NO20012691L - Isomerisering av hydrokarboner - Google Patents

Isomerisering av hydrokarboner

Info

Publication number
NO20012691L
NO20012691L NO20012691A NO20012691A NO20012691L NO 20012691 L NO20012691 L NO 20012691L NO 20012691 A NO20012691 A NO 20012691A NO 20012691 A NO20012691 A NO 20012691A NO 20012691 L NO20012691 L NO 20012691L
Authority
NO
Norway
Prior art keywords
isomerization
carbon atoms
feed stream
catalyst
deactivation
Prior art date
Application number
NO20012691A
Other languages
English (en)
Other versions
NO20012691D0 (no
Inventor
Edgar D Davis
Fan-Nan Lin
Original Assignee
Phillips Petroleum 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 Phillips Petroleum Co filed Critical Phillips Petroleum Co
Publication of NO20012691D0 publication Critical patent/NO20012691D0/no
Publication of NO20012691L publication Critical patent/NO20012691L/no

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/13—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation with simultaneous isomerisation
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
    • C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
    • C07C5/2702—Catalytic processes not covered by C07C5/2732 - C07C5/31; Catalytic processes covered by both C07C5/2732 and C07C5/277 simultaneously
    • C07C5/2724—Catalytic processes not covered by C07C5/2732 - C07C5/31; Catalytic processes covered by both C07C5/2732 and C07C5/277 simultaneously with metals
    • 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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C10G35/06—Catalytic reforming characterised by the catalyst used
    • C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof
    • 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
    • C10G45/62—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 containing platinum group metals or compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Isomeriseringsprosess for omdannelse av minst én isomeriseringstilførsels-strøm som inneholder av alkaner med 4 karbonatomer til 10 karbonatomer pr. molekyl og cykloalkaner med 5 karbonatomer til 10 karbonatomer pr. molekyl, til minst én produkt-hydrokarbonisomer. Isomeriseringstilførselsstrømmen som inneholder minst ett hydrokarbonutgangsmateriale og hydrogen, bringes i en isomeriseringssone ved effektive isomeriseringsbetingelser i kontakt med en katalysator, hvor deaktivering av nevnte katalysator finner sted i nevnte isomeriseringssone. Isomeriseringsprosessen inkluderer nærvær av et additiv i isomeriseringstilfør-selsstrømmen. Konsentrasjonen av additivet er tilstrekkelig til å lindre eller minske deaktiveringen av katalysatoren og å opprettholde en i hovedsak konstant omdannelse av det minst ene utgangshydrokarbonet til den minst ene produkt-hydrokar-bonisomeren ved effektive isomeriseringsbetingelser.
NO20012691A 1998-12-01 2001-05-31 Isomerisering av hydrokarboner NO20012691L (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/203,081 US6140547A (en) 1998-12-01 1998-12-01 Isomerization of hydrocarbons
PCT/US1999/027427 WO2000032544A1 (en) 1998-12-01 1999-11-19 Isomerization of hydrocarbons

Publications (2)

Publication Number Publication Date
NO20012691D0 NO20012691D0 (no) 2001-05-31
NO20012691L true NO20012691L (no) 2001-07-25

Family

ID=22752420

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20012691A NO20012691L (no) 1998-12-01 2001-05-31 Isomerisering av hydrokarboner

Country Status (12)

Country Link
US (1) US6140547A (no)
EP (1) EP1135351A4 (no)
JP (1) JP2002531425A (no)
KR (1) KR20010101104A (no)
CN (1) CN1329585A (no)
AU (1) AU744667B2 (no)
CA (1) CA2350481A1 (no)
ID (1) ID29469A (no)
NO (1) NO20012691L (no)
RU (1) RU2219153C2 (no)
WO (1) WO2000032544A1 (no)
ZA (1) ZA200104228B (no)

