would like to know the better from experience the selection between ejectors or pumps in condensate service. The service is steam condensate generated by reboiler.

I have a steam turbine that suddenly undergoes high radial vibration at the front bearing, this then subsides after about 10 minutes and returns to normal running conditions. There is not much vibrati

I am confused with some authors explanation about pressure surge and slug flow in a pipe line. Can anyone explain the difference between the two..

If I have a LPS entering a coil, but I can not return by gravity. I have to pump the condensate pump back to the bfu, how do I calculate gpm.

A boiler operating 24 Hr now produces 600 psi steam. If I need to use the same boiler for 200 psi steam only, how much minimum cost ( a factor like percent)in fuel cost, I can save?