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EP2369245B1 - Procédé de réglage d'une valeur de consigne de température d'entrée d'une courbe de chauffe d'un système de chauffage - Google Patents

Procédé de réglage d'une valeur de consigne de température d'entrée d'une courbe de chauffe d'un système de chauffage Download PDF

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Publication number
EP2369245B1
EP2369245B1 EP10002716A EP10002716A EP2369245B1 EP 2369245 B1 EP2369245 B1 EP 2369245B1 EP 10002716 A EP10002716 A EP 10002716A EP 10002716 A EP10002716 A EP 10002716A EP 2369245 B1 EP2369245 B1 EP 2369245B1
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EP
European Patent Office
Prior art keywords
heating
temperature
acquisition time
curve
target value
Prior art date
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Application number
EP10002716A
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German (de)
English (en)
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EP2369245A1 (fr
Inventor
Alexander Kelz
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Rehau Automotive SE and Co KG
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Rehau AG and Co
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Priority to EP10002716A priority Critical patent/EP2369245B1/fr
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D19/00—Details
    • F24D19/10—Arrangement or mounting of control or safety devices
    • F24D19/1006—Arrangement or mounting of control or safety devices for water heating systems
    • F24D19/1009—Arrangement or mounting of control or safety devices for water heating systems for central heating
    • F24D19/1015—Arrangement or mounting of control or safety devices for water heating systems for central heating using a valve or valves
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D19/00—Details
    • F24D19/10—Arrangement or mounting of control or safety devices
    • F24D19/1006—Arrangement or mounting of control or safety devices for water heating systems
    • F24D19/1009—Arrangement or mounting of control or safety devices for water heating systems for central heating
    • F24D19/1015—Arrangement or mounting of control or safety devices for water heating systems for central heating using a valve or valves
    • F24D19/1018—Radiator valves
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
    • F24D19/00—Details
    • F24D19/10—Arrangement or mounting of control or safety devices
    • F24D19/1006—Arrangement or mounting of control or safety devices for water heating systems
    • F24D19/1009—Arrangement or mounting of control or safety devices for water heating systems for central heating
    • F24D19/1015—Arrangement or mounting of control or safety devices for water heating systems for central heating using a valve or valves
    • F24D19/1024—Arrangement or mounting of control or safety devices for water heating systems for central heating using a valve or valves a multiple way valve
    • F24D19/1033—Arrangement or mounting of control or safety devices for water heating systems for central heating using a valve or valves a multiple way valve motor operated

Definitions

  • the present invention relates to a method for adjusting a flow temperature setpoint of a heating curve of a heating system during operation of the heating system
  • the required heating energy requirement of a building is not constant, but essentially depends on the prevailing outside temperature.
  • the flow temperature of a heating system is usually determined based on the outside temperature, such as from the document DE 10 2008 040 436 A9 known.
  • a so-called heating curve is used to assign an appropriate outdoor temperature to a corresponding flow temperature. Since the outside temperature is subject to constant fluctuations, the value of the outside temperature used for the heating curve is usually averaged over a period of, for example, 24 hours.
  • the setting of the heating curve is usually done in the initial commissioning by the heating contractor. Often, the heating curve is set too steeply in terms of customer satisfaction in order to prevent customer complaints due to low room temperatures. However, a too steep set heating curve has the consequence that during operation of the heating system, the heat transfer medium is heated to flow temperatures that are higher than actually required, along with a significant reduction in efficiency and energy efficiency. This is particularly problematic when a heat pump is used as the heat generator, which has a constant or substantially constant power output.
  • the pulse width modulated control signal is output by a control device, which for one or more rooms to be heated outputs pulse width modulated signal specific to the particular room.
  • the duty cycle is dependent on the deviation of a measured actual temperature value of the respective room to a predetermined temperature setpoint of the respective room.
