EP0976977A1 - Brûleur à charbon pulvérisé - Google Patents

Brûleur à charbon pulvérisé Download PDF

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Publication number
EP0976977A1
EP0976977A1 EP98114219A EP98114219A EP0976977A1 EP 0976977 A1 EP0976977 A1 EP 0976977A1 EP 98114219 A EP98114219 A EP 98114219A EP 98114219 A EP98114219 A EP 98114219A EP 0976977 A1 EP0976977 A1 EP 0976977A1
Authority
EP
European Patent Office
Prior art keywords
pulverized coal
burner
nozzle
air
furnace
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP98114219A
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German (de)
English (en)
Other versions
EP0976977B1 (fr
Inventor
Toshimitsu Nagasaki R & D Center of Mits Ichinose
Akiyasu Nagasaki R & D Center of Mits Okamoto
Takeshi Nagasaki R & D Center of Mits Suzuki
Masaharu Choryo Engineering Co. Ltd. Oguri
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to EP02006378A priority Critical patent/EP1219893B1/fr
Priority to EP19980114219 priority patent/EP0976977B1/fr
Priority to EP02006379A priority patent/EP1219894B1/fr
Publication of EP0976977A1 publication Critical patent/EP0976977A1/fr
Application granted granted Critical
Publication of EP0976977B1 publication Critical patent/EP0976977B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D1/00—Burners for combustion of pulverulent fuel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C5/00—Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus
    • F23C5/08—Disposition of burners
    • F23C5/32—Disposition of burners to obtain rotating flames, i.e. flames moving helically or spirally
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D2201/00—Burners adapted for particulate solid or pulverulent fuels
    • F23D2201/10—Nozzle tips
    • F23D2201/101—Nozzle tips tiltable
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D2201/00—Burners adapted for particulate solid or pulverulent fuels
    • F23D2201/20—Fuel flow guiding devices

