NZ617431B2 - Apparatus and method for fluidized bed treatment of materials - Google Patents

Abstract

Apparatus and method for treatment of a particulate material including regions of greater and lesser fluidization is disclosed. The apparatus employs a conveyor belt (16') for supporting the particulate material for transport and a source of gas for delivery through the conveyor belt to fluidize the particulate material. A gas distribution system (30) is used for controlling the gas flow to create the regions of greater and lesser fluidization. This approach avoids the use of mechanical agitation of the conveyor belt which improves efficiency and reliability. The apparatus and method find particular application in the handling of particulate foodstuffs in bulk when treatment such as freezing, heating, or blanching of individual food particles is required. particulate material. A gas distribution system (30) is used for controlling the gas flow to create the regions of greater and lesser fluidization. This approach avoids the use of mechanical agitation of the conveyor belt which improves efficiency and reliability. The apparatus and method find particular application in the handling of particulate foodstuffs in bulk when treatment such as freezing, heating, or blanching of individual food particles is required.

Description

APPARATUS AND METHOD FOR FLUIDIZED BED TREATMENT OF MATERIALS FIELD OF THE INVENTION This invention relates to apparatus and methods for treatment of particulate material by creating a fluidized bed of material in which the treated material is maintained as individual, separate particulates. The present invention finds particular application in the food processing industry for freezing of particulate food materials in which the food material is frozen into separate, individual pieces rather than into an agglomerated mass.

BACKGROUND OF THE INVENTION Fluidization is required in thermal air treatment to separate foodstuffs through a continuous process. The term “thermal air treatment” refers to processes such as freezing by means of cold air or gases, drying or heating via introduction of steam, hot air, water or gas. When upwardly rising air is introduced through a perforated trough or foraminous conveyor belt, fluidization of particulate material on the belt, such as foodstuffs, is initiated. In a fluidized state, particulate foodstuffs receive efficient freezing or heating treatment and maintain their particulate nature.

Complete fluidization of foodstuffs results in the material moving in a fluid manner while being treated. Complete fluidization is not always appropriate when dealing with delicate food products such as raspberries or light food products such as diced onions, and it is therefore, important that the level of fluidization be adjustable to accommodate the material being treated.

The creation of fluidized beds of foodstuffs for freezing or heating is a well known technique in the food processing industry. For example, IQF (individually quick frozen) tunnel freezer designs are common in which particulate foodstuffs to be frozen are transported in a fluidized state on a conveyor through an enclosed structure where cooled air is directed upwardly through the foodstuffs. An important aspect of the fluidization process is to create zones of greater and lesser fluidization which assist in maintaining a cascading flow of the product for optimal access of all particles to the upward gas flow through the product. Fluidization techniques have been developed in the past which rely on perforated fixed trays with mechanical agitation and pulsing mechanisms to vary the fluidization within the product bed. Also, fluidization is often initiated with eccentric rollers below a conveyor belt to lift the product and induce product fluidization.

Examples of prior patents employing different techniques for improved transportation and fluidization of foodstuffs include US Patent No. 6,477,845 to Larsson which relies on a perforated trough with cyclical movement of the trough with and against the direction of product travel to initiate fluidization. US Patent No. 5,447,040 to Rothstein discloses an endless foraminous conveyor belt with an electric motor having a control unit for periodically driving the belt in a direction opposite to the direction of product travel to initiate fluidization. US Patent No. 4,301,659 to Martin et al. teaches a conveyor that includes downward steps to cause a thinning of the product bed on the conveyor and increased fluidization by virtue of the velocity of the air being directed through the bed increasing in the region of the thinned product bed.

Prior fluidization techniques tend to rely on manipulation of the conveyor belt by mechanical equipment within the treatment enclosure where cooling or heating is occurring. As such, the equipment is subject to significant wear and tear during normal operation and the cooled or heated treatment enclosure increases the harshness of the operating environment. Therefore, existing mechanical fluidizations systems have a tendency to breakdown during operation resulting in reduction of the effectiveness of fluidization or complete cessation.

SUMMARY OF THE INVENTION To address the problems of prior fluidization systems, applicant has developed an apparatus and method which avoids the use of mechanical components for establishing zones of lesser and greater fluidization with resulting improved reliability.

The present invention eliminates the need for mechanical components inside the freezer for establishing fluidization zones, and provides a more energy efficient system by reducing the amount of air required for fluidization and eliminating motors to drive the mechanical components. Particularly for delicate food products, mechanical agitation causes product damage, and the present invention serves to handle these products more gently.

