Syringe pump abstract
A syringe pump particularly adapted for delivery of small volumes
at a high pressure in an accurate and reproducible manner. The syringe
pump includes a frame, a motor attached to the frame, and a lead
screw drivably connected to the motor. A cover seal is mounted to
the front end of the lead screw, the cover seal having grooves formed
therein to facilitate mounting and demounting of the cover seal.
The pump further includes a cylindrical barrel within which the
cover seal reciprocates, the barrel being made of a ceramic material,
wherein the barrel is fixedly attached to the frame at the front
end and floatably mounted to the frame at the back end. A barrel
head is mounted to the front end of the barrel for closing off that
end of the barrel, the barrel head including an outlet port for
allowing fluid to enter and exit the barrel. In addition, the present
invention includes a multi-syringe gradient syringe pump, a liquid
chromatography system, a cover seal, and a mixer for mixing multiple
flow streams.
Syringe pump claims
We claim:
1. A high pressure micro-volume syringe pump for pumping a working
fluid comprising:
a frame;
a motor attached to the frame;
a lead screw drivably connected to the motor, said lead screw having
a front end and a lead screw translational axis;
a cover seal, the cover seal being mounted to the front end of
the lead screw; and
a cylindrical barrel within which the lead screw and cover seal
undergo reciprocal axial movement, the barrel having a front end,
a back end, and a barrel axis, the barrel axis being coaxially aligned
with the lead screw axis, the barrel being made of a ceramic material,
wherein the barrel is pivotally attached to the frame at the front
end and floatably mounted to the frame at the back end.
2. The high pressure syringe pump of claim 1 wherein the coverseal
has grooves formed in its outside surface to facilitate mounting
and demoting of the cover seal.
3. The high pressure syringe pump of claim 1 further including
a barrel head mounted at the front end of the barrel for closing
off that end of the barrel, the barrel head including an outlet
port for allowing the working fluid to enter and exit the barrel.
4. The high pressure syringe pump of claim 1 further including
a constraining means for preventing rotation of the lead screw while
allowing translation of the lead screw.
5. The high pressure syringe pump of claim 1 further including
a controller.
6. The high pressure syringe pump of claim 1 further including
a power transmission drivably interposed between the motor and the
lead screw.
7. The high pressure syringe pump of claim 6 wherein the power
transmission includes a nut made from Teflon-filled Delrin.
8. The high pressure syringe pump of claim 1 further including
a valve assembly in fluid connection with the outlet/inlet port.
9. The high pressure syringe pump of claim 1 wherein the motor
is a stepper motor.
10. The high pressure syringe pump of claim 9 wherein the stepper
motor is capable of micro-stepping operation.
11. The high pressure syringe pump of claim 1 wherein the lead
screw has an Acme thread profile.
12. The high pressure syringe pump of claim 1 wherein the cover
seal is made from a resilient material.
13. The high pressure syringe pump of claim 12 wherein the cover
seal is made from ultra high molecular weight polyethylene.
14. The high pressure syringe pump of claim 1 wherein the cover
seal comprises:
a cylindrical body having a cavity formed therein and formed from
high molecular weight polyethylene, the body having an outside surface,
the outside surface having grooves formed therein such that when
the outside surface of the body is not constrained, as the cover
seal is pushed onto a mounting member, the radial dimension of the
cavity can increase, thereby facilitating the placement of the cover
seal onto the mounting member and the removal of the cover seal
from the mounting member; and
an energizer mounted in the body to cause the outside surface to
be urged in a radially outward direction.
15. A mutli-syringe gradient syringe pump comprising:
a plurality of high-pressure micro-volume syringe pumps for pumping
multiple working fluids, each syringe pump comprising:
a frame;
a motor attached to the frame;
a lead screw drivably connected to the motor disposed in a barrel
for reciprocal axial movement therein, said lead screw having a
front end and a lead screw translational axis;
a cover seal, the cover seal being mounted to the front end of
the lead screw; and
a cylindrical barrel within which the cover seal undergoes reciprocal
movement, the barrel having a front end, a back end, and a barrel
axis, the barrel axis being coaxially aligned with the lead screw
axis, the barrel being made of a ceramic material, wherein the barrel
is pivotally attached to the time at the front end and floatably
mounted to the frame at the back end; and
a mixer for mixing the working fluids exiting each pump.
16. The mutli-syringe gradient syringe pump of claim 15 further
including a controller.
17. The mutli-syringe gradient syringe pump of claim 15 further
including a power transmission drivably interposed between the motor
and the lead screw.
18. The mutli-syringe gradient syringe pump of claim 15 further
including a valve assembly in fluid connection with the outlet/inlet
port of each of the high-pressure micro-volume syringe pumps.
19. The mutli-syringe gradient syringe pump of claim 15 wherein
the motor is a stepper motor, the stepper motor being capable of
micro-stepping operation.
20. The multi-syringe gradient syringe pump of claim 15 wherein
the mixer comprises:
an enclosed bowl having an inside bottom surface which is a bearing
surface, said bearing surface being made from a ceramic material,
and having an inlet port and an outlet port for providing fluid
communication between the bowl and the surroundings;
a puck adapted to undergo rotational motion inside the bowl, the
puck having helical groves formed on its outside surface and having
a puck magnet located in its interior for rotation therewith;
a motor; and
an external magnet connected to the motor such that the external
magnet undergoes rotational motion, the external magnet being in
magnetic communication with the puck magnet.
