US20050014102A1 - Recuperator burner including recuperator - Google Patents
Recuperator burner including recuperator Download PDFInfo
- Publication number
- US20050014102A1 US20050014102A1 US10/864,156 US86415604A US2005014102A1 US 20050014102 A1 US20050014102 A1 US 20050014102A1 US 86415604 A US86415604 A US 86415604A US 2005014102 A1 US2005014102 A1 US 2005014102A1
- Authority
- US
- United States
- Prior art keywords
- recuperator
- burner
- pleats
- tube
- tube section
- 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
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Classifications
-
- 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
- F23L15/00—Heating of air supplied for combustion
- F23L15/04—Arrangements of recuperators
-
- 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
- F23D14/66—Preheating the combustion air or gas
-
- 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
- F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
- F23L2900/15043—Preheating combustion air by heat recovery means located in the chimney, e.g. for home heating devices
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Definitions
- the invention relates to a ceramic recuperator for a recuperator burner, comprising a tube section, the inner surface and the outer surface of which serving as a heat exchanging surface with flowing fluid and that comprises a plurality of pleats.
- the invention relates to a recuperator burner comprising a burner head, whereon a burner tube yielding into a burner chamber and an exhaust gas guide tube being coaxial to the burner tube are received, wherein between the burner tube and the exhaust gas guide tube a ceramic recuperator having a plurality of pleats is received.
- Such a recuperator burner comprising such a recuperator is known from DE 40 11 190 A1.
- recuperator burners In recuperator burners the efficiency is improved by increasing the heat exchange between the burner feed air and the exhaust gas current of the burner. To this end the recuperator is used that effects a heat exchange between the two flowing gases.
- the recuperator In the recuperator burner as mentioned at the outset the recuperator is made of a ceramic material and, for increasing the heat exchange surface, comprises pleats that extend in longitudinal direction of the recuperator.
- recuperator For effecting a further increase of the heat exchange according to EP 0 803 696 A2 a recuperator is used the heat exchange surface of which is increased by providing naps.
- protrusions and recesses that are oriented in a certain manner are used for increasing the heat exchange surface.
- recuperators all in all an effective heat exchange can be reached when using such recuperators. Due to the high thermal load such recuperators usually consist of a ceramic material. A manufacture using a cast process, in particular a slip cast process, is preferred because of the complicated shaped surface.
- a recuperator burner comprising a burner head, whereon a burner tube yielding into a burner chamber and an exhaust gas guide tube being coaxial to the burner tube are received, wherein between the burner tube and the exhaust gas tube a ceramic recuperator having a plurality of pleats is received, wherein the pleats are spirally wound about the longitudinal axis of the recuperator.
- the recuperator according to the invention comprises a large heat exchange surface for the fluids transferring heat.
- the outer shape of the recuperator is designed in a simple way, thereby also it substantially duplicates the inner shape of the inner wall.
- the pleats are bent gradually, in particular, are shaped undulated.
- the tube section together with an outer tube and an inner tube defines an outer space and an inner space for guiding the fluids, wherein at least between the outer tube and the pleats or between the inner and the pleats there remains a gap.
- the pleats with respect to the longitudinal axis of the recuperator form a helix angle ⁇ that is between 5° and 85°, preferably between 30° and 80°.
- the helix may extend clockwise or counter clockwise with such a helix angle.
- the pleats define a distance L between a wave crest and an adjacent wave crest that is at least twice the thickness d of the tube section, preferably about four times the wall thickness d.
- the amplitude A defined by the difference between the radii of a circle touching the outer surface of the pleats and a circle touching the inner surface of the pleats is larger than the wall thickness of the tube section and is preferably about 2.5 times the wall thickness d.
- the pleat number can be derived and depending thereon an optimized heat transfer can be reached.
- At least one pleat for about 100 mm of an average circumference of the tube section, there is/there are provided at least one pleat, preferably at least two pleats, particularly preferred at least five pleats.
- at least two pleats particularly preferred at least five pleats.
- the pleat number increases accordingly.
- the recuperator is made of a SiC ceramic.
- the recuperator is designed as a cast part, particularly preferred as a slip cast part.
