EP3553408A1 - Hybrid heating device and method for operating a hybrid heating device - Google Patents

Abstract

The invention relates to a method for operating a hybrid heater (1) and a hybrid heater (1). The heater (1) comprises a first heat source (3) based on the combustion of a mixture of fuel gas and air and a second heat source (4) based on electrical energy. If the heat requirement (101) falls below the minimum power (P) of the first heat source, the system switches to the second heat source (4) and vice versa.

Description

The invention relates to a method for operating a hybrid heater and a hybrid heater. A hybrid heater in the context of this invention is a heater that generates heat from both the combustion of a fossil fuel such as natural gas and from an electrical energy source and provides for the heating of a building.

Usually, heaters work monovalent, ie the heat is sourced only from one source of energy. For economic and ecological reasons, this is often natural gas. For technical reasons, however, the range between minimum and maximum power is limited, since the flow rate of the combustion air required for mixture formation is too low. In the patent application EP2735793A2 this is done by additional device features in the mixture forming device.

As a result, the modulation range can be extended downwards, ie in the range of lower powers. Modulation ranges or power ratios between minimum and maximum power of 1:20 are very good values according to the prior art. Nevertheless, there is still a need for heaters covering an even smaller area.

According to the invention this object is achieved with a hybrid heater with a burner according to the prior art and an additional electric heater according to the method of claim 1.

Basically, hybrid heaters or heating systems are known from the prior art. The utility model DE 9004025 U1 shows an additional integrated in a radiator electric immersion heater. It is disclosed that this heating cartridge is put into operation in case of failure of the heater.

The publication DE 3109990 A1 shows a comparable heating cartridge outside the radiator, but also outside the heater. The DE 3109990 A1 teaches to use the electric heating cartridge with low heating demand. Explicit here are called the antifreeze function in the absence or the operation outside the normal heating periods. Again, an either-or-operation is provided.

The DE 3325822 A1 shows a boiler with electric preheater. This serves to avoid condensation.

However, none of the disclosed methods of operating the aforementioned hybrid heating systems or heaters is capable of extending down the modulation range of fossil fuel burning during operation.

Therefore, the method according to the invention according to claim 1, the heat demand of heat sinks for small outputs, which are below the minimum power of the first heat source, in this case a gas burner, to cover by a second electric heat source. In this case, the second heat source as well as the first heat source is integrated in a heating circuit and transfers the heat to a heat transfer medium. The advantage is that, to the outside, the heater has a modulation range extended to lower powers.

In a development of the invention according to claim 2, the two heat sources for large heat demand can also be operated simultaneously. Thus, the modulation range can also be extended in the direction of larger powers.

The current heat demand can be defined for example by a desired flow temperature of the heat transfer medium in the heating circuit. At constant flow rate of the heat transfer medium, ie at constant speed of the circulation pump, there is a direct proportionality between the current heat demand and the desired flow temperature. According to the prior art, the desired flow temperature is determined as a function of the outside temperature and the desired room temperature on the basis of a mathematical building model (heating curves). According to the prior art, a heater adjusts its power by means of a regulator so that the actual flow temperature of the desired flow temperature corresponds. According to claim 3, therefore, the inventive method is carried out on the basis of the flow temperature. The first heat source is not operated below its minimum power. In the event that this power is above the current heat demand, this leads to an increase in the actual flow temperature. As soon as the actual flow temperature is above the desired flow temperature by a certain amount above a certain period of time during operation with minimum power, the first heat source is switched off and the second heat source is switched on, which now supplies the heat sinks with heat. In this case, the flow temperature is still regulated.

Now increases the heat demand again, so according to the invention, the switching to the first heat source according to claim 4 or 5 carried out according to two alternative process variants. Either the second heat source is operated with a maximum of the minimum power or a power slightly above the minimum power of the first heat source. An increased heat requirement leads to a drop in the flow temperature, which leads after exceeding a certain difference over a certain period of time according to the method described above. This is according to the invention, that the second heat source is turned off and the first heat source is turned on. Alternatively, the power of the second heat source may be increased beyond the minimum power of the first heat source. If the second heat source is operated with a power above the minimum power of the first heat source for a certain period of time, this leads according to the invention to switch off the second heat source and to switch on the first heat source.

