The ovens used for baking food products based on a cereal paste vary depending on the specific type of product to be baked. At present there does not exist any standard oven suitable for baking all the types of product in satisfactory manner.
Thus, for crackers, and for soft items such as sponge, it is general practice to use direct gas flame (DGF) ovens.
For pastes from rotary machines or pastes that are extruded and cut to length, cyclothermal or forced-convection ovens are used, in addition to DGF ovens.
Nevertheless, best baking results can be obtained only by using DGF ovens for crackers and soft items, and cyclothermal or forced-convection ovens for-rotary-machine or cut pastes, with the precise configuration of each oven being adjusted in practically unalterable manner for each type of paste.
As presently designed, DGF ovens suffer from drawbacks such as:
With forced convection in present ovens, the energy conveyed by the flow of hot air is dissipated essentially in the form of a convective flux.
At a higher temperature, the energy could be dissipated, in addition or mainly, as radiant flux. This depends on temperature, on flow rate, and on flow speed.
With forced convection, there does not exist any oven in which the temperature of the baking chamber can reach temperatures in the range 350° C. to 400° C. with air at a speed that is less than or equal to 0.5 meters per second (m/s). Unfortunately, that is what is required to obtain a significant radiant flux for baking certain “soda” crackers. Furthermore, the speeds needed in present ovens lie in the range 3 m/s to 6 m/s (at the outlet from the nozzle). Unfortunately, such speeds do not enable light items to be baked since they are blown away by the flow of air inside the oven.
There also exist “impingement” ovens which are forced-convection ovens with air speeds not less than 20 m/s.
Nor do there exist any combined DGF and forced-convection ovens in which it is possible within a single module to modulate, in controlled manner, the quantities of energy supplied by each of those two modes.
The present invention seeks to provide an oven making it possible to mitigate at least one of the above-listed drawbacks, and also to exceed the limitations of all kinds of present oven by enabling a manufacturer to adjust optimally the types of energy that are supplied: DGF, and forced-convection with radiant flux and/or convective flux; and also to make certain innovations possible concerning food products, or to use a single pilot oven to simulate baking in a variety of different industrial ovens.
The invention thus provides a modular oven for food products, the oven including a conveyor device for entraining products from an inlet to an outlet of the oven, and comprising in cascade at least two, and preferably three, individual interchangeable modules, each individual module presenting:
In each individual module, the ceiling and/or the floor may be adjustable in height between at least a high position and a low position, and possibly also a middle position intermediate between the high and low positions.
The drive device may be self-propelled. It may be decoupled from the modules. It may be reversible (capable of operating in both directions). It includes a conveyor belt that is solid or gridded, possibly of variable width. The belt may be made of metal, of plastics material, of glass fiber, or of other materials.
In each individual module, the floor burners and/or the ceiling burners may be adjustable in height between at least a high position and a low position, optionally with a middle position intermediate between the high and low positions. The burners may also be pointable in any direction.
The invention also provides a method of using a modular oven as defined above for baking biscuits or cookies, wherein the oven comprises three individual modules in cascade, with the first module being used to perform a pre-baking and/or rising step, with the second module being used to perform a baking step, and with the third module being used to perform a step of browning and/or drying and/or cooling the product.
In a first variant, to manufacture crackers from a paste of conventional composition, the method implements:
In a second variant, to manufacture sponge from a paste of conventional composition, the method implements:
In a third variant, to manufacture a dry laminated biscuit or cookie from a paste of known type, e.g. to manufacture a “PRINCE” type biscuit as sold by the supplier LU France, the method implements:
In a fourth variant, to manufacture a product from a paste that is delivered in the form of individual unbaked moldings from a rotary machine, said paste being of known composition (which is generally relatively fatty to be unmoldable in a rotary machine provided with molding recesses), the method implements:
In a fifth variant, for baking a paste deposited in the form of individual pieces, in particular by extrusion and cutting, the method implements:
Other characteristics and advantages of the invention appear better on reading the following description given by way of non-limiting example and with reference to the drawings, in which:
As shown in
Two such rack devices 30 and 30′ are shown, giving additional latitude concerning the possibility of using two different vertical positions, one in the upstream or first half of a module, and the other in the downstream or second half of the same module.
The burners 40 are placed in adjustable positions along horizontal rails 16 for the floor burners and 26 for the ceiling burners. On each of these rails, the burners 40 can be added, moved, withdrawn, activated, and/or deactivated in individual manner. The configuration of the burners 40 can thus be adapted along a vertical axis. The number of burners may be greater than in a conventional installation.
As shown in
As shown in
The floor 10 and the floor burners 40 can also be adjusted in height, in positions that are mirror images of the above-described positions about the conveyor belt 5. The conditions concerning the possible positions for the floor and the floor burners are the same as for the ceiling and the ceiling burners, taking account of the “mirror” effect about the belt 5 (in other words the terms “high” and “low” are interchanged).
The forced convection of hot air and/or steam through nozzles 41 (which may be of various shapes) in the ceiling 20 and/or the floor 10 may have the following characteristics: speed at nozzle outlet lying in the range 0.5 m/s to 15 m/s, and temperature lying in the range 50° C. to 400° C.
The oven may also be associated with modules for heating by means of electromagnetic waves. The modules may also be used in a cooling mode by replacing hot air injection with injection of air that is cold and dry.
Number | Date | Country | Kind |
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02 11727 | Sep 2002 | FR | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/FR03/02513 | 8/12/2003 | WO | 00 | 3/23/2005 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2004/026034 | 4/1/2004 | WO | A |
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Number | Date | Country | |
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20060118099 A1 | Jun 2006 | US |