生物量(生态学)
工艺工程
热电联产
超临界流体
火用
废物管理
可用能
环境科学
合成气
环境工程
发电
工程类
氢
化学
热力学
功率(物理)
地质学
有机化学
物理
海洋学
作者
Qijun Zhang,Heng Chen,Bo Li,Peiyuan Pan,Gang Xu,Qinxin Zhao,Xue Jiang
标识
DOI:10.1016/j.applthermaleng.2023.120234
摘要
In order to improve the efficiency of conventional biomass to methanol, a novel cogeneration system is designed that couples an electrolytic water subsystem with a s-CO2 cycle and a conventional biomass to methanol system. The novel cogeneration system uses syngas converted from biomass gasification and hydrogen obtained by water electrolysis for methanol synthesis, and it uses a supercritical CO2 cycle to improve its performance. The proposed process was modeled and calculated using Aspen Plus and MATLAB as the main simulation software to analyze its energy efficiency, exergy efficiency and economics, and to illustrate the advantages of the system compared with the conventional biomass to methanol system from a thermodynamic point of view. Taking a biomass with a mass flow rate of 2.78 kg/s for example, the energy efficiency of the new process was increased by 19.89% for the same biomass consumption conditions. The results show that the system has an energy efficiency of 67.98% and an exergy efficiency of 64.82%. The irreversibility comes from two main components: the gasifier and the electrolyzer. The project is expected to achieve a net present value of $22,948,830 over its 20-year life cycle.
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