Two questions here..
1- I would like some advice and suggestion on how to modify/improve existing surge vessel (2-phase separator) into a 3-phase separator. Any reference or some calculations needed for this problem?
2- Which one is the best?
a-- horizontal open 3-phase settler with boot
b-- horizontal open 3-phase settler with sigle weir
c-- horizontal open 3-phase settler with plate pack
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Modifying 2-phase To 3-phase Separator
Started by drizzt, Jun 12 2007 10:33 AM
2 replies to this topic
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#1
Posted 12 June 2007 - 10:33 AM
#2
Posted 13 June 2007 - 09:08 AM
Hi Driz,
I work in the field of separation technology. Please give me complete details of the system, then I will come up with more questions to understand your system fully. We can discuss then more confidentally.
Regards.
I work in the field of separation technology. Please give me complete details of the system, then I will come up with more questions to understand your system fully. We can discuss then more confidentally.
Regards.
#3
Posted 15 June 2007 - 10:55 PM
Dear Dhirajkumar,
This is the details about the system.
Surge Vessel Operating Conditions
Design Pressure: 85 psig
Design Temperature: 66 C
Operating Pressure: 5 psig
Feed Flowrate: 80000 bbl/day gross
Water: 50000 bbl/day
Nett: 30000 bbl/day
Internal Diameter: 4.42 m
T/T: 13.72 m
Carbon Steel
LEHH: 2.65 m
LEH: 2.575 m
LEL: 0.15 m
NLL: 2.075 m
Feed of the separator is equipped with Schopentoeter nozzles with vortex breaker at liquid outlet.
This is the details about the system.
Surge Vessel Operating Conditions
Design Pressure: 85 psig
Design Temperature: 66 C
Operating Pressure: 5 psig
Feed Flowrate: 80000 bbl/day gross
Water: 50000 bbl/day
Nett: 30000 bbl/day
Internal Diameter: 4.42 m
T/T: 13.72 m
Carbon Steel
LEHH: 2.65 m
LEH: 2.575 m
LEL: 0.15 m
NLL: 2.075 m
Feed of the separator is equipped with Schopentoeter nozzles with vortex breaker at liquid outlet.
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