PROCESS FOR PRODUCING VINYL CHLORIDE POLYMERS

Abstract: A process for producing vinyl chloride polymers is characterized by copolymerizing 100 parts by weight of vinyl chloride monomer with 0.1 to 3 parts by weight of a crosslinking agent consisting of at least one diacrylate or dimethacrylate of a polyether glycol or diacrylate or dimethacrylate of a polyester polyol and having an average molecular wight of 200 or more, while maintaining the copolymerization temperature at a constant value in the range of 30°C to 70°C. According to this process, the polymerization degree is constant without being affected by the amount of the crosslinking agent and also it is possible to adjust the content of tetrahydrofuran-insoluble polymers with a broad range.

Description: Process for producing vinyl chloride polymers BACKGROUND OF THE INVENTION Field of the Invention This invention relates to a process for producing vinyl chloride polymers having a high polymerization degree by copolymerizing vinyl chloride monomer with a crosslinking agent. Description of the Prior Art Processes so far known for commercially producing vinyl chloride polymers having a high polymerization degree include not only a polymerization process merely by lowering the polymerization temperature, but also a process of copolymerizing vinyl chloride with a cross linking agent such as diallyl esters of dibasic acids e.g. diallyl phthalate to obtain vinyl chloride polymers containing branched chains or crosslinked molecular species (Japanese patent publication No.Sho 42-9671/1967). Polymers obtained according to the above process are of a high extent cross linked structure, that is, contain a considerably large amount of gel insoluble in organic solvents in which conventional vinyl chloride polymers are soluble; thus it is known that the polymers exhibit specific values of physical properties and have various improved characteristic properties. Improvement in such characteristic properties includes those in mechanical properties, thermal properties, chemical resistance, combustion characteristic properties, etc. Thus, in order to obtain such characteristic properties, that is, those with which polymers of cross linked structure are to be furnished, it is preferred that the polymers contain gelling portion in an amount as large as possible, and further the process for producing such polymers is preferred to be capable of optionally adjusting the gelling portion in accordance with the desired characteristic. properties -in a necessary polymerization degree. However, in the above case of diallyl phthalate (hereinafter abbreviated to DAP), if the polymerization is carried out with varied contents of DAP at a definite temperature and the polymerization degree of a tetrahydrofuran-soluble portion and the content of a tetrahydrofuran-insoluble portion are measured, then the content of gelling portion is low in a small amount of DAP, whereas it increases rapidly in a certain amount of DAP. Further the polymerization degree varies greatly depending on the amount of DAP and increases rapidly in a certain amount of DAP. These facts raise problems at the time of polymerization and molding and processing. Namely when the amount of DAP is small, it is impossible to obtain characteristic properties of crosslinked structure, and when the amount increases, the polymerization degree increases rapidly depending on the amount of DAP to make it difficult to maintain the polymerization degree at a constant value, and also processability is inferior due to too high polymerization degree. When the amount of DAP further increases, it is possible to obtain characteristic properties with which polymers of cross linked structure are to be furnished, but it is impossible to obtain processed products of smooth surface. Furthermore, polymers having an adequate content of insoluble portion and also having a polymerization degree of 1,000 or less cannot be obtained; hence it is impossible to develop the application fields of such polymers toward the fields of rigid products of plasticizerfree vinyl chloride polymer resins. In order to solve these various problems, the present inventors have made strenuous studies and completed the present invention. An object of the present invention is to provide a process for producing vinyl chloride polymers by copolymerizing vinyl chloride monomer with a crosslinking agent wherein the polymerization degree is kept at a constant value without being affected by the amount of the crosslinking agent and also it is possible to adjust the content of tetrahydrofuran-insoluble polymer- within a broad range. Another object of the present invention is to provide polymers having characteristic properties with which polymers of crosslinked structure are to be furnished and also capable of affording processed products of smooth surface, and also not only polymers having a polymerization degree of 1,000 