Blowdown and venting jet noise suppressor

• US 6,343,672 B1
• Filed: 03/23/2000
• Issued: 02/05/2002
• Est. Priority Date: 03/23/2000
• Status: Expired due to Fees

• Current Assignee: NOVA Gas Transmission Ltd. (TC Energy Corp.)
• Original Assignee: NOVA Gas Transmission Ltd. (TC Energy Corp.)
• Inventors: Jungowski, Wiktor, Petela, Grazyna
• Primary Examiner(s): Nappi, Robert E.
• Assistant Examiner(s): LOCKETT, KIMBERLY R
• Application Number:
  US09/532,438
• Time in Patent Office: 684 Days
• Field of Search: 181/210, 181/248, 181/252, 181/258, 181/279, 181/282
• US Class Current: 181/224
• CPC Class Codes: F01N 1/081 by passing the gases through a mass of particles
• CPC Class Codes: F01N 1/088 using vanes arranged on gas flow path or gas flow tubes with tangentially directed apertures
• CPC Class Codes: F01N 13/0097 the purifying devices are arranged in a single housing
• CPC Class Codes: F04C 29/063 Sound absorbing materials
• CPC Class Codes: F16K 47/08 for decreasing pressure or noise level and having a throttling member separate from the closure member , e.g. screens, slots, labyrinths

Abstract

The present invention relates to a noise suppressor capable of reducing the noise of a fluid vented at high pressure and high mass flow rate from an industrial source, to the environmentally acceptable noise level. The invention combines two principles of dissipation of fluid stream energy: first, stream pressure is reduced by passing the stream through a swirler to split the stream into a number of smaller tangential streams which dissipate their energy along the spiral flow path due to friction; and next, the resulting streams pass through a tightly packed granular bed to reduce further the pressure and velocity of the exiting jet to atmospheric pressure and subsonic velocity, respectively. Such jet will generate much lower noise level, as compared to high pressure jet with cellular structure and supersonic velocity.

Claims

1. A fluid stream pressure and velocity reducing and noise suppressing device comprising in cooperating arrangement:

A. an inlet adapted to cooperate with and receive a fluid stream from a stack of a high pressure system;

B. an annular base for receiving said inlet;

C. an annular cylindrical dissipative swirling member having an internal diameter at least equal to or larger than the diameter of said inlet and an external diameter, said swirling member comprising an annular array of enclosed radially outwardly extending swirling channels, wherein the sum of the minimum cross section areas of said channels is not less than the cross section area of the inlet, said channels having walls defined by a set of vanes mounted on said base around said inlet, to deflect, swirl and discharge said fluid stream in a radially outward and tangential manner;

D. a dissipative annular shroud member comprising;

(i) a housing mounted on said annular base, having an internal diameter larger than said external diameter of said swirling member;

(ii) an inner core mounted on the top of said annular dissipative swirling member, said inner core comprising a first part in the form of a cylindrical segment with a diameter substantially the same as said external diameter of said annular dissipative swirling member, and a second part in the form of a conical segment having a diameter at its base substantially equal to the diameter of said cylindrical segment; and

E. a diffuser being mounted upon said housing and having an opening at its lower end at least as large as the internal diameter of said housing and having one or more outwardly sloping walls, said diffuser defining a final opening of a size so that the pressure of the fluid stream at the exit of said diffuser is atmospheric and the velocity of the fluid jet is subsonic, said diffuser being tightly packed with discrete particulate packing and said diffuser having first and second grates to retain said particulate packing in said diffuser.

2. The device according to claim 1, wherein said diffuser is tightly packed with regularly shaped particles.

3. The device according to claim 2 wherein said diffuser is tightly packed with spherical particles.

4. The device according to claim 1 wherein said diffuser is tightly packed with irregular particulate packing.

5. The device according to claim 4 wherein said diffuser is tightly packed with gravel.

6. The device according to claim 1, wherein the angle α

of the walls of said diffuser is from 10°

to 50°

.

7. The device according to claim 6, wherein said diffuser is a truncated cone.

8. The device according to claim 1, wherein in said annular dissipative swirling member said vanes are uniformly radially spaced.

9. The device according to claim 8, wherein said vanes have a tangential deflective angle greater than 5°

.

10. The device according to claim 9, wherein said vanes have straight parallel deflective edges.

11. The device according to claim 9 wherein said vanes are wedged shaped.

12. The device according to claim 9, wherein said vanes are curved.

13. The device according to claim 1, wherein said internal surface of said housing has threads having a depth from 5 to 8 mm.

14. The device according to claim 1, wherein said external surface of the inner core member has threads having a depth from 5 to 8 mm.

15. The device according to claim 13, wherein the external surface of the inner core member has threads having a depth from 5 to 8 mm.

16. The device according to claim 1 wherein at least one of said first and second grates on said diffuser is removable.

17. A process to vent a fluid under pressure up to 15,000 kPa to atmospheric pressure at a subsonic velocity within a period of time adequate for an emergency shut down of the high pressure fluid, which comprises passing said one or more streams of said fluid through one or more e devices according to claim 1.

18. A process according to claim 17 wherein said time is less than 5 minutes.

19. A process to vent a fluid from a system under pressure up to 15,000 kPa, to atmospheric pressure at a subsonic velocity within a period of time adequate for a planned shut down of the high pressure fluid system, which comprises passing said one or more streams of said fluid through one or more devices according to claim 1.

20. The process according to claim 17 wherein said fluid under high pressure is in a pipeline.

21. The process according to claim 18 wherein said fluid under high pressure is in a pipeline.

22. The process according to claim 19 wherein said fluid under high pressure is in a pipeline.

23. The process according to claim 20 wherein said fluid is natural gas.

24. The process according to claim 21 wherein said fluid is natural gas.

25. The process according to claim 22 wherein said fluid is natural gas.