Patent Application
20230240341
Forming an object of the present invention is a plant for cooling foodstuffs according to the preamble of the main claim.
As known, in the food industry there often arises the need to rapidly bring the foodstuffs (of any kind, for example fruits and vegetables, dairy products, meat, ready-to-eat meals or semi-processed products, etc.) to a temperature sufficiently low to allow the safe storage thereof; for example, in the field of fruits and products derived from harvested fruits (such as grapes) such products are known to be subjected to rapid refrigeration, for example immediately after harvesting.
In particular, there are known plants where foodstuffs in solid pieces (grapes, pizzas, ice-cream, etc.) are subjected to continuous cooling or refrigeration by using cryogenic gases such as CO2 (in atomised liquid form, or, expanding from liquid, in solid form) or nitrogen (in atomised form). A such plant is for example described in US2011/0296853.
For example, in the wine-making industry there are known plants for cooling grapes or crushed grapes which use even considerably large stainless steel tanks in which there are placed the products to be refrigerated or to be cooled and into which there is injected CO2 to obtain the treatment under the desired temperature. These tanks or containers are often significantly large, therefore heavy and cumbersome.
Other plants for cooling, but more frequently for refrigerating or freezing thousands of kilograms of solid food products comprise tunnels which - in the case of mechanical refrigeration - are significantly large. In the case of cryogenic tunnels, such plants are smaller in size, but they can be used for treating solid foodstuffs only.
Generally, such tunnels contain a conveyor belt which conveys such food products while they are impacted by drops of liquid nitrogen emitted by nozzles arranged along the path of the conveyor belt. In both cases (mechanical tunnel or cryogenic tunnel), the plant does not allow to carry out the temperature treatment of liquid products.
An object of the present invention is to provide a plant for cooling foodstuffs or for refrigerating foodstuffs, in particular liquids and/or viscous fluids containing or not containing solid components (such as for example crushed grapes) which is improved with respect to the known plants.
Specifically, an object of the invention is to provide a plant of the type mentioned above that is compact, which can operate continuously (that is without ever stopping for the entire period of time required for the use thereof) and which does not require to pressurise the container in which the foodstuffs are treated.
A further object is to provide a compact plant of the type mentioned above which still allows to cool, in a desired fashion and without causing the freezing thereof, high amounts of food products in liquid and/or viscous form and containing or not containing said solid components.
Another object is to provide a plant where preferably the product is cooled using liquid nitrogen, cryogenic gas which has no negative environmental impact (unlike CO2), and where such gas can be used in low amounts and can also act as protection for the foodstuffs subjected to treatment.
These and other objects which shall be more apparent to the person skilled in the art are attained by a plant according to the attached independent claim.
For a better understanding of the present invention, the following drawings are attached hereto, purely by way of non-limiting example, wherein:
With reference to the aforementioned figures, and, in particular,
The plant comprises a container 2 suitable to receive the foodstuffs after the temperature treatment thereof, said container being represented in cylindrical shape (easy to clean) without prejudice to having other shapes. The container may be made of stainless steel or other material suitable to contain partly solid and partly liquid foodstuffs. Such container has a hatch 2K for access to the internal thereof for the cleaning thereof.
The foodstuffs reach the container 2 coming from a tank or other containment element 3 and they are continuously moved by a pump 4 acting as a means for moving the foodstuffs towards the container 2.
The pump directs the foodstuffs into a spiral duct 5 in which the foodstuffs (hereinafter referred to as “product” or “product to be cooled”) continuously move towards the container 2. The spiral duct 5 has an inlet end 7, connected to the pump 4 in any known manner, and an outlet end 8 arranged at least at the container from which the product flows out. Preferably, such outlet end 8 is inside the container and it is present at the end of a terminal section 10 of a duct arranged inside the container 2. Due to the reasons which will be described below, the section 10 could also have a portion 11 provided with surface openings 12, as shown in the figures.
The duct 5 has a plurality of turns 15 which are arranged, superimposed but on parallel planes, preferably around the container 2 so that the plant 1 can be small in size. However, the spiral duct 5 may also be separated from the container 2 and for example arranged beside it.
Along the turns 15 of the spiral duct 5 there are arranged liquid nitrogen injectors 16 suitable to introduce this cryogenic liquid gas, into the duct while the product to be cooled moves therein; therefore, during such movement, the product comes into contact with the cryogenic gas and it is cooled continuously.
