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    • 2. 发明授权
    • Coal combustor and slag exhausting device therein
    • 煤燃烧器和排渣装置
    • US5331906A
    • 1994-07-26
    • US54301
    • 1993-04-30
    • Keisuke SonodaYoshinori KobayashiFumiya NakashimaKimishiro Tokuda
    • Keisuke SonodaYoshinori KobayashiFumiya NakashimaKimishiro Tokuda
    • C10J3/46C10J3/48C10J3/52F23J1/00F23D1/02
    • C10J3/487C10J3/526
    • In order to stably maintain a combustion capability in a combustion furnace for coal gassification, it is necessary to exhaust molten slag produced within the furnace without the slag stagnating. The present invention provides, in a combustion furnace for coal gassification, a slag exhausting device which is configured in such a manner that the cooling of molten slag being exhausted from the furnace is minimized to prevent the slag from solidifying and causing other slag to stagnate. The slag exhausting device is disposed at the center of a bottom wall of the combustor, and has a lower cylindrical portion and an upper bank opening upwardly and flared at an angle of 300.degree.-45.degree.. The height H from the bottom wall to the top of the upper bank, a height L and an inner diameter ds of the cylindrical lower portion and a diameter D of the combustor are set to satisfy the relations of ds/D=0.2-0.4, L/ds=0.2-0.6 and H/D=0.05-0.15.
    • 为了稳定地保持用于煤气化的燃烧炉中的燃烧能力,需要排出炉内产生的熔渣而不会使炉渣停滞。 本发明在用于煤气化的燃烧炉中提供一种排渣装置,该炉渣排出装置被构造成使得从炉排出的熔渣的冷却最小化,以防止炉渣固化并导致其它炉渣停滞。 炉渣排出装置设置在燃烧器的底壁的中心,具有下圆筒部和上堤开口向上并以300°-45°的角度张开。 从顶壁到顶部的高度H,圆柱形下部的高度L和内径ds以及燃烧器的直径D设定为满足ds / D = 0.2-0.4的关系, L / ds = 0.2-0.6,H / D = 0.05-0.15。
    • 4. 发明授权
    • Coal gasification power generator
    • 煤气化发电机
    • US5765365A
    • 1998-06-16
    • US594407
    • 1996-01-31
    • Yuichi FujiokaKimishiro TokudaToshimitsu IchinoseYoshihiko TsuchiyamaFumiya NakashimaShigeyasu IshigamiSatoshi Uchida
    • Yuichi FujiokaKimishiro TokudaToshimitsu IchinoseYoshihiko TsuchiyamaFumiya NakashimaShigeyasu IshigamiSatoshi Uchida
    • F01K23/06F02C3/28
    • F01K23/067F01K23/068Y02E20/18Y02E20/344
    • In a coal gasification power generator, coal gas 500 obtained by gasifying a coal 100 by a gasifying furnace is introduced into a desulfurization furnace in which the coal gas 500 is desulfurized by limestone 400. A coal gas 501 after desulfurization is burned by a combuster 5 after it has passed through a dust removing unit 3 so that high temperature combustion gas 800 is supplied to a gas turbine. The gas turbine 7 drives a power generating unit. Exhaust gas 801 from the gas turbine is supplied to an exhaust gas boiler 8. Char 60a produced in the gasifying furnace and limestone 60b containing CaS emitted from the desulfurization furnace are burned in an oxidation furnace, and by using the resultant combustion gas, water vapor introduced from the exhaust gas boiler 8 is heated by a heat exchanger, and thereafter it is supplied to the gasifying furnace as a gas. With the above construction, chemical energy possessed by the coal is effectively converted into electric energy, and also the rate of desulfurization of coal gasifying gas is improved thereby reducing emitted sulfur oxide.
