GB2241796A - Fluidic mixers - Google Patents

Fluidic mixers Download PDF

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Publication number
GB2241796A
GB2241796A GB9005459A GB9005459A GB2241796A GB 2241796 A GB2241796 A GB 2241796A GB 9005459 A GB9005459 A GB 9005459A GB 9005459 A GB9005459 A GB 9005459A GB 2241796 A GB2241796 A GB 2241796A
Authority
GB
United Kingdom
Prior art keywords
flow
vortex chamber
chamber
liquid
milk
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
GB9005459A
Other versions
GB9005459D0 (en
Inventor
Michael Joseph Bowe
Lionel Houston Ford
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
UK Atomic Energy Authority
Original Assignee
UK Atomic Energy Authority
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by UK Atomic Energy Authority filed Critical UK Atomic Energy Authority
Priority to GB9005459A priority Critical patent/GB2241796A/en
Publication of GB9005459D0 publication Critical patent/GB9005459D0/en
Publication of GB2241796A publication Critical patent/GB2241796A/en
Withdrawn legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F15FLUID-PRESSURE ACTUATORS; HYDRAULICS OR PNEUMATICS IN GENERAL
    • F15CFLUID-CIRCUIT ELEMENTS PREDOMINANTLY USED FOR COMPUTING OR CONTROL PURPOSES
    • F15C1/00Circuit elements having no moving parts
    • F15C1/16Vortex devices, i.e. devices in which use is made of the pressure drop associated with vortex motion in a fluid

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  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Theoretical Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Mechanical Engineering (AREA)

Abstract

In spiralling through a vortex chamber 6 a liquid flow experiences high resistance to achieve thorough mixing and blending. A particular application is the homogenisation of milk, the constituents of which are thoroughly mixed and blended into a homogenous and stable mixture in spiralling through the vortex chamber. <IMAGE>

Description

Fluidic Mixers The present invention concerns fluidic devices for use as homogenisers.
Homogenisation is the process of thoroughly mixing and blending the constituents of a liquid, or separate and different liquids, into a uniform homogenous and stable mixture. Thus it is known, for example, to pass milk through a homogeniser to break up the fat globules and to resist separation of the fat or cream content of the milk. In a known homogeniser, the milk is forced under pressure through openings in a plate against a solid surface for the purpose of blending the constituents of the milk.
The present invention proposes the use of a fluidic device, in particular a vortex chamber, for blending the constituents of milk into a uniform homogenous and stable mixture.
According to the present invention a process for homogenising liquids comprises passing liquid through a vortex chamber such that the liquid experiences a high resistance to flow in spiralling through the vortex chamber to achieve thorough mixing of the constituents in the liquid.
The liquid can be milk and in spiralling through the chamber from an inlet at the periphery of the chamber to a central axial outlet in an end wall of the chamber the cream or fat content is broken down to mix with the non-fat content of the milk. The breakdown of the fat content is proportional to the pressure drop across the chamber. Conveniently, the flow can be enhanced by recycling a portion of the flow emerging from the vortex chamber. The vortex chamber can be a fluidic diode having a tangential inlet to create a spiralling flow to the central axial outlet. Preferably however, the vortex chamber comprises a vortex amplifier having a radial inlet, an axial outlet and a tangential control port. A control flow at the tangential port causes the main incoming liquid flow at the radial port to spiral through the chamber to the axial port.The control flow can be taken from the flow emerging from the chamber at the axial port. The amount of control flow is adjustable.
The invention will be described further, by way of example, with reference to the accompanying schematic diagrams in which Figures 1 and 2 depict alternative embodiments for homogenising milk.
In Figure 1, a vortex chamber 1 has a tangential inlet 2 and an axial outlet 3 to receive a flow of milk in the direction indicated by the arrows. The chamber is a vortex diode. In swirling through the chamber 1 the milk encounters a resistance to flow and its constituents become thoroughly mixed. The cream or fat content of the milk is broken down and substantially homogenised milk emerges from the outlet 3.
To improve performance a part of the outflow can be recycled along path 4, which includes a pump 5, to the flow at the inlet 1.
Preferably, and as shown in Figure 2, the vortex diode is replaced with a vortex amplifier 6 having a radial inlet 7, an axial outlet 8 and a tangential control 9. As before the control is taken from the flow emerging at the outlet 7 and a selectively adjustable pump 10 is included in the flow line. In this case it is possible to vary the control flow and hence the degree of mixing in the vortex chamber.

Claims (8)

Claims
1. A process for homogenising a liquid or liquids comprising passing a flow of the liquid or liquids through a vortex chamber such that the flow experiences a high resistance in spiralling through the vortex chamber to achieve thorough mixing of the constituents in the liquid or the liquids.
2. A process as claimed in Claim 1 which comprises recycling a portion of the flow from the vortex chamber.
3. A process as claimed in Claim 1 or 2 which comprises introducing the flow tangentially into the vortex chamber.
4. A process as claimed in Claim 1 or 2 which comprises introducing the flow radially into the vortex chamber and causing the flow to spiral through the chamber by introducing a tangential control flow into the chamber.
5. A process as claimed in Claim 4 which comprises taking the tangential control flow from the flow emerging from the vortex chamber.
6. A process as claimed in Claim 5 which comprises selectively adjusting the control flow.
7. A process as claimed in any preceding claim which comprises passing a flow of milk through the vortex chamber.
8. A process for homogenising a liquid or liquids substantially as herein described with reference to the accompanying drawings.
GB9005459A 1990-03-10 1990-03-10 Fluidic mixers Withdrawn GB2241796A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB9005459A GB2241796A (en) 1990-03-10 1990-03-10 Fluidic mixers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB9005459A GB2241796A (en) 1990-03-10 1990-03-10 Fluidic mixers

Publications (2)

Publication Number Publication Date
GB9005459D0 GB9005459D0 (en) 1990-05-09
GB2241796A true GB2241796A (en) 1991-09-11

Family

ID=10672429

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9005459A Withdrawn GB2241796A (en) 1990-03-10 1990-03-10 Fluidic mixers

Country Status (1)

Country Link
GB (1) GB2241796A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6699706B1 (en) 1998-06-13 2004-03-02 Accentus Plc Cell lysis method using a vortex mixer

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1220876A (en) * 1967-02-06 1971-01-27 Monique Legg A down pipe construction
GB1439025A (en) * 1973-02-06 1976-06-09 Skega Ab Flow device
GB1526957A (en) * 1974-09-20 1978-10-04 Hesse R Gas supply device
US4132247A (en) * 1977-05-04 1979-01-02 Owen, Wickersham & Erickson Fluid mixing apparatus
US4183338A (en) * 1977-05-04 1980-01-15 U.S.A. 161 Developments Ltd. Combustion control system adding a liquid, exhaust gases, and PCV gases

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1220876A (en) * 1967-02-06 1971-01-27 Monique Legg A down pipe construction
GB1439025A (en) * 1973-02-06 1976-06-09 Skega Ab Flow device
GB1526957A (en) * 1974-09-20 1978-10-04 Hesse R Gas supply device
US4132247A (en) * 1977-05-04 1979-01-02 Owen, Wickersham & Erickson Fluid mixing apparatus
US4183338A (en) * 1977-05-04 1980-01-15 U.S.A. 161 Developments Ltd. Combustion control system adding a liquid, exhaust gases, and PCV gases

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6699706B1 (en) 1998-06-13 2004-03-02 Accentus Plc Cell lysis method using a vortex mixer

Also Published As

Publication number Publication date
GB9005459D0 (en) 1990-05-09

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Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)