The present invention concerns a method for making an air-containing mixture, where air is introduced into a viscous mass of raw mixture for forming the air-containing mixture, and where the introduction of air is performed in connection with introducing the mixture in a treating unit, where the raw mixture under pressure is pumped through a nozzle. The invention also concerns an apparatus for making an air-containing mixture, where air is introduced into a viscous mass of raw mixture for forming the air-containing mixture, and where the introduction of air is performed in connection with introducing the mixture in a treating unit, where a mixing tank is provided between a pipe for introducing the mixture and the treatment unit.
The present invention has appeared in connection with working with mixtures in the form of ice mixtures for treatment in a treatment unit in the shape of an ice cream freezer. However, the general principle of the invention may be used in connection with other forms of mixing, where there is a need for admixing air in a viscous unit before introducing in a treatment unit.
A continuous ice cream freezer is in principle a scraper heat exchanger in which a fluid mass (called ice mixture) is cooled and partly frozen at the same time as stirring and admixing of air are performed, often in almost as large amounts as the fluid mass so that the finished product (ice cream) is a highly viscous foam.
The scraper heat exchanger is most frequently designed as a pipe (called a freezer tube) which is cooled externally and with a rotating shaft (called scraper shaft) inside. On the rotating shaft is mounted a number of knives that scrape the frozen ice off the pipe as well as producing a certain mixing action due to their movement through the product. The shaft itself may be designed in different ways; sometimes just as a fixed shaft, at other times with a built-in eccentric shaft, possibly with rotors mounted thereon which assist the admixing process.
Normally, the air is supplied through a check valve in immediate vicinity of the pipe where the fluid mass is introduced in the freezer tube.
The admixing of air then occurs exclusively by means of the movement of the scraper shaft through the mass (and thereby the movement of the knives and the eccentric/the rotors).
The entire production process of the ice cream normally occurs under pressure (typically 3-4 bars) as the ice mixture is pumped into the freezer tube by means of a mixing pump, and the ice cream leaves the freezer tube in a controlled way, either by means of a pump or by a suitable restrictor that ensures a correct pressure in the freezer tube itself.
Depending on which type of ice cream to be produced by the freezer, it may be advantageous to operate with different rotational speeds of the scraper shaft. For a very fluid product with high air content, a high speed is required to get the air “whipped” into the product. By a very firm, extrudable product, a lower speed is better in order not to add heat in the form of mechanical energy to the product.
At a very low rotational speed, such as required by a very firm ice cream, it may be difficult to achieve a sufficient mixing of ice mixture and air, whereby there is a risk of variations in the density of the product, large air bubbles and the like. Today, this is often solved by mounting a motorised pre-whipper at the inlet of the freezer tube. The pre-whipper is normally comprised by a number of stators and a number of rotors with small mutual spacing, where the rotors are driven by an electric motor.
Air and ice mixture are supplied together at the inlet of the pre-whipper, and when passing through the pre-whipper the air bubbles are broken due to the intensive movement, so that the freezer is thus receiving a ready-whipped foam for cooling/freezing.
The greatest drawbacks of a pre-whipper is the price and the increased maintenance of bearings and sealings in it.
It is the object of the present invention to indicate a system which includes a method and an apparatus for making an air-containing mixture, whereby the drawbacks of the prior art are avoided and so that it is particularly avoided to provide a motorised pre-whipper at the entrance of a treatment unit. It is a further object to indicate such a system where it is possible also to provide an air-containing mixture with uniform density.
According to the present invention, this is achieved by a method of the type specified in the introduction, which is peculiar in that by pumping the raw mixture through the nozzle, at least one mixing jet is formed which is sprayed through an air space against the surface of the air-containing mixture in a mixing step, so that air is entrained into the mixture, and that the air-containing mixture formed thereby is subsequently introduced in the treatment unit.
The apparatus according to the invention is peculiar in that the mixing tank is partly filled with air-containing mixture, that in this mixing tank there are provided an air intake for supplying air to the mixing tank, a nozzle for pumping the raw mixture in under pressure for forming at least one mixing jet which through an air gap is sprayed against the surface of the air-containing mixture in the mixing tank, and an outlet for air-containing mixture for connection to the treatment unit.
Traditionally, a pump is used for pumping the mixture into the treatment unit. This pump is used simultaneously for pumping the mixture through the nozzle before entering the treatment unit.
At the passage through the nozzle, the mixture experiences a pressure drop, thereby attaining high speed and emerging from the nozzle as a jet with a certain penetrating force. If letting the jet pour down into the mixture surface above which an air space is situated, the jet will draw some air in the form of bubbles down into the mixture as well as these bubbles will be torn apart due to the great difference in speed between the jet and the relatively static mixture. In other words, the jet will be able to produce a fine foam of mixture and air in the surface of the mixture in the impact area.
