Gas phase polymerization process of C2-C8-alk-1-enes using a Ziegler-Natta- or a metallocene catalyst

Gas phase homo- or copolymerisation of 2-8C alk-1-enes with a Ziegler-Natta or metallocene catalyst system is carried out in a stirred bed of finely-divided polymer, with addition of the catalyst solid (I) containing transition metal with the alkene. The novelty is that (I) is introduced into the re...

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Main Authors LANGHAUSER, FRANZ, KERSTING, MEINOLF, WERNER, RAINER ALEXANDER, LUTZ, GERALD
Format Patent
LanguageEnglish
French
German
Published 27.01.1999
Edition6
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Abstract Gas phase homo- or copolymerisation of 2-8C alk-1-enes with a Ziegler-Natta or metallocene catalyst system is carried out in a stirred bed of finely-divided polymer, with addition of the catalyst solid (I) containing transition metal with the alkene. The novelty is that (I) is introduced into the reactor with (part of) the alkene through (almost) vertical pipe(s) projecting down into the gas space and ending above the stirred powder bed. Also claimed is the apparatus used. Preferably the vertical distance between the pipe(s) and the surface of the bed is < 15%, especially < 10% of the distance between the top of the reactor and the bed. The pipe(s) end in the middle of the reactor or are slightly eccentric, such that distance of the end(s) of the pipe(s) from the middle is < 20%, especially < 15% of the radius of the reactor. The bed is agitated with a spiral stirrer.
AbstractList Gas phase homo- or copolymerisation of 2-8C alk-1-enes with a Ziegler-Natta or metallocene catalyst system is carried out in a stirred bed of finely-divided polymer, with addition of the catalyst solid (I) containing transition metal with the alkene. The novelty is that (I) is introduced into the reactor with (part of) the alkene through (almost) vertical pipe(s) projecting down into the gas space and ending above the stirred powder bed. Also claimed is the apparatus used. Preferably the vertical distance between the pipe(s) and the surface of the bed is < 15%, especially < 10% of the distance between the top of the reactor and the bed. The pipe(s) end in the middle of the reactor or are slightly eccentric, such that distance of the end(s) of the pipe(s) from the middle is < 20%, especially < 15% of the radius of the reactor. The bed is agitated with a spiral stirrer.
Author LUTZ, GERALD
LANGHAUSER, FRANZ
KERSTING, MEINOLF
WERNER, RAINER ALEXANDER
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DocumentTitleAlternate Procédé de polymérisation en phase gazeuse de 1-alcènes en C2-C8 utilisant un catalyseur Ziegler-Natta ou métallocene
Verfahren zur Gasphasenpolymerisation von C2-C8-Alk-1-enen mittels Ziegler-Natta- oder Metallocen-Katalysatorsystemen
Edition 6
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Snippet Gas phase homo- or copolymerisation of 2-8C alk-1-enes with a Ziegler-Natta or metallocene catalyst system is carried out in a stirred bed of finely-divided...
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SubjectTerms CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
CHEMISTRY
COMPOSITIONS BASED THEREON
MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVINGCARBON-TO-CARBON UNSATURATED BONDS
METALLURGY
ORGANIC MACROMOLECULAR COMPOUNDS
PERFORMING OPERATIONS
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
THEIR PREPARATION OR CHEMICAL WORKING-UP
THEIR RELEVANT APPARATUS
TRANSPORTING
Title Gas phase polymerization process of C2-C8-alk-1-enes using a Ziegler-Natta- or a metallocene catalyst
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