Packaging sheet for elevated-temperature use
10384854 ยท 2019-08-20
Assignee
Inventors
Cpc classification
A47J27/002
HUMAN NECESSITIES
B32B1/00
PERFORMING OPERATIONS; TRANSPORTING
A47J36/027
HUMAN NECESSITIES
B32B2250/244
PERFORMING OPERATIONS; TRANSPORTING
A23V2002/00
HUMAN NECESSITIES
B65B25/22
PERFORMING OPERATIONS; TRANSPORTING
B32B3/08
PERFORMING OPERATIONS; TRANSPORTING
B65D81/3453
PERFORMING OPERATIONS; TRANSPORTING
B32B7/12
PERFORMING OPERATIONS; TRANSPORTING
B65D1/34
PERFORMING OPERATIONS; TRANSPORTING
B32B3/266
PERFORMING OPERATIONS; TRANSPORTING
B32B2307/54
PERFORMING OPERATIONS; TRANSPORTING
B65D77/20
PERFORMING OPERATIONS; TRANSPORTING
B32B7/02
PERFORMING OPERATIONS; TRANSPORTING
A23L5/15
HUMAN NECESSITIES
B32B3/20
PERFORMING OPERATIONS; TRANSPORTING
B32B3/02
PERFORMING OPERATIONS; TRANSPORTING
B32B2367/00
PERFORMING OPERATIONS; TRANSPORTING
B65B47/02
PERFORMING OPERATIONS; TRANSPORTING
International classification
B65D81/34
PERFORMING OPERATIONS; TRANSPORTING
B65D1/34
PERFORMING OPERATIONS; TRANSPORTING
B65D77/20
PERFORMING OPERATIONS; TRANSPORTING
A47J36/02
HUMAN NECESSITIES
A23L5/10
HUMAN NECESSITIES
B65B25/22
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A packaging sheet is described. The sheet comprises a first layer comprising a first copolyester having a glass transition temperature of from 70 C. to 90 C. and an intrinsic viscosity of from 0.70 dl/g to 0.90 dl/g. The first copolyester comprises from 50% to 85% by volume of the sheet. The sheet also comprises a second layer comprising a second copolyester having a glass transition temperature of equal to or greater than 112 C. The second copolyester comprises from 15% to 50% by volume of the sheet. The sheet is thermally stable after exposure to temperatures up to 112 C. Various embodiments of the sheet are also described.
Claims
1. A sheet comprising a first layer comprising a first copolyester having a glass transition temperature of from 70 C. to 90 C. and an intrinsic viscosity of from 0.70 dl/g to 0.90 dl/g, wherein the first copolyester comprises from 50% to 85% by volume of the sheet; a second layer comprising a second copolyester having a glass transition temperature of equal to or greater than 112 C., wherein the second copolyester comprises from 15% to 50% by volume of the sheet; wherein the sheet is thermally stable after exposure to temperatures up to 112 C.
2. The sheet of claim 1 wherein the first copolyester comprises APET.
3. The sheet of claim 1 wherein the second copolyester has a glass transition temperature of from 112 C. to 250 C.
4. The sheet of claim 1 wherein the first copolyester comprises from 50% to 85% by volume of the sheet and the second copolyester comprises from 15% to 40% by volume of the sheet.
5. The sheet of claim 1 wherein the first copolyester comprises from 70% to 85% by volume of the sheet and the second copolyester comprises from 15% to 30% by volume of the sheet.
6. The sheet of claim 1 wherein the sheet has a clarity after exposure to temperatures up to 112 C. that is substantially similar to a clarity before exposure to temperatures up to 112 C.
7. The sheet of claim 1 wherein the sheet has a haze after exposure to temperatures up to 112 C. that is substantially less than a haze after exposure to temperatures up to 112 C. over a similar time period of another sheet having a similar thickness and comprising the first copolyester but not comprising the second copolyester.
8. The sheet of claim 1 wherein the sheet has a stress at yield after exposure to temperatures up to 112 C. that is substantially greater than a stress at yield after exposure to temperatures up to 112 C. of another sheet having a similar thickness and comprising the first copolyester but not comprising the second copolyester.
9. The sheet of claim 1 wherein the sheet has a thickness of from 10 mil to 50 mil.
10. The sheet of claim 1 wherein the sheet is thermoformable.
11. The sheet of claim 1 wherein the sheet is thermoformed into a package.
12. The sheet of claim 1 wherein the sheet further comprises a third layer comprising the first copolyester and the second layer is positioned between the first layer and the third layer.
