US20180266678A1 - Staged burner - Google Patents
Staged burner Download PDFInfo
- Publication number
- US20180266678A1 US20180266678A1 US15/460,685 US201715460685A US2018266678A1 US 20180266678 A1 US20180266678 A1 US 20180266678A1 US 201715460685 A US201715460685 A US 201715460685A US 2018266678 A1 US2018266678 A1 US 2018266678A1
- Authority
- US
- United States
- Prior art keywords
- tube
- outer gas
- spuds
- burner
- gas spuds
- 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 claims description 13
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 239000007789 gas Substances 0.000 description 24
- 238000000034 method Methods 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
Images
Classifications
-
- 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
- F23D14/24—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 at least one of the fluids being submitted to a swirling motion
-
- 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
- F23D14/02—Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone
-
- 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
- F23C6/00—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
- F23C6/04—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
- F23C6/045—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure
- F23C6/047—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure with fuel supply in stages
-
- 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
- F23D14/46—Details, e.g. noise reduction means
- F23D14/62—Mixing devices; Mixing tubes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
- F23D2900/14—Special features of gas burners
- F23D2900/14002—Special features of gas burners of premix or non premix types, specially adapted for the combustion of low heating value [LHV] gas
Definitions
- the present disclosure relates to a fuel staged burner for improving flame shape and reducing emissions.
- Burner designs are commonly used for introducing fuel into a combustion chamber such as a furnace. Recently, the reduction of carbon monoxide and NO x emissions have become common factors in the design of burners.
- the present application is directed to a burner design for enhanced flame shape and reduced emissions.
- a burner including a body having an air inlet at a first end and an outlet at a second end.
- a gas supply tube is disposed in the body and includes an air swirler and a nozzle at an end thereof.
- a plurality of outer gas spuds are disposed radially outwardly of the burner outlet, the outer gas spuds including a tube and a spud tip having a first set of openings that are directed generally parallel to an axis of the tube of the outer gas spuds and a second set of openings that are directed at an angle of at least ten degrees to the axis of the tube.
- FIG. 1 is a cross-sectional view of the stage burner according to the principles of the present disclosure.
- FIG. 2 is an end plan view of the stage burner shown in FIG. 1 .
- Example embodiments are provided so that this disclosure will be thorough, and will fully convey the scope to those who are skilled in the art. Numerous specific details are set forth such as examples of specific components, devices, and methods, to provide a thorough understanding of embodiments of the present disclosure. It will be apparent to those skilled in the art that specific details need not be employed, that example embodiments may be embodied in many different forms and that neither should be construed to limit the scope of the disclosure. In some example embodiments, well-known processes, well-known device structures, and well-known technologies are not described in detail.
- first, second, third, etc. may be used herein to describe various elements, components, regions, layers and/or sections, these elements, components, regions, layers and/or sections should not be limited by these terms. These terms may be only used to distinguish one element, component, region, layer or section from another region, layer or section. Terms such as “first,” “second,” and other numerical terms when used herein do not imply a sequence or order unless clearly indicated by the context. Thus, a first element, component, region, layer or section discussed below could be termed a second element, component, region, layer or section without departing from the teachings of the example embodiments.
- Spatially relative terms such as “inner,” “outer,” “beneath,” “below,” “lower,” “above,” “upper,” and the like, may be used herein for ease of description to describe one element or feature's relationship to another element(s) or feature(s) as illustrated in the figures. Spatially relative terms may be intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as “below” or “beneath” other elements or features would then be oriented “above” the other elements or features. Thus, the example term “below” can encompass both an orientation of above and below. The device may be otherwise oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.
- the stage burner 10 includes a gas fuel source 12 and a gas supply tube 14 with an air swirler 16 and a nozzle 18 at an end thereof.
- the gas supply tube extends through a venturi-shaped body 20 having an air inlet 22 at a first end and an outlet 24 that opens into a combustion chamber 26 .
