Fluid operated pump

Field of the Invention

0001This invention relates to a pump for conveying a pumped fluid using a actuating fluid, the pump comprising a rigid outer casing defining an interior space, a tube structure accommodated in the interior space, the tube structure being flexible and substantially inelastic, the interior of the tube structure defining a pumping chamber for receiving pumped fluid, the tube structure being movable between laterally expanded and collapsed conditions for varying the volume of the Dumping chamber thereby to provide discharge and intake strokes, the region of the interior space surrounding the tube structure defining an actuating region for receiving and accommodating actuating fluid, the pumping chamber being adapted to receive pumped fluid to cause the tube structure to move towards the expanded condition and the pumping chamber thereby undergoing an intake stroke, the pumping chamber undergoing a discharge stroke upon collapsing of the tube structure in response to the action of actuating fluid in the actuating region.

Background Art

0002The invention has been devised particularly, although not necessarily solely, for dewatering underground mining operations. The invention is suited to applications where very high pressures are required to pump large volumes of soiled fluids. Typically, pressures in the ordered of 2500 m water head and flow rates in the order of 200 m3/hr can be achieved.

0003In dewatering of underground mining operations, the water is invariably contaminated with solids. Typically, piston plunger pumps or piston diaphragm pumps are used for the pumping process- <u>such pumps are for example disclosed in</u><patcit id="pcit0001" dnum="US2345693A"><text>US 2,345,693 (Wilson</text></patcit><u>)</u>. While piston pumps are effective in operation, they involve high capital costs and also high maintenance costs. The high maintenance costs arise due to the high wear rates, which result from, the arduous operating conditions of the pump valving systems which regulate the pumps intake and discharge strokes. Such systems involve pump-operating rates of some 60 to 80 cycles per minute. A further contributing factor to the high maintenance costs for piston plunger pumps is the aggressive action of the contaminated water on the reciprocating pistons and their seals.

0004Diaphragm pumps are not exposed to the same wear rates on the pistons and seals but nevertheless the valving systems are exposed to the same arduous conditions as diaphragm pumps also operate at some 60 to 80 cycles per minute.

0005There is a need for a pump which can operate at lower pumping rates and therefore be less arduous on valving associated with the pump. This requirement can be met by a collapsible chamber pump, which is a variation of a peristaltic pump. Such a pump utilises a flexible tube having a supply end and a discharge end, with a pumping chamber defined within the tube between the supply and discharge ends. Fluid pressure is employed to compress the tube, thereby urging a charge of the fluid within the pumping chamber towards the discharge end. Various proposals for such pumps are disclosed in <patcit id="pcit0002" dnum="US3406633A"><text>US 3,406, 633</text></patcit> (Schomburg), <patcit id="pcit0003" dnum="US4515536A"><text>US 4,515, 536</text></patcit> (van Os), <patcit id="pcit0004" dnum="US6345962A"><text>US 6,345, 962</text></patcit> (Sutter), <patcit id="pcit0005" dnum="GB2195149A"><text>GB 2195149</text></patcit> (SB Services (Pneumatics) Ltd), <patcit id="pcit0006" dnum="WO8201738A"><text>WO 82/01738</text></patcit> (RIHA), <patcit id="pcit0007" dnum="US4257751A"><text>US 4,257, 751</text></patcit> (Kofahl) and <patcit id="pcit0008" dnum="US4886432A"><text>US 4,886, 432</text></patcit> (Kimberlin).

0006Each of these proposals utilise a flexible tube which is elastic so that it is compressible to expel the charge of fluid therein and expandable to receive a further charge of pumped fluid into the flexible tube. Each of these proposals has limitations on the maximum pressure to which the device can operate. The limitation is a result of the maximum pressure differential the flexible tube can withstand if the tube is over-compressed by the pumping fluid. If over-compressed the tube will fail by rupturing at the outlet port.

0007It is against this background, and the deficiencies and problems associated therewith that the present invention has developed.

0008The reference to the abovementioned prior art is for the purposes of background only and is not, and should not be taken as, an acknowledgement or any form of suggestion that the prior art forms part of the general knowledge in Australia.

Disclosure of the Invention

0009According to a first aspect of the invention one end of the tube structure is closed and the other end is connected to a port through which pumped fluid can enter into and discharge from the pumping chamber as the pumping chamber performs intake and discharge strokes-, wherein the tube structure is movably supported to accommodate longitudinal extension and contraction of the tube structure.

0010Preferably, the tube structure is maintained in a taut condition between the ends thereof.

