Self-priming centrifugal pump

Abstract: The present invention relates to a self-priming centrifugal pump (1) which comprises a stator case (2) with a delivery port (5) and an outflow port and a radial-centrifugal bladed impeller (7). An ejector (16) is provided inside the case (2) and comprises an induction chamber which is connected to the intake port (3), an entrainment nozzle (17) connected to the internal chamber of the stator case and a diffusion duct (19) which is coaxial to the impeller (7) and is connected to its inflow section. A conveyor is provided after the impeller and comprises at least one radial-centripetal conveyance channel (24) and an annular outflow section which extends peripherally to the diffusion duct of the ejector. The conveyor (24) has a configuration which is suitable for directing the flow which leaves the impeller toward a central portion of the case which is adjacent to the outer portion of the diffusion duct (19) and is distant from the delivery port (5), and for making said flow laminar so as to facilitate the separation of air and its migration toward the delivery port (5).

Description: The present invention relates to a self-priming centrifugal pump particularly of the kind with built-in ejector. Self-priming pumps of this type, generally termed "jet pumps", comprise, inside the pump casing, an ejector which is connected to the intake port on one side and to the inlet of the impeller on the other. As is known, the impeller of said pumps must generate a total flow Q which is expressed by the formula: Q = Q₁ + Q₂ where Q₁ indicates the useful flow delivered by the pump and Q₂ indicates the partial flow which flows through the ejection nozzle. The flow Q₂, on the basis of the known operating principles of ejectors, draws into to the ejector's negative-pressure chamber a flow Q₁ which arrives from the intake port. Said flow Q₁ mixes in the diffusion duct of the ejector with the flow Q₂ and is then conveyed toward the inlet of the impeller to be subsequently recirculated within the case. The method of operation of said self-priming pumps is as follows. Initially, the case of the pump must be entirely filled with liquid up to the coupling to the intake port which is located above the axis of the impeller. In this manner the ejector is also completely filled with liquid to be pumped. When the pump is started, the impeller imparts a vorticose motion to the liquid, forming a mixture of air and liquid which is discharged into the upper portion of the case, where the separation of the air can occur at low speeds. The separated air partially flows to the delivery port and is partly entrained with the liquid toward the ejection nozzle, where it gradually draws more liquid toward the inlet of the impeller. The recirculation of the air/liquid mixture continues until all the air is eliminated, after which the normal operation of the pump can begin. By means of such a pump-ejector combination as disclosed in US-A-2 631 539 it is possible to automatically prime the system, lifting fluids even from considerable depths, up to approximately 9 meters and over. Said devices, however, are not free from disadvantages, including most of all long priming times and low efficiency in normal running conditions. It has been experimentally demonstrated that the longer priming times correspond to conditions of greater turbulence of the air/liquid mixture which leaves the impeller. Said priming times are also further increased if the flow of the air/liquid mixture is proximate to the delivery port, so as to prevent the separation of air from the mixture and reduce the efficiency of the ejector. Therefore, in order to reduce priming times and increase the overall efficiency of the pump, it is necessary to carefully study the conditions of outflow at the outlet of the impeller and its re-conveyance toward the ejector. Document US-A-2 941 474 discloses, a self-priming ejector pump in accordance with the preamble of Claim 1 in which the flow leaving the impeller, initially guided by an annular diffuser, is subsequently conveyed toward an essentially frustum-shaped interspace and finally discharged through an annular outlet extending peripherally of the axial ejector. The fluid entering the internal chamber of the case has a very high turbolence that does not favor separation of air and its migration toward the discharge port. The self-priming jet pump known from EP-A-0 323 384 has a frustum-shaped interspace that is provided with deflector blade which is connected to one of the front chambers of the annular diffuser and with an arc-like outlet slot. The priming times of said pump are considerably reduced dawn to 