WO2006127290A2 - Hydrophilic coatings for hydrophobic substrates - Google Patents

Hydrophilic coatings for hydrophobic substrates Download PDF

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Publication number
WO2006127290A2
WO2006127290A2 PCT/US2006/018258 US2006018258W WO2006127290A2 WO 2006127290 A2 WO2006127290 A2 WO 2006127290A2 US 2006018258 W US2006018258 W US 2006018258W WO 2006127290 A2 WO2006127290 A2 WO 2006127290A2
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WIPO (PCT)
Prior art keywords
starch
composition
hydrophilic
water
coating
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PCT/US2006/018258
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French (fr)
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WO2006127290A3 (en
Inventor
Damodar R. Patil
George F. Fanta
Frederick C. Felker
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Biotechnology Research & Development Corporation
United States Department Of Agriculture
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Publication date
Priority claimed from US11/138,737 external-priority patent/US20060269679A1/en
Priority claimed from US11/202,794 external-priority patent/US20070036899A1/en
Application filed by Biotechnology Research & Development Corporation, United States Department Of Agriculture filed Critical Biotechnology Research & Development Corporation
Publication of WO2006127290A2 publication Critical patent/WO2006127290A2/en
Publication of WO2006127290A3 publication Critical patent/WO2006127290A3/en

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D101/00Coating compositions based on cellulose, modified cellulose, or cellulose derivatives
    • C09D101/08Cellulose derivatives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04Coating
    • C08J7/0427Coating with only one layer of a composition containing a polymer binder
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04Coating
    • C08J7/043Improving the adhesiveness of the coatings per se, e.g. forming primers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04Coating
    • C08J7/056Forming hydrophilic coatings
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D103/00Coating compositions based on starch, amylose or amylopectin or on their derivatives or degradation products
    • C09D103/02Starch; Degradation products thereof, e.g. dextrin
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D103/00Coating compositions based on starch, amylose or amylopectin or on their derivatives or degradation products
    • C09D103/04Starch derivatives
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D105/00Coating compositions based on polysaccharides or on their derivatives, not provided for in groups C09D101/00 or C09D103/00
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2433/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L3/00Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
    • C08L3/02Starch; Degradation products thereof, e.g. dextrin
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L65/00Compositions of macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain; Compositions of derivatives of such polymers

Definitions

  • This invention relates generally to adhesive coatings. More specifically, this invention relates to hydrophilic adhesive coatings for hydrophobic substrates, for example water-resistant hydrophilic adhesive coatings for hydrophobic substrates. Background of the Invention
  • One approach to surface modification involves altering the hydrophobicity of the polymeric surface by applying a coating having the desired properties.
  • Introduction of a hydrophilic coating to the hydrophobic surface of a polymer material would make these materials suitable for applications that require biocompatibility, compatibility with hydrophilic reagents, reduced electrostatic charge, reduced friction, improved barrier properties and improved absorption of water-based dyes and inks.
  • the application of a hydrophilic coating to a hydrophobic substrate typically results in a surface coating with poor adhesion and durability.
  • hydrophilic coating to a hydrophobic surface may present other drawbacks.
  • the hydrophilic coating is wettable and in some instances, such coatings when subjected to water for extended time periods and rubbed may no longer adhere to the substrate surface.
  • water-resistant nature of a hydrophilic surface is desirable.
  • a hydrophilic coating composition comprising a hydrophilic base material, an adhesion promoter and a surfactant.
  • a water-resistant hydrophilic coating composition comprising a hydrophilic base material, an adhesion promoter, a surfactant and a crosslinking agent.
  • a method of applying a hydrophilic coating to a hydrophobic surface comprising: preparing a hydrophilic coating, heating the hydrophilic coating and spraying the hydrophilic coating on the hydrophobic surface.
  • a method of preparing a hydrophilic coating comprising: preparing a solution of hydrophilic base material, heating the solution of hydrophilic base material and mixing at least a portion of the heated hydrophilic base material solution with an adhesion promoter and a surfactant.
  • a method of applying the water-resistant hydrophilic coating comprising preparing a water-resistant hydrophilic coating, spraying the water- resistant hydrophilic coating on the hydrophobic surface and heating the coated surface.
  • a method of water-proofing a polysaccharide coating comprising crosslinking the starch hydroxyl functionalities.
  • Figure 1 is a schematic of a pneumatic coating sprayer.
  • Figure 2 is a graph of coating adhesion for different hydrophilic coating formulations with 4% starch.
  • Figure 3 is a graph of coating adhesion for different hydrophilic coating formulations with 6% starch.
  • Figure 4A is a scanning electron micrograph of a substrate with a hydrophilic coating.
  • Figure 4B is an annotated scanning electron micrograph of Figure 4A.
  • a hydrophilic coating comprises a hydrophilic base material, an adhesion promoter, and a surfactant.
  • a hydrophilic coating (HC) comprises a hydrophilic base material, an adhesion promoter, a surfactant and a crosslinking agent.
  • the hydrophilic base material may be a water-soluble polymer.
  • water-soluble polymers include natural gums such as karaya, tragacanth, ghatti and guar gum; polyvinyl alcohol; polyvinyl pyrrolidone; modified celluloses such as carboxymethyl, hydroxyethyl or hydroxypropyl cellulose; polyacrylic acid; polyethylenimine; or combinations thereof.
  • the water-soluble polymer is a starch, modified starch or starch mixture.
  • the starch may be a non-gelling starch, a waxy starch, an amylose-containmg starch or combinations thereof.
  • a non-gelling starch is one that does not form a viscous semi-rigid structure upon absorption of water and heating or during the cooling of said solution.
  • a waxy starch is one that contains less than about 10% weight/weight (w/w) amylose.
  • an amylose-containing starch is one having equal to or greater than about 10% amylose.
  • the amylose content of the starch is less than about 13%, alternatively less than about 12%.
  • the starch is a gelling starch wherein gel formation can be reversed or inhibited.
  • the starch may be an amylose-containing starch containing greater than or equal to about 25% amylose.
  • Starch containing greater than or equal to about 25% amylose when dissolved in water and heated forms a gel when the solution is allowed to cool at room temperature.
  • agitating the cooled solution for example by stirring or shaking, may reverse the gel formation.
  • gel formation in a 25% amylose containing starch solution may be inhibited by rapidly cooling the solution. Methods of rapidly cooling a solution are known to one skilled in the art and include for example transfer of the hot solution to an ice bath.
  • Starches suitable for use in the HC include without limitation those isolated from cereal crops such as rice and corn or tuber crops such as cassava and potato.
  • suitable starches include Starch from Rice (S7260) and/or Starch from Cora (S9679) both available from Sigma, Aldrich and Pure Food Grade starch and/or 7350 Waxy starch #1 both available from A. E. Staley.
  • the HC comprises from about 2% w/v to about 8% w/v starch, alternatively from about 4% w/v to about 6% w/v starch.
  • aqueous solution also refers to aqueous dispersions, in which solid materials are intimately dispersed in water so that they do not readily settle or otherwise separate from the aqueous phase.
  • aqueous solutions of each reagent in the HC are prepared by dissolving the reagent in a suitable volume of water. The concentration of the reagents at this point is termed the initial % w/v.
  • the initial % w/v is calculated by dividing the grams of reagent used by the volume in milliliters of solution (e.g., water) added to produce the aqueous solution.
  • these aqueous solutions of reagents are used to prepare the HC.
  • the HC formulations are based on 100 grams of HC, with a resultant calculation of the grams of aqueous reagent required to prepare the 100 grams of HC.
  • the concentration of the reagent is diluted from the initial % w/v to a final % w/v.
  • the starch is provided as an aqueous starch solution.
  • This aqueous starch solution may contain a sufficient amount of starch and water to produce an HC with a viscosity suitable for ease of pouring and/or sprayability.
  • the starch slurry may comprise an initial % w/v of from about 10% to about 20% starch in aqueous solution having a pH of from about 5 to about 7, alternatively about 7.
  • the water-soluble polymer may be substituted with a water- dispersible or water-reducible polymer to provide a final formulation that is less hydrophilic in nature than the HC formed with a water-soluble polymer.
  • a water-dispersible and water-reducible polymers are known to one skilled in the art.
  • HCs formed using water- dispersible or water-reducible polymers as the hydrophilic base material may result in coatings that are less hydrophilic than those formulated using water-soluble polymers as the hydrophilic base material.
  • the HCs prepared with water-reducible or water-dispersible polymers may be more hydrophilic than the substrate surface.
  • an HC having a water-dispersible polymer or water-reducible polymer as the hydrophilic base material may provide a coating that enhances desirable surface properties of the substrate to which it is applied.
  • the term HC refers collectively to coatings prepared with water-dispersible, water-reducible or water-soluble polymers.
  • the HC comprises an adhesion promoter.
  • the adhesion promoter may serve to increase the compatibility between the HC and the hydrophobic substrate through the reduction of interfacial tension.
  • Interfacial tension is defined as the surface free energy that exists between two immiscible liquid phases, such as oil and water, hi an embodiment, the adhesion promoter is any material chemically compatible with the HC that serves to increase the adherence of the HC to the hydrophobic substrate by reducing the interfacial tension.
  • the adhesion promoter is an epoxy resin present in amounts of from about 0.5% to about 2.0% of the HC.
  • adhesion promoters include EPI-REZ Resin 3510-W-60 available from Resolution Performance Products and Epoxy 6128W65 from Pacific Epoxy Polymers.
  • an adhesion promoter for use in the HC e.g., EPI- REZ Resin 3510-W-60
  • Table I has about the physical properties given in Table I. Table I
  • the HC comprises a surfactant.
  • a surfactant in the HC may serve to modify physical properties thereof such as the surface tension, emulsification or cloud point.
  • the surface tension is defined as the free energy between a liquid and air.
  • the surfactant is any material chemically compatible with the HC that is capable of reducing the surface tension of the HC while increasing adhesion of the HC to the substrate.
  • the surfactant is a fluorosurfactant.
  • the surfactant is sodium lauryl sulfate.
  • the HC comprises from about 0.05% to about 0.5% of surfactant, alternatively from about 0.1% to 0.3% of surfactant, alternatively about 0.25% surfactant.
  • suitable surfactants include ZONYL FSA and ZONYL FSP available from Dupont and sodium lauryl sulfate available from Sigma-Aldrich.
