The specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the invention, the technical scheme in the embodiment of the invention is clearly and completely described, obviously, described embodiment only is the present invention's part embodiment, rather than whole embodiment.Based on the embodiment among the present invention, those of ordinary skills belong to the scope of protection of the invention not making the every other embodiment that is obtained under the creative work prerequisite.
Fig. 2 is the schematic diagram of the combustion control system of brown coal unit provided by the invention.Described system comprises: boiler 205, coal pulverizer 204, air preheater 206, dust removal machine 207, air-introduced machine 201, primary air fan 203, overfire air fan 202 and chimney 208; Wherein, coal pulverizer 204 is connected between 203 outlets of boiler 205 primary air fans, overfire air fan 202 outlets connect and boiler 205, in air preheater 206, realize the air preheat of flue, secondary air channel road, a wind pipeline enclosure, deduster 207 is connected between the flue and air-introduced machine 201 inlets of air preheater, and the outlet of air-introduced machine links to each other with chimney 208.
Described system also comprises: flue gas conditioning device 209;
Described flue gas conditioning device 209 is connected between described air-introduced machine 201 outlets and described primary air fan 203 inlets by flue, and the flue gas that air-introduced machine 201 is sent feeds back to described primary air fan 203 inlets;
Described primary air fan 203 mixes the flue gas of feedback with the air sent into of outside, and mist is sent into 205 pairs of brown coal of described boiler by described air preheater 206 and coal pulverizer 204 burns.
In the present embodiment, owing to have certain heat, obtain mist mixing by the air of sending in the outside from the flue gas of air-introduced machine feedback from the flue gas of air-introduced machine feedback.With respect to only using air as drier in the prior art, this example as drier, can utilize the heat of low-temperature flue gas that brown coal are carried out drying described mist, reduces the use amount of air.
In the present embodiment,, the fin of the flue gas in the boiler back end ductwork by inside will be entered air preheat before the boiler to uniform temperature, and help full combustion of fuel and improve the heat exchange performance of boiler, reduce energy consumption by air preheater 206.For energy-conservation, air preheat has great importance.
In the present embodiment, coal pulverizer 204 grinds described fuel and obtains coal dust, and it is in order to increase the surface area of fuel, to be used for more abundant burning that fuel is ground to form coal dust.
What overfire air fan 202 entered the mouth suction is air, is being for coal dust is burnt more fully to importing secondary wind again through the once air-dry dry coal dust later of mixing.
In the present embodiment, described flue gas conditioning device 209 is an adjustable plate, and this adjustable plate is regulated and entered ducted flue gas, that is to say, can regulate the shared ratio of flue gas in the described mist by this adjustable plate.Particularly, this adjustable plate can be for manually adjusting plate.This adjustable plate can also be regulated by PI (proportional integral) adjuster or PID (proportional integral feedforward) adjuster.For the those skilled in the art, under the prerequisite of the technology of technical field, common variation, change or replacement that this adjustable plate is carried out all should be included within protection scope of the present invention under grasping.
Beneficial effect of the present invention is, be connected between described air-introduced machine outlet and the described primary air fan inlet by flue by flue gas conditioning device, in a wind, mix a certain amount of flue gas, not only can reduce the use amount of a wind of boiler, and can be with NO
xBe controlled within the acceptability limit, owing to cancelled the steam air heater of a wind, reduced the resistance in an airduct road simultaneously, reduced the power consumption of primary air fan.
Embodiment two:
Fig. 3 is the schematic diagram of the combustion control system of brown coal unit provided by the invention.Described system comprises: boiler 305, coal pulverizer 304, air preheater 306, dust removal machine 307, air-introduced machine 301, primary air fan 303, overfire air fan 302 and chimney 308; Wherein, coal pulverizer 304 is connected between 303 outlets of boiler 305 primary air fans, overfire air fan 302 outlets connect and boiler 305, in air preheater 306, realize the air preheat of flue, secondary air channel road, a wind pipeline enclosure, deduster 307 is connected between the flue and air-introduced machine 301 inlets of air preheater, and the outlet of air-introduced machine links to each other with chimney 308.
