U.S. patent number 3,653,438 [Application Number 04/859,293] was granted by the patent office on 1972-04-04 for method for recovery of petroleum deposits.
Invention is credited to Robert J. Wagner.
United States Patent |
3,653,438 |
Wagner |
April 4, 1972 |
METHOD FOR RECOVERY OF PETROLEUM DEPOSITS
Abstract
A method for recovery of petroleum deposits, particularly those
deposits which are underlain by a water zone, which method includes
the steps of introducing a dissolving gas product into an upper
region of a petroleum deposit to enable gravity head build-up of
more soluble petroleum products which then flow downward toward a
recovery zone for delivery to a surface recovery unit. The method
is particularly adaptable for utilization with a single well-bore
whereupon a dissolving injection gas can be introduced down an
outer annulus of the pipe string while recovered petroleum can be
withdrawn from a lower recovery zone for conduction up a tubing
string or such to the earth's surface. An inert gas introduced
through another bore into upper regions of the deposit serves to
maintain proper pressure balance throughout the system.
Inventors: |
Wagner; Robert J. (Oklahoma
City, OK) |
Family
ID: |
25330518 |
Appl.
No.: |
04/859,293 |
Filed: |
September 19, 1969 |
Current U.S.
Class: |
166/266; 166/306;
166/401; 166/272.1 |
Current CPC
Class: |
E21B
43/40 (20130101) |
Current International
Class: |
E21B
43/34 (20060101); E21B 43/40 (20060101); E21b
043/24 (); E21b 043/18 () |
Field of
Search: |
;166/266-269,272,303,306,274 |
References Cited
[Referenced By]
U.S. Patent Documents
Other References
kennedy, Harvey T., Oil Recovery by L. P. G. Injection In Oil &
Gas J., June 30, 1952, p. 58..
|
Primary Examiner: Novosad; Stephen J.
Claims
What is claimed is:
1. A method for recovery of petroleum products from a sub-terranean
reservoir utilizing an existing well-bore having standard casing
and tubing installation in communication with the reservoir,
comprising the steps of:
effecting perforation of a well-bore proximate the upper region of
said reservoir;
introducing a gas which is soluble in petroleum product down said
well-bore and through said perforation into contact with petroleum
product in the upper regions of said reservoir;
injecting a gas inert to said petroleum product at pre-selected
pressure at a point removed from said area proximate to the
well-bore perforations into upper regions of said reservoir
relative to said perforations; and
withdrawing reduced viscosity petroleum product from a recovery
zone disposed generally vertically below said perforation area and
moving said recovered petroleum product up through the well-bore
installation to the surface for further processing.
2. A method as set forth in claim 1 wherein said solvent gas is
heated to a preselected temperature relative to the reservoir
temperature before introduction through said well-bore perforation
into the upper regions of said reservoir.
3. A method as set forth in claim 1 which is further characterized
in that:
said method including introduction of solvent gas through
perforations of a well-bore with recovery of dissolved, less
viscous petroleum product therebelow, is effected at each one of a
plurality of well-bores in communication with said reservoir.
4. A method as set forth in claim 1 which further includes steps
of:
processing said recovered petroleum product to extract said soluble
gas therefrom; and
reintroducing said soluble gas down said well-bore and through said
perforation.
5. A method as set forth in claim 1 wherein said soluble gas is
carbon dioxide.
6. A method as set forth in claim 1 wherein said soluble gas is a
mixture of carbon dioxide and liquified petroleum gases.
7. A method as set forth in claim 1 wherein said gas inert to the
petroleum product is nitrogen or other low value gas.
8. A method as set forth in claim 1 which is further characterized
by the step of:
maintaining sufficient back pressure against the petroleum product
in the recovery zone such that additional force must be exerted to
move said recovered petroleum product to the surface without
reducing pressure within the recovery zone.
9. A method as set forth in claim 1 which is further characterized
to include the steps of:
maintaining predetermined back pressure against the less viscous
petroleum product in the recovery zone; and
pumping said less viscous petroleum product to the surface while
maintaining the bottom hole pressure at an optimum level.
