Miscible blends of imide containing polymers with poly(aryl sulfones)

Abstract: This application relates to miscible blends of biphe­ nyl containing poly(aryl sulfones) and isopropylidene based polyimides. These blends are suitable for printed wiring board substrates, flexible printed circuit boards, electrical connectors and fabricated articles requiring heat and chemical resistance. A method for extruding these articles is taught.

Description: The present invention relates to unique combinations of select polyamide-imides that contain an isopropylidene group which are miscible with biphenyl containing polyarylsulfones, and processes for using such combinations. These blends are suitable for printed wiring board substrates, flexible printed circuit boards, electrical connectors and other fabricated articles requiring high heat and chemical resistance, and good dimensional and hydrolytic stability. They are particularly suitable for use as matrix resins in thermoplastic continuous fiber composites. Applicants have directed their attention to making miscible blends of polymers having utility as composite matrices for advanced composite aerospace uses and for use as general purpose injection molding resins. Rather than directing attention to miscible thermoplastic blends, the prior art has been directed to blends of thermoplastics without regard to whether or not they are miscible. US-A-4 293 670 to Robeson et al describes molding compositions of blends of poly(aryl ether) resin and a polyetherimide resin. The poly(aryl ether) resin is taught to be a linear, thermoplastic polyarylene polyether wherein the arylene units are interspersed with ether, sulfone or ketone linkages. Particular formulae of polyetherimides are taught in the reference. A molding composition comprising blends of these materials is claimed and exemplified in the reference. US-A- 4 713 426 describes blends of a biphenyl containing poly(aryl ether sulfone) and a poly(aryl ether ketone). The reference teaches that these blends have limited miscibility and excellent mechanical compatibility. According to the reference, these blends possess, in an article molded therefrom, a good balance of properties including higher modulus, impact resistance, solvent resistance and resistance to environmental stress cracking. As taught, the poly(aryl ether ketones) are used because they offer an exceptional balance of properties, namely, high melting point, excellent thermal stability, excellent hydrolytic stability, high stiffness and strength, good toughness, and excellent solvent and environmental stress rupture resistance. The reference specifically teaches that the results indicate that a low level of miscibility is observed in these blends as the glass transition temperature of the poly(aryl ether sulfone) is slightly decreased. However, the blend contains separate glass transition temperatures for each of the components of the blends. US-A- 4 684 674 to Brooks teaches another blend. Specifically, the reference teaches polyamide-imide-phthalamide copolymers and polyamide-imide copolymers containing aromatic sulfone polymers. However, the blends are two-phase and exemplified by two glass transition temperatures, one for each of the components of the blend. The reference teaches that a completely miscible system exhibits a single glass transition temperature (T g ) while immiscible blends have two T g 's, each at the temperature of one of the components. The reference specifically teaches that the polyamide-imide/polyethersulfone blends taught in the reference show no evidence of a system which is miscible. International Patent Application No. WO 8604-079A describes blends of phenylindane containing polyimides with polyetherimides, polysulfones, polyarylether ketones, polycarbonates, polyarylates or polyphenylene oxides. The compositions are claimed to be useful as adhesives, coatings or matrix resins in carbon fiber reinforced composites. EP-A-91117 discloses blends of a polyetherimide and a polysulfone. EP-A-256761 describes miscible blends of poly-carbonomides, defined as amide and/or imide containing polymers, and a polyarylate. In the field of miscibility or compatibility of polymer blends, the prior art has found predictability to be unattainable, even though considerable work on the matter has been done. According to the authorities: (A) "It is well known that compatible polymer blends are rare". Wang and Cooper, Journal of Polymer Science, Polymer Physics Edition, Vol. 21, p. 11 (1983). (B) "Miscibility in polymer-polymer blends is a subject of widespread theoretical as well as practical interest currently. In the past decade or so, the number of blend systems that are known to be miscible has increased considerably. Moreover, a number of systems have been found that exhibit upper and lower critical solution temperatures, i.e., complete miscibility only in limited temperature ranges. Modern thermodynamic theories have had limited success to date in predicting miscibility behavior in detail. These limitations have spawned a degree of pessimism regarding the likelihood that any practical theory can be developed that can accommodate the real complexities that nature has bestowed on polymer-polymer interactions." Kambour, Bendler, Bopp, Macromolecules, 16, 753 (1983). (C) "The vast majority of polymer pairs form two-phase blends after mixing as can be surmised from the small entropy of mixing for very large molecules. These blends are generally characterized by opacity, distinct thermal transitions, and poor mechanical properties. However, special precautions in the preparation of two-phase blends can yield composites with superior mechanical properties. These materials play a major role in the polymer industry, in several instances commanding a larger market than either of the pure components." Olabisi, Robeson, and Shaw, Polymer-Polymer Miscibility, Academic Press, New