US2595979A - Underground liquefaction of coal - Google Patents
Underground liquefaction of coal Download PDFInfo
- Publication number
- US2595979A US2595979A US72582A US7258249A US2595979A US 2595979 A US2595979 A US 2595979A US 72582 A US72582 A US 72582A US 7258249 A US7258249 A US 7258249A US 2595979 A US2595979 A US 2595979A
- Authority
- US
- United States
- Prior art keywords
- coal
- hydrogen
- liquid
- underground
- hydrogenation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000003245 coal Substances 0.000 title claims description 88
- 238000000034 method Methods 0.000 claims description 32
- 239000001257 hydrogen Substances 0.000 claims description 25
- 229910052739 hydrogen Inorganic materials 0.000 claims description 25
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical class [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 22
- 239000003795 chemical substances by application Substances 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 20
- 238000011084 recovery Methods 0.000 claims description 14
- 239000000126 substance Substances 0.000 claims description 14
- 150000001875 compounds Chemical class 0.000 claims description 3
- 238000005984 hydrogenation reaction Methods 0.000 description 20
- 238000006243 chemical reaction Methods 0.000 description 18
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 229930195733 hydrocarbon Natural products 0.000 description 11
- 150000002430 hydrocarbons Chemical class 0.000 description 11
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- 239000002253 acid Substances 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 229910001868 water Inorganic materials 0.000 description 8
- 150000007513 acids Chemical class 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 5
- 239000012263 liquid product Substances 0.000 description 5
- 238000005065 mining Methods 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- NNBZCPXTIHJBJL-UHFFFAOYSA-N decalin Chemical compound C1CCCC2CCCCC21 NNBZCPXTIHJBJL-UHFFFAOYSA-N 0.000 description 4
- 238000005755 formation reaction Methods 0.000 description 4
- 239000000295 fuel oil Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N tetralin Chemical compound C1=CC=C2CCCCC2=C1 CXWXQJXEFPUFDZ-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 239000004927 clay Substances 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 238000011065 in-situ storage Methods 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 239000002802 bituminous coal Substances 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000012043 crude product Substances 0.000 description 2
- 238000005553 drilling Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 239000011630 iodine Substances 0.000 description 2
- 229910052740 iodine Inorganic materials 0.000 description 2
- OKJPEAGHQZHRQV-UHFFFAOYSA-N iodoform Chemical compound IC(I)I OKJPEAGHQZHRQV-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- BASDZFQDZBHCAV-UHFFFAOYSA-N 1,1,1-triiodoethane Chemical compound CC(I)(I)I BASDZFQDZBHCAV-UHFFFAOYSA-N 0.000 description 1
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 239000012223 aqueous fraction Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 150000001896 cresols Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 1
- 229910000043 hydrogen iodide Inorganic materials 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 1
- INQOMBQAUSQDDS-UHFFFAOYSA-N iodomethane Chemical compound IC INQOMBQAUSQDDS-UHFFFAOYSA-N 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000002790 naphthalenes Chemical class 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- PXXNTAGJWPJAGM-UHFFFAOYSA-N vertaline Natural products C1C2C=3C=C(OC)C(OC)=CC=3OC(C=C3)=CC=C3CCC(=O)OC1CC1N2CCCC1 PXXNTAGJWPJAGM-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/04—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
- C10G1/042—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction by the use of hydrogen-donor solvents
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/06—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/24—Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
-
- 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
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
Definitions
- This invention relatestoa process for the recovery of coal substance from. underground deposits in the formv of a liquid
- this invention relates tov the underground Iiquefaction oi. a liqueable fraction. of a coal deposit. by hydrogenation to produce a liquid extract suitable for use in the. production ofmotor fuels.
- coal in an underground deposit is hydrogen-ated in situ by contact with a. hydrogenating agent.
- the hydrogenation is carried out. at an elevated temperature and pressure, which may be controlled from above ground.
- The. hydrogenation reaction produces a liquid product which is readily recovered ⁇ as a relatively heavy oil.
- the crude liquid product may be subject to further hydrogenation and refining operations. to produce motor fuels and other desired products after recovery from the undergroundformation.
- the hydrogenating. agent used in the present process may be free hydrogen or an organic compound capable of liberating hydrogen.
- Hydroaromatics such as hydrogenated naphthalenes, e. g., tetralin and decalin, and heavy oils obtained by hydrogenation of ⁇ coal are suitable hydrogenating agents.
- Hydroaromatic oils act as solvents in the liquefaction of coal, due primarily to their ability to transfer hydrogen to the coal.
- av bituminous coal may be liqueed by hydrogenation, the extent of the liquefaction depending largely upon the grade of the coal. Approximately 65 per cent by weight of massive or lump coal may be readilyA liquefied' by hydrogenation.
- the hydrogen consumption' generally' ranges from about 1.5 to about 3 percent by weight based on the Weight of the coal reacted.
- the liqueed coal, or extract, obtained on hydrogenation is fluid and substantially free from ash.
- This liquid may be recovered from thefcoal seamY by the process of this invention in a manner analogous to the. production. of crude oil.
- the residual or unhydrogenated portion of the coal comprises unreacted carbon and the mineral matter or ash.
- the residue may also. be utilized advantageously as will be brought out hereinafter.
- the process of the present invention has many advantages over prior methodsof producing hydrocarbons from coal. ⁇
- the methods. of the prior art include conventional hydrogenationa of powdered coal, and methods for thev gasication of coal to produce a mixture of carbon monoxideand hydrogen followed by conversion of the carbon monoxide and hydrogen to liquidv hydrocarbons by theFischer-Tropsch synthesis.
- the coal is mined in the usual manner.. dried, pulverized and made into a paste by. admixing the powdered coal with a heavy oil.
- the paste is mixed with hydrogen and. reacted at a temperature of from about 800 to about 900' F. and at pressures ranging from about 43000. to about 10,000 pounds per square inch.
- The. present process does not. suffer from the depth limitations which are. imposed upon mining operations. At4 adepth of 5,000 feet.. for example, the temperature of' the. earths. crust is about, F'., which makes. the cost @airconditioning and Ventilating the coal seams too.4 expensive to work them by conventional mining. methods. Such underground temperatures. are an advantage of the process of the present. invention.
- Another. important. advantage of this invention derives from the fact that. the unhydrogenated portion of the coal seam is left in a porous or honeycomb state whichv is. almost ideallyl suited for underground gasification.
- the present invention also contemplates recovery of carbon values from the unhydrogenated residue by gasication of the residue. ⁇ in situA by contact with an oxygen-containing gas.
- cation of coal with an oxygen-containing gas is already known inthe art..
- Much diiculty has been experienced with previous methods of gasication due to the fact. that a. complicated system of passagevvays must rst be provided through the coal seam to permit passage of the oxidizing gases therethrough..
- the passageways. are provided by the removal of the hydrogenatable. portion of the coal so that a pervious massief reactivecarbonaceous material remains for the gasication reaction.
- the oxygen-containing. gas mayv be passed directly through this residue-without' the4 Underground gasinecessity of drilling passageways therethrough.
- An object of the present invention is to provide an improved process for the recovery of coal from underground deposits.
- Another object is to provide a process for the liquefaction of coal substances in underground seams.
- Still another object is to provide an improved process for recovery of coal as a liquid from underground deposits.
- Another specific object is to provide an improved method of recovery of coal from underground deposits, partly as a liquid hydrogenation product and partly as a gaseous product of underground gasification.
- coal is liquefied at a temperature above about 550 F. and generally within the range of from about 550 to about 850 F. by direct contact between the virgin coal and the hydrogenating agent.
- the temperature is maintained within the range of 700 to 750 F.
- Pressures above about 1,000 pounds per square inch are suitable.
- the pressure may range up to about 10,000 pounds per square inch where such pressures may be used without excessive loss of hydrogen due to leakage from the coal seam. Structural limitations usually require the use of pressures in the lower portion of this range; higher pressures are desirable wherever practical.
- the rate of reaction, and the reaction temperature may be controlled by control of the pressure at which the reaction is carried out. As the pressure is increased, the rate of reaction and the reaction temperature increase; as the pressure is decreased, the rate and temperature decrease.
- a well bore is drilled into the coal seam through which the hydrogenating agent may be admitted and the resulting liquid product withdrawn.
- the hydrogenating agent is forced under pressure through the well bore into direct contact with the virgin coal in the underground seam.
- Gaseous hydrogen is preferable as the hydrogenating agent.
- the hydrogen permeates the residue relatively thoroughly and produces by reaction with the coal an oil which is an excellent solvent and hydrogen transfer agent.
- the heavy oil or liquefied coal substance obtained by hydrogenation is one of the best hydrogen carriers known at the present time.
- the hydrogen diffuses upwardly into the coal seam, liquefying the more readily liqueable coal substance. This liquid then drains down over the less readily liquefiable portion of the coal, thus acting as a hydrogen carrier to facilitate the liquefaction.
- the reaction is initiated by raising the temperature at the coal face to the reaction temperature.
- Any means of supplying heat may be used; preferable are those involving liberation of heat near the face of the coal seam by chemical means.
- An electrical heater may be placed in the well bore to preheat the reactants.
- Superheated vapors of a hydroaromatic may thus be supplied to the coal whereupon heat is transferred to the coal upon condensation of the vapors to supplement the heat liberated by the reaction.
- the exothermic heat of reaction and the heat transfer between the reactants and reaction products serve to maintain the reaction temperature.
- the ⁇ well bore is preferably drilled into a low portion of the coal seam to permit the liquid product to drain down to the well bore for removal.
- the process is well adapted to working those seams which are inclined at an angle too steep for conventional mining.
- the process is particularly adapted to working those coal seams which are overlain by a relatively impervious stratum.
- the coal seams are overlain with a layer of clay and shale which is relatively impervious and is a good heat insulator.
- the loss of hydrogen into pervious adjacent formations may often be largely eliminated by operating at high temperatures for a period of time such that some of the fusible metal salts in the formations are melted or some of the volatile metal salts associated with the coal are vaporized, thus plugging the walls of the adjacent formation.
- the temperature may be increased by operating at very high pressure to increase the rate of reaction and hence the rate of heat at which heat is liberated by the exothermic heat of reaction.
- Volatile metals may be supplied to the coal seam in the form of a concentrated solution of a soluble salt of one of the metals during the course of reaction. Halides of zinc and lead, for example, are suitable for this purpose.
- a typical product obtainable by underground hydrogenation comprises 60 to 70 per cent liquid hydrocarbons and l0 to 30 per cent gaseous hydrocarbons. About 31/2 to 4 barrels of oil are obtained from each ton of coal reacted. Approximately 27 per cent of the liquid hydrocarbon fraction has a boiling range within the gasoline range that is up to 392 F., 50 per cent between 392 and 572 F. and 23 per cent above 572 F.
- a solvent extraction, based on hydrogenation by hydrogen transfer, may be carried out by using one of the liquid hydrogenating agents for recovery of the coal.
- the hydrogenating agents which are suitable for this purpose are tetrahydro-naphthalene, decahydro-naphthalene, crude cresols, oil from the hydrogenation of coal, aromatic crude oil, and the like.
- the liquid hydrogenating agent is supplemented with gaseous hydrogen.
- the liquid hydrogenating agent may be injected into the coal seam and recovered therefrom either intermittently or continuously.
- the liquid hydrogenating agent may be injected into the upper part of the seam and the liquid product recovered from a lower portion of the seam. Appropriate passages may be provided in the coal seam for injection of the hydrogenating agent and recovery of the product.
- a portion of the product, preferably a heavy fraction may be used effectively as the hydrogenating agent, most suitably after hydrogenation aboveground.
- coal seam is pervious due to structural anomalies, sometimes resulting from foi'- ing or faulting of the strata.
- the permeability of the coal may be increased by dissolution of part or all of the mineral matter, thus opening pores in the coal.
- a concentrated mineral acid, preferably sulfuric acid, may be used for this purpose.
- a catalyst may be used for the hydrogenation reaction.
- Iodine is an effective catalyst for this purpose.
- the iodine may be employed in either the elemental state, as hydrogen iodide, or in the form of an organic compound of iodine, e. g., methyl iodide, iodoform, methyl iodoform, etc.
- the numeral i designates an underground seam of coal above which is a relatively impervious stratum 2, generally of clay and shale, and below which is another relatively impervious stratum 3, e. g., a layer of clay.
- a well bore is drilled from the surface of the earth #i to a low point in the coal seam adjacent the underlying stratum ⁇ 3.
- Separate conduits 5 and 6 extend through the well bore into the coal seam. These conduits may be placed in any convenient manner analogous to the placement of tubing and casing in oil wells. As illustrated in the drawing, conduit 6 is placed within conduit 5 leaving an annular passageway 'l therebetween.
- An enlarged cavity 8 may be formed at the terminus of the Well bore to serve as a collection chamber for liquefied coal.
- the conduit 5 preferably is closed at its lower end and provided with a number of perforations 9 adjacent the coal stratum as outlets for the hydrogenating agent.
- the hydrogenating agent is admitted to conduit 5 through pipe I6, flowing through the annular passageway 'l and the perforations 9 into the coal stratum.
- the liqueed coal or liquid hydrogenation product is withdrawn through pipe 6.
- a plurality of well bores may be employed in carrying out the process, with injection of the hydrogenating agent into one or more wells and recovery of the liquefied coal from one or more additional wells.
- the well may be used alternately for injection and recovery, either alone or in combination with other wells.
- the crude product comprises not only the liquid and gaseous hydrocarbons but also tar acids, tar bases, ammonia, carbon dioxide, carbon monoxide, water, and hydrogen sulfide.
- the crude product is preferably maintained under an elevated pressure of at least 100 pounds per square inch until a separation of the oil and water layers has been effected at the surface of the earth.
- the pressure is released to permit the escape of the excess carbon dioxide from the water fraction.
- the ammonia may then be recovered by makingf the water layer alkaline and heating the water layer to release the ammonia.
- Ammonium carbonate may be produced by combining the recovered ammonia with some of the carbon dioxide originally released from the water layer.
- Sulfur may also be obtained as a by-product by oxidation of the hydrogen sulde in a neutral solution by blowing with air and recovering the resulting sulfur from the water layer by filtration.
- hydrocarbon gases and carbon monoxide dissolved in the liquid hydrocarbon product are separated by stabilization and these gases used for the liquefaction process.
- Hydrogen from any suitable source may be employed in the process.
- the stabilized hydrocarbon may be treated to remove the tar acids and the tar bases.
- the tar acids are suitably removed by a caustic wash and the tar bases by an acid wash, as is known in the art.
- Tar acids and bases may be recovered from the resulting solutions by neutralizing and skimming although it is sometimes desirable to extract the neutral solution with a suitable sol- 'vent such as ether, acetone, or the like.
- the tar acids and bases may be separated into various constituent compounds by conventional methods or, as is often the case, sold and used as mixtures.
- the residual stabilized hydrocarbons may be separated into the usual fractions by distillation and by other refining methods.
