Title of Invention

A MICROFLUIDIC SYSTEM AND A METHOD OF ISOLATING A SUBPOPULATION OF CELLS IN A MIXTURE TO BE USED IN CELL TRANSPLANTATION.

Abstract A SYSTEM (10) AND METHOD FOR SORTING PARTICLES MOVING THROUGH A CLOSED CHANNEL SYSTEM OF CAPILLARY SIZE COMPRISES A BUBBLE VALVE FOR SELECSTIVELY GENERATING A PRESSURE PULSE TO SEPARATE A PARTICLE HAVING A PREDETERMINED CHARACTERISTIC FROM A STREAM OF PARTICLES. THE PARTICLE SORTING SYSTEM MAY FURTHER INCLUDE A BUFFER FOR ABSORBING THE PRESSURE PULSE. THE PARTICLE SORTING SYSTEM (10) MAY INCLUDE A PLURALITY OF CLOSELY COUPLED SORTING MODULES WHICH ARE COMBINED TO FURTHER INCREASE THE SORTING RATE. THE PARTICLE SORTING SYSTEM MAY COMPRISE A MULTI-STAGE SORTING DEVICE FOR SERIALLY SORTING STREAMS OF PARTICLES, IN ORDER TO DECREASE THE ERROR RATE.
Full Text A MICROFLUDIC SYSTEM AND A METHOD OF ISOLATING
A SUBPOPULATION OF CELLS IN A MIXTURE TO BE
USED IN CELL TRANSPLANTATION
Related Applications
The present application claims priority to U.S.Provisional Patent Application
Serial Number 60/411,143 filed September 1.6, 2002, and U.S. Provisional Patent
Application Serial Number 60/411,058, filed September 16, 2002, the contents of
both of applications are herein incorporated by reference. The present application
also claims priority to, and is a continuation-in-part of, U. S. Patent Application
Number 10/329,008, filed December 23, 2002, which is a Continuation-in-part of
U.S. Patent Application 10/179,488, filed June 24, 2002 the contents of which are
incorporated herein by reference.
Field of the invention
The present invention relates to a microfludic system and a method of
isolating a subpopulation of cells in a mixture to be used in cell transplantation
where the input flow path of a sorting module can be split into several output
channels. More particular, the invention relates to a particle sorting system in which
a plurality of sorting modules are interconnected as to yield an increased particle
throughput.
Background of the invention
In the fields of biotechnology, and especially cytology and drug screening, there
is a need for high throughput sorting of particles. Examples of particles that require
sorting are various types of cells, such as blood platelets, white blood cells, tumorous
cells, embryonic cells and the like. These particles are especially of interest in the field
of cytology. Other particles are (macro) molecular species such as proteins, enzymes
and polynucleotides. This family of particles is of particular interest in the field of drug
screening during the development of new drugs.
Methods and apparatus for particle sorting are known, and the majority described
in the prior art work in the condition where the particles are suspended in a liquid
flowing through a channel network having at least a branch point downstream and are
operated according to the detect-decide-deflect principle. The moving particle is first
analyzed for a specific characteristic, such as optical absorption, fluorescent intensity,
size etc. Depending on the outcome of this detection phase, it is decided how the
particle will be handled further downstream. The outcome of the decision is then applied
to deflect the direction of specific particle towards a predetermined branch of the
channel network.
Of importance is the throughput of the sorting apparatus, i.e. how many particles
can be sorted per unit of time. Typical sorting rates for sorters employing flows of
particle suspension in closed channels are in the range from a few hundred particles per
second to thousands of particles per second, for a single sorting unit.
An example of a sorting device is described in U.S. Patent No. 4,175,662, the
contents of which are herein incorporated by reference (hereinafter referred to as the
"662 patent). In the "662 patent, a flow of particles, cells in this case, flows through the
center of a straight channel, which branches into two perpendicular channels at a
branching point downstream (T-branch). The entering particles are surrounded by a
sheath of compatible liquid, keeping the particles confined to the center of the channel.
In normal conditions, the flow ratio through the two branches is adjusted so that the
particles automatically flow through one of the branches, m a section of the channel a
characteristic of the particles is determined using a detector, which can be an optical
system (detection phase). The detector generates a signal when the detector detects a
particle possessing a predetermined characteristic in the decision phase. Once a particle
is detected, a deflector is activated for deflecting the particle in a deflection phase. In
this case, the deflector comprises an electrode pair, positioned in the branch of the
channel where the particles normally flow through in the inactivated state of the
deflector. By the application of current pulses, the aqueous liquid is electrolysed,
yielding a gas bubble evolving between the electrode pair. As the gas bubble increases
in size, the flow rate through this branch is reduced during the evolving phase. After the
current pulse is applied, the bubble growth stops and the gas bubble is carried along with
the flow. As a result, the flow through the specific branch is momentarily reduced and
the particle of interest changes paths and flows down the other branch.
The device of the "662 patent is effective for sorting particles. However one
serious drawback is that gas bubbles are created which potentially can accumulate at
certain points of the fluidic network. This bubble generation can clog the flow channels,
yielding erroneous sorting. Another drawback is that the generated gasses (mostly
oxygen and hydrogen) and ionic species (mostly OH- and H+) influence the particles
flowing through the branch with the electrode pair. In addition, cells and delicate
proteins such as enzymes are very fragile and can be destroyed by the fouling
constituents co-generated with the gas bubble. Another drawback is the complexity of
the overall sorting apparatus. In particular, the micro electrode construction is very
complex to mount and assemble in the small channels of the system. As a result, tne
cost of a sorting unit is relatively large.
Another example of a particle sorting system of the prior art is disclosed in U.S.
3,984,307, the contents of which are herein incorporated by reference (hereinafter the
"307 patent). In the "307 patent, the particles are flowing, confined by a flowing sheath
liquid, through the center of a channel. After passing a detector section, the channel
branches into two channels forming an acute angle therebetween (e.g., Y-branch). Just
before the branching point, an electrically activated transducer is located in the channel
for deflecting a specific particle having an appropriate, predetermined characteristic.
The transducer described is a piezo actuator or ultrasonic transducer, yielding upon
electrical activation a pressure wave in the channel- The generated pressure wave
momentarily disturbs the flow in one branch thus deflecting the partible of interest into
the other branch.
In the device of the "307 patent, as in the previous discussed device, the deflector
is incorporated within the channel system, resulting in relatively large construction
costs. Another drawback of this device is the deflector principle used. The generated
pressure waves are not confined to the branching point, but rather propagate upstream
into the detector section, as well as down both branches. This influences the overall
flow through the channel. This is particularly a drawback if sorters of this type are
connected either in series or in parallel, as is typically done to construct a high
throughput sorting system. Pressure waves generated in one sorter can then influence
the flows and deflection of particles in neighboring sorter units.
Another sorter is described in U.S. Patent No. 4,756,427, the contents of which
are herein incorporated by reference. This sorter is analogous to the sorter in the "662
patent. In this case, however, the flow in one branch is disturbed by momentarily
changing the resistance of the branch. The resistance is changed by changing the height
of the branch channel by an external actuator. In the preferred embodiment, this
external actuator is a piezo disc glued on top of the channel, causing it to move
downwards upon activation.
Although the construction of the sorter described in the "427 patent is less
