US3485300A - Method and apparatus for defoaming crude oil down hole - Google Patents

Method and apparatus for defoaming crude oil down hole Download PDF

Info

Publication number
US3485300A
US3485300A US692223A US3485300DA US3485300A US 3485300 A US3485300 A US 3485300A US 692223 A US692223 A US 692223A US 3485300D A US3485300D A US 3485300DA US 3485300 A US3485300 A US 3485300A
Authority
US
United States
Prior art keywords
oil
well
packer
foamy
down hole
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
US692223A
Inventor
Charles J Engle
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
Application granted granted Critical
Publication of US3485300A publication Critical patent/US3485300A/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
    • E21B43/34Arrangements for separating materials produced by the well
    • E21B43/38Arrangements for separating materials produced by the well in the well

Definitions

  • This invention relates to defoaming crude oil down hole. In one of its aspects it relates to improving pumpability of oil from a well bottom when the oil accumulating therein is foaming. In another of its aspects, the invention relates to the provision of apparatus for better pumping foamy oil by defoaming the same prior to pumping same from the well.
  • the invention provides a method for defoaming oil down hole in an oil well which comprises causing said oil to travel through an upwardly extended heating unit placed down hole in the well just above the oil collecting therein, the unit being adapted to receive the oil through a packer which otherwise bars flow of oil upwardly into the casing. Oil is then caused to overflow through the heating unit and to collect around the same and around a production tubing also extending down into the well. Heating of the oil causes dissolved gases such as carbon dioxide and others to emanate from the top of the heating unit and to pass upwardly through the casing while oil flows downwardly around the heating unit and collects in the bottom of the well above the packer.
  • the production tubing is rendered operative to remove defoamed oil more efficiently from the well.
  • the invention provides apparatus for defoaming and producing a defoamed oil v wardly extending heating unit in open communication 4 through said packer with the oil below the packer, a production tubing extending down the casing to a point just above said packer and pumping means for pumping oil up through said tubing.
  • an upwardly extending tubular heater which extends sufficiently above the level of oil which can accumulate above the packer that oil from which substantially all gases have been as it were boiled off in the heating unit will now pass downwardly outside the heating unit as a film for removal of any residual gases still dissolved in the oil and to further defoam the oil.
  • a method for defoaming and producing foamy crude oil which comprises providing down hole in a well producing such oil heating Zone in which the oil can be heated, passing the foamy oil through said zone, therein heating said oil to a temperature and for a time suflicient to substantially release gases from said oil, then pumping said oil from said well.
  • a packer positioned just above the level at which foamy oil enters into the casing.
  • a tubing which can be heated. This causes oil as it enters from the formation into the well casing to pass upwardly through the heated tubing.
  • the oil overflows the top end of the heated tubing and falls back in the bottom of the well casing just above the packer and is therefore collected and ready for pumping.
  • the usual production tubing equipped with the usual pump extends downwardly into the now defoamed oil and can be used to pump the defoamed oil to the surface.
  • 1 is a well casing
  • 2 is a packer across the bottom of the well casing but above perforations 3 through which foamy oil enters from formation 4 into the very bottom end of the well casing.
  • 5 is a heated tube sealingly engaging the aperture 6 in packer 2.
  • 7 is a production tubing and 8 is a pump operated by a sucker rod 9. 10 are the pump valves of the usual pump.
  • the tubular heater consists of a 10 foot length of 2-inch tubings spirally wound with a Chromalox tubular element obtainable from Edwin L. Wiegand Company of Pittsburgh.
  • heater coils are shown jacketed by a metal such as copper to insure even heating.
  • the copper jacket can be in the form of a fluted or finned tube for added surface.
  • Heater energy is supplied from the surface through Reda pump type electrical cables, not shown for sake of siniplicity, and the heater is also equipped with a thermocouple for surface monitoring of heater temperature, also not shown for sake of simplicity.
  • the foot length and the 2-inch tubing need not b used. If desired, a longer tube, say up to and exceeding feet and a 3-inch tubing can be used for rapid production, if desired.
  • heater dimensions and power requirements will depend upon the rate of oil production and oil temperature required for eflicient gas stripping.
  • the invention as noted is particularly applicable to p'roducing oil from in situ combustion project. As the in situ combustion process progresses and the oil is heated in the reservoir, it will be possible to reduce the heat requirements in the heating zone or stripper. In such event the extended tube through which the oil flows upwardly and down around the outside of which the oil flows downwardly as a film will provide a surface from which any gases in the oil can disengage.
  • a method for producing a foamy oil from a well which comprises causing a foamy oil which is in said well to pass from within said well directly through a heating zone provided down hole in said well, in said heating zone heating said oil in said well to a temperature and for a time sufficient to substantially release gases from said oil and then pumping said oil from said well.
  • a method according to claim 2 wherein there is provided a zone in the bottom of the well which impedes flow of oil upwardly in the well, there is provided a concentric heating zone extending a substantial distance upwardly through said well and communicating through said first mentioned zone upwardly through said heating zone and into the portion of the well above said first mentioned zone and pumped therefrom to the surface of the ground.
  • a method according to claim 1 for producing a foamy oil from a well which comprises accumulating said foamy oil in said well, passing said foamy oil upwardly through a heating zone located in said well in open communication with said foamy oil, discharging heated foamy oil from said heating zone into a zone in said well above and maintained separate from said foamy oil in said zone disengaging gas from said heated foamy oil, passing said gas upward and ultimately from said well, accumulating in said zone heated oil from which gas has now been disengaged and pumping the thus treated and accumulated oil from said well.
  • An apparatus comprising in combination a well casing extending into a well in the ground, a packer across the bottom of said well casing at a point above which liquid in the ground enters into said casing thus impeding flow of liquid accumulating in said casing upwardly through said casing, and means defining a heating zone in said casing just above said packing in direct open communication through said packing with liquid therebelow, means above said packer in said well for pumping liquid therefrom and from above said packer.
  • heating zone means is constituted at least in part by an extended tubing or pipe of a length sufiicient to heat foamy liquid passing therethrough to a temperature and for a time sufiicient to cause gases therein to become disengaged, said pipe extending from the packer to a level above the means for pumping to provide an upflow for heating Oll and an overflow downward for heated oil, thereby permitting gases disengaged from the oil during its heating to become separated from said oil and to pass upwardly in the well.
  • heating tube is provided with fins on at least one surface thereof.

