EP3009741A1 - Boiler or furnace for combustion of fuel in an air staged combustion mode - Google Patents
Boiler or furnace for combustion of fuel in an air staged combustion mode Download PDFInfo
- Publication number
- EP3009741A1 EP3009741A1 EP14188941.0A EP14188941A EP3009741A1 EP 3009741 A1 EP3009741 A1 EP 3009741A1 EP 14188941 A EP14188941 A EP 14188941A EP 3009741 A1 EP3009741 A1 EP 3009741A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- burner
- combustion
- secondary air
- enclosure
- furnace
- 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.)
- Withdrawn
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23M—CASINGS, LININGS, WALLS OR DOORS SPECIALLY ADAPTED FOR COMBUSTION CHAMBERS, e.g. FIREBRIDGES; DEVICES FOR DEFLECTING AIR, FLAMES OR COMBUSTION PRODUCTS IN COMBUSTION CHAMBERS; SAFETY ARRANGEMENTS SPECIALLY ADAPTED FOR COMBUSTION APPARATUS; DETAILS OF COMBUSTION CHAMBERS, NOT OTHERWISE PROVIDED FOR
- F23M5/00—Casings; Linings; Walls
- F23M5/08—Cooling thereof; Tube walls
-
- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L9/00—Passages or apertures for delivering secondary air for completing combustion of fuel
- F23L9/04—Passages or apertures for delivering secondary air for completing combustion of fuel by discharging the air beyond the fire, i.e. nearer the smoke outlet
-
- 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
- F23C2201/00—Staged combustion
- F23C2201/10—Furnace staging
- F23C2201/102—Furnace staging in horizontal direction
-
- 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
- F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
- F23C2900/06041—Staged supply of oxidant
Definitions
- the invention relates to a boiler or furnace for combustion of fuel in an air staged combustion mode.
- Air staging is a well-known design feature for NOx control in boilers and furnaces, e.g. power plant boilers, industrial boilers for generating steam and/or hot water.
- Air staging involves a separation of combustion air into a primary air flow and a secondary air flow.
- the primary air the majority of the total amount of combustion air - is mixed with the respective fuel in a burner, where combustion occurs at a relative low temperature producing a flue gas that is rich in fuel and deficient regarding oxygen, and moderate amounts of NOx are formed.
- the secondary air the remaining combustion air - is introduced into the flue gas downstream of the burner(s) in a secondary combustion zone. There complete combustion and burnout are achieved again at a relatively low temperature minimizing the production of NOx.
- the secondary air is introduced from the outside via ports or nozzles extending through the housing of the boiler or furnace at the required position in the secondary combustion zone.
- the required position depends inter alia on the design of the boiler or furnace including the type of burner(s).
- the housing typically comprises numerous pipes for relatively cooling the housing usually made from refractory materials, as well as generating a heated fluid like hot water and/or steam. At the locations of the secondary air ports these closely spaced apart pipes need to be bended in order to create the necessary accessible area for introducing these ports between the pipes. This makes the design complex, cumbersome and contributes to the manufacturing costs.
- the invention aims at reducing the manufacturing costs of building or retrofitting a boiler or furnace by simplifying the design and/or reduction of required equipment.
- a boiler or furnace for combustion of fuel in an air staged combustion mode comprises an enclosure defining a combustion chamber, of which at least a part is provided with heat exchanging tubes for generating a heated fluid, at least one burner for combustion of fuel provided with a fuel supply and a primary air supply, a secondary air supply and an outlet for discharging flue gas, wherein the secondary air supply is positioned internally of the enclosure and the heat exchanging tubes downstream of the at least one burner.
- the boiler or furnace for combustion of fuel, like oil, gas, or solid fuel such as coal or biomass, in an air staged combustion mode comprises an enclosure.
- the walls of the enclosure define a combustion chamber.
- At least part of the enclosure is provided with heat exchanging tubes, wherein a heat exchange fluid flows, that is heated by the heat resulting from the combustion and simultaneously maintains the enclosure at a relatively low temperature.
- the inlets of the heat exchanging tubes are connected, usually via an appropriate header system, to a source of heat exchange fluid, while the outlets, usually also by means of an appropriate header system, are connected to a discharge for passing the heated fluid to further processes, like electricity generation or heating process streams and/or buildings in an industrial plant Typically water is heated to hot water and/or steam.
- a so called waterwall comprising closely set tubes is a suitable example.
- Membrane tubes are another examples
- the enclosure itself is typically made from refractory materials and/or steel, such as refractory cladded steel.
