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    • 2. 发明授权
    • Calcium sulfide oxidation method
    • 硫化钙氧化法
    • US06245314B1
    • 2001-06-12
    • US09140657
    • 1998-08-26
    • Yoshihiko TsuchiyamaYuichi FujiokaToshihiko SetoguchiKatsuhiko ShinodaKenji TagashiraShigeyasu IshigamiYoshinori Kobayashi
    • Yoshihiko TsuchiyamaYuichi FujiokaToshihiko SetoguchiKatsuhiko ShinodaKenji TagashiraShigeyasu IshigamiYoshinori Kobayashi
    • C01F1146
    • B01J8/1809B01D53/73B01J8/1836B01J8/34B01J8/386B01J2208/00008B01J2208/0084C01F11/46Y10S423/16
    • CaS oxidation has CaS particles oxidized into CaSO4 completely as far as to the interior of the particle. The interior of an oxidation apparatus 1 is partially partitioned by a partition 22 to thereby form a first fluidized bed 20 on the inner side, a second fluidized bed 21 on the outer side and a space portion 23 thereabove. A heat exchanger 27 having a baffle plate is disposed on the inner side of the partition 22 and an in-bed heat exchanger 33 is disposed on the outer side of same. A desulfurizing product-containing fine powder 204 and coarse powder 205 and a mixture gas 206 of nitrogen, oxygen and steam are supplied into the second fluidized bed 21. Also, coal 200 and coal char 201 are supplied into the first fluidized bed 20 from below. Of the particles 304 oxidized in the second fluidized bed 21 and supplied into the first fluidized bed 20 from below with the flow of a mixture gas 208, the fine powder entrains into the space portion 23 as entrained particles 300 and a major part thereof falls down into the second fluidized bed 21 as particles 207. The completely oxidized particles are discharged as discharged ash 303 and entrained ash 302.
    • CaS氧化将CaS颗粒完全氧化成CaSO 4直至颗粒内部。 氧化装置1的内部被隔板22部分地隔开,从而在内侧形成第一流化床20,在外侧形成第二流化床21,在其上形成空间部23。 具有挡板的热交换器27设置在隔板22的内侧,并且在其外侧设置有床内热交换器33。 将含脱硫产物的细粉末204和粗粉末205以及氮气,氧气和蒸汽的混合气体206供给到第二流化床21中。另外,将煤200和煤炭201从下方供给到第一流化床20 。 在第二流化床21中被氧化并从下方供入混合气体208的第一流化床20的颗粒304中,细粉末作为夹带颗粒300进入空间部分23,并且其主要部分下降 作为颗粒207进入第二流化床21.完全氧化的颗粒作为排出的灰分303和夹带的灰分302排出。
    • 3. 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。
    • 4. 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。
    • 6. 发明申请
    • Integrated coal gasification combined cycle plant
    • 综合煤气化联合循环厂
    • US20070137169A1
    • 2007-06-21
    • US11705445
    • 2007-02-13
    • Shigeyasu IshigamiYuichiro KitagawaKatsuya Ito
    • Shigeyasu IshigamiYuichiro KitagawaKatsuya Ito
    • F02C3/28
    • F02C3/28F01K23/067Y02E20/16Y02E20/18
    • A highly efficient integrated coal gasification combined cycle plant is provided having a dust removing system which can reliably exhibit a desired dust removing performance and which can maintain high operational reliability such that the occurrence of dust leaks is prevented. The integrated coal gasification combined cycle plant has a coal gasification furnace configured to yield a coal gas by gasification of coal, a gas turbine generator driven with a gas turbine which is operated using the coal gas as fuel and which discharges a high-temperature combustion exhaust gas, an exhaust heat recovery boiler configured to recover heat from the high-temperature combustion exhaust gas and to produce steam, and a steam turbine generator driven with a steam turbine operated using the steam produced by the exhaust heat recovery boiler. In the above plant, a flue gas desulfurization device configured to desulfurize the coal gas is provided downstream of the gas turbine and the exhaust heat recovery boiler, and the dust removing system which is configured to recover char and to remove dust from the coal gas has at least one line containing a cyclone, a front-stage filter, and a rear-stage filter.
    • 提供了一种高效率的一体式煤气化联合循环装置,其具有可以可靠地呈现期望的除尘性能并且可以保持高操作可靠性的除尘系统,从而防止了灰尘泄漏的发生。 综合煤气化联合循环装置具有煤气化炉,其通过煤气化产生煤气,由燃气轮机驱动的燃气轮机,其使用煤气作为燃料运转,并且排出高温燃烧排气 气体,被配置为从高温燃烧废气中回收热量并产生蒸汽的废热回收锅炉,以及由使用由废热回收锅炉产生的蒸汽操作的蒸汽轮机驱动的蒸汽轮机发电机。 在上述工厂中,在燃气轮机和废热回收锅炉的下游设置有用于对煤气进行脱硫的烟道气脱硫装置,并且构成为回收炭并除去煤气的粉尘的除尘系统具有 包含旋风分离器,前级过滤器和后级过滤器的至少一行。