EP3896339B1 - Procédé d'ajustement d'une commande d'un appareil de chauffage - Google Patents

Procédé d'ajustement d'une commande d'un appareil de chauffage Download PDF

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Publication number
EP3896339B1
EP3896339B1 EP21168555.7A EP21168555A EP3896339B1 EP 3896339 B1 EP3896339 B1 EP 3896339B1 EP 21168555 A EP21168555 A EP 21168555A EP 3896339 B1 EP3896339 B1 EP 3896339B1
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EP
European Patent Office
Prior art keywords
heater
burner
fuel
heating
determined
Prior art date
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Active
Application number
EP21168555.7A
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German (de)
English (en)
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EP3896339C0 (fr
EP3896339A1 (fr
Inventor
Klaus Richter
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Vaillant GmbH
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Vaillant GmbH
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Publication of EP3896339A1 publication Critical patent/EP3896339A1/fr
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Publication of EP3896339B1 publication Critical patent/EP3896339B1/fr
Publication of EP3896339C0 publication Critical patent/EP3896339C0/fr
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N5/00Systems for controlling combustion
    • F23N5/02Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium
    • F23N5/10Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using thermocouples
    • F23N5/102Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using thermocouples using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N3/00Regulating air supply or draught
    • F23N3/002Regulating air supply or draught using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2233/00Ventilators
    • F23N2233/06Ventilators at the air intake
    • F23N2233/08Ventilators at the air intake with variable speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2241/00Applications
    • F23N2241/04Heating water

Definitions

  • the invention relates to a method for adapting a control system for a heater. Also specified are a computer program, a machine-readable storage medium, a control device for a heater and a heater, each of which is provided and set up to carry out the method.
  • the method can be used in particular to compensate for the influences of different exhaust systems on the device performance or heating performance of a heater.
  • Heating devices which each have a conveying device for conveying a fuel-air mixture and a burner for burning the fuel-air mixture.
  • the heat generated by the burner can then be transferred to a liquid circuit of a building in order to heat the building or at least part of it.
  • the heating device and the liquid circuit usually form a heating system for heating the building or part of it.
  • the heat energy emitted by the burner per unit of time is usually referred to as heating output, device output or, if applicable, also generally as the output of the heating device.
  • the heating output of corresponding heating devices is usually only controlled via the drive power of the conveying device. For this purpose, a certain (target) drive power of the conveying device is permanently assigned to a certain (target) heating output.
  • the volume flow of the mixture conveyed by the conveying device does not only depend on the drive power of the conveying device. Rather, it has been found that the pressure losses in the supply air systems and/or in the exhaust systems to which the heaters are usually connected can have a significant influence on the volume flow of the mixture and thus the heating output. In this context, it has been shown in particular that differences in pressure losses that can result from different designs of supply air systems and/or exhaust systems and/or from different ambient conditions can have a significant and therefore considerable influence on the heating output.
  • the pressure loss caused by the exhaust system can, for example, depend significantly on the position of the respective heater on the exhaust system.
  • an unwanted reduction in the burner's output can occur due to comparatively high pressure losses in the exhaust system.
  • a water heating system uses a heated liquid storage tank to ensure a continuous supply of water heated to a desired temperature.
  • a controller varies the speed of a combustion air fan depending on the measured ambient pressure.
  • the object of the invention to provide a method by means of which the problems described in connection with the prior art can be at least partially solved.
  • the method should make it possible to at least partially take into account or compensate for the influences of various supply air systems, exhaust systems and/or ambient conditions on the heating output of a heater.
  • steps a) to c) can be carried out at least once in the order given. Furthermore, steps a) to c) are also repeated (multiple times) or steps a) to c) repeatedly (in the form of a loop) begin with step a). At least parts of steps a) to c), in particular steps a) and b), can be carried out at least partially in parallel or simultaneously.
  • the method can be carried out, for example, during a (first) start-up of the heater in the building, in particular after the heater has been installed in the building.
  • an initial value for the drive power can be stored in the heater control system to determine the initial drive power.
  • the method can be carried out, for example, when the heater is started up several times or even every time, in order to be able to adapt the heater control system to changing environmental conditions, for example.