  • a surfactant for use in the HC e.g., ZONYL FSP
  • ZONYL FSP has about the physical properties given in Table IL
  • the HC comprises a crosslinking agent.
  • a crosslinking agent in the HC may serve to render the HC water-resistant through a reaction of the starch hydroxyl groups with a functionality of the crosslinking agent. Such reactions would make the starch hydroxyl groups unable to hydrogen bond with water thus resulting in a water-resistant coating.
  • the addition of a crosslinking agent to the HC may also increase the resistance of the starch to swelling and gelatinization.
  • the crosslinking agent is a melamine resin, alternatively a methylated melamine resin, alternatively a methylated melamine formaldehyde resin, alternatively a methylated high imino melamine resin, alternatively a derivative of hexamethoxymethylmelamine (HMMM) or combinations thereof.
  • the HC comprises from about 0.5% to about 4% cross-linking agent, alternatively from about 1% to about 3% cross-linking agent, alternatively about 2% cross-linking agent.
  • a representative example of a suitable crosslinking agent is a methylated high imino melamine resin sold as CYMEL 323 by Cytec Industries Inc.
  • a crosslinking agent for use in the HC e.g., CYMEL 323) has about the physical properties given in Table III.
  • M/F/Me refers to the ratio of metholyated melamine to formaldehyde to melamine in the crosslinking agent.
  • the crosslinking agent forms multimers in solution. This value is the approximate amount of HMMM monomer present in solution.
  • the HC may optionally comprise a crosslinking agent accelerator (CAA).
  • CAA crosslinking agent accelerator
  • Such a compound may serve to reduce the reaction time of the crosslinking agent and accelerate the formation of a water-resistant HC.
  • the CAA is any agent chemically compatible with the HC and that is able to accelerate the reaction of the crosslinking agent and hydrophilic base material
  • the CAA is a polymer, alternatively an anionic polymer, alternatively a carboxyl-containing polymer, alternatively a carboxylated styrene- butadiene latex or combinations thereof
  • the HC comprises from about 2% to about 4% CAA.
  • a representative example of a suitable CAA is a carboxylated styrene-butadiene latex sold as ROVENE 4009 by Mallard Creek Polymers Inc.
  • the CAA e.g., ROVENE 4009 has about the physical properties given in Table IV.
  • Tg is the glass transition temperature
  • the HC may further comprise an effective amount of additives for improving or changing the properties thereof, including without limitation emulsifiers, plasticizers or combinations thereof,
  • the HC contains a plasticizer, which may serve to increase the flexibility, durability and shelf life thereof.
  • the HC contains an emulsifier that may prevent separation of the formulation components. Suitable plasticizers and emulsifiers are known to one of ordinary skill in the art.
  • the HC may contain a single compound that functions as both a plasticizer and an emulsifier.
  • a plasticizer that also functions as an emulsifier for use in the HC is a nonionic/anionic wax emulsion sold as AQUABEAD 270E by Micro Powders Inc.
  • Other additives chemically compatible with the formulation may be introduced by one skilled in the art to vary the properties of the HC as needed.
  • the HC may be varied to contain antimicrobial agents or dyes if necessary to impart certain physical properties to the hydrophobic substrate.
  • the HC may comprise from about 4 to about 6% hydrophilic base material, from about 0.5 to about 2% adhesion promoter, from about 0.1 to about 0.25% surfactant and optionally an effective amount of any additional additives with the remainder of the HC being an aqueous carrier fluid, such as water, hi an embodiment, the nongelling starch comprises from about 4% to about 6% solids in the aqueous hydrophilic coating dispersion prior to application.
  • the total solids content may be from about 6 to about 1O g comprising from about 4 to about 6 grams of nongelling starch, hi an embodiment the HC has a viscosity from about 80 centipoise to about 300 centipoise (cp), alternatively from about 100 cp to about 250 cp, alternatively less than about 200 cp. hi an embodiment, the HC has an adhesion of almost 5A as determined in accordance with a modified version of ASTM D 3359-02, the tape test method to be described in detail later herein.
  • the HC may comprise from about 4% to about 6% hydrophilic base material, from about 0.5% to about 2% adhesion promoter, from about 0.1% to about 0.25% surfactant, from about 1% to about 4% crosslinldng agent, from about 2% to about 4% CAA and optionally an effective amount of any additional additives with the remainder of the HC being an aqueous carrier fluid, such as water.
  • the HC may have a total solids content from about 6% to about 18%, alternatively from about 6% to about 15%, alternatively from about 6% to about 10% based on the total weight of the HC.
  • the nongelling starch may comprise from about 4% to about 6% solids in the aqueous HC dispersion prior to application.
  • an aqueous HC having a total solids content of 10 g may comprise from about 4 to about 6 grams of nongelling starch.
  • the HC has a viscosity from about 80 centipoise to about 300 centipoise (cp), alternatively from about 100 cp to about 250 cp, alternatively less than about 200 cp.
  • the hydrophilic base material is heated prior to the addition of other reagents.
  • the hydrophilic base material is a starch that is provided as a starch slurry.
  • the starch slurry may be heated by any method suitable for heating and maintaining the temperature of the starch slurry. Without wishing to be limited by theory, heating the starch slurry may make the starch completely water-soluble by disrupting the starch granules and breaking the hydrogen bonding.
  • the starch slurry may be heated by the process of jet-cooking.
  • jet cooking refers to using a heat transfer device to instantaneously heat a flowing liquid with a hot condensable vapor and hold the heated liquid at a prescribed temperature for a prescribed time. Processes for jet cooking a starch slurry have been disclosed in US Pat.
  • Suitable conditions for jet cooking a starch slurry are known to one skilled in the art.
  • the starch slurry may be jet cooked at a temperature from about 130 °C to about 150 0 C and a pressure from about 20 psig to about 50 psig with a pumping rate of from about 0.75 to about 2.0 liters per minute.
  • the jet-cooked aqueous starch slurry is rapidly cooled by placing the slurry on ice.
  • the jet-cooked aqueous starch slurry is cooled to room temperature and a starch gel forms. The starch gel may then be redispersed in solution by mechanical agitation such as stirring or shaking.
  • the jet-cooked aqueous starch slurry is removed from the heat source and allowed to cool to room temperature.
  • the hydrophilic base material e.g., starch slurry
  • an appropriate amount of heated hydrophilic base material, adhesion promoter, surfactant, crosslinking agent (if present), CAA (if present), additives (if present) and water may be mixed together to prepare the HC.
  • the HC may be transferred to a device for application of the coating to a substrate.
  • a single device may be used to prepare the HC and coat the substrate.
  • the HC may be sprayed onto a hydrophobic surface.
  • Sprayers suitable for use in this application are known to one skilled in the art and include pneumatic sprayers or spray guns. Examples of suitable pneumatic sprayers include without limitation, the EGA Manual Touch-Up Gun available from DeVilbiss Corporation or the AJ-401-LH sprayer available from Jacto.
  • FIG. 1 An embodiment of an apparatus for coating the hydrophobic substrate with the HC is depicted in Figure 1.
  • a pneumatic sprayer 10 is coupled to container 20, reservoir 30, peristaltic pump 40 and solution container 50.
  • Container 20 may contain a compressed gas such as air that is used to atomize the HC.
  • the HC is conveyed to reservoir 30 from solution container 50 by peristaltic pump 40 through lines 100 and 101.
  • pneumatic sprayer 10 is fed by a local reservoir 30 coupled directly to the sprayer.
  • the pneumatic sprayer 10 is directly coupled to line 101 and the contents of solution container 50 are fed directly to pneumatic sprayer 10 by peristaltic pump 40 through lines 100 and 101.
  • any device suitable for storing and/or transferring the HC to the pneumatic sprayer 10 may be employed.
  • the HC may be manually transferred to the pneumatic sprayer 10.
  • the HC, the apparatus for coating the hydrophobic substrate, the hydrophobic substrate itself or combinations thereof may be heated prior to and/or during application of the HC to the substrate.
  • the pneumatic sprayer 10 may be used to apply the HC to a hydrophobic substrate in the presence of "hot air".
  • hot air is defined as having an ambient temperature of greater than about 25 0 C to less than about 60 °C.
  • the temperature of the air can be elevated through the use of a heating device such as a hot gun, heater, blower or other known device suitable for elevating the ambient air temperature.
  • the heating device is a hair dryer that may be set on the highest setting.
  • the stream of atomized HC released from the pneumatic sprayer may be heated prior to contacting the substrate by a heating device integrated or in league with the spray device.
  • a heating device external to the spray device may heat the stream of atomized HC.
  • an operator may simultaneously apply an HC to a substrate while directing a stream of hot air towards the HC as it is released from the pneumatic sprayer.
  • the use of a pneumatic sprayer may allow for the formation of droplets of HC of sufficient size that heating air causes evaporation of a substantial portion of the aqueous carrier fluid prior to the HC contacting a substrate.
  • the HC may be heated as it is being transferred from a reservoir to the spray device.
  • the sprayed HC may form a coating that dries about instantaneously upon contacting the substrate; alternatively the sprayed HC may form a coating that dries in less than about 30 seconds from the time the coating contacts the substrate.
  • a drying device may be used to facilitate drying of the HC coating on the substrate. Suitable drying devices are known to one skilled in the art.
  • the HC may be heated during application of the HC to the substrate, following application of the HC to the substrate or both during and following application of the HC to the substrate.
  • the coated substrate may be heated at any temperature and for any time period using any known heating device that is compatible with both the coating and the substrate and activates the crosslinking agent.
  • activating the crosslinking agent refers to facilitating the reaction of the crosslinking agent and hydrophilic base material.
  • the coated substrate may be heated in an oven at a temperature of equal to or greater than about 80 °C for from about 12 to about 24 hours, alternatively from about 12 hours to greater than about 24 hours.
  • the heating of the HC coated substrate is carried out under vacuum.
  • Process conditions such as time, temperature, pressure and combinations thereof may be adjusted to achieve a desired level of crosslinking and resultant performance of the HC. Such process conditions may also vary based on the HC composition, for example based on the presence and amount of a CAA.
  • the HC may form a monolayer adhesive coating on the substrate.
  • the substrate may be coated repeatedly with the HC to form a multilayer adhesive coating comprising from about 1 to about 24 layers.
  • starch adhesive coating refers to an HC comprising a starch as the hydrophilic base material that has been applied to a substrate in one or more layers.
  • the term SAC refers to an HC comprising a starch as the hydrophilic base material that has been applied to a substrate in one or more layers but that has not been heated to activate the crosslinker.
