1. Field of the Invention
The present invention relates generally to articles having one or more undercuts and to processes for making such articles. More specifically, the present invention relates generally to thermoformed articles having one or more undercuts and to processes for making such articles.
2. Description of the Related Art
Many polyester-based packages and containers available in today's market, especially those produced from thermoforming processes, have various types of undercuts. An “undercut” is any internal or external projection of the nominal wall of a formed article that is perpendicular to the open face of the form or die used to produce the formed article. Undercuts can have a number of different functions. For example, undercuts can be used to prevent the formed article from stripping from the mold during production. Undercuts are also widely used for snap fit assemblies and other fastening applications. They can also be used to enhance the aesthetics of the formed article or enable stacking features within the formed articles.
The size of strippable undercuts is largely dependent upon the size and shape of the mold as well as the plastic material used to produce them. However, undercuts on thermoformed articles have always been limited in size due to the modulus or stiffness of the plastics used to produce them. Furthermore, undercuts on thermoformed parts have traditionally been limited to soft, smoothly blended contours with relatively large radii due to the limitations of the plastics used to produce them.
Accordingly, there is a need for a thermoplastic article having deep undercuts that do not exhibit the deficiencies presently found in conventional thermoplastic articles with undercuts.
One embodiment of the present invention concerns a thermoformed article comprising a wall and an undercut projecting from the wall. The undercut presents an apex and has a maximum undercut draw depth and an average undercut thickness measured at the apex. The ratio of the maximum undercut draw depth to the average undercut thickness is at least 0.5:1. Furthermore, at least a portion of the undercut and at least a portion of the wall are formed from a common layer of a polyester-containing material having a specific gravity of less than 1.
Another embodiment of the present invention concerns a thermoformed article comprising a pair of spaced-apart walls defining a cavity therebetween and an undercut projecting from one of the walls. The undercut presents an apex and has a maximum undercut draw depth and a cross-sectional undercut area measured at the apex. The maximum undercut draw depth is at least 15 millimeters. In addition, the cavity has a cross-sectional cavity and the ratio of the cross-sectional cavity area to the cross-sectional undercut area is at least 1:1 and not more than 100:1. Furthermore, at least a portion of the undercut and at least a portion of the wall from which the undercut projects are formed from a common layer of a polyester-containing material having a void volume of at least 5 percent.
Yet another embodiment of the present invention concerns a method of making a thermoformed article. The method comprises: (a) thermoforming a sheet into a thermoformed item by forcing the sheet into contact with a shaped surface of a mold while said sheet is maintained at an elevated thermoforming temperature, wherein the shaped surface comprises an undercut-forming surface for providing the thermoformed item with an undercut having a maximum undercut draw depth of at least 10 millimeters; (b) cooling the thermoformed item below the thermoforming temperature to thereby provide a cooled thermoformed item; and (c) separating the cooled thermoformed item from contact with the mold by moving the cooled thermoformed item and/or the mold in a pull direction without having first retracted the undercut-forming surface of the mold from the undercut in a direction other than the pull direction.
Embodiments of the present invention are described herein with reference to the following drawing figures, wherein:
In one or more embodiments described herein, the present invention is directed to articles having one or more types of deep undercuts. As used herein, an “undercut” is understood to be any internal or external projection of the nominal wall of a formed article that extends perpendicular to the open face of the form or die used to produce the formed article. Undercuts are one of the plastic product designer's favorite design details. They are widely used for snap fit assemblies and other locating and fastening applications. They are also used to add aesthetically-pleasing details or to enable stacking features within formed parts. As discussed below in further detail, the undercuts described herein provide one or more advantages over undercuts typically found on conventional articles.
In various embodiments described herein, an article is provided that comprises at least one undercut projecting from one of the walls of the article. Generally, the articles described herein comprise a thermoformed article. In one or more embodiments, a thermoformed article is provided that comprises a pair of spaced-apart walls defining a cavity therebetween and an undercut projecting from one of the walls.
