Info required on how to calculate expansion loops in a steam line on a pipe rack and also determining forces due to pipe expansion on anchor bay etc.

Need some opinions/counsel/suggestions/insults on the upper velocity limit for saturated (two-phase) steam. System in question is 50 psig, 65% quality, dirty steam. Rates are 8000-45000 lbm/hr. I am

I have a 3-stage steam jet air ejector system that produces vacuum for a process. The two inter-condensers are direct contact, not surface.

No Loop Or Do Not Pocket in terms of pipelines - are they same meaning? in that case why used in different occasions? Pls. clarify

We have a stand for fluid steam demostration. There is steam traps with glass body and steel. I need know "theorical" equation for determinate the thickness o allowable pressure in a tube (cylindrical