- the hydrocarbon fraction contains relatively large quantities of aromatic constituents. In some instances, it may be desirable to separate some of these materials for chemical uses.
- a process for the recovery of coal from underground deposits which comprises contacting the coal in situ with a hydrogenating agent selected from the group consisting of free hydrogen and hydroaromatic compounds at a temperature within the range from about 550 F. to about 850 F. and a pressure above about 1,000 pounds per square inch gauge effective tohydrogenate a portion of the coal substance to form a liquid, and recovering the resulting liqueed coal substance from the underground deposit.
- a hydrogenating agent selected from the group consisting of free hydrogen and hydroaromatic compounds at a temperature within the range from about 550 F. to about 850 F. and a pressure above about 1,000 pounds per square inch gauge effective tohydrogenate a portion of the coal substance to form a liquid
- a process for the recovery of coal substance from a subterranean coal deposit which comprises drilling a well bore from the surface of the earth into the coal seam, introducing hydrogen through the well bore into Contact with the coal in situ at a pressure above about 1,000 pounds per square inch gauge,'initiating the reaction between hydrogen and coal in said deposit by heating the coal in the area adjacent the well bore to a temperature above about 550 F. whereby hydrogen combines with a portion of the coal substance to form a liquid, maintaining the temperature within the range of from about 550 to about 850 F., collecting the resulting liquefied coal substance in a well bore, withdrawing said liquid from the subterranean deposit through a well bore.
Description
May 6, 1952 E. F. PEVERE ET Al. 2,595,979
UNDERGROUND LIQUEFACTION OF COAL Filed Jan. 25, 1949 Patented May 6, 1952 UNITED STATES PATENT ofi-Fics UNDERGROUND LIQUEFACTION OF COAL Ernest. F'. Revere,` Beacon, and Georgev vB. Arnold,
Glenham.. N.v Y.,. assignors to The Texas Company; New York, N. Y., a corporation of Del- Application January 25, 1949, Serial N o. 72,582`
( Cl. 19E-53) 2' Claims. l.
` This invention relatestoa process for the recovery of coal substance from. underground deposits in the formv of a liquid In oneof. its more specific aspects, this invention relates tov the underground Iiquefaction oi. a liqueable fraction. of a coal deposit. by hydrogenation to produce a liquid extract suitable for use in the. production ofmotor fuels.
In accordance with the present invention, coal in an underground deposit is hydrogen-ated in situ by contact with a. hydrogenating agent. The hydrogenation is carried out. at an elevated temperature and pressure, which may be controlled from above ground. The. hydrogenation reaction produces a liquid product which is readily recovered` as a relatively heavy oil. The crude liquid product may be subject to further hydrogenation and refining operations. to produce motor fuels and other desired products after recovery from the undergroundformation.
The hydrogenating. agent used in the present process may be free hydrogen or an organic compound capable of liberating hydrogen. Hydroaromatics, such as hydrogenated naphthalenes, e. g., tetralin and decalin, and heavy oils obtained by hydrogenation of` coal are suitable hydrogenating agents. Hydroaromatic oils act as solvents in the liquefaction of coal, due primarily to their ability to transfer hydrogen to the coal.
In general, from about 70 to about 90 per cent by weight of av bituminous coal may be liqueed by hydrogenation, the extent of the liquefaction depending largely upon the grade of the coal. Approximately 65 per cent by weight of massive or lump coal may be readilyA liquefied' by hydrogenation. The hydrogen consumption' generally' ranges from about 1.5 to about 3 percent by weight based on the Weight of the coal reacted. The liqueed coal, or extract, obtained on hydrogenation is fluid and substantially free from ash.
This liquid may be recovered from thefcoal seamY by the process of this invention in a manner analogous to the. production. of crude oil. The residual or unhydrogenated portion of the coal comprises unreacted carbon and the mineral matter or ash. The residue may also. be utilized advantageously as will be brought out hereinafter.
The process of the present invention has many advantages over prior methodsof producing hydrocarbons from coal.` The methods. of the prior art include conventional hydrogenationa of powdered coal, and methods for thev gasication of coal to produce a mixture of carbon monoxideand hydrogen followed by conversion of the carbon monoxide and hydrogen to liquidv hydrocarbons by theFischer-Tropsch synthesis.
In the conventional coal hydrogenation process, the coal is mined in the usual manner.. dried, pulverized and made into a paste by. admixing the powdered coal with a heavy oil. The paste is mixed with hydrogen and. reacted at a temperature of from about 800 to about 900' F. and at pressures ranging from about 43000. to about 10,000 pounds per square inch.
An important elementr of cost in conventional coal hydrogenati'on processes is. the cost .of preparation of the coal for hydrogenation. The. ne grinding of the coal to obtain a. powder requires the expenditure of large amounts of' power. In addition, costly high. pressure. reactors, pumps, transfer lines and related equipment. are required.
The mining of bituminous coal., for. example, is in itself a wasteful. procedure. It has been. estimated that on an overall average,v about per cent of the coal in place is recovered from the mines, the remainder being left, as supporting pillars, etc. There is another l0 per. centv loss incurred in the handlingoperations so. that` only about 55 per cent of. thecoal in place is recovered as marketable coal. In addition, a. considerable amount of methane is lost. from` every ton of coal produced. Contact with atmosphericA oxygen results in some chemical. reaction.. rendering the coal somewhat less reactive for hydrogenation.
than is the virgin coal. The recovery of. coal substance from the. deposit iby the-present. process is, therefore, comparable in eiliciency to modern mining methods..
The. present process does not. suffer from the depth limitations which are. imposed upon mining operations. At4 adepth of 5,000 feet.. for example, the temperature of' the. earths. crust is about, F'., which makes. the cost @airconditioning and Ventilating the coal seams too.4 expensive to work them by conventional mining. methods. Such underground temperatures. are an advantage of the process of the present. invention.
Another. important. advantage of this invention derives from the fact that. the unhydrogenated portion of the coal seam is left in a porous or honeycomb state whichv is. almost ideallyl suited for underground gasification. The present invention also contemplates recovery of carbon values from the unhydrogenated residue by gasication of the residue.` in situA by contact with an oxygen-containing gas. cation of coal with an oxygen-containing gas is already known inthe art.. Much diiculty has been experienced with previous methods of gasication due to the fact. that a. complicated system of passagevvays must rst be provided through the coal seam to permit passage of the oxidizing gases therethrough.. In the present process, the passageways. are provided by the removal of the hydrogenatable. portion of the coal so that a pervious massief reactivecarbonaceous material remains for the gasication reaction. The oxygen-containing. gas mayv be passed directly through this residue-without' the4 Underground gasinecessity of drilling passageways therethrough.
An object of the present invention is to provide an improved process for the recovery of coal from underground deposits.
Another object is to provide a process for the liquefaction of coal substances in underground seams.
Still another object is to provide an improved process for recovery of coal as a liquid from underground deposits.
Another specific object is to provide an improved method of recovery of coal from underground deposits, partly as a liquid hydrogenation product and partly as a gaseous product of underground gasification.
Other objects and advantages will be apparent to those skilled in the art from the following detailed description.
In the process of this invention, coal is liquefied at a temperature above about 550 F. and generally within the range of from about 550 to about 850 F. by direct contact between the virgin coal and the hydrogenating agent. Preferably the temperature is maintained within the range of 700 to 750 F. Pressures above about 1,000 pounds per square inch are suitable. The pressure may range up to about 10,000 pounds per square inch where such pressures may be used without excessive loss of hydrogen due to leakage from the coal seam. Structural limitations usually require the use of pressures in the lower portion of this range; higher pressures are desirable wherever practical.
The rate of reaction, and the reaction temperature, may be controlled by control of the pressure at which the reaction is carried out. As the pressure is increased, the rate of reaction and the reaction temperature increase; as the pressure is decreased, the rate and temperature decrease.
In carrying out the present process, a well bore is drilled into the coal seam through which the hydrogenating agent may be admitted and the resulting liquid product withdrawn. The hydrogenating agent is forced under pressure through the well bore into direct contact with the virgin coal in the underground seam. Gaseous hydrogen is preferable as the hydrogenating agent. The hydrogen permeates the residue relatively thoroughly and produces by reaction with the coal an oil which is an excellent solvent and hydrogen transfer agent. The heavy oil or liquefied coal substance obtained by hydrogenation is one of the best hydrogen carriers known at the present time. The hydrogen diffuses upwardly into the coal seam, liquefying the more readily liqueable coal substance. This liquid then drains down over the less readily liquefiable portion of the coal, thus acting as a hydrogen carrier to facilitate the liquefaction.
The reaction is initiated by raising the temperature at the coal face to the reaction temperature.
Any means of supplying heat may be used; preferable are those involving liberation of heat near the face of the coal seam by chemical means. An electrical heater may be placed in the well bore to preheat the reactants. Superheated vapors of a hydroaromatic may thus be supplied to the coal whereupon heat is transferred to the coal upon condensation of the vapors to supplement the heat liberated by the reaction. Once initiated, the exothermic heat of reaction and the heat transfer between the reactants and reaction products serve to maintain the reaction temperature.
The `well bore is preferably drilled into a low portion of the coal seam to permit the liquid product to drain down to the well bore for removal. The process is well adapted to working those seams which are inclined at an angle too steep for conventional mining. The process is particularly adapted to working those coal seams which are overlain by a relatively impervious stratum. Generally, the coal seams are overlain with a layer of clay and shale which is relatively impervious and is a good heat insulator.
The loss of hydrogen into pervious adjacent formations may often be largely eliminated by operating at high temperatures for a period of time such that some of the fusible metal salts in the formations are melted or some of the volatile metal salts associated with the coal are vaporized, thus plugging the walls of the adjacent formation. The temperature may be increased by operating at very high pressure to increase the rate of reaction and hence the rate of heat at which heat is liberated by the exothermic heat of reaction. Volatile metals may be supplied to the coal seam in the form of a concentrated solution of a soluble salt of one of the metals during the course of reaction. Halides of zinc and lead, for example, are suitable for this purpose.
A typical product obtainable by underground hydrogenation comprises 60 to 70 per cent liquid hydrocarbons and l0 to 30 per cent gaseous hydrocarbons. About 31/2 to 4 barrels of oil are obtained from each ton of coal reacted. Approximately 27 per cent of the liquid hydrocarbon fraction has a boiling range within the gasoline range that is up to 392 F., 50 per cent between 392 and 572 F. and 23 per cent above 572 F.
A solvent extraction, based on hydrogenation by hydrogen transfer, may be carried out by using one of the liquid hydrogenating agents for recovery of the coal. Among the hydrogenating agents which are suitable for this purpose are tetrahydro-naphthalene, decahydro-naphthalene, crude cresols, oil from the hydrogenation of coal, aromatic crude oil, and the like. Preferably the liquid hydrogenating agent is supplemented with gaseous hydrogen. The liquid hydrogenating agent may be injected into the coal seam and recovered therefrom either intermittently or continuously. The liquid hydrogenating agent may be injected into the upper part of the seam and the liquid product recovered from a lower portion of the seam. Appropriate passages may be provided in the coal seam for injection of the hydrogenating agent and recovery of the product. A portion of the product, preferably a heavy fraction, may be used effectively as the hydrogenating agent, most suitably after hydrogenation aboveground.
Often the coal seam is pervious due to structural anomalies, sometimes resulting from foi'- ing or faulting of the strata. The permeability of the coal may be increased by dissolution of part or all of the mineral matter, thus opening pores in the coal. A concentrated mineral acid, preferably sulfuric acid, may be used for this purpose.
A catalyst may be used for the hydrogenation reaction. Iodine is an effective catalyst for this purpose. The iodine may be employed in either the elemental state, as hydrogen iodide, or in the form of an organic compound of iodine, e. g., methyl iodide, iodoform, methyl iodoform, etc.
The accompanying drawing illustrates diagrammatically the process of this invention.
With reference to the drawing, the numeral i designates an underground seam of coal above which is a relatively impervious stratum 2, generally of clay and shale, and below which is another relatively impervious stratum 3, e. g., a layer of clay. A well bore is drilled from the surface of the earth #i to a low point in the coal seam adjacent the underlying stratum `3. Separate conduits 5 and 6 extend through the well bore into the coal seam. These conduits may be placed in any convenient manner analogous to the placement of tubing and casing in oil wells. As illustrated in the drawing, conduit 6 is placed within conduit 5 leaving an annular passageway 'l therebetween.
An enlarged cavity 8 may be formed at the terminus of the Well bore to serve as a collection chamber for liquefied coal. The conduit 5 preferably is closed at its lower end and provided with a number of perforations 9 adjacent the coal stratum as outlets for the hydrogenating agent. The hydrogenating agent is admitted to conduit 5 through pipe I6, flowing through the annular passageway 'l and the perforations 9 into the coal stratum. The liqueed coal or liquid hydrogenation product is withdrawn through pipe 6.
As the hydrogenation progresses, a porous, honeycomb-like residue i2 is left in place in the formation. The liquid resulting from the liquefaction drains away from the residue, collects in the cavity 8 and flows through pipe 6 to the surface where it may be subjected to appropriate refining methods.
Obviously, a plurality of well bores may be employed in carrying out the process, with injection of the hydrogenating agent into one or more wells and recovery of the liquefied coal from one or more additional wells. The well may be used alternately for injection and recovery, either alone or in combination with other wells.
The crude product comprises not only the liquid and gaseous hydrocarbons but also tar acids, tar bases, ammonia, carbon dioxide, carbon monoxide, water, and hydrogen sulfide. The crude product is preferably maintained under an elevated pressure of at least 100 pounds per square inch until a separation of the oil and water layers has been effected at the surface of the earth.
In this way, most of the carbon dioxide, ammonia and hydrogen sulfide remain in the water layer, the ammonia in the form of salts of carbon dioxide or hydrogen sulde.
After the separation of the Water layer, the pressure is released to permit the escape of the excess carbon dioxide from the water fraction. The ammonia may then be recovered by makingf the water layer alkaline and heating the water layer to release the ammonia. Ammonium carbonate may be produced by combining the recovered ammonia with some of the carbon dioxide originally released from the water layer. Sulfur may also be obtained as a by-product by oxidation of the hydrogen sulde in a neutral solution by blowing with air and recovering the resulting sulfur from the water layer by filtration.
The hydrocarbon gases and carbon monoxide dissolved in the liquid hydrocarbon product are separated by stabilization and these gases used for the liquefaction process. Hydrogen from any suitable source may be employed in the process.
The stabilized hydrocarbon may be treated to remove the tar acids and the tar bases. The tar acids are suitably removed by a caustic wash and the tar bases by an acid wash, as is known in the art. Tar acids and bases may be recovered from the resulting solutions by neutralizing and skimming although it is sometimes desirable to extract the neutral solution with a suitable sol- 'vent such as ether, acetone, or the like. The tar acids and bases may be separated into various constituent compounds by conventional methods or, as is often the case, sold and used as mixtures.
