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    • 8. 发明申请
    • APPARATUS FOR TREATING FUEL AND METHOD OF STARTING THE SAME
    • 用于处理燃料的装置及其启动方法
    • US20100266909A1
    • 2010-10-21
    • US12740794
    • 2008-11-11
    • Seiji FujiharaYukimune KaniHidenobu WakitaKunihiro Ukai
    • Seiji FujiharaYukimune KaniHidenobu WakitaKunihiro Ukai
    • H01M8/06
    • C01B3/384C01B3/16C01B3/48C01B2203/0233C01B2203/0283C01B2203/044C01B2203/047C01B2203/066C01B2203/085C01B2203/1058C01B2203/1076C01B2203/1604C01B2203/1619C01B2203/169Y02P20/52
    • A fuel processing apparatus according to the present invention is a fuel processing apparatus 100 including a reformer 111, a raw material supply section 112, a moisture supply section 114, a heating section 116, a reforming temperature detection section 117 for detecting the temperature of a reforming catalyst, a shift converter 121, a shift temperature detection section 123, and a control section 200. When the apparatus is booted, the control section 200 activates the raw material supply section 111 to begin supplying a raw material to the reformer 111, and activates the heating section 116 to begin supplying heat to the reforming catalyst. Thereafter, when the reforming temperature detection section 117 detects a temperature equal to or greater than a reforming water supply reference temperature, the control section 200 operates the moisture supply section to supply moisture to the reformer 111, and while the reforming temperature detection section 117 detects a temperature equal to or greater than the reforming water supply reference temperature, determines an amount of moisture to be supplied to the reformer 111 and controls the moisture supply section 114, based on the temperature detected by the shift temperature detection section.
    • 本发明的燃料处理装置是具备重整器111,原料供给部112,水分供给部114,加热部116,检测温度的重整温度检测部117的燃料处理装置100 重整催化剂,换档转换器121,变速温度检测部123和控制部200.当该装置启动时,控制部200启动原料供给部111,开始向重整器111供给原料, 激活加热部分116以开始向重整催化剂供应热量。 此后,当重整温度检测部117检测到重整供水基准温度以上的温度时,控制部200操作供水部,向重整器111供给水分,在重整温度检测部117检测到 基于由变换温度检测部检测出的温度,等于或大于重整供水参考温度的温度确定供应给重整器111的水分量并控制湿气供应部分114。
    • 10. 发明授权
    • Hydrogen generation apparatus, fuel cell system, and hydrogen generation apparatus operation method
    • 氢发生装置,燃料电池系统和氢气发生装置的运行方法
    • US09252443B2
    • 2016-02-02
    • US13497730
    • 2010-12-24
    • Yukimune KaniHidenobu WakitaSeiji FujiharaTomoyuki Nakajima
    • Yukimune KaniHidenobu WakitaSeiji FujiharaTomoyuki Nakajima
    • H01M8/02H01M8/06C01B3/38
    • H01M8/0618C01B3/384C01B2203/0233C01B2203/0283C01B2203/044C01B2203/047C01B2203/066C01B2203/0811C01B2203/1258C01B2203/127C01B2203/148C01B2203/169Y02E60/50
    • A hydrogen generation apparatus (150) includes: a first desulfurizer (13) configured to remove, through adsorption, a sulfur compound in a raw material gas that is to be supplied to a reformer; a second desulfurizer (21) configured to hydrodesulfurize a sulfur compound in the raw material gas that is to be supplied to the reformer; a first passage (16) through which the raw material gas is supplied to the reformer through the first desulfurizer (13); a second passage (17) through which the raw material gas is supplied to the reformer through the second desulfurizer (21), without passing through the first desulfurizer (13); a switch configured to switch a passage through which the raw material gas flows between the first passage (16) and the second passage (17); and a controller. The controller controls the switch such that the raw material gas flows through the first passage (16) in at least one of a pressure compensation operation and a raw material gas purge operation, the pressure compensation operation being an operation of supplying the raw material gas in order to compensate for an internal pressure drop that occurs after an operation of generating a hydrogen-containing gas is stopped, and the raw material gas purge operation being an operation of purging the inside of the hydrogen generation apparatus with the raw material gas.
    • 氢气生成装置(150)包括:第一脱硫装置(13),被配置为通过吸附除去要供给至重整器的原料气体中的硫化合物; 第二脱硫剂(21),其构成为对要供给到所述重整器的原料气体中的硫化合物进行加氢脱硫; 第一通道(16),原料气体通过第一通道(16)通过第一脱硫器(13)供应至重整器; 第二通道(17),原料气体通过第二通道(17)通过第二脱硫器(21)供应至重整器,而不通过第一脱硫器(13); 开关,其构造成切换原料气体在第一通路(16)和第二通路(17)之间流过的通道; 和控制器。 控制器控制开关,使得原料气体以压力补偿操作和原料气体净化操作中的至少一种流过第一通道(16),压力补偿操作是将原料气体供应到 以补偿在停止生成含氢气体的操作之后发生的内部压降,原料气体净化操作是利用原料气体清洗氢气发生装置的内部的操作。