GB2625107A

GB2625107A - Particle sorter

Info

Publication number: GB2625107A
Application number: GB2218339.6A
Authority: GB
Inventors: Agrawal Prashant; Torun Hamdi
Original assignee: Of Northumbria At Newcastle, University of; Northumbria University
Current assignee: Of Northumbria At Newcastle, University of; Northumbria University
Priority date: 2022-12-06
Filing date: 2022-12-06
Publication date: 2024-06-12
Also published as: WO2024121562A1; GB202218339D0

Abstract

A particle sorter comprises a closed chamber 100 having a plurality of ports 140 and a first pump 142 coupled to at least one port to provide oscillations to the at least one port in a first mode of operation with an oscillation frequency of 0.1 Hz to 1000 Hz, in use. A method of sorting particles is also disclosed. In use, the particle sorting chamber 100 is supplied with a liquid carrying particulate, either in a single filling operation or by continuous replenishment. The liquid within the chamber 100 is subjected to oscillations V, from the first pump 142 through port 140A with an oscillation frequency of 0.1 Hz to 1000 Hz, thereby generating complementary oscillations through further ports 140B, 140C that cause a selection of particles within the chamber to accumulate in an accumulation region. Potential applications for the particle sorter include separating particles (e.g. particles with physical properties within a particular range), isolating and enriching emulsions, suspensions of cells (i.e. biological particles), and nanoparticle solutions, water filtration and use in bioanalytical devices for bio-sensing.

Description

PARTICLE SORTER

TECHNICAL FIELD

The present application relates to devices for sorting particles, for example particles with a mean average particle size of 100nm to 1mm, and more particularly, but not exclusively, to sorting the particles by one or more of size, density and visco-elastic properties.

BACKGROUND

Sorting particles from liquids in which they are carried is important in several technical fields, and may be used to separate substantially all particles, or just a selected sub-group of particles with particular properties, from the liquid. Accordingly, from an initial supply of liquid carrying particles, particle sorting is used to produce a first output with a greater concentration of particles, or with a greater concentration of a sub-group of particles with selected properties, and a complementary second output. Technical fields in which particles may be sorted from liquids include chemical and pharmaceutical manufacturing, for example for separating-out particles (e.g. particles within a range of physical properties), enriching emulsions, concentrating particle suspensions, water filtration and use in bio-analytical devices for biosensing.

Bulk industrial particle separation is commonly performed by filtration and centrifugation. However, yield is low, requiring high processing volumes. Commercial application is restricted by low particle resolution (discrimination, e.g. by size).

Microscale methods are known, using electric, magnetic and optic fields. Whilst these methods can have a high particle resolution, they have low processing volumes and require complex and expensive fabrication procedures and equipment.

High frequency vibrations have been used for particle separation in channels, using high frequency vibrations ranging from 10 kHz to MHz frequencies. Limitations of these methods include: high shear forces that damage delicate emulsions or biological cells, reducing particulate yield; high cost due to complex microscale fabrication; low scalability, especially for sub-micron particulates, due to microscale device requirements; and high power requirements due to significant energy dissipation via heating.

Low frequency vibrations have also been used for particle separation in open-topped channels, in which the channel is vibrated to create standing capillary waves at the water-air interface creating a periodic first order velocity field, which causes the accumulation of particles underneath the capillary wave nodes. However, in such devices, the wavelength of the capillary waves and the driving frequency cannot be decoupled, limiting the design, operational yield and throughput.

SUMMARY OF THE DISCLOSURE

According to a first aspect, there is provided a particle sorter comprising: a closed chamber having a plurality of ports; and a first pump coupled to at least one port to provide oscillations to the at least one port in a first mode of operation with an oscillation frequency of 0.1 Hz to 1000 Hz, in use.

According to a second aspect, there is provided a method of sorting particles with a particle sorter according to the first aspect, comprising: providing a port of the chamber with a supply of liquid carrying particles; and providing oscillations to the liquid in the chamber.

