EP1060346A2 - Verfahren und vorrichtung zur verbrennung von flüssigbrennstoff - Google Patents
Verfahren und vorrichtung zur verbrennung von flüssigbrennstoffInfo
- Publication number
- EP1060346A2 EP1060346A2 EP97949901A EP97949901A EP1060346A2 EP 1060346 A2 EP1060346 A2 EP 1060346A2 EP 97949901 A EP97949901 A EP 97949901A EP 97949901 A EP97949901 A EP 97949901A EP 1060346 A2 EP1060346 A2 EP 1060346A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- porous
- liquid fuel
- mixture
- combustion
- agent
- 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.)
- Granted
Links
Classifications
-
- 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
- F23C99/00—Subject-matter not provided for in other groups of this subclass
- F23C99/006—Flameless combustion stabilised within a bed of porous heat-resistant material
Definitions
- EP 0 524 736 A2 discloses a method and a device for carrying out a controlled reaction in a porous matrix.
- gas or steam is conducted from a space m of tubular porous means extending vertically upward therefrom.
- the combustion takes place within the porous medium.
- the heat generated during combustion flows predominantly downstream and enters another room. -
- This method is not suitable for burning liquid fuels.
- the position of the flame front in the porous body is unstable.
- a device for regulating the volume flow coupled to a temperature measuring device is required for position stabilization.
- the heat generated in the known method is incompletely transferred to the surrounding medium by convection. Preheating of the combustion mixture, which increases the efficiency, does not take place. Gas or steam residues remaining in the room after switching off can disadvantageously contribute to spontaneous combustion.
- the known evaporator is disadvantageous in several ways. Because the mixture with air only takes place after the oil has evaporated, a large distance is required to form a homogeneous air / oil mixture. Because of the suction of the oil into the porous plate based on capillary forces, the porous plate must be of very fine pores. However, this means that it is clogged by impurities contained in the oil and must therefore be cleaned regularly. In order to provide a sufficient amount of oil vapor, the porous plate must have a relatively large area that is in full contact with an oil supply. This requirement counteracts a compact design of the known oil burner. Except- This means that it is not possible to start up a burner that has been combined with this evaporator because the formation of the oil vapor takes some time. After the burner has been switched off, an oil vapor / air mixture remains in the evaporator, which can lead to undesired combustion.
- the liquid fuel is distributed by means of a distribution device and transferred to a downstream reactor with a porous agent having a communicating pore space, the Peclet number of which permits flame development within the porous agent.
- the method according to the invention enables a particularly efficient and low-pollution combustion of the liquid fuel used.
- a gaseous oxidizing agent in particular air, is fed to the distribution device and / or the porous agent to form a mixture consisting of the liquid fuel and the oxidizing agent.
- the distribution device can have a device for atomizing the liquid fuel.
- the device for atomization can, for example, be washed around by a stream of gaseous oxidizing agent.
- the atomization device advantageously has a Nozzle that is supplied with liquid fuel under pressure.
- the atomization device can also have a 2-substance nozzle, the liquid fuel and pressurized oxidizing agent are supplied. - This forms a first mixture consisting of oxidizing agent and liquid fuel, which can be enriched with additional oxidizing agent.
- the atomizing device is expediently arranged in the vicinity of the porous agent. It can be moved back and forth in relation to the porous medium. If the porous means is cylindrical, the atomizing device is advantageously arranged in the cylinder axis.
- the reactor has a housing which accommodates the porous agent, the housing being able to surround the porous element and the device for evaporation.
- the porous medium is expediently surrounded by a heat exchanger.
- the porous medium is arranged below the distribution device, so that a counterflow which is produced during combustion and is directed counter to the mass flow is formed. This enables the mixture supplied by the mass flow to be preheated. In addition, the counterflow slows down the mass flow. This keeps the position of the flame front stable.
- FIG. 4 shows a schematic cross section through a third exemplary embodiment of a device according to the invention
- the porous medium 6 extends over an essential section of the housing 14.
- a mixture inlet side 15 of the porous medium 6 is here directly supplied with liquid fuel emerging from the liquid fuel nozzle 11.
