ES2093828T3 - Procedimiento para la produccion de olefinas. - Google Patents

Procedimiento para la produccion de olefinas.

Info

Publication number
ES2093828T3
ES2093828T3 ES92908684T ES92908684T ES2093828T3 ES 2093828 T3 ES2093828 T3 ES 2093828T3 ES 92908684 T ES92908684 T ES 92908684T ES 92908684 T ES92908684 T ES 92908684T ES 2093828 T3 ES2093828 T3 ES 2093828T3
Authority
ES
Spain
Prior art keywords
hydrogen
acceptor
hydrocarbon
donor
pct
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.)
Expired - Lifetime
Application number
ES92908684T
Other languages
English (en)
Inventor
Arthur Gough
Stephen Turner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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
Priority claimed from GB919109691A external-priority patent/GB9109691D0/en
Priority claimed from GB919121732A external-priority patent/GB9121732D0/en
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Application granted granted Critical
Publication of ES2093828T3 publication Critical patent/ES2093828T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • 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
    • C07C5/42—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor
    • C07C5/50—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with an organic compound as an acceptor
    • C07C5/52—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with an organic compound as an acceptor with a hydrocarbon as an acceptor, e.g. hydrocarbon disproportionation, i.e. 2CnHp -> CnHp+q + CnHp-q

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)

Abstract

UN PROCESO PARA LA PRODUCCION DE OLEFINAS QUE CONSISTE EN DESHIDROGENAR AL MENOS UN HIDROCARBURO DONANTE DE HIDROGENO QUE ESTA ESENCIALMENTE LIBRE DE INSATURACION OLEFINICA, POR EJEMPLO, UNA PARAFINA, EN PRESENCIA DE UNA CATALIZADOR DE DESHIDROGENACION Y EN PRESENCIA DE AL MENOS UN HIDROCARBURO RECEPTOR DE HIDROGENO QUE ESTA MAS ALTAMENTE INSATURADO QUE UNA MONOOLEFINA, POR EJEMPLO, UN DIENO Y/O ACETILENO, BAJO CONDICIONES EFECTIVAS PARA CAUSAR QUE AL MENOS PARTE DE DICHO HIDROCARBURO DONANTE DE HIDROGENO SE DESHIDROGENE Y AL MENOS PARTE DEL RECEPTOR DE HIDROGENO SE HIDROGENE. LA CANTIDAD DE RECEPTOR DE HIDROGENO SE TAL QUE HAY 0,5 A 20 MOLES DE DICHO DONANTE DE HIDROGENO PARA CADA MOL DE RECEPTOR DE HIDROGENO. PREFERENTEMENTE LA CANTIDAD DE DICHO HIDROCARBURO RECEPTOR DE HIDROGENO HIDROGENADO ES TAL QUE EL CALOR DE HIDROGENACION DE DICHO HIDROCARBURO RECEPTOR DE HIDROGENO PROPORCIONAR A MENOS 35% DEL CALOR REQUERIDO PARA LA DESHIDROGENACION DE DICHO DONATE DE HIDROGENO. EN UNA FORMA PREFERIDA DE LA INVENCION, UNA CORRIENTE DE HIDROCARBURO QUE CONTIENEN EL RECEPTOR DE HIDROGENO ES UNA CORRIENTE C4 DE UN CRAQUEADOR DE HIDROCARBURO Y ES REACCIONADO CON UNA PARAFINA COMO PROPANO O 2.METILPROPANO COMO EL DONANTE DE HIDROGEO; TRAS LA SEPARACION DE PROPENO Y/O 2.METILPROPENO, AL MENOS PARTE DEL PRODUCTO SE RECICLA EN EL CRAQUEADOR.
ES92908684T 1991-05-03 1992-04-16 Procedimiento para la produccion de olefinas. Expired - Lifetime ES2093828T3 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB919109691A GB9109691D0 (en) 1991-05-03 1991-05-03 Transhydrogenation
GB919121732A GB9121732D0 (en) 1991-10-14 1991-10-14 Olefin production

Publications (1)

Publication Number Publication Date
ES2093828T3 true ES2093828T3 (es) 1997-01-01

Family

ID=26298846

Family Applications (1)

Application Number Title Priority Date Filing Date
ES92908684T Expired - Lifetime ES2093828T3 (es) 1991-05-03 1992-04-16 Procedimiento para la produccion de olefinas.

