US20060286325A1 - Foam-paperboard laminates, articles incorporating same and methods of making the same - Google Patents

Foam-paperboard laminates, articles incorporating same and methods of making the same Download PDF

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Publication number
US20060286325A1
US20060286325A1 US11/454,570 US45457006A US2006286325A1 US 20060286325 A1 US20060286325 A1 US 20060286325A1 US 45457006 A US45457006 A US 45457006A US 2006286325 A1 US2006286325 A1 US 2006286325A1
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United States
Prior art keywords
foam
paperboard
ldpe
laminate
caliper
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Abandoned
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US11/454,570
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English (en)
Inventor
Dean Swoboda
Rana Shehadeh
Anthony Swiontek
Gregory Anderson
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Dixie Consumer Products LLC
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Fort James Corp
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Priority to US11/454,570 priority Critical patent/US20060286325A1/en
Assigned to FORT JAMES CORPORATION reassignment FORT JAMES CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ANDERSON, GREGORY J., SHEHADEH, RANA, SWOBODA, DEAN P., SWIONTEK, ANTHONY J.
Publication of US20060286325A1 publication Critical patent/US20060286325A1/en
Assigned to DIXIE CONSUMER PRODUCTS LLC reassignment DIXIE CONSUMER PRODUCTS LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FORT JAMES CORPORATION
Abandoned legal-status Critical Current

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    • 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
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/02—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
    • B29C44/12—Incorporating or moulding on preformed parts, e.g. inserts or reinforcements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/10—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of paper or cardboard
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B29/00—Layered products comprising a layer of paper or cardboard
    • B32B29/002—Layered products comprising a layer of paper or cardboard as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B29/007—Layered products comprising a layer of paper or cardboard as the main or only constituent of a layer, which is next to another layer of the same or of a different material next to a foam layer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B3/00—Layered products comprising a layer with external or internal discontinuities or unevennesses, or a layer of non-planar shape; Layered products comprising a layer having particular features of form
    • B32B3/02—Layered products comprising a layer with external or internal discontinuities or unevennesses, or a layer of non-planar shape; Layered products comprising a layer having particular features of form characterised by features of form at particular places, e.g. in edge regions
    • B32B3/04—Layered products comprising a layer with external or internal discontinuities or unevennesses, or a layer of non-planar shape; Layered products comprising a layer having particular features of form characterised by features of form at particular places, e.g. in edge regions characterised by at least one layer folded at the edge, e.g. over another layer ; characterised by at least one layer enveloping or enclosing a material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/18—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/30—Multi-ply
    • D21H27/32—Multi-ply with materials applied between the sheets
    • D21H27/34—Continuous materials, e.g. filaments, sheets, nets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B38/00—Ancillary operations in connection with laminating processes
    • B32B2038/0052—Other operations not otherwise provided for
    • B32B2038/0084—Foaming
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2250/00—Layers arrangement
    • B32B2250/44—Number of layers variable across the laminate
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2266/00—Composition of foam
    • B32B2266/02—Organic
    • B32B2266/0214—Materials belonging to B32B27/00
    • B32B2266/025—Polyolefin
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2305/00—Condition, form or state of the layers or laminate
    • B32B2305/02—Cellular or porous
    • B32B2305/022—Foam
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/30—Properties of the layers or laminate having particular thermal properties
    • B32B2307/304—Insulating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/50—Properties of the layers or laminate having particular mechanical properties
    • B32B2307/58—Cuttability
    • B32B2307/581—Resistant to cut
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/70—Other properties
    • B32B2307/744—Non-slip, anti-slip
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2317/00—Animal or vegetable based
    • B32B2317/12—Paper, e.g. cardboard
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2323/00—Polyalkenes
    • B32B2323/04—Polyethylene
    • B32B2323/046—LDPE, i.e. low density polyethylene
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2439/00—Containers; Receptacles
    • B32B2439/70—Food packaging
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D81/00—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents
    • B65D81/38—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents with thermal insulation
    • B65D81/3865—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents with thermal insulation drinking cups or like containers
    • B65D81/3874—Containers, packaging elements, or packages, for contents presenting particular transport or storage problems, or adapted to be used for non-packaging purposes after removal of contents with thermal insulation drinking cups or like containers formed of different materials, e.g. laminated or foam filling between walls
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H19/00—Coated paper; Coating material
    • D21H19/66—Coatings characterised by a special visual effect, e.g. patterned, textured
    • D21H19/70—Coatings characterised by a special visual effect, e.g. patterned, textured with internal voids, e.g. bubble coatings
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/10—Packing paper
    • 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]
    • Y10T428/1376—Foam or porous material containing

Definitions

  • the present invention relates to foam-paperboard laminates prepared using an in situ foaming process.
  • the foam-paperboard laminates of the present invention are formed by extruding LDPE polymer onto a moisture-containing paperboard to provide a LDPE-coated paperboard material. Upon heating of the LDPE-coated paperboard, the moisture in the paperboard causes steam to act as a blowing agent for the LDPE and a LDPE foam is obtained. The foam is adhered by way of physical adhesion of the polymer to the paperboard.
  • the foam-paperboard laminates of the present invention exhibit insulating and cushioning properties.
  • the foam-paperboard laminates are suitable for use in, for example, insulated beverage cups, food service containers, packaging materials, and in other products where insulating and/or cushioning laminate materials can be useful.
  • Foam-paperboard laminates prepared using in situ foaming processes are known for use in insulated beverage cups that are sold commercially as PerfecTouch® by the assignee of the present invention.
  • the basic technology used to prepare the foam surface of the cups is disclosed in U.S. Pat. No. 4,435,344 to Iioka, the disclosure of which is incorporated herein in its entirety by this reference.
  • the beverage cup is fabricated to include a bottom panel and a sidewall, both of which are made of paperboard material.
  • LDPE is extruded to one surface of the sidewall material.
  • a blend of LDPE and HDPE is extruded to the other side of the sidewall material.
  • Foaming of the LDPE-coated outer sidewall surface is carried out in situ by placing the unfoamed beverage cup in an oven and heating it above the melting point of the outer LDPE coating.
  • the moisture within the paperboard causes steam to form and, since steam occupies more volume than liquid water, pressure is created, thus providing a foaming action on the LDPE-coated outer cup surface.
  • the HDPE/LDPE layer on the inside of the cup prevents steam from escaping toward the interior of the beverage cup to result in preferential foaming of the outer layer. Cups made in this manner exhibit superior insulating properties, especially with respect to hot liquids such as coffee, tea, and the like.
  • the cups are also suitably used for cold beverages.
  • the present invention provides foam-paperboard laminates prepared from LDPE having a MI of greater than 8 to about 20 g/10 min, as measured by ASTM 1298.
  • the foam aspect of the foam-paperboard laminates of the present invention is prepared by one or more methods of reducing the orientation of an extruded LDPE coated on the paperboard.
  • the foam is obtained by first extruding the LDPE onto the paperboard to provide a LDPE-coated paperboard material.
  • the material is then heated to provide steam release from the paperboard.
  • the steam operates as a blowing agent and causes the LDPE to foam in situ.
  • the LDPE foam is physically adhered to the paperboard to provide a foam-paperboard laminate.
  • the foam-paperboard laminates of the present invention are suitable for use in insulated beverage cups, packaging materials, as well as many other products.
  • LDPE low density polyethylene
  • the characteristics of the foam prepared in accordance with the present invention are significantly improved over foams prepared using prior art methods.
