INSULATED CONTAINER AND METHOD OF MAKING THE SAME
An insulative cup is formed of a multi-layer sheet. The multi-layer sheet comprises an insulative cellular non-aromatic polymeric material, a film layer, and a polymeric lamination layer. The insulative cellular non-aromatic polymeric material is formed from a formulation comprising a base resin blend and a physical nucleating agent.
This application claims priority to U.S. Non-Provisional application Ser. No. 16/058,131, filed Aug. 8, 2018, which claims priority under 35 U.S.C. § 119(e) to U.S. Provisional Application Ser. No. 62/542,324, filed Aug. 8, 2017, each of which is expressly incorporated by reference herein.
BACKGROUNDThe present disclosure relates to polymeric materials that can be formed to produce a container, and in particular, polymeric materials that insulate. More particularly, the present disclosure relates to containers that are formed of a non-aromatic polymeric material.
SUMMARYA cup in accordance with the present disclosure is formed of a multi-layer sheet including a film layer and an insulative cellular non-aromatic polymeric material. In illustrative embodiments, a blend of polymeric resins and cell-forming agents is extruded or otherwise formed to produce the insulated cellular non-aromatic polymeric material.
In illustrative embodiments, a polymeric-lamination layer couples together the film layer and the insulative cellular non-aromatic polymeric material. The multi-layer sheet may be formed by an extrusion lamination procedure that extrudes the polymer-lamination layer onto the insulative cellular non-aromatic polymeric material.
In some illustrative embodiments, the polymeric-lamination layer comprises a polypropylene, a polyethylene, or a mixture thereof. In some embodiments, the polymeric-lamination layer is substantially free of an adhesive.
In some illustrative embodiments, the insulative cellular non-aromatic polymer material, the polymeric-lamination layer, or both comprise regrind. In some embodiments, regrind is blend of materials recaptured from the steps in forming the multi-layer sheet. In some illustrative embodiments, regrind is substantially free of an adhesive.
In some illustrative embodiments, the cup may have a tear resistance in a machine direction of at least about 75 gf according to ASTM D1922-93. In some illustrative embodiments, the cup has a puncture resistance of at least about 6,000 gf.
Additional features of the present disclosure will become apparent to those skilled in the art upon consideration of illustrative embodiments exemplifying the best mode of carrying out the disclosure as presently perceived.
The detailed description particularly refers to the accompanying figures in which:
An insulative cup 10 in accordance with the present disclosure is formed of a multi-layer sheet 80 as shown in
Insulative cup 10 includes a body 11 having a sleeve-shaped side wall 18 and a floor 20 as shown in
Body 11 is formed of multi-layer sheet 80 as suggested in
Multi-layer sheet 80 includes insulative cellular non-aromatic polymeric material 82, polymeric-lamination layer 54, and printed film layer 70, as shown in
Insulative cellular non-aromatic polymeric material 82 is configured in accordance with the present disclosure to provide means for enabling localized plastic deformation in at least one selected region of body 11 (e.g., side wall 18, rolled brim 16, floor mount 17, and a floor-retaining flange 26 included in floor mount 17) to provide (1) a plastically deformed first material segment having a first density in a first portion of the selected region of body 11 and (2) a second material segment having a relatively lower second density in an adjacent second portion of the selected region of body 11 as suggested, for example, in
One aspect of the present disclosure provides a formulation for manufacturing an insulative cellular non-aromatic polymeric material 82. As referred to herein, an insulative cellular non-aromatic polymeric material 82 refers to an extruded structure having cells formed therein and has desirable insulative properties at given thicknesses. Another aspect of the present disclosure provides a polymeric formulation for manufacturing an extruded structure of insulative cellular non-aromatic polymeric material. Still another aspect of the present disclosure provides an extrudate comprising an insulative cellular non-aromatic polymeric material. Yet another aspect of the present disclosure provides a structure of material formed from an insulative cellular non-aromatic polymeric material. A further aspect of the present disclosure provides a container formed from an insulative cellular non-aromatic polymeric material.
A potential feature of an insulative cup formed of insulative cellular non-aromatic polymeric material according to one aspect of the present disclosure is that it possesses unexpected strength as measured by rigidity. Rigidity is a measurement done at room temperature and at an elevated temperature (e.g., by filling the cup with a hot liquid) and measuring the rigidity of the material. The strength of the cup material is important to minimize deformation of the cup as the cup is being handled by a user.
In illustrative examples, cup 10 has a rigidity as measured in accordance with the Examples described herein. The measured rigidity of cup 10 may be at least 0.25 kg-F, at least 0.275 kg-F, at least 0.3 kg-F, at least 0.325 kg-F, at least 0.35 kg-F, at least 0.4 kg-F, at least 0.5 kg-F, at least 0.6 kg-F, at least 0.7 kg-F, or at least 0.75 kg-F. In some embodiments, the measured rigidity of cup 10 may be selected from a first set of ranges of from about 0.2 kg-F to about 0.50 kg-F, about 0.25 kg-F to about 0.5 kg-F, about 0.25 kg-F to about 0.45 kg-F, about 0.3 kg-F to about 0.45 kg-F, about 0.315 kg-F to about 0.45 kg-F, about 0.325 kg-F to about 0.45 kg-F, about 0.325 kg-F to about 0.425 kg-F. In some embodiments, the measured rigidity of cup 10 may be selected from a second set of ranges of from about 0.3 kg-F to about 1.5 kg-F, about 0.3 kg-F to about 1.3 kg-F, about 0.3 kg-F to about 1.1 kg-F, about 0.3 kg-F to about 0.9 kg-F, about 0.4 kg-F to about 0.9 kg-F, about 0.5 kg-F to about 0.9 kg-F, about 0.5 kg-F to about 0.8 kg-F, or about 0.6 kg-F to about 0.8 kg-F.
In some embodiments, the cup has a rigidity as measured when the cup is filled with cold, room temperature, or hot water and if the cup comprises a lid coupled with the brim. In some exemplary embodiments, the cup has a cold fill lidded rigidity of at least about 1 kg-F. In some embodiments, the cup has a cold fill lidded rigidity of less than about 1.5 kg-F. In some exemplary embodiments, the cup has a cold fill unlidded rigidity of at least about 0.5 kg-F. In some embodiments, the cup has a cold fill unlidded rigidity of less than about 1.2 kg-F. In some exemplary embodiments, the cup has a hot fill lidded rigidity of at least about 0.35 kg-F. In some embodiments, the cup has a hot fill lidded rigidity of less than about 0.75 kg-F. In some exemplary embodiments, the cup has a hot fill unlidded rigidity of at least about 0.2 kg-F. In some embodiments, the cup has a hot fill unlidded rigidity of less than about 0.5 kg-F. In some exemplary embodiments, the cup has a room temperature fill lidded rigidity of at least about 0.6 kg-F. In some embodiments, the cup has a room temperature fill lidded rigidity of less than about 1.7 kg-F. In some exemplary embodiments, the cup has a room temperature fill unlidded rigidity of at least about 0.3 kg-F. In some embodiments, the cup has a room temperature fill unlidded rigidity of less than about 1 kg-F. In some exemplary embodiments, the cup has a room temperature unfilled lidded rigidity of at least about 0.6 kg-F. In some embodiments, the cup has a room temperature fill lidded rigidity of less than about 1.7 kg-F. In some exemplary embodiments, the cup has a room temperature unfilled unlidded rigidity of at least about 0.3 kg-F. In some embodiments, the cup has a room temperature fill unlidded rigidity of less than about 1 kg-F.
Body 11 is formed from a strip of multi-layer sheet 80 as disclosed herein. In accordance with the present disclosure, a strip of multi-layer sheet 80 is configured (by application of pressure—with or without application of heat) to provide means for enabling localized plastic deformation in at least one selected region of body 11 to provide a plastically deformed first material segment having a first density located in a first portion of the selected region of body 11 and a second material segment having a second density lower than the first density located in an adjacent second portion of the selected region of body 11 without fracturing the insulative cellular non-aromatic polymeric material so that a predetermined insulative characteristic is maintained in body 11.
Sleeve-shaped side wall 18 includes an upright inner tab 514, an upright outer tab 512, and an upright fence 513 extending between inner and outer tabs 514, 512 as suggested in
A second region of the selected regions of body 11 in which localized plastic deformation is enabled by the insulative cellular non-aromatic polymeric material is in a rolled brim 16 included in body 11 as suggested in
A third region of the selected regions of body 11 in which localized plastic deformation is enabled by the insulative cellular non-aromatic polymeric material is in a floor mount 17 included in body 11 as suggested in
A fourth region 104 of the selected regions of body 11 in which localized plastic deformation is enabled by the insulative cellular non-aromatic polymeric material is in floor-retaining flange 26 of floor mount 17 as suggested in
Sleeve-shaped side wall 18 of body 11 includes a pair of tabs 514, 512 that mate to provide side wall 18 with a frustoconical shape in the illustrative embodiment shown in
Upright fence 513 of side wall 18 is C-shaped in a horizontal cross-section and each of upright inner and outer tabs 514, 512 has an arcuate shape in a horizontal cross-section. Upright fence 513 includes an upright left side edge and an upright right side edge that is arranged to lie in spaced-apart confronting relation to upright left side edge. Upright outer tab 512 is configured to have the higher first density and mate with upright inner tab 514 also characterized by the higher first density to establish a bridge 512, 514 arranged to interconnect upright left and right side edges of upright fence 513. The bridges are formed of a plastically deformed material having the higher first density.
Upright fence 513 of side wall 18 has an inner surface bounding a portion of interior region 14 and an outer surface facing away from interior region 14 and surrounding inner surface of upright fence 513. The outer surface cooperates with the inner surface of upright fence 513 to define a first thickness therebetween. Upright inner tab 514 includes an inner surface bounding a portion of interior region 14 and an outer surface facing toward upright outer tab 512. Upright outer tab 512 includes an inner surface facing toward interior region 14 and mating with the outer surface of upright inner tab 514 to define the interface between upright inner and outer tabs 514, 512. Upright outer tab 512 further includes an outer face facing away from upright inner tab 514. Inner and outer surfaces of upright inner tab 514 cooperate to define a second thickness therebetween that is less than the first thickness. Inner and outer surfaces of upright outer tab 512 cooperate to define a third thickness that is less than the first thickness.