Definitions

  • the present invention relates to a pulverized coal burning boiler for generating a steam for a power plant, a factory and the like.
  • Reference numeral 01 denotes a boiler furnace main body, and a plurality of burner main bodies 02 are disposed in a vertical direction at each of four corners therein.
  • the burner main body 02 is constituted by a combustion air nozzle 03, an auxiliary air nozzle 04, a pulverized coal mixture nozzle 05, etc. and a pulverized coal mixture 10, a combustion air 11, a main burner air 12 and an additional air 13 are supplied thereto through a pulverized coal mixture feeding pipe 06, an air feeding duct 07, a main burner air duct 08 and an additional air duct 09.
  • Reference numeral 14 denotes an additional air nozzle disposed at an upper position
  • reference numeral 15 denotes a furnace
  • a pulverized coal flame 16 is formed in the furnace 15.
  • Reference numeral 17 denotes an air adjusting damper assembled in each of the burner main bodies 02
  • reference numeral 18 denotes an imaginary circle imagined in the furnace 15 for explanation purpose
  • reference numeral 19 denotes a fire vortex formed in the furnace 15.
  • a coal fed to a coal pulverizing apparatus (not shown) is finely pulverized, is mixed with a carrying air (a hot air) simultaneously fed so as to form the pulverized coal mixture 10, and is fed to the pulverized coal mixture nozzle 05 provided in the burner main body 02 through the pulverized coal mixture feeding pipe 06.
  • the burner main bodies 02 are provided at four corners of the boiler furnace main body 01, and plural sets of burners, each burner comprising the combustion air nozzle 03, the pulverized coal mixture nozzle 05 provided in a center portion thereof and the auxiliary air nozzle 04 provided above and below the combustion air nozzle 03, are installed within each of the burner main bodies 02. (Here, there is a case that the burner main bodies 02 are provided not only at four corners of the boiler furnace main body 01, but also on a wall surface as shown in Fig. 9.)
  • Each set of these nozzles that is, the combustion air nozzle 03, the auxiliary air nozzle 04 and the pulverized coal mixture nozzle 05, is installed in such a manner as to blow the pulverized coal mixture 10 and the main burner air 12 in a tangential direction of an imaginary circle 18 which is set at a center portion on a horizontal cross section of the boiler furnace main body 01.
  • a construction drawing of the conventional pulverized coal mixture nozzle 05 will be shown in Fig. 10.
  • the additional air nozzles 14 are provided at four corners above the burner main bodies 02 in the boiler furnace main body 01.
  • the additional air nozzle 14 is installed in such a manner as to blow the additional air 13 in a tangential direction of an imaginary circle 18 which has a same diameter as that of the imaginary circle 18 with respect to the respective nozzles 03, 04 and 05 of the burner main body 02 and is set at a center portion on a horizontal cross section of the boiler furnace main body 01.
  • the pulverized coal mixture 10 supplied to the pulverized coal mixture nozzle 05 provided in the burner main body 02 is blown into the furnace 15 from the nozzle 05.
  • the combustion air 11 is fed through the air feeding duct 07 by a feeding apparatus (not shown), and is branched into the main burner air 12 and the additional air 13 before entering the burner main body 02.
  • the main burner air 12 is fed to the burner main body 02 through the main burner air duct 08, and is blown into the furnace 15 from the combustion air nozzle 03 and the auxiliary air nozzle 04.
  • An amount of the main burner air 12 is generally set to be equal to or less than a stoichiometric mixture ratio of an amount of the pulverized coal blown as the pulverized coal mixture 10 so as to hold a portion of the furnace 15 below the additional air nozzle 14 in a reducing atmosphere, thereby reducing a nitrogen oxide (hereinafter referred to as to NOx for short) generated by burning the pulverized coal.
  • NOx nitrogen oxide
  • the main burner air 12 and the branched additional air 13 are fed to the additional air nozzle 14, and blown into the furnace 15 so as to be used for completing a burning of a combustible portion left in the combustion gas due to the reduction combustion.
  • the pulverized coal mixture 10 blown into the furnace 15 from the four corners of the boiler furnace main body 01 is ignited by an ignition source (not shown), and forms the pulverized coal flame 16.
  • the pulverized coal flame 16 becomes a swirling flow so as to form the fire vortex 19, and ascend in the furnace 15 with swirling, thereby performing a swirling combustion.
  • the amount of the main burner air 12 blown from the burner main body 02 is equal to or less than the stoichiometric mixture ratio of the amount of the pulverized coal blown as the pulverized coal mixture 10 from the pulverized coal mixture nozzle 05, so that the portion of the furnace 15 below the additional air nozzle 14 portion becomes a reducing atmosphere.
  • a combustion exhaust gas generated by burning the pulverized coal becomes to contain a combustible portion, however, NOx in the combustion exhaust gas generated by burning the pulverized coal is reduced so that an intermediate product such as NH3 and HCN is generated in place thereof.
  • the combustion exhaust gas containing the combustible portion is blown with the additional air 13 in the additional air nozzle 14 portion, and the combustion thereof is completed till an outlet of the furnace.
  • the conventional pulverized coal burner Since a blowing momentum of the pulverized coal mixture 10 blown from the pulverized coal mixture nozzle 05 becomes large when a capacity of the burner becomes large, a degree of collision of the pulverized coal flame 16 with side wall of the furnace 15 is increased, and in addition thereto, it becomes difficult to secure a stable ignitability. As a result, the conventional pulverized coal burner has a disadvantage that it is hard to increase the capacity.
  • the increase of the number of the burners is performed by increasing a number of stages of the burners since the number of the burners on the horizontal cross section of the boiler furnace main body 01 is fixed, however, in this manner, a height of the boiler is increased, so that a cost for constructing the boiler is increased.
  • An object of the present invention is to solve the problems in the conventional one mentioned above, and to provide a pulverized coal burner structured such that a pulverized coal mixture is supplied in a tangential direction of an imaginary circle in a horizontal plane of a furnace so that a concentration of the pulverized coal mixture is made rich on a central side of the imaginary circle and it becomes possible to increase a capacity of the pulverized coal burner.
  • Another object of the invention is to solve the problem in the prior art that the entire furnace is heightened and the cost is increased, accompanying with a trial to provide the additional air port in the upper portion of the furnace so as to disperse the amount of air to reduce the amount of air in the burner windbox portion for reducing the value of NOx, and the problem that the thermal load of the burner portion becomes high and the slag (molten ash) is increasingly attached to the wall of the furnace so as to cause an obstruction in heat transmission and combustion, accompanying with a trial to reduce the height of the burner so as to restrict the height of the entire furnace, thereby providing a preferable burner portion having a high practicality.
