CN106422732A - Thermal power plant W type boiler SNCR denitration system and control method thereof - Google Patents

Thermal power plant W type boiler SNCR denitration system and control method thereof Download PDF

Info

Publication number
CN106422732A
CN106422732A CN201610822505.5A CN201610822505A CN106422732A CN 106422732 A CN106422732 A CN 106422732A CN 201610822505 A CN201610822505 A CN 201610822505A CN 106422732 A CN106422732 A CN 106422732A
Authority
CN
China
Prior art keywords
spray gun
type boiler
long
short
power plant
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610822505.5A
Other languages
Chinese (zh)
Inventor
张向宇
张波
陆续
向小凤
高宁
徐宏杰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Huaneng Group Co Ltd
Xian Thermal Power Research Institute Co Ltd
Original Assignee
China Huaneng Group Co Ltd
Xian Thermal Power Research Institute Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China Huaneng Group Co Ltd, Xian Thermal Power Research Institute Co Ltd filed Critical China Huaneng Group Co Ltd
Priority to CN201610822505.5A priority Critical patent/CN106422732A/en
Publication of CN106422732A publication Critical patent/CN106422732A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/79Injecting reactants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/54Nitrogen compounds
    • B01D53/56Nitrogen oxides
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D7/00Control of flow
    • G05D7/06Control of flow characterised by the use of electric means
    • G05D7/0617Control of flow characterised by the use of electric means specially adapted for fluid materials
    • G05D7/0623Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the set value given to the control element
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/20Reductants
    • B01D2251/206Ammonium compounds
    • B01D2251/2067Urea
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Automation & Control Theory (AREA)
  • General Physics & Mathematics (AREA)
  • Physics & Mathematics (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention discloses a thermal power plant W type boiler SNCR denitration system and a control method thereof. The system comprises long spray guns, a plurality of short spray guns, a laser detection system, a metering module and distribution modules, wherein the long spray guns are arranged in a W type boiler horizontal flue area, the short spray guns are arranged in a W type boiler furnace arch area in layers, and the metering module and the distribution module are sequentially connected. The method includes the steps that a CO concentration signal obtained through the laser detection system adjusts the concentration of a urea solution through the metering module; a temperature distribution signal obtained through the laser detection system adjusts the flow of the urea solution sprayed by each long spray gun through a long spray gun distribution module; the number of operation layers of the short spray guns and the total flow of the urea solution of each layer are controlled according to a unit load interval and an NSR value. The long spray guns provided with multiple nozzles extend into a flue, the sprayed urea solution can completely cover the section of the flue, it is guaranteed that the urea solution and flue gas are sufficiently and evenly mixed, denitration efficiency is improved, and a control mode is simple and easy to implement.