Description

Dec. 23, 1969 c. J. ENGLE 3,485,300
METHOD AND APPARATUS FOR DEFOAMING CRUDE OIL DOWN HOLE Filed Dec. 20, 1967 i [GAS s GAS FREE OIL INVENTOR.
C. J. ENGLE ATTORNEYS United States Patent 0 3,485,300 METHOD AND APPARATUS FOR DEFOAMING CRUDE OIL DOWN HOLE Charles J. Engle, Bartlesville, Okla., assignor to Phillips Petroleum Company, a corporation of Delaware Filed Dec. 20, 1967, Ser. No. 692,223 Int. Cl. E211) 39/00; E211 43/24 US. Cl. 166-265 7 Claims ABSTRACT OF THE DISCLOSURE thereof. This further releases any residual gas. The oil then accumulates above the packer. The production tubing extends into the collected oil and the oil is now dumped efliciently up through said tubing.
This invention relates to defoaming crude oil down hole. In one of its aspects it relates to improving pumpability of oil from a well bottom when the oil accumulating therein is foaming. In another of its aspects, the invention relates to the provision of apparatus for better pumping foamy oil by defoaming the same prior to pumping same from the well.
In one of its concepts the invention provides a method for defoaming oil down hole in an oil well which comprises causing said oil to travel through an upwardly extended heating unit placed down hole in the well just above the oil collecting therein, the unit being adapted to receive the oil through a packer which otherwise bars flow of oil upwardly into the casing. Oil is then caused to overflow through the heating unit and to collect around the same and around a production tubing also extending down into the well. Heating of the oil causes dissolved gases such as carbon dioxide and others to emanate from the top of the heating unit and to pass upwardly through the casing while oil flows downwardly around the heating unit and collects in the bottom of the well above the packer. The production tubing is rendered operative to remove defoamed oil more efficiently from the well. In another of its concepts the invention provides apparatus for defoaming and producing a defoamed oil v wardly extending heating unit in open communication 4 through said packer with the oil below the packer, a production tubing extending down the casing to a point just above said packer and pumping means for pumping oil up through said tubing. In a further concept of the invention there is provided an upwardly extending tubular heater which extends sufficiently above the level of oil which can accumulate above the packer that oil from which substantially all gases have been as it were boiled off in the heating unit will now pass downwardly outside the heating unit as a film for removal of any residual gases still dissolved in the oil and to further defoam the oil.
It has been noted in the field that crude oil produced into production well bores sometimes is quite foamy and cannot be pumped efficiently with the conventional bottom hole pumps. The foaming occurs usually as a result of the release of dissolved gases e.g. CO and others.
3,485,300 Patented Dec. 23, 1969 These gases are ordinarily present especially when in situ combustion has been practiced and the gases are products of combustion. As the pressure on the oil drops from reservoir to bottom hole pressure these gases have a tendency to foam up the oil. In the case of low gravity this is oils .such as Morichal oils as encountered in Venezuela. The foaming is quite extensive and the foam is quite stable.
It is an object of this invention to provide a method for producing foamy oil in a more eflicient manner. It is another object of this invention to provide a method for defoaming oil down hole in a well in which it is being produced. It is a further object of the invention to provide an apparatus for defoaming oil down hole of a well in which it is being produced.
Other aspects, concepts and objects of this invention are apparent from a study of this disclosure, the drawing and the appended claims.
According to the invention, there is provided a method for defoaming and producing foamy crude oil which comprises providing down hole in a well producing such oil heating Zone in which the oil can be heated, passing the foamy oil through said zone, therein heating said oil to a temperature and for a time suflicient to substantially release gases from said oil, then pumping said oil from said well.
In one embodiment of the invention there is provided down hole in the well casing a packer positioned just above the level at which foamy oil enters into the casing. Surmounting an aperture in said packer so oil can flow thereinto is placed a tubing which can be heated. This causes oil as it enters from the formation into the well casing to pass upwardly through the heated tubing. At the top of the heated tubing, owing to increased pressure provided by expansion of the gases the gases are substantially released from the oil. The oil overflows the top end of the heated tubing and falls back in the bottom of the well casing just above the packer and is therefore collected and ready for pumping. The usual production tubing equipped with the usual pump extends downwardly into the now defoamed oil and can be used to pump the defoamed oil to the surface.
Referring now to the drawing, 1 is a well casing, 2 is a packer across the bottom of the well casing but above perforations 3 through which foamy oil enters from formation 4 into the very bottom end of the well casing. 5 is a heated tube sealingly engaging the aperture 6 in packer 2. 7 is a production tubing and 8 is a pump operated by a sucker rod 9. 10 are the pump valves of the usual pump.
In operation the foamy oil entering through perforations 3 passes upwardly through aperture 6 and passes still upwardly into tube 5. The oil ultimately fills tube 5 and overflows at the top as indicated by the arrows and is collected above the packer as shown by the dotted lines. On its way upwardly through the tube the oil temperature is considerably raised say to about 300 degrees Fahrenheit for a time of about 60 seconds. This results in considerable expansion of the gas in the oil which then escapes at the top end of the tubing and passes upwardly through the casing. The now heated oil flows downwardly outside tubing 5. While flowing downwardly this oil can additionally release gas therefrom if any remains therein sufficient to interfere with proper pumping of the same. Collected oil is pumped through valves 10 by means of pump 8 and sucker rod 9 outwardly through production tubing 7.
In the embodiment just described the tubular heater consists of a 10 foot length of 2-inch tubings spirally wound with a Chromalox tubular element obtainable from Edwin L. Wiegand Company of Pittsburgh. The
