WHOLLY AROMATIC POLYESTERS OF ISOPHTHALIC ACID, TEREPHTHALIC ACID, p-HYDROXYBENZOIC ACID, HYDROQUINONE AND AN ARYLENE DIOL

Abstract: Aromatic polyesters based on isophthalic acid, terephthalic acid, p-hydroxybenzoic acid, hydroquinone and an arylene diol are described. The five monomers are used in well-specified proportions and yield polymers that display an excellent overall combination of mechanical and thermal properties. The subject copolyesters have melting points of at least about 260 DEG C; their heat distortion temperatures are at least about 200 DEG C. They have fiber ratings of up to 3. The novel polymers can be melt-fabricated using standard injection moulding, extrusion and melt-spinning techniques.

Description: WH TIΥ A O ATTC POLYESTERS OF TSOPHTW AT τ f AΓTΠ TEREPHTHALIC ACID. P.HYDRθXYBFN7nτr Agp, HYDROOUINONE AND AN A YLENF. T_TOT CROSS REFERENCE TO RELATED APPUCATTON Thia application it a Continuation-In-Part of U.S. Patent Application, Serial No. 255,670 FUtd October 11, 1988, and a Continuation-In-Part of USSN 07/317,525, filed March 1, 1989. FTPrn nFTHE Aromatic polyesten baaed on isophthalic acid, terepfatfaalic add, p-hydroxybehzoic add, hydroquinooe and an arylene ώol are described. The five monomers are used in well-specified proportions and yield potymeπ that display an excellent ovenU combination of mechanical and thermal properties. The subject copdyeaiers have melting points of at least about 260° C; their heat distortion temperatures an at least about 2(X_* C They have fiber ratings of up to 3. The novel polymers can be melt-febricased using standard injection molding, extrusion and melt-spinning techniques. BACKGROUND OPTM INVENTION Wholly aromatic pctyesβr resins have long been known. For instance, 4-hydroxybenzoic add homopotymer and copoiymeπ have been provided in the past and are commexcially available. Such potymeπ are commonly αystalline in nature, relatively high-mehing or possess a decomposition trmpenmre which is below die melting point, and when molten frequently exhibit orientation in the men. The boraopoiymer of p-hydraxybenaoic add is a vety high-melting, insoluble material and, hence, vety difficult β fabrics*. Melting points as high as 610* C were quoted • see W.J. Jackson, The Bririih Poi v __τ lotm i December 1980, p. 155. In order to depress the high melting point of the homopoiytner so as β make it mefc-tώricable, a variety of materials incorporating different types of comonomers were prepared over the years. One such material is, for example, d e resin made from p-hydroxybenaoic acid (PHBA), isophdulic (1A) and or terephthalic adds (TA), and 4,4'-biphenol (BP) as described in, for example, Coras et al., U.S. Patent Nos. 3,637,595 and 3,975,487. The polymer has outstand high-temperature properties; it can be molded to give articles of high modulus and strength. It offered commercially by Amoco Performance Products, Inc. under the tradename of XYDAR Due to the use of PHBA and BP, these polymers can be expensive. A related class of wholly aromatic polyesters based on p-hydroxybenzoic acid, isophth and terephthalic acids, and hydroquinone (HQ) is claimed in commonly assigned U.S. Patent Application entitled "Hydroquinone Poly (Iso-Terεphthalates) Containing Residues of p- Hydroxybenzoic Acid," Serial No. 07/255,670, filed in the names of R. Layton et al., on Octo 11, 1988, which is hereby incorporated by reference. The polymers described in the latter application display high modulus and high strength; they have melting points in the range of fr 3 0°C to 400°C, are melt-processible, and show orientation in the molten state. Compositions filled with about 30 weight percent of glass fibers display heat distortion temperatures (HDTs) about 240° C to about 280°C, when measured under a load of 264 psi. While the overall combination of properties of the above resins is outstanding compare prior art wholly aromatic polyesters based on p-hydroxybenzoic acid, benzene dicarboxylic aci and hydroquinone, they are preferably used in blends with polyesters made from p- hydroxybenzoic acid, isophthalic and terephthalic acids and 4,4'-biphenoi to facilitate moldabil and minimize blistering of large molded parts. In addition, these novel blends display improve mechanical properties; composites containing 30 weight percent of glass fibers show heat distortion temperatures (under a load of 264 psi) of at least 240° C. The subject b.lends are clai in commonly assigned U.S. Patent Application of P. Huspeni et al., entitled "Polymer Compositions Having Improved Molding Characteristics," Serial No. 07/255,632, filed on October 11, 1988. These cases are hereby incorporated by reference. Also, we filed concurrently herewith two applications to heat resistant and high-strengt polymers and blends of hydroquinone poly (Iso-Terephthalates) containing residues of p- hydroybenzoic add by R. Layton et al. which are a Continuation-In-Part of USSN's 255,670 255,632 filed October 11, 1988, our case Nos. 29723 and 29724. These polymers and blends have good mechanical properties, good fiber ratings and ability to vapor phase solder. We considered that if it is possible to incorporate many or all of the desirable properties blend into a single polymer in order to avoid produdng two different polyesters, it would be desirable. We have now found that wholly aromatic polyesters based on five components, i.e., p hydxoxybenzoic acid, isophthalic and terephthalic acids, hydroquinone, and an arylene diol su 4,4-biphenol, for example, used in specified proportions, display excellent mechanical propeπies good moldability, high melting points, high HDTs, good fiber ratings, and yield molded parts having very good surface characteristics. The present discovery was surprising since with some known exceptions, blends of polymeric materials are generally different from polymers. They are immisdble, that is, they consist of domains of chemically distinct phases. Usually, one component