Background
[0001] The present invention relates to the field fluid handling devices and more particularly
to an improved fluid mixing device. Still more particularly the fluid mixing device
may be adapted for use in mixing liquids used in automated clinical chemistry analyzers.
[0002] A common requirement in fluid handling systems is the mixing of two fluid flows to
form a third fluid flow. For example, automated clinical chemistry analyzers frequently
require two fluid flows to be mixed together to form a third fluid flow that is then
analyzed. A first fluid may be, for example, a patient sample such as serum, plasma,
urine or spinal fluid (CSF). The second fluid may be a buffer which, when combined
with the first fluid, controls primarily the pH, ionic strength and surfactant properties
of the resulting mixture.
[0003] One such system requiring the combination of two fluid flows is the SYNCHRON CX®3
automated clinical chemistry analyzer which is commercially available from Beckman
Instruments, Inc. (Brea, California 92621). In this system, a probe carrying the patient
sample is aligned above a sample injection cell. The probe is lowered into the cell
with the tip of the probe coming to rest within a mixing chamber. The sample is pumped
from the probe into the mixing chamber while a buffer solution is pumped through a
separate conduit into the mixing chamber. The resulting mixture flows from the mixing
chamber through an exit conduit to an electrolyte measuring flow cell to measure sodium,
potassium, chloride and CO₂. An essentially identical system is disclosed in U.S.
Patent Number 4,888,998, issued December 26, 1989, which is incorporated herein by
reference.
[0004] A cutaway side view of the mixing chamber in such commercially available system is
illustrated in Figure 5. As seen with reference to Figure 5, a mixing chamber 100
includes a vertical conduit 108 which is adapted to receive a probe 102 having a tip
104. A conduit 106 is "T"-ed into the side of and is perpendicular to the conduit
108. The conduit 106 is connected to a source of buffer which is to mix with sample
ejected through the probe tip 104. An exit conduit 110 forms a right angle with the
conduit 108 to draw the combined sample and buffer from the mixing chamber 100.
[0005] Unfortunately, the "T" configuration of the prior art system may impede mixing of
the sample and buffer for several reasons. As the sample flow from the tip 104 meets
the buffer flow from the conduit 106, the flows may simply combine without mixing,
resulting in laminar, separate flows within the conduits 108 and 110. The degree of
laminar, separate flow is influenced by the vertical position of the tip 104 within
the conduit 108, thus making the system sensitive to routine changes in probe tip
position that occur, for example, due to normal wear and tear and routine replacement
of the probe 102. Further, an air bubble may be trapped directly below the tip 104
within the flow of sample from the tip 104. Such an air bubble vibrates rapidly within
the conduit 108, resulting in pulses or bursts of sample within the flow of buffer.
Also, air trapped above the conduit 106, while not causing pulses or bursts in the
combined flow, does gradually break up, flowing to the flow cell where such disbursed
air can collect, adversely affecting measurements.
[0006] One result of these limitations and drawbacks may be inconsistent electrolyte measurements
and adversely affected average precision. Thus, there is a need for improved fluid
mixing to improve and stabilize the performance of the measurement system.
[0007] The improved fluid mixing device of the present invention overcomes the limitations
noted in the prior device. The improved fluid mixing device may be formed directly
in the sample injection cell and, more particularly, may replace the mixing chamber
found in the prior art sample injection cell. In accordance with the present invention,
the improved fluid mixing device includes a mixing chamber having a cylindrical side
wall, end walls and a major axis parallel to and coaxial with the cylindrical side
wall. A first fluid conduit joins the mixing chamber at a first fluid port formed
in one of the end walls. A second fluid conduit joins the mixing chamber at a second
fluid port, the second port being formed in the cylindrical side wall. The second
fluid conduit and second fluid port are offset with respect to the major axis to direct
a fluid flow from the second conduit through the second port generally along the side
wall and around the major axis of the mixing chamber, creating a swirling action within
the mixing chamber. A third fluid conduit joins the mixing chamber at a third port
in the other end and serves as an exit conduit for the fluids mixed in the mixing
chamber.
[0008] In the embodiment of the invention disclosed herein, the mixing chamber may form
a first stage of a mixing device or configuration. A second stage includes positioning
the third port off-center in the second end and generally aligning the third fluid
conduit with the major axis. Yet a third stage of the mixing device or configuration
disclosed herein may include a fourth conduit intersecting the third conduit. Center
lines of the third and fourth conduits are offset and do not intersect.
[0009] In overall effect, the improved fluid mixing device of the present invention thoroughly
and completely mixes the two streams of inlet fluids. When used in the sample injection
cell of the automated clinical chemistry system described above, the improved mixing
results in more consistent performance and better average precision in the measurement
of electrolytes.
