Sir, where will be pressure drop take place. Kindly explain that. Because from dehydration column rich TEG 30°C 30 bar, after the control valve suddenly the pressure drop to 5bar how, from where it drop. Kindly please explain.
Hi Nick , thanks for your support and my. Question is wether we can add or subtract the friction loss in discharge, I think we can add friction loss in discharge....
Hi nick. Appreciate if you could do this kind of explaination on other system as well (fuel gas system, compression system, gas dehydration system, etc)
Hi, Mr.Nick How to know if the pump requires minimum recirculation line? I don't understand clearly. I have this idea that this minimum recirculation line is related to turndown ratio advised by vendor. Could you explain clearly?
Hi Nick. Thank you very much for your video. I have a question, if i put a pressure gauge at a suction side of the pump. If I substract the vapor pressure of the liquid from the reading of pressure gauge will I get NPSHA? Thank you again.
Hi. If we have pressure gauges on an existing system on the discharge and the suction, we can just look at them right? We don't need to calculate, am I understanding it correctly?
The Head is the same assumed that the viscosity and pump speed are the same. of course, the denser fluid will affect pump efficiency due to hydraulic friction loss, motor power efficiency, etc.