The present invention relates to a milk emulsifying method and unit.
The present invention may be used to particular advantage for emulsifying milk in automatic or non-automatic infusion devices, for producing cappuccini or similar infusion beverages, and to which specific reference is made in the following description.
Infusion devices of the above type normally employ milk emulsifying units of the type described, for example, in EP 1785074, which normally comprise a first milk feed line; a second air feed line; and a third steam feed line, which can be cut off by a valve to produce cold emulsified milk.
The three feed lines converge substantially independently, the first milk feed line always fully independent of the other two, inside an emulsifying chamber—normally a venturi chamber—which mixes the milk, air and steam (if any) to supply emulsified milk at the outlet, i.e. milk with a surface froth or ‘cream’, whose temperature and volume depend on the presence or absence of steam, the steam temperature, and the milk, air and steam ratio, which is controlled by regulating flow from a pump along the first line, and by regulating airflow along the second line by means of hydraulic resistors for regulating flow continuously or in pulses at adjustable frequency.
Though the amount of air, in the form of bubbles, in the emulsified milk is adjustable, known emulsifying units of the above type have the drawback of enabling practically no control over the ‘texture’, i.e. diameter, of the bubbles, which is what determines the stability of the froth produced, i.e. the smaller the bubbles, the more stable the froth is.
The emulsifying chamber being a venturi chamber, in which air is injected into the milk flow at such high speed as to allow absolutely no control over the emulsion produced, there is normally no way of predicting whether the air injected produces a large number of relatively small-diameter bubbles, or only a few large-diameter bubbles, and, in the event of the latter, whether the bubbles are broken up at the emulsifying chamber outlet.
It is an object of the present invention to provide a milk emulsifying method and unit designed to eliminate the above drawbacks.
More specifically, it is an object of the present invention to provide a milk emulsifying method and unit designed to control the number and texture of the air bubbles in the emulsified milk produced.
According to the present invention, there is provided a milk emulsifying method as claimed in claim 1 and preferably in any one of the Claims depending directly or indirectly on claim 1.
According to the present invention, there is also provided a milk emulsifying unit as claimed in claim 7 and preferably in any one of the Claims depending directly or indirectly on claim 7.
A non-limiting embodiment of the present invention will be described by way of example with reference to the accompanying drawings, in which:
Number 1 in
Emulsifying unit 6 comprises a milk feed line 7; an air feed line 8 communicating with feed line 7 at an intermediate ‘Y’ fitting 9, and having an end portion 10 in common with feed line 7 and terminating inside emulsifying chamber 5; and a steam feed line 11 terminating directly inside emulsifying chamber 5 and separate from feed lines 7 and 8.
Feed line 7 comprises a normally refrigerated tank 12, and extends from tank 12 to intermediate fitting 9 via a pump 13—normally, though not necessarily, a gear pump.
Feed line 8 has an inlet 14 communicating with the outside, and extends from inlet 14 to intermediate fitting 9 via, and in the order shown: an optional air filter 15; a valve assembly 16 for controlling airflow along feed line 8; and an optional calibrated non-return valve 17, which permits airflow to intermediate fitting 9, but under no circumstances permits backflow of milk to valve assembly 16 via intermediate fitting 9.
Feed line 11 comprises a boiler 18 supplied with water from a source (not shown), such as the water mains, and which feeds steam to emulsifying chamber 5 via an electrically actuated shut-off valve 20 and at a given temperature controlled by a thermostat unit 19 and preferably on the basis of the milk temperature recorded by a sensor (not shown) at intermediate fitting 9.
As shown in
Schematically, RCU 24 comprises a square wave generator SWG 25 for producing a train of square waves, the frequency of which is regulated by a control circuit on the basis of a given number of partly set and partly recorded quantities (e.g. a given range; an external temperature; beverage characteristics dictated by average consumer preference in the country in which infusion device 1 is operated, etc.); and a pulse width modulator PWM 27 for regulating the duty cycle, i.e. activation time within each pulse, and which is controlled by a control circuit 28 on the basis of a given number of other partly set and partly recorded quantities (e.g. a given range; steam temperature; the temperature inside cup 3, etc.).
RCU 24 is preferably implemented in a PLC or, in general, in an integrated or distributed electronic control system designed to receive and process recorded quantities, calculate the necessary frequency and duty cycle, and supply the necessary power to actuator 23.
Valve assembly 16 is a commercial type, has a very fast response time (in the order of a thousandth of a second), and is used in emulsifying unit 6 to break up or ‘chop’ the continuous airflow drawn through inlet 14 into a succession of ‘segments’, each defining an air bubble on entering the milk flow at intermediate fitting 9.
Because air is drawn from the outside by the low pressure produced along feed line 8, just upstream from intermediate fitting 9, the air ‘segments’ moving along feed line 8 to intermediate fitting 9 all travel at the same speed, like the peaks of a single pressure wave modulated by valve assembly 16, remain separate, and penetrate the milk flow from feed line 7 without compacting, i.e. still remaining separate, on account of the substantially zero relative speed at which the air ‘segments’ enter the milk flow.
In other words, because of the presence of valve assembly 16, pre-emulsification occurs along shared end portion 10, so that what flows out of shared end portion 10 is a highly stable mixture of milk and dispersed air bubbles.
In emulsifying unit 6, RCU 24 serves to adjust the size and number of these air bubbles, and so adjust both the amount and texture of the froth produced, without having to intervene on the cross sectional size of passage 21, which may thus be made large enough to reduce cleaning, which can be further reduced using air filter 15.
The number of air bubbles produced can be adjusted by adjusting the frequency of the square waves controlling actuator 23 by means of SWG 25; and the size, i.e. ‘texture’, of the air bubbles can be adjusted by adjusting the length of the duty cycle, i.e. the opening time of shutter 22, by means of PWM 27.
In other words, regulating the frequency and duration of the activating pulse of shutter 22 by means of PWM 27 provides for both dynamic ‘mean adjustment’ and choking of the airflow to achieve optimum quantity and size of the air bubbles in the emulsion.
Bubble size being strongly affected by beverage temperature, electrically actuated valve 20 is kept closed to produce cold emulsified milk, and the above adjustments preferably also take ambient temperature into account; and, conversely, to produce hot emulsified milk, electrically actuated valve 20 is kept open, and the above adjustments preferably also take into account the temperature setting of thermostat unit 19.
Valve assembly 16 may obviously be kept closed to produce a flat beverage, though this operating mode is outside the scope of the technical problem dealt with herein, and is included solely for the sake of thoroughness.
Number | Date | Country | Kind |
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TO2010A000831 | Oct 2010 | IT | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB11/54412 | 10/6/2011 | WO | 00 | 11/12/2013 |