Dear Process Engineers,
I want to know why do we require to mention crtitical pressure in Control valve datasheets.
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Critical Pressure For Control Valve Datasheet
Started by rahul22yadav, May 21 2012 11:47 PM
5 replies to this topic
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#1
Posted 21 May 2012 - 11:47 PM
#2
Posted 21 May 2012 - 11:57 PM
Rahul,
Consider this resource to support your query .
Breizh
Consider this resource to support your query .
Breizh
#3
Posted 22 May 2012 - 12:19 AM
Thanks for ur reply,
So actually this is applicable where there are chances of chocked flow though control valve.
So actually this is applicable where there are chances of chocked flow though control valve.
#4
Posted 29 May 2012 - 07:08 AM
hello,
I am new to the forum.
I have question regarding the critical pressure?
What if the customer doesn't specify the critical pressure for the application like Solvent + HCs?
I am new to the forum.
I have question regarding the critical pressure?
What if the customer doesn't specify the critical pressure for the application like Solvent + HCs?
#5
Posted 29 May 2012 - 09:42 AM
possibly the resource suggested by breizh suggest a solution,
the formulation to evaluate allowable pressure drop with liquids (chocked flow due to flashing or cavitation) is for pure fluids,
for mixtures things are more difficult, consider for example wide boiling mixtures,
for these cases I average values,
the properties of many fluids are available in books (for example Perry's chemical engineering handbook, Prausnitz's Properties of gases and liquids etc.) or Excel's files etc.
the formulation to evaluate allowable pressure drop with liquids (chocked flow due to flashing or cavitation) is for pure fluids,
for mixtures things are more difficult, consider for example wide boiling mixtures,
for these cases I average values,
the properties of many fluids are available in books (for example Perry's chemical engineering handbook, Prausnitz's Properties of gases and liquids etc.) or Excel's files etc.
#6
Posted 30 May 2012 - 01:55 AM
Thanks paolo for the reply

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