U.S. patent number RE30,836 [Application Number 06/143,883] was granted by the patent office on 1981-12-29 for liquid-gas separator unit.
This patent grant is currently assigned to Kobe, Inc.. Invention is credited to Philip R. Bunnelle.
United States Patent |
RE30,836 |
Bunnelle |
December 29, 1981 |
**Please see images for:
( Certificate of Correction ) ** |
Liquid-gas separator unit
Abstract
A liquid-gas separator unit with superior performance
characteristics is disclosed. The unit is characterized by a high
liquid flow rate capacity at high as well as low accompanying gas
flow rates, and efficient liquid-gas separation capability. The
unit has a unique discharge plug element and a unique intake plug
element that cooperate with a unique impeller means.
Inlet/recirculation openings in the unit casing act to increase the
liquid flow rate.
Inventors: |
Bunnelle; Philip R. (Santa
Clara, CA) |
Assignee: |
Kobe, Inc. (Huntington Park,
CA)
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Family
ID: |
26841491 |
Appl.
No.: |
06/143,883 |
Filed: |
April 25, 1980 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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Reissue of: |
305645 |
Nov 10, 1972 |
03887342 |
Jun 3, 1975 |
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Current U.S.
Class: |
96/214;
166/105.5; 417/313; 55/406 |
Current CPC
Class: |
E21B
43/38 (20130101); B01D 19/0057 (20130101) |
Current International
Class: |
B01D
19/00 (20060101); E21B 43/34 (20060101); E21B
43/38 (20060101); B01D 019/00 () |
Field of
Search: |
;166/265,105.5,201,202
;55/199,203,401-409 ;417/313 ;415/121A,168 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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621476 |
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Jun 1961 |
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CA |
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536356 |
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Oct 1931 |
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DE2 |
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1025380 |
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Mar 1958 |
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DE |
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1407936 |
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Jan 1970 |
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DE |
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477830 |
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Feb 1953 |
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IT |
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831114 |
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Mar 1960 |
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GB |
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Primary Examiner: Nozick; Bernard
Attorney, Agent or Firm: Christie, Parker & Hale
Claims
What is claimed is:
1. A liquid-gas separator unit comprising, in combination, means
defining a chamber having first and second longitudinally spaced
portions, impeller means disposed within the chamber between the
first and second chamber portions, said impeller means including
vanes configured to impart circular motion to liquid after first
imparting upward motion to the liquid, means connected to the
impeller means for rotating said impeller means, intake means
communicating with the first chamber portion for admitting a
liquid-gas mixture into said first chamber portion, discharge means
communicating with the second chamber portion for discharging the
liquid and gas components of the mixture from said second chamber
portion after such components have been separated within the
chamber by the rotation of the impeller means, said discharge means
including passage means for conveying the gas component from the
impeller means, said discharge means further including passageway
means for conveying the liquid component from the impeller means
without causing an abrupt change in the direction and velocity of
the liquid component as it flows into the passageway means.
2. A liquid-gas separator unit comprising, in combination, means
defining a separator chamber having first and second longitudinally
spaced portions, impeller means rotatably disposed within the
chamber between the first and second chamber portions, intake means
communicating with the first chamber portion for admitting a
liquid-gas mixture into said first chamber portion, discharge means
communicating with the second chamber portion for discharging the
liquid and gas components of the mixture from said second chamber
portion after such components have been separated within the
separator chamber by the rotation of the impeller means, said
impeller means including impeller vanes with first portions to
primarily move the mixture away from the first chamber portion
upwardly toward the second chamber portion, said impeller vanes
including second portions to primarily move the mixture in a
circular flow path about the rotation axis of the impeller means,
said first and second impeller vane portions having different
configurations suited for imparting the above mentioned movement to
the mixture.
3. A separator unit comprising, in combination, separator casing
means, a discharge element closing the upper end of the casing
means, an intake element closing the lower end of the casing means,
a rotatable shaft extending through and journalled in the discharge
element and the intake element, an impeller affixed to said shaft
between the discharge element and the intake element, said impeller
including long, narrow vanes configured to impart circular motion
to liquid after first imparting upward motion to the liquid, the
discharge element including channels that spiral upwardly in the
same direction as the direction of impeller rotation, the lower
ends of the channels being sloped to facilitate smooth flow of
liquid from the upper ends of the vanes into the lower ends of
channels, the upper ends of the channels leading to a central
chamber area at the upper end of the discharge element, and a
plurality of internal passages in said discharge element, each
internal passage extending from a lower, central chamber in the
lower end of the discharge element to the element's exterior to
each provide an exhaust path to the exterior of the unit.
4. A separator unit, which can be utilized to separate gas from
liquid, comprising, in combination, a vertically disposed gas
separating chamber defined by a tubular casing or the like, intake
means for admitting liquid that contains gas to the lower portion
of said chamber, means to exhaust separated gas from the upper
portion of the chamber, means to exhaust separated liquid from the
upper portion of the chamber, and means to separate gas from liquid
comprising (a) an elongated impeller adapted to rotate within the
chamber, said impeller comprising a plurality of vertically
disposed elongated impeller vanes each with an upper end and a
lower end, each vane having a helical curvature near its lower end
and having a substantially straight curvature near its upper end
whereby the lower portions of the vanes coact to impell liquid with
gas therein upwardly within the chamber and whereby the upper
portions of the vanes coact to impell the liquid away from the
center of the chamber whereby gas separates from the liquid and
moves toward the center of the chamber.
5. The unit of claim 4 wherein the intake means has at least one
intake opening that slopes upward toward the center of the
chamber.
