This invention relates to chilling and freezing of products such as articles of food, in an apparatus through which the products pass while they are exposed to an atmosphere that chills or freezes the products.
In the field of chilling and freezing products such as articles of food, one well-known technique is to pass the products through a tunnel-like apparatus within which the products are exposed to a very cold atmosphere which causes the products to be chilled, or partially or completely frozen, depending on the temperature of the products entering the apparatus, the temperature within the apparatus, the length of time that the product is inside the apparatus, and the quality of the contact between the products and the cold atmosphere.
Creating the cold atmosphere within the apparatus involves using cryogenic materials, such as liquid nitrogen or liquid or solid carbon dioxide, and which in turn involves the costs associated with the cryogenic materials and the costs such as energy associated with bringing them to the desired low temperature. Thus, there is an ongoing desire to improve the efficiency of apparatus and methods for chilling and freezing, in terms of the extent of chilling and freezing attained per unit of cryogen and/or per unit of energy expended in the operation. The present invention provides a significant improvement in such efficiency.
One aspect of the present invention is apparatus useful for chilling or freezing a product, comprising:
(A) an elongated enclosure having an entrance and an exit;
(B) a movable belt that can carry product to be chilled or frozen on the top surface of the belt within the enclosure between the entrance and the exit, wherein the top surface of the belt lies on a path that crosses first and second points and that includes a segment within the enclosure that is between the first and second points and that is lower than an imaginary horizontal line passing through the lower of the first and second points, and wherein the belt does not pass through any container of cryogenic liquid;
(C) wherein the enclosure includes first and second structures located within the enclosure between the first and second points, each structure extending from above the imaginary line to below said line and above the top surface of the belt, the first and second structures impeding entry of air from the ambient atmosphere into the enclosure and, together with the top, bottom and sides of the enclosure, defining a chilling zone; and
(D) at least one outlet within the enclosure that is capable of dispensing cryogenic refrigerant into the chilling zone.
Preferably, the apparatus includes at least one circulator within the chilling zone.
Another aspect of the present invention is a method of chilling or freezing a product, comprising:
conveying the product through an enclosure on a movable belt that follows a path between first and second points that includes a segment that is below an horizontal imaginary line passing through the lower of the first and second points, wherein the segment is located within a chilling or freezing zone within the enclosure that is defined by the top, bottom and sides of the enclosure and first and second structures located within the enclosure between the first and second points, each structure extending from above the imaginary line to below said line and above the top surface of the belt, the first and second structures defining between them the chilling or freezing zone and impeding entry of air from the ambient atmosphere into said zone, wherein the belt does not pass through liquid cryogen within said enclosure; and injecting cryogen refrigerant within said zone. A pool of cryogen vapor is established in the chilling or freezing zone, and the product is conveyed through the pool of cryogen vapor.
The invention can be carried out using apparatus having the general physical configuration shown in
Apparatus 1 also preferably includes vents 13 and 14 for exhausting cryogen from the interior of apparatus 1. Apparatus 1 includes a section 20 which extends from entrance 11 in a generally downward sloping path, as well as a section 24 which extends in a generally upward sloping path to exit 12 and section 22 between sections 20 and 24. Section 22 is preferably relatively horizontal. However, in an alternative embodiment, section 22 may instead have a portion which extends downward from the closest end of section 20 and a portion which extends upward toward the closest end of section 24. Alternatively, section 22 can be omitted. Apparatus 1 further includes motors 21A, 21B, 21C and 21D which are connected to, and which drive, shafts of circulators which are shown in
Referring to
The opposed ends of belt 30 can be aligned with entrance 11 and exit 12, or one or both of the ends of belt 30 can protrude out of the housing 10 at entrance 11, exit 12, or both, as desired by the operator to facilitate loading and unloading product onto and off of the belt. Belt 30 is made of any material that can withstand the temperatures to which it is exposed within housing 10, and that can withstand having the heat transfer medium (e.g. a very cold material such as liquid nitrogen for cooling applications) applied directly onto the belt material. At least in those embodiments in which heat transfer medium is impinged toward the belt from above and below the belt surface, the belt 30 should preferably be constructed so that liquid and vapor can pass through it. One well-known example of such belt material comprises interlinked loops of metal mesh. Other examples are conventional and well-known in this field.
Belt 30 follows a path in which it crosses first point 31A and second point 31B. Points 31A and 31B are preferably located near entrance 11 and exit 12, respectively, and may be inside or outside the enclosure formed by housing 10. One or both of points 31A and 31B may conveniently be axles over which belt 30 passes and then reverses direction to form reverse pass 32, in the embodiments in which belt 30 is an endless conveyor. In
Belt 30 follows a path between first point 31A and second point 31B which includes at least one segment of belt 30 that is within the enclosure of housing 10, and that is lower than an imaginary horizontal line 35 (seen in e.g.