The first pump may provide oscillations in a first mode of operation with an oscillation frequency of 0.1 Hz to 50 Hz, in use.

The first pump may be configured two switch between the first mode of operation and a second mode of operation to flush accumulated particulate from the chamber.

A second pump may be coupled to a port to flush accumulated particulate from the chamber.

The second pump may be coupled to two ports of the chamber to provide an input flushing liquid to a first port of the chamber and to receive an output flushing fluid from a further port of the chamber.

A pump may be configured to provide an input supply of liquid to the chamber during the first mode of operation.

The first pump may be configured to provide a plurality of different frequency oscillations to the same port of the chamber or different ports of the chamber. The first pump may be coupled to provide first oscillations to a first port and second oscillations to either the first port or a second port, wherein the first and second oscillations have a different oscillation frequency.

The chamber may have an inlet flushing port and a plurality of opposed outlet flushing ports, and oscillation ports are each intermediate the inlet flushing port and an outlet flushing port, wherein the first pump is coupled to opposed oscillation ports and a second pump is coupled to an inlet flushing port to supply a flushing flow through the chamber to the outlet flushing ports.

The second pump may be coupled to opposed outlet flushing ports comprising a central outlet flushing port between lateral outlet flushing ports, and the first pump may be coupled to opposed oscillation ports that are each intermediate the inlet flushing port and a respective lateral outlet flushing port.

The first pump may be coupled to provide first oscillations to a first port and second oscillations to a second port, wherein the first and second oscillations have a common oscillation frequency and a relative phase difference.

The chamber may have a base and a roof, and a pillar extending between the base and the roof.

The chamber may have a base and a roof, and one or both of the base and roof may be provided with a periodically repeating surface profile. The periodically repeating surface profile may be a wave pattern. The periodically repeating surface profile may be an array of dimples.

The chamber may have a base, a roof and side walls and ports are provided in the side walls.

One or more ports may be provided in one or both of the base and the roof of the chamber.

Adjacent a port provided in the base or roof of the chamber, the respective base or roof may be inclined towards the port.

The chamber may have a length, a width and a depth, and ports in the side walls may have a diameter of up to 30% of the length and up to 30% of the width.

The chamber may have a length of 3mm to 50mm, a width of 3mm to 50mm, and a depth of less than 3mm.

The chamber may have a length, a width and a depth, and the depth may be less than one third of each of the length and a width.

The particle sorter may comprise a plurality of serially coupled chambers.

DESCRIPTION OF THE DRAWINGS

Examples are further described hereinafter with reference to the accompanying drawings, in which: * Figures 1A to 1C show views of a particle sorting chamber; * Figure 1D shows a schematic view of a particle sorter comprising the particle sorting chamber of Figure 1A; * Figure 1 E shows a schematic view of an alternative particle sorter comprising the particle sorting chamber of Figure 1A; * Figure 2A shows a schematic view of a particle sorter having a single particle sorting chamber; * Figure 2B show a schematic view of a particle sorter having two serially coupled particle sorting chambers; * Figure 2C shows a schematic view of a further particle sorter having a single particle sorting chamber; * Figures 3A and 3B show schematic plan views of further particle sorting chambers; * Figure 4A shows a schematic view of a further particle sorting chamber, and Figure 4B shows particle motion within the chamber of Figure 4A; * Figure 5A shows a schematic view of a further particle sorting chamber, and Figure 5B shows particle motion within the chamber of Figure 5A; * Figure 6A shows a schematic view of a particle sorting chamber for continuous particle sorting use, and Figure 6B shows a plurality of serially coupled particle sorting chambers of Figure 6A; * Figure 7 shows a schematic view of a hexagonal chamber; and * Figure 8 shows a schematic view of a cut-away view of a chamber with a patterned base.

