US20100159409A1 - Non-centric oxy-fuel burner for glass melting systems - Google Patents
Non-centric oxy-fuel burner for glass melting systems Download PDFInfo
- Publication number
- US20100159409A1 US20100159409A1 US12/651,506 US65150610A US2010159409A1 US 20100159409 A1 US20100159409 A1 US 20100159409A1 US 65150610 A US65150610 A US 65150610A US 2010159409 A1 US2010159409 A1 US 2010159409A1
- Authority
- US
- United States
- Prior art keywords
- burner
- fuel
- delivery member
- gas
- pipe
- 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.)
- Abandoned
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 142
- 238000002844 melting Methods 0.000 title description 5
- 230000008018 melting Effects 0.000 title description 5
- 239000011521 glass Substances 0.000 title description 4
- 239000007800 oxidant agent Substances 0.000 claims abstract description 55
- 230000001590 oxidative effect Effects 0.000 claims abstract description 55
- 238000002485 combustion reaction Methods 0.000 claims abstract description 13
- 239000007789 gas Substances 0.000 claims description 88
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 4
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 239000003915 liquefied petroleum gas Substances 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 239000003345 natural gas Substances 0.000 claims description 2
- 229910052756 noble gas Inorganic materials 0.000 claims description 2
- 150000002835 noble gases Chemical class 0.000 claims description 2
- 239000001294 propane Substances 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 239000000155 melt Substances 0.000 description 12
- 238000010586 diagram Methods 0.000 description 7
- 125000006850 spacer group Chemical group 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/235—Heating the glass
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C5/00—Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus
- F23C5/08—Disposition of burners
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/235—Heating the glass
- C03B5/2353—Heating the glass by combustion with pure oxygen or oxygen-enriched air, e.g. using oxy-fuel burners or oxygen lances
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
- C03B7/02—Forehearths, i.e. feeder channels
- C03B7/06—Means for thermal conditioning or controlling the temperature of the glass
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
- C03B7/02—Forehearths, i.e. feeder channels
- C03B7/06—Means for thermal conditioning or controlling the temperature of the glass
- C03B7/065—Means for thermal conditioning or controlling the temperature of the glass by combustion with pure oxygen or oxygen-enriched air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C5/00—Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus
- F23C5/02—Structural details of mounting
- F23C5/06—Provision for adjustment of burner position during operation
-
- 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
-
- 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
- F23D14/32—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid using a mixture of gaseous fuel and pure oxygen or oxygen-enriched air
-
- 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
- F23D14/46—Details, e.g. noise reduction means
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
Definitions
- the invention relates to burners for furnaces and furnace systems.
- Conical concentric oxy-fuel burners have been used in the crown of glass melting furnaces to melt batch in the furnaces. Once a pre-positioned hole is drilled in the furnace crown and a burner block is installed in the hole, there is limited if no ability to change the direction of the turbulent flame being emitted from the burner. If a different direction is required for the flame, it is required to drill and install an alternate (different) burner hole in order to re-position the burner and hence the flame.
- Existing furnace designs, with their steelwork and crown expansion joints frequently limit the location that burners can be installed in the furnace and as a result optimum flame coverage is not always achieved or blocks are angled excessively so that the burner flame is less effective.
- Concentric oxy-fuel burners produce conical flames perpendicular to the melt which in turn produce circular flame patterns at the melt.
- the resulting flame pattern produced by a plurality of spaced apart burners limits the total flame coverage at the surface of the melt.
- Concentric burners combust uniformly in the combustion space above the melt. This uniformity and intensity of combustion can provide excessive combustion in the free space between the crown and the melt resulting in less than optimum heat transfer and higher oxides of nitrogen (NOx) at the melt surface.
- NOx oxides of nitrogen
- a burner such as an oxy-fuel burner is provided for a furnace or a forehearth, and which includes a gas delivery member, and a fuel delivery member having a portion disposed at an interior of the gas delivery member and offset from a longitudinal axis of the gas delivery member.
- a method for combusting product in a furnace or a forehearth comprising providing a flow of gaseous oxidant along a first flow path to the furnace or the forehearth; providing a flow of gaseous fuel along a second flow path offset from the first flow path to the furnace or the forehearth; exposing the first flow path to the second flowpath; and combusting the gaseous oxidant and the gaseous fuel to provide a non-circular burn area.
- a burner whereby one or more of the gas and fuel delivery members may be rotated along their respective longitudinal axes to control an angle of discharge of the burner flame and the resulting non-circular burn area.
- a flange assembly for orienting the gas delivery member and the fuel delivery member with respect to each other, and securing the members in a fixed position with respect to each other.
- FIG. 1A discloses a partial cross-sectional plan view of a burner of the present invention for use with a furnace.
- FIG. 1B discloses a cross-section of the burner taken along line 1 B- 1 B of FIG. 1A .
- FIG. 2A discloses a diagram of another embodiment of a burner of the present invention.
- FIG. 2B discloses a cross-section diagram taken along line 2 B- 2 B of FIG. 2A .
- FIG. 3A discloses a diagram of another embodiment of a burner of the present invention.
- FIG. 3B discloses a cross-section diagram taken along line 3 B- 3 B of FIG. 3A .
- FIG. 4 discloses a flame footprint provided by the burners of the present invention.
- FIG. 5A discloses a diagram of another embodiment of a burner of the present invention.
- FIG. 5B discloses a cross-section diagram taken along line 5 B- 5 B of FIG. 5A .
- FIG. 6A discloses a partial cross-sectional plan view of another embodiment of the burner of the present invention for use with a furnace.
- FIG. 6B discloses a cross-section of the burner taken along line 6 B- 6 B of FIG. 6A .
- FIG. 7A discloses a partial cross-sectional plan view of still another embodiment of the burner of the present invention for use with a furnace.
- FIG. 7B discloses a cross-section of the burner taken along line 7 B- 7 B of FIG. 7A .
- FIG. 8A discloses a partial cross-sectional plan view of another embodiment of the burner of the present invention for use with a furnace.
- FIG. 8B discloses a cross-section of the burner taken along line 8 B- 8 B of FIG. 8A .
- FIG. 9 discloses a partial cross-sectional plan view of a burner of the present invention mounted in a burner block of a furnace.
- FIG. 10 discloses a partial cross-sectional plan view of another burner embodiment for use with a furnace.
- FIG. 11A discloses a view taken along line 11 A- 11 A of FIG. 10 .
- FIGS. 11B and 11C show schematic views of elements of FIG. 11A arranged in different positions.
- FIGS. 12A-12C show schematic views corresponding to that of FIGS. 11A-11C , respectively.
- FIGS. 13-15 show components of a flange assembly for the burner embodiments of FIGS. 10 and 16 .
- FIG. 16 shows a partial cross-sectional plan view of another burner embodiment for use with a furnace.
- a burner 10 of the present invention for use with a furnace, such as for example an oxy-fuel glass melting furnace or a forehearth of the furnace.
- Reference to use of the burner with a furnace also includes use of the burner with forehearth.
- the burner 10 consists of a gas pipe 12 or conduit, for delivering gaseous oxygen for example, having an exterior sidewall 14 constructed and arranged for disposition in a burner block of a furnace.
- the gas provided to and delivered in the gas pipe 12 is a gaseous oxidant such as for example gaseous oxygen at a purity level of 85%-100%; where less than 100% oxygen, the balance may be nitrogen and/or other noble gases, and combinations thereof.
- An internal space 16 of the gas pipe 12 is of sufficient size and shape to receive a fuel pipe 18 or conduit disposed therein.
- the fuel pipe 18 has an exterior side wall 20 and internal space 22 .
- the gas pipe 12 or oxidant pipe for example, is bent thereby providing an elbow 24 in the gas pipe 12 .
- the pipe 12 is in fluid communication with a gas supply (not shown).
- a threaded exterior end 26 of the gas pipe 12 provides for releasable connection to the gas supply.
- An opposite or distal end 28 of the gas pipe 12 terminates in a burner block of the furnace (not shown) and is disposed at a select position above product melt in the furnace.
- Gaseous oxidant provided may be a single type of oxidant, such as for example oxygen, or selected from a composition of gases as well.
- the interior 16 of the gas pipe 12 is sized and shaped to receive the fuel pipe 18 to be disposed therein, as shown in FIGS. 1A and 1 b .
- the fuel pipe 18 is constructed of a material conducive to being exposed to the oxidant in the gas pipe 12 .
- the fuel pipe 18 has an end or proximal end 30 extending from proximate the elbow 24 of the gas pipe 12 , while an opposed or distal end 32 of the fuel pipe 18 terminates at approximately the same position as the end 28 of the gas pipe 12 .
- the gas pipe 12 and fuel pipe 18 may terminate at the same location.
- the fuel pipe 18 is in fluid communication with a supply of gaseous fuel, such as for example natural gas, propane, liquid petroleum gas (LPG), synthetic gas (derived from organic solid, liquid and or gaseous sources, or combinations thereof), and combinations thereof.
- gaseous fuel such as for example natural gas, propane, liquid petroleum gas (LPG), synthetic gas (derived from organic solid, liquid and or gaseous sources, or combinations thereof), and combinations thereof.
- the fuel used may consist of a single gaseous fuel or a composition of fuels.
- the end 30 of the fuel pipe 18 projecting from the gas pipe 12 may also be threaded 31 for releasable connection to a source (not shown) of gaseous fuel.
- Spacing or support members 34 , 36 , 38 are provided to support the fuel pipe 18 within the gas pipe 12 and provide the spaced relation therebetween without interrupting the flow of gas through the gas pipe 12 .
- a weld or seal 40 is provided to seal the circumference of an inlet 42 in the gas pipe 12 through which the fuel pipe 18 is inserted.
- the disposition of the fuel pipe 18 at the interior 16 of the gas pipe 12 is more clearly shown.
- the gas pipe 12 and fuel pipe 18 are substantially parallel to each other from a point where the gas pipe 12 transits from the elbow 24 to a linear arrangement. It can be seen however that the disposition of the fuel pipe 18 within the gas pipe 12 is non-concentric; i.e., the gas pipe 12 and the fuel pipe 18 do not share a common longitudinal axis. Rather, a longitudinal axis 44 of the gas pipe 12 is offset with respect to a longitudinal axis 46 of the fuel pipe 18 , as will be further discussed below, to provide a burner flame and flame footprint area for the particular furnace and product to be melted within the furnace. The burner can be adjusted to alter the flame footprint. This is accomplished because the gas pipe and fuel pipe are adapted, such as by construction and arrangement of their components, to be rotated about their respective longitudinal axes 44 , 46 .
- the burner 10 of FIGS. 1A and 1B may also be constructed as an integral unit, thereby permitting rotation of the combined gas pipe and fuel pipe unit in the burner block to selectively control the disposition of the flame footprint area being emitted from the burner 10 into the furnace.
- Elements illustrated in those Figures which correspond to the elements described above with respect to FIGS. 1A , 1 B have been designated by corresponding reference numerals increased by one hundred, two hundred, three hundred, four hundred, etc., respectively.
