Oh thank you.
While this thread still seems hot, I have an other question which I'm sure you would know.If I want to increase flow in the existing pump can I do that by increasing the discharge line dia?
Thanks TD2K for the response.
About #3, I was confused how you are gonna find which equation applies on it, whether stokes law, intermediate or Newton's equation. That of course depends on the fluid Reynold#.
Vessel sizing is a bit intricate and its really hard to find the stuff on google for...
ok, to start with,
a. how do I calculate the residence time
b. What is/what is the criteria to select NLL or normal liquid level for vertical vessels
c. how to assess CD, the drag coefficient
Thanks for the quick reply
Hi everybody,
Can anybody tell me how to perform chemical engineering related calculations for pressure vessels, both vertical and horizontal.
Thanks in advance.
