US20040071885A1 - Dip, spray, and flow coating process for forming coated articles - Google Patents

Dip, spray, and flow coating process for forming coated articles Download PDF

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Publication number
US20040071885A1
US20040071885A1 US10/614,731 US61473103A US2004071885A1 US 20040071885 A1 US20040071885 A1 US 20040071885A1 US 61473103 A US61473103 A US 61473103A US 2004071885 A1 US2004071885 A1 US 2004071885A1
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United States
Prior art keywords
coating
article
preform
curing
drying
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Abandoned
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US10/614,731
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English (en)
Inventor
Gerald Hutchinson
Robert Lee
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Advanced Plastics Technologies Luxembourg SA
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Advanced Plastics Technologies Ltd
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Priority to US10/614,731 priority Critical patent/US20040071885A1/en
Assigned to ADVANCED PLASTICS TECHNOLOGIES, LTD. reassignment ADVANCED PLASTICS TECHNOLOGIES, LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HUTCHINSON, GERALD A., LEE, ROBERT A.
Publication of US20040071885A1 publication Critical patent/US20040071885A1/en
Assigned to ADVANCED PLASTICS TECHNOLOGIES LUXEMBOURG S.A. reassignment ADVANCED PLASTICS TECHNOLOGIES LUXEMBOURG S.A. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ADVANCED PLASTICS TECHNOLOGIES, LIMITED
Priority to US11/772,756 priority patent/US20080032051A1/en
Priority to US11/772,717 priority patent/US20080044604A1/en
Priority to US11/772,737 priority patent/US7717057B2/en
Assigned to HUTCHINSON, SHARON reassignment HUTCHINSON, SHARON REDACTED FINDINGS OF FACT, CONCLUSIONS OF LAW AND PERMANENT ORDERS Assignors: HUTCHINSON, GERALD
Assigned to HUTCHINSON, SHARON reassignment HUTCHINSON, SHARON PATENT ASSIGNMENT AND ORDER IN AID OF EXECUTION ON JUDGMENT Assignors: HUTCHINSON, GERALD
Assigned to ADVANCED PLASTICS TECHNOLOGIES LUXEMBOURG S.A. reassignment ADVANCED PLASTICS TECHNOLOGIES LUXEMBOURG S.A. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HUTCHINSON, SHARON
Abandoned legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00—Processes for applying liquids or other fluent materials
    • B05D1/18—Processes for applying liquids or other fluent materials performed by dipping
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/50—Multilayers
    • B05D7/52—Two layers
    • B05D7/54—No clear coat specified
    • B05D7/544—No clear coat specified the first layer is let to dry at least partially before applying the second layer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
    • B05D7/50—Multilayers
    • B05D7/52—Two layers
    • B05D7/54—No clear coat specified
    • B05D7/546—No clear coat specified each layer being cured, at least partially, separately
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04—Coating
    • C08J7/043—Improving the adhesiveness of the coatings per se, e.g. forming primers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04—Coating
    • C08J7/046—Forming abrasion-resistant coatings; Forming surface-hardening coatings
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
    • C08J7/04—Coating
    • C08J7/048—Forming gas barrier coatings
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2949/00—Indexing scheme relating to blow-moulding
    • B29C2949/30—Preforms or parisons made of several components
    • B29C2949/3064—Preforms or parisons made of several components having at least one components being applied using techniques not covered by B29C2949/3032 - B29C2949/3062
    • B29C2949/3074—Preforms or parisons made of several components having at least one components being applied using techniques not covered by B29C2949/3032 - B29C2949/3062 said at least one component obtained by coating
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2433/00—Characterised 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
    • C08J2433/04—Characterised 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 esters
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S118/00—Coating apparatus
    • Y10S118/04—Curtain coater
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/13—Hollow or container type article [e.g., tube, vase, etc.]
    • Y10T428/1352—Polymer or resin containing [i.e., natural or synthetic]