DETAILED DESCRIPTION

In the described examples, like features have been identified with like numerals, albeit in some cases having suffix letters; and typographical marks (e.g. primes). For example, in different figures, 100, 100A, 100B have been used to indicate a particle sorting chamber.

Figure 1A shows a perspective view of a closed particle sorting chamber 100 of a particle sorter, within a housing 120 and having inlet/outlet conduits leading coupling through the

S

housing to chamber ports 140. Figures 1B and 1C show cut-away views of the chamber 100 and housing 120, respectively along the width W and length L of the chamber. Figure 1D shows a particle sorter 190 in a cut-away view through the chamber 100 (parallel to the length and width of the chamber).

The chamber 100 is shallow, being much thinner in one dimension (e.g. Z-axis) than in the perpendicular plane (e.g. the X-Y plane), forming a generally shallow box-shaped void within the housing 120, having side walls 106 with a depth D extending between a base 102 and a roof 104 of the chamber. Figure 1D shows a view that is cut-away in-plane (e.g. cut parallel to the X-Y plane).

A "closed" particle sorting chamber is a chamber 100 that only has openings at the chamber ports 140. The chamber ports 140 are located within faces of the chamber or at corners between faces 106 of the chamber, being within or adjacent the side walls 106, base 102 or roof 104. The chamber ports are much smaller in area than the face of the chamber within which they are provided, or adjacent which they are provided (e.g. being provided where two faces meet, or connecting between two faces).

The use of a closed chamber enables the wavelength of the velocity field of the liquid within chamber, which determines the locations of the accumulation regions A, to be decoupled from the oscillation frequency, instead of being defined by the geometry of the chamber.

Figure 1D shows a particle sorter 190, in which a pump 142 is coupled in a closed loop to two opposed ports 140 of the particle sorting chamber 100 of Figure 1A and adapted to provide oscillations V, V to respective ports 140 of the chamber.

In use, the particle sorting chamber 100 is filled with a liquid carrying particulate (e.g. having a mean average particle size of 100nm to 1mm). The liquid may be introduced through one of the ports 140 coupled to the pump 142, e.g. being supplied by activation of the first pump.

The liquid within the chamber 100 is subjected to oscillations V, V produced by the first pump 142 with an oscillation frequency of 0.1 Hz to 1,000 Hz. The oscillation frequency may be 0.1 Hz to 50 Hz (e.g. 0.1 Hz to 20 Hz), which enables relatively rapid collection of particles. The oscillation V through one port 140 of the chamber 100 is in anti-phase with the oscillation V' through the opposed port 140 (i.e. the volume of the chamber is constant, and the oscillations through the two ports are complementary). Subject to the selected oscillation frequency, the amplitude of the oscillations, and the shape of the chamber, differing levels of selection will be applied to different particles within the liquid according to their physical properties, causing them either to remain dispersed within the liquid or to accumulate in one or more accumulation regions A of the chamber. Figure 10 shows accumulation regions A for oscillations V, V' through the illustrated particle sorting chamber 100.

The properties upon which the selection of particles for accumulation in the accumulation regions A is based may be one or more of the size, density and visco-elastic properties of the particles (e.g. a combination of size, density and visco-elastic properties). For example, with all other properties remaining equal, smaller particles may be more likely to remain dispersed and larger particles may be more likely to accumulate at the accumulations regions A. Each period of oscillation V, V may transfer a volume of 0.1 to 50 pL into and back out of the chamber, for example transferring a volume of 2 to 10 p L. After a sufficient period of particle accumulation, liquid is flushed through the chamber 100 to remove the accumulated particles from the chamber, for example by providing a high intensity flow F through the chamber. The chamber 100 may be flushed through one of the ports 140 coupled to the pump 142. For example, the pump 142 may be switched from operation producing oscillations V, V to operation for flushing F the chamber 100. The liquid and accumulated particulate that is flushed F from the chamber may be collected, and the chamber may be refilled to repeat the accumulation of particles with the oscillations V, V. Alternatively, the particulate may be flushed from the chamber with an external fluid supply, e.g. coupled through one or more valves 150 from an inlet 143 to an outlet 145 (the valves may be solenoid switching valves; the valves may be controlled via a micro-controller). In a further alternative, the particulate may be removed from the chamber through an extraction port at the accumulation regions A, as discussed below, e.g. being removed during on-going accumulation, during a flushing step, or both. Yet further, the chamber 100 may be openable to facilitate the removal of particles from the chamber. Each of the approaches for particle removal may similarly be applied to the other designs of chambers discussed.

