U.S. patent number 3,769,779 [Application Number 05/183,775] was granted by the patent office on 1973-11-06 for degassing apparatus.
This patent grant is currently assigned to Smith International, Inc.. Invention is credited to Walter E. Liljestrand.
United States Patent |
3,769,779 |
Liljestrand |
November 6, 1973 |
**Please see images for:
( Certificate of Correction ) ** |
DEGASSING APPARATUS
Abstract
An apparatus for degassing fluids, particularly drilling muds,
comprising a vessel having an inlet and an outlet for the intake
and discharge of the fluid to be treated, a centrifugal pump
connected to the vessel for circulating the fluid through the
vessel and means for removing gas from the region of the impeller
means in the centrifugal pump. The invention also includes a
centrifugal pump designed for handling gas laden fluids, the pump
having a means for removing gas from the region of the pump
impeller. The invention further includes a centrifugal pump for
handling corrosive and/or abrasive fluids wherein said fluids are
prevented from contacting the pump seal by means of a gas
pressurized compartment adjacent the seal.
Inventors: |
Liljestrand; Walter E.
(Midland, TX) |
Assignee: |
Smith International, Inc.
(Newport Beach, CA)
|
Family
ID: |
22674227 |
Appl.
No.: |
05/183,775 |
Filed: |
September 27, 1971 |
Current U.S.
Class: |
96/167; 96/161;
96/217; 96/196 |
Current CPC
Class: |
B01D
19/0063 (20130101); E21B 21/067 (20130101); B01D
19/0047 (20130101); B01D 19/0052 (20130101); F04D
9/001 (20130101) |
Current International
Class: |
E21B
21/00 (20060101); B01D 19/00 (20060101); E21B
21/06 (20060101); F04D 9/00 (20060101); B01d
019/00 () |
Field of
Search: |
;55/55,41,165-167,171,189,190-193 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Hart; Charles N.
Claims
I claim:
1. In a system for degassing fluids, the combination which
comprises:
a degassing vessel having an inlet and an outlet,
centrifugal pump means connected to said vessel for removing fluid
from said vessel, said pump means including an impeller housing
having an inlet and an outlet, an impeller means and means for
mounting said impeller means in said impeller housing for rotation
about a substantially vertical axis.
chamber defining means defining a chamber having an inlet and an
outlet, said chamber being disposed adjacent said impeller housing,
said inlet to said impeller housing being in open communication
with said outlet of said chamber, said impeller means serving to
induce vortexing of said fluid in said chamber whereby at least a
portion of the gas accumulating in the central region of said
impeller means is vented through the central portion of the vortex
substantially counterflow to the direction of feed of fluid to said
impeller means.
2. The system of claim 1 including means for maintaining
sub-atmospheric pressure within said degassing vessel.
3. The system of claim 1 wherein said means for rotatably mounting
said impeller means includes a rotatable shaft having said impeller
means mounted thereon and seal means surrounding said shaft and
there are means for preventing fluid being handled by said pump
means from contacting said seal means.
4. The system of claim 1 including means for controlling the flow
of fluid into said vessel.
5. The system of claim 4 wherein said means for controlling the
flow of fluid into said vessel includes valve means in said inlet
of said vessel.
6. The system of claim 2 including means for controlling the degree
of vacuum within said vessel in accordance with the fluid level
within said vessel.
7. The system of claim 6 including means responsive to the level of
fluid in said vessel for controlling said valve means.
8. The system of claim 7 wherein said means for controlling said
valve means includes a float operatively connected to said valve
means.
9. The system of claim 8 including means operatively connected to
said valve means for reducing pressure surging in the inlet of said
vessel.
10. The system of claim 2 including means for conducting gas vented
from the region of said impeller means to said vessel.
11. The system of claim 3 wherein said means for preventing said
fluid from contacting said seal means comprises means for forming a
gas barrier adjacent said seal means.
12. The system of claim 11 wherein said means for forming a gas
barrier adjacent said seal means is in open communication with said
chamber whereby at least a portion of the gas being vented from
said impeller means forms said gas barrier.
13. The system of claim 2 wherein said means for rotatably mounting
said impeller means includes a rotatable shaft having said impeller
means mounted thereon and seal means surrounding said shaft and
there are means for preventing fluid being handled by said pump
means from contacting said seal means.
14. The system of claim 13 wherein said seal means is axially
displaced along said shaft and substantially vertically above said
impeller means, said means for preventing fluid from contacting
said seal means includes means forming a compartment adjacent said
seal means, said compartment being in open communication with said
chamber whereby at least a portion of said gas being vented from
said impeller means through said chamber is retained in said
compartment to thereby form a gas barrier against said fluid
contacting said seal means.
15. The system of claim 13 wherein said chamber is formed within
said vessel and is disposed substantially vertically above said
impeller housing, said impeller housing having an axial inlet and a
radial outlet for the intake and discharge respectively of said
fluid, said inlet of said impeller housing and said oultlet of said
chamber being closely adjacent one another, said outlet means being
displaced axially along said shaft below said impeller means, and
said means for preventing fluid from contacting said seal means
comprises means forming a compartment adjacent said seal means,
said compartment having a downwardly facing opening, said impeller
means being mounted in said impeller housing closely adjacent the
inlet of said impeller housing such that fluid being removed from
said chamber is substantially simultaneously thrust radially
outwardly away from the central region of said impeller means
whereby at least a portion of the gas present in said fluid within
said impeller housing migrates to the central region of said
impeller means and collects in said compartment to thereby form a
gas barrier against said fluid contacting said seal means.