0011Preferably, the tube structure is supported at the closed end thereof.

0012Preferably, the closed end of the tube structure may be movably supported in any appropriate fashion such as by way of a spring mechanism.

0013Preferably the actuating region comprises an actuating annulus substantially surrounding the tube structure and an actuating chamber located at the closed end of the pump. Preferably the actuating annulus is in fluid communication with the actuating chamber.

0014Preferably the pump comprises means to bled fluid, such as air, therefrom.

0015Preferably the pump comprises separate means to bled air from the pumping chamber and from the actuating region, wherein the air is bled from the pumping chamber during the intake stroke and air is bled from the actuating region during the discharge stroke. The pump may also comprise a monitoring means to monitor the pump during the intake and discharge stroke.

0016Preferably the monitoring means monitors the condition of the tube structure.

0017According to one embodiment of the invention the monitoring means monitors, directly or indirectly, the position of the closed end of the tube structure. Hence, as the tube structure fills, the longitudinal length is caused to contract, resulting in the movable closed end moving towards the fixed open end of the tube structure.

0018According to another embodiment of the invention the monitoring means monitors the pressure differential between components of the pump.

0019Preferably the monitoring means at least indicates when the discharge and intake strokes have been completed.

0020According to a second aspect of the invention there is provided a pumping system comprising a pump in accordance with the first aspect of the invention, a delivery means for delivering pumped fluid to the pumping chamber in timed sequence for causing the pumping chamber to undergo an intake stroke, and means for supplying actuating fluid to the actuating region in timed sequence to cause the tube structure to laterally collapse whereby the pumping chamber undergoes a discharge stroke.

0021The delivery means may comprise a delivery pump.

0022Typically, the delivery means is only required to operate at a relatively low pressure in the sense that is only required to convey the pumped fluid into the interior of the tube structure to cause lateral expansion thereof and thereby performing an intake stroke of the pumping chamber.

0023The actuating fluid may be of any appropriate form, such as hydraulic oil or water.

0024In the case where the actuating fluid is hydraulic oil, the supply means preferably includes a hydraulic circuit incorporating a reservoir for hydraulic oil and a hydraulic pump. The hydraulic circuit also includes an intake and exit valve system for regulating the delivery of hydraulic oil into, and the discharge of hydraulic oil from, the actuating region in timed sequence.

0025In the case where the actuating fluid is water, the supply means may comprise a water reservoir at an elevated location in order to supply the water at the appropriate pressure head.

0026Preferably the delivery of the actuating fluid to the actuating region is at an opposed end to the port through which pumped fluid enters into and discharges from the pumping chamber. The outlet of the actuating fluid from the actuating region may also be at an opposed end to the port through which pumped fluid enters into and discharges from the pumping chamber.

0027The pumping system may comprise two pumps in accordance with the first aspect of the invention operating sequentially such that the pumping chamber of one pump performs a intake stroke while the pumping chamber of the other pump performs a discharge stroke, and vice versa.

0028Preferably the sequential operation of the two pumps is such that a generally uninterrupted supply of pumped fluid is expelled from the pumping system. This is in contrast to the prior art pumping systems which discharge a given volume of fluid from the flexible tube and then requires the tube to refill prior to subsequent displacements. This results in intermittent output flow of the device that is generally undesirable. When used in extreme high-pressure applications the intermittent output flow will give rise to shock waves (also known as hydraulic hammer) occurring in the outlet piping system. Intermittent flow in the outlet piping system will require the flow to repeatedly accelerate then decelerate resulting in energy consumption and hence inefficiency of the pumping system.

0029The duration of the discharge stroke may be longer than the duration of the intake stroke. Preferably one pump completes its intake stroke and commences its discharge stroke while the other pump is completing its discharge stroke.

0030Preferably the discharge stroke of one pump is completed by the time the discharge from the other pump is equal in flow to the desired flow of pump fluid from the pumping system.

0031Preferably, the two pumps have a common delivery means and a common supply means, with appropriate valve systems controlling the sequence of operation.

0032Preferably, the, or each pump is oriented so that the closed end of the tube structure is elevated in relation to the other end thereof. Preferably the delivery and exit of the actuating fluid to the actuating region is adjacent the closed end.

0033According to a fourth aspect of the invention there is provided a method of operating a pumping system in accordance with the second aspect of the invention wherein the actuating fluid may be of any appropriate form, such as hydraulic oil or water and wherein the duration of the discharge stroke of one pump is longer than the duration of the intake stroke of the other pump, and vice versa, whereby, when operated sequentially, the pumping system delivers a generally uninterrupted supply of fluid.

