CA2875687A1 - Use of electrical heating elements for sagd start-up - Google Patents
Use of electrical heating elements for sagd start-up Download PDFInfo
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- CA2875687A1 CA2875687A1 CA2875687A CA2875687A CA2875687A1 CA 2875687 A1 CA2875687 A1 CA 2875687A1 CA 2875687 A CA2875687 A CA 2875687A CA 2875687 A CA2875687 A CA 2875687A CA 2875687 A1 CA2875687 A1 CA 2875687A1
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- 238000010438 heat treatment Methods 0.000 title claims abstract description 114
- 238000010796 Steam-assisted gravity drainage Methods 0.000 claims abstract description 48
- 238000004891 communication Methods 0.000 claims abstract description 22
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- 239000010426 asphalt Substances 0.000 claims abstract description 17
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- 239000000654 additive Substances 0.000 claims description 4
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- 238000002347 injection Methods 0.000 abstract description 5
- 239000007924 injection Substances 0.000 abstract description 5
- 229930195733 hydrocarbon Natural products 0.000 abstract description 4
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- XQCFHQBGMWUEMY-ZPUQHVIOSA-N Nitrovin Chemical compound C=1C=C([N+]([O-])=O)OC=1\C=C\C(=NNC(=N)N)\C=C\C1=CC=C([N+]([O-])=O)O1 XQCFHQBGMWUEMY-ZPUQHVIOSA-N 0.000 description 10
- 239000003921 oil Substances 0.000 description 10
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Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK 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
- E21B43/2406—Steam assisted gravity drainage [SAGD]
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/04—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using electrical heaters
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B47/00—Survey of boreholes or wells
- E21B47/06—Measuring temperature or pressure
- E21B47/07—Temperature
Landscapes
- 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)
- Geophysics (AREA)
- Resistance Heating (AREA)
Abstract
A SAGD operation is provided, comprising: drilling a SAGD well pair in a bitumen bearing formation, the well pair comprising an injector well and a producer well; introducing an electro-thermal heating element comprising at least one individually controllable heating section in or near either the injector well, the producer well, or both; positioning the at least one individually controllable heating section at or near a sector of either the injector well, the producer well, or both, which sector may require greater thermal heat to establish thermal communication between the injector well and the producer well; and operating the at least one individually controllable heating section at a desired temperature for a period of time sufficient to establish thermal communication between the injector well and the producer well. The electro-thermal heating element having the at least one electrical heating section may remain in the injection well beyond start-up to assist in effectively recovering the hydrocarbons.
Description
USE OF ELECTRICAL HEATING ELEMENTS FOR SAGD START-UP
FIELD OF THE INVENTION
The present invention is directed to Steam Assisted Gravity Drainage (SAGD) in general, and, more particularly, to the use of electrical heating elements to both reduce the start-up time of a SAGD operation and control the amount of heat (thermal energy) used in start-up based on the particular characteristics of a SAGD reservoir. The electrical heating elements may be retained in the injection well after start-up is complete and during normal SAGD operations.
BACKGROUND OF THE INVENTION
Alberta, Canada has some of the world's largest deposits of oils sands. Oil sands are a mixture of sand, water and bitumen, a type of heavy oil that is very thick and thus difficult to flow on its own. Bitumen can be extracted from oil sand by mining oil sands and extracting the bitumen with either hot water or solvents. However, over 80% of oil sands deposits in reservoirs contain oil that is deeper than 75 meters below the earth's surface, making it very difficult to mine.
Thus, a number of in situ methods for extracting bitumen from oil sands have been developed. One of these methods, Steam Assisted Gravity Drainage (SAGD) has proven to be very reliable. Generally, SAGD involves drilling two horizontal, parallel wells (well pairs), a top injector well for injecting steam for reducing the viscosity of the bitumen and a bottom producer well to collect the reduced viscosity bitumen which is lifted to the surface.
Start-up generally involves a pre-heating stage, wherein steam is injected into the injector well, or circulated through both the injector well and the producer well, with the aim of establishing thermal communication between the well pair.
However, the pre-heating stage can take several months before thermal communication is established between the well pair and the production of bitumen can begin.
Thus, there is a need in the industry for a method to reduce the pre-heating time necessary to establish thermal communication between the SAGD well pair.
WSI ega1\00803\00037\11172610v1 Furthermore, there may be some instances where there exists permeability barriers in sections of the formation surrounding either the injector well, the producer well, or both.
Establishing a desireable thermal communication profile between the well pair may be difficult due to the presence of these permeability barriers. In these instances, the pre-heating time may be even greater, as it will take more energy (steam) and time to establish the micro-channels in these permeability barriers which are necessary for fluid to flow during the steam injection and production processes. Thus, there is a need in the industry for a method to also be able to control the amount of heat (thermal energy) used in given areas of the wells in order to also conserve on the energy used during pre-heating of a SAGD well pair.
SUMMARY OF THE INVENTION
The current application is directed to a method for decreasing the start-up time for a SAGD well pair, with the added flexibility of being able to control the amount of heat (thermal energy) used in start-up by controlling the amount of heat used to heat up a given area of the SAGD wells in order to conserve on the energy. It was discovered that by conducting the method of the present invention, one or more of the following benefits may be realized:
(1) Less time is needed to establish initial thermal communication between a pair of SAGD
wells.
FIELD OF THE INVENTION
The present invention is directed to Steam Assisted Gravity Drainage (SAGD) in general, and, more particularly, to the use of electrical heating elements to both reduce the start-up time of a SAGD operation and control the amount of heat (thermal energy) used in start-up based on the particular characteristics of a SAGD reservoir. The electrical heating elements may be retained in the injection well after start-up is complete and during normal SAGD operations.
