EP2844920B1 - Gasvormischungsbrenner - Google Patents

Gasvormischungsbrenner Download PDF

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Publication number
EP2844920B1
EP2844920B1 EP13716263.2A EP13716263A EP2844920B1 EP 2844920 B1 EP2844920 B1 EP 2844920B1 EP 13716263 A EP13716263 A EP 13716263A EP 2844920 B1 EP2844920 B1 EP 2844920B1
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EP
European Patent Office
Prior art keywords
burner
ionization
fiber based
gas
deck
Prior art date
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Active
Application number
EP13716263.2A
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English (en)
French (fr)
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EP2844920A1 (de
Inventor
Dirk Ten Hoeve
Wilhelm Salvatore VAN DEN BERG
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bekaert Combustion Technology BV
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Bekaert Combustion Technology BV
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Priority to EP13716263.2A priority Critical patent/EP2844920B1/de
Publication of EP2844920A1 publication Critical patent/EP2844920A1/de
Application granted granted Critical
Publication of EP2844920B1 publication Critical patent/EP2844920B1/de
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23N—REGULATING OR CONTROLLING COMBUSTION
    • F23N5/00—Systems for controlling combustion
    • F23N5/02—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium
    • F23N5/022—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using electronic means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23N—REGULATING OR CONTROLLING COMBUSTION
    • F23N5/00—Systems for controlling combustion
    • F23N5/02—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium
    • F23N5/12—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using ionisation-sensitive elements, i.e. flame rods
    • F23N5/123—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using ionisation-sensitive elements, i.e. flame rods using electronic means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23N—REGULATING OR CONTROLLING COMBUSTION
    • F23N5/00—Systems for controlling combustion
    • F23N5/02—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium
    • F23N5/14—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using thermo-sensitive resistors
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23N—REGULATING OR CONTROLLING COMBUSTION
    • F23N5/00—Systems for controlling combustion
    • F23N5/02—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium
    • F23N5/14—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using thermo-sensitive resistors
    • F23N5/143—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using thermo-sensitive resistors using electronic means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23N—REGULATING OR CONTROLLING COMBUSTION
    • F23N5/00—Systems for controlling combustion
    • F23N5/16—Systems for controlling combustion using noise-sensitive detectors

