Regenerative pump having vanes and side channels particularly shaped to direct fluid flow

Information

  • Patent Grant
  • 6422808
  • Patent Number
    6,422,808
  • Date Filed
    Friday, November 12, 1999
    24 years ago
  • Date Issued
    Tuesday, July 23, 2002
    22 years ago
Abstract
A regenerative or toric pump adds energy to a fluid using an impeller having an axis of rotation and axially spaced, radially extending first and second surfaces. A casing encloses the impeller and has a fluid inlet and a fluid outlet separated by a stripper. The casing has axially spaced, radially extending first and second sidewalls facing the first and second surfaces of the impeller respectively. Axially and radially extending blades or vanes are formed on an outer radial periphery of the impeller for driving fluid from the inlet toward the outlet as the impeller rotates about the axis of rotation. A fixed surface is formed in at least one sidewall of the casing for directing fluid back toward the impeller. Improved operating characteristics and extended range are accomplished through modification to the vane configuration of the impeller and/or by modification of the side channel configuration of the pump chamber in an asymmetrical fashion. The vanes can be modified to include a radially inward based portion extending in a generally trailing direction with respect to rotation of the impeller and a radially outward tip portion extending in a generally leading direction. The blades may also include a chamfered surface on the trailing edge of the base portion. The impeller chamber can be modified separately by expanding a side channel in the casing, or by insertion of a spacer between the side channel and the remaining portion of the casing defining the impeller chamber.
Description




FIELD OF THE INVENTION




The present invention is directed to a regenerative pump, sometimes referred to as a toric pump, especially designed for economical mass production which is capable of developing higher pressures and flow rates at higher efficiencies than other pumps of comparable design and operating speed, by modifications made to the impeller and/or housing.




BACKGROUND OF THE INVENTION




In an automotive emission control system, a pump supplies air as required to the exhaust system between the manifold and the catalytic converter. In conventional regenerative pumps intended for use in an automotive emission control system, the impeller has straight radially extending blades at its outer periphery and is driven in rotation between a pump housing and a cover formed with a pump chamber. The pump chamber is formed symmetrical with respect to the rotatable impeller, and the surfaces of the housing and the cover. Further descriptions of toric pumps of this construction can be obtained from U.S. Pat. Nos. 5,302,081; 5,205,707 and 5,163,810.




Over time, industry needs have changed as restrictions on emissions have changed. It is now desirable to provide more air to an automotive emission control system than was previously required. Currently, it is desirable to provide at least between 19 and 20 cubic feet per minute (cfm). It is also desirable to meet the minimum fluid flow requirements while maintaining the same size housing. To meet these new fluid flow requirements, it has been necessary to double, and in some instances quadruple, the currently existing fluid flow rates of regenerative single stage pumps. Up to this point in time, the typical regenerative pump used in automotive emission control system applications has been capable of achieving a fluid flow rate of only 4 cubic feet per minute (cfm) at approximately 40 inches (H


2


O) head, and therefore, it is desirable in the present invention to provide a greater fluid flow output at the same or greater pressure for a given size housing configuration. It is further desirable in the present invention to reduce the electrical current or power requirements for a motor used in an electric motor driven pump for a given pressure and/or flow output. It is also desirable in the present invention to reduce the rotational speed of the motor required for a given pressure and/or flow rate output. Additionally, it is desirable in the present invention to increase overall efficiency and to provide for longer life and enhance reliability of regenerative pumps, and in particular, single stage, double channel, electrical air pumps or compressors.




SUMMARY OF THE INVENTION




In a regenerative pump according to the present invention, the rotor vanes of the peripheral regenerative pump are arcuate when viewed from the side, with the upper and lower portions curved forward in the direction of rotation. Preferably, a chamfer, or similar relief is formed on the convex side of the inner portion of all vanes. Bending the root portion of the vane to face forward and the addition of the chamfer are aimed at reducing pressure energy losses in the fluid entry region. Energy losses in the fluid entry region are the dominant loss in this type of regenerative pump. Prototypes of an impeller according to the present invention have been produced and tested. The test results have indicated a pressure increase, for the same rotational speed, of no less than 60% over the whole operating range and no less than 100% over a substantial portion of the whole operating range. In the tests, flow also increases over the operating range. Such dramatic increases in pressure and flow were unexpected.




The present invention also concerns double channel regenerative pumps of the type embodying a central rotor with vanes extending generally radially, either in a straight radial fashion, or in an arcuate fashion. Previously, it has been difficult to achieve a proper matching of the output of such a regenerative pump or compressor to the requirements of a particular application. Although some matching could be achieved by judicial choice of shaft rotational speed, pump efficiency can suffer in the process. Typically, a pump of this type includes a housing means for mounting a drive motor and one of the side channels, a rotor with generally radially extending vanes at its outer region on one or more axial sides of the rotor, and a cover sealingly engaged with the housing and a second side channel. The present invention allows matching of a pump's capacity to the requirements of a particular application without changing shaft rotational speed. Previously the channels and the housing and cover have been equal, or symmetrical in cross-section, and differ only at the channel ends where it is common to place transfer inlet and delivery passages from the housing channel to ducts in the cover or housing. In the present invention, the channels of the housing and cover are formed in a manner which is not symmetrical. The cover, which is freely accessible, can be replaced by alternative covers having channels of various depths, or the cover can be spaced axially outwardly from the impeller by insertable spacers of various depths to change the effective depth of the channel in the cover. Thereby, the specific output of the pump may be varied to suit different fluid flow requirements by providing the appropriate asymmetrical depth of channel. Prototypes of asymmetrical side channels have been constructed and tested. These tests show that a change in capacity of at least 20% can be achieved by varying the axial depth of the channel without loss in the overall efficiency of the regenerative pump. The prototype of the present invention that was tested included a spacer plate inserted between the housing and the cover. The plate increased one of the side channels by a depth according to the thickness of the plate. Thus, a deeper channel can be provided without requiring the costly and time consuming measure of manufacturing a new cover. The magnitude of enhancement to pump performance was unexpected.