BACKGROUND OF THE INVENTION
Alberta, Canada has some of the world's largest deposits of oils sands. Oil sands are a mixture of sand, water and bitumen, a type of heavy oil that is very thick and thus difficult to flow on its own. Bitumen can be extracted from oil sand by mining oil sands and extracting the bitumen with either hot water or solvents. However, over 80% of oil sands deposits in reservoirs contain oil that is deeper than 75 meters below the earth's surface, making it very difficult to mine.
Thus, a number of in situ methods for extracting bitumen from oil sands have been developed. One of these methods, Steam Assisted Gravity Drainage (SAGD) has proven to be very reliable. Generally, SAGD involves drilling two horizontal, parallel wells (well pairs), a top injector well for injecting steam for reducing the viscosity of the bitumen and a bottom producer well to collect the reduced viscosity bitumen which is lifted to the surface.
Start-up generally involves a pre-heating stage, wherein steam is injected into the injector well, or circulated through both the injector well and the producer well, with the aim of establishing thermal communication between the well pair.
However, the pre-heating stage can take several months before thermal communication is established between the well pair and the production of bitumen can begin.
Thus, there is a need in the industry for a method to reduce the pre-heating time necessary to establish thermal communication between the SAGD well pair.
WSI ega1\00803\00037\11172610v1 Furthermore, there may be some instances where there exists permeability barriers in sections of the formation surrounding either the injector well, the producer well, or both.
Establishing a desireable thermal communication profile between the well pair may be difficult due to the presence of these permeability barriers. In these instances, the pre-heating time may be even greater, as it will take more energy (steam) and time to establish the micro-channels in these permeability barriers which are necessary for fluid to flow during the steam injection and production processes. Thus, there is a need in the industry for a method to also be able to control the amount of heat (thermal energy) used in given areas of the wells in order to also conserve on the energy used during pre-heating of a SAGD well pair.
SUMMARY OF THE INVENTION
The current application is directed to a method for decreasing the start-up time for a SAGD well pair, with the added flexibility of being able to control the amount of heat (thermal energy) used in start-up by controlling the amount of heat used to heat up a given area of the SAGD wells in order to conserve on the energy. It was discovered that by conducting the method of the present invention, one or more of the following benefits may be realized:
(1) Less time is needed to establish initial thermal communication between a pair of SAGD
wells.
(2) Less energy in the form of steam is required to establish initial thermal communication between a pair of SAGD wells.
(3) The pre-heating process could be accompanied by fluid injection for enhancing the heat transfer efficiency.
(4) The material of the electro-thermal heating element used in the present invention may be selected for proper heat-capacity and thermal conductivity so that increasing and decreasing temperature (heating and cooling processes) occurs in a timely manner as required.
(5) The electro-thermal heating element can comprise one or more individually controllable heating sections which sections can be placed in either the injector well, producer well, or WSlega1\046803\00037\11172610\1 2 both, at sectors of the well where it is difficult for the steam to reach, e.g., a permeability barrier or localized water pocket.
(6) The electro-thermal heating element can comprise one or more individually controllable heating sections which sections can be placed in either the injector well, producer well, or both, to preferentially heat the higher bitumen-saturation zones and to preferentially avoid heating the lower bitumen-saturated zones.
(7) The electro-thermal heating element can comprise a plurality of individually controllable heating sections, whereby the temperature of each section can be separately controlled and may be switched on/off so that a desired pre-heating temperature profile in the reservoir can be achieved.
(8) The present invention can be used together with a solvent, a surfactant or other additive which changes the wettability or reduces the viscosity of the bitumen present in the oil sand reservoir.
Thus, in one aspect, a method for pre-heating a SAGD operation is provided, comprising:
= drilling a SAGD well pair in a bitumen bearing formation, the well pair comprising an injector well and a producer well;
= introducing an electro-thermal heating element having at least one individually controllable heating section in or near either the injector well, the producer well, or both;
= positioning the at least one individually controllable heating section at or near a sector of either the injector well, the producer well, or both, which sector may require greater thermal heat to establish thermal communication between the injector well and the producer well; and = operating the at least one individually controllable heating section at a desired temperature for a period of time sufficient to establish thermal communication between the injector well and the producer well.
WSLegaI\046803\00037\1l 726lO\'I 3 It is understood that proper casing and well-completion is adopted to accommodate the high temperature source of the present invention. In one embodiment, the at least one individually controllable heating section is positioned at the toe of the injector well, the producer well, or both. In another embodiment, the at least one individually controllable heating section is positioned at or near the middle of the injector well, the producer well, or both. In one embodiment, steam is also circulated through the injector well, the producer well, or both.
Following the pre-heating stage, the electro-thermal heating element that is placed in or near the injector well may be left down hole. Thus, when the steam injection into the injector well commences during the steam assisted gravity drainage process, the electro-thermal heating element can assist in controlling the quality of steam in the injector well.
For example, steam often condenses at the toe of the well. Thus, the electro-thermal heating element may comprise an individually controllable heating section that is positioned at the toe of the well. It is understood, however, that, in most instances, it is generally undesirable to leave an electro-thermal heating element in the producer well and, hence, the element should be removed prior to commencing the SAGD process. Thus, it is understood that in one embodiment, the electro-thermal heating elements are removable.
In one embodiment, the electro-thermal heating element comprises a plurality of individually controllable heating sections so that more heat can be provided to one or more specific sections of either the injector well, the producer well, or both, for example, those sections having poor permeability issues or other undesirable reservoir conditions, than other sections of either the injector well, the producer well, or both. In one embodiment, the electro-thermal heating element can be wrapped around the outside of the injector tubing, or liner, of the injector well, the producer tubing of the producer well, or both. Thus, depending on theimal properties of the formation, i.e., heat capacity, thermal conductivity, thermal expansion, and coefficient, an electro-thermal heating element comprising individually controllable heating sections of varying temperatures may be deployed along the injection well, the production well or both to achieve the desired (e.g., uniform) thermal pattern.
