|Publication number||US3360044 A|
|Publication date||Dec 26, 1967|
|Filing date||Mar 5, 1964|
|Priority date||Mar 21, 1963|
|Also published as||DE1216817B|
|Publication number||US 3360044 A, US 3360044A, US-A-3360044, US3360044 A, US3360044A|
|Original Assignee||Deutsche Erdoel Ag|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (23), Classifications (7)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Dec. 26, 1967 LANGE 3,360,044
H. PROCESS AND APPARATUS FOR THE RECOVERY OF LIQUID BITUMEN FROM UNDERGROUND DEPOSITS Filed March 5, 1964 v Oxygen Q earner Gaseous or liquid bydramrb o/n' Sfeam sfeam generafor' Cambus fion ififeam chamber FIG. I
Com ressar P Liquid I 8 w bydroca rbans #0 be vaporized To borehole HeaIf-fpansf'er l/qu/d INVENTOR HANS. LA we:
BY ma avww ATTORNEYS United States Patent many Filed Mar. 5, 1964, Ser. No. 349,589 Claims priority, application Germany, Mar. 21, 1963,
L 4 11 Claims. (Cl. 166-11) The present invention relates to an improved process for the recovery of liquid bitumen from underground deposits, and to apparatus suitable therefor. More particularly it relates to the use of hot combustion gases in the recovery of liquid bitumen from underground deposits thereof, and to apparatus used therefor.
The term bitumen as used above and hereinafter throughout the specification and claims is intended to mean any number of inflammable mineral substances consisting mainly of hydrocarbon and including the oil petroleum and even the volatile naphthas.
Bitumen has previously been recovered from subterranean deposits by heating and otherwise treating the said deposits so that they could be recovered by pumping. This has customarily been done by introducing heated bitumen and water into the deposits so as to make the removal of the oil by pumping easier. The flow of the liquified bitumen, so as to permit rapid and complete recovery by pumping, is improved by changing the viscosity and the surface and/or interface tensions of the liquid bitumen. The water introduced into the deposit applies pressure to the liquid bitumen in the deposit. The decrease of the yield of a deposit always occurs at the bitumen-contact zone. Therefore, it is desirable in a bitumen field to set up a treatment zone in the vicinity of the bitumen-water contact zone where so-called test drillings are effected and test bores drilled through which the contents of the deposit are removed by bringing the bitumen to the surface in the form of a heated liquid, through a closed, heat-insulated pipe system. The liquid bitumen is heated after removal from the ground and additives mixed with it, and then returned under pressure into the deposit through the so-called treatment bores. These test-bores and treatment bores are so arranged with respect to each other that a direction of flow is set up perpendicular to the continuously progressing direction of the field, resulting from the water introduced into the deposit under pressure.
According to the present invention it has been found that by adding combustion gases to the deposit content, (bitumen and water) brought to the surface by test bores and by returning the deposit content as a heat transfer medium through the treatment bores the removal of the deposit from the ground is materially accelerated. It has been found that the addition of hot combustion gases is particularly effective.
It is well known that gases have previously been added to petroleum deposits for the purpose of increasing the pressures in the deposits and to facilitate the removal of additional petroleum. The method of introduction of the gas depends upon the particular structure in which the petroleum is found; when the gas is introduced into the upper part of the structure it serves to increase the pressure, but when injected deep into the structure it functions in a manner known as Gas Drive. An essential factor in the addition of the gas besides the purpose of increasing the pressure is in dissolving a portion of the gas in the oil inside the deposit so that viscosity is decreased and the forces affecting the adherence of the oil to the oil-bearing rocks are influenced by decreasing both the surface and interfacial-tensions.
When used as a pressure gas, products such as natural gas, air, flue gases etc., have previously been used. The natural gas from the deposit itself is not always available in sufiicient amounts, and the greater part thereof is methane which is not very soluble in the oil. Air has the disadvantage that the higher petroleum hydrocarbons become oxidized, which results in an increase in insolubility, thus resulting in an increase in viscosity and increases the viscosity difference toward the deposit water. Even in the case of flue gas the oxygen fraction is still undesirably high because the combustion in modern heating installations is carried out with 10-30% excess of air. The high nitrogen content is also a disadvantage since nitrogen is dissolved only to a small extent, its solubility in oil or water being only about as that of carbon dioxide. Gases which cannot be dissolved in the oil can be distributed in the latter in the form of tiny gas bubbles. which are liberated from the oil in the same general manner as when gases are subjected to an increase in yield resistance. This increase in the yield resistance through gas discharge is known as the Jamin effect.
