This disclosure generally relates to plastic containers for retaining a commodity, such as a solid or liquid commodity. More specifically, this disclosure relates to a one-piece blown container having a multi-surface pour spout.
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.
In addition, an alternative method may be used to form the finish portion of the container. This alternative method is known as a blown finish. During this alternative process, the finish portion of the container is created in the blow mold utilizing a process similar to the blow molding process described above. This alternative process enables production of a lighter-weight finish portion, and thus container, than is possible through the traditional injection molding production method. Additionally, when produced utilizing a heat setting process, a blown finish may provide superior heat resistance characteristics as compared to traditional injection molded finishes.
In some applications it may be desirable to provide a spout at the opening of the container. In one example, a spout may be formed as a secondary component and subsequently connected to a container after the container has been blown. In some instances, the spout, once connected to the container, may define a generally circular opening oriented at an angle relative to a longitudinal axis of the container to facilitate pouring. While a container having such a spout improves functionality of the container such as during pouring, the two piece design requires significant material and manufacturing costs. Thus, there is a need for a one-piece container design that has a pourable spout feature incorporated into the finish of the container.
Accordingly, the present disclosure provides a one-piece plastic container having a body defining a longitudinal axis. The body includes an upper portion, a sidewall portion and a base portion. The upper portion includes a spout defining an opening into the container. The sidewall portion may be integrally formed with and extend from the upper portion to the base portion. The base portion closes off an end of the container. The opening defines a first plurality of discontinuous radial pour surfaces.
According to additional features, the container opening includes a second plurality of discontinuous radial pour surfaces, wherein each of the second plurality of discontinuous radial pour surfaces are alternately arranged with each of the first plurality of discontinuous radial pour surfaces. The first and second plurality of discontinuous radial pour surfaces may be co-planar and substantially transverse to the longitudinal axis. According to one example, each of the first plurality of discontinuous radial pour surfaces defines a smaller radius than each of the second plurality of discontinuous radial pour surfaces.
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. It will also be appreciated by those skilled in the art to which the present disclosure relates that the container of the present disclosure may be manufactured utilizing alternative blow molding processes to those disclosed above.
The following description is merely exemplary in nature, and is in no way intended to limit the disclosure or its application or uses.
As shown in
The exemplary container 10 may also have a neck 36 (
The plastic 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 one-piece plastic container 10 generally involves the manufacture of a preform 40 (
Returning now to
The finish 20 of the plastic container 10 may include a threaded region 46 having threads 48, and a lower sealing ridge 50. The threaded region 46 provides a means for attachment of a similarly threaded closure or cap (not illustrated). Alternatives may include other suitable devices that engage the finish 20 of the plastic container 10, such as a press-fit or snap-fit cap for example. Accordingly, the closure or cap (not illustrated) engages the finish 20 to preferably provide a hermetical seal of the plastic container 10. The closure or cap (not illustrated) is preferably of a plastic or metal material conventional to the closure industry and suitable for subsequent thermal processing, including high temperature pasteurization and retort.
A land 52 is formed radially at a transition between the finish 20 and the spout 18. In this way, the spout 18 is radially stepped inward relative to the finish 20. The spout 18 defines a continuous radial sidewall 56 extending from the land 52 toward the opening 42.
With specific reference to
In one example, each of the first plurality of discontinuous radial pour surfaces 60 may be geometrically distinct from each of the second plurality of discontinuous radial pour surfaces 62. According to the example shown, each of the first plurality of discontinuous radial pour surfaces 60 defines a first radius R1, while each of the second plurality of discontinuous radial pour surfaces 62 defines a second radius R2. As illustrated, the first radius R1 is less than the second radius R2. In one example, the first radius R1 may define 2-12 mm (0.08-0.47 inch), while the second radius R2 may define 15-30 mm (0.59-1.18 inch). While each of the first radii R1 shown is equivalent, it is contemplated that some or all of the first radii R1 may be distinct from each other. Likewise, while each of the second radii R2 shown is equivalent, it is contemplated that some or all of the second radii R2 may be distinct from each other.
Each of the first plurality of discontinuous radial pour surfaces 60 cooperates with the radial sidewall 56 to define a first plurality of annular pouring grooves 66. Each of the second plurality of discontinuous radial pour surfaces 62 cooperates with the radial sidewall 56 to define a second plurality of annular pouring grooves 68.
As will become appreciated, the opening 42 of the spout 18 provides a user with multiple pouring options. In one example, a user may tilt the container 10, such as along the longitudinal axis 44, thereby defining a tilt angle in a direction toward one of the first plurality of discontinuous radial pour surfaces 60 (or first plurality of annular pouring grooves 66). In another example, when tilting the container 10 in a direction toward one of the first plurality of annular pouring grooves 66, a portion or all of the commodity may be directed toward one of the first plurality of annular pouring grooves 66 by an adjacent one of the second plurality of annular pouring grooves 68. In this way, the selected first plurality of annular pouring grooves 66 of the spout 18 may direct the commodity in a controlled, metered manner when poured from the container 10.
Explained further, a commodity may be directed out of the opening 42 in a relatively compact stream by utilizing one of the first plurality of annular pouring grooves 66. If a user desires to pour contents out of the container 10 more rapidly and/or in a wider stream, the container 10 may be tilted in a direction toward one of the second plurality of annular pouring grooves 68.
In another advantage, each of the respective first and second plurality of discontinuous radial pour surfaces 60, 62 (or respective first and second plurality of annular pouring grooves 66, 68) are arranged at about 120 degrees from each other around the opening 42. As a result, a user may grasp the container 10 and arbitrarily choose a direction to tilt the container 10 during pouring. If the resultant stream, or control of pour is unsatisfactory, a user may simply rotate the container about 60 degrees (about its axis 44) to align with another one of the first and second plurality of discontinuous radial pour surfaces 60, 62 (or respective first and second plurality of annular pouring grooves 66, 68). It is appreciated that altering the tilt angle during pouring will also influence the effect of the respective first and second plurality of annular pouring grooves 66, 68, and the flow rate as a whole.
With continued reference now to
Turning now to
In one example, a machine (not illustrated) places the preform 40 heated to a temperature between approximately 190° F. to 250° F. (approximately 88° C. to 121° C. ) into the mold cavity 80. The mold cavity 80 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 40 within the mold cavity 80 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 44 of the container 10. While the stretch rod extends the perform 40, air having a pressure between 300 PSI to 600 PSI (2.07 MPa to 4.14 MPa) assists in extending the preform 40 in the axial direction and in expanding the preform 40 in a circumferential or hoop direction thereby substantially conforming the polyester material to the shape of the mold cavity 80 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 80 for a period of approximately two (2) to five (5) seconds before removal of the intermediate container from the mold cavity 80. This process is known as heat setting and results in a heat-resistant container suitable for filling with a product at high temperatures.
In another example, a machine (not illustrated) places the preform 40 heated to a temperature between approximately 185° F. to 239° F. (approximately 85° C. to 115° C.) into the mold cavity 80. The mold cavity 80 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 40 within the mold cavity 80 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 44 of the container 10. While the stretch rod extends the preform 40, air having a pressure between 300 PSI to 600 PSI (2.07 MPa to 4.14 MPa) assists in extending the preform 40 in the axial direction and in expanding the preform 40 in a circumferential or hoop direction thereby substantially conforming the polyester material to the shape of the mold cavity 80 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 80 for a period of approximately two (2) to five (5) seconds before removal of the intermediate container from the mold cavity 80. 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 plastic container 10. Those having ordinary skill in the art will readily know and understand plastic container manufacturing method alternatives.
One advantage of the present disclosure is that the mold cavity 80 may be easily manipulated to alter the geometry of any of the first and second plurality of annular pouring grooves 66, 68 and/or the size of the generally triangular opening 42 as a whole. This size adjustment capability will allow for a simple design change when a determination of the pour rate is either known or needs to be determined. Those skilled in the art will appreciate that the pour rate can easily be determined for a given solid or liquid commodity based on the molecular properties of the solid or liquid commodity, size of the opening, angle of descent and other properties. In this way, the size of the generally triangular opening 42 may be specifically determined for a given commodity and be easily incorporated into the mold cavity 80 design.
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.