BACKGROUND OF THE INVENTION
[0001] The present invention relates to an apparatus for transferring a small amount of
fluid and, more particularly, to an apparatus for transferring small amount of fluid
which includes at least one pump series which is composed of a plurality of vibration-type
pumps which exhibit small pulsation of the pumped fluid and which afford easy control
of flow rate of the pumped fluid. The apparatus of the present invention is suitable
for use in apparatus or systems which handle small amounts of specimens which are
generally expensive or difficult to obtain in large quantities, such as biological
active substances, e.g., proteins, enzymes and cells. For instance, the fluid transfer
apparatus of the present invention is suitable for use in bio-technological apparatus,
medical apparatus and medical analyzers, space flight mission devices for life science
such as free flow electrophoresis. The term "transfer of small amount of fluid" in
this specification is used to mean the transfer of a fluid at a very small rate of,
for example, 1 to 500 µℓ/min.
DESCRIPTION OF THE PRIOR ART
[0002] Various vibration type pumps have been proposed for the purpose of transferring small
amounts of fluids, such as electromagnetic pump adapted for vibrating a diaphragm,
and a pump in which, as disclosed in Japanese Patent Unexamined Publication No. 56-9679
or Japanese Patent Unexamined Publication No. 59-63578, a cylindrical vibration element
is directly vibrated to displace a fluid.
[0003] US-A-4 519 751 discloses a piezoelectric pump which includes a hollow cylindrical
piezoelectric crystal with end bells on either end defining a pump chamber. A resilent
diaphragm with an offset orifice provides efferent valving action and by means of
a switch a voltage source is periodically connected to said hollow cyclindrical piezoelectric
crystal.
[0004] All these known vibration type pumps rely upon a vibratory motion of a wall or a
member for cyclically expanding or contracting a closed space to cause a cyclic change
in volume thereby displacing or transferring a fluid. The vibration type pumps generally
exhibit high reliability of operation and are capable of handling a corrosive or highly
viscous fluids because they do not have any rotary or sliding part such as impeller
or piston.
[0005] On the other hand, the vibration type pumps commonly suffer from a disadvantage that
they essentially require check valves at the suction and delivery sides thereof for
the purpose of preventing reversing of the pumped fluid, insofar as they make use
of cyclic change in the internal volume. These check valves operate in response to
the movement of the fluid so that a time delay is inevitably involved in the operation
of the check valves. This undesirably draws a limit in the shortening of the period
of the cyclic change in the volume, and causes a pulsation of the pressure of the
pumped fluid. In particular, in the field which requires transfer of a small amount
of fluid, the fluid-flow characteristic of the system to be supplied with the fluid
tends to be adversely affected by the generation of pulsation. To avoid pulsation
of the pressure of the pumped fluid, it is necessary to use a suitable pulsation prevention
device such as an accumulator. Thus, the known vibration type pumps inconveniently
suffer from problems in the view point of performance, construction and reliability.
Moreover, in a pump system in which such vibration pumps are arranged in parallel
with each other, the respective vibration pumps have different fluid transferring
characteristics because the fluid transferring characteristic of each pump depends
upon the dimensional accuracy and vibration characteristic of the pump. In the pump
system of this class, therefore, it is very difficult to obtain uniformly controlled
fluid transfer rates from all of the parallel pumps.
SUMMARY OF THE INVENTION
[0006] Accordingly, an object of the present invention is to provide an apparatus for transferring
a small amount of fluid, which is improved to suppress generation of pulsation of
the pressure of the fluid which is being transferred.
[0007] Another object of the present invention is to provide an apparatus for transferring
a small amount of fluid, which is improved to enable a fluid to be stably transferred
at a small rate.
[0008] These objects are achieved according to the invention by the features of claim 1.
