IP Library Granted Patent US 7,816,452
Granted Patent B2
US 7,816,452 · App. 10/522,082 · Granted Oct 19, 2010

At least two-stage process for preparing propylene polymer compositions

Assignee: Basell Poliolifine Italia s.r.l.
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Quick Facts
Patent No.
US 7,816,452
App. No.
10/522,082
Granted
Oct 19, 2010
Kind
B2
Abstract

The present invention relates to a process for preparing propylene polymer compositions in at least two-stage process wherein, in a first stage, a propylene homopolymer or a propylene copolymer comprising propylene and at least a CZ-CIO-1-alkenes other than propylene, containing at least 85% by weight of propylene, is prepared by polymerization and, in a second stage, ethylene and at least a comonomer selected from propylene and C4-C,o1alkenes are polymerized to give an ethylene polymer, comprising at least 90% by weight of ethylene, wherein the amount of the ethylene polymer in the propylene polymer composition ranges from 10 to 50% by weight and the propylene polymer composition has a melt flow rate MFR, in accordance with ISO 1133 at 230° C. and 2.16 kg, of from 2 to 50 g/10 min.

Claims (34)

1. A process for preparing a propylene polymer composition in an at least two-stage process, wherein,

in a first polymerization stage, a propylene homopolymer is prepared by polymerization, and

in a second polymerization stage, ethylene and propylene are polymerized to give an ethylene/propylene copolymer comprising more than 97% to 99.5% by weight of ethylene,

wherein the amount of the ethylene/propylene copolymer in the propylene polymer composition ranges from 10 to 50% by weight, and the propylene polymer composition comprises a melt flow rate, MFR, from 2 to 50 g/10 min. in accordance with ISO 1133 at 230° C. and 2.16 kg.

2. The process as claimed in claim 1 , wherein the propylene homopolymer prepared in the first polymerization stage comprises a melt flow rate, MFR, from 5 to 150 g/10 min, in accordance with ISO 1133 at 230° C. and 2.16 kg.

3. The process as claimed in claim 1 , wherein both the first and the second polymerization stages are carried out in gas phase.

4. The process as claimed in claim 3 , wherein in the first polymerization stage the polymerization is carried out at a pressure from 10 to 50 bar and a temperature from 50 to 100° C., in presence of a polymerization-active catalyst system; the propylene homopolymer obtained in the first polymerization stage together with the catalyst system is introduced into an intermediate vessel, depressurized to less than 5 bar for from 0.01 to 5 minutes and the pressure in the intermediate vessel is then increased from 5 to 60 bar by injection of a gas mixture whose composition differs from the composition of the gas mixture of the first polymerization stage; the propylene homopolymer together with the catalyst is subsequently transferred to the second polymerization stage and further polymerized at a pressure from 10 to 50 bar and a temperature from 50 to 100° C.

5. A process for preparing a polymer composition comprising (1) preparing a propylene polymer composition in an at least two-stage process, wherein,

in a first polymerization stage, a propylene homopolymer is prepared by polymerization, and

in a second polymerization stage, ethylene and propylene are polymerized to give an ethylene/propylene copolymer comprising more than 97% to 99.5% by weight of ethylene,

wherein the amount of the ethylene/propylene copolymer in the propylene polymer composition ranges from 10 to 50% by weight, and the propylene polymer composition comprises a melt flow rate, MFR, from 2 to 50 g/10 min, in accordance with ISO 1133 at 230° C. and 2.16 kg; and

(2) subsequently mixing an ethylene-C 3 -C 10 -1-alkene copolymer comprising a crystallinity lower than the ethylene/propylene copolymer formed in the second polymerization stage.

6. A propylene polymer composition obtained by an at least two-stage process, wherein,

in a first polymerization stage, a propylene homopolymer is prepared by polymerization, and

in a second polymerization stage, ethylene and propylene are polymerized to give an ethylene/propylene copolymer comprising more than 97% to 99.5% by weight of ethylene,

wherein the amount of the ethylene/propylene copolymer in the propylene polymer composition ranges from 10 to 50% by weight, and the propylene polymer composition comprises a melt flow rate, MFR, from 2 to 50 g/10 min, in accordance with ISO 1133 at 230° C. and 2.16 kg.