  • the stored initial value for the drive power or a value for the drive power adjusted in a previous execution of the method to achieve the predefined target heating power can be used to determine the initial drive power.
  • the method advantageously enables performance control to be carried out by means of energy measurement.
  • the performance control can in particular contribute to balancing the influences of various air supply systems and/or exhaust systems and/or ambient conditions (such as ambient temperatures and/or ambient pressures) on the device performance or heating output of a heater.
  • the method (therefore) advantageously enables the influences of various air supply systems, exhaust systems and/or ambient conditions on the heating output of a heater to be at least partially taken into account or even at least partially balanced.
  • the heating device is usually a heating device for a building.
  • the fuel can be, for example, a fossil fuel, such as (liquid and/or natural) gas or (natural) oil.
  • the liquid circuit can be, for example, a water circuit.
  • One or more radiators can be connected to the liquid circuit to heat the building or part of it.
  • a heat exchanger can be provided to transfer heat from the burner to the liquid circuit. This heat exchanger can be arranged between the burner and the liquid circuit.
  • the heat exchanger can be assigned to the burner or formed within the heating device and/or in the area of the burner.
  • the control can be implemented, for example, by means of a control device of the heating device.
  • the control such as a (computer) program for controlling the heating device, can be implemented in the control device.
  • the heating device can preferably be a gas heating device.
  • this particularly relates to a heating device which is designed to burn one or more (gaseous) fossil fuels such as liquid gas and/or natural gas, possibly with the supply of ambient air from a building or the surrounding area, in order to generate energy for heating a water circuit for heating the building or part thereof.
  • the heating device can be a so-called gas condensing boiler.
  • the heating device generally has at least one burner and at least one conveying device, such as a fan, which can convey a mixture of fuel (gas) and combustion air (through a mixture channel of the heating device) to the burner.
  • Exhaust gases resulting from combustion can be discharged through an (internal) exhaust pipe of the heater to a (possibly shared or multiple) Exhaust system (of the building).
  • Several heaters can be connected to this (common or multiple-use) exhaust system.
  • Exhaust gases produced by combustion can (thus) be discharged from the burner, for example, via an exhaust system.
  • the exhaust system can comprise an exhaust pipe (internal to the heater) and at least part of an exhaust system (external to the heater) (of the building).
  • the exhaust system can discharge into the environment around the building via at least one chimney.
  • the heater can be connected to various exhaust systems.
  • An exhaust path extending from the heater to the environment can thus be different (exhaust system-specific), in particular differently dimensioned, for example of different lengths.
  • the influences of various exhaust systems and/or exhaust paths on the device performance or heating performance of the heater can be advantageously taken into account and/or balanced out as far as possible.
  • Air that can be used for combustion can, for example, be supplied to a mixing point for mixing fuel and air to form the fuel-air mixture (and thus to the burner) via a supply air system.
  • the mixing point is usually formed in the heater and can usually be connected to the burner via a mixture channel.
  • the supply air system can comprise a supply air pipe (internal to the heater) (which opens at the mixing point) and at least part of a supply air system (external to the heater) (of the building).
  • the supply air system can, for example, open into the environment around the building via at least one intake pipe.
  • the heater can be connected to various supply air systems.
  • a supply air path extending from the heater to the environment can be different (depending on the supply air system), in particular different dimensions, for example different lengths.
  • the method described here can be used to take into account the influences of various The effects of supply air systems and/or supply air routes on the device performance or heating output of the heater should be taken into account in an advantageous manner and/or balanced out as far as possible.
  • the supply air can be mixed with fuel in a predeterminable and/or as constant as possible mixing ratio.
  • the mixing ratio can, for example, be fixed or adjustable (manually or by an installer or skilled tradesman). After the mixing ratio has been set, it is usually kept as constant as possible (until it is adjusted again if necessary). A deviation in the delivery volume of the delivery device therefore usually (in particular pneumatically and/or electronically) also has an (immediate) effect on the amount of fuel supplied and thus the heating output.
  • the mixing ratio can be adjusted and/or kept as constant as possible via a so-called fuel-air connection of the heater, in particular by means of a gas valve on the heater.