In order to better understand the subsequent discussion regarding the undercuts described herein, the initial focus is placed on the embodiments depicted in
The configuration of the undercuts described herein can be determined using a variety of different measurements. Certain of these measurements are illustrated in
The actual dimensions of the undercuts are dependent upon the size and shape of the article as well as the material used to produce the article. Furthermore, the type of mold used to produce the article can influence the number and size of undercuts in an article. For example, female molds generally enable a greater number of undercuts than male molds because of plastic shrinkage. As a rule, the size of undercuts on a female mold will depend on the length, width, and depth of the mold, the location of the undercuts, as well as the thickness and properties of the plastic material to be used, most notably stiffness and toughness.
In various embodiments described herein, at least a portion of the thermoformed articles are formed from a polyester-containing material. In such embodiments, at least a portion of the undercut and at least a portion of the wall in the article can be formed from a common layer of this polyester-containing material.
In one or more embodiments, the polyester-containing material comprises a foamed polyester. In such embodiments, the foamed polyester can have a void volume of at least about 1, 5, 10, 15, 20, 30, or 40 percent and/or not more than about 90, 80, 70, 60, or 50 percent. Further, the foamed polyester can have a void volume of about 5 to about 80 percent, about 15 to about 60 percent, or about 30 to about 50 percent. These foamed polyesters can be produced using any known and conventional method known in the art. For example, the foamed polyesters can be produced using direct gas injection and/or chemical agent foaming.
Some of the possible benefits associated with using foamed polyesters in the articles include, for example, increased opacity in the article; improved flexibility without the use of plasticizers or modifiers; decreased specific gravity which makes the article more sustainable; decreased amount of polyester-containing material needed to produce the articles, and improved yield (i.e., number of articles per unit mass of plastic). Foamed polyesters are generally more resilient, tougher, and flexible than other translucent or opaque low specific gravity polymers used in the prior art, such as, for example, high impact polystyrene. This increased flexibility and resiliency provided by the foamed polyesters can allow for more design freedom in the produced articles. For instance, the foamed polyesters described herein can enable the formation of greater undercuts in an article than is possible with other prior art polymers.
In one or more embodiments, the polyester-containing material has a specific gravity of at least about 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, or 0.9 and/or not more than about 1.4, 1.3, 1.1, 1.0, 0.9, 0.8, 0.7, 0.6, 0.5, 0.4, 0.3, or 0.2. In another embodiment, the polyester-containing material has a density of at least about 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, or 0.9 g/cc and/or not more than 1.3, 1.1, 0.9, 0.7, 0.5, 0.4, or 0.2 g/cc.
In various embodiments, the polyester-containing material can have a Young's Modulus of at least about 50, 100, 200, 300, 400, 500, 600, 700, or 800 Mpa as measured according to ASTM D882. Additionally or alternatively, the polyester-containing material can have a Young's Modulus of not more than about 5,000, 4,000, 3,000, 2,000, 1,000, or 800 Mpa as measured according to ASTM D882.
In various embodiments, the polyester-containing material has an elongation at break percentage of at least 1, 5, 10, 25, 50, 75, 85, or 95 percent as measured according to ASTM D882. Additionally or alternatively, the polyester-containing material can have an elongation at break percentage of not more than about 500, 250, 150, 125, or 125 percent as measured according to ASTM D882.
In various embodiments, the polyester-containing material has a tear resistance energy of at least about 50, 75, 100, 125, 150, 175, or 200 N-mm as measured according to ASTM D1004. In certain embodiments, the polyester-containing material has a total tear energy of at least about 0.001, 0.01, 0.05, 0.1, 0.25, 0.5, 1.0, or 1.5 J as measured according to ASTM D1004.
In various embodiments, the polyester-containing material has an instrumental impact of at least about 0.1, 0.5, 1.0, 1.5, 2.0, or 2.5 J as measured according to ASTM D3763.
In various embodiments, the polyester-containing material can be opaque and can block at least about 25, 50, 75, 90, 95, or 99 percent of light attempting to pass through it as measured according to ASTM D003 in conjunction with ASTM D1746.
Generally, flexible and tough materials like foamed polyesters will be easier to strip from the mold without damaging the article compared to materials like polystyrene. The increased ductility allows the material to flex while stripping off the undercut. In contrast, the brittle behavior of acrylics, impact polystyrene, or crystalline polystyrene used in prior art articles cause the articles to be overstressed or even crack with the same amount of flexing.
In various embodiments, the polyester-containing material comprises an acid component and a glycol component. In one or more embodiments, the glycol component comprises ethylene glycol; cyclohexanedimethanol; diethylene glycol; neopentyl glycol; 2,2,4,4-tetramethyl-1,3-cyclobutanediol; or mixtures thereof. In one embodiment, the glycol component comprises cyclohexanedimethanol and/or 2,2,4,4-tetramethyl-1,3-cyclobutanediol. In certain embodiments, the acid component comprises terephthalic acid, isophthalic acid, or a combination thereof. In another embodiment, the polyester-containing material comprises a polyethylene ethylene terephthalate glycol-modified (“PETG”) polyester. Exemplary polyesters that may be used as the polyester-containing material are further described in U.S. Pat. No. 7,838,620, the entire disclosure of which is incorporated herein by reference. One specific example of a polyester-containing material suitable for use in the articles of the present invention is Tritan™ Copolyester MP100, which is available from Eastman Chemical Company of Kingsport, Tenn.
Various types of additives can be added to the polyester-containing material in order to enhance particular properties. These additives can include, for example, a chain extender, a branching agent, or a combination thereof. In one embodiment, the polyester-containing material comprises a chain extender. In another embodiment, the polyester-containing material comprises a branching agent. For example, the polyester-containing material can comprise one or more branching agents in an amount of at least about 0.01, 0.05, or 0.1 mole percent and/or not more than about 10, 5, or 1.5 mole percent. The branching agent can comprise, for example, an acidic branching agent with a tri-functional or greater monomer, an alcoholic branching agent with a tri-functional or greater monomer, or a combination thereof.
The toughness of the polyester-containing material can be increased by, for example, increasing the branching agent therein, decreasing the amount of foam to increase the density, and/or coextruding or coinjecting the article with natural polyester skin layers.
Using the polyester-containing material described above, undercuts with varying dimensions can be produced. In one or more embodiments, the undercuts can have a maximum draw depth of at least about 10, 15, 18, 22, 24, 26, 28, or 30 mm and/or not more than about 100, 75, 50, 40, or 35 mm. In another embodiment, the undercuts have a cross-sectional area of at least about 50, 100, 150, 200, 250, 300, 350, or 400 mm2 and/or not more than about 2,500, 1,500, 1,000, 800, 600, or 500 mm2. In yet another embodiment, the undercuts have an average thickness of at least 5, 10, 15, or 20 mm and/or not more than about 50, 40, 30, or 25 mm. In still yet another embodiment, the article comprises a ratio of maximum undercut draw depth to average undercut thickness of at least about 0.5:1, 0.6:1, 0.7:1, 0.8:1, 0.9:1, 1:1, 1.1:1, 1.2:1, 1.3:1, 1.4:1, or 1.5:1 and/or not more than about 10:1, 8:1, 6:1, 4:1, or 2:1. In certain embodiments, the article can comprise at least two undercuts having different maximum draw depths and/or cross-sectional areas.
In various embodiments, the height (H) of the article is at least about 20, 25, 30, 35, 40, 45, or 50 mm and/or not more than about 1,000, 500, 250, 100 or 75 mm. In one embodiment, the article comprises a ratio of wall height to maximum undercut draw depth of at least about 0.5:1, 0.75:1, 1:1, 1.25:1, or 1.5:1 and/or not more than about 50:1, 30:1, 20:1, 15:1, 10:1, 6:1, or 4:1. In another embodiment, the article comprises a ratio of wall height to average undercut thickness of at least about 0.5:1, 0.75:1, 1:1, 1.25:1, or 1.5:1 and/or not more than about 50:1, 30:1, 20:1, 15:1, 10:1, 6:1, or 4:1.
As previously discussed in regard to
The article described herein may comprise a monolayered or multilayered structure. In various embodiments, the article comprises at least 1, 2, or 3 layers and/or not more than 10, 6, or 4 layers. In such embodiments, these layers can be used to form the undercuts and/or walls of the article. In one embodiment, the average thickness of the layer or layers forming the undercut and/or wall is at least about 0.01, 0.05, 0.75, 0.1, 0.2, 0.3, 0.4, or 0.5 mm and/or not more than about 10, 8, 6, 4, 2, 1.5, 1.25, or 1 mm. In another embodiment, the ratio of the average undercut thickness to the average thickness of the layer or layers of the undercut and/or wall is at least about 2:1, 3:1, 4:1, 5:1, or 6:1 and/or not more than about 50:1, 30:1, 20:1, or 10:1.
As mentioned above, the article can comprise a minimum undercut radius of curvature. In various embodiments, the minimum undercut radius of curvature is at least about 0.01, 0.05, 0.1, 0.2, or 0.5 mm and/or not more than about 10, 5, 2, 1, or 0.75 mm. In certain embodiments, the article can comprise at least two undercuts having different minimum radii of curvature.
Because undercuts generally require further stretching of the sheet stock, it can be important to keep the draw depth or ratio in mind when designing undercuts. Normally, the distance that the undercut projects into the article is kept to a minimum. With most materials like polystyrene, impact polystyrene, acrylics and the like, it is not generally advisable to have undercuts of more than 0.5 inches (12.7 mm), with typical undercut depths being less than 0.375 inches (9.525 mm). In contrast, due to the flexibility and durability of the polyester-containing materials described herein, deeper undercuts compared to the prior art are possible.
As noted above, the articles described herein generally can be thermoformed articles. The articles described herein can be used, for example, in packaging or transporting food products, medical instruments, and other products which are typically sterilized before consumption or use. In one embodiment, the undercuts are configured to secure a product within the cavity of the article. In another embodiment, the undercuts are configured to provide design aesthetics to the article. In yet another embodiment, the undercuts are configured to provide denesting properties to the article.
In one embodiment, the article comprises a sterilized article. In another embodiment, the article comprises a tray. In yet another embodiment, the article comprises a medical packaging.
In various embodiments, a process for producing a thermoformed article is provided. The process can include the steps of (a) foaming a polyester-containing material to form a foamed polyester; (b) forming a sheet from the foamed polyester using a flat sheeting die; and (c) thermoforming the sheet into the thermoformed article. The thermoforming can comprise, for example, vacuum forming, pressure forming, or a combination thereof.
In various embodiments, a processes for producing a thermoformed article, where the process comprises (a) thermoforming a sheet into a thermoformed item by forcing the sheet into contact with a undercut-forming shaped surface of a mold while the sheet is maintained at an elevated thermoforming temperature; (b) cooling the thermoformed item below the thermoforming temperature to thereby provide a cooled thermoformed item; and (c) separating the cooled thermoformed item from contact with the mold by moving the cooled thermoformed item and/or the mold in a pull direction. In certain embodiments, in step (c), the undercut-forming shaped surface of the mold is only retracted from the formed undercut in the pull direction and not in any other direction.
The thermoforming steps described herein can occur, for example, at temperatures of at least about 40, 60, 80, or 100° C. and/or not more than about 250, 200, 150, or 100° C. The cooling step described herein can reduce the temperature of the thermoformed item to, for example, a temperatures of at least about 10, 20, 30, 40, or 50° C. and/or not more than about 200, 150, 75, or 50° C.