- FIGS. 2A and 2B show schematics of another embodiment of the burner 110 of FIGS. 1A , 1 B.
- the fuel pipe 118 is disposed in the gas pipe 112 in an angled relationship, i.e. not parallel, such that the flame emitted from the burner into the furnace also provides a non-circular footprint at the melt in the furnace.
- the burner 110 may have the gas pipe 112 and fuel pipe 118 formed as an integral unit, whereby rotation of the unit as represented by arrow 60 can occur to provide the flame footprint at select positions on the melt within the furnace. Rotation of the burner unit can be done through 360°.
- FIG. 2A shows the gaseous oxidant flow, for example, and gaseous fuel flow to the furnace.
- the fuel pipe 218 may also be angled sufficiently in the gas pipe 212 such that a distal end 232 of the fuel pipe contacts a distal end 228 of the gas pipe 212 . Such an arrangement is shown in FIGS. 3A and 3B .
- FIG. 4 there is represented a plurality of flame footprints 62 that are provided by the burner 10 ( 110 , 210 , etc.) embodiments in the Figures.
- Each non-circular footprint 62 or burn area represents the footprint from its respective burner.
- the burner 310 is shown having the disposition of the fuel pipe 318 at the interior 316 of the gas pipe 312 .
- the offset of the fuel pipe 318 with respect to the gas pipe 312 is shown in FIG. 5B .
- the burner 410 is similar to the burner 110 diagram shown in FIGS. 2A and 2B .
- the fuel pipe 418 is introduced into the gas pipe 412 at an angle 48 such that the straight or linear portion of the gas pipe 412 and fuel pipe 418 are not parallel and are non-concentric.
- the offset of the fuel pipe 418 with respect to the gas pipe 412 is shown in FIG. 6B .
- FIGS. 7A and 7B disclose a plurality of fuel pipes 518 disposed in a gas pipe 512 .
- the plurality of fuel pipes 518 may be disposed as separate and discrete pipes or alternatively formed or arranged as a nested array or integral unit of fuel pipes, such as shown in FIG. 7B .
- the arrangement of the fuel pipes 518 in FIG. 7A are parallel with respect to each other and to the linear portion of the gas pipe 512 in which the fuel pipes 518 are disposed therein.
- the plurality of fuel pipes 518 and the gas pipe 512 can be formed as an integrated unit for being mounted in the burner block and subsequent rotation within the burner block to control the flame footprint area 562 at the melt in the furnace.
- the offset of the fuel pipes 518 with respect to the gas pipes 512 is shown in FIG. 7B .
- the array of fuel pipes 518 may share a common threaded portion 531 to releasably connect the fuel pipes 518 to a source of fuel.
- FIGS. 8A and 8B there is shown a fuel pipe 631 disposed in concentrically arranged gas pipes. That is, a primary outer gas pipe 612 has an interior sized and shaped to receive a secondary inner gas pipe 50 therein.
- the inner gas pipe 50 has an interior 52 sized and shaped to receive the fuel pipe 618 therein.
- the inner gas pipe 50 has an inlet 54 in registration with the inlet 642 of the outer gas pipe 612 so that the fuel pipe 618 can be inserted into the inner gas pipe 50 .
- the inner gas pipe 50 and fuel pipe 618 have a common longitudinal axis 646 along a back portion of each and are therefore concentric.
- FIG. 8B The orientation of the fuel pipe 618 and the gas pipes 612 , 50 is also shown in FIG. 8B .
- the burner 610 of FIG. 8A may be formed as an integral unit for being mounted in the burner block of the furnace.
- the offset of the fuel pipe 618 with respect to the gas pipes 612 , 50 is shown in FIG. 8B .
- FIG. 9 there is shown a portion of a crown 56 of a furnace 57 in which a burner block 58 is mounted.
- the burner 10 of FIG. 1A is disposed within the burner block 58 .
- the burners 10 , etc. are adapted to move in the direction of arrows 66 , 68 . With respect to the arrow 66 , the burner 10 can be moved into a select position depending upon the amount of combustion that is desired to occur in the burner block 58 .
- the distal ends of the fuel pipe 18 or pipes and gas pipe 12 or pipes terminate within the burner block 58 as shown, otherwise heat of the furnace atmosphere would melt the pipes if such were exposed from the burner block 58 .
- Positioning the burner 10 in the burner block 58 effects combustion in the block 58 , which in turn impacts the momentum and thrust of the flame provided by the burner 10 .
- a higher momentum flame produces a smaller footprint 62 area, while a lower momentum flame produces a larger footprint 62 area.
- There is a lower oxidant concentration at area 70 as the gaseous fuel, for example, burns it uses up the oxidant and tends to seek area 72 where there is a higher concentration of oxidant to burn.
- a rich flame is provided from the burner at a distal end of the burner where the fuel pipe is closest to the sidewall of the gas pipe.
- An oxidized lean flame is provided from the distal end of the burner where the fuel pipe is further away from the side wall of gas pipe.
- the latter provides an increased or more expanded oxygen zone for combustion, thereby providing a relatively oblong shape, as opposed to a circular shape, in the burn area 62 or footprint of the flame impacting the melt of the furnace. See also FIG. 4
- the non-circular footprints shown in FIG. 4 may also be provided by any one or combinations of the embodiments of the burners of the Figures.
- the burners of the present invention may be used for glass melting, refining, and distribution.
- the discharge point of the fuel pipes are not concentric to the oxygen pipes, but staggered or off-set. This off-set and/or rotation of the burners enables the direction of the flame to be changed as well as the resulting flame footprint.
- the degree or amount of staggering or off-set will increase the amount of flame direction that can be achieved.
- the off-set can be further accentuated by angling the fuel conduit relative to the oxygen conduit.
- the gas and fuel pipes have a circular cross-section, however the burner design may include gas and fuel pipes having different cross-sectional shapes, including but not limited to, elliptical, square, triangular, hex, etc.
- the fuel pipe can have a different cross-sectional shape than the gas pipe. Multiple or staged pipes can be utilized as well.
- the arrows 66 , 68 are with respect to all burner 10 , etc. embodiments of the invention as such can be rotated in the block 58 . Such rotation can occur by the individual components of the gas pipes and fuel pipes, or by the integral units formed of a gas pipe or pipes and fuel pipe or pipes.
- the fuel reacts with the oxidant.
- This staging will also provide the benefit of lower oxides of nitrogen (NOx) and increase heat transfer.
- NOx oxides of nitrogen
- the staging lowers the amount of pre-combustion in the burner block 58 and reduces the momentum of the flame emerging from the burner block. Whilst the flame is turbulent the lower momentum flame will reduce the velocity on the batch surface and reduce volatilization of batch components including but not limited to boron and lead.
- the lower momentum of the flame with respect to a furnace increases the residence time of the carbon in fuel and increases luminosity and heat transfer by radiation through sooting.
- the primary benefit of this invention is that the off-set of the gas and fuel pipes 12 , 18 , respectively, and hence the gas and fuel flows, delays the mixing of the gaseous fuel and gaseous oxidant until the flame hits the raw batch surface 64 .
- the excess oxygen from the lean portion of the flame continues in its primary direction away from the remaining fuel components.
- the resulting flame footprint 62 or burn area is non-circular as shown in FIGS. 4 and 9 .
- the non-circular flame burn area enables more energy to be directed into the melting area.
- the lower momentum of the flame with respect to a forehearth or distributor for a furnace provides for the flame not to impact a surface of the melt, but rather to “curl” or alter direction to become substantially parallel to a surface of the melt.
- FIGS. 10-16 disclose other embodiments of the non-centric oxy-fuel burner for a furnace or a forehearth of a furnace.
- the burner 700 includes an oxidant delivery pipe 702 and a fuel delivery pipe 704 (also referred to as a fuel pipe 704 ).
- the oxidant delivery pipe 702 is constructed, in this embodiment, as having a “T-shape”, wherein an end 706 of the oxidant pipe 702 shown in FIG. 10 is threaded for releasably connecting the pipe 702 to a remote source of oxidant (not shown).
- the oxidant used may be similar to that used with the embodiments of FIGS. 1-9 .
- the oxidant pipe 702 branches at 708 to provide a receptor portion 710 into which the fuel delivery pipe 704 is inserted along an interior 712 of the oxidant pipe 702 .
- An end 714 of the fuel pipe 704 is also threaded for releasable connection to a remote fuel source (not shown).
- the fuel used may be similar to that used with the embodiments of FIGS. 1-9 .
- a portion of the fuel pipe 704 is curved or angled upstream of a flange assembly (discussed below) and prior to insertion into and along the interior 712 of the oxidant pipe 702 as shown in FIG. 10 .
- a central longitudinal axis 716 of the oxidant pipe 702 and a central longitudinal axis 718 of the fuel pipe 704 , while parallel, are offset with respect to each other. That is, as shown in FIG. 10 and by way of example, the fuel pipe 704 is disposed within the oxidant pipe 702 such that there respective longitudinal axis are offset, non-centric, from each other. Spacers 720 are connected, by welding for example, to an exterior surface of the fuel pipe 704 to extend at the interior 712 of the oxidant pipe 702 to provide support for and alignment of the fuel pipe 704 for being disposed offset within the oxidant delivery pipe.
- the longitudinal axis 716 of the oxidant pipe 702 extends through the center of each of the movable flange 722 and the fixed flange 730 .
- the longitudinal axis 718 of the fuel pipe 704 is offset or non-centric with respect to the longitudinal axis 716 , due to the spacers 720 .
- a flange assembly is shown for use with the oxidant pipe 702 and the fuel pipe 704 .
- the flange assembly includes a moveable fuel-side flange 722 attached to an exterior 724 of the fuel pipe.
- the flange 722 has a plurality of holes 726 therethrough and through which mechanical fasteners 728 , such as for example nuts and bolts, may be disposed for releasably securing the flange 722 as will be discussed below.
- Rotation of the fuel pipe 704 about the longitudinal axis 716 of the oxidant pipe 702 causes the fuel side flange 722 to rotate concurrently with the rotation of the fuel pipe.
- the fuel pipe 704 is off-set or non-centric, i.e. not at a center of the fuel-side flange 722 , when the fuel flange is released and rotated the flange 722 and fuel pipe 704 rotate around the longitudinal axis 716 of the oxidant pipe 702 , which longitudinal axis 716 is at a center of both the fuel-side flange 722 and the oxidant-side flange 730 . This is shown further with respect to FIGS. 11A-11C and 12 A- 12 C.
- the oxidant pipe 702 is provided with a fixed oxidant-side flange 730 , part of the flange assembly, mounted to the oxidant pipe.
- the fixed flange 730 has a plurality of holes 732 therethrough corresponding in number to that of the plurality of holes 726 of the fuel-side moveable flange 722 .
- the holes 732 of the fixed flange 730 are also constructed and arranged to receive the mechanical fasteners 728 therein.
- the mechanical fasteners 728 function as a fastener assembly to releasably secure the flanges 722 , 730 to each other.
- a portion of the burner 700 is mounted to a burner block 734 as shown in FIG. 10 .
