BACKGROUND
[0001] Multiphase pumps are used in a variety of pumping applications, including subsea
pumping applications involving the movement of hydrocarbon fluids having a mixture
of oil and gas. In multiphase pumps, open impellers provide open impeller blade tips
which allow fluid to leak over the blade tips through a clearance at the blade tips.
This blade tip clearance helps to mix the multiphase fluid but it also can be the
origin of a fluid induced rotor dynamic instability particularly at high head generation.
This induced instability is sometimes called the Thomas-Alford effect.
[0002] Modem pumping operations have demanded impeller systems which create increased differential
pressures. The increased differential pressures, in turn, increase the fluid forces
acting on radial support bearing systems of the multiphase pumps. The increased forces
also have caused increased vibration levels for certain operating conditions where
high energy is present in the hydraulics. In some applications, increased stability
has been provided by using shrouds placed over the blade tips to thus eliminate the
blade tip clearance and the leakage of fluid over the blade tips. However, when using
such a shroud, the mixing effect across the blade tips is lost. Additionally, this
type of shroud can be unstable during, for example, pumping of liquids with medium
to high viscosity.
SUMMARY
[0003] In general, the present disclosure provides a system and methodology for facilitating
operation of a pump, e.g. a multiphase pump. The pump may be provided with an impeller
having a plurality of impeller blades. The impeller blades have blade tips which extend
over an axial length. A ring is positioned along the blade tips to, for example, suppress
fluid induced Alford effects and to add annular seal direct stiffness to the impeller
and to thus provide rotor dynamic stability. However, the axial length of the ring
is limited relative to the axial length of the impeller blade tips to enable flow,
e.g. leakage, across the blade tips in a manner which causes active phase mixing during
pumping of a multiphase fluid.
BRIEF DESCRIPTION OF THE DRAWINGS
[0004] Certain embodiments will hereafter be described with reference to the accompanying
drawings, wherein like reference numerals denote like elements. It should be understood,
however, that the accompanying figures illustrate various implementations described
herein and are not meant to limit the scope of various technologies described herein,
and:
Figure 1 is a schematic cross-sectional illustration of an example of a multiphase
pump, according to an embodiment of the disclosure;
Figure 2 is a schematic cross-sectional illustration taken generally along line 2-2
of Figure 1 and showing an example of an impeller, according to an embodiment of the
disclosure;
Figure 3 is an illustration of a portion of a multiphase pump having an example of
an impeller combined with a ring in a manner able to provide stability and phase mixing,
according to an embodiment of the disclosure; and
Figure 4 is an illustration of a portion of a multiphase pump having another example
of an impeller combined with a ring in a manner able to provide stability and phase
mixing, according to an embodiment of the disclosure.
DETAILED DESCRIPTION
[0005] In the following description, numerous details are set forth to provide an understanding
of some illustrative embodiments of the present disclosure. However, it will be understood
by those of ordinary skill in the art that the system and/or methodology may be practiced
without these details and that numerous variations or modifications from the described
embodiments may be possible.
[0006] The disclosure herein generally relates to a system and methodology for enhancing
pumping capabilities. For example, the system and methodology facilitate operation
of a pump, e.g. a multiphase pump of the type that may be used to pump hydrocarbon-based
fluids having various mixtures of oil and gas. The pump may be provided with at least
one impeller having a plurality of impeller blades. In a variety of applications,
the multiphase pump may comprise a plurality of impellers rotatably mounted within
a pump housing. For example, the impellers may be rotationally fixed to a shaft which
may be rotated to thus rotate the impellers.
[0007] The impeller blades have blade tips which extend over an axial length, as described
in greater detail below. In some embodiments, the impellers may be combined with corresponding
diffusers to establish a desired number of pump stages disposed in the pump housing.
In such embodiments, the impellers are rotated with respect to the diffusers to effectively
pump the fluid, e.g. the multiphase fluid. During operation of the pump, fluid flows
through the diffusers as it moves from one sequential impeller to the next until being
discharged from the pump housing.
[0008] In some embodiments, each impeller has an impeller hub which may be rotationally
fixed to the shaft. The impeller blades extending radially outward from the impeller
hub may each have an impeller blade base affixed to the impeller hub and an impeller
tip located radially outward from the impeller blade base. A ring, e.g. a wear ring,
may be positioned and affixed along the blade tips to, for example, suppress fluid
induced Alford effects and to add annular seal direct stiffness to the impeller. The
ring effectively suppresses fluid induced instability to the impeller, thus providing
rotor dynamic stability during pump operation. In some embodiments, the ring extends
from blade tip to blade tip along the entire circumference of the impeller. However,
the ring may be constructed with breaks such that it extends along a portion of the
impeller circumference.
[0009] The ring of a given impeller also has an axial length, however the ring axial length
is limited relative to the axial length of the impeller blade tips. This reduced axial
length relative to the blade tips enables flow, e.g. leakage, across the blade tips
in a manner which ensures active phase mixing during pumping of a fluid, e.g. a multiphase
fluid. The ring axial length relative to the impeller blade tip axial length may vary
depending on the parameters of a given application. By way of example, the axial length
of the ring may be 80% or less of the axial length of the impeller blade tips, e.g.
15% to 80%. In other embodiments, the ring axial length may be 50% or less of the
axial length of the impeller blade tips, e.g. 15% to 50%. In various applications,
the wear ring axial length may be from 10% to 95% of the axial length of the impeller
blade tips.
[0010] The ring provides rotor dynamic stiffness to the corresponding impeller so as to
limit fluid instabilities in the impeller, the shaft, and the shaft bearings. If the
pump comprises multiple impellers, the impellers (or a desired number of the impellers)
may be combined with corresponding rings to provide the desired stiffness so as to
reduce undesirable fluid based instabilities, e.g. vibrations. In some embodiments,
wear rings may be fixed along blade tips of helico axial impellers in multiphase pumps
to reduce the fluid instabilities otherwise experienced by the impellers and the pump
shaft.
[0011] The wear ring or rings may be constructed to reduce unstable viscosity effects and
thus stabilize Lomakin effects while still allowing leakage past the blade tips to
ensure sufficiently active phase mixing during pumping. It should be noted that instability
may lead to a variety of unwanted vibrations in the impellers and/or shaft to which
the impellers are mounted. For example, at operating conditions of low gas volume
fractions and low flow rates with high differential pressures some synchronous, sub-synchronous,
or super-synchronous vibrations can occur in both forward and backward modes. The
vibrations can result from fluid induced de-stabilizing forces due to the Thomas-Alford
effect. For example, such effects may occur in forward mode for pumping devices such
as turbines and in both forward and backward modes for a variety of pumps, e.g. helico
axial pumps.
[0012] With respect to helico axial impellers, for example, substantial destabilization
forces may not be produced when the differential pressure (dP) at each pump stage
is in the range of 2-5 bars. However, when this differential pressure at each pump
stage is increased to a range of, for example, 10-30 bar, the destabilizing fluid
forces may overcome the pump bearing support forces. This can lead to unwanted vibration
unless the impeller or impellers are stiffened via the ring(s), as described in greater
detail below. The impeller construction effectively promotes active mixing of multiphase
fluids while the increased stiffness afforded by the ring(s) enables operation of
pumps at greater differential pressures and increased head without causing undue instability
of impellers, shaft, or radial bearings.
[0013] Referring generally to Figure 1, a schematic illustration is provided of an example
of a pump 20 for moving a fluid, as represented by arrows 22. The fluid 22 may be
a multiphase fluid such as a hydrocarbon-based fluid containing oil and gas. By way
of example, the pump 20 may be in the form of a helico axial pump. In subsea well
operations, the pump 20 may be in the form of a helico axial pump operated to move
hydrocarbon-based fluid which is in the form of multiphase mixtures of oil and natural
gas.
[0014] In the embodiment illustrated in Figure 1, the pump 20 comprises a pump housing 24
and a shaft 26 rotatably mounted in the pump housing 24. The shaft 26 may be rotatably
mounted on bearings 28 positioned, for example, between the housing 24 and shaft 26.
By way of example, a plurality of radial bearings 28 may be positioned along the shaft
26. Additionally, the pump 20 may comprise at least one impeller 30 and at least one
diffuser 32. In many applications, the pump 20 is constructed with a plurality of
impellers 30 and a plurality of corresponding diffusers 32 arranged in stages 34 which
may be referred to as compression stages. The number of stages 34 may vary depending
on the pumping parameters for a given application and may comprise at least 10 stages,
and sometimes at least 15 stages.
[0015] The impellers 30 may be mounted to shaft 26 for rotation with the shaft 26 during
operation of pump 20. For example, the impellers 30 may be rotationally affixed to
shaft 26 via engaged teeth, key and keyway arrangements, or other suitable mechanisms
for rotationally affixing the impellers 30 to shaft 26. The diffusers 32 may be mounted
stationary with respect to pump housing 24 and may operate to direct fluid 22 from
one sequential impeller 30 to the next. The pump 20 also comprises a discharge opening
36 or a plurality of discharge openings 36 through which the fluid is discharged from
the pump 20 after being pumped through stages 34. The discharge opening(s) 36 may
be arranged in various configurations and locations to direct the fluid 22 into a
corresponding component, e.g. a corresponding flow line.
[0016] To provide a desired rotor dynamic stiffness to each impeller 30, a ring 38 is positioned
along the outer circumference of each impeller 30. By way of example, the ring 38
may be in the form of a wear ring. In some embodiments, the ring 38 is constructed
from a different material than other portions of the impeller 30. For example, the
ring 38 may be constructed from a hardened steel, carbide based material, or other
suitable wear resistant material. Other types of materials also may be selected for
ring 38 to provide desired wear and/or operational characteristics different from
those of the other impeller material. The ring 38 provides stiffness to the corresponding
impeller 30 so as to limit fluid instabilities in both the impeller 30 and the shaft
26. If the pump comprises multiple impellers 30, the full set of impellers 30 or a
desired number of the impellers 30, e.g. a reduced number of the impellers 30, may
be combined with corresponding rings 38 to provide the desired stiffness so as to
reduce undesirable vibrations or other fluid instabilities.
[0017] With additional reference to Figure 2, each impeller 30 may comprise an impeller
hub 40 rotationally affixed to the shaft 26. Each impeller 30 further comprises a
plurality of impeller blades 42 extending radially outward from the impeller hub 40.
Each impeller blade 42 has an impeller blade base 44 and an impeller blade tip 46.
The impeller blade bases 44 may be integrally formed with the impeller hub 40 or otherwise
affixed to the impeller hub 40.
[0018] Additionally, the impeller blade tips 46 have an axial length 48 extending along
an axis 50 of the pump 20. The ring 38 also as an axial length 52, but the ring axial
length 52 is shorter than the impeller blade tip axial length 48. Each ring 38 may
be located along the impeller blade tips 46 of the corresponding impeller 30, as illustrated
in Figure 1. In some embodiments, the ring 38 extends around the entire circumference
of the corresponding impeller 30, as illustrated in Figure 2. However, other embodiments
may utilize rings 38 which extend along a portion (or portions) of the circumference
of the corresponding impellers 30.
[0019] Additionally, the axial length 52 (see, for example, Figures 1 and 3) of the rings
38 relative to the axial length 48 of the corresponding impeller blade tips 46 may
vary according to the parameters of a given pumping application. By way of example,
the ring axial length 52 may be less than 80% of the axial length 48 of the corresponding
impeller blade tips 46. In some embodiments, the ring axial length 52 may be in the
range from 30% to 80% of the axial length 48 of the impeller blade tips 46. In other
embodiments, however, the ring axial length 52 may be in the range from 30% to 50%
of the axial length 48 of the corresponding impeller blade tips 46. Other ratios also
may be used in some applications depending on various factors such as desired ring
strength/stiffness, fluid parameters, differential pressures, and/or other pumping
related parameters. It should be noted the wear ring 38 may be located at an inlet
side of the impeller 30 as illustrated. However, the wear ring 38 also may be located
at other axial positions and other positions along the blade tips 46 in some applications.
For example, the wear ring 38 may be positioned along the impeller blade tips 46 at
the impeller inlet side, the impeller outlet side, or at various positions therebetween.
[0020] The ratio of ring axial length 52 to impeller blade tip axial length 48 is selected
based on the desired stiffening of the corresponding impeller 30 and the desired mixing
of multiphase fluids for a given set of pumping conditions and parameters. The desired
mixing of multiphase fluids results from allowing leakage of fluid 22 past the impeller
blade tips 46 to a gap 54, e.g. a clearance, between the impeller blade tips 46 and
a surrounding housing. In other words, the axially shorter ring 38 does not prevent
flow of fluid in a radially outward direction past impeller blade tips 46 and into
gap 54 (thus promoting mixing). The surrounding housing may be an inside surface of
pump housing 24, a portion of a corresponding diffuser 32 extending along the impeller
30, or another suitable housing. It should be noted the contact surface between the
ring 38 and the impeller blade tips 46 may be a continuous fixed interphase or it
may include bores, slots, and/or other features to provide for fluid flow and mixing
through the bores, slots, and/or other features.
[0021] The leakage or flow of fluid through gap 54 past the impeller blade tips 46 ensures
sufficiently active phase mixing during pumping. By limiting the axial extent of the
ring 38, this flow past the impeller blade tips 46 and resultant mixing is allowed
to occur. Thus, the reduced axial length 52 of ring 38 stiffens the impeller while
still enabling substantial mixing of multiphase fluids to ensure, for example, stable
performance of the impellers 30 even with high viscosity fluids 22.
[0022] Furthermore, the rings 38 are able to reduce or eliminate unstable Bernoulli effects
and thus reduce unstable cross coupled stiffness. In some embodiments, each ring 38
may be positioned along the corresponding impeller 30 to allow for blade tip flow
at a latter part (downstream part) of the impeller blade tips 46 to provide the desired,
active phase mixing. Furthermore, the differential pressure acting on each impeller
30 is mainly created for the first half of the impeller 30. By positioning the ring
38 along the first half of the corresponding impeller 30, the ring 30 is exposed to
the higher differential pressures, thus improving stabilization of the Lomakin effect.
[0023] Referring generally to Figure 3, an embodiment of impeller 30 is illustrated. In
this example, ring 38 is in the form of a wear ring which extends radially outwardly
of the impeller blade tips 46. In some embodiments, the wear ring 38 may be received
in a corresponding slot 56 formed in a surrounding housing 58. As described above,
the surrounding housing 58 may be a portion of the corresponding diffuser 32 as illustrated
in Figure 3. However, the surrounding housing 58 also may be a portion of pump housing
24 or part of another component of pump 20.
[0024] The wear ring 38 may be integrally formed with impeller blades 42. However, the wear
ring 38 also may be a separate component affixed to the impeller blade tips 46 of
the impeller blades 42. By way of example, the wear ring 38 may be affixed to impeller
blades 42 via brazing, welding, adhesive, or other suitable fastening technique. The
fastening technique also may depend on the similarity or dissimilarity of the materials
used to form the wear ring 38 and the impeller blades 42. Additionally, the contact
surface between the ring 38 and the impeller blade tips 46 may be a continuous fixed
interphase or it may include features 60, e.g. bores or slots, to provide for fluid
flow and mixing through the features 60.
[0025] Referring generally to Figure 4, another embodiment of impeller 30 is illustrated.
In this example, the ring 38 also may be in the form of a wear ring. However, the
wear ring 38 is radially coextensive with the impeller blade tips 46. In other words,
the radially outlying surface of the wear ring 38 does not extend radially outwardly
of the impeller tips 46. With either of these embodiments, gap 54 remains between
the impeller blade tips 46 and the surrounding housing 58 along a portion of the axial
length 48 to ensure a desired, substantial mixing of the multiphase fluid 22 as it
is pumped along the interior of pump housing 24 during operation of pump 20.
[0026] It should be noted the ring 38, e.g. wear ring, may be combined with various types
of impellers 30 at different positions along the impeller blade tips 46. In many types
of pumping applications, the impellers 30 may be in the form of helico axial impellers.
For example, each impeller blade 42 may be arranged along the impeller hub 40 in a
generally helical shape. In some embodiments, individual impellers 30 may have more
than one wear ring 38 positioned at desired locations along the impeller blade tips
46, e.g. inlet side, outlet side, and/or suitable positions therebetween. Additionally,
a surface 62 of wear ring 38 adjacent surrounding housing 58 may act as a seal surface
and may have various configurations. For example, the wear ring surface 62 may be
in the form of a plain annular seal, a labyrinth seal, a pocket damper seal, or a
stepped diameter segmented seal.
[0027] The use of wear rings 38 positioned along the blade tips 46 of impeller blades 42
provide impellers 30 with improved rotor dynamic stiffness and dampening. Effectively,
the rings 38 work to stabilize an open axial impeller 30 where fluid mixing and viscosity
effects may be important factors during pumping operations. However, the reduced axial
length 52 of the rings 38 relative to the corresponding impeller blade tip axial length
48 ensures sufficient mixing of multiphase fluid 22 to maintain the multiphase fluid
22 in a desirable condition during pumping. Depending on the parameters of a given
operation, the pump 20 may be used in subsea operations or surface operations.
[0028] Furthermore, the size and configuration of the pump 20 may vary according to the
fluid to be pumped and the desired pumping capacity. The arrangement and number of
pumping stages 34 also may vary according to the parameters of the desired pumping
operations. The number and arrangement of impeller blades 42 as well as the style
of impellers 30 also may vary according to the types of fluids 22, e.g. types of multiphase
fluids, pumping environment, pump location, and/or other pumping operation parameters.
[0029] Although a few embodiments of the system and methodology have been described in detail
above, those of ordinary skill in the art will readily appreciate that many modifications
are possible without materially departing from the teachings of this disclosure. Accordingly,
such modifications are intended to be included within the scope of this disclosure
as defined in the claims.
1. A system for moving fluid, comprising:
a pump having a pump housing, a shaft rotatably mounted in the pump housing, and a
plurality of impellers mounted to the shaft, each impeller comprising:
an impeller hub rotationally fixed to the shaft; and
a plurality of impeller blades extending radially outward from the impeller hub, each
impeller blade having an impeller base proximate the impeller hub and in impeller
tip, the impeller tips having an axial length; and
a wear ring disposed along the tips of the impeller blades and having a wear ring
axial length shorter than the axial length of the impeller tips.
2. The system as recited in claim 1, wherein the wear ring axial length is less than
95% of the axial length of the impeller tips.
3. The system as recited in claim 1, wherein the pump comprises a plurality of diffusers
alternating with the plurality of impellers.
4. The system as recited in claim 1, wherein the wear ring is formed from a different
material than the plurality of impeller blades.
5. The system as recited in claim 1, wherein the wear ring extends radially outwardly
of the impeller tips.
6. The system as recited in claim 5, wherein the wear ring is received in a slot formed
in a surrounding wall.
7. The system as recited in claim 1, wherein the wear ring is provided with a seal surface
having at least one of an annular seal shape; a labyrinth seal shape, a pocket damper
seal shape; and a stepped diameter segmented seal shape.
8. The system as recited in claim 1, wherein the wear ring is radially coextensive with
the impeller tips.
9. The system as recited in claim 1, wherein the impeller comprises a plurality of impellers
disposed between corresponding diffusers to establish pump stages.
10. The system as recited in claim 9, wherein the impellers are helico axial impellers.
11. A method, comprising:
providing a multiphase pump with an impeller having a plurality of impeller blades
with blade tips extending an axial length;
securely positioning a ring along the blade tips to stiffen the impeller; and
limiting a ring axial length to less than the axial length of the blade tips to enable
flow across the blade tips for active phase mixing.
12. The method as recited in claim 11, wherein providing the multiphase pump with the
impeller comprises providing a plurality of helico axial impellers.
13. The method as recited in claim 11, wherein securely positioning comprises positioning
the wear ring at a desired location between an inlet side and an outlet side of the
impeller.
14. The method as recited in claim 11, further comprising providing features at a contact
surface between the ring and the impeller blades to facilitate fluid flow and mixing.
15. The method as recited in claim 11, further comprising providing the ring with a seal
surface having at least one of an annular seal shape; a labyrinth seal shape, a pocket
damper seal shape; and a stepped diameter segmented seal shape.