|Publication number||USH1432 H|
|Application number||US 07/873,336|
|Publication date||Apr 4, 1995|
|Filing date||Apr 20, 1992|
|Priority date||Aug 15, 1988|
|Publication number||07873336, 873336, US H1432 H, US H1432H, US-H-H1432, USH1432 H, USH1432H|
|Inventors||Richard E. Skochdopole|
|Original Assignee||The Dow Chemical Company|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (8), Classifications (9)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This is a continuation of U.S. patent application Ser. No. 655,241, filed Feb. 12, 1991, now abandoned, which is a continuation of Ser. No. 232,256, filed Aug. 15, 1988, now abandoned.
The present invention relates generally to modified polycarbonate compositions with improved impact and environmental stress crack resistance properties. More particularly, the present invention relates to blends of aromatic polycarbonates and high molecular weight hydrogenated styrene-butadiene-styrene triblock copolymers.
Aromatic polycarbonates are well known commercially available materials having a variety of applications in the plastics art. Generally speaking, these resins offer high resistance to attack by mineral acids, have high tensile strength and high impact strength, except in thick sections, good thermal resistance and a dimensional stability far surpassing that of most other thermoplastic materials.
The use of aromatic polycarbonate resins in certain applications is limited, however, because they have a high viscosity in the melt, making molding of complex large and especially formed parts difficult. They also exhibit brittleness under sharp impact conditions in thick section and, regardless of thickness, when small amounts of reinforcements such as glass, or pigments such as titanium dioxide, are added for conventional purposes. In addition, polycarbonate resins exhibit severe environmental stress cracking. The term "environmental stress cracking" refers to the type of premature failure under stress which is hastened by the presence of organic solvents, e.g., acetone, heptane and toluene, when such solvents are in contact with stressed articles fabricated from aromatic polycarbonate resins. Such contact may occur, for example, when solvents are used to clean or degrease stressed parts fabricated from polycarbonates, or when such parts are used around gasoline engines in automotive and recreational applications.
As a result, polycarbonate polymers have been modified by or blended with additional polymers to achieve materials with the desired combination of properties. For example, in U.S. Pat. No. 4,088,711 polycarbonates are combined with block copolymers of a monoalkenyl arene polymer and a completely hydrogenated conjugated diene to form a continuous interlocking network, with the block copolymer acting as a mechanical structural stabilizer. The compositions described in U.S. Pat. Nos. 4,537,930, 4,267,096 and 4,122,131 are blends of polycarbonates and small amounts of vinyl aromatic and olefin elastomer copolymers having improved environmental stress crack resistance. U.S. Pat. No. 4,628,072 describes the improvement of physical properties such as adhesion, impact resistance, weatherability and heat resistance by the addition of block copolymers of a monovinyl substituted aromatic hydrocarbon polymer and unsaturated olefin compound polymer to various thermoplastic polymers. See also U.S. Pat. No. 4,579,903 directed to copolyester carbonate resin compositions incorporating copolymers of vinyl aromatic compounds and olefinic elastomers which provide improved solvent resistance and impact properties.
The present invention is directed toward novel polycarbonate compositions having markedly improved environmental stress crack resistance as well as improved impact resistance properties.
The present invention comprises a blend of an aromatic polycarbonate polymer and a block copolymer comprising an alkenyl arene polymer and a hydrogenated diene elastomer. Preferably the aromatic polycarbonate is a biphenol-based polycarbonate such as bisphenol A, and the block copolymer is a hydrogenated styrene-butadiene-styrene triblock copolymer of a molecular weight greater than about 130,000 and present in amounts greater than about 5% to less than about 15% of the composition by weight. All percentages given herein are by weight unless otherwise indicated. Compositions of the present invention exhibit markedly increased environmental stress crack resistance and improvements in impact resistance properties.
The present invention comprises a blend of an aromatic polycarbonate polymer and a block copolymer comprising an alkenyl arene polymer and a hydrogenated diene elastomer. The block copolymer is of relatively high molecular weight and is present in an amount effective to improve the environmental stress crack resistance of the polycarbonate blend. The amount of copolymer present in the blend is preferably such that substantial improvement of environmental stress crack resistance relative to unmodified polycarbonate is obtained. By "substantial improvement" is meant at least about a 100% increase in the time to fail at a constant stress of 1500 psi in 75% by volume isooctane and 25% by volume toluene relative to unmodified polycarbonate.
Aromatic polycarbonates suitable for compositions of the present invention include, for example, polymers derived from diphenols such as bisphenol A, 1,1(4 hydroxyphenol)ketone, bis-(4-hydroxyphenyl)methane, 1,1-bis-(hydroxyphenyl)-ethane, phenolphthalein, and 1,1 bis(hydroxyphenol) sulfone; and aromatic polycarbonates with alkyl or halogen substituents on the phenyl ring. Preferably, the polycarbonate component of a blend of the present invention is a bisphenol A-based polycarbonate with a melt flow of from about 3 to about 80 g/10 min run at 300° C. and 3.8 kg wt (ASTM) condition O, and more preferably with a melt flow of from about 4.6 to about 15 g/10 min condition O.
