A kind of apparatus and method for changing flow of flue gas control SCR inlet smoke temperature
Technical field
The present invention relates to a kind of apparatus and method for changing flow of flue gas control SCR inlet smoke temperature, belong to coal-burning boiler and subtract
Drainage technique field.
Background technology
With increasingly sharpening for environmental degradation, China has put into effect substantial amounts of energy-saving and emission-reduction measure, and power plant, which stands in the breach, to be become
The important object administered.During " 12th Five-Year Plan ", requirement thermal power generation unit equipment denitrating system in China's controls the discharge of NOx,
Most domestic power plant uses selective catalytic reduction (SCR) flue gas denitrification system.In SCR denitration system operational process, denitration
Catalyst often causes catalytic efficiency low due to smoke temperature is not suitable for, and denitrating system operation is influenced, for this purpose, all multi-experts are to denitrating system
Preceding heat exchanger is transformed.
SCR optimal reaction temperature windows are concentrated mainly on 340~380 DEG C, when inlet flue gas temperature is below 360~380 DEG C,
SCR reaction efficiencies are improved with the raising of temperature.For this phenomenon, presently, there are in economizer feed water by-pass, economizer
Multinomial measure, the economizer such as flue duct bypass, high-temperature flue bypass and economizer hierarchical arrangement are given outside portion's flue duct bypass, economizer
Water bypass reduces the main flow of economizer, so as to reduce economizer caloric receptivity, achievees the purpose that improve SCR inlet smoke temperature;Save coal
Flue duct bypass, high-temperature flue bypass are by controlling economizer exit flue gas and side outside the bypass of device Internal Flue, economizer
The mixed proportion of road flue gas come achieve the purpose that control SCR inlet smoke temperature;Economizer hierarchical arrangement be by reduce flue gas with to
Heat exchange amount between water achievees the purpose that improve SCR inlet smoke temperature.
It also proposed a kind of method for controlling SCR inlet smoke temperature herein, this method is by changing flue gas flow direction, controlling cigarette
The coefficient of heat transfer and heat exchange area between gas and feedwater, so as to control SCR inlet flue-gas temperature.
The content of the invention
It is an object of the invention to control SCR denitration system inlet flue gas temperature, ensure denitrating system normal operation, with economizer
A kind of the problem of to transform object, due to smoke temperature is too low denitrating system being caused to be stopped transport for current coal-burning power plant, it is proposed that change
Flow of flue gas controls the apparatus and method of SCR inlet smoke temperature, to meet existing thermal power plant's pollutant emission standard, reaches environmental protection
It is required that.
The purpose of the present invention is realized by following technical measures:
A kind of apparatus and method for changing flow of flue gas control SCR inlet smoke temperature, it is characterised in that:The device is rolled up by steel
Curtain, regulating rod, motor and switchgear composition.
The control device, along flow of flue gas direction, in economizer both sides arranged for interval, gap size is five layers of pipe
Row.
The steel roller shutter is made of several pieces of steel discs, and steel disc is in flat, and the side of steel disc is welded with annulus, adjacent
The annulus docking of two steel discs is connected by steel pin through annulus, and interface can rotate, and the steel disc after connection is roller shutter,
Roller shutter one end is free end, and the other end is fixed on regulating rod, and with the rotation of regulating rod, roller shutter be free to roll and stretch
Exhibition is connected preferable after roller shutter stretching, extension between steel disc, and seamless, flue gas cannot pass through.
Described regulating rod one end is placed on rotating base, other end welded gear, the gear and another gear phase
Mutually occlusion, gear can rotate under the action of motor, drive regulating rod rotation, so as to control rolling and stretching for steel roller shutter
Exhibition.
The motor is connected with gear, and band moving gear rotates during motor rotation.
The switchgear is connected with motor, can control rotation direction, rotation time and the velocity of rotation of motor,
So as to control the area of steel rolling screen shielding economizer tube wall, the heat exchange amount between flue gas and steam is reduced, controls economizer exit
Flue-gas temperature ensures SCR denitration system normal operation.
The length of the steel roller shutter is the half of flue, prevents the long flue that blocks of roller shutter from causing flue gas normal
Circulation.
Close to hot wall, roller shutter direction of extension can be controlled by having on wall for other two side of the steel roller shutter
Groove, two sides of roller shutter are placed in groove, under the driving of regulating rod, steel roller shutter along groove track forward
Movement.
The motor can under the control of power supply positive and negative rotation, when motor rotates clockwise, control steel
Roller shutter is rolled, and reduces the heat exchange area blocked, and when motor rotated counterclockwise, control steel roller shutter extends, and increase hides
The heat exchange area of gear.
Workflow of the present invention is:When boiler at low load is run, SCR denitration system inlet flue gas temperature reduces, when less than catalysis
During 320 DEG C of agent preference temperature, switchgear power supply is opened, makes motor rotated counterclockwise, band moving gear rotates, and controls to adjust stick edge
It rotates clockwise, under the action of regulating rod, control steel roller shutter extends, and blocks a part of heat exchange area, flue gas is with saving
The heat exchange amount of feedwater is reduced in coal device, the rise of economizer exit smoke temperature, and the rise of denitrating system import smoke temperature ensures that catalyst exists
Normal operation within the temperature range of 320 DEG C to 420 DEG C.Declined according to smoke temperature it is different degrees of, along flow of flue gas direction, successively
The steel roller shutter of economizer both sides is opened, controls the heat exchange area between flue gas and feedwater, so as to control between flue gas and feedwater
Heat exchange amount continuously adjusts denitrating system inlet flue gas temperature, ensures SCR denitration system normal operation.
