ES2059701T3 - Metodo para preparar cumeno. - Google Patents

Metodo para preparar cumeno.

Info

Publication number
ES2059701T3
ES2059701T3 ES89201110T ES89201110T ES2059701T3 ES 2059701 T3 ES2059701 T3 ES 2059701T3 ES 89201110 T ES89201110 T ES 89201110T ES 89201110 T ES89201110 T ES 89201110T ES 2059701 T3 ES2059701 T3 ES 2059701T3
Authority
ES
Spain
Prior art keywords
cumeno
preparing
amstrongs
benzene
free
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
ES89201110T
Other languages
English (en)
Inventor
Fabrizio Cavani
Virginio Arrigoni
Giuseppe Bellussi
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.)
Enichem Sintesi SpA
Eni Tecnologie SpA
Original Assignee
Enichem Sintesi SpA
Eniricerche SpA
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 Enichem Sintesi SpA, Eniricerche SpA filed Critical Enichem Sintesi SpA
Application granted granted Critical
Publication of ES2059701T3 publication Critical patent/ES2059701T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/54Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
    • C07C2/64Addition to a carbon atom of a six-membered aromatic ring
    • C07C2/66Catalytic processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12Silica and alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/617500-1000 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63Pore volume
    • B01J35/633Pore volume less than 0.5 ml/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63Pore volume
    • B01J35/6350.5-1.0 ml/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64Pore diameter
    • B01J35/643Pore diameter less than 2 nm
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66Pore distribution
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C6/00Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
    • C07C6/08Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
    • C07C6/12Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
    • C07C6/126Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of more than one hydrocarbon
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/12Silica and alumina
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)

Abstract

SE PREPARA CUMENO POR ALQUILACION DE BENCENO CON PROPILENO, O POR TRANSALQUILACION DE DIISOPROPILBENCENOS EN PRESENCIA DE BENCENO, SOBRE UN CATALIZADOR EN FORMA DE GEL DE SILICE Y ALUMINA QUE ES AMORFO A LOS RAYOS X Y TIENE UNA PROPORCION SIO2/AL2O3 ENTRE 50/1 Y 300/1, UNA SUPERFICIE ESPECIFICA ENTRE 500 Y 1000 M2/G, UN VOLUMEN DE PORO ENTRE 0.3 Y 0.6 ML/G Y UN DIAMETRO DE PORO MEDIO DEL ORDEN DE 10 AMSTRONGS, Y QUE ESTA LIBRE O SUSTANCIALMENTE LIBRE DE POROS CON UN DIAMETRO QUE EXCEDA DE 30 AMSTRONGS.
ES89201110T 1988-05-06 1989-05-01 Metodo para preparar cumeno. Expired - Lifetime ES2059701T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT20495/88A IT1217525B (it) 1988-05-06 1988-05-06 Procedimento per la preparazione di cumene

Publications (1)

Publication Number Publication Date
ES2059701T3 true ES2059701T3 (es) 1994-11-16

Family

ID=11167802

Family Applications (1)

Application Number Title Priority Date Filing Date
ES89201110T Expired - Lifetime ES2059701T3 (es) 1988-05-06 1989-05-01 Metodo para preparar cumeno.

Country Status (6)

Country Link
US (1) US4992608A (es)
EP (1) EP0340862B1 (es)
JP (1) JP2694180B2 (es)
DE (1) DE68910871T2 (es)
ES (1) ES2059701T3 (es)
IT (1) IT1217525B (es)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SI0669162T1 (en) * 1994-02-24 2000-02-29 Fina Research S.A. Silica-alumina carriers preparation, hydrogenation catalysts preparation therewith and their use for aromatics hydrogenation
US5981818A (en) * 1995-03-21 1999-11-09 Stone & Webster Engineering Corp. Integrated cracking and olefins derivative process utilizing dilute olefins
CN1081478C (zh) * 1997-07-21 2002-03-27 青岛海洋化工集团公司 硅铝胶凝胶粒产品
US6593506B1 (en) 2000-10-12 2003-07-15 Exxonmobil Chemical Patents Inc. Olefin recovery in a polyolefin production process
US6495609B1 (en) 2000-11-03 2002-12-17 Exxonmobil Chemical Patents Inc. Carbon dioxide recovery in an ethylene to ethylene oxide production process
EP1479663A1 (en) * 2003-05-17 2004-11-24 Haldor Topsoe A/S Process for catalytic alkylation of monocyclic aromatic compounds and composition of use therein
ES2247921B1 (es) * 2004-04-07 2007-06-16 Universidad Politecnica De Valencia Un material amorfo microporoso, procedimiento de preparacion y su uso en la conversion catalitica de compuestos organicos.

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA507452A (en) * 1954-11-16 Universal Oil Products Company Alkylation process
US366790A (en) * 1886-12-06 1887-07-19 Charles Orther Brush
GB512979A (en) * 1938-02-15 1939-10-02 United Shoe Machinery Corp Improvements in or relating to the splitting of shoe soles
US2589057A (en) * 1948-08-12 1952-03-11 Koppers Co Inc Alkylation-dealkylation process
US3350469A (en) * 1964-08-19 1967-10-31 Sinclair Research Inc Method for the production of paraxylene
JPS5115523B2 (es) * 1971-10-02 1976-05-18
US3784621A (en) * 1971-11-11 1974-01-08 Texaco Development Corp Disproportionation of alkylaromatic hydrocarbons
USB366790I5 (es) * 1973-06-04 1975-01-28
US4314091A (en) * 1980-03-31 1982-02-02 Texaco Inc. Preparation of 1-methyl-3,5-diisopropyl benzene from charge streams containing diisopropyl toluene
JPS6021802A (ja) * 1983-07-15 1985-02-04 Daido Sanso Kk 均一な細孔を有する金属酸化物、その製造方法およびその金属酸化物からなる触媒用担体
JPS60228435A (ja) * 1984-04-27 1985-11-13 エクソン・リサ−チ・アンド・エンジニアリング・カンパニ− 大孔径無定形シリカ−アルミナ触媒を使用する芳香族分子のアルキル化

Also Published As

Publication number Publication date
DE68910871D1 (de) 1994-01-05
JPH0211527A (ja) 1990-01-16
EP0340862A1 (en) 1989-11-08
EP0340862B1 (en) 1993-11-24
JP2694180B2 (ja) 1997-12-24
US4992608A (en) 1991-02-12
IT1217525B (it) 1990-03-22
DE68910871T2 (de) 1994-05-05
IT8820495A0 (it) 1988-05-06

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