CN201819211U - Gas burner with multi-point burning, long flame and ultra-low nitrogen oxide emission - Google Patents
Gas burner with multi-point burning, long flame and ultra-low nitrogen oxide emission Download PDFInfo
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- CN201819211U CN201819211U CN 201020547515 CN201020547515U CN201819211U CN 201819211 U CN201819211 U CN 201819211U CN 201020547515 CN201020547515 CN 201020547515 CN 201020547515 U CN201020547515 U CN 201020547515U CN 201819211 U CN201819211 U CN 201819211U
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Abstract
The utility model provides a gas burner with multi-point burning, long flame and ultra-low nitrogen oxide emission, which mainly comprises a muffling hoop (1), an air duct (2), an air regulating baffle plate (3), an air box (4), a primary burner (5), a secondary burner (6), a burner block (7) and an incandescent light (8). The gas burner is characterized in that the primary burner (7) is disposed in an air channel (9) of the burner block (7) and is a premixing type burner, NOx emission is further reduced by adopting fume recycle technology, and the secondary burner (6) as a diffusion type burner is further adopted and consists of a secondary fuel air inlet pipe (17) and a secondary fuel nozzle (18). The gas burner adopts grading fuel burning technology, the fume recycle technology and multi-point scattering burning technology so as to reduce fuel burning temperature, is favorable for uniform distribution of a heat field inside a cracking furnace, realizes large-capacity burning and ultra-low NOx emission, and is particularly suitable for use as a bottom burner inside the cracking furnace.
Description
Technical field
The utility model relates to a kind of gas burner of the ultralow discharged nitrous oxides of long flame of multiple spot burning, and particularly a kind of is the big ability of fuel, flat long flame, ultralow NOx gas burner with fuel gas, is specially adapted on the ethane cracking furnace.
Background technology
Fuel gas with burn after air mixes, the hydrocarbon in airborne oxygen and the fuel gas carries out combustion reaction and emits a large amount of heat.But when burning under the condition of high temperature, oxygen excess, airborne nitrogen will react with airborne oxygen and generate NOx.As everyone knows, under the identical situation of other condition, the growing amount of NOx increases along with the rising of ignition temperature.NOx is the material that environment is had harm, it has been generally acknowledged that the discharging of NOx is relevant with minimizing and other environmental problems of ozone.
The influence of environment is obtained day by day before people are concerned about in NOx discharging, common all types of flame heating furnace all adopts single stage burner, low-NOx combustor with present use is compared, this simple single stage burner can produce the NOx discharging of high level, can't satisfy the requirement of current environmental protection standard and regulations.In order to reduce the NOx discharging, just need design low-NOx combustor.
The low-NOx combustor that uses mainly contains two kinds at present.A kind of is the classification air burner.The classification air burner makes combustion air shunting setting up first combustion zone of oxygen deprivation, thereby reduces the formation of NOx, in second combustion zone air of remainder is introduced, thereby is finished whole combustion process.The low-NOx combustor of another kind of type is the classification fuel burner, combustion air is once all introduced first combustion zone, but have only part of fuel burned in first combustion zone, remaining fuel is incorporated into second combustion zone respectively, even the 3rd combustion zone, utilize the oxygen of the first or second combustion zone surplus to burn.In this burner, the air of the first and second combustion zone surpluses has diluted fuel, and ignition temperature is lower, thereby has reduced the formation of NOx.
The another kind of method that reduces ignition temperature is to add diluent, one of method that flue gas recirculation (FGR) technology comes to this.Flue gas recirculation (FGR) is exactly to make the part of smoke circulation of finishing combustion process return bellows, after fresh fuel is mixed, gets back to the combustion zone once more with fuel.Amount of circulating gas accounts for 10%～20% of combustion-supporting air quantity usually, and the level that flue gas recirculation reduces NOx will surpass the level that fractional combustion can reach usually.For gas burner, flue gas recirculation (FGR) is the most effective and the better simply NOx of structure reduces system, another advantage of flue gas recirculation (FGR) is that it can use together with other most NOx control method, to obtain ultralow NOx discharging.
