U.S. patent number 3,814,545 [Application Number 05/325,028] was granted by the patent office on 1974-06-04 for hydrogas lift system.
Invention is credited to William Eugene Waters.
United States Patent |
3,814,545 |
Waters |
June 4, 1974 |
HYDROGAS LIFT SYSTEM
Abstract
A power fluid is pumped downwardly through a power fluid tube
toward the bottom of a well. The power fluid, due to pressure
placed on the power oil fluid by a surface pump, forces the
production fluid through a check valve and upwardly through a
production fluid tube to the surface of the wall. Compressed gas is
used to withdraw the power fluid from the power fluid tube so that
the production fluid may again rise to the level of the production
fluid tube and the pumping cycle is thereafter repeated. The power
oil may also be removed by swabbing, rod pump, rotary pump, or any
other form of artificial lift which may be applicable to the
well.
Inventors: |
Waters; William Eugene
(Maracaibo, VE) |
Family
ID: |
23266127 |
Appl.
No.: |
05/325,028 |
Filed: |
January 19, 1973 |
Current U.S.
Class: |
417/90; 417/109;
417/92 |
Current CPC
Class: |
F04F
1/08 (20130101); E21B 43/121 (20130101) |
Current International
Class: |
E21B
43/12 (20060101); F04F 1/08 (20060101); F04F
1/00 (20060101); F04f 011/00 (); F04f 001/20 () |
Field of
Search: |
;417/92,101,54,55,99,103,108,109,111,90 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Croyle; Carlton R.
Assistant Examiner: Gluck; Richard E.
Attorney, Agent or Firm: Byrne; John J.
Claims
I claim:
1. A system for lifting a production fluid comprising,
a well casing,
a power fluid tube and a production tube within said well
casing,
said production tube including a first one-way valve for allowing
the production fluid to pass only in the upward direction through
the production tube,
a second one-way valve located in said well casing below said first
one-way valve for allowing said production fluid to pass only in
the upward direction,
a compressor for forcing a gas through said well casing,
a reservoir for storing a power fluid,
a pump disposed between said reservoir and said power fluid tube
for driving said power fluid from said reservoir through said power
fluid tube, said power fluid causing said production fluid to be
forced upwardly through said production tube,
first means for displacing said power fluid with said gas after a
predetermined amount of power fluid has been pumped from said
reservoir, and
wherein said first means includes a gas lift valve means for
passing said gas from said well casing to said power fluid tube,
said gas forcing said power fluid back through said power fluid
tube.
2. A system for lifting a production fluid comprising,
a well casing,
a power fluid tube and a production tube within said well
casing,
said production, tube including a first one-way valve for allowing
the production fluid to pass only in the upward direction through
the production tube,
a second one-way valve located in said well casing below said first
one-way valve for allowing said production fluid to pass only in
the upward direction,
a compressor for forcing a gas through said well casing,
a reservoir for storing a power fluid,
a pump disposed between said reservoir and said power fluid tube
for driving said power fluid from said reservoir through said power
fluid tube, said power fluid causing said production fluid to be
forced upwardly through said production tube,
first means for displacing said power fluid with said gas from said
compressor after a predetermined amount of power fluid has been
pumped from said reservoir,
a second means for separating said gas and power fluid,
a bypass line connecting said second means to said power fluid
tube,
a control means for selectively operating said pump, said control
means being responsive to the level of power fluid in said
reservoir,
a bypass valve in said bypass line selectively opened and closed by
said control means, and
wherein said control means is responsive to a predetermined high
level and a predetermined low level of said power fluid in said
reservoir, said control means causing said pump to energize and
said bypass valve to close upon said power fluid attaining said
predetermined high level and said control means causing said pump
to de-energize and said bypass valve to open upon said fluid
attaining said predetermined low level.
3. A system for lifting said production fluid of claim 2 wherein
said power fluid is introduced into said well casing above said
second one-way valve by said pump at a pressure sufficient to close
said second one-way valve.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates generally to the pumping or lifting of a
subsurface liquid by a liquid of a lower density. The lower density
liquid is drawn toward the surface again by means of compressed
gas. The compressed gas and the liquid are then separated at the
surface and recycled in subsequent pumping operations. If another
form of artificial lift is used, then the separator and gas
compression system may be eliminated.
2. Description of the Prior Art
Prior art oil pumping systems oftentimes depend on natural oil
pressure, artificial suction, or the injection of a gas or liquid
to drive or draw petroleum to the surface. Typical of such systems
is that disclosed in the Rich et al. U.S. Pat. No. 3,653,717 which
depicts a system for lifting enriched solvents in solution mining
wells by means of a liquid immiscible with, and lighter than, the
solvent which is extracted.
There are several drawbacks to the prior art methods of operation.
For instance, at great well depths, the efficiency and capacity
decrease. Also, prior art systems often require the use of means to
cope with high pressures at the surface. This often requires the
installation of expensive, low-capacity equipment which renders
such systems uneconomical. Moreover, many prior art systems cannot
control the large drops in pressure that may occur in an oil well.