10. A method for recovery of petroleum products from a
sub-terranean reservoir having an underlying formation containing
water, the method utilizing existing well-bores having standard
casing and tubing installations in communication with the
reservoir, comprising the steps of:
effecting perforation of one of said well-bores proximate the upper
region of said reservoir;
introducing a gas, which is soluble in and effective to reduce the
viscosity of petroleum product, down said one well-bore and through
said perforation into contact with petroleum product in the upper
regions of said reservoir adjacent said one well-bore, said gas
introduction being effected at a pressure which is generally
equivalent to the bottom hole pressure of said well-bore thereby to
prevent flow of water into the bottom hole recovery zone; and
drawing reduced viscosity petroleum product from said recovery zone
disposed generally vertically below said perforation area and
pumping said recovered petroleum product up through said well-bore
installation to the surface for further processing.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates generally to secondary recovery processes for
earth deposits of petroleum product and, more particularly, but not
by way of limitation, it relates to an improved secondary recovery
process for withdrawing high viscosity petroleum from an earth
bound pool or reservoir which is underlain by a water zone.
2. Description of the Prior Art
The prior art includes various methods and types of apparatus for
employ in withdrawing additional petroleum product from earth
reservoirs after initial pressures have reduced, or for use when
the petroleum viscosity versus bottom hole pressure relationship is
such that natural flow is stopped or at least greatly reduced.
There are various forms of such secondary processes such as steam
injection, water flooding, alcohol injection, in situ combustion
and various forms of gas injection.
One well-known form of gas injection process utilizes an input gas
for dissolution of higher viscosity oil within a permeable strata
whereupon constant application of nitrogen under pressure will
cause migration of lowered viscosity petroleum product towards a
recovery zone at an adjacent well bore. Nitrogen gas is introduced
for the purpose of maintaining a relatively constant driving
pressure for any gas cap produced by the injected gas, e.g. carbon
dioxide. While the various recovery processes form migrating heads
of petroleum product in many different compositions of strata with
varying efficiency and degrees of success, none of the prior art
methods has been directed to the utilization of a gravity driven
cap or head which is particularly adaptable for use in a single
well-bore recovery process.
SUMMARY OF THE INVENTION
The present invention contemplates a secondary recovery process for
withdrawing certain forms of petroleum product from an earth
reservoir. In a more limited aspect, the invention consists of a
method for injection of a gas into the upper portion of a petroleum
reservoir, the gas dissolving in the petroleum liquid and thereby
lowering the liquid's viscosity, and the lowered viscosity
petroleum liquid then moved downward under force of gravity towards
a lower recovery zone in the petroleum reservoir. The lower
viscosity petroleum is withdrawn from the recovery zone for
processing and storage at a surface unit and, if desired or even
necessitated, pressure stabilizing inert gas can also be injected
from a surface storage facility in order to occupy the space voided
by the lowered viscosity petroleum liquid which moved toward the
recovery zone.
Therefore, it is an object of the present invention to provide a
recovery process which is more economical and more efficient than
existing recovery processes as employed in certain recovery
situations.
It is also an object of the present invention to provide a
secondary recovery process which can be employed with petroleum
deposits which are underlain by water zones.
Finally, it is an object of the present invention to provide a
secondary recovery process which may be variously employed in well
pools having any of one or more well bores in communication
therewith.
Other objects and advantages of the invention will be evident from
the following detailed description when read in conjunction with
the accompanying drawings which illustrate the invention.
BRIEF DESCRIPTION OF THE DRAWING
FIG. 1 is a sectional, schematic representation of earth including
a petroleum deposit and utilizing the recovery method of the
present invention; and
FIG. 2 is a block diagram of one form of surface processing
equipment which may be utilized in carrying out the method of the
present invention.
DETAILED DESCRIPTION OF THE INVENTION
Referring now to FIG. 1, a section of earth 10, having a surface 12
is underlain by a permeable rock formation 14 in which the upper
portion 16 is occupied by a petroleum reservoir and the lower
portion 18 is occupied by water. The permeable rock formation 14
may be overlain and thereby confined by such as an impermeable
formation 20 while the underside of the water bearing portion 18 is
also limited by a low permeability stratum 22.