Country Status (19)

Country Link
US (1) US5585530A (es)
EP (1) EP0584095B1 (es)
JP (1) JP3107823B2 (es)
KR (1) KR100229048B1 (es)
CN (1) CN1037091C (es)
AT (1) ATE141907T1 (es)
AU (1) AU1567792A (es)
BR (1) BR9205963A (es)
DE (1) DE69213230T2 (es)
DK (1) DK0584095T3 (es)
ES (1) ES2093828T3 (es)
GB (1) GB9208154D0 (es)
GR (1) GR3021056T3 (es)
IN (1) IN185306B (es)
MY (1) MY108111A (es)
PH (1) PH31055A (es)
PT (1) PT100436B (es)
TW (1) TW197409B (es)
WO (1) WO1992019575A1 (es)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993021138A1 (en) * 1991-05-03 1993-10-28 Imperial Chemical Industries Plc Olefin production
DE69312481T2 (de) * 1992-04-14 1998-02-05 Inst Francais Du Petrol Verfahren zur herstellung von olefinen
GB9222416D0 (en) * 1992-10-26 1992-12-09 Ici Plc Hydrocarbons
US6203694B1 (en) * 1998-05-13 2001-03-20 Phillips Petroleum Company Conversion of heavy hydrocarbon to aromatics and light olefins
JP2000148102A (ja) * 1998-11-10 2000-05-26 Nec Shizuoka Ltd 階調表示装置および階調表示方法
EP1741691A1 (en) * 2005-07-06 2007-01-10 Saudi Basic Industries Corporation Process for the production of ethylene
WO2012061272A2 (en) 2010-11-02 2012-05-10 The University Of North Carolina At Chapel Hill Synthesis of para-xylene and toluene
US9260361B2 (en) * 2011-11-22 2016-02-16 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion process
EP2975013A1 (en) * 2013-04-03 2016-01-20 Scg Chemicals Co. Ltd. Catalyst for converting paraffin to olefin
US9346721B2 (en) 2013-06-25 2016-05-24 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion
EP2960223B1 (en) * 2014-06-25 2019-12-18 Borealis AG An endothermic gas phase catalytic dehydrogenation process
JP6298438B2 (ja) * 2014-11-28 2018-03-20 旭化成株式会社 炭化水素の製造方法
CN104672048B (zh) * 2015-02-11 2016-06-08 辽宁省盘锦监狱 一种制备丁二烯和环己烷的方法
WO2017052860A1 (en) 2015-09-25 2017-03-30 Exxonmobil Chemical Patents Inc. Hydrocarbon dehydrocyclization
EP3544732A1 (en) * 2016-11-24 2019-10-02 SCG Chemicals Co., Ltd. Heterogeneous catalysts and uses thereof
US10221110B2 (en) * 2016-12-08 2019-03-05 Evonik Degussa Gmbh Dehydrogenation of olefin-rich hydrocarbon mixtures
US11136279B2 (en) 2019-09-25 2021-10-05 Exxonmobil Research And Engineering Company Integrated process for producing olefins from alkanes by hydrogen transfer
WO2021096772A1 (en) 2019-11-14 2021-05-20 Exxonmobil Chemical Patents Inc. Gas phase polyethylene copolymers

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3211635A (en) * 1961-04-14 1965-10-12 Phillips Petroleum Co Production of olefins from paraffins and acetylenes
US3267170A (en) * 1964-06-30 1966-08-16 Exxon Research Engineering Co Process for forming olefins by hydrogen transfer
DE1925439C3 (de) * 1969-05-19 1978-11-02 Institut Neftechimitscheskogo Sinteza Imeni A.V. Toptschieva Akademii Nauk Ssr, Moskau Verfahren zur Durchführung von Prozessen in einem Reaktionsgefäß mit katalytisch aktiver, semipermeabler Trennwand
US4546204A (en) * 1983-11-07 1985-10-08 Imperial Chemical Industries Australia Limited Process for the manufacture of methyl t-butyl ether
US4684755A (en) * 1985-09-27 1987-08-04 Ici Australia Limited Catalyzed process
US4684455A (en) * 1985-11-27 1987-08-04 Ex-Cell-O Corporation Electrical continuity clamp for ECM machine
US4975097A (en) * 1987-12-08 1990-12-04 Mobil Oil Corporation Iso-olefin etherification, upgrading and paraffin transhydrogenation
US5176719A (en) * 1988-04-11 1993-01-05 Mobil Oil Corporation Upgrading C4 mixed hydrocarbons by transhydrogenation and isobutene etherification
US5227552A (en) * 1992-04-27 1993-07-13 Mobil Oil Corporation Process for hydrogenating alkenes in the presence of alkanes and a heterogeneous catalyst

Also Published As

Publication number Publication date
DK0584095T3 (es) 1997-02-24
US5585530A (en) 1996-12-17
CN1067237A (zh) 1992-12-23
KR100229048B1 (ko) 1999-11-01
EP0584095A1 (en) 1994-03-02
GR3021056T3 (en) 1996-12-31
TW197409B (es) 1993-01-01
JPH06506924A (ja) 1994-08-04
DE69213230D1 (de) 1996-10-02
PT100436A (pt) 1993-08-31
EP0584095B1 (en) 1996-08-28
PT100436B (pt) 1999-08-31
DE69213230T2 (de) 1997-01-09
IN185306B (es) 2000-12-23
JP3107823B2 (ja) 2000-11-13
AU1567792A (en) 1992-12-21
BR9205963A (pt) 1994-09-27
WO1992019575A1 (en) 1992-11-12
CN1037091C (zh) 1998-01-21
PH31055A (en) 1998-02-03
GB9208154D0 (en) 1992-05-27
MY108111A (en) 1996-08-15
ATE141907T1 (de) 1996-09-15

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