[0001] The present invention relates to a pump and method of using same.
[0002] The present invention preferably provides a bladeless pump and method of using the
same to transfer either a single phase fluid or multiphase fluid from a first location
to a second location without damaging the material that comprises the innerphase,
even when the inner phase is of an extremely frangible nature such as the red blood
cells in blood.
[0003] The present invention may provide a bladeless pump that can be used to pump such
diverse materials as fruits, vegetables and berries, as well as marine animals that
include fish, shrimp, crustaceans and the like from a first to a second location when
the materials form the inner phase of a fluid in which the outer phase is a liquid.
[0004] The present invention may provide a pump that is substantially free from cavitation
and erosion, and one that is capable of transferring a liquid that tends to froth
from one location to a second location with a minimum of frothing.
[0005] The present invention may provide a bladeless pump that is capable of efficiently
pumping air or liquid slurries, particularly liquid slurries that have a high solids
content and may contain paper, cloth, and fibrous materials such as occur in sewage,
and also slurries that contained a high percentage of solids in the inner phase thereof,
such as pulverised coal in coal slurry.
[0006] The present invention may provide a bladeless pump capable of efficiently handling
hot geothermal multiphase fluids that contain water, dissolved solids in the water,
steam and gas vapors.
BRIEF DESCRIPTION OF THE DRAWINGS
[0007]
FIG. 1 is a perspective view of the bladeless pump;
FIG. 2 is a side elevational view of the pump shown in FIG. 1;
FIG. 3 is a transverse cross-sectional view of the pump shown in FIG. 2 taken on the
line 3-3 thereon, and illustrating a first form of the pump;
FIG. 4 is a combined vertical cross-sectional and side-elevational view of the pump
shown in FIG. 3, and taken on the line 4-4 thereof;
FIG. 5 is a transverse cross-sectional view of a second form of the bladeless pump;
FIG. 6 is a transverse cross-sectional view of a third form of the bladeless pump;
FIG. 7 is a transverse cross-sectional view of a modification of the first form of
the pump;
FIG. 8 is a transverse cross-sectional view of a fourth form of the bladeless pump;
FIG. 9 is a combined vertical cross-sectional and side elevational view of the bladeless
pump shown in FIG. 8, taken on the line 9-9 thereof;
FIG. 10 is a fragmentary transverse cross- sectional view of a modification of the
fourth form of bladeless pump;
FIG. 11 is a side elevational view of the bladeless pump shown in FIG. 8 with a modified
form of housing, with the fitting and first conduit being shown in section to illustrate
the circular cavity in the fitting that is off-centered relative to the first opening
in the first side wall to impact initial circular motion to fluid through the fitting
from the first conduit prior to the fluid entering the confined space within the pump
housing;
FIG. 12 is a horizontal cross-sectional view of a first modification of the pump structure
shown in FIG. 8 that employs the housing illustrated in FIG. 11;
FIG. 13 is a horizontal cross-sectional view of a first modification of the pump structure
shown in FIG. 3 that employs the housing structure illustrated in FIGS. 11 and 12;
FIG. 14 is a perspective view of the pump shown in FIG. 11 but modified to have the
first conduit normal to the side walls thereof and centered relative to the inlet
opening in the first side wall;
FIG. 15 is a horizontal cross-sectional view of a second modification of the pump
structure shown in FIG. 8;
FIG. 16 is a perspective view of a second modification of the pump shown in FIG. 3;
and
FIG. 17 is a longitudinal cross-sectional view of the pump shown in FIG. 16 taken
on the line 17-17 thereof.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0008] Each of the various-forms of the invention and the modifications thereof specifically
identified in the above description of the drawings, include the pump housing assembly
B and D shown in FIGS. 1 and 11. Pump housing assembly B includes first and second,
laterally spaced side pieces 10 and 12 that are illustrated in the drawings as having
lower horizontal edges 10a and 12a that are adapted to rest on or be secured to a
suitable supporting surface (not shown).
