JPH1194224A - Method for controlling combustion of fluidized bed type incinerator - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a fluidized bed type incinerator which optimizes a flow rate of fuel in relation to temperatures of a sand layer part and a free board part and thereby enables keeping of the temperatures of the sand layer part and the free board part within a prescribed range, and others. SOLUTION: In a method for controlling combustion of a fluidized bed type incinerator 1, the temperature of a sand layer part 12 of the fluidized bed type incinerator 1 composed of the sand layer part 12 and a free board part 13 is controlled by regulating the amount of fuel supply thereto. In this case, the temperature of the sand layer part 12 is measured by a temperature detector 35 and a measured value is inputted to a sand layer part temperature computing unit 2 so as to determine a rate of temperature change per a unit time of the sand layer part 12. Meanwhile, the temperature of the free board part 13 is measured by a temperature detector and a measured value is inputted to a free board part temperature computing unit 3. A temperature deviation of the measured value of the free board part 13 from a reference temperature thereof inputted beforehand to the computing unit 3 is determined and, based on the rate of the temperature change of the sand layer part 12 and the temperature deviation of the free board part 13, the flow rate of fuel is controlled.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion control method for a fluidized bed incinerator for treating sludge or municipal waste generated from sewage or the like.

[0002]

2. Description of the Related Art Conventionally, as one of fluidized bed incinerators, FIG.
Fluidized bed sludge incinerator (hereinafter referred to as incinerator) 11
This incinerator 11 is composed of a sand layer 12 and a free board 13. The sand layer 12 is supplied with fuel from a fuel gun 14 and high-temperature air from an air dispersion pipe 15, and sludge is injected from a sludge input machine 16 provided in the freeboard section 13. . An air preheater 37, a dust collector 38, and a white smoke suppressor 39 are provided in an exhaust duct 31 provided above the incinerator 11, and a furnace pressure control damper 51 and an induction fan 52 are provided downstream thereof. Is provided. Further, a cooling water injector 32 for lowering the temperature of the free board unit 13 is disposed above the incinerator 11 via a cooling water flow control valve 33.

The sludge introduced into the sand layer 12 from the sludge charging machine 16 is heated by the combustion of the high-temperature air from the air dispersion pipe 15 and the fuel from the fuel gun 14 into the flowing sand layer 12. Stirred and crushed, dried and incinerated in a short time. The sludge from which the organic matter has been incinerated becomes only a powdery inorganic matter (incinerated ash) and flows into the air preheater 37 via the exhaust duct 31 from the upper part of the incinerator 11 together with the combustion gas. Heat is exchanged with the air, and the heated high-temperature air is supplied to the air distribution pipe 15.
Sent to After the combustion gas flowing into the air preheater 37 is separated from the incinerated ash by the dust collector 38, it passes through the white smoke suppressor 39 and is discharged to the outside by the induction fan 52 via the furnace pressure control damper 51. Incombustibles or unburned substances remaining in the sand layer 12 without being discharged together with the exhaust gas are discharged from the lower part of the incinerator 11 together with the fluidized medium in the sand layer 12 as a residue.

The fuel is supplied to a fuel gun 14 through a fuel flow detector 17 and a fuel flow control valve 18, and the flowing air is supplied to an air distribution pipe 15 through a damper 23 and an air flow detector 24. The sludge is supplied to the sludge input device 16 via a sludge input pump 27 and a sludge flow rate detector 28. The amount of the sludge supplied to the furnace is controlled by controlling the valve opening and the pump rotation speed, respectively. Is adjusted. In general, in the fluidized bed incinerator 11, the sludge is completely burned by controlling the temperature of the sand layer portion 12 and the freeboard portion 13 or the supply amount of the flowing air, and the unburned portion of the sludge or CO, NOx Furthermore, generation of dioxins and the like is prevented.

