• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a heating device, in particular a boiler, with a combustion chamber (1) for the combustion of solid fuel, in particular biomass, and a subsequent flue gas duct (4) for removing flue gases, the flue gas duct (4) in a condensation heat exchanger with vertical heat exchanger pipes ( 5) opens, the lower ends of which open into a discharge area (6) for the condensate. According to the invention, it is proposed that a displacement cylinder (14) arranged coaxially to the respective heat exchanger tube (5) is provided inside the heat exchanger tubes (5), and between the inner surface of the heat exchanger tube (5) and the outer surface of the displacement cylinder (14) in each case a helical spring-shaped a winding distance A executed swirl body (15) is arranged, wherein the swirl body (15) are movably mounted in the axial direction of the respective heat exchanger tube (5) by a lifting height H, which corresponds to the winding distance A or exceeds it, and above the heat exchanger tubes (5 ) Dispensing nozzles for a cleaning liquid are arranged. This ensures that the heat of combustion is permanently and efficiently transferred to the heat transfer medium with the aid of condensation heat exchangers.
    公开号:AT523241A1
    申请号:T8006/2020
    申请日:2017-04-12
    公开日:2021-06-15
    发明作者:Ortner Herbert
    申请人:Oekofen Forschungs Und Entw M B H；
    IPC主号:
    专利说明:

    The invention relates to a heating device, in particular a boiler, with a combustion chamber for the combustion of solid fuel, in particular biomass, and a flame tube, the inflow area of which faces the combustion chamber and the outflow area of which faces a subsequent flue gas duct for the removal of flue gases, the flue gas duct in a condensation heat exchanger with vertical heat exchanger tubes opens, the lower ends of which each into a discharge area for the
    Open condensate, according to the preamble of claim 1.
    Such heating devices are used to heat a heat transfer medium for use as hot water or for heating purposes with the aid of the combustion of a solid fuel. In practical use, it is crucial, on the one hand, that the efficiency of the heating device is optimized, i.e. that the greatest possible proportion of the combustion heat is transferred to the heat transfer medium, and that, on the other hand, trouble-free operation with the least possible maintenance is guaranteed. To increase the efficiency, the use of condensation heat exchangers is known, in which the hot flue gas is introduced into downwardly directed heat exchanger tubes, in which the flue gas cools down while giving off heat to the heat transfer medium surrounding the heat exchanger tubes, and from which the cooled flue gas exits at temperatures below the dew point temperature. Due to the cooling down to below the dew point temperature, the water vapor contained in the flue gas condenses and is released as condensate in the discharge area. The heat of condensation released in the process can also be transferred to the heat transfer medium, which increases the efficiency
    is additionally increased.
    Basically, in the interest of the highest possible heat dissipation to the heat transfer medium, the longest possible residence time of the hot flue gas within the heat exchanger tubes with a long contact time with the inner surfaces of the heat exchanger tubes is advantageous. In this case, however, the problem arises that deposits and dirt accumulate on the inner surfaces of the heat exchanger tubes due to the particles and entrained in the flue gas
    Suspended solids form, which in turn transfer the heat
    and reduce the efficiency of the heater over time. This problem arises particularly when burning solid fuels, especially biomass, due to the high proportion of combustion particles contained in the flue gas, which over time cause heavy deposits on all components in the flow. The deposited particles prevent efficient heat transfer, whereby it is assumed, that the particles contained in the flue gas form a thermally insulating layer both within the flow and in the form of the deposits mentioned. In previously known systems with condensation heat exchangers that have been optimized for gaseous fuels, combustion particles generally do not pose a problem. An application of these systems to solid fuels
    however, it leads to increased maintenance costs and susceptibility to failure.
    The aim of the present invention is therefore to provide a heating device with which the heat of combustion of solid fuels is permanently and efficiently transferred to the heat transfer medium with the aid of condensation heat exchangers
    can be ensured and the maintenance effort is reduced.
