METHOD FOR MONITORING AND CONTROLLING COMBUSTION IN COMBUSTIBLE GAS BURNERS AND SYSTEM FOR CONTROLLING COMBUSTION OPERATING ACCORDING TO SAID METHOD

Description

[0001] The present invention relates to a method for monitoring and controlling combustion in combustible gas burners for appliances such as boilers, water heaters, fireplaces and the like, equipped with modulating fans for the combustion air. It also relates to a combustion control system operating in accordance with said method.

[0002] In the reference technical sector, it is known that in order to maintain efficient combustion, it is necessary for the ratio between the quantity of air and the quantity of combustible gas injected into the burner to be maintained around a predetermined optimal value, which depends essentially on the type of gas used and, in general, may also depend on the value of the power supplied by the burner, i.e. the gas flow rate.

[0003] This makes it possible to obtain and maintain over time a process of complete combustion without excessive dispersion of energy in the fumes and minimising the production of polluting gases, in compliance with the emission regulations of various countries.

[0004] To achieve this objective of maintaining the optimal air/gas ratio, different devices and methods have been developed in the reference technical field.

[0005] In the specific field of application of the invention, methods are known for monitoring and controlling combustion that are based on an analysis of the flame and, in particular, of the ionisation of the gas in the combustion zone of said flame. Typical methods provide for the use of an electrode located in the flame zone or in the proximity of the same, connected to an electronic circuit that applies a fixed or variable voltage to said electrode and measures the current that flows through said electrode. By means of current signal processing and analysis systems, a calculation is made of one or more parameters relating to the combustion process. Among the processing systems, signal frequency spectrum analysis methods are known that are suitable for identifying frequency spectrums or variations of the same indicating flame instability or sub-optimal combustion, on the basis of which systems are provided for correcting the combustion process in order to return said process to the desired conditions.

[0006] The recognisable limits of the known methods are mainly linked to the reliability of the results of the frequency spectrum analyses and their correlation with the combustion process, as well as to the complexity of the calculation and analysis algorithms used.

[0007] An example of a method for monitoring and controlling combustion in a premix combustible gas burner is also know from WO 2014/049502. The method comprises a first phase of acquiring and processing data from experimental conditions and a second phase of evaluating the desired combustion characteristic, under an actual operating condition of the burner. In the first phase a plurality of experimental combustion conditions are applied to the burner, and in each of these experimental conditions applying an electrical voltage signal to the electrode and carrying out a sampling of the response signal, calculating, on the basis of the sequence of sampled values, the characteristic parameters of the waveform of the signal for each of the experimental conditions, by applying a functional transform, for the purposes of calculating a correlation function. The second phase comprises the steps of applying a voltage signal to the electrode and carrying out sampling of the resultant response signal, calculating, on the basis of the sequence of sampled values, the characteristic parameters of the waveform of the response signal at the electrode, and calculating the estimated value of the desired combustion characteristic by using the correlation function.

[0008] Further limitations in the known methods can also be found in the possible wear and ageing of the electrode used to receive the signal at the ionisation sensor, with consequent repercussions on the reliability and precision of the data analysed by the frequency spectrum processing algorithms.

[0009] The above-mentioned limitations are also amplified when it is desired to perform combustion control in burners of the modulating type, in which it is sought to achieve optimal combustion conditions according to variations in the required power, within the range between a minimum power and a maximum permissible power for the burner.

[0010] It is also known that the volumetric ratio between the gas flow rate and the air flow rate suitable for correct combustion also depends on the type of gas. Each family of combustible gases is therefore correlated with respective and specific regulation curves (which correlate, for example, the gas flow rate with the air flow rate). One of the problems of the known combustion control systems is that relating to the identification of the family of gases and to the association of the optimal regulation curves.

[0011] The problem addressed by the present invention is that of providing a method for monitoring and controlling combustion in a burner of a combustible gas appliance, as well as a combustion control system operating in accordance with said method, that are structurally and functionally designed to overcome the limitations described above with reference to the cited prior art.

[0012] Within the context of this problem, it is an aim of the invention to provide a method and a control system that are suitable for ensuring optimal combustion over the entire range of flow rates (and for various types of gas) or power outputs for which the burner is designed, providing reliability and repeatability of results in the analysis of the signals relating to the combustion process.

[0013] Another aim of the invention is to provide a method and a control system that are simple to manage and characterise both during installation and during use of the burner of the appliance.

[0014] This problem is solved and these aims are achieved by the present invention by means of a method and a system for controlling combustion in a burner of a combustible gas appliance, produced in accordance with the claims that follow.

[0015] The features and advantages of the invention will become clearer from the following detailed description of a preferred embodiment, given by way of non-limitative example, with reference to the accompanying drawings, in which:

• Figure 1 is a schematic view of a burner of an appliance equipped with a combustion control system operating in accordance with the combustion monitoring and control method according to the invention,
• Figure 2 is a graph showing a function of interpolation between the parameters that characterise respective combustion process conditions in corresponding operating conditions of the burner,
• Figures 3 and 4 are graphs showing the trend of the respective parameters of the interpolation function of the previous figure according to variations in some of the parameters that characterise the combustion process,
• Figure 5 is a graph showing the trend of the electrical signal applied to the electrode of the burner according to the method of the present invention, in a specific operating condition with preselected power and air number values, and also showing in a corresponding manner, as the time value changes, the function of the response signal obtained, with the trend illustrated in Figure 2,
• Figure 6 is a graph showing the curves of correlation between operating parameters of a fan and of a modulating gas valve of a burner appliance operating with the combustion control method of the invention.