- At least one burner for combustion of a fuel is provided in one of the walls of the enclosure.
- the fuel typically a gaseous or liquid fuel
- Primary combustion air typically 60 - 90 vol.% of the total amount of combustion air, is also fed to the burner via a primary air supply, suitably a wind-box.
- the enclosure also has an outlet for discharging flue gas resulting from the combustion process.
- a secondary air supply is provided internally of the enclosure and the heat exchanging tubes at a position downstream of the at least one burner.
- Providing an internal supply for the secondary air allows to have as few positions as possible where the pattern of the heat exchanging tubes needs to be adapted around an entry duct, thus reducing the number of bends or other curves therein compared to the external secondary air supply in the prior art and thereby also reducing design and manufacturing costs.
- the inlet of the secondary air supply through the enclosure and between heat exchanging tubes will be at the enclosure wall where the burner is situated, or at the wall opposite the burner.
- the burner opening in the wall itself is used as a hole for this secondary air inlet, as will be explained hereinafter.
- a primary combustion zone and a secondary combustion zone can be distinguished in the combustion chamber.
- fuel is combusted with the bulk of the total combustion air, typically 60-90%, while the secondary combustion air (the remaining volume 10-40% of the total combustion air) is fed to the secondary combustion zone, downstream the primary combustion zone.
- the secondary air supply comprises an inlet duct through the wall of the enclosure in fluid communication with a distribution channel extending along the inner periphery of the enclosure in a direction transverse to the flow direction of the flue gas in operation, wherein the distribution channel is provided with nozzles for injection of secondary air into the flue gas.
- the secondary air supply is a manifold system comprising at least an inlet duct for secondary air in fluid communication with a distribution channel.
- the distribution channel is provided with a plurality of injection nozzles for delivering the secondary air to the flue gas.
- the injection nozzles are spaced apart, such as at predetermined intervals.
- the injection nozzles can be grouped together forming subgroups of closely set nozzles, while the distance between subgroups might vary.
- the size of the nozzle openings might vary as well.
- the injection nozzles are preferably designed, including number, position, dimensions and direction, such that an intimate mixing with the flue gas occurs in the secondary combustion zone.
- the peripheral distribution channel such as an annular passageway, e.g. made from metal, refractory materials and/or concrete, extends in a direction perpendicular to the main flow of gas, and as it projects away from the enclosure wall to the centre, it forms a flow restriction for the flue gas flow.
- This restriction contributes to internal recirculation of flue gas, if any depending on the type of burner and design of boiler or furnace, which is beneficial in suppressing NOx generation
- This restriction also acts as a venturi thereby enhancing the draw of flue gas to the outlet and promoting the thorough mixing of the secondary air with the flue gas, thereby on its turn improving complete combustion and burnout.
- the inlet of the secondary air supply through the enclosure is preferably positioned in the wall thereof, which wall also is provided with the at least one burner. Another preferred position of the inlet is in the wall opposite the burner. Typically these walls are more accessible than the side walls. Furthermore usually the impact of positioning the inlet in one of these walls on the arrangement of the heat exchanging tubes is less than in a situation, where the inlet would be positioned in a side wall extending between the wall having the burner and the opposite wall.
- the secondary air supply may be provided with its own dedicated equipment like a fan, wind-box and control devices in order to control the flow of secondary air, in particular the amount thereof.
- the at least one burner is a throat burner provided in a burner opening in a wall of the enclosure, and the inlet of the secondary air supply is provided in the burner opening.
- This arrangement allows as few as possible openings in the enclosure, simplifying the design and reducing manufacturing costs.
- the inlet duct is integrated in the throat burner.
- the boiler or furnace comprises a wind-box for supplying air to the primary air supply and the secondary air supply.
- a wind-box for supplying air to the primary air supply and the secondary air supply.
- the wind-box is provided with control means for controlling the secondary air flow.
- a damper is a suitable control means.
- the boiler or furnace can be used in power plant facilities, where produced steam is fed to a steam turbine in order to generate electricity in an associated generator.
- the boiler or furnace may also be used in industrial facilities for producing (low pressure) steam or heated fluid, which is processed further for example for heating purposes.
- Fig. 1 is a diagrammatic view of a basic design of an embodiment of a furnace 10 according to the invention.
- the furnace 10 comprises a box like enclosure 12 defining a combustion chamber 14.
- the walls 16 of the enclosure 12 are provided with closely set heat exchanging tubes 18 as a so called water wall, wherein e.g. water and/or steam flows during operation.
