CN106989412A - Powder and by weight air distribution control device and its control method are supplied by coal dust balanced weight - Google Patents

Powder and by weight air distribution control device and its control method are supplied by coal dust balanced weight Download PDF

Info

Publication number
CN106989412A
CN106989412A CN201611225253.4A CN201611225253A CN106989412A CN 106989412 A CN106989412 A CN 106989412A CN 201611225253 A CN201611225253 A CN 201611225253A CN 106989412 A CN106989412 A CN 106989412A
Authority
CN
China
Prior art keywords
weight
air
powder
wind
coal
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.)
Granted
Application number
CN201611225253.4A
Other languages
Chinese (zh)
Other versions
CN106989412B (en
Inventor
邸生才
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.)
Di Shengcai
Hebei Bangruida Technology Co Ltd
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201611225253.4A priority Critical patent/CN106989412B/en
Priority to PCT/CN2017/000410 priority patent/WO2018120256A1/en
Publication of CN106989412A publication Critical patent/CN106989412A/en
Application granted granted Critical
Publication of CN106989412B publication Critical patent/CN106989412B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/02Regulating fuel supply conjointly with air supply
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01PMEASURING LINEAR OR ANGULAR SPEED, ACCELERATION, DECELERATION, OR SHOCK; INDICATING PRESENCE, ABSENCE, OR DIRECTION, OF MOVEMENT
    • G01P5/00Measuring speed of fluids, e.g. of air stream; Measuring speed of bodies relative to fluids, e.g. of ship, of aircraft
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01PMEASURING LINEAR OR ANGULAR SPEED, ACCELERATION, DECELERATION, OR SHOCK; INDICATING PRESENCE, ABSENCE, OR DIRECTION, OF MOVEMENT
    • G01P5/00Measuring speed of fluids, e.g. of air stream; Measuring speed of bodies relative to fluids, e.g. of ship, of aircraft
    • G01P5/14Measuring speed of fluids, e.g. of air stream; Measuring speed of bodies relative to fluids, e.g. of ship, of aircraft by measuring differences of pressure in the fluid
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/70Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Landscapes

  • Engineering & Computer Science (AREA)
  • Aviation & Aerospace Engineering (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Regulation And Control Of Combustion (AREA)

Abstract

The invention discloses a kind of " by coal dust balanced weight for powder and air distribution control device and its control method by weight ", the device is made up of deliver coal powder Weight-measuring device, primary air speed measuring device, secondary wind speed measurement apparatus and blower fan etc. of wind.The device is arranged in existing coal-burning boiler powder, powder-supply system, each air delivery pipe coal dust weight is measured and balanced for powder control, and air distribution control is carried out according to coal dust weight, make coal dust weight with meeting given excess air coefficient α requirements with the ratio between air quantity.Using the present invention each bypass line as-fired coal powder weight can be made consistent, each bypass line coal dust weight is consistent with the ratio between air quantity, make boiler coal-ash flameholding, thermic load, uniformity of temperature profile, coal dust firing is fully efficient, so as to meet efficient, consumption reduction, emission reduction requirement, the stability, security, economy of boiler operatiopn are also improved.

