Modeling and Numerical Simulation of Hydrogen Production by Diesel Reforming Based on ASPEN PLUS

Bin Yuan, Ao Wang, Yung-Feng Liu, Yuan Ting Peng
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Abstract

Diesel reforming for hydrogen production technology is considered to be an important development trend of efficient and clean utilization of diesel. Using Aspen Plus simulation platform, the process flow of diesel reforming for hydrogen production was modeled, and the effects of reforming temperature, reforming pressure, water-to-carbon ratio and raw material composition on diesel reforming reaction were studied. The results show that the hydrogen content in the reforming product firstly increases and then decreases with the reforming temperature. The optimum reforming temperature of n-hexadecane is about 750°C; Lower reaction pressure is beneficial to obtain higher H2 mole fraction, and the optimal reforming pressure is recommended to be set between 1bar and 100bar. In terms of water-to-carbon ratio, the optimal water-to-carbon ratio is about 2.3. The increase of cycloalkanes and other related components in diesel is conducive to higher hydrogen yield, while the increase of aromatic hydrocarbons, alkanes and other related components is not conducive to the reforming reaction.
基于ASPEN PLUS的柴油重整制氢建模与数值模拟
柴油重整制氢技术被认为是柴油高效清洁利用的重要发展趋势。利用Aspen Plus仿真平台,对柴油重整制氢工艺流程进行了建模,研究了重整温度、重整压力、水碳比和原料组成对柴油重整反应的影响。结果表明:随着重整温度的升高,重整产物中氢含量先升高后降低;正十六烷的最佳重整温度约为750℃;较低的反应压力有利于获得较高的H2摩尔分数,建议最佳重整压力在1bar ~ 100bar之间。在水碳比方面,最佳水碳比约为2.3。柴油中环烷烃等相关组分的增加有利于提高产氢率,而芳烃、烷烃等相关组分的增加则不利于重整反应的进行。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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