CRAZE-RESISTANT POLYMODAL LINEAR BLOCK COPOLYMERS WITH TERMINAL TAPERED BLOCKS

Abstract: Sequential charging of initiator and monomers in a multistage solution polymerization process involving conjugated diene and monovinyl­ aromatic monomers wherein the final charge is a mixture of these monomers results in the production of resinous polymodal linear block copolymers each with a terminal tapered block. A typical 5-stage charge sequence is as follows: Stage 1: (S i ); Stage 2: (S i ); Stage 3: (B); Stage 4: (S i ); Stage 5: (S+B) wherein (S i ) is monovinylaromatic monomer and initiator; (B) is conjugated diene monomer and (S+B) is monovinylaromatic monomer and conjugated diene monomer. At each stage, polymerization is allowed to continue until no free monomer is present. The trimodal block copolymer products comprise high, medium and low molecular weight species designated, respectively, as S₁-S₂-B₁-S₃-B₂→S₄; S₂-B₁-S₃-B₂→S₄; and S₃-B₂→S₄ wherein S₁, S₂ and S₃ represent, respectively, polyvinylaromatic blocks resulting from polymer­ ization of the first, second and third charges of monovinylaromatic monomer (stages 1,2 and 4); B₁ represents a polydiene block resulting from polymerization of the first charge of conjugated diene monomer (stage 3); and B₂→S₄ represents a terminal tapered copolymer block resulting from polymerization of the conjugated diene and monovinyl­ aromatic monomers (stage 5). The subject copolymers can be fabricated into sheets and molded objects possessing little color, a high degree of transparency and excellent impact resistance. These fabricated products do not craze on being impacted.

Description: Field of the Invention The invention relates to polymodal linear block copolymers with terminal tapered blocks. In another aspect, the invention relates to a method of preparing polymodal linear block copolymers characterized by a terminal tapered block which involves sequential charging of initiator and monomers to the polymerization zone. Background of the Invention Although substantially transparent block copolymers have been prepared by a variety of initiator and monomer charge sequences, the prior art materials such as described in U.S. 4,335,221 are not entirely satisfactory in regard to transparency, craze-resistance and color. Articles fabricated from some of the available block copolymers are characterized by low impact strength, a tendency to craze on being impacted, a blue coloration and a haziness particularly in thin sheets. EP-A-0153727 discloses a block copolymer of conjugated diene and monovinyl aromatic monomer which is prepared by a sequential 6- or 7-stage polymerisation wherein in the first 5 or 6 stages, initiator and one of the monomeric compounds are charged according to the sequence as defined. The final stage is a coupling reaction. The deficiencies of many available block copolymers are evident in packaging applications such as blister packs for bandages and syringes. These transparent colorless packs are intended to display and protect the contents and maintain a sterile atmosphere within the pack. Crazing of these packs due to squeezing during shipping is very undesirable because the crazed packs and their contents are discarded on the presumption that the sterile atmosphere within the pack has been contaminated by an air leak. Thus, there is a need for block copolymers which possess the capacity to impart craze-resistance as well as transparency and little color to manufactured articles particularly in the packaging field. Invention Thus, it is an object of this invention to provide polymodal linear block copolymers which can be fabricated into products possessing craze-resistance, little color and a high degree of transparency. Another object of this invention is to provide blister packaging possessing craze-resistance and a high degree of transparency. Other aspects, objects and the several advantages of the invention will be apparent to those skilled in the art from the description and the appended claims. The inventive copolymers can be prepared by sequentially charging monomers and initiator to the polymerization zone wherein at least one conjugated diene monomer is copolymerized with at least one monovinylaromatic (monovinylarene) monomer in a 5-stage charge sequence comprising: Stage 1: (S i ): Initiator and monovinylaromatic monomer Stage 2: (S i ): Initiator and monovinylaromatic monomer Stage 3: (B): Conjugated diene monomer Stage 4: (S i ): Initiator and monovinylaromatic monomer Stage 5: (B and S): Conjugated diene monomer and monovinylaromatic monomer At each stage, polymerization is allowed to continue until essentially no free monomer is present. The terminal tapered block is produced in the fifth stage by charging both monomers to the polymerization zone. The instant polymodal linear block copolymers comprise high, medium and low molecular weight species designated, respectively, as S₁-S₂-B₁-S₃-B₂→S₄; S₄-B₁-S₃-B₂→S₄ and S₃-B₂→S₄ wherein S₁, S₂ and S₃ represent, respectively, polyvinylaromatic blocks resulting from polymerization of the first, second and third charges of monovinylaromatic monomer (stages 1,2 and 4); B₁ represents a polydiene block resulting from polymerization of the first charge of conjugated diene monomer (stage 3); and B₂→S₄ represents a terminal tapered copolymer block resulting from the polymerization of the final charge (stage 5) of conjugated diene monomer and monovinylaromatic monomer. The instant copolymers contain about 55 to 95 preferably 70 to 80 weight percent of monovinylaromatic monomer units and 45 to 5 preferably 30 to 20 weight percent conjugated diene monomer units based on total weight of monomers charged to the polymerization zone. Broad and preferred ranges for practicing the instant process are summarized in Table A. The symbols L, S and B represent, respectively, organomonoalkali metal initiator such as n-butyllithium, monovinylaromatic monomer such as styrene and conjugated diene monomer such as 1,3-butadiene. Monomers The conjugated diene monomers contain 4 to 6 carbon atoms and include 1,3-butadiene, isoprene, 2-ethyl-1,3-butadiene; 2,3-dimethyl-1,3-butadiene and piperylene and mixtures thereof. Presently preferred is 1,3-butadiene. The monovinylaromatic monomers contain 8 to 12 carbon atoms and include styrene, alpha-methylstyrene, p-vinyltoluene, m-vinyltoluene, o-vinyltoluene, 4-ethylstyrene, 3-ethylstyrene, 2-ethylstyrene, 4-tertbutylstyrene and 2,4-dimethylstyrene and mixtures thereof. Presently preferred is styrene. Polymerization The polymerization process is carried out in a hydrocarbon diluent at any suitable temperature in the range of -10 to 150°C preferably in the range of 0 to 110°C at pressures sufficient to maintain the reaction mixture substantially in the liquid phase. Preferred hydrocarbon diluents include linear and cycloparaffins such as pentane, hexane, octane, cyclohexane and mixtures thereof. Presently preferred is cyclohexane. Small amounts of polar organic compounds such as tetrahydrofuran are required in the hydrocarbon diluent to improve the effectiveness of n-alkylmonoalkali metal initiators such as n-butyllithium. Amounts of tetrahydrofuran to provide from about 0.01 to 1.0 phm (parts per hundred parts of total monomer), preferably 0.02 to 0.1 phm are suitable. The initiators can be any of the organomonoalkali metal compounds of the formula RM wherein R is an alkyl, cycloalkyl or aryl carbanion containing 4 to 8 carbon atoms and M is an alkali metal cation. The presently preferred initiator is n-butyllithium. Suitable amounts of organomonoalkali metal initiator are encompassed by the ranges given in Table A. The polymerization is carried out in the substantial absence of oxygen and water preferably under an inert gas atmosphere. Prior to the termination treatment, the reaction mass contains a very high percentage of living molecules in which an alkali metal cation is positioned at one end of each polymer chain. Impurities in the feed such as water or alcohol reduce the amount of monoalkali metal living polymer in the reaction mass. At the conclusion of the polymerization process, the system is treated as is known in the art with an active hydrogen compound such as water, alcohol, phenols or linear saturated aliphatic mono- and dicarboxylic acids to convert terminal carbon-lithium bonds on the living polymer molecules to carbon-hydrogen bonds resulting in the separation of copolymer. Preferably, the polymer cement, i.e., the polymer in the polymerization solvent, is treated with terminating agents (water and carbon dioxide) and then antioxidants before the solvent is flashed off to increase the solids content. The resinous copolymers can be and usually are compounded with various additives such as release agents and the like before fabrication into useful articles such as molded objects and sheeting. The following Examples illustrate the invention. Example I This example describes the preparation of inventive polymodal linear block copolymers with one terminal tapered block. Styrene and 1,3-butadiene were copolymerized in a 5-stage process using n-butyllithium initiator. The runs were carried out under nitrogen in a two-gallon jacketed stainless steel reactor. The anhydrous reaction mixtures were stirred continuously during the polymerization process. Termination was effected by the conventional use of carbon dioxide and water. A mixture of Irganox 1076 (0.25 phm) and tris(nonylphenyl)phosphite (TNPP) (1.0 phm) was added prior to isolation of copolymer product. The inventive procedure is summarized in Table I. Referring to the two invention runs in Table I, it is evident that the invention products were prepared in a 5-stage process involving three portions of styrene and initiator (stages 1, 2 and 4), one portion of 1,3-butadiene (stage 3) and a final portion of styrene and 1,3-butadiene (stage 5). This sequence of charging reactants to the polymerization zone results in a terminal tapered block