1. Field of the Invention:
This invention relates to rotodynamic pumps, and specifically relates to means for restricting fluid recirculation and for reducing wear between rotating and non-rotating elements of rotodynamic pumps, particularly those pumps suitable for handling slurries.
2. Description of Related Art:
Rotodynamic pumps, such as centrifugal pumps, are commonly known and used for pumping fluids in many types of industries and for many applications. Such pumps generally comprise an impeller (rotating element) housed within a pump casing (non-rotating element) having a fluid inlet and fluid outlet, or discharge. The impeller is typically driven by a motor external to the casing. The impeller is positioned within the casing so that fluid entering the inlet of the casing is delivered to the center, or eye, of the impeller. Rotation of the impeller acts on the fluid primarily by the action of the impeller vanes which, combined with centrifugal force, move the fluid to the peripheral regions of the casing for discharge from the outlet.
The dynamic action of the vanes, combined with centrifugal forces resulting from impeller rotation, produce pressure gradients within the pump. An area of lower pressure is created nearer the eye of the impeller and an area of higher pressure results at the outer diameter of the impeller and in the volute portion of the casing. An area of pressure change from higher to lower exists in the radially extending gap between the rotating and non-rotating components. The pressure differential within the pump leads to fluid recirculation through the radial gap, between areas of high and low pressure. Such fluid recirculation, typically characterized as leakage, results in a consequent loss of pump performance and, in the presence of solid particles, a dramatic increase in wear. Therefore, pumps are structured with various sealing devices, both on the shaft side of the impeller to prevent external leakage and on the suction side of the impeller to prevent internal recirculating leakage.
Effective sealing arrangements are known and employed in pumps that process clear liquid. For example, U.S. Pat. No. 4,909,707 to Wauligman, et al., describes a floating casing ring that is positioned in the axially-extending radial gap between the impeller and the pump casing. Similar floating seal rings are described in U.S. Pat. No. 4,976,444 to Richards and U.S. Pat. No. 5,518,256 to Gaffal. U.S. Pat. No. 6,082,964 to Kuroiwa discloses a supported annular ring that is thereby allowed to float in surrounding fluid. Such sealing systems are directed to preventing leakage at the axially-extending radial gap between the rotating and non-rotating elements. These sealing arrangements may also include a wear ring element. One purpose of the wear ring is to reduce wear caused by contacting of the rigid components of the seal.
When pumps are used to process slurries, the abrasive particulate matter in the slurry causes wearing between rotating and non-rotating (i.e., stationary) elements of the pump. The wear dramatically increases when fluid recirculation occurs as previously described. Thus, an effective sealing means between rotating and stationary pump elements is desirable in order to effectively reduce fluid recirculation between the rotating and stationary elements of slurry pumps, and thereby effectively reduce wear.
Various examples of sealing arrangements for slurry pumps have been previously disclosed. Some sealing and/or wear ring arrangements have been disclosed for positioning in an essentially axially-extending radial gap between the impeller and the pump casing. Such sealing arrangements are disclosed in U.S. Pat. No. 3,881,840 to Bunjes and U.S. Pat. No. 5,984,629 to Brodersen, et al., both of which describe a fixed ring formed in the pump casing which interacts with a projecting element on the impeller to provide a labyrinthine seal and/or wear ring. It has to be noted that in general, axially-extending radial gaps are not well-suited for handling slurries due to high probability of solid particle entrapment between the rotating and non-rotating elements causing rapid wear in the pump elements.
Radially-extending axial gaps, or tapered gaps which are substantially radially-extending, are much less prone to entrapment of solids. Such sealing and leakage restricting arrangements are widely used in slurry pumps. U.S. Pat. Ser. No. 2004/0136825 to Addie, et al. discloses a fixed projection on either the pump casing or on the impeller to provide a leakage restricting arrangement between the impeller and the pump casing.
U.S. Pat. No. 6,739,829 to Addie discloses a floating ring element positioned between the impeller and pump casing which is also configured with means for receiving and distributing cooling and flushing fluid into the gap between the impeller and pump casing. Like other sealing arrangements, the floating ring seal of the '829 patent is purposefully sized and configured to provide a gap between the impeller and the sealing device to prevent friction between the seal and the impeller, and thereby prevent galling of the seal during rotation of the impeller. A necessary component of this design, therefore, is the presence of a flush system.
