US2668592A - Gas burner and method for burning gas in oil and gas wells - Google Patents
Gas burner and method for burning gas in oil and gas wells Download PDFInfo
- Publication number
- US2668592A US2668592A US97142A US9714249A US2668592A US 2668592 A US2668592 A US 2668592A US 97142 A US97142 A US 97142A US 9714249 A US9714249 A US 9714249A US 2668592 A US2668592 A US 2668592A
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- Prior art keywords
- gas
- air
- burner
- mixing
- combustion
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- 238000000034 method Methods 0.000 title description 8
- 239000007789 gas Substances 0.000 description 40
- 238000002485 combustion reaction Methods 0.000 description 37
- 239000002737 fuel gas Substances 0.000 description 16
- 239000000203 mixture Substances 0.000 description 14
- 239000000446 fuel Substances 0.000 description 10
- 239000010935 stainless steel Substances 0.000 description 5
- 229910001220 stainless steel Inorganic materials 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 230000008878 coupling Effects 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- 238000005755 formation reaction Methods 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000003129 oil well Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000010892 electric spark Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 210000002445 nipple Anatomy 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B36/00—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
- E21B36/02—Heating, cooling or insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using burners
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/20—Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone
- F23D14/22—Non-premix gas burners, i.e. in which gaseous fuel is mixed with combustion air on arrival at the combustion zone with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other
Definitions
- Fig. 1 is a cross-section of a combustible gas burner embodying the principles of our discovery.
- Fig. 2 is an enlarged view of the mixing plate of said burner taken along the line 2-2.
- Fig. 3 is a fragmentary view of Fig. 1 illustrating a method for obtaining limited pre-mixture of air and gas between the mixing plate and the point of ignition.
- ⁇ the ⁇ burner is advantageously of stainless steel, or other heat resistant alloy calculated to withstand extreme conditions of temperature and pressure.
- the burner is composed of two sections of 2" standard stainless steel pipe, section I0 constituting the section II containing the 'combustion elements.
- Combustion chamber I0 is of a length designed to accommodate the turbulent flame and in the embodiment illustrated is II is of similar length and, as shown, is joined to chamber I0 by stainless steel coupling I2.
- mixing plate I3 which, in the embodiment shown, is of stainless steel, welded in place.
- Mixing plate I3 contains three s-inch diameter ducts, air ducts I4 and I5 and gas duct yI5 (refer to Fig. 2), each drilled at a 30 by 30 compound angle with respect to the center line of the mixing plate.
- the ducts may be geometrically positioned in plate I3, but air ducts I4 and I5 are shown as advantageously spaced closely adjacent to gas duct I6 so ⁇ as 'to sandwich it in order to improve mixing.
- the fuel-air mixture is ignited by spark plug I'I centrally located in mixing plate I3.
- Plug I'I is mounted in nipple I8 which is Welded to hexagonal I9 of plug i1, and is joined by coupling 24 to inner pipe 20 which extends the length of pipe section II and provides a protective sheath for high tension cable 2l leading to plug I1.
- Fuel gas is admitted to the burner through pipe and vat a point -well above the combustion zone and is diverted to separate gas line 22, advantageously constructed of steel tubing sections joined by coupling A2?, which leads directly to gas duct I6 of mixing plate I3.
- a spiral vane 25 leading from the'I discharge of the gas and air ports so as to cause all the gas and air to pass under the vane before spilling into the combustion zone.
- the spiral vane is a single turn helix 25 as shown, which may be constructed of stainless steel, and which is welded to the outside of internal cylinder 26. Cylinder 26 is welded around spark plug points 21 and seals spiral vane 25 o-n the inside.
- ⁇ Spiral vane 25 is advantageously Welded to mixing plate I3 at a point just behind the first air duct, thus causing all the gas and air to pass underneath vane 25 before entering the combustion Zone.
- small scoop 28 is formed out of the wall of cylinder 2S advantageously at a point where the gas and air perfect combustion, 1s supplied through the extensions of outer pipe section II at pressuresquantities necessary for the release.
- the fuel and air are mixed at the mixing plate by discharge from angularly directed ducts I4, I5, IIB.