Here, the operation of the incinerator 11 will be described. The temperature of the sand layer portion 12 is determined by providing temperature detectors 35 at three locations in the sand layer portion: upper, middle, and lower. The detected temperature is input to the sand layer temperature controller 41, and the highest detected temperature among the three detected temperatures is compared with a reference temperature (set temperature) previously input to the controller 41. By adjusting the opening of the fuel flow control valve 18 so as to eliminate the temperature deviation, that is, if the temperature of the sand layer 12 is higher than the reference temperature, the fuel flow is reduced, and the temperature of the sand layer 12 is lower than the reference temperature. For example, control is performed by increasing the fuel flow rate.

The temperature of the freeboard section 13 is determined by providing temperature detectors 36 at three locations in the upper, middle, and lower stages of the freeboard section 13, and detecting the temperature detected by the temperature detector 36 as the freeboard temperature. The temperature is input to the controller 42, and the highest one of the detected temperatures from the three locations is compared with a reference temperature (set temperature) previously input to the controller 42, and the temperature of the free board 13 is detected. If the temperature is higher than the reference temperature, the cooling water is supplied from the cooling water injector 32 provided at the top of the incinerator 11 while adjusting the opening of the cooling water flow control valve 33 so that the temperature deviation is eliminated. Prevents excessive rise in board temperature.

Further, the sludge supplied from the sludge input device 16 to the sand layer section 12 inputs the flow rate detected by the sludge flow rate detector 28 to the sludge flow rate controller 43, and the sludge throughput rate of the incinerator which has been input in advance. By comparing the reference flow rate (set flow rate) determined from the above with the detected flow rate to determine the deviation and controlling the number of revolutions of the sludge feed pump 27 so as to eliminate the deviation, constant supply is always performed. .

[0008] Further, the supply amount of the flowing air is also added in advance to the required air amount calculated from the sludge input amount and the sludge component thereof by a variation (increase) of the required air amount due to a variation of the sludge component and the like. In order to prevent the generation of CO or unburned sludge due to lack of air, an air flow controller 45 is set in advance as a reference air amount (set air amount) with air larger than the required air amount.
The reference air amount is compared with the detected flow rate input from the air flow rate detector 24 to obtain a deviation, and by adjusting the opening of the damper 23 to eliminate the deviation,
It is controlled to always supply a constant amount regardless of the temperature of the sand layer portion 12 or the free board portion 13.

[0009]

However, in the fluidized bed incinerator 11, since the heat capacity of the sand layer 12 is considerably larger than the heat capacity of the freeboard section 13, the temperature of the sand layer 12 is kept within an appropriate range. As a result, when the fuel supply increases,
Since the response speed of the sand layer portion 12 to the fuel supply is much lower than that of the freeboard portion 13, the amount of supplied fuel becomes excessive, and the temperature of the freeboard portion 13 tends to rise rapidly. In addition, since the temperature of the sand layer portion 12 and the temperature of the freeboard portion 13 are controlled by separate control systems (single control systems), the fuel supply amount is reduced even if the temperature of the freeboard portion 13 rises abnormally. The supply of fuel is continued without being considered in the control, and the freeboard section 13 must be constantly cooled with the cooling water, resulting in a problem of increased fuel consumption. Further, when the fuel supply amount is reduced, the response speed of the sand layer portion 12 to the fuel supply (suppression) is extremely slow,
The fuel supply amount is suppressed more than necessary, and the free board 13
There is a problem in that the temperature of the mixture becomes too low and unburned components or dioxins are generated.

[0010] Further, the supply amount of the flowing air is controlled by the sand layer portion 12.
Alternatively, the constant supply is always performed irrespective of the temperature change of the free board portion 13, the change of the sludge property, or the increase / decrease of the fuel flow rate. Therefore, the optimum combustion corresponding to the change of the fuel flow rate or the like cannot be performed. , NOx, unburned components and the like increase. SUMMARY OF THE INVENTION The present invention has been made to eliminate such a conventional problem, and optimizes the fuel flow rate with respect to the temperature of the sand layer and the freeboard to maintain the temperature of the sand and freeboard within a certain range. While optimizing the amount of air supply to the amount of fuel supply and sludge input, the C
An object of the present invention is to provide a fluidized bed incinerator capable of reducing the amount of generated O, NOx, dioxins, and the like.