on each high, medium and low molecular weight copolymer in the product. As a result of the sequential charging of initiator in stages 1, 2 and 4 (i.e., 3 charges of initiator), the copolymer products obtained in runs 1 and 2 of Table I are referred to as polymodal, specifically trimodal. This term connotes the production of three molecular weight species: high, medium and low, arising by the initiation of new polymer chains in stages 1, 2 and 4. Thus, in stage 1, living polystyrene chains are initiated by n-butyllithium and propagation continues until no styrene monomer is present resulting ideally in S₁-Li living polymer chains of comparable molecular weight. The further addition of initiator and styrene (stage 2) results in the initiation of new polystyrene chains and propagation of the living S₁-Li chains initiated in stage 1. After two stages wherein all styrene monomer has been polymerized, the bimodal species can be represented as: S₁-S₂-Li and S₂-Li wherein S denotes polystyrene blocks and subscripts indicate the stage of monomer addition. The addition of 1,3-butadiene at stage 3 results in the incorporation of the conjugated diene into each of the above living polymers to give bimodal copolymers: S₁-S₂-B₁-Li and S₂-B₁-Li wherein S₁ and S₂ are polystyrene blocks and B₁ is a polybutadiene block. In stage 4 additional styrene and n-butyllithium are introduced resulting in the initiation of new polystyrene chains and propagation of the existing S₁-S₂-B₁-Li and S₂-B₁-Li living polymers. After stage 4 wherein all monomer has been polymerized, the trimodal species can be represented as: S₁-S₂-B₁-S₃-Li; S₂-B₁-S₃-Li and S₃-Li designating high, medium and low molecular weight species. In stage 5 no additional initiator is charged so that the term trimodal is still descriptive of the copolymers produced. In stage 5 both styrene and 1,3-butadiene are introduced. Preferably, the monomers are charged as a mixture. Alternatively, the 1,3-butadiene is momentarily charged before the styrene. The rate of polymerization of 1,3-butadiene is significantly greater than that of styrene so 1,3-butadiene is incorporated more rapidly leading to living copolymers with terminal blocks enriched in units from the diene. As the free 1,3-butadiene monomer concentration decreases, the living copolymers begin to incorporate both 1,3-butadiene and styrene monomers until a point is reached at which all the 1,3-butadiene has been incorporated and polymerization continues until all the styrene monomer has been incorporated. This results in a terminal tapered block enriched with styrene units at its terminal end preceded by a mixed zone of units derived from styrene and 1,3-butadiene in turn preceded by a block enriched in units derived from 1,3-butadiene. After stage 5 the high, medium and low molecular weight trimodal species are: S₁-S₂-B₁-S₃-B₂→S₄-Li; S₂-B₁-S₃-B₂→S₄-Li and S₃-B₂→S₄-Li wherein S₁, S₂ and S₃ represent, respectively, polystyrene blocks resulting from polymerization of the first, second and third charges of styrene (stages 1,2 and 4); B₁ represents a polybutadiene block resulting from polymerization of the first charge of 1,3-butadiene (stage 3) and B₂→S₄ represents a terminal tapered copolymer block resulting from polymer propagation in the presence of both 1,3-butadiene and styrene. After termination of the polymerization and product recovery, these species can be represented as: S₁-S₂-B₁-S₃-B₂→S₄; S₂-B₁-S₃-B₂→S₄ and S₃-B₂→S₄. Example II This example describes the preparation of linear block copolymers with one terminal tapered block in accordance with the prior art teaching of patent U.S. 4,335,221. Styrene and 1,3-butadiene were copolymerized in a 3-stage process using n-butyllithium initiator. The runs were carried out under nitrogen in a two-gallon jacketed stainless steel reactor. The anhydrous reaction mixtures were stirred continuously during the polymerization process. Termination was effected by the conventional use of carbon dioxide and water. The procedure is summarized in Table II. Referring to the control runs in Table II, it is evident that the products were prepared in a 3-stage process involving two portions of styrene and initiator (stages 1 and 2) followed by a final portion of styrene and 1,3-butadiene (stage 3). This sequence of charging reactants to the polymerization zone results in a terminal tapered block on each high and low molecular weight copolymer in the product. As a result of the sequential charging of initiator in stages 1 and 2 (i.e., 2 charges of initiator,) the copolymer products obtained in runs 1 and 2 of Table II are referred to as polymodal, specifically bimodal, in contrast to the trimodal inventive copolymers of Example I. The term bimodal connotes the production of two molecular weight species: high and low arising by the initiation of new polymer chains in stages 1 and 2. Thus, in stage 1, living polystyrene chains are initiated by n-butyllithium and propagation continues until no styrene