EP1722172B1 - Wärmetauscherelement und Heizanlage mit so einem Wärmetauscherelement - Google Patents

Wärmetauscherelement und Heizanlage mit so einem Wärmetauscherelement Download PDF

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Publication number
EP1722172B1
EP1722172B1 EP06076027.9A EP06076027A EP1722172B1 EP 1722172 B1 EP1722172 B1 EP 1722172B1 EP 06076027 A EP06076027 A EP 06076027A EP 1722172 B1 EP1722172 B1 EP 1722172B1
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EP
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Prior art keywords
heat exchanger
water
exchanger element
flue gas
pins
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EP06076027.9A
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English (en)
French (fr)
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EP1722172A1 (de
Inventor
Pouwel Jelte Gelderloos
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Remeha BV
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Remeha BV
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00Details
    • F24H9/0005Details for water heaters
    • F24H9/001Guiding means
    • F24H9/0026Guiding means in combustion gas channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/22Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
    • F24H1/24Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water mantle surrounding the combustion chamber or chambers
    • F24H1/26Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water mantle surrounding the combustion chamber or chambers the water mantle forming an integral body
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00Details
    • F24H9/0005Details for water heaters
    • F24H9/001Guiding means
    • F24H9/0015Guiding means in water channels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/022Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being wires or pins
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/12Elements constructed in the shape of a hollow panel, e.g. with channels