Definitions

  • This invention relates to methods and apparatus for making coated articles with one or more layers by dip, spray or flow coating.
  • this invention relates to an apparatus and method for making coated containers, preferably comprising polyethylene terephthalate, from coated preforms.
  • Preforms are the products from which containers are made by blow molding.
  • the term “container” is a broad term and is used in its ordinary sense and includes, without limitation, both the preform and bottle container therefrom.
  • a number of plastic and other materials have been used for containers and many are quite suitable.
  • Some products such as carbonated beverages and foodstuffs need a container, which is resistant to the transfer of gases such as carbon dioxide and oxygen. Coating of such containers has been suggested for many years.
  • PET polyethylene terephthalate
  • Biaxially oriented PET containers are strong and have good resistance to creep. Containers of relatively thin wall and light weight can be produced that are capable of withstanding, without undue distortion over the desired shelf life, the pressures exerted by carbonated liquids, particularly beverages such as soft drinks, including colas, and beer.
  • Thin-walled PET containers are permeable to some extent to gases such as carbon dioxide and oxygen and hence permit loss of pressurizing carbon dioxide and ingress of oxygen which may affect the flavor and quality of the bottle contents.
  • gases such as carbon dioxide and oxygen
  • preforms are made by injection molding and then blown into bottles.
  • a shelf life of 12 to 16 weeks can be expected but for smaller bottles, such as half liter, the larger surface-to-volume ratio severely restricts shelf life.
  • Carbonated beverages can be pressured to 4.5 volumes of gas but if this pressure falls below acceptable product specific levels, the product is considered unsatisfactory.
  • barrier layers may be provided by a variety of techniques, including coinjection, chemical vapor deposition, plasma coating with amorphous carbon and/or SiOx, etc., so as to form a laminar coated container.
  • Other examples involve the use of an aqueous dispersion of barrier polymers, and have included dispersions made from vinylidene chloride with acrylonitrile and/or methyl acrylate, optionally containing units derived from other monomers such as methyl methacrylate, vinyl chloride, acrylic acid, or itaconic acid, dispersions made from EVOH and MXD6, etc.
  • the dispersions typically contained surfactants such as sodium alkyl sulphonates.
  • this invention relates to methods and apparatus for making articles, preferably plastic articles, having coatings comprising one or more layers.
  • These layers may comprise thermoplastic materials with good gas-barrier characteristics as well as layers that provide UV protection, scuff resistance, blush resistance, chemical resistance, and/or active properties such as O 2 or CO 2 scavenging.
  • a process for the production of a coated article comprises providing an article, preferably a container or preform comprising polyethylene terephthalate; applying to said article a coating of an aqueous dispersion of a thermoplastic epoxy resin to the article; and curing/drying the coating.
  • the method preferably further comprises a blow molding operation, preferably including stretching the dried coated preform axially and radially, in a blow molding process, at a temperature suitable for orientation, into a bottle-container.
  • thermoplastic epoxy coating is applied by dip, spray, or flow coating of the article and the coating and drying is applied in more than one pass such that the coating properties are increased with each coating layer.
  • the volume of coating deposition may be altered by the article temperature, the article angle, the solution/dispersion temperature, the solution/dispersion viscosity and the number of layers.
  • the multiple coatings of preferred processes result in multiple layers with substantially no distinction between layers, improved coating performance and/or reduction of surface voids and coating holidays.
  • a preferred multiple coating process results in successive layers requiring decreasing amounts of coating material to thoroughly coat the article.
  • the coating and drying process results in enhanced surface tension properties. Furthermore, in preferred processes, the drying process of articles has a repairing effect on surface defects of the finished article. In addition, in preferred processes, the drying/curing process produces articles which exhibit substantially no blushing.
  • thermoplastic resin coated articles comprising: applying an aqueous solution or dispersion of a first thermoplastic resin on the outer surface of an article substrate by dip, spray, or flow coating; withdrawing the article from the dip, spray, or flow coating at a rate so as to form a first coherent film; curing/drying the coated article until the first film is substantially dried so as to form a first coating.
  • the method may further include applying an aqueous solution or dispersion of a second thermoplastic resin on the outer surface of an article substrate by dip, spray, or flow coating; withdrawing the article from the dip, spray, or flow coating at a rate so as to form a second coherent film; curing/drying the coated article until the second film is substantially dried so as to form a second coating.
  • at least one of the first and second thermoplastic resins comprises a thermoplastic epoxy resin, and the first and second resins may be the same or different.
  • a method for dip coating articles comprising the steps of: a) dipping the article into an aqueous coating solution/dispersion contained either in a static vat or in a flow coater with the article rotating to achieve full exposure to the flow; b) withdrawing the article from the static vat or flow coater below the rate at which a coherent film is observed; and c) exposing the article and film to infrared heaters until the film is substantially dried, optionally while cooling the article with air.
  • an apparatus for dip coating articles comprising: an article conveyor that transports the articles through a dip coating system; a tank or vat containing an aqueous solution/dispersion coating material wherein the conveyor draws or dips the articles through the tank or vat; and a curing/drying unit which comprises an oven or chamber in which a curing/drying source is located, wherein the articles are moved through the oven or chamber by the conveyor.
  • the curing/drying unit is optionally coupled with a fan or blower for cooling the article with air.
  • a preferred apparatus may further comprise a second tank or vat of coating material and a second curing/drying unit.
  • the conveyor transports the articles back through the tank and/or the curing/drying unit to provide a second coating on the article.
  • a preferred apparatus may optionally include one or more drip removers positioned between the coating tank or vat and the curing/drying unit, or elsewhere before the curing/drying unit.
  • a method for coating articles comprising the steps of: a) spray coating the article with an aqueous coating solution/dispersion with the article rotating to achieve full exposure to the flow, b) spraying the article at a rate which a coherent film is observed; and c) exposing the article and film to infrared heaters until the film is substantially dried; optionally while cooling the article with air.
  • an apparatus for spray coating articles comprising: an article conveyor that transports the articles through a spray coating system; one or more spray nozzles is in fluid communication with an aqueous solution/dispersion of coating material, such as may be contained in a tank or vat; a coating material collector which receives unused coating material; and a curing/drying unit which comprises an oven or chamber in which a curing/drying source is located, wherein the articles are moved through the oven or chamber by the conveyor.
  • the curing/drying unit is optionally coupled with a fan or blower for cooling the article with air.
  • a preferred apparatus may further comprise a second tank or vat of coating material, a second grouping of one or more spray nozzles, and/or a second curing/drying unit, or, in providing a second coating, one or more components of the first spray coating system may be used.
  • a preferred apparatus may optionally include one or more drip removers positioned between the sprayer and the curing/drying unit, or elsewhere before the curing/drying unit.
  • a method for flow coating articles comprising the steps of: a) flow coating the article with an aqueous coating solution/dispersion with the article rotating to achieve full exposure to the flow, b) withdrawing the article from sheet of the flow coating at a rate which a coherent film is observed; c) exposing the article and film to infrared heaters until the film is substantially dried; and optionally d) cooling the article with air.
  • an apparatus for flow coating articles comprising: an article conveyor that transports the articles through a flow coating system; a tank or vat containing an aqueous solution/dispersion of coating material that is in fluid communication with a fluid guide, wherein the coating material flows off of the fluid guide forming a sheet or falling shower curtain; a coating material collector which receives unused coating material; and a curing/drying unit which comprises an oven or chamber in which a curing/drying source is located, wherein the articles are moved through the oven or chamber by the conveyor.
  • the curing/drying unit is optionally coupled with a fan or blower for cooling the article with air.
  • a preferred apparatus may further comprise a second tank or vat of coating material, a second fluid guide, and/or a second curing/drying unit, or, in providing a second coating, one or more components of the first flow coating system may be used.
  • a preferred apparatus may optionally include one or more drip removers positioned between the coating tank or vat and the curing/drying unit, or elsewhere before the curing/drying unit.
  • a preferred apparatus includes means for entry of the article into the system; dip, spray, or flow coating of the article; optionally removal of excess material; drying or curing; optionally, cooling, during and/or after drying/curing, and ejection from the system.
  • the apparatus is a single integrated processing line that contains multiple stations wherein each station coats the article thereby producing a article with multiple coatings.
  • the system is modular wherein each processing line is self-contained with the ability to handoff to another line, thereby allowing for single or multiple coatings depending on how many modules are connected thereby allowing maximum processing flexibility.
  • a multilayer article comprising: a substrate, and at least one layer comprising thermoplastic epoxy resin coating material disposed on at least a portion of said substrate to form a coated article, wherein the coated article preferably exhibits substantially no blushing or whitening when immersed in water or otherwise directly exposed to water.
  • the coated article preferably exhibits substantially no blushing or whitening when immersed in water or otherwise directly exposed to water.
  • such articles also exhibit substantially no blushing or whitening when exposed to high humidity, including humidity of about 70% or higher.
  • Such exposure or immersion to water or high humidity may occur for several hours or longer, including about 6 hours, 12 hours, 24 hours, 48 hours, and longer and/or may occur at temperatures around room temperature and at reduced temperatures.
  • the coated articles exhibit substantially no blushing or whitening when immersed in or otherwise exposed directly to water at a temperature of about 0° C to 30° C., including about 5° C., 10° C., 15° C., 20° C., 22° C., and 25° C. for about 24 hours.
  • the substrate comprises a polymeric material, preferably a thermoplastic material chosen from the group consisting of polyester, polypropylene, polyethylene, polycarbonate, polyamides and acrylics.
  • the coating is preferably disposed substantially only on the body portion of the preform.
  • one or more additional coating layers are disposed on the article.
  • coating layers preferably there is substantially no distinction between coating layers, and/or one or more additional layers comprise thermoplastic materials.
  • the coating layer(s) may contain one or more of the following characteristics in preferred embodiments: gas-barrier protection, UV protection, scuff resistance, blush resistance, chemical resistance.
  • a multilayer container is produced, preferably a preform or bottle having a body portion and neck portion.
  • the container, preform or bottle comprises a thermoplastic material substrate and one or moore, layers of thermoplastic resin coating material.
  • the thermoplastic substrate material is chosen from the chosen from the group consisting of polyesters, polyolefins, polycarbonates, polyamides and acrylics.
  • the coating layers contain one or more of the following characteristics: gas-barrier protection, UV protection, scuff resistance, blush resistance, chemical resistance.
  • the coating is disposed substantially only on the body portion of the preform.
  • the finished product preferably has substantially no distinction between layers.
  • the coated article or container formed from a coated preform shows substantially no blushing or whitening when exposed to water or high humidity at room temperature or reduced or elevated temperatures (with respect to room temperature) for a period of several hours or longer.
  • the coated article or container exhibits substantially no blushing when immersed in or otherwise exposed to water.
  • the infrared heating is replaced with flame curing, gas heaters, electron beam processing, or UV radiation optionally followed by or combined with cooling with air.
  • FIG. 1 is an uncoated preform as is used as a starting material for preferred embodiments.
  • FIG. 2 is a cross-section of a preferred uncoated preform of the type that is coated in accordance with a preferred embodiment.
  • FIG. 3 is a cross-section of one preferred embodiment of a coated preform.
  • FIG. 4 is an enlargement of a section of the wall portion of a coated preform.
  • FIG. 5 is a cross-section of another embodiment of a coated preform.
  • FIG. 6 is a cross-section of a preferred preform in the cavity of a blow-molding apparatus of a type that may be used to make a preferred coated container of an embodiment of the present invention.
  • FIG. 7 is a coated container prepared in accordance with a blow molding process.
  • FIG. 8 is a cross-section of one preferred embodiment of a coated container having features in accordance with the present invention.
  • FIG. 9 is a three-layer embodiment of a preform.
  • FIG. 10 there is a non-limiting flow diagram that illustrates a preferred process.
  • FIG. 11 is a non-limiting flow diagram of one embodiment of a preferred process wherein the system comprises a single coating unit.
  • FIG. 12 is a non-limiting flow diagram of a preferred process wherein the system comprises multiple coating units in one integrated system.
  • FIG. 13 is a non-limiting flow diagram of a preferred process wherein the system comprises multiple coating units in a modular system.
  • FIG. 14 is a non-limiting top view of one embodiment of a preferred process wherein the system comprises a single flow coating unit.
  • FIG. 15 is a non-limiting front view of one embodiment of a preferred process wherein the system comprises a single flow coating unit.
  • FIG. 16 is a non-limiting cross section view of one embodiment of a preferred process wherein the system comprises a single flow coating unit.
  • FIGS. 17A and 17B depict non-limiting views of one embodiment of a preferred IR drying/curing unit.
  • thermoplastic materials with good gas-barrier characteristics as well as layers or additives that provide UV protection, scuff resistance, blush resistance, chemical resistance, and/or active properties for O 2 and/or CO 2 scavenging.
  • a coated article is a preform of the type used for beverage containers.
  • embodiments of the coated articles of the present invention could take the form of jars, tubes, trays, bottles for holding liquid foods, medical products, or other products sensitive to gas exposure.
  • these embodiments will be described herein primarily as articles or preforms.
  • the articles described herein may be described specifically in relation to a particular substrate, polyethylene terephthalate (PET), but preferred methods are applicable to many other thermoplastics of the polyester type.
  • PET polyethylene terephthalate
  • the term “substrate” is a broad term used in its ordinary sense and includes embodiments wherein “substrate” refers to the material used to form the base article that is coated.
  • suitable article substrates include, but are not limited to, various polymers such as polyesters, polyolefins, including polypropylene and polyethylene, polycarbonate, polyamides, including nylons, or acrylics. These substrate materials may be used alone or in conjunction with each other.
  • More specific substrate examples include, but are not limited to, polyethylene 2,6- and 1,5-naphthalate (PEN), PETG, polytetramethylene 1,2-dioxybenzoate and copolymers of ethylene terephthalate and ethylene isophthalate.
  • PEN polyethylene 2,6- and 1,5-naphthalate
  • PETG PETG
  • polytetramethylene 1,2-dioxybenzoate polytetramethylene 1,2-dioxybenzoate
  • copolymers of ethylene terephthalate and ethylene isophthalate ethylene 2,6- and 1,5-naphthalate
  • PET is used as the polyester substrate which is coated.
  • PET includes, but is not limited to, modified PET as well as PET blended with other materials.
  • One example of a modified PET is “high IPA PET” or IPA-modified PET.
  • high IPA PET refers to PET in which the IPA content is preferably more than about 2% by weight, including about 2-10% IPA by weight.
  • One or more layers of a coating material are employed in preferred methods and processes.
  • the layers may comprise barrier layers, UV protection layers, oxygen scavenging layers, carbon dioxide scavenging layers, and other layers as needed for the particular application.
  • barrier material As used herein, the terms “barrier material,” “barrier resin,” and the like are broad terms and are used in their ordinary sense and refer, without limitation, to materials which, when used to coat articles, preferably adhere well to the article substrate and have a lower permeability to oxygen and carbon dioxide than the article substrate.
  • UV protection and the like are broad terms and are used in their ordinary sense and refer, without limitation, to materials which, when used to coat articles, preferably adhere well to the article substrate and have a higher UV absorption rate than the article substrate.
  • oxygen scavenging and the like are broad terms and are used in their ordinary sense and refer, without limitation, to materials which, when used to coat articles, preferably adhere well to the article substrate and have a higher oxygen absorption rate than the article substrate.
  • carbon dioxide scavenging and the like are broad terms and are used in their ordinary sense and refer, without limitation, to materials which, when used to coat articles, preferably adhere well to the article substrate and have a higher carbon dioxide absorption rate than the article substrate.
  • crosslink As used herein, the terms “crosslink,” “crosslinked,” and the like are broad terms and are used in their ordinary sense and refer, without limitation, to materials and coatings which vary in degree from a very small degree of crosslinking up to and including fully cross linked materials such as a thermoset epoxy. The degree of crosslinking can be adjusted to provide the appropriate degree of chemical or mechanical abuse resistance for the particular circumstances.
  • Preferred methods provide for a coating to be placed on an article, specifically a preform, which is later blown into a bottle. Such methods are, in many instances, preferable to placing coatings on the bottles themselves. Preforms are smaller in size and of a more regular shape than the containers blown therefrom, making it simpler to obtain an even and regular coating. Furthermore, bottles and containers of varying shapes and sizes can be made from preforms of similar size and shape. Thus, the same equipment and processing can be used to coat preforms to form several different types of containers. The blow-molding may take place soon after molding and coating, or preforms may be made and stored for later blow-molding. If the preforms are stored prior to blow-molding, their smaller size allows them to take up less space in storage. Even though it is often times preferable to form containers from coated preforms, containers may also be coated.
  • the blow-molding process presents several challenges.
  • One step where the greatest difficulties arise is during the blow-molding process where the container is formed from the preform.
  • defects such as delamination of the layers, cracking or crazing of the coating, uneven coating thickness, and discontinuous coating or voids can result.
  • suitable coating materials and coating the preforms in a manner that allows for good adhesion between the layers.
  • preferred embodiments comprise suitable coating materials.
  • a suitable coating material When a suitable coating material is used, the coating sticks directly to the preform without any significant delamination and will continue to stick as the preform is blow-molded into a bottles and afterwards.
  • Use of a suitable coating material also helps to decrease the incidence of cosmetic and structural defects which can result from blow-molding containers as described above.
  • One common problem seen in articles formed by coating using coating solutions or dispersions is “blushing” or whitening when the article is immersed in (which includes partial immersion) or exposed directly to water or high humidity (which includes at or above about 70% relative humidity).
  • the articles disclosed herein and the articles produced by methods disclosed herein exhibit minimal or substantially no blushing or whitening when immersed in or otherwise exposed directly to water or high humidity. Such exposure may occur for several hours or longer, including about 6 hours, 12 hours, 24 hours, 48 hours, and longer and/or may occur at temperatures around room temperature and at reduced temperatures, such as would be seen by placing the article in a cooler containing ice or ice water.
  • Exposure may also occur at an elevated temperature, such elevated temperature generally not including temperatures high enough to cause an appreciable softening of the materials which form the container or coating, including temperatures approaching the Tg of the materials.
  • the coated articles exhibit substantially no blushing or whitening when immersed in or otherwise exposed directly to water at a temperature of about 0° C. to 30° C, including about 5° C, 10° C., 15° C., 20° C., 22° C., and 25° C. for about 24 hours.
  • the process used for curing or drying coating layers appears to have an effect on the blush resistance of articles.
  • a preferred uncoated preform 1 is depicted.
  • the preform is preferably made of an FDA approved material such as virgin PET and can be of any of a wide variety of shapes and sizes.
  • the preform shown in FIG. 1 is a 24 gram preform of the type which will form a 16 oz. carbonated beverage bottle, but as will be understood by those skilled in the art, other preform configurations can be used depending upon the desired configuration, characteristics and use of the final article.
  • the uncoated preform 1 may be made by injection molding as is known in the art or by other suitable methods.
  • the uncoated preform 1 has a neck portion 2 and a body portion 4 .
  • the neck portion 2 also called the neck finish, begins at the opening 18 to the interior of the preform 1 and extends to and includes the support ring 6 .
  • the neck 2 is further characterized by the presence of the threads 8 , which provide a way to fasten a cap for the bottle produced from the preform 1 .
  • the body portion 4 is an elongated and cylindrically shaped structure extending down from the neck 2 and culminating in the rounded end cap 10 .
  • the preform thickness 12 will depend upon the overall length of the preform 1 and the wall thickness and overall size of the resulting container. It should be noted that as the terms “neck” and “body” are used herein, in a container that is colloquially called a “longneck” container, the elongate portion just below the support ring, threads, and/or lip where the cap is fastened would be considered part of the “body” of the container and not a part of the “neck”.
  • the coated preform 20 has a neck portion 2 and a body portion 4 as in the uncoated preform 1 in FIGS. 1 and 2.
  • the coating layer 22 is disposed about the entire surface of the body portion 4 , terminating at the bottom of the support ring 6 .
  • a coating layer 22 in the embodiment shown in the figure does not extend to the neck portion 2 , nor is it present on the interior surface 16 of the preform which is preferably made of an FDA approved material such as PET.
  • the coating layer 22 may comprise one layer of a single material, one layer of several materials combined, or several layers of at least two materials.
  • the overall thickness 26 of the preform is equal to the thickness of the initial preform plus the thickness 24 of the coating layer or layers, and is dependent upon the overall size and desired coating thickness of the resulting container.
  • FIG. 4 is an enlargement of a wall section of the preform showing the makeup of the coating layers in one embodiment of a preform.
  • the layer 110 is the substrate layer of the preform while 112 comprises the coating layers of the preform.
  • the outer coating layer 116 comprises one or more layers of material, while 114 comprises the inner coating layer. In preferred embodiments there may be one or more outer coating layers. As shown here, the coated preform has one inner coating layer and two outer coating layers. Not all preforms of FIG. 4 will be of this type.
  • FIG. 5 another embodiment of a coated preform 25 is shown in cross-section.
  • the primary difference between the coated preform 25 and the coated preform 20 in FIG. 3 is that the coating layer 22 is disposed on the support ring 6 of the neck portion 2 as well as the body portion 4 .
  • any coating that is disposed on, especially on the upper surface, or above the support ring 6 is made of an FDA approved material such as PET.
  • the coated preforms and containers can have layers which have a wide variety of relative thicknesses.
  • the thickness of a given layer and of the overall preform or container, whether at a given point or over the entire container, can be chosen to fit a coating process or a particular end use for the container.
  • the coating layer in the preform and container embodiments disclosed herein may comprise a single material, a layer of several materials combined, or several layers of at least two or more materials.
  • a coated preform such as that depicted in FIG. 3, is prepared by a method and apparatus such as those discussed in detail below, it is subjected to a stretch blow-molding process.
  • a coated preform 20 is placed in a mold 28 having a cavity corresponding to the desired container shape.
  • the coated preform is then heated and expanded by stretching and by air forced into the interior of the preform 20 to fill the cavity within the mold 28 , creating a coated container 30 .
  • the blow molding operation normally is restricted to the body portion 4 of the preform with the neck portion 2 including the threads, pilfer ring, and support ring retaining the original configuration as in the preform.
  • FIG. 7 there is disclosed an embodiment of coated container 40 in accordance with a preferred embodiment, such as that which might be made from blow molding the coated preform 20 of FIG. 3.
  • the container 40 has a neck portion 2 and a body portion 4 corresponding to the neck and body portions of the coated preform 20 of FIG. 3.
  • the neck portion 2 is further characterized by the presence of the threads 8 which provide a way to fasten a cap onto the container.
  • the coated container 40 When the coated container 40 is viewed in cross-section, as in FIG. 8, the construction can be seen.
  • the coating 42 covers the exterior of the entire body portion 4 of the container 40 , stopping just below the support ring 6 .
  • the interior surface 50 of the container which is made of an FDA-approved material, preferably PET, remains uncoated so that only the interior surface 50 is in contact with the packaged product such as beverages, foodstuffs, or medicines.
  • a 24 gram preform is blow molded into a 16 ounce bottle with a coating ranging from about 0.05 to about 0.75 grams, including about 0.1 to about 0.2 grams.
  • FIG. 9 there is shown a preferred three-layer preform 76 .
  • This embodiment of coated preform is preferably made by placing two coating layers 80 and 82 on a preform 1 such as that shown in FIG. 1.
  • FIG. 10 there is shown a non-limiting flow diagram that illustrates a preferred process and apparatus.
  • a preferred process and apparatus involves entry of the article into the system 84 , dip, spray, or flow coating of the article 86 , removal of excess material 88 , drying/curing 90 , cooling 92 , and ejection from the system 94 .
  • FIG. 11 there is shown a non-limiting flow diagram of one embodiment of a preferred process wherein the system comprises a single coating unit, A, of the type in FIG. 10 which produces a single coat article.
  • the article enters the system 84 prior to the coating unit and exits the system 94 after leaving the coating unit.
  • FIG. 12 there is shown a non-limiting flow diagram of a preferred process wherein the system comprises a single integrated processing line that contains multiple stations 100 , 101 , 102 wherein each station coats and dries or cures the article thereby producing an article with multiple coatings.
  • the article enters the system 84 prior to the first station 100 and exits the system 94 after the last station 102 .
  • the embodiment described herein illustrates a single integrated processing line with three coating units, it is to be understood that numbers of coating units above or below are also included.
  • each processing line 107 , 108 , 109 is self-contained with the ability to handoff to another line 103 , thereby allowing for single or multiple coatings depending on how many modules are connected thereby allowing maximum flexibility.
  • the article first enters the system at one of several points in the system 84 or 120 .
  • the article can enter 84 and proceed through the first module 107 , then the article may exit the system at 118 or continue to the next module 108 through a hand off mechanism 103 known to those of skill in the art.
  • the article then enters the next module 108 at 120 .
  • the article may then continue on to the next module 109 or exit the system.
  • the number of modules may be varied depending on the production circumstances required. Further the individual coating units 104 105 106 may comprise different coating materials depending on the requirements of a particular production line. The interchangeability of different modules and coating units provides maximum flexibility.
  • FIGS. 14, 15, and 16 there are shown alternate views of non-limiting diagrams of one embodiment of a preferred process.
  • the top view of a system comprising a single flow coater 86 is shown.
  • the preform enters the system 84 and then proceeds to the flow coater 86 wherein the preform 1 passes through the coating material waterfall.
  • the coating material proceeds from the tank or vat 150 through the gap 155 in the tank down the angled fluid guide 160 where it forms a waterfall (not illustrated) as it passes onto the preforms.
  • the gap 155 in the tank may be widened or narrowed to adjust the flow of the material.
  • the material is pumped from the reservoir (not illustrated) into the vat or tank at a rate that maintains the coating material level above that of the gap 155 .
  • this configuration ensures a constant flow of coating material.
  • the excess amount of material also dampens any fluid fluctuations due to the cycling of the pump.
