CN2400695Y - Incinerator of nitrogen oxide waste gas - Google Patents
Incinerator of nitrogen oxide waste gas Download PDFInfo
- Publication number
- CN2400695Y CN2400695Y CN 99257258 CN99257258U CN2400695Y CN 2400695 Y CN2400695 Y CN 2400695Y CN 99257258 CN99257258 CN 99257258 CN 99257258 U CN99257258 U CN 99257258U CN 2400695 Y CN2400695 Y CN 2400695Y
- Authority
- CN
- China
- Prior art keywords
- auxiliary air
- air inlet
- utility
- main burner
- air
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The utility model relates to an incinerator for processing nitrogen oxide exhaust gases, which can process the nitrogen dioxide exhaust gas. The utility model mainly comprises a furnace body, a main burner, an igniter, a primary air inlet and an auxiliary air inlet. The utility model is characterized in that the primary air inlet and an exhaust gas inlet are connected with each other and are installed on the main burner. The main burner is provided with a gas distribution plate. An air jacket is arranged out of the furnace body, and a three stage auxiliary air distributing hole is arranged on the furnace body. The utility model makes the burning sufficient. The auxiliary air is preheated by the air jacket and then enters a furnace hearth. On one hand, the utility model enables the unsafely burned fuel oil to burn sufficiently; on the other hand, the utility model can reduce the temperature of flue gas. The air jacket can also insulate the heat and can reduce the temperature of a furnace wall.
Description
The utility model relates to a kind of incinerator of handling nitrous oxides exhaust gas.
For treatment of waste gas, especially the waste gas of oxidizing atmosphere such as NOx if adopt absorption process, exist absorption not thorough, and the waste liquid after the absorption becomes another kind of liquid stain sources, if adopt the catalyst reduction method, operation easier is big.Existing incinerator all is to be used for the disposal of refuse solid waste, and incineration firing is fallen, and does not also have a kind of being applicable to burn the NOx waste gas combustion furnace at present.
The purpose of this utility model provides a kind of fuel oil incinerator of handling oxidizing atmosphere NOx waste gas.
The purpose of this utility model is achieved in that and comprises body of heater, main burner, igniter, the primary air inlet, exhaust gas entrance, the auxiliary air inlet, main burner, igniter is contained on the end socket of stove, it is characterized in that primary air inlet is communicated with exhaust gas entrance and is contained on the main burner, the front end of main burner is equipped with gas distribution grid, primary air mixes the feeding burner hearth with waste gas, there is air jacket the body of heater outside, the auxiliary air inlet is communicated with air jacket, be evenly equipped with auxiliary air distribution hole on the air jacket inner furnace body circumference and be provided with three grades, auxiliary air distribution hole and air jacket, burner hearth is communicated with.
Described gas distribution grid can be a Circular Plate, is opening 8-24 seam on it.
The quantity in aforesaid auxiliary air distribution hole is 4 of the first order, 8 of the second level, 12 of the third level.
The used fuel oil of aforesaid incinerator can be kerosene or diesel oil.
When using this stove, from the primary air inlet is the tolerance feeding primary air of 0.5-1.3 by coefficient of excess air, it is 1.05-5 that auxiliary air feeds the total coefficient of excess air in back, open igniter, the fuel oil that main burner feeds is lighted, survey temperature in the stove from thermometer hole, when temperature in the stove reaches 500 ℃, feed the nitrogen dioxide waste gas of 10-100% from exhaust gas entrance, adjust the primary air air inflow simultaneously, making the coefficient of excess of interior primary air of stove and nitrogen dioxide total oxidant is 0.5-0.96, auxiliary air feeds the back and guarantees that total coefficient of excess air is 1.05-5, to guarantee completing combustion, discharging tail gas reaches national specified discharge standard through thief hole 14 sample analysis.
The utility model has following advantage compared with prior art:
1. the utility model burns waste gas completely, because the effect of gas distribution grid makes after waste gas and the primary air warp, is in the rotation mode feeding burner hearth and fully burns with fuel oil.
