Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/005—Processes for mixing polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/12—Powdering or granulating
  • C08J3/124—Treatment for improving the free-flowing characteristics
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
  • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L27/04—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
  • C08L27/06—Homopolymers or copolymers of vinyl chloride
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
  • C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
  • C08J2327/04—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
  • C08J2327/06—Homopolymers or copolymers of vinyl chloride
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L73/00—Compositions of macromolecular compounds obtained by reactions forming a linkage containing oxygen or oxygen and carbon in the main chain, not provided for in groups C08L59/00 - C08L71/00; Compositions of derivatives of such polymers

Definitions

• This invention relates to a novel product and process for preparing a free-flowing plasticized powdered polyvinyl chloride composition which is especially useful for slush molding processes.
• Nonporous polyvinyl chloride containing both conventional low molecular weight plasticizers and high molecular weight plasticizers is disclosed in the above-mentioned patent. Incorporating the high and low molecular weight plasticizers with the nonporous polyvinyl chloride is accomplished by blending the composition on a mill above the the melt temperature of the polyvinyl chloride or by blending a solution of polyvinyl chloride in tetrahydrofuran and the high and low molecular weight plasticizers in tetrahydrofuran, followed by evaporating the tetrahydrofuran. In either case, unfortunately, the resulting plasticized polyvinyl chloride is not in powdered form, (which is the only form that can be used in slush molding
• the present invention i ⁇ ' directed to a process for preparing a free-flowing plasticized powdered polyvinyl chloride composition, especially useful for slush molding applications, which comprises blending in a mixer about 20-65 weight percent, based on the weight of polyvinyl chloride and plasticizers, of a combination of a high molecular weight solid ethylene-c ⁇ ntaining copolymer plasticizer for polyvinyl
• SUaSTFTUTl SHEET - 3 - chloride having a melt index at 190*C not greater than 3000 g/10 minutes and iscible with polyvinyl chloride and a low molecular weight liquid plasticizer for polyvinyl chloride having a molecular weight not greater than about 3000 in which the solid ethylene-containing copolymer plasticizer dissolves and wherein the weight ratio of high molecular weight plasticizer to low molecular weight plasticizer is from about 1:10 to 2.5:1 with about 35-80 weight percent, based on the weight of polyvinyl chloride and plasticizers, of porous polyvinyl chloride powder having substantially no impermeable skin and a porosity of from 0.1-0.7 ml/g so that the temperature of the composition during mixing is at least about 70'C but not more than about 130*C and mixing is continued until the plasticizers are absorbed in the porous polyvinyl chloride and a dry free-flowing powdered plasticized polyvinyl chloride is obtained.
• the novel free-flowing plasticized powdered polyvinyl chloride made by the process of this invention are ideally suited for processing, including "slush molding" processes, without any pretreatment.
• DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to the manufacture of free-flowing plasticized powdered polyvinyl chloride compositions that can be used without further treatment in slush molding processes.
• the polyvinyl chlorides are plasticized with a high molecular weight solid ethylene-containing copolymer plasticizer that is dissolved in a low molecular weight liquid plasticizer for the polyvinyl chloride.
• the free-flowing plasticized powdered polyvinyl chloride is obtained by blending in a high speed mixer the solid high molecular weight plasticizer dissolved in the low molecular weight plasticizer with
• High speed mixing conditions result in the temperature of the mixture rising to at least about 70*C but not more than about 130*C, which occurs in about 2-15 minutes, resulting in the low and high molecular weight plasticizers being absorbed into the porous polyvinyl chloride.
• the polyvinyl chloride and plasticizers in the mixer can be heated externally, if desired, but usually particle friction is adequate to reach the required temperature range.
• the plasticizers are absorbed in the polymers a free-flowing plasticized polyvinyl chloride powder is obtained.
• the polyvinyl chloride powder can be cooled while gently agitating the plasticized polymer.
• the free-flowing plasticized polyvinyl chloride polymer in powder form is especially useful in so-called "slush molding" processes.
• the polyvinyl chloride used in the process of this invention has substantially no discernible skin and has a porosity of from 0.1-0.7 ml/g, preferably 0.35-0.7 ml/g, measured according to ASTM D2873-70.