Definitions

  • the invention relates to a heat exchanger element intended for a central heating boiler, which heat exchanger element is designed as a monocasting from substantially aluminum and is manufactured by means of a low pressure casting process, for instance sand casting or die-casting, the heat exchanger element being provided with walls which bound a water-carrying channel, and with at least one wall which bounds at least one flue gas draft to which a burner is connectable, at least one wall which bounds the at least one flue gas draft being water-cooled in that it also forms a boundary of the water-carrying channel, while one said at least one water-cooled wall is provided with heat exchanging surface enlarging pins and/or fins which extend in the respective flue gas draft.
  • Such a heat exchanger element is known from European patent application EP-A-0 889 292 .
  • the heat exchanger element described therein is particularly intended for great outputs and is thereto provided with several flue gas drafts.
  • applicant has marketed central heating boilers with heat exchanger elements with a single flue gas draft. These heat exchanger elements are known as type indications W21C Eco and W28C Eco.
  • the known heat exchanger elements have a weight of approximately 0.4 kg/kW. For a heat exchanger element of approximately 25 kW, which is a customary output for a normal house, the weight is therefore approximately 10 kg. Moreover, the known heat exchanger element with such an output has a water-carrying channel with a content of approximately 2.1 litres. This is, inter alia, the result of the fact that with the known heat exchanger elements, the burner is completely surrounded by heat exchanging surface and associated water channel.
  • the known heat exchanger element is already relatively small for a boiler with such an output, it must be established that in particular when the boiler is used for heating not only central heating water but also tap water, the efficiency can be improved still further, and a still more rapid heating of the tap water is desired.
  • the invention provides a heat exchanger element according to claim 1.
  • pins and/or fins with such a small cross-sectional surface because the pins and/or fins had to have a length of at least 25 mm, this being so because the flue gas draft is to have a particular width for discharging sufficient flue gas and because this width is to be completely filled with the heat exchanging surface enlarging pins and/or fins.
  • Pins with such a length need to have quite a large cross-sectional surface in connection with casting technique requirements.
  • the known pins for instance, have a length of 25 mm and a diameter of 8 mm.
  • the pins and/or fins with the smaller cross-section is that, with the heat exchanging surface remaining the same, the global wall surface, i.e. the dimensions of the wall that bears the pins, can be considerably smaller. This therefore leads to a smaller surface to be cooled with water. As a result thereof, the water-carrying channel will have a smaller content, which also leads to a smaller heat capacity of the heat exchanger element.
  • a so-called heat sink is known, which is provided with pins with a diameter leading to a cross-sectional surface in the claimed range of the present invention.
  • the known pins have a diameter of 2 mm and, hence, a cross-sectional surface of 3.2 mm 2 .
  • a heat sink is a device utilized in electronic equipment, such as computers, for cooling electronic components accommodated therein.
  • the heat sink shown in the US publication comprises a first base plate and a number of pins extending away from this base plate, and a second base plate and a number of pins extending away from this second base plate.
  • the two plates After having been manufactured separately in a casting process, the two plates are interconnected.
  • the known heat sink is therefore not a monocasting. Judging by the diameters of the pins mentioned in the text, and the drawings, which represent reality three times enlarged, the dimensions of the base plates are approximately 3,3 * 2.5 cm.
  • the separate base plates with pins are releasing, and can therefore be manufactured through die-casting. With die-casting, the mold is of metal and can be heated, so that the so-called cold flow occurs much less rapidly. Furthermore, the base plate is relatively thick, so that at there, virtually no cooling of casting material occurs.
  • the liquid metal can be supplied under excess pressure. This is contrary to a heat exchanger element for a central heating boiler.
  • the heat exchanger designed as monocasting is not-releasing. As a result, a mold and cores manufactured from sand, and which are lost after the casting process, have to be utilized. This excludes the possibility of casting under excess pressure. Furthermore, heating a sand cast mold is not possible.
  • the liquid metal will have to run, from one filling point, through the cavities for forming the thin-walled water channels to, only after that, flow into the cavities for forming the pins.
  • the dimensions of an exemplary embodiment of the present invention are in the range of, for instance, 20 - 50 cm, which is not comparable to the dimensions of the known heat sink.
  • the freedom of choice of metal that can be used for casting a central heating heat exchanger element is much more limited than the freedom of choice for a heat sink. The fact is that in the central heating heat exchanger element, in use, there is an environment of flue gases and water vapour which leads to the formation of highly corrosive acids.