forms a continuous phase, while the other component forms roughly spherical domains as inclusions. Under some circumstances, bi-continuous structures are also obtainable. Hence, a blend of two polymers is usually a two-phase system whose properties reflect those of both phases present. On the other hand, a random copolymer is a one-phase material wherein the properties of the constituents are averaged. Thus, a copolymer is expected to be quite different from a two-phase blend. Even if th monomers employed to make the component polymers of the blend were to be the same as those employed to make the corresponding random copolymer, one would not expect similar characteristics for the two systems. In addition, the known prior an suggests that one would not be able to find any useful materials in the compositional region of the instant invention. In fact, th prior an teaches away from the compositional ranges of the current invention. As indicated in application Serial No.07/255,670 filed October 11, 1988 by R., Layton et. al. and assigned to Amoco Inc., the prior an has been unsuccessful in replacing biphenol with hydroquinone without sacrificing properties and/or using expensive comoαomers. While various references discussed below have suggested employing mixtures of hydroquinone and a second arylene diol, none of these describe the polymers of this invention. Dicke et al., U.S. Patent No. 4,603,190, claim five component copolyesters based on terephthalic add, isophthalic add, p-hydroxybenzoic a id, hydroquinone and 4,4'-biphenol wherein the terephthalic acid to isophthalic add ratio is equal to or less than one. The polymers display Vicat B temperatures of about 130°C to about 150°C which translate into even lower HDTs. Polymers with such low Vicat B temperture would be of no interest in applications whic require dimensional stability at high temperatures (eg. equal to or greater than about 200°C). Portugall et al., U.S. Patent No.4,7 1,128, claim five similar component polyesters wherein the molar ratios of terephthalic to isophthalic adds vary from 1.04: 1 to 19: 1; and wherei the hydroquinone to 4,4'-biphenoi molar ratios are in the range of 0.1 : 1 to 2.67 : 1. The copolymers appear to have a satisfactory combination of mechanical and thermal properties with HDTs of up to 248°C. The drawback of the materials, however, is their high cost due to the rather low ratio of the inexpensive hydroquinone to the very expensive 4,4'-biphenol. In fact, U.S. Patent No. 4,751,128 suggests that there are no compositions of interest at hydroquinone t 4,4'-biphenol molar ratios greater than 2.67:1; indeed, according to the patent, it is preferred that the subject ratio be no higher than 2.33:1 (column 2, lines 24-26). ., . , , polyesters from isophthalic and terephthalic acids, p-hydroxybenzoic add, hydroquinone, 4,4'- biphenol, and, optionally, a sixth comonomer selected from 2,6-naphthalene diol, or an alkyl- o chloro- substituted hydroquinone. Once again, the mole ratio of hydroquinone to the 4,4'- biphenol is low, i.e. from 1:1 to 1:19. In fact, polymers outside of the molar percentage criteria are considered undesireable. The application discloses (p. 6) that if the mole percentage of biphenol is less than 50 mole percent (Le., the HQ/BP ratio is greater than 1:1), "the heat resista is poor" (line 9, p. 6); while if the mole percentage of biphenol is more than 0.95 mole percent (Le., the HQ/BP ratio is lower than 1:19), the resulting polymers have poor flow characteristics (See also p. 6). It is noteworthy, that copolymers with hydroquinone 4,4'-biphenol molar ratio greater than one could not be prepared since they solidified during polymerization (see lines 12- p. 14; and Table 2, p. 15). Analysis of the foregoing patents (Le. U.S. Patent Nos. 4,603,190 and 4,751,128; and European Patent Application No. 275,324) also indicates that the polyesters described therein comprise high amounts of another expensive monomer, namely, p-hydroxybenzoic add (PHB Contrary to the commonly held belief that good high-temperature properties of wholly aromatic polyesters can be achieved only at high contents of p-oxybenzoyl moieties, it was now unexpectedly discovered that materials exhibiting excellent high temperature performance can b obtained at very low PHBA contents; even at terephthalic acid to isophthalic add ratios of less t one. Coras et al., U.S. Patent No. 4,563,508, suggest the possibility of preparing copolyest from terephthalic and isophthalic adds, p-hydroxybenzoic arid, hydroquinone and 4,4'-biphen Cotύs, U.S. Patent No. 4,563,508, is directed to the iπφnggp ent of molding compounds bas on wholly aromatic polyesters by the addition of a minor amount of a flow modifier. The flow modifier crystallizes poorly and improves the flow of the highly crystallized base polymer it is added to. The flow modifier does not enhance the end properties of the blend composition. It i be noted that the addition of the flow modifier decreases the HDT of the composition and does increase die strength. The patent does not describe any compositions within the scope of this invention. In summary, therefore, the possibility of preparing polyesters from terephthalic add, isophthalic acid, p-hydroxybenzdc add, hydroquinone and an arylene diol such as 4,4'-biphe for example; with high molar ratios of hydroquinone/arylene diol [e.g. > 3: 1 and at low PHBA contents, e.g., about 0.4 to 0.6 (vide infra)]; having both the desirable thermal, mechanical and molding characteristics as hereinbelow described; and very attractive economics was surprising totally unexpected. In fact, the teachings of the prior an are contrary to our discoveries. THE INVENTION The polyesters of the instant invention are comprised of units (1) - (5) wherein Ar is a divalent substituted mononuclear aromatic radical of the formula wherein X is independently hydrogen, a C\ to C5 alkyl group, a halide atom, or an aryl group such as phenyl; with the