CN102207289B - Device and method for regulating flue gas ingredients of side wall water cooling wall of front-rear wall hedging combustion boiler automatically - Google Patents

Device and method for regulating flue gas ingredients of side wall water cooling wall of front-rear wall hedging combustion boiler automatically Download PDF

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Publication number
CN102207289B
CN102207289B CN201110133813A CN201110133813A CN102207289B CN 102207289 B CN102207289 B CN 102207289B CN 201110133813 A CN201110133813 A CN 201110133813A CN 201110133813 A CN201110133813 A CN 201110133813A CN 102207289 B CN102207289 B CN 102207289B
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control system
flue gas
data management
parameter
smoke components
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CN102207289A (en
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李敏
王春玉
蓝晓村
张步庭
李玲
秦淇
许明峰
王磊
沈辉
张营帅
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State Grid Corp of China SGCC
Electric Power Research Institute of State Grid Henan Electric Power Co Ltd
Henan Jiuyu Enpai Power Technology Co Ltd
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Electric Power Research Institute of State Grid Henan Electric Power Co Ltd
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Abstract

The invention discloses a device for regulating flue gas ingredients of a side wall water cooling wall of a front-rear wall hedging combustion boiler automatically. The device comprises a flue gas online analyzing device, a flue gas continuous monitoring system, a hot air adding device and a data processing and analyzing control system, wherein data output ends of the flue gas online analyzing device and the flue gas continuous monitoring system are connected with a signal input end of the data processing and analyzing control system through a data collecting channel; a signal output end of the data processing and analyzing control system is connected with a signal control end of the hot air adding device; the hot air adding device is arranged on a water cooling wall, and an air outlet of the hot air adding device aims at the water cooling wall. According to the invention, the reducing atmosphere can be eliminated rapidly in real time, and the generation of H2S can be inhibited, thus the problem that pipes of the water cooling wall need changing because of the corrosion of high-temperature reducible sulfur can be overcome, not only is the replacing expense saved, but also the safe and economical operation of a boiler can be ensured.