13. The sheet of claim 12 wherein the first layer and the third layer have a substantially similar thickness.
14. A tray comprising a thermoformed sheet comprising a first layer comprising a first copolyester having a glass transition temperature of from 70 C. to 90 C. and an intrinsic viscosity of from 0.70 dl/g to 0.90 dl/g, wherein the first copolyester comprises from 70% to 85% by volume of the sheet; a second layer comprising a second copolyester having a glass transition temperature of from 112 C. to 250 C., wherein the second copolyester comprises from 15% to 30% by volume of the sheet; a third layer comprising the first copolyester, wherein the second layer is positioned between the first layer and the third layer; wherein the first layer and the third layer have a substantially similar thickness; and wherein the sheet is thermally stable after exposure to temperatures up to 112 C.
15. The tray of claim 14 wherein the sheet has a thickness of from 20 mil to 40 mil.
16. The tray of claim 14 wherein the sheet has a haze after exposure to temperatures up to 112 C. that is substantially less than a haze after exposure to temperatures up to 112 C. over a similar time period of another sheet having a similar thickness and comprising the first copolyester but not comprising the second copolyester.
17. The tray of claim 14 wherein the tray is adapted to package a food product.
18. The tray of claim 17 wherein the food product comprises produce.
19. A method of cooking produce comprising providing a tray comprising a thermoformed sheet comprising (a) a first layer comprising a first copolyester having a glass transition temperature of from 70 C. to 90 C. and an intrinsic viscosity of from 0.70 dl/g to 0.90 dl/g, wherein the first copolyester comprises from 70% to 85% by volume of the sheet, (b) a second layer comprising a second copolyester having a glass transition temperature of equal to or greater than 112 C., wherein the second copolyester comprises from 15% to 30% by volume of the sheet, and (c) a third layer comprising the first copolyester, wherein the second layer is positioned between the first layer and the third layer and the first layer and the third layer have a substantially similar thickness; filling the tray with produce; and heating the filled tray in a microwave oven; wherein the tray is thermally stable after exposure to microwave heating.
20. The method of claim 19 wherein the sheet has a haze after exposure to microwave heating that is substantially less than a haze after exposure to microwave heating over a similar time period of another sheet having a similar thickness and comprising the first copolyester but not comprising the second copolyester.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
(11) Referring to the drawings, with some but not all embodiments depicted, with elements depicted as illustrative and not necessarily to scale, and with the same (or similar) reference numbers denoting the same (or similar) features throughout the drawings,
(12) As depicted in
(13) Polyesters are a class of polymers which have an ester linkage between monomer units. The ester linkage may be represented by the general formula [OROC(O)RC(O))].sub.n where R and R are the same or different alkyl (or aryl) groups and may generally be formed by the polymerization of diacids and dials. Homopolymer polyester is formed when the diacid is terephthalic acid (TPA) and the diol is ethylene glycol (EG). As used throughout this application, the term copolyester refers to a polyester that is polymerized using other diacids and dials instead of or in addition to TPA and EG. A commonly used diacid for copolyesters is isophthalic acid (IPA). Other diacids may be linear, aliphatic, aromatic, or alkyl substituted aromatic (such as IPA). Useful examples of dials used in copolyesters are diethylene glycol (DEG), cyclohexanedimethanol (CHDM), 2,2,4,4-tetramethyl-1,3-cyclobutanedial, and the like. Copolyesters useful for sheet or other packaging applications include but are not limited to amorphous polyester (APET) and polyethylene terephthalate glycol-modified (PETG).
(14) As described in the present application, the first copolyester has a glass transition temperature of from 70 C. to 90 C. As used throughout this application, the term glass transition temperature or T.sub.g refers to the temperature range over which a material transitions from a glassy state to a rubbery state (i.e., the temperature range over which a material softens). The glass transition temperature is, in actuality, a range. However, scientists have agreed to accept a single temperature as the indicator per certain standards, such as those associated with differential scanning calorimetry (DSC), thermomechanical analysis (TMA) and dynamic mechanical analysis (DMA). Glass transition temperature may be determined in accordance with ASTM D3418-15 (Standard Test Method for Transition Temperatures and Enthalpies of Fusion and Crystallization of Polymers by Differential Scanning calorimetry).
(15) The first copolyester also has an intrinsic viscosity of 0.70 dl/g to 0.90 dl/g. As used throughout this application, the term intrinsic viscosity refers to measure of the copolyester's molecular weight and therefore reflects the copolyester's melting point, crystallinity, and tensile strength. Intrinsic viscosity may be determined for the copolyester material itself (i.e., as a resin or pellet) or may be determined for the copolyester as a component in the sheet. As used throughout this application, the term intrinsic viscosity refers to the intrinsic viscosity of the copolyester in any form, i.e., as a resin/pellet or as a component in the sheet.
