United States Patent Office Patented Sept

3,054,768 United States Patent Office Patented Sept. 18, 1962 B. 2 vention are selected from the group consisting of hemimel 3,054,768 PROCESS COMPRESENG BRENDING A HALOSEN litene (1,2,3-trimethylbenzene), pseudocumene (1,2,4-tri AED POLYMER WITH AN ALKY, BENZENE methylbenzene), mesitylene (1,3,5-trimethylbenzene), James Maurice Quinn, Tonawanda, N.Y., assig or to E. H. prehnitene (1,2,3,4-tetramethylbenzene), durene (1,2,4,5- du Pont de Nenaours and Company, Wilmington, Del, tetramethylbenzene), pentamethylbenzene, hexamethyl a corporation of Delaware benzene, p-cymene (4-isopropyl-1-methylbenzene), 1,2-di No Drawing. Fied Oct. 21, 1958, Ser. No. 768,561 ethylbenzene, 1,4-diisopropylbenzene and 1,3,5-triethyl 6 (Cairns. (C. 260-33.6) benzene. The structural formulae of these compounds are given below: This invention relates to the manufacture of shaped 10 articles of polymeric halogenated hydrocarbons. More CH gh, specifically, it relates to the stabilization of the polymeric halogenated hydrocarbons, particularly above their melt CH3 CE ing temperatures, for Successful shaping into articles. The invention will be described as it applies to poly CBIs vinyl chloride or copolymers of vinyl chloride having vinyl chloride as the major constituent, and their forma CE: tion into films for use in packaging applications and the Fenimellitene Pseudocumene like. However, the invention is equally applicable to g H3 CEI polymers and copolymers of vinyl fluoride and may be 20 extended to include all polymeric materials whose thermal decomposition is at least partially attributed to the loss -CH of halogen acid from the composition, thereby leading to discoloration; and the shaping of these polymeric mate CH CH3 CH rials into films, filaments, fibers, foils, coatings, etc. Be 25 sides polyvinyl chloride and polyvinyl fluoride, the in CBs vention applies to such polymeric materials as vinylidene Mesitylene Prehnitene chloride polymers, vinylidene chloride-vinyl chloride co polymers, vinylidene chloride-acrylonitrile copolymers, (H, CH vinylidene fluoride polymers and copolymers, after-chlo 30 - CH3 CH rinated polyvinyl chloride, chloroprene polymers, chloro sulfonated polyethylene, and the like. CH- CE CH3 Polyvinyl chloride is characterized by poor thermal stability, particularly at temperatures above its melting E3 CE3 point. Thermal decomposition is evidenced by a brown Durene Pentamethylbenzene ing of the normally white polymer. As degradation con tinues the polymer becomes progressively darker until CHs CB charring and substantial degradation occur. This lack of thermal stability presents a serious obstacle to the CEs- CE commercial exploitation of the polymer since the pre 40 ferred methods of forming shaped structures involve the CH3- CH: use of heat. The object of the present invention is a substantially stabilized polymer that can be formed into shaped struc CHser CH tures at elevated temperatures, e.g., by melt or plasticized Edexamethylbenzene p-Cymene extrusion, rolling, coalescence or solvent casting, without encountering the aforementioned difficulties. A further CE CH8 object is a polyvinyl chloride composition that can easily N / be melt-extruded into a useful film. Other objects will ghsch, GH appear hereinafter. 50 The objects are accomplished by a composition of mat ter comprising the halogenated hydrocarbon polymer and 1-15% by weight of at least one alkyl substituted benzene Or having 2-6 alkyl substitutions, said alkyl groups having o 1-4 carbon atoms, said alkyl substituted benzene having 55 CHs CEis a molecular weight greater than 106 (at least 107) and 1,2-diethylbenzene 1,4-Diisopropylbenzene a normal boiling point of at least 160° C. The upper limit on molecular weight is 414 which represents a fully CCH substituted benzene having attached alkyl groups of 4. carbon atoms each Ce (C4H9)6. When the alkyl groups 60 are all methyl (one carbon atom), then it is preferred that at least 3 substitutions on the benzene structure are present. When at least one of the alkyl groups has two -O- or more carbon atoms, then two to six substitutions may 1,3,5-Triethylbenzene be present. The preferred halogenated hydrocarbon poly 65 The amount of the alkyl substituted benzene stabilizer mers are those in which the halogen has an atomic weight used, particularly for the melt-extrusion of polyvinyl chlo of 19-36. ride films, should be enough to provide adequate thermal The substituted benzene compounds must have a boil stability during the forming operation but not enough to ing point of at least about 160° C. in order to remain affect the properties of the resulting film adversely. Con present at the temperatures ordinarily used in preparing 70 centrations of at least 1% of the stabilizer, based on the shaped structures of polyvinyl chloride. The alkyl sub weight of the stabilizer plus polymer, have been found stituted benzene compounds preferred in the present in most useful. The maximum used will depend on the 3,054,768 