Prior sealing arrangements have heretofore been specifically directed to providing a seal that has sufficient clearance such that it does not contact the rotating elements of the pump, specifically to reduce or prevent wear and galling in the seal. As a result, such seal arrangements may still be vulnerable to undesirable fluid recirculation and wear between rotating and stationary elements of the pump. Moreover, placement of a sealing arrangement near the eye of the impeller in an axially-extending gap between the casing and impeller does not present the most effective means of preventing solid particle entrapment and subsequent wear between the casing and impeller.
Thus, it would be advantageous in the art to provide a relatively simple sealing arrangement which does not rely on a flush system and that effectively provides resistance to recirculation and wear between rotating and non-rotating elements of the pump, and one which is ideally located within the pump at a position where resistance to recirculation and wear can be most effective.
In accordance with the present invention, a flexible floating seal ring arrangement is provided for restricting fluid recirculation and limiting wear between rotating and non-rotating elements of rotodynamic pumps, and is configured for effectively bridging the radially-extending gap between such rotating and non-rotating elements in a manner that provides more effective resistance to fluid recirculation and wear. The flexible floating seal ring arrangement is described herein with respect to use in a centrifugal pump of the slurry type primarily to reduce wear, but may be adapted for use in any rotodynamic pump with a resulting increase in pump performance.
The flexible floating seal ring arrangement of the present invention generally comprises a ring made of flexible material which renders the ring radially deformable under the influence of centrifugal forces when rotating. The ring is structured to fit within a circular channel comprising a circular groove formed in a substantially radially extending surface of the non-rotating pump casing and a circular groove formed in a substantially radially extending surface of the rotating impeller. The flexible ring is sized in axial length to fit within the circular channel and axially span the radially-extending axial gap between the pump casing and the impeller.
The flexible ring is particularly sized with an inner diameter which, when positioned on the inner diameter of the groove formed in the impeller when the impeller is static (i.e., not rotating), provides a snug fit of the flexible ring on the inner diameter of the impeller groove. Consequently, the inner diameter of the flexible ring is slightly smaller than the inner diameter of the impeller groove so that when the flexible ring in installed in the groove of the impeller at assembly, the flexible ring must be slightly stretched to fit snugly onto the inner diameter of the impeller groove and not wobble when the impeller is static.
Upon rotation of the impeller, the flexible ring deforms radially under centrifugal forces, thereby minimizing the gaps between the flexible ring and the outer diameter of the grooves in the rotating and non-rotating elements. Depending on the speed of rotation of the impeller, the flexible ring may, from time to time, contact the outer diameter of the circular channel in the stationary casing wall. Further depending on the speed of rotation, the flexible ring may rotate at a speed independent of the impeller. The resulting ability of the flexible ring to float within the circular channel, and to minimize gaps, under these conditions has the advantage of restricting recirculation of fluid between the rotating and non-rotating elements of the pump, and also restricts the passage of abrasive material through the radial gap between the rotating and non-rotating elements to limit wear therebetween.
At all times during pump operation, a pressure differential exists on either side of the flexible ring, thereby acting against the outward radial deformation of the flexible ring within the circular channel. Such pressure differential and the ability of the ring to deform radially can be effectively moderated by the presence of expelling or pump out vanes installed on the impeller shroud facing inwardly toward the radial gap and positioned radially outward from the flexible floating ring placement. In addition, selection of the material properties of the ring will affect this radial deformation.
The particular placement of the flexible floating ring arrangement in a radially-extending axial gap between the rotating and non-rotating elements of the pump provides a more effective restriction of fluid recirculation and wear than is effected with sealing arrangements that are positioned in an axially-extending radial gap between rotating and non-rotating pump elements.
In the drawings, which illustrate what is currently considered to be the best mode for carrying out the invention:
The illustrated pump is of a centrifugal slurry type. However, the configuration of the rotodynamic pump 10 illustrated in
The pump 10 is further comprised of an impeller 26 that rotates within the pump casing 12. As best seen in
In the present invention, the impeller 26 is formed with a radially-extending surface 40. An axially-extending groove 42 is formed in the surface 40 of the impeller 26. Likewise, the pump casing 12, and specifically the suction side liner 20 here illustrated, is formed with a radially-extending surface 44 which is opposite to and spaced from the radially-extending surface 40 of the impeller 26. An axial gap 46, as best seen in
The radially-extending surface 44 of the pump casing 12 is likewise formed with an axially-extending groove 50 that is generally aligned with the groove 42 formed in the radial surface 40 of the impeller 26. The generally aligned grooves 42, 50 thereby form a circular channel 52 (
A ring 60 is sized to be received by and is positioned within the circular channel 52 formed by the two grooves 42, 50. The ring 60 is sized in axial length to fit within the circular channel 52 formed by the two grooves 42, 50, and the ring 60 spans the radially-extending axial gap 46 between the rotating impeller 26 and non-rotating pump casing 12.