Preferably, the difference amounts of the flow temperatures are less than 1 K, more preferably less than 0.5 K.

The measurement periods within which the temperature deviation of the actual flow temperature must be greater than the difference in order to effect a switching of the heat source is preferably at least the circulation time of the heat transfer medium in the heating circuit. Under circulation duration is understood as the, which is needed for a complete circulation of the heat transfer medium in the heating circuit. This time depends on the volume flow of the circulation pump and the total volume of the heating circuit.

The minimum power and the maximum power of the first heat source is determined by measures that are already known in the system. This is the speed of the fan, a calculated from the speed of the fan and the power consumption of the fan air mass flow, an air mass flow measured by a volume or mass flow sensor.

An apparatus for carrying out the method is protected according to the independent apparatus claim.

The invention will now be explained in detail with reference to FIGS.

• Figur 1: eine Vorrichtung zum Durchführen des erfindungsgemäßen Verfahrens
• Figur 2, 3: Leistungsverlauf der ersten und zweiten Wärmequelle und Vorlauftemperaturabweichungsverlauf während des Durchführens des erfindungsgemäßen Verfahrens

They show:

• FIG. 1 a device for carrying out the method according to the invention
• FIG. 2 . 3 : Performance curve of the first and second heat source and flow temperature deviation course during the implementation of the method according to the invention

FIG. 1 shows an apparatus for carrying out the method according to the invention. The heater 1 comprises the first heat source 3 and the second heat source 4. The first heat source 3 is a burner operated with fuel gas, to which a fuel gas-air mixture is supplied via a blower 2. About a not shown here exhaust pipe, the exhaust gases are removed. In the heat source 3, the heat produced by the combustion transferred to a heat transfer medium that circulates in a heating circuit 11 by means of a circulating pump 12. In this case, the heat transfer medium transfers the heat to a heat sink 8, for example, a heater for a building or a heat sink 9, for example, a hot water tank for service water. Via a three-way valve 12, the heating circuit 11 can be adjusted so that the heated heat transfer medium is passed either through the heat sink 8 or through the secondary heat exchanger 6, which transfers the heat to the heat sink hot water tank 9.

In the flow direction of the heat transfer medium behind the first heat source 3, a second heat source 4 is arranged. In the present case, it is an electrical heater in the form of, for example, a heating cartridge, which is surrounded by the heat transfer medium. The second heat source 4 can transmit heat to the heat transfer medium alternately or together with the first heat source 3. A control unit 5 controls via the blower 2, the heat source 3 and the heat source 4. In addition, via the flow temperature sensor 13 to the controller 5, the information about the current flow temperature. Furthermore, the control unit 5 is set up, via an outside temperature sensor 7, the selected room temperature and a mathematical model of the Building to specify the current heat demand. This can be done for example in the form of a desired flow temperature. By comparison with the measured by the flow temperature sensor actual flow temperature, the first heat source 3 and the second heat source 4 can be controlled.

In this case, the first heat source 3 is designed such that it has a minimum power and a maximum power. The heat source 3 can not deliver heat below the minimum power without being turned off periodically. For this reason, the second heat source 4 is connected in series behind the first heat source 3, which can heat the heat transfer medium with low power by means of electrical energy.

Furthermore, it is possible for high heat demand, the first heat source 3 and the second heat source 4 to operate simultaneously.

FIG. 2 and 3 show graphically illustrated courses of heat demand 101, deviation of the flow temperature 102 and heat outputs 103, 104 of the first 3 and second heat source 4 Figures 2 and 3 differ by different process variants switch from the second heat source 4 to the first heat source 3 at time t4. Below are the Figures 2 and 3 described together and pointed to differences.

