The disclosure generally relates to a continuous coating of pieces or cores of confectionary product, and more particularly to a continuous coating of pieces or cores of confectionary product via a drum coating arrangement.
There are numerous known processes for coating gum and confectionary products. These processes include batch-type and continuous coating.
For batch-type processes, large rotating containers are utilized to coat confectionary cores or pieces (particularly gum cores or pieces). Initially, the confectionary material may be produced by a standard extrusion or batch processes and formed into rope or large thin sheets of material several inches or a foot or more in width. Separation lines are pressed or formed into the sheets, thereby forming the shapes of the smaller pieces (i.e. “cores”). The material may then be stored in a cooler or under a cooled atmosphere in order to condition them for further processing.
Pursuant to more recent batch-type processes, the confectionary material is dumped into rotating mixers and separated into cores by a tumbling process. Thereafter, a coating solution, such as a sugar syrup, is added to the mixer during mixer rotation. Hot air at a temperature of approximately 120° F. is further applied to dry the coated cores.
In order to form a uniform and consistent coated gum product with a coat of the desired thickness, this process is repeated numerous times until completion of the requisite coating. In order to achieve an acceptable coating, the process is repeated up to 40-50 times with small, thin layers being added each time. This process can take up to 6-7 hours to complete, and involve a good deal of labor.
In an effort to provide an improved upon and more efficient coating process over the batch-type processes discussed above, continuous coating processes have been developed. In such processes, small cores or pieces of confectionary material (particularly gum) are introduced into one or more rotating cylindrical drums. Therein, the pieces are lightly coated with a sugar solution. A continuous flow of heated air is circulated through the drums and dries the coating solution on the gum cores at the same time that the material is being coated. Conduits or conveyors are utilized to interconnect the drums and transport the material being coated from one drum to the other.
The above processes being described, it should be noted that some types of confectionary may desirably call for a coating that is applied in multiple layers, with each layer including compositional differences. As such compositionally different layers may interact differently with the core confectionary pieces to which they are applied (i.e. be absorbed by the cores or bind to the cores at different rates), it may be inefficient to apply coating layers in a single drum or multiple drums that are identically configured and operated. For instance, certain confectionery cores, such as chewy candy cores, and particularly powder-filled chewy candy cores, are delicate in nature. Application of a hard outer coating to such delicate cores can be problematic as the cores may be crushed or collapse under the product weight tumbling in typical batch-type hard coating pans. Accordingly, it may be desirable to coat such cores with a soft pre-coating prior to a subsequent hard outer coating. This can provide a final coated chewy candy product that is more stable than if it were simply hard pan coated alone. Application of such a soft pre-coating may involve applying a liquid material in one drum and a powder material in a second drum, which binds to the liquid material to form the soft coating layer on the chewy candy cores. In such a process, it may be desirable to have a longer residence time in the second drum so that the powder material has sufficient time to bind to the liquid material. Accordingly, a system and method that allows for variation in drum interaction with core confectionary pieces would be desirable.
Disclosed is a system for continuously coating individual pieces of confectionary product, the system including a product feed device, at least one drum coating arrangement configured to continuously receive the individual pieces of confectionary product from the product feed device, the drum coating arrangement including a first rotating drum rotatable about a first drum axis and a second rotating drum rotatable about a second drum axis, a first drum volume defined by the first rotating drum, and a second drum volume defined by the second rotating drum, the first drum volume being communicable with the second drum volume, wherein the drum coating arrangement is configured such that the confectionary product has a longer residence time in the second drum volume than the first drum volume.
Also disclosed is a method for continuously coating individual pieces of confectionary product, the method including continuously feeding the individual pieces of confectionary product from a product feed device into at least one drum coating arrangement, the drum coating arrangement including a first rotating drum and a second rotating drum, transporting the individual pieces of confectionary product through a first drum volume defined by the first rotating drum, the transporting through the first drum volume occurring in a first residence time, applying a first material to the individual pieces of confectionary product during the first residence time, transferring the individual pieces of confectionary product from the first drum volume to a second drum volume defined by the second rotating drum, transporting the individual pieces of confectionary product through the second drum volume, the transporting through the second drum volume occurring in a second residence time, the second residence time being longer than the first residence time, and applying a second material to the individual pieces of confectionary product during the second residence time.
The accompanying drawings incorporated in and forming a part of the specification embodies several aspects of the present invention and, together with the description, serve to explain the principles of the invention. In the drawings:
Referring to
The confectionary pieces 12 enter the system 10 at the product feed device 14. In an exemplary embodiment shown generally in
In the exemplary embodiment of
Once deposited to a desirable depth across a desired length of the second tray 28, a conveyor 34 disposed on the second tray 28 transports the product to the feeder 24. Therein, weight of the product is monitored via an electronic scale 36 disposed under the feeder 24, with the amount of product initially entering the feed device 14 being ultimately conveyed in a continuous flow from the feeder 24 to a chute 29 connecting the feeder to the drum coating arrangement 16a.
It should be noted that actuation of the first tray 26, the conveyors 32,34, the scale 36, the depositing device 30, and the desirable depth to which the first tray 26 deposits product in the second tray 28 are controllable via a computer micro-processor or micro-processors in communication with the various components of the feed device 14 individually or as a whole. These computer(s) may control or communicate with a remainder of the components of the system 10. Product height in the second tray may also be communicated to the computer(s) from devices such as the electronic eye mentioned above. In an exemplary embodiment, the product is deposited across a substantially entirety of the second tray length at a height/depth of approximately 6 to 10 inches. The product is then conveyed from the second tray to the feeder 24, where it is maintained at a desirable height/depth of 1 to 10 inches, as it is further conveyed from the feeder 26 to the chute 29.
Having been desirably accumulated in the feed device 14, the product may now be continuously fed down the chute 29 and into the drum coating arrangement 16a. As shown in
In addition, and as is best shown in
During transport of the pieces 12 from an inlet opening 46 in the first drum 18 (and thus an inlet into the drum arrangement 16a in general) to an outlet opening 48 of the second drum 20 (and thus an outlet from the drum arrangement 16a in general), the pieces 12 will have a longer residence time in the second drum volume 42 than the first drum volume 40 (with each pieces 12 desirably having substantially the same residence time in each drum 18 and 20 to facilitate consistent coating). In an exemplary embodiment, the longer residence time in the second drum volume 42 is achievable because the drums 18, 20 are configured such that the second drum volume 42 is greater than the first drum volume 40 via a greater diameter and/or length of the second drum 20 relative to the first drum 18.
Residence time within each drum is important in the system 10 as described below because of the different materials applied to the pieces 12 of product in the first drum 18 and the second drum 20. Referring first to the first drum 18, a liquid material 49 is desirably chosen for feed into the first drum volume 40. This material may be any conventional sugar-based or sugar-free syrup material that will act as a coating or binding solution, and is fed into the first drum volume 40 via at least one nozzle 50 that is best shown in
As the first drum 18 rotates about a central first drum axis 52, the liquid material 49 coats the pieces 12 about a surface thereof. The pieces 12 are transported from the inlet opening 46 to an outlet opening 54 via an incline of the first drum 18, wherein the inlet opening 46 is higher than the outlet opening 54. During this rotational transportation through the first drum volume 40, the liquid material 49 coats the pieces 12. However, due to potentially adherent qualities of the liquid material 49, some of the pieces 12 may become lodged to an inner surface 56 of the first drum 18. In order to dislodge the adhered pieces 12, a release assist bar 58 is positioned so as to extend into the first drum volume 18 via the outlet opening 54 (as shown in
Also disposed at an outlet opening end of the first drum 18 in the exemplary embodiment of
As the pieces 12 flow past the weir plate 62, the pieces 12 fall from the outlet opening 54 of the first drum 18, and into the second drum volume 42. The pieces 12 that enter the second drum volume 42 do so with the liquid material 49 having already been applied thereto. As is mentioned briefly above, insertion of the end 41 of the first drum 18 into the inlet opening 44 of the second drum 20 forms an annulus 45 between the drums. Importantly, this annulus 45 provides both an entry point for material into the second drum (see below), and a sampling point for analyzing liquid coated pieces 12 flowing from the first drum 18 to the second drum 20.
Referring now to the second drum 20, any conventional dry powder material 66 is desirably chosen for feed into the second drum volume 42 and application to the pieces 12. This material may be any conventional sugar-based or sugar-free dry/finely granulated material (such as bakers special sugar) that will adhere to the liquid material 49 that has already been applied to the pieces 12, and is fed into the second drum volume 42 via a powder tube 68 that is best shown in
Similarly to the first drum 18, as the second drum 20 rotates about a central first drum axis 70, the pieces 12 of confectionary are coated with the powder material 66, whereby the powder material 66 binds to the liquid material 49 (from the first drum 18) that already coats the surface of the pieces 12. The pieces 12 are transported from an annulus position where the pieces 12 fall from the first drum 18 into the second drum volume 42 to an outlet opening 48 of the second drum 20 (the outlet opening being best shown in
After exiting the second drum volume 42, if the system 10 includes multiple drum arrangements (as is the case with the exemplary system 10 shown in
After exiting the final drum arrangement in the system (in the exemplary embodiment of
Following the above discussed conditioning process, a hard outer coating is applied to the cured/sintered soft coating of the pieces 12. Application of this hard outer coating may occur in a typical batch coating mixer.
By way of exemplary embodiment, the following exemplary compositions of the liquid material 49 and powder material 66, and exemplary composition/sizing of pieces 12 should be noted:
By way of exemplary embodiment, the following exemplary conditions of the system 10 should also be noted:
In addition, and similarly to the feed device 14, it should be noted that drum rotational speed, drum inclination, scalper actuation, actuation and speed of the elevator conveyor 76, and the desirable depth to which the pieces 12 accumulate within the drums are controllable via a computer micro-processor or micro-processors in communication with the various components of the drum arrangements 16a, 16b individually or as a whole. In fact, one or more computer(s) may or may not control/communicate with an entirety of the system 10.
Furthermore, the drums 18 and 20 are controllable within the system 10 such that the first drum 18 and second drum 20 may rotate at different speeds and be disposed at different inclinations. As both drum rotational speed and drum inclination can effect residence time within the drums, differences in either the rotational speeds of the drums or the inclination of the drums may contribute to or be solely responsible for the longer residence time of the pieces 12 in the second drum volume 42 than the first drum volume 40.
All references, including publications, patent applications, and patents cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
The use of the terms “a” and “an” and “the” and similar referents in the context of describing the invention (especially in the context of the following claims) is to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. The terms “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms (i.e., meaning “including, but not limited to,”) unless otherwise noted. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Exemplary embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. Variations of those embodiments may become apparent to those of ordinary skill in the art upon reading the foregoing description. The inventors expect skilled artisans to employ such variations as appropriate, and the inventors intend for the invention to be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications and equivalents of the subject matter recited in the claims appended hereto as permitted by applicable law. Moreover, any combination of the above-described elements in all possible variations thereof is encompassed by the invention unless otherwise indicated herein or otherwise clearly contradicted by context.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2012/039973 | 5/30/2012 | WO | 00 | 2/24/2014 |
Number | Date | Country | |
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61495451 | Jun 2011 | US | |
61491759 | May 2011 | US |