阅读说明：本技术 烧结矿的制造方法 (Method for producing sintered ore ) 是由 黒岩将人 野中俊辅 堀川透理 大浦峻典 神野哲也 于 2018-04-20 设计创作，主要内容包括：本发明的目的在于抑制烧结机中的燃烧不均,制造强度高、块成品率高的烧结矿。一种烧结矿的制造方法,将包含粉矿和碳材料的烧结原料装入循环移动的托盘上而形成原料层,对上述原料层表面的碳材料进行点火,并且将上述原料层上方的空气向上述托盘的下方吸引而导入到上述原料层内,在上述原料层内使上述碳材料燃烧而制造烧结矿,所述烧结矿的制造方法中,以40Nm/s以上的流速从喷嘴喷出燃料气体,使喷出的上述燃料气体燃烧而生成燃烧气体,使用上述燃烧气体对上述碳材料进行点火。(The purpose of the present invention is to produce a sintered ore having high strength and high lump yield by suppressing uneven combustion in a sintering machine. A method for producing a sintered ore, comprising charging a sintering material comprising a fine ore and a carbon material onto a circularly moving tray to form a material layer, igniting the carbon material on the surface of the material layer, introducing air above the material layer into the material layer by sucking the air below the tray, and burning the carbon material in the material layer to produce the sintered ore, wherein a fuel gas is jetted from a nozzle at a flow rate of 40Nm/s or more, the jetted fuel gas is burned to produce a combustion gas, and the carbon material is ignited using the combustion gas.)

1. A method for producing sintered ore, comprising charging a sintering material comprising a fine ore and a carbon material onto a circulating tray to form a material layer, igniting the carbon material on the surface of the material layer, introducing air above the material layer into the material layer by sucking the air below the tray, and burning the carbon material in the material layer to produce sintered ore,

The fuel gas is ejected from the nozzle at a flow rate of 40Nm/s or more,

Burning the injected fuel gas to generate a combustion gas,

Igniting the carbon material using the combustion gas.

2. The method for producing sintered ore according to claim 1, wherein the combustion gas is generated by using a burner provided with a main burner part and a sleeve flame burner part,

The main burner unit includes a fuel gas nozzle for ejecting the fuel gas and an air nozzle for ejecting combustion air, and the pilot burner unit is located outside the main burner unit and burns the fuel gas ejected from the main burner unit.

Technical Field

the present invention relates to a method for producing sintered ore, and more particularly to a method for producing sintered ore capable of producing high-strength sintered ore for blast furnace raw materials.

Background

A downward suction type of claus sintering machine (downward suction type of Dwight Lloyd sintering machine) is widely used for manufacturing sintered ore (sintered ore). In a below suction type trolehr sintering machine, a raw material containing fine ore (fine ore) and a carbon material as a fuel such as coke breeze (coke breeze) are mixed and loaded on a tray to form a raw material layer. Then, the coke powder on the surface of the raw material layer is ignited by an ignition furnace provided above the raw material layer, and air above the raw material layer is sucked downward by a negative pressure of a bellows disposed below the tray. As a result, the burning of the coke powder in the raw material layer gradually shifts to the lower part in the layer to sinter the raw material, and a sintered cake is produced. The obtained sintered cake is pulverized into pieces of an ideal grain size, the grain size is adjusted, and then the pieces are charged into a blast furnace, and sintered ore is reduced in the blast furnace to become pig iron.

As the burners used in the ignition furnace of the above sintering machine, a slit burner in which a fuel gas and combustion air are mixed in advance and discharged from a slit-shaped nozzle to be burned, and a linear burner in which a plurality of nozzles for the fuel gas and the combustion air are arranged in the width direction of the ignition furnace (the direction intersecting the moving direction of the raw material layer) are generally used. In recent years, a burner having a structure as described in patent document 1 has also been proposed.

Disclosure of Invention

In the operation of a blast furnace, it is important to use high-strength sintered ore. If a low-strength sintered ore is charged into a blast furnace, the powder generated from the sintered ore hinders the ventilation of the blast furnace, and therefore the sintered ore charged into the blast furnace is required to have a high strength. Further, the high-strength sintered ore is preferable because it is not easily pulverized in the process of crushing, sieving, and processing, and the yield of the lump sintered ore charged into the blast furnace is high. Therefore, development of a method for producing a sintered ore having higher strength has been demanded.