(16) An example of a first copolyester includes but is not limited to polyethylene terephthalate (PET) which is processed (as a non-limiting example, via extrusion quench process) to be amorphous or semi-crystalline. Such processed PET includes but is not limited to APET or bottle-grade APET. Examples of bottle-grade APET (i.e., PET which may be processed to be amorphous or semi-crystalline and which is typically used n blow-molding bottles), each of which has a glass transition temperature of from 70 C. to 90 C. and an intrinsic viscosity of from 0.70 dl/g to 0.90 dl/g, include but are not limited to Laser+ C 9921 (F65A) (having a reported intrinsic viscosity of 0.800.02 dl/g, a reported glass transition temperature of 78.0 C., and a reported nominal melt point of 238 C.), Laser+ C (E60A) (having a reported intrinsic viscosity of 0.810.02 dl/g and a reported nominal melt point of 246 C.), and Laser+ GP 2400 (B12A) (having a reported intrinsic viscosity of 0.840.03 dl/g and a reported nominal melting point of 243 C.), each of which is available from DAK Americas LLC (Chadds Ford, Pa.); Cleartuf 8006C (having a reported intrinsic viscosity of 0.800.02 dl/g and a reported melting point of 248.0 C.), which is available from M&G Polymers USA, LLC (Houston, Tex.); Preformance PET 1708 (having a reported intrinsic viscosity of 0.800.02 dl/g), which is available from StarPet Inc. USA (Asheboro, N.C.); Polyclear Crystal PET 3302 (having a reported intrinsic viscosity of 0.790.02 dl/g and a reported melting point of 248 C. maximum), which is available from Invista S.r.l. (Charlotte, N.C.); and PQB7-080 (having a reported intrinsic viscosity of 0.800.02 dl/g), which is available from PolyQuest, Incorporated (Wilmington, N.C.).
(17) As described in the present application, the second copolyester has a glass transition temperature of equal to or greater than 112 C. In some embodiments, the second copolyester may have a glass transition temperature of from 112 C. to 250 C. (approximately the upper limit of the melting point of the first copolyester). Examples of a second copolyester include but are not limited to Tritan copolyesters, which are available from Eastman Chemical Company (Kingsport, Tenn.). Non-limiting examples of a Tritan copolyester include Eastman Tritan Copolyester FX200, which is an amorphous copolyester having a reported density of 1.19 g/cc and a reported glass transition temperature of 119 C. (DSC) and Eastman Tritan Copolyester MP200, which is an amorphous copolyester having a reported density of density of 1.19 g/cc and a reported glass transition temperature of 119 C. (DSC).
(18) In some embodiments, the first copolyester comprises from 50% to 85% by volume of the sheet; in other embodiments, the first copolyester comprises from 60% to 85% by volume of the sheet; and in still other embodiments, the first copolyester comprises from 70% to 85% by volume of the sheet.
(19) In some embodiments, the second copolyester comprises from 15% to 50% by volume of the sheet, in other embodiments, the second copolyester comprises from 15% to 40% by volume of the sheet; and in still other embodiments, the second copolyester comprises from 15% to 30% by volume of the sheet.
(20) In some embodiments, the first copolyester comprises from 50% to 85% by volume of the sheet and the second copolyester comprises from 15% to 50% by volume of the sheet; in other embodiments, the first copolyester comprises from 60% to 85% by volume of the sheet and the second copolyester comprises from 15% to 40% by volume of the sheet; and in still other embodiments, the first copolyester comprises from 70% to 85% by volume of the sheet and the second copolyester comprises from 15% to 30% by volume of the sheet.
(21) As described in the present application, the first copolyester volume percent in the sheet (i.e., by volume of the sheet) and the second copolyester volume percent in the sheet (i.e., % by volume of the sheet) are the percent of the sheet as a whole, not the percent of a particular layer. The first copolyester may be in one layer or more than one layer of the sheet, and the second copolyester may be in one layer or more than one layer of the sheet. For example, the first layer of the sheet described in the present application comprises the first copolyester, and another layer, such as an optional third layer, may also comprise the first copolyester. The percent by volume of the first copolyester in the sheet is the total contributed by each layer comprising the first copolyester, and the percent by volume of the second copolyester in the sheet is the total contributed by each layer comprising the second copolyester.
(22) Returning to
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(24) In some embodiments of sheet 110, first layer 112a and third layer 112b have a substantially similar thickness, and sheet 110 may be considered to be substantially symmetrical or palindromic in structure. (As used throughout this application, the term substantially refers to being for the most part, primarily, principally, predominantly, chiefly, mainly, mostly, or generally. A property that is substantially may or may not be completely, fully, perfectly, thoroughly, totally, or wholly.) In some non-limiting embodiments, sheet 110 may have an overall thickness of 22 mil. In such sheet, first layer 112a consisting of the first copolyester may have a thickness of 8.25 mil and third layer 112b also consisting of the first copolyester may also have a thickness of 8.25 mil; and, therefore, first layer 112a and third layer 112b have a substantially similar thickness. In such sheet, the first copolyester in first layer 112a comprises 37.5% by volume of the sheet, the first copolyester in third layer 112b comprises 37.5% by volume of the sheet, and the first copolyester in the sheet (as a whole) comprises 75% by volume of the sheet.
