The invention concerns a preferably pulsation-free positive displacement pump consisting of two rotary pistons for the precise distribution at variable flow rate of liquids, medication, foods, detergents, cosmetic products, chemical compounds or any other type of fluid, gel or gas.
There exist different motors and systems employing rotary pistons such as are described in U.S. Pat. Nos. 1,776,843, 4,177,771 and 7,421,986 the operating principle of which consists in driving a rotor containing two parallel eccentric pistons and cylinders in opposition by combustion of the fuel contained in the cylinders.
In U.S. Pat. No. 1,776,843 the pistons are guided by bearings fixed to the ends of the pistons sliding along a cam placed along the interior wall of the stator and a second cam connected to the stator on the rotor side. The to-and-fro movement of the pistons is produced by the movement of the bearings along the two cams.
In U.S. Pat. No. 4,177,771 the pistons are guided by bearings fixed to the ends of the pistons sliding along the stator having an oblong shape. The pistons therefore move radially when the rotor turns. The to-and-fro movement of the pistons can be produced only by coupling two pairs of parallel pistons fixed to the rotor with each pair offset 180° relative to the other pair and eccentric relative to the rotation axis of the rotor so that the movement compressing the gases in one pair of pistons occurs at the time of the explosion of the gases in the other pair.
In U.S. Pat. No. 7,421,986 the pistons are guided by means of a circular cam on the stator in which the drive shafts of the links connected to the pistons slide. The to-and-fro movement of the pistons is produced by the eccentricity of the rotation axis of the rotor relative to the axis of the stator.
Although these systems can potentially be adapted to function as pumping systems, a first problem encountered with these systems is that they comprise numerous parts, which makes their manufacturing and maintenance costs high for use in a medical or food environment, for example, where they must be cleaned or sterilized.
The second problem is that the principle of spring-loaded valves employed for the distributor by these systems is unsuitable for the production of pumping systems using injection-molded plastic parts that normally employ elastomer seals.
The third problem is that these systems have a discontinuous alternating operating cycle that cannot produce a pulsation-free flow if they are used as pumping systems.
A fourth problem that is encountered is that these systems cannot be made from injection-molded plastic parts to produce pumps employing low-cost disposable fluidic modules that can be discarded after use.
The present invention concerns a high-performance pump comprising a small number of parts produced at very low cost for pulsation-free pumping and metering of liquids, viscous products or gases at variable flow rates.
This invention solves the problems described above and enables simplified development for the mass production of pumps with an element in contact with the pumped fluid that is interchangeable and preferably made of disposable low-cost plastic.
The pump comprises two opposite parallel pistons placed in two cylindrical cavities of a rotor turning in a cylindrical stator with at least one inlet port and at least one outlet port having on its interior face a piston guide cam and preferably a housing for a sealing element positioned between the rotor and the stator.
The pumping principle consists in turning the rotor placed inside the stator so as to move the pistons axially in the rotor via the cam located on the interior wall of the stator. The cam is dimensioned with six segments, a short nominal filling segment, two short segments for draining at a flow rate lower than the nominal flow rate of the pump, a long segment for draining at the nominal flow rate of the pump and two segments for changeover of the valves between the inlet and outlet ports of each pumping chamber. During the phase of draining one chamber at the nominal flow rate of the pump the other chamber changes over from the outlet port to the inlet port and is then filled completely and changes over from the inlet port to the outlet port, after which the two chambers discharge to the outlet port, preferably simultaneously, at low flow rates the sum of which is equivalent to the nominal flow rate of the pump so that the outlet flow rate is preferably stable, continuous, uninterrupted and pulsation-free.
In order to produce a high-performance seal with a minimum of components the system for changing over the connections of the inlet and outlet ports to the pumping chambers is adapted to be synchronous with the movement of the pistons without requiring any additional elements.
The drive arrangement of the pump principally consists of a support, a drive head and an actuator, preferably in the form of a motor. The pump is particularly well suited to production at low cost given that it is formed only of parts that are easy to injection mold in plastic and to assemble automatically.
The present invention will be better understood after reading the description of examples given by way of nonlimiting illustration only with reference to the appended drawings, in which:
a is a view of the front face of the invention
b is a side view of the invention
c is a longitudinal section taken along the line A-A according to
d is a longitudinal section taken along the line B-B according to
a is a longitudinal section taken along the line C-C according to
b is a longitudinal section taken along the line D-D according to
a is a longitudinal section taken along the line E-E according to
Second variant
Third variant
Fourth variant
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When the rotor (3) turns from 0° to 45°, the pistons (5, 5′) move along the cam at low flow rates (61,61′), the effect of which is to expel the liquid simultaneously from the chambers (21,21′) to the outlet port (16) via the front channels (19, 19′), the lateral channels (20,20′) of the pistons (5,5′) and the through-holes (9,9′) connected to the outlet cavity (15).
When the rotor (3) turns from 45° to 75°, the piston (5) continues to expel the liquid from the chamber (21) at the nominal flow rate (62). The piston (5′) ceases to move in a linear manner and the lateral channel (20′) is connected via the through-hole (9′) to the port changeover transition area (17′), which closes the chamber (21′). When the rotor (3) turns preferably from 75° to 150°, the piston (5) continues to expel the liquid from the chamber (21) at the nominal flow rate (62). The piston (5′) moves in a linear manner in the opposite direction, the effect of which is to aspirate the liquid in the chamber (21′) from the inlet port (14) via the front channel (19′), the lateral channel (20′) and the through-hole (9′) connected to the inlet cavity (13).