It should be observed that although the use of liquid nitrogen as the refrigerant (cryogenic) gas is preferred, other cryogenic gases or mixtures thereof, such as for example CO2, may also be used.
As mentioned, the product is pushed into the spiral duct 5 by the pump. The power of the latter together with the expansion of the cryogenic gas in the duct enable the quick movement of the product towards the container 2 which therefore acts as a decanter. In the latter, the product to be cooled (for example grape must) however still receives negative calories from the cryogenic gas (nitrogen for example) and continues the cooling process thereof. Lastly, from the container 2 the cooled product may be extracted through a side discharge pipe 18 (preferably provided with a small tank 19 outside the container) and sent to a further container or tank arranged beside the container 2. The through-flow from one container to the other preferably occurs through communicating vessels, although a pump can be used.
A further discharge duct 20 is arranged at a bottom 21 of the container 2 to allow the full discharge of the container. This duct 20 may be connected to a pump - not shown - although it is not necessary given that the product can be discharged from the container 2 even by gravity.
The cryogenic gas or nitrogen, in the example, is injected into the spiral duct 5 through injector means 16 arranged on different turns 15 of such duct. In other words, and as shown in the drawings, the injector means 16 are arranged along different sections (the turns 15) of the duct or spiral 5 so as to be arranged at different heights of such duct (with respect to the container 2 if present in such spiral duct).
In the case of the figures, the various injector means 16 are superimposed with respect to each other and lie on adjacent and contiguous turns 15. Obviously, such injector means 16 may also not be superimposed and/or they may be associated with non-consecutive and adjacent turns: in the former case (shown in the figures) the injector means 16 are on the same side of the spiral duct 5 (and of the possible container 2 arranged in such duct); in the latter case, such injector means may be arranged staggered with respect to each other on different sides of the spiral duct 5.
Furthermore, should the spiral duct 5 have a horizontal extension (that is should it have a horizontal and not vertical median longitudinal axis like the one W in the figures), such injector means 16 are arranged at different distances along such median longitudinal axis along adjacent or non-adjacent consecutive turns.
Each of the injector means 16 comprises a sleeve 25 inserted into the spiral duct 5 (which is therefore obtained from various tubular components which define a single path, but which are connected through the sleeves 25 where the injector means 16 are provided for along the duct 5); such sleeve (or injector) 25 comprises a plurality of openings 26 which directly introduce liquid nitrogen into the spiral duct so as to interfere with the product moving therein.
Each sleeve or injector 25 is connected to other parts of the corresponding injector means 16 and supporting sensors, for example temperature 27 and pressure 28 sensors for checking the temperature and pressure present in the duct 5. Furthermore, such injector means are connected to a pipe 30 connected to a duct 31 of the liquid nitrogen which enables to send such cryogenic gas into the spiral duct 5. On such pipe and on the duct of the cryogenic gas 31 there are usually arranged valves 33 controlled by corresponding actuators 34 which, like the entire plant 1, are in turn commanded and controlled by a control unit (not shown) to which there are connected the aforementioned sensors 27 and 28, each present pump (for example the pump 4) and other components for controlling the plant. In particular, as a function of the fluid (liquid or gaseous) which passes through it, such valves 33 are of two per se known types and that is with electric or pneumatic control.
The duct 31 is supplied by cryogenic gas in any known manner.
It should be observed that when liquid nitrogen is not introduced into the spiral duct 5 through the injector means 16, gaseous nitrogen (or other cryogenic fluid in gaseous phase) is alternatively made to flow through the openings 26 so that such openings 26 do not clog the circulating product; therefore, there is alternated the introduction of liquid nitrogen with gaseous nitrogen into the duct 5.
Similarly, the openings 12 of the portion 11 of the section 10 of the spiral duct 5 in the container 2 allow a better diffusion of the gaseous nitrogen present in the spiral duct into the latter, also reducing the “whiplash” which could be perceived if one were to use the outlet end 8 of the duct alone for the outflow of the gas.
The introduction of nitrogen (gaseous by now) into the container 2 also allows to create - therein - an inert and protective environment for the product, cooled by now, present therein.
