EP1722172B1 - Elément d'un échangeur de chaleur et système de chauffage avec un tel élément - Google Patents
Elément d'un échangeur de chaleur et système de chauffage avec un tel élément Download PDFInfo
- 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
- European Patent Office
- Prior art keywords
- heat exchanger
- water
- exchanger element
- flue gas
- pins
- Prior art date
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- 238000010438 heat treatment Methods 0.000 title claims description 68
- 239000003546 flue gas Substances 0.000 claims description 51
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 36
- 239000008399 tap water Substances 0.000 claims description 34
- 235000020679 tap water Nutrition 0.000 claims description 34
- 238000005266 casting Methods 0.000 claims description 13
- 239000008400 supply water Substances 0.000 claims description 8
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 5
- 238000004512 die casting Methods 0.000 claims description 5
- 238000007528 sand casting Methods 0.000 claims description 3
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 229910001338 liquidmetal Inorganic materials 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000012546 transfer Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000008236 heating water Substances 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
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- 238000005260 corrosion Methods 0.000 description 1
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- 238000004904 shortening Methods 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0005—Details for water heaters
- F24H9/001—Guiding means
- F24H9/0026—Guiding means in combustion gas channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/22—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
- F24H1/24—Water 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
- F24H1/26—Water 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0005—Details for water heaters
- F24H9/001—Guiding means
- F24H9/0015—Guiding means in water channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/022—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being wires or pins
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/12—Elements 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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Claims (21)
- Elément d'échangeur de chaleur (1) destiné à une chaudière de chauffage central, lequel élément d'échangeur de chaleur (1) est conçu comme un moulage unique sensiblement à partir d'aluminium et est fabriqué au moyen d'un processus de moulage basse pression, par exemple moulage au sable ou moulage sous pression, l'élément d'échangeur de chaleur étant pourvu de parois (2, 9) qui bordent un canal d'arrivée d'eau (4), et avec au moins une paroi (2) qui borde au moins un canal d'évacuation de fumée (3) auquel un brûleur peut être connecté, au moins une paroi (2) qui borde l'au moins un canal d'évacuation de fumée (3) étant refroidie par eau en ce qu'il forme aussi une frontière du canal d'arrivée d'eau (4), alors qu'une dite au moins une paroi (2) refroidie par eau est pourvue de picots et/ou d'ailettes (8) d'augmentation de surface d'échange de chaleur qui s'étendent dans le canal d'évacuation de fumée (3) respectif, caractérisé en ce que la surface en section transversale desdits picots et/ou ailettes (8) est inférieure à 25 mm2, dans lequel la longueur desdits picots et/ou ailettes est de 15 mm ou moins, dans lequel la distance entre les deux parois (2) opposées, qui portent les picots et/ou ailettes (8) et bordent un canal d'évacuation de fumée (3), est inférieure à 35 mm, au moins dans une partie aval du canal d'évacuation de fumée (3).
- Elément d'échangeur de chaleur (1) selon la revendication 1, dans lequel la surface de section transversale desdits picots et/ou ailettes (8) est inférieure à 20 mm2.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel les picots (8) ont une section transversale sensiblement circulaire avec un diamètre d'approximativement 4 mm.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications 1-2, dans lequel les picots (8) ont une section transversale sensiblement carrée, dont les côtés ont une longueur d'approximativement 4 mm.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel un canal d'évacuation de fumée (3) est élargi sur un côté sur lequel un brûleur (5) peut être monté, pour former un espace de combustion (3b) qui est très compact, alors que l'élément d'échangeur de chaleur (1) convient pour coopérer avec un brûleur (5) à haute performance avec un espace de combustion (3b) compact.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel la longueur des picots et/ou ailettes (8) sur un côté amont d'un canal d'évacuation de fumée (3) sur lequel un brûleur (5) peut être monté est inférieure à la longueur des picots (8) sur un côté aval.