    This aim is achieved with the aid of the features of claim 1. Claim 1 relates to a heating device, in particular a boiler, with a combustion chamber for the combustion of solid fuel, in particular biomass, as well as a flame tube, the inflow area of which faces the combustion chamber and the outflow area of which faces a subsequent flue gas duct for removing flue gases, the flue gas duct opens into a condensation heat exchanger with vertical heat exchanger tubes, the lower ends of which open into a discharge area for the condensate. According to the invention, it is proposed here that a displacement cylinder is provided in the interior of the heat exchanger tubes, which is arranged coaxially to the respective heat exchanger tube, and between the inner surface of the heat exchanger tube and the outer surface of the displacement cylinder, in each case a helical-spring-shaped swirl body with a winding spacing A is arranged, the swirl body in axial direction of the respective heat exchanger tube by a lifting height
    H, which corresponds to or exceeds the winding spacing A,
    Dispensing nozzles for a cleaning liquid are arranged.
    With the help of the arrangement of the displacement cylinder with the swirl body surrounding the displacement cylinder, it is possible to increase the dwell time of the hot flue gas within a heat exchanger tube and the contact time to the inner surfaces of the heat exchanger tube so that hot flue gas with temperatures of up to 800 ° C is introduced into the A condensation heat exchanger and above the usual Construction heights of generic heating devices can be cooled to about 40 ° C without the need for additional heat exchangers. The flue gas moves between the displacement cylinder and the inner surface of a heat exchanger tube, whereby it is designed in the form of a helical spring
    Swirl body is swirled.
    In order to counteract the formation of deposits that would significantly reduce the efficiency, the invention also provides that the swirl body is movably mounted in the axial direction of the respective heat exchanger tube by a lift height HH which corresponds to or exceeds the winding spacing A. The winding distance A is the distance between two successive windings of the helical spring-shaped turbulence body. At a time interval of a few hours, the arrangement of the displacement cylinder and the swirl body is automatically raised by a lifting height H at least equal to the winding distance A during operation of the M heating device, whereby deposits are loosened and fall in the direction of the delivery area. This ensures that the heat of combustion from solid fuels is permanently and efficiently transferred to the heat transfer medium with the aid of condensation heat exchangers. In order to improve the cleaning of the heat exchanger tubes, it is further proposed that delivery nozzles for a cleaning fluid be installed above the heat exchanger tubes
    are arranged. The dispensing nozzles spray the cleaning liquid,
    preferably water, on cup-shaped receptacles of the displacement cylinders, which subsequently fill with the cleaning fluid, so that the cleaning fluid
    finally flows off on the outer surface of the displacement cylinder.
    The removal of deposits is improved in that the swirl body of a heat exchanger tube is preferably arranged via a suspension with radial play to the inner surface of the heat exchanger tube and the outer surface of the displacement cylinder. As a result, the swirl body strikes the inner surface of the heat exchanger tube and the outer surface of the displacement cylinder during the stroke movement, so that deposits do not occur
    only scraped off but to a certain extent knocked off.
    According to a preferred embodiment, it is proposed that the displacement cylinders each rest with their end facing the delivery area on a lifting device, and the suspension for the swirl body assigned to it is attached to the end of the displacement cylinder facing the smoke gas duct. The lifting device thus raises and lowers the displacement cylinder together with the swirl body, since the displacement cylinders rest on the lifting device and the suspension of the swirl body is attached to the end of the displacement cylinder facing the flue gas duct. The mechanism of the lifting device is therefore not located in the hot flue gas flow in the area of the flue gas duct, but in the delivery area of the heat exchanger pipes, in the more moderate one
    Temperatures prevail.
    In the practical embodiment of the heating device according to the invention, the arrangement of the heat exchanger tubes in two rows of three heat exchanger tubes each, which are moved by a lifting device, has also proven advantageous with the usual sizes of such heating devices. Consequently, the arrangement of a multiple of six heat exchanger tubes turns out to be
    advantageous, so about twelve or eighteen heat exchanger tubes.