Brief Description of the Drawings

0034The invention will be better understood by reference to the following description of a specific embodiment thereof as shown in the accompanying drawings in which: <ul id="ul0001" list-style="none"><li><figref idref="f0001">Figure 1</figref> is schematic elevational view of a pumping system according to an embodiment;</li><li><figref idref="f0002">Figure 2</figref> is a fragmentary view of a pump of the pumping system shown in <figref idref="f0001">Figure 1</figref></li><li><figref idref="f0003 f0004 f0005 f0006 f0007 f0008 f0009 f0010 f0011 f0012 f0013">Figures 3 to 13</figref> are sequential views of the operation of the pumping system according to the embodiment shown in <figref idref="f0001">Figure 1</figref>;</li><li><figref idref="f0014">Figure 14</figref> is a side view of the closed end of a tube structure forming part of the pumping system, shown in a loaded (laterally expanded) condition;</li><li><figref idref="f0014">Figure 15</figref> is an end view of <figref idref="f0014">Figure 14</figref>;</li><li><figref idref="f0014">Figure 16</figref> is a side view of the closed end of the tube structure, shown in a relaxed (laterally collapsed) condition;</li><li><figref idref="f0014">Figure 17</figref> is an end view of <figref idref="f0014">Figure 16</figref>; and</li><li><figref idref="f0015">Figure 18</figref> is a table indicating the sequential operation of the pumping system in relation to <figref idref="f0003 f0004 f0005 f0006 f0007 f0008 f0009 f0010 f0011 f0012 f0013">figures 3 to 13</figref>.</li></ul>

Best Mode (s) for Carrying Out the Invention

0035Referring to <figref idref="f0001 f0002 f0003 f0004 f0005 f0006 f0007 f0008 f0009 f0010 f0011 f0012 f0013">Figures 1 to 13</figref>, there is shown a pumping system 1 suitable for transportation of contaminated water in continuous flow, at high pressure and at large flow rates. The contaminated water contains solids and so typically comprises a slurry. Accordingly, the contaminated water will hereafter be referred to as a slurry.

0036The pumping system 1 comprises two pumps 21,22 operable in timed sequence (as will be explained) in order to discharge slurry by way of a discharge pipeline 56.

0037Referring to <figref idref="f0002">figure 2</figref>, each pump 21,22 comprise a rigid outer casing 25 which is of cylindrical construction and which defines an interior space 26. Each casing 25 has a longitudinal axis inclined to the horizontal such that one end thereof is elevated in relation to the other. A first end plate 34 is mounted on the upper end of the casing 25 and a second end plate 23 is mounted on the lower end thereof.

0038A flexible tube structure 27 is accommodated in the interior space 26 within the outer casing 25 and is supported in a longitudinally taut condition. The flexible tube structure 27 is flexible yet substantially inelastic. The tube structure is substantially inelastic in the sense it does not have a memory tending to cause it to return to a particular state after being deflected therefrom and has tensile strength thereby limiting the elastic stretch of the tube.

0039The interior of the tube structure 27 defines a pumping chamber 28. Because of its flexible nature, the tube structure 27 is movable between laterally collapsed and expanded conditions for varying the volume of the pumping chamber 28.

0040With this arrangement, the pumping chamber 28 can perform intake and discharge strokes.

0041In the laterally collapsed condition, the tube structure 27 is relaxed and essentially collapsed upon itself, apart from the ends thereof which are supported in a manner to be explained later. In the laterally expanded condition, the tube structure 27 is inflated and stresses develop in the tube wall. This results in some longitudinal contraction or shortening of the tube structure, as will be described in more detail later.

0042One end of the tube structure 27 is supported on the lower end plate 23. Specifically, the lower end plate 23 incorporates an opening which defines a port 42 through which slurry undergoing pumping can enter and leave the pumping chamber 28 defined within the tube structure 27. The end plate 23 incorporates a sleeve section 24 onto which the end of the tube structure 27 is sealingly engaged.

0043The other end of the tube structure 27 is attached to a movable support. The movable support comprises a cylindrical rigid end fitting 29, an end wall section 31 and a conical inner profile section 30. The end of the tube structure 27 is sealingly fitted onto the cylindrical rigid end fitting 29. The end wall section 31 is supported on a tubular rod 32 which extends through an opening 38 in the upper end plate 34. The tubular rod 32 is sealingly and slidingly supported in the end plate 34. The outer end section of the tubular rod 32 is fitted with a collar 36, with a compression spring 35 acting between the collar 36 and the outer face of the end plate 34. With this arrangement, the compression spring 35 urges the tubular rod 32 outwardly and thus the end fitting 29 is urged towards the end plate 34.

