CN211551590U - Flameless combustion device with low NOx emission - Google Patents
Flameless combustion device with low NOx emission Download PDFInfo
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- CN211551590U CN211551590U CN201922371709.3U CN201922371709U CN211551590U CN 211551590 U CN211551590 U CN 211551590U CN 201922371709 U CN201922371709 U CN 201922371709U CN 211551590 U CN211551590 U CN 211551590U
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Abstract
The utility model discloses a flameless combustion device that low NOx discharged, this flameless combustion device include the burner block that nozzle body, high temperature resistant refractory material made, set up the precombustion chamber on the burner block to and fuel pipe, primary air passageway, secondary air passageway etc.. At least one fuel nozzle is arranged at the bottom of the precombustion chamber; the bottom of the precombustion chamber is provided with a primary air circular seam; the nozzle brick is provided with secondary air spray holes, each secondary air spray hole consists of a plurality of secondary air small spray holes and a plurality of secondary air large spray holes, and the aperture of each secondary air small spray hole is smaller than that of each secondary air large spray hole. The flameless combustion device with low NOx emission and high regulation ratio can meet industrial practical application, can improve the combustion stability of a low-temperature furnace in a low-temperature combustion stage, and ensures safety; the efficient and low-pollution flameless combustion is realized at the high-temperature stage, the energy consumption and pollution are reduced, the product quality is improved, and the service life of the kiln is prolonged.
Description
Technical Field
The utility model belongs to the field of industrial burners, and relates to a low NOx emission flameless combustion device for high-temperature furnaces and kilns for steel, chemical engineering, boilers, glass, non-ferrous metal smelting and the like.
Background
In industries such as steel, boilers, petrifaction, glass, non-ferrous metal smelting and the like, a large number of high-temperature kilns exist, liquid fuels such as various gas fuels, fuel oil and the like and solid fuels are combusted, and heat and a high-temperature environment required by a production process are provided. High temperature combustion is a violent chemical reaction process, and the flame kiln not only produces various CO2When the exhaust gas is equal to the NOx and SO simultaneously generated2And a plurality of pollutants, CO2And is also the leading cause of climate change. The energy conservation, the reduction of the generation concentration and the total emission of various pollutants are the basic requirements of society and law and are the obligations of various production enterprises.
NOx is an important cause of haze and also causes serious human health problems, and is one of the main industrial kiln air pollutants. In the high-temperature combustion process, the generation of NOx has a mechanism, and based on the research on the formation mechanism of NOx in the combustion process, numerous low-NOx combustors, combustion devices and combustion methods are researched and developed at home and abroad, for example:
published patent application No. CN 104990078A discloses a burner and a combustion method capable of quickly realizing flameless combustion, which are provided with a central gas spray pipe, a loop gas spray pipe, two symmetrical air spray pipes and a loop air spray pipe, and the front ends of the central gas spray pipe and the loop gas spray pipe are connected with a flame stabilizing bluff body with an annular protrusion arranged at the front end, so that the switching between flameless combustion and flameless combustion is quickly realized. Although the patent realizes flameless combustion in principle, the structure is simple, various fuels in industrial practical application and the actual heating process requirement of the industrial kiln are not considered, and the practical application is difficult to meet.
The published patent CN 104266190A discloses an oxygen-enriched flameless gas burner and a control method thereof, wherein a pure oxygen nozzle is arranged on a common conventional burner, and by means of entrainment of high-speed oxygen jet flow to combustion flue gas, the mixing ratio of oxygen and flue gas is controlled, the concentration of oxygen is reduced, and then the oxygen and the gas are combusted, so that flameless combustion is realized, and the purposes of improving temperature uniformity, reducing NOx and saving energy are achieved. However, the publication requires high-speed, high-pressure, pure oxygen without complete elimination of air, and the equipment and the entire combustion piping are complicated; difficult to be applied to the factory lacking oxygen and has high cost.
Published patent CN 104633658A discloses a low-nitrogen oxide burner, the burner body is provided with a fuel nozzle which can introduce fuel into a combustion zone and a primary air nozzle, a secondary air nozzle and a tertiary air nozzle which can introduce air into the combustion zone, and a three-stage combustion structure which is communicated in sequence is adopted, so that air required by combustion is supplied in three stages, stable combustion is ensured, local high-intensity combustion is avoided, and NOx is greatly reduced. However, this publication cannot achieve flameless combustion, has a limited reduction in NOx concentration, and has difficulty in meeting current environmental protection, as well as future environmental protection requirements.