Description of the Drawings
[0010] Figure 1 is an overall exterior view of a sample injection cell including an improved
mixing device or configuration in accordance with the present invention as well as
a sample probe.
[0011] Figure 2 is an enlarged partial cross-section view of the improved fluid mixing configuration
of the injection cell of Figure 1.
[0012] Figure 3 is a partial cross-section view taken along line 3 - 3 of Figure 2 with
the probe removed for clarity.
[0013] Figure 4 is a partial cross-section view taken along line 4 - 4 of Figure 2.
[0014] Figure 5 is a partial cross-section view of a mixing chamber of a prior-art sample
injection cell.
Detailed Description
[0015] With reference to Figure 1, a sample injection cell 10 may include an improved fluid
mixing device or configuration 12 in accordance with the present invention. The sample
injection cell 10 is generally a vertical cylinder and may be formed from cast acrylic.
The cell 10 includes an upper portion 14 and a lower portion 16. The upper portion
14 includes an open end 18 and tapered surfaces 20 leading to a vertical central cylindrical
bore 22. A horizontal conduit 24 leads to and is in communication with the bore 22.
The lower portion 16 includes the mixing configuration 12 more particularly described
with reference to Figures 2 - 4 below. The upper and lower portions 14 and 16 are
joined by, for example, screws 26 (only one of which is shown in Figure 1).
[0016] A sample probe assembly 28 includes a fluid carrying conduit 30 which may be attached
via a hose 32 to pumps, for example, for aspirating sample from sample containers
(not shown) and discharging the aspirated sample into the cell 10. The probe assembly
28 includes an arm 33 connected to a probe assembly positioning device, all of which
is well-known in the art. The probe assembly 28 and cell 10, but for the mixing configuration
12 of the present invention, may be as used in the prior art commercially available
SYNCHRON CX®3 Clinical System described above and is otherwise well-known in the art.
[0017] Turning now to the improved fluid mixing device or configuration 12 as seen in Figure
2, the configuration 12 includes a mixing chamber 34 having a cylindrical side wall
36 and upper and lower ends 38, 40, respectively. The cylindrical wall 36 of the mixing
chamber 34 includes a major central coaxial axis 37. The axis 37 is inclined slightly
with respect to vertical and, in the embodiment disclosed herein, is inclined approximately
8.5 degrees. The end 40 is perpendicular to the axis 37 and the upper end 38 is angled
slightly from the axis 37 to be generally horizontal (as seen in Figure 2). Particularly,
the upper end 38 is angled about 81.5 degrees from the axis, bringing the end 38 to
its generally horizontal position as just described.
[0018] A slightly enlarged bore 42 immediately above the end 38 receives and supports a
rigid washer 44. A second slightly enlarged bore 46 immediately above the bore 42
receives and holds a quad ring 48. The quad ring 48 is retained within the bore 46
by clamping pressure applied via the upper portion 14. The quad rind 48 provides a
seal between the upper portion 14 and lower portion 16 and, as is described below,
provides a seal between the removable probe conduit 30 and the mixing configuration
12.
[0019] The probe conduit 30 may be considered a first fluid conduit when the probe is positioned
as shown in Figure 2 with the probe seated against the quad ring 48. The probe conduit
30 or first fluid conduit enters the mixing chamber 34 through the upper end 38 and
is angled, in the embodiment disclosed herein, approximately 8.5 degrees with respect
to the major axis 37.
[0020] A second fluid conduit 50 (Figures 2 and 3) is in communication with the mixing chamber
34. The second fluid conduit 50 narrows to include a reduced portion 56 proximate
the mixing chamber 34 and enters the mixing chamber 34 via a port 58. The conduit
50 including the reduced portion 56 is offset with respect to the axis 37 and enters
the mixing chamber 34 off-center as illustrated in Figure 3 such that fluid flow through
the port 58 is directly substantially around the axis 37 and along the cylindrical
wall 36.
[0021] A third fluid conduit 52 exits mixing chamber 34 through the lower end 40 via a port
60. A center line of the conduit 52 is generally parallel to the axis 37 of the mixing
chamber 34.
[0022] A fourth fluid conduit 62 is in communication with the lower end of the fluid conduit
52. The center line of the conduit 62, as seen in Figure 4, is offset with respect
to the center line of the conduit 52 and is slightly displaced such that the center
line of the conduit 62 falls substantially at the periphery or is tangential with
respect to the wall of the conduit 52. The conduits 52 and 62 are joined at an intersection
identified generally at 64.
[0023] A drain conduit 66 (Figures 2 and 3) is also in communication with the mixing chamber
34 at a port 68. The drain conduit 66 is offset with respect to the axis 37 and is
generally horizontal as seen in Figure 2. The port 68 is located near the upper end
38 to help reduce the amount of air that may otherwise become trapped at the top of
the mixing chamber 34.