- the mixture is ignited at a pressure of about 40 to 50 p. s. i. g. by electric spark from spark plug I1 which is regulated by gas desired rate of heat controlled from vthe surface through cable 2
- the flame temperature is controlled by admitting secondary air through the tubing or outer case. In this manner, high rates of heat release are achieved under the subterranean combustion conditions while soot pro- ⁇ oil structure duction that might clog the porous is obviated.
- a burner of the type shown in Fig. l but with the ducts positioned 108 from each other was placed in a pressure tight 4 casing.
- propane gas and air were fed to the burner in theoretically correct proportion for perfect combustion, plus enough air feed to the casing to limit the resulting temperature to 1500 F.
- the burner ignited at 40 p. s. i. g.
- the pressure could be built up to p. s. i. g. while maintaining combustion.
- rIhe pressure was maintained on the casing by using a valve to pinch down on the ue gas bled out of the casing. Once the higher pressure, the pressure on the casing could be reduced to a value slightly above atmospheric and the combustion still maintained.
- This test was conducted at a gas feed rate sufficient to give about 500,000 B. t. u. per hour dissipation.
- a burner For operation with natural gas., which is chiefly methane, we have found that a burner incur porating a limited pre-mixture system f 'the type shown in Figs. 2 and 3 shows greatly improved ignition behavior.
- Pre-mixing of gas and air at the spark plug igniter is increased by reducing the spacing between the gas and air ,ducts so as to sandwich the gas duct between the two air ducts and by providing a spiral mixing vane and internal cylinder which together form a mixing passageway from the discharge 4ports of -the lgas and air ducts and opening into -the combustion chamber.
- the intern-al cylinder is vented or provided 'with a scoop to supply mixture to the igniter at the face of the mixing plate.
- our invention in its basic forms which include -a burner characterized by an elongated combustion chamber with a mixing plate at -its head containing separate angularly directed air and -fuel ducts and separate passages for fuel and air to these ports, including a spiral mixing vane with internal cylinder and sidesscoop for eiecting limited pre-mixing prior to the point of ignition; a method of burning fuel gas .under conditions ofl high pressure to obtain high rates of heat release characterized by introducing fuel gas and air separately and angularly to the head of an elongated combustion zone so as to impart a turbulent and whirling tangential motion to the flame resulting from the mixture; and an improvement in thermal methods for recovering oil and gas from oil-bearing formations characterized by burning fuel gas at formation level in an input well in a system wherein fuel gas and air under pressure in approximately theoretical proportion for perfect combustion are separately and angularly introduced to an elongated combustion zone tted within the oil well casing so as to impart a turbulent whi
- a gas burner which comprises first means having an elongated, substantially cylindrical wall forming a combustion chamber; second means connected to the head of the combustion chamber for directing streams of fuel gas and air into the combustion chamber in a manner to accomplish mixing therein; third means for separately delivering fuel gas and air to said second means; said second means including means for separately introducing each of said separatestreams of fuel gas and air into the combustion zone at a location spaced from the axis of the combustion chamber and adjacent said cylindrical wall and in a downstream direction having a directional component outward from said axis and a directional component tangential to a circle normal to said axis having its center at said axis and passing through said location, the last named tangential directional component of each of said streams being in the same direction circumferentially of said second means thereby accomthe axis of said chamber and .eeen .duet its passage through ,said plate .in devvnstreemdrees tion having a direetiona1o
- a gas burner which comprises an elongated combustion chamber having a longitudinal axis and radial planes along said axis, a mixing plate at the head of said chamber, a fuel gas duct in said plate, a plurality of angularly directed air ducts in said plate sandwiching said gas duct, said ducts being similarly positioned at substantially the same distance from the axis of said chamber and each duct in its passage through said plate in downstream direction having a directional component outward from said axis and a directional component normal to its respective radial plane which passes through said laxis and the upstream entrance to said duct, the last named directional component of each of the ducts being in the same direction circumferentially of said plate thereby accomplishing tangential swirling and mixing of the fuel gas yand air adjacent the wall of the combustion chamber, a gas line feeding said gas duct, a tubular air passage charging said air ducts and containing said gas line, means for supplying fuel gas and air to said gas line and air passage respectively, and means
- the improvement which comprises separately passing fuel gas and air streams to a mixing point at the head of a substantially cylindrical combustion zone, separately introducing each of said streams into the combustion zone at a location spaced from the longitudinal axis of the combustion zone and in a downstream direction having a directional component outward from said axis and a directional component tangential to a circle having its center at said axis and passing through said location, the last named tangential directional component of each of said streams being Vin the same direction circumferentially of saidV zone, directing the flow of said streams in a manner to produce peripheral ow in said combustion zone to accomplish tangential swirling and mix-l ing of the fuel gas and air atthe periphery of said combustion zone, and-igniting the resultant fuel gas-air mixture.
