This disclosure generally relates to plastic containers for retaining a commodity, and in particular a liquid commodity. More specifically, this disclosure relates to a plastic preform and resultant container having a groove formed in the molded surface where threads of a given closure will ride during capping.
As a result of environmental and other concerns, plastic containers, more specifically polyester and even more specifically polyethylene terephthalate (PET) containers are now being used more than ever to package numerous commodities previously supplied in glass containers. Manufacturers and fillers, as well as consumers, have recognized that PET containers are lightweight, inexpensive, recyclable and manufacturable in large quantities.
Blow-molded plastic containers have become commonplace in packaging numerous commodities. PET is a crystallizable polymer, meaning that it is available in an amorphous form or a semi-crystalline form. The ability of a PET container to maintain its material integrity relates to the percentage of the PET container in crystalline form, also known as the “crystallinity” of the PET container. The following equation defines the percentage of crystallinity as a volume fraction:
where ρ is the density of the PET material; ρa is the density of pure amorphous PET material (1.333 g/cc); and ρc is the density of pure crystalline material (1.455 g/cc).
Container manufacturers use mechanical processing and thermal processing to increase the PET polymer crystallinity of a container. Mechanical processing involves orienting the amorphous material to achieve strain hardening. This processing commonly involves stretching an injection molded PET preform along a longitudinal axis and expanding the PET preform along a transverse or radial axis to form a PET container. The combination promotes what manufacturers define as biaxial orientation of the molecular structure in the container. Manufacturers of PET containers currently use mechanical processing to produce PET containers having approximately 20% crystallinity in the container's sidewall.
Thermal processing involves heating the material (either amorphous or semi-crystalline) to promote crystal growth. On amorphous material, thermal processing of PET material results in a spherulitic morphology that interferes with the transmission of light. In other words, the resulting crystalline material is opaque, and thus, generally undesirable. Used after mechanical processing, however, thermal processing results in higher crystallinity and excellent clarity for those portions of the container having biaxial molecular orientation. The thermal processing of an oriented PET container, which is known as heat setting, typically includes blow molding a PET preform against a mold heated to a temperature of approximately 250° F.-350° F. (approximately 121° C.-177° C.), and holding the blown container against the heated mold for approximately two (2) to five (5) seconds. Manufacturers of PET juice bottles, which must be hot-filled at approximately 185° F. (85° C.), currently use heat setting to produce PET bottles having an overall crystallinity in the range of approximately 25%-35%.
Typically, an upper portion of the plastic container defines an opening. This upper portion is commonly referred to as a finish and includes some means for engaging a cap or closure to close off the opening. In the traditional injection-stretch blow molding process, the finish remains substantially in its injection molded state while the container body is formed below the finish. The finish may include at least one thread extending radially outwardly around an annular sidewall defining a thread profile. In one application, a closure member or cap may define a complementary thread, or threads, that are adapted to cooperatively mate with the threads of the finish. Generally, clockwise rotation of the cap encourages an upper surface of the cap threads to be retained by lower surfaces of the threads on the finish. In some applications, however, external thread profiles formed on the finish may require a non-desirable large amount of material to manufacture.
Accordingly, the present disclosure provides a finish for a plastic container including an upper portion having a mouth defining an opening into the container. At least one groove is defined around a radial sidewall of the upper portion. The groove slopes gradually downward along the radial sidewall and away from the opening.
A preform adapted to be molded into a plastic container includes an upper portion having a mouth defining an opening into the container. The preform includes at least one groove defined around a radial sidewall of the upper portion. The groove slopes gradually downward along the radial sidewall to a terminal end.
A closure member is adapted to selectively mate with a finish on a container. The closure member includes a lower portion defining an opening and an upper portion defining a cover. At least one thread is formed on an inner surface of a radial sidewall extending between the lower portion and the upper portion.
Additional benefits and advantages of the present disclosure will become apparent to those skilled in the art to which the present disclosure relates from the subsequent description and the appended claims, taken in conjunction with the accompanying drawings.
The following description is merely exemplary in nature, and is in no way intended to limit the disclosure or its application or uses.
