This application is a U.S. National Stage application of International Application No. PCT/EP2015/065355, filed Jul. 6, 2015, which claims priority to EP Application No. 14190157.9, filed Oct. 23, 2014 the contents of each of which is hereby incorporated herein by reference.
Field of Invention
The present invention relates to a method of pumping a liquid medium by a centrifugal pump, a centrifugal pump and an impeller therefor. The present invention relates especially to modifying an impeller of a centrifugal pump in such a way that the pump may be used without risk of damaging a shaft seal or like when pumping of both clean liquids and liquids containing solids, like, for instance, fibrous suspensions.
Background Information
It is already known that, when pumping liquid or a suspension by a centrifugal pump, liquid is entrained into a space behind the impeller of the centrifugal pump when working vanes of the impeller increase the pressure of the liquid while pumping such from in front of the impeller to the volute radially outside the impeller. While increasing the fluid pressure in the volute, the rotating impeller creates suction in the impeller eye tending to move the impeller towards the pump inlet. At the same time, the liquid to be pumped in addition to being discharged to the pressure outlet of the pump also tends to fill the space behind the impeller. Although the liquid between the impeller and the rear wall of the pump rotates, on the average, half the speed of the impeller (provided that there are no so called rear vanes or like ribs on the rear face of the impeller hub or shroud; the relatively thin mainly radially oriented disc-like part extending from the hub is called a shroud) and thus, while generating centrifugal force, reduces to a certain extent the pressure prevailing in the sealing space behind the impeller in the area of the shaft of the pump, a considerable pressure, however, naturally affects in the space behind the impeller. Thus, both the negative pressure, or suction created by the working vanes and the fluid pressure behind the impeller shroud subject the bearings of the pump shaft to a force directed towards the inlet of the pump. Partially, therefore, so called rear vanes have been arranged on the rear face of the impeller shroud, which rear vanes pump the liquid having entered the space outwards, whereby the pressure in the space behind the impeller is substantially decreased. In other words, the rear vanes are used for reducing the axial force the impeller subjects to the shaft of the pump by drawing the shaft towards the inlet of the pump. Thus, the rear vanes are needed in a semi-open impeller to have pressure distribution at both sides, i.e. the front side and the rear side, of the shroud as equal as possible.
The rear vanes may, however, be dimensioned so that they operate optimally only in a certain capacity range of the pump, whereby deviation in either direction from the capacity range results in that the pressure prevailing within the area of the rear vanes and also in the shaft seal space changes. If the output of the pump is increased, the rear vanes generate, in the worst case scenario, a negative pressure, which can, at its worst, also make the liquid in the shaft seal space boil, especially when pumping liquids at a higher temperature. Correspondingly, when decreasing the capacity, for example, by constricting such by a valve, the pressure behind the impeller increases and the stresses increase. At the same time, naturally also the stress on the bearings increases.
Another problem involved in centrifugal pumps is the heat generated at the shaft sealing of the pump. The shaft sealing, in practice irrespective of its type, generates heat that has to be conveyed out of the sealing. Normally, the liquid to be pumped is used to flush the sealing and convey excess heat away. If the sealing starts running hot, the sealing elements may deteriorate either directly by the heat itself or by the liquid present in the sealing cavity boiling, i.e. evaporating, whereafter the sealing starts running dry.
For affecting the above discussed problems the use of balancing holes are suggested. The balancing holes are arranged to run through the hub or shroud. The holes have traditionally been cylindrical, i.e. they have had a linear axis and a constant diameter. Furthermore, the holes have been arranged such that their linear axis is parallel to the axis of the pump close to the hub of the impeller. Thus the liquid or suspension is allowed to flow from the side of the impeller where the pressure is higher to the area of the lower pressure. In other words, the flow in the balancing holes may be in either direction depending on the pressure conditions.