When using the plant 1, the container 2 is initially empty and the pump 4 moves the product to be cooled (for example grapes or grape must) in the duct or spiral 5 for example by drawing it for example from the tank 3 arranged upstream of a destemmer (not shown) or from the destemmer itself. Once a predetermined period of time has elapsed, after which the product is certainly supplied to the duct or after (in a per se known manner) such product has been detected in the duct, the valves 33 open and liquid nitrogen is introduced into the duct 5 through the injector means 16 (or refrigerant means) which direct the cryogenic gas onto the moving product. The power of the pump together with the expansion of the gas enable a rapid movement of the product towards the container 2.
The nitrogen moves with the product and, given that it cannot exit from the spiral duct 5, it follows it up to the container continuously cooling the product.
It should be observed that the product does not freeze in the spiral duct 5 given that it moves with the nitrogen (or similar cryogenic gas). The cryogenic gas is introduced into the duct 5 in a diffused manner along such duct due to the fact that the injector means 16 are arranged on different turns 15 of the spiral duct 5. Such diffused introduction enables to reduce the amount of cryogenic gas used, therefore reducing the costs for operating the plant 1.
Introducing the cryogenic fluid in different points of the spiral duct enables both the continuous movement of the product and the refrigeration thereof simultaneously.
The speed at which the product moves contributes to preventing the freezing thereof. Such speed obviously depends on the power or capacity of the pump and on the cross-section of the spiral duct 5: the first experimental tests showed that a speed of the product comprised between 0.1 and 5 m/s, preferably between 0.25 and 0.5 m/s and advantageously between 0.28 and 0.40 m/s enables to prevent the product from freezing.
For example, a duct having a cross-section measuring 100 mm, a pump having a capacity of 100 q/h and a power frequency of the inverter connected to such pump equal to 50 Hz, enables to obtain a speed of the product amounting to about 0.35 m/s which however prevents the product from freezing and solidifying.
After filling the container 2 with the refrigerated product, the product flows into the duct 18 due to the communicating vessels effect and it can be collected in another tank/container. Therefore, the invention does not use compressed air to move the product and the shape of the duct (spiral-like) enables an optimal cooling of the product. As a matter of fact, the spiral duct is longer than the occupied space and it contributes to keeping the product and the cryogenic gas in contact for a long period of time. Furthermore, the configuration of the duct contributes to avoiding the presence of corners therein, where the foodstuffs could cease the movement thereof.
Furthermore, in order to avoid excessive concentration of cold in the duct 5, besides the continuous movement of the product at a speed deemed optimal, the injectors 16 are advantageously activated intermittently with respect to each other.
The invention allows to obtain a refrigeration of a product or of liquid foodstuffs, or in viscous fluid phase containing or not containing solid components, by means of a compact plant that is easy to build and use. The plant of the invention preferably uses liquid nitrogen, an almost zero-environmental impact cryogenic gas.
The shape of the part of the plant where the product and nitrogen reach and remain in contact (that is the spiral duct) and the diffusion of the points of the duct 5 in which nitrogen is introduced into the duct, enables to obtain a high thermal exchange time between the cryogenic fluid and the product and therefore a high efficiency of the process. Furthermore, this can be obtained with low amounts of cryogenic gas without prejudice to obtaining, at the outlet of the duct in the container 2, temperatures of the product up to and beyond 10° C. and in particular at least amounting to 7-8° C. below the temperature of the product at the inlet of the spiral duct.
Furthermore, the plant is not pressurised, and this facilitates the construction thereof and it can operate continuously. Furthermore, the use of nitrogen enables to create an inert environment in the container 2 and the spiral duct.
The container 2 is always emptied by the duct 20 once the introduction of the refrigerated product has terminated.
It should also be observed that the injector means 16 are arranged at a higher level of the spiral duct 5 with respect to the position in which the injector means 16 are arranged in the solution of
Furthermore, in the solution of
Obviously, the nitrogen may be supplied into the spiral duct 5 even through nozzles shaped differently with respect to the description above and it is known to the person skilled in the art.
Also the plant 1 in the embodiment of
Various preferred embodiments of the invention have been described. However, others can still be obtained based on the description above and according to the teaching of the claims below which define the scope of protection of the invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102022000001718 | Feb 2022 | IT | national |