- the burner block 734 includes a burner block housing 736 , and has space 738 therein in which the oxidant pipe 702 can be disposed, as shown in FIG. 10 .
- the housing 736 for the burner block 734 includes at least one mechanical fastener 746 , such as a set screw, to secure the housing 736 to the burner block 734 .
- a stop collar 740 with a mechanical fastener 742 such as a screw, is secured to the oxidant pipe 702 , thereby preventing the oxidant pipe from slipping downwards out of position into the burner block 734 .
- the burner block 734 itself is mounted to a sleeve 744 , which sleeve is disposed in the crown (not shown) of the furnace or forehearth of the furnace.
- a bushing 748 or adaptor collar is disposed about an exterior surface 750 of the oxidant pipe 702 between the burner block housing 736 and said surface 750 .
- the bushing 748 is also provided with a mechanical fastener 752 to releasably secure the burner 700 into place with respect to the burner block housing 736 .
- a mechanical fastener 754 is provided at the burner block housing 736 to releasably secure the burner block housing to the bushing 748 .
- the respective ends of the oxidant pipe 702 and the fuel pipe 704 are recessed within the burner block 734 so as not to be directly in contact with the furnace atmosphere.
- the mechanical fasteners 728 , 742 , 752 , 754 and 746 are releasably engagable in order to permit the burner 700 in its entirety to be rotated within the burner block 734 and the sleeve 744 .
- the fixed oxidant-side flange 730 is affixed, such as by welding, to the burner 700 .
- the fuel pipe 704 can be rotated with respect to the oxidant pipe 702 , while the oxidant pipe can be rotated with respect to the burner block 734 , as will be discussed below.
- FIGS. 11A-11C and 12 A- 12 C such show the orientation of the fuel pipe 704 with respect to the oxidant pipe 702 as provided for by both the movable fuel-side flange 722 and the fixed oxidant-side flange 730 .
- the mechanical fasteners 728 can be released, thereby permitting the fuel pipe 704 to be rotated about the longitudinal axis 716 of the oxidant pipe 702 with the fuel-side flange 722 moving concurrent with the fuel pipe, and circumscribing the central longitudinal axis 716 of the oxidant pipe 702 , as show in FIGS. 12A-12C .
- a desired position such as represented by, for example, that of FIG.
- the respective holes 726 , 732 at each of the flanges 722 , 730 are moved into registration with each other and the mechanical fasteners 728 engaged or actuated to secure flange 722 of the fuel pipe 704 with respect to the flange 730 of the oxidant pipe 702 .
- the range of rotation afforded the fuel pipe 704 and different positions said pipe can have with respect to the oxidant pipe 702 is only limited by the number of corresponding holes 726 , 732 provided in the flanges 722 , 730 .
- FIGS. 12A-12C show the manner by which they retain the fuel pipe in the offset or non-centric position with respect to the oxidant pipe 702 .
- a sealing arrangement between the moveable fuel-side flange 722 and the fixed oxidant-side flange 730 which includes a seal 756 , such as for example an O-ring, mounted at an indent 758 formed in the fixed oxidant-side flange 730 for coaction with a corresponding portion of the moveable fuel-side flange 722 .
- the indent 758 “seats” the seal 756 in position for contacting the fuel-side flange 722 .
- the seal 756 effectively seals off any leaks which could occur in view of the releasable engagement of the flanges 722 , 730 with respect to each other.
- FIG. 16 another embodiment of a burner is shown generally at 800 .
- a fuel delivery pipe 804 has a straight shape upstream of the flange assembly, as opposed to the curved or angled portion of the embodiment shown in FIG. 10 , prior to entry into the oxidant delivery pipe 802 . All other features and functions are similar to that which was described with respect to the embodiment of FIG. 10 .
- Still another embodiment of a burner having features similar to that which are provided shown in FIGS. 10 and 16 would include the fuel delivery pipe 704 , 804 being angled such as that shown with respect to the embodiment of FIGS. 2A-2B and in FIGS. 3A-3B . That is, the fuel delivery pipe 704 , 804 would be neither parallel to nor concentric with the oxidant delivery pipe 802 , 804 . All other features and functions thereof would otherwise be similar to that which was discussed above with respect to the embodiments of FIGS. 10 and 16 .
- gaseous fuel and gaseous oxidant used with the embodiments of FIGS. 10-16 is similar to that used with the embodiments of FIGS. 1-9 .
- the ends of the fuel and oxidant pipes can have other than threaded ends for connection to fuel and oxidant sources.
- such ends may have connecting flanges, clamps or welds to connect the pipes to such fuel and oxidant sources.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Pre-Mixing And Non-Premixing Gas Burner (AREA)
- Glass Melting And Manufacturing (AREA)
- Combustion Of Fluid Fuel (AREA)
- Gas Burners (AREA)
Abstract
A burner for use in a combustion chamber of a furnace or a forehearth includes a gas delivery member for delivering a gaseous oxidant, a fuel delivery member for delivering a fuel and having a portion disposed at an interior of the gas delivery member and offset from a longitudinal axis of the gas delivery member, and a flange assembly mechanically associated with the gas and fuel delivery members, the flange assembly adapted for rotational movement to releasably secure the gas and fuel delivery members with respect to each other to provide a flame footprint at a select location in the combustion chamber.
Description
- The invention relates to burners for furnaces and furnace systems.
- Conical concentric oxy-fuel burners have been used in the crown of glass melting furnaces to melt batch in the furnaces. Once a pre-positioned hole is drilled in the furnace crown and a burner block is installed in the hole, there is limited if no ability to change the direction of the turbulent flame being emitted from the burner. If a different direction is required for the flame, it is required to drill and install an alternate (different) burner hole in order to re-position the burner and hence the flame. Existing furnace designs, with their steelwork and crown expansion joints, frequently limit the location that burners can be installed in the furnace and as a result optimum flame coverage is not always achieved or blocks are angled excessively so that the burner flame is less effective. Concentric oxy-fuel burners produce conical flames perpendicular to the melt which in turn produce circular flame patterns at the melt. The resulting flame pattern produced by a plurality of spaced apart burners limits the total flame coverage at the surface of the melt. Concentric burners combust uniformly in the combustion space above the melt. This uniformity and intensity of combustion can provide excessive combustion in the free space between the crown and the melt resulting in less than optimum heat transfer and higher oxides of nitrogen (NOx) at the melt surface. The aforementioned limitations and disadvantages occur also with horizontal burners and burners used in forehearths of furnaces.
- A burner such as an oxy-fuel burner is provided for a furnace or a forehearth, and which includes a gas delivery member, and a fuel delivery member having a portion disposed at an interior of the gas delivery member and offset from a longitudinal axis of the gas delivery member.
- There is also provided a method for combusting product in a furnace or a forehearth, comprising providing a flow of gaseous oxidant along a first flow path to the furnace or the forehearth; providing a flow of gaseous fuel along a second flow path offset from the first flow path to the furnace or the forehearth; exposing the first flow path to the second flowpath; and combusting the gaseous oxidant and the gaseous fuel to provide a non-circular burn area.
- There is also provided a burner, whereby one or more of the gas and fuel delivery members may be rotated along their respective longitudinal axes to control an angle of discharge of the burner flame and the resulting non-circular burn area.
- There is further provided a flange assembly for orienting the gas delivery member and the fuel delivery member with respect to each other, and securing the members in a fixed position with respect to each other.
- For a more complete understanding of the present invention, reference may be had to the following Figures, taken in conjunction with the detailed description, of which:
-
FIG. 1A discloses a partial cross-sectional plan view of a burner of the present invention for use with a furnace. -
FIG. 1B discloses a cross-section of the burner taken alongline 1B-1B ofFIG. 1A . -
FIG. 2A discloses a diagram of another embodiment of a burner of the present invention. -
FIG. 2B discloses a cross-section diagram taken alongline 2B-2B ofFIG. 2A . -
FIG. 3A discloses a diagram of another embodiment of a burner of the present invention. -
FIG. 3B discloses a cross-section diagram taken alongline 3B-3B ofFIG. 3A . -
FIG. 4 discloses a flame footprint provided by the burners of the present invention. -
FIG. 5A discloses a diagram of another embodiment of a burner of the present invention. -
FIG. 5B discloses a cross-section diagram taken alongline 5B-5B ofFIG. 5A . -
FIG. 6A discloses a partial cross-sectional plan view of another embodiment of the burner of the present invention for use with a furnace. -
FIG. 6B discloses a cross-section of the burner taken alongline 6B-6B ofFIG. 6A . -
FIG. 7A discloses a partial cross-sectional plan view of still another embodiment of the burner of the present invention for use with a furnace. -
FIG. 7B discloses a cross-section of the burner taken along line 7B-7B ofFIG. 7A . -
FIG. 8A discloses a partial cross-sectional plan view of another embodiment of the burner of the present invention for use with a furnace. -
FIG. 8B discloses a cross-section of the burner taken alongline 8B-8B ofFIG. 8A . -
FIG. 9 discloses a partial cross-sectional plan view of a burner of the present invention mounted in a burner block of a furnace. -
FIG. 10 discloses a partial cross-sectional plan view of another burner embodiment for use with a furnace. -
FIG. 11A discloses a view taken alongline 11A-11A ofFIG. 10 . -
FIGS. 11B and 11C show schematic views of elements ofFIG. 11A arranged in different positions. -
FIGS. 12A-12C show schematic views corresponding to that ofFIGS. 11A-11C , respectively. -
FIGS. 13-15 show components of a flange assembly for the burner embodiments ofFIGS. 10 and 16 . -
FIG. 16 shows a partial cross-sectional plan view of another burner embodiment for use with a furnace. - Referring to
FIGS. 1A and 1B , there is shown aburner 10 of the present invention for use with a furnace, such as for example an oxy-fuel glass melting furnace or a forehearth of the furnace. Reference to use of the burner with a furnace also includes use of the burner with forehearth. Theburner 10 consists of agas pipe 12 or conduit, for delivering gaseous oxygen for example, having anexterior sidewall 14 constructed and arranged for disposition in a burner block of a furnace. The gas provided to and delivered in thegas pipe 12 is a gaseous oxidant such as for example gaseous oxygen at a purity level of 85%-100%; where less than 100% oxygen, the balance may be nitrogen and/or other noble gases, and combinations thereof. Aninternal space 16 of thegas pipe 12 is of sufficient size and shape to receive afuel pipe 18 or conduit disposed therein. Thefuel pipe 18 has anexterior side wall 20 andinternal space 22. - The
