|Publication number||US2917296 A|
|Publication date||Dec 15, 1959|
|Filing date||Mar 8, 1957|
|Priority date||Mar 8, 1957|
|Publication number||US 2917296 A, US 2917296A, US-A-2917296, US2917296 A, US2917296A|
|Inventors||Prentiss Spencer S|
|Original Assignee||Phillips Petroleum Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (9), Referenced by (14), Classifications (7)|
|External Links: USPTO, USPTO Assignment, Espacenet|
Dec. 15, 1959 s. S.'PRENTISS 2,917,296 RECOVERY OF HYDROCARBONFROM OIL SHALE ADJOINING A PERMEABLE-OIL-BEARING STRATUM Filed March a, 1957 RMEABL ION OlL-BEARXNG ONE FORMATION INVENTOR. 5.5. PRENTISS A 7"TOR/VEYS conventional methods.
"ing or; drilling operations. the oil shale for retorting of the shale in furnaces outside United States Patent RECOVERY OF HYDROCARBON FROM OIL SHALE ADJOINING A PERMEABLE OIL- BEARING STRATUM Spencer S. Prentiss, Bartlesville, Okla, assignor to Phillips Petroleum Company, a corporation of Delaware Application March 8, 1957, Serial No. 644,764
2 Claims. (Cl. 262-3) This invention relates .to a process for recovering hydrocarbons from an underground formation including an oil shale stratum lying adjacent a permeable or porous oil-bearing formation.
Large deposits of oil in the form of oil shale are found in various sections of the United States and, particularly, in Colorado and surrounding States. Various methods of recovery of oil from these shale deposits .have been proposed and the principal-difficulty with these methods is the high cost which renders the recovered oil too expensive to compete with petroleum crudes recovered by more The in situ retorting of oil shale 'to recover'the oil contained therein is made diflicult because of the 'nonpermeable nature of the oil shale and the 'difiiculty of applying heat thereto without extensive min- The mining and removal of the formation -is commercially uneconomical in most cases.
Accordingly, it is an object of the invention to provide a process for recovery of hydrocarbon from an oil shale stratum lying adjacent a permeable or oil-bearing stratum. Another object is to provide a process for in situ retorting of oil shale utilizing the heat of combustion of oil in an adjacent permeable stratum as the heat for the retorting step. A further object of the invention is to provide an economical and efiicient process for recovery of hydrocarbon from oil shale deposits. Other objects of the invention will become apparent from a consideration of the accompanying disclosure.
The broadest aspect of the invention comprises establishing and maintaining a combustion zone in an oilbearing porous or permeable stratum lying adjacent an oil-bearing shale so as to retort the shale and distill valuable hydrocarbon therefrom by means of the heat of combustion of hydrocarbon in the permeable stratum thru heat transfer from the permeable hot stratum to the adjacent shale. In one embodiment of the invention, the shale stratum is fractured in a generally horizontal plane parallel with the permeable oil-bearing stratum and is propped by conventional means so as to maintain the resulting fractures 111 an open position. This facilitates retorting and recovery of hydrocarbons from the shale thru perforations in the casing of the borehole thru which the combustion is established. It is also feasible to fracture the permeable oil-bearing stratum at one or more levels so as to facilitate the in situ combustion in this formation as well as recovery of oil therefrom.
A more complete understanding of the invention may be had from a consideration of the accompanying schematic drawing of which Figure l is an elevation, partially in section, of an underground formation in which the invention is applicable and Figure 2 is a plan view of a S-spot well pattern suitable for oil recovery from the formation shown in Figure 1.
Referring to Figure l, oil-bearing shale formations or strata 8 and 9 overlay and underlie permeable and porous oil-bearing stratum or formation 10. Numeral 11 desig- 'nates fractures formed in the various strata. The strata are penetrated by boreholes l2 and 14 which are usually protected by casing 15. A tubing 16 in borehole 12 is provided with a burner 18 or with other suitable means of initiating combustion in the oil bearing formation surrounding the borehole. Well 14 is provided with tubing 29 which may be utilized for injecting air or for the recovery of fluid hydrocarbons or both during different phases of the process. Valved conduits 22 and 24 are connectedwith the well head (or with casing 15) to provide means for introducing and withdrawing fluids to and from the boreholes. Additional conduits 23 and 25 may also be used for the purpose of introducing and withdrawing fluids to and from the boreholes. Perforations 21 in the casings are made in conventional manner to facilitate injection and withdrawal of fluids to and from the producing strata.
