EP2428735B1 - Cooking device with steam generator and method for regulating a steam generator for a cooking device - Google Patents

Cooking device with steam generator and method for regulating a steam generator for a cooking device Download PDF

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Publication number
EP2428735B1
EP2428735B1 EP11007208.9A EP11007208A EP2428735B1 EP 2428735 B1 EP2428735 B1 EP 2428735B1 EP 11007208 A EP11007208 A EP 11007208A EP 2428735 B1 EP2428735 B1 EP 2428735B1
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EP
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Prior art keywords
steam generator
controller
cooking device
steam
cooking
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EP11007208.9A
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German (de)
French (fr)
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EP2428735A3 (en
EP2428735A2 (en
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Thomas Dr. Schreiner
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Rational AG
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Rational AG
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24CDOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
    • F24C7/00Stoves or ranges heated by electric energy
    • F24C7/08Arrangement or mounting of control or safety devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24CDOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
    • F24C15/00Details
    • F24C15/32Arrangements of ducts for hot gases, e.g. in or around baking ovens
    • F24C15/322Arrangements of ducts for hot gases, e.g. in or around baking ovens with forced circulation
    • F24C15/327Arrangements of ducts for hot gases, e.g. in or around baking ovens with forced circulation with air moisturising

Definitions

  • the invention relates to a cooking appliance with a cooking chamber, a steam generator and a controller that controls the steam generator.
  • the invention further relates to a method for controlling a steam generator for a cooking appliance.
  • threshold controllers In cooking appliances for temperature or humidity control threshold regulators are usually used because they can be used usually without specific adaptation to the device size, the type of heating (gas or electric) and the load in the oven. In steam mode, however, threshold controllers have serious disadvantages if a high steam content in the cooking chamber is to be maintained.
  • a threshold controller controls between an upper threshold and a lower threshold. If the upper threshold has been exceeded, the steam generator is switched off. Subsequently, the temperature is reduced by condensing the water vapor inside the cooking chamber (for example, to be cooked products). At the same time, the volume of the gas contained in the interior of the cooking chamber is reduced, so that air has to be sucked in, usually from a condensation or drainage region of the cooking appliance.
  • the steam generator is switched on again. Thereafter, water vapor is again produced until the temperature in the cooking chamber has again reached the upper threshold.
  • a device for controlling cooking, roasting and cooking processes in the cooking chamber of a baking oven wherein a control circuit is provided with an electronic controller, the sensor-controlled adjusts a corresponding oven energy level depending on cooking properties and their associated temperature-time profiles with gargutspezifischen fluctuation ranges is adjustable.
  • the generic WO 2009/065197 A1 discloses a gas-powered home oven that also provides the option of steaming.
  • a controller is provided which, in addition to other alternatives mentioned, may have a two-point controller or a PID controller.
  • the EP 1 761 111 A2 and the EP 1 724 530 A1 also describe home-baking ovens with an integrated steam generator, the ovens having centralized control comprising a PID controller or other suitable controller.
  • a cooking appliance according to the invention with the features of claim 1 is provided.
  • the invention is based on the idea of controlling the steam generator in an operating range in which the steam content is to be kept constant, with the signal of the continuous controller. This prevents the steam generator from being switched off until air has been sucked in.
  • the steam generator has at least two power levels.
  • the steam generator is in principle further operated with discrete power stages, but in the operating range in which the steam content is to be kept constant, be controlled by the continuous controller.
  • the continuous controller operates the steam generator with a maximum average power, which is below the first power level.
  • the steam generator then works with a holding stage, which can be integrated into the threshold controller like an additional smaller heating stage.
  • the first power level is in the range of about 25% to about 50% of the second, maximum power level. It has been found that with such a spreading of the heating stages, the desired performance can be well represented. In addition, these power levels result constructively in an advantageous manner. In an electrically operated steam generator halving the power in star or delta connection can be achieved with a relay or SSR. In the case of a gas-driven steam generator, on the other hand, the smallest heating level will have a capacity of approximately 25% of the maximum power, even if lower powers could be advantageous.
  • the continuous controller operates the steam generator with a power that is about 75% of the power of the first power level.
  • the steam generator operates at a power of 37.5% of the maximum heating power, which has proved to be advantageous for maintaining a constant steam content in the cooking space ,
  • the continuous controller outputs as a control variable a buffer variable, by means of which the controller operates the steam generator in pulse width modulation.
  • a buffer variable by means of which the controller operates the steam generator in pulse width modulation.
  • the cooking chamber is in flow communication with a drain region, wherein in the drain region, a steam buffer is formed whose volume is at least equal to the vapor volume condensed between two heating pulses in the cooking chamber.
  • a steam buffer is formed whose volume is at least equal to the vapor volume condensed between two heating pulses in the cooking chamber.
  • the continuous controller is a PI controller.
  • a controller is sufficient to maintain the setpoint (temperature or humidity) to be maintained in the cooking chamber during the holding phase.
  • a more elaborate PID controller can be dispensed with.
  • a method for controlling a steam generator for a cooking appliance with the features of claim 10 is provided to solve the above object.
  • This method combines the advantage of a robust threshold controller with the advantage of more precise control by means of a continuous regulator.
  • the threshold controller controls the steam generator until the actual value to be controlled in the cooking chamber is at least 90% of the setpoint. It simplifies the design of the continuous controller if it only has to take over control in the vicinity of the setpoint and the approach to the setpoint is taken over by the robust threshold controller.
  • the continuous controller continuously regulates the steam generator. In this way, the quality of control can be increased and the energy consumption can be reduced.
  • FIG. 1 schematically a cooking appliance 10 is shown, which is intended for commercial kitchens and is known as a combination damper. It contains a cooking chamber 12 into which products to be cooked can be introduced. It is a steam generator 14 is provided which can generate water vapor, which can be passed into the interior of the cooking chamber 12.
  • the cooking appliance 10 also has a heater in order to introduce heated air into the cooking chamber. However, since this heater in the context of the present application without meaning, it is not shown here for the sake of clarity.
  • a controller 16 which receives as input signals, inter alia, a signal from a temperature and / or humidity sensor 18, which is arranged in the interior of the cooking chamber 12, and by an operating unit 20.
  • an operator can different cooking conditions in Inside the cooking chamber or select more complex cooking programs.
  • the controller 16 includes a threshold controller 22 and a continuous controller 24, which is designed here as a PI controller.
  • the controller 16 controls the steam generator 14 by specifying whether the steam generator is switched off, is operated with a first power stage 14.1 or a second power stage 14.2.
  • the steam generator has a power that is about 50% of the second, maximum power level.
  • the power levels are specified here by the controller, for example, by the interconnection of three radiators in star or delta connection. Depending on the requirements, other or more power levels may be used.
  • a drain region 26 is provided, which is designed like a box and provided with a condensation device 28. Of the Drain area 26 is connected to an exhaust pipe 30. Between the connection of the exhaust pipe 30 and the connection to the cooking chamber, a separating plate 32 is provided, so that a steam buffer 34 is formed between the cooking chamber and the separating plate.
  • the controller 16 uses only the threshold controller 22 for the control of the steam generator. This operates the steam generator 14 in the second heating stage 14.2, ie with a power of 100% (see the power curve P in the diagram). After almost 200 seconds have elapsed, exceeds the temperature T I in the cooking chamber 12, the threshold above which the steam generator 14 is switched back to the first heating stage 14.1; the power curve P thus drops to a value of 50%.
  • the controller 16 switches from the threshold value controller 22 to the PI controller 24 and uses this to control the steam generator 14. Accordingly, the value for the setpoint power HS S of the steam generator in the holding stage increases to a predetermined value of 75% of the power of the first heating stage (see curve HS S ).
  • This value HS S is treated by the controller 16 as a buffer variable, based on which the steam generator 14 is now operated with the first heating stage 14.1 pulse width modulated.
  • the controller 16 Since the maximum power of the steam generator is set here with 75% of the power of the first heating stage 14.1, the controller 16 switches on the first heating stage 14.1 of the steam generator 14 within a given time interval for 75% of the time and for 25% of the time, if the steam generator should be operated in the holding stage with maximum power. This is the case here as long as the setpoint H S for the holding stage remains at the value of 75%, that is to say just under 250 seconds. At this time The PI controller 24 begins to regulate, as can be seen from the fluctuating values for the setpoint HS S of the holding stage.
  • a continuous regulator in combination with a steam generator which is switched between two discrete power levels, can be used to keep the steam content in the cooking chamber comparatively constant.
  • the controller reaches a steady state after about 400 seconds.
  • the power given by the PI controller 24 for the operation of the steam generator 14 in the holding stage can be represented by a multiplicity of very short heating pulses, between which correspondingly short switch-off times are used.
  • electrically operated steam generators could be adjusted quasi-continuous by switching on and off of individual half-waves of the mains frequency, the heating power. In this way one comes very close to an actually stepless control of the power, which would be advantageous in terms of control quality and energy consumption.
  • FIG. 3 an embodiment is shown, which is characterized by a larger steam buffer 34.
  • This is formed by the fact that the separating plate 32 is arranged closer to the exhaust pipe 30.
  • the function of the separating plate 32 is to prevent a mixing of the steam with the air in the discharge region 26 as far as possible.
  • the volume of the vapor buffer 34 defined with the separating plate 32 is at least as great as the vapor volume which can condense between two heating pulses in the cooking chamber 12. This ensures that air is not sucked in between two heating pulses, but steam from the steam buffer 34 (see the arrow D). Accordingly, the condensation device 28 must also be switched off at least between two heating pulses, so that steam can actually be stored in the vapor buffer 34.
  • FIG. 4 an alternative embodiment is shown.
  • this flow guide plates 36 are used, which extend in the longitudinal direction of the drain.
  • the process can either have a circular cross section (see detail D1) or a box-shaped cross section (see detail D2).
  • the Strömungsleitbleche 36 act as a vortex breaker, similar to the separating plate 32 prevent the air in the drain region 26 mixed with the existing steam there. Thus, as pure as possible vapor can be sucked back into the cooking space in the phases between two heating pulses. Due to the orientation of the flow guide plates 36 in the direction of the drainage channel, the flow in the longitudinal direction is hardly affected, but strongly suppressed in a direction transverse thereto.
  • the flow baffles extending in the flow direction can all be mounted on the top of the drain. This makes it easier to rinse out soiling, so that no impurities can accumulate on the sheets.