In one embodiment, the electro-thermal heating elements can be controlled from surface of the SAGD and each individually controllable heating section can be separately controlled by WSLegah 046803 \00037 \ 111726 I 0 \ 4 controlling or adjusting the current passing through the element and to the individual controllable heating section. In one embodiment, each individually controllable heating section of the electro-thermal heating element has its own thermocouple, DTS sensor, or similar, for measuring the temperature and adjusting the temperature of each section accordingly.
It is further contemplated to use this technique for infihl wells between the SAGD well pairs. The invention will allow for the faster communication of the infill well to steam chambers so that production of the infill well can begin sooner than would be possible without this technique.
In one embodiment, a solvent, a surfactant or other additive which changes the wettability or reduces the viscosity of bitumen is added to either the injector well, the producer well, or both, either prior to or during pre-heating. By being able to control the temperature of individual sectors of a well, one can also control how much solvent or other wettability additive will diffuse into the formation at a particular sector. Useful solvents can be hydrocarbon solvents such as naphtha, butane, propane and the like. It is understood, however, that non-hydrocarbon solvents could also be used.
Surfactants that could be used in this process could be either non-ionic surfactants such as some alcohols (e.g., fatty, cetyl, stearyl) or ionic surfactants such as sulfates, sulfonates, phosphates or carboxylates. Generally, many ionic surfactants are not preferable, due to potential implications downstream in the refining process, but bitumen does have some natural carboxylates that could be enhanced biologically, using the same microbes that are used to help clean up oil spills. In another embodiment, depending on reservoir conditions, surfactants having cationic head groups such as primary, secondary and tertiary amines, which are pH
dependent, or quaternary ammonium cations can be used. The mineral characteristics of the reservoir should be taken into account in all cases when choosing a surfactant.
Thus, the present invention reduces the circulation time of steam in traditional SAGD
operations by reducing the start-up time from a few months to a few weeks. In particular, a midpoint temperature between the injector well and the producer well of 70-195 C may be reached within 60 days or less. In one embodiment, the electro-thermal heating element comprises an electrical cable, such as an ESP cable, at least one temperature gauge and the at WSLega1\046803 \00037 \I I 172610v1 5 least one heating section comprises an electro-thermal heating cable. In another embodiment, the heating sections are spaced along the electrical cable.
DESCRIPTION OF THE DRAWINGS
Referring to the drawings wherein like reference numerals indicate similar parts throughout the several views, several aspects of the present invention are illustrated by way of example, and not by way of limitation, in detail in the figures, wherein:
FIG. 1 is a drawing showing one embodiment of a SAGD operation of the present invention.
FIG. 2 is a drawing showing another embodiment of a SAGD operation of the present invention.
FIG. 3A, 3B and 3C shows the temperature distribution after 90 days of circulation of steam through both the injector well and producer well (3A), 60 days of steam circulation through both the injector well and producer well with a heater of the present invention at the toe of the injector well (3B) and 60 days of steam circulation through both the injector well and producer well with a heater of the present invention at the toe of both the injector well and the producer well (3C).
FIG. 4 is a drawing showing another embodiment of steam-assisted gravity drainage (SAGD) production of the present invention comprising two SAGD well pairs and an infill well therebctween.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The detailed description set forth below in connection with the appended drawings is intended as a description of various embodiments of the present invention and is not intended to represent the only embodiments contemplated by the inventor. The detailed description includes specific details for the purpose of providing a comprehensive understanding of the present invention. However, it will be apparent to those skilled in the art that the present invention may be practiced without these specific details.
WSLega1\046803 \00037 \ 11172610N 1 6 FIG. 1 shows one embodiment of steam-assisted gravity drainage (SAGD) production of the present invention. The SAGD well pair 10 is drilled into a formation 18 (e.g., an oil sands formation) comprising an overburden 12, and underburden 16 and a pay zone 14.
Injector well 20 comprises a vertical section 24 and a horizontal section (or leg) 26 having a toe 28 at its far end. Producer well 22 also comprises a vertical section 32, vertically spaced proximate to vertical section 24 of the injector well 20, and a horizontal section (or leg) 34 having a toe 30 at its far end. Generally, horizontal sections 26 and 34 are parallel to one another and are spaced about 4 to 10 meters from each other. Although drawn vertically in Figure 1, the wells may be drilled directionally as determined by practitioners skilled in the art of drilling.
In conventional SAGD, the injector well 20 injects steam to heat the space between and above the two wells and establish thermal communication between the two wells.
With continuous injection of steam, hydrocarbon (e.g., bitumen) present in the pay zone 14 is heated, mobilized and collected in producer well 22.
In the embodiment of FIG. 1, electro-thermal heating elements 36, 38 comprising electrical cables 46 and 48, respectively, can be inserted into the injector well 20 and the producer well 22, respectively. It is understood, however, that electro-thermal heating element may be inserted in only one of the injector well 20 and the producer well 22.
In this embodiment, electro-thermal heating elements 36, 38 each further comprise an individually controllable heating section, 40, 42, respectively, to thermally heat the formation, i.e., the pay zone 14, to establish thermal communication between the two wells. In one embodiment, each individually controllable heating section 40 and 42 may comprise a temperature gauge (not shown) or a distributed temperature sensing (DTS) device, e.g., an optoelectronic temperature sensing device, and an electro-thermal heating cable (not shown).
In FIG. 1, individually controllable heating section 40 is located in the middle portion of the horizontal leg 26 of injector well 20 and individually controllable heating section 42 is located near the toe 30 of the horizontal leg 34 of producer well 22.
