CA2384612A1 - Improved enhanced oil recovery - Google Patents
Improved enhanced oil recovery Download PDFInfo
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- CA2384612A1 CA2384612A1 CA002384612A CA2384612A CA2384612A1 CA 2384612 A1 CA2384612 A1 CA 2384612A1 CA 002384612 A CA002384612 A CA 002384612A CA 2384612 A CA2384612 A CA 2384612A CA 2384612 A1 CA2384612 A1 CA 2384612A1
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- carbon dioxide
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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
- E21B43/164—Injecting CO2 or carbonated water
Abstract
A method for enhancing the recovery of oil from underground formations is disclosed. A gas mixture which contains greater than 50% by volume carbon dioxide, the remainder being an inert gas, is injected in the underground formation to lower the oil viscosity and surface tension and increase the oil swelling. Preferably, the gas mixture contains greater than 60% by volume carbon dioxide with a gas mixture containing greater than 70% by volume carbon dioxide preferred.
Description
IMPROVED ENHANCED OIL RECOVERY
FIELD OF THE INVENTION
The present invention provides for a method for enhancing the recovery of oil from underground formations. More particularly, the present invention provides for injecting into the oil in the underground formation a gas mixture which contains at least 50% by volume carbon dioxide and the remainder nitrogen or other inert gas.
io BACKGROUND OF THE INVENTION
Oil or gas and any water which is contained in the porous rock surrounding the oil or gas in a reservoir or formation are typically under is pressure due to the weight of the material above them. As such, they will move to an area of lower pressure and higher elevation such as the well head. After some pressure has been released, the oil may still flow to the surface but it does so more slowly. This movement can be helped along by a mechanical pump such as the grasshopper pumps one often sees. These 2o processes are typically referred to as primary oil recovery. Typically, less than 50% of the oil in the oil formation is recovered by primary techniques.
Recovery can be increased by pursuing enhanced oil recovery (EOR) methods. Typically, these methods are divided into two groups: secondary and tertiary.
Secondary FOR generally refers to pumping a fluid, either liquid or gas, into the ground to build back pressure that was dissipated during primary recovery. The most common of these methods is to inject water and is simply called a waterflood.
The tertiary recovery schemes typically use chemical interactions or heat to either reduce the oil viscosity so the oil flows more freely or to change the properties of the interface between the oil and the surrounding rock pores so that the oil can flow out of the small pores in the rock and enter larger channels where the oil can be swept by a driving fluid or move by pressure gradient to a production well. The oil may also be swelled so that a portion of the oil emerges from small pores into the channels or larger pores in the rock.
Typical of these processes are steam injection, miscible fluid injection and surfactant injection.
io Thermal techniques employing steam can be utilized in a well to well scheme or also in a single-well technique which is know as the huff and puff method. In this method, steam is injected via a well in a quantity sufficient to heat the subterranean hydrocarbon-bearing formation in the vicinity of the is well. The well is then shut in for a soaking period after which it is placed on production. After production has declined, the huff and puff method may again be employed on the same well to again stimulate production.
The use of carbon dioxide and its injection into oil reservoirs is known 2o for well to well and single well production enhancement. The carbon dioxide dissolves in the oil easily and causes the oil to swell and reduces the viscosity and surface tension of the oil which in turn leads to additional oil recovery.
The carbon dioxide may also be employed with steam such that the steam and carbon dioxide are injected either simultaneously or sequentially, often 2s followed by a soak period, followed by a further injection of carbon dioxide or other fluids.
US 2,623,596 describes enhanced recovery using gases in an injection well with oil recovery from a separate production well. Enhanced recovery using C02 and N2 mixtures is discussed with data presented showing oil recovery increasing monotonically as C02% in the gas mixture is increased.
However, the data presented does not demonstrate results when between 85% C02 and 100% C02, is employed.
US Patent 3,295,601 teaches that a slug of gas consisting of carbon dioxide and hydrocarbon gases, preferably of two to four carbon atoms, or nitrogen, air, hydrogen sulfide, flue gases and similar gases in a gas mixture, when injected in a well, establishes a transition zone. This transition zone is io then driven through the injection well by a driving fluid which will produce oil from the stratum and reduce viscous fingering. The preferred slug of gas consists of 50% carbon dioxide and a substantial concentration of CZ to C4 hydrocarbon gases such as 10 to 50% by volume. It appears that the remainder of the gases in this gas mixture are selected from the group is consisting of nitrogen, air, hydrogen sulfide and flue gases and similar gases would make up the balance in the preferred composition of carbon dioxide and C2 to C4 hydrocarbon gas.
US Patent 5,725,054 teaches a method for recovering oil from a 2o subterranean formation by injecting into said well a gas mixture which comprises carbon dioxide and a gas selected from the group consisting of methane, nitrogen and mixtures thereof. The gas mixture comprises about 5 to about 50% by volume of carbon dioxide. As noted in the examples, the highest percentages were 50% by volume carbon dioxide.
2s The present inventors have discovered that the use of carbon dioxide in percentages greater than 50%, up to 99%, along with nitrogen or another inert gas as the remainder of the gas mixture will enhance oil production.
SUMMARY OF THE INVENTION
The present invention provides for a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil s a gas mixture comprising at least 50% by volume of carbon dioxide and an inert gas. The present invention further provides for a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil a gas mixture comprising carbon dioxide and nitrogen wherein the carbon dioxide is present in the gas mixture in an amount of at least 50% by to volume. In addition, the present invention will provide for a method for lowering the viscosity and surface tension as well as increasing the volume or swelling of the oil in an underground formation comprising injecting into the oil a gas mixture comprising at least 50% by volume carbon dioxide and an inert gas.
is BRIEF DESCRIPTION OF THE DRAWINGS
Fig. 1 is a graphical representation of the effect of carbon dioxide content of gas on paraffin oil viscosity.
Fig. 2 is a graphical representation of carbon dioxide content of gas on naphthene oil viscosity.
Fig. 3 is a graphical representation of carbon dioxide content of gas on 2s aromatic oil viscosity.
Fig. 4 is a graphical representation of carbon dioxide content of gas on paraffin oil surface tension.
Fig. 5 is a graphical representation of carbon dioxide content of gas on naphthene oil surface tension.
Fig. 6 is a graphical representation of carbon dioxide content of gas on aromatic oil surface tension.
Fig. 7 is a graphical representation of carbon dioxide content of gas on paraffin oil viscosity at various temperatures.
io Fig. 8 is a graphical representation of carbon dioxide content of gas on paraffin oil surface tension at various temperatures.