The exact materials, permeabilities and configurations of
oil-bearing strata and surrounds are variable within wide limits as
the present method is adjusted for whatever the applicable
exigencies. The recovery method is particularly applicable to those
petroleum reservoirs containing high viscosity oils present within
oil-bearing strata having high rock porosities and high
permeability. It is then intended that lowering of the oil
viscosity by a predetermined amount followed by production removal
of the oil from the reservoir without creating large pressure
differentials will enable a more efficient oil recovery.
Assuming then that oil-bearing stratum 16 contains a quantity of
high viscosity petroleum product which it is desirable to recover,
extraction can be effected through any one of a plurality of
well-bores 24, 26 and 28. The well-bores 24, 26 and 28 merely
illustrate a plurality of well-bores in an established oil field or
producing area, any one of which may be utilized for carrying out a
secondary recovery process. Still another bore hole 30 may also be
employed for purposes of pressurizing the oil-bearing stratum 16,
as will be further described below.
With respect to the well-bore 24, an extraction well as employed in
the method, a suitable form of petroleum soluble gas is injected
down the well-bore 24 through the annular volume 32 as may be
defined between casing 34 and a tubing string 36. The casing 34
will be existing structure previously set down, cemented and
finished upon initial completion of the well-bore 24, and the
tubing string 36 may also be the existing or prior-used oil
delivery tube.
The upper reaches of oil-bearing stratum 16 along well-bore 24 are
then determined so that the injected gas from annulus 32 can be
directed into the oil-bearing stratum 16 at that level. Thus, the
casing 34 is suitably perforated in the area 38 to allow passage of
the injection gas in annulus 32 into the upper region of
oil-bearing stratum 16 in the immediate surrounds of well-bore 24.
Any of various dissolving gases may be employed as the injection
material; however, from the standpoint of availability and economy,
it is contemplated that carbon dioxide and/or a mixture of carbon
dioxide and liquid petroleum gas (LPG) may be utilized to form the
dissolving zone in the oil-bearing stratum 16. Where necessary, a
suitable form of packer assembly 40 may be installed between tubing
36 and casing 34 immediately below the perforation area 38. Such a
blocking device or equivalent is generally existant within a
completed well-bore.
The dissolving gas entering through perforation area 38 into the
oil-bearing stratum 16, as shown by arrows 42 near the top of the
producing formation, enters the reservoir and contacts the
under-saturated petroleum products to effect dissolution thereof.
As the amount of gas going into solution increases, the viscosity
of the petroleum will decrease, and such decreased petroleum
viscosity tends to set up a gravity flow head in the area 44 which
migrates downward, as shown generally by arrows 46, to a petroleum
recovery zone 48 at some lower point of well-bore 24.
The action of dissolution in situ tends to create a condition of
increasing volume of lowered viscosity petroleum product per unit
time, such volumetric increase being exponential in nature. That
is, upon introduction of the dissolving gas and initial decrease in
petroleum viscosity, the oil tends to flow by gravity head toward
the recovery zone 48 at continually increasing rate. This
re-exposes additional volume of undersaturated petroleum to the
injected gas so that the process continues. Also, as the injection
gases go into solution, there is a release of heat energy causing a
temperature rise in the oil which, in turn, causes further
reduction in viscosity and increased flow rate.
It is apparent then that an attendant step in the method may
include heating of the dissolving gas prior to injection so that it
will reach the oil-bearing stratum 16 at a temperature which is
appreciably higher than the original formation temperature. This
will cause the gas to heat the formation adjacent to the well bore
24, in the area of perforations 38, to further aid the viscosity
reductions and gravity flow functions.
The flowing petroleum product available at recovery zone 48 may
then be withdrawn up tubing string 36 in conventional manner by
such as an oil pump 50 or other existing pumping equipment, e.g.
hydraulic, pneumatic or electrical submergible pumps.
