CN100431670C - Energy-saving method for denitrogenation of horizontal chained coal fired boiler - Google Patents
Energy-saving method for denitrogenation of horizontal chained coal fired boiler Download PDFInfo
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- CN100431670C CN100431670C CNB2006100726697A CN200610072669A CN100431670C CN 100431670 C CN100431670 C CN 100431670C CN B2006100726697 A CNB2006100726697 A CN B2006100726697A CN 200610072669 A CN200610072669 A CN 200610072669A CN 100431670 C CN100431670 C CN 100431670C
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- boiler
- flue gas
- main furnace
- furnace chamber
- new wind
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Abstract
The present invention discloses a denitrification and energy-saving method for horizontal chain coal-fired boilers. The method comprises: 1. partial flue gas discharged in a flue gas exhaust pipeline of a boiler is led in a blower of the boiler, the oxygen content in the blower of the boiler is controlled by adjusting the proportion of the led flue gas and fresh air in the blower of the boiler, the combustion speed of coal is controlled, and thereby, the temperature of a main boiler chamber of the boiler is controlled; 2. fresh air is led in areas with temperature not below 700 DEG C at the crossed interface of the main boiler chamber of the boiler and a heat exchange chamber or in a flue gas passage in the heat exchange chamber, and combustible gas in the boiler atmosphere can be combusted sufficiently by oxygen in the fresh air. The discharge total amount of flue gas and the content of NO in flue gas are effectively lowered by the method of the present invention, residual heat in partial flue gas is utilized, and the environmental protection discharge of industrial boilers is realized.
Description
Technical field
The present invention relates to the coal-burning boiler field, particularly relate to the denitrogenation power-saving technology of horizontal chained coal fired boiler.
Background technology
Coal-burning boiler can contain NO in the product of burning in combustion process
xEtc. harmful substance, if will have NO
xBurnt gas directly be discharged in the air, can produce bigger harm to natural environment.At present, for NO
xControl technology be mainly the NO that removes in the flue gas
x, when adopting this traditional denitrogenation method, device structure complexity, equipment investment are big, in the process of denitrogenating, also need add other auxiliary substance in flue gas, and it is bigger to denitrogenate cost.For small scall coal-fired boiler, adopt traditional denitrogenation method then to be difficult to more realize.
Summary of the invention
At the deficiencies in the prior art, purpose of the present invention be exactly to provide a kind of invest little, boiler plant itself simply transformed the energy-saving method for denitrogenation that just can realize low emission and energy-conservation suitable horizontal chained coal fired boiler.
For achieving the above object, the energy-saving method for denitrogenation of a kind of horizontal chained coal fired boiler of the present invention is specially:
1) partial fume that is discharged in the boiler exhaust gas pipeline is introduced in the boiler blower, by adjust in the boiler blower the ratio of the flue gas of introducing and fresh air control oxygen content in the air blast, with coal-fired burning velocity in the control boiler, thereby realize to temperature controlling in the boiler main furnace chamber with to NO
xThe inhibition that generates;
2) in being not less than 700 ℃ zone, the temperature at the interface or in the exhaust gases passes in the Heat Room that boiler main furnace chamber and Heat Room intersect introduces new wind, the boiler atmosphere that new wind and main furnace chamber are discharged is mixed, and utilizes the oxygen in the new wind that the fuel gas in the described boiler atmosphere is fully burnt.
Further, the described mode that flue gas is introduced in the boiler blower is idle introducing, the flue gas outlet is arranged on delivery outlet one side of boiler exhaust gas pipeline air-introduced machine, and the malleation of being drawn in the flue gas utilization smoke discharging pipe enters in the bleed pipeline that links to each other with boiler blower automatically.
Further, the oxygen in the described new wind also makes the part NO in the described boiler atmosphere further react generation NO
2
Further, described fuel gas comprises CO and C
mH
n
Further, the mode of the new wind of described introducing is idle introducing, and the negative pressure that at the interface or in the Heat Room inner gas passage temperature of new wind by described main furnace chamber and described Heat Room is not less than in 700 ℃ the zone is sucked automatically.
Further, the new wind of described idle introducing is realized by hermetic sealing substrate is set, described hermetic sealing substrate is arranged on the gas channel of the main furnace chamber of described boiler and Heat Room intersection, hermetic sealing substrate links to each other with the inwall of Heat Room is airtight with the inwall of main furnace chamber, and hermetic sealing substrate is provided with the through hole of some perforation main furnace chambers and Heat Room; One bleed pipeline is used for from the external world gas in main furnace chamber and introduces new wind, and the air outlet of described bleed pipeline is arranged in the main furnace chamber, and the new wind of introducing passes through hole and enters in the Heat Room with after the boiler atmosphere in the main furnace chamber is mixed.