• Such porous polyvinyl chlorides used in the process of this invention may be prepared by first polymerizing the vinyl chloride monomer with a monomer soluble polymerization initiator, such as lauryl peroxide, in the presence of a monomer soluble dispersing agent, to about 5-12% conversion, either in mass or together with a smaller amount of water than monomer such that the monomer is the continuous phase (generally up to one third of the mixture is water) , then adding sufficient water to cause a phase inversion, so that water is the continuous phase (usually water is half or more than half the weight of the mixture) with the partially polymerized monomer dispersed in it, then completing
• Porous substantially skinless polyvinyl chlorides can also be made by suspension polymerization without phase inversion, water always being the continuous phase.
• the process for preparing these polyvinyl chlorides employes an ionic sensitive primary dispersant capable of thickening water and at least one secondary dispersant, where the ionic sensitive dispersant is charged to the polymerization at about 1-5% conversion. This method is further described in detail in U.S. Patent No. 4,711,908.
• a substantially skinless, porous polyvinyl chloride in order to make a plasticized free-flowing powder that contains a high molecular weight plasticizer.
• the skinless porous polyvinyl chloride subjected to high intensity mixing readily absorbs the high molecular weight plasticizer that is dissolved in the low molecular weight plasticizer.
• Such skinless, porous polyvinyl chloride are commercially available and sold under the trade name VYGEN ® polyvinyl chloride resin available from General Tire and Rubber Company and GEON ® polyvinyl chloride resin available from B. F. Goodrich Company.
• the high molecular weight solid ethylene- containing copolymer plasticizers for the substantially skinless, porous polyvinyl chlorides that are used in the process of this invention have a melt index at 190*C not greater than about 3000 g/10 minutes according to ASTM D1238-65T condition E usually 1-3000 g/10 minutes, preferably 5-300 g/10 minutes.
• the solid plasticizers used are miscible with the polyvinyl chloride and they are soluble in the low molecular weight plasticizer.
• the solid high molecular weight plasticizers are dissolved in the low molecular weight plasticizer and blended with a high speed mixer so that the plasticizers are absorbed in the porous polyvinyl chloride.
• the solid ethylene-containing copolymer plasticizers used in the process of this invention include ethylene-containing vinyl acetate copolymers, having at least about 55 weight percent to about 75 weight percent vinyl acetate, thus making the plasticizer miscible with the polyvinyl chloride.
• the ethylene vinyl acetate copolymers plasticizer can also contain either carbon monoxide or sulfur dioxide, usually in amounts of from 2-30 weight percent preferably 5-15 weight percent.
• Ethylene-containing copolymer plasticizers also include ethylene/alkyl ethacrylate/carbon monoxide or sulfur dioxide copolymers, wherein the alkyl group is from 1-8 carbon atoms, preferably 4 or 8 carbon atoms, containing 20-50 weight percent alkyl ethacrylate, and 2-30 weight percent, preferably 5-15 weight percent, of either carbon monoxide or sulfur dioxide, the balance
• Plasticizers include ethylene/vinyl acetate, ethylene/vinyl acetate/carbon monoxide or sulfur dioxide, ethylene/n-butyl acrylate/carbon monoxide, ethylene/methyl ethacrylate/carbon monoxide, or sufur dioxide, ethylene/ethyl acrylate/carbon monoxide or sulfur dioxide, ethylene/methyl acrylate/carbon monoxide or sulfur dioxide, ethylene/hexyl acrylate/sulfur dioxide.
• Plasticizers of the type described above are well known products and are further described in U.S. Patent 3,780,140 and 3,684,778.
• the low molecular weight liquid plasticizers in which the high molecular weight plasticizers are dissolved are well known plasticizer for polyvinyl chloride.
• the low molecular weight plasticizers that can be onomeric or polymeric have a molecular weight not greater than 3500, usually from 1000-3000.
• the amount of low molecular weight plasticizer added to the polyvinyl chloride is generally from, by weight, 5-50 percent, preferably 10-30 percent based on the plasticizer polymer.
