水煤气变换反应
合成气
二氧化碳
停留时间(流体动力学)
环境科学
温室气体
化学工程
催化作用
化学
选择性
摩尔比
工艺工程
材料科学
废物管理
有机化学
工程类
岩土工程
生物
生态学
作者
Magno Fonseca Santos,Antônio E. Bresciani,Newton Libânio Ferreira,Gabriel S. Bassani,Rita M.B. Alves
标识
DOI:10.1016/j.jenvman.2023.118822
摘要
The reverse water gas shift (RWGS) reaction converts carbon dioxide (CO2) and hydrogen (H2) to syngas, which is used to produce various high-added-value chemicals. This process has attracted great interest from researchers as a way of mitigating the potential environmental impacts of this greenhouse gas, with emphasis on global warming. This work aims to model and simulate an industrial catalytic reactor using kinetic data for the RWGS reaction. The simulation was carried out in Aspen Plus® v10. The thermodynamic analysis showed that the appropriate conditions for the reaction are feed molar ratio (H2/CO2) of 0.8:1, 750 °C, and 20 bar. The RWGS process proceeds in a multi-tubular fixed bed reactor with 36.26% CO2 conversion and 96.41% CO selectivity, at residence times in the order of 2.7 s. These results are at near-equilibrium CO2 conversion with higher CO selectivity.
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