- FIG. 1 a longitudinal sectional view through a recuperator burner according to the invention, shown in simplified representation
- FIG. 2 a perspective view of the recuperator according to the invention, shown in FIG. 1 ;
- FIG. 3 a longitudinal sectional view through the recuperator according to FIG. 2 , shown in enlarged representation;
- FIG. 4 a cross-sectional view through the recuperator according to FIGS. 3 ;
- FIG. 5 a cross-sectional view through a pleat section
- FIG. 6 a simplified representation of the recuperator, showing the definition of the helix angle ⁇ .
- FIG. 1 a recuperator burner according to the invention is shown in longitudinal sectional view and designated in total with numeral 10 .
- the recuperator burner 10 comprises a burner head 12 , whereon an air guide tube, the so-called burner tube 14 , is supported at one end.
- the burner tube 14 yields into a burner chamber 16 .
- An outer tube or exhaust gas guide tube 24 is supported by the burner head 12 coaxially to the burner tube 14 . Between the burner tube 14 and the exhaust gas guide tube 24 a recuperator 30 is received.
- Combustion air is fed to the burner head 12 via a lateral channel 26 , as indicated by arrow 28 and passes into an inner space or cavity 32 defined between the burner tube and the recuperator, and finally, after passing there through, it reaches the burner chamber 16 via through openings (not shown) of the burner tube.
- Fuel is fed via a channel 22 arranged within the burner head 12 into a gas lens 20 , as indicated by arrow 23 , and reaches the burner chamber 16 via a swirl plate 21 .
- an igniting electrode 18 is provided which also protrudes with its free end into the burner chamber 16 .
- an outer space or cavity 38 is defined between the recuperator 30 and the exhaust gas guide tube 24 .
- the combustion gases or flue gases flow through the outer space 38 into the exhaust gas channel 46 of the burner head 12 and thereby heat up the recuperator 30 .
- the combustion air fed via channel 26 flows in opposite direction into the inner space between recuperator 30 and burner tube 14 , as indicated by arrows 40 . In this way there is a heat exchange between the combustion gases streaming within the outer space 38 and the combustion air streaming within the inner space 32 , using the counter current principle.
- the recuperator comprises a tube section 50 serving as a heat exchange surface, whereon a plurality of pleats 36 are provided that are spirally wound about the longitudinal axis 58 of the recuperator.
- the tube section 50 which makes up about three quarters of the length of the recuperator 30 is received at its end facing the burner head 12 by a hollow cylindrical section 52 having a collar, and at the opposite end is also enclosed by a hollow cylindrical section 54 which tapers at its free end and wherein an opening 56 is provided.
- This opening 56 is designed so as to be able to receive the burner tube 14 at its exit end 49 for the flame gases.
- the pleats 36 are configured wave-shaped so that at the inner surface as well at the outer surface of the recuperator 30 alternatingly troughs and crests result.
- the recuperator 30 consists of ceramic, for example of a SiC ceramic and is preferably prepared using a slip casting process.
- the pleats 36 are shaped spirally or helically so that for a length of the tube section 50 of e.g. 400 mm they are rotated by 180°, this corresponding to a helix angle ⁇ of 65°.
- the number of the pleats 36 and the helix angle ⁇ depend on the distance L between adjacent wave crests 59 and on the amplitude A (cf. FIG. 5 ), as well as on the respective case of application, in particular on the current velocity of the fluids, i.e. of the combustion air and of the exhaust gases.
- the pleat distance L e.g. could be 24 mm using an amplitude A of 13 mm and a wall thickness d of 6 mm.
- the gaps 34 and 39 may be dimensioned to have about half the wall thickness of the tube section, in the present case it could be about 3 mm for example.
- recuperator 30 Due to its simple geometrical shape the recuperator 30 can be manufactured with high precision using slip casting processing.
Abstract
Description
- This application claims Convention priority of German patent application serial no. 103 26 951.7 filed on Jun. 12, 2003.
- The invention relates to a ceramic recuperator for a recuperator burner, comprising a tube section, the inner surface and the outer surface of which serving as a heat exchanging surface with flowing fluid and that comprises a plurality of pleats.
- In addition, the invention relates to a recuperator burner comprising a burner head, whereon a burner tube yielding into a burner chamber and an exhaust gas guide tube being coaxial to the burner tube are received, wherein between the burner tube and the exhaust gas guide tube a ceramic recuperator having a plurality of pleats is received.