A power supply and control system 50 can control the temperature of each individually controllable heating section 40, 42 by increasing/decreasing the amount of current through electrical cables 46, 48, respectively. For example, the sector of the pay zone surrounding the WSLega1\046803 \00037\11172610v 7 individually controllable heating section 40 may be a sector of the well where it is difficult for the steam to reach, e.g., it is near a permeability barrier. Therefore, while individually controllable heating section 40 will eventually heat up the entire area surrounding the horizontal leg 26, the majority of the heat is initially focused on the area within the permeability barrier. In this way, energy can be used in the most efficient way possible to form the thermal communication between the two wells.
FIG. 2 shows another embodiment of steam-assisted gravity drainage (SAGD) production of the present invention. The SAGD well pair 200 is drilled into a formation 218 (e.g., an oil sands formation) comprising an overburden 212, and underburden 216 and a pay zone 214.
Injector well 220 comprises a vertical section 224 and a horizontal section (or leg) 226 having a toe 228 at its far end. Producer well 222 also comprises a vertical section 232, vertically spaced proximate to vertical section 224 of the injector well 220, and a horizontal section (or leg) 234 having a toe 230 at its far end.
In the embodiment of FIG. 2, electro-thermal heating elements 236, 238 can be inserted into both the injector well 220 and the producer well 222, respectively. In this embodiment, electro-thermal heating element 236 comprises five individually controllable heating sections, 240a, 240b, 240c, 240d and 240e, to thermally heat the formation to establish thermal communication between the two wells.
Similarly, electro-thermal heating element 238 comprises five individually controllable heating sections, 242a, 242b, 242c, 242d and 242e, to thermally heat the formation to establish thermal communication between the two wells. In this embodiment, the thermal properties of a plurality of vertical sectors along the entire width of the pay zone 214 have been determined and each individually controllable heating section is positioned accordingly. Thus, each of the individually controllable heating section is operated according to the thermal properties surrounding it. Power supply and control system 250, together with, optionally, temperature gauges, can control the temperature of each individually controllable heating section by increasing/decreasing the amount of current through the electro-thermal heating elements 236, 238, respectively, and by other means known in the art.
By way of example, in the injector well 220, three of the individually controllable heating sections 240a, 240b and 240c (i.e., closest to the toe 228) may be operated at a much higher WSLega1\046803 \00037 \1117261 0v1 8 temperature than the two individually controllable heating sections 240d and 240e. This would be due to the fact that the sectors of pay zone 214 surrounding horizontal section 226 has a variable geological profile along its width, with the right half having a lower permeability than the left half. However, with respect to the producer well 222, the pay zone 214 surrounding the horizontal section 234 is much more uniform. Thus, individually controllable heating sections242a, 242b, 242c, 242d and 242e are all operated at the same temperature, albeit at a higher temperature that the two left individually controllable heating sections 240d and 240e of injector well 220, as the permeability is lower in the area surround the horizontal section 234 of the producer well 222 than that surrounding the left half of the horizontal section 226 of the injector well 220.
Thus, with the embodiment shown in FIG. 2, any designed heating pattern can be achieved by using an electro-thermal heating element of the present invention comprising a plurality of individually controllable heating sections on an electro-thermal cable, with locations of the individual heating sections being tailored to reservoir conditions.
With reference now to FIG. 4, another embodiment of steam-assisted gravity drainage (SAGD) production of the present invention is illustrated. Two SAGD well pairs 400a and 400b are drilled into a formation 418 (e.g., an oil sands formation) comprising an overburden 412, and underburden 416 and a pay zone 414. Each well pair 400a and 400b comprises an injector well, 420a and 420b, respectively, and a producer well, 422a and 422b, respectively.
An infill well 460 is drilled into the formation 418 in between well pairs 400a and 400b.
Infill well 460 also comprises a vertical section 462 and a horizontal section (or leg) 464. In one embodiment, an electro-thermal heating element 436 can be inserted into the infill well 460, the electro-thermal heating element 436 comprising one or more individually controllable heating sections 440a, 440b, 440c, 440d, to thermally heat the formation, i.e., the pay zone 414, between the two well pairs 400a and 400b, to establish thermal communication between the two well pairs.
Example 1 Electrical elements of approximately 100 m were installed at the toe of the injector only or at the toes of both injector and producer of a SAGD well pair. Generally, circulation start up involves establishing inter well communication by circulating steam through the injector and WSLegal \0µ16803 \00037 \ I 1172610 \ 9 producer. The steam would flow through the tubing string to the toe of each well. The rate of heat transfer and fluid convection into the reservoir formation determine how communication is established along the length of the well pair. In this example, an electrical cable is located at the toe of injector or both the injector/producer, at a maximum temperature of 350 C; steam is also injected into both the injector and producer.
When steam is added, it was discovered through simulation, that the electric cable can heat the condensed steam at the toe of the well and further transfer the heat generated to the mid section of the well, reducing the start up time and creating uniform steam chamber development along the entire well length. The minimum temperature at the midpoint between the two wells of 70 to 100 C is used as an indicator for terminating steam circulation and switching to SAGD
production mode.
Simulation results indicate that having electrical heaters at the toe of the well can improve the heat transfer, which can lead to a favorable development of uniform temperature between the well pairs and faster start up.
FIG. 3 shows temperature distribution after 60-90 days of steam injection. On the right hand side of FIG. 3 is a scale showing temperatures in the ranges of 7-41 C
(dark blue), 41-75 C (medium blue), 75-110 C (light blue), 110-144 C (turquoise), 144-178 (dark green), 178-212 C (medium green), 212-246 (light green), 246-281 C (yellow), 281-315 C
(orange), and 315-349 C (red). In particular, FIG. 3A shows the temperature distribution after 90 days of circulation with steam only in both the injector well and producer well. FIG.