Rolled brim 16 of body 11 is coupled to an upper end of sleeve-shaped side wall 18 to lie in spaced-apart relation to floor 20 and to frame an opening into interior region 14 as suggested in
Floor mount 17 of body 11 is coupled to a lower end of sleeve-shaped side wall 18 and to floor 20 to support floor 20 in a stationary position relative to sleeve-shaped side wall 18 to form interior region 14 as suggested in
Floor 20 of insulative cup 10 includes a horizontal platform 21 bounding a portion of interior region 14 and a platform-support member 23 coupled to horizontal platform 21 as shown, for example, in
Platform-support member 23 of floor 20 has an annular shape and is arranged to surround floor-retaining flange 26 and lie in an annular space provided between horizontal platform 21 and connecting web 25 as suggested in
Floor-retaining flange 26 of floor mount 17 is arranged to lie in a stationary position relative to sleeve-shaped side wall 18 and coupled to floor 20 to retain floor 20 in a stationary position relative to sleeve-shaped side wall 18 as suggested in
Floor-retaining flange 26 of floor mount 17 is ring-shaped and includes an alternating series of upright thick and thin staves arranged to lie in side-to-side relation to one another to extend upwardly toward a downwardly facing underside of horizontal platform 21. A first 261 of the upright thick staves is configured to include a right side edge extending upwardly toward the underside of horizontal platform 21. A second 262 of the upright thick staves is configured to include a left side edge arranged to extend upwardly toward underside of horizontal platform 21 and lie in spaced-apart confronting relation to right side edge of the first 261 of the upright thick staves. A first 260 of the upright thin staves is arranged to interconnect left and right side edges and cooperate with left and right side edges to define therebetween a vertical channel opening inwardly into a lower interior region 264 bounded by horizontal platform 21 and floor-retaining flange 26 as suggested in
Floor-retaining flange 26 of floor mount 17 has an annular shape and is arranged to surround a vertically extending central axis CA intercepting a center point of horizontal platform 21 as suggested in
Insulative cup 10 in accordance with one exemplary embodiment of the present disclosure includes a base 12 formed to include an interior region 14 and a rolled brim 16 coupled to base 12 as shown, for example, in
Side wall 18 extends between rolled brim 16 and support structure 19 as shown in
Referring again to
Support structure 19 includes a floor-retaining flange 26 and a connecting web 25 as shown in
As shown in
The compressibility of the insulative cellular non-aromatic polymeric material used in accordance with the present disclosure to produce insulative cup 10 allows the insulative cellular non-aromatic polymeric material to be prepared for the mechanical assembly of insulative cup 10, without limitations experienced by other polymeric materials. The cellular nature of the insulative cellular non-aromatic polymeric material disclosed herein provides insulative characteristics as discussed below, while susceptibility to plastic deformation permits yielding of the insulative cellular non-aromatic polymeric material without fracture. The plastic deformation experienced when the strip of insulative cellular non-aromatic polymeric material is subjected to a pressure load is used to form a permanent set in the insulative cellular non-aromatic polymeric material after the pressure load has been removed. In some locations, the locations of the permanent set are positioned in illustrative embodiments to provide, for example, controlled gathering of the insulative cellular non-aromatic polymeric material.
Plastic deformation may also be used to create fold lines in the insulative cellular non-aromatic polymeric material to control deformation of the material when being worked during a cup assembly process. When deformation is present, the absence of material in the voids formed by the deformation provides relief to allow the material to be folded easily at the locations of deformation
Each first material segment in the insulative cellular non-aromatic polymeric material has a relatively thin first thickness. Each companion second material segment in the insulative cellular non-aromatic polymeric material has a relatively thicker second thickness.
Body 11 is formed from multi-layer sheet 80 of insulative cellular non-aromatic polymeric material that includes, for example, a strip of insulative cellular non-aromatic polymeric material 82 and printed film layer 70 coupled to one side of the strip of insulative cellular non-aromatic polymeric material as shown in
The insulative cellular non-aromatic polymeric material comprises, for example, a polypropylene base resin having a high melt strength, one or both of a polypropylene copolymer and homopolymer resin, and one or more cell-forming agents. As an example, cell-forming agents may include a primary nucleation agent, a secondary nucleation agent, and a blowing agent defined by gas means for expanding the resins and to reduce density. In one example, the gas means comprises carbon dioxide. In another example, the base resin comprises broadly distributed molecular weight polypropylene characterized by a distribution that is unimodal and not bimodal.
Illustratively, each of insulative cellular non-aromatic polymeric material 82, polymeric-lamination layer 54, and film layer 56 comprise a polymeric material. The polymeric material for each of insulative cellular non-aromatic polymeric material 82, polymeric-lamination layer 54, and film layer 56 can be made, for example, by extruding a formulation. It should be understood that many of the ranges described herein for the formulation apply with equal weight to the extruded polymeric material, except that in some examples the chemical nucleating agent will decompose upon heating. The decomposition of the chemical nucleating agent could cause the relative weight percentages of the remaining components to increase slightly.
As an example, a polymeric formulation for forming insulative cellular non-aromatic polymeric material 82 comprises a base resin blend. In some embodiments, the base resin blend comprises a high melt strength, a polypropylene copolymer, polypropylene homopolymer, or a mixture thereof. In some embodiments, the formulation may comprise cell-forming agents including a chemical nucleating agent and a physical blowing agent such as carbon dioxide. As a further example, insulative cellular non-aromatic polymeric material 82 further comprises a slip agent. As an example, one polypropylene resin has a broadly distributed unimodal (not bimodal) molecular weight distribution.
In exemplary embodiments, a polymeric formulation comprises a base resin blend comprising at least two materials. In some embodiments, the base resin blend comprises a first polymer and a second polymer. In some embodiments, the first polymer is a polypropylene. In some embodiments, the second polymer is a polypropylene. In some embodiments, the first polymer is a polypropylene and the second polymer is a polypropylene. In one exemplary embodiment, a first or second polypropylene polymer comprises a high melt strength polypropylene that has long chain branching. In one exemplary embodiment, the first or second polypropylene polymer also has non-uniform dispersity. In some embodiments, the first polypropylene polymer is a polypropylene homopolymer. In some embodiments, the second polypropylene is a polypropylene homopolymer. In some embodiments, the base resin blend comprises a first polypropylene homopolymer and a second polypropylene homopolymer.
Other polypropylene polymers having suitable melt strength, branching, and melting temperature may also be used. Several base resins may be used and mixed together.
In some embodiments, the base resin blend comprises a polymer that may be, for example, a polymer with sufficient crystallinity. The polymer may also be, for example, a polymer with sufficient crystallinity and melt strength. In exemplary embodiments, the polymer may be at least one crystalline polypropylene homopolymer, an impact polypropylene copolymer, mixtures thereof, or the like. One illustrative example is a high crystalline polypropylene homopolymer, available as F020HC from Braskem. Another illustrative example is an impact polypropylene copolymer commercially available as PRO-FAX SC204™ (available from LyondellBasell Industries Holdings, B.V.). Another illustrative example is Homo PP-INSPIRE 222, available from Braskem. Another illustrative example is the commercially available polymer known as PP 527K, available from Sabic. Another illustrative example is a polymer commercially available as XA-11477-48-1 from LyondellBasell Industries Holdings, B.V. In one aspect the polypropylene polymer may have a high degree of crystallinity, i.e., the content of the crystalline phase exceeds 51% (as tested using differential scanning calorimetry) at 10° C./min cooling rate. In exemplary embodiments, several different polymers may be used and mixed together.
In exemplary embodiments, the base resin blend may comprise polyethylene. In exemplary embodiments, the base resin blend may comprise low-density polyethylene, linear low-density polyethylene, high-density polyethylene, ethylene-vinyl acetate copolymers, ethylene-ethylacrylate copolymers, ethylene-acrylic acid copolymers, polymethylmethacrylate mixtures of at least two of the foregoing and the like. The use of non-polypropylene materials may affect recyclability, insulation, microwavability, impact resistance, or other properties, as discussed further hereinbelow.
In illustrative embodiments, a polymeric formulation comprises a base resin blend. In illustrative embodiments, the base resin blend may include a polypropylene. In illustrative embodiments, an insulative cellular non-aromatic polymeric material comprises a polypropylene having high melt strength, a polypropylene copolymer or homopolymer (or both). It is within the scope of the present disclosure to select an amount of base resin blend of the polymeric formulation to be one of the following values: about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 86%, about 87%, about 88%, about 89%, about 90%, about 91%, about 92%, about 93%, about 94%, about 95%, about 96%, about 97%, about 98%, about 99%, about 99.5%, and about 99.9% by weight of the polymeric formulation. It is within the present disclosure for the amount of base resin blend in the polymeric formulation to fall within one of many different ranges. In a first set of ranges, the range of base resin blend of the polymeric formulation is one of the following ranges: about 50% to about 99.9%, about 70% to about 99.9%, about 80% to about 99.9%, about 85% to about 99.9%, about 90% to about 99.9%, about 95% to about 99.9%, about 98% to about 99.9%, and about 99% to about 99.9% by weight of the polymeric formulation. In a second set of ranges, the range of base resin blend in the polymeric formulation is one of the following ranges: about 85% to about 99%, about 85% to about 98%, about 85% to about 95%, and about 85% to about 90% by weight of the polymeric formulation. In a third set of ranges, the range of base resin blend of the polymeric formulation is one of the following ranges: about 50% to about 99%, about 50% to about 95%, about 50% to about 85%, about 55% to about 85%, about 80% to about 90%, about 80% to about 95%, about 90% to about 99%, and about 95% to about 98% by weight of the polymeric formulation. Each of these values and ranges is embodied in Examples 1 to 12. As defined hereinbefore, the base resin blend may comprise any suitable polymeric material. In addition, the ranges disclosed herein for the formulation apply with equal weight to the ranges for the polymeric material.