or more and also containing a suitable amount of tetrahydrofuran-insoluble polymer but also polymers having a polymerization degree less than 1,000 and useful for rigid products without any plasticizer. SUMMARY OF THE INVENTION The present invention resides in: a process for producing vinyl chloride polymers by copolymerizing vinyl chloride monomer with a crosslinking agent, which process comprises copolymerizing 100 parts by weight of vinyl chloride monomer with 0.1 to 3 parts by weight of a crpsslinking agent consisting of at least one member selected from the group consisting of diacrylate and dimethacrylate of polyether glycols and diacrylate and dimethacrylate of polyester polyols and having an average molecular weight of 200 to 8,000, while maintaining the copolymerization temperature at a constant value in the range of 300C to 700C. More particularly the above diacrylate or dimethacrylate of polyether glycols and diacrylate or dimethacrylate of polyester polyols are respectively expressed by the following general formulae: EMI5.1 and EMI5.2 wherein R represents hydrogen atom or methyl group; DÚ represents an alkanediyl group of 2 to 6 carbon atoms; Dê represents an alkanediyl group of 2 to 6 carbon atoms or phenylene group; n represents a number of 2 to 100; and m represents a number of 2 to 40. The alkanediyls referred to above mean divalent non-cyclic saturated hydrocarbon group such as ethylene group, propylene group, tetramethylene groups 2,2-dimethyl-1,3-propanediyl group, etc. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 shows the relationship of the amount of a crosslinking agent PTMGA added, relative to the polymerization degree of tetrahydrofuran (THF) soluble polymer and the content of THF-insoluble portion. Fig. 2 shows the relationship of the amount of a usual crosslinking agent DAP relative to the above polymerization degree and the above content. DESCRIPTION OF THE PREFERRED EMBODIMENTS The cross linking agent used in the process of the present invention is preferred to be at least one member selected from the group consisting of diacrylates and dimethacrylates of polyethylene glycol, polypropylene glycol and polytetramethylene ether glycol, having an average polymerization degree of 5 to 30, or/and at least one member selected from the group consisting of diacrylates and dimethacrylates of polyester glycols of adipic acid with neopentyl glycol, having an average polymerization degree. of 2 to 10. The average molecular weight of the crosslinking agent of the present invention is in the range of 200 to 8,000, preferably 340 to 4,000, more preferably 340 to 2,400. If the weight is less than 200, the molecular weight of vinyl chloride polymers is liable to vary depending on the amount of the crosslinking agent to make it difficult to obtain those having a definite molecular weight. As for the average polymerization degree of the polyether glycols, n of the above formula (1) is in the range of 2 to 100, preferably 5 to 50, more preferably 5 to 30 As for the average molecular weight of the polyester glycols, m of the above formula (2) is in the range of 2 to 40, preferably 2 to 20, more preferably 2 to 10. Values of n or m less than 2 are undesirable, since similar drawbacks to those in the case of DAP occur; on the other hand, if n exceeds 100 or m exceeds 40, the reactivity at the time of crosslinking polymerization of the diacrylates or dimethacrylates raises a problem and also the lubricating properties at the time of molding and processing of the resulting polymers become excessive; hence such higher values also raise a problem. The amount of the crosslinking agent used is 0.1 to 3 parts by weight based on 100 parts by weight of vinyl chloride monomer. If it is less than 0.1 part by weight, the content of the insoluble portion is so low that it is impossible to obtain characteristic properties with which polymers of crosslinked structure are to be furnished. If it exceeds 3 parts by weight, processability is inferior and it is impossible to obtain molded products of smooth surface. Examples of the cross linking agent of the present invention are polyethylene glycol didcrylates, polyethylene glycol dimethacrylates, polypropylene glycol diacrylates, polypropylene glycol dimethacrylates, polytetramethylene ether glycol diacrylatss, polytetramethylene ether glycol dimethacrylates, polyneopentyl adipate glycol diacrylate, polyneopentyl adipate glycol dimethacrylate, etc. Crosslinking agents other than those of the present invention such as diallyl adipate, diallyl maleate, triallyl cyanurate, triallyl phosphate, divinylbenzene, divinyl ether, etc. are undesirable since they exhibit similar behaviors to those in the case of DAP. As to the production process of the present invention, polymerization is carried out at a definite temperature established within a range of 300C to 700C. The resulting polymers have a polymerization degree