21. A liquid chromatography system comprising:
one or more high-pressure micro-volume syringe pumps, each syringe
pump comprising:
a frame;
a motor attached to the frame;
a lead screw drivably connected to the motor disposed in a barrel
for reciprocal axial movement therein, said lead screw having a
front end and a lead screw translational axis;
a cover seal, the cover seal being mounted to the front end of
the lead screw; and
a cylindrical barrel within which the cover seal undergoes reciprocal
movement, the barrel having a front end, a back end, and a barrel
axis, the barrel axis being coaxially aligned with the lead screw
axis, the barrel being made of a ceramic material, wherein the barrel
is pivotally attached to the frame at the front end and floatably
mounted to the frame at the back end;
a chromatography column in fluid communication with the outlet/inlet
of the syringe pumps;
an injector, disposed between and in fluid communication with the
syringe pump and the chromatography column, and
a detector in communication with the outlet/inlet of the chromatography
column such that material leaving the chromatography column is detectable
by the detector.
22. A high pressure micro-volume syringe pump for pumping a working
fluid comprising:
an elongate barrel mounted on a frame for pivoting about a front
end of the barrel, said barrel having a barrel axis and defining
a containment volume extending through the barrel;
a lead screw disposed in the barrel for reciprocal axial movement
therein, said screw having a front end and a lead screw translational
axis;
a cover seal mounted on the front end of the lead screw providing
a fluid tight seal with said containment volume; and
a means for moving the lead screw axially within the barrel, wherein
alignment between the barrel axis and the lead screw translational
axis is maintained by pivioting of said barrel about said front
end.
23. The high pressure syringe pump of claim 22 wherein the cover
seal is made from ultra high molecular weight polyethylene.
24. The high pressure syringe pump of claim 22 wherein the means
for moving the lead screw is a stepper motor.
25. The high pressure pump of claim 22 further including a constraining
means for preventing rotation of the lead screw while allowing translation
of the lead screw.
Syringe pump description
BACKGROUND
This invention relates to syringe pumps. More specifically, this
invention describes a high-pressure micro-volume syringe pump particularly
suited to for analytical separations.
An important trend in modem analytical chemistry has been the move
towards separation techniques capable of accommodating small sample
volumes, i.e., sample volumes in the range of 1 to 10 .mu.l. This
trend is particularly strong in the area of analytical biotechnology
where samples are frequently derived from scarce natural isolates
or from valuable recombinant products. Typical analytical biotechnology
applications include chromatographic separations used as part of
protein sequencing operations, amino acid analysis, protein/peptide
mapping, quality control of pharmaceutical products, and the like.
To avoid dilution of the sample and thereby maintain the delectability
of the separated components, the scale of the separation columns,
e.g., chromatographic columns, has been reduced to match the scale
of the samples, such micro-scale columns having internal diameters
as small as 50 .mu.m. An added benefit of scaling down the separation
equipment is the reduced volume of working fluid required, e.g.,
chromatographic solvents and/or eluants, leading to reduced costs
for acquiring and disposing of such materials, particularly in the
case of exotic and/or highly toxic materials.
Micro-scale separations place a particular burden on the pumps
used to deliver the working fluid to the separation column. The
performance characteristics of typical HPLC pumps is not adequate
to satisfy the exacting demands of such micro-column separations-where
an error of .+-.1 .mu.l might be undetectable in a HPLC application
running at a flow rate of 2 ml/min, that same error could lead to
unacceptably large errors in a micro-column application running
at a flow rate of less than 10 .mu.l/min.
Syringe pumps are well suited to the demands of micro-column chromatographic
separations. Syringe pumps have several advantages over reciprocating
pumps when used for micro-scale analytical separations, e.g., liquid
chromatography, super critical fluid chromatography, and the like,
including (i) essentially pulse-free fluid flow and (ii) highly
reproducible and accurate volumetric fluid delivery.
However, currently available syringe pumps have a number of important
shortcomings. In particular, existing syringe pumps are not able
to deliver low solvent flow rates at high pressure with the requisite
accuracy and precision desirable for analytical separations. Furthermore,
existing syringe pumps transmit a high level of mechanical vibrations
to the working fluid, thereby interfering with detection of the
separated sample components. Another drawback of existing syringe
pumps is that wear on moving sealing surfaces is such that parts
including such sealing surfaces frequently wear out, leading to
poor run-to-run reproducibility and necessitating frequent pump
disassembly and replacement of the worn parts.
When used in a multiple-pump gradient mode, because of the shortcomings
noted above, existing syringe pumps are unable to produce reproducible
gradients, particularly at very low solvent flow rates and at high
pressure. To achieve low flow rates in a multiple-pump gradient
mode, existing syringe pumps require the use of a solvent splitter
which serves to direct a portion of the outflow from the pump to
a waste stream rather to the separation column, e.g., Moritz et
at., Journal of Chromatography 599:119-130 (1992). Such splitting
techniques introduce large errors in the solvent delivery profile
due to changes in the solvent density and viscosity as the composition
of the solvent is changed throughout the gradient. In addition,
existing systems require mixers which have relatively large internal
volumes, introduce significant noise into the flow stream, and release
particulates into the flow stream as a result of wear of the moving
parts.
