Inline gas liquid separation system with a shared reject vessel

Patent metadata

Field	Value
Publication number	US-9956507-B2
Application number	US-201314404000-A
Country	US
Kind code	B2
Filing date	May 24, 2013
Priority date	May 25, 2012
Publication date	May 1, 2018
Grant date	May 1, 2018

Abstract

The present invention concerns a gas-liquid separation system and a method for operating a gas-liquid separation system.

First claim

The invention claimed is:

1. A gas-liquid separation system comprising:
a splitter which is configured to separate a well stream into liquid and gaseous phases;
the splitter having an outlet for the liquid phase which is connected through a liquid continuous line to an inline degasser that is configured to drive separation of gas and liquid by centripetal acceleration, wherein clean liquid exits the degasser through a liquid outlet pipeline and gas with some liquid is extracted from the degasser into a reject line and flows into a reject vessel; and
the splitter having an outlet for the gaseous phase which is connected through a gas continuous line to an inline deliquidizer that is configured to drive separation of liquid and gas by centripetal acceleration, wherein clean gas exits the deliquidizer through a gas outlet pipeline and liquid with some gas is extracted from the deliquidizer into a reject line and flows into the reject vessel.

2. The system according to claim 1 , wherein the inline degasser comprises two or more inline degassers in parallel and/or the inline deliquidizer comprises two or more inline deliquidizers in parallel.

3. The system according to claim 1 , wherein the reject vessel comprises a conventional separator.

4. The system according to claim 1 , wherein the reject vessel comprises an ID pipe section.

5. The system according to claim 1 , wherein the reject vessel comprises a connection to a stream from a process unit.

6. The system according to claim 1 , wherein a gas outlet from the reject vessel is connected to the gas outlet pipeline from the deliquidizer.

7. The system according to claim 6 , wherein a liquid outlet from the reject vessel is connected to the liquid outlet pipeline from the degasser.

8. The system according to claim 1 , further comprising a number of control valves for controlling flow through at least one of the gas outlet pipeline and the liquid outlet pipeline.

9. The system according to claim 8 , wherein the control valves are configured to be regulated in accordance with the a flow rate and composition of the well stream.

10. A method of operating a gas-liquid separation system, the gas-liquid separation system comprising a splitter which is configured to separate a well stream into liquid and gaseous phases; the splitter having an outlet for the liquid phase which is connected through a liquid continuous line to an inline degasser that is configured to drive separation of gas and liquid by centripetal acceleration, wherein clean liquid exits the degasser through a liquid outlet pipeline and gas with some liquid is extracted from the degasser into a first reject line and flows into a reject vessel; and the splitter having an outlet for the gaseous phase which is connected through a gas continuous line to an inline deliquidizer that is configured to drive separation of liquid and gas by centripetal acceleration, wherein clean gas exits the deliquidizer through a gas outlet pipeline and liquid with some gas is extracted from the deliquidizer into a second reject line and flows into the reject vessel; the method comprising:
transferring an inlet well stream to the splitter;
separating the well stream into a liquid phase and a gaseous phase in the splitter;
transferring a liquid continuous stream from the splitter into the degasser, wherein the liquid continuous stream is set into spin and centripetal acceleration drives separation of gas and liquid, and wherein clean liquid exits the degasser through the liquid outlet pipeline and gas and some liquid are extracted from the degasser into the first reject line and flow into the reject vessel;
transferring a gas continuous stream from the splitter into the deliquidizer, wherein the gas continuous stream is set into spin and centripetal acceleration drives separation of liquid and gas, and wherein clean gas exits the deliquidizer through the gas outlet pipeline and liquid and some gas are extracted from the deliquidizer into the second reject line and flow into the reject vessel;
wherein mixed liquid and gas from the first and second reject lines are separated by gravity in the shared reject vessel; and
wherein degassed liquid from the reject vessel is combined with clean liquid from the degasser in the liquid outlet pipeline and dry gas from the reject vessel is combined with clean gas from the deliquidizer in the gas outlet pipeline.

11. The method according to claim 10 , further comprising controlling flow through at least one of the gas outlet pipeline and the liquid outlet pipeline using a number of valves.

12. The system according to claim 1 , wherein the reject vessel is configured to separate the gas and liquid by gravity.

Assignees

• Fmc Kongsberg Subsea As

Inventors

• Tuvnes Henrik Johan
• Mikkelsen René
• Ellingsen Haakon

Classifications

• B01D19/0063

  Regulation, control including valves and floats (for construction and details of valves F16K) · CPC title

• B01D17/00

  Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion (devices for separating or removing fatty or oily substances or similar floating material from water, waste water, or sewage C02F1/40; cleaning or keeping clear the surface of open water from oil or like materials E02B15/04; arrangements for separating lubricants from refrigerants F25B43/02) · CPC title

• B01D17/0214

  with removal of one of the phases · CPC title

• B01D17/044

  by changing the pressure · CPC title

• B01D19/0068

  General arrangements, e.g. flowsheets (B01D19/0063 takes precedence) · CPC title