Fig. 9 is a graphical representation of carbon dioxide content of gas on paraffin oil volume at various temperatures.
is DETAILED DESCRIPTION OF THE INVENTION
The present invention comprises a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil a gas 2o mixture comprising at least 50% by volume carbon dioxide and an inert gas.
The inert gas is preferably nitrogen. Other inert gases such as helium and argon may also be employed. The present invention also comprises a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil a gas mixture which comprises carbon dioxide 2s and nitrogen. The carbon dioxide is present in the gas mixture in an amount of at least 50% by volume. 'The introduction of a combination of carbon dioxide and nitrogen gas to the formation provides an unexpected advantage of lower oil viscosity and surface tension than the introduction of carbon dioxide or nitrogen alone. This will also provide greater oil swelling than the use of carbon dioxide or nitrogen alone. The use of nitrogen adds an economic advantage to the mixture as there is lower cost than that for pure carbon dioxide consumption.
For purposes of the present invention, Applicants define oil as being a hydrocarbon which comprises paraffin, aromatic or naphthene constituents or mixtures thereof.
The mixture of the carbon dioxide and nitrogen will be injected into the io formation containing the oil at a pressure of 100 pounds per square inch to 20,000 pounds per square inch depending upon the depth of the oil reservoir.
This injection method allows for use of WAG (water alternating gas) well-to-well process whereby an injection of gas is followed by a waterflood to drive the oil and enhance production at the well head. This injection method will is also work in a huff and puff process. In the huff and puff process, the mixture would be injected into the formation. The formation would then be sealed allowing a soak period of determinate length of time, followed by an improved oil recovery or production period.
2o The mixtures of carbon dioxide and nitrogen may be created by any means. Preferably, a carbon dioxide-rich stream and a nitrogen-rich stream are combined or a hydrocarbon is combusted using air or oxygen-enriched air to produce the carbon dioxide. The present inventors assert that in addition to nitrogen, other inert gases, when combined with carbon dioxide in an 2s optimum ratio, will minimize oil viscosity and surface tension while increasing swelling.
One means for producing the carbon dioxide-rich gas stream involves the use of a power plant or co-generation plant at or near the well site.
Oxygen-enriched air and hydrocarbon are combusted to generate power and carbon dioxide-rich gas. The power is used to operate an air separation plant which provides the oxygen for the oxygen enrichment of the power or co-generation plant. Additional nitrogen and/or steam produced may also be used to enhance oil recovery by placing these materials in an injection well either individually or in combination with the carbon dioxide-rich gas stream.
The combination of heat and carbon dioxide can further improve recovery and little carbon dioxide would be lost to the aqueous phase as a result.
io Another means for producing the carbon dioxide is by injection of pure oxygen, oxygen-enriched air or air downhole. For wells that are sufficiently deep enough, the temperature will be sufficient to sustain combustion and produce carbon dioxide. For example, a 8000 foot deep well may have a temperature of 300°F which is hot enough to produce the carbon dioxide is necessary for the enhanced oil recovery.
In a preferred embodiment of the present invention, a carbon dioxide nitrogen mixture with carbon dioxide present greater than 50% by volume is injected into the formation at or near the production well by optimizing the 2o composition of the gas mixture. Due to the varied rates in the uptake of carbon dioxide and nitrogen, a near optimum composition can be maintained in the formation at that injection location. A second mixture of carbon dioxide and nitrogen would then be injected through injection wells) located at a distance from the production well. The composition of this gas mixture would 2s be such that the viscosity and surface tension of the oil is higher than that of the oil near or at the production well but still reduced in comparison to the untreated oil. Gas may be fed continuously to the injection wells) or the wells) can be shut for a period of at least a day to facilitate the uptake of the gas by the oil.
Oil is driven to the production well and fingering or bypass of the gas though the oil is minimized as a result. In this preferred embodiment, more than one remote injection point may be employed such that the viscosity and s surface tension of the oil at the remote injection point becomes higher with each injection point further away from the well head injection point by optimizing the content of the carbon dioxide and nitrogen gas mixture.
Accordingly, the nitrogen content of the gas mixture will increase as one injects the mixture further from the production well. This gradient will result in io a raising of carbon dioxide content above the 50% by volume as one injects at points getting sequentially closer to the production well. In this embodiment, a later possibly intermittent use of carbon dioxide flood, nitrogen flood or water flood to drive the oil to the production well would further improve yields.
is A preferred composition for use in the methods of the present invention is that of at least 50% by volume carbon dioxide, the remainder being nitrogen or other inert gas including helium, argon or steam. In a more preferred embodiment, greater than 60% carbon dioxide by volume with the 2o remainder being inert gases would comprise the gaseous mixture. In the most preferred embodiment, greater than 75% by volume of the gas mixture would be carbon dioxide and the remainder being inert gases.
In an additional embodiment, hydrocarbons can be added to the above 2s described compositions. These hydrocarbons, such as methane, ethane and propane can come from traditional sources but may also come from the associated gas produced during oil production. The hydrocarbons can be separated from oil and reinjected into the ground or may be separated from oil and reinjected into the ground after burning a portion of the hydrocarbon in air, oxygen or oxygen enriched air.
s EXAMPLES
Three model oils were studied to explore the potential of mixtures of carbon dioxide and nitrogen for enhanced oil recovery. A simulation was developed based on the Peng-Robinson equation of state for vapor-liquid io equilibrium, the Twu model for liquid phase viscosity and a modified form of the Brock and Bird equation for surface tension. The three oils employed in this study were of paraffin, naphthene and aromatic types. A gas mixture of carbon dioxide and nitrogen with a usage rate of 1 mole per mole of oil was presumed and a small quantity of water was added to the mixture since is typically carbon dioxide flooding operations follow water flood procedures or are conducted as in the WAG method alternatively with waterflood. The quantity of water was based on 20% saturation for a typical oil. Pressures in the range of 1,500 psia to 2,500 psia and temperatures in the range of 75°F
to 200°F were studied.
As shown in Figs. 1, 2 and 3, and Tables 1, 2 and 3, the relationship of a paraffin, naphthene and aromatic oil viscosity at 75°F to the percentage of carbon dioxide in the oil recovery gas mixture is demonstrated. It can be seen that greater than 50% carbon dioxide in the gas mixture is 2s advantageous in lowering the oil viscosity relative to the use of 100%
carbon dioxide.