16. In a system for degassing fluid, the combination which
comprises:
a degassing vessel having an inlet and an outlet,
centrifugal pump means connected to said vessel for introducing
fluid into said vessel, said pump means including an impeller
housing having an inlet and outlet, an impeller means and means for
mounting said impeller means in said impeller housing for rotation
about a substantially vertical axis,
chamber defining means defining a chamber having an inlet and an
outlet, said chamber being disposed adjacent said impeller housing,
said inlet to said impeller housing being in open communication
with said outlet of said chamber, said impeller means serving to
induce vortexing of said fluid in said chamber whereby at least a
portion of the gas accumulating in the central region of said
impeller means is vented through the central portion of the vortex
substantially counterflow to the direction of feed of fluid to said
impeller means.
17. The system of claim 16 wherein said chamber inlet extends
substantially circumferentially around said chamber defining
means.
18. The system of claim 17 wherein there are vertically disposed
spiral vanes disposed in said chamber, said spiral vanes serving to
impart spiral flow to said fluid being drawn into said chamber.
Description
BACKGROUND OF THE INVENTION
The present invention relates to a system for degassing fluids and
more particularly to a system for degassing drilling muds, said
system including a novel centrifugal pump for circulating the fluid
or mud therethrough.
In numerous industrial operations there exist situations in which
it is desirable to substantially remove gas from a fluid being
processed. A prime example of this is in the oil well drilling
industry where the drilling mud used frequently becomes
contaminated, in the well, with natural gas or air. Since it is
uneconomical to continuously supply a source of new mud, it is
necessary that the mud be recycled. However, the presence of the
natural gas or air in the drilling mud decreases its weight and
viscosity, thus markedly diminishing its effectiveness in
preventing blow outs. Accordingly, it becomes necessary to degasify
the drilling mud prior to recycling it to the well.
Numerous prior art systems have been proposed as systems for
degassing drilling muds. Characteristically these systems utilize a
vacuum tank having some sort of baffle structure over which the mud
flows in a thin film, the vacuum in the vessel serving to allow the
gas to escape from the thin film of mud. The released gas is thus
vented from the vessel as waste or if economically feasible to a
gas recovery system. In mud degassing systems employing the above
described baffled-vacuum tank, it is necessary to utilize some form
of prime mover to circulate the gas laden mud through the vacuum
vessel. Numerous pumping systems have been proposed in this respect
as for example the jet-type pumping systems shown in U.S. Pat. Nos.
2,748,884 and 3,241,295 and the mechanical pumping system shown in
U.S. Pat. No. 3,226,916. From the point of view of economy,
simplicity of operation, and ease of maintenance, a mechanical
pumping system such as one employing a centrifugal pump is most
desirable. However, prior art systems employing centrifugal pumps
have not been completely successful due partially to vapor lock of
the pump which of course results in a diminished supply of clean
mud to the well. Moreover, prior art vapor-vented centrifugal pumps
such as that shown in U.S. Pat. No. 2,815,717 are not suitable for
use in mud degassing systems because rapid wearing of the seals due
to the abrasiveness of the mud results in frequent and expensive
repair.
SUMMARY OF THE INVENTION
It is therefore an object of the present invention to provide a
system for degassing fluids and more particularly for degassing
drilling muds.
It is a further object of the present invention to provide a fluid
degassing system which employs a novel centrifugal pump.
Still a further object of the present invention is to provide a
fluid degassing system employing a centrifugal pump which is
substantially free from vapor lock.
An important object of the present invention is to provide a fluid
degassing system for use in degassing drilling muds which system
employs a novel centrifugal pump in which the pump seal is kept
substantially free from contact with the drilling mud.
Another object of the present invention is to provide an improved
centrifugal pump for handling gas laden fluids particularly gas
laden drilling muds.
Yet another object of the present invention is to provide a
centrifugal pump for handling corrosive and abrasive liquids such
as drilling muds in which the pump seal is kept substantially free
from contact with the drilling mud.
These and other objects of the present invention will become
apparent from the drawings, the description given herein and the
appended claims.
In accordance with the above stated objects, the present invention
provides a fluid degassing system including a vessel having in
inlet and an outlet for the intake and discharge of the fluid being
treated and a centrifugal pump connected to the vessel for
circulating the fluid therethrough the centrifugal pump including
an impeller means and means rotatably mounting the impeller within
the pump and a means for removing gas from the region of the
impeller to thereby prevent vapor lock. In one form of the system,
the pump is provided with a means for providing a gas barrier for
preventing the fluid being handled by the pump from contacting the
pump seal through which the pump shaft extends.
In one embodiment of the present invention, the degassing vessel is
operated under vacuum and the centrifugal pump is connected to the
outlet of the vessel while in another embodiment, the centrifugal
pump is connected to the inlet of the degassing vessel which is at
substantially atmospheric pressure and the fluid to be degassed is
forced under pressure into the vessel.
