Apparatus and method for producing aerated confectionery masses
For producing an aerated confectionery mass, a raw confectionery mass is fed at a feed rate from a supply to an aeration unit for introducing gas into the confectionery mass and wherein the aerated confectionery mass is fed to a production line for the production of confectionery or tablets. The feed rate of the raw confectionery mass is controlled such that it corresponds to the demand of the production line, the amount of introduced gas is controlled in response to the feed rate of the confectionery mass so that the aeration level of the confectionery mass remains substantially constant and the temperature of the aeration mass within the aeration unit is controlled such that it remains substantially constant and independent from the feed rate. The aeration unit may include a rotor for stirring and kneading the confectionery mass containing the introduced gas, the rotational speed of the rotor being controlled such that it is enhanced for higher feed rates and reduced for lower feed rates in order to produce gas bubbles of approximately the same size independent from the feed rate. In order to keep the bubble size small during the depositing step, the depositing is realized via a pressurized manifold containing multiple nozzles.
1. A method for producing an aerated confectionery mass comprising:
providing an aeration unit comprising a stator and a rotor;
feeding a raw confectionery mass at a feed rate from a supply to the aeration unit;
introducing gas into confectionery mass within the space between the stator and the rotor of the aeration unit;
stirring and kneading the confectionery mass containing the introduced gas by the rotor of the aeration unit;
feeding the aerated confectionery mass to a production line for production of confectionery;
controlling the feed rate of the raw confectionery mass from the supply to the aeration unit according to demand of the production line;
controlling amount of introduced gas in response to the feed rate of the confectionery mass so that an aeration level of the confectionery mass remains substantially constant;
controlling temperature of the mass within the aeration unit such that said mass remains substantially constant and independent from the feed rate; and
controlling the rotational speed of the rotor of the aeration unit such that it is increased for higher feed rates and reduced for lower feed rates in order to produce gas bubbles of approximately the same size independent from the feed rate.
2. The method according to claim 1 , wherein pressure in the aeration unit is enhanced for higher feed rates and reduced for lower feed rates.
3. The method according to claim 2 , further comprising filling the confectionery mass under pressure into moulds of a molding line through a pressurized manifold of the production line.
4. The method according to claim 1 , wherein the confectionery mass is a chocolate mass or filling mass.
5. The method according to claim 1 , wherein the confectionery mass is a filling mass.
6. The method according to claim 1 , further comprising receiving a signal at a control unit from a level indicator of a depositor hopper, the signal received at the control unit from the depositor hopper indicating a demand of the production line, a high level indicating a low demand of the production line and a low level indicating a high demand of the production line, and wherein the controlling the feed rate further comprises controlling, via the control unit, the feed rate of the raw confectionery mass in response to the signal received at the control unit from the speed detector according to the indicated demand of the production line.
7. The method according to claim 1 , further comprising receiving a signal at a control unit from a speed detector configured to measure speed of the production line, a high speed indicating a high demand of the production line and a low speed indicating a low demand of the production line, and wherein the controlling the feed rate further comprises controlling, via the control unit, the feed rate of the raw confectionery mass in response to the signal received at the control unit from the speed detector according to the indicated demand of the production line.
8. The method according to claim 1 , further comprising maintaining back-pressure to the aeration unit at 3-4 bar during the feeding of the aerated confectionery mass to the production line for production of confectionery, and increasing the back-pressure to the aeration unit to 5-7 bar in response to a signal received at a control unit indicating that the demand of the production line is high.
9. A method for producing an aerated confectionery mass comprising:
providing an aeration unit comprising a stator and a rotor;
feeding a raw confectionery mass at a feed rate from a supply to the aeration unit;
introducing gas into confectionery mass within the space between the stator and the rotor of the aeration unit;
stirring and kneading the confectionery mass containing the introduced gas by the rotor of the aeration unit;
feeding the aerated confectionery mass to a production line for production of confectionery;
receiving a signal at a control unit from a level indicator of a depositor hopper, the signal received at the control unit from the depositor hopper indicating a demand of the production line, a high level indicating a low demand of the production line and a low level indicating a high demand of the production line;
controlling, via the control unit, the feed rate of the raw confectionery mass from the supply to the aeration unit in response to the signal received at the control unit from the level indicator according to the indicated demand of the production line;
controlling amount of introduced gas in response to the feed rate of the confectionery mass so that an aeration level of the confectionery mass remains substantially constant;
controlling temperature of the mass within the aeration unit such that said mass remains substantially constant and independent from the feed rate; and
controlling the rotational speed of the rotor of the aeration device such that the rotational speed is increased for higher feed rates and reduced for lower feed rates in order to produce gas bubbles of less than about 50 microns independent of the feed rate.