Further, the resh air requirement of introducing by the control valve control of regulating described bleed pipeline.
Further, by regulating the number of openings on the described hermetic sealing substrate or the area of section of through hole, the flow velocity of adjusting boiler atmosphere in the main furnace chamber to be changing the negative pressure degree in the Heat Room, thereby changes the resh air requirement of introducing.
After boiler blower is introduced the ducted flue gas of boiler exhaust gas, reduced the whole oxygen content that blasts in the boiler gas, control reaction speed coal-fired in the boiler, and then reduced boiler main furnace chamber temperature, thereby reduced NO
xGrowing amount; After new wind is introduced in ad-hoc location or zone in boiler, fuel gas in the boiler atmosphere is fully burned, neither causes boiler main furnace chamber temperature to raise, fuel is fully used, make the part NO in the boiler atmosphere continue reaction with the oxygen in the stylish wind, generate NO
2, NO
2Generation make NO in the flue gas again
xFurther absorbed at the flue gas desulfurization treatment fluid, therefore, adopted the inventive method, can be reduced the total emission volumn of boiler smoke and the NO in the flue gas effectively
xContent, and make waste heat in the partial fume obtain utilizing, realized the environment protection emission of Industrial Boiler.
Description of drawings
The vertical view of Fig. 1 horizontal chained coal fired boiler of unpowered bleed device for the present invention is equipped with;
Fig. 2 is the A-A view of Fig. 1.
The specific embodiment
Horizontal chained coal fired boiler is to utilize chain that coal cinder is sent in the burner hearth, below chain, utilize air blast to provide coal combustion required air from the export-oriented main furnace chamber of stove, join with main furnace chamber and to be Heat Room, be provided with flue and the water pipe on flue in the Heat Room, the high-temperature flue gas of main furnace chamber output, by flue with the water in the heat transferred water pipe.Main furnace chamber can dwindle suddenly gradually towards the area of section of outlet one side of Heat Room, and the outlet flare of main furnace chamber with the cross section that the smoke evacuation of dwindling main furnace chamber exports, is accelerated the flow velocity that high-temperature flue gas enters flue in the heating clamber thereby play.The boiler heating clamber is provided with exhaust opening, and the outlet and the exhaust opening of flue join, and the other end of exhaust opening is equipped with smoke discharging pipe, has air-introduced machine on the smoke discharging pipe, utilizes the air-introduced machine extraction of will discharging fume, and the temperature of the smoke evacuation of extraction is generally more than 100 degree.
When coal combustion, the NO in the combustion products
xGeneration and temperature extremely close relation is arranged, when the main furnace chamber temperature of boiler low more, NO in the combustion process
xGeneration few more.
For the temperature that reduces main furnace chamber to reduce NO
xGeneration, smoke evacuation is set between the blast orifice of the smoke discharging pipe of boiler and boiler introduces pipeline, flue gas and fresh air are mixed into the boiler air blast, carry in the direction main furnace chamber under the chain by air blast.The flue-gas temperature of introducing from smoke discharging pipe is more than 100 ℃, and sneaking into of flue gas can make the temperature of air blast improve about 40-50 ℃, improved the overall efficiency of boiler.The oxygen content of flue gas is about 11%, be lower than in the air 20.9% oxygen content, since blending in the air blast of flue gas oxygen content low, slowed down the burning velocity of coal cinder, thereby reduced the temperature of main furnace chamber, by the ratio between flue gas and the fresh air in the adjustment air blast, control the oxygen content in the air blast, control burning of coal speed, thus the main furnace chamber temperature reduced, thus reduced NO
xA large amount of generations.
Air-introduced machine delivery outlet one side of smoke exhaust pipe is a malleation to the smoke discharging pipe between the floss hole of smoke exhaust pipe, and the smoke evacuation outlet just is arranged in this zone, and smoke evacuation utilizes the malleation in the smoke discharging pipe to enter automatically in the bleed pipeline that links to each other with boiler blower.Because the introducing of flue gas has reduced the oxygen content in the boiler air blast, can bring the increase of coal-fired imperfect combustion heat loss, i.e. CO and C
mH
nConcentration Deng fuel gas increases, and the present invention utilizes pneumatic injection principle to install unpowered blower unit additional in the appropriate location of boiler, and new wind is introduced in the boiler, and unburnt CO and C further burn
mH
nDeng combustible, reduce NO to be implemented in
xIn the time of discharging, do not influence the efficiency of combustion of boiler.
Among Fig. 1-2, in an end of the main furnace chamber 1 of horizontal chained coal fired boiler and Heat Room 2 flare all, along on the airflow direction, the area of section of main furnace chamber 1 dwindles gradually, and the area of section of Heat Room 2 increases gradually.Be provided with hermetic sealing substrate 3 between main furnace chamber 1 and Heat Room 2, airtight the linking together of inwall of the periphery of hermetic sealing substrate 3 and main furnace chamber 1 thoroughly separated main furnace chamber 1 and Heat Room 2.And on hermetic sealing substrate 3, have four through holes 6 that are communicated with main furnace chambers 1 and Heat Room 2, main furnace chamber 1 be separately installed with two bleed pipelines 4 that communicate with the external world up and down, the air outlet 5 of bleed pipeline 4 is near through hole 6 places.Fume pipe 7 is installed in the Heat Room 2, and water pipe 8 is coiled on the outer wall of fume pipe 7.
In the present invention, by main furnace chamber 1 is designed to two horn mouths that link to each other with the junction of Heat Room 2, this structure has been accelerated flue gas in the main furnace chamber 1 to the flowing velocity of Heat Room 2, has increased the negative pressure degree in the main furnace chamber 1.Under the effect of negative pressure, new wind is inhaled in the main furnace chamber 1 from the external world by bleed pipeline 4, new wind mixes with high-temperature flue gas, mixed gas is together by the through hole 6 on the hermetic sealing substrate 3, enter in the fume pipe 7 in the Heat Room 2, when flue gas with after newly wind mixes, the fuel gas in the flue gas fully burns, further improved the temperature of flue gas, and the water in the water pipe 8 is heated under the effect of high-temperature flue gas.
For fuel gas is fully burnt, need to regulate the proportionate relationship between new wind and the fuel gas, and the soakage of new wind is relevant with the flow velocity of the area of section of hermetic sealing substrate 3 and flue gas, therefore, adjust hermetic sealing substrate 3 areas of section or the quantity of through hole 6 or the area of section of through hole 6, realize reaching rational proportion between the soakage of new wind and the fuel gas.
In addition, new wind intake can also be arranged on the interior flue of Heat Room, but the temperature of the flue gas at new wind intake place can not be lower than 700 ℃, because in the flue is negative pressure state too, negative pressure in the flue sucks the new wind in the external world in the flue automatically, has increased the oxygen content in the flue gas.After new wind is introduced, increased the oxygen content in the flue gas, unburnt combustible CO and C in the flue gas
mH
nFurther burning, CO and C in reducing smoke evacuation
mH
nConcentration does not influence the combustion thermal efficiency of boiler simultaneously.New wind introducing amount can realize automatic adjusting, guarantees the variation of boiler load.
The flue gas of conventional boiler in being discharged into atmosphere before, all can utilize alkali lye that flue gas is carried out desulfurization and handle, because alkali lye is to NO and NO
2Mist produce absorption near 1: 1, and do not absorb simple NO, therefore, conventional exhaust gas desulfurization processing method can't be removed the NO in the flue gas.Utilize the present invention that flue gas is introduced body of heater again, the NO in the flue gas
xWhen passing through in the boiler high-temperature region once more, have a certain proportion of decomposition, and as NO and NO
2The alkali lye of mist by sulfur removal technology the time, alkali lye is to NO and NO
2Mist produce absorption near 1: 1 because a part of NO has generated NO in burner hearth
2, alkali lye is again to NO and NO
2Mist have absorption near 1: 1, its chemical equation is as follows:
2NO
2+2MOH→MNO
3+MNO
2+H
2O
NO+NO
2+2MOH→2MNO
2+H
2O
2NO
2+Na
2CO
3→NaNO
3+NaNO
2+CO
2
NO+NO
2+Na
2CO
3→2NaNO
3+CO
2
Therefore, adopt this method effectively to play dual removal effect to NO.
Adopt this method, recycling by to flue gas reaches more than 45% the recycling amount of discharged flue gas, utilized the waste heat of discharging flue gas; Because the bulk temperature of burner hearth reduces, reduce NO
xDischarging, and, reduced the exhaust gas discharging total amount in the efficiency of combustion that does not influence boiler, realized denitrogenating purpose of energy saving.Simultaneously, because the maximum temperature of main furnace chamber reduces, external heat radiation reduces, and to reducing boiler heat loss, improves the overall efficiency of boiler.
Claims (8)
1, a kind of energy-saving method for denitrogenation of horizontal chained coal fired boiler is specially:
1) partial fume that is discharged in the boiler exhaust gas pipeline is introduced in the boiler blower, by adjust in the boiler blower the ratio of the flue gas of introducing and fresh air control oxygen content in the air blast, with coal-fired burning velocity in the control boiler, thereby realize to temperature controlling in the boiler main furnace chamber with to NO
xThe inhibition that generates;
2) in being not less than 700 ℃ zone, the temperature at the interface or in the exhaust gases passes in the Heat Room that boiler main furnace chamber and Heat Room intersect introduces new wind, the boiler atmosphere that new wind and main furnace chamber are discharged is mixed, and utilizes the oxygen in the new wind that the fuel gas in the described boiler atmosphere is fully burnt.