York, N.Y., p. 7 (1979). (D) "It is well known that, regarding the mixing of thermoplastic polymers, incompatibility is the rule and miscibility and even partial miscibility is the exception. Since most thermoplastic polymers are immiscible in other thermoplastic polymers, the discovery of a homogeneous mixture or partially miscible mixture of two or more thermoplastic polymers, is, indeed, inherently unpredictable with any degree of certainty; for example, see P. J. Flory, Principles of Polymer Chemistry, Cornell University Press, 1953, Chapter 13, p. 555." Younes, U.S. Patent No. 4,371,672. (E) "The study of polymer blends has assumed an ever increasing importance in recent years and the resulting research effort has led to the discovery of a number of miscible polymer combinations. Complete miscibility is an unusual property in binary polymer mixtures which normally tend to form phase-separated systems. Much of the work has been of a qualitative nature, however, and variables such as molecular weight and conditions of blend preparation have often been overlooked. The criteria for establishing miscibility are also varied and may not always all be applicable to particular systems." Saeki, Cowie and McEwen, Polymer, vol. 25, p. 60 (January 1983). Thus, miscible or compatible polymer blends are not common. The criteria for determining whether or not two polymers are miscible are now well established. According to Olabisi, et al., Polymer-Polymer Miscibility, supra p. 120: "The most commonly used method for establishing miscibility in polymer-polymer blends or partial phase mixing in such blends is through determination of the glass transition (or transitions) in the blend versus those of the unblended constituents. A miscible polymer blend will exhibit a single glass transition between the Tg's of the components with a sharpness of the transition similar to that of the components. In cases of borderline miscibility, broadening of the transition will occur. With cases of limited miscibility, two separate transitions between those of the constituents may result, depicting a component 1-rich phase and a component 2-rich phase. In cases where strong specific interactions occur, the Tg may go through a maximum as a function of the concentration. The basic limitation of the utility of glass transition determinations in ascertaining polymer-polymer miscibility exists with blends composed of components which have equal or similar (20°C difference) Tg's, whereby resolution by the techniques to be discussed by two Tg's is not possible." W. J. MacKnight et al., in Polymer Blends , D. R. Paul and S. Newman, p. 188, Academic press, New York, NY. (1978) state: "Perhaps the most unambiguous criterion of polymer compatibility is the detection of a single glass transition whose temperature is intermediate between those corresponding to the two component polymers." In this passage, it is clear that by compatibility the authors mean miscibility, i.e., single phase behavior. See, for example, the discussion in Chapter 1 by D. R. Paul in the same work. However, the miscible blends disclosed in this application are one phase based on them having a single glass transition temperature giving the resulting blends improved chemical resistance compared to the immiscible multiphase blends having similar constituents. Further, the miscible blends show improved thermal and optical performance over immiscible blends. This is attributable to discovering that select polyamide-imides having an isopropylidene group are miscible with biphenyl containing polyarylsulfones. Herein, the term "polyimide" refers to polymers containing the following linkage: or mer unit. This invention relates to a miscible blend of a poly(aryl sulfone) and a polyamide-imide comprising: (a) poly(aryl sulfone) containing the following unit: and (b) polyamide-imide containing the following unit: This invention also relates to a process for producing a miscible blend of biphenyl containing poly(aryl sulfone), and isopropylidene containing polyamide-imide comprising adding the monomers used to form the latter polymer to the poly(aryl sulfone) in a vented extruder. Disclosed herein is a method of improving the flow of polyamide-imides (PAI) while at the same time improving the chemical resistance of poly(aryl sulfones) (PAS) by alloying the two polymers together. A major factor limiting the applicability of the alloying approach is that the majority of polymer alloys are not miscible. That is, the alloys are two-phase; and the continuous phase is usually the lower viscosity component. Thus, immiscible blends will likely be a poly(aryl sulfone) filled with the polyamide-imide component as inclusions. Such a morphology generally results in an improvement in flow (e.g. reduced viscosity). However, the chemical resistance of such an alloy will be closer to that of the continuous phase than to the inclusions and may be expected to be poor. Additionally, in the event the T g s of the two components are significantly different, the upper use temperature of the alloy will not be significantly higher than that of the lower T g constituent. In the case of continuous fiber composites wherein the alloy is the matrix resin, the reason for this is that a high matrix modulus is necessary to prevent buckling of carbon fibers when a composite is loaded in compression. An immiscible blend has two T g s (usually near those of the constituents); and at each T g , the matrix modulus drops significantly. If such a blend is used as the composite matrix, then the useful temperature range of the composite is limited to the lower T g . It has been discovered unexpectedly that a select group of poly(aryl sulfones) is miscible with a select group of polyamide-imides. The poly(aryl sulfone) must contain biphenyl linkages while the polyamide-imides must contain isopropylidene linkages. These blends show markedly improved chemical