  • the coating material collector (not illustrated) receives any unused coating waterfall and returns the material back to the coating tank or vat.
  • the excess material is then removed from the bottom of the preform 88 .
  • the preform then moves toward the drying/curing unit 90 before being ejected from the system 94 . As shown here, the preforms are allowed to rest before ejection to cool.
  • the collection reservoir and coating material collector preferably empty into the reservoir that feeds the tank or vat so as to allow for reduction of waste from the system.
  • FIG. 17A and 17B there are shown non-limiting views of one embodiment of a preferred IR drying/curing unit 90 .
  • the unit 90 is open.
  • the arrow at the bottom of the unit indicates how the unit would close.
  • On one side of the processing line there is shown a series of ten lamps 200 .
  • Below the preforms there is shown an angled reflector 210 which reflects heat towards the bottom of the preforms for more thorough curing.
  • a semicircular reflector 230 Opposite to the lamps is a semicircular reflector 230 which reflects the IR heat back onto the preforms allowing for a more thorough and efficient cure. Reflectors of other shapes and sizes may also be used.
  • FIG. 17B there is an enlarged section detailing the lamp placement in one embodiment of a preferred IR drying/curing unit 90 .
  • the lamps in this embodiment are adjustable 220 and may be moved closer to or farther away from the preform allowing for maximum drying/curing flexibility.
  • the glass transition temperature (Tg) is a property relating to the transition of a polymer from a glassy form to a plastic form. In a range of temperatures above its Tg, a material will become soft enough to allow it to flow readily when subjected to an external force or pressure, yet not so soft that its viscosity is so low that it acts more like a liquid than a pliable solid.
  • the temperature range above Tg is a preferred temperature range for performing a blow-molding process, as the material is soft enough to flow under the force of the air blown into the preform to fit the mold but not so soft that it breaks up or becomes uneven in texture. Thus, when materials have similar glass transition temperatures, they will have similar preferred blowing temperature ranges, allowing the materials to be processed together without compromising the performance of either material.
  • the preform In the blow-molding process to produce a bottle from a preform, the preform is heated to a temperature slightly above the Tg of the preform material so that when air is forced into the preform's interior, it will be able to flow to fill the mold in which it is placed. If one does not sufficiently heat the preform the preform material will be too hard to flow properly, and would likely crack, craze, or not expand to fill the mold. Conversely, if one heats the preform to a temperature well above the Tg, the material would likely become so soft that it would not be able to hold its shape or it would crystallize and would process improperly.
  • the material which forms a coating layer has a Tg similar to that of the chosen substrate material, it will have a blowing temperature range similar to the substrate.
  • a blowing temperature can be chosen that allows both materials to be processed within their preferred blowing temperature ranges. If the coating were to have a Tg dissimilar to that of PET, it would be difficult, if not impossible, to choose a blowing temperature suitable for both materials.
  • coating materials comprise polymers having a Tg similar to PET (or the chosen substrate material)
  • the coated preform behaves during blow molding substantially as if it were made of one material, expanding smoothly and creating a cosmetically appealing container with an even thickness and uniform coating of the material where it is applied.
  • the glass transition temperature of PET occurs in a window of about 75-85° C., depending upon how the PET has been processed previously. Therefore, the Tg for preferred coating materials to coat PET preferably range from about 55 to about 140° C., more preferably from about 90 to about 110 ° C., including about 60, 65, 70, 80, 95, 100, 105, 115, 120, and 130.
  • the Tg of the coating material is greatly diminished in importance because the need for blow molding is absent.
  • coating materials be amorphous rather than crystalline. This is because materials in an amorphous state are easier to form into bottles and containers by use of a blow molding process than materials in a crystalline state.
  • PET can exist in both crystalline and amorphous forms. However, in certain embodiments of the present invention, it is preferred that the crystallinity of the PET be minimized and the amorphous state maximized in order to create a semicrystalline state which, among other things, aids interlayer adhesion and in the blow molding process.
  • amorphous substrates and/or coatings is not important, and may even be contraindicated.
  • Preferred coating materials may have tensile strength and creep resistance similar to PET or the chosen substrate material. If so, they may act as a structural component of the container, allowing the coating material to displace some of the polyethylene terephthalate in the preform without sacrificing preform performance. Similarity in tensile strength between PET and the coating materials helps the container to have structural integrity while similarity in creep resistance between PET and the coating materials helps the container to retain its shape. Creep resistance relates to the ability of a material to resist changing its shape in response to an applied force. Although certain preferred embodiments may have coatings that provide structural integrity, other preferred embodiments may not.
  • preferred coating materials have an index of refraction similar to that of PET or the chosen substrate material.
  • the preforms and, perhaps more importantly, the containers blown therefrom are optically clear and, thus, cosmetically appealing for use as a beverage container where clarity of the bottle is frequently desired.
  • the two materials have substantially dissimilar refractive indices when they are placed in contact with each other, the resulting combination may have visual distortions and may be cloudy or opaque, depending upon the degree of difference in the refractive indices of the materials.
  • Polyethylene terephthalate has an index of refraction for visible light within the range of about 1.40 to 1.75, depending upon its physical configuration.
  • the refractive index is preferably within the range of about 1.55 to 1.75, and more preferably in the range of 1.55-1.65.
  • the wall of the final product may be characterized as a biaxially-oriented film since it is subject to both hoop and axial stresses in the blow molding operation.
  • Blow molded PET generally exhibits a refractive index within the range of about 1.40 to 1.75, usually about 1.55 to 1.75, depending upon the stretch ratio involved in the blow molding operation.
  • the stretch ratios referred to herein are biaxial stretch ratios resulting from and include the product of the hoop stretch ratio and the axial stretch ratio.
  • the stretch ratio will be about 8.75 (2.5 ⁇ 3.5).
  • the ratio between the values n i and n o is preferably 0.8-1.3, more preferably 1.0-1.2, most preferably 1.0-1.1.
  • the distortion due to refractive index will be at a minimum, because the two indices are identical. As the ratio progressively varies from one, however, the distortion increases progressively.
  • the coating materials comprise thermoplastic epoxy resins (TPEs).
  • TPEs thermoplastic epoxy resins
  • a further preferred embodiment includes “phenoxy” resins which are a subset of thermoplastic epoxy resins. Phenoxy resins, as that term is used herein, include a wide variety of materials including those discussed in WO 99/20462.
  • a further subset of phenoxy resins, and thermoplastic epoxy resins are preferred hydroxy-phenoxyether polymers, of which polyhydroxyaminoether copolymers (PHAE) is a further preferred material. See for example, U.S. Pat. Nos.
  • each Ar individually represents a divalent aromatic moiety, substituted divalent aromatic moiety or heteroaromatic moiety, or a combination of different divalent aromatic moieties, substituted aromatic moieties or heteroaromatic moieties;
  • R is individually hydrogen or a monovalent hydrocarbyl moiety;
  • each Ar 1 is a divalent aromatic moiety or combination of divalent aromatic moieties bearing amide or hydroxymethyl groups;
  • each Ar 2 is the same or different than Ar and is individually a divalent aromatic moiety, substituted aromatic moiety or heteroaromatic moiety or a combination of different divalent aromatic moieties, substituted aromatic moieties or heteroaromatic moieties;
  • R 1 is individually a predominantly hydrocarbylene moiety, such as a divalent aromatic moiety, substituted divalent aromatic moiety, divalent heteroaromatic moiety, divalent alkylene moiety, divalent substituted alkylene moiety or divalent heteroalkylene moiety or a combination of such moieties;
  • R 2 is individually a
  • Y is nil, a covalent bond, or a linking group, wherein suitable linking groups include, for example, an oxygen atom, a sulfur atom, a carbonyl atom, a sulfonyl group, or a methylene group or similar linkage; n is an integer from about 10 to about 1000; x is 0.01 to 1.0; and y is 0 to 0.5.
  • prodominantly hydrocarbylene means a divalent radical that is predominantly hydrocarbon, but which optionally contains a small quantity of a heteroatomic moiety such as oxygen, sulfur, imino, sulfonyl, sulfoxyl, and the like.
  • the hydroxy-functional poly(amide ethers) represented by Formula I are preferably prepared by contacting an N,N′-bis(hydroxyphenylamido)alkane or arene with a diglycidyl ether as described in U.S. Pat. Nos. 5,089,588 and 5,143,998.
  • the poly(hydroxy amide ethers) represented by Formula II are prepared by contacting a bis(hydroxyphenylamido)alkane or arene, or a combination of 2 or more of these compounds, such as N,N′-bis(3-hydroxyphenyl) adipamide or N,N′-bis(3-hydroxyphenyl)glutaramide, with an epihalohydrin as described in U.S. Pat. No. 5,134,218.
  • the amide- and hydroxymethyl-functionalized polyethers represented by Formula III can be prepared, for example, by reacting the diglycidyl ethers, such as the diglycidyl ether of bisphenol A, with a dihydric phenol having pendant amido, N-substituted amido and/or hydroxyalkyl moieties, such as 2,2-bis(4-hydroxyphenyl)acetamide and 3,5-dihydroxybenzamide.
  • diglycidyl ethers such as the diglycidyl ether of bisphenol A
  • a dihydric phenol having pendant amido, N-substituted amido and/or hydroxyalkyl moieties such as 2,2-bis(4-hydroxyphenyl)acetamide and 3,5-dihydroxybenzamide.
  • the hydroxy-functional polyethers represented by Formula IV can be prepared, for example, by allowing a diglycidyl ether or combination of diglycidyl ethers to react with a dihydric phenol or a combination of dihydric phenols using the process described in U.S. Pat. No. 5,164,472.
  • the hydroxy-functional polyethers are obtained by allowing a dihydric phenol or combination of dihydric phenols to react with an epihalohydrin by the process described by Reinking, Barnabeo and Hale in the Journal of Applied Polymer Science, Vol. 7, p. 2135 (1963).
  • the hydroxy-functional poly(ether sulfonamides) represented by Formula V are prepared, for example, by polymerizing an N,N′-dialkyl or N,N′-diaryldisulfonamide with a diglycidyl ether as described in U.S. Pat. No. 5,149,768.
  • the poly(hydroxy ester ethers) represented by Formula VI are prepared by reacting diglycidyl ethers of aliphatic or aromatic diacids, such as diglycidyl terephthalate, or diglycidyl ethers of dihydric phenols with, aliphatic or aromatic diacids such as adipic acid or isophthalic acid. These polyesters are described in U.S. Pat. No. 5,171,820.
  • the hydroxy-phenoxyether polymers represented by Formula VII are prepared, for example, by contacting at least one dinucleophilic monomer with at least one diglycidyl ether of a cardo bisphenol, such as 9,9-bis(4-hydroxyphenyl)fluorene, phenolphthalein, or phenolphthalimidine or a substituted cardo bisphenol, such as a substituted bis(hydroxyphenyl)fluorene, a substituted phenolphthalein or a substituted phenolphthalimidine under conditions sufficient to cause the nucleophilic moieties of the dinucleophilic monomer to react with epoxy moieties to form a polymer backbone containing pendant hydroxy moieties and ether, imino, amino, sulfonamido or ester linkages.
  • a cardo bisphenol such as 9,9-bis(4-hydroxyphenyl)fluorene, phenolphthalein, or phenolphthalimidine
  • a substituted cardo bisphenol such as a substituted bis(hydroxyphen
  • poly(hydroxyamino ethers) (“PHAE” or polyetheramines) represented by Formula VIII are prepared by contacting one or more of the diglycidyl ethers of a dihydric phenol with an amine having two amine hydrogens under conditions sufficient to cause the amine moieties to react with epoxy moieties to form a polymer backbone having amine linkages, ether linkages and pendant hydroxyl moieties.
  • PHAE poly(hydroxyamino ethers)
  • polyetheramines represented by Formula VIII are prepared by contacting one or more of the diglycidyl ethers of a dihydric phenol with an amine having two amine hydrogens under conditions sufficient to cause the amine moieties to react with epoxy moieties to form a polymer backbone having amine linkages, ether linkages and pendant hydroxyl moieties.
  • polyhydroxyaminoether copolymers can be made from resorcinol diglycidyl ether, hydroquinone diglycidyl ether, bis
  • phenoxy thermoplastics commercially available from Phenoxy Associates, Inc., PAPHEN 25068-38-6 as one example, are suitable for use in the present invention.
  • These hydroxy-phenoxyether polymers are the condensation reaction products of a dihydric polynuclear phenol, such as bisphenol A, and an epihalohydrin and have the repeating units represented by Formula IV wherein Ar is an isopropylidene diphenylene moiety.
  • Ar is an isopropylidene diphenylene moiety.
  • preferred TPE including phenoxy and PHAE
  • coating materials form stable aqueous based solutions or dispersions.
  • the coating properties of the solutions/dispersions are not adversely affected by contact with water.
  • Preferred coating materials range from about 10% solids to about 50% solids, including about 15%, 20%, 25%, 30%, 35%, 40% and 45%, and ranges encompassing such percentages.
  • the coating material used dissolves or disperses in polar solvents. These polar solvents include, but are not limited to, water, alcohols, and glycol ethers. See, for example, U.S. Pat. Nos. 6,455,116, 6,180,715, and 5,834,078 which describe some preferred TPE solutions and/or dispersions.
  • thermoplastic epoxy coating material is a polyhydroxyaminoether copolymer (PHAE), represented by Formula VIII, dispersion or solution.
  • PHAE polyhydroxyaminoether copolymer
  • the dispersion or solution when applied to a container or preform, greatly reduces the permeation rate of a variety of gases through the container walls in a predictable and well known manner.
  • One dispersion or latex made thereof comprises 10-30 percent solids.
  • a PHAE solution/dispersion may be prepared by stirring or otherwise agitating the PHAE in a solution of water with an organic acid, preferably acetic or phosphoric acid, but also including lactic, malic, citric, or glycolic acid and/or mixtures thereof.
  • organic acid preferably acetic or phosphoric acid, but also including lactic, malic, citric, or glycolic acid and/or mixtures thereof.
  • These PHAE solution/dispersions also include organic acid salts produced by the reaction of the polyhydroxyaminoethers with these acids.
  • PHAE solutions are examples of suitable TPE solutions.
  • One suitable material is BLOX® experimental barrier resin, for example XU-19061.00 made with phosphoric acid manufactured by Dow Chemical Corporation. This particular PHAE dispersion is said to have the following typical characteristics: 30% percent solids, a specific gravity of 1.30, a pH of 4, a viscosity of 24 centipoise (Brookfield, 60 rpm, LVI, 22° C.), and a particle size of between 1,400 and 1,800 angstroms.
  • Other suitable materials include BLOX® 599-29 resins based on resorcinol have also provided superior results as a barrier material.
  • This particular dispersion is said to have the following typical characteristics: 30% percent solids, a specific gravity of 1.2, a pH of 4.0, a viscosity of 20 centipoise (Brookfield, 60 rpm, LVI, 22° C.), and a particle size of between 1500 and 2000 angstroms.
  • Other variations of the polyhydroxyaminoether chemistry may prove useful such as crystalline versions based on hydroquinone diglycidylethers.
  • Other suitable materials include polyhydroxyaminoether solutions by Imperial Chemical Industries (“ICI,” Ohio, USA) more specifically coded EXP12468 and EXP12468-4B including cross-linked materials which exhibit high chemical resistance, low blushing and low surface tension. Other suitable solutions are disclosed in U.S.
  • BLOX® 5000 resin that is a proprietary material available from ICI, which comprises ICI-coded components PXR-15700, E6039, and F3473, which exhibits good cross-linking, chemical resistance and does not exhibit excessive foaming.
  • Other suitable materials include BLOX® 5000 resin dispersion intermediate, BLOX® XUR 588-29, BLOX® 0000 and 4000 series resins.
  • the solvents used to dissolve these materials include, but are not limited to, polar solvents such as alcohols, water, glycol ethers or blends thereof.
  • thermoplastic epoxies are soluble in aqueous acid.
  • a polymer solution/dispersion may be prepared by stirring or otherwise agitating the thermoplastic epoxy in a solution of water with an organic acid, preferably acetic or phosphoric acid, but also including lactic, malic, citric, or glycolic acid and/or mixtures thereof.
  • the acid concentration in the polymer solution is preferably in the range of about 5% -20%, including about 5% -10% by weight based on total weight. In other preferred embodiments, the acid concentration may be below about 5% or above about 20%; and may vary depending on factors such as the type of polymer and its molecular weight.
  • the amount of dissolved polymer in a preferred embodiment ranges from about 0.1% to about 40%.
  • a uniform and free flowing polymer solution is preferred.
  • a 10% polymer solution is prepared by dissolving the polymer in a 10% acetic acid solution at 90° C. Then while still hot the solution is diluted with 20% distilled water to give an 8% polymer solution. At higher concentrations of polymer, the polymer solution tends to be more viscous.
  • Examples of preferred copolyester coating materials and a process for their preparation is described in U.S. Pat. No. 4,578,295 to Jabarin. They are generally prepared by heating a mixture of at least one reactant selected from isophthalic acid, terephthalic acid and their C 1 to C 4 alkyl esters with 1,3 bis(2-hydroxyethoxy)benzene and ethylene glycol. Optionally, the mixture may further comprise one or more ester-forming dihydroxy hydrocarbon and/or bis(4- ⁇ -hydroxyethoxyphenyl)sulfone.
  • Especially preferred copolyester coating materials are available from Mitsui Petrochemical Ind. Ltd. (Japan) as B-010, B-030 and others of this family.
  • Examples of preferred polyamide coating materials include MXD-6 from Mitsubishi Gas Chemical (Japan).
  • Other preferred polyamide coating materials are blends of polyamide and polyester, including those comprising about 1-10% polyester by weight, where the polyester is preferably PET or a modified PET.
  • the blends may be ordinary blends or they may be compatibilized with an antioxidant or other material. Examples of such materials include those described in U.S. patent application Ser. No. 10/395,899, filed Mar. 21, 2003, which is hereby incorporated by reference in its entirety.
  • Polyamide materials may also be used as substrate materials.
  • PEN polyethylene naphthalate
  • PEN copolyester polyethylene naphthalate
  • PET/PEN blends polyethylene naphthalate (PEN)
  • PEN materials can be purchased from Shell Chemical Company.
  • An advantage of preferred methods disclosed herein are their flexibility allowing for the use of multiple functional additives. Additives known by those of ordinary skill in the art for their ability to provide enhanced CO 2 barriers, O 2 barriers, UV protection, scuff resistance, blush resistance, impact resistance and/or chemical resistance may be used.
  • Preferred additives may be prepared by methods known to those of skill in the art.
  • the additives may be mixed directly with a particular coating solution/dispersion, they may be dissolved/dispersed separately and then added to a particular coating solution/dispersion, or they may be combined with a particular coating prior to addition of the solvent that forms the solution/dispersion.
  • preferred additives may be used alone as a single coating layer.
  • the barrier properties of a coating layer may be enhanced by the addition of different additives.
  • Additives are preferably present in an amount up to about 40% of the coating solution/dispersion, also including up to about 30%, 20%, 10%, 5% and 1% of the coating solution/dispersion.
  • additives are preferably stable in aqueous conditions.
  • derivatives of resorcinal m-dihydroxybenzene
  • Another additive that may be used are nanoparticles or nanoparticular materials. These nanoparticles are tiny particles of materials which enhance the barrier properties of a material by creating a more tortuous path for migrating oxygen or carbon dioxide.
  • One preferred type of nanoparticular material is a microparticular clay-based product available from Southern Clay Products.
  • the UV protection properties of the coating may be enhanced by the addition of different additives.
  • the UV protection coating material used provides UV protection up to about 350 nm or greater, preferably about 370 nm or greater, more preferably about 400 nm or greater.
  • the UV protection material may be used as an additive with layers providing additional functionality or applied separately as a single coat.
  • additives providing enhanced UV protection are present in the coating solution/dispersion from about 1 to 20%, but also including about 3%, 5%, 10%, and 15%.
  • the UV protection material is added in a form that is compatible with aqueous based solutions/dispersions.
  • a preferred UV protection material is Milliken UV390A clear shield.
  • UV390A is an oily liquid for which mixing is aided by first blending the liquid with water, preferably in roughly equal parts by volume. This blend is then added to the TPE solution, for example, BLOX® 599-29, and agitated. The resulting solution contains about 10% UV390A and provides UV protection up to 400 nm when applied to a PET preform. As previously described, in another embodiment the UV390A solution is applied as a single coating.
  • CO 2 scavenging properties can be added to the coating.
  • such properties are achieved by including an active amine which will react with CO 2 forming a high gas barrier salt. This salt will then act as a passive CO 2 barrier.
  • the active amine may be an additive or it may be one or more moieties in the thermoplastic resin material of one or more layers.
  • O 2 scavenging properties can be added to the coating by including O 2 scavengers such as anthroquinone and others known in the art. In other embodiments, these O 2 scavengers may also be used alone as a separate coating. These O 2 scavenging materials must first be activated by UV which can be done prior to the drying/curing process.
  • a top coat is applied to provide chemical resistance to harsher chemicals.
  • these top coats are aqueous based polyesters or acrylics which are optionally partially or fully cross linked.
  • a preferred aqueous based polyester is polyethylene terephthalate, however other polyesters may also be used.
  • a preferred aqueous based acrylic is ICI PXR 14100 Carboxyl Latex.
  • a preferred aqueous based polyester resin is described in U.S. Pat. No. 4,977,191 (Salsman), incorporated herein by reference. More specifically, U.S. Pat. No. 4,977,191 describes an aqueous based polyester resin, comprising a reaction product of 20-50% by weight of waste terephthalate polymer, 10-40% by weight of at least one glycol an 5-25% by weight of at least one oxyalkylated polyol.
  • Another preferred aqueous based polymer is a sulfonated aqueous based polyester resin composition as described in U.S. Pat. No. 5,281,630 (Salsman), herein incorporated by reference. Specifically, U.S. Pat. No. 5,281,630 (Salsman), herein incorporated by reference. Specifically, U.S. Pat. No. 5,281,630 (Salsman), herein incorporated by reference. Specifically, U.S. Pat. No.
  • 5,281,630 describes an aqueous suspension of a sulfonated water-soluble or water dispersible polyester resin comprising a reaction product of 20-50% by weight terephthalate polymer, 10-40% by weight at least one glycol and 5-25% by weight of at least one oxyalkylated polyol to produce a prepolymer resin having hydroxyalkyl functionality where the prepolymer resin is further reacted with about 0.10 mole to about 0.50 mole of alpha, beta-ethylenically unsaturated dicarboxylic acid per 100 g of prepolymer resin and a thus produced resin, terminated by a residue of an alpha, beta-ethylenically unsaturated dicarboxylic acid, is reacted with about 0.5 mole to about 1.5 mole of a sulfite per mole of alpha, beta-ethylenically unsaturated dicarboxylic acid residue to produce a sulfonated-terminated resin.
  • U.S. Pat. No. 5,726,277 (Salsman), incorporated herein by reference.
  • U.S. Pat. No. 5,726,277 describes coating compositions comprising a reaction product of at least 50% by weight of waste terephthalate polymer and a mixture of glycols including an oxyalkylated polyol in the presence of a glycolysis catalyst wherein the reaction product is further reacted with a difunctional, organic acid and wherein the weight ratio of acid to glycols in is the range of6:1 to 1:2.
  • 4,104,222 describes a dispersion of a linear polyester resin obtained by mixing a linear polyester resin with a higher alcohol/ethylene oxide addition type surface-active agent, melting the mixture and dispersing the resulting melt by pouring it into an aqueous solution of an alkali under stirring Specifically, this dispersion is obtained by mixing a linear polyester resin with a surface-active agent of the higher alcohol/ethylene oxide addition type, melting the mixture, and dispersing the resulting melt by pouring it into an aqueous solution of an alkanolamine under stirring at a temperature of 70-95° C., said alkanolamine being selected from the group consisting of monoethanolamine, diethanolamine, triethanolamine, monomethylethanolamine, monoethylethanolamine, diethylethanolamine, propanolamine, butanolamine, pentanolamine, N-phenylethanolamine, and an alkanolamine of glycerin, said alkanolamine being present in the aqueous solution in an amount of 0.2 to
  • U.S. Pat. No. 4,528,321 discloses a dispersion in a water immiscible liquid of water soluble or water swellable polymer particles and which has been made by reverse phase polymerization in the water immiscible liquid and which includes a non-ionic compound selected from C 4-12 alkylene glycol monoethers, their C 1-4 alkanoates, C 6-12 polyakylene glycol monoethers and their C 1-4 alkanoates.
  • the coating materials may be cross-linked to enhance thermal stability of coatings for hot fill applications.
  • Inner layers may comprise low-cross linking materials while outer layers may comprise high crosslinking materials or other suitable combinations.
  • the inner coating on the PET surface may utilize non or low cross-linked material, such as the BLOX® 599-29, and the outer coat may utilize material, such as EXP 12468-4B, capable of cross linking to ensure maximum adhesion to the PET.
  • Suitable additives capable of cross linking may be added to the coating layer.
  • Suitable cross linkers can be chosen depending upon the chemistry and functionality of the resin to which they are added. For example, amine cross linkers may be useful for crosslinking resins comprising epoxide groups.
  • cross linking additives if present, are present in an amount of about 1% to 10% of the coating solution/dispersion, preferably about 1% to 5%, also including 2%, 3%, 4%, 6%, 7%, 8%, and 9%.
  • the coating material solutions or dispersions form foam and/or bubbles which can interfere with the coating process.
  • One way to avoid this interference is to add anti-foam/bubble agents to the coating solution/dispersion.
  • Suitable anti-foam agents include, but are not limited to, nonionic surfactants, alkylene oxide based materials, siloxane based materials, and ionic surfactants.
  • anti-foam agents are present in an amount of about 0.01% to about 0.3% of the coating solution/dispersion, preferably about 0.01% to about 0.2%, but also including about 0.02%, 0.03%, 0.04%, 0.05%, 0.06%, 0.07%, 0.08%, 0.09%, 0.1%, 0.25%, and ranges encompassing these amounts.
  • An advantage of the present invention is the ability to handle many types of additives and coatings in an aqueous based system. This makes the present invention easy to use and economical as compared to other systems. For example, since the present invention is aqueous based, there is no need for expensive systems to handle VOC's used in other systems such as epoxy thermosets. In addition, most of the solvents can contact human skin without irritation allowing for ease of use in manufacturing.
  • preferred articles herein include preforms or containers having one or more coating layers.
  • the coating layer or layers preferably provide some functionality such as barrier protection, UV protection, impact resistance, scuff resistance, blush resistance, chemical resistance, antimicrobial properties, and the like.
  • the layers may be applied as multiple layers, each layer having one or more functional characteristics, or as a single layer containing one or more functional components. The layers are applied sequentially with each coating layer being partially or fully dried/cured prior to the next coating layer being applied.
  • a preferred substrate is a PET preform or container as described above.
  • substrate materials may also be utilized.
  • suitable substrate materials include, but are not limited to, polyesters, polypropylene, polyethylene, polycarbonate, polyamides and acrylics.
  • the inner layer is a primer or base coat having functional properties for enhanced adhesion to PET, O 2 scavenging, UV resistance and passive barrier and the one or more outer coatings provide passive barrier and scuff resistance.
  • inner is taken as being closer to the substrate and outer is taken as closer to the exterior surface of the container. Any layers between inner and outer layers are generally described as “intermediate” or “middle”.
  • multiple coated articles comprise an inner coating layer comprising an O 2 scavenger, an intermediate active UV protection layer, followed by an outer layer of the partially or highly cross-linked material.
  • multiple coated preforms comprise an inner coating layer comprising an O 2 scavenger, an intermediate CO 2 scavenger layer, an intermediate active UV protection layer, followed by an outer layer of partially or highly cross-linked material.
  • an inner coating layer comprising an O 2 scavenger, an intermediate CO 2 scavenger layer, an intermediate active UV protection layer, followed by an outer layer of partially or highly cross-linked material.
  • the final coating and drying of the preform provides scuff resistance to the surface of the preform and finished container in that the solution or dispersion contains diluted or suspended paraffin or wax, slipping agent, polysilane or low molecular weight polyethylene to reduce the surface tension of the container.
  • the preform is preferably coated in a manner that promotes adhesion between the two materials.
  • the discussion which follows is in terms of preforms, such discussion should not be taken as limiting, in that the methods and apparatus described may be applied or adapted for containers and other articles.
  • adherence between coating materials and the preform substrate increases as the surface temperature of the preform increases. Therefore it is preferable to perform coating on a heated preform, although preferred coating materials will adhere to the preform at room temperature.
  • Plastics generally, and PET preforms specifically, have static electricity that results in the preforms attracting dust and getting dirty quickly.