  • the present invention has for its object to provide a method for adjusting a flow temperature setpoint of a heating curve of a heating system during operation of the heating system, which in contrast to known solution with much less technical effort to an existing heating system, in which the control of the room temperatures by means pulse width modulated control signals for the alternating opening and closing of the control valves is carried out, is feasible.
  • This object is achieved with a method for adjusting a flow temperature setpoint of a heating curve of a heating system during operation of the heating system with the features of claim 1.
  • At least one heating element of the plurality of heating elements is provided.
  • the heating element may e.g. in the form of a radiator or a heating circuit of a surface heating (eg. A floor, ceiling and / or wall heating) may be formed.
  • Each of the heating elements has at least one control valve and each heating element is in the open state of the control valve from the heat transfer medium, such. Water, permeable.
  • each control valve with a manipulated variable in the form of a pulse width modulated control signal for alternately opening and closing the Control valve controlled, wherein the duty cycle of the pulse width modulated signal depends on the deviation of a measured temperature actual value of the respective room to a predetermined temperature setpoint of the respective room.
  • the duty cycle of the pulse width modulated signal depends on the deviation of a measured actual temperature value of the respective room to a predetermined temperature setpoint of the respective room or varies depending on the deviation of a measured temperature actual value of the respective room to a predetermined temperature setpoint of the respective room.
  • At least one room temperature control device is provided, which outputs for one or more rooms to be heated the pulse width modulated signal intended for the respective actuator.
  • an actuator can be provided for each control valve, which is set up, the pulse width modulated control signal e.g. receive from the room temperature controller and to open and close the control valve alternately according to the pulse width modulated control signal.
  • the heating system further comprises a heat generator for heating the heat transfer medium.
  • a heat generator for heating the heat transfer medium.
  • a conventional piping system or pipe system In order to supply the heat transfer medium to the heating elements or to remove them from these, e.g. be provided a conventional piping system or pipe system.
  • a flow temperature control device of the heating system is adapted to regulate the flow temperature of the heating medium to be supplied or supplied heat transfer medium using a flow temperature set value, which is assigned according to the heating curve an outdoor temperature value during operation of the heating system by averaging outdoor temperatures determined during operation.
  • the means can be carried out, for example, over a fixed period of time, such as a period of 24 hours or 10 hours.
  • the flow temperature setpoint can be determined, which is assigned to the outside temperature value according to the heating curve.
  • the means can, in particular, also be carried out continuously, for example, so that the corresponding flow temperature setpoint is continually or continuously determined.
  • the flow temperature setpoint determined in this way is determined by the flow temperature control device used for control, with the aim of keeping the flow temperature to the flow temperature setpoint or to approach this.
  • the process according to the invention comprises stages A to H.
  • the heating curve is set, the temperature set values are set for each of the rooms, the heating system is operated using the predetermined heating curve and the predetermined temperature set values, and the specification of a detection time.
  • the detection time may be e.g. a few hours, e.g. 4 hours. More preferably, the detection time is within a range of 2 to 6 hours.
  • stage C measuring the outside temperature in the environment of the building at least two different times during the detection time.
  • step D the calculation of an average outside temperature T A, detection time in the vicinity of the building using outside temperatures measured in step C takes place.
  • the measurement of the outside temperature during the detection time is preferably carried out continuously or cyclically, such that, for example, at least every 5 min, preferably at least every 2 min, a measurement of the outside temperature is made. Particularly preferably, the measurement of the outside temperature takes place continuously during the detection time.
  • This provides an average outdoor temperature T A, detection time , which does not overstate short-term fluctuations in the outside temperature.
  • step E the determination of respective total opening times for each of the control valves during the detection time based on the course of the pulse width modulated control signal during the detection time.
  • the course of the pulse-width-modulated control signal during the detection time is in this case preferably removed from a room temperature control device which has output this pulse-width-modulated control signal during the detection time for regulating the room temperature.
  • the profile of the pulse-width-modulated control signal can preferably be taken from the duty cycles set during the detection time by the room temperature controller for generating the pulse width modulated control signal, which can preferably be stored on a memory unit of the room temperature control device.
