Patent Application
20180031233
The present disclosure relates to a gas analysis device for analyzing a gas concentration distribution and a temperature distribution inside a furnace, a control system and a control assistance system for a combustion facility provided with the gas analysis device, and a gas analysis method performed by the gas analysis device.
In a combustion facility such as a boiler for combusting fuel and a garbage incinerator for combusting garbage, high-temperature combustion air (gas) is produced from combustion of substances in the furnace. In a combustion facility, it is desirable to measure a gas concentration distribution and a temperature distribution inside the furnace to optimize or monitor the combustion state. Such a gas concentration distribution and a temperature distribution inside the furnace can be normally obtained at a certain level of accuracy through actual measurement at some points in the furnace if the gas concentration and the temperature are uneven and the size of the furnace is relatively small. However, if the furnace is extensive, there is only a limited number of methods for measurement. A known type of such measurement method is to calculate a gas concentration and a temperature as a two-dimensional distribution, by analyzing a cumulative value of an absorption amount of laser light with a computation processing device like a computer, in a plurality of measurement paths in which laser light is emitted so as to transmit through combustion gas inside the furnace from a plurality of laser ports provided for the furnace.
In this method, an analysis parameter is set for each of the measurement paths for laser emission. Thus, to improve the analysis accuracy, it is necessary to provide a sufficient number of laser ports. However, an actual combustion facility such as a boiler is equipped with piping that carries a fluid (coolant water) to be heated by combustion air inside the furnace, and the piping is arranged along the inner wall of the furnace. Thus, only a limited number of laser ports can be provided.
Patent Document 1 discloses a solution to the above problem. In Patent Document 1, mesh division is performed on the two-dimensional space inside the furnace to be laser-measured, and a gas concentration value is calculated on the basis of the laser absorption amount in each mesh. Then, assuming that the distribution of gas concentration in each mesh is the continuous Gausian Process (GP), a solution is sought by the Bayesian method to obtain the gas concentration distribution. As described above, in Patent Document 1, the condition of continuity is required to be satisfied, and thereby a reliable analysis result can be obtained even if there is a small number of analysis parameters.
Patent Document 1: JP2006-522938A (translation of a PCT application)
Concentration measurement that uses laser light as in Patent Document 1 is based on the absorption amount that depends on electronic level transition that corresponds to components contained in combustion air. The laser absorption amount has a characteristic of depending not only on the concentration but also on the temperature of combustion air. According to Patent Document 1, a concentration distribution close to an actual one is obtained by imposing the condition of continuity on a concentration distribution obtained on the basis of the laser absorption amount. However, in the process of deriving the concentration out from the laser absorption amount, the dependence of the laser absorption amount on the temperature is not taken into consideration, which may prevent achievement of a sufficient analysis accuracy.
At least one embodiment of the present invention was made in view of the above described problem, and an object is to provide a gas analysis device for accurately analyzing a gas concentration distribution and a temperature distribution in a system in which combustion gas inside a furnace is not evenly mitigated, a control system and a control assistance system for a combustion facility, and a gas analysis method.
(1) To solve the above problem, a gas analysis device according to at least one embodiment of the present invention is for analyzing a concentration distribution of a combustion gas in a furnace and a temperature distribution inside the furnace, and the gas analysis device comprises: a measurement part configured to measure an absorption amount of a laser light including an absorption wavelength corresponding to at least two electronic level transitions having the same component contained in the combustion gas, by emitting the laser light on a plurality of measurement paths disposed so as to pass through the combustion gas; a standard setting part configured to set a standard gas concentration distribution and a standard temperature distribution on the basis of a measurement result of the measurement part; and an analysis part configured to obtain the gas concentration distribution and the temperature distribution by solving a function including the gas concentration distribution and the temperature distribution as variables so as to minimize a difference between the absorption amount measured by the measurement part and a standard absorption amount obtained on the basis of the standard gas concentration distribution and the standard temperature distribution.
