US3738792A - Industrial burner - Google Patents

Industrial burner Download PDF

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US3738792A
US3738792A US00225583A US3738792DA US3738792A US 3738792 A US3738792 A US 3738792A US 00225583 A US00225583 A US 00225583A US 3738792D A US3738792D A US 3738792DA US 3738792 A US3738792 A US 3738792A
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space
supply
air
combination
opening
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US00225583A
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C Feng
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Selas Corp of America
SELAS CORP
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Selas Corp of America
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Assigned to FIRST PENNSYLVANIA BANK N A, A NATIONAL BANKING ASSOCIATION reassignment FIRST PENNSYLVANIA BANK N A, A NATIONAL BANKING ASSOCIATION SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SELAS CORPORATION OF AMERICA A CORP OF PA
Assigned to SELAS CORPORATION OF AMERICA A CORP. OF PA reassignment SELAS CORPORATION OF AMERICA A CORP. OF PA RELEASED BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: FIRST PENNSYLVANIA BANK N.V., FOR ITSELF AND AS AGENT FOR THE PHILADELPHIA NATIONAL BANK
Assigned to BANCBOSTON FINANCIAL COMPANY reassignment BANCBOSTON FINANCIAL COMPANY SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SELAS CORPORATION OF AMERICA
Assigned to SELAS CORPORATION OF AMERICA reassignment SELAS CORPORATION OF AMERICA RELEASED BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: BANCBOSTON FINANACIAL COMPANY A MA TRUST
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D17/00Burners for combustion conjointly or alternatively of gaseous or liquid or pulverulent fuel

Definitions

  • the invention relates to an industrial burner of the combustion chamber type that is used for submer combustion.
  • the burner will 0 fuel.
  • the present invention relates to industrial burners, and more particularly to a submerged combustion type of burner that can use either gas or oil as the fuel.
  • FIG. 1 is a section through the burner
  • FIG. 2 is a view taken on line 2-2 of FIG. 1;
  • FIG. 3 is a sectional view of a portion of a modified burner.
  • a burner which is enclosed in a substantially cylindrical metal casing consisting of spaced apart outer wall 1 and inner wall 2. One end of the walls is reduced in diameter, as shown, to form a restricted outlet opening 3.
  • the cylindrical casing is lined with a high temperature ceramic liner 4, the interior of which is a combustion chamber 5. One end of the liner is reduced to correspond to the reduction in the casing, while the other end is closed by a distributor member 6 through which fuel and air are supplied to the combustion chamber 5.
  • This member provides a space having an axial wall 7 provided with a plurality of tangential openings 8 and having anend wall 9 provided with a central opening 11 and a ring of smaller openings 12.
  • Gas fuel is supplied through a sleeve 13 which abuts closely against the outside of wall 9 and which is provided with a gas inlet 14.
  • the other end of the sleeve is closed by a cap 15 to form a gas inlet chamber.
  • Oil is supplied to the burner by an atomizer 16 which is mounted in a sleeve 17 that is concentric with sleeve 13 and is fastened to disc 15.
  • the inner end of sleeve 17 has a flange 18 which is located concentrically in sleeve 13 by a plurality of spacers. 19.
  • the space between the periphery of flange 18 and sleeve 13 forms an annular gas passage 20.
  • a strainer 21 may be attached to the back of the atomizer.
  • a disc 22 is attached to the exterior of sleeve 13 which disc supports a cylindrical partition 23 that is received between the casing walls 1 and 2.
  • This partition provides annular passages 24 and 25 through which the air flows to a chamber 26 before being discharged into combustion chamber 5 through openings 8.
  • a disc 27 which is also attached to the exterior of sleeve 13 which disc is provided with an air inlet opening 28.
  • This disc and the parts attached thereto are held in position by means of bolts extending therethrough into a flange 29 formed on the lower end of wall 1.
  • a series of small partitions'31 may be provided at the upper end of the casing at a point connecting passages 24 and 25 in order to even out the flow of the air around the annulus of the two passages 24 and 25.
  • the burner is ignited by means of a spark between an igniter rod 32 which is connected to one terminal of an electric source (not shown) and the wall 9 which is connected through a switch to the other terminal of said source to form a circuit.
  • This igniter rod is held in position a short distance from the back surface of wall 9 by means of an insulator 33 that extends through flanges 15 and 18.
  • the air supplied to the burner flows through concen tric passages 24 and 25 before being discharged into chamber 26 and through openings 8.
  • the air is preheated, preferably, to about 700F, thus increasing the temperature of combustion.
  • oil can be supplied as the fuel. Fuel oil is almost completely vaporized at this temperature.
  • the oil supply can be turned on and the gas cut off.
  • Atomizer. l6 sprays oil in fine droplets toward the combustion chamber 5 in a cone which is small enough to avoid impingement upon axial wall 7 of the distributor.
  • the oil droplets are picked up, vaporized and mixed with the preheated air flowing through openings 8.
  • the tangential path of the air increases turbulence and mixing so that combustion is completed in the combustion chamber with hot products of combustion being discharged at high velocity through the restricted outlet opening 3.
  • both gas and oil can be supplied simultaneously to the burner as fuel. No difference is observed in the operation of the burner whether gas or oil or a combination of the two is being used as fuel.
  • FIG. 3 A portion of the air supplied to the burner will be exhausted through passage 36 to sweep across the inner surface of passage 3 thereby helping to cool it as well as tempering the exhausting products of combustion.
  • structure forming a refractory lined combustion chamber having a restricted opening at one end, a fuel distributor member at the opposite end of said chamber, said member being provided with a cylindrical'spaceaxially aligned with and open to said chamber, said space being bounded by a cylindrical wall and an end wall, a plurality of openings extending tangentially through said cylindrical wall, means to supply combustion air to said space through said openings, an axially extending opening in said end wall, means to supply a fuel gas to said space through said axially extending opening, an oil atomizer spaced axially from and concentric with said axially extending opening, and means to supply oil to said atomizer to be discharged thereby into said space.
  • the combination'of claim 1 including an igniting.
  • said means to supply air includes a pair of connected concentric passages surrounding the refractory lining of said combustion chamber, means to direct air to the outer of said passages and means to direct air from the inner of said passages to said tangential openings.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Nozzles For Spraying Of Liquid Fuel (AREA)