  • stage G After forming an average of all total opening times in stage F, the determination of the flow temperature set value of the heating curve predetermined in stage A takes place in stage G, which according to this heating curve is assigned to the average outdoor temperature T A, detection time calculated in stage D.
  • step H the flow temperature set value determined in step G is increased when the percentage ratio of the average formed in step F to the detection time is greater than or equal to an upper limit, the upper limit being at least 55%, or decreasing in the step G determined flow temperature setpoint when the percentage ratio of the average value formed in step F is less than or equal to a lower limit, the lower limit is at most 45%, or maintaining the set flow temperature setpoint in step G, when the percentage ratio of the average value formed in step F at the detection time is in a range between the lower limit and the upper limit.
  • the method of the invention it is decided on the basis of the percentage ratio of the average value formed in stage F to the detection time, whether the set flow temperature set value of the predetermined heating curve determined in step G requires a correction in the form of an increase or decrease.
  • the percentage ratio of the mean value formed in stage F to the detection time is greater than or equal to the upper limit, this indicates a flow temperature which is too low for an optimal or sufficiently high efficiency, since the control valves are opened on average by a substantial amount of time longer than are closed, in order to provide a desired heating or temperature determined by the temperature set values of the rooms, so that an increase of the set flow temperature setpoint in step G is made, which according to the predetermined heating curve is assigned to the average outdoor temperature T A, detection time calculated in step D. ,
  • the percentage ratio of the mean value formed in stage F to the detection time is less than or equal to the lower limit, this indicates a flow temperature that is too high for an optimal or sufficiently high efficiency, since the control valves are closed on average by a substantial amount of time longer than are open, in order to provide a desired heating or tempering determined by the temperature set values of the rooms, so that a reduction of the set flow temperature setpoint determined in step G is is made, which is assigned in accordance with the predetermined heating curve of the calculated in step D average outdoor temperature T A, detection time .
  • the percentage ratio of the mean value formed in stage F lies in a range between the upper limit and the lower limit, this indicates a suitable flow temperature for optimum or sufficiently high efficiency, so that the flow temperature setpoint determined in stage G is maintained.
  • the flow temperature setpoint determined in step G is increased by a positive temperature value A when the percentage ratio of the average formed in step F is greater than or equal to the upper limit, the positive value A being preferably selected such that when operating the heating system with such a corrected or changed flow temperature setpoint and the average outside temperature T A associated with this setpoint , detection time in a further passage of the method according to the invention, the percentage ratio of the mean value formed in step F to the detection time in the range between the upper limit and would be the lower limit if the temperature set points of the rooms would have been kept unchanged.
  • the positive value A can be chosen such that, after the further passage, the percentage ratio of the mean value formed in step F to the detection time is 50% or substantially 50%. It has been shown that at this percentage ratio, a very efficient operation of the heating system is possible.
  • step H the flow temperature set value determined in step G is further decreased by a positive temperature value B when the percentage ratio of the average value formed in step F to the detection time is less than or equal to the lower limit
  • the positive value B is preferably selected in that, when the heating system is operated with a corrected or modified flow temperature set value and the average outside temperature T A, detection time in a further passage of the method according to the invention, the percentage ratio of the mean value formed in step F to the detection time in the range between the upper limit and the lower limit, provided that the temperature set points of the rooms were kept unchanged.
  • the positive value B may be particularly preferably selected such that after the further passage, the percentage ratio of the average value formed in step F to the detection time is 50% or substantially 50%.
  • the flow temperature setpoint determined in step (G) in step (H) is increased or decreased by 0.2% to 10% of the actual flow temperature in ° C, i. the values A and B are between 0.2% and 10% of the current flow temperature in ° C.
