Hello All,
I was wondering if i need to flow salt water and natural gas condensate (oil) alternativley from the progressing cavity pump, what are the basic design criteria i need to worry about besides NPSHa?
1) I have made sure that i have at least 2ft more NPSHa compared to NPSHr for the...
If we have 50 psi seperator with gas, water and natural gas condensate(oil), the gas seperates and goes out from the seperator from top. The water and liquid comes out from the bottom. If i need to transfer liquid from the seperator to 200 miles far to the tank, then i need pump to transfer the...
How do we size the pulsation stabilizer for progressive cavity pump? When i contacted vendor they ask me for the bore and stroke information. It is PD pump but does not have piston.
Sorry if this is the dumb question but i am recently graduated, new hire engineeer.
Hello,
PSV set at 313 psig
Is it a good idea to relief this PSV into a atmospheric closed water tank? I heard that presure will convert into velocity and turbulenace when it exit from the tailpipe of PSV into a 180 barrel water tank.
Thank you!
Hello all,
I am recent graduate engineer. I am currently working on the PSV sizing project. I want to understand between the crtical vs. subsonic flow calculation while sizing PSV. When you have critical flow or sub-sonic flow,what is actually hapening?
Do i have to worry about critical...