Described system also comprises: flue gas conditioning device 309;
Described flue gas conditioning device 309 is connected between described air-introduced machine 301 outlets and described primary air fan 303 inlets by flue, and the flue gas that air-introduced machine 301 is sent feeds back to described primary air fan 303 inlets;
Described primary air fan 303 mixes the flue gas of feedback with the air sent into of outside, and mist is sent into 305 pairs of brown coal of described boiler by described air preheater 306 and coal pulverizer 304 burns.
In the present embodiment, owing to have certain heat, obtain mist mixing by the air of sending in the outside from the flue gas of air-introduced machine 301 feedbacks from the flue gas of air-introduced machine 301 feedbacks.With respect to only using air as drier in the prior art, this example as drier, can utilize the heat of low-temperature flue gas that brown coal are carried out drying described mist, reduces the use amount of air.
In the present embodiment,, the fin of the flue gas in the boiler back end ductwork by inside will be entered air preheat before the boiler to uniform temperature, and help full combustion of fuel and improve the heat exchange performance of boiler, reduce energy consumption by air preheater 306.For energy-conservation, air preheat has great importance.
In the present embodiment, coal pulverizer 304 grinds described fuel and obtains coal dust, and it is in order to increase the surface area of fuel, to be used for more abundant burning that fuel is ground to form coal dust.
What overfire air fan 302 entered the mouth suction is air, is being for coal dust is burnt more fully to importing secondary wind again through the once air-dry dry coal dust later of mixing.
In the present embodiment, described flue gas conditioning device 309 is an adjustable plate, and this adjustable plate is regulated and entered ducted flue gas, that is to say, can regulate the shared ratio of flue gas in the described mist by this adjustable plate.Particularly, this adjustable plate can be for manually adjusting plate.For the those skilled in the art, under the prerequisite of the technology of technical field, common variation, change or replacement that this adjustable plate is carried out all should be included within protection scope of the present invention under grasping.
Described system also comprises: oxygen sensor 310 is installed between described primary air fan 303 outlets and the air preheater 307, and is electrically connected with described flue gas conditioning device 309.Preferably, oxygen sensor 310 also can be connected to distribution control system (Distributed Control System, DCS) in, be used to control the total amount of the mixture of a wind air/flue gas, the ratio of air, flue gas is then regulated by the gas baffle that installs additional.
Preferably, as shown in Figure 4, described flue gas conditioning device 309 comprises: adjustable plate 3091 and adjustable plate controller 3092, described controller 3092 is electrically connected with described sensor 310, receives oxygen content signal that described oxygen sensor detects and according to described oxygen content signal described adjustable plate 3091 is controlled.Described adjustable plate controller 3092 can be adjuster or PID (proportional integral feedforward) adjuster.In actual applications, suppose when oxygen content is lower than a certain setting value, then open big baffle plate,, then close small front apron if instead the oxygen amount in the air quantity is higher than this value.For the those skilled in the art, under the prerequisite of the technology of technical field, common variation, change or replacement that flue gas conditioning device 309 is carried out all should be included within protection scope of the present invention under grasping.
Beneficial effect of the present invention is, be connected between described air-introduced machine outlet and the described primary air fan inlet by flue by flue gas conditioning device, in a wind, mix a certain amount of flue gas, not only can reduce the use amount of a wind of boiler, and can be with NO
xBe controlled within the acceptability limit, owing to cancelled the steam air heater of a wind, reduced the resistance in an airduct road simultaneously, reduced the power consumption of primary air fan.
