U.S. patent number 3,680,633 [Application Number 05/101,888] was granted by the patent office on 1972-08-01 for situ combustion initiation process.
This patent grant is currently assigned to Sun Oil Company (Delaware). Invention is credited to John D. Bennett.
United States Patent |
3,680,633 |
Bennett |
August 1, 1972 |
SITU COMBUSTION INITIATION PROCESS
Abstract
The initiation of in situ combustion in formations penetrated by
a wellbore is accomplished by extracting a portion of the air
stream being injected into the formation, removing oxygen from the
extracted air portion, and adding the oxygen to the air stream
being injected into the formation.
Inventors: |
Bennett; John D. (Denton,
TX) |
Assignee: |
Sun Oil Company (Delaware)
(Dallas, TX)
|
Family
ID: |
22286990 |
Appl.
No.: |
05/101,888 |
Filed: |
December 28, 1970 |
Current U.S.
Class: |
166/256;
166/90.1 |
Current CPC
Class: |
E21B
43/243 (20130101) |
Current International
Class: |
E21B
43/243 (20060101); E21B 43/16 (20060101); E21b
043/24 (); E21b 033/03 () |
Field of
Search: |
;166/75,256,260,257 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Leppink; James A.
Claims
What is claimed is:
1. In an in situ combustion process wherein air is supplied to a
formation being ignited, the improvement comprising: separating a
portion of the air stream being supplied to the formation; removing
the oxygen from the separated air stream; and injecting the oxygen
removed from the separated air stream into the air stream being
supplied to the formation.
2. The process of claim 1 wherein the oxygen is removed from the
separated air stream by successive stages of compression and
expansion of the air until the air is liquefied, and then boiling
off the nitrogen component of the air.
3. The process of claim 2 including cooling the separated portion
of the air stream by heat exchanging such separated air portion
with the nitrogen boiled from the liquefied air.
4. The process of claim 1 including supplying heat to the formation
being ignited.
5. In an in situ combustion initiation process where compressed air
is supplied to the formation being ignited, the improvement
comprising: separating a portion of the compressed air being
supplied to the formation; removing the oxygen from the separated
air portion; and injecting the oxygen removed from the separated
air portion into the air stream being supplied to the
formation.
6. The process of claim 5 wherein the oxygen is removed from the
separated air portion by liquefying the air portion and boiling off
the nitrogen component of the air.
7. The process of claim 5 wherein the expansive power of the
compressed air portion is used to supply energy for the machinery
to liquefy the air portion.
8. The process of claim 6 wherein the nitrogen boiled from the
liquefied air is used to cool the separated air portion prior to
liquefaction.
9. Apparatus for initiating in situ combustion in an earth
formation penetrated by a wellbore compris gas conduit means
connected to the wellbore for passing air into the wellbore and
into the formation; means attached to the condui means for
extracting a portion of the air stream from the gas conduit means;
air liquefaction means connected with the extracti means; means for
boiling nitrogen from the liquid air which is in communication with
the air liquefaction means; and means in communication with the air
liquefaction means and attached to the conduit means for injecting
into the gas conduit means the oxygen portion remaining after
boiling the nitrogen from the air.
10. The apparatus of claim 9 including means positioned in the
wellbore for heating the oxygen enriched air entering the
formation.
11. The apparatus of claim 9 including heat exchanger means
adjacent the air stream portion extraction means, and connected
with the nitrogen boiling means.
Description
BACKGROUND OF THE INVENTION
This invention relates to a method for initiating in situ
combustion. In situ combustion is a process which involves burning
hydrocarbon fluids contained in a formation. This process is
employed for several purposes. The primary purpose of in situ
combustion is to stimulate the recovery of hydrocarbon fluids.
Another purpose of in situ combustion is to consolidate the
formation adjacent the wellbore so that particles of the formation
do not clog the well or damage well equipment.
Ordinarily in situ combustion involves several steps. Usually air
is injected into the formation through an injection well. The
injection pressure is maintained at a level to cause air to flow
through the formation from the injection well to one or more
producing wells, and it is injected at a sufficient rate to support
a combustion reaction of a fraction of the oil in the formation. In
order to initiate the combustion reaction in most oil bearing
formations, it is necessary to inject heat along with the air. The
heat is carried by the air into the reservoir, where it contacts
the formation fluids. By flowing a sufficient volume of hot air
into the reservoir, the crude oil in the vicinity of the injection
well is heated to its ignition temperature and commences to burn.
As the flame front of the ignited formation fluids moves away from
the injection well, the heat and pressure created aids movement of
unburned hydrocarbon fluids to production wells. The process just
described is the most common process of reservoir stimulation by in
situ combustion.
In a process of sand consolidation, the in situ combustion process
usually operates quite differently. In such a process, air is
usually injected in wells adjacent the well having a sand
consolidation problem, and heat is provided in the well having such
a problem. Upon achieving the ignition of formation fluids, the
flame front will move outwardly from the wellbore having the sand
consolidation problem toward the source of air injected in the
adjacent wells. This burning of reservoir fluids is continued until
the area to be consolidated has been traversed. This process is
ordinarily termed a "reverse burn" in situ combustion process. A
characteristic of such a reverse burn is that a residue of coke is
left on the particles making up the formation. This coke residue
effectively bonds together the elements of the formation, thereby
eliminating the deficiency in formation consolidation.
The most common methods of initiating in situ combustion in the
formation is to apply heat by using downhole heaters. These heaters
usually consist of downhole electrical heaters, gas burners, and
catalytic reactors. Even with a high injection rate of a heated gas
in the formation, several days are often necessary before
combustion is initiated. Several days are needed in order to supply
a sufficient amount of heat to initiate an oxygen-hydrocarbon burn
in the formation. Because of the substantial cost of wellbore
heating services, it is desirable to initiate in situ combustion as
quickly as possible. Another reason for the lengthy time required
for initiating the in situ combustion relates to a temperature
limitation. In order to prevent well damage due to excessive heat,
heater temperatures should be maintained below approximately
800.degree. F. It is therefore an object of the present invention
to provide an improved method of initiating in situ combustion.
SUMMARY OF THE INVENTION
With these and other objects in view, the present invention
includes injecting air into the formation, which together with
hydrocarbon fluids contained in the formation comprises a fuel
mixture. Oxygen is added to the air stream being injected into the
formation to make a more combustible fuel mixture. This oxygen is
supplied by extracting a portion of the air being supplied to the
wellbore, liquefying such air, vaporizing the nitrogen, and
subsequently injecting the remaining oxygen into the air stream
entering the formation.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a cross section of a wellbore with a heater contained
therein and a schematic illustration of an oxygen enriching system
connected therewith.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to the FIGURE, a wellbore 10 is shown penetrating a
formation 50. The wellbore 10 comprises casing 40 extending from
the surface 54 through the formation 50. Located within casing 40
and extending from the surface to a point adjacent and above the
formation 50 is tubing 42. At the lower end of tubing 42 is seating
nipple 46 which is an annular flange for seating wellbore tools.
Suspended in tubing 42 by line 52 is heater 48. Line 52 may be an
armored electrical cable if the heater 48 is electrical or an
armored thermocouple cable if the heater is catalytic, or a
combination of the two. Heater 48 is suspended in the tubing by
resting on seating nipple 46.
Wellhead 44 atop wellbore 10 has an air line 66 connected thereto
through valve 38. Air compressor 14 having air inlet 12 is
connected with air line 66 for providing air to the wellbore
through the annular space between casing 40 and tubing 42. An air
tap 16 located in air line 66 allows a portion of air leaving air
compressor 14 to enter heat exchanger 18. The heat exchanger 18 may
consist of two helical conduit coils 56 and 58, immersed in a heat
transfer fluid occupying the chamber housing the helical coils 56
and 58. Located in series with heat exchanger 18 by line 19 is
expansion valve 20. The expansion valve 20 comprises a valve which
allows for quick expansion of a gas flowed through the valve.
Connected with expansion valve 20 by line 21 is liquefier 22.
Liquefier 22 may comprise a series of compressors and expansion
valves located in area 24 of such liquefier 22.
Liquids removal tap 32 is located on the lower side of liquefier
22, and may be float controlled. In such a system, a float may be
connected to a gravity seated valve so that as the liquid level
rises, it raises the float and connected valve to drain certain
liquids from the liquefier 22. The liquefier may be one of the well
known types such as the Hampson-Linde Regenerative Process or the
Claude System of liquefying air both of which are described on
Pages 4-58, 59, of MARK'S MECHANICAL ENGINEERS HANDBOOK, Sixth
Edition. Both of these liquefaction processes utilize successive
steps of compression and expansion.
Area 26 of liquefier 22 contains a gas port 28 located on its upper
side for removal of gaseous material. Such gas port is a one way
pressure operated valve. Located on the lower end of area 26 is
liquid tap 30. Such liquid tap 30 may also be float valve operated
in the same manner as liquid removal tap 32. The gas port 28 is
connected to helical coil 56 of heat exchanger 18 by line 29.
Helical coil 56 extends through the heat exchanger 18 and connects
with exit port 34. Liquid tap 30 which also may be float valve
operated as are liquids removal tap 32 and liquid tap 30 is located
at the lower end of liquefier section 26 and connects with gasifier
60 through line 31. Gasifier 60 comprises a chamber which is
constructed to provide for a controlled elevation in temperature.
It may be a heavily insulated chamber having a liquid circulating
therein in enclosed pipes whose temperature may be accurately
controlled by an air conditioning system. Heat for such a system
may be derived from the compressor or cold may be derived from
gases being vaporized in area 26.
In the operation of the apparatus previously described, air is
extracted from the atmosphere through air inlet 12 whereupon it is
compressed in air compressor 14. The air exiting air compressor 14
flows through air line 66 which connects with wellhead 44. A
substantial portion of the air stream leaving air compressor 14
flows through air tap 16. Such flow is caused by a lower pressure
in the initial portion of the system connected with air tap 16. A
sufficient amount of air is extracted at air tap 16 so that a
portion of the compressed air can be utilized to operate the air
liquefaction equipment located downstream from air tap 16. This
extracted air portion then flows through the heat exchanger 18,
where the air is cooled by a cold nitrogen stream coming from
liquefier 22 through line 29. After the air leaves heat exchanger
18 through line 19 by the force supplied by compressor 14, it
passes through expansion valve 20 where the air is quickly expanded
in order to further reduce its temperature.
The air which is now cold enters liquefier 22 where in area 24 it
is subjected to the successive steps of compressing, cooling, and
expansion until the air is liquefied. The liquefier 22 is operated
by utilizing the expansive powers of the extracted air portion. The
compressed air is allowed to expand to drive pistons which supply
energy for operation of the compressor in liquefier 22. During
liquefaction of the air, water vapor and carbon dioxide are the
first to liquefy. They may be separated from the liquefier through
the float operated valve of liquids removal tap 32. The water vapor
and carbon dioxide may also be allowed to solidify before
separation.
The liquefied air is then pumped to area 26 of liquefier 22,
whereupon its temperature is raised above the boiling point of
nitrogen, but is kept below the boiling point of oxygen. The
nitrogen boils from the liquid air in area 26 and exits through gas
port 28. The gasified nitrogen under its own pressure then passes
through line 29 to heat exchanger 18. In the heat exchanger, the
cold nitrogen is used to cool the air passing through the heat
exchanger which has been extracted from line 66. The nitrogen in
passing through helical coil 56 cools the heat transfer fluid which
surrounds coils 56 and 58, and such fluid in turn cools the air in
helical coil 58. The nitrogen is then exhausted through port 34 to
the atmosphere.
The liquid oxygen remaining after the nitrogen has been boiled off,
is removed by gravity from liquid tap 30 which is a float operated
valve located on the underside of area 26 of the liquefier 22. This
liquid stream of oxygen then enters gasifier 60 through line 31.
The gasifier allows controlled temperature elevation to permit the
temperature to exceed the boiling point of oxygen. As the oxygen is
boiled from the liquid in gasifier 60, it is removed through
overhead outlet 33, and proceeds through valve 68 into line 66
through oxygen inlet port 36, where it joins the main air stream
entering wellbore 10.
This oxygen enriched air stream is then pumped down the annulus
between casing 40 and tubing 42, whereupon it flows past heater 48
and enters formation 50 through perforations 49 in casing 40. Upon
entering the formation, the oxygen enriched air starts to oxidize
hydrocarbon fluids contained in the formation 50. Once sufficient
oxidation has occurred, the formation fluids will commence to burn
and the burning front will move away from the wellbore 10. When gas
analysis from adjacent wells indicate that in situ combustion has
commenced, oxygen enrichment of the air stream entering wellbore 10
may be terminated, so that the full capacity of the air compressor
14 can be utilized to provide sufficient air to support the in situ
combustion.
The downhole heater 48 is not always essential in this process of
initiating in situ combustion. Some reservoirs will ignite using an
oxygen enriched air stream which has not been heated. Other
reservoirs may require that such oxygen enriched stream be heated
before in situ combustion will commence. Heaters which may be
employed can be of any conventional type, i.e., downhole gas
burners or electrical and catalytic heaters.
An advantage of the method of supplying oxygen to the formation
described herein is the availability of excess compressor capacity
for use in providing energy for the liquefaction of the air. A
large compressor is required to supply air to support a flame front
when the front covers a large area because of its distance from the
wellbore. Accordingly, since only a small amount of air is needed
for initiation of in situ combustion adjacent the wellbore, there
is excess compressor capacity available for other purposes. The
above described process makes use of this capacity by using it to
provide energy for liquefaction of air. It is not essential to the
operation of this process to have a pure oxygen stream being
injected into the air line 66. This lack of a purity requirement
will result in a savings in equipment and operational costs.
While particular embodiments of the present invention have been
shown and described, it is apparent that changes and modifications
may be made without departing from this invention in its broader
aspects, and therefore, the aim in the appended claims is to cover
all such changes and modifications as fall within the true spirit
and scope of this invention.
* * * * *