Accordingly, a first aspect of the present invention provides apparatus for treatment of a particulate material comprising: means for supporting the particulate material for transport between an entrance and an exit to the apparatus; means for supplying a gas flow through the means for supporting the material; and means for distributing the gas flow to fluidize the particulate material on the means for supporting the particulate material to create a plurality of repeating regions of greater and lesser fluidization within the particulate material between the entrance and exit.

Described herein is an apparatus for treatment of a particulate material in a fluidized bed comprising: means for supporting the particulate material for transport; means for distributing a gas flow through the particulate material to create the fluidized bed on the means for supporting the particulate material and to create regions of greater and lesser fluidization within the bed.

Also described is an apparatus for treatment of a particulate material in a fluidized bed comprising: a conveyor belt for supporting the particulate material for transport; a gas distribution system for controlling a gas flow through the particulate material to create the fluidized bed on the conveyor belt and to create regions of greater and lesser fluidization within the bed.

In a further aspect of the invention, there is provided a method for treatment of a particulate material comprising: supporting the particulate material for transport in a transport direction; supplying a gas flow through the particulate material; and distributing the gas flow to fluidize the particulate material to create a plurality of repeating regions of greater and lesser fluidization in the particulate material as the material is moved in the transport direction.

Described herein is a method for treatment of a particulate material comprising: creating a fluidized bed by supplying a gas flow through the particulate material; and distributing the gas flow to create regions of greater and lesser fluidization within the fluidized bed.

BRIEF DESCRIPTION OF THE DRAWINGS Aspects of the present invention are illustrated, merely by way of example, in the accompanying drawings in which: Figure 1 is a side elevation view of a food processing tunnel incorporating apparatus according to an embodiment of the present invention taken along line 1-1 of Figure 2 or 3; Figure 2 is a top plan view of the food processing tunnel of Figure 1 taken along line 2-2 of Figure 1 or 3; Figure 3 is an end elevation view of the food processing tunnel of Figure 1 taken along line 3-3 of Figure 1 or 2; Figure 4 is a detail view of a conveyor belt and gas distribution system according to an embodiment of the invention; Figures 5A to 5E are cross-sections through the conveyor belt and gas distribution system showing schematically different embodiments of the invention; and Figures 6A to 6F are plan views of various gas distribution systems according to different embodiments of the invention.

DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to Figures 1 to 3, there is shown a food processing unit 2 for treatment of particulate foodstuffs according to an embodiment of the apparatus of the present invention. Food processing unit 2 comprises an insulated enclosure or tunnel 4 with means for supplying a gas flow in the form one or more gas circulation fans 8 driven by external motors 10 to circulate gas through tunnel 2 in a cyclical flow best shown by arrows 12 in Figure 3. The illustrated arrangement is designed for the freezing of material and a heat exchange unit in the form of a refrigeration unit 6 is provided within the enclosure to generate cooled air. Instead of circulating cooled air, other arrangements are possible including, for example, the use of steam for blanching particulate foodstuffs or the use of alternative gases such as nitrogen or carbon dioxide to freeze foodstuffs. These other arrangements would require appropriate sealing of the tunnel 4 and replacement of refrigeration unit 6 with an appropriate heat exchange unit.

The apparatus of the present invention also includes means for supporting the particulate foodstuff for transport during exposure to the treatment gas, preferably, in the form of a movable conveyor belt. In the illustrated embodiment of Figures 1 to 3, the conveyor belt comprises a pair of endless loop conveyor belts 16 and 16'. Conveyor belt 16 is a first conveyor belt on which foodstuff material is introduced into tunnel 4 at entrance 18, and conveyor belt 16' is a second conveyor belt onto which foodstuff is transferred from the first belt at transition point 20 for movement out of the tunnel via exit 22. In other words, in the illustrated embodiment, the foodstuff travels from entrance 18 to exit 22 in the direction indicated by arrow 15 in Figures 1 and 2. Other conveyor belt configurations are possible, and will be apparent to a person skilled in the art. It is necessary that the belts convey untreated foodstuffs through tunnel 4 to emerge in a treated (frozen, blanched) form.

Each conveyor belt is preferably formed from plastic or stainless steel and is driven by a motor 24 which is preferably external to the tunnel 4. Each conveyor belt is also perforated to allow passage of the treatment gas upwardly through the belt and through the particulate material on the belt.

