ES2147959T3 - Procedimiento para la produccion de olefinas c3 y c4 a partir de una mezcla inicial que contiene olefinas c4 a c7. - Google Patents

Procedimiento para la produccion de olefinas c3 y c4 a partir de una mezcla inicial que contiene olefinas c4 a c7.

Info

Publication number
ES2147959T3
ES2147959T3 ES97113718T ES97113718T ES2147959T3 ES 2147959 T3 ES2147959 T3 ES 2147959T3 ES 97113718 T ES97113718 T ES 97113718T ES 97113718 T ES97113718 T ES 97113718T ES 2147959 T3 ES2147959 T3 ES 2147959T3
Authority
ES
Spain
Prior art keywords
olefins
mixture containing
sub
procedure
production
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
ES97113718T
Other languages
English (en)
Inventor
Friedrich-Wilhelm Dr Moeller
Peter Dr Koenig
Christopher Higman
Hans-Dieter Dr Holtmann
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.)
GEA Group AG
Original Assignee
Metallgesellschaft AG
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 Metallgesellschaft AG filed Critical Metallgesellschaft AG
Application granted granted Critical
Publication of ES2147959T3 publication Critical patent/ES2147959T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06Catalytic processes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00Catalysts comprising molecular sieves
    • C07C2529/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/40Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins

Landscapes

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

Abstract

LA MEZCLA DE APLICACION QUE CONTIENE OLEFINAS C SUB,4} A C SUB,7}ES EVAPORADA Y MEZCLADA CON VAPOR DE AGUA, AJUSTANDOSE UNA PROPORCION EN PESO H SUB,2}O : HIDROCARBUROS DE ENTRE 0,5 : 1 A 3 : 1. LA MEZCLA DE APLICACION QUE CONTIENE VAPOR DE AGUA ES CONDUCIDA A UNA TEMPERATURA DE ENTRADA DE ENTRE 380 A 700 C A UN REACTOR QUE CONTIENE UN TERRAPLENADO FORMADO POR UN CATALIZADOR DE ZEOLITA GRANULADO Y CON FORMA SELECTIVA. LA ZEOLITA ES DEL TIPO DEL PENTASILO Y TIENE UNA PROPORCION ATOMICA SI : AL DE ENTRE 10 : 1 A 200 : 1. DEL TERRAPLENADO SE EXTRAE UNA MEZCLA DE PRODUCTO, CUYA TEMPERATURA DE 20 A 80 A LA TEMPERATURA DE ENTRADA Y CUYO CONTENIDO TOTAL DE PROPILENO E ISOMEROS BUTENICOS ES DE AL MENOS UN 60 % EN PESO DE LOS COMPONENTES OLEFINICOS DE LA MEZCLA DE APLICACION.
ES97113718T 1996-11-26 1997-08-08 Procedimiento para la produccion de olefinas c3 y c4 a partir de una mezcla inicial que contiene olefinas c4 a c7. Expired - Lifetime ES2147959T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19648795A DE19648795A1 (de) 1996-11-26 1996-11-26 Verfahren zum Erzeugen von C¶3¶- und C¶4¶-Olefinen aus einem C¶4¶- bis C¶7¶-Olefine enthaltenden Einsatzgemisch

Publications (1)

Publication Number Publication Date
ES2147959T3 true ES2147959T3 (es) 2000-10-01

Family

ID=7812714

Family Applications (1)

Application Number Title Priority Date Filing Date
ES97113718T Expired - Lifetime ES2147959T3 (es) 1996-11-26 1997-08-08 Procedimiento para la produccion de olefinas c3 y c4 a partir de una mezcla inicial que contiene olefinas c4 a c7.

Country Status (11)

Country Link
US (1) US5981819A (es)
EP (1) EP0844224B1 (es)
AT (1) ATE192130T1 (es)
CO (1) CO4560575A1 (es)
DE (2) DE19648795A1 (es)
ES (1) ES2147959T3 (es)
GR (1) GR3033537T3 (es)
IN (1) IN192312B (es)
MY (1) MY117528A (es)
PT (1) PT844224E (es)
TW (1) TW369523B (es)