[0016] With initial reference to Figure 1, 1 indicates overall a burner, represented only schematically, equipped with a combustion control system, produced to operate in accordance with the combustion monitoring and control system of the present invention.

[0017] The burner 1 is housed in an appliance, not represented, intended for the production of domestic hot water and/or slaved to a room heating circuit, in a manner that is known per se and not illustrated in the figures.

[0018] The burner 1 comprises a combustion chamber 2, which is fed by a first pipe 3 and a second pipe 4, suitable for introducing into said combustion chamber 2 a flow of air and, respectively, a flow of combustible gas. Preferably, the second pipe 4 enters the first pipe 3 upstream of the combustion chamber 2 (premix burner). On the air/gas mixing section is provided a fan 5 with variable rotation speed. In the configuration of Figure 1, the fan is located downstream of the mixing zone, but may also alternatively be located upstream of said air/gas mixing zone. 6 indicates a modulating valve located on the gas pipe 4 for regulating the flow of gas injected into the burner.

[0019] The combustion chamber 2 is connected downstream to a flue 7, through which the combustion exhaust gases are evacuated. 8 indicates a combustion monitoring sensor, described in greater detail below, which is connected to a control device 9 provided with an electronic circuit unit suitable for controlling the burner according to the method of the present invention, as illustrated below. The control device is also operatively connected both to the fan 5 and to the modulating valve 6 for regulating said units.

[0020] The sensor 8 is arranged in the proximity of the burner flame, and is suitable for being powered by a voltage generator, as well as being connected to an electronic circuit suitable for measuring the resulting potential at the sensor. The sensor 8 comprises an electrode, indicated by E, which is placed in the flame or in the proximity thereof. The electrode E, in a preferred embodiment designed as a mono-electrode structure, can conveniently serve both as a flame ignition element and as an element suitable for measuring the potential generated in response to the application of a voltage signal to the electrode, during the combustion process, in accordance with the method of the present invention. A suitable switching unit is provided for electrically connecting the electrode E with the respective control circuits of the above-mentioned functions. Conveniently, the electrode E, when it measures the response signal, is disconnected from the voltage generator (and connected to the measuring device).

[0021] According to what is known of the physics of the plasmas that develop during combustion processes, if an external load is introduced into the plasma, said load, due to the electrical field that it produces, causes a motion of the loads that constitute the plasma; this motion increases as the introduced external load increases. However, there is an electrical field value above which the flow of load particles does not increase any further (saturation). The motion is significantly different for electrons and for ions: since electrons are much lighter and smaller, they move much more quickly and undergo far fewer collisions along their course of travel. This means that the above-mentioned phenomenon of saturation occurs much earlier in the case of positive ions, while it occurs later for electrons. The macroscopic effect generated by the introduced external load, due to the movement of the load particles, is an alteration of the electrical field of the plasma. This electrical field is propagated around the particle over a distance in the order of the 'Debye length'. This distance, as mentioned above, is greater for electrons, i.e. in cases where the introduced load is positive. On the other hand, it is smaller in the case of positive ions, i.e. when the introduced load is negative.

[0022] Returning to the method of the invention, an electrical voltage signal with a determined wave form over time is applied to the electrode E; this potential is equivalent to the interference load mentioned in the preceding description. The electrode assumes a potential value determined by the motion of the plasma loads caused by the voltage signal applied to the electrode and responding to the dynamics described above. The changes in this potential are then measured by the electronic circuit and processed in the manner that will be described below.

[0023] The underlying concept of the method of the invention is therefore the fact that the trend of the resulting response signal at the electrode E is unequivocally determined by the composition of the fuel/air mixture prior to combustion. Knowledge of this composition is essential in order to be able to predict certain key effects of the combustion process, such as the quantities of CO₂ and CO produced and the thermal power produced. In this way, among other things, it is possible to compensate for the effects of gases other than the nominal gases, referred to in the sector as G20 and G31. Therefore, knowledge of the air number (indicated elsewhere by the symbol "λ"), understood as the ratio between the quantity of air in the combustion process and the quantity of air for stoichiometric combustion, makes it possible to produce a system for controlling the combustion of a gas burner appliance.

[0024] More particularly, according to the invention, an impulsed periodic electrical voltage signal is applied to the electrode E, and said signal has an interference effect on the motion of the loads present in the plasma, such that said electrode, once the applied impulse has ceased, assumes a potential value determined by the motion of said loads, which is measured by the electronic circuit and processed in the manner that will be described below.

[0025] The method of the invention essentially comprises two macro operating phases: a first phase, indicated by A, of acquisition and processing of data relating to operating conditions applied to the burner, and a second phase, indicated by B, of calculating the air number λ or the generated thermal power P, in a real operating condition of the burner.

[0026] Both of these phases comprise, in turn, a sequence of operating steps that will be described in detail below.

[0027] In the description that follows, the steps relating in particular to the calculation of the air number λ will be described, but these can also be applied in the same way for other parameters relating to the combustion process.

[0028] A first operating step of phase A, indicated by A1, involves identifying and reproducing in the burner a plurality (1, 2, ..., n) of combustion conditions, in each of which a respective power P (P1, P2, ..., Pn) is applied and for each power (i.e. deriving from the combustion of a corresponding flow of combustible mixture) an air number (λ1, λ2, ..., λm) is applied, said air number λ expressing the ratio between the quantity of air in the combustion process and the quantity of air for stoichiometric combustion. Each condition can also be repeated a preset number of times, in order to verify that the measurements made are not influenced by conditions of anomalous operation of the burner or by drift or by variability of the flame.

