Microwave -activated structured reactors to maximize propylene selectivity in the oxidative dehydrogenation of propane

被引:43
|
作者
Ramirez, Adrian [1 ,2 ,5 ]
Hueso, Jose L. [1 ,2 ,3 ,4 ]
Mallada, Reyes [1 ,2 ,3 ,4 ]
Santamaria, Jesus [1 ,2 ,3 ,4 ]
机构
[1] Univ Zaragoza, Inst Nanosci Aragon, C Mariano Esquillor S-N, Zaragoza 50018, Spain
[2] Univ Zaragoza, Dept Chem & Environm Engn, C Mariano Esquillor S-N, Zaragoza 50018, Spain
[3] Networking Res Ctr Bioengn Biomat & Nanomed CIBER, Madrid 28029, Spain
[4] Univ Zaragoza, Consejo Super Invest Cient CSIC, Inst Ciencia Mat Aragon ICMA, Zaragoza, Spain
[5] King Abdullah Univ Sci & Technol KAUST, Thuwal 23955, Saudi Arabia
基金
欧洲研究理事会;
关键词
PROMOTED MAGNESIA CATALYST; VANADIA CATALYSTS; HEAT-TRANSFER; HOT-SPOTS; OXIDE; ALKANES; ETHANE; GENERATION; CONVERSION; MONOLITHS;
D O I
10.1016/j.cej.2020.124746
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Microwave (MW) heating has been applied to increase the selectivity to propylene in the oxidative dehydrogenation (ODH) of propane. The preferential heating of the solid monolith (made of SiC, a good microwave susceptor), allows working with a lower gas phase temperature, reducing the formation of undesired by-products in the gas phase via homogeneous reactions. Conversion levels of ~ 21% and selectivity to propylene up to 70% have been achieved with MW-heated straight channel monolithic reactors coated with a VMgO catalyst. These competitive values contrast with the more limited performance delivered by the same catalytic system when it is subjected to conventional heating in a fixed-bed reactor configuration, thereby corroborating the advantage of working under a significant gas–solid temperature gap to minimize the extent of homogeneous reactions. © 2020 Elsevier B.V.
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页数:8
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