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(26) In some embodiments of sheet 210, first layer 212a and fifth layer 212c have a substantially similar first thickness and second layer 214a and fourth layer 214b have a substantially similar second thickness. In such embodiments, sheet 210 may be considered to be substantially symmetrical or palindromic in structure.
(27) As is the first copolyester in sheet 110 in
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(29) First intermediate layer 316 and second intermediate layer 318 may comprise tie material, barrier material, or other materials as known to a person of ordinary skill in the packaging arts. As used throughout this application, the term tie material or tie refers to a polymeric material serving a primary purpose or function of adhering two surfaces to one another, such as the planar surfaces of two sheet or film layers. For example, a tie material adheres one sheet layer surface to another sheet layer surface or one area of a sheet layer surface to another area of a sheet layer surface. Tie material may comprise any polymer, copolymer, or blend of polymers having a polar group or any other polymer, homopolymer, copolymer, or blend of polymers, including modified and unmodified polymers (such as grafted copolymers) which provide sufficient interlayer adhesion to adjacent layers comprising otherwise non-adhering polymers. In some embodiments, tie material may comprise but is not limited to peelable adhesive and permanent adhesive. In various embodiments, first intermediate layer 316 and second intermediate layer 318 may be monolayer or multilayer layer films.
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(31) Sealant film 420 is a film included in sheet 410 (or any other sheet of the various embodiments described in the present application) involved in the sealing of the sheet to itself or to another layer of another film, sheet, etc. Sealant film 420 may be monolayer or multilayer. Either as monolayer or multilayer layer, sealant film 420 comprises a sealant layer. The term sealant layer or sealant layers refers to the specific layer or layers of sealant film 420 involved in the sealing to itself or to another layer. Sealant film 420 may be a blown film sealant, an extrusion coated sealant, a heat seal lacquer or coating, or other sealant material known to a person of ordinary skill in the packaging arts. Sealant film 420 may be continuous or patterned.
(32) As depicted in
(33) Various methods for making the sheet described in the present application exist. In some embodiments, the first layer and the second layer (and optional third or other layers) are created by flat-die cast co-extrusion. A sealant film may be cast co-extruded with such layers or may be adhesive laminated, thermal laminated, extrusion laminated, coated or otherwise added to the sheet after such layers are cast co-extruded. In other embodiments of the sheet, such as those in which the sheet has a lesser thickness (i.e., lower in the range of from 10 mil to 50 mil as described below), the sheet may be made by blown film co-extrusion.
(34) The sheet described in the present application may be thermoformable. As used throughout this application, the term thermoformable refers to a sheet capable of being formed or thermoformed into a desired shape by the application of a differential pressure between the sheet and a mold, by the application of heat, by the combination of the application of heat and a differential pressure between the sheet and a mold, or by any thermoforming technique known to a person of ordinary skill in the packaging arts.
(35) The sheet described in the present application may be thermoformed into a package. Thermoforming and other similar techniques are well known in the packaging arts. (See Throne, Thermoforming, Encyclopedia of Polymer Science and Technology, Third Edition, 2003, Volume 8, pp. 222-251 (John Wiley & Sons, Inc., Hoboken, N.J.); see also Irwin, Thermoforming, Modern Plastics Encyclopedia, 1984-1985, pp. 329-336 (McGraw-Hill, Inc., New York, N.Y.); see also Thermoforming, The Wiley Encyclopedia of Packaging Technology, Second Edition, 1997, pp. 914-921 (John Wiley & Sons, Inc., New York, N.Y.).) Suitable thermoforming methods include standard, deep-draw, or plug-assist vacuum forming. During standard vacuum forming a thermoplastic web, such as the sheet described in the present application, is heated and a vacuum is applied beneath the web allowing atmospheric pressure to force the web into a preformed mold. When relatively deep molds are employed, the process is referred to as a deep-draw application. In a plug-assist vacuum forming method, after the thermoplastic web has been heated and sealed across a mold cavity, a plug shape similar to the mold shape impinges on the thermoplastic web and, upon the application of vacuum, the thermoplastic web conforms to the mold surface.