  • certain flow temperature setpoint in step (H) by 0.5% to 1.5% of the current flow temperature in ° C, more preferably by 0.5% to 1.2% of the current flow temperature in ° C and in particular by about 1.0% of the current flow temperature in ° C increased or decreased
  • the corrected by means of the values A and B flow temperature setpoints can, if they have been provided or determined according to the inventive method in each case for a plurality of average outdoor temperatures T A, detection time , serve as bases for calculating an approximation curve or interpolation curve, which a first example factory preset heating curve with a fixed predefined slope, for example.
  • the respective average outside temperatures T A, detection time of the support points for example, could have a substantially constant distance of a few degrees Celsius or one degree Celsius to one another. Due to the thus possible generation of interpolation points in connection with the determination of an approximation curve or interpolation curve, it is possible to optimally adapt the predetermined heating curve to the respective system and user behavior.
  • a corrected by the value A or B flow temperature setpoint can be assigned according to the respective average outdoor temperatures T A, detection time and a determined heating limit temperature of a Wiengradtagsiere.
  • This Bankgradtagsiere can be determined from values that are preferably the flow temperature control device available, in such a way that the heating limit temperature is specified for example in the flow temperature control device, and that the outside temperature measured and the corresponding measured values of the flow temperature control device are available , An installation of additional measuring probes is not required.
  • the degree of heating degree is a quantity generally known from heating technology, which is calculated by subtracting the average outdoor temperature of one day (for example 5 ° C.) from the heating limit temperature of the building (for example 15 ° C.) (VDI 3807), so:
  • Bankgradtagsiere Heating limit - mean outdoor temperature of a heating day ,
  • the heating limit temperature is in this case the temperature below which a heating of the rooms is necessary in order to keep the room temperature or the room temperatures at a desired value. Therefore internal gains as well as the desired room temperatures of the users are included in this heating limit temperature.
  • an optimal adaptation of the flow temperature setpoint values to the requirements according to the room control is possible, accompanied by an optimal comfort, since this adaptation can in particular also ensure that the room temperatures sufficiently approximate their predetermined temperature setpoints correspond.
  • this adaptation can effectively prevent operation of the heating system at operating points where e.g. a control valve of a heating element is permanently open without even approaching the predetermined temperature setpoint of the room in question. An undersupply of the rooms is therefore effectively avoided.
  • this adaptation can also be used to avoid oversupply, which is characterized by excessive room temperatures with associated increased energy losses or lower efficiency. Overall, a desired level of comfort can thus be achieved while reducing the losses, in particular because, according to the invention, a self-optimization can take place on the respective heating system.
  • the adaptation can preferably be carried out automatically during the operation of the heating system without the user or the installer having to intervene.
  • the method according to the invention can be applied to any system combinations in which the room temperature is regulated according to a pulse width modulation.
  • step (G) the flow temperature setpoint of the heating curve predetermined in step (A) is determined, which according to this heating curve is the difference between the mean value of the temperature setpoint values specified in step (A) and that in step (D). calculated average outdoor temperature T A, acquisition time is assigned.
  • the usage behavior of the user of the heating system predetermined by the temperature set values of the rooms is automatically taken into account in the method according to the invention.
  • the inventive method is carried out in contrast to the known solution with much less effort on the heating system.
  • the adjustment of the flow temperature setpoint takes place only on the basis of the outside temperature, preferably on the basis of the difference between the mean of the predetermined temperature setpoints and the average outside temperature, and the course of the pulse width modulated control signal, which is e.g. can be provided by an already existing room temperature control device, so that no complicated additional installations must be made to carry out the method according to the invention.
  • the upper limit is within a range of 60% to 70%, and the lower limit is within a range of 30% to 40%.
  • the upper limit may be 60% to 65%, and the lower limit may be 35% to 40%, with an upper limit of 60% or 65% and a lower limit of 35% or 40% being particularly preferred.
  • the limits provided for in this practical embodiment for the percentage ratio of the mean value formed in stage F to the detection time are particularly advantageous when there are non-systematic influences such as changing internal loads or solar radiation etc. and / or strongly fluctuating outside temperatures.
