Background of the Art [0002] The preparation of block copolymers of mono alkenyl arenes and conjugated dienes is well known. One of the first patents on linear ABA block copolymers made with styrene and butadiene is U. S. Pat. 3,149, 182. Over the last forty plus years a large number of new styrene diene polymers have been developed. Now a novel anionic block copolymer based on mono alkenyl arene end blocks and controlled distribution mid blocks of mono alkenyl arenes and conjugated dienes has been discovered and is described in copending, commonly assigned U. S. patent application Serial Number 60/355,210, entitled "NOVEL BLOCK COPOLYMERS AND METHOD FOR MAKING SAME", and its continuing applications. Methods for making such polymers are described in detail in the above-mentioned patent application.

[0003] What has now been found is that blends or compounds of these novel block copolymers with processing oils and other polymers have surprising property advantages, and show promising utility in a variety of end-use applications, including injection molding, extruded goods and polymer modification.

Summary of the Invention [0004] In one aspect of the present invention we have discovered that a novel composition comprising at least one block copolymer having a controlled distribution block of a mono alkenyl arene and conjugated diene, and optionally including another component, has superior properties for many applications. We have also discovered that these compositions can be used in various forming processes, and that they also have a number of advantages in processing.

[0005] Accordingly, the broad aspect of the present invention is an article comprising at least one block copolymer and, optionally, at least one other component selected from the group consisting of olefin polymers, styrene polymers, tackifying resins, polymer extending oils and engineering thermoplastic resins, wherein said block copolymer has at least one A block and at least one B block, and wherein (a.) each A block is a mono alkenyl arene homopolymer block and each B block is a controlled distribution copolymer block of at least one conjugated diene and at least one mono alkenyl arene; (b. ) each A block having an average molecular weight between 3,000 and 60,000 and each B block having an average molecular weight between 30,000 and 300,000 ; (c. ) each B block comprises terminal regions adjacent to the A blocks that are rich in conjugated diene uni « s and one or more regions not adjacent to the A blocks that"are-rich in mono alkenyl arene units; (d. ) the total amount of mono alkenyl arene in the block copolymer is 20 to 80 percent weight; and (e. ) the weight percent of mono alkenyl arene in the B block is between 10 and 75 percent.

[0006] In another aspect of the present invention we have shown that the article can be formed in a wide variety of processes,

including injection molding, compression molding, over molding, dipping, extrusion, roto molding, slush molding, fiber spinning, blow molding, polymer modification, cast film making, blown film making and foaming.

[0007] In yet another aspect of the present invention, the article can be processed into the form of a film, sheet, multi layer laminate, coating, band, strip, profile, molding, foam, tape, fabric, thread, filament, ribbon, fiber, plurality of fibers, or fibrous web.

[0008] As for advantages of the present invention, it has long been desired to have a polymer with high polystyrene content that is still elastomeric. The invention described herein consists of styrenic block copolymers with polystyrene contents ranging from 35%-80% with elastomeric properties.

Elastomeric performance is indicated by the absence of a distinct yield point as well as recovery upon release of an applied load. One feature of such a polymer is a high rubber modulus in conjunction with a relatively low Young's modulus.

For example, a polymer can be produced with a very stiff rubber response that is still relatively soft. This is unique in comparison with the prior art polymers because the controlled distribution gives the polymers of the present invention improved elasticity, softness, and clarity. Another feature of such a polymer is that it has a tendency not to degrade conjoined adhesives. This is due to a lower solubility of oils and tackifying resins in the polymer itself giving a lower tendency to partition such compounding ingredients out of adjacent adhesives. This attribute combined with high stiffness, high flow, and good elasticity make this polymer useful for personal hygiene applications. It has also been desired to have a polymer which can be blended with large amounts of polystyrene and remain elastomeric for low cost

elastomeric compounding solutions. Compounds containing up to 50% polystyrene exhibit high rubber stiffness and elastomeric behavior. Another feature of such a polymer is a lower hardness than prior art, which combined with improved rubber stiffness, makes this polymer useful for molded and extruded goods as well as for over molding. Still another feature of such a polymer is the ability to tune the rubber Tg depending on the amount of styrene incorporated in the rubber mid block.

This attribute could be useful in sound and vibration dampening applications where energy dissipation must be tunable to the frequency of the sound or vibration. A polymer with a high rubber Tg is also useful for certain packaging applications like shrink-wrap film or candy wrap film. One of the benefits to having an elastomer with at least 75% polystyrene content is that the elastomer will carry FDA approval of a"plastic"so it will be approved for direct food contact including fatty foods. This factor, along with low °2 and CO2 permeability will make the polymer useful for food wrap film as well.

[0009] The controlled distribution copolymers of the present invention offer additional advantages in their ability to be easily processed using equipment generally designed for processing thermoplastic polystyrene, which is one of the most widely known and used alkenyl arene polymers. Melt processing can be accomplished via extrusion or injection molding using either single screw or twin screw techniques that are common to the thermoplastics industry. Solution or spin casting techniques can also be used as appropriate.

[0010] Finally, the copolymers of the present invention can be compounded with other components not adversely affecting the copolymer properties. Exemplary materials that could be used as additional components would include, without limitation,

pigments, antioxidants, stabilizers, surfactants, waxes, and flow promoters. The polymers of the present invention are useful in a wide variety of applications including, for example, molded and extruded goods such as toys, grips, handles, shoe soles, tubing, sporting goods, sealants, gaskets, and oil gels. The compositions also find use as rubber toughening agents for polyolefins, polyvinyl chloride, polystyrene, polyamide, polyurethane, polyester, polycarbonate and epoxy resins. The polymers of the present invention are also useful in alloys and blends, and as compatibilizers for a variety of polymers and other materials.

Detailed Description of the Preferred Embodiments [0011] The key component of the present invention is the novel block copolymer containing mono alkenyl arene end blocks and a unique midblock of a mono alkenyl arene and a conjugated diene. Surprisingly, the combination of (1) a unique control for the monomer addition and (2) the use of diethyl ether or other modifiers as a component of the solvent (which will be referred to as"distribution agents") results in a characteristic distribution of the two monomers (herein termed a"controlled distribution"polymerization, i. e. , a polymerization resulting in a"controlled distribution" structure), and also results in the presence of certain mono alkenyl arene rich regions and certain conjugated diene rich regions in the polymer block. For purposes hereof,"controlled distribution"is defined as referring to a molecular structure having the following attributes: (1) terminal regions adjacent to the mono alkenyl arene homopolymer ("A") blocks that are rich in (i. e. , having a greater than average amount of) conjugated diene units; (2) one or more regions not adjacent to the A blocks that are rich in (i. e. having a greater than average amount of) mono alkenyl arene units; and (3) an

overall structure having relatively low blockiness. For purposes thereof, "rich in"is defined as greater than the average amount, preferably greater than 5% the average amount.

