流化床
流态化
制氢
化学链燃烧
材料科学
核工程
氢
太阳炉
太阳能
废物管理
化学工程
工艺工程
环境科学
化学
工程类
有机化学
电气工程
作者
Tetsuro Etori,Nobuyuki Gokon,Akane Takeuchi,Takuma Miki,Mikiya Yokota,Tetsuya Kodama
标识
DOI:10.1016/j.egypro.2015.03.143
摘要
Hydrogen production by solar thermochemical process uses concentrated solar radiation as its energy source. Various thermochemical processes operating at technically manageable temperatures which are a solar thermochemical two-step water splitting and solar gasification of carbonaceousmaterial have been extensivelystudied and demonstrated by researchers around the world. These processes arecapable of converting high-temperature heat from concentrated solar radiation into clean hydrogen from water.In this study, in order to control a flowability (fluidization state) of bed materials in a fluidized bed reactor for thermochemical processes (two-step water splitting cycle and gasification of coal coke),firstly, a basic relationship between pressure drop of inlet gas and gas flow rate was experimentally examined using bed materials with different particle sizes by a small-scale quartz reactor at ambient pressure and temperature. Secondly, the CeO2 particles having the size determined by above-describedflowability test were tested using a windowed fluidized bed reactor prototype. The fluidized bed of CeO2 particles was exposed to a concentrated Xe light by sun-simulator with an input power of about 5 kWth for the T-R step in order to release oxygen. The production rate and productivity of oxygen and the reactivity of CeO2 particles were examined in this paper.
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