The invention relates to an axial piston pump with variable flow rate. This pump is particularly suitable for processing a cleaning fluid in a cleaning apparatus, for example a high-pressure cleaner. The cleaning fluid may be water to which detergent substances may have been added. The invention further relates to a cleaning apparatus provided with said pump.
In high-pressure cleaning machines axial piston pumps are usually used. Known axial piston pumps comprise a swash plate rotationally driven by a motor shaft which, during rotation, reciprocates a plurality of pistons inside respective cylinders. A pump of this type is for example disclosed in the European patent application EP 1435457, in which an elastic element is arranged below the swash plate. Owing to the elastic element, it is possible to vary the flow rate of the cleaning fluid depending on the dispensing pressure of said fluid, which is selectable by a user by means of a separate pressure-adjusting device. The elastic element in fact enables the angle between the swash plate and the motor shaft to be modified when the dispensing pressure varies. Thus, the stroke of the pistons is modified, i.e. the volume of cleaning fluid that the pistons are able to displace changes.
A drawback of the pump disclosed in EP 1435457 is that, as will be explained in greater detail below, the flow rate of the cleaning fluid decreases very rapidly when the dispensing pressure selected by the user increases. The elastic element, which -is substantially parallel to the pistons, is in fact almost completely compressed when the dispensing pressure of the cleaning fluid exceeds a relatively low value. In this situation, the swash plate is almost perpendicular to the motor shaft, which implies that the stroke of the pistons is short and the volume of cleaning fluid displaced by the pump is low.
A rapid decrease in the flow rate as pressure increases is not desired, because in certain applications it is preferable to combine a high pressure with a high flow rate. A high pressure ensures an effective cleaning action, whereas a high flow rate enables the cleaning fluid to reach zones that are relatively far away from the dispensing point.
An object of the invention is to improve existing pumps and cleaning apparatuses.
A further object is to provide an axial piston pump in which the flow rate of the fluid processed by the pump is as constant as possible as the dispensing pressure increases.
In a first aspect of the invention, there is provided a pump comprising a plurality of pistons movable in a direction, a swash plate arrangement forming an angle with said direction so as to reciprocate said plurality of pistons in said direction, an elastic element interacting with said swash plate arrangement to enable said angle to be modified, wherein between said elastic element and said swash plate arrangement a transmission device is interposed for receiving a force from said swash plate arrangement and transmitting a fraction of said force to said elastic element.
Owing to this aspect of the invention, it is possible to obtain a pump in which, when pressure increases, the flow rate decreases only to a limited extent. The transmission device in fact enables only a fraction of the force exerted by the swash plate arrangement to be transmitted to the elastic element. This force depends on the thrust exerted on the swash plate arrangement by the pistons, i.e. on the pressure of the processed fluid. At a preset dispensing pressure selected by the user, the elastic element is thus less stressed than the elastic element disclosed in EP 1435457 and is able to keep the swash plate arrangement in a more inclined position, in which the pistons perform relatively long strokes. Thus, relatively high flow rates of fluid can be processed.
In a second aspect of the invention, there is provided a pump comprising a plurality of pistons movable in a direction, a swash plate arrangement forming an angle with said direction so as to reciprocate said plurality of pistons in said direction, said swash plate arrangement being oscillatable substantially around a point to modify said angle, wherein said swash plate arrangement is supported by a sliding element and a further sliding element movable along respective substantially rectilinear paths, said paths approximating to circumference arcs centred on said point.
Owing to this aspect of the invention, it is possible to obtain a pump provided with a swash plate arrangement oscillating around a substantially stationary point, which can be constructed in a relatively simple and economical manner. It is not constructionally complicated to provide a sliding element and a further sliding element that are movable along respective substantially rectilinear paths.
The invention will be better understood and carried out with reference to the attached drawings, which show an exemplifying and not restrictive embodiment thereof, in which:
With reference to
When the motor shaft rotates the plate 102, the pistons 103, by interacting with the inclined flat surface 104, which also rotates, reciprocate parallely to the longitudinal axis Z1. Thus the pistons 103 alternatingly penetrate inside the respective cylinders and subsequently exit from the cylinders, thereby pressurising the cleaning fluid and sending it from the intake conduit to the delivery conduit. The pump 101 further comprises an elastic element 105 interposed between the swash plate 102 and the support 107 to enable the flow rate of cleaning fluid to be varied depending on the dispensing pressure. The elastic element 105 may be a coil spring or a sleeve made of elastomeric material, extending around an axis Z2 that is substantially parallel to the longitudinal axis Z1.
