Subsea well having a submersible pump assembly with a gas separator located at the pump discharge
A subsea rotary gas separator system has a separator located adjacent the discharge of the pump for separating gas from the high pressure liquid stream exiting the pump. Some of the high pressure liquid is recycled back to the inlet of the pump to maintain a liquid-rich inlet stream for the pump.
1. A submersible pump assembly, comprising:
an inlet for receiving intake fluid comprising liquids and gas, and an outlet;
a motor, a lift pump, and a seal between the motor and pump, all mounted between the inlet and the outlet such that the pump draws the intake fluid through the inlet and discharges outlet fluid;
a gas separator located downstream from the lift pump for receiving fluid from the lift pump, the gas separator discharging a mixed flow stream of gas and liquid to the outlet, and a liquid stream that is separate from the mixed flow stream; and
a conduit for recycling the liquid stream to the inlet for maintaining a liquid-rich inlet stream for the lift pump.
2. The pump assembly according to claim 1 , wherein the gas separator receives fluid from the lift pump through a discharge tube, is located adjacent to the outlet and connected to the outlet with a tube, and the liquid stream is approximately 100% liquid.
3. The pump assembly according to claim 1 , wherein the gas separator utilizes one of a centrifuge and a static device with enhanced gravity.
4. The pump assembly according to claim 1 , wherein the inlet comprises a jet pump venturi eductor and the liquid stream is reintroduced via the jet pump venturi eductor.
5. The pump assembly according to claim 4 , further comprising a gas accumulator adjacent the inlet for accumulating gas, and wherein the jet pump venturi eductor has a vena contracta for introducing gas from the gas accumulator.
6. The pump assembly according to claim 4 , wherein the jet pump venturi eductor further comprises a flow conditioner for measuring a density of the intake fluid by pressure drop, mass flow rate or Coriolis effect whereby high pressure is recovered by reflowing recycled liquid through a vena contracta.
7. The pump assembly according to claim 1 , wherein the mixed flow stream of gas and liquid is substantially dry having an entrained liquid drop size of less than approximately 10 μm.
8. The pump assembly according to claim 1 , wherein the conduit has a feedback flow control that monitors at least one of fluid density and mass flow rate.
9. The pump assembly according to claim 1 , wherein recycling of the liquid stream is suspended when the intake fluids for the lift pump exceed a minimum threshold density, whereby a venturi comprising a flow conditioner is used to measure density by pressure drop or Coriolis effect.
10. The pump assembly according to claim 1 , wherein the motor, lift pump, seal and gas separator are located in one of a capsule and a permanent well casing.
11. The pump assembly according to claim 1 , wherein a discharge of the lift pump comprises well fluids being pumped to the surface.
12. A system for a submersible pump assembly, comprising:
a capsule having an inlet for receiving intake fluid comprising liquids and gas, and an outlet located opposite the inlet;
a motor, a lift pump, and a seal between the motor and the lift pump, all mounted coaxially in the capsule between the inlet and the outlet such that the lift pump draws the intake fluid through the inlet and discharges outlet fluid;
a gas separator located downstream from the lift pump for receiving fluid from the lift pump, the gas separator discharging a mixed flow stream of gas and liquid to the outlet having an entrained liquid drop size of less than approximately 10 μm, and a liquid stream that is separate from the mixed flow stream; and
a conduit for recycling the liquid stream to the inlet for maintaining a liquid-rich inlet stream for the lift pump.
13. The system according to claim 12 , wherein the gas separator is located adjacent to the outlet, and the liquid stream is approximately 100% liquid.
14. The system according to claim 12 , wherein the conduit extends through one of an interior and an exterior of the capsule.
15. The system according to claim 12 , wherein the gas separator utilizes one of a centrifuge and a static device with enhanced gravity.
16. The system according to claim 12 , wherein the inlet comprises a jet pump venturi eductor and the liquid stream is reintroduced via the jet pump venturi eductor.
17. The system according to claim 16 , further comprising a gas accumulator adjacent the capsule for accumulating gas, and wherein the jet pump venturi eductor has a vena contracta for introducing gas from the gas accumulator.
18. The system according to claim 16 , wherein the jet pump venturi eductor further comprises a flow conditioner for measuring a density of the intake fluid by pressure drop, mass flow rate or Coriolis effect whereby high pressure is recovered by reflowing recycled liquid through the vena contracta.
19. The system according to claim 12 , wherein the conduit has a feedback flow control that monitors at least one of fluid density and mass flow rate.
20. The system according to claim 12 , wherein the capsule is a permanent well casing, and recycling of the liquid stream is suspended when the intake flow for the lift pump exceeds a minimum threshold density, whereby a venturi comprising a flow conditioner is used to measure density by pressure drop or Coriolis effect.