US3004603A - Heater - Google Patents

Heater Download PDF

Info

Publication number
US3004603A
US3004603A US719890A US71989058A US3004603A US 3004603 A US3004603 A US 3004603A US 719890 A US719890 A US 719890A US 71989058 A US71989058 A US 71989058A US 3004603 A US3004603 A US 3004603A
Authority
US
United States
Prior art keywords
combustion
stratum
conduit
burner
borehole
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
Application number
US719890A
Inventor
Allen S Rogers
James R Hurley
Harry W Parker
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Phillips Petroleum Co
Original Assignee
Phillips Petroleum Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Phillips Petroleum Co filed Critical Phillips Petroleum Co
Priority to US719890A priority Critical patent/US3004603A/en
Application granted granted Critical
Publication of US3004603A publication Critical patent/US3004603A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B36/00Heating, cooling, insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
    • E21B36/02Heating, cooling, insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using burners

Definitions

  • This invention relates to gas fired heaters for heating a well bore. 1 a t In situ combustion in the recoveryof hydrocarbons from underground strata containingcarbonaceous material is becoming more prevalent in' the petroleum industry. In this technique of production, combustion is initiated in the carbonaceous stratum and the resulting combustion zone is caused to move thru the stratum by either inverse or direct air. drive whereby the. heat of combustion of a substantial proportion of the hydrocarbon'in the stratum drives out and usually upgrades a substantial proportion of the remaininghydrocarbon material. i
  • a downhole heater of such construction that the adjacent borehole can be adequately heated to combustion supporting temperature without contacting the wall of the -borehole with combustion gas from the heater-and without overheating'the conduit on which the heater is suspended;
  • Another object ofthe inventiomis ta provide a downhole heater of .high efliciency, for initiating in ,situ combustion in a carbonaceous stratum.
  • jAfurther obje'ct is to provide downhole heating apparatuswhich prevents overheating .of the apparatus.
  • the heater is preferably made of a length which corresponds to the thickness of the formation to be ignited so that the upper end of the burner is adjacent the upper level of the formation and the exhaust conduit extends to the lower level of the stratum. In this manner heat is applied rather uniformly to the entire wall of the borehole from the top to the bottom of the stratum.
  • FIGURE 1 is an elevation of one embodiment of the downhole heater of the invention positioned in a borehole adjacent. a carbonaceous stratum with the auxiliary apparatus for initiating combustion in a carbonaceous stratum;
  • FIGURE 2 is an elevation, partly in section, of one embodiment of the burner of the invention;
  • FIGURE 3 is an elevation showing another embodiment of a downhole heater in a borehole with auxiliary equipment;
  • FIGURE 4 is a cross section of the apparatus of FIGURE 3 taken on the line 4-4.
  • a carbonaceous stratum 10 is penetrated by a borehole 12 in which is positioned a casing 14 closed at the top by well head 16.
  • Heater 22 is suspended in borehole 12 Within stratum 10 and isof alength substantially corresponding to the thickness of the stratum. The heater is suspended by means of conduits 24 and 26.
  • Conduit 24 contains a concentric inner'conduit or burner feed line 28 which is supplied with a combustible mixture of fuel gas and air by means of lines 30 and 32, respectively, which connect with a mixing valve 34.
  • a coolant supply line 36 connects with the annulus between conduit 24 and feed line 28.
  • the heater 22 includes a burner comprising a metal shell 42 in the form of a cylinderor tube lined with a ceramic material 44 forming a downwardly flared combustion zone or chamber '46, a closure plate 50, an inlet at the upper end thru conduit 28, and outlet 58 at its lower end, and may also include an ignitor 54.
  • Ceramic material 44 may comprise any suitable highly refractory ceramic material such as Babcock & Wilcox Companys fKaokast or Johns-Manvilles 3X Firecrete. These materials are mixed with water to form a plastic mud or mortar whichis introduced into shell 42 onwhich it is held by stainless steel rods 48 welded to the shell at the outer ends.
  • the upper end of burner 42 is closed by plate50 thru whichfeed line 28 passes into the inlet end of the burner.
  • FIGURE 3 illustrates an embodiment of theinvention wherein burner 40, feed line 28 and exhaust line 26 are enclosed within a closed tubing 62 within well casing 14 'so as to provide an annular space between the casing and the tubing for injection of air thru line 18 to the combustion area during initiation of combustion, and withdrawal of gas and oil vapor thru line 20 after inverse air injection has been established.
  • Burner 40 comprises an annular burner body 64 surrounding exhaust conduit 26 and is provided with a ring of downwardly directed nozzles or jets 66 on its lower side. Burner 40 is positioned at the level of the upper surface of the carbonaceous formation and the inlet end of the exhaust conduit 26 is positioned near the level of the bottom surface of thestratum so that hot combustion gases traverse the thickness of the formation before entering the exhaust conduit, thereby heating the encasing' tubin 62 along that portion of the tubing lying adjacent the stratum; Air introduced thru conduit 36 cools'the feed line 28 and exhaust conduit 26 down to the burner level and also aids the combustion process at nozzles or jets 66. The cooling air not utilized for combustion is exhausted thru conduit 26. This burner may also be fed a combustible mixture, of fuel gas and air as in the embodiment of the invention shown in FIG- URES 1 and 2.
  • FIGURE '4 merely shows the plan arrangement of the elements of FIGURES and is self-explanatory.
  • circulation of a coolant in contact with the feed line to the burner, and the exhaust line therefrom is provided by the construction shown.
  • This is an essential feature of the burner in that it prevents the burning off of the feed line and/ or exhaust conduit during the critical time when combustion of the oil or other carbonaceous deposit in the stratum is eflected.
  • Another advantageous feature of the'burner construction shown lies in the length of its heating section which is co-extensive with the thickness of the formation thereby facilitating initiation of combustion along the entire wall of the borehole adjacent the carbonaceous stratum.
  • fuel gas is burned in combustion zone 46 (or adjacent nozzles 66) and the hot combustion gases heat the burner shell42 (or tubing 62) adjacent the stratum and the combustion and heating are continued until the temperature of the stratum is raised to the ignition point of the carbonaceous material in the stratum and, at this time, air or other O -containing gas is brought into contact with'the hot stratum so that ignition takes place.
  • air is introduced thru line 18 to initiate and sustain the combustion and when the ignition is by inverse air injection, air is injected thru the stratum from a ring of boreholes therein so that it arrives at the hot section of stratum adjacent borehole -12 and initiates and sustains combustion therein.
  • test burner apparatus was constructed of 304 stainless steel, including the lengths of pipe connected to the burner, the exhaust conduit, and crossover conduit 60 (FIGURE 2). In fact, every element shown in FIGURE 2, except ceramic material 44, was constructed of 304 stainless steel. Of course, the apparatus shown and described maybe made of other heat resistant alloys capable of withstanding ambient temperatures in the downhole initiation of combustion.
  • Apparatus for downhole heating in an oil well comprising in combination an elongated burner including a shell enclosing a combustion chamber, an inlet for fuel and'O at one end of said shell, an outlet for exhaust gases at the opposite end thereof, and an igniter in said combustioncharnber; a fluid feed line connected with said inlet; a conduit concentric with said feed line forming an annular passageway around said feed line for a cooling fluid; an exhaust conduit connected with said outlet, making a U-turn and passing back' along said concentric conduit beyond said inlet; and a connecting conduit between said concentric conduit and said exhaust conduit just above said burner for flow of coolant into said exhaust conduit from said concentricconduit, said fluid feed line, said shell, and said exhaust conduit forming a closed circuit for gases within said well.
  • the apparatus of claim 4 including a casing in said well bore extending to a level adjacent the top of said air injectionis readily instituted by'cutting off'the flow of direct air thru line '18 and injecting air thru the stratum to-the combustion-area from air injection boreholes positioned close by.
  • borehole-12 becomes a production borehole during inverse air injection through 10116201 moresurrounding air injection boreholes and production is removed thru'line 20 or thru tubing inserted thru well head'l'6', by conventional means.
  • borehole 12 serves as an'air'injection borehole and produced hydrocarbons and combustion gases are removed from surrounding boreholes by conventional means.
  • FIG- URE 2 burner constructed substantially as shown in FIG- URE 2 was utilized on several occasions to initiate combustion'in tar sands at a depth of 50 to 75 .feet below the surface.
  • the time required to heat. the tar-sand adjacent the borehole in which the burner was positioned toa temperature sufiicient to support combustion and to actually initiate combustion in the tar sand was about two days in each instance.
  • the best available electric heaters required about 7 days and it was extremely diflicult to prevent damage to the electric heaters.
  • conduit connects with said well head for injecting combustion-supporting gas into said borehole 'for combustion of carbonaceous material in said stratum;
  • Apparatus for downhole heating in an oil well comprising inwcombination an elongated upright burner including a shelbencldsinga combustion chamber, inlet .rneans forfuel and 0 at the upper'end of said shell, and