resistance and a single T g intermediate to those of the constituents resulting from their miscible character. Thus, the upper use temperature of the alloy may be significantly improved over that of the lower T g constituent. Further, by reducing the T g of the higher T g constituent, it is typically more processable. As a consequence of this, these alloys can be used as injection moldable thermoplastic materials having improved flow and toughness characteristics as well as better chemical resistance. The components of the miscible blend of polyamide-imides with poly(aryl sulfones) will be discussed below. Also to be discussed is the need or criticality of the mixture to exhibit a negative miscibility factor. The poly(aryl sulfone)s which are suitable for use in the invention contain at least one biphenyl unit in the structure. The presence of the biphenyl unit in the poly(aryl sulfone) is critical to obtain miscibility between the poly(aryl sulfone) and the polyamide-imide. Poly(aryl sulfone) polymers are characterized by inherently high heat distortion temperatures, excellent dimensional stability, creep resistance, low loss AC dielectric properties, and high mechanical strength as shown below. Typical Properties of Poly(aryl sulfone) Resins Property Units Typical Range Tensile Strength psi (=6.895 KPa) 12,500-15,000 Elongation to Break % >40 Tensile Modulus psi (=6.895 KPa) 300-400,000 Flexural Strength psi (=6.895 KPa) 13,000-20,000 Heat Deflection Temperature °C 170-250 Density g/cm 3 1.2-1.4 AC Dielectrics Dielectric Constant 60 HZ -- 3.0-4.0 1 KHZ -- 3.0-4.0 1 MHZ -- 3.0-3.5 Dissipation Factor 60 Hz -- 0.0005-0.005 1 KHZ -- 0.0005-0.003 1 MHZ -- 0.004-0.01 Dielectric Strength 1/8" (=3.175 mm) specimen Volts/mil (=25.4 µm) 350-550 Poly(aryl sulfone) polymers are easily processed utilizing standard injection molding machinery and practice. Prior to molding, resins should be dried to obtain optimum performance in a dehumidified hopper drier or circulating air oven. The rheological characteristics of poly(aryl sulfone) polymers provide excellent flow for filling thin and intricate wall sections typically encountered in injection molding. The polymers process readily at stock temperatures in the 288-399°C (550°-750°F) range. Mold temperatures of 66-205°C (150°-400°F) are typically used. The poly(aryl sulfone) may be random or may have an ordered structure. The poly(aryl sulfone)s according to this invention contain at least one biphenyl unit in the repeat unit. The preferred biphenyl containing poly(aryl sulfone) contains the repeating unit: where x 1 and X 2 are independently -O-, -SO 2 -, -NHCO-, C-(CH 3 ) 2 or a direct bond with the proviso that at least one of x 1 or X 2 is a direct bond, and R, S and T are independently 0 or 1; with the proviso that at least one of R or S is 1. The preferred poly(aryl sulfones) employed in the process of this invention include those having the following recurring units: Examples of commercially available biphenyl containing poly(aryl sulfones) are the polymers known as Radel® R and Radel®C sold by Amoco Performance Products, Inc. of Ridgefield, Connecticut. The poly(aryl sulfone)s are produced by methods well known in the art such as those described in U.S. Patent Nos. 3,634,355; 4,008,203; 4,108,837 and 4,175,175. The preferred method of preparation, herein referred to as method A, involves the reaction of a dihydric phenol with a dihalobenzenoid compound in substantially equal molar amounts in a mixture of alkali metal carbonates and an aprotic solvent. The ratio of reactive halogen groups in the dihalobenzenoid compound to hydroxyl groups in the dihydric phenol is preferably from 0.98 to 1.02. Preferred dihalobenzenoid compounds include 4,4'dichlorodiphenylsulfone (DCDPS) and 4,4'-Bis[(4-chlorophenylsulfonyl)] 1,1′-biphenyl (BCPSB). Preferred dihydric phenols include 4,4'-dihydroxybiphenyl (BP), 4,4'-dihydroxydiphenylsulfone (Bis-S), 1,4-dihydroxybenzene (HQ), and Bis(4-hydroxyphenyl) 1-methylethylidene (Bis A). The poly(aryl sulfones) are prepared by contacting substantially equimolar amounts of the dihydric phenols and dihalobenzenoid compounds with from about 0.5 to 1.0 mole of an alkali metal carbonate per mole of hydroxyl group in a solvent mixture comprising a solvent which forms an azeotrope with water to maintain the reaction medium at substantially anhydrous conditions during polymerization. The reaction of the mixture is kept at from about 120° to about 180°C for about 1 to 5 hours, then raised and kept at about 200° to 250°C for about 1 to 10 hours. The reaction is carried out in an inert atmosphere, e.g., nitrogen, at atmospheric pressure. The poly(aryl sulfone) may be recovered by conventional techniques such as coagulation and solvent evaporation. The resultant polymers have reduced viscosities in the range from 0.4 to 1.5 dl/g, as measured in N-methylpyrrolidone at 25°C. The other component of the blend is a polyamide-imide that contains an isopropylidene group. The isopropylidene group is critical to the miscibility of the blend constituents of this invention. Polyamide-imides are characterized by the presence of the phthalimide structure in the polymer backbone: The polyamide-imides which are suitable for use in this invention comprise those containing the following repeating units: wherein X 4 , x 5 , X 6 , U, V and W are as defined above. The preferred polyamide-imides also comprise those having the following recurring units: and Polyimides may be made by methods well known in the art such as those described in U.S. Patent No. 4,713,438. They are preferably prepared by the reaction of a dianhydride (or mixture of dianhydrides) with a diamine (or mixture of diamines) in substantially equimolar amounts in a solvent followed by chemical dehydration of the intermediate poly(amide-acid), hereafter referred to as Method B. Preferred dianhydrides include 1,2,4,5-benzene tetracarboxylic