During operation of the high-pressure cleaner, the user may select a desired dispensing pressure with which the cleaning fluid is dispensed on a surface to be cleaned, by means of a pressure-adjusting device arranged downstream of the pump 101. Thus the user selects the delivery pressure of the pump 101.
The swash plate 102 exerts on the elastic element 105 a force F1 that depends on the thrust exerted by the pistons 103 on the swash plate 102 and therefore on the delivery pressure that the cleaning fluid has to reach before leaving the cylinders of the pump 101. The force F1, as shown diagrammatically in
Tests have shown that in the known pump 101 the flow rate decreases very rapidly as the dispensing pressure selected by the user increases. When the dispensing pressure increases, the force F1 exerted by the swash plate 102 very rapidly compresses the elastic element 105 so that the swash plate 102 is positioned in its configuration of minimum inclination. In this configuration, the stroke of the pistons 103 is minimal and as a result the flow rate of processed fluid is rather limited.
In order to remedy the rapid decrease of flow rate that occurs in the pump according to EP 1435457 as the dispensing pressure increases, a pump 1 as shown in
Each piston 3 is bound at the bottom thereof by a rounded end 17 kept in contact with the annular plate 16 by a respective spring 18. In the embodiment of
As shown in
The transmission device further comprises a lever 24, having a first end pivoted on the first slide 19 and a second end pivoted on a second slide 25. The lever 24 extends along an inclined axis J that may oscillate inside a recess 26 obtained in the support 7.
The second slide 25 is slidable in a slide direction S owing to a guide surface 27 and to a further guide surface 28 that shapingly engage with corresponding surfaces obtained in a groove 29 of the support 7. The second slide 25 is provided, at an end opposite the lever 24, with an articulated joint 30 by means of which the second slide 25 is connected to the base 15 of the swash plate 2. The articulated joint 30 is associated with the swash plate 2 near the outer perimeter of the base 15.
A further articulated joint 31 is associated with the swash plate 2, the further articulated joint 31 being arranged in a position diametrically opposite the articulated joint 30. The further articulated joint 31 is obtained on a sliding block 32, slidable in a translation direction V along a track 33 obtained on the support 7, and shapingly engages with a cavity 34 obtained on the base 15.
When the pump 1 is mounted in a high-pressure cleaner, downstream of the pump 1 there is usually provided a pressure-adjusting mechanism of known type, by means of which a user can select the dispensing pressure with which a cleaning fluid processed by the pump 1 is dispensed onto a surface to be cleaned. The dispensing pressure selected by the user corresponds, apart from the pressure losses that occur in the connecting pipe between the pump 1 and the pressure-adjusting mechanism, to the delivery pressure of the pump 1, i.e. to the pressure of the cleaning fluid inside the cylinders 8 when the respective delivery valves are open.
