Issues regarding tray efficiency in tower design
Thread Content
I would like to ask everyone: when some people perform calculations for absorption trays, they enter the Murphree efficiency and vaporization efficiency, and only do so for individual trays. How are these Murphree efficiency and vaporization efficiency values determined? Was it also calculated inversely using the process package data?
Various channels, process packages, manufacturer information, empirical data, and even guesswork
Engineering design generally takes into account the overall tower efficiency, while the efficiency of individual plates holds theoretical and academic significance.