A further problem with prior art systems is that when gas lift
valves are used in cooperation with compressed gas to lift crude
petroleum from a well, the crude will frequently emulsify and
become a foam. Typically, the foam is of very light density and
little crude is brought to the surface in this manner. It is
difficult to separate compressed gas from the crude petroleum once
the foam reaches the surface. The present invention provides an
improved solution to these problems.
SUMMARY OF THE INVENTION
The present invention is designed to overcome the deficiencies of
the prior art as described above. Also, a system has been provided
that is rugged and simple and contains few moving parts. A
principal advantage of the gas-hydraulic system described herein is
that maintenance costs are kept to a minimum. The working
environment of an oil field demands that all equipment have the
capability to withstand rough daily punishment.
With this in mind, a system has been developed using both gas and a
power fluid in an artificial lift system. A power fluid is pumped
down a power fluid tube into an enclosed chamber at the bottom of
the pipe string. The bottom of the chamber includes a check valve
permitting the production fluid to enter the chamber when the
pressure above the valve is lower than the pressure below the
valve. As the power fluid is pumped into the chamber, production
fluid is forced upwardly via a dip tube and through a discharge
type check valve into a production tube. Compressed gas may be used
to withdraw the power fluid or other conventional forms of
artifical lift may be employed to evacuate the power oil from the
power oil string.
A principal object of this system is to accomplish pumping from
very deep wells with a high pumping efficiency.
Another object of this invention is to be able to control the well
from the surface, thus eliminating the high cost of a work-over rig
if one is necessary.
A further object is to develop a hydraulic pump with a relatively
low surface pressure requirement and which is rugged and requires
few moving parts.
A still further object of this invention is to increase the rate of
production of an oil well while maintaining the pressure at the
bottom of the well relatively constant.
BRIEF DESCRIPTION OF THE DRAWINGS
For a better understanding of the invention, reference is made to
the following description of representative embodiments thereof and
to the accompanying drawings wherein:
FIG. 1 is a schematic depicting the hydrogas lift system at the end
of the power fluid pump cycle when the power fluid in the power oil
storage reservoir has reached the level of the low level control.
The power fluid in the power fluid tubing is returned back to the
power fluid reservoir via a separator by means of compressed gas
introduced into the power fluid tubing; and
FIG. 2 shows the hydrogas lift system of FIG. 1 wherein the power
fluid is in contact with the high level control on the power fluid
reservoir. The pumping cycle is about to begin.
DESCRIPTION OF AN EMBODIMENT
In describing this invention, reference is made to both FIG. 1 and
FIG. 2 wherein like elements are similarly numbered. FIG. 1 and
FIG. 2 show the hydrogas lift system at different points in the
lift. The system includes a production tube 10 and a power fluid
tube 12 which fits inside and extends the entire length of a power
string casing 14. At the bottom end of the production tube 10 there
is a one-way discharge valve 16. The discharge valve 16 allows
production fluid 58 to flow upwardly through the valve into the
production tube 10 but does not allow production fluid 58 to flow
back through the production tube.
A dual packing 18 is provided at the bottom of the power fluid tube
12 in order to contain the compressed gas stored within the power
string casing 14 and to support the power fluid tube 12 and the
production tube 10. A similar packing is shown at the top of the
well as element 20. The packings 18 and 20 are designed to prevent
the compressed gas 22 from leaking from the well casing 14.
A one-way standing check valve 24 is shown at a location below
discharge valve 16. The packing is provided about the standing
valve 24 to form a pressure-tight chamber 26 between the packing 18
and the standing valve 24. A series of gas lift valves 28 are
placed at intervals along the power fluid tubing 12. Conventional
gas lift valves such as the CM2FS-RC type made by the MACCO Oil
Tool Company, Inc. are satisfactory for this type of operation. Gas
lift valves are valves which permit a compressed gas to enter a
pipe string when the differential pressure between the fluid in the
pipe string and the compressed gas reaches a predetermined point.
In this particular application, compressed gas may enter the pipe
string at the end of the pumping cycle when triplex pump 36 shuts
off. The gas lift valves allow the compressed gas 22 inside the
casing 14 to flow into the power fluid tubing 12 at the end of the
pump cycle thereby returning power fluid 30 to a separator 32 and
then to a power fluid reservoir 34.
The power fluid reservoir stores the power fluid 30 and the now
decompressed gas 22 is returned to the compressor 46 for
recompression. A triplex type pump 36, driven by an electric motor
38, is connected to the bottom discharge line 40 from the power
fluid reservoir 34. The pump 36 powers the fluid 30 downwardly
through the power fluid tubing 12.
Mounted within the power fluid reservoir 34 is a high level control
48 and a low level control 50. Controls 48 and 50 are sensitive to
the fluid level in the power fluid reservoir. They, in turn,
control the opening and closing of motor valve 44 and the operation
of electric motor 38 which drives triplex pump 36.
