Selective Oxidation of Methane with Hydrogen Peroxide Towards Formic Acid in a Micro Fixed-Bed Reactor

2017 ◽  
Vol 89 (12) ◽  
pp. 1759-1765 ◽  
Author(s):  
Hualiang Zuo ◽  
Vera Meynen ◽  
Elias Klemm
2019 ◽  
Vol 98 (3) ◽  
pp. 757-766
Author(s):  
Yonghui Li ◽  
Chao Lu ◽  
Xingxing Cao ◽  
Zhongfeng Geng ◽  
Minhua Zhang

Polyhedron ◽  
2018 ◽  
Vol 155 ◽  
pp. 390-397 ◽  
Author(s):  
P. Tamizhdurai ◽  
Subramanian Sakthinathan ◽  
P. Santhana Krishnan ◽  
A. Ramesh ◽  
A. Abilarasu ◽  
...  

2021 ◽  
Author(s):  
Tom Winkler ◽  
Fabien Baccot ◽  
Kari Eränen ◽  
Johan Wärnå ◽  
Gerd Hilpmann ◽  
...  

2020 ◽  
Vol 353 ◽  
pp. 269-278 ◽  
Author(s):  
Saeed Al-Shihri ◽  
Christian J. Richard ◽  
Hamid Al-Megren ◽  
David Chadwick

2013 ◽  
Vol 7 (2) ◽  
pp. 202-209 ◽  
Author(s):  
Hainan Shi ◽  
Yaquan Wang ◽  
Guoqiang Wu ◽  
Wenping Feng ◽  
Yi Lin ◽  
...  

2019 ◽  
Vol 21 (4) ◽  
pp. 106-115
Author(s):  
Ireneusz Grubecki ◽  
Katarzyna Kazimierska-Drobny

Abstract The problems of process costs and pollution of residual waters in the textile industry require increasing attention due to the new ecological regulations and also those resulting from an economic point of view. Hence, the behavior of non-isothermal fixed-bed reactor applied for hydrogen peroxide decomposition by immobilized Terminox Ultra catalase attached onto the outer surface of glass beads was studied to determine the operational conditions at which hydrogen peroxide decomposition is most effectively. A dispersion model for bioreactor applied in this work, and verified experimentally, took into account the coupled mass and heat balances as well as the rate equation for parallel enzyme deactivation. The effect of feed temperature, feed flow rate, feed hydrogen peroxide concentration, and diffusional resistances were analysed. In the calculations the global effectiveness factor based on the external mass-transfer model developed previously was employed to properly predict the real bioreactor behavior.


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