Description

A kind of thermal power plant W type boiler SNCR denitration system and its control method
Technical field
The present invention relates to thermal power plant's SNCR denitration technology, specially a kind of thermal power plant W type boiler SNCR denitration system and its Control method.
Background technology
W flame boiler, in low volatile coal, has that low-load combustion-stabilizing ability is strong, combustion stability is good, band is negative Lotus performance is strong, reliable the features such as, therefore W flame boiler has become in China and has used the low volatilization such as anthracite or meager coal inferior Divide main force's type of furnace of coal, but it has the high problem of NOx discharge in actual motion.In the face of NOx emission concentration 50mg/ m3Ultra-clean emission request, simple transformation SCR denitration system is not only invested higher with operating cost, also affects the peace of unit simultaneously Quan Xing.From technology and many-sided considerations such as economic angle, increase SNCR denitration device on the basis of making full use of former SCR device It is the reasonable selection realizing W type boiler nitrogen oxides minimum discharge.
SNCR method (SNCR) gas denitrifying technology be station boiler, fluidized-bed combustion boiler, cement kiln and The mainstream technology of flue gas of refuse burning denitration.In 880 DEG C of -1050 DEG C of temperature ranges, under no catalysts conditions, spray into ammonia Or the amino reductive such as carbamide, the NOx in flue gas is optionally reduced into harmless nitrogen and water.SNCR technique is with burner hearth For reactor, can be by realizing to the transformation of boiler, the construction period is short, cost of investment and operating cost and other denitrating flue gas skills It is all that ratio is relatively low that art is compared, and is suitable for the transformation to medium small boiler.Modern SNCR technology can control NOx emission reduce by 20~ 50%, increase with unit capacity, size of burner hearth and unit load excursion expand, and increased reaction temperature window and reduction Agent mixed uniformly control difficulty, causes denitration efficiency to reduce.For 600MW unit, it is less than 10 μ L/ controlling ammonia slip concentration Under the conditions of L, denitration efficiency only 30% about.Generally higher due to using anthracitic W type boiler NOx initial concentration, for protecting Card NOx emission reaches 50mg/m3, the denitration efficiency of SNCR section must reach more than 45%, therefore research and develop efficient thermoelectricity Factory W type boiler SNCR denitration system is extremely urgent.
The denitration efficiency of SNCR be subject to temperature, CO concentration, NOx initial value, NSR, burning condition, coal, the type of furnace, the escaping of ammonia etc. because The impact of element, wherein temperature and CO concentration are two major influence factors.For improving SNCR technique denitration efficiency, correlational study carries Go out the method using controlling ammonia nitrogen ratio under different load to adjust reduction agent flux, as disclosed in Chinese patent CN105169917A A kind of SNCR-SCR combined denitration system and method based on the detection of ammonia nitrogen mol ratio and regulation and control, Chinese patent A kind of SNCR SNCR response system, Chinese patent disclosed in CN201520543068.4 The ammonia spraying amount control method of SNCR flue gas denitrification system in a kind of manufacture of cement disclosed in CN201510188180.5, but this control Method processed extremely complex it is difficult in engineering realize.In addition research is had to be distributed by measurement temperature to control spray gun by reducing agent It is injected in the temperature province of suitable SNCR reaction, realize the dynamic tracking to each SNCR spray gun temperature window, such as China specially A kind of point-to-point spraying system of efficient SNCR disclosed in sharp CN104307347A, and for example disclosed in Chinese patent CN104117279A A kind of station boiler SNCR denitration control system and its control method, the difficult point of this control method is that spray gun quantity is more, right Every spray gun carries out precise control and will dramatically increase system cost.CO concentration in flue gas be impact SNCR denitration efficiency important because Element, result of study shows, when CO concentration is less than 1000ppm, SNCR denitration efficiency increases with CO concentration and increases;When CO concentration During more than 1000ppm, SNCR denitration efficiency increases with CO concentration and reduces.Because CO concentration in flue gas is difficult to survey online Amount, generally ignores the impact of CO concentration in current SNCR control system, and this also becomes the important of restriction SNCR denitration efficiency Reason.
Content of the invention
For problems of the prior art, the present invention provide a kind of thermal power plant W type boiler SNCR denitration system and its Control method, out of stock efficiency high, control simple, transformation is convenient.
The present invention is to be achieved through the following technical solutions:
