IP Library › Granted Patent US 12,576,410
Granted Patent B2
US 12,576,410 · App. 17/296,714 · Granted Mar 17, 2026

Centrifugal separation system and method with flow control to a heavy phase receiving container

Inventors: Kasper Höglund (Rönninge, SE); Peter Thorwid (Sundbyberg, SE); Staffan Königsson (Tumba, SE)
Assignee: ALFA LAVAL CORPORATE AB
B04B13/00B04B1/08B04B7/14B04B11/02B04B2013/006
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Quick Facts
Patent No.
US 12,576,410
App. No.
17/296,714
Granted
Mar 17, 2026
Kind
B2
Abstract

A centrifugal separation system includes a centrifugal separator, a liquid feed mixture conduit, a light phase conduit, a heavy phase conduit, and a flow control system. The flow control system includes a controller, a flow control valve arranged in a light phase conduit, a liquid feed mixture measuring device, and at a light phase measuring device and/or a heavy phase measuring device. The controller is configured to control the flow control valve based on measurements from the liquid feed mixture measuring device and measurements from the light phase measuring device and/or the heavy phase measuring device.

Claims (60)

1 . A centrifugal separation system comprising:

a centrifugal separator, a liquid feed mixture conduit, a light phase conduit, a heavy phase conduit, and a flow control system,

wherein the centrifugal separator comprises a rotor configured to rotate about an axis of rotation and being provided with a separation space, a stack of separation discs arranged inside the separation space, a first stationary portion arranged at a first axial end of the rotor, a second stationary portion arranged at a second axial end of the rotor,

wherein an inlet passage extends into the separation space via the first or second stationary portion, a light phase outlet passage extends from the separation space via the first or second stationary portion, a heavy phase outlet passage extends from the separation space via the first or second stationary portion,

wherein the heavy phase outlet passage comprises at least one channel extending within the rotor from a radially outer portion of the separation space towards a central portion of the rotor,

wherein each of the inlet passage, the light phase outlet passage, and the heavy phase outlet passage is mechanically hermetically sealed between the rotor and respective of the first and second stationary portions,

wherein the inlet passage enters the rotor centrally on the axis of rotation at R 0 , the heavy phase outlet passage exits the rotor at a first radius R 1 , and the light phase outlet passage exits the rotor at a second radius R 2 , wherein R 2 ≥R 1 ≥R 0 and R 2 >R 0 ,

wherein the flow control system comprises a controller, a flow control valve arranged in the light phase conduit, a liquid feed mixture measuring device, and a light phase measuring device and/or a heavy phase measuring device,

wherein the controller is configured to control the flow control valve based on measurements from the liquid feed mixture measuring device and measurements from the light phase measuring device and/or the heavy phase measuring device,

wherein the heavy phase conduit is configured to extend to a heavy phase receiving container,

wherein the heavy phase conduit forms an unrestricted passage from the centrifugal separator to the heavy phase receiving container when a flow of heavy phase exits from the heavy phase outlet passage to the heavy phase receiving container,

wherein the inlet passage enters the first axial end of the rotor parallel and centrally on the axis of rotation, and the light phase outlet passage enters the first axial end of the rotor parallel and offset from the axis of rotation and being separated from the inlet passage, and

wherein the heavy phase outlet passage enters the second axial end of the rotor parallel and centrally on the axis of rotation.

2 . The centrifugal separation system according to claim 1 , wherein the liquid feed mixture conduit is configured to be connected to a source of pressurised liquid feed mixture.

3 . The centrifugal separation system according to claim 1 , comprising a feed pump arranged in the liquid feed mixture conduit.

4 . The centrifugal separation system according to claim 1 , comprising a liquid feed mixture container and means for controlling a pressure within the liquid feed mixture container.

5 . The centrifugal separation system according to claim 1 , comprising a shut-off valve arranged in the heavy phase conduit.

6 . The centrifugal separation system according to claim 1 , wherein the centrifugal separator comprises an exchangeable separation insert, and

wherein the exchangeable insert comprises a rotor casing, and the first and second stationary portions are arranged at respective axial ends of the rotor casing, wherein the rotor casing forms part of the rotor of the centrifugal separator and comprises the separation space, the separation discs, and the at least one channel.

7 . The centrifugal separation system according to claim 6 , wherein the rotor comprises a rotatable member and the rotor casing, and wherein the rotor casing is engaged in an inner space of the rotatable member.

8 . The centrifugal separation system according to claim 1 , comprising a liquid feed mixture container, wherein a stirring member is arranged within the liquid feed mixture container.

9 . The centrifugal separation system according to claim 1 , wherein the measurements from the liquid feed measuring device relate to a flow of liquid feed mixture, the measurements from the light phase measuring device and/or the heavy phase measuring device relate to a flow of light phase and/or a flow of heavy phase, wherein the controller is configured to control the flow control valve towards a desired relationship between the flow of liquid feed mixture and the flow of light phase and/or the flow of heavy phase.

10 . The centrifugal separation system according to claim 9 , wherein the flow of liquid feed mixture and the flow of light phase and/or the flow of heavy phase are volume flows.

11 . The centrifugal separation system according to claim 9 , wherein the flow of liquid feed mixture and the flow of light phase and/or the flow of heavy phase are mass flows.