Description

Die Erfindung betrifft ein Gargerät mit einem Garraum, einem Dampfgenerator und einer Steuerung, die den Dampfgenerator ansteuert. Die Erfindung betrifft ferner ein Verfahren zur Regelung eines Dampfgenerators für ein Gargerät.The invention relates to a cooking appliance with a cooking chamber, a steam generator and a controller that controls the steam generator. The invention further relates to a method for controlling a steam generator for a cooking appliance.

In Gargeräten werden zur Temperatur- oder Feuchteregelung üblicherweise Schwellwertregler eingesetzt, weil diese in der Regel ohne spezifische Anpassung an die Gerätegröße, an die Beheizungsart (Gas oder Elektro) und die Last im Garraum verwendet werden können. In der Betriebsart Dampf haben Schwellwertregler jedoch gravierende Nachteile, wenn ein hoher Dampfgehalt im Garraum aufrechterhalten werden soll. Ein Schwellwertregler regelt zwischen einem oberen Schwellwert und einem unteren Schwellwert hin und her. Wenn der obere Schwellwert überschritten wurde, wird der Dampfgenerator abgeschaltet. Anschließend verringert sich durch Kondensieren des Wasserdampfs im Inneren des Garraums (beispielsweise an zu garenden Produkten) die Temperatur. Gleichzeitig verringert sich das Volumen des im Inneren des Garraums enthaltenen Gases, sodass Luft nachgesaugt werden muss, üblicherweise aus einem Kondensations- oder Ablaufbereich des Gargeräts. Wenn die Temperatur im Garraum schließlich den unteren Schwellwert des Schwellwertreglers erreicht hat, wird der Dampfgenerator wieder eingeschaltet. Danach wird wieder so lange Wasserdampf produziert, bis die Temperatur im Garraum wieder den oberen Schwellwert erreicht hat.In cooking appliances for temperature or humidity control threshold regulators are usually used because they can be used usually without specific adaptation to the device size, the type of heating (gas or electric) and the load in the oven. In steam mode, however, threshold controllers have serious disadvantages if a high steam content in the cooking chamber is to be maintained. A threshold controller controls between an upper threshold and a lower threshold. If the upper threshold has been exceeded, the steam generator is switched off. Subsequently, the temperature is reduced by condensing the water vapor inside the cooking chamber (for example, to be cooked products). At the same time, the volume of the gas contained in the interior of the cooking chamber is reduced, so that air has to be sucked in, usually from a condensation or drainage region of the cooking appliance. When the temperature in the cooking chamber has finally reached the lower threshold value of the threshold controller, the steam generator is switched on again. Thereafter, water vapor is again produced until the temperature in the cooking chamber has again reached the upper threshold.

