Separator and a method for separating milk

Patent metadata

Field	Value
Publication number	US-12022795-B2
Application number	US-201816954677-A
Country	US
Kind code	B2
Filing date	Nov 6, 2018
Priority date	Dec 19, 2017
Publication date	Jul 2, 2024
Grant date	Jul 2, 2024

Abstract

A separator for separating raw milk into a skimmed milk phase, a cream phase and an ejection phase that comprises solid impurities is disclosed. The separator includes an ejection port arranged at a periphery of the separator to eject the ejection phase. A cyclone is connected to the ejection port to receive and decelerate the ejection phase, and a vessel in fluid communication with an ejection phase outlet of the cyclone to receive and collect the ejection phase from the cyclone. The cyclone includes a port that is open to the atmosphere, such that pressure build-up created in the cyclone when the ejection phase is ejected from the separator into the cyclone is released.

First claim

The invention claimed is:

1. A separator for separating raw milk into a skimmed milk phase, a cream phase and an ejection phase that comprises solid impurities, the separator comprises:
a centrifuge bowl comprising
an inlet for the raw milk and outlets for the skimmed milk phase and the cream phase,
an ejection port arranged at a periphery of the centrifuge bowl to eject the ejection phase from the centrifuge bowl,

a cyclone connected to the ejection port to receive and decelerate the ejection phase ejected from the centrifuge bowl, the cyclone comprising an ejection phase outlet and a pressure release port, and
a vessel in fluid communication with the ejection phase outlet of the cyclone to receive and collect the ejection phase from the cyclone,
wherein the cyclone is configured such that, when the cyclone is operating to receive the ejection phase from the centrifuge bowl:
(i) the pressure release port is open directly to the atmosphere to release pressure build-up created in the cyclone when the ejection phase is ejected from the centrifuge bowl into the cyclone, and
(ii) the through-flow area of the ejection phase outlet of the cyclone is smaller than the through-flow area of the pressure release port at least during the time when the cyclone receives the ejection phase from the centrifuge bowl to thereby facilitate the release of the pressure build-up and minimize vibrations of the cyclone.

2. The separator according to claim 1 , wherein the vessel is arranged at a lower part of the cyclone, and the pressure release port is arranged in an opposite, upper part of the cyclone.

3. The separator according to claim 1 , comprising a conduit connected to the pressure release port, wherein the conduit is deflected from a direction that is parallel to the center axis of the cyclone.

4. The separator according to claim 1 , wherein the through-flow area of the ejection phase outlet of the cyclone is less than 20% of the through-flow area the pressure release port.

5. The separator according to claim 1 , wherein the ejection phase outlet comprises a flow restrictor that is arranged to set a flow of the ejection phase past the ejection phase outlet to a predefined rate.

6. The separator according to claim 1 , wherein the vessel is vertically aligned with respect to the cyclone, underneath the cyclone so that the ejection phase can gather in the vessel under the influence of the gravitational force.

7. The separator according to claim 1 , wherein the ejection phase outlet comprises a flange that extends into at least a part of the vessel.

8. The separator according to claim 7 , wherein an overflow passage that is open to the atmosphere is arranged between the flange and the vessel, such that the overflow passage allows ejection phase to leave the vessel via the overflow passage.

9. The separator according to claim 8 , wherein the overflow passage is arranged vertically above a lowermost part of the flange.

10. The separator according to claim 8 , wherein the cyclone and the flange at the ejection phase outlet are freely moveable relative the vessel.

11. The separator according to claim 1 , comprising a cleaning unit arranged adjacent the pressure release port and the ejection phase outlet.

12. The separator according to claim 1 , comprising a pump connected to the vessel at a lower part thereof for expelling the ejection phase from the vessel, wherein the pump is connected to the vessel via a flexible conduit.

13. The separator according to claim 1 , wherein the vessel comprises a sensor arranged to detect a level of ejection phase in the vessel to trigger expulsion of the ejection phase from the vessel via a pump connected to the vessel.

14. The separator according to claim 1 , wherein (ii) the through-flow area of the ejection phase outlet of the cyclone is smaller than the through-flow area of the pressure release port at least during the time when (a) the cyclone receives the ejection phase from the centrifuge bowl and (b) both the ejection phase outlet and the pressure release port are open, to thereby facilitate the release of the pressure build-up and minimize vibrations of the cyclone.

15. The separator according to claim 1 , wherein the through-flow area of the ejection phase outlet is defined by an opening in a flow restrictor.

16. A method for separating raw milk into a skimmed milk phase, a cream phase and an ejection phase that comprises solid impurities, the method comprises:
receiving the raw milk into a centrifuge bowl,
ejecting the ejection phase from the centrifuge bowl through an ejection port,
receiving and decelerating the ejection phase ejected from the centrifuge bowl in a cyclone connected to the ejection port,
receiving and collecting the ejection phase from the cyclone through an ejection phase outlet of the cyclone, and
releasing pressure build-up created in the cyclone, when the ejection phase is ejected from the centrifuge bowl into the cyclone, through a pressure release port in the cyclone that is open directly to the atmosphere,
wherein the through-flow area of the ejection phase outlet of the cyclone is smaller than the through-flow area the pressure release port at least during the time when the cyclone receives the ejection phase from the centrifuge bowl, thereby facilitating the release of the pressure build-up and minimize vibrations of the cyclone.

17. The method according to claim 16 , wherein (ii) the through-flow area of the ejection phase outlet of the cyclone is smaller than the through-flow area of the pressure release port at least during the time when (a) the cyclone receives the ejection phase from the centrifuge bowl and (b) both the ejection phase outlet and the pressure release port are open, to thereby facilitate the release of the pressure build-up and minimize vibrations of the cyclone.

18. The method according to claim 16 , wherein the through-flow area of the ejection phase outlet is defined by an opening in a flow restrictor.

Assignees

• Tetra Laval Holdings & Finance

Inventors

• Leufstedt Max

Classifications

• B04C5/22

  with cleaning means · CPC title

• B04C5/185

  Dust collectors · CPC title

• B04C5/13

  formed as a vortex finder and extending into the vortex chamber {(exits with bulkheads preventing reverse flow vortex B04C3/00)}; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow · CPC title

• B04B11/04

  Periodical feeding or discharging; Control arrangements therefor · CPC title

• B04B5/10 Primary

  Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges (B04B5/12 takes precedence; magnetic or electrostatic separators B03C; {amassing particles by electric fields, e.g. by agglomeration B03C3/0175}) · CPC title