JP6761558B1 - Boiler tube group adhering ash removal system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a boiler tube group adhering ash removing system for quickly and appropriately removing adhering ash of a tube group while ensuring economic efficiency. SOLUTION: A boiler tube group adhering ash removal system controls a soot blower arranged between a plurality of tube groups, an attracting blower that attracts exhaust gas downstream of the tube group, and a soot blower to control the heat transmission coefficient of the boiler. It has a control device for calculating. The control device activates the soot blower once at a predetermined interval when the heat transmission coefficient K is equal to or higher than the predetermined value, executes the adhesion ash determination process when the heat transmission coefficient is less than the predetermined value, and responds to the result. And start the soot blower continuously. The adhering ash determination process is executed including at least one of four conditions: the main steam amount of the pipe group, the pressure difference of the exhaust gas, the rotation speed of the attracting blower, and the total amount of combustion air supplied to the furnace. [Selection diagram] Fig. 1

Description

The present invention relates to a boiler tube group adhering ash removal system.

In a thermal power plant equipped with a coal-cooking boiler, or in a plant such as a waste incinerator or a gasification melting furnace equipped with a waste heat boiler to generate power, incineration contained in exhaust gas generated by combustion of coal or waste. Ash easily adheres to and accumulates on a group of tubes (a group of tubes composed of a boiler screen tube, a heating tube, an evaporative tube, an economizer water tube, etc.). If the incineration ash accumulates on the pipe group, the pipe group may be corroded and the power generation efficiency may be deteriorated. For this reason, in general, a steam type or shock pulse type soot blower is activated at a predetermined time interval (constant cycle) to remove ash accumulated in the pipe group (hereinafter referred to as "adhered ash"), that is, ""Removes attached ash".
However, if the amount of adhering ash deposited on the tube group is small, the amount of adhering ash removed even when the sootblower is started is small, so the amount of attached ash removed for the cost of electricity, steam, or gas consumed or used by the sootblower. The effect of is small. On the other hand, when the amount of accumulated ash deposited on the tube group is large, the attached ash cannot be sufficiently removed by starting the soot blower at regular intervals, and the attached ash left in the tube group without being removed is the next soot blower. It may solidify by the time it is started, making it difficult to remove the adhering ash with a soot blower.
Therefore, various boiler tube group adhering ash removal systems have been developed in order to appropriately remove the adhering ash of the tube group using a soot blower.

For example, Patent Document 1 discloses a system that changes the cycle according to the degree of contamination of the pipe group, that is, the degree of accumulation of attached ash on the pipe group. Further, Patent Document 2 discloses a system for activating the soot blower in consideration of conditions other than the degree of contamination of the tube group. Further, Patent Document 3 discloses a system in which the pressures upstream and downstream of the exhaust gas flowing through the pipe group are measured, and the soot blower is activated when the difference between these pressures becomes a predetermined value or more.

The steam type has been mainly used for the soot blower, but in recent years, a shock pulse type that does not use steam has been developed and introduced to the market.
When the steam type soot blower is started, it continues to inject steam for a predetermined time, and when the predetermined time elapses, the steam injection is stopped.
On the other hand, the shock pulse type soot blower is also called a pressure wave type or shock wave type soot blower or a shock pulse generator (SPG), and when it is started, the flammable gas filled inside the soot blower explodes and shock pulse. (Also called "shock wave" or "pressure wave") is emitted. Once the shock pulse type soot blower is started, it is necessary to refill the gas for the next start. The filling generally takes about 1 to 10 minutes.

Japanese Unexamined Patent Publication No. 62-210316 Japanese Unexamined Patent Publication No. 63-286609 Japanese Unexamined Patent Publication No. 2017-181007

In each of the techniques disclosed in Patent Documents 1 to 3, the soot blower is activated only once after a predetermined condition such as the arrival of the above cycle is satisfied.
However, as described above, depending on the amount of deposited ash deposited, it is not always possible to sufficiently remove the adhered ash by starting the soot blower once. Therefore, if the adhered ash is not effectively removed even though the soot blower is started, the technique disclosed in Patent Documents 1 to 3 re-establishes the soot blower after a predetermined condition is satisfied, such as the arrival of the next cycle. You have to wait for it to start. Therefore, with these techniques, the heat exchange performance of the boiler cannot be restored at an early stage if the adhered ash is not sufficiently removed by starting the soot blower once.
Therefore, when starting the soot blower, it is conceivable to start it not only once but continuously a plurality of times.
However, although the adhered ash may be sufficiently removed by starting the soot blower once, it is uneconomical to start the soot blower a plurality of times each time when the above predetermined conditions are satisfied.

Therefore, an object of the present invention is to provide a boiler tube group adhering ash removing system that removes adhering ash quickly and appropriately while ensuring economic efficiency.

The boiler tube group adhering ash removing system of the present invention is a boiler tube group adhering ash removing system for removing the adhering ash of a plurality of boiler tube groups that recover heat from the exhaust gas generated in the furnace, and is a boiler tube group adhering ash removing system of the plurality of tube groups. It has a soot blower arranged between them, an attraction blower arranged downstream of the plurality of pipe groups to attract the exhaust gas, and a control device for controlling the activation of the soot blower.
The control device calculates the heat transmission coefficient of the boiler, and when the calculated heat transmission coefficient is equal to or higher than a predetermined value, the soot blower is started only once at a predetermined interval, and then again at the predetermined interval or When the heat transmission coefficient calculated is less than the predetermined value by executing one start with an interval different from this, the adhered ash determination process for selectively determining either the first determination or the second determination is performed. When the first determination is obtained by the adhered ash determination process, the soot blower is continuously activated a plurality of times without setting the predetermined interval, and the adhered ash determination process is performed. When the second determination is obtained, the above-mentioned one-time activation is executed.
In the adhering ash determination process, the first condition is that the main steam amount of the plurality of pipe groups is equal to or higher than the first threshold value, and the pressure difference between the exhaust gas at the inlet and outlet of the plurality of pipe groups is equal to or higher than the second threshold value. At least one of the second condition that the rotation speed of the attracting blower is equal to or higher than the third threshold, and the fourth condition that the total amount of combustion air supplied to the furnace is equal to or higher than the fourth threshold. Executed with conditions.
When the adhering ash determination process is executed based on only one of the four conditions, the first determination is obtained when the one condition is satisfied, and the one condition is not satisfied. When the second determination is obtained and the adhesion ash determination process is executed including any two, three, or four conditions among the four conditions, the two, three , Or the first determination is obtained when all the conditions including the four conditions are satisfied, and the second determination is obtained when any of the conditions including the two, three, or four conditions is not satisfied. Is obtained.

According to the boiler tube group adhering ash removal system of the present invention, one-time activation and continuous activation are used properly based on the heat transmission coefficient. Furthermore, if the heat transmission coefficient is less than the predetermined value, the attached ash determination process can be executed to appropriately determine whether or not the soot blower is to be continuously activated. Therefore, the attached ash can be quickly and appropriately determined while ensuring economic efficiency. Removal can be done.

It is a schematic block diagram of the boiler pipe group adherent ash removal system which concerns on embodiment and 1st modification. It is an example of a flowchart explaining the control that the boiler tube group adhering ash removal system activates a soot blower. (A) to (d) are examples of a specific processing flow of step S16 (adhesion ash determination processing) in FIG. (A) to (c) are schematic block diagrams showing a part of the boiler tube group adherent ash removal system which concerns on the 2nd modification. It is a schematic block diagram of the boiler tube group adherent ash removal system which concerns on the 3rd modification. It is a schematic block diagram of the boiler tube group adherent ash removal system which concerns on the 4th modification.

Hereinafter, an embodiment and a boiler tube group adhering ash removal system as a modified example will be described with reference to the drawings. The configurations shown below are merely examples, and there is no intention to exclude the application of various modifications and techniques that are not specified. The configurations and the like shown below can be variously modified and implemented without departing from their purpose. In addition, it can be selected as needed, or can be combined as appropriate.

[1. Overview of boiler tube group adhering ash removal system]
FIG. 1 is a schematic configuration diagram of the boiler tube group adhering ash removal system 1 (hereinafter referred to as “removal system 1”) of the present embodiment. Note that FIG. 1 also serves as a diagram showing a first modification (removal system 1') described later.
In FIGS. 1 and 4 to 6, which will be described later, an orthogonal coordinate system including an X-axis and a Y-axis will be illustrated and described. The X-axis is horizontal and the Y-axis is vertical. The direction of the arrow on the Y-axis is a vertical direction and an upward direction.

In this embodiment, as an example, a removal system 1 applied to a waste incinerator plant equipped with a boiler for generating electricity will be described. Of course, the boiler tube group adhering ash removal system of the present invention can also be applied to other plants such as thermal power plants and gasification melting furnaces.
Boilers are roughly classified into a two drum type equipped with a steam drum and a water drum and a one drum type equipped with a steam drum. The removal system 1 is any of the boilers. May be used. Although the steam drum is not shown in FIG. 1, a waste incinerator plant equipped with a one-drum type boiler is illustrated.

The removal system 1 is a system for removing adhering ash from a plurality of pipe groups 2 of a boiler that recovers heat from exhaust gas generated in a furnace, and is a soot blower 3 arranged between the plurality of pipe groups 2 and a plurality of pipes. It is arranged downstream of the group 2 and has an attracting blower 13 for attracting exhaust gas and a control device 4 for controlling the activation of the soot blower 3.

As will be described in detail later, the control device 4 calculates the heat transmission coefficient K of the boiler, and when the heat transmission coefficient K is a predetermined value α1 or more, the soot blower 3 is started only once at a predetermined interval. The "one-time activation" is executed again with the predetermined interval or an interval different from the predetermined interval.
Further, the control device 4 selectively determines either the first determination or the second determination when the calculated heat transmission coefficient K is less than the predetermined value α1 and less than the predetermined value α2. Execute the judgment process. When the first determination is obtained in the adhered ash determination process, the control device 4, in principle, executes "continuous activation" in which the soot blower 3 is continuously activated a plurality of times without setting a predetermined interval, and the adhered ash determination is made. If the second determination is obtained in the process, "start once" is executed.

