This application claims the benefit of Japanese Patent Application No. 2009-080233 filed Mar. 27, 2009, and Japanese Patent Application No. 2009-163133 filed Jul. 9, 2009, the entire contents of each of which are incorporated by reference herein.
The present invention relates to a device that converts an electric current to pump pressure.
Positive displacement pumps and turbopumps are commonly used as fluid pumps. Japanese Laid-Open Patent Publication No. 2004-060640 discloses a diaphragm pump, which is a type of positive displacement pump, and Japanese Laid-Open Patent Publication No. 2009-011767 discloses a centrifugal pump, which is a type of turbopump.
A positive displacement pump requires a valve structure, or a shielding mechanism for a valve. When deteriorated, shielding mechanisms adversely affect the pump performance. Thus, the energy conversion efficiency of positive displacement pumps is lower than that of turbopumps. In contrast, turbopumps are superior in energy conversion efficiency and have a wide application range for the flow rate and discharge pressure. However, since a drive motor is attached to the outside of the pump, the overall size of a turbopump tends to be large. Further, a typical turbopump requires a shaft shielding mechanism for preventing liquid leakage (fluid leaks) about the shaft. To eliminate the shaft shield, a magnetic shaft may be used. However, a magnetic shaft requires an advanced type of magnetic control mechanism. Also, Japanese Laid-Open Patent Publication No. 2007-289911 does not disclose the details for an embodiment when the invention is used in a pump.
Accordingly, it is an objective of the present invention to provide a turbopump that requires no valve and has a simple structure suitable for miniaturization, and further to provide a pump structure requiring no shaft shield.
In accordance with one aspect of the present invention, an angular oscillation centrifugal pump is provided that includes a case, an angular oscillator accommodated in the case to be rotatable in a reciprocating manner, a retaining portion that is provided in the case to retain the angular oscillator, and an electromagnetic coil provided in the case. The angular oscillator has a first magnetic dipole and a pressure feed passage. The pressure feed passage has a pressure feed inlet for receiving fluid and a pressure feed outlet for discharging the fluid. The retaining portion retains the angular oscillator based on magnetic force generated by the first magnetic dipole. The retaining portion includes a second magnetic dipole or a magnetic body. The angular oscillator is oscillatable relative to the retaining portion. The magnetic force defines a rest point for the oscillation of the angular oscillator and the natural frequency of the oscillation. When a current that is synchronized with the natural frequency is supplied to the electromagnetic coil, the angular oscillator is resonated. As a result, fluid in the pressure feed passage receives centrifugal force, so that the fluid is discharged from the pressure feed outlet.
Since the invention of claim 1 provides a turbopump requiring no valve, claim 1 is superior to positive displacement pumps. A conventional centrifugal pump requires a drive unit at the outside of the pump structure. In contrast, since the centrifugal pump of the present invention has a resonance oscillation motor incorporated therein, the pump structure and the drive mechanism are integrated. This structure is suitable for miniaturization. Further, a pump with a perfect shield performance with no fluid leakage can be provided. Since the angular oscillation of the angular oscillator is a reciprocating rotation within a range less than 360°, no structure for shielding the rotary shaft is required. Further, the pump of the present invention is simple and easy to manufacture, and also has a small number of failure factors. Also, as shown in table 2 shown below, the output performance is high for the size of the pump, and the pump performance can be designed for a wide range.
According to the invention of claim 2, an angular oscillator as shown in
Other aspects and advantages of the invention will become apparent from the following description, taken in conjunction with the accompanying drawings, illustrating by way of example the principles of the invention.
