WO2013130704A1

WO2013130704A1 - Ionomer-poly(vinylalcohol) blends and coatings

Info

Publication number: WO2013130704A1
Application number: PCT/US2013/028152
Authority: WO
Inventors: Elliott Echt; Richard Allen Hayes
Original assignee: E. I. Du Pont De Nemours And Company
Priority date: 2012-02-29
Filing date: 2013-02-28
Publication date: 2013-09-06
Also published as: IN2014DN06526A; CN104136556A; JP2015516472A; AU2013226014A1

Abstract

Disclosed are compositions comprising a blend of a poly(vinyl alcohol) composition comprising a poly(vinyl alcohol) characterized by (i) a hydrolysis level of from 80 to 94 mole % and a 4 weight % aqueous viscosity of 15 centipoise (cP) or less; or (ii) a hydrolysis level of 95 mole % to 100 %; and an ionomer comprising a parent acid copolymer that comprises ethylene and 18 to 30 weight % of acrylic acid or methacrylic acid, the acid copolymer having a melt flow rate from 200 to 1000 g/10 min., wherein 50% to 70% of the carboxylic acid groups of the copolymer are neutralized to carboxylic acid salts comprising potassium cations, sodium cations or combinations thereof. Articles and multilayer structures comprising the blend composition on a substrate and methods for their preparation are also disclosed.

Description

TITLE

IONOMER-POLYfVINYLALCOHOL BLENDS AND COATINGS

FIELD OF THE INVENTION

This application claims priority to U.S. Patent Application Serial Number 13/407,829, filed February 29, 2012 and U.S. Patent Application Serial Number 13/407,858, filed February 29, 2012.

The present invention is directed to compositions, aqueous dispersions and articles comprising ionomer-poly(vinyl alcohol) blends, methods to prepare them, and methods to form coatings comprising the blends on a substrate.

BACKGROUND OF THE INVENTION

Ionomers of ethylene copolymers with alpha,beta-ethylenically unsaturated carboxylic acids are known in the art, wherein at least a portion of the carboxylic acid groups of the copolymer are neutralized to form carboxylate salts comprising alkali metal, alkaline earth metal or transition metal cations. See U.S. Patents 3,264,272; 3,338,739; 3,355,319; 5,155,157; 5,244,969; 5,304,608; 5,542,677; 5,591,803; 5,688,869; 6,100,336; 6,245,858; 6,518,365; and U.S. Patent Application Publication 2009/0297747.

Aqueous dispersions of ionomers are also known in the art. See U.S. Patents 3,896,065;

3,904,569; 4, 136,069; 4,508,804; 5,409,765; and Japanese Patent Applications JP01009338 and

JP05075769. They have been produced by dissolving the acid copolymer precursors in a solvent, neutralization of the acid functionalities with generally ammonia, amines or alkali metal ions, and dilution of the solution into water followed by partial or complete removal of the solvent. See U.S. Patents 2,313, 144; 3,296,172; 3,389, 109; 3,562,196; 5,430, 1 1 1 ; 5,591,806; British Patent GB 1243303; and Japanese Patent Applications JP50084687 and JP2009091426.

Aqueous ionomer dispersions have also been produced by heating acid copolymer precursors or ionomers in hot aqueous ammonia and other neutralizing agents. See U.S. Patents 3,644,258; 3,674,896; 3,823, 108; 3,970,626; 4,540,736; 5,330,788; 5,550, 177; U.S. Patent Application Publication

2007/01 17916; Japanese Patent Application JP06000872; and PCT Patent Application Publication WO2000/044801.

Aqueous ionomer dispersions have also been produced by dispersing the acid copolymer precursor in aqueous solutions of neutralizing agents at temperatures under high shear process conditions above the boiling point of water, necessitating the use of pressure vessels such as autoclaves and extruders. See U.S. Patents 4,775,713; 4,970,258; 4,978,707; 5,374,687; 5,445,893; 7,279,513;

7,528,080; U.S. Patent Application Publications 2005/0100754; 2006/0124554; 2007/0141323;

2007/0144697; 2007/0292705; 2007/0295464; 2007/0295465; 2008/0000598; 2008/0000602;

2008/0041543; 2008/0073045; 2008/0073046; 2008/0118728; 2008/0135195; 2008/0176968;

2008/0182040; 2008/0216977; 2008/0230195; 2008/0292833; 2008/0295985; 2009/0194450;

2009/0253321 ; European Patent Application EP1 163276; PCT Patent Applications WO201 1/0581 19; WO201 1/058121 ; WO2011/068525; and Japanese Patent Applications JP2958120; JP10006640; and JP50135141.

Aqueous ionomer dispersions have also been produced by dispersing the ionomer in aqueous solutions under high shear process conditions at temperatures above the boiling point of water, necessitating the use of pressure vessels such as autoclaves and extruders. See U.S. Patents 4, 173,669; 4,329,305; 4,410,655; 4,440,908; 6,458,897; Japanese Applications JP1 1 158332; JP2000328046;

JP2005075878; and PCT Patent Application Publication WO 1999/10276.

Aqueous ionomer dispersions have also been produced by dispersing highly neutralized, low melt index (MI) ionomers in hot water. See U.S. Patents 3,321,819; 3,472,825; and 4,181,566.

Ammonia-neutralized ionomer aqueous dispersions have been used to coat certain substrates. See U.S. Patents 3,872,039; 3,899,389; 3,983,268; 4,340,659; 4,400,440; 4,714,728; 5,336,528; and

6,852,792. As is well known in the art, ammonia-neutralized ionomers liberate the ammonia upon drying to reform the parent acid copolymer and are not redispersable in hot water.

Low molecular weight ionomer waxes have been used as temporary coatings removable with hot water. See U.S. Patent 5,292,794.

Certain ionomer articles have been dispersed in aqueous caustic solutions (U.S. Patent 6,162,852).

Certain ionomer dispersions have been used as primer coatings for substrates, such as PET, biaxially oriented polypropylene (BOPP) and aluminum foil films. See U.S. Patents 5,419,960;

6,013,353; 7,364,800; 7,470,736; and U.S. Patent Application Publication 2005/0271888.

Highly neutralized ionomer dispersions have been used as fabric or paper treatments. See U.S. Patents 5,082,697; 5,206,279; and 5,387,635.

Ionomer dispersions, produced through autoclave or extrusion processes, have been used as internal and external paper sizing or paper additives. See U.S. Patents 5,993,604; 6,482,886; 7,588,662; U.S. Patent Application Publications 2007/0137808; 2007/0137809; 2007/0137810; 2007/013781 1 ;

2007/0137813; 2007/0141936; 2007/0243331 ; and 2007/0284069.

Certain ionomer dispersions have been used in repulpable paper compositions. See U.S. Patent 5, 160,484.

Blends of aqueous ionomer dispersions with poly(vinyl alcohol) solutions are known in the art. See U.S. Patents US 3,674,896; 3,896,065; 4,547,456; 4,575,532; 4,600,746; 5,192,620; 5,358,790;

6,821,373; European Patent Application EP 868363; Japanese Applications JPH09124975;

JP2003049035; and JP60072973. The blends suffer the shortcoming of a complicated ionomer dispersion process, as disclosed above.

Ammonia-neutralized ionomer aqueous dispersions have been used to coat certain substrates. See U.S. Patents 3,872,039; 3,899,389; 3,983,268; 4,340,659; 4,400,440; 4,714,728; 5,336,528; and 6,852,792. As is well known in the art, ammonia-neutralized ionomers liberate the ammonia upon drying to reform the parent acid copolymer and are not redispersable in hot water.

Ionomer dispersions produced through autoclave or extrusion processes have been used as internal and external paper sizing or paper additives. See U.S. Patents 5,993,604; 6,482,886; 7,588,662; U.S. Patent Application Publications 2007/0137808; 2007/0137809; 2007/0137810; 2007/013781 1 ;

2007/0137813; 2007/0141936; 2007/0243331 ; and 2007/0284069.

SUMMARY OF THE INVENTION

The invention relates to a blend composition comprising or consisting essentially of

(a) 99 to 1 weight %, based on the combination of (a) and (b), of a poly(vinyl alcohol) composition comprising a poly(vinyl alcohol) characterized by

(i) a hydrolysis level of 80 to 94 mole % and a 4 weight % aqueous viscosity at 20 °C of 15 centipoise (cp) or less; or

(ii) a hydrolysis level of 95 mole % to 100 %; and

(b) 1 to 99 weight %, based on the combination of (a) and (b), of an ionomer composition comprising a parent acid copolymer that comprises or consists essentially of copolymerized units of ethylene and 18 to 30 weight % of copolymerized units of acrylic acid or methacrylic acid, based on the total weight of the parent acid copolymer, the acid copolymer having a melt flow rate (MFR) from 200 to 1000 g/10 min., measured according to ASTM D 1238 at 190 °C with a 2160 g load, wherein 50% to 70% of the carboxylic acid groups of the copolymer, based on the total carboxylic acid content of the parent acid copolymer as calculated for the non-neutralized parent acid copolymer, are neutralized to carboxylic acid salts comprising potassium cations, sodium cations or combinations thereof.

The invention also relates to an aqueous ionomer-poly(vinyl alcohol) dispersion comprising or consisting essentially of water and about 0.001 to about 50 weight % of the combination of (a) and (b) described above.

The invention also provides a method for making an aqueous ionomer-poly(vinyl alcohol) dispersion comprising a mixture of an ionomer composition and a poly(vinyl alcohol) composition, the method comprising or consisting essentially of (1) providing an aqueous poly(vinyl alcohol) solution comprising or consisting essentially of water and the poly(vinyl alcohol) composition described in (a) above;

(2) providing an ionomer composition comprising or consisting essentially of the ionomer composition described in (b) above; and

(3) mixing the ionomer composition with the aqueous poly(vinyl alcohol) composition solution optionally with heating to provide a heated aqueous blend dispersion; and

(4) optionally cooling the heated aqueous blend dispersion to a temperature of 20 to 30 °C, wherein the combination remains dispersed in the liquid phase;

wherein the aqueous ionomer-poly(vinyl alcohol) dispersion is as described above.