proviso that when die valence bonds are para to each other, at least one group X must be other than hydrogen; and/or a divalent dinuclear aromatic radical of the formul wherein X is as defined above, and Q is selected from the group of 0, S, SO, S-S, SO2, CO an chemical bond; and/or a divalent naphthalene radical of the formula or isomers thereof. In the formulae (1) - (5) a + b is approximately equal to d + e; the ratio of a t b is in the range of about 1.4:1 to about 10:1, preferably about 1.5:1 to about 5:l; the ratio of d to is from about 3:1 to about 21:1, preferably from about 3.5:1 to about 20:1; and c is in the range o from about 0.6 to about 7, preferably from about 0.7 to about 4, moles per each mole of monomers corresponding to the sum of units (1) and (2). It was also unexpectedly discovered that very attractive properties are realized with polyesters comprising the units (1) - (5) wherein a + b is approximately equal to d + e; the ratio o a to b is in the range of from about 0.42:1 to about 2.33:1, preferably from about 0.75:1 to about 2:1; the ratio of d to e is in the range of from about 3:1 to about 99:1, preferably 5:1 to about 99:1 and more preferably from about 10:1 to about 70: 1; and c is in the range of from about 0.15 to about 0.8 moles per each mole of monomer corresponding to the sum of units (1) and (2), preferably from about 0.25 to about 0.75 moles. Arylene diols useful for the purposes of the instant invention are, for example, resorcinol methylhydroquinone, chlorohydroquinone, t-butylhydroquiπone, phenylhydroquinone, the 4,4' 4,3'-, and 3,3'-biphenols; the 4,4'-, 4,3'-, and 3,3'-dihydroxydiphenyl ethers; the 4,4'-, 4,3'-, and 3,3'-dihydroxydiphenyl sulfides; the 4,4'-, 4,3'-, and 3,3'-dihydroxydiphenyl sulfoxides; t 4,4'-, 4,3'-, and 3,3'-dihydroxydiphenyl disulfides; the 4,4'-, 4,3'-, and 3,3'-dihydroxydiphen sulfones; the 4,4'-, 4,3'-, and 3,3'-dihydroxybenzophenones; and the naphthalene diols; such as the 1,4-, 1,5-, 2,6-, and 2,7-naphthalene diols; the 4,4'-, 4,3'-, and 3,3'-biphenols are preferre The subject resins form a stable oriented melt phase at about 260°C or higher, the melt phase is tractable and can be melt-extruded below its decomposition temperature to form quality, high-performance fibers, films, molded articles, and the like. Fabricated products show a smoot surface, and a minimal tendency to blister. The polyesters display high modulus and strength, good fiber ratings, as well as good retention of properties at high temperatures. The polymers have heattdistortion temperatures of at least about 200°C, preferably at least about 220°C when measured under a load of 264 psi. It is important to point out that melting points and heat distortion temperatures (HDTs) a basic property parameters that determine polymer performance. Thus, a very high melting point results in materials that are either difficult to melt-fabricate or plain intractable. Low melting poi lead to resins having low HDTs. For high heat applications such as ovenware, heat distortion temperaturervalues are very important since they indicate the upper temperature at which the particular polymer is useful, especially in structural applications. Other parameters are the crystallization temperature and the rate of crystallization. Both provide an indication of how quickly the_molten material develops the desirable crystallinity characteristics. The heat distortion temperatures were determined by using the ASTM method D-648. Melting points, crystallization temperatures (also referred to as the "onsets of crystallization") an the crystallization rates were measured using X-ray techniques. A brief description follows. The crystalline melting point is measured by following the intensity of the X-ray reflectio of the most intensive peak as a function of temperature. The most intensive diffraction peak is located at a spacing of about 4.5 A. Based on literature data [J. Polymer Sc , Polym. Chem. Ed 14, 2207 (1976); J. Polym. Sri., Polym. Chem. Ed., 2 2249 (1983)] the subject peak has bee tentatively assigned to the distance between the polymer chains. The point at which the intensity reaches a minimum is taken for the polymer mdt temperature. The rate of temperature change is 100°C per minute. The onset of crystallization is taken as the temperature at which there is a sharp increase i the intensity of the X-ray peak referred to above. Again, the rate of cooling is 100°C per minute. Crystallization rate is defined as the difference between the intensities of the above X-ray peak at the crystallization temperature and at 40°C below that temperature, the rate of cooling bein 100° C per minute. A detailed description of the three methods is given in the Experimental. Note that throughout this patent, all melting and crystallization data refer to the second heating/cooling cycl of the sample (see Experimental). A surprising and unexpected feature of the copolyesters of the instant invention is their ability to yield molded materials that display good surface characteristics, good fiber ratings and _ generally a lowered tendency to blister. The phenomenon of blistering has been known. Blisters may occur near a surface or in t bulk of the sample. Here, we are mainly concerned with surface blisters; note, however, that sm internal blisters or voids can also be detrimental to material performance. Moldings based on polymers that show orientation in the melt, display skin-core effects. Hence, phenomena observed in these systems are often analogous to those encountered in coatin and composites. In composites, for example, blistering and delamination occur especially betwe two layeπ of different composition. In coatings, blistering is known to be a localized delaminati at an interface; it depends on the diffusion of chemicals such as water and degradation by-produ The difference in the thermal expansion coefficient between a coating and the substrate can create stresses and may weaken the