When the rotor (3) turns preferably from 150° to 180°, the piston (5) continues to expel the liquid from the chamber (21) at the nominal flow rate (62). The piston (5′) ceases to move in a linear manner and the lateral channel (20′) is connected via the through-hole (9′) to the port changeover transition area (17), which closes the chamber (21′).
When the rotor (3) turns preferably from 180° to 225°, the pistons (5, 5′) move along the cam at low flow rates (63,63′), the effect of which is to expel the liquid simultaneously from the chambers (21,21′) to the outlet port (16) via the front channels (19, 19′), the lateral channels (20,20′) of the pistons (5,5′) and the through-holes (9,9′) connected to the outlet cavity (15).
When the rotor (3) turns from 225° to 255°, the piston (5′) continues to expel the liquid from the chamber (21′) at the nominal flow rate (62′). The piston (5) ceases to move in a linear manner and the lateral channel (20) is connected via the through-hole (9) to the port changeover transition area (17′), which closes the chamber (21).
When the rotor (3) turns from 255° to 330°, the piston (5′) continues to expel the liquid from the chamber (21′) at the nominal flow rate (62′). The piston (5) moves in a linear manner in the opposite direction, the effect of which is to aspirate the liquid in the chamber (21) from the inlet port (14) via the front channel (19), the lateral channel (20) and the through-hole (9) connected to the inlet cavity (13).
When the rotor (3) turns preferably from 330° to 360°, the piston (5′) continues to expel the liquid from the chamber (21′) at the nominal flow rate (62′). The piston (5) ceases to move in a linear manner and the lateral channel (20) is connected via the through-hole (9) to the port changeover transition area (17), which closes the chamber (21).
When the rotor (3) is turned 360° relative to the stator (2) it returns to the 0° position, which corresponds to a complete pumping cycle of the pump (1).
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Guide elements (76,76′), preferably in the form of pins, are placed inside the holes (75,75′) in the pistons (5,5′) so as to guide the pistons (5,5′) along the cam (10) of the stator (2) and the cam (10′), which is symmetrical with respect to the cam (10), on the interior face of the cap (70). The ends of the guide elements (76,76′) are therefore guided perfectly in a symmetrical manner making the movements of the pistons (5,5′) more effective and ensuring improved resistance to forces when the pump turns at a high speed or delivers at a high pressure. The guide elements (76,76′) turn freely inside the holes (75,75′) of the pistons (5,5′) so as to reduce the friction with the cam (10) and the cam (10′).
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The return element (90) may be adapted so that the function is reversed and the rotor (3) must be drawn toward the direction opposite to the return element (90) to bear on the sealing element (4).
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During operation of the pump (1), pressure variations occurring in the pumping chambers (21,21′) deform the respective flexible elements (87,87′), which transmit the pressure from each cavity (94,94′) to the cavities (95,95′), respectively. It is then possible to measure the pressure at the inlet and at the outlet of the pump by placing two pressure sensors (not shown) at the exterior ends of the channels (102,102′). The flexible elements (87,87′) provide the isolation and the seal between the internal fluidic circuit of the pump and the exterior, as well as making it possible to measure pressure variations occurring at the inlet and at the outlet of the pump. This system is particularly suitable for measuring leaks or detecting blockages at the inlet or at the outlet of the pump without having to connect pressure gauges to the external tubes of the pump. Integrating the flexible elements (87,87′) into the pump (1) makes it possible to reduce the overall size of the system, which is extremely important in portable pumps, for example, notably in the medical field.
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The pumping principle described above is reversible by having the rotor turn in the other direction.
The angle values defined above are given by way of example and may be different according to the dimensions of the cam or the required flow rate curve.
The low flow rates (61,61′,63, 63′) are preferably equivalent to half the nominal flow rate of the pump.
The cam may be adapted to produce a pulsed or semi-pulsed flow.
In another variant, not shown, the housing (11) and the sealing element (4) may be on the interior face of the rotor (3).
In another variant, not shown, the cavities (13,15) and the changeover transition areas (17,17′) may be perpendicular to the rotation axis of the pump. In this case, the sealing element is preferably at the periphery of the rotor of the pump.
In another variant, not shown, the rotor may be adapted to receive a magnetic element so that it can be driven in rotation with the aid of a magnet or any other exterior electromagnetic element. Thus the pump may be coupled to a contactless drive arrangement. This variant is particularly suitable if the pump is implanted under the skin or in the body and must be actuated from the outside.
In another variant, not shown, the cap may be adapted to receive the inlet and outlet ports of the pump.
The seal between the mobile parts is preferably produced by means of an elastomer, an overmolded seal or any other sealing element. However, it is possible to produce the pump with no sealing element between the stator or the cap and the rotor, for example by virtue of the fit between them. The elements constituting the pump are preferably made of plastic and disposable. The pump may be sterilized for the distribution of food or medication for example. The choice of materials is not limited to plastics, however.
Although the invention has been described with reference to a plurality of embodiments, there exist other variants that are not described. The scope of the invention is therefore not limited to the embodiments described above.
Number | Date | Country | Kind |
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PCT IB2012/001003 | May 2012 | IB | international |
PCT IB2012/002451 | Nov 2012 | IB | international |
Filing Document | Filing Date | Country | Kind |
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PCT/IB2013/000819 | 5/2/2013 | WO | 00 |