petrona
Chemical
- Aug 26, 2008
- 15
THERE IS A PIPE L = 100 METERS,
TWO VALVE ARE CLOSED AT ITS ENDS,
I MUST CALCULATE THE FLOWRATE IN THE TRV VALVE WHEN THE TEMPERATURE OF THE FLUID (OIL) INSIDE RISES BY RADIATION OF TUBE. (Ti=30°C, Tair=40°C, DN 150, L 100m).
SOMEONE CAN GIVE ME A METHOD?
IT FOLLOW MY FIRST APPROXIMATION METHOD
1 SUN RADIATION IS REDUCT BY ATMOSPHERE TO 800W/M2
2 I SUPPOSE THE SURFACE REFLECTS 10% SO REMAIN 720 W/M2
3 I SUPPOSE THAT THERE ARE NOT OTHER HEAT CONVECTION WITH AIR AND ALL THIS POWER IS ABSORBED BY THE FLUID.
De=0.168M, Di=0.154M
L*=1M2/0.168M=5.9524M (ESPOSITION SURFACE)
V*=0.1108M3
MASS*= V*xDENSITY= 0.1108x750= 83KG
DELTAT=Q*/(CpxMASS*)=619/(0.42x83)=18°C
FINAL TEMPERATURE = 48°C
I SUPPOSE THAT THE PIPE DON'T SOTTRACT HEAT TO RISE ITS T
THEN
DELTA V = V°(1+3gDELTAT)=0.0965 M3
FLOWRATE = 0.0965 M3/H = 73 KG/H
THANKS
BYE
TWO VALVE ARE CLOSED AT ITS ENDS,
I MUST CALCULATE THE FLOWRATE IN THE TRV VALVE WHEN THE TEMPERATURE OF THE FLUID (OIL) INSIDE RISES BY RADIATION OF TUBE. (Ti=30°C, Tair=40°C, DN 150, L 100m).
SOMEONE CAN GIVE ME A METHOD?
IT FOLLOW MY FIRST APPROXIMATION METHOD
1 SUN RADIATION IS REDUCT BY ATMOSPHERE TO 800W/M2
2 I SUPPOSE THE SURFACE REFLECTS 10% SO REMAIN 720 W/M2
3 I SUPPOSE THAT THERE ARE NOT OTHER HEAT CONVECTION WITH AIR AND ALL THIS POWER IS ABSORBED BY THE FLUID.
De=0.168M, Di=0.154M
L*=1M2/0.168M=5.9524M (ESPOSITION SURFACE)
V*=0.1108M3
MASS*= V*xDENSITY= 0.1108x750= 83KG
DELTAT=Q*/(CpxMASS*)=619/(0.42x83)=18°C
FINAL TEMPERATURE = 48°C
I SUPPOSE THAT THE PIPE DON'T SOTTRACT HEAT TO RISE ITS T
THEN
DELTA V = V°(1+3gDELTAT)=0.0965 M3
FLOWRATE = 0.0965 M3/H = 73 KG/H
THANKS
BYE