complex than the previously described sorter structures, it is still problematic to couple
multiple sorter modules of the described type together to increase the sorting rate. This
is, as in the sorter described in the "307 patent because of the generated pressure waves
causing interference with other sorter modules.
Another particle sorting device is described in U.S. Patent Number 5,837,200,
the contents of which are herein incorporated by reference. The "200 patent describes a
sorting device that uses a magnetic deflection module to classify or select particles based
on their magnetic properties. The "200 patent further describes processing and
separating individual particle streams in parallel.
Summary of the invention
The present invention provides a method and apparatus for sorting particles
moving through a closed channel system of capillary size. The particle sorting system of
the invention provides a sorting module that can be assembled at low cost while
providing an accurate means of sorting large amounts of particles per unit of time. The
particle sorting system may include a plurality of closely coupled sorting modules which
arecombined to further increase the sorting rate. The particle sorting system may
comprise a multi-stage sorting device for serially sorting streams of particles, in order to
decrease the error rate.
The particle sorting system implements an improved fluidic particle switching
method and switching device according to the present invention. The particle sorting
system comprises a closed channel system of capillary size for sorting particles. The
channel system comprises a first supply duct for introducing a stream of particles and a
second supply duct for supplying a carrier liquid. The first supply duct forms a nozzle
to introduce a stream of particles into the flow of carrier liquid. The first supply duct
and the second supply duct are in fluid communication with a measurement duct, which
branches into a first branch and a second branch at a branch point. A measurement
region is defined in the measurement duct and is associated with a detector to sense a
predetermined characteristic of particles in the measurement region. Two opposed
bubble valves are positioned in communication with the measurement duct and are
spaced opposite each other. The bubble valves communicate with the measurement duct
through a pair of opposed side passages. Liquid is allowed to partly fill these side
passages to form a meniscus therein which interfaces the carrier liquid with the reservoir
of the bubble valves. An external actuator is also provided for actuating one of the
bubble valves. When the external actuator is activated, the pressure in the reservoir of
the activated bubble valve increases, deflecting the meniscus and causing a flow
disturbance in the measurement duct to deflect the flow therein.
When a sensor located in the measuring region senses a predetermined
characteristic in a particle flowing through the measurement region, the sensor produces
a signal in response to the sensed characteristic. The external actuator is responsive to
the sensor to cause a pressure pulse in a compression chamber of a first bubble valve to
deflect the particle with the predetermined characteristic, causing the selected particle to
flow down the second branch duct.
In one aspect, the invention comprises a method of sorting particles including the
steps of providing a measurement duct having an inlet and a branching point at which
the duct separates into two branch ducts, and conducting a stream of fluid into the duct
inlet with a stream of particles suspended therein, such that the particles normally flow
through a first one of the branch ducts and providing upstream from the branching point
two opposing side passages for momentarily deflecting the stream in the duct. A first
one of the side passages is hydraulically connected to a compression chamber of a first
bubble valve, which is acted upon by an external actuator for varying the pressure
therein. A second of the side passages is hydraulically connected with a buffer chamber
of a second bubble valve for absorbing pressure variations. The method further
comprises providing a measurement station along the measurement duct upstream of the
side passages for sensing a predetermined characteristic of particles in the stream and for
producing a signal when the predetermined characteristic is sensed. The method further
comprises the step of, in response to sensing the predetermined characteristic, activating
the external actuator for creating a flow disturbance in the duct between the side
passages, thereby deflecting the particle having the predetermined characteristics and
causing the selected particle to flow down the second branch duct.
In further aspects of the invention, the particle sort rate is respectively increased
or the type of particles sorted being increased, by respectively connecting a plurality of
sorting modules in parallel or serially connecting a plurality of sorting modules in a
binary tree like configuration.
According to one aspect of the invention, a particle sorting system is provided.
The particles sorting system comprises a first duct for conveying a stream of suspended
particles confined in a carrier liquid, comprising an inlet, a first outlet and a second
outlet, a sensor for sensing a predetermined characteristic in a particle, a side channel in
communication with the first duct, a sealed chamber positioned adjacent to the side
channel, wherein the carrier fluid forms a meniscus in the side channel to separate the
sealed chamber from the carrier fluid; and an actuator. The actuator modifies the
pressure in the sealed chamber to deflect the meniscus when the sensor senses the
predetermined characteristic. The deflection of the meniscus causes the particle having
the predetermined characteristic to flow into the second outlet while particles that do not
have the predetermined characteristic flow into the first outlet.
It is contemplated that the present invention will be of major value in high-
throughput screening; e.g., in screening a large number of candidate compounds for
activity against one or more cell types. It has particular value, for example, in screening
synthetic or natural product libraries for active compounds or biochemical
characterization.
It is also contemplated that the present invention will be of major value in high-
throughput screening of a sample for a plurality of molecules, such as biological
molecules. The present invention can be used to screen a sample for the presence of a
large number of biological molecules such as polypeptides, receptor ligands, enzymatic
substrates, agonists or antagonists of enzymatic or receptor activity, or nucleic acids.
BRIEF DESCRIPTION OF THE ACCOMPANYING DRAWINGS
FIG. 1 is a schematic view of a particle sorting system according to an
illustrative embodiment of the invention.
FIGS. 2 through 4 illustrate the operation of the particle sorting system of FIG 1.
FIG. 5 illustrates a particle sorting system showing alternate positions for the
actuator chamber and the buffer chamber.
FIG. 6 illustrates the particle sorting system according to another embodiment of
the invention.
FIG. 7 illustrates a bubble valve suitable for use in the particle sorting system of
the present invention.
FIG. 8 is a schematic diagram of the particle sorting system of an illustrative
embodiment of the present invention.
FIG. 9 shows one embodiment of a particle sorting system for sorting parallel
streams of particles according to the teachings of the present invention.
FIG. 10 shows one embodiment of a particle sorting system configured in a
binary tree-like configuration of sorting modules according to the teachings of the
present invention.
FIG. 11 illustrates another embodiment of a multi-stage particle sorting system
for sorting parallel streams of particles in multiple stages.
FIG. 12 illustrates a parallel particle sorting system according to an alternate
embodiment of the present invention.
FIG. 13 illustrates a parallel particle sorting system according to another
embodiment of the present invention.
FIG 14a and 14b illustrate a particle sorting system according to another
embodiment of the invention, including an optical mask to allow measurement of a
particle size and/or velocity.
FIG. 15 illustrates a parallel sorting system having variable channels according
to another embodiment of the present invention.
FIG. 16 illustrates a variable array design of a parallel sorting system according