In illustrative embodiments, the base resin blend comprises a polypropylene. In some embodiments, the base resin blend comprises a first polymer and a second polymer. In some embodiments, the first polymer is a first polypropylene. In some embodiments, the polypropylene is a first polypropylene homopolymer. In some embodiments, the first polypropylene homopolymer is DAPLOY™ WB140 homopolymer (available from Borealis A/S). It is within the scope of the present disclosure to select an amount of the first polymer of the base resin blend to be one of the following values: about 40%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 81%, about 82%, about 83%, about 84%, about 85%, about 86%, about 87%, about 88%, about 89%, about 90%, about 91%, about 92%, about 93%, about 94%, about 95%, about 96%, about 97%, or about 99% by weight of the base resin blend. It is within the present disclosure for the amount of the first polymer of the base resin blend to fall within one of many different ranges. In a first set of ranges, the range of first polymer in the base resin blend is one of the following ranges: about 40% to about 99%, about 60% to about 99%, about 70% to about 99%, about 80% to about 99%, or about 85% to about 99.9% by weight of the base resin blend. In a second set of ranges, the range of first polymer in the base resin blend is one of the following ranges: about 40% to about 97%, about 40% to about 95%, about 40% to about 92%, or about 40% to about 90% by weight of the base resin blend. In a third set of ranges, the range of first polymer in the base resin blend is one of the following ranges: about 50% to about 99%, about 50% to about 95%, about 60% to about 95%, about 65% to about 95%, about 65% to about 92%, about 70% to about 92%, about 75% to about 92%, or about 80% to about 92% by weight of the base resin blend.
In illustrative embodiments, the base resin blend includes a second polymer. In some embodiments, the second polymer is a polyethylene. In some embodiments, the second polymer is a polypropylene. In some embodiments, the second polypropylene is a second polypropylene homopolymer. In some embodiments, the second polypropylene is a second polypropylene copolymer. It is within the scope of the present disclosure to select an amount of the second polymer of the base resin blend to be one of the following values: about 1%, about 2%, about 3%, about 4%, about 5%, about 6%, about 7%, about 8%, about 9%, about 10%, about 11%, about 12%, about 13%, about 14%, about 15%, about 20%, about 25%, about 30%, about 35%, about 40%, about 45%, about 50%, or about 60% by weight of the base resin blend. It is within the present disclosure for an amount of the second polymer of the base resin blend to fall within one of many different ranges. In a first set of ranges, the range of base resin is one of the following ranges: about 1% to about 60%, about 1% to about 50%, about 1% to about 40%, about 1% to about 30%, about 1% to about 25%, about 1% to about 20%, about 1% to about 15%, about 1% to about 10%, or about 1% to about 5% by weight of the base resin blend. In a second set of ranges, the range of the second polymer of the base resin blend is one of the following ranges: about 1% to about 50%, about 10% to about 60%, about 15% to about 60%, about 20% to about 60%, about 30% to about 60%, or about 40% to about 60% by weight of the base resin blend. In a third set of ranges, the range of second polymer of the base resin blend is one of the following ranges: about 2% to about 60%, about 2% to about 50%, about 2% to about 40%, about 2% to about 30%, about 4% to about 30%, about 4% to about 25%, about 4% to about 20%, about 5% to about 20%, about 5% to about 20%, or about 5% to about 15% by weight of the base resin blend. In an embodiment, the base resin blend lacks a second polymer. In a particular embodiment, a second polypropylene can be a high crystalline polypropylene homopolymer, such as F020HC (available from Braskem) or PP 527K (available from Sabic). In an embodiment, a polymeric material lacks a secondary resin.
The polymer resins may be blended with any additional desired components and melted to form a resin formulation mixture.
In some embodiments, one or more nucleating agents are used to provide and control nucleation sites to promote the formation of cells, bubbles, or voids in a molten resin during the extrusion process. A nucleating agent can be a chemical or physical material that provides sites, i.e. nucleation sites, for cells to form in the molten resin mixture. Nucleating agents may be physical agents or chemical agents. When a suitable temperature is reached, the nucleating agent acts to enable the formation of gas bubbles that create cells in the molten resin.
Suitable physical nucleating agents have a desirable particle size, aspect ratio, top-cut properties, shape, and surface compatibility. Examples include, but are not limited to, talc, CaCO3, mica, kaolin clay, chitin, aluminosilicates, graphite, cellulose, and mixtures of at least two of the foregoing. The nucleating agent may be blended with the base resin blend that is introduced into hopper 113. Alternatively, the nucleating agent may be added to the molten resin mixture in an extruder 111.
After decomposition, the chemical nucleating agent forms small gas cells, which further serve as nucleation sites for larger cell growth from physical blowing agents or other types thereof. An illustrative example of a chemical nucleating agent is citric acid or a citric acid-based material. One representative example is Hydrocerol™ CF-40E™ (available from Clariant Corporation), which contains citric acid and a crystal nucleating agent. Another representative example is Hydrocerol™ CF-05E™ (available from Clariant Corporation), which contains citric acid and a crystal nucleating agent. In illustrative embodiments, one or more catalysts or other reactants may be added to accelerate or facilitate the formation of cells.
As described herein, the polymeric formulation may comprise a physical nucleating agent, a chemical nucleating agent, or both. In some embodiments, the nucleating agent is up to about 1%, up to about 3%, up to about 5%, up to about 7%, or up to about 10% by weight of the polymeric formulation. It is within the scope of the present disclosure to select an amount of a nucleating agent to be one of the following values: about 0%, about 0.5%, about 1%, about 1.5%, about 2%, about 2.5%, about 3%, about 4%, and about 5%, about 6%, about 7%, about 8%, about 9%, about 10%, about 12%, about 14%, by weight of the total formulation of the polymeric layer. It is also within the scope of the present disclosure for the weight percentage (w/w) of a nucleating agent to fall within one of many different ranges. In a first set of ranges, the weight percentage of a nucleating agent is one of the following ranges: about 0.1% to about 20% (w/w), about 0.25% to about 20%, about 0.5% to about 20%, about 0.75% to about 20%, about 1% to about 20%, about 1.5% to about 20%, about 2% to about 20%, about 2.5% to about 20%, about 3% to about 20%, about 4% to about 20%, about 4.5% to about 20%, and about 5% to about 20%. In a second set of ranges, the range of a nucleating agent is one of the following ranges: about 0.1% to about 10%, about 0.25% to about 10%, about 0.5% to about 10%, about 0.75% to about 10%, about 1% to about 10%, about 1.5% to about 10%, about 2% to about 10%, about 3% to about 10%, about 4% to about 10%, and about 5% to about 10% of the total formulation of the polymeric layer by weight percentage. In a third set of ranges, the range of a nucleating agent is one of the following ranges: about 0.1% to about 5%, about 0.25% to about 5%, about 0.5% to about 5%, about 0.75% to about 5%, about 1% to about 5%, about 1.5% to about 5%, about 2% to about 5%, about 2.5% to about 5%, about 3% to about 5%, about 3.5% to about 5%, about 4% to about 5%, and about 4.5% to about 5% of the total formulation of the polymeric layer by weight percentage. The nucleating agent may be up to about 5%, up to about 10%, up to about 15%, up to about 20% by weight of the polymeric formulation. In an embodiment, the polymeric formulation lacks a nucleating agent.
In certain exemplary embodiments, one or more blowing agents may be incorporated. Blowing agent may be either a physical or a chemical material (or a combination of materials) that acts to expand nucleation sites. Illustratively, nucleating agents and blowing agents may work together to control the size and or quality of the formed cell. The blowing agent acts to reduce density by forming cells in the molten resin. The blowing agent may be added to the molten resin mixture in extruder 111 through a physical blowing agent port as suggested in
In exemplary embodiments, physical blowing agents are typically gasses that are introduced as liquids under pressure into the molten resin via a port in the extruder as suggested in
Illustrative physical blowing agents include agents that are gasses. Representative examples of physical blowing agents include, but are not limited to, carbon dioxide, nitrogen, helium, argon, air, water vapor, pentane, butane, other alkane mixtures of the foregoing and the like. In some embodiments, a physical blowing agent can be selected from the group consisting of carbon dioxide, nitrogen, helium, argon, methane, pentane, butane, ethane, propane, n-butane, isobutene, n-pentane, isopentane, neopentane, methyl fluoride, perfluoromethane, ethyl fluoride, 1,1-difluoroethane, 1,1,1-trifluoroethane, 1,1,1,2-tetrafluoro-ethane, pentafluoroethane, perfluoroethane, 2,2-difluoropropane, 1,1,1-trifluoropropane, perfluoropropane, perfluorobutane, perfluorocyclobutane, methyl chloride, methylene chloride, ethyl chloride, 1,1,1-trichloroethane, 1,1-dichloro-1-fluoroethane, 1-chloro-1,1-difluoroethane, 1,1-dichloro-2,2,2-trifluoroethane, 1-chloro-1,2,2,2-tetrafluoroethane, trichloromonofluoromethane, dichlorodifluoromethane, trichlorotrifluoroethane, dichlorotetrafluoroethane, chloroheptafluoropropane, dichlorohexafluoropropane, methanol, ethanol, n-propanol, and isopropanol. In certain exemplary embodiments, a processing aid may be added to the formulation to enhance the solubility of the physical blowing agent. Alternatively, the physical blowing agent may be a hydrofluorocarbon, such as 1,1,1,2-tetrafluoroethane, also known as R134a, a hydrofluoroolefin, such as, but not limited to, 1,3,3,3-tetrafluoropropene, also known as HFO-1234ze, or other haloalkane or haloalkane refrigerant. Selection of the blowing agent may be made to consider environmental impact.
One example of a physical blowing agent is nitrogen (N2). The N2 is pumped as a supercritical fluid into the molten formulation via a port in the extruder. The molten material with the N2 in suspension then exits the extruder via a die where a pressure drop occurs. As the pressure drop happens, N2 moves out of suspension toward the nucleation sites where cells grow. Excess gas blows off after extrusion with the remaining gas trapped in the cells formed in the extrudate. Other suitable examples of physical blowing agents include, but are not limited to, carbon dioxide (CO2), helium, argon, air, pentane, butane, or other alkane mixtures of the foregoing and the like.
In an illustrative example, a physical blowing agent may be introduced at a rate of about 0.02 pounds per hour (lbs/h) to about 1.3 (lbs/h). In another illustrative example, the physical blowing agent may be introduced at a rate of about 0.03 (lbs/h) to about 1.25 (lbs/h). In another illustrative example, the physical blowing agent may be introduced at a rate of about 0.02 (lbs/h) to about 0.15 (lbs/h). In another illustrative example, the physical blowing agent may be introduced at a rate of about 0 (lbs/h) to about 0.15 (lbs/h). In another illustrative example, the physical blowing agent may be introduced at a rate of about 0.02 (lbs/h) to about 0.22 (lbs/h). In another illustrative example, the physical blowing agent may be introduced at a rate of about 0.02 (lbs/h) to about 0.25 (lbs/h). In still yet another illustrative example the physical blowing agent may be introduced at a rate of about 0.07 (lbs/h) to about 0.27 (lbs/h). In some embodiments, the physical blowing agent is used between about 0.01 lbs/h to about 0.2 lbs/h, about 0.01 lbs/h to about 0.17 lbs/h, about 0.01 lbs/h to about 0.15 lbs/h, about 0.01 lbs/h to about 0.1 lbs/h, about 0.05 lbs/h to about 0.2 lbs/h, about 0.05 lbs/h to about 0.17 lbs/h, about 0.05 lbs/h to about 0.15 lbs/h, about 0.05 lbs/h to about 0.1 lbs/h, about 0.1 lbs/h to about 0.2 lbs/h, about 0.1 lbs/h to about 0.17 lbs/h, or about 0.1 lbs/h to about 0.15 lbs/h.
In further embodiments, the physical blowing agent is measured in saturation percentage (%). In exemplary embodiments, physical blowing agent saturation can have a range that is about 0.1% to about 0.4%, about 0.1% to about 0.35%, about 0.1% to about 0.3%, about 0.1% to about 0.25%, 0.15% to about 0.4%, about 0.15% to about 0.35%, about 0.15% to about 0.3%, about 0.15% to about 0.25%, 0.2% to about 0.4%, about 0.2% to about 0.35%, about 0.2% to about 0.3%, or about 0.2% to about 0.25%.
Chemical blowing agents are materials that degrade or react to produce a gas. Chemical blowing agents may be endothermic or exothermic. Chemical blowing agents typically degrade at a certain temperature to decompose and release gas. In one aspect the chemical blowing agent may be one or more materials selected from the group consisting of azodicarbonamide, azodiisobutyro-nitrile, benzenesulfonyl hydrazide, 4,4-oxybenzene sulfonylsemicarbazide, p-toluene sulfonyl semi-carbazide, barium azodicarboxylate, N,N′-dimethyl-N,N′-dinitrosoterephthalamide, trihydrazino triazine, sodium bicarbonate, sodium carbonate, ammonium bicarbonate, ammonium carbonate, ammonium nitrite, N,N′-dinitrosopentamethylene tetramine, azobisisobutylonitrile, azocyclohexylnitrile, azodiaminobenzene, toluene sulfonyl hydrazide, p,p′-oxybis(benzene sulfonyl hydrazide), diphenyl sulfone-3,3′-disulfonyl hydrazide, calcium azide, 4,4′-diphenyl disulfonyl azide, and p-toluene sulfonyl azide. In some embodiments, the chemical blowing agent is Hydrocerol™ CF®-40E available from Clariant. In some embodiments, the chemical blowing agent is Ecocell® P available from the Polyfil Corporation.
The amount of a chemical blowing agent may be one of several different values or fall within one of several different ranges. It is within the scope of the present disclosure to select an amount of a chemical blowing agent to be one of the following values: about 0%, about 0.1%, about 0.2%, about 0.3%, about 0.4%, about 0.5%, about 0.75%, about 1%, about 1.5%, or about 2% of the total formulation of the polymeric layer by weight percentage. It is within the scope of the present disclosure for the amount of a chemical blowing agent in the formulation to fall within one of many different ranges. In a first set of ranges, the range of a chemical blowing agent is one of the following ranges: about 0% to about 5%, about 0.1% to about 5%, about 0.25% to about 5%, about 0.5% to about 5%, about 0.75% to about 5%, about 1% to about 5%, about 1.5% to about 5%, about 2% to about 5%, about 3% to about 5%, and about 4% to about 5% of the total formulation of the polymeric layer by weight percentage. In a second set of ranges, the range of a chemical blowing agent is one of the following ranges: about 0.1% to about 4%, about 0.1% to about 3%, about 0.1% to about 2%, and about 0.1% to about 1% of the total formulation by weight percentage. In a third set of ranges, the range of a chemical blowing agent is one of the following ranges: about 0.25% to about 4%, about 0.75% to about 4%, about 1% to about 4%, about 1.5% to about 4%, about 2% to about 4%, about 3% to about 4%, about 0% to about 3%, about 0.25% to about 3%, about 0.5% to about 3%, about 0.75% to about 3%, about 1% to about 3%, about 1.5%, to about 3%, about 2% to about 3%, about 0% to about 2%, about 0.25% to about 2%, about 0.5%, to about 2%, about 0.75% to about 2%, about 1% to about 2%, about 1.5% to about 2%, about 0% to about 1%, about 0.5% to about 1%, and about 0.75% to about 1% of the total formulation of the polymeric layer by weight percentage. In one aspect of the present disclosure, where a chemical blowing agent is used, the chemical blowing agent may be introduced into the material formulation that is added to the hopper.
In one aspect of the present disclosure, where a chemical blowing agent is used, the chemical blowing agent may be introduced into the resin formulation that is added to the hopper.
In one aspect of the present disclosure, the chemical blowing agent may be a decomposable material that forms a gas upon decomposition. A representative example of such a material is citric acid or a citric-acid based material. In one exemplary aspect of the present disclosure, it may be possible to use a mixture of physical and chemical blowing agents.
In one aspect of the present disclosure, at least one slip agent may be incorporated into the resin mixture to aid in increasing production rates. Slip agent (also known as a process aid) is a term used to describe a general class of materials, which are added to a resin mixture and provide surface lubrication to the polymer during and after conversion. Slip agents may also reduce or eliminate die drool. Representative examples of slip agent materials include amides of fats or fatty acids, such as, but not limited to, erucamide and oleamide. In one exemplary aspect, amides from oleyl (single unsaturated C18) through erucyl (C22 single unsaturated) may be used. Other representative examples of slip agent materials include low molecular weight amides and fluoroelastomers. Combinations of two or more slip agents can be used. Slip agents may be provided in a master batch pellet form and blended with the resin formulation. One example of a slip agent that is commercially available as AMPACET™ 102109 Slip PE MB. Another example of a slip agent that is commercially available is AMAPACET™ 102823 Process Aid PE MB. In some embodiments, the insulative cellular non-aromatic polymeric material lacks a process aid.
The amount of a slip agent may be one of several different values or fall within one of several different ranges. It is within the scope of the present disclosure to select an amount of a slip agent to be one of the following values: about 0%, about 0.5%, 1%, about 2%, about 3%, about 4%, about 5%, about 6%, about 7%, about 8%, about 9%, or about 10% of the total formulation of the polymeric layer by weight percentage. It is within the scope of the present disclosure for the amount of a slip agent in the formulation to fall within one of many different ranges. In a first set of ranges, the range of a slip agent is one of the following ranges: about 0% to about 10% (w/w), about 0.5% to about 10%, about 1% to about 10%, about 2% to about 10%, about 3% to about 10%, about 4% to about 10%, about 5% to about 10%, about 6% to about 10%, about 7% to about 10%, about 8% to about 10%, and about 9% to about 10% of the total formulation of the polymeric layer by weight percentage. In a second set of ranges, the range of a slip agent is one of the following ranges: about 0% to about 9%, about 0% to about 8%, about 0% to about 7%, about 0% to about 6%, about 0% to about 5%, about 0% to about 4%, about 0% to about 3%, about 0% to about 2%, about 0% to about 1%, and about 0% to about 0.5% of the total formulation of the polymeric layer by weight percentage. In a third set of ranges, the range of a slip agent is one of the following ranges: about 0.5% to about 5%, about 0.5% to about 4%, about 0.5% to about 3%, about 0.5%, to about 2%, about 1% to about 2%, about 1% to about 3%, about 1% to about 4%, about 1% to about 5%, about 2% to about 3%, about 2% to about 4%, and about 2% to about 5% of the total formulation by weight percentage. In an embodiment, the formulation lacks a slip agent.
One or more additional components and additives optionally may be incorporated, such as, but not limited to, impact modifiers, colorants (such as, but not limited to, titanium dioxide), and compound regrind. One example of a commercially available colorant is COLORTECH® blue-white colorant. Another example of a commercially available colorant is COLORTECH® J11 white colorant.
The amount of a colorant may be one of several different values or fall within one of several different ranges. It is within the scope of the present disclosure to select an amount of a colorant to be one of the following values: about 0%, about 0.1%, about 0.5%, about 0.6%, about 0.7%, about 0.8%, about 0.9%, about 1%, about 1.5%, about 2%, about 3%, about 4%, about 5%, about 6%, about 7%, about 8%, about 9%, 1 about 0%, about 15%, or about 20% of the total formulation of the polymeric layer by weight percentage. It is within the scope of the present disclosure for the amount of a colorant in the formulation to fall within one of many different ranges. In a first set of ranges, the range of a colorant is one of the following ranges: about 0% to about 20% (w/w), about 0% to about 10%, about 0% to about 5%, and about 0% to about 4%. In a second set of ranges, the range of a colorant is one of the following ranges: about 0.1% to about 4%, about 0.25% to about 4%, about 0.5% to about 4%, about 0.75% to about 4%, about 1% to about 4%, about 1.5% to about 4%, about 2% to about 4%, about 2.5% to about 4%, and about 3% to about 4% of the total formulation of the polymeric layer by weight percentage. In a third set of ranges, the range of a colorant is one of the following ranges: about 0% to about 3%, about 0% to about 2.5%, about 0% to about 2.25%, about 0% to about 2%, about 0% to about 1.5%, about 0% to about 1%, about 0% to about 0.5%, about 0.1% to about 3.5%, about 0.1% to about 3%, about 0.1% to about 2.5%, about 0.1% to about 2%, about 0.1% to about 1.5%, about 0.1% to about 1%, about 1% to about 5%, about 1% to about 10%, about 1% to about 15%, about 1% to about 20%, and about 0.1% to about 0.5% of the total formulation by weight percentage. In an embodiment, the formulation lacks a colorant.