12 . The centrifugal separation system according to claim 1 , wherein the liquid feed mixture measuring device is a volume flow meter.

13 . The centrifugal separation system according to claim 12 , comprising a mass flow meter arranged in the liquid feed mixture conduit.

14 . The centrifugal separation system according to claim 1 , wherein the liquid feed mixture measuring device is a mass flow meter.

15 . The centrifugal separation system according to claim 1 , wherein the liquid feed mixture measuring device measures the particle content of the liquid feed mixture, and

wherein the controller is configured to control the flow control valve based on the particle content of the liquid feed mixture and a target particle content of the heavy phase to set a ratio between flow in the light phase outlet passage and flow in the heavy phase outlet passage.

16 . A method of controlling a centrifugal separation system, the centrifugal separation system comprising a centrifugal separator, a liquid feed mixture conduit, a light phase conduit, a heavy phase conduit, and a flow control system,

wherein the centrifugal separator comprises a rotor configured to rotate about an axis of rotation and being provided with a separation space, a stack of separation discs arranged inside the separation space, a first stationary portion arranged at a first axial end of the rotor, a second stationary portion arranged at the second axial end of the rotor,

wherein an inlet passage extends into the separation space via the first or second stationary portion, a light phase outlet passage extends from the separation space via the first or second stationary portion, and a heavy phase outlet passage extends from the separation space via the first or second stationary portion,

wherein the heavy phase outlet passage comprises at least one channel extending within the rotor from a radially outer portion of the separation space towards a central portion of the rotor,

wherein each of the inlet passage, the light phase outlet passage, and the heavy phase outlet passage is mechanically hermetically sealed between the rotor and respective of the first and second stationary portions,

wherein the inlet passage enters the rotor centrally on the axis of rotation at R 0 , the heavy phase outlet passage exits the rotor at a first radius R 1 , and the light phase outlet passage exits the rotor at a second radius R 2 , wherein R 2 ≥R 1 ≥R 0 and R 2 >R 0 ,

wherein the flow control system comprises a flow control valve arranged in the light phase conduit, a liquid feed mixture measuring device, and a light phase measuring device and/or a heavy phase measuring device,

wherein the method comprises steps of:

rotating the rotor;

conducting a flow of liquid feed mixture into the separation space via the liquid feed mixture conduit and the inlet passage;

separating the liquid feed mixture into a heavy phase and a light phase in the separation space;

measuring the flow of liquid feed mixture;

measuring a flow of light phase and/or a flow of heavy phase;

controlling the flow control valve based on measurements acquired in the step of measuring the flow of liquid feed mixture and measurements acquired in the step of measuring the flow of light phase and/or the flow of heavy phase; and

removing the heavy phase through the heavy phase conduit extending to a heavy phase receiving container,

wherein the heavy phase conduit forms an unrestricted passage from the centrifugal separator to the heavy phase receiving container when a flow of heavy phase exits from the heavy phase outlet passage to the heavy phase receiving container,

wherein the step of conducting the flow of liquid feed mixture into the separation space comprises the step of:

conducting the flow of liquid feed mixture comprising a cell culture mixture to flow the cell culture mixture into the separation space,

wherein the inlet passage enters a first side of the rotor parallel and centrally on the axis of rotation, and the light phase outlet passage enters the first side of the rotor parallel and offset from the axis of rotation and being separated from the inlet passage, and

wherein the heavy phase outlet passage enters a second side opposite the first side of the rotor parallel and centrally on the axis of rotation.

17 . The method according to claim 16 , comprising a step of:

controlling a pressure of the liquid feed mixture.

18 . The method according to claim 17 , wherein the step of controlling the pressure of the liquid feed mixture comprises a step of:

controlling a feed pump arranged in the liquid feed mixture conduit.

19 . The method according to claim 17 , wherein the centrifugal separation system comprises a liquid feed mixture container, and wherein the step of controlling the pressure of the liquid feed mixture comprises a step of:

controlling a pressure within the liquid feed mixture container.

20 . The method according to claim 16 , wherein the centrifugal separation system comprises a shut-off valve arranged in the heavy phase conduit, and wherein the method comprises steps of:

maintaining the shut-off valve closed during an initial separation phase of separating a batch of liquid feed mixture while an interface between the light phase and heavy phase forms within the separation space; and

maintaining the shut-off valve fully open during a main separation phase of separating the batch of liquid feed mixture when the interface has formed.

21 . The method according to claim 16 , wherein the step of controlling the flow control valve comprises a step of:

controlling the flow control valve towards a desired relationship between the flow of liquid feed mixture and the flow of light phase and/or the flow of heavy phase.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 25, 2021
From: HÖGLUND, KASPER; THORWID, PETER; KÖNIGSSON, STAFFAN
To: ALFA LAVAL CORPORATE AB
Reel/Frame 056344/0241 →
Priority Claims (4)
EP 18211238 · Dec 10, 2018 · regional
EP 18211242 · Dec 10, 2018 · regional
EP 18211243 · Dec 10, 2018 · regional
EP 19158273 · Feb 20, 2019 · regional
Continuity (1)
Related Publication 20220023892A1 · Jan 27, 2022
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