3B shows temperature distribution after only 60 days of circulation with steam where a 100 m heater is located at the toe of the injector well only. FIG. 3C shows temperature distribution after only 60 days of circulation with steam where a 100 m heater is located at the toe of both the injector well and the producer well. The results of the simulation show a reduction in steam circulation time and uniform temperature between the injector and producer. The temperature distribution profiles show that focused electrical heating could reduce both the steam required and start up time.
From the foregoing description, one skilled in the art can easily ascertain the essential characteristics of this invention. However, the scope of the claims should not be limited by the WSLegal\ 046803 \00037 111172610N 1 10 preferred embodiments set forth in the examples, but should be given the broadest interpretation consistent with the description as a whole.
WSLega1\046803 \00037 \II 172610v1 11
Thus, in one aspect, a method for pre-heating a SAGD operation is provided, comprising:
= drilling a SAGD well pair in a bitumen bearing formation, the well pair comprising an injector well and a producer well;
= introducing an electro-thermal heating element having at least one individually controllable heating section in or near either the injector well, the producer well, or both;
= positioning the at least one individually controllable heating section at or near a sector of either the injector well, the producer well, or both, which sector may require greater thermal heat to establish thermal communication between the injector well and the producer well; and = operating the at least one individually controllable heating section at a desired temperature for a period of time sufficient to establish thermal communication between the injector well and the producer well.
WSLegaI\046803\00037\1l 726lO\'I 3 It is understood that proper casing and well-completion is adopted to accommodate the high temperature source of the present invention. In one embodiment, the at least one individually controllable heating section is positioned at the toe of the injector well, the producer well, or both. In another embodiment, the at least one individually controllable heating section is positioned at or near the middle of the injector well, the producer well, or both. In one embodiment, steam is also circulated through the injector well, the producer well, or both.
Following the pre-heating stage, the electro-thermal heating element that is placed in or near the injector well may be left down hole. Thus, when the steam injection into the injector well commences during the steam assisted gravity drainage process, the electro-thermal heating element can assist in controlling the quality of steam in the injector well.
For example, steam often condenses at the toe of the well. Thus, the electro-thermal heating element may comprise an individually controllable heating section that is positioned at the toe of the well. It is understood, however, that, in most instances, it is generally undesirable to leave an electro-thermal heating element in the producer well and, hence, the element should be removed prior to commencing the SAGD process. Thus, it is understood that in one embodiment, the electro-thermal heating elements are removable.
In one embodiment, the electro-thermal heating element comprises a plurality of individually controllable heating sections so that more heat can be provided to one or more specific sections of either the injector well, the producer well, or both, for example, those sections having poor permeability issues or other undesirable reservoir conditions, than other sections of either the injector well, the producer well, or both. In one embodiment, the electro-thermal heating element can be wrapped around the outside of the injector tubing, or liner, of the injector well, the producer tubing of the producer well, or both. Thus, depending on theimal properties of the formation, i.e., heat capacity, thermal conductivity, thermal expansion, and coefficient, an electro-thermal heating element comprising individually controllable heating sections of varying temperatures may be deployed along the injection well, the production well or both to achieve the desired (e.g., uniform) thermal pattern.
In one embodiment, the electro-thermal heating elements can be controlled from surface of the SAGD and each individually controllable heating section can be separately controlled by WSLegah 046803 \00037 \ 111726 I 0 \ 4 controlling or adjusting the current passing through the element and to the individual controllable heating section. In one embodiment, each individually controllable heating section of the electro-thermal heating element has its own thermocouple, DTS sensor, or similar, for measuring the temperature and adjusting the temperature of each section accordingly.
It is further contemplated to use this technique for infihl wells between the SAGD well pairs. The invention will allow for the faster communication of the infill well to steam chambers so that production of the infill well can begin sooner than would be possible without this technique.
In one embodiment, a solvent, a surfactant or other additive which changes the wettability or reduces the viscosity of bitumen is added to either the injector well, the producer well, or both, either prior to or during pre-heating. By being able to control the temperature of individual sectors of a well, one can also control how much solvent or other wettability additive will diffuse into the formation at a particular sector. Useful solvents can be hydrocarbon solvents such as naphtha, butane, propane and the like. It is understood, however, that non-hydrocarbon solvents could also be used.
Surfactants that could be used in this process could be either non-ionic surfactants such as some alcohols (e.g., fatty, cetyl, stearyl) or ionic surfactants such as sulfates, sulfonates, phosphates or carboxylates. Generally, many ionic surfactants are not preferable, due to potential implications downstream in the refining process, but bitumen does have some natural carboxylates that could be enhanced biologically, using the same microbes that are used to help clean up oil spills. In another embodiment, depending on reservoir conditions, surfactants having cationic head groups such as primary, secondary and tertiary amines, which are pH
dependent, or quaternary ammonium cations can be used. The mineral characteristics of the reservoir should be taken into account in all cases when choosing a surfactant.
Thus, the present invention reduces the circulation time of steam in traditional SAGD
operations by reducing the start-up time from a few months to a few weeks. In particular, a midpoint temperature between the injector well and the producer well of 70-195 C may be reached within 60 days or less. In one embodiment, the electro-thermal heating element comprises an electrical cable, such as an ESP cable, at least one temperature gauge and the at WSLega1\046803 \00037 \I I 172610v1 5 least one heating section comprises an electro-thermal heating cable. In another embodiment, the heating sections are spaced along the electrical cable.
DESCRIPTION OF THE DRAWINGS
Referring to the drawings wherein like reference numerals indicate similar parts throughout the several views, several aspects of the present invention are illustrated by way of example, and not by way of limitation, in detail in the figures, wherein:
FIG. 1 is a drawing showing one embodiment of a SAGD operation of the present invention.
