Systems and methods for utilizing turbine systems within gas processing systems

Patent metadata

Field	Value
Publication number	US-9764272-B2
Application number	US-201414525081-A
Country	US
Kind code	B2
Filing date	Oct 27, 2014
Priority date	Oct 28, 2013
Publication date	Sep 19, 2017
Grant date	Sep 19, 2017

Abstract

A system includes a solvent gas processing system having a high pressure reaction vessel configured to remove an acid gas from an untreated feed gas using a solvent in a lean solvent fluid stream. The system includes a high pressure reaction vessel is configured to output a treated clean gas and a first flow of a high pressure fluid stream via a first flow path. The system includes a turbine having a main nozzle, an auxiliary nozzle, and an outlet. The main nozzle is configured to receive a second flow of the high pressure fluid stream from the first flow path via a main flow path. The system includes an auxiliary nozzle valve disposed along an auxiliary flow path. The auxiliary nozzle valve is configured to control a third flow of the high pressure fluid stream into the auxiliary nozzle of the turbine.

First claim

The invention claimed is:

1. A system, comprising:
a solvent gas processing system, comprising:
a high pressure reaction vessel configured to remove an acid gas from an untreated feed gas using a solvent in a lean solvent fluid stream, wherein the high pressure reaction vessel is configured to output a treated clean gas and a first flow of a high pressure fluid stream via a first flow path;
a turbine having a main nozzle, an auxiliary nozzle, and an outlet, wherein the main nozzle is configured to receive a second flow of the high pressure fluid stream from the first flow path via a main flow path, and wherein the second flow of the high pressure fluid stream is a portion of the first flow, and wherein the high pressure fluid stream is configured to drive the turbine;
an auxiliary nozzle valve disposed along an auxiliary flow path, wherein the auxiliary nozzle valve is configured to control a third flow of the high pressure fluid stream into the auxiliary nozzle of the turbine, and wherein the third flow of the high pressure fluid stream is a portion of the first flow;
a first throttle valve disposed along an outlet flow path, wherein the first throttle valve is configured to control a fourth flow of a low pressure fluid stream out of the outlet; and
a bypass valve disposed along a bypass flow path, wherein the bypass flow path routes a portion of the high pressure fluid stream from the first flow path directly to the outlet flow path.

2. The system of claim 1 , wherein the auxiliary nozzle valve is configured to open or partially open when the first flow or a desired first flow of the high pressure fluid stream is greater than a first flow capacity of the main nozzle.

3. The system of claim 2 , wherein the auxiliary nozzle valve is configured to close or partially close when the first flow or the desired first flow of the high pressure fluid stream is less than the first flow capacity of the main nozzle.

4. The system of claim 1 , wherein the bypass valve is configured to open or partially open when the third flow or a desired third flow of the high pressure fluid stream is greater than a second flow capacity of the auxiliary nozzle.

5. The system of claim 1 , wherein the first throttle valve is configured to close or partially close when the first flow or a desired first flow of the high pressure fluid stream is less than a first flow capacity of the main nozzle.

6. The system of claim 5 , wherein the first throttle valve is configured to close or partially close when the fourth flow or a desired fourth flow of the low pressure fluid stream from the outlet is less than a third flow capacity of the outlet.

7. The system of claim 1 , comprising a second throttle valve disposed along the main flow path or the first flow path, wherein the second throttle valve is configured to control the flow of the high pressure fluid stream from the high pressure reaction vessel.

8. The system of claim 1 , wherein the turbine is configured to receive a first pressure of the high pressure fluid stream and output a second pressure of the low pressure fluid stream, and wherein the turbine is configured to generate rotational mechanical energy based on the difference between the first pressure and the second pressure.

9. The system of claim 1 , comprising a controller configured to receive feedback related to at least one operating parameter of the system, wherein the controller is configured to adjust an operating parameter of the system to control the first flow of the high pressure stream.

10. A system, comprising:
a high pressure reaction vessel configured to remove an acid gas from an untreated feed gas using a solvent in a lean solvent stream, wherein the high pressure reaction vessel is configured to output a treated clean gas and a first flow of a high pressure fluid stream via a first flow path; and
a solvent gas processing controller comprising at least one processor, and a memory configured to execute instructions stored on the memory, wherein the at least one processor is configured to:
receive feedback from one or more sensors disposed throughout a solvent gas processing system related to one or more operating parameters of the solvent gas processing system;
determine whether the first flow of the high pressure fluid stream from the high pressure reaction vessel and into a turbine system is within an operational flow range for a main nozzle of the turbine system based on the received feedback;
open an auxiliary nozzle valve if the first flow of the high pressure fluid stream exceeds the operational flow range; and
close the auxiliary nozzle valve if the first flow of the high pressure fluid stream falls below the operational flow range;
wherein the one or more sensors comprises a level transmitter disposed within the high pressure reaction vessel, and wherein the level transmitter is configured to transmit information related to the first flow of the high pressure fluid stream.

11. The system of claim 10 , wherein the one or more operating parameters of the system comprises a pressure, a flow rate, a temperature, or a combination thereof.

12. The system of claim 10 , wherein the controller is configured to adjust a bypass valve or a throttle valve to increase or decrease the first flow of the high pressure fluid stream into the turbine system.

13. The system of the claim 12 , wherein the controller is configured to adjust the throttle valve to increase or decrease a second flow of a low pressure fluid stream exiting the turbine system.

14. The system of claim 10 , wherein the controller comprises a display having user inputs and outputs configured to receive the operational flow range from an operator.

15. A method, comprising:
removing an acid gas from an untreated feed gas within a high pressure reaction vessel, wherein the high pressure reaction vessel is configured to output a treated clean gas and a first flow of a high pressure fluid stream via a first flow path;
receiving the first flow of the high pressure stream from the high pressure reaction vessel via a turbine system, wherein the high pressure stream is configured to drive the turbine system;
determining, via a solvent gas processing controller, whether the first flow of the high pressure fluid stream falls within an operational flow range of a main nozzle of the turbine system;
adjusting one or more operational parameters of the turbine system if the first flow of the high pressure fluid stream falls outside of the operational flow range of the main nozzle;
controlling an auxiliary nozzle valve, a bypass valve, or a throttle valve to increase or decrease the first flow of the high pressure fluid stream to the turbine system if the first flow of the high pressure fluid stream falls outside of the operational flow range of the main nozzle; and
controlling the bypass valve or the throttle valve to increase or decrease the first flow of the high pressure stream to the turbine system if the first flow of the high pressure fluid stream falls outside of the operational flow range of the main nozzle and a second operational flow range of the auxiliary nozzle.

16. The method of claim 15 , wherein adjusting the one or more operational parameters comprises controlling the first flow of the high pressure fluid stream through the turbine system.

17. A system, comprising:
a solvent gas processing system, comprising:
a high pressure reaction vessel configured to remove an acid gas from an untreated feed gas using a solvent in a lean solvent fluid stream, wherein the high pressure reaction vessel is configured to output a

Assignees

• Energy Recovery Inc
• Energy Recovery Inc

Inventors

• Martin Jeremy Grant
• Sienkiewicz John
• Krish Prem
• Ma Ying
• Richter Mark
• Winkler Felix

Classifications

• B01D53/1475

  Removing carbon dioxide · CPC title

• B01D53/1456 Primary

  Removing acid components · CPC title

• B01D53/1468

  Removing hydrogen sulfide · CPC title

• B01D2256/24

  Hydrocarbons · CPC title

• B01D53/18

  Absorbing units; Liquid distributors therefor (B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32) · CPC title