Systems and methods for subsea fluid phase separation

Patent metadata

Field	Value
Publication number	US-10648314-B2
Application number	US-201415106691-A
Country	US
Kind code	B2
Filing date	Dec 22, 2014
Priority date	Dec 20, 2013
Publication date	May 12, 2020
Grant date	May 12, 2020

Abstract

Systems and methods for subsea fluid phase separation. A two phase embodiment of the subsea fluid separation system separates a multiphase flow into gas and liquid phases. A three phase embodiment of the subsea fluid separation system separates multiphase flow into gas, oil, and water phases. The subsea fluid separation systems include a wellhead desander system to remove solids from the multiphase flow, a vertical gas-liquid separation module having associated valves disposed in series with a horizontal gas-liquid separation module having associated valves, one or more pumps to provide fluid flow to the vertical and horizontal separators, and a control system to control operation of the valves and pumps. The three phase embodiment further includes oil-water separators and multi-stage hydrocyclones for produced water treatment in a subsea environment.

First claim

What is claimed is:

1. A system for subsea fluid phase separation, comprising:
a vertical gas-liquid separation module having at least one associated valve and configured to produce a liquid output stream;
a horizontal gas-liquid separation module having at least one associated valve and disposed in series with the vertical gas-liquid separation module, wherein the horizontal gas-liquid separation module is configured to produce an oil-water mixture stream and to receive the liquid output stream produced by the vertical gas-liquid separation module, and wherein the horizontal gas-liquid separation module comprises a first inlet in fluid communication with the vertical gas-liquid separation module and configured to receive the liquid output stream, a second inlet, and a plurality of outlets disposed in a bottom portion of the horizontal gas-liquid separation module;
one or more first pumps to provide fluid flow out of the vertical and horizontal gas-liquid separation modules; and
a control system to control operation of the one or more first pumps and the associated valves.

2. The system of claim 1 , wherein the horizontal gas-liquid separation module further comprises a header device configured to disperse fluid entering the second inlet across the bottom portion of the horizontal gas-liquid separation module for settled solids removal.

3. The system of claim 2 , wherein the fluid entering the second inlet is a portion of a fluid discharged from the one or more first pumps.

4. The system of claim 1 wherein the control system further comprises:
a split-range controller configured to:
adjust at least one of the associated valves and adjust a discharge speed of at least one of the one or more first pumps to optimize operation.

5. The system of claim 4 , wherein a minimum flow control loop of the at least one of the one or more first pumps is configured to be utilized for a desanding operation of the vertical and horizontal gas-liquid separation modules.

6. The system of claim 1 , further comprising:
an oil-water separation module comprising at least one vessel having an associated valve; and
one or more second pumps to enable produced water re-injection;
wherein the control system is further configured to control operation of the valve associated with the at least one vessel of the oil-water separation module.

7. The system of claim 6 , further comprising:
at least one liquid-liquid hydrocyclone in series with a solid-liquid hydrocyclone in series with an additional liquid-liquid hydrocyclone for produced water treatment to enable water re-injection.

8. The system of claim 7 , further comprising:
an ejector configured to boost pressure of a reject flow exiting one or more of the liquid-liquid hydrocyclones and/or the solid-liquid hydrocyclone.

9. A method for subsea fluid phase separation, comprising:
configuring a horizontal vessel in series with a vertical gas-liquid separation vessel;
producing a liquid output stream from the vertical gas-liquid separation vessel;
flowing the liquid output stream from the vertical gas-liquid separation vessel into the horizontal vessel;
flowing an oil-water mixture stream from the horizontal vessel to a first oil-water separation vessel;
flowing a separated oil stream from the first oil-water separation vessel to a second oil-water separation vessel;
receiving an indication of a level or a pressure of the horizontal vessel and the vertical gas-liquid separation vessel; and
performing, based on the indication, a processing operation that:
generates a control signal to control operation of a pump that provides fluid flow into and/or out of the vessels; or
generates a control signal to control operation of at least one valve associated with the vessels.

10. The method of claim 9 , further comprising using a level control valve to generate motive fluid for a solids accumulator flushing operation.

11. The method of claim 9 further comprising combining a dynamic multiphase flow simulation model with a dynamic process simulation model.

12. The method of claim 11 further comprising:
including processing conditions in the dynamic multiphase flow simulation model using the dynamic process simulation model; then
predicting a slugging profile using the dynamic multiphase flow simulation model.

13. A method to control and discharge hydrocyclone rejects to an oil pipeline using an ejector subsea, the method comprising:
controlling a motive fluid rate to the ejector by setting a constant differential pressure across a control valve that receives a flow of rejects exiting a last hydrocyclone in a series of hydrocyclones, thereby providing a driving force for the rejects from the series of hydrocyclones and optimizing the motive fluid rate.

14. The method of claim 13 wherein the series of hydrocyclones further comprises at least one liquid-liquid hydrocyclone in series with a solid-liquid hydrocyclone in series with an additional liquid-liquid hydrocyclone.

15. A system comprising:
a configuration of multi-stage hydrocyclones, including a liquid-liquid hydrocyclone in series with a solid-liquid hydrocyclone in series with another liquid-liquid hydrocyclone, for produced water treatment in a subsea environment to enable water re-injection; and
a control system comprising a dynamic multiphase flow simulation model coupled with a dynamic process simulation model;
wherein the configuration of multi-stage hydrocyclones causes breaking of solids-stabilized emulsion particles in the water and solids removal from the water prior to water re-injection.

16. The system of claim 15 wherein the control system is configured to combine processing conditions of the dynamic process simulation model with a slugging profile of the dynamic multiphase flow simulation model.

17. The system of claim 15 , further comprising:
an ejector configured to boost pressure of a reject flow exiting one or more of the liquid-liquid hydrocyclones and/or the solid-liquid hydrocyclone.

18. The system of claim 15 , wherein the process simulation model incorporates the configuration of multi-stage hydrocyclones.

Assignees

• Onesubsea Ip Uk Ltd

Inventors

• Unnam Jagadeesh
• Byeseda John

Classifications

• B01D17/12

  Auxiliary equipment particularly adapted for use with liquid-separating apparatus, e.g. control circuits · CPC title

• B01D21/267

  by using a cyclone · CPC title

• B01D17/0208

  by sedimentation · CPC title

• B01D19/0036

  Flash degasification (the other groups take precedence) · CPC title

• B01D17/06

  Separation of liquids from each other by electricity · CPC title