FIG. 2 is a drawing showing another embodiment of a SAGD operation of the present invention.
FIG. 3A, 3B and 3C shows the temperature distribution after 90 days of circulation of steam through both the injector well and producer well (3A), 60 days of steam circulation through both the injector well and producer well with a heater of the present invention at the toe of the injector well (3B) and 60 days of steam circulation through both the injector well and producer well with a heater of the present invention at the toe of both the injector well and the producer well (3C).
FIG. 4 is a drawing showing another embodiment of steam-assisted gravity drainage (SAGD) production of the present invention comprising two SAGD well pairs and an infill well therebctween.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The detailed description set forth below in connection with the appended drawings is intended as a description of various embodiments of the present invention and is not intended to represent the only embodiments contemplated by the inventor. The detailed description includes specific details for the purpose of providing a comprehensive understanding of the present invention. However, it will be apparent to those skilled in the art that the present invention may be practiced without these specific details.
WSLega1\046803 \00037 \ 11172610N 1 6 FIG. 1 shows one embodiment of steam-assisted gravity drainage (SAGD) production of the present invention. The SAGD well pair 10 is drilled into a formation 18 (e.g., an oil sands formation) comprising an overburden 12, and underburden 16 and a pay zone 14.
Injector well 20 comprises a vertical section 24 and a horizontal section (or leg) 26 having a toe 28 at its far end. Producer well 22 also comprises a vertical section 32, vertically spaced proximate to vertical section 24 of the injector well 20, and a horizontal section (or leg) 34 having a toe 30 at its far end. Generally, horizontal sections 26 and 34 are parallel to one another and are spaced about 4 to 10 meters from each other. Although drawn vertically in Figure 1, the wells may be drilled directionally as determined by practitioners skilled in the art of drilling.
In conventional SAGD, the injector well 20 injects steam to heat the space between and above the two wells and establish thermal communication between the two wells.
With continuous injection of steam, hydrocarbon (e.g., bitumen) present in the pay zone 14 is heated, mobilized and collected in producer well 22.
In the embodiment of FIG. 1, electro-thermal heating elements 36, 38 comprising electrical cables 46 and 48, respectively, can be inserted into the injector well 20 and the producer well 22, respectively. It is understood, however, that electro-thermal heating element may be inserted in only one of the injector well 20 and the producer well 22.
In this embodiment, electro-thermal heating elements 36, 38 each further comprise an individually controllable heating section, 40, 42, respectively, to thermally heat the formation, i.e., the pay zone 14, to establish thermal communication between the two wells. In one embodiment, each individually controllable heating section 40 and 42 may comprise a temperature gauge (not shown) or a distributed temperature sensing (DTS) device, e.g., an optoelectronic temperature sensing device, and an electro-thermal heating cable (not shown).
In FIG. 1, individually controllable heating section 40 is located in the middle portion of the horizontal leg 26 of injector well 20 and individually controllable heating section 42 is located near the toe 30 of the horizontal leg 34 of producer well 22.
A power supply and control system 50 can control the temperature of each individually controllable heating section 40, 42 by increasing/decreasing the amount of current through electrical cables 46, 48, respectively. For example, the sector of the pay zone surrounding the WSLega1\046803 \00037\11172610v 7 individually controllable heating section 40 may be a sector of the well where it is difficult for the steam to reach, e.g., it is near a permeability barrier. Therefore, while individually controllable heating section 40 will eventually heat up the entire area surrounding the horizontal leg 26, the majority of the heat is initially focused on the area within the permeability barrier. In this way, energy can be used in the most efficient way possible to form the thermal communication between the two wells.
FIG. 2 shows another embodiment of steam-assisted gravity drainage (SAGD) production of the present invention. The SAGD well pair 200 is drilled into a formation 218 (e.g., an oil sands formation) comprising an overburden 212, and underburden 216 and a pay zone 214.
Injector well 220 comprises a vertical section 224 and a horizontal section (or leg) 226 having a toe 228 at its far end. Producer well 222 also comprises a vertical section 232, vertically spaced proximate to vertical section 224 of the injector well 220, and a horizontal section (or leg) 234 having a toe 230 at its far end.
In the embodiment of FIG. 2, electro-thermal heating elements 236, 238 can be inserted into both the injector well 220 and the producer well 222, respectively. In this embodiment, electro-thermal heating element 236 comprises five individually controllable heating sections, 240a, 240b, 240c, 240d and 240e, to thermally heat the formation to establish thermal communication between the two wells.
Similarly, electro-thermal heating element 238 comprises five individually controllable heating sections, 242a, 242b, 242c, 242d and 242e, to thermally heat the formation to establish thermal communication between the two wells. In this embodiment, the thermal properties of a plurality of vertical sectors along the entire width of the pay zone 214 have been determined and each individually controllable heating section is positioned accordingly. Thus, each of the individually controllable heating section is operated according to the thermal properties surrounding it. Power supply and control system 250, together with, optionally, temperature gauges, can control the temperature of each individually controllable heating section by increasing/decreasing the amount of current through the electro-thermal heating elements 236, 238, respectively, and by other means known in the art.
By way of example, in the injector well 220, three of the individually controllable heating sections 240a, 240b and 240c (i.e., closest to the toe 228) may be operated at a much higher WSLega1\046803 \00037 \1117261 0v1 8 temperature than the two individually controllable heating sections 240d and 240e. This would be due to the fact that the sectors of pay zone 214 surrounding horizontal section 226 has a variable geological profile along its width, with the right half having a lower permeability than the left half. However, with respect to the producer well 222, the pay zone 214 surrounding the horizontal section 234 is much more uniform. Thus, individually controllable heating sections242a, 242b, 242c, 242d and 242e are all operated at the same temperature, albeit at a higher temperature that the two left individually controllable heating sections 240d and 240e of injector well 220, as the permeability is lower in the area surround the horizontal section 234 of the producer well 222 than that surrounding the left half of the horizontal section 226 of the injector well 220.