In operation of the process utilizing the arrangement shown in Figure 1, combustion is initiated in the formation adjacent gas burner 18 in borehole 12 by burning a gas such as propane in said burner so as to bring the temperature of the formation up to combustion supporting temperature and injecting air into the heated area thru line 22 or 23 leading into borehole 12. Of course, other means may be utilized for establishing combustion in the permeable oil bearing formation around borehole 12. vThe temperature of the air may be elevated before injection so as to facilitate the heating of the formation as anaid in combustion, or cooled to control the temperature in the formation where such is necessary.
In formations which are not susceptible to plugging during direct injection of air andadvancing of the combustion front, this technique may be followed so as to drivethe combustion front to one or more surrounding wells 14. In most formations direct injection of air and advancement of the combustion front build up a wall of high viscosity hydrocarbon in front of the advancing combustion front and it is necessary to utilize inverse air injection thru Wells 14in order to avoid plugging of the permeable sand or stratum thru which the fluids must pass. If inverse air injection is to be utilized, a substantial combustion zone 26 is established and the injection of air is then transferred from borehole 12 to borehole 14 so as to advance the combustion front thru the formation toward the injection well countercurrently to the flow of air. At an intermediate stage of the process, the combustion front is in the vicinity of 28.
With continued inverse air injection, combustion zone 28 advances thru the permeable formation leaving a carbonized residue therein and arriving at the injection wells 14. With continued air injection thru wells 14, the combustion front is reversed in direction and moves back thru the formation to well 12 around which combustion was initiated, feeding on the carbon residue left in the formation during the inverse air injection phase.
During the movement of the combustion zone or front thru the permeable oil-bearing stratum between well 12 and Wells 14, high temperatures are developed which heat up the formation and because of the heat differential between the permeable formation and the adjacent shale formations a tremendous amount of heat is imparted to the latter so that oil or kerogen deposited in the shale is retorted and distilled therefrom into the adjacent permeable formation and also into the fractures in the shale so that produced fluids are driven thru the perforations 21 into casings 15 from which they are recovered in conventional manner as by pumping, application of vacuum, etc. As the kerogen is driven from the shale, the residual structure becomes porous and eventually the shale formation is rendered permeable from the 'original permeable stratum to the fractures in the shale,
which facilitates distillation and heat transfer by passage of hot gases thru the formation from the combustion area. The carbonized residue deposited in the shale structure is also susceptible to combustion and the combustion zone spreads from the permeable oil-bearing stratum into the now permeableshale structure so as to drive additional hydrocarbon material from the shale structure.
It is also feasible to utilize alternate direct and inverse air injection in moving the combustion zone or front thru the permeable oil-bearing stratum. This technique comprises driving the combustion zone by direct air injection until the permeability decreases appreciably then moving the front by inverse air injection so as to establish high permeability and then reestablishing direct air injection until permeability is again substantially decreased, etc.
Figure 2 shows the relative positions of wells 12 and 14 in a -spot well pattern and the position of combustion zone 28 at an intermeditate stage of the process.
In in situ combustion recovery of hydrocarbons in accordance with the invention,-the combustion supporting gas is usually air but air may be either increased or decreased in oxygen content, as by the mixing of combustion gas or oxygen therewith, Where conditions warrant. While Figure 1 shows a porous oil bearing formation sandwiched in between tWo impermeable shale strata, it is to be understood that the invention is also applicable to the production of shale oil from structures in which shale is both overlain and underlain by a porous oil bearing stratum. In this type of structure production of oil from the porous strata by in situ combustion transfers heat into the shale formation from both above and below.
Certain modifications of the invention will become apparent to those skilled in the art and the illustrative details disclosed are not to be construed as imposing unnecessary limitations on the invention.
1. A process for recovering fluid hydrocarbons from an oil-bearing impermeable shale and from an adjoining permeable oil-bearing stratum which comprises fracturing said shale horizontally in at least one level therein so that the resulting fractures connect with a production borehole therein; initiating combustion in said stratum around an ignition borehole therein and driving the re sulting combustion front thru said stratum to an injection borehole therein by inverse air injection thru said injection borehole whereby heat of combustion is passed directly into the adjoining shale and kerogen therein is fluidized and driven therefrom into said production borehole, rendering said shale permeable from said stratum to said fractures; as said combustion front reaches said injection borehole, continuing the injection of air thru said injection borehole so as to drive said front back thru said stratum, feeding on the carbon residue left by the first burn thru so as to further heat said shale and cause hot gases to pass thru the permeable shale into said fractures, thereby producing additional hydrocarbons therefrom; and recovering the produced hydrocarbons fro said shale and said stratum.
