US1457479A - Method of increasing the yield of oil wells - Google Patents

Method of increasing the yield of oil wells Download PDF

Info

Publication number
US1457479A
US1457479A US350935A US35093520A US1457479A US 1457479 A US1457479 A US 1457479A US 350935 A US350935 A US 350935A US 35093520 A US35093520 A US 35093520A US 1457479 A US1457479 A US 1457479A
Authority
US
United States
Prior art keywords
oil
well
petroleum
pressure
deposit
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
US350935A
Inventor
Edson R Wolcott
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to US350935A priority Critical patent/US1457479A/en
Application granted granted Critical
Publication of US1457479A publication Critical patent/US1457479A/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
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/24Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
    • 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
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/24Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
    • E21B43/2401Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection by means of electricity

Definitions

  • This invention relates to means for increasin the yield of oil wells or producing an additional amount of oil from walls which have become substantially exhausted in producing oil therefrom by the usual pumping means.
  • In the operation of the oil pumping process on oil deposits only-a very partial recovery of the oil is generally obtained and, in fact, after the wells have become exhausted from such operation the major portion of the oil still remains in the ground being retained in the body of oil sand or shale partly by reason of its lack of fluidity and partly by reason of the lack of any expelling force capable of forcing it into the cavities from which the oil is pumped.
  • the present invention is directed to improved means for obtaining a considerable part of the oil thus remaining in the ground after substantial exhaustion as far as regards recovery by the usual pumping means.
  • I apply heat to the body of oil remaining in the ground in such manner as both to increase its fluidity and to produce a force tending to expel the oil from the ground and to bring it into position wherefrom it niay be umped, the necessary heat for this purpose eing obtained mainly by combustion of a portion of the oil or hydrocarbon remaining in the ground.
  • Fig. 1 is a diagrammatic vertical section of a well provided with means for increasing the flow of oil therein;
  • Fig.2 is a vertical section showing two wells provided with means whereby heat enerated at or adjacent to one of the wells is utilized for increasing the flow of another well.
  • FIG. 1 the well therein shown is assumed to be bored through overlying strata, indicated at 1, into a bed or stratum of oil sand, indicated at 2.
  • An upper casing 3 is provided in the bore of the well, this casing being, if desired, the usual well casing such as is usually present in oil wells, but being preferably sealed ofl, if necessary, so as to prevent escape of gas around the outside of the well casin and enable pressure to be maintained wit in the well.
  • this well casing is closed by a 7 cap 4 and aninner pipe or tube 5may extend downwardly through this cap to the lower end of the well and preferably into the bed of oil sand 2'.
  • the outer casing 3 is utilized as a means for conducting a stream or body of air from an air supply pipe 6 down into'the bed of oil sand and the inner pipe 5 is shown as utilized for conducting or drawing away gas from the bed of oil sand, but, if desired, the inner pipe may be utilized for supplying the air and the outer pipe or casing may be used for conducting away the gas in case the later operation is considered necessary.
  • Suitable means are preferably provided for applying heat directly to the bed of oil sand, for example, an electrical heating element,-indicated at 7, of any suitable construction, may be connected at one end tov ground (for example, throu h ipe 5) and at the other end through a wi i'e r conductor 8 to a source of electric current (such as a dynamo-electric machine) indicated at 9, which has a ground connection 10 to complete the circuit.
  • the heatin element 7 is preferably positioned in the lower part of the well and within ordirectly adjacent to the bed of oil sand or oil-bearing material from which it is desired to obtain the oil.
  • Suitable means are also provided for pumping or otherwise obtaining from the well the oil or hydrocarbon which is made available by the operation of the apparatus described above.
  • any suitable pumping means may be used: pipe or well tube 12,v provided at its lower end with the usual working barrel or other pumping means operated by a sucker rod 13 and discharging the oil through an outlet 14 at the upper end of the well tube 12 or, if desired, an air lift pumping means ma be used.
  • the well tube 12 may be either wlthin the inner pipe 5 or at any lace within the outer casing 3, or, if desire the inner pipe 5, which is used for drawing away the gaseous products, may also be used as a well tube ftiilr drawing away the liquid hydrocarbon or o for example, a
  • the inner tube 5 may be connected to any terial will tend to flow an increase in the vapor pressure of suitable means for pumpin or drawing away the gaseous products, for example, a pumpindicated at 16.
  • the electric generator is set in operation to generate an electric current which is conducted through wire 8 to the electric heating element 7, the circuit being completed through the ground connections shown, the resultant generation of heat at the electric heating means causes heat to be produced in the bed of oil in the oil-bearing stratum 2 in such manner as to warm the adjacent mass of oil or hydrocarbon and thereby increases the fluidity thereof, tending to aid in the flow of the oil under the action of gravity assisted, if desired, by maintaining a condition of suction in the inner pipe 5 so as to draw gas from the interior of the well casing and the adjacent portion of the oil-bearing stratum and thereby reducing the pressure of gas at such portion below atmospheric pressure so that the Oil remaining in the oil sand or oil-bearing mato the intake of the well pump by reason of its increased fluidity.
  • the heating of the oil in the manner above stated also has the effect of producing any I volatile constituents that may be contained pressure adjacent in the oil with the result that a condition of pressure is produced in the body or bed of oil or petroleum tending to expel the 011 or force it to the region or zone of reduced to the well casing.
  • the expense of furnishing the heat required for heating the deposit of petroleum. as above described, is, according to my invention reduced to a minimum by utilizing a portion of the petroleum within the well generating the required heat by combust on of the oil or hydrocarbon in the well cavity.
  • a supply of air under suitable pressure which may be either low pressure or high pressure, as desired, is forced through the pipe 6 and casing 3 into the well cavity at the bottom of the well and current is passed through the electrical heating element 7 to cause ignition of the body of hydrocarbon, -whether liquid or gaseous, or both liquid and gaseous constitu-tents thereof, which for the time being are present in the cavity.
  • the outlet pipe 5 may be partially closed by suitable valve means so as to enable a condition of pressure to be developed in the well cavity, but,-in general, it is desirable to maintain sufiicient outlet through pipe 5to allow a continual supply of fresh air to the well cavity so as to enable the combustion of the hydrocarbon to be maintained for a sufiicient time to heat the adjacent body of petroleum in the oil eavers sand.- After operating under pressure in this manner for a given time the pipe 5 may be opened fully and,if desired, acondition of suction may be produced therein by the pumping means, indicated at 16, so as to enable the petroleum in the.
  • FIG. 2 shows an apparatus suitable for applying the invention in such a connection.
  • the respective oil-bearing strata, the well casing and the air supply pipe are indicated by the same reference letters, as above, and the electric heating circuit may be the same as above described but, in this case, the heating means or element is shown as comprising electrodes 20 and 21 connected to the heating circuit 22 and 23, including a dynamo-electric machine 24, said electrodes being insulated and supported in such manner as to provide for the production of the electric are between the same when current of suitable potential diiference is passed through the circuit 23 and 24.
  • the well casing 3 in this case is assumed to be in suflicient proximity to one or more well casings, such as indicated at 30, to enable the thermal and pressure conditions produced adjacent to the well casing 3 to influence the flow of petroleum in such adjacent wells.
  • Each of the adjacent wells 30 may be provided with a. cap 31 and with a suction pipe 32 feeding the pump 33 whereby gases may be drawn from the well or from the cavity at the bottom of the well, and also with a pumping means 34 of any suitable construction.
  • a condition of pressure and increased temperature is produced in the lower part of the well casing 3 by any of the means above mentioned, for example, by heat produced by the electric heating element 20, 21, or by combustion of a portion of the hydrocarbon in the adjacent bed of oil sand, whether such hydrocarbon be in the form of gases, or by a combination of electric heating operation and combustion in such manner that the bed of oil sand adjacent to the well casing 3 is heated to a sutliciently high temperature to considerably increase the fluidity thereof.
  • the heating of the residual oil or petroleum and the resultant increase of fluidity is an important factor in increasing the flow, as it enables the oil to be freed from the sand particles or rock in a manner which is not possible in the thick semi-solid petroleum which usually constitutes the residual hydrocarbon in such cases.
  • Althrough pumping means have been shown for removing the petroleum from the oil wells.
  • my invention is by no means limited to this method, since by increasing the gaseous pressure acting upon the petroleum in the oil sands, more especially by the electrical means when the air inlet valve is closed, a condition of pressure may be attained suflicient to produce a flowing well.
  • any suitable preheating means may be employed, for example, the electrical heating unit 7 may be extended to any desired length Within the casing 3 so that the incoming air may pass around it and assume the desired temperature.
  • the method for increasing the flow of petroleum from deposits thereof which consists in increasing the fluidity of the petrolei um and the pressure Within the deposit, by supplying oxygen to the deposit, causing combustion of a portion of the petroleum in the deposit by means of such oxygen, and thereby generating heat within the deposit substantially without the supply of external fuel thereto.
  • the method which consists in supplying oxygen-bearing gas to a deposit of petrolenm, applying suflicient heat to said deposit adjacent to the point of such gas supply to cause heating of the petroleum and ignition of a portion of the petroleum and continuing to supply oxygen-bearing gas to said deposit to cause combustion of a portion of the petroleum in said deposit in such manner as to heat the deposit of petroleum substantially without the supply of external fuel thereto and to thereby increase the fluidity of the petroleum and the pressure existing thereon and withdrawing petroleum from the deposit under the increased flow produced by such heating action.
  • the method of increasing the flow of petroleum from an oil well which consists in heating a portion oi the oil-hearing material by causing combustion of a portion of the hydrocarbon in such material by means of oxygen supplied thereto and withdrawing the products of combustion under such control as to maintain a condition of pressure within the deposit.
  • the method for increasing the flow of petroleum from deposits thereof which consists in generating hot gases under pressure by burning a portion ol the hydrocarbon contained in the deposit by means of oxygenbearing gas forced into the deposit confining the gases so generated within the deposit to maintain the condition of pressure, and removing the )etroleum from the deposit under the condition of increased fluidity and pressure due to the presence of such hot gases under pressure.