A kind of thermal power plant W type boiler SNCR denitration system, including the long spray gun being arranged on W type boiler horizontal gas pass region, Divide the multiple short spray gun of multilamellar setting in W type boiler furnace arch, furnace nose region, and laser detection system and the metering mould being sequentially connected Block and distribute module;Distribute module includes the long spray gun distribute module of the outfan long spray gun of connection and outfan connects short spray gun Short spray gun distribute module;Metering module input for controlling urea concentration connects crude urine element solution reservoir respectively and removes Brine reservoir, outfan connects long spray gun distribute module and short spray gun distribute module respectively;Described laser detection system includes Central control cabinet, diode laser, fibre multiplexer, optical fiber and the multigroup laser instrument being sequentially connected;Central control cabinet For flue-gas temperature distribution signal and CO concentration signal are detected by laser instrument;Its outfan connects long spray respectively through engineer station Rifle distribute module and metering module;Multiple long spray guns are in uniformly multi-tier arrangement on the cross section of horizontal flue, and long spray gun divides Join the urea liquid flow that module controls each long lance ejection respectively according to the control signal of engineer station;Every layer short spray gun Urea liquid entrance one electrically operated valve is set, short spray gun distribute module is according to the unit load of W type boiler and NSR value Control every layer of electrically operated valve aperture.
Preferably, long spray gun is provided with six altogether, and is in uniformly three layers of arrangement on the cross section of horizontal flue, long spray Four groups of laser instrument are uniformly arranged on the section of rifle place;Laser instrument and long spray gun interval setting;Every group of laser instrument includes a transmitting End and a receiving terminal, transmitting terminal connects optical fiber, and receiving terminal connects central control cabinet.
Preferably, long spray gun cools down the outfan that end entrance connects desalination water storage tank, and colling end outlet connects demineralized water storage The input of tank.
Preferably, also include compressed air reservoir, the outfan of compressed air reservoir is respectively used to cooling air and is connected to The cooling end entrance of short spray gun, is connected between metering module and distribute module for atomizing air.
Preferably, described metering module includes blender, and the control valve being separately positioned on blender two entrances And effusion meter;The outfan of crude urine element solution reservoir and desalination water storage tank is passed through fluid filling pump respectively and is connected with corresponding mixer entrance Connect.
Preferably, every short spray gun arranges a manually-operated gate, and all manually-operated gate apertures are consistent.
A kind of thermal power plant W type boiler SNCR denitration control method, based on a kind of thermal power plant W type boiler of the present invention In SNCR denitration system, including,
The step that urea concentration is adjusted by metering module according to the CO concentration signal that laser detection system obtains;
Each long spray gun spray is adjusted by long spray gun distribute module according to the temperature distribution signal that laser detection system obtains The step of the urea liquid flow penetrated;
Step according to unit load interval put into operation with the NSR value short spray gun of the control number of plies and every layer of urea liquid total flow.
Preferably, the step adjusting urea concentration is specific as follows,
Laser detection system obtains the CO concentration signal in horizontal flue using TDLAS measuring method, and CO concentration signal exists It is converted into a road valve opening signal in engineer station and sends in metering module, adjust the opening of control valve of desalination water loop Degree, thus control the urea concentration of long lance ejection;
Raise with CO concentration, increase desalination discharge;Reduce with CO concentration, reduce desalination discharge.
Preferably, the step adjusting the urea liquid flow of each long lance ejection is specific as follows,
Laser detection system obtains the temperature distribution signal of flue gas in horizontal flue using TDLAS measuring method, and temperature is divided Cloth signal is converted into multi-way valve opening amount signal in engineer station and sends in long spray gun distribute module, adjusts each long spray The aperture of rifle control valve, thus control the urea liquid flow of every long lance ejection.
Preferably, control short spray gun put into operation the number of plies and every layer of urea liquid total flow step specific as follows,
Short spray gun point two-layer is arranged on W type boiler furnace arch, furnace nose region, is the short spray gun of ground floor and second from the bottom up successively The short spray gun of layer;
When the unit of W type boiler is underload, the short spray gun of the ground floor that puts into operation, the short spray gun of the second layer cuts out, and according to NSR Value adjusts the aperture of ground floor valve;
When the unit of W type boiler is middle load, the two-layer that simultaneously puts into operation spray gun, and two-layer valve is adjusted according to NSR value Aperture;
When the unit of W type boiler is high load capacity, put into operation second layer spray gun, and the short spray gun of ground floor cuts out, and according to NSR value Adjust the aperture of second layer valve.
Compared with prior art, the present invention has following beneficial technique effect:
The present invention stretches in the middle part of flue by arranging the long spray gun of multiple nozzles, and the urea liquid of long lance ejection can be complete Cover flue cross section it is ensured that urea liquid fully, is uniformly mixed with flue gas, improve denitration efficiency;Long spray gun is entered using demineralized water Row cooling, cooling water reusable edible, reduces operating cost.Arrange multigroup laser detector in long spray gun region simultaneously, The distribution of measurement flue-gas temperature and CO concentration simultaneously, and according to every long spray gun urea liquid stream of temperature distribution signal real-time adjustment Amount, according to CO concentration signal real-time adjustment desalination discharge, thus ensureing that the denitrification reducing agent spraying into is in optimum reaction condition, Improve SNCR system denitration efficiency.Short spray gun urea liquid flow adopts every layer of centralized Control, according to unit load range restraint The number of plies that puts into operation and every layer of urea liquid total flow, and it is evenly distributed to every spray gun, control mode is simple, easily realization.
Brief description
Fig. 1 is W type boiler SNCR denitration system of the present invention.
Fig. 2 is long gun controls loop in denitrating system of the present invention.
In figure:Long spray gun 1, short spray gun 2, urea liquid storage tank 3, desalination water storage tank 4, metering module 6, blender 61, point Join module 7, long spray gun distribute module 71, central control cabinet 81, diode laser 82, fibre multiplexer 83, optical fiber 84, Transmitting terminal 85, receiving terminal 86, engineer station 9, W type boiler 10.
Specific embodiment
With reference to specific embodiment, the present invention is described in further detail, described be explanation of the invention and It is not to limit.
A kind of present invention thermal power plant W type boiler SNCR denitration system, as shown in figure 1, it includes being arranged on W type boiler 10 water The long spray gun 1 in flat flue region, divides the multiple short spray gun 2 of multilamellar setting in W type boiler 10 furnace arch, furnace nose region, and laser detection System and the metering module 6 being sequentially connected and distribute module 7;The long spray gun that distribute module 7 includes the outfan long spray gun 1 of connection divides Join module 71 and outfan connects the short spray gun distribute module of short spray gun 2;Metering module 6 for controlling urea concentration is defeated Enter end and connect crude urine element solution reservoir 3 and desalination water storage tank 4 respectively, outfan connects long spray gun distribute module 71 and short spray respectively Rifle distribute module 72;Central control cabinet 81 that described laser detection system includes being sequentially connected, diode laser 82, optical fiber Multiplexer 83, optical fiber 84 and multigroup laser instrument;Central control cabinet 81 is used for detecting flue-gas temperature distribution letter by laser instrument Number and CO concentration signal;Its outfan connects long spray gun distribute module 71 and metering module 6 respectively through engineer station 9;Multiple length Spray gun 1 is in uniformly multi-tier arrangement on the cross section of horizontal flue, and long spray gun distribute module 71 is according to the control of engineer station 9 Signal controls the urea liquid flow of each long spray gun 1 injection respectively;The urea liquid entrance setting of every layer short spray gun 2 One electrically operated valve, short spray gun distribute module 72 controls every layer of electrodynamic valve according to the unit load of W type boiler 10 and NSR value Door.Wherein, also include compressed air reservoir 5, the outfan of compressed air reservoir 5 is respectively used to cooling air and is connected to short spray gun 2 cooling end entrance, is connected between metering module 6 and distribute module 7 for atomizing air.Central control cabinet 81 is used for detecting With process laser signal;Fibre multiplexer 83 is used for the coupling of two wave band of laser signals;Diode laser 82 generates Laser signal;Optical fiber 84 transmits laser signal;Preferably laser detector also includes the protection for purging and pneumatic decoking Device.
In this preferred embodiment, as shown in Fig. 2 long spray gun 1 is provided with six altogether, and on the cross section of horizontal flue uniformly In three layers arrange, long spray gun 1 place section is uniformly arranged four groups of laser instrument;Laser instrument and long spray gun 1 interval setting;Every group Laser instrument includes a transmitting terminal 85 and a receiving terminal 86, and transmitting terminal 85 connects optical fiber 84, and receiving terminal 86 connects central control Cabinet 81.
In this preferred embodiment, long spray gun 1 cools down the outfan that end entrance connects desalination water storage tank 4, and colling end outlet connects The input of desalination water storage tank 4.Metering module 6 includes blender 61, and the control being separately positioned on blender 61 two entrances Valve processed and effusion meter;The outfan of crude urine element solution reservoir 3 and desalination water storage tank 4 passes through fluid filling pump and corresponding blender respectively 61 entrances connect.
A kind of present invention thermal power plant W type boiler SNCR denitration control method, including the CO being obtained according to laser detection system The step that concentration signal adjusts urea concentration by metering module 6;Believed according to the Temperature Distribution that laser detection system obtains The step number adjusting the urea liquid flow of each long spray gun 1 injection by long spray gun distribute module 71;According to unit load area Between and the NSR value short spray gun 2 of control put into operation the step of the number of plies and every layer of urea liquid total flow.Preferably, short 2 points of two-layers of spray gun set Put in W type boiler 10 furnace arch, furnace nose region, be the short spray gun of ground floor and the short spray gun of the second layer from the bottom up successively.