- the improvement which comprises separately passing fuel gas and air streams to a mixing point at the head of a substantially cylindrical combustion zone in said well, separately introducing each of said streams into the combustion zone at a location spaced from the longitudinal axis of the combustion zone and in a downstreamV direction having a directional component outward from said axis and a directional component tangential to a circle having its center at said axis and passing through said location, the last named tangential directional component ofv each of said streams being ⁇ in the same direction circumferentially of said zone, directing the flow of said streams in a manner to produce peripheral iiow in said combustion zone to accomplish tangential swirling and mixing of the fuel gas and airat the periphery of said combustion zone, igniting the resultant fuel gas-air mixture, and controlling the temperature of the flame by introducing secondary air into said well and around said combustion zone.
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- Life Sciences & Earth Sciences (AREA)
- Mining & Mineral Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Description
Feb. 9, 1954 J. J. PlRos ET AL GAS BURNER AND METHOD FOR BURNING GAS IN OIL AND GAS WELLS Filed June 4, 1949 el! @ma TToRNEYs Patented Feb. 9, 1954 GAS BURNER AND METHOD FDR BURNING GAS IN QIL AND GAS .WELLS long .period of time, which may amount to many months, and Which is situated at the end of a tubing string that may be many hundreds or thousands of feet in length, must be reliable. And quite obviously, the combustion space for its operation is very limited and the pressures relatively high'. In addition, serious problems obtain in controlling the temperature below that which.
of drilling expense, rarely exceeds a diameter suicient to accommodate '7" O. D. pipe. We have found, however, that our burning system, constructed to enter a 4 O. D. pipe, ignites with a gas and air feed corresponding to a heat release of 600,000 B. t. u per hour under bottom-hole operating conditions.
A useful burner exemplifying our invention is illustrated somewhat diagrammatically in the accompanying drawing in which:
Fig. 1 is a cross-section of a combustible gas burner embodying the principles of our discovery.
Fig. 2 is an enlarged view of the mixing plate of said burner taken along the line 2-2.
Fig. 3 is a fragmentary view of Fig. 1 illustrating a method for obtaining limited pre-mixture of air and gas between the mixing plate and the point of ignition.
The construction of `the `burner is advantageously of stainless steel, or other heat resistant alloy calculated to withstand extreme conditions of temperature and pressure. As represented in Fig. 1 the burner is composed of two sections of 2" standard stainless steel pipe, section I0 constituting the section II containing the 'combustion elements. Combustion chamber I0 is of a length designed to accommodate the turbulent flame and in the embodiment illustrated is II is of similar length and, as shown, is joined to chamber I0 by stainless steel coupling I2.
Situated at the head of combustion chamber I0 isf a mixing plate I3 which, in the embodiment shown, is of stainless steel, welded in place.
Mixing plate I3 contains three s-inch diameter ducts, air ducts I4 and I5 and gas duct yI5 (refer to Fig. 2), each drilled at a 30 by 30 compound angle with respect to the center line of the mixing plate. The ducts may be geometrically positioned in plate I3, but air ducts I4 and I5 are shown as advantageously spaced closely adjacent to gas duct I6 so `as 'to sandwich it in order to improve mixing. The fuel-air mixture is ignited by spark plug I'I centrally located in mixing plate I3. Plug I'I is mounted in nipple I8 which is Welded to hexagonal I9 of plug i1, and is joined by coupling 24 to inner pipe 20 which extends the length of pipe section II and provides a protective sheath for high tension cable 2l leading to plug I1.