interface. A blister may then form with less pressure difference du to volatiles, than in cases where these stresses are absent. In summary thus, blistering is due to a surface layer delamination and can be caused eith by trapped volatiles or by built-in stresses. Most probably both factors are at work. Two types of blistering are encountered with polymeric materials; (1) molding blisters a (2) oven blisters. Blisters which occur during molding generally indicate the presence of degrad m . u n mo ng. However, when these parts are treated at high temperatures for a certain period of time, blisters ("oven blisters") often appear. These do not necessarily indicate the presence of degraded materi as a result of molding. It is of paramount importance that molding of the polymer does not yield parts having a blistered surface. It should be noted that the configuration of a pan is also quite often a factor in mold-blistering. In any event, if molding blisters are detected upon visual examination, the part will generally blister to a considerably greater extent when exposed to heat treatment. Thus, the particular molding compound is most probably of inadequate quality. If, on the other hand, a good-looking molding pan is obtained, there is no assurance as to what the results of "oven testing" will be. For high-temperature applications, it is imperative that oven blistering be also either absent or significantly minimi7cri. The oven test and the method of blister rating are described in the "Experimental." Astonishingly, the copolyesters of the instant invention show a decreased tendency to blister-both during molding and in the oven test. It is important to point out that the novelty of the instant invention does not reside in the u of novel monomers; the critical factor of the present invention is the discovery that polymers having a combination of outstanding characteristics can be obtained when the five monomers, L p-hydroxybenzoic add (PHBA), hydroquinone (HQ), an arylene diol, e.g., 4,4'-biphenol (BP), isophthalic acid (IA), and terephthalic add (TA), are used in the sperified ratios. Clearly, (vide supra), the existence of these, very interesting materials was neither anticipated nor predicted by t existing prior art The synthesis of the polyesters of die instant invention is described in detail in Cottis et a U.S. Patent No. 3,637,595 entided "P-Oxybenzoyl Copolyesters" and in Finestone, U.S. Paten No.4,742,149 entided "Production of Melt Consistent Aromatic Polyesters"; the disclosure of t aforementioned two patents is incorporated herein by reference. The bulk condensation of aromatic polyesters is described in the patent literature and broadly considered involves an alkanoylation step in which a suitable dicarboxylic arid, hydroxybenzoic acid and diol are reacted with an add anhydride; a prepolymerization step in whi the reaction product of the first step is polycondensed to prepare a prepolymer, and the prepolym is.thereafter heated in a third step to produce a polycondensate of the desired degree of polymerization. Thus, in somewhat greater detail, the instant copolyesters are prepared by charging into t reactor the required amounts of isophthalic and terephthalic adds, p-hydroxybenzoic acid, hydroquinone and an arylene diol such as 4,4'-biphenol. An anhydride of a lower monocarbox acid, preferably an anhydride of a C2 to C4 monocarboxylic add, is added in at least stoichiome amounts. It is most preferred to use acetic anhydride; its amount is preferably from about 5 to about 20 mole percent over that required for the acetylation of all of the hydroxyl groups. The acetylation reaction takes place at about 140°C for a period of time of from about 2 to about 6 hours. The reaction mixture is then heated to about 240°C to about 320°C at a rate of about 20° about 40°C per hour, and is kept at about 240°C to about 320°C for approximately a few minute about 4 additional hours. The low molecular weight polymer obtained is then solid state advan to the required high molecular wdght by heating to a temperature of from about 280°C to about 320°C, for a period of from about one to about 24 hours. A preferred variant as described in Finestone, U.S. Patent No. 4,742,149 comprises adding a salt, particularly an alkaline earth metal salt or an alkali metal salt, preferably potassiu sulfate, during the preparation of the resin and, particularly to the prepolymer melt prior to advancement of the final product to the desired degree of polymerization. The incorporation of stabilizing amounts of phosphites, as described in Coras, U.S. Patent No. 4,639,504 is also advantageous. The polyesters of the present invention commonly exhibit or C CH 3 - C OH end groups depending upon the synthesis route selected. As will be apparent to those skilled i the an, the end groups optionally may be capped, e.g., acidic end groups may be capped with a variety of alcohols, and hydroxyl end groups may be ped with a variety of organic adds. For instance, end capping units such as phenyl ester methyl ester optionally may be included at the end of the polymer chains. The polymers may be annealed below thrir melting points for a period of time; or the polymers may be oxidatively crosslinked to at least some degree, if desired, by heating in an oxygen-containing atmosphere (e.g., in air) while in bulk form or as a previously shaped article at a temperature below their melting points for a limited period of time (e.g., for a few minutes). The polyesters of die present invention tend to be substantially insoluble in all common polyester solvents such as hexafluoroisopropanol and o-chlorophenol, and accordingly are not susceptible to solution processing. They can surprisingly be readily processed by known melt- processing techniques as discussed hereafter. The polyesters of the present invention commonly exhibit weight average molecular weights of about 2,000 to about 200,000, preferably about 10,000 to about 50,000 and