The adhering ash determination process is executed including at least one of the following first to fourth conditions.
First condition: The main steam amount Qs of the pipe group 2 is equal to or higher than the first threshold value. Second condition: The pressure difference ΔPg of the exhaust gas at the inlet and outlet of the pipe group 2 is equal to or higher than the second threshold value. Third condition: Attracting blower 13 Fourth condition: The total amount of combustion air Qc supplied to the furnace is equal to or more than the fourth threshold value. From the experience of the inventor, each condition was satisfied for each of these four conditions. In this case, since there is a high possibility that a large amount of adhered ash is accumulated in the tube group 2, it is a condition that it is considered desirable to perform "continuous activation" of the soot blower 3.

In FIG. 3, which will be described in detail later, only the above four conditions (first condition, second condition, third condition, and fourth condition) will be described as an example, but these four conditions may be used depending on the design. Other conditions (eg, fifth condition, sixth condition, seventh condition, eighth condition, ...) may be added to the condition.
The other condition, for example, the fifth condition is "the temperature of the main steam of the tube group 2 is less than the fifth threshold" measured by the outlet steam temperature measuring device 24b described later, for example, the sixth condition is ". The amount of water sprayed by the overheat reducer 17 (described later) is less than the sixth threshold value. ”For example, as the seventh condition,“ the tube group 2 measured by the gas temperature measuring device 15b (outlet gas temperature measuring device) described later). The gas temperature of the exhaust gas at the outlet is above the seventh threshold. "
Although not shown, the exhaust gas recirculation technology (Exhaust Gas Recirculation (EGR)) that circulates a part of the exhaust gas downstream of the dust remover 11 to the vicinity of the stoker 7 may be adopted in the waste incinerator plant. sell. In this case, as the other condition, for example, as the eighth condition, a gas flow rate measuring device for measuring the gas flow rate of the circulated exhaust gas (circulated exhaust gas) is installed separately from the gas flow rate measuring devices 16a and 16b described later. Then, "the gas flow rate of the circulating exhaust gas is equal to or higher than the eighth threshold value" measured by the gas flow rate measuring device may be added.
As with the first to fourth conditions, these other conditions also branch into two based on the evaluation formula. Specifically, under these other conditions, if the conditions of the evaluation formula are satisfied, there is a high possibility that a large amount of adhered ash has accumulated in the tube group 2, so it is recommended to perform "continuous activation" of the soot blower 3. Desirably, when the condition of the evaluation formula is not satisfied, the condition that can be said that "continuous activation" of the soot blower 3 is unnecessary (hence, "single activation" is sufficient) is selected.
When the adhered ash determination process is executed based on only one of the four conditions of the first to fourth conditions described above, the first determination is obtained when the one condition is satisfied. Be done. Then, when the one condition is not satisfied, the second determination is obtained.
Further, when the adhering ash determination process is executed including any two, three, or four conditions out of the above four conditions (the above fifth condition or the like may be added), the said The first decision is obtained when all the conditions including two, three, or four conditions are satisfied. Then, a second determination is obtained when any of all the conditions including the two, three, or four conditions is not satisfied.

Hereinafter, in addition to the above-mentioned configuration that the removal system 1 has at least, other configurations will be described. Then, after the description of the configuration, the control (including the adhesion ash determination process) relating to the activation of the soot blower 3 will be described in detail.

[2. System configuration]
As shown in FIG. 1, the removal system 1 includes a hopper 5 for storing incinerated materials such as dust, and a feeder 6 for pushing out the incinerated material stored in the hopper 5 from below the hopper 5 (in the Y-axis direction and below). A stoker 7 for incinerating the incinerated material extruded to the feeder 6 while being conveyed, and an ash chute 8 for discharging the residue incinerated by the stoker 7 are provided.

Further, the removal system 1 is an economizer 9 (a type of tube group) arranged in each tube group 2 and downstream thereof for the heat of the exhaust gas containing fly ash generated by incinerating the incinerated object with the stoker 7. , Also called "economizer") to exchange heat. Then, the removal system 1 is dust-removed via a heat-reducing tower 10 that cools the heat-exchanged exhaust gas, and a dust-removing device 11 (for example, a bag filter) that removes soot and dust from the cooled exhaust gas. Exhaust gas is discharged from the chimney 12 to the atmosphere.

The exhaust gas path from the stoker 7 to the opening of the chimney 12 is formed by a water cooling wall, a duct, or the like, and is substantially sealed. Of the routes, the route extending from directly above the stalker 7 in the Y-axis direction and upward is "1 pass" ("pass" means "pass" in English), and it bends at the upper end of 1 pass and 1 pass. The path adjacent to the Y-axis and extending downward is called "2 pass", and the path adjacent to the 2 pass and extending downward in the Y-axis direction is called "3 pass". The exhaust gas generated by the stoker 7 flows so as to go up 1 pass, go down 2 passes, and go up 3 passes, as shown by the arrows in FIG. In addition, in order to attract the flow of the exhaust gas from one pass toward the chimney 12, the attracting blower 13 is arranged in the path between the dust removing device 11 and the chimney 12.

The removal system 1 is arranged in one pass and is arranged in the pressure measuring device 14a (inlet pressure measuring device) for measuring the pressure of the exhaust gas and the exhaust gas path between the economizer 9 and the temperature reducing tower 10 to measure the pressure of the exhaust gas. It is provided with a pressure measuring device 14b (outlet pressure measuring device) for measuring.

The arrangement of the pressure measuring devices 14a and 14b is not limited to these. Depending on the design of the plant, the inlet pressure measuring device 14a may be installed at any location upstream of the pipe group 2 arranged at the uppermost stream among the plurality of pipe groups 2 to be removed from the adhering ash in the exhaust gas path, that is, It suffices to be arranged at the “inlet of a plurality of pipe groups 2”, and the outlet pressure measuring device 14b is a pipe group arranged at the most downstream of the plurality of pipe groups 2 to be removed of adhering ash in the exhaust gas path. It may be arranged at any place downstream of 2, that is, at the "exhaust of a plurality of pipe groups 2". However, it is desirable that these arbitrary locations are as close as possible to the plurality of pipe groups 2 to be removed from the adhered ash.

The removal system 1 is a gas arranged below the pipe group 21 located at the uppermost stream (lower side) of the plurality of pipe groups 2 to be removed from the adhering ash arranged in 3 passes and measuring the temperature of the exhaust gas. In the exhaust gas path between the temperature measuring device 15a (inlet gas temperature measuring device) and the tube group 22c located at the most downstream (upper side) of the plurality of tube groups 2 arranged in 3 paths and the economizer 9. It is provided with a gas temperature measuring device 15b (outlet gas temperature measuring device) that is arranged to measure the temperature of the exhaust gas.

The arrangement of the gas temperature measuring devices 15a and 15b is not limited to these. Depending on the design of the plant, the inlet gas temperature measuring device 15a may be installed at any location upstream of the pipe group 2 arranged at the uppermost stream among the plurality of pipe groups 2 to be removed from the adhering ash in the exhaust gas path. That is, it may be arranged at the "inlet of the plurality of pipe groups 2", and the outlet gas temperature measuring device 15b is arranged at the most downstream of the plurality of pipe groups 2 to be removed from the adhering ash in the exhaust gas path. It may be arranged at an arbitrary place downstream of the tube group 2, that is, at "the outlets of a plurality of tube groups 2". However, it is desirable that these arbitrary locations are as close as possible to the plurality of pipe groups 2 to be removed from the adhered ash.

In other words, in the present embodiment and the modified examples described later, the "plurality of pipe groups 2" to be removed from the adhered ash is between the two pressure measuring devices 14a and 14b, and the two gas temperature measuring devices 15a. , 15b means a group of tubes arranged between.
FIG. 1 shows, as an example, a configuration in which a plurality of tube groups 2 are arranged in three paths. The economizer 9 also has a pipe group (see FIG. 6), but in the configuration of FIG. 1, the economizer 9 is arranged downstream of the outlets of the plurality of pipe groups 2, that is, downstream of the outlet gas temperature measuring device 15b. Therefore, in the present embodiment, the tube group included in the economizer 9 is not considered as the tube group to be removed from the adhered ash. As will be described later, an example in which the tube group included in the economizer 9 is also considered as a "plurality of tube groups 2" is a fourth modification of the present embodiment.

In the 3rd pass, a pipe group 2 composed of a hanging pipe (screen pipe) 21 is arranged at the uppermost flow (lowermost in the Y-axis direction) of the exhaust gas flow, and is downstream from the pipe group 21 (in the Y-axis direction). The tube group 2 composed of each of the superheater tubes (super heaters) 22a, 22b, and 22c is sequentially arranged toward the upper side).

FIG. 1 shows, as an example, a configuration in which the soot blower 3 (3a) is arranged between a plurality of tube groups 2 of the same type. That is, among the tube groups composed of superheated tubes, the tube group 2 composed of the superheated tube 22a located at the uppermost stream and the tube group arranged adjacent to the tube group 2 downstream of the tube group 2. The soot blower 3a is arranged between 2 (tube group 2 composed of superheated tubes 22b). The arrangement of the soot blower 3 (3a) is not limited to this, and among the pipe groups 2 composed of different types of pipe groups 2, for example, boiler screen pipes, superheat pipes, evaporation pipes, economizer water pipes, etc., they are adjacent to each other. The soot blower 3 may be arranged between different types of tubes arranged in the same manner. The soot blower 3 may be a steam type or a shock pulse type, but here, the description will proceed assuming that it is a shock pulse type soot blower.

