|
Process design pressure at 250°F (psi/MPa) |
250/ 1.725 |
|
Process design temperature (°F/°C) |
-20° to 250°/ -29° to 121° |
|
Maximum working pressure at 250°F (psi/MPa) |
250 /1.725 |
|
Maximum oil rate (normal liquid level) (bbl/d, cu m/d) |
40,000/6,359 |
|
Maximum gas rate (normal liquid level) (MM cu ft/d, MM cu m/d) |
5/ 0.142 |
|
Compartments |
Twin |
|
Capacity (bbls/cu m) |
100 /16 |
|
Service conditions |
H₂S / CO₂ |
|
Outside dimensions (L × W × H) (ft/m) |
19.88 × 8.00 × 9.50/ 6.058 × 2.438 × 2.896 |
|
Approximate empty weight (lb/kg) |
19,842/ 9,000 |
|
Fluid inlet |
3-in. Figure 602 union thread |
|
Fluid outlet - gas |
3-in. Figure 602 union wing |
|
Fluid outlet - oil |
3-in. Figure 602 union wing |
|
Fluid outlet - drain |
3-in. Figure 602 union wing |
|
Fluid outlet - vent |
3-in. Figure 602 union wing |
|
Steam inlet |
2-in. Figure 602 union thread |
|
Steam outlet |
2-in. Figure 602 union wing |
|
Full-bore valves and bypass manifold |
Yes |
|
Pressure sensing points |
Oil and water lines |
|
Temperature sensing points |
Oil and water lines |
|
Fluid sampling points |
Oil and water lines |
|
Gas measurement equipment |
Not applicable |
|
Oil measurement equipment |
Calibrated sight glass |
|
Water measurement equipment |
Calibrated sight glass |
|
Oil heating coil |
Applicable |
|
Vessel pressure control equipment on gas Line |
3-in. Fail-open pneumatic pressure control valve with Fisher pressure controller |
|
Safety devices |
Pressure safety valve and Rupture Disc mounted directly on independent vessel nozzles with 3-in. vent line to base skid edge
Hi-Lo level alarm system with twin air horns
2 × grounding points on opposite diagonals of base skid |
|
Vessel manway |
20-in. diameter, ANSI 150RF flange, located at rear of vessel |
|
Standards |
ASME VIII Div I
ANSI B.31.3
NACE MR-01-75 |