With the above configuration (1), when obtaining the gas concentration distribution and the temperature distribution on the basis of the absorption amount of the laser light in the plurality of measurement paths passing through the combustion gas, the gas concentration distribution and the temperature distribution are obtained by solving a function including the gas concentration distribution and the temperature distribution as variables by numerical analysis so as to minimize a difference between the absorption amount measured by the measurement part and a standard absorption amount obtained on the basis of the standard distribution set by the standard setting part. Such a function includes the concentration distribution and the temperature distribution as a common variable, and thus can reflect the correlation between the concentration and the temperature, which is an actual phenomenal background. Thus, it is possible to obtain an analysis solution closer to the actual distribution, and to distinguish the effects of the gas concentration and the temperature on the absorption amount (for instance, it is possible to distinguish a decrease in the absorption amount due to a temperature increase from a decrease in the absorption amount due to a gas-concentration decrease). As described above, according to the present embodiment, even in a situation in which only a limited number of laser ports can be disposed in the furnace, it is possible to obtain a gas concentration distribution and a temperature distribution closer to those of the actual system taking into consideration the temperature dependency of the absorption amount of the laser light.
(2) In some embodiments, in the above configuration (1), the function is set corresponding to a shape of the furnace.
With the above configuration (2), using a function corresponding to the shape of the furnace containing combustion gas to be analyzed makes it possible to seek a solution closer to an actual value efficiently when solving the function during analysis.
(3) In some embodiments, in the above configuration (2), the function is set so as to include at least one of a center axis position, a coordinate ovalization rate, or a circumferential distribution term as a parameter, with respect to a cylindrical coordinate system.
With the above configuration (3), the shape of the furnace is determined with the above parameters, and thus it is possible to express the gas concentration distribution and the temperature distribution with fewer parameters. Accordingly, the computation load for solving the function is reduced, and it is possible to seek a solution closer to the actual system efficiently.
(4) In some embodiments, in any one of the above configurations (1) to (3), the standard setting part is configured to set the standard concentration distribution and the standard temperature distribution on the basis of an average temperature of the combustion gas obtained on the basis of a ratio of the absorption amount at wavelengths corresponding to different electronic level transitions included in the laser light in the plurality of measurement paths.
With the above configuration (4), an average temperature inside the furnace is calculated on the basis of the laser absorption amount in the plurality of measurement paths, and the standard concentration distribution and the standard temperature distribution are set on the basis of the average temperature. The standard concentration distribution and the standard temperature distribution set as described above serve as initial values suitable for seeking a final solution efficiently when the function is solved by numerical analysis. For instance, the standard temperature distribution may be set as a situation in which the temperature distribution in the furnace is in relaxation at the average temperature obtained as described above. Alternatively, a gradient may be applied to the distribution if the Marquardt method is used for the convergence analysis calculation.
(5) In some embodiments, in the above configuration (4), the same component is H2O.
With the above configuration (5), compared to O2, CO2, and the like, H2O has an absorption wavelength range corresponding to adjacent two electronic level transitions in a relatively close range. Thus, if the wavelength of the laser light is scanned by controlling a driving current of a laser diode of a wavelength sweep type, it is possible to cover adjacent two electronic level transitions within the sweep range of a single laser diode, which makes it possible to simplify the device configuration.
(6) To solve the above problem, a control system for a combustion facility according to at least one embodiment of the present invention comprises: a fuel supply unit configured to supply fuel to the furnace; an air supply unit configured to supply air to the furnace; the gas analysis device according to any one of the above (1) to (5); and a control unit configured to control a supply amount of the fuel and the air to the furnace by adjusting the fuel supply unit and the air supply unit on the basis of the gas concentration distribution and the temperature distribution analyzed by the gas analysis device.
With the above configuration (6), the fuel supply unit and the air supply unit are adjusted on the basis of the gas concentration distribution and the temperature distribution obtained by gas analysis in the furnace, and thereby it is possible to control the amount of fuel and air to the furnace. Accordingly, it is possible to achieve an optimum operation in which the temperature unbalance of combustion gas and excess/shortage of oxygen supply in the furnace are solved, and to improve the power generation efficiency and suppress an increase in the NOx generation due to excessive O2.
(7) To solve the above problem, a control assistant system for a combustion facility according to at least one embodiment of the present invention comprises: a fuel supply unit configured to supply fuel to the furnace; an air supply unit configured to supply air to the furnace; the gas analysis device according to any one of claims 1 to 5; and a display unit configured to display the gas concentration distribution and the temperature distribution analyzed by the gas analysis device.
With the above configuration (7), the analysis result of the gas analysis device is visualized through display on a display unit such as a display monitor, thus making it possible for an operator of the combustion facility to easily determine the combustion state inside the furnace, and thereby it is possible to improve the efficiency of the operator's work to adjust the fuel condition.