The present invention has been made in view of the above circumstances, and an object thereof is to provide a method for producing sintered ore capable of producing high-strength sintered ore for blast furnace raw materials.

The inventors considered that in order to produce a sintered ore having high strength, it was necessary to reduce the unevenness of calcination in the raw material layer. The reason is that if there is unevenness in calcination, the strength of the sintered ore, which is a part insufficiently calcined, is insufficient, and powder is easily generated. Further, it is considered that in order to reduce the firing unevenness in the raw material layer, it is important to uniformly ignite the upper layer of the raw material layer, and intensive studies are made on a method of uniformly igniting.

As a result, it has been found that, by igniting the raw material layer with a high-speed flame in an ignition furnace at a flow velocity of gas to be burned for igniting the raw material layer higher than that in the conventional art, unevenness in firing of the raw material layer is reduced, and a sintered ore having a high briquette yield and high strength can be produced.

However, as a result of the study, it has been found that the burner used in the conventional ignition furnace cannot sufficiently increase the ejection flow rate of the fuel gas, and there is a limit to the reduction of the firing unevenness.

for example, fig. 10 is a schematic view showing an example of a premix burner used in a conventional ignition furnace. In the premix burner 100, a combustible fuel gas 101 and air 102 are mixed in advance inside the premix burner 100 to prepare a mixed gas, and the mixed gas is ejected from the premix burner 100 and burned to form a flame 103.

However, if the flow velocity of the fuel gas or air is simply increased in order to increase the ejection velocity, the flame becomes unstable. Further, if the flow rate is further increased, the mutual balance between the combustion rate and the gas flow rate is lost, and so-called blowout occurs in which the flame is blown off downstream and extinguished. Therefore, the conventional burner cannot increase the ejection speed significantly.

In addition, patent document 1 proposes a method of using a burner including a main burner and a pilot burner for assisting combustion in the main burner, as a method of stabilizing a flame and suppressing blowout. However, although patent document 1 discloses that ignitability can be improved and fuel specific consumption can be reduced by suppressing blow-out, it does not discuss that strength of a sintered ore is improved by increasing a gas flow rate, and there is a limit to increase the gas flow rate.

The present invention has been completed based on the above findings, and the gist thereof is as follows.

1. A method for producing sintered ore, comprising charging a sintering material comprising fine ore and a carbon material onto a circulating tray to form a material layer, igniting the carbon material on the surface of the material layer, introducing air above the material layer into the material layer by sucking the air below the tray, and burning the carbon material in the material layer to produce sintered ore,

The fuel gas is ejected from the nozzle at a flow rate of 40Nm/s or more,

The injected fuel gas is combusted to generate a combustion gas,

Igniting the carbon material using the combustion gas.

2. The method for producing sintered ore according to the above 1, wherein the combustion gas is generated by using a burner provided with a main burner part and a sleeve flame burner part (sleeve flame バ ー ナ part),

The main burner unit includes a fuel gas nozzle for ejecting the fuel gas and an air nozzle for ejecting combustion air, and the pilot burner unit is located outside the main burner unit and burns the fuel gas ejected from the main burner unit.

According to the present invention, it is possible to produce a sintered ore having high strength and high lump yield by firing the sintered layer with a combustion gas having a high ejection speed to reduce uneven burning of the sintered ore.

Drawings

Fig. 1 is a schematic view showing a structure of a burner according to an embodiment of the present invention.

Fig. 2 is a schematic view showing the structure of a main burner unit in an embodiment of the present invention.

Fig. 3 is a schematic diagram showing a structure of a cuff flame burner unit according to an embodiment of the present invention.

Fig. 4 is a schematic diagram showing a structure of a cuff flame burner unit according to another embodiment of the present invention.

Fig. 5 is a graph showing the ejection speed in each of the burners of the example and the comparative example.

fig. 6 is a graph showing the flow rate of the fuel gas and the powder fraction of the sintered ore in the ignition furnace.

Fig. 7 is a photograph showing the surface condition of the raw material layer after ignition in the ignition furnace.

Fig. 8 is a diagram showing heating forces in the respective burners.

Fig. 9 is a diagram showing an example of measurement of temperature distribution in the combustor 1 and the combustor 3.

Fig. 10 is a schematic view showing an example of a premix burner used in a conventional ignition furnace.