. This relatively low blockiness can be shown by either the presence of only a single ("Tg, ") for said controlled distribution polymer block intermediate between the Tg's of either monomer alone, when analyzed using differential scanning calorimetry ("DSC") thermal methods or via mechanical methods, or as shown via proton nuclear magnetic resonance ("H-NMR") methods. The potential for blockiness can also be inferred from measurement of the UV-visible absorbance in a wavelength range suitable for the detection of polystyryllithium end groups during the polymerization of the B block. A sharp and substantial increase in this value is indicative of a substantial increase in polystyryllithium chain ends. In this process, this will only occur if the conjugated diene concentration drops below the critical level to maintain controlled distribution polymerization. Any styrene monomer that is present at this point will add in a blocky fashion. The term"styrene blockiness", as measured by those skilled in the art using proton NMR, is defined to be the proportion of S units in the polymer having two S nearest neighbors on the polymer chain. The styrene blockiness is determined after using H-1 NMR to measure two experimental quantities as follows: First, the total number of styrene units (i. e. arbitrary instrument units which cancel out when ratioed) is determined by integrating the total styrene aromatic signal in the H-1 NMR spectrum from 7.5 to 6.2ppm and dividing this quantity by 5 to account for the 5 aromatic hydrogens on each styrene aromatic ring.

Second, the blocky styrene units are determined by integrating that portion of the aromatic signal in the H-1 NMR spectrum

from the signal minimum between 6.88 and 6.80 to 6.2ppm and dividing this quantity by 2 to account for the 2 ortho hydrogens on each blocky styrene aromatic ring. The assignment of this signal to the two ortho hydrogens on the rings of those styrene units which have two styrene nearest neighbors was reported in F. A. Bovey, High Resolution NMR of Macromolecules (Academic Press, New York and London, 1972), chapter 6.

The styrene blockiness is simply the percentage of blocky styrene to total styrene units: Blocky % = 100 times (Blocky Styrene Units/Total Styrene Units) Expressed thus, Polymer-Bd-S- (S) n-S-Bd-Polymer, where n is greater than zero is defined to be blocky styrene. For example, if n equals 8 in the example above, then the blockiness index would be 80%. It is preferred that the blockiness index be less than 40. For some polymers, having styrene contents of ten weight percent to forty weight percent, it is preferred that the blockiness index be less than 10.

[0012] This controlled distribution structure is very important in managing the strength and Tg of the resulting copolymer, because the controlled distribution structure ensures that there is virtually no phase separation of the two monomers, i. e. , in contrast with block copolymers in which the monomers actually remain as separate"microphases", with distinct Tg's, but are actually chemically bonded together. This controlled distribution structure assures that only one Tg is present and that, therefore, the thermal performance of the resulting copolymer is predictable and, in fact, predeterminable.

Furthermore, when a copolymer having such a controlled distribution structure is then used as one block in a di-

block, tri-block or multi-block copolymer, the relatively higher Tg made possible by means of the presence of an appropriately constituted controlled distribution copolymer region will tend to improve flow and processability.

Modification of certain other properties is also achievable.

[0013] Starting materials for preparing the novel controlled distribution copolymers of the present invention include the initial monomers. The alkenyl arene can be selected from styrene, alpha-methylstyrene, para-methylstyrene, vinyl toluene, vinylnaphthalene, and para-butyl styrene or mixtures thereof. Of these, styrene is most preferred and is commercially available, and relatively inexpensive, from a variety of manufacturers. The conjugated dienes for use herein are 1,3-butadiene and substituted butadienes such as isoprene, piperylene, 2, 3-dimethyl-1, 3-butadiene, and 1-phenyl-1, 3- butadiene, or mixtures thereof. Of these, 1,3-butadiene is most preferred. As used herein, and in the claims,"butadiene" refers specifically to"1,3-butadiene".

[0014] As discussed above, the controlled distribution polymer block has diene rich region (s) adjacent to the A block and an arene rich region not adjacent to the A block, and typically near the center of the block. Typically the region adjacent to the A block comprises the first 15 to 25% of the block and comprises the diene rich region (s), with the remainder considered to be arene rich. The term"diene rich"means that the region has a measurably higher ratio of diene to arene than the arene rich region. Another way to express this is the proportion of mono alkenyl arene units increases gradually along the polymer chain to a maximum near the middle or center of the block (if we are describing an ABA structure) and then decreases gradually until the polymer block is fully polymerized. This structure is distinct and different from the

tapered and/or random structures discussed in the prior art.

[0015] For the controlled distribution block B the weight percent of mono alkenyl arene in each B block is between 10 and 75 percent, preferably from 20 to 75 percent. For the overall total polymer the weight percent mono alkenyl arene is from 20 to 80 percent, preferably from 35 to 80 percent.

[0016] As used herein, "thermoplastic block copolymer"is defined as a block copolymer having at least one block of a mono alkenyl arene, such as styrene and at least one block of a controlled distribution copolymer of diene and mono alkenyl arene. The method to prepare this thermoplastic block copolymer is via any of the methods generally known for block polymerizations. Reference is made to copending patent application Serial Number 60/355,210 and its continuing application for details on the preparation of the block copolymers used in this application. The present invention includes as an embodiment a thermoplastic copolymer composition, which may be either a di-block, tri-block copolymer or multi-block composition. In the case of the di- block copolymer composition, one block is the alkenyl arene- based homopolymer block and polymerized therewith is a second block of a controlled distribution copolymer of diene and alkenyl arene. In the case of the tri-block composition, it comprises, as end-blocks the glassy alkenyl arene-based homopolymer and as a mid-block the controlled distribution copolymer of diene and alkenyl arene. Where a tri-block copolymer composition is prepared, the controlled distribution diene/alkenyl arene copolymer can be herein designated as"B" and the alkenyl arene-based homopolymer designated as"A". The A-B-A, tri-block compositions can be made by either sequential polymerization or coupling. In the sequential solution polymerization technique, the mono alkenyl arene is first

introduced to produce the relatively hard aromatic block, followed by introduction of the controlled distribution diene/alkenyl arene mixture to form the mid block, and then followed by introduction of the mono alkenyl arene to form the terminal block. In addition to the linear, A-B-A configuration, the blocks can be structured to form a radial (branched) polymer, (A-B) nX or (A-B-A) nX, or various types of structures can be combined in a mixture. For example, when employing a silane, such as tetra ethoxy-silane as a coupling agent, the resulting polymer is typically a mixture of linear coupled product, i. e. (A-B) 2X, and 10 to 30% weight of the three arm radial polymer, i. e. (A-B) 3X. Some A-B diblock polymer can be present but preferably at least 70 weight percent of the block copolymer is A-B-A or radial (or otherwise branched so as to have 2 or more terminal resinous blocks per molecule) so as to impart strength.