[0009] The above and other objects, features and advantages of the present invention will
become clear from the following description of the preferred embodiments when the
same is read in conjunction with the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0010]
Fig. 1 is a schematic sectional view of an embodiment of the apparatus of the present
invention for transferring a small amount of fluid;
Fig. 2 is a circuit diagram of a control circuit for controlling the operation of
the apparatus shown in Fig. 1;
Fig. 3 is a graph showing operation characteristics of a vibrator in response to different
vibration frequencies;
Fig. 4 is a graph showing patterns of pressure distribution in fluid transfer pipes
as observed when the apparatus for transferring a small amount of fluid constituted
by three transfer pipes is energized for vibration with three kinds of phase differential;
Fig. 5 is a schematic perspective view of another embodiment of the apparatus of the
invention for transferring a small amount of fluid;
Fig. 6 is a circuit diagram of a control circuit for controlling the operation of
the apparatus shown in Fig. 5; and
Fig. 7 is a sectional view of another example of a pressure differential sensor used
in the apparatus shown in Fig. 1 and also in the apparatus shown in Fig. 5.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0011] An embodiment of the apparatus in accordance with the present invention for transferring
a small amount of fluid will be described hereinunder with reference to Fig. 1 which
is a sectional view of the apparatus and also to Fig. 2 which is a circuit diagram
of a control circuit for controlling the operation of the apparatus shown in Fig.
1. Referring to Fig. 1, the apparatus has a fluid transfer passage having a plurality
of cylindrical fluid transfer pipes 1a to 1d connected in series. These fluid transfer
pipes 1a to 1d are respectively embraced by cylindrical vibrators 2a to 2d which fit
on the outer peripheral surfaces of the respective pipes. These cylindrical vibrators
are typically constituted by piezoelectric elements or electrostrictive elements.
The vibrators 2a to 2d are surrounded by outer peripheral electrodes 3a to 3d in such
a manner that the outer peripheral surface of each vibrator is not covered by the
outer electrode at a portion adjacent to one axial end of each vibrator. In addition,
inner electrodes 4a to 4d are provided such that these inner electrodes 4a to 4d lay
on the outer peripheral surfaces of the vibrators 2a to 2d at the above-mentioned
axial end portions which are not covered by the outer electrodes 3a to 3d and such
that these inner electrodes covers the entire inner peripheral surfaces of the vibrators
2a to 2d. These electrodes are intended for causing respirating action, i.e., radial
expansion and contraction, of the associated fluid transfer pipes by the vibration
of the respective vibrators. The outer electrodes 3a to 3d and the inner electrodes
4a to 4d are insulated from each other. External high-frequency power supplies 6a
to 6d are connected between the outer electrodes 3a to 3d and the corresponding inner
electrodes 4a to 4d, respectively. Thus, the fluid transfer pipes 1a to 1d, the vibrators
2a to 2d, the outer electrodes 3a to 3d, the inner electrodes 4a to 4d and the power
supplies 6a to 6d constitute respective vibration pump units. The fluid transfer pipes
1a to 1d are provided at their outlet ends with orifice means constituted by fluid
diodes 5a to 5d which produce large flow resistance against reversing flow of the
fluid. In the illustrated embodiment, although not exclusively, each of the fluid
diodes 5a to 5d is of a flow-nozzle type which has an entrance end defined by a smooth
curvature and an exit end which opens at an acute angle to pose a large resistance
to reversing flow of the fluid.
[0012] In operation, a high-frequency voltage is applied across the outer electrodes 3a
to 3d and the inner electrodes 4a to 4d on the respective vibrators 2a to 2d of the
respective pump units. As a result, the vibrators 2a to 2d start to vibrate in the
radial direction so as to cause respirating actions of the respective fluid transfer
pipes 1a to 1d, i.e., radial expansion and contraction, as indicated by the double-headed
arrows 7a to 7d in Fig. 1. As a result of the respirating actions, induction flow
components 8a to 8d and 9b to 9d are generated in the respective fluid transfer pipes
1a to 1d along the inner peripheral surfaces of these pipes. The induction flow components
8a to 8d causes displacement of the fluid towards the fluid diodes 5a to 5d on the
outlet ends of the respective fluid transfer pipes 1a to 1d because the entrance ends
of the fluid diodes 5a to 5d are smoothly shaped to produce only a small flow resistance.
On the other hand, the induction flow components 9b to 9d, which are directed towards
the inlet ends of the respective fluid transfer pipes 1a to 1d encounter large flow
resistance produced by the exit ends the fluid diodes on the outlet ends of the fluid
transfer pipes immediately upstream thereof, because the exit ends of these fluid
diodes form restricted openings having an acute angle as illustrated. In consequence,
the induction flow components 9b to 9d are reflected and reversed so as to be directed
towards the fluid diodes of the respective fluid transfer pipes 1a to 1d. In consequence,
the fluid in each of the fluid transfer pipes 1a to 1d is displaced towards the fluid
diode, as indicated by arrows 10a to 10d.