Also provided are means for distributing the gas flow to fluidize the particulate material on the conveyor belts into regions of greater and lesser fluidization. In the embodiment of Figures 1 to 3, the means for distributing the gas flow comprises a gas distribution system to deliver gas upwardly through the conveyor belt and distribute the gas flow into zones of concentrated and dispersed flow to create the regions of greater and lesser fluidization, respectively.

Figure 4 is a detailed view of an exemplary conveyor belt 16' with a gas distribution system in the form of at least one plate 30 below the belt. Conveyor belt 16' comprises a movable stainless steel mesh 32 which permits the passage of a gas therethrough. The edges of the steel mesh are support by interconnected roller links 34 that serve to guide and drive the conveyor by engagement of at least some of the links by a rotatable driving sprocket (not shown). The conveyor belt can also be formed of a material such as perforated plastic. As best shown in Figure 3, roller links 34 at the edges of the conveyor 16' are positioned between upstanding side walls 17 and 19 such that particulate material on the belt that is fluidized by the upward movement of gas through the belt is constrained to remain on the belt.

In the illustrated embodiment of Figure 4, there are a plurality of plates 30 positioned below conveyor belt 16' in a fixed, stationary configuration with the plates defining an array of openings therethrough. The openings are arranged in various patterns to define the zones of concentrated and dispersed gas flow. In the embodiment of Figure 4, each plate 30 is formed with a plurality of smaller openings 36 therethrough to define a zone of dispersed gas flow. In this case, the plurality of smaller openings 36 comprise an array of generally circular openings with each opening creating a small column of gas which is directed through the conveyor belt when a gas is directed upwardly past the plate.

Together, the plurality of openings 36 create a plurality of gas columns spread over the area of the plate that, in turn, generate a region of lesser fluidization in the particulate material on the conveyor as the conveyor passes over the plate. In addition, in the arrangement of Figure 4, each of the plurality of plates 30 is spaced apart from an adjacent plate by a gap 38, and each gap 38 between adjacent plates defines a zone of concentrated gas flow in which a single jet of air extending across the belt is directed through the conveyor belt to create a region of greater fluidization in the particulate material on the conveyor as the material is transported by the conveyor over a gap 38. In the present invention, the regions of lesser and greater fluidization are created without the mechanical agitation of the conveyor belt used with prior systems.

As an additional feature of the embodiment of Figure 4, each of the plurality of plates 30 is preferably formed with a flanged edge 40 adjacent to and running parallel to gap 38 between adjacent plates. Flanged edges 40 are arranged in pairs on opposite sides of a gap and serve to define a passage for controlling the concentrated gas flow. Various arrangements are possible as illustrated in Figures 5A through 5D which show schematic cross-sections through links 34 of the conveyor belt and plates 30 below the belt with different flanged edges 40. Figure 5A shows an arrangement in which the flange edges 40 of adjacent plates cooperate to define a passage 41 which tapers inwardly upwardly to a generally parallel upper portion 42. Figures 5B and 5C show arrangements in which the flanged edges 40 define a constant width passage 44 or 46. In Figure 5B, the flanges depend downwardly from the plates 30, while in Figure 5C the flanges extend upwardly from the plates. The arrangement of Figure 5C permits a wider space between the stationary plates and the moving conveyor belt for cleaning purposes. Figure 5D shows an arrangement identical to that of Figure 4 in which flanged edges 40 of adjacent plates cooperate to define a passage 48 which tapers constantly inwardly upwardly. Passages which narrow create a venturi effect which accelerates the gas flow to create greater fluidization.

Figure 5E shows an alternative arrangement which employs individual gas chambers 49 between plates to generate the zones of concentrated gas flow. Each chamber comprises a plenum extending across the width of the conveyor with a slot or plurality of openings 51 adjacent an upper edge of the plenum to direct gas upwardly through the conveyor belt. For example, each chamber may be an air knife unit. Gas may be supplied to each gas chamber 49 by the same fan units 10 that deliver gas to the zones of dispersed gas flow. In a preferred arrangement, a separate gas supply (not shown) is used to provide gas to the gas chambers to ensure a reliable flow.

Figures 6A to 6D illustrate schematically alternative schemes for gas distribution systems according to the invention which rely on plate arrangements to deliver gas upwardly through the conveyor belt distributed into zones of concentrated and dispersed flow to create the regions of greater and lesser fluidization, respectively.

For example, Figure 6A shows the same arrangement as used in the embodiment of Figure 4 with a plurality of spaced, rectangular plates 30 having a regular array of smaller, generally circular openings 36 extending through the plates to define zones of dispersed gas flow. Gaps 38 between adjacent plates define zones of concentrated gas flow.