Wherein, laser detection system obtains the CO concentration signal in horizontal flue using TDLAS measuring method, and CO concentration is believed Number it is converted into a road valve opening signal in engineer station 9 and sends in metering module 6, adjust the control of desalination water loop The aperture of valve, thus control the urea concentration of long spray gun 1 injection.
Wherein, laser detection system obtains the temperature distribution signal of flue gas in horizontal flue using TDLAS measuring method, temperature Degree distribution signal is converted into multi-way valve opening amount signal in engineer station 9 and sends in long spray gun distribute module 71, adjusts The aperture of each long spray gun 1 control valve, thus control the urea liquid flow of every long spray gun 1 injection.
In the present invention, concrete arrangement and control are as follows.
1) as shown in figure 1, six long spray guns divide three layers to be arranged in W type boiler horizontal gas pass region, the injection urine in flue gas Plain solution.Long spray gun stretches into flue center and comprises multiple spouts, and the urea liquid of injection can cover whole flue cross section.Long spray Rifle adopts desalination water cooling, cooling water circulation utilization.
2) as shown in figure 1, dividing two-layer to arrange branched short spray gun in W type boiler furnace arch, furnace nose region, stretch into spray at about 1 meter in stove Penetrate urea liquid.Short spray gun is cooled down using compressed air, and cooling air is directly blown in burner hearth.
3) as shown in Fig. 2 arranging four groups of laser instrument in long spray gun place section, every group of laser instrument comprise a transmitting terminal and One receiving terminal.The laser beam of the specific wavelength that transmitting terminal is sent passes through receiving end collection after boiler, in being then fed into In the switch board of centre, the ratio not absorbing light and absorbed light line is measured by central control cabinet, so that it is determined that flue-gas temperature distribution And CO concentration.Flue-gas temperature distribution signal is converted into six tunnel valve opening signals in engineer station and sends into long spray gun distribution Module, adjusts the aperture of electrically operated valve in each long spray gun loop, thus controlling the urea liquid flow of every long lance ejection. CO concentration signal is converted into a road valve opening signal in engineer station and sends into metering module, adjusts desalination water loop electricity The aperture of movable valve, thus controlling the urea concentration of long lance ejection, specially raising with CO concentration, increasing demineralized water Flow;Reduce with CO concentration, reduce desalination discharge.
4) short spray gun urea liquid flow adopts every layer of centralized Control, is put into operation the number of plies and every according to unit load range restraint Layer urea liquid total flow, and it is evenly distributed to every short spray gun.The urea liquid entrance being specially every layer short spray gun sets One electrically operated valve, valve opening is adjusted according to unit load.When unit is for underload, for example, reach fully loaded 50%, The short spray gun of the ground floor that puts into operation, the short spray gun of the second layer cuts out, and adjusts the aperture of ground floor valve according to NSR value;In unit is During load, for example, reach fully loaded 75%, the short spray gun of the two-layer that simultaneously puts into operation, and the aperture of two-layer valve is adjusted according to NSR value; When unit is for high load capacity, for example, reach fully loaded 100%, the short spray gun of the second layer that puts into operation, the short spray gun of ground floor cuts out, and root Adjust the aperture of second layer valve according to NSR value.Every short spray gun arranges a manually-operated gate, and all manually-operated gate apertures keep Unanimously.
Wherein, laser detection system adopts TDLAS (Tunable Diode Laser Absorption Spectroscopy, tunable diode laser can absorb spectrum) technology, collect two wavelength lasers in an optical fiber, then make The light sending sequentially passes through the horizontal flue section of W type boiler.Receptor collection light after passed back central control cabinet, by Ratio the light quantity that centre switch board is absorbed to benchmark light quantity and the measured matter molecule of the specific wavelength through boiler is entered Row compares, so that it is determined that the concentration of each measurand, gas temperature is then according to two CO2The ratio of characteristic absorpting spectruming line is surveying Amount.Emitter and receptor, can be joined from dynamic(al) correction to guarantee also to obtain optimal light quantity transmission in boiler disturbance simultaneously There are instrument air-blowing sweeping device and pneumatic coke removing appts, to ensure the unimpeded of exploration hole.In the present invention, in the two ends of horizontal flue dress There are transmitting terminal 85 and receiving terminal 86, when laser sends from side, after the receiving terminal 86 of corresponding end receives, shape in horizontal flue Become a measuring route, these paths can measure CO concentration and fire box temperature in burner hearth simultaneously.
The principle of TDLAS measurement is that gas molecule has an Absorption to the light of characteristic frequency (wavelength), absorbance with Temperature, pressure, path are related with gas concentration.For a known path and gas pressure, by collecting simultaneously Analysis absorbance in a characteristic absorption frequency range for the laser is it may be determined that the temperature of flue gas and concentration of component.

