Method of olefin polymerization utilizing hydrogen pulsing, products made therefrom, and method of hydrogenation
AssigneeFina Technology, Inc.
InventorsEdwar S. Shamshoum, David J. Rauscher
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Abstract
An olefin polymerization process in which at least two introductions of hydrogen are made during the olefin polymerization reaction. Suitable catalysts include metallocenes of the general formula (Cp).sub.m TiX.sub.n, wherein Cp is a substituted or unsubstituted cyclopentadienyl ring, X is a halogen, m=1-2, n=2-3, and wherein m+n=4, and conventional Ziegler-Natta catalysts blended with or modified by such metallocenes.
Claims20
A process for the polymerization of olefins, comprising:
- (a) contacting together in a reaction zone for a reaction residence time, olefin monomer in the presence of a catalyst system to form a polymer product;
- (b) introducing hydrogen at an addition rate to the reaction zone during the contacting of step (a), wherein the hydrogen is introduced to achieve a first hydrogen concentration, with the introduction subsequently stopped to allow the hydrogen to deplete at a depletion rate to a second hydrogen concentration;
- and
- (c) repeating step (b) prior to expiration of the reaction residence time.
A process for the polymerization of olefins, comprising:
- (a) contacting together in a reaction zone for a reaction residence time, olefin monomer in the presence of a catalyst system to form a polymer product, wherein the catalyst system comprises a Ziegler-Natta catalyst modified by a metallocene of the general formula (Cp).sub.m TiX.sub.n, wherein Cp is a substituted or unsubstituted cyclopentadienyl ring, X is a halogen, m=1-2, n=2-3, and wherein m+n=4;
- (b) introducing hydrogen at an addition rate to the reaction zone during the contacting of step (a), wherein the hydrogen is introduced to achieve a first hydrogen concentration, with the introduction subsequently stopped to allow the hydrogen to deplete at a depletion rate to a second hydrogen concentration;
- and
- (c) repeating step (b) prior to expiration of the reaction residence time.
A process for the polymerization of propylene, comprising:
- (a) contacting together in a reaction zone for a reaction residence time, propylene in the presence of a catalyst system to form a polymer product, wherein the catalyst system comprises a Ziegler-Natta catalyst modified by a metallocene of the general formula (Cp).sub.m TiX.sub.n, wherein Cp is a substituted or unsubstituted cyclopentadienyl ring, X is a halogen, m=1-2, n=2-3, and wherein m+n=4;
- (b) introducing hyrogen at an addition rate to the reaction zone during the contacting of step (a), wherein the hydrogen is introduced to achieve a first hydrogen concentration, with the introduction subsequently stopped to allow the hydrogen to deplete at a depletion rate to a second hydrogen concentration;
- and
- (c) repeating step (b) prior to expiration of the reaction residence time.
A process for the polymerization of propylene, comprising:
- (a) contacting together in a reaction zone for a reaction residence time, propylene monomer in the presence of a catalyst system to form a polymer product, wherein the catalyst system comprises a Ziegler-Natta catalyst modified by Cp.sub.2 TiCl.sub.2 or CpTiCl.sub.3 ;
- (b) introducing hydrogen at an addition rate to the reaction zone during the contacting of step (a), wherein the hydrogen is introduced to achieve a first hydrogen concentration, with the introduction subsequently stopped to allow the hydrogen to deplete at a depletion rate to a second hydrogen concentration;
- and
- (c) repeating step (b) prior to expiration of the reaction residence time.
Dependencies are inferred from the claim text.