  • the interval limits of the interval provided in this practical embodiment within which no change of the flow temperature setpoint is made, the effects of unsystematic influences or strongly fluctuating outside temperatures on the operation of the heating system, which can be compensated by the pulse width modulation, can be effectively damped, along with an optimization of the efficiency.
  • a return to stage B takes place after stage H and the subsequent stages are repeated, with the aim of maintaining a further flow temperature setpoint of the predetermined heating curve or possibly to change, this flow temperature setpoint over the heating curve is now assigned to a calculated according to level D average outdoor temperature T A, detection time , which is different from that in the previous run due constantly changing environmental conditions.
  • the method is only continued if the average outside temperature T A calculated in step (D) is at least 0.5 ° C. smaller, preferably at least 0.2 ° C.
  • the associated over the heating curve mean outdoor temperatures at a distance of at least 0.5 ° C, preferably at least 0.2% to each other. This can be provided by corresponding repetition for the heating curve, a number of bases, which have a sufficient distance from each other in terms of the average outdoor temperature.
  • the heat generator is a heat pump with a constant power output.
  • the heating system may preferably have a conventional mixing device for mixing amounts of heat transfer medium, which have been removed from the heating elements, with heat transfer medium amounts to be supplied to the heating element have.
  • the flow temperature control device is adapted to control the flow temperature using a control variable for controlling the mixing device.
  • the inventive method is particularly in heating systems with a heat generator in the form of a heat pump, which has a constant power output or a substantially constant power output of advantage, since by means of the inventive method, an adjustment of a flow temperature setpoint even without a lowering mode for measuring the return temperature after a longer lowering time is possible. In a heat pump with a constant power output, such a lowering operation is generally not worthwhile or not practicable.
  • the invention further relates to a heating system for a building, wherein the heating system is adapted to carry out a method according to one of claims 1 to 8.
  • the Fig. 1 shows a schematic flow diagram of an embodiment of the method according to the invention.
  • the method illustrated by the flowchart includes steps A through H.
  • step A the heating curve is set, the temperature set values are set for each of the rooms, the heating system is operated using the predetermined heating curve and the predetermined temperature set values, and the specification of a detection time.
  • step C After measuring the outside temperature during the detection time according to step C, the average outside temperature is calculated in step D.
  • T A acquisition time of the building using outdoor temperatures measured in stage C
  • step E the determination of respective total opening times for each of the control valves during the detection time based on the course of the pulse width modulated control signal during the detection time.
  • stage F the determination of the flow temperature set value of the heating curve predetermined in stage A takes place in stage G, which according to this heating curve is assigned to the average outdoor temperature T A, detection time calculated in stage D.
  • step H the flow temperature set value determined in step G is increased when the percentage ratio of the average formed in step F to the detection time is greater than or equal to the upper limit or the flow temperature set value determined in step G is decreased percentage ratio of the average value formed in step F to the detection time is less than or equal to the lower limit, or maintaining the flow temperature setpoint determined in step G when the percentage ratio of the average value formed in step F to the detection time is in a range between the lower limit and the upper limit.
  • FIG. 12 is a schematic diagram illustrating possible percentage ratios of average values formed in stage F at the respective detection time in accordance with the average outdoor temperature T A, detection time .
  • the percentage ratio is plotted against the average outside temperature T A, detection time , so that the diagram shows a state image from which necessary changes in the heating curve can be derived.
  • the symbols shown in the form of a circle indicate the percentage ratios at different average outside temperatures T A calculated according to stage D , detection time at intervals of 5 ° C., where the percentage ratios are greater than 55%, so that an increase in the respective flow temperature Setpoint of the heating curve, for example, by raising the slope of the heating curve, is provided according to the inventive method. Only in the Fig. 2 rightmost circle lies within the interval provided according to stage H, so that there is no need for a change for this operating point.