[0011]

In order to solve the above-mentioned problems, a first invention is to provide a freeboard section in which a sand layer section to which fuel and flowing air are supplied and an exhaust gas duct through which combustion exhaust gas flows are connected. In a combustion control method for a fluidized bed incinerator wherein the temperature of the sand layer is controlled by adjusting the amount of fuel supplied to the sand layer of the fluidized bed incinerator comprising a temperature detector for detecting the temperature of the sand layer. Measure and input the measured value to the sand layer temperature calculator to determine the rate of temperature change per unit time of the sand layer portion, and measure the temperature of the freeboard portion with a temperature detector and calculate the measured value with the freeboard. The temperature difference between the reference temperature of the freeboard unit and the measured value previously input to the arithmetic unit, and the temperature change rate of the sand layer and the temperature deviation of the freeboard unit are input to the unit temperature calculator. Based on the fuel flow rate It was Gosuru way.

According to a second aspect of the present invention, the temperature of the sand layer is measured by a temperature detector, and the measured value is input to a sand layer temperature calculator, and the reference temperature of the sand layer previously input to the calculator is measured. And the amount of sludge introduced into the sand layer is controlled based on the temperature deviation of the sand layer.

Further, the third invention is characterized in that the O ₂ concentration and the NOx concentration in the combustion exhaust gas are measured by an O ₂ concentration detector and a NOx concentration.
Prompted to enter the measured value in the supply air flow controller as measured by the concentration detector, the reference O ₂ concentration and the reference NOx concentration which is inputted in advance the controller a deviation between the measured values, respectively,
Wherein based on the said O ₂ concentration deviation and the NOx concentration deviation so as to control the supply amount of the fluidizing air.

[0014]

Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a fluidized-bed sludge incinerator (hereinafter referred to as an incinerator) 1 which is one of the fluidized-bed incinerators according to the first invention. The fluidized-bed sludge incinerator 1 shown in FIG.
Portions common to 1 are denoted by the same reference numerals.

In the incinerator 1, the upper part of the sand layer 12
The detected temperatures from the temperature detectors 35 provided at the three middle and lower stages are input to the sand layer temperature calculator 2, and the highest of the detected temperatures from the three locations is input to the calculator 2 in advance. The temperature difference of the sand layer 12 per unit time, that is, the sand layer temperature change rate (Δ
T / Δt). Further, the detected temperatures from the temperature detectors 36 provided at the upper, middle, and lower stages in the freeboard unit 13 are input to the freeboard temperature calculator 3, and the highest of the detected temperatures from the three locations is obtained. The free board unit temperature deviation is calculated by comparing the temperature of the free board unit with a reference temperature (set temperature) of the free board unit 13 which is input to the computing unit 3 in advance.

The sand layer temperature change rate and the free board temperature deviation are input to a fuel flow controller 4 to which the detected flow from the fuel flow detector 17 is input. A control signal for adjusting the opening of the fuel flow control valve 18 is output to the flow control valve 18 so as to eliminate the temperature deviation of the freeboard section 13 while considering the temperature change rate of the sand layer section 12. At this time, the fuel flow controller 4 may perform the PID control as in the related art, but since the response speed of the temperature change of the free board unit 13 to the change in the fuel flow rate is fast, it is expected control (probable control). Preferably, fuzzy control with elements is performed. By employing the fuzzy control, the fuel flow rate control that has been conventionally performed based on the experience of the operator can be automatically performed.

In the above-described example, the temperatures of the sand layer 12 and the freeboard 13 are respectively set to three levels of the upper, middle, and lower levels.
Although the number of detections is detected at each location, the number of detections is not limited to three. For example, the temperature detector at the upper stage of the sand layer section 12 may be used to supply (e.g., change (especially decrease) the amount of sand forming the sand layer), to supply sludge or to influence the cooling water supplied from the cooling water injector 32 in an emergency. It is difficult to accurately detect the temperature of the sand layer portion 12 because the temperature fluctuation factors other than the above are large, so the temperature is excluded from the detection target, and the sand layer portion 12 is detected and compared at the two temperatures of the middle stage and the lower stage. Good, and the temperature detection position does not need to be limited to the upper, middle, and lower stages,
For example, the central part and the peripheral part may be detected only in the middle part, or the central part and the peripheral part may be detected in each of the upper part, the middle part, and the lower part. There is no problem even if it is detected by. Further, only one point representing the sand layer portion 12 or the free board portion 13 may be detected without detecting the temperatures at a plurality of points as described above. For example, by detecting the temperature of the upper stage of the freeboard section 13, the temperature of the combustion exhaust gas supplied to the air preheater 37 is controlled, and the fuel flow rate is controlled while preventing the air preheater 37 from being damaged by the combustion exhaust gas. Control may be performed.
As described above, the position and number of temperature detection can be freely set.

On the other hand, the sand layer temperature deviation calculated by the sand layer temperature calculator 2 is input to the sludge flow controller 5 to which the detected flow from the sludge flow detector 28 is input. , A control signal for adjusting the rotation speed of the sand layer portion 12 is output to the sludge input pump 27 so as to eliminate the temperature deviation of the sand layer portion 12. However, since the sludge input amount is uniquely determined from the sludge treatment amount, the input amount is controlled by controlling the fuel supply amount described above.
Is not adjusted to the predetermined value. Also,
The control by the sludge flow controller 5 may be either fuzzy control or PID control.

Further, in the incinerator 1, the exhaust duct 3
The detection flow from the air flow detector 24 is input to the detection concentration from the O ₂ concentration detector 6 and the NOx concentration detector 7 provided at an arbitrary position (for example, between the air preheater 37 and the dust collector 38). The detected concentration and O ₂ and N ₂ previously input to the flow controller 8 are supplied to the supply air flow controller 8.
Ox is compared with a reference concentration (set concentration) to calculate each concentration deviation, and the flow controller 8 outputs a control signal for adjusting the opening degree of the damper 23 so as to eliminate the deviation. At this time, the supply air flow controller 8 sets P
Although ID control may be performed, it is preferable to perform fuzzy control capable of predictively controlling (estimating control) the damper opening based on the relationship between the O ₂ concentration and the NOx concentration.

Here, the relationship between the sludge treatment amount and the reference fuel flow rate and the reference flow air amount with respect to the treatment amount is shown in Table 1, and the opening degree of the fuel flow rate control valve 18 and the damper 2 are controlled.
Tables 2 and 3 show an example of fuzzy control for the opening degree adjustment of No. 3.

[Table 1]

[0021]

[Table 2]

[0022]

[Table 3]

In Table 2, each signal in the row indicating the magnitude of the temperature deviation (detected temperature-reference temperature) of the free board means the following cases. The reference temperature of the free board portion is, for example, 850 ° C. in order to suppress generation of dioxins. NL: when the deviation is negative and its absolute value is large
(Example: Near -50 ° C) NS: When the deviation is negative and its absolute value is small
(Example: near -20 ° C) ZR: When the deviation is close to zero PS: When the deviation is positive and its absolute value is small
(Example: Near + 20 ° C) PL: When the deviation is positive and its absolute value is large
(Example: Near + 50 ° C)-: Not controlled

In Table 2, the rate of temperature change of the sand layer, that is, the amount of change in temperature of the sand layer per unit time (ΔT / Δ
Each symbol in the column representing the size of t) means the following case. NL: When the rate of change is negative and its absolute value is large
(Example: near -40 ° C / h) NS: When the rate of change is negative and its absolute value is small
(Example: near -20 ° C / h) ZR: When the rate of change is close to zero PS: When the rate of change is positive and its absolute value is small
(Example: near + 20 ° C / h) PL: When the rate of change is positive and its absolute value is large
(Example: Near + 40 ° C / h)

Each symbol indicating the control amount in the table according to the magnitude of the deviation and the magnitude of the rate of change has the following meaning. However, the reference value of the fuel flow rate is determined by the sludge treatment amount of the incinerator, and an example is shown in Table 1 above. The reference opening of the fuel flow control valve 18 differs for each sludge treatment amount, and the opening for supplying the reference fuel flow rate determined by the sludge treatment amount is the reference opening. NL: Turn the fuel flow control valve largely in the closing direction. (Example: Set near the reference value of −20 l / h) NS: Turn the fuel flow control valve slightly in the closing direction. (Example: Set near the reference value -10 l / h) ZR: Do not move the fuel flow control valve. That is, the reference opening determined by the sludge treatment amount is maintained. PS: Turn the fuel flow control valve slightly in the opening direction. (Example: Set near the reference value +10 l / h) PL: Turn the fuel flow control valve largely in the opening direction. (Example: Set to near the reference value +20 l / h)

Next, in Table 3, each symbol in the row indicating the magnitude of the deviation of the NOx concentration (detection concentration-reference concentration) means the following cases. The reference concentration of NOx is, for example, 50 ppm. NL, NS: NOx concentration lower than the reference value is not subject to control because there is no problem ZR: When the deviation is close to zero PS: When the deviation is positive and its absolute value is small
(Example: near +25 ppm) PL: When the deviation is positive and its absolute value is large
(Example: Near +50 ppm)

Further, in Table 3, each symbol in the column indicating the magnitude of the deviation of the O ₂ concentration (detection concentration−reference concentration) means the following cases. The reference concentration of O ₂ is, for example, 6%. NL: When the deviation is negative and its absolute value is large (example: near -1.5%) NS: When the deviation is negative and its absolute value is small (example: near -0.5%) ZR: When the deviation is close to zero PS: When the deviation is positive and its absolute value is small (eg, near + 0.5%) PL: When the deviation is positive and its absolute value is large (Example: + 1.5%)

The symbols indicating the control amounts in the table according to the magnitude of the deviation of the NOx concentration and the magnitude of the deviation of the O ₂ concentration have the following meanings. However, the reference value of the flowing air amount is determined by the sludge treatment amount of the incinerator, and an example is shown in Table 1 above. The reference opening of the damper 23 differs for each sludge processing amount, and the opening for supplying the reference flowing air amount determined from the sludge processing amount is the reference opening. NL: Turn the damper largely in the closing direction. (Example: Reference value-
400m ³ N / h to near) NS: Turn the damper small in the closing direction. (Example: Reference value-
(Rearly 200 m ³ N / h) ZR: Do not move the damper. That is, the reference opening determined by the sludge treatment amount is maintained. PS: Turn the damper slightly in the opening direction. (Example: Reference value +
200m ³ N / h to near) PL: Turn the damper increases in the opening direction. (Example: Reference value +
400m ³ N / h)

Further, the sludge input amount is determined unambiguously from the throughput of the incinerator, and is supplied quantitatively regardless of the temperature of the sand layer portion and the freeboard portion. Only when the temperature of the unit 12 cannot maintain the predetermined value, the sludge input amount is controlled as shown in Table 4. Then, when the temperature of the sand layer portion 12 is adjusted to a predetermined value by the input of the sludge, the input amount of the sludge is maintained at the input amount determined by the processing amount.

[Table 4]

In Table 4, each symbol in the row representing the temperature deviation (detected temperature-reference temperature) of the sand layer means the following cases. The reference temperature of the sand layer is, for example, 7
00 ° C. NL: When the deviation is negative and its absolute value is large (eg, near −50 ° C.) NS: When the deviation is negative and its absolute value is small (eg, near −20 ° C.) ZR: When the deviation is small When close to zero PS: When the deviation is positive and its absolute value is small (eg, near + 20 ° C.) PL: When the deviation is positive and its absolute value is large (eg, near + 50 ° C.)

