This disclosure generally relates to containers for retaining a commodity, such as a solid or liquid commodity. More specifically, this disclosure relates to a blown polyethylene terephthalate (PET) container having a blown container finish including a threaded area and a tamper evident (TE) band area.
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%.
In many applications, it is desirable to provide a closure or cap for mating with a finish of the bottle or container. Many such bottle and cap combinations are designed with a Tamper Evident (TE) breakaway band on the cap. Such a band is attached to the cap when initially applied to the corresponding bottle finish and upon opening the bottle for the first time, the band is designed to break away from the cap and remain on the bottle. Since the band can only break away one time, the resulting effect proves whether or not a bottle has been tampered with, or more specifically, if the cap has been removed prior to the actual customer opening the bottle.
With reference to
Within the realms of the PET blow molding industry, where it is desirable to convert injection molded PET performs into blow molded PET containers, it has been shown that any blow moldable detail that is designed and built into any given blow mold, be sized in such a way that ensures duplication of that mold detail onto the moldable surface of the given container. The inherent nature of PET causes the molded container to become stiffer as it biaxially orientates. As a result, it is important to define any embossed detail as having a height dimension (i.e. in a direction along the axis of the container) to be sufficiently greater than a depth dimension (i.e. in a direction generally transverse to the axis of the container).
Accordingly, the present disclosure provides a container and a method of making a container. In one example, the container includes a body having an upper portion, a sidewall portion and a base portion. The upper portion includes a blown finish defining a longitudinal axis and an opening into the container. A first portion defines a tamper evident (TE) band formed on the finish and defines a first diameter at an outermost surface. A second portion is formed on the finish, offset toward the base portion relative to the first portion and defines a second diameter. The second diameter is less than the first diameter. A transition portion is formed between the first and second portions. The transition portion defines an annular taper from the first portion to the second portion.
According to additional features, a third portion is formed on the finish and offset away from the base portion relative to the first portion and defines a third diameter. A difference between the first diameter and the third diameter defines a TE band depth. A height defined along the longitudinal axis between the second portion and the third portion defines a TE band height. The TE band height is substantially about three times the TE band depth. The first portion defines a first height along the longitudinal axis. The transition portion defines a transition height along the longitudinal axis. The first height and the transition height collectively define the TE band height. The transition height is at least 25% of the TE band height.
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.
The container 10 according to the present teachings defines a body 20 and includes an upper portion 22 having a finish 24. The finish 24 defines an opening 30 into the container 10. Integrally formed with the finish 24 and extending downward therefrom is a shoulder region 32. The shoulder region 32 merges into and provides a transition between the finish 24 and a sidewall portion 36. The sidewall portion 36 extends downward from the shoulder region 32 to a base portion 40 having a base 42. An upper bumper portion 44 may be defined at a transition between the shoulder region 32 and the sidewall portion 36. A lower bumper portion 45 may be defined at a transition between the base portion 40 and the sidewall portion 36.
Those skilled in the art know and understand that a neck (not illustrated) may also be included having an extremely short height, that is, becoming a short extension from the finish 24, or an elongated height, extending between the finish 24 and the shoulder region 32. The container 10 has been designed to retain a commodity. The commodity may be in any form such as a solid or liquid product. In one example, a liquid commodity may be introduced into the container 10 during a thermal process, typically a hot-fill process. For hot-fill bottling applications, bottlers generally fill the container 10 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 10 with the cap 12 before cooling. In addition, the container 10 may be suitable for other high-temperature pasteurization or retort filling processes or other thermal processes as well. In another example, the commodity may be introduced into the container 10 under ambient temperatures.
With continued reference to
Exemplary dimensions for the finish 24 will be described. It is appreciated that other dimensions may be used. A diameter D1 is defined at an outermost surface 86 of the TE band 50 (also identified as A-diameter, A2). A diameter D2 is defined at an outer surface 90 of the second portion 60 (also identified as B-diameter, B2). A diameter D3 is defined at an outer surface 92 of the third portion 80. A TE band depth 94 is defined laterally between the outermost surface 86 of the TE band 50 and the outer surface 92 of the third portion 80. A TE band height 98 is defined along the longitudinal axis 84 of the finish 24 between the second portion 60 and the third portion 80. In this way, the TE band height 98 is defined collectively by a first portion height 100 and a transition portion height 102. The transition portion height 102 is at least 25% of the TE band height 98. An aspect ratio is defined between the TE band height 98 relative to the TE band depth 94. According to the present teachings, the blow-molded PET finish provides an aspect ratio in the range of approximately 2.5:1 to 4:1, and preferably 3:1.
The threaded region 46 provides a means for attachment of a similarly threaded closure or cap, such as the cap 12. Alternatives may include other suitable devices that engage the finish 24 of the container 10. Accordingly, the closure or cap engages the finish 20 to preferably provide a hermetical seal of the container 10.
With continued reference to
Turning now to
The container 10 of the present invention is a blow molded, biaxially oriented container with a unitary construction from a single or multi-layer material. A well-known stretch-molding, heat-setting process for making the container 10 generally involves the manufacture of a preform 122 (
Turning now to
In one example, a machine (not illustrated) places the preform 122 heated to a temperature between approximately 190° F. to 250° F. (approximately 88° C. to 121° C.) into the mold cavity 124. The mold cavity 124 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 122 within the mold cavity 124 to a length approximately that of the intermediate container 136 thereby molecularly orienting the polyester material in an axial direction generally corresponding with the central longitudinal axis 84 of the container 10. While the stretch rod extends the perform 122, air having a pressure between 300 PSI to 600 PSI (2.07 MPa to 4.14 MPa) assists in extending the preform 122 in the axial direction and in expanding the preform 122 in a circumferential or hoop direction thereby substantially conforming the polyester material to the shape of the mold cavity 124 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 136. The pressurized air holds the mostly biaxial molecularly oriented polyester material against the mold cavity 124 for a period of approximately two (2) to five (5) seconds before removal of the intermediate container 136 from the mold cavity 124.
In another example, a machine (not illustrated) places the preform 122 heated to a temperature between approximately 185° F. to 239° F. (approximately 85° C. to 115° C.) into the mold cavity 124. The mold cavity 124 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 122 within the mold cavity 124 to a length approximately that of the intermediate container thereby molecularly orienting the polyester material in an axial direction generally corresponding with the central longitudinal axis 84 of the container 10. While the stretch rod extends the preform 122, air having a pressure between 300 PSI to 600 PSI (2.07 MPa to 4.14 MPa) assists in extending the preform 122 in the axial direction and in expanding the preform 122 in a circumferential or hoop direction thereby substantially conforming the polyester material to the shape of the mold cavity 124 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. The pressurized air holds the mostly biaxial molecularly oriented polyester material against the mold cavity 124 for a period of approximately two (2) to five (5) seconds before removal of the intermediate container from the mold cavity 124. 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, polyethylene naphthalate (PEN), a PET/PEN blend or copolymer, and various multilayer structures may be suitable for the manufacture of container 10. Those having ordinary skill in the art will readily know and understand container manufacturing method alternatives.
Once the intermediate container 136 has been formed, the intermediate container 136 may be removed from the mold cavity 124. As can be appreciated, the intermediate container 136 defines the container 10 (
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.