  • the Fig. 3 schematically shows the course of a predetermined or originally set heating curve, together with three corrected according to the inventive method flow temperature setpoints, which are symbolized by crosses, in which case a decrease in the flow temperature setpoints has been made.
  • the flow temperature setpoints symbolized by the crosses can be used, for example, as interpolation curves or approximation curves (illustrated schematically by the dashed curve), which completely or partially replaces the originally set heating curve, this interpolation curve or approximation curve then also being the flow temperature Regulatory basis.
  • the Fig. 4 shows a schematic diagram illustrating the operation of an embodiment of a room temperature control device which is adapted to control an actuator of a heating element with a manipulated variable in the form of a pulse width modulated control signal for alternately opening and closing the control valve.
  • the duty cycle of the pulse width modulated signal in this case depends on the deviation of a measured temperature actual value of the respective room to a predetermined temperature setpoint of the respective room.
  • the measured temperature actual value lies within a band bounded by the positive temperatures T soll + and T soll- (where T soll + is greater than T soll , and where T soll- is smaller than T soll ), ie if the measured actual temperature value is greater than or equal to T soll- and none or equal to T soll + (see in FIG. 4 the second diagram from above) varies the duty cycle according to a sine curve as a function of the deviation of the measured actual temperature value from the desired value T soll . If the measured actual temperature value is above or below the limits specified by the temperatures T soll + and T soll- , the duty cycle, ie the ratio of the length of the switched-on state to the pulse width or period T (T is in FIG.
  • the period may, for example, have a length of 20 minutes. Usually, the period can be within a range of 10 to 60 minutes, preferably 20 to 30 minutes.
  • the duty cycle ie the ratio of the length of the switched-on state to the pulse width or period T, is set to zero by the room temperature controller (cf. See the corresponding waveform in the lower diagram of the Fig. 4 ), accompanied by a closing of the control valve during the entire period T.
  • the room temperature controller cf. See the corresponding waveform in the lower diagram of the Fig. 4
  • a closing of the control valve during the entire period T.
  • the duty cycle to 1 ⁇ 2 or 50% is set (see FIG. Point 2).
  • the duty ratio ie the ratio of the length of the switched-on state to the pulse width or period T, is set to 1 or 100% by the room temperature controller. accompanying opening of the control valve throughout the period.
  • the duty cycle is set to a value between 0 and 1 or between 0% and 100% according to the course of the sinusoid.
  • a predetermined temperature setpoint T soll of the room in question can be set or approximated, with the duty cycle being varied for setting or approaching this setpoint value T soll .
  • the room temperature control device for setting or approaching the desired setpoint the respective actuator or the respective control valve with a pulse width modulated signal with a duty cycle of 50% or substantially 50%, along with a very efficient operation of the heating system.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Steam Or Hot-Water Central Heating Systems (AREA)

Claims (9)

  1. Procédé pour adapter une valeur de consigne de température aller d'une courbe de chauffage d'une installation de chauffage pendant le fonctionnement de l'installation de chauffage, l'installation de chauffage étant une installation de chauffage d'un bâtiment comprenant une pluralité de pièces qui sont prévues pour un chauffage au moyen de l'installation de chauffage, l'installation de chauffage comprenant les éléments suivants :
    - un générateur de chaleur pour réchauffer un fluide caloporteur,
    - une pluralité d'éléments chauffants qui peuvent être traversés par l'écoulement du fluide caloporteur,