    In order to coordinate the lifting process and, above all, the lowering movement of the displacement cylinders and the turbulence bodies, it is further proposed that the ends of the displacement cylinders facing the flue gas duct are connected to one another via cross members. The cross member can be attached to the respective suspensions. In this way, the noise is also arranged with play
    Turbulence bodies reduced in the course of the lifting and lowering movements.
    Connects heat exchanger tubes.
    In order to improve the cleaning of the heat exchanger tubes, it is further proposed that the dispensing nozzles for the cleaning liquid arranged above the heat exchanger tubes are each directed at the ends of the displacement cylinders facing the smoke gas duct, the ends of the displacement cylinders facing the smoke gas duct being designed as cup-shaped receptacles for the cleaning liquid are. The dispensing nozzles spray the cleaning liquid, preferably water, onto the cup-shaped receptacles, which then fill up with the cleaning liquid, so that the cleaning liquid finally arrives at the
    Outer surface of the displacement cylinder flows off.
    The uniform filling of the cup-shaped receptacles with the cleaning liquid is improved in that the suspension is fastened in the bottom area of the cup-shaped receptacle and has passage openings for the cleaning liquid arranged inside the cup-shaped receptacle. The suspension fastened in the bottom area of the cup-shaped receptacle otherwise impairs the uniform filling of the cup-shaped receptacles with the cleaning liquid, which with the aid of the passage openings
    is avoided.
    Generic heating devices are conventionally provided with a suction fan which sucks the flue gases from the combustion chamber via the flue gas duct and the heat exchanger pipes to a discharge opening in the direction of a chimney. The suction fan is usually arranged in a condensate pan with a horizontal suction fan axis in order to free the fan blades of the suction fan of deposits from the flue gas with the aid of the condensate and the cleaning liquid. The suction axis corresponds to the axis of rotation of the fan blades of the suction fan. However, practical experience shows that the sides of the fan blades facing away from the sucked in flue gas are not adequately cleaned and that deposits on these sides cannot be permanently prevented. It is therefore preferable to propose
    that the discharge area is connected to a condensate pan or
    Is part of a condensate pan, and a suction fan with a vertical induced draft axis is arranged above the condensate pan. The suction fan is in this way neither the condensate nor the
    Exposed to cleaning fluid.
    A condensate drain is provided for the condensate collected in the condensate pan and the used cleaning liquid, via which the condensate and the cleaning liquid can be discharged from the housing of the heating device. Since deposits can form in the condensate drain, which increasingly clog the condensate drain, it is therefore proposed that the condensate pan have a condensate drain with an inlet
    is provided for rinsing water.
    Preferred embodiments of the invention are described in more detail below with reference to the accompanying drawings. Show it
    the
    La is a sectional view through a boiler according to the invention in a lowered position of the displacement cylinder and the
    Vortex bodies,
    Fig. 1b is a sectional view through a boiler according to the invention in a raised position of the displacement cylinder and the
    Vortex bodies,
    2a shows an enlarged illustration of the displacement cylinder and the swirl body according to the embodiment of FIG. 1 in a lowered position of the displacement cylinder and the
    Vortex bodies,
    FIG. 2b shows an enlarged illustration of the displacement cylinders and the turbulence bodies according to the embodiment of FIG. 1 in a raised position of the displacement cylinders and the
    Vortex bodies, and the
    3 shows a further sectional view through an inventive
    Boiler.