[0029] In a second subsequent operating step, indicated by A2, an electrical voltage signal is applied in each of said (n * m) operating conditions (Pi, λj) to the electrode E.

[0030] Reference will be made below to the choice of operating conditions of the burner with applied power values and air numbers, it being understood that the method can be applied in a similar manner with an alternative choice of parameters characterising the operating conditions, for example with applied power and CO2 (and/or CO) concentration values.

[0031] In a third step A3, a measurement is made, for example by means of a sampling, of the resulting voltage signal at the electrode E, calculating the respective parameters of the wave form of the response signal for each of said operating conditions applied to the burner.

[0032] In a further subsequent operating step, indicated by A4, an interpolation function or correlation table is calculated, indicated by F, based on the previously acquired data, suitable to allow the unequivocal interpolation or correlation of the power P, the air number λ and the characteristic parameters of the wave form of the response signal at the electrode E in the combustion process of the burner.

[0033] Conveniently, it is provided that in the operating step A2, in each preselected operating condition of the burner (Pi, λj), an impulsed periodic voltage signal S is applied to the electrode E and the trend over time of the resulting electrical voltage signal S' at the electrode is measured (measuring the dimensions of the characteristic values of the signal), once the application of the impulsed signal S has ceased.

[0034] The signal S comprises, over the signal period T, a first positive impulse N1 of preset amplitude, followed by a second negative impulse N2 of preset amplitude. The times of application of the impulses are preferably the same, for example in the order of approximately 10 milliseconds, the duration of the time interval between the first and second impulses being less than the duration of the time interval between the second impulse and a subsequent first impulse, the period of the signal S being selected appropriately, for example preferably in the order of 50 milliseconds to 1 second, and more preferably in the order of approximately 100 milliseconds. The amplitude of the impulse of the signal S is selected according to convenience and is preferably the same in terms of absolute value for both the impulses N1 and N2.

[0035] Alternatively, it can be provided that the impulsed signal S is not periodic. Figure 5 shows the trend of the voltage signal S' measured at the electrode E following the application of the first and second impulses. It has been observed that both the wave forms of the signal S' associated respectively with the first and the second impulse have a decreasing exponential trend in terms of absolute value relative to the ground potential, with different time constants for each of them.

[0036] The exponential trends of both the first and second sections of the curve of the signal S' (as responses respectively to the first and second impulses) are characterised by respective time constants τ₁ and τ₂ (or equivalently by respective gradients a₁, a₂ of the tangents at the origin of the respective exponential curves). The exponential curves can be expressed as follows:



where K₁ and K₂ are two constants and S₀ represents a residual voltage that has been observed in operating conditions and is therefore introduced into each of the exponential functions that characterise the response to the signal S applied to the electrode E.

[0037] Figure 2 shows schematically the trend of the correlation function F relating to the plotting of the data acquired in phase A. The graph illustrates, along the three Cartesian axes, the power (P), the time (t) and the signal S' obtained in the data acquisition phases. For example, for each power value P applied, the curves of each signal S' are reported (characterised by a pair of values for the time constants τ₁,τ₂), measured in the corresponding condition of the air number applied (Pi, λj).

[0038] Alternatively, the values assumed by the function F can be represented in the form of a correlation table, in which the values for the power P, air number λ and time constants τ₁ and τ₂ are correlated for each operating condition applied to the burner.

[0039] The correlation function or table F, obtained in phase A, therefore serves to correlate, in an unequivocal manner, the significant parameters of the combustion characteristics (power and air number) with the respective time constants of the characteristic exponential functions of the trend of the response signal S' measured at the electrode E in the combustion process of the burner.

[0040] This correlation function or table F is used, in the manner described below, to evaluate the combustion process in a real operating condition of the burner, in other words to derive the values of the significant parameters of the combustion process (for example, power and air number) by calculating the values of the time constants τ₁ and τ₂ that characterise the response signal S' to the signal S in that operating condition.

[0041] The second phase B provides for the following operating steps, for example designed to calculate the air number in a real operating condition of the burner.

[0042] One of the possible applications of the method may provide for phase A to be applied to a sample appliance or boiler in order to identify, by means of the correlation function or table, the relationship between the combustion parameters, while phase B is applied to the same or other appliances for verifying and if necessary correcting the combustion parameters in a real operating condition of the respective burner.

[0043] A first operating step, indicated by B1, provides for the application of the voltage signal S to the electrode E and for the acquisition, in a second operating step B2, of the electrical signal S' measured on the electrode after the application of the signal S, in a manner entirely similar to that described for phase A.

[0044] A third subsequent step B3 provides for the calculation of the time constants τ₁ and τ₂ (or equivalently the gradients a₁, a₂) that characterise the respective sections of the curve relating to the response signal S' to the impulsed signal S applied to the electrode E in the real operating condition.

[0045] From the calculated value of τ₂ it is possible to obtain, by means of the correlation function or table F, the power value Px at the burner that characterises the operating condition in question.

[0046] Figure 3 shows the bundle of parameterised curves with the air number (λ1, λ2, λ3,..., λn) that represent the trend of the constant τ₂ according to changes in the power at the burner. The graph of Figure 3 is therefore a different way of visualising the data present in the table or function F of Figure 2. It should be noted that the power P is relatively insensitive to changes in the air number λ, and it is therefore possible to estimate, with a good approximation, the power value Px (or a limited range of power values) to which the value assumed by the constant τ₂ corresponds. It may be provided that, for a certain value of the constant τ₂, the average value of the power values visible in the graph at τ₂ is calculated.

