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thank you gents for this information actually i'm process engineer,and if there are any checks you advise me to check before keeping this valve partially closed i welcome

the valve will be closed 50% and still on this position for ever pressure drop is 3 bar delta T =5 degrees valve material ball is SS seat PFTE what is the problem ?

fluid is LPG flow rate 15-20 M^3/h valve upstream pressure is 8 bar and down stream pressure is 5 bar

i have reduced bore ball valve and i'm opening it partially,not fully open. prssure differential acroos the valve is 3 bar ball material is SS316 seat PTFE any body know is that going to affect the valve,can i keep partially open?

we have an axial gas compressor and we are looking to increase the capacity any body can help to increase the capacity of it just guid line steps

the MCC is inside a building

we have MCC system equiped with co2 supresion system,we like to remove this system is that normal practice?