I am debating with a fellow engineer which term is appropriate to use. In my experience as a site design engineer, I have seen "limit of disturbance (LOD)" or "limit of clearance (LOC)" used to descr

My case would be a vessel 90% full of liquid being drained with nothing else open. Is it as simple as P1*V1=P2*V2, where I would solve for P2 when I have 100% empty vessel?

I am struggling to make a sensible basis for sizing thermal expansion pot basis. Due to pipework configuration and fluid properties we cannot easily return the thermal expansion RV back to source. T

I m facing problem with Mp filtri particle counter fixed in fitration trolley (for offline operations) the display always showing NAS15 class whereas the oil we are using is AW68/ NAS7 Clean.

7.1.1: Shell Test Pressure - Each valve shall be given a shell test at a gage pressure no less than 1.5 times the 38C(100F) pressure rating, rounded off to the next higher 25 psi(1 bar) increment.

Out of curiosity I have been "collecting" V8 firing orders. So far I have found 5 unique firing orders for a conventional 90 deg bank angle cruciform crank V8.

I have a 2" pipe that is running water at 50 psi (city pressure) with a valve on the end. Total length from the city main to the valve is about 100 ft. If I open this pipe up, fully open, to fill up

I'm designing a piping system for steam, say withDesign pressure 12 bar(g)