TrevorT
Chemical
- Jun 24, 2005
- 5
I've been tasked with determining whether our subsea choke valves are at risk due to erosion. The design data is:
flow of water = 4000 m3/day (SG = 0.96)
flow of oil = 2000 m3/day (SG = 0.87)
flow of NG = 1,800,000 Sm3/day (SG = 0.67)
Calculated Cv = 300
T1 = 95 deg C
dP = 610 kPa
The realtime data is: dP = 7600 Kpa. The valve is operating about 35% open. I have the plot of valve travel vs. Cv. The current flow is about 5000 m3/day total fluids.
My questions is, flow rate is currently almost at design, but at only 35% open. My guess is the U/S pressure is higher to push the same volume through a much smaller area. Obviously this would increse the velocity through the valve (plug and cage, linear). Will it increase the velocity so much as to cause erosion in the trim?
flow of water = 4000 m3/day (SG = 0.96)
flow of oil = 2000 m3/day (SG = 0.87)
flow of NG = 1,800,000 Sm3/day (SG = 0.67)
Calculated Cv = 300
T1 = 95 deg C
dP = 610 kPa
The realtime data is: dP = 7600 Kpa. The valve is operating about 35% open. I have the plot of valve travel vs. Cv. The current flow is about 5000 m3/day total fluids.
My questions is, flow rate is currently almost at design, but at only 35% open. My guess is the U/S pressure is higher to push the same volume through a much smaller area. Obviously this would increse the velocity through the valve (plug and cage, linear). Will it increase the velocity so much as to cause erosion in the trim?