Definitions

  • the invention relates to a gas premix burner with a fiber based burner deck.
  • An ionization pen measuring the flame current is used to determine the air to gas ratio.
  • the air to gas ratio of the gas premix burner according to the invention can be controlled over a broader burner load range by means of a control system using an ionization pen as sensor.
  • Such gas premix burner can e.g. be used in boilers or in instantaneous water heaters.
  • Detection of the ionization current in the flame of a gas premix burner by means of an ionization pen is commonly used as a way to detect whether or not ignition has occurred.
  • the ionization current is not only used to detect burner ignition, but its value is also used as a means for flame control, and more precisely for the control of the air to gas premix ratio.
  • DE19632983 discloses an ionization pen to measure the flame current and an associated regulating device in a gas burner, wherein an air to gas ratio reference value for low emissions is set by means of an ionization electrode.
  • Gas premix burners with fiber based burner decks are known in the state of the art. Such burners can have a metal fiber based knitted or woven fabric as burner deck positioned on a perforated plate or woven screen which is acting as gas distribution plate. It is a benefit of such burners that the metal fiber based burner deck (e.g. a knitted or woven fabric) can freely expand when hot. Such burners are e.g. known from US4657506 and WO2004/092647 . Document US 4900245 discloses a gas premix burner according to the preamble of claim 1.
  • the ionization current of gas premix burners should be readily and reliably measurable over the load range of the burner. It is a problem, also with gas premix burners with a fiber based burner deck, that in the low power range of the burner the ionization current drops drastically which is rendering flame control by means of ionization current measurement unreliable in the low power range of gas premix burners. For a number of applications it is desirable that burners can operate in a broad load range, and that air to gas ratio control by means of measurement of ionization current with an ionization pen can be performed over the broad load range.
  • the primary objective of the invention is to provide a gas premix burner with a fiber based burner deck that is allowing control of air to gas ratio over a broad load range of the burner by means of the ionization current as measured by an ionization pen.
  • a gas premix burner comprising:
  • the fiber based burner deck is thicker in a region of at least 5 mm, preferably in a region of at least 8 mm, more preferably in a region of at least 12 mm, at both sides of at least 50%, and preferably of at least 65%, more preferably of at least 85% of the length of the perpendicular projection of the ionization pen onto the burner deck. And even more preferably the fiber based burner deck is thicker in the indicated regions around the full length of the ionization pen and even more preferred over 120% of the length of the ionization pen.
  • the fiber based burner deck has a same mass per surface area over the full surface of the burner deck.
  • the burner deck is less compressed in the at least part of the region where the ionization pen is located compared to other regions of the fiber based burner deck, resulting in it that the fiber based burner deck is thicker in the at least part of the region where the ionization pen is located compared to other regions of the fiber based burner deck.
  • "Less compressed” includes that the burner deck can be not compressed in the at least part of the region where the ionization pen is located and compressed in other regions of the fiber based burner deck. It also includes that the burner deck is compressed to a lesser degree in the at least part of the region where the ionization pen is located compared to other regions of the fiber based burner deck.
  • the thickness of the fiber based burner deck in at least part of the region where the ionization pen is located is at least 40%, preferably at least 50%, even more preferably at least 60% higher, even more preferably at least 100% higher and still even more preferred 150% higher than the average of the thickness outside said at least part of said region where the ionization pen is located.
  • a larger difference in thickness increases the positive effects of the invention. Such effects are especially remarkable as of a 40% higher thickness of the fiber based burner deck at the ionization pen; and even more pronounced as of a 60% higher thickness; and still even more pronounced as of 100% higher thickness and yet even more pronounced as of a 150% higher thickness.
  • the porosity of the fiber based burner deck where it is thicker in at least part of the region where the ionization pen is located is less than 92%. It is a benefit of this feature that risk is absent of flashback of the flame into the mixing chamber under the fiber based burner deck and under the perforated plate, woven wire mesh or expanded metal sheet.
  • the average porosity of the fiber based burner deck outside the at least part of the region where the ionization pen is located is higher than 75%, but preferably below 85%.