anhydride (PMDA), bis(4-phthalic anhydride) 1-methylethylidene (IPAN), 3,3',4,4'-biphenyltetracarboxylic anhydride (BPDA), 3,3',4,4'-diphenylether tetracarboxylic anhydride (OPAN) and 3,3',4,4'-benzophenone tetracarboxylic anhydride (BTDA). Preferred diamines include 4,4'-(1-methylethylidene)bisaniline (BAA), 4,4'-[1,4-phenylene bis (1-methyl ethylidene)] bisaniline (BAP), bis(4-amino phenoxy-4-phenyl) 1-methylethylidene (BAPP), 4,4'-diaminodiphenylether (OBA), and 1,3-diaminobenzene (MPD). The solvents useful in the solution polymerization process for synthesizing the polyamide-acid compositions are the organic solvents whose functional groups do not react with either of the reactants (the diamines or the dianhydrides) to any appreciable extent. In addition to being inert to the system, and preferably, being a solvent for the polyamide-acid, the organic solvent must be a solvent for at least one of the reactants, preferably for both of the reactants. The normally liquid organic solvents of the N,N-dialkylcarboxylamide class are useful as solvents in the process. The preferred solvents are the lower molecular weight members of this class, particularly N,N-dimethylformamide and N,N-diethylacetamide. Other useful solvents are N,N-diethylformamide, N,N-diethylacetamide, N,N-dimethylmethoxyacetamide and N-methyl caprolactam. Other solvents which may be used include dimethylsulfoxide, N-methyl-2-pyrrolidone, tetramethyl urea, pyridine, dimethylsulfone, hexamethylphosphoramide, tetramethylene sulfone, formamide, N-methyl-formamide, butyrolactone and phenols such as m-cresol. The solvents can be used alone, in combinations, or in combination with poorer solvents such as benzene, benzonitrile, dioxane, xylene, toluene and cyclohexane. Another group of solvents that are very useful for the preparation of polyimides as well as of poly(amide-imides) are the diaryl sulfones and diaryl ketones; they may be used alone or in combination with other solvents such as the hydrocarbons, chlorinated hydrocarbons, etc. Typical representatives are diphenyl sulfone and benzophenone. These solvents are of interest because they allow for the use of high temperatures and are, therefore, adequate in cases where the amine reaction reactivity is low; or in cases where low solubility of the polymer is encountered. In both instances, use of higher reaction temperatures may be necessary. Also, the thermal cyclization of the poly(amide-acids) to the corresponding polyimides can be performed in the same solvent by simply increasing the temperature to the required level. The same is feasible with phenolic solvents such as the cresols; the diaryl sulfones and ketones have the added advantage of low toxicity, however. For most combinations of diamines and dianhydrides falling within the definition given above, it is possible to form compositions of 100% poly(amide-acid) by conducting the reaction below 100°C. However, temperatures up to 175°C and higher may be tolerated to provide shapeable compositions. The degree of polymerization of the poly(amide-acid) is subject to deliberate control. The use of equal molar amounts of the reactants under the prescribed conditions provides poly(amide-acids) of high molecular weight. The use of either reactant in large excess limits the extent of polymerization. In addition to using an excess of one reactant to limit the molecular weight of the poly(amideacid), a chain terminating agent such as phthalic anhydride may be used to "cap" the ends of the polymer chains. Typical useful capping agents are less than 5 wt. % of monoanhydrides or monoamines such as phthalic anhydride, aniline, p-methylaniline, and the amine and anhydride shown below: and In the preparation of the poly(amide-acid), it is desired that the molecular weight be such that the inherent viscosity of the polymer is at least 0.1, preferably 0.3-1.5. The inherent viscosity is measured at 25°C at a concentration of 0.5% by weight of the polymer in a suitable solvent such as N-methylpyrolidone. The quantity of organic solvent used in the process need only be sufficient to dissolve enough of one reactant, preferably the diamine, to initiate the reaction of the diamine and the dianhydride. It has been found that the most successful results are obtained when the solvent represents at least 60% of the final solution. That is, the solution should contain 0.05-40% of the polymeric component. The second step of the process is performed by treating the poly(amide-acid) with a dehydrating agent, alone or in combination with a tertiary amine, such as acetic anhydride or an acetic anhydride-pyridine mixture. The ratio of acetic anhydride to pyridine can vary from just above zero to infinite mixtures. In addition to acetic anhydride, lower fatty acid anhydrides and aromatic monobasic acid anhydrides may be used. The lower fatty acid anhydrides include propionic, butyric and valeric. The aromatic monobasic acid anhydrides include the anhydride of benzoic acid and those of the following acids: o-, m-, and p-toluic acids; m- and p-ethyl benzoic acids; p-propyl benzoic acid; p-isopropyl benzoic acid; anisic acid; o-, m- and p-nitro benzoic acids; o-, m-, and p-halo benzoic acids; the various dibromo and dichloro benzoic acids; the tribromo and trichloro benzoic acids. Tertiary amines having approximately the same activity as the preferred pyridine can be used in the process. These include isoquinoline, 3,4-lutidine, 3,5-lutidine, 4-methyl pyridine, 3-methyl pyridine, 4-isopropyl pyridine, N,N-dimethyl benzyl amine, 4-benzyl pyridine, and N,N-dimethyl dodecyl amine. These amines are generally used from 0.3 to equimolar amounts with that of the anhydride converting agent. Trimethyl amine and triethylene diamines are much more reactive, and therefore are generally used in still smaller amounts. On the other hand, the following operable amines are less reactive than pyridine; 2-ethylpyridine, 