Description

Automatically regulate the apparatus and method of Opposite Firing Boiler side water wall smoke components
Technical field
The invention belongs to the Opposite Firing Boiler field, relate in particular to a kind of method that can regulate Opposite Firing Boiler water-cooling wall smoke components automatically.
Background technology
The characteristics of the front-back wall opposed firing of Opposite Firing Boiler cause flame impingement boiler side water wall, and a large amount of unburnt coal dusts burn herein, form strong reducing atmosphere: high CO concentration, low O 2Concentration.If the sulfur content that uses in the coal is higher, under the effect of reducing atmosphere, sulphur is prone to generate the very strong H of corrosivity 2S forms so-called high-temperature reductibility sulfur corrosion, thereby water-cooling wall tubing is had a negative impact.And the fume continuous monitoring system at desulphurization system place can only play monitoring desulphurization system inlet flue gas composition at present; Can't directly monitor the smoke components at water-cooling wall place; Do not control the function of smoke components automatically; When the water screen tube attenuate seriously just needs the large tracts of land replace tubes, therefore cause the running time of boiler short, have a strong impact on boiler safety, operation economically.
Summary of the invention
The purpose of this invention is to provide a kind of apparatus and method that can regulate Opposite Firing Boiler water-cooling wall smoke components automatically, the boiler side water wall is not corroded, thereby make boiler safety, operation economically.
The present invention adopts following technical proposals: a kind of device of automatic adjusting Opposite Firing Boiler side water wall smoke components; Comprise flue gas on-line analysis device, fume continuous monitoring system; Also comprise hot blast adding set and Data Management Analysis control system; The data output end of said flue gas on-line analysis device and fume continuous monitoring system is connected through the signal input part of data acquisition channel with Data Management Analysis control system; The signal output part of Data Management Analysis control system is connected with the signal controlling end of hot blast adding set, and the hot blast adding set is arranged on the water-cooling wall, and its air outlet is aimed at water-cooling wall.
The signal input part of Data Management Analysis control system also is connected through the data output end of data acquisition channel with unit operation control system.
A kind of method of automatic adjusting Opposite Firing Boiler side water wall smoke components may further comprise the steps: the operational factor of unit operation control system, flue gas on-line analysis device and fume continuous monitoring system is collected by (1), described Data Management Analysis control system through data acquisition channel; (2), Data Management Analysis control system screens the parameter that receives, and filters out the parameter that need judge; (3), Data Management Analysis control system judges the parameter of screening, thereby the output control signal is given the valve of hot blast adding set, controls its valve opening and regulates smoke components.
The parameter that need judge in the described step (2) is: the O in the flue gas on-line analysis device 2, CO 2, H 2SO in S content, the fume continuous monitoring system parameter 2Furnace outlet oxygen amount in the parameter of content, unit operation control system; Rule of judgment in the step (3) is: (a), if the smoke components of flue gas on-line analysis device in O 2+ CO 2<17% (percent by volume), and H 2SO in the parameter of S>=0.01% (percent by volume) or fume continuous monitoring system 2>=3000mg/Nm 3Or furnace outlet oxygen amount in the parameter of unit operation control system<1.5% (percent by volume), then Data Management Analysis control system output signal makes the valve of hot blast adding set transfer to maximum; (b), as if O in the smoke components of flue gas on-line analysis device 2+ CO 2>=19% (percent by volume), and the duration surpass 3 minutes, then Data Management Analysis control system output signal makes the valve of hot blast adding set transfer to minimum; (c), if in the smoke components of flue gas on-line analysis device: 17%≤O 2+ CO 2<19%, (percent by volume), this moment, then Data Management Analysis control system output signal made the valve of hot blast adding set transfer to the adaptation aperture, changed the smoke components of water-cooling wall position.
The present invention can real-time collecting Opposite Firing Boiler water-cooling wall smoke components, unit operation parameter and fume continuous monitoring system operational factor; Carry out the parameter analysis then; Automatically control the smoke components that the hot blast adding set changes the boiler side water wall again; Can eliminate reducing atmosphere real-time, suppress H 2The generation of S can not changed the tubing of water-cooling wall because of the high-temperature reductibility sulfur corrosion, has both practiced thrift renewal cost, guaranteed again boiler can be safely, operation economically.
Description of drawings
Fig. 1 is an apparatus structure sketch map of the present invention;
Fig. 2 is a method flow diagram of the present invention.
The specific embodiment
As shown in Figure 1; The device that the present invention regulates Opposite Firing Boiler side water wall smoke components automatically comprises flue gas on-line analysis device, fume continuous monitoring system, hot blast adding set and Data Management Analysis control system; Flue gas on-line analysis device is installed on the side water wall; Be used for detecting smoke components; Fume continuous monitoring system is installed in the porch of desulphurization system; Desulphurization system porch flue gas is monitored, and the data output end of flue gas on-line analysis device and fume continuous monitoring system is connected through the signal input part of data acquisition channel with Data Management Analysis control system, and the signal input part of Data Management Analysis control system also is connected with unit operation control system through data acquisition channel; The signal output part of Data Management Analysis control system is connected with the signal controlling end of hot blast adding set; Wherein Data Management Analysis control system adopts single-chip microcomputer or computer; The hot blast adding set is a mature technology; It is arranged on outside the water-cooling wall, and air outlet is aimed at water-cooling wall, regulates the hot blast rate that its valve opening can be controlled its output.
Utilize the automatically adjust method of Opposite Firing Boiler side water wall smoke components of said apparatus may further comprise the steps: (1), utilize the flue gas on-line analysis device test smoke components that is installed on the side water wall, like O 2, CO 2, CO, H 2S; Simultaneously through unit operation control systematic collection unit operation parameter, like unit load, furnace outlet oxygen amount, total fuel quantity, milling systems mode, coal-supplying amount, secondary wind air distribution mode, secondary air separating air quantity, secondary air separating air door baffle opening; Also collect the fume continuous monitoring system operational factor, like desulphurization system inlet SO 2Concentration of emission, flue gas oxygen content, total exhaust gas volumn are delivered to Data Management Analysis control system with above-mentioned data through data acquisition channel; (2), the side water wall smoke components of collecting, unit operation parameter and fume continuous monitoring system operational factor are screened, filter out the parameter that to judge: i.e. O in the flue gas on-line analysis device 2, CO 2, H 2SO in S content, the fume continuous monitoring system parameter 2Furnace outlet oxygen amount in content, the unit operation control systematic parameter; (3) these parameters are carried out following judgment processing: (a), if the smoke components of flue gas on-line analysis device in O 2+ CO 2<17%, and H 2SO in S>=0.01% (percent by volume) or the fume continuous monitoring system parameter 2>=3000mg/Nm 3Or the furnace outlet oxygen amount in the unit operation control systematic parameter<1.5% (percent by volume), then Data Management Analysis control system output signal makes the valve of hot blast adding set transfer to maximum; (b), as if O in the smoke components of flue gas on-line analysis device 2+ CO 2>=19% (percent by volume), and the duration surpass 3 minutes, then Data Management Analysis control system output signal makes the valve of hot blast adding set transfer to minimum; (c), if in the smoke components of flue gas on-line analysis device: 17%≤O 2+ CO 2<19% (percent by volume), this moment, then Data Management Analysis control system output signal made the valve of hot blast adding set transfer to the adaptation aperture, changed the smoke components of water-cooling wall position.