Published patent CN 102230623A discloses a flat combustion device, which comprises a nozzle arrangement unit, an air inlet unit and a flame control unit, wherein the air inlet unit and the flame control unit are respectively connected to two sides of the nozzle arrangement unit, and a gas nozzle, a primary air nozzle, a secondary air nozzle and a flame stabilizing area are arranged on the nozzle arrangement unit. The flat fuel nozzles and the specially arranged multi-stage air nozzles are adopted, so that the staged combustion is realized, the flat shape of flame is combusted, and the uniformity of heating temperature is improved. However, the disclosed patent also adopts the traditional combustion mode with obvious flame, and has the defect of higher NOx.
SUMMERY OF THE UTILITY MODEL
The utility model discloses the technical problem that will solve is: aiming at the defects in the prior art, the flameless combustion device with low NOx emission for high-temperature furnaces and kilns for steel, chemical industry, boilers, glass, non-ferrous metal smelting and the like is provided.
The utility model provides a flameless combustion device that low NOx discharged, through the air jet who special design and arrange, and the hierarchical of air is supplied, make air and fuel before the co-combustion, respectively mix with the tail gas that the burning produced earlier, the formation does not have the flame shape, combustion reaction produces the flameless combustion state that the temperature is even and do not have obvious high temperature region in whole furnace region or combustion space, can improve the temperature homogeneity of whole heating region greatly, maximum reduction NOx's emission, this is different from the general use has the conventional combustor of obvious flame form.
The flameless combustion device with low NOx emission realizes normal-temperature ignition and low-temperature stable operation by setting primary air circumferential seams to stabilize combustion flame based on normal-temperature ignition, low-temperature start of the kiln or flame temperature during operation under the condition of industrial practical application and safety consideration of the kiln; the air regulating valve is arranged at the inlet of the air main pipe to regulate and control the proportion and/or the switch of primary air and secondary air, so that the free switching of the high/low temperature working mode of the combustion device is realized, the reliability of low-temperature operation is ensured, the high-temperature mode can be switched under the high-temperature state of the kiln, and the clean and efficient combustion with ultra-low pollution of fuel is realized.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a flameless combustion device that low NOx discharged, including the burner block with set up in be the precombustion chamber of expansion form on the burner block, wherein:
at least one fuel nozzle is arranged at the bottom of the precombustion chamber;
a primary air circular seam is arranged at the bottom of the pre-combustion chamber and is annularly arranged on the periphery of the fuel nozzle;
the secondary air jet holes are formed in the burner block and consist of a plurality of first secondary jet holes arranged on the upper side and the lower side of the fuel nozzle and a plurality of second secondary jet holes arranged on the left side and the right side of the fuel nozzle, and the aperture of each first secondary jet hole is smaller than that of each second secondary jet hole.
Further, the fuel nozzle is positioned on a circular or elliptical track of the geometric center position of the precombustion chamber;
the primary air circular seam is positioned on a circular or elliptical track of the geometric center position of the pre-combustion chamber outside the fuel nozzle; and
the secondary air jet holes are positioned on a circular or elliptical track at the geometric center of the precombustion chamber.
Further, the first secondary nozzle hole is parallel to a geometric center line of the precombustion chamber or has a deviation angle beta towards the inner side relative to the geometric center line, and the deviation angle beta is 0-60 degrees. Preferably, said deviation angle β is between 0 and 55 °; more preferably, the deviation angle β is 5-40 °.
Further, the second secondary nozzle hole is parallel to a geometric center line of the precombustion chamber, or has an expansion angle gamma towards the outer side relative to the geometric center line, and the expansion angle gamma is 0-60 degrees. Preferably, said deviation angle γ is between 5 and 55 °; more preferably, the deviation angle γ is 10-50 °.
Further, the fuel nozzle is circular or elliptical, and the fuel flow rate is 8-200 m/s; preferably, the fuel flow rate is 15-140 m/s; more preferably, the fuel flow rate is 20-130 m/s.
Furthermore, a swirl plate is arranged in the primary air circular seam, and the air injected by the swirl plate accounts for 0-100% of oxygen required by the complete combustion of the fuel; the air flow rate at the primary air circular seam is 0.1-1.5 times of the fuel flow rate; preferably, the air flow rate at the primary air circular seam is 0.2-1.3 times of the fuel flow rate; more preferably, the air flow rate at the primary air annular gap is 0.5-1.2 times the fuel flow rate.
Further, the primary air sprayed at the primary air circumferential seams and/or the secondary air sprayed at the secondary air spray holes can be dynamically adjusted between the respective proportions of 0-100%.