After removal of the tar acids and bases, the residual stabilized hydrocarbons may be separated into the usual fractions by distillation and by other refining methods. The hydrocarbon fraction contains relatively large quantities of aromatic constituents. In some instances, it may be desirable to separate some of these materials for chemical uses.
Obviously many modifications and variations of the invention, as hereinbefore set forth, may be made without departing from the spirit and scope thereof and, therefore, only such limitations should be imposed as are indicated in the appended claims.
Vle claim:
. 1. A process for the recovery of coal from underground deposits which comprises contacting the coal in situ with a hydrogenating agent selected from the group consisting of free hydrogen and hydroaromatic compounds at a temperature within the range from about 550 F. to about 850 F. and a pressure above about 1,000 pounds per square inch gauge effective tohydrogenate a portion of the coal substance to form a liquid, and recovering the resulting liqueed coal substance from the underground deposit.
2. A process for the recovery of coal substance from a subterranean coal deposit which comprises drilling a well bore from the surface of the earth into the coal seam, introducing hydrogen through the well bore into Contact with the coal in situ at a pressure above about 1,000 pounds per square inch gauge,'initiating the reaction between hydrogen and coal in said deposit by heating the coal in the area adjacent the well bore to a temperature above about 550 F. whereby hydrogen combines with a portion of the coal substance to form a liquid, maintaining the temperature within the range of from about 550 to about 850 F., collecting the resulting liquefied coal substance in a well bore, withdrawing said liquid from the subterranean deposit through a well bore.
ERNEST F. PEVERE. GEORGE B. ARNOLD.
REFERENCES CITED The following references are of record in the le of this patent:
UNITED STATES PATENTS Number Name Date 345,586 Hall July 13, 1886 947,608 Betts Jan. 25, 1910 1,532,826 Lessing Apr. 7, 1925 1,669,439 Bergius May 15, 1928 2,039,459 Seguy May 5, 1936 2,119,647 Pier et al June 7, 1938 2,165,940 Pier et al. July 11, 1939 2,177,376 Pier et al Oct. 24, 1939
Claims (1)
1. A PROCESS FOR THE RECOVERY OF COAL FROM UNDERGROUND DEPOSITS WHICH COMPRISES CONTACTING THE COAL IN SITU WITH A HYDROGENATING AGENT SELECTED FROM THE GROUP CONSISTING OF FREE HYDROGEN AND HYDROAROMATIC COMPOUNDS AT A TEMPERATURE WITHIN THE RANGE FROM ABOUT 550* F. TO ABOUT 850* F. AND A PRESSURE ABOVE ABOUT 1,000 POUNDS PER SQUARE INCH GAUGE EFFECTIVE TO HYDROGENATE A PORTION OF THE COAL SUBSTANCE TO FORM A LIQUID, AND
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US72582A US2595979A (en) | 1949-01-25 | 1949-01-25 | Underground liquefaction of coal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US72582A US2595979A (en) | 1949-01-25 | 1949-01-25 | Underground liquefaction of coal |
Publications (1)
Publication Number | Publication Date |
---|---|
US2595979A true US2595979A (en) | 1952-05-06 |
Family
ID=22108536
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US72582A Expired - Lifetime US2595979A (en) | 1949-01-25 | 1949-01-25 | Underground liquefaction of coal |
Country Status (1)
Country | Link |
---|---|
US (1) | US2595979A (en) |
Cited By (73)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2857002A (en) * | 1956-03-19 | 1958-10-21 | Texas Co | Recovery of viscous crude oil |
US2937987A (en) * | 1957-12-19 | 1960-05-24 | Socony Mobil Oil Co Inc | Underground hydrogenation |
US2939895A (en) * | 1956-11-13 | 1960-06-07 | Texaco Inc | Conducting chemical reactions in an underground storage cavern |
US3051235A (en) * | 1958-02-24 | 1962-08-28 | Jersey Prod Res Co | Recovery of petroleum crude oil, by in situ combustion and in situ hydrogenation |
US3084919A (en) * | 1960-08-03 | 1963-04-09 | Texaco Inc | Recovery of oil from oil shale by underground hydrogenation |
US3102588A (en) * | 1959-07-24 | 1963-09-03 | Phillips Petroleum Co | Process for recovering hydrocarbon from subterranean strata |
US3208514A (en) * | 1962-10-31 | 1965-09-28 | Continental Oil Co | Recovery of hydrocarbons by in-situ hydrogenation |
US3302707A (en) * | 1964-09-30 | 1967-02-07 | Mobil Oil Corp | Method for improving fluid recoveries from earthen formations |
US3327782A (en) * | 1962-09-10 | 1967-06-27 | Pan American Petroleum Corp | Underground hydrogenation of oil |
US3412011A (en) * | 1966-09-02 | 1968-11-19 | Phillips Petroleum Co | Catalytic cracking and in situ combustion process for producing hydrocarbons |
US3520794A (en) * | 1968-03-29 | 1970-07-14 | Universal Oil Prod Co | Solvent extraction method |
US3598182A (en) * | 1967-04-25 | 1971-08-10 | Justheim Petroleum Co | Method and apparatus for in situ distillation and hydrogenation of carbonaceous materials |
US3766982A (en) * | 1971-12-27 | 1973-10-23 | Justheim Petrol Co | Method for the in-situ treatment of hydrocarbonaceous materials |
US3948320A (en) * | 1975-03-14 | 1976-04-06 | In Situ Technology, Inc. | Method of in situ gasification, cooling and liquefaction of a subsurface coal formation |
US3973628A (en) * | 1975-04-30 | 1976-08-10 | New Mexico Tech Research Foundation | In situ solution mining of coal |
US3990513A (en) * | 1972-07-17 | 1976-11-09 | Koppers Company, Inc. | Method of solution mining of coal |
US3999607A (en) * | 1976-01-22 | 1976-12-28 | Exxon Research And Engineering Company | Recovery of hydrocarbons from coal |
US4059151A (en) * | 1975-07-14 | 1977-11-22 | In Situ Technology, Inc. | Methods of fluidized production of coal in situ |
US4141417A (en) * | 1977-09-09 | 1979-02-27 | Institute Of Gas Technology | Enhanced oil recovery |
US4189184A (en) * | 1978-10-13 | 1980-02-19 | Green Harold F | Rotary drilling and extracting process |
US4250964A (en) * | 1979-11-15 | 1981-02-17 | Gulf Research & Development Company | Process for recovering carbonaceous organic material from a subterranean formation |
US4337148A (en) * | 1980-10-20 | 1982-06-29 | Phillips Petroleum Company | Lead pressured extraction of carbonaceous material |
US4455215A (en) * | 1982-04-29 | 1984-06-19 | Jarrott David M | Process for the geoconversion of coal into oil |
US4476928A (en) * | 1982-07-23 | 1984-10-16 | Dimar Holding Corporation | Method and apparatus for solvent generation and recovery of hydrocarbons |
US4501445A (en) * | 1983-08-01 | 1985-02-26 | Cities Service Company | Method of in-situ hydrogenation of carbonaceous material |
US4537252A (en) * | 1982-04-23 | 1985-08-27 | Standard Oil Company (Indiana) | Method of underground conversion of coal |
US4662439A (en) * | 1984-01-20 | 1987-05-05 | Amoco Corporation | Method of underground conversion of coal |
US4772379A (en) * | 1985-10-29 | 1988-09-20 | Ann Arbor Nuclear, Inc. | Extraction and liquefaction of fossil fuels using gamma irradiation and solvents |
WO2001083945A1 (en) | 2000-04-24 | 2001-11-08 | Shell Internationale Research Maatschappij B.V. | A method for treating a hydrocarbon containing formation |
US20020046883A1 (en) * | 2000-04-24 | 2002-04-25 | Wellington Scott Lee | In situ thermal processing of a coal formation using pressure and/or temperature control |
US20030080604A1 (en) * | 2001-04-24 | 2003-05-01 | Vinegar Harold J. | In situ thermal processing and inhibiting migration of fluids into or out of an in situ oil shale formation |
US20030079877A1 (en) * | 2001-04-24 | 2003-05-01 | Wellington Scott Lee | In situ thermal processing of a relatively impermeable formation in a reducing environment |
US20030098605A1 (en) * | 2001-04-24 | 2003-05-29 | Vinegar Harold J. | In situ thermal recovery from a relatively permeable formation |
US6588504B2 (en) | 2000-04-24 | 2003-07-08 | Shell Oil Company | In situ thermal processing of a coal formation to produce nitrogen and/or sulfur containing formation fluids |
US20030155111A1 (en) * | 2001-04-24 | 2003-08-21 | Shell Oil Co | In situ thermal processing of a tar sands formation |
US20030173081A1 (en) * | 2001-10-24 | 2003-09-18 | Vinegar Harold J. | In situ thermal processing of an oil reservoir formation |
US20030173085A1 (en) * | 2001-10-24 | 2003-09-18 | Vinegar Harold J. | Upgrading and mining of coal |
US20030196810A1 (en) * | 2001-10-24 | 2003-10-23 | Vinegar Harold J. | Treatment of a hydrocarbon containing formation after heating |
US6698515B2 (en) | 2000-04-24 | 2004-03-02 | Shell Oil Company | In situ thermal processing of a coal formation using a relatively slow heating rate |
US6715546B2 (en) | 2000-04-24 | 2004-04-06 | Shell Oil Company | In situ production of synthesis gas from a hydrocarbon containing formation through a heat source wellbore |
US6715548B2 (en) | 2000-04-24 | 2004-04-06 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce nitrogen containing formation fluids |
US20040144541A1 (en) * | 2002-10-24 | 2004-07-29 | Picha Mark Gregory | Forming wellbores using acoustic methods |
US20050269093A1 (en) * | 2004-04-23 | 2005-12-08 | Sandberg Chester L | Variable frequency temperature limited heaters |
US7011154B2 (en) | 2000-04-24 | 2006-03-14 | Shell Oil Company | In situ recovery from a kerogen and liquid hydrocarbon containing formation |
US7090013B2 (en) | 2001-10-24 | 2006-08-15 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce heated fluids |
US7096953B2 (en) | 2000-04-24 | 2006-08-29 | Shell Oil Company | In situ thermal processing of a coal formation using a movable heating element |
US7104319B2 (en) | 2001-10-24 | 2006-09-12 | Shell Oil Company | In situ thermal processing of a heavy oil diatomite formation |
US7121342B2 (en) | 2003-04-24 | 2006-10-17 | Shell Oil Company | Thermal processes for subsurface formations |
US7165615B2 (en) | 2001-10-24 | 2007-01-23 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden |
US20070034568A1 (en) * | 2003-04-08 | 2007-02-15 | Foster Neil R | Particle synthesis apparatus and method |
US20070045265A1 (en) * | 2005-04-22 | 2007-03-01 | Mckinzie Billy J Ii | Low temperature barriers with heat interceptor wells for in situ processes |
US20070095536A1 (en) * | 2005-10-24 | 2007-05-03 | Vinegar Harold J | Cogeneration systems and processes for treating hydrocarbon containing formations |
US20070108201A1 (en) * | 2005-04-22 | 2007-05-17 | Vinegar Harold J | Insulated conductor temperature limited heater for subsurface heating coupled in a three-phase wye configuration |
US20070227729A1 (en) * | 2006-03-29 | 2007-10-04 | Pioneer Invention, Inc. D/B/A Pioneer Astronautics | Apparatus and method for extracting petroleum from underground sites using reformed gases |
US20070278344A1 (en) * | 2006-06-06 | 2007-12-06 | Pioneer Invention, Inc. D/B/A Pioneer Astronautics | Apparatus and Method for Producing Lift Gas and Uses Thereof |
US20080038144A1 (en) * | 2006-04-21 | 2008-02-14 | Maziasz Phillip J | High strength alloys |
US20080128134A1 (en) * | 2006-10-20 | 2008-06-05 | Ramesh Raju Mudunuri | Producing drive fluid in situ in tar sands formations |
US20080296018A1 (en) * | 2007-05-29 | 2008-12-04 | Zubrin Robert M | System and method for extracting petroleum and generating electricity using natural gas or local petroleum |
US20090071652A1 (en) * | 2007-04-20 | 2009-03-19 | Vinegar Harold J | In situ heat treatment from multiple layers of a tar sands formation |
US20090189617A1 (en) * | 2007-10-19 | 2009-07-30 | David Burns | Continuous subsurface heater temperature measurement |
US20090236093A1 (en) * | 2006-03-29 | 2009-09-24 | Pioneer Energy, Inc. | Apparatus and Method for Extracting Petroleum from Underground Sites Using Reformed Gases |
US20090260823A1 (en) * | 2008-04-18 | 2009-10-22 | Robert George Prince-Wright | Mines and tunnels for use in treating subsurface hydrocarbon containing formations |
US20100089584A1 (en) * | 2008-10-13 | 2010-04-15 | David Booth Burns | Double insulated heaters for treating subsurface formations |
US20100088951A1 (en) * | 2008-07-17 | 2010-04-15 | Pioneer Astronautics | Novel Methods of Higher Alcohol Synthesis |
US20100258290A1 (en) * | 2009-04-10 | 2010-10-14 | Ronald Marshall Bass | Non-conducting heater casings |
US20100314136A1 (en) * | 2007-05-20 | 2010-12-16 | Zubrin Robert M | Systems and methods for generating in-situ carbon dioxide driver gas for use in enhanced oil recovery |
US8631866B2 (en) | 2010-04-09 | 2014-01-21 | Shell Oil Company | Leak detection in circulated fluid systems for heating subsurface formations |
US8701768B2 (en) | 2010-04-09 | 2014-04-22 | Shell Oil Company | Methods for treating hydrocarbon formations |
US8820406B2 (en) | 2010-04-09 | 2014-09-02 | Shell Oil Company | Electrodes for electrical current flow heating of subsurface formations with conductive material in wellbore |
US9016370B2 (en) | 2011-04-08 | 2015-04-28 | Shell Oil Company | Partial solution mining of hydrocarbon containing layers prior to in situ heat treatment |
US9033042B2 (en) | 2010-04-09 | 2015-05-19 | Shell Oil Company | Forming bitumen barriers in subsurface hydrocarbon formations |
US9309755B2 (en) | 2011-10-07 | 2016-04-12 | Shell Oil Company | Thermal expansion accommodation for circulated fluid systems used to heat subsurface formations |
US10047594B2 (en) | 2012-01-23 | 2018-08-14 | Genie Ip B.V. | Heater pattern for in situ thermal processing of a subsurface hydrocarbon containing formation |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US345586A (en) * | 1886-07-13 | Oil from wells | ||
US947608A (en) * | 1906-12-27 | 1910-01-25 | Anson G Betts | Method of utilizing buried coal. |
US1532826A (en) * | 1921-09-12 | 1925-04-07 | Lessing Rudolf | Treatment of coal |
US1669439A (en) * | 1926-11-24 | 1928-05-15 | Bergius Friedrich | Process for distilling and liquefying coal |
US2039459A (en) * | 1932-12-14 | 1936-05-05 | Universal Oil Prod Co | Process for treating hydrocarbons |
