The invention relates to a device and method for making sheeted products. More particularly, the invention relates to a device and process for preparing sheeted food products and, in particular, a product from caramel and popcorn.
Snack bars, treats and confectionary products have become increasingly popular in recent years. As society becomes more mobile, the need for healthy food-on-the-go alternatives has become increasingly important. To that end, a group of food snacks have been developed which are a combination of grains and/or flavoring ingredients, as well as binder materials which add consistency to the food snack. Example grains include granola, oats, barley, bulgur, flaxseed, quinoa, rye, rice and popped corn (popcorn), while example flavoring ingredients include dried fruits, nuts and chocolate products. Binder materials vary and can include syrups consisting of caramel, marshmallow, karo syrup, corn syrup and/or sugars.
The food snacks can be manufactured via multiple methods such as extrusion, slab forming and sheeting, among others. Manufacturing requirements include ensuring that the food constituents be kept in a malleable form capable of shape formation into a packable, storable, consumable solid. This is often achieved through mixing constituents of different physical form to provide an even mixture of adequate organoleptic properties to meet consumer tastes. Further manufacturing requirements include ensuring that the food product is shaped into a viable form that meets the taste, texture and/or mouthfeel tastes of the consumer.
In addition to the above organoleptic properties, there has been a long felt need for snack bars and like confectionaries which are well-formed and having a minimal thickness. While the prior art discloses that such thin-sized bars can be achieved when utilizing a homogenous mixture (see, for example, U.S. Pat. No. 5,505,978), there has been difficulty in forming stable, thin-form usable food stuff from a heterogeneous mixture, e.g., a granular solid with a semisolid or solid flavoring agent and liquid binding agent. For example, U.S. Pat. No. 6,200,611 discloses a method and apparatus for preparing a bar containing a heterogeneous mixture of popcorn and molten binder, yet the disclosed bar has a minimum thickness of ¾ inch. Similarly, U.S. Pat. No. 7,037,551 discloses methods of preparing bite-size granola bars via extrusion methods, yet discloses that the bars typically have a thickness of ½ inch.
It is believed that when trying to manufacture thin-sized bars containing heterogeneous mixtures problems have been experienced due to the naturally adhesive properties of binding agents. Specifically, such binding agents will adhere to the manufacturing apparatus, creating obstructions and impeding the flow of the product. Even if obstructions do not occur, the dry ingredients in heterogeneous mixture are not adequately covered by the binding agent, resulting in a product with inferior organoleptic properties.
Thus, a need exists for a sheeted bar or confectionary having a minimal thickness and containing heterogeneous constituents, yet still maintaining desirable organoleptic properties.
Disclosed herein is a method of preparing a sheeted mixture comprising a binding agent and a dry ingredient, the method comprising the steps of heating said binding agent; mixing said dry ingredient with said binding agent to form a mixture; transferring said mixture to an extruder, wherein said extruder comprises feed rollers coated with a non-stick coating; extruding a sheet comprising said mixture; and cooling said sheet comprising said mixture, wherein said sheet comprising said mixture has a thickness of less than ½ inch.
Separately disclosed herein is an apparatus for extruding material comprising: a hopper; a housing containing feed rollers, said housing being in fluid communication with said hopper, wherein the exterior of said feed rollers and are coated with a non-stick coating; a conveyor in fluid communication with said housing; means to actuate said feed rollers and said conveyor; and means to control the rate of movement of said feed rollers, and said conveyor.
With reference to
The hopper 10 may be any shape that promotes gravity feeding and, as such, may be rectangular, cylindrical, conical, a frustum, etc. In one preferred embodiment, best shown in
Hopper 10 is in fluid communication with, and is situated directly above, housing 12. Housing 12 receives the food ingredients and contains machinery to process the food ingredients. As such, housing 12 may be any shape which can accommodate both the machinery and the food ingredients. In one embodiment, as shown in
As shown in
Feed rollers 14a and 14b are preferably cylindrical, however other geometries that can be rotatably mounted may also be utilized. The dimensions of feed rollers 14a and 14b can vary. In one embodiment, as shown in
Feed rollers 14a and 14b may be coated with a non-stick coating 24. Non-stick coating 24 prevents the food ingredients from adhering to feed rollers 14a and 14b and thus prevents obstructions of gap 20. Non-stick coating 24 includes, but is not limited to Teflon®, polytetrafluoroethylene, or other appropriate non-stick coatings.