(8) To solve the above problem, a gas analysis method for analyzing a concentration distribution of combustion gas and a temperature distribution inside a furnace, according to at least one embodiment of the present invention, comprises: a measurement step of measuring an absorption amount of a laser light including an absorption wavelength corresponding to at least two electronic level transitions having the same component contained in the combustion gas, by emitting the laser light on a plurality of measurement paths disposed so as to pass through the combustion gas; a standard setting step of setting a standard gas concentration distribution and a standard temperature distribution on the basis of a measurement result in the measurement step; and an analysis step of obtaining the gas concentration distribution and the temperature distribution by solving a function including the gas concentration distribution and the temperature distribution as variables so as to minimize a difference between the absorption amount measured in the measurement step and a standard absorption amount obtained on the basis of the standard gas concentration distribution and the standard temperature distribution.
The above method (8) can be suitably performed by the above described gas analysis device (including the above various configurations).
According to at least one embodiment of the present embodiment, it is possible to provide a gas analysis device for accurately analyzing a gas concentration distribution and a temperature distribution in a system in which combustion gas inside a furnace is not evenly mitigated, a control system and a control assistance system for a combustion facility, and a gas analysis method.
Embodiments of the present invention will now be described in detail with reference to the accompanying drawings. It is intended, however, that unless particularly specified, dimensions, materials, shapes, relative positions and the like of components described in the embodiments shall be interpreted as illustrative only and not intended to limit the scope of the present invention.
For instance, an expression of relative or absolute arrangement such as “in a direction”, “along a direction”. “parallel”, “orthogonal”, “centered”, “concentric” and “coaxial” shall not be construed as indicating only the arrangement in a strict literal sense, but also includes a state where the arrangement is relatively displaced by a tolerance, or by an angle or a distance whereby it is possible to achieve the same function.
Further, for instance, an expression of a shape such as a rectangular shape or a cylindrical shape shall not be construed as only the geometrically strict shape, but also includes a shape with unevenness or chamfered corners within the range in which the same effect can be achieved.
On the other hand, an expression such as “comprise”, “include”, “have”, “contain” and “constitute” are not intended to be exclusive of other components.
With reference to
The combustion facility 1 includes a combustion furnace 2 for combusting fuel, a flue 4 for guiding combustion air produced in the furnace 2, a re-heating unit 6 for obtaining thermal energy from the combustion air, a combustion controller 8 for controlling a combustion state inside the furnace 2 by adjusting supply of fuel and air to the furnace 2, and a gas analysis device 10 which analyzes the combustion air (gas) in the furnace 2.
The furnace 2 is configured to be surrounded by a wall surface comprising a heat resistant material in a substantially box shape. In the furnace 2, fuel and air supplied from the combustion controller 8 described below is combusted, and thereby high-temperature combustion air is produced. The furnace 2 has an upper side, in the vertical direction, open, and the open side is connected to the flue 4. The high-temperature combustion air produced in the furnace 2 forms a flow path so as to be guided into the flue 4.
The re-heating unit 6 comprises a plurality of re-heaters, and is disposed in the flow path of the combustion air in the furnace 2 and the flue 4. A re-heater comprises a piping member, and a liquid or a gas is sealed inside the piping member. The liquid or gas sealed inside the re-heater obtains thermal energy through heat exchange with high-temperature combustion air, and thereby turns into steam. The steam travels along a predetermined path from the re-heating unit 6, and rotary-drives a non-depicted turbine, thereby converting thermal energy into electrical energy or mechanical energy and outputting the converted energy.
As described above, the combustion facility 1 functions as a generator or a driving machine. However, the usage of the combustion facility 1 is not limited to this, and may be a heater for heating a substance with thermal energy obtained by the re-heating unit 6.
The combustion controller 8 controls a combustion state inside the furnace 2 by adjusting fuel and air supplied to the furnace 2. The combustion controller 8 includes a fuel supply unit 12 and an air supply unit 14 for supplying fuel and air, respectively, to the furnace 2.
The fuel supply unit 12 includes a powdered-coal burner 16 (hereinafter, referred to as “burner” when needed) for combusting fuel, a powdered-coal supply part 18 for supplying a powdered coal that serves as a fuel, a blower 20 for generating a wind for carrying the fuel, a flow-rate adjustment valve 22 for adjusting the flow rate of the fuel, and a pipe 24 connecting the above to one another.
The powdered-coal supply part 18 is a mechanism configured to supply fuel to the pipe 24. The powdered-coal supplied to the pipe 24 is carried through the pipe 24 by the blower 20, and mixed with air introduced from a main pipe 32 of the air supply unit 14 via the flow-rate adjustment valve 22, before being supplied to the burner 16. The burner 16 is a combustor disposed so as to have a nozzle exposed inside the furnace 2. The burner 16 injects a fuel supplied via the pipe 24 and combusts the fuel inside the furnace 2.
