AR027321A1 - HYDROISOMERIZATION PROCESS OF A SINGLE STAGE IN MULTIPLE ZONES AND FISCHER AND TROPSCH HYDROCARBON SYNTHESIS PROCESS - Google Patents

HYDROISOMERIZATION PROCESS OF A SINGLE STAGE IN MULTIPLE ZONES AND FISCHER AND TROPSCH HYDROCARBON SYNTHESIS PROCESS

Info

Publication number
AR027321A1
AR027321A1 ARP010100400A ARP010100400A AR027321A1 AR 027321 A1 AR027321 A1 AR 027321A1 AR P010100400 A ARP010100400 A AR P010100400A AR P010100400 A ARP010100400 A AR P010100400A AR 027321 A1 AR027321 A1 AR 027321A1
Authority
AR
Argentina
Prior art keywords
fraction
zone
hydroisomerized
degree
fischer
Prior art date
Application number
ARP010100400A
Other languages
Spanish (es)
Original Assignee
Exxonmobil Res & Eng 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 Exxonmobil Res & Eng Co filed Critical Exxonmobil Res & Eng Co
Publication of AR027321A1 publication Critical patent/AR027321A1/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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only

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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Hidrocarburos sintetizados por el proceso de Fischer-Tropsch que comprenden tanto una fraccion pesada de 500 - 750 degree F + (260 - 371,1 degree C+) como una fraccionpesada de 500 - 750 degree F- (260 - 371,1 degree C-) se hidroisomerizan por separado por medio de un proceso d e hidroisomerizacion de una unica etapa endos zonas, en elcual por lo menos una porcion de la fraccion liviana se hidroisomeriza en la primera zona conteniendo el efluente total de la primera zona hidrogeno sinreaccionar y un hidroisomerizado liviano . El efluente de la primera zona y la fraccion pesada son transferidos a la segunda zona para formar un efluente de lasegunda zona que comprende el producto hidroisomerizado. El producto es fraccionado para obtener una pluralidad e fracciones de prod ucto, inlcuyendo unafraccion de combustibles destilados que contiene una fraccion de combustible para motores a reaccion. Se utiliza gas de tratamiento con hidrogeno para separaruna porcion de la fraccion liviana de la fraccion pesada con anteriorida d a la hidroisomerizacion.Hydrocarbons synthesized by the Fischer-Tropsch process that comprise both a heavy fraction of 500 - 750 degree F + (260 - 371.1 degree C +) and a fraction of 500 - 750 degree F- (260 - 371.1 degree C-) ) they are hydroisomerized separately by means of a single stage hydroisomerization process in both areas, in which at least a portion of the light fraction is hydroisomerized in the first zone containing the total effluent of the first unreacted hydrogen zone and a light hydroisomerized . The effluent from the first zone and the heavy fraction are transferred to the second zone to form an effluent from the second zone comprising the hydroisomerized product. The product is fractionated to obtain a plurality of product fractions, including a fraction of distilled fuels containing a fraction of fuel for jet engines. Hydrogen treatment gas is used to separate a portion of the light fraction from the heavy fraction prior to hydroisomerization.

ARP010100400A 2000-02-03 2001-01-29 HYDROISOMERIZATION PROCESS OF A SINGLE STAGE IN MULTIPLE ZONES AND FISCHER AND TROPSCH HYDROCARBON SYNTHESIS PROCESS AR027321A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US49743800A 2000-02-03 2000-02-03

Publications (1)

Publication Number Publication Date
AR027321A1 true AR027321A1 (en) 2003-03-19

Family

ID=23976869

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP010100400A AR027321A1 (en) 2000-02-03 2001-01-29 HYDROISOMERIZATION PROCESS OF A SINGLE STAGE IN MULTIPLE ZONES AND FISCHER AND TROPSCH HYDROCARBON SYNTHESIS PROCESS

Country Status (8)

Country Link
EP (1) EP1254199A1 (en)
JP (1) JP2003522252A (en)
AR (1) AR027321A1 (en)
AU (1) AU3285901A (en)
BR (1) BR0108019A (en)
CA (1) CA2399070A1 (en)
NO (1) NO20023682L (en)
WO (1) WO2001057160A1 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7198710B2 (en) * 2003-03-10 2007-04-03 Chevron U.S.A. Inc. Isomerization/dehazing process for base oils from Fischer-Tropsch wax
WO2004090078A1 (en) * 2003-04-11 2004-10-21 Sasol Technology (Pty) Ltd Low sulphur diesel fuel and aviation turbine fuel
BRPI0517785A (en) 2004-11-18 2008-10-21 Shell Int Research process for optimizing the yield of base oils from a fischer-tropsch-derived feed
JP2008520787A (en) * 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 Gas oil production method
JP4791167B2 (en) 2005-12-09 2011-10-12 Ｊｘ日鉱日石エネルギー株式会社 Hydrorefining method
KR101211376B1 (en) * 2010-09-30 2012-12-13 한국에너지기술연구원 Fischer-tropsch bubble column reactor feasible multi reaction
CN104673384B (en) * 2015-03-02 2016-09-14 武汉凯迪工程技术研究总院有限公司 A kind of hydrofinishing process of Low Temperature Fischer Tropsch full distillate oil fecund intermediate oil
FR3084082B1 (en) 2018-07-18 2020-08-07 Ifp Energies Now USE OF A BIFUNCTIONAL ZEOLITHE IZM-2-BASED CATALYST FOR THE HYDROISOMERIZATION OF LIGHT PARAFFINIC LOADS FROM FISCHER-TROPSCH SYNTHESIS

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4919786A (en) * 1987-12-18 1990-04-24 Exxon Research And Engineering Company Process for the hydroisomerization of was to produce middle distillate products (OP-3403)
US5378348A (en) * 1993-07-22 1995-01-03 Exxon Research And Engineering Company Distillate fuel production from Fischer-Tropsch wax
US5660714A (en) * 1995-07-14 1997-08-26 Exxon Research And Engineering Company Hydroconversion process utilizing a supported Ni-Cu hydroconversion catalyst

Also Published As

Publication number Publication date
NO20023682D0 (en) 2002-08-02
WO2001057160A1 (en) 2001-08-09
BR0108019A (en) 2002-10-29
NO20023682L (en) 2002-09-25
AU3285901A (en) 2001-08-14
JP2003522252A (en) 2003-07-22
EP1254199A1 (en) 2002-11-06
CA2399070A1 (en) 2001-08-09

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