Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
383 words
A process for preparing multilayer articles consisting of at least two layers made of different thermoplastic materials and characterized in being impermeable to gases, vapors and odors, by coextruding at least two different thermoplastic polymers at least one of which is polyvinyl alcohol having a polymerization degree of from 600 to 1,500 and a hydrolysis degree of at least 85% by mols, and successively molding the coextruded article, said process comprising the following steps: (a) feeding to an extruder connected with a coextrusion head a polyvinyl alcohol having the stated hydrolysis degree pre-mixed with an aqueous mixture of plasticizing compounds in an amount not higher than 50% by weight with respect to the polyvinyl alcohol and heating the polyvinyl alcohol/aqueous plasticizing compounds mixture in the extruder under pressure to bring it to the plastisol state; (b) raising the temperature of the polyvinyl alcohol/aqueous plasticizing compounds mixture, before the mixture enters the coextrusion head, to the temperature at least equal to that reached by the mixture in the coextrusion head, and subjecting the mixture, while it is at such relatively high temperature, to rapid decompression with simultaneous venting of the evolved vapors; (c) separately feeding at least one other thermoplastic polymer in the molten state and selected from the group consisting of polystyrene, polyvinyl chloride, foamed polystyrene, nylon 6, nylon 66, polyethylene terephthalate, chlorinated polyethylene, polyvinylidene chloride, polyvinyl acetate, polyolefins obtained by polymerizing ethylenically unsaturated monomers of the formula CH 2 ═CHR, in which R is hydrogen or a hydrocarbon radical containing 1 to 20 C atoms either alone or with one another, and polymers obtained by polymerizing said monomers CH 2 ═CHR with other comonomers copolymerizable therewith and containing from 0.05 to 20% by weight of comonomer, to the same coextrusion head; (d) adjusting the temperature of the polymers when they are in contact so that the temperature of the polyvinyl alcohol is at least equal to the temperature of the other coextruded polymer or polymers; (e) adjusting the flow rate of the polymers so that the outflow linear velocities are equal or differ no more than ±10%; and (f) coextruding the polyvinyl alcohol/aqueous mixture of plasticizing compounds and the other thermoplastic polymer and molding the article comprising the coextruded and bonded layers leaving the coextrusion head to obtain a shaped, manufactured article.
Claim 2
Dependent Claim
383 words
A process for preparing multilayer articles consisting of at least two layers made of different thermoplastic materials and characterized in being impermeable to gases, vapors and odors, by coextruding at least two different thermoplastic polymers at least one of which is polyvinyl alcohol having a polymerization degree of from 600 to 1,500 and a hydrolysis degree of at least 85% by mols, and successively molding the coextruded article, said process comprising the following steps: (a) feeding to an extruder connected with a coextrusion head a polyvinyl alcohol having the stated hydrolysis degree pre-mixed with an aqueous mixture of plasticizing compounds in an amount not higher than 50% by weight with respect to the polyvinyl alcohol and heating the polyvinyl alcohol/aqueous plasticizing compounds mixture in the extruder under pressure to bring it to the plastisol state; (b) raising the temperature of the polyvinyl alcohol/aqueous plasticizing compounds mixture, before the mixture enters the coextrusion head, to the temperature at least equal to that reached by the mixture in the coextrusion head, and subjecting the mixture, while it is at such relatively high temperature, to rapid decompression with simultaneous venting of the evolved vapors; (c) separately feeding at least one other thermoplastic polymer in the molten state and selected from the group consisting of polystyrene, polyvinyl chloride, foamed polystyrene, nylon 6, nylon 66, polyethylene terephthalate, chlorinated polyethylene, polyvinylidene chloride, polyvinyl acetate, polyolefins obtained by polymerizing ethylenically unsaturated monomers of the formula CH 2 ═CHR, in which R is hydrogen or a hydrocarbon radical containing 1 to 20 C atoms either alone or with one another, and polymers obtained by polymerizing said monomers CH 2 ═CHR with other comonomers copolymerizable therewith and containing from 0.05 to 20% by weight of comonomer, to the same coextrusion head; (d) adjusting the temperature of the polymers when they are in contact so that the temperature of the polyvinyl alcohol is at least equal to the temperature of the other coextruded polymer or polymers; (e) adjusting the flow rate of the polymers so that the outflow linear velocities are equal or differ no more than ±10%; and (f) coextruding the polyvinyl alcohol/aqueous mixture of plasticizing compounds and the other thermoplastic polymer and molding the article comprising the coextruded and bonded layers leaving the coextrusion head to obtain a shaped, manufactured article.