[0009] The first and second side pieces 10 and 12 have a circular end piece 14 extending
therebetween, which end piece is secured to the side pieces by screws 15 or other
suitable fastening means. Side pieces 10 and 12 and end piece 14 cooperate to define
a vertically extending, circular confined space C'of substantial width.
[0010] The first side piece 10 has a first opening 16 therein that is centered relative
to the circular end piece 14. A fitting 18 is in fixed sealing relationship with the
exterior surface of the first side piece 10. The fitting 18 has an off centered first
passage 20 defined in the interior thereof that is in communication with the first
opening 10, as well as the interior of a first upwardly and outwardly extending conduit
22. The passage 20 is of such curved configuration that initial rotary motion is imparted
to the fluid flowing therethrough prior to the fluid entering the confined space C.
The first conduit 22 extends to a first location (not shown) at which the fluid to
be pumped is stored Or is available to be pumped.
[0011] A second opening 24 is formed in the second end piece 12 and is preferably coaxially
aligned with the first opening 16. The second opening 24 has a bearing 28 operatively
associated therewith, and the bearing supporting a shaft 30 that extends into the
confined space C and is normally disposed to the second end piece 12. A seal 28 is
mounted on the exterior portion of the end piece 12 and is in rotatable sealing engagement
with the shaft 30.
[0012] The shaft 30 has an interiorly position shouldered end portion 32. The end portion
32 of the shaft 30 most remote from the second end piece 12 is illustrated as being
driven by a prime mover 34, wuch as an electric motor or the like. A flat disc 36
is disposed within the confines of the confined space C, with the disc having a centered
opening therein through which the shouldered end portion 32 of the shaft 30 extends.
An apertured plato 38 is mounted on the first end portion 32 of the shaft 30, and
is urged into pressure abutting contact with the central portion of the disc by a
nut 40 that engages the first end 32. When the nut 40 is tightened the disc 36 is
frictionally gripped between the shouldered end portion 32 and plate 38 and cannot
rotate relative to the shaft.
[0013] A number of circumferentially spaced pins 42 are illustrated in FIG. 3 as projecting
from the disc 36, with the pins having externally threaded free end portions adjacent
the first side piece 10 that are engaged by nuts 44. A number of ring-shaped discs
46 are provided and disposed within the confined space C as shown in FIG. 3, with
the ring-shaped discs having a number of circumferentially spaced openings therein
that engage the pins 42. Spacers 50 are mounted on the pins 42 and situated between
the ring-shaped discs 46, with the discs defining ring-shaped spaces 52 therebetween.
The ring-shaped discs 46 have inner peripheries 54 that are axially aligned and cooperate
to define a transverse second passage 56 as shown in FIG. 3, which second passage
is in communication with the ring-shaped spaces 52 defined between the ring-shaped
discs 46.
[0014] When the disc 36 and ring-shaped discs 46 are rotated concurrently by the prime mover
32 driving the shaft 30, fluid that has entered the confined space C tends to rotate
therein as a circular mass. In FIG..4 it will be seen that this circular mass of fluid
rotates in a counterclockwise direction and as the fluid so rotates it discharges
through a tangentially disposed discharge outlet 58 in the upper portion of the housing
B to subsequently flow through a diverging tubular member 60 to a second conduit 62
which conduit leads to a second location (not shown) at which it is desired to pump
the fluid. The tubular member 60 is illustrated in FIG. 1 as formed from extensions
of the side walls 10 and 12 and end wall 14. Fluid in flowing through tubular member
60 decreases in velocity with an accompanying increase in the static pressure head
thereon.
[0015] When prime mover 32 is rotating the disc 36 and the ring-shaped discs 46 concurrently
as a unit, boundary layers of the fluid will adhere to the disc 36 and ring-shaped
discs 46 adjacent the ring-shaped spaces 52. Such boundary layers adhere to the disc
36 and ring-shaped discs 46 and occupy substantially fixed positions thereon. These
boundary layers are sheared from the balance of the fluid in the confined space C
as the disc 36 and ring-shaped discs 46 rotate, and this shearing imparting sufficient
rotary force to the circular body of fluid in the confined space to cause the circular
body of fluid to rotate in a counterclockwise direction. As the fluid so rotates in
the counterclockwise direction a portion thereon flows through the discharge outlet
58 and ultimately through the member 60 and second conduit'62 to the second location
(not shown). As fluid leaves the housing B as above-described, additional fluid flows
into the confined space C from the first passage 20. The fluid in entering the second
passage 56 has a low rotational velocity. As fluid is discharged from the outlet 58,
this fluid that has entered the second passage 56 tends to flow outwardly through
the spaces 52. The spaces 52 aro each in width substantially greater than twice the
thickness of the boundary layer of fluid on the ring-shaped discs 46 that define the
ring-shaped spaces 52 to provide maximum shearing force on the outwardly moving fluid.
The outwardly moving fluid is subjected concurrently to two forces, the first being
a radially directed force, and the second a centrifugal force, with the centrifugal
force increasing as the fluid moves outwardly from the second recess 56. As a result
of these two forces, fluid after entering the second recess 56 and discharging therefrom,
pursues a spiral path prior to discharging from the discharge outlet 58.
[0016] The interior surfaces of the first and second side pieces 10 and 12, as well as the
end piece 14 also have boundary layers of fluid that tend to adhere thereto, and as
the circular body of fluid rotate in the confined space C, the shearing of these boundary
layers from the rotating body of fluid tends to restrain the rotation of the body
of fluid in the confined space. Thus, the rate at which the flat disc 36 and ring-shaped
discs 46 are rotated concurrently must be at such a rate that the drag force imposed
on fluid moving outwardly through the ring-shaped spaces 52 is sufficient to impart
rotary motion.to the body of fluid in the circular confined space and overcome the
tendency of the boundary layers on the interior surfaces of the first and second side
pieces 10 and 12 and end piece 14 to resist such rotary motion. in the forms of the
invention shown in FIGS. 12, 13 and 15, this resisting tendenoy is minimized by the
side surfaces that define the confined space C being free to rotate with the circular
body of fluid. Under such circumstances there is a minimum differential between the
rate of rotation of the circular body of fluid and the side surfaces that partially
define this body of fluid.
[0017] The first form A-1 of the invention above-described is capable of being used to pump
either single phase or multiphase fluid from a first location to a second location.
When a multiphase fluid is being pumped in which the first phase is a liquid or gas,
and the second phase a number of spaced solid objects, the spaces 52 must be of sufficient
width as to allow the objects of largest cross section to move therethrough with the
gaseous or liquid phase with which they are associated.
[0018] From an experience it has been found that the boundary layers of a fluid, either
gaseous or a liquid, are not penetrated by solid objects entrained therewith, and
as a result when a multiphase fluid is being pumped that contains solid objects, these
objects will not contact the inner surface of the housing assembly B or the surfaces
of the disc 36 or ring-shaped discs 46. Thus, the solid objects have minimum abrasive
action on the surfaces of the pump during the passage therethrough. The pump A is
also free of cavitation, for bubbles entrained with the fluid are not physically contacted
by any lifting surfaces and pass between the discs They enter the pump as bubbles
and discharge from the pump as bubbles, although smaller as a result of the increased
pressure at the discharge.
[0019] The second form of the invention A-2 shown in FIG. 5 is similar to the first form,
other than that the disc 36 and the ring-shaped discs 46 have outer peripheral portions
that taper towards one another and are identified on the drawing by the notation 36a
and 46a. Due to the above-mentioned construction in the second form A-2 of the pump,
the fluid will tend to remain in the spaces 52 a greater length of time, and will
be subjected to rotary shear for a greater length of time, to be delivered to the
discharge outlet 58 at a higher pressure than would normally be achieved when the
first form A-l of the pump is' used. In FIG. 5 it will be seen that the second form
A-2 of pump also has the outer peripheral portions of the first and second side pieces
10a and 12a tapering inwardly towards one another.
[0020] The third form A-3 of the pump is shown in FIG. 6 differs from the first form A-l
only in that the ring-shaped discs 46 are not of uniform wall thickness, but taper
outwardly from the inner periphery 54 thereof and are of maximum thickness at the
outer periphery of the discs. The ring-shaped discs 46 of the above-described structure
result in ring-shaped spaces 52 being defined therebetween when spacers 50 are mounted
on the pins 42, which ring-shaped spaces are of maximum width adjacent inner periphery
54 and are of minimum width adjacent the outer periphery of the ring-shaped discs
46. By varying the wall thickness of the ring-shaped discs 46 as shown in FIG. 6,
the rotary boundary layer drag on the fluid as it rotates as a circular body within
the confined space C, may be conveniently varied, to provide fluid at the discharge
outlet 58 of a desired pressure.,
[0021] In FIG. 7 a modification A'-1 of the first form of the invention is shown, with the
modified form A'-1 varying from the first form only in that the inner peripheries
54 of the ring-shaped discs 46 vary in diameter, and this. variance in diameter varying
the area of the surfaces of the ring-shaped discs 46 that may impose a rotary motion
to the circular body of the fluid in the confined space C, as the ring-shaped discs
46 and disc 36 rotate relative thereto.
[0022] The fourth form A-4 of the invention as shown in FIG. 8 differs from the first form
A-l in that the flat. disc 36 and ring-shaped discs 46 are removed from the first
form and replaced by a single disc 64 that has a centered hub 66 that has an opening
therein that engages the shouldered end 32 of the shaft 30 and is held thereon by
a nut 40. The hub 66 is illustrated in FIG. 8 as having the major portion thereof
curve radially in a stream line configuration. The disc 64 as may be seen in FIG.
8 extends towards the interior surface of the second side piece 12. The fourth form
A-4 of the pump is particularly adapted for use in transferring multiphase fluid from
a first to a second location, such as when the first phase is a liquid, and the second
phase a number of objects, such as potatoes, cherry tomatoes, fruits, vvegetables,
and marine animals including fish, shrimp, and the like. When the confined space C
has been filled with a multiphase fluid from the first location as previously described,
the prime mover 32 is actuated to cause rotation of-the disc 64, and this disc when
rotated in a counterclockwise direction as viewed in FIG. 9 imparting circular motion
to the circular body of fluid within the confined space C. The body of fluid is rotated
due to the boundary layer adhereing to the disc 64 and hub 66 being sheared therefrom
by rotation of the disc, and this shearing force imparting rotary motion to the circular
body of multiphase fluid in the confined space . C. As the circular body of fluid
in the confined space C rotates clockwise, the solid objects in the first liquid phase
are subjected to increasing centrifugal force as they move outwardly relative to the
hub in a generally spiral path to be ejected with the liquid first phase sequentially
through the discharge outlet 58 to flow through the conduit 62 to the second location.
For either single phase or multiphase fluid to discharge from the discharge outlet
58, the rate of rotation of the disc 64 and hub 66- must be sufficient as to generate
a rotary shearing force on the circular body of the fluid in the confined space C
as to cause the same to rotate, and overcome the shearing of the boundary layers on
the interior surfaces of the first and second side pieces 10 and 12 and end piece
14 that tead to resist such rotation.
[0023] A modification A'-4 of the fourth form of the invention is shown in FIG.10, which
includes a number of circumferentially spaced pins 42 that project from the . disc
64 towards the first end piece 10, with the pins engaging pairs of ring-shaped discs
46. The ring-shaped discs 46 in each pair are separated by a spacer 68 mounted on
one of the pins 42, and the spacer resulting in each pair of ring-shaped discs having
a ring-shaped space 70 defined therebetween through which fluid may discharge outwardly
towards the end piece 14 as the disc 64 and ring-shaped discs 46 rotate in unison.
The pairs of ring-shaped discs 46 are separated from the disc 64 and from one another
by spacers 72 mounted on the pins 42, and these spacers being of a soft resilient
material such as rubber or the like. As the fluid flows into the confined space C
through the first opening 16, the fluid whether single phase or multiphase is subjected
to rotary motion by rotation of the disc 64 and the pairs of adjacently disposed ring-shaped
discs 46. This rotary motion occurs due to the shearing of the boundary layer on the
disc 64, and on the ring-shaped discs 46, from the balance of the circular body of
fluid in the confined space C, and this shearing imparting rotary motion to the circular
body of fluid to cause the same to be ejected from the discharge opening 58 as previously
described. The spacing between the disc 64 and the pairs of ring-shaped discs 46 must
be sufficiently great that the largest of the solids entrained with the fluid are
able to pass radially therethrough as thcy describe substantially spiral patha prior
to being ejected from the discharge opening 58. The spaces 70 between the pairs of
spaced ring-shaped discs 46'provide additional surfaces on the ring-shaped discs 46
that have boundary layers thereon that are sheared from the baiance of the circular
body of fluid, and increase the circular drag on the circular body of fluid as the
disc 64 and pairs of ring-shaped discs 46 rotate relative thereto. Due to the increased
areas that have boundary layers thereon that rotate relative the circular body of
fluid, the drag force imposed on the circular body of fluid will be sufficiently great
as to overcome the resistance drag force imposed by boundary layers on the interior
surfaces of the first and second side pieces and end piece 14. As a result fluid entering
the confined space C may be caused to rotate when the shaft 30 is rotated at a relatively
slow speed. The spacers 72 serve a dual function, not only of maintaining the pairs
of ring-shaped discs 46 in laterally spaced relationship with one another, but preventing
damage to frangible objects entrained with a liquid or gas as the object and liquid
are caused to flow through the modified form A'-4 of the fourth form of the invention
to discharge to the second location through the second conduit 62.
[0024] The pump D illustrated in FIGS. 11 and 3.2 is a first modification of the bladeless
pump illustrated in FIG. 8 and has a housing 69 that includes first and second laterally
spaced side walls 70 and 72 that have extensions 70a and 72a that partially define
the diverging outlet structuro 74 as' shown in FIG. 14. An end wall 76 is disposed
between the first and second side walls and cooperates therewith to define a circular
confined space 78 of substantial width. The end wall 76 has spaced extensions 76a
that cooperate with the extensions 70a and 72a to define the diverging outlet structure
74.
[0025] The first and second side walls 70 and 72 on the adjacent faces thereof have circular
ribs 70b and 72b that project towards one anotherand are in abutting sealing contact
with oppositely disposed side surfaces of end piece 76. The end piece 76 as may be
seen in FIG. 12 is of greater thickness than the depth of the ribs 70b and 72b and
cooperates with the ribs to define first and second circular recesses 80 and 82 shown
in FIG. 12.
[0026] First side wall 70 has a centered first opening 84 therein that serves as a fluid
inlet. A fluid conducting fitting 86 is secured to the exterior surface of first side
wall 70 as illustrated in FIGS. 11 and 12. The fitting defines a generally circular
cavity 88 within the interior thereof that is of substantially greater diameter than
the first centered opening 84 in first side wall 70, which first opening serves as
a fluid inlet. Cavity 88 and first opening 84 are in communication but off centered
relative to one another. Cavity 88 is also in communication with a longitudinal .passage
90 in a first conduit 92 that extends to a first location (not shown) where the fluid
to be pumped is situated. The passage 90 is tangentially disposed relative to cavity
88. Fluid entering the cavity 88 from passage 90 has initial, rotary motion imparted
thereto prior to discharging into confined space 78 through the first opening 84..
The first side wall 70 has a ring-shaped boss 94 projecting inwardly from the interior-surface
thereof as shown in FIG. 12, which surrounds first opening 84. Boss 94 supports a
bearing 96 that in turn rotatably supports a first circular plate 98 that has the
circumferential edge portion slidably and rotatably disposed in first circular recess
82. Ribs 70b, 72b and end piece 76 have spaced transverse bores (not shown) therein
through which bolts 100 extend that hold the housing together as an integral unit.
[0027] Second side wall 72 has a second opening 102 therein that is preferably axially aligned
with first opening. 84. A power driven shaft 104 extends into confined space 78 through
second opening 102, and is rotatably supported by a bearing and seal 106 that is preferably
secured to the exterior surface of second side wall 72. The shaft 104 has an externally
threaded shouldered end portion 108 situated within confined space 78 that extends
through an opening (not shown) in the hub portion 110 of a disc 112 that has a diameter
less than that of the confined space 78. A nut 113 engages threaded end portion 108
and serves to removably secure disc 112 thereto. The disc 112 preferalby includes
a reinforcing structure 114 in engagement with shaft 104.
[0028] A-second circular plate 114 is rotatably supported on shaft 104 and is disposed between
disc 112 and the interior surface of the second side wall 72. Second plate 114 is
of such diameter that the peripheral edge portion thereof. is rotatably disposed in
the second circular recess 82.
[0029] When driven shaft 104 rotates,disc 112 rotates concurrently therewith. Fluid that
has initial rotation imparted thereto in fitting 86 flows into confined space 78 and
due to rotational drag imparted thereto by disc 112 rotates in the confined space
78 is subjected to a minimum restraining force in the housing 69 as the first and
second plates 98 and 114 are free to rotate therewith. The fluid as it rotates in
confined space 78 sequentially flows through the diverging discharge structure 74
to a second conduit 114 that leads to a second location (not shown) to which it is
desired to transfer the fluid. Shaft 104 is maintained by conventional means (not
shown) at a fixed position relative to housing 69. The disc 112 is separated from
second plate 114.by a space 116.
[0030] The pump E illustrated in FIG. 13 employs the assembly of elements common to the
pump D, but with the disc 112 being replaced by a rotor assembly 120. Elements of
the pump E common to the pump D illustrated in FIG. 12 are identified by the numerals
previously used but with primes . being added thereto.
[0031] The disc 112 of pump D is replaced by a flat first disc 122 in pump E that forms
a part of rotor assembly 120. Disc 122 has a number of circumferentially spaced pins
124 projecting therefrom that extend towards first side wall 98'. The pins 124 serve
to support a number of second discs 126 thereon which discs are of ring-shape and
are held in spaced relationship with one another in the same manner as described.
in detail with the pump illustrated in FIG. 3. The inner peripheries 128 of the second
discs 126 define a second transverse passage 130 that is in communication with ring-shaped
spaces 132 formed between the second discs 126. The second pump E operates in the
same manner as the pump illustrated in FIG. 3, but requires less power to operate
as the first and second plates 98' and 114' are free to rotate with the rotating body
of fluid in the confined space 78'. Thus, as the body of fluid rotates in the confined
space 78' there is a minimum in the differential in the rate of rotation of the body
of fluid and the side plates 98' and 114'.
[0032] The pump F shown in FIG. 14 is of the same internal structure as pump D illustrated
in FIG. 11, and differs from pump D in that fitting 86 is eliminated, with first conduit
92 being disposed normal to the pump housing and in direct communication with first
opening 84.
[0033] The pump G shown in FIG. 15 is of the same general structure as the pump D, and differs
from the'latter by having the second plate 114 omitted, and the disc 112" of such
diameter that the peripheral portion thereof is rotatably disposed in second recess
82". Elements in pump G common to pump D are identified on the drawings by the same
numerals previously used but with double primes being added thereto. Pump G operates
in the same manner as pump D illustrated in FIG. 12. Pumps D and G are particularly
adapted for pumping multiphase fluids in which the inner phase has a high content
of solids and may contain pieces of paper, rags and other fibrous or stringy materials.
Such materials have no adverse effect on the operation of these. pumps.
[0034] The pumps D and G are useful in transferring objects, either animate or inanimate
from a first location to a second location. The objects are mixed with fluid at a
first location to.provide a multiphase fluid in which the outer phase is fluid and
the inner phase the objects. The objects may have such diverse physical characteristics
as those common to vegetables, fruits and berries, as well as to fish, shrimp, crustaceans
and the like, as well as to granular materials such as powdered coal. The multiphase
fluid may also be either a liquid or air slurry, raw or partially treated sewage and
the like.
[0035] The pump J illustrated in FIGS. 16 and 17 includes a housing 200 that is defined
by two laterally spaced side pieces 202 and an arcuate end piece.204 that extends
therebetween to define a circular confined space 206. The end piece 206 has extensions
projecting therefrom that cooperate with extensions of the side pieces 204 to define
a fluid discharge 208 that is preferably of diverging configuration. The side piece
202 have transversely aligned fluid inlet openings 210 therein as may best be seen
in FIG. 17.
[0036] Fluid may flow from a source (not shown) through a conduit 212,'which conduit develops
adjacent the pump J into a pair of conduit extensions 214 of lesser transverse cross-section
that are in communication with the inlet openings 210. The conduit extensions 214
have laterally spaced bosses 216 projecting outwardly therefrom, with the bosses being
axially aligned and centered relative to the inlet opening 210. Each boss supports
a bearing 218 and a low pressure seal 220, both of which may be of conventional present
day design.
[0037] The bearings 220 rotatably support a shaft 222 that is in sealing engagement with
the seals 220, and the shaft extending transversely across confined space 206. Shaft
222 by a coupling 224 is connected to the drive shaft 226 of a prime mover.228, preferably
an electric motor.
[0038] Shaft 222 at the center of confined space 206 has a circular plate 230 of substantial
strength secured thereto. A number of elongate, circumferentially spaced rigid members
232 extend outwardly equal distances from opposite sides of the plate, which members
may be bolts or the like. The members 232 in cooperation with spacers 234 mounted
thereon serve to support two sets of ring-shaped discs 236 on opposite sides of the
plate 230. The ring-shaped discs 236 have axially aligned centered opening 238 therein.
The .ring-shaped discs 236 in each set are separated by spaces, 240.
[0039] When prime mover 228 is operating, the plate 230 and the two sets of ring-shaped
discs 236 are rotated concurrently. Fluid is drawn into the confined space 206 through
inlet openings 210 at the same rate and exerts oppositely directed forces on the plate
230, and as a result the shaft 222 has no appreciable longitudinal thrust exerted
thereon. The fluid after entering.confined space 206. is discharged therefrom through
fluid discharge 208 in the same manner as in pump A-1 shown in FIG. 3.
[0040] The bladeless pumps have been described previously in detal as to structure and the
method of using the same and need not be repeated.
1. A method of concurrently pumping a plurality of solid objects that may be of a
frangible nature and a fluid in which they are disposed from a first location to .a
second location without damage to said objects, said method comprising the steps of:
a. defining a vertically extending circular . confined space between first and second
laterally spaced side surfaces that are connected by a circular end surface of substantially
greater width than the maximum dimension of each of said objects, said confined space
situated intermediate said first and second locations, said first side surface having.a
centrally disposed inlet opening therein of sufficient transverse area as to permit
said objects to pass therethrough, and said end surface having a discharge .opening
in the portion thereof of highest-elevation through which said objects may pass;
b. providing a substantially smooth rotatable circular surface in said confined space
intermediate said first and second side surface and rotatable in a plane substantially
parallel thereto;
c. rotating said circular surface in said confined space in a first direction at not
less than a first rate;
d. allowing said fluid with said objects entrained therewith to sequentially flow
from said first location through said inlet opening into said confined space and be
transformed into a circular rotating body of said fluid by the rotation of said circular
surface, said circular surface having a first boundary layer of said fluid that adhores
thereto that is sheared from the balance of said circular body. of said fluid as said
circular surface rotates, said shearing imparting said rotary motion to said circular
body of fluid and said objects in said confined space, and said first rate of sufficient
magnitude as to impose a centrifugal force on said objects to the extent that they
sequentially follow spiral paths outwardly through said rotating body of fluid in
said confined space and be sequentially ejected through said discharge opening together
with said fluid from said confined space;
e. sequentially conducting fluid and said objects ejected through said discharge opening
to said second location.
2. The method as defined in Claim 1 in which said first side surface is free to rotate
with said body of fluid in said confined space.
as defined in said first and second side surfaces are free to rotate with said body
of fluid in said confined space.
4 . A pump for use in transferring either a single phaso or multiphase fluid from
a first location to a second location which includes:'
a. a housing assembly that includes first and second vertically disposed, laterally
spaced first and second side walls and'a continuous end wall that extends transversely
therebetween to cooperate therewith to define a circular confined space, a centrally
disposed first opening in said first side wall in communication with said first location,
a discharge opening in said end wall that is at a higher elevation than said first
opening and is in communication with said second location, and a second .opening in
said second side wall that is oppositely disposed from said first opening, said housing
assembly formed from a rigid material resistant to action by said fluid;
b. a rotatable drive shaft that has first and second ends;
c. bearing and seal means supported in a fixed relationship with said second end wall
and coaxially aligned with said second opening therein, said bearing and seal means
rotatably supporting said drive shaft, with said first end of the latter disposed
within said confined space and adjacent the latter;
d. a substantially smooth first circular disc in said confined space secured to said
first end of said drive shaft and intermediately positioned between said'first and
second side walls with said second end of drive shaft when rotated at greater than
a first rate causing a circular body of said fluid in said confined space to rotate
due to a rotary forco oxerted on said body of fluid as a boundary layer of said fluid
on the exterior surface of said first circular disc is rotated relative to said body
of water to be sheared therefrom, and said fluid entering said confined space through
said first opening having increasing rotary velocity imparted thereto to sequentially
move outwardly in a spiral path due to the centrifugal force imposed thereon and be
sequentially ejected from said discharge opening to flow to said second location.
5. A pump as defined in Claim 18 in which said fluid is a multiphase includes a first
phase that is liquid and a second phase that is a plurality of objects of a non-flowable
nature disposed in said first phase, and said first opening, discharge opening and
the transverse spacing between said disc and first side wall being of sufficient magnitude
to permit said first and second phases to flow through said confined space concurrently
in said spiral paths to be ejected through said discharge opening.
6. A pump as defined in Claim 19 in which said first side wall and end wall at the
junction thereof define a circumfcrcntially extending first recess that is in communication
with said confined space, and said pump in addition including;
e. a first ring-shaped side plate rotatably supported in said confined space adjacent
said first side wall, and said first side plate having the outer peripheral edge portion
thereof rotatably supported in said recess, said first side plate including a centered
opening axially aligned with said first opening in said first side wall, with said
first side plate free to rotate with said circular body of water to minimize the frictional
drag on said circular body of fluid as said circular body rotates relative to said
housing.
7. A pump as defined in Claim 20 which in addition includes:
f. a plurality of circumferentially spaced pins that project from said first disc
towards said first side plate; and
g. at lease one ring-shaped second disc supported on said pins in transverse spaced
relationship with said first disc and first side plate to increase the rotating area
that exerts a rotary force on said fluid in said confined space to cause the latter
to rotate as said body of fluid.