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'Preliminary results of hydrogen production from water vapor decomposition using DBD plasma in a PMCR reactor'

机译:'在PMCR反应器中使用DBD等离子体从水蒸气分解产生氢的初步结果'

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The water decomposition is considered one of the most attractive chemical processes for the production of hydrogen. The present work describes the preliminary results obtained in the experimental study of the water vapor dissociation into hydrogen and oxygen species using Dielectric-Barrier Discharge (DBD) plasma in a plate micro-channel reactor (PMCR). The water vapor molecules are injected without using carrier gas into the PMCR reactor at pressure of 100 kPa and temperature of 573 K. The applied high voltage of the plasma was within range of 14-18 kV and different steam flow rates have been analyzed within range of 100-200 ml/h. The product gases have been separated in ice trap which it was connected directly to the PMCR reactor to prevent the recombination of hydrogen and oxygen species. The concentration of the outlet species has been measured in a gas phase chromatography (GC) instrument. The PMCR reactor heating temperature effect on the water vapor decomposition has been analyzed. It was found that the water vapor is dissociated into their constituent molecular elements of hydrogen and oxygen gas using plasma. The maximum obtained mole fraction, hydrogen flow rate and conversion rate were 2.3%, 9.42 g/h, 42.51% respectively, at steam temperature of 573 K, pressure 100 kPa, PMCR heating temperature 403 K, steam flow rate of 200 ml/h and the plasma discharge high voltage of 18 kV. It was observed that the amount of evolved hydrogen concentration increased with the increase of the PMCR reactor heating temperature. Also, the thermal efficiencies versus the heat supplied have been calculated and the maximum obtained efficiency was 49.32%. Consequently, the evolved hydrogen flow rate appears to depend mainly on the plasma voltage, PMCR reactor heating temperature and the separating temperature of outlet hydrogen and oxygen species. The steam dissociation experiment will be extended to separate hydrogen and oxygen species elements at high temperature conditions. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:水分解被认为是产生氢的最有吸引力的化学过程之一。本工作描述了在平板微通道反应器(PMCR)中使用介电势垒放电(DBD)等离子体将水蒸气分解为氢和氧的实验研究中获得的初步结果。在不使用载气的情况下,在100 kPa的压力和573 K的温度下将水蒸气分子注入PMCR反应器中。施加的等离子体高压在14-18 kV范围内,并且在该范围内分析了不同的蒸汽流速100-200 ml / h。产物气体已在冰阱中分离,然后将其直接连接到PMCR反应器,以防止氢和氧物种重新结合。出口物质的浓度已通过气相色谱仪(GC)进行了测量。分析了PMCR反应器加热温度对水蒸气分解的影响。发现利用等离子体将水蒸气分解成氢和氧气的组成分子元素。在蒸汽温度为573 K,压力为100 kPa,PMCR加热温度为403 K,蒸汽流速为200 ml / h的条件下,获得的最大摩尔分数,氢气流速和转化率分别为2.3%,9.42 g / h,42.51%。等离子放电高压为18 kV。观察到,随着PMCR反应器加热温度的升高,析出的氢浓度增加。此外,已经计算出热效率与所供热量的关系,最大效率为49.32%。因此,放出的氢气流速似乎主要取决于等离子体电压,PMCR反应器加热温度以及出口氢气和氧气物质的分离温度。蒸汽分解实验将扩展到在高温条件下分离氢和氧物种元素。 (C)2019氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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