水煤气变换反应
甲醇
二氧化碳
水煤气
化学
甲醇重整装置
催化作用
合成气
体积热力学
净化
天然气
化学工程
有机化学
废物管理
蒸汽重整
热力学
制氢
工程类
物理
作者
Oh‐Shim Joo,Kwang‐Deog Jung,Il Moon,A. Ya. Rozovskii,Galina I. Lin,Sung-Hwan Han,Sung‐Jin Uhm
摘要
The CAMERE process (carbon dioxide hydrogenation to form methanol via a reverse-water-gas-shift reaction) was developed and evaluated. The reverse-water-gas-shift reactor and the methanol synthesis reactor were serially aligned to form methanol from CO2 hydrogenation. Carbon dioxide was converted to CO and water by the reverse-water-gas-shift reaction (RWReaction) to remove water before methanol was synthesized. With the elimination of water by RWReaction, the purge gas volume was minimized as the recycle gas volume decreased. Because of the minimum purge gas loss by the pretreatment of RWReactor, the overall methanol yield increased up to 89% from 69%. An active and stable catalyst with the composition of Cu/ZnO/ZrO2/Ga2O3 (5:3:1:1) was developed. The system was optimized and compared with the commercial methanol synthesis processes from natural gas and coal.
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