  • FIG. 1 is a schematic view in elevation and section of an insulated beverage cup prepared from a foam-paperboard laminate of the present invention
  • FIG. 1 a is a detail of the insulated beverage cup of FIG. 1 showing the various layers schematically in the area where the bottom panel is joined to the paperboard sidewall.
  • FIG. 2 is a schematic diagram illustrating coating of paperboard with a LDPE using a slit die apparatus.
  • FIG. 2 a is a schematic view of a foam-paperboard laminate in accordance with an aspect of the present invention comprising an occlusive layer on an interior side, and a LDPE foam layer on the other side.
  • FIG. 3 is a photomicrograph in section of a foam-paperboard laminate where LDPE having a melt index of 5.7 g/10 min was applied to the paperboard at a web speed of 200 ft/min.
  • FIG. 4 is a photomicrograph in section of a foam-paperboard laminate where LDPE having a MI of 5.7 g/10 min was applied to the paperboard at a web speed of 450 ft/min, where the extrusion conditions were not optimized.
  • FIG. 5 is a photomicrograph in section of a foam-paperboard laminate where LDPE having a MI of 5.7 g/10 min was applied to the paperboard web speed of 200 ft/min.
  • FIG. 6 is a photomicrograph in section of a foam-paperboard laminate where LDPE having a MI of 5.7 g/10 min was applied to the paperboard at a web speed of 450 ft/min where the extrusion conditions were not optimized.
  • FIG. 7 is a plot of polymer foam caliper versus coat weight in pounds/ream of LDPE after foaming for 5.7 MI LDPE for various melt temperatures and extrusion speeds.
  • FIG. 8 is a plot of polymer foam caliper versus coat weight in pounds/ream of LDPE after foaming for 5.7 MI LDPE for various melt temperatures at an extrusion speed of 300 fpm.
  • FIG. 9 is a plot of polymer foam caliper versus coat weight in pounds/ream of LDPE after foaming for 5.7 MI LDPE for various melt temperatures at an extrusion speed of 450 fpm.
  • FIG. 10 is a plot of polymer foam caliper versus coat weight in pounds/ream of LDPE after foaming for 5.7 MI for various extrusion speeds.
  • FIG. 11 is a plot of polymer foam caliper versus coat weight in pounds/ream of LDPE after foaming for 5.7 MI LDPE at various extrusion speeds.
  • FIG. 12 is a plot of polymer foam caliper versus coat weight in pounds/ream of LDPE after foaming for 4.5 MI LDPE at various extrusion speeds.
  • FIG. 13 is a plot of polymer foam caliper versus coat weight in pounds/ream of LDPE after foaming for 12.0 MI LDPE at various extrusion speeds.
  • FIG. 14 is a plot of average polymer foam caliper in mils versus LDPE melt index for various MI LDPE at a web speed of 300 fpm.
  • FIG. 15A is a photomicrograph of a foam-paperboard laminate produced from 5.7 MI LDPE at a web speed of 450 feet per minute using a 40 mil die gap and 5′′ air gap.
  • FIG. 15B is a further view of the foam-paperboard laminate of FIG. 15A .
  • FIG. 16A is a photomicrograph of a foam-paperboard laminate produced from 5.7 MI LDPE at a web speed of 450 feet per minute using a 20 mil die gap and 9′′ air gap.
  • FIG. 16B is a further view of the foam-paperboard laminate of FIG. 16A .
  • FIG. 17A is a photomicrograph of a foam-paperboard laminate produced from 5.7 MI LDPE at a web speed of 450 feet per minute using a 20 mil die gap, 13′′ air gap and a coat weight of 22 pounds per ream.
  • FIG. 17B is a further view of the foam-paperboard laminate of FIG. 17A .
  • FIG. 18A is a photomicrograph of a foam-paperboard laminate produced from 13.7 MI LDPE at a web speed of 450 feet per minute using a 20 mil die gap, 13′′ air gap and a coat weight of 24 pounds per ream.
  • FIG. 18B is a further view of the foam-paperboard laminate of FIG. 18A .
  • FIG. 19A is a photomicrograph of a foam-paperboard laminate produced from 4.5 MI LDPE at a web speed of 450 feet per minute using a 20 mil die gap, 9′′ air gap and a coat weight of 22 pounds per ream.
  • FIG. 19B is a further view of the foam-paperboard laminate of FIG. 19A .
  • FIG. 19A is a photomicrograph of a foam-paperboard laminate produced from 12.0 MI LDPE at a web speed of 450 feet per minute using a 20 mil die gap, 13′′ air gap and a coat weight of 26 pounds per ream.
  • FIG. 20B is a further view of the foam-paperboard laminate of FIG. 20A .
  • FIGS. 21A and 21B are laser-scanned surface images of various foam-paperboard laminates.
  • FIGS. 22A and 22B are angular plots of isotropy for the samples of FIGS. 21A and 21B .
  • FIG. 23 is a plot of polymer foam caliper for 13.7 MI LDPE at various melt temperatures and extrusion speeds at an air gap of 11′′ and a die gap of 20 mils.
  • FIG. 24 is a plot of polymer foam caliper for various MI LDPE at various extrusion speeds.
  • FIG. 25 is a plot of polymer foam caliper for 5.7 MI LDPE at various oven temperatures and residence times.
  • FIG. 26 is a plot of polymer foam caliper for 12.0 MI LDPE at various oven temperature and residence times.
  • FIG. 27 is a plot of polymer foam caliper for 13.7 MI LDPE at various oven temperatures and residence times.
  • FIG. 28 is a plot of polymer foam caliper for 5.7 MI LDPE at various oven temperatures and residence times, where the oven temperatures are higher than those in FIG. 25 .
  • FIG. 29 is a plot of polymer foam caliper for 12.0 MI LDPE at various oven temperatures and residence times, where the oven temperatures are higher than those in FIG. 26 .
  • FIG. 30 is a plot of polymer foam caliper for 13.7 MI LDPE at various oven temperatures and residence times, where the oven temperatures are higher than those in FIG. 27 .
  • FIG. 31 is a comparison of polymer foam caliper visual characteristics and caliper for 12.0 MI LDPE at various oven temperatures and residence times.
  • ranges are expressed herein as from “about” one particular value, and/or to “about” another particular value. When such a range is expressed, another embodiment includes from the one particular value and/or to the other particular value. Similarly, when values are expressed as approximations, by use of the antecedent “about,” it will be understood that the particular value forms another embodiment. It will be further understood that the endpoints of each of the ranges are significant both in relation to the other endpoint, and independently of the other endpoint.
  • melt index is measured according to ASTM 1298 and has the units g/10 mins.
  • melt index may be abbreviated herein as “MI.”
  • the stated melt index may also be presented without the units; however, it should be understood that when presented without units, the stated melt index has the units g/1 0 mins and the melt index is measured in accordance with ASTM 1298.
  • Melt temperature refers to the temperature at the extrusion die used to apply a coating to paperboard.
  • Per ream means per 3000 square feet of paperboard, which is a common measurement used by one of ordinary skill in the art.
  • an ASTM test method referred to means the version in effect as of Jun. 1, 2005 unless specifically stated otherwise.
  • Each ASTM referenced in this application is incorporated herein in its entirety by this reference.
  • Foam thickness of a foam-paperboard laminates is determined by measuring overall caliper of a foam-paperboard laminates.
  • the foam thickness is presented as a total thickness (in mils) of the foam layer, the paperboard layer and the occlusive layer on the inner surface of the paperboard.
  • the paperboard used for all examples herein was about 15 mils.
  • the thickness of the occlusive layer was negligible. Accordingly, a thickness reported as, for example, about 25 mils, will have a paperboard thickness of about 15 mils and a LDPE thickness of about 10 mils.