Da die nachgesaugte Luft sich aber mit dem Dampf im Garraum vermischt, muss der vom Dampfgenerator erzeugte und in den Garraum eingebrachte Wasserdampf ein Gemisch aus Wasserdampf und nachgesaugter Luft verdrängen, um den Dampfgehalt und die Temperatur im Garraum zu erhöhen. Dadurch muss sehr viel mehr Dampf produziert werden, als Luft nachgesaugt worden ist. Als Beispiel wird angenommen, dass bei 90 % Feuchte 1 Liter Wasserdampf im Garraum kondensiert, der durch Luft ersetzt wird. Daraufhin muss das Gerät 10 Liter Dampfgemisch durch 10 Liter reinen Wasserdampf ersetzen, um die nachgesaugte Luft zu verdrängen.However, since the sucked-in air mixes with the steam in the cooking chamber, the steam generated by the steam generator and introduced into the cooking chamber must displace a mixture of water vapor and sucked-in air in order to increase the steam content and the temperature in the cooking chamber. As a result, much more steam must be produced than air has been sucked. As an example, it is assumed that at 90% humidity, 1 liter of water vapor condenses in the oven, which is replaced by air. Thereupon the device must Replace 10 liters of steam mixture with 10 liters of pure water vapor to displace the sucked air.

Aus der DE 42 23 653 A1 ist eine Vorrichtung zum Steuern von Gar-, Brat- und Kochvorgängen im Garraum eines Backofens bekannt, wobei eine Steuerschaltung mit einem elektronischen Regler vorgesehen ist, die in Abhängigkeit von gargutspezifischen Eigenschaften und diesen zugeordneten Temperatur-Zeitprofilen sensorgesteuert ein entsprechendes Backofen-Energieniveau einstellt, das mit gargutspezifischen Schwankungsbreiten regelbar ist.From the DE 42 23 653 A1 a device for controlling cooking, roasting and cooking processes in the cooking chamber of a baking oven is known, wherein a control circuit is provided with an electronic controller, the sensor-controlled adjusts a corresponding oven energy level depending on cooking properties and their associated temperature-time profiles with gargutspezifischen fluctuation ranges is adjustable.

Die gattungsbildende WO 2009/065197 A1 offenbart einen gasbetriebenen Backofen für den Privathaushalt, der zusätzlich die Möglichkeit des Dampfgarens vorsieht. Hierbei ist eine Steuerung vorgesehen, die neben weiteren genannten Alternativen einen Zweipunkt-Regler oder einen PID-Regler aufweisen kann.The generic WO 2009/065197 A1 discloses a gas-powered home oven that also provides the option of steaming. In this case, a controller is provided which, in addition to other alternatives mentioned, may have a two-point controller or a PID controller.

Die EP 1 761 111 A2 und die EP 1 724 530 A1 beschreiben ebenfalls Backöfen für den privaten Haushalt mit einem integrierten Dampfgenerator, wobei die Öfen eine zentrale Steuerung aufweisen, die einen PID-Regler oder einen anderen geeigneten Regler umfasst.The EP 1 761 111 A2 and the EP 1 724 530 A1 also describe home-baking ovens with an integrated steam generator, the ovens having centralized control comprising a PID controller or other suitable controller.

Aus der US 2006/0081592 A1 wiederum ist ein Dampfgarer bekannt, der auf natürlicher Konvektion beruht und einen Ablaufbereich mit einem Kondensatabscheider aufweist.From the US 2006/0081592 A1 Again, a steamer is known, which is based on natural convection and has a drainage area with a condensate.

Es ist die Aufgabe der Erfindung, ein Gargerät und ein Verfahren zur Regelung eines Dampfgenerators zu schaffen, mit dem besonders bei hohem Dampfgehalt eine bessere Regelung dahingehend möglich ist, dass das Nachsaugen von Luft weitgehend vermieden ist.It is the object of the invention to provide a cooking appliance and a method for controlling a steam generator, with which, especially at high steam content, a better control is possible to the effect that the intake of air is largely avoided.

Zur Lösung dieser Aufgabe ist erfindungsgemäß ein Gargerät mit den Merkmalen des Anspruchs 1 vorgesehen. Die Erfindung beruht auf dem Grundgedanken, den Dampfgenerator in einem Betriebsbereich, in welchem der Dampfgehalt konstant gehalten werden soll, mit dem Signal des stetigen Reglers anzusteuern. Auf diese Weise wird verhindert, dass der Dampfgenerator so lange ausgeschaltet bleibt, bis Luft nachgesaugt wurde.To achieve this object, a cooking appliance according to the invention with the features of claim 1 is provided. The invention is based on the idea of controlling the steam generator in an operating range in which the steam content is to be kept constant, with the signal of the continuous controller. This prevents the steam generator from being switched off until air has been sucked in.