2-methyl pyridine, triethyl amine, N-ethyl morpholine, N-methyl morpholine, diethyl cyclohexylamine, N,N-dimethyl cyclohexylamine, 4-benzoyl pyridine, 2,4-lutidine, 2,6-lutidine and 2,4,6-collidine, and are generally used in larger amounts. Dehydration of the poly(amide-acid) to form the polyimide, that is imidization, can also be performed by heating the poly(amide-acid) solution to temperatures at or above 200°C at reflux to remove the water which is a byproduct of the reaction. Additionally, a catalyst, such as p-toluenesulfonic acid, and/or an azeotroping agent, such as monochlorobenzene, can be added to assist the thermal imidization. A novel class of solvents for the polymerization of imide containing polymers are the poly(arylsulfones) of the present invention. The combination of the diamines and dianhydride can be added to the molten poly(arylsulfone) at temperatures between 200° and 400°C; preferably between 300° and 380°C. While not generally considered solvents for the poly(amide-acid) intermediates, these poly(arylsulfones) are by virtue of being miscible true solvents for the imide containing polymers. However, because the reaction between the aromatic amine and anhydride end groups takes place at such high temperatures, the amide-acid intermediate is never formed and thus the poly(arylsulfone) performs all of the desired functions of a good solvent including solubilization of the reaction product. Because of the relatively high viscosity of the resulting solution, the reaction can be best accomplished in an extruder or other device capable of conveying viscous polymer solutions. Such devices are known in the art and are described in any good text on polymer processing such as J. L. Throne, "Plastics Process Engineering," Marcel Dekker, New York, 1979, hereby incorporated by reference. The extruder or other device should preferably be vented to provide for the removal of the by products (water) of the reaction. This process has several advantages. Firstly, because the processing takes place above 200°C, imidization occurs spontaneously and not in a separate step after the formation of the poly(amide acid). Secondly, the solvent (i.e., the poly(arylsulfone)) does not have to be removed via a recovery step after the polymerization is complete. Lastly, the blend is formed in situ and not during a subsequent compounding step. The elimination of these three intermediate steps results in considerably better economics. The resulting imide containing polymers can be homopolymers, random copolymers, and block copolymers. They have reduced viscosities as measured in N-methylpyrolidone at concentrations of 0.5% by weight at 25°C between 0.1 and 1.5 dl/g and higher. The polyamide-imides of this invention may be made by methods well known in the art such as those described in U.S. Patent No. 4,713,438. The preparation of the poly(amide-imides) is preferably performed using reactions that are similar to those discussed for the preparation of polyimides. This method of preparation will be referred to as Method C. Typically a tricarboxylic acid monoanhydride or derivative thereof is reacted with a diamine (or mixture of diamines) as shown below and as described in, for example, Japanese Patent Application Nos. 61/126,136 and 61/126,137. Preferred tricarboxylic acid monoanhydride derivatives include 1,2,4-benzenetricarboxylic anhydride and 1,2,4-benzenetricarboxylic anhydride acid chloride. The preferred diamines include those described for the polyimides. Typical aprotic solvents which are the same as those used for polyimides, e.g., N,N-dimethylacetamide or N-methylpyrrolidone are useful. In another embodiment, these polymers can be prepared via the reaction of diisocyanate and tricarboxylic acid monoanhydride. The reaction is base-catalyzed. See for example, Japanese Patent Application No. 61/14,218. It is illustrated below: Experimental details are generally the same as those described for the corresponding preparation of polyimides. The resulting polyamide-imides of the instant invention can be homopolymers, random copolymers, and block copolymers. They have reduced viscosities as measured in N-methylpyrrolidone at concentrations of 0.5% by weight at 25°C between 0.1 and 1.5 dl/g and higher. Not all blends containing the components mentioned above are miscible. However, a novel way has been determined to select those that are miscible with each other. It has been determined that the miscibility factor for the components must be negative for the components to be miscible and to form a polymer with a single glass transition temperature. As mentioned previously, polymer miscibility cannot be predicted. There is recent evidence that once several examples are found where polymers of a class 1 are miscible with polymers of a class 2, then the phase behavior of blends of polymers of class 1 and polymers of class 2 can be correlated with structure. The net result is that a mathematical inequality can be written which correctly predicts when other polymers chosen from class 1 and class 2 are miscible. There is evidence that the miscibility of two polymers composed of several different types of mer units can be correlated by an equation of the type: where F C is a small positive number (or zero), the K are related to the number of mers of type i in polymer K, and the B ij represents the interaction energy between mers of type i and j. A mer is a small substructual component of a polymer repeat unit. For example, in Paul, et al., Polymer 25, pp. 487-494 (1984), the miscibility of the polyhydroxy ether of bisphenol A is successfully correlated with a series of aliphatic polyesters using (equation 10 in the above reference). 