6. The unit of claim 4 wherein the means to exhaust liquid and gas
is comprised of respective passage means for channelling separated
gas and separated liquid out of the chamber through
noninterconnected passageways, said discharge element including a
liquid conveying passageway that is tapered to effect a decrease in
liquid velocity as liquid flows along the passageway.
7. In a separator unit wherein the gas and liquid components of a
liquid-gas mixture are separated the combination comprising, means
defining a vertically oriented separation chamber, intake means
communicating with the chamber for admitting a liquid-gas mixture
into a lower portion of said chamber, discharge means communicating
with the chamber for discharging separated gas and separated liquid
from an upper portion of said chamber, impeller means disposed
within the chamber and being rotatable about a vertical axis to
impell the gas-liquid mixture in the chamber from the intake means
toward the discharge means, the impeller means having upper and
lower portions of different configuration that coact to centrifuge
the liquid-gas mixture after impelling it upwardly within the
chamber, the portions acting to cause the liquid component of the
mixture to move away from the center of the chamber while also
acting to cause the gas component of the mixture to move toward a
central region of the chamber, the lower portion of the impeller
means having means to primarily impell the liquid-gas mixture
upwardly within the chamber, the upper portion of the impeller
means having means to primarily impell the liquid-gas mixture into
a circular orbit, the impeller means acting to impell relatively
gas free liquid in an upwardly spiralling .[.oribt.]. .Iadd.orbit
.Iaddend.from the upper end of the impeller means into a liquid
conveying passage in the discharge means while permitting gas,
separated by the impeller means from the liquid, to rise from the
central region of the chamber into a gas conveying passage in the
discharge means.
8. The separator unit of claim 7 wherein the unit includes a
plurality of liquid conveying passages.
9. The unit of claim 7 wherein the impeller means has a plurality
of vanes which rotate about the aforesaid axis.
10. The separator unit of claim 7 wherein the lower end of the
liquid conveying passage is below the lower end of the gas
conveying passage.
11. The separator unit of claim 7 wherein the liquid conveying
passage and the gas conveying passage are formed in a body defining
the discharge means and wherein the gas conveying passage follows a
path such that the upwardly spiraling liquid flows to the liquid
conveying passage in an unobstructed flow path that is not
obstructed by the portion of the body which defines the gas
conveying passage.
12. The separator unit of claim 7 wherein the liquid conveying
passage curves in an upward direction around the aforesaid axis to
facilitate liquid flow from the upper end of the impeller means
into the liquid conveying passage with little concomitant change in
liquid flow direction.
13. The unit of claim 12 wherein the impeller means has a plurality
of vertically oriented vanes which include upper and lower vane
segments, the upper vane segments providing substantially axially
oriented vane surfaces, the lower vane segments providing
substantially helically oriented vane surfaces curving upward about
the aforesaid axis in a circular direction opposite to the
direction of upward curvature of the aforesaid curved liquid
conveying passage of said discharge means.
14. The separator unit of claim 7 wherein the gas conveying passage
leads upwardly to the outside of the unit to discharge gas from the
unit in a generally upward direction.
15. The separator unit of claim 11 wherein the unit includes a
plurality of gas conveying passages.
16. The unit of claim 7 wherein the chamber defining means includes
opening defining means in the lower portion thereof approximate the
lower portion of the impeller means, said opening defining means
functioning as auxiliary inlet ports to increase liquid capacity of
the separator unit.
17. The unit of claim 16 wherein the opening defining means is
comprised of a plurality of discrete openings.
18. The unit of claim 17 wherein the discrete openings are oriented
toward the center of the chamber.
19. The unit of claim 17 wherein the discrete openings slant
upwardly toward the chamber.
20. The unit of claim 17 wherein the discrete openings are arranged
symmetrically about the chamber.
21. The unit of claim 17 wherein the discrete openings are arranged
into vertically spaced rows.
22. In a separator unit, the combination comprising: casing means
defining a vertically oriented cylindrical chamber wherein an
impeller means is operative to separate gas from a liquid gas
mixture, a discharge element operably connected with the upper end
of the casing means, the discharge element being located
immediately above the impeller means, the discharge element
comprising a body with upper and lower portions, the upper portion
defining a central chamber serving as a liquid receiving chamber,
the lower portion defining a central chamber serving as a gas
collection chamber, a plurality of passageways leading upwardly
through the body from the gas collection chamber to respective
passageway ports, a plurality of passages leading upwardly in the
body from its lower end to passage ports communicating with the
liquid reservoir chamber.
23. .Iadd.In a separator unit, .Iaddend.the combination .[.set
forth in claim 22.]. .Iadd.comprising: casing means defining a
vertically oriented cylindrical chamber wherein an impeller means
is operative to separate gas from a liquid gas mixture, a discharge
element operably connected with the upper end of the casing means,
the discharge element being located immediately above the impeller
means, the discharge element comprising a body with upper and lower
portions, the upper portion defining a central chamber serving as a
liquid receiving chamber, the lower portion defining a central
chamber serving as a gas collection chamber, a plurality of
passageways leading upwardly through the body from the gas
collection chamber to respective passageway ports, and a plurality
of passages leading upwardly in the body from its lower end to
passage ports communicating with the liquid reservoir chamber,
.Iaddend.wherein the passages curve upwardly in a substantially
spiral path from the lower end of the body, whereby liquid can flow
upwardly into the passages with little change in flow direction of
the liquid.
24. The combination set forth in claim .[.22.]. .Iadd.23
.Iaddend.wherein each passageway port is adapted to discharge a
stream of gas in a substantially upward direction.
25. A liquid-gas separator unit comprising, in combination, casing
means defining a cylindrical chamber containing an impeller means
which has a lowermost portion adapted to impell liquid upward
through the chamber and which has an uppermost portion adapted to
centrifuge the liquid, a discharge element connected to the
uppermost portion of the casing means near the uppermost portion of
the impeller means, an intake element connected to the lowermost
portion of the casing means near the lowermost portion of the
impeller means, a first discharge passage within the discharge
element, the discharge passage sloping upward along a curved
helical path, a second discharge passageway within the discharge
element, the discharge passageway sloping upward from the lowermost
portion of the discharge element to the exterior of the discharge
element, at least one upwardly sloping intake opening in the intake
element, whereby normal operation of the unit results in flow of a
gas and liquid mixture through the intake opening into the chamber
wherein the impeller means rotates to cause gas to separate from
liquid and move toward the center of the chamber from whence the
gas rises into and through the discharge passageway while the
impeller means rotates to impart upwardly spiraling motion to the
liquid causing it to flow from the uppermost portion of the
impeller means along a flow path that is substantially in line with
the spiral path of the first mentioned discharge passage so that
the liquid flows with minimum change in flow direction into the
discharge passage.
26. The unit of claim 25 wherein the casing means has opening means
in its lowermost portion effective to increase the liquid
throughput capacity characteristic of the unit.
27. The unit of claim 25 wherein the impeller means has a plurality
of vanes each of which has an upper portion extending downwardly to
a curved lower portion.
28. A liquid-gas separator unit comprising, in combination, a
vertically oriented casing providing a cylindrical chamber, a
discharge element connected to the upper end of the casing to
provide a closure for the upper end of the chamber, said discharge
element having gas and liquid outlets communicating with the
chamber, an intake element connected to the lower end of the casing
to provide a closure for the lower end of the chamber, an impeller
within the chamber, said impeller including a plurality of
vertically oriented vanes, said vanes being configured to define an
upper impeller zone wherein the impeller vanes coact upon rotating
to impell liquid away from the center of the chamber by centrifugal
force, said vanes being configured to define a lower impeller zone
wherein the impeller vanes coact upon rotating to impell liquid
upward within the chamber, said discharge element including
discharge channels that slope downwardly toward the impeller in
respective curved paths.
29. The separator unit of claim 28 wherein the discharge channels
include tapered segments that progressively increase in area with
increasing distance from the impeller.
30. A separator unit, which may be utilized to separate gas from
liquid, comprising, in combination, a vertically disposed casing
forming a cylindrical chamber therein, a discharge plug connected
to the upper end of the casing, an intake plug connected to the
lower end of the casing, a shaft having portions that extend
through the discharge plug and intake plug, an impeller secured to
said shaft within said chamber between the discharge plug and
intake plug, the impeller being rotatable to impell liquid through
said chamber, the impeller including a lower portion adapted to
impell liquid toward the discharge plug and including an upper
portion adapted to impell liquid away from the center of the
chamber, rotation of the impeller being effective to separate gas
from liquid causing gas to move toward the center of the chamber
from whence separated gas flows through a passage of the discharge
plug, the liquid being impelled by the impeller into and through a
passageway of the discharge plug.
31. The unit of claim 30 wherein the discharge plug includes a
plurality of liquid conveying passageways that are symmetrically
arranged to promote uniform liquid flow through the discharge
plug.
32. The unit of claim 30 wherein the discharge plug includes a
tubular upper portion that provides a chamber that opens upwardly
and wherein the passageway communicates with the chamber.
33. A separator unit, that may be utilized to separate gas from
liquid, comprising, in combination, a vertically disposed casing
forming a cylindrical chamber therein; a discharge element
connected with the upper end of the casing to provide a closure for
the top end of the chamber, to provide a discharge passage for
conducting separated liquid from the chamber, and to provide an
exhaust passage for conducting separated gas from the chamber; an
impeller disposed within the chamber and secured to a shaft that
extends through the discharge element and through an intake element
that is connected with the lower end of the casing to provide a
closure for the bottom end of the chamber and to provide an inlet
passage for admitting liquid and gas into the chamber, said
impeller including a plurality of vertically oriented elongated
vanes each of which has a vertically elongated segment that merges
with a spiral segment that extends to the lower end of the
vane.
34. The unit of claim 33 wherein the casing includes opening means
providing communication between the chamber and the outside of the
casing.
35. The unit of claim 33 wherein the casing includes multiple
opening means for allowing flow of liquid through some of the
opening means into the chamber and for allowing flow of liquid
through some of the opening means out of the chamber.
36. The unit of claim 33 wherein the discharge element includes a
central gas collection chamber that opens downward toward the
impeller, the exhaust passage extending from the collection chamber
with which it communicates to the outside of the unit.
37. The unit of claim 33 wherein the discharge passage curves
upward from the lower end of the discharge element along a path
that includes a spiral segment and communicates with an upper
portion of the discharge element from whence liquid can be
conveyed.
38. In a separator unit that can be used to separate gas from
liquid, a discharge plug connected to the upper end of a separator
unit casing to provide a closure for the top end of a chamber, the
plug including a central vertical bore in which an impeller shaft
is journalled, a downwardly opening gas collection chamber at the
lower end of the plug, a gas conveying passage extending from the
gas collection chamber upwardly to the outside of the plug, a
liquid conveying passage provided on said plug which passage
spirals upwardly to permit easy flow of upwardly spiralling liquid
into and through the passage to the top end of the plug, and
impeller means to impart spiral and upward movement of liquid, and
separation of gas from said liquid, in said separator unit.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to improvements in liquid-gas separator
units that are adapted for use with downhole oil well pumps to
separate gas from the liquid to be pumped from the well.
2. Description of the Prior Art
Liquid-gas separator units are used downhole in oil producing wells
to perform the task of separating gas from well liquid before it is
pumped out of the wells. Any significant amount of free gass
present in undissolved form in an oil producing well hinders the
pumping of the well liquid, which may include other liquids in
addition to crude oil, out of the well. Various United States
patents, such as U.S. Pat. No. 2,104,339 to Arutinoff, U.S. Pat.
No. 2,311,963 to Pyle, U.S. Pat. No. 2,285,169 to Pyle and
3,624,822 to Carle, describe liquid-gas separator units and provide
information as to why such units are used. As evidenced by these
patents, there are different kinds of units that work according to
different physical principles, and their performance
characteristics, as might be expected, depend upon their particular
features. There does not appear to be any particular unit, of which
applicant is aware, that is not limited, in one way or another, in
its performance capabilities.
A superior separator unit, in general, is one that is capable of
discharging liquid at a high flow rate, after separating free or
undissolved gas from the liquid, to provide relatively gas free
liquid. Moreover, a superior liquid-gas separator unit can function
to separate widely varying quantities of free gas, ranging from
negligible gas flow rates constituting negligible proportions of a
liquid flow rate up to large gas flow rates corresponding to
several times the liquid flow rate, without any significant change
(i.e., decrease) in the liquid flow rate through the unit and, in
addition, can perform the separation function with essentially
negligible gas carryover in the liquid discharged from the unit.
Inherently, a high performance unit is one which efficiently
separates gas from liquid and discharges liquid which has only a
relatively small amount of undissolved gas remaining therein,
because significant quantities of free gas in the discharged liquid
may hinder efficient pumping of liquid form a well in which such a
unit is utilized. A truly superior unit is capable of effective use
in wells wherein large quantities of undissolved gas are present in
the well liquid.
SUMMARY OF THE INVENTION
The goal of the present invention is to provide a liquid-gas
separator unit having superior performance characteristics. In
pursuit of this goal a unique separator unit, to be described, has
been developed. The unit slightly resembles units shown in U.S. Pat
Nos. 2,285,169 and 2,311,963 to H. C. Pyle, in that is has an
impeller that rotates to effect liquid-gas separation by
centrifuging a liquid-gas mixture.
A salient feature of the unit is a special impeller that has a
lower portion that primarily serves to pump a liquid-gas mixture
through the unit, and an upper portion that primarily serves to
centrifuge the pumped mixture to separate gas and liquid before the
separated gas and liquid are passed through respective passages of
an adjacent discharge element. The impeller protions are comprised
of specially shaped vanes. Other salient features of the unit
include a unique discharge element, a unique intake element, and
inlet/recirculation openings in the unit casing. The above features
uniquely promote the goal of the invention.
In summary, the present invention provides a separator unit having
an efficient combination of unique component parts tailored to
produce improved results.
The nature of the present invention will become apparent upon
review of the following detailed description taken in conjunction
with the figures of the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a central vertical section of a unique separator unit
with other parts connected to it.
FIG. 2 is a side elevation with portions broken away showing a
unique impeller used in the separator unit of FIG. 1.
FIG. 3 is an end view taken in the direction of arrows 3--3 of FIG.
2.
FIG. 4 is a side elevation showing fragment of the impeller of FIG.
2.
FIG. 5 is an end view taken in the direction of arrows 5--5 of FIG.
4.
FIG. 6 is a side elevation of a unique discharge plug element used
in the unit of FIG. 1.
FIG. 7 is a plan view, taken in the direction of arrows 7--7 of
FIG. 6, of the element shown in FIG. 6.
FIG. 8 is a central section taken along line 8--8 of FIG. 7.
FIG. 9 is a bottom view of the element shown in FIG. 6.
FIG. 10 is a central section taken along line 10--10 of FIG. 9.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The separator unit 10 illustrated in FIG. 1 is comprised of a
vertically disposed tubular casing 12 forming a cylindrical chamber
12a wherein a rotatable impeller 16 is disposed. Impeller 16 has a
tubular hub 18 with a longitudinal bore 19 and a plurality of long,
thin, narrow vanes 20. Hub 18 includes an upper counterbore wherein
a corrugated ring sleeve 24 is press fitted between it and an
impeller shaft 26, and further includes a lower counterbore
containing a corrugated ring sleeve 28 press fitted between hub 18
and shaft 26. Sleeves 24 and 28 coact to affix impeller 16 to shaft
26.
A discharge plug element 30 is threaded into the internally
threaded upper end of casing 12, and an intake plug element 32 is
threaded into the internally threaded lower end of casing 12.
Intake plug element 32 includes six intake openings or ports 32a
that are uniformly circumferentially spaced about plug 32. Each
port 32a slants upwardly (e.g., at an angle of about 60.degree.
with respect to a horizontal plane) toward the casing axis and is
radially oriented. Intake element 32 further includes a relatively
wide diameter tubular upper portion 32b with exernal threads for
use in joining it to the lower end of casing 12, a relatively
narrow diameter tubular lower portion 32c, and an intermediate
tapered portion 32d wherein intake ports 32a are located. The body
of element 32 defines an interior chamber 32e that communicates
with the lowermost portion of casing chamber 12a.
Intake plug element 32 may be provided with a plurality of vanes
that extend inwardly from the interior wall of the element's body
toward the center of the chamber. For example, six vanes 32f,
indicated by phantom lines in FIG. 1, may be added to element 32,
and these vanes could be axially oriented, also as indicated in
FIG. 1. These vanes could be located in equispaced relation about
the interior body wall between the six intake ports 32a, and could
be appropriately configured (i.e., straight, vertically elongated
or helically curved) to interact with liquid-gas mixtures flowing
through ports 32a toward impeller 16. Such vanes, if provided,
could be used to alter and/or control the flow of liquid-gas
mixtures upward through the chamber defined by the body of intake
element 32 whereby a liquid-gas mixture flowing past them would
impinge on the lower ends of the impeller vanes in such fashion as
to set up an efficient mixture flow pattern.
The externally threaded lower end of a liquid conductor casing 34
is threaded into the internally threaded upper end of discharge
element 30. The upper end of conductor casing 34 is fastened to the
lower end of a pump casing 36 (constituting part of a pump stage,
not shown) by screws 38 in the manner indicated in FIG. 1. The
lower end of intake plug element 32 is screw fastened to the upper
end of a motor casing 40 by screws 41 in the manner indicated in
FIG. 1. The pump casing 36 confines conventional pump impellers
(not shown) that are affixed to a pump shaft 42 having a lower end,
which is shown in FIG. 1, that is axially coupled to impeller shaft
26. Shafts 42 and 26 are coupled together, so that they will rotate
together, by a key pin 44 within aligned key slots in shafts 42 and
26 and a corresponding keyseat in a coupling sleeve 46. A coupling
pin (not shown) fits within a transverse hole in shaft 42 and
diametrically opposed transverse holes in sleeve 46, to secure the
sleeve to the shaft.
Discharge plug element 30 has a central, vertical bore containing a
sleeve brushing 48 affixed therein to provide a journal for a
portion of shaft 26 that passes through the bushing. Intake plug
element 32 has a bore, coaxial with the discharge plug element
bore, with tubular bushing 50 that provides a journal for a
coresponding portin of a shaft coupling 52. Shaft coupling 52 is
connected to shaft 26 by a key pin 54 disposed within a keyway of
shaft 26 and a keyseat of shaft 52. A retainer pin 56, securely
fitted into a transverse bore in shaft coupling 52, protrudes
radially into the lower end of the corresponding connecting shaft
key slot to prevent the key pin 54 from falling out of the coupling
52. A coupling pin (not shown) fits within a transverse hole in
impeller shaft 26 and diametrically opposed transverse holes in
coupling 52 to affix the coupling to the shaft. Two diametrically
opposed openings 32g are provided in element 32 to allow for the
insertion of the pin into the holes of coupling 52 and shaft 26.
The upper end of an electric motor shaft 58 is fitted into the
lower end of shaft coupling 52 and secured thereto by a key pin 59
seated within a key slot of coupling 52 and a keyseat of shaft 58.
A set screw 60 screw threaded into a transverse hole in coupling
52, extends into a radial opening in shaft 58 to fasten the
coupling and shaft together.
The lower end of the separator casing 12 includes three vertically
spaced circular rows of inlet/recirculation openings or ports that
surround the lower end of impeller 16 in the illustrated unit 10.
The topmost row comprises 24 openings 62 that are uniformly spaced
about the casing. The lowermost row likewise comprises 24 openings
64 that also are uniformly spaced about the casing, with each
opening 64 located axially below a respective opening 62. The
intermediate row, i.e., between the aforesaid rows, similarly
comprises 24 openings 66 that are uniformly spaced about the casing
and staggered in relation to openings 62 and 64. Each opening 62,
64 and 66 is radially oriented and slants upward toward the
casing's central axis.
Five impeller vanes 20 (FIGS. 2-5) are spaced uniformly at
72.degree. intervals around the impeller hub 18, and these vanes
extend lengthwise along the hub approximately its entire length.
These vanes comprise straight, axially oriented strip segments 20a
extending from the upper end of the hub down to spiral shaped strip
segments 20b that extend to the hub's lower end. The vane segments
20a and 20b of each vane 20 merge in the lower half of the vane.
The vanes have outermost edges 20c each located the same distance
from the hub's axis. Each vane segment 20b curves spirally downward
in a clockwise direction (as viewed from above) to terminate in a
lowermost vane edge 20d that is disposed within a radial plane A
(FIG. 2) taken perpendicular to the impeller's vertical axis W.
Each straight vane segment 20a is disposed within an axial plane B
(FIG. 3) taken through the impeller's vertical axis. Thus it is
understood that the planes A and B are normal to each other. As
seen in FIG. 3, each vane edge 20d is also disposed in an axial
plane C (FIG. 3) located 90.degree. clockwise from the axial plane
B wherein the segment 20a of the same vane is disposed.
In operation, impeller 16 is caused to revolve in a clockwise
direction i.e., in the direction indicated by the arrow D in FIG.
1. The impeller vanes 20 act to develop a high pressure head in the
chamber 12a below discharge element 30. Since each vane segment 20b
spirals 90.degree. downward from an axially oriented vane segment
20a to an axially oriented edge 20d the slope angle X (see FIG. 4)
at the vane's radially inner edge 20e is greater than the slope
angle Y at the vane's radially outer edge 20d. In the example, the
angle Y (see FIG. 4) is about 12.degree. while the angle X is about
30.degree..
The discharge plug element 30, illustrated in FIGS. 6-10, is
comprised of a generally cylindrical body 70, including an
upstanding tubular lip 72 forming a liquid receiving chamber 72a at
its upper end that conducts liquid coming from passages 100 upward
into the liquid conductor casing 34. Lip 72 has internal threads 76
(FIG. 8) used to screw together element 30 and conductor casing 34
in the manner shown in FIG. 1. Body 70 has outer threads 78 used to
screw element 30 into the upper end of separator casing 12 as shown
in FIG. 1. Body 70 includes a tapered flange-like body portion 80
forming an annular shoulder 80a that seats upon the upper end of
casing 12 when element 30 is assembled with the casing. Body 70 has
a central hub portion 82 forming a bore 84, concentric with the
central vertical axis of body 70, that receives bushing 48 and
impeller shaft 26 in the manner indicated in FIG. 1. Hub 82 merges
with a tubular lip 86 forming a cylindrical gas collection chamber
86a.
As seen best in FIGS. 9 and 10, 70 has four internal gas channels
or passages 96 symmetrically arranged about the body axis and
leading upward from inlets 96b at the lower body chamber 86a to
four respective passage outlets 96a spaced 90.degree. apart on
tapered body portion 80. Body 70 also has four symmetrically
arranged exterior liquid channels, passageways, or slots 100 each
of which spirals upward in a clockwise direction (as viewed from
the upper end of element 30) from an inlet 100b at the lower end of
element 30 to a respective outlet 100a communicating with upper
body chamber 72a. The four outlets 100a are located at 90.degree.
intervals (see FIG. 7) with each outlet 100a offset 45.degree. from
adjacent interior ports 96a.
The configuration of body 70, the network of gas conveying passages
96 and liquid conveying passageways 100, and the proximity of body
70 to impeller 16 cooperate to facilitate the flow of liquid from
impeller 16 to passageways 100 with minimum loss in the
hydrokinetic energy of the liquid. Since body 70 lies immediately
above impeller 16 and is vertically spaced therefrom by only a
small vertical gap, the liquid flowing from the upper end of
impeller 16 approaches inlets 100b with essentially the same flow
velocity that it has as it spirals upwardly from the impeller. The
body portion defining ports or inlets 96b of passages 96 is located
above the ports or inlets 100b of passageways 100 and does not pose
an obstacle to the flow of liquid into the passageways 100. The
passages 96 and passageways 100 are arranged so that liquid can
flow in an unobstructed path away from impeller 16 into the
passageway inlets 100b without having to flow past a body portion
containing passages 96. This arrangement is advantageous because
the obstruction-free liquid flow path allows for substantial
conservation of liquid hydrokinetic energy as liquid flows toward
passageways 100.
In the illustrated embodiment of the invention all the passageways
or channels 100 are identical. Each channel 100 (see FIG. 6) is
defined by two slot walls 104 and 106 extending from the channel
inlet 100b to the channel outlet 100a. Each channel 100 includes a
lowermost upwardly sloping portion of small slope angle Z
(20.degree. with respect to a horizontal plane in the illustrated
embodiment) merging with an uppermost, upwardly sloping channel
portion whose slope angle varies and approaches 90.degree. at the
channel outlets 100a. The .[.slop.]. .Iadd.slope .Iaddend.angle Z
is such that liquid energy loss sustained in the liquid flowing
from the impeller 16 into channels 100 is minimized. The width of
at least a segment of the lowermost portion of each channel 100
increases with increasing distance from lower end 30a of element
30. The changing width of the channel segments provides an increase
in channel area in the direction of liquid flow therethrough. Thus,
in the illustrated embodiment, each channel 100 has straight wall
portions 104a, 106a, extending between points P1, P2 and P3, P4
respectively, that diverge in the channel direction toward the
associated uppermost channel portion which is of constant width.
The lowermost channel portions are therefore widest at points P1
and P3 where the uppermost channel portions begin. In the
illustrated discharge plug element 30, the wall portions 104a, 106a
of each channel 100 diverge at an angle of 5.degree. from a
centerline L of the channel. Thus, the angular divergence between
wall portions 104a, 106a is 10.degree..
OPERATION OF SEPARATOR UNIT 10
Separator unit 10 operates as follows. As motor shaft 58 revolves
at a constant rate impeller shaft 26 and impeller 16 likewise
revolve, whereupon impeller 16 draws a liquid-gas mixture through
intake openings 32a, into the chamber 12a. As this liquid-gas
mixture moves upwardly within chamber 12a, the revolving impeller
vanes 20 impart a compound motion to it. Impeller vane segments 20b
impell the mixture primarily upwardly through chamber 12a, while
vane segments 20a primarily impart circular motion to the upwardly
moving mixture, thereby centrifuging the liquid component of the
mixture outwardly away from impeller hub 18 and causing undissolved
gas present in the liquid to move inwardly toward hub 18. The
separated liquid flows up through discharge channels 100 into
discharge element chamber 72a. The separated gas forms a
liquid-free gas column around hub 18, which column of gas moves
upwardly into discharge element chamber 86a from whence the gas
flows into inlets 96b and through gas conducting channels 96 to
stream from gas discharge outlets 96a in nearly vertical, upward
directions. The channel outlets 96a discharge discrete high
velocity gas streams of separated gas that are substantially
upwardly directed to promote upward movement of the discharged gas
within a well bore (not shown) wherein unit 10 is situated.
The liquid entering the inlets 100b of channels 100 possesses both
hydrostatic and hydrokinetic energy. The liquid flowing upwardly
through channels 100 flows at a velocity that diminishes as the
liquid flows along the tapered channel portions defined by wall
portions 104a, 106a between points P1, P2, P3 and P4 (FIG. 6). The
path of channels 100 is such that the liquid velocity is diminished
within the channel segments extending between wall portions 104a,
106a before the liquid flows to and through the uppermost channel
portions. The flow path promotes liquid flow through channel 100
with minimal liquid energy loss. As liquid flows through the
tapered channel portion (between points P1, P2, P3 and P4 in the
illustrated embodiment) of each channel 100, a portion of the
liquid hydrokinetic energy, which is proportional to the square of
the liquid velocity, is converted into hydrostatic energy thereby
raising the hydrostatic pressure of the liquid delivered to the
lower end of the pump casing 36. The lowermost portions of channels
100 are oriented at a slope angle Z (FIG. 6) to allow flow of
upwardly spiralling liquid into channel inlets 100b without any
substantial change occurring in the direction or velocity of liquid
flow from the uppermost end of impeller 16.
The mixture inlet openings 32a (FIG. 1) of intake plug element 32
slope upward at an angle of about 60.degree. (with respect to a
horizontal plane) so that the liquid-gas mixture flows through them
toward impeller 16 with little change in flow direction. The
approximately vertical orientation of openings 32a, and the
substantial intake area provided by them, facilitates transfer of a
large quantity of mixture through the unit in a relatively short
amount of time.
The inlet/recirculation openings 62, 64, 66 (FIG. 1) significantly
increase the mixture flow rate through unit 10. During operation of
unit 10 a hydrodynamic condition is established wherein liquid-gas
mixture flows into chamber 12a through some of the openings 62, 64,
66 and flows out from chamber 12a through others; resulting in a
net flow of liquid into chamber 12a. It should be understood,
however, that the inlet/recirculation openings 62, 64, 66 are not
essential to the operation of unit 10 and can be eliminated but
they are provided because they extend the unit's liquid throughput
capacity and reduce gas carryover with the discharged liquid. The
lowermost openings 64 increase liquid throughput capacity at low
gas rates (i.e., a liquid-gas mixture with a relatively small
proportion of component gas), and the openings 62, 66 increase
liquid throughput capacity at higher gas rates (i.e., a liquid-gas
mixture with a relatively high proportion of component gas).
The described unit 10 possesses several advantageous performance
characteristics. Liquid is discharged from unit 10 with a
substantial pressure head due to the coaction of impeller 16 with
the liquid conveying channels 100 of discharge element 30.
At the discharge element 30 the separated liquid enters liquid
conveying channels 100 that act as diffuser passages wherein liquid
velocity head is recovered, and wherein the liquid flow is turned
in an upward axial direction prior to discharge from outlets 100a.
Pressure recovery in discharge element channels 100 reduces the
volume of any carryover gas entrained with separated liquid while
providing a supercharging effect at inlet 36a (see FIG. 1) of pump
casing 36. This supercharging improves the pumping action (i.e.,
raises the volumetric efficiency of the pump) and pressurizes the
liquid at inlet 36a so as to reduce the likeihood that dissolved
gas within the liquid will come out of solution and produce
undesirable cavitation in the pump, which cavitation could impair
the pump's action or cause physical damage to it. In channels 100
the reduction of liquid velocity is accomplished in the channel
segments between portions 104a, 106a before any change in direction
of this liquid stream occurs, reducing the friction loss associated
with such changes in direction.
The ports or outlets 96a of gas conveying channels 96 are oriented
to discharge upwardly directed discrete gas jets whereby, as is
desirable, the likelihood of recirculation of the discharged gas to
the intake openings 32a of intake element 32 is minimized. These
gas jets assist in the upward expulsion of the discharge gas
through the annular space between unit 10 and the well casing (not
shown) to the top of the well where free gas escapes into a
collection apparatus capping the upper end of the well bore. In
this way, inefficient repetitive recirculation of discharged gas
through unit 10 is minimized. Moreover, these gas jets create a
minimal amount of turbulence in the well liquid outside unit 10
near gas discharge outlets 96a so that the tendency of discharged
gas to become re-entrained with well liquid upon leaving outlets
96a is restricted. The increased annular area provided about
discharge element body portion 80 between casing 34 and the
surrounding well casing (not shown) permits any carryover liquid
that might flow through passages 96 from chamber 86a to separate
out of a supporting gas discharge jet and flow downward between the
jets of gas issuing from passage outlets 96a toward intake element
32 without re-entraining gas. The unit 10 acts like a centrifugal
pump in that the rate of discharge of liquid decreases with
accompanying increases in hydrostatic pressure head and vice versa.
The unit 10 will operate with a negative head (i.e., discharge
pressure less than suction pressure).
The liquid-gas mixture enters chamber 12a due to the pumping action
of impeller vane portions 20b, and the straight vane portions 20a
whirl the mixture at high velocity. Impeller 16 accomplishes
liquid-gas separation so effectively that there is little gas
carryover with liquid even at high gas flow rates and low liquid
discharge pressures, presumably because the depth of liquid near
the wall of casing 12 is sufficient to completely fill the
liquid-conveying channels 100 or because inward flow from channels
100 to chamber 72a via ports or outlets 100a tends to exclude gas
from entering this chamber. Gas is discharged through gas discharge
outlets 96a due to the hydrostatic pressure head provided by energy
imparted by impeller 16 to the separated gas and/or by the pressure
gradient which exists between intake element 32 and discharge
element 30.
