ES2178401T3 - Proceso para la preparacion de estrechos. - Google Patents

Proceso para la preparacion de estrechos.

Info

Publication number
ES2178401T3
ES2178401T3 ES99910226T ES99910226T ES2178401T3 ES 2178401 T3 ES2178401 T3 ES 2178401T3 ES 99910226 T ES99910226 T ES 99910226T ES 99910226 T ES99910226 T ES 99910226T ES 2178401 T3 ES2178401 T3 ES 2178401T3
Authority
ES
Spain
Prior art keywords
zeolite
binder
catalyst
grams
per gram
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
ES99910226T
Other languages
English (en)
Inventor
Giezen Joseph Cornelis Van
Jean-Paul Lange
Carolus Matthias Anna Mesters
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.)
SHELL INT RESEARCH
Shell Internationale Research Maatschappij BV
Original Assignee
SHELL INT RESEARCH
Shell Internationale Research Maatschappij BV
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 SHELL INT RESEARCH, Shell Internationale Research Maatschappij BV filed Critical SHELL INT RESEARCH
Application granted granted Critical
Publication of ES2178401T3 publication Critical patent/ES2178401T3/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
    • C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
    • C07C15/40—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals
    • C07C15/42—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic
    • C07C15/44—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic the hydrocarbon substituent containing a carbon-to-carbon double bond
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
    • 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
    • C07C2529/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • 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
    • C07C2529/18—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the mordenite type
    • 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
    • C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • 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
    • C07C2529/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/82—Phosphates
    • C07C2529/84—Aluminophosphates containing other elements, e.g. metals, boron
    • C07C2529/85—Silicoaluminophosphates (SAPO compounds)

Landscapes

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

Abstract

Un proceso para la preparación de estireno o estirenos sustituidos de la fórmula general Ar-CR=CH2 donde Ar es un grupo fenilo, tolilo o xililo y R es H o un grupo metilo que comprende deshidratar en fase gaseosa 1- feniletanol o 1-feniletanol sustituido de la fórmula general Ar-C(R)(CH3)-OH, donde Ar y R son como se ha definido anteriormente, en presencia de un catalizador sólido ácido que contiene una zeolita y un material aglutinante, en el que la proporción en peso de zeolita respecto al aglutinante está en intervalo de 1:99 a 90:10 y al que le corresponde la siguiente relación: 0 < K < 5 (1) con: K = V/S * [(Pz * fz) + (Pb * fb)]1/2 (2) donde: V/S es la relación volumen/superficie del catalizador utilizado en mm; fz es la fracción en peso de zeolita presente en el catalizador en gramos de zeolita por gramo de catalizador; fb es la fracción en peso de aglutinante presente en el catalizadoren gramos de aglutinante por gramo de catalizador; Pz es la productividad intrínseca de la zeolita expresada como gramos de estireno producidos por gramo de zeolita por hora, medida para muestras de zeolita pura de un tamaño de partículas < 0,1 mm a la temperatura aplicada en la deshidratación en fase gaseosa y con una conversión del 1- feniletanol en estireno por debajo de 80%; y Pb es la productividad intrínseca del aglutinante expresada como gramos de estireno producidos por gramo de aglutinante por hora, medida para muestras de aglutinante puro de un tamaño de partículas < 0,1 mm en las mismas condiciones utilizadas para determinar Pz.
ES99910226T 1998-02-18 1999-02-16 Proceso para la preparacion de estrechos. Expired - Lifetime ES2178401T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP98200513 1998-02-18

Publications (1)

Publication Number Publication Date
ES2178401T3 true ES2178401T3 (es) 2002-12-16

Family

ID=8233402

Family Applications (1)

Application Number Title Priority Date Filing Date
ES99910226T Expired - Lifetime ES2178401T3 (es) 1998-02-18 1999-02-16 Proceso para la preparacion de estrechos.

Country Status (9)

Country Link
US (1) US6395946B1 (es)
EP (1) EP1056696B1 (es)
JP (1) JP2002503711A (es)
KR (1) KR100584830B1 (es)
AU (1) AU2926399A (es)
CA (1) CA2322041A1 (es)
DE (1) DE69902755T2 (es)
ES (1) ES2178401T3 (es)
WO (1) WO1999042425A1 (es)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100839680B1 (ko) 2000-12-27 2008-06-19 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 오염물량이 감소된 유기 하이드로과산화물을 제조하는 방법
AU2003244447B2 (en) 2002-02-06 2008-06-19 Shell Internationale Research Maatschappij B.V. Process for preparing alkylaryl hydroperoxide containing product
US6844454B2 (en) 2002-04-12 2005-01-18 Shell Oil Company Process
US20050085677A1 (en) * 2003-10-15 2005-04-21 Fina Technology, Inc. Method for improved production of cyclohexenyl and alkenyl aromatic compounds
US7863493B2 (en) 2006-04-12 2011-01-04 Shell Oil Company Process for preparing an organic hydroperoxide, industrial set-up therefore and process wherein such organic hydroperoxide is used in the preparation of an alkylene oxide
KR101478850B1 (ko) 2006-11-13 2015-01-02 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 에틸벤젠을 에틸벤젠 하이드로퍼옥사이드로 액상 산화하는 방법
US9221775B2 (en) 2014-01-03 2015-12-29 Shell Oil Company Alkylene oxide production
RU2608303C1 (ru) * 2015-08-06 2017-01-17 Общество с ограниченной ответственностью "Научно-производственное объединение ЕВРОХИМ" Кальцийфосфатный катализатор для парофазной дегидратации фракции метилфенилкарбинола
CN110753575A (zh) 2017-06-07 2020-02-04 日本碍子株式会社 脱水方法及脱水装置

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU988803A2 (ru) * 1980-10-21 1983-01-15 Институт Теоретических Проблем Химической Технологии Ан Азсср Способ получени стирола
JPS6172727A (ja) * 1984-09-17 1986-04-14 Nippon Sheet Glass Co Ltd スチレンの製造方法
JPS61293936A (ja) * 1985-06-21 1986-12-24 Kureha Chem Ind Co Ltd 芳香族側鎖α−位アルコ−ルの液相脱水法

Also Published As

Publication number Publication date
CA2322041A1 (en) 1999-08-26
KR20010024913A (ko) 2001-03-26
EP1056696A1 (en) 2000-12-06
JP2002503711A (ja) 2002-02-05
DE69902755D1 (de) 2002-10-10
KR100584830B1 (ko) 2006-05-30
US6395946B1 (en) 2002-05-28
EP1056696B1 (en) 2002-09-04
AU2926399A (en) 1999-09-06
DE69902755T2 (de) 2003-08-14
WO1999042425A1 (en) 1999-08-26

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