The features of the present invention that are believed to be novel are set forth with particularity in the appended claims. The invention, together with objects and advantages thereof, may best be understood by reference to the following description of the presently preferred embodiments together with the accompanying drawings in which:
a) is a cross-sectional plan view of an angular oscillator shown in
b) is a cross-sectional view taken along line 1B-1B of
c) is a longitudinal cross-sectional view;
a) is a cross-sectional plan view illustrating an angular oscillation centrifugal pump according to a first embodiment of the present invention;
b) is a cross-sectional view taken along line 2B-2B of
c) is a longitudinal cross-sectional view;
d) is a cross-sectional plan view showing an operation;
a) is a cross-sectional plan view of a centrifugal pump according to a second embodiment, which has an improved energy conversion efficiency;
b) is a cross-sectional view taken along line 3B-3B of
c) is a longitudinal cross-sectional view;
d) is a cross-sectional plan view showing an operation;
a) is a cross-sectional plan view of a centrifugal pump according to a third embodiment;
b) is a cross-sectional view taken along line 4B-4B of
a) is a cross-sectional plan view of a centrifugal pump according to a fourth embodiment;
b) is a cross-sectional view taken along line 5B-5B of
a) is a cross-sectional view of a centrifugal pump according to a fifth embodiment; and
b) is a cross-sectional view taken along line 7B-7B of
As shown in
a) to 2(c) show an angular oscillation centrifugal pump according to a first embodiment that has a structure for causing the angular oscillator 1 to angularly oscillate. The centrifugal pump incorporates the resonance oscillation motor of Japanese Laid-Open Patent Publication No. 2007-289911.
The angular oscillator 1 is accommodated in a case 3, which is formed as a hollow box. The case 3 has a pair of bearing portions 4, which are partly located in the axial hole 1a of the angular oscillator 1 to rotatably support the angular oscillator 1. Contacting portions of the inner circumferential surface of the axial hole 1a and the outer circumferential surface of the bearing portions 4 are subjected to surface treatment so that the angular oscillator 1 smoothly performs angular oscillation.
The case 3 further has an outlet opening 5, to which a discharge pipe 9 is connected, and two suction openings 6, which extend from the outside of the case 3 to the axial hole 1a through the bearing portions 4. With the discharge pipe 9 received in the outlet opening 5, hermetic sealing treatment is applied to the periphery of the outlet opening 5 to disconnect the interior of the case 3 from the outside. A suction pipe 8 is branched into two outside the case 3, and each branch passes through the corresponding suction opening 6, extends through the axial hole 1a of the angular oscillator 1, and is connected to one of the radial through holes 2. In the present embodiment, the branches of the suction pipe 8 are inserted in the radial through holes 2 and extend to the outer circumferential surface 1b of the angular oscillator 1. Since the distal ends 8a of the suction pipe 8 are required to be deformed smoothly in response to angular oscillation of the radial through holes 2, the suction pipe 8 is preferably made of soft material, such as a silicone rubber pipe. As a result, the suction pipe 8 is capable of continuously supplying fluid to the radial through holes 2 during angular oscillation. That is, since the suction pipe 8 extends from the suction openings 6 to the radial through holes 2, the centrifugal pump exerts a perfect shielding performance against fluid leakage. The radially inner end of each radial through hole 2 is referred to as a pressure feed inlet 2a, and the radially outer end of each radial through hole 2 is referred to as a pressure feed outlet 2b. The pressure feed inlets 2a are connected to the suction openings 6 to receive fluid from the suction openings 6 by the suction pipe 8. The pressure feed outlets 2b are connected to the discharge openings 5 so as to send fluid to the discharge openings 5 through the interior of the case 3.
A magnet is used as the angular oscillator 1, so that it functions as a first magnetic dipole. A magnet is embedded in the case 3 so that the case 3 functions as a second magnetic dipole. The second magnetic dipole is a retainer (stator) that retains the angular oscillator 1 based on the magnetic force of the first magnetic dipole. A nonmagnetic member may be used as the angular oscillator 1. In this case, a magnet is embedded in the angular oscillator 1 so that it functions as the first magnetic dipole. Further, a magnet may be used as the case 3 itself, so that it functions as the second magnetic dipole.
The magnetic field of the first magnetic dipole and the magnetic field of the second magnetic dipole interact with each other to determine the stable position of the angular oscillator 1, or the rest point of oscillation. For example, as shown in
For example, in a case where
It is sufficient if the radial through holes 2 extend from the axial hole 1a, which extends along the axis C of the angular oscillator 1, to the outer circumferential surface 1b. The stable position of the angular oscillator 1 may be any rotational position about the axis C. This is because when the angular oscillator 1 angularly oscillates, centrifugal force acts on fluid in the radial through holes 2, so that pump action is generated.