Gemäß einer bevorzugten Ausführungsform der Erfindung ist vorgesehen, dass der Dampfgenerator mindestens zwei Leistungsstufen aufweist. Gemäß dieser Ausgestaltung wird der Dampfgenerator grundsätzlich weiterhin mit diskreten Leistungsstufen betrieben, die aber in dem Betriebsbereich, in welchem der Dampfgehalt konstant gehalten werden soll, vom stetigen Regler angesteuert werden. Durch die Verwendung von zwei oder mehr Leistungsstufen kann eine optimale Anpassung an den jeweiligen Leistungsbedarf erfolgen.According to a preferred embodiment of the invention it is provided that the steam generator has at least two power levels. According to In this embodiment, the steam generator is in principle further operated with discrete power stages, but in the operating range in which the steam content is to be kept constant, be controlled by the continuous controller. By using two or more power levels, an optimal adaptation to the respective power requirement can be made.

Vorzugsweise ist vorgesehen, dass der stetige Regler den Dampfgenerator mit einer maximalen mittleren Leistung betreibt, die unterhalb der ersten Leistungsstufe liegt. Der Dampfgenerator arbeitet dann mit einer Haltestufe, die wie eine zusätzliche kleinere Heizstufe in den Schwellwertregler integriert werden kann.Preferably, it is provided that the continuous controller operates the steam generator with a maximum average power, which is below the first power level. The steam generator then works with a holding stage, which can be integrated into the threshold controller like an additional smaller heating stage.

Vorzugsweise ist vorgesehen, dass die erste Leistungsstufe im Bereich von etwa 25 % bis etwa 50 % der zweiten, maximalen Leistungsstufe beträgt. Es hat sich herausgestellt, dass mit einer solchen Spreizung der Heizstufen das gewünschte Betriebsverhalten gut abgebildet werden kann. Außerdem ergeben sich diese Leistungsstufen konstruktiv in vorteilhafter Weise. Bei einem elektrisch betriebenen Dampfgenerator kann eine Halbierung der Leistung bei Stern- oder Dreiecksschaltung mit einem Relais bzw. SSR erreicht werden. Bei einem gasbetriebenen Dampfgenerator wird die kleinste Heizstufe dagegen konstruktiv bedingt eher eine Leistung von etwa 25 % der maximalen Leistung haben, auch wenn noch geringere Leistungen vorteilhaft sein könnten.It is preferably provided that the first power level is in the range of about 25% to about 50% of the second, maximum power level. It has been found that with such a spreading of the heating stages, the desired performance can be well represented. In addition, these power levels result constructively in an advantageous manner. In an electrically operated steam generator halving the power in star or delta connection can be achieved with a relay or SSR. In the case of a gas-driven steam generator, on the other hand, the smallest heating level will have a capacity of approximately 25% of the maximum power, even if lower powers could be advantageous.

Vorzugsweise ist dabei vorgesehen, dass der stetige Regler den Dampfgenerator mit einer Leistung betreibt, die etwa 75 % der Leistung der ersten Leistungsstufe beträgt. Anders ausgedrückt arbeitet der Dampfgenerator (unter der Annahme einer Leistung in der ersten Heizstufe von 50% der Maximalleistung) in der Haltestufe mit einer Leistung von 37,5 % der maximalen Heizleistung, was sich als vorteilhaft herausgestellt hat, um einen konstanten Dampfgehalt im Garraum aufrechtzuerhalten.Preferably, it is provided that the continuous controller operates the steam generator with a power that is about 75% of the power of the first power level. In other words, assuming a power in the first heating stage of 50% of the maximum power) in the holding stage, the steam generator operates at a power of 37.5% of the maximum heating power, which has proved to be advantageous for maintaining a constant steam content in the cooking space ,

Gemäß der bevorzugten Ausführungsform ist vorgesehen, dass der stetige Regler als Steuergröße eine Puffervariable ausgibt, anhand derer die Steuerung den Dampfgenerator pulsweitenmoduliert betreibt. Auf diese Weise können die Vorteile eines stetigen Reglers genutzt werden, ohne dass ein stufenlos regelbarer Dampfgenerator genutzt werden muss.According to the preferred embodiment, it is provided that the continuous controller outputs as a control variable a buffer variable, by means of which the controller operates the steam generator in pulse width modulation. In this way, the advantages of a continuous controller can be used without having to use a continuously variable steam generator.

Vorzugsweise ist vorgesehen, dass der Garraum mit einem Ablaufbereich in Strömungsverbindung steht, wobei im Ablaufbereich ein Dampfpuffer gebildet ist, dessen Volumen mindestens gleich dem Dampfvolumen ist, das zwischen zwei Heizpulsen im Garraum kondensiert. Diese Ausgestaltung berücksichtigt, dass aufgrund von zulassungsrechtlichen Vorgaben in einigen Ländern die Häufigkeit der erlaubten Schaltvorgänge je Zeiteinheit begrenzt ist. Dies führt dazu, dass beim Betrieb des Dampfgenerators in der Haltestufe gewisse Wartezeiten eingehalten werden müssen, bevor nach dem Ausschalten des Dampfgenerators dieser wieder eingeschaltet werden darf. Dadurch lässt sich nicht verhindern, dass während der Wartezeit eine gewisse Dampfmenge kondensiert, deren Volumen durch nachgesaugtes Gas ausgeglichen werden muss. Die Verwendung eines Dampfpuffers im Ablaufbereich gewährleistet, dass keine Luft nachgesaugt wird, sondern Dampf.It is preferably provided that the cooking chamber is in flow communication with a drain region, wherein in the drain region, a steam buffer is formed whose volume is at least equal to the vapor volume condensed between two heating pulses in the cooking chamber. This embodiment takes into account that due to regulatory requirements in some countries, the frequency of the permitted switching operations per unit time is limited. As a result, certain waiting times must be maintained during operation of the steam generator in the holding stage, before it can be switched on again after switching off the steam generator. This does not prevent a certain amount of steam from condensing during the waiting period, the volume of which must be compensated for by sucked gas. The use of a steam buffer in the discharge area ensures that no air is sucked in, but steam.