[0017] It is also important to control the molecular weight of the various blocks. For an AB diblock, desired block weights are 3,000 to 60,000 for the mono alkenyl arene A block, and 30,000 to 300,000 for the controlled distribution conjugated diene/mono alkenyl arene B block. Preferred ranges are 5000 to 45,000 for the A block and 50,000 to 250,000 for the B block.

For the triblock, which may be a sequential ABA or coupled (AB) 2 X block copolymer, the A blocks should be 3,000 to 60,000, preferably 5000 to 45,000, while the B block for the sequential block should be 30,000 to 300,000, and the B blocks (two) for the coupled polymer half that amount. The total average molecular weight for the triblock copolymer should be from 40,000 to 500,000, and for the radial copolymer from 60,000 to 600,000. These molecular weights are most accurately determined by light scattering measurements, and are expressed as number average molecular weights.

[0018] An important aspect of the present invention is to control the microstructure or vinyl content of the conjugated diene in the controlled distribution copolymer block. The term "vinyl content"refers to the fact that a conjugated diene is polymerized via 1,2-addition (in the case of butadiene-it would be 3,4-addition in the case of isoprene). Although a pure"vinyl"group is formed only in the case of 1,2-addition polymerization of 1,3-butadiene, the effects of 3,4-addition polymerization of isoprene (and similar addition for other conjugated dienes) on the final properties of the block copolymer will be similar. The term"vinyl"refers to the presence of a pendant vinyl group on the polymer chain. When referring to the use of butadiene as the conjugated diene, it is preferred that 20 to 80 mol percent of the condensed butadiene units in the copolymer block have 1,2 vinyl configuration as determined by proton NMR analysis. For the unsaturated block copolymerized in this application, preferably 20 to 40 mol percent of the condensed butadiene units should have 1,2-vinyl configuration. This is effectively controlled by varying the relative amount of the distribution agent. As will be appreciated, the distribution agent serves two purposes-it creates the controlled distribution of the mono alkenyl arene and conjugated diene, and also controls the microstructure of the conjugated diene. Suitable ratios of distribution agent to lithium are disclosed and taught in US Pat. Re 27,145, which disclosure is incorporated by reference.

[0019] An important feature of the thermoplastic elastomeric di- block and tri-block polymers of the present invention, including one or more controlled distribution diene/alkenyl arene copolymer blocks and one or more mono alkenyl arene blocks, is that they have at least two Tg's, the lower being the single Tg of the controlled distribution copolymer block which is an intermediate of its constituent monomers'Tg's.

Such Tg is preferably at least-60°C, more preferably from-40 degrees C to + 30°C. The second Tg, that of the mono alkenyl arene"glassy"block, is preferably more than +70°C, more preferably from +75 to +110°C. The presence of the two Tg's, illustrative of the microphase separation of the blocks, contributes to the notable elasticity and strength of the material in a wide variety of applications, and its ease of processing and desirable melt-flow characteristics.

[0020] One of the surprising compositions of the present invention is the combination of the block copolymer and a polymer extending oil. While in the absence of oil, these polymers exhibit a stiffer elastomeric behavior than a traditional triblock polymer, in the presence of oil they exhibit a softer elastomeric behavior. Especially preferred are the types of oil that are compatible with the elastomeric segment of the block copolymer. While oils of higher aromatics content are satisfactory, those petroleum-based white oils having low volatility and less than 50% aromatic content are preferred. Typical paraffinic processing oils can be used to soften and extend polymers of the present invention; however, processing oils with a higher naphthenic content are more compatible with the controlled distribution rubber block.

Processing oils with a naphthenic content between 40% and 55% and an aromatic content less than 10% are preferred. The oils should additionally have low volatility, preferable having an initial boiling point above 260°C (500°F). The amount of oil employed varies from 0 to 300 parts by weight per hundred parts by weight rubber, or block copolymer, preferably from 20 to 150 parts by weight.

[0021] The block copolymers of the present invention may be blended with a large variety of other polymers, including

olefin polymers, styrene polymers, tackifying resins, and engineering thermoplastic resins.

[0022] In addition, the controlled distribution polymers of the present invention may be blended with conventional styrene/diene and hydrogenated styrene/diene block copolymers, such as the block copolymers available from KRATON Polymers.

These block copolymers include linear S-B-S, S-I-S, S-EB-S, S- EP-S block copolymers. Also included are radial block copolymers based on styrene along with isoprene and/or butadiene and selectively hydrogenated radial block copolymers.

[0023] Olefin polymers include, for example, ethylene homopolymers, ethylene/alpha-olefin copolymers, propylene homopolymers, propylene/alpha-olefin copolymers, high impact polypropylene, butylene homopolymers, butylene/alpha olefin copolymers, and other alpha olefin copolymers or interpolymers. Representative polyolefins include, for example, but are not limited to, substantially linear ethylene polymers, homogeneously branched linear ethylene polymers, heterogeneously branched linear ethylene polymers, including linear low density polyethylene (LLDPE), ultra or very low density polyethylene (ULDPE or VLDPE), medium density polyethylene (MDPE), high density polyethylene (HDPE) and high pressure low density polyethylene (LDPE). Other polymers included hereunder are ethylene/acrylic acid (EEA) copolymers, ethylene/methacrylic acid (EMAA) ionomers, ethylene/vinyl acetate (EVA) copolymers, ethylene/vinyl alcohol (EVOH) copolymers, ethylene/cyclic olefin copolymers, polypropylene homopolymers and copolymers, propylene/styrene copolymers, ethylene/propylene copolymers, polybutylene, ethylene carbon monoxide interpolymers (for example, ethylene/carbon monoxide (ECO) copolymer, ethylene/acrylic acid/carbon monoxide

terpolymer and the like. Still other polymers included hereunder are polyvinyl chloride (PVC) and blends of PVC with other materials.