  • Overall caliper is generally measured on at least 5 locations on a sample and averaged.
  • LDPE means “Low Density Polyethylene.” LDPE is also known as “high pressure polyethylene” because it is typically produced at pressures ranging from 82-276 MPA (800-2725 atm). LDPE is generally produced in either a tubular or stirred autoclave reactor. Traditionally, LDPE has been defined as a homo-polymer having a density from about 0.915 and 0.940 g/cm 3 ; however comonomers are sometimes used in LDPE products (products having a density above 0.940 g/cm 3 are considered HDPE).
  • HDPE means “High Density Polyethylene.”
  • HDPE is defined by ASTM D 1248-84 as a product of ethylene polymerization with a density of 0.940 g/cm 3 or higher. This range includes both homo-polymers of ethylene and its copolymers with small amounts of alpha-olefins.
  • SEM scanning electron micrograph
  • FPM feet per minute
  • foam-paperboard laminates not made using an in situ process are generally made by first foaming LDPE to provide a foam structure. This foam structure is then separately adhered, such as with an adhesive, to the paperboard to provide a laminate.
  • foaming uses a traditional blowing agent, such as a gas (e.g. a hydrocarbon gas or CO 2 ) or chemical blowing agent to prepare the foam.
  • a gas e.g. a hydrocarbon gas or CO 2
  • chemical blowing agent to prepare the foam.
  • the primary mechanism for producing foam in an in situ process is the creation of steam by way of evaporation of water from the paperboard.
  • This in situ method has been found by the inventors herein to require a careful balance between LDPE properties, the extruded coating properties and the paperboard properties to provide a foam-paperboard laminates having a satisfactory foam as discussed further herein where the foam is suitably adhered to the surface of the paperboard without application of a separate adhesive.
  • LDPE is extruded onto a paperboard material having a certain amount of moisture therein.
  • the foam-paperboard laminate is then placed into an oven or other type of heating system. During heating, the polymer softens and the moisture in the paperboard turns into steam. The steam causes the LDPE coating to soften and the steam acts as a blowing agent to deform the LDPE coating to provide foam cells.
  • the inventors herein have determined that the properties of the LDPE suitable to provide satisfactory foam formation are significantly different from the properties required for general applications of extruded LDPE coated paperboard structures, such as those used in packaging applications.
  • the inventors herein have determined that the properties of the extruded LDPE coating are highly significant to obtaining satisfactory LDPE foams.
  • the properties of the LDPE coating in the present invention are determined by the properties of the LDPE itself, and also by processing parameters as discussed further herein.
  • low melt index LDPE polymers are used to prepare extruded coatings; higher melt index polymers, which are generally “softer” polymers and exhibit better flow properties, are used for injection molding applications.
  • higher melt index polymers which are generally “softer” polymers and exhibit better flow properties, are used for injection molding applications.
  • One of ordinary skill in the art would normally not seek to use a higher melt index polymer for extrusion coating because the resulting coating would be thought to be too soft to provide an article with useful properties.
  • foam-paperboard laminates of the present invention incorporate an extruded LDPE polymer coating
  • further processing of this extruded coating is necessary to provide the foam aspect of the foam-paperboard laminates.
  • Prior art would thus dictate that a lower melt index polymer should be used to prepare an extruded LDPE coating.
  • low melt index LDPE did not provide suitable foaming.
  • the resulting foam for example, exhibited low aspect ratio and poor adhesion.
  • the present invention provides foam-paperboard laminates prepared using an in situ foaming process.
  • a LDPE polymer is extruded onto a paperboard material having a suitable amount of moisture to provide an LDPE-coated paperboard material.
  • This material is then placed into an oven, whereby the moisture in the paperboard turns to steam.
  • This steam then acts as a blowing agent for the LDPE to provide LDPE foam.
  • the foam is adhered to the paperboard surface to provide the foam-paperboard laminates of the present invention.
  • the extruded LDPE coating must comprise a coating that is “soft” enough to provide foam with a suitable aspect ratio. After foaming, the extruded LDPE foam must also be suitably adhered to the paperboard surface to provide good foam quality.
  • the foam-paperboard laminates of the present invention are prepared from an extruded LDPE as discussed herein, along with a paperboard material having a suitable amount of moisture included therein, the inventive foam-paperboard laminates can be obtained using significantly higher speed operations than that possible previously.
  • the foam aspect of the foam-paperboard laminates of the present invention is of a better quality and consistency than obtainable using the prior art in situ foaming process disclosed in U.S. Pat. No. 4,435,344 (previously incorporated by reference), the disclosure of which is incorporated herein in its entirety by this reference.
  • the improved quality of the foam obtained herein allows the foam-paperboard laminates to provide better insulation properties. Further, the laminate surface is more consistent in appearance and quality.
  • foam-paperboard laminates of the present invention are therefore more aesthetically pleasing than foam-paperboard laminates obtainable previously. Still further, since the foam aspect of the foam-paperboard laminates of the present invention is improved in consistency, it is expected that the cushioning properties of the foam-paperboard laminates of the present invention will also be improved.
  • the inventors herein determined that to obtain suitable foam using the in situ process, it was necessary to provide an LDPE coating wherein the molecular orientation of the polymer was minimized.
  • speeding up of the web speed without modification of any other variables resulted in increased orientation of the LDPE, which, in turn, reduced the ability of the LDPE to foam and/or suitably adhered to the surface of the paperboard after foaming.
  • the inventors determined that, in contrast to the low melt index LDPE typically used to prepare extruded LDPE coatings, foam-paperboard laminates could be suitably prepared from LDPE polymers having higher melt indices. This was found to be due to the fact that the in situ foaming process was adversely affected by the use of low melt index polymer when a high speed process was conducted as a result of the increased orientation of the LDPE when a high speed extrusion process was conducted.
  • the present invention pertains to foam-paperboard laminates prepared from LDPE having a MI of from greater than 8.0 to about 20 g/10 min, as measured by ASTM 1298.
  • the LDPE of the present invention consists essentially of a MI of greater than 8.0 to about 20 g/10 min, as measured by ASTM 1298. LDPE having such MI's have been found to orient less substantially when the extrusion process is conducted at speeds greater than about 350 feet per minute. As discussed, this lesser orientation is believed to result in the formation of a higher foam quality in the in situ process of the present invention.
  • foam-paperboard laminates of the present invention are prepared from a LDPE having a MI of greater than 8.0, 8.5, 9.0, 9.5 or 10.0 g/10 min., as measured by ASTM 1298. Yet further, the foam-paperboard laminates of the present invention are prepared from a LDPE having a MI of about 8.5, 9.0, 10.0. 11.0. 12.0, 13.0, 14.0, 15.0, 16.0, 17.0, 18.0, 19.0 or 20.0 g/10min, as measured by ASTM 1298, where any of the stated values can comprise an upper or a lower endpoint, as appropriate. Such polymers are available, for example, from Westlake Chemical (Houston, Tex.).
  • a melted LDPE having a MI conforming to the specified range set out herein is extruded onto a paperboard substrate.
  • the extrusion melt temperatures suitable for the present invention are discussed in more detail herein.
  • substantially linear ethylene polymers may be used as the extruded polyethylene material.
  • Such polymers are disclosed in U.S. Pat. Nos. 5,272,236 and 5,278,272, the disclosures of which are herein incorporated in their entireties by this reference.
  • Suitable examples of substantially linear ethylene polymers are available from Dow Global Technologies (Freeport, Tex.).
  • a particularly suitable paperboard substrate for use in the present invention is solid bleached sulfate (“SBS”).
