JP2007205704A - Steam pressure control method in automatic start/stop of waste processing boiler - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a control method of automatic start/stop of a waste heat recovery boiler capable of improving safety and stability of operation by executing secure pressure-increasing/decreasing control in response to not only prediction but also heat input by acquiring an actual pressure condition. <P>SOLUTION: In this automatic pressure increasing/decreasing control method of a boiler for waste of a waste processing facility, a main steam pressure regulation valve is closed, and a purge regulation valve is opened to increase main steam pressure while releasing steam in starting the boiler of the waste processing facility; when it reaches normal pressure, the main steam pressure regulation valve is opened and the purge regulation valve is closed; and the main steam pressure regulation valve is closed in stopping the heat recovery boiler, and the purge regulation valve is opened to decrease the main steam pressure while releasing the steam. In the control method, a measured value PV detected by a main steam pressure detector is introduced into set values SV<SB>2</SB>and SV<SB>3</SB>of a purge valve, and the set values of the purge valve are changed stepwise at a certain width (mKPa). <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a steam pressure control method for automatically starting and stopping a waste treatment boiler disposed in a waste treatment facility including an incinerator, a melting furnace, and the like.

  In the waste treatment facility, municipal waste and other general waste, industrial waste such as waste tires and car shredder dust are incinerated or melted, and the generated combustible gas is burned in the combustion chamber of the exhaust gas treatment system. Heat is recovered from the combustion exhaust gas by a waste treatment boiler.

  FIG. 6 is a schematic view showing an example of a waste melting treatment facility. Waste, auxiliary materials such as coke and limestone are introduced into the melting furnace 8 from the upper part of the furnace, and air and oxygen are blown from the tuyere 9. In the melting furnace, it is discharged as a melt from the tap 10 through the processes of drying, pyrolysis, combustion and melting. The combustible matter is discharged from the duct 11 as combustible gas and combustible dust, and the combustible dust is collected by the collection device 12 and blown into the furnace from the tuyere 9.

  The combustible gas from the collection device 12 is combusted in the combustion chamber 13, and the combustion exhaust gas is heat recovered by heat exchange in the boiler 14. The steam generated in the boiler 14 is sent to the steam turbine / power generation device 15 for power generation. The exhaust gas from the boiler 14 is solid-gas separated by a dust collector 16 and discharged from a chimney 18 by a blower 17 (see Patent Document 1).

  Before throwing waste into the melting furnace or incinerator, the combustion chamber is heated with an auxiliary burner or the like, and then the waste is thrown in or ignited. Using the heat source in the temperature rising process of combustion, the pressure of steam is increased by a boiler.

  Patent Document 2 discloses automating the pressure increase accompanying the start of the boiler or the pressure decrease accompanying the stop.

  FIG. 7A is a schematic diagram of a conventional boiler facility, and FIG. 7B is a step-up / step-down diagram of the facility.

  In FIG. 7A, a steam stop valve 21 is provided in the steam pipe 20 of the boiler 19, and a diffusion pressure adjusting valve 22 and a diffusion stop valve 23 are provided in the steam release pipe 21 branched from the steam pipe 20. . At the time of steady operation, the steam stop valve 21 is opened and the diffusion stop valve 23 is closed, and all generated steam is ventilated to the steam use destination through the steam pipe 20 and the steam stop valve 21. During starting or stopping, the steam is released into the atmosphere while the steam stop valve 21 is closed and the release stop valve 23 is opened and the steam pressure is controlled by the release pressure control valve 22.

In FIG. 7B, in the case of automatic start-up of the boiler, the diffusion stop valve 23 is opened, the steam stop valve 21 is closed, the set value of the pressure control of the generated steam is set to Ps0 selected in advance, and the generated steam pressure is set. When the value Ps0 is reached, the set value of the generated steam pressure and the set value of the temperature control are changed to the right with the passage of time according to the preselected boosting curve shown in FIG. 7B, and the set value of the generated steam pressure is selected in advance. When the minimum value Psmin of the normal pressure is reached, the steam stop valve 21 is opened and the radiation stop valve 23 is closed, and the operation is steady at a pressure between the minimum value Psmin and the maximum value Psmax.
JP 2001-021123 A JP-A-4-257601

  The step-up / step-down line shown in FIG. 7 (b) is determined based on a set value selected in advance. This is because the combustion of the combustion burner as a heat source is controlled so that the amount of heat input hardly fluctuates. Is applicable. However, in waste treatment facilities, the amount of waste to be treated varies widely, such as general waste and industrial waste, and there are large variations in quality and water content, so the calories are not constant, and the heat source is due to waste In addition, the amount of heat input to the combustion chamber in the front stage of the boiler varies greatly, so that it is very difficult to predict the pressure increase / decrease curve. In addition, when there is a large amount of heat input due to fluctuations in the combustible gas, the temperature is rapidly increased and the vapor pressure is rapidly increased, and the equipment may be affected by heat. Therefore, the current situation is that the automatic start / stop control based on the set value by prediction cannot be stably controlled.