0044This arrangement movably supports the upper end of the tube structure 27 and accommodates longitudinal extension and contraction of the tube structure as will be explained later. Additionally, it assists in maintaining the tube structure 27 in the longitudinally taut condition.

0045The region of the interior space 26 surrounding the tube structure 27, and internal of the rigid outer casing 25, defines an actuating annulus 41 for receiving an actuating fluid. The region external of the circular end wall 31 and internal of the end plate 34 defines an actuating chamber 40 for receiving the actuating fluid, the actuating chamber 40 being in fluid communication with the actuating annulus 41 to provide the actuating region.

0046Upon commencement, and during the discharge stroke, the actuating fluid enters the actuating chamber 40 via port 39 before passing into the actuating annulus 41. Port 39 is connected to the upper end of outer casing 25 so that the flow of actuating fluid, when entering the actuating chamber 40, is not directly inline with the tube structure 27 and therefore does not impinge thereagainst.

0047Upon commencement, and during the intake stroke, the actuating fluid passes through the actuating annulus 41 into the actuating chamber 40 before exiting via port 33. Port 33 is connected to the upper end of the outer casing 25 and in the upper most elevated position. This configuration allows for entrapped air to be dispelled from the actuating chamber 40 upon discharge of the actuating fluid.

0048Referring to <figref idref="f0001">figure 1</figref>, the pumping system 1 further includes a delivery means 50 for delivering slurry to the pumping chambers 28 in timed sequence as will be explained. The delivery means 50 communicates with a slurry reservoir 51, and includes a priming pump 52 and a delivery line 53 which extends from the priming pump 52 and which branches into two delivery branch lines 54,55. Specifically, each delivery branch line 54,55 communicates with a respective pumping chamber 28 of the respective pump via port 42. An inlet check valve 61,63 in each respective branch line 54,55 controls the flow direction of slurry along the branch line.

0049Each port 42 also communicates with the discharge pipeline 56 by way of a respective discharge branch line 57,58. Each respective discharge branch line 57,58 includes an outlet check valve 62,64 for controlling the flow direction of discharging slurry along the branch line.

0050A supply means 70 is also provided for supplying actuating fluid to each actuating chamber 40 in-timed sequence.

0051In this embodiment, the actuating fluid is hydraulic oil and the supply means 70 comprises a hydraulic circuit communicating with the actuating chamber 40 of each pump 21,22. The supply means 70 includes a reservoir 71 for hydraulic oil and an electric motor driven hydraulic pump 72 for delivery of hydraulic oil under pressure along branch lines 75,76 to the actuating chambers 40. Hydraulic valves 73,74 enable relief pressure flow in respective branch lines 75,76 back to the reservoir 71.

0052The actuating chamber 40 of each pump 21,22 communicates with branch lines 75,76 by way of transfer lines 77,78 connected between the respective branch lines 75,76 and the port 39.

0053Branch line 76 incorporates a precharge inlet valve 81 associated with pump 22, and a precharge inlet valve 84 associated with pump 21. Branch line 75 incorporates a supply inlet valve 82 associated with pump 22 and a supply inlet valve 85 associated with pump 21.

0054The supply means 70 also comprises return pipeline 95.

0055Return pipeline 95 is in communication with ports 33 on each pump 21,22 and incorporate discharge valve 86 associated with pump 21 and discharge valve 83 associated with pump 22.

0056Valves 81 to 86 are adapted to operate in timed sequence under the control of a control system (not shown). Typically, the valves 81 to 86 are operable in response to electrical signals from the control system.

0057While operation of the valves 81 to 86 is controlled in timed sequence by the control system, it should be noted that valves 61-64 associated with slurry intake into, and discharge from, the pumping chambers 28 are simply check valves which respond to fluid pressures.

0058As alluded to above, a charge of slurry is expelled from each pumping chamber 28 under the influence of a charge of hydraulic oil entering the surrounding actuating annulus 41 and actuating chamber, 40. The charge of hydraulic oil is spent at the completion of the discharge stroke. The spent charge of hydraulic oil is subsequently expelled from the actuating annulus 41 and actuating chamber 40 by inflation of the tube structure 27 during the next intake stroke of the pumping chamber 28. This sequence is of course controlled by timed actuation of the control valves 81 to 86. Specifically, a discharge stroke for each respective pump 21,22 is performed when the respective inlet valve 82,85 is open and the respective outlet valve 83,86 is closed. Similarly, an intake stroke is performed when the respective outlet valve 83,86 is open and the respective inlet valve 82, 85 is closed. The respective outlet valve 83,86 is open to allow expulsion of the actuating fluid and allow space for the tube structure 27 to move to its expanded condition upon intake of slurry.