SUMMARY
An object of our invention is to provide a syringe pump capable
of delivering very low flow rates, i.e., less than 10 .mu.l/min,
at high pressures, i.e., greater than 700 psi, in a highly precise
and accurate manner.
A further object of our invention is to provide a syringe pump
having a mechanism which minimizes mechanical vibrations, thereby
minimizing the mechanical noise reaching any attached detector.
Another object of our invention is to provide a syringe pump having
a design which minimizes wear on any moving sealing surfaces, thereby
increasing the lifetime of components including such moving sealing
surfaces.
Yet another object of our invention is to provide a multiple-syringe
gradient syringe pump capable of providing a solvent composition
gradient which is highly reproducible, i.e., having a relative standard
deviation of less than 0.25% when operating at low flow rates, i.e.,
less than 10 .mu.l/min, and at high pressures, i.e., greater than
700 psi.
A further object of our invention is to provide a multiple-syringe
gradient syringe pump capable of operating at very low flow rates,
e.g., less than 10 .mu.l/min, without splitting the solvent stream.
Another object of our invention is to provide a mixer for mixing
multiple fluid streams which has a small internal volume, thoroughly
mixes the fluid streams, introduces a minimum amount of noise into
the flow stream, and does not release particulates into the flow
stream as a result of wear.
The foregoing and other objects of the present invention are achieved
by a high pressure micro-volume syringe pump which includes, in
one aspect, a frame for mounting the components of the pump, and
a motor attached to the frame. The pump further includes a lead
screw which is drivably connected to the motor, and a cover seal,
the cover seal being mounted to the lead screw, the cover seal having
slits formed therein to facilitate mounting and demoting of the
cover seal. The cover seal undergoes reciprocal movement inside
a cylindrical barrel, the barrel axis being coaxially aligned with
the lead screw axis. The barrel is made of a ceramic material and
is fixedly attached to the frame at one end and floatably mounted
to the frame at the other end. Finally, a barrel head is mounted
to one end of the barrel for closing off that end, the barrel head
including an outlet/inlet port for allowing a working fluid to enter
and exit the barrel.
In another aspect, the invention includes a mutli-syringe gradient
syringe pump including a plurality of high-pressure micro-volume
syringe pumps as described above and a mixer for mixing the fluids
exiting each of the pumps.
In yet another aspect, the invention includes a liquid chromatography
system including one or more high-pressure micro-volume syringe
pumps as described above, a chromatography column connected to the
outlet/inlet of the syringe pumps, an injector, located between
and in fluid communication with the syringe pump and the chromatography
column, and a detector in communication with the outlet/inlet of
the chromatography column such that material leaving the chromatography
column is detectable by the detector.
In another aspect, the invention includes a cover seal for use
in a high-pressure micro-volume syringe pump, the cover seal being
adapted to mount onto a cover seal mounting member. The cover seal
includes a cylindrical body in which a cavity is formed, the body
being made of high molecular weight polyethylene. The outside surface
of the body has grooves formed therein such that when the outside
surface of the body is not constrained, as the cover seal is pushed
onto the mounting member, the radial dimension of the cavity can
increase, thereby facilitating the placement of the cover seal onto
the mounting member and the removal of the cover seal from the mounting
member.
In another aspect, the invention includes a mixer for mixing multiple
fluid streams. The mixer includes an enclosed bowl having an inside
bottom surface which is a bearing surface, the bearing surface being
made from a ceramic material. The bowl further includes an inlet
port and an outlet port for providing fluid communication between
the bowl and the surroundings. A puck adapted to undergo rotational
motion is located inside the bowl. The puck has helical groves formed
on its outside surface and a puck magnet located in its interior.
The mixer also includes a motor and an external magnet connected
to the motor such that the external magnet undergoes rotational
motion. The external magnet is located such that it is in magnetic
communication with the puck magnet so that rotation of the external
magnet causes rotation of the puck.
These and other objects, features, and advantages of the present
invention will become better understood with reference to the following
description, drawings, and appended claims.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 shows a schematic representation of the high-pressure micro-volume
syringe pump of the present invention.
FIG. 2 shows a preferred drive assembly of the high-pressure micro-volume
syringe pump of the present invention.
FIGS. 3A and 3B show a preferred linear drive train of the high-pressure
micro-volume syringe pump of the present invention.
FIG. 3C shows an isometric view of the rear portion of a preferred
linear drive train of the high-pressure micro-volume syringe pump
of the present invention.
FIG. 4A shows a preferred cover seal of the high-pressure micro-volume
syringe pump of the present invention.
FIG. 4B shows the preferred cover seal of FIG. 4A mounted on a
cover seal mounting member.
FIG. 5A shows a preferred barrel assembly of the high-pressure
micro-volume syringe pump of the present invention.
FIG. 5B shows an expanded view of the floating end of a preferred
barrel assembly of the present invention.
FIG. 6 shows a flow diagram of a preferred valve assembly of the
high-pressure micro-volume syringe pump of the present invention.
FIG. 7 shows a preferred flow diagram of a mutli-syringe gradient
syringe pump system of the present invention.
FIGS. 8A-C shows an exploded view of a preferred mixer of the present
invention.