Description

June 5, 1923. 1,457,479
I E. R. WOLCOTT METHOD OF INCREASING THE YIELD OF OIL WELLS Filed Jan. 12, 1920 IN VE IV TOR Patented June 5, 1323.
UNITED STATES EDSON WOLCOTT, 015 LOS ANGELES, CALIFORNIA. v
METHOD OF INCREASING THE YIELD OIL WELLS.
Application filed January 12, 1920. Serial No. 850,985.
T all whom it may concern:
Be it known that I, EDSON R. IVoLco'rr, a
- citizen of the United States. residing at Los Angeles. in the county of Los Augeles and State of California, have invented a new and useful Method of Increasing the Yield of Oil Wells, of which the following is a specification. ,i
This invention relates to means for increasin the yield of oil wells or producing an additional amount of oil from walls which have become substantially exhausted in producing oil therefrom by the usual pumping means. In the operation of the oil pumping process on oil deposits only-a very partial recovery of the oil is generally obtained and, in fact, after the wells have become exhausted from such operation the major portion of the oil still remains in the ground being retained in the body of oil sand or shale partly by reason of its lack of fluidity and partly by reason of the lack of any expelling force capable of forcing it into the cavities from which the oil is pumped.
The present invention is directed to improved means for obtaining a considerable part of the oil thus remaining in the ground after substantial exhaustion as far as regards recovery by the usual pumping means. For this purpose I apply heat to the body of oil remaining in the ground in such manner as both to increase its fluidity and to produce a force tending to expel the oil from the ground and to bring it into position wherefrom it niay be umped, the necessary heat for this purpose eing obtained mainly by combustion of a portion of the oil or hydrocarbon remaining in the ground.
The accompanying drawings illustrate different forms of the apparatus for carrying out my invention, and referring thereto:
Fig. 1 is a diagrammatic vertical section of a well provided with means for increasing the flow of oil therein;
Fig.2 is a vertical section showing two wells provided with means whereby heat enerated at or adjacent to one of the wells is utilized for increasing the flow of another well.
Referring to Fig. 1, the well therein shown is assumed to be bored through overlying strata, indicated at 1, into a bed or stratum of oil sand, indicated at 2. An upper casing 3 is provided in the bore of the well, this casing being, if desired, the usual well casing such as is usually present in oil wells, but being preferably sealed ofl, if necessary, so as to prevent escape of gas around the outside of the well casin and enable pressure to be maintained wit in the well. The
upper end of this well casing is closed by a 7 cap 4 and aninner pipe or tube 5may extend downwardly through this cap to the lower end of the well and preferably into the bed of oil sand 2'.
As shown in the drawing, the outer casing 3 is utilized as a means for conducting a stream or body of air from an air supply pipe 6 down into'the bed of oil sand and the inner pipe 5 is shown as utilized for conducting or drawing away gas from the bed of oil sand, but, if desired, the inner pipe may be utilized for supplying the air and the outer pipe or casing may be used for conducting away the gas in case the later operation is considered necessary.
Suitable means are preferably provided for applying heat directly to the bed of oil sand, for example, an electrical heating element,-indicated at 7, of any suitable construction, may be connected at one end tov ground (for example, throu h ipe 5) and at the other end through a wi i'e r conductor 8 to a source of electric current (such as a dynamo-electric machine) indicated at 9, which has a ground connection 10 to complete the circuit. The heatin element 7 is preferably positioned in the lower part of the well and within ordirectly adjacent to the bed of oil sand or oil-bearing material from which it is desired to obtain the oil.
Suitable means are also provided for pumping or otherwise obtaining from the well the oil or hydrocarbon which is made available by the operation of the apparatus described above., For this pur ose any suitable pumping means may be used: pipe or well tube 12,v provided at its lower end with the usual working barrel or other pumping means operated by a sucker rod 13 and discharging the oil through an outlet 14 at the upper end of the well tube 12 or, if desired, an air lift pumping means ma be used. The well tube 12 may be either wlthin the inner pipe 5 or at any lace within the outer casing 3, or, if desire the inner pipe 5, which is used for drawing away the gaseous products, may also be used as a well tube ftiilr drawing away the liquid hydrocarbon or o for example, a
The inner tube 5 may be connected to any terial will tend to flow an increase in the vapor pressure of suitable means for pumpin or drawing away the gaseous products, for example, a pumpindicated at 16.
The operation of my process in the above described apparatus is as follows:
The parts having been positioned as above described, the electric generator is set in operation to generate an electric current which is conducted through wire 8 to the electric heating element 7, the circuit being completed through the ground connections shown, the resultant generation of heat at the electric heating means causes heat to be produced in the bed of oil in the oil-bearing stratum 2 in such manner as to warm the adjacent mass of oil or hydrocarbon and thereby increases the fluidity thereof, tending to aid in the flow of the oil under the action of gravity assisted, if desired, by maintaining a condition of suction in the inner pipe 5 so as to draw gas from the interior of the well casing and the adjacent portion of the oil-bearing stratum and thereby reducing the pressure of gas at such portion below atmospheric pressure so that the Oil remaining in the oil sand or oil-bearing mato the intake of the well pump by reason of its increased fluidity. The heating of the oil in the manner above stated also has the effect of producing any I volatile constituents that may be contained pressure adjacent in the oil with the result that a condition of pressure is produced in the body or bed of oil or petroleum tending to expel the 011 or force it to the region or zone of reduced to the well casing.
The expense of furnishing the heat required for heating the deposit of petroleum. as above described, is, according to my invention reduced to a minimum by utilizing a portion of the petroleum within the well generating the required heat by combust on of the oil or hydrocarbon in the well cavity. For this purpose a supply of air under suitable pressure, which may be either low pressure or high pressure, as desired, is forced through the pipe 6 and casing 3 into the well cavity at the bottom of the well and current is passed through the electrical heating element 7 to cause ignition of the body of hydrocarbon, -whether liquid or gaseous, or both liquid and gaseous constitu-tents thereof, which for the time being are present in the cavity. It is to be understood that under these conditions the outlet pipe 5 may be partially closed by suitable valve means so as to enable a condition of pressure to be developed in the well cavity, but,-in general, it is desirable to maintain sufiicient outlet through pipe 5to allow a continual supply of fresh air to the well cavity so as to enable the combustion of the hydrocarbon to be maintained for a sufiicient time to heat the adjacent body of petroleum in the oil eavers sand.- After operating under pressure in this manner for a given time the pipe 5 may be opened fully and,if desired, acondition of suction may be produced therein by the pumping means, indicated at 16, so as to enable the petroleum in the. oil sand, which has been rendered more fluid by reason of the heat, to flow to the well cavity by the action of gravity assisted by the gas pressure developed in the petroleum by the action of the heat. \Vhen theprocess is carried out in this manner under considerable pressure during the heating operation, the effect of such pressure is to tend to cause the hot gases to be forced through the more or less porous oil sand so as to carry the heat to a larger portion or zone of the oil-bearing material,
and on reduction of the pressure in the manner stated during the pumping operation the condition of pressure previously developed in the oil sand is of assistance in forcing the petroleum into the well cavity.
Another important application of my invention is connected with the recovery of the residual petroleum inan exhausted oil field in which a large number of abandoned wells exist in more or less close relation, Fig. 2 showing an apparatus suitable for applying the invention in such a connection. In said Fig. 2 the respective oil-bearing strata, the well casing and the air supply pipe are indicated by the same reference letters, as above, and the electric heating circuit may be the same as above described but, in this case, the heating means or element is shown as comprising electrodes 20 and 21 connected to the heating circuit 22 and 23, including a dynamo-electric machine 24, said electrodes being insulated and supported in such manner as to provide for the production of the electric are between the same when current of suitable potential diiference is passed through the circuit 23 and 24. The well casing 3 in this case is assumed to be in suflicient proximity to one or more well casings, such as indicated at 30, to enable the thermal and pressure conditions produced adjacent to the well casing 3 to influence the flow of petroleum in such adjacent wells. Each of the adjacent wells 30 may be provided with a. cap 31 and with a suction pipe 32 feeding the pump 33 whereby gases may be drawn from the well or from the cavity at the bottom of the well, and also with a pumping means 34 of any suitable construction. In carrying out my invention with the equipment shown in Fig. 2 a condition of pressure and increased temperature is produced in the lower part of the well casing 3 by any of the means above mentioned, for example, by heat produced by the electric heating element 20, 21, or by combustion of a portion of the hydrocarbon in the adjacent bed of oil sand, whether such hydrocarbon be in the form of gases, or by a combination of electric heating operation and combustion in such manner that the bed of oil sand adjacent to the well casing 3 is heated to a sutliciently high temperature to considerably increase the fluidity thereof.
It will be understood that in this form of the invention in order to maintain combustion for any considerable length of time, it will be necessary to continuously supply air with the air inlet pipe (3. In many cases the porosity of the oil sand after a portion of the oil has been extracted therefrom by the usual methods is such that ,l'resh air can be continually forced into the well casing 3 and the products of combustion find vent through the pores or interstices of the oil sand in the oil-bearing stratum. In carrying out my invention in this manner, I prel'cr to shut oti' or cap all but one of the surrounding or adjacent wells. that is. those in the same oil-bearing strata. only one of the wells, for example, the one indicated at 30, being provided with an outlet pipe, indicated at 32. and under these conditions the gaseous products of combustion or gases under pressure emanating from the well casing 3 in which combustion is maintained, will eventually find their "S ay mainly to this adjacent well casing 30 and will be drawn off through the outlet pipe 32. The described method of operation therefor in producing a considerable increase of temperature and pressure in and adjacent to the well casing 3 and in the adjacent body of oil sand accompanied if desired,by areduction of pressure by operation of the pump 33 in the well 30 and the oil sand adjacent thereto will cause a large portion of the oil remaining in the body of oil sand between the well casings 3 and 30 to flow under the action of the difference of pressure in said well casings assisted by the action of gravity in the well cavity at the bottom of the well casing 30. In this case, however, as well as in the application of my invention above described, the heating of the residual oil or petroleum and the resultant increase of fluidity is an important factor in increasing the flow, as it enables the oil to be freed from the sand particles or rock in a manner which is not possible in the thick semi-solid petroleum which usually constitutes the residual hydrocarbon in such cases.
Althrough pumping means have been shown for removing the petroleum from the oil wells. my invention is by no means limited to this method, since by increasing the gaseous pressure acting upon the petroleum in the oil sands, more especially by the electrical means when the air inlet valve is closed, a condition of pressure may be attained suflicient to produce a flowing well.
Whenever it is desired to preheat the air or oxygen delivered to the petroleum in the oil sands to promote more efficient combustion or to bring it to a sutliciently high temperature to ignite the petroleum, any suitable preheating means may be employed, for example, the electrical heating unit 7 may be extended to any desired length Within the casing 3 so that the incoming air may pass around it and assume the desired temperature.
'hat I claim is:
1. The process of obtaining petroleumv from. oil sand, etc, which consists in supplying oxygen to the deposit of petroleum, causing combustion of aportion of the petroleum in the deposit by means of such oxygen so as to generate heat within the deposit of petroleum substantially without the supply of fuel from an external source, and thereby heating the deposit of petroleum in the oil sand in such manner as to increase the fluidity of same and generating pressure within the body of petroleum, and then subjecting the body of petroleum to pumping action.
2. A process as set forth in claim 1, wherein the body of petroleum is subjected at a certain portion thereof to suctional effect to decrease the barometric pressure in such portion to assist in the flow of petroleum to such portion of reduced pressure, and the petroleum is then pumped from such portion at reduced pressure.
3. The method for increasing the flow of petroleum from deposits thereof, which consists in increasing the fluidity of the petrolei um and the pressure Within the deposit, by supplying oxygen to the deposit, causing combustion of a portion of the petroleum in the deposit by means of such oxygen, and thereby generating heat within the deposit substantially without the supply of external fuel thereto.
4. The method which consists in supplying oxygen-bearing gas to a deposit of petrolenm, applying suflicient heat to said deposit adjacent to the point of such gas supply to cause heating of the petroleum and ignition of a portion of the petroleum and continuing to supply oxygen-bearing gas to said deposit to cause combustion of a portion of the petroleum in said deposit in such manner as to heat the deposit of petroleum substantially without the supply of external fuel thereto and to thereby increase the fluidity of the petroleum and the pressure existing thereon and withdrawing petroleum from the deposit under the increased flow produced by such heating action.
5. The-method which consists in producing heat within apetroleum deposit by the action of an electrical current, supplying oxygen-bearing gas to said deposit to effect combustion of a portion of the petroleum in said deposit which is ignited by the heating action of such current thereby generating heat Within the deposit in addition to that &
furnished by the electrical current. substantially without the use of fuel from an external source, and causin increase of fluidity of the petroleum and oi the pressure thereon and withdrawing the petroleum from the deposit under the resulting conditions of increased fluidity and pressure.
6. The method of increasing the flow of petroleum from an oil well which consists in heating a portion oi the oil-hearing material by causing combustion of a portion of the hydrocarbon in such material by means of oxygen supplied thereto and withdrawing the products of combustion under such control as to maintain a condition of pressure within the deposit.
7. The method for increasing the flow of petroleum from deposits thereof, which consists in generating hot gases under pressure by burning a portion ol the hydrocarbon contained in the deposit by means of oxygenbearing gas forced into the deposit confining the gases so generated within the deposit to maintain the condition of pressure, and removing the )etroleum from the deposit under the condition of increased fluidity and pressure due to the presence of such hot gases under pressure.
8. The method of operating oil wells consisting of closing the top of a central well, pumping air into said well, producing combustion therein, and pumping the surrounding Wells.
In testimony whereof I have hereunto subscribed my name this 7th day of January, 1920.
EDSON R. VVOLCOTT.
US350935A 1920-01-12 1920-01-12 Method of increasing the yield of oil wells Expired - Lifetime US1457479A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US350935A US1457479A (en) 1920-01-12 1920-01-12 Method of increasing the yield of oil wells