to another embodiment of the present invention.
FIG. 17 illustrates a parallel sorting system according to another embodiment of
the present invention.
FIG. 18 illustrates drug screening system implementing the particle sorting
system of the present invention.
Detailed Description of the Invention
The present invention provides a particle sorting system for sorting particles
suspended in a liquid. The particle sorting system provides high-throughput, low error
sorting of particles based on a predetermined characteristic. The present invention will
be described below relative to illustrative embodiments. Those skilled in the art will
appreciate that the present invention may be implemented in a number of different
applications and embodiments and is not specifically limited in its application to the
particular embodiments depicted herein.
The terms "duct" "channel" and "flow channel" as used herein refers to a
pathway formed in or through a medium that allows for movement of fluids, such as
liquids and gases. The channel in the microfluidic system preferably have cross-
sectional dimensions in the range between about 1.0 µm and about 500 µm, preferably
between about 25 µm and about 250 µm and most preferably between about 50 µm and
about 150 µm. One of ordinary skill in the art will be able to determine an appropriate
volume and length of the flow channel. The ranges are intended to include the above-
recited values as upper or lower limits. The flow channel can have any selected shape or
arrangement, examples of which include a linear or non-linear configuration and a U-
shaped configuration.
The term "particle" refers to a discrete unit of matter, including, but not limited
to cells.
The term "sensor" as used herein refers to a device for measuring a characteristic
of an object, such as a particle.
The term "bubble valve" as used herein refers to a device that generates pressure
pulses to control flow through a channel.
The term "carrier fluid" as used herein refers to a sheath of compatible liquid
surrounding a particle for carrying one or more particles through a duct or channel.
FIG. 1 is a schematic depiction of a particle sorting system 10 according to the
teachings of the present invention. According to one application of the present
invention, the particle sorting system 10 comprises a closed channel system of capillary
. size for sorting particles. The channel system comprises a first supply duct 12 for
introducing a stream of particles 18 and a second supply duct 14 for supplying a carrier
liquid. The first supply duct 12 forms a nozzle 12a, and a stream of particles is
introduced into the flow of the carrier liquid. The first supply duct 12 and the second
supply duct 14 are in fluid communication with a measurement duct 16 for conveying
the particles suspended in the carrier liquid. The measurement duct branches into a first
branch channel 22a and a second branch channel 22b at a branch point 21. A
measurement region 20 is defined in the measurement duct 16 and is associated with a
detector 19 to sense a predetermined characteristic of the particles passing through the
measurement region 20. Two opposed bubble valves 100a and 100b are positioned
relative to the measurement duct and disposed in fluid communication therewith. The
valves are spaced opposite each other, although those of ordinary skill will realize that
other configurations can also be used. The bubble valves 100a and 100b communicate
with the measurement duct 16 through a pair of opposed side passages 24a and 24b,
respectively. Liquid is allowed to partly fill these side passages 24a and 24b to form a
meniscus 25 therein. The meniscus defines an interface between the carrier liquid and
another fluid, such as a gas in the reservoir of the associated bubble valve 100. An
actuator 26 is also provided for actuating either bubble valve, which momentarily causes
a flow disturbance in the duct to deflect the flow therein when activated by the actuator
26. As illustrated, the actuator is coupled to the bubble valve 100b. The second bubble
valve 100a serves as a buffer for absorbing the pressure pulse created by the first bubble
valve 100b.
The first side passage 24b is hydraulically connected to a compression chamber
70b in the first bubble valve 100b, so that if the pressure in this chamber is increased,
the flow in the measurement duct near the side passage is displaced inwards,
substantially perpendicular to the normal flow in the duct. The second side passage 24a,
positioned opposite of the first side passage 24b is hydraulically connected to a buffer
chamber 70a in the second bubble valve 100a for absorbing pressure transients. This
first side passage 24b co-operates with the second side passage 24a to direct the before
mentioned liquid displacement caused by pressurizing the compression chamber 70b, so
that the displacement has a component perpendicular to the normal flow of the particles
through the measurement duct
Upon pressurizing the compression chamber 70b an amount of liquid is
transiently discharged from the first side passage 24b. The resiliency of the second side
passage 24a results upon a pressurized discharge, in a transient flow of the liquid in the
duct into the second side passage 24a. The co-operation of the two side passages and the
fluidic structures they interconnect causes the flow through the measurement duct 16 to
be transiently moved sideways back and forth upon pressurizing and depressurising of
the compression chamber 70b induced by the external actuator 26 in response to the
signal raised by the detection means 19. This transient liquid displacement, having a
component perpendicular to the normal flow in the duct, can be applied in deflecting
particles having predetermined characteristics to separate them from the remaining
particles in the mixture.
As shown, the measurement duct 16 branches at the branch point 21 into two
branches 22a, 22b and the flow rates in these branches are adjusted so that the particles
normally stream through the second of the two branches 22b. The angle between the
branches 22a, 22b is between 0 and 180 degrees, and preferably between 10 and 45
degrees. However, the angle can even be 0 degrees, which corresponds to two parallel
ducts with a straight separation wall between them.
The particles to be sorted are preferably supplied to a measurement position in a
central fluid current, which is surrounded by a particle free liquid sheath. The process of
confining a particle stream is known, and often referred to as a "sheath flow"
configuration. Normally, confinement is achieved by injecting a stream of suspended
particles through a narrow outlet nozzle into a particle free carrier liquid flowing in the
duct 16. By adjusting the ratio of flow rates of the suspension and carrier liquid, the
radial confinement in the duct as well as the inter particle distance can be adjusted. A
relatively large flow rate of the carrier liquid results in a more confined particle stream
having a large distance between the particles.
In a suspension introduced by the first supply duct 12, two types of particles can
be distinguished, normal particles 18a and particles of interest 18b. Upon sensing the
predetermined characteristic in a particle 18b in the measurement region 20, the detector
19 raises a signal. The external actuator 26 activates the first actuator bubble valve 100b,
when signaled by the detector 19 in response to sensing the predetermined characteristic,
to create a flow disturbance in the measurement duct 16 between the side passages 24a,
24b. The flow disturbance deflects the particle 18b having the predetermined
characteristic so that it flows down the first branch duct 22a rather than the second
branch duct 22b. The detector communicates with the actuator 26, so that when the
detector 19 senses a predetermined characteristic in a particle, the actuator activates the
first bubble valve 100b to cause pressure variations in the reservoir 70b of the first
bubble valve. The activation of the first bubble valves deflects the meniscus 25b in the
first bubble valve 100b and causes a transient pressure variation in the first side passage
24b. The second side passage 24a and the second bubble valve 100a absorb the transient
pressure variations in the measurement duct 16 induced via the actuator 26. Basically,
the reservoir 70a of the second bubble valve 100a is a buffer chamber having a resilient