[0024] Styrene polymers include, for example, crystal polystyrene, high impact polystyrene, medium impact polystyrene, styrene/acrylonitrile copolymers, styrene/acrylonitrile/butadiene (ABS) polymers, syndiotactic polystyrene, styrene/methyl-methacrylate copolymers and styrene/olefin copolymers. Representative styrene/olefin copolymers are substantially random ethylene/styrene copolymers, preferably containing at least 10, more preferably equal to or greater than 25 weight percent copolymerized styrene monomer. Also included are styrene-grafted polypropylene polymers, such as those offered under the tradename Interloy0 polymers, originally developed by Himont, Inc. (now Basell).

[0025] For the purposes of the specification and claims, the term"engineering thermoplastic resin"encompasses the various polymers found in the classes listed in Table A below, and further defined in US Patent No. 4,107, 131, the disclosure of which is hereby incorporated by reference.

Table A 1. Thermoplastic Polyester 2. Thermoplastic Polyurethane 3. Poly (aryl ether) and Poly (aryl sulfone) 4. Polycarbonate 5. Acetal resin 6. Polyamide 7. Halogenated thermoplastic 8. Nitrile barrier resin 9. Poly (methyl methacrylate) 10. Cyclic olefin copolymers

[0026] Tackifying resins include polystyrene block compatible resins and midblock compatible resins. The polystyrene block compatible resin may be selected from the group of coumarone- indene resin, polyindene resin, poly (methyl indene) resin, polystyrene resin, vinyltoluene-alphamethylstyrene resin, alphamethylstyrene resin and polyphenylene ether, in particular poly (2, 6-dimethyl-1, 4-phenylene ether). Such resins are e. g. sold under the trademarks"HERCURES","ENDEX", "KRISTALEX","NEVCHEM"and"PICCOTEX". Resins compatible with the (mid) block may be selected from the group consisting of compatible C5 hydrocarbon resins, hydrogenated C5 hydrocarbon resins, styrenated CS resins, C5/Cg resins, styrenated terpene resins, fully hydrogenated or partially hydrogenated Cg hydrocarbon resins, rosins esters, rosins derivatives and mixtures thereof. These resins are e. g. sold under the trademarks"REGALITE","REGALREZ","ESCOREZ"and"ARKON".

[0027] The polymer blends of the present invention may be compounded further with other polymers, oils, fillers, reinforcements, antioxidants, stabilizers, fire retardants,

antiblocking agents, lubricants and other rubber and plastic compounding ingredients without departing from the scope of this invention.

[0028] Examples of various fillers that can be employed are found in the 1971-1972 Modern Plastics Encyclopedia, pages 240-247. A reinforcement may be defined simply as the material that is added to a resinous matrix to improve the strength of the polymer. Most of these reinforcing materials are inorganic or organic products of high molecular weight. Various examples include glass fibers, asbestos, boron fibers, carbon and graphite fibers, whiskers, quartz and silica fibers, ceramic fibers, metal fibers, natural organic fibers, and synthetic organic fibers. Especially preferred are reinforced polymer blends of the instant invention containing 2 to 80 percent by weight glass fibers, based on the total weight of the resulting reinforced blend. Coupling agents, such as various silanes, may be employed in the preparation of the reinforced blends.

[0029] Regarding the relative amounts of the various ingredients, this will depend in part upon the particular end use and on the particular block copolymer that is selected for the particular end use. Table B below shows some notional compositions expressed in percent weight, which are included in the present invention. For the"Polymer"amount, a portion may include conventional styrene block copolymers: Table B: Applications, Compositions and Ranges Application Ingredients Composition Films, Molding, Polymer 1-99% Alloys Ethylene copolymers : 99-1% EVA, Ethylene/styrene Personal Hygiene Polymer 10-75% Films and Fibers PE 0-30% PP 0-30% Tackifying Resin 5-30% End Block Resin 5-20% Personal Hygiene Polymer 50-90% Films and Fibers PE 5-30% Tackifying Resin 0-40% Personal Hygiene Polymer 45-90% Films and Fibers PS 10-50% Oil 0-30% Injection Molded Polymer 25-100% articles Polyolefin 0-50% PS 0-50% Oil 0-50% Injection Polymer 55-90% molded/extrusion PPO 0-50% PS 0-50% Engineering Plastic 0-50% Filler 0-50% Oil 0-50% Cap Seals Polymer 25-90% Oil and/or Tackifying 0-50% Resin 0-50% PP 0-25% Filler 0 to 3% Lubricant Engineering Polymer or Maleated 5-30% Thermoplastic Polymer 70-95% toughening Engineering thermoplastic, e. g. Nylon 6,6, TPU Dipped Goods Polymer 60-100% Plasticizer, oil 0-40% Polymer Polymer 5-95% Modification ABS, PS, HIPS, Cyclic 95-5% olefin copolymers

[0030] The polymer of the present invention may be used in a large number of applications, either as a neat polymer or in a compound. The following various end uses and/or processes are

meant to be illustrative, and not limiting to the present invention: 'Polymer modification applications Injection molding of toys, medical devices Extruding films, tubing, profiles Over molding applications for personal care, grips, soft touch applications, for automotive parts, such as airbags, steering wheels, etc Dipped goods, such as gloves Thermoset applications, such as in sheet molding compounds or bulk molding compounds for trays rot molding for toys and other articles Slush molding of automotive skins Thermal spraying for coatings Blown film for medical devices Transparent tubing for medical purposes having improved kink resistance Blow molding for automotive/industrial parts Films and fibers for personal hygiene applications Examples [0031] The following examples are provided to illustrate the present invention. The examples are not intended to limit the scope of the present invention and they should not be so interpreted. Amounts are in weight parts or weight percentages unless otherwise indicated.

Example 1 [0032] Various controlled distribution block copolymers of the present invention were prepared according to the process disclosed in Illustrative Embodiment &num III of the continuing

and copending patent application to Serial Number 60/355,210 referenced above and filed concurrently with this application.

All polymers are unsaturated block copolymers where the A blocks are polystyrene blocks and the B blocks are styrene/butadiene controlled distribution blocks having terminal regions adjacent to the A blocks that are rich in butadiene units and other regions not adjacent to the A blocks that are rich in styrene units. All polymers were coupled polymers, where the coupling agent was tetra ethoxy-silane.

Under the polymerization conditions the predominant species is the linear product, i. e. (A-B) 2X, although 10 to 30 weight percent of the 3-armed radial product, i. e. (A-B) 3X is also formed, along with some uncoupled diblock, i. e. A-B. For purposes herein, the coupling agent residue or remnant can be ignored. The various polymers are shown in Table 1 below.