  • the preforms are taken directly from the injection-molding machine and coated, including while still warm. By coating the preforms immediately after they are removed from the injection-molding machine, not only is the dust problem avoided, it is believed that the warm preforms enhance the coating process.
  • the methods also allow for coating of preforms that are stored prior to coating. Preferably, the preforms are substantially clean, however cleaning is not necessary.
  • an automated system is used.
  • a preferred method involves entry of the preform into the system, dip, spray, or flow coating of the preform, optional removal of excess material, drying/curing, cooling, and ejection from the system.
  • the system may also optionally include a recycle step.
  • the apparatus is a single integrated processing line that contains two or more dip, flow, or spray coating units and two or more curing/drying units that produce a preform with multiple coatings.
  • the system comprises one or more coating modules. Each coating module comprises a self-contained processing line with one or more dip, flow, or spray coating units and one or more curing/drying units. Depending on the module configuration, a preform may receive one or more coatings.
  • one configuration may comprise three coating modules wherein the preform is transferred from one module to the next, in another configuration, the same three modules may be in place but the preform is transferred from the first to the third module skipping the second.
  • This ability to switch between different module configurations allows for flexibility.
  • either the modular or the integrated systems may be connected directly to a preform injection-molding machine and/or a blow-molding machine. The injection molding machine prepares preforms for use in the present invention.
  • the coating solution/dispersion is at a suitable temperature and viscosity to deposit about 0.06 to about 0.20 grams of coating material per coating layer on a 24 gram preform, also including about 0.07, 0.08, 0.09, 0.1, 0.11, 0.12, 0.13, 0.14, 0.15, 0.16. 0.17, 0.18, and 0.19 grams per coating layer on a 24 gram preform.
  • Preferred depostion amounts for articles of varying sizes may be scaled according to the increase or decrease in surface area as compared to a 24 gram preform. Accordingly, articles other than 24 gram preforms may fall outside of the ranges stated above. Furthermore, in some embodiments, it may be desired to have a single layer or total coating amount on a 24 gram preform that lies outside of the ranges stated above.
  • the apparatus and methods may also be used for other similarly sized preforms and containers, or may adapted for other sizes of articles as will be evident to those skilled in the art in view of the discussion which follows.
  • preferred coating materials include, TPEs, preferably phenoxy type resins, more preferably PHAEs, including the BLOX resins noted supra.
  • the preforms are first brought into the system.
  • An advantage of one preferred method is that ordinary preforms such as those normally used by those of skill in the art may be used. For example, 24 gram monolayer preforms of the type in common use to make 16 ounce bottles can be used without any alteration prior to entry into the system.
  • the system is connected directly to a preform injection molding machine providing warm preforms to the system.
  • stored preforms are added to the system by methods well known to those skilled in the art including those which load preforms into an apparatus for additional processing.
  • the stored preforms are pre-warmed to about 100° F. to about 130° F., including about 120° F., prior to entry into the system.
  • the stored preforms are preferably clean, although cleaning is not necessary.
  • PET preforms are preferred, however other preform and container substrates can be used.
  • Other suitable article substrates include, but are not limited to, various polymers such as polyesters, polyolefins, including polypropylene and polyethylene, polycarbonate, polyamides, including nylons, or acrylics.
  • a suitable coating material can be prepared and used for either dip, spray, or flow coating.
  • the material preparation is essentially the same for dip, spray, and flow coating.
  • the coating material comprises a solution/dispersion made from one or more solvents into which the resin of the coating material is dissolved and/or suspended.
  • the temperature of the coating solution/dispersion can have a drastic effect on the viscosity of the solution/dispersion. As temperature increases, viscosity decreases and vice versa. In addition, as viscosity increases the rate of material deposition also increases. Therefore temperature can be used as a mechanism to control deposition.
  • the temperature of the solution/dispersion is maintained in a range cool enough to minimize curing of the coating material but warm enough to maintain a suitable viscosity. In one embodiment, the temperature is about 60° F.-80° F., including about 70° F. In some cases, solutions/dispersions that may be too viscous to use in spray or flow coating may be used in dip coating.
  • a solution or dispersion may be used at any temperature wherein it exhibits suitable properties for the application.
  • a temperature control system is used to ensure constant temperature of the coating solution/dispersion during the application process.
  • the addition of water may decrease the viscosity of the solution/dispersion.
  • Other embodiments may also include a water content monitor and/or a viscosity monitor that provides a signal when viscosity falls outside a desired range and/or which automatically adds water or other solvent to achieve viscosity within a desired range.
  • the solution/dispersion is at a suitable temperature and viscosity to deposit about 0.06 to about 0.2 grams per coat on a 24 gram preform, also including about 0.07, 0.08, 0.09, 0.1, 0.11, 0.12, 0.13, 0.14, 0.15, 0.16. 0.17, 0.18, and 0.19 grams per coating layer on a 24 gram preform.
  • Preferred deposition amounts for articles of varying sizes may be scaled according to the increase or decrease in surface area as compared to a 24 gram preform. Accordingly, articles other than 24 gram preforms may fall outside of the ranges stated above. Furthermore, in some embodiments, it may be desired to have a single layer on a 24 gram preform that lies outside of the ranges stated above.
  • coated preforms produced from dip, spray, or flow coating are of the type seen in FIG. 3.
  • the coating 22 is disposed on the body portion 4 of the preform and does not coat the neck portion 2 .
  • the interior of the coated preform 16 is preferably not coated. In a preferred embodiment this is accomplished through the use of a holding mechanism comprising an expandable collet or grip mechanism that is inserted into the preform combined with a housing surrounding the outside of the neck portion of the preform.
  • the collet expands thereby holding the preform in place between the collet and the housing.
  • the housing covers the outside of the neck including the threading, thereby protecting the inside of the preform as well as the neck portion from coating.
  • coated preforms produced from dip, spray, or flow coating produce a finished product with substantially no distinction between layers. Further, in dip and flow coating procedures, it has been found that the amount of coating material deposited on the preform decreases slightly with each successive layer.
  • the coating is applied through a dip coating process.
  • the preforms are dipped into a tank or other suitable container that contains the coating material.
  • the dipping of the preforms into the coating material can be done manually by the use of a retaining rack or the like, or it may be done by a fully automated process.
  • the apparatus shown in FIG. 14 depicts one embodiment of an automated flow coating unit, in certain embodiments utilizing automated dip coating, the position of the flow coater 86 would represent the positioning of the dip coating tank or other suitable container containing the coating material.
  • the preforms are rotating while being dipped into the coating material.
  • the preform preferably rotates at a speed of about 30 -80 RPM, more preferably about 40 RPM, but also including 50, 60, and 70 RPM. This allows for thorough coating of the preform. Other speeds may be used, but preferably not so high as to cause loss of coating material due to centrifugal forces.
  • the preform is preferably dipped for a period of time sufficient to allow for thorough coverage of the preform. Generally, this ranges from about 0.25 to about 5 seconds although times above and below this range are also included. Without wishing to be bound to any theory, it appears that longer residence time does not provide any added coating benefit.
  • the turbidity of the coating material should also be considered. If the speed is too high the coating material may become wavelike and splatter causing coating defects. Another consideration is that many coating material solutions or dispersions form foam and/or bubbles which can interfere with the coating process. To avoid this interference, the dipping speed is preferably chosen to avoid excessive agitation of the coating material. If necessary anti-foam/bubble agents may be added to the coating solution/dispersion.
  • the coating is applied through a spray coating process.
  • the preforms are sprayed with a coating material that is in fluid connection with a tank or other suitable container that contains the coating material.
  • the spraying of the preforms with the coating material can be done manually with the use of a retaining rack or the like, or it may be done by a fully automated process.
  • the apparatus shown in FIG. 14 depicts one embodiment of an automated flow coating unit, in certain embodiments utilizing automated spray coating, the position of the flow coater 86 would represent the positioning of the spray coating apparatus.
  • the preforms are rotating while being sprayed with the coating material.
  • the preform preferably rotates at a speed of about 30 -80 RPM, more preferably about 40 RPM, but also including about 50, 60, and 70 RPM.
  • the preform rotates at least about 360° while proceeding through the coating spray. This allows for thorough coating of the preform.
  • the preform may, however, remain stationary while spray is directed at the preform.
  • the preform is preferably sprayed for a period of time sufficient to allow for thorough coverage of the preform.
  • the amount of time required for spraying depends upon several factors, which may include the spraying rate (volume of spray per unit time), the area encompassed by the spray, and the like.
  • the coating material is contained in a tank or other suitable container in fluid communication with the production line.
  • a closed system is used in which unused coating material is recycled. In one embodiment, this may be accomplished by collecting any unused coating material in a coating material collector which is in fluid communication with the coating material tank.
  • Many coating material solutions or dispersions form foam and/or bubbles which can interfere with the coating process.
  • the coating material is preferably removed from the bottom or middle of the tank. Additionally, it is preferable to decelerate the material flow prior to returning to the coating tank to further reduce foam and/or bubbles. This can be done by means known to those of skill in the art. If necessary anti-foam/bubble agents may be added to the coating solution/dispersion.
  • the properties of the coating material should also be considered. If the speed is too high and/or the nozzle size incorrect, the coating material may splatter causing coating defects. If the speed is too slow or the nozzle size incorrect, the coating material may be applied in a manner thicker than desired. Suitable spray apparatus include those sold by Nordson Corporation (Westlake, Ohio). Another consideration is that many coating material solutions or dispersions form foam and/or bubbles which can interfere with the coating process. To avoid this interference, the spraying speed, nozzle used and fluid connections are preferably chosen to avoid excessive agitation of the coating material. If necessary anti-foam/bubble agents may be added to the coating solution/dispersion.
  • the coating is applied through a flow coating process.
  • the object of flow coating is to provide a sheet of material, similar to a falling shower curtain or waterfall, that the preform passes through for thorough coating.
  • preferred methods of flow coating allow for a short residence time of the preform in the coating material. The preform need only pass through the sheet a period of time sufficient-to coat the surface of the preform. Without wishing to be bound to any theory, it appears that longer residence time does not provide any added coating benefit.
  • FIGS. 14, 15, and 16 there are shown alternate views of non-limiting diagrams of one embodiment of a preferred flow coating process.
  • the top view of a system comprising a single flow coater 86 is shown.
  • the preform enters the system 84 and then proceeds to the flow coater 86 wherein the preform 1 passes through the coating material waterfall (not illustrated).
  • the coating material proceeds from the tank or vat 150 through the gap 155 in the tank down the angled fluid guide 160 where it forms a waterfall as it passes onto the preforms.
  • Other embodiments may have fluid guides that are substantially horizontal.
  • the gap 155 in the tank 150 may be widened or narrowed to adjust the flow of the material.
  • the material is pumped from the reservoir (not illustrated) into the vat or tank 150 at a rate that maintains the coating material level above that of the gap 155 .
  • this configuration ensures a constant flow of coating material.
  • the excess amount of material also dampens any fluid fluctuations due to the cycling of the pump.
  • the preform is preferably rotating while it proceeds through the sheet of coating material.
  • the preform preferably rotates at a speed of about 30 -80 RPM, more preferably about 40 RPM, but also including 50, 60, and 70 RPM.
  • the preform rotates at least about two full rotations or 720° while being proceeding through the sheet of coating material.
  • the preform is rotating and placed at an angle while it proceeds through the coating material sheet.
  • the angle of the preform is preferably acute to the plane of the coating material sheet. This advantageously allows for thorough coating of the preform without coating the neck portion or inside of the preform.
  • the sheet 16 is vertical, or perpendicular to the floor, while it proceeds through the coating material sheet. It has been found that as the coating material sheet comes into contact with the preform the sheet tends to creep up the wall of the preform from the initial point of contact.
  • One of skill in the art can control this creep effect by adjusting parameters such as the flow rate, coating material viscosity, and physical placement of the coating sheet material relative to the preform. For example, as the flow increases the creep effect may also increase and possibly cause the coating material to coat more of the preform than is desirable. As another example, by decreasing the angle of the perform relative to the coating material sheet, coating thickness may be adjusted to retain more material at the center or body of the perform as the angle adjustment decreases the amount of material removed or displaced to the bottom of the preform by gravity. The ability to manipulate this creep effect advantageously allows for thorough coating of the preform without coating the neck portion or inside of the preform.
  • the coating material is contained in a tank or other suitable container in fluid communication with the production line in a closed system. It is preferable to recycle any unused coating material. In one embodiment, this may be accomplished by collecting the returning waterfall flow stream in a coating material collector which is in fluid communication with the coating material tank. Many coating material solutions or dispersions form foam and/or bubbles which can interfere with the coating process. To avoid this interference, the coating material is preferably removed from the bottom or middle of the tank. Additionally, it is preferable to decelerate the material flow prior to returning to the coating tank to further reduce foam and/or bubbles. This can be done by means known to those of skill in the art. If necessary anti-foam/bubble agents may be added to the coating solution/dispersion.
  • the flow rate velocity determines the accuracy of the sheet of material. If the flow rate is too fast or too slow, the material may not accurately coat the preforms. When the flow rate is too fast, the material may splatter and overshoot the production line causing incomplete coating of the preform, waste of the coating material, and increased foam and/or bubble problems. If the flow rate is too slow the coating material may only partially coat the preform.
  • the length and the diameter of the preform to be coated should also be considered when choosing a flow rate.
  • the sheet of material should thoroughly cover the entire preform, therefore flow rate adjustments may be necessary when the length and diameter of preforms are changed.
  • Another factor to consider is the spacing of the preforms on the line. As the preforms are run through the sheet of material a so-called wake effect may be observed. If the next preform passes through the sheet in the wake of the prior preform it may not receive a proper coating. Therefore it is important to monitor the speed and center line of the preforms. The speed of the preforms will be dependant on the throughput of the specific equipment used.
  • Advantageously preferred methods provide such efficient deposition that virtually all of the coating on the preform is utilized (i.e. there is virtually no excess material to remove). However there are situations where it is necessary to remove excess coating material after the preform is coated by dip, spray or flow methods.
  • the rotation speed and gravity will work together to normalize the sheet on the preform and remove any excess material.
  • preforms are allowed to normalize for about 5 to about 15 seconds, more preferably about 10 seconds. If the tank holding the coating material is positioned in a manner that allows the preform to pass over the tank after coating, the rotation of the preform and gravity may cause some excess material to drip off of the preform back into the coating material tank. This allows the excess material to be recycled without any additional effort. If the tank is situated in a manner where the excess material does not drip back into the tank, other suitable means of catching the excess material and returning it to be reused, such as a coating material collector or reservoir in fluid communication with the coating tank or vat, may be employed.
  • a drip remover 88 may be used to remove the excess material. See e.g. FIGS. 14, 15, and 16 .
  • suitable drip removers include one or more of the following: a wiper, brush, sponge roller, air knife or air flow, which may be used alone or in conjunction with each other. Further, any of these methods may be combined with the rotation and gravity method described above. Preferably any excess material removed by these methods is recycled for further use.
  • the coated preform is then dried and cured 90 .
  • the drying and curing process is preferably performed by infrared (IR) heating 90 .
  • IR infrared
  • a 1000 W quartz IR lamp 200 is used as the source.
  • a preferred source is a General Electric Q1500 T3/CL Quartzline Tungsten-Halogen lamp. This particular source and equivalent sources may be purchased commercially from any of a number of sources including General Electric and Phillips.
  • the source may be used at full capacity, or it may be used at partial capacity such as at about 50%, about 65%, about 75% and the like.
  • Preferred embodiments may use a single lamp or a combination of multiple lamps. For example, six IR lamps may be used at 70% capacity.
  • Preferred embodiments may also use lamps whose physical orientation with respect to the preform is adjustable. As shown in FIGS. 17A and 17B, the lamp position 200 may be adjusted 220 to position the lamp closer to or farther away from the preform. For example, in one embodiment with multiple lamps, it may be desirable to move one or more of the lamps located below the bottom of the preform closer to the preform. This advantageously allows for thorough curing of the bottom of the preform.
  • Embodiments with adjustable lamps may also be used with preforms of varying widths. For example, if a preform is wider at the top than at the bottom, the lamps may be positioned closer to the preform at the bottom of the preform to ensure even curing.
  • the lamps are preferably oriented so as to provide relatively even illumination of all surfaces of the coating.
  • reflectors are used in combination with IR lamps to provide thorough curing.
  • lamps 200 are positioned on one side of the processing line while one or more reflectors 210 230 are located on the opposite side of or below the processing line. This advantageously reflects the lamp output back onto the preform allowing for a more thorough cure.
  • an additional reflector 210 is located below the preform to reflect heat from the lamps upwards towards the bottom of the preform. This advantageously allows for thorough curing of the bottom of the preform.
  • various combinations of reflectors may be used depending on the characteristics of the articles and the IR lamps used. More preferably reflectors are used in combination with the adjustable IR lamps described above.
  • FIG. 17 depicts a view of one non-limiting embodiment of a preferred IR drying/curing unit.
  • a series of lamps 200 On one side of the processing line there is shown a series of lamps 200 .
  • an angled reflector 210 which reflects heat towards the bottom of the preforms for more thorough curing.
  • a semicircular reflector 230 Opposite to the lamps is a semicircular reflector 230 which reflects the IR heat back onto the preforms allowing for a more thorough and efficient cure.
  • FIG. 17B is an enlarged section of the lamp which demonstrates an embodiment where the lamp placement is adjustable 220 . The lamps may be moved closer to or farther away from the preform allowing for maximum drying/curing flexibility.
  • thermoplastic epoxy for example PHAE
  • IR heating can reduce blushing and improve chemical resistance.
  • IR heating be combined with forced air.
  • the air used may be hot, cold, or ambient.
  • the combination of IR and air curing provides the unique attributes of superior chemical, blush, and scuff resistance of preferred embodiments. Further, without wishing to be bound to any particular theory, it is believed that the coating's chemical resistance is a function of crosslinking and curing. The more thorough the curing, the greater the chemical resistance.
  • the surface temperature of the preform As it relates to the glass transition temperature (T g ) of the substrate and coating materials.
  • T g glass transition temperature
  • the surface temperature of the coating exceeds the T g of the coating materials without heating the substrate above the substrate T g during the curing/drying process. This provides the desired film formation and/or crosslinking without distorting the preform shape due to overheating the substrate.
  • the preform surface is preferably heated to a temperature above the T g of the coating while keeping the substrate temperature at or below the substrate T g .
  • One way of regulating the drying/curing process to achieve this balance is to combine IR heating and air cooling, although other methods may also be used.
  • An advantage of using air in addition to IR heating is that the air regulates the surface temperature of the preform thereby allowing flexibility in controlling the penetration of the radiant heat. If a particular embodiment requires a slower cure rate or a deeper IR penetration, this can be controlled with air alone, time spent in the IR unit, or the IR lamp frequency. These may be used alone or in combination.
  • the preform rotates while proceeding through the IR heater.
  • the preform preferably rotates at a speed of about 30 -80 RPM, more preferably about 40 RPM. If the rotation speed is too high, the coating will spatter causing uneven coating of the preform. If the rotation speed is too low, the preform dries unevenly. More preferably, the preform rotates at least about 360° while proceeding through the IR heater. This advantageously allows for thorough curing and drying.
  • Electron Beam Processing may be employed in lieu of IR heating or other methods.
  • Electron Beam Processing has not been used for curing of polymers used for and in conjunction with injection molded performs and containers primarily due to its large size and relatively high cost. However recent advances in this technology, are expected to give rise to smaller less expensive machines.
  • EBP accelerators are typically described in terms of their energy and power. For example, for curing and crosslinking of food film coatings, accelerators with energies of 150-500 keV are typically used.
  • EBP polymerization is a process in which several individual groups of molecules combine together to form one large group (polymer). When a substrate or coating is exposed to highly accelerated electrons, a reaction occurs in which the chemical bonds in the material are broken and a new, modified molecular structure is formed. This polymerization causes significant physical changes in the product, and may result in desirable characteristics such as high gloss and abrasion resistance. EBP can be a very efficient way to initiate the polymerization process in many materials.
  • EBP crosslinking is a chemical reaction, which alters and enhances the physical characteristics of the material being treated. It is the process by which an interconnected network of chemical bonds or links develop between large polymer chains to form a stronger molecular structure.
  • EBP may be used to improve thermal, chemical, barrier, impact, wear and other properties of inexpensive commodity thermoplastics.
  • EBP of crosslinkable plastics can yield materials with improved dimensional stability, reduced stress cracking, higher set temperatures, reduced solvent and water permeability and improved thermomechanical properties.
  • crosslinking those that are molecular weight-increasing in nature
  • siissioning those that are molecular weight-reducing in nature
  • radiation resistant polymers those in which no significant change in molecular weight is observed.
  • Certain polymers may undergo a combination of (1) and (2). During irradiation, chain scissioning occurs simultaneously and competitively with crosslinking, the final result being determined by the ratio of the yields of these reactions.
  • Aromatic polystyrene and polycarbonate are relatively resistant to EBP.
  • Aromatic polyamides are considerably responsive to ionizing radiation. After exposure the tensile strength of aromatic polyamides does not improve, but for a blend of aromatic polyamides with linear aliphatic polyamides, an increase in tensile strength is derived together with a substantial decrease in elongation.
  • EBP may be used as an alternative to IR for more precise and rapid curing of TPE coatings applied to preforms and containers.
  • EBP when used in conjunction with dip, spray, or flow coating, EBP may have the potential to provide lower cost, improved speed and/or improved control of crosslinking when compared to IR curing. EBP may also be beneficial in that the changes it brings about occur in solid state as opposed to alternative chemical and thermal reactions carried out with melted polymer.
  • gas heaters UV radiation, and flame may be employed in addition to or in lieu of IR or EPB curing.
  • the drying/curing unit is placed at a sufficient distance or isolated from the coating material tank and/or the flow coating sheet as to avoid unwanted curing of unused coating material.
  • the preform is then cooled.
  • the cooling process combines with the curing process to provide enhanced chemical, blush and scuff resistance. It is believed that this is due to the removal of solvents and volatiles after a single coating and between sequential coatings.
  • the cooling process occurs at ambient temperature. In another embodiment, the cooling process is accelerated by the use of forced ambient or cool air.
  • the surface temperature of the preform is below the T g of the lower of the T g of the preform substrate or coating.
  • some coating materials have a lower T g than the preform substrate material, in this example the preform should be cooled to a temperature below the T g of the coating.
  • the preform substrate has the lower T g the preform should be cooled below the T g of the preform substrate.
  • Cooling time is also affected by where in the process the cooling occurs.
  • multiple coatings are applied to each preform.
  • cooling times may be reduced as elevated preform temperature is believed to enhance the coating process.
  • cooling times vary, they are generally about 5 to 40 seconds for 24 gram preforms with about 0.05 to about 0.75 grams of coating material.
  • the preform once the preform has cooled it will be ejected from the system and prepared for packaging. In another embodiment the preform will be ejected from the coating system and sent to a blow-molding machine for further processing. In yet another embodiment, the coated preform is handed off to another coating module where a further coat or coats are applied. This further system may or may not be connected to further coating modules or a blow molding-machine.
  • bottles made by, or resulting from, a preferred process described above may be easily recycled.
  • the coating can be easily removed from the recovered PET.
  • a polyhydroxyaminoether based coating applied by dip coating and cured by IR heating can be removed in 30 seconds when exposed to an 80° C. aqueous solution with a pH of 12.
  • aqueous solutions with a pH equal to or lower than 4 can be used to remove the coating.
  • Variations in acid salts made from the polyhydroxyaminoethers may change the conditions needed for coating removal.
  • the acid salt resulting from the acetic solution of a polyhydroxyaminoether resin can be removed with the use of an 80° C. aqueous solution at a neutral pH.
  • the recycle methods set forth in U.S. Pat. No. 6,528,546, entitled Recycling of Articles Comprising Hydroxy-phenoxyether Polymers may also be used. The methods disclosed in this application are herein incorporated by reference.
  • a lab scale flow coating system was used to coat 24 gram PET preforms.
  • a system, as illustrated in FIGS. 14 through 16 was used, and comprised a single flow coating unit with an IR curing/drying unit.
  • the preforms were manually loaded onto the processing line.
  • the collets used to hold the 24 gram preforms were spaced 1.5′′ on center from each other. It was found that this distance provided the proper spacing to avoid any wake effect while the preforms passed through the coating waterfall or sheet.
  • the coating material was pumped into a tank using a non-shearing pump. The coating material then flowed out of the tank forming a waterfall or sheet that coated the preforms as they passed through the sheet.
  • the preforms moved along the line at a rate of three inches per second in order to ensure two full rotations while passing through the coating sheet. Once through the sheet the line speed allowed the preforms to drip for approximately 10 seconds before passing over a sponge roller to remove an excess coating material from the bottom of the preform.
  • the preforms then moved into the IR curing/drying unit. Five 1000 W General Electric Q1500 T3/CL Quartzline Tungsten-Halogen lamps at 60% capacity were used as the source. The lamps were positioned at 0.6 inches on the centerline. The preforms remained in the IR curing/drying unit for about 10 seconds. As the preforms moved out of the curing/drying unit they were cooled for about 10 seconds with forced ambient air before being removed from the system.
  • the coating material used in this example was a PHAE dispersion, BLOX® XUR 588-29 (from The Dow Chemical Company), having 30% solids.
  • the average deposition (single layer on a 24 gram preform) was about 97 mg.