wall or containing a compressible fluid, such as a gas. The resilient properties allow the
flow of liquid from the measurement duct into the second side passage 24a, allowing the
pressure pulse to be absorbed and preventing disturbance to the flow of the non-selected
particles in the stream of particles.
At the measurement region 20, individual particles are inspected, using a suitable
sensor 19, for a particular characteristic, such as size, form, fluorescent intensity, as well
as other characteristics obvious to one of ordinary skill. Examples of applicable sensor,
known in the art, are various types of optical detection systems such as microscopes,
machine vision systems and electronic means for measuring electronic properties of the
particles. Particularly well known systems in the field are systems for measuring the
fluorescent intensity of particles. These systems comprise a light source having a
suitable wavelength for inducing fluorescence and a detection system for measuring the
intensity of the induced fluorescent light. This approach is often used in combination
with particles that are labelled with a fluorescent marker, i.e. an attached molecule that
upon illuminating with light of a particular first wavelength produces light at another
particular second wavelength (fluorescence). If this second wavelength light is detected,
the characteristic is sensed and a signal is raised.
Other examples include the measurement of light scattered by particles flowing
through the measurement region. Interpreting the scattering yield information on the size
and form of particles, which can be adopted to raise a signal when a predetermined
characteristic is detected.
The actuator 26 for pressurizing the compression chamber of the first bubble
valve can comprise an external actuator that responds to a signal from the sensor that a
particle has a selected predetermined characteristic. There are two classes of external
actuators that are suitable for increasing the pressure. The first class directly provides a
gas pressure to the liquid in the first side passage 24b. For example, the actuator may
comprise a source of pressurized gas connected with a switching valve to the liquid
column in the side passage 24b. Activation of the switch connects the passage to the
source of pressurized gas, which deflects the meniscus in the liquid. Upon deactivation,
the switch connects the passage 24b back to the normal operating pressure.
Alternatively, a displacement actuator may be used in combination with a closed
compression chamber having a movable wall. When the displacement actuator displaces
the wall of the compression chamber inward, the pressure inside increases. If the
movable wall is displaced back to the original position, the pressure is reduced back to
the normal operating pressure. An example of a suitable displacement actuator is an
electromagnetic actuator, which causes displacement of a plunger upon energizing a
coil. Another example is the use of piezoelectric material, for example in the form of a
cylinder or a stack of disks, which upon the application of a voltage produces a linear
displacement. Both types of actuators engage the movable wall of the compression
chamber 70 to cause pressure variations therein.
Figures 2 through 4 illustrate the switching operation of switch 40 in the particle
sorting system 10 of Figure 1. In Figure 2, the detector 19 senses the predetermined
characteristic in a particle and generates a signal to activate the actuator 26. Upon
activation of the actuator, the pressure within the reservoir 70b of the first bubble valve
100b is increased, deflecting the meniscus 25b and causing a transient discharge of
liquid from the first side passage 24b, as indicated by the arrow. The sudden pressure
increase caused at this point in the duct causes liquid to flow into the second side
passage 24a, because of the resilient properties of the reservoir of the second bubble
valve 100a. This movement of liquid into the second side passage 24a is indicated with
an arrow. As a result, as can be seen in the figure, the flow through the measurement
duct 16 is deflected, causing the selected particle of interest 18b located between the first
side passage 24b and the second side passage 24a to be shifted perpendicular to its flow
direction in the normal state. The flow resistances to the measurement duct 16, the first
branch 22a and the second branch 22b is chosen so that the preferred direction of the
flow to and from the first side passage 24b and the second side passage 24a has an
appreciable component perpendicular to the normal flow through the measurement duct
16. This goal can for instance be reached by the first branch 22a and the second branch
22b so that their resistances to flow is large in comparison with the flow resistances of
the first side passage 24b and the second side passage 24a.
Figure 3 shows the particle sorting system 10 during the relief of the first bubble
valve reservoir when the particle of interest 18b has left the volume between the first
side passage 24b and the second side passage 24a. The actuator 26 is deactivated,
causing the pressure inside the reservoirs 70a, 70b to return to the normal pressure.
During this relief phase there is a negative pressure difference between the two
reservoirs 70a, 70b of the bubble valves, causing a liquid flow through the first side
passage 24b and the second side passage 24a opposite to the liquid flow shown in the
previous figure and as indicated by the arrows.
Figure 4 illustrates the particle sorting system 10 after completion of the
switching sequence. The pressures inside the reservoirs of the bubble valves are
equalized, allowing the flow through the measurement duct 16 to normalize. As the
particle of interest 18b has been displaced radially, it will flow into the first branch 22a,
while the other particle continue to flow into the second branch 22b, thereby separating
the particles based on the predetermined characteristic.
This process of detecting and selective deflecting of particles may be repeated
many times per second for sorting particles at a high rate. Adopting the fluid switching
as described, switching operations may be executed up to around several thousand
switching operations per second, yielding sorting rates in the order of million sorted
particles per hour.
According to another embodiment of the invention, the actuator bubble valve
100a and the buffer bubble valve 100b maybe placed in different positions. For
example, as shown in Figure 5, the actuator bubble valve 100a and the first side passage
24a and/or the buffer bubble valve 100b and the second side passage 24b may be place
upstream from the branch point 21. The components may be placed in any suitable
location, such that the flow resistance between the actuator chamber 70a and the buffer
chamber 70b is less than the flow resistance between any of these latter components and
other pressure sources. More particularly, the actuator chamber 70a and the buffer
chamber 70b may be placed such that the flow resistance between them is less than the
flow resistance between a selected particle and a subsequent particle in the stream of
particles. The positioning of the components in this manner thus prevents a pressure
wave generated by the above-described method of deflecting a single selected particle,
from travelling upstream or downstream and affecting the flow of the remaining
particles in the stream of particles. A larger difference in flow resistances results in a
higher level of isolation of the fluidic switching operation with associated pressure
transients from the flow characteristics in the rest of the system. Moreover, the in-situ
dampening of generated pressure pulses applied for sorting allows the implementation of
sorting networks comprising a plurality of switches 40, each of which is hydraulically
and pneumatically isolated from the others.
According to another embodiment, shown in Figure 6, the particle sorting system
of the present invention may use any suitable pressure wave generator (in place of a
bubble valve) in combination one or more bubble valves serving as a buffer, such as
valve 100b. For example, the pressure wave generator 260 may comprise an actuator
such as a piezoelectric column or a stepper motor, provided with a plunger that can act
upon the flowing liquid, either directly or via deflection of the channel system, to
selectively deflect particles when the actuator is activated by a signal. Other suitable