The above-described recovery method is especially useful when the
oil-bearing stratum 16 is underlain by an active water zone such as
water-bearing stratum 18. The injection gas can be introduced into
the producing well or well-bore 24 at a pressure which is
sufficiently high to maintain the bottom hole pressure essentially
constant at original pressure levels. This then prevents water from
flowing into the recovery zone. In the case where the oil is not
underlain by water, the pressure need only be high enough to give
the desired oil production rate. In either case, the injected
volume of dissolving gas will be dependent upon the injection
pressure, the solubility of the injection gas in the oil, and
whatever the desired oil production rate. Care must be taken that
the injection rate of the dissolving gas is not so high as to cause
a pressure buildup above desired levels at the producing wells.
The injection gas, e.g. a carbon dioxide and/or LPG combination as
previously described, may be obtained from a suitable form of
injection gas generator 52 for conduction via conduit 54 for
injection in annulus 32 of well-bore 24. Recovered petroleum
product from tubing string 36 is conducted via a suitable conduit
56 to a conventional mode of output processing 58. While the oil
entering the lower portion of tubing string 36 is pumped from the
well or tubing string by the pumping unit 50, a back pressure must
be maintained on the tubing string to prevent the oil from flowing
naturally from the well. If the well were allowed to flow, a
pressure differential may be created in the reservoir which could
result in flow of water from the water-bearing stratum 18 upward to
the recovery zone 48 of the well bore 24. After the oil product
reaches the surface, the pressure may be partially reduced for flow
through gathering lines or conduit 56 to output processing 58. Gas
products may be recovered in output processing 58 for recycling in
the method, as will be further described below.
The bore hole 30, generally selected as that bore in the field or
area in communication with the highest point of the oil-bearing
stratum 16, may also be utilized for pressurizing the field. Thus,
nitrogen or any other low value gas from a suitable source or
generator 60 is conducted via line 62 for input under preselected
pressure to the upper terminal of bore hole 30. The bore hole 30 is
perforated by suitable means in the area 64, the upper reaches of
well bearing strata 16, to build up a pressure head as indicated
generally by dash line 66. This pressurizing may be continually
increased in accordance with withdrawal of petroleum product to
maintain a desired quiescent pressure sufficient to hold the
overall reservoir pressure essentially constant.
While the foregoing is directed primarily to the simultaneous
injection and production from a single well-bore 24, it should be
understood that the similar producing activity can be carried out
for each of the additional well-bores 26, 28 and whatever. Thus,
with respect to well-bore 26, the solvent gas from injection gas
generator 52 is applied via conduit 54 to an annulus 68 formed by
casing 70 and tubing string 72. The well-bore 26 is also pre-worked
so that it includes a perforated zone 74 to allow introduction of
the solvent gas to form its gas cap head for gravity flow downward
toward a recovery zone 76. In like manner, well-bore 28 may
constitute similar structure arrayed for parallel production
function. That is, it includes similar annulus 78 between a casing
80 and tubing 82, and it would be pre-worked to have a perforation
zone 84 and lower recovery zone 86.
Various forms of surface support equipment may be employed in
carrying out the present method, and the block diagram of FIG. 2
illustrates a generalized form of such supporting installation. As
shown in FIG. 2, the respective units of output processing 58,
injection gas generator 52, and nitrogen generator 60 are each
shown in dish-line outline with the respective input conduits 56
and output lines 54 and 62 in communication therewith. While
description proceeds with respect to this particular type of
installation, it should be understood that there are various forms
of supporting equipment which may be employed in carrying out the
respective output processing, injection gas generation and other
satellite functions.
The output processing 58 may consist of such as conventional forms
of heater unit 90, a separator 92 and heater-treater 94. An oil and
gas mixture as recovered from an oil production reservoir, e.g.
from well tubings 36, 72 and/or 82, is available in conduit 56 for
input to a heater 90. Heater 90 serves to increase the temperature
of the oil and gas mixture so that a more efficient separation of
the gas and oil will occur in the next following phase. The heater
90 also receives input via conduit 96 of carbon dioxide which is
obtained, for example, from nitrogen generator 60 in a manner as
will be further described below; and also, LPG may be introducted
at input 98 for mixture with the CO.sub.2 as applied in conduit 96
to heater 90.
A heated component of LPG and carbon dioxide is supplied out via
line 102 while the heated oil and gas mixture is applied in line
104 to separator 92. The separator 92 serves to divide as between
the oil or petroleum product and gas components, the gas components
being conducted in line 106 for mixture with the CO.sub.2 -LPG
components in line 102, while the liquid components are present
through line 108 to the heater-treater 94. Depending upon
prevailing pressure conditions, it may be more efficient to employ
two or more separators operating in series, each functioning at a
different, selected pressure.
Upon leaving the separator 92, the degassed liquid in line 108
flows into heater-treater 94 whereupon any free or entrained water
is separated from the oil. The water recovery is then conducted in
line 110 for proper disposal and the petroleum products are
separately conducted for further disposition. That is, any
remaining vapors or volatile end products from the oil product are
conducted through a line 112 for further use in such as nitrogen
generator 60, as will be described, and the liquid product is
conducted in a line 114 for flow to storage or pipe line and
subsequent sales disposition.
Referring again to separator 92, the output of gases in line 106
are combined with any LPG and carbon dioxide gases present in line
102, and the combined gases are supplied to a dehydrator 116 within
the injection gas generator 52. The dehydrator 116 serves to remove
all water vapor to minimize corrosion problems whereupon the
mixture of petroleum solvent gases are applied in a line 118 for
input to a compressor 120. The compressor 120 serves to repressure
the solvent gases, i.e. carbon dioxide and/or LPG mixtures thereof,
so that it will flow through line 54 back to the producing wells
for re-entry into the annulus spaces as previously described. In
some cases, it may be desirable to further heat the injection or
solvent gas prior to re-injection, and this may be carried out by
passing the output from compressor 120 through a suitable heater
122 with further conduction through input conduit 54 to the
selected well sites.
The nitrogen generator 60 may be such as a conventional form of
flue gas plant which not only provides the reservoir pressuring
nitrogen as applied on line 62, but also provides a source of
carbon dioxide as applied in line 96 back to the heater 90 of
output processing 58. Thus, fuel gas such as that available on line
122 from heater-treater 94 is supplied along with air on line 124
as input to a flue gas generator 126. After combustion in the flue
gas generator 126, there is provided an output on line 128 which
includes a mixture of nitrogen and carbon dioxide for application
to a compressor 130 wherein partial repressuring takes place. The
repressured gas mixture then flows through a line 132 for input to
a separation system 134 wherein the nitrogen and carbon dioxide
components are separated into their individual streams. While
various commercial methods of separation are available, a very
economical method consists of the separation system 134 as shown.
The input from line 132 is supplied to an absorber unit 136
utilizing production oil such as might be obtained from output oil
line 114. The resulting oil and dissolved carbon dioxide may then
be routed back through heater 90 and separator 92 for
separation.
Gas output from absorber unit 136 is conducted via line 138 to a
compressor 140. The gas output is a high purity nitrogen gas and it
is then sufficiently repressured in compressor 140 for conduction
via line 62 for input to the bore hole 30 at some selected pressure
to repressure the petroleum reservoir 14. If an absorbtion liquid
other than production oil from output oil line 114 is used, that
absorbtion liquid is supplied to separator 144 through line 142. In
separator 144 the carbon dioxide evolves from the absorbtion liquid
and leaves through line 96. The now lean absorbtion liquid is
pumped back through line 146 to the absorber 136 to again extract
the carbon dioxide from the flue gas.
The foregoing discloses a novel method for effecting secondary
recovery of petroleum products from sub-terranean reservoirs. The
method is particularly adapted to those situations where an
oil-bearing strata is laden with high viscosity oil and, at the
same time, is underlain by a water zone of appreciably more mobile
fluids. The method of the present invention can then enable the
setting up of a gas cap head of reduced viscosity oil which
migrates under gravitational forces to a petroleum recovery zone,
and such migration is affected without allowing the more mobile
water to flow upward into the recovery zone.
Changes may be made in the combination and arrangement of steps as
heretofore set forth in the specification and shown in the
drawings; it being understood that changes may be made in the
embodiment disclosed without departing from the spirit and scope of
the invention.
* * * * *