These polymers were then used in the various applications described in the other Examples. Tables 1 and la list the various analytical results for the unsaturated polymers. Block I MW is the molecular weight of the first A or polystyrene block in units of 1000, Block II MW is the cumulative molecular weight of the B or controlled distribution block in units of 1000 and Block III MW is the molecular weight of the final A or polystyrene block in units of 1000. Regarding Step II MW, the first number is the 1,3-butadiene portion and the second number is the styrene portion. For example, in Polymer #16 the B block has a molecular weight of 85,000 butadiene and 31,000 styrene, for a total of 116,000. The 1,2-vinyl configuration is given as 23.5 mol percent, along with the weight percent styrene in the entire polymer and in the mid block. For example, for Polymer #16, the entire polymer has about 42 weight percent styrene and the mid-block has about 27 weight percent styrene ("Calc. Mid PSC"in Table la). Coupling efficiency (or CE) is given for each polymer. The styrene

blockiness for each polymer is calculated and shown in Table la ("Calc. Mid Blocky"). Finally the melt flow rate is given for some of the polymers.

Example 2 [0033] In this example one controlled distribution block copolymer (Polymer #17) was compared against a commercial sample of Styroflex@ BX6105, an unsaturated SBS block copolymer from BASF, which has a random styrene/butadiene mid- block. Polymer #17 is made with a controlled distribution styrene/butadiene mid-block according to the present invention. Both have similar overall styrene contents as shown in Table 2. As shown in Table 2, Polymer # 17 has a much improved melt flow measured under 200 ° C/5 kg conditions.

Hardness and haze were measured on injection molded plaques with melt temperatures/injection pressures of 204 °C/1000 psi and 190 ° C/800 psi for Styroflex and Polymer #17, respectively. Polymer #17 has a lower shore A hardness by approximately 20 points and 57% lower haze than Styroflex.

Mechanical properties were measured on compression-molded plaques pressed at 175 ° C and 1250 psi. Even though the tensile strengths are nearly identical, Polymer #17 has a higher elongation at break. Polymer #17 is also more compliant than Styroflex as indicated by the consistently lower moduli between 25% and 500%. Under a cyclic loading condition, Polymer #17 is more elastic as it recovers twice as much energy with half the permanent set of Styroflex.

[0034] The controlled distribution polymer #17 clearly exhibits much lower stress at low elongations compared to Styroflex, a polymer typical of the current art of randomized mid block polymers with a similar total styrene content. The stiffness at low elongations is typically characterized by the tensile modulus, or Young's modulus. For example the Young's modulus

of polymer #17 is only 1,400 psi (10 MPa) while for Styroflex is 5,000 psi (35 MPa). The rubber modulus, or slope between 100 and 300% elongation for polymer#17 is slightly higher, 94 psi (0.65MPa), than for Styroflex, 90 psi (0.62 MPA). Thus the controlled distribution polymer retains the stiff stretch at high elongations and high tensile strength of a random polymer but with the added benefit of much more elastic behavior at low elongations.

Example 3 [0035] In this example two different controlled distribution block copolymers (Polymer #19 and Polymer #17) were blended online (compound 3-1 comprising 100 percent Polymer #19 and compound 3-2 comprising 70 percent Polymer #17 and 30 weight percent of KRATON D-1403, a 75% weight styrene content styrene/butadiene block copolymer) and extruded into film using a cast film line. Both compounds have high levels of polystyrene (over about 70 weight percent). Test results are shown in Table 3. Due to processing-induced orientation, Compound 3-1 exhibits a distinct yield point in both machine and transverse directions with a mechanical response similar to a polyolefin, while compound 3-2 is more elastomeric. Both film compounds have high tensile strengths making them suitable for food wrap and flexible packaging film applications. Compound 3-2 also demonstrates good cling characteristics. In cases where the PSC is over 70%, it is possible to obtain polymer with a distinct yield point depending on processing conditions. Using this attribute either a semi-rigid or flexible film can be made.

Example 4 [0036] In this example one controlled distribution block copolymer (Polymer # 17) was prepared into a solvent cast film

from a 10% wt. toluene solution. Oxygen and carbon dioxide permeability coefficients are shown in Table 4 along with reported values for LDPE (0.914 density) and polystyrene. The units are 1013cm3xcm/cm2xSxPa. As shown in Table 4, the controlled distribution polymer of the present invention has permeability coefficients that are of the same order as those reported for LDPE and PS.

Example 5 [0037] Blends of a controlled distribution Polymer # 17 (containing 63% total polystyrene) were made with homopolystyrene having 13 melt index, Chevron-Phillips MC3600.

In Table 5 examples 5-2 through 5-6 show that surprisingly, the addition of up to 40 wt% homopolystyrene still results in an elastic film with good recovery and low permanent set. The total styrene content of the film 5-5 is nearly 78%. It is well known in the art that block copolymer films with a majority of polystyrene content are plastic rather than elastic. Examples 5-2 through 5-6 were prepared in a Brabender mixing head. Of particular note is the recovery of more than 50% of the strain energy and only 14% permanent set after elongation to 100% for homopolystyrene contents less than 50%.

Blend 5-7 shows that the addition of oil can be used to reduce the modulus of the blend and improve its recovery.

[0038] Also shown in Table 5 is data for poly (vinyl chloride) ("PVC"). Compounds 5-3,5-4 and 5-5 resemble the performance of PVC with similar hardness, improved tensile strengths, and improved hysteresis with comparable stiffness.

[0039] In addition the high styrene content of the blends allows them to be painted and printed on directly without pretreatment.

Example 6 [0040] In Example 6 controlled distribution block copolymers # 17,19 and 20 were compounded with varying amounts of a polypropylene homopolymer (PP 5A15H), a polystyrene homopolymer (Chevron-Phillips MC3600), a paraffinic oil (Drakeol@ 34), and a naphthenic oil (Renoil@ 471) as shown in Table 6. The compounds were prepared using a Brabender mixing head followed by compression molding at 175 °C. As shown in Table 6, compounds can be prepared with polystyrene and polypropylene with or without oil to have high tensile strengths and various hardnesses.