• Representative low molecular weight liquid plasticizers that can be used in the present process that are conventionally used to plasticize polyvinyl chloride include phthalates, adipates, azealates, trimellitates, phosphate esters and polyesters. The phthalate esters are most commonly
• the adipates and azelates impart improved low temperature properties to the polymers.
• the phosphates render the polymers flame retardant.
• Higher alkyl phthalates, e.g., diundecyl phthalate improves fogging resistance of the polymer when used, for example, as dashboard covers in automobiles.
• Representative specific low molecular weight liquid plasticizers that can be used in the process of this invention include dio ⁇ tyl phthalate, diundecyl phthalate, dibutyl adipate, dibenzylazelate, trioctyltrimellitate, diphenyl octylphosphate and low molecular weight polyesters and polypropylene glycol. These low molecular weight plasticizers for polyvinyl chloride are well known in the art and they are described in Modern Plastics Encyclopedia, Vol. 57, page 222, 1980-1981.
• the weight ratio of high molecular weight solid plasticizer to low molecular weight liquid plasticizer is from 1:10 to 2.5:1, preferably from 1:5 to 1:2.5. If the ratio is less than 1:10 then tear strength of products made from the polymer is not improved significantly and if the ratio is greater than 2.5:1 then uniform and rapid incorporation of plasticizers is not achieved and slush molding is not feasible.
• nonporous dispersion grade polyvinyl chloride can be added to the porous polyvinyl chloride and plasticizers in the mixer.
• stabilizers are invariably added to the polymer.
• a large variety of stabilizers are used that are customized for polyvinyl chloride that include inorganic and organometallic compounds, such as lead, barium-cadmium, cadmium-zinc, also nitrogenous and epoxy compounds are well know stabilizers.
• Such stabilizers used by those working in this technology include a barium-zinc soap stabilizer, epoxidized soybean oil and inorganic salts. Usually, these stabilizers are present in amounts from about 5 to 10 weight percent based on the polyvinyl chloride.
• Antioxidants are added to ethylene copolymers because of their sensitivity to air oxidation.
• Antioxidants used are selected phenolic types and secondary antioxidants such as thioethers and phosphites.
• Representative antioxidants include dilauryl thiodipropionate, ditridecyl thiodipropionate, tris(nonylphenyl)phosphite, butylated hydroxy toluene, and tetrakis methylene (3,5-di-tert-butyl-4- hydroxyhydrocinna ate) methane.
• these antioxidants are present in amounts of 300 to 1600 ppm for the phenolics, and in amounts of 300 to 10,000 ppm for the thioethers and phosphites based on the ethylene copolymers.
• Slush molding is an inexpensive process which enables powdered materials to be molded in an open hollow mold, without pressure or shear. Open hollow shapes are produced by this technique with lightweight inexpensive molds. Simulated slush molding was carried out on the plasticized composition prepared in the following examples by spreading the free-flowing plasticized powdered polyvinyl chloride inside a chase on a metal plate, covering the polyvinyl chloride powder filled cavity with another plate and placing the
• Example 1 Six hundred forty grams (30 wt. %) of the low molecular weight liquid plasticizer diundecyl phthalate (DUP) having a molecular weight of 474, 0.21 grams of Irganox 1010, a hindered phenolic antioxidant, i.e., tetrakis ethylene (3,5-di-tert-butyl-4- hydroxyhydrocinnamate) ethane, and 1.07 grams of the antioxidant dilauryl thiodipropionate (DLTDP) , was heated to 120 * C with mechanical stirring.
• DUP low molecular weight liquid plasticizer diundecyl phthalate
• SUBSTITUTESHEET - 11 - having substantially no impervious skin and a porosity greater than 0.35 ml/g, 46.4 grams of a barium zinc soap stabilizer (Mark 6708) , 28 grams of an inorganic salt containing sodium and calcium cations and perchlorate anions. 61 grams of epoxidized soybean oil stabilizer were added to a high speed Welex mixer operated at 2500 rpm. Mixing was continued until the temperature of the PVC composition reached 80*C.