of 350 to 5,000. At higher temperatures than 70 C, polymers of a lower polymerization degree are obtained and characteristic properties of vinyl chloride polymer resins are not obtained. On the other hand, at lower temperatures than 30 C, the polymerization degree is so high that processing in conventional manner becomes difficult. Vinyl chloride monomer used in the present invention includes not only vinyl chloride monomer alone, but also mixtures thereof with vinyl monomers copolymerizable therewith, composed mainly of vinyl chloride monomer. Such copolymerizable vinyl monomers are well known to persons skilled in the art and examples thereof are olefins such as ethylene, propylene, etc., vinyl esters such as vinyl acetate, etc., vinyl ethers such as ethyl vinyl ether, cetyl vinyl ether, etc., acrylic acid esters, maleic acid or fumaric acid esters and anhydrides thereof, aromatic vinyl compound such as styrene, acrylonitrile, etc. Polymerization initiators and other additives (dispersant, emulsifier., etc.) used in the polymerization of the present invention may be not those which are specified and particular, but those which are well known and generally used by persons skilled in the art. Examples of dispersants and emulsifiers are protective colloid type chemicals or natural high molecular compounds such as partially saponified products of polyvinyl acetate, acrylic acid copolymers, maleic anhydride copoloners, cellulose derivatives, gelatin, starch, etc., nonionic emulsifiers such as esters of higher fatty acids with polyols, polyoxyethylene derivatives, etc., anionic emulsifiers such as metal salts of higher fatty acids, metal salts of sulfuric acid esters of higher alcohols, etc. Examples of polymerization initiators are organic peroxides such as benzoyl peroxide, lauroyl peroxide, dioctyl peroxydicarbonate, di-3-methoxybutyl peroxycarbonate, acetylcyclohexylsulfonyl peroxide, etc., azo compounds such as azobisisobutyronitrile, a, a azobis-2,4-dimethylvaleronitrile. etc., persulphates such as potassium persulfate, ammonium persulfate, etc. Addition of known additives used together with suspending agents or emulsifiers to the polymerization system does not harm the effectiveness of the present invention. When polymers having a lower polymerization degree (600 or less) are produced in the present invention, chain transfer agents may be used as in the case of usual polymerization. The effectiveness of the production process of the present invention is that the tetrahydrofuran soluble portion of the resulting vinyl chloride polymers has a constant polymerization degree independently of the amount of crosslinking agents, and further that the content of the tetrahydrofuraninsoluble polymer (polymer of crosslinked structure) does not increase rapidly in a certain amount of crosslinking agents unlike the case of DAP. Thus it is possible to adjust the content of the gelling portion (polymer of cross linked structure) within a broad range thereof, with each grade of polymers having various polymerization degrees. Namely, mere variation of the amount of crosslinking agent used at a definite temperature may be sufficient. Thus it is possible for the polymers obtained according to the present invention, to provide the most suitable material for application fields over a range from those of plasticizer-free, rigid molded products to those of super-flexible molded products containing a large amount pf plasticizer. If a rigid sheet exhibiting characteristic properties with which polymers of cross linked structure are to be furnished is needed, it is possible to provide polymers having a polymerization degree of 700 to 800 and a gel content of 5 to 50%, and similarly if a flexible molded product is needed, it is possible to provide polymers having a polymerization degree of 1,000 to 1,300, while if an elastomeric molded product is needed, it is possible to provide polymers having a polymerization degree of 2,000 to 3,000. Further it is also possible to use polymers containing a gelling portion of 508 or more together with usual vinyl chloride polymers in admixture. This case, however, is disadvantageous in the aspect of physical properties since uniform mixing is difficult; thus it is preferable to carry out copolymerization so as to contain a required amount of gelling portion in the resulting copolymer and use this copolymer alone. In other words, the production process of the present invention can be also referred to as a process capable of optionally deriving characteristic properties with which polymers of crosslinked structure are to be furnished, correspondingly to uses. The effectiveness of the present invention will be described by way of examples (Examples and Comparative examples). The polymerization degree of the tetrahydrofuran-soluble portion of the copolymers obtained in the examples and the content of the tetrahydrofuran-insoluble portion of the