An oscillating system has a natural frequency, which can be adjusted by changing the shapes, arrangement, and the intensity of the magnets of the first magnetic dipole and second magnetic dipole. Further, the natural frequency changes in accordance with the load on the angular oscillator 1. When the angular oscillator 1 angularly oscillates, the change in the angular velocity, which is determined by the shapes, arrangement and the magnet intensity of the first magnetic dipole and second magnetic dipole, generally approximates to a sine wave corresponding to the rotational angle.
The second magnetic dipole of the case 3 may be a magnetic body that is not a magnet. That is, it is sufficient if the magnetic filed generated by the angular oscillator 1 acts on the magnetic body of the case 3, so that the rest point of the angular oscillator 1 is defined. The second magnetic dipole or the magnetic body of the case 3 functions as a retainer that retains the angular oscillator 1 relative to the case 3 by using the magnetism generated by the angular oscillator 1.
First magnetic field lines are generated between the first magnetic dipole and the second magnetic dipole. An electromagnetic coil 7 is provided to generate second magnetic field lines that include components perpendicular to the first magnetic lines. In
When a current is supplied to the electromagnetic coil 7, the electromagnetic coil 7 generates the second magnetic field lines, thereby oscillating the angular oscillator 1. When a periodic current is supplied to the electromagnetic coil 7, and the current frequency is adjusted such that the frequency of the magnetic field of the coil 7 coincides with the natural frequency of the angular oscillator 1, the angular oscillator 1 resonates and generates a highly efficient oscillating motion. That is, the oscillating system of the centrifugal pump converts the energy supplied by the current into the rotational velocity energy and the potential energy of the magnetic field, and stores the converted energy. When the moment of inertia of the angular oscillator 1 is expressed by I [Kg·m2], and the maximum angular velocity in a single cycle is expressed by ω [rad/s], the amount of energy stored in the centrifugal pump is expressed by Iω2/2 [J].
While such resonance is taking place, continuous supply of fluid from the suction pipe 8 to the radial through holes 2 causes the fluid to receive centrifugal force in the radial through holes 2. The fluid is thus continuously discharged to the outside from the angular oscillator 1. That is, the radial through holes 2 are oscillated to apply centrifugal force to the fluid in the radial through holes 2 so that the fluid is moved under pressure and discharged through the pressure feed outlets 2b. The energy used for conveying the fluid is the output energy of the oscillating system, and consumed from the oscillating system. The angular oscillator 1 is thus resonated to compensate for the consumed output energy.
As described above, a turbo type centrifugal pump utilizing angular oscillation is obtained by integrally incorporating the mechanism of a resonance oscillation motor into the pump mechanism.
The above described embodiment provides the following advantages (operational effects).
(1) The centrifugal pump causes the angular oscillator 1 to angularly oscillate, so as to apply centrifugal force to fluid in the radial through holes 2 to pressure feed the fluid. That is, the angular oscillator 1 is oscillated by electromagnetic force supplied from the outside of the case 3 in a state where the angular oscillator 1 is mechanically and rotatably supported to the case 3 by the bearing portions 4. This allows the case 3 to be sealed in the structure for applying the force to the angular oscillator 1. For example, unlike a structure in which the angular oscillator 1 is driven by a drive motor from the outside of the case 3 through a rotary shaft extending through the case 3, the present embodiment requires no shaft shielding structure and is suitable for miniaturization.
(2) The angular oscillator 1 is formed simply by forming the radial through holes 2 in a cylindrical magnet. The angular oscillator 1 is therefore easy to manufacture.
(3) The suction pipe 8 pass through the interior of the bearing portions 4, which are partly located in the axial hole 1a of the angular oscillator 1. Therefore, the structure for supplying fluid to the radial through holes 2 is formed by effectively utilizing the structure for rotatably supporting the angular oscillator 1. The bearing portions 4 stably support the suction pipe 8.
a) to 3(c) illustrate a centrifugal pump according to a second embodiment.