Example 7 [0041] In Example 7 Chevron-Phillips MC3600 homopolystyrene was compounded with a controlled distribution polymer in a single screw extruder film line. The controlled distribution polymer # 17 was tumbled with homopolystyrene pellets and the mixture was fed into the extruder operating under standard conditions for film formation. The screw in the extruder was a normal compression screw with no mixing elements. The films were tested according to ASTM D412 in the machine and transverse directions. In these blends orientation is apparent in the machine direction resulting in very stiff films. In the transverse direction, however, the films remain elastic with good recovery. The high styrene contents of these films also allows adhesives to be used against the film without degradation of the adhesive properties.. To demonstrate this feature, a film of sample 7-3 was aged at 65°C for two weeks in contact with an adhesive composed of 25% SIS polymer, 60% tackifying resin and 15% oil. The peel strength after aging dropped from 4.2 pli to 2.9 pli. The adhesive was analyzed afterward and found to contain approximately 39% SIS polymer and 61% combined tackifying resin and oil. This indicates that

some of the tackifying resin and oil had been absorbed into the 7-2 film, thus explaining the loss of adhesion. By comparison a typical elastomeric film based on a traditional SEBS block copolymer lost all of its adhesion after aging in contact with the same adhesive for two weeks at 65°C. After aging the adhesive was found to contain 83% SIS polymer and 17% tackifying resin and oil. This indicated that almost all of the tackifying resin and oil had migrated into the elastomeric film destroying the adhesion.

Example 8 [0042] In this example one controlled distribution block copolymer (Polymer # 19) was prepared into cast film on a single screw extruder equipped with a chill roll, nip rollers, and a coat hanger film die. The sample was prepared with the chill roll operating at 30 rpm and the nip rollers at 50 rpm.

Samples were then drawn to either 100% or 200% strain at 25°C and/or 50°C as shown in Table 8 below. Drawn samples were allowed to equilibrate at 25°C for two hours prior to submersion in 40°C water for 30 seconds. Prior to submersion in the water, bench marks were placed on the sample so that a percent shrinkage could be determined as ( (length after submersion-length prior to submersion) /length prior to submersion). The as cast, undrawn control exhibits 6% shrinkage after 30 seconds in 40°C water. Film drawn to 200% strain at 25°C exhibits approximately 38% shrinkage after 30 seconds at 40°C. The effect of shrinkage temperature was also evaluated on the film drawn to 200% strain at 25°C. Shrinkage of approximately 54% is observed after submersion in 70°C water for 30 seconds. As shrinkage occurs in the machine directions, expansion also occurs in the transverse direction

of 34%. Finally, the natural shrinkage of the film was measured by drawing the as cast film to 100% strain and measuring the shrinkage at 25°C on an unconstrained film.

After 60 minutes the film exhibits a natural shrinkage of approximately 37%.

Example 9 [0043] Controlled distribution, styrenic block copolymers of the present invention offer processing advantages when used as modifiers for styrene monomer based thermoset applications. As shown in Table 9, controlled distribution Polymers #17 and #19 afforded lower viscosity solutions in styrene monomer (15% wt polymer, 25°C) than did Comparative S-B-S Polymer I ("CP I"), a linear styrene-butadiene-styrene triblock copolymer; this inspite of the controlled distribution polymers being over 75% higher in molecular weight. When compared to a linear S-B-S polymer more their size, Comparative S-B-S Polymer II ("CP II"), Polymers #17 and #19 afforded solution viscosities that were less than 25% of that of conventional polymer. Clearly the styrene solutions of Polymers #17 and #19 will be easier to handle, more freely flowing, than similar solutions prepared from Comparative S-B-S Polymer II. In Table 9, the Brookfield viscosity is measured with Spindle 21 at 100 rpm, and PSC is the polystyrene content of the block copolymer.

[0044] Illustrative embodiment Polymer #20 had a much lower styrene content than did Polymers #17 and #19. Though polymer #20 was lower in MW than either #17 or #19, the viscosity of a styrene solution of Polymer #20 was more than twice that of either of the larger polymers. These results support the hypothesis that polymers of the current invention which have higher styrene levels will be preferred over polymers having styrene levels below 50% wt. The higher in styrene content, controlled distribution polymers will be easier to process in

styrene based thermoset systems than analogous polymers having styrene contents below 50% wt.

[0045] In view of the viscosity performance in styrene monomer, it is expected that the controlled distribution polymers of the present invention would be good candidates for sheet molding compound (SMC) and bulk molding compound (BMC) applications. See, e. g. , US Patent No. 4,400, 478, which is herein incorporated by reference, which discloses formulations and technology for employing block copolymers in SMC and BMC applications.

Example 10 [0046] In Example 10 a controlled distribution polymer of the present invention (Polymer # 17) was compounded with a polypropylene homopolymer (Novolene 100 UC) in order to determine its suitability in slush molding applications (amounts are in parts by weight). The compound (10-2) was compared with a compound based on Styroflex BX-6105 (10-1). As shown in Table 10, the properties of the two compounds are similar, but the melt flow for the compound based on the controlled distribution polymer is significantly higher, making it a better candidate for slush molding applications.

Example 11 [0047] In Example 11 a controlled distribution copolymer was used in a compound for overmolding on various substrates, and was used as a neat polymer for overmolding, and was compared with a commercial formulation used in overmolding. The substrates used for the testing were Nylon 6 (N6), high impact polystyrene (HIPS) and an acrylonitrile butadiene styrene terpolymer (ABS).

[0048] In compound 11-1, a maleated hydrogenated block copolymer

(KRATON 1901X) was compounded with controlled distribution copolymer # 17, Renoil 471 oil and calcium carbonate. Compound 11-2 is a commercial overmolding compound based on KRATON 1901X and a selectively hydrogenated SBS block.

[0049] Substrates were injection molded using a Krauss Maffai molding machine. Nylon 6 was dried under vacuum for 24 hours at 180 F before molding. ABS was dried under vacuum for 2 hours at 180 F before molding. Selected materials were then over molded onto the substrates using the Krauss Maffai molding machine.

[0050] Over molded plaques were cut into 1 inch strips.

Approximately inch of the over molded material was peeled back from the substrate. The peeled part of the substrate was then bent, in a heated press, to a 90 degree angle. Five strips of each material were tested for 90 degree peel strength using an Instron 1120 tensile tester. The test was run at 2 inches per minute. Average initial peel strengths are shown in Table 12.

[0051] The results indicate that for ABS and HIPS substrates, the neat unsaturated Polymer # 17 performs even better than the commercial over molding compound and much better than the 11-1 compound. Results with Nylon 6 show almost equivalent performance with the commercial over molding compound. The neat Polymer # 17 also maintains a superior clarity over both the commercial compound and the 11-1 compound blend.

Example 12 [0052] In Example 12 three different controlled distribution polymers were compounded with varying amounts of polystyrene (PS) and styrene/methyl methacrylate (SMMA) polymers to determine the effect on overall properties. The three

controlled distribution polymers were Polymers 17,19 and 20.

