Flow conditioner for a gas transport pipe

• US 6,145,544 A
• Filed: 02/16/1999
• Issued: 11/14/2000
• Est. Priority Date: 03/13/1998
• Status: Expired due to Fees

• Current Assignee: Gaz de France
• Original Assignee: Gaz de France
• Inventors: De Laharpe, Vincent, Dutertre, Dominique
• Primary Examiner(s): HOOK, JAMES F
• Application Number:
  US09/250,122
• Time in Patent Office: 637 Days
• Field of Search: 138/39, 138/42, 366/336, 366/337, 366/338, 366/340
• US Class Current: 138/39
• CPC Class Codes: F15D 1/025 by means of orifice or throttle elements
• CPC Class Codes: F16L 55/02718 placed transversely
• CPC Class Codes: G01F 15/00 Details of, or accessories for, apparatus of groups G01F1/00 - G01F13/00 insofar as such details or appliances are not adapted to particular types of such apparatus

Abstract

The flow conditioner for a gas transport pipe comprises at least one perforated plate disposed essentially perpendicularly to the axis XX'"'"' of the pipe and comprising a central hole and sets of additional holes that are regularly distributed over at least three concentric rings centered on the axis of the pipe so as to define a perforated plate that is axially symmetrical. Within any one ring all of the circular holes are of the same diameter d₁, d₂, d₃. On going away from the central hole and on passing from any one ring to an adjacent concentric ring, the diameter of the holes changes alternately in a reduction direction and in an increase direction. Each ring has a number of holes that is equal to or greater than six. The perforated plate is advantageously associated with a porous plate situated upstream from the perforated plate and parallel thereto.

Claims

1. A flow conditioner for a gas transport pipe having an axis XX'"'"', the conditioner comprising at least one perforated plate disposed essentially perpendicularly to the axis XX'"'"' of the pipe and including a central circular hole together with sets of additional circular holes that are regularly distributed over concentric rings centered on the axis of the pipe, wherein the additional circular holes are distributed over at least three concentric rings so as to define an axially-symmetrical perforated plate, wherein within any one ring all the additional circular holes have a same diameter d₁, d₂, d₃, wherein, on going outwards from the central hole and passing to an adjacent concentric ring, the diameter of the holes changes alternately in a reduction direction and in an increase direction, wherein each ring comprises a number of holes equal to or greater than six.

2. A flow conditioner according to claim 1, wherein the perforated plate comprises a central hole, twelve holes of small diameter d₁ constituting an inner first ring, eight holes of large diameter d₂ constituting an intermediate second ring, and twenty holes of intermediate diameter d₃ constituting an outer third ring.

3. A flow conditioner according to claim 1, wherein the perforated plate comprises around the central circular hole, on going away from the axis XX'"'"' of the pipe, an inner first ring comprising a set of holes of small diameter d₁, an intermediate second ring comprising a set of holes of large diameter d₂, and an outer third ring comprising a set of holes of intermediate diameter d₃ of a size intermediate between the small diameter d₁ and the large diameter d₂.

4. A flow conditioner according to claim 3, wherein the intermediate diameter d₃ of the holes constituting the outer third ring of the perforated plate is close to a diameter d₀ of the central hole.

5. A flow conditioner according to claim 3, wherein the perforated plate is of a thickness θ

substantially equal to the large diameter d₂ of the holes of the intermediate second ring.

6. A flow conditioner according to claim 3, wherein, in the perforated plate and for D1 designating an inside diameter of the pipe with which the flow conditioner is associated;

the holes of small diameter d₁ are distributed over an inner first ring of mean diameter D₁ equal to about 0.23 D1;

the holes of large diameter d₂ are distributed over an intermediate second ring of mean diameter D₂ equal to about 0.46 D1; and

the holes of intermediate diameter d₃ are distributed over an outer third ring of mean diameter D₃ equal to about 0.84 D1.

7. A flow conditioner according to claim 3, wherein, in the perforated plate and for D1 designating an inside diameter of the pipe with which the flow conditioner is associated;

the central hole has a diameter d₀ equal to about 0.12 D1;

the holes of the inner first ring have a small diameter d₁ equal to about 0.05 D1;

the holes of the intermediate second ring have a large diameter d₂ equal to about 0.16 D1; and

the holes of the outer third ring have an intermediate diameter d₃ equal to about 0.12 D1.

8. A flow conditioner according to claim 1, wherein the perforated plate is associated with a porous plate that is situated upstream from the perforated plate and that is parallel thereto.

9. A flow conditioner according to claim 8, wherein the porous plate is made of a homogeneous material having porosity lying in the range 90% to 96%, and whose area of contact with a flow is a function of the mesh size thereof and lies in the range 500 m² /m³ to 2500 m² /m³.

10. A flow conditioner according claim 8, wherein the porous plate has a thickness of about 10 mm and is made of a very open nickel-chromium foam.

11. A flow conditioner according to claim 1, including an outer annular support for mounting between two flanges of the pipe and within which the perforated plate is placed together with the porous plate.

12. A flow conditioner according to claim 11, wherein the outer annular support has a downstream annular shoulder serving as an abutment for the perforated plate, and wherein the perforated plate is held pressed against said downstream annular shoulder by means of a removable spacer ring, the porous plate being interposed between the removable spacer ring and the perforated plate which is itself in abutment against the downstream annular shoulder.

13. A flow conditioner according to claim 12, wherein the outer annular support has radial pressure take-offs situated respectively level with the upstream removable spacer and level with the downstream shoulder to enable differential pressure measurements to be made.

14. A flow conditioner according to claim 1, disposed downstream from a regulator-expander and upstream from a meter, and is of a size in an axial direction that does not exceed about one-third of a nominal diameter DN of the gas pipe.

15. A flow conditioner according to claim 14, wherein the perforated plate is associated with a porous plate that is situated upstream from the perforated plate and that is parallel thereto, wherein the conditioner includes an external annular support for mounting between two flanges of the pipe and within which the perforated plate is placed together with the porous plate, and wherein the outer annular support is pierced by a radial hole for connecting an exhaust from a pilot of the regulator-expander, which radial hole is situated level with the porous plate to diffuse a jet caused by a pilot flow.