gas pipe 12, or oxidant pipe for example, is bent thereby providing anelbow 24 in thegas pipe 12. Thepipe 12 is in fluid communication with a gas supply (not shown). A threadedexterior end 26 of thegas pipe 12 provides for releasable connection to the gas supply. An opposite ordistal end 28 of thegas pipe 12 terminates in a burner block of the furnace (not shown) and is disposed at a select position above product melt in the furnace. Gaseous oxidant provided may be a single type of oxidant, such as for example oxygen, or selected from a composition of gases as well. - The interior 16 of the
gas pipe 12 is sized and shaped to receive thefuel pipe 18 to be disposed therein, as shown inFIGS. 1A and 1 b. Thefuel pipe 18 is constructed of a material conducive to being exposed to the oxidant in thegas pipe 12. Thefuel pipe 18 has an end orproximal end 30 extending from proximate theelbow 24 of thegas pipe 12, while an opposed ordistal end 32 of thefuel pipe 18 terminates at approximately the same position as theend 28 of thegas pipe 12. Thegas pipe 12 andfuel pipe 18 may terminate at the same location. Thefuel pipe 18 is in fluid communication with a supply of gaseous fuel, such as for example natural gas, propane, liquid petroleum gas (LPG), synthetic gas (derived from organic solid, liquid and or gaseous sources, or combinations thereof), and combinations thereof. The fuel used may consist of a single gaseous fuel or a composition of fuels. Theend 30 of thefuel pipe 18 projecting from thegas pipe 12 may also be threaded 31 for releasable connection to a source (not shown) of gaseous fuel. - Spacing or
support members fuel pipe 18 within thegas pipe 12 and provide the spaced relation therebetween without interrupting the flow of gas through thegas pipe 12. A weld or seal 40 is provided to seal the circumference of aninlet 42 in thegas pipe 12 through which thefuel pipe 18 is inserted. - Referring also to
FIG. 1B , the disposition of thefuel pipe 18 at the interior 16 of thegas pipe 12 is more clearly shown. Thegas pipe 12 andfuel pipe 18 are substantially parallel to each other from a point where thegas pipe 12 transits from theelbow 24 to a linear arrangement. It can be seen however that the disposition of thefuel pipe 18 within thegas pipe 12 is non-concentric; i.e., thegas pipe 12 and thefuel pipe 18 do not share a common longitudinal axis. Rather, alongitudinal axis 44 of thegas pipe 12 is offset with respect to alongitudinal axis 46 of thefuel pipe 18, as will be further discussed below, to provide a burner flame and flame footprint area for the particular furnace and product to be melted within the furnace. The burner can be adjusted to alter the flame footprint. This is accomplished because the gas pipe and fuel pipe are adapted, such as by construction and arrangement of their components, to be rotated about their respectivelongitudinal axes - The
burner 10 ofFIGS. 1A and 1B may also be constructed as an integral unit, thereby permitting rotation of the combined gas pipe and fuel pipe unit in the burner block to selectively control the disposition of the flame footprint area being emitted from theburner 10 into the furnace. - Other exemplary embodiments of a burner constructed in accordance with the present invention are illustrated in
FIGS. 2A , 2B; 3A, 3B; 6A, 5B; 7A, 7B; and 8A, 8B, respectively. Elements illustrated in those Figures which correspond to the elements described above with respect toFIGS. 1A , 1B have been designated by corresponding reference numerals increased by one hundred, two hundred, three hundred, four hundred, etc., respectively. -
FIGS. 2A and 2B show schematics of another embodiment of theburner 110 ofFIGS. 1A , 1B. InFIGS. 2A and 2B , thefuel pipe 118 is disposed in thegas pipe 112 in an angled relationship, i.e. not parallel, such that the flame emitted from the burner into the furnace also provides a non-circular footprint at the melt in the furnace. Theburner 110 may have thegas pipe 112 andfuel pipe 118 formed as an integral unit, whereby rotation of the unit as represented byarrow 60 can occur to provide the flame footprint at select positions on the melt within the furnace. Rotation of the burner unit can be done through 360°.FIG. 2A shows the gaseous oxidant flow, for example, and gaseous fuel flow to the furnace. - The
fuel pipe 218 may also be angled sufficiently in thegas pipe 212 such that adistal end 232 of the fuel pipe contacts adistal end 228 of thegas pipe 212. Such an arrangement is shown inFIGS. 3A and 3B . - In
FIG. 4 there is represented a plurality offlame footprints 62 that are provided by the burner 10 (110, 210, etc.) embodiments in the Figures. Eachnon-circular footprint 62 or burn area represents the footprint from its respective burner. - Referring to
FIGS. 5A and 5B , theburner 310 is shown having the disposition of thefuel pipe 318 at theinterior 316 of thegas pipe 312. The offset of thefuel pipe 318 with respect to thegas pipe 312 is shown inFIG. 5B . - In
FIGS. 6A and 6B , theburner 410 is similar to theburner 110 diagram shown inFIGS. 2A and 2B . In particular, thefuel pipe 418 is introduced into thegas pipe 412 at anangle 48 such that the straight or linear portion of thegas pipe 412 andfuel pipe 418 are not parallel and are non-concentric. The offset of thefuel pipe 418 with respect to thegas pipe 412 is shown inFIG. 6B . -
FIGS. 7A and 7B disclose a plurality offuel pipes 518 disposed in agas pipe 512. The plurality offuel pipes 518 may be disposed as separate and discrete pipes or alternatively formed or arranged as a nested array or integral unit of fuel pipes, such as shown inFIG. 7B . The arrangement of thefuel pipes 518 inFIG. 7A are parallel with respect to each other and to the linear portion of thegas pipe 512 in which thefuel pipes 518 are disposed therein. As with other embodiments of the invention, the plurality offuel pipes 518 and thegas pipe 512 can be formed as an integrated unit for being mounted in the burner block and subsequent rotation within the burner block to control the flame footprint area 562 at the melt in the furnace. The offset of thefuel pipes 518 with respect to thegas pipes 512 is shown inFIG. 7B . The array offuel pipes 518 may share a common threadedportion 531 to releasably connect thefuel pipes 518 to a source of fuel. - In
FIGS. 8A and 8B , there is shown afuel pipe 631 disposed in concentrically arranged gas pipes. That is, a primaryouter gas pipe 612 has an interior sized and shaped to receive a secondaryinner gas pipe 50 therein. Theinner gas pipe 50 has an interior 52 sized and shaped to receive thefuel pipe 618 therein. Theinner gas pipe 50 has aninlet 54 in registration with theinlet 642 of theouter gas pipe 612 so that thefuel pipe 618 can be inserted into theinner gas pipe 50. InFIGS. 8A , 8B, theinner gas pipe 50 andfuel pipe 618 have a commonlongitudinal axis 646 along a back portion of each and are therefore concentric. The orientation of thefuel pipe 618 and thegas pipes FIG. 8B . As with other embodiments of the present invention, theburner 610 ofFIG. 8A may be formed as an integral unit for being mounted in the burner block of the furnace. The offset of thefuel pipe 618 with respect to thegas pipes FIG. 8B . - Referring to
FIG. 9 , there is shown a portion of acrown 56 of afurnace 57 in which aburner block 58 is mounted. Theburner 10 ofFIG. 1A is disposed within theburner block 58. It should be understood that other embodiments of the burner (110, 210, 310, 410, 510, 610) disclosed herein may be mounted in theburner block 58 as well. Theburners 10, etc. are adapted to move in the direction ofarrows arrow 66, theburner 10 can be moved into a select position depending upon the amount of combustion that is desired to occur in theburner block 58. The distal ends of thefuel pipe 18 or pipes andgas pipe 12 or pipes terminate within theburner block 58 as shown, otherwise heat of the furnace atmosphere would melt the pipes if such were exposed from theburner block 58. Positioning theburner 10 in theburner block 58 effects combustion in theblock 58, which in turn impacts the momentum and thrust of the flame provided by theburner 10. A higher momentum flame produces asmaller footprint 62 area, while a lower momentum flame produces alarger footprint 62 area. There is a lower oxidant concentration atarea 70, as the gaseous fuel, for example, burns it uses up the oxidant and tends to seekarea 72 where there is a higher concentration of oxidant to burn. - As shown in
FIG. 9 , a rich flame is provided from the burner at a distal end of the burner where the fuel pipe is closest to the sidewall of the gas pipe. An oxidized lean flame is provided from the distal end of the burner where the fuel pipe is further away from the side wall of gas pipe. The latter provides an increased or more expanded oxygen zone for combustion, thereby providing a relatively oblong shape, as opposed to a circular shape, in theburn area 62 or footprint of the flame impacting the melt of the furnace. See alsoFIG. 4 - The non-circular footprints shown in
FIG. 4 may also be provided by any one or combinations of the embodiments of the burners of the Figures. - The burners of the present invention may be used for glass melting, refining, and distribution. The discharge point of the fuel pipes are not concentric to the oxygen pipes, but staggered or off-set. This off-set and/or rotation of the burners enables the direction of the flame to be changed as well as the resulting flame footprint. The degree or amount of staggering or off-set will increase the amount of flame direction that can be achieved. The off-set can be further accentuated by angling the fuel conduit relative to the oxygen conduit. By way of example, the gas and fuel pipes have a circular cross-section, however the burner design may include gas and fuel pipes having different cross-sectional shapes, including but not limited to, elliptical, square, triangular, hex, etc. The fuel pipe can have a different cross-sectional shape than the gas pipe. Multiple or staged pipes can be utilized as well.
- The
arrows burner 10, etc. embodiments of the invention as such can be rotated in theblock 58. Such rotation can occur by the individual components of the gas pipes and fuel pipes, or by the integral units formed of a gas pipe or pipes and fuel pipe or pipes. - In the combustion process, the fuel reacts with the oxidant. By off-setting the
pipes burner block 58 and reduces the momentum of the flame emerging from the burner block. Whilst the flame is turbulent the lower momentum flame will reduce the velocity on the batch surface and reduce volatilization of batch components including but not limited to boron and lead. - The lower momentum of the flame with respect to a furnace increases the residence time of the carbon in fuel and increases luminosity and heat transfer by radiation through sooting. The primary benefit of this invention is that the off-set of the gas and
fuel pipes raw batch surface 64. The excess oxygen from the lean portion of the flame continues in its primary direction away from the remaining fuel components. The resultingflame footprint 62 or burn area is non-circular as shown inFIGS. 4 and 9 . The non-circular flame burn area enables more energy to be directed into the melting area. - The lower momentum of the flame with respect to a forehearth or distributor for a furnace provides for the flame not to impact a surface of the melt, but rather to “curl” or alter direction to become substantially parallel to a surface of the melt.