2. owing on the body of heater air jacket is arranged, auxiliary air after auxiliary air inlet enters the chuck preheating again the hole of auxiliary air distribution vertically enter burner hearth, on the one hand the fuel oil of not burning is fully fully burnt, can reduce flue-gas temperature on the other hand, another of air jacket act as heat insulation, reduced furnace wall temperature.
The utility model embodiment accompanying drawings is as follows:
Fig. 1 is the utility model structural representation.
Fig. 2 is the A-A cutaway view of Fig. 1.
Fig. 3 is the structural representation of gas distribution grid.
Fig. 4 is the left view of Fig. 3.
Fig. 6 is the B-B cutaway view of Fig. 3.
As shown in the figure: the 1st, primary air inlet, the 2nd, exhaust gas entrance, the 3rd, main burner, the 4th, igniter, the 5th, main burner fuel nozzle, the 6th, gas distribution plate, the 7th, the auxiliary air inlet, the 8th, body of heater, the 9th, auxiliary air distribution hole, the 10th, air jacket, the 11st, thermometer hole, the 12nd, flame-observing hole, the 13rd, chimney, the 14th, thief hole.
8 is the tubular body of heater, igniter 4, main burner 3, be contained on the stove end socket, flame-observing hole 12 also is housed on the stove end socket, primary air inlet 1, exhaust gas entrance 2 are located on the main burner 3, and main burner 3 front ends are equipped with gas distribution grid 6, after primary air and waste gas mix, feed through being rotation mode behind the gas distribution grid 6, with the abundant mixed combustion of fuel oil that under certain oil pressure, is the shape that atomizes through the fuel nozzle ejection.Air jacket 10 is equipped with in body of heater 8 outsides, the auxiliary air inlet is located on the air jacket 10, body of heater 8 circumference are provided with auxiliary air distribution hole 9, and on body of heater 8, be provided with three grades of auxiliary air distribution holes, the first order is near burner, auxiliary air distribution hole 9 and air jacket 10, auxiliary air inlet 7, burner hearth are communicated with, after auxiliary air at first enters the interior preheating of annular air chuck of body of heater, enter in the burner hearth through auxiliary air distribution hole 9 again, imperfect combustion fuel oil is burnt away fully, and air jacket 10 another effects are heat insulation, reduce furnace wall temperature.Igniter 4 self-organizing systems have oil pump, fan, electronic striking and protection system, only need during igniting power connection is pressed start button, and igniter will start automatically, and burning is also lighted main burner 3.Thermometer hole 11 is used for monitoring delivery temperature, and combustion tail gas enters atmosphere by chimney 13 emptyings, and exhaust gas component is by thief hole 14 sample analysis.
Feed primary air from primary air inlet 1, the adjusting flow is 14m
3/ h, feeding auxiliary air by auxiliary air inlet 7 is 20m
3/ h, the firing point firearm starts main oil pump then, the main burner burning, oil inlet quantity is 2.8kg/h, smooth combustion 20 minutes, the preheating body of heater when temperature in the stove reaches 500 ℃, feeds NO by exhaust gas entrance 2 subsequently
2Waste gas, waste gas tolerance are 10m
3/ h contains NO in the waste gas
230%, (be that once oxidation agent coefficient is 0.96, the total oxidant coefficient is 1.6) discharging tail gas reaches national specified discharge standard through thief hole 14 sample analysis.
Claims (3)
1. incinerator of handling nitrous oxides exhaust gas, comprise body of heater (8), main burner (3), igniter (4), primary air inlet (1), exhaust gas entrance (2), auxiliary air inlet (7), main burner (3), igniter (4) is contained on the end socket of stove, it is characterized in that primary air inlet (1) is communicated with exhaust gas entrance (2) and is contained on the main burner (3), the front end of main burner (3) is equipped with gas distribution grid (6), primary air mixes the feeding burner hearth with waste gas, air jacket (10) is arranged on the body of heater (8), auxiliary air inlet (7) is communicated with air jacket (10), be evenly equipped with auxiliary air distribution hole (9) on air jacket (10) inner furnace body (8) circumference, and three grades of auxiliary air holes (9) are arranged, quadratic distribution hole (9) and auxiliary air inlet (7) on body of heater (8), air jacket (10) and burner hearth are communicated with.
