EP2846092B1 - Brenner - Google Patents
Brenner Download PDFInfo
- Publication number
- EP2846092B1 EP2846092B1 EP14183751.8A EP14183751A EP2846092B1 EP 2846092 B1 EP2846092 B1 EP 2846092B1 EP 14183751 A EP14183751 A EP 14183751A EP 2846092 B1 EP2846092 B1 EP 2846092B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- burner
- heat
- fuel
- heat pipe
- heat exchanger
- 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.)
- Active
Links
- 239000007800 oxidant agent Substances 0.000 claims description 40
- 239000000446 fuel Substances 0.000 claims description 33
- 239000002826 coolant Substances 0.000 claims description 26
- 238000009833 condensation Methods 0.000 claims description 24
- 230000005494 condensation Effects 0.000 claims description 24
- 238000006243 chemical reaction Methods 0.000 claims description 23
- 238000001816 cooling Methods 0.000 claims description 18
- 238000001704 evaporation Methods 0.000 claims description 15
- 230000008020 evaporation Effects 0.000 claims description 15
- 239000001301 oxygen Substances 0.000 claims description 13
- 229910052760 oxygen Inorganic materials 0.000 claims description 13
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 3
- 229910001092 metal group alloy Inorganic materials 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000003570 air Substances 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 9
- 239000007789 gas Substances 0.000 description 7
- 238000009835 boiling Methods 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000012429 reaction media Substances 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 239000012080 ambient air Substances 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910003251 Na K Inorganic materials 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 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
- F23D14/46—Details, e.g. noise reduction means
- F23D14/72—Safety devices, e.g. operative in case of failure of gas supply
- F23D14/78—Cooling burner parts
-
- 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
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2214/00—Cooling
Definitions
- the invention relates to a burner with a burner housing equipped with feeds for fuel and oxidant, which projects in the intended installation state with a burner tip into a reaction zone and to which a cooling device for cooling the burner tip is assigned.
- Such burners are, for example, externally mixing burners, via which a liquid, solid or gaseous fuel and an oxygen-containing gas are fed into each other in a reaction zone (combustion chamber) separated from one another by flow, mixed together and ignited.
- the burners are provided with a cooling device in which a cooling medium is passed through cooling channels, which run through the projecting into the reaction zone parts of the burner jacket.
- cooling medium is usually used cooling water, such as in the WO 00/70102 A1 described.
- the burner jacket of a burner is equipped with a radially surrounding the outlet nozzles of the reaction media water-bearing tract, which is in flow connection via inlet and outlet lines with a cooling water circuit.
- GB2476253 discloses a fuel injector cooled by a heat pipe.
- heat pipe refers to a closed system in which heat transfer medium is vaporized, which evaporates as a result of the heat supplied in a region of the heat pipe designated here as the "evaporation zone". wherein the heat pipe is designed so that the heat transfer medium at a remote from the evaporation zone portion of the heat pipe, here as Referred to as "condensation zone", condensed by heat exchange with a cooling medium and flows back within the heat pipe.
- the heat transfer medium in the heat pipe in the region of the burner tip absorbs heat, evaporates and is supplied in the gaseous state to the thermally connected to one or more heat exchangers section (condensation zone) in which it condenses while heat to a in the heat exchanger or in the heat exchangers used cooling medium.
- a cooling medium for receiving the heat from the heat pipe for example, a gas, in particular air, or a liquid, for example water, comes into consideration.
- the heat is transferred from the heat pipe to a reaction medium supplied to the burner, ie fuel and / or oxidant.
- the burner according to the invention thus comes without a guided through the burner tip cooling water circuit and the associated problems.
- Heat pipes of the type mentioned here are known per se and are described for example in the patents US Pat. No. 3,229,759 B1 . US Pat. No. 3,532,159 B1 . DE 24 39 442 A1 . EP 0 040 255 A1 described.
- Heat pipes can be adjusted so that they have a valve function during heat transfer. Depending on the boiling or condensation temperature of the heat transfer medium used ensures that a heat transfer takes place only above a predetermined temperature.
- Heat pipes used in the invention may also have the shape of a closed loop or a ring in which or the Heat transfer medium from an evaporation zone into a condensation zone and is passed back through a circuit, such as in the EP 0 040 255 A1 shown. All of these variants can also be used within the scope of the invention.