The liquid carrying particulate may be provided to the chamber 100 and continuously replenished by a gentle flow (e.g. sufficiently gentle not to significantly disturb the accumulation of particles within the chamber), before accumulated particles are removed by periodic flushing (e.g. high intensity flow) or emptying of the chamber.

Potential applications for the particle sorter include separating particles (e.g. particles with physical properties within a particular range), isolating and enriching emulsions, suspensions of cells (i.e. biological particles), and nanoparticle solutions, water filtration and use in bioanalytical devices for bio-sensing.

The use of oscillations V. V with relatively low frequencies applies low shear forces upon the particles enabling enhanced throughput of accumulated particles, using a mechanically simple chamber that enables particle sorting based upon physical properties of the particulates (e.g. sorting particles with mean average sizes in the range 100nm to 1mm), with low energy consumption due to the low shear forces, and with independent control over selection precision and throughput, e.g. being controlled by the choice of chamber dimensions and oscillation frequency.

The particle sorting chamber 100 of Figure 1A is a single empty chamber with a flat floor and ceiling, and ports provided only in the side walls of the chamber. In alternative arrangements, at least one of: a plurality of chambers may be coupled together to provide enhanced particle selection performance; the chamber may be provided with an extraction port in the base or roof of the chamber, aligned with a particle accumulation region of the chamber; and the chamber may be provided with a pillar, which changes the velocity field within the chamber, and may increase the rate of particle accumulation and the number of particle accumulation regions A. The particle selection properties of a particle sorting chamber are subject to several parameters, including the shape and size of the chamber, and the oscillation driving arrangement of the chamber.

The closed chamber may be a simple convex polygonal shape. For example, the chamber may have a base that is triangular, square, pentagonal or hexagonal. The chamber may have a base that is oval.

Figure 1E shows an alternative particle sorter 190' with an in-plane cut-away view through the closed particle sorting chamber 100 of Figure 1A. The pump 142 is configured to produce oscillations V and is coupled to one port 140 of the particle sorting chamber 100 and to an inlet 143. An opposed chamber port 140 is coupled to an outlet 145 that may optionally be closable with a valve 150.

In use, the particle sorting chamber 100 is filled (or continuously replenished) with a liquid carrying particulate (e.g. having a mean average particle size of 100nm to 1mm), for example through the port 140 coupled to the pump 142 (e.g. the other port 140 remains open, e.g. the chamber is filled through the pump 142 from inlet 143). The liquid within the chamber 100 is subjected to oscillations V with an oscillation frequency of 0.1 Hz to 1,000 Hz (e.g. 0.1 Hz to 50 Hz, or 0.1 Hz to 20 Hz), causing particles either to remain dispersed within the liquid or to accumulate in one or more accumulation regions A' of the chamber.

After a sufficient period of particle accumulation, liquid is flushed through the chamber 100 to remove the accumulated particles, for example by flushing liquid F through the port 140 that is coupled to the pump 142 (e.g. replenishing with further liquid carrying particulate for further accumulation). For example, the oscillation V may be halted, the pump 142 may be switched to produce a flushing flow F to flush the accumulated particulate from the chamber 100 with a vigorous fluid flow (e.g.: out through valve 150 and outlet 145; the valve may be a solenoid switching valve; and the pump 142 may be connected to a fluid supply). During flushing F, accumulated particulate swept from the chamber may be separated from the flushed fluid by filtration. Alternatively, the particulate may be removed from the chamber through an extraction port at the accumulation regions A', as discussed below. In a further alternative, the chamber 100 may be openable and the particles may be removed by opening the chamber.