The polystyrene was EB 3300 from Chevron Phillips and the SMMA was CET-130 from Resirene. Also used was KRATON D 1403, a high styrene content styrene/butadiene block copolymer having a PSC of about 75% weight; KR03, a high styrene block copolymer from Chevron Phillips having a styrene content of about 75% weight; Finaclear 520 from Fina having a styrene content of about 73% ; and Styrolux 3G55 from BASF, also having a styrene content of about 75% weight. The various components were first dry blended, and the blend was injection molded on an Engel injection molding machine. The tensile properties were tested based on ASTM D-638, and the optical properties were tested based on ASTM D-1003. The results and various formulations (expressed as percent by weight) are listed in Table 13.

[0053] With regard to the 100% polymer comparisons, all polymers had approximately the same styrene contents. However, Polymer # 19 according to the present invention had higher elongation than D1403, KR03, and Styrolux 3G55. Regarding the 50/50 blends, the blend with Polymer # 19 had the highest elongation, i. e. more than 10 times higher than the elongation of a blend of PS with a conventional high styrene-content SBS block copolymer-D 1403, and higher than the competitive blends.

[0054] In 70/30 blends with SMMA polymers, the elongation for blends with Polymer # 19 was nearly twice that for the blend with D-1403.

[0055] These comparisons show that Polymer # 19 may have higher efficiency in modifying PS and SMMA to make rigid packaging products and molded goods, i. e. you will need less styrene block copolymer to modify the PS or SMMA when using the controlled distribution polymers of the present invention.

Example 13 [0056] Some polymers of the current invention may be used as damping materials. For damping applications it is important to have a glass transition temperature as measured by dynamic mechanical testing in the range of-10°C to +30°C. It is also important to be able to readily tune the glass transition temperature to achieve damping either of selected frequencies or at selected temperatures. Table 14 shows that the Tg of Polymer #17 is 4. 6°C, which is in the range commonly used for damping. Example 14-2 and 14-3 show that the Tg can be readily increased by the addition of a midblock resin such as Regalrez 1085 or an end block resin such as Kristallex 1120. Example 14-4 and 14-5 show that the addition of oil reduces the Tg of the polymer whether or not there is a homopolystyrene present.

Increases in Tg are accompanied by increasing stiffness and conversely decreased Tg's are accompanied by decreasing stiffness. In all cases good strength and elongation are maintained.

Table 1: Analytical Results for Unsaturated S/Bd Mid-Block Polymers Polymer Block I Block II Block Distri 1, 2-BD PSC CE MFR No. MM MM III bution (200C/ MW Agent 5kg) (%) (%) (%) (g/10 min) 16 15.5 85/31 15.5 DEE 23.5 42 >90 0.6 17 15.6 50/50 15.6 DEE 24.6 63 >90 17.6 18 11.7 75/25 11.7 nBE 22.8 40 70 10.8 19 21 38/69 21 DEE 24.3 76 95 11.7 20 12.5 78/25 12.5 ODMB 23.7 38.8 92 21 21.2 36/65 21.2 DEE 32.6 76 95 22 20.1 30/65 20.1 ODMB 30 74 94 23 14.8 49/49 14.8 ODMB 25 64.5 90 Table la: NMR Results for Polymers at the end of Step II Polymer Expt. Expt. Calc. Calc. Mid Number NMR PSC#NMR Mid PSC Blocky Blocky 16 42. 3 56 26.9 12 17 61. 8 45 49.9 11 18 40. 0 59 26.0 22 19 75. 4 56 65.7 30 20 38. 7 57 23. 8 13 21 76. 9 55 67.1 27 22 74. 3 59 63.4 32 23 64. 5 57 53.8 33 Table 2 Polymer Styroflex #17 BX6105 PSC (%) 63 66 MFR (g/lOmin) 17.7 10.5 Shore A Hardness 62 84 (10s) Haze (%) 21. 8 51.3 Tensile TS (psi) 4298 4338 Elongation (%) 950 734 25% Modulus 152 429 (psi) 50% Modulus 203 465 (psi) 100% Modulus 255 524 (psi) 200% Modulus 366 760 (psi) 300% Modulus 517 1122 (psi) 500% Modulus 917 2125 (psi) 150% Hysteresis Recovered Energy 59.1 30.7 (%) Permanent Set 18. 9 38.9 (%) Table 3 Compound Number 3-1 3-2 Polymer # 19 100 Polymer # 17 70 D1403 30 Tensile (MD) Tensile Strength (psi) 3785 3685 Elongation (%) 397 464 100% Modulus (psi) 1577 988 300% Modulus (psi) 2929 1918 Tensile (PMD) Tensile Strength (psi) 3650 4020 Elongation (%) 390 560 100% Modulus (psi) 1545 455 300% Modulus (psi) 2846 1170 100% Hysteresis (MD) Recovered Energy (%) 4. 7 18 Permanent Set (%) 86 45 100% Hysteresis (PMD) Recovered Energy (%) 4. 6 36 Permanent Set (%) 86 21 200% Hysteresis (MD) Recovered Energy (%) 5. 2 15 Permanent Set (%) 168 102 200% Hysteresis (PMD) Recovered Energy (%) 5. 1 34 Permanent Set (%) 168 41 MD = machine direction; PMD = perpendicular to machine direction (also called transverse direction, TD)

