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    • 4. 发明申请
    • A METHOD FOR REDUCING NITROGEN OXIDE EMISSIONS OF A BUBBLING FLUIDIZED BED BOILER AND AN AIR DISTRIBUTION SYSTEM OF A BUBBLING FLUIDIZED BED BOILER
    • 一种用于减少泡沫流化床锅炉的氮氧化物排放的方法和一种泡沫流化床锅炉的空气分配系统
    • WO2006084954A1
    • 2006-08-17
    • PCT/FI2006/050056
    • 2006-02-09
    • KVAERNER POWER OYDERNJATIN, PauliFABRITIUS, MarkoRÖPPÄNEN, Jukka
    • DERNJATIN, PauliFABRITIUS, MarkoRÖPPÄNEN, Jukka
    • F23C10/22F23G7/10F23K3/02
    • F23C10/00F23C2201/101F23G5/30F23G7/10
    • A method for reducing nitrogen oxide emissions of a bubbling fluidized bed boiler burning biofuel and an air distribution system for a bubbling fluidized bed boiler biofuel. A fluidized bed (2) is arranged in the lower part of a furnace (1) of the bubbling fluidized bed boiler, which is fluidized by means of fluidizing gas, which comprises at least primary air. Fuel is fed to the fluidized bed (2), which dries and pyrolizes into pyrolysis gas comprising volatile matter of fuel, which gas rises upwards in the furnace and burns there. Secondary air is supplied above the fluidized bed (2) from secondary air nozzles (6), and tertiary air is supplied above the secondary air nozzles (6). A part of primary air is supplied in connection with fuel feeding in such a manner that the fuel is forced substantially on the surface of the fluidized bed (2), thus pyrolizing entirely, and at least a part of the pyrolysis gases formed in the pyrolysis is burnt by means of primary air in such a manner that the air coefficient in relation to the volatile matter of fuel in the pyrolysis gases is in the substoichiometric area.
    • 一种用于减少燃烧生物燃料的鼓泡流化床锅炉和用于鼓泡流化床锅炉生物燃料的空气分配系统的氮氧化物排放的方法。 流化床(2)设置在鼓泡流化床锅炉的炉(1)的下部,其通过流化气体流化,该流化气体至少包括一次空气。 燃料被供给到流化床(2),其被干燥和热解成包括燃料挥发物的热解气体,该气体在炉中向上升起并在那里燃烧。 二次空气从二次空气喷嘴(6)供应到流化床(2)上方,三次空气供应到二次空气喷嘴(6)上方。 主要空气的一部分以燃料供给的方式供应,使得燃料基本上被迫在流化床(2)的表面上,从而完全热解,并且在热解中形成的至少一部分热解气体 以相对于热分解气体中的燃料的挥发物质的空气系数处于亚化学计量区域的方式通过一次空气燃烧。
    • 5. 发明申请
    • METHOD OF BURNING FUEL AND A BOILER
    • 燃烧燃料和锅炉的方法
    • WO2017212108A1
    • 2017-12-14
    • PCT/FI2016/050408
    • 2016-06-08
    • FORTUM OYJ
    • DERNJATIN, PauliHUTTUNEN, Marko
    • F23C5/08F23C7/00F23D23/00
    • The invention relates to a method of burning fuel, wherein the method comprises supplying fuel and combustion air into a boiler furnace(1)through a set of burners (3) located at or about a certain horizontal burner level (4). The flame of each of the burners is stabilized by providing the fuel feed pipe (5) with a flame stabilizing ring (7).The method further comprises setting the air coefficient (SR wing )of each of the wing burners (9) at 0.95 or above, and the air coefficient (SR center ) of the at least one center burner (8) at 0.9 or below; setting the swirl number (S wing ) of the secondary air supplied through each of the wing burners (9) at 0 –0.3; and broadening the shape of the flame of the at least one center burner (8) by producing an outer recirculation zone around the inner recirculation zone produced downstream of the flame stabilizing ring (7).The invention further relates to a boiler.
    • 本发明涉及一种燃烧燃料的方法,其中所述方法包括通过位于某个水平燃烧器处或附近的一组燃烧器(3)将燃料和燃烧空气供应到锅炉炉膛(1) 级别(4)。 通过向燃料供给管(5)提供火焰稳定环(7)来稳定每个燃烧器的火焰。该方法进一步包括设定每个燃烧器的空气系数(SR (9)处于0.95或以上,并且所述至少一个中心燃烧器(8)的空气系数(SR中心)在0.9或以下; 将通过每个机翼燃烧器(9)供应的二次空气的涡流数(S wing )设置为0〜0.3; 以及通过在火焰稳定环(7)的下游产生的内部再循环区域周围产生外部再循环区域来扩大至少一个中心燃烧器(8)的火焰形状。本发明还涉及一种锅炉。 >
    • 6. 发明申请
    • METHOD FOR BURNING FUEL, BURNER AND BOILER
    • WO2020120828A1
    • 2020-06-18
    • PCT/FI2018/050928
    • 2018-12-14
    • FORTUM OYJ
    • DERNJATIN, PauliHUTTUNEN, Marko
    • F23D23/00F23C7/00F23C6/04F23R3/14F23D1/02
    • A method for burning fuel is disclosed. The method comprises supplying cold non- preheated combustion air and dust fuel into a combustion chamber of a boiler through a burner (10) for producing a flame, the combustion air comprising primary air (100), secondary air (200), tertiary air (300). The flame is stabilised by providing a flame stabilising ring (50) at a downstream end of the annular fuel nozzle and primary air is directed through a swirl generator (30) at the primary air nozzle so that primary air has a swirl number (Sp). A stream of tertiary air is guided off with a guide sleeve (40) aligned with a burner throat (41) at an angle (α), so that an inner recirculation zone (IRZ) is formed between a stream of primary air and the stream of tertiary air. The swirl number of primary air is set at 0,4 to 1,0 by the swirl generator; the primary air velocity at the primary air nozzle orifice is set to 30 m/s or less;and the carrier air velocity at the downstream end of the annular fuel nozzle is set to 15 m/s or less. The tertiary air velocity is set so that at the end of the guide sleeve (40), the tertiary air velocity is 35 to 50 m/s. Further disclosed are a burner (10) and a boiler comprising a burner.