The invention also provides a method to form a coating comprising a blend of ionomer and poly(vinyl alcohol) on a substrate, the method comprising or consisting essentially of

(1) providing a blend composition as described above;

(2) providing a substrate; and

(3) coating the blend composition onto the substrate.

In one embodiment, the blend composition is provided in the form of an aqueous dispersion comprising or consisting essentially of water and 0.001 to 50 weight % of the combination of (a) and (b); the blend composition is coated onto the substrate as the aqueous dispersion and the method further comprises (4) drying the coated substrate at a temperature of 20 to 150 °C.

In another embodiment, the blend composition is provided in the form of a preformed film comprising or consisting essentially of the combination of (a) and (b); (3) comprises (3a) producing a pre laminate structure comprising the poly(vinyl alcohol) film layer adjacent to the substrate; and (3b) laminating the poly(vinyl alcohol) film layer to the substrate at a temperature from 50 to 150 °C, optionally with applied pressure; and the method further comprises (4) cooling the coated substrate to a temperature of 20 to 30 °C.

The invention also provides an article comprising or consisting essentially of the blend composition above. The invention also provides an article or multilayer structure comprising the coated substrate as described above.

DETAILED DESCRIPTION OF THE INVENTION

Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. In case of conflict, the specification, including definitions, will control.

Although methods and materials similar or equivalent to those described herein can be used in the practice or testing of the invention, suitable methods and materials are described herein.

Unless stated otherwise, all percentages, parts, ratios, etc., are by weight. When an amount, concentration, or other value or parameter is given as either a range, preferred range or a list of lower preferable values and upper preferable values, this is to be understood as specifically disclosing all ranges formed from any pair of any lower range limit or preferred value and any upper range limit or preferred value, regardless of whether ranges are separately disclosed. Where a range of numerical values is recited herein, unless otherwise stated, the range is intended to include the endpoints thereof, and all integers and fractions within the range. It is not intended that the scope of the invention be limited to the specific values recited when defining a range.

As used herein, the terms "comprises," "comprising," "includes," "including," "containing," "characterized by," "has," "having" or any other variation thereof, are intended to cover a non-exclusive inclusion. For example, a process, method, article, or apparatus that comprises a list of elements is not necessarily limited to only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Further, unless expressly stated to the contrary, "or" refers to an inclusive or and not to an exclusive or.

The transitional phrase "consisting essentially of limits the scope of a claim to the specified materials or steps and those that do not materially affect the basic and novel characteristic(s) of the claimed invention. Where applicants have defined an invention or a portion thereof with an open-ended term such as "comprising," unless otherwise stated the description should be interpreted to also describe such an invention using the term "consisting essentially of.

Use of "a" or "an" are employed to describe elements and components of the invention. This is merely for convenience and to give a general sense of the invention. This description should be read to include one or at least one and the singular also includes the plural unless it is obvious that it is meant otherwise.

In describing certain polymers it should be understood that sometimes applicants are referring to the polymers by the monomers used to produce them or the amounts of the monomers used to produce the polymers. While such a description may not include the specific nomenclature used to describe the final polymer or may not contain product-by -process terminology, any such reference to monomers and amounts should be interpreted to mean that the polymer comprises copolymerized units of those monomers or that amount of the monomers, and the corresponding polymers and compositions thereof.

The term "copolymer" is used to refer to polymers formed by copolymerization of two or more monomers. Such copolymers include dipolymers consisting essentially of two copolymerized comonomers.

As used herein, "disperse," "dispersing" and related terms refer to a process in which solid articles such as pellets of polymer are mixed with water and over a brief period of time disappear into the liquid phase. The terms "aqueous dispersion" and "dispersion" describe a free-flowing liquid with no solids visible to the human eye. No characterization is made regarding the interaction of the polymer molecules disperses readily in hot (80 to 100 °C) water without need for additional dispersants or reagents.

Viscosity is a measure of the resistance of a fluid to movement by shear stress. In everyday terms for fluids only, viscosity may be thought of as "thickness" or "internal friction". For example, water is "thin", having a lower viscosity, while honey is "thick", having a higher viscosity. The less viscous a fluid is, the greater its ease of movement (fluidity). As used herein, viscosity refers to dynamic or absolute viscosity.

As used herein, the terms "poly(vinyl alcohol)" and "PVOH" refer generally to poly(vinyl alcohol) homopolymers or copolymers unless specified with more particularity.

The coating methods described herein provides coated substrates using blend compositions comprising ionomers and certain poly(vinyl alcohol)s. The ionomer-poly(vinyl alcohol) coating on the substrate as disclosed herein can be in the form of a monolithic membrane that functions as a barrier to penetration of fluids into or through the substrate. Monolithic membranes have high water-entry pressure and are waterproof and liquidproof. The coating also allows for providing a heat-sealable surface on a substrate that is not heat-sealable. Printing properties may be improved by altering the surface of the paper to make it more hydrophobic by the coating.

Articles comprising the coated substrate provide easily recyclable articles of commerce, for example, through repulping of the coated paper, paperboard and the like.

Poly(Vinyl Alcohol) Composition

The blends and aqueous dispersions contain poly(vinyl alcohol) compositions comprising or consisting essentially of a poly(vinyl alcohol) wherein the poly(vinyl alcohol) is characterized by

(i) a hydrolysis level of 80 to 94 mole % and a 4 weight % aqueous viscosity of 15 centipoise (cP) or less; or

(ii) a hydrolysis level of 95 mole % to 100 %.

The combination of the hydrolysis level and the 4 weight % aqueous viscosity of the poly(vinyl alcohol) composition provides the desirable solubility/dispersability attributes needed to form aqueous dispersions when blended with ionomers.

Poly(vinyl alcohol) compositions can be obtained by known and conventional methods.

Poly(vinyl alcohol) compositions are typically obtained through polymerization of vinyl acetate monomer, followed by conversion of the as-made poly(vinyl acetate) composition to the poly(vinyl alcohol) composition through alcoholysis or hydrolysis processes. Strictly, alcoholysis is carried out with a basic catalyst in alcohol as reaction medium and leads to the corresponding alkyl acetate and the poly(vinyl alcohol) unit. Hydrolysis, in water, generally uses larger amounts of metallic caustic base, leading to the poly(vinyl alcohol) unit and the corresponding metal acetate rather than alkyl acetate. Formation of metal salts, i.e. acetates, has led to use of the term "saponification" for the process, akin to formation of metal salts of fatty acids with caustic, in making soaps. When aqueous alcohol is used as the reaction medium both hydrolysis and alcoho lysis may occur. However, U.S. Patent 2,940,948 discloses that under specific circumstances, even with aqueous alcohol, alcoholysis rather than hydrolysis occurs. While the distinction strictly depends on reaction products, the terms have tended to be used non-rigorously. The poly(vinyl alcohol) products are typically referred to as "hydrolyzed" or "saponified".

It is common to use the terms "partially hydrolyzed", "partially saponified", and "intermediately hydrolyzed" when not all the acetate groups are completely converted to alcohol groups. When poly(vinyl acetate) homopolymer is only partially hydrolyzed, the resulting poly(vinyl alcohol) is actually a vinyl alcohol/vinyl acetate copolymer. However, as noted, such polymers are generally referred to as partially hydrolyzed poly(vinyl alcohol) homopolymers. Commercially, the term partially hydrolyzed is typically used for PVOH with 86 to 89 % hydrolysis levels and the term intermediately hydrolyzed is used for PVOH with 89 to 98 % hydrolysis levels. Below 86 % hydrolysis there is no standard term, but "sub- partially hydrolyzed" has been used. However, for simplicity of description, the term "partially hydrolyzed" is used herein for PVOH with hydrolysis levels of 80 to 94 mole %.

Surprisingly, we have found that some partially hydrolyzed poly(vinyl alcohol) compositions when combined with the ionomers described below provide aqueous dispersions under the mild conditions described herein. The degree of hydrolysis of the poly(vinyl alcohol) composition useful in preparing such aqueous dispersions may be from 80 to 94 mole %, preferably from 85 to 93 mole % and more preferably from 87 to 90 mole %.

The viscosity of poly(vinyl alcohol) as a 4 weight % aqueous solution at 20 °C serves as an industrial standard relating to the degree of polymerization and average molecular weight of the poly(vinyl alcohol) polymer.

The 4 weight % aqueous viscosity at 20 °C of the partially hydrolyzed poly(vinyl alcohol) composition may be 15 centipoise (cP) or less, preferably from 1 to 15 cP, or 7 cp or less. Of note are partially hydrolyzed poly(vinyl alcohol)s with 4 weight % aqueous viscosity at 20 °C from a lower limit of 1, 2 or 4 cP to an upper limit of 7, 10 or 15 cP. Specific partially hydrolyzed poly(vinyl alcoho l)s have a hydrolysis level of 87 to 89 % and 4 weight % aqueous viscosity at 20 °C of 5 to 6 cP, 8 to 10 cP or 1 1 to 14 cP.

Aqueous solutions comprising 5 to 20 weight % of such poly(vinyl alcohol) compositions may have viscosity at 20 °C of 5 to 2000 cp, or higher.

Surprisingly, we have also found that highly hydrolyzed poly(vinyl alcohol) compositions when combined with the ionomers described below provide aqueous dispersions under mild conditions described herein. As used herein, "highly hydrolyzed" refers to poly(vinyl alcohol) polymers with a hydrolysis level of 95 mole % to 100 %, such as between 95 and 97%, or between 95 and 99%, or between 97 and 99 %, or greater than 98%. Polyvinyl alcohol) polymers with a hydrolysis level of 98 % or greater are also described herein as "fully hydrolyzed."