    Fig. 1 shows a heating device according to the invention in the form of a boiler for heating a heat transfer medium by combustion
    of solid fuel, especially biomass. In a combustion chamber 1
    a burner plate 2 is arranged for this, to which the solid fuel is fed, for example in the form of pourable or pourable fuel (e.g. pellets). The ash collects below the burner plate 2 and is transported into the ash container by an ash screw. As indicated in FIG. 1, the combustion chamber 1 has a lateral opening through which pourable material to be fired can be conveyed from a storage container 22 to the burner plate 2 by means of a conveying device with a conveying drive 23 (see FIG. 3). The conveying device can for example be an automatically controlled screw conveyor. The storage container 22 contains about an amount of fuel sufficient for a day of heating and is therefore also called
    Day container designated.
    Above the burner plate 2, a flame tube 3 is arranged vertically, the inflow area of which faces the combustion chamber 1 and opens into the combustion chamber 1. The flame tube 3 is of appropriate thickness and made of a thermally insulating material, preferably ceramic material or (fire) concrete. At the upper end of the flame tube 3, the flue gases emerge in an outflow area of the flame tube 3 in an approximately laminar flow and enter a subsequent flue gas duct 4. Downwardly directed heat exchanger tubes 5 of a condensation heat exchanger open into the flue gas duct 4, the lower ends of which each enter a discharge area 6 for the Drain condensate. The heat exchanger tubes 5 are surrounded by fluid-filled, in particular water-filled spaces 7. In these rooms 7 is for heating purposes or
    for use as hot water to be heated heat transfer medium.
    The discharge area 6 is connected to a condensate pan 8 (see also FIG. 3) or is part of a condensate pan 8. The condensate pan 8 has a condensate drain 9 which is provided with an inlet 10 for rinsing water (see also FIG. 3). The rinsing water removes deposits in the condensate drain 9, which could otherwise clog the condensate drain 9, and feeds them to a sewer outside the housing 11 of the heating device. A suction fan 12 with a vertical suction fan axis is arranged above the condensate pan 8 and to the side of a discharge opening 13 (see also FIG. 3). The dispensing opening 13 can be at an outside of the
    Housing 11 running chimney can be connected to flue gases
    to enable the condensate pan 8.
    Inside each of the heat exchanger tubes 5 there is provided a displacement cylinder 14, which is arranged coaxially to the respective heat exchanger tube 5, so that an annular channel with an annular cross section through which the flue gases flow forms between the inner surface of the heat exchanger tube 5 and the outer surface of the displacement cylinder 14. In this annular channel, a helical spring-shaped turbulence body 15 designed with a winding spacing A is arranged in each case. The flue gas is in its downward movement in the direction of the delivery area 6 between the displacement cylinder 14 and the inner surface of the relevant heat exchanger tube 5 from
    helical spring-shaped turbulence body 15 swirled.
    The swirl body 15 of a heat exchanger tube 5 is arranged via a suspension 16 with radial play to the inner surface of the heat exchanger tube 5 and to the outer surface of the displacement cylinder 14. The displacement cylinder 14 and the swirl body 15 are also movably mounted in the axial direction of the respective heat exchanger tube 5 by a lifting height H which corresponds to the winding spacing A or exceeds it (see FIG. 2). Due to the radial play of the swirl body 15 within the annular space between the displacement cylinder 14 and the inner surface of the heat exchanger tube 5, the swirl body 15 strikes the inner surface of the heat exchanger tube 5 and the outer surface of the displacement cylinder 14 during the stroke movement, so that deposits not only
    scraped off but to a certain extent knocked off.
    The displacement cylinders 14 each rest with their end facing the delivery area 6 on a lifting device 17 with which a lifting and lowering movement of the displacement cylinder 14 is carried out
    can be. At the end of each facing the flue gas duct 4
    Displacement cylinder 14 is attached to the suspension 16 for the swirl body 15 assigned to it in each case. The lifting device 17 thus raises and lowers the displacement cylinder 14 together with it
    the swirl body 15.
    In the exemplary embodiment shown, the heat exchanger tubes 5 are arranged in two rows, each with three heat exchanger tubes 5, so that a total of six heat exchanger tubes 5 are used, which are connected by one
    Lifting device 17 are moved.