most preferably about 20,000 to about 25,000. These molecular weights are determined by techniques that do not involve solutioπing of the polymer, e.g., by end-group determination, and the like. The instant polyesters can be melt-processed in the substantial absence of polymer degradation to form a variety of relatively stiff-shaped articles, e.g:, molded three-dimensional articles, fibers, films, tapes, etc. The polyesters are suitable for molding applications and may be molded via standard injection-molding techniques commonly utilized when forming molded articles. Unlike d e polyesters commonly encountered in the prior art, it is not essential that more severe injection-molding conditions (e.g., higher temperatures), compression-molding, impact-molding, or plasma-spraying techniques be utilized. Fibers or films may be melt- extruded. In some instances, as described in Cottis et al., U.S. Patent No. 4,563,508, melt- fabrication may be facilitated by adding flow aids. Molding compounds may be formed from die subject copolyesters by incorporating therein reinforcing agents and or fillers. Representative reinforcing media include glass fibers, glass beads, asbestos, graphitic carbon fibers, amorphous carbon fibers, synthetic polymeric fibers, aluminum fibers, aluminum silicate fibers, oxide of aluminum fibers, titanium fibers, magnesium fibers, rock wool fibers, steel fibers, tungsten fibers, cotton, wool, and wool cellulose fibers, etc. Representative filler materials include calcium silicate, silica, clays, talc, mica, polytetrafluoroediylene, carbon black, graphite, alumina trihydrate, sodium aluminum carbonate; barium ferrite, wollastonite, titanium dioxide, etc These molding compounds are useful in a variety of applications; for example, in cookware articles, and the like. The polymers of this invention may contain up to 10 mole percent (based on total reactants) of carbonate linkages and/or comonomers other than (1) - (5), provided that the use o sa car onate n ages an or comonomers oes not un avorably affect die very attractive properties of the instant copolyesters, Le., (1) melt-processibility below the decomposition temperature; (2) a mdting point of at least about 260° C; (3) an HDT of at least about 200° C when measured under a load of 264 psi using the method described in ASTM D-648; and (4) the ability to form molded articles having good surface characteristics and a decreased tendency to blister. EXAMPLES The following examples serve to give specific illustrations of the practice of this invention but diey are not intended in any way to limit the scope of this invention. A, EAwrimttUal Prcwdvrss The following procedures were used to obtain die data given in the examples. .. A.l. X-rav Measurements a) Ap p aratus. X-ray diffraction data were obtained using a Philips XRG-3000 X- ray generator equipped with a vertical diffractometer, a long, fine focus copper X-ray tube, a Paar HTK-10 high-temperature dϋfractometer attachment and a Paar HTK-Hcat Controller. Diffractometer position is controlled by computer, which also measures and records radiation count rate produced by sample crystallinity and sample temperature. b) Determination of the Polv er Melting Point A sample of the polymer is submitted to a preliminaiy X-ray diffraction scan between 15 and 25 degrees two-theta angle by increasing the temperature by increments of 60°C within a temperature range from about 200 to about 480°C. This allows determination of me approximate temperature at which the peak located at approximately 19.7 degrees two-dieta (4.50 Angstroms d-spacing) reaches its minimum value, Le., an approximate melting point A second-degree polynomial equation is derived from the above data; diis polynomial equation now allows to follow the peak angle as die sample temperature is varied. The temperature at which the peak hright reaches a minimum (Le., touches d e baseline) is considered to be dre melting point The polymer sample is now heated and cooled at a rate of 100°C per minute between the previously-mentioned temperature limits, and its melting point is determined. Since the mdting pdnt of a crystalline material often changes on heating and cooling (due to recrystallization, further polymerization, etc.) the sample is coded and reheated. This allows determination of die melting point on die second ' heating cycle. Generally, die second cycle yields a mdting point which remains approximately constant if additional heating or cooling cycles are performed. Therefore, the value obtained in tive second heating cycle is taken as die polymer melting point constant a ona eat ng or coo ng cyc es are per orme . ere ore, t e va ue o ta ne n die second heating cycle is taken as the polymer melting point c) Crystallization Temperature (Onset of Crystallization). The onset of crystallization is measured in the same manner except that the scanning (for details, see above), is performed while the sample is cooled at 100°C per minute. The temperature at which the peak emerges from the baseline during the second cooling cycle is considered as the onset of crystallization. d) Crystallization Rate. At every temperature below the sample melting point, the intensity of X-ray diffraction of a crystalline material can be expressed as counts per second (or any unit of time). The increase in the number of counts per unit of time while the sample is being cooled at a certain rate (100°C per minute) is therefore proportional to the rate of crystallization. A temperature interval starting at die onset of crystallization and 40°C below that temperature was arbitrarily chosen. Rates of crystallization are expressed as the increase in counts per minute for a sample cooled within these temperature limits during die second cooling cycle. A.2. Blister Rating Samples to be tested are preconditioned at 20°C to 25° C, 50 ± 5 percent relative humidity, for 24 hours. Test sample lot normally includes 5 tensile bars (1/8" thick), 5 HDT