Table 1. Effect of C02 Content of Gas on Paraffin Oil Viscosity at Various Pressures and 75 F
C02 Oil Oil Oil content viscosityviscosityviscosity of at at at gas 1500 psia2000 2500 psia (%) (cP) psia (cP) (cP) 0 0.592 0.571 0.552 25 0.557 0.534 0.513 50 0.515 0.49 0.468 68 0.478 0.453 0.437 75 0.462 0.443 0.449 80 0.45 1J.451 0.457 85 0.451 0.46 0.466 88 0.456 0.465 0.472 92 0.464 0.472 0.479 100 0.478 IJ.487 0.493 Table 2. Effect of C02 Content of Gas on Naphthene Oil Viscosity at Various Pressures and 75 F
C02 Oil Oil Oil content viscosityviscosityviscosity of at at at gas 1500 psia2000 psia2500 (%) (cP) (cP) psia (cP) 0 1.93 1.87 1.82 25 1.69 1.62 1.57 50 1.44 1.38 1.32 68 1.26 1.19 1.14 75 1.18 1.12 1.07 80 1.12 1.06 1.02 85 1.06 1.01 0.997 88 1.02 U.993 1.01 92 0.986 1.01 1.02 100 1.02 1.04 1.05 Table 3. Effect of C02 Content of Gas on Aromatic Oil Viscosity at Various Pressures and 75 F
C02 Oil Oil Oil content viscosityviscosityviscosity of at at at gas 1500 psia2000 2500 psia (%) (cP) psia (cP) (cP) 0 0.827 0.811 0.797 25 0.7566 0.738 0.722 50 0.679 0.658 0.642 68 0.615 0.595 0.578 75 0.587 0.567 0.552 80 0.566 6.547 0.532 85 0.544 0.526 0.512 88 0.529 0.512 0.519 92 0.51 0.52 0.527 100 0.527 0.537 0.544 Figs. 4, 5 and 6 and Tables 4, 5 and 6 show the relationship of a to paraffin, naphthene and aromatic oil surface tension at 75°F to the percentage carbon dioxide and the oil recovery gas mixture for three different pressures. As can be seen in Figs. 4, 5 and 6, greater than 60% carbon dioxide in the gas mixture is advantageous in reducing surface tension in comparison to the use of pure carbon dioxide.
Table 4. Effect of C02 Content of Gas on Paraffin Oil Surface Tension at Various Pressures and 75 F' C02 Oil surfaceOil surfaceOil surface content tension tension tension of at at at gas 1500 2000 psia2500 psia (%) psia (dyne/cm)(dyne/cm) (dyne/cm) 0 19.22 18.39 17.65 25 17.1 16.19 15.41 50 14.93 13.99 13.21 68 13.27 12.35 11.8 75 12.59 11.86 11.86 80 12.09 11.91 11.9 85 11.96 11.95 11.95 88 11.98 11.98 11.98 92 12.02 12.02 12.02 100 12.09 12.1 12.1 Table 5. Effect of C02 Content of Gas on Naphthene Oil Surface Tension at Various Pressures and 75 F
C02 Oil surfaceOil surfaceOil surface content tension tension tension of at at at gas 1500 2000 psia2500 psia (%) psia (dyne/cm)(dynelcm) (d ne/cm) 0 29.21 28.56 27.96 25 26.14 25.3 24.59 50 22.93 21.97 21.23 68 20.4 19.44 18.73 75 19.34 18.42 17.72 80 18.53 17.64 16.97 85 17.69 16.85 16.59 88 17.16 16.61 16.62 92 16.65 16.86 16.66 100 16.72 16.73 16.73 Table 6. Effect of C02 Content of Gas on Aromatic Oil Surface Tension at Various Pressures and 75 F
C02 Oil surfaceOil surfaceOil surface content tension tension tension of at at at gas 1500 psia2000 psia2500 psia (%) (dyne/cm)(d ne/cm)(dyne/cm) 0 29.84 29.29 28.79 25 26.71 25.96 25.33 50 23.41 22.53 21.87 68 20.81 19.94 19.28 75 19.73 18.87 18.25 80 18.92 18.08 17.48 85 18.06 17.28 16.72 88 17.52 16.77 16.76 92 16.8 16.8 16.8 100 16.86 16.86 16.86 Figs. 7 and 8 and Tables 7 and 8 show the relationship of a paraffin oil viscosity and surface tension at various temperatures to the percentage carbon dioxide and the oil recovery gas mixture. As demonstrated in the earlier examples, greater than 50% carbon dioxide in the gas mixture is advantageous in comparison to the use of pure carbon dioxide. Oil viscosity to is greatly reduced at around 70 to 80% carbon dioxide while surface tension remains approximately constant at the higher carbon dioxide concentrations.
Table 7. Effect of C02 Content of Gas on Paraffin Oil Viscosity at Various Temperatures and 2000 psia C02 Oil Oil Oil Oil Oil contentviscosityviscosityviscosityviscosityviscosity of gas at 75 at 100 at 125 at 150 at 200 (%) F F F F F
(cP) (cP) (cP) (cP) (cP) 0 0.571 0.486 0.419 0.365 0.282 50 0.49 0.429 0.375 0.329 0.257 75 0.443 0.387 0.341 0.301 0.235 80 0.451 0.394 0.342 0.298 0.229 85 0.46 0.402 0.348 0.304 0.23 88 0.465 0.407 0.352 0.307 0.233 92 0.472 0.413 0.358 0.312 0.237 100 0.487 0.426 0.369 0.321 0.244 s Table 8. Effect of C02 Content of Gas on Paraffin Oil Surface Tension at Various Temperatures and 2000 psia C02 Oil Oil Oil Oil Oil contentsurfacesurfacesurfacesurfacesurface of gas tensiontensiontensiontensiontension (%) at 75 at 100 at 125 at 150 at 200 F F F F F
(dyne/cm)(dyne/cm)(dyne/cm)(dyne/cm)(dyne/cm) 0 18.39 17.3 16.21 15.13 13 50 13.99 12.91 12.29 11.63 10.26 75 11.86 10.53 10.06 9.582 8.574 80 11.91 10.52 9.887 9.265 8.167 85 11.95 10.52 9.888 9.266 8.044 88 11.98 10.52 9.887 9.266 8.046 92 12.02 10.52 9.888 9.266 8.044 100 12.1 10.52 9.887 9.265 8.045 Fig. 9 and Table 9 show the relationship of a paraffin oil relative to volume at various temperatures as to the percentage carbon dioxide in the oil recovery gas mixture. The relative volume is taken in comparison to a standard oil volume. Roughly 70% to 99% carbon dioxide in the gas mixture is advantageous in comparison to the use of pure carbon dioxide to maximize swelling in this case. As swelling of the oil increases, the oil will exit small is pores within the subterranean formation and can be swept or driven to the production well by use of the various flood techniques.