5-6 minutes; however, the efficiency of the pump-ejector assembly in normal running conditions is still not adequate. This is due to the fact that the outflow of the mixture through the arc-like slot is still predominantly turbulent and does not ensure a uniform feeding of the ejection nozzle. The Italian application n. 85644A88 describes a jet pump in which the conventional radial diffuser is replaced with an axial diffuser and in which the turbolence of the fluid is only partially eliminated. This pump has a lower efficiency than it would have if it incorporated a radial diffuser. The aim of the present invention is indeed to eliminate, or at least reduce, the disadvantages described above, by providing a self-priming centrifugal pump with built-in ejector which allows to drastically reduce priming times by means of a simple and economical solution. Within the scope of the above described aim, a particular object of the present invention is to provide a conveyance of the fluid which leaves the impeller in substantially laminar conditions, so as to allow an effective separation of the air mixed with the liquid during priming and facilitate its migration toward the delivery port. A further object of the present invention is to provide a conveyance device which reduces fluidodynamic losses during the priming period and in normal running conditions. Not least object of the invention is to obtain a centrifugal pump which is highly reliable and has reduced maintenance costs, in order to make the assembly rational and advantageous from a merely economical point of view. This aim, these objects and others which will become apparent hereinafter are achieved by a self-priming centrifugal pump according to the accompanying claim 1. Further characteristics and advantages of the invention will become apparent from the description of two preferred but not exclusive embodiments of the self-priming centrifugal pump according to the invention, illustrated only by way of non-limitative example in the accompanying drawings, wherein: figure 1 is a partially sectional side view of a first embodiment according to the invention; figure 2 is a sectional and partially exploded front view of the device of figure 1, taken along the line II-II; figure 3 is a partially sectional side view of a second embodiment of the pump according to the invention; figure 4 is a partially sectional side view of an embodiment of the pump according to the invention which is similar to that of figure 3 in the case of a double impeller. With reference to figures 1 and 2, the pump according to the invention, generally indicated by the reference numeral 1, comprises a casing or stator case 2 which has an essentially cylindrical shape and is provided with an intake port 3 defined on the front wall 4 and with a delivery port 5 arranged on the cylindrical side wall 6 in an upward position. Both ports 3 and 5 have couplings for connection to external channels, not illustrated, and are arranged above the axis of the case. Plugs for filling and draining liquid are furthermore provided and are engaged in appropriate threaded cavities of the case. The case 2 internally supports an impeller 7 which is keyed on a shaft 8 which is driven by the electric motor 9. The impeller 7, which has a per se known shape, has a hub 10, a crown 11 and a plurality of radial-centrifugal blades 12 with an appropriate profile. An inlet section 13 and an outlet section 14 are defined at the ends of the set of blades of the impeller 7 and determine the direction of flow during the rotation of the impeller. An ejector, generally indicated by the reference numeral 16, is arranged in the internal chamber 15 of the stator case 2 and comprises an entrainment nozzle 17 which is traversed by the recirculation flow Q₂, a chamber 18 connected to the intake port 3 for drawing the useful flow Q₁, and a diffusion duct 19 in which the flows Q₁ and Q₂ are mixed and are subsequently conveyed through a divergent section 20 which is adjacent to the inlet of the impeller 7. After the outlet section 14 of the impeller 7 there is a diffuser 21 which is fixed to the case 2 and has blades 22 of a per se known shape. Re-conveyance chambers 23 are furthermore provided and direct the flow leaving the diffuser toward the internal chamber 15 of the case. According to a peculiar characteristic of the invention, after the impeller 7 and the diffuser 21 there is a radial-centripetal conveyor, generally indicated by the reference numeral 24, which has an annular outlet section which extends peripherally to the diffusion duct of the ejector 17. In particular, the radial-centripetal conveyor 24 is formed by a pair of