甲醇
蒸汽重整
制氢
生物量(生态学)
氢
木材气体发生器
甲醇重整装置
合成气
废物管理
过程(计算)
化学工程
化学
工艺工程
当量比
制浆造纸工业
材料科学
环境科学
有机化学
工程类
计算机科学
地质学
操作系统
煤
海洋学
燃烧室
燃烧
作者
Wei Feng,Peijun Ji,Biaohua Chen,Danxing Zheng
标识
DOI:10.1002/ceat.201000346
摘要
Abstract A biomass‐based methanol production process was investigated. The process consists of a biomass gasifier, steam reformer, and methanol synthesis reactor as the main units. Reactors were simulated by applying the kinetic models previously developed and the process was analyzed based on the simulation results. The key parameters, the equivalence ratio in biomass gasification, the temperature in steam reforming, and the recycle of hydrogen in methanol synthesis were identified. These parameters affect the methanol production. The process analysis indicates that the optimal combinations of the parameters can greatly enhance the methanol production and the thermodynamic efficiency. Finally, the elemental analysis for carbon and hydrogen along the process was carried out.
科研通智能强力驱动
Strongly Powered by AbleSci AI