7. A method for producing films, fibers or moldings comprising extruding or molding a propylene polymer composition to form the films, fibers or moldings, the propylene polymer composition obtained by an at least two-stage process, wherein,

in a first polymerization stage, a propylene homopolymer is prepared by polymerization, and

in a second polymerization stage, ethylene and propylene are polymerized to give an ethylene/propylene copolymer comprising more than 97% to 99.5% by weight of ethylene,

wherein the amount of the ethylene/propylene copolymer in the propylene polymer composition ranges from 10 to 50% by weight, and the propylene polymer composition comprises a melt flow rate, MFR, from 2 to 50 g/10 min, in accordance with ISO 1133 at 230° C. and 2.16 kg.

8. A film, fiber or molding comprising a propylene polymer composition, the propylene polymer composition obtained by a process, wherein, the process comprises at least two-stages, and

in a first polymerization stage, a propylene homopolymer is prepared by polymerization, and

in a second polymerization stage, ethylene and propylene are polymerized to give an ethylene/propylene copolymer comprising more than 97% to 99.5% by weight of ethylene; and

wherein the amount of the ethylene/propylene copolymer in the propylene polymer composition ranges from 10 to 50% by weight, and the propylene polymer composition comprises a melt flow rate, MFR, from 2 to 50 g/10 min in accordance with ISO 1133 at 230° C. and 2.16 kg.

9. A propylene polymer composition obtained by a process comprising (1) preparing a propylene polymer composition in an at least two-stage process, wherein,

in a first polymerization stage, a propylene homopolymer is prepared by polymerization, and

in a second polymerization stage, ethylene and propylene are polymerized to give an ethylene/propylene copolymer comprising more than 97% to 99.5% by weight of ethylene,

wherein the amount of the ethylene/propylene copolymer in the propylene polymer composition ranges from 10 to 50% by weight, and the propylene polymer composition comprises a melt flow rate, MFR, from 2 to 50 g/10 min, in accordance with ISO 1133 at 230° C. and 2.16 kg; and

(2) subsequently mixing an ethylene-C 3 -C 10 -1-alkene copolymer comprising a crystallinity lower than the ethylene/propylene copolymer formed in the second polymerization stage.

10. A film, fiber or molding comprising a propylene polymer composition obtained by a process comprising (1) preparing a propylene polymer composition in an at least two-stage process, wherein,

in a first polymerization stage, a propylene homopolymer is prepared by polymerization, and

in a second polymerization stage, ethylene and propylene are polymerized to give an ethylene/propylene copolymer comprising more than 97% to 99.5% by weight of ethylene,

wherein the amount of the ethylene/propylene copolymer in the propylene polymer composition ranges from 10 to 50% by weight, and the propylene polymer composition comprising a melt flow rate, MFR, from 2 to 50 g/10 min, in accordance with ISO 1133 at 230° C. and 2.16 kg; and

(2) subsequently mixing an ethylene-C 3 -C 10 -1-alkene copolymer comprising a crystallinity lower than the ethylene/propylene copolymer formed in the second polymerization stage.

Assignments (5)
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0705 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0856 →
SECURITY AGREEMENT Recorded Aug 4, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; BASELL POLYOLEFIN GMBH; LYONDELL CHEMICAL COMPANY; EQUISTAR CHEMICALS, L.P.
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 021354/0708 →
GRANT OF SECURITY INTEREST IN UNITED STATES PATENTS AND PATENT APPLICATIONS Recorded Mar 26, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; EQUISTAR CHEMICALS. LP.; LYONDELL CHEMICAL COMPANY; LYONDELL CHEMICAL TECHNOLOGY, L.P.; LYONDELL PETROCHEMICAL COMPANY; NATIONAL DISTILLERS AND CHEMICAL CORPORATION; OCCIDENTAL CHEMICAL CORPORATION; OLIN CORPORATION; QUANTUM CHEMICAL CORPORATION; BASELL POLYOLEFIN GMBH
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 020704/0562 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 21, 2005
From: DAHN, ULRICH CLEMENS; BIDELL, WOLFGANG; ZIMMERMANN, HANG-JURGEN; ROESCH, JOACHIM; SCHWEIER, GUENTHER
To: BASELL POLYOLEFINE GMBH
Reel/Frame 016774/0015 →
Priority Claims (1)
DE 102 33 700 · Jul 24, 2002 · national
Continuity (2)
Provisional Application 6040194700 · Aug 8, 2002
Related Publication 20050239967A1 · Oct 27, 2005