- Suitable fuels for the burner according to the invention are gaseous fuels, such as natural gas, as well as liquid fuels atomized into an aerosol or fluidized solid particles (dusts).
- the heat transferred from the heat pipe or from the heat pipes is used for preheating fuel and / or oxidant.
- the condensation zone of the heat pipe or the heat pipes is thermally connected to a heat exchanger, which is arranged in a feed line for fuel or for oxidizing agent.
- a heat exchanger which is arranged in a feed line for fuel or for oxidizing agent.
- thermally connect the condensation zone of the heat pipe and the heat pipes with a heat exchanger from an external Coolant is flowed through.
- external cooling medium is understood here a medium that is not used in the context of the combustion process in the reaction chamber. is used.
- an external cooling medium is in particular a gaseous or liquid cooling medium is used, such as air or water, wherein the external cooling medium can also be recycled in turn.
- an external cooling medium flowed through the heat exchanger can also be used to control the temperature of the preheated reaction medium by the external cooling medium as needed, for example, depending on the temperature of the reaction medium or the temperature in the region of the burner tip, is switched on .
- a fan can be used, which transfers the heat supplied from the heat pipe to the ambient air.
- Yet another embodiment of the invention is characterized in that the heat exchanger (s) thermally connected to the condensation zone (s) with the condensation zones of the heat pipe (s) is / are arranged within the burner housing. This embodiment reduces the construction costs and allows the use of comparatively short heat pipes with a high heat transfer capacity.
- such an "internal" heat exchanger can also be used in addition to one of the aforementioned “external” heat exchangers.
- any heat transfer medium used in commercial heat pipes can be used.
- the minimum temperature on the surface of the part of the burner (burner tip) projecting into the reaction chamber is correspondingly increased during burner operation and thus the condensation of at least some of the corrosive constituents of the reaction space atmosphere on the surface of the burner jacket is effectively avoided.
- the energy consumption is reduced when using the burner (compared to water-cooled burners of the same power).
- the invention is suitable both for burners that work with air as an oxidant, as well as for burners, the oxygen-enriched air (with an oxygen content of about 21 vol .-%) or pure oxygen (with an oxygen content of> 95 vol .-%), and burners, in which the oxygen content of the oxidizing agent used can be variably adjusted.
- the burner according to the invention can be used in a large number of different applications, in particular in smelting metallurgy, in furnaces in chemistry, in waste recycling or in glass melting furnaces.
- FIG. 1 shows schematically the structure of a burner according to the invention in longitudinal section.
- the burner 1 comprises a substantially cylindrical (only partially shown in the drawing) burner housing 2, in which a central fuel channel 3 is arranged.
- the fuel channel 3 is fluidly connected via a fuel feed line 4 with a source of fuel, not shown here.
- Coaxial with the fuel channel 3 is in the embodiment according to Fig. 1 an annular channel 6 arranged for oxidizing agent.
- a coaxial arrangement of fuel channel 3 and oxidant channel 6 other burner designs are also conceivable within the scope of the invention, for example a plurality of oxidant channels arranged radially at the fuel channel 3 at equal angular intervals, or parallel within a burner housing juxtaposed fuel and oxidant feeds.
- the oxidant channel 6 is supplied via an oxidant supply line 7 with an oxidizing agent, for example air or oxygen, from a source not shown here.
- an oxidizing agent for example air or oxygen
- the burner 1 projects with its burner tip 8 into a metallurgical reaction space 9, for example a combustion chamber.
- the burner further comprises an ignition device, not shown here, for igniting the fuel-oxidizing agent mixture forming in front of the burner tip 8 in the reaction space 9.
- the burner 1 can be accommodated in an also not shown manner within an exhaust pipe, through which are discharged in the reaction of the fuel with the oxidant fuel gases from the reaction chamber 9.
- the burner 1 is equipped with a cooling device by means of which during the operation of the burner 1, the high thermal load of the burner housing 2 in the region of the burner tip 8 is mitigated.
- the cooling device comprises a plurality of radially on the outside of the oxidant channel 6 at equal angular intervals arranged heat pipes, of which in the embodiment, only the heat pipes 11, 12 are shown.