  • the invention is made for achieving the objects mentioned above, and provides a pulverized coal burner for supplying a pulverized coal mixture in a tangential direction of an imaginary circle in a horizontal plane of a furnace so as to be burned, characterized in that a rich/lean separating body is arranged within a pulverized coal mixture nozzle so that the pulverized coal mixture becomes rich on a central side of the imaginary circle.
  • the pulverized coal mixture blown from the pulverized coal mixture nozzle is blown such that an outer peripheral side of a fire vortex formed in the central portion of the furnace is made lean and an inner portion side thereof is made rich, and a supply amount of a combustion air supplied from a combustion air nozzle, for example, provided on the outer periphery of the pulverized coal mixture nozzle is increased on the lean pulverized coal mixture side, thereby the pulverized coal flame is prevented from colliding with the wall surface of the furnace, so that a slagging is reduced and it becomes possible to make a capacity of the pulverized coal burner larger.
  • the invention provides a pulverized coal burner, characterized in that a mixture injecting port of a front end of the pulverized coal mixture nozzle is divided into upper and lower portions and a means for introducing an ignition promoting air is provided between the divided injecting ports. Accordingly, an ignition stability of the pulverized coal flame is improved by dividing the pulverized coal mixture blown from the pulverized coal mixture nozzle into the upper and lower directions so as to reduce to half an amount of the pulverized coal mixture blown from one of the directions thereof and by blowing a high temperature combustion air between the pulverized coal mixtures flown from two directions, thereby making it possible to increase a capacity of the pulverized coal burner.
  • the invention provides a pulverized coal burner for supplying a pulverized coal mixture in a tangential direction of an imaginary circle in a horizontal plane of a furnace so as to be burned, characterized in that a pulverized coal mixture nozzle is made eccentric with respect to an air nozzle so that the pulverized coal mixture becomes rich on a central side of the imaginary circle.
  • an axis of the pulverized coal mixture nozzle and an axis of the air nozzle are moved and shifted to be eccentric with each other so that a concentration of the pulverized coal of the pulverized coal mixture blown to an outer peripheral side of a fire vortex (near the wall surface of the furnace) formed in the furnace from the pulverized coal mixture nozzle is reduced and a concentration of the pulverized coal blown to an inner portion side of the fire vortex becomes rich, thereby the pulverized coal flame is prevented from colliding with the furnace wall and an amount of an air near the inner wall surface of the furnace is increased to form an oxidation atmosphere. Therefore, the molten ash is prevented from attaching by increasing an ash melting point.
  • the invention provides a pulverized coal burner, characterized in that a means for applying a swirl to a combustion air supplied from an outer periphery of the pulverized coal mixture nozzle is provided. Accordingly, an ignition stability with an increased capacity of a burner, a flame stability at a time of load changes, a short flame and a lowness of soot and dust can be secured by applying a swirl to the combustion air and by using, for example, a combined flame stabilizer, if necessary.
  • the invention provides a pulverized coal burner, characterized in that a means for directing a front end portion of the burner in vertical and lateral directions is provided. Accordingly, a position of the fire vortex can be changed by making the structure capable of changing the nozzle direction in the vertical and lateral directions, so that a distribution of the thermal load in the furnace can be adjusted.
  • the invention provides a pulverized burner characterized in comprising a burner having an increased width and a reduced height so as to effect in a high thermal load combustion of fuel in a narrow area, a separately provided additional air port disposed above the burner, a twist plate disposed within a pulverized fuel pipe for biasing a pulverized fuel to an inner side of the furnace and a combustion secondary air injection port for increasing an amount of air close to a furnace wall side by increasing an opening area close to the furnace wall side.
  • the height of the burner is reduced in correspondence that the width of the burner is increased, thereby performing a high thermal load combustion for burning the fuel at the narrow area
  • the separately provided additional air port is arranged above the burner so as to reduce a generation of NOx in the burner portion
  • the twist plate disposed within the pulverized fuel pipe biases the pulverized fuel to the inner side of the furnace
  • the opening area of the combustion secondary air injection port is increased in the portion close to the wall side of the furnace so as to increase the amount of the air close to the wall side of the furnace. Therefore, a melting point of the slag (the molten ash) is increased and the molten slag is prevented from attaching to the furnace wall in the high thermal load.
  • reference numerals 101 to 119 correspond to the reference numerals 01 to 19 in the conventional structure, a description will be simplified as much as possible, and an ignition promoting air hole 120 provided in a pulverized coal mixture nozzle 105, an ignition promoting air chamber 121, an ignition promoting air chamber inlet port 122, a guiding plate 123, a rich/lean separating body 124, etc. will be described in detail.
  • a coal fed to a coal pulverizing apparatus (not shown) is pulverized there, is mixed with a carrying air (a hot air) simultaneously fed so as to form a pulverized coal mixture 110, and is fed to a pulverized coal mixture nozzle 105 provided in a burner main body 102 through a pulverized coal mixture transporting pipe 106.
  • the pulverized coal mixture nozzle 105 is constituted by a pulverized coal mixture pipe connected to the pulverized coal mixture transporting pipe 106, and a mixture injecting nozzle attached to a front end thereof.
  • the rich/lean separating body 124 is provided within the pulverized coal mixture pipe near an inlet of the mixture injecting nozzle.
  • An injecting port of the mixture injecting nozzle is branched into upper and lower directions with an optional angle, for example, an angle of 10 degrees to 30 degrees in one direction with respect to a horizontal axis, and the ignition promoting air chamber 121 is provided between the upper and lower injecting ports.
  • the combustion air nozzle 103 is provided on an outer periphery of the mixture injecting nozzle, and blows the main burner air 112 into the furnace 114 from a blowing port constituted by the mixture injecting nozzle and the combustion air nozzle 103.
  • the pulverized coal mixture 110 fed to the pulverized coal mixture nozzle 105 flows in a biased manner at the pulverized coal mixture pipe outlet portion by the rich/lean separating body 124.