Specific poly(vinyl alcohol)s have a hydrolysis level of 95 to 97 % and 4 weight % aqueous viscosity at 20 °C of 25 to 30 cP, or a hydrolysis level of greater than 99 % and 4 weight % aqueous viscosity at 20 °C of 27 to 33 cP.

Aqueous solutions comprising 5 to 16 weight % of such poly(vinyl alcohol) compositions may have viscosity at 20 °C of 35 to 10,000 cp or higher.

Optionally, poly(vinyl alcohol) copolymers are also useful for forming aqueous dispersions with ionomers, provided they have the hydrolysis and viscosity attributes described above. The term

"copolymer" in this regard is used herein for materials which result from hydrolysis of a vinyl acetate copolymer also containing units derived from a monomer other than vinyl acetate, such an alkyl acrylate, including for example methyl acrylate or methyl methacrylate.

The poly(vinyl alcohol) composition may also contain other additives known in the art. The additives may include, but are not limited to, processing aids, flow enhancing additives, lubricants, pigments, dyes, flame retardants, impact modifiers, nucleating agents, anti-blocking agents such as silica, thermal stabilizers, UV absorbers, UV stabilizers, surfactants, chelating agents, and/or coupling agents. Ionomer Composition

The ionomer used herein is derived from certain parent acid copolymers comprising

copolymerized units of ethylene and 18 to 30 weight % of copolymerized units of an alpha, beta- ethylenically unsaturated carboxylic acid such as acrylic acid or methacrylic acid. Preferably, the parent acid copolymer used herein comprises 19 to 25 weight %, or more preferably 19 to 23 weight %, of the alpha, beta-ethylenically unsaturated carboxylic acid, based on the total weight of the copolymer.

Preferably, the alpha, beta-ethylenically unsaturated carboxylic acid is methacrylic acid. Of note are acid copolymers consisting essentially of copolymerized units of ethylene and copolymerized units of the alpha, beta-ethylenically unsaturated carboxylic acid and 0 weight % of additional comonomers; that is, dipolymers of ethylene and the alpha, beta-ethylenically unsaturated carboxylic acid. Preferred acid copolymers are ethylene methacrylic acid dipolymers.

The parent acid copolymers used herein may be polymerized as disclosed in U.S. Patents 3,404, 134; 5,028,674; 6,500,888; and 6,518,365.

The parent acid copolymers used herein preferably have a melt flow rate (MFR) of 200 to about 1000 grams/ 10 min as measured by ASTM D 1238 at 190°C using a 2160 g load. Alternatively, the parent acid copolymers have MFR from a lower limit of 200, 250 or 300 to an upper limit of 400, 500, 600 or 1000. The preferred melt flow rate of the parent acid copolymer provides ionomers that allow for rapid self-dispersion in hot water. Ionomers derived from parent acid copolymers with melt flow rates below 200 grams/ 10 minutes have minimal hot water self-dispersability, while ionomers derived from parent acid copolymer with melt flow rates of greater than 1000 grams/ 10 minutes may reduce the physical properties in the intended enduse.

In some embodiments, blends of two or more ethylene acid copolymers may be used, provided that the aggregate components and properties of the blend fall within the limits described above for the ethylene acid copolymers. For example, two ethylene methacrylic acid dipolymers may be used such that the total weight % of methacrylic acid is 18 to 30 weight % of the total polymeric material and the melt flow rate of the blend is 200 to 1000 grams/ 10 min.

The ionomers disclosed herein are produced from the parent acid copolymers, wherein from 50 to 70%, or preferably from 55 to 60%, such as 59 to 60 %, of the total carboxylic acid groups of the parent acid copolymers, as calculated for the non-neutralized parent acid copolymers, are neutralized to form carboxylic acid salts with sodium ions, potassium ions or mixtures thereof. The parent acid copolymers may be neutralized using methods disclosed in, for example, U.S. Patent 3,404, 134. Preferably, the ionomers disclosed herein are produced from the parent acid copolymers wherein the carboxylic acid groups of the parent acid copolymers are neutralized to form carboxylic acid salts with sodium ions.

Importantly, the ionomer compositions combine the properties of being self-dispersable in hot water along with being thermoplastic. Preferably, the ionomers used herein have a melt flow rate (MFR) of at least 1 gram/ 10 min, such as 1 to 20 grams/ 10 min as measured by ASTM D1238 at 190°C using a 2160 g load. More preferably, the ionomer composition has a MFR of 1 to 10 grams/ 10 min, and most preferably a MFR of 1 to 5 grams/ 10 min. The combination of the above described parent acid copolymer melt flow rates and the neutralization levels provides ionomers that combine the properties of being easily self-dispersable in hot water and easily melt fabricated into articles of commerce. Preferably, the ionomer composition comprises at least 1 1 weight % methacrylic acid salt and has a MFR of at least 1 g/10 min.

In some embodiments, blends of two or more ionomers may be used, provided that the aggregate components and properties of the blend fall within the limits described above for the ionomers.

Aqueous dispersions comprising 5 to 20 weight % of such ionomers may have viscosity at 23 °C of 1 to 30 cp.

The ionomer composition may also contain other additives known in the art. The additives may include, but are not limited to, processing aids, flow enhancing additives, lubricants, pigments, dyes, flame retardants, impact modifiers, nucleating agents, anti-blocking agents such as silica, thermal stabilizers, UV absorbers, UV stabilizers, surfactants, chelating agents, and coupling agents.

Blend Composition

The PVOH and ionomer can be combined into blend compositions, including aqueous dispersions. The blend composition comprises or consists essentially of a combination of 1 to 99 weight % of a poly(vinyl alcohol) composition and 99 to 1 weight % of an ionomer composition, wherein the ionomer and poly(vinyl alcohol) are as described above. Of note are compositions wherein the ionomer is present in the combination in an amount from a lower limit of 10, 20, 30, 40 or 50 weight % to an upper limit of 60, 70, 80, 90, or 95 weight %, the poly(vinyl alcohol) being present in a complementary amount. Also of note are compositions wherein the ionomer is present in the combination in an amount from a lower limit of 60, 70, or 75 weight % to an upper limit of 80, 85, 90 or 95 weight %, the poly(vinyl alcohol) being present in a complementary amount.

Preferably, the ionomer and the PVOH may be blended in an aqueous dispersion as discussed in greater detail below, which avoids heating the PVOH above its melting point. Preferably the pH of the aqueous dispersion is above 8.5. Below pH of 8.5 the ionomer is not well dispersed. The aqueous blend dispersion can in turn be processed into a solid by drying (removal of water) to provide an article. For example, the aqueous blend dispersion may be formed into a cast film by forming a thin layer of the aqueous blend, followed by drying.

The ionomer-PVOH composition may also contain other additives known in the art. The additives may include, but are not limited to, processing aids, flow enhancing additives, lubricants, pigments, dyes, flame retardants, impact modifiers, nucleating agents, anti-blocking agents such as silica, thermal stabilizers, UV absorbers, UV stabilizers, surfactants, chelating agents, and coupling agents.

The blend composition article may take any physical form desired, such as powder, pellets, melt cut pellets, coatings, films, sheets, molded articles and the like.

Dispersion Method

A method for making an aqueous ionomer-poly(vinyl alcohol) dispersion comprising a mixture of an ionomer composition and a poly(vinyl alcohol) composition comprises or consists essentially of

(1) providing an aqueous poly(vinyl alcohol) solution comprising or consisting essentially of water and the poly(vinyl alcohol) composition described in (a) above;

(3) mixing the ionomer composition with the aqueous poly(vinyl alcohol) composition solution optionally with heating; and

(4) optionally cooling the heated aqueous blend dispersion to a temperature of 20 to 30 °C, wherein the combination remains dispersed in the liquid phase; and wherein the aqueous ionomer- poly(vinyl alcohol) dispersion is as described above.

The dispersion method described herein surprisingly allows for the production of aqueous dispersions of combinations of poly(vinyl alcohol) and ionomers under very mild process conditions, such as low shear (e.g. simply stirring a mixture of a heated poly(vinyl alcohol) and an ionomer, either as a solid or as an aqueous dispersion) and relatively low temperature (less than the boiling point of water at atmospheric pressure), requiring less energy than prior art dispersion processes. This dispersion method further provides an inherently safer dispersion process through the use of preformed blend compositions by allowing for the avoidance of strong bases, such as aqueous sodium hydroxide (caustic), aqueous potassium hydroxide or ammonia, during the dispersion process.

Strictly speaking, the blend dispersion generally includes a solution of the poly(vinyl alcohol) composition, and a dispersion of the ionomer composition hereinafter referred to as a dispersion for brevity.

The aqueous poly(vinyl alcohol) solution may be prepared by any method disclosed in the art. Generally, such processes include forming a mixture of the PVOH composition in water at a temperature of 20 °C to 30 °C, followed by heating the mixture at a temperature and for a time until the PVOH composition dissolves to form the aqueous PVOH composition solution. The aqueous dissolution temperature of the PVOH is generally dependent on the hydrolysis level of the specific PVOH composition. For PVOH compositions with hydrolysis levels equal to or less than 89 mole %, the aqueous dissolution temperature may be generally in the temperature range from 20 °C to 40 °C. For PVOH compositions with hydrolysis levels in the range of 90 mole % to 97 mole %, the aqueous dissolution temperature may be generally in the temperature range from 40 °C to 60 °C. For PVOH compositions with hydrolysis levels in the range above 97 mole %, the aqueous dissolution temperature may be generally in the temperature range from 60 °C to 100 °C. In order to prepare the solution faster, it may be useful to heat the mixture of water and PVOH at temperatures higher than the threshold temperature for dissolution. For example, the water-PVOH mixture may be heated to 90 to 95 °C, regardless of hydrolysis level.

