Hi! I've been working as a process engineer for 2 years now and currently involved in the thermal design of shell and tube heat exchangers. As I am relatively new to this field and no experience in operations, I would like to ask from experienced members of this forum to help enlighten me on this topic.
Generally, we size shell and tube heat exchangers for maximum flowrate (e.g. normal flowrate x 1.2 or as specified in the process datasheet). I am thinking that the shell and tube heat exchanger is always filled with liquid (assuming no phase change, just sensible heating/cooling) during this maximum flowrate operation. but how about during normal operation (without the multiplier) or turndown operation (like half or so of the normal flowrate). will the shell side still be fully filled with liquid just moving at a low velocity?
Thank you in advance!
Edit: I think I should've posted this in the process heat transfer section. Will post in the right section in the future.
Edited by lance21, 24 August 2013 - 11:11 PM.