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6558532B1 (en) * 1999-11-24 2003-05-06 Phillips Petroleum Company Catalytic reforming process
US6458266B1 (en) * 1999-11-24 2002-10-01 Phillips Petroleum Company Catalytic reforming process with inhibition of catalyst deactivation
US6610196B1 (en) * 1999-11-24 2003-08-26 Conocophillips Company Catalytic reforming process
US6478952B1 (en) * 2000-07-19 2002-11-12 Phillips Petroleum Company Catalytic reforming process including the addition of organic aluminum halide
WO2002102929A2 (en) * 2001-06-14 2002-12-27 Conocophillips Company Improved catalytic reforming process
US20030114726A1 (en) * 2001-12-19 2003-06-19 Williams Linda D. Novel catalytic isomerization process
US20040116764A1 (en) * 2002-12-12 2004-06-17 Randolph Bruce B. Disproportionation of hydrocarbons
US20040116759A1 (en) * 2002-12-13 2004-06-17 Randolph Bruce B. Oligomerization of hydrocarbons
US20060270885A1 (en) * 2005-05-31 2006-11-30 Boyer Christopher C Normal heptane isomerization
US7659438B1 (en) 2009-02-17 2010-02-09 Conocophillips Company Isomerization of wet hexanes
US8426666B2 (en) * 2009-02-17 2013-04-23 Phillips 66 Company Isomerization of wet hexanes
US8163067B2 (en) * 2009-06-16 2012-04-24 Uop Llc Apparatus and process for isomerizing a hydrogen stream
US8157893B2 (en) * 2009-06-16 2012-04-17 Uop Llc Apparatus and process for isomerizing a hydrocarbon stream
US8163068B2 (en) * 2009-06-16 2012-04-24 Uop Llc Apparatus and process for isomerizing a hydrocarbon stream
US8198501B2 (en) * 2009-11-30 2012-06-12 Chevron U.S.A. Inc. Zeolite catalyst for hydroisomerization of light paraffins to produce high octane gasoline
US20130261358A1 (en) * 2012-03-29 2013-10-03 Uop Llc Methods and apparatuses for isomerization of paraffins
US20140171702A1 (en) * 2012-12-14 2014-06-19 Uop Llc Methods and apparatuses for increasing alkyl-cyclopentane concentrations in aromatic-rich streams
EA032895B1 (ru) * 2014-04-22 2019-07-31 Басф Се Способ получения циклогексана из бензола и метилциклопентана с предварительным гидрированием бензола
CN105399591B (zh) * 2014-08-27 2017-08-11 中国石油化工股份有限公司 甲基戊烷的制备方法
CN105439801B (zh) * 2014-08-27 2018-04-06 中国石油化工股份有限公司 环己烷的制备方法
CN104892337B (zh) * 2015-05-15 2017-01-04 中国石油大学(华东) 一种低碳正构烷烃低温异构化的方法
CN104892339B (zh) * 2015-06-05 2017-03-01 常州瑞华化工工程技术有限公司 一种由异丁烷制备正丁烷的方法
CN106622305A (zh) * 2015-10-28 2017-05-10 中国石油化工股份有限公司 一种烷烃异构化催化剂及其制备方法
CN108080009A (zh) * 2016-11-21 2018-05-29 中国石油大学(华东) 一种烷烃异构化反应-再生装置及方法
CN108144652B (zh) * 2016-12-04 2019-12-03 中国科学院大连化学物理研究所 一种费托合成蜡异构化催化剂及制备和应用
CN113122312A (zh) * 2019-12-30 2021-07-16 中国石油大学(北京) 一种以环烷烃为共催化剂助催化生产烷基化汽油的方法
US11034629B1 (en) * 2020-01-06 2021-06-15 Uop Llc Integrated perchloroethylene decomposition reactor design for C4 and C5-6 isomerization units

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2945910A (en) * 1958-06-09 1960-07-19 Phillips Petroleum Co Aluminum chloride-hydrocarbon complex sludge catalyst separation
US3158662A (en) * 1960-08-26 1964-11-24 Exxon Research Engineering Co Isomerization process
US3192286A (en) * 1961-12-08 1965-06-29 Phillips Petroleum Co Process for isomerization of hexanes
US5294328A (en) * 1990-05-24 1994-03-15 Uop Production of reformulated gasoline
US5654247A (en) * 1994-03-08 1997-08-05 Phillips Petroleum Company Method for the reactivation of a deactivated hydrocarbon isomerization catalyst
US5474964A (en) * 1994-09-16 1995-12-12 Phillips Petroleum Company Hydrocarbon isomerization catalyst and use thereof
US5543374A (en) * 1994-11-15 1996-08-06 Phillips Petroleum Company Isomerization catalyst and use thereof in alkane/cycloalkane isomerization
US5557029A (en) * 1995-09-06 1996-09-17 Phillips Petroleum Company Isomerization of saturated hydrocarbons

Also Published As

Publication number Publication date
JP2002531425A (ja) 2002-09-24
AU1629100A (en) 2000-06-19
CA2350481A1 (en) 2000-06-08
CN1329585A (zh) 2002-01-02
KR20010101104A (ko) 2001-11-14
NO20012691D0 (no) 2001-05-31
US6140547A (en) 2000-10-31
WO2000032544A1 (en) 2000-06-08
ID29469A (id) 2001-08-30
EP1135351A1 (en) 2001-09-26
RU2219153C2 (ru) 2003-12-20
EP1135351A4 (en) 2002-08-21
ZA200104228B (en) 2002-08-23
AU744667B2 (en) 2002-02-28

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