US2119647A (en) * | 1934-09-04 | 1938-06-07 | Standard Ig Co | Production of valuable hydrocarbons |
US2165940A (en) * | 1936-12-28 | 1939-07-11 | Standard Ig Co | Process for improving fuel oil |
US2177376A (en) * | 1936-02-06 | 1939-10-24 | Standard Ig Co | Production of valuable hydrocarbon products |
-
1949
- 1949-01-25 US US72582A patent/US2595979A/en not_active Expired - Lifetime
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US345586A (en) * | 1886-07-13 | Oil from wells | ||
US947608A (en) * | 1906-12-27 | 1910-01-25 | Anson G Betts | Method of utilizing buried coal. |
US1532826A (en) * | 1921-09-12 | 1925-04-07 | Lessing Rudolf | Treatment of coal |
US1669439A (en) * | 1926-11-24 | 1928-05-15 | Bergius Friedrich | Process for distilling and liquefying coal |
US2039459A (en) * | 1932-12-14 | 1936-05-05 | Universal Oil Prod Co | Process for treating hydrocarbons |
US2119647A (en) * | 1934-09-04 | 1938-06-07 | Standard Ig Co | Production of valuable hydrocarbons |
US2177376A (en) * | 1936-02-06 | 1939-10-24 | Standard Ig Co | Production of valuable hydrocarbon products |
US2165940A (en) * | 1936-12-28 | 1939-07-11 | Standard Ig Co | Process for improving fuel oil |
Cited By (473)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2857002A (en) * | 1956-03-19 | 1958-10-21 | Texas Co | Recovery of viscous crude oil |
US2939895A (en) * | 1956-11-13 | 1960-06-07 | Texaco Inc | Conducting chemical reactions in an underground storage cavern |
US2937987A (en) * | 1957-12-19 | 1960-05-24 | Socony Mobil Oil Co Inc | Underground hydrogenation |
US3051235A (en) * | 1958-02-24 | 1962-08-28 | Jersey Prod Res Co | Recovery of petroleum crude oil, by in situ combustion and in situ hydrogenation |
US3102588A (en) * | 1959-07-24 | 1963-09-03 | Phillips Petroleum Co | Process for recovering hydrocarbon from subterranean strata |
US3084919A (en) * | 1960-08-03 | 1963-04-09 | Texaco Inc | Recovery of oil from oil shale by underground hydrogenation |
US3327782A (en) * | 1962-09-10 | 1967-06-27 | Pan American Petroleum Corp | Underground hydrogenation of oil |
US3208514A (en) * | 1962-10-31 | 1965-09-28 | Continental Oil Co | Recovery of hydrocarbons by in-situ hydrogenation |
US3302707A (en) * | 1964-09-30 | 1967-02-07 | Mobil Oil Corp | Method for improving fluid recoveries from earthen formations |
US3412011A (en) * | 1966-09-02 | 1968-11-19 | Phillips Petroleum Co | Catalytic cracking and in situ combustion process for producing hydrocarbons |
US3598182A (en) * | 1967-04-25 | 1971-08-10 | Justheim Petroleum Co | Method and apparatus for in situ distillation and hydrogenation of carbonaceous materials |
US3520794A (en) * | 1968-03-29 | 1970-07-14 | Universal Oil Prod Co | Solvent extraction method |
US3766982A (en) * | 1971-12-27 | 1973-10-23 | Justheim Petrol Co | Method for the in-situ treatment of hydrocarbonaceous materials |
US3990513A (en) * | 1972-07-17 | 1976-11-09 | Koppers Company, Inc. | Method of solution mining of coal |
US3948320A (en) * | 1975-03-14 | 1976-04-06 | In Situ Technology, Inc. | Method of in situ gasification, cooling and liquefaction of a subsurface coal formation |
US3973628A (en) * | 1975-04-30 | 1976-08-10 | New Mexico Tech Research Foundation | In situ solution mining of coal |
US4059151A (en) * | 1975-07-14 | 1977-11-22 | In Situ Technology, Inc. | Methods of fluidized production of coal in situ |
US3999607A (en) * | 1976-01-22 | 1976-12-28 | Exxon Research And Engineering Company | Recovery of hydrocarbons from coal |
US4141417A (en) * | 1977-09-09 | 1979-02-27 | Institute Of Gas Technology | Enhanced oil recovery |
US4189184A (en) * | 1978-10-13 | 1980-02-19 | Green Harold F | Rotary drilling and extracting process |
US4250964A (en) * | 1979-11-15 | 1981-02-17 | Gulf Research & Development Company | Process for recovering carbonaceous organic material from a subterranean formation |
US4337148A (en) * | 1980-10-20 | 1982-06-29 | Phillips Petroleum Company | Lead pressured extraction of carbonaceous material |
US4537252A (en) * | 1982-04-23 | 1985-08-27 | Standard Oil Company (Indiana) | Method of underground conversion of coal |
US4455215A (en) * | 1982-04-29 | 1984-06-19 | Jarrott David M | Process for the geoconversion of coal into oil |
US4476928A (en) * | 1982-07-23 | 1984-10-16 | Dimar Holding Corporation | Method and apparatus for solvent generation and recovery of hydrocarbons |
US4501445A (en) * | 1983-08-01 | 1985-02-26 | Cities Service Company | Method of in-situ hydrogenation of carbonaceous material |
US4662439A (en) * | 1984-01-20 | 1987-05-05 | Amoco Corporation | Method of underground conversion of coal |
US4772379A (en) * | 1985-10-29 | 1988-09-20 | Ann Arbor Nuclear, Inc. | Extraction and liquefaction of fossil fuels using gamma irradiation and solvents |
US6948563B2 (en) | 2000-04-24 | 2005-09-27 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with a selected hydrogen content |
US6866097B2 (en) | 2000-04-24 | 2005-03-15 | Shell Oil Company | In situ thermal processing of a coal formation to increase a permeability/porosity of the formation |
WO2001083945A1 (en) | 2000-04-24 | 2001-11-08 | Shell Internationale Research Maatschappij B.V. | A method for treating a hydrocarbon containing formation |
US8789586B2 (en) | 2000-04-24 | 2014-07-29 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation |
US8485252B2 (en) | 2000-04-24 | 2013-07-16 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation |
US7096953B2 (en) | 2000-04-24 | 2006-08-29 | Shell Oil Company | In situ thermal processing of a coal formation using a movable heating element |
US7096941B2 (en) | 2000-04-24 | 2006-08-29 | Shell Oil Company | In situ thermal processing of a coal formation with heat sources located at an edge of a coal layer |
US7086468B2 (en) | 2000-04-24 | 2006-08-08 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using heat sources positioned within open wellbores |
US7036583B2 (en) | 2000-04-24 | 2006-05-02 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to increase a porosity of the formation |
US7017661B2 (en) | 2000-04-24 | 2006-03-28 | Shell Oil Company | Production of synthesis gas from a coal formation |
US7011154B2 (en) | 2000-04-24 | 2006-03-14 | Shell Oil Company | In situ recovery from a kerogen and liquid hydrocarbon containing formation |
US6997255B2 (en) | 2000-04-24 | 2006-02-14 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation in a reducing environment |
US6581684B2 (en) | 2000-04-24 | 2003-06-24 | Shell Oil Company | In Situ thermal processing of a hydrocarbon containing formation to produce sulfur containing formation fluids |
US6994161B2 (en) | 2000-04-24 | 2006-02-07 | Kevin Albert Maher | In situ thermal processing of a coal formation with a selected moisture content |
US6588504B2 (en) | 2000-04-24 | 2003-07-08 | Shell Oil Company | In situ thermal processing of a coal formation to produce nitrogen and/or sulfur containing formation fluids |
US6591907B2 (en) | 2000-04-24 | 2003-07-15 | Shell Oil Company | In situ thermal processing of a coal formation with a selected vitrinite reflectance |
US6591906B2 (en) | 2000-04-24 | 2003-07-15 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with a selected oxygen content |
US6994168B2 (en) | 2000-04-24 | 2006-02-07 | Scott Lee Wellington | In situ thermal processing of a hydrocarbon containing formation with a selected hydrogen to carbon ratio |
US6994160B2 (en) | 2000-04-24 | 2006-02-07 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce hydrocarbons having a selected carbon number range |
US6991031B2 (en) | 2000-04-24 | 2006-01-31 | Shell Oil Company | In situ thermal processing of a coal formation to convert a selected total organic carbon content into hydrocarbon products |
US8225866B2 (en) | 2000-04-24 | 2012-07-24 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation |
US6973967B2 (en) | 2000-04-24 | 2005-12-13 | Shell Oil Company | Situ thermal processing of a coal formation using pressure and/or temperature control |
US20110088904A1 (en) * | 2000-04-24 | 2011-04-21 | De Rouffignac Eric Pierre | In situ recovery from a hydrocarbon containing formation |
US7798221B2 (en) | 2000-04-24 | 2010-09-21 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation |
US20090101346A1 (en) * | 2000-04-24 | 2009-04-23 | Shell Oil Company, Inc. | In situ recovery from a hydrocarbon containing formation |
US6966372B2 (en) | 2000-04-24 | 2005-11-22 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce oxygen containing formation fluids |
US6959761B2 (en) | 2000-04-24 | 2005-11-01 | Shell Oil Company | In situ thermal processing of a coal formation with a selected ratio of heat sources to production wells |
US6953087B2 (en) | 2000-04-24 | 2005-10-11 | Shell Oil Company | Thermal processing of a hydrocarbon containing formation to increase a permeability of the formation |
US6805195B2 (en) | 2000-04-24 | 2004-10-19 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce hydrocarbon fluids and synthesis gas |
US6607033B2 (en) | 2000-04-24 | 2003-08-19 | Shell Oil Company | In Situ thermal processing of a coal formation to produce a condensate |
US6923258B2 (en) | 2000-04-24 | 2005-08-02 | Shell Oil Company | In situ thermal processsing of a hydrocarbon containing formation to produce a mixture with a selected hydrogen content |
US6609570B2 (en) | 2000-04-24 | 2003-08-26 | Shell Oil Company | In situ thermal processing of a coal formation and ammonia production |
US6913078B2 (en) | 2000-04-24 | 2005-07-05 | Shell Oil Company | In Situ thermal processing of hydrocarbons within a relatively impermeable formation |
US6910536B2 (en) | 2000-04-24 | 2005-06-28 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using a natural distributed combustor |
US6902004B2 (en) | 2000-04-24 | 2005-06-07 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using a movable heating element |
US6902003B2 (en) | 2000-04-24 | 2005-06-07 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation having a selected total organic carbon content |
US6896053B2 (en) | 2000-04-24 | 2005-05-24 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using repeating triangular patterns of heat sources |
US6889769B2 (en) | 2000-04-24 | 2005-05-10 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with a selected moisture content |
US6880635B2 (en) | 2000-04-24 | 2005-04-19 | Shell Oil Company | In situ production of synthesis gas from a coal formation, the synthesis gas having a selected H2 to CO ratio |
US6877554B2 (en) | 2000-04-24 | 2005-04-12 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using pressure and/or temperature control |
US6871707B2 (en) | 2000-04-24 | 2005-03-29 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with carbon dioxide sequestration |
US6688387B1 (en) | 2000-04-24 | 2004-02-10 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce a hydrocarbon condensate |
US6698515B2 (en) | 2000-04-24 | 2004-03-02 | Shell Oil Company | In situ thermal processing of a coal formation using a relatively slow heating rate |
US20020046883A1 (en) * | 2000-04-24 | 2002-04-25 | Wellington Scott Lee | In situ thermal processing of a coal formation using pressure and/or temperature control |
US6702016B2 (en) | 2000-04-24 | 2004-03-09 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with heat sources located at an edge of a formation layer |
US6708758B2 (en) | 2000-04-24 | 2004-03-23 | Shell Oil Company | In situ thermal processing of a coal formation leaving one or more selected unprocessed areas |
US6712137B2 (en) | 2000-04-24 | 2004-03-30 | Shell Oil Company | In situ thermal processing of a coal formation to pyrolyze a selected percentage of hydrocarbon material |
US6712135B2 (en) | 2000-04-24 | 2004-03-30 | Shell Oil Company | In situ thermal processing of a coal formation in reducing environment |
US6712136B2 (en) | 2000-04-24 | 2004-03-30 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using a selected production well spacing |
US6715547B2 (en) | 2000-04-24 | 2004-04-06 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to form a substantially uniform, high permeability formation |
US6715546B2 (en) | 2000-04-24 | 2004-04-06 | Shell Oil Company | In situ production of synthesis gas from a hydrocarbon containing formation through a heat source wellbore |
US6715548B2 (en) | 2000-04-24 | 2004-04-06 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce nitrogen containing formation fluids |
US6715549B2 (en) | 2000-04-24 | 2004-04-06 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with a selected atomic oxygen to carbon ratio |
US6719047B2 (en) | 2000-04-24 | 2004-04-13 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation in a hydrogen-rich environment |
US6722430B2 (en) | 2000-04-24 | 2004-04-20 | Shell Oil Company | In situ thermal processing of a coal formation with a selected oxygen content and/or selected O/C ratio |
US6722431B2 (en) | 2000-04-24 | 2004-04-20 | Shell Oil Company | In situ thermal processing of hydrocarbons within a relatively permeable formation |
US6722429B2 (en) | 2000-04-24 | 2004-04-20 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation leaving one or more selected unprocessed areas |
US6725921B2 (en) | 2000-04-24 | 2004-04-27 | Shell Oil Company | In situ thermal processing of a coal formation by controlling a pressure of the formation |
US6725920B2 (en) | 2000-04-24 | 2004-04-27 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to convert a selected amount of total organic carbon into hydrocarbon products |
US6725928B2 (en) | 2000-04-24 | 2004-04-27 | Shell Oil Company | In situ thermal processing of a coal formation using a distributed combustor |
US6729395B2 (en) | 2000-04-24 | 2004-05-04 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with a selected ratio of heat sources to production wells |
US6729401B2 (en) | 2000-04-24 | 2004-05-04 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation and ammonia production |