0 > B 13  1 ' + B 23  2 ' - B 12  1 ' 2 ' Equation (2) is equivalent to equation (1) if the following change of notation is made: F C = 0 1  ' 1 =  1 1  ' 2 =  1 2  2 3 = 1 and all other  K i = 0. In this case, the  K / i are taken to be the volume fraction mer i in polymer K. The B ij were essentially taken as adjustable parameters representing the enthalpy of interaction between group i and j. Paul and coworkers considered the polymer blend system to be made up of three groups, or mers: (i) -CH 2 - and (ii) which make up the aliphatic polyesters, and (iii) which makes up the polyhydroxy ether. Kambour, et al, Macromolecules, 16, pp. 753-757 (1983) used a similar equation to correlate the miscibility of poly(styrene-co-bromostyrene) with poly(xylenyl co-bromoxylenyl-ether). In the case where polymer 1 contained only mers of type i and polymer 2 contained mers of type j and k, the condition of miscibility that is arrived at is (see equation 4 on page 756 of the above cited work): x C AB > (1- x c )x ij + x c (x ik ) - x c (1- x c )x kj Note the mistake in the third term of equation 4 in Kambour, et al, which is corrected in equation (3) above. Equation (3) is seen to be identical with equation (1) if the following change of notation is made: F c = x C AB x c =  2 j (1- x c ) =  2 k  1 i = 1 All other  K i = 0 x ij = B ij for all i & j. In this instance, Kambour has taken the  k / i to be the mole fraction mer i in polymer K. Again the B ij were taken to be adjustable parameters. There is a precedent, then, for correlating miscibility using equation (1). We have seen that the  k / i may be interpreted as volume fractions or mole fractions. Prausnitz, et al, in the Properties of Gases and Liquids, Third Edition, published by McGraw Hill Book Co., New York, N.Y. (1977), recommend the use of molecular area fractions in equations similar to equation (1) (See Chapter 8 in Frausnitz, et al). They recommend the use of the group contribution method developed by A. Bondi in the Physical Properties of Molecular Liquids, Crystals and Glasses, Chapter 14, published by John Wiley and Sons, New York, N.Y. (1968), for the estimation of the surface area of mer units. It has been found that when poly(aryl sulfones) are miscible with imide containing polymers, the miscible blend comprises separately made biphenyl containing polysulfones with isopropylidene based polyamide-imides formed into an intimate moldable mixture by physical methods such as melt extrusion. Miscible combinations have been correlated for poly(aryl sulfone) and polyamide-imide alloys. It is highly probable that they will be miscible if the Miscibility Factor (MF) defined by the following equation is less than 0.05: where  ℓ / K is the area fraction mer K in polymer ℓ(ℓ = 1 (PAES), 2(PAI)). The mers are chosen from the list in Table I where their estimated molar surface areas are also given. The miscibility factor in Equation (4) may be thought of as a function of the composition of the PAES, designed by  1 / 1,  1 / 2,  1 / 3, . . .  1 / m, and the PI or PAI, by  2 / 1,  2 / 2,  2 / 3, . . .  2 / n. If this function is less than 0.05, polymers 1 and 2 will be completely miscible. If this function is greater than 0.05, then polymers 1 and 2 will be for all practical purposes immiscible. Of course, when this function is near 0.05 then polymer 1 and 2 are likely to be partially miscible. The quantity  ℓ / K may be calculated if the mole fractions of the various mers in polymer ℓ are known. If X i is the mole fraction mer i in polymer ℓ, then  ℓ k = XA k' ΣXA i where A i is the molar surface area of mer i (given in Table I) and the sum is over all types of mers which are given in Table I. The blends of this invention are miscible. Preferably, the blends of this invention are miscible in all proportions. Preferably, the blends contain from about 2 to about 98, more preferably, the blends contain from about 15 to about 85 weight % of the poly(aryl sulfone), the balance being the polyamide-imide constituent. The individual concentrations are readily chosen by those skilled in the art. The blends of this invention are prepared by conventional mixing methods. For example, the polymer components are mixed with each other and any other optional ingredients in powder or granular form in an extruder. The mixture is extruded into strands. The strands are chopped into pellets; the pellets are molded into the desired article. Additives which may be used with the thermoplastic alloy include reinforcing and/or non-reinforcing fillers such as wollastonite, asbestos, talc, alumina, clay, mica, glass beads, fumed silica, gypsum, graphite powder, molybdenum disulfide; and reinforcement fibers such as aramid, boron, carbon, graphite, and glass. Glass fiber is the most widely used reinforcement in the form of chopped strands, ribbon, yarn, filaments, or woven mats. Mixtures of reinforcing and non-reinforcing fillers may be used, such as a mixture of glass fibers and talc or wollastonite. These reinforcing agents are used in amounts of from about 10 to about 80 weight percent, whereas the non-reinforcing fillers are used in amounts of up to 50 weight percent. Other additives include stabilizers, pigments, flame retardants, plasticizers, processing aids, coupling agents, lubricants and mold release agents . These additives are used in amounts which achieve the desired result. A particularly useful additive, especially when either of the blend constituents contains a carbonyl linkage, is a hydrate such as that described in EP-A-376 347 corresponding to US-A-4 963 627 entitled Injection Moldable Blends of Poly(Etherketones) and Poly Amide-Imides to Smyser et al. Examples The following examples serve to give specific illustrations of the practice of this invention but are not intended to limit the scope of this invention. They are exemplary, not exclusive. The examples show the unexpected discovery noted above. Table II compiles the polymers used in the following blending experiments along with their structures in terms of  K / 1,  K / 2 . . .  