Description of the drawings
The present invention is described in further detail with specific example below in conjunction with the accompanying drawings:
Fig. 1 is the present invention in coal-burning power plant's back-end ductwork usage state diagram;
Fig. 2 continuously adjusts schematic diagram when being run for boiler at low load, the heat exchange area between flue gas and feedwater is reduced;
Fig. 3 continuously adjusts schematic diagram when being run for boiler at low load, compared with Fig. 2, the heat exchange area between flue gas and feedwater
It is further reduced;
Fig. 4 continuously adjusts schematic diagram when being run for boiler at low load, compared with Fig. 3, the heat exchange area between flue gas and feedwater
It is further reduced;
Fig. 5 is a whole set of control device;
Fig. 6 is steel roller shutter.
Reference sign,
1- economizer exit headers, 2- economizer import headers, 3- economizers, 4-SCR denitrating systems, 5,7- economizers it is left
Side steel roller shutter, steel roller shutter on the right side of 6- economizers, 8- motor, 9,11- gears, 10- universal driving shafts, 12- regulating rods, 13- bottoms
Seat, 14- roller shutter head ends, 15- roller shutters end, 16,17- roller shutters side, A- not by sweep of gases area, B- not by sweep of gases area,
C- is not by sweep of gases area.
Specific embodiment
The present invention is further illustrated with reference to the accompanying drawings and detailed description, but the present invention be not limited to it is following
Embodiment.Boiler can be all models formula, it is illustrated that by taking Π type boilers as an example, but the actual not merely limitation diagram type of furnace.
This paper presents a kind of apparatus and method for changing flow of flue gas control SCR inlet smoke temperature, arrange after-burning of the present invention
Coal-fired plant's back-end ductwork equipment state is as shown in Figure 1, control device is made of steel roller shutter, regulating rod, motor and switchgear.
The system has several set control devices, and along flow of flue gas direction, in economizer both sides arranged for interval, gap size is five layers of pipe
Row.
Steel roller shutter in the present embodiment is made of several pieces of steel discs, and steel disc is in flat, and the side of steel disc is welded with circle
Ring, the annulus docking of two neighboring steel disc are connected by steel pin through annulus, and interface can rotate, and the steel disc after connection is
For roller shutter, roller shutter one end is free end, and the other end is fixed on regulating rod, and with the rotation of regulating rod, roller shutter be free to
It rolls and stretches, be connected preferable between steel disc after roller shutter stretching, extension, seamless, flue gas cannot pass through.
Regulating rod one end in the present embodiment is placed on rotating base, other end welded gear, the gear and another
Gear is mutually twisted, and gear can rotate under the action of motor, regulating rod rotation is driven, so as to control the volume of steel roller shutter
It rises and stretches.
Motor in the present embodiment is connected with gear, and band moving gear rotates during motor rotation.
Switchgear in the present embodiment is connected with motor, can control the rotation direction of motor, rotation time and turn
Dynamic speed so as to control the area of steel rolling screen shielding economizer tube wall, reduces the heat exchange amount between flue gas and steam, and control saves coal
Device exit gas temperature ensures SCR denitration system normal operation.
The length of steel roller shutter in the present embodiment is the half of flue, prevents the long flue that blocks of roller shutter from causing flue gas not
It can normally circulate.Close to hot wall, roller shutter direction of extension can be controlled by having on wall for other two side of steel roller shutter
Groove, two sides of roller shutter are placed in groove, under the driving of regulating rod, steel roller shutter along groove track forward
Movement.
Motor in the present embodiment can under the control of power supply positive and negative rotation, when motor rotates clockwise, control
Steel roller shutter processed is rolled, and reduces the heat exchange area blocked, and when motor rotated counterclockwise, control steel roller shutter extends,
Increase the heat exchange area blocked.
Workflow of the present invention is:When boiler at low load is run, SCR denitration system inlet flue gas temperature reduces, when less than catalysis
During 320 DEG C of agent preference temperature, switchgear power supply is opened, makes motor rotated counterclockwise, band moving gear rotates, and controls to adjust stick edge
It rotates clockwise, under the action of regulating rod, control steel roller shutter extends, and blocks a part of heat exchange area, flue gas is with saving
The heat exchange amount of feedwater is reduced in coal device, the rise of economizer exit smoke temperature, and the rise of denitrating system import smoke temperature ensures that catalyst exists
Normal operation within the temperature range of 320 DEG C to 420 DEG C.Declined according to smoke temperature it is different degrees of, along flow of flue gas direction, successively
The steel roller shutter of economizer both sides is opened, controls the heat exchange area between flue gas and feedwater, so as to control between flue gas and feedwater
Heat exchange amount continuously adjusts denitrating system inlet flue gas temperature, ensures SCR denitration system normal operation.
The present invention do not limit to above-mentioned specific embodiment, according to the above, according to the ordinary technical knowledge of this field
And customary means, under the premise of the above-mentioned basic fundamental thought of the present invention is not departed from, the present invention can also make other diversified forms
Equivalent modifications, replacement or change, all fall among protection scope of the present invention.