  • the pulverized coal mixture 110 is structured such that a concentration of the pulverized coal becomes lean on the rich/lean separating body 124 attaching side at the mixture injecting nozzle outlet port due to a force of inertia and a concentration of the pulverized coal on the opposite side not attaching the same becomes rich.
  • a blowing port of the main burner air 112 formed by the mixture injecting nozzle and the combustion air nozzle 103 is formed wider on the lean pulverized coal side of the pulverized coal mixture 110 and narrower on the rich pulverized coal side.
  • a portion, blown into a central side of the fire vortex 119, of the pulverized coal mixture 110 injected from the mixture injecting nozzle becomes to an upstream side of the swirling combustion flow, so that said portion is in a state of easily igniting having a large radiant heat from the adjacent pulverized coal flame 116.
  • the pulverized coal mixture 110 is set such that the rich pulverized coal side is blown to the central side of the fire vortex 119.
  • a new device is further added to the mixture injecting nozzle in order to improve an ignition stability of the pulverized coal flame 116.
  • the mixture injecting nozzle is structured such that the injecting port thereof is branched to the upper and lower directions with an optional angle, the ignition promoting air chamber 121 is provided between the upper and lower injecting ports, and the guiding plate 123 and the ignition promoting air chamber inlet hole 122 are provided in the inlet of said air chamber 121.
  • the ignition promoting air chamber 121 is formed by disposing a plate on a side facing to the the furnace 115, and the ignition promoting air hole 120 is bored on the plate so as to blow the main burner air 112, which has flown to the ignition promoting air chamber 121 through the ignition promoting air chamber inlet hole 122, between two pulverized coal mixtures 110 injected from the mixture injecting nozzle.
  • the main burner air 112 blown from the ignition promoting air hole 120 prevents flows of the pulverized coal mixture 110 blown from two injection ports of the mixture injecting nozzle from joining to togetherer earlier, and since a temperature of the main burner air 112 is high to be about 300 °C in comparison that a temperature of the pulverized coal mixture 110 is generally 100 °C or less (in many cases, about 80 °C), an effect that a generation of a volatile matter between the pulverized coal mixtures 110 is promoted can be obtained, so that an igniting stability of the pulverized coal flame 116 can be secured.
  • Reference numeral 201 denotes a pulverized coal mixture nozzle, and a secondary air nozzle 202 and a tertiary air nozzle 203 are arranged in a periphery thereof.
  • Reference numeral 204 denotes a swirler, arranged at an upstream position of an outlet of the tertiary air nozzle 203.
  • Reference numeral 205 denotes a hollow core provided at an upstream position of an outlet of the pulverized coal mixture nozzle 201.
  • Reference numeral 206 denotes a tilt bar connected to a spherical connecting portion 210 at a front end portion of each of the nozzles 201, 202 and 203, and each of the nozzles 201, 202 and 203 can be directed in a vertical direction around the connecting portion 210 by moving the tilt bar 206 laterally as shown by arrows in the drawing.
  • a tilt bar 206 connected to the tertiary air nozzle 203 operates a motion in the vertical direction of the tertiary air nozzle 203, and the pulverized coal mixture nozzle 201 and the secondary air nozzle 202 are interlocked by a supporting rod 207 and the tilt bar 206 is connected to the secondary air nozzle 202, thereby the pulverized coal mixture nozzle 201 together with the secondary air nozzle 202 change the direction in the vertical direction.
  • reference numeral 208 denotes a flame stabilizer, arranged at the front end of each of the nozzles 201, 202 and 203, for serving a flame stabilizing effect.
  • a concentration distribution of the pulverized coal in the pulverized coal mixture injecting flow is made rich on the peripheral side, and by the flame stabilizer 208, an ignition stability is increased.
  • the injecting direction of the pulverized coal mixture, the secondary air and the tertiary air can be changed in the vertical and lateral directions by moving the tilt bar 206 in the front and rear direction.
  • the pulverized coal mixture nozzle and the secondary air nozzle are interlocked to be fixed together by the supporting rod 107, the injecting flow therefrom is directed in the same direction.
  • FIG. 6(a) shows a cross section of a boiler
  • Fig. 6(b) shows a burner windbox arranged at each of four corners of Fig. 6(a) and a separately provided additional air port arranged above the burner windbox
  • Fig. 6(c) shows a front of one of fuel nozzles of Fig. 6(b)
  • Fig. 6(d) shows a pulverized fuel pipe for supplying a fuel to the fuel nozzle of Fig. 6(c).
  • reference numeral 301 denotes a cross section of a furnace, a periphery of which is surrounded by a wall of the furnace in a square shape, and a burner windbox 302 is arranged at each of four corners thereof.
  • Reference numeral 303 denotes a flame and reference numeral 304 denotes a section close to the furnace wall.
  • Fig. 6(b) shows a detail of the burner windbox 302 structured in five stages. That is, auxiliary air portions 305b and 305a are arranged at upper and lower ends, a first stage fuel nozzle portion 306a is placed on the lower end auxiliary air portion 305a, a second stage fuel nozzle portion 306b is placed thereon via an oil nozzle portion 307a, and a third stage fuel nozzle portion 306c, a fourth stage fuel nozzle portion 306d and a fifth stage fuel nozzle portion 306e are likewise placed via an oil nozzle portion 307b, an oil nozzle portion 307c and an oil nozzle portion 307d, respectively, up to the upper end auxiliary air portion 305b overlappedly with no gap being placed between each of them.
  • the fifth stage fuel nozzle portion 306e is constituted by a fuel injecting port 308, disposed in a central portion, for injecting a pulverized fuel and a carrying air, and a combustion secondary air injecting port 309, surrounding a periphery thereof, for injecting a secondary air.
  • the other fuel nozzle portions 306a to 306d are also constituted in the same manner as that of the fifth stage fuel nozzle portion 306e. Further, the pulverized fuel and the carrying air to be injected from the fuel injecting port 308 are carried through the pulverized fuel pipe 310 shown in Fig. 6(d) and reach the fuel injecting port 308.
  • the furnace cross section 301 the periphery of which is surrounded by the furnace wall in a square shape, is provided with the burner windbox 302 at each of four corners, however, the first to fifth stage fuel nozzle portions 306a to 306e, which constitute a main portion of the burner disposed here, and the respective oil nozzle portions 307a to 307d disposed therebetween are structured with an elongated horizontal width and a reduced height.
  • the horizontal width is made to be 1 to 1.5 times the height, however, in this embodiment, the shape is formed such that the horizontal width is made to be about three times the height, and the height is reduced corresponding to the horizontal width, so elongated, so that the total height of the five stages is made lower.