This disclosure provides for a container finish having a significantly reduced weight, while enhancing the interface between a closure member or cap and the container, and meeting filling line temperature and speed demands. Significant weight reductions are achieved through the elimination of material from the container wall of a standard thread profile as well as the elimination of material in other areas of the finish, which represent areas where plastic can be removed without negatively affecting the sealability function of the closure member or cap and the container.
Additionally, a by-product of the disclosed container finish is an improvement to closure function. In this regard, the disclosed finish may be less damaging to frangible connectors incorporated in tamper-evidence closures, reducing the potential for premature closure/tamper-evidence band separation during application. The smoother, more cylindrical finish disclosed provides an opportunity to keep an applied closure member or cap more concentric with the finish, reducing the potential for uneven loading on the frangible connectors which secure the tamper-evidence band to the body of the closure member or cap. Such stability improves tamper-evidence band separation.
Traditionally, the distance between the top seal surface of a container and the start of the container's threads varies slightly during normal production. As this distance varies, it affects the rotational position of an applied closure, and thus the relative location of the tamper-evidence band retention features to the mating features on the finish. The disclosed container finish eliminates the above-mentioned distance and variability, and thereby contributes to improved tamper-evidence band closure performance.
With initial reference to
The groove entrance 32 is generally defined at an intersection between an inward sweeping radial lip 36 and an outward sweeping radial lip 38. As best illustrated in
As shown in
The pair of grooves 30 of the finish 10 each define a debossed (grooved) threaded profile around the annular sidewall 18. When compared to traditional injection molded finishes having an embossed (raised) threaded profile, the finish 10 of the present disclosure may represent a material savings of about 15% to about 20% of the overall container weight and more specifically about 50%, in weight, of traditional injection molded finishes. The present disclosure is particularly useful in hot-fill applications where thicker, heavier finishes have been required to withstand the heat generated from hot-fill processes thereby allowing for traditional opening diameters and finish wall thicknesses to be maintained while significantly light weighting the container. Thus, the disclosed finish 10 is capable of withstanding the rigors associated with hot-fill processes, resulting in the same or less distortion as is found in traditional container designs having thicker, heavier finishes.
In another advantage over traditional threaded finish containers, a finish 10 having grooves 30 is more comfortable for a user's mouth to engage and therefore drink from. In this way, a user's mouth can rest more comfortably on a finish free of projecting threads. Furthermore, it is easier for a user to form a seal between their mouth and the finish 10 having grooves 30 as compared to a finish having projecting threads.
A plastic container may be designed to retain a commodity during a thermal process, typically a hot-fill process. For hot-fill bottling applications, bottlers generally fill the container with a liquid or product at an elevated temperature between approximately 155° F. to 205° F. (approximately 68° C. to 96° C.) and seal the container at the finish 10 with the closure member or cap 12 before cooling. In addition, the plastic container may be suitable for other high-temperature pasteurization or retort filling processes or other thermal processes as well.
Turning now to
With continued reference to
Turning now to
The mold cavity (not illustrated) may be heated to a temperature between approximately 250° F. to 350° F. (approximately 121° C. to 177° C.). A stretch rod apparatus (not illustrated) stretches or extends the heated preform 50 within the mold cavity to a length approximately that of the resultant container thereby molecularly orienting the polyester material in an axial direction generally corresponding with a central longitudinal axis of the resultant container. While the stretch rod extends the preform 50, air having a pressure between 300 PSI to 600 PSI (2.07 MPa to 4.14 MPa) assists in extending the preform 50 in the axial direction and in expanding the preform 50 in a circumferential or hoop direction thereby substantially conforming the polyester material to the shape of the mold cavity and further molecularly orienting the polyester material in a direction generally perpendicular to the axial direction, thus establishing the biaxial molecular orientation of the polyester material in most of the container. Typically, material within the finish 10 and a sub-portion of the base are not substantially molecularly oriented. The pressurized air holds the mostly biaxial molecularly oriented polyester material against the mold cavity for a period of approximately two (2) to five (5) seconds before removal of the container from the mold cavity.