A dip tube 52 extends from the bottom of production tube 10 into
production fluid 58. Discharge valve 16 is located at the lower end
of dip tube 52. Another one-way check valve 54 is mounted on the
discharge port 56 of the triplex pump 36. Valve 21 prevents
compressed gas 22 and power fluid mixture from returning to the
pump 36.
DESCRIPTION OF OPERATION
FIG. 2 shows a hydrogas lift system immediately after to the
beginning of the power fluid pump cycle. Prior to this stage, power
fluid 30 is entering reservoir 34. When the level of power fluid
reaches the high level control 48, motor valve 44 is caused to
close and motor 38 is energized and pump 36 is operated. By action
of pump 36, the power fluid 30 from reservoir 34 is driven through
check valve 54 and downwardly through power fluid tube 12. It is,
of course, understood that power fluid 30 is of a lower density
than that of production fluid 58. Typically, power fluid 30 is an
oil rated about 55 gravity crude. As a result of the pumping
action, power fluid 18 will fill the chamber 26 between packing 18
and standing valve 24. As chamber 26 is filled with power fluid 18,
production fluid 58 trapped within the chamber is displaced and
forced to flow through discharge valve 16 of production tube 1 and
towards the surface. At this time, standing valve 24 is closed
because the pressure above the valve is higher than the pressure
below it. Similarly, discharge valve 16 is caused to open because
the pressure below it is higher than the pressure above it.
After a predetermined amount of power fluid 38 is pumped out of
reservoir 34, the low level control 50 is tripped. The low level
control 50, in turn, de-energizes electric motor 38, pump 36 stops,
and the motor valve 44 is opened. This stage of the operation is
shown at FIG. 1.
At this point, gas lift valves 28 open and the compressed gas 22
within the casing 14 flows into the power fluid tube 12 causing the
power fluid 30 within the tube to rise through motor valve 44 and
the by-pass line into separator 32. In operation, the gas lift
valves would not all operate simultaneously but rather would be
operated in sequence with the valve or valves closest to the
surface opening first and with the lower valve sequentially opening
as the differential pressure between the power fluid and the
compressed gas reaches the predetermined point at which the
particular selected gas lift valve will operate. The gas lift
valves do not have to be located equidistant from one another along
the power fluid string. In fact, it is preferred that the gas lift
valves be located closer to one another the deeper those valves are
located on the power fluid string. The purpose of placing the gas
lift valves closer to each other at deeper depths is to give added
boosting power where it is needed. The deeper valves have to
provide more power because they must lift not only the increment
between themselves and the nearest valve up the string, but they
must also lift all of the foam and residue in the power string
located between the next uppermost valve and the surface of the
well. The compressed gas and power fluid mixture does not flow back
into pump 36 because check valve 54 is closed. The compressed gas
22 displaces power fluid 30 and causes its withdrawal from chamber
26. As power fluid 30 is withdrawn from chamber 26 an equal volume
of production fluid 58 is drawn through one-way standing check
valve 24 to replace the power fluid that has been withdrawn. The
pressure within chamber 26 at this time is lower than during the
pump cycle and discharge valve 16 is closed due to the higher
pressure of the production fluid 58 within tube 10. The compressed
gas and power fluid mixture flows into separator 32 where it is
segregated. The compressed gas 22 is returned to casing 14 by means
of compressor 46, and power fluid 30 is returned to power fluid
reservoir 34. As the power fluid 30 is returned to the power fluid
reservoir, the level of the power fluid 30 rises. When a sufficient
amount of the power fluid 30 is withdrawn from chamber 26, the
level of the power fluid in power fluid reservoir 34 will again
reach the high level control 48. At this point, the pump cycle as
shown in FIG. 2 begins again. Each operation of the pump cycle
causes a pre-determined increment of production fluid 58 to flow up
production tube 10. Repeated pumping eventually causes this
increment to reach ground level.
While gas lift valves have been shown as a preferred means of
removing the power oil from the power oil string, it is clear that
there are many other ways of performing the same function. For
instance, it would be further possible to withdraw the power oil by
means of a swab which is drawn up the power oil string at
predetermined intervals. Also, a rod pump or a rotary pump or any
other form of artificial lift may be used to withdraw the power
oil.
Other modifications of the described embodiment may be obvious to
one of ordinary skill in the art. For instance, separator 32 which
has been shown in FIGS. 1 and 2 to be of the conventional,
horizontal variety, may be vertical instead. Also, it is clear that
this application is not intended to be limited to the production of
petroleum. This method instead may be employed to lift any type of
suitable production fluid by means of a lighter power fluid.
In a general manner, while there has been described an effective
and efficient embodiment of the invention, it should be well
understood that the invention is not limited to such an embodiment,
as there might be changes made in the arrangement, disposition, and
form of the parts without departing from the principle of the
present invention as comprehended within the scope of the
accompanying claims.
* * * * *