  • SBS solid bleached sulfate
  • This paperboard is available as “cupstock” or “platestock” from Georgia- Pacific Corporation (Atlanta, Ga.).
  • SBS exhibits good surface properties (e.g., smoothness) such that the inventors herein have found the adhesion between the foam and the paperboard to be exceedingly good.
  • paperboard are also currently thought to be suitable to prepare the foam-paperboard laminates of the present invention, as long as such paperboard products comprise suitable amounts of moisture to act as a blowing agent for the LDPE (as discussed in more detail herein) and has suitable surface properties to provide adequate adhesion between the foam and the paperboard surface.
  • LDPE blowing agent for the LDPE
  • coated unbleached Kraft paperboard could be used in the present invention.
  • recycled paperboard either or both of pre- or post-consumer recycled
  • the LDPE contains no added adhesive material, such as a maleic anhydride graft copolymer or other type of adhesive polymer.
  • the adhesion of the LDPE to the paperboard occurs by way of adhesion of the LDPE coating to the paperboard. This is a physical attachment of the extruded LDPE to the surface of the paperboard by the LDPE component itself.
  • the paperboard surface must be somewhat rough to provide adequate points of attachment of the LDPE. Some surface roughness is believed to provide more surface area for contact of the LDPE coating to the paperboard surface.
  • board surface roughness is only one factor that influences adhesion of the LDPE to the paperboard surface.
  • the extruded LDPE coating is attached to the paperboard surface firmly, it will be appreciated that when foam is generated, the LDPE will be attached to the paperboard surface in a markedly different manner than a LDPE extrusion coating. That is, when an extruded coating of LDPE is applied to a surface to provide a laminate (such as in a coated packaging material), substantially the entire inner surface of the LDPE will be coextensive with the corresponding surface of the paperboard. When foam is prepared from this LDPE coating, the LDPE will be attached to the paperboard in a much less extensive manner because the air voids defining the foam cells represent a loss of contact for the LDPE coating.
  • the adhesion of the LDPE to the paperboard surface can be improved by applying a surface treatment to the paperboard surface prior to extrusion of the LDPE onto the paperboard surface.
  • the paperboard can be subjected to a corona treatment prior to extrusion of the LDPE.
  • Chemical treatments that provide oxidation effects to the paperboard surface can also be used to promote adhesion.
  • a tie layer can be applied to the paperboard surface to improve the adhesion of the LDPE to the paperboard. Suitable tie layer materials can be identified by one of ordinary skill in the art without undue experimentation.
  • the thickness of the paperboard material is not particularly significant to the resulting foam qualities.
  • paperboard having a wide range of thicknesses can be used to prepare the foam-paperboard laminates of the present invention.
  • thicknesses can be used to prepare the foam-paperboard laminates of the present invention.
  • paperboard of from about 10 to about 50 mils, or from about 15 to about 30 mils can suitably be used herein.
  • the thickness of the resulting foam-paperboard laminates of the present invention will be dictated in large part by the thickness of the paperboard used, since the thickness of the foam-paperboard laminates comprises the sum of the thickness of the foam and the paperboard used.
  • the basis weight of the paperboard suitably used in the present invention is not believed to significantly effect the properties of the resulting foam-paperboard laminates.
  • the basis weight of the paperboard used is generally dictated by the desired end use for the foam-paperboard laminates. For example, if the foam-paperboard laminate is to be used to prepare beverage cups, a desirable basis weight for the paperboard is from about 100 to about 220 pounds per ream or from about 140 to about 180 pounds per ream. If the foam-paperboard laminate is to be used to prepare disposable plates or containers, a desirable basis weight for the paperboard is from about 100 to about 280 pounds per ream or from about 160 to about 220 pounds per ream. Suitable further paperboard basis weights can be determined by one of ordinary skill in the art without undue experimentation.
  • the paperboard used must comprise a suitable amount of moisture in the paperboard prior to heating so as to allow enough steam to escape from the paperboard, so as to operate as a blowing agent for the LDPE to result in foaming.
  • the amount of moisture is highly significant to the qualities of the resulting foam.
  • the amount of moisture in the board should be from about 4 to about 10%, as measured by the weight of the board.
  • the amount of moisture in the board can be from about 5 to about 7%, as measured by the weight of the board.
  • the amount of moisture can be from about 4, 5, 6, 7, 8, 9 or 10% as measured by weight of the board, where any value can form an upper or a lower endpoint, as appropriate.
  • any suitable extrusion equipment can be used to coat the paperboard; for example, one suitable coating apparatus is an Egan 34 (Egan, Sommerville, N.J.) extrusion coater provided with a 36 inch wide EDI die having a multi-layer configuration with a screw feeding a Cloeren combining block.
  • Egan 34 Egan, Sommerville, N.J.
  • LDPE having the properties set forth above is extruded onto a paperboard having the features discussed previously.
  • a number of parameters have been found to be significant to provide foam-paperboard laminates having good foam qualities.
  • Various extrusion parameters are believed to significantly affect the resulting orientation of the LDPE coating prior to foaming.
  • the inventors herein have determined that the significant extrusion parameters comprise at least: die gap, air gap (h), rotational speed i.e., speed of the polymer exiting the die (v 0 ) and web speed (v 1 ). These parameters have been found to affect foaming level through the elongational strain, ⁇ , that the polymer experiences upon extrusion, which is believed to be due to machine direction (“MD”) molecular orientation.
  • MD machine direction
  • the inventors herein believe that in order to improve foam caliper and foam cell quality, the elongational strain of the LDPE polymer must be minimized.
  • elongational strain can be minimized through use of a LDPE having a MI of greater than about 8.0 when the extrusion process is conducted at speeds of greater than about 350 feet per minute.
  • MI the amount of elongational strain when modifying several extrusion parameters.
  • these extrusion parameters were found to be useful even when using LDPE having MI's of greater than about 8.0.
  • Ratio of Web Speed to Rotational Speed ( v 1 v 0 ) ⁇ The ratio of screw rotational speed to web speed has been found to affect the draw-down of the LDPE as it is exits the extruder. In relation to the foam aspect of the foam-paperboard laminates of the present invention, it has been found that increasing this ratio (that is extruding a higher volume of LDPE onto the paperboard surface while keeping web speed constant) will increase the flexural stiffness of the LDPE layer which, in turn, will create more resistance to foaming. Thus, the screw rotational speed must be considered in the present invention so as to obtain a suitable coat weight at a desired web speed to obtain good quality LDPE foams.
  • Die Gap and Air Gap The inventors have also determined that reducing die gap reduces the draw down ratio of the LDPE and, consequently, the elongational strain of the LDPE. Without being bound by theory, it has been determined that increasing the air gap allows more time for molecular relaxation prior to reaching the extruder nip. This is believed to result in less orientation in the polymer, which, in turn, results in better foaming under the conditions of the in situ foaming process.
  • the air gap (the distance between the extruder nip and the web) can be from about 9 to about 20 inches, or from about 10 to about 13 inches. Still further, the air gap can be from 9, 10, 11, 12, 13, 14, 15, 17 or 20 inches, where any value can serve as an upper or lower endpoint, as appropriate.
  • the extruder die gap can be from about 10 to about 25 mils or from about 13 to about 17 mils, where any value can serve as an upper or lower endpoint, as appropriate. Yet further, the extruder die gap can be from about 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 22 or 25 mils, where any value can serve as an upper or lower endpoint, as appropriate.