Figures 6B and 6C show arrangements similar to that of Figure 6A except the zones of dispersed gas flow are defined by an array of slots 50 rather than an array of circular openings. In the arrangement of Figure 6B, slots 50 run transversely to the direction of travel of the conveyor belt, while in the arrangement of Figure 6C, slots 50 run parallel to the belt travel. Gaps 38 between adjacent plates define zones of concentrated gas flow.

Figure 6D shows an arrangement in which the plurality of plates 55 are generally triangular in shape to define gaps 57 between adjacent plates for concentrated gas flow that extend obliquely to each other. In the illustrated embodiment, plates 55 are formed with a regular array of generally circular openings to create zones of dispersed gas flow, however, it will be appreciated that a regular array of slots can also be used.

Figures 6E and 6F show possible arrangements for a single plate 58 that extends below the entire length of the conveyor belt. In these cases, regular arrays of smaller openings in the form of circles 60 (Figure 6E) or slots 62 (Figure 6F) define zones of dispersed gas flow, while at least one larger opening define a zone of concentrated gas flow. In these cases, the at least one larger opening comprises a plurality of aligned, generally circular larger openings 64, and it will be appreciated that large slots can be substituted for the circular openings.

Of course, the skilled person will appreciate that other combinations and permutations of perforations or slots formed in the plates are possible. It is sufficient that the generally smaller openings through and/or between adjacent plates serve to distribute air evenly below the belt to create zones of dispersed gas flow with resultant regions of lesser fluidization in the material bed, while the larger openings serve to establish concentrated higher velocity gas flow zones across the conveyor to generate regions of greater fluidization of the material bed.

In a preferred arrangement, the apparatus of the present invention includes means to control a volume of gas flow delivered from at least one of the zones of concentrated and dispersed gas flow. As shown in Figure 5C, this preferably takes the form of a damper 70 associated with one or more openings of plates 30. The dampers are movable back and forth as indicated by arrow 72 to adjust the area of the openings available for gas flow. In the illustrated example of Figure 5C, each damper 70 is associated with a gap 38 between plates defining a zone of concentrated gas flow. Dampers 70 may also be associated with the array of smaller openings in a plate 30 to control the volume of gas delivered through the zones of dispersed gas flow by covering and uncovering wholly or partially a plurality of openings through the plate. Dampers 70 may be installed to operate independently of each other or for movement in a co-ordinated manner by virtue of being joined together by a common control system.

In an alternative approach to controlling the volume of gas flow through plates 30, it is also possible to equip gas circulation fans 8 with variable speed drive motors 10, whereby varying the speed of the motors varies the volume of gas flow delivered to the array of plate openings.

The various embodiments of the apparatus of the present invention described above function most efficiently when the conveyor belt transports the particulate material in a flow of substantially constant depth.

In another aspect, the present invention provides a method of treating particulate material involving the steps of supporting the particulate material for transport, supplying a gas flow through the particulate material, and distributing the gas flow to fluidize the particulate material to create regions of greater and lesser fluidization.

It is contemplated that the present invention can be retrofitted into an existing food processing unit for handling particulate material in a fluidized bed which already makes use of a tunnel enclosure and equipment for generating a gas flow. The retrofittable apparatus would include means for supporting the particulate material for transport, such as a conveyor belt, and means for distributing the gas flow through the particulate material to create the fluidized bed on the conveyor belt with regions of greater and lesser fluidization within the bed. The means for distributing the gas flow may include the plate gas distribution system discussed above.

In another aspect, the present invention provides a method for treatment of a particulate material involving creating a fluidized bed by supplying a gas flow through the particulate material, and distributing the gas flow to create regions of greater and lesser fluidization within the fluidized bed.

As with the prior art, the apparatus and methods of the present invention serves to transport particulate material, preferably, pieces of food or goods, in a partially fluidized bed for treatment, such as freezing or heating, as individual particles. The apparatus and method of the present invention differ from conventional food processing fluidization techniques in that the present invention makes use of variable gas flow through the bed of material to agitate the bed in selected regions to promote fluidization and treatment of the material. The above described apparatus and method avoid the use of mechanical agitating components within the treatment enclosure thereby improving the efficiency and reliability of the treatment.

Although the present invention has been described in some detail by way of example for purposes of clarity and understanding, it will be apparent that certain changes and modifications may be practised within the scope of the appended claims.

The term ‘comprising’ as used in this specification and claims means ‘consisting at least in part of’. When interpreting statements in this specification and claims which include the term ‘comprising’, other features besides the features prefaced by this term in each statement can also be present. Related terms such as ‘comprise’ and ‘comprised’ are to be interpreted in a similar manner.