Ethane cracking furnace base burning device, except environmental requirement, also to the flame profile of base burning device, the length of flame, flame rigidity, heat capacity, adjusting than and along all multifactor very harsh requirements that have such as heat flow density distribution of pyrolysis furnace short transverse, if it is improper to design, may bring adverse effect to the performance and the operation of pyrolysis furnace.For ethane cracking furnace, the problem of combustion system-as the rigidity of flame profile, the length of flame, flame and heat flow density distribute unreasonable, fatal often, it can cause serious problems such as the serious flexural deformation of boiler tube, stove shortening service cycle, the boiler tube lost of life.
CN200720032397.8 provides the gas burner of a kind of ethane cracking furnace with long flame low-nitrogen oxide discharging, adopted the fuel staging technology to reduce the NOx discharging, its NOx discharge capacity is lower than 35 ppmvd, the burner ability is big, heat flux distribution reasonable, stable operation, adjusting can reach 8:1 than the ratio of minimum load (the burner peak load with), the operator can optimize and stable heat flux characteristics under carry out the operation of pyrolysis furnace.But this base burning device is not owing to adopt the multiple spot combustion technology, and is higher over against the regional temperature of base burning device so, is the high-temperature region, and temperature is lower between two base burning devices, is low-temperature space, causes in the stove temperature distributing disproportionation even.In addition, owing to do not adopt flue gas recirculation (FGR) technology, the NOx discharge capacity is still higher, and the space of further reduction is arranged.Certainly, at ethane cracking furnace with the base burning device, except environmental requirement, the problem of combustion system-as the rigidity of flame profile, the length of flame, flame and heat flow density distribute unreasonable, fatal often, it can cause serious problems such as the serious flexural deformation of boiler tube, stove shortening service cycle, the boiler tube lost of life.
Summary of the invention
The purpose of this utility model is to provide a kind of gas burner of the ultralow discharged nitrous oxides of long flame of multiple spot burning, it not only can obtain ultralow NOx discharging, and can obtain good base burning device flame profile, the length of flame, flame rigidity and heat flow density distribution, this gas burner can realize that multiple spot disperses burning, can be according to the specific requirement of heat supply in the stove, the decanting point of reasonable Arrangement fuel, help the even distribution of thermal field in the stove, therefore be specially adapted on the ethane cracking furnace.
The purpose of this utility model is achieved in that
The utility model provides a kind of gas burner of the ultralow discharged nitrous oxides of long flame of multiple spot burning, mainly by silencer cover 1, air channel 2, transfer windshield plate 3, bellows 4, one-level burner 5, two stage burner 6, burner block 7, altar lamp 8 is formed, it is characterized in that burner block 7 places the stove bottom, the boring place is an air flow channel 9, at its entrance 10 are the straight runners that cross-sectional area is constant, the cross-sectional area of outlet section 11 diminishes gradually and forms the air contracted channel, be beneficial to form flat flame, the level angle that outlet section 11 air contracted channels inwardly shrink gradually is β; Be provided with one-level burner 5 in the air flow channel 9 of burner block 7, one-level burner 5 is a pre-mixing type combustion apapratus, adopts flue gas recirculating technique, further reduces the NOx discharging.One-level burner 5 is made up of one-level fuel nozzle 12, injector 13, nozzles 14, cycle flue 15, has fire hole 16 on the nozzles 14, disperses burning to realize multiple spot; Also be provided with duct 22 between the inner and outer wall of burner block 7 with one-level burner axially parallel, be provided with two stage burner 6 in the duct 22, two stage burner 6 is a diffusion flame burner, form by secondary fuel air inlet pipe 17, secondary fuel nozzle 18, have secondary fuel spray orifice 19 on the secondary fuel nozzle 18, in 22 exits, duct of placing two stage burner 6 is a groove 24 greater than the cross section, duct, and groove 24 is built-in with secondary fuel nozzle 18; Also have flue 21 on the burner block 7, be communicated with the cycle flue 15 of one-level burner 5 and realize flue gas recirculation; Combustion air is by air channel 2 and transfer windshield plate 3 to enter bellows 4, enters entrance 10, the outlet section 11 of air flow channel then successively, enters in the burner hearth at last.
This gas burner is particularly suitable for using as the base burning device in pyrolysis furnace, can form flat long flame, realizes that multiple spot disperses burning, is beneficial to the even distribution of thermal field in the pyrolysis furnace, and realizes big ability burning and ultralow NOx discharging.