The poly(vinyl alcohol) solution may be produced in any suitable vessel, such as a tank, vat, pail or the like. Stirring is important to provide effective contact of the bulk solid poly(vinyl alcohol) composition with water as dissolution proceeds to avoid clumping of the PVOH. The solution may be produced in about 1 hour at 90 °C for batch processes.

Alternatively, it is further contemplated that the dissolution process may be conducted in a continuous process. For example a continuous or "jet" cooker can be used, where a suspension of polyvinyl alcohol is mixed with steam in a closed pipe under pressure and exits the pressurized pipe portion fully dissolved, or hot enough to complete the dissolving process in a few minutes, depending on the particle size of the polyvinyl alcohol.

The aqueous poly(vinyl alcohol) solution preferably comprises from a lower limit of 0.001, 0.01, 0.1 or 1 % to an upper limit of 10, 20, 30 or 50 weight %, of the poly(vinyl alcohol) composition based on the total weight of the blend composition and the water.

In some embodiments, the dispersion method comprises providing a preformed aqueous solution of a poly(vinyl alcohol) composition and mixing it with a preformed aqueous dispersion of an ionomer composition. The aqueous ionomer dispersion may be formed by mixing the solid ionomer composition with water heated to a temperature from 80 to 100 °C (under low shear conditions) to provide a heated aqueous ionomer composition dispersion; optionally followed by cooling to a temperature of 20 to 30 °C, wherein the ionomer remains dispersed in the aqueous phase.

The aqueous dispersion of an ionomer composition can be produced by contacting the solid ionomer composition, for example in the form of melt cut pellet(s), with water at a temperature from 80 to 100 °C. In some embodiments, the temperature is in the range from 85 to 90 °C. Surprisingly, the ionomer compositions described herein can be dispersed in water at 80 to 100 °C, lower than that expected based on the prior art and requiring significantly less energy. However, one can appreciate that if the ionomer compositions disperse in that temperature range they can also be dispersed at temperatures above 100 °C.

The ionomer dispersion may be produced in any suitable vessel, such as a tank, vat, pail or the like. Stirring is useful to provide effective contact of the bulk solid ionomer composition with water as dispersion proceeds. Preferably the dispersion is produced in about 1 hour or less, such as in 30 minutes or in 20 minutes or less. Smaller particle size of the solid ionomer may reduce time of dispersion. Due to the surprisingly rapid dispersability of the ionomer compositions, it is further contemplated that the process may proceed within a pipeline in which the components of the dispersion are charged at one end of the pipeline and form the dispersion as they proceed down the length of the pipeline. For example, the ionomer composition may be mixed with water and passed through a heated zone, with or without added mixing, such as through static mixers. Alternatively, the ionomer composition may be mixed with hot water and passed through a pipeline, with or without added mixing, such as through static mixers.

In one embodiment, the ionomer composition is mixed with water under low shear conditions at room temperature (20 to 25 °C) and the temperature is raised to 80 to 100 °C. In another embodiment, the ionomer composition is mixed with water under low shear conditions at room temperature and the temperature is raised to 85 to 90 °C.

In another embodiment, the ionomer composition is mixed with water preheated to a temperature of 80 to 100 °C under low shear conditions. In another embodiment, the ionomer composition is mixed with water preheated to a temperature of 85 to 90 °C under low shear conditions.

The aqueous dispersion of the ionomer preferably comprises ionomer in an amount from a lower limit of 0.001 or 1 % to an upper limit of 10, 20, 30 or 50 weight %, of the total weight of the ionomer and the water. Preferably the pH of the the aqueous dispersion is above 8.5. Below pH of 8.5 the ionomer is not well dispersed.

Once prepared, the aqueous poly(vinyl alcohol) solution and the aqueous ionomer dispersion may be mixed together by any suitable means, with or without additional heating. In some instances, the aqueous poly(vinyl alcohol) solution and the aqueous ionomer dispersion may be maintained at or near the elevated temperatures necessary for their preparation through the mixing step. The resulting aqueous blend may be used in additional operations at the elevated temperatures necessary for its preparation. Alternatively, the resulting aqueous blend may then be cooled to ambient temperatures (20 to 30 °C) for storage or subsequent use.

The blend dispersion may also be prepared by mixing the aqueous PVOH solution with the aqueous ionomer dispersion, both at 20 to 30 °C before and through the mixing step.

The order of mixing the aqueous PVOH solution and the aqueous ionomer dispersion is not critical, provided the PVOH is in the form of an aqueous solution prior to mixing with the ionomer dispersion. For example, the PVOH solution may be prepared in a suitable vessel and the aqueous ionomer dispersion, prepared separately, is subsequently added to the vessel. The mixing can occur in any suitable mixing vessel, such as a tank, vat, pail or the like. Stirring may be useful to provide sufficient rapid mixing of the poly(vinyl alcohol) solution and the ionomer dispersion. The mixing may proceed within a pipeline in which the PVOH solution and the ionomer dispersion components of the blend dispersion are charged at one end of the pipeline and form the blend as they proceed down the length of the pipeline, with or without added mixing, such as through static mixers.

In other embodiments, the ionomer in solid form, such as melt cut pellets, may be mixed with the aqueous poly(vinyl alcohol) solution with heating to prepare the blend dispersion.

In one such embodiment, the method comprises or consists essentially of

(1) heating a mixture of water and a poly(vinyl alcohol) composition described above to provide an aqueous poly(vinyl alcohol) solution;

(2) the ionomer composition comprising or consisting essentially of the ionomer described above is in solid form;

and the mixing of step (3) comprises

(a) heating the aqueous poly(vinyl alcohol) solution to a temperature from 80 to 100 °C (under low shear conditions);

(b) contacting a solid ionomer composition with the heated aqueous poly(vinyl alcohol) solution;

(c) continuing heating at a temperature from 80 to 100 °C (under low shear conditions) until the solid ionomer composition has completely dispersed; and

(4) optionally cooling to a temperature of 20 to 30 °C;

In another such embodiment, the method comprises or consists essentially of

and the mixing of step (3) comprises (d) contacting the solid ionomer composition with the aqueous poly(vinyl alcohol) solution to provide a mixture;

(e) heating the mixture to a temperature from 80 to 100 °C (under low shear conditions) until the solid ionomer composition has completely dispersed; and

(4) optionally cooling to a temperature of 20 to 30 °C;

The order of mixing the aqueous PVOH solution and the solid ionomer dispersion is not critical, provided the PVOH is in the form of an aqueous solution prior to mixing with the ionomer. For example, the PVOH solution may be prepared in a suitable vessel and the solid ionomer is subsequently added to the vessel.

The mixing can occur in any suitable mixing vessel, such as a tank, vat, pail or the like. Stirring may be useful to provide sufficient rapid mixing of the poly(vinyl alcohol) solution and the solid ionomer. Smaller particle size of the solid ionomer may reduce time of dispersion. The mixing may proceed within a heated pipeline in which the PVOH solution and the solid ionomer components of the blend dispersion are charged at one end of the pipeline and form the blend as they proceed down the length of the pipeline, with or without added mixing, such as through static mixers.

Additional water may be added after the initial mixing, if desired, to provide dispersions with lower concentrations of PVOH and ionomer. For example a concentrated dispersion may be prepared and stored for a period of time and then diluted with water to provide a dispersion with lower concentration at the time of use.

The dispersion may include other additives known in the art. For example, the composition may include a wax additive, such as a microcrystalline wax or a polyethylene wax, which serves as an antiblocking agent as well as to improve the coefficient of friction. Other types of additives include fumed silica, which reduces tack of the blend composition at room temperature, fillers, cross-linking agents, antistatic agents, defoamers, dyes, brighteners, processing aids, flow enhancing additives, lubricants, dyes, pigments, flame retardants, impact modifiers, nucleating agents, anti-blocking agents, thermal stabilizers, UV absorbers, UV stabilizers, chelating agents, coupling agents and the like.

Inorganic fillers include calcium carbonate, titanium dioxide, silica, talc, barium sulfate, carbon black, ceramics, chalk or mixtures thereof. Clay fillers natural clays, synthetic clays, treated clays, untreated clays, organoclays, smectite clays, bentonite clays, hectorite days, wollastonite clays, montmorillonite clays, kaolin, or mixtures thereof. Organic fillers include natural starch, modified starch, chemically modified starch, rice starch, corn starch, wood flour, cellulose, and mixtures thereof.

Starch is a natural product composed of various amounts of amylose and amylopectin. As used herein "starch" refers generally to starch, starch derivatives, modified starch, thermoplastic starch, cationic starch, anionic starch, starch esters, such as starch acetate, starch hydroxyethyl ether, alkyl starches, amine starches, phosphate starches and dialdehyde starches. Important plant source of starch used in the paper industry are potato, barley, wheat corn, waxy maize (corn with no amylose in the starch), and tapioca. Starch can be modified in a number of ways. The viscosity of the starch can be reduced by use of enzymes, thermal treatment, ammonium persulfate, hypochlorite, or acid. In addition, the starch can be chemically modified, for example via hydroxyethylation, carboxymethylation, acetylation, or phosphatizing. Thermoplastic starch may be produced, for example, as disclosed in U.S. Patent 5,362,777, which discloses the mixing and heating of native or modified starch with high boiling plasticizers, such as glycerin or sorbitol, in such a way that the starch has little or no crystallinity, a low glass transition temperature and a low water content. Preferably, the starch does not comprise high viscosity ethoxylated (or "ethylated") starches.

Once prepared, the ionomer-PVOH composition may be coated onto a substrate as described below.

Substrate Materials

The substrate may be any material providing support, shape, esthetic effect, protection, surface texture, bulk volume, weight, or combinations of two or more thereof to enhance the functionality and handability of the structure. Essentially any substrate material known in the art may be used.

Any support or substrate meeting these desired characteristics may be used with the ionomer- PVOH composition. Cellulosic materials such as paper webs (for example Kraft or rice paper), materials made from synthetic fiber spun fabrics, nonwoven textiles, films, open-cell foams, closed-cell foams, microporous films, or even perforated films having large percentages of open areas such as perforated PE films, may be used as materials for the substrate(s), for example. Metallic foils such as aluminum foil may also be used as substrates.