JP- patent publication 58192995 discusses a specific type of a centrifugal pump, i.e. a pump where the impeller is a closed one and sealed on both axial sides, i.e. the front side of the front shroud and the rear side of the rear shroud, thereof by slide impeller sealings located radially at about half the diameter of that of the impeller outer circumference. There are holes arranged through the rear shroud of the impeller, the holes entering the rear side of the rear shroud between the impeller sealings and the shaft of the impeller. This kind of a pump functions always such that the liquid to be pumped flows at the rear side of the impeller radially inwardly towards the shaft via a narrow gap in the slide impeller sealing. The purpose of the holes in the rear shroud is to allow fluid to flow out of the rear side of the impeller back to the impeller eye in front of the working vanes. Such a flow is usually aided by arranging the inlet to the hole at the rear side of the shroud at a smaller radius than the outlet from the hole at the front side of the shroud, whereby, in practice, the hole acts as a small centrifugal pump. The construction keeps the pressure behind the impeller low reducing thus the axial load to the bearings. However, the construction has a few weaknesses. Firstly, the capacity to transfer heat from the shaft sealing, which has to be there between the shaft and the housing irrespective of the outer impeller sealing, is dependent on the amount of flow allowed to bleed through the narrow gap of the impeller sealing. Secondly, the recirculation of the liquid to be pumped via the cavity at the rear side of the impeller shroud means loss of energy, as a part, though a small one, of the liquid to be pumped has to be pumped twice through the impeller. And thirdly, the described construction works only with clean liquid, as, if liquids containing solids are pumped, the solids block the impeller sealing, stop the liquid circulation and result in the shaft sealing running dry as the hole through the shroud pumps the liquid present in the rear side of the shroud away to the front side of the shroud.
SU-A1-1751429 discusses a centrifugal pump having a curved conduit provided through its hub/shroud. In fact the pump of the Russian application resembles the above discussed JP- patent publication 58192995, where the flow direction of the fluid flowing in the conduit is from the rear sides of the shroud to the front side thereof
Furthermore, although both balancing methods, i.e. the rear vanes and the hole through the shroud, are in use, it has been noticed, as discussed in U.S. Pat. No. 7,326,029 that when moving along a so called pump curve in the H, Q (head, capacity) chart, i.e. to the right in the direction of higher capacity, the balancing in accordance with the prior art is not always capable of sufficiently preventing the pressure in the sealing space from dropping below the pressure prevailing in front of the impeller of the pump. This is problematic because the negative pressure in the sealing space leads to the fact that the lubricating effect of the liquid to be pumped or other liquid on seals decreases when the liquid escapes from the seals. Depending on the seal type, the escaping of the liquid from the seal may cause the seal to run dry, which leads with some seal types very quickly to a seal damage.
The above mentioned US-patent suggests an impeller, in which the balancing holes are located in the impeller shroud in such a manner that the opening of each hole in the front face (the face on which the working vanes of the impeller are arranged) of the shroud are both in the rotational direction of the impeller ahead of the opening located in the rear face (the face on which the rear vanes are arranged) of the shroud and closer to the axis of the pump than the opening in the rear face of the impeller shroud. The holes have still had a linear axis and a constant diameter.
However, in spite of the fact that the inclined balancing hole or conduit of the US-patent is a great improvement compared to earlier, traditional balancing holes oriented parallel to the axis of the impeller, it has now been learned that the balancing hole of the US-patent may still be improved for at least the following two reasons.
Firstly, the opening in the front face of the shroud has traditionally been located between the working vanes, and in the pump of the above discussed US-patent, the opening is at least partially between the working vanes. This means, in practice, that the pressure the balancing hole or conduit “sees” is the pressure between the working vanes, and not the inlet pressure (pressure at the impeller eye, in front of the impeller). In other words, the working vane has, due to its function, subjected the medium to be pumped to a centrifugal force component that changes the pressure conditions, by reducing the pressure, between the working vanes. For instance, when the pump is operating above its optimal operating point, the pressure in a vane passage, i.e. in a cavity between two successive working vanes, is below atmospheric pressure. It means that the pump sealing behind the impeller is subjected to the reduced pressure, which may cause the sealing to run dry and result in seal failure sooner or later.
Generally speaking, the centrifugal pump is not always working at the optimal conditions it has been designed for but more or less outside its optimal operating point. Depending on which side of and how far from the optimal operating point the pump is operating the working vanes, more or less efficiently, cavitate and generate vapour in the vane passage between the working vanes. The generation of vapour means, in practice, reduced pressure and suction to the sealing cavity.