  • a smaller die gap can reduce the propensity of the LDPE polymer chains to align during the extrusion process, thereby generally increasing the number of amorphous regions in the LDPE extruded coating. This, in turn, is believed to result in a “softer” LDPE extruded coating, which improves the foamability and adhesion of the LDPE polymer when subjected to the conditions of the in situ process.
  • Polymer thickness It has been found by the inventors herein that increasing the thickness of LDPE extruded on paperboard decreases the draw down ratio (when all other variables are kept constant), which has been found to reduce residual polymer stress in the extruded LDPE coating prior to foaming. It has been also found by the inventors herein that thicker LDPE coatings exhibit higher flexural stiffness, which generally inhibits foam formation. These two parameters should be considered when preparing the foam-paperboard laminates of the present invention.
  • the extruded coat weight can be less than about 30 pounds per ream to obtain suitable foam.
  • the coat weight can be less than about 27 pounds per ream.
  • the coat weight is from about 15 to about 27 pounds per ream.
  • the coat weight is at least about 15, 17, 19, 21, 23, 25 or less than about 27 pounds per ream, where any value can serve as an upper or lower endpoint, as appropriate. Note that the coat weight values assume that the polymer is evenly applied to the surface of the paperboard.
  • Extrusion Melt Temperature It is believed that increasing melt temperature increases LDPE temperature at the extruder nip. Such higher LDPE temperature is believed to result in better adhesion of the LDPE extruded coat to the paperboard surface. This is further thought to improve adhesion. In addition, at higher temperatures, it is believed that there is an increase in polymer chain relaxation and a reduction in elongational strain.
  • the melt temperature of the LDPE can be from about 550 to about 650° F. or from about 580 to about 620° F.
  • a significant aspect of the present invention is that using LDPE having the specified characteristics and methods of the present invention, the web speed can be run significantly faster than in the prior art, while still obtaining an excellent foam qualities in the foam-paperboard laminates of the present invention.
  • the web speed is greater than about 325 feet per minute. Yet further, the web speed is greater than about 350 feet per minute. Still further, the web speed is from about 350 to about 900 feet per minute.
  • the web speed can be about 325, 350, 400, 450, 500, 550, 600, 650, 700, 750, 800, 850 or 900 feet per minute, where any value can be used as an upper or lower endpoint, as appropriate.
  • foam for use to prepare LDPE foam is typically prepared by adding chemical blowing agent or physical blowing agent.
  • the only known use of the in situ process herein is the PerfecTouch® beverage cups process conducted by the assignee of the present invention.
  • the blowing agent for the LDPE coating results from the creation of steam (evaporation of water from the paperboard).
  • steam evaporation of water from the paperboard.
  • the LDPE-coated paperboard material having the stated amount of moisture are placed in an oven to provide the foam.
  • the oven temperatures can be from about 200 to about 330° F. Yet further, the oven temperatures can be from about 245 to about 275° F.
  • the residence time (that is, the time the LDPE-coated laminate is subjected to heat so as to provide the foam) can be from about 30 to about 120 seconds. Yet further, the residence time can be 60 to about 90 seconds. In order to provide a high speed generation of the foam, it can be desirable to decrease the residence time of the LDPE-coated paperboard material. Keeping all variables the same, the residence time can be decreased by increasing the oven temperature. However, as discussed elsewhere herein, while higher oven temperatures result in a quicker formation of steam and, accordingly, a faster activation of the coating, if the LDPE-coated paperboard material is heated too quickly, the resulting foam quality often will be unsuitable. Thus, the oven temperature must be moderated so as to provide suitable quality foam.
  • this material can be used immediately to prepare the foam-paperboard laminate of the present invention.
  • the LDPE-coated paperboard can be stored for later preparation of the foam-paperboard laminate as long as the paperboard retains or is provided with suitable moisture prior to the foaming process.
  • the above-stated percentages of moisture are relevant when the paperboard surface opposite the LDPE-coated paperboard surface is provided with an occlusive layer.
  • an occlusive layer of a polyolefin such as a blend of LDPE and HDPE, can be extruded onto one side of the paperboard.
  • This HDPE-coated inner surface will become the side of the cup that is in contact with the liquid during use.
  • the HDPE layer prevents the moisture in the paperboard from exiting the paperboard through the HDPE-coated surface. A pressure build up also happens at this time.
  • the inner surface of the paperboard is so coated with an occlusive layer (which can also be other polymeric material, wax, etc.)
  • the previously stated amount of moisture e.g. about 4 to about 10% by weight of the board
  • the individual foam cells comprising the foam-paperboard laminates of the present invention can be from about 40 to about 150 square microns on average. Still further, the individual foam cells comprising the foam-paperboard laminate of the present invention can be from about 40, 50, 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 170, 180, 190 or200 square microns on average, where any value can form an upper or a lower end point, as appropriate. Yet further, at least about 90% or at least about 95% of the individual foam cells conform to the specified size range. It would be understood that small foam cells are not thought to be undesireable, as long as the aspect ratios were as set forth herein.
  • more than about 90% of the foam cells comprise an elongate structure extending away from the paperboard, wherein their aspect ratio is greater than about 2, with less than about 10% of the cells are in the form of large cells having that have aspect ratios of less than 2.
  • “Aspect ratio” means the ratio of the height of the foam cells divided by the average horizontal span of the cell over a single sample of foam-paperboard laminate.
  • an aspect ratio of greater than about 2 means that the height of the foam cells is at least about 2 times the width of the cells.
  • 5% or less of the foam cells have aspect ratios of less than about 2.
  • Further suitable foams can have a regular microstructure wherein the cells have an average MD ratio of less than about 1.5 or less than about 1.25.
  • MD ratio is the length of the cell in the machine direction as observed by surface SEM, divided by the length of the cell in the cross machine direction as observed by surface SEM.
  • Unrestrained MD linear thermal shrinkage resistance at 110° C. is determined in accordance with ASTM test method, ASTM 2732-03, except that thermal shrinkage resistance at 110° C. is reported as a percent of the original length of the specimen. For example, a specimen having a 100 mm length prior to immersion in the heated bath and a MD length of 90 mm after immersion for 10 seconds has an unrestrained MD linear thermal shrinkage resistance of about 90%. This parameter is believed significant in connection with foam quality of foams produced from the extruded LDPE as will be appreciated from the discussion which follows hereinafter. It will be appreciated also from the data that follows that the shrinkage resistance is sensitive to the speed at which the board web is traveling in the machine direction as well as other variable as the LDPE coating is applied. In general, a MD shrink value of from about 80% to up to about 100% provides a good quality foam (where 100% represents no shrinkage and, therefore, substantially no orientation in the extruded LDPE coating).
  • a sample of foam-paperboard laminate for shrink resistance testing may be obtained by placing a Kevlar or other LDPE coating on the paperboard prior to extrusion so that a foam sample can readily separate from the paperboard.
  • a sample may be removed from coated board by sulfuric acid solution. If a sample is to be obtained by way of sulfuric acid solution, a MD specimen is cut using a 6 inch by 1 ⁇ 2 inch die cutter. The paperboard is split in half exposing the paper fibers and only the half that has the extruded LDPE is retained. The sample is placed in an 800 ml beaker covered with 72 percent H 2 SO 4 aqueous solution and let stand for five to eight hours with occasional stirring. The sample is washed with tap water and dried prior to shrink resistance testing.
  • the foam surface of the foam-paperboard laminates of the present invention can be printed with ink or mineral oil, for example, in order to provide designs which are attractive and can mimic, for example, embossments or debossments.