The description is based on a heat demand 101 which is initially above the minimum power P _{1, min} and below the maximum power P _{2, max of} the first heat source 3. The heat requirement is initially covered exclusively by the first heat source 3. The heat demand sings continuously at first. At time t1, the heat requirement falls below the minimum power P _{1, min of} the first heat source 3. The power of the first heat source 3 can not be further reduced, so that the deviation of the flow temperature slowly rises. The flow temperature exceeds a first difference amount ΔT ₁ . After this at time t2, this first difference .DELTA.T ₁ is present over a minimum period .DELTA.t _1, it is recognized that a certain duration .DELTA.t ₁ is a lower demand for heat. The first heat source 3 is turned off, the graph of the graph 103 falls to zero. At the same time, the second heat source 4 is put into operation, so that the graph 104 increases from zero. Since there is already an excess temperature of the flow temperature, the power of the second heat source 4 only slowly approaches the course of the heat demand.

The described threshold values in the form of the first measurement space Δt ₁ and the first difference ΔT ₁ serve to ensure that the switchover from the first heat source 3 to the second heat source 4 takes place only when the heat requirement 101 has dropped safely. Thus, a frequent switching back and forth between the heat sources 3 and 4 is avoided in the transition region.

The heat demand 101 then rises again and exceeds the minimum power of the first heat source at time t3. In the in FIG. 2 As shown, the maximum power of the second heat source is limited to the minimum power of the first heat source. Alternatively, it is also possible to provide a power limitation just above, for example, 110% of the minimum power P _{1, min of} the first heat source 3. Analogous to the method described above at the times t1 and t2, a certain time is also waited for at the times t3 and t4, in which the actual flow temperature falls below the desired flow temperature by the difference amount ΔT ₂ . Then, at time t4, the second heat source 4 is turned off, so that the graph 104 falls to zero. At the same time, the first heat source is switched on again, so that the graph 103 rises from zero and initially shoots beyond the course of the graph of the heat demand 101 to compensate for the deviation of the flow temperature. Subsequently, the graph 103 of the heating power of the first heat source 3 follows the graph 101 of the heat demand.

Deviating from this is in the FIG. 3 shown course of the heating power of the second heat source, this heating power continues to track the heat demand 101. After the third minimum period Δt ₃ , the increased heat demand is detected and as in FIG. 2 At time t4, the second heat source 4 is turned off and the first heat source 3 is turned on.

Finally, at time t5, the heat demand 101 exceeds the maximum power P _{1, max of} the first heat source 3. In an optional development of the invention, the second heat source 4 is now operated in addition to the first heat source 3, which can be recognized by the rising graph 104. The services 103 of the first heat source 3 and 104 of the second heat source 4 in total cover the heat demand 101.

LIST OF REFERENCE NUMBERS

1

heater

2

fan

3

First heat source

4

Second heat source

5

control unit

6

Secondary heat exchanger

7

Outdoor temperature sensor

8th

Heat sink heating

9

Heat sink Hot water tank

10

Three-way valve

11

heating circuit

12

circulating pump

13

Flow temperature sensor

101

heat demand

102

Deviation of the flow temperature

103

Heating power of the first heat source

104

Heating power of the second heat source

P _{1, min}

Minimum power of the first heat source

P _{1, max}

Maximum power of the first heat source

ΔT ₁

First difference amount of the flow temperature

ΔT ₂

Second differential amount of the flow temperature

Δt ₁

First measurement period

Δt ₂

Second measurement period

Δt ₃

Third measurement period

t1 - t5

time

Claims (10)