Cellulosic materials include paper, paperboard, cardboard, and pulp-molded shapes. Paper, paperboard, cardboard and the like refer to physical forms derived from cellulose or its derivatives that have been processed as a pulp and formed by heat and/or pressure into sheets. Paper describes thin sheets made from cellulose pulp that are somewhat flexible or semi-rigid. In general, paperboard and cardboard are thicker, rigid sheets or structures based on paper. Typically, a paperboard is defined as a paper with a basis weight above 224 g/m². In accordance with the present disclosure, the paper layer or paperboard layer used in the substrate may have a thickness of about 30-600 μιη and a basis weight of 25 to 500 g/m², or 100 to 300 g/m². Cardboard can be a monolithic sheet or can have a more complex structure, such as corrugation. Corrugated cardboard comprises a sheet of corrugated paper adhesively sandwiched between two flat sheets of paper. A coating of the ionomer-PVOH blend may be useful as an adhesive for producing the corrugated cardboard. Pulp-molded shapes are typically nonplanar shapes in which the cellulosic pulp is molded into a rigid shape by application of pressure and/or heat. An example pulp- molded shape is an egg carton. Example substrates also include a textile or porous sheet material. A textile may also include nonwoven textiles prepared from polypropylene, polyethene, polyesters such as polyethylene

terephthalate or mixtures thereof, and other spun bonded polymer fabrics. Sheets made from synthetic fiber spun fabrics, such as nonwoven textiles, may be used as a textile substrate. Cloth that is woven, knitted or the like is also suitable as a textile substrate. Natural fibers alone or in combination with man- made fibers can also be used in textile substrates. A fabric may comprise flame retardant(s), filler(s), or additive(s) disclosed above.

The substrate material may be in the form of a film, sheet, woven fabric, nonwoven fabric and the like. The substrate material may be unoriented or oriented, such monoaxially or biaxially oriented. The substrate material may comprise a polymeric or a metal composition. The substrate may be treated to enhance, for example, adhesion with the coating. The treatment may take any form known in the art such as for example, adhesive, primer or coupling agent treatments or surface treatments, such as chlorine treatments, flame treatments (see, e.g., U.S. Patents 2,632,921 ; 2,648,097; 2,683,894; and 2,704,382), plasma treatments (see e.g., U.S. Patent 4,732,814), electron beam treatments, oxidation treatments, chemical treatments, chromic acid treatments, hot air treatments, ozone treatments, ultraviolet light treatments, sand blast treatments, solvent treatments or corona treatments and combinations of the above.

Specific examples of substrate materials include poly(ethylene terephthalate) (PET) films, biaxially-oriented poly(propylene) (BOPP) films, polyamide films, aluminum foil, paper, paperboard, and the like. Preferably, the substrate material is paper, paperboard and the like to allow for repulpability after use.

The substrate material may be any thickness, but generally range from 0.1 to 20 mils thick, more generally from 0.5 to 10 mils thick.

Methods to form a coating comprising a blend of ionomer and poly(vinyl alcohol) on a substrate comprise or consist essentially of (1) providing a blend composition comprising or consisting essentially of the PVOH and ionomers described above; (2) providing a substrate described above; and (3) coating the blend composition onto the substrate.

Coating methods include embodiments where the blend combination is in the form of an aqueous dispersion, extrusion coating wherein the blend combination is in molten form and lamination methods wherein the blend combination is in the form of a preformed film.

Dispersion Coating Method

One embodiment of the coating method is wherein the blend composition is in the form of an aqueous ionomer-poly(vinyl alcohol) dispersion comprising or consisting essentially of water and 0.001 to 50 weight % of the combination of (a) and (b) described above. In this embodiment, providing the blend composition may comprise or consist essentially of the dispersion methods described above. This embodiment further comprises (4) drying the coated substrate at a temperature of 20 to 150 °C. In some embodiments the polymer composition can be coated directly on a substrate using impregnation and coating techniques. For example, the ionomer-PVOH composition may be a coating applied directly on the substrate (via spraying, painting or other appropriate application methods). Such coating can be applied using spreading methods known in the art such as with a rubber doctor blade.

The composition can be applied to one side or both sides of a substrate. In the case where the substrate is coated or laminated on one side, the composition may be applied to the side that is directly exposed to the environment to provide a liquid-impermeable outer surface. Alternatively, in applications where mechanical wear or abrasion is likely, the composition may be applied to the side of the substrate opposite the side exposed to the mechanical wear to afford protection of the polymeric composition.

In other embodiments the composition can be impregnated in a substrate or the substrate can be impregnated in the polymer.

The ionomer-PVOH composition may be formed at least partially in the substrate by

impregnating the substrate with the coating composition as an aqueous dispersion and then drying the composition while it is in contact with the pores of the substrate.

The composition can be dispersed throughout the substrate such as a loosely woven fabric where the composition fills gaps in the substrate and does not just adhere on the surface of a substrate. The substrate can be impregnated inside the ionomer-PVOH composition through coating processes to have the ionomer-PVOH compositions on both sides of the substrate.

The coating as an aqueous dispersion can be applied to the substrate in any suitable manner known in the art, including gravure coating, curtain coating, blade coating, air knife coating, roll coating, wire rod coating, dip coating, flexographic printing, spray coating and the like. Excess aqueous dispersion coating composition can be removed by squeeze rolls, doctor knives and the like, if desired.

For the preferred paper and paperboard substrates, the substrates may be applied to the preformed paper or paperboard substrate, as described above, or during the manufacture of the paper or paperboard substrates using, for example, size presses, such as a puddle size press, a metering size press, a vertical size press, an inclined size press and a horizontal size press, roll coaters, gate-roll coaters, blade coaters, bill blade coaters, and sprayers to coat the coating composition onto the paper or paperboard substrate.

After coating the substrate, the aqueous dispersion is dried to provide a solid coating of the ionomer-PVOH blend on the substrate. As used herein, "drying" means removal of water from the aqueous dispersion, such as by evaporation, freeze drying, or the like. Drying may include allowing the dispersion to dry under ambient conditions (temperatures of 20 to 30 °C and atmospheric pressure).

Alternatively, drying may include application of elevated temperatures (such as up to 100 °C in an oven or heating tunnel) and/or reduced pressure. Freeze drying involves rapid freezing and drying in a high vacuum. Barrier properties may be improved if the coating is dried in a manner so that the dried ionomer is heated above 85 °C. Non-Dispersion Coating Methods

Another embodiment is wherein the blend composition is in the form of a preformed film. In this embodiment, the invention provides a method to form a coating comprising an ionomer and PVOH on a substrate, the method comprising or consisting essentially of

(a) providing a preformed film of an ionomer-PVOH composition as described above;

(b) producing a prelaminate structure comprising the ionomer-PVOH film layer adjacent to a substrate layer;

(c) laminating the ionomer film layer to the substrate layer at a temperature from 50 to 150 °C and optionally with applied pressure;

(d) cooling the coated substrate to a temperature of 20 to 30 °C.

The preformed film of the ionomer-PVOH composition may be produced by any known art method. For example, thin films can be formed by dipcoating; by providing a thin layer of an aqueous ionomer-PVOH dispersion followed by drying; or any other processes known to those skilled in the art.

In the film lamination method, the ionomer-PVOH coating layer can be included in a multilayer structure with one or more layers of additional material(s) to provide a multilayer coating. In such processes, the ionomer-PVOH coating layer may be applied so it is in direct contact with the substrate, or it may be applied so it is in contact with a layer intervening between the substrate and the ionomer-PVOH layer.

The actual making of the multilayer film and corresponding film structures can generally be by any such method as practiced in the art. As such, film and film structures used as a substrate for the ionomer-PVOH composition can be typically cast, extruded, co-extruded and the like including orientation (either axially or biaxially) by various methodologies (e.g., blown film, bubble techniques, mechanical stretching or the like, or lamination). It should be appreciated that various additives as generally practiced in the art can be present in the respective film layers including the presence of tie layers and the like, provided their presence does not substantially alter the properties of the film or film structure. Thus, it is contemplated that various additives such as antioxidants and thermal stabilizers, ultraviolet (UV) light stabilizers, pigments and dyes, fillers, anti-slip agents, plasticizers, other processing aids, and the like may be advantageously employed.

The preformed film of the ionomer-PVOH composition can be applied to one or both sides of the substrate. Preferably, the ionomer-PVOH composition layer has a thickness of 0.1 mil to 20 mils, more preferably a thickness of 0.3 mil to 10 mils and most preferably a thickness of 0.5 mil to 5 mils.

The laminate structures may be produced by any known art method. For example, the prelaminate structure can be produced by plying the preformed film of the ionomer-PVOH composition with the substrate followed by passing through heated nip rolls or through an oven to form the laminate. In these non-dispersion coating methods, after coating the substrate, the coated substrate is cooled to provide a solid ionomer-PVOH coating on the substrate. As used herein, "cooling" includes allowing the ionomer-PVOH coating to cool under ambient conditions (temperatures of 20 to 30 °C and atmospheric pressure) and/or by application of reduced temperatures such as by use of chill rolls or the like.

Additional layers may be applied to the coated substrate following coating. For example, additional aqueous or solvent-based dispersions not comprising an ionomer-PVOH combination may be applied to the coated substrate. Alternatively, multilayer structures may comprise additional

thermoplastic materials applied over the ionomer-PVOH layer by extrusion coating, lamination or the like. In such cases, the ionomer-PVOH coating becomes an inner layer in a multilayer structure.

The ionomer-PVOH coating composition can also be accommodated between two layers of substrate in a sandwich-like manner. Several layer assemblies can also be assembled one above the other. For example, the configuration can comprise the ionomer-PVOH layer, a substrate layer, another ionomer-PVOH layer, another substrate layer, and so on, depending upon desired applications of the structure. Other configurations can comprise variations of the aforementioned sandwich configuration, including a plurality of ionomer-PVOH layers, a plurality of substrate layers, and so forth, including mixtures thereof.