K / 7. Example 1 A 50/50 blend of PAES-I (Radel® R5000 obtained from Amoco Performance Products, RV = 0.56 dl/g as measured in 0.5% N-methylpyrrolidone (NMP) solution at 25°C) and PAI-I, as defined in Table II, (I.V. = 0.90 dl/g as measured in 0.5% NMP solution at 25°C) are melt mixed in a Brabender mixing head at 360°C and 50 RPM for five minutes. The blend is compression molded into a 101 x 101 x 0.5 mm (4x4x0.02 inch) plaque at about 350°C. The molded plaque is observed to be transparent with low haze. The plaque is tested for tensile strength, 1% secant modulus and elongation at break according to a procedure similar to ASTM D-638. The pendulum impact strength of the plaque is also measured. Pendulum impact strength is measured as follows. A steel pendulum is used, cylindrical in shape with a diameter of 21 mm (0.83 inch) and weighing 7.085 kg (1.562 pounds). The striking piece, mounted almost at the top of the pendulum, is a cylinder 7.6 mm 0.3 inch in diameter. Film specimens, 101 mm (4 inches) long, 3.17 mm (0.125 inch) wide and about 25.4 to 762 µm (1 to 30 mils) thick are clamped between the jaws of the tester so that the jaws are spaced one inch apart. The 3.17 mm (0.125 inch) width of the film is mounted vertically. The pendulum is raised to a constant height to deliver 34,5 cm (1.13 foot) pounds at the specimen. When the pendulum is released, the cylindrical striking piece hits the specimen with its flat end, breaks the film, and travels to a measured height beyond. The difference in the recovery height (i.e., the difference in the potential energy of the pendulum at the maximum point of the upswing), represents the energy absorbed by the specimen during the rupture. The impact strength, expressed in foot-pounds per cubic inch (= 0.0827 Nm/cm 3 ), is obtained by dividing the pendulum energy loss by the volume of the specimen. The modulus-temperature and resilience-temperature relationship for the blend is determined using an Instron testing device equipped with a sample chamber capable of being heated to 400°C at 1.6°C/min. From this information, the (Tg or Tgs) of the blend is (are) extracted as the minimum (minima) in the resilience-temperature curve at a strain rate of 0.2 inches (= 5.08 mm)/minute. See the discussion in Olabisi et al, Polymer-Polymer Miscibility, pp. 126-127, Academic Press, New York (1979), for a discussion of the modulus-resilience method. The results of the testing are shown in Table III. Example 2 (Comparative) Example 1 is repeated except PAES-II (Victrex® PES-200P obtained from ICI Americas RV = 0.5 dl/g as measured in 0.5% NMP solution at 25°C) is substituted for PAES-I and the composition is 60/40 PAES-II/PAI-I. The molded plaque is translucent with noticeable haze. The results of the testing are given in Table III. Example 3 (Comparative) A 50/50 blend of PAES-III (Udel® P-1700 obtained from Amoco Performance Products, RV = 0.5 dl/g as measured in 0.5% CHCl 3 solution at 23°C) and PAI-I is made by dissolving 3 grams of each in NMP to make a 10% solution. It is coagulated into an 80/20 water/methanol mixture and filtered. The filtrate is reslurried in water and boiled for 5 hours, refiltered, and dried. The dry cake is compression molded as in Example 1. Its Tgs are determined as in Example 1 and are given in Table III. Controls A, B, C and D PAES-I, PAES-II, PAES-III, and PAI-I are compression molded at about 350°C. The moldings are tested as in Example 1. The results of the testing are given in Table III. As can be seen, the blend of PAES-I and PAI-I is miscible by virtue of its intermediate single Tg and transparency. Conversely, blends of PAES-II or PAES-III with PAI-I are seen to be immiscible as two Tgs are detected and by virtue of the poor optical properties of the blends. Example 4 A 50/50 blend of PAES-I and PAI-II (I.V. = 0.25 dl/g as measured in 0.5% NMP solution at 25°C) is melt homogenized in a Brabender mixing head at 360°C and 50 rpm. The blend is molded and tested as in Example 1 with the exception that the Tg is determined using a Polymer Laboratories DMTA operating in tensile mode at 10 Hz and scanning at 5°C/min. The Tg is taken as the maximum in the tan δ curve. The results are given in Table III. The molding is transparent with little haze. Example 5 (Comparative) A 50/50 blend of PAES-III and PAI-II is melt homogenized in a Brabender mixing head at 360°C and 50 rpm. The blend is molded and tested as in Example 4. The results are given in Table III. The molding is translucent with significant haze. Example 6 (Comparative) A 50/50 blend of PAES-IV (RV = 0.92 as measured in a 1% NMP solution at 25°C) and PAI-II is melt homogenized in a Brabender mixing head at 360°C and 50 rpm. The blend is molded and tested as in Example 4. The results are given in Table III. The molding is translucent with considerable haze. Controls E and F PAI-II (I.V. = 0.79 dl/g as measured in 0.5% NMP solution at 25°C; same as used in Example 4, except solid state advanced to a higher MW) and PAES-IV are compression molded into 101 x 101 x 0.5 mm (4x4x0.20 inch) plaques at 360°C and tested as in Example 4. The results are given in Table III. Examples 7 through 19 The phase behavior of the blends of Examples 1 through 6 are summarized in Table V. Further, the phase behavior of several additional 50/50 blends of various poly(aryl sulfones) with various polyamide-imides are also summarized in Table V as Examples 10 through 35. The blends are made by the same methods used to prepare Examples 1 through 6, except where noted. The blends are compression molded and the Tg(s) of the moldings are determined by a) modulus/resilience, b) DMTA or c) DSC. The blends are judged to be miscible (immiscible) on the basis of one (two) Tg(s) existing between (similar to) those of the constituents. Only poly(aryl sulfones) containing biphenyl linkages are found to be miscible with polyamide-imides. Thus, biphenyl linkages in the poly(aryl sulfone) appear to be necessary. Further, the polyamide imides all contain an