[0047] With the value of the constant τ₁, calculated in the operating step B3, on the other hand, the value of the air number λ is read by means of the function or table F.

[0048] Figure 4 shows the bundle of parameterised curves with the power value (P1, P2, ..., Pn) that represent the trend of the air number λ according to changes in the constant τ₁. The graph of Figure 4 therefore represents a different way of visualising the data present in the correlation table or function F of Figure 2.

[0049] In the graph of Figure 4, in order to correlate in an unequivocal manner the constant τ₁ with the air number λ (with reference to the corresponding power P), it is preferred to exclude the area of the graph relating to values of λ substantially less than 1.

[0050] Since it has been observed that for values of λ less than 1 the residual voltage assumes negative values sharply at odds with the assumed values for λ greater than 1 (in a residual voltage S' - air number λ graph, a stepped trend is seen in the residual voltage in the passage from values of λ < 1 to λ > 1), in the data acquisition phase A conditions corresponding to λ < 1 are also plotted, and a residual voltage threshold value is decided, beneath which incorrect combustion is recognised.

[0051] It follows from this that for the value of τ₁ calculated in step B3, the value of λ corresponding to the power Px previously read in the correlation function or table F can be read in the graph of Figure 4. The estimated value of the air number (λ_stim) that characterises the combustion process of the analysed real operating condition is then read. It is understood that the method has useful application even if one limits oneself only to identifying the power Px correlated with the value of the time constant τ₂ as explained in the preceding steps.

[0052] In addition, as mentioned previously, it is possible to refer in phase B to a correlation table, deriving therefrom the values for power (P_stim) and air number (λ_stim) correlated with the values of the tabulated time constants τ₁ and τ₂, which are therefore suitable for characterising the combustion process of the analysed real operating condition.

[0053] By means of the correlation function or table, a calculation is then made of the value of the air number (λ_stim) correlated with the combustion process of the operating condition of the burner. By comparing λ_stim with the target air number (λ_ob), i.e. the number suitable for ensuring correct and efficient combustion, it is possible to act on the control system of the burner (by acting on the fan and/or the gas modulating valve) in order to modify the conditions of the combustion process with the aim of approaching the target air number (λ_ob).

[0054] Since phenomena of drift may arise and affect the curves that characterise the correlation function or table F, for example caused by the electrode being positioned outside the tolerances or by degradation of the electrode due to ageing or wear, the method of the invention may provide for a calibration or recentring cycle, which may be based on observation of the ionisation current and/or on the values of the characteristic time constants τ₁ and τ₂ (or equivalently on the values of the respective gradients a₁, a₂).

[0055] The calibration cycle may, for example, provide for the burner to be made to operate with increasingly rich air/fuel mixtures, increasing the percentage of the gas flow delivered to the burner. In these conditions, the air number λ tends to gradually reduce from values >1 to values <1, passing via the condition of λ=1, in which the ionisation current is known to have a maximum value and the time constant τ₁ has a minimum value. The cycle provides that, based on the operating condition identified by λ=1 (where the maximum ionisation current or the minimum value of the characteristic constant τ₁ is measured), one begins to increase the quantity of air delivered, acting on the speed of the fan until a condition is reached in which the air flow is increased for example by 30%, reaching in this condition a correspondingly increased air number value (λ=1.3); when the time constant τ₁ is used, after identifying the minimum value of τ₁ for λ=1 it is possible to find the value of τ₁ corresponding to combustion at λ=1.3 by multiplying the value by a suitably identified constant.

[0056] With respect to this known operating condition, the curves of the correlation function or table F can then be recentred and calibrated, recovering any previously accumulated deviations or drifts.

[0057] Using the above method, it is also possible to diagnose conditions of the appliance that differ from the nominal conditions, for example caused by the electrode being positioned outside the tolerances or by degradation of the electrode due to ageing. To achieve this end it is sufficient to use, instead of λj, a suitable parameter that represents the condition of the appliance (nominal or anomalous) existing in the condition "j".

[0058] It should also be noted that, unlike the known methods for monitoring and controlling combustion, the method of the invention, based on voltage measurements, is not based on measurement of the ionisation current and is therefore less affected by problems arising from wear and ageing of the electrodes.

[0059] Another advantage is linked to the speed with which the response to the voltage signal applied to the electrode is obtained, which renders the method extremely rapid compared with the known solutions.

[0060] A further advantage resides in the fact that the electrode used in the method of the invention makes it possible to use quite low voltage potentials. This property makes the electrode less costly compared with the traditionally proposed solutions.

[0061] A further advantage is that the method of the invention advantageously provides for the use of a single electrode for applying the voltage signal in the flame and receiving the response signal.

[0062] A system for controlling and regulating combustion, for the burner 1, operating with the method of the invention, provides for example the following operating phases, with reference to the graph of Figure 6, where the abscissa expresses the number of revolutions (n) of the fan, the ordinates of the upper quadrant express the current (I) of actuation of the modulating gas valve, and the ordinates of the lower quadrant express the flow rate (Q) of gas delivered (correlated with the power need).

[0063] The curves C, C' of regulation of the above-mentioned parameters are typically preset in the control circuit, as illustrated in the diagram. Thus, for example, a number of revolutions n1 and a current I1 correspond to a need Q1.