Table 4 Carbon Dioxide Oxygen Permeability Permeability Coefficient Coefficient Polymer # 17 15.6 2.0 LDPE 9.5 2.2 PS 7.9 1.9 Table 5 Compound 5-1 5-2 5-3 5-4 5-5 5-6 5-7 5-8 PVC Number Polymer #17 100 90 80 68 60 50 61. 2 61. 2 PS (MC3600) 10 20 32 40 50 28.8 28.8 Drakeol 34 10 Renoil 471 10 Tensile Tensile 4298 3492 3780 4088 3251 2192 2992 2888 2168 Strength (psi) Elongation 950 770 604 534 404 229 713 657 409 (%) 50% Modulus 203 236 286 360 450 956 178 207 488 (psi) 100% 255 309 418 577 789 1372 273 308 751 Modulus (psi) 200% 366 491 816 1213 1620 2055 534 606 1196 Modulus (psi) 100% Hysteresis Peak Stress 281 352 498 691 1229 288 252 (psi) Recovered Energy 58.9 57.5 55.5 50.5 27.3 63.7 65.6 26 (o) Permanent Set 16.2 14.5 14.3 14.6 20.2 11.1 11.1 37 (%) Shore A 71 73 75 70 Hardness (lOs) Table 6 Compound 6-1 6-2 6-3 6-4 6-5 6-6 PVC Number Polymer # 17 61. 2 87 87 Polymer # 19 100 95 Polymer # 20 70 PS (MC3600) 28. 8 5 30 PP (5A15H) 13 Drakeol 34 10 Renoil 471 13 Shore A Hardness (lOs) 64 94. 5 67 65 47 70 Tensile Tensile 2992 3670 4315 3187 4837 3394 2168 Strength (psi) Elongation 713 447 457 807 874 1070 409 (%) 50% Modulus 178 1228 1266 223 272 138 488 (psi) 100% 273 1370 1493 302 370 170 751 Modulus (psi) 200% 534 1922 2160 536 624 225 1196 Modulus (psi) 100% Hysteresis Peak Stress 288 (psi) Recovered 63.7 26 Energy (%) Permanent Set 11.1 37 (%) Table 7: Cast Films Mixed in the Extruder Compound # 7-1 7-2 7-3 7-4 Polymer 17,100 80 70 60 % w PS, % w 0 20 30 40 Tensile MD PMD MD PMD MD PMD MD PMD Tensile 4527 4518 4207 4542 4000 4300 3656 4690 Strength (psi) Elongation 733 746 439 513 406 537 283 396 (%) 25% Modulus 201 191 603 285 731 310 1367 543 (psi) 50% Modulus 249 231 767 357 916 391 1626 713 (psi) 100% 293 270 1060 493 1240 540 2060 1060 Modulus (psi) 2000 408 373 1730 978 1930 1030 2890 2140 Modulus (psi) 300% 584 535 2550 1860 2750 1840 3870 3390 Modulus (psi) 500% 1410 1321 4300 3410 Modulus (psi) 100% Hysteresis Peak Stress 365 332 1160 488 1287 553 2167 992 (psi) Recovered 37.4 42 20.8 45 16. 7 41. 7 9. 9 30. 4 Energy (%) Permanent Set 25.6 23.3 38.3 17 47.5 18.3 69 24.6 (%) Table 8 Shrink Performance of Polymer # 19 Cast Film Natural shrinkage at 25°C (%) 30 minutes 34.4 60 minutes 36.7 30s MD Shrinkage (%) at 40°C Undrawn Control 6.3 Drawn to 100% Strain 23.3 at 25° C Drawn to 100% Strain 28.8 at 50° C Drawn to 200% Strain 37.7 at 25° C Drawn to 200% Strain 40°C 70°C 30s MD Shrinkage (%) 37. 7 53.6 30s PMD Expansion (%) 20 34 Table 9-Solution Viscosities at 15 wt% in Styrene (25° C) Materi PSC MM Viscosity al (103) (cPs) Polyme 40% 120 378 r # 20 Polyme 63% 128 153 r # 17 Polyme 75% 135 126 r # 19 CP 1 30% 72 162 CP II 35% 140 648 Table 10: Polymer &num 17 comparison with Styroflex BX6105 in PP formulation Components 10-1 10-2 Polymer # 17-60 Styroflex BX-6105 60- PP Novolene 1100 40 40 MD PMD MD PMD Yield Mpa 16.5 14.6 16.2 13.8 Tensile Mpa 19.3 21.7 16.7 20.2 Strength Mod 100% Mpa 570 660 560 700 Mod 300% Mpa 14.4 13.1 14.3 13.3 Mod 500% Mpa 14.8 13.8 14.4 13.2 Elongation at % 17.3 16.4 16.1 15.1 break MFR g/1 33 38 230°C/2. 16kg 0' Table 11 11-1 PHR % wt 41.0 KRATON 1901X 70 17.5 Polymer # 17 30 7 Renoil 471 20 11. 7 2 Calcium 29. 2 Carbonate 9 Table 12 Material Avg and initial substrate peel strength (pli) 11-1 ABS 1.5 11-1 N6 1. 8 11-1 HIPS 9.1 Polymer 17 13.8 - ABS Polymer 17 2.9 - N6 Polymer 17 20 - HIPS 11-2 ABS 10.1 11-2 N6 3.6 11-2 HIPS 13.3 Table 13 Stress @ Stress @ % Strain Light SAMPLES: max. auto. brea @ Haze, % trans., load, k, psi auto. bre % psi ak 100% polymer comparisons EB3300 PS, 100% 9269. 6 9232. 9 3.96 n/a n/a Polymer # 19, 100% 2308 2307 338 n/a n/a D1403, 100% 4019.5 2998.1 153.8 1.9 90.0 KR03, 100% n/a 2747 311 3.06 90.54 STYROLUX 3G55, 100% n/a 2887 245 11 87.1 FINACLEAR 520, 100% 2807 >500 1.76 90. 56 50/50 blend comparisons PS/D1403, 50/50 7296. 2 6721. 4 5. 87 22. 7 80. 7 (84. 8% ca 1) PS/Polymer # 19,4782. 4 3563.1 62.6 28.9 71.3 50/50 PS/KR03, 50/50 6777.2 4415.3 12.4 n/a n/a PS/STYROLUX 3G55,5590. 5 4005.4 25.7 n/a n/a 50/50 PS/FINACLEAR 520,6617. 9 4973.3 8.1 n/a n/a 50/50 95/5 blend comparisons PS/D1155, 95/5 9028. 2 9028.2 6.07 40. 6 55. 8 PS/Polymer # 20, 8881.2 8881.2 3.42 54.1 (76% 51.4 95/5 cal) PS/Polymer # 17, 9086.9 9086.9 3.58 27.8 81.0 95/5 70/25/5 blend comparisons PS/D1403/D1155, 8103. 4 7982. 4 3. 82 22. 1 73. 6 70/25/5 PS/D1403/7825. 4 6947.8 5.48 19.5 64.0 Polymer # 20, 70/25/5 PS/D1403/8090. 4 7318.6 5.38 16.4 79.9 Polymer # 17, 70/25/5 70/30 blends with SMMA comparisons CET-130 SMMA/7845. 8 7845. 8 3. 71 6. 8 88. 9 D1403, 70/30 CET-130 SMMA/6961. 9 6156.3 7.15 n/a n/a Polymer # 19,70/30 Table 14 Compound 14-1 14-2 14-3 14-4 14-5 Number Polymer #17 100 80 80 87 61.2 Regalrez 1085 20 Kristalex 20 1120 Renoil 471 13 10 PS (MC3600) 28.8 Tensile Tensile 4298 3826 3601 3394 2888 Strength (psi) Elongation 950 972 859 1070 657 (%) 50% Modulus 203 164 323 138 207 (psi) 100% 255 216 356 170 308 Modulus (psi) 200% 366 327 488 225 606 Modulus (psi) TG (°C) 4.6 12.0 47.4-4. 0-3.9