3 4. process of forming the shaped structures. However, the white light. Its tensile strength was 7000 p.s. i., the elon maximum concentration of the stabilizer remaining in the gation was 266% and the modulus was 276,000 p.s.i. ultimate product is preferably no greater than 15%. For In a control experiment showing the effect of using no extrusion operations where only a minor portion of the stabilizer, a mixture of 98 parts of the same polyvinyl stabilizer would be lost by evaporation during the form chloride resin as used above with 2 parts of "Lubricin' ing operation, up to 15% may therefore be used in the V-3 was fed into the extruder heated to 205 C. The starting mixture. In solvent casting, dispersion coales mixture was converted to a bubbly, black mass part way cence, or plasticized extrusion, where a larger proportion through the heated zone of the extruder and could not be of the stabilizer may be evaporated during formation of extruded due to plugging of the equipment. Essentially the shaped structure, a still higher concentration, e.g., up 0 the same results were obtained in other attempted experi to 25%, may be used in the starting composition. ments using this mixture at extrusion temperatures rang Besides improving thermal stability and lowering the ing from 185° C. to 230° C. Below 185° C. the poly melt viscosity of the polymeric halogenated hydrocarbons, vinyl chloride resin did not coalesce. the stabilizer compounds of the compositions of this in Example III vention provide other advantages. They are substantially 5 inert chemically to normal compounding ingredients. A mixture consisting of 90 parts polyvinyl chloride res They are compatible with the polymers over a wide range in and 10 parts hexamethylbenzene was prepared by ball of compositions and therefore can be easily mixed uni milling the ingredients together as in Example I. A one formly with the polymers; also they show no tendency to gram sample of this mixture was pressed for 6 minutes be exude to the surface of the ultimately produced polymeric 20 tween ferrotype plates under a total force of 30 tons in a articles. Thus, they do not interfere with post-processing Carver laboratory press heated to 210 C. The film was operations such as printing. These compounds are essen clear and substantially free of bubbles and particles, but tially insoluble in water so that the final articles are not had a somewhat brownish cast in 10 mill thickness when rendered water-sensitive by their presence. Most import viewed against a source of white light. ant, the films produced are substantially clear, being vir Example IV tually bubble-free and particle-free. The process for forming shaped structures involves A mixture of 90 parts polyvinyl chloride resin and 10 blending a mixture of the halogenated hydrocarbon poly parts 1,4-diisopropylbenzene was prepared as in Example mer and the alkyl substituted benzene having 2-6 alkyl I. A one-gram sample of this mixture was pressed for 6 substitutions, each alkyl group having 1-4 carbon atoms; 30 minutes between ferrotype plates under a total force of 30 then heating the mixture until it is converted into a homo tons in a Carver laboratory press heated to 210° C. The geneous single phase composition; and, thereafter, forming film was clear and substantially free of bubbles and par the homogeneous single phase into a shaped structure and ticles. cooling the structure. Examples V-XI Specific embodiments falling within the definition of 35 Example I was repeated using 90 parts of the polyvinyl the process and composition of the invention will be ap chloride resin and 10 parts of the compounds listed below: parent from the following examples. It is understood Example: Compound that the examples should not be considered to limit the V-----------------. 1,2,3-trimethylbenzene. Scope of the present invention. In the examples, all parts VI----------------- 1,2,4-trimethylbenzene. are by weight unless otherwise specified. 40 VII---------------- 1,2,3,4-tetramethylbenzene. Example I VIII--------------- 1,2,4,5-tetramethylbenzene. X----------------- 4-isopropyl-1-methylbenzene. A mixture consisting of 90 parts (weight basis) of a X----------------- 1,2-diethylbenzene. polyvinyl chloride resin (the resin having an inherent vis 45 X----------------- 1,3,5-triethylbenzene. cosity of 1.21 deciliters per gram measured at 0.25% con In all the examples, a clear film substantially free of centration in hexamethylphosphoramide at 30° C.) and bubbles and particles was produced. 10 parts of mesitylene (1,3,5-trimethylbenzene) was pre The compositions of this invention are useful in the pared by ball milling the ingredients together for 60 min preparation of shaped structures of all types. They are utes. A one gram sample of this mixture was pressed for extremely useful in preparing films, filaments, fibers, foils 5 minutes between ferrotype plates under a total force of and the like and as coatings for wood, metals, etc.

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