- water is fed to the tubes 18 and converted into steam, which is discharge, as indicated by arrows.
- a number of burners 22, in this case two are positioned, which are fed with primary air and fuel, like gas or oil, via primary air supply line 24 and fuel supply line 26 respectively. Flue gas is discharged from the combustion chamber14 via exhaust 28.
- the internal secondary air supply line 34 comprises inlet channels 38 at the top and bottom of the enclosure 12, which channels 38 extend from their inlets 40 connected to the secondary air supply 32, along the walls 16 in the direction of the main direction of flue gas (indicated by arrow 42).
- the channels 38 are connected to a distribution channel 46, which extends along the periphery of the enclosure 12 at the inside thereof.
- the distribution channel 46 is transverse to the main flow direction of flue gas in the combustion chamber 14 as indicated by an arrow.
- the distribution channel 34 comprises a number of nozzles 48.
- Fig. 2 shows an another embodiment. Parts similar to those shown in Fig. 1 are indicated by the same reference numeral.
- the furnace or boiler 10 comprises an enclosure 12 defining a combustion chamber 14. In the walls 16 of the enclosure 12 heat exchanging tubes 18 are provided.
- a throat burner 22 is mounted in a burner opening 49 in the wall 20 of the enclosure 12.
- the burner 22 receives fuel from fuel supply line 26.
- a wind-box 50 is provided, which passes the primary air via channel 52 to the burner and the secondary air via channels 54 each provided with a damper 56 for controlling the secondary air flow, into channels 38 and further into distribution channel 46 having nozzles 48.
- Reference numeral 58 indicates the primary flame, while the internal flue gas recirculation, if any, bears reference numeral 60.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Combustion Of Fluid Fuel (AREA)
Abstract
The invention relates to a boiler or furnace (10) for combustion of fuel in an air staged combustion mode, comprising an enclosure (12) defining a combustion chamber (14), of which at least a part is provided with heat exchanging tubes (18) for generating a heated fluid, at least one burner (22) for combustion of fuel provided with a fuel supply (26) and a primary air supply (24), and a secondary air supply (32), and an outlet (28) for discharge of flue gas, wherein the secondary air supply (32) is positioned internally of the enclosure (12) downstream of the at least one burner (22).
Description
- The invention relates to a boiler or furnace for combustion of fuel in an air staged combustion mode.
- Air staging (also known as overfire air) is a well-known design feature for NOx control in boilers and furnaces, e.g. power plant boilers, industrial boilers for generating steam and/or hot water. Air staging involves a separation of combustion air into a primary air flow and a secondary air flow. The primary air - the majority of the total amount of combustion air - is mixed with the respective fuel in a burner, where combustion occurs at a relative low temperature producing a flue gas that is rich in fuel and deficient regarding oxygen, and moderate amounts of NOx are formed. The secondary air - the remaining combustion air - is introduced into the flue gas downstream of the burner(s) in a secondary combustion zone. There complete combustion and burnout are achieved again at a relatively low temperature minimizing the production of NOx.
- In the prior art systems the secondary air is introduced from the outside via ports or nozzles extending through the housing of the boiler or furnace at the required position in the secondary combustion zone. The required position depends inter alia on the design of the boiler or furnace including the type of burner(s). The housing typically comprises numerous pipes for relatively cooling the housing usually made from refractory materials, as well as generating a heated fluid like hot water and/or steam. At the locations of the secondary air ports these closely spaced apart pipes need to be bended in order to create the necessary accessible area for introducing these ports between the pipes. This makes the design complex, cumbersome and contributes to the manufacturing costs. Also in retrofitting operations overfire air involves tube modifications to create the ports for the secondary air nozzles and the addition of ducts, dampers and a wind-box. In addition there may be objects in the vicinity of the boiler or furnace obstructing access to the side walls. See e.g. http://www.iea-coal.org.uk/site/ieacoal/databases/ccts/air-staging-for-nox-control-overfire-air-and-two-stage-combustion.
- The invention aims at reducing the manufacturing costs of building or retrofitting a boiler or furnace by simplifying the design and/or reduction of required equipment.
- According to the invention a boiler or furnace for combustion of fuel in an air staged combustion mode comprises an enclosure defining a combustion chamber, of which at least a part is provided with heat exchanging tubes for generating a heated fluid, at least one burner for combustion of fuel provided with a fuel supply and a primary air supply, a secondary air supply and an outlet for discharging flue gas, wherein the secondary air supply is positioned internally of the enclosure and the heat exchanging tubes downstream of the at least one burner.