In some embodiments, the polymeric formulation comprises regrind. Regrind may be formed by recovering the excess material, sometimes called a blank-carrier sheet 94, produced during a blank forming step 150, as shown in
In some embodiments, regrind comprises ink. In some embodiments, the ink is from ink layer 66. In some embodiments, regrind is substantially free of ink. In some embodiments, the regrind comprises polypropylene, polyethylene, a physical nucleating agent, a slip agent, or a combination thereof. Illustratively, regrind is substantially free of an adhesive. In some embodiments, regrind is substantially free of an epoxy. In some embodiments, regrind comprises polypropylene, polyethylene, and bi-axially oriented polypropylene (BOPP).
As described above, in some embodiments, regrind is substantially free of an adhesive. Illustratively, adhesives may present issues when included in regrind used in materials that contact food products. Illustrative adhesives include epoxies, urethanes, acrylates, maleimides or any suitable alternative. In some embodiments, regrind substantially free of an adhesive may be reincorporated back into insulative cellular non-aromatic polymeric material 82. Accordingly, the process as suggested in
It was also surprisingly found that including regrind into the formulation for insulative cellular non-aromatic polymeric material 82 had minimal negative effects on performance. As shown below in the Examples, regrind has lower melt strength that virgin resin. In particular, regrind had an average load at break of less than about 0.1 N. In some embodiments, the average load at break of the regrind may be less than 0.3 N, less than about 0.2 N, or less than about 0.1 N. In contrast, the tested virgin materials had an average load at break of at least 0.4 N. In some embodiments, the virgin materials may have an average load at break of at least 0.35 N, at least about 0.4 N, or at least about 0.45 N. Illustratively, a ratio of the average load at break for the virgin material compared to the regrind may be at about 1:1, about 2:1, about 3:1, about 4:1, or about 5:1. Accordingly, maintaining the properties of the foam when substituting regrind for virgin resin allows for improved efficiency and minimizes waste.
In some embodiments, regrind comprises ink. In some embodiments, the ink is from ink layer 66. In some embodiments, regrind is substantially free of ink. In some embodiments, the regrind comprise polypropylene, polyethylene, a physical nucleating agent, a slip agent, or a combination thereof. Illustratively, regrind is substantially free of an adhesive. In some embodiments, regrind is substantially free of an epoxy. In some embodiments, regrind comprises polypropylene, polyethylene, and BOPP.
In some embodiments, the polymeric formulation comprises regrind. It is within the scope of the present disclosure to select an amount of regrind to be up to about 5%, up to about 10%, up to about 15%, up to about 20%, up to about 25%, up to about 30%, up to about 35%, up to about 40%, up to about 45%, up to about 50%, up to about 55%, up to about 60%, up to about 65%, up to about 75%, up to about 85%, or up to about 95% by weight of the polymeric formulation. The percentage by weight of regrind in the polymeric formulation may be about 0%, about 0.5%, about 1%, about 3%, about 4%, about 5%, about 7%, about 10%, about 15%, about 20%, about 25%, about 30%, about 35%, about 40%, about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 755, about 80%, about 85%, about 90%, or about 95% by weight of the polymeric formulation. In a first set of ranges, the range of a regrind in the polymeric formulation is one of the following ranges: about 0.5% to about 95%, about 3% to about 95%, about 5% to about 95%, about 10% to about 95%, about 15% to about 95%, about 20% to about 95%, about 25% to about 95%, about 30% to about 40% to about 95%, about 50% to about 95%, about 60% to about 95%, about 75% to about 95%, or about 85% to about 95% by weight of the polymeric formulation. In a second set of ranges, the range of regrind in the polymeric formulation is one of the following ranges: about 0.5% to about 90%, about 0.5% to about 85%, about 0.5% to about 75%, about 0.5% to about 60%, about 0.5% to about 50%, about 0.5% to about 45%, about 0.5% to about 40%, about 0.5% to about 35%, about 0.5% to about 30%, about 0.5% to about 25%, about 0.5% to about 20%, about 0.5% to about 15%, or about 0.5% to about 10% by weight of the polymeric formulation. In a third set of ranges, the range of regrind in the polymeric formulation is one of the following ranges: about 1% to about 90%, about 1% to about 85%, about 1% to about 75%, about 1% to about 50%, about 3% to about 50%, about 3% to about 45%, about 5% to about 45%, about 5% to about 40%, about 5% to about 35%, about 10% to about 40%, about 10% to about 35%, about 10% to about 45%, about 20% to about 45%, about 5% to about 40%, about 5% to about 30%, about 15% to about 30%, or about 30% to about 40% by weight of the polymeric formulation.
As described herein, a polymeric formulation, sometimes illustrated as polymeric formulation as in
The insulative cellular non-aromatic polymeric material that forms insulative cellular non-aromatic polymeric material strip 82 has a density that is generally lower than a non-foamed equivalent material. It is within the scope of the present disclosure that the density of the extruded insulative cellular non-aromatic material be up to about 0.25 g/cm3, up to about 0.2 g/cm3, up to about 0.18 g/cm3, up to about 0.16 g/cm3, up to about 0.14 g/cm3, up to about 0.13 g/cm3, or up to about 0.12 g/cm3. In some embodiments, the density of the polymeric material is less than about 0.2 g/cm3, less than about 0.18 g/cm3, less than about 0.16 g/cm3, less than about 0.15 g/cm3, less than about 0.14 g/cm3, or less than about 0.13 g/cm3. The density of the insulative-cellular non-aromatic polymeric material may be about 0.01 g/cm3, about 0.03 g/cm3, about 0.05 g/cm3, about 0.06 g/cm3, about 0.07 g/cm3, about 0.08 g/cm3, about 0.09 g/cm3, about 0.1 g/cm3, about 0.11 g/cm3, about 0.12 g/cm3, about 0.13 g/cm3, about 0.14 g/cm3, about 0.15 g/cm3, about 0.16 g/cm3, about 0.18 g/cm3, about 0.2 g/cm3, or about 0.25 g/cm3. In a first set of ranges, the density of the insulative cellular non-aromatic polymeric material is one of the following ranges: about 0.01 g/cm3 to about 0.2 g/cm3, about 0.05 g/cm3 to about 0.25 g/cm3, about 0.05 g/cm3 to about 0.2 g/cm3, about 0.05 g/cm3 to about 0.19 g/cm3, about 0.07 g/cm3 to about 0.2 g/cm3, about 0.08 g/cm3 to about 0.2 g/cm3, about 0.09 g/cm3 to about 0.2 g/cm3, about 0.1 g/cm3 to about 0.2 g/cm3, about 0.11 g/cm3 to about 0.2 g/cm3, or about 0.12 g/cm3 to about 0.2 g/cm3. In a second set of ranges, the density of the insulative cellular non-aromatic polymeric material is one of the following ranges: about 0.06 g/cm3 to about 0.25 g/cm3, about 0.06 g/cm3 to about 0.2 g/cm3, about 0.06 g/cm3 to about 0.18 g/cm3, about 0.06 g/cm3 to about 0.16 g/cm3, about 0.06 g/cm3 to about 0.14 g/cm3, or about 0.06 g/cm3 to about 0.12 g/cm3. In a third set of ranges, the density of the insulative cellular non-aromatic polymeric material is one of the following ranges: about 0.05 g/cm3 to about 0.2 g/cm3, about 0.05 g/cm3 to about 0.15 g/cm3, about 0.07 g/cm3 to about 0.15 g/cm3, about 0.09 g/cm3 to about 0.15 g/cm3, about 0.11 g/cm3 to about 0.15 g/cm3, about 0.08 g/cm3 to about 0.2 g/cm3, about 0.08 g/cm3 to about 0.18 g/cm3, about 0.08 g/cm3 to about 0.16 g/cm3, about 0.08 g/cm3 to about 0.14 g/cm3, about 0.09 g/cm3 to about 0.14 g/cm3, about 0.09 g/cm3 to about 0.13 g/cm3, about 0.1 g/cm3 to about 0.14 g/cm3, or about 0.1 g/cm3 to about 0.12 g/cm3.
The insulative cellular non-aromatic polymeric material that forms insulative cellular non-aromatic polymeric material strip 82 has a thickness that is generally greater than a non-foamed equivalent material. It is within the scope of the present disclosure that the thickness of the extruded insulative cellular non-aromatic material be less than about 0.1 inches, less than about 0.08 inches, less than about 0.07 inches, or less than about 0.06 inches. In some embodiments, the thickness of the insulative cellular non-aromatic polymeric material is at least 0.01 inches, at least 0.03 inches or higher, or at least 0.04 inches.
Illustratively, the insulative cellular non-aromatic polymeric material is a polymeric material comprising cells. In illustrative embodiments, the cell morphology of an extruded sheet of insulative cellular polypropylene-based material in accordance with the present disclosure is a function of formulation and process conditions, which conditions have an effect on the quality of an article, such as an insulative container, formed therewith. In particular, the effects of such conditions on cell density and cell dimensional attributes, and ultimately on crease/wrinkle resistance, results in a wrinkle-resistance prediction model based on power law regression.
In illustrative embodiments, the cell aspect ratio of an extruded sheet of insulative cellular polypropylene-based material in accordance with the present disclosure has an effect on the wrinkle resistance of that material during mechanical convolution. Parameters such as cell density and aspect ratio contribute to the control limits that result in a wrinkle-resistance model for the extruded sheet.
Direct evidence of polymer cell structure is provided by microscopy studies. There is a close relationship between the regularity of molecular structure and malleability. Cell morphology describes polymer cell density, cell structure, cell wall thickness, cell shape, and cell size distribution of cells. Polymer cell structures may have the same general shape and appearance, being composed predominantly of oval cells, and the same lognormal cell distribution, but possess a different cell aspect ratio and cell wall thickness. Illustratively, cell aspect ratio is the ratio between lengths of the ovular polymer cells to widths of the ovular polymer cells. In some embodiments, the cell aspect ratio of the insulative cellular non-aromatic polymeric material is at least 0.5, at least 1, at least 1.1, at least 1.2, at least 1.5, at least 1.7, or at least 2. In some embodiments, the cell aspect ratio of the cells of the insulative cellular non-aromatic polymeric material is less than 7, less than 6, less than 4, less than 3.5, less than 3, less than 2.5, or less than 2. In some embodiments, the aspect ratio of the cells of the insulative cellular non-aromatic polymeric material is selected from a range of 0.5 to about 4, about 1 to about 4, about 1 to about 3.5, about 1 to about 3, or about 1 to about 2.
