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作 者:XIN Fang XU Min LI Xun-Feng HUAI Xiu-Lan
机构地区:[1]Institute of Engineering Thermophysics,Chinese Academy of Sciences [2]University of Chinese Academy of Sciences
出 处:《Journal of Thermal Science》2013年第6期613-618,共6页热科学学报(英文版)
基 金:supported by the National Natural Science Foundation of China under Grant No 51276181,Grant No.51106158;the National Basic Research Program of China under Grant No 2011CB710705
摘 要:The dehydrogenation reaction of isopropanol occurring at low temperature is of great industrial importance. It is a key procedure in isopropanol/acetone/hydrogen chemical heat pump system. An experimental investigation was performed to study the behavior of the liquid phase dehydrogenation of isopropanol over amorphous alloy Raney nickel catalysts. Un-promoted and promoted catalysts were used and their performances were compared under various catalyst amounts, acetone content in the reactant and reaction temperature ranging from 348 K to 355 K.It is found that there exists an optimum catalyst concentration which is about 0.34 g in 300 ml isopropanol. The temperature has evident effect on the reaction. The presence of activities of Fe-promoted catalyst decrease slightly compared to the un-promoted catalyst when the temperature are 348 K and 351 K. Besides, the reaction rate decreases almost linearly with the increase of acetone volume fraction in the reactant.
关 键 词:Chemical heat pump Liquid-phase dehydrogenation ISOPROPANOL
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