pressure wave generators include electromagnetic actuators, thermopneumatic actuators
and a heat pulse generator for generating vapor bubbles in the flowing liquid by
applying heat pulses. The buffer bubble valve 100b is positioned to absorb the pressure
wave created by the pressure wave generator 260 to prevent flow disturbance in the
other particles of the particle stream. The spring constant of the buffer 100b may be
varied according to the particular requirements by varying the volume of the buffer
chamber 70b, the cross-sectional area of the side passage 24b and/or the stiffness or the
thickness of a flexible membrane (reference 72 in Figure 7) forming the buffer chamber
70b.
Fig. 7 illustrates an embodiment of a valve 100 suitable for creating a pressure
pulse to separate particles of interest from other particles in a stream of particles and/or
acting as a buffer for absorbing a pressure pulse according to the teachings of the present
invention. As shown, the valve 100 is formed adjacent to a side passage 24a or 24b
formed in a substrate which leads to the measurement duct 16. The side passage 24a
includes a fluid interface port 17 formed by an aperture in the side wall of the passage.
A sealed compression chamber 70 is positioned adjacent to the side passage 24a and
communicates with the side passage through the fluid interface port. The illustrative
chamber 70 is formed by a seal 71 and a flexible membrane 72. The carrier fluid in the
side passage 24a forms a meniscus 25 at the interface between the side passage and the
chamber. The actuator 26 depresses the flexible membrane to increase the pressure in
the chamber, which deflects the meniscus and causes a pressure pulse in the carrier fluid.
Fig. 8 shows a sorting module 50 having an appropriate supply duct 52 for
providing a stream of particles to be sorted as well as a first outlet duct 54 and a second
outlet duct 56, either of which can carry the particles sorted in the sorting module 50.
The sorting module 50 comprises a detector system 19 for sensing particles entering the
sorting module 50 via the supply duct 52 can be operationally connected to a switch 40
for providing the required switching capabilities to sort particles. The first branch 22b
and the second branch 22a, Figure 1, can be disposed in fluidic connection with the
outlet duct 54 and the second outlet duct 56.
Fig. 9 shows a particle sorting system 500 according to an alternate embodiment
of the invention, comprising a plurality of sorting modules 50 that can be coupled
together in any appropriate configuration. For example, the modules 50 in this
embodiment are coupled in parallel. The outlet ducts 54 of the sorting modules 50 are
coupled to a first combined outlet 58, the second outlet ducts 56 are coupled to a second
combined outlet 60. The parallel arrangement of sorting modules yields a system of
combined sorting module 50 having an overall sorting rate of N times the sorting rate of
an individual sorting module 50, where N is the number of parallel connected sorting
module 50.
Fig. 10 shows a particle sorting system 550 according to another embodiment,
comprising a first sorting module 50a in series with a second sorting module 50b. The
second sorting module 50b may be equipped for sorting particles having a
predetermined characteristic the same or different than the predetermined characteristic
of the particles sorted by the first sorting module 50a. The particle stream enters the first
sorting module 50a through the supply duct 52 and may contain at least two types of
particles. A first type of particle is sorted in the first sorting module 50a and exits
through the first outlet duct 54a. The remaining particles exit the first sorting module
50a through second outlet duct 56a and are introduced into the second sorting module
50b via the second supply duct 52b. From this stream of particles, particles having the
other predetermined characteristic are sorted and exit through the second outlet duct 54b
Particles that posses neither of the two predetermined characteristics exit the second
sorting module 50b via the second outlet duct 56b. Those of ordinary skill will readily
recognize that any suitable type of sorting module 50 can be used, and can be coupled
together in a variety of ways, depending upon the desired results.
Figure 11 shows a hierarchical architecture for high throughput-low error sorting
according to another embodiment of the present invention. The illustrated embodiment
is a two-stage particle sorting system 800 for sorting a plurality of parallel particles
streams in a first stage, aggregating the outputs of the first stage and then performing a
secondary sorting process on the output of the first stage. An input stream of particles in
suspension 80 from a particle input chamber 88 is split among N single sorting channels
81a-81n, each channel being capable of sorting a selected number of particles per
second. Each channel 81 includes a detection region 84 for examining the particles and
identifying particles that have a predetermined characteristic, and a switching region 82
for separating the particles having the predetermined characteristic from the other
particles in the stream, as described above. The switching region 82 produces two
output streams of particles: a "selected" stream and a "rejected" stream in its switching
region 82 based on the measured particle characteristics at the detection region 84. The
"selected" streams from each channel are aggregated in an aggregation region 86 into
one stream to be sorted again in a secondary sorting channel 810. As shown, the
secondary sorting channel 810 repeats the sorting process of detecting and sorting based
on a predetermined characteristic.
Given that each single channel sorting process produces some error (y) rate (y is
a probability less than one of a particle being "selected" by mistake) of mistaken
selections, the hierarchical architecture produces an lower error rate of y2 for a 2-stage
hierarchy as drawn or yn for an n-stage hierarchy. For example, if the single channel
error rate is 1% the 2-stage error rate is 0.01% or one part in 104.
Alternatively, the architecture could have M primary sets of N sorting channels
per secondary channel. Given that the application wants to capture particles that have a
presence in the input at rate z and single channel sorters have a maximum sorting rate x
particles per second. The system throughput is M*N*x in particles per second. The
number of particles aggregated in N channels per second is N*x*z and so N*z must be
less than 1 so that all particles aggregated from N channels can be sorted by a single
secondary channel. To increase throughput above N=1/z one must add parallel groups
of N primary + 1 secondary channels. Overall throughput then comes from M*N*x with
M secondary channels.
Figure 12 show a parallel-serial particle sorting system 160 according to another
embodiment of the invention. The parallel-serial particle sorting system 160 includes a
first parallel sorting module 161 and a second parallel sorting module 162. The first
sorting module 161 is applied in multiple marked particles and particles having both
markers are sorted out and conveyed through the exit channel 165.
Figure 13 shows another parallel-serial particle sorting system 170. The first
parallel sorting module 171 separates particles having a first marker, collects the
particles from the different channels and conveys the particles having the first marker
through the first exit channel 175. All other particles are then fed into a second parallel
sorter 172 for sorting particles having a second marker. The particles having the second
marker are collected and conveyed through a second exit channel 176. Particles having
neither the first marker nor the second marker are conveyed through a third exit channel
177.
According to one embodiment of the invention, shown in Figures 14a and 14b,
the particle sorting system may include sensors for measuring velocity, location and/or
size of particles. The measurement of velocity, location and/or size may be made
simultaneously with classification of the particles for sorting or at a different time. In
parallel channel based systems, as shown in Figure 11, the different channels may have
different flow resistances, causing the velocity of the particles or cells in each channel to
be different. In systems where the detection region 84 is separated from the switching
