首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >An integrated process for hydrogen-rich gas production from cotton stalks: The simultaneous gasification of pyrolysis gases and char in an entrained flow bed reactor
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An integrated process for hydrogen-rich gas production from cotton stalks: The simultaneous gasification of pyrolysis gases and char in an entrained flow bed reactor

机译:棉秸秆生产富氢气体的集成工艺:在气流床反应器中同时气化热解气和焦炭

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An integrated process (pyrolysis, gas-solid simultaneous gasification and catalytic steam reforming) was utilized to produce hydrogen-rich gas from cotton stalks. The simultaneous conversion of the pyrolysis products (char and pyrolysis gases) was emphatically investigated using an entrained flow bed reactor. More carbon of char is converted into hydrogen-rich gas in the simultaneous conversion process and the carbon conversion is increased from 78.84% to 92.06% compared with the two stages process (pyrolysis and catalytic steam reforming). The distribution of tar components is also changed in this process. The polycyclic aromatic compounds (PACs) of tar are converted into low-ring compounds or even chain compounds due to the catalysis of char. In addition, the carbon deposition yield over NiO/MgO catalyst in the steam reforming process is approximately 4 times higher without the simultaneous process. The potential H-2 yield increases from 47.71 to 78.19 g/kg cotton stalks due to the simultaneous conversion process. (C) 2015 Elsevier Ltd. All rights reserved.
机译:利用集成工艺(热解,气固同时气化和催化蒸汽重整)从棉秆中生产富氢气体。使用夹带流化床反应器着重研究了热解产物(焦炭和热解气体)的同时转化。与两步法(热解和催化蒸汽重整)相比,在同时转化过程中,有更多的炭碳转化为富氢气体,并且碳转化率从78.84%增加到92.06%。焦油成分的分布在此过程中也发生了变化。由于焦炭的催化作用,焦油的多环芳族化合物(PAC)被转化为低环化合物甚至链状化合物。另外,在不进行同时处理的情况下,在蒸汽重整过程中,NiO / MgO催化剂上的碳沉积产率大约高出4倍。由于同时进行转化,潜在的H-2产量从47.71克/千克棉秆增加到78.19克/千克棉秆。 (C)2015 Elsevier Ltd.保留所有权利。

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