The advantages of this characteristic are described further, below. In
The structures can alternatively include part of the housing 10 itself. An example of this alternative is shown in
Optionally, and preferably, the apparatus of the present invention also includes third, fourth, fifth and sixth structures that are located within the housing 10, between the aforementioned first and second points (i.e. points 31A and 31B of
Apparatus 1 also includes at least one outlet 60 to introduce cryogen into the enclosure. Preferred cryogens include liquid nitrogen, liquid carbon dioxide, and solid carbon dioxide (preferably introduced as carbon dioxide “snow”). Outlet 60 is connected by suitable piping and controls to a source outside apparatus 1 which contains the cryogen and which enables controllable flow of the cryogen from the source into the enclosure.
Apparatus 1 also preferably includes one or more circulators or fans within the enclosure. These are shown in
Exhaust ports 13 and 14 may include an exhaust fan, and may include a duct which contains an adjustable damper by which the amount of cryogen vapor that leaves the housing 10 can be adjusted, and appropriate controls to enable adjustment of the amount of cryogen vapor that is picked-up from the exhaust area by adjustment of the speed of the exhaust fan, the position of the damper, or both, so as to achieve the desired amount of cryogen exhaust, and the amount of ambient air that is also drawn through each exhaust port.
In the preferred mode of operating, belt 30 moves in a direction such that product that is placed on belt 30 at entrance 11 enters housing 10 and leaves housing 10 at exit 12. Cryogen is injected through outlet 60 (or through each outlet 60 if more than one outlet 60 is provided) toward the upper surface of belt 30 and toward the product thereon. With the circulators and exhaust vents operating, cryogen vapor that is formed by vaporization of the injected cryogen fills the chilling zone which is in the space bounded by the bottom and sides of housing 10, by the first and second structures described above, and by either the top of housing 10 or the imaginary line 35, whichever is lower.
The present invention minimizes air infiltration by angling the belt 30 in the regions near entrance 11 and exit 12 as shown in the Figures, as opposed to a path of travel that is essentially horizontal. The present invention effectively closes off the path of air from outside the apparatus into the housing 10 by forming a cryogenic vapor pool that extends above the upper edge of the openings at entrance 11 and exit 12. In
For practical reasons, β angles of 5° to 20°, preferably near 10°, are useful relative to height clearances at opening 8 as well as for enabling product to travel well on a typical conveyor belt. Excessively steep angles or large β values would risk having the product slide on the belt surface, thus requiring additional equipment or features on the belt's upper surface to hold the product along the belt. Depending on the placement of the outermost structures 44 and 46 between the belt and outside the freezer cooling zone, the height of opening 8 can be determined based on angle β. In
H=L tan β
When the equation above is not satisfied and H is larger than (L*tan β), air can enter into the enclosure which reduces the efficiency of the apparatus because some of the cooling value of the cryogen that is fed into the apparatus is consumed in cooling the air that has entered. Preferably, the value of H should not exceed 1.5 times (L*tan β), to realize the benefits of the invention.
Another advantageous feature is that at the bottom of vent 13, one side 121 is longer than the opposing side 123. The difference in length has been found to change the pickup velocity along the conveyor belt surface. With this design the practical function is that for the same energy input, vapor at the conveyor belt surface enters the exhaust system rather than slipping by the exhaust pickup. The longer edge can be located on either side of the vent, but preferably the shorter side 123 at the base of the vent 13 is on the side closer to apparatus 10 to preferentially collect air along with the cryogen vapor being collected.
In representative operation, apparatus embodying this invention is generally at least about 6 feet in length. There is no absolute maximum length for successful operation; rather, the length is typically set by the desired dwell time of product passing through the enclosure and by the available space in which the apparatus would be operated. Typically, suitable apparatus is 20 to 50 feet long. The number of circulators to employ depends mainly on the length of the apparatus. The circulation fans should be spaced about 3 to 5 feet apart. Preferably, baffles can be provided between adjacent circulators to improve the circulation of cryogen vapor and/or minimize air infiltration into the enclosure.
The apparatus and methods described herein greatly lessen the amount of ambient air that enters into the chilling zone.
This application claims the benefit of priority to U.S. non-provisional application Ser. No. 16/659,637 filed on Oct. 22, 2019, which claims priority from non-provisional application Ser. No. 16/000,014 filed on Jun. 5, 2018, which claims priority from non-provisional application Ser. No. 14/595,867 filed on Jan. 13, 2015, which claims priority from provisional application Ser. No. 61/928,195 filed on Jan. 16, 2014, the disclosure of which is incorporated by reference herein in its entirety.
Number | Date | Country | |
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61928195 | Jan 2014 | US |
Number | Date | Country | |
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Parent | 16659637 | Oct 2019 | US |
Child | 17551630 | US | |
Parent | 16000014 | Jun 2018 | US |
Child | 16659637 | US | |
Parent | 14595867 | Jan 2015 | US |
Child | 16000014 | US |