heater coils are shown jacketed by a metal such as copper to insure even heating. The copper jacket can be in the form of a fluted or finned tube for added surface. Heater energy is supplied from the surface through Reda pump type electrical cables, not shown for sake of siniplicity, and the heater is also equipped with a thermocouple for surface monitoring of heater temperature, also not shown for sake of simplicity.
The foot length and the 2-inch tubing need not b used. If desired, a longer tube, say up to and exceeding feet and a 3-inch tubing can be used for rapid production, if desired.
Thus the heater dimensions and power requirements will depend upon the rate of oil production and oil temperature required for eflicient gas stripping.
Although an electrical heater has been described a "ga fire heater can be used to carry out this invention. At present the electrical means appears to be simpler. Accordingly, the invention has been described with such a means.
The invention as noted is particularly applicable to p'roducing oil from in situ combustion project. As the in situ combustion process progresses and the oil is heated in the reservoir, it will be possible to reduce the heat requirements in the heating zone or stripper. In such event the extended tube through which the oil flows upwardly and down around the outside of which the oil flows downwardly as a film will provide a surface from which any gases in the oil can disengage.
Thus, according to the invention natural and in situ combustion gases flow to the surface in the annulus between the casing and the producing tubing and the oil flows out the top of the tubular heater or its equivalent and into the space above the packer so that a conventional sucker rod pump or the like can lift the oil to the surface. The invention is a specific helpful adjunct to the pumping operation in that the pump is now supplied with ample oil which more readily flows into the areas around the pump since gases, particularly the excess gases have been removed.
Reasonable variation and modification are possible within the scope of the foregoing disclosure, the drawing and the appended claims to the invention the essence of which is that there has been provided a method and a concomitant apparatus for down hole heating of a foamy oil and causing said oil to release its gas so that its gas will not impede the pumping operation, the method providing down hole in the well producing such foamy oil the heating zone in which the oil can be heated passing the foamy oil through said zone and therein heating said oil to a temperature and for a time sufficient to substantially release gases from said oil and then pumping said oil from said well; the apparatus comprising in combination down hole in a well casing and packer a heated tube or equivalent surmounting said packer a distance sufficient to suitably heat the oil to cause gases therein to develop enough pressure to disengage themselves from the oil, which can be quite viscous, the oil then flowing downwardly around said tubing or equivalent, there being also above said packer space for accumulation of oil and there being in said casing a production tubing enclosing a pump means wherewith the pump accumulated oil from above the packer to the ground surface.
I claim:
1. A method for producing a foamy oil from a well which comprises causing a foamy oil which is in said well to pass from within said well directly through a heating zone provided down hole in said well, in said heating zone heating said oil in said well to a temperature and for a time sufficient to substantially release gases from said oil and then pumping said oil from said well.
2. A method according to claim 1 wherein the oil is passed through an upwardly extending heated zone and down around said zone and collected in the well from which it is then pumped to the surface.
3. A method according to claim 2 wherein there is provided a zone in the bottom of the well which impedes flow of oil upwardly in the well, there is provided a concentric heating zone extending a substantial distance upwardly through said well and communicating through said first mentioned zone upwardly through said heating zone and into the portion of the well above said first mentioned zone and pumped therefrom to the surface of the ground.
4. A method according to claim 1 for producing a foamy oil from a well which comprises accumulating said foamy oil in said well, passing said foamy oil upwardly through a heating zone located in said well in open communication with said foamy oil, discharging heated foamy oil from said heating zone into a zone in said well above and maintained separate from said foamy oil in said zone disengaging gas from said heated foamy oil, passing said gas upward and ultimately from said well, accumulating in said zone heated oil from which gas has now been disengaged and pumping the thus treated and accumulated oil from said well.
- 5. An apparatus comprising in combination a well casing extending into a well in the ground, a packer across the bottom of said well casing at a point above which liquid in the ground enters into said casing thus impeding flow of liquid accumulating in said casing upwardly through said casing, and means defining a heating zone in said casing just above said packing in direct open communication through said packing with liquid therebelow, means above said packer in said well for pumping liquid therefrom and from above said packer.
6. An apparatus according to claim 5 wherein the heating zone means is constituted at least in part by an extended tubing or pipe of a length sufiicient to heat foamy liquid passing therethrough to a temperature and for a time sufiicient to cause gases therein to become disengaged, said pipe extending from the packer to a level above the means for pumping to provide an upflow for heating Oll and an overflow downward for heated oil, thereby permitting gases disengaged from the oil during its heating to become separated from said oil and to pass upwardly in the well.
7. An apparatus according to claim 6 wherein the heating tube is provided with fins on at least one surface thereof.
References Cited UNITED STATES PATENTS 1,820,291 8/ 1931 Strandell 1666 X 2,134,610 10/1938 Hogg 166-60 2,3 62,680 11/1944 Troupe 16660 2,980,184 4/1961 Reed 16639 X 3,113,622 12/1963 Carpenter l66-39 STEPHEN I NOVOSAD, Primary Examiner US. Cl. X.R. 16660, 302, 314
US692223A 1967-12-20 1967-12-20 Method and apparatus for defoaming crude oil down hole Expired - Lifetime US3485300A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US69222367A 1967-12-20 1967-12-20

Publications (1)

Publication Number Publication Date
US3485300A true US3485300A (en) 1969-12-23

Family

ID=24779721

Family Applications (1)

Application Number Title Priority Date Filing Date
US692223A Expired - Lifetime US3485300A (en) 1967-12-20 1967-12-20 Method and apparatus for defoaming crude oil down hole

Country Status (1)

Country Link
US (1) US3485300A (en)

Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4762176A (en) * 1987-03-23 1988-08-09 Miller Orand C Air-water separator
WO1998037306A1 (en) * 1997-02-20 1998-08-27 Rangewest Technologies Ltd. Enhanced lift method and apparatus for the production of hydrocarbons
US6009940A (en) * 1998-03-20 2000-01-04 Atlantic Richfield Company Production in frigid environments
US6554066B2 (en) * 2000-01-27 2003-04-29 Petroleo Brasileiro S.A.-Petrobras Gas separator with automatic level control
US20050045332A1 (en) * 2003-08-26 2005-03-03 Howard William F. Wellbore pumping with improved temperature performance
WO2005106191A1 (en) * 2004-04-23 2005-11-10 Shell International Research Maatschappij B.V. Inhibiting reflux in a heated well of an in situ conversion system
US20070137857A1 (en) * 2005-04-22 2007-06-21 Vinegar Harold J Low temperature monitoring system for subsurface barriers
US20090071647A1 (en) * 2003-04-24 2009-03-19 Vinegar Harold J Thermal processes for subsurface formations
US7644765B2 (en) 2006-10-20 2010-01-12 Shell Oil Company Heating tar sands formations while controlling pressure
US7673786B2 (en) 2006-04-21 2010-03-09 Shell Oil Company Welding shield for coupling heaters
US20100126727A1 (en) * 2001-10-24 2010-05-27 Shell Oil Company In situ recovery from 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
US7798221B2 (en) 2000-04-24 2010-09-21 Shell Oil Company In situ recovery from a hydrocarbon containing formation
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
US7866386B2 (en) 2007-10-19 2011-01-11 Shell Oil Company In situ oxidation of subsurface formations
US8151880B2 (en) 2005-10-24 2012-04-10 Shell Oil Company Methods of making transportation fuel
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
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
US8327932B2 (en) 2009-04-10 2012-12-11 Shell Oil Company Recovering energy from a subsurface formation
US8608249B2 (en) 2001-04-24 2013-12-17 Shell Oil Company In situ thermal processing of an oil shale formation
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
WO2017214303A1 (en) * 2016-06-09 2017-12-14 Sylvester Glenn Clay Downhole heater
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
US1820291A (en) * 1930-03-17 1931-08-25 Strandell Arthur Oil extracting device
US2134610A (en) * 1937-04-26 1938-10-25 Coy C Hogg Oil-bearing sand heater
US2362680A (en) * 1941-05-17 1944-11-14 Donald F Troupe Electrothermic oil well processor
US2980184A (en) * 1958-09-22 1961-04-18 Shell Oil Co Method and apparatus for producing wells
US3113622A (en) * 1959-10-14 1963-12-10 Union Oil Co Method and apparatus for heating oil sands

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1820291A (en) * 1930-03-17 1931-08-25 Strandell Arthur Oil extracting device
US2134610A (en) * 1937-04-26 1938-10-25 Coy C Hogg Oil-bearing sand heater
US2362680A (en) * 1941-05-17 1944-11-14 Donald F Troupe Electrothermic oil well processor
US2980184A (en) * 1958-09-22 1961-04-18 Shell Oil Co Method and apparatus for producing wells
US3113622A (en) * 1959-10-14 1963-12-10 Union Oil Co Method and apparatus for heating oil sands