Gemäß der bevorzugten Ausführungsform ist vorgesehen, dass der stetige Regler ein PI-Regler ist. Ein solcher Regler ist ausreichend, um den einzuhaltenden Sollwert (Temperatur oder Feuchte) im Garraum während der Haltephase aufrechtzuerhalten. Auf einen aufwendigeren PID-Regler kann verzichtet werden.According to the preferred embodiment, it is provided that the continuous controller is a PI controller. Such a controller is sufficient to maintain the setpoint (temperature or humidity) to be maintained in the cooking chamber during the holding phase. A more elaborate PID controller can be dispensed with.

Erfindungsgemäß ist zur Lösung der oben genannten Aufgabe auch ein Verfahren zur Regelung eines Dampfgenerators für ein Gargerät mit den Merkmalen des Anspruchs 10 vorgesehen. Dieses Verfahren kombiniert den Vorteil eines robusten Schwellwertreglers mit dem Vorteil der präziseren Regelung mittels eines stetigen Reglers.According to the invention, a method for controlling a steam generator for a cooking appliance with the features of claim 10 is provided to solve the above object. This method combines the advantage of a robust threshold controller with the advantage of more precise control by means of a continuous regulator.

Der Schwellwertregler steuert den Dampfgenerator, bis der zu regelnde Istwert im Garraum mindestens 90 % des Sollwertes beträgt. Es vereinfacht die Auslegung des stetigen Reglers, wenn dieser lediglich die Regelung in der Nähe des Sollwertes übernehmen muss und die Annäherung an den Sollwert vom robusten Schwellwertregler übernommen wird.The threshold controller controls the steam generator until the actual value to be controlled in the cooking chamber is at least 90% of the setpoint. It simplifies the design of the continuous controller if it only has to take over control in the vicinity of the setpoint and the approach to the setpoint is taken over by the robust threshold controller.

Gemäß einer Ausführungsvariante ist vorgesehen, dass der stetige Regler den Dampfgenerator stufenlos regelt. Auf diese Weise kann die Regelgüte erhöht und der Energieverbrauch verringert werden.According to one embodiment, it is provided that the continuous controller continuously regulates the steam generator. In this way, the quality of control can be increased and the energy consumption can be reduced.

Die Erfindung wird nachfolgend anhand einer Ausführungsform beschrieben, die in den beigefügten Zeichnungen dargestellt ist. In diesen zeigen:

  • Figur 1 schematisch ein erfindungsgemäßes Gargerät;
  • Figur 2 ein Diagramm zur Erläuterung des erfindungsgemäßen Verfahrens;
  • Figur 3 schematisch in vergrößertem Maßstab den mit III in Figur 1 gekennzeichneten Ablaufbereich; und
  • Figur 4 eine alternative Ausgestaltung zum in Figur 3 gezeigten Ablaufbereich.
The invention will be described below with reference to an embodiment shown in the accompanying drawings. In these show:
  • FIG. 1 schematically a cooking appliance according to the invention;
  • FIG. 2 a diagram for explaining the method according to the invention;
  • FIG. 3 schematically on an enlarged scale that with III in FIG. 1 marked drain area; and
  • FIG. 4 an alternative embodiment to in FIG. 3 shown drain area.

In Figur 1 ist schematisch ein Gargerät 10 gezeigt, das für Großküchen vorgesehen ist und als Kombi-Dämpfer bekannt ist. Es enthält einen Garraum 12, in den zu garende Produkte eingebracht werden können. Es ist ein Dampfgenerator 14 vorgesehen, der Wasserdampf erzeugen kann, welcher in das Innere des Garraums 12 geleitet werden kann. Das Gargerät 10 weist natürlich auch eine Heizung auf, um erwärmte Luft in den Garraum einzubringen. Da diese Heizung im Rahmen der vorliegenden Anmeldung jedoch ohne Bedeutung ist, ist sie hier der besseren Übersichtlichkeit halber nicht dargestellt.In FIG. 1 schematically a cooking appliance 10 is shown, which is intended for commercial kitchens and is known as a combination damper. It contains a cooking chamber 12 into which products to be cooked can be introduced. It is a steam generator 14 is provided which can generate water vapor, which can be passed into the interior of the cooking chamber 12. Of course, the cooking appliance 10 also has a heater in order to introduce heated air into the cooking chamber. However, since this heater in the context of the present application without meaning, it is not shown here for the sake of clarity.

Weiterhin ist eine Steuerung 16 vorgesehen, die als Eingangssignale unter anderem ein Signal von einem Temperatur- und/oder Feuchtesensor 18 erhält, der im Inneren des Garraums 12 angeordnet ist, sowie von einer Bedieneinheit 20. Über die Bedieneinheit 20 kann ein Bediener verschiedene Garbedingungen im Inneren des Garraums oder komplexere Garprogramme vorwählen.Furthermore, a controller 16 is provided, which receives as input signals, inter alia, a signal from a temperature and / or humidity sensor 18, which is arranged in the interior of the cooking chamber 12, and by an operating unit 20. About the operating unit 20, an operator can different cooking conditions in Inside the cooking chamber or select more complex cooking programs.

Die Steuerung 16 enthält einen Schwellwertregler 22 sowie einen stetigen Regler 24, der hier als PI-Regler ausgeführt ist. Von der Steuerung 16 wird unter anderem der Dampfgenerator 14 angesteuert, indem sie vorgibt, ob der Dampfgenerator ausgeschaltet ist, mit einer ersten Leistungsstufe 14.1 oder einer zweiten Leistungsstufe 14.2 betrieben wird. In der ersten Leistungsstufe 14.1 hat der Dampfgenerator eine Leistung, die etwa 50 % der zweiten, maximalen Leistungsstufe beträgt. Die Leistungsstufen sind hier durch die Steuerung vorgegeben, beispielsweise durch die Verschaltung von drei Heizkörpern in Stern- oder Dreiecksschaltung. In Abhängigkeit von den Anforderungen können auch andere oder mehr Leistungsstufen verwendet werden.The controller 16 includes a threshold controller 22 and a continuous controller 24, which is designed here as a PI controller. Among other things, the controller 16 controls the steam generator 14 by specifying whether the steam generator is switched off, is operated with a first power stage 14.1 or a second power stage 14.2. In the first power stage 14.1, the steam generator has a power that is about 50% of the second, maximum power level. The power levels are specified here by the controller, for example, by the interconnection of three radiators in star or delta connection. Depending on the requirements, other or more power levels may be used.