bars (5" x 1/2" x 1/4" thick) and 5 flex bars (5" x 1/2" x 1/8" thick). The samples are carefully inspected and any existing cracks and/or blisters are circled. The samples are then annealed in an oven j Which has been equilibrated at 232° C (450°F), for a period of 4 hours. They are dien removed, cooled and inspected. Rating codes follow: 0 - no new blisters; 1 - very slight blistering (one or two very small blisters); 2 - slight blistering (three to six small blisters); 3 - moderate blistering (a few large blisters and/or many small blisters); and 4 - heavy blistering (many large or small blisters covering more than half of the specimen surface). The numerical blister rating is calculated using the equation n R = l/n ∑ X t 2 i=l where R = numerical blister rating (0-16); n = number of samples tested; and Xj = blister rating (0-4) of sample L n ie a ove ca cu a on ie n v ua rat ngs or e ent re set of test samples (tensile bars, HDT bars, flex bars) are generally treated as a single population. The ratings vary within die range of 0 (no blistering) to 16 (severe blistering, worst case). A.3 Determination of the Fiber Rating Fiber ratings were obtained using a hot bar apparatus with a temperature range from 270 to 415°C. A 2 to 5 gram sample of polymer is diinly and evenly sprinkled on die upper portion of the hot bar using a spatula and is allowed to melt Using a large pair of tweezers, grab a small portion of material from die melted pool and slowly draw a fiber at a steady speed. The following rating system is used: 0 • Material does not melt or does not draw a fiber 1 - Material draws a shon fiber with poor strength 2 - Material draws an intermediate length fiber with intermediate level of tenacity or material draws a long fiber with poor strength 3 - Material draws a long fiber with good strength L - An additional rating of L is added to the rating of 0-3 if a low melt temperature occurs which indicates low molecular wright A - An additional rating of A is added if the melted material is clear which indicates the material is amorphous in the melt state A .4 Miscellaneous The flexural strength and the flexural modulus of die experimental samples were measured according to the procedure of ASTM D-790-84A; HDT (DTUL) data were obtained using die mediod described in ASTM D-648. Example 1 This is an example of the synthesis of a novel polyester based on terephthalic acid (TA) , isophthalic arid (IA) , p-hydroxybenzoic acid (PHBA) , hydroquinone (HQ), and 4,4'-biphenol (BP) in the nominal mole ratio of 0.615/0.385/0.750/0.9/0.1 The following ingredients were combined in the manner described. - Items A through G were charged to a 15 gallon, oil-heated vessel equipped with an anchor-type stirrer, reflux condenser, after condenser, and distillate receiver. After purging widi nitrogen, the contents were heated with stirring to 141° C and held under reflux at that temperature for 3 hours. Distillation was tiien started while increasing the temperature over a 6.7 hour period to 275° C. The contents of the vessel were transferred to a sigma blade mixer that had been preheated to 305° C After mixing for 5 hours at this temperature under an atmosphere of nitrogen, the mixer was cooled to near room temperature at which point the pdymer was removed as a granular solid. The yield was 15.2 Kg (95 percent of theoretical). Examination by X-ray diffraction showed a melting temperature of 369° C, crystallization temperature of 314° C and a crystallization rate of 560 counts per minute. A sample of the polymer was pelletized and molded by standard techniques. The test specimens had a Heat Distortion Temperature of 268° C and a room temperature flexural strength of 28,000 psi and room temperature flexural modulus of 2,460,000 psi. The blister rating was excellent at 1.5. A molding composition containing 70 weight percent of the above polymer and 30 weight percent of milled glass fiber was prepared by compounding on a twin screw extruder and molded into test specimens. The heat distortion temperature (ASTM D-648) was 265° C. The room temperature flexural strength and modulus (psi) were 27,200 and 2,240,000 respectively. Com arative Exampfc \ The preparation and properties of a wholly aromatic polyester based on four components, i.e. isophthalic acidΛerephthalic acid/p-hydroxybenzoic arid/hydroquinone in the nominal mole ratio of 0.4 0.6/0.5/1.0 are described. The following ingredients were combined in a manner described: Usm frgsdfcffi Amount A B C D E F G Items A dirough F were charged into a 15-gallon, oil heated vessel equipped with an anchor-type stirrer, reflux condenser, after condenser, injection pon and distillate receiver. After purging with nitrogen, the contents were heated with stirring to 141° C and held under reflux at d at temperature for 3 hours. Distillation was dien started while increasing the temperature over a 4.8 hour period to 285° C. Item G was then injeαed into die vessel. After an additional 15 minutes he contents of the vessel were transferred to a sigma blade mixer that had been preheated to 320° C. After mixing for 4 hours at this temperature under an atmosphere of nitrogen, d e mixer was cooled to near room temperature where the contents were removed as a granular solid The melting point of die polymer (X-ray) was 359° C; its crystallization temperature was 336° C with a crystallization rate of 2400. The material was pelletized and molded into standard test specimens having a blister rating of 15. Items identified in Example 1 were the same for the following examples: 2-15 and 23- 73. The polymerization procedure was similar to that of Example 1 (except for Examples 11- 16, 18, and 31); the amounts of ingredients are shown in Tables I, π, & V Properties are listed in Table HI and V. Crystallinity data are summarized in Table IV. Examples 11 to 15 (Table Examples 11-15 use die amounts of ingredients as shown in Table II (A - G are the same monomers as Example 1). These