The hollow portion of a case 13 is cylindrical. That is, the case 13 has an inner circumferential surface 13a the size of which is substantially equal to that of the angular oscillator 1. The diameter of the case inner circumferential surface 13a is slightly greater than the outer diameter of the angular oscillator 1. To allow the case inner circumferential surface 13a to rotatably support the outer circumferential surface 1b of the angular oscillator 1, facing portions of these are subjected to mirror coating. That is, no structure like the bearing portions 4, which are partly located in the axial hole 1a of the angular oscillator 1, is required to allow the case inner circumferential surface 13a to function as a bearing as shown in
Outlet openings 5 extend in the circumferential direction along the case inner circumferential surface 13a, so as to encompass the reciprocating motion range A (see
The centrifugal pump of
(4) In the centrifugal pump shown in
a) and 4(b) illustrate a centrifugal pump according to a third embodiment, which has a simple structure.
A case 3 is formed by a rectangular frame-like inner case 3a and an outer case 3b, which hermetically accommodates the inner case 3a. An outlet opening 5 and a suction openings 6 are formed in the outer case 3b. The inner case 3a rotatably supports a hollow shaft 11 with a pair of bearings 4. An angular oscillator 1, which is a magnet of a first dipole, and through hole support arms 12 are attached to the hollow shaft 11 so as to rotate integrally. The through hole support arms 12 function as through hole accommodating arms that pass the clearance of the rectangular frame of the inner case 3a and extend in the radial direction, so as to project outward from the angular oscillator 1. The hole support arm 12 includes two radial through holes 2 that communicate with the axial hole 11a of the hollow shaft 11.
A suction pipe 8 is drawn from the outside to the inside of the outer case 3b, and passed through the axial hole 11a of the hollow shaft 11. The suction pipe 8 is branched into two, and each branch passes through the corresponding radial through hole 2 to the distal end of the through hole support arm 12. An electromagnetic coil 7 is wounded about the inner case 3a. Two stator magnets 14, each serving as a second dipole, or a retainer, are attached to the inner surface of the outer case 3b. That is, the outer case 3b hermetically accommodates the inner case 3a, the electromagnetic coil 7, the stator magnets 14, and the hollow shaft 11. A discharge pipe 9 is attached to the outlet opening 5 of the outer case 3b. First magnetic field lines generated by the first dipole and the second dipole extend along vertical direction in each of
The device shown in
(5) The through hole support arms 12 are used for extending the radial through holes 2, while reducing the outer radius of the angular oscillator 1. The smaller the outer radius of the angular oscillator 1, the smaller the moment of inertia becomes of the angular oscillator 1. Accordingly, the resonant frequency of the angular oscillator 1 can be raised, and a more intense centrifugal force can be generated. In other words, the smaller the outer diameter of the angular oscillator 1, the easier it is to increase the pump output. On the other hand, the longer the radial through holes 2, the easier it is to generate a more intense centrifugal force for the same frequency and to increase the pump output.
According to the structure of the centrifugal pump shown in
A pulse current of approximately 50 Hz was supplied to the electromagnetic coil 7, and the frequency of the pulse current was sequentially adjusted. At about 70 Hz, the angular oscillator 1 performed angular oscillation while resonating at the natural frequency. The oscillation angle, or the angle of amplitude, was approximately 2 radians. As a result, the angular oscillator 1 functioned as a centrifugal pump and exerted a pumping water level of up to approximately 110 cm. That is, the pump pressure was about 11 kpa. When no pressure load was acting on the discharge pipe 9, the discharge flow rate was approximately 50 ml/min, and the work of the pump was approximately 0.01 W. The water pumping performance to a height of 50 cm was approximately 30 ml/min.
a), 5(b), and 6 illustrate a fourth embodiment, which is suitable for an artificial heart pump. This centrifugal pump has a property of not destroying blood.