Abstract

The invention relates to an industrial burner of the combustion chamber type that is used for submerged combustion. The burner will operate on gas or oil as a fuel.

Description

14 1 June 12,1973
3,260,587 7/1966 Dolf et al......... 431/158 1/1969 Wang et INDUSTRIAL BURNER inventor: Chung Liao Feng, Dresher, Pa.
L J t H o D B m v r a C e m m m E W a m n P a .w r e m A l o n o u m Wm W .1 e s m n m e S D e n b S S A T 7 Attorney-E. Wellford Mason ABSTRACT The invention relates to an industrial burner of the combustion chamber type that is used for submer combustion. The burnerwill 0 fuel.
80 m H1 1 k 2 F 52 us. 51] 1111. C1.
[58] Field 01 Search...
ged perate on gas or oil as a References Cited UNITED STATES PATENTS 5 Claims, 3 Drawing Figures 2,725,929 Massier............................... 431/158 i \i slul iiiii.11 Il /l/Il II/ /1 4. 15 7 ll 0 1 4 7/9 2 722 115,511!!! wit-iv l INDUSTRIAL BURNER SUMMARY OF THE INVENTION The present invention relates to industrial burners, and more particularly to a submerged combustion type of burner that can use either gas or oil as the fuel.
It has been determined in the melting of various materials that good mixing and efficiency can be obtained cept that its internal construction is entirely altered so that either gas or oil or a combination of the two may be used as fuel. I
The various features of novelty which characterize my invention are pointed out with particularity in the claims annexed to and forming a part of this specification. For a better understanding of the invention, however, its advantages and specific objects attained with its use, reference should be' had to the accompanying drawings and descriptive matter in which I have illustrated and described a preferred embodiment of the invention.
IN THE DRAWINGS FIG. 1 is a section through the burner;
FIG. 2 is a view taken on line 2-2 of FIG. 1; and
FIG. 3 is a sectional view of a portion of a modified burner.
DETAILED DESCRIPTION Referring to the drawing, there is shown a burner which is enclosed in a substantially cylindrical metal casing consisting of spaced apart outer wall 1 and inner wall 2. One end of the walls is reduced in diameter, as shown, to form a restricted outlet opening 3. The cylindrical casing is lined with a high temperature ceramic liner 4, the interior of which is a combustion chamber 5. One end of the liner is reduced to correspond to the reduction in the casing, while the other end is closed by a distributor member 6 through which fuel and air are supplied to the combustion chamber 5. This member provides a space having an axial wall 7 provided with a plurality of tangential openings 8 and having anend wall 9 provided with a central opening 11 and a ring of smaller openings 12.
Gas fuel is supplied through a sleeve 13 which abuts closely against the outside of wall 9 and which is provided with a gas inlet 14. The other end of the sleeve is closed by a cap 15 to form a gas inlet chamber. Oil is supplied to the burner by an atomizer 16 which is mounted in a sleeve 17 that is concentric with sleeve 13 and is fastened to disc 15. The inner end of sleeve 17 has a flange 18 which is located concentrically in sleeve 13 by a plurality of spacers. 19. The space between the periphery of flange 18 and sleeve 13 forms an annular gas passage 20. It is noted that a strainer 21 may be attached to the back of the atomizer.
A disc 22 is attached to the exterior of sleeve 13 which disc supports a cylindrical partition 23 that is received between the casing walls 1 and 2. This partition provides annular passages 24 and 25 through which the air flows to a chamber 26 before being discharged into combustion chamber 5 through openings 8. There is provided a disc 27 which is also attached to the exterior of sleeve 13 which disc is provided with an air inlet opening 28. This disc and the parts attached thereto are held in position by means of bolts extending therethrough into a flange 29 formed on the lower end of wall 1. It is noted that a series of small partitions'31 may be provided at the upper end of the casing at a point connecting passages 24 and 25 in order to even out the flow of the air around the annulus of the two passages 24 and 25.
The burner is ignited by means of a spark between an igniter rod 32 which is connected to one terminal of an electric source (not shown) and the wall 9 which is connected through a switch to the other terminal of said source to form a circuit. This igniter rod is held in position a short distance from the back surface of wall 9 by means of an insulator 33 that extends through flanges 15 and 18.