A method of operating a hybrid heater (1), wherein the heater (1) comprises a first heat source (3) based on combustion of a mixture of fuel gas and air, the mixture or air being supplied with a blower (2) the heating device (1) comprises a second heat source (4) based on electrical energy, wherein the first (3) and the second heat source (4) transfers the heat to a liquid heat transfer medium which is conveyed by means of a circulating pump (12) between the heater ( 1) and one or more heat sinks (8, 9) circulates in a heating circuit (11), wherein a control device (5) controls the first (3) and the second heat source (4) such that a predetermined heat requirement of the heat sinks (8, 9) is satisfied, and wherein the first heat source (3) has a minimum power (P _{1, min} ) and a maximum power (P _{1, max} ), characterized in that the current heat demand or a characteristic for the current heat edarf is determined continuously and that the second heat source (4) is operated with the heat demand when the current heat demand is less than the minimum power (P _{1, min} ) of the first heat source (3), or that the first heat source (3) with the Heat requirement is operated when the current heat demand is greater than or equal to the minimum power (P _{1, min} ) of the first heat source (3). A method according to claim 1, characterized in that the first heat source (3) with the maximum power (P _{1, max} ) is operated and that the second heat source (4) with the difference between the current heat demand and the maximum power (P _{1, max} ) the first heat source (3) is operated when the heat demand is greater than the maximum power (P _{1, max} ) of the first heat source (3). A method according to claim 1 or 2, characterized in that the current heat demand is defined by a desired flow temperature of the heat transfer medium and the controller (5) adjusts the power of the first (3) or the second heat source (4) so that the actual Flow temperature is equalized to the desired flow temperature, wherein in the case that the first heat source (3) with the minimum power (P _{1, min} ) is operated and the actual flow temperature at least over a first measurement period (At ₁ ) at least a first Difference amount (.DELTA.T ₁ ) is above the target flow temperature, the first heat source (3) is turned off and the second heat source (4) is operated. A method according to claim 3, characterized in that the second heat source (4) is operated at a maximum power equal to or above the minimum power (P _{1, min} ) of the first heat source (3) and that in the case that the second heat source (4 ) is operated at the maximum power and the actual flow temperature is at least a second difference (ΔT ₂ ) at least a second difference (ΔT ₂ ) below the target flow temperature, the second heat source is turned off and the first heat source (3) operated becomes. A method according to claim 3, characterized in that in the case that the second heat source (4) with a power over a third measuring period (At ₃ ) above the minimum power (P _{1, min} ) of the first heat source (3) operated, the second Heat source (4) is turned off and the first heat source is operated. Method according to one of claims 3 to 5, characterized in that the first and / or second difference amount (.DELTA.T _1, .DELTA.T ₂ ) is less than 1 K. Method according to one of claims 3 to 6, characterized in that the first and / or second difference amount (.DELTA.T ₁ , .DELTA.T ₂ ) is less than 0.5 K. Method according to one of claims 3 to 7, characterized in that the first (At ₁ ) and / or second (At ₂ ) and / or third measuring period (At ₃ ) is at least the circulation time of the heat transfer medium in the heating circuit (11). Method according to one of the preceding claims, characterized in that the minimum power (P _{1, min} ) or maximum power (P _{1, max} ) of the first heat source (3) by the speed of the blower (2), by a speed and power consumption of the blower (2) formed mass flow characteristic or by a measured by a volume or mass flow sensor volume or mass flow of the air, the gas or the gas-air mixture is determined. A hybrid heater (1) having a first heat source (3) based on the combustion of a mixture of fuel gas and air, the mixture or air being supplied with a fan (2), the first heat source (3) having a minimum power (P _{1 , min} ) and a maximum power (P _{1, max} ), with a second heat source (4) based on electrical energy, wherein the first (3) and the second heat source (4) transfers the heat to a liquid heat transfer medium, with a Circulation pump (12), which circulates during operation the heat transfer medium between the heater (1) and one or more to the heater (1) in a heating circuit (11) connectable heat sinks (8, 9), and with a control unit (5), the the first (3) and the second heat source (4) drives, characterized in that the second heat source (4) in the heating circuit (11) in the conveying direction of the circulation pump (12) in series behind the first heat source (3) is arranged and that S Expensive device (5) is designed so that it carries out the method according to one of claims 1 to 9.

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