Thus, with the embodiment shown in FIG. 2, any designed heating pattern can be achieved by using an electro-thermal heating element of the present invention comprising a plurality of individually controllable heating sections on an electro-thermal cable, with locations of the individual heating sections being tailored to reservoir conditions.
With reference now to FIG. 4, another embodiment of steam-assisted gravity drainage (SAGD) production of the present invention is illustrated. Two SAGD well pairs 400a and 400b are drilled into a formation 418 (e.g., an oil sands formation) comprising an overburden 412, and underburden 416 and a pay zone 414. Each well pair 400a and 400b comprises an injector well, 420a and 420b, respectively, and a producer well, 422a and 422b, respectively.
An infill well 460 is drilled into the formation 418 in between well pairs 400a and 400b.
Infill well 460 also comprises a vertical section 462 and a horizontal section (or leg) 464. In one embodiment, an electro-thermal heating element 436 can be inserted into the infill well 460, the electro-thermal heating element 436 comprising one or more individually controllable heating sections 440a, 440b, 440c, 440d, to thermally heat the formation, i.e., the pay zone 414, between the two well pairs 400a and 400b, to establish thermal communication between the two well pairs.
Example 1 Electrical elements of approximately 100 m were installed at the toe of the injector only or at the toes of both injector and producer of a SAGD well pair. Generally, circulation start up involves establishing inter well communication by circulating steam through the injector and WSLegal \0µ16803 \00037 \ I 1172610 \ 9 producer. The steam would flow through the tubing string to the toe of each well. The rate of heat transfer and fluid convection into the reservoir formation determine how communication is established along the length of the well pair. In this example, an electrical cable is located at the toe of injector or both the injector/producer, at a maximum temperature of 350 C; steam is also injected into both the injector and producer.
When steam is added, it was discovered through simulation, that the electric cable can heat the condensed steam at the toe of the well and further transfer the heat generated to the mid section of the well, reducing the start up time and creating uniform steam chamber development along the entire well length. The minimum temperature at the midpoint between the two wells of 70 to 100 C is used as an indicator for terminating steam circulation and switching to SAGD
production mode.
Simulation results indicate that having electrical heaters at the toe of the well can improve the heat transfer, which can lead to a favorable development of uniform temperature between the well pairs and faster start up.
FIG. 3 shows temperature distribution after 60-90 days of steam injection. On the right hand side of FIG. 3 is a scale showing temperatures in the ranges of 7-41 C
(dark blue), 41-75 C (medium blue), 75-110 C (light blue), 110-144 C (turquoise), 144-178 (dark green), 178-212 C (medium green), 212-246 (light green), 246-281 C (yellow), 281-315 C
(orange), and 315-349 C (red). In particular, FIG. 3A shows the temperature distribution after 90 days of circulation with steam only in both the injector well and producer well. FIG.
3B shows temperature distribution after only 60 days of circulation with steam where a 100 m heater is located at the toe of the injector well only. FIG. 3C shows temperature distribution after only 60 days of circulation with steam where a 100 m heater is located at the toe of both the injector well and the producer well. The results of the simulation show a reduction in steam circulation time and uniform temperature between the injector and producer. The temperature distribution profiles show that focused electrical heating could reduce both the steam required and start up time.
From the foregoing description, one skilled in the art can easily ascertain the essential characteristics of this invention. However, the scope of the claims should not be limited by the WSLegal\ 046803 \00037 111172610N 1 10 preferred embodiments set forth in the examples, but should be given the broadest interpretation consistent with the description as a whole.
WSLega1\046803 \00037 \II 172610v1 11
Claims (16)
1. A method for pre-heating a SAGD operation, comprising:
drilling a SAGD well pair in a bitumen bearing formation, the well pair comprising an injector well and a producer well;
introducing an electro-thermal heating element comprising at least one individually controllable heating section in or near either the injector well, the producer well, or both;
positioning the at least one individually controllable heating section at or near a sector of either the injector well, the producer well, or both, which sector may require greater thermal heat to establish thermal communication between the injector well and the producer well; and operating the at least one individually controllable heating section at a desired temperature for a period of time sufficient to establish thermal communication between the injector well and the producer well.
drilling a SAGD well pair in a bitumen bearing formation, the well pair comprising an injector well and a producer well;
introducing an electro-thermal heating element comprising at least one individually controllable heating section in or near either the injector well, the producer well, or both;
positioning the at least one individually controllable heating section at or near a sector of either the injector well, the producer well, or both, which sector may require greater thermal heat to establish thermal communication between the injector well and the producer well; and operating the at least one individually controllable heating section at a desired temperature for a period of time sufficient to establish thermal communication between the injector well and the producer well.
2. The method as claimed in claim 1, wherein the at least one individually controllable heating section is positioned at the toe of the injector well, the producer well, or both.
3. The method as claimed in claim 1, wherein the at least one individually controllable heating section is positioned at or near the middle of the injector well, the producer well, or both.
4. The method as claimed in claim 1, wherein the at least one individually controllable heating section is positioned based on reservoir characteristics.
5. The method as claimed in claim 1, wherein steam is also circulated through the injector well, the producer well, or both.
6. The method as claimed in claim 1, wherein following the establishment of thermal communication between the injector well and the producer well, the electro-thermal heating element that is placed in or near the injector well is left down hole.
7. The method as claimed in claim 1, wherein the electro-thermal heating element comprises an electrical cable having a plurality of individually controllable heating sections spaced along the electrical cable.
