制氢
氢
环境科学
蒸汽重整
产量(工程)
蒸汽注入
过程模拟
工艺工程
核工程
废物管理
过程(计算)
材料科学
化学
工程类
计算机科学
冶金
操作系统
有机化学
作者
Mohsen Motahari-Nezhad
标识
DOI:10.1080/10916466.2016.1154868
摘要
A heavy oil gasification model that can predict the hydrogen yield has been developed for a high pressure circulating fluidized bed. The model is based on the Aspen Plus package, which is a professional software for simulation of thermal process. To illustrate the effects of the steam/fuel ratio and temperature, several conditions have been examined. The results show that the gasification temperature plays a major role in the process. As gasification temperature increases from 600 to 800°C, the production of hydrogen increases dramatically. The influence of steam/fuel ratio (0.50–0.80) is also considerable, but shows a constant rate at the higher steam/fuel. Simulation results were validated against experimental data available in the literature.
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