The unit 10, by providing a hydrostatic pressure head at liquid
reservoir chamber 86a, reduces the tendency for cavitation to occur
in the pump (not shown) operatively connected to unit 10. Also,
since liquid velocity head is recovered in the channel segment
defined by wall portions 104a, 106a of channels 100 the liquid
pressure increases whereby the liquid discharged from such channel
segments is at a pressure such that the liquid is not saturated
with gas. It therefore is less likely that dissolved gas will be
released from the liquid at points of reduced pressure downstream
of the location defined by points P1-P3 of discharge element
channels 100.
With no undissolved gas present in the liquid entering chamber 12a
via intake element 32, liquid is discharged through gas-conveying
passages 96. Whenever any amount of gas, however small, is present
in the liquid entering chamber 12a a stable gas core, it is
theorized, is formed with the impeller driven liquid forming a
liquid ring or annulus around the core. The depth of this ring is
self regulating, and is such that all the liquid is at a greater
radius than the inlets 96b to the gas conveying passages 96.
Consequently, as is rather amazing, with any small amount of gas
present in the liquid entering chamber 12a via intake element 32
essentially no liquid discharges from gas discharge outlets 96a
under an extremely wide range of liquid or gas flow rates. This
characteristic is highly desirable since any liquid that does
carryover into and through passages 96 recirculates down the
outside of casing 12 toward intake element 32 and may, in doing so,
re-entrain discharged gas in the process.
Preliminary laboratory tests of unit 10 have been conducted and,
although lab tests can not fully duplicate actual use conditions,
they indicated (1) that unit 10 effects a degree of liquid-gas
separation that greatly exceeds the separation capability of
existing units, (2) that unit 10 can, under test conditions,
efficiently separate the liquid and gas components of a liquid-gas
mixture and discharge large quantities of free gas and relatively
gas free liquid at substantial flow rates, and (3) that unit 10
can, under test conditions, effect substantial separation of gas
from a liquid-gas mixture that contains a high proportion of
undissolved gas. The test results indicated that unit 10 possesses
performance characteristics that surpass those of existing
units.
During the tests the unit 10 and an existing unit were tested using
the same test apparatus. The test data showed the way in which
liquid flow rate through each unit varied with positive or negative
pressure head. It was found that the pressure head or discharge
pressure (measured in feet) generated by unit 10 greatly exceeded,
by a large factor, the pressure head generated by the existing unit
over a wide range of liquid flow rates (measured in gallons of
liquid per minute). The discharge pressure is the pressure head
generated by a unit. When gas free liquid was supplied to each unit
it was found that the liquid flow rate through unit 10 greatly
exceeded, by a large multiple factor, that of the existing unit for
the same pressure head level. It was found that at zero discharge
pressure the liquid flow rate through the existing unit was only
about 17 gallons per minute while that through the unit 10 was
about 82 gallons per minute. It was found that when the positive
pressure head of the existing unit was equal to about 7 feet of
water the liquid flow rate was zero gallons per minute. By
comparison, when the positive pressure head of the unit 10 was
equal to about 40 feet the liquid flow rate was about 30 gallons
per minute.
Startling results were observed when comparative tests were carried
out to determine the discharge pressure versus liquid flow rate
curves of unit 10 and the existing unit when liquid-gas mixtures
containing varying proportions of gas therein were supplied to the
intake openings of the units. When as little as 0.55 cubic feet per
minute of gas was introduced into the liquid going into the intake
openings of the existing unit it was found that the unit's liquid
flow rate reduced to zero gallons per minute. By comparison, it was
found that when 26 cubic feet per minute of gas was introduced into
the liquid going into the intake opneings 32a of unit 10 the liquid
discharge rate exceeded 70 gallons per minute at zero feet of water
of discharge pressure. Moreover, it was found that the discharge
pressure versus liquid flow rate curve of unit 10 shifted only
small amounts with increases in the amount of gas introduced into
the liquid supplied to intake openings 32a up to large gas flows.
More particularly, the liquid flow rate at a given pressure head
decreased in small amounts with increases in the quantity of gas,
measured in cubic feet per minute, entrained with the liquid going
into unit 10. These measurements taken during the test clearly
indicate the vast superiority of the unit 10 over the other unit
that was tested.
The laboratory tests were conducted using air as the gas and water
as the liquid, together with a surfactant to reduce surface tension
of the water. The existing unit and the unit 10 effect separation
of gas and liquid by using different principles. The unit 10 relies
upon an impeller to achieve liquid gas separation, whereas the
existing unit primarily relies upon a series of conventional
separator cups to achieve liquid-gas separation. The existing unit
is a duplicate of some units that have been used in recent years in
numerous oil wells to separate out hydrocarbon and other gases from
crude petroleum prior to pumping the petroleum (and any other
liquids that may have been introduced into the subterranean
formation containing a well to facilitate the petroleum recovery
process). The existing unit is also typical of virtually all the
units in recent years in this application in that they employ such
separator cups. Since these units have been extensively used in oil
producing wells it is believed that the laboratory tests have
substantial validity in demonstrating the usefulness of the
liquid-gas separation unit 10 for oil well applications. Although
unit 10 is intended for use in oil well applications the tests
clearly demonstrated that it can be used as a liquid-gas separator
in other applications wherein liquid and gas other than petroleum
and hydrocarbon gases are to be separated for a useful purpose.
Presumably the unit could be used to separate immiscible liquids of
different densities.
The unit could be used as a pump or with pumps driven either by a
line shaft or a submersible motor.
Although the best mode contemplated for carrying out the present
invention has been herein shown and described, it will be apparent
that modification and variation may be made without departing from
what is regarded to the subject matter of the invention.
* * * * *