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  • Chemical & Material Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Details Of Rigid Or Semi-Rigid Containers (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Coating Apparatus (AREA)
US10/614,731 2002-07-03 2003-07-03 Dip, spray, and flow coating process for forming coated articles Abandoned US20040071885A1 (en)

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US10/614,731 US20040071885A1 (en) 2002-07-03 2003-07-03 Dip, spray, and flow coating process for forming coated articles
US11/772,756 US20080032051A1 (en) 2002-07-03 2007-07-02 Dip, spray, and flow coating process for forming coated articles
US11/772,717 US20080044604A1 (en) 2002-07-03 2007-07-02 Dip, spray, and flow coating process for forming coated articles
US11/772,737 US7717057B2 (en) 2002-07-03 2007-07-02 Dip, spray, and flow coating process for forming coated articles

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US39409202P 2002-07-03 2002-07-03
US42225102P 2002-10-28 2002-10-28
US44171803P 2003-01-21 2003-01-21
US10/614,731 US20040071885A1 (en) 2002-07-03 2003-07-03 Dip, spray, and flow coating process for forming coated articles
WOPCT/US03/22333 2003-07-03
PCT/US2003/022333 WO2004004929A1 (en) 2002-07-03 2003-07-03 Dip, spray, and flow coating process for forming coated articles

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US11/772,737 Division US7717057B2 (en) 2002-07-03 2007-07-02 Dip, spray, and flow coating process for forming coated articles

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US11/772,737 Expired - Fee Related US7717057B2 (en) 2002-07-03 2007-07-02 Dip, spray, and flow coating process for forming coated articles
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US11/772,717 Abandoned US20080044604A1 (en) 2002-07-03 2007-07-02 Dip, spray, and flow coating process for forming coated articles

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Cited By (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030012904A1 (en) * 1997-10-17 2003-01-16 Hutchinson Gerald A. Polyester laminate materials
US20030219555A1 (en) * 1997-10-17 2003-11-27 Hutchinson Gerald A. Coated polyester preforms and articles
US20040151937A1 (en) * 2002-11-08 2004-08-05 Hutchinson Gerald A. Injection mold having a wear resistant portion and a high heat transfer portion
US20050070660A1 (en) * 2003-08-11 2005-03-31 Daniel Bode Curable polymeric water based coating compositions and resulting coatings with barrier properties for gases and coated substrates and containers
US20050136201A1 (en) * 2003-12-22 2005-06-23 Pepsico, Inc. Method of improving the environmental stretch crack resistance of RPET without solid stating
US20050227083A1 (en) * 2004-04-07 2005-10-13 Pepsico, Inc. High Tg coatings
US20060051451A1 (en) * 2004-06-10 2006-03-09 Hutchinson Gerald A Methods and systems for controlling mold temperatures
US20060065992A1 (en) * 2004-04-16 2006-03-30 Hutchinson Gerald A Mono and multi-layer articles and compression methods of making the same
US20060099360A1 (en) * 2004-11-05 2006-05-11 Pepsico, Inc. Dip, spray, and flow coating process for forming coated articles
WO2006060104A1 (en) * 2004-11-05 2006-06-08 Pepsico, Inc., A North Carolina Corporation Catalyzed process for forming coated articles
US20060292323A1 (en) * 2005-04-18 2006-12-28 Hutchinson Gerald A Water-resistant coated articles and methods of making same
US20070031673A1 (en) * 2003-08-11 2007-02-08 Daniel Bode Curable polymeric water based coating compositions and resulting coatings with barrier properties for gases and laminate structures
WO2007027606A1 (en) 2005-08-30 2007-03-08 Advanced Plastics Technologies Luxembourg S.A. Methods and systems for controlling mold temperatures
US20070087131A1 (en) * 2005-10-14 2007-04-19 Hutchinson Gerald A Methods of forming multilayer articles by surface treatment applications
WO2007087470A3 (en) * 2006-01-27 2008-01-10 Gen Patent Llc Improved shock wave treatment device
US20080044605A1 (en) * 2000-09-05 2008-02-21 Advanced Plastics Technology Luxembourg S.A. Multilayer containers and preforms having barrier properties
US20090047531A1 (en) * 2007-08-17 2009-02-19 Ppg Industries Ohio, Inc. Packages having radiation-curable coatings
US20090176031A1 (en) * 2006-05-24 2009-07-09 Alberto Armellin Container coating system and process
US20110056947A1 (en) * 2009-09-07 2011-03-10 Kraft Foods Global Brands Llc Multi-faceted container and reclosable lid for food products
US20110223070A1 (en) * 2010-03-12 2011-09-15 David Offord Container having oxygen scavenging system
US20110223069A1 (en) * 2010-03-12 2011-09-15 David Offord Container having an oxygen scavenging activation system
US20110223068A1 (en) * 2010-03-12 2011-09-15 David Offord Container having an oxygen scavenging indication system
WO2011163562A3 (en) * 2010-06-25 2012-04-19 Amcor Limited Oxygen scavenging system for a container
US20120125353A1 (en) * 2009-06-29 2012-05-24 John Wollin Nicotine delivery system
US20120241406A1 (en) * 2011-03-25 2012-09-27 Beuerle Frederick C Barrier system for wide mouth containers
US20120274002A1 (en) * 2011-04-27 2012-11-01 Canon Kabushiki Kaisha Method for manufacturing seamless belt for electrophotography
US8551589B2 (en) 2004-04-16 2013-10-08 The Concentrate Manufacturing Company Of Ireland Mono and multi-layer articles and extrusion methods of making the same
USD705659S1 (en) * 2007-12-21 2014-05-27 Silgan Plastics Llc Preform for dosing bottle
US8962740B2 (en) 2012-09-10 2015-02-24 Kraft Foods Group Brands Llc Oxygen scavenger system in a polyolefin matrix
US20150158204A1 (en) * 2013-12-10 2015-06-11 Krones Ag Method and apparatus for producing plastic preforms
USD769720S1 (en) 2007-12-21 2016-10-25 Silgan Plastics Llc Preform for dosing bottle
US20170158390A1 (en) * 2015-12-04 2017-06-08 Mead Johnson Nutrition Company Powder dosing closure
US20170340899A1 (en) * 2016-05-25 2017-11-30 Boston Scientific Scimed, Inc. Radioactive stent
JP2020037415A (ja) * 2018-08-31 2020-03-12 株式会社吉野工業所 合成樹脂製容器、合成樹脂製容器の製造方法、及び積層プリフォーム
US20200338590A1 (en) * 2015-09-30 2020-10-29 Suntory Holdings Limited Preform coating device and preform coating method
US20220218570A1 (en) * 2021-01-13 2022-07-14 Lisa Stahl Teether
US20220258919A1 (en) * 2021-02-12 2022-08-18 Plastipak Packaging, Inc. Plastic container with barrier