  • This range of porosities has the benefit that good and clean combustion with low emissions (of NOX) is obtained.
  • the burner load range over which the ionization pen can be used to modulate the air to gas ratio is further extended in a synergetic way, as the burner can be operated at higher loads by this feature.
  • the fiber based burner deck can comprise metal fibers.
  • metal fibers are stainless steel fibers.
  • a specifically preferred range of stainless steel fibers are chromium and aluminium comprising stainless steel fibers as in DIN 1.4767, e.g. as are known under the trademark FeCrAlloy.
  • Metal fibers for the burner deck e.g. stainless steel fibers, with a diameter less than 40 micrometers, e.g. less than 25 micrometers, can be obtained by a bundle drawing technique.
  • This technique is disclosed e.g. in US-A-2050298 , US-A-3277564 and in US-A-3394213 .
  • Metal wires are forming the starting material and are covered with a coating such as iron or copper.
  • a bundle of these covered wires is subsequently enveloped in a metal pipe. Thereafter the thus enveloped pipe is reduced in diameter via subsequent wire drawing steps to come to a composite bundle with a smaller diameter.
  • the subsequent wire drawing steps may or may not be alternated with an appropriate heat treatment to allow further drawing.
  • the initial wires have been transformed into thin fibers which are embedded separately in the matrix of the covering material.
  • a bundle preferably comprises no more than 2000 fibers, e.g. between 500 and 1500 fibers.
  • the covering material can be removed e.g. by solution in an adequate pickling agent or solvent. The final result is the naked fiber bundle.
  • metal fibers for the burner deck such as stainless steel fibers can be manufactured in a cost effective way by machining a thin plate material.
  • a strip of a thin metal plate is the starting material. This strip is wound around the cylindrical outer surface of a rotatably supported main shaft a number of times and is fixed thereto. The main shaft is rotated at constant speed in a direction opposite to that in which the plate material is wound.
  • a cutter having an edge line expending perpendicularly to the axis of the main shaft is fed at constant speed. The cutter has a specific face angle parallel to the axis of the main shaft. The end surface of the plate material is cut by means of the cutter.
  • Another alternative way of producing metal fibers is machining fibers from a solid block of metal.
  • ceramic fibers can be used in the fiber based burner deck.
  • the fiber based burner deck can e.g. comprise or be a woven fabric or a knitted fabric or a braided fabric comprising yarns with e.g. metal fibers, preferably stainless steel fibers.
  • the yarns can be spun from stretchbroken fibers (such as bundle drawn stretch broken fibers) or yarns made from shaved or machined fibers.
  • the yarns can be plied yarns, e.g. two ply, three ply...
  • Preferred fabrics made from metal fibers have a weight of between 0.6 and 3 kg/m 2 ; preferably between 0.7 and 3 kg/m 2 , even more preferred between 1.2 and 2.5 kg/m 2 .
  • Alternative fiber based burner decks that can be used in the invention can comprise or can be nonwovens, e.g. comprising metal fibers (preferably stainless steel fibers).
  • the nonwovens can be consolidated by different techniques (e.g. needle punching) and can be sintered or not sintered.
  • the gas premix burner according to the invention can be provided in a wide range of different shapes. Examples are flat burners, cylindrical burners and burners that have a conical or frustoconical shape. As known by the person skilled in the art a flat burner can have and mostly has a curved shape or can even have an undulated shape.
  • the class of flat burners is distinguished from the other main class of gas premix burners comprising burners that have a conical, cylindrical or frustoconical shape.
  • the gas premix burner comprises a control system.
  • the control system uses the ionization current measured by the ionization pen as indication for the gas to air ratio and as input value to modulate the air to gas ratio of the premix supply to the burner.
  • the ionization current depends on the burner load (as determined by the amount of gas supply) and the air to gas ratio in the gas premix supply.
  • the ionization current can be reliably measured, and knowing the burner load (amount of gas supply) the air to gas ratio of the premix can be derived from the ionization current as measured by the ionization pen.
  • a correct air to gas ratio of the burner is required to obtain clean combustion.
  • the modulation of the premix supply can e.g. be performed by means of volume control of the supply of or air to the premix in order to obtain for each burner load (determined by the amount of gas supply) the correct air to gas ratio leading to clean and optimum combustion.
  • a second aspect of the invention is a method to control the air to gas ratio of a gas premix burner, wherein a gas premix burner is used as in the first aspect of the invention and wherein the ionization current measured by means of the ionization pen is used in a control system to modulate the air to gas ratio.