• a barium zinc soap stabilizer Mark 6708
• the ENB ⁇ CO copolymer plasticizer dissolved in DUP was then added slowly to the Welex high speed mixer, operated at 2500 rpm, containing the porous PVC. The temperature during mixing without external heating was allowed to rise to about 110 ° C due to particle friction. The Welex mixer was run until the addition of the ENBACO copolymer dissolved in the DUP plasticizer was complete. Sixty-one grams (2.8 weight percent) of a fine powdered dispersion grade nonporous PVC (Geon ® 141) was then added to the blend in the mixer to further improve the flow characteristic of the plasticized PVC powder.
• a fine powdered dispersion grade nonporous PVC Geon ® 141
• the speed of the mixer was then lowered to 1000 rpm and with cool water circulated in a jacket on the mixer the PVC composition was cooled to 60 * c.
• the resulting plasticized PVC composition containing the high and low molecular weight plasticizers absorbed therein was in the form of a dry free-flowing powder.
• the dry powder was screened using a 20 mesh screen and was successfully slush molded as described hereinabove. Tear strength on a plaque of the slush molded plasticized PVC was determined using die C tear ASTM D624 and the value was 307 lbs./inch.
• Example 2 The procedure described above in Example 1 was substantially repeated except 222 grams (10.39 weight percent) of the solid plasticizer (64%)
• Example 4 The procedure described above in Example 1 was substantially repeated except 337 grams (15.8 weight percent) of the solid plasticizer (51.3%) ethylene/(38.9%) n-butyl aerylate/(9.8%) carbon monoxide copolymer (ENBACO) having a melt index at 190" of 85.6 was added to 517 grams (24.2 weight percent) of the liquid plasticizer DUP containing 0.34 grams Irganox 1010. (The DLTDP was omitted from this formulation.) The solution of plasticizers was added to 1220 grams (57.2 weight percent) of the porous substantially skinless PVC. The resulting plasticized dry free-flowing powdered PVC was successfully slush molded as described hereinabove. Tear strength on a plaque of the molded plasticized PVC was 316 lbs./inch.
• Example 4 Example 4
• Example 2 The procedure described above in Example 1 was substantially repeated except ' that 214 grams (10 weight percent) of the solid plasticizer (31%) ethylene/(69%) vinyl acetate copolymer (EVA) having a melt index at 190°C of 21.3 was added in place of the ENBACO to 640 grams (30 weight percent) of the liquid plasticizer DUP. The resulting solution was then added to the porous substantially skinless PVC. The resulting plasticized dry free-flowing powdered PVC was
• Example 5 The procedure described above in Example 1 was substantially repeated except that 222 grams (10.5 weight percent) of the solid plasticizer (57.3%) ethylene/(32.8%) n-butyl acrylate/(9.9%) carbon monoxide copolymer (ENBACO) having a melt index at 190*C of 11.6 was added to 666 grams (31.6 weight percent) of the liquid plasticizer DUP.
• ENBACO carbon monoxide copolymer
• the resulting solution was added to 1220 grams (57.9%) of the porous substantially skinless PVC containing 31.7 grams of a barium zinc soap stabilizer mixture, 19 grams of a perchlorate salt stabilizer and 63.4 grams of epoxidized soybean oil stabilizer in the high speed Welex mixer. (Dispersion grade nonporous PVC was omitted from this formulation.)
• the resulting plasticized dry powdered PVC was successfully slush molded as described hereinabove.

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• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
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• Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

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• 1992
  • 1992-05-12 CA CA002103274A patent/CA2103274A1/en not_active Abandoned
  • 1992-05-12 AU AU20263/92A patent/AU659466B2/en not_active Ceased
  • 1992-05-12 JP JP50007693A patent/JP3361094B2/ja not_active Expired - Fee Related
  • 1992-05-12 WO PCT/US1992/003778 patent/WO1992020742A1/en active IP Right Grant
  • 1992-05-12 EP EP92912659A patent/EP0587727B1/en not_active Expired - Lifetime
  • 1992-05-12 DE DE69205280T patent/DE69205280T2/de not_active Expired - Fee Related
  • 1992-05-21 TW TW81103979A patent/TW252137B/zh active
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