  • U.S. patents the disclosures of which are incorporated herein in there entireties by this reference: U.S. Pat. No. 5,490,631 to Iioka et al.; U.S. Pat. No. 5,725,916 to Ishii et al.; U.S. Pat. No. 5,766,709 to Geddes et al.; U.S. Pat. No. 5,840,139 to Geddes et al.; U.S. Pat.
  • the foam-paperboard laminates of the present invention are suitable for use in a number of different applications.
  • a significant use is for insulating beverage cups sold commercially by the assignee of this invention as PerfecTouch.
  • the processes and methods used to prepare such cups are disclosed in detail in the following U.S. patents (the disclosures of which are incorporated herein in their entireties): U.S. Pat. No.6,129,653 to Fredericks et al.; U.S. Pat. No. 6,416,829 to Breining et al.; U.S. Pat. No. 6,482,481 to Fredericks et al.; U.S. Pat. No. 6,565,934 also to Fredericks et al.; U.S. Pat. No.
  • sealing of the cups can be facilitated by doping of the LDPE layer with an amount of HDPE, where the inner layer is coated with HDPE to serve as an occlusive layer.
  • the occlusive coating and the foamable coating are both LDPE-based, the two coatings will adhere well to one another when melt-bonded.
  • the modified LDPE containing HDPE will not foam under conditions utilized to foam the LDPE outer coating.
  • doping is also believed to be feasible when the foam-paperboard laminates of the present invention are to be converted into, for example, packaging materials, such as boxes or other types of structures having edges or surfaces that are adhered together.
  • FIGS. 1 and 1 a There is shown in FIGS. 1 and 1 a a paperboard cup 10 which includes a bottom panel 12 as well as a sidewall 14 and a curled brim 16 .
  • Bottom panel 12 has a polymer occlusive layer 18 which may be a blend of LDPE and HDPE, for example, as well as paperboard layer 20 .
  • the bottom side of paperboard layer 20 of panel 12 does not have a occlusive layer since it is not typically foamed.
  • the various layers are particularly concentrated in the area of attachment of the sidewall and bottom panel. This structure becomes even more complex in the area of a seam as well be appreciated by one skilled in the art.
  • the occlusive layer 18 is predominantly a blend of LDPE/HDPE and the foam layer 22 of sidewall 14 consists essentially of LDPE such that the two layers will readily melt bond when they come in contact at a seam (not shown).
  • sidewall 14 includes a foamed layer 22 which comprises an in situ foamed LDPE coating.
  • Sidewall 14 also comprises a paperboard layer 24 as well as a occlusive layer 26 on its inner surface.
  • Layer 26 is suitably a modified LDPE which incorporates about 10% by weight of HDPE.
  • Any suitable polymer composition suitably one which does not foam under conditions used to foam the in situ foamed coating on the outside of the cup, may be used as the occlusive layer.
  • the foam-paperboard laminates of the present invention have a number of utilities.
  • the foam-paperboard laminates of the present invention can be used as containers for take-out food items, such as hamburger or sandwich “clamshells.”
  • the foam-paperboard laminates of the present invention can also be used as a substitute for polystyrene foam take out containers.
  • the insulating qualities of the foam-paperboard laminates of the present invention are believed to be suitable for use in hot food applications.
  • the foam-paperboard laminates of the present invention comprise primarily paperboard material, they are compostable. In the foodservice area where foam waste is generally undesirable, the foam-paperboard laminates of the present invention would be quite desirable.
  • the foam-paperboard laminates provide utility for types of packaging where insulation is desirable.
  • the foam-paperboard laminates of the present invention can be used to package frozen food, such as ice cream, vegetables, dinners, pizzas, meats and the like.
  • the foam-paperboard laminates are heat resistant, the foam-paperboard laminates can be used to heat the frozen food for end use.
  • the foam-paperboard laminates can also be used for refrigerated food where insulation is desirable, such as a wrapper for butter, cheese and the like.
  • the insulating character of the foam-paperboard laminates also make them suitable for use as insulating sleeves for hot beverages.
  • Such an example is a hot cup sleeve.
  • the foam-paperboard laminates are also grease and fat resistant due to the polymeric nature of the coating, which also makes these materials suitable for packaging products such as butter, cheese and the like.
  • the foam-paperboard laminates can also be used as an insulating sleeve or box to assist in transporting frozen or refrigerated goods.
  • the insulating sleeve or box can be used to transport hot and cold items from the grocery store to a residence by a consumer or the like.
  • the cushion characteristics of the present invention make the foam-paperboard laminates of the present invention suitable for use in packaging materials where cushioning is desirable.
  • the foam-paperboard laminates can be used as cushioning for fragile items, such as plates or other dishware.
  • the foam-paperboard laminates can also be used as cushioned shipping envelopes, such as for transporting CD's or photos or the like.
  • the foam-paperboard laminates can also be used as a cushioning or insulating material inside of a packaging material.
  • the cushioning material will provide protection against scuffing or marring of easily damaged products.
  • the foam-paperboard laminates of the present invention can also be used in any application where a fairly thin foam laminate made from plastic has been used previously. Since the foam-paperboard laminates of the present invention are compostable, it would be expected that these inventive materials will have utility when it is desirable to reduce plastic waste. When coated with a barrier material, such as HDPE, the foam-paperboard laminates can be expected to function well as disposable products even in moist environments. To this end, the foam-paperboard laminates of the present invention can be used as shoe inserts, sandals or the like.
  • the foam-paperboard laminates of the present invention can be useful in applications where it is desirable to increase the slip-resistance of an item.
  • the foam-paperboard laminates can be used in preparing slip-resistant beverage cartons or in other applications where grippability is desirable.
  • the foam-paperboard laminates of the present invention can be used as foodservice containers for greasy foods, such as popcorn or fried chicken.
  • the textured surface of the container assists in holding thereof if the outer surface of the container becomes greasy.
  • the coated container is resistant to grease, thus making the container substantially impermeable to the greasy food inside the container.
  • the foam-paperboard laminates of the present invention has an appearance that can be described as “pearlescent” or “opalescent.” Such an appearance lends itself to premium packaging materials where aesthetic desirability is highly valued. To this end, the foam-paperboard laminates of the present invention are suitable for use in “high end” packaging materials where insulation or cushioning are not readily needed. Such potential applications include perfume and/or jewelry packaging.
  • the foam-paperboard laminates can also be used as a disposable cutting board due to the cut resistance of the foam.
  • the foam-paperboard laminates can also be used as a disposable trivet due to its heat resistant qualities.
  • the foam-paperboard laminates can also be used to store knives safely.
  • the foam-paperboard laminates can be used as shelf liner, place mat, wall covering, acoustic barrier for wall or floor, floor mat and polishing material.
  • foam-paperboard laminates of the present invention additional components besides the primary polymer materials can be added; such as stabilizers, nucleants, fillers, compatible blended in polymers and so forth, so long as the additional ingredients do not change the basic and novel characteristics of the foam-paperboard laminates, that is, its ability to be foamed in situ.
  • polymers such as LDPE or HDPE may contain amounts of co-monomers in addition to ethylene which is the predominant monomer.
  • the foam-paperboard laminates used to form sidewall 14 includes paperboard layer 24 , barrier layer 26 and a foamable coating layer 22 a.
  • the foam-paperboard laminates can be produced on an apparatus shown schematically in part in FIG. 2 .
  • the structure of the foam-paperboard laminates prior to foaming is shown in FIG. 2 a.
  • Coating station 30 including a coating nip 32 defined between a support roll 34 and a chill roll 36 .
  • Coating station 30 also includes an extruder 38 feeding a slit die 40 which has a die gap or width indicated at 42 .