Further preferably, the primary air supplied at the primary air circular seam can be completely closed and opened, or the secondary air supplied by the secondary air spray holes can be completely closed and opened, or the primary air and the secondary air are quantitatively distributed according to a certain proportion, so that dynamic adjustment is realized.
Further preferably, the primary air circular seam and the secondary air jet holes are communicated with an air inlet manifold through air transmission channels, and an air regulating valve for regulating the feeding ratio of the primary air and the secondary air is arranged on the air inlet manifold.
Further, the ratio of the spacing of the first secondary nozzle holes from the geometric center line of the precombustion chamber to the aperture of the first secondary nozzle holes is larger than 5.
Further, the air flow rate of the secondary air jet holes is 10-300m/s, and the secondary air jet holes and tail gas generated by combustion are mixed in advance to form a mixture with the oxygen concentration of 2-18%.
Further preferably, the air flow rate of the secondary air jet holes is 15-200m/s, and the secondary air jet holes and tail gas generated by combustion are premixed to form a mixture with the oxygen concentration of 2-9%.
More preferably, the air flow rate of the secondary air jet holes is 20-150m/s, and the secondary air jet holes and tail gas generated by combustion are premixed to form a mixture with the oxygen concentration of 3-8%.
Still more preferably, the air flow rate of the secondary air injection holes is 30-120m/s, and the secondary air injection holes are premixed with the tail gas generated by combustion to form a mixture with the oxygen concentration of 4-7%.
Further, an oxidant jet hole is formed in the geometric center of the bottom of the pre-combustion chamber and is arranged on the inner side of the fuel jet hole.
Further, the oxidant sprayed out of the oxidant spray holes is ordinary air, oxygen-enriched air with the oxygen concentration of more than 21% or pure oxygen with the oxygen concentration of more than 90%; the fuel sprayed out of the fuel nozzle is natural gas, coal gas, liquefied petroleum gas, fuel oil, coal or petroleum coke.
The above technical scheme is adopted in the utility model, compared with the prior art, following technological effect has:
(1) the flameless combustion device with low NOx emission adopts the grading, high-speed and multi-point feeding of combustion-supporting air, particularly, the structural design that a first secondary spray hole with a small aperture is matched with a second secondary spray hole with a large aperture, so that the premixing of air and tail gas (or combustion products) generated by combustion is greatly enhanced, the spreading surface and the spreading form of combustion reaction are effectively improved, the flameless combustion meeting the industrial application is realized, a flame high-temperature area is thoroughly eliminated, the temperature uniformity of the whole heating space is improved, the NOx emission level is greatly reduced, and the requirements of the current and future environmental protection emission regulations can be met;
(2) the air quantity sprayed at the primary air and/or secondary air blowholes is controlled through the air regulating valve, so that the distribution proportion of the primary air and the secondary air is dynamically regulated in the actual use process, the flameless combustion device with low NOx emission has a low-temperature mode and a high-temperature mode which are dynamically regulated in real time, stable combustion and safe heating are realized at a low-temperature stage, and explosion accidents are prevented; flameless combustion is realized at a high-temperature stage, and the temperature uniformity in the length and width directions is ensured, so that the emission of NOx is reduced;
(3) the flameless combustion device with low NOx emission can meet industrial practical application, and the stability of low-temperature furnace starting combustion is improved and the safety is ensured through a low-temperature combustion mode; the efficient and low-pollution flameless combustion is realized at the high-temperature stage, the energy consumption and pollution are reduced, the product quality is improved, and the service life of the kiln is prolonged.
Drawings
FIG. 1 is a schematic top view of a low NOx emission flameless combustion device according to the present invention;
FIG. 2 is a schematic cross-sectional view of section A-A of the low NOx emission flameless combustion device of FIG. 1;
FIG. 3 is a schematic cross-sectional view of section B-B of the low NOx emission flameless combustion device of FIG. 1;
wherein each reference numeral;
1-burner block, 2-precombustion chamber, 3-fuel nozzle, 4-primary air circumferential seam, 5-first secondary nozzle, 6-second secondary nozzle, 7-oxidant nozzle, 8-air main pipe, 9-air regulating valve, 10-air conveying channel, 11-vortex sheet, 12-primary air channel, 13-secondary air channel, 14-clapboard, 15-fuel main pipe, 16-fuel branch pipe and 17-oxidant pipe.