Detailed Description

Next, a method for carrying out the present invention will be specifically described. The following description shows preferred embodiments of the present invention, and the present invention is not limited to the following description.

in a method for producing sintered ore according to an embodiment of the present invention, a sintering material including fine ore and a carbon material is loaded on a tray that moves in a circulation manner to form a material layer, the carbon material on the surface of the material layer is ignited, air above the material layer is sucked by a wind box disposed below the tray and introduced into the material layer, and the carbon material is burned in the material layer to produce sintered ore.

The above-described manufacturing method is not particularly limited, and any sintering machine may be used as long as it is a sintering machine provided with a tray, an ignition unit (ignition furnace), and a mechanism for sucking air above the raw material layer. That is, a general downward suction type trolehr type sintering machine can be used. Further, a gaseous fuel supply device may be provided downstream of the ignition furnace to supply gaseous fuel to the upper side of the raw material layer.

In the present invention, the fuel gas is ejected from a nozzle at a flow rate of 40Nm/s or more, the ejected fuel gas is ignited to generate a combustion gas, and the carbon material is ignited using the combustion gas. The quantity of heat transfer Q from the flames to the surface of the object is proportional to the heat transfer coefficient α, which is larger as the velocity V0 of the flames is larger. Therefore, in the present invention, the fuel gas is ejected at a high speed of 40Nm/s or more, and the fuel gas is ignited to generate a high-speed combustion gas (flame). By making the high-speed combustion gas collide with the surface of the raw material layer as the object to be heated, heat can be supplied to the raw material layer with extremely high efficiency. According to the present invention, since the surface of the raw material layer can be uniformly heated and the carbon material contained in the raw material layer can be uniformly ignited, a sintered ore having high strength and high lump yield can be produced.

Ignition of the carbon material may be performed by any device as long as it is a device capable of generating combustion gas by ejecting fuel gas at a flow velocity satisfying the above conditions and igniting the fuel gas.

In one embodiment of the present invention, the combustion gas may be generated by using a burner including a main burner portion having a fuel gas nozzle for ejecting fuel gas and an air nozzle for ejecting combustion air, and a cuff burner portion located outside the main burner portion for burning the fuel gas ejected from the main burner portion. Hereinafter, a case of using the above burner will be described.

The main burner unit includes a fuel gas nozzle for ejecting fuel gas and an air nozzle for ejecting combustion air, and forms combustion gas for heating an object to be heated by combusting the fuel gas ejected from the main burner unit with the air. The sleeve flame burner unit has a function of igniting the fuel gas discharged from the main burner unit.

Here, it is important that the cuff burner part is located outside the burner with respect to the main burner part. By setting such a positional relationship, the flame can be stably held even at a higher ejection speed than in the case of setting other positional relationship.

The reason why the flame can be stably held even at a high ejection speed by setting the positional relationship is presumed as follows. That is, as proposed in patent document 1, when the fuel gas and the combustion air are arranged so as to sandwich the cuff burner and so as to collide with each other in the fuel gas ejection direction, a vortex is generated, and the kinetic energy loss is increased due to flow disturbance, so that a high flow velocity cannot be maintained. In contrast, in the technique of the present invention, the cuff flame burner part is positioned outside the burner with respect to the main burner part, so that the flow disturbance of the main stream of fuel gas and combustion air can be suppressed and a high flow rate can be maintained. Further, by making the fuel gas ejected from the main burner portion parallel to the ejection direction of the combustion air, flow disturbance can be further suppressed, and a high flow velocity can be maintained.

Further, when the fuel gas nozzle is located at the center, the sleeve flame burner is disposed outside the fuel gas nozzle, and the combustion air nozzle is further disposed outside the fuel gas nozzle, the fuel gas needs to be ejected toward the sleeve flame on both sides, and the fuel gas nozzles are needed on both sides. Therefore, the number of nozzles is increased, and thus the diameter of each nozzle is reduced to increase the ejection speed, so that the attenuation of the gas speed after ejection is increased, and the high flow speed after ejection cannot be maintained. In contrast, in the technique of the present invention, the fuel gas does not need to be divided into two sides, and therefore a high flow rate is maintained.

[ Fuel gas ]

The fuel gas is not particularly limited, and any fuel gas may be used as long as it is a combustible gas. For example, natural gas or LPG may be generally used, or a process gas by-produced in an iron works may be used as the fuel gas. As the process gas, it is particularly preferable to use an M gas in which coke oven gas and blast furnace gas are mixed.