Alternatively, other manufacturing methods using other conventional materials including, for example, polypropylene, high density polyethylene, polyethylene naphthalate (PEN), a PET/PEN blend or copolymer, and various multilayer structures may be suitable for the manufacture of plastic containers. Those having ordinary skill in the art will readily know and understand plastic container manufacturing method alternatives.
The preform 50 may be defined in terms of complementary features of a finished container. For exemplary purposes, a formed plastic container 56 is shown in phantom in
With specific reference now to
With reference to
To initiate gripping of the threads 70 within the respective grooves 30, the closure member or cap 12 may be placed on the top 14 and rotated until both leads of threads 70 are accepted at the groove entrance 32. The ramp 40 (
The closure member or cap 12 is shown with the TE band 47. The closure member or cap 12 can also generally include a cover 80 at an upper end. The TE band 47 is further defined by a band body 82 and a flap 84 extending therefrom. The flap 84 extends generally inboard of the band body 82. The TE band 47 of the closure member or cap 12 is designed to ride over the annular sidewall 18 of the finish 10 in a forward (downward) direction when the closure member or cap 12 is initially applied to the plastic container 56. When the closure member or cap 12 is initially unscrewed (moved upward), the flap 84 engages the annular sidewall 18 and thereafter breaks away the TE band 47 from the closure member or cap 12. The prevention of the TE band 47 moving back up on the finish 10 when the closure member or cap 12 is removed creates the necessary engagement interface and force that effectively removes the TE band 47 from the closure member or cap 12, leaving it on the container finish 10.
Turning now to
In one example, a machine (not illustrated) places the preform 100 heated to a temperature between approximately 190° F. to 250° F. (approximately 88° C. to 121° C.) into the mold cavity 102. The mold cavity 102 may be heated to a temperature between approximately 250° F. to 350° F. (approximately 121° C. to 177° C.). A stretch rod apparatus (not illustrated) stretches or extends the heated preform 100 within the mold cavity 102 to a length approximately that of the intermediate container 110, thereby molecularly orienting the polyester material in an axial direction generally corresponding with a central longitudinal axis 120 of the intermediate container 110. While the stretch rod extends the preform 100, air having a pressure between 300 PSI to 600 PSI (2.07 MPa to 4.14 MPa) assists in extending the preform 100 in the axial direction and in expanding the preform 100 in a circumferential or hoop direction thereby substantially conforming the polyester material to the shape of the mold cavity 102 and further molecularly orienting the polyester material in a direction generally perpendicular to the axial direction, thus establishing the biaxial molecular orientation of the polyester material in most of the intermediate container 110. The pressurized air holds the mostly biaxial molecularly oriented polyester material against the mold cavity 102 for a period of approximately two (2) to five (5) seconds before removal of the intermediate container 110 from the mold cavity 102.
In another example, a machine (not illustrated) places the preform 100 heated to a temperature between approximately 185° F. to 239° F. (approximately 85° C. to 115° C.) into the mold cavity 102. The mold cavity 102 may be chilled to a temperature between approximately 32° F. to 75° F. (approximately 0° C. to 24° C.). A stretch rod apparatus (not illustrated) stretches or extends the heated preform 100 within the mold cavity 102 to a length approximately that of the intermediate container 110, thereby molecularly orienting the polyester material in an axial direction generally corresponding with the central longitudinal axis 120 of the intermediate container 110. While the stretch rod extends the preform 100, air having a pressure between 300 PSI to 600 PSI (2.07 MPa to 4.14 MPa) assists in extending the preform 100 in the axial direction and in expanding the preform 100 in a circumferential or hoop direction thereby substantially conforming the polyester material to the shape of the mold cavity 102 and further molecularly orienting the polyester material in a direction generally perpendicular to the axial direction, thus establishing the biaxial molecular orientation of the polyester material in most of the intermediate container 110. The pressurized air holds the mostly biaxial molecularly oriented polyester material against the mold cavity 102 for a period of approximately two (2) to five (5) seconds before removal of the intermediate container 110 from the mold cavity 102. This process is utilized to produce containers suitable for filling with product under ambient conditions or cold temperatures.