    In order to synchronize the lifting process and especially the lowering movement of the displacement cylinder 14 and the swirl body 15, the ends of the displacement cylinders 14 facing the flue gas duct 4 are connected to one another via cross members 18 (see in particular FIG. 3). The cross member 18 is attached to the respective suspensions 16. In this way, the development of noise from the turbulence bodies 15, which are arranged with play, is reduced in the course of the lifting and lowering movements. In particular, the cross member 18 connects the three displacement cylinders 14 of the arranged in a row
    Heat exchanger tubes 5.
    In order to improve the cleaning of the heat exchanger tubes 5, dispensing nozzles for a cleaning liquid are arranged above the heat exchanger tubes 5, which are each directed at the ends of the displacement cylinders 14 facing the flue gas duct 4, the ends of the displacement cylinders 14 facing the flue gas duct 4 each as cup-shaped receptacles 19 are designed for the cleaning liquid (see Fig. 2). The dispensing nozzles are arranged along a supply pipe 20 running between the two rows of heat exchanger pipes 5 and spray the cleaning liquid, preferably water, onto the cup-shaped receptacles 19, which subsequently fill with the cleaning liquid, so that the cleaning liquid finally reaches the outer surface of the displacement cylinder 14 drains. The uniform filling of the cup-shaped receptacles 19 with the cleaning fluid is improved in that the suspension 16 is fastened in the bottom area of the cup-shaped receptacle 19 and is arranged inside the cup-shaped receptacle 19
    Has passage openings 21 for the cleaning liquid
    (see in particular Fig. 3). The suspension 16 fastened in the bottom area of the cup-shaped receptacle 19 otherwise impairs the uniform filling of the cup-shaped receptacles 19 with the cleaning liquid, which is achieved with the aid of the passage openings 21
    is avoided.
    In order to counteract the formation of deposits that would significantly reduce the efficiency of the heating device, it is provided that the displacement cylinder 14 and the swirl body 15 in the axial direction of the respective heat exchanger tube 5 by a stroke height H which corresponds to or exceeds the winding spacing A, is moved with the aid of the lifting device 17 (see in particular FIG. 2). At a time interval of a few hours, the arrangement of the displacement cylinder 14 and the swirl body 15 is automatically raised by a lifting height H at least equal to the winding distance A during operation of the heating device, whereby deposits are loosened and fall in the direction of the delivery area 6. In this way, the heat of combustion of solid fuels is permanently and efficiently transferred to the heat transfer medium
    ensured by means of the condensation heat exchanger.
    With the help of the arrangement of the displacement cylinder 14 and the swirl body 15 surrounding the displacement cylinder 14, it is also possible to increase the dwell time of the hot flue gas within a heat exchanger tube 5 and the contact time to the inner surfaces of the heat exchanger tube 5 so that hot flue gas with temperatures of up to 800 ° C is increased introduced into the condensation heat exchanger and can be cooled to around 40 ° C by generic heating devices over the usual structural heights without it
    additional heat exchanger is required.
    With the help of the invention, a heating device is therefore provided with which a permanently efficient transfer of the heat of combustion of solid fuels to the heat transfer medium
    can be ensured with the aid of condensation heat exchangers.
    11718
    10
    11
    12th
    13th
    14th
    15th
    16
    17th
    18th
    19th
    20th
    21
    22nd
    23
    24
    25th
    Combustion chamber Burn plate Flame tube Flue gas duct Heat exchanger tubes Discharge area Water-filled rooms Condensate pan Condensate drain inlet
    casing
    Suction fan discharge opening displacement cylinder swirl body suspension lifting device cross member mountings
    Feed pipe Passages Reservoir Conveyor drive Fan motor
    Fan housing
    11
    权利要求:
    Claims (3)
    [1]
    Expectations:
    l. Heating device, in particular boiler, with a combustion chamber (1) for burning solid fuel, in particular biomass, and a flame tube (3), the inflow area of which faces the combustion chamber (1) and the outflow area of which faces a subsequent flue gas duct (4) for the removal of flue gases is, wherein the flue gas duct (4) opens into a condensation heat exchanger with vertical heat exchanger tubes (5), the lower ends of which each open into a discharge area (6) for the condensate, characterized in that inside each of the heat exchanger tubes (5) one to the respective heat exchanger tube (5) a coaxially arranged displacement cylinder (14) is provided, and between the inner surface of the heat exchanger tube (5) and the outer surface of the displacement cylinder (14) a helical spring-shaped swirl body (15) designed with a winding spacing A is arranged, the swirl body ( 15) in the axial direction of the respective heat exchanger tube it (5) by a lifting height H, which corresponds to the winding distance A or exceeds it, are movably mounted, and above the heat exchanger tubes
    (5) Dispensing nozzles for a cleaning liquid are arranged.
    [2]
    2. Heating device according to claim 1, characterized in that the swirl body (15) of a heat exchanger tube (5) via a suspension (16) with radial play to the inner surface of the heat exchanger tube (5) and the outer surface of the
    Displacement cylinder (14) is arranged.
    [3]
    3. Heating device according to claim 2, characterized in that the displacement cylinders (14) each rest with their end facing the delivery area (6) on a lifting device (17), and at the end of the displacement cylinder (14) facing the flue gas duct (4) Attachment (16) for the swirl body (15) assigned to it
    is.
    13th
    Heating device according to claim 2 or 3, characterized in that the heat exchanger tubes (5) in two rows of three
    Heat exchanger tubes (5) are arranged.
    Heating device according to one of Claims 1 to 4, characterized in that the ends of the displacement cylinders (14) facing the smoke gas duct (4) via cross members
    (18) are interconnected.
    Heating device according to claim 4 and 5, characterized in that the cross member (18) each has the three displacement cylinders (14) of the heat exchanger tubes (5) arranged in a row
    connects.
    Heating device according to one of the preceding claims, characterized in that the dispensing nozzles for the cleaning liquid arranged above the heat exchanger tubes (5) are each directed towards the ends of the displacement cylinders (14) facing the flue gas duct (4), the ends facing the flue gas duct (4) the displacement cylinder (14) each as cup-shaped recordings
    (19) are designed for the cleaning fluid.
    Heating device according to Claims 2 and 7, characterized in that the suspension (16) is fastened in the bottom region of the cup-shaped receptacle (19) and through openings (21) for the
    Has cleaning fluid.
    Heating device according to one of Claims 1 to 8, characterized in that the discharge area (6) is connected to a condensate pan (8) or is part of a condensate pan (8), and a suction fan above the condensate pan (8)
    (12) is arranged with a vertical suction axis.
    Heating device according to claim 9, characterized in that the condensate pan (8) has a condensate drain (9) which
    is provided with an inlet (10) for rinsing water.
    类似技术:
    公开号 | 公开日 | 专利标题
    AT523241B1|2021-08-15|Heating device
    DE102008012961B4|2010-02-25|Cooking device with a Wrasenkondensiereinrichtung
    CH663715A5|1988-01-15|GRILL AND FRYING EQUIPMENT.
    DE102009050507B4|2012-08-30|Solid fuel burner with heat exchanger for heat transfer to a liquid circuit
    AT15025U2|2016-11-15|heater
    DE102008022696A1|2009-11-12|Firing device with a cleaning device
    DE102016116977B3|2017-06-22|Liquid tank with a heater
    DE1778074A1|1972-02-17|boiler
    DE2204602C2|1973-12-06|Slot seal for walking beam oven
    EP1918667B1|2013-01-16|Heat exchanger with several cleaning devices
    DE102013110738B4|2015-05-28|heat exchangers
    EP2351966B1|2013-11-20|Heat exchange system
    DE2115257A1|1971-12-02|Water heater
    DE3110205C2|1985-05-15|Chimney arrangement for firing systems
    DE2346412A1|1975-03-27|Gas or oil fired high pressure steam cleaner boiler - has a second, supplemental heat exchanger fitted parallel to the main unit
    AT502821B1|2007-06-15|Method for condensation of flue gas of biomass boiler/solid fuel boiler in a condensation part cooled by heater water, comprises supplying hot flue gas in channels open towards the bottom over the surface of the fluid- or condensation bath
    DE157516C|
    AT71973B|1916-06-26|Device for heating the water, especially in breweries.
    DE888607C|1953-09-03|Cooking stove with a boiler enclosing the combustion chamber
    DE8316370U1|1983-08-25|BOILER
    AT7216U1|2004-11-25|HEAT EXCHANGER FOR RECOVERING THE HEAT OF EXHAUST GAS
    DE202007004485U1|2007-06-14|Wood pellets combustion furnace comprises a heat exchange unit with heat exchange sections arranged over each other with each section having longitudinal modular heat exchanger segments with heat removing panels
    DE4120251A1|1992-12-24|HEAT EXCHANGER
    DE10025729A1|2002-01-17|A boiler has a modular tubular heat exchanger heated by the down draught of a gas burner.
    DE1253388B|1967-11-02|Device for heating coils for oil refining
    同族专利:
    公开号 | 公开日
    DK3246652T3|2020-05-18|
    EP3246652B1|2020-02-19|
    DE202017007192U1|2020-01-20|
    AT517955A4|2017-06-15|
    RS60157B1|2020-05-29|
    PL3246652T3|2020-06-29|
    AT517955B1|2017-06-15|
    EP3246652A1|2017-11-22|
    AT523241B1|2021-08-15|
    ES2785677T3|2020-10-07|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US553689A|1896-01-28|Steam-generator |
    DE1094912B|1955-06-15|1960-12-15|William Herbert Smith|Device for cleaning the flue gas side of the flue pipes of standing boilers|
    FR2224728A1|1973-04-09|1974-10-31|Rouchy Christian|Spirally wound scraper rod - for automatic internal cleaning of heat exchanger tubes|
    AT508157A4|2009-08-04|2010-11-15|Schiefer Erwin|DEVICE FOR CLEANING A HEAT EXCHANGER|
    EP2926909A2|2014-04-03|2015-10-07|GILLES Energie- und Umwelttechnik GmbH & Co KG|Boiler|
    FR2589229B1|1985-10-25|1988-01-08|Neu Ets|AUTOMATIC METHOD AND DEVICE FOR CLEANING A HEAT EXCHANGER FOR GASEOUS FLUIDS|
    DE8604638U1|1986-02-21|1987-07-23|Ruhrkohle Ag, 4300 Essen, De|
    AT513734A1|2012-12-04|2014-06-15|Kofen Forschungs Und Entwicklungsgesellschaft M B H|Boiler with heat engine|
    AT516061B1|2015-03-04|2016-02-15|Gerlinger Ernst|boiler|EP3495045A1|2017-12-06|2019-06-12|Fröling Heizkessel- Und Behälterbau Gesellschaft M.B.H|Condensing boiler|
    FR3081108A1|2018-05-19|2019-11-22|Yvan Pesenti|PROCESS FOR TREATING SMOKE GENERATED BY WOOD COMBUSTION AND DEVICE FOR IMPLEMENTING THE METHOD.|
    CN108731532B|2018-05-31|2019-12-31|贵州环科环境工程有限公司|High-temperature flue gas cooling device|
    EP3798513A1|2019-09-26|2021-03-31|ÖKOFEN Forschungs- und Entwicklungsgesellschaft m.b.H.|Heating device|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50461/2016A|AT517955B1|2016-05-18|2016-05-18|heater|
    ATA50232/2019A|AT521304B1|2018-06-06|2019-03-19|Barn for the pig fattening|
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