Families Citing this family (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20070041558A (ko) * 2004-07-09 2007-04-18 어드밴스드 플라스틱스 테크놀로지즈 룩셈부르크 에스.에이. 코팅된 물품 형성을 위한 코팅 방법 및 장치
EP1880480B1 (en) 2005-05-13 2016-02-03 Dspace Pty Ltd Method and system for communicating information in a digital signal
US20070141282A1 (en) 2005-12-20 2007-06-21 Yihua Chang Flexible barrier membranes employing poly (hydroxy amino ethers)
US8440318B2 (en) * 2006-07-05 2013-05-14 The Procter & Gamble Company Water-soluble substrate with resistance to dissolution prior to being immersed in water
US8265990B2 (en) * 2008-05-15 2012-09-11 Utrom Processing Co. L.L.C. Method and system for selecting and delivering media content via the internet
GB0903297D0 (en) * 2009-02-26 2009-04-08 Univ Surrey A method of making a hard latex and a hard latex
GB0918976D0 (en) * 2009-10-29 2009-12-16 Univ Surrey A method of making a patterned dried polymer and a patterned dried polmer
EP2537335B1 (en) 2010-02-19 2019-01-16 InterDigital Madison Patent Holdings Media content spatial navigation
RU2460590C1 (ru) * 2011-09-01 2012-09-10 Государственное научное учреждение Всероссийский научно-исследовательский институт использования техники и нефтепродуктов Российской академии сельскохозяйственных наук (ГНУ ВНИИТиН Россельхозакадемии) Устройство для нагрева защитной смазки при нанесении
EP2808095A4 (en) * 2012-01-23 2016-05-11 Ngk Insulators Ltd DRYING PROCESSING AND COATING FILM DRYING OVEN FOR A COATING FILM MADE ON A PET FILM SURFACE
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US9051441B2 (en) * 2012-03-29 2015-06-09 Xerox Corporation Process for chemical passivation of polymer surfaces
US9389337B1 (en) 2012-10-24 2016-07-12 Chia-Jean Wang Selective coating of a component using a potting process
RU2525493C1 (ru) * 2013-03-04 2014-08-20 Государственное научное учреждение Всероссийский научно-исследовательский институт использования техники и нефтепродуктов Российской академии сельскохозйственных наук (ГНУ ВНИИТиН Россельхозакадемии) Устройство для нагрева защитной смазки при нанесении на сельхозмашины
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US8889222B1 (en) * 2013-12-03 2014-11-18 Advenira Enterprises, Inc. Coating material distribution using simultaneous rotation and vibration
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US9821505B2 (en) * 2015-02-27 2017-11-21 Dr Pepper/Seven Up, Inc. High stretch ratio preforms and related containers and methods
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MX2018012105A (es) * 2016-04-06 2019-03-28 Amcor Rigid Plastics Usa Llc Preforma y recipiente de multicapas.
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KR102028191B1 (ko) * 2017-10-19 2019-11-04 (주)나노피엔씨 폴리우레아가 도포된 보강시트 및 그 제조방법
US11260417B2 (en) 2017-12-25 2022-03-01 Suntory Holdings Limited Preform coating device
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RU188724U1 (ru) * 2018-10-05 2019-04-22 Федеральное государственное бюджетное образовательное учреждение высшего образования "Рязанский государственный агротехнологический университет имени П.А. Костычева" (ФГБОУ ВО РГАТУ) Пистолет для консервации сельскохозяйственной техники
KR102235810B1 (ko) * 2019-01-21 2021-04-06 주식회사 비케이이앤씨 증발기 초발수 코팅 방법
RU2705955C1 (ru) * 2019-04-15 2019-11-12 Федеральное государственное бюджетное научное учреждение "Всероссийский научно-исследовательский институт использования техники и нефтепродуктов в сельском хозяйстве" (ФГБНУ ВНИИТиН) Устройство для нагрева мастики при консервации сельхозмашин
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GB2616831B (en) 2022-03-08 2024-06-05 Diageo Great Britain Ltd A beverage container

Citations (90)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1702043A (en) * 1923-09-15 1929-02-12 Turner Tanning Machinery Co Method and apparatus for applying and treating varnish
US3305528A (en) * 1960-11-30 1967-02-21 Union Carbide Corp Poly (hydroxyethers) and a method for their preparation
US3317471A (en) * 1959-03-12 1967-05-02 Dow Chemical Co Thermoplastic resinous reaction product of a diglycidyl ether and an amino compound
US3395118A (en) * 1962-10-15 1968-07-30 Union Carbide Corp Modified thermoplastic polyhydroxyethers
US3654894A (en) * 1970-05-11 1972-04-11 Integral Process Syst Inc Pastry coating apparatus
US3900286A (en) * 1971-11-19 1975-08-19 Ciba Geigy Ag Dyestuff preparations and processes for the dyeing of synthetic organic material
US3966378A (en) * 1974-05-28 1976-06-29 Valyi Emery I Apparatus for making oriented hollow plastic articles
US4040233A (en) * 1970-09-14 1977-08-09 Valyi Emery I Method of obtaining a filled, fluid barrier resistant plastic container
US4149645A (en) * 1975-07-02 1979-04-17 Valyi Emery I Plastic article and method for making same
US4267143A (en) * 1978-02-13 1981-05-12 Rhone-Poulenc Industries Process for the manufacturing of bioriented hollow bodies
US4370368A (en) * 1980-05-07 1983-01-25 Toyo Seikan Kaisha, Ltd. Plastic bottles and process for preparation thereof
US4381277A (en) * 1980-05-29 1983-04-26 Plm Ab Method for producing containers
US4393106A (en) * 1980-10-31 1983-07-12 Toyo Seikan Kaisha Ltd. Laminated plastic container and process for preparation thereof
US4438254A (en) * 1983-02-28 1984-03-20 The Dow Chemical Company Process for producing epoxy resins
US4461857A (en) * 1982-09-29 1984-07-24 Desoto, Inc. Thermosetting aqueous coating compositions containing epoxy-phosphate dispersions
US4499262A (en) * 1984-03-09 1985-02-12 Eastman Kodak Company Process for the preparation of sulfo-modified polyesters
US4505951A (en) * 1983-07-18 1985-03-19 Owens-Illinois, Inc. Method for making a polyvinylidene chloride coated biaxially oriented polyethylene terephthalate container
US4515836A (en) * 1982-07-16 1985-05-07 Nordson Corporation Process for coating substrates with aqueous polymer dispersions
US4528321A (en) * 1983-04-06 1985-07-09 Allied Colloids Limited Polymer dispersions and their preparation
US4564541A (en) * 1983-02-08 1986-01-14 Toyo Seikan Kaisha, Ltd. Plastic laminate structure and vessel
US4569869A (en) * 1978-11-20 1986-02-11 Yoshino Kogyosho Co., Ltd. Saturated polyester bottle-shaped container with hard coating and method of fabricating the same
US4573429A (en) * 1983-06-03 1986-03-04 Nordson Corporation Process for coating substrates with aqueous polymer dispersions
US4578295A (en) * 1984-07-16 1986-03-25 Owens-Illinois, Inc. High barrier polymer blend and articles prepared therefrom
US4646925A (en) * 1983-09-29 1987-03-03 Toyo Seikan Kaisha, Ltd. Multi-layer preform for draw-blow forming a bottle
US4647648A (en) * 1985-08-26 1987-03-03 The Dow Chemical Company Polyhydroxyethers from hydroxybiphenyls
US4731266A (en) * 1981-06-03 1988-03-15 Rhone-Poulenc, S.A. Water-resistant polyvinyl alcohol film and its application to the preparation of gas-impermeable composite articles
US4741936A (en) * 1983-12-27 1988-05-03 Toyo Seikan Kaisha, Ltd. Laminate preform for a multi-layer polyester bottle
US4809640A (en) * 1985-11-02 1989-03-07 Metal Box Public Limited Company Coating of articles
US4818575A (en) * 1986-02-28 1989-04-04 Toyo Seikan Kaisha, Ltd. Biaxially drawn polyester vessel having resistance to heat distortion and gas barrier properties and process for preparation thereof
US4847129A (en) * 1988-09-16 1989-07-11 Continental Pet Technologies, Inc. Multilayer preform for hot fill containers
US4940616A (en) * 1982-11-15 1990-07-10 Mitsui Petrochemical Industries Multilayered container and method for making
US5006381A (en) * 1988-02-04 1991-04-09 Ppg Industries, Inc. Ungelled polyamine-polyepoxide resins
US5026462A (en) * 1990-03-06 1991-06-25 Ail Corporation Method and apparatus for electrochemical machining of spray holes in fuel injection nozzles
US5079034A (en) * 1988-11-21 1992-01-07 Nippon Shokubai Kagaku Kogyo Co., Ltd. Method for manufacturing a water absorbent composite by applying an aqueous polymerizable solution to a substrate and polymerizing the coating against polymerization inner surfaces
US5089588A (en) * 1990-10-17 1992-02-18 The Dow Chemical Company Hydroxy-functional poly(amide ethers) as thermoplastic barrier resins
US5115075A (en) * 1990-05-08 1992-05-19 The Dow Chemical Company Amide and hydroxymethyl functionalized polyethers as thermoplastic barrier resins
US5134218A (en) * 1991-06-06 1992-07-28 The Dow Chemical Company Hydroxy-functional poly(amide ethers) as thermoplastic barrier resins
US5184472A (en) * 1991-01-08 1993-02-09 Pierre Guilbault Add on heat pump swimming pool heater control
US5184373A (en) * 1990-12-22 1993-02-09 Albert Schulte Sohne Gmbh & Co. Caster with conductors between the tire of its wheel and the carrier of its wheel frame
US5196469A (en) * 1991-03-28 1993-03-23 Mica Corporation Ethylene/vinyl alcohol coatings
US5218075A (en) * 1990-05-08 1993-06-08 The Dow Chemical Company Amide and hydroxymethyl functionalized polyethers as thermoplastic barrier resins
US5275853A (en) * 1990-10-03 1994-01-04 The Dow Chemical Company Hydroxyl functionalized polyetheramines as barrier packaging for oxygen-sensitive materials
US5281630A (en) * 1991-12-18 1994-01-25 The Seydel Companies Sulfonated water-soluble or water-dispersible polyester resin compositions
USRE34537E (en) * 1987-09-23 1994-02-08 E. I. Du Pont De Nemours And Company Plastic composite barrier structures
US5300541A (en) * 1988-02-04 1994-04-05 Ppg Industries, Inc. Polyamine-polyepoxide gas barrier coatings
US5300326A (en) * 1993-01-22 1994-04-05 Ppg Industries, Inc. Method of coating a plastic substrate with an aqueous coating composition for plastic substrates
US5302417A (en) * 1991-02-15 1994-04-12 Kurarav Co., Ltd. Aqueous dispersion and substrate coated with the same
US5314751A (en) * 1990-06-19 1994-05-24 Imperial Chemical Industries Plc Coating process and product
US5328724A (en) * 1993-09-02 1994-07-12 E. I. Du Pont De Nemours And Company Solution coating process for packaging film
US5409983A (en) * 1990-06-15 1995-04-25 Imperial Chemical Industries Plc Refillable bottle of polyethylene terephthalate copolymer and its manufacture
US5509965A (en) * 1992-03-18 1996-04-23 Continental Pet Technologies, Inc. Preform coating apparatus and method
US5637365A (en) * 1994-12-16 1997-06-10 Ppg Industries, Inc. Epoxy-amine barrier coatings with aryloxy or aryloate groups
US5645183A (en) * 1994-07-06 1997-07-08 Plastipak Packaging, Inc. Multi-layer containers
US5646924A (en) * 1993-06-07 1997-07-08 Ricoh Company, Ltd. Recording and simultaneous verifying method of phase-changing type of information recording medium
US5726277A (en) * 1994-02-02 1998-03-10 Seydel Companies, Inc. Adhesive compositions from phthalate polymers and the preparation thereof
US5731094A (en) * 1996-10-22 1998-03-24 The Dow Chemical Company Hydroxy-phenoxyether polyester coextruded laminates
US5753358A (en) * 1994-08-25 1998-05-19 W. L. Gore & Associates, Inc. Adhisive-filler polymer film composite
US5759656A (en) * 1992-07-07 1998-06-02 Continental Pet Technologies, Inc. Method of forming multilayer preform and container with low crystallizing interior layer
US5780128A (en) * 1996-04-15 1998-07-14 Pepsico Inc. Polyethylene preform and container
US6011111A (en) * 1993-10-18 2000-01-04 The Dow Chemical Company Hydroxy-phenoxyether polymer thermoplastic composites
US6068900A (en) * 1996-07-05 2000-05-30 Wella Ag Plastic container having a high resistance to chemical attack and method of making same
US6086991A (en) * 1996-06-12 2000-07-11 Hoechst Trespaphan Gmbh Method of priming poly(ethylene terephthalate) articles for coating
US6180715B1 (en) * 1999-09-03 2001-01-30 The Dow Chemical Company Aqueous solution and dispersion of an acid salt of a polyetheramine
US6184281B1 (en) * 1999-06-21 2001-02-06 The Glidden Company Strippable aqueous emulsion inomeric coating for recyclable plastic containers
US6218013B1 (en) * 1994-06-23 2001-04-17 Cellresin Technologies, Llc Barrier material comprising a thermoplastic and a compatible cyclodextrin derivative
US20020001686A1 (en) * 1998-03-12 2002-01-03 Mitsubishi Gas Chemical Company, Inc Oxygen-absorbing multi-layer laminate, production method thereof and packaging container
US6346596B1 (en) * 2000-07-14 2002-02-12 Valspar Corporation Gas barrier polymer composition
US6350796B1 (en) * 1998-10-28 2002-02-26 Vianova Resins Ag Ionically on nonionically stabilized epoxy adducts as water-dilutable base resins for 2-component isocyanate crosslinkable systems
US6352426B1 (en) * 1998-03-19 2002-03-05 Advanced Plastics Technologies, Ltd. Mold for injection molding multilayer preforms
US20020028870A1 (en) * 2000-05-30 2002-03-07 Amcol International Corporation Layered clay intercalates and exfoliates having a low quartz content
US6372318B1 (en) * 1992-07-07 2002-04-16 Continental Pet Technologies, Inc. Method of forming container with high-crystallinity sidewall and low-crystallinity base
US20020048682A1 (en) * 1998-09-01 2002-04-25 Subramanian Pallatheri M. Multilayer structures of poly(1,3-propylene 2,6 napthalate) and poly (ethylene terephthalate)
US6391408B1 (en) * 1997-10-17 2002-05-21 Advanced Plastics Technologies, Ltd. Coated polyester preforms and method of making same
US20020061371A1 (en) * 1996-03-07 2002-05-23 Steven L. Schmidt Multilayer container resistant to elevated temperatures and pressures, and method of making the same
US6393803B1 (en) * 1998-11-06 2002-05-28 Graham Packaging Company, L.P. Process for coating blow-molded plastic containers
US6403231B1 (en) * 2000-05-12 2002-06-11 Pechiney Emballage Flexible Europe Thermoplastic film structures having improved barrier and mechanical properties
US20020090473A1 (en) * 2000-09-05 2002-07-11 Lee Robert A. Multilayer containers and preforms having barrier properties utilizing recycled material
US6418636B1 (en) * 1999-08-11 2002-07-16 Eisermann Maschinenbau Kg Drier for a lacquering line
US6426135B1 (en) * 1994-01-24 2002-07-30 Sumitomo Chemical Co., Ltd. Resin composition laminate and laminate film
US6515067B2 (en) * 2001-01-16 2003-02-04 Chevron Phillips Chemical Company Lp Oxygen scavenging polymer emulsion suitable as a coating, an adhesive, or a sealant
US20030031814A1 (en) * 2000-04-28 2003-02-13 Hutchinson Gerald A. Bottles and preforms having a crystalline neck
US6524672B1 (en) * 1999-02-12 2003-02-25 Plastipak Packaging, Inc. Multilayer preform and container with co-extruded liner
US6592956B2 (en) * 1999-08-06 2003-07-15 Plastipak Packaging, Inc. Plastic container having a carbon-treated internal surface
US6673874B1 (en) * 1994-12-21 2004-01-06 Imperial Chemical Industries Plc Modified polymers
US6709735B2 (en) * 2001-11-14 2004-03-23 Mitsubishi Polyester Film, Llc Oxygen barrier coating and coated film
US6723431B2 (en) * 2000-01-24 2004-04-20 Exxonmobil Oil Corporation Multilayer metallized polyolefin film
US6863988B2 (en) * 1996-09-23 2005-03-08 Bp Corporation North America Inc. Oxygen scavenging monolayer bottles
US6872802B2 (en) * 2000-11-06 2005-03-29 The Procter & Gamble Company Plastic articles digestible by hot alkaline treatment
US6893730B2 (en) * 2002-09-24 2005-05-17 Honeywell International Inc. Barrier film with reduced dynamic coefficient of friction
US6982119B2 (en) * 2002-04-15 2006-01-03 The Coca-Cola Company Coating composition containing an epoxide additive and structures coated therewith