When starting the burner in operation, gas is always used regardless of the fuel to be used later on. After the burner has heated up it can be shifted to oil. When starting the burner, air and gas flow are adjusted to minimum rates with the ratio being adjusted to give a lean mixture. Under this condition some air will flow through opening 34 to cause a partial premix through gas passage 20 to produce a more favorable ratio for ignition. When the gas and air are flowing, the ignition circuit is closed, producing a spark between the end of igniter rod 32 and end wall 9 to ignite the mixture. Thereafter, the gas supply will be adjusted to bring the air-gas ratio to stoichiometric proportions. The supplies of gas and air can now be increased as desired to the maximum capacity of the burner. The air flowing through tangential openings 8 into the space therein is turbulently mixed with the gas flowing through passage 20 and opening 11. Gas flowing through ports 12 creates pilot flames that help stabilize the main combustion. This results in rapid combustion that is completed in chamber 5. Only hot products of combustion are exhausted through restricted discharge opening 3.
The air supplied to the burner flows through concen tric passages 24 and 25 before being discharged into chamber 26 and through openings 8. During its passage the air is preheated, preferably, to about 700F, thus increasing the temperature of combustion. After the burner is first ignited and the air has reached a temperature of about 400F, oil can be supplied as the fuel. Fuel oil is almost completely vaporized at this temperature.
After the burner has been operating a sufficient time to heat up, the oil supply can be turned on and the gas cut off. Atomizer. l6 sprays oil in fine droplets toward the combustion chamber 5 in a cone which is small enough to avoid impingement upon axial wall 7 of the distributor. The oil droplets are picked up, vaporized and mixed with the preheated air flowing through openings 8. The tangential path of the air increases turbulence and mixing so that combustion is completed in the combustion chamber with hot products of combustion being discharged at high velocity through the restricted outlet opening 3. If desired, both gas and oil can be supplied simultaneously to the burner as fuel. No difference is observed in the operation of the burner whether gas or oil or a combination of the two is being used as fuel.
For some uses it may be desirable to reduce somewhat the temperature of the jet of gases, and to increase the cooling of the outer end of the casing. The construction of FIG. 3 is used for this purpose. A portion of the air supplied to the burner will be exhausted through passage 36 to sweep across the inner surface of passage 3 thereby helping to cool it as well as tempering the exhausting products of combustion.
While in accordance with the provisions of the Statutes I have illustrated and described the best form of embodiment of my invention now known to me, it will be apparent to those skilled in the art that changes may be made in the form of the apparatus disclosed without departing from the spirit and scope of the invention set forth in the appended claims, and that in some cases certain features of my invention may be used to advantage without a corresponding use of other features.
What is claimed is:
1. In an industrial burner, structure forming a refractory lined combustion chamber having a restricted opening at one end, a fuel distributor member at the opposite end of said chamber, said member being provided with a cylindrical'spaceaxially aligned with and open to said chamber, said space being bounded by a cylindrical wall and an end wall, a plurality of openings extending tangentially through said cylindrical wall, means to supply combustion air to said space through said openings, an axially extending opening in said end wall, means to supply a fuel gas to said space through said axially extending opening, an oil atomizer spaced axially from and concentric with said axially extending opening, and means to supply oil to said atomizer to be discharged thereby into said space.
2. The combination of claim 1 in which said means to supply combustion air includes a passage surrounding the lining of said combustion chamber.
3. The combination'of claim 1 including an igniting.
rod, means to .locate said rod with an end thereof located adjacent to said axially extending opening and said atomizer.
4. The combination of claim 1 in which said means to supply air includes a pair of connected concentric passages surrounding the refractory lining of said combustion chamber, means to direct air to the outer of said passages and means to direct air from the inner of said passages to said tangential openings.
5. The combination of claim 4 including means forming an additional passage between said inner concentric passage and said restricted opening.

