选择性
催化作用
脱氢
1,3-丁二烯
乙醇
羟醛缩合
化学工程
蒸发
材料科学
无机化学
化学
有机化学
物理
工程类
热力学
作者
Xianquan Li,Yujia Zhao,Jifeng Pang,Pengfei Wu,Wenguang Yu,Peifang Yan,Yang Su,Shangru Zhai,Mingyuan Zheng
出处
期刊:Resources chemicals and materials
[Elsevier]
日期:2023-09-01
卷期号:3 (1): 27-37
被引量:1
标识
DOI:10.1016/j.recm.2023.08.005
摘要
Catalytic upgrading of bio-ethanol to 1,3-butadiene (1,3-BD, ETB) is a renewable and low-carbon technology for the bulk chemical production. Exploring robust catalysts and getting in-depth understanding of the relationship between the structure of catalytic sites and reaction selectivity are of great significance for ETB process applications. In this study, we constructed a robust Cu-Zr/SiO2 catalyst by an ammonia evaporation and post-impregnation method. Over the optimal 2%Cu-8%Zr/SiO2 catalyst, superior performance of 69.6% 1,3-BD selectivity and 71.2% ethanol conversion were obtained. Systematic characterizations revealed that three types of Cu-Zr-Si active sites were probably constructed on the Cu-8%Zr/SiO2 catalysts as varying the Cu loadings from 0.5-20%, affording greatly different activity and selectivity in the ETB process. The 1,3-BD productivity over the (SiO)2(CuO)Zr-OH sites was 8.2 and 77.2 times higher than that of (CuO)2-Zr-(OSi)2 and Cu-(O)2-Zr-(OSi)2 sites, respectively, attributed to the high activities and good balance among the reactions of dehydrogenation, aldol condensation, and MPVO reduction.
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