The utility model is the improvement of CN200720032397.8, it has continued to use the former fuel-staged combustion technology, but in order further to reduce the NOx discharging and to obtain Temperature Distribution in the uniform more pyrolysis furnace, the utility model has also adopted flue gas recirculating technique and multiple spot combustion technology.By adopting flue gas recirculating technique to make the part of smoke of finishing combustion reaction in the burner hearth return bellows, after fresh one-level fuel gas mixes, get back to the combustion zone together once more and burn.When burning gas, the level that flue gas recirculation reduces NOx will surpass the level that fractional combustion can reach usually; By adopting the multiple spot combustion technology to make fuel can disperse burning, eliminated over against the low-temperature space between the high-temperature region of base burning device and two the base burning devices, thereby obtained more uniformly Temperature Distribution in the pyrolysis furnace, the cycle of operation of having improved pyrolysis furnace.
The gas burner of the ultralow discharged nitrous oxides of long flame of a kind of multiple spot burning of the present utility model has adopted classification fuel combustion techniques, flue gas recirculating technique and multiple spot to disperse combustion technology.One-level fuel is via one-level fuel nozzle 12, spray into injector 13 from the one-level fuel jet orifice in the free jet mode, at low-pressure area of injector 13 inner formation, thereby the flue gas in the burner hearth is sucked injector 13 by flue 21 on the burner block 7 and cycle flue 15, after circulating flue gas and one-level fuel mix in injector 13, be preferably a plurality of strip fire holes via the fire hole 16(on the nozzles 14) spray into the air flow channel 9 of burner block 7, mix with combustion air and burn, form first combustion zone.Specific requirement according to heat flux distribution in the stove, have secondary fuel spray orifice 19 on the secondary fuel nozzle 18 of two stage burner 6, also can offer three grades of fuel jet orifices 20, the profile of secondary fuel nozzle 18 is preferably " spade " structure, be easy to the dispersed placement of secondary fuel spray orifice 19 and three grades of fuel jet orifices 20, be convenient to realize that multiple spot disperses burning.Secondary fuel enters secondary fuel air inlet pipe 17, via secondary fuel nozzle 18, spray into burner hearth from secondary fuel spray orifice 19 and three grades of fuel jet orifices 20, mix with residue combustion air and burn from first combustion zone, after first combustion zone, form second combustion zone and the 3rd combustion zone successively.Combustion air is by air channel 2 and transfer windshield plate 3 to enter bellows 4, enters the entrance 10 straight runners and outlet section 11 contracted channels of burner block then successively, enters burner hearth at last.
The air intake section 10 of the utility model gas burner burner block 7 is that a cross section is constant, and preferably cross section is rectangle or foursquare cuboid air flow channel, and the long limit of this runner is parallel to the stove side wall.Burner block air flow channel outlet section 11 is that a runner shrinks gradually, and length-width ratio becomes big air contracted channel gradually, so the air outlet slit of burner block 7 is square-sections bigger with respect to the air intake length-width ratio.In the air contracted channel, combustion air is by continuous speedup, so that adapt with flat long flame, the outlet section 11 of burner block air flow channel links to each other with burner hearth.
Burner block is installed in the stove bottom, and the internal face of close stove side wall 25, and combustion flame is owing to wall effect is pressed close to the furnace wall internal face, and the mobile and burning along the furnace wall internal face, therefore produces one than uniform heat flux distribution at the furnace wall internal face.Simultaneously, one-level burner 5 and two stage burner 6 have all adopted multiple spot to disperse combustion technology, can be optimized design to position, direction, quantity and the size of fire hole 16, secondary fuel spray orifice 19 and three grades of fuel jet orifices 20 according to concrete condition, thereby obtain that thermal field distributes in the more gratifying stove.
More specifically give an example, gas burner preferably has 2～4 one-level burners 5, and 2～4 one-level burners 5 can form a line, and its line of centres is parallel to stove side wall 25; When 4 one-level burners 5,4 one-level burners 5 also can be lined up two row, 2 of every row, and the line of centres of the one-level burner 5 of every row is parallel to stove side wall 25, when fire hole 16 was the fire hole composition of a plurality of strips, the long limit of strip fire hole also was parallel to stove side wall 25.Burner block 7 has the burner block flue 21 that is communicated with burner hearth and cycle flue 15 away from the one side 23 of side wall, and flue 21 is communicated with cycle flue 15, to realize inner flue gas of the stove recirculation.