Alternatively, other manufacturing methods using other conventional materials including, for example, polypropylene, high density polyethylene, polyethylene naphthalate (PEN), a PET/PEN blend or copolymer, and various multilayer structures may be suitable for the manufacture of the intermediate container 110. Those having ordinary skill in the art will readily know and understand container manufacturing method alternatives.
Once the intermediate container 110 has been formed, the intermediate container 110 may be removed from the mold cavity 102. As can be appreciated, the intermediate container 110 defines the resultant container and the moil 116 prior to formation of the opening 16 (
While the above description constitutes the present disclosure, it will be appreciated that the disclosure is susceptible to modification, variation and change without departing from the proper scope and fair meaning of the accompanying claims.
This application is a continuation-in-part of U.S. patent application Ser. No. 11/698,009 filed Jan. 25, 2007, now U.S. Pat. No. 7,918,356, issued Apr. 5, 2011. U.S. patent application Ser. No. 11/698,009 claims a benefit of U.S. Provisional Patent Application No. 60/763,203 filed on Jan. 27, 2006. The entire disclosures of each of the above applications are incorporated herein by reference.
Number | Name | Date | Kind |
---|---|---|---|
3497096 | Smith et al. | Feb 1970 | A |
3757487 | Fauth | Sep 1973 | A |
4005799 | Mannaerts | Feb 1977 | A |
4257526 | Weits et al. | Mar 1981 | A |
4373641 | Banich et al. | Feb 1983 | A |
4730747 | Schiemann | Mar 1988 | A |
4895265 | Luch et al. | Jan 1990 | A |
4896782 | Hawkins et al. | Jan 1990 | A |
4993571 | Conti | Feb 1991 | A |
5533633 | King | Jul 1996 | A |
5702014 | Nielsen | Dec 1997 | A |
5845798 | Carrier | Dec 1998 | A |
6415935 | Hins | Jul 2002 | B1 |
6471909 | Czesak | Oct 2002 | B1 |
6561369 | Clodfelter et al. | May 2003 | B1 |
6841117 | Smith et al. | Jan 2005 | B1 |
6989124 | Miller et al. | Jan 2006 | B2 |
7207451 | Taylor et al. | Apr 2007 | B2 |
7455914 | Bromley et al. | Nov 2008 | B2 |
7531125 | Dygert et al. | May 2009 | B2 |
7918355 | Penny | Apr 2011 | B2 |
7918356 | Penny | Apr 2011 | B2 |
20050067365 | Hanafusa et al. | Mar 2005 | A1 |
20050205575 | Kobayashi et al. | Sep 2005 | A1 |
20050263476 | Harrison et al. | Dec 2005 | A1 |
20070175854 | Penny | Aug 2007 | A1 |
20070175855 | Penny | Aug 2007 | A1 |
Number | Date | Country |
---|---|---|
3916797 | Dec 1989 | DE |
2631932 | Dec 1989 | FR |
11-222217 | Aug 1999 | JP |
2000-326998 | Nov 2000 | JP |
2003-339822 | Dec 2003 | JP |
2004-035036 | Feb 2004 | JP |
2005-001677 | Jan 2005 | JP |
2005-170475 | Jun 2005 | JP |
2005-212872 | Aug 2005 | JP |
WO 9100220 | Jan 1991 | WO |
WO 9422734 | Oct 1994 | WO |
WO 03057583 | Jul 2003 | WO |
WO 2004041669 | May 2004 | WO |
WO 2005097610 | Oct 2005 | WO |
WO 2007089552 | Aug 2007 | WO |
WO 2007089566 | Aug 2007 | WO |
Number | Date | Country | |
---|---|---|---|
20100270255 A1 | Oct 2010 | US |
Number | Date | Country | |
---|---|---|---|
60763203 | Jan 2006 | US |
Number | Date | Country | |
---|---|---|---|
Parent | 11698009 | Jan 2007 | US |
Child | 12648462 | US |