- Such a recuperator burner comprising such a recuperator is known from
DE 40 11 190 A1. - In recuperator burners the efficiency is improved by increasing the heat exchange between the burner feed air and the exhaust gas current of the burner. To this end the recuperator is used that effects a heat exchange between the two flowing gases. In the recuperator burner as mentioned at the outset the recuperator is made of a ceramic material and, for increasing the heat exchange surface, comprises pleats that extend in longitudinal direction of the recuperator.
- For effecting a further increase of the heat exchange according to EP 0 803 696 A2 a recuperator is used the heat exchange surface of which is increased by providing naps.
- According to EP 0 773 407 A2 protrusions and recesses that are oriented in a certain manner are used for increasing the heat exchange surface.
- All in all an effective heat exchange can be reached when using such recuperators. Due to the high thermal load such recuperators usually consist of a ceramic material. A manufacture using a cast process, in particular a slip cast process, is preferred because of the complicated shaped surface.
- However, herein a problem arises with the generation of delicately structured surfaces, such as necessary for the known recuperators. Delicately structured outer surfaces became rounded more or less and loose their desired delicate structures.
- Therefore, it is a first object of the invention to provide a ceramic recuperator that effects a good heat transfer.
- It is a second object of the invention to disclose a ceramic recuperator that allows a simple, precise and cost effective manufacture.
- It is a third object of the invention to disclose a ceramic recuperator that is highly efficient as a heat exchanger.
- It is a forth object of the invention to disclose a recuperator burner comprising a ceramic recuperator providing a high efficiency.
- It is a fifth burner object of the invention to disclose a recuperator burner comprising a ceramic recuperator that allows a simple, precise and cost effective manufacture.
- These and other objects of the invention are achieved by designing the pleats of a recuperator to be spirally wound about the longitudinal axis of the recuperator.
- In addition, the object of the invention is achieved by a recuperator burner comprising a burner head, whereon a burner tube yielding into a burner chamber and an exhaust gas guide tube being coaxial to the burner tube are received, wherein between the burner tube and the exhaust gas tube a ceramic recuperator having a plurality of pleats is received, wherein the pleats are spirally wound about the longitudinal axis of the recuperator.
- The object of the invention is thus fully achieved.
- The recuperator according to the invention comprises a large heat exchange surface for the fluids transferring heat. The outer shape of the recuperator is designed in a simple way, thereby also it substantially duplicates the inner shape of the inner wall.
- In this way the manufacture using a casting process, in particular a slip casting process, is particularly facilitated, wherein a precise design of the desired surface is guaranteed. By making the pleats spirally wound on the tube section of the recuperator serving as a heat exchange surface, the flow path of the media transferring heat is enlarged, thereby improving effiency.
- Preferably, the pleats are bent gradually, in particular, are shaped undulated.
- In this way a simple manufacture together with a large heat exchange surface can be guaranteed.
- According to a further design of the invention the tube section together with an outer tube and an inner tube defines an outer space and an inner space for guiding the fluids, wherein at least between the outer tube and the pleats or between the inner and the pleats there remains a gap.
- The gap which, preferably is formed between the outer tube and the pleats as well as between the inner tube and the pleats, preferably is at least 0.3 times the wall thickness of the tube section, preferably about half of the wall thickness of the tube section.
- By these measures an increased turbulence is effected, whereby, the heat exchange is improved. When the fluids enter into the pleats, a part of the media flows along the wave troughs, while an other part flows above the wave crests through the remaining gap between the recuperator and the outer tube and the inner tube, respectively, thus through the respective area contractions that result at the crests. After the crests there are cross sectional enlargements, and thereby the current separates, and secondary currents are generated. This part also mixes with the part of the current that can be found within the next wave trough. In this way the generation of interface layers is considerably impaired, and the efficiency is considerably improved.
- According to a further feature of the invention the pleats with respect to the longitudinal axis of the recuperator form a helix angle α that is between 5° and 85°, preferably between 30° and 80°.
- Using such a helix angle depending on the current velocity of the flowing fluids an optimized heat transition can be reached. It will be understood that the helix may extend clockwise or counter clockwise with such a helix angle.