ingredients, in the amounts shown in the table below, were charged to a 2 liter resin kettle fitted with a heating mande, mechanical stirrer, reflux condenser, and distillate take-off apparatus. The mixture was heated to reflux and stirred for diree hours. Distillation was then started and die temperature of die reaction mixture increased at die rate of 30° C per hour until approximately 97 percent of die dieorctical distillate was collected The hot mixture was then poured into an aluminum pan to cool to a brittle sheet The material was then pulverized to a granular powder fine enough to pass a 2 mm screen. The powder was heated-up slowly (22° C per hour) under nitrogen to 300° C and held for 4 hours at diat temperature o a ne even at very high HQ/BP molar ratios. Contrary to the statement of the European Patent Application EP 275,324 that at molar ratios of HQ/BP higher than 1 : 1 "the heat resistance is poor", die melting points of die copolyesters actually have a tendency to increase widi die increase of the hydroquinone content This, in turn, indicates better (not poorer) heat resistance. Also, no experimental problems were encountered in preparing the copolyesters of the instant invention. Table IV depicts die crystallinity characteristics of die polymer of Tables I and II (Examples 1-15). The data in Table V indicates that many of die materials of the present invention exhibit excellent fiber ratings In Table V, Examples 16-22 are controls or comparative examples of a polymer derived from 4 monomers. All examples in Table V (except for examples 16„ 18„ and 31) were prepared in the same monomer as Comparative Example 1. Examples 16, 18, and 31 were prepared in the laboratory using the procedure as shown for exampls 11-15. The following data clearly show that die instant five-component polyesters display excellent moldability characteristics and a generally lowered tendency to blister especially in glass-filled systems. Several of the materials listed exhibit vastly improved tensile and flexural strengths and moduli. TABLE III ■Polymer Properties of Examples from Table I HQ/BP Fle xu ral Te nsi le Ex. mole Blister Strength Modulus Strength Modulus Elongation HDT MΩ__ Description* ratio Ratine (psi) si x 10 6 ) ( si) fpsi λ lQ 6 ). (%) CO 2 Neat 19:1 8.6 12,180 1.14 6,210 1.51 0.4 220 30% glass filled 5.2 14,750 1.61 8,890 1.86 0.6 227 3 Neat 3:1 30% glass Filled 4 Neat 30% glass filled 5 Neat 30% glass filled 6 Neat 30% glass filled 7 Neat 30% glass filled 8 Neat 30% glass filled 9 Neat 30% glass filled 10 Neat 9:1 30% glass filled 0.3 Comparative Neat 8.0 16,990 1.4 6,320 1.63 0.4 245 Example 1 30% glass filled 9.6 15,670 1.83 11 ,360 2.18 0.61 268 Henr and Frick, 1/16" milled lass fiber. 1 HQ * hydroquinone; BP - 4,4'-biphenol.

Claims: WE CLAM: 24 A wholly aromatic polyester comprising the units (1), (2), (3), (4) and (5) wherein Ar comprises at least one member selected from the group consisting of I, a divalent substituted mononuciear aromatic radical of the formula wherein X is independcndy hydrogen, a C\ to C5 alkyl group, a halide atom or an aryl group; with the proviso that when the valence bonds are para to each other at least one group X must be other than hydrogen; and π, a divalent dinuclear aromatic radical of the formula wherein X is as previously defined, and Q is selected from the group consisting of 0, S, SO, S-S, SO2, CO and a chemical bond; and HI, a divalent naphthalene radical of the formula or isomers thereof, and wherein a + b is approximately equal to d + e; the ratio of a to b being in the range of from about 0.42:1 to about 2.33: 1; the ratio of d to e being in the range of from about 5:1 to about 99:1; and c being in the range of from about 0.15 to about 0.8 moles per each mole of monomers corresponding to the sum of units (1) and (2). 2. A wholly aromatic polyester comprising the units (1), (2), (3), (4) and (5) wherein Ar comprises at least one member selected from the group consisting of I, a divalent substituted mononuclear aromatic radical of the formula wherein X is independendy hydrogen, a C\ to C5 alkyl group, a halide atom or an aryl group; with die proviso diat when the valence bonds are para to each other at least one group X must be other than hydrogen; and π, a divalent dinuclear aromatic radical of the formula wherein X is as previously defined, and Q is selected from the group consisting of O, S, SO, S-S, SCb, CO and a chemical bond; and El, a divalent naphd alene radical of the formula or isomers thereof, and wherein a + b is approximately equal to d + e; the ratio of a to b being in the range of from about 1.4: 1 to about 10: 1; the ratio of d to e being in the range of from about 3: 1 to about 21 : 1; and c being in the range of from about 0.6 to about 7 moles per each mole of monomers corresponding to units (1) and (2). 3. A wholly aromatic polyester as defined in claim 1 which has a melting point of at least about 260° C, a heat distortion temperature of at least about 200° C when measured under a load of 264 psi, and which yields molded articles having good surface characteristics. 4. A process for preparing the polyesters of claim 1 which comprises reacting terephthalic acid, isophthalic acid, p-hydroxybenzoic acid, hydroquinone, and an arylene diol other than hydroquinone with an anhydride of a lower monocarboxylic acid to form a prepolymer, followed by solid state advancement of said prepolymer to die desired high molecular weight polyester. 5. A wholly aroinatic polyester as defined in claim 1 wherein the group Ar consists essentially of biphenylene. 