region 82 by a distance L, the velocity of the particles in the channel 81 must be known
in order to set the switching time delay T (i.e., the time to delay switch actuation relative
to the moment of detection of a target particle).
In most optical systems for detecting cells or particles, the region in which the
cell creates light on the photo detector in the detection region will have a much greater
size than the size of a cell diameter. Therefore, when light is detected in the detection
region, the cell may be anywhere in the region, making it difficult to pinpoint the exact
location of the cell. To provide more accurate detection, many pixels of an optical
detector could be packed across the detection region, but this would have a large cost
and require complex support electronics.
According to an illustrative embodiment of the invention, an optical mask 140
may be added to the detection region to provide accurate velocity detection by
depositing a "masking pattern" directly on the sorting chip. The masking patterns can be
deposited so that an edge in the masking pattern is precisely located (to with current technology) relative to the cell sorting actuator region 82. A single optical
detector catching light from the cell in the detection region 84 will see light when the
cell is not masked. The duration of the light being turned off by one of the connected
opaque parts "bars" of the mask of known length gives a measurement of velocity.
A mask pattern that has several bars 141 of size ranging from 10um to 30um in
lum steps results in only bars of size larger than the cell minimizing the signal from the
cell. Therefore, such a pattern can also be used to measure the size of the cell
independently of its signal. Such a "gradient mask" also produces a pattern in the optical
detector that can be analyzed to measure velocity several times for reducing the variance
in the velocity estimate. The pattern in the light induced by the mask 140 also allows
the detector to identify each edge in. the mask 140. If the bars 141 were all the same, the
light signal for each bar would be the same, and one could only tell them apart by
sequence. Therefore, a gradient mask pattern will allow a single detector looking at a
broad region (several times the size of a cell) to measure the velocity of the cell, measure
the exact position inside the detection region 84 with about lum precision relative to the
channel structures and the actuator location on chip and identify the size of the cell to
precision given by the gradient pattern. The gradient mask 140 allows the detector to
measure these parameters independent of the magnification of the optical system or the
nature of the optical detector itself.
One skilled in the art will recognize that other devices for measuring the size,
position and or velocity of a particle in the sorting system in accordance with the
teachings of the invention. Suitable devices are readily available and known to those of
ordinary skill in the art.
According to another embodiment, shown in Figure 15, the particle sorting
system comprises an array 8000 of non-identical sorting channels. The use of a parallel
array comprising a series of non-identical sorter channels 810a-810n is more efficient in
terms of space, use of optical power and adaptation to optimal external actuators. Since
the velocity of particles can be accurately sensed, the channels do not require a fixed
delay between the detection of a property and actuation of a switch to deflect a particle
having the detected property. Therefore, certain parameters of the channel, such as the
distance L between a detector 84 and a switch 82 or the shape of the path between the
detector 84 and the switch 82 can be varied.
Using a single laser for each wavelength optical illumination directed
perpendicular to the chip, the laser is required to illuminate an area defined by: (number
of channels)X((channel width at detection regjon)+(inter channel spacing C)) (See
Figure 15). However, the active area where light can be absorbed to create fluorescence
is only the area of the channels: (number of channels)X(channel width), which leaves a
fill factor of: (channel width)/(channel width + C). The fill factor is preferably close to
100% to avoid wasting available input light.
Therefore, minimizing the interchannel spacing in a parallel sorting system is
important to the optical detection region and optical system efficiency. In the variable
array design of the present invention, shown in Figure 16, the spacing of the channels in
the detection region 84 approaches the width of the channels, so that light utilization
approaches about 50 %. The channel spacing in the actuation region 82 may be larger,
as shown in Figure 16. The location of actuators26 along the channel may also be varied
to make a larger available radius for external driver actuators.
The variable array 8000 may also include meanders in selected channels for
balancing flow resistances of all the channels so that given a constant pressure drop
across all the channels the velocities of particles are nearly matched. These can be
added either upstream or downstream of the illustrated system, i.e., on in the region
between the detectors and actuators. As the lengths Li between each channel"s detection
region 821 and its actuator 26i is known from the design, the measurement of the particle
velocity at the same time as the determination regarding which particles to keep provides
an improved cell sorting system.
Figure 17 illustrates a particle sorting system 1700 according to yet another
embodiment of the invention. The particle sorting system 1700 includes a plurality of
sorting modules 1701 operating in parallel. The system 1700 includes an input region
1710 for introducing samples to each sorting module and a detection region 1720 for
measuring a predetermined characteristic of particles each sorting channel 1702 in the
detection region. The system also includes a switch region 1730, including an actuator in
each sorting module for separating particles having a predetermined characteristic from
particles that do not have the predetermined characteristic. As shown, in the
embodiment of Figure 17, the sorting channels 1702 distance between each sorting
channel in the detection region 1720 is less than the inter-channel distance in the switch
region 1730. The close spacing in the detection region enables cost saving when a laser
is used to detect the particles, while the more distant separation in the switch region
1730 accommodates various sized actuators.
The particle sorting system 1700 may also include a secondary sorting module
1740 for repeating the sorting process of detecting and sorting based on a predetermined
characteristic to increase the accuracy of the sorting process. According to one
embodiment, the system may include an enrichment region 1750 between the array of
primary sorting modules 1701 and the secondary sorting module 1740 for transitioning
the particles from the primary sorting process to the secondary sorting process.
According to an illustrative embodiment, the enrichment region 1750 transitions the
particles by removing excess carrier fluid from the particles before passing the particles
to the secondary sorting module 1740. The enrichment region 1750 may also include a
hydration device for adding secondary sheet fluid to the particles after enrichment. The
enrichment region 1750 may comprise a membrane inserted into outlet channel 1703, an
enrichment channel intersecting the outlet channel 1703 and a membrane separating the
outlet channel from the enrichment channel. Excess carrier fluid is removed from the
stream of selected particles in the outlet channel 1703 through the membrane and into
the enrichment channel before passing the selected particles into the secondary sorting
module 1740.
A suitable system for forming the enrichment region is described in U.S. Patent
Application Number 10/329,018, entitled "Implementation of Microfluidic Components
in aMicrofluidic System", the contents of which are herein incorporated by reference
According to the illustrative embodiment, the removed carrier fluid may be
recycled and fed back into the inlet of the primary channels. A recycling channel or
other device may connect the enrichment region to the primary channel to allow re-use
of the carrier fluid for subsequent sorting process. Alternatively, the carrier fluid may be
removed from rejected particles and introduced into the primary channel inlets prior to