- the heat pipes 11, 12 are closed fluid systems in which a heat transfer medium between an evaporation zone 13, 14, in which the medium evaporates and thereby absorbs heat from the environment, and a condensation zone 16, 17, in which the medium condenses and while giving off heat to the environment, fluctuates.
- the evaporation zone 13 of the heat pipe 11 and the evaporation zone 14 of the heat pipe 12 are in the region of the burner tip 8 in which a particularly high heat load occurs during operation of the burner 1.
- the condensation zone 16 of the heat pipe 11 and the condensation zone 17 of the heat exchanger 12 (indicated here for reasons of clarity) is located outside the burner housing 2 in the exemplary embodiment.
- In the region of the condensation zones 16, 17 of the heat pipes 11, 12 are two heat exchangers 18, 19 are provided, which are thermally connected to the condensation zones 16, 17.
- the heat transfer medium present in the heat pipes 11, 12 is thermally in contact with the heat transfer medium via the oxidant supply line 7 connected oxidant and connected via the heat exchanger 12 with an external cooling medium, such as air or water, which is brought on demand via a cooling medium line 21.
- an external cooling medium such as air or water
- the valve 22 is opened and fuel, for example natural gas, oil or fluidized coal dust, flows via the fuel supply line 4 and the fuel channel 3 into the reaction space 9.
- fuel for example natural gas, oil or fluidized coal dust
- the valve 23 is opened and oxidizing agent, for example oxygen or air, likewise flows into the reaction space 9 via the oxidant conduit 7 and the oxidant conduit 6.
- oxidizing agent for example oxygen or air
- the heat transferred from the combustion chamber 9 to the burner tip 8 and from there to the heat transfer medium present in the evaporation zones 13, 14 of the heat pipes 11, 12 leads to evaporation of the heat transfer medium.
- the heat transfer medium Via transport channels, not shown here, within the heat pipes 11, 12, the heat transfer medium reaches the respective condensation zone 16, 17, and gives off heat in the heat exchanger 18 to the oxidizing agent introduced in the oxidant supply line 7.
- the heat absorbed by the heat pipes 11, 12 serves in this way for preheating the oxidizing agent; Such preheating can, moreover, be carried out in place of or in addition to a (known per se and therefore not shown here) preheating of the oxidizing agent with the aid of the flue gases discharged from the reaction zone 9.
- the minimum temperature at the outer surface of the burner tip 8 during operation of the burner 1 can be adjusted.
- the boiling point of thermal oils is about 150 ° C to 300 ° C and the specific metal alloys (for example Na-K mixtures) about 800 ° C.
- the burner 1 can therefore be operated at considerably higher operating temperatures than conventional, water-cooled burner.
- the temperature on the outer surface of the burner tip 8 can be maintained at a value which is above the dew point of corrosive constituents of the atmosphere in the reaction space 9.
- the condensation zones 16, 17 of the heat pipes 11, 12 to heat exchanger 19 with a cooling medium can be thermally connected, which can be brought on demand via the cooling medium line 21 by opening the valve 23 and possibly switching on a conveyor, not shown here.
- the cooling medium is, for example, ambient air or water;
- the heat exchanger 19 is a fan which blows ambient air onto the outer surface of the heat pipes 11, 12 in the region of the condenser zones 16, 17.