The level angle β that outlet section 11 air contracted channels inwardly shrink gradually is preferably 45
o～80
oNon-burning brick or the burned brick of high alumina matter that burner block 7 preferably adopts the band stainless steel cloth to reinforce.
22 exits, duct that are being equipped with two stage burner 6, a groove is arranged, be provided with a secondary fuel nozzle 18 at groove, on secondary fuel nozzle 18, have secondary fuel spray orifice 19, specific requirement according to heat flux distribution, also can offer three grades of fuel jet orifices 20, leave the gap of 10～15mm between the duct 22 of secondary fuel nozzle 18 and burner block 7, be beneficial to the cooling of combustion air secondary fuel nozzle 18; Secondary fuel spray orifice 19 is preferably 60 with the angle of horizontal plane
o～80
oThree grades of fuel jet orifices 20 are preferably 70 with the angle of horizontal plane
o～90
o, generally speaking, the angle of three grades of fuel jet orifices 20 and horizontal plane is greater than or equals the angle of secondary fuel spray orifice (19) and horizontal plane.Two stage burner 6 preferably has 4～8.
Silencer cover 1 can be filled with the noise reduction cotton in the utility model gas burner, is connected with air channel 2 with adpting flange by stay bolt.
The air channel 2 in the utility model gas burner, and inside can be lined with the noise reduction cotton, adopt flanges to be connected with bellows 4 or weld; 2 inside, air channel are provided with transfers windshield plate 3.
When using the utility model, preferably adopt computational fluid dynamics (CFD) method to carry out the design of injector 13, cycle flue 15, burner block air flow channel 9 and flue 21; Adopt computational fluid dynamics (CFD) method to determine quantity, layout and the orientation of fire hole 16, secondary fuel spray orifice 19, three grades of fuel jet orifices 20, thereby obtain gratifying flame profile and heat flux distribution.The utility model gas burner can contain 5,4～8 two stage burners 6 of 2～4 one-level burners, and fire hole 16 is preferably rectangle, preferably has 4～20.The burning load of one-level burner 5 preferably accounts for 10%～50% of total fuel load; The burning load of two stage burner 6 preferably accounts for 90%～50% of total fuel load.
The utility model provides the gas burner of the ultralow discharged nitrous oxides of long flame of a multiple spot burning that is used for ethane cracking furnace, its NOx discharge capacity is lower than 25 ppmvd, compare with low-NOx combustor with the pyrolysis furnace of CN200720032397.8, ability is bigger, heat flux distribution is reasonable more, operation is more stable, eliminated over against the low-temperature space between the high-temperature region of base burning device and two the base burning devices, thereby can obtain the interior Temperature Distribution of pyrolysis furnace more uniformly, the cycle of operation of improving pyrolysis furnace.And, burner of the present utility model safeguard and control on simpler, the operator who allows pyrolysis furnace optimize and stable heat flux characteristics under operate, be specially adapted on the ethane cracking furnace.
Other and further target of the present utility model, feature and advantage are by being described further in the following specific embodiment and the accompanying drawing.
Description of drawings
Fig. 1 is the main cutaway view (band furnace wall) of the utility model burner;
Fig. 2 is the left-hand cutaway view (band furnace wall) of the utility model burner;
Fig. 3 is the vertical view (band furnace wall) of the utility model burner;
Fig. 4 is the main cutaway view (band cycle flue) of the one-level burner of the utility model burner;
Fig. 5 is the vertical view of the utility model combustor nozzle brick;
Fig. 6 is the A-A cutaway view of the utility model combustor nozzle brick;
Fig. 7 is the B-B cutaway view of the utility model combustor nozzle brick.
The specific embodiment
Shown in Figure 1 is a kind of gas burner of using the ultralow discharged nitrous oxides of long flame of the multiple spot burning that is used for ethane cracking furnace of the present utility model, and it mainly is made up of silencer cover 1, air channel 2, accent windshield plate 3, bellows 4, one-level burner 5, two stage burner 6, burner block 7, altar lamp 8.It only is a kind of form of the present utility model, and the utility model is not limited in this.
