Combination of expansion and cooling to enhance separation

• US 8,657,935 B2
• Filed: 05/19/2011
• Issued: 02/25/2014
• Est. Priority Date: 07/20/2010
• Status: Expired due to Fees

• Current Assignee: Dresser-Rand Group Incorporated (Siemens AG)
• Original Assignee: Dresser-Rand Group Incorporated (Siemens AG)
• Inventors: Lardy, Pascal, Kidd, H. Allan, Maier, William C.
• Primary Examiner(s): Bui, Dung H
• Application Number:
  US13/704,797
• Publication Number:
  US 20130298764A1
• Time in Patent Office: 1,013 Days
• Field of Search: 553/15, 55317-319, 55400-401, 554/67, 554/06, 952/71, 626/46, 415/121.2
• US Class Current: 95/271
• CPC Class Codes: B01D 19/0036 Flash degasification the other groups take precedence
• CPC Class Codes: B01D 19/0042 modifying the liquid flow B01D19/0021 takes precedence
• CPC Class Codes: B01D 45/12 by centrifugal forces centrifuges B04B; cyclones B04C

Abstract

A method and system for expanding, separating, and compressing a multi-phase fluid. An expander receives and expands the multi-phase fluid to generate a lower-pressure fluid which can more efficiently be separated in a separator. Expanding the fluid also drives a main shaft adapted to drive at least the separator and a compressor coupled thereto. The separator receives the lower-pressure fluid, separates any higher-density components from the lower-density components disposed therein, and provides a substantially dry gas to the compressor to be re-compressed and discharged from the system.

Claims

1. A fluid separation apparatus, comprising:

an expander coupled to a main shaft and configured to receive and expand a working fluid feed stream, the expander being adapted to provide rotational energy to the main shaft and generate an expander outlet feed stream having a lower pressure than the working fluid feed stream;

a rotary separator coupled to and driven by the main shaft, the rotary separator being configured to receive the expander outlet feed stream and separate higher-density components from lower-density components in the expander outlet feed stream, thereby generating a separated lower-density feed stream and a separated higher-density stream; and

a compressor coupled to and driven by the main shaft, the compressor being configured to receive the separated lower-density feed stream from the rotary separator and increase a pressure of the separated lower-density feed stream to generate a compressed lower-density stream.

2. The fluid separation apparatus of claim 1, wherein the expander is an axial flow turbine.

3. The fluid separation apparatus of claim 1, wherein the compressor is a multi-stage centrifugal compressor.

4. The fluid separation apparatus of claim 1, wherein the working fluid feed stream has an inlet pressure of about 3,000 psi and the expander is configured to lower the inlet pressure to less than or equal to about 1,500 psi.

5. The fluid separation apparatus of claim 4, wherein the separated lower-density feed stream has a pressure of about 1,500 psi or less and the compressor is configured to raise the pressure to greater than 3,000 psi.

6. The fluid separation apparatus of claim 1, wherein the rotary separator is configured to direct the separated higher-density stream through a separator discharge outlet.

7. The fluid separation apparatus of claim 1, wherein the expander is configured to separate a higher-density working fluid component from a lower-density working fluid component in the working fluid feed stream and direct the higher-density working fluid component through an expander discharge outlet.

8. The fluid separation apparatus of claim 1, wherein the compressor is configured to separate a separable higher-density component from the lower-density feed stream and direct the separable higher-density component through a compressor discharge outlet.

9. The fluid separation apparatus of claim 1, further comprising a static separator disposed about the rotary separator.

10. The fluid separation apparatus of claim 1, further comprising an auxiliary motor coupled to the main shaft to provide supplemental rotational energy to the main shaft.

11. The fluid separation apparatus of claim 1, further comprising one or more magnetic bearings configured to rotationally support the main shaft.

12. A method for removing higher-density components from lower-density components in a working fluid feed stream, comprising:

expanding the working fluid feed stream in an expander to generate an expander outlet feed stream, the expander being coupled to a shaft;

generating rotational energy with the expander that is transferred to the shaft;

driving a separator using the rotational energy to separate higher-density components from lower-density components present in the expander outlet feed stream;

discharging a separated lower-density feed stream from the separator into a compressor;

driving the compressor using the rotational energy; and

compressing the separated lower-density feed stream to generate a compressed lower-density stream.

13. The method of claim 12, further comprising directing the higher-density components through a separator discharge outlet.

14. The method of claim 12 further comprising:

separating with the expander a higher-density working fluid component from a lower-density working fluid component in the working fluid feed stream; and

directing the higher-density working fluid component through an expander discharge outlet.

15. The method of claim 12 further comprising:

separating with the compressor a separable higher-density component from the separated lower-density feed stream; and

directing the separable higher-density component through a compressor discharge outlet.

16. The method of claim 12, further comprising supplying supplemental rotational energy to the shaft via an auxiliary motor.

17. The method of claim 12, further comprising lowering the pressure of the working fluid feed stream in the expander from about 3,000 psi to less than or equal to about 1,500 psi.

18. The method of claim 12, further comprising compressing the separated lower-density feed stream with the compressor to a pressure of about 3,000 psi or higher.

19. A fluid separation apparatus, comprising:

an expander coupled to a main shaft and configured to receive and expand a working fluid feed stream, the expander being adapted to provide rotational energy from the working fluid feed stream to the main shaft and generate an expander outlet feed stream having a lower pressure than the working fluid feed stream;

a rotary separator coupled to and driven by the main shaft, the rotary separator being configured to receive the expander outlet feed stream and separate a higher-density component from a lower-density component in the expander outlet feed stream, thereby generating a separated lower-density feed stream and a separated higher-density stream;

a static separator disposed about the rotary separator;

a multi-stage centrifugal compressor coupled to and driven by the main shaft, the compressor being configured to receive and compress the separated lower-density feed stream to generate a compressed lower-density stream; and

an auxiliary motor coupled to the main shaft and configured to provide supplemental rotational energy to the main shaft.

20. The apparatus of claim 19, further comprising:

a first housing having the expander, rotary separator, and static separator disposed therein; and

a second housing coupled to the first housing and having the multi-stage compressor disposed therein.