High temperature energy storage performances of methane reforming with carbon dioxide in a tubular packed reactor

作者：Lu, Jianfeng^*; Chen, Yuan; Ding, Jing; Wang, Weilong

来源：Applied Energy, 2016, 162: 1473-1482.

DOI：10.1016/j.apenergy.2015.03.140

• Tubular packed reactor
• Porous medium
• Computational fluid dynamics
• Thermochemical storage
• Solar energy

High temperature heat transfer and energy storage performances of methane reforming with carbon dioxide in tubular packed reactor are investigated under different operating conditions. Experimental results show that the methane reforming in tubular packed reactor can efficiently store high temperature thermal energy, and the sensible heat and heat loss besides thermochemical energy storage play important role in the total energy storage process. When the operating temperature is increased, the thermochemical storage efficiency first increases for methane conversion rising and then decreases for heat loss rising. As the operating temperate is 800 degrees C, the methane conversion is 79.6%, and the thermochemical storage efficiency and total energy efficiency can be higher than 47% and 70%. According to the experimental system, the flow and reaction model of methane reforming is established using the laminar finite-rate model and Arrhenius expression, and the simulated methane conversion and energy storage efficiency fit with experimental data. Along the flow direction, the fluid temperature in the catalyst bed first decreases because of the endothermic reaction and then increases for the heat transfer from reactor wall. As a conclusion, the maximum thermochemical storage efficiency will be obtained under optimal operating temperature and optimal flow rate, and the total energy efficiency can be increased by the increase of bed conductivity and decrease of heat loss coefficient.

• 出版日期2016-1-15
• 单位中山大学