The removal system 1 is a gas flow rate measuring device 16a arranged in two paths to measure the flow rate of the exhaust gas, and a gas flow rate measuring device arranged in the exhaust gas path between the dust removing device 11 and the attracting blower 13 to measure the flow rate of the exhaust gas. At least one of the devices 16b is provided. As described above, the exhaust gas path from the stoker 7 to the opening of the chimney 12 is substantially sealed. Therefore, by installing one gas flow rate measuring device, the heat transmission coefficient K described later can be calculated. Information on the gas flow rate of the required exhaust gas can be obtained.

The arrangement of the gas flow rate measuring devices 16a and 16b is not limited to these. At least one may be installed in the exhaust gas path. From the viewpoint of reducing the cleaning frequency of the gas flow rate measuring device, it is desirable to arrange the gas flow rate measuring device downstream from the dust removing device 11. That is, when selecting either one of the gas flow rate measuring devices 16a and 16b, it is desirable to install the gas flow rate measuring device 16b.
Further, instead of installing the gas flow rate measuring device 16a, the gas flow rate of the exhaust gas in the two passes may be calculated by calculation and used for the calculation of the heat transmission coefficient K described later.

The removal system 1 includes a superheat reducer (desuperheater) 17 that sprays water into the superheated pipe in order to appropriately cool the steam passing through the inside of the pipe group 2 composed of the superheated pipe. In FIG. 1, the superheat reducer 17 is arranged in the tube group 2 composed of the superheat tube 22c arranged at the most downstream of the four tube groups 2 arranged in the three paths. The amount of water sprayed by the overheat reducer 17 is measured by the spray water amount measuring device 18.

The removal system 1 is a steam temperature measuring device 24a that is arranged inside the superheating pipe 22a located at the uppermost stream among the superheating pipes included in the plurality of pipe groups 2 to be removed from the adhering ash and measures the steam temperature. (Inlet steam temperature measuring device) and a steam temperature measuring device 24b (outlet steam temperature measuring device) arranged inside the heating tube 22c located at the most downstream side and measuring the temperature of steam are provided. The steam temperature measuring devices 24a and 24b are installed in the superheated pipe among the plurality of pipe groups 2.

The removal system 1 includes a main steam amount measuring device 25 for measuring the amount of main steam flowing inside the superheater tube. Here, the main steam amount measuring device 25 is arranged inside the superheated pipe 22a located at the uppermost stream among the superheated pipes included in the plurality of pipe groups 2.
The removal system 1 includes a primary air supply device 26 located below the stoker 7, a secondary air supply device 27 located one path above the stoker 7, and these air supply devices 26, 27 to the exhaust gas path. It is provided with a combustion air amount measuring device 28 for measuring the total amount of the supplied primary air and secondary air (total amount of combustion air).

Each pressure measuring device 14a, 14b, each gas temperature measuring device 15a, 15b, gas flow rate measuring device 16a, 16b, sprayed water amount measuring device 18, each steam temperature measuring device 24a, 24b, main steam amount measuring device 25, combustion air amount. Various information measured by the measuring device 28 is input to the control device 4. The control device 4 is an electronic control device (computer) included in the removal system 1, and is equipped with a processor and a timer that operate with a clock, and a storage device (all not shown).

[3. Control configuration (flow chart)]
As described above, the control device 4 calculates the heat transmission coefficient K of the boiler, and in accordance with the heat transmission coefficient K, appropriately executes the adhesion ash determination process while starting the soot blower 3 "once" or ". "Continuous start".
Hereinafter, control (including adhesion ash determination processing) relating to activation of the soot blower 3 will be described in detail with reference to the flowcharts shown in FIGS. 2 and 3 (a) to 3 (d). Here, the dust removing device 11 will be described as a bug filter.

First, when the operator operates the start switch, control panel, etc. (not shown), the operation of the plant such as the incinerator is started, and the removal system 1 is also started, and the “start” of the flowchart shown in FIG. Each subsequent process is executed by the control device 4.
The initial values of time t1, Tmin, Tmax, and Δt, the initial value of dirty heat transmission coefficient Kd, the initial value of flag F, the predetermined values α1, α2, and the recovery threshold value R appearing in this flowchart are as follows. It is set and stored in the storage device in advance before the "start" of this flowchart.
Since the initial value of the clean heat transmission coefficient Kc is the value of the heat transmission coefficient calculated first when the removal system 1 is started, it is not necessary to set it in advance before the "start" of this flowchart.

The time t1 is the first time when the timer is counted down (the remaining time of the timer), and corresponds to the interval when the soot blower 3 is "started once". The initial value of the time t1 is a predetermined value that satisfies the relationship of “0 <Tmin <t1 ≦ Tmax”. Tmin is the minimum value (shortest interval) of the interval at which the soot blower 3 is activated, and is set to, for example, one hour. Further, Tmax is the maximum value (maximum interval) of the interval for activating the soot blower 3, and is set to, for example, 3 hours.
The initial value of the time t1 is set to the time obtained by, for example, "2/3 x Tmax-Δt (for example, Δt is 0.5 hours)". For the sake of simplicity, the values of Tmin and Tmax are set to integer multiples of Δt, respectively. Further, the time t1 is then changed from the initial value by steps S7 and S19 described later.

The dirty heat transmission coefficient Kd is a heat transmission coefficient when it is considered that the attached ash is deposited and contaminated on the pipe group 2 to be removed.
The initial value of the dirty heat transmission coefficient Kd is set to a predetermined value (for example, Kd = 0.5) that satisfies the relationship of “0 <Kd <α2”. The dirty heat transmission coefficient Kd is then changed from the initial value by step S3 described later.
The initial value of the flag F is set to F = 0 (first value). After that, the flag F is set to any one of F = 0 (first value), F = 1 (second value), and F = 2 (third value) according to steps S9, S20, and S14 described later. Is changed to.

The first predetermined value α1 and the second predetermined value α2 indicate that the soot blower 3 is “started once” in each of steps S5 and S15 described later, as compared with the heat transmission coefficient K (clean heat transmission coefficient Kc). It is a judgment threshold of whether or not to do. Further, the second predetermined value α2 is also a determination threshold value for whether or not to execute the adhesion ash determination process in comparison with the heat transmission coefficient K (clean heat transmission coefficient Kc) in step S15 described later. The relationship of "0 <α2 <α1" is satisfied. Here, for the sake of simplicity, the description will be continued assuming that the relationship of "0 <α2 <1 <α1" is satisfied.
The clean heat transmission coefficient Kc is a heat transmission coefficient calculated immediately after the start of the soot blower 3. In other words, the clean heat transmission coefficient Kc is the heat transmission coefficient when it is considered that the heat exchange rate has been improved by removing the attached ash of the tube group 2 to some extent because the soot blower 3 has just been activated. is there.
The first predetermined value α1 is set to a value at which it can be said that the heat exchange of the tube group 2 is clearly good and there is no deposit of adhered ash or the deposit of adhered ash is extremely small if the clean heat transmission coefficient is Kc of α1 or more. To. Here, for the sake of simplicity, the first predetermined value α1 is set to only “one-time activation” of the soot blower, that is, single-shot activation of the soot blower immediately after the flag F is changed to F = 2 in step S20 described later. The clean heat transmission coefficient Kc does not become α1 or more only by itself, and is set to a value that can be achieved only by activating the soot blower 3 continuously at least twice or more as "continuous activation". For example, the first predetermined value α1 is set to α1 = 1.2 (W / m ² K).
Further, if the second predetermined value α2 is a clean heat transmission coefficient Kc of α2 or more and less than α1, the heat exchange of the tube group 2 is clearly not good, but the accumulation of adhered ash is still in the operation of the plant. Since it does not have a large effect, it is set to a value that can be said to be sufficient if the soot blower is "started once". In other words, if the clean heat transmission coefficient Kc is less than α2, it is set to a value that requires the adhesion ash determination process described later. For the sake of simplicity of explanation here, the second predetermined value α2 is not limited to “one-time activation” of the soot blower 3, that is, only one-shot activation of the soot blower immediately after the flag F is changed to F = 2 in step S20 described later. The clean heat transmission coefficient Kc never becomes α2 or more, and is set to a value achieved only by starting the soot blower 3 continuously at least twice or more as “continuous start”. For example, the second predetermined value α2 is set to α2 = 0.8 (W / m ² K).
Therefore, in the flowchart of FIG. 2 described later, once the flag F is changed to F = 2 in step S20 described later, as a general rule, the control device unless the second determination is made in the adhesion ash determination process described later. According to 4, the soot blower 3 is "continuously activated" at least twice in a row.
Here, for the sake of simplicity of explanation, the values of α1 and α2 are set as described above assuming that the relationship of “0 <α2 <1 <α1” is satisfied, but as long as the relationship of “0 <α2 <α1” is satisfied, the design is performed. Therefore, the values of α1 and α2 may be set as appropriate. In this case, immediately after the flag F is changed to F = 2 in step S20 described later, the soot blower 3 is basically "continuously activated", but it is not always "continuously activated", and "1". It may be "started twice".
The recovery threshold value R is a threshold value for determining the effect of removing the adhered ash (the degree of improvement of the heat transmission coefficient K) as compared with the recovery rate (Kc / Kd), and the initial value thereof is the relationship of “1 ≦ R”. It is set to a predetermined value (for example, R = 1) that satisfies. Here, the recovery rate is a variable indicating how much the heat transmission coefficient K has recovered (improved) before and after the activation of the soot blower 3, and is a value obtained by dividing the clean heat transmission coefficient Kc by the dirty heat transmission coefficient Kd.
Each of the first predetermined value α1, the second predetermined value α2, and the recovery threshold value R is a constant that is not changed from the respective initial values appropriately set according to the design. Further, each of the above-mentioned Tmin, Tmax, and Δt is also a constant that is not changed from the respective initial values appropriately set according to the design.

In step S1, the control device 4 determines whether or not a predetermined time has elapsed after the start of operation of the plant (for example, an incinerator). This is because the environmental conditions (for example, temperature, pressure, etc.) in the plant are not stable until a predetermined time has passed since the operation of the plant was started. The control device 4 repeatedly executes the process of step S1 from the start of the operation of the plant until the predetermined time elapses, and executes the process of step S2 when the predetermined time elapses.