[0013] Suitable phase differentials are introduced between the high-frequency signals applied
from the high-frequency power supplies 6a to 6d to the respective vibrators 2a to
2d. For instance, the high-frequency signals are applied by the respective power supplies
6a to 6d at phase differentials which are expressed as follows.
where A₀ to A₃ represent amplitudes of vibration, ω represents angular or circular
vibration frequency, t represents time and α ₁ to α ₃ represents the phases. Thus,
the fluid transfer pipe 1d which is on the upstream end of the pump unit series is
vibrated, i.e., cylindrically expands and contracts as indicated by the arrow 7a,
as represented by A₀ sin (ωt). Similarly, the downstream fluid transfer pipes 1b to
1d make respirating actions 7b to 7d as represented by A₁ sin (ωt + α ₁), A₂ sin (ωt
+ α ₂) and A₃ sin (ωt + α ₃), respectively. It is possible to accelerate the flow
of the fluid induced in the series of fluid transfer pipes 1a to 1d and, in addition,
to obtain a high discharge pressure at the downstream end of the pump unit series,
while diminishing undesirable pulsation of the fluid pressure, by establishing optimal
phase relations between the respirating actions 7a to 7d of the successive pump units,
through a suitable selection of the phase differentials α ₁ to α ₃. To this end, the
described embodiment employs a control circuit 11 which is capable of controlling
the output levels, frequencies and phases of the high-frequency signals from the high-frequency
power supplies 6a to 6d, upon detection of and in accordance with the pressure differential
across at least one, e.g., 5d, of the plurality of fluid diodes 5a to 5d. The detection
of the pressure differential is conducted by means of a pressure differential sensor
14 capable of sensing a very small pressure differential upon receipt of pressures
derived from pressure measuring ports 12 and 13 communicating with the fluid passage
on the upstream and downstream sides of the fluid diode 5d. The output from the pressure
differential sensor 14 is input to an amplifier 15 so as to be amplified to form a
pressure differential signal 16 which is input to the control circuit 11.
[0014] Fig. 2 shows the practical circuit arrangement of the control circuit 11 shown in
Fig. 1. This control circuit 11 is designed to cause vibration of the four fluid transfer
pipes 1a to 1d at different phases as described. More specifically, the control circuit
11 is capable of digitally producing a plurality of, four in the illustrated case,
high-frequency signals in response to the pressure differential signal 16 derived
from the amplifier 15, and causing a plurality of, four in the illustrated case, vibrators
to vibrate in accordance with these high-frequency signals. As shown in Fig. 2, the
control circuit 11 includes a pulse generator 17 (clock) for generating clock pulses,
a reference counter 18a, a subordinate counter 18b to 18d, memories 19a to 19d, D/A
converters 20a to 20d, amplifiers 21a to 21d, digital switches 22a to 22c and an operation
unit 23 for controlling these constituent elements. In the described embodiment, the
vibration is caused by applying to the respective pump units sine-wave vibration signals
having phase differentials. More specifically, the application of the sine-wave vibration
signals is effected in a manner which will be explained hereinunder. Each of the memories
19a to 19d has n₀ bits of address which store digital data corresponding to one period
of the sine-wave signal. Digital pulses 24 generated by the pulse generator 17 are
counted by the reference counter 18a and subordinate counters 18b to 18d. The reference
counter 18a is an n₀-notation counter which is capable of counting up to the value
n₀ designated by the operation unit 23 and, after counting the value n₀, clearing
the content to commence counting again from the initial value 1. The reference counter
18a, upon counting the value n₀, generates a synchronizing pulse 25 in accordance
with which the subordinate counters 18b to 18d commence counting of the pulses from
values n₁ to n₃ which are set by digital switches 22a to 22c in accordance with the
instructions given by the operation unit 23.
[0015] The values n₀ to n₃ are determined to meet the condition represented by the following
formula (1).