discarding the rejected particles.
The particle sorting system of the present invention has a variety of applications
in the microfluidic art. According to one application, the particle sorting system may be
implemented in a drug screening system, as shown in Figure 18. As shown in Figure 18,
a drug screening system 140 includes a particle sorting module 10 for identifying and
separating target cells from a sample containing the target cells. The sample containing
the target cells is introduced to the screening system through an input channel and passes
to the particle sorting module, which separates the target cells from the rest of the
sample and passes the target cell to a mixing and incubation region 141. Test
compounds are introduced to the mixing and incubation region 141 through a test
channel 142 and contact the target cells provided from the particle sorting subsystem 10.
The effect of the test compound on the target cells is then detected in a detection region
145.
The illustrative drug screening system 140 with the particle sorter 10 may be
used with a variety of types of markers. The drug screening system enables use of
markers that allow measurement of the activity of a specific enzyme, thereby allowing a
search for modulators of the pathways that the enzyme exists in. The drug screening
system also enables use of markers that allow measurement of the concentration of any
intracellular messenger/signal and markers to identify specific cell types, particularly
rare (less than one per one-hundred cells) types. For example, suitable markers include,
but are not limited to, cell surface markers, such as antibodies and recombinant display
technologies, as well as fluorogenic enzyme substrate markers, intracellular signal
binding compounds, such as Ca++ binding fluorescent dyes (Fura-3, Indo-1), and bio-
luminescent enzyme substrate markers. In fluorogenic enzyme substrate markers,
compounds enter cells and are converted by specific intracellular enzymes to be
fluorescent. Examples are Bodipy aminoacetaldehyde or BAAA for ALDH enzymes,
MUP ( 4-methylumbelliferyl phosphate) for Phosphatases and Dihydrorhodamine 123
for cell Redox systems. Other examples of fluorescent dyes that can be used in
methods of the instant invention include, In bio-luminescent enzyme substrate markers,
compounds enter cells and interact with specific intracellular enzymes generate light
directly. Often this technology can be tied to reporter genes to observe gene activation.
Examples include D-Luciferin and associated reporter genes, as well as DMNPE and
associated reporter genes.
In the illustrative application, any number of different compounds may be
screened for their effects on a variety of chemical and biochemical systems. For
example, compounds may be screened for effects in blocking, slowing or otherwise
inhibiting key events associated with biochemical systems whose effect is undesirable.
For example, test compounds may be screened for their ability to block systems that are
responsible, at least in part, for the onset of disease or for the occurrence of particular
symptoms of diseases, including, e.g., hereditary diseases, cancer, bacterial or viral
infections and the like. Compounds which show promising results in these screening
assay methods can then be subjected to further testing to identify effective
pharmacological agents for the treatment of disease or symptoms of a disease.
Alternatively, compounds can be screened for their ability to stimulate, enhance
or otherwise induce biochemical systems whose function is believed to be desirable,
e.g., to remedy existing deficiencies in a patient.
The invention may be used to isolate rare cells (i.e., comprising less than .1%-
1% of the input sample) for a variety of applications, such as, but not limited to: cell
reimplantation, cell transplantation and cell transfection or genetic modification
followed by reimplantation or transplantation. The invention may also be used to isolate
tumor cells in a sample for development of tailored treatments.
The invention may be utilized to screen compounds on primary cells, for
example, taking 1011 cells by apheresis and screening on any sub population, rather than
cell lines. The invention may also be used to screen compounds on imperfect cell lines,
where less than 100% of the cell line expresses the correct genes for the screening
program. The invention may also be utilized to screen compounds on cells at specific
cell-cycle stages, for example, screening on cells only in the replication phase.
The present invention has been described relative to an illustrative embodiment.
Since certain changes may be made in the above constructions without departing from
the scope of the invention, it is intended that all matter contained in the above
description or shown in the accompanying drawings be interpreted as illustrative and not in a limiting sense.
It is also to be understood that the following claims are to cover all generic and
specific features of the invention described herein, and all statements of the scope of the
invention which, as a matter of language, might be said to fall therebetween.
Having described the invention, what is claimed as new and protected by
Letters Patent is:
WE CLAIM :
1. A microfluidic system comprising :
a substrate;
a cell sorting system formed on the substrate for sorting cells based on the
predetermined characteristic; and
a screening system formed on the substrate for screening cells, said screening
system having a mixing region for mixing cells having the predetermined characteristic
with a test compound and a detection region for detecting the effect of the test
compound on the cells having the predetermined characteristic.
2. The microfluidic system as claimed in claim 1, comprising a connecting channel
between the cell sorting system and the screening system for conveying selected cells
from the cell sorting system to the screening system.
3. The microfluidic system as claimed in claim 1, wherein the cell sorting system
comprises:
a first duct for conveying a stream of suspended cells in a carrier liquid,
comprising an inlet, a first outlet and a second outlet;
a sensor for sensing a predetermined characteristic in a particle and one of a
size and a velocity of a particle;
a side channel in communication with the first duct;
a sealed chamber positioned adjacent to the side channel, wherein the carrier
fluid forms a meniscus in the side channel to separate the sealed chamber from the
carrier fluid; and
an actuator for modifying the pressure in the sealed chamber to deflect the
meniscus when the sensor senses said predetermined characteristic, whereby the
deflection of the meniscus causes the cells having said predetermined characteristic
to flow into the second outlet while cells that do not have said predetermined
characteristic flow into the first outlet.
4. The microfluidic system as claimed in claim 3, wherein the cell sorting system
comprises a buffer for absorbing pressure variations in the first duct.
5. The microfluidic system as claimed in claim 3, wherein the actuator comprises
a source of pressurized gas.
6. The microfluidic system as claimed in claim 3, wherein the sealed chamber
comprises a movable wall.
7. The microfluidic system as claimed in claim 5, wherein the actuator comprises
a displacement actuator for moving the movable wall of the sealed chamber to modify
the pressure in the sealed chamber.
8. The microfluidic system as claimed in claim 7, wherein the actuator comprises
one of an electromagnetic actuator and a piezoelectric element.
9. A method for screening for the ability of a compound to modulate the activity of
a cell, wherein said cell is contacted with a test compound and said cells response to
said test compound is monitored using the microfluidic system as claimed in claim 1.
A system (10) and method for sorting particles moving through a closed
channel system of capillary size comprises a bubble valve for selectively generating
a pressure pulse to separate a particle having a predetermined characteristic from a
stream of particles. The particle sorting system may further include a buffer for
absorbing the pressure pulse. The particle sorting system (10) may include a
plurality of closely coupled sorting modules which are combined to further increase
the sorting rate. The particle sorting system may comprise a multi-stage sorting
device for serially sorting streams of particles, in order to decrease the error rate.

