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Publication numberUSH1518 H
Publication typeGrant
Application numberUS 08/304,974
Publication dateFeb 6, 1996
Filing dateSep 13, 1994
Priority dateNov 3, 1993
Publication number08304974, 304974, US H1518 H, US H1518H, US-H-H1518, USH1518 H, USH1518H
InventorsLie K. Djiauw, Michael J. Modic, Richard Gelles, Glenn R. Himes
Original AssigneeShell Oil Company
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Impact modification of polypropylene with styrene/isoprene triblock copolymers
US H1518 H
Abstract
Compositions consisting essentially of from 60% to 95% by weight of the polymer components of a high flow polypropylene and from 40% to 5% by weight of a polystyrene-hydrogenated polyisoprene-polystyrene block copolymer have excellent low temperature impact strength and high heat distortion temperature for molding large automobile parts.
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Claims(4)
What is claimed is:
1. A polypropylene molding composition, comprising:
from 60% to 95% by weight of the polymer components of a high flow polypropylene having a melt flow from 50 to 80 dg/min, wherein the polypropylene is selected from a group consisting of homopolymers of propylene, random copolymers of propylene and an olefin selected from ethylene and C4 -C10 alpha-olefins, and random terpolymers of propylene with two alpha-olefins selected from ethylene and C4 -C10 alpha-olefins; and
from 40% to 5% by weight of the polymer components of a polystyrene-hydrogenated polyisoprene-polystyrene block copolymer having a peak molecular weight from 4,500 to 8,000 for each polystyrene block and a polystyrene content from 13% to 20%.
2. The composition of claim 1, wherein each polystyrene block in the block copolymer has a peak molecular weight from 5,000 to 5,500.
3. The composition of claim 1, wherein the high flow polypropylene comprises from 80% to 95% of the polymer components.
4. The composition of claim 1, further comprising up to about 80 parts of a filler per 100 parts of the total polymer components.
Description

This is a continuation of application Ser. No. 08/150,654, filed Nov. 3, 1993, now abandoned.

FIELD OF THE INVENTION

The invention relates to compositions that contain polyolefin resins and elastomeric block copolymers. More specifically, the invention relates to polypropylene molding compositions that have improved impact resistance.

BACKGROUND OF THE INVENTION

Polypropylene molding compositions containing low or medium flow polypropylene have good impact resistance when the composition includes a high molecular weight styrenic block copolymer having the structure polystyrene-hydrogenated polybutadiene-polystyrene, e.g. KRATON® G1650 thermoplastic elastomer. The impact strengths are suitable for use of the molding compositions in large automotive parts. However, research has established that polypropylene molding compositions for large automotive parts must also have improvements in rigidity, heat deformation resistance, low temperature impact resistance, and surface appearance.

High flow polypropylene molding compositions that are suitable for large automotive parts except for inferior low temperature impact strength and inferior high temperature heat deformation are produced by blending low molecular weight polystyrene with low molecular weight diblock copolymers of polystyrene-hydrogenated butadiene. A blend of the triblock and diblock copolymers is commercially available as KRATON® G1657 elastomer which is available from Shell.

U.S. Pat. No. 5,045,589 describes much improved polypropylene molding compositions comprising a crystalline ethylene/propylene block copolymer, an amorphous polypropylene copolymer, and a thermoplastic elastomer which can be a polystyrene-hydrogenated polybutadiene-polystyrene elastomer, e.g. KRATON® G1650 elastomer, or a polystyrene-hydrogenated polyisoprene-polystyrene elastomer.

SUMMARY OF THE INVENTION

The present invention provides a high flow polypropylene molding composition that is excellent for large automobile parts, the polypropylene composition containing a low molecular weight polystyrene-hydrogenated polyisoprene-polystyrene elastomer which is superior to butadiene based elastomers for improving low temperature impact strength and high temperature heat distortion. The isoprene based triblock polymers are also excellent modifiers for blends containing ethylene/propylene block polymers.