[0016] Similarly to the reference counter 18a, the subordinate counters 18b to 18d are n₀-notation
counters which are adapted to count up to n₀ and then to be reset to start counting
again from the initial value 1. In consequence, a plurality of number serieses {a
i}, {b
i}, {c
i} and {d
i}, are formed. The number series {b
i} to {d
i} are digital period number serieses which have phase differentials n₁ to n₃, respectively,
with respect to the number series {a
i} formed by the reference counter 18a. The count output from the reference counter
18a is considered in relation to time. The components a
j, b
j, c
j and d
j of the respective number series at a moment t
j corresponds to the addresses in the respective memories 19a to 19d so that the memories
19a to 19d output and deliver digital waveform data which are beforehand stored in
these memories and which correspond to the designated addresses. These digital waveform
data are converted into analog signals 26a to 26d by the respective D/A converters
20a to 22d and are then amplified by means of the respective amplifiers 21a to 21d.
Then, the high-frequency power supplies 6a to 6d are controlled in accordance with
the amplified analog waveform data so as to energize the vibrators 2a to 2d. As will
be seen from Fig. 3, the analog signals 26a to 26d are signals which have continuous
sine waveforms and which are set at phases α ₁ to α ₃. As described before, the phase
differentials α ₁ to α ₃ are controllable through suitably setting by means of the
operation unit 23, the counting initial values n₁ to n₃ from which the counting operations
are to be commenced by the respective subordinate counters 18b to 18d which are triggered
by the synchronizing pulse signal 25 produced by the reference counter 18a. It is
to be noted, however, that the following relationships exist between the phases α
₁ to α ₃ and the counting initial values n₀ to n₃:

[0017] It will thus be seen that the phases α ₁ to α ₃, i.e., the phase differences, can
freely be varied by setting the values n₁ to n₃ by means of digital switches 22a to
22c.
[0018] In the described embodiment, the control circuit 11 is so designed that it operates
the operation unit 23 to control the frequency of the pulses generated by the pulse
generator 17, counting initial values n₁ to n₃ to be counted by the digital switches
22a to 22c, and the amplification factors of the amplifiers 21a to 21d in such a manner
that the DC component B₁ and the AC component B₀ are maximized and minimized, respectively,
in the following formula (3) which represents the waveform F of the pressure differential
signal 16 representing the pressure differential across at least one 5d of the plurality
of fluid diodes 5a to 5d:
[0019] Fig. 3 shows the relationships between the analog signals 26a to 26d produced by
the control circuit 11 shown in Fig. 2 and the waveform of the pressure differential
signal indicative of the pressure differential across the fluid diode 5d sensed by
the pressure differential sensor 14. It will be seen that a pressure differential
signal 16 having a small vibration amplitude or a pressure differential 16' having
a large vibration amplitude are obtainable according to the values of the phase differentials.
[0020] The pressure differential signal 16 shown in Fig. 3 is obtained when the phase differentials
α ₁ to α ₃ are selected to meet the condition of the following formula (4):
[0021] On the other hand, the pressure differential signal 16′ shown in Fig. 3 is obtained
when the phase differentials α ₁ to α ₃ are selected to meet the condition of the
following formula (5):
[0022] From Fig. 3, it will be understood that a fluid transfer apparatus which suffers
from a small pulsation is obtained when the phase differentials α ₁ to α ₃ are selected
to meet the condition given by the formula (4).
[0023] The fluid transferring effect is enhanced and, therefore, the rate of transfer of
the fluid is increased when the phase differentials are selected to meet the condition
given by the following formula (6):
where N represents the number of the fluid transfer pipes. This fact will be described
in more detail with specific reference to Fig. 4.