In such cases, in aqueous dispersion coating methods the ionomer coating may be maintained in an aqueous state during assembly of the layered structure, followed by drying. In the resulting layered structures, the ionomer-PVOH coating may function as an adhesive layer to bond substrate layers together.

The coated substrates described herein may be used as film or sheet goods for various end uses. Alternatively, the initially prepared coated substrate may be further treated to provide more finished articles.

For example, the coated substrate may be part of a package comprising the coated substrate. The packages may comprise films or sheets of the coated substrate wrapped around the packaged product and optionally comprising other packaging materials. Packages may also be formed of one or more portions of the coated substrate bonded together, for example by heat sealing. The ionomer-PVOH coating is readily heat sealable, allowing for production of packages comprising a coated paper substrate that does not need additional adhesive for sealing. Such packages or containers may be in the form of pouches, bags, boxes, cartons, cups, packets, and the like.

A film or sheet comprising the coated substrate could be further processed by thermoforming into a shaped article. For example, a film or sheet comprising the coated substrate as described herein could be formed into a shaped piece that could be included in packaging. Thermoformed articles typically have a shape in which a sheet of material forms a concave surface such as a tray, cup, can, bucket, tub, box or bowl. The thermoformed article may also comprise a film or sheet with a cup-like depression formed therein. In some cases, the thermoformed film or sheet is shaped to match the shape of the material to be packaged therein. Flexible films when thermoformed as described retain some flexibility in the resulting shaped article. Thicker thermoformed sheets may provide semi-rigid or rigid articles. Thermoformed articles may be combined with additional elements, such as a generally planar film that serves as a lid sealed to the thermoformed article.

Preferably, the container is suitable for containing, transporting or storing food that may contain grease or oil, including snack foods such as chips, crackers, cookies, cereal or nuts; dry noodles, soup mix, coffee, French fries, sandwiches, pet foods and the like. Frozen or chilled foods such as ice cream, vegetables, waffles and the like may also be packaged in packages comprising the coated substrate. Nonfood items such as detergents and soaps may also be packaged in packages comprising the coated substrate. Products for serving foods may also be prepared from the coated substrate such as cold drink cups, plates, bowls and the like.

Pouches are formed from coated web stock by cutting and heat sealing separate pieces of coated web stock and/or by a combination of folding and heat sealing with cutting. Coated substrates may be formed into pouches by overlaying and heat sealing the edges of the substrate to form a seal and then sealing across the lengthwise direction of the tube (transverse seal). Other packages include containers, optionally further comprising lidding films such as cups or tubs prepared from coated substrates as described herein and flexible packages made by laminating the coated substrate to another webstock to improve characteristics such as stiffness and appearance.

Preferred packages comprise one or more of the preferred or notable or structures as described herein. Preferred packaged products comprise one or more of the preferred or notable compositions, films, structures or packages as described herein.

After preparation, the coated substrates can then take advantage of the ready dispersability of the ionomer-PVOH composition in water, for example to allow for recyclability.

Once used for its intended purpose such as for packaging or serving food, the coated substrate is easily recyclable by treatment with hot water. The ionomer-PVOH coating is readily dispersed in hot water, allowing it to be removed from the substrate. For the pereferred paper substrate, the paper is recyclable by normal means used in the paper industry within limits on coat weight and ionomer content and the weight of the paper.

The recycling process may be thought of as recovering usable fiber from the substrate, such as paper, and may include contacting the container with water at a temperature as low as ambient to about 80°C. In some embodiments, the temperature is in the range from 80 to 90°C, or 80 to 85°C, or 85 to 90°C. However, one can appreciate that if the water-dispersable ionomer-PVOH compositions can disperse in such temperatures, they can also be dispersed at temperatures above 90°C. Also, in some embodiments, the container may be cut into pieces before being contacted with water. The recovered fiber can be reused to prepare other articles, including new containers.

In normal circumstances, the water-dispersable compositions could be sufficiently dispersed in warm water in 1 hour or less, such as in 30 minutes or less or in 20 minutes or less. Once the water- dispersable ionomer composition is dispersed in the water, the substrate materials (i.e. recyclable fiber) can be recovered by standard methods. For example, the non-water dispersable materials comprised in the container, such as paperboard base material or aluminum foil, could be separated from the aqueous phase by, for example filtration, for recycling. In some cases, it may not be necessary to separate completely dispersed ionomer-PVOH composition from paper pulp. The fiber can be reused because recycled paper typically contains some small fraction of dispersed "plastic", waxes, hot melt components, etc., and minimal amounts can be tolerated if the particle size is small.

Removing the coating from the substrate materials and/or recovering the substrate materials may involve one of the following embodiments:

The container (preferably after use) disclosed herein is first mixed with water under low shear conditions at room temperature (20 to 25°C) and then the temperature or the mixture is raised to 80 to 90°C.

The container (preferably after use) disclosed herein is mixed with water under low shear conditions at room temperature and then the temperature of the mixture is raised to 85 to 90°C.

The container (preferably after use) disclosed herein is mixed with water that is preheated to a temperature of 80 to 90°C under low shear conditions.

The container (preferably after use) disclosed herein is mixed with water that is preheated to a temperature of 85 to 90°C under low shear conditions.

Following treatment with hot water to remove the coating, the substrate materials can be collected and recycled into new articles. For example, paper and paperboard materials can be repulped by methods known in the art and processed into new articles.

The resulting aqueous ionomer-PVOH dispersion can also be further processed to recover the ionomer-PVOH composition. For example, excess water can be removed by distillation, evaporation, freeze drying, or the like to provide the composition in solid form. Alternatively, the ionomer can be purified from other water-soluble materials by subjecting the aqueous dispersion to acid treatment, providing the base ethylene acid copolymer that is insoluble in water. The solid acid copolymer can be re -neutralized according to methods disclosed herein to provide the ionomer.

EXAMPLES

Table 1 summarizes the ethylene methacrylic acid dipolymers with copolymerized units of methacrylic acid at the indicated weight % of the total acid copolymer used to prepare the ionomers in Table 2. Ionomers were prepared from the acid copolymers using standard conditions. Melt flow rate (MFR) was measured according to ASTM D 1238 at 190°C using a 2160 g load; a similar test is ISO 1 133.

Table 1

Methacrylic acid (weight %) MFR (g/10 min)

ACR-1 19 400

ACR-2 19 250

ACR-3 23 270

Ionomers

Table 2 summarizes the ionomers derived from the ethylene methacrylic acid dipolymers, with the indicated percentage of the carboxylic acid groups neutralized with sodium hydroxide to form sodium salts or potassium carbonate to form potassium salts. The water dispersability was determined according to the following procedure, which illustrates addition of the non-neutralized acid copolymer or ionomer to heated water. The procedure produced a mixture of water and 10 weight % solid loading (as weighed prior to addition to the water). Into a 1 quart (946.4 ml) metal can placed into a heating mantle element was added 500 ml of distilled water. An overhead paddle stirrer (3-paddle propeller type stirrer) was positioned into the center of the metal can and turned on to provide slow mixing. A thermocouple was positioned below the water surface between the paddle stirrer and the metal can surface. The paddle stirrer was typically set at a speed of about 170 rpm at the beginning of the process and generally raised to about 300 to 470 rpm as the viscosity built during dispersion formation. The distilled water was then heated with an Omega temperature controller to a temperature of 90 °C. The ionomer (55.5 grams, in the form of melt cut pellets) indicated in Table 2 was then added in one portion and the resulting mixture was stirred for a total of 20 minutes. The resulting mixture was then allowed to cool to room temperature. For those materials that formed a dispersion at a given temperature (denoted as "Yes" in Table 2), the dispersion was generally formed in less than 10 minutes and was stable even after being cooled to room temperature. As used herein, "stable" means that the dispersion, a liquid with no visible solids, did not exhibit any visual change after the initial cooling or on storage at room temperature. The sample dispersions remained as liquids with no settling after storing at room temperature for periods of several weeks or longer. Table 2

Neutralization Water Dispersability lonomer Base Copolymer Ion Level (%) MFR (g/10 min.) at 80 °C at 90 °C

ION-1 ACR-1 Na 50 5.3 No Yes

ION-2 ACR-2 Na 60 1.4 Yes Yes

ION-3 ACR-1 Na 70 1 - Yes

ION-4 ACR-3 Na 55 1.4 - Yes

ION-5 ACR-2 K 50 3.9 - Yes

ION-6 ACR-1 K 50 5.4 - Yes

ION-7 ACR-1 Na 60 1.5 Yes Yes

ION-8 ACR-1 Na 65 1.4 No Yes

ION-9 ACR-2 Na 65 1.1 No Yes

ION-2 and ION-7 demonstrate a surprisingly preferred embodiment of forming dispersions at the lower temperature of 80 °C, even though equivalent compositions based on the same parent ethylene acid copolymers with higher neutralization levels (ION-9 and ION-8, respectively) did not demonstrate the same advantage.

Samples of poly(vinyl alcohol) (PVOH) compositions are commercially available from DuPont under the Elvanol^® tradename, with their hydrolysis levels and 4 weight % aqueous viscosity at 20 °C reported in Table 3. PVOH-7 is a PVOH copolymer, so it is not characterized in terms of % hydrolysis. However, it is considered fully hydrolyzed, since there are very few acetate groups remaining. PVOH-8 and PVOH-9 were commercially obtained from Chang Chun Petrochemical Co. (CCPC) of Taiwan. Aqueous solutions of the PVOH materials in Table 3 were prepared by suspending the solid material in cool water and then heating to 90 to 95 °C with stirring until all solid material disappeared. The poly(vinyl alcohol) solutions were clear, transparent solutions.