- the mixing, homogenization and evaporation of the mixture takes place in the vicinity of the inlet side 15 of the porous body.
- the mass flow is directed vertically downward.
- the combustion creates a counterflow, which is directed vertically upwards.
- the counterflow slows down the mass flow. As a result, the position of the flame front in the porous medium is kept stable.
- the 2-substance nozzle 17 consists of a liquid fuel nozzle 11 which is surrounded by an air nozzle 18.
- the air nozzle 18 is provided with openings 19 for sucking in air.
- the air / liquid fuel mixture exits through an opening 20 provided in the air nozzle 18.
- FIG. 6a shows a cross section through a distributor 2.
- This essentially consists of a cylinder 21, the interior of which is connected to the environment via radially arranged nozzles 22 Connection is established.
- the arrangement of the nozzles 22 is particularly clear from Fig. 6b.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Spray-Type Burners (AREA)
- Feeding And Controlling Fuel (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Wick-Type Burners And Burners With Porous Materials (AREA)
- Combustion Of Fluid Fuel (AREA)
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19646957A DE19646957B4 (de) | 1996-11-13 | 1996-11-13 | Verfahren und Vorrichtung zur Verbrennung von Flüssigbrennstoff |
DE19646957 | 1996-11-13 | ||
PCT/DE1997/002622 WO1998021523A2 (de) | 1996-11-13 | 1997-11-10 | Verfahren und vorrichtung zur verbrennung von flüssigbrennstoff |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1060346A2 true EP1060346A2 (de) | 2000-12-20 |
EP1060346B1 EP1060346B1 (de) | 2003-02-05 |
Family
ID=7811583
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP97949901A Expired - Lifetime EP1060346B1 (de) | 1996-11-13 | 1997-11-10 | Verfahren und vorrichtung zur verbrennung von flüssigbrennstoff |
Country Status (12)
Country | Link |
---|---|
US (1) | US6257868B1 (de) |
EP (1) | EP1060346B1 (de) |
JP (1) | JP4029179B2 (de) |
CN (1) | CN1227476C (de) |
AT (1) | ATE232281T1 (de) |
CA (1) | CA2270971A1 (de) |
DE (2) | DE19646957B4 (de) |
DK (1) | DK1060346T3 (de) |
EA (1) | EA001328B1 (de) |
ES (1) | ES2195188T3 (de) |
PT (1) | PT1060346E (de) |
WO (1) | WO1998021523A2 (de) |
Families Citing this family (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT406414B8 (de) * | 1998-02-27 | 2000-07-25 | Windhager Zentralheizung Gmbh | Vorrichtung in mit flüssigen brennstoffen betriebenen heizungsanlagen |
DE19951000C2 (de) * | 1999-10-22 | 2001-08-16 | Bosch Gmbh Robert | Strahlungsbrenner mit einem porösen Brennkörper |
CA2449205C (en) | 2001-06-02 | 2010-05-18 | Gvp Gesellschaft Zur Vermarktung Der Porenbrennertechnik Mbh | Method and device for low-emission non-catalytic combustion of a liquid fuel |
DE10230149B4 (de) * | 2002-07-04 | 2008-08-07 | Sgl Carbon Ag | Vorrichtung zur Erzeugung von Wasserstoff |
DE10246231A1 (de) * | 2002-10-04 | 2004-04-15 | Robert Bosch Gmbh | Nachbrenneinrichtung |
US7101175B2 (en) * | 2003-04-04 | 2006-09-05 | Texaco Inc. | Anode tailgas oxidizer |
US7235217B2 (en) * | 2003-04-04 | 2007-06-26 | Texaco Inc. | Method and apparatus for rapid heating of fuel reforming reactants |