copolymers were measured according to the following methods: o Polymerization degree: according to the method of JIS K-6721. Tetrahydrofuran-insolubre portion (%) (hereinafter abbreviated to insoluble portion): A sample (3 g) was allowed to stand in tetrahydrofuran for 12 hours, followed by subjecting the resulting material to a high speed centrifugal separator (8,000 revolutions, 10 minutes), washing the insoluble portion with tetrahydrofuran and drying in vacuo (50 C, 10 hours or longer), to measure the value of the portion. Further, the resulting copolymers were molded under the conditions listed in the following Table: Table EMI14.1 <tb> <SEP> Examples <SEP> and <tb> <SEP> Comparative <SEP> examples <tb> <SEP> A, <SEP> B <SEP> and <SEP> C <SEP> D <SEP> and <SEP> E <tb> <SEP> Polymer <SEP> formed <SEP> (parts <SEP> by <SEP> 100 <SEP> 100 <tb> <SEP> weight) <tb> <SEP> S: <tb> <SEP> o <SEP> DOP <SEP> ( <SEP> I <SEP> ) <SEP> 90 <SEP> 90 <tb> <SEP> o <SEP> Heavy <SEP> calcium <SEP> carbonate <SEP> 30 <SEP> 20 <tb> <SEP> o <SEP> ( <SEP> I <SEP> ) <tb> <SEP> Ca-Zn <SEP> composite <SEP> 2 <tb> <SEP> o <SEP> stabilizer <SEP> ( <SEP> n <SEP> ) <SEP> 2 <tb> <SEP> Black <SEP> pigment <SEP> ( <SEP> n <SEP> ) <SEP> 0.2 <SEP> 0.2 <tb> 75 <SEP> 75 <SEP> g <SEP> Henschel <SEP> mixer <tb> <SEP> C: <tb> <SEP> Dry-up <SEP> temp. <SEP> (OC) <SEP> 110 <SEP> 110 <tb> <SEP> C: <tb> <SEP> Number <SEP> of <SEP> revolutions <SEP> 820 <SEP> - <SEP> 1640 <SEP> 820 <SEP> 1640 <tb> <SEP> m <SEP> (rpm) <tb> <SEP> 65 <SEP> mm <SEP> Extruder <tb> <SEP> Number <SEP> of <SEP> revolutions <SEP> 40 <SEP> 40 <tb> <SEP> o <SEP> (rpm) <tb> <SEP> 0 <tb> <SEP> Cylinder <SEP> temperature <tb> (0C) <tb> <SEP> < <SEP> C1 <SEP> 105 <SEP> 110 <tb> <SEP> C: <SEP> 1 <SEP> 105 <tb> <SEP> X <SEP> C2 <SEP> 115 <SEP> 120 <tb> <SEP> 2 <SEP> 115 <SEP> 120 <tb> <SEP> O <SEP> C3 <SEP> 120 <SEP> 130 <tb> <SEP> Die <SEP> temp. <SEP> ( C) <SEP> 130 <SEP> 145 <tb> <SEP> 40 <SEP> O <SEP> mm <SEP> Extruder <tb> <SEP> Number <SEP> of <SEP> revolutions <SEP> 40 <SEP> 40 <tb> <SEP> (rpm) <tb> <SEP> Cylinder <SEP> temperature <tb> <SEP> (0C) <tb> <SEP> C1 <SEP> 140 <SEP> 140 <tb> <SEP> C2 <SEP> 155 <SEP> 165 <tb> <SEP> C3 <SEP> 170 <SEP> 180 <tb> <SEP> Die <SEP> temp. <SEP> f C) <SEP> 180 <SEP> 190 <tb> Processability, delustering extent and characteristic properties of molded products were evaluated according to the following methods: Processability: A belt-form extrudate was prepared under the conditions listed in the Table and the surface state was observed. The evaluation standards are as follows: o Smooth surface Somewhat smooth surface A ..... Partly projected and depressed surface x Surface has a large number of projections and depressions. o Delustering extent: The above belt-form extrudate was observed and evaluated under the following standards: xx Roughened surface x ..... Lustrous A Somewhat lustrous o Good delustering Very Very good delustering o Characteristic properties (with which polymers of crosslinked structure are to be furnished): The mechanical characteristic properties (tensile, impact strengths, etc.), thermal character istic properties (heat shrinkage, etc.), chemical resistance (resistance to solvent), life (stress cracking, etc.) and combustion characteristic properties (reduction in drip) were collectively observed. 0 Characteristic properties with whcih polymers of crosslinked structure are to be furnished were exhibited. A The characteristic properties were partly exhibited. The characteristic properties were not exhibited at all. xx ... . Processing was impossible. Examples and Comparative examples (A) Into a 200 Q capacity stainless polymerization vessel were fed purified water (200 parts by weight), a partially saponified polyvinyl acetate (0.2 part by weight), cr,ar'-azobis 2,4-dimethylvaleronitrile (0.035 part by weight) and a crosslinking agent (a given amount)-tfollowed by deaerating the mixture in vacuo with stirring, then feeding vinyl chloride (100 parts by weight) and raising the temperature up to 630C with stirring to polymerize vinyl chloride. When the percentage polymerization reached a range of 86 to 90%, unreacted monomer was discharged and the resulting copolymer was washed with water, dehydrated and dried. Physical properties of the copolymer and characteristi= properties of molded product therefrom were measured. The results are shown in Table A. Examples and Comparative examples (B) Examples and Comparative examples (A) were repeated except that dioctyl peroxydicarbonate (0.03 part by weight) was used as an initiator and the temperature was 57 C. The results are shown in Table B. Examples and Comparative examples (C) Examples and Comparative examples (A) were repeated except that di-3-methoxybutyl peroxydicarbonate (0.025 part by weight) and acetylcyclohexylsulfonyl peroxide (0.01 part by weight) were used as initiators and the temperature was 520C. The results are shown in Table C. Table A EMI18.