  • the building can generally be a residential building and/or a commercial building.
  • the heating device can be used in particular to heat only a part of the building, such as a single apartment and/or a single room. Alternatively or cumulatively, the heating device can also be used to heat a water system (e.g. heating water circuit) of the building or an apartment.
  • a water system e.g. heating water circuit
  • the heating device is operated with a specific, initial drive power of the conveyor device.
  • the operation of the heating device comprises in particular operating the burner and/or heating at least part of the liquid circuit, while the conveyor device is operated with the initial drive power, such as a specific electrical drive power of a motor of the Conveying device and/or a specific motor speed of the conveying device.
  • the initial drive power such as a specific electrical drive power of a motor of the Conveying device and/or a specific motor speed of the conveying device.
  • at least one initial value for the drive power to determine the initial drive power can be stored in the control system of the heater.
  • the initial value can, for example, be permanently stored (for example, permanently programmed) or can be adjusted or specified manually and/or automatically.
  • the initial value can be adjusted or specified by an installer or skilled tradesman or a user of the heater (if required).
  • the initial value for the drive power to determine the initial drive power can, for example, be selected such that the target heating output can be achieved as expected (for example, based on experience with a reference exhaust system, a reference air supply system and/or reference ambient conditions). Furthermore, the initial value can, for example, be adjusted or specified automatically, for example by the control system itself, for example depending on a value for the drive power adjusted in a previous execution of the method to achieve the predefined target heating output.
  • an actual heating power of the heater is determined, which is delivered to the liquid circuit at the initial drive power of the conveyor.
  • the heating power is determined that is introduced into the liquid circuit by the heater while the conveyor is operated with the initial drive power.
  • the determination can be made, for example, via a (sensory) energy measurement.
  • the heat output from the burner and/or the heat input into the liquid circuit can be measured (sensory). If this energy(s) is considered in relation to a unit of time, the actual heating power can be determined or calculated from this, for example.
  • a sensor assigned to the burner and/or a sensor assigned to the liquid circuit can be used.
  • the sensors can be For example, temperature sensors and/or flow sensors can be used. Alternatively or cumulatively, the burner output or the heat output that is emitted by the burner can also be determined as the actual heat output.
  • the control of the heater is adjusted depending on the determined actual heating output and a predefined target heating output.
  • the predefined target heating output is in particular the heating output that is to be achieved with the initial drive power of the conveyor.
  • the predefined target heating output can describe a specific operating point of the heater and/or a heating system (comprising the heater and the liquid circuit).
  • the operating point can be, for example, a maximum operating point or full load point.
  • at least one specific value for defining the predefined target heating output can be stored in the control of the heater.
  • the specific value can, for example, be permanently stored (for example, permanently programmed) or can be manually adjusted or specified.
  • the specific value can be adjusted or specified by an installer or skilled tradesman or a user of the heater (if necessary).
  • the (actual and/or target) heating output can basically refer to the (thermal) output introduced into the liquid circuit and/or the (thermal) output delivered by the burner. These (thermal) outputs can be converted into one another using a (thermal) efficiency (of the heater or the heat transfer from the burner to the liquid circuit).
  • control can be adjusted and/or adjust itself depending on a comparison between the determined actual heating output and the predefined target heating output.
  • the control can be adjusted depending on be adjusted to any deviation or difference between the determined actual heating output and the predefined target heating output and/or adjust themselves.
  • the drive power of the conveyor and/or a fuel proportion of the fuel-air mixture can be increased if the determined actual heating output is (significantly, for example by more than 5%) below the predefined target heating output. This makes it advantageous to carry out power control by means of energy measurement.
  • a specification for the drive power of the conveyor system stored in the control system is adjusted.
  • the specification can be implemented, for example, in the form of a characteristic curve, a characteristic map, a mathematical function and/or a table (for example a so-called "look-up table").
  • the specification can, for example, assign a specific drive power of the conveyor system to one or more target heating outputs.
  • the specification is adjusted overall in particular so that, for example, all assignments of target heating output to drive power are adjusted simultaneously or in parallel.
  • the specification can, for example, be increased (overall) if the actual heating output determined in step b) is (significantly, for example by more than 5%) below the predefined target heating output.