Description

Powder and by weight air distribution control device and its control method are supplied by coal dust balanced weight
Technical field
It is related to coal-burning boiler equilibrium by weight and supplies powder and by weight air distribution.
Background technology
Coal-burning boiler, such as coal-fired power station boiler, big thermoelecrtic boiler, Industrial Boiler, cement kiln boiler are sent using wind Pipeline supplies powder to boiler, for example:Powder processed, the powder-supply system of large-sized station boiler, powder, one coal-grinding of every layer of use are supplied using multilayer Mechanism powder, powder is supplied with multiple air delivery pipes.Large-sized boiler is typically three layers --- and six layers supply powder, one coal pulverizer of every layer of use, band Four pipelines, 12-24 pipeline altogether, each layer device therefor is identical.(such as Fig. 1 is expressed as follows with one layer of powder processed, for powder equipment It is shown):
Certain mass coal dust enters stove burning, need to match somebody with somebody the air of certain volume.1Kg (or 1m3) fuel burn completely (burning Afterwards without remaining oxygen) needed for bottom line air capacity (with V0Represent) it is referred to as theoretical air requirement, during boiler operatiopn, to make Fuel after-flame, the air capacity of effective supply is (with VkRepresent), always slightly larger than theoretical air requirement V0, itsReferred to as excess air Coefficient, i.e.,:
α --- represented with exhaust gas volumn, β --- represented with air capacity;
Weight of fuel W(kg)Burning completely need to be with air capacity:
Can excess air coefficient size, in addition to directly affecting coal dust and burn completely, can also influence fuel fire, burning Thermal losses and pollutant yield in stability and flue gas.It can be seen that α or β are the important parameters of boiler operatiopn.
Existing powder processed, powder-supply system are with two loops pairWhat ratio was adjusted.One is that fuel quantity is adjusted back Road, heat load adjustment needed for fuel quantity tracking generates electricity, two be to match somebody with somebody air quantity according to oxygen content regulation in flue gas, maintains excess air Factor alpha is in the certain limit of setting, oxygen content and α relations:
O2--- amount of oxygen
Oxygen content is aware of, formula can calculate excess air coefficient α by (3).
Existing powder processed, powder-supply system regulation fuel quantity/there is problem with air quantity have:
1st, air quantity is matched somebody with somebody according to flue gas oxygen content regulation, is that one kind lags regulation, flue gas oxygen content only reflects coal dust firing shape Condition (burning deficiency, excessive, burning completely of burning).This regulation that lags, it is impossible to air quantity is matched somebody with somebody according to coal dust adjustment of weight, madeThe ratio between reach the complete burning condition of coal dust in real time;
2nd, existing powder processed, powder-supply system, each branch road air delivery pipe coal dust weight change and each bypass line deviation of weight become Change and influenced each other with the change of each branch road air distribution amount of Secondary Air and change of error, cause each branch roadThe ratio between change it is big, from And causing uneven, the unstable and burning quality that burnt in stove to decline, such as oxygen content is more in flue gas, should lower with air quantity, but this Shi Ruguo as-fired coal powder amounts increase, and opposite air distribution effect can be caused by being lowered with air quantity.
There is problem for above-mentioned, the invention discloses a kind of " by coal dust balanced weight for powder and air distribution control by weight Device and its control method ", can be achieved balanced by weight for powder and air distribution control by weight.
The content of the invention
The control device of the present invention is made up of two control loops, and one is that as-fired coal powder weight and Secondary Air air quantity are equal Weigh control loop, and two be according to coal dust weight air distribution control loop.The technical problem solved is:
1st, using " wind deliver coal powder Weight-measuring device ", solve the problems, such as that wind is delivered coal coal dust weight measurement in powder pipeline;
2nd, using Balance route technology, each bypass line coal dust weight W of First air is solvedA、WB、WC、WDConsistent equilibrium For powder problem;
3rd, using Balance route technology, solve each bypass line of Secondary Air and match somebody with somebody air quantity V2A、V2B、V3C、V4DConsistent equilibrium Air distribution problem, realizes that equilibrium, for powder, balanced air feed, can make coal dust firing in stove uniformly, stably, improve burning quality;
4th, according to air quantity is matched somebody with somebody after coal dust weight after equilibrium and equilibrium, (become using from motion tracking variable element and set controlling value) Control technology, make each branch road coal dust weight and each branch road with air quantity i.e.The ratio between it is consistent, the air distribution ratio again with it is given Excess air coefficient α it is consistent, meet the complete burning condition of as-fired coal powder weight, can fully, efficient burning.
One kind " balanced by weight to supply powder and by weight air distribution control device " of the present invention, installed in existing coal-burning boiler In powder processed, powder-supply system, it is technically characterized in that, including:
Wind is delivered coal powder Weight-measuring device (12) or (12A), (12B), (12C), (12D), installed in an air delivery pipe House steward (6) or branch pipe (6A), (6B), (6C), (6D) above, for measuring coal dust weight W or W in house steward or branch pipeA、WB、WC、 WD
First air blower fan (4) (being existing powder processed, powder-supply system equipment), in front of coal pulverizer (2), for producing First air, and bring the coal dust worn into an air delivery pipe, deliver to burner (7A), (7B), (7C), (7D);
Primary air speed measuring device (11), installed in an air delivery pipe house steward (6) or each branch pipe (6A), (6B), On (6C), (6D), for measuring air delivery pipe house steward's wind speedOr branch pipe wind speed
Secondary Air blower fan (10) (being existing powder processed, powder-supply system equipment), installed in Secondary Air air delivery pipe initiating terminal, For producing Secondary Air and delivering to burner (7A), (7B), (7C), (7D);
Secondary wind wind speed measurement apparatus (14), installed in Secondary Air air delivery pipe total pipeline (9) or each branch pipe(tube) (9A), On (9B), (9C), (9D), for measuring Secondary Air air delivery pipe (9) wind speedOr