    - un dispositif de régulation de la température aller, le dispositif de régulation de la température aller étant configuré pour réguler la température aller du fluide caloporteur à acheminer aux éléments chauffants en utilisant une valeur de consigne de la température aller, laquelle est associée, conformément à la courbe de chauffage, à une valeur de la température extérieure qui est déterminée pendant le fonctionnement de l'installation de chauffage par des moyennes des températures extérieures qui sont mesurées pendant le fonctionnement,
    au moins l'un des éléments chauffants étant prévu pour chaque pièce, chaque élément chauffant présentant au moins une vanne de réglage et chaque élément chauffant, lorsque la vanne de réglage est ouverte, pouvant être traversé par l'écoulement du fluide caloporteur,
    pour la régulation de la température des pièces, chaque vanne de réglage pouvant être commandée avec une grandeur de commande sous la forme d'un signal de commande modulé en largeur d'impulsion pour l'ouverture et la fermeture alternées de la vanne de réglage, le rapport cyclique du signal modulé en largeur d'impulsion dépendant de l'écart entre une valeur réelle mesurée de la température de la pièce correspondante et une valeur de consigne prédéfinie de la température de la pièce correspondante,
    le procédé comprenant les étapes suivantes :
    (A) prédéfinition de la courbe de chauffage, prédéfinition de valeurs de consigne de la température pour chacune des pièces et exploitation de l'installation de chauffage en utilisant la courbe de chauffage prédéfinie et les valeurs de consigne de la température prédéfinies,
    (B) prédéfinition d'une période d'acquisition,
    (C) mesure de la température extérieure dans l'environnement du bâtiment en au moins deux instants différents pendant la période d'acquisition,
    (D) calcul d'une température extérieure moyenne TA,Erfassungszeit dans l'environnement du bâtiment en utilisant les températures extérieures mesurées à l'étape (C),
    (E) détermination des temps d'ouverture totaux respectifs pour chacune des vannes de réglage pendant la période d'acquisition au moyen de l'évolution du signal de commande modulé en largeur d'impulsion pendant la période d'acquisition,
    (F) formation d'une valeur moyenne à partir de tous les temps d'ouverture totaux, et
    (G) détermination de la valeur de consigne de la température aller de la courbe de chauffage prédéfinie à l'étape (A), laquelle est associée conformément à cette courbe de chauffage à la température extérieure moyenne TA,Erfassungszeit calculée à l'étape (D),
    (H) augmentation de la valeur de consigne de la température aller déterminée à l'étape (G) lorsque le rapport en pourcentage entre la valeur moyenne formée à l'étape (F) et la période d'acquisition est supérieur ou égal à une limite haute, la limite haute étant au moins égale à 55 %, ou
    diminution de la valeur de consigne de la température aller déterminée à l'étape (G) lorsque le rapport en pourcentage entre la valeur moyenne formée à l'étape (F) et la période d'acquisition est inférieur ou égal à une limite basse, la limite basse étant égale au maximum à 45 %, ou
    maintien de la valeur de consigne de la température aller déterminée à l'étape (G) lorsque le rapport en pourcentage entre la valeur moyenne formée à l'étape (F) et la période d'acquisition se trouve dans une plage comprise entre la limite basse et la limite haute.
  2. Procédé selon la revendication 1, caractérisé en ce que la valeur de consigne de la température aller déterminée à l'étape (G) est augmentée ou diminuée à l'étape (H) de 0,2 % à 10 % de la valeur actuelle de la température aller en °C.
  3. Procédé selon la revendication 1 ou la revendication 2, caractérisé en ce que dans l'étape (G) est déterminée la valeur de consigne de la température aller de la courbe de chauffage prédéfinie à l'étape (A), laquelle est associée conformément à cette courbe de chauffage à la différence entre la valeur moyenne des valeurs de consigne de la température prédéfinies à l'étape (A) et la température extérieure moyenne TA,Erfassungszeit calculée à l'étape (D).
  4. Procédé selon l'une des revendications précédentes, caractérisé en ce qu'un retour à l'étape (B) a lieu après l'étape (H) et les étapes suivantes sont répétées.
  5. Procédé selon la revendication 4, caractérisé en ce qu'une poursuite du procédé n'a lieu après l'étape (D) que si la température extérieure moyenne TA,Erfassungszeit calculée à l'étape (D) est inférieure d'au moins 0,5 °C ou supérieure d'au moins 0,5 °C à la température extérieure moyenne TA,Erfassungszeit calculée à l'étape (D) lors de l'exécution précédente du procédé.