CA2436480A1 (en) * | 2003-07-31 | 2005-01-31 | University Technologies International Inc. | Porous media gas burner |
JP4617079B2 (ja) * | 2003-12-19 | 2011-01-19 | Jx日鉱日石エネルギー株式会社 | 改質器用バーナおよび燃料電池システム |
DE102004049903B4 (de) * | 2004-10-13 | 2008-04-17 | Enerday Gmbh | Brennervorrichtung mit einem Porenkörper |
US8177545B2 (en) * | 2004-12-17 | 2012-05-15 | Texaco Inc. | Method for operating a combustor having a catalyst bed |
DE102005004062A1 (de) * | 2005-01-21 | 2006-07-27 | Deutsches Zentrum für Luft- und Raumfahrt e.V. | Porenkörpereinrichtung für einen Porenbrenner, Verfahren zur Herstellung eines Porenkörpers für einen Porenbrenner und Porenbrenner |
DE102007015753B4 (de) | 2007-03-30 | 2018-08-09 | Khs Gmbh | Schrumpftunnel, Schrumpfgaserhitzer und Verfahren zum Aufschrumpfen von Schrumpffolien auf Verpackungen oder Verpackungseinheiten |
US7493876B2 (en) * | 2007-07-11 | 2009-02-24 | Joseph Robert Strempek | Passive mixing device for staged combustion of gaseous boiler fuels |
TWI450439B (zh) * | 2009-10-22 | 2014-08-21 | Atomic Energy Council | 應用於高溫燃料電池之多孔性介質燃燒器 |
CN101900332B (zh) * | 2010-05-07 | 2011-12-28 | 大连海事大学 | 蓄热式超低热值燃气处理及能量利用装置 |
DE102011119162A1 (de) | 2011-11-23 | 2013-05-23 | Man Truck & Bus Ag | Wärmetauscher sowie Anordnung eines Wärmetauschersin einem Abgaskanal einer Brennkraftmaschine, insbesondere einer Brennkraftmaschine eines Fahrzeuges |
CN102563641B (zh) * | 2011-12-30 | 2014-11-05 | 西安交通大学 | 一种液体燃料蓄热式燃烧器 |
US9976740B2 (en) * | 2012-06-12 | 2018-05-22 | Board of Regents of the Nevada Systems of Higher Educations, on Behalf of the University of Nevada, Reno | Burner |
WO2015123381A1 (en) * | 2014-02-14 | 2015-08-20 | Clearsign Combustion Corporation | Down-fired burner with a perforated flame holder |
DE102014209529A1 (de) * | 2014-05-20 | 2015-11-26 | Siemens Aktiengesellschaft | Verbrennung von Lithium bei unterschiedlichen Temperaturen, Drücken und Gasüberschüssen mit porösen Rohren als Brenner |
CN105509044B (zh) * | 2014-09-26 | 2018-05-04 | 承德坤元环保科技有限公司 | 一种燃油气化燃烧器的制造方法 |
DE102014117115A1 (de) * | 2014-11-23 | 2016-05-25 | Webasto SE | Verdampferanordnung |
US11255538B2 (en) * | 2015-02-09 | 2022-02-22 | Gas Technology Institute | Radiant infrared gas burner |
US10539326B2 (en) | 2016-09-07 | 2020-01-21 | Clearsign Combustion Corporation | Duplex burner with velocity-compensated mesh and thickness |
US20220389872A1 (en) * | 2020-07-23 | 2022-12-08 | Sierra Turbines Inc. | Additively manufactured gas turbine fuel injector ring and uni-body turbine engine |
CN116293676B (zh) * | 2023-05-18 | 2023-08-01 | 佛山仙湖实验室 | 一种多孔介质燃烧装置、氨气燃烧系统及燃烧控制方法 |
Family Cites Families (17)
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US1846978A (en) * | 1925-10-02 | 1932-02-23 | Arthur R Parker | Method for burning fluid fuel |
US2095065A (en) | 1933-01-25 | 1937-10-05 | Joseph W Hays | Surface combustion process |
DE637940C (de) * | 1933-06-23 | 1936-11-06 | Degussa | Einrichtung zur flammenlosen Verbrennung von gasfoermigen, fluessigen oder staubfoermigen Brennstoffen in OEfen |
US4047876A (en) * | 1975-03-24 | 1977-09-13 | Comstock & Wescott, Inc. | Catalytic fuel combustion apparatus and method |