Detailed Description
The utility model provides a low NOx's flameless combustion device, especially one kind realizes that flameless combustion reaches low NOx or the burner and the combustion method that ultralow NOx discharged, its main technical scheme is the fuel nozzle 3 of design mutually supporting on furnace burner block, primary air circumferential weld 4 and secondary air orifice, in operation, primary air is the annular through primary air circumferential weld 4 around fuel nozzle 3 and spouts into, secondary air spouts the spout into through arranging the secondary air orifice in the 4 outsides of primary air circumferential weld, and secondary air orifice position keeps away from fuel nozzle 3 more, the secondary air orifice contains the first secondary orifice 5 and the second secondary orifice 6 in two at least different apertures.
In the low-NOx flameless combustion device, according to the jet entrainment principle, the specific orifice design and the flow rate selection of the secondary air orifice can ensure that a large amount of combustion products or combustion tail gas are entrained to form a mixture with the oxygen concentration of 2-10 percent before the secondary air is mixed with the fuel, and then the mixture is mixed and combusted with the fuel, thereby realizing the condition that no obvious flame form exists and the combustion reaction is carried out in the whole hearth space or a heating area; the combustion mode is different from the traditional combustion with obvious flame shape, commonly called as 'flameless combustion', the combustion reaction of the flameless combustion is carried out in the whole hearth region, the temperature distribution of the heating region is uniform, and the heating temperature uniformity can be greatly improved; and because the peak flame temperature is eliminated, the maximum flame temperature is greatly lower than that of the traditional flame combustion, and the method for flameless combustion is proved to greatly reduce the emission of NOx according to theoretical analysis and numerous tests and practical applications.
In addition, the secondary air jet hole adopts a plurality of jet hole structural designs with two different apertures or a plurality of different apertures, particularly, the structural design of the first secondary jet hole 5 with a small aperture and the second secondary jet hole 6 with a large aperture is adopted, so that the length of flame can be favorably controlled, the combustion reaction area is wider, and the temperature uniformity is better; the burner block is particularly beneficial to spreading of combustion reaction in the horizontal width direction of the burner block, and the heating temperature uniformity in the length direction and the horizontal width direction is improved. Meanwhile, in order to improve the working range and the load regulation ratio of the combustion device, an oxidant jet hole 7 can be arranged at the central line position of the precombustion chamber 2, and air, oxygen-enriched air or pure oxygen is supplied through the oxidant jet hole 7.
The present invention will be described in detail and specifically with reference to specific embodiments so as to provide a better understanding of the present invention, but the following embodiments do not limit the scope of the present invention.
Example 1
Referring to fig. 1-3, the present embodiment provides a flameless combustion apparatus with low NOx emission, which includes a burner block 1 made of a high temperature resistant refractory material, an expanding pre-combustion chamber 2 disposed on the burner block 1, a fuel pipe, a primary air passage 12, a secondary air passage 13, and the like. The burner block 1 is a hearth of a high-temperature furnace such as steel, chemical engineering, boilers, glass, non-ferrous metal smelting and the like and is made of refractory materials; the prechamber 2 has a divergence angle α, which is 30-60 °. Preferably, said deviation angle α is between 0 and 55 °; more preferably, the deflection angle α is 10-55 °; more preferably, the deflection angle α is 25-50 °.
In this embodiment, please refer to fig. 1, a fuel branch pipe 16 is disposed on a burner block 1, a far end of the fuel branch pipe 16 is connected to a fuel main pipe 15, a near end of the fuel branch pipe 16 is disposed with at least one fuel nozzle 3 at the bottom of the combustion chamber 2, and the fuel nozzle 3 is located on a circular or elliptical trajectory of a geometric center position of the precombustion chamber 2. The bottom of precombustion chamber 2 is provided with primary air circumferential weld 4, primary air circumferential weld 4 be the annular set up in the periphery of fuel spout 3, just primary air circumferential weld 4 is located circular or the ellipse circular orbit of the geometric centre position of precombustion chamber 2.
In this embodiment, referring to fig. 1, a secondary air injection hole is disposed on the burner block 1 made of refractory brick material, at a position further away from the fuel nozzle 3 from the outer side of the primary air circular seam 4, and the secondary air injection hole is divided into at least two types of injection holes with different apertures, and both of the injection holes are located on a circular or elliptical trajectory at the geometric center of the precombustion chamber 2. As a preferred embodiment, as shown in fig. 1, the secondary air injection holes are composed of a plurality of first secondary injection holes 5 arranged on the upper and lower sides of the fuel nozzle 3 and a plurality of second secondary injection holes 6 arranged on the left and right sides, and the aperture of the first secondary injection holes 5 is smaller than that of the second secondary injection holes 6.