Unterhalb des Garraums 12 ist ein Ablaufbereich 26 vorgesehen, der kastenartig ausgeführt und mit einer Kondensationseinrichtung 28 versehen ist. Der Ablaufbereich 26 ist mit einem Abluftrohr 30 verbunden. Zwischen dem Anschluß des Abluftrohres 30 und der Verbindung zum Garraum ist ein Trennblech 32 vorgesehen, so dass ein Dampfpuffer 34 zwischen dem Garraum und dem Trennblech gebildet ist.Below the cooking chamber 12, a drain region 26 is provided, which is designed like a box and provided with a condensation device 28. Of the Drain area 26 is connected to an exhaust pipe 30. Between the connection of the exhaust pipe 30 and the connection to the cooking chamber, a separating plate 32 is provided, so that a steam buffer 34 is formed between the cooking chamber and the separating plate.

Anhand von Figur 2 wird nun erläutert, wie in der Betriebsart "Dampf" ein möglichst konstanter Temperatur- bzw. Dampfgehalt im Garraum 12 aufrechterhalten wird. Bei diesem Beispiel ist eine Solltemperatur Ts vorgegeben. Das Verfahren arbeitet jedoch in derselben Weise, wenn anstelle der Temperatur eine bestimmte Feuchte im Garraum als Sollwert vorgegeben ist.Based on FIG. 2 will now be explained how in the operating mode "steam" as constant as possible temperature or steam content in the cooking chamber 12 is maintained. In this example, a target temperature T s is given. However, the method works in the same way, if instead of the temperature of a certain humidity in the oven is specified as the setpoint.

Zu Beginn des Verfahrens befindet sich die Isttemperatur TI im Garraum deutlich unterhalb der Solltemperatur TS, die hier rund 95 °C beträgt. Daher verwendet die Steuerung 16 für die Ansteuerung des Dampfgenerators ausschließlich den Schwellwertregler 22. Dieser betreibt den Dampfgenerator 14 in der zweiten Heizstufe 14.2, also mit einer Leistung von 100 % (siehe die Leistungskurve P im Diagramm). Nachdem knapp 200 Sekunden verstrichen sind, überschreitet die Temperatur TI im Garraum 12 den Schwellwert, bei dessen Überschreiten der Dampfgenerator 14 auf die erste Heizstufe 14.1 zurückgeschaltet wird; die Leistungskurve P sinkt also auf einen Wert von 50 % ab.At the beginning of the process, the actual temperature T I in the cooking chamber is significantly below the setpoint temperature T S , which is around 95 ° C here. Therefore, the controller 16 uses only the threshold controller 22 for the control of the steam generator. This operates the steam generator 14 in the second heating stage 14.2, ie with a power of 100% (see the power curve P in the diagram). After almost 200 seconds have elapsed, exceeds the temperature T I in the cooking chamber 12, the threshold above which the steam generator 14 is switched back to the first heating stage 14.1; the power curve P thus drops to a value of 50%.

Nachdem rund 230 Sekunden verstrichen sind, hat sich die Isttemperatur TI so weit an die Solltemperatur TS angenähert, dass die Steuerung 16 vom Schwellwertregler 22 auf den PI-Regler 24 umschaltet und diesen für die Ansteuerung des Dampfgenerators 14 verwendet. Dementsprechend steigt der Wert für die Sollleistung HSS des Dampfgenerators in der Haltestufe auf einen vorgegebenen Wert von 75 % der Leistung der ersten Heizstufe (siehe Kurve HSS). Dieser Wert HSS wird von der Steuerung 16 als Puffervariable behandelt, anhand derer der Dampfgenerator 14 nun mit der ersten Heizstufe 14.1 pulsweitenmoduliert betrieben wird. Da die maximale Leistung des Dampfgenerators hier vorgegeben ist mit 75 % der Leistung der ersten Heizstufe 14.1, schaltet also die Steuerung 16 die erste Heizstufe 14.1 des Dampfgenerators 14 innerhalb eines gegebenen Zeitintervalls für 75 % der Zeit ein und für 25 % der Zeit aus, wenn der Dampfgenerator in der Haltestufe mit maximaler Leistung betrieben werden soll. Dies ist hier der Fall, solange der Sollwert HS für die Haltestufe auf dem Wert von 75 % verbleibt, also bis knapp 250 Sekunden. Zu diesem Zeitpunkt beginnt der PI-Regler 24 zu regeln, wie an den schwankenden Werten für den Sollwert HSS der Haltestufe zu sehen ist.After about 230 seconds have elapsed, the actual temperature T I has approached the setpoint temperature T S so far that the controller 16 switches from the threshold value controller 22 to the PI controller 24 and uses this to control the steam generator 14. Accordingly, the value for the setpoint power HS S of the steam generator in the holding stage increases to a predetermined value of 75% of the power of the first heating stage (see curve HS S ). This value HS S is treated by the controller 16 as a buffer variable, based on which the steam generator 14 is now operated with the first heating stage 14.1 pulse width modulated. Since the maximum power of the steam generator is set here with 75% of the power of the first heating stage 14.1, the controller 16 switches on the first heating stage 14.1 of the steam generator 14 within a given time interval for 75% of the time and for 25% of the time, if the steam generator should be operated in the holding stage with maximum power. This is the case here as long as the setpoint H S for the holding stage remains at the value of 75%, that is to say just under 250 seconds. At this time The PI controller 24 begins to regulate, as can be seen from the fluctuating values for the setpoint HS S of the holding stage.

Auf diese Weise kann ein stetiger Regler in Kombination mit einem Dampfgenerator, der zwischen zwei diskreten Leistungsstufen geschaltet wird, dazu verwendet werden, den Dampfgehalt im Garraum vergleichsweise konstant zu halten. Am annäherungsweise konstanten Wert für den Integralanteil PI des PI-Reglers ist zu erkennen, dass der Regler nach etwa 400 Sekunden einen stabilen Zustand erreicht.In this way, a continuous regulator in combination with a steam generator, which is switched between two discrete power levels, can be used to keep the steam content in the cooking chamber comparatively constant. At approximately constant value for the integral portion I P of the PI controller will be appreciated that the controller reaches a steady state after about 400 seconds.