Suitable block copolymers for blends of the present invention are alkenyl arene-hydrogenated diene triblock copolymer of a relatively high molecular weight. Suitable structural arrangements of block copolymers useful in compositions of the present invention include linear triblock copolymers or, alternatively, for example, star block copolymers. More preferred are alkenyl arene-diene-alkenyl arene linear triblock copolymers. Most preferred are hydrogenated styrene-butadiene-styrene linear triblock elastomers. Block copolymers suitable for compositions of the present invention are also those of a relatively high molecular weight. Suitable copolymers include those of a molecular weight of greater than about 70,000, and more preferably, greater than about 130,000. Most preferred are block copolymers of a molecular weight of about 175,000.
Suitable compositions ranges of the block copolymer in a blend of the present invention include greater than from about 5% block copolymer, more preferably from greater than about 5% to less than about 15%, and still more preferably from about 8% to about 12% block copolymer. Most preferably, the block copolymer comprises about 10% of a blend of the present invention. Although the block copolymer must be present in an amount to impart improved environmental stress crack resistance properties to the blend, too high an amount of block copolymer may adversely affect the molding properties of the blend. By "adversely affects" is meant that the blend shows gross nonhomogeneity upon molding, giving a very poor surface and a layered structure that shows some poor physical properties. Thus, although preferred ranges are given, they should not be construed as limiting and should be selected to maximize the environmental stress cracking resistance without adversely affecting molding properties and fabrication. It should also be appreciated that, as more fully described below in Specific Examples IX and X, at the preferred concentrations the block copolymer does not form an interconnecting network in the blend.
Compositions of the present invention comprising an aromatic polycarbonate and block copolymer can also include additional resins, preferably in amounts of less than about 50% of the final blend. Suitable additional resins for compositions of the present invention include engineering resins such as acrylonitrile-butadiene-styrene copolymer (ABS), polybutylene terephthalate (PBT), polyethylene terephthalate (PET), nylon and polyacetal resins.
The components of the subject composition can be blended by any technique which effects intimate intermixing of components without significant mechanical or thermal degradation of the polymer components. For example, the components can be dissolved or dispersed in a compatible diluent, blended together to produce a homogenous dispersion or solution and the diluent removed.
One particularly convenient method for preparing blends of the present invention is to first dry blend particulates of each respective component. This dry blend is directly fed into a heat fabricating apparatus such as a screw extruder or a reciprocating screw injection molding machine with sufficient mixing. While the particular manner of mixing these components in heat plasticized form is not critical, sufficient mixing should be employed to ensure a uniform distribution of each of the components throughout the resulting blend. In addition to the foregoing mixing procedures, other conventional mixing procedures may be employed including hot roll milling, kneading and the like. The preferred method of blending the polymer components of the present invention is by extrusion at a temperature and shear rate which will effect intimate mixing without significant polymer degradation.
Any of the various types of extrusion devices capable of bringing polymeric components into the melted state and providing a continuous or intermittent flow of the composition through the die may be employed to prepare a composition of the invention. Such devices can include single screw, double screw, or multiple screw extruders having either a planetary screw or plate or both for transformation of the mixtures into finished or semifinished products.
A preferred composition of the present invention comprises a blend of a bisphenol A-based polycarbonate and a hydrogenated styrene-butadiene-styrene linear block copolymer. The polycarbonate is of the general structure ##STR1## where n is preferably selected to provide the polycarbonate with a weight average molecular weight of about 31,000. The block copolymer is preferably of a molecular weight of about 175,000, where the styrene unit molecular weights are about 25,000 and the butadiene unit molecular weights are about 125,000.
Suitable amounts of styrene-butadiene-styrene block copolymer in preferred compositions of the invention includes greater than about 5% block copolymer, more preferably from greater than about 5% to less than about 15% block copolymer, and still more preferably from about 8% to 12% block polymer. Most preferred is a blend of about 10% hydrogenated styrene-butadiene-styrene triblock copolymer and about 90% bisphenol A polycarbonate.
Compositions of the present invention exhibit a dramatic increase in environmental stress crack resistance toward organic solvents and improved impact resistance. Such improved solvent and impact resistance is documented by the data summarized in the specific examples which follow.
A polymer composition of 85 parts polycarbonate with 4.6 melt flow rate and 15 parts of a hydrogenated styrene-butadiene-styrene triblock polymer of a molecular weight of approximately 175,000, commercially available from Shell Chemical Company as Kraton® G1651, was compounded on a Werner & Pfleiderer ZSK30 twin screw extruder through a strand die, water bath and chopper. These granules were then injection molded on a Newbury 30-ton injection molder.