Embodiment three:
Fig. 5 is the schematic diagram of the combustion control system of brown coal unit provided by the invention.Described system comprises: boiler 505, coal pulverizer 504, air preheater 506, dust removal machine 507, air-introduced machine 501, primary air fan 503, overfire air fan 502 and chimney 508; Wherein, coal pulverizer 504 is connected between 503 outlets of boiler 505 primary air fans, overfire air fan 502 outlets connect and boiler 505, in air preheater 506, realize the air preheat of flue, secondary air channel road, a wind pipeline enclosure, deduster 507 is connected between the flue and air-introduced machine 501 inlets of air preheater, and the outlet of air-introduced machine links to each other with chimney 508.
Described system also comprises: flue gas conditioning device 509;
Described flue gas conditioning device 509 is connected between described air-introduced machine 501 outlets and described primary air fan 503 inlets by flue, and the flue gas that air-introduced machine 501 is sent feeds back to described primary air fan 503 inlets;
Described primary air fan 503 mixes the flue gas of feedback with the air sent into of outside, and mist is sent into 505 pairs of brown coal of described boiler by described air preheater 506 and coal pulverizer 504 burns.
In the present embodiment, owing to have certain heat, obtain mist mixing by the air of sending in the outside from the flue gas of air-introduced machine 501 feedbacks from the flue gas of air-introduced machine 501 feedbacks.With respect to only using air as drier in the prior art, this example as drier, can utilize the heat of low-temperature flue gas that brown coal are carried out drying described mist, reduces the use amount of air.
In the present embodiment,, the fin of the flue gas in the boiler back end ductwork by inside will be entered air preheat before the boiler to uniform temperature, and help full combustion of fuel and improve the heat exchange performance of boiler, reduce energy consumption by air preheater 506.For energy-conservation, air preheat has great importance.
In the present embodiment, coal pulverizer 504 grinds described fuel and obtains coal dust, and it is in order to increase the surface area of fuel, to be used for more abundant burning that fuel is ground to form coal dust.
What overfire air fan 502 entered the mouth suction is air, is being for coal dust is burnt more fully to importing secondary wind again through the once air-dry dry coal dust later of mixing.
In the present embodiment, described flue gas conditioning device 509 is an adjustable plate, and this adjustable plate is regulated and entered ducted flue gas, that is to say, can regulate the shared ratio of flue gas in the described mist by this adjustable plate.Particularly, this adjustable plate can be for manually adjusting plate.For the those skilled in the art, under the prerequisite of the technology of technical field, common variation, change or replacement that this adjustable plate is carried out all should be included within protection scope of the present invention under grasping.
Described system also comprises: oxygen sensor 510 is installed between described primary air fan 503 outlets and the air preheater 507, and is electrically connected with described flue gas conditioning device 509.Preferably, oxygen sensor 510 also can be connected to distribution control system (Distributed Control System, DCS) in, be used to control the total amount of the mixture of a wind air/flue gas, the ratio of air, flue gas is then regulated by the gas baffle that installs additional.
Preferably, as shown in Figure 4, described flue gas conditioning device 309 comprises: adjustable plate 3091 and adjustable plate controller 3092, described controller 3092 is electrically connected with described sensor 310, receives oxygen content signal that described oxygen sensor detects and according to described oxygen content signal described adjustable plate 3091 is controlled.Described adjustable plate controller 3092 can be adjuster or PID (proportional integral feedforward) adjuster.In actual applications, suppose when oxygen content is lower than a certain setting value, then open big baffle plate,, then close small front apron if instead the oxygen amount in the air quantity is higher than this value.For the those skilled in the art, under the prerequisite of the technology of technical field, common variation, change or replacement that flue gas conditioning device 309 is carried out all should be included within protection scope of the present invention under grasping.
Described system also comprises: conditioner 511;
Described conditioner 511 is connected in described primary air fan 503 inlets by flue, the outside is sent into the air capacity of described primary air fan 503 and is regulated.
Preferably, as shown in Figure 6, described conditioner 511 comprises: adjustable plate 5111 and adjustable plate controller 5112, described adjustable plate controller 5112 is electrically connected with described sensor 503, receives oxygen content signal that described oxygen sensor 503 detects and according to described oxygen content signal described adjustable plate 5111 is controlled.