  • an additional air port 314 is provided above the burner windbox 302 constructed in five stages overlappedly, and the position of the additional air port 314 is set to be substantially same as the height at which the uppermost element of the conventional general fuel nozzle portions is arranged.
  • the hatched fifth stage fuel nozzle portion 306e in the overlapped body is structured such that the front shape is constituted, as shown in Fig. 1(c), by the fuel injecting port 308, arranged on the inner side, for injecting the pulverized fuel and the carrying air, and the combustion secondary air injecting port 309, surrounding the fuel injecting port 308, for injecting the secondary air, however, the fuel injecting port 308 on the inner side is biased rightward as seen in the drawing in the fuel secondary air injecting port 309, surrounding the fuel injecting port 308.
  • the structure is such that an opening portion of the fuel secondary air injecting port 309 is broader in a portion close to the furnace wall and a portion close to the center is narrower by that degree, so that the combustion secondary air is injected more to the portion close to the furnace wall by increasing an air flow area in the portion close to the furnace wall, and a lean fuel flame 311 is formed within the section 304 close to the furnace wall on the furnace wall side of the flame 303 around the center.
  • a block 313 is disposed at a portion at which a flow of the pulverized fuel and the carrying air curves, so that the pulverized fuel etc. is biased outwardly of the curved portion above the block by a centrifugal force and then, by use of a twist plate 312 which is arranged so as to twist a flow 90 degrees, the rich pulverized fuel etc. is biased to the inner side of the furnace and the concentration thereof in the portion close to the furnace wall is reduced.
  • the pulverized fuel flows with an increased area for receiving a radiation heat from the flame so as to promote the ignition by expanding the width of the so-called burner portion comprising the first to fifth stage fuel nozzle portions 306a to 306e and by reducing the height of the burner, and a combustion is done in a narrow area, thereby elevating an atmospheric temperature and improving a combustibility.
  • the additional air port 314 installed separately from the burner portion is provided at the height position substantially corresponding to the uppermost stage of the conventional general burners and a sufficient amount of air corresponding to about 30 to 40 % of all the combustion air is supplied there, thereby making the burner portion a reducing area with a shortage of air, and further, reduction of the height of the entire burner portion secures a residence time for the pulverized fuel and the combustion gas moving from the burner portion to the additional air port 314, so that the NOx reducing area is further strengthened in addition to the promotion of ignition and the increase of the atmospheric temperature.
  • twist plate 312 and the block 313 disposed inside the pulverized fuel pipe 310 first bias the pulverized fuel within the cross section of the pulverized fuel pipe 310 by a centrifugal force due to the block 313 and the curve of the pulverized fuel pipe 310, and next the twist plate 312 twists the pulverized fuel in the rich area to be injected to the inner side of the furnace, and reduces the pulverized fuel amount near the furnace wall, so that amount of ash content is reduced also.
  • a compound having a low melting temperature is formed in a state that the peripheral atmosphere is short of air and a bonding force is increased, so that an air amount close to the furnace wall where the opening area is broad is increased, and such component is prevented from occurring with the sufficient air.
  • the concentration of the pulverized coal of the pulverized coal mixture blown into the furnace is made rich in the portion blowing to the central side of the fire vortex and lean in the portion blowing to the outer peripheral side, thereby preventing the pulverized coal flame from colliding with the wall surface of the furnace, and the slagging can be reduced and the capacity of the pulverized coal burner can be enlarged.
  • the axis of the pulverized coal mixture nozzle and the axis of the air nozzle are shifted to be eccentric with each other so that the concentration of the pulverized coal in the pulverized coal mixture blown from the pulverized coal mixture nozzle to the portion on the outer peripheral side of the fire vortex formed in the furnace, that is, the portion close to the wall surface of the furnace is made lean and the concentration of the pulverized coal blown to the portion the inner side of the fire vortex is made rich, thereby the pulverized coal flame is prevented from colliding with the furnace wall and the air amount near the furnace wall is increased so as to form an oxidation atmosphere and increase the ash melting point, and the molten slag is prevented from attaching.
  • the structure for freely changing the direction of the front end portion of the burner in the vertical and lateral directions is employed, the optimum position of the nozzle opening is selected in accordance with the condition, the position of the fire vortex can be changed and the distribution of the thermal load within the furnace can be adjusted.
  • the burner is structured such as to have an increased width and a reduced height so as to burn a fuel at a narrow area to effect a high thermal load combustion, an separately provided additional air port disposed above the burner, a twist plate disposed within a pulverized fuel pipe for biasing the pulverized fuel to an inner side of the furnace and a combustion secondary air injection port for increasing an amount of air close to the furnace wall side by increasing an opening area close to the furnace wall side, thereby the height of the entire burner is reduced so that a high thermal load combustion for burning the fuel at the narrow area is effected and the combustion air is consumed in the separately provided additional air port arranged above the burner, so that the combustion air is throttled in the burner portion so as to reduce a generation of NOx, and further the twist plate biases the pulverized fuel flowing within the pulverized fuel pipe to the inner side of the furnace, and the combustion secondary air injection port having the opening area enlarged in the portion close to the furnace wall increases the amount
  • the pulverized coal burner in which the height of the burner is restricted, the manufacturing cost is reduced, the generation of NOx in the burner portion is reduced, the burning performance is promoted by the high thermal load combustion so as to reduce the unburned component, and the molten ash is easily taken off from the furnace wall, can be obtained, so that the apparatus having a practicality, a suitability and a high reliability can be obtained.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
EP19980114219 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé Expired - Lifetime EP0976977B1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP02006378A EP1219893B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé
EP19980114219 EP0976977B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé
EP02006379A EP1219894B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP19980114219 EP0976977B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé

Related Child Applications (4)

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EP02006379A Division EP1219894B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé
EP02006378A Division EP1219893B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé
EP02006378.0 Division-Into 2002-03-21
EP02006379.8 Division-Into 2002-03-21

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EP0976977A1 true EP0976977A1 (fr) 2000-02-02
EP0976977B1 EP0976977B1 (fr) 2003-03-26

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EP19980114219 Expired - Lifetime EP0976977B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé
EP02006378A Expired - Lifetime EP1219893B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé
EP02006379A Expired - Lifetime EP1219894B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé

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EP02006379A Expired - Lifetime EP1219894B1 (fr) 1998-07-29 1998-07-29 Brûleur à charbon pulvérisé

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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001077583A1 (fr) * 2000-04-12 2001-10-18 Saar Energie Gmbh Procede mis en oeuvre pour la combustion d'un combustible pulverise dans une chaudiere d'une centrale
DE10019114A1 (de) * 2000-04-18 2001-10-25 Bbp Energy Gmbh Feuerung und Verfahren zur Verbrennung von Kohlenstaub
EP1306614A1 (fr) * 2000-08-04 2003-05-02 Babcock-Hitachi Kabushiki Kaisha Bruleur a combustible solide et procede de combustion au moyen d'un bruleur a combustible solide
FR2848641A1 (fr) * 2002-12-11 2004-06-18 Alstom Switzerland Ltd Systeme de chauffe indirecte avec valorisation des particules de combustible ultra fines
JP2013113501A (ja) * 2011-11-29 2013-06-10 Mitsubishi Heavy Ind Ltd バーナおよびこれを備えたボイラ
CN103322561A (zh) * 2013-07-04 2013-09-25 哈尔滨锅炉厂有限责任公司 双腔深度分级煤粉燃烧装置
CN104494034A (zh) * 2014-12-26 2015-04-08 东莞市秋天塑胶材料有限公司 Pvc发泡炉供热系统
JP2015096789A (ja) * 2013-11-15 2015-05-21 三菱日立パワーシステムズ株式会社 ボイラ
US20160356489A1 (en) * 2011-04-01 2016-12-08 Mitsubishi Heavy Industries, Ltd. Combustion burner, solid-fuel-combustion burner, solid-fuel-combustion boiler, boiler, and method for operating boiler
WO2017108484A1 (fr) * 2015-12-22 2017-06-29 Siemens Aktiengesellschaft Brûleur principal coudé
CN107083258A (zh) * 2017-06-23 2017-08-22 航天长征化学工程股份有限公司 一种气化烧嘴装置
RU2635947C2 (ru) * 2016-04-12 2017-11-17 федеральное государственное автономное образовательное учреждение высшего образования "Южно-Уральский государственный университет" (национальный исследовательский университет) Котел и способ его работы
CN108397766A (zh) * 2018-03-01 2018-08-14 中国神华能源股份有限公司 锅炉以及锅炉的配风方法
JP2018132278A (ja) * 2017-02-17 2018-08-23 三菱日立パワーシステムズ株式会社 燃焼バーナ及びこれを備えたボイラ
EP3438533A1 (fr) * 2017-07-31 2019-02-06 General Electric Technology GmbH Ensemble de buse de charbon pour un appareil de génération de vapeur
CN109458612A (zh) * 2017-09-06 2019-03-12 晋能电力集团有限公司 一种煤粉气化燃烧的低氮燃烧装置及燃烧方法
CN113790440A (zh) * 2021-10-26 2021-12-14 西安热工研究院有限公司 一种煤粉燃烧器的一次风喷口