- The boiler or furnace for combustion of fuel, like oil, gas, or solid fuel such as coal or biomass, in an air staged combustion mode according to the invention comprises an enclosure. The walls of the enclosure define a combustion chamber. At least part of the enclosure is provided with heat exchanging tubes, wherein a heat exchange fluid flows, that is heated by the heat resulting from the combustion and simultaneously maintains the enclosure at a relatively low temperature. In operation the inlets of the heat exchanging tubes are connected, usually via an appropriate header system, to a source of heat exchange fluid, while the outlets, usually also by means of an appropriate header system, are connected to a discharge for passing the heated fluid to further processes, like electricity generation or heating process streams and/or buildings in an industrial plant Typically water is heated to hot water and/or steam. A so called waterwall comprising closely set tubes is a suitable example. Membrane tubes are another examples The enclosure itself is typically made from refractory materials and/or steel, such as refractory cladded steel. At least one burner for combustion of a fuel is provided in one of the walls of the enclosure. The fuel, typically a gaseous or liquid fuel, is fed to the burner via the fuel supply from a fuel source. Primary combustion air, typically 60 - 90 vol.% of the total amount of combustion air, is also fed to the burner via a primary air supply, suitably a wind-box. The enclosure also has an outlet for discharging flue gas resulting from the combustion process. According to the invention a secondary air supply is provided internally of the enclosure and the heat exchanging tubes at a position downstream of the at least one burner. Providing an internal supply for the secondary air allows to have as few positions as possible where the pattern of the heat exchanging tubes needs to be adapted around an entry duct, thus reducing the number of bends or other curves therein compared to the external secondary air supply in the prior art and thereby also reducing design and manufacturing costs. Typically the inlet of the secondary air supply through the enclosure and between heat exchanging tubes will be at the enclosure wall where the burner is situated, or at the wall opposite the burner. In a preferred embodiment the burner opening in the wall itself is used as a hole for this secondary air inlet, as will be explained hereinafter.
- During operation a primary combustion zone and a secondary combustion zone can be distinguished in the combustion chamber. In the primary combustion zone fuel is combusted with the bulk of the total combustion air, typically 60-90%, while the secondary combustion air (the remaining volume 10-40% of the total combustion air) is fed to the secondary combustion zone, downstream the primary combustion zone.
- In a preferred embodiment the secondary air supply comprises an inlet duct through the wall of the enclosure in fluid communication with a distribution channel extending along the inner periphery of the enclosure in a direction transverse to the flow direction of the flue gas in operation, wherein the distribution channel is provided with nozzles for injection of secondary air into the flue gas. In this embodiment the secondary air supply is a manifold system comprising at least an inlet duct for secondary air in fluid communication with a distribution channel. The distribution channel is provided with a plurality of injection nozzles for delivering the secondary air to the flue gas. E.g. the injection nozzles are spaced apart, such as at predetermined intervals. The injection nozzles can be grouped together forming subgroups of closely set nozzles, while the distance between subgroups might vary. The size of the nozzle openings might vary as well. The injection nozzles are preferably designed, including number, position, dimensions and direction, such that an intimate mixing with the flue gas occurs in the secondary combustion zone. The peripheral distribution channel such as an annular passageway, e.g. made from metal, refractory materials and/or concrete, extends in a direction perpendicular to the main flow of gas, and as it projects away from the enclosure wall to the centre, it forms a flow restriction for the flue gas flow. This restriction contributes to internal recirculation of flue gas, if any depending on the type of burner and design of boiler or furnace, which is beneficial in suppressing NOx generation This restriction also acts as a venturi thereby enhancing the draw of flue gas to the outlet and promoting the thorough mixing of the secondary air with the flue gas, thereby on its turn improving complete combustion and burnout.
- As said the inlet of the secondary air supply through the enclosure is preferably positioned in the wall thereof, which wall also is provided with the at least one burner. Another preferred position of the inlet is in the wall opposite the burner. Typically these walls are more accessible than the side walls. Furthermore usually the impact of positioning the inlet in one of these walls on the arrangement of the heat exchanging tubes is less than in a situation, where the inlet would be positioned in a side wall extending between the wall having the burner and the opposite wall. The secondary air supply may be provided with its own dedicated equipment like a fan, wind-box and control devices in order to control the flow of secondary air, in particular the amount thereof.
