IP Library › Granted Patent US 12,359,373
Granted Patent B2
US 12,359,373 · App. 17/446,072 · Granted Jul 15, 2025

Polyvinyl alcohol coated cellulosic products

Inventors: John Williams (Chirbury, GB); Sian Griffiths (Conwy, GB); Robert Ashworth (Conwy, GB); David Lee Meadows (Hartpury, GB)
Assignee: Aquapak IP Limited
D21H19/20C09D7/48C09D7/63C09D129/04D21H23/46C08K5/06C08K5/098C08K5/3412C08K2201/014
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Quick Facts
Patent No.
US 12,359,373
App. No.
17/446,072
Granted
Jul 15, 2025
Kind
B2
Abstract

A method of manufacture of a coated material is provided. A polyvinyl alcohol polymer, where the polyvinyl alcohol polymer has a degree of hydrolysis of 90% or greater and a melting point in the range of 180° C. to 225° C. is melted on a cellulosic substrate and extruded to form a molten polyvinyl alcohol polymeric film which is then applied directly to the surface of the substrate to form the coated material.

Claims (30)

1. A method of manufacture of a coated material comprising the steps of:

providing a cellulosic substrate;

melting a polyvinyl alcohol polymer which includes one or more plasticizers, wherein the polyvinyl alcohol polymer is a blend of two or more homopolymeric polymer grades having low and high respective molecular weights;

each homopolymeric polymer has a degree of hydrolysis of 90 wt % or greater and a melting point in the range of 200° C. to 225° C.;

extruding the melted polyvinyl alcohol polymer to form a molten polyvinyl alcohol polymeric film;

applying the molten polyvinyl alcohol polymeric film directly to the surface of the substrate; and

allowing the molten polyvinyl alcohol polymeric film to solidify on the surface to form a coated material.

2. The method of claim 1 , wherein the molten polyvinyl alcohol polymeric film is applied directly to the surface of the substrate without use of an adhesive or intermediate bonding layer.

3. The method of claim 1 , wherein the polyvinyl alcohol polymer is formed by hydrolysis of polyvinyl acetate homopolymer.

4. The method of claim 1 , wherein the polyvinyl alcohol polymer has a degree of hydrolysis of 93 wt % or greater.

5. The method of claim 4 , wherein the degree of hydrolysis is in the range of 93 wt % to 96 wt %.

6. The method of claim 1 , wherein the one or more plasticizers are selected from the following plasticizers and mixtures thereof:

(a) sugar alcohols selected from the group consisting of: diglycerol, triglycerol, fructose, ribose, xylose, D-mannitol, triacetin, and mixtures thereof;

(b) polyols selected from the group consisting of: pentaerythritol, dipentaerythritol, and mixtures thereof;

(c) diols selected from the group consisting of: methyl pentanediol, 1,2-propanediol, 1,4-butanediol, 2-hydroxy-1,3-propanediol, 3-methyl-1,3-butanediol, 3,3-dimethyl-,2-butanediol, and mixtures thereof;

(d) glycols selected from the group consisting of: polyethylene glycol 300, polyethylene glycol 400, alkoxylated polyethylene glycol, and mixtures thereof; and

(e) caprolactam, cyclic trimethylolpropane formal, rosin esters, euricamide, and mixtures thereof.

7. The method of claim 1 , wherein the cellulosic substrate is paper, board or card.

8. The method of claim 1 , wherein the blend comprises a first grade having a molecular weight in the range of 13,000 to 27,000 and a degree of polymerization of 300 to 600 and a second grade having a molecular weight in the range of 107,000 to 120,000 and a degree of polymerization of 2,400 to 2,600.

9. The method of claim 1 , wherein the polyvinyl alcohol polymer includes one or more reactive stabilizers selected from the group consisting of:

calcium stearate, stearic acid, sodium stearate, potassium oleate, potassium sorbate, sodium benzoate and mixtures thereof.

10. The method of claim 1 , wherein a reduced viscosity is maintained when shear is applied to the molten polyvinyl alcohol polymer, the reduced viscosity being maintained if the shear is applied for a period up to one hour or longer.

11. The method of claim 1 , wherein the viscosity of the molten polyvinyl alcohol polymer decreases with increasing shear rate from a viscosity at a shear rate of 80l/s to a viscosity at a shear rate of 1000l/s, the viscosities being measured at steady states following application of shear to the molten polyvinyl alcohol polymer for up to one hour.

12. The method of claim 1 , wherein the polyvinyl alcohol polymer is pseudoplastic.

13. The method of claim 1 , wherein the polyvinyl alcohol polymer has a degree of hydrolysis of 95 wt % or greater.

14. The method of claim 8 , wherein the two or more polyvinyl alcohol polymer grades have the same hydrolysis degree (HD) value.

15. The method of claim 1 , wherein the one or more plasticizers are diglycerol, triglycerol, xylose, D-mannitol, triacetin, dipentaerythritol, 1,4-butanediol, 3,3-dimethyl-,2-butanediol, caprolactam and mixtures thereof.

16. The method of claim 1 , wherein the polyvinyl alcohol polymer dissolves in 10 minutes in water having a temperature from about 30° C. to about 60° C. and 100% of the undissolved cellulose fibers are released from the coated material.

17. The method of claim 16 , wherein the coated material is processable in a conventional paper mill.

18. The method of claim 9 , wherein the polyvinyl alcohol polymer includes sodium benzoate.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 16, 2025
From: AQUAPAK POLYMERS LTD
To: AQUAPAK IP LTD
Reel/Frame 069898/0851 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 3, 2025
From: WILLIAMS, JOHN; GRIFFITHS, SIAN; ASHWORTH, ROBERT; MEADOWS, DAVID LEE
To: AQUAPAK IP LIMITED
Reel/Frame 069729/0815 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 6, 2023
From: AQUAPAK POLYMERS LIMITED
To: AQUAPAK IP LIMITED
Reel/Frame 062601/0498 →
SECURITY INTEREST Recorded Dec 15, 2022
From: AQUAPAK HYDROPOLYMERS LTD; AQUAPAK POLYMERS LTD; AQUAPAK IP HOLDINGS LTD; AQUAPAK IP LTD
To: U.S. BANK TRUST COMPANY, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 062099/0846 →
Priority Claims (1)
EP 20192950 · Aug 26, 2020 · regional
Continuity (1)
Related Publication 20220064860A1 · Mar 3, 2022
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