Description

Oct. 17, 1961 s, o ERs ETAL 3,004,603
HEATER Filed March 7, 1958 55 56 COMBUSTION GASES AIR I 'l 57 FUEL GAS 2a FUEL GAS 30 2o PRODUCED GASES 24 INVENTORS A.S. ROGERS J.R. HURLEY BY H.W. PARKER ATTORNE Y$ "therein.
3,004,603 Patented Oct. 17, 1961 7 3,004,603 7 HEATER Allen S.',Rogers, .lames R. Hurley, and Harry W. Parker,
Bartlesville, Okla, assignors to Phillips Petroleum Company, a corporation of Delaware Filed Mar. 7, 1958, Ser. No. 719,890 1 '1 8 Claims. (Cl. 166-59) This invention relates to gas fired heaters for heating a well bore. 1 a t In situ combustion in the recoveryof hydrocarbons from underground strata containingcarbonaceous material is becoming more prevalent in' the petroleum industry. In this technique of production, combustion is initiated in the carbonaceous stratum and the resulting combustion zone is caused to move thru the stratum by either inverse or direct air. drive whereby the. heat of combustion of a substantial proportion of the hydrocarbon'in the stratum drives out and usually upgrades a substantial proportion of the remaininghydrocarbon material. i
The'ignition of carbonaceous material in a stratum around a borehole therein, followed by injection of air thru the ignition borehole. and recovery of product hydrocarbons and combustion gas thru another borehole in the stratum, is a direct air drive process for effecting in situ combustion and recovery of hydrocarbons from the stratum. In this type of operation the stratum usually plugs in front of the combustion zone because a heavy viscous fluid .bank collects in the stratum inadvance of thecombustion zone which prevents movement of air to ,the combustion process. To. overcome this difliculty and ,permit the continued progress of the combustion zone thru the stratum, inverse air injection has been resorted to. By this technique, a combustion zone is established United States Patent Ofiice around an ignition. borehole by any suitable means and one or more surrounding boreholes.
carbonaceous material in thestratum around a borehole heaters have been found difiicult to design to withstand -the downhole heat and have also been rather slowin heating the formation up to combustion supporting temair is fed thru the stratum to the combustion zone from One method of ignition utilizes a "downhole heater either of the electric or gas fired type. Electric perature. -Conventiona1 gas fired heaters vent the com ,bustion gas into the. borehole and interfere to some extent with the contacting of the borehole wall with gas of, high enough oxygen concentration to readily ignite carbonaceous material. A number of downhole gasfired heaters phave been used which burned ed the tubing on which the heater was positioned before the combustion was fully established in V the adjacent stratum.
Accordingly, it is an object of the invention to provide a downhole heater of such construction that the adjacent borehole can be adequately heated to combustion supporting temperature without contacting the wall of the -borehole with combustion gas from the heater-and without overheating'the conduit on which the heater is suspended; Another object ofthe inventiomis taprovide a downhole heater of .high efliciency, for initiating in ,situ combustion in a carbonaceous stratum. jAfurther obje'ct is to provide downhole heating apparatuswhich prevents overheating .of the apparatus. I Other objects of the invention will become apparent upon consideration of the accompanying disclosure.
circulatesaround the feed line to the'heater and also in contact with the exhaust line therefrom. The heater is preferably made of a length which corresponds to the thickness of the formation to be ignited so that the upper end of the burner is adjacent the upper level of the formation and the exhaust conduit extends to the lower level of the stratum. In this manner heat is applied rather uniformly to the entire wall of the borehole from the top to the bottom of the stratum.
1 A more complete understanding of the invention may be' had by reference to the accompanying schematic drawing of which FIGURE 1 is an elevation of one embodiment of the downhole heater of the invention positioned in a borehole adjacent. a carbonaceous stratum with the auxiliary apparatus for initiating combustion in a carbonaceous stratum; FIGURE 2 is an elevation, partly in section, of one embodiment of the burner of the invention; FIGURE 3 is an elevation showing another embodiment of a downhole heater in a borehole with auxiliary equipment; and FIGURE 4 is a cross section of the apparatus of FIGURE 3 taken on the line 4-4.
Referring to FIGURE 1, a carbonaceous stratum 10 is penetrated by a borehole 12 in which is positioned a casing 14 closed at the top by well head 16.. 'Conduits .18 and .20 .are provided for introducing combustion air and for withdrawing produced gases, respectively, from the casing. Heater 22 is suspended in borehole 12 Within stratum 10 and isof alength substantially corresponding to the thickness of the stratum. The heater is suspended by means of conduits 24 and 26. Conduit 24 contains a concentric inner'conduit or burner feed line 28 which is supplied with a combustible mixture of fuel gas and air by means of lines 30 and 32, respectively, which connect with a mixing valve 34. A coolant supply line 36 connects with the annulus between conduit 24 and feed line 28.
' Referringto FIGURE 2, the heater 22 includes a burner comprising a metal shell 42 in the form of a cylinderor tube lined with a ceramic material 44 forming a downwardly flared combustion zone or chamber '46, a closure plate 50, an inlet at the upper end thru conduit 28, and outlet 58 at its lower end, and may also include an ignitor 54. Ceramic material 44 may comprise any suitable highly refractory ceramic material such as Babcock & Wilcox Companys fKaokast or Johns-Manvilles 3X Firecrete. These materials are mixed with water to form a plastic mud or mortar whichis introduced into shell 42 onwhich it is held by stainless steel rods 48 welded to the shell at the outer ends. The upper end of burner 42 is closed by plate50 thru whichfeed line 28 passes into the inlet end of the burner.
such as battery 55, through-switch 57. i
An'exhaust conduit 26 makes a U-turn or a turn of and connects with the exhaust endtof heater 22 or 'burnerf42 by means of conduit 58. A conduit 60 connects the annulus around conduit 28 with exhaust conduit 26 just above the heater to provide flow, of coolant therebetween. i 1' FIGURE 3 illustrates an embodiment of theinvention wherein burner 40, feed line 28 and exhaust line 26 are enclosed within a closed tubing 62 within well casing 14 'so as to provide an annular space between the casing and the tubing for injection of air thru line 18 to the combustion area during initiation of combustion, and withdrawal of gas and oil vapor thru line 20 after inverse air injection has been established. Burner 40 comprises an annular burner body 64 surrounding exhaust conduit 26 and is provided with a ring of downwardly directed nozzles or jets 66 on its lower side. Burner 40 is positioned at the level of the upper surface of the carbonaceous formation and the inlet end of the exhaust conduit 26 is positioned near the level of the bottom surface of thestratum so that hot combustion gases traverse the thickness of the formation before entering the exhaust conduit, thereby heating the encasing' tubin 62 along that portion of the tubing lying adjacent the stratum; Air introduced thru conduit 36 cools'the feed line 28 and exhaust conduit 26 down to the burner level and also aids the combustion process at nozzles or jets 66. The cooling air not utilized for combustion is exhausted thru conduit 26. This burner mayalso be fed a combustible mixture, of fuel gas and air as in the embodiment of the invention shown in FIG- URES 1 and 2.
FIGURE '4 merely shows the plan arrangement of the elements of FIGURES and is self-explanatory.
I In either embodiment of the invention shown in the drawing, circulation of a coolant in contact with the feed line to the burner, and the exhaust line therefrom is provided by the construction shown. This is an essential feature of the burner in that it prevents the burning off of the feed line and/ or exhaust conduit during the critical time when combustion of the oil or other carbonaceous deposit in the stratum is eflected. Another advantageous feature of the'burner construction shown lies in the length of its heating section which is co-extensive with the thickness of the formation thereby facilitating initiation of combustion along the entire wall of the borehole adjacent the carbonaceous stratum.
In utilizing the apparatus in initiating in situ combustion, fuel gas is burned in combustion zone 46 (or adjacent nozzles 66) and the hot combustion gases heat the burner shell42 (or tubing 62) adjacent the stratum and the combustion and heating are continued until the temperature of the stratum is raised to the ignition point of the carbonaceous material in the stratum and, at this time, air or other O -containing gas is brought into contact with'the hot stratum so that ignition takes place. When ignition by direct injection is practiced, air is introduced thru line 18 to initiate and sustain the combustion and when the ignition is by inverse air injection, air is injected thru the stratum from a ring of boreholes therein so that it arrives at the hot section of stratum adjacent borehole -12 and initiates and sustains combustion therein. After initiation'of combustion by direct air injection and establishment of ;-a substantial combustion area, inverse The test burner apparatus was constructed of 304 stainless steel, including the lengths of pipe connected to the burner, the exhaust conduit, and crossover conduit 60 (FIGURE 2). In fact, every element shown in FIGURE 2, except ceramic material 44, was constructed of 304 stainless steel. Of course, the apparatus shown and described maybe made of other heat resistant alloys capable of withstanding ambient temperatures in the downhole initiation of combustion.
Certain modifications of the invention will become apparent to those skilled in the art and the illustrative details disclosed are not to be construed as imposing unnecessary limitations on the invention.
We claim: j
1. Apparatus for downhole heating in an oil well comprising in combination an elongated burner including a shell enclosing a combustion chamber, an inlet for fuel and'O at one end of said shell, an outlet for exhaust gases at the opposite end thereof, and an igniter in said combustioncharnber; a fluid feed line connected with said inlet; a conduit concentric with said feed line forming an annular passageway around said feed line for a cooling fluid; an exhaust conduit connected with said outlet, making a U-turn and passing back' along said concentric conduit beyond said inlet; and a connecting conduit between said concentric conduit and said exhaust conduit just above said burner for flow of coolant into said exhaust conduit from said concentricconduit, said fluid feed line, said shell, and said exhaust conduit forming a closed circuit for gases within said well. 1
2. The apparatus of claim '1 wherein said shell is lined with ceramic material.
3. The apparatus of claim 2 wherein said shell is a cylinder of high temperature alloy and said ceramic material forms a combustion zone diverging downstream. I 4.'The apparatus of claim 1 wherein said burner is positioned in a well bore adjacenta carbonaceous stratum; said feed line is connected with a source of combustible mixture of fuel and oxygen above ground; said concentric conduit is connected to a source of air; said exhaust conduit is vented to the atmosphere; and said igniter is an electrical heating means.
5. The apparatus of claim 4 including a casing in said well bore extending to a level adjacent the top of said air injectionis readily instituted by'cutting off'the flow of direct air thru line '18 and injecting air thru the stratum to-the combustion-area from air injection boreholes positioned close by.
When utilizing either direct or inverse air injection to initiate the combustion of carbonaceous material around borehole 12, the burner-is'withdrawn from the borehole after combustion is .well established. Borehole-12 becomes a production borehole during inverse air injection through 10116201 moresurrounding air injection boreholes and production is removed thru'line 20 or thru tubing inserted thru well head'l'6', by conventional means. During direct injection insitu combustion, borehole 12 serves as an'air'injection borehole and produced hydrocarbons and combustion gases are removed from surrounding boreholes by conventional means.
burner constructed substantially as shown in FIG- URE 2 was utilized on several occasions to initiate combustion'in tar sands at a depth of 50 to 75 .feet below the surface. The time required to heat. the tar-sand adjacent the borehole in which the burner was positioned toa temperature sufiicient to support combustion and to actually initiate combustion in the tar sand was about two days in each instance. In contrast, the best available electric heaters required about 7 days and it was extremely diflicult to prevent damage to the electric heaters.
line, said concentric conduit, and said exhaust. conduit pass; conduit means connected with said well head for injecting combustion-supporting gas into said borehole 'for combustion of carbonaceous material in said stratum;
and conduit means'connected with said well head for re-v moval of combustion .gases and produced fluids.
6. Apparatus for downhole heating in an oil well comprising inwcombination an elongated upright burner including a shelbencldsinga combustion chamber, inlet .rneans forfuel and 0 at the upper'end of said shell, and
an'outlet-for exhaust gases at the lowerend of said shell; an exhaust conduit leading from said outlet upwardly out of-said well; feed conduit means connected with said inlet means for'feeding fuel and O to said burner, extending upwardly out of said well; andconduit means for circulating cooling fluidalong said feed conduitmeans and said exhaust'conduit leading outof said well, said burner and'connect ing conduits forming a closed circuit for gases "within said well so as to prevent contact of heater combustion gases with said stratum.
- 7.1 Tlie apparatus of claim "6 wherein said burner,isaid feed line, and said' exhaust conduit are housed in a well tubing 'forming an annulus with said borehole and including an inlet for air in said tubing at its upper end whereby air-circulates around said-feed line and exhaust conduit and passes into the combustion area from which unburned air passes with combustion gases into the lower end of said exhaust conduit.
8. The apparatus of claim 6 wherein said burner surfounds said exhaust conduit and comprises a ring of jets extending downwardly from said burner.
References Cited in the file of this patent UNITED STATES PATENTS Kweager May 3, 1927
US719890A 1958-03-07 1958-03-07 Heater Expired - Lifetime US3004603A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US719890A US3004603A (en) 1958-03-07 1958-03-07 Heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US719890A US3004603A (en) 1958-03-07 1958-03-07 Heater

Publications (1)

Publication Number Publication Date
US3004603A true US3004603A (en) 1961-10-17

Family

ID=24891792

Family Applications (1)

Application Number Title Priority Date Filing Date
US719890A Expired - Lifetime US3004603A (en) 1958-03-07 1958-03-07 Heater

Country Status (1)

Country Link
US (1) US3004603A (en)

Cited By (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3180417A (en) * 1962-08-13 1965-04-27 California Research Corp Method and apparatus for burning a combustible mixture in a well
US3225829A (en) * 1962-10-24 1965-12-28 Chevron Res Apparatus for burning a combustible mixture in a well
US3371713A (en) * 1966-07-25 1968-03-05 Pan American Petroleum Corp Submerged combustion in wells
US3372754A (en) * 1966-05-31 1968-03-12 Mobil Oil Corp Well assembly for heating a subterranean formation
US3746088A (en) * 1971-09-07 1973-07-17 Chevron Res Apparatus for use in wells
US4401159A (en) * 1981-05-18 1983-08-30 Flying K Equipment System, Inc. Jet engine pump and downhole heater
US4502535A (en) * 1981-05-18 1985-03-05 Kofahl William M Jet engine pump and downhole heater
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
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
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
US20030173085A1 (en) * 2001-10-24 2003-09-18 Vinegar Harold J. Upgrading and mining of coal
US20030173081A1 (en) * 2001-10-24 2003-09-18 Vinegar Harold J. 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
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
US20050269090A1 (en) * 2004-04-23 2005-12-08 Vinegar Harold J Temperature limited heaters with thermally conductive fluid used to heat subsurface formations
US7011154B2 (en) 2000-04-24 2006-03-14 Shell Oil Company In situ recovery from a kerogen and liquid hydrocarbon containing formation
US7066254B2 (en) 2001-04-24 2006-06-27 Shell Oil Company In situ thermal processing of a tar sands formation
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
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
US20070045266A1 (en) * 2005-04-22 2007-03-01 Sandberg Chester L In situ conversion process utilizing a closed loop heating system
US20070095536A1 (en) * 2005-10-24 2007-05-03 Vinegar Harold J Cogeneration systems and processes for treating hydrocarbon containing formations
US20080035346A1 (en) * 2006-04-21 2008-02-14 Vijay Nair Methods of producing transportation fuel
US20080128134A1 (en) * 2006-10-20 2008-06-05 Ramesh Raju Mudunuri Producing drive fluid in situ in tar sands formations
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
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
US20100258290A1 (en) * 2009-04-10 2010-10-14 Ronald Marshall Bass Non-conducting heater casings
US8631866B2 (en) 2010-04-09 2014-01-21 Shell Oil Company Leak detection in circulated fluid systems for heating subsurface formations
US8701769B2 (en) 2010-04-09 2014-04-22 Shell Oil Company Methods for treating hydrocarbon formations based on geology
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 (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1626940A (en) * 1925-12-19 1927-05-03 William A J Kreager Burner for oil-well cleaners
US2225775A (en) * 1940-01-26 1940-12-24 David L Garrett Apparatus for deparaffining oil wells
US2384836A (en) * 1941-02-26 1945-09-18 Galvin Mfg Corp Heater
US2418882A (en) * 1942-06-15 1947-04-15 Galvin Mfg Corp Fuel conditioning means
US2506853A (en) * 1945-05-30 1950-05-09 Union Oil Co Oil well furnace

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1626940A (en) * 1925-12-19 1927-05-03 William A J Kreager Burner for oil-well cleaners
US2225775A (en) * 1940-01-26 1940-12-24 David L Garrett Apparatus for deparaffining oil wells
US2384836A (en) * 1941-02-26 1945-09-18 Galvin Mfg Corp Heater
US2418882A (en) * 1942-06-15 1947-04-15 Galvin Mfg Corp Fuel conditioning means
US2506853A (en) * 1945-05-30 1950-05-09 Union Oil Co Oil well furnace

Cited By (405)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3180417A (en) * 1962-08-13 1965-04-27 California Research Corp Method and apparatus for burning a combustible mixture in a well
US3225829A (en) * 1962-10-24 1965-12-28 Chevron Res Apparatus for burning a combustible mixture in a well
US3372754A (en) * 1966-05-31 1968-03-12 Mobil Oil Corp Well assembly for heating a subterranean formation
US3371713A (en) * 1966-07-25 1968-03-05 Pan American Petroleum Corp Submerged combustion in wells
US3746088A (en) * 1971-09-07 1973-07-17 Chevron Res Apparatus for use in wells
US4401159A (en) * 1981-05-18 1983-08-30 Flying K Equipment System, Inc. Jet engine pump and downhole heater
US4502535A (en) * 1981-05-18 1985-03-05 Kofahl William M Jet engine pump and downhole heater
US6997255B2 (en) 2000-04-24 2006-02-14 Shell Oil Company In situ thermal processing of a hydrocarbon containing formation in a reducing environment
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
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
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
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
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
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
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
US6994161B2 (en) 2000-04-24 2006-02-07 Kevin Albert Maher In situ thermal processing of a coal formation with a selected moisture content
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
US6607033B2 (en) 2000-04-24 2003-08-19 Shell Oil Company In Situ thermal processing of a coal formation to produce a condensate
US6609570B2 (en) 2000-04-24 2003-08-26 Shell Oil Company In situ thermal processing of a coal formation and ammonia production
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
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
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
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
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
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
US6913078B2 (en) 2000-04-24 2005-07-05 Shell Oil Company In Situ thermal processing of hydrocarbons within a relatively impermeable formation
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
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
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
US6712135B2 (en) 2000-04-24 2004-03-30 Shell Oil Company In situ thermal processing of a coal formation in reducing environment
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
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
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
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
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
US6725928B2 (en) 2000-04-24 2004-04-27 Shell Oil Company In situ thermal processing of a coal formation using a distributed combustor
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
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
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
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
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
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
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
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
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
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
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
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
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
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
US6745832B2 (en) 2000-04-24 2004-06-08 Shell Oil Company Situ thermal processing of a hydrocarbon containing formation to control product composition
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
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
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
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
US6729401B2 (en) 2000-04-24 2004-05-04 Shell Oil Company In situ thermal processing of a hydrocarbon containing formation and ammonia production
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
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
US6871707B2 (en) 2000-04-24 2005-03-29 Shell Oil Company In situ thermal processing of a hydrocarbon containing formation with carbon dioxide sequestration
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
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
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
US6994169B2 (en) 2001-04-24 2006-02-07 Shell Oil Company In situ thermal processing of an oil shale formation with a selected property
US6923257B2 (en) 2001-04-24 2005-08-02 Shell Oil Company In situ thermal processing of an oil shale formation to produce a condensate
US6877555B2 (en) 2001-04-24 2005-04-12 Shell Oil Company In situ thermal processing of an oil shale formation while inhibiting coking
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
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
US20030079877A1 (en) * 2001-04-24 2003-05-01 Wellington Scott Lee In situ thermal processing of a relatively impermeable formation in a reducing environment
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
US20030098605A1 (en) * 2001-04-24 2003-05-29 Vinegar Harold J. In situ thermal recovery from a relatively permeable formation
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
US6918442B2 (en) 2001-04-24 2005-07-19 Shell Oil Company In situ thermal processing of an oil shale formation in a reducing environment
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
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
US8608249B2 (en) 2001-04-24 2013-12-17 Shell Oil Company In situ thermal processing of an oil shale 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
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
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
US7096942B1 (en) 2001-04-24 2006-08-29 Shell Oil Company In situ thermal processing of a relatively permeable formation while controlling pressure
US6951247B2 (en) 2001-04-24 2005-10-04 Shell Oil Company In situ thermal processing of an oil shale formation using horizontal heat sources
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
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
US20030116315A1 (en) * 2001-04-24 2003-06-26 Wellington Scott Lee In situ thermal processing of a relatively permeable formation
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
US20030164239A1 (en) * 2001-04-24 2003-09-04 Wellington Scott Lee In situ thermal processing of an oil shale formation in a reducing environment
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
US20030136559A1 (en) * 2001-04-24 2003-07-24 Wellington Scott Lee In situ thermal processing while controlling pressure in an oil shale formation
US7735935B2 (en) 2001-04-24 2010-06-15 Shell Oil Company In situ thermal processing of an oil shale formation containing carbonate minerals
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
US20030146002A1 (en) * 2001-04-24 2003-08-07 Vinegar Harold J. Removable heat sources for in situ thermal processing of an oil shale formation
US20100270015A1 (en) * 2001-04-24 2010-10-28 Shell Oil Company In situ thermal processing of an oil shale formation
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
US7055600B2 (en) 2001-04-24 2006-06-06 Shell Oil Company In situ thermal recovery from a relatively permeable formation with controlled production rate
US7051811B2 (en) 2001-04-24 2006-05-30 Shell Oil Company In situ thermal processing through an open wellbore in an oil shale formation
US7051807B2 (en) 2001-04-24 2006-05-30 Shell Oil Company In situ thermal recovery from a relatively permeable formation with quality control
US7040398B2 (en) 2001-04-24 2006-05-09 Shell Oil Company In situ thermal processing of a relatively permeable formation in a reducing environment
US20030141066A1 (en) * 2001-04-24 2003-07-31 Karanikas John Michael In situ thermal processing of an oil shale formation while inhibiting coking
US6981548B2 (en) 2001-04-24 2006-01-03 Shell Oil Company In situ thermal recovery from a relatively permeable formation
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
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
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
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
US6991036B2 (en) 2001-04-24 2006-01-31 Shell Oil Company Thermal processing of a relatively permeable formation
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
US7066254B2 (en) 2001-04-24 2006-06-27 Shell Oil Company In situ thermal processing of a tar sands 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
US7040400B2 (en) 2001-04-24 2006-05-09 Shell Oil Company In situ thermal processing of a relatively impermeable formation using an open wellbore
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
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
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
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
US20030131993A1 (en) * 2001-04-24 2003-07-17 Etuan Zhang In situ thermal processing of an oil shale formation with a selected property
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
US7077198B2 (en) 2001-10-24 2006-07-18 Shell Oil Company In situ recovery from a hydrocarbon containing formation using barriers
US20030196810A1 (en) * 2001-10-24 2003-10-23 Vinegar Harold J. Treatment of a hydrocarbon containing formation after heating
US7128153B2 (en) 2001-10-24 2006-10-31 Shell Oil Company Treatment of a hydrocarbon containing formation after heating
US20040040715A1 (en) * 2001-10-24 2004-03-04 Wellington Scott Lee In situ production of a blending agent from a hydrocarbon containing formation
US7077199B2 (en) 2001-10-24 2006-07-18 Shell Oil Company In situ thermal processing of an oil reservoir formation
US8627887B2 (en) 2001-10-24 2014-01-14 Shell Oil Company In situ recovery from a hydrocarbon containing formation
US7051808B1 (en) 2001-10-24 2006-05-30 Shell Oil Company Seismic monitoring of in situ conversion 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
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
US20030201098A1 (en) * 2001-10-24 2003-10-30 Karanikas John Michael In situ recovery from a hydrocarbon containing formation using one or more simulations
US7066257B2 (en) 2001-10-24 2006-06-27 Shell Oil Company In situ recovery from lean and rich zones 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
US6969123B2 (en) 2001-10-24 2005-11-29 Shell Oil Company Upgrading and mining of coal
US7461691B2 (en) 2001-10-24 2008-12-09 Shell Oil Company In situ recovery from a hydrocarbon containing formation
US20030173085A1 (en) * 2001-10-24 2003-09-18 Vinegar Harold J. Upgrading and mining of coal
US7090013B2 (en) 2001-10-24 2006-08-15 Shell Oil Company In situ thermal processing of a hydrocarbon containing formation to produce heated fluids
US6991045B2 (en) 2001-10-24 2006-01-31 Shell Oil Company Forming openings in a hydrocarbon containing formation using magnetic tracking
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
US7100994B2 (en) 2001-10-24 2006-09-05 Shell Oil Company Producing hydrocarbons and non-hydrocarbon containing materials when treating a hydrocarbon containing formation
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
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
US7219734B2 (en) 2002-10-24 2007-05-22 Shell Oil Company Inhibiting wellbore deformation during in situ thermal processing of a hydrocarbon containing formation
US8238730B2 (en) 2002-10-24 2012-08-07 Shell Oil Company High voltage 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
US8224164B2 (en) 2002-10-24 2012-07-17 Shell Oil Company Insulated conductor temperature limited heaters
US8224163B2 (en) 2002-10-24 2012-07-17 Shell Oil Company Variable frequency temperature limited heaters
US7121342B2 (en) 2003-04-24 2006-10-17 Shell Oil Company Thermal processes for subsurface formations
US8579031B2 (en) 2003-04-24 2013-11-12 Shell Oil Company Thermal processes for subsurface formations
US7360588B2 (en) 2003-04-24 2008-04-22 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
US20050269091A1 (en) * 2004-04-23 2005-12-08 Guillermo Pastor-Sanz Reducing viscosity of oil for production from a hydrocarbon containing formation
US8355623B2 (en) 2004-04-23 2013-01-15 Shell Oil Company Temperature limited heaters with high power factors
US20050269090A1 (en) * 2004-04-23 2005-12-08 Vinegar Harold J Temperature limited heaters with thermally conductive fluid used to heat subsurface formations
US20050269088A1 (en) * 2004-04-23 2005-12-08 Vinegar Harold J Inhibiting effects of sloughing in wellbores
US20050269313A1 (en) * 2004-04-23 2005-12-08 Vinegar Harold J Temperature limited heaters with high power factors
US20050269077A1 (en) * 2004-04-23 2005-12-08 Sandberg Chester L Start-up of temperature limited heaters using direct current (DC)
US7510000B2 (en) 2004-04-23 2009-03-31 Shell Oil Company Reducing viscosity of oil for production from a hydrocarbon containing formation
US20050269089A1 (en) * 2004-04-23 2005-12-08 Sandberg Chester L Temperature limited heaters using modulated DC power
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
US7320364B2 (en) 2004-04-23 2008-01-22 Shell Oil Company Inhibiting reflux in a heated well of an in situ conversion system
US20050269095A1 (en) * 2004-04-23 2005-12-08 Fairbanks Michael D Inhibiting reflux in a heated well of an in situ conversion system
US20050269094A1 (en) * 2004-04-23 2005-12-08 Harris Christopher K Triaxial temperature limited heater
US20050269092A1 (en) * 2004-04-23 2005-12-08 Vinegar Harold J Vacuum pumping of conductor-in-conduit heaters
US7431076B2 (en) 2004-04-23 2008-10-07 Shell Oil Company Temperature limited heaters using modulated DC power
US7353872B2 (en) 2004-04-23 2008-04-08 Shell Oil Company Start-up of temperature limited heaters using direct current (DC)
US7357180B2 (en) 2004-04-23 2008-04-15 Shell Oil Company Inhibiting effects of sloughing in wellbores
US7424915B2 (en) 2004-04-23 2008-09-16 Shell Oil Company Vacuum pumping of conductor-in-conduit heaters
US20050269093A1 (en) * 2004-04-23 2005-12-08 Sandberg Chester L Variable frequency temperature limited heaters
US7370704B2 (en) 2004-04-23 2008-05-13 Shell Oil Company Triaxial temperature limited heater
US20060005968A1 (en) * 2004-04-23 2006-01-12 Vinegar Harold J Temperature limited heaters with relatively constant current
US7383877B2 (en) 2004-04-23 2008-06-10 Shell Oil Company Temperature limited heaters with thermally conductive fluid used to heat subsurface formations
US20060289536A1 (en) * 2004-04-23 2006-12-28 Vinegar Harold J Subsurface electrical heaters using nitride insulation
US20070045265A1 (en) * 2005-04-22 2007-03-01 Mckinzie Billy J Ii Low temperature barriers with heat interceptor wells for in situ processes
US20070144732A1 (en) * 2005-04-22 2007-06-28 Kim Dong S Low temperature barriers for use with in situ processes
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
US20070045267A1 (en) * 2005-04-22 2007-03-01 Vinegar Harold J Subsurface connection methods for subsurface 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
US8224165B2 (en) 2005-04-22 2012-07-17 Shell Oil Company Temperature limited heater utilizing non-ferromagnetic conductor
US7575053B2 (en) 2005-04-22 2009-08-18 Shell Oil Company Low temperature monitoring system for subsurface barriers
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
US7986869B2 (en) 2005-04-22 2011-07-26 Shell Oil Company Varying properties along lengths of temperature limited heaters
US7942197B2 (en) 2005-04-22 2011-05-17 Shell Oil Company Methods and systems for producing fluid from an in situ conversion process
US7527094B2 (en) 2005-04-22 2009-05-05 Shell Oil Company Double barrier system for an in situ conversion process
US20070133961A1 (en) * 2005-04-22 2007-06-14 Fairbanks Michael D Methods and systems for producing fluid from an in situ conversion process
US7435037B2 (en) 2005-04-22 2008-10-14 Shell Oil Company Low temperature barriers with heat interceptor wells for in situ processes
US20070137856A1 (en) * 2005-04-22 2007-06-21 Mckinzie Billy J Double barrier system for an in situ conversion process
US20070108200A1 (en) * 2005-04-22 2007-05-17 Mckinzie Billy J Ii Low temperature barrier wellbores formed using water flushing
US20070119098A1 (en) * 2005-04-22 2007-05-31 Zaida Diaz Treatment of gas from an in situ conversion process
US7860377B2 (en) 2005-04-22 2010-12-28 Shell Oil Company Subsurface connection methods for subsurface heaters
US7831134B2 (en) 2005-04-22 2010-11-09 Shell Oil Company Grouped exposed metal heaters
US20070045266A1 (en) * 2005-04-22 2007-03-01 Sandberg Chester L In situ conversion process utilizing a closed loop heating system
US7500528B2 (en) 2005-04-22 2009-03-10 Shell Oil Company Low temperature barrier wellbores formed using water flushing
US7584789B2 (en) 2005-10-24 2009-09-08 Shell Oil Company 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
US8606091B2 (en) 2005-10-24 2013-12-10 Shell Oil Company Subsurface heaters with low sulfidation rates
US20070131420A1 (en) * 2005-10-24 2007-06-14 Weijian Mo Methods of cracking a crude product to produce additional crude products
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
US20070131427A1 (en) * 2005-10-24 2007-06-14 Ruijian Li Systems and methods for producing hydrocarbons from tar sands formations
US20070127897A1 (en) * 2005-10-24 2007-06-07 John Randy C Subsurface heaters with low sulfidation rates
US20070221377A1 (en) * 2005-10-24 2007-09-27 Vinegar Harold J Solution mining systems and methods for treating hydrocarbon containing formations
US7559368B2 (en) 2005-10-24 2009-07-14 Shell Oil Company Solution mining systems and methods 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
US7635025B2 (en) 2005-10-24 2009-12-22 Shell Oil Company Cogeneration systems and processes for treating hydrocarbon containing formations
US7581589B2 (en) 2005-10-24 2009-09-01 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
US7562706B2 (en) 2005-10-24 2009-07-21 Shell Oil Company Systems and methods for producing hydrocarbons from tar sands formations
US20080107577A1 (en) * 2005-10-24 2008-05-08 Vinegar Harold J Varying heating in dawsonite zones in hydrocarbon containing formations
US7549470B2 (en) 2005-10-24 2009-06-23 Shell Oil Company Solution mining and heating by oxidation 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
US20070125533A1 (en) * 2005-10-24 2007-06-07 Minderhoud Johannes K Methods of hydrotreating a liquid stream to remove clogging compounds
US7559367B2 (en) 2005-10-24 2009-07-14 Shell Oil Company Temperature limited heater with a conduit substantially electrically isolated from the formation
US7591310B2 (en) 2005-10-24 2009-09-22 Shell Oil Company Methods of hydrotreating a liquid stream to remove clogging compounds
US7793722B2 (en) 2006-04-21 2010-09-14 Shell Oil Company Non-ferromagnetic overburden casing
US7631689B2 (en) 2006-04-21 2009-12-15 Shell Oil Company Sulfur barrier for use with in situ processes for treating formations
US8857506B2 (en) 2006-04-21 2014-10-14 Shell Oil Company Alternate energy source usage methods for in situ heat treatment processes
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
US20080038144A1 (en) * 2006-04-21 2008-02-14 Maziasz Phillip J High strength alloys
US20080035348A1 (en) * 2006-04-21 2008-02-14 Vitek John M Temperature limited heaters using phase transformation of ferromagnetic material
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
US7912358B2 (en) 2006-04-21 2011-03-22 Shell Oil Company Alternate energy source usage for in situ heat treatment processes
US8083813B2 (en) 2006-04-21 2011-12-27 Shell Oil Company Methods of producing transportation fuel
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
US7533719B2 (en) 2006-04-21 2009-05-19 Shell Oil Company Wellhead with non-ferromagnetic materials
US20100272595A1 (en) * 2006-04-21 2010-10-28 Shell Oil Company High strength alloys
US20080173450A1 (en) * 2006-04-21 2008-07-24 Bernard Goldberg Time sequenced heating of multiple layers in a hydrocarbon containing formation
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
US7635023B2 (en) 2006-04-21 2009-12-22 Shell Oil Company 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
US7610962B2 (en) 2006-04-21 2009-11-03 Shell Oil Company Sour gas injection for use with in situ heat treatment
US20080173444A1 (en) * 2006-04-21 2008-07-24 Francis Marion Stone Alternate energy source usage for in situ heat treatment processes
US20080174115A1 (en) * 2006-04-21 2008-07-24 Gene Richard Lambirth Power systems utilizing the heat of produced formation fluid
US20080173449A1 (en) * 2006-04-21 2008-07-24 Thomas David Fowler Sour gas injection for use with in situ heat treatment
US8192682B2 (en) 2006-04-21 2012-06-05 Shell Oil Company High strength alloys
US20080135253A1 (en) * 2006-10-20 2008-06-12 Vinegar Harold J Treating tar sands formations with karsted zones
US20080217003A1 (en) * 2006-10-20 2008-09-11 Myron Ira Kuhlman Gas injection to inhibit migration during an in situ heat treatment process
US7631690B2 (en) 2006-10-20 2009-12-15 Shell Oil Company Heating hydrocarbon containing formations in a spiral startup staged sequence
US20080142216A1 (en) * 2006-10-20 2008-06-19 Vinegar Harold J Treating tar sands formations with dolomite
US8191630B2 (en) 2006-10-20 2012-06-05 Shell Oil Company Creating fluid injectivity 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
US7644765B2 (en) 2006-10-20 2010-01-12 Shell Oil Company Heating tar sands formations while controlling pressure
US7673681B2 (en) 2006-10-20 2010-03-09 Shell Oil Company Treating tar sands formations with karsted zones
US7562707B2 (en) 2006-10-20 2009-07-21 Shell Oil Company Heating hydrocarbon containing formations in a line drive staged process
US7677310B2 (en) 2006-10-20 2010-03-16 Shell Oil Company Creating and maintaining a gas cap in tar sands formations
US7677314B2 (en) 2006-10-20 2010-03-16 Shell Oil Company Method of condensing vaporized water in situ to treat tar sands formations
US7681647B2 (en) 2006-10-20 2010-03-23 Shell Oil Company Method of producing drive fluid in situ in tar sands formations
US7540324B2 (en) 2006-10-20 2009-06-02 Shell Oil Company Heating hydrocarbon containing formations in a checkerboard pattern staged process
US20080135254A1 (en) * 2006-10-20 2008-06-12 Vinegar Harold J In situ heat treatment process utilizing a closed loop heating system
US20080185147A1 (en) * 2006-10-20 2008-08-07 Vinegar Harold J Wax barrier for use with in situ processes for treating formations
US7635024B2 (en) 2006-10-20 2009-12-22 Shell Oil Company Heating tar sands formations to visbreaking temperatures
US7703513B2 (en) 2006-10-20 2010-04-27 Shell Oil Company Wax barrier for use with in situ processes for treating formations
US20080217015A1 (en) * 2006-10-20 2008-09-11 Vinegar Harold J Heating hydrocarbon containing formations in a spiral startup staged sequence
US20080217004A1 (en) * 2006-10-20 2008-09-11 De Rouffignac Eric Pierre Heating hydrocarbon containing formations in a checkerboard pattern staged process
US20080277113A1 (en) * 2006-10-20 2008-11-13 George Leo Stegemeier Heating tar sands formations while controlling pressure
US20090014181A1 (en) * 2006-10-20 2009-01-15 Vinegar Harold J Creating and maintaining a gas cap in tar sands formations
US7717171B2 (en) 2006-10-20 2010-05-18 Shell Oil Company Moving hydrocarbons through portions of tar sands formations with a fluid
US7730946B2 (en) 2006-10-20 2010-06-08 Shell Oil Company Treating tar sands formations with dolomite
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
US7730947B2 (en) 2006-10-20 2010-06-08 Shell Oil Company Creating fluid injectivity 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
US8555971B2 (en) 2006-10-20 2013-10-15 Shell Oil Company Treating tar sands formations with dolomite
US20090014180A1 (en) * 2006-10-20 2009-01-15 George Leo Stegemeier Moving hydrocarbons through portions of tar sands formations with a fluid
US7845411B2 (en) 2006-10-20 2010-12-07 Shell Oil Company In situ heat treatment process utilizing a closed loop heating system
US20080128134A1 (en) * 2006-10-20 2008-06-05 Ramesh Raju Mudunuri Producing drive fluid in situ in tar sands formations
US7841401B2 (en) 2006-10-20 2010-11-30 Shell Oil Company Gas injection to inhibit migration during an in situ heat treatment process
US20100276141A1 (en) * 2006-10-20 2010-11-04 Shell Oil Company Creating fluid injectivity in tar sands formations
US8327681B2 (en) 2007-04-20 2012-12-11 Shell Oil Company Wellbore manufacturing processes for in situ heat treatment processes
US8381815B2 (en) 2007-04-20 2013-02-26 Shell Oil Company Production from multiple zones of a tar sands formation
US9181780B2 (en) 2007-04-20 2015-11-10 Shell Oil Company Controlling and assessing pressure conditions during treatment of tar sands formations
US20090120646A1 (en) * 2007-04-20 2009-05-14 Dong Sub Kim Electrically isolating insulated conductor heater
US8791396B2 (en) 2007-04-20 2014-07-29 Shell Oil Company Floating insulated conductors for heating subsurface formations
US20090084547A1 (en) * 2007-04-20 2009-04-02 Walter Farman Farmayan Downhole burner systems and methods for heating subsurface formations
US20090078461A1 (en) * 2007-04-20 2009-03-26 Arthur James Mansure Drilling subsurface wellbores with cutting structures
US20090090509A1 (en) * 2007-04-20 2009-04-09 Vinegar Harold J In situ recovery from residually heated sections in a hydrocarbon containing formation
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
US7841408B2 (en) 2007-04-20 2010-11-30 Shell Oil Company In situ heat treatment from multiple layers of a tar sands formation
US20090095476A1 (en) * 2007-04-20 2009-04-16 Scott Vinh Nguyen Molten salt as a heat transfer fluid for heating a subsurface formation
US7841425B2 (en) 2007-04-20 2010-11-30 Shell Oil Company Drilling subsurface wellbores with cutting structures
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
US7849922B2 (en) 2007-04-20 2010-12-14 Shell Oil Company In situ recovery from residually heated sections in a hydrocarbon containing formation
US7798220B2 (en) 2007-04-20 2010-09-21 Shell Oil Company In situ heat treatment of a tar sands formation after drive process treatment
US20090321075A1 (en) * 2007-04-20 2009-12-31 Christopher Kelvin Harris Parallel heater system for subsurface formations
US20090126929A1 (en) * 2007-04-20 2009-05-21 Vinegar Harold J Treating nahcolite containing formations and saline zones
US20090095480A1 (en) * 2007-04-20 2009-04-16 Vinegar Harold J In situ heat treatment of a tar sands formation after drive process treatment
US20090095477A1 (en) * 2007-04-20 2009-04-16 Scott Vinh Nguyen Heating systems for heating subsurface formations
US20090095479A1 (en) * 2007-04-20 2009-04-16 John Michael Karanikas Production from multiple zones of a tar sands formation
US7931086B2 (en) 2007-04-20 2011-04-26 Shell Oil Company Heating systems for heating subsurface formations
US8459359B2 (en) 2007-04-20 2013-06-11 Shell Oil Company Treating nahcolite containing formations and saline zones
US8042610B2 (en) 2007-04-20 2011-10-25 Shell Oil Company Parallel heater system for subsurface formations
US7950453B2 (en) 2007-04-20 2011-05-31 Shell Oil Company Downhole burner systems and methods for heating subsurface formations
US20090200854A1 (en) * 2007-10-19 2009-08-13 Vinegar Harold J Solution mining and in situ treatment of nahcolite beds
US8011451B2 (en) 2007-10-19 2011-09-06 Shell Oil Company Ranging methods for developing wellbores in subsurface formations
US8536497B2 (en) 2007-10-19 2013-09-17 Shell Oil Company Methods for forming long subsurface heaters
US20090194269A1 (en) * 2007-10-19 2009-08-06 Vinegar Harold J Three-phase heaters with common overburden sections for heating subsurface formations
US20090200025A1 (en) * 2007-10-19 2009-08-13 Jose Luis Bravo High temperature methods for forming oxidizer fuel
US20090194282A1 (en) * 2007-10-19 2009-08-06 Gary Lee Beer In situ oxidation of subsurface formations
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
US20090194333A1 (en) * 2007-10-19 2009-08-06 Macdonald Duncan Ranging methods for developing wellbores in subsurface formations
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
US20090200031A1 (en) * 2007-10-19 2009-08-13 David Scott Miller Irregular spacing of heat sources for treating hydrocarbon containing formations
US7866388B2 (en) 2007-10-19 2011-01-11 Shell Oil Company High temperature methods for forming oxidizer fuel
US8276661B2 (en) 2007-10-19 2012-10-02 Shell Oil Company Heating subsurface formations by oxidizing fuel on a fuel carrier
US20090194329A1 (en) * 2007-10-19 2009-08-06 Rosalvina Ramona Guimerans Methods for forming wellbores in heated formations
US20090194524A1 (en) * 2007-10-19 2009-08-06 Dong Sub Kim Methods for forming long subsurface heaters
US8196658B2 (en) 2007-10-19 2012-06-12 Shell Oil Company Irregular spacing of heat sources for treating hydrocarbon containing formations
US8272455B2 (en) 2007-10-19 2012-09-25 Shell Oil Company Methods for forming wellbores in heated formations
US8240774B2 (en) 2007-10-19 2012-08-14 Shell Oil Company Solution mining and in situ treatment of nahcolite beds
US20090189617A1 (en) * 2007-10-19 2009-07-30 David Burns Continuous subsurface heater temperature measurement
US8636323B2 (en) 2008-04-18 2014-01-28 Shell Oil Company 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
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
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
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
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
US20090260824A1 (en) * 2008-04-18 2009-10-22 David Booth Burns Hydrocarbon production from mines and tunnels used in 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
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
US8162405B2 (en) 2008-04-18 2012-04-24 Shell Oil Company Using tunnels 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
US8281861B2 (en) 2008-10-13 2012-10-09 Shell Oil Company Circulated heated transfer fluid heating of subsurface hydrocarbon formations
US8353347B2 (en) 2008-10-13 2013-01-15 Shell Oil Company Deployment of insulated conductors for treating subsurface formations
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
US8256512B2 (en) 2008-10-13 2012-09-04 Shell Oil Company Movable heaters for treating subsurface hydrocarbon containing formations
US9129728B2 (en) 2008-10-13 2015-09-08 Shell Oil Company Systems and methods of forming subsurface wellbores
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
US20100096137A1 (en) * 2008-10-13 2010-04-22 Scott Vinh Nguyen Circulated heated transfer fluid heating of subsurface hydrocarbon formations
US20100101783A1 (en) * 2008-10-13 2010-04-29 Vinegar Harold J Using self-regulating nuclear reactors in treating a subsurface formation
US8267185B2 (en) 2008-10-13 2012-09-18 Shell Oil Company Circulated heated transfer fluid systems used to treat a subsurface formation
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
US20100108379A1 (en) * 2008-10-13 2010-05-06 David Alston Edbury Systems and methods of forming subsurface wellbores
US8267170B2 (en) 2008-10-13 2012-09-18 Shell Oil Company Offset barrier wells in subsurface formations
US20100147522A1 (en) * 2008-10-13 2010-06-17 Xueying Xie Systems and methods for treating a subsurface formation with electrical conductors
US9051829B2 (en) 2008-10-13 2015-06-09 Shell Oil Company Perforated electrical conductors for treating subsurface formations
US20100147521A1 (en) * 2008-10-13 2010-06-17 Xueying Xie Perforated electrical 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
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
US8261832B2 (en) 2008-10-13 2012-09-11 Shell Oil Company Heating subsurface formations with fluids
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
US8434555B2 (en) 2009-04-10 2013-05-07 Shell Oil Company Irregular pattern treatment of a subsurface formation
US20100258265A1 (en) * 2009-04-10 2010-10-14 John Michael Karanikas Recovering energy from a subsurface formation
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
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
US9033042B2 (en) 2010-04-09 2015-05-19 Shell Oil Company Forming bitumen barriers in subsurface hydrocarbon formations
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
US8701769B2 (en) 2010-04-09 2014-04-22 Shell Oil Company Methods for treating hydrocarbon formations based on geology
US9022109B2 (en) 2010-04-09 2015-05-05 Shell Oil Company Leak detection in circulated fluid systems for heating 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
US9399905B2 (en) 2010-04-09 2016-07-26 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
US8739874B2 (en) 2010-04-09 2014-06-03 Shell Oil Company Methods for heating with slots in hydrocarbon formations
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
US3004603A (en) Heater
US3007521A (en) Recovery of oil by in situ combustion
US3010513A (en) Initiation of in situ combustion in carbonaceous stratum
US2994376A (en) In situ combustion process
US3010516A (en) Burner and process for in situ combustion
US3024013A (en) Recovery of hydrocarbons by in situ combustion
US3181613A (en) Method and apparatus for subterranean heating
US2506853A (en) Oil well furnace
US2997105A (en) Burner apparatus
US3116792A (en) In situ combustion process
US4228856A (en) Process for recovering viscous, combustible material
US3372754A (en) Well assembly for heating a subterranean formation
US3095031A (en) Burners for use in bore holes in the ground
US3250327A (en) Recovering nonflowing hydrocarbons
US4079784A (en) Method for in situ combustion for enhanced thermal recovery of hydrocarbons from a well and ignition system therefor
US3050123A (en) Gas fired oil-well burner
US3191679A (en) Melting process for recovering bitumens from the earth
US4050515A (en) Insitu hydrogenation of hydrocarbons in underground formations
US3241615A (en) Downhole burner for wells
US3315745A (en) Bottom hole burner
US5488990A (en) Apparatus and method for generating inert gas and heating injected gas
US2973812A (en) Process and apparatus for in situ combustion
US3410347A (en) Heater apparatus for use in wells
US2985240A (en) Bottom hole burner
US3414055A (en) Formation consolidation using a combustible liner