  • the die is located at height 44 (also referred to as air gap 44 ) above the center of nip 32 as shown in the diagram.
  • a web 50 of paperboard 24 is fed to the nip in the machine direction as shown by arrows 25 while a curtain 32 of molten LDPE is fed from die 42 on to the board.
  • Chill roll 36 cools the polymer as it adheres to the board.
  • the curtain 52 thus becomes a foamable LDPE layer 22 a as shown in FIG. 2 a.
  • LDPE paperboard samples were prepared and foamed in situ at a temperature of about 130° C. for from about 1 minute to about 2 minutes.
  • the paperboard used had a thickness of about 15 mils.
  • the paperboard was extrusion-coated on one side with 90% LDPE/10% HDPE at about 5 pounds per ream. This coating had a thickness of about 0.4 mils.
  • the other side of the paperboard was extrusion-coated with LDPE at from about 18 and about 35 pounds per ream using different web speeds, air gaps, die gaps, melt temperatures and polymers of different melt indices as set out in more detail below.
  • FIGS. 3 through 6 Photomicrographs of foamed composites appear in FIGS. 3 through 6 .
  • FIG. 3 a foam-paperboard laminate is shown that was coated as noted above and subsequently foamed at approximately 130° C. in an oven for about I to 2 minutes.
  • the foamable LDPE used in FIGS. 3 and 4 was 5.7 g/10 min MI LDPE.
  • the sample in FIG. 3 was coated at 200 ft/min, whereas the sample shown in FIG. 4 was coated at a web speed of 450 ft/min. It will be appreciated from the photomicrographs that the foam of FIG.
  • the aspect ratio referred to here is the height of the cell away from the paperboard divided by its average width (horizontal or parallel to the board).
  • FIG. 4 it is seen that the paperboard that was extrusion coated with LDPE at higher speed without optimized extrusion conditions resulted in foam having an irregular pattern.
  • the foam appears as large macrovoids which appear to comprise agglomerated or merged cells that have are quite large and have a low aspect ratio. These macrovoids have horizontal spans much larger than the remainder of the foam.
  • FIGS. 5 and 6 are photomicrographs of samples of LDPE with a MI of 5.7.
  • the sample of FIG. 5 was coated at 200 ft/min prior to foaming, whereas the sample in FIG. 6 was coated at a web speed of 450 ft/min.
  • the foam prepared from a MI of 12.0 had a generally regular structure consisting essentially of higher aspect ratio foam cells.
  • FIG. 7 a plot of caliper after foaming in mils versus the LDPE coat weight in pounds per ream at different coating speeds for the 5.7 MI polymer utilizing an air gap of 11 inches and 20 mil extruder die gap. It is seen in FIG. 7 that the 5.7 MI LDPE deposits coated at 300 ft/min generally had a higher caliper after foaming than did the paperboard coated at 450 ft/min at a coat weight above about 22 pounds per ream. It is also seen in FIG. 7 that a decrease in melt temperature during coating adversely affected caliper at any LDPE coat weight.
  • FIG. 8 is another plot of caliper of the foam-paperboard laminates after foaming in mils versus extruded LDPE coat weight in pounds per ream. Here it is also seen that lower melt temperatures also decreased caliper generally, all other things being equal.
  • FIG. 9 is another plot of caliper after foaming versus polymer coat weight in pounds/reams for the 5.7 MI LDPE. It is confirmed in FIG. 9 that the higher melt temperatures produced a higher caliper, up to a LDPE coat weight of about 28 pounds per ream.
  • FIG. 10 is another plot of caliper after foaming in mils versus LDPE extrusion coat weight in pounds per ream for 5.7 MI LDPE at optimized die gap and air gap conditions.
  • relatively high calipers are achieved with low coat weight. This is an unexpected and very useful result; especially with increasing polymer costs.
  • FIG. 11 is a plot of caliper after foaming for the 13.7 MI LDPE.
  • the effect of coat weight on foam caliper is more significant.
  • the higher melt index polymer produced surprisingly high caliper in situ foam-paperboard laminates at lower coat weights.
  • this higher melt index polymer foamed well when coating at web speeds of up to about 450 fpm were used. Previous experiments had shown that higher web speeds resulted in a degradation of foam height and quality.
  • FIG. 12 is a plot of caliper after foaming of the foam-paperboard laminates versus coat weight for a 4.5 MI LDPE tested. Here is seen that the calipers were quite low as opposed to the higher melt index polymers, regardless of coat weight.
  • FIG. 13 is another plot of caliper after foaming of the foam-paperboard laminates versus coat weight for a LDPE having a MI of about 12.0.
  • high calipers were achieved with coat weights below 25 pounds per ream at web speeds of 300 feet per minute and 450 feet per minute.
  • FIG. 14 is a plot of average caliper after foaming of the foam-paperboard laminates versus polymer melt index in g/10 min.
  • the LDPE coat weight of this example was 25 pounds per ream.
  • FIG. 15A is a surface SEM of a foamed composite wherein the foamed coating was produced from 5.7 MI LDPE extrusion coated a coat weight of 30 pounds per ream.
  • the LDPE was applied to the board at a web speed of 450 feet per minute using a 40 mil die gap and 5′′ air gap. It is seen in FIG. 15A that the foam cells have considerable MD ratio, that is, are elongated in the machine direction when viewed from top to bottom in the photograph.
  • FIG. 15B (comparative) is a view in section of the foam layer of FIG. 15A , wherein the cross machine direction is from left to right and wherein it is seen that the foam is irregular, with large foam cells of low aspect ratio.
  • FIG. 16A is a surface SEM of a foamed composite sample using the same 5.7 MI LDPE as in FIGS. 15A and 15B at the same coat weight and coating speed, however, the air gap was increased to 9′′ and the die gap reduced to 20 mils. Here there is seen much less MD ratio (top to bottom in the photograph) elongation of the foam cells.
  • FIG. 16B is an SEM in section of the foam of FIG. 16A (cross machine direction left to right) and it is seen that the foam microstructure is considerably more regular.
  • FIGS. 17A through 20B further illustrate the influence of polymer selection and coat weight on the resulting foam-paperboard laminates.
  • FIGS. 17A, 18A , 19 A and 20 A are surface SEMs wherein the machine direction of the paperboard web is from top to bottom
  • FIGS. 17B, 18B , 19 B and 20 B are SEMs of foam sections, wherein the cross machine direction of the coated web is from left to right.
  • Polymers utilized in each case and coating conditions are indicated in Table 14 below. In all cases the die gap was 20 mils.
  • FIGS. 17A and 17B it is seen that good quality coatings are produced with the 5.7 MI LDPE using a large air gap, a small die gap and a coating speed of 450 feet per minute.
  • FIGS. 18A and 18B that good quality coatings are produced under similar conditions with the 13.7 MI LDPE.
  • FIGS. 19A and 19B it is seen that under these conditions, the 4.5 melt index LDPE would not foam properly; there were large areas of unfoamed polymer.
  • FIGS. 20A and 20B it is seen in FIGS. 20A and 20B , that the 12.0 MI LDPE produced excellent in situ foamed coatings from extruded coatings coated at 450 fpm.
  • the present invention was tested at a commercial facility in order to confirm that manufacturing speeds could be increased in accordance with the invention.
  • Composite production speeds were increased to 400 fpm.
  • Air gap was increased, die gap and coat weight were decreased in order to achieve the incremental production.
  • the melt temperature of the LDPE has been found to strongly influence ultimate foam quality, reinforcing the qualitative observation that coatings that were strongly adhered to the paperboard tended to produce better foams.