    • 在煤气化发电机中,将通过气化炉气化煤100获得的煤气500引入到通过石灰石400将煤气500脱硫的脱硫炉中。通过燃烧器5将脱硫后的煤气501燃烧 在通过除尘单元3之后,将高温燃烧气体800供给到燃气轮机。 燃气轮机7驱动发电单元。 来自燃气轮机的废气801被供给到废气锅炉8.在气化炉中生成的Char 60a和从脱硫炉排出的含有CaS的石灰石60b在氧化炉中燃烧,通过使用所得到的燃烧气体, 从废气锅炉8引入的热交换器被加热,之后作为气体供给到气化炉。 通过上述建设,煤炭所具有的化学能有效转化为电能,提高了煤气化气的脱硫率,减少了排放的硫氧化物。
    • 6. 发明授权
    • Coal gasification power generator
    • 煤气化发电机
    • US5517815A
    • 1996-05-21
    • US375520
    • 1995-01-18
    • Yuichi FujiokaKimishiro TokudaToshimitsu IchinoseYoshihiko TsuchiyamaFumiya NakashimaShigeyasu IshigamiSatoshi Uchida
    • Yuichi FujiokaKimishiro TokudaToshimitsu IchinoseYoshihiko TsuchiyamaFumiya NakashimaShigeyasu IshigamiSatoshi Uchida
    • F01K23/06F02C3/28F02C6/18
    • F01K23/068F01K23/067Y02E20/18Y02E20/344
    • In a coal gasification power generator, a coal gas 500 obtained by gasifying coal 100 by a gasifying furnace 1 is introduced into a desulfurization furnace 2 in which the coal gas 500 is desulfurized by limestone 400. A coal gas 501 after desulfurization is burned by a combuster 5 after it has passed through a dust removing unit 3 so that a high temperature combustion gas 800 is supplied to a gas turbine 7. The gas turbine 7 drives a power generating unit. An exhaust gas 801 from the gas turbine 7 is supplied to an exhaust gas boiler 8. A char 60a produced in the gasifying furnace 1 and limestone 60b containing CaS emitted from the desulfurization furnace 2 are burned in an oxidation furnace 4, and by using the resultant combustion gas, water vapor 30a introduced from the exhaust gas boiler 8 is heated by a heat exchanger 10, and thereafter it is supplied to the gasifying furnace 1 as a gas 700. With the above construction, chemical energy possessed by the coal 100 is effectively converted into electric energy, and also the rate of desulfurization of coal gasifying gas is improved thereby reducing emitted sulfur oxide.
    • 在煤气化发电机中,将通过气化炉1气化煤100获得的煤气500引入到通过石灰石400将煤气500脱硫的脱硫炉2中。脱硫后的煤气501被烧成 燃烧器5在通过除尘单元3之后,将高温燃烧气体800供给到燃气轮机7.燃气轮机7驱动发电单元。 来自燃气轮机7的废气801被供给到废气锅炉8.在氧化炉4中,在气化炉1中产生的炭60a和含有从脱硫炉2排出的CaS的石灰石60b在氧化炉4中燃烧, 得到的燃烧气体,从排气锅炉8引入的水蒸汽30a由热交换器10加热,然后作为气体700供给到气化炉1.通过上述结构,煤100具有的化学能为 有效地转化为电能,提高了煤气化气体的脱硫率,减少了排放的硫氧化物。
    • 9. 发明授权
    • Pulverized fuel firing apparatus
    • 粉煤燃烧装置
    • US4669398A
    • 1987-06-02
    • US777878
    • 1985-09-20
    • Yasuro TakahashiYukihisa FujimaKimishiro Tokuda
    • Yasuro TakahashiYukihisa FujimaKimishiro Tokuda
    • F23C7/00F23C7/02F23D23/00F23D1/06
    • F23C7/02F23C7/00F23D23/00
    • A pulverized fuel firing apparatus comprises a first pulverized fuel injection compartment so constructed that the combined amount of primary air and secondary air to be consumed is less than the theoretical amount of air required for the combustion of the pulverized fuel to be fed as mixed with the primary air to a furnace, a second pulverized fuel injection compartment so constructed that the combined primary and secondary air amount is substantially equal to the theoretical air for the pulverized fuel to be fed together with the primary air, and a supplementary air compartment for injecting supplementary air into the furnace. The three compartments are arranged close to one another and control the NOx production upon combustion of the pulverized fuel.
    • 粉碎燃料的燃烧装置包括第一粉碎燃料喷射室,其被构造成使得被消耗的一次空气和二次空气的组合量小于与被混合的粉末燃料的燃烧所需的理论空气量 一次空气到炉中,第二粉碎燃料喷射室被构造成使得一次和二次空气量的组合基本上等于用于与一次空气一起供给的粉碎燃料的理论空气,以及用于喷射辅助空气的辅助空气室 空气进入炉。 三个隔间彼此靠近配置,并控制燃烧燃烧时的NOx产生。