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首页> 外文期刊>The Korean journal of chemical engineering >Catalytic application of metallic iron from the dyeing sludge ash for benzene steam reforming reaction in tar emitted from biomass gasification
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Catalytic application of metallic iron from the dyeing sludge ash for benzene steam reforming reaction in tar emitted from biomass gasification

机译:污泥灰分中金属铁的催化应用在生物质气化焦油中苯蒸汽重整反应中

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摘要

Because it is the most promising method for reforming tar in a gasification system, a catalytic steam reforming reaction of tar using a dyeing sludge ash catalyst that contains mostly iron oxide has been modeled using benzene to investigate whether a steam reforming catalyst produced from waste is viable. The catalytic activity of the ash catalyst is similar to that of the commercially available iron-chrome-based catalyst for the same equivalent total amount of Fe2O3. The activity over the ash catalyst has been examined in terms of the weight hour space velocity (WHSV) and the reaction temperature to develop a model for the reaction kinetics. Using a power law model, the reaction order coefficients of the benzene and steam were estimated to be 0.43 and 0, respectively. The activation energy required for the ash catalyst was approximately 187.6 kJ mol(-1). In addition, the reductive properties of the iron oxide in the ash catalyst were also examined via XRD and H-2-TPR analyses.
机译:因为这是在气化系统中重整焦油的最有前途的方法,所以使用苯模拟了使用主要包含氧化铁的染色污泥灰分催化剂进行焦油的催化蒸汽重整反应,并使用苯模拟了由废物产生的蒸汽重整催化剂是否可行。对于相同当量的Fe2O3,灰烬催化剂的催化活性类似于市售的铁铬基催化剂。已经根据重时空速(WHSV)和反应温度检查了灰分催化剂上的活性,以建立反应动力学模型。使用幂律模型,苯和蒸汽的反应阶数系数分别估计为0.43和0。灰分催化剂所需的活化能约为187.6 kJ mol(-1)。另外,还通过XRD和H-2-TPR分析检查了灰分催化剂中氧化铁的还原性能。

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