Hi All,
Can some one guide me on how to carry out the sizing of Liquid Liquid separator when there is a coalescing media present in the separator ?
Lot of information is available on gravity settlers but little very info is available on the vessel size calculation when a coalescing media/screen/mesh pad is used.
Regards,
Vinay Mathur
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Liquid Liquid Separator Sizing
Started by vinay, Dec 06 2007 04:12 AM
5 replies to this topic
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#1
Posted 06 December 2007 - 04:12 AM
#2
Posted 06 December 2007 - 10:49 AM
Vinay,..
U may size ur drum by considering 0.015 m/s of velocity of liquid phase. (for coaleser pad)
pls. follow the guideline of terminal velocity of heavy and light phase partical to float light particles in heavy phase and settle down heavy particles in light phase.
hope this will work.
thanks
U may size ur drum by considering 0.015 m/s of velocity of liquid phase. (for coaleser pad)
pls. follow the guideline of terminal velocity of heavy and light phase partical to float light particles in heavy phase and settle down heavy particles in light phase.
hope this will work.
thanks
#3
Posted 07 December 2007 - 05:49 AM
Dear Jetul,
UOP guidelines are 3 ft/sec (~ 0.91 mt/sec) velocity across mesh pad/coalescer. Your number seems to be too low . Can you please specify the source of your recommendation ?
Regards,
Vinay
UOP guidelines are 3 ft/sec (~ 0.91 mt/sec) velocity across mesh pad/coalescer. Your number seems to be too low . Can you please specify the source of your recommendation ?
Regards,
Vinay
#4
Posted 10 December 2007 - 09:56 AM
Dear Vinay,
As Per Shell guide line,
1) The C/S of the mat shll be sufficiently large to limit the average velocity of the total liquid flow to at most 1.5 cm/s, i.e. 0.015 m/s.
2) If small amount of heavy phase is present and the "de-oiling" of it is not critical, then it is not necessary to maintain and interface level in the vessel and a boot can be used.
pls. refer attached mail for reference....
thanks
As Per Shell guide line,
1) The C/S of the mat shll be sufficiently large to limit the average velocity of the total liquid flow to at most 1.5 cm/s, i.e. 0.015 m/s.
2) If small amount of heavy phase is present and the "de-oiling" of it is not critical, then it is not necessary to maintain and interface level in the vessel and a boot can be used.
pls. refer attached mail for reference....
thanks
Attached Files
#5
Posted 11 December 2007 - 05:53 AM
Dear Jetul,
Thank you very much for you kind help.
Regards,
Vinay
Thank you very much for you kind help.
Regards,
Vinay
#6
Posted 16 January 2008 - 11:17 AM
Vinay,
See API 12J - Specification for Oil and Gas Separators - Appendix C, for vessel with wire mesh.
Lucas
See API 12J - Specification for Oil and Gas Separators - Appendix C, for vessel with wire mesh.
Lucas
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