Sizing sheet of Pressure Safety Valve (PSV) for two phase flow using API-520
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Descripción: For the Aberrant Roleplaying System. It's okay. Like the system but this particular book is kinda meh.
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Three Phase Separator
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Two Phase vertical Separator sizing Process data 1 2 3 4 5 6 7 8 9 10
Gas flow rate Oil flow rate Operating pressure Operating temperature
MMscfd BOPD Psia O F R µm Min
Droplet size to be removed Retention time Specific gravity of gas API gravity of liquid Viscosity of liquid(µ) Compressibility factor (Z)
O
API Cp
10 2000 1000 60 520 140 3 0.6 40 0.013 0.84
Assumption 1 Drag co-efficient(Cd) 2 Rentention time
Density of liquid(ρL) Density of gas(ρg) Terminal velocity of droplets(Vt) Reynolds No Calcuated drag co efficient(Ccd) Gas Capacity Constraint Diameter Liquid capacity constraint height(h) Seem to Seem length(Lss) Slenderness ratio(SR) Selected diameter(Ds) Selected Seem to Seem length(SLss) Selected slederness ratio
lb/ft3 lb/ft3 ft/sec
51.5077 3.70879 0.54694 107.041 0.85418
in
21.886
ft
104.385 15.0321 8.24205 36 9.55 3.18
in ft
Note: 1) Start by assuming a value of CD, such as 0.34, and calculate Vt. Then, using Vt, solve for Re. Then,may be solved for CD. If the calculated value of CD equals the assumed value, the solution has been reached. If not, then the procedure should be repeated using the calculated CD as a new assumption.The original assumption of 0.34 for CD was used because this is the limiting value for large Reynolds numbers.
Two Phase Horizontal Separator sizing Process data 1 2 3 4 5 6 7 8 9 10
Gas flow rate Oil flow rate Operating pressure Operating temperature
MMscfd BOPD Psia O F R µm Min
Droplet size to be removed Retention time Specific gravity of gas API gravity of liquid Viscosity of liquid(µ) Compressibility factor (Z)
O
API Cp
10 2000 1000 60 520 140 3 0.6 40 0.013 0.84
Assumption 1 Drag co-efficient(Cd) 2 Rentention time
min
0.85419 2
Calculation & Results Density of liquid(ρL) Density of gas(ρg) Terminal velocity of droplets(Vt) Reynolds No Calcuated drag co efficient(Ccd) Gas Capacity Constraint 6a Diameter*effective length 7 Liquid capacity constraint 7a height 8 Seem to Seem length 9 Slenderness ratio: 1 2 3 4 5 6