As seen in
However, as further seen in
Alternatively, as shown in
The flexible ring 60 of the present invention is made of elastic material that enables the ring 60 to deform radially outwardly under centrifugal forces applied to the ring 60 by rotation of the impeller 26. The ring 60 is conversely able to contract radially inwardly again so that the inner diameter 62 of the flexible ring 60 comes into contact with the inner diameter 56 of the groove 42 when the impeller 26 ceases to rotate or when the rotation of the impeller 26 is not sufficient to maintain the radial expansion of the ring 60. The ring 60 may be made of any suitable material that provides the radial deformation capabilities as described. Some exemplar materials include, but are not limited to, low friction polymers.
As the rotation speed of the impeller 26 increases, centrifugal forces acting on the flexible ring 60 cause it to deform radially outwardly so that the inner diameter 62 of the ring 60 no longer contacts either the inner diameter 56 of groove 42 in the impeller 26 or the inner diameter 66 of the groove 50 in the pump casing 12. At that point, the ring 60 is floating in the circular channel 52, as illustrated in
When the impeller 26 is rotating during operation of the pump, a pressure differential is created such that high pressure exists on side A of flexible ring 60 and low pressure exists on side B of the flexible ring 60. The high pressure exerted on the ring 60 from side A of the ring is counterbalanced by the centrifugal forces exerted on the flexible ring 60, and the flexible ring 60 is consequently maintained in a state of flotation within the circular channel 52, as illustrated in
As the flexible ring 60 begins to float in the circular channel 52, centrifugal forces on the flexible ring 60 decrease and the flexible ring 60 will begin to deform radially inwardly again with a consequent contact between the inner diameter 62 of the flexible ring 60 and the inner diameter 56 of the groove 42 of the impeller 26. When such contact is made between the flexible ring 60 and the groove 42, the centrifugal forces again act upon the flexible ring 60 to cause it to float within the circular channel 52. Thus, the flexible ring 60 will fluctuate between a first state of floating in the circular channel 52 free of the impeller 26 and a second state of contacting the impeller 26 as described. These fluctuating states are also influenced by the rotational speed of the impeller 26.
The differential pressures between side A and side B of the flexible ring 60 further influence the position of the flexible ring 60 in the circular channel 52 at any given time. As shown in
It may also be noted that the differential pressures that are exerted on the flexible ring 60 are influenced by the existence of expelling vanes positioned along the radial surface of the impeller shroud, and the configuration and/or dimension of those expelling vanes. That is, the existence of expelling vanes in general tends to decrease the pressure forces exerted on side A of the flexible ring 60. Also, the radial length dimension of the expelling vanes will influence the pressure forces, and thereby influence the radial deformation of the flexible ring 60.
The ring 60 bridging the axial gap 46 increases the hydraulic resistance of the axial gap 46 to fluid recirculation between the rotating impeller 26 and the stationary pump casing 12. Consequently, the resistance of fluid recirculation also increases the resistance to abrasive particulates in the fluid from infiltrating between the rotating and non-rotating elements of the pump, thereby reducing wear therebetween. Further, the ability of the ring 60 to float in the circular channel 52 reduces mechanical losses due to friction, and reduces wear in the ring 60 itself as a result of reduced rotational velocity.
The ring 60 of the floating ring seal arrangement is shown in
As further shown in
The flexible floating ring seal arrangement of the present invention is particularly directed to use in rotodynamic pumps of the type which are used to process slurries. However, those of skill in the art will appreciate the advantages provided by the flexible floating ring seal arrangement of the present invention and will appreciate that the invention may be adapted for use in a variety of types of rotodynamic pumps. Hence, reference herein to specific details or embodiments of the invention are by way of illustration only and not by way of limitation.