LPG Liquid Line Sizing
LPG Liquid Line Sizing
(OP)
All:
I am currently working on LPG terminal project. For LPG line sizing, what pressure drop and velocity guidelines should be considered? LPG operating temperature is about-40F
Also I am trying to find out the isolation philosophy to be used for isolating piping and equipments and where an ESDV should be used as oppossed to manual or an automatic XV valve for my P&ID development.
Does API or NFPA address these issues?
Any help or comments would be appreciated.
Regards,
npf
I am currently working on LPG terminal project. For LPG line sizing, what pressure drop and velocity guidelines should be considered? LPG operating temperature is about-40F
Also I am trying to find out the isolation philosophy to be used for isolating piping and equipments and where an ESDV should be used as oppossed to manual or an automatic XV valve for my P&ID development.
Does API or NFPA address these issues?
Any help or comments would be appreciated.
Regards,
npf





RE: LPG Liquid Line Sizing
While you're thinking about that, check these,
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go here and search "LPG"
ht
CFRs for NGL facilities might help.
ht
"I'm all in favor of keeping dangerous weapons out of the hands of fools. Let's start with typewriters."
- Frank Lloyd Wright (1868-1959)
RE: LPG Liquid Line Sizing
RE: LPG Liquid Line Sizing
"I'm all in favor of keeping dangerous weapons out of the hands of fools. Let's start with typewriters."
- Frank Lloyd Wright (1868-1959)
RE: LPG Liquid Line Sizing
Thanks for the information. Right now we are working on LPG terminal project.I will try to look onto NFPA58 for more information.
Regards,
npf
RE: LPG Liquid Line Sizing
"I think it would be a good idea."
- Mahatma Gandhi (1869-1948),
when asked about Western civilization