Hi.
How can i calculate the size for packed-bed reactor for Oxidative Dehydrogenation of Ethane (ODE) ?
Also, how do i determine the residence time as it is not mentioned in the article for ODE.
Basically, i cant design the reactor based on my project mass flowrate inlet at 99.62 kg/hr.
Thanks for any help.
*based on this article, i cant find any step/calculations how they get the design, please help me
https://pubs.acs.org....1021/ie100738q
https://www.research...eoretical_study