- According to a further preferred embodiment of the invention the pleats define a distance L between a wave crest and an adjacent wave crest that is at least twice the thickness d of the tube section, preferably about four times the wall thickness d.
- In addition, preferably the amplitude A defined by the difference between the radii of a circle touching the outer surface of the pleats and a circle touching the inner surface of the pleats is larger than the wall thickness of the tube section and is preferably about 2.5 times the wall thickness d.
- In this way by designing the pleat shape the pleat number can be derived and depending thereon an optimized heat transfer can be reached.
- According to a further preferred design of the invention for about 100 mm of an average circumference of the tube section, there is/there are provided at least one pleat, preferably at least two pleats, particularly preferred at least five pleats. Herein with an increase of the average diameter also the pleat number increases accordingly.
- In this way by adjusting the pleat number and the rotation angle of the pleats depending thereon an optimized heat transfer can be reached.
- Preferably, the recuperator is made of a SiC ceramic.
- As mentioned before, preferably, the recuperator is designed as a cast part, particularly preferred as a slip cast part.
- It will be understood that the above-mentioned and following features of the invention are not limited to the given combinations, but are applicable in other combinations or taken alone without departing from the scope of the invention.
- Further features and advantages of the invention will become apparent from the following description of a preferred embodiment taken in conjunction with the drawings. In the drawings show:
-
FIG. 1 a longitudinal sectional view through a recuperator burner according to the invention, shown in simplified representation; -
FIG. 2 a perspective view of the recuperator according to the invention, shown inFIG. 1 ; -
FIG. 3 a longitudinal sectional view through the recuperator according toFIG. 2 , shown in enlarged representation; -
FIG. 4 a cross-sectional view through the recuperator according toFIGS. 3 ; -
FIG. 5 a cross-sectional view through a pleat section; and -
FIG. 6 a simplified representation of the recuperator, showing the definition of the helix angle α. - In
FIG. 1 a recuperator burner according to the invention is shown in longitudinal sectional view and designated in total withnumeral 10. - The
recuperator burner 10 comprises aburner head 12, whereon an air guide tube, the so-calledburner tube 14, is supported at one end. Theburner tube 14 yields into aburner chamber 16. An outer tube or exhaustgas guide tube 24 is supported by theburner head 12 coaxially to theburner tube 14. Between theburner tube 14 and the exhaust gas guide tube 24 arecuperator 30 is received. - Combustion air is fed to the
burner head 12 via alateral channel 26, as indicated byarrow 28 and passes into an inner space orcavity 32 defined between the burner tube and the recuperator, and finally, after passing there through, it reaches theburner chamber 16 via through openings (not shown) of the burner tube. Fuel is fed via achannel 22 arranged within theburner head 12 into agas lens 20, as indicated byarrow 23, and reaches theburner chamber 16 via aswirl plate 21. In addition, for igniting the fuel/air mixture an ignitingelectrode 18 is provided which also protrudes with its free end into theburner chamber 16. - Between the
recuperator 30 and the exhaustgas guide tube 24 an outer space orcavity 38 is defined. As shown byarrows 44, the combustion gases or flue gases flow through theouter space 38 into theexhaust gas channel 46 of theburner head 12 and thereby heat up therecuperator 30. The combustion air fed viachannel 26 flows in opposite direction into the inner space betweenrecuperator 30 andburner tube 14, as indicated byarrows 40. In this way there is a heat exchange between the combustion gases streaming within theouter space 38 and the combustion air streaming within theinner space 32, using the counter current principle. - As can be seen from FIGS. 2 to 6 in more detail, the recuperator comprises a
tube section 50 serving as a heat exchange surface, whereon a plurality ofpleats 36 are provided that are spirally wound about thelongitudinal axis 58 of the recuperator. Thetube section 50 which makes up about three quarters of the length of therecuperator 30 is received at its end facing theburner head 12 by a hollowcylindrical section 52 having a collar, and at the opposite end is also enclosed by a hollowcylindrical section 54 which tapers at its free end and wherein anopening 56 is provided. Thisopening 56 is designed so as to be able to receive theburner tube 14 at itsexit end 49 for the flame gases. - As can be seen in particular from
FIGS. 4 and 5 , thepleats 36 are configured wave-shaped so that at the inner surface as well at the outer surface of therecuperator 30 alternatingly troughs and crests result. - The
recuperator 30 consists of ceramic, for example of a SiC ceramic and is preferably prepared using a slip casting process. - The
pleats 36 are shaped spirally or helically so that for a length of thetube section 50 of e.g. 400 mm they are rotated by 180°, this corresponding to a helix angle α of 65°. - The number of the
pleats 36 and the helix angle α depend on the distance L between adjacent wave crests 59 and on the amplitude A (cf.FIG. 5 ), as well as on the respective case of application, in particular on the current velocity of the fluids, i.e. of the combustion air and of the exhaust gases. - When using an average recuperator diameter of about 120 mm, for example there could be provided 21 pleats. Herein the pleat distance L e.g. could be 24 mm using an amplitude A of 13 mm and a wall thickness d of 6 mm.