To avoid the above discussed weakness in the impeller construction the present invention suggests positioning the balancing holes such that their inlets at the front face of the impeller shroud are always inside the circumference of the leading edges of the working vanes making the balancing holes insensitive to the function of the working vanes. The pressure the inlet openings to the balancing conduits “see” is the inlet pressure of the pump, not the pressure affected by the working vanes.
Secondly, to avoid the circulation of fluid from behind the impeller shroud back into the impeller eye, and to ensure proper flushing of the shaft seal, the balancing conduits are positioned in the impeller shroud such that the inlet opening at the front face of the impeller shroud is at a smaller radius than the outlet opening at the rear face of the impeller shroud. Thus the balancing conduits function like small centrifugal pumps pumping fluid from in front of the impeller to the rear side thereof
The two above mentioned features ensure that in all operating conditions of the pump the flow in the balancing conduits is towards the rear side of the impeller shroud, form where the rear vanes further take the fluid with the heat transferred to the fluid from the shaft sealing to the pump volute.
Thirdly, when looking for efficiency improvement from the hydraulics viewpoint, the working vanes of the impeller should be brought as close to the axis of the impeller as possible. This requires moving the front openings (at the front face of the impeller) into the balancing holes or conduits closer to the axis of the impeller to be able to make the holes/conduits insensitive to the function of the working vanes. Moving the working vanes to have their origin closer to the axis of the impeller means, in practice, that material from the front surface of the hub is removed, i.e. the hub is made smaller. However, now that the shroud, i.e. the mainly radial extension of the hub is made thinner and the front openings located closer to the axis than the inner end of the leading edges of the working vanes, it is, sometimes, impossible to extend a linear balancing conduit from the front opening to the rear opening without cutting the front face of the hub or that of the shroud open. Furthermore, the above together with moving the front openings closer to the axis of the impeller may, in some cases, require constructing the shaft-impeller fastening in another manner, as there may be no room for extending the end of the shaft directly through the hub of the impeller.
Thus, an object of the present invention is to design a novel impeller for a centrifugal pump such that the balancing of the pressure conditions at the front and rear sides of the impeller could be more reliable and less sensitive to the operating point of the centrifugal pump.
Another object of the present invention is to design a novel impeller for a centrifugal pump by which the hydraulic efficiency of the impeller may be improved.
Yet another object of the present invention is to design a novel impeller for a centrifugal pump such that the working vanes may be brought closer to the axis of the impeller for improving the hydraulic efficiency of the impeller.
A further object of the present invention is to design a novel impeller such that the heat generated in the shaft sealing is reliably conveyed out of the sealing area in all operating conditions of the pump.
A still further object of the present invention is to design a novel impeller such that the flow in the balancing conduit is always from the impeller eye, i.e. area upstream of the leading edges of the working vanes, to the rear side of the impeller shroud.
A still another object of the present invention is to design a novel impeller for a centrifugal pump such that the balancing conduits, or, in fact, the front openings thereof, could be brought, at the front face of the impeller, as close to the axis of the impeller as technically possible, whereby the sealing cavity behind the impeller is arranged in communication with the pump inlet pressure and not the varying pressure prevailing in the vane passages.
A yet another object of the present invention is to design such a novel impeller for a centrifugal pump that may be used to pump both clean liquids and solids-containing liquids like fiber suspensions of pulp and paper industry reliably and with high efficiency.
At least some of the above objects of the present invention are met with a novel impeller structure for a centrifugal pump, comprising at least a hub having an axis, a shroud extending outwardly from the hub and dividing the impeller to a front side and a rear side, at least one working vane arranged on a first face of the hub and the shroud at the front side of the impeller, at least one rear vane arranged on a second face of the shroud at the rear side of the impeller, and at least one balancing conduit extending through said hub from a first opening at the first face to a second opening at the rear side of the impeller, the first opening of the at least one balancing conduit in the first face of the hub being located closer to the axis of the impeller than the second opening at the rear side of the impeller, the first opening of at least one balancing conduit in the first face of the hub being located within the circle C formed by the radially innermost part of the at least one working vane, while the impeller is rotated about the axis, wherein the second opening of the at least one balancing conduit at the rear side of the impeller is located at the smallest diameter of the shroud.