If, starting from the configuration of
The force F applied by the swash plate 2 to the first slide 25 is directed parallely to the direction D along which the pistons 3 are movable, i.e. vertically in the example of FIGS. 4 to 7. The force F can be resolved into a first component Fs, directed in the slide direction S along which the second slide 25 is slidable, and into a second component FSP, perpendicular to the slide direction S. Whilst the first component Fs acts on the second slide 25, the second component FSP acts on the support 7. The first component Fs is then transmitted from the second slide 25 to the lever 24, and may in turn be resolved into a third component FJ directed along the inclined axis J of the lever 24, and into a fourth component FJP perpendicular to said axis. Only the third component FJ acts on the lever 24, which in turn transmits the third component FJ to the first slide 19. In particular, the third component FJ can be resolved, at the point in which the lever 24 is pivoted on the first slide 19, into a fifth component FK parallel to the line of action K and into a sixth component FKP perpendicular to said line of action. Whilst the sixth component FKP acts on the support 7, the fifth component FK is transmitted to the elastic element 5, which is compressed proportionally to the fifth component FK. Due to compression of the elastic element 5, the first slide 19 moves parallely to the line of action K and penetrates deeper inside the seat 23. Correspondingly, the lever 24 rotates around its fulcrum inside the recess 26, and the second slide 25 slides in the slide direction S inside the groove 29, thereby moving towards the recess 26, as shown in
It is noted that, at a constant dispensing pressure selected by the user, the flow rate decreases less than it did in known pumps of the type shown in
If the user further increases the dispensing pressure, the elastic element 5 is compressed more and more, as shown in
The elastic element 5 may be further compressed until it reaches the configuration shown in
If the user decreases the selected dispensing pressure, the force F exerted by the swash plate 2 on the second slide 25 decreases. As a result, the fifth component FK that acts on the elastic element 5 also decreases. The elastic element 5 is less compressed and, through the first slide 19 and the lever 24, pushes the second slide 25 towards the outside of the groove 29. Thus, the swash plate 2 inclines more, i.e. the angle of inclination β increases. As a result, the stroke of the pistons 3 increases and thus the flow rate of cleaning fluid processed by the pump 1 increases.
Tests have shown that, by using the transmission device of FIGS. 3 to 8, relatively high flow rates may be obtained with dispensing pressures up to about 40 bar. This constitutes a significant improvement over the prior art, in which the flow rate decreased significantly when the dispensing pressure exceeded 15-20 bar. This is visible in the graph of
The curve obtained by joining the points indicated by stars refers to a pump of the type disclosed in EP 1435457. This curve has a slope that is much greater than the slope of the curve relating to a pump having a swash plate of constant inclination. This means that the flow rate of fluid delivered by the pump of the type disclosed in EP 1435457 decreases very rapidly as the dispensing pressure increases, for the reasons that were set out previously. For example, at a dispensing pressure of 5 bar the pump dispenses a flow rate of 10.90 l/min, but at a pressure of 41 bar the flow rate has already decreased to 7.90 l/min, i.e. it has decreased by almost 30%.
The curve obtained by joining the triangles refers to a pump of the type disclosed with reference to FIGS. 3 to 8. This pump is so dimensioned that, at a relatively low dispensing pressure, the flow rate is almost the same as the initial flow rate of the pump disclosed in EP 1435457. In particular, a flow rate of 11.40 l/min corresponds to a dispensing pressure of 12.40 bar. It is noted that, in a wide range of dispensing pressure values, the curve has a very reduced slope, almost equal to the slope of the curve for pumps having a swash plate of constant inclination. Over this range the flow rate decreases very slowly as the dispensing pressure increases. For example, at 42 bar the flow rate is still 10.40 l/min, i.e. it has decreased by only about 14% compared with the initial value. At around 50 bar, the flow rate drops suddenly, and then starts decreasing slowly with a slope that is approximately equal to the slope of the curve relating to a pump having a swash plate of constant inclination.
In a pump as disclosed with reference to FIGS. 3 to 8 two distinct operating zones are thus identifiable. In a first zone, from 0 to about 40 bar, the pump is able to process high flow rates of fluid, that vary little as the dispensing pressure increases. A jet of cleaning fluid is thereby obtained that, owing to its high flow rate, has a good cleaning efficiency even far from the dispensing point. In a second zone, comprised between about 50 bar and the maximum dispensing pressure processed by the pump, the dispensing pressure of the cleaning fluid is very high, which means that it is possible to clean effectively the region in which the cleaning fluid is dispensed.
The curve identified by joining the rhombus refers to a pump of the kind disclosed in FIGS. 3 to 8, in which, however, certain geometrical parameters have been modified.
In particular, the pistons 3 have a diameter of 12 mm, whereas in the pump examined previously the pistons 3 had a diameter of 14 mm. By diminishing the diameter of the pistons and keeping other conditions unchanged, the flow rate of fluid processed by the pump obviously decreases. For example, the flow rate is equal to 8.80 l/min when the dispensing pressure is 7 bar. Nevertheless, the curve has the same shape as the curve relating to a pump with pistons diameter of 14 mm. In particular, when the dispensing pressure is equal to 44 bar, the flow rate is still equal to 8.10 l/min, i.e. it has decreased by less than 10% in relation to the initial value. This shows that the slow decrease in flow rate obtained by the pump of FIGS. 3 to 8 does not depend on a particular value of a single constructional parameter of the pump, but is rather due to the transmission device.