0059To ensure satisfactory operation of the pump, air must be bled from both the actuating annulus 41 and actuating chamber 40, as well as the pumping chamber 28. Port 33 is located at the upper most point of actuating chamber 40 and will discharge air entrapped in the actuating annulus 41 and actuating chamber 40 in each pump 21,22 when respective control valve 83,86 is opened as described prior. Whereas air entrapped in the respective pumping chamber 28 is exited through port 37.

0060As can be seen in <figref idref="f0002">figure 2</figref>, port 37 is connected to the pump chamber 28 by the hollow tubular rod 32. Conical inner profile section 30 guides entrapped air in the pumping chamber 28 to the hollow tubular rod 32. When an outlet valve 65 in communication with the tubular rod 32 is open and the pumping chamber 28 is caused to fill with slurry during the intake stroke, slurry will flow out through the hollow tubular rod 32 thus forcing entrapped air to be expelled from the pumping chamber 28.

0061It is to be understood that the expulsion of entrapped air from the pumping chamber 18 may be through a variety of other means such as via a bled tube position at the most elevated position of the tube structure 27.

0062Operation of the pumping system 1 according to the first embodiment will now be described. The operating sequence is tabulated in <figref idref="f0015">figure 18</figref>.

0063At the commencement of a pumping operation using the pumping system 1, it is necessary to prime both pumps 21,22 so that the pumping chamber 28 of each pump is fully loaded with slurry, as shown in <figref idref="f0003">figures 3</figref> and <figref idref="f0004">4</figref>.

0064The control system is then operated to deliver hydraulic oil to the actuating chamber 40 of pump 22. As the hydraulic oil fills the actuating chamber 40 and actuating annulus 41 of pump 22, it causes the tube structure 27 exposed to the actuating fluid to, expell slurry contained therein through the port 42, along the discharge branch line 57 to pipeline 56, as shown in <figref idref="f0005">figures 5</figref> and <figref idref="f0006">6</figref>. Near the completion of the discharge stroke of the pump 22, pump 21 commences its discharge stroke, as shown in <figref idref="f0007">figure 7</figref>. Constant pressure is achieved by simultaneously discharging both pumps 22,21 for a momentary time, thereby ensuring constant flow of the slurry though delivery pipeline 56 is maintained during transition between pumps 21,22. Having established a smooth transition between pumps 21,22 the discharge stroke of pump 22 finishes followed by the commencement of its intake stroke, as shown in <figref idref="f0008">figure 8</figref>.

0065During the intake stroke, the slurry is delivered to the pump 22 by way of the delivery means 50. The cycle then repeats, as shown in <figref idref="f0009 f0010 f0011 f0012 f0013">figures 9-13</figref>, so that slurry is continuously pumped through the discharge pipeline 56 by the two pumps 21,22 operating in timed sequence, such that a constant flow is delivered by the pumping system 1-.

0066In order for there to be a substantially un-interrupted delivery of pumped slurry to the discharge pipeline 56, it is necessary that the time taken to perform the intake stroke be quicker than the time allowed for the discharge stroke. This provides time necessary for the operation of the various control valves in the change-oversequence from one pump to the other.

0067At the commencement of each pump stroke, the actuating annulus 41 and actuating chamber 40 of one pump is pressurised to the same pressure as the actuating annulus 41 and actuating chamber 40 of the other pump (which is nearing the end of its discharge stroke). If the actuating annulus 41 and actuating chamber 40 of the pump about to commence its discharge stroke is not so pressurised prior to commencement of its discharge stroke, there will be a pressure loss that will disrupt continuous delivery to the discharge pipeline 56.

0068During operation of the pumping system 1, it is most important to ensure that each pumping chamber 28 is fully filled with slurry prior to commencement of its pumping stroke. Without this requirement being satisfied, the tube structure 27 could ultimately be damaged after repeated discharge strokes within the respective pumping chamber 28. This could, for example, lead to the tube structure 27 being forced through the port 42.

