Abstract
Experimental data are presented concerning the local solid-liquid mass transfer coefficients in a packed column operated with a cocurrent downflow of gas and liquid. The experiments were carried out for two diameters of spherical particles, with the flow rates of both phases and the physicochemical properties of the liquid varied over a wide range. The experimental results are correlated and compared with the appropriate literature data.
Sign-in/Register to access full text options 
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 callMore From: Chemical Engineering & Processing: Process Intensification
Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