The above objects are further accomplished by a centrifugal pump
for handling gas laden fluids, the pump having a housing with an
inlet and an outlet for the intake and discharge respectively of
the fluids, an impeller means, means for rotatably mounting the
impeller means in the housing and means for venting gas from the
region of the impeller means. The novel centrifugal pump may
further include, when a pump seal is employed, a means for
preventing the fluid being handled by the pump from contacting the
seal. In a preferred embodiment of the centrifugal pump the fluid
is prevented from contacting the seal means through the use of a
gas filled compartment adjacent the seal, the gas filled
compartment serving to form a gas barrier between the fluid and the
seal. The novel gas barrier principle of preventing the fluid from
contacting the seal permits the centrifugal pump to be used for
handling corrosive and/or abrasive materials which would otherwise
cause excessive wear and damage to the seal.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a schematic elevation, partly in section, of the novel
fluid treating system of the present invention.
FIG. 2 is an elevational view, partly in section, showing a
modified centrifugal pumping means for use with the system shown in
FIG. 1.
FIG. 3 is a view similar to FIG. 2 of yet another modification of a
centrifugal pumping means for use with the fluid treating system
shown in FIG. 1.
FIG. 4 is a view taken along the line 4--4 of FIG. 3.
FIG. 5 is a view similar to FIG. 2 of another embodiment of a
centrifugal pumping means for use with the fluid treating system
shown in FIG. 1.
FIG. 6 is a slightly modified variation of the centrifugal pumping
means shown in FIG. 1.
FIG. 7 is a variation, shown in elevation, of the novel fluid
treating system of the present invention.
FIG. 8 is a view, reduced in size, taken along the line 8--8 of
FIG. 7.
FIG. 9 is an elevational view, in section, of another embodiment of
the novel fluid treating system of the present invention.
FIG. 10 is a top view, partly broken away, of the system shown in
FIG. 9.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
In the description that follows, the present invention will be
described with reference to the degassing of drilling muds. It is
to be understood however, that the system can be used for degassing
other fluids containing entrained or dissolved gas.
Referring then to FIG. 1, there is shown a conduit 10 leading from
an oil well (not shown) which feeds a return mud tank 11 with used
drilling mud 12 contaminated with drill cuttings, other solid
materials and gas. Return mud tank 11 communicates with clean mud
tank 13 by means of a restricted conduit 14 thereby assuring that a
constant supply of mud is always available to be fed into the well.
Mud to the well is supplied via pump 15 and conduit 16 which
extends down into clean mud tank 13 to thereby draw in clean mud 17
contained therein. Since the function of the drilling mud in oil
well drilling operations is well known, it is not necessary for
purposes of describing the invention that the process be described.
It is however noteworthy to point out that one of the prime
functions of drilling mud is to provide a fluid head in the well
which will resist the discharge from the well of fluid from a high
pressure zone resulting in a blow out. Because of this latter
function, it is important that the returned, contaminated mud 12 be
freed of gas which may be dissolved or entrained with the mud since
the presence of such gas in excess quantities reduces the specific
gravity of the mud thus lightening the fluid head in the well
annulus. The apparatus herein described and claimed is designed to
effectively degas and otherwise treat the returned drilling mud 12
thereby making it suitable for continuous recycle in the drilling
operation.
Leading from returned mud tank 11 is a pipe or conduit 19 which
opens into a second conduit 19a which in turn opens into the top of
a vacuum treating vessel 20. The open end of conduit 19a is
provided with a threaded cap 19b to allow access into conduit 19a
if necessary. It should be noted that while in the embodiment shown
mud is delivered through the top of vessel 20, the system can be
designed such that it is delivered into vessel 20 from the side
closely adjacent the top.
While vessel 20 can assume any shape, in the embodiment shown
herein, it has a generally cylindrical sidewall 21, flat top wall
22 and downward sloping bottom walls 23 and 24 somewhat axially
displaced from one another so as to form an opening 25 near the
bottom of vessel 20. Vessel 20 has a base portion consisting of a
lower extension 21a of sidewall 21, flat bottom portion 26 and a
lower vertical side section 27 which allows vessel 20 to rest upon
skid 28, vessel 20 being secured thereto by means of an angle iron
bracket 29 which extends around the lower part of the vessel. Skid
28 rests upon supports 30 and 31 so as to allow the entire treating
system to be moved adjacent mud tanks located above the surface of
the ground.
Mounted within vessel 20 closely adjacent the top thereof is a
baffle 32 consisting of a cylindrical upper section 33 adjoined to
an inverted truncated conical lower section 34, truncated conical
section 34 containing an opening 35 at its inverted apex. Also
contained within vessel 20 is a float 36 secured to upper and lower
spindles 37 and 38 respectively. Lower spindle 38 is slidably
mounted in lower sleeve 39 secured to the bottom wall 24 of vessel
20, a stop 39a secured to spindle 38 serving to limit the downward
movement of float 36 should the fluid level drop too low. Spindle
37 extends through flexible diaphragm 40 which is secured at its
periphery between an inwardly extending annular shoulder 19c and
the inner end of cap 19b. Diaphragm 40 is secured to spindle 37 by
being clamped between an annular shoulder 37b and a washer 40a and
retaining nut 40b on the threaded end of spindle 37. A passageway
37a in spindle 37 leads from the space above diaphragm 40 to vessel
20 below valve member 41 thus ensuring equal pressure above
diaphragm 40 and below valve member 4. Affixed to upper spindle 37
by means of a collar 41a is a disc shaped member 41 which has an
area substantially equal to or somewhat greater than the
cross-sectional area of conduit 19a at the point where it opens
into vessel 20. Disc shaped member 41 serves the function of a
control valve such that if float 36 is caused to move upwardly as
the level of fluid in vessel 20 rises, member 41 will effectively
reduce the size of the opening from conduit 19a into vessel 20 as
much as necessary to regulate the flow of fluid into vessel 20.