0069In the event of excessive discharge from the tube structure 27, the tube structure will shorten in length as the volume of the pumping chamber 28 is decreased by the discharge of slurry, and given that the tube structure 27 is substantially inelastic. The movable support assembly, tubular rod 32 and spring 35 accommodate the shortening of the tube structure 27. The extent of the shortening can be measured, for example with reference to movement of the tubular rod 32. This can then be used to provide a signal indicating that the tube structure is fully discharged, that is, when the tubular rod 32 is in its inner most position the discharge stroke is complete.

0070There are various ways in which operation of the pumping system can be monitored to ensure that each pumping chamber 28 is filling correctly prior to commencement of a discharge stroke. One-way would involve monitoring the pressure differential existing between the actuating chamber 40 and the pumping chamber 28. By way of explanation, when slurry is entering one of the pumping chambers 28 through the respective port 42, actuating fluid is being discharged from the actuating chamber 40. In other words, the respective outlet control valve 83,86 in the hydraulic circuit associated with that particular actuating chamber 40 is open to allow the expulsion of the actuating fluid. As there is minimal backpressure in the actuating chamber 40 (because the outlet valve 83,86 is open), the slurry can inflate the tube structure 27 as the actuating fluid is expelled. When the tube structure 27 is fully loaded, the delivery means 50 continues to apply pressure to the tube structure 27, with the pressure being absorbed by the tensile properties of the tube structure 27. The internal pressure within the tube structure 27 causes the tube structure 27 to become tight and so assume its maximum possible inflated condition. As the outlet valve 83,86 from the actuating chamber 40 is still open when the tube structure 27 is in this condition, there will be no pressure exerted on the actuating fluid remaining in the actuating chamber 40 (as the tube structure 27 can expand no further). Consequently, there is a pressure differential which can be detected and thereby used to provide an indication that the pumping chamber 28 is fully loaded.

0071Another detection system may utilise the shortening effect of each tube structure 27 when it moves from a relaxed condition to a fully loaded condition. The shortening effect can be seen with reference to <figref idref="f0014">Figures 14-17</figref> of the drawings.

0072<figref idref="f0014">Figures 14 and 15</figref> illustrate the closed end section of the tube structure 27 when it is fully loaded. As can be seen with reference to <figref idref="f0014">Figures 16</figref> and17, when the tube structure 27 is in a relaxed state, the radial expansion shown at 91 of the tube structure leads to longitudinal contraction, as shown at 90, with the result that there is an overall shortening of the tube structure 27. The shortening of the tube structure 27 is accommodated by the movable support assembly, tubular rod 32 and spring 35. The extent of the shortening can be measured, for example with reference to movement of the tubular rod 32. This can then be used to provide a signal indicating that the pumping chamber 28 is fully loaded, that is, when the tubular rod 32 is in its inner most position.

0073It should be understood that the end of the tubular structure 27 can be closed in any appropriate way.

0074The inclination of the pumps 21,22 is so selected that if settlement of solid particles within the slurry were to occur while the slurry is within the pumping chamber 28, the settled particles will accumulate at the lower end of the pumping chamber 28 adjacent the port 42. The settled particles are then collected and discharged by the outgoing slurry charge during the next discharge stroke as a result of the higher velocity flow which exists at the outlet port 42.

0075From the foregoing, it is evident that the present invention provides a simple yet highly effective pumping system which can pump fluids at high pressure in a uniform flow regime. The pump system 1 can operate at relatively slow pumping cycles in comparison to the high operating cycles of conventional reciprocating piston type pumps and as such valve systems used in the pump system are operating under less arduous conditions. By way of example, each pump 21,22 within the pump system 1 can operate at a rate of about 2 to 4 cycles per minute which is significantly lower than the usual rate of 60 to 80 cycles per minute for conventional piston type pumps used in industrial environments.

0076It should be appreciated that the scope of the invention is not limited to the scope of the embodiment described. In this regard, it should be understood that a pumping system according to the invention may have applications in various areas where fluid pumping is required.

0077Further, it should be understood that while the pump system 1 according to the embodiment utilises two pumps 21,22 operating in timed sequence, there may be applications where only one pump is required (where intermittent discharge flow is acceptable), or alternatively there may be applications where it is possible to use a series of more than two pumps operating in sequence.

0078Improvements and modifications may be incorporated without departing from the scope of the invention, which is defined by the appended claims.

0079Throughout the specification, unless the context requires otherwise, the word "comprise"or variations such as"comprises"or"comprising", will be understood to imply the inclusion of a stated integer or group of integers but not the exclusion of any other integer or group of integers.