Due to the penetration force of the jet, a pre-whipping is provided in which admixing of air into the mixture is established, without need for extra motors for whipping air into the mixture. Maintenance of bearings, sealings etc required in connection with a pre-whipping unit is thus avoided.
When the idea of the invention is used in connection with ice cream production, the mixture will be a raw mixture of ice cream and the treatment unit will be a freezer tube.
In general, a system according to the invention will therefore consist of an independent unit which can be inserted into a known apparatus between a mixer pump and the point where the mixture is fed into the treatment unit.
In general, it may be said that the system according to the invention will include:
The invention will then be explained in more detail with reference to the accompanying drawing, where
In
A raw mixture 5 is introduced by means of a pump 6 via a pipe 7 to the freezer tube. In the pipe 7 air 8 is supplied via a check valve 9 into the raw mixture pumped in.
The freezer tube has an outlet 10 which is connected with a pump 11 to pump out air admixed ice cream 12 from the freezer pipe.
A mixture inlet 14 for a mixing tank 15 is provided in the apparatus, where mixture 7 admixed with air is provided in a lower part of the tank so as to extend to a level 16. Above the level 16 there is provided a space 17 which is introduced via the line 8 to the mixing tank 15. In the shown situation, the air supply appears in the upper part of the tank in the space 17 where air is provided. Alternatively, the supply may be effected at a position below the level 16, i.e. into the air-admixed mixture.
In the inlet 14, a nozzle 18 is provided. Under the action of the pump 6, the ice mixture is thus pumped through the nozzle so that a pressure drop occurs, whereby the mixture is provided a high speed when emerging from the nozzle as a jet 19. This jet has a penetrating force providing that it strikes the mixture face in an impact area 20 in the mixture surface 21. The jet 19 will hereby entrain air in the form of bubbles 22 into the mixture so that a mixture admixed with air is formed. The jet 19 will thus be capable of forming a fine foam consisting of a mixture of mixture and air. This mixed foam is drawn via the connecting line 7 to the treatment unit 13.
Due to the speed of the jet, a stirring in the tank is also produced, ensuring that the foam will not settle in the upper part of the mixture but will be well mixed into the entire volume of the mixture.
As an example can be mentioned that at a capacity of about 1000 l/hr, stirring may be established in the entire mixing tank when this is largely cylindric and has a diameter of about 100 mm and a length of 250-300 mm at a pressure drop between 1½ and 2 bar across the nozzle and with jet speeds of about 15-20 m/s.
The nozzle 18 may be provided as a nozzle producing a single jet, or with a slotted aperture for formation of a fan-shaped jet. Alternatively, there may be provided a nozzle forming more jets which are directed against different areas of the surface 21, in order thereby to utilise the volume of the mixing tank 15 optimally.
The nozzle 14 can be made adjustable so that it has variable geometry, whereby an approximately constant speed for the jet 19 can be maintained over a wide range of flow rates. The area of the nozzle aperture can be changed so that a greater flow goes through the nozzle with the same pressure drop across the nozzle. The nozzle 14 may e.g. be changed by adjusting a slotted nozzle aperture by means of a rotatable piston inside the nozzle, or by blocking more or less of a number of nozzle apertures in a multiple nozzle.
In
By this embodiment, it will be possible to concentrate the action of the jet 19 to a limited volume of ice mixture. This may provide a better whipping and thereby better admixing of air. Besides, turbulence at the outlet of the mixing tank 15 is avoided. Thus it becomes possible to avoid that large bubbles can be drawn out via the outlet 7. Large bubbles may rise in the air-mixed ice mixture 7 located at the bottom of the mixing tank 15.
The nozzles used in an apparatus according to the invention may provide one jet or be provided as multiple nozzles forming a bundle of jets in order to act on a larger part of the mixture surface 21. Alternatively, the nozzle may be provided as a film nozzle with a slotted aperture, so that a fan-shaped jet is provided. This fan-shaped jet may either be rectilinear or curving. The nozzle 18 may be fixed or be mounted for turning so that the jet can be directed to different areas 20 of the mixture face 21.
In an apparatus according to the invention, there may thus, as illustrated in
In the above, the invention is explained with reference to specific embodiments in connection with making ice mixture in a freezer tube. However, the invention may also find application in connection with other kinds of mixture to be admixed with air before entering into a treatment unit. This is the case with other kinds of confectionery products, but may in principle be applied in connection with any viscous product in which air is to be admixed before treatment is to be performed.
Number | Date | Country | Kind |
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PA200501404 | Oct 2005 | DK | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/DK2006/000547 | 10/4/2006 | WO | 00 | 9/24/2007 |