In step S2, the control device 4 calculates the heat transmission coefficient K based on the temperature information and the flow rate information. Then, after calculating the heat transmission coefficient K, the control device 4 executes the process of step S3.
The heat transmission coefficient K is represented by the following (Equation 1).

The temperature information and the flow rate information are measured as follows and transmitted to the control device 4. That is, the superheater inlet gas temperature Tgin is measured by the inlet gas temperature measuring device 15a, and the superheater outlet gas temperature Tgout is measured by the outlet gas temperature measuring device 15b. The superheater inlet steam temperature Tsin is measured by the inlet steam temperature measuring device 24a, and the superheater outlet steam temperature Tsout is measured by the outlet steam temperature measuring device 24b. Further, the gas flow rate Wg is measured by either one of the gas flow rate measuring devices 16a and 16b, or is acquired by calculation. The gas specific heat Cpg is the specific heat of the exhaust gas and is a constant corresponding to the components of the exhaust gas. Further, the heat transfer area A is the total heat transfer area of the superheater among the plurality of tube groups 2.

In step S3, the control device 4 sets the heat transmission coefficient K calculated in step S2 to either a clean heat transmission coefficient Kc or a dirty heat transmission coefficient Kd according to the value of the flag F at the time of processing in step S3. On the other hand, it is stored in a storage device (not shown).
Specifically, the control device 4 sets Kc = K when the flag F is the first value, here F = 0, and Kd = K when the flag F is the second value, here F = 1. Then, when the flag F is a third value, here F = 2, Kd = K is set and stored in the storage device.
Immediately after starting this flowchart, the flag F is an initial value, that is, F = 0, so that the control device 4 stores the heat transmission coefficient K calculated immediately before as a clean heat transmission coefficient Kc in the storage device (that is,). Kc = K).
Then, the control device 4 executes the process of step S4.

In step S4, the control device 4 determines whether or not the flag F is F = 0. When the flag F is F = 0, that is, immediately after the "start" of this flowchart, or immediately after the activation of the soot blower 3 in step S13 described later, the control device 4 executes the process of step S5.
When the flag F is not F = 0 (when F = 1 and F = 2), the control device 4 executes the process of step S10 in order to proceed with the processing flow toward the activation of the soot blower 3 in step S13 described later.

In step S5, the control device 4 determines whether or not the value of the clean heat transmission coefficient Kc stored in the storage device is equal to or higher than the first predetermined value α1.
When the value of the clean heat transmission coefficient Kc is equal to or higher than the first predetermined value α1, it is considered that the heat exchange of the tube group 2 is clearly good, and there is no or extremely little adhesion ash. Therefore, the control device 4 executes the process of step S6 in order to advance the process flow toward the process of changing the activation interval of the soot blower 3 for a long time.
When the value of the clean heat transmission coefficient Kc is less than α1, the heat exchange of the tube group 2 is not always good, so the control device 4 executes the process of step S15.

In step S6, the control device 4 determines whether or not the time t1 is less than Tmax, which is the longest interval.
When the value of the time t1 is less than Tmax (here, 3 hours), the control device 4 executes the process of step S7 in order to greatly change the value of the time t1 (longer the time t1).
When the value of the time t1 is Tmax, the time t1 cannot be changed any more. Therefore, the control device 4 executes the process of step S8 without changing the value of the time t1 (skipping step S7). ..

In step S7, the control device 4 changes the value of time t1 to the value of “t1 + Δt”. In other words, the control device 4 changes the value of t1 of the above storage device with t1 = t1 + Δt, and re-stores it in the storage device. That is, the control device 4 resets the interval longer than the value set immediately before.
If the clean heat transmission coefficient Kc is equal to or greater than the first predetermined value α1, the soot blower 3 will be activated excessively at the current interval, which is not desirable from the viewpoint of cost effectiveness. Therefore, the soot blower 3 has a longer interval than before. This is to perform "start once".
Then, the control device 4 executes the process of step S8.

The control device 4 starts the timer (counter) in step S8. The started timer counts down from the time t1 to 0 according to the clock provided in the control device 4. For example, if the time t1 at the time of starting is 2 hours, 2 hours (7200 seconds) are counted, and the timer is stopped when the count value becomes 0. After the timer is stopped, the control device 4 executes the process of step S9.

In step S9, the control device 4 changes the value of the flag F stored in the storage device to F = 1 and re-stores it in the storage device. Then, the control device 4 returns the processing flow to step S2, and executes the processing of step S2 again.
Since the processes of step S2, step S3, and step S4 have already been described, the processes from step S4 to the process of step S10 as the next step will be briefly described below.
That is, the control device 4 calculates the heat transmission coefficient K after setting an interval by the timer (step S2), and in the next step S3, since the flag F is F = 1, the heat transmission coefficient K calculated immediately before is calculated. Is stored in the above storage device as a dirty heat transmission coefficient Kd (that is, Kd = K). Then, since the flag F is F = 1 at the present time, the control device 4 determines that the flag F is not F = 0 in step S4, and executes the process of step S10 as the next process.

In step S10, the control device 4 determines whether or not the bug filter, which is the dust removing device 11, is backwashing. Since the control device 4 controls the execution of the "backwash" of the bug filter, it is possible to determine whether or not the bug filter is in the backwash.
When it is determined that the bug filter is being backwashed, the control device 4 repeatedly executes the process of step S10, and when it is determined that the bug filter is not being backwashed, the control device 4 executes the process of step S11. As a result, the control device 4 can start the soot blower 3 after waiting for the end of the back wash without starting the soot blower 3 while the backwash of the bug filter is being executed.

The reason why the control device 4 repeats the process of step S10 when it is determined that the bug filter is in the process of backwashing is as follows.
Backwashing of the bug filter is usually done by stopping the flow of exhaust gas. Therefore, if the shock pulse type soot blower 3 is activated during the backwashing of the bag filter, the pressure inside the duct serving as the flue through which the exhaust gas flows increases remarkably, which may cause a failure in the plant. However, in the removal system 1, the control device 4 does not start the soot blower 3 during the backwashing of the bug filter, but waits for the end of the backwash to start the sootblower 3, so that the above-mentioned failure can be prevented.
Here, since the soot blower 3 is described as being of the shock pulse type, step S10 is provided, but when the soot blower 3 is of the steam type, step S10 can be omitted. Therefore, in this case, the step next to step S4 is step S11.

In step S11, the control device 4 determines whether or not the value of the flag F stored in the storage device is F = 1. When the flag F is F = 1, the control device 4 executes the process of step S12. Further, when the flag F is not F = 1, that is, when F = 2, the control device 4 executes the process of step S13.
Here, since the flag F is F = 1 at the present time, the control device 4 executes the process of step S12. In step S12, the control device 4 returns the count value of the timer to the time t1, that is, resets it. Next, the control device 4 executes the process of step S13.
The control device 4 activates the soot blower 3 only once in step 13.
Then, the control device 4 executes the process of step S14.
In step S11, when the flag F is not F = 1, that is, when F = 2, the control device 4 skips step S12 and executes the process of step S13, so that the timer count value is not reset. .. In the case of F = 2, the control device 4 generally executes "continuous activation" of the soot blower 3 until the clean heat transmission coefficient Kc becomes the second predetermined value α2 or more, but at this time, even one process is performed. This is because the soot blower 3 is started continuously at a higher speed.

In step S14, the control device 4 changes the value of the flag F stored in the storage device to F = 0 and re-stores it in the storage device. This is because the heat transmission coefficient K calculated in the process of the next step S2 is the value immediately after the start of the soot blower 3, so this value is used as the clean heat transmission coefficient Kc in the process of the next step S3 as described above. This is to store in a storage device.
Then, the control device 4 returns the processing flow to step S2 and executes the processing of step S2. Since the processes of step S2, step S3, step S4, and step S5 have already been described, the description thereof will be omitted again.

From this, a case where the process of step S15 is executed by the control device 4 as the next step of step S5 (when the value of the clean heat transmission coefficient Kc is less than α1 in step S5) will be described.
In step S15, the control device 4 determines whether or not the value of the clean heat transmission coefficient Kc stored in the storage device is less than the second predetermined value α2.
When the value of the clean heat transmission coefficient Kc is not less than the second predetermined value α2, that is, when α2 ≦ Kc <α1, the heat conduction of the tube group 2 is not clearly good, but the deposition of adhered ash is caused by the plant. Since it is considered that the operation is not significantly affected yet, the control device 4 executes the process of step S8 described above in order to proceed to the process flow for activating the soot blower 3 at intervals.
When the value of the clean heat transmission coefficient Kc is less than the second predetermined value α2, the control device 4 performs the process of step S16 in order to determine whether or not the value of the clean heat transmission coefficient Kc is lowered due to the adhered ash. That is, the adhered ash determination process is executed.

The control device 4 executes the adhesion ash determination process in step S16. An example of a specific treatment in the adhesion ash determination treatment will be described later with reference to FIG.
In the adhering ash determination process, "the amount of adhering ash deposited on the plurality of pipe groups 2 is large, and the heat exchange between the exhaust gas and the boiler is not sufficiently performed" (first judgment), or "adhered ash". Although the amount of heat exchange is small and does not adversely affect heat exchange, the clean heat transmission coefficient Kc is calculated to be less than the second predetermined value α2 depending on the operating environment of the plant or various operating conditions. " This is a process of selectively selecting and judging one of (second judgment).
When the first determination is obtained in the adhered ash determination process, the control device 4 executes the process of step S17 in order to continuously activate the soot blower 3 according to the recovery rate (Kc / Kd).
When the second determination is obtained in the adhered ash determination process, the control device 4 executes the process of step S21 in order to confirm the state of the plant or determine whether or not the plant should be stopped.