FIG. 9 shows a schematic diagram of a preferred chromatography
system of the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Reference will now be made in detail to the preferred embodiments
of the invention, examples of which are illustrated in the accompanying
drawings. While the invention will be described in conjunction with
the preferred embodiments, it will be understood that they are not
intended to limit the invention to those embodiments. On the contrary,
the invention is intended to cover alternatives, modifications,
and equivalents, which may be included within the invention as defined
by the appended claims.
Referring now to the drawings, where like numbers indicate like
elements, FIG. 1 shows a schematic representation of the syringe
pump of the present invention (100) comprising a drive assembly
(200) for providing rotational mechanical power to the pump, a linear
drive train (300) for converting the rotational mechanical power
into linear motion, a barrel assembly (500) for defining a high-pressure
containment volume, and a cover seal (400) for providing a movable
sealing surface for varying the internal volume of the barrel assembly.
The syringe pump also includes a valve assembly (600) for controlling
the flow of material leaving the pump during pumping and/or entering
the pump during filling, and a controller (655) for monitoring and
controlling various aspects of the pump.
1. Drive Assembly
FIG. 2 shows a detailed drawing of a preferred drive assembly of
the syringe pump of the present invention. Generally, the preferred
drive assembly (200) includes a means for moving a lead screw, preferably
a motor (205), drivably connected to a nut (245) by a power transmission
(211), the rotation of the nut transmitting energy to the linear
drive train.
The motor should be capable of being controlled by an electronic
controller and provide an output which can be delivered in small
increments of rotation, e.g., increments on the order of 0.03.degree.
/step. The small increments of rotation coupled with a small inner
diameter of the barrel assembly, allow for very precise delivery
of liquid at low flow rates. Preferably, the motor is a stepper
motor, i.e., a motor in which the extent of rotation is controllable
in discrete steps. More preferably, the motor is a stepper motor
capable of micro-stepping operation, i.e., stepping in increments
of 10000 or more steps per revolution. Additionally, the preferred
motor should be able to produce a static torque of at least 60 oz-in.
An exemplary motor is the Model 23H-530A stepper motor available
from American Precision Industries, Inc., Rapidsyn Division, Oceanside,
Calif.
Preferably, the power transmission (211) drivably connecting the
motor (205) and the nut (245) should (i) decrease the effective
step size of the motor's output rotation, where as used herein,
the "effective step size" is defined as the ratio of the
angular rotation of the nut to the angular rotation of the motor;
(ii) increase the torque produced by the motor and transmitted to
the nut; and (iii) provide mechanical dampening to reduce the amount
of vibration transmitted from the motor (205) to the nut (245).
A preferred power transmission includes a first timing pulley (215)
mounted to a motor drive shaft (210), a second timing pulley (225)
mounted to a jack shaft (230), and a timing belt (220) drivably
connecting the first timing pulley (215) and the second timing pulley
(225). Rotational motion is transmitted from the jack shaft (230)
to a drive gear (240) through a pinion gear (235) mounted on the
jack shaft (230). The drive gear (240) is mounted on the nut (245),
thereby transmitting its rotational motion to the nut.
The optimal amount of gear reduction between the motor (205) and
the nut (245) is based on a compromise between minimizing the effective
step size of the motor output and minimizing the time required to
fill the pump. Thus, as the amount of gear reduction is increased,
the effective step size of the motor is decreased, but the time
required to refill the pump is increased. In the pump of the present
invention, a preferred gear reduction is 5:1 such gear reduction
being accomplished by making the diameter of the drive gear five
times that of the pinion gear while making the diameters of the
first and second timing pulleys equal.
The rotational motion of the preferred drive assembly described
above is translated into linear motion of a lead screw (303 FIG.
3A) through the nut (245), the nut having a nut rotational axis
(246) and the lead screw having a lead screw translational axis
(304). Threads formed on the inside bore of the nut drivably engage
the lead screw (303) such that rotation of the nut (245) by the
drive gear (240) imparts a linear translation to the lead screw
(303) along a lead screw axis (304). Preferably, the nut (245) is
made from a material which is both (i) compliant and (ii) has a
low coefficient of friction. The compliance of the material serves
to dampen mechanical noise in the system while the low coefficient
of friction allows the nut to operate without any external lubrication.
By eliminating external lubrication, the pump is easier to maintain,
and more importantly, the opportunity for contamination of the working
fluids is greatly reduced. Preferred materials for forming the nut
include oil-filled bronze, Rulon.RTM., Delrin.RTM., and the like.
More preferably the nut is made from Teflon.RTM.-filled Delrin.RTM.,
e.g., Turcite-X.RTM., e.g., Product Bulletin, Turcite Internally
Lubricated Materials, W. S. Shamban & Co., Newbury Park, Calif.
(1989), reference herein incorporated by reference.
The nut is mounted onto a forward bearing (250) and a rear bearing
(255) such that the nut is free to rotate but is prevented from
undergoing translational motion. One or more preload springs (330)
serve to urge the nut against the rear bearing (255) thereby taking
up the mechanical tolerances of the system. In addition, the bearings
serve to maintain alignment of the nut with respect to the barrel
assembly (500) such that the lead screw (303) is held coaxially
with respect to the barrel assembly (500).