The burner 16 is disposed at a plurality of positions inside the furnace 2, preferably in such a layout that air injected from each burner 16 forms a swirling air flow inside the furnace 2.
The powdered-coal supply part 18 may be a mechanism that produces powdered coal by pulverizing coal and supplies the powdered coal to the pipe 24, or a mechanism that stores a powdered coal produced in advance and supplies the stored powdered coal to the pipe 24.
The air supply unit 14 includes a primary-air supply unit 26 and a secondary-air supply unit 28 for supplying primary air and secondary air, respectively, to the furnace 2, a blower 30 which is a blower or a fan for sending air to the primary-air supply unit 26 and the secondary-air supply unit 28 with the above described fuel supply unit 12, and a main pipe 32 connecting the above to one another.
The primary-air supply unit 26 includes a first pipe 36 disposed so that an outlet 34 is exposed inside the furnace 2, and a flow-rate adjustment valve 38 configured to adjust the flow rate of air in the first pipe 36. The first pipe 36 is connected to the main pipe 32 via the flow-rate adjustment valve 38, and is configured to be capable of introducing air taken into the main pipe 32 by the blower 30 to the outlet 34. The outlet 34 is disposed downstream of the burner 16, in the flow path of the combustion air inside the furnace 2. The flow-rate adjustment valve 38 is disposed at a connection part between the main pipe 32 and the first pipe 36, to adjust the amount of air to be supplied to the first pipe 36 from the main pipe 32.
The secondary-air supply unit 28 includes a second pipe 42 disposed so that an outlet 40 is exposed inside the furnace 2, and a flow-rate adjustment valve 44 configured to be capable of adjusting the flow rate of air in the second pipe 42. The second pipe 42 is connected to the main pipe 32 via the flow-rate adjustment valve 44, and is configured to be capable of introducing air taken into the main pipe 32 by the blower 30 to the outlet 40. The outlet 40 is disposed downstream of the outlet 34, in the flow path of the combustion air inside the furnace 2. The flow-rate adjustment valve 44 is disposed at a connection part between the main pipe 32 and the second pipe 42, and adjusts the amount of air to be supplied to the second pipe 42 from the main pipe 32.
The distribution control unit 46 adjusts the opening degrees of the flow-rate adjustment valves 22, 38, 44, and thereby distributes air taken in by the blower 30 to the fuel supply unit 12, the primary-air supply unit 26, and the secondary-air supply unit 28 at a predetermined ratio. In the present embodiment, the distribution control unit 46 is configured to be controlled automatically on the basis of a control signal from an infrared measurement analysis unit disposed in a control chamber.
With the above configuration, as depicted in
Referring again to
A measurement laser light transmitting system 60 and a measurement laser light receiving system 62 are disposed on opposite positions inside the furnace 2, so that laser light emitted from the measurement laser light transmitting system 60 transmits through the combustion air in the furnace 2 is received by the measurement laser light receiving system 62. Particularly in the present embodiment, the measurement laser light transmitting system 60 and the measurement laser light receiving system 62 are disposed on a two-dimensional plane substantially along the horizontal direction at the downstream side of the outlet 40, and thereby the combustion air in the combustion completion region 52 can be analyzed.
The measurement laser light transmitting system 60 includes a laser diode capable of emitting a laser light which has an infrared wavelength range. The laser diode is a wavelength scanning type laser diode which is capable of adjusting the wavelength of the laser light output by driving electric current, and is capable of wavelength sweep on the basis of a command from the measurement laser controller 54. The wavelength scanning range of the measurement laser light transmitting system 60 is selected so as to include the wavelength corresponding to at least two electronic level transitions of the same gas type contained in the combustion air. Particularly in the present embodiment, the laser diode is selected so as to include wavelength corresponding to two electronic level transitions of H2O, which is a type of gas contained in the combustion air. This is because, compared to O2, CO2, and the like also contained in the combustion air, H2O has a wavelength range corresponding to adjacent two electronic level transitions in a relatively close range.