- the nozzle 18 is provided in a center of the venturi-shaped body 20 and terminates short of the outlet 24 .
- the air swirler 16 surrounds the nozzle 18 near the outlet end of the nozzle.
- a plurality of outer gas spuds 27 are disposed radially outwardly of the venturi-shaped body 20 and the outlet 24 and extend into the combustion chamber 26 through openings 28 through a wall 30 of the combustion chamber 26 . Although four gas spuds 27 are shown in FIG. 2 , it should be understood that as few as three and as many as eight gas spuds 27 can be utilized.
- Each of the outer gas spuds 27 have a tube 31 and a spud tip 32 that is provided with a plurality of openings 34 A, 34 B.
- a first set of the opening 34 A are directed generally parallel to an axis of the tube 31 of the outer gas spuds 27 .
- a second set of the openings 34 B of the spud tips 32 open in a direction that is angled at an angle ⁇ to the axis of the outer gas spuds that is angled relative to a center axis of the outer gas spuds 27 .
- the angle ⁇ as shown in FIG. 1 is between 10 and 30 degrees and more particularly 20 degrees.
- the spud tips 32 are further oriented at an angle ⁇ so that the second set of openings 34 B are directed to inject fuel in a tangent fashion to the primary swirling airflow as shown in FIG. 2 .
- the angle ⁇ as shown in FIG. 2 is between 30 and 60 degrees and more particularly 45 degrees.
- the pipes of the outer gas spuds 27 can be angled inward at an angle a that can be angled relative to an axis that is parallel to a center axis X of the venturi shaped body 20 .
- the openings 28 through the wall 30 can be elongated so that the position of the outer gas spuds can be adjusted along the desired angle a as shown in FIG. 1 .
- the center axis of the outer gas spuds 27 can be directed toward the angle a so that the gas injection direction is into the air flow exiting the venturi-shaped body 20 as shown in FIG. 1
- the angle a illustrated in FIG. 1 is 2°.
- the narrowing air inlet side of the venturi-shaped body 20 is designed to quickly and uniformly accelerate the air stream and then the expanding outlet side of the venturi-shaped body 20 is designed to gradually slow down the air stream for uniform mixing with the fuel.
- the fuel is staged to achieve lower NOx emissions (lower than so called ‘conventional’ burners which tend to mix the air and fuel in one step very quickly).
- the fuel staging is accomplished by injecting from 10-40% of the total gas through the center gas gun/nozzle 18 for stability purposes. This first stage of fuel gas mixes with the air immediately downstream of the air swirler 16 to achieve a stable flame.
- the swirler 16 is designed to swirl the air stream very hard which then creates a recirculation zone in front of the swirler 16 to achieve a stable flame.
- the outer gas spuds 27 are designed with very high exit gas velocity in order to entrain large amounts of products of combustion to create a so called ‘internal flue gas recirculation’ in the furnace which helps to suppress the flame temperature and subsequently NOx generation.
- the effect of the 2 sets of holes 34 A, 34 B in the spud tips is to create a faster mixing inner core of flame which then reacts more quickly to catch the outermost spud tip fuel resulting in an overall shorter and narrower flame than is otherwise possible with using axial only spud injectors.
- the effect of angling the injectors radially inboard also drives the mixing slightly faster for optimum flame shape.
- the design of the staged fuel injectors can be varied depending upon a particular application to provide the ability to match the staged fuel to mix with the air as desired for the available combustion volume/space which will change depending on the type of boiler so as to provide optimum emissions performance.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gas Burners (AREA)
Abstract
Description
- The present disclosure relates to a fuel staged burner for improving flame shape and reducing emissions.
- This section provides background information related to the present disclosure which is not necessarily prior art.
- Burner designs are commonly used for introducing fuel into a combustion chamber such as a furnace. Recently, the reduction of carbon monoxide and NOx emissions have become common factors in the design of burners.
- The present application is directed to a burner design for enhanced flame shape and reduced emissions.