Claims (5)

1. In an industrial burner, structure forming a refractory lined combustion chamber having a restricted opening at one end, a fuel distributor member at the opposite end of said chamber, said member being provided with a cylindrical space axially aligned with and open to said chamber, said space being bounded by a cylindrical wall and an end wall, a plurality of openings extending tangentially through said cylindrical wall, means to supply combustion air to said space through said openings, an axially extending opening in said end wall, means to supply a fuel gas to said space through said axially extending opening, an oil atomizer spaced axially from and concentric with said axially extending opening, and means to supply oil to said atomizer to be discharged thereby into said space.
2. The combination of claim 1 in which said means to supply combustion air includes a passage surrounding the lining of said combustion chamber.
3. The combination of claim 1 including an igniting rod, means to locate said rod with an end thereof located adjacent to said axially extending opening and said atomizer.
4. The combination of claim 1 in which said means to supply air includes a pair of connected concentric passages surrounding the refractory lining of said combustion chamber, means to direct air to the outer of said passages and means to direct air from the inner of said passages to said tangential openings.
5. The combination of claim 4 including means forming an additional passage between said inner concentric passage and said restricted opening.
US00225583A 1972-02-11 1972-02-11 Industrial burner Expired - Lifetime US3738792A (en)

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Cited By (62)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2452946A1 (en) * 1979-04-02 1980-10-31 Outokumpu Oy IMMERSION TYPE EVAPORATOR
US4384434A (en) * 1980-01-16 1983-05-24 Browning Engineering Corporation High velocity flame jet internal burner for blast cleaning and abrasive cutting
US4539034A (en) * 1984-07-19 1985-09-03 Ppg Industries, Inc. Melting of glass with staged submerged combustion
US4545800A (en) * 1984-07-19 1985-10-08 Ppg Industries, Inc. Submerged oxygen-hydrogen combustion melting of glass
US4676744A (en) * 1983-03-11 1987-06-30 British Gas Plc Regenerative heating apparatus
US5055032A (en) * 1988-10-12 1991-10-08 Ruhrgas Aktiengesellschaft A burner with a flame retention device
US5257926A (en) * 1991-12-17 1993-11-02 Gideon Drimer Fast, safe, pyrogenic external torch assembly
EP1022514A1 (en) 1999-01-22 2000-07-26 Saint-Gobain Vitrage Method and device for controlling the gaseous fuel flow
US6389814B2 (en) 1995-06-07 2002-05-21 Clean Energy Systems, Inc. Hydrocarbon combustion power generation system with CO2 sequestration
US6523349B2 (en) 2000-03-22 2003-02-25 Clean Energy Systems, Inc. Clean air engines for transportation and other power applications
US6622470B2 (en) 2000-05-12 2003-09-23 Clean Energy Systems, Inc. Semi-closed brayton cycle gas turbine power systems
US20040128975A1 (en) * 2002-11-15 2004-07-08 Fermin Viteri Low pollution power generation system with ion transfer membrane air separation
US6868677B2 (en) 2001-05-24 2005-03-22 Clean Energy Systems, Inc. Combined fuel cell and fuel combustion power generation systems
US20050236747A1 (en) * 2004-04-27 2005-10-27 Rue David M Process and apparatus for uniform combustion within a molten material
