By Larry W Lake; Kenneth E Arnold; Society of Petroleum Engineers (U.S.)
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Example text
A bottom flat plate, in conjunction with the perforated cylinder, spreads the liquid flow out more uniformly. The cyclonic-type inlet device is used to diffuse the momentum of the incoming feed stream and allows for the removal of any bulk liquids and solids that may be present. The cyclonic inlet device is designed such that it can operate at both high and low gas/oil ratios without the possibility of gas blow-by and excessive liquid re-entrainment into the gas phase. The main characteristics to look for in an inlet cyclone are listed next.
12 shows that the liquid capacity is the dominant parameter. Hence, a 24-in. 6-ft vessel is sufficient, as it has a slenderness ratio within the typical 3 to 5 range. This size should be rounded up to 24 in. × 7 ft. 3: Vertical Three-Phase Separator. Given Values. 8 lbm / ft3 Operating pressure 1,000 psia Operating temperature 60 ° F Liquid-retention time 10 minutes each phase Inlet nozzle 12 in. Drop removal from gas 100 μm Water density Step 1. Calculate vessel diameter based on gas capacity from Eq.
This can be accomplished by ensuring that the liquid flow channels within the cyclone are relatively large and that any perforated holes are of the correct size to minimize shear. • Minimum gas blow-by to the liquid outlet: Gas blow-by is seen when gas exits with the liquid phase from the bottom of the cyclone. If the amount of gas is considerable, a bubbling mass of liquid/gas is formed, which has a negative effect because of foam generation and mixing. Care must be taken when designing inlet cyclones for separators.
Petroleum engineering handbook Volume III, Facilities and construction engineering by Larry W Lake; Kenneth E Arnold; Society of Petroleum Engineers (U.S.)
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