Table 9. Effect of C02 Content of Gas on Paraffin Oil Relative Volume at Various Temperatures and 2000 psia*
C02 Oil Oil Oil Oil Oil contentrelativerelativerelativerelativerelative of gas volume volume volume volume volume (%) at 75 at 100 at 125 at 150 at 200 F F F F F
0 1.036 1.053 1.071 1.090 1.131 50 1.118 1.135 1.154 1.176 1.235 75 1.193 1.222 1.244 1.27 1.353 80 1.188 1.217 1.249 1.287 1.392 85 1.183 1.211 1.243 1.280 1.398 88 1.179 1.207 1.239 1.276 1.391 92 1.175 1.203 1.234 1.271 1.383 100 1.167 1.194 1.224. 1.261 1.366 ~ I
*Relative volume is in comparison to a standard oil volume io While this invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modifications of the invention will be obvious to those skilled in the art.
The appended claims of this invention generally should be construed to cover all is such obvious forms and modifications which are within the true spirit and scope of the present invention.
FIELD OF THE INVENTION
The present invention provides for a method for enhancing the recovery of oil from underground formations. More particularly, the present invention provides for injecting into the oil in the underground formation a gas mixture which contains at least 50% by volume carbon dioxide and the remainder nitrogen or other inert gas.
io BACKGROUND OF THE INVENTION
Oil or gas and any water which is contained in the porous rock surrounding the oil or gas in a reservoir or formation are typically under is pressure due to the weight of the material above them. As such, they will move to an area of lower pressure and higher elevation such as the well head. After some pressure has been released, the oil may still flow to the surface but it does so more slowly. This movement can be helped along by a mechanical pump such as the grasshopper pumps one often sees. These 2o processes are typically referred to as primary oil recovery. Typically, less than 50% of the oil in the oil formation is recovered by primary techniques.
Recovery can be increased by pursuing enhanced oil recovery (EOR) methods. Typically, these methods are divided into two groups: secondary and tertiary.
Secondary FOR generally refers to pumping a fluid, either liquid or gas, into the ground to build back pressure that was dissipated during primary recovery. The most common of these methods is to inject water and is simply called a waterflood.
The tertiary recovery schemes typically use chemical interactions or heat to either reduce the oil viscosity so the oil flows more freely or to change the properties of the interface between the oil and the surrounding rock pores so that the oil can flow out of the small pores in the rock and enter larger channels where the oil can be swept by a driving fluid or move by pressure gradient to a production well. The oil may also be swelled so that a portion of the oil emerges from small pores into the channels or larger pores in the rock.
Typical of these processes are steam injection, miscible fluid injection and surfactant injection.
io Thermal techniques employing steam can be utilized in a well to well scheme or also in a single-well technique which is know as the huff and puff method. In this method, steam is injected via a well in a quantity sufficient to heat the subterranean hydrocarbon-bearing formation in the vicinity of the is well. The well is then shut in for a soaking period after which it is placed on production. After production has declined, the huff and puff method may again be employed on the same well to again stimulate production.
The use of carbon dioxide and its injection into oil reservoirs is known 2o for well to well and single well production enhancement. The carbon dioxide dissolves in the oil easily and causes the oil to swell and reduces the viscosity and surface tension of the oil which in turn leads to additional oil recovery.
The carbon dioxide may also be employed with steam such that the steam and carbon dioxide are injected either simultaneously or sequentially, often 2s followed by a soak period, followed by a further injection of carbon dioxide or other fluids.
US 2,623,596 describes enhanced recovery using gases in an injection well with oil recovery from a separate production well. Enhanced recovery using C02 and N2 mixtures is discussed with data presented showing oil recovery increasing monotonically as C02% in the gas mixture is increased.
However, the data presented does not demonstrate results when between 85% C02 and 100% C02, is employed.
US Patent 3,295,601 teaches that a slug of gas consisting of carbon dioxide and hydrocarbon gases, preferably of two to four carbon atoms, or nitrogen, air, hydrogen sulfide, flue gases and similar gases in a gas mixture, when injected in a well, establishes a transition zone. This transition zone is io then driven through the injection well by a driving fluid which will produce oil from the stratum and reduce viscous fingering. The preferred slug of gas consists of 50% carbon dioxide and a substantial concentration of CZ to C4 hydrocarbon gases such as 10 to 50% by volume. It appears that the remainder of the gases in this gas mixture are selected from the group is consisting of nitrogen, air, hydrogen sulfide and flue gases and similar gases would make up the balance in the preferred composition of carbon dioxide and C2 to C4 hydrocarbon gas.
US Patent 5,725,054 teaches a method for recovering oil from a 2o subterranean formation by injecting into said well a gas mixture which comprises carbon dioxide and a gas selected from the group consisting of methane, nitrogen and mixtures thereof. The gas mixture comprises about 5 to about 50% by volume of carbon dioxide. As noted in the examples, the highest percentages were 50% by volume carbon dioxide.
2s The present inventors have discovered that the use of carbon dioxide in percentages greater than 50%, up to 99%, along with nitrogen or another inert gas as the remainder of the gas mixture will enhance oil production.
SUMMARY OF THE INVENTION
The present invention provides for a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil s a gas mixture comprising at least 50% by volume of carbon dioxide and an inert gas. The present invention further provides for a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil a gas mixture comprising carbon dioxide and nitrogen wherein the carbon dioxide is present in the gas mixture in an amount of at least 50% by to volume. In addition, the present invention will provide for a method for lowering the viscosity and surface tension as well as increasing the volume or swelling of the oil in an underground formation comprising injecting into the oil a gas mixture comprising at least 50% by volume carbon dioxide and an inert gas.
is BRIEF DESCRIPTION OF THE DRAWINGS
Fig. 1 is a graphical representation of the effect of carbon dioxide content of gas on paraffin oil viscosity.
Fig. 2 is a graphical representation of carbon dioxide content of gas on naphthene oil viscosity.
Fig. 3 is a graphical representation of carbon dioxide content of gas on 2s aromatic oil viscosity.
Fig. 4 is a graphical representation of carbon dioxide content of gas on paraffin oil surface tension.
Fig. 5 is a graphical representation of carbon dioxide content of gas on naphthene oil surface tension.
Fig. 6 is a graphical representation of carbon dioxide content of gas on aromatic oil surface tension.
Fig. 7 is a graphical representation of carbon dioxide content of gas on paraffin oil viscosity at various temperatures.
io Fig. 8 is a graphical representation of carbon dioxide content of gas on paraffin oil surface tension at various temperatures.