2, energy-saving method for denitrogenation according to claim 1, it is characterized in that, the described mode that flue gas is introduced in the boiler blower is idle introducing, the flue gas outlet is arranged on delivery outlet one side of boiler exhaust gas pipeline air exhauster, and the malleation of being drawn in the flue gas utilization smoke discharging pipe enters in the bleed pipeline that links to each other with boiler blower automatically.
3, energy-saving method for denitrogenation according to claim 1 is characterized in that, the oxygen in the described new wind also makes the part NO in the described boiler atmosphere further react and generates NO
2
4, energy-saving method for denitrogenation according to claim 1 is characterized in that, described fuel gas comprises CO and C
mH
n
5, energy-saving method for denitrogenation according to claim 1, it is characterized in that, the mode of the new wind of described introducing is idle introducing, and the negative pressure that at the interface or in the Heat Room inner gas passage temperature of new wind by described main furnace chamber and described Heat Room is not less than in 700 ℃ the zone is sucked automatically.
6, energy-saving method for denitrogenation according to claim 5, it is characterized in that, the new wind of described idle introducing is realized by hermetic sealing substrate is set, described hermetic sealing substrate is arranged on the gas channel of the main furnace chamber of described boiler and Heat Room intersection, hermetic sealing substrate reaches with the inwall of main furnace chamber and links to each other with the inwall of Heat Room is airtight, and hermetic sealing substrate is provided with the through hole of some perforation main furnace chambers and Heat Room; One bleed pipeline is used for from the external world gas in main furnace chamber and introduces new wind, and the air outlet of described bleed pipeline is arranged in the main furnace chamber, and the new wind of introducing passes through hole and enters in the Heat Room with after the boiler atmosphere in the main furnace chamber is mixed.
7, energy-saving method for denitrogenation according to claim 6 is characterized in that, controls the resh air requirement of introducing by the control valve of regulating described bleed pipeline.
8, energy-saving method for denitrogenation according to claim 7, it is characterized in that, by regulating the number of openings on the described hermetic sealing substrate or the area of section of through hole, the flow velocity of adjusting boiler atmosphere in the main furnace chamber to be changing the negative pressure degree in the Heat Room, thereby changes the resh air requirement of introducing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100726697A CN100431670C (en) | 2006-04-07 | 2006-04-07 | Energy-saving method for denitrogenation of horizontal chained coal fired boiler |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100726697A CN100431670C (en) | 2006-04-07 | 2006-04-07 | Energy-saving method for denitrogenation of horizontal chained coal fired boiler |
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| Publication Number | Publication Date |
|---|---|
| CN1843573A CN1843573A (en) | 2006-10-11 |
| CN100431670C true CN100431670C (en) | 2008-11-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
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| CN106861397A (en) * | 2017-03-03 | 2017-06-20 | 黄永乐 | A kind of boiler exhaust gas treatment facilities and the boiler using the structure |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1054199A (en) * | 1990-01-27 | 1991-09-04 | Gea空冷设备公司 | The denitrogenation of hot waste gas and the method and apparatus of desulfurization |
| US5135387A (en) * | 1989-10-19 | 1992-08-04 | It-Mcgill Environmental Systems, Inc. | Nitrogen oxide control using internally recirculated flue gas |
| US5429811A (en) * | 1992-02-07 | 1995-07-04 | Societe Francaise Hoechst | Process for the thermochemical decomposition of dinitrogen oxide |
| US5576970A (en) * | 1992-12-25 | 1996-11-19 | Kabushiki Kaisha Toshiba | Nitrogen oxide removal control method |
| CN2257008Y (en) * | 1996-04-08 | 1997-06-25 | 北京通用能源动力公司 | Circulation fluidized bed boiler transformed by chain boiler |
-
2006
- 2006-04-07 CN CNB2006100726697A patent/CN100431670C/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5135387A (en) * | 1989-10-19 | 1992-08-04 | It-Mcgill Environmental Systems, Inc. | Nitrogen oxide control using internally recirculated flue gas |
| CN1054199A (en) * | 1990-01-27 | 1991-09-04 | Gea空冷设备公司 | The denitrogenation of hot waste gas and the method and apparatus of desulfurization |
| US5429811A (en) * | 1992-02-07 | 1995-07-04 | Societe Francaise Hoechst | Process for the thermochemical decomposition of dinitrogen oxide |
| US5576970A (en) * | 1992-12-25 | 1996-11-19 | Kabushiki Kaisha Toshiba | Nitrogen oxide removal control method |
| CN2257008Y (en) * | 1996-04-08 | 1997-06-25 | 北京通用能源动力公司 | Circulation fluidized bed boiler transformed by chain boiler |
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| CN1843573A (en) | 2006-10-11 |
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