Claims (10)

1. a kind of thermal power plant W type boiler SNCR denitration system is it is characterised in that include being arranged on W type boiler (10) horizontal flue The long spray gun (1) in region, divides the multiple short spray gun (2) of multilamellar setting in W type boiler (10) furnace arch, furnace nose region, and laser detection System and the metering module (6) being sequentially connected and distribute module (7);
Distribute module (7) includes long spray gun distribute module (71) and the outfan short spray gun of connection that outfan connects long spray gun (1) (2) short spray gun distribute module;
Metering module (6) input for controlling urea concentration connects crude urine element solution reservoir (3) and demineralized water respectively Storage tank (4), outfan connects long spray gun distribute module (71) and short spray gun distribute module respectively;
Central control cabinet (81) that described laser detection system includes being sequentially connected, diode laser (82), fiber optic Multiplexer (83), optical fiber (84) and multigroup laser instrument;Central control cabinet (81) is used for detecting flue-gas temperature distribution by laser instrument Signal and CO concentration signal;Its outfan connects long spray gun distribute module (71) and metering module respectively through engineer station (9) (6);
Multiple long spray guns (1) are in uniformly multi-tier arrangement on the cross section of horizontal flue, long spray gun distribute module (71) basis The control signal of engineer station (9) controls the urea liquid flow that each long spray gun (1) is sprayed respectively;Every layer short spray gun (2) Urea liquid entrance one electrically operated valve is set, short spray gun distribute module (72) is born according to the unit of W type boiler (10) Lotus and the electrically operated valve aperture of every layer of NSR value control.
2. a kind of thermal power plant W type boiler SNCR denitration system according to claim 1 is it is characterised in that long spray gun (1) is common It is provided with six, and is in uniformly three layers of arrangement on the cross section of horizontal flue, long spray gun (1) place section is uniformly arranged Four groups of laser instrument;Laser instrument and long spray gun (1) interval setting;Every group of laser instrument includes a transmitting terminal (85) and a receiving terminal (86), transmitting terminal (85) connects optical fiber (84), and receiving terminal (86) connects central control cabinet (81).
3. a kind of thermal power plant W type boiler SNCR denitration system according to claim 1 is it is characterised in that long spray gun (1) is cold But end entrance connects the outfan of desalination water storage tank (4), and colling end outlet connects the input of desalination water storage tank (4).
4. a kind of thermal power plant W type boiler SNCR denitration system according to claim 1 is it is characterised in that also include compressing Air reservoir (5), the outfan of compressed air reservoir (5) is respectively used to cooling air and is connected to the colling end of short spray gun (2) enter Mouthful, it is connected between metering module (6) and distribute module (7) for atomizing air.
5. a kind of thermal power plant W type boiler SNCR denitration system according to claim 1 is it is characterised in that described metering Module (6) includes blender (61), and control valve and the effusion meter being separately positioned on blender (61) two entrances;Crude urine element The outfan of solution reservoir (3) and desalination water storage tank (4) is passed through fluid filling pump respectively and is connected with corresponding blender (61) entrance.
6. a kind of thermal power plant W type boiler SNCR denitration system according to claim 1 is it is characterised in that every short spray gun (2) manually-operated gate is set, and all manually-operated gate apertures are consistent.
7. a kind of thermal power plant W type boiler SNCR denitration control method is it is characterised in that based on a kind of fire described in claim 1 In power plant W type boiler SNCR denitration system, including,
The step that urea concentration is adjusted by metering module (6) according to the CO concentration signal that laser detection system obtains;
Each long spray gun (1) is adjusted by long spray gun distribute module (71) according to the temperature distribution signal that laser detection system obtains The step of the urea liquid flow of injection;
Step according to unit load interval put into operation with the NSR value short spray gun of control (2) number of plies and every layer of urea liquid total flow.
8. a kind of thermal power plant W type boiler SNCR denitration control method according to claim 7 is it is characterised in that adjust urine The step of plain solution concentration is specific as follows,
Laser detection system obtains the CO concentration signal in horizontal flue using TDLAS measuring method, and CO concentration signal is in engineering It is converted into a road valve opening signal in teacher station (9) and sends in metering module (6), adjust the control valve of desalination water loop Aperture, thus control the urea concentration that long spray gun (1) sprays;
Raise with CO concentration, increase desalination discharge;Reduce with CO concentration, reduce desalination discharge.
9. a kind of thermal power plant W type boiler SNCR denitration control method according to claim 7 is it is characterised in that adjust every The step of the urea liquid flow that individual long spray gun (1) is sprayed is specific as follows,
Laser detection system obtains the temperature distribution signal of flue gas in horizontal flue using TDLAS measuring method, and Temperature Distribution is believed Number it is converted into multi-way valve opening amount signal in engineer station (9) and sends in long spray gun distribute module (71), adjust each The aperture of long spray gun (1) control valve, thus control the urea liquid flow that every long spray gun (1) is sprayed.
10. a kind of thermal power plant W type boiler SNCR denitration control method according to claim 7 is it is characterised in that control short Spray gun (2) put into operation the number of plies and every layer of urea liquid total flow step specific as follows,
Short spray gun (2) point two-layer is arranged on W type boiler (10) furnace arch, furnace nose region, is the short spray gun of ground floor and from the bottom up successively Two layers of short spray gun;
When the unit of W type boiler (10) is underload, the short spray gun of the ground floor that puts into operation, the short spray gun of the second layer cuts out, and according to NSR Value adjusts the aperture of ground floor valve;
When the unit of W type boiler (10) is middle load, the two-layer that simultaneously puts into operation spray gun, and two-layer valve is adjusted according to NSR value Aperture;
When the unit of W type boiler (10) is high load capacity, put into operation second layer spray gun, and the short spray gun of ground floor cuts out, and according to NSR value Adjust the aperture of second layer valve.
CN201610822505.5A 2016-09-13 2016-09-13 Thermal power plant W type boiler SNCR denitration system and control method thereof Pending CN106422732A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610822505.5A CN106422732A (en) 2016-09-13 2016-09-13 Thermal power plant W type boiler SNCR denitration system and control method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610822505.5A CN106422732A (en) 2016-09-13 2016-09-13 Thermal power plant W type boiler SNCR denitration system and control method thereof