Consult Fig. 1～Fig. 4, gas burner has 2 one-level burners 5 and 4 two stage burners 6.One-level burner 5 is made up of one-level fuel nozzle 12, injector 13, nozzles 14, cycle flue 15, has the fire hole 16 of 12 strips on the nozzles 14.One-level fuel is via one-level fuel nozzle 12, spray into injector 13 from the one-level fuel jet orifice in the free jet mode, at low-pressure area of injector 13 inner formation, thereby the flue gas in the burner hearth is sucked injector 13 by flue 21 on the burner block 7 and cycle flue 15, after circulating flue gas and one-level fuel mix in injector 13, spray into the air flow channel 9 of burner block 7 via the fire hole 16 of 12 strips on the nozzles 14, mix with combustion air and burn after enter burner hearth.
Consult Fig. 1～Fig. 3, two stage burner 6 is made up of secondary fuel air inlet pipe 17 and secondary fuel nozzle 18.Secondary fuel enters secondary fuel air inlet pipe 17, via secondary fuel nozzle 18, from secondary fuel spray orifice 19 and 20 ejections of three grades of fuel jet orifices, mix with combustion air and burn after enter burner hearth.
Consult Fig. 1, combustion air is by air channel 2 and transfer windshield plate 3, enters bellows 4, enters the entrance 10 and the outlet section 11 of burner block 7 air flow channels then successively, enters burner hearth at last, and fuel and combustion air carry out fractional combustion in burner hearth.
Consult Fig. 5～Fig. 7, the air intake section 10 of this utility model combustor nozzle brick 7 is that cross section is constant and be rectangle or foursquare cuboid runner, air outlet slit section 11 runners shrink gradually, forming a cross section is rectangle, and length-width ratio becomes big contracted channel gradually, make runner become flat gradually, the continuous speedup of combustion air, therefore the air outlet slit section 11 of burner block 7 be one with respect to the bigger square-section of air intake section 10 length-width ratios, so that adapt with flat long flame.
Consult Fig. 4～Fig. 6, this utility model combustor nozzle brick 7 has 2 flues 21, and the bottom is communicated with cycle flue 15, makes the flue gas in the burner hearth suck injector 13 by flue 21 and cycle flue 15, and mixes with one-level fuel gas, finishes flue gas recirculation.
Consult Fig. 3, the fire hole 16 of 12 strips is arranged on the nozzles 14 of one-level burner 5, its long limit is parallel to stove side wall 25.
Consult Fig. 1, Fig. 7,22 exits, duct being equipped with two stage burner 6 are provided with groove 24, at each groove 24 place a secondary fuel nozzle 18 are arranged.
The design of the strip fire hole 16 among Fig. 1～Fig. 4, injector 13, cycle flue 15, secondary fuel spray orifice 19 and three grades of fuel jet orifices 20, layout, quantity and orientation adopt computational fluid dynamics (CFD) method to design.
The design of the air flow channel 9 of burner block 7, flue 21 adopts computational fluid dynamics (CFD) method to carry out among Fig. 5～Fig. 7.
This gas burner NOx discharge capacity is lower than 25 ppmvd, and flame is flat upright and outspoken, and heat flux distribution is reasonable.
Claims (15)
1. the gas burner of the ultralow discharged nitrous oxides of long flame of multiple spot burning, mainly by silencer cover (1), air channel (2), transfer windshield plate (3), bellows (4), one-level burner (5), two stage burner (6), burner block (7), altar lamp (8) is formed, it is characterized in that burner block (7) places the stove bottom, the boring place is air flow channel (9), at its entrance (10) is a straight runner that cross-sectional area is constant, the cross-sectional area of outlet section (11) diminishes gradually and forms the air contracted channel, be beneficial to form flat flame, at this moment cross section and internal face angulation β; Be provided with one-level burner (5) in the air flow channel (9) of burner block (7), one-level burner (5) is a pre-mixing type combustion apapratus; One-level burner (5) is made up of one-level fuel nozzle (12), injector (13), nozzles (14), cycle flue (15), has fire hole (16) on the nozzles (14), disperses burning to realize multiple spot; Also be provided with duct (22) between the inner and outer wall of burner block (7) with one-level burner axially parallel, be provided with two stage burner (6) in the duct (22), two stage burner (6) is a diffusion flame burner, form by secondary fuel air inlet pipe (17), secondary fuel nozzle (18), have secondary fuel spray orifice (19) on the secondary fuel nozzle (18), in the exit, duct (22) of placing two stage burner (6) is a groove greater than the cross section, duct (24), and groove (24) is built-in with secondary fuel nozzle (18); Also have flue (21) on the burner block (7), be communicated with the cycle flue (15) of one-level burner (5) and realize flue gas recirculation; Combustion air is by air channel (2) and transfer windshield plate (3) to enter bellows (4), enters entrance (10), the outlet section (11) of air flow channel then successively, enters in the burner hearth at last.
2. gas burner according to claim 1 is characterized in that the secondary fuel nozzle (18) of two stage burner (6) is gone up except that having secondary fuel spray orifice (19), also offers three grades of fuel jet orifices (20).
3. gas burner according to claim 2 is characterized in that the profile of secondary fuel nozzle (18) is " spade " structure.
4. gas burner according to claim 1 it is characterized in that 4～20 fire holes (16) are arranged on the nozzles (14), and fire hole (16) is a strip.
5. gas burner according to claim 1 is characterized in that gas burner has 2～4 one-level burners (5).
6. gas burner according to claim 5 is characterized in that 2～4 one-level burners of gas burner (5) form a line, and its line of centres is parallel to stove side wall (25).
7. gas burner according to claim 4 is characterized in that the long limit of the fire hole (16) of strip is parallel to stove side wall (25).
8. gas burner according to claim 1, it is characterized in that burner block (7) has the burner block flue (21) that is communicated with burner hearth and cycle flue (15) away from the one side (23) of side wall, flue (21) is communicated with cycle flue (15), to realize inner flue gas of the stove recirculation.
9. gas burner according to claim 1 is characterized in that the angle beta that outlet section (11) air contracted channel inwardly shrinks gradually is preferably 45
o～80
o
10. gas burner according to claim 1 is characterized in that the secondary fuel spray orifice (19) and the angle of horizontal plane are 60
o～80
o
11. gas burner according to claim 1 is characterized in that the three grades of fuel jet orifices (20) and the angle of horizontal plane are 70
o～90
o
12. gas burner according to claim 1 is characterized in that having 1～4 one-level burner (5).
13. gas burner according to claim 1 is characterized in that having 4～8 two stage burners (6).
14. gas burner according to claim 1 is characterized in that leaving between the duct (22) of secondary fuel nozzle (18) and burner block (7) gap of 10～15mm.
15. gas burner according to claim 1 is characterized in that the non-burning brick or burned brick of high alumina matter that burner block (7) adopts the band stainless steel cloth to reinforce.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020547515 CN201819211U (en) | 2010-09-29 | 2010-09-29 | Gas burner with multi-point burning, long flame and ultra-low nitrogen oxide emission |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020547515 CN201819211U (en) | 2010-09-29 | 2010-09-29 | Gas burner with multi-point burning, long flame and ultra-low nitrogen oxide emission |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201819211U true CN201819211U (en) | 2011-05-04 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201020547515 Expired - Lifetime CN201819211U (en) | 2010-09-29 | 2010-09-29 | Gas burner with multi-point burning, long flame and ultra-low nitrogen oxide emission |
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| Country | Link |
|---|---|
| CN (1) | CN201819211U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100975A (en) * | 2013-04-08 | 2014-10-15 | 新日铁住金工程技术株式会社 | Combustion Device, Operation Method Thereof And Furnace Bottom Rotary Type Heating Furnace |
| CN110486722A (en) * | 2019-07-31 | 2019-11-22 | 南京天华化学工程有限公司 | A kind of bottom gas burner of the low NOx of hypoxemia |
-
2010
- 2010-09-29 CN CN 201020547515 patent/CN201819211U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104100975A (en) * | 2013-04-08 | 2014-10-15 | 新日铁住金工程技术株式会社 | Combustion Device, Operation Method Thereof And Furnace Bottom Rotary Type Heating Furnace |
| CN104100975B (en) * | 2013-04-08 | 2018-03-27 | 新日铁住金工程技术株式会社 | Burner, its method of operation and revolving burner bottom-type heating furnace |
| CN110486722A (en) * | 2019-07-31 | 2019-11-22 | 南京天华化学工程有限公司 | A kind of bottom gas burner of the low NOx of hypoxemia |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100728 Beijing, Chaoyangmen, North Street, No. 22, No. Patentee after: Sinopec Corp. Patentee after: Tianhua Institute of Chemical Machinery & Automation Co., Ltd. Address before: 100728 Beijing, Chaoyangmen, North Street, No. 22, No. Patentee before: Sinopec Corp. Patentee before: Tianhua Chemical Machinery & Automation Research Inst. |
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Granted publication date: 20110504 |