2. The process of claim 1 wherein the combustion zone is driven into the permeable shale, thereby producing additional hydrocarbons therefrom.
References Cited in the file of this patent UNITED STATES PATENTS 1,422,204 Hoover et al July 11, 1922 2,584,605 Merriam et al. Feb. 5, 1952 2,584,606 Merriam et al Feb. 5, 1952 2,596,845 Clark May 15, 1952 2,718,263 Hellman et al Sept. 20, 1955 I 2,734,579 Elkins Feb. 14, 1956 I 2,780,449 Fisher et a1 Feb. 5, 1957 2,793,696 Morse May 28, 1957 2,818,118 Dixon Dec. 31, 1957
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US1422204 *||Dec 19, 1919||Jul 11, 1922||Brown Thomas E||Method for working oil shales|
|US2584605 *||Apr 14, 1948||Feb 5, 1952||Frederick Squires||Thermal drive method for recovery of oil|
|US2584606 *||Jul 2, 1948||Feb 5, 1952||Frederick Squires||Thermal drive method for recovery of oil|
|US2596845 *||May 28, 1948||May 13, 1952||Stanolind Oil & Gas Co||Treatment of wells|
|US2718263 *||Feb 6, 1952||Sep 20, 1955||Exxon Research Engineering Co||Underground retorting for secondary oil recovery|
|US2734579 *||Jun 28, 1952||Feb 14, 1956||Production from bituminous sands|
|US2780449 *||Dec 26, 1952||Feb 5, 1957||Sinclair Oil & Gas Co||Thermal process for in-situ decomposition of oil shale|
|US2793696 *||Jul 22, 1954||May 28, 1957||Pan American Petroleum Corp||Oil recovery by underground combustion|
|US2818118 *||Dec 19, 1955||Dec 31, 1957||Phillips Petroleum Co||Production of oil by in situ combustion|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3024841 *||Jul 30, 1958||Mar 13, 1962||Jersey Prod Res Co||Method of oil recovery by in situ combustion|
|US3058730 *||Jun 3, 1960||Oct 16, 1962||Fmc Corp||Method of forming underground communication between boreholes|
|US3111986 *||Jun 29, 1960||Nov 26, 1963||Socony Mobil Oil Co Inc||Procedure of in-situ combustion for recovery of hydrocarbon material|
|US3115928 *||Aug 14, 1959||Dec 31, 1963||Pan American Petroleum Corp||Heavy oil recovery|
|US3116792 *||Jul 27, 1959||Jan 7, 1964||Phillips Petroleum Co||In situ combustion process|
|US3127935 *||Apr 8, 1960||Apr 7, 1964||Marathon Oil Co||In situ combustion for oil recovery in tar sands, oil shales and conventional petroleum reservoirs|
|US3205942 *||Feb 7, 1963||Sep 14, 1965||Socony Mobil Oil Co Inc||Method for recovery of hydrocarbons by in situ heating of oil shale|
|US3223158 *||Dec 10, 1962||Dec 14, 1965||Socony Mobil Oil Co Inc||In situ retorting of oil shale|
|US3292699 *||Aug 10, 1964||Dec 20, 1966||Mobil Oil Corp||Process for in situ retorting of oil shale|
|US3349849 *||Feb 5, 1965||Oct 31, 1967||Shell Oil Co||Thermoaugmentation of oil production from subterranean reservoirs|
|US3385362 *||Oct 26, 1966||May 28, 1968||Mobil Oil Corp||Thermal recovery of viscous oil with selectively spaced fractures|
|US4084640 *||Nov 4, 1976||Apr 18, 1978||Marathon Oil Company||Combined combustion for in-situ retorting of oil shales|
|US4192381 *||Nov 28, 1978||Mar 11, 1980||Occidental Oil Shale, Inc.||In situ retorting with high temperature oxygen supplying gas|
|US4444258 *||Nov 10, 1981||Apr 24, 1984||Nicholas Kalmar||In situ recovery of oil from oil shale|
|U.S. Classification||166/245, 166/259, 175/12|
|International Classification||E21B43/243, E21B43/16|