Next, a more specific description will be given with reference to the drawings.

Fig. 1 is a schematic view of a combustor 1 of one embodiment of the present invention, showing a structure in a cross section of the combustor 1. The burner 1 includes a burner body 10, and a main burner unit 20 and a pilot burner unit 30 provided in the burner body 10. A recess 40 is provided at the tip (side where the flame is formed) of the burner 1, and the recess 40 includes a bottom portion 41 and a tapered portion 42 gradually widening from the bottom portion 41 toward the tip of the burner 1.

Fig. 2 is a schematic view showing the structure of the main burner part 20 in one embodiment of the present invention. The main burner unit 20 includes a fuel gas nozzle 21 for ejecting fuel gas and an air nozzle 22 for ejecting combustion air. The air nozzles 22 are arranged in a left-right symmetrical manner so as to sandwich the fuel gas nozzle 21.

in the example shown in fig. 2, a cross section of one burner is shown, but a plurality of burners are preferably arranged in a direction perpendicular to the paper surface to form a linear burner. In this case, the fuel gas nozzles, the combustion air nozzles, and the fuel gas discharge ports of the sleeve need not be located on the same cross section. The burner disposed in the linear burner is preferably provided with 20 or more fuel gas nozzles at intervals as uniform as possible for every 1m length of the linear burner. The more the number of fuel gas nozzles per unit length provided in the linear burner is, the more uniform heating is facilitated, but if the number is too large, the 1 nozzle diameter becomes too small, so it is preferable to provide 20 to 150 fuel gas nozzles per 1m of the linear burner, and it is more preferable to provide 30 to 60 fuel gas nozzles per 1m of the linear burner. The fuel gas discharge port of the linear burner is preferably located 300 to 900mm above the surface of the raw material layer.

the fuel gas is supplied as indicated by arrow G and is ejected from the fuel gas nozzle 21. Further, combustion air is supplied as indicated by arrow a and is ejected from the air nozzle 22. The fuel gas is not ignited at the time of being injected, but is ignited by the cuff flame 50 formed by the cuff flame burner unit 30 as shown in fig. 1, thereby forming a flame 60. Generally, the flame refers to a portion where a combustion reaction occurs to generate light and heat, and the combustion gas in the present invention includes both the flame and the gas generated by combustion. Ignition of the raw material layer containing the carbon material may be performed by heat of the flame, or may be performed by a high-temperature gas not accompanied by the flame generated by combustion.

The shapes of the fuel gas nozzle 21 and the air nozzle 22 are not particularly limited, and may be any shape. However, as shown in fig. 2, a straight tube structure having no conical structure of the nozzle tip is preferable. By using a nozzle having a straight tube structure, energy loss due to a vortex of gas or the like is reduced and a speed reduction due to a decay of a gas speed after ejection is reduced as compared with a case of using a nozzle forming a swirling flow or the like.

In order to improve the heating efficiency of the burner, the diameters of the fuel gas nozzle 21 and the air nozzle 22 are preferably determined so that the nozzle ejection flow rate in the commonly used flow rate region is 50 to 80 Nm/s. The gas flow rate at the time of maximum combustion is preferably 150Nm/s or less. Hereinafter, the diameters of the fuel gas nozzle and the air nozzle are simply referred to as "nozzle diameters".

Further, if the nozzle diameter is 3mm or more, the velocity decay after the ejection from the nozzle can be further suppressed. Therefore, the nozzle diameter is preferably 3mm or more, and more preferably 5mm or more. On the other hand, if the nozzle diameter is 30mm or less, the increase in the flow rate of the fuel gas due to the high-speed gas ejection can be suppressed, and the heat load on the combustor can be reduced. Therefore, the nozzle diameter is preferably 30mm or less.

When the diameter of the fuel gas nozzle 21 is set to dNG and the diameter of the air nozzle 22 is set to dNA, the interval between the fuel gas nozzle and the air nozzle (nozzle pitch) L1 preferably satisfies 2dNG ≦ L1 ≦ 15 dNA. When the burners are arranged to form a linear burner, the fuel gas nozzle interval (nozzle pitch) L2 of each burner preferably satisfies 2dNG ≦ L2 ≦ 15 dNA. This ensures combustion stability and prevents the gas velocity from decreasing.