Fuel gas is admitted to the burner through pipe and vat a point -well above the combustion zone and is diverted to separate gas line 22, advantageously constructed of steel tubing sections joined by coupling A2?, which leads directly to gas duct I6 of mixing plate I3.
Air enters the burner Athrough pipe section II in 75 a high velocity stream surrounding and tending elongated combustion chamber and' 24 inches. Pipe section li by 55s-inch stainlessV to cool inner pipe 20 and gas line 22, and passesl through air ducts I4 and I5 which impart a whirling tangential motion to the flame by reason of their compound angular construction.
In the modification of Fig. 3, limited pre-mixture of gas and lair is achieved by providing a spiral vane 25 leading from the'I discharge of the gas and air ports so as to cause all the gas and air to pass under the vane before spilling into the combustion zone. The spiral vane is a single turn helix 25 as shown, which may be constructed of stainless steel, and which is welded to the outside of internal cylinder 26. Cylinder 26 is welded around spark plug points 21 and seals spiral vane 25 o-n the inside. `Spiral vane 25 is advantageously Welded to mixing plate I3 at a point just behind the first air duct, thus causing all the gas and air to pass underneath vane 25 before entering the combustion Zone. In order to supply a small portion of the pre-mixed gas and air to the spark plug igniter, small scoop 28 is formed out of the wall of cylinder 2S advantageously at a point where the gas and air perfect combustion, 1s supplied through the extensions of outer pipe section II at pressuresquantities necessary for the release. The fuel and air are mixed at the mixing plate by discharge from angularly directed ducts I4, I5, IIB. The mixture is ignited at a pressure of about 40 to 50 p. s. i. g. by electric spark from spark plug I1 which is regulated by gas desired rate of heat controlled from vthe surface through cable 2|,l
properly extended. The flame temperature is controlled by admitting secondary air through the tubing or outer case. In this manner, high rates of heat release are achieved under the subterranean combustion conditions while soot pro-` oil structure duction that might clog the porous is obviated.
For example, a burner of the type shown in Fig. l but with the ducts positioned 108 from each other was placed in a pressure tight 4 casing. When propane gas and air were fed to the burner in theoretically correct proportion for perfect combustion, plus enough air feed to the casing to limit the resulting temperature to 1500 F., the burner ignited at 40 p. s. i. g. We found that the pressure could be built up to p. s. i. g. while maintaining combustion. rIhe pressure was maintained on the casing by using a valve to pinch down on the ue gas bled out of the casing. Once the higher pressure, the pressure on the casing could be reduced to a value slightly above atmospheric and the combustion still maintained. This test was conducted at a gas feed rate sufficient to give about 500,000 B. t. u. per hour dissipation.
We found however that it was not possible to ignite such Accordingly, for operation at atmospheric pressure it is desirable' to provide a separate gas tube passing through the mixing plate to emerge close to the outlet of each air duct and so arranged that the gas flows directly into the high velocity air burner was ignited at the a burner at atmospheric pressure.-
assetati ment insures explosive mixture @tall points,
down stream from the mixing spiate,
For operation with natural gas., which is chiefly methane, we have found that a burner incur porating a limited pre-mixture system f 'the type shown in Figs. 2 and 3 shows greatly improved ignition behavior. Pre-mixing of gas and air at the spark plug igniter is increased by reducing the spacing between the gas and air ,ducts so as to sandwich the gas duct between the two air ducts and by providing a spiral mixing vane and internal cylinder which together form a mixing passageway from the discharge 4ports of -the lgas and air ducts and opening into -the combustion chamber. The intern-al cylinder is vented or provided 'with a scoop to supply mixture to the igniter at the face of the mixing plate.
We have described our invention in its basic forms which include -a burner characterized by an elongated combustion chamber with a mixing plate at -its head containing separate angularly directed air and -fuel ducts and separate passages for fuel and air to these ports, including a spiral mixing vane with internal cylinder and sidesscoop for eiecting limited pre-mixing prior to the point of ignition; a method of burning fuel gas .under conditions ofl high pressure to obtain high rates of heat release characterized by introducing fuel gas and air separately and angularly to the head of an elongated combustion zone so as to impart a turbulent and whirling tangential motion to the flame resulting from the mixture; and an improvement in thermal methods for recovering oil and gas from oil-bearing formations characterized by burning fuel gas at formation level in an input well in a system wherein fuel gas and air under pressure in approximately theoretical proportion for perfect combustion are separately and angularly introduced to an elongated combustion zone tted within the oil well casing so as to impart a turbulent whirling tangential motion to the tiame resulting from the mixture and controlling the temperature of the flame by introducing secondary air through the oil well casing. There are obvious variations and substitutions, of course, which can be made by those skilled in the art in the number, position and form of mechanical elements involved, the materials and dimensions of the structural elements, the proportioning of air and fuel and control of temperature and soot formation, etc. We contemplate that such changes in form or substitution of equivalents lie within the following claims.
We claim:
l. A gas burner which comprises first means having an elongated, substantially cylindrical wall forming a combustion chamber; second means connected to the head of the combustion chamber for directing streams of fuel gas and air into the combustion chamber in a manner to accomplish mixing therein; third means for separately delivering fuel gas and air to said second means; said second means including means for separately introducing each of said separatestreams of fuel gas and air into the combustion zone at a location spaced from the axis of the combustion chamber and adjacent said cylindrical wall and in a downstream direction having a directional component outward from said axis and a directional component tangential to a circle normal to said axis having its center at said axis and passing through said location, the last named tangential directional component of each of said streams being in the same direction circumferentially of said second means thereby accomthe axis of said chamber and .eeen .duet its passage through ,said plate .in devvnstreemdrees tion having a direetiona1oornponent outward roni said axis and a ydirectional, .component normal to its respective radial plane which passes .through the upstream entrance to said duet. the .last named direetionaleomponent ofeach of 7the duets being in the same direction Inferentially of -tial said plate, thereby accomplishing t swirling and mixing :of the` fuel ,gas t.
,Y i iuel ses and air passages respectively, and eans for igniting the fuel gas-air mixture.
3. A gas burner which comprises an elongated combustion chamber having a longitudinal axis and radial planes along said axis, a mixing plate at the head of said chamber, a fuel gas duct in said plate, a plurality of angularly directed air ducts in said plate sandwiching said gas duct, said ducts being similarly positioned at substantially the same distance from the axis of said chamber and each duct in its passage through said plate in downstream direction having a directional component outward from said axis and a directional component normal to its respective radial plane which passes through said laxis and the upstream entrance to said duct, the last named directional component of each of the ducts being in the same direction circumferentially of said plate thereby accomplishing tangential swirling and mixing of the fuel gas yand air adjacent the wall of the combustion chamber, a gas line feeding said gas duct, a tubular air passage charging said air ducts and containing said gas line, means for supplying fuel gas and air to said gas line and air passage respectively, and means for igniting the fuel gas-air mixture at the face of the mixing plate.
4. A gas burner in accordance with claim 2 and including a cylinder extending downstream from said mixing plate and surrounding said igniting means, and a spiral mixing vane surrounding said cylinder and forming a mixing passage way from said ducts opening into said combustion chamber, said cylinder having a scoop arranged to supply a small portion of the fuel gas-air mixture to said igniting means.
5. In the method of burning fuel gas, the improvement which comprises separately passing fuel gas and air streams to a mixing point at the head of a substantially cylindrical combustion zone, separately introducing each of said streams into the combustion zone at a location spaced from the longitudinal axis of the combustion zone and in a downstream direction having a directional component outward from said axis and a directional component tangential to a circle having its center at said axis and passing through said location, the last named tangential directional component of each of said streams being Vin the same direction circumferentially of saidV zone, directing the flow of said streams in a manner to produce peripheral ow in said combustion zone to accomplish tangential swirling and mix-l ing of the fuel gas and air atthe periphery of said combustion zone, and-igniting the resultant fuel gas-air mixture. Y
6. In the method of producing hot combustion gases at an input well for the' thermal recovery of oil and gas, the improvement which comprises separately passing fuel gas and air streams to a mixing point at the head of a substantially cylindrical combustion zone in said well, separately introducing each of said streams into the combustion zone at a location spaced from the longitudinal axis of the combustion zone and in a downstreamV direction having a directional component outward from said axis and a directional component tangential to a circle having its center at said axis and passing through said location, the last named tangential directional component ofv each of said streams being` in the same direction circumferentially of said zone, directing the flow of said streams in a manner to produce peripheral iiow in said combustion zone to accomplish tangential swirling and mixing of the fuel gas and airat the periphery of said combustion zone, igniting the resultant fuel gas-air mixture, and controlling the temperature of the flame by introducing secondary air into said well and around said combustion zone.