  Therefore, the present invention captures the actual steam pressure situation in the boiler of a waste treatment facility, and performs reliable automatic step-up / step-down control based on heat input rather than prediction to improve operational stability and safety. The present invention provides a steam pressure control method for automatically starting and stopping a boiler.

  The present invention closes the main steam pressure control valve provided in the steam pipe when starting up the boiler of the waste treatment facility, and opens the purge valve provided in the purge line branched from the exhaust pipe to dissipate the generated steam. When the main steam pressure is increased while the main steam pressure reaches the normal pressure, the main steam pressure control valve is opened and the purge control valve is closed, and when the heat recovery boiler is stopped, the main steam pressure control valve is closed. Detected by the main steam pressure detector provided in the steam pipe in the steam pressure control method in the automatic start and stop of the waste treatment boiler that opens the purge control valve to dissipate the generated steam to lower the main steam pressure. The measured value of the main steam pressure is taken into the set value of the steam pressure of the purge valve, and the set value is changed stepwise to increase or decrease the pressure.

  In the present invention, the main steam pressure is detected, and the set value is changed based on the detected actual value to perform the automatic pressure increase / decrease control. Therefore, the automatic start / stop can be performed at the optimum pressure increase / decrease speed. In addition, since stable pressure increase / decrease with a rapid change in the main steam pressure is ensured, it is possible to eliminate the thermal influence and ensure the safety of the device.

  FIG. 1 is a schematic view of boiler equipment to which an automatic start / stop control method according to the present invention is applied.

  In FIG. 1, combustion exhaust gas serving as a heat source is supplied to a boiler 1 from a combustion chamber (not shown) of a waste melting facility located upstream thereof. The combustion exhaust gas is recovered by the boiler to generate steam. The generated steam is sent to the steam pipe 2.

  The steam pipe 2 is sequentially provided with a pressure detection end 3 for detecting the main steam pressure, a main steam flow rate detection end 7 for detecting the main steam flow rate, and a main steam pressure control valve 4 for adjusting the main steam pressure according to the opening degree. . Further, a purge control valve 6 is provided in the steam pipe 2 to disperse the steam into a purge line 5 branched between the main steam flow rate detection end 7 and the main steam pressure control valve 4.

  In the above configuration, at the time of automatic startup, the main steam pressure control valve 4 is closed, the purge control valve 6 is opened, the main steam pressure is increased while releasing the steam while raising the temperature of the boiler 1, and reaches the normal pressure. Then, the purge control valve is closed and the purge valve is closed. At the time of automatic stop, the main steam pressure control valve 4 is closed, the purge control valve 6 is opened, and the main steam pressure is reduced while releasing the steam.

  In the present invention, in order to reduce the thermal influence accompanying the fluctuation of the heat input amount of the boiler and suppress the rapid increase or decrease of the main steam pressure, the automatic startup or automatic stop is performed in the following steps.

  First, the automatic boost control method of the present invention will be described.

  FIG. 2 is a flowchart showing the steps (S1 to S7) of the boost control according to the present invention, and FIG. 3 is a graph showing the relationship between the boiler pressure and time in the boost control of the present invention.

Step S1:
The set value (SV ₁ value) of the purge control valve 6 installed in the purge line 5 is set to the specified pressure 1 until the main steam pressure (boiler pressure) detected at the pressure detection end 3 rises to the specified pressure 1. The purge control valve 6 sets a valve opening lower limit so as not to be closed. At this time, the main steam pressure adjustment valve 4 is closed. The specified pressure 1 is the minimum pressure (for example, 1000 KPa) necessary for enabling normal control of the valve.

Step S2:
After the main steam pressure exceeds the specified pressure 1, the measured value (PV value) of the main steam pressure of the purge control valve 6 is nKPa (for example, 50 KPa) before the next set value (SV ₂ value) ( That is, a pressure increase up to PV value = SV ₂ value−nKPa) is detected. The set value (SV ₂ value) is set by adding a pressure (mKPa described later, for example, 100 KPa) to be boosted from the previous set value (SV ₁ value). The pressure to be increased is appropriately determined depending on the scale of the equipment, but is set to mKPa (for example, 100 KPa) described later. The reason why the increase up to nKPa is detected is because it is difficult to control it so as to coincide with the set value (SV ₂ value), so that it is detected early.

Step S3:
After the actually measured value reaches PV value = SV ₂ value−nKPa, it is held for a certain time T (for example, 1 minute) using a timer.

Step S4:
After a certain time T has elapsed, the next set value (SV ₃ value) of the purge control valve 6 is increased by mKPa (for example, m = 100 KPa) from the previous set value (SV ₂ value) (SV ₃ value = SV ₂ value + mKPa). ) Set.

Step S5:
The processing from step S1 to step S4 is repeatedly performed to increase the main steam pressure, and the pressure is increased until a specified pressure 2 (for example, 3700 KPa) that is a rated pressure of the heat recovery boiler is reached.