- Elément d'échangeur de chaleur (1) selon la revendication 6, dans lequel la longueur des picots et/ou ailettes (8) dans la partie élargie du canal d'évacuation de fumée (3) formant l'espace de combustion (3b) augmente quand les picots et/ou ailettes (8) sont agencées plus en aval du brûleur (5), alors que les picots et/ou ailettes (8) dans une partie plus en aval du canal d'évacuation de fumée (3) ont sensiblement la même longueur.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel la sortie par kW du canal d'eau (4), a un volume qui est inférieur à 0,05 l/kW, plus particulièrement inférieur à 0,04 l/kW, de préférence approximativement 0,03 l/kW.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel dans le canal d'eau (4) des picots et/ou ailettes (10) d'agrandissement de surface d'échange de chaleur sont agencés, lesquels picots et/ou ailettes (10) côté eau sont connectés à une base avec une paroi (2) qui borde un dit canal d'évacuation de fumée (3).
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel le poids de l'élément d'échangeur de chaleur (1) par kW à fournir est inférieur à 0,2 kg/kW, de préférence inférieur à 0,16 kg/kW.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel la distance entre la paroi (9) qui borde, sur l'un côté, le canal d'arrivée d'eau (4) et, sur l'autre côté, un extérieur de l'élément d'échangeur de chaleur (1), et la paroi (2) qui borde, sur l'un côté, le canal d'arrivée d'eau (4) et, sur l'autre côté, le canal d'évacuation de fumée (3), est inférieure à 10 mm, de préférence inférieure à 8 mm.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel le brûleur (5) peut être monté sur un côté supérieur de l'élément d'échangeur de chaleur (1), alors que la direction d'écoulement de fumée est dirigée du haut vers le bas.
- Elément d'échangeur de chaleur (1) selon l'une quelconque des revendications précédentes, dans lequel le canal d'arrivée d'eau (4) est pourvu d'un orifice d'entrée (6) pour l'eau à chauffer, cette entrée étant placée adjacente à l'extrémité aval de l'au moins un canal d'évacuation de fumée (3), alors que le canal d'arrivée d'eau (4) est pourvu d'un orifice de sortie (7) pour l'eau chauffée, cet orifice de sortie (7) étant placé adjacent à une extrémité amont de l'au moins un canal d'évacuation de fumée (3).
- Elément d'échangeur de chaleur selon l'une quelconque des revendications 1-13, dans lequel dans le processus de moulage, utilisation est faite d'un noyau côté eau pour former le canal d'eau et d'un noyau côté fumée pour former le canal d'évacuation de fumée.
- Chaudière de chauffage (11) incluant :l'élément d'échangeur de chaleur (1, 14) de chauffage central selon l'une quelconque des revendications 1-14, etun brûleur (5, 17) haute performance qui est monté sur l'élément d'échangeur de chaleur (1, 14).
- Chaudière de chauffage (11) incluant :l'élément d'échangeur de chaleur (1, 14) de chauffage central selon l'une quelconque des revendications 1-14 ;un brûleur ;un échangeur de chaleur (16) d'eau du robinet qui peut être connecté à un orifice de sortie (7) du canal d'arrivée d'eau (4) et un orifice d'entrée (6) du canal d'arrivée d'eau (4),une pompe (18) pour transporter l'eau à travers l'élément d'échangeur de chaleur (1, 14) de chauffage central et l'échangeur de chaleur (16) d'eau du robinet, dans lequel l'élément d'échangeur de chaleur (1, 14) de chauffage central, l'échangeur de chaleur (16) d'eau du robinet, le brûleur (5, 17) et la pompe (18) sont ajustés ensemble de telle manière que, avec l'eau du robinet en utilisation, la différence entre la température d'eau d'alimentation, c'est à dire, la température de l'eau venant du canal d'arrivée d'eau (4) qui est amenée vers l'échangeur de chaleur (16) d'eau du robinet, et la température d'eau de retour, c'est à dire la température de l'eau venant de l'échangeur de chaleur (16) d'eau du robinet qui est amenée dans l'orifice d'entrée (6) du canal d'arrivée d'eau (4), est supérieure à 25° et est de préférence supérieure à 30°.