Data acquisition controller (13), for receive wind deliver coal powder Weight-measuring device (12) or (12A), (12B), (12C), (12D) signal W or WA、WB、WC、WD, primary air speed measuring device (11) or (11A), (11B), (11C), (11D) letter NumberOrWith secondary wind speed measurement apparatus (14) or (14A), (14B), (14C), (14D) SignalOr
Data acquisition controller (13) is controlled according to signal and given excess air coefficient α progress equilibriums is received for powder Air distribution is controlled by weight.
" supplying powder and by weight air distribution control device by coal dust balanced weight " is characterized in that, data acquisition controller (13) Balance route technology is used, to WA、WB、WC、WDControl is adjusted, makes WA、WB、 WC、WDIt is consistent.
" supplying powder and by weight air distribution control device by coal dust balanced weight " is characterized in that, data acquisition controller (13), according to coal dust gross weight W and given excess air coefficient α, calculate and secondary needed for W match somebody with somebody air quantityWithAnd according toControl is adjusted to Secondary Air rotation speed of fan, to increase or decrease V2, make V2WithIt is consistent.
" supplying powder and by weight air distribution control device by coal dust balanced weight " is characterized in that, data acquisition controller (13) coal dust weight summation W (W=W after each pipeline equilibrium are calculatedA+WB+WC+WD), and given excess air coefficient α, calculate W It is required secondary with air quantityWithFoundationControl is adjusted to Secondary Air rotation speed of fan, to increase Add deduct few V2, make V2WithIt is consistent.
" supplying powder and by weight air distribution control device by coal dust balanced weight ", it is characterised in that also adjusted including a wind speed Regulating device (15), install Secondary Air send between total pipeline (9) and bypass line (9A), (9B), (9C), (9D), for adjust into Enter wind speed in each bypass line of Secondary Air Namely adjust air quantity V corresponding thereto2A、 V2B、V3C、V4D
" supplying powder and by weight air distribution control device by coal dust balanced weight ", it is characterised in that data acquisition controller (13), using Balance route technology, control signal is sent to wind-speed adjusting device (15), adjustedMakeIt is consistent.
" supplying powder and by weight air distribution control device by coal dust balanced weight ", it is characterised in that the Balance route technology It is:Data acquisition controller (13) is calculatedOr With WIt is flatOr V2 is flatAs setting controlling value, Δ W is calculatedA=WIt is flat-WA, Δ WB=WIt is flat-WB, Δ WC=WIt is flat-WC, Δ WD=WIt is flat-WDOr ΔV2A=V2 is flat- V2A, Δ V2B=V2 is flat-V2B, Δ V2C=V2 is flat-V2C, Δ V2D=V2 is flat-V2D;According to Δ WA、ΔWB、 ΔWC、ΔWD Control signal is sent to pulverized coal distributor (5), makes WA、WB、WC、WDWith WIt is flatIt is consistent;Or according to Δ V2A、ΔV2B、ΔV2C、Δ V2DRegulation control signal is sent to wind-speed adjusting device (15), makes V2A、 V2B、V2C、V2DWith V2 is flatIt is consistent.
" supplying powder and by weight air distribution control device by coal dust balanced weight ", it is characterised in that data acquisition controller root After equilibrium, each branch road coal dust weight sum W (W=W of First airA+WB+WC+WD) and it is balanced after each branch road air quantity of Secondary Air it And V2(V2=VA+VB+VC+VD), and excess air coefficient α is given, the Secondary Air needed for calculating W values matches somebody with somebody air quantityWith its differenceAnd withSecondary Air rotation speed of fan is adjusted, V is increased or decreased2, make V2WithIt is consistent.
Current wind powder weight measurements of delivering coal mainly have:Ionization radiation method, heat balance method of, energy method, light-electro-detection Method, capacitance method, microwave method, capacitance chromatography imaging method, laser method, electrostatic induction method etc., control device apoplexy of the present invention are delivered coal powder Any wind that the above method may be selected in Weight-measuring device is delivered coal powder Weight-measuring device.
" balanced by weight for powder and air distribution device by weight ", it is characterised in that " wind deliver coal powder Weight-measuring device " (12) it is that ionising radiation formula wind delivers coal powder Weight-measuring device or heat balance method of wind is delivered coal powder Weight-measuring device, or energy Amount method wind is delivered coal powder measurement apparatus, or optical-electronic detection method wind is delivered coal powder Weight-measuring device, or capacitance method wind is delivered coal powder Measurement apparatus, or capacitance chromatography imaging method wind are delivered coal powder Weight-measuring device, or microwave method wind is delivered coal powder weight measurement dress Put, or laser method wind is delivered coal powder Weight-measuring device, or electrostatic induction method wind is delivered coal powder Weight-measuring device.
" supplying powder and by weight air distribution control device by coal dust balanced weight ", it is characterised in that primary air speed measuring device It is differential pressure type wind speed measuring device backrest tubular type wind speed measuring device or flute-form wind with secondary wind speed measurement apparatus Speed measuring device, or wing type wind speed measuring device, or double-venturi tubular type wind speed measuring device.
A kind of control method of " supplying powder and by weight air distribution control device by coal dust balanced weight ", it is characterised in that bag Include following steps:
Step 1, data acquisition, data acquisition controller gathers following signal:
(1) coal dust weight signal W or WA、WB、WC、WD
(2) primary air velocity signalOr
(3) secondary wind speed signalOr
Step 2, equilibrium supplies powder, and data acquisition controller (13) uses Balance route technology, pulverized coal distributor (5) is entered Row regulation control, makes WA、WB、WC、WDIt is consistent;
Step 3, judge whether to also need to air distribution control
NO --- return
Yes --- carry out air distribution control
Step 4, air distribution is controlled by weight
Step 4.1 carries out air distribution control by coal dust gross weight
Data acquisition controller (13), according to gross weight W and given α values, calculates and matches somebody with somebody air quantity required for WAnd it is poor ValueAnd pressControl is adjusted to overfire air fan, makes V2WithIt is consistent;
Step 4.2 is by balanced for the control of powder weight air distribution
Data acquisition controller (13), according to W=WA+WB+WC+WDWith given side reaction coefficient, W is calculated required with air quantity And differenceAnd pressControl is adjusted to Secondary Air blower fan, makes V2WithIt is consistent;