[0064] If the power need changes from Q1 to Q2, the number of revolutions is increased to n2, in which condition the control circuit associates the current value 12 with the modulator. These values are correlated with a target air number (λ_ob) considered optimal for combustion. In this new operating condition, the effective air number (λ_stim) is calculated using the method described above, and a comparison is made between λ_ob and λ_stim, making the appropriate corrections to the parameters - current I - or - number of revolutions n - in order to obtain an air number essentially coincident with the target air number. Preferably, the current to the modulator is altered, for example by increasing it to the value I2'. At this point, the operating curve C is further updated for the air number equal to the target air number, and thus becomes the curve C'.

[0065] The updating of the regulation curve may for example be performed by accumulating a certain number of correction points and calculating the regression curve that correlates with them, said curve becoming the new regulation curve. Alternatively, it is possible to perform exclusively a correction, where appropriate, on each operating point, based on the comparison - λ_ob / λ_stim - without identifying a new operating curve (by means of linear regression).

[0066] The regulation system described above represents simply a non-limitative example for the application of the combustion monitoring and control system of the invention. It is understood that by this method it is possible to provide specific logics for controlling and regulating the burner according to the respective operating and system needs, said logics providing for a comparison between a target air number, optimal for combustion, and the air number calculated by the method of the invention.

[0067] The invention therefore achieves the proposed aims, overcoming the limitations pointed out with respect to the prior art, demonstrating the advantages described with respect to the known solutions.

Claims

1. Method for monitoring and controlling combustion in a premix combustible gas burner (1) with fan, of the type comprising a sensor with an electrode (E) placed in the flame or in the proximity thereof and suitable for being powered by a voltage generator as well as being connected to an electronic circuit suitable of measuring the resulting potential at the electrode,
said method comprising:

- a first phase of acquisition and processing of data from a series of combustion conditions of the burner, comprising the following steps:

identifying a plurality of combustion conditions of the burner (1), in each of said conditions

- applying in the burner a power (P1, P2, ...., Pn) deriving from the combustion of a corresponding flow rate of combustible mixture, and applying for each power an air number value (λ1, λ2, ...., λm), said air number expressing the ratio between the quantity of air in the combustion process and the quantity of air for stoichiometric combustion,

- applying, in each of said (n * m) test conditions (Pi, λj), an impulsed electrical voltage signal (S) to said electrode (E) and measuring the trend over time of the resulting electrical signal (S') at the electrode, once the application of the impulsed signal (S) has ceased, said signal applied to the electrode (E) comprising, in the period of the signal (S), a first impulse (N1) of positive amplitude, followed by a second impulse (N2) of negative amplitude,

- identifying, for each of said combustion conditions, the curve of the trend over time of the response signal (S') at the electrode (E), said trend being expressed for each impulse (N1, N2) by an exponential function decreasing over time in absolute terms,

- calculating, for a first section of the curve relating to the first impulse (N1), as well as for a second curve section relating to the second impulse (N2), the respective first and second time constants (τ₁, τ₂), characteristic of the exponential trend for the respective first and second curve sections,

- thus obtaining an interpolation function or correlation table (F), based on the acquired test data, suitable for unequivocally interpolating or correlating at least one significant parameter of the combustion characteristics (power or air number) with the respective time constants of the exponential functions characteristic of the trend in the response signal measured at the electrode, in the combustion process of the burner,

- said method comprising a second phase of calculating the air number (λ) in a real operating condition of the burner, comprising the following steps:

- acquiring in said operating condition the electrical response signal measured on the electrode after the application of the impulsed signal,

- calculating, for said operating condition of the burner, said first and second time constants (τ₁, τ₂) characteristic of the respective curve sections relating to the trend in the resulting voltage signal at the electrode, following the application of the said impulsed signal,

- calculating the estimated value of the air number (λ_stim) by using the interpolation function or correlation table (F) which correlates the power (P) and the air number (λ) with the time constants (τ₁, τ₂) characteristic of the curve relating to the trend in the response signal (S') measured at the electrode (E).

2. Method according to claim 1, in which provision is made, in the said second phase, for preliminarily obtaining the power value (Px) characteristic of the operating condition of the burner, by introducing into said interpolation function or correlation table (F) the value of the second time constant (τ₂) calculated for said operating condition, and for subsequently obtaining the estimated value of the air number (λ_stim) for said operating condition, by introducing into the said interpolation function or correlation table (F) the power value (Px) and the value of the first time constant (τ₁) calculated for said operating condition.

3. Method according to claim 1 or 2, in which the impulsed signal (S) applied to the electrode (E) is periodic.

4. Method according to one of the preceding claims, wherein provision is made for recording the value of a residual voltage (S₀), in order to express the exponential function of the response signal (S') at the electrode (E) relative to the time constants (τ₁, τ₂).

5. Method according to one of the preceding claims, said burner comprising:

- a combustion chamber,

- a first pipe suitable for introducing air into said combustion chamber,

- first regulation means associated with said first pipe, suitable for varying the quantity of air introduced into said first pipe,

- a second pipe suitable for introducing a combustible gas into said combustion chamber,

- second regulation means associated with said second pipe, suitable for varying the quantity of gas introduced into said second pipe;

said method comprising the additional phases of:

- setting one of said first and second regulation means to a first setting value,

- associating, on the basis of regulation curves preset in the control circuit, a corresponding setting value for the other regulation means, said values being correlated with a target air number (λ_ob) considered optimal for combustion,

- calculating, in the operating condition achieved, the actual value of the air number (λ_stim) by using the method of one or more of the preceding claims,

- comparing the target air number (λ_ob) with the actual air number (λ_stim) and correcting one and/or the other of the said first and second regulation means in such a way as to obtain an actual air number (λ_stim) essentially coincident with the target air number (λ_ob).