Family Cites Families (95)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH352934A (de) * 1957-04-15 1961-03-15 Steinemann Ulrich Ag Lackfördereinrichtung an einer Lackaufgiessmaschine
EP0586772B1 (de) * 1992-09-09 1996-01-10 Ciba-Geigy Ag Vorrichtung zur Beschichtung von plattenförmigem Gut, insbesondere von Leiterplatten
GB1455091A (en) * 1974-02-11 1976-11-10 Toyo Boseki Dispersion of linear polyester resin
US4225650A (en) 1975-10-22 1980-09-30 Exxon Research & Engineering Co. Crosslinkable polymer powder and laminate
US4127633A (en) 1976-04-21 1978-11-28 Imperial Chemical Industries Limited Process for fabricating biaxially oriented container of polyethylene terephthalate coated with a copolymer of vinylidene chloride
FR2421928A1 (fr) 1978-02-13 1979-11-02 Rhone Poulenc Ind Composition polymere de revetement et son emploi pour la fabrication d'emballages stratifies
JPS5677143A (en) 1979-11-30 1981-06-25 Yoshino Kogyosho Co Ltd Polyethylene terephthalate resin product
NL8102376A (nl) 1980-05-29 1981-12-16 Plm Ab Werkwijze en inrichting voor het vormen van een houder.
GR76013B (xx) * 1981-05-22 1984-08-03 Akzo Nv
JPS5820263A (ja) 1981-07-28 1983-02-05 Mitsubishi Rayon Co Ltd 合成樹脂成形品の表面硬化処理方法およびその装置
JPS5878732A (ja) 1981-11-05 1983-05-12 Toyo Seikan Kaisha Ltd 被覆配向プラスチツクびんの製造方法
JPS58208046A (ja) 1982-05-28 1983-12-03 東洋製罐株式会社 配向された被覆を有するプラスチツク容器及びその製法
CA1213790A (en) * 1982-07-16 1986-11-12 Walter H. Cobbs, Jr. Process for barrier coating polyethylene terephthalate containers with a copolymer of vinylidene chloride
US4551368A (en) 1982-09-07 1985-11-05 The Goodyear Tire & Rubber Company Polyester melt blends having high gas barrier properties
US4403090A (en) 1982-09-07 1983-09-06 The Goodyear Tire & Rubber Company Polyisophthalates and copolymers thereof having high barrier properties
JPS6099364A (ja) * 1983-11-07 1985-06-03 Toyo Seikan Kaisha Ltd 外面塗膜が形成された中空体の製造方法
US4478874A (en) 1983-12-09 1984-10-23 Cosden Technology, Inc. Methods for improving the gas barrier properties of polymeric containers
US4487789A (en) 1984-02-09 1984-12-11 Nippon Gohsei Kagaku Kogyo Kabushiki Kaisha Process for forming film of hydrolyzed ethylene-vinyl acetate copolymer
US4609516A (en) 1984-02-17 1986-09-02 Continental Pet Technologies, Inc. Method of forming laminated preforms
US4632053A (en) 1984-04-05 1986-12-30 Amoco Corporation Apparatus for coating containers
US4534995A (en) * 1984-04-05 1985-08-13 Standard Oil Company (Indiana) Method for coating containers
DE8416309U1 (de) 1984-05-26 1985-03-28 Opticproduct GmbH + Co Vertriebs KG, 6100 Darmstadt Kompakte vorrichtung zur kontinuierlichen kratzfestbeschichtung von kunststoff-formkoerpern
US4543909A (en) 1984-06-01 1985-10-01 Nordson Corporation Exteriorly mounted and positionable spray coating nozzle assembly
US4538542A (en) 1984-07-16 1985-09-03 Nordson Corporation System for spray coating substrates
JPS61108542A (ja) 1984-10-31 1986-05-27 三菱瓦斯化学株式会社 多層容器
DE3519953A1 (de) * 1985-06-04 1986-12-04 BASF Lacke + Farben AG, 4400 Münster Latente primaere aminogruppen enthaltende, wasserverduennbare bindemittel fuer kationische elektrotauchlacke und verfahren zu ihrer herstellung
US4560741A (en) 1985-04-12 1985-12-24 Eastman Kodak Company Polyester resins capable of forming containers having improved gas barrier properties
EP0203630A3 (en) 1985-04-29 1988-04-06 Shell Internationale Researchmaatschappij B.V. Multiple-layer materials
US4942008A (en) 1985-07-10 1990-07-17 Cahill John W Process for molding a multiple layer structure
EP0218245B1 (en) 1985-10-09 1991-05-15 Kuraray Co., Ltd. Injection stretch blow container
US4844987A (en) 1985-10-29 1989-07-04 Teijin Limited Polyamide molding material and hollow-molded body obtained therefrom
JPS63194912A (ja) 1987-02-09 1988-08-12 Nissei Ee S B Kikai Kk 二軸配向容器用プリフオ−ム及びその成形方法
US4764405A (en) * 1987-07-22 1988-08-16 Air Products And Chemicals, Inc. Method for increasing barrier properties of thermoplastic substrates
CA2002369C (en) 1988-11-08 2000-10-31 Mikio Hashimoto Copolyester, polyester composition containing the copolyester, and polyester laminated structure having layer composed of the copolyester or the polyester composition
US4954376A (en) 1988-12-30 1990-09-04 Continental Pet Technologies, Inc. Two material three/five layer preform
JPH0677717B2 (ja) 1989-02-27 1994-10-05 日本合成化学工業株式会社 エチレン―酢酸ビニル共重合体ケン化物の塗膜形成方法
GB8909249D0 (en) 1989-04-24 1989-06-07 Ici Plc Polyester composition
US5143998A (en) 1989-04-26 1992-09-01 The Dow Chemical Company Hydroxy-functional poly(amide ethers) as thermoplastic barrier resins
US4977191A (en) 1989-06-27 1990-12-11 The Seydel Companies, Inc. Water-soluble or water-dispersible polyester sizing compositions
US5028462A (en) * 1989-07-21 1991-07-02 Amoco Corporation Molded bottles and method of producing same
US5136970A (en) * 1989-10-06 1992-08-11 Fuji Photo Film Co., Ltd. Coating apparatus with vertically movable solution receiver
US5164472A (en) 1990-01-18 1992-11-17 The Dow Chemical Company Hydroxy-functional polyethers as thermoplastic barrier resins
US5171820A (en) 1991-05-13 1992-12-15 The Dow Chemical Company Hydroxy-functional polyesters as thermoplastic barrier resins
US5149768A (en) 1991-06-21 1992-09-22 The Dow Chemical Company Hydroxy-functional poly(ether sulfonamides) as thermoplastic barrier resins
US5939188A (en) 1991-07-15 1999-08-17 Pilkington Aerospace, Inc. Transparent coating systems for improving the environmental durability of transparency substrates
US5652034A (en) 1991-09-30 1997-07-29 Ppg Industries, Inc. Barrier properties for polymeric containers
US5814373A (en) 1991-11-26 1998-09-29 Dow Chemical Company Heat-resistant hydroxy-functional polyethers as thermoplastic barrier resins
WO1993023449A1 (en) 1992-05-15 1993-11-25 Imperial Chemical Industries Plc Modified polyester polymers
GB9309024D0 (en) 1993-04-30 1993-06-16 Ici Plc Composite sheet
BR9302624A (pt) 1993-08-02 1994-05-31 Rocha De Albuquerque Antonio J Aplicação de policloreto de vinilideno (PVDC) em pré-formas de polietileno tereftalato (PET) para redução da permeabilidade na fabricação de embalagens
US5443766A (en) 1993-09-10 1995-08-22 Plastipak Packaging, Inc. Method of making multi-layer preform used for plastic blow molding
ZA946726B (en) 1993-09-10 1995-04-21 Plastipak Packaging Inc Polyethylene terephthalate multi-layer preform used for plastic blow molding and method for making the preform.
JPH07156349A (ja) 1993-12-10 1995-06-20 Kureha Chem Ind Co Ltd 多層容器
US5472753A (en) 1994-06-28 1995-12-05 Pepsico Inc. Polyethylene terephthalate-containing laminate
JP2755285B2 (ja) 1994-07-27 1998-05-20 東洋製罐株式会社 香味保持性に優れた包装材料
US5759653A (en) 1994-12-14 1998-06-02 Continental Pet Technologies, Inc. Oxygen scavenging composition for multilayer preform and container
US6121387A (en) 1994-12-21 2000-09-19 Imperial Chemical Industries, Plc Process for preparing a coating composition
FR2728547B1 (fr) 1994-12-22 1997-02-28 Sidel Sa Dispositif de support de preforme
US5505995A (en) 1995-02-02 1996-04-09 Minnesota Mining And Manufacturing Company Method and apparatus for coating substrates using an air knife
PE24697A1 (es) 1995-03-29 1997-09-01 Continental Pet Technologies Envase presurizado para rellenar resistente al resquebrajamiento del bebedero, preforma y metodo para fabricarlos
US5749970A (en) 1995-03-30 1998-05-12 Ngk Insulators, Ltd. Apparatus for coating outer peripheral surface of columnar structural body with a coating material
JPH0939082A (ja) * 1995-08-02 1997-02-10 Nippon Synthetic Chem Ind Co Ltd:The 中空容器の製造法
WO1997011996A1 (en) 1995-09-29 1997-04-03 Avery Dennison Corporation Process for preparing hot water whitening resistant emulsion pressure sensitive adhesives
US5972445A (en) 1996-01-17 1999-10-26 Mitsubishi Chemical Corporation Multilayer polyester sheet
US5716683A (en) 1996-01-30 1998-02-10 Becton, Dickinson And Company Blood collection tube assembly
US6228561B1 (en) 1996-02-01 2001-05-08 Tokyo Electron Limited Film forming method and film forming apparatus
US6485804B1 (en) 1996-02-21 2002-11-26 Mitsui Petrochemical Industries, Ltd. Polyester compositions and laminates and processes for producing biaxially stretched polyester bottles
JPH09296056A (ja) 1996-04-30 1997-11-18 Nippon Ester Co Ltd ラミネート用ポリエステルフィルム及びレトルト処理飲食品用容器
DE69701814T2 (de) 1996-09-23 2000-10-12 Bp Amoco Corp., Chicago Nicht sauerstoffdurchlässige kunstoffflasche für bier und andere anwendungen
AU730163B2 (en) 1996-11-06 2001-03-01 Rohm And Haas Company Method of curing coating compositions
US5942563A (en) 1997-07-18 1999-08-24 The Glidden Company Aqueous dispersed acrylic-epoxy, branched epoxy protective coatings
US6090337A (en) 1997-07-30 2000-07-18 Plastipak Packaging, Inc. Method for making multi-layer plastic preform for blow molding
US5834078A (en) 1997-08-14 1998-11-10 The Dow Chemical Company Hydroxy-functionalized poly(amino ether) salts
DK1015511T3 (da) 1997-09-05 2002-07-22 Dow Chemical Co Emulsioner med højt forhold af intern fase og stabile, vandige dispersioner af hydroxy-funktionelle polymerer
US6129784A (en) * 1997-09-30 2000-10-10 Shiseido Co., Ltd. Color titanated mica pigment and coated-body using the same
US6123211A (en) 1997-10-14 2000-09-26 American National Can Company Multilayer plastic container and method of making the same
US6312641B1 (en) 1997-10-17 2001-11-06 Plastic Fabrication Technologies Llc Method of making containers and preforms incorporating barrier materials
JPH11263938A (ja) * 1998-01-13 1999-09-28 Kansai Paint Co Ltd 水性塗料組成物
JPH11349713A (ja) * 1998-06-05 1999-12-21 Ai Plus Kk ポリエチレンテレフタレート製ボトルの製造方法
US6004680A (en) 1998-07-09 1999-12-21 Hoechst Trespaphan Gmbh Method of coating pre-primed polyolefin films
US6109006A (en) 1998-07-14 2000-08-29 Advanced Plastics Technologies, Ltd. Process for making extruded pet containers
US6946175B2 (en) 1998-07-31 2005-09-20 Chevron Phillips Chemical Co., Lp Oxygen scavenging polymers as active barrier tie layers in multilayered structures
US6315549B1 (en) 1999-03-19 2001-11-13 Husky Injection Molding Systems Ltd. Hot tip insulator retainer
US6475579B1 (en) 1999-08-06 2002-11-05 Plastipak Packaging, Inc. Multi-layer plastic container having a carbon-treated internal surface and method for making the same
US6455620B1 (en) 1999-08-10 2002-09-24 Eastman Chemical Company Polyether containing polymers for oxygen scavenging
US6673432B2 (en) 1999-11-30 2004-01-06 Elk Premium Building Products, Inc. Water vapor barrier structural article
US6309757B1 (en) 2000-02-16 2001-10-30 Ppg Industries Ohio, Inc. Gas barrier coating of polyamine, polyepoxide and hydroxyaromatic compound
US6720052B1 (en) 2000-08-24 2004-04-13 The Coca-Cola Company Multilayer polymeric/inorganic oxide structure with top coat for enhanced gas or vapor barrier and method for making same
US6740378B1 (en) 2000-08-24 2004-05-25 The Coca-Cola Company Multilayer polymeric/zero valent material structure for enhanced gas or vapor barrier and uv barrier and method for making same
EP1193185A1 (en) 2000-10-02 2002-04-03 Heineken Technical Services B.V. Glass container with improved coating
US6461699B1 (en) 2000-10-06 2002-10-08 Plastipak Packaging, Inc. Plastic container having a carbon-treated internal surface for non-carbonated food products
US20030220036A1 (en) 2000-12-20 2003-11-27 Lee Robert A. Laminates and coated materials comprising hydroxy-phenoxyether polymers
US6455116B1 (en) 2001-09-14 2002-09-24 Dow Global Technologies Inc. Poly(hydroxy amino ether) composition, method for preparing the same and articles prepared therefrom
US7072248B2 (en) 2002-09-09 2006-07-04 E. I. Du Pont De Nemours And Company Rapidly low temperature curable high gas barrier coating
US20050070660A1 (en) 2003-08-11 2005-03-31 Daniel Bode Curable polymeric water based coating compositions and resulting coatings with barrier properties for gases and coated substrates and containers