- During operation hot flame gases exit from
burner chamber 16 via itsexit opening 49 and heat up the exhaustgas guide tube 24. From the end facing the burner combustion air streams into the helically locatedpleats 36 of theinner surface 32, while simultaneously flue gases enter into the spirally shapedpleats 36 of theouter space 38 from the outer end. Herein the helical arrangement effects an enlarged current path along therecuperator 30. In addition, continuously parts of the combustion air steam against the provided pleats on the inner side, as well as exhaust gases on the outer side. A portion of the media, respectively, flows through thegaps pleats 36 and theburner tube 14 and the exhaustgas guide tube 24, respectively. Thus secondary currents are generated by the mixture between the media flowing along the spirally wound pleats 36 and of the media flowing through thegaps gaps tube section 50. - In this way a very good heat exchange between the flue gases and the combustion air is reached.
- Due to its simple geometrical shape the
recuperator 30 can be manufactured with high precision using slip casting processing.
Claims (50)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE10326951.7 | 2003-06-12 | ||
DE10326951A DE10326951A1 (en) | 2003-06-12 | 2003-06-12 | Recuperator burner and recuperator for this purpose |
Publications (1)
Publication Number | Publication Date |
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US20050014102A1 true US20050014102A1 (en) | 2005-01-20 |
Family
ID=33185799
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US10/864,156 Abandoned US20050014102A1 (en) | 2003-06-12 | 2004-06-09 | Recuperator burner including recuperator |
Country Status (3)
Country | Link |
---|---|
US (1) | US20050014102A1 (en) |
EP (1) | EP1486728B1 (en) |
DE (1) | DE10326951A1 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080014537A1 (en) * | 2006-07-13 | 2008-01-17 | Arvind Atreya | Method of waste heat recovery from high temperature furnace exhaust gases |
US20110143292A1 (en) * | 2009-12-16 | 2011-06-16 | Eclipse, Inc. | Burner with improved heat recuperator |
US20110165528A1 (en) * | 2008-09-10 | 2011-07-07 | Five Stein | Recuperator for a radiating tube burner |
US20110244409A1 (en) * | 2008-12-10 | 2011-10-06 | Soichiro Kato | Comubstor |
JP2013194977A (en) * | 2012-03-19 | 2013-09-30 | Spinworks Llc | Radiant tube type heating device |
US20170067634A1 (en) * | 2014-02-21 | 2017-03-09 | WS Wärmeprozesstechnik GmbH | Recuperator burner with auxiliary heat exchanger |
JP2019020028A (en) * | 2017-07-14 | 2019-02-07 | 熱産ヒート株式会社 | Spiral heat exchanger manufacturing method, spiral heat exchanger, and direct fire type heat exchanger-integrated burner |
JP2020159634A (en) * | 2019-03-27 | 2020-10-01 | 東京瓦斯株式会社 | Exhaust heat recovery type burner |
US11365880B2 (en) * | 2014-09-25 | 2022-06-21 | Saint-Gobain Ceramics & Plastics, Inc. | Low NOx, high efficiency, high temperature, staged recirculating burner and radiant tube combustion system |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007048487B4 (en) * | 2007-10-09 | 2009-07-30 | Ibs Industrie-Brenner-Systeme Gmbh | Burner for an industrial furnace |
DE102011103106A1 (en) | 2011-05-25 | 2012-11-29 | Erbicol S.A. | Heat exchanger made of ceramic material, in particular for recuperative burners, and method for its production |