Step S6:
When the main steam pressure exceeds the specified pressure 2, the main steam pressure adjusting valve 4 is opened, and the set pressure of the main steam pressure adjusting valve 4 is set to a specified pressure 3 (rated pressure, for example, 3900 KPa) which is a normal pressure.

Step S7:
Then, the main steam pressure adjusting valve 4 is opened, the valve opening (MV) of the purge adjusting valve 6 is set to 0%, and steam is supplied to the subsequent supply destination.

  Through the above steps, the present invention reliably increases the main steam pressure while stepping up the set value step by step based on the measured value of the main steam pressure in accordance with the heat input when automatically starting the boiler. Therefore, the safety and stability of operation can be improved.

  Next, an automatic step-down control method will be described.

  FIG. 4 is a flowchart showing steps (steps T1 to T7) of step-down control according to the present invention, and FIG. 5 is a graph showing the relationship between boiler pressure and time in step-down control of the present invention.

Step T1:
After starting the boiler pressure reduction, the main steam flow rate detection end 7 installed in the steam pipe 2 confirms that the main steam flow rate is less than the specified flow rate 1, and the supply of main steam to the boiler has decreased. Make sure. The specified flow rate 1 is a value substantially close to zero. When the specified flow rate is 1 or less, the main steam pressure control valve 4 is closed by automatic control.

Step T2:
The purge control valve 6 is opened, and the set value (SV _P1 ) of the purge control valve 6 is reduced by mKPa (for example, 100 KPa) from the set value (SV _S1 value) of the main steam pressure control valve 4 (SV _P1 = SV _S1 − Vapor is dissipated with automatic control at mKPa). The set value (SV _S1 value) is set to the value of the normal pressure of the main steam pressure (the specified pressure 3 in step S6 in FIG. 2). The mKPa may be the same as the above boost value (for example, 100 KPa).

Step T3:
Thereafter, the actual measured value (PV value) of the main steam pressure detected at the pressure detection end 3 is nKPa (for example, 50 KPa) before the set value (SV _S1 value) of the purge control valve 6 (PV = SV _S1 + nKPa). Detects step-down pressure. The reason why the pressure drop before nKPa is detected is to detect the pressure drop early.

Step T4:
After the actual measurement value reaches PV value = SV _S1 + nKPa, it is held for a certain time T (for example, 1 minute) using a timer.

Step T5:
After the predetermined time T has elapsed, the next set value (SV _P2 value) of the purge control valve 6 is set to be lower by mKPa than the previous set value (SV _P1 value) (SV _P2 = SV _P1 −mKPa).

Step T6:
The process from step T2 to T5 is repeated until the specified pressure 4 is reached, and the boiler is stepped down. When the main steam pressure falls below the specified pressure 4, the pressure reduction is completed.

Step T7:
The MV (open altitude) of the main steam pressure control valve 4 is 0%.

  This control makes it possible to step down the boiler in response to fluctuations in heat input when the furnace is stopped.

It is the schematic of the boiler equipment to which the control method of the automatic starting stop by this invention is applied. It is a flowchart which shows the step of the pressure | voltage rise control by this invention. It is a graph which shows the relationship between the boiler pressure and time in the pressure | voltage rise control of this invention. It is a flowchart which shows the step of the pressure | voltage fall control by this invention. It is a graph which shows the relationship between the boiler pressure and time in the pressure | voltage fall control of this invention. It is the schematic which shows an example of a waste melting processing facility. (A) is the schematic of the conventional boiler equipment, (b) is a step-up / step-down curve diagram of the equipment.

Explanation of symbols

1: Boiler 2: Steam piping 3: Pressure detection end 4: Main steam pressure control valve 5: Purge line 6: Purge control valve 7: Main steam flow rate detection end 8: Waste melting furnace v
9: tuyere 10: outlet 11: duct 12: collector 13: combustion chamber 14: boiler 15: steam turbine / power generator 16: dust collector 17: blower 18: chimney 19: heat recovery boiler 20: steam Pipe 21: Steam stop valve 22: Emission pressure control valve 23: Emission stop valve

Claims (1)

When starting up the boiler of the waste treatment facility, the main steam pressure control valve provided in the steam pipe is closed and the purge valve provided in the purge line branched from the exhaust pipe is opened to dissipate the generated steam while releasing the generated steam. When the main steam pressure reaches the normal pressure, the main steam pressure control valve is opened and the purge control valve is closed. When the heat recovery boiler is stopped, the main steam pressure control valve is closed and the purge control valve is closed. In the steam pressure control method in the automatic start and stop of the waste treatment boiler, which releases the generated steam to reduce the main steam pressure by opening the
The measured value of the main steam pressure detected by the main steam pressure detector provided in the steam pipe is taken in the set value of the steam pressure of the purge valve, and the set value is changed stepwise to increase and decrease the pressure. Steam pressure control method for automatic start and stop of waste treatment boiler.

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