DETAILED DESCRIPTION OF THE INVENTION

Polypropylene molding compositions comprising 60-95%, preferably 80-95%, by weight of the polymer components of a high flow polypropylene homopolymer or copolymer and 40-5%, preferably 20-5%, by weight of the polymer components of a low molecular weight polystyrene-hydrogenated polyisoprene-polystyrene block copolymer have excellent physical and appearance properties including superior low temperature impact strength and superior high temperature heat deformation. The peak molecular weight of the block copolymers ranges from 58,000 to 82,000 with a polystyrene content from 13% to 20%.

The high flow propylene polymer can be (i) a homopolymer of propylene, (ii) a random copolymer of propylene and an olefin selected from ethylene and C4 -C10 alpha-olefins, or (iii) a random terpolymer of propylene with two alpha-olefins selected from the group consisting of ethylene and C4 -C10 alpha olefin, provided that the propylene polymer has a melt flow higher than 30 dg/min as measured by ASTM Method D 1238-82 (230° C./5 kg). Preferably, the polypropylene has a melt flow from 50 to 80 dg/min. The C4 -C10 alpha-olefins include linear and branched C4 -C10 alpha-olefins such as 1-butene, 1-pentene, 4-methyl-pentene-1, 3-methyl-1-butene, 1-hexene, 3-4-dimethyl-1-butene, 1-heptene, 3-methyl-1-hexene, 1-octene and the like.

The elastomeric block copolymers employed in the molding compositions of the present invention have two polystyrene endblocks and one hydrogenated isoprene midblock in a linear arrangement (S-EP-S). The polystyrene endblocks each preferably have a peak molecular weight from 4,500 to 8,000, most preferably from 5,000 to 5,500, which results in formation of weak polystyrene domains and low melt viscosity.

The hydrogenated isoprene blocks have a residual unsaturation less that 5%, preferably less than 2%, and may have from 30% to 100% 1,4-addition of the isoprene. The block copolymers are readily prepared by anionic polymerization and selective hydrogenation processes known in the art to give polymers having low polydispersity.

The polypropylene molding compositions could further contain polyethylene-polypropylene block copolymers as described in U.S. Pat. No. 5,045,589 which is incorporated by reference herein.

Fillers and reinforcing agents, e.g. carbon black and glass fibers, as well as inorganic powders such as calcium carbonate, talc, mica, and glass, may be included in the composition of the invention at concentration levels up to about 80 parts by weight per 100 parts by weight of the total polymer components. In addition to the economic benefit such fillers afford, greater stiffness and a higher heat distortion temperature can be attained.

The components of the composition can be blended or admixed in any conventional mixing apparatus, such as an extruder or a Banbury mixer.

EXAMPLES

The following examples, presented for illustrative purposes, describe various embodiments of the polypropylene molding composition of the invention.

In all of the examples and control experiments, the polypropylene and the S-EP-S block copolymer, as well as any other modifier used in comparison, were mixed and extruded in a single pass through a co-rotating twin-screw extruder. A stabilizer composition (0.08 weight%), known as Irganox 1010, was added to all batches before compounding to minimize oxidation. The extruder temperature was in the 200°-245° C. range. The extruded blends were molded into test specimens.

The test methods used to evaluate the molded specimens were ASTM D-256 (notched Izod impact at room temperature), ASTM D-638 (tensile strength), ASTM D-790 (flexural modulus), and ASTM-648 (Heat Distortion Temperature at 1820 kPa).

EXAMPLES 1-2

Two polypropylene molding compositions of the invention were made and tested as described above. In these compositions the block copolymer was a S-EP-S block copolymer. Two control compositions containing known styrene/butadiene block copolymers also were made and tested in the same manner.

The propylene polymer used in the preparation of the molding compositions was a pelletized polypropylene resin, commercially available from UBE (UBE ZT772), a nominal melt flow rate (ASTM Method D 1238-82, 230° C./5 kg) of 66 dg/min.

The block copolymers are further described in Table I and the polypropylene molding compositions and results of the evaluations performed on the Example 1-2 compositions and the two control compositions are shown in Table II.