Flushing flow F and oscillation V may be provided through the same ports 140, for example 20 with the pump 142 switching between the two operations. The pump 142 may provide both oscillations V and a continuous replenishment flow of replenishing particulate carrying liquid.

In a further alternative, the chamber may be periodically filled and emptied, e.g. by a syringe. In a yet further alternative, the particle sorter may be provided with a pump that may be periodically switched between an oscillation generation mode of operation and a flushing mode of operation.

Figure 2A shows a further particle sorter 190, in which a first pump 142 is coupled to a port 140A of the chamber 100 to provide oscillations V, and a second pump 144 is coupled in a closed loop to two different, opposed ports 140B, 140C of the chamber to provide both a continuous gentle replenishment of liquid carrying the particulate during particle sorting, and for use in flushing F with a vigorous fluid flow (when required to remove accumulated particulate, e.g. out through valve 150 and outlet 145; the valve may be a solenoid switching valve). During flushing F, the liquid and accumulated particulate is swept from the chamber, and may be separated from the closed loop by filtration. Alternatively, the particulate may be removed from the chamber through an extraction port at the accumulation regions (e.g. during on-going particle sorting), as discussed below.

In use, the particle sorting chamber 100 is supplied with liquid carrying particulate, either in a single filling operation or by continuous replenishment. The liquid within the chamber 100 is subjected to oscillations V, from the first pump 142 through port 140A with an oscillation frequency of 0.1 Hz to 1000 Hz (e.g. 0.1 Hz to 50 Hz, or 0.1 Hz to 20 Hz), generating complementary oscillations through the other ports 140B, 140C, each with approximately half the amplitude, and causing the selection of particles within the chamber, with the selected particles accumulating in the accumulation region A, shown in Figure 3A.

In the illustrated particle sorter 190, the second pump 144 is coupled in a closed loop.

Alternatively the liquid carrying the particulate may only be supplied to the chamber 100 from the pump to provide a liquid supply to an inlet port of the chamber, and an outlet port of the chamber may be configured for discharge from the particle sorter.

The particle sorters may be easily scaled, by the connection of chambers in parallel, in series, or both in parallel and in series. Each of the described chamber designs may be connected in parallel, in series, or both in parallel and in series.

Figure 2B shows a plurality of chambers 100A, 100B coupled in series. Series coupled chambers 100A, 100B may be operated similarly, to enhance particle selection on the basis of a common criteria. For example, series coupled chambers may preferentially accumulate particles with a mean average particle size above the same threshold.

Alternatively, the series coupled chambers 100A, 100B may be operated with different particle selection criteria, enabling the combined chambers to select particles falling within a narrow range of properties. For example, the first chamber 100A may preferentially select the accumulation of particles falling above a first threshold mean average size to accumulate in the first chamber, and the second chamber 100B may preferentially select particles falling above a lower second threshold mean average size to remain in dispersion. Accordingly, particles falling between the two thresholds may be preferentially accumulated in the second chamber 100B.

The ports that open at the chamber are small in area relative to the size of chamber (e.g. no more than 30% of the length and width of the chamber), so that the wavelength of the velocity field of the liquid within the chamber, which determines the locations of the accumulation regions, is governed by the chamber size.

The depth of the chamber may be less than each of the length and the width. The particle sorting chambers may be shallow, e.g. having a depth D that is less than one third of each of the length L and the width W of the chamber. Being shallow improves particle sorting performance, and in particular may enhance the collection of smaller particles.

The chamber may have a length of 3mm to 50mm (e.g. 3mm to 15mm), a width of 3mm to 50mm (e.g. 3mm to 15mm), and a depth of up to 3mm (e.g. up to 2mm, up to 1mm or up to 500pm).

The chamber may have a depth of at least three times the mean average particle diameter (e.g. threshold diameter of particles being accumulated). For example, for sorting particles having a mean average particle diameter of up to 66pm, the chamber may have a depth of 200pm.

The arrangement of the ports through which the oscillations V, V', and optionally any continuous replenishment flow through the chamber are provided determines where the particle accumulation region(s) A arise, and the particle selection criteria applied.

For example, Figure 3A shows the location of the accumulation region A with oscillation V provided perpendicularly through a port 140 on only one side, whereas Figure 3B shows a differently located accumulation region A with both antiphase oscillations V' additionally being provided through an opposed port to that of the oscillation V in Figure 3A. In each case, a pump is configured to provide a flushing flow F when the chamber is periodically emptied of accumulated particulate (and optionally a gentle replenishment flow), through a pair of opposed ports that are perpendicular to the orientation of the oscillation.

A chamber 100 may be provided with oscillations through each port in a mirror symmetric arrangement, with the oscillations V through two opposed ports 140 being in phase, but in anti-phase with the oscillations V' through perpendicular ports.

In a further example, Figure 4A shows an arrangement in which a first pair of opposed ports are driven in phase with each other (i.e. simultaneous in-flow at both ports) with oscillation V, and driven with anti-phase oscillations V' at a perpendicular second pair of opposed ports (the arrangements of a flushing flow and an optional replenishing flow are not shown). This driving pattern causes particle accumulation in four accumulation regions A spaced apart around the square chamber symmetrically between the ports 140 (e.g. the chamber has two-fold mirror symmetry, and the accumulation regions A are arranged with corresponding symmetry). The accumulation regions A are the regions of slowest velocity field. Figure 4B shows the corresponding streaming field and the motion of particles 180 subject to accumulation, within the chamber of Figure 4A.

As shown in Figure 5A, a pillar 148 may be provided within the chamber, e.g. centrally, e.g. extending between the floor and roof of the chamber, to change the way in which the particles move in response to oscillations V. The provision of a pillar (or more than one pillar) may change the particle selection criteria of the chamber, e.g. may enhance the collection of smaller particles, and may reduce the collection size threshold. The provision of the pillar(s) may increase particle collection rates and may increase the number of particle accumulation regions A (which may facilitate bio-sampling and analysis).

Figure 5B shows the streaming field and particle motion in a square chamber, with the same pattern of oscillations V, V as shown in Figure 4B, but with the chamber of Figure 5A, which has an additional central pillar 148. The addition of the pillar 148 may enhance the speed of particle collection. The addition of the pillar 148 may enhance the collection of smaller sized particles. The addition of the pillar 148 may increase the number of particle accumulation regions A. Each of the other described chamber designs may be provided with one or more pillars.

As indicated in Figures 3A and 3B, an extraction port 146 may optionally be provided in the base 102 (or roof) of the chamber 100 for the extraction of the particles that accumulate in a corresponding accumulation region A. For example, the accumulated particles may fall into the extraction port 146 under gravity, or may be extracted by a liquid flow drawn out of the extraction port 146 (e.g. by a pump).

Adjacent an extraction port 146 provided in the base (or roof) of the chamber the respective base (or roof) is inclined towards the port, relative to the surrounding base (or roof), e.g. the extraction port may have a funnel-shaped opening into the chamber, to enhance flow of accumulated particles from the chamber to the extraction port and into the connecting conduit. The inclination may be by less than 30° relative to the surrounding base (or roof).

Each of the other described chamber designs may be provided with one or more extraction ports at their accumulation region(s).

The ports may all be in the side walls 106 of each chamber 100 (e.g. in faces of the chamber extending parallel to the height of the chamber). Alternatively, some of the ports may be provided in the base 102 or roof 104 of the chamber.

In an alternative arrangement, oscillations V may be provided through a central port provided in the base 102 or roof 104 of the chamber 100 (e.g. in addition to, or instead of, oscillations provided through one or more ports provided in side walls of the chamber).

Figure 6A shows an alternative chamber for continuous in-plane particle sorting 100T. The chamber 100T is triangular, fanning out from an input supply port 1405 to a plurality of outlet ports in the opposite end of the chamber 1001, being a central outlet port 1400 between lateral outlet ports 140L. Part way along each side wall 106, opposed ports 140V are provided with complementary oscillations V, V', causing spatial sorting of particles carried in the liquid flow F passing through the chamber from the input supply port 1405, providing a different distribution of particles in the outlet flows through the central outlet port 1400 and the lateral outlet ports 140L. In the illustrated example, the inlet flow F contains equal percentages of particles having a smaller and larger mean average particle size (e.g. of smaller and larger radius rp), and larger particles are preferentially passed to the lateral outlet ports 140L, and preferentially (e.g. substantially only) smaller particles are passed to the central outlet port 1400, relative to the particle distribution of the inlet flow. Similarly, if the inlet flow F contains only smaller or larger particles, the chamber 100T may be used to produce an outlet flow with an enriched concentration of particles.

Figure 6B shows an arrangement of serially coupled chambers for continuous in-plane particle sorting 100T, as shown in Figure 6A. The inlet ports 1405 of the second stage of chambers 100T2 are coupled to the lateral outlet ports 140L of first stage chamber 100T1, and as shown in the distribution graphs, the second stage of particle sorting further enhances the concentration of larger particles in the outlet from the second stage lateral outlet ports 140L.

Oscillations at the same frequency but with different phases may be provided to different ports of the chamber.

In the illustrated example hexagonal chamber 100 of Figure 7, pairs of adjacent ports are driven with oscillations in antiphase (e.g. VO, V01), with a phase shift between successive pairs of ports around the side wall of the chamber. The use of more than two different phases of driving oscillations may enable the simultaneous collection of a plurality of different particles in different particle accumulation regions.

Oscillations at different frequencies may be provided to the same port or different ports of the chamber.

The use of more than two different frequencies of driving oscillations may enable the simultaneous collection of a plurality of different particles in different particle accumulation regions.

The chambers may be provided with a two or more different frequencies of oscillations, which may cause different types of particles to accumulate at different accumulations regions of the chamber (which may be provided with corresponding extraction ports).

The base 102 or roof 104 of the chamber 100 may be patterned to modify the movement of particles within the chamber under the action of the provided oscillations. For example, the patterning may be a wave pattern or a two-dimensional array of dimples. Figure 8 shows a chamber with a wave pattern 102P provided on the base 102 of the chamber. The provision of a patterned base or roof may simply fabrication of the chamber. The provision of a patterned base or roof may enable more efficient particle sorting and so the use of more compact particle sorting chambers, which may assist with the construction of multiple devices in a limited footprint.

The figures provided herein are schematic and not to scale.

Throughout the description and claims of this specification, the words "comprise" and "contain" and variations of them mean "including but not limited to", and they are not intended to (and do not) exclude other moieties, additives, components, integers or steps. Throughout the description and claims of this specification, the singular encompasses the plural unless the context otherwise requires. In particular, where the indefinite article is used, the specification is to be understood as contemplating plurality as well as singularity, unless the context requires otherwise.

Features, integers, characteristics, compounds, chemical moieties or groups described in conjunction with a particular aspect, embodiment or example of the invention are to be understood to be applicable to any other aspect, embodiment or example described herein unless incompatible therewith. All of the features disclosed in this specification (including any accompanying claims, abstract and drawings), and/or all of the steps of any method or process so disclosed, may be combined in any combination, except combinations where at least some of such features and/or steps are mutually exclusive. The invention is not restricted to the details of any foregoing embodiments. The invention extends to any novel one, or any novel combination, of the features disclosed in this specification (including any accompanying claims, abstract and drawings), or to any novel one, or any novel combination, of the steps of any method or process so disclosed.