In the present invention a combustion gas is employed whose CO components are enrichedso as to have a good solubility in bitumen and accordingly not only the viscosity of the bitumen is decreased, but also the surface and interface tensions thereof are advantageously changed. For such further enrichment with solubilityincreasing compounds, the combination of the combustion gas production with an enrichment with parafiinic C -C hydrocarbon vapors is suggested. In this Way a loaded combustion gas is obtained which contains largely carbon dioxide, water vapor and paraflinic C C- light hydrocarbons as solution enhancing components, and at the same time the nitrogen and oxygen, which have an unfavorable effect, are materially reduced in amount. Depending upon the kind and state of the deposit into which it is to be introduced, the composition of the loaded combustion gas and/or its ap lication may be varied so that the gas with high CO content has steam and light hydrocarbons added to it, or only steam alone. It can also be advantageous to feed the hydrocarbons into the deposit as liquids and then to introduce the combustion gas.
Hot combustion gases are added above the ground to the heat transfer medium, i.e. the bitumen or deposit water removed close to the bitumen-water-contact zone. The individual components of the hot combustion gases, such as carbon dioxide, Water vapor, nitrogen, hydrocarbon gas and/or vapor form a completely homogeneous mixture. The component ratios are adjusted'to the pressure and temperature of the heat transfer medium so that all of the components become completely dissolved therein. The water vapor contained in the gas as a combustion product releases its sensible and its latent heat of combustion to the heat transfer medium, dissolves, when in the liquid state, the carbon dioxide from the combustion gas and distributes in fine aqueous droplet form the dissolved carbon dioxide with the heat transfer medium in the bitumen deposit ahead of the moving bitumen-water-contact zone and facilitates, due to the influence of the carbon dioxide in changing the interfaceand surface-tensions, the release of the bitumen layer from the carrier medium, i.e. from the grains of sand of the deposit.
It is preferred to subdivide the loaded combustion gas mechanically into small gas bubbles, i.e. about 0.15 mm. in diameter, at the point where it is mixed with the heat transfer medium. After the condensation of the water vapor in the colder portions of the deposit water droplets of about 0.15 mm. diameter saturated with carbon dioxide are formed therefrom. These droplets are surbasis of these data, per unit of heat transfer medium, the composition of the combustion gas may vary between the tolerance limits set forth below:
rounded by liquefied hydrocarbons which also carry dissolved carbon dioxide. The water droplets, therefore, are surrounded by a protective film of carbon dioxide which penetrating deep into the deposit produce in the latter over a wide area changes in the surface-and interfacialtensions on both the bitumen and the water.
The combustion gas can, if preferred, be introduced into the deposit through drilled holes without having been previously mixed with the heat transfer medium.
An embodiment of the apparatus suitable for the generation of a combustion gas for use in the present invention is shown in the figures.
In the figures:
FIGURE 1 is a cross-section of the apparatus for producing modified and activated gases of combustion;
FIGURE 2 is a plan view of the distributor disk located in the apparatus of FIGURE 1; and
FIGURE 3 is a plan view of the rotating disk located in the apparatus of FIGURE 1.
In FIGURE 1, attached hereto and a part of the present disclosure, is shown a typical form oi apparatus for the generation of a loaded combustion gas mixed with the heat transfer medium suitable for use in the present invention. In this apparatus simultaneous mixing is effected with additional components with which the combustion gas will form a homogeneous mixture in the form of very small bubbles by distribution with heat transfer medium. The apparatus consists of a combustion chamber to which gaseous or liquid hydrocarbons are supplied through line 1 at pressures ranging from -20 atmospheres gauge. An oxygen carrier containing 80-95% oxygen is introduced through line 2. Combustion takes place in the burner 3. The combustion products formed in the burner contain a higher thermal energy than is either necessary or desirable for the next step of the process, i.e., the evaporation of the light hydrocarbons and the mixing thereof with the combustion gas. The combustion chamber 5 is accordingly surrounded by a steam generator 4 in which part of the thermal energy is transferred into high-pressure steam of 55-75 atmospheres gauge (56-76 absolute atmospheres) pressure at a temperature of 475- 525 C. The amount of the thermal energy that must be utilized in this manner depends upon the amount and composition of the light hydrocarbons to be evaporated. Water is supplied to the boiler through pipe and the steam formed is removed through conduit 19.
Paraffinic light hydrocarbons having 1 to 7 carbon atoms are introduced through conduit 7, containing liquid distributors 6, into the combustion chamber 5 where they are evaporated and homogeneously mixed with the gas, which at this point has a temperature which makes it possible to evaporate the C -C hydrocarbons at the existing pressure with no substantial degree of cracking. Should additional cooling be required in the evaporation zone, part of the heat transfer medium to be treated can be supplied through a pipe (not shown in the drawing) from the conduit 15.