  • the water content of the water-carrying channel can be reduced still further by reducing to less than 10 mm, for instance less than 8 mm, the distance between the wall which bounds, on the one side, the water-carrying channel and, on the other side, an outside of the heat exchanger element, and the wall which bounds, on the one side, the water-carrying channel and, on the other side, the flue gas draft.
  • a heat exchanger element with an output of 28 kW can be provided, with the water-carrying channel having a water content of 0.83 liter instead of the 2.1 litres for 25 kW that was customary heretofore. That is to say, 0.03 l/kW instead of 0.084 l/kW which was customary heretofore. Also this dramatic reduction of water to be heated leads to a smaller heat capacity of the heat exchanger element and, hence, to a quicker heating.
  • a problem that may arise as a result of the smaller dimensions of the water-carrying channel is that the heat exchanging surface of the wall that forms the boundary between the water-carrying channel and the flue gas draft on the water-side, is insufficient. According to a further elaboration of the invention, this problem can be solved by providing the respective wall with water-side heat exchanging surface enlarging pins and/or fins.
  • An improvement of the efficiency and a more rapid heating of tap water can be provided by a heating boiler provided with a central heating heat exchanger element according to any of the claims 1-14, while the heating boiler is also provided with a tap water heat exchanger that can be connected to an outlet of the water-carrying channel and an inlet of the water-carrying channel, a pump being provided for transporting the water through the central heating heat exchanger element and the tap water heat exchanger, while the central heating heat exchanger element, the tap water heat exchanger, the burner the pump have been/are adjusted to each other such that, with tap water in use, the difference between the supply temperature, i.e.
  • the temperature of the water coming from the water-carrying channel, that is led to the tap water heat exchanger, and the return water temperature, i.e. the temperature of the water coming from the tap water heat exchanger that is led into the inlet of the water-carrying channel, is higher than 25°C, and preferably higher than 30°C.
  • This is preferably effected by maintaining the central heating side flow rate low.
  • the average temperature of the central heating heat exchanger element is much lower.
  • the supply water temperature was, for instance, 70°C, and the return water temperature 50°C.
  • the average temperature across the central heating heat exchanger element was therefore 60°C.
  • the return water temperature is reduced to, for instance, 30°C, the average temperature of the central heating heat exchanger element is 50°C.
  • the central heating heat exchanger element which, generally, is maintained at approximately 30°C, needs only heat up 20 degrees instead of 30 degrees. It will be clear that this leads to a considerably acceleration of the required heating up time, so that hot tap water is available more rapidly.
  • the flue gases can cool down further so that an increased condensation of the flue gases is possible, which results in a better efficiency.
  • the lower return water temperature is, in particular, achieved by reducing the central heating side flow rate, i.e. the flow rate in the water-carrying channel of the central heating heat exchanger element. Also as a result of the limited water flow through the central heating heat exchanger element, the heat transfer coefficient in the water-carrying channel will decrease. As a result thereof, the presence of the water-side pins and/or fins mentioned hereinabove may be required for compensating for this lower heat transfer coefficient.
  • the exemplary embodiment of a central heating heat exchanger element 1 shown in Figs. 1 - 3 is a one-piece monocasting from substantially aluminum.
  • the heat exchanger element 1 is provided with a number of walls 2. At least one of these walls 2 bounds a flue gas draft 3, a few of these walls bound a water-carrying channel 4, and at least one wall bounds both the flue gas draft 3 and the water-carrying channel 4, and are therefore water-cooled.
  • a burner 5 (see Fig. 2 ) can be connected to the flue gas draft 3.
  • three of the walls 2 bounding the flue gas draft are water-cooled in that the water-carrying channel 4 extends therealong.
  • the water channel has a U-shaped configuration, which is clearly visible in Fig. 3 .
  • the water flows from an inlet 6 to an outlet 7 while, each time, travelling a U-shaped path and, thus, flowing in a zig-zag manner around the flue gas draft 3 in upward direction from the inlet 6 to the outlet 7.
  • the walls 2 are provided, on the side of the flue gas draft 3, with heat exchanging surface enlarging pins and/or fins 8.
  • the pins and/or fins 8 have a cross-sectional surface that is smaller than 25 mm 2 .
  • the pins 8 In the part 3a of the flue gas draft where the walls 2 extend parallel to each other, which, in the present exemplary embodiment, is the lower portion, the pins 8 have a length of approximately 15 mm.
  • the pins 8 Preferably, have a cross-sectional surface of 20 mm 2 or less. They can have a circular cross-section with a diameter of approximately 4 mm, a square cross-section, with the sides having a length of approximately 4 mm, or an ellipsoid or fin-shaped cross-section with a mentioned cross-sectional surface.
  • the flue gas draft 3 is of widened design for forming a burn out space 3b (see Fig. 3 ).
  • the burn out space 3b is very compact and the exemplary embodiment shown is particularly suitable for cooperation with a high-performance burner 5 with a compact burn out space.