                                  TABLE I__________________________________________________________________________        Comparison Example No.                      Example No.        A.sup.(a)               B.sup.(b)                      1      2__________________________________________________________________________Triblock/Diblock in        100% S-EB-S               70% S-EB-S                      100% S-EP-S                             100% S-EP-SBlock Copolymer (wt %)               30% S-EBMolecular Weight (peak)        71,000 82,000 62,000 59,000Triblock/Diblock    41,000Polystyrene (wt %).sup.(c)        30     13     18     19Melt Flow dg/min.sup.(d)        No Flow               20-29  14     29Tensile strength psi        3,100  2,550  3,100  3,125__________________________________________________________________________ .sup.(a) Commercially availableKRATON ® G1650 elastomer from Shell. .sup.(b) Commercially availableKRATON ® G1657 elastomer from Shell. .sup.(c) Measured prior to hydrogenation. .sup.(d) ASTM D1238 (230° C./5 kg).

              TABLE II______________________________________          Comparison          Example No.                    Example No.Polypropylene Comp..sup.(a)            A       B       1     2______________________________________Heat Distortion Temperature            109.0   104.1   105.6 --(°C.)Brittleness Temp. (°C.)            -37.6   -40.8   -45.0 --Izod Impact (Kg-cm/cm2)            15.8    21      38    57Melt Flow dg/min.sup.(b)            40      59      57    60Flex Modulus (Kg/cm2)            12,450  12,070  12,040                                  11,410______________________________________ .sup.(a) Contains 90% high flow polypropylene and 10% block copolymer wit 0.08% Irganox 1010. .sup.(b) ASTM 1238 230° C./5 kg.
Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US5026752 *Aug 28, 1989Jun 25, 1991Minnesota Mining And Manufacturing CompanyAmorphous-polypropylene-based hot melt adhesive
US5045589 *Nov 20, 1989Sep 3, 1991Ube Industries, Ltd.Blend of ethylene-propylene copolymer with thermoplastic elastomer, automobile bumpers
US5060818 *Feb 11, 1991Oct 29, 1991Japan Crown Cork Co., Ltd.Butadiene-styrene copolymer, liquid paraffin, and propylene resin; seals
US5086109 *Nov 28, 1990Feb 4, 1992Ube Industries, Ltd.A blends of ethylene-propylene and hydrogenated block copolymers, inorganic fillers; heat resistance, impact strength, nondeforming
US5256734 *Feb 11, 1992Oct 26, 1993Mitsui Toatsu Chemicals, Inc.Blend with hydrogenated butadiene(or isoprene)-styrene copolymer
US5374677 *Jun 19, 1992Dec 20, 1994Mitsubishi Petrochemical Company LimitedEthylene-propylene copolymer, ethylene copolymer, propylene polymer and talc
EP0308001A2 *Sep 2, 1988Mar 22, 1989Shell Internationale Research Maatschappij B.V.Polymeric composition
JPH0570699A * Title not available
JPH05163394A * Title not available
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Classifications
U.S. Classification525/98
International ClassificationC08L53/00, C08L53/02, C08L23/10
Cooperative ClassificationC08L53/02, C08L23/10
European ClassificationC08L23/10
Legal Events
DateCodeEventDescription
Feb 24, 2011ASAssignment
Owner name: KRATON POLYMERS U.S. LLC, TEXAS
Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:UBS AG, STAMFORD BRANCH;REEL/FRAME:025845/0795
Effective date: 20110211
Mar 26, 2009ASAssignment
Effective date: 20010228
Free format text: CHANGE OF NAME;ASSIGNOR:SHELL OIL COMPANY;REEL/FRAME:022452/0851
Owner name: SHELL ELASTOMERS LLC, TEXAS
Free format text: AFFIDAVIT OF NAME CHANGE;ASSIGNOR:SHELL ELASTOMERS LLC;REEL/FRAME:022452/0984
Owner name: KRATON POLYMERS U.S. LLC, TEXAS
Effective date: 20090323
Jan 2, 2004ASAssignment
Free format text: SECURITY INTEREST;ASSIGNOR:KRATON POLYMERS U.S. LLC;REEL/FRAME:014242/0281
Owner name: UBS AG, STAMFORD BRANCH, CONNECTICUT
Effective date: 20031223
Jul 17, 1995ASAssignment
Owner name: SHELL OIL COMPANY, TEXAS
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:DJIAUW, LIE KHONG;MODIC, MICHAEL JOHN;GELLES, RICHARD;AND OTHERS;REEL/FRAME:007579/0927
Effective date: 19940103