Process for producing sheet-like structures from vinyl alcohol polymers

Claim 2

A process for the production of a sheet-like structure from a vinyl alcohol polymer which comprises, in sequence, the following steps: separately feeding into a self-cleaning multi-screw extruder, in the direction of product flow, first the vinyl alcohol polymer and then an amount of water which is insufficient to dissolve the polymer under standard conditions of temperature and pressure, and, while transporting them through the extruder, mixing the vinyl alcohol polymer and the water at temperatures in the range of from 20° to 100° C. to achieve uniform distribution of the polymer and the water, melting the polymer/water mixture and homogenizing the melt at temperatures in the range of from 80° to 200° C., devolatilizing the homogeneous melt to remove any excess water and to adjust the water content of the melt to the water content desired in the end product without the extrudability of the melt being adversely affected hereby and to remove other undesirable volatile constituents, and discharging the melt from the extruder while simultaneously shaping it into the sheet-like structure, wherein the stated temperatures being the barrel temperatures of the extruder.

Claim 3

The process of claim 1, wherein the amount of water added is about 5 to 40% by weight, based on the vinyl alcohol polymer.

Claim 4

The process of claim 1, wherein the melt is discharged from the extruder at temperatures in the range of from 80° to 130° C.

Claim 5

The process of claim 1, wherein further compounds are fed into the extruder and are homgeneously mixed into the vinyl alcohol polymer, said compounds being fed into the extruder at any point after the feed point of the vinyl alcohol polymer and before devolatilizing the homogeneous melt.

Claim 6

The process of claim 4, wherein said further compounds are selected from the group consisting of fillers, plasticizers, lubricants, dyes, pigments, stabilizers and compatible low molecular weight organic compounds.

Claim 7

The process of claim 1, wherein the vinyl alcohol polymer and water are mixed at temperatures in the range of 20° to 60° C.

Claim 8

The process of claim 1, wherein the melting of the polymer/water mixture and the homogenization of the melt is carried out at temperatures in the range of from 120° to 190° C.

Claim 9

A process for the production of a sheet-like structure of a vinyl alcohol polymer having homogeneously incorporated at least one compatible, ethylenically unsaturated, low molecular weight organic compound and at least one polymerization initiator, which process comprises the following steps: separately feeding into a self-cleaning multi-screw extruder in the direction of product flow, first the vinyl alcohol polymer and then an amount of water which is insufficient to dissolve the polymer under standard conditions of temperature and pressure, and while transporting them through the extruder, mixing the vinyl alcohol polymmer and the water at temperatures in the range of from 20° to 100° C. to achieve uniform distribution of the polymer and the water and melting the polymer/water mixture and homogenizing the melt at temperatures in the range of from 80° to 200° C., further feeding into the extruder, at any point after the feed point of the vinyl alcohol polymer but before the subsequent devolatilizing step, at least one ethylenically unsaturated, low molecular weight organic compound, which is compatible with the vinyl alcohol polymer, and at least one polyerization initiator and homogeneously mixing said further compounds with the vinyl alcohol polymer to finally achieve a homogeneous melt of the vinyl alcohol polymer containing the water and said further compounds, devolatilizing said homogeneous melt to remove excess water adjusting its water content to the water content desired in the end product without hereby adversely affecting the extrudability of the melt and to remove other undesirable volatile constituents, and discharging the melt from the extruder while simultaneously shaping it into the sheet-like structure, wherein the stated temperatures being the barrel temperatures of the extruder and are so adjusted that said ethylenically unsaturated organic compounds and said polymerization initiator do not react during extrusion.

Claim 10

A process for the production of a sheet-like structure of a vinyl alcohol polymer having homogeneously incorporated at least one compatible, ethylenically unsaturated, low molecular weight organic compound and at least one polymerization initiator, which process comprises the following steps: separately feeding into a self-cleaning multi-screw extruder in the direction of product flow, first the vinyl alcohol polymer and then an amount of water which is insufficient to dissolve the polymer under standard conditions of temperature and pressure, and while transporting them through the extruder, mixing the vinyl alcohol polymmer and the water at temperatures in the range of from 20° to 100° C. to achieve uniform distribution of the polymer and the water and melting the polymer/water mixture and homogenizing the melt at temperatures in the range of from 80° to 200° C., further feeding into the extruder, at any point after the feed point of the vinyl alcohol polymer but before the subsequent devolatilizing step, at least one ethylenically unsaturated, low molecular weight organic compound, which is compatible with the vinyl alcohol polymer, and at least one polyerization initiator and homogeneously mixing said further compounds with the vinyl alcohol polymer to finally achieve a homogeneous melt of the vinyl alcohol polymer containing the water and said further compounds, devolatilizing said homogeneous melt to remove excess water adjusting its water content to the water content desired in the end product without hereby adversely affecting the extrudability of the melt and to remove other undesirable volatile constituents, and discharging the melt from the extruder while simultaneously shaping it into the sheet-like structure, wherein the stated temperatures being the barrel temperatures of the extruder and are so adjusted that said ethylenically unsaturated organic compounds and said polymerization initiator do not react during extrusion.

Claim 11

The process of claim 8, wherein the amount of water added is about 5 to 40% by weight, based on the vinyl alcohol polymer.

Claim 12

The process of claim 8, wherein the melt is discharged from the extruder at temperatures in the range of from 80° to 130° C.

Claim 13

The process of claim 8, wherein further to the ethylenically unsaturated, low molecular weight organic compound and the polymerizationn initiator, one or more additives, selected from the group consisting of fillers, plasticizers, lubricants, dyes, pigments, stabilizers, thermal polymerization inhibitors and compatible, saturated, low molecular weight organic compounds, are fed into the extruder and are homogeneously mixed in the vinyl alcohol polymer, said additives being fed into the extruder at any point after the feed point of the vinyl alcohol polymer and before devolatilizing the homogeneous melt.

Claim 14

The process of claim 8, wherein said ethylenically unsaturated low molecular weight compound is a photopolymerizable compound and said polymerization initiator is a photoinitiator.

Claim 15

The process of claim 12, wherein the ratio of the vinyl alcohol polymer to the photopolymerizable low molecular weight compound is from 90:10 to 50:50 by weight.

Claim 16

The process of claim 8, wherein the mixing of the vinyl alcohol polymer with the water is carried out at temperatures in the range of from 20° to 60° C.

Claim 17

The process of claim 8, wherein the melting of the polymer/water mixture and the homogenization of the melt is carried out at temperatures in the range of from 120° to 190° C.

Claim 18

The process of claim 1, wherein the melt is extruded in form of a sheeting or panel, the thickness of which is subsequently adjusted by passing the extruded sheeting or panel through a two-roll or multi-roll calendar.

Claim 19

The process of 8, wherein the melt is extruded in form of a sheeting or panel, the thickness of which is subsequently adjusted by passing the extruded sheeting or panel through a two-roll or multi-roll calendar.

Claim 20

The process of 8, wherein the melt is extruded in form of a sheeting or panel, the thickness of which is subsequently adjusted by passing the extruded sheeting or panel through a two-roll or multi-roll calendar.