Documents:

400-KOLNP-2005-CORRESPONDENCE-1.1.pdf

400-KOLNP-2005-CORRESPONDENCE.pdf

400-KOLNP-2005-EXAMINATION REPORT.pdf

400-kolnp-2005-granted-abstract.pdf

400-kolnp-2005-granted-claims.pdf

400-kolnp-2005-granted-correspondence.pdf

400-kolnp-2005-granted-description (complete).pdf

400-kolnp-2005-granted-drawings.pdf

400-kolnp-2005-granted-examination report.pdf

400-kolnp-2005-granted-form 1.pdf

400-kolnp-2005-granted-form 13.pdf

400-kolnp-2005-granted-form 18.pdf

400-kolnp-2005-granted-form 3.pdf

400-kolnp-2005-granted-form 5.pdf

400-kolnp-2005-granted-gpa.pdf

400-kolnp-2005-granted-letter patent.pdf

400-kolnp-2005-granted-reply to examination report.pdf

400-kolnp-2005-granted-specification.pdf

400-KOLNP-2005-PA.pdf


Patent Number 214089
Indian Patent Application Number 400/KOLNP/2005
PG Journal Number 05/2008
Publication Date 01-Feb-2008
Grant Date 30-Jan-2008
Date of Filing 11-Mar-2005
Name of Patentee CYTONOME, INC.
Applicant Address 84, ROSEDALE ROAD, WATERTOWN, MA, 02472
Inventors:
# Inventor's Name Inventor's Address
1 GILBERT JOHN R. 69 NAPLES ROAD, BROOKLINE, MA 02446
2 BOHM SEBASTIAN 9 MUIRFIELD COURT, INVERNESS IV2 4DP
3 DESHPANDE MANISH 34 APPLE BLOSSOM WAY, CANTON, MA, 02021
PCT International Classification Number G01N 21/27
PCT International Application Number PCT/US2003/029198
PCT International Filing date 2003-09-16
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 60/411,058 2002-09-16 U.S.A.