- This section provides a general summary of the disclosure, and is not a comprehensive disclosure of its full scope or all of its features.
- A burner including a body having an air inlet at a first end and an outlet at a second end. A gas supply tube is disposed in the body and includes an air swirler and a nozzle at an end thereof. A plurality of outer gas spuds are disposed radially outwardly of the burner outlet, the outer gas spuds including a tube and a spud tip having a first set of openings that are directed generally parallel to an axis of the tube of the outer gas spuds and a second set of openings that are directed at an angle of at least ten degrees to the axis of the tube.
- Further areas of applicability will become apparent from the description provided herein. The description and specific examples in this summary are intended for purposes of illustration only and are not intended to limit the scope of the present disclosure.
- The drawings described herein are for illustrative purposes only of selected embodiments and not all possible implementations, and are not intended to limit the scope of the present disclosure.
-
FIG. 1 is a cross-sectional view of the stage burner according to the principles of the present disclosure; and -
FIG. 2 is an end plan view of the stage burner shown inFIG. 1 . - Corresponding reference numerals indicate corresponding parts throughout the several views of the drawings.
- Example embodiments will now be described more fully with reference to the accompanying drawings.
- Example embodiments are provided so that this disclosure will be thorough, and will fully convey the scope to those who are skilled in the art. Numerous specific details are set forth such as examples of specific components, devices, and methods, to provide a thorough understanding of embodiments of the present disclosure. It will be apparent to those skilled in the art that specific details need not be employed, that example embodiments may be embodied in many different forms and that neither should be construed to limit the scope of the disclosure. In some example embodiments, well-known processes, well-known device structures, and well-known technologies are not described in detail.
- The terminology used herein is for the purpose of describing particular example embodiments only and is not intended to be limiting. As used herein, the singular forms “a,” “an,” and “the” may be intended to include the plural forms as well, unless the context clearly indicates otherwise. The terms “comprises,” “comprising,” “including,” and “having,” are inclusive and therefore specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof. The method steps, processes, and operations described herein are not to be construed as necessarily requiring their performance in the particular order discussed or illustrated, unless specifically identified as an order of performance. It is also to be understood that additional or alternative steps may be employed.
- When an element or layer is referred to as being “on,” “engaged to,” “connected to,” or “coupled to” another element or layer, it may be directly on, engaged, connected or coupled to the other element or layer, or intervening elements or layers may be present. In contrast, when an element is referred to as being “directly on,” “directly engaged to,” “directly connected to,” or “directly coupled to” another element or layer, there may be no intervening elements or layers present. Other words used to describe the relationship between elements should be interpreted in a like fashion (e.g., “between” versus “directly between,” “adjacent” versus “directly adjacent,” etc.). As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed items.
- Although the terms first, second, third, etc. may be used herein to describe various elements, components, regions, layers and/or sections, these elements, components, regions, layers and/or sections should not be limited by these terms. These terms may be only used to distinguish one element, component, region, layer or section from another region, layer or section. Terms such as “first,” “second,” and other numerical terms when used herein do not imply a sequence or order unless clearly indicated by the context. Thus, a first element, component, region, layer or section discussed below could be termed a second element, component, region, layer or section without departing from the teachings of the example embodiments.
- Spatially relative terms, such as “inner,” “outer,” “beneath,” “below,” “lower,” “above,” “upper,” and the like, may be used herein for ease of description to describe one element or feature's relationship to another element(s) or feature(s) as illustrated in the figures. Spatially relative terms may be intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as “below” or “beneath” other elements or features would then be oriented “above” the other elements or features. Thus, the example term “below” can encompass both an orientation of above and below. The device may be otherwise oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.