Cited By (120)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4762176A (en) * 1987-03-23 1988-08-09 Miller Orand C Air-water separator
WO1998037306A1 (en) * 1997-02-20 1998-08-27 Rangewest Technologies Ltd. Enhanced lift method and apparatus for the production of hydrocarbons
US6039121A (en) * 1997-02-20 2000-03-21 Rangewest Technologies Ltd. Enhanced lift method and apparatus for the production of hydrocarbons
US6009940A (en) * 1998-03-20 2000-01-04 Atlantic Richfield Company Production in frigid environments
US6554066B2 (en) * 2000-01-27 2003-04-29 Petroleo Brasileiro S.A.-Petrobras Gas separator with automatic level control
US8789586B2 (en) 2000-04-24 2014-07-29 Shell Oil Company 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
US8225866B2 (en) 2000-04-24 2012-07-24 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
US8608249B2 (en) 2001-04-24 2013-12-17 Shell Oil Company In situ thermal processing of an oil shale formation
US20100126727A1 (en) * 2001-10-24 2010-05-27 Shell Oil Company In situ recovery from a hydrocarbon containing formation
US8627887B2 (en) 2001-10-24 2014-01-14 Shell Oil Company In situ recovery from a hydrocarbon containing formation
US20090071647A1 (en) * 2003-04-24 2009-03-19 Vinegar Harold J Thermal processes for subsurface formations
US7942203B2 (en) 2003-04-24 2011-05-17 Shell Oil Company Thermal processes for subsurface formations
US8579031B2 (en) 2003-04-24 2013-11-12 Shell Oil Company Thermal processes for subsurface formations
US20050045332A1 (en) * 2003-08-26 2005-03-03 Howard William F. Wellbore pumping with improved temperature performance
US7314089B2 (en) * 2003-08-26 2008-01-01 Weatherford/Lamb, Inc. Method of wellbore pumping apparatus with improved temperature performance and method of use
US20060289536A1 (en) * 2004-04-23 2006-12-28 Vinegar Harold J Subsurface electrical heaters using nitride insulation
CN1946917B (en) * 2004-04-23 2012-05-30 国际壳牌研究有限公司 Method for processing underground rock stratum
WO2005106191A1 (en) * 2004-04-23 2005-11-10 Shell International Research Maatschappij B.V. Inhibiting reflux in a heated well of an in situ conversion system
US20070137857A1 (en) * 2005-04-22 2007-06-21 Vinegar Harold J Low temperature monitoring system for subsurface barriers
US7860377B2 (en) 2005-04-22 2010-12-28 Shell Oil Company Subsurface connection methods for subsurface heaters
US8233782B2 (en) 2005-04-22 2012-07-31 Shell Oil Company Grouped exposed metal heaters
US7942197B2 (en) 2005-04-22 2011-05-17 Shell Oil Company Methods and systems for producing fluid from an in situ conversion process
US7986869B2 (en) 2005-04-22 2011-07-26 Shell Oil Company Varying properties along lengths of temperature limited heaters
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
US8224165B2 (en) 2005-04-22 2012-07-17 Shell Oil Company Temperature limited heater utilizing non-ferromagnetic conductor
US8230927B2 (en) 2005-04-22 2012-07-31 Shell Oil Company Methods and systems for producing fluid from an in situ conversion process
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
US7831134B2 (en) 2005-04-22 2010-11-09 Shell Oil Company Grouped exposed metal heaters
US8070840B2 (en) 2005-04-22 2011-12-06 Shell Oil Company Treatment of gas from an in situ conversion process
US8606091B2 (en) 2005-10-24 2013-12-10 Shell Oil Company Subsurface heaters with low sulfidation rates
US8151880B2 (en) 2005-10-24 2012-04-10 Shell Oil Company Methods of making transportation fuel
US8857506B2 (en) 2006-04-21 2014-10-14 Shell Oil Company Alternate energy source usage methods for in situ heat treatment processes
US8083813B2 (en) 2006-04-21 2011-12-27 Shell Oil Company Methods of producing transportation fuel