-
FIGS. 10-16 disclose other embodiments of the non-centric oxy-fuel burner for a furnace or a forehearth of a furnace. - Referring to
FIG. 10 , there is shown a burner generally at 700 for use in a furnace (not shown) or a forehearth (not shown) of the furnace. Theburner 700 includes anoxidant delivery pipe 702 and a fuel delivery pipe 704 (also referred to as a fuel pipe 704). Theoxidant delivery pipe 702 is constructed, in this embodiment, as having a “T-shape”, wherein anend 706 of theoxidant pipe 702 shown inFIG. 10 is threaded for releasably connecting thepipe 702 to a remote source of oxidant (not shown). The oxidant used may be similar to that used with the embodiments ofFIGS. 1-9 . In this embodiment, theoxidant pipe 702 branches at 708 to provide areceptor portion 710 into which thefuel delivery pipe 704 is inserted along an interior 712 of theoxidant pipe 702. Anend 714 of thefuel pipe 704 is also threaded for releasable connection to a remote fuel source (not shown). The fuel used may be similar to that used with the embodiments ofFIGS. 1-9 . A portion of thefuel pipe 704 is curved or angled upstream of a flange assembly (discussed below) and prior to insertion into and along theinterior 712 of theoxidant pipe 702 as shown inFIG. 10 . - A central
longitudinal axis 716 of theoxidant pipe 702 and a centrallongitudinal axis 718 of thefuel pipe 704, while parallel, are offset with respect to each other. That is, as shown inFIG. 10 and by way of example, thefuel pipe 704 is disposed within theoxidant pipe 702 such that there respective longitudinal axis are offset, non-centric, from each other.Spacers 720 are connected, by welding for example, to an exterior surface of thefuel pipe 704 to extend at theinterior 712 of theoxidant pipe 702 to provide support for and alignment of thefuel pipe 704 for being disposed offset within the oxidant delivery pipe. Accordingly, thelongitudinal axis 716 of theoxidant pipe 702 extends through the center of each of themovable flange 722 and the fixedflange 730. Thelongitudinal axis 718 of thefuel pipe 704 is offset or non-centric with respect to thelongitudinal axis 716, due to thespacers 720. - Referring also to
FIGS. 11A-11C , a flange assembly is shown for use with theoxidant pipe 702 and thefuel pipe 704. Referring to thefuel pipe 704, the flange assembly includes a moveable fuel-side flange 722 attached to anexterior 724 of the fuel pipe. Theflange 722 has a plurality ofholes 726 therethrough and through whichmechanical fasteners 728, such as for example nuts and bolts, may be disposed for releasably securing theflange 722 as will be discussed below. Rotation of thefuel pipe 704 about thelongitudinal axis 716 of theoxidant pipe 702 causes thefuel side flange 722 to rotate concurrently with the rotation of the fuel pipe. Since thefuel pipe 704 is off-set or non-centric, i.e. not at a center of the fuel-side flange 722, when the fuel flange is released and rotated theflange 722 andfuel pipe 704 rotate around thelongitudinal axis 716 of theoxidant pipe 702, whichlongitudinal axis 716 is at a center of both the fuel-side flange 722 and the oxidant-side flange 730. This is shown further with respect toFIGS. 11A-11C and 12A-12C. - Referring as well to
FIGS. 13-14 , theoxidant pipe 702 is provided with a fixed oxidant-side flange 730, part of the flange assembly, mounted to the oxidant pipe. The fixedflange 730 has a plurality ofholes 732 therethrough corresponding in number to that of the plurality ofholes 726 of the fuel-sidemoveable flange 722. Theholes 732 of the fixedflange 730 are also constructed and arranged to receive themechanical fasteners 728 therein. Themechanical fasteners 728 function as a fastener assembly to releasably secure theflanges - A portion of the
burner 700 is mounted to aburner block 734 as shown inFIG. 10 . Theburner block 734 includes aburner block housing 736, and hasspace 738 therein in which theoxidant pipe 702 can be disposed, as shown inFIG. 10 . Thehousing 736 for theburner block 734 includes at least onemechanical fastener 746, such as a set screw, to secure thehousing 736 to theburner block 734. Astop collar 740 with amechanical fastener 742 such as a screw, is secured to theoxidant pipe 702, thereby preventing the oxidant pipe from slipping downwards out of position into theburner block 734. - The
burner block 734 itself is mounted to asleeve 744, which sleeve is disposed in the crown (not shown) of the furnace or forehearth of the furnace. Abushing 748 or adaptor collar is disposed about anexterior surface 750 of theoxidant pipe 702 between theburner block housing 736 and saidsurface 750. Thebushing 748 is also provided with amechanical fastener 752 to releasably secure theburner 700 into place with respect to theburner block housing 736. Amechanical fastener 754 is provided at theburner block housing 736 to releasably secure the burner block housing to thebushing 748. - While the
sleeve 744 andburner block 734 are directly exposed to a combustion atmosphere of the furnace, the respective ends of theoxidant pipe 702 and thefuel pipe 704 are recessed within theburner block 734 so as not to be directly in contact with the furnace atmosphere. - The
mechanical fasteners burner 700 in its entirety to be rotated within theburner block 734 and thesleeve 744. - The fixed oxidant-
side flange 730 is affixed, such as by welding, to theburner 700. Thefuel pipe 704 can be rotated with respect to theoxidant pipe 702, while the oxidant pipe can be rotated with respect to theburner block 734, as will be discussed below. - Referring to
FIGS. 11A-11C and 12A-12C, such show the orientation of thefuel pipe 704 with respect to theoxidant pipe 702 as provided for by both the movable fuel-side flange 722 and the fixed oxidant-side flange 730. Themechanical fasteners 728 can be released, thereby permitting thefuel pipe 704 to be rotated about thelongitudinal axis 716 of theoxidant pipe 702 with the fuel-side flange 722 moving concurrent with the fuel pipe, and circumscribing the centrallongitudinal axis 716 of theoxidant pipe 702, as show inFIGS. 12A-12C . When thefuel pipe 704 has been rotated to a desired position, such as represented by, for example, that ofFIG. 11B or 11C, therespective holes flanges mechanical fasteners 728 engaged or actuated to secureflange 722 of thefuel pipe 704 with respect to theflange 730 of theoxidant pipe 702. The range of rotation afforded thefuel pipe 704 and different positions said pipe can have with respect to theoxidant pipe 702 is only limited by the number ofcorresponding holes flanges flanges fuel pipe 704 can have with respect to theoxidant pipe 702. Thespacers 720 are connected to or may extend from theexterior surface 724 of thefuel pipe 704 and accordingly,FIGS. 12A-12C show the manner by which they retain the fuel pipe in the offset or non-centric position with respect to theoxidant pipe 702. - Referring also to
FIGS. 13-15 , a sealing arrangement between the moveable fuel-side flange 722 and the fixed oxidant-side flange 730 is shown which includes aseal 756, such as for example an O-ring, mounted at anindent 758 formed in the fixed oxidant-side flange 730 for coaction with a corresponding portion of the moveable fuel-side flange 722. Theindent 758 “seats” theseal 756 in position for contacting the fuel-side flange 722. Theseal 756 effectively seals off any leaks which could occur in view of the releasable engagement of theflanges - In
FIG. 16 , another embodiment of a burner is shown generally at 800. The only difference between the embodiment ofFIG. 16 from that ofFIG. 10 is that afuel delivery pipe 804 has a straight shape upstream of the flange assembly, as opposed to the curved or angled portion of the embodiment shown inFIG. 10 , prior to entry into theoxidant delivery pipe 802. All other features and functions are similar to that which was described with respect to the embodiment ofFIG. 10 . - Still another embodiment of a burner having features similar to that which are provided shown in
FIGS. 10 and 16 , would include thefuel delivery pipe FIGS. 2A-2B and inFIGS. 3A-3B . That is, thefuel delivery pipe oxidant delivery pipe FIGS. 10 and 16 . - The gaseous fuel and gaseous oxidant used with the embodiments of
FIGS. 10-16 is similar to that used with the embodiments ofFIGS. 1-9 . - For all of the embodiments discussed above with respect to
FIGS. 1-16 , the ends of the fuel and oxidant pipes can have other than threaded ends for connection to fuel and oxidant sources. For example, such ends may have connecting flanges, clamps or welds to connect the pipes to such fuel and oxidant sources. - It will be understood that the embodiments described herein are merely exemplary, and that a person skilled in the art may make many variations and modifications without departing from the spirit and scope of the invention. All such variations and modifications are intended to be included within the scope of the claims as described herein. It should be understood that embodiments described above are not only in the alternative, but may also be combined.
Claims (18)
1. A burner for use in a combustion chamber of a furnace or a forehearth, comprising a gas delivery member for delivering a gaseous oxidant, a fuel delivery member for delivering a fuel and having a portion disposed at an interior of the gas delivery member and offset from a longitudinal axis of the gas delivery member, and a flange assembly mechanically associated with the gas and fuel delivery members, the flange assembly adapted for rotational movement to releasably secure the gas and fuel delivery members with respect to each other to provide a flame footprint at a select location in the combustion chamber.
2. The burner of claim 1 , wherein a portion of the gas delivery member and the portion of the fuel delivery member are parallel with each other.
3. The burner of claim 1 , wherein the portion of the fuel delivery member is disposed at an angle at the interior of the gas delivery member.
4. The burner of claim 1 , wherein only the fuel delivery member is rotatable at the flange assembly.
5. The burner of claim 1 , wherein the gas delivery member comprises a gas pipe.
6. The burner of claim 1 , wherein the fuel delivery member comprises a fuel pipe.
7. The burner of claim 1 , wherein the fuel delivery member comprises a plurality of fuel pipes.
8. The burner of claim 7 , wherein the plurality of fuel pipes are an integral unit.
9. The burner of claim 7 , wherein the plurality of fuel pipes are disposed at an angle at the interior of the gas delivery member.
10. The burner of claim 1 , further comprising at least one support member disposed in the gas delivery member to support the fuel delivery member in spaced relation with respect to the gas delivery member and offset from the longitudinal axis of the gas delivery member during the rotational movement to releasably secure the gas and fuel delivery members.
11. The burner of claim 1 , wherein the flange assembly comprises a first flange mounted to the gas delivery member, the first flange having a first plurality of holes therethrough; a second flange mounted to the fuel delivery member, the second flange having a second plurality of holes therethrough; the first plurality of holes in the first flange and the second plurality of holes in the second flange arranged for being in registration with each other upon rotational movement of the first and second flanges to a select position with respect to each other; and a fastener assembly to releasably secure the first and second flanges to each other at the select position.
12. The burner of claim 11 , wherein the second flange is fixed to the fuel delivery member for rotation therewith.
13. The burner of claim 12 , wherein the fuel delivery member is rotatable to circumscribe a path around a central longitudinal axis of the gas delivery member.
14. The burner of claim 11 , further comprising a seal mounted to at least one of the first flange or the second flange for providing sealing engagement of the first and second flanges.
15. The burner of claim 11 , further comprising a collar mounted to an exterior surface of the gas delivery member, the collar having a mechanical fastener associated therewith for releasably securing the collar to the exterior surface of the gas delivery member for preventing the gas delivery member from moving into the furnace or the forehearth.
16. The burner of claim 1 , wherein the fuel delivery member comprises an angled portion upstream of the flange assembly.
17. The burner of claim 1 , wherein the gaseous oxidant is selected from the group consisting of oxygen, oxygen and nitrogen, oxygen and other noble gases, and combinations thereof; and the fuel is selected from the group consisting of natural gas, propane, liquid petroleum gas, synthetic gas, and combinations thereof.
18. The burner of claim 11 , wherein the fastener assembly comprises mechanical fasteners for coacting with the first and second flanges.