- With reference to
FIGS. 1 and 2 , the stage burner 10 according to the principles of the present disclosure will now be described. The stage burner 10 includes agas fuel source 12 and agas supply tube 14 with anair swirler 16 and anozzle 18 at an end thereof. The gas supply tube extends through a venturi-shaped body 20 having anair inlet 22 at a first end and anoutlet 24 that opens into acombustion chamber 26. Thenozzle 18 is provided in a center of the venturi-shaped body 20 and terminates short of theoutlet 24. Theair swirler 16 surrounds thenozzle 18 near the outlet end of the nozzle. - A plurality of
outer gas spuds 27 are disposed radially outwardly of the venturi-shaped body 20 and theoutlet 24 and extend into thecombustion chamber 26 throughopenings 28 through awall 30 of thecombustion chamber 26. Although fourgas spuds 27 are shown inFIG. 2 , it should be understood that as few as three and as many as eightgas spuds 27 can be utilized. Each of theouter gas spuds 27 have atube 31 and aspud tip 32 that is provided with a plurality ofopenings tube 31 of theouter gas spuds 27. A second set of theopenings 34B of thespud tips 32 open in a direction that is angled at an angle β to the axis of the outer gas spuds that is angled relative to a center axis of theouter gas spuds 27. Although other angles can be used, the angle β as shown inFIG. 1 is between 10 and 30 degrees and more particularly 20 degrees. In addition, thespud tips 32 are further oriented at an angle θ so that the second set ofopenings 34B are directed to inject fuel in a tangent fashion to the primary swirling airflow as shown inFIG. 2 . Although other angles can be utilized, the angle θ as shown inFIG. 2 is between 30 and 60 degrees and more particularly 45 degrees. - As shown in
FIG. 1 , the pipes of theouter gas spuds 27 can be angled inward at an angle a that can be angled relative to an axis that is parallel to a center axis X of the venturi shaped body 20.Theopenings 28 through thewall 30 can be elongated so that the position of the outer gas spuds can be adjusted along the desired angle a as shown inFIG. 1 . The center axis of theouter gas spuds 27 can be directed toward the angle a so that the gas injection direction is into the air flow exiting the venturi-shaped body 20 as shown inFIG. 1 Although other angles can be used depending upon the configuration of the burner chamber and other factors, the angle a illustrated inFIG. 1 is 2°. - The narrowing air inlet side of the venturi-
shaped body 20 is designed to quickly and uniformly accelerate the air stream and then the expanding outlet side of the venturi-shaped body 20 is designed to gradually slow down the air stream for uniform mixing with the fuel. The fuel is staged to achieve lower NOx emissions (lower than so called ‘conventional’ burners which tend to mix the air and fuel in one step very quickly). The fuel staging is accomplished by injecting from 10-40% of the total gas through the center gas gun/nozzle 18 for stability purposes. This first stage of fuel gas mixes with the air immediately downstream of theair swirler 16 to achieve a stable flame. Theswirler 16 is designed to swirl the air stream very hard which then creates a recirculation zone in front of theswirler 16 to achieve a stable flame. - Then the balance of the gas (60-90% by volume) is staged via the
outer gas spuds 27 directly into thecombustion chamber 26. Theouter gas spuds 27 are designed with very high exit gas velocity in order to entrain large amounts of products of combustion to create a so called ‘internal flue gas recirculation’ in the furnace which helps to suppress the flame temperature and subsequently NOx generation. - The effect of the 2 sets of