  6. Procédé selon l'une des revendications précédentes, caractérisé en ce que la limite haute se trouve à l'intérieur d'une plage de 60 % à 70 % et en ce que la limite basse se trouve à l'intérieur d'une plage de 30 % à 40 %.
  7. Procédé selon l'une des revendications précédentes, caractérisé en ce que la limite haute vaut de 60 % à 65 % et en ce que la limite basse vaut de 35 % à 40 %.
  8. Procédé selon l'une des revendications précédentes, caractérisé en ce que le générateur de chaleur est une pompe à chaleur à puissance délivrée constante.
  9. Installation de chauffage pour un bâtiment, l'installation de chauffage étant configurée pour mettre en oeuvre un procédé selon l'une des revendications 1 à 8.
EP10002716A 2010-03-16 2010-03-16 Procédé de réglage d'une valeur de consigne de température d'entrée d'une courbe de chauffe d'un système de chauffage Active EP2369245B1 (fr)

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EP10002716A EP2369245B1 (fr) 2010-03-16 2010-03-16 Procédé de réglage d'une valeur de consigne de température d'entrée d'une courbe de chauffe d'un système de chauffage

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EP10002716A EP2369245B1 (fr) 2010-03-16 2010-03-16 Procédé de réglage d'une valeur de consigne de température d'entrée d'une courbe de chauffe d'un système de chauffage

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3779286A1 (fr) * 2019-08-12 2021-02-17 Huu-Thoi Le Procédé de fonctionnement d'une installation de chauffage
DE102019005722A1 (de) * 2019-08-12 2021-02-18 Huu-Thoi Le Verfahren zum Betrieb einer Heizungsanlage

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH717496B1 (de) * 2020-06-04 2023-03-31 Horst Gruening Hoka Therm Heizsysteme Gruening Verfahren zur Steuerung der Wärmeerzeugung und -verteilung in einer Heizungsanlage.

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FR2213707A5 (fr) * 1973-01-09 1974-08-02 Saunier Duval
EP0594886B1 (fr) 1992-10-29 2001-07-18 Landis & Gyr Technology Innovation AG Procédé de régulation d'une installation de chauffage et dispositif pour sa mise en oeuvre
DE10056453A1 (de) 2000-11-14 2002-05-23 Felix Gausch Heizlastabhängige Anpassung der Vorlauftemperatur einer mischerbetriebenen Heizungsanlage für Gebäude mit geregelten Raumheizkörpern
EP1456727B2 (fr) 2001-12-19 2017-06-14 Techem Energy Services GmbH Procede et dispositif permettant d'adapter la puissance thermique d'installations de chauffage
DE102004020607B3 (de) 2004-04-27 2005-10-27 Bbt Thermotechnik Gmbh Verfahren zum Regeln einer Heizungsanlage
DE102006013098C5 (de) 2006-03-20 2010-08-19 Techem Energy Services Gmbh Verfahren und Vorrichtung zur bedarfsgeführten Wärmebereitstellung in einer Heizungsanlage
US7857233B2 (en) * 2006-09-01 2010-12-28 Flow Design, Inc. Electronically based control valve with feedback to a building management system (BMS)
CH698872B1 (de) 2007-08-09 2009-11-30 Markus Brueckner Verfahren zum Ermitteln einer Sollvorlauftemperatur für eine Regelung einer Warmwasserheizung eines Gebäudes.
KR100924147B1 (ko) * 2007-12-04 2009-10-28 주식회사 경동네트웍 난방시스템 제어방법

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3779286A1 (fr) * 2019-08-12 2021-02-17 Huu-Thoi Le Procédé de fonctionnement d'une installation de chauffage
DE102019005722A1 (de) * 2019-08-12 2021-02-18 Huu-Thoi Le Verfahren zum Betrieb einer Heizungsanlage

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