The main technical scheme of the flameless combustion device with low NOx emission in the embodiment is as follows: the burner block 1 is provided with a fuel nozzle 3, a primary air circular seam 4 and a secondary air jet hole which are matched with each other. The fuel nozzle 3, the primary air circular seam 4 and the secondary air jet holes are used for realizing the grading, high-speed and multi-point feeding of combustion air, particularly, the first secondary jet hole 5 with a small aperture is matched with the structural design of the second secondary jet hole 6 with a large aperture, so that the mixing of air and combustion tail gas is greatly enhanced, the spreading surface and the spreading form of combustion reaction are effectively improved, flameless combustion meeting industrial application is realized, the NOx emission level is greatly reduced, and the requirements of the current and future environmental protection emission regulations can be met.
Example 2
Referring to fig. 1 to 3, unlike the foregoing embodiment 1, in the low NOx emission flameless combustion device of this embodiment, the secondary air injection holes are composed of a plurality of first secondary injection holes 5 and a plurality of second secondary injection holes 6, and the diameter of the first secondary injection holes 5 is smaller than that of the second secondary injection holes 6. The first secondary injection holes 5 with small apertures are arranged at the upper and lower sides of the fuel nozzle 3, and the second secondary injection holes 6 with large apertures are arranged at the left and right sides of the fuel nozzle 3.
In the present embodiment, please refer to fig. 2, the first secondary nozzle hole 5 is parallel to a geometric centerline of the prechamber 2, or has a deviation angle β inward with respect to the geometric centerline, the deviation angle β is 0-60 °, and preferably, the deviation angle β is 0-55 °; more preferably, the deviation angle β is 5-40 °. That is, the first secondary nozzle holes 5 with small hole diameter can be horizontally arranged or set a certain angle beta to the geometric central line of the precombustion chamber 2, and the part of the high-speed fine air flow jetted from the first secondary nozzle holes 5 strengthens the mixing of the secondary air and the combustion tail gas, and ensures the combustion reaction in the area near the combustion device and the flame stability in the low-temperature stage.
In this embodiment, referring to fig. 3, the second secondary nozzle holes 6 are parallel to a geometric centerline of the prechamber 2, or have an angle γ of divergence outward from the geometric centerline, the angle γ of divergence is 0 to 60 °, and preferably, the angle γ of divergence is 5 to 55 °; more preferably, the deviation angle γ is 10-50 °. That is, the large-diameter second secondary nozzle holes 6 disposed on the left and right sides of the fuel nozzle 3 may be parallel to the geometric center line of the precombustion chamber 2 or have a certain expansion angle γ deviating from the geometric center line of the precombustion chamber 2, so that the air flow passing through the large-diameter second secondary nozzle holes 6 deviates from the fuel air flow, and the distribution and expansion of the combustion reaction in the horizontal width direction are guided.
Example 3
Based on the above-described embodiments 1 and 2, the present embodiment provides a more specific flameless combustion device with low NOx emissions. The fuel nozzle 3 is circular or elliptical to form a specific flame shape and to facilitate maximum premixing with the combustion exhaust gases; the flow velocity of the fuel nozzle is between 8 and 200 m/s; preferably, the fuel flow rate is 15-140 m/s; more preferably, the fuel flow rate is 20-130 m/s; more preferably, the fuel flow rate is 50-120 m/s; more preferably, the fuel flow rate is 75-105 m/s.
In this embodiment, the primary air is injected from the primary air circumferential seam 4 on the periphery of the fuel nozzle 3, in order to promote the primary air injected from the primary air circumferential seam 4 to be fully mixed with the fuel injected from the fuel nozzle 3 to the utmost extent and ensure the flame stability, a spinning disk 11 can be arranged in the primary air circumferential seam 4, the spinning disk 11 can enable the primary air jet injected from the primary air circumferential seam 4 to rotate around the geometric center of the fuel nozzle 3, and the rotating jet promotes the mixing of the primary air and the fuel on the one hand and ensures the stable combustion; on the other hand, a large amount of high-temperature combustion products are sucked, and the ignition stability is ensured.
In the embodiment, the air injected from the primary air annular seam 4 accounts for 0-100% of oxygen required by the total combustion of the fuel; the air flow rate at the primary air circular seam 4 is 0.1-1.5 times of the fuel flow rate. Preferably, the air flow rate at the primary air circular seam is 0.2-1.3 times of the fuel flow rate; more preferably, the air flow rate at the primary air circular seam is 0.3-1.2 times of the fuel flow rate; more preferably, the air flow rate at the primary air annular gap is 0.6-1.0 times the fuel flow rate.
