Regarding the pressure-reduced steam return line
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This post was last edited by yf20081370 on 2020-11-22 09:08. Experts, is there anyone who knows something about the vapor return lines in pressure relief towers and stripping towers? Such as the design principles for steam return lines? Why is the vapor return line of the pressure reduction tower designed below the distillation outlet, and what is the basis for this? For example, what significance does the temperature on the vapor return line have for the operation of the tower? What can be determined from the level of the return tower temperature? Welcome to communicate, thank you.
Why isn’t anyone discussing it? I’ll post again
I welcome everyone to discuss and share their valuable opinions. I think this topic involves quite a bit of technical complexity, and it’s indeed difficult to understand. I would be extremely grateful for any guidance you can provide.