Priority Applications (16)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/651,506 US20100159409A1 (en) | 2006-06-05 | 2010-01-04 | Non-centric oxy-fuel burner for glass melting systems |
MYPI2012003017A MY166569A (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
BR112012016443A BR112012016443A2 (en) | 2010-01-04 | 2010-12-22 | Uncentrated Oxygen and Fuel Burner for Glass Fusion Systems |
KR1020127020417A KR101838761B1 (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
CN201080060479.8A CN102713434B (en) | 2010-01-04 | 2010-12-22 | For the oxy-fuel burners of the non-centering of glass melting systems |
UAA201209493A UA110469C2 (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
PT108415910T PT2521881T (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
ES10841591.0T ES2671058T3 (en) | 2010-01-04 | 2010-12-22 | Non-centralized oxygen-fuel burner for glass smelting systems |
EP10841591.0A EP2521881B1 (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
RU2012133451/06A RU2577682C2 (en) | 2010-01-04 | 2010-12-22 | Non-central powder burner for glass melting system |
PL10841591T PL2521881T3 (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
PCT/US2010/061785 WO2011082062A1 (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
TR2018/07129T TR201807129T4 (en) | 2010-01-04 | 2010-12-22 | Decentralized oxygen fuel burner for glass melting systems. |
CA2785792A CA2785792A1 (en) | 2010-01-04 | 2010-12-22 | Non-centric oxy-fuel burner for glass melting systems |
JP2012548029A JP5756126B2 (en) | 2010-01-04 | 2010-12-22 | Non-coaxial oxygen burner for glass melting systems |
ZA2012/04973A ZA201204973B (en) | 2010-01-04 | 2012-07-03 | Non-centric oxy-fuel burner for glass melting systems |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/446,738 US20070281264A1 (en) | 2006-06-05 | 2006-06-05 | Non-centric oxy-fuel burner for glass melting systems |
US12/651,506 US20100159409A1 (en) | 2006-06-05 | 2010-01-04 | Non-centric oxy-fuel burner for glass melting systems |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/446,738 Continuation-In-Part US20070281264A1 (en) | 2006-06-05 | 2006-06-05 | Non-centric oxy-fuel burner for glass melting systems |
Publications (1)
Publication Number | Publication Date |
---|---|
US20100159409A1 true US20100159409A1 (en) | 2010-06-24 |
Family
ID=44226773
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US12/651,506 Abandoned US20100159409A1 (en) | 2006-06-05 | 2010-01-04 | Non-centric oxy-fuel burner for glass melting systems |
Country Status (16)
Country | Link |
---|---|
US (1) | US20100159409A1 (en) |
EP (1) | EP2521881B1 (en) |
JP (1) | JP5756126B2 (en) |
KR (1) | KR101838761B1 (en) |
CN (1) | CN102713434B (en) |
BR (1) | BR112012016443A2 (en) |
CA (1) | CA2785792A1 (en) |
ES (1) | ES2671058T3 (en) |
MY (1) | MY166569A (en) |
PL (1) | PL2521881T3 (en) |
PT (1) | PT2521881T (en) |
RU (1) | RU2577682C2 (en) |
TR (1) | TR201807129T4 (en) |
UA (1) | UA110469C2 (en) |
WO (1) | WO2011082062A1 (en) |
ZA (1) | ZA201204973B (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120037054A1 (en) * | 2009-04-24 | 2012-02-16 | Fl Smith A/S | Burner |
WO2012084575A3 (en) * | 2010-12-22 | 2012-08-16 | Thyssenkrupp Polysius Ag | Tubular burner and method for operating a tubular burner |
US20130309618A1 (en) * | 2009-03-25 | 2013-11-21 | Wallace Horn | Laminar Flow Jets |
EP3152490A4 (en) * | 2014-06-09 | 2017-11-01 | Zeeco Inc. | Non-symmetrical low nox burner apparatus and method |
WO2019023117A1 (en) * | 2017-07-28 | 2019-01-31 | Nabors James K Jr | Oxygen-fuel burner for a glass melting furnace |
CN110294594A (en) * | 2018-03-22 | 2019-10-01 | 信越化学工业株式会社 | The manufacturing device of optical fiber base material |
US20200255315A1 (en) * | 2016-06-22 | 2020-08-13 | Jushi Group Co., Ltd. | Glass tank furnace and glass melting method |
US11326777B2 (en) * | 2017-03-13 | 2022-05-10 | Htt Engineering, Spol. S R.O. | Combined burner for blowing oxidizing gas and fuel into melting furnace |
EP4407232A1 (en) | 2023-01-27 | 2024-07-31 | Deutsches Zentrum für Luft- und Raumfahrt e.V. | Burner head and burner system |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110282860A (en) * | 2019-07-15 | 2019-09-27 | 中国建材国际工程集团有限公司 | A kind of burner |
Citations (66)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2263170A (en) * | 1938-12-07 | 1941-11-18 | Nat Machine Works | Gas burner |
US3115851A (en) * | 1960-05-11 | 1963-12-31 | Foster Wheeler Corp | Multi-fuel burner |
US3127156A (en) * | 1964-03-31 | Figure | ||
US3152635A (en) * | 1960-10-31 | 1964-10-13 | Paul D Cox | Gas burner including gas and air mixing apparatus |
US3337324A (en) * | 1963-04-30 | 1967-08-22 | Union Carbide Corp | Process for melting and refining glass batch |
US3635646A (en) * | 1970-08-27 | 1972-01-18 | Cox Mfg Co Inc | Gas burner |
US4032287A (en) * | 1975-06-16 | 1977-06-28 | United States Steel Corporation | Combination burner |
US4140477A (en) * | 1976-10-28 | 1979-02-20 | Envirotech Corporation | Steam atomizing burner |
US4170981A (en) * | 1976-04-02 | 1979-10-16 | Sky Bussan Kabushiki Kaisha | Burner of air adjustment type provided with annular air passage |
US4297093A (en) * | 1978-09-06 | 1981-10-27 | Kobe Steel, Ltd. | Combustion method for reducing NOx and smoke emission |
US4424793A (en) * | 1980-06-16 | 1984-01-10 | R. W. Beckett Corporation | Power gas burner |
US4473388A (en) * | 1983-02-04 | 1984-09-25 | Union Carbide Corporation | Process for melting glass |
US4531960A (en) * | 1983-05-20 | 1985-07-30 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Glassmaking process and equipment |
US4539035A (en) * | 1984-03-26 | 1985-09-03 | Messer Griesheim Industries, Inc. | Method and apparatus for improving oxygen burner performance in a glass furnace |
US4541796A (en) * | 1980-04-10 | 1985-09-17 | Union Carbide Corporation | Oxygen aspirator burner for firing a furnace |
US4565560A (en) * | 1984-12-19 | 1986-01-21 | Ppg Industries, Inc. | Energy efficient and anti-corrosive burner nozzle construction and installation configuration |
US4642047A (en) * | 1984-08-17 | 1987-02-10 | American Combustion, Inc. | Method and apparatus for flame generation and utilization of the combustion products for heating, melting and refining |
US4679733A (en) * | 1986-03-13 | 1987-07-14 | The Dow Chemical Company | Two-fluid nozzle for atomizing a liquid-solid slurry |
US4816056A (en) * | 1987-10-02 | 1989-03-28 | Ppg Industries, Inc. | Heating and agitating method for multi-stage melting and refining of glass |
US4878830A (en) * | 1988-06-20 | 1989-11-07 | Exxon Research And Engineering Company | Substoichiometric fuel firing for minimum NOx emissions |
US4909727A (en) * | 1987-03-04 | 1990-03-20 | Combustion Tec, Inc. | Oxygen enriched continuous combustion in a regenerative furance |
US4911637A (en) * | 1987-08-29 | 1990-03-27 | The Boc Group Plc | Flame treatment method and apparatus |
US4986748A (en) * | 1989-12-15 | 1991-01-22 | Corning Incorporated | Wide range oxy-fuel burner and furnace operation |
US5085156A (en) * | 1990-01-08 | 1992-02-04 | Transalta Resources Investment Corporation | Combustion process |
US5116399A (en) * | 1991-04-11 | 1992-05-26 | Union Carbide Industrial Gases Technology Corporation | Glass melter with front-wall oxygen-fired burner process |
US5139558A (en) * | 1991-11-20 | 1992-08-18 | Union Carbide Industrial Gases Technology Corporation | Roof-mounted auxiliary oxygen-fired burner in glass melting furnace |
US5203859A (en) * | 1992-04-22 | 1993-04-20 | Institute Of Gas Technology | Oxygen-enriched combustion method |
US5215455A (en) * | 1990-01-08 | 1993-06-01 | Tansalta Resources Investment Corporation | Combustion process |
US5238396A (en) * | 1992-06-18 | 1993-08-24 | The Boc Group, Inc. | Fuel-burner method and apparatus |
US5256058A (en) * | 1992-03-30 | 1993-10-26 | Combustion Tec, Inc. | Method and apparatus for oxy-fuel heating with lowered NOx in high temperature corrosive environments |
US5267850A (en) * | 1992-06-04 | 1993-12-07 | Praxair Technology, Inc. | Fuel jet burner |
US5269679A (en) * | 1992-10-16 | 1993-12-14 | Gas Research Institute | Staged air, recirculating flue gas low NOx burner |
US5299929A (en) * | 1993-02-26 | 1994-04-05 | The Boc Group, Inc. | Fuel burner apparatus and method employing divergent flow nozzle |
US5413477A (en) * | 1992-10-16 | 1995-05-09 | Gas Research Institute | Staged air, low NOX burner with internal recuperative flue gas recirculation |
US5431559A (en) * | 1993-07-15 | 1995-07-11 | Maxon Corporation | Oxygen-fuel burner with staged oxygen supply |
US5454712A (en) * | 1993-09-15 | 1995-10-03 | The Boc Group, Inc. | Air-oxy-fuel burner method and apparatus |
US5458483A (en) * | 1993-07-15 | 1995-10-17 | Maxon Corporation | Oxygen-fuel burner with integral staged oxygen supply |
US5545033A (en) * | 1993-11-30 | 1996-08-13 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Asymmetric oxygen/fuel burner |
US5567141A (en) * | 1994-12-30 | 1996-10-22 | Combustion Tec, Inc. | Oxy-liquid fuel combustion process and apparatus |
US5611682A (en) * | 1995-09-05 | 1997-03-18 | Air Products And Chemicals, Inc. | Low-NOx staged combustion device for controlled radiative heating in high temperature furnaces |
US5643348A (en) * | 1992-09-14 | 1997-07-01 | Schuller International, Inc. | Oxygen/fuel fired furnaces having massive, low velocity, turbulent flame clouds |
US5683238A (en) * | 1994-05-18 | 1997-11-04 | Praxair Technology, Inc. | Method for operating a furnace |