- Chaudière de chauffage selon la revendication 16, dans laquelle le dimensionnement de l'élément d'échangeur de chaleur de chauffage central et de l'échangeur de chaleur d'eau du robinet, et le dimensionnement, ou la commande de la pompe est tel que le débit dans le canal d'arrivée d'eau de l'élément d'échangeur de chaleur de chauffage central est relativement faible, ayant pour résultat ladite relativement grande différence de température.
- Chaudière de chauffage selon la revendication 16 ou 17, dans laquelle la température d'eau de retour avec l'eau du robinet en utilisation est approximativement de 30°C.
- Chaudière de chauffage selon l'une quelconque des revendications 16-18, dans laquelle la température d'eau d'alimentation avec l'eau du robinet en utilisation est dans la plage de 65-90, plus particulièrement d'approximativement 70°C.
- Chaudière de chauffage (11) selon l'une quelconque des revendications 16-19, dans laquelle le débit fourni par la pompe (18) est réglable.
- Chaudière de chauffage (11) selon l'une quelconque des revendications 16-20, dans laquelle la sortie fournie par le brûleur (5, 17) est réglable.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL1029004A NL1029004C2 (nl) | 2005-05-10 | 2005-05-10 | Warmtewisselaarelement alsmede een verwarmingsstelsel voorzien van een dergelijk warmtewisselaarelement. |
Publications (2)
Publication Number | Publication Date |
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EP1722172A1 EP1722172A1 (fr) | 2006-11-15 |
EP1722172B1 true EP1722172B1 (fr) | 2018-09-19 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06076027.9A Active EP1722172B1 (fr) | 2005-05-10 | 2006-05-09 | Elément d'un échangeur de chaleur et système de chauffage avec un tel élément |
Country Status (2)
Country | Link |
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EP (1) | EP1722172B1 (fr) |
NL (1) | NL1029004C2 (fr) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101503960B1 (ko) * | 2007-10-25 | 2015-03-18 | 베카에르트 컴버스천 테크놀러지 비.브이. | 저 일산화탄소 및 산화질소 배출 연소기용 연소 챔버를 구비한 열교환기 요소 |
EP2201306A1 (fr) * | 2007-10-25 | 2010-06-30 | Bekaert Combust. Technol. B.V. | Corps poreux métallique incorporé par coulée dans un échangeur de chaleur |
WO2010037719A2 (fr) * | 2008-10-03 | 2010-04-08 | Bekaert Combust. Technol. B.V. | Élément d’échange thermique à haute efficacité |
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 (fr) | 2015-10-28 | 2019-12-18 | Remeha B.V. | Échangeur de chaleur et son procédé de fabrication |
EP3173723B1 (fr) | 2015-11-25 | 2018-04-25 | Daikin Industries, Limited | Echangeur de chaleur |
EP3173721B1 (fr) * | 2015-11-25 | 2018-04-25 | Daikin Industries, Ltd. | Echangeur de chaleur |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0794392A1 (fr) * | 1996-03-08 | 1997-09-10 | Dejatech B.V. | Echangeur de chaleur coulé de métal léger, essentiellement cylindrique |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2000268B (en) * | 1977-06-09 | 1982-01-27 | Ass Eng Ltd | Improvements in or relating to heat exchangers |
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. |
NL1006456C2 (nl) * | 1997-07-02 | 1999-01-05 | Remeha Fabrieken Bv | Warmtewisselaar en CV-ketel voorzien van een dergelijke warmtewisselaar. |
US5829514A (en) * | 1997-10-29 | 1998-11-03 | Eastman Kodak Company | Bonded cast, pin-finned heat sink and method of manufacture |
-
2005
- 2005-05-10 NL NL1029004A patent/NL1029004C2/nl not_active IP Right Cessation
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2006
- 2006-05-09 EP EP06076027.9A patent/EP1722172B1/fr active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0794392A1 (fr) * | 1996-03-08 | 1997-09-10 | Dejatech B.V. | Echangeur de chaleur coulé de métal léger, essentiellement cylindrique |
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NL1029004C2 (nl) | 2006-11-13 |
EP1722172A1 (fr) | 2006-11-15 |
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