  • WRSAC water-resistant starch adhesive coating
  • a water-resistant coating refers to a coating whose adhesion after exposure to water for some time period is equivalent to its adhesion prior to water exposure.
  • the adhesion of dried coatings to hydrophobic surfaces such as polyethylene (PE) surfaces was evaluated by a modified version of ASTM testing method D 3359-02.
  • the ASTM method was modified to make it more suitable for the rapid testing of thin, flexible plastic films. Specifically, a 2.3 x 2.6 cm strip of pressure-sensitive adhesive tape (Permacel 99, from K. R. Anderson, Inc., Morgan Hill, CA) was affixed to a flat metal surface to provide a 2.3 x 2.6 cm section of adhesive. This adhesive surface was pressed firmly onto the coated PE film and was then removed by rapidly pulling it straight up at an angle of about 90° to the surface. The surface was then visually examined to estimate the amount of coating removed. Classification of test results, shown in Table V, was the same as for ASTM method D 3359-02.
  • a water-resistant coating is a coating, which passes the Rub Test.
  • the Rub Test refers to a procedure wherein the putative WRSAC is exposed to water for some period and then subjected to manual rubbing. The WRSAC is considered to have passed the Rub Test and is therefore characterized as water resistant if it continues to adhere to the substrate surface after this process.
  • the HC may be used to coat a suitable substrate thus providing a hydrophilic layer to a surface.
  • the HC containing a crosslinking agent may be used to coat a suitable substrate thus providing a water-resistant hydrophilic layer to a surface.
  • Suitable substrates for the HC include but are not limited to hydrophobic surfaces, alternatively polymeric surfaces, alternatively polyolefin surfaces.
  • the substrate may comprise a homopolymer, copolymer, or blends thereof.
  • suitable material surfaces that may serve as substrates for the HC include without limitation polyethylene terepthalate; polyethylenes such as high-density polyethylene, low-density polyethylene, linear low-density polyethylene; polypropylene; polyvinyl chloride; polystyrene and combinations thereof.
  • Polymer resins having the previously described properties may be formed into articles of manufacture or end use articles using techniques known in the art such as extrusion, blow molding, injection molding, fiber spinning, thermo forming, and casting.
  • a polymer resin may be extruded into a sheet, which is then thermoformed into an end use article such as a container, a cup, a tray, a pallet, a toy, or a component of another product.
  • end use articles into which the polymer resins may be formed include pipes, films, bottles, fibers, and so forth.
  • the substrate is an article of packaging of a consumer product. Additional end use articles would be apparent to those skilled in the art. The surface of such articles may serve as substrates for the HC.
  • the HC produces a SAC or WRSAC capable of adhering to a hydrophobic substrate with an adhesion strength of from about 3 to about 5, alternatively from about 4 to about 5 as determined in accordance with the modified version of ASTM D 3359-02, previously described, hi an embodiment, the SAC formed upon application of the HC to the substrate has an adhesion that is increased by heating the HC and substrate to activate the crosslinking agent and form a WRSAC.
  • the SAC prior to heating may have an adhesion of 4; however, following heating and the formation of a crosslinked material, the WRSAC may have an adhesion of 5.
  • the adhesion of the WRSAC is about 20% greater than that of the SAC having an identical composition, hi an embodiment, the WRSAC adheres sufficiently to the substrate surface to resist separation from the surface of the substrate when the surface is manually and/or mechanically bent or flexed, hi an embodiment, the WRSAC adheres sufficiently to the substrate surface to resist separation from the substrate surface when the WRSAC is manually rubbed, soaked in water or combinations thereof.
  • a SAC and/or a WRSAC may form a uniform hydrophilic coating on the substrate surface with a monolayer thickness of less than about 2 to less than about 5 microns.
  • a SAC and/or a WRSAC formed by the methodology disclosed herein may have starch absorbed from about 0.01 to 0.2 mg per square cm of substrate, alternatively from about 0.035 to about 0.15 mg per square cm of substrate.
  • a SAC and/or a WRSAC of this disclosure may have an opaque (turbid) appearance.
  • Scanning electron microscopy may be used to characterize the morphology and interfacial rnicrostructure of the SAC. SACs of this disclosure display a uniform coating with the appearance of some micropores and cracking that may not affect the adhesion of the coatings.
  • Substrates having HCs of this disclosure may display desirable surface properties such as biocompatibility, compatibility with hydrophilic reagents, reduced electrostatic charge, reduced friction, improved barrier properties, and water resistance.
  • the hydrophobic substrate having an HC may then display improved absorption of water-based dyes and inks, hi one embodiment, an article surface having an HC may be further processed for example, by the application of an image or colorant directly to the article.
  • Starch slurries were prepared by jet cooking 700 g of waxy corn starch in 3500 ml of water at 140 0 C and 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker. Referring to Table VI, an HC was prepared by mixing the indicated amounts of reagents. The final starch concentration was 6% w/v. All percentages in the examples are of final w/v unless otherwise indicated.
  • the HC was stirred for 30 minutes and the viscosity of the HC measured by a Brookfield Viscometer Model LV at 60 RPM.
  • the HC was fed to a pneumatic sprayer (EGA Manual Touch-Up Gun), which was used to coat a plastic surface. During application of the coating, a hot air gun set on the highest setting was aimed at the pneumatic sprayer. The HC dried upon contacting the plastic surface.
  • % w/v refers to the final % w/v in the HC.
  • the above HC had a total solids content of 9.45% and showed no settling of particles after being kept for 72 hours at 25 0 C.
  • the total solids content was varied by adjusting the amount of starch slurry in the HC from 4 to 6%.
  • the extent of adhesion for three HCs with the indicated total solids content were determined in accordance with the modified version of ASTM D3359-02, (the tape test method) as previously described and are given in Table VII.
  • Starch slurries were prepared, viscosity measured and the formulations applied to a substrate as described in Example 1. The formulation was used to coat a 6"x 6"polyethylene surface with up to 24 layers and the adhesion of the coating determined in accordance with the modified version of ASTM D 3359-02 as previously described.
  • an HC was prepared by mixing the indicated amounts of reagents, hi the presence of all of the indicated reagents, 6.0% starch, 2.0% EPI-REZ Resin 3510-W-60, 1.2% Aquabead 270E and 0.25% Zonyl FSA, the formulation has an adhesion of almost 5A. Table VIII presents the adhesion values in the absence of the indicated reagent with all other reagents remaining the same. Table Vm
  • ** % w/v refers to the final % w/v in the HC.
  • Starch slurries were prepared, viscosity measured and the formulations applied to the substrate as described in Example 1.
  • the formulation has an adhesion of almost 5A.
  • Reagents in the formulation were substituted as indicated in Table IX with the remainder of the formulation staying the same.
  • the formulation was used to coat a polyethylene surface and the adhesion of the coating determined in accordance with the modified version of ASTM D 3359-02 tape test method as previously described.
  • starch coatings displaying adhesion in the range of 4A to 5A can be prepared using a suitable combination of starch, adhesion promoter and surfactant.
  • a plasticizer or emulsifier has no effect on the adhesion but imparts other desirable properties to the formulation such as increased shelf life and preventing the separation of formulation components.
  • Starch slurries were prepared by jet cooking 75Og of starch in 3500ml of water at 140 °C and at 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker.
  • the amylose content for each of the starches used is given in Table X.
  • An HC was prepared by adding either 0.8 or 1.2% Aquabead 270E as indicated, 0.25% Zonyl FSA, water and the indicated amounts of starch slurry and EPI-REZ Resin 3510-W-60.
  • Starch slurries containing a gelling starch were also prepared.
  • slurries were prepared by jet cooking 150 g of starch (25% amylose) in 1000ml of water at 140 0 C and at 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker. This suspension was divided into two fractions: one fraction was cooled at ambient temperature (1 st Fraction) and second fraction was cooled in ice (2 nd Fraction). The fraction cooled at room temperature formed gel that could be re-dispersed by stirring or shaking. The fraction cooled in ice stayed in fluid form without forming a gel.
  • An HC was prepared by adding 0.8% Aquabead 270E as indicated, 0.25% Zonyl FSA, water and the indicated amounts of starch slurry containing the 25% amylose containing starch and EPI-REZ Resin 3510-W-60. This formulation is denoted in Table X as 25% amylose cooked once.
  • a second formulation was also prepared having the gelling 25% amylose containing starch as the hydrophilic base material, hi this preparation, after the first pass through the jet cooker, the resulting dispersion was cooked a second time under the same conditions.
  • This suspension was divided into two fractions: one fraction was cooled at ambient temperature (1 st Fraction) and second fraction was cooled in ice (2 nd Fraction).
  • the fraction cooled at room temperature formed gel that could be re-dispersed by stirring or shaking.
  • the fraction cooled in ice stayed in fluid form without forming a gel.
  • This formulation is denoted in Table X as 25% amylose cooked twice.
  • HC was stirred for 30 minutes and the viscosity of the HC measured by a Brookfield Viscometer Model LV at 60 RPM. A sample was then fed to a pneumatic sprayer, the EGA Manual Touch-Up Gun.
  • the formulation was used to coat a polyethylene surface and the adhesion of the coating determined in accordance with the modified version of ASTM D 3359-02 as previously described.
  • Figures 2 and 3 show graphs of the adhesion of the starch coating to a polyethylene substrate as a function of the concentration of EPI-REZ Resin 3510-W-60, the final concentration of starch and the amylose content of the starch. Table X lists the viscosities of the formulations.
  • Starch slurries were prepared by jet cooking 700 g of waxy cornstarch in 3500 ml of water 140 °C and at 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker.
  • An HC containing waxy starch was prepared as described in Example 1 and used to coat a polyethylene substrate. Dried samples were sputter coated with gold-palladium and were examined and photographed with SEM. Scanning electron micoscopy examination was performed with a Jeol 6400V electron microscope at a beam voltage of 15KV. Micrographs were recorded following the application of two layers of the HC, Figure 4A.
  • Figure 4B is the SEM shown in Figure 4A with annotation.
  • the SEMs show the surface morphology of the polyethylene plastic coated with 2 layers of the SAC to be essentially uniform having high areas of homogeneity, as shown in Figure 4B Structure 1 (outlined), with the appearance of micropores, as shown in Figure 4B Structure 2, and cracks, as shown in Figure 4B Structure 3.
  • the micropores may be due to air bubbles formed during coating, and cracks may be caused by localized heating during examination of surfaces by SEM.