2. Linear Drive Train
FIGS. 3A-C show a detailed view of a preferred linear drive train
of the present invention including the lead screw (303), the lead
screw having a front end (301) and a back end (302), a cover seal
mounting member (305), a cover seal (400), and a lead screw follower
(320). Preferably, the thread form of the lead screw is chosen such
that unnecessary wear and stress on the nut is minimized. More preferably,
the lead screw thread profile is an Acme thread profile, e.g., Machinery's
Handbook, 24th Edition, pages 1604-1607 Industrial Press, Inc.,
N.Y. (1992), the reference herein incorporated by reference. Even
more preferably, the lead screw thread profile is an Acme thread
profile having a 3/16 inch nominal major diameter and a lead resulting
in 20 turns per inch, and is and made from stainless steel.
Preferably, the back end (302) of the lead screw includes a constraining
means for preventing rotation of the lead screw while allowing translation
of the lead screw. In the preferred embodiment shown in FIGS. 3A
and 3B, the back end of the lead screw is attached to a follower
(320) having a pair guide blocks (326) attached thereto. The follower
(320) and the guide blocks (326) are located within a follower guide
(327), the follower guide having a rectangular internal cross section.
In operation, as rotational force is applied to the lead screw (300),
the guide blocks (326) engage the follower guide (327), thereby
preventing the lead screw from rotating.
In one preferred embodiment, a position sensor flag (325) is located
at the end of the follower (320) at which the jam nuts (326) are
mounted. The position sensor flag serves to indicate to a lead screw
position sensor (331) when the lead screw (303) has reached the
end of its allowed extent of travel. The position sensor (331) can
be an optical sensor, an electrical sensor, or any other like sensor
capable of indicating the presence or absence of the lead screw
(300) at a defined location. More preferably, the sensor is an optical
sensor.
Mounted on the from end (301) of the lead screw (303) is a cover
seal mounting member (305). The cover seal mounting member serves
to mount the cover seal (400) to the lead screw (303) in a detachable
manner. Preferably, the cover seal mounting member includes a retaining
barb (306) and a guide bushing (307). The retaining barb (306) serves
to hold the cover seal (400) onto the mount in a removable manner,
while the guide bushing (307) serves to reduce the radial loads
on the cover seal and to assist in maintaining the proper alignment
between the linear drive train (300) and the barrel assembly (500).
The guide bushing (307) is mounted in a guide bushing mounting grove
(340) such that the guide bushing (307) is flush with the outside
surface of the cover seal mounting member. Preferably the guide
bushing (307) is made of an elastomeric material which (i) is wear
resistant, (ii) which will not scratch the inside surface of the
barrel, and (iii) is chemically inert to solvents typically used
in chromatography, e.g., polyetheretherketone PEEK, e.g., Material
Specification for Compound 1043 from American Variseal, Broomfield,
Colo., the reference herein incorporated by reference.
3. Cover seal
FIGS. 4A and 4B show an expanded view of a preferred cover seal
(400) of the present invention. The preferred cover seal includes
a body (405) with a cavity formed therein (415), the cavity designed
to fit over the cover seal mounting member (305). At the front of
the perimeter of the cover seal are a plurality of sealing ridges
(430) for providing superior sealing between the barrel assembly
(500) and the cover seal. Formed in the front of the cover seal
is a mounting groove (440) for containing an energizer (435) for
providing force in a radially outward direction for the purpose
of maintaining a seal between the cover seal (400) and the barrel
assembly (500). Preferably, the energizer is an O-ring formed of
an elastomeric material, a round-strip loading spring, a U/V circular
loading spring, a helical spring, or any other like means for providing
radial force. More preferably, the energizer is a helical spring.
The energizer (435) serves to force the sealing ridges (430) in
a radially outward direction to provide positive sealing between
the sealing ridges and the inside wall of the barrel assembly (500)
when the seal is not under pressure.
In an important aspect of the cover seal of the present invention
(400), the outside surface (420) of the body (405) of the cover
seal has grooves (425) formed therein, the grooves running in an
axial direction. The grooves (425) serve to facilitate the expansion
of the internal diameter of the cavity (415) as the cover seal is
mounted to or removed from the cover seal mounting member (305).
However, when the cover seal is located inside the barrel assembly
(500), the cover seal is firmly held onto the cover seal mounting
member (305) because the walls of the barrel assembly prevent expansion
of the cavity. This preferred design facilitates manual replacement
of worn cover seals.
Preferably, the cover seal is made from a resilient material which
withstands wear due to friction, has a minimum of stick-slip when
in contact with ceramic surfaces, and does not cold flow. Preferred
materials include Teflon.RTM., Kel-F.RTM., Tercel.RTM., and the
like. More preferably, the preferred cover seal is made from ultra
high molecular weight polyethylene, e.g., Compound 1103 available
from the America Veriseal Company, Broomfield, Colo., Material Specification
for Compound 1103 herein incorporated by reference.
4. Barrel Assembly
A preferred barrel assembly (500) is shown in FIGS. 5A and 5B.
A barrel (510) is contained in a barrel housing (505) with one end
capped by a cylinder head (520) and the other end open to receive
the linear drive train (300), the barrel having a floating end (511)
and a fixed end (512). A cylinder head (525) is mounted to a barrel
housing (505), preferably using a retaining nut (515) which is threaded
onto the exterior of the barrel housing (505). The cylinder head
(525) has an inlet/outlet port (530) formed therein to facilitate
the fluid connection of the pump to associated tubing preferably,
a high pressure seal is formed between the cylinder head (525) and
the barrel housing (505) by a head seal (520).