  • Methods of promoting adhesion that might be employed include increasing coat weight, increasing melt temperature or treating the paperboard surface (by corona treatment, for example). While a precise threshold of adhesion for superior foaming may vary depending on the materials and conditions employed, it is believed that the more contact points between the foamed coating and the paperboard substrate, the better the foam quality and less material required for a given thickness. More contact points likely exist after foaming of the LDPE if the coating is strongly adhered prior to foaming.
  • melt index and coat weight results suggest that resistance to flow in the polymer coating as it is foamed in situ plays an important role as well.
  • Higher melt index foams are unexpectedly superior, when all other variables are kept constant.
  • Thinner coatings (especially thinner higher melt index coatings) tend to foam better than like thicker coatings, producing thicker coatings at lower coat weight.
  • effects of melt rheology are important and may override any adverse effect on adhesion by lowering the coat weight, provided that adhesion is adequate.
  • the coat weight effect on in situ foaming may be related to stiffness of the unfoamed coating that is strongly related to caliper. Bending stiffness is generally proportional to the caliper of a coating to the third power.
  • coat weights of less than about 25 pounds per ream are possible with weights of from about 20 to about 25 pounds per ream being suitable to obtain good quality foam (that is, high aspect ratio foam with good adhesion).
  • This coat weight is markedly below the coat weight of the prior art in situ process where a coat weight of around 30 pounds per ream were specified.
  • the surface of cups having in situ formed LDPE foamed coatings prepared as discussed above were laser-profiled using the Taylor Hobson—Talysurf CLI 1000 Scanning Laser Profilometer fitted with a 10 mm triangulation gauge.
  • a surface 5 mm by 5 mm was collected using a lateral resolution of 5 ⁇ m in both the MD and CD directions and a gauge resolution of 0.17 ⁇ m.
  • the samples were oriented with the X axis corresponding to the machine direction (stock curvature in the cross-machine direction).
  • each sample dataset was processed with standard software as follows: 1.) missing data was filled using a technique employing a morphological dilation operation and substitution based on interpolation of a smoothed shape calculated from the neighborhood of the missing points; 2.) stock curvature was removed by fitting a 2nd order polynomial to the surface; 3.) the Z-axis was inverted in order to present the data a positive image; 4.) The dataset was spatially filtered (median 3 by 3 kernel) to eliminate ultra-fine scale texture.
  • the texture aspect ratio, Str assumes values between 0 and 1, with 1 representing an isotropic surface.
  • “Isotropy” as that term is used herein refers to the laser Str value measured as described above, or may be expressed in percent (Str ⁇ 100%). For example, a sample with an Str value of 0.75 has an isotropy of 0.75 or 75%.
  • Texture direction, Std assumes values between ⁇ 90 and 90 with 0 aligned with the cross-machine direction. This parameter has meaning when Str assumes values less than 0.5.
  • Planarity was assessed by the magnitude of the developed surface, Sdr. This parameter will assume a value of 0% for a flat surface: the more convoluted the surface, the higher the value of Sdr.
  • the density of peaks, SPc measures the number of peaks per square millimeter that extend above C2 and below C1. Both C2 and C1 are expressed relative to the surface mean plane. Default values of 0.01 mm and 0.001 mm were used for C2 and C1, respectively. This parameter measures the uniformity of the surface relative to the specified thresholds C2 and C1.
  • FIG. 21A is a laser scanned surface image of the in situ foam surface of sample 46 (4.5 MI, 450 fpm) showing large, irregular cells.
  • FIG. 21B is an angular plot showing that isotropy is quite low.
  • FIG. 22A is a laser scanned surface image of the foam of sample 50 (MI 12, 450 fpm) showing a much finer microstructure than that of FIG. 21A .
  • FIG. 22B is an angular plot showing a much more isotropic surface than is the case in FIG. 21B ; confirming the results seen in Table 15 and the accompanying photomicrographs.
  • FIG. 23 shows foam caliper as a function of coat weight for 5.7 MI LDPE (Westlake EC 479) polymer at two different extrusion speeds and two different melt temperatures.
  • the results confirmed that increasing melt temperature had a positive effect on foam caliper.
  • the inventors herein therefore determined that increasing the temperature at which the polymer exits the die (extrusion melt temperature) improved foam caliper by increasing micro-level adhesion as well as allowing for molecular relaxation.
  • the melt temperature needs to be below the decomposition temperature of the polymer.
  • Foam caliper increased as LDPE coating thickness (as measured by coat weight) increases. However, foam caliper reached a maximum at a certain thickness and decreased at higher LDPE coating thickness. This is believed to be the result of two opposing forces: the lower the coating thickness, the lower the flexural stiffness of the coating and the easier it is to deform. However, as coating thickness was decreased, the draw down ratio increased, thus resulting in higher residual stress in the extruded LDPE coating and reducing foam caliper.
  • the inventors herein investigated the LDPE extruded coating properties significant to foam formation. These were found to include: lower stiffness, higher draw ability and higher melt strength.
  • FIG. 24 shows that for the 12.0 MI LDPE and the 13.7 MI LDPE polymers, web speed did not influence foam caliper as seen with the 5.7 MI LDPE polymer having the lower MI.
  • 13.7 MI LDPE polymer provided a higher foam caliper at equivalent web speed and extruded coat thickness when compared to the lower MI 12.0 MI LDPE polymer.
  • the inventors proceeded to investigate both the 12.0 MI LDPE and 13.7 MI LDPE polymers and to test these polymers in a manufacturing environment. Converting trials at a Georgia-Pacific extrusion facility validated the lab scale experimental results.
  • the 12.0 MI LDPE polymer produced target foam caliper of about 30 mil (paperboard and foam) at only 25 pounds/ream of LDPE while the 13.7 MI LDPE polymer produced target foam caliper with only 20 pounds/ream of LDPE.
  • these manufacturing scale results indicated that it was possible to obtain good foam qualities through use of a lighter extruded coat weight of LDPE.
  • the inventors examined the effects of oven parameters on resulting foam caliper in order to gain a better understanding of the foaming mechanism inside the oven and to identify a process to produce consistent foam appearance.
  • the oven residence time tested ranged from 60 seconds to 180 seconds and the temperature ranged from 235° F. to 265° F. (Previous manufacturing conditions were 255° F. oven temperature and residence time of 120 seconds using 5.7 MI LDPE). Results of R&D foam caliper measurements for the three polymers are shown in FIGS. 25 to 27 .
  • FIGS. 25-27 show that it is possible to decrease oven residence time if oven temperature is correspondingly increased. However, it was necessary to understand the limitations of increasing oven temperature and its affects on foam caliper and appearance.
  • FIGS. 28-30 should be interpreted with care.
  • the 13.7 MI LDPE polymer reached higher foam caliper than the 12.0 MI LDPE polymer, which had higher caliper than the previously used LDPE polymer having a MI of 5.7.
  • all LDPE polymers tested reached a maximum caliper at a certain residence time, which depended on the type of polymer and the temperature of the oven. For example, for the 12.0 MI LDPE polymer, the maximum caliper at the lower oven temperatures of 265° F. and 275° F. was reached after 60 seconds. This time is reduced to 45 seconds for the 285° F. and 300° F. oven temperature.
  • oven residence time can be significantly reduced if the oven temperature was increased.
  • the inventors herein found that foam appearance and insulation levels can be adversely affected by an increase in temperature.

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EP1901921A1 (en) 2008-03-26
DE602006012488D1 (de) 2010-04-08
HK1120244A1 (en) 2009-03-27
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ATE458608T1 (de) 2010-03-15
CA2611417A1 (en) 2006-12-28

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