GB1547810A (en) * | 1975-03-24 | 1979-06-27 | Comstock & Wescott | Catalytic combustion apparatus and method and catalyst therefor |
CS197610B1 (en) * | 1975-11-18 | 1980-05-30 | Vaclav Rybar | High-grade fuel combusting device |
JPS584010Y2 (ja) * | 1976-06-03 | 1983-01-24 | ダイキン工業株式会社 | ポット式燃焼器 |
GB2041181B (en) | 1978-12-29 | 1983-08-17 | Hutni Druhovyroba | Flameless combustion method and a boiler utilizing such method |
DE3332572C2 (de) * | 1983-09-09 | 1986-10-30 | Insumma Projektgesellschaft mbH, 8500 Nürnberg | Brennwertgerät für Kohlenwasserstoffe |
US4643667A (en) * | 1985-11-21 | 1987-02-17 | Institute Of Gas Technology | Non-catalytic porous-phase combustor |
US5141432A (en) * | 1990-07-18 | 1992-08-25 | Radian Corporation | Apparatus and method for combustion within porous matrix elements |
ES2111048T3 (es) * | 1991-07-05 | 1998-03-01 | Thermatrix Inc A Delaware Corp | Metodo y aparato para la reaccion controlada en una matriz de reaccion. |
US5165884A (en) * | 1991-07-05 | 1992-11-24 | Thermatrix, Inc. | Method and apparatus for controlled reaction in a reaction matrix |
DE4317554C2 (de) | 1993-05-26 | 1997-03-06 | Fraunhofer Ges Forschung | Warmwasserbereiter |
DE4322109C2 (de) * | 1993-07-02 | 2001-02-22 | Franz Durst | Brenner für ein Gas/Luft-Gemisch |
US5624252A (en) * | 1995-12-26 | 1997-04-29 | Carrier Corporation | Low no burner |
US5890886A (en) * | 1997-07-21 | 1999-04-06 | Sulzer Chemtech Ag | Burner for heating systems |
-
1996
- 1996-11-13 DE DE19646957A patent/DE19646957B4/de not_active Expired - Lifetime
-
1997
- 1997-11-10 CA CA002270971A patent/CA2270971A1/en not_active Abandoned
- 1997-11-10 WO PCT/DE1997/002622 patent/WO1998021523A2/de active IP Right Grant
- 1997-11-10 CN CNB971996938A patent/CN1227476C/zh not_active Expired - Fee Related
- 1997-11-10 DK DK97949901T patent/DK1060346T3/da active
- 1997-11-10 ES ES97949901T patent/ES2195188T3/es not_active Expired - Lifetime
- 1997-11-10 PT PT97949901T patent/PT1060346E/pt unknown
- 1997-11-10 EP EP97949901A patent/EP1060346B1/de not_active Expired - Lifetime
- 1997-11-10 AT AT97949901T patent/ATE232281T1/de not_active IP Right Cessation
- 1997-11-10 EA EA199900465A patent/EA001328B1/ru not_active IP Right Cessation
- 1997-11-10 JP JP52203698A patent/JP4029179B2/ja not_active Expired - Fee Related
- 1997-11-10 DE DE59709288T patent/DE59709288D1/de not_active Expired - Fee Related
- 1997-11-10 US US09/308,202 patent/US6257868B1/en not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
See references of WO9821523A2 * |
Also Published As
Publication number | Publication date |
---|---|
JP2001504204A (ja) | 2001-03-27 |
DE59709288D1 (de) | 2003-03-13 |
ATE232281T1 (de) | 2003-02-15 |
DE19646957B4 (de) | 2005-03-17 |
PT1060346E (pt) | 2003-06-30 |
EA001328B1 (ru) | 2001-02-26 |
EP1060346B1 (de) | 2003-02-05 |
JP4029179B2 (ja) | 2008-01-09 |
CN1227476C (zh) | 2005-11-16 |
WO1998021523A3 (de) | 1998-11-12 |
DE19646957A1 (de) | 1998-05-14 |
WO1998021523A2 (de) | 1998-05-22 |
ES2195188T3 (es) | 2003-12-01 |
DK1060346T3 (da) | 2003-05-26 |
US6257868B1 (en) | 2001-07-10 |
EA199900465A1 (ru) | 1999-12-29 |
CN1237239A (zh) | 1999-12-01 |
CA2270971A1 (en) | 1998-05-22 |
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