In an important feature of the barrel assembly (500), one end of
the barrel is "floating", i.e., the floating end (511),
while the opposite end (512) is pivotally mounted to the frame.
By allowing the floating end to float, the barrel (510) can adjust
to compensate for any nonuniformity in the rotation of the lead
screw (300), nut (245), or front bearings (250). Ideally, the nut
rotational axis (246) and the lead screw translational axis (304)
are coaxial. However, because of imperfections in the fabrication
of the nut (245) and the lead screw (300), these axis are not perfectly
coaxial. Therefore, the rotation of the nut (245) can cause a side
loading on the lead screw (300) which in turn can cause a side load
on the cover seal (400). This side load on the cover seal can lead
to excessive wear of the cover seal (400) and/or leaking of fluid
past the cover seal into the mechanism of the pump, leading to corrosion
of the pump reduced precision of the pump.
FIG. 5B shows the floating end of the barrel (511) and how it is
floatably mounted to the barrel housing (505). By allowing an appropriate
clearance (513) between the barrel (510) and the barrel housing
(505), side loads transmitted from the nut to the lead screw (300)
will result in a radial movement of the barrel with respect to the
barrel housing rather than an increased side load on the cover seal
(400).
Another important feature of the preferred barrel assembly (500)
is that the barrel (510) is made of a ceramic material, where, as
used herein, the term "ceramic" refers to materials which
are compounds of metallic and nonmetallic elements, e.g., Al.sub.2
O.sub.3 Cu--Zn, Cu--Sn, Al--Cu, Al--Mg, Fe--O, and the like, e.g.,
Van Vlack, Elements of Materials Science and Engineering Fourth
Edition, Chapter 9 (Addison-Wesley, Menlo Park, 1980) said reference
incorporated herein by reference. Ceramic materials are preferred
because of (i) their smooth surface, which reduces the wear on the
cover seal and improves the sealing between the cover seal and the
barrel; (ii) their extreme chemical stability; and (iii) their resistance
to scratching. Preferably the ceramic material is 99.8% Al.sub.2
O.sub.3. More preferably, the ceramic materials used in the present
invention are made by a process which uses no flow enhancing agents
to facilitate processing, e.g., elastomeric additives or emulsifiers.
By not using such additives, the resulting ceramic product has smaller
grains, resulting a material which is harder and smoother. More
preferably, the ceramic materials used in the present inventions
are formed by the isostatic pressing process, e.g., Richerson, Modem
Ceramic Engineering, pages 438-489 Marcel Dekker, N.Y. (1992),
the reference hereby incorporated by reference.
Preferably, the inside diameter of the barrel (510) and all associated
elements of the barrel assembly and the linear drive train are chosen
to accommodate micro-volume pumping applications. Preferably, the
inside diameter of the barrel is less than 0.25 inches. By having
a small diameter barrel, any errors in the linear translation of
the linear drive train (300) will result in only small errors in
the volume of fluid pumped.
5. Single Pump Valve Assembly
In a preferred embodiment of the syringe pump of the present invention,
the syringe pump includes a valve assembly (600) for directing flow
into or out of the syringe pump. A detailed flow diagram of a preferred
valve assembly is shown in FIG. 6 the valve assembly being capable
of directing flow out of the syringe pump to waste or to an application,
e.g., a liquid chromatography column, supercritical chromatography
column, or the like, or directing flow from a solvent reservoir
into the syringe pump for filling the pump.
The preferred valve assembly shown in FIG. 6 includes first (610)
and second (630) 3-way valves, a pressure transducer (605), a flow
manifold (650), and a controller (701). Preferably, the first 3-way
valve (610) includes a common port (615), a first selectable port
(620), and a second selectable port (625), where the common port
(615) is alternatively connected to the first selectable port (620)
or the second selectable port (625). In the preferred arrangement
shown in FIG. 6 the common port (615) is connected to the output
of the pump, the first selectable port (620) is connected to the
second valve (630), and the second selectable port (625) is connected
to the manifold (650). An exemplary preferred valve is the Rheodyne
Model 7030S valve (Rheodyne, Inc., Cotatti, Calif.).
Similarly, the second 3-way valve (630) includes a common port
(635), a first selectable port (640), and a second selectable port
(645), where the common port (635) is alternatively connected to
the first selectable port (640) or the second selectable port (645).
In the preferred arrangement shown in FIG. 6 the common port (635)
is connected to the first selectable port of the first valve (620),
the first selectable port (640) is connected to the application,
and the second selectable port (645) is connected to the manifold
(650).
Preferably, at least one of the valve ports is connected to the
flow manifold (650) having a waste position (655) and a solvent
position (660).
A pressure transducer (605) is included in the preferred valve
assembly (600) to warn of an overpressure and/or underpressure condition
in the flow path caused by clogging and/or valve malfunction.
In a more preferred embodiment the controller (701) is used to
control inputs and outputs for monitoring and directing the operation
of the pump and associated systems. Typical inputs would include
inputs from (i) a user interface, (ii) the pressure transducer,
(iii) an external start signal, (iv) valve position sensors, and
(v) the head screw position sensor. Typical outputs from the controller
would include (i) outputs to the motor for controlling the motor
speed, (ii) outputs to a user interface, (iii) outputs to valve-position
serves, and (iv) outputs to a RS232-type serial interface. A typical
controller would be any suitable PC-based controller, e.g., the
Turbochrome System from Perkin-Elmer Corporation, Norwalk, Conn.