Families Citing this family (6)

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Publication number Priority date Publication date Assignee Title
US20090305179A1 (en) * 2005-06-03 2009-12-10 Zakrytoe Aktsionernoe Obschestvo "Otes-Sibir' Steam-Generator Furnace
CN101598333B (zh) * 2009-06-30 2012-09-26 上海锅炉厂有限公司 一种低氮氧化物排放煤粉切向燃烧装置
JP2011127836A (ja) * 2009-12-17 2011-06-30 Mitsubishi Heavy Ind Ltd 固体燃料焚きバーナ及び固体燃料焚きボイラ
JP5374404B2 (ja) 2009-12-22 2013-12-25 三菱重工業株式会社 燃焼バーナおよびこの燃焼バーナを備えるボイラ
DE102010052464A1 (de) * 2010-11-24 2012-05-24 Ludwig Müller Dreh-Strom-Feuerung (DSF)
US9377191B2 (en) 2013-06-25 2016-06-28 The Babcock & Wilcox Company Burner with flame stabilizing/center air jet device for low quality fuel

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2343572A (en) * 1940-07-01 1944-03-07 Comb Eng Co Inc Finely divided fuel burner
DE890254C (de) * 1950-03-05 1953-09-17 Kohlenscheidungs Ges M B H Verfahren und Einrichtung zum Betrieb von Kohlenstaubfeuerungen fuer Hochleistungs-Dampfkessel
JPS58129105A (ja) * 1982-01-29 1983-08-02 Mitsubishi Heavy Ind Ltd 微粉炭焚タンゼンシヤルフアイアリングボイラの燃焼方法
EP0405294A2 (fr) * 1989-06-24 1991-01-02 Balcke-Dürr AG Dispositif de combustion des combustibles dans une chambre de combustion
US5315939A (en) * 1993-05-13 1994-05-31 Combustion Engineering, Inc. Integrated low NOx tangential firing system
US5329866A (en) * 1993-09-03 1994-07-19 The Babcock & Wilcox Company Combined low NOx burner and NOx port
JPH08178210A (ja) * 1994-12-26 1996-07-12 Mitsubishi Heavy Ind Ltd 旋回燃焼火炉用バーナ装置
US5593298A (en) * 1995-04-10 1997-01-14 Combustion Components Associates, Inc. Pollutant reducing modification of a tangentially fired furnace

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2343572A (en) * 1940-07-01 1944-03-07 Comb Eng Co Inc Finely divided fuel burner
DE890254C (de) * 1950-03-05 1953-09-17 Kohlenscheidungs Ges M B H Verfahren und Einrichtung zum Betrieb von Kohlenstaubfeuerungen fuer Hochleistungs-Dampfkessel
JPS58129105A (ja) * 1982-01-29 1983-08-02 Mitsubishi Heavy Ind Ltd 微粉炭焚タンゼンシヤルフアイアリングボイラの燃焼方法
EP0405294A2 (fr) * 1989-06-24 1991-01-02 Balcke-Dürr AG Dispositif de combustion des combustibles dans une chambre de combustion
US5315939A (en) * 1993-05-13 1994-05-31 Combustion Engineering, Inc. Integrated low NOx tangential firing system
US5329866A (en) * 1993-09-03 1994-07-19 The Babcock & Wilcox Company Combined low NOx burner and NOx port
JPH08178210A (ja) * 1994-12-26 1996-07-12 Mitsubishi Heavy Ind Ltd 旋回燃焼火炉用バーナ装置
US5593298A (en) * 1995-04-10 1997-01-14 Combustion Components Associates, Inc. Pollutant reducing modification of a tangentially fired furnace

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 007, no. 244 (M - 252) 28 October 1983 (1983-10-28) *
PATENT ABSTRACTS OF JAPAN vol. 096, no. 011 29 November 1996 (1996-11-29) *