6. A wholly aromatic polyester as defined in claim 1 wherein the group Ar consists essentially of at least one member selected from wherein Y is methyl, chlorine, t-butyl or phenyl 7. A wholly aromatic polyester as defined in claim 1 wherein d e group Ar consists essentially of at least one member selected from O— O wherein Q is 0, S, SO, S-S, SO2, CO or a chemical bond. 8. A wholly aromatic polyester as defined in claim 1 wherein the group Ar consists essentially of at least one member selected from wholly aromatic polyester comprising the units (1), (2), (3), (4) and (6) ( 1) (2) (3 ) (4) («) wherein a + b is approximately equal to d + f, the ratio of a to b being in the range of from about 1.4:1 to about 10:1; the ratio of d to f being in the range of from about 3:1 to about 21:1; and c being in die range of from about 0.6 to about 7 moles per one mole of monomers corresponding to units (1) and (2). 10. A wholly aromatic polyester consisting essentially of die units (1), (2), (3), (4), and (6) ( 1) (2) ( 3 ) ( 4 ) ( 6) wherein a + b is approximately equal to d + f; the ratio of a to b being in the range of from about 1.4:1 to about 10:1; die ratio of d to f being in the range of from about 3:1 to about 21:1; and die ratio of c being in he range of from about 0.6:1 to about 7:1 moles per each mole of monomers corresponding to units (1) and (2). 11. A wholly aromatic polyester as defined in claim 10 wherein the ratio of d to f is in the range of from about 3.5: 1 to about 20: 1. 12. A molding compound formed from the copolyester of claim 1 and at least one agent selected from glass fibers, asbestos, graphitic carbon fibers, amorphous carbon fibers, glass beads, synthetic polymeric fibers, aluminum fibers, aluminum silicate fibers, oxide of aluminum fibers, titanium fibers, magnesium fibers, rock wool fibers, steel fibers, tungsten fibers, cotton, wool, and wool cellulose fibers, calcium silicate, silica, clays, talc, mica, polytetrafluoroethylene, carbop black, graphite, alumina trihydrate, sodium aluminum carbonate, barium ferrite, wollastonite and titanium dioxide. 13. An ovenware article comprising of die compounds of claim 12. 14. A wholly aromatic polyester comprising die units (1), (2), (3), (4) and (5) - f ( 5 ) + wherein Ar comprises at least one member selected from die group consisting of: I, a divalent substituted mononuclear aromatic radical of die formula wherein X is independendy hydrogen, a C\ to C5 alkyl group, a halide atom or an aryl group; with die proviso tiiat when the valence bonds are para to each other at least one group X must be other than hydrogen; and π, a divalent dinuclear aromatic radical of die formula wherein X is as previously defined, and Q is selected from the group of O, S, SO, S-S, SO2, CO and a chemical bond; and HI, a divalent naphthalene radical of the formula or isomers thereof and wherein a + b is approximately equal to d + e; die ratio of a to b is in the range of from about 0.42: 1 to about 2.33:1; the ratio of d to e is in the range of from about 3: 1 to about 99: 1 ; and die ratio of ' c to (a + b) is in die range of from about 0.15:1 to about 0.8:1. 15. A wholly aromatic polyester as defined in claim 2 which has a melting point of at least about 260° C, a heat distortion temperature of at least about 200° C when measured under a load of 264 psi, and which yields molded articles having good surface characteristics. 16. A wholly aromatic polyester as defined in claim 2 which has a melting point of at least about 260° C, a heat distortion temperature of at least about 230° C when measured under a load of 264 psi, and which yields molded articles having good surface characteristics. 17. A process for preparing the polyesters of claim 2 which comprises reacting terephthalic acid, isophthalic acid, p-hydroxybenzoic acid, hydroquinone, and an arylene diol w i an an y e o a ower monocar oxy c ac to orm a prepo ymer, o lowed by solid state advancement of said prepolymer to the desired high molecular weight polyester. 18. A wholly aromatic polyester as defined in claim 2 wherein the group Ar consists essentially of biphenylene. 19. A wholly aromatic polyester as defined in claim 2 wherein Ar comprises essentially of at least one member selected from the group consisting of wherein Y is methyl, chlorine, t-butyl or phenyl. 20. A wholly aromatic polyester as defined in claim 2 wherein Ar comprises at least one member wherein Q is O, S, SO, S-S, SO2, CO or a chemical bond. 21. A wholly arojnatic polyester as defined in claim 2 wherein Ar consists essentially of at least one member selected from 22. A wholly aromatic polyester comprising die units (1), (2), (3), (4) and (6) ( 1) ( - ) ( 3 ) (4) <«> wherein a + b is approximately equal to d + f; die ratio of a to b is in the range of from about 0.42:1 to about 2.33:1; die ratio of d to f is in the range of from about 3:1 to about 99:1; and the ratio of c to (a + b) is in the range of from about 0.15:1 to about 0.8:1. 23. A wholly aromatic polyester consisting essentially of die units (1), (2), (3), (4), and (6) ( 1) (2) ( 3 ) (4) ( β> wherein a + b is approximately equal to d + f; die ratio of a to b is in the range of from about 0.42:1 to about 2.33:1; die ratio of d to f is in the range of from about 3:1 to about 99:1; and the ratio of c to (a + b) is in die range of from about 0.15:1 to about 0.8:1. 24. A wholly aromatic polyester as defined in claim 23 wherein die ratio of d to f is- in die range of from about 10:1 to about 70:1. 25. A molding compound formed from the copolyester of claim 2 and at least one agent selected from glass fibers, glass beads, asbestos, graphitic carbon fibers, amorphous carbon fibers, synthetic polymeric fibers, aluminum fibers, aluminum silicate , , , , , fibers, tungsten fibers, cotton, wool, and wool cellulose fibers, calcium silicate, silica, clays, talc, mica, polytetrafluoroethylene, carbon black, graphite, alumina trihydrate, sodium aluminum carbonate, barium feπite, wollastonite and titanium dioxide. 26. An ovenware article comprising one or more of the compounds of claim 25.

Inventors: LAYTON RICHARD, MATZNER MARCUS, STERN BRIAN ALLEN, LAYTON, RICHARD, MATZNER, MARCUS, STERN, BRIAN, ALLEN
Applicants: AMOCO CORP, AMOCO CORPORATION
Application year: 1989
Main classification: C08G63
IPC codes: A47J36, C08G63, C08K3, C08K7, C08L67