8. The method as claimed in claim 7, wherein each individually controllable heating section can be separately controlled by controlling or adjusting the current passing through the electrical cable and to the individual controllable heating sections.
9. The method as claimed in claim 7, wherein each individually controllable heating section of the electro-thermal heating element has its own thermal couple or distributed temperature sensing (DTS) device or similar for measuring the temperature and then adjusting the temperature of each section accordingly.
10. The method as claimed in claim 1, wherein the electro-thermal heating element can be controlled from surface of the SAGD operation.
11. The method as claimed in claim 1, wherein a solvent, a surfactant or other additive which changes the wettability or reduces the viscosity of bitumen is added to either the injector well, the producer well, or both, either prior to or during pre-heating.
12. A method for pre-heating a SAGD operation, comprising:
drilling two SAGD well pairs in a bitumen bearing formation, each well pair comprising an injector well and a producer well;
drilling an infill well between the two SAGD well pairs in the bitumen bearing formation, introducing an electro-thermal heating element in or near the infill well, the electro-thermal having at least one individually controllable heating section.
drilling two SAGD well pairs in a bitumen bearing formation, each well pair comprising an injector well and a producer well;
drilling an infill well between the two SAGD well pairs in the bitumen bearing formation, introducing an electro-thermal heating element in or near the infill well, the electro-thermal having at least one individually controllable heating section.
13. The method as claimed in claim 12, wherein the electro-thermal heating element comprises an electrical cable having a plurality of individually controllable heating sections spaced along the electrical cable.
14. The method as claimed in claim 13, wherein each individually controllable heating section can be separately controlled by controlling or adjusting the current passing through the electrical cable and to the individual controllable heating sections.
15. The method as claimed in claim 13, wherein each individually controllable heating section of the electro-thermal heating element has its own thermal couple or distributed temperature sensing (DTS) device or similar for measuring the temperature and then adjusting the temperature of each section accordingly.
16. The method as claimed in claim 12, wherein the electro-thermal heating element can be controlled from surface of the SAGD operation.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201461969731P | 2014-03-24 | 2014-03-24 | |
| US61/969,731 | 2014-03-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2875687A1 true CA2875687A1 (en) | 2015-09-24 |
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ID=54141628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA2875687A Abandoned CA2875687A1 (en) | 2014-03-24 | 2014-12-23 | Use of electrical heating elements for sagd start-up |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US20150267522A1 (en) |
| CA (1) | CA2875687A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10344579B2 (en) | 2013-11-06 | 2019-07-09 | Cnooc Petroleum North America Ulc | Processes for producing hydrocarbons from a reservoir |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10794162B2 (en) | 2017-12-12 | 2020-10-06 | Baker Hughes, A Ge Company, Llc | Method for real time flow control adjustment of a flow control device located downhole of an electric submersible pump |
| US11441403B2 (en) | 2017-12-12 | 2022-09-13 | Baker Hughes, A Ge Company, Llc | Method of improving production in steam assisted gravity drainage operations |
| US10550671B2 (en) | 2017-12-12 | 2020-02-04 | Baker Hughes, A Ge Company, Llc | Inflow control device and system having inflow control device |
| CN109138976B (en) * | 2018-07-23 | 2022-01-04 | 中国石油天然气股份有限公司 | Method for judging time for converting double-horizontal-well preheating into SAGD (steam assisted gravity drainage) and double-horizontal-well preheating device |
Family Cites Families (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2780450A (en) * | 1952-03-07 | 1957-02-05 | Svenska Skifferolje Ab | Method of recovering oil and gases from non-consolidated bituminous geological formations by a heating treatment in situ |
| US4498535A (en) * | 1982-11-30 | 1985-02-12 | Iit Research Institute | Apparatus and method for in situ controlled heat processing of hydrocarbonaceous formations with a controlled parameter line |
| US5449251A (en) * | 1993-05-04 | 1995-09-12 | The Regents Of The University Of California | Dynamic underground stripping: steam and electric heating for in situ decontamination of soils and groundwater |
| US6112808A (en) * | 1997-09-19 | 2000-09-05 | Isted; Robert Edward | Method and apparatus for subterranean thermal conditioning |
| AU5791999A (en) * | 1998-08-25 | 2000-03-14 | Baker Hughes Incorporated | Method of using a heater with a fiber optic string in a wellbore |
| US8528639B2 (en) * | 2011-03-07 | 2013-09-10 | Conocophillips Company | Method for accelerating start-up for steam-assisted gravity drainage (SAGD) operations |
| CA2791725A1 (en) * | 2011-10-07 | 2013-04-07 | Shell Internationale Research Maatschappij B.V. | Treating hydrocarbon formations using hybrid in situ heat treatment and steam methods |
| WO2013070266A2 (en) * | 2011-11-11 | 2013-05-16 | Delp Daniel | Composite cable systems for use in an in situ oil production process |
| US9557437B2 (en) * | 2012-08-29 | 2017-01-31 | Selkermetrics, LLC | Monitoring movement in fluid-containing environment via variable heating |
| US10113403B2 (en) * | 2013-08-29 | 2018-10-30 | Delphi Technologies, Inc. | Heater and method of operating |
| WO2015066796A1 (en) * | 2013-11-06 | 2015-05-14 | Nexen Energy Ulc | Processes for producing hydrocarbons from a reservoir |
-
2014
- 2014-12-23 US US14/581,553 patent/US20150267522A1/en not_active Abandoned
- 2014-12-23 CA CA2875687A patent/CA2875687A1/en not_active Abandoned
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10344579B2 (en) | 2013-11-06 | 2019-07-09 | Cnooc Petroleum North America Ulc | Processes for producing hydrocarbons from a reservoir |
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