Illustratively, the polymer cells can have a cell aspect ratio in the machine direction (MD) and in the cross direction (CD). As confirmed by microscopy, in one exemplary embodiment the average cell dimensions in a machine direction 67 (machine or along the web direction) of an extruded strip 82 of insulative cellular non-aromatic polymeric material were about 0.0362 inches (0.92 mm) in width by about 0.0106 inches (0.27 mm) in height. As a result, a machine direction cell size aspect ratio is about 3.5. The average cell dimensions in a cross direction (cross-web or transverse direction) was about 0.0205 inches (0.52 mm) in width and about 0.0106 inches (0.27 mm) in height. As a result, a cross-direction aspect ratio is 1.94. In one exemplary embodiment, it was found that for the strip to withstand a compressive force during cup forming, one desirable average cell aspect ratio was between about 1.0 and about 3.0. In one exemplary embodiment, one desirable average cell aspect ratio was between about 1.0 and about 2.0. In another exemplary embodiment, a desirable average cell aspect ratio in the cross direction was about 0.5 to about 4. In another exemplary embodiment, a desirable average cell aspect ratio in the machine direction was about 1 to about 7.
The ratio of machine direction to cross direction cell length is used as a measure of anisotropy of the extruded strip. In exemplary embodiments, a strip of insulative cellular non-aromatic polymeric material may be bi-axially oriented, with a coefficient of anisotropy ranging between about 1.5 and about 3. In one exemplary embodiment, the coefficient of anisotropy was about 1.8.
If the circumference of the cup is aligned with machine direction 67 of extruded strip 82 with a cell aspect ratio exceeding about 3.0, deep creases with a depth exceeding about 200 microns are typically formed on inside surface of the cup making it unusable. Unexpectedly, it was found, in one exemplary embodiment, that if the circumference of the cup was aligned in the cross direction of extruded strip 82, which can be characterized by cell aspect ratio below about 2.0, no deep creases were formed inside of the cup, indicating that the cross direction of extruded strip 82 was more resistant to compression forces during cup formation.
One possible reason for greater compressibility of an extruded strip with cells having aspect ratio below about 2.0 in the direction of cup circumference, such as in the cross direction, could be due to lower stress concentration for cells with a larger radius. Another possible reason may be that the higher aspect ratio of cells might mean a higher slenderness ratio of the cell wall, which is inversely proportional to buckling strength. Folding of the strip into wrinkles in the compression mode could be approximated as buckling of cell walls. For cell walls with a longer length, the slenderness ratio (length to diameter) may be higher. Yet another possible factor in relieving compression stress might be a more favorable polymer chain packing in cell walls in the cross direction allowing polymer chain re-arrangements under compression force. Polymer chains are expected to be preferably oriented and more tightly packed in machine direction 67.
The insulative-cellular non-aromatic polymeric materials in accordance with the present disclosure may have a cell density of about 1×105 to about 2.5×106 cells/in3.
In exemplary embodiments, alignment of the formed cup circumference along the direction of the extruded strip has a cell aspect ratio below about 2.0. As a result, the surface of extruded strip with crystal domain size below about 100 angstroms facing inside the cup may provide favorable results of achieving a desirable surface topography with imperfections less than about 5 microns deep.
A material-forming process 100 uses a polymeric formulation in accordance with the present disclosure to produce a strip 82 of insulative cellular non-aromatic polymeric material as shown in
Material-forming process 100 includes an extruding stage 110, a laminating stage 130, a blank forming stage 150, a cup forming stage 170, and a regrinding stage 190, as shown in
Cup forming stage 170 forms cup 10 from body blank 92, as shown in
The formulation and insulative cellular non-aromatic polymeric material of the present disclosure satisfies a long-felt need for a material that can be formed into an article, such as a cup, that includes many if not all of the features of insulative performance, ready for recyclability, puncture resistance, frangibility resistance, microwavability and other features as discussed herein. Others have failed to provide a material that achieves combinations of these features as reflected in the appended claims. This failure is a result of the features being associated with competitive design choices. As an example, others have created materials and structures therefrom that based on design choices are insulated but suffer from poor puncture resistance, inability to effectively be recyclable, and lack microwavability. In comparison, the formulations and materials disclosed herein overcome the failures of others by using an insulative cellular non-aromatic polymeric material. Reference is hereby made to U.S. application Ser. No. 13/491,007 filed Jun. 7, 2012, and entitled INSULATED CONTAINER for disclosure relating to articles, such as cups, formed from such insulative cellular non-aromatic polymeric materials, which application is hereby incorporated in its entirety herein. Reference is hereby made to U.S. application Ser. No. 14/462,073 filed Aug. 18, 2014, and entitled POLYMERIC MATERIAL FOR AN INSULATED CONTAINER for disclosure relating to insulative cellular non-aromatic polymeric materials, which application is hereby incorporated in its entirety herein.
An insulative cup 10 in accordance with the present disclosure can be formed during a cup forming process. Localized plastic deformation is provided in accordance with the present disclosure in, for example, four regions of a body 11 of insulative cup 10 comprising an insulative cellular non-aromatic polymeric material as suggested in
Aromatic molecules typically display enhanced hydrophobicity when compared to non-aromatic molecules. As a result, it would be expected that changing from a polystyrene-based insulative cellular polymeric material to a polypropylene-based insulative cellular polymeric material would result in a change in hydrophobicity with a concomitant, but not necessarily predictable or desirable, change in surface adsorption properties of the resulting material. In addition, by virtue of the hydrocarbon chain in polystyrene, wherein alternating carbon centers are attached to phenyl groups, neighboring phenyl groups can engage in so-called pi-stacking, which is a mechanism contributing to the high intramolecular strength of polystyrene and other aromatic polymers. No similar mechanism is available for non-aromatic polymers such as polypropylene. Moreover, notwithstanding similar chemical reactivity and chemical resistance properties of polystyrene and polypropylene, polystyrene can be either thermosetting or thermoplastic when manufactured whereas polypropylene is exclusively thermoplastic. As a result, to the extent that surface adsorption properties, manufacturing options, and strength properties similar to those of polystyrene are sought, likely alternatives to polystyrene-based insulative cellular polymeric materials would be found in another aromatic polymer rather than in a non-aromatic polymer.
In illustrative embodiments, the insulative cellular non-aromatic polymeric material is used as a substrate in a composite sheet that includes a film laminated to the insulative cellular non-aromatic polymeric material. The film is reverse printed before being laminated to the substrate so that the printing is visible through the film, with the film forming a protective cover over the printing. In some embodiments, the film is not reverse printed.
In illustrative embodiments, the insulative cellular non-aromatic polymeric material may include one or more polypropylene materials as a base material. The laminated film is also polypropylene so that the entire cup may be ground up and re-used in the same process.
In one illustrative aspect, an exemplary polypropylene-based insulative cellular non-aromatic polymeric material formed as an insulative cellular non-aromatic polymeric material sheet may have a thickness ranging from about 60 mils to about 80 mils. In another illustrative aspect, an exemplary polypropylene-based insulative cellular non-aromatic polymeric material formed as an insulative cellular non-aromatic polymeric material sheet may have a density ranging from about 0.05 g/cm3 to about 0.20 g/cm3. The insulative cellular non-aromatic polymeric material is used in cup-manufacturing process 100 to produce insulative cup 10 having a region of localized plastic deformation. The region of localized plastic deformation may be the result of compressing the insulative cellular non-aromatic polymeric material. The region of localized plastic deformation has a first density in a range of about 0.3 g/cm3 to about 0.4 g/cm3. The insulative cellular non-aromatic polymeric material surrounding the region of localized plastic deformation is uncompressed and has a second density in a range of about 0.05 g/cm3 to about 0.20 g/cm3.
In another illustrative aspect, an exemplary polypropylene-based insulative cellular non-aromatic polymeric material formed as a strip of insulative cellular non-aromatic polymeric material may have a tensile strength in the machine direction and cross direction ranging from about 4.0 MPa to about 7.0 MPa and from about 3.0 MPa to about 6.0 MPa, respectively. In another illustrative aspect, an exemplary polypropylene-based insulative cellular non-aromatic polymeric material formed as a strip of insulative cellular non-aromatic polymeric material may have an elastic modulus in the machine direction and cross direction ranging from about 160 MPa to about 240 MPa and from about 120 MPa to about 170 MPa, respectively.
In another illustrative aspect, an exemplary insulative cellular non-aromatic polymeric material formed as a strip of insulative cellular non-aromatic polymer material may have cells in the shape of oriented, stretched ovals. In another illustrative aspect, an exemplary polypropylene-based insulative cellular non-aromatic polymeric material formed as a strip of insulative cellular non-aromatic polymeric material may average cell dimensions in machine direction of about 0.0362 inches (0.92 mm) in width by 0.0106 inches (0.27 mm) in height, resulting in a machine direction cell size aspect ratio of about 3.5. The average cell dimensions in cross direction or transverse to machine direction 67 are about 0.0204 inches (0.52 mm) in width and about 0.0106 inches (0.27 mm) in height, resulting in a cross direction cell size aspect ratio of 1.94. As a result, the aspect ratio of foam cells is between about 1.0 and 3.0. In another example, the aspect ratio of foam cells is between about 1.0 and about 2.0.
Another potential feature of an insulative cup formed of insulative cellular non-aromatic polymeric material according to the present disclosure is that the cup can be placed in and go through a conventional residential or commercial dishwasher cleaning cycle (top rack) without noticeable structural or material breakdown or adverse effect on material properties. This is in comparison to beaded expanded polystyrene cups or containers, which can break down under similar cleaning processes. Accordingly, a cup made according to one aspect of the present disclosure can be cleaned and reused.
Another potential feature of an insulative cup formed of insulative cellular non-aromatic polymeric material according to various aspects of the present disclosure is that the insulative cup and scrap material can be recycled. Recyclable means that a material can be added (such as regrind) back into an extrusion or other formation processes without segregation of components of the material. As an example, an insulative cup formed the insulative cellular non-aromatic polymeric material does not have to be manipulated to remove one or more materials or components prior to re-entering the extrusion process.