In step S17, the control device 4 calculates a recovery rate (Kc / Kd) from the clean heat transmission coefficient Kc and the dirty heat transmission coefficient Kd stored in the storage device, and this recovery rate is the storage device described above. It is determined whether or not it is equal to or higher than the recovery threshold value R stored in.
If the recovery rate is less than the recovery threshold value R, it is unlikely that the heat transmission coefficient K will improve even if the soot blower 3 is started any more. Therefore, the control device 4 executes the process of step S21.
When the recovery rate is equal to or higher than the recovery threshold value R, the effect of removing the adhering ash can be expected by activating the soot blower 3. In order to proceed, the control device 4 executes the process of step S18.

In step S18, the control device 4 determines whether or not the time t1 is larger than Tmin, which is the shortest interval.
When the time t1 is larger than Tmin, the control device 4 executes the process of step S19 in order to shorten the interval when the soot blower 3 is "started once". Due to the nature of the ash, the attached ash could not be effectively removed in the initial "one-time start" interval. Therefore, in view of the fact that the first judgment was obtained in the attached ash judgment process, after the "continuous start" was completed, This is because when the control device 4 "starts" the soot blower 3 "once", the soot blower 3 is "started once" at a shorter interval than before (in other words, at a timing earlier than before).
In step S19, the control device 4 changes the value of time t1 to the value of “t1-Δt”. In other words, the control device 4 changes the value of t1 of the above storage device with t1 = t1-Δt, and re-stores it in the storage device. Then, the control device 4 executes the process of step S20.
When the time t1 is Tmin, the time t1 cannot be changed any more. Therefore, the control device 4 executes the process of step S20 without changing the value of the time t1 (skipping step S19).

In step S20, the control device 4 changes the value of the flag F stored in the storage device to F = 2 and re-stores it in the storage device. Then, the control device 4 returns the processing flow to step S2 and executes the processing of step S2.
Since the processes of step S2, step S3, and step S4 have already been described, the processes from step S4 to the process of step S10 as the next step will be briefly described below.
That is, the control device 4 calculates the heat transmission coefficient K when the recovery rate is equal to or higher than the recovery threshold value R (step S2), and in the next step S3, since the flag F is F = 2, the heat transmission flow calculated immediately before is calculated. The rate K is stored in the above storage device as a dirty heat transmission coefficient Kd (that is, Kd = K). Then, in the next step S4, since the flag F is F = 2 at the present time, the control device 4 determines that the flag F is not F = 0, and executes the next step S10. Then, in step S10, the control device 4 executes the process of step S11 when it is determined that the bug filter is not in the backwash. In step S11, since the flag F is F = 2 at the present time, the control device 4 skips step S12 and executes the process of step S13.
That is, when the flag F is F = 2, the control device 4 executes the process of step S13 in order to immediately start the soot blower 3 without resetting the timer.

After activating the soot blower 3 in step S13, as described above, the control device 4 changes the flag F to F = 0 in step S14, and returns the processing flow to step S2 again.
Here, in the next processing flow, step S2, step S3, step S4, step S5, step S15, step S16, step S17, step S18, step S19 (which is skipped in some cases), step S20, and so on. When the control device 4 proceeds with the process in sequence, the control device 4 then proceeds with the processes of step S2, step S3, step S4, step S10, step S11, and step S13.
Therefore, in this case, since the processing flow is such that step S13 is executed without going through the timer start of step S8, the soot blower 3 is "continuously started".

Then, as an explanation of the flowchart of FIG. 2, finally, when the second determination is obtained by the adhesion ash determination process in step S16, or when the recovery rate is less than the recovery threshold value R in step S17, the control device 4 The step S21 to be executed will be described.
In step S21, the control device 4 determines whether or not the operator or worker has started the work for checking the state of the plant or stopping the operation of the plant (for example, operating the control panel). Since the control device 4 controls the operation of various devices arranged in the plant, it is possible to determine whether or not the work has been started.
When the control device 4 determines that the work has not been started, the control device 4 executes the process of step S8. That is, in this case, since it has been found that the soot blower 3 cannot be effectively removed even if the soot blower 3 is started in step S17, the soot blower 3 is not "continuously started" from the viewpoint of cost effectiveness. In order to reduce the further accumulation of ash on the tube group 2, the process flow for executing the "one-time activation" of the soot blower 3 is advanced.
On the other hand, when it is determined that the work has been started, the control device 4 does not execute any of the processes of steps S1 to S20, and then executes another process necessary for the work. After that, the operation of the entire removal system 1 including the control device 4 is completed, that is, the operation of the plant is stopped.

According to this flowchart, when the soot blower 3 that sets the interval by the timer is "started once", if the clean heat transmission coefficient Kc is equal to or more than the first predetermined value α1, the interval is made longer than the previous interval to clean. When the heat transmission coefficient Kc is less than the first predetermined value α1, the interval is not changed from the previous interval, or the interval is shortened from the previous interval.
Further, according to this flowchart, even in the case of "continuous activation" of the soot blower 3 without an interval by the timer, the heat transmission coefficient K is calculated every time the soot blower 3 is activated. Then, in the control device 4, as long as the value of the recovery rate R based on the calculated heat transmission coefficient K (clean heat transmission coefficient Kc, dirty heat transmission coefficient Kd) increases, the clean heat transmission coefficient Kc becomes the second predetermined value α2. Until the above is reached, the "continuous activation" of the soot blower 3 is executed.
That is, the number of activations of the soot blower 3 in "continuous activation" is variable, and if the value of the recovery rate R ascending speed is large (if the ascending speed is fast), the number of times is automatically reduced and the ascending is performed. If the speed value is small (the climbing speed is slow), the number of times is automatically increased.
The ascending speed is the value of the recovery rate calculated each time the control device 4 executes step S17 and the time information at the time of calculation are sequentially stored in the above storage device, and the value of the recovery rate calculated at the present time is used. It can be obtained by calculation using the value of the latest recovery rate and the value of the difference (time interval or time difference) between the two time information. Specifically, the control device 4 calculates the ascending speed by the equation [{(recovery rate calculated at present time)-(recent recovery rate)} / (time difference)]. If the gas refill time of the shock pulse type soot blower is, for example, less than 3 minutes (3 min), the ascending speed is high, for example, the number of "continuous activations" is 2 times (less than 6 min) or 3 times. When the ascending speed ending in (less than 9 min) is 0.04 (/ min) or more, and the ascending speed is slow, for example, the number of ascending times requires 4 times or more (12 min or more). This is the case when the speed is less than 0.04 (/ min).

Next, the details of the adhered ash determination process, that is, step S16, will be described with reference to FIGS. 3 (a) to 3 (d).
Here, based on the experience of the inventor, only the above-mentioned four conditions are targeted, and the following four patterns will be described according to how many of these conditions are used. However, as described above, in addition to the above four conditions, other conditions may be added depending on the design.
In the following description, it is assumed that the control device 4 executes the process of step S161 as the next process of step S15 of FIG.
Then, explanations will be given sequentially from FIG. 3A.
FIG. 3A is a processing flow (pattern 1) in which the adhering ash determination processing is executed based on all the four conditions described above. The control device 4 determines whether or not the main steam amount Qs measured by the main steam amount measuring device 25 in step S161 is equal to or greater than the lower limit main steam amount qsmin (first threshold value) allowed in the operation of the plant. judge. When the main steam amount Qs is less than qsmin, the control device 4 assumes that the "second determination" is obtained, and then executes the process of step S21 of FIG. When the main steam amount Qs is qsmin or more, the control device 4 executes the process of the next step, here, step S162.

The control device 4 calculates the pressure difference of the exhaust gas at the inlet and outlet of the plurality of pipe groups 2, that is, the gas differential pressure ΔPg in the furnace, using the pressure information measured by the pressure measuring devices 14a and 14b in step S162. Then, it is determined whether or not the gas differential pressure ΔPg in the furnace is equal to or higher than the lower limit gas differential pressure pgmin (second threshold) allowed in the operation of the plant. When the gas differential pressure ΔPg in the furnace is less than pgmin, the control device 4 assumes that the “second determination” is obtained, and then executes the process of step S21 in FIG. When the gas differential pressure ΔPg in the furnace is pgmin or more, the control device 4 executes the process of the next step, here, step S163.

In step S163, the control device 4 determines whether or not the rotation speed Qr of the induction blower 13 is equal to or higher than the lower limit rotation speed qrmin (third threshold value) allowed in the operation of the plant. When the rotation speed Qr is less than qrmin, the control device 4 assumes that the "second determination" is obtained, and then executes the process of step S21 of FIG. When the rotation speed Qr is qrmin or more, the control device 4 executes the process of the next step, here, step S164. Since the control device 4 controls the rotation speed Qr of the attracting blower 13, the rotation speed Qr is grasped.

The control device 4 determines whether or not the total amount of combustion air Qc measured by the combustion air amount measuring device 28 in step S164 is equal to or greater than the lower limit of the total amount of combustion air qcmin (fourth threshold value) allowed in the operation of the plant. judge. When the total amount of combustion air Qc is less than qcmin, the control device 4 assumes that the "second determination" is obtained, and then executes the process of step S21 of FIG. When the total amount of combustion air Qc is qcmin or more, the control device 4 executes the process of the next step. Here, assuming that the "first determination" is obtained, the process of step S17 of FIG. 2 is executed next.
The order of the processing flows of the four processes of steps S161 to S164 is not limited to this, and may be changed as appropriate.

The processing flow (pattern 2) of FIG. 3B executes the three determination elements of steps S161 to S163 among the four determination elements included in the processing flow of FIG. 3A. FIG. 3B is an example of a flowchart in which the adhesion ash determination process is executed based on any three of the above four conditions, and any three of the four determination elements in steps S161 to S164 are used. May be used, and the order of processing may come first.

The processing flow (pattern 3) of FIG. 3C executes two determination elements of steps S161 and S162 among the four determination elements included in the processing flow of FIG. 3A. FIG. 3C is an example of a processing flow in which the adhering ash determination processing is executed based on any two of the above four conditions, and is any two of the four determination elements of steps S161 to S164. One may be used, and the order of determination may be first.