[0024] Fig. 4 illustrates the patterns of pressure distribution in the fluid transfer pipes
in an apparatus embodying the invention and constituted by three pump units connected
in series, in each of three cases: namely, curves (a), (b); (c), (d) and (e), (f)
which are obtained with different values of the phase differentials. The broken-line
curves in Fig. 4 show the patterns of the pressure distribution as observed in the
piping connected to the downstream end of the fluid transfer apparatus. More specifically,
curves (a) and (b), curves (c) and (d) and curves (e) and (f) in Fig. 4 represent
the patterns of distribution of the fluid pressure in the direction of flow of the
fluid as obtained at a moment t = 0 and a moment t = π/3ω , respectively, when the
phase differential α is selected to be π, π/3 and 2π/3, respectively. As will be seen
from the curves (a) and (b), when the phase difference α is selected to be π, the
fluid pressure in the apparatus exhibits such a distribution pattern that the nodes
are fixed at the points of connection between the successive pump units. Namely, the
fluid which is flowing through the apparatus exhibits a pressure pulsation of a frequency
corresponding to the vibration frequency. In this case, therefore, the pulsation of
the fluid pressure is not at all suppressed. In the second case where the phase differential
α is selected to be π/3, the nodes of the pressure waveform proceed in the direction
of flow indicated by X as will be seen from the curves (c) and (d). In this case,
however, the pressure waveform vary in a random manner, so that this value of phase
differential is not preferred from the view point of prevention of pressure differential.
Referring now to the third case where the phase differential α is selected to be 2π/3,
the pressure waveform gently varies in the direction X of flow of the fluid as will
be seen from the curves (e) and (f). Thus, the pressure wave in this case is a progressive
wave having peaks progressively moved in the direction of flow. It will also be seen
that the pulsation is appreciably suppressed in this case. From these facts, it is
understood that the phase differential α is selected to be 2π/3 when the apparatus
is constituted by three pump units connected in series.
[0025] It will also be apparent to those skilled in the art that, when the apparatus includes
more than three vibration pump units, the favorable effect as shown by the curves
(e) and (f) in Fig. 4 is obtainable provided that the phase differential α is selected
to meet the condition give by the formula (6).
[0026] It will thus be seen that the rate of transfer of the fluid can easily be controlled
by varying the frequency and the amplitude of the pulses.
[0027] Figs. 5 and 6 show another embodiment of the apparatus in accordance with the present
invention for transferring a small amount of fluid. This embodiment employs a plurality
of serieses or rows 29 to 29n of pump units disposed in parallel, each series having
a plurality of pump units of the type described above and connected in series. The
major constituents of each series of pump units are materially the same as those in
the pump unit series as shown in Fig. 5. In general, this type of apparatus encounters
a difficulty in equalizing the flow rates of the transfer of fluid by all pump unit
series. In this embodiment, the apparatus is controlled by a control circuit shown
in Fig. 6 in such a manner that the flow rates of the fluid in all the pump unit serieses
are equalized.
[0028] More specifically, the control circuit shown in Fig. 6 has a plurality of control
circuits 11 to 11n each of which is similar to that described before in connection
with Fig. 2. These control circuits 11 to 11n are connected to the pulse generator
17 which is the same as that explained before with reference to Fig. 2 and are capable
controlling the plurality of serieses 29 to 29n of the pump units. The control circuit
shown in Fig. 6 also has pressure differential sensors 14 to 14n which are capable
of sensing the pressure differentials across the fluid diodes or orifice means 30
to 30n on the downstream ends of the respective serieses 29 to 29n of the pump units.
The outputs from the respective pressure differential sensors 14 to 14n are input
to and amplified by amplifiers 15 to 15n. The control circuit shown in Fig. 6 further
has a mean processing unit 27 which computes the means value of the pressure differential
signals derived from the respective serieses of pump units, and pressure differential
deviation computing circuits 28 to 28n which compute and output deviations of the
pressure differential signals from the respective amplifiers 15 to 15n from the mean
of the pressure differentials computed by the mean processing unit 27. The thus determined
pressure differential deviations are input to the operation unit 23. The operation
unit 23 operates to control the respective serieses of the pump units independently
of one another in accordance with the pressure differential deviation signals input
thereto. It is thus possible to construct an apparatus having a plurality of pump
unit serieses which are connected in parallel and each of which includes a plurality
of pump units connected in series as shown in Fig. 1, while enabling the flow rates
of the fluid in all the parallel pump unit serieses to be equalized without difficulty.
[0029] Fig. 7 shows a modification of the pressure differential sensor 14 which is used
in each of the embodiments of Figs. 1 and 5 for the purpose of sensing the pressure
differential across the fluid diode. In the embodiments shown in Figs. 1 and 5, the
pressure differential sensor is designed to detect the pressure differential across
at least one of the fluid diodes 5a to 5d annexed to the series of pump units. However,
when the flow rate of the transferred fluid is small, only a small pressure differential
is developed across the flow-nozzle type fluid diode, so that it is difficult to obtain
high precision of detection of the pressure differential. In addition, the pressure
measuring ports 12 and 13, through which the pressure differential sensor 14 is communicated
with the upstream and downstream sides of the fluid diode 5d (see Fig. 1), produce
damping effect to damp the vibration of the fluid pressure caused by the high-frequency
vibrations of pump units, with the result that the frequency characteristics of the
pressure differential waveform to be detected by the sensor 14 is impaired.
[0030] This problem, however, can be overcome by the modification shown in Fig. 7. Namely,
in the modification shown in Fig. 7, a housing 34 having an internal space greater
than that of the fluid transfer pipe 1d is connected to the fluid transfer pipe 1d
at the outlet end thereof. An orifice plate 31 made of, for example, a piezoelectric
element is provided in the housing. Electrodes 32 and 33, which are insulated from
each other, are adhered to both sides of the orifice plate 31. These electrodes 32
and 33 are connected to an amplifier 15. Since the orifice plate 31 has an outer diameter
greater than that of the fluid transfer pipe 1d, it can easily detect the waveform
of vibration of the fluid 10 in the fluid transfer pipe 1d. In operation, a pressure
differential of the fluid is formed across the orifice plate 10 and, at the same time,
the orifice plate 31 defects in response to the pressure variation of the fluid 10d
on the upstream side of the orifice plate 31. By constructing the orifice plate 31
from a vibrator element such as a piezoelectric element, therefore, it is possible
to obtain a voltage of a level corresponding to the vibration amplitude. This voltage
is picked up by the electrodes 32 and 33 and is input to the amplifier 15. It is thus
possible to detect both the pressure differential across the orifice plate 31 and
the cyclical variation of the pressure differential directly and with a high degree
of accuracy. Therefore, the accuracy of control of the flow rate or flow rates performed
by the embodiments shown in Figs. 1 and 5 can be further improved when these embodiments
are modified to employ the arrangement shown in Fig. 7.
1. An apparatus for transferring a small amount of fluid, including:
a plurality of vibration pump units, each consisting of a fluid transfer pipe (1a
- 1d), having inlet and outlet ends,
a vibrator (2a - 2d), surrounding said fluid transfer pipe (1a - 1d) to cause the
same to make respiring vibration, an inner peripheral electrode (4a - 4d) disposed
between said fluid transfer pipe (1a - 1d) and said vibrator (2a - 2d), an outer peripheral
electrode (3a - 3d) disposed on an outer periphery of said vibrator (2a - 2d), said
electrodes (3a - 3d, 4a - 4d) being connected to a high-frequency power supply (6a
- 6d), and
an orifice means (5a - 5d), which allows a fluid to flow in a predetermined direction
in said transfer pipe (1a - 1d) and which exhibits a resistance to a reversing flow
of the fluid;
characterized by
at least one row of a plurality of vibration pump units connected in series;
orifice means (5a - 5d) disposed between each adjacent pair of vibration pump units
for allowing a fluid to flow easily from one of the pair of pump units into the other;
additional orifice means (30 - 30n) connected to the fluid outlet end of the most
downstream pump unit;
a pressure differential sensor (14), provided for detecting a pressure differential
across at least one of all of said orifice means (5a - 5d); and
a control circuit (11) for controlling the high frequency power supply (6a - 6d) of
said vibrators (2a - 2d) in accordance with a pressure differential signal (16) derived
from said pressure differential sensor (14), such that the respective vibration pump
units are operated with a predetermined phase difference maintained between adjacent
pairs of said vibration pump units, to minimize the pulsation of the fluid outlet
end of the most downstream vibration pump unit.
2. An apparatus according to claim 1,
characterized in that
said orifice means (5a - 5d) is of a flow nozzle type.
3. An apparatus according to claim 1,
wherein said pressure differential sensor comprises an orifice plate (31) of a piezoelectric
material,
having an outer diameter greater than that of a fluid transfer pipe (1d), and electrodes
(32, 33) adhered on both sides thereof.
4. An apparatus according to claim 1,
wherein a plurality of vibration pump units connected in series (29 to 29n) are disposed
in parallel,
each of the plurality of vibration pump units connected in series (29 to 29n) having
a control circuit (11 to 11n) of its own and pressure differential sensors (14 to
14n) respectively;
a mean processing unit (27) computes the mean value of the pressure differential signals
derived from the respective serieses (29 to 29n) of the vibration pump units,
pressure differential deviation computing circuits (28 to 28n) compute and output
deviations of the pressure differential signals from the mean value of the pressure
differentials, computed by the mean processing unit (27), and the thus determined
pressure differential deviations are inputted to an operation unit (23) which controls
the respective serieses (29 to 29n) of the vibrating pump units independently of one
another.
1. Vorrichtung zum Fördern von einer kleinen Fluidmenge, die umfaßt:
mehrere Vibrationspumpeneinheiten, die aus einem Fluidtransferrohr (1a - 1d) mit einem
Einlaß- und einem Auslaßende bestehen,
einen Vibrator (2a - 2d), der das Fluidtransferrohr (1a - 1d) umgibt, so daß dasselbe
eine Respirationsvibration durchführt, wobei eine innere Umfangselektrode (4a - 4d)
zwischen dem Fluidtransferrohr (1a - 1d) und dem Vibrator (2a - 2d) angeordnet ist,
eine äußere Umfangselektrode (3a - 3d) an einem äußeren Umfang des Vibrators (2a -
2d) angeordnet ist und die Elektroden (3a - 3d, 4a - 4d) mit einer Hochfrequenzstromversorgung
(6a - 6d) verbunden sind,
und
ein Durchgangsstück (5a - 5d), das einen Fluidstrom in eine vorbestimmte Richtung
in dem Transferrohr (1a - 1d) erlaubt und das einen Widerstand gegen einen Umkehrstrom
des Fluids ausübt,
gekennzeichnet durch
mindestens eine Reihe mehrerer Vibrationspumpeneinheiten, die in Serie miteinander
verbunden sind,
Durchgangsstücke (5a - 5d), die zwischen jedem benachbarten Paar von Vibrationspumpeneinheiten
angeordnet sind, so daß ein Fluid leicht von einem Paar Pumpeneinheiten in das andere
strömen kann,
zusätzliche Durchgangsstücke (30 - 30n), die mit dem Fluidauslaßende der weitest stromab
liegenden Pumpeneinheit verbunden sind,
ein Differenzdrucksensor (14), der zum Erfassen des Differenzdruckes über mindestens
eines der Durchgangsstücke (5a - 5d) vorgesehen ist, und
eine Steuerschaltung (11) zum Steuern der Hochfrequenzstromversorgung (6a - 6d) der
Vibratoren (2a - 2d) in Übereinstimmung mit einem Differenzdrucksignal (16) von dem
Differenzdrucksensor (14), so daß die entsprechenden Vibrationspumpeneinheiten mit
einer vorbestimmten Phasendifferenz zwischen benachbarten Paaren der Vibrationspumpeneinheiten
betrieben werden, zur Minimierung der Pulsation des Fluidauslaßendes der weitest stromab
liegenden Vibrationspumpeneinheit.
2. Vorrichtung nach Anspruch 1,
dadurch gekennzeichnet, daß
die Durchgangsstücke (5a - 5d) Strömungsmeßdüsen sind.
3. Vorrichtung nach Anspruch 1,
in der der Differenzdrucksensor eine Blende (31) aus einem piezoelektrischen Material,
mit einem äußeren Durchmesser, der größer ist als der eines Fluidtransferrohrs (1d),
und Elektroden (32, 33), die an beide Seiten der Blende (31) geklebt sind, enthält.
4. Vorrichtung nach Anspruch 1, in der mehrere in Serie (29 - 29n) miteinander verbundene
Vibrationspumpeneinheiten parallel angeordnet sind,
jede der Vielzahl der in Serie (29 - 29n) miteinander verbundenen Vibrationspumpeneinheiten
eine eigene Steuerschaltung (11 - 11n) und Differenzdrucksensoren (14 - 14n) aufweisen,
eine Mittelwertverarbeitungseinheit (27) den Mittelwert der Differenzdrucksignale
von den Serien (29 - 29n) der Vibrationspumpeneinheiten ermittelt,
Differenzdruckabweichungsermittlungsschaltungen (28 - 28n) Abweichungen der Differenzdrucksignale
von dem von der Mittelwertverarbeitungseinheit (27) ermittelten Mittelwert der Differenzdrücke
ermittelt und ausgibt und wobei die dadurch bestimmten Differenzdruckabweichungen
in eine Verarbeitungseinheit (23) eingegeben werden, die die Serien (29 - 29n) der
Vibrationspumpeneinheiten unabhängig voneinander steuert.