Table 3

PVOH Hydrolysis Level (%) 4 weight % aqueous viscosity at 20 °C (cP) (weight %)

PVOH-1 99+ 27-33 11.5

PVOH-2 95-97 25-30 10.6

PVOH-3 87-89 5-6 12.6

PVOH-4 87-89 11-14 10

PVOH-5 87-89 8-10 About 10

PVOH-6 99+ 12-15 10

PVOH-7 Fully hydrolyzed 24-32 10

PVOH-8 90-93 27-33 11.2

PVOH-9 95-97 25-30 10.6

Preparative Samples 1-12 and Comparative Samples C1-C4

These samples show the method of mixing preformed aqueous PVOH solutions with a preformed aqueous ionomer dispersion. An 11.6 weight % aqueous dispersion of ION-2 was prepared by suspending the solid material in hot (90 to 95 °C) water and stirring until all solid material disappeared. The ionomer dispersion was a translucent milky liquid. Blends of the aqueous ionomer dispersion with the aqueous PVOH solutions summarized in Table 3 were prepared by mixing them together at room temperature to prepare the blend compositions summarized in Table 4. Specifically, each of the aqueous PVOH solutions were mixed with the aqueous ionomer dispersion in ratios of 80:20; 60:40; 40:60 and 20:80 (weigh weight).

The viscosities of the Examples and Comparative Examples were measured using a TA

Instruments AR 2000 controlled-stress rheometer equipped with narrow-gap (1 mm) concentric cylinder geometry. The concentric cylinder geometry consists of a temperature controlled jacket, a cup (or stator), and a DIN rotor (or bob). When a test is performed, the sample is placed in the cup and then the rotor is inserted. A more cylindrical rotor and often higher rpm is used for very low viscosity fluids such as the ionomer dispersions. Higher viscosity fluids such as the PVOH solutions or the ionomer- PVOH blend dispersions require rotors consisting of a narrow shaft with a disk, run at lower rpm. Since the drag of the fluid on the rotor is proportional to the surface area, the contribution to the measured torque from the shaft of the rotor was small relative to the thick part of the rotor. As a result, the height of the fluid on the shaft was not critical and the cup was filled so that the height of the fluid in the cup was above the thick part of the rotor when the rotor is inserted. A solvent cover was placed over the top of the cup. This helped to minimize the effects of solvent evaporation or moisture absorption on the measured properties.

Instrument bias was checked using a nominal 10 cP (actual viscosity 9.5 cP) and a nominal 10,000 cP (actual viscosity 9860 cP) viscosity standard. The bias was 4% or less for both standards at shear rates from 0.1 to 100 sec^"1.

The viscosity of each test sample was measured at 25 °C. The concentric cylinder geometry was set at the desired test temperature. Proportional amounts of each material for a total of 20 mL were loaded into the cup using a syringe, the solutions were mixed using a spatula for 10 seconds, the DIN was lowered to a gap of 5920 μιη between the bottom of the rotor and the cup, a cover was placed over the geometry, and the test was started. A time sweep was performed at a shear rate of 20 sec^"1. The viscosity for each sample was monitored as a function of time by taking data points every 10 seconds up to 1800 seconds. The measurement was performed at least in duplicate with a fresh sample loading each time and the average values are reported in Table 4 at representative time points. The column entry "Viscosity Ratio" denotes the ratio of the viscosity of the ionomer- PVOH blend dispersion to the viscosity of the PVOH dispersion without ionomer, each measured at 1800 seconds. Table 4

Composition Viscosity

Sample (weight % in water) Viscosity (cP) after time (seconds) Ratio

10 100 500 1000 1500 1800

CI ION-2 (11.6) 3 3 2 2 2 2 -

C2 PVOH-1 (11.5) 792 773 767 767 766 766 -

1 PVOH-1 (9.2) 368 373 399 423 448 463 0.6

ION-2 (2.3)

2 PVOH-1 (6.9) 152 156 172 187 201 211 0.28

ION-2 (4.6)

3 PVOH-1 (4.6) 51 52 58 63 67 70 0.09

ION-2 (7.0)

4 PVOH-1 (2.3) 15 15 16 17 18 19 0.03

ION-2 (9.3)

C3 PVOH-2 (10.6) 484 478 476 476 476 476 -

5 PVOH-2 (8.5) 415 423 455 492 534 562 1.18

ION-2 (2.3)

6 PVOH-2 (6.4) 328 338 386 440 510 560 1.17

ION-2 (4.6)

7 PVOH-2 (4.2) 247 260 319 382 455 510 1.07

ION-2 (7.0)

8 PVOH-2 (2.1) 118 124 156 185 215 236 0.49

ION-2 (9.3)

C4 PVOH-3 (12.6) 32 31 31 31 31 31 -

9 PVOH-3 (10.1) 28 27 27 28 28 28 0.91

ION-2 (2.3)

10 PVOH-3 (7.6) 27 27 28 29 29 30 0.96

ION-2 (4.6)

11 PVOH-3 (5.0) 30 30 31 33 35 37 1.19

ION-2 (7.0)

12 PVOH-3 (2.5) 23 22 23 25 26 27 0.87

ION-2 (9.3)

Table 5 summarizes a similar comparison using a 10 weight % aqueous solution of PVOH-4 blended with a 10 weight % aqueous dispersion of ION-2. Viscosity measurements on ION-2 were run at 100 rpm and 20 °C using a cylindrical rotor and the PVOH-4 and the blend at 60 rpm and 20 °C using a rotor consisting of a shaft with a disc.

Table 5

Composition Viscosity (cP) after time (seconds) Viscosity

Sample (weight % in water) 0 300 600 900 1200 1500 1800 Ratio

C5 ION-2 (10) - - 5.2 -

C6 PVOH-4 (10) - - 236 -

13 PVOH-4 (6) 229 209 211 229 214 205 206 0.87

ION-8 (4)

The viscosity behavior for the 60:40 blend of PVOH-4 and ION-2 was similar to the behavior of the other samples. Similar viscosity behavior was also observed for blends of PVOH-6, PVOH-7, PVOH- 8 and PVOH-9 with ION-2 in aqueous dispersions. Coating Examples 1-24 and Comparative Examples C1-C7

These examples, summarized in Tables 6 and 7, demonstrate coating paperboard with aqueous dispersions. Aqueous ionomer-PVOH dispersions were prepared according to the general procedure above. The substrate was a 0.22-inch caliper, nominal 77-pound basis weight paperboard coated on one side with clay for printability commercially available as CartonMate^® Bleached Board from RockTenn Converting Company, Demopolis AL. An 8-inch by 1 1 -inch sample of the substrate was coated on the side opposite to the clay coating in the following manner: The sample was weighed and then attached to a flat piece of plywood with a spring loaded clip at one end. Approximately 80 ml of the ionomer-PVOH dispersion prepared as above was applied to the clipped end and the dispersion spread and smoothed with a 0.0036-inch wire-wound Meyer rod in one motion to cover the remaining portion of the paper sample. The excess dispersion was removed in the spreading operation. Because of the difficulty in drying to constant weight, the dry coating weight pickup was estimated by immediately reweighing the sample to determine the wet coating weight and calculating the amount of polymer present from the weight % of the dispersion. Depending on the diameter of the wire wound around the rod, the coating weight may be about 4 to about 12 grams per square meter. In these examples, the coating weight was about 6 to about 12 grams per square meter.

The wet coated sample was dried in a forced air oven set at 105 °C for five minutes. After drying the sample was allowed to cool at room temperature and then further conditioned as required for additional testing. The ionomer-PVOH coatings appeared colorless, uniform and slightly glossier than an uncoated control.

Table 6

Weight ratio Dry Pickup

Example ION-2 PVOH Dry Weight Wet Weight g % g/m²

CI 100 0 24.29 29.69 0.540 2.22 8.47

C2 0 PVOH-6 100 24.80 28.82 0.402 1.62 6.18

C3 0 PVOH-6 100 24.40 29.28 0.488 2.00 7.62

1 20 PVOH-6 80 24.34 28.21 0.387 1.59 6.06

2 20 PVOH-6 80 24.41 28.12 0.371 1.52 5.79

3 40 PVOH-6 60 24.44 28.97 0.453 1.85 7.06

4 40 PVOH-6 60 24.48 28.35 0.387 1.58 6.02

5 60 PVOH-6 40 24.35 30.12 0.577 2.37 9.03

6 60 PVOH-6 40 24.63 29.72 0.509 2.07 7.87

7 80 PVOH-6 20 24.54 30.78 0.624 2.54 9.69

8 80 PVOH-6 20 24.44 30.19 0.575 2.35 8.96

C4 0 PVOH-7 100 24.51 28.64 0.413 1.69 6.42

C5 0 PVOH-7 100 24.47 30.46 0.599 2.45 9.33

9 20 PVOH-7 80 25.30 29.81 0.451 1.78 6.79

10 20 PVOH-7 80 25.58 33.15 0.757 2.96 11.28

11 40 PVOH-7 60 24.64 28.83 0.419 1.70 6.48

12 40 PVOH-7 60 24.76 29.01 0.425 1.72 6.54

13 60 PVOH-7 40 24.45 29.35 0.490 2.00 7.64

14 60 PVOH-7 40 24.46 29.34 0.488 2.00 7.60

15 80 PVOH-7 20 24.28 29.39 0.511 2.10 8.02

16 80 PVOH-7 20 24.48 30.92 0.644 2.63 10.02

Table 7

Volume ratio (%) Weight ratio (%) Dry Wet Dry Pickup

Example ION-2 PVOH ION-2 PVOH Weight Weight g % g/m²

C6 0 PVOH-8 100 0 100 22.05 25.44 0.372 1.69 6.44

17 20 PVOH-8 80 22 78 25.04 30 0.54 2.18 8.30

18 40 PVOH-8 60 43 57 24.87 29.47 0.51 2.03 7.75

19 60 PVOH-8 40 63 37 24.62 29.64 0.55 2.24 8.55

20 80 PVOH-8 20 82 18 24.6 29.69 0.56 2.28 8.67

C7 0 PVOH-9 100 0 100 21.33 25.49 0.458 2.15 8.17

21 20 PVOH-9 80 23 77 24.62 29.15 0.50 2.02 7.71

22 40 PVOH-9 60 44 56 25.25 30.49 0.58 2.28 8.70

23 60 PVOH-9 40 64 36 24.72 29.26 0.50 2.02 7.70

24 80 PVOH-9 20 83 17 25.4 30.43 0.55 2.18 8.30

The coated samples were tested in the Kit test (TAPPI T 559) for grease resistance. The Kit test uses a series of mixed solvents, combinations of castor oil, n-heptane and toluene, numbered from 1 (100% castor oil) to 12 (45/55 ratio of toluene/n-heptane), in order of decreasing viscosity and surface tension. The reported number is the highest number solvent that shows no sign of staining the tested material after 15 seconds of contact.