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Note <tb> Run <SEP> ization <tb> <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Deluster- <SEP> Charactemper Kind <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <SEP> teristic <tb> ature <tb> degree <SEP> (%) <SEP> property <SEP> properties <tb> ( C) <tb> Compar. <tb> A-1 <SEP> 63 <SEP> PTMGA** <SEP> 0 <SEP> 800 <SEP> 0 <SEP> o <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 2 <SEP> " <SEP> " <SEP> 0.05 <SEP> 810 <SEP> 0 <SEP> o <SEP> x <SEP> x <SEP> " <tb> " <SEP> 3 <SEP> " <SEP> " <SEP> 0.1 <SEP> 800 <SEP> 0 <SEP> o <SEP> # <SEP> x <SEP> Example <tb> " <SEP> 4 <SEP> " <SEP> " <SEP> 0.2 <SEP> 830 <SEP> 5.7 <SEP> o <SEP> # <SEP> # <SEP> " <tb> " <SEP> 5 <SEP> " <SEP> " <SEP> 0.5 <SEP> 780 <SEP> 15 <SEP> o <SEP> # <SEP> o <SEP> " <tb> " <SEP> 6 <SEP> " <SEP> " <SEP> 1.0 <SEP> 770 <SEP> 22.2 <SEP> o <SEP> # <SEP> o <SEP> " <tb> " <SEP> 7 <SEP> " <SEP> " <SEP> 2.0 <SEP> 760 <SEP> 32.0 <SEP> o <SEP> # <SEP> o <SEP> " <tb> " <SEP> 8 <SEP> " <SEP> " <SEP> 3.0 <SEP> 760 <SEP> 35.0 <SEP> # <SEP> # <SEP> # <SEP> " <tb> Compar. <tb> " <SEP> 9 <SEP> " <SEP> DAP <SEP> 0.05 <SEP> 920 <SEP> 0 <SEP> o <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 10 <SEP> " <SEP> " <SEP> 0.1 <SEP> 990 <SEP> 0 <SEP> o <SEP> x <SEP> x <SEP> " <tb> " <SEP> 11 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1220 <SEP> 2.0 <SEP> o <SEP> x <SEP> x <SEP> " <tb> " <SEP> 12 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1500 <SEP> 36.0 <SEP> x <SEP> o <SEP> # <SEP> " <tb> " <SEP> 13 <SEP> " <SEP> " <SEP> 1.0 <SEP> 920 <SEP> 77.0 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> " <SEP> 14 <SEP> " <SEP> " <SEP> 1.3 <SEP> 800 <SEP> 92.0 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> * Based on 100 parts by weight of vinyl chloride (this applies to the following Tables) ** Polytetramethylene ether glycol diacrylate (n=10, this applies to the following Tables). Table B EMI19.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Run <SEP> Note <tb> ization <tb> temper- <SEP> Kind <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Deluster- <SEP> Characature <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <SEP> teristic <tb> ( C) <SEP> degree <SEP> (%) <SEP> property <SEP> properties <tb> Compar. <tb> <SEP> B-1 <SEP> 57 <SEP> PTMGA** <SEP> 0 <SEP> 1030 <SEP> 0 <SEP> o <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 2 <SEP> " <SEP> " <SEP> 0.05 <SEP> 1040 <SEP> 0.3 <SEP> o <SEP> x <SEP> x <SEP> " <tb> " <SEP> 3 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1000 <SEP> 3.0 <SEP> o <SEP> # <SEP> # <SEP> Example <tb> " <SEP> 4 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1040 <SEP> 7.5 <SEP> o <SEP> o <SEP> o <SEP> " <tb> " <SEP> 5 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1030 <SEP> 17.0 <SEP> o <SEP> # <SEP> o <SEP> " <tb> " <SEP> 6 <SEP> " <SEP> " <SEP> 1.0 <SEP> 1000 <SEP> 27.4 <SEP> o <SEP> # <SEP> o <SEP> " <tb> " <SEP> 7 <SEP> " <SEP> " <SEP> 2.0 <SEP> 980 <SEP> 39.0 <SEP> o <SEP> # <SEP> # <SEP> " <tb> " <SEP> 8 <SEP> " <SEP> " <SEP> 3.0 <SEP> 980 <SEP> 42.1 <SEP> # <SEP> # <SEP> # <SEP> " <tb> Compar. <tb> " <SEP> 9 <SEP> " <SEP> DAP <SEP> 0.05 <SEP> 1150 <SEP> 0 <SEP> o <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 10 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1320 <SEP> 0 <SEP> o <SEP> x <SEP> x <SEP> " <tb> " <SEP> 11 <SEP> " <SEP> 0.2 <SEP> 1740 <SEP> 5.0 <SEP> x <SEP> # <SEP> x <SEP> " <tb> " <SEP> 12 <SEP> " <SEP> " <SEP> 0.3 <SEP> 220 <SEP> 15.0 <SEP> x <SEP> o <SEP> o <SEP> " <tb> " <SEP> 13 <SEP> " <SEP> " <SEP> 0.4 <SEP> 1580 <SEP> 30.0 <SEP> x <SEP> # <SEP> o <SEP> " <tb> " <SEP> 14 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1350 <SEP> 43.0 <SEP> x <SEP> # <SEP> o <SEP> " <tb> " <SEP> 15 <SEP> " <SEP> " <SEP> 0.7 <SEP> 1050 <SEP> 65 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> " <SEP> 16 <SEP> " <SEP> " <SEP> 1.0 <SEP> 860 <SEP> 83.0 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> Table C EMI20.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Note <tb> Run <SEP> ization <tb> temper- <SEP> Kind <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Deluster- <SEP> Characature <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <SEP> teristic <tb> ( C) <SEP> degree <SEP> (%) <SEP> property <SEP> properties <tb> Compar. <tb> C-1 <SEP> 52 <SEP> PTMGA** <SEP> 0 <SEP> 1300 <SEP> 0 <SEP> o <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 2 <SEP> " <SEP> " <SEP> 0.05 <SEP> 1310 <SEP> 2.0 <SEP> o <SEP> x <SEP> x <SEP> " <tb> " <SEP> 3 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1350 <SEP> 4.6 <SEP> o <SEP> # <SEP> # <SEP> Example <tb> " <SEP> 4 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1340 <SEP> 9.8 <SEP> o <SEP> o <SEP> o <SEP> " <tb> " <SEP> 5 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1300 <SEP> 17.8 <SEP> o <SEP> # <SEP> o <SEP> " <tb> " <SEP> 6 <SEP> " <SEP> " <SEP> 1.0 <SEP> 1270 <SEP> 26.5 <SEP> o <SEP> # <SEP> o <SEP> " <tb> " <SEP> 7 <SEP> " <SEP> " <SEP> 2.0 <SEP> 1270 <SEP> 40.0 <SEP> o <SEP> # <SEP> # <SEP> " <tb> " <SEP> 8 <SEP> " <SEP> " <SEP> 3.0 <SEP> 1250 <SEP> 43.0 <SEP> # <SEP> # <SEP> # <SEP> " <tb> Compar. <tb> " <SEP> 9 <SEP> " <SEP> DAP <SEP> 0.05 <SEP> 1420 <SEP> 0.5 <SEP> o <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 10 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1600 <SEP> 0.5 <SEP> o <SEP> x <SEP> x <SEP> " <tb> " <SEP> 11 <SEP> " <SEP> " <SEP> 0.2 <SEP> 2100 <SEP> 6.0 <SEP> x <SEP> &num; <SEP> &num; <SEP> " <tb> " <SEP> 12 <SEP> " <SEP> " <SEP> 0.25 <SEP> 3980 <SEP> 11.0 <SEP> x <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 13 <SEP> " <SEP> " <SEP> 0.4 <SEP> 1500 <SEP> 36.0 <SEP> x <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 14 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1280 <SEP> 44 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> " <SEP> 15 <SEP> " <SEP> " <SEP> 1.0 <SEP> 800 <SEP> 86 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> Examples and Comparative examples (D) Examples and Comparative examples (A) were repeated except that acetylcyclohexylsulfonyl peroxide (0.03 part by weight) was used as an initiator and the temperature was 41.5 C. The results are shown in Table D. Examples and Comparative examples (E) Examples and Comparative examples (A) were repeated except that acetylcyclohexylsulfonyl peroxide (0.035 part by weight') was used as an initiator and the temperature was 39,5cm. The results are shown in Table E. Table D EMI22.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Note <tb> Run <SEP> ization <tb> temper- <SEP> Kind <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Deluster- <SEP> Characature <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <SEP> teristic <tb> ( C) <SEP> degree <SEP> (%) <SEP> property <SEP> properties <tb> Compar. <tb> D-1 <SEP> 41.5 <SEP> PTMGA** <SEP> 0 <SEP> 2100 <SEP> 0 <SEP> &num; <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 2 <SEP> " <SEP> " <SEP> 0.05 <SEP> 2110 <SEP> 2.3 <SEP> &num; <SEP> x <SEP> x <SEP> " <tb> " <SEP> 3 <SEP> " <SEP> " <SEP> 0.1 <SEP> 2100 <SEP> 5.0 <SEP> o <SEP> x <SEP> x <SEP> Example <tb> " <SEP> 4 <SEP> " <SEP> " <SEP> 0.2 <SEP> 2050 <SEP> 10.0 <SEP> o <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 5 <SEP> " <SEP> " <SEP> 0.5 <SEP> 2010 <SEP> 22.0 <SEP> o <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 6 <SEP> " <SEP> " <SEP> 1.0 <SEP> 2020 <SEP> 33.2 <SEP> o <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 7 <SEP> " <SEP> " <SEP> 2.0 <SEP> 2000 <SEP> 47.0 <SEP> &num; <SEP> &num; <SEP> &num; <SEP> " <tb> " <SEP> 8 <SEP> " <SEP> " <SEP> 3.0 <SEP> 2000 <SEP> 56.5 <SEP> x <SEP> xx <SEP> &num; <SEP> " <tb> Compar. <tb> " <SEP> 9 <SEP> " <SEP> DAP <SEP> 0.05 <SEP> 2310 <SEP> 1.0 <SEP> o <SEP> x <SEP> x <tb> ex. <tb> " <SEP> 10 <SEP> " <SEP> " <SEP> 0.1 <SEP> 2520 <SEP> 5.0 <SEP> o <SEP> &num; <SEP> &num; <SEP> " <tb> " <SEP> 11 <SEP> " <SEP> " <SEP> 0.15 <SEP> 3000 <SEP> 10.0 <SEP> o <SEP> o <SEP> o <SEP> " <tb> " <SEP> 12 <SEP> " <SEP> " <SEP> 0.2 <SEP> 2000 <SEP> 20.0 <SEP> o <SEP> o <SEP> o <SEP> " <tb> " <SEP> 13 <SEP> " <SEP> " <SEP> 0.3 <SEP> 1400 <SEP> 40.0 <SEP> &num; <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 14 <SEP> " <SEP> " <SEP> 0.5 <SEP> 990 <SEP> 63.0 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> " <SEP> 15 <SEP> " <SEP> " <SEP> 1.0 <SEP> 600 <SEP> 92.0 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> Table E EMI23.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Note <tb> Run <SEP> ization <tb> temper- <SEP> Kind <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Deluster- <SEP> Characature <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <SEP> teristic <tb> ( C) <SEP> degree <SEP> (%) <SEP> property <SEP> properties <tb> Compar. <tb> E-1 <SEP> 39.5 <SEP> PTMGA** <SEP> 0 <SEP> 2500 <SEP> 0 <SEP> &num; <SEP> &num; <SEP> x <tb> ex. <tb> " <SEP> 2 <SEP> " <SEP> " <SEP> 0.05 <SEP> 2520 <SEP> 3.0 <SEP> &num; <SEP> &num; <SEP> x <SEP> " <tb> " <SEP> 3 <SEP> " <SEP> " <SEP> 0.1 <SEP> 2490 <SEP> 6.5 <SEP> o <SEP> &num; <SEP> &num; <SEP> Example <tb> " <SEP> 4 <SEP> " <SEP> " <SEP> 0.2 <SEP> 2400 <SEP> 13.4 <SEP> o <SEP> o <SEP> o <SEP> " <tb> " <SEP> 5 <SEP> " <SEP> " <SEP> 0.5 <SEP> 2450 <SEP> 26.7 <SEP> o <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 6 <SEP> " <SEP> " <SEP> 1.0 <SEP> 2450 <SEP> 41.0 <SEP> o <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 7 <SEP> " <SEP> " <SEP> 2.0 <SEP> 2400 <SEP> 57.5 <SEP> &num; <SEP> &num; <SEP> &num; <SEP> " <tb> " <SEP> 8 <SEP> " <SEP> " <SEP> 3.0 <SEP> 2380 <SEP> 67.0 <SEP> x <SEP> xx <SEP> &num; <SEP> " <tb> Compar. <tb> " <SEP> 9 <SEP> DAP <SEP> 0.05 <SEP> 2570 <SEP> 3.4 <SEP> o <SEP> &num; <SEP> x <tb> ex. <tb> " <SEP> 10 <SEP> " <SEP> " <SEP> 0.1 <SEP> 2710 <SEP> 7.0 <SEP> &num; <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 11 <SEP> " <SEP> " <SEP> 0.15 <SEP> 2500 <SEP> 15.0 <SEP> o <SEP> &num; <SEP> &num; <SEP> " <tb> " <SEP> 12 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1750 <SEP> 25.0 <SEP> o <SEP> &num; <SEP> x <SEP> " <tb> " <SEP> 13 <SEP> " <SEP> " <SEP> 0.3 <SEP> 1300 <SEP> 43.0 <SEP> o <SEP> &num; <SEP> o <SEP> " <tb> " <SEP> 14 <SEP> " <SEP> " <SEP> 0.5 <SEP> 920 <SEP> 67.0 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> " <SEP> 15 <SEP> " <SEP> " <SEP> 0.8 <SEP> 650 <SEP> 87.0 <SEP> x <SEP> xx <SEP> xx <SEP> " <tb> The relationship of the polymerization degree of the tetrahydrofuran - soluble polymer of the copolymers of the above Examples and Comparative examples A- E and the content (%) of the tetrahydrofuran-insoluble portion of the copolymers, relative to the amount of crosslinking agent added at the time of copolymerization are illustrated in the accompanying drawings. Fig. 1 shows the case of crosslinking agent PTMGA and Fig. 2 shows the case of DAP. First, as to the relationship between the amount of crosslinking agent added and the polymerization degree, it is seen from Fig. 1 that in the case of the present invention, the polymerization degree is constant irrespectively of the amount of crosslinking agent added, whereas it is seen from Fig. 2 that in the case of DAP, there is a drawback that when its amount added reaches a certain amount, the polymerization degree rapidly increases. Next, as to the relationship between the amount of crosslinking agent added and the content of the tetrahydrofuran-insoluble portion, it is seen that as its amount added increases, the content gradually increases, and by merely varying the amount of crosslinking agent added, it is possible to optionally adjust the content of the insoluble portion of copolymer. Whereas in the case of DAP of Fig. 2, if its amount added is small, the amount of the insoluble portion is small and rapidly increases in a certain amount of the amount added; hence it is seen that it is very difficult to optionally adjust the content of the insoluble portion at a certain polymerization degree. Examples and Comparative examples (F) Examples and Comparative examples (B) were repeated except that the crosslinking agent was replaced by polyethylene glycol diacrylate (n=14) (hereinafter abbreviated to PEGDA), polypropylene glycol diacrylate (n=12) (hereinafter abbreviated to PPGDA), polytetramethylene ether glycol dimethacrylate (n=10) (herein- after abbreviated to PTMGMA), diacrylate of polyester polyol of adipic acid with neopentyl glycol (n=5) (hereinafter abbreviated to PESDA), dimethacrylate of the above polyester polyol (n=5) (hereinafter abbreviated to PESMA) or triallyl cyanurate (hereinafter abbreviated to TAC). The results are shown in Table F. Table F (1) EMI26.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Note <tb> Run <SEP> ization <tb> temper- <SEP> Kind <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Delusterature <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <tb> ( C) <SEP> degree <SEP> (%) <SEP> property <tb> Compar. <tb> F-1 <SEP> 57 <SEP> PEGDA <SEP> 0 <SEP> 1040 <SEP> 0 <SEP> o <SEP> x <tb> ex. <tb> " <SEP> 2 <SEP> " <SEP> " <SEP> 0.05 <SEP> 1030 <SEP> 0.2 <SEP> o <SEP> x <SEP> " <tb> " <SEP> 3 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1020 <SEP> 2.7 <SEP> o <SEP> &num; <SEP> Example <tb> " <SEP> 4 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1010 <SEP> 9.0 <SEP> o <SEP> o <SEP> " <tb> " <SEP> 5 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1010 <SEP> 17.0 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 6 <SEP> " <SEP> " <SEP> 1.0 <SEP> 1010 <SEP> 30.0 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 7 <SEP> " <SEP> " <SEP> 2.0 <SEP> 1000 <SEP> 41.8 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 8 <SEP> " <SEP> " <SEP> 3.0 <SEP> 980 <SEP> 48.5 <SEP> &num; <SEP> &num; <SEP> " <tb> Compar. <tb> " <SEP> 9 <SEP> " <SEP> PPGDA <SEP> 0 <SEP> 1020 <SEP> 0 <SEP> o <SEP> x <tb> ex. <tb> " <SEP> 10 <SEP> " <SEP> " <SEP> 0.05 <SEP> 1040 <SEP> 0.2 <SEP> o <SEP> x <SEP> " <tb> " <SEP> 11 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1030 <SEP> 2.5 <SEP> o <SEP> &num; <SEP> Example <tb> " <SEP> 12 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1030 <SEP> 8.5 <SEP> o <SEP> o <SEP> " <tb> " <SEP> 13 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1010 <SEP> 16.5 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 14 <SEP> " <SEP> " <SEP> 1.0 <SEP> 1000 <SEP> 28.0 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 15 <SEP> " <SEP> " <SEP> 2.0 <SEP> 1010 <SEP> 41.5 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 16 <SEP> " <SEP> " <SEP> 3.0 <SEP> 990 <SEP> 45.3 <SEP> &num; <SEP> &num; <SEP> " <tb> Table F (2) EMI27.