Fig. 9 is a graphical representation of carbon dioxide content of gas on paraffin oil volume at various temperatures.
is DETAILED DESCRIPTION OF THE INVENTION
The present invention comprises a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil a gas 2o mixture comprising at least 50% by volume carbon dioxide and an inert gas.
The inert gas is preferably nitrogen. Other inert gases such as helium and argon may also be employed. The present invention also comprises a method for enhancing the recovery of oil from an underground formation comprising injecting into the oil a gas mixture which comprises carbon dioxide 2s and nitrogen. The carbon dioxide is present in the gas mixture in an amount of at least 50% by volume. 'The introduction of a combination of carbon dioxide and nitrogen gas to the formation provides an unexpected advantage of lower oil viscosity and surface tension than the introduction of carbon dioxide or nitrogen alone. This will also provide greater oil swelling than the use of carbon dioxide or nitrogen alone. The use of nitrogen adds an economic advantage to the mixture as there is lower cost than that for pure carbon dioxide consumption.
For purposes of the present invention, Applicants define oil as being a hydrocarbon which comprises paraffin, aromatic or naphthene constituents or mixtures thereof.
The mixture of the carbon dioxide and nitrogen will be injected into the io formation containing the oil at a pressure of 100 pounds per square inch to 20,000 pounds per square inch depending upon the depth of the oil reservoir.
This injection method allows for use of WAG (water alternating gas) well-to-well process whereby an injection of gas is followed by a waterflood to drive the oil and enhance production at the well head. This injection method will is also work in a huff and puff process. In the huff and puff process, the mixture would be injected into the formation. The formation would then be sealed allowing a soak period of determinate length of time, followed by an improved oil recovery or production period.
2o The mixtures of carbon dioxide and nitrogen may be created by any means. Preferably, a carbon dioxide-rich stream and a nitrogen-rich stream are combined or a hydrocarbon is combusted using air or oxygen-enriched air to produce the carbon dioxide. The present inventors assert that in addition to nitrogen, other inert gases, when combined with carbon dioxide in an 2s optimum ratio, will minimize oil viscosity and surface tension while increasing swelling.
One means for producing the carbon dioxide-rich gas stream involves the use of a power plant or co-generation plant at or near the well site.
Oxygen-enriched air and hydrocarbon are combusted to generate power and carbon dioxide-rich gas. The power is used to operate an air separation plant which provides the oxygen for the oxygen enrichment of the power or co-generation plant. Additional nitrogen and/or steam produced may also be used to enhance oil recovery by placing these materials in an injection well either individually or in combination with the carbon dioxide-rich gas stream.
The combination of heat and carbon dioxide can further improve recovery and little carbon dioxide would be lost to the aqueous phase as a result.
io Another means for producing the carbon dioxide is by injection of pure oxygen, oxygen-enriched air or air downhole. For wells that are sufficiently deep enough, the temperature will be sufficient to sustain combustion and produce carbon dioxide. For example, a 8000 foot deep well may have a temperature of 300°F which is hot enough to produce the carbon dioxide is necessary for the enhanced oil recovery.
In a preferred embodiment of the present invention, a carbon dioxide nitrogen mixture with carbon dioxide present greater than 50% by volume is injected into the formation at or near the production well by optimizing the 2o composition of the gas mixture. Due to the varied rates in the uptake of carbon dioxide and nitrogen, a near optimum composition can be maintained in the formation at that injection location. A second mixture of carbon dioxide and nitrogen would then be injected through injection wells) located at a distance from the production well. The composition of this gas mixture would 2s be such that the viscosity and surface tension of the oil is higher than that of the oil near or at the production well but still reduced in comparison to the untreated oil. Gas may be fed continuously to the injection wells) or the wells) can be shut for a period of at least a day to facilitate the uptake of the gas by the oil.
Oil is driven to the production well and fingering or bypass of the gas though the oil is minimized as a result. In this preferred embodiment, more than one remote injection point may be employed such that the viscosity and s surface tension of the oil at the remote injection point becomes higher with each injection point further away from the well head injection point by optimizing the content of the carbon dioxide and nitrogen gas mixture.
Accordingly, the nitrogen content of the gas mixture will increase as one injects the mixture further from the production well. This gradient will result in io a raising of carbon dioxide content above the 50% by volume as one injects at points getting sequentially closer to the production well. In this embodiment, a later possibly intermittent use of carbon dioxide flood, nitrogen flood or water flood to drive the oil to the production well would further improve yields.
is A preferred composition for use in the methods of the present invention is that of at least 50% by volume carbon dioxide, the remainder being nitrogen or other inert gas including helium, argon or steam. In a more preferred embodiment, greater than 60% carbon dioxide by volume with the 2o remainder being inert gases would comprise the gaseous mixture. In the most preferred embodiment, greater than 75% by volume of the gas mixture would be carbon dioxide and the remainder being inert gases.
In an additional embodiment, hydrocarbons can be added to the above 2s described compositions. These hydrocarbons, such as methane, ethane and propane can come from traditional sources but may also come from the associated gas produced during oil production. The hydrocarbons can be separated from oil and reinjected into the ground or may be separated from oil and reinjected into the ground after burning a portion of the hydrocarbon in air, oxygen or oxygen enriched air.
s EXAMPLES
Three model oils were studied to explore the potential of mixtures of carbon dioxide and nitrogen for enhanced oil recovery. A simulation was developed based on the Peng-Robinson equation of state for vapor-liquid io equilibrium, the Twu model for liquid phase viscosity and a modified form of the Brock and Bird equation for surface tension. The three oils employed in this study were of paraffin, naphthene and aromatic types. A gas mixture of carbon dioxide and nitrogen with a usage rate of 1 mole per mole of oil was presumed and a small quantity of water was added to the mixture since is typically carbon dioxide flooding operations follow water flood procedures or are conducted as in the WAG method alternatively with waterflood. The quantity of water was based on 20% saturation for a typical oil. Pressures in the range of 1,500 psia to 2,500 psia and temperatures in the range of 75°F
to 200°F were studied.
As shown in Figs. 1, 2 and 3, and Tables 1, 2 and 3, the relationship of a paraffin, naphthene and aromatic oil viscosity at 75°F to the percentage of carbon dioxide in the oil recovery gas mixture is demonstrated. It can be seen that greater than 50% carbon dioxide in the gas mixture is 2s advantageous in lowering the oil viscosity relative to the use of 100%
carbon dioxide.