In the main burner unit 20, a pressure equalizing chamber 23 is provided upstream of each of the fuel gas nozzles 21 and the air nozzles 22, and a perforated plate 24 having holes for passing fuel gas or air is provided on the side (upstream side) opposite to the nozzles of the pressure equalizing chamber 23. If the pressure equalizing chamber 23 is provided in this way, the gas can be ejected more uniformly, and therefore the flame can be stabilized further, and the ejection speed can be increased further. The pressure equalizing chamber 23 may be provided only on the upstream side of either the fuel gas nozzle 21 or the air nozzle 22, but is preferably provided on both sides as shown in fig. 2.

Fig. 3 is a schematic diagram showing the structure of the cuff flame burner unit 30 according to the embodiment of the present invention. In this example, the cuff burner unit 30 is constituted by a surface burner. A perforated plate 31 is provided at the tip of the surface burner, and fuel gas for flame and air are supplied to the perforated plate 31 as indicated by arrows G and a. In this burner, since the fuel gas and the air are ejected from the main burner part 20 at a high speed, an accompanying flow accompanying the air flow is formed in the vicinity of the tip end of the burner 1, particularly, inside the concave portion 40. For example, when the flow velocity of the gas jetted from the main burner unit is 50m/s, the flow velocity of the accompanying flow also reaches a high velocity of 20 to 30m/s, and therefore the cuff flame 50 formed by the cuff flame burner unit 30 may become unstable. However, in the surface burner, since the ignition point exists on the surface or inside the perforated plate, the sleeve fire can be stably maintained without being affected by the accompanying flow.

The porous plate 31 is not particularly limited, and a plate-like member made of any porous material may be used. The porous body may be made of a material such as metal, alloy, or ceramic. As the porous plate 31, for example, a metal mesh (formed by stacking metal fibers) can be used. The surface of the porous plate 31 is preferably arranged on the same plane as the surface of the tapered portion 42.

As shown in fig. 1, the fuel gas and air ejected from the main burner unit 20 are ignited by the sleeve flames 50. Therefore, from the viewpoint of reliable ignition, it is preferable that the main burner unit 20 and the cuff burner unit 30 are arranged such that the ejection axis (ejection direction) of the main burner unit 20 and the ejection axis (ejection direction) of the cuff burner unit 30 intersect on the extension line thereof. More specifically, the angle θ formed by the bottom portion 41 and the tapered portion 42 constituting the recess 40 is preferably 20 ° or more. If θ is less than 20 °, the flame of the cuff flame burner portion does not easily reach the air flow jetted from the main burner portion, and thus there is a high possibility of occurrence of misfire. The above θ is more preferably 30 ° or more. On the other hand, the upper limit of θ is not particularly limited, but is usually preferably 80 ° or less, and more preferably 60 ° or less.

The distance between the main burner unit and the cuff burner unit is determined so that the flame (cuff flame 50) of the cuff burner unit reaches the jet flow from the main burner unit. When the effective flame length of the cuff flame burner is F, the distance in which the flame of the cuff flame burner reaches the direction parallel to the surface of the bottom portion 41 is F · sin θ, and therefore the distance between the main burner portion and the cuff flame burner portion may be determined so that the distance between the position of the end of the main burner portion and the center position of the cuff flame burner portion is equal to or less than F · sin θ in the direction parallel to the surface of the bottom portion 41. Specifically, when the effective flame length of the cuff flame burner unit is 100mm, the width of the main burner (the distance between the outermost nozzles of the main burner unit) is 50mm, and θ is 30 °, the distance between the center of the main burner unit and the center of the cuff flame burner unit is 75mm or less. Considering the preferable range of θ, the distance between the center of the main burner part and the center of the cuff burner part is preferably 60 to 110 mm. The effective flame length may be determined as the length from the combustion surface or the tapered surface of the region that reaches the ignition temperature of the gas or higher based on the measurement result of the flame temperature.