- the invention is suitable both for burners that use air as the oxidant, and for burners that use oxygen (with a purity of ⁇ 95 vol .-%) as the oxidant.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL14183751T PL2846092T3 (pl) | 2013-09-07 | 2014-09-05 | Palnik |
RS20181265A RS57898B1 (sr) | 2013-09-07 | 2014-09-05 | Gorionik |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102013014988.6A DE102013014988A1 (de) | 2013-09-07 | 2013-09-07 | Brenner |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2846092A2 EP2846092A2 (de) | 2015-03-11 |
EP2846092A3 EP2846092A3 (de) | 2015-03-25 |
EP2846092B1 true EP2846092B1 (de) | 2018-07-25 |
Family
ID=51492200
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP14183751.8A Active EP2846092B1 (de) | 2013-09-07 | 2014-09-05 | Brenner |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP2846092B1 (pl) |
DE (1) | DE102013014988A1 (pl) |
ES (1) | ES2692353T3 (pl) |
PL (1) | PL2846092T3 (pl) |
RS (1) | RS57898B1 (pl) |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1027719A (pl) | 1963-12-02 | |||
US3532159A (en) | 1968-07-24 | 1970-10-06 | Trw Inc | High performance heat pipe |
GB1272832A (en) * | 1968-10-18 | 1972-05-03 | Eberspaecher J | Combustion apparatus in which carbonisation of the combustion chambers thereof is prevented |
JPS5723194B2 (pl) | 1973-08-17 | 1982-05-17 | ||
US4052144A (en) * | 1976-03-31 | 1977-10-04 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Fuel combustor |
DE2619177C2 (de) * | 1976-04-30 | 1977-09-29 | E. Schlüter Fachhandel für Schweißtechnik, 3014 Laatzen | Schweiß-, Schneid-, Heiz- oder Flämmbrenner |
DE2916635C3 (de) | 1979-04-25 | 1982-08-26 | Messer Griesheim Gmbh, 6000 Frankfurt | Brennerkopf eines Brennstoff-Sauerstoff-Brenners |
CA1129406A (en) | 1980-05-19 | 1982-08-10 | Masaaki Munekawa | Device for releasing heat |
US4516631A (en) * | 1981-11-04 | 1985-05-14 | Combustion Engineering, Inc. | Nozzle cooled by heat pipe means |
DE3220482A1 (de) * | 1982-05-29 | 1983-12-01 | Buderus Ag, 6330 Wetzlar | Vorrichtung zum vorwaermen und/oder verdampfen des brennstoffes bei oelbrennern |
FR2583144B1 (fr) * | 1985-06-10 | 1989-05-12 | Sofresid | Perfectionnements apportes aux bruleurs autorecuperateurs |
DE8605274U1 (de) * | 1986-02-27 | 1986-05-28 | Joh. Vaillant Gmbh U. Co, 5630 Remscheid | Gasbrenner |
US4736693A (en) * | 1987-07-31 | 1988-04-12 | Shell Oil Company | Partial combustion burner with heat pipe-cooled face |
DE29512230U1 (de) | 1995-07-28 | 1996-12-19 | AGA AB, Lidingö | Brenner für die Feuerpolitur von Glas |
DE19922509A1 (de) | 1999-05-15 | 2000-11-23 | Messer Griesheim Gmbh | Vorrichtung und Verfahren zur Eindüsung von Erdgas und/oder Sauerstoff |
DE10154868A1 (de) * | 2001-11-08 | 2003-06-05 | Bosch Gmbh Robert | Vorrichtung zum Verbrennen eines fluidischen Brennstoffes |
DE102005029317A1 (de) | 2005-06-22 | 2006-12-28 | Linde Ag | Vorrichtung zum Einleiten von Stoffen in einen Reaktionsraum |
DE102006034007A1 (de) * | 2006-07-22 | 2008-02-07 | Messer Group Gmbh | Verfahren und Vorrichtung zum Eintragen eines Mediums in einen thermischen Behandlungsraum |
US20110100009A1 (en) * | 2009-10-30 | 2011-05-05 | Nuovo Pignone S.P.A. | Heat Exchanger for Direct Evaporation in Organic Rankine Cycle Systems and Method |
GB2476253A (en) * | 2009-12-17 | 2011-06-22 | Rolls Royce Plc | Fuel Injector Cooled by a Heat Pipe |
-
2013
- 2013-09-07 DE DE102013014988.6A patent/DE102013014988A1/de not_active Ceased
-
2014
- 2014-09-05 EP EP14183751.8A patent/EP2846092B1/de active Active
- 2014-09-05 PL PL14183751T patent/PL2846092T3/pl unknown
- 2014-09-05 ES ES14183751.8T patent/ES2692353T3/es active Active
- 2014-09-05 RS RS20181265A patent/RS57898B1/sr unknown
Non-Patent Citations (1)
Title |
---|
None * |
Also Published As
Publication number | Publication date |
---|---|
DE102013014988A1 (de) | 2015-03-26 |
EP2846092A3 (de) | 2015-03-25 |
EP2846092A2 (de) | 2015-03-11 |
ES2692353T3 (es) | 2018-12-03 |
RS57898B1 (sr) | 2019-01-31 |
PL2846092T3 (pl) | 2019-02-28 |
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