US20050241311A1 (en) * 2004-04-16 2005-11-03 Pronske Keith L Zero emissions closed rankine cycle power system
US20050255995A1 (en) * 2004-05-14 2005-11-17 Gas Technology Institute Method for producing catalytically-active materials
US7021063B2 (en) 2003-03-10 2006-04-04 Clean Energy Systems, Inc. Reheat heat exchanger power generation systems
US20070044479A1 (en) * 2005-08-10 2007-03-01 Harry Brandt Hydrogen production from an oxyfuel combustor
US20070167307A1 (en) * 2006-01-13 2007-07-19 Brodie Sally H Novel composition
EP2397446A2 (en) 2010-06-17 2011-12-21 Johns Manville Panel-cooled submerged combustion melter geometry and methods of making molten glass
EP2433911A1 (en) 2010-09-23 2012-03-28 Johns Manville Methods and apparatus for recycling glass products using submerged combustion
EP2578547A2 (en) 2011-10-07 2013-04-10 Johns Manville Submerged combustion glass manufacturing systems and methods
WO2013162986A1 (en) 2012-04-27 2013-10-31 Johns Manville Submerged combustion melter comprising a melt exit structure designed to minimize impact of mechanical energy, and methods of making molten glass
WO2013188082A1 (en) 2012-06-11 2013-12-19 Johns Manville Apparatus, systems and methods for conditioning molten glass
WO2013188167A1 (en) 2012-06-11 2013-12-19 Manville, Johns Submerged combustion melting processes producing glass and similar materials, and systems for carrying out such processes
WO2014008045A1 (en) 2012-07-03 2014-01-09 Manville, Johns Processes for producing molten glasses from glass batches using turbulent submerged combustion melting, and systems for carrying out such processes
US8875544B2 (en) 2011-10-07 2014-11-04 Johns Manville Burner apparatus, submerged combustion melters including the burner, and methods of use
WO2014193388A1 (en) 2013-05-30 2014-12-04 Johns Manville Submerged combustion glass melting systems and methods of use
US8973400B2 (en) 2010-06-17 2015-03-10 Johns Manville Methods of using a submerged combustion melter to produce glass products
US8973405B2 (en) 2010-06-17 2015-03-10 Johns Manville Apparatus, systems and methods for reducing foaming downstream of a submerged combustion melter producing molten glass
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US9021838B2 (en) 2010-06-17 2015-05-05 Johns Manville Systems and methods for glass manufacturing
US9032760B2 (en) 2012-07-03 2015-05-19 Johns Manville Process of using a submerged combustion melter to produce hollow glass fiber or solid glass fiber having entrained bubbles, and burners and systems to make such fibers
US9096452B2 (en) 2010-06-17 2015-08-04 Johns Manville Methods and systems for destabilizing foam in equipment downstream of a submerged combustion melter
US9115017B2 (en) 2013-01-29 2015-08-25 Johns Manville Methods and systems for monitoring glass and/or foam density as a function of vertical position within a vessel
US9227865B2 (en) 2012-11-29 2016-01-05 Johns Manville Methods and systems for making well-fined glass using submerged combustion
US20160107914A1 (en) * 2013-05-30 2016-04-21 Johns Manville Submerged combustion burners, submerged combustion glass melters including the burners, and methods of use
US9533905B2 (en) 2012-10-03 2017-01-03 Johns Manville Submerged combustion melters having an extended treatment zone and methods of producing molten glass
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US11912608B2 (en) 2019-10-01 2024-02-27 Owens-Brockway Glass Container Inc. Glass manufacturing