2. a kind of incinerator of handling nitrous oxides exhaust gas as claimed in claim 1 is characterized in that described gas distribution grid (6) is the garden ring flat-plate, is opening 8-24 bar seam thereon equably.
3. a kind of incinerator of handling the waste gas nitrogen oxide as claimed in claim 1, the quantity that it is characterized in that described auxiliary air distribution hole (9) are 4 of the first order, 8 of the second level, 12 of the third level.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99257258 CN2400695Y (en) | 1999-12-13 | 1999-12-13 | Incinerator of nitrogen oxide waste gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99257258 CN2400695Y (en) | 1999-12-13 | 1999-12-13 | Incinerator of nitrogen oxide waste gas |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2400695Y true CN2400695Y (en) | 2000-10-11 |
Family
ID=34040183
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 99257258 Expired - Fee Related CN2400695Y (en) | 1999-12-13 | 1999-12-13 | Incinerator of nitrogen oxide waste gas |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2400695Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100501238C (en) * | 2004-11-19 | 2009-06-17 | 中国科学院山西煤炭化学研究所 | Method for treating dinitrogen tetroxide and/or dimazine spent liquor and incinerator |
CN107191949A (en) * | 2017-07-06 | 2017-09-22 | 郑仲新 | A kind of organic waste thermal cracking tail gas burner |
-
1999
- 1999-12-13 CN CN 99257258 patent/CN2400695Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100501238C (en) * | 2004-11-19 | 2009-06-17 | 中国科学院山西煤炭化学研究所 | Method for treating dinitrogen tetroxide and/or dimazine spent liquor and incinerator |
CN107191949A (en) * | 2017-07-06 | 2017-09-22 | 郑仲新 | A kind of organic waste thermal cracking tail gas burner |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2316655A1 (en) | Fuel dilution methods and apparatus for nox reduction | |
CN101532662A (en) | Method for reducing nitrogen oxides by coal dust boiler of internal combustion burner | |
CA2350262A1 (en) | Fuel dilution methods and apparatus for nox reduction | |
GB2048456A (en) | Reducing NOx emission from burners | |
CN109838795A (en) | A kind of incinerator and method for realizing high nitrogenous exhaust gas, waste liquid nitrogen oxides minimizing discharge | |
CN101169241B (en) | Combustion apparatus for solid fuel boiler | |
CN2400695Y (en) | Incinerator of nitrogen oxide waste gas | |
CN210568384U (en) | Low NO of inferior coal for combustion in coal-fired power plantXBurner with a burner head | |
CN2404005Y (en) | Incinerator for treating combustable waste gas | |
WO1992001194A1 (en) | Method for reducing emissions of oxides of nitrogen in combustion of various kinds of fuels | |
CN215766534U (en) | Tail gas waste heat recycling device of active carbon carbonization furnace | |
CN212746502U (en) | Novel exhaust gas treatment system | |
CN210165376U (en) | Low-nitrogen combustor and low-nitrogen combustion system | |
CN111649342B (en) | Low NOx combustor is burnt out to extremely low calorific value associated gas resource utilization and carbon black | |
CN107490296A (en) | A kind of method and device that hot wind ignition is carried out using high-temperature waste flue gas | |
CN2292978Y (en) | Incinerating device by thermal decomposition to burn out gas | |
EP0276086A2 (en) | Afterburners | |
CN111720839A (en) | Environment-friendly multi-stage combustion device applied to waste gas liquid incineration treatment | |
CN111981478A (en) | Low-nitrogen combustor, low-nitrogen combustion system and combustion method thereof | |
SU1733844A1 (en) | Boiler | |
CN2511874Y (en) | Heat storing burner for blast furnace gas | |
CN211876023U (en) | Low-nitrogen combustor and low-nitrogen combustion system | |
CN111765472B (en) | Using method of transition secondary combustion chamber for garbage incineration system | |
CN218119746U (en) | Special marsh gas blending combustion device for circulating fluidized bed boiler | |
CN217519863U (en) | Sludge coupling incineration system of coal-fired power plant |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |