CA1303974C - Method of producing viscous oil from subterranean formations - Google Patents
Method of producing viscous oil from subterranean formationsInfo
- Publication number
- CA1303974C CA1303974C CA000603313A CA603313A CA1303974C CA 1303974 C CA1303974 C CA 1303974C CA 000603313 A CA000603313 A CA 000603313A CA 603313 A CA603313 A CA 603313A CA 1303974 C CA1303974 C CA 1303974C
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- Canada
- Prior art keywords
- hot water
- flow path
- steam
- well
- pay zone
- Prior art date
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-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
Viscous oil is recovered from a subterranean formation by (a) establishing flow communication between an injection well and a production well in a flow path along the lower portion of a formation pay zone containing the viscous oil, (b) heating the flow path and adjacent portions of the pay zone with hot water or low quality steam, (c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the oil to liquify and drain into the heated flow path and to be displaced toward the production well, (d) displacing substantially all of the oil in the heated path by hot water, and (e) recovering produced fluids through the production well.
The flow path is conveniently created by placing a hori-zontal well from the vertical injection well into the pay zone.
Viscous oil is recovered from a subterranean formation by (a) establishing flow communication between an injection well and a production well in a flow path along the lower portion of a formation pay zone containing the viscous oil, (b) heating the flow path and adjacent portions of the pay zone with hot water or low quality steam, (c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the oil to liquify and drain into the heated flow path and to be displaced toward the production well, (d) displacing substantially all of the oil in the heated path by hot water, and (e) recovering produced fluids through the production well.
The flow path is conveniently created by placing a hori-zontal well from the vertical injection well into the pay zone.
Description
PATENT
Sufi et al.
13~$~t~
s METHOD OF PRODUCING VISCOUS OIL FROM
SUBTERRANEAN FORMATIONS
1. Field of the Invention This invention pertains to a method of producing viscous oil from a formation pay zone penetrated by an injection well and a production well. The method utili~es 15 alternating slugs of steam and hot water through the injection well into the pay zone overlyin~ a heated flow path between the injection and production wellsO
Sufi et al.
13~$~t~
s METHOD OF PRODUCING VISCOUS OIL FROM
SUBTERRANEAN FORMATIONS
1. Field of the Invention This invention pertains to a method of producing viscous oil from a formation pay zone penetrated by an injection well and a production well. The method utili~es 15 alternating slugs of steam and hot water through the injection well into the pay zone overlyin~ a heated flow path between the injection and production wellsO
2. Description of the Prior Art In the annotated manual of "Oil and Gas Terms,"
20 7th Edition, by Howard R. Williams (1987) the term "Terti-ary Recovery" is identified as: Enhanced recovery methods for the production of crude oil or natural gas. Enhanced recovery of crude oil requires a means for displacing oil from the reservoir rock, modifying the properties of the 25 fluids in the reservoir and/or the reservoir rock to cause movement of crude oil in an efficient manner, and provid-ing the energy and drive mechanism to force its flow to a production well. Chemicals or energy are injected as required for displacement and for the control of flow rate ~' ~
...... . . . . .
', ~3~
and flow pattern in the reservoir, and a fluid drive is provided to force the oil toward a production well. Basic methods include thermal methods wherein heat energy is added to the Formation~
Such thermal methods have been investigated extensively as a means for recovering viscous oil from subterranean formations. The viscosity of the oil makes it essentially immobile under formation conditions, and therefore it is essentially unrecoverable by primary and 10 secondary recovery methods. The oil typically has an API
gravity of less than about 20 and a viscosity of up to about 10,000 centipoise (cps) or more. The primary classes of oils meeting this standard are referred to in the industry as "heavy oils," "tar sands" and "bitumen."
15 For example: heavy oil has a viscosity of about 100 to 10,000 cps and an API gravity of 10 to 20 whereas the tar sand oil has a viscosity of 10,000 cps or more and an API
gravity of 10 or less. There are several major formations in North America (and elsewhere) that contain petroleum 20 (oil) which has such physical properties and is too vis-cous to be recovered by ordinary production methods. The viscous oil reserves in Utah, California and Alberta, Canada, is reasonably estimated in the billions of bar-rels. See, for example, USP 4,696,345 (Lo Hsueh, issued 25 September 29, 1987) at column 1, lines 8-14. The economic incentive to recover such reserves is huge.
Many thermal methods have been suggested as a means to recover viscous oil, and some of them have even been successful in producing oil~ Some methods have pro-3~3~
pos~d using slotted liners posi-tioned in the formations as conduits for hot fluids. Others have applied heat to the formation by use of steam or hot water or by underground combustion. Many of these methods were unsuccessful 5 because of the difficulty of forming and maintaining fluid communication between the injection well and the pro duction well. One of the techniques used to address this communication problem has been to drill a horizontal well placed from the injection well into the pay zone and, in 10 some instances, to the production well. Another technique utilizes the horizontal well approach and adds piping that let steam and/or hot water circulate through the piping to warm the adjacent formation. This later technique is illustrated, for example, in USP 3,994,340 ~D. J. Anderson 15 et al. is~ued November 30, 1976) and USP 4,696,345.
Steam flooding is anoth~r thermal method that has been used with varying degrees of success. Steam is considerably lighter than the oil and water present in the formation and thus, because of gravity segregation, it 20 tends to rise to the top of the formation when vertical communication exists. Consequently, the injected steam channels through the top of the formation to the producing well overriding a major portion of the formation and con-tacting only a small fraction of the formatlon oil. Once 25 steam override has begun, continued injection of steam into the formation will accomplish very little additional oil recovery. This behavior results in an inefficient oil recovery and low vertical sweep efficiency. USP 4,607,695 ., . ~
.. ..
D3~
~S. C. Weber, issued August 26, 1986) attempts to address this problem by injecting a mixture of steam, a noncon-densable gas, and a special class of surfactants into the formation to create a "stable foam" which acts as a 5 diverting agent to decrease the permeability of one zone ~i.e., channel) and to divert steam into other portions of the formation. The present invention also addresses sweep efficiency of a steam flood, but with an entirely differ-ent approach.
Another steam flooding technique is described in USP 4,597,443 (W. R. Shu et alO, issued July 1, 198Ç~.
There, a predetermined amount of steam, not greater than l.0 pore volume, is injected into the formation through an injection well at an injection rate of 4 to 7 barrels of 15 steam (cold water equivalent) per day per acre-foot of formation and produced fluids, including oil, are recov-ered through a production well. The steam temperature is within the range of 500 to 700F and it has a quality of S0 to 90 percent. The high steam injection rate was said 20 to be essential in the process to minimize heat loss to surrounding underground strata. The process also requires shutting in the injection well periodically to let the injected steam condense in the formation and let the resulting heat dissipate into the formation to reduce the 25 viscosity of the oil. Then, a predetermined amount of hot water or low quality steam , not greater than l.0 pore volume, is injected into the formation with no inter-ruption of production during the steps. The process in USP 4,597,443 is "related" to the present invention in ~4--`~ ~3~3~7~
that both utilize steam and hot water in the process.
The processes in USP 4,535,845 (A. Brown et al., issued August 20, 1985) and USP 4,037,658 (D. J. Anderson, 5 issued July 26, 1977) are also "related" to the present invention in that both use an injection well and a produc~
ing well in a ste.am flood and the present method can use horizontal wells described in USP 4,535,845 and USP 4,037,658 to create the heated path between the 10 injection and production well~.
Other steam f looding and thermal recovery tech-niques are disclosed in the following nonexhaustive list of U . S . patents : USP 4 , 515 , 215 , C . E. Hermes et al., issued May 7, 1985; USP 4,489,783, W. R. Shu, iesued 15 December 25, 1984; USP 4,466,485, W. R. Shu, issued August 21, 1984; USP 4,465,137, A. J. Sustek et al., i~ued August 14, 1984; USP 4,460,044, L. T. Porter, is#ued July 17, 1984; USP 4,450,911, W. R. Shu et al., i~sued May 29, 1984; USP 4,392,530, A. F. Odeh et al., 20 issued July 12, 1983; USP 4,390,067, B. T. Willman, i~ued June 28, 1983; USP 4,303,126, T. R. Blevins, i~sued Decem-ber 1, 1981; USP 4,020,901, P. Pisio et al., is~ued May 3, 1977; USP 3,994,340; USP 3j847,219, K. H. Wang et al., is~ued November 12j 1974; USP 3,68~,244, R. W. Bowman 25 et al., is~ued August 8, 1972; USP 3,572,437, J. 13. Mar-berry et al., issued March 30, 1971 ; and references cited therein .
_ , . , -- .
. .
~3~
SUMMARY 0~ THE INVENTION
A new method for producing viscous oil from sub-terranean formations has now been discovered. The new method comprises the steps of:
~a) establishing fluid flow communication (a flow channel) between the injection well and the production well in a flow path (channel) along lower portions of a formation pay zone containing said vis-cous oil;
(b) heating the flow path and adjacent por-tions of the pay zone with hot water or low quality steam;
(c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the viscous oil to liquify and drain into the heated flow path and to be displaced toward the production well by hot water, (d) displacing substantially all of the oil in the heated path by hot water; and (e) recovering produced fluids through the production well.
The new method enhances sweep efficiency and utilization of heat units in the injected fluids and it 25 also enhances the recovery of viscous oil.
BRIEF DESCRIPTION OF THE DRAWINGS
Figures l(a~ and l(b) graphically illustrate the theory of the present process. Figure l(a) shows the steam injection cycle in which steam enters the formation, .
:
. .
.
.
~3~
rises and causes the heated, liquified oil to drain into the heated "zone" or "flow path~" Figure l(b) shows the alternating hot water injection cycle in which hot water is used to displace the mobile oil through the heated path 5 toward the production well where the produced fluids (including oil) are withdrawn.
Figures 2 through 5 are production curves based on experiments further detailed below.
DETAILED DESCRIPTION OF THE INVENTION
The novel process can be used to enhance recov-ery from any subterranean formation that contains oil that is too viscous to remove by conventional recovery tech-niques. As noted above such oil is typically referred to as heavy oil, tar sand or bitumen. The formation pay 15 zones containing viscous oil are commonly (sandwiched) located between two relatively impermeable rock formations or "capped" with such an impermeable formation with an underlying formation that is water permeable. In the first instance, a lateral or horizontal well placed from 20 the injection well or drilled separately will be the pre~
ferred means of establishing fluid flow communications and a flow path between an injection well and a spaced apart production well which penetrates the formation pay zone The lateral or horizontal well can also be used when the 25 pay zone has an adjacent underlying water permeable forma-tion, such as most of the tar sand formations. In this later instance, however, a horizontal well is not required to establish fluid communication between the injection and , production wells but it may still be preerred to betker control the heated flow path.
It will be understood that the practice of this invention requires two wells, but may involve others. The 5 injection and production wells may be part of a "spot pat-ternll which has been designed to maximize prod~ction from the field. Thus, the injection well may be used to pro-vide steam/hot water to stimulate the flow of oil which is received in a plurality of producer wells, and vice versa.
lQ Fluid communication between the injection and production wells leads to a flow path that `can be heated.
If the communication link is a horizontal well, cased or uncased, hot water and/or steam on ot~er heated fluid can be circulated through the wells to heat the adjacent for-15 mation. If the horizontal well contains the appropriate piping, the heating medium can be circulated within the well to heat the ormation; e.g., the HASDrive* technique in USP 4,696,345 and USP 3,994,340. If the pay zone has an underlying water permeable zone, then hot water and/or 20 low quality steam can be used to establish the fluid com-munication between wells and the heated flow path by injection of same through the injection well and recover~
ing the condensed/cooled fluids through the production well. The heated medium is injected into and through the 25 flow path for a time sufficient to raise the temperature of the adjacent pay zone and viscous oil to a temperature at least sufficient to liquify the viscous oil and make it mobile in the heated zone. Typically, the temperature of the heated medium is from about 300 to about 500F. The *trademark -8-~'~
., .,.,_.
-'. .
'~ -.,. ~
3~
injection of such heated fluids normally proceeds from about three months to twelve months. And, the temperature of the heat flow path in formation is normally raised to about 150 to about 300F during this step of the present 5 invention.
Once fluid communication is established and the flow path heated, alternating slugs of hot water and steam are injected through the injection well into the lower pay zone. Hot water is injected to establish injectivity and 10 flow paths into the pay zone and to displace mobile oil in the heated flow path. The following slug of steam tends to follow such flow paths into the pay zone, but the injection rate usually falls quickly, at which point hot water is started again until injectivity is reestablished, 15 then steam is iniected, etc. The injection rate or length of time that steam can be injected normally increases with each hot water/steam cycle until steam can be injected at the maximum or optimum rate prescribed by the operator for a particular formation. This, of course, is the ultimate 20 goal because the high injectability rate of steam indi-cates the viscous oil has been swept from the formation.
EXPERIMENTAL
The Steam-Water Alternating Process (SWAP) is shown in Figures la and lb. For a flow path near the base 25 of the formation, injected steam will rise as shown in Figure la. ~he flow path itself can either be a naturally occurring higher water saturation zone or a region heated by circulating steam in an unperforated horizontal well fEom the injector to the producer. As steam, rises, i3~?39~
heated oil will drain into the flow path, limiting the flow capacity. The injection is then converted to hot water which can flow more easily in the reservoir because of the lower specific volume of waker compared to steam.
5 The water then displaces the oil drained into the flow path and re-establishes the zones mobility. The steam-hot water cycles are repeated until a maximum injection rate of steam in~ection is obtained.
This process was tested using a scaled physical 10 steamflood model. The model and associated flow equipment is described in CIM paper No. 88-39~61 titled "Injectivity Enhancement in Tar Sands - A Physical Model Study." This paper was presented at the 39th annual technical meeting o the Petroleum Society of CIM in Calgary, June 12~16, 15 1988. The equipment was modified to include a horizontal well. This was a 1/8th inch stainless steel tube placed in the model from the injector to the producer. Using control valves, flow could be initially directed to this tube to heat the region surrounding it b~ heat conduction.
20 Once a heated zone had been established, steam or hot water could then be directed to the vertical injector.
The irst run consisted of flowing steam through the horizontal well for 80 minutes after which steam injection into the vertical well was attempted. This 25 resulted in a negligible mass injection rate into the model. In run 2, steam was again circulated in the hori-zontal well for 80 minutes after Which the SWAP process was attempted. Figure 2 shows the cold water equivalent 3~t.~
(CWE) injection rates into the model. The scale on the left corresponds to the rates observed in the laboratory.
The scale on the right is the field equivalent scaled rates in barrels per day. As can be seen, during periods 5 of hot water injection, the injection rate built up to the maximum injection rate of the pumps. During the steam injection cycles, the rate fell~ The minimum rate during each steam subseque~t steam cycle however, increased until the maximum rate was achieved during steam injection.
lO Figure 3 shows the oil production during this period. It shows the oil production increasing steadily to a maximum at about 300 minutes.
In run 3, the initial steam circulation time was reduced to 40 minutes after which the SWAP process was 15 initiated. Figure 4 shows the injection rates during the steam and hot water injection cycles. The CWE injection rate increased during hot water injection to the maximum pump output rate. During steam injection, the rates were lower. In this run, the final steam injection rate was 20 lower then the maximum rate. This was a result of the shorter heating time of 40 minutes at the start of the test. The shorter time resulted in a less mobile flow path during the experiment. The oil production from this test is shown in Figure 5. It shows the oil reaching a 25 maximum and then following an established decline till the end of the test~ In this test, 76.4% of the oil-in-place was recoveredO
'
20 7th Edition, by Howard R. Williams (1987) the term "Terti-ary Recovery" is identified as: Enhanced recovery methods for the production of crude oil or natural gas. Enhanced recovery of crude oil requires a means for displacing oil from the reservoir rock, modifying the properties of the 25 fluids in the reservoir and/or the reservoir rock to cause movement of crude oil in an efficient manner, and provid-ing the energy and drive mechanism to force its flow to a production well. Chemicals or energy are injected as required for displacement and for the control of flow rate ~' ~
...... . . . . .
', ~3~
and flow pattern in the reservoir, and a fluid drive is provided to force the oil toward a production well. Basic methods include thermal methods wherein heat energy is added to the Formation~
Such thermal methods have been investigated extensively as a means for recovering viscous oil from subterranean formations. The viscosity of the oil makes it essentially immobile under formation conditions, and therefore it is essentially unrecoverable by primary and 10 secondary recovery methods. The oil typically has an API
gravity of less than about 20 and a viscosity of up to about 10,000 centipoise (cps) or more. The primary classes of oils meeting this standard are referred to in the industry as "heavy oils," "tar sands" and "bitumen."
15 For example: heavy oil has a viscosity of about 100 to 10,000 cps and an API gravity of 10 to 20 whereas the tar sand oil has a viscosity of 10,000 cps or more and an API
gravity of 10 or less. There are several major formations in North America (and elsewhere) that contain petroleum 20 (oil) which has such physical properties and is too vis-cous to be recovered by ordinary production methods. The viscous oil reserves in Utah, California and Alberta, Canada, is reasonably estimated in the billions of bar-rels. See, for example, USP 4,696,345 (Lo Hsueh, issued 25 September 29, 1987) at column 1, lines 8-14. The economic incentive to recover such reserves is huge.
Many thermal methods have been suggested as a means to recover viscous oil, and some of them have even been successful in producing oil~ Some methods have pro-3~3~
pos~d using slotted liners posi-tioned in the formations as conduits for hot fluids. Others have applied heat to the formation by use of steam or hot water or by underground combustion. Many of these methods were unsuccessful 5 because of the difficulty of forming and maintaining fluid communication between the injection well and the pro duction well. One of the techniques used to address this communication problem has been to drill a horizontal well placed from the injection well into the pay zone and, in 10 some instances, to the production well. Another technique utilizes the horizontal well approach and adds piping that let steam and/or hot water circulate through the piping to warm the adjacent formation. This later technique is illustrated, for example, in USP 3,994,340 ~D. J. Anderson 15 et al. is~ued November 30, 1976) and USP 4,696,345.
Steam flooding is anoth~r thermal method that has been used with varying degrees of success. Steam is considerably lighter than the oil and water present in the formation and thus, because of gravity segregation, it 20 tends to rise to the top of the formation when vertical communication exists. Consequently, the injected steam channels through the top of the formation to the producing well overriding a major portion of the formation and con-tacting only a small fraction of the formatlon oil. Once 25 steam override has begun, continued injection of steam into the formation will accomplish very little additional oil recovery. This behavior results in an inefficient oil recovery and low vertical sweep efficiency. USP 4,607,695 ., . ~
.. ..
D3~
~S. C. Weber, issued August 26, 1986) attempts to address this problem by injecting a mixture of steam, a noncon-densable gas, and a special class of surfactants into the formation to create a "stable foam" which acts as a 5 diverting agent to decrease the permeability of one zone ~i.e., channel) and to divert steam into other portions of the formation. The present invention also addresses sweep efficiency of a steam flood, but with an entirely differ-ent approach.
Another steam flooding technique is described in USP 4,597,443 (W. R. Shu et alO, issued July 1, 198Ç~.
There, a predetermined amount of steam, not greater than l.0 pore volume, is injected into the formation through an injection well at an injection rate of 4 to 7 barrels of 15 steam (cold water equivalent) per day per acre-foot of formation and produced fluids, including oil, are recov-ered through a production well. The steam temperature is within the range of 500 to 700F and it has a quality of S0 to 90 percent. The high steam injection rate was said 20 to be essential in the process to minimize heat loss to surrounding underground strata. The process also requires shutting in the injection well periodically to let the injected steam condense in the formation and let the resulting heat dissipate into the formation to reduce the 25 viscosity of the oil. Then, a predetermined amount of hot water or low quality steam , not greater than l.0 pore volume, is injected into the formation with no inter-ruption of production during the steps. The process in USP 4,597,443 is "related" to the present invention in ~4--`~ ~3~3~7~
that both utilize steam and hot water in the process.
The processes in USP 4,535,845 (A. Brown et al., issued August 20, 1985) and USP 4,037,658 (D. J. Anderson, 5 issued July 26, 1977) are also "related" to the present invention in that both use an injection well and a produc~
ing well in a ste.am flood and the present method can use horizontal wells described in USP 4,535,845 and USP 4,037,658 to create the heated path between the 10 injection and production well~.
Other steam f looding and thermal recovery tech-niques are disclosed in the following nonexhaustive list of U . S . patents : USP 4 , 515 , 215 , C . E. Hermes et al., issued May 7, 1985; USP 4,489,783, W. R. Shu, iesued 15 December 25, 1984; USP 4,466,485, W. R. Shu, issued August 21, 1984; USP 4,465,137, A. J. Sustek et al., i~ued August 14, 1984; USP 4,460,044, L. T. Porter, is#ued July 17, 1984; USP 4,450,911, W. R. Shu et al., i~sued May 29, 1984; USP 4,392,530, A. F. Odeh et al., 20 issued July 12, 1983; USP 4,390,067, B. T. Willman, i~ued June 28, 1983; USP 4,303,126, T. R. Blevins, i~sued Decem-ber 1, 1981; USP 4,020,901, P. Pisio et al., is~ued May 3, 1977; USP 3,994,340; USP 3j847,219, K. H. Wang et al., is~ued November 12j 1974; USP 3,68~,244, R. W. Bowman 25 et al., is~ued August 8, 1972; USP 3,572,437, J. 13. Mar-berry et al., issued March 30, 1971 ; and references cited therein .
_ , . , -- .
. .
~3~
SUMMARY 0~ THE INVENTION
A new method for producing viscous oil from sub-terranean formations has now been discovered. The new method comprises the steps of:
~a) establishing fluid flow communication (a flow channel) between the injection well and the production well in a flow path (channel) along lower portions of a formation pay zone containing said vis-cous oil;
(b) heating the flow path and adjacent por-tions of the pay zone with hot water or low quality steam;
(c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the viscous oil to liquify and drain into the heated flow path and to be displaced toward the production well by hot water, (d) displacing substantially all of the oil in the heated path by hot water; and (e) recovering produced fluids through the production well.
The new method enhances sweep efficiency and utilization of heat units in the injected fluids and it 25 also enhances the recovery of viscous oil.
BRIEF DESCRIPTION OF THE DRAWINGS
Figures l(a~ and l(b) graphically illustrate the theory of the present process. Figure l(a) shows the steam injection cycle in which steam enters the formation, .
:
. .
.
.
~3~
rises and causes the heated, liquified oil to drain into the heated "zone" or "flow path~" Figure l(b) shows the alternating hot water injection cycle in which hot water is used to displace the mobile oil through the heated path 5 toward the production well where the produced fluids (including oil) are withdrawn.
Figures 2 through 5 are production curves based on experiments further detailed below.
DETAILED DESCRIPTION OF THE INVENTION
The novel process can be used to enhance recov-ery from any subterranean formation that contains oil that is too viscous to remove by conventional recovery tech-niques. As noted above such oil is typically referred to as heavy oil, tar sand or bitumen. The formation pay 15 zones containing viscous oil are commonly (sandwiched) located between two relatively impermeable rock formations or "capped" with such an impermeable formation with an underlying formation that is water permeable. In the first instance, a lateral or horizontal well placed from 20 the injection well or drilled separately will be the pre~
ferred means of establishing fluid flow communications and a flow path between an injection well and a spaced apart production well which penetrates the formation pay zone The lateral or horizontal well can also be used when the 25 pay zone has an adjacent underlying water permeable forma-tion, such as most of the tar sand formations. In this later instance, however, a horizontal well is not required to establish fluid communication between the injection and , production wells but it may still be preerred to betker control the heated flow path.
It will be understood that the practice of this invention requires two wells, but may involve others. The 5 injection and production wells may be part of a "spot pat-ternll which has been designed to maximize prod~ction from the field. Thus, the injection well may be used to pro-vide steam/hot water to stimulate the flow of oil which is received in a plurality of producer wells, and vice versa.
lQ Fluid communication between the injection and production wells leads to a flow path that `can be heated.
If the communication link is a horizontal well, cased or uncased, hot water and/or steam on ot~er heated fluid can be circulated through the wells to heat the adjacent for-15 mation. If the horizontal well contains the appropriate piping, the heating medium can be circulated within the well to heat the ormation; e.g., the HASDrive* technique in USP 4,696,345 and USP 3,994,340. If the pay zone has an underlying water permeable zone, then hot water and/or 20 low quality steam can be used to establish the fluid com-munication between wells and the heated flow path by injection of same through the injection well and recover~
ing the condensed/cooled fluids through the production well. The heated medium is injected into and through the 25 flow path for a time sufficient to raise the temperature of the adjacent pay zone and viscous oil to a temperature at least sufficient to liquify the viscous oil and make it mobile in the heated zone. Typically, the temperature of the heated medium is from about 300 to about 500F. The *trademark -8-~'~
., .,.,_.
-'. .
'~ -.,. ~
3~
injection of such heated fluids normally proceeds from about three months to twelve months. And, the temperature of the heat flow path in formation is normally raised to about 150 to about 300F during this step of the present 5 invention.
Once fluid communication is established and the flow path heated, alternating slugs of hot water and steam are injected through the injection well into the lower pay zone. Hot water is injected to establish injectivity and 10 flow paths into the pay zone and to displace mobile oil in the heated flow path. The following slug of steam tends to follow such flow paths into the pay zone, but the injection rate usually falls quickly, at which point hot water is started again until injectivity is reestablished, 15 then steam is iniected, etc. The injection rate or length of time that steam can be injected normally increases with each hot water/steam cycle until steam can be injected at the maximum or optimum rate prescribed by the operator for a particular formation. This, of course, is the ultimate 20 goal because the high injectability rate of steam indi-cates the viscous oil has been swept from the formation.
EXPERIMENTAL
The Steam-Water Alternating Process (SWAP) is shown in Figures la and lb. For a flow path near the base 25 of the formation, injected steam will rise as shown in Figure la. ~he flow path itself can either be a naturally occurring higher water saturation zone or a region heated by circulating steam in an unperforated horizontal well fEom the injector to the producer. As steam, rises, i3~?39~
heated oil will drain into the flow path, limiting the flow capacity. The injection is then converted to hot water which can flow more easily in the reservoir because of the lower specific volume of waker compared to steam.
5 The water then displaces the oil drained into the flow path and re-establishes the zones mobility. The steam-hot water cycles are repeated until a maximum injection rate of steam in~ection is obtained.
This process was tested using a scaled physical 10 steamflood model. The model and associated flow equipment is described in CIM paper No. 88-39~61 titled "Injectivity Enhancement in Tar Sands - A Physical Model Study." This paper was presented at the 39th annual technical meeting o the Petroleum Society of CIM in Calgary, June 12~16, 15 1988. The equipment was modified to include a horizontal well. This was a 1/8th inch stainless steel tube placed in the model from the injector to the producer. Using control valves, flow could be initially directed to this tube to heat the region surrounding it b~ heat conduction.
20 Once a heated zone had been established, steam or hot water could then be directed to the vertical injector.
The irst run consisted of flowing steam through the horizontal well for 80 minutes after which steam injection into the vertical well was attempted. This 25 resulted in a negligible mass injection rate into the model. In run 2, steam was again circulated in the hori-zontal well for 80 minutes after Which the SWAP process was attempted. Figure 2 shows the cold water equivalent 3~t.~
(CWE) injection rates into the model. The scale on the left corresponds to the rates observed in the laboratory.
The scale on the right is the field equivalent scaled rates in barrels per day. As can be seen, during periods 5 of hot water injection, the injection rate built up to the maximum injection rate of the pumps. During the steam injection cycles, the rate fell~ The minimum rate during each steam subseque~t steam cycle however, increased until the maximum rate was achieved during steam injection.
lO Figure 3 shows the oil production during this period. It shows the oil production increasing steadily to a maximum at about 300 minutes.
In run 3, the initial steam circulation time was reduced to 40 minutes after which the SWAP process was 15 initiated. Figure 4 shows the injection rates during the steam and hot water injection cycles. The CWE injection rate increased during hot water injection to the maximum pump output rate. During steam injection, the rates were lower. In this run, the final steam injection rate was 20 lower then the maximum rate. This was a result of the shorter heating time of 40 minutes at the start of the test. The shorter time resulted in a less mobile flow path during the experiment. The oil production from this test is shown in Figure 5. It shows the oil reaching a 25 maximum and then following an established decline till the end of the test~ In this test, 76.4% of the oil-in-place was recoveredO
'
Claims (5)
1. A method for producing viscous oil from a subterranean formation penetrated by an injection well and a spaced apart production well, said method comprising the steps of:
(a) establishing fluid flow communication between the injection well and the production well in a flow path along lower portions of a formation pay zone containing said viscous oil;
(b) heating the flow path and adjacent por-tions of the pay zone by injecting hot water or low quality steam into and through the flow path for a time sufficient to liquify the viscous oil in the heated zone and make it mobile and displaceable by injecting hot water or low quality steam into and through the flow path for a time sufficient to liquify the viscous oil in the heated zone and make it mobile and displaceable by hot water;
(c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the viscous oil in the pay zone to liquify and drain into the heated flow path and to be displaced toward the production well by hot water;
(d) subsequent to Step (c), displacing sub-stantially all of the oil in the heated path by hot water; and (e) recovering produced fluids through the production well.
(a) establishing fluid flow communication between the injection well and the production well in a flow path along lower portions of a formation pay zone containing said viscous oil;
(b) heating the flow path and adjacent por-tions of the pay zone by injecting hot water or low quality steam into and through the flow path for a time sufficient to liquify the viscous oil in the heated zone and make it mobile and displaceable by injecting hot water or low quality steam into and through the flow path for a time sufficient to liquify the viscous oil in the heated zone and make it mobile and displaceable by hot water;
(c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the viscous oil in the pay zone to liquify and drain into the heated flow path and to be displaced toward the production well by hot water;
(d) subsequent to Step (c), displacing sub-stantially all of the oil in the heated path by hot water; and (e) recovering produced fluids through the production well.
2. The method defined by Claim 1 wherein said flow path is established, at least in part, by a lateral or horizontal well placed into the pay zone.
3. The method defined by Claim 2 wherein said flow path is established, at least in part, by a lateral or horizontal well placed from the vertical injection well into the pay zone.
4. The method defined by Claim 1 wherein hot water is used to heat the flow path and adjacent portions of the pay zone in step (b).
5. A method for producing viscous oil from a subterranean formation penetrated by an injection well and a spaced apart production well, said method comprising the steps of:
(a) establishing fluid flow communication between the injection well and the production well in a flow path along lower portions of a formation pay zone containing said viscous oil;
(b) heating the flow path and adjacent por-tions of the pay zone by injecting hot water or low quality steam into and through the flow path for a time sufficient to liquify the viscous oil in the heated zone and make it mobile and displaceable by hot water;
(c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the viscous oil in the pay zone to liquify and drain into the heated flow path and to be displaced toward the production well by hot water; in this step (c), hot water is first injected to establish injectivity and flow channels into the pay zone, and steam is then injected until the injection rate begins to fall, at which point hot water is injected again until injectivity is reestablished, then a following slug of steam is injected until the injection rate begins to fall, and this alternating cycle of hot water/steam injection is continued until the maximum or optimum rate of steam injection prescribed by the operator for the particular formation being treated is achieved;
(d) subsequent to Step (c), displacing sub-stantially all of the oil in the heated path by hot water; and (e) recovering produced fluids through the production well.
(a) establishing fluid flow communication between the injection well and the production well in a flow path along lower portions of a formation pay zone containing said viscous oil;
(b) heating the flow path and adjacent por-tions of the pay zone by injecting hot water or low quality steam into and through the flow path for a time sufficient to liquify the viscous oil in the heated zone and make it mobile and displaceable by hot water;
(c) injecting alternating slugs of hot water and steam through the injection well and into the pay zone overlying the heated flow path to cause the viscous oil in the pay zone to liquify and drain into the heated flow path and to be displaced toward the production well by hot water; in this step (c), hot water is first injected to establish injectivity and flow channels into the pay zone, and steam is then injected until the injection rate begins to fall, at which point hot water is injected again until injectivity is reestablished, then a following slug of steam is injected until the injection rate begins to fall, and this alternating cycle of hot water/steam injection is continued until the maximum or optimum rate of steam injection prescribed by the operator for the particular formation being treated is achieved;
(d) subsequent to Step (c), displacing sub-stantially all of the oil in the heated path by hot water; and (e) recovering produced fluids through the production well.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/246,223 US4874043A (en) | 1988-09-19 | 1988-09-19 | Method of producing viscous oil from subterranean formations |
| US246,223 | 1988-09-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1303974C true CA1303974C (en) | 1992-06-23 |
Family
ID=22929799
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000603313A Expired - Lifetime CA1303974C (en) | 1988-09-19 | 1989-06-20 | Method of producing viscous oil from subterranean formations |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US4874043A (en) |
| CA (1) | CA1303974C (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7073577B2 (en) * | 2003-08-29 | 2006-07-11 | Applied Geotech, Inc. | Array of wells with connected permeable zones for hydrocarbon recovery |
| US7809538B2 (en) | 2006-01-13 | 2010-10-05 | Halliburton Energy Services, Inc. | Real time monitoring and control of thermal recovery operations for heavy oil reservoirs |
| US7770643B2 (en) | 2006-10-10 | 2010-08-10 | Halliburton Energy Services, Inc. | Hydrocarbon recovery using fluids |
| US7832482B2 (en) | 2006-10-10 | 2010-11-16 | Halliburton Energy Services, Inc. | Producing resources using steam injection |
| US9051508B2 (en) * | 2007-10-16 | 2015-06-09 | Halliburton Energy Services, Inc. | Methods of preventing emulsification of crude oil in well bore treatment fluids |
| US10385666B2 (en) * | 2014-01-13 | 2019-08-20 | Conocophillips Company | Oil recovery with fishbone wells and steam |
| CA2972203C (en) | 2017-06-29 | 2018-07-17 | Exxonmobil Upstream Research Company | Chasing solvent for enhanced recovery processes |
| CA2974712C (en) | 2017-07-27 | 2018-09-25 | Imperial Oil Resources Limited | Enhanced methods for recovering viscous hydrocarbons from a subterranean formation as a follow-up to thermal recovery processes |
| CA2978157C (en) | 2017-08-31 | 2018-10-16 | Exxonmobil Upstream Research Company | Thermal recovery methods for recovering viscous hydrocarbons from a subterranean formation |
| CA2983541C (en) | 2017-10-24 | 2019-01-22 | Exxonmobil Upstream Research Company | Systems and methods for dynamic liquid level monitoring and control |
| RU2669950C1 (en) * | 2017-12-28 | 2018-10-17 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Тюменский индустриальный университет" (ТИУ) | Method for development of high-viscosity oil deposit |
| RU2696740C1 (en) | 2018-09-21 | 2019-08-05 | Общество С Ограниченной Ответственностью "Илмасоник-Наука" | Method and device of complex action for heavy oil and bitumen production by means of wave technology |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3375870A (en) * | 1965-11-19 | 1968-04-02 | Pan American Petroleum Corp | Recovery of petroleum by thermal methods |
| US3439742A (en) * | 1966-01-17 | 1969-04-22 | Shell Oil Co | Method of producing hydrocarbons from an underground formation |
| NL154577B (en) * | 1967-11-15 | 1977-09-15 | Shell Int Research | PROCEDURE FOR THE WINNING OF HYDROCARBONS FROM A PERMEABLE UNDERGROUND FORMATION. |
| US3477510A (en) * | 1968-02-01 | 1969-11-11 | Exxon Production Research Co | Alternate steam-cold water injection for the recovery of viscous crude |
| US3847219A (en) * | 1973-10-03 | 1974-11-12 | Shell Canada Ltd | Producing oil from tar sand |
| US3994340A (en) * | 1975-10-30 | 1976-11-30 | Chevron Research Company | Method of recovering viscous petroleum from tar sand |
| US4249604A (en) * | 1979-05-23 | 1981-02-10 | Texaco Inc. | Recovery method for high viscosity petroleum |
| US4303126A (en) * | 1980-02-27 | 1981-12-01 | Chevron Research Company | Arrangement of wells for producing subsurface viscous petroleum |
| US4465137A (en) * | 1982-06-25 | 1984-08-14 | Texaco Inc. | Varying temperature oil recovery method |
| US4466485A (en) * | 1982-12-07 | 1984-08-21 | Mobil Oil Corporation | Viscous oil recovery method |
| US4696345A (en) * | 1986-08-21 | 1987-09-29 | Chevron Research Company | Hasdrive with multiple offset producers |
-
1988
- 1988-09-19 US US07/246,223 patent/US4874043A/en not_active Expired - Lifetime
-
1989
- 1989-06-20 CA CA000603313A patent/CA1303974C/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| US4874043A (en) | 1989-10-17 |
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