[0024] In operation (Figures 1 - 4), the probe assembly 28 is inserted into the cell 10
with probe tip 70 coming to rest within the mixing chamber 34. A tapered surface 72
formed on the outside of the conduit 30 and proximate the tip 70 is urged against
the quad ring 48, sealing the tip 70 within the mixing chamber 34. Fluid sample, which
may be in the form of liquid patient serum, is held within the probe conduit 30. The
conduit 50 is connected to a source of fluid, such as liquid buffer as described above.
[0025] With the probe tip 70 positioned within the mixing chamber 34, pumping means (not
shown) are operated to eject the serum sample from the probe conduit 30 into the mixing
chamber. Simultaneously, pumping means pumps diluent or buffer via the fluid conduit
50 through the port 58 into the mixing chamber 34. Advantageously, the stream formed
by the buffer entering the mixing chamber 34 creates a rapid fluid vortexing action
about the axis 37 within the chamber 34. Interference by the probe conduit 30 in the
flow from the conduit 50 and port 58 prevent a coherent vortex or cyclone from forming
within the mixing chamber 34, introducing turbulence into the vortex to help prevent
the sample from becoming trapped within the center of the vortex. Gas bubbles which
generally collect between the port 58 and the rigid washer 44 are immediately sweep
away by this rapid vortexing fluid action within the mixing chamber 34.
[0026] As seen in Figure 2, the probe conduit 30, which may also be considered as a first
fluid conduit, is generally vertical and is thus angled slightly (in the embodiment
disclosed, about 8.5 degrees) with respect to the axis 37. The angle difference directs
the fluid flow from the conduit 30 toward the lower bottom corner of the mixing chamber
34 and into the rapidly circulating or spinning wall or side of the fluid vortex created
within the mixing chamber 34. The fluid flow from the conduit 30 is not injected into
the center of the vortex created within the mixing chamber 34 where it might otherwise
become entrapped, decreasing the mixing action. The result is a thorough and rapid
mixing of the two fluids within the mixing chamber 34.
[0027] The fluids continue their vortexing action, and are forced through the port 60 into
the fluid conduit 52. At the interface formed by the port 60 between the mixing chamber
34 and the conduit 52, further turbulence is created. The port 60 in effect slices
off the advancing rapidly vortexing fluid within the mixing chamber 34. This slicing,
rotation-inducing action creates further mixing and in turn creates a vortexing or
rotational fluid action or movement within the conduit 52. At the intersection 64,
the rotating column of fluid moving through the fluid conduit 52 is again subject
to not only a change in direction but a further change in rotation, the advancing
fluid creating yet another rotational or vortexing action within the conduit 62.
[0028] Stated somewhat differently, the mixing configuration 12 may be considered as including
three distinct mixing stages. The first stage comprises the mixing chamber 34 in which
the rapid vortexing and injection action between first and second fluid flows is created.
The second stage includes the port 60 which "slices" this rapidly rotating fluid mass
as the mass advances from the mixing chamber 34 into the fluid conduit 52. The intersection
64 and the conduit 62 form yet a third mixing stage, with the change in direction
of the fluid mass as well as the creation of yet another vortexing or rotational effect
within the conduit 62 yet further enhancing the mixing action of the configuration
12.
[0029] Once sample injection and mixing is completed as just described the probe 30 may
be raised slightly, wash fluid introduced via the conduit 24 with the drain conduit
66 operating to aspirate or drain the wash fluid from the sample cell 10.
[0030] The present invention provides significant improvements over the prior-art system
described in the Background. The placement of the port 58 near the upper end 38 and
flow of fluid from port 58 parallel to the upper end 38 substantially reduces the
volume of air that could be trapped with the mixing chamber 34. The rapid vortexing
action created within the chamber 34 rapidly and completely sweeps any trapped air
from the chamber 34. This action passes entrapped air through the electrolyte measuring
flow cell before measurements are made and eliminates air that might otherwise become
trapped in the flow from the conduit 30, leading to bursts or pulses of sample entrained
within the buffer flow. Further, the rapid vortexing action within the chamber 34,
as well as the mixing occurring at the port 60 and intersection 64 eliminates laminar
flow otherwise present in the prior-art system. The mixing distance of the prior-art
system in Figure 5, that is, the linear length of the fluid travel within the conduits
108, 110 through which mixing may occur before the fluid leaves the cell is effectively
many times multiplied by the vortexing, sectioning and rotational actions created
by the mixing configuration 12.
[0031] Thus, the mixing device or configuration 12 of the present invention overcomes the
limitations of the prior art, providing rapid, sure, effective mixing without substantial
increased costs or external parts.
[0032] It is to be recognized that modifications to the present invention are possible to
accommodate varying liquid viscosities and flow rates. For example, the flow rate
of fluid from the port 58 may be effected by the diameter of the reduced portion 56
and the speed at which fluid rotates within the mixing chamber can be altered by the
amount by which the port 58 is offset from the axis 37. Further, the conduit 30 and
end 70 may be replaced by a conduit entering the mixing chamber 34 through a port
formed in the end 38. In such an instance, such a port and conduit should direct the
fluid flow into the fluid wall or side of the spinning fluid vortex to accomplish
rapid, thorough mixing. Such modifications and others may be developed through routine
experimentation where high "shutter" speed video recording may be used to assist in
the evaluation of such modifications.
[0033] It will be further recognized by those skilled in the art that the present invention
is not to be limited to the particular embodiment disclosed herein but is to be afforded
the full scope of the claims appended hereto.
1. An improved fluid mixing device comprising:
a mixing chamber having end walls, a generally cylindrical side wall, and an axis
coaxial with the cylindrical side wall;
a first fluid conduit joining the mixing chamber at a first fluid port, the first
fluid port being in one of the end walls;
a second fluid conduit joining the mixing chamber at a second fluid port formed
in the cylindrical side wall, the second fluid conduit offset with respect to the
mixing chamber to direct a fluid flow from the second conduit through the second port
along the wall of the mixing chamber and around mixing chamber axis to thereby create
a swirling action as fluid is injected into the mixing chamber from the second conduit;
and
a third fluid conduit joining the mixing chamber at a third port in the second
end.
2. A device as in Claim 1 wherein the third conduit is generally parallel to the mixing
chamber axis.
3. A device as in Claim 1 wherein the third port is offset with respect to the axis in
the second end.
4. A device as in Claim 1 including a fourth conduit intersecting the third conduit,
the center lines of the third and fourth conduit being offset.
5. A device as in Claim 1 wherein the first conduit includes an extending portion that
extends into the mixing chamber and the first port is as the end of the extending
portion.
6. A device as in Claim 5 wherein the first conduit is angled with respect to the mixing
chamber axis to direct fluid from the first conduit toward the side wall.
7. A device as in Claim 1 wherein the first conduit is angled with respect to the mixing
chamber axis to direct fluid from the first conduit toward the side wall.
8. A mixing device, comprising:
a mixing chamber having end walls, a generally cylindrical side wall, and an axis
coaxial with the cylindrical side wall;
means for receiving a first fluid conduit in one end, the first fluid conduit having
a first fluid port;
a second fluid conduit joining the mixing chamber at a second fluid port formed
in the cylindrical side wall, the second fluid conduit offset with respect to the
mixing chamber to direct a fluid flow from the second conduit through the second port
along the wall of the mixing chamber and around mixing chamber axis to thereby create
a swirling action as fluid is injected into the mixing chamber from the second conduit;
and
a third fluid conduit joining the mixing chamber at a third port in the other end.
9. A device as in Claim 8 wherein the third conduit is generally parallel to the mixing
chamber axis.
10. A device as in Claim 8 wherein the third port is offset with respect to the axis in
the second end.
11. A device as in Claim 8 including a fourth conduit intersecting the third conduit,
the center lines of the third and fourth conduit being offset.
12. A device as in Claim 8 wherein the first conduit is angled with respect to the mixing
chamber axis to direct fluid from the first conduit toward the side wall.
13. A sample injection cell adapted to receive a probe having a tip, the cell comprising:
an open end adapted to receive the probe tip;
a mixing chamber having end walls, a generally cylindrical side wall, and an axis
coaxial with the cylindrical side wall;
means for receiving the probe tip in one end of the mixing chamber, the probe tip
including a first fluid port;
a second fluid conduit joining the mixing chamber at a second fluid port formed
in the cylindrical side wall, the second fluid conduit offset with respect to the
mixing chamber to direct a fluid flow from the second conduit through the second port
along the wall of the mixing chamber and around mixing chamber axis to thereby create
a swirling action as fluid is injected into the mixing chamber from the second conduit;
and
a third fluid conduit joining the mixing chamber at a third port in the other end.
14. A device as in Claim 13 wherein the third conduit is generally parallel to the mixing
chamber axis.
15. A device as in Claim 13 wherein the third port is offset with respect to the axis
in the second end.
16. A device as in Claim 13 including a fourth conduit intersecting the third conduit,
the center lines of the third and fourth conduit being offset.
17. A device as in Claim 13 wherein the first conduit is angled with respect to the mixing
chamber axis to direct fluid from the first conduit toward the side wall.