Particularly, the requirement of a wind total amount is by brown coal moisture decision, is that 40% brown coal are example with total moisture, if adopt pure air drying, need 50% primary air ratio, promptly dry 1t coal approximately needs 3~4t air, and the coal pulverizer outlet temperature can only arrive about 60 ℃.Adopt air/smoke mixture drying, because flue gas specific heat is big, it is smaller to reach the total amount that uniform temp needs, but because the amount of oxygen in the flue gas reduces, coal pulverizer requirement of explosion proof, outlet temperature can be brought up to 70~80 ℃.
Below to control primary air ratio specifically introduce:
1) total exhaust gas volumn/air capacity total amount and the primary air fan outlet oxygen amount according to the primary air fan outlet obtains a wind air capacity:
In the formula:
M
PrABe the air capacity in primary air fan outlet cigarette/empty mixture;
M
A﹠amp; GBe primary air fan outlet cigarette/empty amount of the mixture;
O
2, prABe the oxygen volume ratio in primary air fan outlet cigarette/empty mixture.
2) condition of based on fuel is determined the flow of the mixture of primary air and flue gas:
In the formula:
Max is big for getting;
M
CoalBe the quality of fuel flow, get the coal-supplying amount output of feeder;
K is a coal-air ratio control parameter, i.e. the ratio of the mass flow of a wind air/smoke mixture and coal-supplying amount, it is directly proportional with fuel quantity, roughly the coal pulverizer outlet temperature is controlled at 60~80 ℃ want within the scope;
M
MinMinimum air quantity for coal pulverizer can bear is determined by coal pulverizer itself.
3) adjusting of baffle plate is used to control the ratio between wind problem and the exhaust gas volumn, suppose that it was 12% (ratio of flue gas and air is about 1: 1 in the wind total amount of this moment), if air quantity oxygen amount is lower than this value, then open big baffle plate, if instead the oxygen amount in the air quantity is higher than this value, then close small front apron.An available PI or PID adjuster are regulated.
4) temperature that exports by coal pulverizer is accurately controlled the total amount of a wind and smoke mixture, calculate the total amount of a minimum wind and smoke mixture earlier by condition (2), carry out the initial value that PI regulates as fundamental line, if outlet temperature is low, the total amount of the total wind and smoke mixture of XXL, otherwise, then reduce the total amount of a wind and smoke mixture; If below minimum air quantity, the coal pulverizer outlet temperature is also high, then reduces and extracts exhaust gas volumn, no matter oxygen amount definite value.
Can fall the total amount of oxygen in wind get off by aforesaid operations, realized high moisture content brown coal fuel dry with burning, reduce NO
xTriple requirements.The wind temperature adjustment wind art designs at present commonly used of cancellation simultaneously makes an all wind all the time through the air preheater heat absorption, has guaranteed boiler efficiency.
Beneficial effect of the present invention is, be connected between described air-introduced machine outlet and the described primary air fan inlet by flue by flue gas conditioning device, in a wind, mix a certain amount of flue gas, not only can reduce the use amount of a wind of boiler, and can be with NO
xBe controlled within the acceptability limit, owing to cancelled the steam air heater of a wind, reduced the resistance in an airduct road simultaneously, reduced the power consumption of primary air fan.
Embodiment four:
The schematic diagram of the method for controlling combustion of Fig. 7 brown coal unit provided by the invention.Described method comprises:
S701: the flue gas that the air-introduced machine outlet is sent feeds back to the primary air fan inlet;
S702: described primary air fan mixes the flue gas of feedback with the air sent into of outside, and mist is sent into described boiler by air preheater and coal pulverizer brown coal are burnt.