walls 25, 26 which are approximately parallel to the crown 11 of the impeller 7 and define between one another a substantially annular or torus-like interspace which is suitable for conveying the fluid which leaves the impeller partially toward the center of the case 2. Inside said interspace there is a plurality of straightening blades 27 of appropriate profile which determine a plurality of conveyance channels 28 with an approximately constant transverse cross section. The conveyance channels 28 have an end portion which is substantially parallel to the diffusion duct 19 of the ejector, with a transverse annular outlet section 29 which is substantially perpendicular to the axis of the impeller. The inner walls of the conveyance channels, particularly at the inlet and outlet portions, are accurately blended so that the outflowing liquid is as regularized as possible and approximately laminar, creating a roughly tubular fluid nappe which aids the separation of the air contained in the fluid mixture accelerated by the impeller and facilitates the migration of air toward the delivery port. The laminar outflow conditions furthermore facilitate the recirculation of the flow Q₂ toward the ejection nozzle 17, increasing the efficiency of the ejector and consequently the flow Q₂ of the drawn liquid. This leads to a significant reduction in priming times, which by means of tests have been found to be comprised between 3.5 and 4.5 minutes. The efficiency of the pump in normal running conditions is furthermore also considerably increased up to 0.30-0.35. Figures 3 and 4 illustrate a second embodiment of the pump according to the invention, wherein, differently from the first embodiment, the annular diffuser is not provided at the output of the impeller. In particular, figure 3 illustrates a single-stage pump and figure 4 illustrates a two-stage pump with double impeller. By analogy, the component elements which are identical to those of the first embodiment have been identified by the same reference numerals followed by a prime. The centripetal radial conveyor 24′ of figure 3 is formed by the walls 25′, 26′ and by the straightening blades 27′ which define the conveyance channels 28′. The outflow cross section 29′ of the conveyor has an annular shape and is arranged peripherally to the outer portion of the diffusion duct 19′ of the ejector 16′. At the output of the impeller 7′, or of the impeller 7″, the flow is deflected toward the conveyor 24′ through a plurality of re-conveyance channels which comprise a series of radial-centripetal channels 30, a first axial annular duct 31, adjacent to the hub 11′ of the impeller 7′, an annular radial-centripetal duct 32 which extends parallel to the series of channels 30, and a second peripheral axial annular duct 33 which is connected to the conveyance channels 28′. By means of this succession of re-conveyance channels, the flow is guided through the channels 28′ of the conveyor 24′ and is directed into the inner chamber 15′ of the case 2′. In this case, too, the total flow rate Q produced by the impeller 3′ is conveyed toward the central portion of the case adjacent to the outer wall of the diffusion duct 19′, in a position which is sufficiently distant from the delivery port 5′ to facilitate the separation and migration of air toward the delivery port 5′. From the constructive point of view, the conveyors 24, 24′ can be provided by means of the same materials used for the stator case of the pump or of the ejector and can be applied to, or provided monolithically with, one of the fixed components of the pump casing. The shape and number of the straightening blades 27, 27′ can be determined by means of the conventional calculation processes for re-conveyance ducts arranged after diffusers, typical of multi-stage centrifugal pumps. In particular, the angles of radial divergence must be concordant with those of the impeller at the inflow and nil at the outflow; the number of blades or chambers may be conveniently comprised between 3 and 10 and is preferably equal to 5. In practice it has been observed that the self-priming centrifugal pump according to the invention fully achieves the intended aim since it allows a drastic reduction of priming times and the obtainment of high operating efficiencies in normal running conditions. The self-priming centrifugal pump according to the invention is susceptible to numerous modifications and variations, all of which are within the scope of the inventive concept defined in the accompanying claims; all the details may furthermore be replaced with technically equivalent elements. In practice, the materials employed, so long as compatible with the specified use, as well as the dimensions and shapes, may be any according to the requirements and the state of the art. WHERE TECHNICAL FEATURES MENTIONED IN ANY CLAIM ARE FOLLOWED BY REFERENCE SIGNS, THOSE REFERENCE SIGNS HAVE BEEN INCLUDED FOR THE SOLE PURPOSE OF INCREASING THE INTELLIGIBILITY OF THE CLAIMS