Step 4.3 presses balanced coal dust weight and balanced secondary air flow carries out air distribution control
Data acquisition controller (13) utilizes Balance route technology, and pulverized coal distributor (5) is controlled, makes WA、WB、 WC、WDIt is consistent;Using Balance route technology, wind-speed adjusting device (15) is controlled, makes V2A、V2B、V2C、V2DXiang Yi Cause, and calculate W=WA+WB+WC+WDAnd V2=V2A+V2B+V2C+V2D, according to W and α, needed for calculating WWithAnd pressSecondary Air blower fan is controlled, makes V2WithIt is consistent.
Brief description of the drawings
Fig. 1 mono- layers of a coal-grinding mechanism powder, powder-supply system capital equipment schematic diagram
1 --- feeder
2 --- coal pulverizer
3 --- thick, pulverized-coal collector
4 --- First air blower fan
5 --- pulverized coal distributor
6 --- First air total pipeline
6A, 6B, 6C, 6D --- First air bypass line
7A, 7B, 7C, 7D --- burner
8 --- boiler
9 --- Secondary Air total pipeline
9A, 9B, 9C, 9D --- Secondary Air bypass line
10 --- Secondary Air blower fan
Fig. 2 (a) inventions control device installs schematic diagram on total pipeline in Fig. 1
11 --- First air wind speed measuring device
12 --- wind is delivered coal powder Weight-measuring device
13 --- data acquisition controller
14 --- secondary wind wind speed measurement apparatus
Fig. 2 (b) inventions control device installs each branch road air delivery pipe schematic diagram in Fig. 1
Fig. 3 apparatus of the present invention are installed realizes that equilibrium supplies powder, by weight air distribution schematic diagram in Fig. 1
12A, 12B, 12C, 12D --- wind are delivered coal powder Weight-measuring device
Fig. 4 control devices of the present invention are installed realizes equilibrium for powder, balanced air feed and weight air distribution schematic diagram in Fig. 1
14A, 14B, 14C, 14D --- secondary wind wind speed measurement apparatus
15 --- wind-speed adjusting device
Fig. 5 is controlled and air distribution control method block diagram by weight by coal dust balanced weight for powder
Embodiment
Technical scheme and implementation are further described below with reference to accompanying drawing:
Fig. 1 is one layer of a coal-grinding mechanism powder, powder-supply system capital equipment schematic diagram.Fig. 2 (a), Fig. 2 (b), Fig. 3, Fig. 4 It is the different device that control device of the present invention is included when completing different task, schematic diagram in Fig. 1 is installed.This will again Illustrate, the equipment or measurement apparatus included by control device of the present invention are complete together with existing powder processed, the equipment of powder-supply system Into powder and air distribution task is supplied, the device that control device of the present invention should include is existing in Fig. 1, in force may not be used Set up again.
Fig. 2 (a) wind delivers coal powder Weight-measuring device (12) on air delivery pipe total pipeline (6), is sent for measuring wind Pipeline (6) coal dust gross weight W, wind speed measuring device (11) is arranged on air delivery pipe (6), for measuring wind speedCount according to this Calculate air quantityd1--- First air send pipe diameter, and wind send speed measuring device (14) to measure Secondary Air and sent Air velocity ductAir output is calculated according to thisd2--- Secondary Air send pipe diameter;Fig. 2 (b) wind is sent Coal dust Weight-measuring device (12A), (12B), (12C), (12D) be arranged on bypass line (6A), (6B), (6C), on (6D), For measuring each bypass line coal dust weight WA、WB、WC、WD, wind speed measuring device (11A), (11B), (11C), (11D) also pacify On bypass line (6A), (6B), (6C), (6D), for measuringAnd calculate W=WA+ WB+WC+WDAnd V1=V1A+V1B+V1C+V1D, Fig. 2 (a), Fig. 2 (b) data acquisition controller are according to W and excess air coefficient α Calculate needed for W secondary matches somebody with somebody air quantityWithAnd pressSecondary Air blower fan is entered Row regulation control, makes V2WithIt is consistent.
Fig. 2 (a), Fig. 2 (b) embodiment are to complete air distribution control by coal dust gross weight, so as to realize coal dust gross weight Consistent with excess air α with the ratio between secondary air distribution total amount, its weak point is, each bypass line coal dust weight of First air with Each branch road of Secondary Air differs larger with each other with the ratio between air quantity, influences burning quality.
Fig. 3 embodiments, being completed for task is:
(1) realize that coal dust balanced weight supplies powder;
(2) air distribution control is carried out according to balanced coal dust weight.
The program supplies powder due to equilibrium, makes WA、WB、WC、WDIt is consistent, thus reduce each bypass line coal dust weight with Each branch road improves each branch road air distribution quality with the difference between the ratio between air quantity, the program be the present invention preferred scheme it One.
Fig. 4 embodiments are balanced for powder and balanced air feed and weight air distribution control program, and each branch road of First air can be achieved Coal dust weight is consistent, and each branch road wind supply quantity of Secondary Air is consistent, and the weight of each branch road is with the air distribution with air quantity than also phase one Cause, and the air distribution is more consistent than with given excess air coefficient α.The embodiment is optimum implementation.
During Fig. 5 is the block diagram of control method of the present invention, figure:
Step 1,2,3 are to complete coal dust balanced weight to control for powder;Step 1,2,3,4.1 are completed by coal dust gross weight W Carry out air distribution control;Step 1,2,3,4.2 are to complete balanced for powder and by the control of coal dust weight air distribution;Step 1,2,3,4.3 are Complete balanced for powder, balanced air feed and by the control of coal dust weight air distribution.
It is of the invention that with uniform for powder, air feed is uniform compared with existing powder processed, powder-supply system, each branch road coal dust weight with It is consistent with the ratio between air quantity, and the ratio is consistent with given excess air coefficient, so as to reach that boiler coal-ash burning is in center Flame stabilization, thermic load, uniformity of temperature profile, coal dust firing are in abundant, efficient optimum state, improve the thermal efficiency, reduce Flue gas thermal losses, reduces fluff pulp, is that enterprise brings considerable economic benefit and social benefit.
The control device of the present invention can complete independently:
1st, coal dust balanced weight is controlled for powder;
2nd, controlled by coal dust weight air distribution;
3rd, equilibrium is for powder control, balanced air feed control and air distribution control by weight.
Function above controls to belong to the protection domain of this patent.