(36) As used throughout this application, the term package refers to any article used to wholly or partially surround or contain an item. A package may take many, various forms. For example, the term package may include pouches that wholly surround or contain an item (or items) to be packaged. The term package may also include films, sheets, etc. that partially surround or contain an item (or items) to be packaged and, when used in conjunction with another film, sheet, etc. wholly surround or contain an item (or items). The term package may further include trays, cups, lidding materials, plates or other items.
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(39) In various embodiments, lidding material 70 (i.e., lidding material formed from a sheet according to the present application) may be used with another package not formed from a sheet according to the present application or may be used with another package formed from a sheet according to the present application.
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(41) The various embodiments of the sheet or the package described in the present application may exhibit various properties, as exemplified and further described in the Examples below.
(42) In some embodiments, the sheet or the package may have a thickness of from 10 mil to 50 mil or from 20 mil to 40 mil or from 20 mil to 30 mil.
(43) In some embodiments, as further described in the Examples below, the sheet may have a free shrink at 100 C. in each of the machine direction and the transverse direction of less than 1.0%. As used throughout this application, the term machine direction or MD refers to the direction of sheet transport during or after extrusion or film conversion. As used throughout this application, the term transverse direction or TD refers to the direction perpendicular to the machine direction
(44) In various embodiments, the sheet or the package is thermally stable, i.e., it maintains dimensionality and shape and does not substantially distort or deform after exposure to temperatures up to 112 C. As described above, as a thermally stable article, in various embodiments, the sheet or the package does not substantially deform when hot fill materials having temperatures of 68 C. to 80 C. or 71 C. to 110 C. or up to 112 C. are placed in or on the article; and, it does not substantially deform when placed in boiling water at 100 C. or subjected to steam sterilization or to microwave heating or to other heating during which the contents of the package (including but not limited to steam) reach temperatures up to 112 C.
(45) In some embodiments, the sheet or the package may have various clarity properties. As used throughout this application, the term clarity refers to the see-through quality of a material. It refers to the specific light transmitting and narrow-angle-light scattering properties of a material and is determined in an angle range less than 2.5 degrees. Clarity may be determined in accordance with ASTM D1003-13 (Standard Test Method for Haze and Luminous Transmittance of Transparent Plastics). Clarity values are reported in percent. A high clarity value generally reflects a material that is less cloudy and more transparent to visible wavelengths.
(46) The sheet or the package may have a clarity of greater than 99% or a clarity of from 98% to 99.9% before, during, or after exposure to temperatures up to 112 C. The sheet or the package described in the present application may have a clarity after exposure to temperatures up to 112 C. that is substantially similar to a clarity before exposure to temperatures up to 112 C.
(47) In some embodiments, the sheet or the package may have various haze properties. As used throughout this application, the term haze refers to the scattering of light as it passes through a material, it refers to the specific light-transmitting and wide-angle-light scattering properties of planar sections of a material. Haze may be determined in accordance with ASTM D1003-13 (Standard Test Method for Haze and Luminous Transmittance of Transparent Plastics). Haze values are reported in percent. A high haze value generally reflects a material that is more cloudy and less transparent to visible wavelengths.
(48) The sheet or the package may have a haze less than 1.5% before exposure to temperatures up to 112 C. and a haze less than or equal to 20% after five minutes of exposure to temperatures up to 112 C. As further described in the Examples below, this is in contrast to a sheet comprising the first copolyester but not comprising the second copolyester (i.e., a copolyester having a glass transition temperature of equal to or greater than 112 C.); such comparative sheet may have a haze of greater than 4% before exposure to temperatures up to 112 C. and greater than 40% after five minutes of exposure to temperatures up to 112 C. The sheet or the package described in the present application may have a haze after exposure to temperatures up to 112 C. that is substantially less than a haze after exposure to temperatures up to 112 C. over a similar time period of another sheet having a similar thickness and comprising the first copolyester but not comprising the second copolyester.
(49) In some embodiments, the sheet or the package may have various tensile properties after exposure to temperatures up to 112 C. These tensile properties include stress at yield, stress at break, and elongation at break. As used throughout this application, the term stress at yield refers to the tensile stress at which the rise in the stress-strain curve initially equals zero; it also refers to the tensile stress at the initial yield point, i.e., the point at which the sheet experiences initial plastic deformation (in contrast to elastic deformation such as rupture, tear, or break). Stress at yield is often expressed in force per unit area, e.g., psi. As used throughout this application, the term stress at break refers to the tensile stress at which a sheet ruptures, tears, or breaks, either partially or fully. Stress at break is often expressed in force per unit area, e.g., psi. As used throughout this application, the term elongation at break refers to the extension (i.e. lengthening or stretching) of a sheet produced by the tensile stress at the moment of partial or full rupture, tear, or break. Elongation at break is often expressed as a percentage of the original length of the specimen.
(50) The sheet or the package may have a stress at yield after exposure to temperatures up to 112 C. of greater than 1000 psi or greater than 1150 psi or from 1000 psi to 2000 psi. As further described in the Examples below, this is in contrast to a sheet comprising the first copolyester but not comprising the second copolyester; such comparative sheet may have a have a stress at yield after exposure to temperatures up to 112 C. of less than 300 psi. The sheet or the package described in the present application requires almost five times the force to create initial plastic deformation. The sheet or the package described in the present application has a stress at yield after exposure to temperatures up to 112 C. that is substantially greater than a stress at yield after exposure to temperatures up to 112 C. of another sheet having a similar thickness and comprising the first copolyester but not comprising the second copolyester.
(51) The sheet or the package may have a stress at break after exposure to temperatures up to 112 C. that is comparable to the stress at break of a sheet comprising the first copolyester but not comprising the second copolyester, assuming such comparative sheet actually breaks. Such stress at break may be greater than 1000 psi or greater than 1400 psi or from 1000 psi to 2000 psi.
(52) The sheet or the package may have an elongation at break after exposure to temperatures up to 112 C. of less than 400%. As further described in the Examples below, this is in contrast to a sheet comprising the first copolyester but not comprising the second copolyester (i.e., a copolyester having a glass transition temperature of equal to or greater than 112 C.); such comparative sheet may have an elongation at break after exposure to temperatures up to 112 C. of greater than 1100%. As such, the sheet or the package described in the present application does not elongate substantially after exposure to temperature up 112 C. before breaking in contrast to a sheet comprising the first copolyester but not comprising the second copolyester.
(53) The sheet and the package (such as the various trays) described in the present application with the various properties described above may be adapted to package both non-food and food product. Non-limiting examples of non-food products include pet foods, medications (including but not limited to cough syrup), personal care items (including but not limited to massage oils or soothing rubs), etc. Non-limiting examples of food products include produce (including but not limited to respiring produce, fruits, and vegetables such as potatoes, broccoli, carrots, beans, corn, peas, and blends of such), baked goods, ready meals, frozen snacks, frozen meals, condiments, syrups, dips (including but not limited to fruit-based (e.g., apple) and dairy-based (e.g., cheese) dips), beverages, etc.
(54) Accordingly, another embodiment of the present application comprises e hod of cooking produce using a tray comprising the sheet as described in the present application. This method comprises providing a tray comprising such thermoformed sheet, filling the tray with produce in a method known to a person of ordinary skill in the packaging arts, and heating the filled tray in a microwave oven. As such tray is formed from an embodiment of the sheet described in the present application, the tray is thermally stable after exposure to microwave heating.
EXAMPLES
(55) To further exemplify the various embodiments of the present application, several example and comparative example sheets were produced via cast coextrusion and evaluated for various properties. TABLE 1 provides information regarding the composition of the various examples and comparative examples.
(56) TABLE-US-00001 TABLE 1 % Sheet % Sheet % Sheet % Sheet Volume Volume Volume Volume First Second Other Sheet First (layer Second (layer Third (layer Copoly- Copoly- Copoly- Thickness Layer thickness) Layer thickness) Layer thickness) ester ester ester Example 1 22 mil APET1 37.5% FX200 25% APET1 37.5% 75% 25% (8.25 mil) (5.5 mil) (8.25 mil) Example 2 26 mil APET2 42.5% FX200 15% APET2 42.5% 85% 15% (11.05 mil) (3.9 mil) (11.05 mil) Example 3 26 mil APET2 40% FX200 20% APET2 40% 80% 20% (10.4 mil) (5.2 mil) (10.4 mil) Example 4 26 mil APET2 35% FX200 30% APET2 35% 70% 30% (9.1 mil) (7.8 mil) (9.1 mil) Example 5 26 mil APET2 32.5% FX200 35% APET2 32.5% 65% 35% (8.45 mil) (9.1 mil) (8.45 mil) Example 6 26 mil APET2 30% FX200 40% APET2 30% 60% 40% (7.8 mil) (10.4 mil) (7.8 mil) Example 7 26 mil APET2 27.5% FX200 45% APET2 27.5% 55% 45% (7.15 mil) (11.7 mil) (7.15 mil) Comparative 22 mil APET1 100% 100% 0% Example 1 .sup.(22 mil) Comparative 26 mil APET2 100% 100% 0% Example 2 .sup.(26 mil) Comparative 26 mil APET2 45% FX200 10% APET2 45% 90% 10% Example 3 (11.7 mil) (2.6 mil) (11.7 mil) Comparative 26 mil APET2 42.5% FX100 15% APET2 42.5% 85% 15% Example 4 (11.05 mil) (3.9 mil) (11.05 mil) Comparative 26 mil APET2 35% FX100 30% APET2 35% 70% 30% Example 5 (9.1 mil) (7.8 mil) (9.1 mil) Comparative 26 mil APET2 30% FX100 40% APET2 30% 60% 40% Example 6 (7.8 mil) (10.4 mil) (7.8 mil)
(57) APET1 was Laser+ C (E60A), having an intrinsic viscosity of 0.810.02 dl/g and a glass transition temperature of from 70 C. to 90 C. and, therefore, meeting the characteristics of the first copolyester as described in this application.
(58) APET2 was Cleartuf 8006C, having an intrinsic viscosity of 0.800.02 dl/g and a glass transition temperature of from 70 C. to 90 C. and, therefore, meeting the characteristics of the first copolyester as described in this application.
(59) FX200 was Eastman Tritan Copolyester FX200, having a glass transition temperature of 119 C. (DSC) and, therefore, meeting the characteristics of the second copolyester as described in this application.
(60) FX100 was Eastman Tritan Copolyester FX100, having a glass transition temperature of 110 C. (DSC) and, therefore, not meeting the characteristics of either the first copolyester or the second copolyester as described in this application (and so noted in TABLE 1 as other copolyester.)
(61) Example 1 and Comparative Example 1 were evaluated for clarity and haze before and after exposure to temperatures up to 112 C. To evaluate, a 4 inch by 4 inch square was cut from two samples of each sheet; each replicate was then boiled (i.e., placed in boiling water) over a range of time. TABLE 2 reports the average results.
(62) TABLE-US-00002 TABLE 2 Example 1 Comparative Example 1 Boil Time (min) Clarity Haze Clarity Haze 0 99.45 1.22 99.40 4.19 1 99.60 2.64 99.05 14.90 2 99.70 8.10 99.45 30.95 3 99.45 9.04 98.50 45.00 4 99.00 20.00 98.80 31.65 5 98.60 15.95 97.55 36.95
(63) As reported in TABLE 2, while the haze of Example 1 did increase substantially as a function of boiling time, the clarity at the longest boiling interval decreased by less than 1% relative to the clarity prior to boiling (i.e., at 0 minutes boil time). As such, Example 1 has a clarity after exposure to temperatures up to 112 C. that is substantially similar to a clarity before exposure to temperatures up to 112 C.
(64) As also reported in TABLE 2, the clarity of Comparative Example 1 decreases at a faster rate as a function of boiling time compared to the clarity of Example 1. Additionally, the haze of Comparative Example 1 increases at a faster rate as a function of boiling time compared to the haze of Example 1. As such, Example 1 has a haze after exposure to temperatures up to 112 C. that is substantially less than the haze of Comparative Example 1 after exposure to temperatures up to 112 C. over a similar time period, with Comparative Example 1 as another sheet having a similar thickness to Example 1 and comprising the first copolyester but not comprising the second copolyester.
(65) Example 3 was also evaluated for clarity and haze before exposure to boiling or other elevated temperatures. Example 3 was determined to have a clarity of 98.9% and a haze of 0.90%.
(66) Example 1 and Comparative Example 1 were further evaluated via tensile testing for resistance to deformation at elevated temperatures (e.g., temperatures up to 112 C.). ASTM D882, Standard Test Method for Tensile Properties of Thin Plastic Sheeting was used to determine various tensile properties such as stress at yield, stress at break, and elongation at break of three samples of each of Example 1 and Comparative Example 1 at 100 C., using a 0.5 inch span and 20 inch per minute crosshead speed. TABLE 3 reports the average results.
(67) TABLE-US-00003 TABLE 3 Measured Stress Stress Elongation Thickness at Yield at Break at Break (mil) (psi) (psi) (%) MD TD MD TD MD TD MD TD Example 1 21.99 21.50 1279 1197 1646 1451 333 317 Comparative 21.28 21.49 258 242 NA 1663 1250+ 1148 Example 1
The machine direction stress at break of Comparative Example 1 is reported as NA as none of the three samples of Comparative Example 1 exhibited a break, either partially or fully, in the machine direction. Accordingly, the machine direction elongation at break of Comparative Example 1 reported as 1250+%, with 1250% as the upper limit of the testing equipment.
(68) The data of TABLE 3 may also be depicted graphically.
(69) TABLE 3 and
(70) Example 1 and Comparative Example 1 were also evaluated for heat shrinkage values. As used throughout this application, the term shrinkage value refers to values obtained by measuring unrestrained (or free) shrink of a ten-centimeter square sample immersed in water at 100 C. for five seconds. For the present application, three test specimens were cut from each of Example 1 and Comparative Example 1. The specimens were cut into squares of ten-centimeter length in the machine direction by ten-centimeter length in the transverse direction. Each specimen was completely immersed for five seconds in a 100 C. water bath. Each specimen was then removed from the bath and the distance between the ends of each shrunken specimen was measured for both the machine and transverse directions. The difference in the measured distance for the shrunken specimen and the original ten-centimeter side was multiplied by ten to obtain the percent of shrinkage for the specimen n each direction. TABLE 4 reports the average free shrink values of the three specimens of each of Example 1 and Comparative Example 1 in each of the machine direction and the transverse direction.