The reader's attention is directed to all papers and documents which are filed concurrently with or previous to this specification in connection with this application and which are open to public inspection with this specification, and the contents of all such papers and documents are incorporated herein by reference.

Claims

CLAIMS1. A particle sorter comprising: a closed chamber having a plurality of ports; and a first pump coupled to at least one port to provide oscillations to the at least one port in a first mode of operation with an oscillation frequency of 0.1 Hz to 1000 Hz, in use.
2. The particle sorter according to claim 1, wherein the first pump provides oscillations in a first mode of operation with an oscillation frequency of 0.1 Hz to 50 Hz, in use.
3. The particle sorter according to claim 1 or claim 2, wherein the first pump is configured two switch between the first mode of operation and a second mode of operation to flush accumulated particulate from the chamber.
4. The particle sorter according to claim 1 or claim 2, comprising a second pump coupled to a port to flush accumulated particulate from the chamber.
5. A particle sorter according to claim 4, wherein the second pump is coupled to two ports of the chamber to provide an input flushing liquid to a first port of the chamber and to receive an output flushing fluid from a further port of the chamber.
6. The particle sorter according to any preceding claim, wherein a pump is configured to provide an input supply of liquid to the chamber during the first mode of operation.
7. A particle sorter according to any preceding claim, wherein the first pump is configured to provide a plurality of different frequency oscillations to the same port of the chamber or different ports of the chamber.
8. A particle sorter according to any preceding claim, wherein the chamber has an inlet flushing port and a plurality of opposed outlet flushing ports, and oscillation ports are each intermediate the inlet flushing port and an outlet flushing port, wherein the first pump is coupled to opposed oscillation ports and a second pump is coupled to an inlet flushing port to supply a flushing flow through the chamber to the outlet flushing ports.
9. A particle sorter according to claim 8, wherein the second pump is coupled to opposed outlet flushing ports comprising a central outlet flushing port between lateral outlet flushing ports, and the first pump is coupled to opposed oscillation ports that are each intermediate the inlet flushing port and a respective lateral outlet flushing port.
10. A particle sorter according to any preceding claim, wherein the first pump is coupled to provide first oscillations to a first port and second oscillations to a second port, wherein the first and second oscillations have a common oscillation frequency and a relative phase difference.
11. A particle sorter according to any preceding claim, wherein the chamber has a base and a roof, and a pillar extending between the base and the roof.
12. A particle sorter according to any preceding claim, wherein the chamber has a base and a roof, and one or both of the base and roof are provided with a periodically repeating surface profile.
13. A particle sorter according to any preceding claim, wherein the chamber has a base, a roof and side walls and ports are provided in the side walls.
14. A particle sorter according to claim 13, wherein one or more ports are provided in one or both of the base and the roof of the chamber.
15. A particle sorter according to claim 14, wherein adjacent a port provided in the base or roof of the chamber, the respective base or roof is inclined towards the port.
16. A particle sorter according to any preceding, wherein the chamber has a length, a width and a depth, and ports in the side walls have a diameter of up to 30% of the length and up to 30% of the width.
17. A particle sorter according to any preceding claim, wherein the chamber has a length of 3mm to 50mm, a width of 3mm to 50mm, and a depth of less than 1mm.
18. A particle sorter according to any preceding claim, wherein the chamber has a length, a width and a depth, and the depth is less than one third of each of the length and a width.
19. A particle sorter according to any preceding claim, comprising a plurality of serially coupled chambers.
20. A method of sorting particles with a particle sorter according to any preceding claim, comprising: providing a port of the chamber with a supply of liquid carrying particles; and providing oscillations to the liquid in the chamber.