Fig. 4 is a schematic diagram showing a structure of a cuff flame burner unit according to another embodiment of the present invention. In this embodiment, the cuff flame burner unit 30 includes the cuff flame nozzle 32 having a diameter d, and the tip of the cuff flame nozzle 32 is provided at a position deeper than or equal to d from the surface of the tapered portion 42. The fuel gas discharged from the sleeve flame nozzle 32 is ignited in the space 33, and its flame (sleeve flame) is formed to extend outward beyond the surface of the tapered portion 42. By positioning the tip of the sleeve flame nozzle 32 at a position deep into the burner body 10 in this way, the above-described influence of the accompanying flow can be suppressed and the sleeve flame can be stably maintained even without using the surface burner. In the case where the cuff flame burner unit 30 includes a slit nozzle having a width d in the short side direction as the cuff flame nozzle 32, it is also preferable to provide the tip of the cuff flame nozzle 32 at a position deeper than or equal to d from the surface of the tapered portion 42. From the viewpoint of suppressing the influence of the accompanying flow, it is more preferable to set the tip of the cuff flame nozzle 32 at a position deeper by 2d or more from the surface of the tapered portion 42. On the other hand, if the tip of the sleeve fire nozzle 32 is set at a position deeper than 15d from the surface of the tapered portion 42, the flame temperature may be lowered. Therefore, the tip of the sleeve fire nozzle 32 is preferably located at a distance of not more than 15d, more preferably not more than 4d, from the surface 15d of the tapered portion 42.

[ Ejection velocity ]

As described above, according to the burner, even at a high ejection speed, the flame can be stably maintained without misfiring.

Here, the ejection velocity refers to the gas flow velocity in the straight pipe portions of the fuel gas nozzle and the air nozzle of the main burner portion, and is determined from the ejection velocity, which is the gas flow rate per unit time of a single nozzle/the nozzle cross-sectional area. In a nozzle having no straight tube portion, the cross-sectional area of the nozzle outlet portion is considered as the nozzle cross-sectional area. In a burner having many nozzles or many holes, when a conical portion is provided in front of the nozzles as illustrated in fig. 10, the total flow rate of the sum of the fuel gas and air discharged from the burner is divided by the cross-sectional area of the outlet of the conical portion to determine the discharge velocity of the burner.

Preferably, the ejection speed of the fuel gas is substantially equal to the ejection speed of the combustion air. Specifically, the ratio of the ejection speed of the fuel gas to the ejection speed of the combustion air (ejection flow rate ratio) is preferably 0.8 to 1.2. In the burner having a conical cone, the above-mentioned ratio of the discharge flow rate in the nozzle hole portion near the cone is preferably 0.8 to 1.2.

[ fuel gas flow rate ratio ]

The ratio of the fuel gas flow rate in the main burner portion to the fuel gas flow rate in the cuff burner portion (hereinafter, also referred to as "fuel gas flow rate ratio") greatly affects the stability and heating capability of the flame. Therefore, the ignition furnace preferably includes flow rate adjusting means capable of independently adjusting the flow rate of the fuel gas in the main burner unit and the flow rate of the fuel gas in the pilot burner unit. The combustion air amount can be determined by multiplying the fuel gas flow rate by the theoretical air amount of the fuel gas and the air ratio. The ignition furnace preferably includes flow rate adjusting means capable of independently adjusting the flow rate of the combustion air of the main burner unit and the flow rate of the combustion air of the pilot burner unit. As the flow rate adjusting means, a flow rate adjusting valve or the like can be used.

When the total of the fuel gas flow rate in the main burner unit and the fuel gas flow rate in the cuff burner unit is 100%, if the fuel gas flow rate in the cuff burner unit is less than 15%, the flame temperature is significantly reduced by the accompanying flow, and a misfire may occur in the main burner. Therefore, it is preferable that the fuel gas flow rate in the cuff burner unit is 15% or more, in other words, the ratio of the fuel gas flow rate in the main burner unit to the fuel gas flow rate in the cuff burner unit is 85: 15 or less. On the other hand, if the fuel gas flow rate of the cuff flame burner portion is too high, the flame of the main burner portion becomes small although the flame is stabilized, and thus the heating capacity is lowered. Therefore, it is preferable that the fuel gas flow rate in the cuff burner unit is 30% or less, in other words, the ratio of the fuel gas flow rate in the main burner unit to the fuel gas flow rate in the cuff burner unit is 70: more than 30.

(evaluation of Limit discharge Rate)

Next, in order to confirm the capability of the above burner, the limit ejection speed at which the flame can be held without blow-out was evaluated using the following 3 types of burners. The specifications of each burner are shown in table 1.