The processing flow (pattern 4) of FIG. 3D executes only the determination element of step S161 among the four determination elements included in the processing flow of FIG. 3A. FIG. 3D is an example of a flowchart in which the adhesion ash determination process is executed based on any one of the above four conditions, and is one of the four determination elements in steps S161 to S164. May be used.
In any of the above patterns 1 to 4, it is preferable to include step S161 that uses the information of the main steam amount Qs that is not used in the calculation of the heat transmission coefficient K.

[4. effect]
As described above, in the removal system 1, the control device 4 properly uses the “one-time activation” and the “continuous activation” of the soot blower 3 based on the calculated heat transmission coefficient K, so that the efficiency can be ensured at an early stage. Adhering ash can be removed appropriately.

The adhering ash determination process includes conditions based on the inventor's experience, that is, conditions based on at least one of the main steam amount Qc, the gas differential pressure ΔPg in the furnace, the rotation speed Qr of the attracting blower 13, and the total combustion air amount Qc. Since it is executed, the state of accumulation of attached ash on the tube group 2 can be appropriately determined.

In the removal system 1, when the first judgment is obtained by the adhesion ash judgment process, the recovery rate is calculated from the dirty heat transmission rate Kd and the clean heat transmission rate Kc, and when the recovery rate is equal to or higher than the recovery threshold value R, the soot blower Adhering ash can be removed at an early stage by "continuously starting" 3.
Further, in the removal system 1, the control device 4 automatically reduces the number of activations of the soot blower 3 in "continuous activation" when the increase rate of the recovery rate is large, and the number of times when the increase rate of the recovery rate is small. Is automatically increased. Therefore, the control device 4 appropriately increases or decreases the number of activations of the soot blower 3 in the "continuous activation" according to the condition of the adhered ash, so that the adhered ash is more effective than the case where the number of times is a fixed value. It can be removed and economic efficiency can be guaranteed.

According to the removal system 1, when the clean heat transmission coefficient Kc is equal to or higher than the first predetermined value α, the control device 4 determines that the heat conduction of the tube group 2 is extremely good (no or very little adhered ash is accumulated). Since the interval of "one-time activation" is reset to a long time, it is possible to avoid excessive activation of the soot blower 3, and as a result, the economic efficiency can be further secured. On the other hand, when the recovery rate is equal to or higher than the recovery threshold value R, the interval of the "single start" following the end of the "continuous start" is reset short, so that the ash is so adherent that "continuous start" is required. Even with the above properties, since the soot blower 3 is "started once" at short intervals, the attached ash can be removed before the ash is thickly deposited on the tube group 2. Therefore, it is not necessary to frequently perform "continuous activation", and as a result, economic efficiency can be further secured.

According to the removal system 1, the control device 4 does not start the soot blower 3 while the backwash of the bug filter as the dust remover 11 is being executed, but waits for the end of the backwash to start the sootblower 3. , It is possible to avoid the failure of the plant.

The soot blower 3 may be either a steam type or a shock pulse type. However, since the steam type soot blower uses steam generated by heat exchange between the exhaust gas and the boiler, the amount of steam supplied by the boiler to the turbine for power generation is reduced, and as a result, the amount of power generated in the plant is reduced. Can be done. Therefore, when the amount of power generated by the plant is important, it is desirable to arrange a shock pulse type soot blower that does not use steam.

The soot blower 3 is usually installed on a wall surface such as a duct forming a path for exhaust gas. Therefore, when the soot blower 3 of FIG. 1 is a steam type, the direction in which the injection nozzle of the soot blower 3 expands and contracts is a direction on a plane including the X axis and orthogonal to the Y axis, and from the injection nozzle to the Y axis direction. Inject steam.
On the other hand, when the soot blower 3 is of the shock pulse type, the injection direction of the shock pulse is a direction on a plane including the X axis and orthogonal to the Y axis.
Therefore, in the case of the removal system 1 provided with the shock pulse type soot blower 3, if a shock pulse is emitted toward the wall surface between the 3rd pass and the 2nd pass in FIG. 1, the wall surface is vibrated and the tube group 2 Not only the adhered ash but also the ash adhering to the wall surface can be removed.

[5. Modification example]
Hereinafter, a modified example of the removal system 1 having a plurality of soot blowers 3 will be described. The first modification is an example in which the soot blower indicated by the dotted line 3'and the reference 3 "is used in FIG. 1. The second modification is an example as shown in FIGS. 4 (a) to 4 (c). This is an example in which the number of pipe groups 2 arranged in the three paths of FIG. 1 is larger than that of FIG. 1. The third modification is an example in which the boiler structure of the plant is a tail end type as shown in FIG. In the fourth modification, as shown in FIG. 6, the boiler structure of the plant is an example of a two-drum type boiler.
In the following description, the same elements as the removal system 1 of FIG. 1 described above are designated by the same reference numerals, and duplicate description will be omitted. Note that in FIGS. 5 and 6, the control device 4 shown in FIG. 1 and the signal line (thin solid line) input to or output from the control device 4 are not shown.

[5-1. First modification]
In FIG. 1, a removal system 1 in which only one soot blower 3 is arranged has been described as an embodiment, but a removal system 1 ′ in which a plurality of soot blowers 3 are arranged depends on the number of pipe groups 2 or the design of the plant. It is also possible to do.
The soot blower 3 generally effectively removes the adhering ash of the tube group 2 placed in close proximity to it. Therefore, in the configuration of the removal system 1, the attached ash of the two pipe groups 2 (the pipe group 2 composed of the superheated pipes 22a and 22b) in the vicinity of the soot blower 3a is effectively removed. .. However, since the tube group 2 composed of the superheated tube 22c located at the most downstream position is arranged at a position away from the soot blower 3a, there is a possibility that the removal of the adhered ash of the tube group 2 (22c) is insufficient. is there.

Therefore, as shown by the dotted line in FIG. 1, in the removal system 1', in addition to the soot blower 3a, the position of the wake of the tube group 2 (22c) [next to the tube group 2 (22c) and in the Y-axis direction. By separately arranging the soot blower 3'on the above], the attached ash of the tube group 2 (22c) can be effectively removed.
At this time, if the soot blower arranged separately from the soot blower 3a is a shock pulse type soot blower, the soot blower is placed at the position indicated by the reference numeral 3 "in place of the soot blower indicated by the reference numeral 3'or together with the soot blower indicated by the reference numeral 3'. It may be arranged. The soot blower 3 ″ shown by the broken line in FIG. 1 indicates a soot blower installed near the wall surface of the ceiling of 3 passes, and is arranged so as to emit a shock pulse in the Y-axis direction and downward. For example, not only the tube group 2 (22c) but also the adhered ash of the tube group 2 (22b) arranged upstream thereof can be removed more effectively.

Even when a plurality of soot blowers 3, 3', 3 "are arranged in the removal system 1', the control device 4 is used for each soot blower as in the above-described configuration in which only one soot blower 3 is arranged. , The process of FIG. 2 is executed.
However, in the process of step S13, the control device 4 shifts the start timing of each of the soot blowers 3, 3 ′, and 3 ″, and starts them one by one in order. That is, the control device 4 starts. , Do not start the plurality of soot blowers 3, 3', 3 "at the same time.
When a plurality of steam type soot blowers are arranged and started at the same time, the steam supplied from the boiler to the turbine is significantly reduced, so that the amount of power generation is significantly reduced and stable power transmission becomes difficult. In addition, if a plurality of shock pulse type soot blowers are arranged and started at the same time, the pressure inside the furnace and the pressure inside the duct may rise remarkably, and a failure may occur in the plant.
Therefore, in the removal system 1', the activation of these soot blowers 3 is staggered in time and sequentially activated.
Since the order in which the control device 4 sequentially activates the plurality of soot blowers 3 is the same as that of the second modification shown in FIG. 4 described later, the description thereof will be omitted.

[5-2. Second variant]
In the removal systems 1A to 1C of the second modification shown in FIGS. 4A to 4C, the number of tube groups 2, the number of soot blowers 3, and the arrangement of the outlet steam temperature measuring device 24b are different from those of the removal system 1. different. In the second modification, a plurality of pipe groups 2 are arranged in the Y-axis direction, that is, in the vertical direction, and a plurality of soot blowers 3 are arranged. FIG. 4A is a removal system 1A in which four tube groups 2 composed of superheated tubes 22 are arranged in the three paths of FIG. FIG. 4B is a removal system 1B in which five tube groups 2 composed of superheated tubes 22 are arranged in the three paths of FIG. FIG. 4C is a removal system 1C in which six tube groups 2 composed of superheated tubes 22 are arranged in the three paths of FIG.
In the second modification as well, as in the first modification, the control device 4 executes the process of FIG. 2 for each of the plurality of soot blowers.

In the removal system 1A shown in FIG. 4A, in addition to the configuration of FIG. 1, the superheated pipes are arranged adjacent to each other downstream (in the Y-axis direction and upward) of the pipe group 2 composed of the superheated pipes 22c. The tube group 2 composed of 22d is arranged. Further, the soot blower 3b is arranged between the tube group 2 composed of the superheated tube 22c and the tube group 2 composed of the superheated tube 22d.
In the removal system 1C shown in FIG. 4 (c), in addition to the configuration of FIG. 4 (a), the removal system 1C is arranged adjacent to the pipe group 2 composed of the superheat pipe 22d and is composed of the superheat pipe 22e. The tube group 2 and the tube group 2 arranged adjacent to the tube group 2 downstream of the tube group 2 (in the Y-axis direction and above) and composed of the superheated tube 22f are further arranged. Further, the soot blower 3d is arranged between the tube group 2 composed of the superheated tube 22e and the tube group 2 composed of the superheated tube 22f.
As shown in FIGS. 4 (a) and 4 (c), when the number of tube groups 2 (here, tube group 2 composed of superheated tubes 22) for removing adhering ash with the soot blower 3 is plural and even. , The soot blower 3 is not placed in all of the pipe groups 2 of the target. In consideration of the cost-effectiveness of removing the adhering ash, a set of two pipe groups 2 in order from the upstream pipe group 2 of the target pipe group 2 is formed, and one soot blower 3 is provided for each unit. Deploy. Therefore, the number of the plurality of soot blowers 3 to be arranged is half of the number of the target tube group 2.

