Centrifugal separator and method for determining suitable moment for removal of heavy phase content

Patent metadata

Field	Value
Publication number	US-9975127-B2
Application number	US-201414787358-A
Country	US
Kind code	B2
Filing date	May 27, 2014
Priority date	May 27, 2013
Publication date	May 22, 2018
Grant date	May 22, 2018

Abstract

A centrifugal separator for separating a fluid mixture into components, including a non-rotating part, a rotor which is attached to a shaft which is rotatably supported in the non-rotating part around a rotational axis, which rotor forms within itself a separation space delimited by a rotor wall. The separator includes an inlet extending into the rotor for supply of a fluid mixture to be separated in the separation space, at least one sensor measuring unbalance conditions in the frame; a level determining arrangement including two or more space defining elements of arbitrary form arranged on the interior surface of, or close to, the rotor wall, where each space defining element defines a space which communicates with the separation space or another of the space defining elements through at least one inlet opening arranged at a certain radius from the rotational axis and not outside that radius and where that certain radii of the space defining elements are different. Methods for determining when a predetermined amount of heavy phase fluid (purification) or sludge (clarification) has been separated are also disclosed. The separator and methods make it possible to determine when the level of separated heavy phase fluid or sludge is high enough for emptying or discharge of the separator.

First claim

The invention claimed is:

1. A centrifugal separator for separating a fluid mixture into components, comprising:
a non-rotating part;
a rotor, said rotor being attached to a shaft rotatably supported in the non-rotating part around a rotational axis, the rotor forming within itself a separation space delimited by a rotor wall;
an inlet extending into the rotor for supply of a fluid mixture to be separated in the separation space;
at least one sensor measuring unbalance conditions in the non-rotating part; and
a heavy phase level determining arrangement comprising two or more space defining elements arranged on an interior surface of, or close to, the rotor wall,
wherein each space defining element defines a space which communicates with the separation space or another of said space defining elements through at least one inlet opening arranged at a certain radius from the rotational axis, and
wherein certain radii of the space defining elements are different, and the space defining elements being provided to displace a heavy phase component until a heavy phase level reaches the inlet opening of the respective space defining element.

2. The centrifugal separator according to claim 1 , wherein at least two space defining elements are arranged at different angular positions around the rotational axis.

3. The centrifugal separator according to claim 1 , wherein at least two space defining elements are arranged opposite each other, one space defining element on each side of the rotational axis.

4. The centrifugal separator according to claim 1 , wherein the space defining elements are diametrically opposed.

5. The centrifugal separator according to claim 1 , wherein a shape of the space defining elements is that of a truncated cone or a truncated tri-, quadric- or polylateral pyramid, and
wherein walls of the space defining elements provide a tapering and a roof marks the truncation.

6. The centrifugal separator according to claim 1 , wherein a roof of each of the space defining elements is inclined.

7. The centrifugal separator according to claim 5 , wherein the roof of each of the space defining elements is a mansard roof.

8. The centrifugal separator according to claim 1 , where the space defining elements have at least one evacuation opening, each evacuation opening being placed radially more inwardly than the inlet opening.

9. A method for determining when a predetermined amount of heavy phase fluid has been separated in a centrifugal separator according to claim 1 , said method comprising the steps of:
bringing the rotor to rotate;
filling the rotor with fluid to be separated; and
where said heavy phase fluid is forming a growing peripheral layer on the inside of the rotor wall:
continually measuring the unbalance condition in the non-rotating part;
determining a first signal deriving from a first change in vibrations in the non-rotating part, said first change signal indicating a first level of separated heavy phase fluid being present in the rotor, where said first change derives from a first change in distribution of said heavy phase fluid layer around the periphery of the rotor wall;
determining a second signal deriving from a second change in vibrations in the non-rotating part, said second change signal indicating a second level of separated heavy phase fluid slightly higher than said first level, being present in the rotor, where said second change derives from a second change in distribution of said heavy phase fluid layer around the periphery of the rotor wall; and
upon determination of both the first and the second signals, initiation of emptying or discharging of the separator rotor of heavy-phase fluid.

10. A method for determining when a predetermined amount of sludge has been separated in a centrifugal separator according to claim 1 , said method comprising the steps of:
bringing the rotor to rotate;
filling the rotor with fluid to be separated;
where said sludge is forming a growing peripheral layer on the inside of the rotor wall:
stopping the flow of fluid to be separated;
continually measuring the unbalance condition in the non-rotating part; and
then adding an amount of indicating fluid having higher density than the fluid to be separated but lower than the sludge;
where said indicating fluid is forming a layer on the inside of said sludge layer:
determining a first signal deriving from a first change in vibrations in the non-rotating part, said first change signal indicating a first level of separated sludge plus the indicating fluid being present in the rotor, where said first change derives from a first change in distribution of the indicating fluid layer;
determining a second signal deriving from a second change in vibrations in the non-rotating part, said second change signal indicating a second level of separated sludge plus indicating fluid slightly higher than said first level, where said second change derives from a second change in distribution of the indicating fluid layer; and
upon determination of both the first and the second signals, initiation of emptying or discharging of the separator rotor of sludge.

Assignees

• Alfa Laval Corp Ab

Inventors

• Hillström Lars
• Moberg Hans
• Rundström Finn
• Thorwid Peter
• Isaksson Roland
• Skoog Jan

Classifications

• B04B9/146

  Imbalance detection devices · CPC title

• B04B11/04

  Periodical feeding or discharging; Control arrangements therefor · CPC title

• B04B1/14 Primary

  with periodical discharge · CPC title

• B04B13/00 Primary

  Control arrangements specially designed for centrifuges; Program control of centrifuges (control arrangements for feed, charge or discharge B04B11/00) · CPC title

• B04B11/043

  Load indication with or without control arrangements · CPC title