Patent Citations (100)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1702043A (en) * 1923-09-15 1929-02-12 Turner Tanning Machinery Co Method and apparatus for applying and treating varnish
US3317471A (en) * 1959-03-12 1967-05-02 Dow Chemical Co Thermoplastic resinous reaction product of a diglycidyl ether and an amino compound
US3305528A (en) * 1960-11-30 1967-02-21 Union Carbide Corp Poly (hydroxyethers) and a method for their preparation
US3395118A (en) * 1962-10-15 1968-07-30 Union Carbide Corp Modified thermoplastic polyhydroxyethers
US3654894A (en) * 1970-05-11 1972-04-11 Integral Process Syst Inc Pastry coating apparatus
US4040233A (en) * 1970-09-14 1977-08-09 Valyi Emery I Method of obtaining a filled, fluid barrier resistant plastic container
US3900286A (en) * 1971-11-19 1975-08-19 Ciba Geigy Ag Dyestuff preparations and processes for the dyeing of synthetic organic material
US3966378A (en) * 1974-05-28 1976-06-29 Valyi Emery I Apparatus for making oriented hollow plastic articles
US4149645A (en) * 1975-07-02 1979-04-17 Valyi Emery I Plastic article and method for making same
US4267143A (en) * 1978-02-13 1981-05-12 Rhone-Poulenc Industries Process for the manufacturing of bioriented hollow bodies
US4569869A (en) * 1978-11-20 1986-02-11 Yoshino Kogyosho Co., Ltd. Saturated polyester bottle-shaped container with hard coating and method of fabricating the same
US4370368A (en) * 1980-05-07 1983-01-25 Toyo Seikan Kaisha, Ltd. Plastic bottles and process for preparation thereof
US4370368B1 (xx) * 1980-05-07 1990-05-08 Toyo Seikan Kaisha Ltd
US4381277A (en) * 1980-05-29 1983-04-26 Plm Ab Method for producing containers
US4393106A (en) * 1980-10-31 1983-07-12 Toyo Seikan Kaisha Ltd. Laminated plastic container and process for preparation thereof
US4731266A (en) * 1981-06-03 1988-03-15 Rhone-Poulenc, S.A. Water-resistant polyvinyl alcohol film and its application to the preparation of gas-impermeable composite articles
US4515836A (en) * 1982-07-16 1985-05-07 Nordson Corporation Process for coating substrates with aqueous polymer dispersions
US4461857A (en) * 1982-09-29 1984-07-24 Desoto, Inc. Thermosetting aqueous coating compositions containing epoxy-phosphate dispersions
US4940616A (en) * 1982-11-15 1990-07-10 Mitsui Petrochemical Industries Multilayered container and method for making
US4564541A (en) * 1983-02-08 1986-01-14 Toyo Seikan Kaisha, Ltd. Plastic laminate structure and vessel
US4438254A (en) * 1983-02-28 1984-03-20 The Dow Chemical Company Process for producing epoxy resins
US4528321A (en) * 1983-04-06 1985-07-09 Allied Colloids Limited Polymer dispersions and their preparation
US4573429A (en) * 1983-06-03 1986-03-04 Nordson Corporation Process for coating substrates with aqueous polymer dispersions
US4505951A (en) * 1983-07-18 1985-03-19 Owens-Illinois, Inc. Method for making a polyvinylidene chloride coated biaxially oriented polyethylene terephthalate container
US4646925A (en) * 1983-09-29 1987-03-03 Toyo Seikan Kaisha, Ltd. Multi-layer preform for draw-blow forming a bottle
US4741936A (en) * 1983-12-27 1988-05-03 Toyo Seikan Kaisha, Ltd. Laminate preform for a multi-layer polyester bottle
US4499262A (en) * 1984-03-09 1985-02-12 Eastman Kodak Company Process for the preparation of sulfo-modified polyesters
US4578295A (en) * 1984-07-16 1986-03-25 Owens-Illinois, Inc. High barrier polymer blend and articles prepared therefrom
US4647648A (en) * 1985-08-26 1987-03-03 The Dow Chemical Company Polyhydroxyethers from hydroxybiphenyls
US4809640A (en) * 1985-11-02 1989-03-07 Metal Box Public Limited Company Coating of articles
US4818575A (en) * 1986-02-28 1989-04-04 Toyo Seikan Kaisha, Ltd. Biaxially drawn polyester vessel having resistance to heat distortion and gas barrier properties and process for preparation thereof
USRE34537E (en) * 1987-09-23 1994-02-08 E. I. Du Pont De Nemours And Company Plastic composite barrier structures
US5489455A (en) * 1988-02-04 1996-02-06 Ppg Industries, Inc. Container with polyamine-polyepoxide gas barrier coating
US5639848A (en) * 1988-02-04 1997-06-17 Ppg Industries, Inc. Ungelled polyamine-polyepoxide resins
US5491204A (en) * 1988-02-04 1996-02-13 Ppg Industries, Inc. Gas barrier coating from reacting polyamine, alkanolamine and polyepoxide
US5006381A (en) * 1988-02-04 1991-04-09 Ppg Industries, Inc. Ungelled polyamine-polyepoxide resins
US5300541A (en) * 1988-02-04 1994-04-05 Ppg Industries, Inc. Polyamine-polyepoxide gas barrier coatings
US4847129A (en) * 1988-09-16 1989-07-11 Continental Pet Technologies, Inc. Multilayer preform for hot fill containers
US5079034A (en) * 1988-11-21 1992-01-07 Nippon Shokubai Kagaku Kogyo Co., Ltd. Method for manufacturing a water absorbent composite by applying an aqueous polymerizable solution to a substrate and polymerizing the coating against polymerization inner surfaces
US5026462A (en) * 1990-03-06 1991-06-25 Ail Corporation Method and apparatus for electrochemical machining of spray holes in fuel injection nozzles
US5115075A (en) * 1990-05-08 1992-05-19 The Dow Chemical Company Amide and hydroxymethyl functionalized polyethers as thermoplastic barrier resins
US5218075A (en) * 1990-05-08 1993-06-08 The Dow Chemical Company Amide and hydroxymethyl functionalized polyethers as thermoplastic barrier resins
US5409983A (en) * 1990-06-15 1995-04-25 Imperial Chemical Industries Plc Refillable bottle of polyethylene terephthalate copolymer and its manufacture
US5314751A (en) * 1990-06-19 1994-05-24 Imperial Chemical Industries Plc Coating process and product
US5275853A (en) * 1990-10-03 1994-01-04 The Dow Chemical Company Hydroxyl functionalized polyetheramines as barrier packaging for oxygen-sensitive materials
US5089588A (en) * 1990-10-17 1992-02-18 The Dow Chemical Company Hydroxy-functional poly(amide ethers) as thermoplastic barrier resins
US5184373A (en) * 1990-12-22 1993-02-09 Albert Schulte Sohne Gmbh & Co. Caster with conductors between the tire of its wheel and the carrier of its wheel frame
US5184472A (en) * 1991-01-08 1993-02-09 Pierre Guilbault Add on heat pump swimming pool heater control
US5302417A (en) * 1991-02-15 1994-04-12 Kurarav Co., Ltd. Aqueous dispersion and substrate coated with the same
US5196469A (en) * 1991-03-28 1993-03-23 Mica Corporation Ethylene/vinyl alcohol coatings
US5134218A (en) * 1991-06-06 1992-07-28 The Dow Chemical Company Hydroxy-functional poly(amide ethers) as thermoplastic barrier resins
US5281630A (en) * 1991-12-18 1994-01-25 The Seydel Companies Sulfonated water-soluble or water-dispersible polyester resin compositions
US5509965A (en) * 1992-03-18 1996-04-23 Continental Pet Technologies, Inc. Preform coating apparatus and method
US6372318B1 (en) * 1992-07-07 2002-04-16 Continental Pet Technologies, Inc. Method of forming container with high-crystallinity sidewall and low-crystallinity base
US5759656A (en) * 1992-07-07 1998-06-02 Continental Pet Technologies, Inc. Method of forming multilayer preform and container with low crystallizing interior layer
US5300326A (en) * 1993-01-22 1994-04-05 Ppg Industries, Inc. Method of coating a plastic substrate with an aqueous coating composition for plastic substrates
US5646924A (en) * 1993-06-07 1997-07-08 Ricoh Company, Ltd. Recording and simultaneous verifying method of phase-changing type of information recording medium
US5328724A (en) * 1993-09-02 1994-07-12 E. I. Du Pont De Nemours And Company Solution coating process for packaging film
US6011111A (en) * 1993-10-18 2000-01-04 The Dow Chemical Company Hydroxy-phenoxyether polymer thermoplastic composites
US6426135B1 (en) * 1994-01-24 2002-07-30 Sumitomo Chemical Co., Ltd. Resin composition laminate and laminate film
US5726277A (en) * 1994-02-02 1998-03-10 Seydel Companies, Inc. Adhesive compositions from phthalate polymers and the preparation thereof
US6218013B1 (en) * 1994-06-23 2001-04-17 Cellresin Technologies, Llc Barrier material comprising a thermoplastic and a compatible cyclodextrin derivative
US6391946B2 (en) * 1994-06-23 2002-05-21 Cellresin Technologies, Llc Rigid polymeric beverage bottles with improved resistance to permeant elution
US5645183A (en) * 1994-07-06 1997-07-08 Plastipak Packaging, Inc. Multi-layer containers
US5753358A (en) * 1994-08-25 1998-05-19 W. L. Gore & Associates, Inc. Adhisive-filler polymer film composite
US5637365A (en) * 1994-12-16 1997-06-10 Ppg Industries, Inc. Epoxy-amine barrier coatings with aryloxy or aryloate groups
US6673874B1 (en) * 1994-12-21 2004-01-06 Imperial Chemical Industries Plc Modified polymers
US20020061371A1 (en) * 1996-03-07 2002-05-23 Steven L. Schmidt Multilayer container resistant to elevated temperatures and pressures, and method of making the same
US5780128A (en) * 1996-04-15 1998-07-14 Pepsico Inc. Polyethylene preform and container
US6086991A (en) * 1996-06-12 2000-07-11 Hoechst Trespaphan Gmbh Method of priming poly(ethylene terephthalate) articles for coating
US6068900A (en) * 1996-07-05 2000-05-30 Wella Ag Plastic container having a high resistance to chemical attack and method of making same
US6863988B2 (en) * 1996-09-23 2005-03-08 Bp Corporation North America Inc. Oxygen scavenging monolayer bottles
US5731094A (en) * 1996-10-22 1998-03-24 The Dow Chemical Company Hydroxy-phenoxyether polyester coextruded laminates
US20030012904A1 (en) * 1997-10-17 2003-01-16 Hutchinson Gerald A. Polyester laminate materials
US20030001315A1 (en) * 1997-10-17 2003-01-02 Hutchinson Gerald A. Methods for preparing coated polyester articles
US6391408B1 (en) * 1997-10-17 2002-05-21 Advanced Plastics Technologies, Ltd. Coated polyester preforms and method of making same
US6676883B2 (en) * 1997-10-17 2004-01-13 Advanced Plastics Technologies Methods for preparing coated polyester articles
US20020001686A1 (en) * 1998-03-12 2002-01-03 Mitsubishi Gas Chemical Company, Inc Oxygen-absorbing multi-layer laminate, production method thereof and packaging container
US6352426B1 (en) * 1998-03-19 2002-03-05 Advanced Plastics Technologies, Ltd. Mold for injection molding multilayer preforms
US20020048682A1 (en) * 1998-09-01 2002-04-25 Subramanian Pallatheri M. Multilayer structures of poly(1,3-propylene 2,6 napthalate) and poly (ethylene terephthalate)
US6350796B1 (en) * 1998-10-28 2002-02-26 Vianova Resins Ag Ionically on nonionically stabilized epoxy adducts as water-dilutable base resins for 2-component isocyanate crosslinkable systems
US6393803B1 (en) * 1998-11-06 2002-05-28 Graham Packaging Company, L.P. Process for coating blow-molded plastic containers
US6524672B1 (en) * 1999-02-12 2003-02-25 Plastipak Packaging, Inc. Multilayer preform and container with co-extruded liner
US6184281B1 (en) * 1999-06-21 2001-02-06 The Glidden Company Strippable aqueous emulsion inomeric coating for recyclable plastic containers
US6746769B2 (en) * 1999-08-06 2004-06-08 Plastipak Packaging, Inc. Plastic container having a carbon-treated internal surface
US6592956B2 (en) * 1999-08-06 2003-07-15 Plastipak Packaging, Inc. Plastic container having a carbon-treated internal surface
US6418636B1 (en) * 1999-08-11 2002-07-16 Eisermann Maschinenbau Kg Drier for a lacquering line
US6180715B1 (en) * 1999-09-03 2001-01-30 The Dow Chemical Company Aqueous solution and dispersion of an acid salt of a polyetheramine
US6723431B2 (en) * 2000-01-24 2004-04-20 Exxonmobil Oil Corporation Multilayer metallized polyolefin film
US20030031814A1 (en) * 2000-04-28 2003-02-13 Hutchinson Gerald A. Bottles and preforms having a crystalline neck
US6709759B2 (en) * 2000-05-12 2004-03-23 Pechiney Emballage Flexible Europe Thermoplastic film structures having improved barrier and mechanical properties
US6403231B1 (en) * 2000-05-12 2002-06-11 Pechiney Emballage Flexible Europe Thermoplastic film structures having improved barrier and mechanical properties
US20020028870A1 (en) * 2000-05-30 2002-03-07 Amcol International Corporation Layered clay intercalates and exfoliates having a low quartz content
US6346596B1 (en) * 2000-07-14 2002-02-12 Valspar Corporation Gas barrier polymer composition
US20020090473A1 (en) * 2000-09-05 2002-07-11 Lee Robert A. Multilayer containers and preforms having barrier properties utilizing recycled material
US6872802B2 (en) * 2000-11-06 2005-03-29 The Procter & Gamble Company Plastic articles digestible by hot alkaline treatment
US6515067B2 (en) * 2001-01-16 2003-02-04 Chevron Phillips Chemical Company Lp Oxygen scavenging polymer emulsion suitable as a coating, an adhesive, or a sealant
US6709735B2 (en) * 2001-11-14 2004-03-23 Mitsubishi Polyester Film, Llc Oxygen barrier coating and coated film
US6982119B2 (en) * 2002-04-15 2006-01-03 The Coca-Cola Company Coating composition containing an epoxide additive and structures coated therewith
US6893730B2 (en) * 2002-09-24 2005-05-17 Honeywell International Inc. Barrier film with reduced dynamic coefficient of friction

Cited By (60)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030219555A1 (en) * 1997-10-17 2003-11-27 Hutchinson Gerald A. Coated polyester preforms and articles
US20040247735A1 (en) * 1997-10-17 2004-12-09 Hutchinson Gerald A. Preform molds incorporating high heat conductivity material
US20080061476A1 (en) * 1997-10-17 2008-03-13 Advanced Plastics Technologies Luxembourg S.A Coated polyester preforms and articles
US7645135B2 (en) 1997-10-17 2010-01-12 Advanced Plastics Technologies Luxembourg S.A. Mold for injecting molding preforms
US20030012904A1 (en) * 1997-10-17 2003-01-16 Hutchinson Gerald A. Polyester laminate materials
US20080044605A1 (en) * 2000-09-05 2008-02-21 Advanced Plastics Technology Luxembourg S.A. Multilayer containers and preforms having barrier properties
US20040151937A1 (en) * 2002-11-08 2004-08-05 Hutchinson Gerald A. Injection mold having a wear resistant portion and a high heat transfer portion
US20080203617A1 (en) * 2002-11-08 2008-08-28 Advanced Plastics Technologies Luxembourg S.A. Injection mold having a wear resistant portion and a high heat transfer portion
US20070031673A1 (en) * 2003-08-11 2007-02-08 Daniel Bode Curable polymeric water based coating compositions and resulting coatings with barrier properties for gases and laminate structures
US20050070660A1 (en) * 2003-08-11 2005-03-31 Daniel Bode Curable polymeric water based coating compositions and resulting coatings with barrier properties for gases and coated substrates and containers
US8247051B2 (en) * 2003-08-11 2012-08-21 The Glidden Company Curable polymeric water based coating compositions and resulting coatings with barrier properties for gases and laminate structures
US20050136201A1 (en) * 2003-12-22 2005-06-23 Pepsico, Inc. Method of improving the environmental stretch crack resistance of RPET without solid stating
US7150902B2 (en) * 2004-04-07 2006-12-19 Pepsico, Inc. High Tg coatings
US20050227083A1 (en) * 2004-04-07 2005-10-13 Pepsico, Inc. High Tg coatings
US8551589B2 (en) 2004-04-16 2013-10-08 The Concentrate Manufacturing Company Of Ireland Mono and multi-layer articles and extrusion methods of making the same
US20060065992A1 (en) * 2004-04-16 2006-03-30 Hutchinson Gerald A Mono and multi-layer articles and compression methods of making the same
US20060051451A1 (en) * 2004-06-10 2006-03-09 Hutchinson Gerald A Methods and systems for controlling mold temperatures
US20080138455A1 (en) * 2004-06-10 2008-06-12 Advanced Plastics Technologies Luxembourg S.A Methods and systems for controlling mold temperatures
WO2006052659A3 (en) * 2004-11-05 2006-12-07 Pepsico Inc Dip, spray and flow coating process for forming coated articles
WO2006060104A1 (en) * 2004-11-05 2006-06-08 Pepsico, Inc., A North Carolina Corporation Catalyzed process for forming coated articles
WO2006052659A2 (en) * 2004-11-05 2006-05-18 Advanced Plastics Technologies Luxembourg S.A. Dip, spray and flow coating process for forming coated articles
US20060099360A1 (en) * 2004-11-05 2006-05-11 Pepsico, Inc. Dip, spray, and flow coating process for forming coated articles
US20060292323A1 (en) * 2005-04-18 2006-12-28 Hutchinson Gerald A Water-resistant coated articles and methods of making same
US20070108668A1 (en) * 2005-08-30 2007-05-17 Hutchinson Gerald A Methods and systems for controlling mold temperatures
US7717697B2 (en) 2005-08-30 2010-05-18 Sharon Hutchinson Methods and systems for controlling mold temperatures
WO2007027606A1 (en) 2005-08-30 2007-03-08 Advanced Plastics Technologies Luxembourg S.A. Methods and systems for controlling mold temperatures
US20070087131A1 (en) * 2005-10-14 2007-04-19 Hutchinson Gerald A Methods of forming multilayer articles by surface treatment applications
WO2007087470A3 (en) * 2006-01-27 2008-01-10 Gen Patent Llc Improved shock wave treatment device
US20090176031A1 (en) * 2006-05-24 2009-07-09 Alberto Armellin Container coating system and process
US9188385B2 (en) * 2006-05-24 2015-11-17 S.I.P.A. Società Industrializzazione Progettazione E Automazione S.P.A. Container coating system and process
US20090047531A1 (en) * 2007-08-17 2009-02-19 Ppg Industries Ohio, Inc. Packages having radiation-curable coatings
USD769720S1 (en) 2007-12-21 2016-10-25 Silgan Plastics Llc Preform for dosing bottle
USD705659S1 (en) * 2007-12-21 2014-05-27 Silgan Plastics Llc Preform for dosing bottle
US9848641B2 (en) * 2009-06-29 2017-12-26 John Wollin Nicotine delivery system
US20120125353A1 (en) * 2009-06-29 2012-05-24 John Wollin Nicotine delivery system
US20110056947A1 (en) * 2009-09-07 2011-03-10 Kraft Foods Global Brands Llc Multi-faceted container and reclosable lid for food products
US20110223069A1 (en) * 2010-03-12 2011-09-15 David Offord Container having an oxygen scavenging activation system
WO2011112775A3 (en) * 2010-03-12 2012-01-19 Amcor Limited Container having oxygen scavenging system
US8496885B2 (en) 2010-03-12 2013-07-30 Amcor Limited Container having oxygen scavenging system
US8524157B2 (en) 2010-03-12 2013-09-03 Amcor Limited Container having an oxygen scavenging activation system
US20110223070A1 (en) * 2010-03-12 2011-09-15 David Offord Container having oxygen scavenging system
US8551419B2 (en) 2010-03-12 2013-10-08 Amcor Limited Container having an oxygen scavenging indication system
US20110223068A1 (en) * 2010-03-12 2011-09-15 David Offord Container having an oxygen scavenging indication system
US9289938B2 (en) 2010-03-12 2016-03-22 Amcor Limited Container having oxygen scavenging system
WO2011163562A3 (en) * 2010-06-25 2012-04-19 Amcor Limited Oxygen scavenging system for a container
US9108176B2 (en) 2010-06-25 2015-08-18 Amcor Limited Oxygen scavenging system for a container
US9662622B2 (en) 2010-06-25 2017-05-30 Amcor Limited Oxygen scavenging system for a container
US9707732B2 (en) * 2011-03-25 2017-07-18 Amcor Limited Barrier system for wide mouth containers
US20120241406A1 (en) * 2011-03-25 2012-09-27 Beuerle Frederick C Barrier system for wide mouth containers
US9017591B2 (en) * 2011-04-27 2015-04-28 Canon Kabushiki Kaisha Method for manufacturing seamless belt for electrophotography
US20120274002A1 (en) * 2011-04-27 2012-11-01 Canon Kabushiki Kaisha Method for manufacturing seamless belt for electrophotography
US8962740B2 (en) 2012-09-10 2015-02-24 Kraft Foods Group Brands Llc Oxygen scavenger system in a polyolefin matrix
US20150158204A1 (en) * 2013-12-10 2015-06-11 Krones Ag Method and apparatus for producing plastic preforms
US20200338590A1 (en) * 2015-09-30 2020-10-29 Suntory Holdings Limited Preform coating device and preform coating method
US20170158390A1 (en) * 2015-12-04 2017-06-08 Mead Johnson Nutrition Company Powder dosing closure
CN108367843A (zh) * 2015-12-04 2018-08-03 Mjn 美国控股有限责任公司 粉末定量加料封盖
US20170340899A1 (en) * 2016-05-25 2017-11-30 Boston Scientific Scimed, Inc. Radioactive stent
JP2020037415A (ja) * 2018-08-31 2020-03-12 株式会社吉野工業所 合成樹脂製容器、合成樹脂製容器の製造方法、及び積層プリフォーム
US20220218570A1 (en) * 2021-01-13 2022-07-14 Lisa Stahl Teether
US20220258919A1 (en) * 2021-02-12 2022-08-18 Plastipak Packaging, Inc. Plastic container with barrier

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US7717057B2 (en) 2010-05-18
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US20080041304A1 (en) 2008-02-21

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