DE102014116126A1 (en) | 2014-11-05 | 2016-05-12 | Noxmat Gmbh | recuperative burner |
DE102015113794A1 (en) | 2015-08-20 | 2017-02-23 | AICHELIN Holding GmbH | Recuperative burner with ceramic recuperator and method of manufacture |
EP3073194A1 (en) | 2015-03-24 | 2016-09-28 | Linde Aktiengesellschaft | Heat exchanging system for a furnace |
IT201600111870A1 (en) * | 2016-11-07 | 2018-05-07 | Esa S P A | SELF-RESEARCHING BURNER |
KR20190130940A (en) | 2018-05-15 | 2019-11-25 | (주)넥스이앤에스 | Helical recuperator and recuperative burner |
KR20240021979A (en) | 2021-06-18 | 2024-02-19 | 셩크 인제니어커라미크 게엠베하 | Recuperator burner with recuperator device for guiding countercurrent fluid |
WO2022263006A1 (en) | 2021-06-18 | 2022-12-22 | Schunk Ingenieurkeramik Gmbh | Recuperator burner with a recuperator for guiding counter-flowing fluids |
Citations (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US249547A (en) * | 1881-11-15 | John a | ||
US343708A (en) * | 1886-06-15 | Retort gas-lamp | ||
US650575A (en) * | 1899-08-31 | 1900-05-29 | Charles W Whitney | Metal tube. |
US770599A (en) * | 1904-09-20 | Half to e | ||
US2115769A (en) * | 1936-08-22 | 1938-05-03 | Henry H Harris | Radiant heating tube |
US2122504A (en) * | 1936-05-02 | 1938-07-05 | Wilson Lee | Heating apparatus |
US2910285A (en) * | 1958-09-30 | 1959-10-27 | Dow Furnace Company | Heat treating furnace |
US2992676A (en) * | 1957-07-10 | 1961-07-18 | Selas Corp Of America | Industrial gas burner |
US3285240A (en) * | 1963-07-10 | 1966-11-15 | Indugas Ges Fur Ind Gasverwend | Industrial gas burner |
US3529812A (en) * | 1967-08-17 | 1970-09-22 | Aichelin Fa J | Burner with air-preheated recovery |
US3636982A (en) * | 1970-02-16 | 1972-01-25 | Patterson Kelley Co | Internal finned tube and method of forming same |
US3696863A (en) * | 1970-01-02 | 1972-10-10 | Itt | Inner-outer finned heat transfer tubes |
US4298333A (en) * | 1977-09-19 | 1981-11-03 | J. Aichelin | Industrial heating installation and method of operation |
US4408983A (en) * | 1980-08-29 | 1983-10-11 | British Gas Corporation | Recuperative burners |
US4589844A (en) * | 1984-07-25 | 1986-05-20 | Advanced Combustion Inc. | Heat exchange apparatus for industrial furnaces |
US4617072A (en) * | 1983-07-30 | 1986-10-14 | Mtu Motoren-Und Turbinen-Union Muenchen Gmbh | Method for producing a composite ceramic body |
US5160258A (en) * | 1989-03-20 | 1992-11-03 | Triline Ab | Device at a heat treatment oven |
US5833450A (en) * | 1995-11-10 | 1998-11-10 | Ws Warmeprozesstechnik Gmbh | Recuperator and recuperator burner |
US20030235798A1 (en) * | 2001-05-10 | 2003-12-25 | Moore Edward E. | U-tube diffusion flame burner assembly having unique flame stabilization |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1551761A1 (en) * | 1967-08-17 | 1970-03-19 | Aichelin Fa J | Industrial burner with recuperative air preheating |
DE4011190A1 (en) * | 1988-10-12 | 1991-10-17 | Ruhrgas Ag | Recuperative burner for industrial plant |
DE19616288A1 (en) | 1996-04-24 | 1997-10-30 | Lbe Beheizungsanlagen Gmbh | Recuperator made of ceramic material |
-
2003
- 2003-06-12 DE DE10326951A patent/DE10326951A1/en not_active Ceased
-
2004
- 2004-05-28 EP EP04012672.4A patent/EP1486728B1/en not_active Not-in-force
- 2004-06-09 US US10/864,156 patent/US20050014102A1/en not_active Abandoned