By mixing with light hydrocarbons a loaded combustion gas is obtained having the composition shown in the table below. Depending upon the operating pressure and temperature, the kind of deposit being treated, and the weight ratio of the loaded combustion gas to be supplied on the It has been found that under such operating conditions the amount of nitrogen present is completely dissolved in the heat transfer medium.
The loaded combustion gas is compressed 'by the compressor 8 to a pressure of 40-75 atmospheres gauge into the mixing space 9. The heat transfer medium is fed into space 9 through conduit 15. The gas is dissolved therein and the heat transfer efiected. In order to bring both phases into intimate contact with each other, the stream of heat transfer medium is subdivided at the point of introduction into the mixing space by the action of the perforated disk 14, the combustion gas being introduced through the distributor disk 10, in which a number of holes 18 are arranged in lines and circles (as shown in the drawing), and ahead of which a winged cross 11 rotates and which is driven by the motor 13 through shaft 12. In this manner at one revolution e.g. 600 holes are covered at one time, causing the gas to be distributed in the heat transfer medium in the form of small bubbles. During this operation the heat transfer medium is heated to a temperature of 50125 C. higher than that at which it enters the chamber. If required, additional heating can be effected by adding to the mixture high pressure steam from the boiler 4 through the conduit 17. The heat transfer medium thus mixed with the loaded combustion gas and heated to a higher temperature is then passed through conduit 16 into treatment bore through which it passes into the deposit to be recovered.
The following specific example will illustrate the operation of the new process and apparatus disclosed in the drawings which are the subject of the present invention and furnish numerical values concerning the production, composition and use of combustion gases. It is understood, however, that the invention is not limited to the specific values shown in this example, which are for purposes of illustration only, and that variations known to one skilled in the art can be made within the limitations set forth herein and claimed in the appended claims.
EXAMPLE Combustion gas was produced by burning in the burner 3 of the steam boiler 5 of the drawing 700 m per hour of natural gas with an upper heating value of (H of 11150 Kcal. per normal cubic meter with 1740 rn. per hour of enriched oxygen carrier oxygen, 10% nitrogen) at 15 atmospheres gauge, thus obtaining 7.8 x 10 Kcal. heat per hour. Of this heat 10% was lost when being transformed, but 4.88 x 10 Koal. per hour were transferred into steam at 65 atmospheres gauge and 525 C. superheat. If the feed water enters the boiler from 20 at a temperature of 65 C. the steam may then be used to generate about 2150 kwh. of electricity per hour. The remaining amounts of heat (2.38 x 10 Kcal./h.) were employed to heat 42.0 long tons of liquid bitumen per hour to C. (including heat losses) arriving from 15. The heating of the liquid bitumen occurs by solution of the loaded combustion gas, which is low in nitrogen and oxygen, in liquid bitumen under a pressure of 65 atmospheres gauge. Because the combustion gases have been saturated with 950 kilograms of light hydrocarbons, delivered through 7, the combustion gas transports per hour (in kilograms) 1510 carbon dioxide, 1300 water, 5
oxygen, 176 nitrogen, 101 methane, 134 ethane, 115 propane, 128 butane, 134 pentane, 287 hexane and 51 heptane. In each cubic meter of heated liquid bitumen is dissolved the following (in kilograms), which are introduced into it through the bubble distributor, the combination of 13, 11, 10 and 14 of the drawings, 31.5 carbon dioxide, 27.7 water, 0.103 oxygen, 3.67 nitrogen and 19.8 hydrocarbons, 2.8 kg. of the carbon dioxide being in the 27.7 kg. of water droplets. Inside the deposit, after delivery via lid 16 and treatment bore holes when the pressures are higher than 65 atmospheres gauge, all of these materials are in solution without the formation of any gas bubbles.
As the water droplets from the condensed water vapor (steam) are free from any salt, the amount of sodium chloride in the saline deposit water of the oil will be lowered, and accordingly less sodium chloride will be present in the emulsified oil phase, so that on occasion it is possible to operate without a desalting operation. However, if the formation of the deposits contain clays which swell, then, on the contrary, it may actually become necessary to add salts and/or swelling agents to the water of the heat transfer medium.
What is claimed is:
1. Apparatus for the production of compositions for the recovery of liquid bitumens from subterranean deposits comprising a combustion chamber surrounded by a steam generator, in which chamber is located a burner, a conduit for the introduction of hydrocarbons under pressure to said burner, a second conduit for the introduction of enriched oxygen carriers to said burner, a mixing chamber adjacent to and connected to said combustion chamber, means for introducing light hydrocarbons into the combustion gases in the said mixing chamber, means for distributing said light hydrocarbons into said combustion gases, and means for withdrawing the mixture of combustion gases and light hydrocarbons from said mixing chamber.
2. A process for the recovery of liquid bitumen from subterranean bituminous deposits by treating said deposits through drill holes with fluid media which comprises introducing through said drill holes into said deposits a mixture of a heat transfer medium and heated combustion gases and removing liquid bitumen through adjacent drill holes, said heated combustion gases produced by the combustion of hydrocarbons with an oxygen carrier containing 80 to 95% O and the resulting modified gases of combustion being then mixed with said heat transfer medium comprising C -C hydrocarbons.
3. A process for the recovery of liquid bitumen from subterranean bituminous deposits by treating said deposits through drill holes with fluid media comprising burning hydrocarbons under increased pressure with an oxygen carrier containing 80 to 95% thereby producing a hot modified gas of combustion comprising mainly steam and CO delivering stratum contents through certain of said drill holes to above ground, mixing said modified gas of combustion with portions of said stratum contents under increased pressure whereby the temperature of said portions is raised 50 to 125 C. thereby forming a heat transfer medium for return to said deposits, and introducing through other of said drill holes said heat transfer medium under pressure and at a temperature whereby the treated section of said deposits contains only liquid contents.
4. The process of claim 3, wherein steam is introduced into the mixture of modified gas of combustion and stratum contents in such amounts that the temperature of said stratum contents is raised 50 to 125 C.
5. The process of claim 4, wherein said loaded modified gas of combustion has an average composition of approximately 37.16 to 79.62% by volume of water vapor, 21.02 to 34.15% by volume of CO 20.43 to 35.74% by volume of C -C hydrocarbons and 2.31 to 6.01% by volume N whereby said composition is present only in liquid form after being forced into said deposits.
6. In the process of claim 4 wherein said modified gas of combustion is produced in a combustion chamber surrounded by a steam generator and having a mixing chamber adjacent to and connected to said combustion chamber for mixing said modified gas of combustion,
said stratum contents, and said steam produced by said steam generator, and said heat transfer medium is forced into the stratum by means at the top of said drill holes for forcing said heat transfer medium.
7. The process of claim 3, wherein said loaded modified gas of combustion has an average composition of approximately 37.16 to 79.62% by volume of water vapor, 21.02 to 34.15 by volume of CO 20.43 to 35.74% by volume of C -C hydrocarbons and 2.31 to 6.01% by volume N whereby said composition is present only in liquid form after being forced into said deposits.
8. A process for the recovery of liquid bitumen from subterranean bituminous deposits by treating said deposits through drill holes with fluid media comprising burning hydrocarbons with an oxygen carrier containing to 0 thereby producing a hot modified gas of combustion, loading said hot modified gas of combustion with parafiinic C -C hydrocarbons, delivering stratum contents through certain said drill holes, mixing the loaded modified gas of combustion with portions of said stratum contents under increased pressure whereby the temperature of the fluid that is to be returned to said deposits is increased 50 to C. thereby forming a heat transfer medium and introducing through other of said drill holes said heat transfer medium under pressure and at a temperature whereby the heated section of said deposits contains only liquid contents.
9. The process of claim 8, wherein steam is introduced into the mixture of modified gas of combustion and stratum contents in such amounts that the temperature of said stratum contents is raised 50* to 125 C.
10. The process of claim 8, wherein said loaded modified gas of combustion has an average composition of approximately 37.16 to 79.62% by volume of water vapor, 21.02 to 34.15% by volume of CO 20.43 to 35.74% by volume of C -C hydrocarbons and 2.31 to 6.01% by volume N whereby said composition is present only in liquid form after being forced into said deposits.
11. An apparatus for the production of modified gas of combustion loaded with light hydrocarbons and thoroughly mixed with stratum contents from a bituminous deposit comprising a combustion chamber surrounded by a steam generator, said combustion chamber having a high pressure burner and separate conduits for hydrocarbons and oxygen enriched carrier, a mixing chamber adjacent to and connected to said combustion chamber, means for introducing light hydrocarbons into said mixing chamber to load modified gas of combustion with said light hydrocarbons, means connected to said mixing chamber for rigorously mixing and distributing loaded modified gas of combustion under pressure with portions of stratum contents which have been brought above ground, said means comprising a foraminous distributor disk having rows and circles of holes in combination with a bladed member in front of said disk, and conduits for delivering stratum contents and additional steam to said mixing means in combination with means for forcing heated stratum contents mixed with loaded modified gases of combustion through drill holes into the stratum.