To maintain sub-atmospheric pressure within vessel 20, a vacuum
pump 42 is connected via a conduit 43 which opens into vessel 20 at
a point always above the liquid level. To control the level of
vacuum within the vessel 20, float 44 is connected through a
linkage 44a to a check valve 45. Check valve 45 is located in
conduit 43 between vacuum pump 42 and the end of conduit 43 which
opens into vessel 20. Upward movement of float 44 closes valve 45
while downward movement opens valve 45.
Connected to the outlet 25 of vessel 20 is a centrifugal pump shown
generally at 46. In the embodiment shown in FIG. 1, the pump
housing comprises a generally cylindrical side wall 47, a flat top
wall 55 and an impeller housing 51 which faces impeller 50. Shaft
48 extends through top wall 55 and is aligned generally
concentrically with side wall 47. The outlet 49 of pump 46 leads
from the impeller housing 51. On the lower end of shaft 48 is
mounted impeller 50, impeller 50 being secured to shaft 48 by hub
51a. Shaft 48 is rotatably mounted at its upper end through a seal
52, seal 52 acting as a barrier against fluids entering the bearing
section 52a. Shaft 48 is driven by a motor (not shown) which
connects by means of a belt 53 to a pulley 54 secured to shaft
48.
Spaced axially from the upper wall 55 and toward impeller 50 is a
baffle 56 which has an opening 57 through which shaft 48 extends.
Opening 57 has a cross-sectional area larger than the
cross-sectional area of shaft 48 such that shaft 48 does not fit
snugly therein. Baffle 56 along with the upper portion of side wall
47 and top wall 55 serve to form a compartment 58 adjacent seal
member 52. A conduit 59 having one end which opens into vessel 20
is in open communication with the interior of pump 46 below
partition 56. Conduit 59 can open into vessel 20 either above or
below the liquid level therein. A baffle 59a is mounted in vessel
20 above the end of conduit 59 and forms a pocket 59b adjacent the
open end of conduit 59 in vessel 20. This arrangement allows gas
escaping through conduit 59 to vent into vessel 20 more easily.
Moreover, when little or no gas is venting through conduit 59, the
pocket 59b maintains a pressure sufficient to prevent fluid from
flowing up into the pocket and down conduit 59. The result is that
the flow through opening 25 into pump 46 is very uniform.
As can be seen from the above description, pump 46 is vertically
mounted, i.e., cylindrical side wall 47 and concentrically disposed
shaft 48 are aligned such that their long axes are substantially
vertical, the drive mechanism of pump 46 being attached to the
uppermost end of shaft 48 and the pumping mechanism i.e., impeller
50, being mounted at the lowermost end of shaft 48. It is this
vertical, axial displacement of the pump drive mechanism from the
pumping mechanism per se which permits the unique operation of the
system shown in FIG. 1 and hereinafter described.
In operation, the system described above and shown in FIG. 1 works
as follows. Contaminated mud 12 from the well flows through line 10
into tank 11 from whence it is drawn up through a conduit 19 by
means of pump 46 into vessel 20. As the mud enters vessel 20, it
impinges upon disc shaped member 41 and because of its velocity
upon entering vessel 20 and the restricted space between member 41
and the opening of conduit 19a into vessel 20, it sprays radially
outward in fine droplets towards the cylindrical wall 33 of baffle
32, where it flows in a relatively thin film downwardly falling
through outlet 35 in baffle 32 onto float 36 where it again flows
in a thin film and finally into the lower portion of vessel 20.
Since vessel 20 is under sub-atmospheric pressure, any gas
dissolved or entrained in the mud is released to the space above
the liquid in vessel 20 and is pumped via conduit 43 to atmosphere
or if economical to a gas collecting system.
To ensure that the mud level in vessel 20 does not exceed a volume
which can be effectively handled by pump 46, the level controller
consisting of float 36 and valve member 41 is employed. When the
level of mud in vessel 20 becomes too great, float 36 will move
upwardly causing disc shaped valve member 41 to partially seal off
conduit 19a, thus regulating the flow of mud into vessel 20.
Diaphragm 40 aids in eliminating pressure surges in conduit 19 and
accordingly prevents pressure surging acting against valve member
41.
In order to control the sub-atmospheric pressure existing in vessel
20, float 44, linkage 44a, and valve 45 in conjunction with vacuum
pump 42 is employed. When the level of mud in vessel 20 rises to a
certain level, float 44, via linkage 44a will act to close check
valve 45 thus cutting off the suction from pump 42. This of course
will prevent excessive reduction of pressure in the upper part of
vessel 20 above the liquid level and will in effect maintain an
adequate pressure in vessel 20 to permit pump 46 to more easily
draw mud from the bottom vessel 20.
The mud which has been degassified and which is in the bottom
portion of vessel 20 is pulled into pump 46 via inlet 60, being
ejected by impeller 50 from pump 46 through outlet 49 into clean
mud tank 13. The unique construction of pump 46, i.e., with the
seal 52 axially displaced from impeller 50 along shaft 48 results
in a generally cylindrical void in the vicinity of shaft 48. The
cylindrical void allows any gas which is collecting in the eye of
impeller 50 to move upwardly adjacent shaft 48, a part passing
through opening 57 in baffle 56 and eventually filling compartment
58, the greater portion entering conduit 59 and passing through
conduit 59 into pocket 59b formed by baffle 59a and then into
vessel 20 to thereby be removed via conduit 43 and pump 42. Besides
the above described functions, the gas pocket collected in baffle
59a prevents direct access of fluid into conduit 59 during the time
when there is little or no gas in the pumped fluid. It should be
noted that at all times a pocket of gas will be maintained in
compartment 58 adjacent to seal 52 thus forming a gas barrier or
seal which substantially prevents any fluid from entering the space
between shaft 48 and seal 52 causing damage to the latter. At the
same time, the unique construction of pump 46 which results in the
formation of the cylindrical void around shaft 48 provides a means
whereby gas collecting in the eye of the impeller will be allowed
to escape thus increasing the efficiency of pump 46. The
degassified and cleaned mud 17 contained in tank 13 is then
returned to the well via conduit 16 and pump 15.
As will be readily appreciated from the above description, while
the pump shown in FIG. 1 has been described as being vertically
mounted, i.e., with the long axis of pump shaft 48 and cylindrical
side wall 47 in a generally vertical position, it is to be
understood that vertical disposition is not necessary. It is only
necessary that pump 46 be disposed at some angle to the horizontal
such that the seal means is elevated above the impeller means such
that gas collecting near the impeller will flow upwardly through
the pump housing and be allowed to enter compartment 58 thus
forming a gas barrier or seal and preventing any fluid from
entering the space between shaft 48 and seal 52 causing damage to
the latter. Thus while mechanical convenience and design dictates
generally vertical disposition of shaft 48, such is not necessary
to enable pump 46 to operate in the fashion described.
Turning now to FIG. 2, there is shown a modification of the pump
system shown in FIG. 1. In this embodiment, the centrifugal pump
shown generally as 61 comprises a bearing casing 62 through which
extends the pump shaft 63 rotatably mounted by means of bearings 64
and 65. Shaft 63 is driven by suitable motor (not shown). Shaft 63
extends into the impeller housing 66 in which is contained impeller
67 secured to the end of shaft 63. Fluid is taken into pump 61 via
inlet 68 and forced out of pump 61 through outlet 69 into the
return mud tank 13. To prevent gas from accumulating in the eye of
impeller 67 thereby reducing the efficiency of pump 61, a conduit
70 extends into pump 61 opening on one end closely adjacent the
central region of impeller 67 and opening on the other end into the
space in vessel 20 above the liquid level.
In the cases shown in FIGS. 1 and 2, the gas being removed from the
region of impellers 50 and 67 respectively, is vented back to the
sub-atmospheric region of vessel 20. It is to be understood
however, that in those cases and in all other embodiments of the
present invention, the gas being removed from the region of the
impeller need only be drained to a region of lower pressure than
that existing in the pump.
In FIGS. 3 and 4 are shown slightly modified embodiments of the
system in FIG. 1. Pump 46 is connected to vessel 20a by horn-shaped
inlet 72 formed by substantially flat horizontal bottom 73 which
also forms the bottom of vessel 20a, substantially flat, vertical
side wall 72b, substantially flat, vertical side wall 72c and a
substantially flat horizontal upper wall 72a. Side walls 72b and
72c converge towards one another at the inlet to pump 46 and
diverge at the point where they adjoin vessel 20a thus forming the
horn-shaped inlet 72. Side wall 47a of pump 46 rather than being
substantially cylindrical as the embodiment of FIG. 1 is distorted
such that it has a snail shell appearance when viewed in a plane
normal to pump shaft 48. Vertical side wall 72b adjoins pump side
wall 47a approximately at the point where the distance between
shaft 48 and wall 47a is greatest while vertical side wall 72c
adjoins pump side wall 47a at approximately the point where the
distance between shaft 48 and side wall 47a is minimal. As will be
observed the overall effect of such a configuration is to funnel
the fluid leaving vessel 20a into pump 46a in such a fashion that
it flows tagentially into pumP 46 up against the inner surface of
side wall 47a. This tagential funneling action coupled with the
action of impeller 50 serves to form a vortex having a void 107 in
the immediate vicinity of shaft 48. This vortexing also results in
a gas space 108 in open communication with void 107 and the open
space above the level of the fluid in vessel 20a. Thus, gas which
collects in the eye of impeller 50 moves upwardly through void 107
adjacent shaft 48 passing through annular opening 57 in partition
56 where it is trapped in compartment 58 thus causing a gas barrier
and preventing the ingress of fluid through opening 57 into
compartment 58 from where it would eventually splash into the space
between shaft 48 and seal 52 thus causing wear on the latter. As
will also be observed, excessive gas escaping from the eye of
impeller 50 and moving up void 107 will collect under upper wall
72a in space 108 and move counter flow to the liquid into the space
in vessel 20a above the liquid level. Thus it is seen that the
embodiment in FIG. 3 also provides a pumping system wherein the eye
of the impeller is continuously freed from any gas which might
build up thereby reducing the pump's efficiency. Unlike the case
shown in FIG. 1, however, the outlet 49 from pump 46 is not
disposed below the level of the liquid in the clean mud tank 13.
Rather the degassed mud is transferred via pipe 74 to the clean mud
tank. This of course is necessitated by the fact that the casing or
lower portion 51 of pump 46 has its upper surface substantially
flush with the bottom 73 of vacuum tank 20a.
As will be observed, the embodiments shown in FIGS. 1 and 3 are
quite similar in that the pump shaft is generally vertically
disposed and there is a compartment displaced axially along the
pump shaft from the impeller which serves as a means for
maintaining a gas barrier between liquid being handled by the pump
and the spacing between the pump shaft and the seal. As we noted
above for the pump design shown in FIG. 1, it is not absolutely
necessary in the embodiment of FIGS. 3 and 4 that the shaft of the
pump be vertically aligned.
Reference is now made to FIG. 5 for yet another embodiment of the
present. An S-shaped conduit 74a leads from the bottom portion of
vacuum vessel 20b to the intake 76 of pump 75. Pump shaft 77,
driven via pulley 77a attached to a motor (not shown), is rotatably
mounted in bearings 78 and 79 which are in turn secured by a
suitable mounting bracket 80. Impeller 81 is secured to the end of
shaft 77 and faces wear plate 82 attached to one end of conduit
74a. A bleed line 83 extends into pump 75 having one open end
disposed closely adjacent the central region or eye of impeller 81.
Bleed line 83 extends upward out of clean mud tank 13 through a
flanged fitting 84 mounted on the side of vessel 20b and then into
vessel 20b, the other open end of bleed line 83 being disposed this
time in the space above the liquid level in vessel 20b. As before
in the other embodiment, bleed line 83 serves the purpose of
allowing gas which may accumulate in the eye of impeller 81 to
escape to the vacuum of vessel 20b thus maintaining the overall
efficiency of pump 75.
Referring now to FIG. 7, there is shown a still further embodiment
of the degassing apparatus of the present invention. Vacuum vessel
shown generally at 20c mounted on legs 85 and 86 has a generally
hemispherical bottom 87 adjoined to a cylindrical side wall 88. For
purposes of simplicity, only the lower section of vessel 20c is
depicted, it being understood that the inlet and liquid
level-controlling systems employed but not shown are substantially
the same as those shown in the previous embodiments with the
exception of a slightly modified float design hereinafter
described. Connected to the lowermost section of vessel 20c and
preferably made integral therewith is an impeller housing 89, the
interior of housing 89 and the interior of vessel 20c being in open
communication via an aperture 20d comprising the outlet of vessel
20c and the inlet of housing 89. Mounted in housing 89 is an
impeller, shown at 90, secured to a shaft 91 by a suitable
retaining nut 92. Shaft 91 is rotatably mounted in bearings 92 and
93 and extends through the end of bearing casing 94, shaft 91
having affixed to the end extending from casing 94 a pulley 95
driven by a motor (not shown) via belts 96. Bearing casing 94 is
removably secured to impeller housing 89 by means of bolts 97.
Impeller 90, which is disposed closely adjacent aperture 20d,
comprises vanes 97 affixed to and extending upward from disc 98 and
has extending from the bottom side of disc 98 a shroud 99 which
forms a cavity 100 partially partitioned by an annular upwardly
extending projection 101 from bearing casing 94. The radially
innermost portion of cavity 100 forms a seal compartment in which
is mounted a seal 102 secured to and rotating with shaft 91,
non-rotating seal ring 103 being supported by resilient seal 104, a
spring in seal 102 urging seal 102 against ring 103 to effect
adequate sealing. Leading from impeller housing 89 is a discharge
pipe 105 through which the degassed fluid flows into tank 13.
Secured to the bottom of vessel 20c are a plurality of spiral fins
109. Connected to several of the spiral fins 109, although, if
desired, to all of fins 109 are brackets 110 which extend inwardly
toward the center of vessel 20c where they are commonly connected
to a guide spindle 111 which is slidably mounted in a suitable
passageway 112 in the underside of float 113. Float 113 unlike
float 36 shown in FIG. 1 has a concave surface 114 on its underside
resulting in the formation of a cavity 115 which forms an air
pocket under float 113. Leading from cavity or air pocket 115 is a
conduit 116, one end of which opens into cavity 115 the other of
which opens above the level of fluid in tank 20c. Spiral fins 109
while acting to induce a fluid flow pattern hereinafter described
also serve the purpose of acting as a stop to limit the downward
movement of float 113 should the level of liquid in vessel 20c drop
too low. As explained, the diaphragm and valve system plus the
means used to control the vacuum in the system in FIG. 7 is
identical with that shown in FIG. 1.
In operation, the system described in FIG. 7 works as follows:
fluid in vessel 20c is drawn through opening 20d by impeller 90.
Because of the presence of spiral fins 109, the fluid is diverted
into a clockwise flow pattern as it leaves vessel 20c. As the fluid
enters impeller housing 89, it is immediately thrust radially
outward away from the eye of impeller 90. The combination of the
clockwise induced flow and the action of impeller 90 results in the
formation in vessel 20c of a vortex having a void 106 up through
which gas present in the fluid and being disengaged at the impeller
90 escapes and collects in space 115 where it passes via conduit
116 to the air space in vessel 20c. Since the action of impeller 90
in the system shown in FIG. 7 is to move the fluid being handled
radially outward away from the eye, an annular lower pressure
region is formed on the underside of disc 98 adjacent shaft 91. Any
gas which enters impeller housing 89 will migrate to this lower
pressure region on the underside of plate 98 and will in fact
gather in cavity 100 thus forming a gas barrier and effectively
preventing any fluid within impeller housing 89 from contacting the
seal comprised of components 102 and 103. Although impeller 90 is
seen as having a shroud 99 extending from the underside of plate
98, the presence of such is not necessary in order to ensure that
any gas entering impeller housing 89 will collect on the underside
of plate 98 and be trapped in cavity 100. Such a shroud however
aids in maintaining gas which has collected under impeller plate 98
in cavity 100. In effect, the operation of the system is similar to
a centrifuge where the heavier materials, i.e., the degassed
liquid, is thrown radially outward by the impeller whereas the
lighter material, i.e., the gas, migrates to the central region
thus providing the gas barrier necessary to prevent contact of the
seal means with the fluid being handled by the system.
Reference is now made to FIG. 9 and 10 for an embodiment of the
present invention in which the degassing vessel is not operated
under sub-atmospheric pressure conditions. The degassing vessel,
shown generally at 120, comprises a cylindrical upper section 121
and an inverted, truncated conical lower section 122. A conduit 123
leads from the inverted apex of conical section 122 and has an
opening 124 through which degassed mud discharges into clean mud
tank 125. A second conduit 126 extends up through the central
portion of vessel 120 forming inlet 127 to vessel 120. A vent pipe
128 leads from the interior of vessel 120 through flat top wall 129
thus providing substantially ambient pressure operation of vessel
120. A removable hatch 130 secured to wall 129 provides access to
the interior of vessel 120, hatch 130 being secured by a threaded
connection, bolting or some other such means of removably fastening
it to wall 129. Affixed to the underside of hatch 130 and extending
into vessel 120 is a downwardly projecting member 131 having a
longitudinally extending slideway 132 which opens into vessel 120.
Slidably positioned in slideway 132 is a spindle 133 which on one
end is secured to disc shaped plate 134. Disc shaped plate 134 is
also secured to one end of a coil spring 135, the other end of
which is attached to the underside of hatch 130, spring 135 being
concentrically disposed about member 131, slideway 132 and spindle
133. As will be seen, removal of hatch 130 results in removal of
the assemblege consisting of spring 135, disc 134 and member
131.
The inlet 127 to vessel 120 is closely adjacent the bottom side of
disc 134 such that fluid being forced into vessel 120 impinges on
the underside of disc 134 and because of the restricted nature of
the opening between the end of conduit 126 and disc 134, is sprayed
out radially from opening 127 in fine droplets whence it impinges
on walls 121 and 122 and then flows in a thin film to the bottom of
vessel 120 eventually passing out through outlet 124. Since disc
134 is resiliently biased by coil spring 135, it serves somewhat as
a flow regulator to the extent that if the flow through conduit 126
becomes large, disc 134 will be moved upwardly against the biasing
of spring 135 thus allowing a greater flow of fluid into vessel 120
while still ensuring that the fluid entering vessel 120 will flow
radially outwardly in fine droplets in the manner herein before
described. It should also be noted that spring biased disc 134 is
not necessary for operation of the system shown in FIG. 9. Indeed,
the apparatus shown in FIG. 9 can be somewhat simplified by moving
the inlet 127 to vessel 120 closer to the top wall of vessel 120
and fabricating top wall 120 of relatively thin sheet metal which
has some degree of flexibility and therefore a built in biasing
characteristic.
Extending from the cylindrical side wall 121 of vessel 120 is a
bracket 136 secured to an I-beam 137. Extending from I-beam 137 are
bearing mounting brackets 138 and 139. Secured to the lower portion
of I-beam 137 is a centrifugal pump shown generally at 140
comprised of an open ended, cylindrical, upper wall section 141, a
truncated, conical, intermediate wall section 142 and a cylindrical
lower wall section 143. Cylindrical lower wall section 143, which
forms a housing for the pump impeller 154, has extending
tangentially therefrom pump outlet 144, pump outlet 144 being in
open communication with conduit 126. Extending radially outward
from the lowermost edges of conical wall section 142 is an annular
flange 145, the outside diameter of annular flange 145 being
approximately the same as the outside diameter of cylindrical lower
wall section 143. An impeller wear plate 146 having a generally
centrally disposed aperture 147 is secured at its outer edges to
the uppermost edge of wall section 143. Extending vertically upward
from and attached to the top surface of wear plate 146 are a series
of radially disposed spiral vanes 148, vanes 148 being connected at
their upper edges to the underside of annular flange 145. It will
thus be observed that wear plate 146 serves to divide pump 140 into
an upper chamber 149 and a lower chamber 150, upper and lower
chambers 149 and 150 respectively being in open communication via
aperture 147. A circumferentially extending inlet 151 is formed
between the underside of annular flange 145 and the upper surface
of wear plate 146, the only impediment to flow of fluid through
inlet 151 being the spiral vanes 148 disposed therein.
A shaft 152 rotatably mounted in upper and lower bearings (not
shown) held in upper and lower bearing brackets 138 and 139
respectively extends substantially vertically down into pump 140,
passing through aperture 147 in wear plate 146 and terminating in
lower chamber 150. Secured to the end of shaft 152 in chamber 150
by means of a hub 153 is impeller 154 having upwardly projecting
vanes 155. Attached to the uppermost end of shaft 152 is a drive
pulley 156 which is driven by means of belt 157, motor pulley 158,
shaft 159 and motor 160. Motor 160 is secured to motor mounting
bracket 161 suitably attached to the mounting assembly comprised of
members 136 and 137. Pump 140 is disposed in return mud tank 161
such that, when the system is operating, the intake 151 will be
submerged below the level of mud in tank 161. A right angle conduit
162 connects clean mud tank 125 and return mud tank 161 and serves
to ensure that return mud tank 161 will always have a supply of
fluid. When the level of mud in clean mud tank 125 reaches a
certain level, it will begin to flow back into return mud tank 161
thus ensuring that a supply of mud will always be available for
pump 140 to circulate.
In operation, the used mud is drawn into the circumferential inlet
151 of pump 140 where vanes 148 cause a clockwise flow to be
imparted to the mud. The momentum of the spiraling fluid is
conserved as it is drawn into the lower chamber 150 by impeller 154
which acts to thrust the mud radially outwardly, the mud eventually
passing through tangential outlet 144, conduit 126 and into
degassing vessel 120. The combined action of the spiral vanes 148
and impeller 154 serve to produce a vortex having a void 163
disposed generally concentrically about shaft 152 and up through
which gas being disengaged at impeller 154 is vented to atmosphere
through the open end 164 of pump 140. The fluid being pumped
through conduit 126 and discharged into vessel 120 impinges on the
underside of disc 134 as it enters vessel 120. Due to its velocity
upon entering vessel 120, and because of the fact that the
discharge area into vessel 120 is relatively confined, the fluid is
forced to spray radially outwardly towards the walls of vessel 120
and subsequently flows in a relatively thin film downwardly over
the inside of vessel 120. Because of the large surface area
exposed, any gas entrained or dissolved in the mud is allowed to
escape therefrom and is vented to atmosphere through vent pipe 128.
Thus, the mud flowing out of vessel 120 and into clean mud tank 125
is essentially free of any dissolved or entrained gas and may then
be returned to the well. As in the other embodiments shown, the
system shown in FIG. 9 and 10 provides a degassing system wherein
the centrifugal pump employed to circulate the fluid through the
degassing vessel contains a means whereby gas being disengaged from
the fluid in the region of the impeller can be vented.
As can be seen from the desciptions given above of the various
embodiments of the present invention, the degassing systems all are
provided with means whereby gas accumulation occurring in the
region of the pump impeller can be reduced. While in all cases
shown, gas is removed from the eye or central region of the
impeller, it is to be understood that it may be desirable to
provide a gas vent radially outward from the eye of the impeller,
i.e., near the ends of the vanes such that any gas accumulating in
the vanes will be dispelled. This could be accomplished, for
example, by providing a vent in the top plate of impeller housing
51 (FIG. 1) and running a conduit from the vent back through the
pump housing 47, and allowing the end of the conduit to open
closely adjacent shaft 48. Gas thus removed from above the vanes of
the impeller would move up the cylindrical void counter flow to the
liquid around shaft 48 in the manner above described.
It is well known that gas accumulation in centrifugal pumps can
cause vapor lock thus reducing the efficiency of the pump. In cases
such as oil well drilling where it is absolutely necessary that a
source of mud be available at all times to maintain a sufficient
head in the well annulus to prevent a well blow out, the pump being
used to pass the used mud through the treating system must operate
effectively and continuously. In prior art degassing systems
employing centrifugal pumps of conventional design, it has been
noted that the liquid output is intermittent to the extent that
when much gas is present in the liquid, very little liquid is
pumped out of the system because of the fact that the gas has no
where to escape and accordingly must be discharged by the pump into
the clean mud tank. The system of the present invention circumvents
this problem because of the fact that the gas is allowed to escape
counter flow through the liquid being handled by the pump such that
it is not necessary for the pump to discharge such gas through the
discharge outlet into the receiving tank. This of course results in
a virtually continuous and constant quantity of mud or other such
liquid being delivered by the system rather than an intermittent
delivery of mud or liquid from the system as is usually the case
with the prior art systems.
As explained above, while the system has been described with
particular reference to the degassing of drilling muds, the pump
embodiments shown in FIGS. 1, 3, and 6 are particularly suitable
for handling abrasive and/or corrosive fluids containing virtually
no gas. In pumping such materials, a common source of trouble is
the wearing of the pump seal due to the seepage of the abrasive or
corrosive material between the seal and the pump shaft and the
sliding or movable members of the seal. The utilization of the gas
barrier in compartment 58 acts as a means to prevent such materials
from seeping into the space between the shaft and the seal. Thus in
cases where gas free abrasive and/or corrosive materials are being
handled, an external source of gas can be supplied. For example, in
the embodiment shown in FIG. 6, line 71 could be used as a means to
introduce a gas into compartment 58 thereby building up a pressure
sufficient to prevent the seepage of the abrasive and/or corrosive
material through space 57 into compartment 58. Likewise, such
provisions could be carried out with the embodiment shown in FIG. 1
and FIG. 3, simply by providing a means to introduce gas into
compartment 58 and pressurizing it sufficiently to prevent any back
flow of fluid into compartment 58. Likewise a conduit could be
disposed to lead from cavity 100 (FIG. 7) to atmosphere whereby air
would be drawn in forming the gas barrier.
* * * * *