6. Method according to claim 5, wherein said first regulation means comprise a fan with a preselected regulation curve (number of revolutions - air flow), and said second regulation means comprise a gas valve of the modulating type with a preselected regulation curve (current - gas flow), said setting values being the speed of the fan and/or the pilot current of the valve modulator

7. System for controlling combustion in a premix combustible gas burner (1) with fan of a combustible gas appliance, comprising a sensor (8) arranged in the proximity of the burner flame with an electrode (E) placed in the flame or in the proximity thereof and suitable for being powered by a voltage generator as well as connected to an electronic circuit suitable of measuring the resulting potential at the electrode (E), said system operating according to the method of one or more of the preceding claims.

Ansprüche

1. Verfahren zum Überwachen und Steuern einer Verbrennung in einem Vormisch-Gasbrenner (1) mit Gebläse des Typs, der einen Sensor mit einer Elektrode (E) aufweist, die in der Flamme oder in der zugehörigen Umgebung angeordnet ist, und durch einen Spannungsgenerator angetrieben wird sowie mit einer elektronischen Schaltung verbunden ist, die zum Messen des resultierenden Potentials an der Elektrode geeignet ist,
wobei das Verfahren aufweist:

- eine erste Phase zur Erfassung und Verarbeitung von Daten aus einer Reihe von Verbrennungsbedingungen des Brenners, die folgende Schritte aufweist:

- Identifizieren einer Mehrzahl von Verbrennungsbedingungen des Brenners (1), wobei jede der Bedingungen aufweist:

- Anlegen einer Stromversorgung (P1, P2, ..., Pn) im Brenner, die von der Verbrennung einer entsprechenden Durchflussmenge einer brennbaren Mischung abgeleitet wird, und für jeden Strom Anlegen eines Luftzahlenwerts (λ₁, λ₂, ..., λ_m), wobei die Luftzahl das Verhältnis zwischen der Luftmenge im Verbrennungsprozess und der Luftmenge für eine stöchiometrische Verbrennung ausdrückt,

- in jeder der (n*m) Testbedingungen (Pi, λj) Anlegen eines elektrischen Impuls-Spannungssignals (S) an der Elektrode (E) und Messen des Trends im Laufe der Zeit des resultierenden elektrischen Signals (S') an der Elektrode, sobald das Anlegen des Impulssignals (S) beendet ist, wobei das Signal, das an der Elektrode (E) angelegt ist, in der Periode des Signals (S) einen ersten Impuls (N1) einer positiven Amplitude, gefolgt von einem zweiten Impuls (N2) einer negativen Amplitude, aufweist,

- für jede der Verbrennungsbedingungen Identifizieren der Kurve des Trends im Laufe der Zeit des Antwortsignals (S') an der Elektrode (E), wobei der Trend für jeden Impuls (N1, N2) durch eine Exponentialfunktion, die im Laufe der Zeit in absoluten Zahlen abnimmt, ausgedrückt wird,

- Berechnen der jeweiligen ersten und zweiten Zeitkonstanten (τ₁, τ₂) für einen ersten Abschnitt der Kurve, der sich auf den ersten Impuls (N1) bezieht, sowie für einen zweiten Kurvenabschnitt, der sich auf den zweiten Impuls (N2) bezieht, die für den Exponentialtrend für die jeweiligen ersten und zweiten Kurvenabschnitte charakteristisch sind,

- dadurch Erhalten einer Interpolationsfunktion oder einer Korrelationstabelle (F) auf der Basis der erfassten Testdaten, die für ein eindeutiges Interpolieren oder Korrelieren von zumindest einem Signifikanten Parameter der Verbrennungscharakteristiken (Strom oder Luftzahl) mit den jeweiligen Zeitkonstanten der Exponentialfunktionen, die charakteristisch für den Trend im Antwortsignal, das an der Elektrode gemessen wird, im Verbrennungsprozess des Brenners sind,

- wobei das Verfahren eine zweite Phase zum Berechnen der Luftzahl (λ) in einer realen Betriebsbedingung des Brenners aufweist, mit folgenden Schritten:

- Erfassen des elektrischen Antwortsignals in der Betriebsbedingung, das an der Elektrode nach dem Anlegen des Impulssignals gemessen wird,

- Berechnen für die Betriebsbedingung des Rechners der ersten und zweiten Zeitkonstanten (τ₁, τ₂), die für die jeweiligen Kurvenabschnitte bezüglich des Trends im resultierenden Spannungssignal an der Elektrode, im Anschluss an das Anlegen des Impulssignals, charakteristisch sind,

- Berechnen des geschätzten Werts der Luftzahl (λ_stim) unter Verwendung der Interpolationsfunktion oder einer Korrelationstabelle (F), die den Strom (P) und die Luftzahl (λ) mit den Zeitkonstanten (τ₁, τ₂) korreliert, die für die Kurve bezüglich des Trends im Antwortsignal (S'), das an der Elektrode (E) gemessen wird, charakteristisch sind.

2. Verfahren gemäß Anspruch 1, in dem eine Festlegung in der zweiten Phase zum vorläufigen Erhalten des Stromwerts (Px), der charakteristisch für die Betriebsbedingung des Brenners ist, durch Einführen in die Interpolationsfunktion oder Korrelationstabelle (F) des Werts der zweiten Zeitkonstante (τ₂), die für diese Betriebsbedingung berechnet wird, und zum nachfolgenden Erhalten des geschätzten Werts der Luftzahl (λ_stim) für den Betriebszustand durch Einführen in die Interpolationsfunktion oder Korrelationstabelle (F) des Stromwerts (Px) und des Werts der ersten Zeitkonstante (τ₁), das für die Betriebsbedingung berechnet wird, vorgesehen ist.