The coated samples were also tested in the Cobb test (TAPPI T 441) for water resistance. This test measures the weight gain due to water absorption under standard conditions. The Cobb test time can be varied according to the paper type. The test used herein used was conducted by pouring 100 ml of water onto a paper sample clamped under a ring enclosing 100 square centimeters and pouring off the water after two minutes exposure. The weight gain is multiplied by 100 to report the results in grams/square meter.

The results of both Kit and Cobb tests are summarized in Table 8, reported as the average of two samples. The uncoated substrate had very poor results in the Kit test for grease resistance and relatively high water absorption in the Cobb test. The substrate coated with an aqueous dispersion of ION-2 alone (Comparative Example CI) showed improvement over the uncoated substrate in both Kit and Cobb tests. Substrates coated with PVOH-6 alone (Comparative Examples C3 and C4) had better results in the Kit test than those coated with the ionomer, but absorbed more water. Examples 1-8, coated with aqueous dispersions of ionomer and PVOH-6 provided excellent grease resistance, as indicated by the high scores in the Kit test, and provided reduced water absorption compared to the uncoated substrate. The Kit test results are surprisingly superior to that expected from a weighted average of the substrates coated with ionomer or PVOH-6 alone. The results of samples coated with blends of ION-2 with PVOH-7, PVOH-8 and PVOH-9 were similar. In general, excellent grease resistance could be obtained with PVOH:ionomer ratios from about 10:90 to about 40:60, while providing the best water absorption resistance.

Table 8

Example Kit Test 2 minute Cobb Test, g/m²

Uncoated Substrate 0 36

CI 6 5

C2 and C3 9 42

1 and 2 11 34

3 and 4 11 26

5 and 6 11 24

7 and 8 10 21

C4 and C5 10 50

9 and 10 11 57

11 and 12 10 43

13 and 14 11 28

15 and 16 11 32

C6 12 34.4

17 12 52.5

18 11 35

19 12 31

20 10 12.5

C7 12 40.9

21 12 50.7

22 12 32

23 12 26.9

24 12 12.1

The results summarized in Table 8 show that aqueous blends of ionomers and PVOH can be used as coatings to provide excellent grease resistance and improved water resistance for paper and paperboard substrates. Addition of relatively small amounts of PVOH to ionomer dispersions can dramatically improve grease resistance. The best results were provided by aqueous dispersions of ION-2 with PVOH-9, which has a hydrolysis level of 95 to 97 % and 4 weight % aqueous viscosity at 20 °C of 25 to 30 cP.

Claims

CLAIMS What is claimed is:

1. A blend composition comprising

(ii) a hydrolysis level of 95 mole % to 100 %; and

(b) 1 to 99 weight %, based on the combination of (a) and (b), of an ionomer composition comprising a parent acid copolymer that comprises copolymerized units of ethylene and 18 to 30 weight % of copolymerized units of acrylic acid or methacrylic acid, based on the total weight of the parent acid copolymer, the acid copolymer having a melt flow rate (MFR) from 200 to 1000 g/10 min., measured according to ASTM D 1238 at 190 °C with a 2160 g load, wherein 50% to 70% of the carboxylic acid groups of the copolymer, based on the total carboxylic acid content of the parent acid copolymer as calculated for the non-neutralized parent acid copolymer, are neutralized to carboxylic acid salts comprising potassium cations, sodium cations or combinations thereof.

2. The blend composition of claim 1 wherein (b) is present in the combination of (a) and (b) in an amount from 10 to 95 weight %, preferably wherein (b) is present in the combination of (a) and (b) in an amount from 60 to 95 weight %, (a) being present in a complementary amount.

3. The blend composition of claim 1 or 2 wherein the poly(vinyl alcohol) is characterized by a hydrolysis level of 80 to 93 mole % and a 4 weight % aqueous viscosity at 20 °C of 7 cp or less.

4. The blend composition of claim 1 or 2 wherein the poly(vinyl alcohol) is characterized by a hydrolysis level of 95 to 100 mole %.

5. The blend composition of claim 1, 2, 3 or 4 wherein the acid copolymer has a MFR from 250 to 400 g/10 min.

6. The composition of claim 1, 2, 3, 4 or 5 in the form of an aqueous dispersion comprising water and 0.001 to 50 weight % of the combination of (a) and (b).

7. An article comprising the blend composition of claim 1, 2, 3, 4 or 5.

8. The article of claim 7 comprising a multilayer structure comprising a coated substrate comprising a surface layer on the substrate and the surface layer comprises the blend composition of claim 1, 2, 3, 4 or 5, preferably wherein the substrate comprises paper, paperboard, cardboard, pulp-molded shape, textile, material made from a synthetic fiber spun fabric, film, open-cell foam, closed-cell foam, or metallic foil, more preferably paper, paperboard, cardboard, or pulp-molded shape.

9. A method to produce an aqueous dispersion of claim 6 comprising (1) providing an aqueous poly(vinyl alcohol) solution comprising water and a poly(vinyl alcohol) composition comprising a poly(vinyl alcohol) characterized by

(1) a hydrolysis level of 80 to 94 mole % and a 4 weight % aqueous viscosity at 20 °C of 15 cp or less; or

(ii) a hydrolysis level of 95 mole % to 100 %;

(2) providing an ionomer composition comprising an ionomer comprising a parent acid copolymer that comprises copolymerized units of ethylene and 18 to 30 weight % of copolymerized units of acrylic acid or methacrylic acid, based on the total weight of the parent acid copolymer, the acid copolymer having a melt flow rate (MFR) from 200 to 1000 g/10 min., measured according to ASTM D 1238 at 190 °C with a 2160 g load, wherein 50% to 70% of the carboxylic acid groups of the copolymer, based on the total carboxylic acid content of the parent acid copolymer as calculated for the non- neutralized parent acid copolymer, are neutralized to carboxylic acid salts comprising potassium cations, sodium cations or combinations thereof;

(4) optionally cooling the heated aqueous blend dispersion to a temperature of 20 to 30 °C, wherein the combination remains dispersed in the liquid phase.

10. The method of claim 9 wherein the aqueous poly(vinyl alcohol) solution comprises from 0.001 to 50 weight % of the poly(vinyl alcohol), based on the total weight of the poly(vinyl alcohol) and water, preferably wherein the poly(vinyl alcohol) is characterized by a hydrolysis level of 80 to 93 mole % and a 4 weight % aqueous viscosity at 20 °C of 7 cp or less.

1 1. The method of claim 9 or 10 wherein the ionomer composition is an aqueous dispersion comprising the ionomer and water, wherein the aqueous dispersion is produced by contacting a solid ionomer composition with water at a temperature from 80 to 100 °C; optionally followed by cooling to a temperature of 20 to 30 °C, wherein the ionomer remains dispersed in the aqueous phase; and wherein the aqueous dispersion comprises from 0.001 to 50 weight % of the ionomer, based on the total weight of the ionomer and water.

12. The method of claim 9 or 10 wherein the ionomer composition is in solid form and the mixing comprises

(1) (a) heating the aqueous poly(vinyl alcohol) solution to a temperature from 80 to 100 °C;

(b) contacting the solid ionomer composition with the heated aqueous poly(vinyl alcohol) solution;

(c) continuing heating at a temperature from 80 to 100 °C until the solid ionomer composition has completely dispersed; or (2) (d) contacting the solid ionomer composition with the aqueous poly(vinyl alcohol) solution to provide a mixture; and

(e) heating the mixture to a temperature from 80 to 100 °C until the solid ionomer composition has completely dispersed.

13. A method to form a coating comprising a blend of ionomer and poly(vinyl alcohol) on a substrate, the method comprising

(1) providing the blend composition of claim 1, 2, 3, 4 or 5;

(2) providing a substrate; and

(3) coating the blend composition onto the substrate.

14. The method of claim 13 wherein the substrate comprises paper, paperboard, cardboard, pulp-molded shape, textile, material made from a synthetic fiber spun fabric, film, open-cell foam, closed- cell foam, or metallic foil, preferably paper, paperboard, cardboard, or pulp-molded shape.

15. The method of claim 13 or 14 wherein the blend composition is provided in the form of an aqueous dispersion comprising water and 0.001 to 50 weight % of the combination of (a) and (b), preferably prepared according to the method of claim 9, 10, 1 1 or 12; the blend composition is coated onto the substrate as the aqueous dispersion and the method further comprises (4) drying the coated substrate at a temperature of 20 to 150 °C.

16. The method of claim 13 or 14 wherein the blend composition is provided in the form of a preformed film comprising the combination of (a) and (b); (3) comprises (3a) producing a prelaminate structure comprising the ionomer-polyolefin film layer adjacent to the substrate; and (3b) laminating the ionomer-polyolefin film layer to the substrate at a temperature from 50 to 150 °C, optionally with applied pressure; and the method further comprises (4) cooling the coated substrate to a temperature of 20 to

30 °C.