Hydrogenation Kinetics of M-Dinitrobenzene in a Continuous Micro-packed Bed Reactor

2021 ◽  
pp. 117113
Author(s):  
Xiaonan Duan ◽  
Jiabin Yin ◽  
Mengmeng Huang ◽  
Aoxing Feng ◽  
Weisong Fu ◽  
...  
1998 ◽  
Vol 37 (9) ◽  
pp. 97-104 ◽  
Author(s):  
Zhishi Wang

To evaluate the engineering feasibility of autotrophic denitrification, a program of theoretical and experimental investigations of the granular sulfur/lime packed bed autotrophic denitrification system was planned and completed. This program evaluated the stoichiometric, kinetic and physical characteristics of the process. This paper will focus on the results of that project which are concerned with the kinetics of autotrophic denitrification of groundwater.


1970 ◽  
Vol 34 (2) ◽  
pp. 193-197,a1 ◽  
Author(s):  
Yoshikazu Shimizu ◽  
Keiichi Inoue ◽  
Hiroyuki Nishikata ◽  
Yutaka Koenuma ◽  
Yasuhiro Takemura ◽  
...  

2020 ◽  
Vol 5 (9) ◽  
pp. 1751-1758
Author(s):  
Xiaonan Duan ◽  
Jiacheng Tu ◽  
Andrew R. Teixeira ◽  
Le Sang ◽  
Klavs F. Jensen ◽  
...  

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.


2020 ◽  
Vol 34 (5) ◽  
pp. 6158-6167 ◽  
Author(s):  
Kun Wang ◽  
Qingbo Yu ◽  
Qi Wang ◽  
Jialiang Hua ◽  
Ruijie Peng

Author(s):  
Natalia Semagina ◽  
Rosanne Tam ◽  
James Sawada

The study addresses the reduction of ethylene levels in postharvest storage applications using a Pd-Zn-Sn/TiO2 catalyst, which is capable of reacting trace concentrations of ethylene at temperatures as low as 278 K and at relative humidity as high as 90%. The rate law is derived from data collected using a constant volume batch reactor and a model for a storage room with associated packed bed reactor is developed. The amount of catalyst required to maintain an ethylene concentration of 0.1 ppmv in a room containing 20 tons of fruit having an ethylene metabolism of 0.1 ul/kg hr was calculated as a function of air temperature and water content. While the catalyst is capable of continuously removing ethylene from saturated, refrigerated air, the amount of catalyst required can be reduced significantly by incorporating conventional air conditioning solutions upstream of the catalyst bed. Such combined systems and their functions are discussed


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