Families Citing this family (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2331613A1 (en) * 1998-05-05 1999-11-11 Johannes P. Verduijn (Deceased) Hydrocarbon conversion to propylene with high silica medium pore zeolite catalysts
DE19933063A1 (de) * 1999-07-15 2001-01-18 Metallgesellschaft Ag Verfahren zum Erzeugen von C¶2¶- bis C¶4¶-Olefinen aus einem C¶4¶- bis C¶8¶-Olefine enthaltenden Einsatzgemisch
DE10000889C2 (de) * 2000-01-12 2002-12-19 Mg Technologies Ag Verfahren zum Erzeugen von C¶2¶- und C¶3¶-Olefinen aus Kohlenwasserstoffen
DE10113041A1 (de) * 2001-03-17 2002-09-26 Linde Ag Verfahren zur Gewinnung von Kohlenwasserstoffprodukten durch thermische Dampfspaltung und nachfolgende katalytische Behandlung
AT411256B (de) * 2001-12-06 2003-11-25 Oemv Ag Vorrichtung zum spalten von vorwiegend gesättigten kohlenwasserstoffen
DE10161665A1 (de) * 2001-12-14 2003-06-26 Lurgi Ag Verfahren zur thermischen Entkokung eines Zeolith-Katalysators
DE10217863A1 (de) * 2002-04-22 2003-10-30 Linde Ag Verfahren und Vorrichtung zur Olefinherstellung
DE10217866A1 (de) * 2002-04-22 2003-11-06 Linde Ag Verfahren und Vorrichtung zur Olefinherstellung
DE10233069C1 (de) * 2002-07-19 2003-09-18 Lurgi Ag Verfahren zur Herstellung von Propylen aus einem C¶4¶ bis C¶8¶ Olefine enthaltenden Einsatzstrom
EP1424128B1 (de) * 2002-12-01 2008-12-31 Süd-Chemie Ag Verwendung eines Katalysators auf der Basis von kristallinem Alumosilicat
CZ298836B6 (cs) * 2004-04-15 2008-02-20 Výzkumný ústav anorganické chemie, a. s. Zeolitový katalyzátor struktury ZSM-5 pro selektivní krakování alkenu a zpusob jeho výroby
CN1303044C (zh) * 2004-05-28 2007-03-07 中国石油化工股份有限公司 烯烃裂解制丙烯、乙烯的催化剂
CN1294107C (zh) * 2004-05-28 2007-01-10 中国石油化工股份有限公司 用于烯烃催化裂解生产丙烯、乙烯的方法
JP2008510032A (ja) * 2004-08-10 2008-04-03 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 炭化水素供給原料から中間留分生成物及び低級オレフィンを製造する方法及び装置
US20060047176A1 (en) * 2004-08-25 2006-03-02 Gartside Robert J Butane removal in C4 upgrading processes
CN100368359C (zh) * 2005-08-15 2008-02-13 中国石油化工股份有限公司 增产丙烯的生产方法
CN100460369C (zh) * 2005-09-07 2009-02-11 中国石油化工股份有限公司 碳四及其以上烯烃催化裂解生产丙烯的方法
CN100413821C (zh) * 2005-09-07 2008-08-27 中国石油化工股份有限公司 含碳烯烃混合物催化裂解生产轻质烯烃的方法
CN100413822C (zh) * 2005-09-07 2008-08-27 中国石油化工股份有限公司 含碳烯烃混合物催化裂解增产丙烯乙烯的方法
CN100443453C (zh) * 2005-09-07 2008-12-17 中国石油化工股份有限公司 烯烃催化裂解生产丙烯、乙烯的方法
CN101045665B (zh) * 2006-03-27 2010-05-12 中国石油化工股份有限公司 含碳烯烃催化裂解生产丙烯和乙烯的方法
CN101190414B (zh) * 2006-11-21 2010-05-12 中国石油化工股份有限公司 催化裂解生产烯烃的流化床催化剂
EP2142619A1 (en) * 2007-04-30 2010-01-13 Shell Internationale Research Maatschappij B.V. Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
CN101952394B (zh) 2007-10-10 2013-09-11 国际壳牌研究有限公司 由烃原料制备中间馏分产物和低级烯烃的系统和方法
EP2231821A1 (en) * 2007-11-29 2010-09-29 Shell Internationale Research Maatschappij B.V. Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
US8137631B2 (en) * 2008-12-11 2012-03-20 Uop Llc Unit, system and process for catalytic cracking
US8246914B2 (en) * 2008-12-22 2012-08-21 Uop Llc Fluid catalytic cracking system
US8889076B2 (en) * 2008-12-29 2014-11-18 Uop Llc Fluid catalytic cracking system and process
WO2013121433A1 (en) 2012-02-14 2013-08-22 Reliance Industries Ltd., A process for catalytic conversion of low value hydrocarbon streams to light olefins
CN106552666B (zh) * 2015-09-30 2019-09-10 中国石油化工股份有限公司 一种催化裂解制烯烃催化剂及其制备方法和应用
CN107586246B (zh) * 2016-07-08 2020-03-27 中国石油化工股份有限公司 芳构化生产芳香烃的方法

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1004878B (zh) * 1987-08-08 1989-07-26 中国石油化工总公司 制取低碳烯烃的烃类催化转化方法
DE3838710A1 (de) * 1988-11-15 1990-05-17 Sued Chemie Ag Katalysator auf der basis von kristallinen alumosilikaten

Also Published As

Publication number Publication date
EP0844224A1 (de) 1998-05-27
EP0844224B1 (de) 2000-04-26
DE19648795A1 (de) 1998-05-28
DE59701506D1 (de) 2000-05-31
ATE192130T1 (de) 2000-05-15
PT844224E (pt) 2000-08-31
US5981819A (en) 1999-11-09
MY117528A (en) 2004-07-31
IN192312B (es) 2004-04-03
TW369523B (en) 1999-09-11
CO4560575A1 (es) 1998-02-10
GR3033537T3 (en) 2000-09-29

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