Method for monitoring flow in centrifugal separator

Patent metadata

Field	Value
Publication number	US-12042802-B2
Application number	US-201917260928-A
Country	US
Kind code	B2
Filing date	Sep 5, 2019
Priority date	Sep 5, 2018
Publication date	Jul 23, 2024
Grant date	Jul 23, 2024

Abstract

A centrifugal separator for industrial separation of a liquid-gas mixture, including a centrifugal separator body having a centrifugal separator body wall, the centrifugal separator body including a cylindrical section and a conical section, a gas outlet positioned at the top end of the centrifugal separator body and a liquid outlet positioned at the bottom end of the centrifugal separator body, the centrifugal separator body further including a liquid-gas mixture inlet orifice, positioned in the cylindrical section of the centrifugal separator body, and a detector for detecting the thickness of the liquid on the centrifugal separator body wall, wherein the detector is positioned in the cylindrical section. A method for monitoring the flow through such a centrifugal separator.

First claim

The invention claimed is:

1. A centrifugal separator for industrial separation of a liquid-gas mixture, comprising:
a centrifugal separator body having a centrifugal separator body wall, the centrifugal separator body comprising a cylindrical section positioned vertically above a conical section;
a gas outlet positioned at a top end of the cylindrical section of the centrifugal separator body;
a liquid outlet positioned at a bottom end of the conical section of the centrifugal separator body; and
a liquid-gas mixture inlet orifice extending through the centrifugal separator body wall in the cylindrical section of the centrifugal separator body, the liquid-gas mixture inlet orifice being spaced apart from and below the gas outlet,
wherein the centrifugal separator body further comprises means for detecting a thickness of the liquid on the centrifugal separator body wall, wherein the means for detecting the thickness of the liquid are positioned in the cylindrical section between the gas outlet and the liquid-gas mixture inlet orifice.

2. The centrifugal separator according to claim 1 , wherein the means for detecting is positioned in an upper half of the cylindrical section.

3. The centrifugal separator according to claim 1 , wherein the means for detecting is positioned between a height of at least 50% to at most 67% of the height of the cylindrical section.

4. The centrifugal separator according to claim 1 , wherein the liquid-gas mixture inlet orifice is provided in a bottom half of the cylindrical section.

5. The centrifugal separator according to claim 1 , wherein the centrifugal separator separates a gas and liquid mixture, wherein the liquid comprises at least one nitrate salt.

6. The centrifugal separator according to claim 1 , wherein the centrifugal separator separates a gas and liquid mixture, wherein the liquid has a salt concentration of at least 0 to at most 1600 g/l.

7. The centrifugal separator according to claim 1 , wherein the centrifugal separator separates a gas and liquid mixture, wherein the liquid has density of at least 10 kg/m 3 to at most 2000 kg/m 3 .

8. The centrifugal separator according to claim 1 , wherein a ratio between a height of the position of the means for detecting in the cylindrical section and a height of the liquid-gas mixture inlet orifice in the cylindrical section is greater than 1.0/1.0.

9. The centrifugal separator according to claim 8 , wherein the ratio is at least 1.3/1.0.

10. The centrifugal separator according to claim 8 , wherein the ratio is at least 1.6/1.0.

11. The centrifugal separator according to claim 1 , wherein the means for detecting comprises a wave source and a wave detector.

12. The centrifugal separator according to claim 11 , wherein the wave source emits gamma-rays.

13. The centrifugal separator according to claim 11 , wherein the wave source and the wave detector are positioned at a same height.

14. The centrifugal separator according to claim 11 , wherein the wave source is an electromagnetic wave source and the wave detector is an electromagnetic wave detector.

15. A method for detecting a thickness of a liquid layer of a liquid moving along a symmetrical spiral path within a centrifugal separator, the centrifugal separator comprising a centrifugal separator body having a centrifugal separator body wall, the centrifugal separator body comprising a cylindrical section positioned vertically above a conical section, a gas outlet positioned at a top end of the cylindrical section of the centrifugal separator body and a liquid outlet positioned at a bottom end of the conical section of the centrifugal separator body, a liquid-gas mixture inlet orifice extending through the centrifugal separator body wall in the cylindrical section of the centrifugal separator body, the liquid-gas mixture inlet orifice being spaced apart from and below the gas outlet, wherein the centrifugal separator body further comprises means for detecting the thickness of the liquid on the centrifugal separator body wall, said means for detecting being positioned in the cylindrical section between the gas outlet and the liquid-gas mixture inlet orifice,
wherein the method comprises steps of:
a) providing a flow of the liquid moving along a symmetrical spiral path within the centrifugal separator;
b) monitoring an output signal of the means for detecting;
c) converting the output signal to a liquid thickness.

16. The method of claim 15 , wherein the centrifugal separator is a centrifugal separator according to claim 1 .

17. The method according to claim 15 , wherein the liquid comprises at least one nitrate salt.

18. The method according to claim 15 , wherein the liquid has a salt concentration of at least 0 to at most 1600 g/l.

19. The method according to claim 15 , wherein the liquid has density of at least 10 kg/m 3 to at most 2000 kg/m 3 .

Assignees

• Yara Int Asa

Inventors

• Bujalski Jakub
• Karlsen Stine
• Andersen Lars-Erik

Classifications

• B04C3/00

  Apparatus in which the axial direction of the vortex {flow following a screw-thread type line} remains unchanged {; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct (combined with other devices B04C9/00)} · CPC title

• G01F23/288

  X-rays; Gamma rays {or other forms of ionising radiation} · CPC title

• B04C5/00

  Apparatus in which the axial direction of the vortex is reversed {(combined with other devices B04C9/00)} · CPC title

• B01D19/0063

  Regulation, control including valves and floats (for construction and details of valves F16K) · CPC title

• B01D19/0057

  the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet · CPC title