Table 1. Effect of C02 Content of Gas on Paraffin Oil Viscosity at Various Pressures and 75 F
C02 Oil Oil Oil content viscosityviscosityviscosity of at at at gas 1500 psia2000 2500 psia (%) (cP) psia (cP) (cP) 0 0.592 0.571 0.552 25 0.557 0.534 0.513 50 0.515 0.49 0.468 68 0.478 0.453 0.437 75 0.462 0.443 0.449 80 0.45 1J.451 0.457 85 0.451 0.46 0.466 88 0.456 0.465 0.472 92 0.464 0.472 0.479 100 0.478 IJ.487 0.493 Table 2. Effect of C02 Content of Gas on Naphthene Oil Viscosity at Various Pressures and 75 F
C02 Oil Oil Oil content viscosityviscosityviscosity of at at at gas 1500 psia2000 psia2500 (%) (cP) (cP) psia (cP) 0 1.93 1.87 1.82 25 1.69 1.62 1.57 50 1.44 1.38 1.32 68 1.26 1.19 1.14 75 1.18 1.12 1.07 80 1.12 1.06 1.02 85 1.06 1.01 0.997 88 1.02 U.993 1.01 92 0.986 1.01 1.02 100 1.02 1.04 1.05 Table 3. Effect of C02 Content of Gas on Aromatic Oil Viscosity at Various Pressures and 75 F
C02 Oil Oil Oil content viscosityviscosityviscosity of at at at gas 1500 psia2000 2500 psia (%) (cP) psia (cP) (cP) 0 0.827 0.811 0.797 25 0.7566 0.738 0.722 50 0.679 0.658 0.642 68 0.615 0.595 0.578 75 0.587 0.567 0.552 80 0.566 6.547 0.532 85 0.544 0.526 0.512 88 0.529 0.512 0.519 92 0.51 0.52 0.527 100 0.527 0.537 0.544 Figs. 4, 5 and 6 and Tables 4, 5 and 6 show the relationship of a to paraffin, naphthene and aromatic oil surface tension at 75°F to the percentage carbon dioxide and the oil recovery gas mixture for three different pressures. As can be seen in Figs. 4, 5 and 6, greater than 60% carbon dioxide in the gas mixture is advantageous in reducing surface tension in comparison to the use of pure carbon dioxide.
Table 4. Effect of C02 Content of Gas on Paraffin Oil Surface Tension at Various Pressures and 75 F' C02 Oil surfaceOil surfaceOil surface content tension tension tension of at at at gas 1500 2000 psia2500 psia (%) psia (dyne/cm)(dyne/cm) (dyne/cm) 0 19.22 18.39 17.65 25 17.1 16.19 15.41 50 14.93 13.99 13.21 68 13.27 12.35 11.8 75 12.59 11.86 11.86 80 12.09 11.91 11.9 85 11.96 11.95 11.95 88 11.98 11.98 11.98 92 12.02 12.02 12.02 100 12.09 12.1 12.1 Table 5. Effect of C02 Content of Gas on Naphthene Oil Surface Tension at Various Pressures and 75 F
C02 Oil surfaceOil surfaceOil surface content tension tension tension of at at at gas 1500 2000 psia2500 psia (%) psia (dyne/cm)(dynelcm) (d ne/cm) 0 29.21 28.56 27.96 25 26.14 25.3 24.59 50 22.93 21.97 21.23 68 20.4 19.44 18.73 75 19.34 18.42 17.72 80 18.53 17.64 16.97 85 17.69 16.85 16.59 88 17.16 16.61 16.62 92 16.65 16.86 16.66 100 16.72 16.73 16.73 Table 6. Effect of C02 Content of Gas on Aromatic Oil Surface Tension at Various Pressures and 75 F
C02 Oil surfaceOil surfaceOil surface content tension tension tension of at at at gas 1500 psia2000 psia2500 psia (%) (dyne/cm)(d ne/cm)(dyne/cm) 0 29.84 29.29 28.79 25 26.71 25.96 25.33 50 23.41 22.53 21.87 68 20.81 19.94 19.28 75 19.73 18.87 18.25 80 18.92 18.08 17.48 85 18.06 17.28 16.72 88 17.52 16.77 16.76 92 16.8 16.8 16.8 100 16.86 16.86 16.86 Figs. 7 and 8 and Tables 7 and 8 show the relationship of a paraffin oil viscosity and surface tension at various temperatures to the percentage carbon dioxide and the oil recovery gas mixture. As demonstrated in the earlier examples, greater than 50% carbon dioxide in the gas mixture is advantageous in comparison to the use of pure carbon dioxide. Oil viscosity to is greatly reduced at around 70 to 80% carbon dioxide while surface tension remains approximately constant at the higher carbon dioxide concentrations.
Table 7. Effect of C02 Content of Gas on Paraffin Oil Viscosity at Various Temperatures and 2000 psia C02 Oil Oil Oil Oil Oil contentviscosityviscosityviscosityviscosityviscosity of gas at 75 at 100 at 125 at 150 at 200 (%) F F F F F
(cP) (cP) (cP) (cP) (cP) 0 0.571 0.486 0.419 0.365 0.282 50 0.49 0.429 0.375 0.329 0.257 75 0.443 0.387 0.341 0.301 0.235 80 0.451 0.394 0.342 0.298 0.229 85 0.46 0.402 0.348 0.304 0.23 88 0.465 0.407 0.352 0.307 0.233 92 0.472 0.413 0.358 0.312 0.237 100 0.487 0.426 0.369 0.321 0.244 s Table 8. Effect of C02 Content of Gas on Paraffin Oil Surface Tension at Various Temperatures and 2000 psia C02 Oil Oil Oil Oil Oil contentsurfacesurfacesurfacesurfacesurface of gas tensiontensiontensiontensiontension (%) at 75 at 100 at 125 at 150 at 200 F F F F F
(dyne/cm)(dyne/cm)(dyne/cm)(dyne/cm)(dyne/cm) 0 18.39 17.3 16.21 15.13 13 50 13.99 12.91 12.29 11.63 10.26 75 11.86 10.53 10.06 9.582 8.574 80 11.91 10.52 9.887 9.265 8.167 85 11.95 10.52 9.888 9.266 8.044 88 11.98 10.52 9.887 9.266 8.046 92 12.02 10.52 9.888 9.266 8.044 100 12.1 10.52 9.887 9.265 8.045 Fig. 9 and Table 9 show the relationship of a paraffin oil relative to volume at various temperatures as to the percentage carbon dioxide in the oil recovery gas mixture. The relative volume is taken in comparison to a standard oil volume. Roughly 70% to 99% carbon dioxide in the gas mixture is advantageous in comparison to the use of pure carbon dioxide to maximize swelling in this case. As swelling of the oil increases, the oil will exit small is pores within the subterranean formation and can be swept or driven to the production well by use of the various flood techniques.
Table 9. Effect of C02 Content of Gas on Paraffin Oil Relative Volume at Various Temperatures and 2000 psia*
C02 Oil Oil Oil Oil Oil contentrelativerelativerelativerelativerelative of gas volume volume volume volume volume (%) at 75 at 100 at 125 at 150 at 200 F F F F F
0 1.036 1.053 1.071 1.090 1.131 50 1.118 1.135 1.154 1.176 1.235 75 1.193 1.222 1.244 1.27 1.353 80 1.188 1.217 1.249 1.287 1.392 85 1.183 1.211 1.243 1.280 1.398 88 1.179 1.207 1.239 1.276 1.391 92 1.175 1.203 1.234 1.271 1.383 100 1.167 1.194 1.224. 1.261 1.366 ~ I
*Relative volume is in comparison to a standard oil volume io While this invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modifications of the invention will be obvious to those skilled in the art.
The appended claims of this invention generally should be construed to cover all is such obvious forms and modifications which are within the true spirit and scope of the present invention.
Claims (37)
1. A method for enhancing the recovery of oil from an underground formation comprising injecting into said oil a gas mixture comprising at least 50% by volume carbon dioxide.
2. The method as claimed in claim 1 wherein the remainder of said gas mixture is selected from the group consisting of an inert gas, mixtures of inert gases, hydrocarbons, steam, air or mixtures of these.
3. The method as claimed in claim 2 wherein said inert gas is selected from the group consisting of nitrogen, helium and argon.
4. The method as claimed in claim 1 wherein said gas mixture comprises greater than 60% by volume carbon dioxide.
5. The method as claimed in claim 1 wherein said gas mixture comprises greater than 70% carbon dioxide by volume.
6. The method as claimed in claim 1 wherein said gas mixture is injected into said oil at the well head.
7. The method as claimed in claim 1 wherein said gas mixture is injected into a single production well head.
8. The method as claimed in claim 7 wherein said injection is cyclical.
9. The method as claimed in claim 7 wherein said gas mixture is injected into an injection well different from said production well head.
10. The method as claimed in claim 9 wherein said gas mixture is injected in an alternating pattern with a driving fluid.
11. The method as claimed in claim 10 wherein said driving fluid is selected from the group consisting of steam, water, nitrogen, carbon dioxide and air.
12. The method as claimed in claim 9 wherein there are a plurality of different injection wells.
13. The method as claimed in claim 1 wherein said gas mixture is injected into said oil at a pressure ranging from about 100 psi to about 20,000 psi.
14. The method as claimed in claim 1 wherein said carbon dioxide is obtained from a power plant or co-generation plant or from in situ combustion through the injection of air, oxygen enriched air, or pure oxygen.
15. The method as claimed in claim 1 wherein said nitrogen is obtained from an air separation plant.
16. The method as claimed in claim 1 wherein after injection of said gas mixture said underground formation is sealed for at least one day.
17. The method as claimed in claim 16 wherein said sealed underground formation is opened and a flood of a material selected from the
18 group consisting of carbon dioxide, nitrogen, water or brine is driven through said injection point.
18. A method for enhancing the recovery of oil from an underground formation comprising injecting info said oil a gas mixture comprising carbon dioxide and nitrogen wherein said carbon dioxide is present in said gas mixture in an amount of at least 50% by volume.
18. A method for enhancing the recovery of oil from an underground formation comprising injecting info said oil a gas mixture comprising carbon dioxide and nitrogen wherein said carbon dioxide is present in said gas mixture in an amount of at least 50% by volume.
19. The method as claimed in claim 18 wherein said carbon dioxide is present in said gas mixture in an amount greater than 60% by volume.
20. The method as claimed in claim 18 wherein said carbon dioxide is present in said gas mixture in an amount greater than 70% by volume.
21. The method as claimed in claim 18 wherein said carbon dioxide is present in said gas mixture in an amount greater than 50% by volume and less than 99% by volume.
22. The method as claimed in claim 18 wherein said gas mixture is injected into said formation at a pressure of about 100 psi to about 20,000 psi.
23. The method as claimed in claim 18 wherein steam is additionally injected into said underground formation.
24. A method for enhancing the recovery of oil from an underground formation having at least one production well comprising injecting into said underground formation in at least two distinct injection points a gas mixture comprising carbon dioxide and nitrogen wherein said carbon dioxide is present in said gas mixture in an amount of at least 50% by volume at the first injection point and further wherein the volume percentage of nitrogen in said mixture is higher at said second injection point than said first injection point, and said first injection point is closer to said at least one production well than said second injection point.
25. The method as claimed in claim 24 wherein the volume percentage of nitrogen in said gas mixture increases at each injection point further from said production well.
26. The method as claimed in claim 24 wherein the viscosity and surface tension of said oil at said second injection point is higher than the surface tension and viscosity at said first injection point.
27. The method as claimed in claim 24 wherein said underground formation is sealed for at least one day.
28. The method as claimed in claim 27 wherein said underground formation is opened and flooded with a material selected from the group consisting of carbon dioxide, nitrogen, water and brine to improve oil recovery.
29. A method for lowering the viscosity and surface tension of oil in an underground formation comprising injecting the said oil a gas mixture comprising at least 50% by volume carbon dioxide.
30. The method as claimed in claim 29 wherein the remainder of said gas mixture is selected from the group consisting of an inert gas, mixtures of inert gases, hydrocarbons, steam, air or mixtures of these.
31. The method as claimed in claim 29 wherein said inert gas is selected from the group consisting of nitrogen, helium and argon.
32. The method as claimed in claim 29 wherein said gas mixture comprises at least 60% by volume carbon dioxide.
33. The method as claimed in claim 29 wherein said carbon dioxide comprises at least 70% by volume of said gas mixture.
34. The method as claimed in claim 29 wherein said gas mixture comprises about 50% to about 99% by volume carbon dioxide and about 1 to about 49% nitrogen by volume.
35. The method as claimed in claim 29 wherein said gas mixture is injected into said underground formation at a pressure of about 100 psi to about 20,000 psi.
36. The method as claimed in claim 29 wherein said hydrocarbons are derived from associated gas produced during the production of oil.
37. The method as claimed in claim 29 wherein said hydrocarbons are present in said mixture in an amount ranging from about 1 % to about 50%.
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|---|---|---|---|
| US09/858,363 | 2001-05-16 | ||
| US09/858,363 US20030037928A1 (en) | 2001-05-16 | 2001-05-16 | Enhanced oil recovery |
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| EP (1) | EP1258595A3 (en) |
| CN (1) | CN1385595A (en) |
| AU (1) | AU4058402A (en) |
| CA (1) | CA2384612A1 (en) |
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| US7493952B2 (en) * | 2004-06-07 | 2009-02-24 | Archon Technologies Ltd. | Oilfield enhanced in situ combustion process |
| GB2417739B (en) * | 2004-09-01 | 2006-07-26 | Statoil Asa | Method |
| US7506685B2 (en) * | 2006-03-29 | 2009-03-24 | Pioneer Energy, Inc. | Apparatus and method for extracting petroleum from underground sites using reformed gases |
| US9605522B2 (en) * | 2006-03-29 | 2017-03-28 | Pioneer Energy, Inc. | Apparatus and method for extracting petroleum from underground sites using reformed gases |
| WO2008097666A1 (en) * | 2007-02-10 | 2008-08-14 | Vast Power Portfolio, Llc | Hot fluid recovery of heavy oil with steam and carbon dioxide |
| CN201031676Y (en) * | 2007-03-30 | 2008-03-05 | 辽河石油勘探局 | Boiler flue gas pressurization absorption CO2 gaseous state pouring well oil production device |
| US8616294B2 (en) | 2007-05-20 | 2013-12-31 | Pioneer Energy, Inc. | Systems and methods for generating in-situ carbon dioxide driver gas for use in enhanced oil recovery |
| US7650939B2 (en) * | 2007-05-20 | 2010-01-26 | Pioneer Energy, Inc. | Portable and modular system for extracting petroleum and generating power |
| CN101126312B (en) * | 2007-08-17 | 2013-01-23 | 中国科学院武汉岩土力学研究所 | Fluctuation petroleum exploitation method |
| US20090140444A1 (en) * | 2007-11-29 | 2009-06-04 | Total Separation Solutions, Llc | Compressed gas system useful for producing light weight drilling fluids |
| US8450536B2 (en) * | 2008-07-17 | 2013-05-28 | Pioneer Energy, Inc. | Methods of higher alcohol synthesis |
| US7937948B2 (en) * | 2009-09-23 | 2011-05-10 | Pioneer Energy, Inc. | Systems and methods for generating electricity from carbonaceous material with substantially no carbon dioxide emissions |
| CN101718192B (en) * | 2009-12-04 | 2012-07-18 | 北京高新利华催化材料制造有限公司 | Method for carrying out tertiary oil production on oil field |
| MX341392B (en) | 2010-06-04 | 2016-08-18 | Dow Global Tech Llc * | Oil recovery. |
| NO337537B1 (en) * | 2010-09-29 | 2016-05-02 | Statoil Petroleum As | Methods for introducing carbon dioxide (CO2) into underground geological formations for permanent storage therein. |
| US20130206403A1 (en) * | 2011-08-09 | 2013-08-15 | Stevan Jovanovic | Enhanced oil recovery process |
| DE102011110213A1 (en) | 2011-08-16 | 2013-02-21 | Thyssenkrupp Uhde Gmbh | Method and device for recirculating exhaust gas from a gas turbine with subsequent waste heat boiler |
| CN102392623B (en) * | 2011-10-31 | 2014-07-23 | 中国石油天然气股份有限公司 | Air-drive oil production method for low-permeability reservoir |
| CN102606117B (en) * | 2012-04-05 | 2014-11-05 | 中国石油天然气股份有限公司 | Air and nitrogen alternating displacement exploitation method for mid-deep zone low-permeability thin oil reservoir |
| US9586827B2 (en) | 2013-09-06 | 2017-03-07 | David LeRoy Hagen | CO2 producing calciner |
| CN104632158B (en) * | 2013-11-13 | 2017-02-08 | 中国石油化工股份有限公司 | Oil well response stage dividing and distinguishing method under carbon dioxide miscible displacement condition |
| US10519757B2 (en) | 2016-02-09 | 2019-12-31 | Frank Thomas Graff, JR. | Multi-directional enhanced oil recovery (MEOR) method |
| US10066469B2 (en) | 2016-02-09 | 2018-09-04 | Frank Thomas Graff | Multi-directional enhanced oil recovery (MEOR) method |
| WO2017201020A1 (en) | 2016-05-17 | 2017-11-23 | Nano Gas Technologies, Inc. | Downhole separation |
| US11193359B1 (en) | 2017-09-12 | 2021-12-07 | NanoGas Technologies Inc. | Treatment of subterranean formations |
| PL3986596T3 (en) | 2019-08-23 | 2024-01-29 | John W. SCHULTES | Method and a direct reduction plant for producing direct reduced iron |
| CN114427392A (en) * | 2020-09-29 | 2022-05-03 | 中国石油化工股份有限公司 | Method for exploiting heavy oil reservoir |
| US20230112608A1 (en) | 2021-10-13 | 2023-04-13 | Disruptive Oil And Gas Technologies Corp | Nanobubble dispersions generated in electrochemically activated solutions |
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| US2623596A (en) * | 1950-05-16 | 1952-12-30 | Atlantic Refining Co | Method for producing oil by means of carbon dioxide |
| US3084743A (en) * | 1958-09-16 | 1963-04-09 | Jersey Prod Res Co | Secondary recovery of petroleum |
| US3295601A (en) * | 1964-03-20 | 1967-01-03 | Phillips Petroleum Co | Transition zone formation in oil production |
| US4736792A (en) * | 1986-12-30 | 1988-04-12 | Texaco Inc. | Viscous oil recovery method |
| US5046561A (en) * | 1990-03-12 | 1991-09-10 | Texaco Inc. | Application of multiphase generation process in a CO2 flood for high temperature reservoirs |
| US5285848A (en) * | 1992-11-16 | 1994-02-15 | Atlantic Richfield Company | Method for improving the recovery of oil from a subterranean formation by solvent concentration grading |
| US5725054A (en) | 1995-08-22 | 1998-03-10 | Board Of Supervisors Of Louisiana State University And Agricultural & Mechanical College | Enhancement of residual oil recovery using a mixture of nitrogen or methane diluted with carbon dioxide in a single-well injection process |
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2001
- 2001-05-16 US US09/858,363 patent/US20030037928A1/en not_active Abandoned
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| US20030037928A1 (en) | 2003-02-27 |
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| CN1385595A (en) | 2002-12-18 |
| EP1258595A3 (en) | 2004-03-03 |
| AU4058402A (en) | 2002-11-21 |
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