Prior to compounding, the polycarbonate was dried at least four hours at 121° C. and Kraton® G1651 was dried at least 16 hours at 61° C., both in circulated air ovens. The resins were then dry-blended in a Hobart planetary mixer for at least one minute prior to loading into the compounding hopper. The extruder was run at about 30 lb/hr rate with heating zones set from 260° to 280° C.
This composition was again dried for over four hours at 121° C. prior to molding on the Newbury Injection Molder. The injection molding heaters were set at 600° to 625° F. and the molding pressure was 3000 psi. The mold temperature was set at 150° F. Problems with poor surface were encountered during the entire molding trial and the sample also delaminated upon tensile testing, indicating that this composition was too high in Kraton® G1651 for good molding properties.
The following compositions were prepared by a similar procedure outlined in Example I.
______________________________________Example Polycarbonate Elastomer______________________________________II 90% 10% Kraton ® G1651III 95% 5% Kraton ® G1651IV 90% 10% Acryloid ® KM330V 100% 0%______________________________________
Injection molded bars of each of the above compositions were exposed to a synthetic gasoline mixture of 75% by volume isooctane and 25% by volume toluene at various stress levels and the time observed at which the sample failed by rupture.
______________________________________Time to Fail in Minutes at Designated Stress LevelExample 3000 psi 2500 psi 2000 psi 1500 psi 1000 psi______________________________________II 53 95 400 566 5,333III 8 11 18 84 1,000IV 13 25 42 90 900V 4 7 26 166 --______________________________________
These data show that although 5% Kraton® G1651 shows no improvement in environmental stress crack resistance performance, 10% Kraton® G1651 is much improved compared to pure polycarbonate. The data of Example IV also indicates that another very commonly used elastomer for impact toughening, a methyl methacrylate shell/butylacrylate core multipolymer commercially available from Rohm & Haas Company as Acryloid® KM330, does not improve the environmental stress crack resistance performance of polycarbonate.
Polymer samples with the following compositions were prepared and molded in a manner similar to Example I. In this case, good surfaces were obtained with all samples. The toughness qualities of these materials were evaluated by measuring the Notched Izod Impact (ASTM D256) at different notch sizes, temperatures, and after elevated temperature aging. The results were as follows:
______________________________________ Notched 131° C. Aging Izod, RT 0° F. 10 mil NIExample Composition 10 mil 5 mil 10 mil 24 hr 20 hr______________________________________VI 5% Kraton ® 16.8 14.2 15.8 14.4 13.0 G1651VII 5% Kraton ® 13.8 10.8 7.1 3.7 3.3 G1650aVIII 5% Kraton ® 13.2 10.8 11.8 6.0 -- G1652b______________________________________ a Kraton ® G1650 is a hydrogenated styrenebutadiene triblock polymer of a molecular weight of about 70,000, available commercially fro Shell Chemical Company. b Kraton ® G1652 is a hydrogenated styrenebutadiene triblock polymer of a molecular weight of about 50,000, available commercially fro Shell Chemical Company.
As seen from the above data, the impact properties of the higher molecular weight Kraton® G1651 was clearly superior to the other two lower molecular weight Kraton® G materials.
Transmission electron micrographs were taken in directions perpendicular and parallel to flow in an injection molded test bar of 90% polycarbonate and 10% Kraton® G1651.
The Kraton® light colored domains do not interconnect in any direction to form and interlocking network, but instead remain discretely dispersed in the blend.
It should be appreciated that a latitude of modification, change and substitution is intended in the foregoing disclosure and, accordingly, it is appropriate that the appended claims be construed broadly and in a manner consistent with the spirit and scope of the invention herein.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US4088711 *||May 5, 1977||May 9, 1978||Shell Oil Company||Polycarbonate/block copolymer blend|
|US4122131 *||Sep 14, 1977||Oct 24, 1978||General Electric Company||Polyblend composition comprising aromatic polycarbonate, polyolefin, selectively hydrogenated block copolymer and olefinic copolymer|
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|US4424303 *||Feb 25, 1982||Jan 3, 1984||General Electric Company||Composition of an aromatic carbonate polymer, a styrene-butadiene styrene radial black copolymer and an acrylate copolymer|
|US4537930 *||Dec 29, 1982||Aug 27, 1985||General Electric Company||Composition of a polycarbonate resin and a selectively hydrogenated copolymer of a vinyl aromatic compound and an olefinic elastomer|
|US4579903 *||Dec 19, 1984||Apr 1, 1986||General Electric Company||Copolyester-carbonate composition|
|US4628072 *||Aug 13, 1982||Dec 9, 1986||Asahi Kasei Kogyo Kabushiki Kaisha||Modified block copolymer composition|
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|International Classification||C08L53/02, C08L69/00|
|Cooperative Classification||C08L69/00, C08L53/025, C08L69/005|
|European Classification||C08L53/02B, C08L69/00B, C08L69/00|