To fill the barrel (510) using the preferred valve assembly (600)
shown in FIG. 6 the first valve (610) is positioned such that the
common port (615) is connected to the second selectable port (625),
thereby eliminating the second valve (630) from the flow path and
connecting the barrel (500) to the solvent port (660) of the manifold
(650). Thus, when a negative pressure is generated in the syringe
pump by retracting the cover seal, solvent will flow from the solvent
port (660) of the manifold (650) into the barrel (510) of the pump.
To pump the contents of the syringe pump (100) to waste, the first
valve (610) is positioned such that the common port (615) is connected
to the first selectable port (620), thereby connecting the first
valve (610) to the second valve (630), and the second valve (630)
is positioned such that the common port (635) is connected to the
second selectable port (645). Alternatively, to pump the fluid contents
of the barrel (510) to an application, the first valve (610) is
positioned such that the common port (615) is connected to the first
selectable port (620), thereby connecting the first valve (610)
to the second valve (630), and the second valve (630) is positioned
such that the common port (635) is connected to the first selectable
port (640).
6. Multiple Pump Valve Assembly
In an alternative embodiment, the valve assembly of the present
invention is arranged such that multiple syringe pumps can be used
in combination to create solvent composition gradients. FIG. 7 shows
such a multiple pump valve assembly having two syringe pumps. Obviously
it would be possible to use three or more pumps to provide solvent
gradients based on the same principles.
Generally, the preferred multiple pump valve assembly (700) shown
in FIG. 7 includes first (720) and second (755) double 3-way valves,
a pressure transducer (715), a flow manifold (790), a controller
(701), a mixing tee (794) and a solvent mixer (800).
Preferably, the first double 3-way valve (720) includes a first
group of three ports consisting of a first selectable port (725),
a second selectable port (735), and a first common port (730), where
the first common port (730) is alternatively connected to the first
selectable port (725) or the second selectable port (735), and a
second group of three ports consisting of a third selectable port
(740), a fourth selectable port (750), and a second common port
(745), where the second common port (745) is alternatively connected
to the third selectable port (740) or the fourth selectable port
(750). In the preferred arrangement shown in FIG. 7 the ports of
the first group of ports of the first double 3-way valve (720) are
connected as follows: the first common port (730) is connected to
the output of the first syringe pump (705), the first selectable
port (725) is connected to the second double 3-way valve (755),
and the second selectable port (735) is connected to the manifold
(650) at a solvent "A" position. Similarly, the ports
of the second group of ports of the first double 3-way valve (720)
are connected as follows: the second common port (745) is connected
to the output of the second syringe pump (710), the third selectable
port (740) is connected to the second double 3-way valve (755),
and the fourth selectable port (750) is connected to the manifold
(650) at a solvent "B" position.
In a manner analogous to the first double 3-way valve (720), the
second double 3-way valve (755) includes a first group of three
ports consisting of a first selectable port (760), a second selectable
port (770), and a first common port (765), where the first common
port (765) is alternatively connected to the first selectable port
(760) or the second selectable port (770), and a second group of
three ports consisting of a third selectable port (775), a fourth
selectable port (785), and a second common port (780), where the
second common port (780) is alternatively connected to the third
selectable port (775) or the fourth selectable port (785). In the
preferred arrangement shown in FIG. 7 the ports of the first group
of ports of the second double 3-way valve (755) are connected as
follows: the first common port (765) is connected to the first double
3-way valve (720), the first selectable port (760) is connected
to the mixer (800) through the mixing tee (794), and the second
selectable port (770) is connected to the manifold (790) at a waste
position (791). Similarly, the ports of the second group of ports
of the second double 3-way valve (755) are connected as follows:
the second common port (780) is connected to the first double 3-way
valve (720), the third selectable port (775) is connected to the
mixer (800) through the mixing tee (794), and the fourth selectable
port (785) is connected to the manifold (790) at the waste position.
Any suitable mixer may be used in the present invention. Preferably
the mixer (i) has a small internal volume, i.e., less than two times
the fluid volume being pumped through the system in a minute, (ii)
thoroughly mixes multiple flow streams, (iii) introduces a minimum
mount of noise, i.e., high frequency pressure fluctuations, into
the flow stream, and (iv) does not introduce particulate debris
into the flow stream as a result of disintegration of moving components.
An important aspect of the present invention is the discovery of
a mixer which is particularly well suited to micro-scale, high pressure
applications where multiple fluid streams must be thoroughly mixed,
e.g., gradient liquid chromatography.
With reference to FIGS. 8A-C, generally, the preferred mixer of
the present invention includes a body (850) having a bowl (865)
formed therein, a puck (820) including a puck magnet (840), and
driver magnet (895) which is mounted external to the bowel but in
magnetic communication with the puck magnet (840) and which is rotatably
driven by a motor (898). Therefore, the rotating driver magnet (895)
serves to cause rotation of the puck (820), thereby causing agitation
of the fluid located in the bowel (865).