It should be noted that the processes described herein can utilize a male mold or a female mold to produce the article. Thus, the methods of production described herein are equally applicable for producing articles with internal and/or external undercuts.
This invention can be further illustrated by the following examples of embodiments thereof, although it will be understood that these examples are included merely for the purposes of illustration and are not intended to limit the scope of the invention unless otherwise specifically indicated.
In this example, the opacity and light blocking properties of the foamed polyester-containing material were tested. In order to produce the thermoplastic article, a polyester resin (Tritan™ Copolyester MP100 from Eastman Chemical Company) was dried in desiccant dryers using standard practices at −40° C. dew point air and 1 cfm air flow/lb/hr of resin to achieve a polyester pellet with a residual moisture content below 200 ppm.
Sheeting of the foamed polyester pellet was performed on a Welex extrusion line with a standard 3.5″, 24/1 L/D Egan-Davis-Standard extruder/screw with a barrier and a Maddock mixing section design. Foaming of the polyester was achieved during this step by introducing a gas or chemical blowing agent directly into the extrusion chamber with the polyester pellet. Consequently, a core layer (i.e., layer B) was formed containing the foamed polyester resin. In addition, unfoamed skin layers (i.e., layer A) were separately produced from the polyester pellets using a 1.5″ 24/1 L/D Egan-Davis-Standard satellite extruder with a barrier screw design. Typical copolyester extrusion temperatures (about 470° F. to 480° F.) were used in the above extrusion processes. A Welex feed block was then used in the feed block to direct the flow of the melted polyesters from the extruders to a 36″ wide Cloeren coat hanger flat sheet type die in order to produce a multilayered sheet having an A/B/A configuration. The temperatures of the feed block and die were lowered as much as possible, but high enough to prevent excess pressure or motor amps. Generally, the temperature at the feed block and die was about 400° F. to 450° F.
The sheets exiting the die were allowed to cool on a three-roll vertical chill roll stack. The roll gap was set to that of the desired overall sheet thickness, but a minimum amount of nip pressure was applied. Once cooled by the roll stack, the sheet was transported upstream of the die and wound onto cores as normal sheet/film extrusion practice. The produced sheet had an A/B/A configuration, meaning that it had a foamed polyester core (layer B) and unfoamed polyester skins (layer A).
The opacity and light blocking properties of the foamed polyester core (layer B) were then tested using a Perk and Elmer UV-Vis Spectroscope. Using the process described above, two separate sheets were produced. Both sheets contained an A/B/A configuration as described above, but the foamed core layer differed in thickness (15 mil and 40 mil). The foamed polyester in both samples had a density of 0.55 g/cc.
In this example, the change in the flexibility of the sheeting was compared to the specific gravity of the polyester. For this example, sheets containing the A/B/A configuration were produced from Tritan™ Copolyester MP100 from Eastman Chemical Company and Eastar™ Copolyester GN001 from Eastman Chemical Company using the process described in Example 1. In order to test the influence of the polyester's specific gravity on the flexibility of the resulting sheets, the Young's Modulus was measured according to ASTM D882 for each sheet along with the foamed polyester's specific gravity. These results are depicted in TABLE 1 and
In this example, the maximum undercut depth for thermoformed articles produced using various types of polymers was analyzed. Sheets having the A/B/A configuration were produced in accordance with the procedure outlined in Example 1 above. Samples A1-A4 contained a foamed core layer (layer B) and were produced from Tritan™ Copolyester MP100 and Eastar™ Copolyester GN001 (both from Eastman Chemical Company). Samples B1-B8 contained unfoamed core layers (layer B) and were produced from various rigid polymers including PCTG, PETG, rigid PVC, Eastar™ Copolyester GN001, high impact polystyrene, amorphous PET, impact acrylic, polystyrene, and acrylic. The rigid PVD was from Formosa Plastics and the high impact polystyrene was from Americas Styrenics. The rest of the tested polymers were from Eastman Chemical Company. TABLE 2, below, depicts the specific gravity, Young's Modulus measured according to ASTM D882, and elongation at break measured according to ASTM D882 for each of the samples.
