Method and system for fluid separation with an integrated control system

Patent metadata

Field	Value
Publication number	US-9901847-B2
Application number	US-201114367617-A
Country	US
Kind code	B2
Filing date	Dec 22, 2011
Priority date	Dec 22, 2011
Publication date	Feb 27, 2018
Grant date	Feb 27, 2018

Abstract

A system for separating an input fluid flow comprising gas and liquid into separate gas and liquid flows is provided. The system includes a primary separator configured to receive the input fluid flow and to separate the input fluid flow into a primary separator liquid output flow and a primary separator gas output flow, a first secondary inline separator connected downstream from the primary separator to polish the primary separator gas output flow, a second secondary inline separator connected downstream from the primary separator to polish the primary separator liquid output flow, a system gas outlet, a system liquid outlet, a primary separator gas output valve on the primary separator gas output flow, and a control system configured to receive measurements of liquid level within the primary separator, and identify, using the received measurements, whether a position of the primary separator gas output valve is to be changed.

First claim

The invention claimed is:

1. A system for separating an input fluid flow comprising gas and liquid into separate gas and liquid flows, the system comprising:
a gas-liquid cylindrical cyclone primary separator configured to receive said input fluid flow and to separate said input fluid flow into a primary separator liquid output flow and a primary separator gas output flow, wherein the primary separator comprises at least one downwardly sloped tangential inlet pipe and is a gravity separator at a first production rate and a cyclonic separator at a different, higher production rate, the primary separator having a primary separator gas outlet to guide the primary separator gas output flow;
a primary separator gas output valve coupled to said primary separator gas outlet to receive said primary separator gas output flow;
a first secondary inline separator connected downstream from said primary separator, wheiein said first secondary inline separator is a secondary gas separator and is connected to said primary separator gas output valve to receive and polish said primary separator gas output flow and to separate said received primary separator gas output flow into a first secondary separator liquid output flow and a first secondary separator gas output flow;
a second secondary inline separator connected downstream from said primary separator, wherein said second secondary inline separator is a secondary liquid separator and is connected to said primary separator to receive and polish said primary separator liquid output flow and to separate said received primary separator liquid output flow into a second secondary separator liquid output flow and a second secondary separator gas output flow;
a system gas outlet connected to said first secondary inline separator to output a system gas output flow;
a system liquid outlet connected to said second secondary inline separator to output a system liquid output flow; and
a control system comprising:
a sensor to generate measurements of liquid level within the primary, gas-liquid cylindrical cyclone separator;
a link to convey the measurements of liquid level within the primary separator; and
a controller coupled to the link and to the primary separator gas output valve, the controller configured to control, based on said received measurements of liquid level within the primary, gas-liquid cylindrical cyclone separator, a position of said primary separator gas output valve to prevent liquid flooding into the first secondary inline separator,
whereby said control system is configured to regulate flow through said primary separator and said first and second secondary inline separators to ensure a flow of gas from said system gas outlet with a maximum amount of liquid carry-over and a flow of liquid from said system liquid outlet with a maximum amount of entrained gas.

2. The system according to claim 1 , wherein at least one of said control system, said primary separator and said first and second secondary inline separators sis configured to regulate transient input fluid flows and ensure a positive flow of gas from said gas output and a positive flow of liquid from said liquid output.

3. The system according to claim 1 , wherein at least one of said control system, said primary separator and said first and second secondary inline separators is configured to control at least one of the quality and quantity of flow in the primary separator liquid output flow and the primary separator gas output flow.

4. The system according to claim 1 , wherein said control system is configured to determine whether said input fluid flow is above a threshold value and to regulate flow through the primary separator according to said determination.

5. The system according to claim 1 wherein said primary separator is configured to primarily function as a pre-separation stage and a slug damper when said input fluid flow is above a threshold flow.

6. The system according to claim 5 wherein, if said input fluid flow is determined to be below said threshold, said primary separator is configured so that said primary separator liquid output flow has less than said maximum amount of entrained gas and said primary separator gas output flow meets said specified amount of liquid carry-over.

7. The system according to claim 1 , further comprising a pump downstream from the system liquid outlet.

8. The system according to claim 7 , further comprising a minimum flow pipe line connected from downstream from the pump to a location upstream from the pump.

9. The system according to claim 1 , further comprising a compressor downstream from said system gas outlet.

10. The system according to claim 9 , further comprising an anti-surge pipe line connected from downstream from said compressor to a location upstream from said compressor.

11. The system according to claim 1 , wherein said primary separator is a cyclonic separator.

12. The system according to claim 1 , wherein said secondary gas separator has a retention time in the range of a fraction of a second to a few seconds.

13. The system according to claim 1 , wherein said second secondary inline separator is connected to said secondary gas separator to receive and polish a liquid output flow.

14. The system according to claim 1 , wherein said first secondary inline separator is connected to said secondary liquid separator to receive and polish a gas output flow.

15. The system according to claim 1 , further comprising a plurality of valves which are manipulated by said control system to regulate at least one of said primary separator's output flows or said first and second secondary inline separators' output flows.

16. The system according to claim 15 , wherein the control system is configured to receive measurements for a plurality of state variables within the system and stabilise flow within the system by controlling said plurality of valves based on said measurements.

17. The system according to claim 16 , wherein the control system is configured to receive state variable measurements selected from the group consisting of the primary separator liquid output flow, the primary separator gas output flow, the secondary separator liquid output flow, the secondary separator gas output flow, the system gas output flow and the system liquid output flow.

18. The system according to claim 1 , further comprising a liquid-liquid separator downstream from the first or second secondary inline separators.

19. The system according to claim 1 , further comprising a sand removal separator upstream the primary separator or downstream from the first or second secondary inline separators.

20. The system according to claim 1 , further comprising a valve on the second secondary inline separator gas output flow and said parameter to be changed is a position of said second secondary separator gas output valve.

21. A method for controlling a system for separating an input fluid flow comprising gas and liquid into separate gas and liquid flows, the system comprising:
a primary separator configured to receive said input fluid flow and to separate said input fluid flow into a primary separator liquid output flow and a primary separator gas output flow, wherein the primary separator is a gravity separator at a first production rate and cyclonic separator a different, higher production rate, wherein the primary separator is a gas-liquid cylindrical cyclone separator comprising at least one downwardly sloped tangential inlet pipe and having a primary separator gas outlet to g

Assignees

• Høydal Jan
• Kristiansen Olav
• Eikrem Gisle Otto
• Fjalestad Kjetil
• Statoil Petroleum As

Inventors

• Høydal Jan
• Kristiansen Olav
• Eikrem Gisle Otto
• Fjalestad Kjetil

Classifications

• G05D7/06

  characterised by the use of electric means {(G05D7/005 takes precedence)} · CPC title

• B04C11/00

  Accessories, e.g. safety or control devices, not otherwise provided for {, e.g. regulators, valves in inlet or overflow ducting}(with electrostatic precipitating arrangements B03C3/14) · CPC title

• B04C3/06

  Construction of inlets or outlets to the vortex chamber · CPC title

• B04C3/00

  Apparatus in which the axial direction of the vortex {flow following a screw-thread type line} remains unchanged {; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct (combined with other devices B04C9/00)} · CPC title

• B01D45/12

  by centrifugal forces (centrifuges B04B; cyclones B04C) · CPC title