On the other hand, in the removal system 1B shown in FIG. 4B, unlike FIG. 4C, the removal system 1B is arranged adjacent to the downstream (Y-axis direction and upward) of the tube group 2 composed of the superheated tubes 22d. , Only the tube group 2 composed of the superheated tube 22e is added to the configuration of FIG. 4A. Therefore, in FIG. 4B, the number of tube groups 2 (tube group 2 composed of superheated tubes 22) from which the adhering ash is removed by the soot blower 3 is plural and odd. In this case, a tube group 2 in which the above-mentioned "unit" cannot be formed is generated. In FIG. 4B, the above-mentioned "unit" cannot be formed for the tube group 2 composed of the superheated tube 22e.
However, if the adhered ash of the tube group 2 composed of the superheated tube 22e cannot be overlooked, the soot blower 3c is arranged downstream of the tube group 2.

In the above second modification, the tube group 2 to be removed from the adhered ash is arranged in the vertical direction (Y-axis direction). Then, the outlet steam temperature measuring device 24b is arranged inside the superheated pipe 22 constituting the pipe group 2 located at the most downstream side.
When a certain soot blower 3 is activated and the attached ash is removed, the movement of the removed attached ash is as follows: [1] when it falls vertically and downward due to gravity, and [2] the flow of exhaust gas is strong and the exhaust gas is exhausted. There are two possible situations when moving to the wake along the flow of.
Therefore, in the case of [1], when the control device 4 “starts once” or “continuously starts” the soot blower 3, the timing is directed from the soot blower 3 arranged at the most downstream toward the soot blower 3 arranged at the upstream. Start in order by shifting. That is, in the case of FIG. 4A, the soot blower 3a is started after the soot blower 3b is started. Further, in the case of FIG. 4B, after starting the soot blower 3c, the soot blower 3b is started, the soot blower 3b is started, and then the soot blower 3a is started. Similarly, in the case of FIG. 4C, the soot blower 3d is started, then the soot blower 3b is started, the soot blower 3b is started, and then the soot blower 3a is started.
By activating each soot blower 3 in this order, even when the attached ash removed by the soot blower 3 in a certain tube group 2 falls downward due to gravity and reattaches to another tube group arranged upstream. , The adhering ash that has reattached can be reliably removed.
On the other hand, in the case of [2], when the control device 4 “starts once” or “continuously starts” the soot blower 3, the timing is directed from the soot blower 3 arranged at the uppermost stream toward the soot blower 3 arranged downstream. Start in order by shifting. That is, in the case of FIG. 4A, after starting the soot blower 3a, the soot blower 3b is started. Further, in the case of FIG. 4B, after starting the soot blower 3a, the soot blower 3b is started, the soot blower 3b is started, and then the soot blower 3c is started. Similarly, in the case of FIG. 4C, the soot blower 3a is started, then the soot blower 3b is started, the soot blower 3b is started, and then the soot blower 3d is started.
By activating each soot blower 3 in this order, the adhering ash removed by the soot blower 3 in one tube group 2 moves downstream along with the flow of exhaust gas and reattaches to another tube group arranged downstream. Even in such a case, the adhering ash that has reattached can be reliably removed.

In the second modification, the configurations corresponding to the first tube group, the second tube group, the third tube group, the fourth tube group, the first soot blower, and the second soot blower in claim 6 of the present application are as follows. Is.
That is, in FIGS. 4 (a) and 4 (b), the tube group 2 composed of the superheated tube 22a is the first tube group, the tube group 2 composed of the superheated tube 22b is the second tube group, and the superheated tube 22c. The tube group 2 composed of is corresponding to the third tube group, and the tube group 2 composed of the superheated tube 22d corresponds to the fourth tube group. Further, the soot blower 3a corresponds to the first soot blower, and the soot blower 3b corresponds to the second soot blower. In FIG. 4 (c), in addition to the same cases as in FIGS. 4 (a) and 4 (b), the tube group 2 composed of the superheated tube 22c is the first tube group, and the tube group 2 composed of the superheated tube 22d. Is the second tube group, the tube group 2 composed of the superheated tube 22e is the third tube group, the tube group 2 composed of the superheated tube 22f is the fourth tube group, the soot blower 3b is the first soot blower, and the soot blower 3d is the second. It may correspond to a soot blower.

[5-3. Third variant]
Next, a third modification will be described with reference to FIG.
In the removal system 1D of the third modification, an exhaust gas flow path extending in the horizontal direction (X-axis direction) is added between the three paths in FIG. 1 and the economizer 9, and a plurality of flow paths in the horizontal direction are also added. The tube group 2 of the above is arranged, and a plurality of soot blowers 3 are arranged. The boiler structure of the plant in the third modification is called the tail end type. Then, the outlet steam temperature measuring device 24b is arranged inside the superheated pipe 22f constituting the pipe group 2 located at the most downstream side.
In the third modification, in the configuration of FIG. 4C, which is one of the second modifications, the soot blower 3b covers the tube group 2 composed of the superheated tube 22c to the tube group 2 composed of the superheated tube 22f. 3d is included, and the configuration is arranged in the horizontal direction without changing the order from upstream to downstream. Here, it is considered that the tube group 2 composed of the superheated tube 22b and the tube group 2 composed of the superheated tube 22c are arranged adjacent to each other as in the second modification.
Therefore, in the third modification, a plurality of pipe groups 2 sequentially arranged from upstream (Y-axis direction and downward) to downstream (Y-axis direction and upward) in the vertical direction and one direction (X) in the horizontal direction. There are a plurality of tube groups 2 sequentially arranged in the axial direction).
In the third modification as well, the control device 4 executes the process of FIG. 2 for each of the plurality of soot blowers, as in the first modification and the second modification.

Here, a plurality of tube groups 2 sequentially arranged in one direction (X-axis direction) in the horizontal direction, that is, the tube group 2 composed of the superheated tube 22c in FIG. 5 and the tube composed of the superheated tube 22d. Focusing on the group 2, the tube group 2 composed of the superheated tube 22e, and the tube group 2 composed of the superheated tube 22f, when the soot blower 3b or 3d is started to remove the adhering ash, the adhering ash is removed. Is likely to move to the wake along the flow of exhaust gas.
Therefore, when the soot blower 3 is "started once" or "continuously started", the control device 4 is started in order from the soot blower 3 arranged at the uppermost stream toward the soot blower 3 arranged downstream. To do. That is, the control device 4 activates the soot blower 3d and then activates the soot blower 3d.
By activating each soot blower 3 in this order, the adhering ash removed by the soot blower 3 in one tube group 2 moves downstream along with the flow of exhaust gas and reattaches to another tube group arranged downstream. Even in such a case, the adhering ash that has reattached can be reliably removed.

Further, in FIG. 5, when the plurality of pipe groups 2 arranged in the horizontal direction and the plurality of pipe groups 2 arranged in the vertical direction are comprehensively considered, the case of [2] described in the second modification is described. Therefore, when the soot blower 3 is "started once" or "continuously started", the control device 4 shifts the timing from the soot blower 3 arranged at the uppermost stream toward the soot blower 3 arranged downstream. And start in order. That is, the control device 4 activates the soot blower 3a, then activates the soot blower 3b, activates the soot blower 3b, and then activates the soot blower 3d.
By activating each soot blower 3 in this order, the adhering ash removed by the soot blower 3 in one tube group 2 moves downstream along with the flow of exhaust gas and reattaches to another tube group arranged downstream. Even in such a case, the adhering ash that has reattached can be reliably removed.

In the third modification, the configurations corresponding to the first tube group, the second tube group, the third tube group, the fourth tube group, the first soot blower, and the second soot blower in claim 6 of the present application are as follows. Is.
That is, when focusing on a plurality of tube groups 2 arranged in the horizontal direction, the tube group 2 composed of the superheated tube 22c is the first tube group, and the tube group 2 composed of the superheated tube 22d is the second tube group. The tube group 2 composed of the superheated tube 22e corresponds to the third tube group, the tube group 2 composed of the superheated tube 22f corresponds to the fourth tube group, the soot blower 3b corresponds to the first soot blower, and the soot blower 3d corresponds to the second soot blower.
Further, when comprehensively considering the plurality of pipe groups 2 arranged in the horizontal direction and the plurality of pipe groups 2 arranged in the vertical direction, in FIG. 5, the pipe group 2 composed of the superheated pipe 22a is The first tube group, the tube group 2 composed of the superheated tube 22b is the second tube group, the tube group 2 composed of the superheated tube 22c is the third tube group, and the tube group 2 composed of the superheated tube 22d is the fourth tube group. The tube group, the soot blower 3a corresponds to the first soot blower, and the soot blower 3b corresponds to the second soot blower.
According to the removal system 1D of the third modification, in addition to the effect obtained in the above embodiment, the adhered ash including the reattached adhered ash can be reliably removed.