3. Verfahren gemäß Anspruch 1 oder 2, in dem das Impulssignal (S), das an der Elektrode (E) angelegt ist, periodisch ist.

4. Verfahren gemäß einem der vorhergehenden Ansprüche, wobei eine Festlegung zum Aufzeichnen des Werts einer Restspannung (S₀) vorgesehen ist, um die Exponentialfunktion des Antwortsignals (S') an der Elektrode (E) bezüglich der Zeitkonstanten (τ₁, τ₂) auszudrücken.

5. Verfahren gemäß einem der vorhergehenden Ansprüche, wobei der Brenner aufweist:

- eine Verbrennungskammer,

- eine erste Leitung, die zum Einleiten von Luft in die Verbrennungskammer geeignet ist,

- eine erste Reguliereinrichtung, die mit der ersten Leitung in Verbindung ist, die zum Ändern der Luftmenge geeignet ist, die in die erste Leitung eingeleitet wird,

- eine zweite Leitung, die zum Einleiten eines Brenngases in die Verbrennungskammer geeignet ist,

- eine zweite Reguliereinrichtung, die mit der zweiten Leitung in Verbindung ist, die zum Ändern der Gasmenge geeignet ist, die in die zweite Leitung eingeleitet wird,

- wobei das Verfahren die zusätzlichen Phasen aufweist:

- Einstellen einer der ersten oder zweiten Reguliereinrichtungen auf einen ersten Einstellwert,

- Zuordnen, auf der Basis von Regelkurven, die in der Steuerschaltung voreingestellt sind, eines entsprechenden Einstellwerts für die andere Reguliereinrichtung, wobei die Werte mit einer Soll-Luftzahl (λ_ob), die für eine Verbrennung als optimal betrachtet wird, korreliert werden,

- Berechnen, in der erreichten Betriebsbedingung, des tatsächlichen Werts der Luftzahl (λ_stim) unter Verwendung des Verfahrens von einem oder mehreren der vorhergehenden Ansprüche,

- Vergleichen der Soll-Luftzahl (λ_ob) mit der tatsächlichen Luftzahl (λ_stim) und Korrigieren der einen und/oder der anderen der ersten und zweiten Reguliereinrichtungen in der Weise, um eine tatsächliche Luftzahl (λ_stim) zu erhalten, die im Wesentlichen mit der Soll-Luftzahl (λ_ob) übereinstimmt.

6. Verfahren gemäß Anspruch 5, wobei die erste Reguliereinrichtung ein Gebläse mit einer vorgewählten Regelkurve (Drehzahl - Luftstrom) aufweist, und die zweite Reguliereinrichtung ein Gas-Steuerventil mit einer vorgewählten Regelkurve (Strom - Gasstrom) aufweist, wobei die Einstellwerte die Drehzahl des Gebläses und/oder der Steuerstrom des Ventilmodulators sind.

7. System zum Steuern einer Verbrennung in einem Vormisch-Gasbrenner (1) mit Gebläse einer Brenngasvorrichtung, die einen Sensor (8), der in der Umgebung der Gasflamme angeordnet ist, mit einer Elektrode (E) aufweist, die in der Flamme oder in der zugehörigen Umgebung angeordnet ist, und durch einen Spannungsgenerator angetrieben wird sowie mit einer elektronischen Schaltung verbunden ist, die zum Messen des resultierenden Potentials an der Elektrode (E) geeignet ist, wobei das System gemäß dem Verfahren eines oder mehrerer der vorhergehenden Ansprüche betrieben wird.

Revendications

1. Procédé pour surveiller et commander une combustion dans un brûleur à gaz combustible à prémélange (1) avec un ventilateur, du type comprenant un capteur avec une électrode (E) placée dans la flamme ou à proximité de celle-ci et approprié pour être alimenté en énergie par un générateur de tension ainsi que pour être connecté à un circuit électronique approprié pour mesurer le potentiel résultant au niveau de l'électrode,
ledit procédé comprenant :

- une première phase d'acquisition et de traitement de données à partir d'une série de conditions de combustion du brûleur, comprenant les étapes suivantes :

l'identification d'une pluralité de conditions de combustion du brûleur (1), dans chacune desdites conditions

- l'application dans le brûleur d'une puissance (P1, P2, ..., Pn) dérivée de la combustion d'un débit correspondant de mélange combustible, et l'application pour chaque puissance d'une valeur numérique d'air (λ1, λ2, ..., λn), ledit nombre d'air exprimant le rapport entre la quantité d'air dans le processus de combustion et la quantité d'air pour une combustion stoechiométrique,

- l'application, dans chacune desdites conditions d'essai (n * m) (Pi, λj), d'un signal de tension électrique pulsé (S) à ladite électrode (E) et la mesure de la tendance dans le temps du signal électrique résultant (S') au niveau de l'électrode, une fois que l'application du signal pulsé (S) a cessé, ledit signal appliqué à l'électrode (E) comprenant, dans la période du signal (S), une première impulsion (N1) d'amplitude positive, suivie par une seconde impulsion (N2) d'amplitude négative,

- l'identification, pour chacune desdites conditions de combustion, de la courbe de la tendance dans le temps du signal de réponses (S') au niveau de l'électrode (E), ladite tendance étant exprimée pour chaque impulsion (N1, N2) par une fonction exponentielle décroissant dans le temps en termes absolus,