  • the ratio of the ionization current at maximum load of the gas premix burner installed in the boiler is less than 50% higher than the ionization current at minimum load of the gas premix burner installed in the boiler. It is a further benefit of this embodiment that even better control possibility exist, as the ionization signal is less dependent from the burner load and more constant at a high level over a broad range of the burner load.
  • a third aspect of the invention relates to the use of the burner of the first aspect of the invention.
  • Examples of use are boilers or instantaneous water heaters that comprise a gas premix burner as in the first aspect of the invention and/or that is using a method as in the second aspect of the invention to control the air to gas ratio supplied to the gas premix burner.
  • the hot flue gas generated by the gas premix is transferring its heat to a fluid (mostly water) in a heat exchanger.
  • FIGS. 1 and 2 show a flat gas premix burner 100 according to the invention.
  • the gas premix burner 100 has a frame 105 to which a fiber based burner deck 110 is connected, e.g. a knitted fabric made out of yarns spun from stainless steel fibers.
  • the fiber based burner deck 110 is placed on a perforated plate or woven wire mesh (115 in figure 2, figure 2 shows the cross section of the gas premix burner of figure 1 along line I-I').
  • the perforated plate or the woven wire mesh has a uniform perforation pattern over their full surface.
  • the perforated plate or the woven wire mesh are advantageously made out of stainless steel.
  • the burner of the example is a flat burner, having a length L 1 of 105 mm and a width L 2 of 30 mm.
  • the burner deck of the flat burner can have a curved shape or can even have an undulated shape.
  • the fiber based burner deck is thicker (in the region indicated with reference number 140) than in the remainder of the fiber based burner deck 110.
  • the region at the ionization pen 130 where the fiber based burner deck is thicker 140 is having a length L 3 of 40 mm and a width L 4 of 24 mm.
  • the ionisation pen 130 has e.g. a length L 5 of 30 mm.
  • a fabric knitted from yarns made out of stainless steel fibers using an alloy according to DIN 1.4767 was used as fiber based burner deck.
  • the knitted fabric has a surface weight of 1.4 kg/m 2 .
  • the knitted fabric In the region 140 of the ionization pen 130, the knitted fabric has a thickness of 1.7 mm with a porosity of 89.7%. Outside this region, the thickness of the knitted fabric is 1.07 mm with a porosity of 82.5%.
  • the difference in thickness can be obtained by compressing the knitted fabric in the region outside the ionization pen.
  • the thickness of the fabric at the ionization pen is 60% higher than outside this region.
  • the ionization current at minimum load of the burner is 43 microampere.
  • the knitted fabric in the region 140 of the ionization pen 130, has a thickness of 2.7 mm with a porosity of 93.5%. Outside this region, the thickness of the knitted fabric is 1.07 mm with a porosity of 82.5%. The thickness of the knitted fabric in the region of the ionization pen is 150% higher than outside this region.
  • the ionization current at the same minimum load of the burner is 58 microampere. The results have been compared with a prior art burner with uniform fabric thickness for which the ionization current at the same minimum load was measured as being only 25 microampere.
  • FIG. 3 shows a cylindrical gas premix burner 300 according to the invention.
  • the burner has a length L1 (e.g. between 50 and 2000 mm), e.g. 400 mm and a diameter D1 (e.g. between 30 and 300 mm), e.g. 98 mm.
  • the gas premix burner 300 has a flange 305, an inlet 308 for gas premix, a cylindrical fiber based burner deck 310 on a cylindrical perforated plate (not shown in the figure) and an end cap 315.
  • region 340 at ionization pen 330 which is mounted in a holder 332, the fiber based burner deck is thicker than in the remainder of the fiber based burner deck 310.
  • the region at the ionization pen 330 where the fiber based burner deck is thicker 340 is having a length L 3 of 50 mm and a width L 4 of 24 mm.
  • the ionisation pen 130 has a length L 5 of 40 mm.
  • a fabric knitted from yarns made out of stainless steel fibers of an alloy according to DIN 1.4767 was used as fiber based burner deck.
  • the knitted fabric has a surface weight of 1.4 kg/m 2 .
  • the knitted fabric has a thickness of 1.7 mm with a porosity of 89.7%. Outside this region, the thickness of the knitted fabric is 1 mm with a porosity of 82.5%.
  • the difference in thickness can be obtained by compressing the knitted fabric in the region outside the ionization pen.
  • the knitted fabric in the region 340 of the ionization pen 330, has a thickness of 2.7 mm with a porosity of 93.5%. Outside this region, the thickness of the knitted fabric is 1 mm with a porosity of 82.5%.
  • Figure 4 shows the ionization current (Y, in microampere) measured by the ionization pen as a function of burner load (X, expressed in kW)for a prior art burner (indicated with curve A in figure 4 ) and for the burner according to the invention as described the example in figures 1 and 2 (indicated with curve B in figure 4 ) for a burner where the knitted fabric has a thickness of 2.7 mm in the region of the ionization pen and a thickness of 1 mm outside this region.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gas Burners (AREA)