Example 4
Unlike the above embodiments, referring to fig. 1-2, the low NOx emission flameless combustion device of the present embodiment further includes an air adjustment valve 9 for dynamically adjusting the air supply to the primary air annular gap 4 and the secondary air injection holes. The air regulating valve 9 is arranged on an air inlet header pipe 8, and the air inlet header pipe 8 is communicated with the secondary air circular seam 4 and the secondary air jet holes through an air transmission channel 10 and respectively provides air for the secondary air circular seam 4 and the secondary air jet holes. The air transmission channel 10 is divided into a left secondary air cavity channel 12 and a right secondary air cavity channel 13 by a partition plate 14, the secondary air cavity channel 12 is communicated with secondary air spray holes, and the primary oxygen cavity channel 13 is communicated with the primary air circular seam 4 and respectively provides air for the primary air circular seam 4 and the secondary air spray holes.
In the embodiment, during the use of the flameless combustion device with low NOx emission, the proportion of the primary air at the primary air circular seam 4 and/or the secondary air at the secondary air injection hole can be dynamically adjusted through the air adjusting valve 9, and the primary air and the secondary air can be dynamically adjusted between 0-100% of the proportion respectively. Specifically, for example, in the low-temperature stage when the kiln is just ready to start, all the air required for fuel combustion is injected through the primary air circumferential seam 4, and the secondary air injection holes are all closed; in the high-temperature stage of stable combustion, all air required by fuel combustion is sprayed from the secondary air spray holes, and the secondary air spray holes are far away from the fuel spray nozzle 3, so that a large amount of tail gas is entrained by the high-speed fine air jet flow sprayed from the secondary air spray holes, and flameless combustion is formed.
Example 5
In contrast to the above embodiments, referring to fig. 1, in the flameless combustion device with low NOx emission injected by the present embodiment, the secondary air injection holes include a first secondary injection hole 5 and a second secondary injection hole 6 with different inner diameters of the two injection holes, wherein a ratio of a distance from the first secondary injection hole 5 to a geometric center of the fuel injection hole 3 to a diameter of the first secondary injection hole 5 is greater than 5. The second secondary spray holes 6 are respectively expanded towards the left side and the right side on the burner block 1 to form fan-shaped spreading, and the expansion angle of the second secondary spray holes 6 is 0-60 degrees. The plurality of first secondary injection holes 5 and the plurality of second secondary injection holes 6 are arranged at circular or elliptical positions around the fuel nozzle, and the plurality of first secondary injection holes 5 are arranged on a circular or elliptical track at the geometric center position of the fuel nozzle 3.
In the embodiment, the air flow rate of the secondary air jet hole is 10-300m/s, and the secondary air jet hole and tail gas generated by combustion are mixed in advance to form a mixture with the oxygen concentration of 2-18%; preferably, it is premixed with the tail gas from combustion to form a mixture with an oxygen concentration of 2-15%; more preferably, it is premixed with the tail gas from combustion to form a mixture with an oxygen concentration of 2-10%; more preferably, it is premixed with the tail gas from the combustion to form a mixture having an oxygen concentration of 4-8%. Preferably, the air flow rate of the secondary air jet holes is 15-200m/s, and the secondary air jet holes are premixed with tail gas generated by combustion to form a mixture with the oxygen concentration of 2-9%. More preferably, the air flow rate of the secondary air jet holes is 20-150m/s, and the secondary air jet holes and tail gas generated by combustion are premixed to form a mixture with the oxygen concentration of 3-8%. More preferably, the air flow rate of the secondary air injection holes is 30-120m/s, and the secondary air injection holes are premixed with tail gas generated by combustion to form a mixture with the oxygen concentration of 4-7%. According to the jet entrainment principle, the orifice design and the flow rate selection of the secondary air orifices can ensure that a large amount of combustion products or combustion tail gas is entrained before the secondary air is mixed with the fuel to form a mixture with the oxygen concentration of 2-10 percent and then the mixture is mixed with the fuel, thereby realizing flameless combustion.
The embodiment adopts two secondary air jet holes 5 and 6 with different sizes and different apertures, and adopts a specific arrangement design, thereby being beneficial to controlling the length of flame, forming flat flame with horizontal width being far larger than vertical height, and improving the uniformity of heating temperature in the length direction and the horizontal width direction.
Example 6
On the basis of the above embodiments, please refer to fig. 1 and fig. 2, in order to improve the working range and the load regulation ratio of the low NOx emission flameless combustion device, an oxidant nozzle 7 is further disposed on the low NOx emission flameless combustion device, the oxidant nozzle 7 is connected to an oxidant conduit 17, and the oxidant conduit 17 is located on the center line of the prechamber 2. The oxidant jet hole 7 is arranged at the geometric center position of the bottom of the precombustion chamber 2, and the oxidant jet hole 7 is arranged at the inner side of the fuel jet 3. The oxidant sprayed out from the oxidant spray hole 7 is common air, oxygen-enriched air with the oxygen concentration of more than 21 percent or pure oxygen with the oxygen concentration of more than 90 percent; the fuel sprayed out of the fuel nozzle 3 is natural gas, coal gas, liquefied petroleum gas, fuel oil, coal or petroleum coke.
In this embodiment, the fuel, the central oxidant and the primary air, which are sequentially injected from the fuel nozzle 3, the oxidant nozzle 7 and the primary air circumferential seam 4, are injected into the furnace or the heating region inside the pre-combustion chamber 2 made of refractory material, and the high-temperature combustion exhaust gas, i.e., flue gas, is entrained, and after diluting the oxygen concentration in the air and the central oxidant and the concentration of the fuel in the fuel, the mixed combustion is performed in the pre-combustion chamber 2.
Example 7
On the basis of the flameless combustion device with low NOx emission injected in the above embodiment, the embodiment provides a flameless combustion method with low NOx emission, which can be used in high temperature furnaces such as steel, chemical engineering, boilers, glass, non-ferrous metal metallurgy, and specifically, the flameless combustion method comprises the following steps:
(1) and (3) starting the furnace at normal temperature: when the temperature of the burner block of the hearth is normal temperature or the process temperature is lower than about 850 ℃, primary air is supplied to a primary air circumferential seam through an air regulating valve, and fuel is supplied to a fuel nozzle for ignition;
(2) and (3) a low-temperature combustion stage: after normal temperature ignition combustion, the temperature of a burner block of a hearth rises, the air supply of the primary air circumferential joint is increased through the air regulating valve, or air is supplied into the secondary air spray holes through the air regulating valve while the air is supplied to the primary air circumferential joint, so that all oxygen required by combustion is supplied by the primary air or supplied by the primary air and the secondary air together, and stable low-temperature combustion is carried out;
(3) and (3) high-temperature combustion stage: when the temperature of the burner block of the hearth or the process temperature is higher than the self ignition point of the fuel, the secondary air supplied by the secondary air spray holes is increased through the air regulating valve, or the oxygen required by combustion is completely supplied by the secondary air and is mixed with the combustion products to form a mixture with the oxygen concentration of 2-18 percent, and then the mixture is mixed with the fuel to carry out flameless combustion without obvious flame.
In the present embodiment, the fuel flow rate is 8 to 200 m/s; the flow rate of the primary air is 0.1-1.5 times of the flow rate of the fuel; the flow velocity of the secondary air is 10-300 m/s.
In this embodiment, in step 1, the primary air supplied from the primary air circular seam 4 can ensure reliable ignition and flame temperature, and is convenient for use in normal temperature furnace start or low temperature stage; the secondary air supplied from the secondary air injection holes is the key to realize flameless combustion, ensure low NOx emission in normal high-temperature stage and uniform heating temperature. In order to realize normal-temperature ignition and low-temperature use in the using process, an air regulating valve 9 for the proportion of primary air and secondary air is arranged in the air inlet main pipe 8. The air regulating valve 9 can close and open the primary air or close and open the secondary air completely or quantitatively distribute the primary air and the secondary air according to a certain proportion by controlling the rotating angle of the regulating baffle plate, thereby realizing dynamic regulation.
Specifically, the primary air and/or the secondary air can be adjusted to be 0-100% of the air required by combustion at will in the actual use process of the combustion device through the air adjusting valve 9; since the nozzle holes of the primary air annular slits 4 are closer to the fuel nozzle 3, combustion can be promoted. In the actual use process, at the stage that the temperature of the hearth is normal temperature or lower than about 850 ℃, the combustion is often unstable, so that the safety hidden danger caused by stable combustion and reliable ignition is ensured, and flame extinguishment is prevented. Therefore, in the low-temperature stage, more or all air required by combustion is often sprayed in from the primary air circumferential seams 4, so that the combustion temperature is ensured, and flameout is prevented; when the temperature of the hearth or the process temperature is higher than the self ignition point of the fuel, the combustion reaches a certain temperature, the hidden danger of flame extinction does not exist, more air or all air is sprayed in through the secondary air spray holes, due to the special design and the flow rate of the plurality of secondary air spray holes, the air is mixed with the combustion tail gas in advance inside the hearth to form a mixture with the oxygen concentration of 2-18%, and then the mixture is mixed and combusted with the fuel, so that a flameless combustion state without obvious flame is formed, the purposes of uniform temperature and great reduction of NOx are achieved, and two combustion modes of low temperature and high temperature of the combustion device are realized.
The above detailed description of the embodiments of the present invention is only for exemplary purposes, and the present invention is not limited to the above described embodiments. Any equivalent modifications and substitutions to those skilled in the art are also within the scope of the present invention. Accordingly, variations and modifications in equivalents may be made without departing from the spirit and scope of the invention, which is intended to be covered by the following claims.
Claims (10)
1. The utility model provides a flameless combustion device of low NOx emission which characterized in that, include the burner block with set up in be the precombustion chamber of expansion form on the burner block, wherein:
at least one fuel nozzle is arranged at the bottom of the precombustion chamber;
a primary air circular seam is arranged at the bottom of the pre-combustion chamber and is annularly arranged on the periphery of the fuel nozzle;
the secondary air jet holes are formed in the burner block and consist of a plurality of first secondary jet holes arranged on the upper side and the lower side of the fuel nozzle and a plurality of second secondary jet holes arranged on the left side and the right side of the fuel nozzle, and the aperture of each first secondary jet hole is smaller than that of each second secondary jet hole.
2. The low NOx emission flameless combustion device of claim 1 wherein the fuel jet is located on a circular or elliptical trajectory at the geometric center of the prechamber;
the primary air circular seam is positioned on a circular or elliptical track of the geometric center position of the pre-combustion chamber outside the fuel nozzle; and
the secondary air jet holes are positioned on a circular or elliptical track at the geometric center of the precombustion chamber.
3. The low NOx-emissions flameless combustion device according to claim 1, wherein said first secondary nozzle orifice is parallel to a geometric centerline of said pre-combustion chamber or has a deviation angle β inward with respect to said geometric centerline, said deviation angle β being 0-60 °.
4. The low NOx-emissions flameless combustion device according to claim 1, wherein said second secondary nozzle hole is parallel to a geometric centerline of said pre-combustion chamber or has an angle of divergence γ towards the outside with respect to the geometric centerline, said angle of divergence γ being comprised between 0 ° and 60 °.
5. The low NOx emission flameless combustion device of claim 1 wherein the fuel jets are circular or elliptical and the fuel flow rate is between 8 and 200 m/s.
6. The low NOx emission flameless combustion device of claim 1 wherein swirl plates are disposed within the primary air annulus and inject air in the range of 0-100% of the oxygen required for total combustion of the fuel; the air flow rate at the primary air circular seam is 0.1-1.5 times of the fuel flow rate.
7. The low NOx emission flameless combustion device of claim 1 wherein the primary air injected at the primary air annular gap and/or the secondary air injected at the secondary air injection orifices are dynamically adjustable between respective proportions of 0-100%.
8. The low NOx emission flameless combustion device of claim 7 wherein said primary air annulus and said secondary air jet orifices are each in communication with an air inlet manifold through an air transfer passage, said air inlet manifold having an air adjustment valve disposed thereon for adjusting the ratio of the primary air to the secondary air feed.
9. The low NOx-emitting flameless combustion device of claim 1 wherein a ratio of a spacing of the first secondary orifice from a geometric centerline of the precombustor to an aperture thereof is greater than 5.
10. The low NOx emissions flameless combustion device of claim 1 wherein an oxidant orifice is disposed at a geometrically central location of the bottom of the prechamber, said oxidant orifice being disposed inside the fuel nozzle orifice.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112050215A (en) * | 2020-09-30 | 2020-12-08 | 江苏泷涛环境技术有限公司 | Efficient air multistage injection smoke internal circulation low-nitrogen combustor and application |
| CN112664978A (en) * | 2020-12-29 | 2021-04-16 | 上海交通大学 | Opposite-impact type cold flame combustion system |
| CN113566198A (en) * | 2021-06-09 | 2021-10-29 | 上海交通大学 | Flameless combustor suitable for variable load and use method thereof |
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2019
- 2019-12-26 CN CN201922371709.3U patent/CN211551590U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112050215A (en) * | 2020-09-30 | 2020-12-08 | 江苏泷涛环境技术有限公司 | Efficient air multistage injection smoke internal circulation low-nitrogen combustor and application |
| CN112664978A (en) * | 2020-12-29 | 2021-04-16 | 上海交通大学 | Opposite-impact type cold flame combustion system |
| CN113566198A (en) * | 2021-06-09 | 2021-10-29 | 上海交通大学 | Flameless combustor suitable for variable load and use method thereof |
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