Claims (27)

What we claim is:

1. Apparatus for treatment of a particulate material comprising: 5 means for supporting the particulate material for transport between an entrance and an exit to the apparatus; means for supplying a gas flow through the means for supporting the material; and 10 means for distributing the gas flow to fluidize the particulate material on the means for supporting the particulate material to create a plurality of repeating regions of greater and lesser fluidization within the particulate material between the entrance and the exit.

2. Apparatus as claimed in claim 1 in which the means for supporting the particulate 15 material is adapted to transport the particulate material in a flow having a substantially constant depth.

3. Apparatus as claimed in claim 1 or 2 in which the means for supporting the particulate material for transport comprises a perforated conveyor belt.

4. Apparatus as claimed in claim 1, 2 or 3 in which the means for supplying a gas flow comprises at least one fan unit.

5. Apparatus as claimed in claim 1, 2, 3 or 4 in which the gas is cooled air for freezing 25 the particulate material.

6. Apparatus as claimed in claim 1, 2, 3 or 4 in which the gas is steam for blanching the particulate material.

7. Apparatus as claimed in claim 3 in which the means for distributing the gas flow comprises a gas distribution system to deliver gas upwardly through the means for supporting the particulate material, the gas flow being distributed in zones of concentrated and dispersed gas flow to create the regions of greater and lesser fluidization, respectively.

8. Apparatus as claimed in claim 7 in which the gas distribution system comprises at least one plate below the means for supporting the particulate material, the at least one plate defining an array of openings to define the zones of concentrated and dispersed gas flow.

9. Apparatus as claimed in claim 8 in which the at least one plate is formed with a plurality of smaller openings therethrough to define the zones of dispersed gas flow.

10. Apparatus as claimed in claim 9 in which the plurality of smaller openings are an 15 array of generally circular openings.

11. Apparatus as claimed in claim 9 in which the plurality of smaller openings are an array of slots. 20

12. Apparatus as claimed in claim 9, 10 or 11 in which the at least one plate is formed with at least one larger opening therethrough to define the zones of concentrated gas flow.

13. Apparatus as claimed in claim 12 in which the at least one larger opening is a slot. 25

14. Apparatus as claimed in claim 12 in which the at least one larger opening is a series of aligned generally circular openings.

15. Apparatus as claimed in any one of claims 8 to 11 in which the at least one plate comprises a plurality of plates spaced apart by a gap between adjacent plates, each gap between adjacent plates defining the zones of concentrated gas flow.

16. Apparatus as claimed in claim 15 in which the plurality of plates are generally triangular to define gaps between adjacent plates that extend obliquely to each other.

17. Apparatus as claimed in claim 15 in which the plurality of plates are generally rectangular to define gaps between adjacent plates that extend parallel to each other.

18. Apparatus as claimed in claim 15, 16 or 17 in which each of the plurality of plates 10 includes a flanged edge adjacent each gap to define a pair of flanged edges on opposite sides of the gap.

19. Apparatus as claimed in claim 18 in which each pair of flanged edges is adapted to define a passage for controlling the concentrated gas flow.

20. Apparatus as claimed in any one of claims 8 to 19 including means to control a volume of gas flow delivered from at least one of the zones of concentrated and dispersed gas flow. 20

21. Apparatus as claimed in claim 20 in which the means to control a volume of gas flow comprises dampers associated with the array of openings, the dampers being movable to adjust the area of the openings available for gas flow.

22. Apparatus as claimed in claim 20 in which the means to control a volume of gas 25 flow comprises variable speed drive means associated with the means for supplying a gas flow, whereby varying the speed of the drive means varies the volume of gas flow delivered to the array of openings.

23. Apparatus as claimed in claim 15 in which each gap between adjacent plates includes a air knife unit defining the zones of concentrated gas flow.

24. A method for treatment of a particulate material comprising: 5 supporting the particulate material for transport in a transport direction; supplying a gas flow through the particulate material; and distributing the gas flow to fluidize the particulate material to create a plurality of repeating 10 regions of greater and lesser fluidization in the particulate material as the material is moved in the transport direction.

25. Apparatus as claimed in claim 1, substantially as herein described with reference to any embodiment disclosed.

26. Apparatus for treatment of a particulate material, substantially as herein described with reference to any embodiment shown in the accompanying figures.

27. Method as claimed in claim 24, substantially as herein described with reference to 20 any embodiment disclosed.