Claims (11)

1. a kind of equilibrium by weight supplies powder and by weight air distribution control device, installed in existing coal-burning boiler powder, powder-supply system In, it is technically characterized in that, including:
Wind is delivered coal powder Weight-measuring device (12) or (12A), (12B), (12C), (12D), installed in an air delivery pipe house steward (6) or branch pipe (6A), (6B), (6C), (6D) above, for measuring coal dust weight W or W in house steward or branch pipeA、WB、WC、WD
First air blower fan (4) (being existing coal dust preparation system equipment), in front of coal pulverizer (2), for producing First air, And bring the coal dust worn into an air delivery pipe, deliver to burner (7A), (7B), (7C), (7D);
Primary air speed measuring device (11), installed in an air delivery pipe house steward (6) or each branch pipe (6A), (6B), (6C), (6D) On, for measuring air delivery pipe house steward's wind speed ν1Or branch pipe wind speed ν1A、ν1B、ν1C、ν1D
Secondary Air blower fan (10) (being existing coal dust preparation system equipment), installed in Secondary Air air delivery pipe initiating terminal, for producing Raw Secondary Air simultaneously delivers to burner (7A), (7B), (7C), (7D);
Secondary wind wind speed measurement apparatus, installed in Secondary Air air delivery pipe total pipeline (9) or each branch pipe(tube) (9A), (9B), (9C), On (9D), for measuring Secondary Air air delivery pipe (9) wind speed ν2Or each bypass line ν2A、ν2B、ν2C、ν2D
Data acquisition controller (13), for receive wind deliver coal powder Weight-measuring device 12 or 12A, 12B, 12C, 12D signal W or WA、WB、WC、WD, primary air speed measuring device (11) or (11A), (11B), (11C), (11D) signal ν1Or ν1A、ν1B、ν1C、ν1D、 With secondary wind speed measurement apparatus (14) or (14A), (14B), (14C), (14D) signal ν2Or ν2A、ν2B、ν2C、ν2D
Data acquisition controller (13) carries out equilibrium for powder control and by weight according to signal and given excess air coefficient α is received Measure air distribution control.
2. according to claim 1, supply powder and by weight air distribution control device by coal dust balanced weight, it is characterised in that number Balance route technology is used according to acquisition controller (13), to WA、WB、WC、WDControl is adjusted, makes WA、WB、WC、WDIt is consistent.
3. according to claim 1, supply powder and by weight air distribution control device by coal dust balanced weight, it is characterised in that number According to acquisition controller (13), according to coal dust gross weight W and given excess air coefficient α, calculate and secondary needed for W match somebody with somebody air quantity WithAnd according toControl is adjusted to overfire air fan rotating speed, to increase or decrease V2, make V2WithIt is consistent.
4. according to claim 1, supply powder and by weight air distribution control device by coal dust balanced weight, it is characterised in that number Coal dust weight summation W (W after each pipeline equilibrium are calculated according to acquisition controller (13)A+WB+WC+WD), and according to W and given surplus It is secondary needed for air coefficient α calculating W to match somebody with somebody air quantityWithFoundationOverfire air fan rotating speed is adjusted Section control, to increase or decrease V2, make V2WithIt is consistent.
5. according to claim 1, supply powder and by weight air distribution control device by coal dust balanced weight, it is characterised in that also Including a wind-speed adjusting device (15), install Secondary Air send total pipeline (9) and bypass line (9A), (9B), (9C), (9D) it Between, enter wind speed ν in each branch pipe(tube) for adjusting2A、ν2B、ν2C、ν2DThat is, adjust air quantity V corresponding thereto2A、V2B、 V2C、V2D
6. according to claim 1,5, powder and by weight air distribution control device are supplied by coal dust balanced weight, it is characterised in that Data acquisition controller (13) uses Balance route technology, and control signal is sent to wind-speed adjusting device (15), adjusts ν2A、ν2B、 ν2C、ν2DMake air quantity V2A、V2B、V2C、V2DIt is consistent.
7. according to claim 1,2,6, powder and by weight air distribution control device are supplied by coal dust balanced weight, its feature exists In the Balance route technology is:Data acquisition controller (13) is calculatedOrWith WIt is flatOr V2 is flatAs setting controlling value, Δ W is calculatedA=WIt is flat-WA, Δ WB=WIt is flat-WB, ΔWC=WIt is flat-WC, Δ WD=WIt is flat-WDOr Δ V2A=V2 is flat-V2A, Δ V2B=V2 is flat-V2B, Δ V2C=V2 is flat-V2C, Δ V2D=V2 is flat-V2D; According to Δ WA、ΔWB、ΔWC、ΔWDRegulation control signal is sent to pulverized coal distributor (5), makes WA、WB、WC、WDWith WIt is flatIt is consistent; Or according to Δ V2A、ΔV2B、ΔV2C、ΔV2DControl signal is sent to wind-speed adjusting device (15), makes V2A、V2B、V2C、V2DWith V2 is flat It is consistent.