Each symbol indicating the control amount in the table according to the magnitude of the deviation has the following meaning. In addition,
Table 3 shows an example of the reference value of the sludge input amount. NL: Sludge input value is greatly reduced. (Example: Reference value -10 t / day) NS: Decrease the set value of sludge input amount. (Example: Reference value -5t / day) ZR: The rotation speed of the sludge feeding pump is not changed. That is,
Maintain the number of revolutions to supply the reference input. PS: Increase the set value of sludge input. (Example: reference value + 5 t / day) PL: The set value of the sludge input amount is greatly increased. (Example: Reference value + 10 t / day)

In the present invention, the cooling water injector 3
2 is not necessarily required, but this incinerator 1
If an abnormal situation occurs and the temperature deviation of the freeboard section 13 indicated by the temperature signal input to the freeboard section temperature calculator 3 exceeds an allowable value, the freeboard section is used as an emergency means. A control signal for opening the cooling water flow control valve 33 is output from the temperature calculator 3 to inject the cooling water to the free board unit 13 so that the temperature of the free board unit 13 can be lowered. It is.

As described above, in the incinerator 1 described above, when the temperature of the sand layer portion 12 is maintained at a predetermined value, the heat capacity of the incinerator 1 is small, while taking into account the temperature change rate of the sand layer portion 12 having a large heat capacity and a low response speed. Free board section 13 with high speed
The fuel flow rate is controlled so as to keep the temperature of the freeboard section 13 at a predetermined value, so that the freeboard section 13 abnormally rises in temperature due to excessive supply of fuel to the sand layer section 12 and abnormally decreases in the freeboard section 13 due to insufficient fuel supply. And the optimum amount of fuel can always be supplied with respect to a change in temperature of the sand layer portion 12 due to a change in sludge properties or the like. Further, when the temperature of the sand layer 12 cannot be maintained at a predetermined value only by controlling the fuel flow rate, the sludge input amount is controlled by changing the set value of the sludge treatment amount, and the temperature of the sand layer 12 is adjusted. Can be.

Further, since the O ₂ concentration and the NOx concentration are detected at a predetermined position of the exhaust duct 31 and the amount of flowing air is controlled so that the two concentrations are maintained at the predetermined values, a change in the fuel flow rate or a sludge property may be caused. Even if the required air amount changes due to a change or the like, the optimum air amount can always be supplied, whereby CO generation due to insufficient air and NO due to excessive air
The generation of x can be suppressed. In the above-described embodiment, a fluidized bed incinerator in which the material to be incinerated is sludge has been described as an example of a fluidized bed incinerator. Naturally, the present invention can be applied similarly to the fluidized bed type sludge incinerator only when the object to be incinerated is changed even if the object is municipal waste.

[0035]

As is apparent from the above description, according to the present invention, a sand layer portion to which fuel and flowing air are supplied and a free board portion in which an exhaust gas duct through which combustion exhaust gas flows are connected. In the combustion control method for a fluidized bed incinerator, which controls the temperature of the sand bed by adjusting the amount of fuel supplied to the sand bed of the fluidized bed incinerator, the temperature of the sand bed is measured by a temperature detector. The measured value is input to a sand layer temperature calculator to determine the rate of temperature change of the sand layer per unit time, while the temperature of the freeboard section is measured by a temperature detector and the measured value is calculated as the freeboard temperature. Input to a computing unit, find the temperature deviation between the reference temperature of the freeboard unit and the measured value previously input to the computing unit, and based on the temperature change rate of the sand layer and the temperature deviation of the freeboard unit, Control fuel flow It is so. Further, the amount of sludge input is controlled based on the temperature deviation of the sand layer.

