Enhanced hydrogen production from biomass via the sulfur redox cycle under hydrothermal conditions

Enhanced hydrogen production from biomass via the sulfur redox cycle under hydrothermal conditions
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DOI:
10.1016/j.ijhydene.2011.06.012
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发表时间:
2011-08
影响因子:
7.2
通讯作者:
P. Setiani;J. Vilcáez;N. Watanabe;Atsushi Kishita;N. Tsuchiya
P. Setiani;J. Vilcáez;N. Watanabe;Atsushi Kishita;N. Tsuchiya
中科院分区:
工程技术2区
文献类型:
--
作者:
P. Setiani;J. Vilcáez;N. Watanabe;Atsushi Kishita;N. Tsuchiya

文献摘要

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提出了一种中温硫氧化还原循环生物质制氢的新方法。该方法可利用来自烃精炼过程的过量硫和废热或地热,由两个半循环组成:(1)在水的亚临界条件下从碱性水溶液制氢,其中硫化物HS-和S2-充当水的还原剂,和(2)在温和得多的条件下硫化物再生,其中来自生物质的有机化合物充当在前半循环中形成的多硫化物Sn 2 −和硫氧阴离子SxOy 2 −的还原剂。在硫化钠水溶液的60分钟反应期间,在≥280 °C和相应的饱和蒸气压下观察到氢气产生。在本发明的10分钟反应中,在300 °C下产生氢气后向溶液中添加D-葡萄糖C6 H12 O 6导致在≥60 °C的温度下硫化物再生。此外,证明了通过硫氧化还原循环从葡萄糖制氢,其中制氢和硫化物再生分别在300 °C和105 °C下进行。结果表明,在高达500 °C的更高温度下,从1 mol葡萄糖的产氢量大于葡萄糖的水热气化。
A new method of hydrogen production from biomass via a sulfur redox cycle at moderate temperatures has been proposed. This method, which can utilize excess sulfur from hydrocarbon refining processes and waste or geothermal heat, consists of two half cycles: (1) hydrogen production from an aqueous alkaline solution at subcritical conditions of water, where sulfide, HS−and S2−, acts as a reducing agent of water, and (2) sulfide regeneration under much milder conditions, with an organic compound derived from biomass acting as a reducing agent of polysulfide, Sn2−, and sulfur oxyanion, SxOy2−, formed in the first half cycle. During a 60-min reaction of an aqueous sodium sulfide solution, hydrogen production was observed at ≥280 °C and corresponding saturated vapor pressures. Addition of D-glucose, C6H12O6, to the solution after hydrogen production at 300 °C resulted in sulfide regeneration at temperatures ≥60 °C in the present 10-min reaction. Moreover, hydrogen production from glucose via the sulfur redox cycle was demonstrated, where the hydrogen production and sulfide regeneration were conducted at 300 °C and 105 °C, respectively. Results indicated that hydrogen production from 1 mol glucose was greater than that by hydrothermal gasification of glucose at much higher temperatures up to 500 °C.