Grundsätzlich kann die jeweils vom PI-Regler 24 vorgegebene Leistung für den Betrieb des Dampfgenerators 14 in der Haltestufe durch eine Vielzahl von sehr kurzen Heizpulsen dargestellt werden, zwischen denen entsprechend kurze Ausschaltzeiten verwendet werden. Bei elektrisch betriebenen Dampfgeneratoren könnte durch Ein- und Ausschalten einzelner Halbwellen der Netzfrequenz die Heizleistung quasi stufenlos eingestellt werden. Auf diese Weise kommt man einer tatsächlich stufenlosen Regelung der Leistung sehr nahe, die hinsichtlich der Regelgüte und des Energieverbrauchs vorteilhaft wäre.In principle, the power given by the PI controller 24 for the operation of the steam generator 14 in the holding stage can be represented by a multiplicity of very short heating pulses, between which correspondingly short switch-off times are used. In electrically operated steam generators could be adjusted quasi-continuous by switching on and off of individual half-waves of the mains frequency, the heating power. In this way one comes very close to an actually stepless control of the power, which would be advantageous in terms of control quality and energy consumption.

Sowohl aus praktischen als auch aus zulassungsrechtlichen Gründen ist es jedoch nicht in allen Ländern möglich, die Ausschaltzeit zwischen zwei aufeinanderfolgenden Heizpulsen beliebig kurz zu wählen. Die Ausschaltzeit oder Wartezeit zwischen zwei aufeinanderfolgenden Heizpulsen führt daher dazu, dass im Garraum Dampf kondensiert. Das entsprechende Dampfvolumen muss in den Garraum nachgesaugt werden.However, for both practical and regulatory reasons, it is not possible in all countries to choose the switch-off time between two consecutive heating pulses as short as desired. The switch-off time or waiting time between two successive heating pulses therefore leads to steam condensing in the cooking chamber. The corresponding volume of steam must be sucked into the oven.

In Figur 3 ist eine Ausführungsform gezeigt, die sich durch einen größeren Dampfpuffer 34 auszeichnet. Dieser ist dadurch gebildet, dass das Trennblech 32 näher am Abluftrohr 30 angeordnet ist. Die Funktion des Trennblechs 32 besteht darin, ein Vermischen des Dampfs mit der Luft im Ablaufbereich 26 weitestgehend zu verhindern. Das Volumen des mit dem Trennblech 32 definierten Dampfpuffers 34 ist mindestens so groß wie das Dampfvolumen, das zwischen zwei Heizpulsen im Garraum 12 kondensieren kann. Dies gewährleistet, dass zwischen zwei Heizpulsen nicht Luft nachgesaugt wird, sondern Dampf aus dem Dampfpuffer 34 (siehe den Pfeil D). Mindestens zwischen zwei Heizpulsen muss dementsprechend auch die Kondensationseinrichtung 28 abgeschaltet sein, damit im Dampfpuffer 34 auch tatsächlich Dampf vorgehalten werden kann.In FIG. 3 an embodiment is shown, which is characterized by a larger steam buffer 34. This is formed by the fact that the separating plate 32 is arranged closer to the exhaust pipe 30. The function of the separating plate 32 is to prevent a mixing of the steam with the air in the discharge region 26 as far as possible. The volume of the vapor buffer 34 defined with the separating plate 32 is at least as great as the vapor volume which can condense between two heating pulses in the cooking chamber 12. This ensures that air is not sucked in between two heating pulses, but steam from the steam buffer 34 (see the arrow D). Accordingly, the condensation device 28 must also be switched off at least between two heating pulses, so that steam can actually be stored in the vapor buffer 34.

In Figur 4 ist eine alternative Ausgestaltung gezeigt. Bei dieser werden Strömungsleitbleche 36 verwendet, die sich in Längsrichtung des Ablaufs erstrecken. Der Ablauf kann dabei entweder einen kreisförmigen Querschnitt (siehe Detail D1) oder einen kastenförmigen Querschnitt haben (siehe Detail D2). Die Strömungsleitbleche 36 wirken als Wirbelbrecher, die ähnlich wie das Trennblech 32 verhindern, dass sich die Luft im Ablaufbereich 26 mit dem dort vorhandenen Dampf vermischt. Somit kann möglichst reiner Dampf in den Phasen zwischen zwei Heizpulsen in den Garraum zurückgesaugt werden. Durch die Ausrichtung der Strömungsleitbleche 36 in Richtung des Ablaufkanals wird die Strömung in Längsrichtung kaum beeinträchtigt, in einer Richtung quer dazu dagegen stark unterdrückt.In FIG. 4 an alternative embodiment is shown. In this flow guide plates 36 are used, which extend in the longitudinal direction of the drain. The process can either have a circular cross section (see detail D1) or a box-shaped cross section (see detail D2). The Strömungsleitbleche 36 act as a vortex breaker, similar to the separating plate 32 prevent the air in the drain region 26 mixed with the existing steam there. Thus, as pure as possible vapor can be sucked back into the cooking space in the phases between two heating pulses. Due to the orientation of the flow guide plates 36 in the direction of the drainage channel, the flow in the longitudinal direction is hardly affected, but strongly suppressed in a direction transverse thereto.

Gemäß einer Ausführungsvariante können die Strömungsleitbleche, die sich in Strömungsrichtung erstrecken, alle auf der Oberseite des Ablaufs angebracht werden. Dies erleichtert, Verschmutzungen auszuspülen, damit sich keine Verunreinigungen an den Blechen ansammeln können.According to one embodiment, the flow baffles extending in the flow direction can all be mounted on the top of the drain. This makes it easier to rinse out soiling, so that no impurities can accumulate on the sheets.

BezugszeichenlisteLIST OF REFERENCE NUMBERS

10:10:
GargerätCooking appliance
12:12:
Garraumoven
14:14:
Dampfgeneratorsteam generator
14.1:14.1:
erste Heizstufefirst heating stage
14.2:14.2:
zweite Heizstufesecond heating stage
16:16:
Steuerungcontrol
18:18:
Sensorsensor
20:20:
Bedieneinheitoperating unit
22:22:
Schwellwertreglerthreshold value controller
24:24:
PI-ReglerPI controller
26:26:
Ablaufbereichdrainage area
28:28:
Kondensationseinrichtungcondensation device
30:30:
Abluftrohrexhaust pipe
32:32:
TrennblechDivider
34:34:
Dampfpuffersteam buffer
36:36:
Strömungsleitblechflow baffle

Claims (12)

  1. A cooking device (10) comprising a cooking chamber (12), a steam generator (14), and a control unit (16) which drives the steam generator (14), the control unit (16) including a threshold controller (22), characterized in that the control unit (16) additionally includes a continuous controller (24),
    wherein in an approximation phase in which an actual value to be closed-loop controlled in a cooking chamber (12) of the cooking device (10) approximates a desired value, the steam generator (14) is controlled by the threshold controller (22) until the actual value to be closed-loop controlled in the cooking chamber (12) amounts to at least 90% of the desired value, and
    in an operating range which corresponds to a holding phase which follows the approximation phase and in which the steam content is to be kept constant, the steam generator (14) is driven with the signal of the continuous controller (24).
  2. The cooking device (10) according to claim 1, characterized in that the steam generator (14) has at least two power stages (14.1, 14.2).
  3. The cooking device according to claim 2, characterized in that the continuous controller (24) operates the steam generator (14) at a power that is below the first power stage (14.1).
  4. The cooking device according to claim 2 or claim 3, characterized in that the first power stage (14.1) amounts to about 50% of the second, maximum power stage (14.2).
  5. The cooking device according to claim 4, characterized in that the continuous controller (24) operates the steam generator (14) at a power that amounts to about 75% of the power of the first power stage (14.1).
  6. The cooking device according to any of the preceding claims, characterized in that the continuous controller (24) outputs a buffer variable (HSs) as a controlled variable based on which the controller (16) operates the steam generator (14) using pulse width modulation.
  7. The cooking device according to claim 6, characterized in that the cooking chamber (12) is in fluid communication with a drainage region (26), the drainage region (26) having a steam buffer (34) formed therein the volume of which is at least equal to the steam volume that condenses in the cooking chamber (12) between two heating pulses.
  8. The cooking device according to claim 6 or claim 7, characterized in that at least one separating plate (32) and/or one flow baffle plate (36) is/are provided in the drainage region.
  9. The cooking device according to any of the preceding claims, characterized in that the continuous controller is a PI controller (24).
  10. A method for closed-loop controlling a steam generator (14) of a cooking device (10) according to any of the preceding claims, characterized in that in an approximation phase in which an actual value to be closed-loop controlled in a cooking chamber (12) of the cooking device (10) approximates a desired value, the steam generator (14) is controlled by a threshold controller (22) until the actual value to be closed-loop controlled in the cooking chamber (12) amounts to at least 90% of the desired value and, in a subsequent holding phase in which the actual value is near the desired value, the steam generator (14) is controlled by a continuous controller (24).
  11. The method according to claim 10, characterized in that the continuous controller (24) controls the steam generator (14) in a continuously variable manner.
  12. The method according to claim 11, characterized in that the steam generator (14) is electrically operated and the output of the steam generator (14) is closed-loop controlled by switching individual half-waves of the mains frequency on and off.
EP11007208.9A 2010-09-13 2011-09-06 Cooking device with steam generator and method for regulating a steam generator for a cooking device Active EP2428735B1 (en)

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DE102010045198A DE102010045198A1 (en) 2010-09-13 2010-09-13 Cooking appliance with steam generator and method for controlling a steam generator for a cooking appliance

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EP2428735A2 EP2428735A2 (en) 2012-03-14
EP2428735A3 EP2428735A3 (en) 2014-07-02
EP2428735B1 true EP2428735B1 (en) 2018-11-07

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DE102012112810A1 (en) * 2012-12-20 2014-06-26 Miele & Cie. Kg Cooking appliance and method for operating a cooking appliance

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DE1902063A1 (en) * 1969-01-16 1970-08-13 Philips Patentverwaltung Gmbh, 2000 Hamburg Controlling oil or gas fired furnaces over - wide feed-ranges
DE2608295C2 (en) * 1976-02-28 1982-11-18 Brown, Boveri & Cie Ag, 6800 Mannheim Electronic temperature controller for regulating the energy supply for an electrical heating element
CH656204A5 (en) * 1982-03-16 1986-06-13 Schoenmann Wilfred Ernst STEAM BOILER WITH ELECTRIC RESISTANT HEATING.
DE4223653C2 (en) * 1992-07-17 2003-12-11 Bsh Bosch Siemens Hausgeraete Process for regulating cooking processes and associated oven
DE4341410A1 (en) * 1993-12-04 1995-06-08 Licentia Gmbh Baking and roasting oven with a cooking space and a steam generator for the cooking space
DE10015747A1 (en) * 2000-03-29 2001-10-04 Bsh Bosch Siemens Hausgeraete Steam cooker has arrangement that forms temperature demand value for evaporating water by heater corresponding to air pressure at altitude entered into regulator via input device
US7049551B2 (en) * 2004-09-30 2006-05-23 Middleby Marshall, Inc. Natural convection steam cooking device
US20060249137A1 (en) * 2005-05-03 2006-11-09 Malcolm Reay System and method for draining water from a steam oven
US20070062927A1 (en) * 2005-09-06 2007-03-22 Sells Joel M Steam generator system for a household oven
BRPI0705924A2 (en) * 2007-11-23 2009-07-21 Whirlpool Sa gas oven for steam cooking and stove
DE102008056324B4 (en) * 2008-11-07 2016-07-07 Rational Ag Method for refilling a steam generator with water, steam generator therefor and cooking appliance therewith

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DE102010045198A1 (en) 2012-03-15
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