  • Starch slurries were prepared by jet cooking 700 g of waxy cornstarch in 3500 ml of water at 140 0 C and 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker.
  • an HC was prepared by mixing the indicated amounts of reagents.
  • the remainder of the formulation i.e. the balance to total 100 grams
  • the final starch concentration was 6% w/v. All percentages in the examples are of final % w/v unless otherwise indicated.
  • the HC was stirred for 30 minutes and the viscosity of the HC measured by a Brookfield Viscometer Model LV at 60 RPM.
  • the HC was fed to a pneumatic sprayer (EGA Manual Touch-Up Gun), which was used to coat a 6" x 6" polyethylene surface.
  • a hot air gun set on the highest setting was aimed at the pneumatic sprayer in order to facilitate the HC drying upon contacting the plastic surface.
  • % refers to the final % w/v calculated as described herein while in parentheses next to each reagent is given the initial % w/v.
  • the above HC had a total solids content of 9.45% and showed no settling of particles after being kept for 72 hours at 25 °C.
  • the total solids content was varied by adjusting the amount of starch slurry in the HC from 4% to 6%.
  • the extent of adhesion for three HCs with the indicated total solids content were determined in accordance with the modified version of ASTM D 3359-02 previously described, (the tape test method) and are given in Table XII.
  • a HC was prepared as described in Comparative Example 6 with addition of the crosslinking agent CYMEL 323 to a final % w/v of 2.
  • the formulation was used to coat a PE substrate as described in Example 6 and the coated substrate was further treated by oven heating at 80 0 C in a vacuum oven for 24 hours to activate the crosslinking agent.
  • the resultant WRSAC was hydrophilic, did not separate from the surface when the substrate was manually bent or flexed and did not separate from the surface of the substrate when the coatings were manually rubbed after being soaked in water for 30 min.
  • Formulations were prepared containing different concentrations of the crosslinking agent, CYMEL 323, as indicated in Table XIIIa. Table XHIa
  • Starch slurries were prepared by jet-cooking amylose-containing starch once as described in Example 6.
  • the hot starch dispersions obtained from jet-cooking amylose- containing starch were further divided into two fractions.
  • One fraction (1 st fraction) was cooled at ambient temperature while the second fraction (2 nd fraction) was rapidly cooled by placing on ice.
  • the 1 st fraction formed a gel upon cooling that could be redispersed by stirring or shaking while the 2 nd fraction remained fluid and no gel formation was observed.
  • a second starch slurry was prepared by cooking the amylose-containing starch two times. This twice- cooked slurry was then divided into two fractions and treated as described previously.
  • Starch slurries were prepared as described in Example 6.
  • An HC was prepared by adding 6% jet-cooked starch as the hydrophilic base material, the combined plasticizer and emulsifier 1.2% AQUABEAD 270E, the adhesion promoter 2% Epi-Rez Resin 3510-W-60, the fluorosurfactant 0.25% ZONYL FSA, water, the indicated amounts of crosslinking agent, CYMEL 323 and 2%-4% of the CAA ROVENE 4009 (Table XVa-XVc).
  • HC coated substrates were prepared as previously described and heated for the indicated time periods at 80 0 C.

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Abstract

A hydrophilic coating composition comprising a hydrophilic base material, an adhesion promoter, a surfactant, and optionally a crosslinking agent. A method of applying a hydrophilic coating to a hydrophobic surface comprising preparing a hydrophilic coating, heating the hydrophilic coating and spraying the hydrophilic coating on the hydrophobic surface. A method of preparing a hydrophilic coating comprising preparing a solution of hydrophilic base material, heating the solution of hydrophilic base material and mixing at least a portion of the heated hydrophilic base material solution with an adhesion promoter and a surfactant. A method of applying a water-resistant hydrophilic coating to a hydrophobic surface comprising; preparing the water-resistant hydrophilic coating, spraying the water-resistant hydrophilic coating on the hydrophobic surface and heating the coated surface. A method of water-proofing a polysaccharide coating comprising crosslinking the starch hydroxyl functionalities.

Description

HYDROPHILIC COATINGS FOR HYDROPHOBIC SUBSTRATES
BACKGROUND OF THE INVENTION Field of the Invention
[0001] This invention relates generally to adhesive coatings. More specifically, this invention relates to hydrophilic adhesive coatings for hydrophobic substrates, for example water-resistant hydrophilic adhesive coatings for hydrophobic substrates. Background of the Invention
[0002] Articles constructed from synthetic polymeric materials such as polyethylene (PE) and polypropylene (PP) have found widespread use in our daily lives. While such polymeric materials have desirable bulk mechanical properties they often exhibit undesirable surface properties. This may limit their utility since the surface properties of polymeric materials are often a major determinant in their usage. Thus, despite their widespread applications, a need exists to remedy certain limitations associated with the usage of synthetic polymeric materials. One method of increasing the adaptability of these polymeric materials to new uses has been to modify their surface properties. In particular, modifications of the surface of hydrophobic polymeric materials are often required to extend their utility.
[0003] One approach to surface modification involves altering the hydrophobicity of the polymeric surface by applying a coating having the desired properties. Introduction of a hydrophilic coating to the hydrophobic surface of a polymer material would make these materials suitable for applications that require biocompatibility, compatibility with hydrophilic reagents, reduced electrostatic charge, reduced friction, improved barrier properties and improved absorption of water-based dyes and inks. However, due to their very different properties, the application of a hydrophilic coating to a hydrophobic substrate typically results in a surface coating with poor adhesion and durability. Furthermore, the currently known methodologies for introducing a hydrophilic coating to a hydrophobic surface typically require immersion of a hydrophobic surface into a solution containing the liquefied hydrophilic composition followed by drying. This methodology from a manufacturing standpoint is both time consuming and costly.
[0004] The application of a hydrophilic coating to a hydrophobic surface may present other drawbacks. The hydrophilic coating is wettable and in some instances, such coatings when subjected to water for extended time periods and rubbed may no longer adhere to the substrate surface. Furthermore, there are many applications for which the water-resistant nature of a hydrophilic surface is desirable.
[0005] Given the foregoing problems it would be desirable to develop a hydrophilic coating for hydrophobic substrates that exhibits a high degree of adhesion. Likewise, it would be desirable to develop a hydrophilic coating for hydrophobic substrates that is water resistant. Furthermore, there also exists a need for an improved methodology for the application of a hydrophilic coating to a hydrophobic surface.
BRIEF SUMMARY OF SOME OF THE PREFERRED EMBODIMENTS [0006] hi an embodiment, a hydrophilic coating composition is disclosed comprising a hydrophilic base material, an adhesion promoter and a surfactant.
[0007] In an embodiment, a water-resistant hydrophilic coating composition is disclosed comprising a hydrophilic base material, an adhesion promoter, a surfactant and a crosslinking agent.
[0008] In an embodiment, a method of applying a hydrophilic coating to a hydrophobic surface is disclosed comprising: preparing a hydrophilic coating, heating the hydrophilic coating and spraying the hydrophilic coating on the hydrophobic surface. [0009] hi an embodiment, a method of preparing a hydrophilic coating is disclosed comprising: preparing a solution of hydrophilic base material, heating the solution of hydrophilic base material and mixing at least a portion of the heated hydrophilic base material solution with an adhesion promoter and a surfactant.
[0010] hi an embodiment, a method of applying the water-resistant hydrophilic coating is disclosed comprising preparing a water-resistant hydrophilic coating, spraying the water- resistant hydrophilic coating on the hydrophobic surface and heating the coated surface. [0011] hi an embodiment, a method of water-proofing a polysaccharide coating is disclosed comprising crosslinking the starch hydroxyl functionalities.
[0012] The foregoing has outlined rather broadly the features and technical advantages of the present invention in order that the detailed description of the invention that follows may be better understood. Additional features and advantages of the invention will be described hereinafter that form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and the specific embodiments disclosed may be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0013] For a detailed description of the preferred embodiments of the invention, reference will now be made to the accompanying drawings in which: [0014] Figure 1 is a schematic of a pneumatic coating sprayer.
[0015] Figure 2 is a graph of coating adhesion for different hydrophilic coating formulations with 4% starch.
[0016] Figure 3 is a graph of coating adhesion for different hydrophilic coating formulations with 6% starch.
[0017] Figure 4A is a scanning electron micrograph of a substrate with a hydrophilic coating. [0018] Figure 4B is an annotated scanning electron micrograph of Figure 4A.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS [0019] In an embodiment, a hydrophilic coating (HC) comprises a hydrophilic base material, an adhesion promoter, and a surfactant. In an embodiment, a hydrophilic coating (HC) comprises a hydrophilic base material, an adhesion promoter, a surfactant and a crosslinking agent. The hydrophilic base material may be a water-soluble polymer. Without limitation, examples of water-soluble polymers include natural gums such as karaya, tragacanth, ghatti and guar gum; polyvinyl alcohol; polyvinyl pyrrolidone; modified celluloses such as carboxymethyl, hydroxyethyl or hydroxypropyl cellulose; polyacrylic acid; polyethylenimine; or combinations thereof. Alternatively, the water-soluble polymer is a starch, modified starch or starch mixture.
[0020] In an embodiment, the starch may be a non-gelling starch, a waxy starch, an amylose-containmg starch or combinations thereof. As used herein, a non-gelling starch is one that does not form a viscous semi-rigid structure upon absorption of water and heating or during the cooling of said solution. As used herein a waxy starch is one that contains less than about 10% weight/weight (w/w) amylose. As used herein an amylose-containing starch is one having equal to or greater than about 10% amylose. In an embodiment, the amylose content of the starch is less than about 13%, alternatively less than about 12%. Without wishing to be limited by theory, the reduced amylose content in the HC may prevent retrogradation and gel formation thereof. [0021] In some embodiments, the starch is a gelling starch wherein gel formation can be reversed or inhibited. For example, the starch may be an amylose-containing starch containing greater than or equal to about 25% amylose. Starch containing greater than or equal to about 25% amylose when dissolved in water and heated forms a gel when the solution is allowed to cool at room temperature. However, agitating the cooled solution, for example by stirring or shaking, may reverse the gel formation. Alternatively, gel formation in a 25% amylose containing starch solution may be inhibited by rapidly cooling the solution. Methods of rapidly cooling a solution are known to one skilled in the art and include for example transfer of the hot solution to an ice bath.