US5755818A (en) * | 1995-06-13 | 1998-05-26 | Praxair Technology, Inc. | Staged combustion method |
US5772427A (en) * | 1993-10-01 | 1998-06-30 | L'air Liquide, Societe Anonyme Pour L'etudes Et L'exploitation Des Procedes Georges Claude | Burner and utilization of such a burner in a glass furnace |
US5807418A (en) * | 1996-05-21 | 1998-09-15 | Praxair Technology, Inc. | Energy recovery in oxygen-fired glass melting furnaces |
US5823769A (en) * | 1996-03-26 | 1998-10-20 | Combustion Tec, Inc. | In-line method of burner firing and NOx emission control for glass melting |
US5833447A (en) * | 1995-07-17 | 1998-11-10 | L'air Liquide, Societe Anonyme Pour L'etude Et, L'exploitation Des Procedes Georges Claude | Combustion process and apparatus therefore containing separate injection of fuel and oxidant streams |
US5837028A (en) * | 1992-11-27 | 1998-11-17 | Pilkington Glass Limited | Method for reducing CO emissions from a regenerative glass furnace |
US5853448A (en) * | 1996-01-05 | 1998-12-29 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes George Claude | Method of heating the charge of a glass furnace |
US5863195A (en) * | 1996-08-05 | 1999-01-26 | The Boc Group Plc | Oxygen-fuel burner |
US5924858A (en) * | 1995-06-13 | 1999-07-20 | Praxair Technology, Inc. | Staged combustion method |
US5984667A (en) * | 1995-07-17 | 1999-11-16 | American Air Liquide, Inc. | Combustion process and apparatus therefore containing separate injection of fuel and oxidant streams |
US5993203A (en) * | 1995-11-01 | 1999-11-30 | Gas Research Institute | Heat transfer enhancements for increasing fuel efficiency in high temperature furnaces |
US6047565A (en) * | 1996-07-11 | 2000-04-11 | Saint Gobain Vitrage | Method and device for reducing the NOx emission in a glass furnace |
US6096106A (en) * | 1990-04-03 | 2000-08-01 | The Standard Oil Company | Endothermic reaction apparatus |
JP2000337615A (en) * | 1999-05-28 | 2000-12-08 | Tokyo Yogyo Co Ltd | Burner for flame-regardant material |
US6206686B1 (en) * | 1998-05-01 | 2001-03-27 | North American Manufacturing Company | Integral low NOx injection burner |
US6237639B1 (en) * | 1998-03-18 | 2001-05-29 | Zodiac International | Dump-valve device for a craft and pneumatic craft fitted with same |
US6250915B1 (en) * | 2000-03-29 | 2001-06-26 | The Boc Group, Inc. | Burner and combustion method for heating surfaces susceptible to oxidation or reduction |
US6354110B1 (en) * | 1999-08-26 | 2002-03-12 | The Boc Group, Inc. | Enhanced heat transfer through controlled interaction of separate fuel-rich and fuel-lean flames in glass furnaces |
US6422041B1 (en) * | 1999-08-16 | 2002-07-23 | The Boc Group, Inc. | Method of boosting a glass melting furnace using a roof mounted oxygen-fuel burner |
US6519973B1 (en) * | 2000-03-23 | 2003-02-18 | Air Products And Chemicals, Inc. | Glass melting process and furnace therefor with oxy-fuel combustion over melting zone and air-fuel combustion over fining zone |
US6705117B2 (en) * | 1999-08-16 | 2004-03-16 | The Boc Group, Inc. | Method of heating a glass melting furnace using a roof mounted, staged combustion oxygen-fuel burner |
US20070281264A1 (en) * | 2006-06-05 | 2007-12-06 | Neil Simpson | Non-centric oxy-fuel burner for glass melting systems |
WO2009057839A1 (en) * | 2007-10-30 | 2009-05-07 | Korea Institute Of Energy Research | Eccentric jet oxyfuel burner with low nitrogen oxide emission |
US20120070788A1 (en) * | 2010-09-20 | 2012-03-22 | Korea Institute Of Energy Research | ECCENTRIC JET TYPE LOW NOx OXYFUEL BURNER |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59210209A (en) * | 1983-05-16 | 1984-11-28 | Nippon Furnace Kogyo Kaisha Ltd | Radiant burner |
JP3096749B2 (en) * | 1992-12-25 | 2000-10-10 | 荏原ボイラ株式会社 | Burner |
JP3580438B2 (en) * | 1994-12-22 | 2004-10-20 | 日本電気硝子株式会社 | Gaseous fuel-oxygen burner |
RU2143640C1 (en) * | 1997-10-28 | 1999-12-27 | Муниципальное предприятие "РЕМСТРОЙБЛАГОУСТРОЙСТВО" | Gas burner with adjustable section of heat field |
JP2002295805A (en) * | 2001-03-29 | 2002-10-09 | Noritake Co Ltd | Incinerator |
KR100725264B1 (en) | 2004-10-01 | 2007-06-04 | 한국에너지기술연구원 | eccentric type burnertile |
US8454354B2 (en) * | 2008-05-08 | 2013-06-04 | Air Products And Chemicals, Inc. | Highly radiative burner and combustion process |
RU2391603C2 (en) * | 2008-06-03 | 2010-06-10 | Леонид Анатольевич Ярыгин | Gas burner |
-
2010
- 2010-01-04 US US12/651,506 patent/US20100159409A1/en not_active Abandoned
- 2010-12-22 BR BR112012016443A patent/BR112012016443A2/en not_active Application Discontinuation
- 2010-12-22 KR KR1020127020417A patent/KR101838761B1/en active IP Right Grant
- 2010-12-22 WO PCT/US2010/061785 patent/WO2011082062A1/en active Application Filing
- 2010-12-22 UA UAA201209493A patent/UA110469C2/en unknown
- 2010-12-22 RU RU2012133451/06A patent/RU2577682C2/en not_active IP Right Cessation
- 2010-12-22 MY MYPI2012003017A patent/MY166569A/en unknown
- 2010-12-22 TR TR2018/07129T patent/TR201807129T4/en unknown
- 2010-12-22 JP JP2012548029A patent/JP5756126B2/en not_active Expired - Fee Related
- 2010-12-22 CA CA2785792A patent/CA2785792A1/en not_active Abandoned
- 2010-12-22 CN CN201080060479.8A patent/CN102713434B/en active Active
- 2010-12-22 PL PL10841591T patent/PL2521881T3/en unknown
- 2010-12-22 PT PT108415910T patent/PT2521881T/en unknown
- 2010-12-22 ES ES10841591.0T patent/ES2671058T3/en active Active
- 2010-12-22 EP EP10841591.0A patent/EP2521881B1/en active Active
-
2012
- 2012-07-03 ZA ZA2012/04973A patent/ZA201204973B/en unknown
Patent Citations (71)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3127156A (en) * | 1964-03-31 | Figure | ||
US2263170A (en) * | 1938-12-07 | 1941-11-18 | Nat Machine Works | Gas burner |
US3115851A (en) * | 1960-05-11 | 1963-12-31 | Foster Wheeler Corp | Multi-fuel burner |
US3152635A (en) * | 1960-10-31 | 1964-10-13 | Paul D Cox | Gas burner including gas and air mixing apparatus |
US3337324A (en) * | 1963-04-30 | 1967-08-22 | Union Carbide Corp | Process for melting and refining glass batch |
US3635646A (en) * | 1970-08-27 | 1972-01-18 | Cox Mfg Co Inc | Gas burner |
US4032287A (en) * | 1975-06-16 | 1977-06-28 | United States Steel Corporation | Combination burner |
US4170981A (en) * | 1976-04-02 | 1979-10-16 | Sky Bussan Kabushiki Kaisha | Burner of air adjustment type provided with annular air passage |
US4140477A (en) * | 1976-10-28 | 1979-02-20 | Envirotech Corporation | Steam atomizing burner |
US4297093A (en) * | 1978-09-06 | 1981-10-27 | Kobe Steel, Ltd. | Combustion method for reducing NOx and smoke emission |
US4541796A (en) * | 1980-04-10 | 1985-09-17 | Union Carbide Corporation | Oxygen aspirator burner for firing a furnace |
US4424793A (en) * | 1980-06-16 | 1984-01-10 | R. W. Beckett Corporation | Power gas burner |
US4473388A (en) * | 1983-02-04 | 1984-09-25 | Union Carbide Corporation | Process for melting glass |
US4531960A (en) * | 1983-05-20 | 1985-07-30 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Glassmaking process and equipment |
US4539035A (en) * | 1984-03-26 | 1985-09-03 | Messer Griesheim Industries, Inc. | Method and apparatus for improving oxygen burner performance in a glass furnace |
US4642047A (en) * | 1984-08-17 | 1987-02-10 | American Combustion, Inc. | Method and apparatus for flame generation and utilization of the combustion products for heating, melting and refining |
US4565560A (en) * | 1984-12-19 | 1986-01-21 | Ppg Industries, Inc. | Energy efficient and anti-corrosive burner nozzle construction and installation configuration |
US4679733A (en) * | 1986-03-13 | 1987-07-14 | The Dow Chemical Company | Two-fluid nozzle for atomizing a liquid-solid slurry |
US4909727A (en) * | 1987-03-04 | 1990-03-20 | Combustion Tec, Inc. | Oxygen enriched continuous combustion in a regenerative furance |
US4911637A (en) * | 1987-08-29 | 1990-03-27 | The Boc Group Plc | Flame treatment method and apparatus |
US4816056A (en) * | 1987-10-02 | 1989-03-28 | Ppg Industries, Inc. | Heating and agitating method for multi-stage melting and refining of glass |
US4878830A (en) * | 1988-06-20 | 1989-11-07 | Exxon Research And Engineering Company | Substoichiometric fuel firing for minimum NOx emissions |
US4986748A (en) * | 1989-12-15 | 1991-01-22 | Corning Incorporated | Wide range oxy-fuel burner and furnace operation |
US5215455A (en) * | 1990-01-08 | 1993-06-01 | Tansalta Resources Investment Corporation | Combustion process |
US5085156A (en) * | 1990-01-08 | 1992-02-04 | Transalta Resources Investment Corporation | Combustion process |
US6096106A (en) * | 1990-04-03 | 2000-08-01 | The Standard Oil Company | Endothermic reaction apparatus |
US5116399A (en) * | 1991-04-11 | 1992-05-26 | Union Carbide Industrial Gases Technology Corporation | Glass melter with front-wall oxygen-fired burner process |
US5139558A (en) * | 1991-11-20 | 1992-08-18 | Union Carbide Industrial Gases Technology Corporation | Roof-mounted auxiliary oxygen-fired burner in glass melting furnace |
US5256058A (en) * | 1992-03-30 | 1993-10-26 | Combustion Tec, Inc. | Method and apparatus for oxy-fuel heating with lowered NOx in high temperature corrosive environments |
US5346390A (en) * | 1992-03-30 | 1994-09-13 | Air Products And Chemicals, Inc. | Method and apparatus for oxy-fuel heating with lowered NOx in high temperature corrosive environments |
US5203859A (en) * | 1992-04-22 | 1993-04-20 | Institute Of Gas Technology | Oxygen-enriched combustion method |
US5267850A (en) * | 1992-06-04 | 1993-12-07 | Praxair Technology, Inc. | Fuel jet burner |