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US350935A US1457479A (en) 1920-01-12 1920-01-12 Method of increasing the yield of oil wells

Publications (1)

Publication Number Publication Date
US1457479A true US1457479A (en) 1923-06-05

Family

ID=23378821

Family Applications (1)

Application Number Title Priority Date Filing Date
US350935A Expired - Lifetime US1457479A (en) 1920-01-12 1920-01-12 Method of increasing the yield of oil wells

Country Status (1)

Country Link
US (1) US1457479A (en)

Cited By (78)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2421528A (en) * 1944-07-26 1947-06-03 Ralph M Steffen Underground oil recovery
US2500990A (en) * 1945-07-28 1950-03-21 Linde Air Prod Co Apparatus for increasing production of oil wells
US2506853A (en) * 1945-05-30 1950-05-09 Union Oil Co Oil well furnace
US2634961A (en) * 1946-01-07 1953-04-14 Svensk Skifferolje Aktiebolage Method of electrothermal production of shale oil
US2636445A (en) * 1946-12-27 1953-04-28 Fred S Tutton Production method and apparatus
US2647585A (en) * 1949-02-12 1953-08-04 Viola Violet Roberts Heater for oil and other wells
US2707029A (en) * 1950-07-28 1955-04-26 Carroll H Van Hartesveldt Apparatus for obtaining liquids from deep wells
US2732195A (en) * 1956-01-24 Ljungstrom
US2734579A (en) * 1956-02-14 Production from bituminous sands
US2777679A (en) * 1952-03-07 1957-01-15 Svenska Skifferolje Ab Recovering sub-surface bituminous deposits by creating a frozen barrier and heating in situ
US2780450A (en) * 1952-03-07 1957-02-05 Svenska Skifferolje Ab Method of recovering oil and gases from non-consolidated bituminous geological formations by a heating treatment in situ
US2785753A (en) * 1954-06-28 1957-03-19 Spearow Ralph Single packer oil production method
US2795279A (en) * 1952-04-17 1957-06-11 Electrotherm Res Corp Method of underground electrolinking and electrocarbonization of mineral fuels
US2819761A (en) * 1956-01-19 1958-01-14 Continental Oil Co Process of removing viscous oil from a well bore
US2832417A (en) * 1954-08-27 1958-04-29 Sinclair Oil & Gas Company Bottom hole igniter and burner
US2841375A (en) * 1954-03-03 1958-07-01 Svenska Skifferolje Ab Method for in-situ utilization of fuels by combustion
US2858891A (en) * 1952-05-16 1958-11-04 Union Rheinische Braunkohlen Pressure maintenance and repressuring in oil and gas fields
US2874777A (en) * 1954-07-19 1959-02-24 Shell Dev Producing petroleum by underground combustion
US2889881A (en) * 1956-05-14 1959-06-09 Phillips Petroleum Co Oil recovery by in situ combustion
US2906340A (en) * 1956-04-05 1959-09-29 Texaco Inc Method of treating a petroleum producing formation
US2917112A (en) * 1956-11-13 1959-12-15 Phillips Petroleum Co Inverse air injection technique
US2923535A (en) * 1955-02-11 1960-02-02 Svenska Skifferolje Ab Situ recovery from carbonaceous deposits
US2924276A (en) * 1955-08-08 1960-02-09 Jersey Prod Res Co Secondary recovery operation
US2939689A (en) * 1947-06-24 1960-06-07 Svenska Skifferolje Ab Electrical heater for treating oilshale and the like
US2946382A (en) * 1956-09-19 1960-07-26 Phillips Petroleum Co Process for recovering hydrocarbons from underground formations
US3003555A (en) * 1956-09-18 1961-10-10 Jersey Prod Res Co Oil production from unconsolidated formations
US3026937A (en) * 1957-05-17 1962-03-27 California Research Corp Method of controlling an underground combustion zone
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
US3113620A (en) * 1959-07-06 1963-12-10 Exxon Research Engineering Co Process for producing viscous oil
US3139928A (en) * 1960-05-24 1964-07-07 Shell Oil Co Thermal process for in situ decomposition of oil shale
US3170519A (en) * 1960-05-11 1965-02-23 Gordon L Allot Oil well microwave tools
US3171482A (en) * 1961-07-31 1965-03-02 California Research Corp Method of increasing the production of petroleum from subterranean formations
US3180418A (en) * 1961-08-16 1965-04-27 Norman A Macleod Casing descaling method and apparatus
US3207220A (en) * 1961-06-26 1965-09-21 Chester I Williams Electric well heater
US3503446A (en) * 1968-05-13 1970-03-31 Clarence W Brandon Method and apparatus for forming and/or augmenting an energy wave
US3718186A (en) * 1970-03-17 1973-02-27 Brandon O Method and apparatus for forming and/or augmenting an energy wave
US4997044A (en) * 1989-12-01 1991-03-05 Stack Walter E Apparatus for generating hydraulic shock waves in a well
WO2001081239A2 (en) * 2000-04-24 2001-11-01 Shell Internationale Research Maatschappij B.V. In situ recovery from a hydrocarbon containing formation
US20030066642A1 (en) * 2000-04-24 2003-04-10 Wellington Scott Lee In situ thermal processing of a coal formation producing a mixture with oxygenated hydrocarbons
US20030079877A1 (en) * 2001-04-24 2003-05-01 Wellington Scott Lee In situ thermal processing of a relatively impermeable formation in a reducing environment
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
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
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
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
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
US20050269091A1 (en) * 2004-04-23 2005-12-08 Guillermo Pastor-Sanz Reducing viscosity of oil for production from a hydrocarbon containing formation
US7011154B2 (en) 2000-04-24 2006-03-14 Shell Oil Company In situ recovery from a kerogen and liquid hydrocarbon containing 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
US20070045267A1 (en) * 2005-04-22 2007-03-01 Vinegar Harold J Subsurface connection methods for subsurface heaters
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
US20070131427A1 (en) * 2005-10-24 2007-06-14 Ruijian Li Systems and methods for producing hydrocarbons from tar sands formations
US20080038144A1 (en) * 2006-04-21 2008-02-14 Maziasz Phillip J High strength alloys
US20090194333A1 (en) * 2007-10-19 2009-08-06 Macdonald Duncan Ranging methods for developing wellbores in subsurface formations
US7640987B2 (en) 2005-08-17 2010-01-05 Halliburton Energy Services, Inc. Communicating fluids with a heated-fluid generation system
US20100147521A1 (en) * 2008-10-13 2010-06-17 Xueying Xie Perforated electrical conductors for treating subsurface formations
US7770643B2 (en) 2006-10-10 2010-08-10 Halliburton Energy Services, Inc. Hydrocarbon recovery using fluids
US7809538B2 (en) 2006-01-13 2010-10-05 Halliburton Energy Services, Inc. Real time monitoring and control of thermal recovery operations for heavy oil reservoirs
US20100258290A1 (en) * 2009-04-10 2010-10-14 Ronald Marshall Bass Non-conducting heater casings
US7832482B2 (en) 2006-10-10 2010-11-16 Halliburton Energy Services, Inc. Producing resources using steam injection
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
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
US9353611B2 (en) 2012-11-02 2016-05-31 Trimeteor Oil & Gas Corp. Method and apparatus for the downhole injection of superheated steam
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