(burner 1) conventional general premix burner shown in fig. 10

(burner 2) burner shown in fig. 1 of patent document 1

(burner 3) burner of the construction shown in FIGS. 1 to 3

The combustor 1 is a conventional premix combustor having a cross-sectional shape shown in fig. 10. The nozzle shape of the burner 1 is a slit-shaped nozzle having a length of 1 m. Here, the length of the nozzle means the length of the slit nozzle in the longitudinal direction, that is, the length of the nozzle in the direction perpendicular to the paper surface of fig. 10. The width of the slit-shaped nozzle was 10mm at the linear portion and 100mm at the tip of the conical portion. Here, the width of the nozzle is a width of an opening of the slit in a cross section perpendicular to the longitudinal direction of the slit, that is, a width in the left-right direction of the paper surface of fig. 10. Therefore, the total cross-sectional area of the linear portion of the slit nozzle was 100cm 2.

The burner 2 is a linear burner having a length of 1m and provided with a plurality of nozzles having a cross-sectional shape shown in fig. 1 of patent document 1. The nozzles are arranged in 60 groups in a straight line in the longitudinal direction of the linear burner. The nozzle diameter of the fuel gas nozzle of the main burner part of the burner 2 was 6 mm. The nozzle diameter of the air nozzle of the main burner part of the burner 2 is the same as the nozzle diameter of the fuel gas nozzle. In the combustor described in patent document 1, since 2 fuel gas nozzles are provided for each 1 combustor, the number of fuel gas nozzles is 120. Therefore, the total cross-sectional area of the fuel gas nozzles of the main burner part of the burner 2 was 33.8cm 2. Since the flame is unstable when 50 sets of nozzles are arranged in the combustor 2, 60 sets of nozzles are provided to stabilize the flame.

The burner 3 is a linear burner having a length of 1m and including a plurality of nozzles having the cross-sectional shapes shown in fig. 1 to 3. The nozzles are arranged in 50 groups in a straight line in the longitudinal direction of the linear burner. The nozzle diameter of the fuel gas nozzle of the main burner part of the burner 3 was 6 mm. The nozzle diameter of the air nozzle of the main burner portion of the burner 3 is the same as the nozzle diameter of the fuel gas nozzle. As shown in fig. 2, since the combustor includes 1 fuel gas nozzle per 1 combustor, the number of fuel gas nozzles is 50. Therefore, the total cross-sectional area of the fuel gas nozzles of the main burner part of the burner 3 was 14.1cm 2.

table 1 shows the ratio (fuel gas flow rate ratio) of the flow rate of the fuel gas in the main burner portion and the flow rate of the fuel gas in the pilot burner portion of each of the burners 2 and 3.

[ Table 1]

TABLE 1

Ratio of flow rate of fuel gas in main burner unit to flow rate of fuel gas in cuff burner unit

The above evaluation was carried out using an experimental burner having a combustion space of 1.4m × 1.4m × 0.4m in size. The flow rate of the fuel gas and the combustion air was increased while keeping the flow rate ratio constant, and the limit blowout flow rate at which the flame could be maintained without blowing out the flame was measured.

Here, as the fuel gas, M gas (a mixed gas of coke oven gas and blast furnace gas) which is a by-product gas in an iron plant is used. The main component of the M gas is H2: 26.5%, CO: 17.6%, CH 4: 9.1%, N2: 30.9 percent.

The measurement results are shown in fig. 5. In the burner 1, if the flow velocity in the straight portion of the nozzle exceeds 30Nm/s, the flame cannot be maintained and blowout occurs. The flow velocity in the straight portion is 3Nm/s when converted to the flow velocity at the tip of the conical portion. In the burner 2, if the flow rate in the nozzle straight tube portion exceeds 40Nm/s, the flame cannot be maintained and blowout occurs. On the other hand, in the burner 3, even if the flow velocity in the nozzle portion exceeds 40Nm/s and the flame is discharged, the flame is stable, and if it exceeds 100Nm/s, the flame becomes unstable and the blowout occurs at 120 Nm/s.

From the above results, it is understood that the burner of the present invention can stably burn even at a significantly higher discharge flow rate than the conventional burner. In the case where the burner of the present invention is actually used in industrial applications or the like, since there is a possibility that the risk of blowout may be increased due to operation variations of the supply system when used in the vicinity of the blowout limit flow rate, it is preferable to use the burner so that the flow rate is smaller than the blowout limit flow rate. An example of an actual commonly used flow rate is also shown in fig. 5.