Claim 3
Dependent Claim
17 words
The process of claim 1, in which the polyvinyl alcohol has a polymerization degree higher than 900.
Claim 4
Dependent Claim
21 words
The process of claim 1, in which the polyvinyl alcohol is plasticized with a mixture of water with a polyvalent alcohol.
Claim 5
Dependent Claim
29 words
The process of claim 3, in which the plasticizing mixture contains from 7 to 20% by weight of water and from 8 to 25% weight of a polyvalent alcohol.
Claim 6
Dependent Claim
12 words
The process of claim 3, in which the polyvalent alcohol is glycerin.
Claim 7
Dependent Claim
35 words
The process of claim 1, in which the polyvinyl alcohol is stabilized with 1 to 3 parts percent of a stearate of a metal of the first or second group of the Mendelyeev Periodic Table.
Claim 8
Dependent Claim
47 words
The process of claim 1, in which the extruder by which the polyvinyl alcohol is fed to the coextrusion head has a high length/diameter ratio and in said extruder the polyvinyl alcohol is brought to the plastisol state by heating to a temperature higher than 150° C.
Claim 9
Dependent Claim
17 words
The process of claim 7, in which the length/diameter ratio of the extruder is higher than 25.
Claim 10
Dependent Claim
24 words
The process of claim 1, in which the pressure to which the polyvinyl alcohol is subjected in the extruder is higher than 30 atmospheres.
Claim 11
Dependent Claim
74 words
The process of claim 1, in which the screw of the extruder for the polyvinyl alcohol is shaped so as to divide the extruder into the folloiwng five zones maintained at different temperatures, the temperature increasing until the third zone: feeding zone of the polymer: maintained at 140°-200° C.; compression zone: maintained at 150°-210° C.; decompression zone: maintained at 170°-220° C.; recompression zone: maintained at 170°-215° C.; and proportioning zone: maintained at 170°-205° C.
Claim 12
Dependent Claim
22 words
The process of claim 10, in which the coextrusion head is maintained at a temperature lower than that of the decompression zone.
Claim 13
Dependent Claim
31 words
The process of claim 1, in which the thermoplastic polymer different from polyvinyl alcohol is molten and fed to the extrusion head at a temperature comprised between 120° and 200° C.
Claim 14
Dependent Claim
41 words
The process of claim 1, in which the temperature of the polyvinyl alcohol is at least equal to that of the other coextruded polymer or polymers, when it comes in contact therewith, the temperature difference being not higher than 70° C.
Claim 15
Dependent Claim
27 words
The process of claim 1, in which molding of the parison into a manufactured article occurs in the shortest possible time and not longer than 5 minutes.
Claim 16
Dependent Claim
19 words
The process of claim 1, in which the extruder is equipped, in proximity to the vent, with an exhauster.
Claim 17
Dependent Claim
31 words
The process of claim 1, in which the temperature of the polyvinyl alcohol is higher than the temperature of the other coextruded polymer or polymers, when it comes in contact therewith.
Claim 18
Dependent Claim
32 words
The process of claim 10, in which the temperature in the coextrusion head is lower than the temperature in the decompression zone and in the range from 160° C. to 200° C.
Claim 19
Dependent Claim
14 words
The process of claim 1, in which the coextruded thermoplastic polymer is a polyolefin.
Claim 20
Dependent Claim
23 words
The process of claim 18, in which the polyolefin is high density polyethylene, low density polyethylene, or polypropylene having a high isotactic index.