Cited By (319)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2732195A (en) * 1956-01-24 Ljungstrom
US2734579A (en) * 1956-02-14 Production from bituminous sands
US2421528A (en) * 1944-07-26 1947-06-03 Ralph M Steffen Underground oil recovery
US2506853A (en) * 1945-05-30 1950-05-09 Union Oil Co Oil well furnace
US2500990A (en) * 1945-07-28 1950-03-21 Linde Air Prod Co Apparatus for increasing production of oil wells
US2634961A (en) * 1946-01-07 1953-04-14 Svensk Skifferolje Aktiebolage Method of electrothermal production of shale oil
US2636445A (en) * 1946-12-27 1953-04-28 Fred S Tutton Production method and apparatus
US2939689A (en) * 1947-06-24 1960-06-07 Svenska Skifferolje Ab Electrical heater for treating oilshale and the like
US2647585A (en) * 1949-02-12 1953-08-04 Viola Violet Roberts Heater for oil and other wells
US2707029A (en) * 1950-07-28 1955-04-26 Carroll H Van Hartesveldt Apparatus for obtaining liquids from deep wells
US2780450A (en) * 1952-03-07 1957-02-05 Svenska Skifferolje Ab Method of recovering oil and gases from non-consolidated bituminous geological formations by a heating treatment in situ
US2777679A (en) * 1952-03-07 1957-01-15 Svenska Skifferolje Ab Recovering sub-surface bituminous deposits by creating a frozen barrier and heating in situ
US2795279A (en) * 1952-04-17 1957-06-11 Electrotherm Res Corp Method of underground electrolinking and electrocarbonization of mineral fuels
US2858891A (en) * 1952-05-16 1958-11-04 Union Rheinische Braunkohlen Pressure maintenance and repressuring in oil and gas fields
US2841375A (en) * 1954-03-03 1958-07-01 Svenska Skifferolje Ab Method for in-situ utilization of fuels by combustion
US2785753A (en) * 1954-06-28 1957-03-19 Spearow Ralph Single packer oil production method
US2874777A (en) * 1954-07-19 1959-02-24 Shell Dev Producing petroleum by underground combustion
US2832417A (en) * 1954-08-27 1958-04-29 Sinclair Oil & Gas Company Bottom hole igniter and burner
US2923535A (en) * 1955-02-11 1960-02-02 Svenska Skifferolje Ab Situ recovery from carbonaceous deposits
US2924276A (en) * 1955-08-08 1960-02-09 Jersey Prod Res Co Secondary recovery operation
US2819761A (en) * 1956-01-19 1958-01-14 Continental Oil Co Process of removing viscous oil from a well bore
US2906340A (en) * 1956-04-05 1959-09-29 Texaco Inc Method of treating a petroleum producing formation
US2889881A (en) * 1956-05-14 1959-06-09 Phillips Petroleum Co Oil recovery by in situ combustion
US3003555A (en) * 1956-09-18 1961-10-10 Jersey Prod Res Co Oil production from unconsolidated formations
US2946382A (en) * 1956-09-19 1960-07-26 Phillips Petroleum Co Process for recovering hydrocarbons from underground formations
US2917112A (en) * 1956-11-13 1959-12-15 Phillips Petroleum Co Inverse air injection technique
US3026937A (en) * 1957-05-17 1962-03-27 California Research Corp Method of controlling an underground combustion zone
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
US3113620A (en) * 1959-07-06 1963-12-10 Exxon Research Engineering Co Process for producing viscous oil
US3170519A (en) * 1960-05-11 1965-02-23 Gordon L Allot Oil well microwave tools
US3139928A (en) * 1960-05-24 1964-07-07 Shell Oil Co Thermal process for in situ decomposition of oil shale
US3207220A (en) * 1961-06-26 1965-09-21 Chester I Williams Electric well heater
US3171482A (en) * 1961-07-31 1965-03-02 California Research Corp Method of increasing the production of petroleum from subterranean formations
US3180418A (en) * 1961-08-16 1965-04-27 Norman A Macleod Casing descaling method and apparatus
US3503446A (en) * 1968-05-13 1970-03-31 Clarence W Brandon Method and apparatus for forming and/or augmenting an energy wave
US3718186A (en) * 1970-03-17 1973-02-27 Brandon O Method and apparatus for forming and/or augmenting an energy wave
US4997044A (en) * 1989-12-01 1991-03-05 Stack Walter E Apparatus for generating hydraulic shock waves in a well
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
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
GB2379469A (en) * 2000-04-24 2003-03-12 Shell Int Research In situ recovery from a hydrocarbon containing formation
US20030066642A1 (en) * 2000-04-24 2003-04-10 Wellington Scott Lee In situ thermal processing of a coal formation producing a mixture with oxygenated hydrocarbons
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
US6994161B2 (en) 2000-04-24 2006-02-07 Kevin Albert Maher In situ thermal processing of a coal formation with a selected moisture 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
US7096953B2 (en) 2000-04-24 2006-08-29 Shell Oil Company In situ thermal processing of a coal formation using a movable heating element
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
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
US6973967B2 (en) 2000-04-24 2005-12-13 Shell Oil Company Situ thermal processing of a coal formation using pressure and/or temperature control
US6588503B2 (en) 2000-04-24 2003-07-08 Shell Oil Company In Situ thermal processing of a coal formation to control product composition
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
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
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
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
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
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
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
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
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
US6609570B2 (en) 2000-04-24 2003-08-26 Shell Oil Company In situ thermal processing of a coal formation and ammonia production
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
US8789586B2 (en) 2000-04-24 2014-07-29 Shell Oil Company In situ recovery from a hydrocarbon containing formation
WO2001081239A3 (en) * 2000-04-24 2002-05-23 Shell Oil Co In situ recovery from a hydrocarbon containing 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
US8485252B2 (en) 2000-04-24 2013-07-16 Shell Oil Company In situ recovery from a hydrocarbon containing formation
US8225866B2 (en) 2000-04-24 2012-07-24 Shell Oil Company In situ recovery from a hydrocarbon containing formation
WO2001081239A2 (en) * 2000-04-24 2001-11-01 Shell Internationale Research Maatschappij B.V. In situ recovery from a hydrocarbon containing formation
US20110088904A1 (en) * 2000-04-24 2011-04-21 De Rouffignac Eric Pierre In situ recovery from a hydrocarbon containing formation
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
US6729401B2 (en) 2000-04-24 2004-05-04 Shell Oil Company In situ thermal processing of a hydrocarbon containing formation and ammonia production
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
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
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
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
GB2379469B (en) * 2000-04-24 2004-09-29 Shell Int Research In situ recovery from a hydrocarbon containing formation
US8608249B2 (en) 2001-04-24 2013-12-17 Shell Oil Company In situ thermal processing of an oil shale formation
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
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
US20100270015A1 (en) * 2001-04-24 2010-10-28 Shell Oil Company In situ thermal processing of an oil shale formation