In another example, an insulative cup formed from a sheet including a printed film skin laminated to an exterior of an insulative cellular non-aromatic polymeric material may be recyclable if one does not need to separate out the film layer prior to the insulative cup being ground into particles. In contrast, a paper-wrapped expanded polystyrene cup may not be recyclable because the polystyrene material could not practicably be used as material in forming an expanded polystyrene cup, even though the cup material may possibly be formed into another product.
As a further example, an insulative cup formed from a non-expanded polystyrene material having a layer of printed film adhered thereto may be considered non-recyclable because it would require the segregation of the film layer, which would not be desirable to introduce as part of the regrind into the extrusion process. Recyclability of articles formed using the insulative cellular non-aromatic polymeric material of the present disclosure minimizes the amount of disposable waste created. In comparison, beaded expanded polystyrene cups that break up into beads and thus ordinarily cannot be reused easily in a manufacturing process with the same material from which the article was formed. In addition, paper cups that typically have an extrusion coated plastic layer or a plastic lamination for liquid resistance ordinarily cannot be recycled because the different materials (paper, adhesive, film, and plastic) normally cannot be practicably separated in commercial recycling operations.
A potential feature of an insulative cup formed of insulative cellular non-aromatic polymeric material according to one aspect (a non-laminate process) of the present disclosure is that the outside (or inside or both) wall surface of the insulative cellular polypropylene sheet (prior to being formed into an insulative cup, or during cup formation, depending on the manufacturing process employed) can accept printing of high-resolution graphics. In contrast, beaded expanded polystyrene cups have a surface which typically is not smooth enough to accept printing other than low-resolution graphics. Like beaded expanded polystyrene cups, uncoated paper cups also typically do not have a smooth enough surface for such high-resolution graphics. Paper cups have difficulty reaching insulation levels and require a designed air gap incorporated into or associated with the paper cup to achieve insulation. Such designed air gap may be provided by a sleeve slid onto and over a portion of the paper cup.
In some embodiments, the polymeric material, a laminated sheet comprising the polymeric material, or a cup formed of the laminated sheet has a puncture resistance, as measured in inches for either a ¼″ probe or a ⅛″ probe. In some embodiments, the puncture resistance for the polymeric material, the laminated sheet, or the cup (elongation at peak load) is at least about 0.2 inches. In some embodiments, the puncture resistance for the polymeric material, the laminated sheet, or the cup (elongation at peak load) is less than about 0.75 inches.
In some embodiments, the polymeric material, a laminated material comprising the polymeric material, or the cup formed of the laminated material were tested using the Elmendorf test method described in ASTM D1922-93. In some embodiments, the Elmendorf Arm MD for the polymeric material is at least about 500 g. In some embodiments, the Elmendorf Arm MD for the laminated material is at least about 1500 g. In some embodiments, the Elmendorf Arm MD for the cup is at least about 1500 g. In some embodiments, the Elmendorf Arm TD for the polymeric material is at least about 500 g. In some embodiments, the Elmendorf Arm TD for the laminated material is at least about 1500 g. In some embodiments, the Elmendorf Arm TD for the cup is at least about 1500 g.
It is within the scope of the present disclosure that the density of the multi-layer sheet be up to about 0.25 g/cm3, up to about 0.2 g/cm3, up to about 0.18 g/cm3, up to about 0.16 g/cm3, up to about 0.14 g/cm3, up to about 0.13 g/cm3, or up to about 0.12 g/cm3. In some embodiments, the density of the multi-layer sheet is less than about 0.2 g/cm3, less than about 0.18 g/cm3, less than about 0.16 g/cm3, less than about 0.15 g/cm3, less than about 0.14 g/cm3, or less than about 0.13 g/cm3. The density of the multi-layer sheet may be about 0.01 g/cm3, about 0.03 g/cm3, about 0.05 g/cm3, about 0.06 g/cm3, about 0.07 g/cm3, about 0.08 g/cm3, about 0.09 g/cm3, about 0.1 g/cm3, about 0.11 g/cm3, about 0.12 g/cm3, about 0.13 g/cm3, about 0.14 g/cm3, about 0.15 g/cm3, about 0.16 g/cm3, about 0.18 g/cm3, about 0.2 g/cm3, or about 0.25 g/cm3. In a set of ranges, the density of the multi-layer sheet is one of the following ranges: about 0.01 g/cm3 to about 0.2 g/cm3, about 0.05 g/cm3 to about 0.19 g/cm3, about 0.05 g/cm3 to about 0.18 g/cm3, about 0.05 g/cm3 to about 0.17 g/cm3, about 0.1 g/cm3 to about 0.17 g/cm3, about 0.11 g/cm3 to about 0.17 g/cm3, or about 0.12 g/cm3 to about 0.16 g/cm3.
In some embodiments, cup 10 formed of multi-layer sheet 80 was tested using the Elmendorf test method described in ASTM D1922-93. In some embodiments, the Elmendorf Tear MD for the polymeric material is at least about 75 gf. In some embodiments, the Elmendorf Tear MD for the polymeric material is less than about 350 gf. In some embodiments, the Elmendorf Tear MD for the laminated material is at least about 65 gf. In some embodiments, the Elmendorf Tear MD for the laminated material is less than about 700 gf. In some embodiments, the Elmendorf Tear MD for cup 10 is at least about 125 gf, at least about 200 gf, at least about 300 gf, or at least about 400 gf. In some embodiments, the Elmendorf Tear MD for cup 10 is less than about 700 gf, less than about 600 gf, less than about 500 gf. In some embodiments, the Elmendorf Tear MD for cup 10 is in a range of about 200 gf to about 700 gf, about 300 gf to about 700 gf, about 400 gf to about 700 gf, or about 400 gf to about 600 gf.
In some embodiments, the Elmendorf Tear TD for the polymeric material is at least about 10 gf, at least about 50 gf, or at least about 125 gf. In some embodiments, the Elmendorf Tear TD for the polymeric material is less than about 450 gf. In some embodiments, the Elmendorf Tear TD for the laminated material is at least about 65 gf, at least about 100 gf, or at least about 200 gf. In some embodiments, the Elmendorf Tear TD for the laminated material is less than about 600 gf. In some embodiments, the Elmendorf Tear TD for cup 10 at least about 200 gf, at least about 300 gf, or at least about 400 gf. In some embodiments, the Elmendorf Tear TD for cup 10 is less than about 700 gf or less than about 650 gf. In some embodiments, the Elmendorf Tear TD of cup 10 is about 200 gf to about 700 gf, about 300 gf to about 700 gf, or about 400 gf to about 700 gf.
In some exemplary embodiments, a cup formed from the polymeric material can have a frangibility measurement measured when the cup is either hot or cold. In some embodiments, the cup has a frangibility of at least about 20 lbf when the cup is hot. In some embodiments, the cup has a frangibility less than about 60 lbf when the cup is hot. In some embodiments, the cup has a frangibility of at least about 25 lbf when the cup is cold. In some embodiments, the cup has a frangibility less than about 55 lbf when the cup is cold.
In some embodiments, a cup formed from the polymeric material reaches a temperature when filled with hot liquid. In some embodiments, the hot fill temperature (max side wall) is at least about 130° C. In some embodiments, the hot fill temperature (max side wall) is less than about 170° C. In some embodiments, the hot fill temperature (min internal) is at least about 135° C. In some embodiments, the hot fill temperature (min internal) is less than about 160° C.
In some exemplary embodiments, the polymeric material has a melting crystallinity at 5° C./min, 10° C./min or 15° C./min. In some exemplary embodiments, the melting crystallinity at 5° C./min is at least about 20%. In some exemplary embodiments, the melting crystallinity at 5° C./min is up to about 60%. In some exemplary embodiments, the melting crystallinity at 10° C./min is at least about 10%. In some exemplary embodiments, the melting crystallinity at 10° C./min is up to about 60%. In some exemplary embodiments, the melting crystallinity at 15° C./min is at least about 15%. In some exemplary embodiments, the melting crystallinity at 15° C./min is up to about 65%.
In some embodiments, the polymeric material, a laminated sheet comprising the polymeric material, or a cup formed of the laminated sheet has a puncture resistance, as measured in inches for either a ¼″ probe or a ⅛″ probe. In some embodiments, the puncture resistance for the polymeric material, the laminated sheet, or the cup (elongation at peak load) is at least about 0.2 inches. In some embodiments, the puncture resistance for the polymeric material, the laminated sheet, or the cup (elongation at peak load) is less than about 0.75 inches.
In some embodiments, cup 10 formed of the multi-layer sheet 80 has a puncture resistance, as measured in max load for either a ¼″ probe or a ⅛″ probe. In some embodiments, the puncture resistance for cup 10 (max load) is at least about 1,000 gf, at least about 3,000 gf, at least about 6,000 gf, at least about 8,000 gf, at least about 9,000 gf, or at least about 9,500 gf. In some embodiments, the puncture resistance for the cup 10 (max load) is less than about 20,000 gf, less than about 18,000 gf, less than about 12,000 gf, or less than about 10,000 gf. In some embodiments, the puncture resistance for cup 10 (max load) is in a range of about 1,000 gf to about 12,000 gf, about 3,000 gf to about 12,000 gf, about 6,000 gf to about 12,000 gf, about 7,000 gf to about 12,000 gf, about 7,000 gf to about 11,000 gf, about 8,000 gf to about 11,000 gf, about 8,000 gf to about 10,000 gf, or about 9,000 gf to about 10,000 gf.
In some exemplary embodiments, cup 10 has a seam. In some embodiments, the seam thickness is at least about 0.03 inches. In some embodiments, the seam thickness is less than about 1.2 inches.
In some embodiments, cup 10 or the polymeric material has a thermal conductivity at 21° C. In some embodiments, the thermal conductivity at 21° C. is at least about 0.05 W/m-K or at least about 0.052 W/m-K. In some embodiments, the thermal conductivity at 21° C. is less than about 0.057 W/m-K, less than about 0.056 W/m-K, or less than about 0.053 W/m-K. In some embodiments, cup 10 has a thermal conductivity at 21° C. in a range of about 0.05 W/m-K to about 0.06 W/m-K, about 0.05 W/m-K to about 0.059 W/m-K, about 0.052 W/m-K to about 0.059 W/m-K, or about 0.054 W/m-K to about 0.057 W/m-K.