As shown in
A suction pipe 8 is connected to either end of the hollow shaft 11. Each end of the hollow shaft 11 passes through the corresponding bearing portion 4. Each suction pipe 8 is passed through a suction opening 6 formed in the corresponding auxiliary case 3d, while closely contacting and being fixed to the auxiliary cases 3d. That is, even if fluid exists outside the auxiliary cases 3d, the fluid outside the auxiliary cases 3d is isolated from the bearing portions 4 by the auxiliary cases 3d.
The device shown in
(6) The present embodiment is designed for being embedded in the human body. That is, the bearing portions 4 are sealed by the elastic sealing members 15 and the auxiliary cases 3d. As a result, fluid that flows into the centrifugal pump through the suction pipes 8, receives centrifugal force, and is discharged from the discharge pipes 9 does not contact the bearing portions 4. The following description is about case in which the pump of the present embodiment pressure feeds blood, which carries particles such as red blood cells, is used as fluid that carries fine particles, or carrier fluid. In this case, particles contained in the carrier fluid (for example, red blood cells in blood) are prevented from being mashed by the bearing portions 4.
The suction pipes 8 closely contact and are fixed to the auxiliary cases 3d, and a portion of the interior of each auxiliary cases 3d that corresponds to the suction pipe 8 is smoothly deformed according to angular oscillation of the hollow shaft 11. As a result, the hollow shaft 11 is rotatable relative to the case 3. For example, amber natural rubber or silicone rubber may be used for the elastic sealing member 15.
Further, as shown in
The oscillator disk 16 has four radial through holes 2, which are spaced by 90°. Each radial through hole 2 communicates with the interior of the hollow shaft 11, and extends from the inner circumferential surface to the outer circumferential surface of the oscillator disk 16.
Two stator magnets 14 are arranged on the case 3 at an interval of 180°. Further, six electromagnetic coils 7 are attached to the top plate as shown in
Likewise, two stator magnets 14 and six electromagnetic coils 7 are attached to the bottom plate of the case 3. The stator magnets 14 of the top plate of the case 3 and the stator magnets 14 of the bottom plate of the case 3 face each other so as to be attracted to each other. Each magnet in the top plate and a corresponding magnet in the bottom plate of the case 3 form a second dipole. That is, the case 3 has two second dipoles, each arranged in a direction of repelling the two first dipoles of the oscillator disk 16. Thus, the oscillator disk 16 is rotatable about its axis, and is at a resting position when the oscillator magnets 17 are spaced from the stator magnets 14 by 90° about the axis. The electromagnetic coils 7 on the bottom plate of the case 3 each face the corresponding one of the electromagnetic coils 7 on the top plate with respect to the axial direction.
The above described device provides the following advantages.
(7) If the oscillator magnets 17 are arranged close to the axis, it is easy to adjust the angular oscillation of the oscillator disk 16 to obtain a high resonant frequency. On the other hand, when the radius of the oscillator disk 16 is increased, the radial through holes 2 are elongated, so that a great centrifugal force can be applied to the fluid in the radial through holes 2.
This configuration gives pump characteristics to carrier fluid, while preventing particles contained in the carrier fluid in the case 3 from being mashed. That is, the bearing portions 4 are isolated from the carrier fluid by the elastic sealing members 15 and the auxiliary cases 3d. That is, the contacting surfaces of the hollow shaft 11 and the suction openings 6 serving as shaft receiving holes is hermetically isolated from the carrier fluid. As a result, the particles in the carrier fluid are prevented from being mashed.
(8) Since the conventional centrifugal pump needs to have a drive source such as a motor outside the case 3, the clearance between the drive source and the shaft needs to be sealed. In contrast, since the drive source of the centrifugal pump of the present embodiment does not need to be located outside the case 3, the hermetic sealing of the case 3 is easy.
The case 3 has a plurality of the outlet openings 5, to each of which a discharge pipe 9 is attached. The interior of the case 3 has a shape that allows fluid to smoothly flow in one direction. As shown by arrows in
For example, the length of each radial through hole 2 is approximately 3.5 cm. The cross-section of each radial through hole 2 is rectangular, and the total cross sectional area of the four radial through holes 2 is approximately 0.5 cm2. The sizes of and distances between the oscillator magnets 17 and the stator magnets 14 are determined such that the angular oscillator 1 has a resonant frequency that is higher or equal to 40 cycles. The outer diameter and the thickness of the oscillator disk 16 are set to 70 mm and 8 mm, respectively.
The electromagnetic coils 7 are driven periodically. Each cycle is split into multiple phases so that the timing at which each coil is driven and switching of the direction of currents are controlled to facilitate angular oscillation. Table 1 shows one example of control. For purposes of illustration, the six electromagnetic coils 7 are divided into three pairs of coils, or two first coils 7a, two second coils 7b, and two third coils 7c. The coils in each set are separated by 180°. The pattern of excitation of eight phases, which are the zeroth phase to the seventh phase, is shown in Table 1. In table 1, “+” represents a state in which the exited electromagnetic coil 7 is driven to attract the oscillator magnet 17, and “−” represents a state in which the excited electromagnetic coil 7 repels the electromagnetic coil 17.
When the pressure load of the centrifugal pump fluctuates, the natural frequency of the oscillator disk 16 also fluctuates. In order to feed the frequency fluctuation of the oscillator disk 16 back to the drive control of the centrifugal pump, a position sensor 20 that detects the position and the rotation direction of the oscillator disk 16 is attached to the case 3 (shown in
As a result, the fluid pump shown in
a) and 7(b) illustrate a fifth embodiment, which is suitable as an air pump.
That is, a device shown in
A part of or the entirety of the angular oscillator 1 is formed of magnet, and the magnetic force of the angular oscillator 1 and the stator magnet 14 attract each other in the vertical direction as viewed in
Hereinafter, the operating principles and estimate of pumping performance for the centrifugal pump according to the present invention will be described.
For illustration purposes, the inner diameter and the outer diameter of the angular oscillator 1 are expressed by r2 [m] and r2 [m] as shown in
The oscillation angle of the angular oscillation of the angular oscillator 1 is expressed by α [radian] (see
In a case where the angular velocity ω in angular oscillation changes along a sine wave, and the average angular velocity in a single cycle is expressed by ω1, if the phase position of the cycle is θ [radian], and one cycle=2π [radian], the angular velocity ω(θ) relative to the cycle phase position is represented by the following equation: ω(θ)=(π/2)ω1 sin θ In this case, the centrifugal acceleration a acting on an object in the radial through hole 2 at a position away from the cylinder enter by r [m] is represented by the following equation:
a(θ)=(π2/4)rω12 sin2θ
The average centrifugal acceleration a1 in one cycle is obtained by averaging the integral of one cycle, and represented by a1=(π2/4)rω12.
Therefore, it is assumed that the liquid filling the radial through hole 2 receives, from the center to a side of the cylinder, the averaged centrifugal acceleration a1=(π2/4)rω12=π2·rα2f2.
When the cross-sectional area of the radial through hole 2 is expressed by S [m2], S=πs(Φ/2)2. The volume y [m3] of the liquid in the radial through hole satisfies the equation y=Sr3. When the liquid specific gravity is expressed by g [g/cm3], and the weight of the liquid in the radial through holes 2 is expressed by m [kg], m=1000 gy. The liquid in the radial through holes 2 receives centrifugal force F [N] directed from the cylinder center to a side of the cylinder. If averaged, F [N]=ma1, that is, F=62.5π2gSr32α2f2. The centrifugal force is pump discharging force, and if the pump pressure is expressed by A [N/m2], A=F/S, that is, A=250π2gr32α2f2. Since A [N/m2] is equal to A [pa], if the pump pressure is expressed by B [kpa], B=A/1000.
The average amount of time t [s] required for liquid to pass through the radial through hole 2 is t=√{square root over ( )}(r3/a1), and the averaged speed v [m/s] of liquid to pass through the radial through hole 2 is v=r3/t. When the pressure load at the output side of the pump is zero, the displaced volume per second is expressed by Y [m2/s] and the displaced weight per second is expressed by M [kg/s], Y=y/t and M=m/t. The discharge flow rate Z [ml/min] per minute when the pressure load is zero is Z=6×107 Y. When the work per second consumed through the pump operation is expressed by P [N·m/s], P=Fv, and the unit is [N·m/s], or [W].
Three factors of the pump output, that is, the pump pressure B [kpa], the discharge flow rate Z [ml/min] per minute when the pressure load is zero, and the pump work P [W] are expressed by the following parameters of the pump. The pump parameters include the length r3 [m] of the radial through hole, the diameter Φ [m] of the radial through hole, the number s of the radial through holes, the oscillation angle α [radian] of the angel oscillation, the frequency f of the radial oscillation [cycle/s], and the liquid specific gravity g [g/cm3].
B=(π2/4)gr32α2f2
Z=7500000π2sΦ2r3αf
P=31.25π4sgΦ2r33α3f3
These three equations B, Z, P explicitly show that the pump pressure B is proportional to the square of the radial through hole length r3, the square of the oscillation angle α, and the square of the frequency f, that the discharge flow rate Z [ml/min] per minute when the pressure load is zero is proportional to the radial through hole length r3, the oscillation angle α, and the frequency f, and that the pump work P is proportional to the cube of the radial through hole length r3, the cube of the oscillation angle α, and the cube of the frequency f. Further, the discharge flow rate Z per minute when the pressure load is zero and that the pump work P are both proportional to the number of the radial through holes 2 and to the square of the diameter Φ of the radial through hole 2.
Further, the flow rate in a case where there is pressure load A1 [pa] is calculated. A corrected pump pressure obtained by subtracting the pressure load is expressed by A2 [pa], a corresponding corrected centrifugal force is expressed by F2 [N], and a corrected centrifugal acceleration is expressed a2 [m/s2]. In this case, A2=A−A1, F2=A2S, and a2=F2/m.
In this case, when a corrected average amount time required for liquid to pass through the radial through hole 2 is expressed by t2, t2=√{square root over ( )}(r3/a2). The corrected displaced volume per second is expressed by Y2 [m3]=y/t2, and the correction flow rate per minute Z2 [ml/min]=60000000Y2.
This is expressed by the pump parameters and the pressure load A1.
Z2=1500000πsΦ2√{square root over ( )}(25π2r32α2f2−A1/10g2)
By substituting concrete numbers into the above equations, the pump performance can be calculated. Table 2 shows examples of substitution. Table 2 shows calculations in a case where the liquid handled is water having a specific gravity of 1.
In Table 2, Condition 1, Output 1, and Load output 1 represent a case where the length r3 and the diameter Φ of the radial through hole 2 are 1 cm and 1 mm, and resonant angular oscillation of an oscillation angle of 1 radian was caused at 100 cycles. In this case, the pump pressure, or the output, was 2.4 kpa, and the discharge flow rate with no pressure load was 73 ml/min. Further, the pump output was 0.003 W, and the discharge flow rate with a pressure load of 1 kpa was 57 ml/min.
Condition 2 corresponds to the embodiment shown in
In this manner, Table 2 shows that the following pump parameters are obtained when the length of the radial through hole 2 is changed in a range between 1 cm to 4 cm, the oscillation angle is changed in a range between 1 radian to 2 radians, the cycle of angular oscillation is changed in a range between 50 cycles and 200 cycles. The pump is adjustable in a wide range of parameters. That is, the pump pressure can be adjusted between 2 kpa and 40 kpa, the flow rate with no pressure with load 5 ml/min. to 13000 ml/min., and the work of the pump is between 1 mW to 8 mW.
The above described embodiments may be modified as follows.
The direction in which each radial through hole 2 extends is not limited to a radial direction with respect to the angular oscillator 1, but may be inclined or bent at one point. In other words, any flow passages may be used as long as fluid in the passage receives centrifugal force generated by reciprocating rotation of the angular oscillator 1 and is moved under pressure to the outlet.
The number of the radial through holes 2 is not limited to two, but may be one, or three or more.
Number | Date | Country | Kind |
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2009-080233 | Mar 2009 | JP | national |
2009-163133 | Jul 2009 | JP | national |
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