Publications (1)

Publication Number Publication Date
CN106422732A true CN106422732A (en) 2017-02-22

Family

ID=58167917

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610822505.5A Pending CN106422732A (en) 2016-09-13 2016-09-13 Thermal power plant W type boiler SNCR denitration system and control method thereof

Country Status (1)

Country Link
CN (1) CN106422732A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107551783A (en) * 2017-10-18 2018-01-09 中国华能集团公司 A kind of two-stage SNCR denitration system and method
CN108786428A (en) * 2018-06-07 2018-11-13 光大环保技术研究院(南京)有限公司 A kind of SNCR denitration optimal control system and control method
CN108854485A (en) * 2018-08-13 2018-11-23 中国华能集团有限公司 A kind of efficient SNCR denitration system of multistage spray ammonia and method
CN110975582A (en) * 2020-03-03 2020-04-10 山东中航天业科技有限公司 Flue gas desulfurization, denitrification and dust removal system of biomass circulating fluidized bed boiler
CN112516767A (en) * 2020-11-10 2021-03-19 西安热工研究院有限公司 Control method of SNCR (selective non-catalytic reduction) denitration system of coal-fired unit

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040244367A1 (en) * 2003-06-05 2004-12-09 Swanson Larry William Multi-compartment overfire air and N-agent injection system and method for nitrogen oxide reduction in flue gas
CN101433799A (en) * 2008-12-04 2009-05-20 哈尔滨工业大学 Selective non-catalytic reduction method for gasifying and atomizing biomass and used boiler
JP2009162762A (en) * 2003-03-31 2009-07-23 Zolo Technologies Inc Method and apparatus for monitoring and control of combustion
CN102301103A (en) * 2009-01-30 2011-12-28 三菱重工业株式会社 Exhaust gas cleaning device
CN202683062U (en) * 2012-07-26 2013-01-23 北京同方亚热能技术有限公司 Amino selective non-catalytic reduction (SNCR) flue gas denitration device
CN203220850U (en) * 2013-03-27 2013-10-02 合肥水泥研究设计院 Jet system suitable for SNCR (selective non-catalytic reduction) flue gas denitrification system of cement kiln
CN105289233A (en) * 2015-11-11 2016-02-03 中国华能集团公司 Coal-fired boiler SNCR and SCR combined denitration system and method thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009162762A (en) * 2003-03-31 2009-07-23 Zolo Technologies Inc Method and apparatus for monitoring and control of combustion
US20040244367A1 (en) * 2003-06-05 2004-12-09 Swanson Larry William Multi-compartment overfire air and N-agent injection system and method for nitrogen oxide reduction in flue gas
CN101433799A (en) * 2008-12-04 2009-05-20 哈尔滨工业大学 Selective non-catalytic reduction method for gasifying and atomizing biomass and used boiler
CN102301103A (en) * 2009-01-30 2011-12-28 三菱重工业株式会社 Exhaust gas cleaning device
CN202683062U (en) * 2012-07-26 2013-01-23 北京同方亚热能技术有限公司 Amino selective non-catalytic reduction (SNCR) flue gas denitration device
CN203220850U (en) * 2013-03-27 2013-10-02 合肥水泥研究设计院 Jet system suitable for SNCR (selective non-catalytic reduction) flue gas denitrification system of cement kiln
CN105289233A (en) * 2015-11-11 2016-02-03 中国华能集团公司 Coal-fired boiler SNCR and SCR combined denitration system and method thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
战佳宇等: "《固体废弃协同处理与综合利用》", 31 December 2014 *
毛志伟等: "《氮氧化物减排》", 31 August 2014 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107551783A (en) * 2017-10-18 2018-01-09 中国华能集团公司 A kind of two-stage SNCR denitration system and method