References Cited UNITED STATES PATENTS 2,734,579 2/1956 Walter 166--11 2,839,141 6/1958 Walter 16640 X 2,875,832 3/1959' Martin et a1. 166--9 3,228,467 1/ 1966 Schlinger 1667 STEPHEN I. NOV OSAD, Primary Examiner.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2734579 *||Jun 28, 1952||Feb 14, 1956||Production from bituminous sands|
|US2839141 *||Jan 30, 1956||Jun 17, 1958||Worthington Corp||Method for oil recovery with "in situ" combustion|
|US2875832 *||Oct 23, 1952||Mar 3, 1959||Oil Recovery Corp||Gaseous hydrocarbon and carbon dioxide solutions in hydrocarbons|
|US3228467 *||Apr 30, 1963||Jan 11, 1966||Texaco Inc||Process for recovering hydrocarbons from an underground formation|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3405761 *||May 12, 1967||Oct 15, 1968||Phillips Petroleum Co||Steam flooding oil-bearing limestone strata|
|US3439743 *||Jul 13, 1967||Apr 22, 1969||Gulf Research Development Co||Miscible flooding process|
|US3456730 *||Aug 22, 1967||Jul 22, 1969||Deutsche Erdoel Ag||Process and apparatus for the production of bitumens from underground deposits having vertical burning front|
|US3473610 *||Aug 4, 1967||Oct 21, 1969||Deutsche Erdoel Ag||Process for obtaining bitumens from underground deposits|
|US3700035 *||Jun 4, 1970||Oct 24, 1972||Texaco Ag||Method for controllable in-situ combustion|
|US3768559 *||Jun 30, 1972||Oct 30, 1973||Texaco Inc||Oil recovery process utilizing superheated gaseous mixtures|
|US3809159 *||Oct 2, 1972||May 7, 1974||Continental Oil Co||Process for simultaneously increasing recovery and upgrading oil in a reservoir|
|US3948323 *||Jul 14, 1975||Apr 6, 1976||Carmel Energy, Inc.||Thermal injection process for recovery of heavy viscous petroleum|
|US4026357 *||Jun 26, 1974||May 31, 1977||Texaco Exploration Canada Ltd.||In situ gasification of solid hydrocarbon materials in a subterranean formation|
|US4033411 *||Jan 2, 1976||Jul 5, 1977||Goins John T||Method for stimulating the recovery of crude oil|
|US4099568 *||Dec 22, 1976||Jul 11, 1978||Texaco Inc.||Method for recovering viscous petroleum|
|US4127170 *||Sep 28, 1977||Nov 28, 1978||Texaco Exploration Canada Ltd.||Viscous oil recovery method|
|US4133384 *||Aug 22, 1977||Jan 9, 1979||Texaco Inc.||Steam flooding hydrocarbon recovery process|
|US4159743 *||Mar 13, 1978||Jul 3, 1979||World Energy Systems||Process and system for recovering hydrocarbons from underground formations|
|US4199024 *||Jan 18, 1979||Apr 22, 1980||World Energy Systems||Multistage gas generator|
|US4271905 *||Feb 21, 1979||Jun 9, 1981||Alberta Oil Sands Technology And Research Authority||Gaseous and solvent additives for steam injection for thermal recovery of bitumen from tar sands|
|US4325432 *||Apr 7, 1980||Apr 20, 1982||Henry John T||Method of oil recovery|
|US4385661 *||Jan 7, 1981||May 31, 1983||The United States Of America As Represented By The United States Department Of Energy||Downhole steam generator with improved preheating, combustion and protection features|
|US8602103 *||Nov 19, 2010||Dec 10, 2013||Conocophillips Company||Generation of fluid for hydrocarbon recovery|
|US20110120717 *||Nov 19, 2010||May 26, 2011||Conocophillips Company||Generation of fluid for hydrocarbon recovery|
|US20120227964 *||Sep 13, 2012||Conocophillips Company||Carbon dioxide gas mixture processing with steam assisted oil recovery|
|DE2808690A1 *||Mar 1, 1978||Sep 6, 1979||Messerschmitt Boelkow Blohm||Einrichtung zum erzeugen von heissen daempfen zur tertiaeren foerderung von erdoel|
|EP0039824A1 *||Apr 28, 1981||Nov 18, 1981||Zimpro-Aec, Ltd||A process for enhanced oil recovery by gas injection and apparatus for use therein|
|U.S. Classification||166/260, 166/90.1, 166/57|
|International Classification||E21B43/16, E21B43/24|