- In a preferred embodiment the at least one burner is a throat burner provided in a burner opening in a wall of the enclosure, and the inlet of the secondary air supply is provided in the burner opening. This arrangement allows as few as possible openings in the enclosure, simplifying the design and reducing manufacturing costs. In a further preferred embodiment thereof the inlet duct is integrated in the throat burner.
- Advantageously the boiler or furnace comprises a wind-box for supplying air to the primary air supply and the secondary air supply. Again having a common wind-box for both of the primary air and secondary is beneficial in view of costs. Optionally the wind-box is provided with control means for controlling the secondary air flow. A damper is a suitable control means.
- The boiler or furnace can be used in power plant facilities, where produced steam is fed to a steam turbine in order to generate electricity in an associated generator. The boiler or furnace may also be used in industrial facilities for producing (low pressure) steam or heated fluid, which is processed further for example for heating purposes.
- The invention will be illustrated by means of the attached drawing, wherein
-
Fig. 1 is a diagrammatic cross section of a basic layout of an embodiment of a furnace according to the invention; and -
Fig. 2 is a diagrammatic cross section of a preferred embodiment of a furnace according to the invention. -
Fig. 1 is a diagrammatic view of a basic design of an embodiment of afurnace 10 according to the invention. Thefurnace 10 comprises a box likeenclosure 12 defining acombustion chamber 14. Thewalls 16 of theenclosure 12 are provided with closely setheat exchanging tubes 18 as a so called water wall, wherein e.g. water and/or steam flows during operation. In the embodiment as shown, water is fed to thetubes 18 and converted into steam, which is discharge, as indicated by arrows. In the front wall 20 a number ofburners 22, in this case two, are positioned, which are fed with primary air and fuel, like gas or oil, via primaryair supply line 24 andfuel supply line 26 respectively. Flue gas is discharged from the combustion chamber14 viaexhaust 28. In thefront wall 20 two through-bores or holes 30 are provided for asecondary air supply 32, connected to the secondaryair supply line 34, which is provided with acontrol valve 36. The internal secondaryair supply line 34 comprisesinlet channels 38 at the top and bottom of theenclosure 12, whichchannels 38 extend from theirinlets 40 connected to thesecondary air supply 32, along thewalls 16 in the direction of the main direction of flue gas (indicated by arrow 42). At the opposite outlet ends 44 thechannels 38 are connected to adistribution channel 46, which extends along the periphery of theenclosure 12 at the inside thereof. Thedistribution channel 46 is transverse to the main flow direction of flue gas in thecombustion chamber 14 as indicated by an arrow. Thedistribution channel 34 comprises a number ofnozzles 48. -
Fig. 2 shows an another embodiment. Parts similar to those shown inFig. 1 are indicated by the same reference numeral. The furnace orboiler 10 comprises anenclosure 12 defining acombustion chamber 14. In thewalls 16 of theenclosure 12heat exchanging tubes 18 are provided. Athroat burner 22 is mounted in aburner opening 49 in thewall 20 of theenclosure 12. Theburner 22 receives fuel fromfuel supply line 26. As an air supply for both the primary air and the secondary air a wind-box 50 is provided, which passes the primary air viachannel 52 to the burner and the secondary air viachannels 54 each provided with adamper 56 for controlling the secondary air flow, intochannels 38 and further intodistribution channel 46 havingnozzles 48.Reference numeral 58 indicates the primary flame, while the internal flue gas recirculation, if any, bearsreference numeral 60.
Claims (6)
- Boiler or furnace (10) for combustion of fuel in an air staged combustion mode, comprising an enclosure (12) defining a combustion chamber (14), of which at least a part is provided with heat exchanging tubes (18) for generating a heated fluid, at least one burner (22) for combustion of fuel provided with a fuel supply (26) and a primary air supply (24), and a secondary air supply (32), and an outlet (28) for discharge of flue gas, wherein the secondary air supply (32) is positioned internally of the enclosure (12) downstream of the at least one burner (22).
- Boiler or furnace (10) according to claim 1, wherein the secondary air supply (32) comprises an inlet (38; 54) through a wall of the enclosure (12) in fluid communication with a distribution channel (46) extending along the inner periphery of the enclosure (12) in a direction transverse to the main flow of flue gas during operation, wherein the distribution channel (46) is provided with a plurality of nozzles (48) for injection of secondary air into the flue gas.
- Boiler or furnace (10) according to any one of the preceding claims, wherein the secondary air supply (32) comprises an inlet (38) into the enclosure (12) in the wall (20), wherein the at least one burner (22) is positioned.
- Boiler or furnace (10) according to any one of the preceding claims, wherein the at least one burner (22) is a throat burner provided in a burner opening (30) in a wall (20) of the enclosure (12) and wherein the inlet (54) of the secondary air supply (32) is provided in the burner opening (30).
- Boiler or furnace (10) according to any one of the preceding claims, wherein the inlet (54) is an integral part of the throat burner.
- Boiler or furnace (10) according to any one of the preceding claims, comprising a wind-box (50) for supplying air to the primary air supply and the secondary air supply, wherein the wind-box (50) is provided with control means (56) for controlling the secondary air.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP14188941.0A EP3009741A1 (en) | 2014-10-15 | 2014-10-15 | Boiler or furnace for combustion of fuel in an air staged combustion mode |
CN201410655095.0A CN105674250A (en) | 2014-10-15 | 2014-11-17 | Boiler or furnace for combustion of fuel in air staged combustion mode |
PCT/EP2015/073787 WO2016059117A1 (en) | 2014-10-15 | 2015-10-14 | Boiler or furnace for combustion of fuel in an air staged combustion mode |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP14188941.0A EP3009741A1 (en) | 2014-10-15 | 2014-10-15 | Boiler or furnace for combustion of fuel in an air staged combustion mode |
Publications (1)
Publication Number | Publication Date |
---|---|
EP3009741A1 true EP3009741A1 (en) | 2016-04-20 |
Family
ID=51726405
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP14188941.0A Withdrawn EP3009741A1 (en) | 2014-10-15 | 2014-10-15 | Boiler or furnace for combustion of fuel in an air staged combustion mode |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP3009741A1 (en) |
CN (1) | CN105674250A (en) |
WO (1) | WO2016059117A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110486714A (en) * | 2019-09-18 | 2019-11-22 | 江苏河海新能源股份有限公司 | Plasma low nitrogen combustion apparatus |
CN110848668A (en) * | 2019-09-25 | 2020-02-28 | 西安交通大学 | Natural gas ultralow NOxCombustion system and method |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107869738B (en) * | 2017-12-08 | 2023-12-26 | 广州市东霸节能科技有限公司 | Furnace end |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6138309A (en) * | 1984-07-31 | 1986-02-24 | Obara Yasunori | Combustion equipment |
US5575243A (en) * | 1994-11-30 | 1996-11-19 | The Babcock & Wilcox Company | Low NOx integrated boiler-burner apparatus |
WO2006114654A2 (en) * | 2005-04-25 | 2006-11-02 | TÓTH, Béla | Method for the automatic combustion of solid granular fuels, particularly pellets, and burner for the boiler |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4050877A (en) * | 1974-07-12 | 1977-09-27 | Aqua-Chem, Inc. | Reduction of gaseous pollutants in combustion flue gas |
US4496306A (en) * | 1978-06-09 | 1985-01-29 | Hitachi Shipbuilding & Engineering Co., Ltd. | Multi-stage combustion method for inhibiting formation of nitrogen oxides |
US6837702B1 (en) * | 1994-12-01 | 2005-01-04 | Wartsila Diesel, Inc. | Method of operating a combined cycle power plant |
-
2014
- 2014-10-15 EP EP14188941.0A patent/EP3009741A1/en not_active Withdrawn
- 2014-11-17 CN CN201410655095.0A patent/CN105674250A/en active Pending
-
2015
- 2015-10-14 WO PCT/EP2015/073787 patent/WO2016059117A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6138309A (en) * | 1984-07-31 | 1986-02-24 | Obara Yasunori | Combustion equipment |
US5575243A (en) * | 1994-11-30 | 1996-11-19 | The Babcock & Wilcox Company | Low NOx integrated boiler-burner apparatus |
WO2006114654A2 (en) * | 2005-04-25 | 2006-11-02 | TÓTH, Béla | Method for the automatic combustion of solid granular fuels, particularly pellets, and burner for the boiler |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110486714A (en) * | 2019-09-18 | 2019-11-22 | 江苏河海新能源股份有限公司 | Plasma low nitrogen combustion apparatus |
CN110848668A (en) * | 2019-09-25 | 2020-02-28 | 西安交通大学 | Natural gas ultralow NOxCombustion system and method |
CN110848668B (en) * | 2019-09-25 | 2020-10-27 | 西安交通大学 | Natural gas ultralow NOxCombustion system and method |
Also Published As
Publication number | Publication date |
---|---|
CN105674250A (en) | 2016-06-15 |
WO2016059117A1 (en) | 2016-04-21 |
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