US20030209348A1 (en) * 2001-04-24 2003-11-13 Ward John Michael In situ thermal processing and remediation of an oil shale formation
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
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
US20030155111A1 (en) * 2001-04-24 2003-08-21 Shell Oil Co In situ thermal processing of a tar sands 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
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
US20030141066A1 (en) * 2001-04-24 2003-07-31 Karanikas John Michael In situ thermal processing of an oil shale formation while inhibiting coking
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
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
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
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
US20030136559A1 (en) * 2001-04-24 2003-07-24 Wellington Scott Lee In situ thermal processing while controlling pressure in 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
US7735935B2 (en) 2001-04-24 2010-06-15 Shell Oil Company In situ thermal processing of an oil shale formation containing carbonate minerals
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
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
US6951247B2 (en) 2001-04-24 2005-10-04 Shell Oil Company In situ thermal processing of an oil shale formation using horizontal heat sources
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
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
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
US20030131994A1 (en) * 2001-04-24 2003-07-17 Vinegar Harold J. In situ thermal processing and solution mining of an 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
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
US20030130136A1 (en) * 2001-04-24 2003-07-10 Rouffignac Eric Pierre De In situ thermal processing of a relatively impermeable formation using an open wellbore
US20030116315A1 (en) * 2001-04-24 2003-06-26 Wellington Scott Lee In situ thermal processing of a relatively permeable formation
US6981548B2 (en) 2001-04-24 2006-01-03 Shell Oil Company In situ thermal recovery from a relatively permeable formation
US6991033B2 (en) 2001-04-24 2006-01-31 Shell Oil Company In situ thermal processing while controlling pressure in an oil shale formation
US6991036B2 (en) 2001-04-24 2006-01-31 Shell Oil Company Thermal processing of a relatively permeable formation
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
US20030102125A1 (en) * 2001-04-24 2003-06-05 Wellington Scott Lee In situ thermal processing of a relatively permeable formation in a reducing environment
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
US20030102124A1 (en) * 2001-04-24 2003-06-05 Vinegar Harold J. In situ thermal processing of a blending agent from a relatively permeable formation
US20030102130A1 (en) * 2001-04-24 2003-06-05 Vinegar Harold J. In situ thermal recovery from a relatively permeable formation with quality control
US6994169B2 (en) 2001-04-24 2006-02-07 Shell Oil Company In situ thermal processing of an oil shale formation with a selected property
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
US20030098605A1 (en) * 2001-04-24 2003-05-29 Vinegar Harold J. In situ thermal recovery from a relatively permeable formation
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
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
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
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
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
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
US7040400B2 (en) 2001-04-24 2006-05-09 Shell Oil Company In situ thermal processing of a relatively impermeable formation using an open wellbore
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
US7051807B2 (en) 2001-04-24 2006-05-30 Shell Oil Company In situ thermal recovery from a relatively permeable formation with quality control
US7051811B2 (en) 2001-04-24 2006-05-30 Shell Oil Company In situ thermal processing through an open wellbore in an oil shale formation
US7096942B1 (en) 2001-04-24 2006-08-29 Shell Oil Company In situ thermal processing of a relatively permeable formation while controlling pressure
US7055600B2 (en) 2001-04-24 2006-06-06 Shell Oil Company In situ thermal recovery from a relatively permeable formation with controlled production rate
US20030079877A1 (en) * 2001-04-24 2003-05-01 Wellington Scott Lee In situ thermal processing of a relatively impermeable formation in a reducing environment
US20030201098A1 (en) * 2001-10-24 2003-10-30 Karanikas John Michael In situ recovery from a hydrocarbon containing formation using one or more simulations
US8627887B2 (en) 2001-10-24 2014-01-14 Shell Oil Company In situ recovery from a hydrocarbon containing formation
US20100126727A1 (en) * 2001-10-24 2010-05-27 Shell Oil Company In situ recovery 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
US7077198B2 (en) 2001-10-24 2006-07-18 Shell Oil Company In situ recovery from a hydrocarbon containing formation using barriers
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
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
US6991045B2 (en) 2001-10-24 2006-01-31 Shell Oil Company Forming openings in a hydrocarbon containing formation using magnetic tracking
US20030173081A1 (en) * 2001-10-24 2003-09-18 Vinegar Harold J. In situ thermal processing of an oil reservoir formation
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
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
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
US7128153B2 (en) 2001-10-24 2006-10-31 Shell Oil Company Treatment of a hydrocarbon containing formation after heating
US7156176B2 (en) 2001-10-24 2007-01-02 Shell Oil Company Installation and use of removable heaters in a hydrocarbon containing formation
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
US6969123B2 (en) 2001-10-24 2005-11-29 Shell Oil Company Upgrading and mining of coal
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
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
US20040040715A1 (en) * 2001-10-24 2004-03-04 Wellington Scott Lee In situ production of a blending agent from a hydrocarbon containing formation
US20030205378A1 (en) * 2001-10-24 2003-11-06 Wellington Scott Lee In situ recovery from lean and rich zones in a hydrocarbon containing formation
US20030196810A1 (en) * 2001-10-24 2003-10-23 Vinegar Harold J. Treatment of a hydrocarbon containing formation after heating
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
US8238730B2 (en) 2002-10-24 2012-08-07 Shell Oil Company High voltage 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
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
US7942203B2 (en) 2003-04-24 2011-05-17 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
US7121342B2 (en) 2003-04-24 2006-10-17 Shell Oil Company Thermal processes for subsurface formations
US7510000B2 (en) * 2004-04-23 2009-03-31 Shell Oil Company Reducing viscosity of oil for production from a hydrocarbon containing formation
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
US8355623B2 (en) 2004-04-23 2013-01-15 Shell Oil Company Temperature limited heaters with high power factors
US20070045268A1 (en) * 2005-04-22 2007-03-01 Vinegar Harold J Varying properties along lengths of temperature limited heaters