Cited By (127)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2452946A1 (en) * 1979-04-02 1980-10-31 Outokumpu Oy IMMERSION TYPE EVAPORATOR
US4384434A (en) * 1980-01-16 1983-05-24 Browning Engineering Corporation High velocity flame jet internal burner for blast cleaning and abrasive cutting
US4676744A (en) * 1983-03-11 1987-06-30 British Gas Plc Regenerative heating apparatus
US4539034A (en) * 1984-07-19 1985-09-03 Ppg Industries, Inc. Melting of glass with staged submerged combustion
US4545800A (en) * 1984-07-19 1985-10-08 Ppg Industries, Inc. Submerged oxygen-hydrogen combustion melting of glass
EP0171638A1 (en) * 1984-07-19 1986-02-19 Ppg Industries, Inc. Melting of glass with staged submerged combustion
US5055032A (en) * 1988-10-12 1991-10-08 Ruhrgas Aktiengesellschaft A burner with a flame retention device
US5257926A (en) * 1991-12-17 1993-11-02 Gideon Drimer Fast, safe, pyrogenic external torch assembly
US6598398B2 (en) 1995-06-07 2003-07-29 Clean Energy Systems, Inc. Hydrocarbon combustion power generation system with CO2 sequestration
US7043920B2 (en) 1995-06-07 2006-05-16 Clean Energy Systems, Inc. Hydrocarbon combustion power generation system with CO2 sequestration
US6389814B2 (en) 1995-06-07 2002-05-21 Clean Energy Systems, Inc. Hydrocarbon combustion power generation system with CO2 sequestration
US20040003592A1 (en) * 1995-06-07 2004-01-08 Fermin Viteri Hydrocarbon combustion power generation system with CO2 sequestration
FR2788839A1 (en) 1999-01-22 2000-07-28 Saint Gobain Vitrage METHOD AND DEVICE FOR REGULATING A GASEOUS FUEL CURRENT
EP1022514A1 (en) 1999-01-22 2000-07-26 Saint-Gobain Vitrage Method and device for controlling the gaseous fuel flow
US6523349B2 (en) 2000-03-22 2003-02-25 Clean Energy Systems, Inc. Clean air engines for transportation and other power applications
US20050236602A1 (en) * 2000-05-12 2005-10-27 Fermin Viteri Working fluid compositions for use in semi-closed Brayton cycle gas turbine power systems
US20040065088A1 (en) * 2000-05-12 2004-04-08 Fermin Viteri Semi-closed brayton cycle gas turbine power systems
US6824710B2 (en) 2000-05-12 2004-11-30 Clean Energy Systems, Inc. Working fluid compositions for use in semi-closed brayton cycle gas turbine power systems
US6910335B2 (en) 2000-05-12 2005-06-28 Clean Energy Systems, Inc. Semi-closed Brayton cycle gas turbine power systems
US6637183B2 (en) 2000-05-12 2003-10-28 Clean Energy Systems, Inc. Semi-closed brayton cycle gas turbine power systems
US6622470B2 (en) 2000-05-12 2003-09-23 Clean Energy Systems, Inc. Semi-closed brayton cycle gas turbine power systems
US6868677B2 (en) 2001-05-24 2005-03-22 Clean Energy Systems, Inc. Combined fuel cell and fuel combustion power generation systems
US20040128975A1 (en) * 2002-11-15 2004-07-08 Fermin Viteri Low pollution power generation system with ion transfer membrane air separation
US6945029B2 (en) 2002-11-15 2005-09-20 Clean Energy Systems, Inc. Low pollution power generation system with ion transfer membrane air separation
US7021063B2 (en) 2003-03-10 2006-04-04 Clean Energy Systems, Inc. Reheat heat exchanger power generation systems
US20050241311A1 (en) * 2004-04-16 2005-11-03 Pronske Keith L Zero emissions closed rankine cycle power system
US7882692B2 (en) 2004-04-16 2011-02-08 Clean Energy Systems, Inc. Zero emissions closed rankine cycle power system
US20050236747A1 (en) * 2004-04-27 2005-10-27 Rue David M Process and apparatus for uniform combustion within a molten material
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