In order to set forth the method that the embodiment of the invention provides in more detail.Herein, the combustion control system of the brown coal unit that please provides referring to Fig. 5.In the present embodiment, owing to have certain heat, obtain mist mixing by the air of sending in the outside from the flue gas of air-introduced machine 501 feedbacks from the flue gas of air-introduced machine 501 feedbacks.With respect to only using air as drier in the prior art, this example as drier, can utilize the heat of low-temperature flue gas that brown coal are carried out drying described mist, reduces the use amount of air.
In the present embodiment, described method also comprises: the oxygen content of the described mist that primary air fan is sent is checked, and according to described oxygen content the exhaust gas volumn that feeds back to the primary air fan inlet is regulated.
In the present embodiment, described method also comprises: the oxygen content of the described mist that primary air fan is sent is checked, and according to described oxygen content the air capacity that feeds back to the primary air fan inlet is regulated.
Described method also comprises: obtain the mist total amount of described primary air fan outlet, according to the ratio of described oxygen content and mist the exhaust gas volumn that feeds back to the primary air fan inlet is regulated.
Described method also comprises: obtain the air content in the mist of described primary air fan outlet, according to described air content the air capacity that feeds back to the primary air fan inlet is regulated.
Below to control primary air ratio specifically introduce:
1) total exhaust gas volumn/air capacity total amount and the primary air fan outlet oxygen amount according to the primary air fan outlet obtains a wind air capacity:
In the formula:
M
PrABe the air capacity in primary air fan outlet cigarette/empty mixture;
M
A﹠amp; GBe primary air fan outlet cigarette/empty amount of the mixture;
O
2, prABe the oxygen volume ratio in primary air fan outlet cigarette/empty mixture.
2) condition of based on fuel is determined the flow of the mixture of primary air and flue gas:
In the formula:
Max is big for getting;
M
CoalBe the quality of fuel flow, get the coal-supplying amount output of feeder;
K is a coal-air ratio control parameter, i.e. the ratio of the mass flow of a wind air/smoke mixture and coal-supplying amount, it is directly proportional with fuel quantity, roughly the coal pulverizer outlet temperature is controlled at 60~80 ℃ want within the scope;
M
MinMinimum air quantity for coal pulverizer can bear is determined by coal pulverizer itself.
3) adjusting of baffle plate is used to control the ratio between wind problem and the exhaust gas volumn, suppose that it was 12% (ratio of flue gas and air is about 1: 1 in the wind total amount of this moment), if air quantity oxygen amount is lower than this value, then open big baffle plate, if instead the oxygen amount in the air quantity is higher than this value, then close small front apron.An available PI or PID adjuster are regulated.
4) temperature that exports by coal pulverizer is accurately controlled the total amount of a wind and smoke mixture, calculate the total amount of a minimum wind and smoke mixture earlier by condition (2), carry out the initial value that PI regulates as fundamental line, if outlet temperature is low, the total amount of the total wind and smoke mixture of XXL, otherwise, then reduce the total amount of a wind and smoke mixture; If below minimum air quantity, the coal pulverizer outlet temperature is also high, then reduces and extracts exhaust gas volumn, no matter oxygen amount definite value.
Beneficial effect of the present invention is, be connected between described air-introduced machine outlet and the described primary air fan inlet by flue by flue gas conditioning device, in a wind, mix a certain amount of flue gas, not only can reduce the use amount of a wind of boiler, and can be with NO
xBe controlled within the acceptability limit, owing to cancelled the steam air heater of a wind, reduced the resistance in an airduct road simultaneously, reduced the power consumption of primary air fan.
It will be appreciated by those skilled in the art that accompanying drawing is the schematic diagram of a preferred embodiment, unit in the accompanying drawing or flow process might not be that enforcement the present invention is necessary.The invention described above embodiment sequence number is not represented the quality of embodiment just to description.
Above embodiment is the preferred embodiments of the disclosure, and the common variation that the those skilled in the art carries out in the technical scheme of the embodiment of the invention, change or replacement all should be included within protection scope of the present invention.