  • a fan of the conveyor device is operated at a certain initial speed.
  • a fan that can be driven by an electric motor can represent a particularly advantageous embodiment of the conveyor device.
  • the drive power of the conveyor device can, for example, describe the electrical power that is made available to the electric motor of the fan.
  • the speed of the The conveying capacity of the conveying device or the blower can be adjusted.
  • a specification stored in the control system for the speed of the fan of the conveyor device is adjusted.
  • the specification can be implemented, for example, in the form of a characteristic curve, a characteristic map, a mathematical function and/or a table (for example a so-called "look-up table").
  • the specification can, for example, assign a specific speed of the fan to one or more target heating outputs.
  • the specification is adjusted overall, in particular, so that, for example, all assignments of target heating output to speed are adjusted simultaneously or in parallel.
  • the specification can, for example, be increased (overall) if the actual heating output determined in step b) is (significantly, for example by more than 5%) below the predefined target heating output.
  • step b) the actual heating output is determined using sensor data from sensors that are assigned to the liquid circuit.
  • sensors that are assigned to the liquid circuit.
  • two temperature sensors and a flow sensor can be used as sensors, for example. Of the two temperature sensors, one can be assigned to the flow and one to the return of the liquid circuit, for example.
  • the flow sensor can be a mass flow sensor or volume flow sensor, for example.
  • the actual heating output is determined using an efficiency, wherein the efficiency is determined using sensor data from sensors that are assigned to the liquid circuit.
  • the efficiency is determined using sensor data from sensors that are assigned to the liquid circuit.
  • two temperature sensors can be used as sensors. Of the two temperature sensors, one can be assigned to the flow and one to the return of the liquid circuit.
  • the actual heating output determined using the efficiency is in particular an actual burner output (actual thermal output emitted by the burner).
  • the control of the heater can be adjusted depending on the determined actual burner output and a predefined target burner output. In particular, the actual burner output can be compared with a target burner output.
  • an actual burner output is determined using an efficiency, whereby the efficiency is determined using sensor data from sensors that are assigned to the liquid circuit, and that this actual burner output is determined in particular in addition to an actual heating output determined in step b) that is entered into the liquid circuit.
  • the corresponding additional information about the actual burner output can, for example, help to ensure that burner-specific criteria, such as standardization requirements and/or approval requirements, can be checked.
  • a computer program for carrying out a method described here can be specified here.
  • this relates in particular to a computer program (product) comprising instructions which, when the program is executed by a computer, cause the computer to carry out a method described here.
  • the machine-readable storage medium is usually a computer-readable data storage device.
  • a control device for a heating device is also proposed, wherein the control device is provided and set up to carry out a method described here.
  • the control device can be, for example, a control device of the heating device, which is set up to carry out the method.
  • the control device can comprise a processor (controller) that can carry out at least part of the method.
  • the processor can, for example, execute the computer program, for which purpose the processor can access the storage medium.
  • the storage medium can be a component of the control device or can be connected to it.
  • a heating device is also proposed.
  • the heating device has a control device as described here.
  • the heating device or a heating system, comprising the heating device and the liquid circuit can comprise appropriate sensors for carrying out the method, such as two temperature sensors and a flow sensor.
  • Figure 1 shows schematically an exemplary sequence of a method described here for adapting a control of a heating device 1, in which the heating device 1 has a conveying device 2 for conveying a fuel-air mixture and a burner 3 for burning the fuel-air mixture, and wherein heat generated by means of the burner 3 can be transferred to a liquid circuit 14 of a building (cf. Fig.2 ).
  • the sequence of steps a), b) and c) shown in blocks 110, 120 and 130 is exemplary and can be carried out, for example, during a regular operating sequence to carry out the method.
  • step 110 the heater 1 is operated with a specific, initial drive power of the conveyor device 2.
  • step 120 an actual heating power of the heater 1 is determined, which is delivered to the liquid circuit 14 at the initial drive power of the conveyor device 2.
  • step c the control of the heater 1 is adjusted depending on the determined actual heating power and a predefined target heating power.
  • step c) a specification stored in the control system for the drive power of the conveyor device 2 can be adjusted.
