US5689031A (en) 1995-10-17 1997-11-18 Exxon Research & Engineering Company Synthetic diesel fuel and process for its production
US5866748A (en) * 1996-04-23 1999-02-02 Exxon Research And Engineering Company Hydroisomerization of a predominantly N-paraffin feed to produce high purity solvent compositions
CA2204270A1 (en) * 1996-06-04 1997-12-04 Robert J. Wittenbrink Pillared clay catalysts for hydroconversion
US5766274A (en) 1997-02-07 1998-06-16 Exxon Research And Engineering Company Synthetic jet fuel and process for its production
ES2384559T3 (en) * 2001-06-15 2012-07-06 Shell Internationale Research Maatschappij B.V. Microcrystalline wax
GB2455995B (en) * 2007-12-27 2012-09-26 Statoilhydro Asa A method of producing a lube oil from a Fischer-Tropsch wax

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4647369A (en) * 1985-06-14 1987-03-03 Mobil Oil Corporation Catalyst dewaxing process using a slurry phase bubble column reactor
US5187138A (en) * 1991-09-16 1993-02-16 Exxon Research And Engineering Company Silica modified hydroisomerization catalyst
US5370788A (en) * 1992-12-18 1994-12-06 Texaco Inc. Wax conversion process
US5378348A (en) * 1993-07-22 1995-01-03 Exxon Research And Engineering Company Distillate fuel production from Fischer-Tropsch wax

Also Published As

Publication number Publication date
MY115196A (en) 2003-04-30
AU6051196A (en) 1997-01-23
CA2179093A1 (en) 1997-01-15
AU702829B2 (en) 1999-03-04
SG67953A1 (en) 1999-10-19
EP0753563B1 (en) 1999-11-03
EP0753563A1 (en) 1997-01-15
DE69604978D1 (en) 1999-12-09
NO962940D0 (en) 1996-07-12
JPH09169984A (en) 1997-06-30
JP3860863B2 (en) 2006-12-20
DE69604978T2 (en) 2000-05-04

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