8. according to claim 1,2,6, powder and by weight air distribution control device are supplied by coal dust balanced weight, its feature exists In data acquisition controller (13), according to each road coal dust weight sum W (W=W of First air after equilibriumA+WB+WC+WD), it is balanced after Each branch road of Secondary Air matches somebody with somebody air quantity sum V2(V2=V2A+V2B+V2C+V2D) and give excess air coefficient α, calculate two needed for W values Secondary wind matches somebody with somebody air quantityWith its differenceAnd withSecondary Air rotation speed of fan is adjusted, V is increased or decreased2, Make V2WithIt is consistent.
9. according to claim 1, balanced by weight for powder and air distribution device by weight, it is characterised in that " wind is delivered coal powder weight Measuring device " (12) is that ionising radiation formula wind is delivered coal powder Weight-measuring device, or heat balance method of wind is delivered coal powder weight measurement Device, or energy method wind are delivered coal powder measurement apparatus, or optical-electronic detection wind is delivered coal powder Weight-measuring device, or capacitance method Wind is delivered coal powder measurement apparatus, or capacitance chromatography imaging method wind is delivered coal powder Weight-measuring device, or microwave method wind is delivered coal powder weight Measuring device, or laser method wind are delivered coal powder Weight-measuring device, or electrostatic induction method wind is delivered coal powder Weight-measuring device.
10. according to claim 1, " supply powder and by weight air distribution control device by coal dust balanced weight ", it is characterised in that Primary air speed measuring device and secondary wind speed measurement apparatus are differential pressure type wind speed measuring device or backrest tubular type measuring wind speed dress Put or flute-form wind speed measuring device, or wing type wind speed measuring device, or double-venturi tubular type measuring wind speed dress Put.
11. according to claim 1-10, the controlling party of " supplying powder and by weight air distribution control device by coal dust balanced weight " Method, it is characterised in that comprise the following steps:
Step 1, data acquisition, data acquisition controller (13) gathers following signal:
(1) coal dust weight signal W or WA、WB、WC、WD
(2) primary air velocity signal ν1Or ν1A、ν1B、ν1C、ν1D
(3) secondary wind speed signal ν2Or ν2A、ν2B、ν2C、ν2D
Step 2, equilibrium supplies powder, and data acquisition controller (13) uses Balance route technology, pulverized coal distributor (5) is adjusted Control, makes WA、WB、WC、WDIt is consistent;
Step 3, judge whether to also need to air distribution control
NO --- return
Yes --- carry out air distribution control;
Step 4, air distribution is controlled by weight
Step 4.1 carries out air distribution control by coal dust gross weight
Data acquisition controller, according to gross weight W and given α values, matches somebody with somebody air quantity required for calculatingAnd differenceAnd pressControl is adjusted to Secondary Air blower fan, makes V2WithIt is consistent;
Step 4.2 is by balanced for the control of powder weight air distribution
Data acquisition controller (13), according to W=WA+WB+WC+WDWith given factor alpha, W is calculated required with air quantityAnd it is poor ValueAnd pressControl is adjusted to Secondary Air blower fan, makes V2WithIt is consistent;
Step 4.3 presses balanced coal dust weight and balanced Secondary Air air quantity carries out air distribution control
Data acquisition controller (13) utilizes Balance route technology, and pulverized coal distributor (5) is controlled, makes WA、WB、WC、WDPhase Unanimously;Using Balance route technology, wind-speed adjusting device (15) is controlled, makes V2A、V2B、V2C、V2DIt is consistent, and calculate Go out W=WA+WB+WC+WDAnd V2=V2A+V2B+V2C+V2D, air quantity is matched somebody with somebody according to needed for W and α calculate WWithAnd pressControl is adjusted to Secondary Air blower fan, makes V2WithIt is consistent.
CN201611225253.4A 2016-12-28 2016-12-28 Balanced powder supply and weight air distribution control device according to weight of pulverized coal and control method thereof Active CN106989412B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201611225253.4A CN106989412B (en) 2016-12-28 2016-12-28 Balanced powder supply and weight air distribution control device according to weight of pulverized coal and control method thereof
PCT/CN2017/000410 WO2018120256A1 (en) 2016-12-28 2017-06-27 Control device for supplying powder in a balanced manner according to coal dust weight and distributing air according to weight and control method therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611225253.4A CN106989412B (en) 2016-12-28 2016-12-28 Balanced powder supply and weight air distribution control device according to weight of pulverized coal and control method thereof