isopropylidene group. Imide groups in conjunction with isopropylidene groups also appear to be necessary as no polyamide-imide not containing an isopropylidene linkage is found to be miscible with a poly(aryl sulfone). The required proportions of biphenyl linkages in the PAES and isopropylidene linkages in the PAI are determined by Equation 4. If the Miscibility Factor is less than 0.05 then the blend will very likely be miscible in all proportions. If the Miscibility Factor is very near 0.05, a borderline case exists and the blend may be miscible or immiscible, or most likely partially miscible. Finally, if the Miscibility Factor is greater than 0.05 then the blend will very likely be immiscible and not within the scope of this invention. The last column in Table V gives the value of the Miscibility Factor calculated for the particular polymer combination given in columns 2 and 4. As can be seen, the Miscibility Factor is less than or equal to 0.05 in every miscible example. Likewise, the Miscibility Factor is greater than or equal to 0.05 in every immiscible example. Note that when the Miscibility Factor is equal to 0.05, then the Example may be miscible (Example 15), or partially miscible (Example 13). Thus the deviation of the Miscibility Factor from the value of 0.05 is a measure of the blend compatibility. Example 20 A 50/50 blend of PAES-I (RADEL® R5000 obtained from Amoco Performance Products, Inc.) and PAI-II (I.V. = 0.30 dl/g as measured in 0.5% NMP solution at 25°C) is made in a one inch single screw (L/D = 36) extruder at about 350°C. The extrudate is chopped into pellets, dried to remove absorbed moisture and injection molded at about 340°C into ASTM test specimens. The molded blend is tested as shown in Table VI. Example 21 (Comparative) A 50/50 blend of PAES-II (Victrex® 200P obtained from I.C.I. Americas, Inc.) and PAI-II (same as in Example 20) is made and tested as described in Example 20. The results are given in Table VI. Controls J and K Pellets of the PAES-I and PAES-II of Examples 20 and 21 are injection molded and tested in Example 20. The results are given in Table VI. Examples 20 and 21 clearly depict the advantages of miscible blends over immiscible blends. For example, consider heat distortion temperature (HDT). PAES-I and PAES-II have similar Tgs and heat distortion temperatures (214°C for PAES-I and 224°C for PAES-II). Blending each with PAI-II to make a 50% blend resulted in the increase in HDT depicted in Table VII. Recall that PAES-I is miscible with PAI-II (See Table V, Example 4) while PAES-II is immiscible with PAI-II (See Table V, Example 15). Thus, it is seen that miscibility resulted in a substantial increase in HDT while immiscibility resulted in very little. Comparing Examples 20 and 21, it is also seen that miscibility produced a substantial benefit in toughness. The miscible blend (Example 20) has significantly higher elongation at break, tensile impact strength, and unnotched Izod than their immiscible counterpart (Example 21) even though these values for the two controls (J and K) are almost identical. The improvement in environmental stress rupture resistance (chemical) is also dramatic. Tensile bars of controls J and K and Examples 20 and 21 are loaded in flexure to an outer fiber stress of 20.685 MPa (3000 psi). Methylethylketone (MEK) is applied to the surfaces. MEK is a common ingredient of paint thinners. The times required for the bars to rupture are given in Table VIII. Note that both controls are rapidly attacked by MEK and that the immiscible blend is not significantly better. The miscible blend of PAES-I and PAI-II, however, is unaffected by MEK for an extended period of time. EFFECT OF MISCIBILITY ON HDT Example Example 20 Example 21 (Miscible) (Immiscible) -50% PAI-II- Composition 50% PAES-I 50% PAES-II Increase in HDT °C over PAES Component 10 -1 CHEMICAL RESISTANCE Control J Control K Example 20 Example 21 Composition PAES-I PAES-II 50% PAES-I 50% PAES-II 50% PAI-II 50% PAI-II MEK at 23°C and 20,685 MPa (3000 psi) Rupture after 5 min. Immediate Rupture No effect after 24 hrs. Immediate Rupture

Claims: A miscible blend of a poly(aryl sulfone) and a polyamide-imide comprising: (a) poly(aryl sulfone) containing the following unit: and (b) polyamide-imide containing the following unit: The miscible blend according to claim 1, wherein the poly(aryl sulfone) comprises units of the following structure: in the molar ratios given by m 1 ... m 7 , wherein m 1 ... m 7 are between 0 and 1, with the proviso that m 2 and m 4 are not equal to 0, said units being connected by oxygen, and the polyamide-imide comprises units of the following structure: in the molar ratios given by n 1 ... n 7 , wherein n 1 ... n 7 are between 0 and 1 with the proviso that n 3 and n 6 are not equal to 0. The miscible blend according to claim 1, wherein the poly(aryl sulfone) contains at least one of the following recurring units or comprises polymers or copolymers having at least one of the following recurring units: The miscible blend according to claim 1, wherein the polyamide-imide contains at least one of the following recurring units: A process for producing a miscible blend of biphenyl containing poly(aryl sulfone) and isopropylidene and imide containing polymer comprising adding the monomers used to form the latter polymer to the poly(aryl sulfone) in a vented extruder. The process according to claim 5, wherein the monomers are an essentially stoichiometric mixture of a dianhydride and diamine, wherein at least one of the monomers contains an isopropylidene linkage. The process according to claim 6, wherein less than 5 wt.% of monoanhydride or monoamine are added to control molecular weight.

Inventors: BROOKS GARY THOMAS, HARRIS JAMES ELMER, BROOKS, GARY THOMAS, HARRIS, JAMES ELMER
Applicants: AMOCO CORP, AMOCO CORPORATION
Application year: 1989
Main classification: C08L81
IPC codes: C08L81, H05K1, C08L79