10. The method according to claim 9 , wherein pressure in the aeration unit is enhanced for higher feed rates and reduced for lower feed rates.
11. The method according to claim 9 , wherein the method further comprises controlling backpressure in the aeration unit in response to the feed rate of the confectionary mass, wherein the backpressure and the rotational speed of the rotor of the aeration device are controlled such that the rotational speed and backpressure are increased for higher feed rates and reduced for lower feed rates.
12. The method according to claim 9 , wherein no portion of the confectionary mass is returned from the aeration device to the supply.
13. The method according to claim 9 , further comprising maintaining back-pressure to the aeration unit at 3-4 bar during the feeding of the aerated confectionery mass to the production line for production of confectionery, and increasing the back-pressure to the aeration unit to 5-7 bar in response to a signal received at a control unit indicating that the demand of the production line is high.
14. A method for producing an aerated confectionery mass comprising:
providing an aeration unit comprising a stator and a rotor;
feeding a raw confectionery mass at a feed rate from a supply to the aeration unit;
introducing gas into confectionery mass within the space between the stator and the rotor of the aeration unit;
stirring and kneading the confectionery mass containing the introduced gas by the rotor of the aeration unit;
feeding the aerated confectionery mass to a production line for production of confectionery;
receiving a signal at a control unit from a speed detector configured to measure speed of the production line, a high speed indicating a high demand of the production line and a low speed indicating a low demand of the production line;
controlling, via the control unit, the feed rate of the raw confectionery mass from the supply to the aeration unit in response to the signal received at the control unit from the speed detector according to the indicated demand of the production line;
controlling amount of introduced gas in response to the feed rate of the confectionery mass so that an aeration level of the confectionery mass remains substantially constant;
controlling temperature of the mass within the aeration unit such that said mass remains substantially constant and independent from the feed rate; and
controlling the rotational speed of the rotor of the aeration device such that the rotational speed is increased for higher feed rates and reduced for lower feed rates in order to produce gas bubbles of less than about 50 microns independent of the feed rate.
15. The method according to claim 14 , wherein pressure in the aeration unit is enhanced for higher feed rates and reduced for lower feed rates.
16. The method according to claim 14 , further comprising maintaining back-pressure to the aeration unit at 3-4 bar during the feeding of the aerated confectionery mass to the production line for production of confectionery, and increasing the back-pressure to the aeration unit to 5-7 bar in response to a signal received at a control unit indicating that the demand of the production line is high.
17. A method for producing an aerated confectionery mass comprising:
providing an aeration unit comprising a stator and a rotor;
feeding a raw confectionery mass at a feed rate from a supply to the aeration unit;
introducing gas into confectionery mass within the space between the stator and the rotor of the aeration unit;
stirring and kneading the confectionery mass containing the introduced gas by the rotor of the aeration unit;
feeding the aerated confectionery mass to a production line for production of confectionery;
receiving a signal at a control unit from a level indicator of a depositor hopper, the signal received at the control unit from the depositor hopper indicating a demand of the production line, a high level indicating a low demand of the production line and a low level indicating a high demand of the production line;
controlling, via the control unit, the feed rate of the raw confectionery mass from the supply to the aeration unit in response to the signal received at the control unit from the level indicator according to the indicated demand of the production line;
controlling amount of introduced gas in response to the feed rate of the confectionery mass so that an aeration level of the confectionery mass remains substantially constant;
controlling temperature of the mass within the aeration unit such that said mass remains substantially constant and independent from the feed rate; and
controlling the rotational speed of the rotor such that it is increased for higher feed rates and reduced for lower feed rates in order to produce gas bubbles less than a desired maximum size independent from the feed rate and the rotational speed controlled to not be higher than necessary for producing gas bubbles of the desired size.
18. The method according to claim 17 , further comprising maintaining back-pressure to the aeration unit at 3-4 bar during the feeding of the aerated confectionery mass to the production line for production of confectionery and increasing the back-pressure to the aeration unit to 5-7 bar in response to a signal received at a control unit indicating that the demand of the production line is high.