Claims (12)

  1. Gasvormischungsbrenner (100, 300), umfassend
    - eine perforierte Platte (115), ein Drahtgeflecht oder Streckmetallblech;
    - ein auf Fasern basierendes Brennerdeck (110, 310), das auf die perforierte Platte (115), das Drahtgeflecht oder das Streckmetallblech platziert ist;
    - eine Ionisierungssonde (130, 330), um den Ionisierungsstrom über der Flamme des Gasvormischungsbrenners (100, 300) zu messen,
    dadurch gekennzeichnet, dass das auf Fasern basierende Brennerdeck (110, 310) in mindestens einem Teil des Bereiches (140, 340), in welchem sich die Ionisierungssonde (130, 330) befindet, im Verhältnis zu anderen Bereichen des auf Fasern basierenden Brennerdecks (110, 310) dicker ist.
  2. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, wobei das auf Fasern basierende Brennerdeck in einem Bereich von mindestens 5 mm auf beiden Seiten von mindestens 50 % der Länge der senkrechten Projektion der Ionisierungssonde auf das Brennerdeck dicker ist.
  3. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, wobei das auf Fasern basierende Brennerdeck dieselbe Masse pro Oberfläche über die gesamte Oberfläche des Brennerdecks aufweist, und in dem mindestens einen Teil des Bereiches, in welchem sich die Ionisierungssonde befindet, im Verhältnis zu anderen Bereichen des auf Fasern basierenden Brennerdecks weniger komprimiert ist, wodurch das auf Fasern basierende Brennerdeck in dem mindestens einen Teil des Bereiches, in welchem sich die Ionisierungssonde befindet, im Verhältnis zu anderen Bereichen des auf Fasern basierenden Brennerdecks dicker ist.
  4. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, wobei die Dicke des auf Fasern basierenden Brennerdecks in mindestens einem Teil des Bereiches, in welchem sich die Ionisierungssonde befindet, mindestens 40 % höher als der Durchschnitt der Dicke außerhalb des mindestens einen Teils des Bereiches ist, in welchem sich die Ionisierungssonde befindet.
  5. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, wobei die Porosität des auf Fasern basierenden Brennerdecks, an der Stelle, an der es in mindestens einen Teil des Bereiches, in welchem sich die Ionisierungssonde befindet, dicker ist, weniger als 92 % beträgt.
  6. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, wobei die durchschnittliche Porosität des auf Fasern basierenden Brennerdecks außerhalb des mindestens einen Teils des Bereiches, in welchem sich die Ionisierungssonde befindet, höher als 75 % ist.
  7. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, wobei das auf Fasern basierende Brennerdeck Metallfasern umfasst.
  8. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, wobei das auf Fasern basierende Brennerdeck einen gewebten, gewirkten, geflochtenen oder einen Vliesstoff umfasst.
  9. Gasvormischungsbrenner nach einem der vorhergehenden Ansprüche, des Weiteren ein Steuersystem umfassend, welches den Ionisierungsstrom, der durch die Ionisierungssonde gemessen wird, als Eingangswert verwendet, und das Luft-/Gasverhältnis in der Vormischungszufuhr zu dem Brenner regelt.
  10. Verfahren zum Regeln des Luft-/Gasverhältnisses eines Gasvormischungsbrenners, wobei ein Gasvormischungsbrenner nach einem der Ansprüche 1 bis 10 verwendet wird, und wobei der Ionisierungsstrom, der durch die Ionisierungssonde gemessen wird, in einem Steuersystem verwendet wird, um das Luft-/Gasverhältnis in der Vormischungszufuhr zu dem Brenner zu modulieren.
  11. Verfahren zum Regeln des Luft-/Gasverhältnisses eines Gasvormischungsbrenners nach Anspruch 10, wobei der Brenner in einem Kessel installiert ist, und wobei das Verhältnis des Ionisierungsstroms bei maximaler Last des Brenners in dem Kessel weniger als 50 % höher als der Ionisierungsstrom bei minimaler Last des Brenners in dem Kessel beträgt.
  12. Kessel oder Durchlaufwassererhitzer, umfassend einen Gasvormischungsbrenner nach einem der Ansprüche 1 bis 9.
EP13716263.2A 2012-05-03 2013-04-08 Gasvormischungsbrenner Active EP2844920B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP13716263.2A EP2844920B1 (de) 2012-05-03 2013-04-08 Gasvormischungsbrenner

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP12166512 2012-05-03
EP13716263.2A EP2844920B1 (de) 2012-05-03 2013-04-08 Gasvormischungsbrenner
PCT/EP2013/057299 WO2013164159A1 (en) 2012-05-03 2013-04-08 Gas premix burner

Publications (2)

Publication Number Publication Date
EP2844920A1 EP2844920A1 (de) 2015-03-11
EP2844920B1 true EP2844920B1 (de) 2016-05-18

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WO (1) WO2013164159A1 (de)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3572728B1 (de) 2018-05-22 2022-04-06 Bekaert Combustion Technology B.V. Vorgemischgasbrenner
DE102021125524A1 (de) 2021-10-01 2023-04-06 Vaillant Gmbh Flammensperre, Gasbrenner und Gasheizgerät

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2050298A (en) 1934-04-25 1936-08-11 Thos Firth & John Brown Ltd Metal reducing method
US3394213A (en) 1964-03-02 1968-07-23 Roehr Prod Co Inc Method of forming filaments
US3277564A (en) 1965-06-14 1966-10-11 Roehr Prod Co Inc Method of simultaneously forming a plurality of filaments
US4657506A (en) 1984-12-10 1987-04-14 Glowcore Corporation Gas burner
EP0319959B1 (de) 1987-12-09 1993-04-21 Nibex Company, Ltd. Verfahren und Vorrichtung zur Faserherstellung
US4900245A (en) * 1988-10-25 1990-02-13 Solaronics Infrared heater for fluid immersion apparatus
US5165887A (en) * 1991-09-23 1992-11-24 Solaronics Burner element of woven ceramic fiber, and infrared heater for fluid immersion apparatus including the same
US5380192A (en) * 1993-07-26 1995-01-10 Teledyne Industries, Inc. High-reflectivity porous blue-flame gas burner
DE19632983C2 (de) 1996-08-16 1999-11-04 Stiebel Eltron Gmbh & Co Kg Regeleinrichtung für einen Gasbrenner
KR20110104080A (ko) 2003-04-18 2011-09-21 엔브이 베카에르트 에스에이 금속 버너 멤브레인
ITMO20070167A1 (it) * 2007-05-21 2008-11-22 Worgas Bruciatori Srl Bruciatore modulante

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WO2013164159A1 (en) 2013-11-07

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