Publications (2)

Publication Number Publication Date
CN106989412A true CN106989412A (en) 2017-07-28
CN106989412B CN106989412B (en) 2023-07-14

Family

ID=59414076

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611225253.4A Active CN106989412B (en) 2016-12-28 2016-12-28 Balanced powder supply and weight air distribution control device according to weight of pulverized coal and control method thereof

Country Status (1)

Country Link
CN (1) CN106989412B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112718223A (en) * 2021-01-13 2021-04-30 桂林鸿程矿山设备制造有限责任公司 Pulverizer fan frequency processing system and method and storage medium
CN114353857A (en) * 2020-10-13 2022-04-15 邸生才 Wind and powder two-phase flow measuring system of wind conveying pipeline and two-phase flow control system

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4501206A (en) * 1981-03-17 1985-02-26 L. & C. Steinmuller Gmbh Method of igniting a pulverized-coal pilot-burner flame
CN102032590A (en) * 2010-12-31 2011-04-27 北京华电天仁电力控制技术有限公司 Boiler combustion optimizing control system and optimizing control method based on accurate measurement system
CN102425807A (en) * 2011-11-23 2012-04-25 华北电力大学(保定) Combustion feedforward and feedback composite optimization controlling method for pulverized coal fired boiler
CN203187097U (en) * 2013-03-12 2013-09-11 上海题桥能源科技发展有限公司 Coal dust pneumatic transmission system
CN104728854A (en) * 2013-12-20 2015-06-24 邸生才 Pulverized coal preparation system and method with air-blew pulverized coal heat measurement and control functions
CN105181515A (en) * 2015-10-19 2015-12-23 广东电网有限责任公司电力科学研究院 Method and system for detecting combustion dynamic characteristics of pulverized coal in boiler hearth
CN208635143U (en) * 2016-12-28 2019-03-22 邸生才 By coal dust balanced weight powder supply and air distribution control device by weight