US6729397B2 (en) | 2000-04-24 | 2004-05-04 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation with a selected vitrinite reflectance |
US6729396B2 (en) | 2000-04-24 | 2004-05-04 | Shell Oil Company | In situ thermal processing of a coal formation to produce hydrocarbons having a selected carbon number range |
US6732795B2 (en) | 2000-04-24 | 2004-05-11 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to pyrolyze a selected percentage of hydrocarbon material |
US6732796B2 (en) | 2000-04-24 | 2004-05-11 | Shell Oil Company | In situ production of synthesis gas from a hydrocarbon containing formation, the synthesis gas having a selected H2 to CO ratio |
US6732794B2 (en) | 2000-04-24 | 2004-05-11 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce a mixture with a selected hydrogen content |
US6736215B2 (en) | 2000-04-24 | 2004-05-18 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation, in situ production of synthesis gas, and carbon dioxide sequestration |
US6739394B2 (en) | 2000-04-24 | 2004-05-25 | Shell Oil Company | Production of synthesis gas from a hydrocarbon containing formation |
US6739393B2 (en) | 2000-04-24 | 2004-05-25 | Shell Oil Company | In situ thermal processing of a coal formation and tuning production |
US6742589B2 (en) | 2000-04-24 | 2004-06-01 | Shell Oil Company | In situ thermal processing of a coal formation using repeating triangular patterns of heat sources |
US6742587B2 (en) | 2000-04-24 | 2004-06-01 | Shell Oil Company | In situ thermal processing of a coal formation to form a substantially uniform, relatively high permeable formation |
US6742593B2 (en) | 2000-04-24 | 2004-06-01 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using heat transfer from a heat transfer fluid to heat the formation |
US6742588B2 (en) | 2000-04-24 | 2004-06-01 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce formation fluids having a relatively low olefin content |
US6745832B2 (en) | 2000-04-24 | 2004-06-08 | Shell Oil Company | Situ thermal processing of a hydrocarbon containing formation to control product composition |
US6745831B2 (en) | 2000-04-24 | 2004-06-08 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation by controlling a pressure of the formation |
US6745837B2 (en) | 2000-04-24 | 2004-06-08 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using a controlled heating rate |
US6749021B2 (en) | 2000-04-24 | 2004-06-15 | Shell Oil Company | In situ thermal processing of a coal formation using a controlled heating rate |
US6752210B2 (en) | 2000-04-24 | 2004-06-22 | Shell Oil Company | In situ thermal processing of a coal formation using heat sources positioned within open wellbores |
US6758268B2 (en) | 2000-04-24 | 2004-07-06 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using a relatively slow heating rate |
US6761216B2 (en) | 2000-04-24 | 2004-07-13 | Shell Oil Company | In situ thermal processing of a coal formation to produce hydrocarbon fluids and synthesis gas |
US6763886B2 (en) | 2000-04-24 | 2004-07-20 | Shell Oil Company | In situ thermal processing of a coal formation with carbon dioxide sequestration |
US6820688B2 (en) | 2000-04-24 | 2004-11-23 | Shell Oil Company | In situ thermal processing of coal formation with a selected hydrogen content and/or selected H/C ratio |
US6769485B2 (en) | 2000-04-24 | 2004-08-03 | Shell Oil Company | In situ production of synthesis gas from a coal formation through a heat source wellbore |
US6769483B2 (en) | 2000-04-24 | 2004-08-03 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using conductor in conduit heat sources |
US6789625B2 (en) | 2000-04-24 | 2004-09-14 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using exposed metal heat sources |
US20030141067A1 (en) * | 2001-04-24 | 2003-07-31 | Rouffignac Eric Pierre De | In situ thermal processing of an oil shale formation to increase permeability of the formation |
US20030131995A1 (en) * | 2001-04-24 | 2003-07-17 | De Rouffignac Eric Pierre | In situ thermal processing of a relatively impermeable formation to increase permeability of the formation |
US20040211557A1 (en) * | 2001-04-24 | 2004-10-28 | Cole Anthony Thomas | Conductor-in-conduit heat sources for in situ thermal processing of an oil shale formation |
US20030080604A1 (en) * | 2001-04-24 | 2003-05-01 | Vinegar Harold J. | In situ thermal processing and inhibiting migration of fluids into or out of an in situ oil shale formation |
US20030079877A1 (en) * | 2001-04-24 | 2003-05-01 | Wellington Scott Lee | In situ thermal processing of a relatively impermeable formation in a reducing environment |
US20030209348A1 (en) * | 2001-04-24 | 2003-11-13 | Ward John Michael | In situ thermal processing and remediation of an oil shale formation |
US20030098605A1 (en) * | 2001-04-24 | 2003-05-29 | Vinegar Harold J. | In situ thermal recovery from a relatively permeable formation |
US6877555B2 (en) | 2001-04-24 | 2005-04-12 | Shell Oil Company | In situ thermal processing of an oil shale formation while inhibiting coking |
US6880633B2 (en) | 2001-04-24 | 2005-04-19 | Shell Oil Company | In situ thermal processing of an oil shale formation to produce a desired product |
US20030100451A1 (en) * | 2001-04-24 | 2003-05-29 | Messier Margaret Ann | In situ thermal recovery from a relatively permeable formation with backproduction through a heater wellbore |
US20030098149A1 (en) * | 2001-04-24 | 2003-05-29 | Wellington Scott Lee | In situ thermal recovery from a relatively permeable formation using gas to increase mobility |
US7096942B1 (en) | 2001-04-24 | 2006-08-29 | Shell Oil Company | In situ thermal processing of a relatively permeable formation while controlling pressure |
US20030102125A1 (en) * | 2001-04-24 | 2003-06-05 | Wellington Scott Lee | In situ thermal processing of a relatively permeable formation in a reducing environment |
US7066254B2 (en) | 2001-04-24 | 2006-06-27 | Shell Oil Company | In situ thermal processing of a tar sands formation |
US7055600B2 (en) | 2001-04-24 | 2006-06-06 | Shell Oil Company | In situ thermal recovery from a relatively permeable formation with controlled production rate |
US20030173078A1 (en) * | 2001-04-24 | 2003-09-18 | Wellington Scott Lee | In situ thermal processing of an oil shale formation to produce a condensate |
US20030164239A1 (en) * | 2001-04-24 | 2003-09-04 | Wellington Scott Lee | In situ thermal processing of an oil shale formation in a reducing environment |
US6915850B2 (en) | 2001-04-24 | 2005-07-12 | Shell Oil Company | In situ thermal processing of an oil shale formation having permeable and impermeable sections |
US6918443B2 (en) | 2001-04-24 | 2005-07-19 | Shell Oil Company | In situ thermal processing of an oil shale formation to produce hydrocarbons having a selected carbon number range |
US6918442B2 (en) | 2001-04-24 | 2005-07-19 | Shell Oil Company | In situ thermal processing of an oil shale formation in a reducing environment |
US6923257B2 (en) | 2001-04-24 | 2005-08-02 | Shell Oil Company | In situ thermal processing of an oil shale formation to produce a condensate |
US20030155111A1 (en) * | 2001-04-24 | 2003-08-21 | Shell Oil Co | In situ thermal processing of a tar sands formation |
US6929067B2 (en) | 2001-04-24 | 2005-08-16 | Shell Oil Company | Heat sources with conductive material for in situ thermal processing of an oil shale formation |
US7051811B2 (en) | 2001-04-24 | 2006-05-30 | Shell Oil Company | In situ thermal processing through an open wellbore in an oil shale formation |
US20030146002A1 (en) * | 2001-04-24 | 2003-08-07 | Vinegar Harold J. | Removable heat sources for in situ thermal processing of an oil shale formation |
US6948562B2 (en) | 2001-04-24 | 2005-09-27 | Shell Oil Company | Production of a blending agent using an in situ thermal process in a relatively permeable formation |
US6951247B2 (en) | 2001-04-24 | 2005-10-04 | Shell Oil Company | In situ thermal processing of an oil shale formation using horizontal heat sources |
US20030148894A1 (en) * | 2001-04-24 | 2003-08-07 | Vinegar Harold J. | In situ thermal processing of an oil shale formation using a natural distributed combustor |
US7225866B2 (en) | 2001-04-24 | 2007-06-05 | Shell Oil Company | In situ thermal processing of an oil shale formation using a pattern of heat sources |
US6964300B2 (en) | 2001-04-24 | 2005-11-15 | Shell Oil Company | In situ thermal recovery from a relatively permeable formation with backproduction through a heater wellbore |
US6966374B2 (en) | 2001-04-24 | 2005-11-22 | Shell Oil Company | In situ thermal recovery from a relatively permeable formation using gas to increase mobility |
US20030141066A1 (en) * | 2001-04-24 | 2003-07-31 | Karanikas John Michael | In situ thermal processing of an oil shale formation while inhibiting coking |
US7051807B2 (en) | 2001-04-24 | 2006-05-30 | Shell Oil Company | In situ thermal recovery from a relatively permeable formation with quality control |
US20030142964A1 (en) * | 2001-04-24 | 2003-07-31 | Wellington Scott Lee | In situ thermal processing of an oil shale formation using a controlled heating rate |
US7040400B2 (en) | 2001-04-24 | 2006-05-09 | Shell Oil Company | In situ thermal processing of a relatively impermeable formation using an open wellbore |
US7735935B2 (en) | 2001-04-24 | 2010-06-15 | Shell Oil Company | In situ thermal processing of an oil shale formation containing carbonate minerals |
US20030141068A1 (en) * | 2001-04-24 | 2003-07-31 | Pierre De Rouffignac Eric | In situ thermal processing through an open wellbore in an oil shale formation |
US20100270015A1 (en) * | 2001-04-24 | 2010-10-28 | Shell Oil Company | In situ thermal processing of an oil shale formation |
US20030136559A1 (en) * | 2001-04-24 | 2003-07-24 | Wellington Scott Lee | In situ thermal processing while controlling pressure in an oil shale formation |
US7040397B2 (en) | 2001-04-24 | 2006-05-09 | Shell Oil Company | Thermal processing of an oil shale formation to increase permeability of the formation |
US7040399B2 (en) | 2001-04-24 | 2006-05-09 | Shell Oil Company | In situ thermal processing of an oil shale formation using a controlled heating rate |
US7040398B2 (en) | 2001-04-24 | 2006-05-09 | Shell Oil Company | In situ thermal processing of a relatively permeable formation in a reducing environment |
US20030102130A1 (en) * | 2001-04-24 | 2003-06-05 | Vinegar Harold J. | In situ thermal recovery from a relatively permeable formation with quality control |
US20030136558A1 (en) * | 2001-04-24 | 2003-07-24 | Wellington Scott Lee | In situ thermal processing of an oil shale formation to produce a desired product |
US6981548B2 (en) | 2001-04-24 | 2006-01-03 | Shell Oil Company | In situ thermal recovery from a relatively permeable formation |
US20030131994A1 (en) * | 2001-04-24 | 2003-07-17 | Vinegar Harold J. | In situ thermal processing and solution mining of an oil shale formation |
US6991033B2 (en) | 2001-04-24 | 2006-01-31 | Shell Oil Company | In situ thermal processing while controlling pressure in an oil shale formation |
US6991032B2 (en) | 2001-04-24 | 2006-01-31 | Shell Oil Company | In situ thermal processing of an oil shale formation using a pattern of heat sources |
US6991036B2 (en) | 2001-04-24 | 2006-01-31 | Shell Oil Company | Thermal processing of a relatively permeable formation |
US20030131996A1 (en) * | 2001-04-24 | 2003-07-17 | Vinegar Harold J. | In situ thermal processing of an oil shale formation having permeable and impermeable sections |
US7032660B2 (en) | 2001-04-24 | 2006-04-25 | Shell Oil Company | In situ thermal processing and inhibiting migration of fluids into or out of an in situ oil shale formation |
US20030131993A1 (en) * | 2001-04-24 | 2003-07-17 | Etuan Zhang | In situ thermal processing of an oil shale formation with a selected property |
US20040211554A1 (en) * | 2001-04-24 | 2004-10-28 | Vinegar Harold J. | Heat sources with conductive material for in situ thermal processing of an oil shale formation |
US20030116315A1 (en) * | 2001-04-24 | 2003-06-26 | Wellington Scott Lee | In situ thermal processing of a relatively permeable formation |
US6994169B2 (en) | 2001-04-24 | 2006-02-07 | Shell Oil Company | In situ thermal processing of an oil shale formation with a selected property |
US20030111223A1 (en) * | 2001-04-24 | 2003-06-19 | Rouffignac Eric Pierre De | In situ thermal processing of an oil shale formation using horizontal heat sources |
US6997518B2 (en) | 2001-04-24 | 2006-02-14 | Shell Oil Company | In situ thermal processing and solution mining of an oil shale formation |
US7004251B2 (en) | 2001-04-24 | 2006-02-28 | Shell Oil Company | In situ thermal processing and remediation of an oil shale formation |
US7004247B2 (en) | 2001-04-24 | 2006-02-28 | Shell Oil Company | Conductor-in-conduit heat sources for in situ thermal processing of an oil shale formation |
US20030102126A1 (en) * | 2001-04-24 | 2003-06-05 | Sumnu-Dindoruk Meliha Deniz | In situ thermal recovery from a relatively permeable formation with controlled production rate |
US7013972B2 (en) | 2001-04-24 | 2006-03-21 | Shell Oil Company | In situ thermal processing of an oil shale formation using a natural distributed combustor |
US20030102124A1 (en) * | 2001-04-24 | 2003-06-05 | Vinegar Harold J. | In situ thermal processing of a blending agent from a relatively permeable formation |
US20050092483A1 (en) * | 2001-10-24 | 2005-05-05 | Vinegar Harold J. | In situ thermal processing of a hydrocarbon containing formation using a natural distributed combustor |
US20030196801A1 (en) * | 2001-10-24 | 2003-10-23 | Vinegar Harold J. | In situ thermal processing of a hydrocarbon containing formation via backproducing through a heater well |
US20070209799A1 (en) * | 2001-10-24 | 2007-09-13 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation |
US20040040715A1 (en) * | 2001-10-24 | 2004-03-04 | Wellington Scott Lee | In situ production of a blending agent from a hydrocarbon containing formation |
US7461691B2 (en) | 2001-10-24 | 2008-12-09 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation |
US8627887B2 (en) | 2001-10-24 | 2014-01-14 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation |
US7090013B2 (en) | 2001-10-24 | 2006-08-15 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation to produce heated fluids |
US7051808B1 (en) | 2001-10-24 | 2006-05-30 | Shell Oil Company | Seismic monitoring of in situ conversion in a hydrocarbon containing formation |
US6932155B2 (en) | 2001-10-24 | 2005-08-23 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation via backproducing through a heater well |
US20030173081A1 (en) * | 2001-10-24 | 2003-09-18 | Vinegar Harold J. | In situ thermal processing of an oil reservoir formation |
US7063145B2 (en) | 2001-10-24 | 2006-06-20 | Shell Oil Company | Methods and systems for heating a hydrocarbon containing formation in situ with an opening contacting the earth's surface at two locations |
US20030173085A1 (en) * | 2001-10-24 | 2003-09-18 | Vinegar Harold J. | Upgrading and mining of coal |
US7066257B2 (en) | 2001-10-24 | 2006-06-27 | Shell Oil Company | In situ recovery from lean and rich zones in a hydrocarbon containing formation |
US7128153B2 (en) | 2001-10-24 | 2006-10-31 | Shell Oil Company | Treatment of a hydrocarbon containing formation after heating |
US7077198B2 (en) * | 2001-10-24 | 2006-07-18 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation using barriers |
US7077199B2 (en) | 2001-10-24 | 2006-07-18 | Shell Oil Company | In situ thermal processing of an oil reservoir formation |
US20030196810A1 (en) * | 2001-10-24 | 2003-10-23 | Vinegar Harold J. | Treatment of a hydrocarbon containing formation after heating |
US6991045B2 (en) | 2001-10-24 | 2006-01-31 | Shell Oil Company | Forming openings in a hydrocarbon containing formation using magnetic tracking |
US6969123B2 (en) | 2001-10-24 | 2005-11-29 | Shell Oil Company | Upgrading and mining of coal |
US20030205378A1 (en) * | 2001-10-24 | 2003-11-06 | Wellington Scott Lee | In situ recovery from lean and rich zones in a hydrocarbon containing formation |
US7086465B2 (en) | 2001-10-24 | 2006-08-08 | Shell Oil Company | In situ production of a blending agent from a hydrocarbon containing formation |
US20030201098A1 (en) * | 2001-10-24 | 2003-10-30 | Karanikas John Michael | In situ recovery from a hydrocarbon containing formation using one or more simulations |
US7100994B2 (en) | 2001-10-24 | 2006-09-05 | Shell Oil Company | Producing hydrocarbons and non-hydrocarbon containing materials when treating a hydrocarbon containing formation |
US7104319B2 (en) | 2001-10-24 | 2006-09-12 | Shell Oil Company | In situ thermal processing of a heavy oil diatomite formation |
US7114566B2 (en) | 2001-10-24 | 2006-10-03 | Shell Oil Company | In situ thermal processing of a hydrocarbon containing formation using a natural distributed combustor |
US7165615B2 (en) | 2001-10-24 | 2007-01-23 | Shell Oil Company | In situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden |
US7156176B2 (en) | 2001-10-24 | 2007-01-02 | Shell Oil Company | Installation and use of removable heaters in a hydrocarbon containing formation |
US8238730B2 (en) | 2002-10-24 | 2012-08-07 | Shell Oil Company | High voltage temperature limited heaters |
US8224164B2 (en) | 2002-10-24 | 2012-07-17 | Shell Oil Company | Insulated conductor temperature limited heaters |
US7121341B2 (en) | 2002-10-24 | 2006-10-17 | Shell Oil Company | Conductor-in-conduit temperature limited heaters |
US7073578B2 (en) | 2002-10-24 | 2006-07-11 | Shell Oil Company | Staged and/or patterned heating during in situ thermal processing of a hydrocarbon containing formation |
US20040144541A1 (en) * | 2002-10-24 | 2004-07-29 | Picha Mark Gregory | Forming wellbores using acoustic methods |
US8224163B2 (en) | 2002-10-24 | 2012-07-17 | Shell Oil Company | Variable frequency temperature limited heaters |
US7219734B2 (en) | 2002-10-24 | 2007-05-22 | Shell Oil Company | Inhibiting wellbore deformation during in situ thermal processing of a hydrocarbon containing formation |
US20070034568A1 (en) * | 2003-04-08 | 2007-02-15 | Foster Neil R | Particle synthesis apparatus and method |
US7121342B2 (en) | 2003-04-24 | 2006-10-17 | Shell Oil Company | Thermal processes for subsurface formations |
US7360588B2 (en) | 2003-04-24 | 2008-04-22 | Shell Oil Company | Thermal processes for subsurface formations |
US8579031B2 (en) | 2003-04-24 | 2013-11-12 | Shell Oil Company | Thermal processes for subsurface formations |
US7640980B2 (en) | 2003-04-24 | 2010-01-05 | Shell Oil Company | Thermal processes for subsurface formations |
US7942203B2 (en) | 2003-04-24 | 2011-05-17 | Shell Oil Company | Thermal processes for subsurface formations |
US20050269094A1 (en) * | 2004-04-23 | 2005-12-08 | Harris Christopher K | Triaxial temperature limited heater |
US7353872B2 (en) | 2004-04-23 | 2008-04-08 | Shell Oil Company | Start-up of temperature limited heaters using direct current (DC) |
US20050269093A1 (en) * | 2004-04-23 | 2005-12-08 | Sandberg Chester L | Variable frequency temperature limited heaters |
US20050269091A1 (en) * | 2004-04-23 | 2005-12-08 | Guillermo Pastor-Sanz | Reducing viscosity of oil for production from a hydrocarbon containing formation |
US20050269313A1 (en) * | 2004-04-23 | 2005-12-08 | Vinegar Harold J | Temperature limited heaters with high power factors |
US20050269092A1 (en) * | 2004-04-23 | 2005-12-08 | Vinegar Harold J | Vacuum pumping of conductor-in-conduit heaters |
US7510000B2 (en) | 2004-04-23 | 2009-03-31 | Shell Oil Company | Reducing viscosity of oil for production from a hydrocarbon containing formation |
US7490665B2 (en) | 2004-04-23 | 2009-02-17 | Shell Oil Company | Variable frequency temperature limited heaters |
US7481274B2 (en) | 2004-04-23 | 2009-01-27 | Shell Oil Company | Temperature limited heaters with relatively constant current |
US20050269089A1 (en) * | 2004-04-23 | 2005-12-08 | Sandberg Chester L | Temperature limited heaters using modulated DC power |
US20050269088A1 (en) * | 2004-04-23 | 2005-12-08 | Vinegar Harold J | Inhibiting effects of sloughing in wellbores |
US20050269095A1 (en) * | 2004-04-23 | 2005-12-08 | Fairbanks Michael D | Inhibiting reflux in a heated well of an in situ conversion system |
US7431076B2 (en) | 2004-04-23 | 2008-10-07 | Shell Oil Company | Temperature limited heaters using modulated DC power |
US7424915B2 (en) | 2004-04-23 | 2008-09-16 | Shell Oil Company | Vacuum pumping of conductor-in-conduit heaters |
US20050269077A1 (en) * | 2004-04-23 | 2005-12-08 | Sandberg Chester L | Start-up of temperature limited heaters using direct current (DC) |
US20050269090A1 (en) * | 2004-04-23 | 2005-12-08 | Vinegar Harold J | Temperature limited heaters with thermally conductive fluid used to heat subsurface formations |
US20060005968A1 (en) * | 2004-04-23 | 2006-01-12 | Vinegar Harold J | Temperature limited heaters with relatively constant current |
US20060289536A1 (en) * | 2004-04-23 | 2006-12-28 | Vinegar Harold J | Subsurface electrical heaters using nitride insulation |
US8355623B2 (en) | 2004-04-23 | 2013-01-15 | Shell Oil Company | Temperature limited heaters with high power factors |
US7320364B2 (en) | 2004-04-23 | 2008-01-22 | Shell Oil Company | Inhibiting reflux in a heated well of an in situ conversion system |
US7383877B2 (en) | 2004-04-23 | 2008-06-10 | Shell Oil Company | Temperature limited heaters with thermally conductive fluid used to heat subsurface formations |
US7370704B2 (en) | 2004-04-23 | 2008-05-13 | Shell Oil Company | Triaxial temperature limited heater |
US7357180B2 (en) | 2004-04-23 | 2008-04-15 | Shell Oil Company | Inhibiting effects of sloughing in wellbores |
US20070045267A1 (en) * | 2005-04-22 | 2007-03-01 | Vinegar Harold J | Subsurface connection methods for subsurface heaters |
US20070133961A1 (en) * | 2005-04-22 | 2007-06-14 | Fairbanks Michael D | Methods and systems for producing fluid from an in situ conversion process |
US7575053B2 (en) | 2005-04-22 | 2009-08-18 | Shell Oil Company | Low temperature monitoring system for subsurface barriers |
US20070119098A1 (en) * | 2005-04-22 | 2007-05-31 | Zaida Diaz | Treatment of gas from an in situ conversion process |
US20070045268A1 (en) * | 2005-04-22 | 2007-03-01 | Vinegar Harold J | Varying properties along lengths of temperature limited heaters |
US7546873B2 (en) | 2005-04-22 | 2009-06-16 | Shell Oil Company | Low temperature barriers for use with in situ processes |
US7575052B2 (en) | 2005-04-22 | 2009-08-18 | Shell Oil Company | In situ conversion process utilizing a closed loop heating system |
US20070045266A1 (en) * | 2005-04-22 | 2007-03-01 | Sandberg Chester L | In situ conversion process utilizing a closed loop heating system |
US20070108201A1 (en) * | 2005-04-22 | 2007-05-17 | Vinegar Harold J | Insulated conductor temperature limited heater for subsurface heating coupled in a three-phase wye configuration |
US20070045265A1 (en) * | 2005-04-22 | 2007-03-01 | Mckinzie Billy J Ii | Low temperature barriers with heat interceptor wells for in situ processes |
US7527094B2 (en) | 2005-04-22 | 2009-05-05 | Shell Oil Company | Double barrier system for an in situ conversion process |
US20070133959A1 (en) * | 2005-04-22 | 2007-06-14 | Vinegar Harold J | Grouped exposed metal heaters |
US8230927B2 (en) | 2005-04-22 | 2012-07-31 | Shell Oil Company | Methods and systems for producing fluid from an in situ conversion process |
US8233782B2 (en) | 2005-04-22 | 2012-07-31 | Shell Oil Company | Grouped exposed metal heaters |
US7831134B2 (en) | 2005-04-22 | 2010-11-09 | Shell Oil Company | Grouped exposed metal heaters |
US7831133B2 (en) | 2005-04-22 | 2010-11-09 | Shell Oil Company | Insulated conductor temperature limited heater for subsurface heating coupled in a three-phase WYE configuration |
US8224165B2 (en) | 2005-04-22 | 2012-07-17 | Shell Oil Company | Temperature limited heater utilizing non-ferromagnetic conductor |
US7500528B2 (en) | 2005-04-22 | 2009-03-10 | Shell Oil Company | Low temperature barrier wellbores formed using water flushing |
US20070133960A1 (en) * | 2005-04-22 | 2007-06-14 | Vinegar Harold J | In situ conversion process systems utilizing wellbores in at least two regions of a formation |
US8070840B2 (en) | 2005-04-22 | 2011-12-06 | Shell Oil Company | Treatment of gas from an in situ conversion process |
US8027571B2 (en) | 2005-04-22 | 2011-09-27 | Shell Oil Company | In situ conversion process systems utilizing wellbores in at least two regions of a formation |
US20080217321A1 (en) * | 2005-04-22 | 2008-09-11 | Vinegar Harold J | Temperature limited heater utilizing non-ferromagnetic conductor |
US7986869B2 (en) | 2005-04-22 | 2011-07-26 | Shell Oil Company | Varying properties along lengths of temperature limited heaters |
US7860377B2 (en) | 2005-04-22 | 2010-12-28 | Shell Oil Company | Subsurface connection methods for subsurface heaters |
US20070108200A1 (en) * | 2005-04-22 | 2007-05-17 | Mckinzie Billy J Ii | Low temperature barrier wellbores formed using water flushing |
US20070144732A1 (en) * | 2005-04-22 | 2007-06-28 | Kim Dong S | Low temperature barriers for use with in situ processes |
US7435037B2 (en) | 2005-04-22 | 2008-10-14 | Shell Oil Company | Low temperature barriers with heat interceptor wells for in situ processes |
US7942197B2 (en) | 2005-04-22 | 2011-05-17 | Shell Oil Company | Methods and systems for producing fluid from an in situ conversion process |
US20070137856A1 (en) * | 2005-04-22 | 2007-06-21 | Mckinzie Billy J | Double barrier system for an in situ conversion process |
US7635025B2 (en) | 2005-10-24 | 2009-12-22 | Shell Oil Company | Cogeneration systems and processes for treating hydrocarbon containing formations |
US20070095536A1 (en) * | 2005-10-24 | 2007-05-03 | Vinegar Harold J | Cogeneration systems and processes for treating hydrocarbon containing formations |
US20110168394A1 (en) * | 2005-10-24 | 2011-07-14 | Shell Oil Company | Methods of producing alkylated hydrocarbons from an in situ heat treatment process liquid |
US8151880B2 (en) | 2005-10-24 | 2012-04-10 | Shell Oil Company | Methods of making transportation fuel |
US20070131419A1 (en) * | 2005-10-24 | 2007-06-14 | Maria Roes Augustinus W | Methods of producing alkylated hydrocarbons from an in situ heat treatment process liquid |
US20070221377A1 (en) * | 2005-10-24 | 2007-09-27 | Vinegar Harold J | Solution mining systems and methods for treating hydrocarbon containing formations |
US7559367B2 (en) | 2005-10-24 | 2009-07-14 | Shell Oil Company | Temperature limited heater with a conduit substantially electrically isolated from the formation |
US7559368B2 (en) | 2005-10-24 | 2009-07-14 | Shell Oil Company | Solution mining systems and methods for treating hydrocarbon containing formations |
US7556096B2 (en) | 2005-10-24 | 2009-07-07 | Shell Oil Company | Varying heating in dawsonite zones in hydrocarbon containing formations |
US20070131420A1 (en) * | 2005-10-24 | 2007-06-14 | Weijian Mo | Methods of cracking a crude product to produce additional crude products |
US7556095B2 (en) | 2005-10-24 | 2009-07-07 | Shell Oil Company | Solution mining dawsonite from hydrocarbon containing formations with a chelating agent |
US20070131428A1 (en) * | 2005-10-24 | 2007-06-14 | Willem Cornelis Den Boestert J | Methods of filtering a liquid stream produced from an in situ heat treatment process |
US20070125533A1 (en) * | 2005-10-24 | 2007-06-07 | Minderhoud Johannes K | Methods of hydrotreating a liquid stream to remove clogging compounds |
US7562706B2 (en) | 2005-10-24 | 2009-07-21 | Shell Oil Company | Systems and methods for producing hydrocarbons from tar sands formations |
US8606091B2 (en) | 2005-10-24 | 2013-12-10 | Shell Oil Company | Subsurface heaters with low sulfidation rates |
US20090301724A1 (en) * | 2005-10-24 | 2009-12-10 | Shell Oil Company | Methods of producing alkylated hydrocarbons from an in situ heat treatment process liquid |