  • FIG. 2 shows schematically an exemplary structure of a heater 1 described here.
  • the heater 1 has a control device 7.
  • the Control device 7 is intended and configured to carry out a method described here.
  • a fan of the conveyor device 2 can be operated at a specific, initial speed.
  • a specification stored in the control system for the speed of the fan of the conveyor device 2 can also be adjusted in step c).
  • the actual heating power can be determined using sensor data from sensors 6, 9, 11 that are assigned to the liquid circuit 14.
  • sensors 6, 9, 11 For example, two temperature sensors 6, 11 and a flow sensor 9 can be used for this purpose. Of the two temperature sensors 6, 11, one can be assigned to the flow and one to the return of the liquid circuit.
  • the flow sensor 9 can be a mass flow sensor or volume flow sensor, for example.
  • the actual heating output or additional information about the actual burner output can be determined using an efficiency, wherein the efficiency is determined using sensor data from sensors 6, 11 that are assigned to the liquid circuit 14.
  • the efficiency is determined using sensor data from sensors 6, 11 that are assigned to the liquid circuit 14.
  • sensors 6, 11 can be used for this purpose. Of the two temperature sensors 6, 11, for example, one can be assigned to the flow and one to the return of the liquid circuit.
  • the heating device 1 (for example a gas condensing boiler) is equipped with a burner system in which the fuel, in this case gas, and the combustion air are brought together in front of a conveyor device 2, which is designed, for example, in the form of a fan. This mixture is then transported by the conveyor device 2 or the fan via a mixture channel 12 to the burner 3, where combustion then takes place.
  • a burner system in which the fuel, in this case gas, and the combustion air are brought together in front of a conveyor device 2, which is designed, for example, in the form of a fan. This mixture is then transported by the conveyor device 2 or the fan via a mixture channel 12 to the burner 3, where combustion then takes place.
  • the gas is provided by a gas valve 5 depending on the fan speed.
  • the exhaust gases produced by the combustion are led through an internal exhaust pipe 10 to the exhaust system 15 after they have been cooled down, for example by means of a heat exchanger 13.
  • the energy is transferred by the heat exchanger 13 to a liquid circuit 14, which is formed here as a water circuit, for example.
  • a temperature sensor 6, 11 (for example designed as an NTC) is installed in front of and behind the heat exchanger 13.
  • the temperature sensor 6 forms a flow temperature sensor and the temperature sensor 11 forms a return temperature sensor.
  • a water volume flow or water mass flow sensor 9 is also installed in the water path to or from the heat exchanger 13.
  • the current power that is delivered to the heating system or from the heater 1 to the liquid circuit 14 can be calculated.
  • Q ab denotes the heat energy released
  • m the water mass
  • c pk the specific heat capacity
  • dT the temperature difference between the (flow) temperature sensor 6 and the (return) temperature sensor 11.
  • the expected efficiency can be derived, for example, from the average water temperature in the heat exchanger 13 (T VL -T RL )/2 or only from the flow temperature or return temperature.
  • Corresponding efficiency values can, for example, be determined in advance for the respective heater 1 and stored in the control or control device 7, for example in the form of a characteristic curve.
  • the conveyor device 2 can first be driven with the determined initial drive power and, for example, the fan speed can be set to the value stored in the control system for the desired device output.
  • the actual heating output determined using the procedure described above (which is entered into the liquid circuit 14) can then be compared with the desired value (Q target ). If a control deviation determined in this way is present, the fan speed can then be increased or reduced (accordingly) until the desired output is reached.
  • the burner output determined using the efficiency can be provided as additional information.
  • the method described here can be used to compensate, in an advantageous manner, for different variants or causes of pressure losses in the supply air system and/or the exhaust gas system, in particular caused by different lengths, installations, wind or weather conditions.
  • a method is thus provided by means of which the problems described in connection with the prior art can be at least partially solved.
