Isobaric pressure exchanger in amine gas processing

Patent metadata

Field	Value
Publication number	US-9604889-B2
Application number	US-201314074530-A
Country	US
Kind code	B2
Filing date	Nov 7, 2013
Priority date	Nov 8, 2012
Publication date	Mar 28, 2017
Grant date	Mar 28, 2017

Abstract

A system includes an amine gas processing system that includes a contactor configured to remove an acid gas from an untreated natural gas using an amine in a lean amine stream, output a treated natural gas, and output a rich amine stream. The system also includes a regenerator configured to regenerate the amine in the rich amine stream, output the lean amine stream, and output the acid gas. The system also includes an isobaric pressure exchanger (IPX) configured to transfer the rich amine stream from the contactor to the regenerator and to transfer the lean amine stream from the regenerator to the contactor.

First claim

The invention claimed is:

1. A system, comprising:
an amine gas processing system, comprising:
a contactor configured to remove an acid gas from an untreated natural gas using an amine in a lean amine stream, output a treated natural gas, and output a rich amine stream;
a regenerator configured to regenerate the amine in the rich amine stream, output the lean amine stream, and output the acid gas; and
an isobaric pressure exchanger configured to transfer the rich amine stream from the contactor to the regenerator and to transfer the lean amine stream from the regenerator to the contactor, wherein the isobaric pressure exchanger is configured to transfer pressure from the rich amine stream entering the isobaric pressure exchanger at a first pressure to the lean amine stream leaving the isobaric pressure exchanger at a second pressure, wherein the first pressure is greater than the second pressure.

2. The system of claim 1 , wherein the isobaric pressure exchanger comprises at least one of a rotary isobaric pressure exchanger, a non-rotary isobaric pressure exchanger, a reciprocating isobaric pressure exchanger, or a bladder-based isobaric pressure exchanger, or any combination thereof.

3. The system of claim 1 , wherein an outer housing of the isobaric pressure exchanger comprises duplex stainless steel.

4. The system of claim 1 , wherein the isobaric pressure exchanger comprises at least one of flanged connectors, or threaded connectors, or any combination thereof.

5. The system of claim 1 , wherein the isobaric pressure exchanger comprises:
a housing having a body portion;
first and second ends plates at opposite ends of the body portion, wherein each of the end plates has an inlet aperture and an outlet aperture for respective liquid flow; and
a rotor disposed in the body portion of the housing, wherein the rotor has ends in substantially sealing contact with the end plates, wherein the rotor has at least one channel therein extending substantially longitudinally from one end of the rotor to an opposite end of the rotor, wherein the channel has an opening in each of the ends of the rotor configured to contain at least one of the rich amine stream, or the lean amine stream, or any combination thereof.

6. The system of claim 1 , comprising a flow control valve configured to transfer the rich amine stream from the contactor to the regenerator, wherein the flow control valve is disposed in a rich amine bypass loop around the isobaric pressure exchanger.

7. The system of claim 1 , comprising a flow control valve disposed between the isobaric pressure exchanger and the regenerator, wherein the flow control valve is configured to adjust a flow rate of the rich amine stream to the regenerator.

8. The system of claim 1 , comprising a first pump configured to transfer the lean amine stream from the regenerator to the isobaric pressure exchanger.

9. The system of claim 8 , comprising a second pump configured to transfer the lean amine stream from the regenerator to the first pump.

10. The system of claim 1 , comprising a circulation pump configured to transfer the lean amine stream from the isobaric pressure exchanger to the contactor.

11. The system of claim 1 , comprising a third pump configured to transfer the lean amine stream from the regenerator to the contactor, wherein the third pump is disposed in a lean amine bypass loop around the isobaric pressure exchanger.

12. The system of claim 1 , wherein the isobaric pressure exchanger comprises an integrated fourth pump configured to transfer the lean amine stream from the isobaric pressure exchanger to the contactor.

13. A system, comprising:
an amine gas processing system, comprising:
a contactor configured to remove an acid gas from an untreated natural gas using an amine in a lean amine stream, output a treated natural gas, and output a rich amine stream;
a regenerator configured to regenerate the amine in the rich amine stream, output the lean amine stream, and output the acid gas;
an isobaric pressure exchanger configured to transfer the rich amine stream from the contactor to the regenerator and to transfer the lean amine stream from the regenerator to the contactor, and the isobaric pressure exchanger is configured to transfer pressure from the rich amine stream entering the isobaric pressure exchanger at a first pressure to the lean amine stream leaving the isobaric pressure exchanger at a second pressure, wherein the first pressure is greater than the second pressure, wherein the isobaric pressure exchanger comprises:
a housing having a body portion;
first and second ends plates at opposite ends of the body portion, wherein each of the end plates has an inlet aperture and an outlet aperture for respective liquid flow; and
a rotor disposed in the body portion of the housing, wherein the rotor has ends in substantially sealing contact with the end plates, wherein the rotor has at least one channel therein extending substantially longitudinally from one end of the rotor to an opposite end of the rotor, wherein the channel has an opening in each of the ends of the rotor configured to contain at least one of the rich amine stream, or the lean amine stream, or any combination thereof;

a flow control valve configured to transfer the rich amine stream from the contactor to the regenerator, wherein the flow control valve is disposed in a rich amine bypass loop around the isobaric pressure exchanger;
a first pump configured to transfer the lean amine stream from the regenerator to the isobaric pressure exchanger; and
a circulation pump configured to transfer the lean amine stream from the isobaric pressure exchanger to the contactor.

Assignees

• Energy Recovery Inc

Inventors

• Arluck James Lee
• Martin Jeremy Grant
• Krish Prem

Classifications

• F04F13/00

  Pressure exchangers · CPC title

• C07C9/04

  Methane (production by treatment of sewage C02F11/04; natural gas, synthetic natural gas C10L3/06) · CPC title

• C07C7/11 Primary

  by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids · CPC title

• C10L3/102

  of acid contaminants · 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