Process for manufacture of plasticized homopolymeric polyvinyl alcohol and plasticized polyvinyl alcohol polymer obtained therefrom
The invention describes a method for the manufacture of a plasticized polyvinyl alcohol polymer mixture including the steps of: introducing into a mixing reactor a polyvinyl alcohol polymer comprising homopolymeric polyvinyl alcohol or a blend thereof having a degree of hydrolysis in the range of 93% to less than 98% or more; where the plasticizer comprises two or more compounds selected from the group consisting of diglycerol, triglycerol, xylose, D-mannitol, triacetin, dipentaerythritol, 1,4-butanediol, 3,3-dimethyl-1,2-butanediol, and caprolactam; reacting the water, the plasticizer and the polyvinyl alcohol polymer in the reaction zone to form the plasticized polymer; and allowing the plasticized polyvinyl alcohol polymer to pass from the primary outlet.
1. A method for manufacture of plasticized homopolymeric polyvinyl alcohol, the method comprising the steps of:
introducing into a mixing reactor a polyvinyl alcohol polymer comprising polyvinyl alcohol or a blend thereof having a degree of hydrolysis in the range of 93 wt % or greater;
wherein the mixing reactor comprises a blending chamber having a primary inlet, a primary outlet and at least two inter-engaging components extending between the primary inlet and the primary outlet, the inter-engaging components being arranged to apply a shearing force to the polyvinyl alcohol polymer while the polyvinyl alcohol polymer is conveyed by the components from the primary inlet through a reaction zone to the primary outlet;
one or more secondary inlets located downstream from the primary inlet for introducing reactants comprising a processing aid, a plasticizer and a reactive stabilizer to the blending chamber to form a reaction mixture;
wherein the plasticizer comprises two compounds selected from the group consisting of: diglycerol, triglycerol, xylose, D-mannitol, dipentaerythritol, triacetin, 1,4 butanediol, 3,3-dimethyl-1,2-butanediol, caprolactam and mixtures thereof;
wherein the reactive stabilizer is selected from the group consisting of:
potassium oleate, sodium benzoate, and mixtures thereof;
wherein the blending chamber comprises a plurality of heated regions arranged so that the mixture is subjected to a temperature profile whereby the temperature increases from the primary inlet to the primary outlet;
a secondary outlet located between the reaction zone and primary outlet arranged to allow removal of processing aid from the chamber;
reacting the processing agent, plasticizer and polyvinyl alcohol polymer in the reaction zone to form plasticizer polyvinyl alcohol polymer; and
allowing the plasticized polyvinyl alcohol polymer to pass from the primary outlet.
2. The method as claimed in claim 1 , wherein the reactive stabilizer is sodium benzoate.
3. The method as claimed in claim 1 , wherein the amount of the reactive stabilizer is from 0.2 wt % to 5 wt %.
4. The method as claimed in claim 3 , wherein the amount of the reactive stabilizer is from 0.5 wt % to 3 wt %.
5. The method as claimed in claim 4 , wherein the amount of the reactive stabilizer is from 0.5 wt % to 2 wt %.
6. The method as claimed in claim 5 , wherein the amount of reactive stabilizer is from 0.5 wt % to 1.5 wt %.
7. The method as claimed in claim 1 , wherein the polyvinyl alcohol polymer comprises polyvinyl alcohol or a blend thereof wherein the polyvinyl alcohol has a degree of hydrolysis of 93 wt % to less than 98 wt %.
8. The method as claimed in claim 7 , wherein the degree of hydrolysis is 93 wt % to 97 wt %.
9. The method as claimed in claim 8 , wherein the degree of hydrolysis is 93 wt % to 95 wt %.
10. The method as claimed in claim 1 , wherein the polyvinyl alcohol polymer is a blend of two or more homopolymeric polyvinyl alcohol polymers with a relatively high molecular weight and a relatively low molecular weight respectively.
11. The method as claimed in claim 10 , wherein the blend comprises a low viscosity grade having a molecular weight in the range 13,000 to 27,000 and a degree of polymerization of 300-600 and a medium/high viscosity grade having a molecular weight in the range 107,000 to 120,000 and a degree of polymerization of 2,400 to 2,600.
12. The method as claimed in claim 1 , wherein the plasticizer comprises two compounds selected from the group consisting of: D-mannitol, triacetin, dipentaerythritol- and caprolactam.
13. The method as claimed in claim 1 , wherein the plasticizer comprises triacetin and dipentaerythritol, triacetin and caprolactam or D-mannitol and dipentaerythritol.
14. The method as claimed in claim 5 , wherein the amount of reactive stabilizer is 1 wt %.