  • the method can make it possible to at least partially take into account or compensate for the influences of various supply air systems, exhaust systems and/or ambient conditions on the heating output of a heater.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Regulation And Control Of Combustion (AREA)

Claims (12)

  1. Procédé d'ajustement d'une commande d'un appareil de chauffage (1) afin de pouvoir prendre en considération ou compenser au moins partiellement les influences de différents systèmes d'air frais, systèmes de gaz d'échappement et/ou conditions ambiantes sur la puissance de chauffage de l'appareil de chauffage (1), dans lequel l'appareil de chauffage (1) présente un appareil de transport (2) pour le transport d'un mélange combustible-air et un brûleur (3) pour la combustion du mélange combustible-air, et dans lequel de la chaleur générée au moyen du brûleur (3) peut être transmise dans un circuit de fluide (14) d'un bâtiment,
    comprenant au moins les étapes suivantes :
    a) le fonctionnement de l'appareil de chauffage (1) avec une puissance d'entraînement initiale déterminée du dispositif de transport (2),
    b) la détermination d'une puissance de chauffage réelle de l'appareil de chauffage (1) qui est émise pour la puissance d'entraînement initiale du dispositif de transport (2) au niveau du circuit de fluide (14) du bâtiment,
    c) l'ajustement de la commande de l'appareil de chauffage (1) en fonction de la puissance de chauffage réelle déterminée et d'une puissance de chauffage de consigne prédéfinie.
  2. Procédé selon la revendication 1, dans lequel le procédé est mis en oeuvre pendant une première mise en service de l'appareil de chauffage dans le bâtiment.
  3. Procédé selon la revendication 1 ou 2, dans lequel le combustible est un gaz liquide.
  4. Procédé selon la revendication 1 ou 2, dans lequel le combustible est un gaz naturel.
  5. Procédé selon l'une quelconque des revendications précédentes, dans lequel dans l'étape c), une consigne enregistrée dans la commande pour la puissance d'entraînement du dispositif de transport (2) est ajustée.
  6. Procédé selon l'une quelconque des revendications précédentes, dans lequel dans l'étape a), un ventilateur de l'appareil de transport (2) est exploité avec une vitesse de rotation initiale déterminée.
  7. Procédé selon la revendication 6, dans lequel dans l'étape c), une consigne enregistrée dans la commande pour la vitesse de rotation du ventilateur de l'appareil de transport (2) est adaptée.
  8. Procédé selon l'une quelconque des revendications précédentes, dans lequel la détermination est effectuée selon l'étape b) par le biais d'une mesure d'énergie.
  9. Procédé selon l'une quelconque des revendications précédentes, dans lequel dans l'étape b), la puissance de chauffage réelle est déterminée en utilisant des données de capteur de capteurs (6, 9, 11) qui sont associés au circuit de fluide (14).
  10. Procédé selon l'une quelconque des revendications précédentes, dans lequel dans l'étape b), la puissance de chauffage réelle est déterminée en utilisant un rendement, dans lequel le rendement est déterminé en utilisant des données de capteur de capteurs (6, 11) qui sont associés au circuit de fluide (14).
  11. Dispositif de commande (7) pour un appareil de chauffage (1), dans lequel le dispositif de commande (7) est prévu et conçu pour la réalisation d'un procédé selon l'une quelconque des revendications précédentes.
  12. Appareil de chauffage (1) avec un dispositif de transport (2) pour le transport d'un mélange combustible-air et avec un brûleur (3) pour la combustion du mélange combustible-air, dans lequel de la chaleur générée au moyen du brûleur (3) peut être transmise dans un circuit de fluide (14) d'un bâtiment, avec deux capteurs de température (6, 11) et un débitmètre (9) pour la détermination de la puissance de chauffage réelle de l'appareil de chauffage (1) et avec un dispositif de commande (7) selon la revendication 11.
EP21168555.7A 2020-04-17 2021-04-15 Procédé d'ajustement d'une commande d'un appareil de chauffage Active EP3896339B1 (fr)

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Application Number Priority Date Filing Date Title
DE102020110482.0A DE102020110482A1 (de) 2020-04-17 2020-04-17 Verfahren zur Anpassung einer Steuerung eines Heizgeräts

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EP3896339A1 EP3896339A1 (fr) 2021-10-20
EP3896339B1 true EP3896339B1 (fr) 2024-05-29
EP3896339C0 EP3896339C0 (fr) 2024-05-29

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