  • the length of the pins 8 is smaller on an upstream side 3b of the flue gas draft 3, to which the burner 5 can be fitted, than the length of the pins 5 on a downstream side 3a of the flue gas draft 3.
  • the ends of the relatively short pins 8 are therefore close to the water-carrying channel 4, so that the risk of these ends overheating is reduced to a minimum.
  • the length of the pins and/or fins 8 increases in the widened part 3b forming the burn out space of the flue gas draft 3, according as the pins and/or fins 8 are arranged further downstream of the burner.
  • the present exemplary embodiment shows a heat exchanger element with an output of approximately 25 kW.
  • the weight of the heat exchanger element per kW to provide is less than 0.20 kg/kW.
  • the weight is only 0.16 kg/kW.
  • the water-carrying channel 4 has a volume smaller than 1 litre. In the present exemplary embodiment, the water volume is even only 0.9 litre.
  • This limited volume is, inter alia, achieved in that the distance between the wall 9 which bounds, on the one side, the water-carrying channel 4 and, on the other side, the outside of the heat exchanger element 1 and the wall 2, which bounds, on the one side, the water-carrying channel and, on the other side, the flue gas draft, is smaller than 10 mm, preferably smaller than 8 mm.
  • the flue gases flow from the top to the bottom through the flue gas draft 3, and the water to be heated flows from the bottom, via the already described U-shaped zig-zag path, to the top.
  • the heat exchanger element 1 is preferably manufactured by means of a casting process, such as, for instance, sand casting or die-casting. Preferably, use is then made of one water-side core for forming the water channel and one flue gas side core for forming the flue gas channel.
  • the water-side core has substantially a shape as represented in Fig. 3 .
  • a burner 5 is to be fitted on the heat exchanger element, while, for the present exemplary embodiment, preferably, a high-performance burner 5 is used.
  • This high-performance burner 5 is schematically represented, in part, in Fig. 2 .
  • a flue gas discharge is connected, extending in upward direction.
  • Fig. 4 shows a schematic exemplary embodiment of a heating boiler 11 connected to a central heating water pipe system 12.
  • the central heating heat exchanger element 14 of the heating boiler 11 can also be connected, via a valve assembly 15, to a tap water heat exchanger 16.
  • a valve assembly 15 to a tap water heat exchanger 16.
  • the weight of the central heating heat exchanger element 14 according to the invention is so limited, and as, furthermore, the water content of the water-carrying channel 4 is so limited, the heat capacity of the central heating heat exchanger element 14 is particularly limited. This leads to a very rapid heating of the heat exchanger element 14 when the burner 17 is switched on. In particular with tap water in use, such a rapid heating is of great importance for realizing a good convenience time, for preventing a temperature dip from occurring when tapping hot tap water, and for realizing a high efficiency.
  • This efficiency can even be further increased by adjusting to each other the pump 18, provided for transporting water through the central heating heat exchanger element 14 and the tap water heat exchanger 16, the central heating heat exchanger element 14, the tap water heat exchanger 16 and the burner, in a manner such that the difference between supply water temperature and the return water temperature is greater than 25°C and, more particularly, greater than 30°C.
  • This is preferably effected by maintaining the central heating side flow rate, i.e. the flow rate in the water-carrying channel of the central heating heat exchanger element, low.
  • the temperature of the supply water that is led from the central heating heat exchanger element to the tap water heat exchanger is then in the range of 65 to 90°C, more particularly approximately 70°C, and when, for instance, the return water temperature is approximately 30°C, the average temperature of the central heating heat exchanger element is lower than was customary heretofore.
  • the return water temperature is 50°C
  • the supply temperature is approximately 70°C. Due to this lower average temperature, heating the central heating heat exchanger element requires less heat, which, with the tap water in use, results in a rapid response. Due to the low return water temperature, the flue gases can be cooled further, and in a condensing manner, which, with the tap water in use, results in a better efficiency.
  • heat exchanging surface enlarging pins 10 are provided in the water-carrying channel 4.
  • water-side pins 10 can also be designed as fins and they can also have, instead of a circular cross-section, a square, rectangular or other cross-section.
  • the great temperature difference between the supply water temperature and return water temperature has the advantages described not only with the heat exchanger element, but leads to the described advantages with any type of heating boiler provided with a central heating heat exchanger element which can be connected to a tap water heat exchanger. It will be clear that the combination of the new heat exchanger element described herein, and an embodiment of a heating boiler with tap water heat exchanger with the great ⁇ T between supply water temperature and return water temperature, leads to particularly rapid heating of tap water with tap water in use in combination with a high efficiency.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
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  • Combustion & Propulsion (AREA)
  • Details Of Fluid Heaters (AREA)

Claims (21)

  1. Wärmetauscherelement (1), bestimmt für einen Zentralheizungsboiler, welches Wärmetauscherelement (1) als ein Monoguss aus im Wesentlichen Aluminium konzipiert ist und mittels eines Niederdruck-Gießverfahrens, zum Beispiel Sandstrahlen oder Spritzguss, hergestellt wird, das Wärmetauscherelement versehen mit Wänden (2, 9), die einen Wasser führenden Kanal (4) begrenzen, und mit mindestens einer Wand (2), die mindestens einen Rauchgasabzug (3) begrenzt, an den ein Brenner angeschlossen werden kann, und mindestens einer Wand (2), die den mindestens einen Rauchgasabzug (3), der wassergekühlt ist, begrenzt, indem sie auch eine Begrenzung des Wasser führenden Kanal (4) begrenzt, während die mindestens eine wassergekühlte Wand (2) versehen ist mit die Wärmetauscheroberfläche vergrößernden Stiften und/oder Flossen (8), die sich in den jeweiligen Rauchgasabzug (3) erstrecken, dadurch gekennzeichnet, dass die Querschnittsoberfläche der Stifte und/oder Flossen (8) kleiner als 25 mm2 ist, wobei die Länge der Stifte und/oder Flossen 15 mm oder weniger ist, wobei der Abstand zwischen zwei gegenüberliegenden Wänden (2), die die Stifte und/oder Flossen (8) tragen und einen Rauchgasabzug (3) begrenzen, kleiner als 35 mm ist, zumindest in einem stromabwärts liegenden Abschnitt des jeweiligen Rauchgasabzugs (3).
  2. Wärmetauscherelement (1) nach Anspruch 1, wobei die Querschnittsoberfläche der Stifte und/oder Flossen (8) kleiner als 20 mm2 ist.
  3. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei die Stifte (8) einen im Wesentlichen kreisförmigen Querschnitt mit einem Durchmesser von ungefähr 4 mm haben.
  4. Wärmetauscherelement (1) nach einem der Ansprüche 1-2, wobei die Stifte (8) einen im Wesentlichen quadratischen Querschnitt haben, dessen Seiten eine Länge von ungefähr 4 mm haben.
  5. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei der Rauchgasabzug (3) auf einer Seite, an der ein Brenner (5) angebracht werden kann, erweitert ist, um einen Ausbrennraum (3b), der sehr kompakt ist, zu bilden, währen das Wärmetauscherelement (1) zum Zusammenarbeiten mit einem Hochleistungsbrenner (5) mit kompaktem Ausbrennraum (3b) geeignet ist.
  6. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei die Länge der Stifte und/oder Flossen (8) auf einer stromaufwärts liegenden Seite eines Rauchgasabzugs (3), an dem ein Brenner (5) angebracht werden kann, kleiner als die Länge der Stifte (8) auf einer stromabwärts liegenden Seite ist.
  7. Wärmetauscherelement (1) nach Anspruch 6, wobei die Länge der Stifte und/oder Flossen (8) in dem erweiterten Teil des Rauchgasabzugs (3), der den Ausbrennraum (3b) bildet, zunimmt, je weiter die Stifte und/oder Flossen (8) stromabwärts von dem Brenner (5) angeordnet sind, während die Stifte und/oder Flossen (8) ein einem weiter stromabwärts liegenden Teil des Rauchgasabzugs (3) im Wesentlichen dieselbe Länge haben.
  8. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei der Wasserkanal (4) pro kW Ausgabe ein Volumen hat, das kleiner als 0,05 l/kW ist, insbesondere kleiner als 0,04 l/kW, bevorzugt ungefähr 0,03 l/kW.
  9. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei in dem Wasserkanal (4) die Wärmetauscheroberfläche vergrößernde Stifte und/oder Flossen (10) angeordnet sind, welche wasserseitigen Stifte und/oder Flossen (10) mit einer Basis mit einer Wand (2), die den Rauchgasabzug (3) begrenzt, verbunden sind.
  10. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei das Gewicht des Wärmetauscherelements (1) pro bereitzustellendem kW weniger als 0,20 kg/kW ist, bevorzugt weniger als 0,16 kg/kW.
  11. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei der Abstand zwischen der Wand (9), die auf der einen Seite den Wasser führenden Kanal (4) und auf der anderen Seite eine Außenseite des Wärmetauscherelements (1) begrenzt, und der Wand (2), die auf der einen Seite den Wasser führenden Kanal (4) und auf der anderen Seite den Rauchgasabzug (3) begrenzt, kleiner als 10 mm ist, bevorzugt kleiner als 8 mm.
  12. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei der Brenner (5) an einer Oberseite des Wärmetauscherelements (1) angebracht werden kann, während die Rauchgasfließrichtung von der Oberseite zur Unterseite gerichtet ist.
  13. Wärmetauscherelement (1) nach einem der vorhergehenden Ansprüche, wobei der Wasser führende Kanal (4) mit einem Einlass (6) für zu erhitzendes Wasser versehen ist, welcher Eingang neben dem stromabwärts liegenden Ende des mindestens einen Rauchgasabzugs (3) bereitgestellt ist, während der Wasser führende Kanal (4) mit einem Auslass (7) für erhitztes Wasser versehen ist, welcher Auslass (7) neben einem stromaufwärts liegenden Ende des mindestens einen Rauchgasabzugs (3) bereitgestellt ist.
  14. Wärmetauscherelement nach einem der Ansprüche 1-13, wobei in dem Gießverfahren ein wasserseitiger Kern zum Bilden des Wasserkanals und ein rauchgasseitiger Kern zum Bilden des Rauchgaskanals verwendet werden.
  15. Heizungsboilder (11), umfassend:
    • das Zentralheizungs-Wärmetauscherelement (1, 14) nach einem der Ansprüche 1-14 und
    • einen Hochleistungsbrenner (5, 17), der an dem Wärmetauscherelement (1, 14) angebracht ist.
  16. Heizungsboiler (11), umfassend:
    • das Zentralheizungs-Wärmetauscherelement (1, 14) nach einem der Ansprüche 1-14;
    • einen Brenner;
    • einen Leitungswasser-Wärmetauscher (16), der an einen Auslass (7) des wasserführenden Kanals (4) und einen Einlass (6) des Wasser führenden Kanals (4) angeschlossen werden kann;
    • eine Pumpe (18) zum Transportieren des Wassers durch den Zentralheizungs-Wärmetauscherelement (1, 14) und den Leitungswasser-Wärmetauscher (16), wobei das Zentralheizungs-Wärmetauscherelement (1, 14), der Leitungswasser-Wärmetauscher (16), der Brenner (5, 17) und die Pumpe (18) so aneinander angepasst sind, dass, bei Verwendung von Leitungswasser, der Unterschied zwischen der Versorgungswassertemperatur, d. h., der Temperatur des von dem Wasser führenden Kanal (4) kommende Wasser, das zu dem Leitungswasser-Wärmetauscher (16) geleitet wird, und die Rückführwassertemperatur, d. h., die Temperatur des von dem Leitungswasser-Wärmetauscher (16) kommende Wasser, das in den Einlass (6) des wasserführenden Kanals (4) geleitet wird, größer als 25 C ist und bevorzugt größer als 30 C ist.
  17. Heizungsboiler nach Anspruch 16, wobei die Dimensionierung des Zentralheizungs-Wärmetauscherelement und des Leitungswasser-Wärmetauschers und die Dimensionierung oder die Steuerung der Pumpe derart ist, dass die Strömungsrate in dem wasserführenden Kanal des Zentralheizungs-Wärmetauscherelements relativ niedrig ist, was zu dem relativ großen Temperaturunterschied führt.
  18. Heizungsboiler nach Anspruch 16 oder 17, wobei die Rückführwassertemperatur bei Verwendung von Leitungswasser ungefähr 30 C ist.
  19. Heizungsboiler nach einem der Ansprüche 16-18, wobei die Versorgungswassertemperatur bei Verwendung von Leitungswasser im Bereich von 65 - 90, insbesondere ungefähr 70 C ist.
  20. Heizungsboiler (11) nach einem der Ansprüche 16-19, wobei die von der Pumpe (18) bereitgestellte Strömungsrate einstellbar ist.
  21. Heizungsboiler (11) nach einem der Ansprüche 16-20, wobei die von dem Brenner (5, 17) bereitgestellte Ausgabe einstellbar ist.
EP06076027.9A 2005-05-10 2006-05-09 Wärmetauscherelement und Heizanlage mit so einem Wärmetauscherelement Active EP1722172B1 (de)

