首页|通过产物转化分离推动CO2加氢制甲醇过程的研究进展

通过产物转化分离推动CO2加氢制甲醇过程的研究进展

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将过量排放的CO2加氢合成高附加值甲醇的过程因受热力学限制使其原料转化利用率较低,通过产物转化分离的方式能够打破热力学平衡,从而推动反应正向进行,提高CO2转化率.本文以将甲醇作为中间体耦合其他反应继续转化成低碳烯烃、芳烃等化工原料,以及利用膜反应器将副产水原位脱除等两种典型的产物转化分离方式为中心,分别展开论述其在促进CO2加氢反应过程中,耦合反应条件优化、催化剂筛选制备以及分子筛膜反应器设计与改性等方面的研究现状.重点讨论了耦合反应的双功能型催化剂中分子筛载体的酸性与孔道结构对反应性能的影响,并分析了膜反应器未来的研发重点与难点在于进一步提高其制备可重复性.
Promoting CO2 hydrogenation to methanol through product transformation and separation
The synthesis of high value-added methanol by hydrogenation of excess CO2 is limited by thermodynamics equilibrium,resulting in lower conversion and utilization efficiency of raw materials.Product transformation and separation can promote the forward progress of CO2 hydrogenation reaction.This article centers around two most typical methods,namely using methanol as an intermediate to further produce low-carbon olefins and aromatics,and utilizing membrane reactors to remove by-product water in situ.The research progress in promoting CO2 hydrogenation process through the above two means is specifically discussed from the aspects of condition optimization of coupled reaction,catalysts preparation,and membrane reactors design and modification.The influence of acidity and pore structure of molecular sieve supports on coupled reaction performance is also analyzed.Moreover,the key and challenge for further research of membrane reactors is to improve the preparation repeatability.

CO2 hydrogenationmethanolthermodynamicslow-carbon olefinsaromaticsmembrane reactors

周秋明、牛丛丛、吕帅帅、李红伟、文富利、徐润、李明丰

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中石化石油化工科学研究院有限公司,北京 100083

CO2加氢 甲醇 热力学 低碳烯烃 芳烃 膜反应器

国家重点研发计划

2021YFE0191200

2024

化工进展
中国化工学会,化学工业出版社

化工进展

CSTPCD北大核心
影响因子:1.062
ISSN:1000-6613
年,卷(期):2024.43(5)
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