Liquefaction system using a turboexpander

Patent metadata

Field	Value
Publication number	US-10072889-B2
Application number	US-201514749390-A
Country	US
Kind code	B2
Filing date	Jun 24, 2015
Priority date	Jun 24, 2015
Publication date	Sep 11, 2018
Grant date	Sep 11, 2018

Abstract

The subject matter disclosed herein relates to a liquefaction system. Specifically, the present disclosure relates to systems and methods for condensing a pressurized gaseous working fluid, such as natural gas, using at least one turboexpander in combination with other cooling devices and techniques. In one embodiment, a turboexpander may be used in combination with a heat exchanger using vapor compression refrigeration to condense natural gas.

First claim

The invention claimed is:

1. A gas feed liquefaction system, comprising:
a flow path configured to convey a working fluid comprising a pressurized vapor in a downstream direction;
an initial cooling phase in a first heat exchange :relationship with the flow path, wherein the initial cooling phase comprises a heat exchanger;
a compressor positioned downstream of the initial cooling phase;
a second cooling phase in a second heat exchange relationship with the flow path, wherein the second cooling phase is downstream from the compressor and comprises a first turboexpander and a second turboexpander are arranged in a series configuration, wherein the first turboexpander is configured to simultaneously provide power to the compressor, cool the pressurized vapor, and condense at least a portion of the pressurized vapor into a liquid, and wherein the second turboexpander is configured to simultaneously provide power to an additional compressor, cool a remaining portion of the pressurized vapor into the liquid;
a separation vessel downstream of the second turboexpander and configured to separate a second portion of the remaining portion of the pressurized vapor from the liquid; and
a recycle stream configured to direct the second portion of the remaining portion of the pressurized vapor through the heat exchanger toward a mixer, wherein the mixer is configured to combine the second portion of the remaining portion of the pressurized vapor with the flow path upstream of the second cooling phase.

2. The gas feed liquefaction system of claim 1 , wherein one or both of the first turboexpander and the second turboexpander comprises between 7 and 15 stages.

3. The gas feed liquefaction system of claim 1 , wherein the second cooling phase comprises a third turboexpander.

4. The gas feed liquefaction system of claim 1 , wherein the heat exchanger is configured to transfer thermal energy from the flow path to a refrigerant of a vapor compression refrigeration cycle.

5. The gas feed liquefaction system of claim 1 , comprising an additional separation vessel along the flow path upstream of the compressor and downstream of the initial cooling phase, wherein the additional separation vessel is configured to remove heavy hydrocarbons or contaminants from flow path.

6. The gas feed liquefaction system of claim 1 , wherein a pressure ratio across at least one of the first turboexpander and the second turboexpander is between 1 and 5.

7. The gas feed liquefaction system of claim 1 , wherein a pressure of the flow path upstream of the initial cooling phase is greater than 40 atmosphere.

8. The gas feed liquefaction system of claim 1 , comprising a moisture removal device upstream of the initial cooling phase.

9. The gas feed liquefaction system of claim 1 , comprising a third cooling phase upstream of the initial cooling phase, wherein the third cooling phase comprises a vapor compression refrigeration cycle.

10. The gas feed liquefaction system of claim 9 , wherein the recycle stream is configured to pass through the third cooling phase before entering the mixer.

11. The gas feed liquefaction system of claim 1 , wherein the first turboexpander is configured to separate the remaining portion of the pressurized vapor from the liquid and configured to direct the remaining portion of the pressurized vapor or the liquid to the second turboexpander.

12. A gas feed liquefaction system, comprising:
a flow path configured to convey a working fluid comprising a pressurized vapor in a downstream direction;
an initial cooling phase in a first heat exchange relationship with the flow path, wherein the initial cooling phase comprises a heat exchanger;
a compressor positioned downstream of the initial cooling phase;
a second cooling phase in a second heat exchange relationship with the flow path, wherein the second cooling phase is downstream from the compressor and comprises a first turboexpander and a second turboexpander are arranged in a series configuration, wherein the first turboexpander is configured to simultaneously provide power to the compressor, cool the pressurized vapor, and condense at least a portion of the pressurized vapor into a liquid, and the second turboexpander is configured to simultaneously provide power to an additional compressor, cool a remaining portion of the pressurized vapor, and condense at least a first portion of the remaining portion of the pressurized vapor into the liquid;
a splitter positioned downstream of the first turboexpander and upstream of the second turboexpander, wherein the splitter directs a first stream of the flow path through the heat exchanger and a second stream of the flow path to the second turboexpander, wherein the second stream comprises the remaining portion of the pressurized vapor;
a separation vessel downstream of the second turboexpander and configured to separate a second portion of the remaining portion of the pressurized vapor from the liquid; and
a recycle stream configured to direct the second portion of the remaining portion of the pressurized vapor through the heat exchanger to a mixer, wherein the mixer is configured to combine one or more of the first stream, the second portion, and the flow path upstream of the second cooling phase.

13. The gas feed liquefaction system of claim 12 , wherein one or both of the first turboexpander and the second turboexpander comprises between 7 and 15 stages.

14. The gas feed liquefaction system of claim 12 , wherein the additional compressor is configured to compress the first stream and direct the first stream towards the mixer.

15. The gas feed liquefaction system of claim 12 , wherein a pressure ratio across at least one of the first turboexpander and the second turboexpander is between 1 and 5.

Assignees

• Gen Electric

Inventors

• Lissianski Vitali Victor
• Hofer Douglas Carl
• Shisler Roger Allen
• Sipoecz Nikolett
• Bi Xianyun

Classifications

• F25J1/0283

  Gas turbine as the prime mechanical driver · CPC title

• F25J2245/02

  Recycle of a stream in general, e.g. a by-pass stream · CPC title

• F25J1/021

  using a deep flash recycle loop · CPC title

• F25J2240/40

  Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval · CPC title

• F25J1/004

  by flash gas recovery (F25J1/0267 takes precedence) · CPC title