CN107551783B (en) * 2017-10-18 2023-10-20 中国华能集团公司 Two-stage SNCR denitration system and method
CN108786428A (en) * 2018-06-07 2018-11-13 光大环保技术研究院(南京)有限公司 A kind of SNCR denitration optimal control system and control method
CN108854485A (en) * 2018-08-13 2018-11-23 中国华能集团有限公司 A kind of efficient SNCR denitration system of multistage spray ammonia and method
CN108854485B (en) * 2018-08-13 2024-06-11 中国华能集团有限公司 Multistage ammonia injection efficient SNCR denitration system and method
CN110975582A (en) * 2020-03-03 2020-04-10 山东中航天业科技有限公司 Flue gas desulfurization, denitrification and dust removal system of biomass circulating fluidized bed boiler
CN112516767A (en) * 2020-11-10 2021-03-19 西安热工研究院有限公司 Control method of SNCR (selective non-catalytic reduction) denitration system of coal-fired unit

Similar Documents

Publication Publication Date Title
CN206027413U (en) W of thermal power plant type boiler SNCR deNOx systems
CN106422732A (en) Thermal power plant W type boiler SNCR denitration system and control method thereof
CN104226110B (en) Coal-fired boiler SCR (Selective Catalytic Reduction) denitration control method and system
CN107405567B (en) Multiple injection grid arrangement
CN108896510B (en) SCR outlet ammonia concentration plane distribution online detection system and method
US7846405B2 (en) Method and apparatus for measuring and controlling selective catalytic reduction (SCR) emission control systems
CN205216566U (en) SNCR (Selective non catalytic reduction) denitration device
CN105473942A (en) Injector grid for high and low dust environment selective catalytic reduction systems
CN201907975U (en) Pyrolysis device for utilizing urea for ammonia preparation
CN105854598A (en) Uniform ammonia spraying system and method for controlling same
CN105920997A (en) Coal-fired boiler denitration system and method with over fire air and SNCR coupled
CN104147912A (en) Flue-gas denitration method and device by mixing of selective non-catalytic reduction method SNCR and selective catalytic reduction method SCR
CN207913518U (en) The accurate spray ammonia system of the adaptive leveling of full load
CN107764774A (en) It is a kind of while measure the device and method of nitric oxide and ammonia in denitrating flue gas
CN106552509B (en) A kind of boiler run control method for preventing SCR denitration area from blocking
CN107008144B (en) Device for realizing SCR flue gas denitration multistage ammonia spraying and flue gas denitration method
CN108816043A (en) A kind of denitration device and its autocontrol method
CN106310933A (en) Flue gas denitration system for coal water slurry boiler and method for denitrating flue gas
CN113091050A (en) Optimization system combining tail denitration and in-furnace combustion and control method thereof
CN210303177U (en) SNCR and SCR coupling flue gas denitration device of pulverized coal furnace
CN206853478U (en) Utilize the ammonia spraying and mixing system of outside filtering type dust catcher gas purifying chamber structure
CN202087235U (en) Multi-level thermolysis coupling denitrification device with pre-flow field equalizing device
CN101687142B (en) System and method for decreasing Nox emissions from fluidized bed combustion system
CN211302681U (en) Ammonia spraying device with accurate and controllable ammonia spraying amount in SCR system
CN101284203A (en) Method and apparatus for removing SO3 from flue gas

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination