I'm contacting you as I have visit your site on the internet and it might be that you could help or guide me to solve the problems mentioned below.

I am wondering what the best diameter of pipe is for a given volume flow rate. I understand that conductors are sized based on flow velocity, surface roughness etc. but I have read that fluid frictio

I'm working on a project where the client wants to run an 8" sch.40 C.Stl. buried pipeline approx. 10 miles. This is a hot commodity with operating temp.s between 140 to 195 Deg.s F, pressure around 9

We are trying to size a control valve to feed an heat exchanger.  The inlet pressure is 100 psig for a flowrate estimated at 195 lb/hr.  What is the rule or how can I figure the dP

I am working for a company that wants me to setup a Chart. It is so they can give to contractors to tell them what maximum valve class they are allowed to use for hydrotest purposes.