In order to determine the maximum depth of the undercuts for each of the sheet samples, thermoformed articles were produced using samples A1-A4 and B1-B8. The thermoforming process was performed using standard conditions known in the art and varied depending on the material being thermoformed. The maximum draw depth for each article was estimated by observing each of the above samples in the thermoforming trials. As shown in TABLE 2, foamed samples A1-A4 were able to produce undercuts having a greater maximum draw depth.
In this example, the effect of branching agents on the tear resistance energy of the sheet was observed. Sheets having an A/B/A configuration were produced from Tritan™ Copolyester MP100 (CoPET1) and Eastar™ Copolyester GN001 (CoPET2) using the process described in Example 1. To demonstrate the effects of a branching agent, separate sheets were produced using CoPET1 and CoPET2 which had a branching agent (Joncryl J4368 from BASF) added therewith prior to producing the sheets. More specifically, two separate sheets were created from CoPET1 having 0.3 weight percent of the branching agent and 1.2 weight percent of the branching agent. Likewise, an additional sheet was produced from CoPET2 having 1.2 weight percent of the branching agent. The core layers (layer B) in all these sheets were foamed.
In this example, the effect of skin layer thickness on tear resistance was observed. Sheets were produced from Eastar™ Copolyester GN001 in accordance with the process described in Example 1. In order to determine the effect of skin layer thickness, sheets having the A/B/A configuration, where B was the foamed layer, were compared to a single foamed layer without skin layers (i.e., layer B by itself). The tear resistance of each sheet was measured according to ASTM D1004. As shown in
In this example, the effect of skin layer thickness on instrumental impact was observed. Sheets were produced from Tritan™ Copolyester MP100 and Eastar™ Copolyester GN001 in accordance with the process described in Example 1. In order to determine the effect of skin layer thickness, sheets having the A/B/A configuration, where B was the foamed layer, were produced having skin layers (layers A) having varying thickness. In addition, a single foamed layer without skin layers (i.e., layer B by itself) was produced from Eastar™ for comparison purposes. The instrumental impact of each sheet was measured according to ASTM D3763. As shown in
In this example, thermoformed articles were producing using an array of polymer compositions. The articles were produced using the processes described in Examples 1 and 3. TABLE 3, below, provides the various measurements of these thermoformed articles. These articles included trays which generally contained at least one cavity. A channel refers to a cavity within the tray. Unless otherwise indicated, all samples were unfoamed. The tested polymers included Tritan™ Copolyester MP100 and Eastar™ Copolyester GN001 (“PETG”). The PVC was from Formosa, the HIPS was from Americas Styrenics, and the COC was from TOPAS. The last two foamed samples had an A/B/A configuration, the PETG/COC sample had a 5 layer configuration (PETG/tie/COC/tie/PETG), and the remaining samples had only one layer.
The preferred forms of the invention described above are to be used as illustration only, and should not be used in a limiting sense to interpret the scope of the present invention. Modifications to the exemplary embodiments, set forth above, could be readily made by those skilled in the art without departing from the spirit of the present invention.
The inventors hereby state their intent to rely on the Doctrine of Equivalents to determine and assess the reasonably fair scope of the present invention as it pertains to any apparatus not materially departing from but outside the literal scope of the invention as set forth in the following claims.
This application claims priority to U.S. Provisional Application No. 61/835,211 filed Jun. 14, 2013, the disclosure of which is incorporated herein by reference in its entirety.
Number | Date | Country | |
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61835211 | Jun 2013 | US |