Cited By (28)

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Publication number Priority date Publication date Assignee Title
WO2001077583A1 (fr) * 2000-04-12 2001-10-18 Saar Energie Gmbh Procede mis en oeuvre pour la combustion d'un combustible pulverise dans une chaudiere d'une centrale
DE10019114A1 (de) * 2000-04-18 2001-10-25 Bbp Energy Gmbh Feuerung und Verfahren zur Verbrennung von Kohlenstaub
EP1306614A1 (fr) * 2000-08-04 2003-05-02 Babcock-Hitachi Kabushiki Kaisha Bruleur a combustible solide et procede de combustion au moyen d'un bruleur a combustible solide
EP1306614A4 (fr) * 2000-08-04 2005-11-16 Babcock Hitachi Kk Bruleur a combustible solide et procede de combustion au moyen d'un bruleur a combustible solide
CZ303467B6 (cs) * 2000-08-04 2012-10-03 Babcock-Hitachi Kabushiki Kaisha Horák na pevné palivo a zpusob regulace spalování uskutecneného tímto horákem
FR2848641A1 (fr) * 2002-12-11 2004-06-18 Alstom Switzerland Ltd Systeme de chauffe indirecte avec valorisation des particules de combustible ultra fines
WO2004055435A1 (fr) * 2002-12-11 2004-07-01 Alstom (Switzerland) Ltd Systeme de chauffe indirecte avec valorisation des particules de combustible ultra fines
US20060254483A1 (en) * 2002-12-11 2006-11-16 Alstom (Switzerland) Ltd Indirect heating system with upgrading of ultra-fine fuel particles
US8316782B2 (en) 2002-12-11 2012-11-27 Alstom Technology Ltd Indirect heating system with upgrading of ultra-fine fuel particles
US20160356489A1 (en) * 2011-04-01 2016-12-08 Mitsubishi Heavy Industries, Ltd. Combustion burner, solid-fuel-combustion burner, solid-fuel-combustion boiler, boiler, and method for operating boiler
US20170045221A1 (en) * 2011-04-01 2017-02-16 Mitsubishi Heavy Industries, Ltd. Combustion burner, solid-fuel-combustion burner, solid-fuel-combustion boiler, boiler, and method for operating boiler
JP2013113501A (ja) * 2011-11-29 2013-06-10 Mitsubishi Heavy Ind Ltd バーナおよびこれを備えたボイラ
CN103322561A (zh) * 2013-07-04 2013-09-25 哈尔滨锅炉厂有限责任公司 双腔深度分级煤粉燃烧装置
JP2015096789A (ja) * 2013-11-15 2015-05-21 三菱日立パワーシステムズ株式会社 ボイラ
CN104494034A (zh) * 2014-12-26 2015-04-08 东莞市秋天塑胶材料有限公司 Pvc发泡炉供热系统
CN104494034B (zh) * 2014-12-26 2016-08-31 东莞市秋天塑胶材料有限公司 Pvc发泡炉供热系统
WO2017108484A1 (fr) * 2015-12-22 2017-06-29 Siemens Aktiengesellschaft Brûleur principal coudé
US10746395B2 (en) 2015-12-22 2020-08-18 Siemens Aktiengesellschaft Angled main burner
RU2635947C2 (ru) * 2016-04-12 2017-11-17 федеральное государственное автономное образовательное учреждение высшего образования "Южно-Уральский государственный университет" (национальный исследовательский университет) Котел и способ его работы
JP2018132278A (ja) * 2017-02-17 2018-08-23 三菱日立パワーシステムズ株式会社 燃焼バーナ及びこれを備えたボイラ
CN107083258A (zh) * 2017-06-23 2017-08-22 航天长征化学工程股份有限公司 一种气化烧嘴装置
CN107083258B (zh) * 2017-06-23 2024-03-26 航天长征化学工程股份有限公司 一种气化烧嘴装置
EP3438533A1 (fr) * 2017-07-31 2019-02-06 General Electric Technology GmbH Ensemble de buse de charbon pour un appareil de génération de vapeur
WO2019025289A1 (fr) * 2017-07-31 2019-02-07 General Electric Technology Gmbh Ensemble buse à charbon pour un appareil de production de vapeur
US11248785B2 (en) 2017-07-31 2022-02-15 General Electric Technology Gmbh Coal nozzle assembly for a steam generation apparatus
CN109458612A (zh) * 2017-09-06 2019-03-12 晋能电力集团有限公司 一种煤粉气化燃烧的低氮燃烧装置及燃烧方法
CN108397766A (zh) * 2018-03-01 2018-08-14 中国神华能源股份有限公司 锅炉以及锅炉的配风方法
CN113790440A (zh) * 2021-10-26 2021-12-14 西安热工研究院有限公司 一种煤粉燃烧器的一次风喷口

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EP0976977B1 (fr) 2003-03-26
EP1219894B1 (fr) 2006-04-05

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