A regenerative pump for adding energy to a fluid, according to the present invention, includes an impeller having an axis of rotation and axially spaced, radially extending first and second surfaces. A radially split casing encloses the impeller and has a fluid inlet and a fluid outlet separated by a stripper. The stripper generally has a close clearance to a periphery of the impeller. The casing has axially spaced, radially extending first and second side walls facing the first and second surfaces respectively. Axially and radially extending blade means is formed on an outer radial periphery of the pump for driving fluid from the inlet toward the outlet as the impeller rotates about the axis of rotation. Means, formed in at least one side wall of the casing, directs fluid back toward the impeller.




The blade means preferably includes a plurality of vanes spaced circumferentially around the outer radial periphery of the impeller. Each vane has a radially inward base portion extending in a generally trailing direction with respect to rotation of the impeller and a radially outward tip portion extending in a generally leading direction with respect to rotation of the impeller.




Chamfer means is preferably formed on the base portion of each vane for deflecting fluid from the inlet toward the pocket defined between two adjacent vanes and the casing. Preferably, the chamfer means is formed on a trailing edge of the base portion of each vane. The chamfer means may be formed at an angle with respect to a radially extending plane normal to the axis of rotation of the impeller at a range selected from between 10° and 45° inclusive. Alternatively, the chamfer means may be formed as a curved surface having a predetermined radius connecting a generally radially extending surface of each vane to a generally axially extending surface of the respective vane along a trailing edge.




The blade means may include a plurality of vanes spaced circumferentially around the outer radial periphery of the impeller, where each vane is bent in radial direction with respect to the axis of rotation of the impeller about an axis generally parallel with the axis of rotation of the impeller. Alternatively, the blade means may include at least one set of radially bent vanes with respect to the axis of rotation, where the set of vanes is defined by at least two circumferentially spaced vanes collaborating with one another to form a single circular annulus.




The base portion of each vane preferably forms an entry angle with respect to a radially extending plane normal to the axis of rotation of the impeller in a range selected from between 20° and 30° inclusive. The tip portion preferably forms an exit angle with respect to a radially extending plane normal to the axis of rotation of the impeller in a range selected from between 20° and 45° inclusive.




The impeller has a generally radially extending plane or web normal to the axis of rotation and connected to the blade means. The web extends radially into the blade means to a position generally midway between the base and the tip of each vane. Preferably, the right angle surfaces, formed by the web and an annular hub of the impeller supporting the base of each vane, is filled in to provide an angled, stepped, or preferably radially curved transition between the axially extending hub portion of the impeller and the radially extending web between each adjacent set of vanes.




The fluid directing means preferably includes a fixed shaped surface. The fluid directing means may include at least one of the first and second side walls having a generally ring-shaped, side channel portion formed in the casing around the axis of rotation for directing fluid helically back into contact with the blade means as the impeller rotates. Preferably, the side channel portion is generally perpendicular to and along an arc of constant radius centered on the axis of rotation. In the preferred embodiment, the fluid directing means includes each of the first and second side walls having a generally ring-shaped side channel portion formed therein around the axis of rotation of the impeller for directing fluid helically back into contact with the blade means as the impeller rotates. Preferably, the fluid directing side channel portion of one of the first and second side walls is enlarged with respect to the other fluid directing side channel portion. Preferably, the enlarged one of the side channel portions is enlarged in the axial direction. The fluid directing means preferably is formed asymmetrically in the first and second side walls of the casing around the axis of rotation of the impeller.




In an additional embodiment, a means for defining a flow path between the fluid inlet and the fluid outlet is formed in at least one of the first and second side walls of the casing. The flow path defining means is tapered so that the cross-sectional area at the fluid inlet is greater than the cross-sectional area at the fluid outlet. The flow path defining means may include the side channel portions wherein the side channel portions preferably taper axially inward toward said impeller at a constant slope from said fluid inlet to said fluid outlet.




Regenerative pumps have traditionally been constructed, when there are two channels, with side channels equal in cross-section. The present invention demonstrates that unequal channels cause no significant loss in efficiency or other deleterious effects. The option of using unequal channels facilitates convenient capacity modifications so that a single pump design may have its pumping characteristics modified to satisfactorily meet more than one specific application requirement. The asymmetric channels according to the present invention may be used with a standard configuration impeller for a regenerative pump, or may be used in combination with the arcuate vane impeller configuration according to the present invention for further performance enhancement. The rear swept lower, or entry, or base portion of the vane with forward swept tip approximately midway up from the root of the vane, as previously described with respect to the present invention, can advantageously be used in combination with the asymmetric channels. The arcuate vane configuration, as previously described, can also include the modification of chamfer means for easing entry of fluid, particularly where the entry angle is large relative to the impeller axis. As the flow rate is reduced and the pressure rises, the ease of entry for fluid into the impeller is a feature that is associated with results that reveal improved maximum pressure for a given shaft speed and higher efficiency. As previously described, the chamfer means may also take an alternative curvilinear profile.




Other objects, advantages and applications of the present invention will become apparent to those skilled in the art when the following description of the best mode contemplated for practicing the invention is read in conjunction with the accompanying drawings.











BRIEF DESCRIPTION OF THE DRAWINGS




The description herein makes reference to the accompanying drawings wherein like reference numerals refer to like parts throughout the several views, and wherein:





FIG. 1

is a front end view, with certain parts broken away, of a conventional toric pump;





FIG. 2

is a detailed cross sectional view of the pump of

FIG. 1

taken on line


2





2


of

FIG. 1

;





FIG. 3

is a front end view of the impeller housing of the pump of

FIG. 1

;





FIG. 4

is a detailed cross sectional view of the impeller housing taken on line


4





4


of

FIG. 3

;





FIG. 5

is a detailed cross sectional view of the impeller housing taken on line


5





5


of

FIG. 3

;





FIG. 6

is a front end view of the impeller cover of the pump of

FIG. 1

;





FIG. 7

is a rear end view of the impeller cover;





FIG. 8

is a detailed cross sectional view taken on the line


8





8


of

FIG. 6

;





FIG. 9

is a detailed cross sectional view of the impeller cover taken on line


9





9


of

FIG. 6

;





FIG. 10

is a detailed cross sectional view of the impeller cover taken on line


10





10


of

FIG. 6

;





FIG. 11

is a perspective view of an impeller according to the present invention;





FIG. 12

is a detailed view of a portion of an impeller according to the present invention;





FIG. 13

is a cross-sectional detailed view of the impeller taken on line


13





13


of

FIG. 12

;





FIG. 14

is a cross-sectional detailed view of the impeller taken on line


14





14


of

FIG. 13

;





FIG. 15

is a cross-sectional detailed view of an asymmetrical pump chamber formed with a spacer according to the present invention;





FIG. 16

is a cross-sectional detailed view of an asymmetrical pump chamber according to the present invention formed integrally in the impeller cover;





FIG. 17

is a graph of overall efficiency versus flow rate in cubic feet per minute at 40 inches of water back pressure showing various curves for different size spacers;





FIG. 18

is a graph of flow rate in cubic feet per minute versus back pressure in inches of water showing flow lines comparing pump chambers with and without spacers, and corresponding electrical current lines of the pump with and without a spacer;





FIG. 19

is a graph of overall efficiency versus flow in standard cubic feet per minute showing curves comparing pump chambers with and without a spacer;





FIG. 20

is a rear end view of the impeller cover with the side wall channels tapered;





FIG. 21

is a detailed cross-sectional view of the impeller cover taken on line


21





21


of

FIG. 20

showing the tapered side wall channels of the impeller cover;





FIG. 22

is a graph of the airflow in kilograms per hour versus discharge pressure in millibars showing curves comparing the taper applied to the impeller cover, impeller housing and neither the impeller cover nor impeller housing; and





FIG. 23

is a graph of overall pump efficiency versus discharge pressure in millibars showing curves comparing the taper applied to the impeller cover, impeller housing and neither the impeller cover nor impeller housing.











DESCRIPTION OF THE PREFERRED EMBODIMENT




The interrelationship of the various parts of a conventional toric pump or regenerative pump are best seen in the assembly views of

FIGS. 1 and 2

, while details of the individual parts are shown in

FIGS. 3-10

.




Referring first to

FIGS. 1 and 2

, a pump includes an impeller housing designated generally


20


, an impeller cover designated generally


22


mounted upon the front of housing


20


, and a filter cover designated generally


24


mounted on the front of impeller cover


22


. A pump impeller


26


is mounted in operative relationship with a pump chamber designated generally


28


cooperatively defined by the assembled impeller housing


20


and impeller cover


22


, the impeller


26


being fixedly coupled to the drive shaft


30


(

FIG. 2

) of an electric motor


32


mounted or integrated with the rear of the impeller housing. An inlet port or fitting


34


opens through filter cover


24


into a filter chamber


36


defined by the assembled impeller cover and filter cover. A passage or opening in impeller cover


22


places the filter chamber


36


in. communication with pump chamber


20


, a sponge-like block of filter media


40


being fitted in filter chamber


36


between inlet port


34


and passage


38


to filter air passing into the pump through inlet port


34


before the air passes through passage


38


into pump chamber


28


.




For purposes of the present application, the conventional pump impeller


26


and the configuration of pump chamber


28


may be assumed to be identical to the impeller and pump chamber disclosed in U.S. Pat. Nos. 5,302,081, 5,205,707 and/or 5,163,810, and further details of the impeller and pump operation of a conventional pump may be had from those patents, whose disclosure is incorporated herein by reference. The invention of the present application is especially concerned with modifications to the configuration and interrelationship of the impeller and the side channel in the casing, details of which are set forth in detail below with respect to

FIGS. 11-19

.




The construction of impeller housing


20


is best seen in

FIGS. 3

,


4


and


5


. Housing


20


is initially formed as a metal casting with a portion of pump chamber


28


and an impeller receiving recess formed in the casting. Impeller housing


20


, if die cast from a suitable material such as SAE 413 aluminum, will require, the machined finishing of only two surfaces and the drilling and tapping of four holes for the reception of mounting bolts.




Referring to

FIG. 4

, two surfaces which require precise machining are what will be referred to as the front end surface


50


of housing


20


and a parallel surface


52


which defines the bottom of an impeller receiving recess in impeller housing


20


. Surfaces


50


and


52


are finished accurately flat and parallel with each other and are spaced axially from each other by a distance which only slightly exceeds the axial thickness of the impeller


26


used. The amount by which the spacing between surfaces


50


and


52


exceeds the impeller thickness establishes the clearance between surface


52


and one side


26


A (

FIG. 2

) of the impeller and between the opposite side


26


B of the impeller and an opposed surface


56


of the impeller cover when the impeller, impeller housing and impeller cover are assembled as in FIG.


2


. These clearances must be sufficient to avoid rubbing between the impeller sides and housing elements during rotation of the impeller, while at the same time being small enough to minimize any flow of air between the last mentioned opposed surfaces.




A central bore


58


through the impeller housing serves to pilot the front motor boss


32




a


of motor


32


which carries a shaft bearing, not shown, which locates the axis of motor shaft relative to the impeller housing.




The location and diameter of bore


58


and the radius of stripper surface


74




a


are the other dimensions (other than surfaces


50


and


52


) of housing


20


which must be machined to tight tolerances. The radial outer surface


28




a


of the pump chamber portion of the recess may be established with sufficient precision by the die casting process. Alternatively, bore


58


may receive a shaft bearing directly, rather than a boss on the motor housing in which the shaft bearing is located. Bore


58


establishes the location of the motor shaft axis relative to the housing, stripper surface


74




a


is machined at a precise distance from and concentric to this axis to establish radial clearance between impeller and housing across the stripper. The diameter of bore


58


is such as to receive the motor boss (or shaft bearing) with a transition or locational interference fit. The motor housing is fixedly attached to the rear side of the impeller housing as by bolts


60


(

FIG. 2

) which pass through bores


62


at the bottom of a central recess


64


. Mounting lugs


66


may be integrally formed on housing


20


to enable the pump to be mounted on a suitable mounting bracket. Tapped bores


68


(

FIGS. 3 and 5

) are formed in housing


20


to accommodate mounting bolts employed to mount impeller cover


22


on impeller housing


20


.




As is conventional in toric pumps, the pump chamber


28


extends circumferentially about the axis of the impeller from an inlet end


70


(

FIG. 3

) to an outlet end


72


. The recessed inlet and outlet ends


70


,


72


are separated from each other by a stripper portion


74


of surface


52


which, when the impeller is in place, cooperates with the adjacent side surface of the impeller to form a flow restriction between the two surfaces functionally equivalent to a seal between the inlet and outlet. This prevents high pressure air at outlet


72


from flowing across the stripper portion


74


to the low pressure region at inlet end


70


.




The structure of impeller cover


22


is best seen in FIGS.


6


. Impeller cover


22


is a molded one-piece part of a suitable thermoplastic material. The flat surface


56


referred to above is formed on the rear side of impeller cover


22


to be seated in face to face engagement with the machined surface


50


of impeller housing


20


. An annular recess


28




c


in the flat rear surface


56


forms a pump chamber portion in the rear surface of impeller housing


20


which is coextensive with and matched to pump chamber


28


of housing


20


. As best seen in

FIGS. 9 and 10

, the flat rear surface


56


of the impeller cover is recessed slightly to form an axially projecting peripheral flange


76


which fits over the front end of impeller housing


20


to locate the housing and cover relative to each other upon assembly. As best seen in

FIG. 2

, bolts


78


passing through bores


80


in impeller cover


22


are received in the tapped bore


68


in impeller housing


20


to fixedly secure housing


20


and cover


22


into assembled relationship with each other. As best seen in

FIGS. 7 and 9

, the outlet end


72




a


of the pump chamber portion


28


C communicates with a passage


82


extending through a nipple


84


on impeller cover


22


to define an outlet port for the pump chamber


28


,


28


A,


28


C of the pump.




At the front side of impeller cover


22


, a cup shaped recess


86


, best seen in

FIGS. 9 and 10

, is formed.




A flow passage


88


leads rearwardly from the bottom of recess


86


to open through the flat rear surface


56


of the impeller cover. Passage


88


opens into the inlet end


70




a


of the pump chamber portion


28


C in impeller cover


22


and constitutes the inlet to the combined pump chamber


28


,


28


A,


28


C of the pump defined by the assembled housing


20


and cover


22


. A central post


90


is integrally formed on cover


22


within the recess


86


and projects forwardly to a flat front end


92


co-planar with the front end edge


94


of cover


22


. A bore


96


for receiving a self tapping mounting screw extends rearwardly into post


90


, with a square recess


98


at the front end of bore


96


. A radially extending web


100


(

FIGS. 6 and 8

) projects radially from central post


100


entirely across recess


86


to be integrally joined to the side wall


102


of the recess.




The forward edge


104


(

FIG. 8

) of web


100


is co-planar with the front edge


94


of the impeller cover. Other stiffening webs such as


106


may be formed at appropriate locations in recess


86


but, as best seen in

FIG. 8

, these other webs


106


have edges which are spaced well rearwardly of front edge


94


. Recess


86


constitutes a portion of a filter chamber adapted to receive filter


40


(see FIG.


2


). Cover


24


is of a generally cup shaped configuration, the recess


110


of the cup opening rearwardly. The recess


110


in filter cover


24


is conformed to mate with and form an extension of the filter receiving recess


86


of impeller cover


22


, as seen in FIG.


2


. Like impeller cover


22


, a central post


112


is formed in the filter receiving recess


110


. A bore through post


112


receives a mounting bolt


118


threaded into bore


96


in the impeller cover to hold the filter cover seated on the impeller cover


22


. The filter element designated generally


40


is formed from a block of a sponge-like material, such as a reticulated polyester foam. The axial thickness of filter element


40


is chosen to slightly exceed the axial dimension of the filter chamber defined by the mated filter receiving recesses


86


,


110


of the impeller cover


22


and filter cover


24


when the two covers are assembled. Filter element


40


is formed with a central bore


130


adapted to receive central posts


90


and


112


, as seen in FIG.


2


.




The pump impeller


26


can be modified from the conventional straight radially extending vanes to a bent shape of vane as illustrated in

FIG. 11

or a curvilinear form as illustrated in

FIGS. 12-14

. In any case, the pump impeller


26


includes axially and radially extending blade means


140


formed on an outer radial periphery


142


of the impeller


26


for driving fluid from the inlet end


70


toward the outlet end


72


as the impeller


26


rotates about the axis of rotation. The blade means


140


includes a plurality of vanes


144


spaced circumferentially around the outer radial periphery


142


of the impeller


26


. Each vane


144


has a radially inward base portion


146


connected to an axially extending cylindrical sidewall or hub


148


of the impeller


26


. The base portion


146


extends in a generally trailing direction with respect to rotation of the impeller


26


. As illustrated in

FIG. 11

, the impeller would rotate in a counter-clockwise direction. A radially outward tip portion


150


of each vane


144


extends in a generally leading direction with respect to rotation of the impeller


26


. The base portion


146


forms an entry angle φ


1


, with respect to a radially extending plane containing the axis of rotation of the impeller


26


in a range selected from between 20° and 30° inclusive, with a preferable range selected from between 26° and 30° inclusive, and a most preferred angle of 26°. The tip portion


150


forms an exit angle φ


2


with respect to a radially extending plane containing the axis of rotation of the impeller


26


in a range selected from between 20° and 45° inclusive, with a preferable range selected from between 20° and 30° inclusive, and a most preferred angle of 20°. The blade means


140


preferably includes a plurality of vanes spaced circumferentially around the outer radial periphery


142


of the impeller


26


with each vane


144


bent or curved in radial direction with respect to the axis of rotation of the impeller


26


about an axis generally parallel with the axis of rotation. The blade means


140


may include at least one set of radially bent vanes


144


with respect to the axis of rotation, where the set of vanes


144


is defined by at least two circumferentially spaced vanes


144


cooperating with one another to form a single circular annulus. As best seen in

FIGS. 11-14

, the impeller


26


preferably includes a generally radially extending planar web


152


disposed normal to the axis of rotation and connected to the blade means


140


. The web


152


extends at least radially outwardly from the axially extending, cylindrical sidewall or hub


148


of the impeller


26


. Preferably, the transition surface


154


formed between the web


152


and the annular hub


148


of the impeller


26


is filled in to provide an angled, stepped, or most preferably a radially curved transition surface


154


between the axially extending hub


148


of the impeller


26


and the radially extending web


152


between each adjacent set of vanes


144


. The web


152


preferably extends radially into the blade means


140


to a position generally midway between the base portion


146


and the tip portion.


150


of each vane


144


. If the web


152


is extended radially outwardly to the outer radial periphery


142


of the impeller


26


(not shown), each vane


144


can be axially separated or isolated from one another if desired for a particular application. It has been found that optimum performance characteristics are achieved if the web


152


is maintained at a position located between the base portion


146


and a tip portion


150


of each vane, and preferably at a position generally midway between the base portion


146


and the tip portion


150


. It should be recognized that the base portion


146


may be of the same, or a differing length, with respect to the tip portion


150


of each vane


144


. Preferably, the base portion


146


forms a percentage of the overall radial length of each vane


144


in a range selected from between 30% and 70% inclusive, with a preferable range of 40% to 60% inclusive and a most preferable value of approximately 50%. Preferably, each vane


144


is identical with the other corresponding vanes


144


formed on the outer radial periphery


142


of the impeller


26


.




Chamfer means


158


is preferably formed on the base portion


146


of each vane


144


for deflecting fluid from the inlet toward a pocket


160


defined between two adjacent vanes


144


and the casing sidewalls defining the pump chamber


28


. The chamfer means


158


is preferably formed on a trailing edge of the base portion


146


. The chamfer means


158


can be formed at an angle φ


3


with respect to a radially extending plane normal to the axis of rotation of the impeller at a range selected from between 10° and 45° inclusive, with a preferred value of approximately 45°. The chamfer means


158


could also be formed as a curved or radial surface (not shown) having a predetermined radius connecting a generally radially extending surface


162


of the vane


144


to a generally axially extending surface


164


of the vane


144


along a trailing edge.




Fluid directing means


166


is preferably formed in at least one sidewall of the casing defining the pump chamber


28


for directing fluid back toward the impeller


26


. The fluid directing means


166


preferably takes the form of a fixed surface


168


defining a portion of the pump chamber


28


. The fluid directing means


166


can include at least one of the first and second sidewalls


52


,


56


having a generally ring-shaped, side channel portion


28


A,


28


C formed in the casing around the axis of rotation for directing fluid helically back into contact with the blade means


140


as the impeller


26


rotates. The side channel portion


28


A or


28


C is generally perpendicular to the axis of rotation and extends along an arc of constant radius centered on the axis of rotation. The fluid directing means


166


may also include each of the first and second sidewalls


52


,


56


having generally ring-shaped side channel portion


28


A,


28


C respectively formed therein around the axis of rotation for directing fluid helically back into contact with the blade means


140


as the impeller


26


rotates. In the preferred configuration, as best seen in

FIGS. 15 and 16

, the fluid directing side channel portion


28


C of one of the first and second sidewalls


52


,


56


is enlarged with respect to the other fluid directing side channel portion


28


A. Preferably, the enlarged fluid directing side channel portion


28


C is enlarged in the axial direction. The axial enlargement can be accomplished by placing a spacer


170


between the impeller housing


20


and the impeller cover


22


, as best seen in FIG.


15


. The spacer


170


is formed to extend the wall defining the side channel portion


28


C in axial direction with sidewall extension


172


. The sidewall extension


172


is formed to closely follow the contour of the side channel portion


28


C of the pump chamber


28


formed in the impeller cover


22


. Of course, it should be recognized that the combination of the spacer


170


and impeller cover


22


can be replaced with a unitary impeller cover


22


formed with the appropriate enlarged side channel portion


28


C, as is illustrated in FIG.


16


. The fluid directing means


166


preferably is formed asymmetrically in the first and second side walls


52


,


56


of the casing.





FIG. 17

is a graph of an extended range electrical air pump according to the present invention showing overall pump efficiency versus flow rate in standard cubic feet per minute at 40 inches H


2


O back pressure with an 85 mm diameter impeller, no filter and powered by 13.5 volt power source. The various curves show operating characteristics for different sizes of spacers placed between the impeller housing


20


and the impeller cover


22


. The first curve


174


illustrates the device with no spacer interposed between the impeller housing


20


and the impeller cover


22


. The second curve


176


illustrates the performance characteristics of the modified pump with a spacer having a thickness of 1.0 mm. The third curve


178


illustrates the performance characteristics of the pump with a 1.5 mm spacer interposed between the housing


20


and the cover


22


disclosed as illustrated in FIG.


15


. The fourth curve


180


illustrates the performance characteristics of the pump with a 2.5 mm spacer between the impeller housing


20


and the impeller cover


22


. Each of these curves were obtained through the use of a prototype configuration including the arcuate vanes


144


as described in greater detail above with an entry angle of 26°, an exit angle of 30° and a 45° chamfer on the trailing edge of the base portion of the vane. The test results are summarized in the table below.



















SCFM FLOW AT




BEST CHOICE




OVERALL








40 INCH H


2


O




SPACER




EFFICIENCY




RPM




AMPS



























10




1.0 mm




20.75




13,460




16.8






16




1.0 mm




21.5




16,430




28.5






20




1.5 mm




20.3




18,300




33.5















FIG. 18

is a graph of flow in cubic feet per minute versus back pressure in inches of water and further showing the current in amps versus back pressure in inches of water. The first line


182


shows flow characteristics of a pump according to the present invention without a spacer, while the second line


184


shows the fluid flow characteristics of the pump with a spacer of 2.5 mm in size. The third line


186


depicts the current used by the pump when operated without a space corresponding to the fluid flow of the first line


182


while the fourth line


188


corresponds to the current flow through the pump with a spacer corresponding to the fluid flow characteristics of the second line


184


. The data obtained for a back pressure of 10 inches of water was at 15,337 revolutions per minute (RPM), while the data points for approximately 25 inches back pressure were at 15,075 revolutions per minute (RPM). The data points corresponding to 40 inches of back pressure and 60 inches of back pressure were obtained at 14,860 revolutions per minute (RPM) and 14,319 revolutions per minute (RPM) respectively. Each of these curves were obtained through the use of a prototype configuration including the arcuate vanes


144


as described in greater detail above with an entry angle of 26°, an exit angle of 30° and a 45° chamfer on the trailing edge of the base portion of the vane, with an 85 mm diameter impeller, no filter and powered by 13.5 volt power source.





FIG. 19

is a graph depicting overall efficiency in percent versus flow in standard cubic feet per minute. The first or lower curve


190


illustrates the pump characteristics without a spacer, while the upper or second curve


192


illustrates the pump characteristics with a spacer of a size of 2.5 mm. The plotted data points along each curve starting from the right or highest flow rate proceeding toward the lower flow rate correspond to 10 inches, 25 inches and 40 inches (H


2


O) back pressure respectively along each of the two curves,


190


and


192


. Each of these curves were obtained through the use of a prototype configuration including the arcuate vanes


144


as described in greater detail above with an entry angle of 26°, an exit angle of 30° and a 45° chamfer on the trailing edge of the base portion of the vane, with an 85 mm diameter impeller, no filter and powered by 13.5 volt power source.




In an additional embodiment, the airflow of the pump may be increased while not detrimentally effecting the overall efficiency of the pump by tapering the cross-sectional area of the pump chamber


28


from a maximum area at the inlet end


70


A to a lesser area at the outlet end


72


A, as seen in

FIGS. 20-21

. The impeller cover


22


shown in

FIG. 20

is similar to that previously described. The flat surface


56


formed on the rear side of impeller cover


22


is seated in face to face engagement with the machined surface


50


of the impeller housing


20


. The annular recess or side channel portion


28


C in the flat rear surface


56


of the impeller cover


22


forms a portion of the pump chamber


28


which is coextensive with and matched to the portion of the pump chamber


28


in the impeller housing


20


. The impeller cover


22


provides the peripheral flange


76


for fitting over the front end of the impeller housing


20


as well as providing bores


80


in impeller cover


22


for receiving bolts to connect the impeller cover


22


to the impeller housing


20


. The impeller cover


22


also provides a fluid inlet


200


having the inlet end


70


A opening into the side channel portion


28


C which in turn communicates with the outlet end


72


A opening into a fluid outlet


202


of the impeller cover


22


.




A flow path defining means is preferably formed in at least one side wall


52


,


56


of the casing defining the pump chamber


28


for defining a flow path


204


between the fluid inlet


200


and the fluid outlet


202


. As previously described, the flow path defining means may include at least one of the first and second side walls


52


,


56


, respectively, having a generally ring-shaped, side channel portion


28


C formed in the casing around the axis of rotation for directing fluid back in contact with the impeller


26


as the impeller


26


rotates. The side channel portion


28


C is generally perpendicular to the axis of rotation and extends along an arc of constant radius centered on the axis of rotation.




The flow path defining means provides a cross-sectional area of said pump chamber


28


wherein the cross-sectional area of the pump chamber


28


at the fluid inlet


200


is greater than the cross-sectional area of the pump chamber


28


at the fluid outlet


202


. The reduction in the cross-sectional area of the pump chamber


28


is provided by tapering the side channel portions


28


C of the side walls


52


,


56


which define the flow path


204


between the fluid inlet


200


and the fluid outlet


202


. Preferably, the side channel portions


28


C are tapered axially inward toward the impeller


26


while maintaining a constant radial width or radial spacing of the side channel portions


28


C. Preferably, the taper occurs on a constant slope, as shown in FIG.


21


. In addition, the reduction in the cross-sectional area provided by the taper may be reduced ten to fifty percent between the cross-sectional area at the fluid inlet


200


and the cross-sectional area at the fluid outlet


202


. Preferably, the taper may reduce the cross-sectional area of the flow path


204


by twenty-five percent when extended from the fluid inlet


200


to the fluid outlet


202


. It should be noted that the flow path defining means need not be symmetrical between the first and second side walls


52


,


56


but rather may be asymmetrical such that the previously described spacers


170


or the larger incorporated side channel portions


28


C may be utilized with this embodiment.





FIG. 22

is a graph of an electrical air pump according to the present invention showing air flow in kilograms per hour of the pump versus discharge pressure in millibars wherein the data compiled was generated from a prototype pump having an 85 millimeter diameter impeller, no filter and a 13.5 volt power source. The various curves show operating characteristics for tapers applied to the impeller housing


20


, the impeller cover


22


and to neither the impeller housing


20


nor the impeller cover


22


. The first curve


206


illustrates the device with no taper applied to either the impeller housing


20


or the impeller cover


22


. The impeller housing


20


has a constant depth of 6.0 millimeters, and the impeller cover


22


has a constant depth of 6.9 millimeters throughout the side channel portion


28


C. The second curve


208


illustrates the performance characteristics of the modified pump with a taper applied to the impeller housing


20


and no taper applied to the impeller cover


22


. The taper applied to the impeller housing


20


extends from a depth of 8.4 millimeters at the inlet end


70


A to a depth of 6.0 millimeters at the outlet end


72


A. The depth of the side channel portion


28


C is maintained at a constant depth of 6.9 millimeters in the impeller cover


22


. The third curve


210


illustrates the performance characteristics of the pump with the impeller cover


22


tapered from 8.4 millimeters at the inlet end


70


A to a depth of 6.0 millimeters at the outlet end


72


A. The impeller housing


20


has its side channel portion


28


C maintained at a constant depth of 7.6 millimeters.





FIG. 23

is a graph depicting overall efficiency in percent versus discharge pressure in millibars wherein the data was compiled from a prototype pump having an 85 millimeter diameter impeller, no filter and a 13.5 volt power source. The various curves again illustrate the operating characteristics for the pump wherein the taper is applied to the impeller housing


20


, the impeller cover


22


and neither the impeller housing


20


nor the impeller cover


22


. The first curve


212


illustrates the device with neither the side channel portion


28


C of the impeller housing


20


nor the side channel portion


28


C of the impeller cover


22


tapered. The side channel portion


28


C of the impeller housing


20


is maintained at a constant depth of 6.0 millimeters, and the side channel portion


28


C of the impeller cover


22


is maintained at a constant depth of 6.9 millimeters. The second curve


214


illustrates the performance characteristics of the modified pump wherein the depth of the side channel portion


28


C of the impeller housing


20


is 8.4 millimeters at the inlet end


70


A and 6.0 millimeters at the outlet end


72


A. The side channel portion


28


C of the impeller cover


22


is maintained at a constant depth of 6.9 millimeters. The third curve


216


illustrates the performance characteristics of the pump with a taper applied to the side channel portion


28


C of the impeller cover


22


wherein the inlet end


70


A of the impeller cover


22


has a depth of 8.4 millimeters, and the outlet end


72


A has a depth of 6.0 millimeters. The depth of the side channel portion


28


C of the impeller housing


20


provides a constant depth of 7.6 millimeters.




While the invention has been described in connection with what is presently considered to be the most practical and preferred embodiment, it is to be understood that the invention is not to be limited to the disclosed embodiments but, on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims, which scope is to be accorded the broadest interpretation so as to encompass all such modifications and equivalent structures as is permitted under the law.



Claims
  • 1. A regenerative pump for adding energy to a fluid comprising:a casing having a fluid inlet and a single fluid outlet separated by a stripper, said casing being radially split and including an impeller housing and an impeller cover, having axially spaced, radially extending first and second side walls defined therein; an impeller having a series of impeller blades enclosed within said casing, and said impeller having an axis of rotation and axially spaced, radially extending first and second surfaces facing said first and second side walls of said casing, respectively, forming a blade system open between impeller blades at its radial end; and a pair of flow chambers, one flow chamber formed in each of said impeller cover and said impeller housing and axially on either side of said impeller, for defining a flow path between said fluid inlet and said single fluid outlet, said flow path defining at least one of said chambers tapering axially along substantially all of its length between said fluid inlet and said single fluid outlet such that a first cross-sectional area at said fluid inlet is greater than a second cross-sectional area at said single fluid outlet.
  • 2. The regenerative pump as stated in claim 1, further comprising:said flow path defining means tapering axially inward toward said impeller from said fluid inlet to said fluid outlet.
  • 3. The regenerative pump as stated in claim 2, further comprising:said flow path defining means tapering axially inward toward said impeller at a constant slope from said fluid inlet to said fluid outlet.
  • 4. The regenerative pump as stated in claim 1, further comprising:said flow path defining means formed asymmetrically in said first and second side walls of said casing around said axis of rotation for directing fluid back toward said impeller as said impeller rotates.
  • 5. The regenerative pump as stated in claim 1, wherein said flow path defining means further comprises:at least one of said first and second side walls having a generally ring-shaped, side channel portion formed in said casing around said axis of rotation for directing fluid toward said impeller as said impeller rotates.
  • 6. The regenerative pump as stated in claim 5, further comprising:said side channel portion generally perpendicular to and along an arc of constant radius centered on said axis of rotation.
  • 7. A regenerative pump for adding energy to a fluid comprising:a casing being radially split and including an impeller housing and an impeller cover having a fluid inlet and a single fluid outlet separated by a stripper, said casing having axially spaced, radially extending first and second side walls defined therein; an impeller having a series of impeller blades enclosed within said casing, and said impeller having an axis of rotation and axially spaced, radially extending first and second surfaces facing said first and second side walls of said casing, said impeller being open between impeller blades at its radially outer end, respectively; and a pair of flow chambers, one flow chamber being formed in each of said impeller cover and said impeller housing and axially on either side of said impeller for defining a flow path between said fluid inlet and said single fluid outlet, said flow path defining means continuously tapering in an axial direction inward along substantially all of its length toward said impeller from said fluid inlet to said single fluid outlet as said fluid is directed back toward said impeller as said impeller rotates.
  • 8. A regenerative pump for adding energy to a fluid comprising:a casing having a fluid inlet and a fluid outlet separated by a stripper, said casing having axially spaced, radially extending first and second side walls; an impeller enclosed within said casing, and said impeller having an axis of rotation and axially spaced, radially extending first and second surfaces facing said first and second side walls of said casing, respectively; and means, formed in at least one side wall of said casing, for defining a flow path between said fluid inlet and said fluid outlet, and said flow path defining means tapering axially inward toward said impeller from said fluid inlet to said fluid outlet as said fluid is directed back toward said impeller as said impeller rotates.
  • 9. The regenerative pump as stated in claim 8, further comprising:said flow path defining means having a first cross-sectional area at said fluid inlet and a second cross-sectional area at said fluid outlet wherein said second cross-sectional area is 25% less than said first cross-sectional area.
  • 10. The regenerative pump as stated in claim 8, further comprising:said flow path defining means tapering axially inward toward said impeller at a constant slope from said fluid inlet to said fluid outlet.
  • 11. The regenerative pump as stated in claim 8, further comprising:said flow path defining means formed asymmetrically in said first and second side walls of said casing around said axis of rotation for directing fluid back toward said impeller as said impeller rotates.
  • 12. The regenerative pump as stated in claim 8, wherein said flow path defining means further comprises:at least one of said first and second side walls having a generally ring-shaped, side channel portion formed in said casing around said axis of rotation for directing fluid toward said impeller as said impeller rotates.
  • 13. The regenerative pump as stated in claim 12, further comprising:said side channel portion generally perpendicular to and along an arc of constant radius centered on said axis of rotation.
  • 14. A regenerative pump for adding energy to a fluid comprising:an impeller having a series of impeller blades, an axis of rotation and axially spaced, radially extending first and second surfaces and being open between impeller blades at its radially outer most end; a radially split casing for forming an impeller housing and an impeller cover portion enclosing the impeller and having a fluid inlet with a first cross-sectional area and a single fluid outlet with a second cross-sectional area separated by a stripper, the casing having axially spaced, radially extending first and second side walls, said first and second side walls facing said first and second surfaces of said impeller, respectively; axially and radially extending blade means formed on an outer radial periphery of said impeller for driving fluid from said inlet toward said outlet as said impeller rotates about said axis of rotation; and a generally ring shaped side channel portion formed by a flow channel formed in each of said housing and cover portions at least one of said flow channels defining a flow path between said fluid inlet and said single fluid outlet, and said side channel portion tapering on a constant slope axially inward along substantially all of its length toward said impeller from said fluid inlet to said single fluid outlet for reducing the cross-sectional area from said first cross-sectional area to said second cross-sectional area by from about 10% to about 50% and directing fluid back into contact with blade means as said impeller rotates.
  • 15. The regenerative pump as stated in claim 14, further comprising:said side channel portion tapering axially inward toward said impeller at a constant slope from said fluid inlet to said fluid outlet.
  • 16. The regenerative pump as stated in claim 14, further comprising:said side channel portion formed asymmetrically in said first and second side walls of said casing around said axis of rotation for directing fluid back into contact with said blade means as said impeller rotates.
  • 17. The regenerative pump as stated in claim 14, further comprising:said side channel portion generally perpendicular to and along an arc of constant radius and centered on said axis of rotation.
  • 18. The regenerative pump as stated in claim 14, further comprising:said casing radially split and including an impeller housing and an impeller cover wherein said side channel portion is formed in both said impeller housing and said impeller cover.
  • 19. The regenerative pump as stated in claim 14, further comprising:said side channel portion having a constant radial width extending from said fluid inlet to said fluid outlet.
Parent Case Info

The following is a continuation of Ser. No. 08/596,612 filed Feb. 5, 1996 abandoned, which is a Continuation-In-Part application of application Ser. No. 08/253,543 filed on Jun. 3, 1994 now U.S. Pat. No. 5,527,149.

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Entry
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Continuations (1)
Number Date Country
Parent 08/596612 Feb 1996 US
Child 09/439320 US
Continuation in Parts (1)
Number Date Country
Parent 08/253543 Jun 1994 US
Child 08/596612 US