Claims (4)

1. device of automatically regulating Opposite Firing Boiler side water wall smoke components; Comprise flue gas on-line analysis device, fume continuous monitoring system; It is characterized in that: described flue gas on-line analysis device is installed on the side water wall; Fume continuous monitoring system is installed in the porch of desulphurization system; Also comprise hot blast adding set and Data Management Analysis control system, the data output end of said flue gas on-line analysis device and fume continuous monitoring system is connected through the signal input part of data acquisition channel with Data Management Analysis control system, and the signal output part of Data Management Analysis control system is connected with the signal controlling end of hot blast adding set; The hot blast adding set is arranged on the water-cooling wall, and its air outlet is aimed at water-cooling wall.
2. the device of automatic adjusting Opposite Firing Boiler side water wall smoke components according to claim 1 is characterized in that: the signal input part of Data Management Analysis control system also is connected through the data output end of data acquisition channel with unit operation control system.
3. device according to claim 2 is regulated the method for Opposite Firing Boiler side water wall smoke components automatically, it is characterized in that: may further comprise the steps: the operational factor of unit operation control system, flue gas on-line analysis device and fume continuous monitoring system is collected by (1), described Data Management Analysis control system through data acquisition channel; (2), Data Management Analysis control system screens the parameter that receives, and filters out the parameter that need judge; (3), Data Management Analysis control system judges the parameter of screening, thereby the output control signal is given the valve of hot blast adding set, controls its valve opening and regulates smoke components.
4. the method for automatic adjusting Opposite Firing Boiler side water wall smoke components according to claim 3 is characterized in that: the parameter that need judge in the described step (2) is: the O in the flue gas on-line analysis device 2, CO 2, H 2SO in S content, the fume continuous monitoring system parameter 2Furnace outlet oxygen amount in the parameter of content, unit operation control system; Rule of judgment in the step (3) is: (a), if the smoke components of flue gas on-line analysis device in O 2+ CO 2<17% (percent by volume), and H 2SO in the parameter of S>=0.01% (percent by volume) or fume continuous monitoring system 2>=3000mg/Nm 3Or furnace outlet oxygen amount in the parameter of unit operation control system<1.5% (percent by volume), then Data Management Analysis control system output signal makes the valve of hot blast adding set transfer to maximum; (b), as if O in the smoke components of flue gas on-line analysis device 2+ CO 2>=19% (percent by volume), and the duration surpass 3 minutes, then Data Management Analysis control system output signal makes the valve of hot blast adding set transfer to minimum; (c), if in the smoke components of flue gas on-line analysis device: 17%≤O 2+ CO 2<19% (percent by volume), this moment, then Data Management Analysis control system output signal made the valve of hot blast adding set transfer to the adaptation aperture, changed the smoke components of water-cooling wall position.
CN201110133813A 2011-05-23 2011-05-23 Device and method for regulating flue gas ingredients of side wall water cooling wall of front-rear wall hedging combustion boiler automatically Active CN102207289B (en)

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CN103423730A (en) * 2013-07-31 2013-12-04 广东电网公司电力科学研究院 Method for measuring adherent smoke of front-back oppose swirling combustion boiler

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Publication number Priority date Publication date Assignee Title
CN102563692B (en) * 2011-12-19 2014-04-23 西安交通大学 Early-warning adjustment system and early-warning adjustment method for preventing detonation of large-scale power station pulverized-fuel boiler furnace
CN106196149B (en) * 2016-08-03 2017-12-19 国网山东省电力公司电力科学研究院 Boiler water wall surface oxidation atmosphere active strengthening system and method, boiler

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CN202118942U (en) * 2011-05-23 2012-01-18 河南电力试验研究院 Device for automatically adjusting components of smoke on water cooled wall of lateral wall of front-back-wall hedging combustion boiler

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CN101706110A (en) * 2009-11-17 2010-05-12 西安交通大学 Near-wall air device for preventing high-temperature corrosion of water-cooled wall of power station boiler
CN202118942U (en) * 2011-05-23 2012-01-18 河南电力试验研究院 Device for automatically adjusting components of smoke on water cooled wall of lateral wall of front-back-wall hedging combustion boiler

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