US5238396A (en) * | 1992-06-18 | 1993-08-24 | The Boc Group, Inc. | Fuel-burner method and apparatus |
US5643348A (en) * | 1992-09-14 | 1997-07-01 | Schuller International, Inc. | Oxygen/fuel fired furnaces having massive, low velocity, turbulent flame clouds |
US5413477A (en) * | 1992-10-16 | 1995-05-09 | Gas Research Institute | Staged air, low NOX burner with internal recuperative flue gas recirculation |
US5269679A (en) * | 1992-10-16 | 1993-12-14 | Gas Research Institute | Staged air, recirculating flue gas low NOx burner |
US5837028A (en) * | 1992-11-27 | 1998-11-17 | Pilkington Glass Limited | Method for reducing CO emissions from a regenerative glass furnace |
US5360171A (en) * | 1993-02-26 | 1994-11-01 | The Boc Group, Inc. | Fuel burner apparatus and method employing divergent flow nozzle |
US5299929A (en) * | 1993-02-26 | 1994-04-05 | The Boc Group, Inc. | Fuel burner apparatus and method employing divergent flow nozzle |
US5431559A (en) * | 1993-07-15 | 1995-07-11 | Maxon Corporation | Oxygen-fuel burner with staged oxygen supply |
US5458483A (en) * | 1993-07-15 | 1995-10-17 | Maxon Corporation | Oxygen-fuel burner with integral staged oxygen supply |
US5454712A (en) * | 1993-09-15 | 1995-10-03 | The Boc Group, Inc. | Air-oxy-fuel burner method and apparatus |
US5772427A (en) * | 1993-10-01 | 1998-06-30 | L'air Liquide, Societe Anonyme Pour L'etudes Et L'exploitation Des Procedes Georges Claude | Burner and utilization of such a burner in a glass furnace |
US5545033A (en) * | 1993-11-30 | 1996-08-13 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Asymmetric oxygen/fuel burner |
US5683238A (en) * | 1994-05-18 | 1997-11-04 | Praxair Technology, Inc. | Method for operating a furnace |
US5567141A (en) * | 1994-12-30 | 1996-10-22 | Combustion Tec, Inc. | Oxy-liquid fuel combustion process and apparatus |
US5755818A (en) * | 1995-06-13 | 1998-05-26 | Praxair Technology, Inc. | Staged combustion method |
US5924858A (en) * | 1995-06-13 | 1999-07-20 | Praxair Technology, Inc. | Staged combustion method |
US6068468A (en) * | 1995-07-17 | 2000-05-30 | American Air Liquide, Inc. | Refractory block for use in a burner assembly |
US5833447A (en) * | 1995-07-17 | 1998-11-10 | L'air Liquide, Societe Anonyme Pour L'etude Et, L'exploitation Des Procedes Georges Claude | Combustion process and apparatus therefore containing separate injection of fuel and oxidant streams |
US5984667A (en) * | 1995-07-17 | 1999-11-16 | American Air Liquide, Inc. | Combustion process and apparatus therefore containing separate injection of fuel and oxidant streams |
US5611682A (en) * | 1995-09-05 | 1997-03-18 | Air Products And Chemicals, Inc. | Low-NOx staged combustion device for controlled radiative heating in high temperature furnaces |
US5993203A (en) * | 1995-11-01 | 1999-11-30 | Gas Research Institute | Heat transfer enhancements for increasing fuel efficiency in high temperature furnaces |
US5853448A (en) * | 1996-01-05 | 1998-12-29 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes George Claude | Method of heating the charge of a glass furnace |
US6041622A (en) * | 1996-01-05 | 2000-03-28 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method and apparatus for heating the change of a glass furnace |
US5934899A (en) * | 1996-03-26 | 1999-08-10 | Combustion Tec | In-line method of burner firing and NOx emission control for glass melting |
US5823769A (en) * | 1996-03-26 | 1998-10-20 | Combustion Tec, Inc. | In-line method of burner firing and NOx emission control for glass melting |
US5807418A (en) * | 1996-05-21 | 1998-09-15 | Praxair Technology, Inc. | Energy recovery in oxygen-fired glass melting furnaces |
US6047565A (en) * | 1996-07-11 | 2000-04-11 | Saint Gobain Vitrage | Method and device for reducing the NOx emission in a glass furnace |
US5863195A (en) * | 1996-08-05 | 1999-01-26 | The Boc Group Plc | Oxygen-fuel burner |
US6237639B1 (en) * | 1998-03-18 | 2001-05-29 | Zodiac International | Dump-valve device for a craft and pneumatic craft fitted with same |
US6206686B1 (en) * | 1998-05-01 | 2001-03-27 | North American Manufacturing Company | Integral low NOx injection burner |
JP2000337615A (en) * | 1999-05-28 | 2000-12-08 | Tokyo Yogyo Co Ltd | Burner for flame-regardant material |
US6422041B1 (en) * | 1999-08-16 | 2002-07-23 | The Boc Group, Inc. | Method of boosting a glass melting furnace using a roof mounted oxygen-fuel burner |
US6705117B2 (en) * | 1999-08-16 | 2004-03-16 | The Boc Group, Inc. | Method of heating a glass melting furnace using a roof mounted, staged combustion oxygen-fuel burner |
US6354110B1 (en) * | 1999-08-26 | 2002-03-12 | The Boc Group, Inc. | Enhanced heat transfer through controlled interaction of separate fuel-rich and fuel-lean flames in glass furnaces |
US6519973B1 (en) * | 2000-03-23 | 2003-02-18 | Air Products And Chemicals, Inc. | Glass melting process and furnace therefor with oxy-fuel combustion over melting zone and air-fuel combustion over fining zone |
US6250915B1 (en) * | 2000-03-29 | 2001-06-26 | The Boc Group, Inc. | Burner and combustion method for heating surfaces susceptible to oxidation or reduction |
US20070281264A1 (en) * | 2006-06-05 | 2007-12-06 | Neil Simpson | Non-centric oxy-fuel burner for glass melting systems |
WO2009057839A1 (en) * | 2007-10-30 | 2009-05-07 | Korea Institute Of Energy Research | Eccentric jet oxyfuel burner with low nitrogen oxide emission |
US20120070788A1 (en) * | 2010-09-20 | 2012-03-22 | Korea Institute Of Energy Research | ECCENTRIC JET TYPE LOW NOx OXYFUEL BURNER |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20130309618A1 (en) * | 2009-03-25 | 2013-11-21 | Wallace Horn | Laminar Flow Jets |
US9587823B2 (en) * | 2009-03-25 | 2017-03-07 | Wallace Horn | Laminar flow jets |
US20120037054A1 (en) * | 2009-04-24 | 2012-02-16 | Fl Smith A/S | Burner |
WO2012084575A3 (en) * | 2010-12-22 | 2012-08-16 | Thyssenkrupp Polysius Ag | Tubular burner and method for operating a tubular burner |
EP3152490A4 (en) * | 2014-06-09 | 2017-11-01 | Zeeco Inc. | Non-symmetrical low nox burner apparatus and method |
US20200255315A1 (en) * | 2016-06-22 | 2020-08-13 | Jushi Group Co., Ltd. | Glass tank furnace and glass melting method |
US11326777B2 (en) * | 2017-03-13 | 2022-05-10 | Htt Engineering, Spol. S R.O. | Combined burner for blowing oxidizing gas and fuel into melting furnace |
WO2019023117A1 (en) * | 2017-07-28 | 2019-01-31 | Nabors James K Jr | Oxygen-fuel burner for a glass melting furnace |
CN110294594A (en) * | 2018-03-22 | 2019-10-01 | 信越化学工业株式会社 | The manufacturing device of optical fiber base material |
EP4407232A1 (en) | 2023-01-27 | 2024-07-31 | Deutsches Zentrum für Luft- und Raumfahrt e.V. | Burner head and burner system |
DE102023102018A1 (en) | 2023-01-27 | 2024-08-01 | Deutsches Zentrum für Luft- und Raumfahrt e.V. | Burner head and burner system |
Also Published As
Publication number | Publication date |
---|---|
MY166569A (en) | 2018-07-17 |
BR112012016443A2 (en) | 2017-03-07 |
EP2521881B1 (en) | 2018-03-28 |
ES2671058T3 (en) | 2018-06-04 |
JP5756126B2 (en) | 2015-07-29 |
CA2785792A1 (en) | 2011-07-07 |
KR20120107005A (en) | 2012-09-27 |
CN102713434A (en) | 2012-10-03 |
PL2521881T3 (en) | 2018-09-28 |
EP2521881A1 (en) | 2012-11-14 |
UA110469C2 (en) | 2016-01-12 |
RU2012133451A (en) | 2014-02-20 |
PT2521881T (en) | 2018-05-25 |
TR201807129T4 (en) | 2018-06-21 |
KR101838761B1 (en) | 2018-03-14 |
ZA201204973B (en) | 2013-03-27 |
RU2577682C2 (en) | 2016-03-20 |
JP2013516385A (en) | 2013-05-13 |
CN102713434B (en) | 2015-11-25 |
WO2011082062A1 (en) | 2011-07-07 |
EP2521881A4 (en) | 2013-05-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2521881B1 (en) | Non-centric oxy-fuel burner for glass melting systems | |
EP1053060B1 (en) | Low firing rate oxy-fuel burner | |
CN101063524B (en) | Ultra-low Nox burner assembly | |
US10551058B2 (en) | Multi-nozzle combustion assemblies including perforated flame holder, combustion systems including the combustion assemblies, and related methods | |
WO1997036134A1 (en) | IN-LINE METHOD OF BURNER FIRING AND NOx EMISSION CONTROL FOR GLASS MELTING | |
US9447969B2 (en) | Low NOx combustion process and burner therefor | |
CN104266189B (en) | Control method of low-calorific-value gas radiant tube burner | |
EP2904341B1 (en) | Process and apparatus for improving the combustion of secondary fuel in a rotary kiln and process for retrofitting a rotary kiln with a burner assembly | |
JPH062817A (en) | Radiant gas burner | |
US20230043686A1 (en) | Burner for fuel combustion and combustion method therefor | |
EP1979675B1 (en) | Flat- flame vault burner with low polluting emissions | |
US20070281264A1 (en) | Non-centric oxy-fuel burner for glass melting systems | |
CN103782099B (en) | The oxygen enrichment of premixed air-gas burner | |
KR20050075286A (en) | Remote staged radiant wall furnace burner configurations and methods | |
CN204084368U (en) | Low-heat value gas radiant tube burner | |
RU2558702C2 (en) | Burner | |
KR101595678B1 (en) | Tubular flame burner | |
CN100523610C (en) | High-speed uniformly mixing ceramic burner | |
JP2023523122A (en) | Oxygen flat flame burner and block assembly |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: LINDE AKTIENGESELLSCHAFT,GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:RICHARDSON, ANDREW P.;WAINFORD, JOHN ALLEN;SIMPSON, NEIL;SIGNING DATES FROM 20100113 TO 20100126;REEL/FRAME:023909/0446 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |