An automated flow platform for accurate determination of gas-liquid-solid reaction kinetics

被引:38
作者
Duan, Xiaonan [1 ]
Tu, Jiacheng [1 ]
Teixeira, Andrew R. [3 ]
Sang, Le [1 ]
Jensen, Klavs F. [2 ]
Zhang, Jisong [1 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 100084, Peoples R China
[2] MIT, Dept Chem Engn, Cambridge, MA 02139 USA
[3] Worcester Polytech Inst, Dept Chem Engn, 100 Inst Rd, Worcester, MA 01609 USA
基金
中国国家自然科学基金;
关键词
MASS-TRANSFER; BATCH KINETICS; PHASE HYDROGENATION; PALLADIUM; HYDRODYNAMICS; TRANSPORT; OXIDATION; MICROREACTORS; OPTIMIZATION; NITROBENZENE;
D O I
10.1039/d0re00191k
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
An automated flow platform based on a tube-in-tube contactor and micro-packed bed reactor is developed to measure the kinetics of gas-liquid-solid hydrogenation reactions. The liquid flowing in the inner tube of the tube-in-tube contactor is rapidly saturated to ensure a constant H(2)concentration before entering the micro-packed bed, which transforms the gas-liquid-solid system into a liquid-solid system. A ramping strategy is adopted in which the continuously varied residence time and the corresponding conversion data are obtained in a single experiment. Two reactions including hydrogenation of alpha-methylstyrene and nitrobenzene are chosen to demonstrate the accuracy and efficiency of this automated platform. Varying the flow rate ramping shows that accurate kinetic determination requires a specific range of flow rate ramps. A kinetic curve of conversionversusresidence time (more than ten thousand data points) can be obtained in a single experiment within 50 min. The kinetic parameters obtained with this strategy agree well with literature values. The automated flow platform with flow rate ramping enables accurate determination of gas-liquid-solid reaction kinetics with higher efficiency and lower reagent cost compared with other methods.
引用
收藏
页码:1751 / 1758
页数:8
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