[0022] Starches suitable for use in the HC include without limitation those isolated from cereal crops such as rice and corn or tuber crops such as cassava and potato. Without limitation, examples of suitable starches include Starch from Rice (S7260) and/or Starch from Cora (S9679) both available from Sigma, Aldrich and Pure Food Grade starch and/or 7350 Waxy starch #1 both available from A. E. Staley. Ih an embodiment, the HC comprises from about 2% w/v to about 8% w/v starch, alternatively from about 4% w/v to about 6% w/v starch. The w/v is defined as the number of grams of a component in a solution divided by the total volume in milliliters of the solution multiplied by 100%. Herein, the term aqueous solution also refers to aqueous dispersions, in which solid materials are intimately dispersed in water so that they do not readily settle or otherwise separate from the aqueous phase. In an embodiment, aqueous solutions of each reagent in the HC are prepared by dissolving the reagent in a suitable volume of water. The concentration of the reagents at this point is termed the initial % w/v. The initial % w/v is calculated by dividing the grams of reagent used by the volume in milliliters of solution (e.g., water) added to produce the aqueous solution. In an embodiment, these aqueous solutions of reagents are used to prepare the HC. For convenience, the HC formulations are based on 100 grams of HC, with a resultant calculation of the grams of aqueous reagent required to prepare the 100 grams of HC. Upon addition of each of the reagents to the HC, the concentration of the reagent is diluted from the initial % w/v to a final % w/v. The final % w/v of each reagent in the HC is determined by multiplying the initial % w/v of each component by the number of grams of component used in preparing the 100 grams of the HC. The sum of the % w/v contribution of each component in the HC is referred to herein as the total solids content. Hereafter, the numerical values given with percentages refer to the final % w/v unless noted otherwise. [0023] In an embodiment, the starch is provided as an aqueous starch solution. This aqueous starch solution may contain a sufficient amount of starch and water to produce an HC with a viscosity suitable for ease of pouring and/or sprayability. In an embodiment, the starch slurry may comprise an initial % w/v of from about 10% to about 20% starch in aqueous solution having a pH of from about 5 to about 7, alternatively about 7.
[0024] hi some embodiments, the water-soluble polymer may be substituted with a water- dispersible or water-reducible polymer to provide a final formulation that is less hydrophilic in nature than the HC formed with a water-soluble polymer. Examples of water-dispersible and water-reducible polymers are known to one skilled in the art. HCs formed using water- dispersible or water-reducible polymers as the hydrophilic base material may result in coatings that are less hydrophilic than those formulated using water-soluble polymers as the hydrophilic base material. However, when compared with the surface of a suitable hydrophobic polymeric substrate, the HCs prepared with water-reducible or water-dispersible polymers may be more hydrophilic than the substrate surface. Thus, application of an HC having a water-dispersible polymer or water-reducible polymer as the hydrophilic base material may provide a coating that enhances desirable surface properties of the substrate to which it is applied. However, for simplicity herein the term HC refers collectively to coatings prepared with water-dispersible, water-reducible or water-soluble polymers.
[0025] In an embodiment, the HC comprises an adhesion promoter. Without wishing to be limited by theory, the adhesion promoter may serve to increase the compatibility between the HC and the hydrophobic substrate through the reduction of interfacial tension. Interfacial tension is defined as the surface free energy that exists between two immiscible liquid phases, such as oil and water, hi an embodiment, the adhesion promoter is any material chemically compatible with the HC that serves to increase the adherence of the HC to the hydrophobic substrate by reducing the interfacial tension. In an embodiment, the adhesion promoter is an epoxy resin present in amounts of from about 0.5% to about 2.0% of the HC. [0026] Without limitation, examples of suitable adhesion promoters include EPI-REZ Resin 3510-W-60 available from Resolution Performance Products and Epoxy 6128W65 from Pacific Epoxy Polymers. In an embodiment, an adhesion promoter for use in the HC (e.g., EPI- REZ Resin 3510-W-60) has about the physical properties given in Table I. Table I
Figure imgf000008_0001
[0027] In an embodiment, the HC comprises a surfactant. Without wishing to be limited by theory, a surfactant in the HC may serve to modify physical properties thereof such as the surface tension, emulsification or cloud point. The surface tension is defined as the free energy between a liquid and air. In an embodiment, the surfactant is any material chemically compatible with the HC that is capable of reducing the surface tension of the HC while increasing adhesion of the HC to the substrate. In an embodiment, the surfactant is a fluorosurfactant. In an alternative embodiment, the surfactant is sodium lauryl sulfate. In an embodiment the HC comprises from about 0.05% to about 0.5% of surfactant, alternatively from about 0.1% to 0.3% of surfactant, alternatively about 0.25% surfactant. Without limitation, examples of suitable surfactants include ZONYL FSA and ZONYL FSP available from Dupont and sodium lauryl sulfate available from Sigma-Aldrich. In an embodiment, a surfactant for use in the HC (e.g., ZONYL FSP) has about the physical properties given in Table IL
Table II
Figure imgf000008_0002
[0028] In an embodiment, the HC comprises a crosslinking agent. Without wishing to be limited by theory, a crosslinking agent in the HC may serve to render the HC water-resistant through a reaction of the starch hydroxyl groups with a functionality of the crosslinking agent. Such reactions would make the starch hydroxyl groups unable to hydrogen bond with water thus resulting in a water-resistant coating. The addition of a crosslinking agent to the HC may also increase the resistance of the starch to swelling and gelatinization. m an embodiment, the crosslinking agent is a melamine resin, alternatively a methylated melamine resin, alternatively a methylated melamine formaldehyde resin, alternatively a methylated high imino melamine resin, alternatively a derivative of hexamethoxymethylmelamine (HMMM) or combinations thereof. In an embodiment, the HC comprises from about 0.5% to about 4% cross-linking agent, alternatively from about 1% to about 3% cross-linking agent, alternatively about 2% cross-linking agent. Without limitation, a representative example of a suitable crosslinking agent is a methylated high imino melamine resin sold as CYMEL 323 by Cytec Industries Inc. hi an embodiment, a crosslinking agent for use in the HC (e.g., CYMEL 323) has about the physical properties given in Table III.
Table IH
Figure imgf000009_0001
M/F/Me refers to the ratio of metholyated melamine to formaldehyde to melamine in the crosslinking agent.
2 The crosslinking agent forms multimers in solution. This value is the approximate amount of HMMM monomer present in solution.
[0029] The HC may optionally comprise a crosslinking agent accelerator (CAA). Such a compound may serve to reduce the reaction time of the crosslinking agent and accelerate the formation of a water-resistant HC. hi an embodiment, the CAA is any agent chemically compatible with the HC and that is able to accelerate the reaction of the crosslinking agent and hydrophilic base material, hi an embodiment, the CAA is a polymer, alternatively an anionic polymer, alternatively a carboxyl-containing polymer, alternatively a carboxylated styrene- butadiene latex or combinations thereof, hi an embodiment, the HC comprises from about 2% to about 4% CAA. Without limitation, a representative example of a suitable CAA is a carboxylated styrene-butadiene latex sold as ROVENE 4009 by Mallard Creek Polymers Inc. In an embodiment, the CAA (e.g., ROVENE 4009) has about the physical properties given in Table IV.
Table IV
Figure imgf000010_0001
cps=centipoises 2 Tg is the glass transition temperature
[0030] The HC may further comprise an effective amount of additives for improving or changing the properties thereof, including without limitation emulsifiers, plasticizers or combinations thereof, hi an embodiment, the HC contains a plasticizer, which may serve to increase the flexibility, durability and shelf life thereof. Alternatively, the HC contains an emulsifier that may prevent separation of the formulation components. Suitable plasticizers and emulsifiers are known to one of ordinary skill in the art. hi an embodiment, the HC may contain a single compound that functions as both a plasticizer and an emulsifier. Without limitation, an example of a plasticizer that also functions as an emulsifier for use in the HC is a nonionic/anionic wax emulsion sold as AQUABEAD 270E by Micro Powders Inc. [0031] Other additives chemically compatible with the formulation may be introduced by one skilled in the art to vary the properties of the HC as needed. By way of example, the HC may be varied to contain antimicrobial agents or dyes if necessary to impart certain physical properties to the hydrophobic substrate.
[0032] hi an embodiment, the HC may comprise from about 4 to about 6% hydrophilic base material, from about 0.5 to about 2% adhesion promoter, from about 0.1 to about 0.25% surfactant and optionally an effective amount of any additional additives with the remainder of the HC being an aqueous carrier fluid, such as water, hi an embodiment, the nongelling starch comprises from about 4% to about 6% solids in the aqueous hydrophilic coating dispersion prior to application.
[0033] For example, based on lOOg of aqueous HC, the total solids content may be from about 6 to about 1O g comprising from about 4 to about 6 grams of nongelling starch, hi an embodiment the HC has a viscosity from about 80 centipoise to about 300 centipoise (cp), alternatively from about 100 cp to about 250 cp, alternatively less than about 200 cp. hi an embodiment, the HC has an adhesion of almost 5A as determined in accordance with a modified version of ASTM D 3359-02, the tape test method to be described in detail later herein.
[0034] In an embodiment, the HC may comprise from about 4% to about 6% hydrophilic base material, from about 0.5% to about 2% adhesion promoter, from about 0.1% to about 0.25% surfactant, from about 1% to about 4% crosslinldng agent, from about 2% to about 4% CAA and optionally an effective amount of any additional additives with the remainder of the HC being an aqueous carrier fluid, such as water. In an embodiment, the HC may have a total solids content from about 6% to about 18%, alternatively from about 6% to about 15%, alternatively from about 6% to about 10% based on the total weight of the HC. In an embodiment, the nongelling starch may comprise from about 4% to about 6% solids in the aqueous HC dispersion prior to application. For example, an aqueous HC having a total solids content of 10 g may comprise from about 4 to about 6 grams of nongelling starch. In an embodiment, the HC has a viscosity from about 80 centipoise to about 300 centipoise (cp), alternatively from about 100 cp to about 250 cp, alternatively less than about 200 cp. [0035] In an embodiment, for preparation of the HC, the hydrophilic base material is heated prior to the addition of other reagents. In an embodiment, the hydrophilic base material is a starch that is provided as a starch slurry. The starch slurry may be heated by any method suitable for heating and maintaining the temperature of the starch slurry. Without wishing to be limited by theory, heating the starch slurry may make the starch completely water-soluble by disrupting the starch granules and breaking the hydrogen bonding. The starch slurry may be heated by the process of jet-cooking. Herein the process of "jet cooking" refers to using a heat transfer device to instantaneously heat a flowing liquid with a hot condensable vapor and hold the heated liquid at a prescribed temperature for a prescribed time. Processes for jet cooking a starch slurry have been disclosed in US Pat. Nos. 3,988,483, 4,232,046 and 6,709,763, each of which is incorporated by reference herein in its entirety. Examples of heat transfer devices suitable for use in jet cooking an aqueous starch slurry are the HYDROHEATER available from Attec, the AWEC 2400 mixing jet cooker available from Q- Jet DSI Inc., and Penick and Ford Laboratory Model Steam Jet cooker.
[0036] Suitable conditions for jet cooking a starch slurry are known to one skilled in the art. The starch slurry may be jet cooked at a temperature from about 130 °C to about 150 0C and a pressure from about 20 psig to about 50 psig with a pumping rate of from about 0.75 to about 2.0 liters per minute. In an embodiment, the jet-cooked aqueous starch slurry is rapidly cooled by placing the slurry on ice. In another embodiment, the jet-cooked aqueous starch slurry is cooled to room temperature and a starch gel forms. The starch gel may then be redispersed in solution by mechanical agitation such as stirring or shaking. In yet another embodiment, the jet-cooked aqueous starch slurry is removed from the heat source and allowed to cool to room temperature.
[0037] After treating the hydrophilic base material (e.g., starch slurry) as described, an appropriate amount of heated hydrophilic base material, adhesion promoter, surfactant, crosslinking agent (if present), CAA (if present), additives (if present) and water may be mixed together to prepare the HC. In some embodiments, the HC may be transferred to a device for application of the coating to a substrate. Alternatively, a single device may be used to prepare the HC and coat the substrate. The HC may be sprayed onto a hydrophobic surface. Sprayers suitable for use in this application are known to one skilled in the art and include pneumatic sprayers or spray guns. Examples of suitable pneumatic sprayers include without limitation, the EGA Manual Touch-Up Gun available from DeVilbiss Corporation or the AJ-401-LH sprayer available from Jacto.
[0038] An embodiment of an apparatus for coating the hydrophobic substrate with the HC is depicted in Figure 1. Referring to Figure 1, a pneumatic sprayer 10 is coupled to container 20, reservoir 30, peristaltic pump 40 and solution container 50. Container 20 may contain a compressed gas such as air that is used to atomize the HC. In an embodiment, the HC is conveyed to reservoir 30 from solution container 50 by peristaltic pump 40 through lines 100 and 101. hi an alternative embodiment, (not depicted), pneumatic sprayer 10 is fed by a local reservoir 30 coupled directly to the sprayer. In another alternative embodiment, (not depicted), the pneumatic sprayer 10 is directly coupled to line 101 and the contents of solution container 50 are fed directly to pneumatic sprayer 10 by peristaltic pump 40 through lines 100 and 101. Alternatively, any device suitable for storing and/or transferring the HC to the pneumatic sprayer 10 may be employed. Alternatively, the HC may be manually transferred to the pneumatic sprayer 10.
[0039] In an embodiment, the HC, the apparatus for coating the hydrophobic substrate, the hydrophobic substrate itself or combinations thereof may be heated prior to and/or during application of the HC to the substrate. For example, the pneumatic sprayer 10 may be used to apply the HC to a hydrophobic substrate in the presence of "hot air". Herein hot air is defined as having an ambient temperature of greater than about 25 0C to less than about 60 °C. The temperature of the air can be elevated through the use of a heating device such as a hot gun, heater, blower or other known device suitable for elevating the ambient air temperature. In an embodiment, the heating device is a hair dryer that may be set on the highest setting. The stream of atomized HC released from the pneumatic sprayer may be heated prior to contacting the substrate by a heating device integrated or in league with the spray device. Alternatively, a heating device external to the spray device may heat the stream of atomized HC. For example, an operator may simultaneously apply an HC to a substrate while directing a stream of hot air towards the HC as it is released from the pneumatic sprayer. Without wishing to be limited by theory, the use of a pneumatic sprayer may allow for the formation of droplets of HC of sufficient size that heating air causes evaporation of a substantial portion of the aqueous carrier fluid prior to the HC contacting a substrate. In another alternative embodiment, the HC may be heated as it is being transferred from a reservoir to the spray device.
[0040] The sprayed HC may form a coating that dries about instantaneously upon contacting the substrate; alternatively the sprayed HC may form a coating that dries in less than about 30 seconds from the time the coating contacts the substrate. Li some embodiments, a drying device may be used to facilitate drying of the HC coating on the substrate. Suitable drying devices are known to one skilled in the art.
[0041] In an embodiment, the HC may be heated during application of the HC to the substrate, following application of the HC to the substrate or both during and following application of the HC to the substrate. The coated substrate may be heated at any temperature and for any time period using any known heating device that is compatible with both the coating and the substrate and activates the crosslinking agent. Herein the term activating the crosslinking agent refers to facilitating the reaction of the crosslinking agent and hydrophilic base material. Alternatively, the coated substrate may be heated in an oven at a temperature of equal to or greater than about 80 °C for from about 12 to about 24 hours, alternatively from about 12 hours to greater than about 24 hours. In some embodiments, the heating of the HC coated substrate is carried out under vacuum. Process conditions such as time, temperature, pressure and combinations thereof may be adjusted to achieve a desired level of crosslinking and resultant performance of the HC. Such process conditions may also vary based on the HC composition, for example based on the presence and amount of a CAA. [0042] The HC may form a monolayer adhesive coating on the substrate. Alternatively, the substrate may be coated repeatedly with the HC to form a multilayer adhesive coating comprising from about 1 to about 24 layers. Hereafter, the term starch adhesive coating (SAC) refers to an HC comprising a starch as the hydrophilic base material that has been applied to a substrate in one or more layers. In embodiments where the SAC further comprises a crosslinker, the term SAC refers to an HC comprising a starch as the hydrophilic base material that has been applied to a substrate in one or more layers but that has not been heated to activate the crosslinker. Hereafter, the term water-resistant starch adhesive coating (WRSAC) refers to an HC comprising a starch as the hydrophilic base material, an adhesion promoter, a surfactant and a crosslinking agent that has been applied to a substrate in one or more layers and has been heated to activate the crosslinker. Herein a water-resistant coating refers to a coating whose adhesion after exposure to water for some time period is equivalent to its adhesion prior to water exposure.
[0043] The adhesion of dried coatings to hydrophobic surfaces such as polyethylene (PE) surfaces was evaluated by a modified version of ASTM testing method D 3359-02. The ASTM method was modified to make it more suitable for the rapid testing of thin, flexible plastic films. Specifically, a 2.3 x 2.6 cm strip of pressure-sensitive adhesive tape (Permacel 99, from K. R. Anderson, Inc., Morgan Hill, CA) was affixed to a flat metal surface to provide a 2.3 x 2.6 cm section of adhesive. This adhesive surface was pressed firmly onto the coated PE film and was then removed by rapidly pulling it straight up at an angle of about 90° to the surface. The surface was then visually examined to estimate the amount of coating removed. Classification of test results, shown in Table V, was the same as for ASTM method D 3359-02.
Table V
Figure imgf000014_0001
[0044] Alternatively, a water-resistant coating is a coating, which passes the Rub Test. Herein the Rub Test refers to a procedure wherein the putative WRSAC is exposed to water for some period and then subjected to manual rubbing. The WRSAC is considered to have passed the Rub Test and is therefore characterized as water resistant if it continues to adhere to the substrate surface after this process.
[0045] The HC may be used to coat a suitable substrate thus providing a hydrophilic layer to a surface. Likewise, the HC containing a crosslinking agent may be used to coat a suitable substrate thus providing a water-resistant hydrophilic layer to a surface. Suitable substrates for the HC include but are not limited to hydrophobic surfaces, alternatively polymeric surfaces, alternatively polyolefin surfaces. The substrate may comprise a homopolymer, copolymer, or blends thereof. Examples of suitable material surfaces that may serve as substrates for the HC include without limitation polyethylene terepthalate; polyethylenes such as high-density polyethylene, low-density polyethylene, linear low-density polyethylene; polypropylene; polyvinyl chloride; polystyrene and combinations thereof.
[0046] Polymer resins having the previously described properties may be formed into articles of manufacture or end use articles using techniques known in the art such as extrusion, blow molding, injection molding, fiber spinning, thermo forming, and casting. For example, a polymer resin may be extruded into a sheet, which is then thermoformed into an end use article such as a container, a cup, a tray, a pallet, a toy, or a component of another product. Examples of other end use articles into which the polymer resins may be formed include pipes, films, bottles, fibers, and so forth. In an embodiment, the substrate is an article of packaging of a consumer product. Additional end use articles would be apparent to those skilled in the art. The surface of such articles may serve as substrates for the HC.
[0047] hi an embodiment, the HC produces a SAC or WRSAC capable of adhering to a hydrophobic substrate with an adhesion strength of from about 3 to about 5, alternatively from about 4 to about 5 as determined in accordance with the modified version of ASTM D 3359-02, previously described, hi an embodiment, the SAC formed upon application of the HC to the substrate has an adhesion that is increased by heating the HC and substrate to activate the crosslinking agent and form a WRSAC. For example, the SAC prior to heating may have an adhesion of 4; however, following heating and the formation of a crosslinked material, the WRSAC may have an adhesion of 5. In an embodiment, the adhesion of the WRSAC is about 20% greater than that of the SAC having an identical composition, hi an embodiment, the WRSAC adheres sufficiently to the substrate surface to resist separation from the surface of the substrate when the surface is manually and/or mechanically bent or flexed, hi an embodiment, the WRSAC adheres sufficiently to the substrate surface to resist separation from the substrate surface when the WRSAC is manually rubbed, soaked in water or combinations thereof. [0048] A SAC and/or a WRSAC may form a uniform hydrophilic coating on the substrate surface with a monolayer thickness of less than about 2 to less than about 5 microns. A SAC and/or a WRSAC formed by the methodology disclosed herein may have starch absorbed from about 0.01 to 0.2 mg per square cm of substrate, alternatively from about 0.035 to about 0.15 mg per square cm of substrate. A SAC and/or a WRSAC of this disclosure may have an opaque (turbid) appearance. [0049] Scanning electron microscopy may be used to characterize the morphology and interfacial rnicrostructure of the SAC. SACs of this disclosure display a uniform coating with the appearance of some micropores and cracking that may not affect the adhesion of the coatings.
[0050] Substrates having HCs of this disclosure may display desirable surface properties such as biocompatibility, compatibility with hydrophilic reagents, reduced electrostatic charge, reduced friction, improved barrier properties, and water resistance. In an embodiment, the hydrophobic substrate having an HC may then display improved absorption of water-based dyes and inks, hi one embodiment, an article surface having an HC may be further processed for example, by the application of an image or colorant directly to the article.
EXAMPLES
[0051] The invention having been generally described, the following examples are given as particular embodiments of the invention and to demonstrate the practice and advantages thereof. It is to be understood that the examples are given by way of illustration and are not intended to limit the specification of the claims in any manner.
FIRST HC EMBODIMENT SHOWN IN EXAMPLES 1-5
EXAMPLE l
[0052] Starch slurries were prepared by jet cooking 700 g of waxy corn starch in 3500 ml of water at 140 0C and 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker. Referring to Table VI, an HC was prepared by mixing the indicated amounts of reagents. The final starch concentration was 6% w/v. All percentages in the examples are of final w/v unless otherwise indicated.
[0053] The HC was stirred for 30 minutes and the viscosity of the HC measured by a Brookfield Viscometer Model LV at 60 RPM. The HC was fed to a pneumatic sprayer (EGA Manual Touch-Up Gun), which was used to coat a plastic surface. During application of the coating, a hot air gun set on the highest setting was aimed at the pneumatic sprayer. The HC dried upon contacting the plastic surface.
Table VI Formulation for Starch Adhesive coating
Figure imgf000016_0001
Figure imgf000017_0001
* In parentheses is given the initial w/v of each reagent. % w/v refers to the final % w/v in the HC.
[0054] The above HC had a total solids content of 9.45% and showed no settling of particles after being kept for 72 hours at 25 0C. The total solids content was varied by adjusting the amount of starch slurry in the HC from 4 to 6%. The extent of adhesion for three HCs with the indicated total solids content were determined in accordance with the modified version of ASTM D3359-02, (the tape test method) as previously described and are given in Table VII.
Table VH Effect of Total Solids Content on Adhesion
Figure imgf000017_0002
[0055] The results demonstrate that HCs having a total solids content in the range of 6.0% to 9.45% produced SACs with an adhesion of almost 5A. However, HCs containing greater than 6% starch concentration were highly viscous and formed coatings with reduced adhesion. Furthermore, HCs with less than 4% starch concentration were too dilute for coating applications.
EXAMPLE 2
[0056] Starch slurries were prepared, viscosity measured and the formulations applied to a substrate as described in Example 1. The formulation was used to coat a 6"x 6"polyethylene surface with up to 24 layers and the adhesion of the coating determined in accordance with the modified version of ASTM D 3359-02 as previously described. Referring to Table VIII, an HC was prepared by mixing the indicated amounts of reagents, hi the presence of all of the indicated reagents, 6.0% starch, 2.0% EPI-REZ Resin 3510-W-60, 1.2% Aquabead 270E and 0.25% Zonyl FSA, the formulation has an adhesion of almost 5A. Table VIII presents the adhesion values in the absence of the indicated reagent with all other reagents remaining the same. Table Vm
Figure imgf000018_0001
In parentheses is given the initial w/v of each reagent.
** % w/v refers to the final % w/v in the HC.
[0057] These results demonstrate the relative contribution of each component of the HC to the adhesive properties of the coating.
EXAMPLE 3
[0058] Starch slurries were prepared, viscosity measured and the formulations applied to the substrate as described in Example 1. In the presence of 6.0% starch, 2.0% EPI-REZ Resin 3510-W-60, 1.2% Aquabead 270E and 0.25% Zonyl FSA, the formulation has an adhesion of almost 5A. Reagents in the formulation were substituted as indicated in Table IX with the remainder of the formulation staying the same. The formulation was used to coat a polyethylene surface and the adhesion of the coating determined in accordance with the modified version of ASTM D 3359-02 tape test method as previously described.
Table IX Effect of Alternative Reagents on Adhesion
Figure imgf000018_0002
Figure imgf000019_0001
[0059] These results demonstrate that starch coatings displaying adhesion in the range of 4A to 5A can be prepared using a suitable combination of starch, adhesion promoter and surfactant. The addition of a plasticizer or emulsifier has no effect on the adhesion but imparts other desirable properties to the formulation such as increased shelf life and preventing the separation of formulation components.
EXAMPLE 4
[0060] Starch slurries were prepared by jet cooking 75Og of starch in 3500ml of water at 140 °C and at 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker. The amylose content for each of the starches used is given in Table X. An HC was prepared by adding either 0.8 or 1.2% Aquabead 270E as indicated, 0.25% Zonyl FSA, water and the indicated amounts of starch slurry and EPI-REZ Resin 3510-W-60. Starch slurries containing a gelling starch were also prepared. For the gelling starch, slurries were prepared by jet cooking 150 g of starch (25% amylose) in 1000ml of water at 140 0C and at 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker. This suspension was divided into two fractions: one fraction was cooled at ambient temperature (1st Fraction) and second fraction was cooled in ice (2nd Fraction). The fraction cooled at room temperature formed gel that could be re-dispersed by stirring or shaking. The fraction cooled in ice stayed in fluid form without forming a gel. An HC was prepared by adding 0.8% Aquabead 270E as indicated, 0.25% Zonyl FSA, water and the indicated amounts of starch slurry containing the 25% amylose containing starch and EPI-REZ Resin 3510-W-60. This formulation is denoted in Table X as 25% amylose cooked once.
[0061] A second formulation was also prepared having the gelling 25% amylose containing starch as the hydrophilic base material, hi this preparation, after the first pass through the jet cooker, the resulting dispersion was cooked a second time under the same conditions. This suspension was divided into two fractions: one fraction was cooled at ambient temperature (1st Fraction) and second fraction was cooled in ice (2nd Fraction). The fraction cooled at room temperature formed gel that could be re-dispersed by stirring or shaking. The fraction cooled in ice stayed in fluid form without forming a gel. This formulation is denoted in Table X as 25% amylose cooked twice. For all formulations, HC was stirred for 30 minutes and the viscosity of the HC measured by a Brookfield Viscometer Model LV at 60 RPM. A sample was then fed to a pneumatic sprayer, the EGA Manual Touch-Up Gun. The formulation was used to coat a polyethylene surface and the adhesion of the coating determined in accordance with the modified version of ASTM D 3359-02 as previously described. Figures 2 and 3 show graphs of the adhesion of the starch coating to a polyethylene substrate as a function of the concentration of EPI-REZ Resin 3510-W-60, the final concentration of starch and the amylose content of the starch. Table X lists the viscosities of the formulations. Final starch concentrations were either 4 or 6% for Figures 2 and 3 respectively, hi the case of the 25% amylose containing starch, formulations having a final concentration of 6% starch were too viscous to spray and thus values for the adhesive coatings were not determined.
Table X Viscosity of HC solutions in cp*
Figure imgf000020_0001
Figure imgf000021_0001
* cp = centipoise
[0062] The result is that the highest levels of adhesion were achieved with final starch concentrations of 4% that maintained a viscosity below 200 cp because of the smaller droplet size due to the decrease in viscosity. EXAMPLE 5
[0063] Starch slurries were prepared by jet cooking 700 g of waxy cornstarch in 3500 ml of water 140 °C and at 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker. An HC containing waxy starch was prepared as described in Example 1 and used to coat a polyethylene substrate. Dried samples were sputter coated with gold-palladium and were examined and photographed with SEM. Scanning electron micoscopy examination was performed with a Jeol 6400V electron microscope at a beam voltage of 15KV. Micrographs were recorded following the application of two layers of the HC, Figure 4A. Figure 4B is the SEM shown in Figure 4A with annotation. The SEMs show the surface morphology of the polyethylene plastic coated with 2 layers of the SAC to be essentially uniform having high areas of homogeneity, as shown in Figure 4B Structure 1 (outlined), with the appearance of micropores, as shown in Figure 4B Structure 2, and cracks, as shown in Figure 4B Structure 3. The micropores may be due to air bubbles formed during coating, and cracks may be caused by localized heating during examination of surfaces by SEM. SECOND HC EMBODIMENT SHOWN IN EXAMPLES 6-9
COMPARATIVE EXAMPLE 6
[0064] Starch slurries were prepared by jet cooking 700 g of waxy cornstarch in 3500 ml of water at 140 0C and 40 psig at a rate of 1 liter/minute in a Penick and Ford Laboratory Model Steam Jet Cooker. Referring to Table XI, an HC was prepared by mixing the indicated amounts of reagents. Hereafter, the remainder of the formulation (i.e. the balance to total 100 grams) is water. The final starch concentration was 6% w/v. All percentages in the examples are of final % w/v unless otherwise indicated.
[0065] The HC was stirred for 30 minutes and the viscosity of the HC measured by a Brookfield Viscometer Model LV at 60 RPM. The HC was fed to a pneumatic sprayer (EGA Manual Touch-Up Gun), which was used to coat a 6" x 6" polyethylene surface. During application of the coating, a hot air gun set on the highest setting was aimed at the pneumatic sprayer in order to facilitate the HC drying upon contacting the plastic surface.
Table XI Formulation for Starch Adhesive coating
Figure imgf000022_0001
Figure imgf000023_0001
* In parentheses is given the initial w/v of each reagent. % refers to the final % w/v in the HC.
[0066] In this and all subsequent examples, % refers to the final % w/v calculated as described herein while in parentheses next to each reagent is given the initial % w/v. The above HC had a total solids content of 9.45% and showed no settling of particles after being kept for 72 hours at 25 °C. The total solids content was varied by adjusting the amount of starch slurry in the HC from 4% to 6%. The extent of adhesion for three HCs with the indicated total solids content were determined in accordance with the modified version of ASTM D 3359-02 previously described, (the tape test method) and are given in Table XII.
Table XII Effect of Total Solids Content on Adhesion
Figure imgf000023_0002
[0067] The results demonstrate that HCs having a total solids content in the range of 6% to 9.45% produced hydrophilic coatings with an adhesion of almost 5 A. However, HCs containing greater than 6% starch concentration were highly viscous and formed hydrophilic coatings with no improvements or increases in adhesion above those observed at the 6% starch concentration. HCs with less than 4% starch concentration were too dilute for coating applications. Additionally, the hydrophilic coatings formed in this experiment were not water- resistant (i.e. they failed the Rub Test).