As depicted in
The infrared measurement analysis unit 56 obtains a measurement result by the measurement laser light receiving system 62, and performs a gas analysis utilizing two-dimensional solution analysis (tomography) on the basis of the measurement result. Next, with reference to
As depicted in
First, the standard setting part 66 sets a standard gas concentration distribution Dcr and a standard temperature distribution Dtr on the basis of the measurement result obtained by the measurement part 64 (step S101). The standard gas concentration distribution Dcr and the standard temperature distribution Dtr function as initial values when performing convergence calculation with the gas concentration distribution Dc and the temperature distribution Dt being variables, in the analysis performed by the analysis part 68.
The standard gas concentration distribution Dcr and the standard temperature distribution Dtr are set on the basis of an absorption amount (absorption spectrum) measured by the measurement laser light receiving systems 62 from laser light emitted into the combustion air by the measurement laser light transmitting system 60, the laser light including an absorption wavelength corresponding to at least two electronic level transitions of the same gas type contained in the combustion air.
The peak rate of the absorption spectra S1 to S2 changes depending on the temperature of the combustion air. Thus, by determining in advance a correlation between the peak ratio of the absorption spectra S1 to S2 and the temperature of combustion air, it is possible to obtain the temperature of combustion air corresponding to the peak ratio of absorption spectra S1 to S2 based on an actual measurement value. The temperature of combustion air obtained as described above corresponds to an average temperature in the measurement path on which the absorption spectrum is measured. The standard setting part 66 utilizes such temperature dependency of the peak ratio to obtain the average temperature in each measurement path on the basis of the absorption wavelength spectra S1 and S2 measured in the respective measurement paths P. Then, the average temperatures of the respective measurement paths are further averaged, thereby calculating the average temperature of combustion air in the furnace 2. Then, the standard setting part 66 sets the standard gas concentration distribution Dcr and the standard temperature distribution Dtr so as to obtain a temperature distribution in which temperatures are constant at the average temperature calculated accordingly over the plane including the plurality of measurement paths P.
Referring again to
In the following description, absorption spectra S corresponding to the respective 2n measurement paths P are individually referred to as “S1, S2, . . . , S2n”.
The analysis part 68 estimates the gas concentration distribution Dck and the temperature distribution Dtk, which are two-dimensional distributions, by reconfiguration, on the basis of the absorption spectra S1, S2, S3, . . . , S2n corresponding to the plurality of measurement paths (step S105). In the estimation calculation of step S105, the analysis part 68 determines the gas concentration distribution Dck and the temperature distribution Dtk as functions including common variable parameters. The function is set corresponding to the shape of the furnace 2 where combustion air to be analyzed exists, on the basis of, for instance, a common cylindrical coordinate system (e.g. the radial directional low-order Fourier series expansion or the Gaussian distribution), further using a two-dimensional distribution function including parameters such as a position of the center axis of the cylindrical coordinate system, an ovalization rate of the coordinate, and a circumferential directional distribution term.
Particularly in the present embodiment, taking into consideration that there is correlation between the gas concentration distribution Dck and the temperature distribution Dtk, the functions representing the gas concentration distribution Dck and the temperature distribution Dtk are set so that the functions share at least the parameters of the position of the center axis of the cylindrical coordinate system and the ovalization rate of the coordinate. Accordingly, an impact of the temperature distribution of combustion air is taken into consideration when calculating the gas concentration distribution, and thereby it is possible to obtain an analysis result that is closer to the actual distribution. Described below is an example of a function derived from the above technical idea.
In the expression (1), x is the gas concentration distribution Dck, and y is the temperature distribution Dtk, satisfying the following expression.
In the expression (1), A is the physical-amount center value, B and C are radial distribution coefficients, Dk and Ek are circumferential distribution coefficients, widx and widy are ovalization rates of the coordinate, and xc and yc are center-axis positions of the cylindrical coordinate system.
In the iterative calculation, the Marquardt method is used, for instance, to update each of the parameters (A, Bi, Ci, Dk, Ek, widx, widy, xc, yc) so as to reduce the difference between the obtained absorption spectrum S and the analytic absorption spectrum Sr.
Next, a standard absorption spectrum Sr in a plurality of measurement paths is obtained on the basis of the standard gas concentration distribution Dcr and the standard temperature distribution Dtr set in step S101 (S106), and the difference Δk between the standard absorption spectrum Sr and the absorption spectrum S obtained in step S104 is obtained from an expression: Δk=|S−Sr| (Step S107).
Subsequently, the analysis part 68 determines whether Δk obtained in step S107 is equal to or greater than Δk-1 (step S108). If Δk is less than Δk-1. (step S108: NO), it means that the difference is reduced compared to the previous control loop, and thus the gas concentration distribution Dck and the temperature distribution Dtk estimated in step S105 are updated as the standard gas concentration distribution Dcr and the standard temperature distribution Dtr (step S109). Then, an increment variable is added (step S110), and the process is returned to step S107.
As a result of repetition of the process of steps S107 to S110, if Δk becomes not less than Δk-1 (step S108: NO), the analysis part 68 determines that the solution has converged, and outputs the gas concentration distribution Dck and the temperature distribution Dtk estimated in step S105 as analysis results (step S111). As described above, in the present embodiment, when the two-dimensional distribution of the gas concentration is calculated, the gas concentration distribution Dck and the temperature distribution Dtk are treated as variables at the same time, and a solution is sought so as to minimize the difference Δk.
The gas concentration distribution Dck and the temperature distribution Dtk, which are solutions derived as described above, are transmitted to the distribution control unit 46 and the two-dimensional measurement result display part 58 as analysis results. The distribution control unit 46 adjusts the flow-rate adjustment valves 22, 38, 44 on the basis of the gas concentration distribution Dck and the temperature distribution Dtk analyzed by the gas analysis device 10, and thereby controls the fuel supply unit 12, the primary-air supply unit 26, and the secondary-air supply unit 28.
Now, with reference to
First, the distribution control unit 46 determines whether the total amount of the O2 concentration in the furnace 2 is equal to or less than an upper limit target value on the basis of the gas concentration distribution Dck (step S201). If the total amount of the O2 concentration is greater than the upper limit target value (step S201: NO), the distribution control unit 46 controls the burner 16 and the flow-rate adjustment valves 22, 38, 44 so as to reduce the total amount of the primary air and the secondary air (step S202).
On the other hand, if the total amount of the O2 concentration is equal to or less than the upper limit target value (step S201: YES), the distribution control unit 46 further determines whether the total amount of CO2 concentration is equal to or less than the upper limit target value (step S203). If the total amount of the CO2 concentration is greater than the upper limit target value (step S203: NO), the distribution control unit 46 controls the burner 16 and the flow-rate adjustment valves 22, 38, 44 so as to reduce the total amount of the primary air and the secondary air (step S204).
In contrast, if the total amount of the CO2 concentration is equal to or less than than the upper limit value (YES in step S203), the distribution control unit 46 feedback-controls the balance of the burner 16 and the flow-rate adjustment valves 22, 38, 44 on the basis of the unbalance in the gas concentration distribution Dck and the temperature distribution Dtk (step S204). During such a feedback control, it is determined whether the combustion facility 1 is stopped (step S205). If the combustion facility 1 is in operation (step S205: NO), the process is returned to S201, and the above control is repeated. On the other hand, if the combustion facility 1 stops (step S205: YES), the series of processes is ended (END).
As described above, the distribution control unit 46 controls the supply amount of the fuel, the primary air, and the secondary air to the furnace 2, and thereby achieves an optimum operation in which the temperature unbalance and excess/shortage of oxygen supply in the furnace 2 are solved, thus improving the power generation efficiency and suppressing an increase in the NOx generation due to excessive O2. Further, the two-dimensional measurement display part 58 visualizes the gas concentration distribution Dck and the temperature distribution Dtk for an operator with a display unit such as a display monitor, which makes it easier to monitor the combustion state in the furnace 2.
In the control chamber, a two-dimensional measurement result display part 58 is disposed, which displays an analysis result by the infrared measurement analysis unit 56. The two-dimensional measurement result display part 58 is, for instance, a unit for visualizing an analysis result for an operator in the control chamber, on a display unit such as a display monitor.
An operator of the control panel 70 refers to an analysis result displayed on the two-dimensional measurement result display part 58, which is a display unit such as a display monitor, and thereby determines the combustion state inside the furnace 2 and operates the control panel 70 in accordance with the determination result. As described above, in the present embodiment, the operator can perform works efficiently while determining the combustion state of the furnace 2 easily.
As described above, according to the present embodiment, it is possible to provide a gas analysis device for accurately analyzing a gas concentration distribution and a temperature distribution in a system in which combustion gas inside a furnace is not evenly mitigated, a control system and a control assistance system for a combustion, and a gas analysis method.
The present disclosure can be applied to a gas analysis device for analyzing a gas concentration distribution and a temperature distribution inside a furnace, a control system and a control assistance system for a combustion facility provided with the gas analysis device, and a gas analysis method performed by the gas analysis device.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015-066847 | Mar 2015 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2015/083005 | 11/25/2015 | WO | 00 |