JOHN J. PIROS.
OLIVER F. CAMPBELL.
References Cited in the file of this patent UNITED STATES PATENTS Number l Name Date 686,157 Spinney Nov. 5, 1901 1,231,726 Gault July 3, 1917 1,473,348 Howard Nov. 6, 1923 1,626,940 Kreager May 3, 1927 1,656,907 Bansen Jan. 24, 1928 2,225,775 Garrett, Dec. 24, 1940 2,390,770 Barton et a1. Dec. 1'1, 1945 2,443,259 Martin June 15, 1948 2,444,755 Steffen July 6, 1948 2,473,435 Luzader June 14, 1949 2,500,787- Lelgemann Mar. 14, 1950 2,506,853 Berg et al May 9, 1950 2,511,380 Stadler June 13, 1950 2,561,200 yHess July 17, 195i
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US97142A US2668592A (en) | 1949-06-04 | 1949-06-04 | Gas burner and method for burning gas in oil and gas wells |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US97142A US2668592A (en) | 1949-06-04 | 1949-06-04 | Gas burner and method for burning gas in oil and gas wells |
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US2668592A true US2668592A (en) | 1954-02-09 |
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US97142A Expired - Lifetime US2668592A (en) | 1949-06-04 | 1949-06-04 | Gas burner and method for burning gas in oil and gas wells |
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Cited By (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2761512A (en) * | 1954-11-08 | 1956-09-04 | Pure Oil Co | Combustion and halosilane reaction treatment of a formation to increase production |
US2877847A (en) * | 1955-09-26 | 1959-03-17 | Sinclair Oil & Gas Company | Combustion in well with steel liner |
US2887160A (en) * | 1955-08-01 | 1959-05-19 | California Research Corp | Apparatus for well stimulation by gas-air burners |
US2888066A (en) * | 1952-03-10 | 1959-05-26 | Edward D Wilson | Electrical ignition gas torch |
US2892733A (en) * | 1955-09-16 | 1959-06-30 | Plax Corp | Method and apparatus for treating synthetic resin containers |
US2895555A (en) * | 1956-10-02 | 1959-07-21 | California Research Corp | Gas-air burner with check valve |
US2913050A (en) * | 1955-05-12 | 1959-11-17 | Phillips Petroleum Co | Preventing explosions in bore holes during underground combustion operations for oil recovery |
US2918118A (en) * | 1954-08-30 | 1959-12-22 | Phillips Petroleum Co | Burner |
US2985240A (en) * | 1959-05-21 | 1961-05-23 | Sinclair Oil & Gas Company | Bottom hole burner |
US2988350A (en) * | 1953-11-09 | 1961-06-13 | Midland Ross Corp | Combustion apparatus |
US2997105A (en) * | 1956-10-08 | 1961-08-22 | Pan American Petroleum Corp | Burner apparatus |
US3004600A (en) * | 1957-06-17 | 1961-10-17 | Gulf Research Development Co | Single well in-situ combustion process for production of oil |
US3018827A (en) * | 1957-06-17 | 1962-01-30 | Gulf Research Development Co | Single well vertical drive in-situ combustion process |
US3104705A (en) * | 1960-02-08 | 1963-09-24 | Jersey Prod Res Co | Stabilizing a formation |
US3180417A (en) * | 1962-08-13 | 1965-04-27 | California Research Corp | Method and apparatus for burning a combustible mixture in a well |
US3195632A (en) * | 1957-06-17 | 1965-07-20 | Gulf Res & Developement Compan | Radial burning in-situ combustion process utilizing a single well |
US3315745A (en) * | 1964-07-29 | 1967-04-25 | Texaco Inc | Bottom hole burner |
US3361185A (en) * | 1966-04-15 | 1968-01-02 | North Western Gas Board | Gas burners |