In some embodiments, cup 10 has a thermal conductivity at 93° C. In some embodiments, the thermal conductivity at 93° C. is at least about 0.061 W/m-K or at least about 0.062 W/m-K. In some embodiments, the thermal conductivity at 93° C. is less than about 0.065 W/m-K, less than about 0.064 W/m-K, or less than about 0.0642 W/m-K. In some embodiments, cup 10 has a thermal conductivity at 93° C. in a range of about 0.061 W/m-K to about 0.065 W/m-K, about 0.063 W/m-K to about 0.065 W/m-K, about 0.063 W/m-K to about 0.0645 W/m-K.
In some embodiments, cup 10, when filled with a hot liquid has a time to cool from about 200° F. to about 140° F. In some embodiments, the time to cool is at least 3400 seconds. In some embodiments, the time to cool extended past the allotted measured time.
In some embodiments, cup 10 has a top load measurement. In some embodiments, the top load is at least about 70 lbf, at least about 90 lbf, or at least about 115 lbf. In some embodiments, the top load is less than about 200 lbf, less than about 175 lbf, or less than about 150 lbf. In some embodiments, the top load is in a range of about 70 lbf to about 250 lbf, about 70 lbf to about 200 lbf, about 70 lbf to about 180 lbf, about 70 lbf to about 160 lbf, about 80 lbf to about 160 lbf, about 90 lbf to about 160 lbf, or about 100 lbf to about 160 lbf.
In some embodiments, cup 10 formed of multi-layer sheet 80 has a weight. In some embodiments, the weight of the cup is at least about 9 g, at least about 10 g, or at least about 12 g. In some embodiments, the weight of the cup is less than about 15 g, less than about 14 g, or less than about 12 g. Illustratively, cup 10 may be formed to be a 12 oz. cup, a 14 oz. cup, a 16 oz. cup, an 18 oz. cup, a 20 oz. cup, a 22 oz. cup, a 24 oz. cup, a 26 oz. cup, a 28 oz. cup, or a 30 oz. cup.
In some embodiments, the multi-layer sheet consists of the film layer, the insulative cellular non-aromatic polymeric layer, and the polymeric-lamination layer. In some embodiments, the multi-layer sheet consists of the film layer, the insulative cellular non-aromatic polymeric layer, the polymeric-lamination layer, and an ink layer printed onto the film layer to locate the film layer between the ink layer and the polymeric-lamination layer.
In some embodiments, the polymeric-lamination layer consists of regrind, polypropylene, polyethylene, and a colorant. In some embodiments, the polymeric-lamination layer consists essentially of regrind, polypropylene, and polyethylene.
A potential feature of an insulative cup formed of insulative cellular non-aromatic polymeric material according to the present disclosure is that insulative cup is resistant to puncture, such as by a straw, fork, spoon, fingernail, or the like, as measured by standard impact testing, as described hereinbelow. Test materials demonstrated substantially higher impact resistance when compared to a beaded expanded polystyrene cup. As a result, an insulative cup in accordance with the present disclosure may minimize the likelihood of puncture and leakage of hot liquid.
Insulative cup 10 of the present disclosure satisfies a long-felt need for a vessel that includes many if not all the features of insulative performance, regrindability, ready for recyclability, high-quality graphics, chemical resistance, puncture resistance, frangibility resistance, stain resistance, microwavability, and resistance to leaching undesirable substances into products stored in the interior region of the drink cup as discussed above. Others have failed to provide a vessel that achieves combinations of these features as reflected in the appended claims. This failure is a result of the many features being associated with competitive design choices. As an example, others have created vessels that based on design choices are insulated but suffer from poor puncture resistance, lack of microwavability, and leech undesirable substances into products stored in the interior region. In comparison, insulative cup 10 overcomes the failures of others by using an insulative cellular non-aromatic polymeric material.
Reference is hereby made to U.S. application Ser. No. 13/491,007 filed Jun. 7, 2012, and entitled INSULATED CONTAINER for disclosure relating to insulative containers, which application is hereby incorporated in its entirety herein.
EXAMPLESThe following examples are set forth for purposes of illustration only. Parts and percentages appearing in such examples are by weight unless otherwise stipulated. All ASTM, ISO, and other standard test method cited or referred to in this disclosure are incorporated by reference in their entirety.
Example 1—Formulation and ExtrusionA base resin blend comprised DAPLOY™ WB140 polypropylene homopolymer (available from Borealis A/S) and F020HC high crystallinity polypropylene homopolymer, available from Braskem. The base resin blend was blended with: Hydrocerol® CF-40E™ as a chemical blowing agent (CBA), talc as a physical nucleation agent, CO2 as a physical blowing agent, a slip agent, and Ampacet blue-white as a colorant. The colorant can be added to the base resin or to the secondary resin and may be done prior to mixing of the two resins. Percentages were:
The formulation was added to an extruder hopper. The extruder heated the formulation to form a molten resin mixture. CO2 was added to the molten resin mixture to expand the resin and reduce density. The formed mixture was extruded through a die head into a strip.
A polymeric-lamination layer comprised Dow 4012 LDPE and ExxonMobil™ 3155 PP3155. The two resins were blended with J11 as the colorant.
Percentages by weight were:
The formulation was added to an extruder hopper. The extruder heated the formulation to form a molten resin mixture. The molten mixture was between the film (Jindal Films Bicor™ 18 LPX-2) and the insulative cellular non-aromatic polymeric material described above to form the multi-layer sheet. Blanks were cut from the multi-layer sheet and used to form cups in accordance with the present disclosure.
Example 2Insulative Cellular Non-Aromatic Polymeric Material Properties.
The properties insulative cellular non-aromatic material of Example 1 were evaluated according to procedures known in the art and are shown in Table 1.
Multi-Layer Sheet Properties.
The properties of the multi-layer sheet formed according to Example 1 are shown below in Table 2.
Cup Properties
A cup was formed using the multi-layer sheet of Example 1. The properties for the cup are shown in Table 3.
A base resin blend comprised Braskem Amppleo® 1025MA, JPP MFX6 PP Resin, and Braskem TI215OC. The base resin blend was blended with regrind and a chemical blowing agent. The chemical blowing agent was Ecocell® P. Percentages were about:
The formulation was added to an extruder hopper. The extruder heated the formulation to form a molten resin mixture. The molten mixture was extruded between the extruded insulative cellular non-aromatic polymeric material and the film, as suggested in
A polymeric-lamination layer comprised reground insulative cellular-nonaromatic polymeric material and Flint Hills P9H8M-015 Polypropylene. The two resins were blended with Colortech E-1274 Blue White as the colorant.
Percentages by weight were about:
The formulation was added to an extruder hopper. The extruder heated the formulation to form a molten resin mixture. The molten mixture was extruded between the extruded insulative cellular non-aromatic polymeric material and the film, as suggested in
The resulting composite material had properties according to Table 4.
An example of the regrinding process is described in the Figures. Amppleo® 1025MA from Braskem, Daploy™ WB140 HMS from Borealis, Waymax MFX6 from JPP, and regrind material were tested for melt elasticity. Briefly, the resins were extruded using an extruder having a wheel position about 114 mm below the die, ambient wheel temperature, a barrel diameter of 12 mm, a die entry angle of about 180°, a 2 mm die diameter, a 30 mm die length, with a 6 minute preheat time and a 200° C. barrel temperature. The experiments were repeated in triplicate. The results are shown in Table 5.
Polymeric material for forming the cup bottom was prepared as follows. A base resin blend comprised a high melt strength polypropylene, a polypropylene homopolymer, and a polypropylene elastomer. The base resin blend was blended with regrind, a chemical blowing agent, an antioxidant, and a nucleating agent. Percentages were:
The formulation was added to an extruder hopper. The extruder heated the formulation to form a molten resin mixture. CO2 was added to the molten resin mixture to expand the resin at a rate of 11.8 lbs/hr. The formed mixture was extruded through a die head into a strip.
Although only a number of exemplary embodiments have been described in detail above, those skilled in the art will readily appreciate that many modifications are possible in the exemplary embodiments without materially departing from the novel teachings and advantages. Accordingly, all such modifications are intended to be included within the scope of this disclosure as defined in the following claims.
As used in the specification and the appended claims, the singular forms “a,” “an” and “the” include plural referents unless the context clearly dictates otherwise. Ranges may be 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.
“Optional” or “optionally” means that the subsequently described event or circumstance may or may not occur, and that the description includes instances where said event or circumstance occurs and instances where it does not.
Throughout the description and claims of this specification, the word “comprise” and variations of the word, such as “comprising” and “comprises,” means “including but not limited to,” and is not intended to exclude, for example, other additives, components, integers or steps. “Exemplary” means “an example of” and is not intended to convey an indication of a preferred or ideal embodiment. “Such as” is not used in a restrictive sense, but for explanatory purposes.
Disclosed are components that can be used to perform the disclosed methods, equipment, and systems. These and other components are disclosed herein, and it is understood that when combinations, subsets, interactions, groups, etc. of these components are disclosed while specific reference of each various individual and collective combinations and permutation of these may not be explicitly disclosed, each is specifically contemplated and described herein, for all methods, equipment, and systems. This applies to all aspects of this application including, but not limited to, steps in disclosed methods. Thus, if there are a variety of additional steps that can be performed it is understood that each of these additional steps can be performed with any specific embodiment or combination of embodiments of the disclosed methods.
It will be apparent to those skilled in the art that various modifications and variations can be made without departing from the scope or spirit of the present disclosure. Other embodiments will be apparent to those skilled in the art from consideration of the specification and practice disclosed herein. It is intended that the specification and examples be considered as exemplary only.
It should further be noted that any publications and brochures referred to herein are incorporated by reference in their entirety.
Claims
1. An insulative cup comprising
- a container formed to include an interior region bounded by a side wall and a floor, wherein the side wall includes an inner surface and an outer surface and comprises an insulative cellular non-aromatic polymeric material,
- a film layer having an inner surface coupled to and substantially surrounding the outer surface of the side wall of the container, and
- a polymeric-lamination layer extending between and interconnecting the outer surface of the side wall and the film layer.
Type: Application
Filed: Jun 30, 2021
Publication Date: Oct 21, 2021
Inventors: John B. EULER (Evansville, IN), Anvit GUPTA (Evansville, IN), Gerald S. SUTTON (Boonville, IN), Chris BOLEK (Evansville, IN)
Application Number: 17/363,551