[5-4. Fourth variant]
Next, the fourth modification will be described with reference to FIG.
In the third modification, the removal system 1E of the fourth modification removes the exhaust gas flow path extending in the horizontal direction between the three paths and the economizer 9, but instead removes the steam drum between the three paths and the economizer 9. It is a configuration in which a two-drum type boiler equipped with 19 and a water drum 20 is installed. Since the flow path is removed, the pipe groups 2 (22c to 22f) and the soot blower 3 (3b, 3d) arranged in the flow path in the third modification are also removed.
Further, in the fourth modification, the suspension pipe 21 and the soot blower 3a of the third modification are removed, the superheat pipes 22a and 22b are suspended from the ceiling of three passes, and the superheat pipe 22a is arranged upstream of the superheat pipe 22a. The soot blower 3 (3e) is placed adjacent to the.
Further, in FIG. 1, the tube group 2 of the economizer 9 was not considered as the tube group to be removed from the attached ash, but in the fourth modification, the plurality of tube groups 2 of the economizer 9 are also to be removed from the attached ash. And. Therefore, a plurality of pipe groups 2 arranged in the vertical direction (Y-axis direction) inside the economizer 9, that is, the pipe group 2 composed of the water pipe 23a and the pipe group 2 adjacent to the pipe group 2 and arranged downstream thereof. Moreover, the soot blower 3f is installed between the pipe group 2 and the water pipe 23b.
In this case as well, as described above, the "plurality of tube groups 2" to be removed from the adhering ash is between the two pressure measuring devices 14a and 14b and between the two gas temperature measuring devices 15a and 15b. It is placed in between.
In FIG. 6, the pipe group 2 to be removed from the adhered ash includes a different type of pipe group 2, that is, a pipe group 2 composed of a superheated pipe 22, and a pipe group 2 composed of a water pipe 23. Another pipe group 2 that acts as a resistance to the flow of exhaust gas is arranged between the pipe group 2 composed of the superheated pipe 22 (22b) and the pipe group 2 composed of the water pipe 23 (23a). Absent.
Then, unlike FIG. 1, the temperature measuring device 15b for measuring the temperature of the exhaust gas at the “outlet” of the plurality of pipe groups 2 is arranged most downstream among the plurality of pipe groups 2 to be removed from the adhering ash. It is arranged downstream of the pipe group 2 composed of the water pipe 23b. In FIG. 6, the temperature measuring device 15b is arranged at substantially the same position as the pressure measuring device 14b of FIG. Then, the outlet steam temperature measuring device 24b is arranged inside the superheating pipe 22b located at the most downstream side of the superheating pipe 22.
In the fourth modification as well, the control device 4 executes the process of FIG. 2 for each of the plurality of soot blowers, as in the first modification to the third modification.

In the fourth modification, when the soot blower 3 is "started once" or "continuously started", the control device 4 temporally moves from the soot blower 3 arranged at the uppermost stream toward the soot blower 3 arranged downstream. Start in order with the timing shifted. That is, the control device 4 activates the soot blower 3f and then activates the soot blower 3f.
By activating each soot blower 3 in this order, the adhering ash removed by the soot blower 3 in the pipe group 2 arranged upstream moves downstream along with the flow of exhaust gas, and another pipe arranged downstream. Even when reattached to the group, the reattached ash can be reliably removed.

In the fourth modification, the configurations corresponding to the first tube group, the second tube group, the third tube group, the fourth tube group, the first soot blower, and the second soot blower in claim 7 of the present application are as follows. Is.
That is, the tube group 2 composed of the superheated tube 22a is the first tube group, the tube group 2 composed of the superheated tube 22b is the second tube group, the tube group 2 composed of the water tube 23a is the third tube group, and the water tube. The tube group 2 composed of 23b corresponds to the fourth tube group, the soot blower 3e corresponds to the first soot blower, and the soot blower 3f corresponds to the second soot blower.
According to the removal system 1E of the fourth modification, in addition to the effect obtained in the above embodiment, the adhered ash including the reattached adhered ash can be reliably removed.

Although the embodiments and modifications of the present invention have been described above, the technical scope of the present invention is not limited to the embodiments or modifications, and various modifications can be made without departing from the spirit of the present invention. Is.

1,1', 1A-1E Boiler tube group adhering ash removal system (removal system)
2 Tube group 3, 3'3 ″, 3a to 3f Soot blower 4 Control device 5 Hopper 6 Feeder 7 Stalker 8 Ash chute 9 Economizer (a type of tube group)
10 Heat reducing tower 11 Dust remover (bug filter)
12 Chimney 13 Attracting blower 14a, 14b Pressure measuring device 15a, 15b Gas temperature measuring device 16a, 16b Gas flow measuring device 17 Overheat reducing device 18 Sprayed water amount measuring device 19 Steam drum 20 Water drum 21 Suspended pipe (screen tube)
22a-22f Superheater tube (super heater)
23a, 23b Water pipe 24a, 24b Steam temperature measuring device 25 Main steam amount measuring device 26 Primary air supply device 27 Secondary air supply device 28 Combustion air amount measuring device K Heat transmission rate Kc Clean heat transmission rate Kd Dirty heat transmission rate Kc / Kd Recovery rate ΔPg Differential pressure pgmin Second threshold Qc Total amount of combustion air qcmin Fourth threshold Qr Number of rotations of induced blower qrrmin Third threshold Qs Main steam amount qsmin First threshold R Recovery threshold α1 First predetermined value α2 Second predetermined value

Claims (8)

A boiler tube group adhering ash removal system that removes adhering ash from multiple boiler tube groups that recover heat from the exhaust gas generated in the furnace.
With a soot blower placed between the plurality of tube groups,
An attracting blower arranged downstream of the plurality of pipe groups to attract the exhaust gas,
It has a control device that controls the activation of the soot blower.
The control device is
Calculate the heat transmission coefficient of the boiler and calculate
When the calculated heat transmission coefficient is equal to or greater than a predetermined value, the soot blower is activated only once at a predetermined interval, and then once again at the predetermined interval or an interval different from the predetermined interval.
When the calculated heat transmission coefficient is less than the predetermined value, an adhering ash determination process for selectively determining either the first determination or the second determination is executed.
When the first determination is obtained by the adhered ash determination process, the soot blower is continuously activated a plurality of times without the interval, and continuous activation is executed.
When the second determination is obtained by the adhesion ash determination process, the one-time activation is executed.
In the adhering ash determination process, the first condition is that the main steam amount of the plurality of pipe groups is equal to or higher than the first threshold value, and the pressure difference between the exhaust gas at the inlet and outlet of the plurality of pipe groups is equal to or higher than the second threshold value. At least one of the second condition that the rotation speed of the attracting blower is equal to or higher than the third threshold, and the fourth condition that the total amount of combustion air supplied to the furnace is equal to or higher than the fourth threshold. It is executed with conditions,
When the adhering ash determination process is executed based on only one of the four conditions, the first determination is obtained when the one condition is satisfied, and the one condition is not satisfied. The second judgment is obtained at the time of
When the adhering ash determination process is executed including any two, three, or four conditions of the four conditions, all the conditions including the two, three, or four conditions are satisfied. The boiler tube group is characterized in that the first determination is obtained when both are satisfied, and the second determination is obtained when any of the two, three, or four conditions is not satisfied. Adhesive ash removal system. The control device is
When the first determination is obtained by the adhered ash determination process, the dirty heat transmission coefficient indicating the heat transmission coefficient calculated before starting the soot blower and the heat transmission coefficient calculated after starting the soot blower are calculated. Calculate the recovery rate from the clean heat transmission coefficient shown and
When the recovery rate is equal to or higher than the recovery threshold value, the continuous activation is executed.
The boiler tube group adhering ash removal system according to claim 1, wherein when the recovery rate is less than the recovery threshold value, the one-time activation is performed. When the clean heat transmission coefficient is equal to or higher than the predetermined value, the control device resets the predetermined interval longer than the value set immediately before, and when the recovery rate is equal to or higher than the recovery threshold value, the predetermined interval is set. The boiler tube group adhering ash removal system according to claim 2, wherein the interval is reset to a value shorter than the value set immediately before. At the time of the continuous activation, the control device reduces the number of activations in the continuous activation when the increase rate of the recovery rate is large, and reduces the number of activations in the continuous activation when the increase rate of the recovery rate is small. The boiler tube group adhering ash removing system according to claim 3, characterized in that the number is increased. Further having a bug filter arranged downstream of the plurality of pipe groups to remove soot and dust from the exhaust gas.
The fourth aspect of claim 4, wherein the control device does not activate the soot blower while the backwash of the bug filter is being executed, and waits for the completion of the backwash to start the sootblower. Boiler tube group adhering ash removal system. The plurality of tube groups include a first tube group, a second tube group arranged adjacent to the first tube group downstream of the first tube group, and the second tube group downstream of the second tube group. It is provided with a third tube group arranged adjacent to the tube group and a fourth tube group arranged adjacent to the third tube group downstream of the third tube group.
The soot blower includes a first soot blower arranged between the first tube group and the second tube group, and a second soot blower arranged between the third tube group and the fourth tube group. Prepare,
When the first soot blower and the second soot blower are started once or continuously, the control device is used.
When the first pipe group to the fourth pipe group are sequentially arranged from the lower side to the upper side in the vertical direction, the first soot blower is started after the second soot blower is started, or the first soot blower is started. After starting the first soot blower, start the second soot blower,
When the first tube group to the fourth tube group are sequentially arranged in one direction in the horizontal direction, the first soot blower is started, and then the second soot blower is started.
The first pipe group and the second pipe group are sequentially arranged from the lower side to the upper side in the vertical direction, and the third pipe group and the fourth pipe group are sequentially arranged in the horizontal direction in one direction. In this case, the boiler tube group adhering ash removing system according to claim 5, wherein the first soot blower is started and then the second soot blower is started. The plurality of tube groups were arranged in the first tube group, the second tube group arranged adjacent to the first tube group downstream of the first tube group, and downstream of the second tube group. It is provided with a third pipe group and a fourth pipe group arranged adjacent to the third pipe group downstream of the third pipe group.
The soot blower is a first soot blower arranged adjacent to the first tube group upstream of the first tube group, and a second soot blower arranged between the third tube group and the fourth tube group. With and
5. The control device is characterized in that, when the first soot blower and the second soot blower are started once or continuously, the second soot blower is started after the first soot blower is started. Boiler tube group adhering ash removal system described in. The boiler tube group adhering ash removing system according to any one of claims 1 to 7, wherein the soot blower is a pressure wave type soot blower that generates a pressure wave by exploding a gas.