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4501206A (en) * 1981-03-17 1985-02-26 L. & C. Steinmuller Gmbh Method of igniting a pulverized-coal pilot-burner flame
CN102032590A (en) * 2010-12-31 2011-04-27 北京华电天仁电力控制技术有限公司 Boiler combustion optimizing control system and optimizing control method based on accurate measurement system
CN102425807A (en) * 2011-11-23 2012-04-25 华北电力大学(保定) Combustion feedforward and feedback composite optimization controlling method for pulverized coal fired boiler
CN203187097U (en) * 2013-03-12 2013-09-11 上海题桥能源科技发展有限公司 Coal dust pneumatic transmission system
CN104728854A (en) * 2013-12-20 2015-06-24 邸生才 Pulverized coal preparation system and method with air-blew pulverized coal heat measurement and control functions
CN105181515A (en) * 2015-10-19 2015-12-23 广东电网有限责任公司电力科学研究院 Method and system for detecting combustion dynamic characteristics of pulverized coal in boiler hearth
CN208635143U (en) * 2016-12-28 2019-03-22 邸生才 By coal dust balanced weight powder supply and air distribution control device by weight

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114353857A (en) * 2020-10-13 2022-04-15 邸生才 Wind and powder two-phase flow measuring system of wind conveying pipeline and two-phase flow control system
CN112718223A (en) * 2021-01-13 2021-04-30 桂林鸿程矿山设备制造有限责任公司 Pulverizer fan frequency processing system and method and storage medium
CN112718223B (en) * 2021-01-13 2022-02-22 桂林鸿程矿山设备制造有限责任公司 Pulverizer fan frequency processing system and method and storage medium

Also Published As

Publication number Publication date
CN106989412B (en) 2023-07-14

Similar Documents

Publication Publication Date Title
CN101939589B (en) Oxy-fuel combustion system with closed loop flame temperature control
CN103939939B (en) Pulverized-coal fired boiler digital combustion control and optimization method and system
WO2018120256A1 (en) Control device for supplying powder in a balanced manner according to coal dust weight and distributing air according to weight and control method therefor
CN101251263A (en) Power boiler low NOx combustion method and control system based on wind powder closed-loop control
CN108679592B (en) A kind of the boiler load control system and control method of biomass boiler
CN103471101B (en) Multi-spray-nozzle bulky combustion low-NOx gas combustor
CN105408502A (en) Device and method for controlling combustion exhaust gas of regenerative heating furnace
CN208635143U (en) By coal dust balanced weight powder supply and air distribution control device by weight
CN106989412A (en) Powder and by weight air distribution control device and its control method are supplied by coal dust balanced weight
CN105240869A (en) Combustion system based on material flow and temperature automatic regulation and control method thereof
CN103807852B (en) The secondary-wind distributing device of pulverized-coal fired boiler and Secondary Air air distribution method
CN106556026B (en) Air delivery pipe coal dust weight measurement instrument and multiple pipeline equilibrium powder supply control systems
CN103363804B (en) Method and system for controlling flow of sintering ignition furnace
CN206803202U (en) Steam generator system
CN205898268U (en) Radiant type wind send pipeline buggy weight measurement appearance and a plurality of pipeline balanced powder control system that supplies
US6659026B1 (en) Control system for reducing NOx emissions from a multiple-intertube pulverized-coal burner using true delivery pipe fuel flow measurement
CN104728854B (en) Pulverized coal preparation system and method with air-blew pulverized coal heat measurement and control functions
CN209876975U (en) Load-variable air-coal matching control device for boiler of coal-fired power plant
CN105509035B (en) A kind of method, apparatus and automatic control system of determining opposed firing intake
CN204042968U (en) Pulverized-coal fired boiler digital combustion control and optimization system
CN214840781U (en) Primary air powder amount control system suitable for peak regulation
CN204084340U (en) The secondary-wind distributing device of pulverized-coal fired boiler
CN111561694B (en) Method and system for improving low-load SCR inlet smoke temperature of coal-fired boiler
CN111306571A (en) Reforming existing boiler combustion system by using in-furnace pulverized coal heat measurement system
CN103822225B (en) Integrated low nitrogen burning system and control method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20210521

Address after: 100037, Beijing, Xicheng District, 2 million meters in the middle of the building, 5 doors, room 402

Applicant after: Di Shengcai

Applicant after: Hebei bangruida Technology Co.,Ltd.

Address before: 100037, Beijing, Xicheng District, 2 million meters in the middle of the building, 5 doors, room 402

Applicant before: Di Shengcai

GR01 Patent grant
GR01 Patent grant