Other features characteristic of the present invention become apparent from the accompanying claims.
The impeller of the present invention brings at least some of the following advantages compared to prior art impellers.
Referring now to the attached drawings which form a part of this original disclosure.
Also, in performed experiments it has been learned that, though the arranging of the front/inlet and rear/outlet openings at different diameters slightly helps in the balancing, the pressure fluctuations in the sealing cavity 40 are too high, and there is a risk of running the seals dry. Performed experiments have shown that the solution to the problem relating to the pressure fluctuations is the correct location of the front/inlet opening to the balancing conduit. The location has to be such that the first or front or inlet opening is entirely inside the circle C (shown in
However, these modifications have required reconfiguration of the at least one balancing conduit 58 to have, in this embodiment of the present invention, a curved, i.e. non-linear configuration. The curved configuration is needed, as, if the at least one conduit 58 were taken via a linear path from the front or first or inlet opening 64 to the rear or second opening 66, the conduit could not run within the hub/shroud material, but would open a lengthy groove into the front or first face of the hub/shroud. However, the benefit of having the balancing conduit open inside the innermost parts of the at least one working vane would, then, be lost. Thus, in accordance with the preferred embodiment of
However, already at this stage it is worthwhile to understand that the balancing conduit may also be manufactured by drilling at least two holes such that there is no actual curved bend but a kind of a sharp bend between the linear parts of the conduit.
As to the optimal location of the second or outlet opening 66 of the balancing conduit 58 it is at the outer circumference 52′ of the hub 52 of the impeller 50 such that no shoulder is left between the outlet opening 66 and the hub surface 52′ (or the shaft surface or the shaft sleeve surface). This kind of a construction ensures that the heat generated in the shaft sealing 48 is easily conveyed away from the sealing area. The flushing of the shaft sealing 48 actually functions such that the fluid entering the rear side of the shroud 54 has a relatively high speed based on the pump inlet pressure and the balancing conduit 58 acting as a pump, whereby fluid from the space in front of the shaft sealing 48 is drawn to a cavity between the rear wall 4 of the pump and the shroud 54. The fluid that was drawn away at the outlet opening 66 is replaced with new fluid from adjacent circumferential areas, i.e. areas outside the effective range of the outlet opening 66, where the radially outward flow is weaker, whereby a small-scale liquid circulation is ensured in front of the shaft sealing 48. In other words, it is advantageous, but not totally necessary, that the shaft sealing 48 is arranged on the same hub (or shaft or shaft sleeve) surface 52′ to which the outlet opening 66 of the balancing conduit 58 opens. However, as there are various types of shaft sealings, which may be used in this position, like for instance packing box-type seals or mechanical seals, the installation of which on the shaft differs a great deal from one another, an exact dimensioning of the outlet opening 66 in relation to the sealing 48 is hard to determine. The only two ways to express that any cavity inside the diameter of the surface 52′ of the hub (or the shaft or the shaft sleeve) in front of the shaft sealing is not desired is to say that the diameter of the shaft sealing is substantially the same or longer than that of the surface 52′ of the hub or the shaft or the shaft sleeve, or that the shaft sealing 48 is arranged at the same or longer distance from the axis 8 than the outlet opening 66 of the balancing conduit 58 in the hub or the shaft or the shaft sleeve.
Basically, the impeller 150 of
The drawings illustrate with broken lines the location of the balancing conduits 58, 158 in the impeller hub 52, 152 and shroud 54, 154. The drawings of these two embodiments show that the balancing conduits 58, 158 run circumferentially inclined and curved, i.e. each conduit is turned to follow the general direction of the working vanes. Thus, each balancing conduit is inclined, and curved both in the peripheral and radially outward directions from the front or first opening 64, 164 in the front or first face of the impeller hub 52, 152. In other words, the second openings 66, 166 of the balancing conduits 58, 158 in the rear or second face of the impeller shroud 54, 154 are located in the rotational direction of the impeller behind the opening 64, 164 at the opposite end of the balancing conduit 58, 158, i.e. in the front or first face of the hub 52, 152 and also radially outside thereof The aim with the balancing conduit 58, 158 extending in the impeller hub and shroud at least substantially in the direction of the impeller vane is, on the one hand, that the speed of the liquid flowing via the conduit 58, 158 to the rear vane area is in the right direction so that less work is required from the rear vanes to pump the flowing liquid out of the space behind the impeller 50, 150. On the other hand, the aim is to increase the flow of the liquid through the balancing conduits 58, 158 to the rear vane area so that the pressure in the sealing space (discussed in connection with
A feature worthwhile to understand is that the impeller provided with the balancing conduit/s of the present invention may not only be a semi-open impeller but also a closed one, i.e. one having another shroud, so called front shroud, arranged on the edge/s of the working vane/s facing the volute 2. Such a front shroud may, if so desired, have so called front vane/s on its face opposite to the face where the working vane/s are located. However, It is clear from the description above that irrespective of the impeller type the impeller of the present invention does not have impeller sealing/s discussed in the introductory part of the specification by referring to JP-58192995, as they result in such an operation of the centrifugal pump that is clearly different from that discussed in connection with
The above description discusses very generally balancing conduits and their direction. It should be noted about the conduits that they may vary a lot, for example, in both their direction and shape. In other words, it is possible that the balancing conduits are not inclined in circumferential direction (in the front view corresponding to
It should further be understood that the balancing conduits may be curved for all their length and that the direction and radius of the curvature may change along the length of the bend. However, the balancing conduits may as well also be formed of two linear bores meeting within the body of the hub of the impeller. As to the shape of the balancing conduits, all round, oval and angular cross-sectional shapes may come into question. The cross-sectional area of the conduits may either be constant throughout the whole length of the conduit or it may vary at least for a portion of the length of the conduit. Further, it must be noted that both in the description above and in the accompanying claims, the direction of the conduit refers more to the direction of the centreline or axis of the conduit than to the direction of any specific wall thereof. The combined cross sectional flow area of the balancing conduits should preferably range between 5 and 20% of the area of the inlet opening of the pump, the area corresponding to the area limited by the outer tips of the flow receiving, or upstream, or leading edges of the working vanes when rotating. By such dimensioning it is ensured that the balancing conduits allow free and lossless flow of medium along the conduits. By which it is ensured that the pressure fluctuations in the sealing cavity are minimized. Another dimensioning feature of the balancing conduit/s is that the radially outer point of the front or first opening thereof is within the circle C formed by the radially innermost part of the working vanes, while the impeller is rotated about the axis. Preferably, the radially outer points of the front or first openings form a circle having a diameter 0.9 times, more preferably 0.8 times, most preferably 0.7 times the diameter of the circle C formed by the radially innermost part of the working vanes.
It has to be understood that the drawings do not pay any attention to how the impeller is fastened on the shaft. One feasible option is to arrange the impeller on the shaft for rotation with the shaft by a key or alike connection and to secure the connection immobile in the axial direction by a bolt arranged to run axially through the front face of the hub to a threaded blind hole at the end of the shaft. Naturally, an option is to arrange at the end of the shaft an extension having a smaller diameter to extend through the hub such that a nut may be used to secure the impeller axially immobile on the shaft. And a third option is to use a headless bolt screwed in a blind threaded hole at the end of the shaft and use a nut to secure the impeller axially immobile on the shaft. In the case of the embodiment of
As can be seen from the above description, a new impeller has been developed, eliminating at least some disadvantages of the prior art impellers. An impeller in accordance with the present invention enables the use of the pump also at capacities higher than that of the optimal operating point, without a risk of damaging seals. While the invention has been herein described by way of examples in connection with what are at present considered to be the preferred embodiments, it is to be understood that the invention is not limited to the disclosed embodiments, but is intended to cover various combinations and/or modifications of its features and other applications within the scope of the invention as defined in the appended claims.
Number | Date | Country | Kind |
---|---|---|---|
14190157.9 | Oct 2014 | EP | regional |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2015/065355 | 7/6/2015 | WO | 00 |