(71) TABLE-US-00004 TABLE 4 Free Shrink, % Example 1 Comparative Example 1 MD TD MD TD 0.3 0.7 2.0 1.0
(72) To further exemplify the various embodiments of the present application, Example 2, Example 3, Comparative Example 2, and Comparative Example 3 were thermoformed with a tray mold having a 1.5 inch draw depth to form a tray similar to the tray of
(73) TABLE-US-00005 TABLE 5 Visual Evaluation Example 2 Slight, barely detectable deformation on a side wall Example 3 No visible deformation of any kind Comparative Visibly melted Example 2 Lost almost half of its depth Comparative Visible moderate deformation on bottom and side walls Example 3
The slight, barely detectable deformation of Example 2 was acceptable in and of itself and is assumed to disappear completely in the absence of any additional stress (e.g., the weight of the water) compared to the minimal stress of its own weight as, for example, a lidding material.
(74) Examples 4-7 and Comparative Examples 4-6 were thermoformed with a cup mold (cf., a fruit cup mold) to form a cup similar to the cup of
(75) TABLE-US-00006 TABLE 6 Visual Evaluation Example 4 No physical deformation Looked identical to pre-cooked part except for slight blue haze on bottom Example 5 No physical deformation Looked identical to pre-cooked part except for slight blue haze on bottom Example 6 No physical deformation Looked identical to pre-cooked part except for slight blue haze on bottom Example 7 No physical deformation Looked identical to pre-cooked part except for slight blue haze on bottom Comparative Physical deformation on bottom and side walls Example 4 Comparative Physical deformation on bottom and side walls Example 5 Comparative No physical deformation Example 6
The slight blue haze of cooked Examples 4-7 was deemed acceptable for end-user purposes. Further, while cooked Comparative Example 6 showed no physical deformation, as described above Comparative Example 6 includes a first copolyester but does not include a second copolyester as described in the present application. Additionally, the required 40% by volume loading of the other copolyester in Comparative Example 6 to achieve no physical deformation does not provide desired flexibility in manufacturing processes or costs.
(76) Each and every document cited in this present application, including any cross-referenced or related patent or application, is incorporated in this present application in its entirety by this reference, unless expressly excluded or otherwise limited. The citation of any document is not an admission that it is prior art with respect to any embodiment disclosed or claimed in this present application or that it alone, or in any combination with any other reference or references, teaches, suggests, or discloses any such embodiment. Further, to the extent that any meaning or definition of a term in this present application conflicts with any meaning or definition of the same term in a document incorporated by reference, the meaning or definition assigned to that term in this present application (including the appended claims) governs.
(77) Unless otherwise indicated, all numbers expressing sizes, amounts, ranges, limits, and physical and other properties used in the present application (including the appended claims) are to be understood as being preceded in all instances by the term about. Accordingly, unless expressly indicated to the contrary, the numerical parameters set forth in the present application (including the appended claims) are approximations that can vary depending on the desired properties sought to be obtained by a person of ordinary skill in the packaging arts without undue experimentation using the teachings disclosed in the present application.
(78) As used in the present application (including the appended claims), the singular forms a, an, and the encompass embodiments having plural referents, unless the context clearly dictates otherwise. As used in the present application (including the appended claims), the term or is generally employed in its sense including and/or, unless the context clearly dictates otherwise.
(79) Spatially related terms, including but not limited to, lower, upper, beneath, below, above, bottom, and top, if used in the present application (including the appending claims), are used for ease of description to describe spatial relationships of element(s) to another. Such spatially related terms encompass different orientations of the package in use or operation, in addition to the particular orientations depicted in the drawings and described in the present application (including the appended claims). For example, if an object depicted in the drawings is turned over or flipped over or inverted, elements previously described as below or beneath other elements would then be above those other elements.
(80) The description, examples, embodiments, and drawings disclosed are illustrative only and should not be interpreted as limiting. The present invention includes the description, examples, embodiments, and drawings disclosed; but it is not limited to such description, examples, embodiments, or drawings. The reader should assume that features of one disclosed embodiment can also be applied to all other disclosed embodiments, unless expressly indicated to the contrary. Modifications and other embodiments will be apparent to a person of ordinary skill in the packaging arts, and all such modifications and other embodiments are intended and deemed to be within the scope of the present invention as described in the claims.