Claims: Self-priming centrifugal pump, comprising: a case (2) having an internal chamber (15) delimited by a substantially cylindrical lateral wall (6) and a front wall (4); at least one bladed impeller (7) of the radial centrifugal type rotatably supported within said internal chamber (15), said at least one impeller (7) having a hub (10) and a crown (11); an intake port (3) and a delivery port (5) respectively arranged on said front wall (4) and said lateral wall (6) above the impeller axis; an ejector (16) arranged inside said case (2) and having a drawing chamber (18) connected to said intake port (3), an entrainment nozzle (17) communicating with said internal chamber (15) and a diffusion duct (19) coaxial to said impeller (7) and connected to the inlet thereof; a conveyor (24) for directing the flow induced by said impeller toward a central portion of said internal chamber (15), said conveyor having an annular outflow section (29) which extends peripherally of said diffusion duct (19) of said ejector (16); a radial diffuser (21) interposed between said impeller (7) and said conveyor (24); characterized in that said conveyor comprises at least one substantially radial conveyance channel (28), said radial diffuser (21) having outlet sections (23) which coincide with the inlet section of said at least one radial conveyance channel (28), said conveyor (24) being no axial-type diffuser, the end portion of said conveyor (24) being at least partially parallel to said diffusion duct (19) so as to direct the fluid adjacent to the outer periphery of said diffusion duct under substantially laminar flow condition to thereby facilitate separation of air and migration thereof toward said delivery port (5). Self-priming centrifugal pump according to Claim 1, characterized in that said conveyor (24) comprises at least one pair of substantially trunco-conical walls (25, 26) which are mutually spaced apart and substantially parallel to the crown (11) of said impeller so as to define an annular interspace at least partially facing said radial diffuser (21), and a plurality of straightening blades (27) extending within said annular interspace from the oulet sections of said radial impeller (7) to the annular outflow section (29) of said conveyor (24) to define a plurality of radial-centripetal conveyance channels (28). Self-priming centrifugal pump according to Claim 2, characterized in that said straightening blades (27) have an angle of radial divergence which is concordant with that of the blades of said impeller (7) and in that the number of said blades (27) is comprised between 3 and 10, and is preferably equal to 5. Self-priming centrifugal pump according to one or more of the preceding claims, characterized in that said conveyor (24) has inner surfaces which are carefully blended so as to minimize losses due to friction and separation of boundary layer. Self-priming centrifugal pump according to one or more of the preceding claims, characterized in that a plurality of serially connected reconveyance ducts (28') is arranged between said at least one impeller (7, 7') and said conveyor (24'). Self-priming centrifugal pump according to Claim 5, characterized in that, said serially connected reconveyance ducts (28') comprise, sequentially in the flow direction, a series of radial centripetal ducts (30) extending adjacent to the hub (10) of said at least one impeller (7, 7'), a first axial annular duct (31) extending peripherally to said hub (10) and directed away from the suction side of the pump, a radial-centrifugal duct (32) which is substantially parallel to said series of radial-centripetal ducts, a second annular duct (33) arranged peripherally to said at least one impeller (7, 7'), directed toward the suction side of the pump and connected to said conveyor (24'). Self-priming centrifugal pump according to one or more of the preceding claims, characterized in that the transverse cross section of said conveyance channels (28, 28') is substantially constant. Self-priming centrifugal pump according to one or more of the preceding claims, characterized in that the transverse cross section of said conveyance channels (28, 28') gradually decreases with continuity.

Inventors: CAODURO BRUNO, CAODURO, BRUNO
Applicants: EBARA CORP, EBARA CORPORATION
Application year: 1990
Main classification: F04D9
IPC codes: F04D29, F04D9