As described above, since the fuel supply amount is controlled by unifying the temperature control of the sand layer portion and the freeboard portion having greatly different heat capacities, the temperature of the sand layer portion and the freeboard portion can be controlled while optimizing the fuel supply amount. Can always be maintained at a predetermined value. Further, when the sand layer temperature cannot be maintained at a predetermined value only by controlling the fuel supply amount, the sand layer temperature is maintained at a predetermined value by controlling the amount of sludge supplied. Is always maintained at an optimum temperature, and generation of unburned components or generation of dioxins can be suppressed. In addition, since the supply amount of the flowing air is suppressed based on the measured values of the O ₂ concentration and the NOx concentration in the combustion exhaust gas, the optimum amount is always adjusted according to the change in the sludge property, the change in the fuel supply amount, and the like. By supplying an air amount that can maintain the combustion state, the generation of CO or NOx can be reduced.

[Brief description of the drawings]

FIG. 1 is a diagram showing an overall configuration of a fluidized bed sludge incinerator according to the present invention.

FIG. 2 is a diagram showing an entire configuration of a conventional fluidized bed sludge incinerator.

[EXPLANATION OF SYMBOLS] 1 fluidized bed sludge incinerator 2 sand layer portion temperature calculator 3 freeboard temperature calculator 4 fuel flow adjustment controller 5 Sludge flow controller 6 O ₂ concentration detector 7 NOx concentration detector 8 charge air Flow controller 12 Sand layer part 13 Free board part 17 Fuel flow detector 18 Fuel flow control valve 20 Blower 23 Damper 24 Air flow detector 27 Sludge input pump 28 Sludge flow detector 31 Exhaust duct 35 Temperature detector (sand layer part) 36 Temperature detector (free board part)

──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. ⁶ Identification code FI F23G 5/50 ZAB F23G 5/50 ZABN F23C 11/00 ZAB F23C 11/00 ZAB 311 311 11/02 ZAB 11/02 ZAB 301 301 309 309 F23G 5/30 ZAB F23G 5/30 ZABP (72) Inventor Masaru Onishi 2-4-7 Kyomachibori, Nishi-ku, Osaka-shi, Osaka Inside Chugai Furnace Industry Co., Ltd.

Claims (3)

[Claims] The amount of fuel supplied to the sand layer portion of a fluidized bed incinerator comprising a sand layer portion to which fuel and flowing air are supplied and a freeboard portion provided with an exhaust gas duct through which combustion exhaust gas flows is connected. In a combustion control method for a fluidized bed incinerator wherein the temperature of the sand layer is controlled by adjusting the temperature of the sand layer, the temperature of the sand layer is measured by a temperature detector, and the measured value is input to a sand layer temperature calculator to obtain the sand layer. While the temperature change rate per unit time of the unit is determined, the temperature of the freeboard unit is measured by a temperature detector, and the measured value is input to the freeboard unit temperature calculator, which is previously input to the calculator. A fluidized bed, wherein a temperature deviation between a reference temperature of the freeboard portion and the measured value is obtained, and the fuel flow rate is controlled based on a temperature change rate of the sand layer portion and a temperature deviation of the freeboard portion. Type incinerator fuel Control method. 2. The temperature of the sand layer is measured by a temperature detector, and the measured value is input to a sand layer temperature calculator, and the temperature deviation from the reference temperature of the sand layer previously input to the calculator is calculated. 2. The method for controlling combustion in a fluidized bed incinerator according to claim 1, wherein the amount of sludge introduced into the sand layer is controlled based on the temperature deviation of the sand layer. Wherein the O ₂ concentration and the NO in the flue gas
x concentration is measured by an O ₂ concentration detector and a NO x concentration detector, and the measured value is inputted to a supply air flow rate controller, and the reference O ₂ concentration and the reference NO x concentration previously inputted to the controller are measured. a deviation between the value respectively, fluidized bed incineration of claim 1 or 2, characterized in that as the control the feed rate of fluidizing air based on the said O ₂ concentration deviation and the NOx concentration deviation Furnace combustion control method.