Patent Citations (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US343708A (en) * | 1886-06-15 | Retort gas-lamp | ||
US770599A (en) * | 1904-09-20 | Half to e | ||
US249547A (en) * | 1881-11-15 | John a | ||
US650575A (en) * | 1899-08-31 | 1900-05-29 | Charles W Whitney | Metal tube. |
US2122504A (en) * | 1936-05-02 | 1938-07-05 | Wilson Lee | Heating apparatus |
US2115769A (en) * | 1936-08-22 | 1938-05-03 | Henry H Harris | Radiant heating tube |
US2992676A (en) * | 1957-07-10 | 1961-07-18 | Selas Corp Of America | Industrial gas burner |
US2910285A (en) * | 1958-09-30 | 1959-10-27 | Dow Furnace Company | Heat treating furnace |
US3285240A (en) * | 1963-07-10 | 1966-11-15 | Indugas Ges Fur Ind Gasverwend | Industrial gas burner |
US3529812A (en) * | 1967-08-17 | 1970-09-22 | Aichelin Fa J | Burner with air-preheated recovery |
US3696863A (en) * | 1970-01-02 | 1972-10-10 | Itt | Inner-outer finned heat transfer tubes |
US3636982A (en) * | 1970-02-16 | 1972-01-25 | Patterson Kelley Co | Internal finned tube and method of forming same |
US4298333A (en) * | 1977-09-19 | 1981-11-03 | J. Aichelin | Industrial heating installation and method of operation |
US4408983A (en) * | 1980-08-29 | 1983-10-11 | British Gas Corporation | Recuperative burners |
US4617072A (en) * | 1983-07-30 | 1986-10-14 | Mtu Motoren-Und Turbinen-Union Muenchen Gmbh | Method for producing a composite ceramic body |
US4589844A (en) * | 1984-07-25 | 1986-05-20 | Advanced Combustion Inc. | Heat exchange apparatus for industrial furnaces |
US5160258A (en) * | 1989-03-20 | 1992-11-03 | Triline Ab | Device at a heat treatment oven |
US5833450A (en) * | 1995-11-10 | 1998-11-10 | Ws Warmeprozesstechnik Gmbh | Recuperator and recuperator burner |
US20030235798A1 (en) * | 2001-05-10 | 2003-12-25 | Moore Edward E. | U-tube diffusion flame burner assembly having unique flame stabilization |
US6872070B2 (en) * | 2001-05-10 | 2005-03-29 | Hauck Manufacturing Company | U-tube diffusion flame burner assembly having unique flame stabilization |
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US20080014537A1 (en) * | 2006-07-13 | 2008-01-17 | Arvind Atreya | Method of waste heat recovery from high temperature furnace exhaust gases |
US9618200B2 (en) * | 2008-09-10 | 2017-04-11 | Fives Stein | Recuperator for a radiating tube burner |
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JP2013194977A (en) * | 2012-03-19 | 2013-09-30 | Spinworks Llc | Radiant tube type heating device |
US20170067634A1 (en) * | 2014-02-21 | 2017-03-09 | WS Wärmeprozesstechnik GmbH | Recuperator burner with auxiliary heat exchanger |
US10161632B2 (en) * | 2014-02-21 | 2018-12-25 | WS Wärmeprozesstechnik GmbH | Recuperator burner with auxiliary heat exchanger |
US11365880B2 (en) * | 2014-09-25 | 2022-06-21 | Saint-Gobain Ceramics & Plastics, Inc. | Low NOx, high efficiency, high temperature, staged recirculating burner and radiant tube combustion system |
JP2019020028A (en) * | 2017-07-14 | 2019-02-07 | 熱産ヒート株式会社 | Spiral heat exchanger manufacturing method, spiral heat exchanger, and direct fire type heat exchanger-integrated burner |
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Also Published As
Publication number | Publication date |
---|---|
EP1486728A3 (en) | 2010-01-27 |
EP1486728A2 (en) | 2004-12-15 |
EP1486728B1 (en) | 2013-09-04 |
DE10326951A1 (en) | 2005-01-13 |
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