monomer is present resulting ideally in S₁-Li living polymer chains of comparable molecular weight. The further addition of initiator and styrene (stage 2) results in the initiation of new polystyrene chains and propagation of the living S₁-Li chains initiated in stage 1. After two stages wherein all styrene monomer has been polymerized, the bimodal species can be represented as: S₁-S₂-Li and S₂-Li wherein S denotes polystyrene blocks and subscripts indicate the stage of monomer addition. The addition of 1,3-butadiene and styrene in stage 3 with no additional initiator does not change the modality of the products. In stage 3 both styrene and 1,3-butadiene are introduced to cause formation of tapered blocks. Preferably, the monomers are charged as a mixture. The rate of polymerization of 1,3-butadiene is significantly greater than that of styrene so 1,3-butadiene is incorporated more rapidly leading to living copolymers with terminal blocks enriched in units from the 1,3-butadiene. As the free 1,3-butadiene monomer concentration decreases, the living copolymers begin to incorporate both 1,3-butadiene and styrene monomers until a point is reached at which all the 1,3-butadiene has been incorporated and polymerization continues until all the styrene monomer has been incorporated. This results in a tapered 1,3-butadiene/styrene block enriched with styrene units at its terminal end preceded by a mixed zone of units derived from styrene and 1,3-butadiene in turn preceded by a block enriched with units derived from 1,3-butadiene. After stage 3 the high and low molecular weight bimodal species are: S₁-S₂-B₁→S₃-Li and S₂-B₁→S₃-Li wherein S₁ and S₂ represent, respectively, polystyrene blocks resulting from polymerization of the first and second charges of styrene (stages 1 and 2) and B₁→S₃ represents a terminal tapered copolymer block resulting from polymer propagation in the presence of both 1,3-butadiene and styrene. After termination of the polymerization and product recovery, the high and low molecular weight bimodal species can be represented as: S₁-S₂-B₁→S₃ and S₂-B₁→S₃. The copolymer species present in the Example I products (inventive) and the copolymer species present in the Example II products (prior art copolymers) can be compared as below: Example III This example compares the properties exhibited by test samples of invention copolymers (trimodal) with the properties of test samples prepared from the control copolymers (bimodal). The invention copolymers were prepared by the procedure summarized in Table I of Example I. The control copolymers were prepared by the procedure summarized in Table II of Example II. The comparative results are compiled in Table III. Referring to the summary in Table III, it is evident that the trimodal invention copolymers were clearly superior to the bimodal control copolymers in regard to blueness in that the Hunter (-) "b" values are lower for the instant copolymers indicating a very slight blue tint (values 4.6 and 6.0) compared to the distinct blueness in the control copolymers (values 14.7 and 24.7). In regard to % Haze and Gardner Impact values, the invention copolymers and control copolymers were comparable; however, the bimodal control copolymers crazed on being impacted whereas the instant trimodal copolymers did not craze on being impacted. Reasonable variations and modifications of the present invention which will become apparent to those skilled in the art can be made in this invention without departing from the spirit and scope thereof.

Claims: Claims for the following Contracting States : BE, CH, DE, FR, GB, IT, LI, LU, NL, SE A process for producing polymodal, craze-resistant, low-color, transparent linear resinous copolymers each with a terminal tapered copolymer block of said monomers by polymerizing under solution polymerization conditions at least one monovinylaromatic monomer containing 8-12 carbon atoms and at least one conjugated diene monomer containing 4-6 carbon atoms in a ratio of 55-95 weight-% monovinylaromatic monomer and 45-5 weight-% conjugated diene monomer in a sequential charge polymerization process, characterized in that two separate charges consisting of said monovinylaromatic monomer and an organomonoalkali metal initiator precede a separate charge of conjugated diene monomer followed by an additional separate charge of said monovinylaromatic monomer and said initiator before a final charge of said monovinylaromatic monomer and said conjugated diene monomer, each monomer charge being polymerized to substantial completion prior to addition of any subsequent charge, wherein said sequential charge polymerization process employs a 5-stage charge sequence: stage 1: initiator and monovinylaromatic monomer (S i ) stage 2: initiator and monovinylaromatic monomer (S i ) stage 3: conjugated diene monomer (B) stage 4: initiator and monovinylaromatic monomer (S i ) stage 5: conjugated diene monomer and monovinylaromatic monomer (B and S). The process of claim 1 characterized by employing ranges of monomer additions and of organomonoalkali metal initiator added at each stage: wherein L represents organomonoalkali metal initiator, B represents conjugated diene monomer, S represents monovinylaromatic monomer, phm represents parts by weight per 100 parts by weight of total monomers and mhm represents gram-millimoles per 100 grams of total monomers. The process of claim 2 characterized by employing ranges of monomer additions and of organomonoalkali metal initiator added at each stage: The process of any of the preceding claims characterized by employing 1,3-butadiene as said conjugated diene monomer. The process of any of the preceding claims characterized by employing styrene as said monovinylaromatic monomer. The process of any of the preceding claims characterized by employing n-butyllithium as said organomonoalkali metal initiator. The process of any of the preceding claims characterized in that in stage 1 the charge includes 0.01 to 1.0 parts by weight of tetrahydrofuran based on 100 parts of the total amount of monomers charged. The process of any of the preceding claims characterized by employing a ratio of 70 - 80 weight percent of monovinylaromatic monomer units to 30 - 20 weight percent of conjugated diene monomer units. The polymodal linear block copolymers with terminal tapered blocks as obtained in any of claims 1 to 8. The use of the copolymers of claim 9 for making blister packs. Claims for the following Contracting States : AT, ES A process for producing polymodal, craze-resistant, low-color, transparent linear resinous copolymers each with a terminal tapered copolymer block of said monomers by polymerizing under solution polymerization conditions at least one monovinylaromatic monomer containing 8-12 carbon atoms and at least one conjugated diene monomer containing 4-6 carbon atoms in a ratio of 55-95 weight-% monovinylaromatic monomer and 45-5 weight-% conjugated diene monomer in a sequential charge polymerization process, characterized in that two separate charges consisting of said monovinylaromatic monomer and an organomonoalkali metal initiator precede a separate charge of conjugated diene monomer followed by an additional separate charge of said monovinylaromatic monomer and said initiator before a final charge of said monovinylaromatic monomer and said conjugated diene monomer, each monomer charge being polymerized to substantial completion prior to addition of any subsequent charge, wherein said sequential charge polymerization process employs a 5-stage charge sequence: stage 1: initiator and monovinylaromatic monomer (S i ) stage 2: initiator and monovinylaromatic monomer (S i ) stage 3: conjugated diene monomer (B) stage 4: initiator and monovinylaromatic monomer (S i ) stage 5: conjugated diene monomer and monovinylaromatic monomer (B and S). The process of claim 1 characterized by employing ranges of monomer additions and of organomonoalkali metal initiator added at each stage: Stage 1: L-1 (mhm) 0.312 - 0.625 S-1 (phm) 30 - 40 Stage 2: L-2 (mhm) 0.312 - 0.625 S-2 (phm) 10 - 20 Stage 3: B-1 (phm) 15 - 2.5 Stage 4: L-3 (mhm) 0.625 - 1.875 S-3 (phm) 10 - 20 Stage 5: B-2 (phm) 30 - 2.5 S-4 (phm) 5 - 15 Totals: S (phm) 55 - 95 B (phm) 45 - 5 L (mhm) 1.25 - 3.125 wherein L represents organomonoalkali metal initiator, B represents conjugated diene monomer, S represents monovinylaromatic monomer, phm represents parts by weight per 100 parts by weight of total monomers and mhm represents gram-millimoles per 100 grams of total monomers. The process of claim 2 characterized by employing ranges of monomer additions and of organomonoalkali metal initiator added at each stage: Stage 1: L-1 (mhm) 0.312 - 0.625 S-1 (phm) 30 - 40 Stage 2: L-2 (mhm) 0.312 - 0.469 S-2 (phm) 10 - 15 Stage 3: B-1 (phm) 10 - 4 Stage 4: L-3 (mhm) 0.625 - 1.563 S-3 (phm) 20 - 10 Stage 5: B-2 (phm) 20 - 16 S-4 (phm) 10 - 15 Totals: S (phm) 70 - 80 B (phm) 30 - 20 L (mhm) 1.25 - 2.657. The process of any of the preceding claims characterized by employing 1,3-butadiene as said conjugated diene monomer. The process of any of the preceding claims characterized by employing styrene as said monovinylaromatic monomer. The process of any of the preceding claims characterized by employing n-butyllithium as said organomonoalkali metal initiator. The process of any of the preceding claims characterized in that in stage 1 the charge includes 0.01 to 1.0 parts by weight of tetrahydrofuran based on 100 parts of the total amount of monomers charged. The process of any of the preceding claims characterized by employing a ratio of 70 - 80 weight percent of monovinylaromatic monomer units to 30 - 20 weight percent of conjugated diene monomer units. The use of the copolymers as obtained in any of claims 1 to 8 for making blister packs.

Inventors: KITCHEN, ALONZO GENE, SZALLA, FRANK JOHN
Applicants: PHILLIPS PETROLEUM COMPANY
Application year: 1987
Main classification: C08F297
IPC codes: C08F4, C08L53, C08F297