US20070045267A1 (en) * 2005-04-22 2007-03-01 Vinegar Harold J Subsurface connection methods for subsurface heaters
US8233782B2 (en) 2005-04-22 2012-07-31 Shell Oil Company Grouped exposed metal heaters
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
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
US20070133959A1 (en) * 2005-04-22 2007-06-14 Vinegar Harold J Grouped exposed metal heaters
US8224165B2 (en) 2005-04-22 2012-07-17 Shell Oil Company Temperature limited heater utilizing non-ferromagnetic conductor
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
US8230927B2 (en) 2005-04-22 2012-07-31 Shell Oil Company Methods and systems for producing fluid from an in situ conversion process
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
US7831134B2 (en) 2005-04-22 2010-11-09 Shell Oil Company Grouped exposed metal heaters
US20080217321A1 (en) * 2005-04-22 2008-09-11 Vinegar Harold J Temperature limited heater utilizing non-ferromagnetic conductor
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
US7640987B2 (en) 2005-08-17 2010-01-05 Halliburton Energy Services, Inc. Communicating fluids with a heated-fluid generation system
US7562706B2 (en) 2005-10-24 2009-07-21 Shell Oil Company Systems and methods for producing hydrocarbons from tar sands formations
US7559367B2 (en) 2005-10-24 2009-07-14 Shell Oil Company Temperature limited heater with a conduit substantially electrically isolated from the formation
US20070131427A1 (en) * 2005-10-24 2007-06-14 Ruijian Li Systems and methods for producing hydrocarbons from tar sands formations
US7809538B2 (en) 2006-01-13 2010-10-05 Halliburton Energy Services, Inc. Real time monitoring and control of thermal recovery operations for heavy oil reservoirs
US20100272595A1 (en) * 2006-04-21 2010-10-28 Shell Oil Company High strength alloys
US20080035347A1 (en) * 2006-04-21 2008-02-14 Brady Michael P Adjusting alloy compositions for selected properties in temperature limited heaters
US20080038144A1 (en) * 2006-04-21 2008-02-14 Maziasz Phillip J High strength alloys
US7683296B2 (en) 2006-04-21 2010-03-23 Shell Oil Company Adjusting alloy compositions for selected properties in temperature limited heaters
US8192682B2 (en) 2006-04-21 2012-06-05 Shell Oil Company High strength alloys
US7785427B2 (en) 2006-04-21 2010-08-31 Shell Oil Company High strength alloys
US7832482B2 (en) 2006-10-10 2010-11-16 Halliburton Energy Services, Inc. Producing resources using steam injection
US7770643B2 (en) 2006-10-10 2010-08-10 Halliburton Energy Services, Inc. Hydrocarbon recovery using fluids
US8113272B2 (en) 2007-10-19 2012-02-14 Shell Oil Company Three-phase heaters with common overburden sections for heating subsurface formations
US8146661B2 (en) 2007-10-19 2012-04-03 Shell Oil Company Cryogenic treatment of gas
US8536497B2 (en) 2007-10-19 2013-09-17 Shell Oil Company Methods for forming long subsurface heaters
US8162059B2 (en) 2007-10-19 2012-04-24 Shell Oil Company Induction heaters used to heat subsurface formations
US8146669B2 (en) 2007-10-19 2012-04-03 Shell Oil Company Multi-step heater deployment in a subsurface formation
US7866388B2 (en) 2007-10-19 2011-01-11 Shell Oil Company High temperature methods for forming oxidizer fuel
US8240774B2 (en) 2007-10-19 2012-08-14 Shell Oil Company 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
US8196658B2 (en) 2007-10-19 2012-06-12 Shell Oil Company Irregular spacing of heat sources for treating hydrocarbon containing formations
US7866386B2 (en) 2007-10-19 2011-01-11 Shell Oil Company In situ oxidation of subsurface formations
US20090194333A1 (en) * 2007-10-19 2009-08-06 Macdonald Duncan Ranging methods for developing wellbores in subsurface formations
US8272455B2 (en) 2007-10-19 2012-09-25 Shell Oil Company Methods for forming wellbores in heated formations
US8276661B2 (en) 2007-10-19 2012-10-02 Shell Oil Company Heating subsurface formations by oxidizing fuel on a fuel carrier
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
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
US8562078B2 (en) 2008-04-18 2013-10-22 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
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
US8162405B2 (en) 2008-04-18 2012-04-24 Shell Oil Company Using tunnels for treating subsurface hydrocarbon containing formations
US8636323B2 (en) 2008-04-18 2014-01-28 Shell Oil Company Mines and tunnels for use in treating subsurface hydrocarbon containing formations
US8353347B2 (en) 2008-10-13 2013-01-15 Shell Oil Company Deployment of insulated conductors for treating subsurface formations
US9129728B2 (en) 2008-10-13 2015-09-08 Shell Oil Company Systems and methods of forming subsurface wellbores
US20100147521A1 (en) * 2008-10-13 2010-06-17 Xueying Xie Perforated electrical conductors for treating subsurface formations
US8267170B2 (en) 2008-10-13 2012-09-18 Shell Oil Company Offset barrier wells in subsurface formations
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
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
US20100206570A1 (en) * 2008-10-13 2010-08-19 Ernesto Rafael Fonseca Ocampos Circulated heated transfer fluid systems 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
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
US9022118B2 (en) 2008-10-13 2015-05-05 Shell Oil Company Double insulated heaters 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
US8327932B2 (en) 2009-04-10 2012-12-11 Shell Oil Company Recovering energy from a subsurface formation
US20100258290A1 (en) * 2009-04-10 2010-10-14 Ronald Marshall Bass Non-conducting heater casings
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
US8448707B2 (en) 2009-04-10 2013-05-28 Shell Oil Company Non-conducting heater casings
US20110042084A1 (en) * 2009-04-10 2011-02-24 Robert Bos Irregular pattern treatment of a subsurface formation
US20100258309A1 (en) * 2009-04-10 2010-10-14 Oluropo Rufus Ayodele Heater assisted fluid treatment of a subsurface formation
US20100258291A1 (en) * 2009-04-10 2010-10-14 Everett De St Remey Edward Heated liners for treating subsurface hydrocarbon containing formations
US8851170B2 (en) 2009-04-10 2014-10-07 Shell Oil Company 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
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
US9022109B2 (en) 2010-04-09 2015-05-05 Shell Oil Company Leak detection in circulated fluid systems for heating subsurface formations
US9033042B2 (en) 2010-04-09 2015-05-19 Shell Oil Company Forming bitumen barriers in subsurface hydrocarbon formations
US8739874B2 (en) 2010-04-09 2014-06-03 Shell Oil Company Methods for heating with slots in hydrocarbon formations
US9399905B2 (en) 2010-04-09 2016-07-26 Shell Oil Company Leak detection in circulated fluid systems for heating subsurface formations
US9127538B2 (en) 2010-04-09 2015-09-08 Shell Oil Company Methodologies for treatment of hydrocarbon formations using staged pyrolyzation
US8701768B2 (en) 2010-04-09 2014-04-22 Shell Oil Company Methods for treating hydrocarbon formations
US8701769B2 (en) 2010-04-09 2014-04-22 Shell Oil Company Methods for treating hydrocarbon formations based on geology
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
US9353611B2 (en) 2012-11-02 2016-05-31 Trimeteor Oil & Gas Corp. Method and apparatus for the downhole injection of superheated steam