The body (850) has a fluid inlet port (860) for providing fluid
communication between the bowl (865) of the mixer (800) and other
elements of the pumping system. The bottom surface of the bowel
is a bearing surface (870) on which the puck (820) rotates. Preferably,
this bearing surface (870) is formed from a hard material, i.e.,
hard with respect to the puck material, which is resistant to deterioration
under the wear of the spinning puck (820), thereby minimizing the
opportunity for particulate debris to be introduced into the fluid
stream. More preferably, the bearing surface is made from a ceramic
material. The top surface of the bowl is formed by a mixer cap (805)
which is sealably attached to the body (850) of the mixer, where
the mixer cap has a fluid outlet port (810) formed therein to provide
fluid communication between the bowl (865) an other elements of
the system.
The size and composition of the puck magnet (840) should be such
that the magnetic force between the puck magnet (840) and the driver
magnet (895) is sufficient to overcome the frictional drag between
the puck and the bowl and the frictional drag between the puck and
the agitated fluid stream while providing a rotational velocity
of the puck (820) sufficient to fully agitate the fluid stream.
The puck magnet may be formed from any material having a magnetic
dipole, e.g., iron and the like, however, because of the size limitations
on the magnet imposed by the size of the puck (820), a strongly
magnetic material is preferred; a particularly preferred magnetic
material being a samarium-cobalt alloy.
In a preferred arrangement the puck magnet (840) is made part of
a puck magnet assembly (830), said assembly including a canister
(835), the puck magnet (840), and a canister cap (845). When fully
assembled, the puck magnet (840) is sealed inside the canister (835)
by welding the canister cap (845) in place. Preferably, the welding
is laser welding which produces a small heat affected zone. The
canister material should be particularly resistant to corrosion,
e.g., type 316 L stainless steel, to minimize contamination of the
fluid stream. By enclosing the puck magnet (840) inside the corrosion
resistant canister (835), the fluid stream is protected from contamination
from the puck magnet.
Preferably, the outside surface of the puck (822) has a helical
grove (821) formed therein. As the puck spins, the helical grove
serves to cause circulation of the fluid resulting in extreme agitation
of the fluid. To enhance agitation and to reduce the dead volume
of the mixer, the diameter of the puck (820) should be such that
only a small distance separates the outside surface of the puck
(822) and the inside surface of the bowl (865); preferably this
distance is less than 1 mm. In a preferred embodiment, the puck
includes a magnet mounting hole (825) for firmly holding the puck
magnet (840) or magnet assembly (830) such that the rotational force
applied to the puck magnet (840) by the rotating driver magnet (845)
is efficiently transmitted to the puck itself.
Preferably, the driver magnet (895) is mounted to the motor (898)
by a magnet holder (896), said holder being securely attached to
a motor drive shaft (899).
In the preferred embodiment shown in FIGS. 8A-C, the mixer is assembled
as follows: the mixer cap (805), the body (850) and a motor mounting
plate (875) are held together by a plurality of bolts (890) or other
like fastening means, and the motor (898) is securely fastened to
the motor mounting plate (875), wherein the motor drive shaft (899),
the driver magnet (895), the bowl (865) all lie substantially on
a mixer rotational axis (801).
Clearly, other suitable mixers may be used with the general pumping
system of the present invention. Possible alternative mixers include
static mixers, e.g., INSTAC/LIF Technical Handbook, pages 66-69
The Lee Company, Los Angeles, Calif. (1987)
In a preferred arrangement, a mixing tee (794) is placed upstream
of the mixer (800) to "premix" the converging flow streams.
In operation, to form a solvent gradient with the preferred dual
pump valve assembly (700) shown in FIG. 7 flow from both the first
syringe pump (705) and the second syringe pump (710) are mixed,
where each pump is filled with a different solvent composition.
The gradient is achieved by varying the flow rates of each pump
such that the combined volumetric flow form the pumps is held substantially
constant, while the composition is changed by varying the flow rates
of each pump. To achieve flow from both pumps simultaneously, the
solvent from the first syringe pump (705) passes through open valve
ports (730), (725), (765), and (760), while the solvent from the
second syringe pump (710) passes through open valve ports (745),
(740), (780), and (775), then on to the mixer (800) where the flows
originating from both of the syringe pumps are mixed then transmitted
to the application.
7. Liquid Chromatography System:
In a particularly preferred application, the syringe pump of the
present invention may be used in a liquid chromatography system
(900), more preferably in a micro-volume chromatography system.
The preferred chromatography system shown in FIG. 9 includes a
pumping system (905) where the pumping system comprises one or more
syringe pumps as described herein, a sample injector (910) for injecting
sample onto a chromatography column (915), a detector (920) and
a data output device (925). A complete discussion of how liquid
chromatography systems are assembled is given elsewhere, e.g., Krstulovic
et al., Reversed-Phase High-performance Liquid Chromatography, Chapter
3 John Wiley & Sons, New York (1982); and Model 172 Series
HPLC Separation System Installation Manual, Part Number 0054-0012
Applied Biosystems Division of the Perkin-Elmer Corporation, Foster
City, Calif. (May 1992).
Although only a few embodiments have been described in detail above,
those having ordinary skill in the arts of chromatography or pump
design will clearly understand that many modifications are possible
in the preferred embodiment without departing from the teachings
thereof. All such modifications are intended to be encompassed within
the following claims. |