holes - The foregoing description of the embodiments has been provided for purposes of illustration and description. It is not intended to be exhaustive or to limit the disclosure. Individual elements or features of a particular embodiment are generally not limited to that particular embodiment, but, where applicable, are interchangeable and can be used in a selected embodiment, even if not specifically shown or described. The same may also be varied in many ways. Such variations are not to be regarded as a departure from the disclosure, and all such modifications are intended to be included within the scope of the disclosure.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US15/460,685 US20180266678A1 (en) | 2017-03-16 | 2017-03-16 | Staged burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US15/460,685 US20180266678A1 (en) | 2017-03-16 | 2017-03-16 | Staged burner |
Publications (1)
Publication Number | Publication Date |
---|---|
US20180266678A1 true US20180266678A1 (en) | 2018-09-20 |
Family
ID=63519121
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/460,685 Abandoned US20180266678A1 (en) | 2017-03-16 | 2017-03-16 | Staged burner |
Country Status (1)
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US (1) | US20180266678A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110173692A (en) * | 2019-05-29 | 2019-08-27 | 广东东实开能能源有限公司 | An ultra-low nitrogen combustion system for low calorific value gas |
CN112963833A (en) * | 2021-02-24 | 2021-06-15 | 西安交通大学 | Multistage cyclone burner of low nitrogen of ammonia |
US20210394134A1 (en) * | 2020-06-23 | 2021-12-23 | Noritz Corporation | Premixing device and combustion device equipped with the premixing device |
WO2023179824A3 (en) * | 2022-03-23 | 2023-11-16 | Dürr Systems Ag | Jet burner apparatus |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4257863A (en) * | 1978-06-12 | 1981-03-24 | The Broken Hill Proprietary Company Limited | Gas sensors and method of making such sensors |
US4303386A (en) * | 1979-05-18 | 1981-12-01 | Coen Company, Inc. | Parallel flow burner |
US4915619A (en) * | 1988-05-05 | 1990-04-10 | The Babcock & Wilcox Company | Burner for coal, oil or gas firing |
US5195884A (en) * | 1992-03-27 | 1993-03-23 | John Zink Company, A Division Of Koch Engineering Company, Inc. | Low NOx formation burner apparatus and methods |
US5238395A (en) * | 1992-03-27 | 1993-08-24 | John Zink Company | Low nox gas burner apparatus and methods |
US5269678A (en) * | 1990-09-07 | 1993-12-14 | Koch Engineering Company, Inc. | Methods and apparatus for burning fuel with low NOx formation |
US9593847B1 (en) * | 2014-03-05 | 2017-03-14 | Zeeco, Inc. | Fuel-flexible burner apparatus and method for fired heaters |
-
2017
- 2017-03-16 US US15/460,685 patent/US20180266678A1/en not_active Abandoned
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4257863A (en) * | 1978-06-12 | 1981-03-24 | The Broken Hill Proprietary Company Limited | Gas sensors and method of making such sensors |
US4303386A (en) * | 1979-05-18 | 1981-12-01 | Coen Company, Inc. | Parallel flow burner |
US4915619A (en) * | 1988-05-05 | 1990-04-10 | The Babcock & Wilcox Company | Burner for coal, oil or gas firing |
US5269678A (en) * | 1990-09-07 | 1993-12-14 | Koch Engineering Company, Inc. | Methods and apparatus for burning fuel with low NOx formation |
US5195884A (en) * | 1992-03-27 | 1993-03-23 | John Zink Company, A Division Of Koch Engineering Company, Inc. | Low NOx formation burner apparatus and methods |
US5238395A (en) * | 1992-03-27 | 1993-08-24 | John Zink Company | Low nox gas burner apparatus and methods |
US9593847B1 (en) * | 2014-03-05 | 2017-03-14 | Zeeco, Inc. | Fuel-flexible burner apparatus and method for fired heaters |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110173692A (en) * | 2019-05-29 | 2019-08-27 | 广东东实开能能源有限公司 | An ultra-low nitrogen combustion system for low calorific value gas |
US20210394134A1 (en) * | 2020-06-23 | 2021-12-23 | Noritz Corporation | Premixing device and combustion device equipped with the premixing device |
US11819811B2 (en) * | 2020-06-23 | 2023-11-21 | Noritz Corporation | Premixing device and combustion device equipped with the premixing device |
CN112963833A (en) * | 2021-02-24 | 2021-06-15 | 西安交通大学 | Multistage cyclone burner of low nitrogen of ammonia |
WO2023179824A3 (en) * | 2022-03-23 | 2023-11-16 | Dürr Systems Ag | Jet burner apparatus |
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