首页> 外文期刊>International journal of hydrogen energy >Performance of potassium-modified Fe_2O_3/Al_2O_3 oxygen Carrier in coal-direct chemical looping hydrogen generation
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Performance of potassium-modified Fe_2O_3/Al_2O_3 oxygen Carrier in coal-direct chemical looping hydrogen generation

机译:钾改性的Fe_2O_3 / Al_2O_3氧载体在煤直接化学循环制氢中的性能

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Coal-direct chemical looping hydrogen generation (CLHG) is an innovative technology developed to produce hydrogen with in situ CO2 capture. Most oxygen carrier (OC) candidates for other chemical looping processes are not suitable for the technology. In this work, potassium modified Fe2O3/Al2O3 OCs were prepared by co-precipitation method, and screening tests were conducted to selected appropriate OC and char particle size. Experiments on the technology were carried out in a fixed bed reactor to evaluate the redox and cyclic performance of the composite OCs using Shenmu char as fuel. The OC residues in the process were characterized by X-ray diffraction (XRD), scanning electron microscope (SEM) and N-2 adsorption analyzer. Moreover, the variations of potassium content in OC residues were also discussed. The results show that the appropriate particle ranges were 425 mu m 600 mu m for OC and less than 75 mu m for char. During the first cycle, the carbon conversion could reach about more than 95% within 45 min and the total H-2 concentration under an N-2 free basis in steam oxidation period was about 99.3%. In the multi-cycle tests, the carbon conversion and hydrogen yield remained almost unchanged during the first three cycles and decreased thereafter. The selectivity toward CO2 was less than 80% during the first three cycles, increased in the next five cycles and reached about 99.3% in the 8th cycle. The OC exhibited a good anti-sintering ability and stable pore structure in the eight cycles. The decrease of potassium content in OCs was the reason for the decline of carbon conversion and hydrogen yield, and the supplement of K2CO3 could recover the reactivity of OCs. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:煤直接化学循环制氢(CLHG)是一项创新技术,旨在通过原位CO2捕集生产氢气。其他用于化学循环过程的大多数氧气载体(OC)候选者均不适合该技术。在这项工作中,通过共沉淀法制备了钾改性的Fe2O3 / Al2O3 OCs,并进行了筛选试验,以选择合适的OC和炭粒度。在固定床反应器中进行了该技术的实验,以神木炭为燃料评估了复合OC的氧化还原和循环性能。通过X射线衍射(XRD),扫描电子显微镜(SEM)和N-2吸附分析仪对过程中的OC残留进行表征。此外,还讨论了OC残留物中钾含量的变化。结果表明,合适的颗粒范围是:对于OC为425微米至600微米,对于炭为小于75微米。在第一个循环中,碳转化率可在45分钟内达到约95%以上,并且在N-2游离基条件下,蒸汽氧化期间的总H-2浓度约为99.3%。在多循环测试中,前三个循环的碳转化率和氢产率几乎保持不变,此后下降。在前三个循环中,对CO2的选择性低于80%,在接下来的五个循环中有所提高,在第8个循环中达到约99.3%。在八个循环中,OC表现出良好的抗烧结能力和稳定的孔结构。 OCs中钾含量的下降是碳转化率和氢气产率下降的原因,而K2CO3的添加可以恢复OCs的反应性。 (C)2018氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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