The transmission device may also have different geometry from the one disclosed so far. It is for example possible to use a lever mechanism different from that shown in FIGS. 4 to 8, or to interpose between the first slide and the second slide more than one lever, or again to modify the angle formed between the line of action K and the slide direction S. By varying the geometry of the transmission device, the fraction of force that is transmitted to the elastic element changes. Accordingly, when choosing the configuration of the transmission device, the fraction of force that it is desired to transmit to the elastic element has to be taken into account.
During operation of a theoretical pump, the point Q, which was previously defined as the point of intersection between the inclined axis X2 and the thrust plane 4, lies on the longitudinal axis X1. Whatever the inclination of the thrust plane 4, in a theoretical situation the point Q is in a stationary position along the longitudinal axis X1. To reproduce this theoretical situation in reality, it would be necessary to support the swash plate 2 so that it oscillates around a stationary point. The sliding block 32 and the second slide 25 should therefore be movable along respective circular paths, centred on a point lying on the longitudinal axis X1 and coinciding with the intersection between the inclined axis X2 and the thrust plane 4. To this end, the sliding block 32 and the second slide 25 should be provided with circular guides that would make the support 7, the sliding block 32 and the second slide 25 difficult to manufacture and would thus increase costs of the pump 1.
It has therefore been thought to adopt the arrangement shown schematically in
This Figure schematically shows the swash plate, the thrust plane of which has been indicated by 4′, in the position of minimum inclination, in which the angle of inclination is equal to βmin. In this position, the pivot at which the base 15 is pivoted on the second slide 25 is in a first position A1, whereas the further pivot at which the base 15 is pivoted on the sliding block 32 is in a further first position B1.
It is now supposed that the point of intersection between the thrust plane and the inclined axis X2 is kept in a stationary position Qteor along the longitudinal axis X1 and that the swash plate is oscillated around this point of intersection until the swash plate reaches the position of maximum inclination, in which the thrust plane is indicated by 4″ and the angle of inclination is equal to βmax.
When the swash plate moves from the position of minimum inclination to the position of maximum inclination, the pivot at which the base 15 is pivoted on the second slide 25 moves away from the longitudinal axis X1 until it reaches a second position A2, whereas the further pivot at which the base 15 is pivoted on the sliding block 32 moves closer to the longitudinal axis X1, until it reaches a further second position B2.
In a theoretical condition in which the point Q is perfectly stationary, the points A1, A2, B1 and B2 are on the same circumference centred on Q. To reproduce this condition with good accuracy, it was decided to move the second slide 25 and the sliding block 32 along respective rectilinear paths, which approximate to the circular path along which the second slide 25 and the sliding block 32 would move in the theoretical case. In other words, the circumference arc that joins the points A1 and A2 has been replaced by a rectilinear segment that is arranged in the slide direction S and approximates to said arc. The further circumference arc that joins the points B1 and B2 has been replaced by a further rectilinear segment arranged in the translation direction V and which approximates to said further arc. For example, the arc that joins the points A1 and A2 can be replaced by the segment A1-A2 or by a segment parallel to the chord A1-A2 but passing through the middle point of the corresponding arc. The further arc that joins the points B1 and B2 can be approximated according to similar methods.
By adopting these approximations, when the inclination of the swash plate 2 varies, the point Q of intersection between the thrust plane and the inclined axis X2 moves slightly away from the longitudinal axis X1. Nevertheless, tests have shown that by proceeding as described above, the point Q undergoes an insignificant displacement if compared with the dimensions of the swash plate 2. As shown in
An example of swash plate and transmission device dimensioned according to the criterion explained above is shown in
It has also been seen that when the dimensions shown in
The inclinations of the translation direction V and of the slide direction S indicated above are an example suitable for a pump having the dimensions shown in
Number | Date | Country | Kind |
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MO2004A000306 | Nov 2004 | IT | national |