As shown in
In a preferred embodiment, grooves 22a and 22b are designed such that the ratio of the diameter of the feed rollers to the depth of grooves is 72:1, and the ratio of the diameter of the feed rollers to the width of the groove is 12:1. As such, where feed rollers 14a and 14b have a 9 inch diameter, grooves 22a and 22b will have a depth of ⅛ inch and a width of ¾ inch.
As shown in
Hopper 10, housing 12 and conveyor 26 are all supported by a base 30. Base 30 may be any shape which can accommodate the hopper 10, housing 12 and conveyor 26. In a preferred embodiment, base 30 is cuboid shaped and has dimensions 80 inches by 35 and ½ inches by 39 and ½ inches.
A controller 32, an embodiment of which is disclosed in
Referring to
Once the dry ingredient is adequately covered by the binding agent, the mixture is removed from the heated container and immediately deposited in hopper 10, such that there is no significant cooling of the mixture. In a preferred embodiment, the transfer of the mixture from the heated container to hopper 10 is completed in less than 60 seconds. Hopper 10 guides the mixture via gravity to housing 12, where the mixture is contacted with feed rollers 14a and 14b. Additionally the mixture may also be guided by press 11. Grooves 22a and 22b of feed rollers 14a and 14b aid in the communication of the mixture through gap 20, forming a sheeted product.
Where the mixture has adhesive characteristics, the combination of grooves 22a, 22b and non-stick coating 24 prevent accumulation of the mixture on the feed rollers 14a and 14b, thus allowing the mixture to proceed through gap 20 unobstructed. Because of this, gap 20 may be smaller than gaps found in conventional extruders, allowing the claimed extruder 1 to produce a sheeted product that has a thickness of less than ½ inch, and preferably between ¼ inch and ⅜ inch.
Having passed through feed rollers 14a, 14b and gap 20, the mixture is deposited onto conveyor 26 as a sheeted product. Conveyor 26 transports the sheeted product away from hopper 10 and housing 12. The sheeted product cools and further solidifies as it progresses along the conveyor 26.
A mixture is prepared from the ingredients set forth in Table 1:
Alternatively, a mixture is prepared from the ingredients set forth in Table 2:
Alternatively, a mixture is prepared from the ingredients set forth in Table 3:
Alternatively, a mixture may be prepared from the general ranges for the ingredients set forth in Table 4:
The dried fruits referenced in Tables 1 to 3 include, but are not limited to, dried cherries and dried cranberries. The nuts referenced in Tables 1 to 3 include, but are not limited to pumpkin seeds, peanuts and almonds. Additionally, the popped popcorn referenced in Tables 1 to 3 can vary in size, type or shape, and can include popcorn that is first coated in cheese.
The butter, corn syrup, white sugar, brown sugar and salt are first blended together in an open flame copper kettle while the temperature of the mixture is monitored using a non-contact infrared thermometer. Once the mixture reaches between 292° F. and 295° F., the popcorn and any dried fruits or nuts are added to the mixture. The mixture is then blended for another two to three minutes, during which time the mixture is visually inspected to confirm that the popcorn, dried fruits and nuts are adequately covered by the remaining ingredients of the mixture.
Once the blending is complete, the mixture is immediately transferred to an extruder and poured into the extruder's hopper. Preferably, the transfer of the mixture from the kettle to the hopper is completed in under 60 seconds. The hopper gravity feeds the popcorn-containing mixture through the feed rollers of the extruder. Additionally, a press may be utilized to force the mixture through the hopper. Due to the combination of the grooves of the feed rollers, the feed rollers' non-stick coating and the size of the gap between the feed rollers, a thin sheet of mixture, less than ½ inch thick, is extruded onto the conveyor.
The thin sheet of mixture cools and solidifies as it progresses through the conveyor. The thins sheet of mixture is subsequently broken into pieces and packaged at the end of the conveyor.
Although the present invention has been described by reference to its preferred embodiment as is disclosed in the specification and drawings above, many more embodiments of the present invention are possible without departing from the invention. Thus, the scope of the invention should be limited only by the appended claims.
Filing Document | Filing Date | Country | Kind |
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PCT/US2017/032359 | 5/12/2017 | WO | 00 |
Number | Date | Country | |
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62335960 | May 2016 | US |