1. Dispositif pour transférer une faible quantité de fluide, comprenant :
une pluralité d'unités de pompes vibrantes,
constituées chacune par une canalisation (1a-1d) de transfert du fluide, comportant
des extrémités d'entrée et de sortie,
un vibrateur (2a-2d), qui entoure ladite canalisation (1a-1d) de transfert du fluide
de manière à soumettre ce dernier à une vibration respiratoire, une électrode périphérique
intérieure (4a-4d) disposée entre ladite canalisation (1a-1d) de transfert du fluide
et ledit vibrateur (2a-2d), une électrode périphérique extérieure (3a-3d) disposée
sur un pourtour extérieur dudit vibrateur (2a-2d), lesdites électrodes (3a-3d, 4a-4d)
étant raccordées à une alimentation en énergie à haute fréquence (6a-6d), et
des moyens en forme d'orifices (5a-5d), qui permettent l'écoulement d'un fluide dans
une direction prédéterminée dans ladite canalisation de transfert (1a-1d) et présentent
une résistance à un écoulement inverse du fluide,
caractérisé par
au moins une rangée d'une pluralité d'unités de pompes vibrantes branchées en série;
des moyens en forme d'orifices (5a-5d) disposés entre chaque couple d'unités adjacentes
de pompes vibrantes pour permettre un écoulement aisé du fluide depuis une unité du
couple d'unités de pompes dans l'autre;
des moyens additionnels en forme d'orifices (30-30n) raccordés à l'extrémité de sortie
du fluide de l'unité de pompe la plus en aval;
un capteur de pression différentielle (14) prévu pour détecter une différence de pression
au niveau d'au moins l'un de l'ensemble desdits moyens en forme d'orifices (5a-5d);
et
un circuit de commande (11) servant à commander l'alimentation en énergie à haute
fréquence (6a-6d) desdits vibrateurs (2a-2d) en fonction d'un signal de différence
de pression (16) délivré par ledit capteur de pression différentielle (14), de sorte
que les unités respectives de pompes vibrantes fonctionnent avec une différence de
phase prédéterminée maintenue entre des couples adjacents desdites unités de pompes
vibrantes afin de réduire la pulsation de l'extrémité de sortie du fluide de l'unité
de pompe vibrante la plus en aval.
2. Dispositif selon la revendication 1, caractérisé en ce que lesdits moyens en forme
d'orifices (5a-5d) sont du type à buses d'écoulement.
3. Dispositif selon la revendication 1, dans lequel ledit capteur de pression différentielle
comprend une plaque à orifice (31) réalisée en un matériau piézoélectrique et possédant
un diamètre extérieur supérieur à celui d'une canalisation (1d) de transfert du fluide,
et des électrodes (32 , 33) fixées sur les deux faces de cette plaque.
4. Dispositif selon la revendication 1, dans lequel une pluralité d'unités de pompes
vibrantes raccordées en série (29 à 29n) sont branchées en parallèle,
chaque unité de la pluralité d'unités de pompes vibrantes connectées en série (29
à 29n) comportant un circuit de commande (11 à 11n) qui lui est propre et respectivement
des capteurs de pression différentielle (14 à 14n);
une unité de calcul de valeur moyenne (27) calcule la valeur moyenne des signaux de
pression différentielle délivrés par les ensembles respectifs en série (29 à 29n)
des unités de pompes vibrantes,
des circuits (28 à 28n) de calcul de l'écart de pression différentielle calculent
et délivrent des écarts des signaux de pression différentielle par rapport à la valeur
moyenne des différences de pression, calculée par l'unité de calcul de moyenne (27),
et les écarts ainsi déterminés des différences de pression sont envoyés à une unité
opérationnelle (23), qui commande les ensembles respectifs en série (29 à 29n) des
unités de pompes vibrantes indépendamment les uns des autres.