Abstract
A model for mass transfer processes in column apparatuses has been done. The model may be modified for different volume source (chemical reaction, interphase mass transfer). The using of the average velocities and concentration permits to solve the scale-up problem. A hierarchical approach for model parameter identification has been proposed.
Full Text 
Sign-in/Register to access full text options
Sign-in/Register to access full text options 
Published version (
Free)
Free) 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a call