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Note <tb> Run <SEP> ization <tb> temper- <SEP> Kind <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Delusterature <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <tb> ( C) <SEP> degree <SEP> (%) <SEP> property <tb> Compar. <tb> F-17 <SEP> 57 <SEP> PTMGMA <SEP> 0 <SEP> 1040 <SEP> 0 <SEP> o <SEP> x <tb> ex. <tb> " <SEP> 18 <SEP> " <SEP> " <SEP> 0.05 <SEP> 1020 <SEP> 0.2 <SEP> o <SEP> x <SEP> " <tb> " <SEP> 19 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1030 <SEP> 2.5 <SEP> o <SEP> &num; <SEP> Example <tb> " <SEP> 20 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1010 <SEP> 8.1 <SEP> o <SEP> o <SEP> " <tb> " <SEP> 21 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1030 <SEP> 15.8 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 22 <SEP> " <SEP> " <SEP> 1.0 <SEP> 1010 <SEP> 28.0 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 23 <SEP> " <SEP> " <SEP> 2.0 <SEP> 1000 <SEP> 37.5 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 24 <SEP> " <SEP> " <SEP> 3.0 <SEP> 990 <SEP> 41.8 <SEP> &num; <SEP> &num; <SEP> " <tb> Compar. <tb> " <SEP> 25 <SEP> " <SEP> PESDA <SEP> 0 <SEP> 1040 <SEP> 0 <SEP> o <SEP> x <tb> ex. <tb> " <SEP> 26 <SEP> " <SEP> " <SEP> 0.05 <SEP> 1020 <SEP> 0.3 <SEP> o <SEP> x <SEP> " <tb> " <SEP> 27 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1030 <SEP> 3.0 <SEP> o <SEP> &num; <SEP> Example <tb> " <SEP> 28 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1020 <SEP> 9.0 <SEP> o <SEP> o <SEP> " <tb> " <SEP> 29 <SEP> " <SEP> " <SEP> 0.5 <SEP> 990 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 30 <SEP> " <SEP> " <SEP> 1.0 <SEP> 1000 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 31 <SEP> " <SEP> " <SEP> 2.0 <SEP> 980 <SEP> 45.0 <SEP> &num; <SEP> &num; <SEP> " <tb> " <SEP> 32 <SEP> " <SEP> " <SEP> 3.0 <SEP> 980 <SEP> 52.6 <SEP> x <SEP> &num; <SEP> " <tb> Table (F) EMI28.1 <SEP> Polymer- <SEP> Crosslinking <SEP> agent <SEP> Copolymer <SEP> Molded <SEP> product <tb> Note <tb> Run <SEP> ization <tb> temper- <SEP> Kind <SEP> Part <SEP> by <SEP> Polymer- <SEP> Insoluble <SEP> Process- <SEP> Delusterature <SEP> weight <SEP> * <SEP> ization <SEP> portion <SEP> ability <SEP> ing <tb> ( C) <SEP> degree <SEP> (%) <SEP> properties <tb> Compar. <tb> F-33 <SEP> 57 <SEP> PESMA <SEP> 0 <SEP> 1030 <SEP> 0 <SEP> o <SEP> x <tb> ex. <tb> " <SEP> 34 <SEP> " <SEP> " <SEP> 0.05 <SEP> 1010 <SEP> 0.3 <SEP> o <SEP> x <SEP> " <tb> " <SEP> 35 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1030 <SEP> 3.1 <SEP> o <SEP> &num; <SEP> Example <tb> " <SEP> 36 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1020 <SEP> 9.25 <SEP> o <SEP> o <SEP> " <tb> " <SEP> 37 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1000 <SEP> 20.0 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 38 <SEP> " <SEP> " <SEP> 1.0 <SEP> 970 <SEP> 31.6 <SEP> o <SEP> &num; <SEP> " <tb> " <SEP> 39 <SEP> " <SEP> " <SEP> 2.0 <SEP> 980 <SEP> 45.0 <SEP> &num; <SEP> &num; <SEP> " <tb> " <SEP> 40 <SEP> " <SEP> " <SEP> 3.0 <SEP> 970 <SEP> 53.0 <SEP> x <SEP> &num; <SEP> " <tb> Compar. <tb> " <SEP> 41 <SEP> " <SEP> TAC <SEP> 0.05 <SEP> 1180 <SEP> 2.0 <SEP> o <SEP> x <tb> ex. <tb> " <SEP> 42 <SEP> " <SEP> " <SEP> 0.1 <SEP> 1340 <SEP> 8.0 <SEP> o <SEP> x <SEP> " <tb> " <SEP> 43 <SEP> " <SEP> " <SEP> 0.2 <SEP> 1800 <SEP> 11.0 <SEP> x <SEP> &num; <SEP> " <tb> " <SEP> 44 <SEP> " <SEP> " <SEP> 0.3 <SEP> 2100 <SEP> 22.0 <SEP> x <SEP> o <SEP> " <tb> " <SEP> 45 <SEP> " <SEP> " <SEP> 0.4 <SEP> 1600 <SEP> 36.5 <SEP> x <SEP> &num; <SEP> " <tb> " <SEP> 46 <SEP> " <SEP> " <SEP> 0.5 <SEP> 1350 <SEP> 48.0 <SEP> x <SEP> &num; <SEP> " <tb> " <SEP> 47 <SEP> " <SEP> " <SEP> 1.0 <SEP> 840 <SEP> 85.0 <SEP> x <SEP> xx <SEP> " <tb>

Claims: CLAIMS 1. A process for producing vinyl chloride polymers by copolymerizing vinyl chloride monomer with a crosslinking agent, which comprises copolymerizing 100 parts by weight of vinyl chloride monomer with 0.1 to 3 parts by weight of a crosslinking agent which is at least one compound which is a diacrylate or dimethacrylate of a polyether glycol or a diacrylate or dimethacrylate of a polyester glycol and has an average molecular weight of 200 to 2,000, while maintaining the copolymerization temperature at a constant value in the range of 300C to 70 C. 2. A process according to claim 1, wherein the crosslinking agent includes a diacrylate or dimethacrylate of a polyether glycol expressed by the general formula EMI29.1 and/or the crosslinking agent includes a diacrylate or dimethacrylate of polyester polyol expressed by the general formula EMI29.2 (wherein R is a hydrogen atom or methyl group; D is an alkanediyl group of 2 to 6 carbon atoms; D2 is an alkanediyl group of 2 to 6 carbon atoms or a phenylene group; n is an integer of 2 to 200; and m is an integer of 2 to 40).

Inventors: KOGA, SHIGEHIRO, NAKANO, KAZUAKI, SATOMI, KATSUHIRO, UEMURA, KATSUOKI, YAMADA, TETSUYA
Applicants: CHISSO CORPORATION
Application year: 1983
Main classification: C08F14
IPC codes: C08L27, C08F299, C08F20, C08F214, C08F14