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NL1029004A NL1029004C2 (nl) 2005-05-10 2005-05-10 Warmtewisselaarelement alsmede een verwarmingsstelsel voorzien van een dergelijk warmtewisselaarelement.

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US8726851B2 (en) 2007-10-25 2014-05-20 Bekaert Combustion Technology B.V. Heat exchanger element with a combustion chamber for a low CO and NOx emission combustor
US20100242863A1 (en) * 2007-10-25 2010-09-30 Bekaert Combustion Technology B.V. Metallic porous body incorporated by casting into a heat exchanger
WO2010037719A2 (en) * 2008-10-03 2010-04-08 Bekaert Combust. Technol. B.V. High efficiency heat exchanger element
NL2010442C2 (en) * 2013-03-12 2014-09-16 Dejatech Ges B V Heat exchanger and body therefore, and a method for forming a heat exchanger body.
CN104792193B (zh) * 2015-04-30 2016-07-06 樊付辉 一种扁平型冷凝式热交换器
EP3368490B1 (de) 2015-10-28 2019-12-18 Remeha B.V. Wärmetaucher und verfahren zu seiner herstellung
EP3173723B1 (de) 2015-11-25 2018-04-25 Daikin Industries, Limited Wärmetauscher
EP3173721B1 (de) * 2015-11-25 2018-04-25 Daikin Industries, Ltd. Wärmetauscher

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EP0794392A1 (de) * 1996-03-08 1997-09-10 Dejatech B.V. Gegossener,leichtmetallender,im wesentlichen zylindrischer Wärmetaucher

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DE3046454A1 (de) * 1980-12-10 1982-07-15 Ewald 7100 Heilbronn Staiger Heizungskessel
NL9300100A (nl) 1993-01-19 1994-08-16 Radson Alutherm Nv Drie-weg combi-ketel.
DE4421671A1 (de) * 1994-06-23 1996-01-04 Broetje August Gmbh & Co Wärmetauscher, insbesondere für einen gasbeheizten Heizkessel
NL1003624C2 (nl) * 1996-07-17 1998-01-21 Holding J H Deckers N V Gelede verwarmingsketel en verwarmingsinrichting, voorzien van een dergelijke ketel.
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EP1722172A1 (de) 2006-11-15

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