Similar Documents

Publication Publication Date Title
US1457479A (en) Method of increasing the yield of oil wells
US4498537A (en) Producing well stimulation method - combination of thermal and solvent
US1510655A (en) Process of subterranean distillation of volatile mineral substances
US2390770A (en) Method of producing petroleum
US4597441A (en) Recovery of oil by in situ hydrogenation
US4429745A (en) Oil recovery method
US3139928A (en) Thermal process for in situ decomposition of oil shale
US3993132A (en) Thermal recovery of hydrocarbons from tar sands
JP4050620B2 (en) Method for recovering hydrocarbons from hydrocarbon reservoirs and apparatus for carrying out the same
CA1048431A (en) Thermal recovery of hydrocarbon from tar sands
US4037655A (en) Method for secondary recovery of oil
US3379248A (en) In situ combustion process utilizing waste heat
US2506853A (en) Oil well furnace
US2584605A (en) Thermal drive method for recovery of oil
US3400762A (en) In situ thermal recovery of oil from an oil shale
US3003555A (en) Oil production from unconsolidated formations
US1473348A (en) Method of operating oil wells
US2421528A (en) Underground oil recovery
US5255740A (en) Secondary recovery process
US2188737A (en) Apparatus for recovering oil from subterranean oil pockets
US4429744A (en) Oil recovery method
US4427066A (en) Oil recovery method
US3024841A (en) Method of oil recovery by in situ combustion
US3411578A (en) Method for producing oil by in situ combustion with optimum steam injection
US4566537A (en) Heavy oil recovery