US3372754A (en) * | 1966-05-31 | 1968-03-12 | Mobil Oil Corp | Well assembly for heating a subterranean formation |
US3674093A (en) * | 1970-06-24 | 1972-07-04 | Dale C Reese | Method and apparatus for stimulating the flow of oil wells |
US3727691A (en) * | 1970-12-16 | 1973-04-17 | Exxon Production Research Co | Method and apparatus for treating subterranean formations |
US4079784A (en) * | 1976-03-22 | 1978-03-21 | Texaco Inc. | Method for in situ combustion for enhanced thermal recovery of hydrocarbons from a well and ignition system therefor |
US4245701A (en) * | 1979-06-12 | 1981-01-20 | Occidental Oil Shale, Inc. | Apparatus and method for igniting an in situ oil shale retort |
US4301866A (en) * | 1980-02-08 | 1981-11-24 | Occidental Oil Shale, Inc. | Method and apparatus for igniting an in situ oil shale retort |
US4380267A (en) * | 1981-01-07 | 1983-04-19 | The United States Of America As Represented By The United States Department Of Energy | Downhole steam generator having a downhole oxidant compressor |
FR2532405A1 (en) * | 1982-08-25 | 1984-03-02 | Air Liquide | METHOD AND DEVICE FOR ELECTRICALLY IGNITING AN OXYCOMBUSTIBLE BURNER |
WO1998026216A1 (en) * | 1996-12-11 | 1998-06-18 | Siemens Westinghouse Power Corporation | Gas pilot with radially displaced, high momentum fuel outlet, and method thereof |
US20060278100A1 (en) * | 2005-06-14 | 2006-12-14 | Aga Ab | Seal for burners |
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WO2014123955A1 (en) * | 2013-02-06 | 2014-08-14 | Siemens Aktiengesellschaft | Nozzle with multi-tube fuel supply passageway for gas turbine engines |
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US2888066A (en) * | 1952-03-10 | 1959-05-26 | Edward D Wilson | Electrical ignition gas torch |
US2988350A (en) * | 1953-11-09 | 1961-06-13 | Midland Ross Corp | Combustion apparatus |
US2918118A (en) * | 1954-08-30 | 1959-12-22 | Phillips Petroleum Co | Burner |
US2761512A (en) * | 1954-11-08 | 1956-09-04 | Pure Oil Co | Combustion and halosilane reaction treatment of a formation to increase production |
US2913050A (en) * | 1955-05-12 | 1959-11-17 | Phillips Petroleum Co | Preventing explosions in bore holes during underground combustion operations for oil recovery |
US2887160A (en) * | 1955-08-01 | 1959-05-19 | California Research Corp | Apparatus for well stimulation by gas-air burners |
US2892733A (en) * | 1955-09-16 | 1959-06-30 | Plax Corp | Method and apparatus for treating synthetic resin containers |
US2877847A (en) * | 1955-09-26 | 1959-03-17 | Sinclair Oil & Gas Company | Combustion in well with steel liner |
US2895555A (en) * | 1956-10-02 | 1959-07-21 | California Research Corp | Gas-air burner with check valve |
US2997105A (en) * | 1956-10-08 | 1961-08-22 | Pan American Petroleum Corp | Burner apparatus |
US3018827A (en) * | 1957-06-17 | 1962-01-30 | Gulf Research Development Co | Single well vertical drive in-situ combustion process |
US3004600A (en) * | 1957-06-17 | 1961-10-17 | Gulf Research Development Co | Single well in-situ combustion process for production of oil |
US3195632A (en) * | 1957-06-17 | 1965-07-20 | Gulf Res & Developement Compan | Radial burning in-situ combustion process utilizing a single well |
US2985240A (en) * | 1959-05-21 | 1961-05-23 | Sinclair Oil & Gas Company | Bottom hole burner |
US3104705A (en) * | 1960-02-08 | 1963-09-24 | Jersey Prod Res Co | Stabilizing a formation |
US3180417A (en) * | 1962-08-13 | 1965-04-27 | California Research Corp | Method and apparatus for burning a combustible mixture in a well |
US3315745A (en) * | 1964-07-29 | 1967-04-25 | Texaco Inc | Bottom hole burner |
US3361185A (en) * | 1966-04-15 | 1968-01-02 | North Western Gas Board | Gas burners |
US3372754A (en) * | 1966-05-31 | 1968-03-12 | Mobil Oil Corp | Well assembly for heating a subterranean formation |
US3674093A (en) * | 1970-06-24 | 1972-07-04 | Dale C Reese | Method and apparatus for stimulating the flow of oil wells |
US3727691A (en) * | 1970-12-16 | 1973-04-17 | Exxon Production Research Co | Method and apparatus for treating subterranean formations |
US4079784A (en) * | 1976-03-22 | 1978-03-21 | Texaco Inc. | Method for in situ combustion for enhanced thermal recovery of hydrocarbons from a well and ignition system therefor |
US4137968A (en) * | 1976-03-22 | 1979-02-06 | Texaco Inc. | Ignition system for an automatic burner for in situ combustion for enhanced thermal recovery of hydrocarbons from a well |
US4245701A (en) * | 1979-06-12 | 1981-01-20 | Occidental Oil Shale, Inc. | Apparatus and method for igniting an in situ oil shale retort |
US4301866A (en) * | 1980-02-08 | 1981-11-24 | Occidental Oil Shale, Inc. | Method and apparatus for igniting an in situ oil shale retort |
US4380267A (en) * | 1981-01-07 | 1983-04-19 | The United States Of America As Represented By The United States Department Of Energy | Downhole steam generator having a downhole oxidant compressor |
FR2532405A1 (en) * | 1982-08-25 | 1984-03-02 | Air Liquide | METHOD AND DEVICE FOR ELECTRICALLY IGNITING AN OXYCOMBUSTIBLE BURNER |
US4494923A (en) * | 1982-08-25 | 1985-01-22 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Oxy-fuel burners |
WO1998026216A1 (en) * | 1996-12-11 | 1998-06-18 | Siemens Westinghouse Power Corporation | Gas pilot with radially displaced, high momentum fuel outlet, and method thereof |
US5941698A (en) * | 1996-12-11 | 1999-08-24 | Siemens Westinghouse Power Corporation | Gas pilot with radially displaced, high momentum fuel outlet, and method thereof |
US20060278100A1 (en) * | 2005-06-14 | 2006-12-14 | Aga Ab | Seal for burners |
WO2007130111A1 (en) * | 2006-05-10 | 2007-11-15 | Owens-Brockway Glass Container Inc. | Glassware mold lubrication burner |
US7699602B2 (en) | 2006-05-10 | 2010-04-20 | Owens-Brockway Glass Container Inc. | Glassware mold lubrication burner |
AU2006343304B2 (en) * | 2006-05-10 | 2011-10-06 | Owens-Brockway Glass Container Inc. | Glassware mold lubrication burner |
CN101438103B (en) * | 2006-05-10 | 2011-12-14 | 欧文斯-布洛克威玻璃容器有限公司 | Glassware mold lubrication burner |
TWI395724B (en) * | 2006-05-10 | 2013-05-11 | Owens Brockway Glass Container | Glassware mold lubrication burner |
WO2014123955A1 (en) * | 2013-02-06 | 2014-08-14 | Siemens Aktiengesellschaft | Nozzle with multi-tube fuel supply passageway for gas turbine engines |
JP2016508593A (en) * | 2013-02-06 | 2016-03-22 | シーメンス アクチエンゲゼルシヤフトSiemens Aktiengesellschaft | Nozzle with multi-tube fuel supply passage for gas turbine engine |
US9562692B2 (en) | 2013-02-06 | 2017-02-07 | Siemens Aktiengesellschaft | Nozzle with multi-tube fuel passageway for gas turbine engines |
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