- le calcul, pour une première section de la courbe liée à la première impulsion (N1), ainsi que pour une seconde section de courbe liée à la seconde impulsion (N2), des première et seconde constantes de temps respectives (τ₁, τ₂), caractéristiques de la tendance exponentielle pour les première et seconde sections de courbe respectives,

- ainsi, l'obtention d'une fonction d'interpolation ou d'une table de corrélation (F), sur la base des données d'essai acquises, appropriée pour interpoler et mettre en corrélation explicitement au moins un paramètre significatif des caractéristiques de combustion (puissance ou nombre d'air) avec les constantes de temps respectives des fonctions exponentielles caractéristiques de la tendance dans le signal de réponse mesuré au niveau de l'électrode, dans le processus de combustion du brûleur,

- ledit procédé comprenant une seconde phase de calcul du nombre d'air (λ) en condition de fonctionnement réel du brûleur, comprenant les étapes suivantes :

- l'acquisition dans ladite condition de fonctionnement du signal de réponse électrique mesuré sur l'électrode après l'application du signal pulsé,

- le calcul, pour ladite condition de fonctionnement du brûleur, desdites première et seconde constantes de temps (τ₁, τ₂) caractéristiques des sections de courbe respectives liées à la tendance dans le signal de tension résultant au niveau de l'électrode, suivant l'application dudit signal pulsé,

- le calcul de la valeur estimée du nombre d'air (λ_stim) en utilisant la fonction d'interpolation ou la table de corrélation (F) qui met en corrélation la puissance (P) et le nombre d'air (λ) avec les constantes de temps (τ1, τ2) caractéristiques de la courbe liée à la tendance dans le signal de réponse (S') mesuré au niveau de l'électrode (E).

2. Procédé selon la revendication 1, dans lequel il est prévu, dans ladite seconde phase, l'obtention préalable de la valeur de puissance (Px) caractéristique de la condition de fonctionnement du brûleur, par l'introduction dans ladite fonction d'interpolation ou table de corrélation (F) de la valeur de la seconde constante de temps (τ2) calculée pour ladite condition de fonctionnement, et l'obtention ultérieure de la valeur estimée du nombre d'air (λ_stim) pour ladite condition de fonctionnement, par l'introduction dans ladite fonction d'interpolation ou table de corrélation (F) de la valeur de puissance (Px) et de la valeur de la première constante de temps (τ1) calculée pour ladite condition de fonctionnement.

3. Procédé selon la revendication 1 ou 2, dans lequel le signal pulsé (S) appliqué à l'électrode (E) est périodique.

4. Procédé selon l'une quelconque des revendications précédentes, dans lequel il est prévu l'enregistrement de la valeur d'une tension résiduelle (S₀), afin d'exprimer la fonction exponentielle du signal de réponses (S') au niveau de l'électrode (E) par rapport aux constantes de temps (τ1, τ2).

5. Procédé selon l'une quelconque des revendications précédentes, ledit brûleur comprenant :

- une chambre de combustion,

- un premier tuyau approprié pour introduire de l'air à l'intérieur de ladite chambre de combustion,

- un premier moyen de régulation associé audit premier tuyau, approprié pour faire varier la quantité d'air introduite à l'intérieur dudit premier tuyau,

- un second tuyau approprié pour introduire un gaz combustible à l'intérieur de ladite chambre de combustion,

- un second moyen de régulation associé audit second tuyau, approprié pour faire varier la quantité de gaz introduite à l'intérieur dudit second tuyau,

ledit procédé comprenant les phases supplémentaires suivantes :

- le réglage de l'un desdits premier et second moyens de régulation sur une première valeur de réglage,

- l'association, sur la base des courbes de régulation préréglées dans le circuit de commande, d'une valeur de réglage correspondante pour l'autre moyen de régulation, lesdites valeurs étant mises en corrélation avec un nombre d'air cible (λ_ob) considéré comme optimal pour la combustion,

- le calcul, dans la condition de fonctionnement obtenue, de la valeur réelle du nombre d'air (λ_stim) en utilisant le procédé de l'une ou plusieurs des revendications précédentes,

- la comparaison du nombre d'air cible (λ_ob) avec le nombre d'air réel (λ_stim) et la correction d'un et/ou de l'autre desdits premier et second moyens de régulation de manière à obtenir un nombre d'air réel (λ_stim) qui coïncide essentiellement avec le nombre d'air cible (λ_ob).

6. Procédé selon la revendication 5, dans lequel ledit premier moyen de régulation comprend un ventilateur avec une courbe de régulation présélectionnée (nombre de tours - écoulement d'air), et ledit second moyen de régulation comprend une soupape de gaz du type à modulation avec une courbe de régulation présélectionnée (courant - écoulement de gaz), lesdites valeurs de réglage étant la vitesse du ventilateur et/ou le courant pilote du modulateur à soupape.

7. Système pour commander une combustion dans un brûleur à gaz combustible à prémélange (1) avec un ventilateur d'un appareil à gaz combustible, comprenant un capteur (8) agencé à proximité de la flamme du brûleur avec une électrode (E) placée dans la flamme ou à proximité de celle-ci et approprié pour être alimenté en énergie par un générateur de tension ainsi que connecté à un circuit électronique approprié pour mesurer le potentiel résultant au niveau de l'électrode (E), ledit système fonctionnant selon le procédé de l'une ou plusieurs des revendications précédentes.

Drawing