US8192682B2 (en) 2006-04-21 2012-06-05 Shell Oil Company High strength alloys
US7683296B2 (en) 2006-04-21 2010-03-23 Shell Oil Company Adjusting alloy compositions for selected properties in temperature limited heaters
US7793722B2 (en) 2006-04-21 2010-09-14 Shell Oil Company Non-ferromagnetic overburden casing
US7866385B2 (en) 2006-04-21 2011-01-11 Shell Oil Company Power systems utilizing the heat of produced formation fluid
US7785427B2 (en) 2006-04-21 2010-08-31 Shell Oil Company High strength alloys
US7912358B2 (en) 2006-04-21 2011-03-22 Shell Oil Company Alternate energy source usage for in situ heat treatment processes
US7673786B2 (en) 2006-04-21 2010-03-09 Shell Oil Company Welding shield for coupling heaters
US8191630B2 (en) 2006-10-20 2012-06-05 Shell Oil Company Creating fluid injectivity in tar sands formations
US7730946B2 (en) 2006-10-20 2010-06-08 Shell Oil Company Treating tar sands formations with dolomite
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
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
US7703513B2 (en) 2006-10-20 2010-04-27 Shell Oil Company Wax barrier for use with in situ processes for treating formations
US7845411B2 (en) 2006-10-20 2010-12-07 Shell Oil Company In situ heat treatment process utilizing a closed loop heating system
US8555971B2 (en) 2006-10-20 2013-10-15 Shell Oil Company Treating tar sands formations with dolomite
US7717171B2 (en) 2006-10-20 2010-05-18 Shell Oil Company Moving hydrocarbons through portions of tar sands formations with a fluid
US7730947B2 (en) 2006-10-20 2010-06-08 Shell Oil Company Creating fluid injectivity in tar sands formations
US7841401B2 (en) 2006-10-20 2010-11-30 Shell Oil Company Gas injection to inhibit migration during an in situ heat treatment process
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
US8791396B2 (en) 2007-04-20 2014-07-29 Shell Oil Company Floating insulated conductors for heating subsurface formations
US7931086B2 (en) 2007-04-20 2011-04-26 Shell Oil Company Heating systems for heating subsurface formations
US8042610B2 (en) 2007-04-20 2011-10-25 Shell Oil Company Parallel heater system for subsurface formations
US7849922B2 (en) 2007-04-20 2010-12-14 Shell Oil Company In situ recovery from residually heated sections in a hydrocarbon containing formation
US7841425B2 (en) 2007-04-20 2010-11-30 Shell Oil Company Drilling subsurface wellbores with cutting structures
US7841408B2 (en) 2007-04-20 2010-11-30 Shell Oil Company In situ heat treatment from multiple layers of a tar sands formation
US7832484B2 (en) 2007-04-20 2010-11-16 Shell Oil Company Molten salt as a heat transfer fluid for heating a subsurface formation
US8459359B2 (en) 2007-04-20 2013-06-11 Shell Oil Company Treating nahcolite containing formations and saline zones
US8381815B2 (en) 2007-04-20 2013-02-26 Shell Oil Company Production from multiple zones of a tar sands 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
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
US8327681B2 (en) 2007-04-20 2012-12-11 Shell Oil Company Wellbore manufacturing processes for in situ heat treatment processes
US7950453B2 (en) 2007-04-20 2011-05-31 Shell Oil Company Downhole burner systems and methods for heating subsurface formations
US9181780B2 (en) 2007-04-20 2015-11-10 Shell Oil Company Controlling and assessing pressure conditions during treatment of tar sands formations
US8536497B2 (en) 2007-10-19 2013-09-17 Shell Oil Company 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
US8162059B2 (en) 2007-10-19 2012-04-24 Shell Oil Company Induction heaters used to heat subsurface formations
US7866386B2 (en) 2007-10-19 2011-01-11 Shell Oil Company In situ oxidation of 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
US7866388B2 (en) 2007-10-19 2011-01-11 Shell Oil Company High temperature methods for forming oxidizer fuel
US8113272B2 (en) 2007-10-19 2012-02-14 Shell Oil Company Three-phase heaters with common overburden sections for heating subsurface formations
US8240774B2 (en) 2007-10-19 2012-08-14 Shell Oil Company Solution mining and in situ treatment of nahcolite beds
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
US8011451B2 (en) 2007-10-19 2011-09-06 Shell Oil Company Ranging methods for developing wellbores in subsurface formations
US8636323B2 (en) 2008-04-18 2014-01-28 Shell Oil Company 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
US8562078B2 (en) 2008-04-18 2013-10-22 Shell Oil Company Hydrocarbon production from mines and tunnels used in treating subsurface hydrocarbon containing formations
US8172335B2 (en) 2008-04-18 2012-05-08 Shell Oil Company Electrical current flow between tunnels for use in heating subsurface hydrocarbon containing formations
US9528322B2 (en) 2008-04-18 2016-12-27 Shell Oil Company Dual motor systems and non-rotating sensors for use in developing wellbores in subsurface formations
US8162405B2 (en) 2008-04-18 2012-04-24 Shell Oil Company Using tunnels for 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
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
US8267170B2 (en) 2008-10-13 2012-09-18 Shell Oil Company Offset barrier wells in subsurface formations
US8261832B2 (en) 2008-10-13 2012-09-11 Shell Oil Company Heating subsurface formations with fluids
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
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
US9051829B2 (en) 2008-10-13 2015-06-09 Shell Oil Company Perforated electrical conductors for treating subsurface formations
US9022118B2 (en) 2008-10-13 2015-05-05 Shell Oil Company Double insulated heaters for treating subsurface formations
US8881806B2 (en) 2008-10-13 2014-11-11 Shell Oil Company Systems and methods for treating a subsurface formation with electrical conductors
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
US8327932B2 (en) 2009-04-10 2012-12-11 Shell Oil Company Recovering energy from a subsurface formation
US8448707B2 (en) 2009-04-10 2013-05-28 Shell Oil Company Non-conducting heater casings
US8851170B2 (en) 2009-04-10 2014-10-07 Shell Oil Company Heater assisted fluid treatment of a subsurface formation
US8434555B2 (en) 2009-04-10 2013-05-07 Shell Oil Company Irregular pattern treatment of a subsurface formation
US8701769B2 (en) 2010-04-09 2014-04-22 Shell Oil Company Methods for treating hydrocarbon formations based on geology
US9127538B2 (en) 2010-04-09 2015-09-08 Shell Oil Company Methodologies for treatment of hydrocarbon formations using staged pyrolyzation
US8739874B2 (en) 2010-04-09 2014-06-03 Shell Oil Company Methods for heating with slots in hydrocarbon 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
US8833453B2 (en) 2010-04-09 2014-09-16 Shell Oil Company Electrodes for electrical current flow heating of subsurface formations with tapered copper thickness
US8701768B2 (en) 2010-04-09 2014-04-22 Shell Oil Company Methods for treating hydrocarbon formations
US8631866B2 (en) 2010-04-09 2014-01-21 Shell Oil Company Leak detection in circulated fluid systems for heating subsurface formations
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
US9399905B2 (en) 2010-04-09 2016-07-26 Shell Oil Company Leak detection in circulated fluid systems for heating subsurface 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
WO2017214303A1 (en) * 2016-06-09 2017-12-14 Sylvester Glenn Clay Downhole heater

Similar Documents

Publication Publication Date Title
US3485300A (en) Method and apparatus for defoaming crude oil down hole
US2881838A (en) Heavy oil recovery
US2244255A (en) Well clearing system
US3908763A (en) Method for pumpin paraffine base crude oil
Butler et al. Theoretical studies on the gravity drainage of heavy oil during in‐situ steam heating
US2244256A (en) Apparatus for clearing wells
US3119674A (en) Method and apparatus for producing oil and gas wells
US2980184A (en) Method and apparatus for producing wells
US3066732A (en) Production of crude oil
US2104327A (en) Method of recovering earth components from wells
US3500917A (en) Method of recovering crude oil from a subsurface formation
EP3102780B1 (en) A method for preventing wax deposition in oil wells with packers
US4066127A (en) Processes for producing bitumen from tar sands and methods for forming a gravel pack in tar sands
US3040809A (en) Process for recovering viscous crude oil from unconsolidated formations
US3062289A (en) Oil well heater
US3342259A (en) Method for repressurizing an oil reservoir
US5040605A (en) Oil recovery method and apparatus
US1511067A (en) Process of and apparatus for extracting oil from oil-bearing strata
US3014531A (en) Method of cleaning oil wells
US3196947A (en) Method for facilitating the production of viscous petroleum through a well
US2229541A (en) Apparatus for pumping oil wells
US3565174A (en) Method of in situ combustion with intermittent injection of volatile liquid
US5913363A (en) Method for downhole separation of natural gas from brine with injection of spent brine into a disposal formation
US1886886A (en) Method of and apparatus for the recovery of matter from wells
US3208516A (en) Control method in underground combustion drives