EXAMPLE 7
[0068] A HC was prepared as described in Comparative Example 6 with addition of the crosslinking agent CYMEL 323 to a final % w/v of 2. The formulation was used to coat a PE substrate as described in Example 6 and the coated substrate was further treated by oven heating at 80 0C in a vacuum oven for 24 hours to activate the crosslinking agent. The resultant WRSAC was hydrophilic, did not separate from the surface when the substrate was manually bent or flexed and did not separate from the surface of the substrate when the coatings were manually rubbed after being soaked in water for 30 min. Formulations were prepared containing different concentrations of the crosslinking agent, CYMEL 323, as indicated in Table XIIIa. Table XHIa
Figure imgf000024_0001
[0069] The viscosity of the HC and the adhesion of the resultant SAC and WRSAC were determined as described in Example 6. In Table XIIIa, the sprays/samples indicate the number of layers of HC applied to the substrate. The adhesion of the SAC (i.e., before heating) is given in the row labeled Adhesion and of the WRSAC (i.e. after heating) is given in the row labeled WR/Adhesion. These results demonstrate the addition of a crosslinking agent to the HC results in the formation of a WRSAC once the sample is heated to activate the crosslinking agent. Furthermore, the adhesion of the HC formulation increases to 5 with heating and the activation of the crosslinking agent.
Table XIIIb
Figure imgf000024_0002
[0070] The activation of the crosslinking agent in the HC occurred when the compositions were heated at temperatures above 60 °C for 24 hours. When samples having the same compositions given in Table XIIIa were heated at 60 °C for 24 hours, the formation of a WRSAC was not observed, Table XIDb.
EXAMPLE 8
[0071] Starch slurries were prepared by jet-cooking amylose-containing starch once as described in Example 6. The hot starch dispersions obtained from jet-cooking amylose- containing starch were further divided into two fractions. One fraction (1st fraction) was cooled at ambient temperature while the second fraction (2nd fraction) was rapidly cooled by placing on ice. The 1st fraction formed a gel upon cooling that could be redispersed by stirring or shaking while the 2nd fraction remained fluid and no gel formation was observed. A second starch slurry was prepared by cooking the amylose-containing starch two times. This twice- cooked slurry was then divided into two fractions and treated as described previously. Each of these fractions of jet-cooked amylose-containing starch was used to prepare HCs containing 4% starch as the hydrophilic base material, the adhesion promoter 2% EPI-REZ Resin 3510-W-60, the combined plasticizer and emulsifier 0.8% AQUABEAD 270E, the fluorosurfactant 0.25% ZONYL FSA and the indicated amounts of crosslinking agent, CYMEL 323. The formulations were used to coat a polyethylene surface, as described in Example 7, and the viscosity of the HC and the adhesion of the resultant SAC and WRSAC were determined as described in Example 6. The compositions, amounts of each reagent, viscosity measurements and adhesion measurements are given in Tables XIVa-XIVd.
Table XIVa
Figure imgf000025_0001
Figure imgf000026_0001
[0072] All formulations using the amylose-containing starch formed a WRSAC whose adhesion increased from about 4 to an adhesion of 5 when the HC coated substrate was heated for 24 hours at 80 °C. These results demonstrate the ability to form a WRSAC with a high- degree of adhesion using a traditionally gelling starch whose gel formation is inhibited by either rapidly cooling the starch or reversed by mechanical agitation.
EXAMPLE 9
[0073] Starch slurries were prepared as described in Example 6. An HC was prepared by adding 6% jet-cooked starch as the hydrophilic base material, the combined plasticizer and emulsifier 1.2% AQUABEAD 270E, the adhesion promoter 2% Epi-Rez Resin 3510-W-60, the fluorosurfactant 0.25% ZONYL FSA, water, the indicated amounts of crosslinking agent, CYMEL 323 and 2%-4% of the CAA ROVENE 4009 (Table XVa-XVc). HC coated substrates were prepared as previously described and heated for the indicated time periods at 80 0C.
Table XVa
Figure imgf000027_0001
Table XVb
Figure imgf000028_0001
Table XVc
Figure imgf000028_0002
Figure imgf000029_0001
[0074] The results demonstrate the formation of a WRSAC when the samples were heated for 12 hours in the presence of the CAA, ROVENE 4009. The addition of either 2% ROVENE 4009 (Table XVa), 3% ROVENE 4009 (Table XVb) or 4% ROVENE 4009 (Table XVc) decreased the reaction time of the crosslinking agent at 80 0C by approximately 50%. [0075] While preferred embodiments of the invention have been shown and described, modifications thereof can be made by one skilled in the art without departing from the spirit and teachings of the invention. The embodiments described herein are exemplary only, and are not intended to be limiting. Many variations and modifications of the invention disclosed herein are possible and are within the scope of the invention. Where numerical ranges or limitations are expressly stated, such express ranges or limitations should be understood to include iterative ranges or limitations of like magnitude falling within the expressly stated ranges or limitations (e.g., from about 1 to about 10 includes, 2, 3, 4, etc.; greater than 0.10 includes 0.11, 0.12, 0.13, etc.). Use of the term "optionally" with respect to any element of a claim is intended to mean that the subject element is required, or alternatively, is not required. Both alternatives are intended to be within the scope of the claim. Use of broader terms such as comprises, includes, having, etc. should be understood to provide support for narrower terms such as consisting of, consisting essentially of, comprised substantially of, etc. [0076] Accordingly, the scope of protection is not limited by the description set out above but is only limited by the claims which follow, that scope including all equivalents of the subject matter of the claims. Each and every claim is incorporated into the specification as an embodiment of the present invention. Thus, the claims are a further description and are an addition to the preferred embodiments of the present invention. The discussion of a reference herein is not an admission that it is prior art to the present invention, especially any reference that may have a publication date after the priority date of this application. The disclosures of all patents, patent applications, and publications cited herein are hereby incorporated by reference, to the extent that they provide exemplary, procedural or other details supplementary to those set forth herein.
^*7ΛS m/noΛ nrwm

Claims

CLAIMSWhat is claimed is:
1. A hydrophilic coating composition comprising: a hydrophilic base material, an adhesion promoter and a surfactant.
2. The composition of claim 1 wherein the hydrophilic base material is a water-soluble polymer, a water-dispersible polymer, a water-reducible polymer or combinations thereof.
3. The composition of claim 2 wherein the water-soluble polymer is a starch, a starch mixture, a modified starch, a gum, polyvinyl pyrrolidone, modified cellulose, polyvinyl alcohol, polyacrylic acid, polyethyleneimine or combinations thereof.
4. The composition of claim 3 wherein the starch, starch mixture or modified starch is nongelling.
5. The composition of claim 4 wherein the nongelling starch contains less than about 12% amylose.
6. The composition of claim 4 wherein the nongelling starch comprises from about 4% to about 6% solids in the aqueous hydrophilic coating dispersion prior to application.
7. The composition of claim 1 wherein the hydrophilic base material is a gelling starch.
8. The composition of claim 7 wherein the gelling starch is inhibited from gel formation by mechanical agitation or rapid cooling.
9. The composition of claim 1 wherein the adhesion promoter is an epoxy resin.
10. The composition of claim 1 wherein the surfactant is a fluorosurfactant, sodium lauryl sulfate, or combinations thereof.
11. The composition of claim 1 further comprising a crosslinking agent.
12. The composition of claim 11 wherein the coating is water-resistant upon application to a substrate.
13. The composition of claim 11 wherein the crosslinking agent is a methylated melamine formaldehyde resin, a methylated high imino melamine resin, a derivative of hexamethoxymethylmelamine or combinations thereof.
14. The composition of claim 11 further comprising a crosslinking agent accelerator.
15. The composition of claim 14 wherein the crosslinking agent accelerator is a polymer, an anionic polymer, a carboxyl-containing polymer, a carboxylated styrene-butadiene latex or combinations thereof.
16. The composition of claim 1 further comprising a plasticizer, an emulsifer or both.
17. The composition of claim 16 wherein the plasticizer, emulsifer or both comprises a nonionic/anionic wax emulsion.
18. The composition of claim 1 having an adhesion of from about 4 to about 5 as determined in accordance with a modified version of ASTM D 3359-02.
19. The composition of claim 1 having a viscosity of from about 80 cps to about 300 cps.
20. A method of applying a hydrophilic coating to a hydrophobic surface comprising: preparing a hydrophilic coating, heating the hydrophilic coating and spraying the hydrophilic coating on the hydrophobic surface.
21. The method of claim 20 wherein the hydrophilic coating is sprayed using a pneumatic sprayer.
22. The method of claim 20 further comprising simultaneously heating and spraying the hydrophilic coating onto the hydrophobic substrate.
23. The method of claim 20 wherein the hydrophilic coating comprises a water-soluble polymer, an adhesion promoter, a surfactant, and optionally a crosslinking agent.
24. The method of claim 23 further comprising a plasticizer, an emulsifier or both.
25. The method of claim 23 wherein the water-soluble polymer is a nongelling starch, a gelling starch, starch mixture, a modified starch or combinations thereof.
26. The method of claim 20 wherein the hydrophobic surface comprises a nonpolar homopolymer, copolymer, polymer blend or combinations thereof.
27. A method of preparing a hydrophilic coating comprising: preparing a solution of 'hydrophilic base material, heating the solution of hydrophilic base material and mixing at least a portion of the heated hydrophilic base material solution with an adhesion promoter and a surfactant.
28. A method of applying the hydrophilic coating to a hydrophobic surface comprising: preparing the hydrophilic coating, spraying the hydrophilic coating on the hydrophobic surface and heating the coated surface.
29. The method of claim 28 wherein the hydrophobic surface comprises a nonpolar homopolymer, copolymer, polymer blend or combinations thereof.
30. The method of claim 28 wherein the hydrophilic composition is sprayed using a pneumatic spray device.
31. The method of claim 28 wherein the coated surface is heated at greater than or equal to about 80 °C.
32. The method of claim 28 wherein the coated surface is heated under vacuum.
33. The method of claim 28 wherein the coated surface is heated for from about 12 hours to about 24 hours.
34. A method of water-proofing a polysaccharide coating comprising crosslinking the starch hydroxyl functionalities.
35. The method of claim 34 wherein waterproofing results in a coating that adheres to a surface following exposure to water and manual rubbing.
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