US7549470B2 (en) | 2005-10-24 | 2009-06-23 | Shell Oil Company | Solution mining and heating by oxidation for treating hydrocarbon containing formations |
US20070127897A1 (en) * | 2005-10-24 | 2007-06-07 | John Randy C | Subsurface heaters with low sulfidation rates |
US20080107577A1 (en) * | 2005-10-24 | 2008-05-08 | Vinegar Harold J | Varying heating in dawsonite zones in hydrocarbon containing formations |
US7591310B2 (en) | 2005-10-24 | 2009-09-22 | Shell Oil Company | Methods of hydrotreating a liquid stream to remove clogging compounds |
US7584789B2 (en) | 2005-10-24 | 2009-09-08 | Shell Oil Company | Methods of cracking a crude product to produce additional crude products |
US7581589B2 (en) | 2005-10-24 | 2009-09-01 | Shell Oil Company | Methods of producing alkylated hydrocarbons from an in situ heat treatment process liquid |
US20070131427A1 (en) * | 2005-10-24 | 2007-06-14 | Ruijian Li | Systems and methods for producing hydrocarbons from tar sands formations |
US9605522B2 (en) | 2006-03-29 | 2017-03-28 | Pioneer Energy, Inc. | Apparatus and method for extracting petroleum from underground sites using reformed gases |
US20090236093A1 (en) * | 2006-03-29 | 2009-09-24 | Pioneer Energy, Inc. | Apparatus and Method for Extracting Petroleum from Underground Sites Using Reformed Gases |
WO2007117933A3 (en) * | 2006-03-29 | 2007-12-06 | Robert M Zubrin | Apparatus, methods, and systems for extracting petroleum and natural gas |
WO2007117933A2 (en) * | 2006-03-29 | 2007-10-18 | Zubrin Robert M | Apparatus, methods, and systems for extracting petroleum and natural gas |
US7506685B2 (en) * | 2006-03-29 | 2009-03-24 | Pioneer Energy, Inc. | Apparatus and method for extracting petroleum from underground sites using reformed gases |
US20070227729A1 (en) * | 2006-03-29 | 2007-10-04 | Pioneer Invention, Inc. D/B/A Pioneer Astronautics | Apparatus and method for extracting petroleum from underground sites using reformed gases |
US8602095B2 (en) | 2006-03-29 | 2013-12-10 | Pioneer Energy, Inc. | Apparatus and method for extracting petroleum from underground sites using reformed gases |
US20080038144A1 (en) * | 2006-04-21 | 2008-02-14 | Maziasz Phillip J | High strength alloys |
US8083813B2 (en) | 2006-04-21 | 2011-12-27 | Shell Oil Company | Methods of producing transportation fuel |
US7635023B2 (en) | 2006-04-21 | 2009-12-22 | Shell Oil Company | Time sequenced heating of multiple layers in a hydrocarbon containing formation |
US8857506B2 (en) | 2006-04-21 | 2014-10-14 | Shell Oil Company | Alternate energy source usage methods for in situ heat treatment processes |
US20080035348A1 (en) * | 2006-04-21 | 2008-02-14 | Vitek John M | Temperature limited heaters using phase transformation of ferromagnetic material |
US20080035347A1 (en) * | 2006-04-21 | 2008-02-14 | Brady Michael P | Adjusting alloy compositions for selected properties in temperature limited heaters |
US20080035346A1 (en) * | 2006-04-21 | 2008-02-14 | Vijay Nair | Methods of producing transportation fuel |
US20080035705A1 (en) * | 2006-04-21 | 2008-02-14 | Menotti James L | Welding shield for coupling heaters |
US7793722B2 (en) | 2006-04-21 | 2010-09-14 | Shell Oil Company | Non-ferromagnetic overburden casing |
US7785427B2 (en) | 2006-04-21 | 2010-08-31 | Shell Oil Company | High strength alloys |
US7866385B2 (en) | 2006-04-21 | 2011-01-11 | Shell Oil Company | Power systems utilizing the heat of produced formation fluid |
US20100272595A1 (en) * | 2006-04-21 | 2010-10-28 | Shell Oil Company | High strength alloys |
US20080173449A1 (en) * | 2006-04-21 | 2008-07-24 | Thomas David Fowler | Sour gas injection for use with in situ heat treatment |
US7533719B2 (en) | 2006-04-21 | 2009-05-19 | Shell Oil Company | Wellhead with non-ferromagnetic materials |
US7912358B2 (en) | 2006-04-21 | 2011-03-22 | Shell Oil Company | Alternate energy source usage for in situ heat treatment processes |
US8192682B2 (en) | 2006-04-21 | 2012-06-05 | Shell Oil Company | High strength alloys |
US7597147B2 (en) | 2006-04-21 | 2009-10-06 | Shell Oil Company | Temperature limited heaters using phase transformation of ferromagnetic material |
US7604052B2 (en) | 2006-04-21 | 2009-10-20 | Shell Oil Company | Compositions produced using an in situ heat treatment process |
US7683296B2 (en) | 2006-04-21 | 2010-03-23 | Shell Oil Company | Adjusting alloy compositions for selected properties in temperature limited heaters |
US7673786B2 (en) | 2006-04-21 | 2010-03-09 | Shell Oil Company | Welding shield for coupling heaters |
US7610962B2 (en) | 2006-04-21 | 2009-11-03 | Shell Oil Company | Sour gas injection for use with in situ heat treatment |
US20080173450A1 (en) * | 2006-04-21 | 2008-07-24 | Bernard Goldberg | Time sequenced heating of multiple layers in a hydrocarbon containing formation |
US20080173442A1 (en) * | 2006-04-21 | 2008-07-24 | Vinegar Harold J | Sulfur barrier for use with in situ processes for treating formations |
US20080174115A1 (en) * | 2006-04-21 | 2008-07-24 | Gene Richard Lambirth | Power systems utilizing the heat of produced formation fluid |
US20080173444A1 (en) * | 2006-04-21 | 2008-07-24 | Francis Marion Stone | Alternate energy source usage for in situ heat treatment processes |
US7631689B2 (en) | 2006-04-21 | 2009-12-15 | Shell Oil Company | Sulfur barrier for use with in situ processes for treating formations |
US7871036B2 (en) | 2006-06-06 | 2011-01-18 | Pioneer Astronautics | Apparatus for generation and use of lift gas |
US7735777B2 (en) | 2006-06-06 | 2010-06-15 | Pioneer Astronautics | Apparatus for generation and use of lift gas |
US20070278344A1 (en) * | 2006-06-06 | 2007-12-06 | Pioneer Invention, Inc. D/B/A Pioneer Astronautics | Apparatus and Method for Producing Lift Gas and Uses Thereof |
US8191630B2 (en) | 2006-10-20 | 2012-06-05 | Shell Oil Company | Creating fluid injectivity in tar sands formations |
US7703513B2 (en) | 2006-10-20 | 2010-04-27 | Shell Oil Company | Wax barrier for use with in situ processes for treating formations |
US7631690B2 (en) | 2006-10-20 | 2009-12-15 | Shell Oil Company | Heating hydrocarbon containing formations in a spiral startup staged sequence |
US7644765B2 (en) | 2006-10-20 | 2010-01-12 | Shell Oil Company | Heating tar sands formations while controlling pressure |
US20080142216A1 (en) * | 2006-10-20 | 2008-06-19 | Vinegar Harold J | Treating tar sands formations with dolomite |
US7673681B2 (en) | 2006-10-20 | 2010-03-09 | Shell Oil Company | Treating tar sands formations with karsted zones |
US7677314B2 (en) | 2006-10-20 | 2010-03-16 | Shell Oil Company | Method of condensing vaporized water in situ to treat tar sands formations |
US7677310B2 (en) | 2006-10-20 | 2010-03-16 | Shell Oil Company | Creating and maintaining a gas cap in tar sands formations |
US20080142217A1 (en) * | 2006-10-20 | 2008-06-19 | Roelof Pieterson | Using geothermal energy to heat a portion of a formation for an in situ heat treatment process |
US7681647B2 (en) | 2006-10-20 | 2010-03-23 | Shell Oil Company | Method of producing drive fluid in situ in tar sands formations |
US20080135244A1 (en) * | 2006-10-20 | 2008-06-12 | David Scott Miller | Heating hydrocarbon containing formations in a line drive staged process |
US20080185147A1 (en) * | 2006-10-20 | 2008-08-07 | Vinegar Harold J | Wax barrier for use with in situ processes for treating formations |
US20080217003A1 (en) * | 2006-10-20 | 2008-09-11 | Myron Ira Kuhlman | Gas injection to inhibit migration during an in situ heat treatment process |
US20080217004A1 (en) * | 2006-10-20 | 2008-09-11 | De Rouffignac Eric Pierre | Heating hydrocarbon containing formations in a checkerboard pattern staged process |
US20080217015A1 (en) * | 2006-10-20 | 2008-09-11 | Vinegar Harold J | Heating hydrocarbon containing formations in a spiral startup staged sequence |
US7635024B2 (en) | 2006-10-20 | 2009-12-22 | Shell Oil Company | Heating tar sands formations to visbreaking temperatures |
US20080277113A1 (en) * | 2006-10-20 | 2008-11-13 | George Leo Stegemeier | Heating tar sands formations while controlling pressure |
US20090014180A1 (en) * | 2006-10-20 | 2009-01-15 | George Leo Stegemeier | Moving hydrocarbons through portions of tar sands formations with a fluid |
US20080135253A1 (en) * | 2006-10-20 | 2008-06-12 | Vinegar Harold J | Treating tar sands formations with karsted zones |
US20080135254A1 (en) * | 2006-10-20 | 2008-06-12 | Vinegar Harold J | In situ heat treatment process utilizing a closed loop heating system |
US7717171B2 (en) | 2006-10-20 | 2010-05-18 | Shell Oil Company | Moving hydrocarbons through portions of tar sands formations with a fluid |
US7730947B2 (en) | 2006-10-20 | 2010-06-08 | Shell Oil Company | Creating fluid injectivity in tar sands formations |
US7730945B2 (en) | 2006-10-20 | 2010-06-08 | Shell Oil Company | Using geothermal energy to heat a portion of a formation for an in situ heat treatment process |
US7730946B2 (en) | 2006-10-20 | 2010-06-08 | Shell Oil Company | Treating tar sands formations with dolomite |
US7540324B2 (en) | 2006-10-20 | 2009-06-02 | Shell Oil Company | Heating hydrocarbon containing formations in a checkerboard pattern staged process |
US7562707B2 (en) | 2006-10-20 | 2009-07-21 | Shell Oil Company | Heating hydrocarbon containing formations in a line drive staged process |
US20090014181A1 (en) * | 2006-10-20 | 2009-01-15 | Vinegar Harold J | Creating and maintaining a gas cap in tar sands formations |
US7845411B2 (en) | 2006-10-20 | 2010-12-07 | Shell Oil Company | In situ heat treatment process utilizing a closed loop heating system |
US7841401B2 (en) | 2006-10-20 | 2010-11-30 | Shell Oil Company | Gas injection to inhibit migration during an in situ heat treatment process |
US8555971B2 (en) | 2006-10-20 | 2013-10-15 | Shell Oil Company | Treating tar sands formations with dolomite |
US20100276141A1 (en) * | 2006-10-20 | 2010-11-04 | Shell Oil Company | Creating fluid injectivity in tar sands formations |
US20080128134A1 (en) * | 2006-10-20 | 2008-06-05 | Ramesh Raju Mudunuri | Producing drive fluid in situ in tar sands formations |
US8381815B2 (en) | 2007-04-20 | 2013-02-26 | Shell Oil Company | Production from multiple zones of a tar sands formation |
US8662175B2 (en) | 2007-04-20 | 2014-03-04 | Shell Oil Company | Varying properties of in situ heat treatment of a tar sands formation based on assessed viscosities |
US20090095476A1 (en) * | 2007-04-20 | 2009-04-16 | Scott Vinh Nguyen | Molten salt as a heat transfer fluid for heating a subsurface formation |
US7950453B2 (en) | 2007-04-20 | 2011-05-31 | Shell Oil Company | Downhole burner systems and methods for heating subsurface formations |
US9181780B2 (en) | 2007-04-20 | 2015-11-10 | Shell Oil Company | Controlling and assessing pressure conditions during treatment of tar sands formations |
US20090095479A1 (en) * | 2007-04-20 | 2009-04-16 | John Michael Karanikas | Production from multiple zones of a tar sands formation |
US20090084547A1 (en) * | 2007-04-20 | 2009-04-02 | Walter Farman Farmayan | Downhole burner systems and methods for heating subsurface formations |
US7798220B2 (en) | 2007-04-20 | 2010-09-21 | Shell Oil Company | In situ heat treatment of a tar sands formation after drive process treatment |
US8791396B2 (en) | 2007-04-20 | 2014-07-29 | Shell Oil Company | Floating insulated conductors for heating subsurface formations |
US20090078461A1 (en) * | 2007-04-20 | 2009-03-26 | Arthur James Mansure | Drilling subsurface wellbores with cutting structures |
US20090071652A1 (en) * | 2007-04-20 | 2009-03-19 | Vinegar Harold J | In situ heat treatment from multiple layers of a tar sands formation |
US7832484B2 (en) | 2007-04-20 | 2010-11-16 | Shell Oil Company | Molten salt as a heat transfer fluid for heating a subsurface formation |
US20090321075A1 (en) * | 2007-04-20 | 2009-12-31 | Christopher Kelvin Harris | Parallel heater system for subsurface formations |
US7841425B2 (en) | 2007-04-20 | 2010-11-30 | Shell Oil Company | Drilling subsurface wellbores with cutting structures |
US7841408B2 (en) | 2007-04-20 | 2010-11-30 | Shell Oil Company | In situ heat treatment from multiple layers of a tar sands formation |
US20090126929A1 (en) * | 2007-04-20 | 2009-05-21 | Vinegar Harold J | Treating nahcolite containing formations and saline zones |
US7849922B2 (en) | 2007-04-20 | 2010-12-14 | Shell Oil Company | In situ recovery from residually heated sections in a hydrocarbon containing formation |
US8042610B2 (en) | 2007-04-20 | 2011-10-25 | Shell Oil Company | Parallel heater system for subsurface formations |
US20090090509A1 (en) * | 2007-04-20 | 2009-04-09 | Vinegar Harold J | In situ recovery from residually heated sections in a hydrocarbon containing formation |
US8327681B2 (en) | 2007-04-20 | 2012-12-11 | Shell Oil Company | Wellbore manufacturing processes for in situ heat treatment processes |
US20090095477A1 (en) * | 2007-04-20 | 2009-04-16 | Scott Vinh Nguyen | Heating systems for heating subsurface formations |
US20090120646A1 (en) * | 2007-04-20 | 2009-05-14 | Dong Sub Kim | Electrically isolating insulated conductor heater |
US20090095478A1 (en) * | 2007-04-20 | 2009-04-16 | John Michael Karanikas | Varying properties of in situ heat treatment of a tar sands formation based on assessed viscosities |
US7931086B2 (en) | 2007-04-20 | 2011-04-26 | Shell Oil Company | Heating systems for heating subsurface formations |
US20090095480A1 (en) * | 2007-04-20 | 2009-04-16 | Vinegar Harold J | In situ heat treatment of a tar sands formation after drive process treatment |
US8459359B2 (en) | 2007-04-20 | 2013-06-11 | Shell Oil Company | Treating nahcolite containing formations and saline zones |
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 |
US20100314136A1 (en) * | 2007-05-20 | 2010-12-16 | Zubrin Robert M | Systems and methods for generating in-situ carbon dioxide driver gas for use in enhanced oil recovery |
US9605523B2 (en) | 2007-05-20 | 2017-03-28 | Pioneer Energy, Inc. | Systems and methods for generating in-situ carbon dioxide driver gas for use in enhanced oil recovery |
US20080296018A1 (en) * | 2007-05-29 | 2008-12-04 | Zubrin Robert M | System and method for extracting petroleum and generating electricity using natural gas or local petroleum |
US20090194282A1 (en) * | 2007-10-19 | 2009-08-06 | Gary Lee Beer | In situ oxidation of subsurface formations |
US8536497B2 (en) | 2007-10-19 | 2013-09-17 | Shell Oil Company | Methods for forming long subsurface heaters |
US8011451B2 (en) | 2007-10-19 | 2011-09-06 | Shell Oil Company | Ranging methods for developing wellbores in subsurface formations |
US20090200031A1 (en) * | 2007-10-19 | 2009-08-13 | David Scott Miller | Irregular spacing of heat sources for treating hydrocarbon containing formations |
US20090200025A1 (en) * | 2007-10-19 | 2009-08-13 | Jose Luis Bravo | High temperature methods for forming oxidizer fuel |
US20090200854A1 (en) * | 2007-10-19 | 2009-08-13 | Vinegar Harold J | Solution mining and in situ treatment of nahcolite beds |
US20090189617A1 (en) * | 2007-10-19 | 2009-07-30 | David Burns | Continuous subsurface heater temperature measurement |
US8113272B2 (en) | 2007-10-19 | 2012-02-14 | Shell Oil Company | Three-phase heaters with common overburden sections for heating subsurface formations |
US8146669B2 (en) | 2007-10-19 | 2012-04-03 | Shell Oil Company | Multi-step heater deployment in a subsurface formation |
US8146661B2 (en) | 2007-10-19 | 2012-04-03 | Shell Oil Company | Cryogenic treatment of gas |
US20090194524A1 (en) * | 2007-10-19 | 2009-08-06 | Dong Sub Kim | Methods for forming long subsurface heaters |
US7866388B2 (en) | 2007-10-19 | 2011-01-11 | Shell Oil Company | High temperature methods for forming oxidizer fuel |
US7866386B2 (en) | 2007-10-19 | 2011-01-11 | Shell Oil Company | In situ oxidation of subsurface formations |
US8162059B2 (en) | 2007-10-19 | 2012-04-24 | Shell Oil Company | Induction heaters used to heat subsurface formations |
US8276661B2 (en) | 2007-10-19 | 2012-10-02 | Shell Oil Company | Heating subsurface formations by oxidizing fuel on a fuel carrier |
US8272455B2 (en) | 2007-10-19 | 2012-09-25 | Shell Oil Company | Methods for forming wellbores in heated formations |
US20090194329A1 (en) * | 2007-10-19 | 2009-08-06 | Rosalvina Ramona Guimerans | Methods for forming wellbores in heated formations |
US20090194333A1 (en) * | 2007-10-19 | 2009-08-06 | Macdonald Duncan | Ranging methods for developing wellbores in subsurface formations |
US8196658B2 (en) | 2007-10-19 | 2012-06-12 | Shell Oil Company | Irregular spacing of heat sources for treating hydrocarbon containing formations |
US20090194269A1 (en) * | 2007-10-19 | 2009-08-06 | Vinegar Harold J | Three-phase heaters with common overburden sections for heating subsurface formations |
US8240774B2 (en) | 2007-10-19 | 2012-08-14 | Shell Oil Company | Solution mining and in situ treatment of nahcolite beds |
US8636323B2 (en) | 2008-04-18 | 2014-01-28 | Shell Oil Company | Mines and tunnels for use in treating subsurface hydrocarbon containing formations |
US20090272535A1 (en) * | 2008-04-18 | 2009-11-05 | David Booth Burns | Using tunnels for treating subsurface hydrocarbon containing formations |
US20090272533A1 (en) * | 2008-04-18 | 2009-11-05 | David Booth Burns | Heated fluid flow in mines and tunnels used in heating subsurface hydrocarbon containing formations |
US20090260824A1 (en) * | 2008-04-18 | 2009-10-22 | David Booth Burns | Hydrocarbon production from mines and tunnels used in treating subsurface hydrocarbon containing formations |
US20090260823A1 (en) * | 2008-04-18 | 2009-10-22 | Robert George Prince-Wright | Mines and tunnels for use in treating subsurface hydrocarbon containing formations |
US20090272578A1 (en) * | 2008-04-18 | 2009-11-05 | Macdonald Duncan Charles | Dual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations |
US8752904B2 (en) | 2008-04-18 | 2014-06-17 | Shell Oil Company | Heated fluid flow in mines and tunnels used in heating subsurface hydrocarbon containing formations |
US8162405B2 (en) | 2008-04-18 | 2012-04-24 | Shell Oil Company | Using tunnels for treating subsurface hydrocarbon containing formations |
US8562078B2 (en) | 2008-04-18 | 2013-10-22 | Shell Oil Company | Hydrocarbon production from mines and tunnels used in treating subsurface hydrocarbon containing formations |
US8151907B2 (en) | 2008-04-18 | 2012-04-10 | Shell Oil Company | Dual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations |
US20100071904A1 (en) * | 2008-04-18 | 2010-03-25 | Shell Oil Company | Hydrocarbon production from mines and tunnels used in treating subsurface hydrocarbon containing formations |
US8177305B2 (en) | 2008-04-18 | 2012-05-15 | Shell Oil Company | Heater connections in mines and tunnels for use in treating subsurface hydrocarbon containing formations |
US8172335B2 (en) | 2008-04-18 | 2012-05-08 | Shell Oil Company | Electrical current flow between tunnels for use in heating subsurface hydrocarbon containing formations |
US9528322B2 (en) | 2008-04-18 | 2016-12-27 | Shell Oil Company | Dual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations |
US20100088951A1 (en) * | 2008-07-17 | 2010-04-15 | Pioneer Astronautics | Novel Methods of Higher Alcohol Synthesis |
US8785699B2 (en) | 2008-07-17 | 2014-07-22 | Pioneer Energy, Inc. | Methods of higher alcohol synthesis |
US8450536B2 (en) | 2008-07-17 | 2013-05-28 | Pioneer Energy, Inc. | Methods of higher alcohol synthesis |
US9129728B2 (en) | 2008-10-13 | 2015-09-08 | Shell Oil Company | Systems and methods of forming subsurface wellbores |
US20100101784A1 (en) * | 2008-10-13 | 2010-04-29 | Vinegar Harold J | Controlling hydrogen pressure in self-regulating nuclear reactors used to treat a subsurface formation |
US8281861B2 (en) | 2008-10-13 | 2012-10-09 | Shell Oil Company | Circulated heated transfer fluid heating of subsurface hydrocarbon formations |
US8267185B2 (en) | 2008-10-13 | 2012-09-18 | Shell Oil Company | Circulated heated transfer fluid systems used to treat a subsurface formation |
US9051829B2 (en) | 2008-10-13 | 2015-06-09 | Shell Oil Company | Perforated electrical conductors for treating subsurface formations |
US20100089584A1 (en) * | 2008-10-13 | 2010-04-15 | David Booth Burns | Double insulated heaters for treating subsurface formations |
US20100089586A1 (en) * | 2008-10-13 | 2010-04-15 | John Andrew Stanecki | Movable heaters for treating subsurface hydrocarbon containing formations |
US8267170B2 (en) | 2008-10-13 | 2012-09-18 | Shell Oil Company | Offset barrier wells in subsurface formations |
US20100096137A1 (en) * | 2008-10-13 | 2010-04-22 | Scott Vinh Nguyen | Circulated heated transfer fluid heating of subsurface hydrocarbon formations |
US8261832B2 (en) | 2008-10-13 | 2012-09-11 | Shell Oil Company | Heating subsurface formations with fluids |
US20100101783A1 (en) * | 2008-10-13 | 2010-04-29 | Vinegar Harold J | Using self-regulating nuclear reactors in treating a subsurface formation |
US8353347B2 (en) | 2008-10-13 | 2013-01-15 | Shell Oil Company | Deployment of insulated conductors for treating subsurface formations |
US20100108379A1 (en) * | 2008-10-13 | 2010-05-06 | David Alston Edbury | Systems and methods of forming subsurface wellbores |
US8256512B2 (en) | 2008-10-13 | 2012-09-04 | Shell Oil Company | Movable heaters for treating subsurface hydrocarbon containing formations |
US20100108310A1 (en) * | 2008-10-13 | 2010-05-06 | Thomas David Fowler | Offset barrier wells in subsurface formations |
US9022118B2 (en) | 2008-10-13 | 2015-05-05 | Shell Oil Company | Double insulated heaters for treating subsurface formations |
US20100147521A1 (en) * | 2008-10-13 | 2010-06-17 | Xueying Xie | Perforated electrical conductors for treating subsurface formations |
US20100147522A1 (en) * | 2008-10-13 | 2010-06-17 | Xueying Xie | Systems and methods for treating a subsurface formation with electrical conductors |
US8881806B2 (en) | 2008-10-13 | 2014-11-11 | Shell Oil Company | Systems and methods for treating a subsurface formation with electrical conductors |
US20100224368A1 (en) * | 2008-10-13 | 2010-09-09 | Stanley Leroy Mason | Deployment of insulated conductors for treating subsurface formations |
US20100206570A1 (en) * | 2008-10-13 | 2010-08-19 | Ernesto Rafael Fonseca Ocampos | Circulated heated transfer fluid systems used to treat a subsurface formation |
US8220539B2 (en) | 2008-10-13 | 2012-07-17 | Shell Oil Company | Controlling hydrogen pressure in self-regulating nuclear reactors used to treat a subsurface formation |
US20110042084A1 (en) * | 2009-04-10 | 2011-02-24 | Robert Bos | Irregular pattern treatment of a subsurface formation |
US8448707B2 (en) | 2009-04-10 | 2013-05-28 | Shell Oil Company | Non-conducting heater casings |
US20100258290A1 (en) * | 2009-04-10 | 2010-10-14 | Ronald Marshall Bass | Non-conducting heater casings |
US20100258291A1 (en) * | 2009-04-10 | 2010-10-14 | Everett De St Remey Edward | Heated liners for treating subsurface hydrocarbon containing formations |
US8327932B2 (en) | 2009-04-10 | 2012-12-11 | Shell Oil Company | Recovering energy from a subsurface formation |
US8851170B2 (en) | 2009-04-10 | 2014-10-07 | Shell Oil Company | Heater assisted fluid treatment of a subsurface formation |
US20100258309A1 (en) * | 2009-04-10 | 2010-10-14 | Oluropo Rufus Ayodele | Heater assisted fluid treatment of a subsurface formation |
US20100258265A1 (en) * | 2009-04-10 | 2010-10-14 | John Michael Karanikas | Recovering energy from a subsurface formation |
US8434555B2 (en) | 2009-04-10 | 2013-05-07 | Shell Oil Company | Irregular pattern treatment of a subsurface formation |
US9022109B2 (en) | 2010-04-09 | 2015-05-05 | Shell Oil Company | Leak detection in circulated fluid systems for heating subsurface formations |
US9399905B2 (en) | 2010-04-09 | 2016-07-26 | Shell Oil Company | Leak detection in circulated fluid systems for heating subsurface formations |
US8739874B2 (en) | 2010-04-09 | 2014-06-03 | Shell Oil Company | Methods for heating with slots in hydrocarbon formations |
US9033042B2 (en) | 2010-04-09 | 2015-05-19 | Shell Oil Company | Forming bitumen barriers in subsurface hydrocarbon formations |
US8701769B2 (en) | 2010-04-09 | 2014-04-22 | Shell Oil Company | Methods for treating hydrocarbon formations based on geology |
US8701768B2 (en) | 2010-04-09 | 2014-04-22 | Shell Oil Company | Methods for treating hydrocarbon formations |
US9127523B2 (en) | 2010-04-09 | 2015-09-08 | Shell Oil Company | Barrier methods for use in subsurface hydrocarbon formations |
US9127538B2 (en) | 2010-04-09 | 2015-09-08 | Shell Oil Company | Methodologies for treatment of hydrocarbon formations using staged pyrolyzation |
US8875788B2 (en) | 2010-04-09 | 2014-11-04 | Shell Oil Company | Low temperature inductive heating of subsurface formations |
US8820406B2 (en) | 2010-04-09 | 2014-09-02 | Shell Oil Company | Electrodes for electrical current flow heating of subsurface formations with conductive material in wellbore |
US8631866B2 (en) | 2010-04-09 | 2014-01-21 | Shell Oil Company | Leak detection in circulated fluid systems for heating subsurface formations |
US8833453B2 (en) | 2010-04-09 | 2014-09-16 | Shell Oil Company | Electrodes for electrical current flow heating of subsurface formations with tapered copper thickness |
US9016370B2 (en) | 2011-04-08 | 2015-04-28 | Shell Oil Company | Partial solution mining of hydrocarbon containing layers prior to in situ heat treatment |
US9309755B2 (en) | 2011-10-07 | 2016-04-12 | Shell Oil Company | Thermal expansion accommodation for circulated fluid systems used to heat subsurface formations |
US10047594B2 (en) | 2012-01-23 | 2018-08-14 | Genie Ip B.V. | Heater pattern for in situ thermal processing of a subsurface hydrocarbon containing formation |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2595979A (en) | Underground liquefaction of coal | |
US2970826A (en) | Recovery of oil from oil shale | |
CA1056302A (en) | Recovery of hydrocarbons from coal | |
US4067390A (en) | Apparatus and method for the recovery of fuel products from subterranean deposits of carbonaceous matter using a plasma arc | |
US3084919A (en) | Recovery of oil from oil shale by underground hydrogenation | |
US4448251A (en) | In situ conversion of hydrocarbonaceous oil | |
US3770398A (en) | In situ coal gasification process | |
US4005752A (en) | Method of igniting in situ oil shale retort with fuel rich flue gas | |
US2695163A (en) | Method for gasification of subterranean carbonaceous deposits | |
US3734184A (en) | Method of in situ coal gasification | |
US3516495A (en) | Recovery of shale oil | |
US2584605A (en) | Thermal drive method for recovery of oil | |
US2857002A (en) | Recovery of viscous crude oil | |
US3442332A (en) | Combination methods involving the making of gaseous carbon dioxide and its use in crude oil recovery | |
US2481051A (en) | Process and apparatus for the recovery of volatilizable constituents from underground carbonaceous formations | |
US2969226A (en) | Pendant parting petro pyrolysis process | |
US3598182A (en) | Method and apparatus for in situ distillation and hydrogenation of carbonaceous materials | |
AU2001252353B2 (en) | Enhanced oil recovery by in situ gasification | |
US3208519A (en) | Combined in situ combustion-water injection oil recovery process | |
US3228468A (en) | In-situ recovery of hydrocarbons from underground formations of oil shale | |
US4379489A (en) | Method for production of heavy oil from tar sands | |
US3327782A (en) | Underground hydrogenation of oil | |
US4241952A (en) | Surface and subsurface hydrocarbon recovery | |
US3193006A (en) | Petroleum recovery with inert gases | |
US3929193A (en) | Recovery of organic matter from organic mineral-containing deposits |