EP2499437B1 - Heat exchanger with improved thermal efficiency - Google Patents
Heat exchanger with improved thermal efficiency Download PDFInfo
- Publication number
- EP2499437B1 EP2499437B1 EP10768981.2A EP10768981A EP2499437B1 EP 2499437 B1 EP2499437 B1 EP 2499437B1 EP 10768981 A EP10768981 A EP 10768981A EP 2499437 B1 EP2499437 B1 EP 2499437B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- coiled duct
- heat exchanger
- section
- transverse cross
- coiled
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000012530 fluid Substances 0.000 claims description 27
- 239000007789 gas Substances 0.000 claims description 22
- 238000002485 combustion reaction Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000003517 fume Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000000670 limiting effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000009428 plumbing 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
- 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
- F24H1/40—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes
- F24H1/43—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes helically or spirally coiled
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
- F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
- F28D7/14—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically both tubes being bent
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/14—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
- F28F1/16—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally the means being integral with the element, e.g. formed by extrusion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/34—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely
- F28F1/36—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely the means being helically wound fins or wire spirals
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/42—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/42—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
- F28F1/422—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element with outside means integral with the tubular element and inside means integral with the tubular element
Definitions
- the present invention relates to a heat exchanger with improved thermal efficiency.
- heat exchangers In the field of heat exchangers and the like, for boilers to be used for heating sanitary water or water for central heating systems, the use is known of heat exchangers that are constituted, generally, by a metal container body inside which a combustion chamber is provided, which accommodates one or more coiled ducts inside which the fluids to be heated circulate.
- the combustible mixture which is typically constituted by air and gas, is sent forcibly into the burner under the thrust of a fan and, after the combustion that occurs in an appropriate chamber, as a result of the thrust from the fan, the burned gases strike the duct by way of the spaces provided in the coiled duct, thus achieving the desired exchange of heat.
- EP 1 750 070 A1 discloses a condensation gas-burning boiler with a heat exchanger through which combustion fumes and water flow, for producing hot water.
- a finned tube through which water flows is arranged inside a cylindrical casing, whereby the finned tube coils about the longitudinal axis of the casing to form a helix comprising a succession of adjacent turns each located adjacent the cylindrical lateral wall of the casing.
- a central deflecting disk is arranged to direct the fumes radially perpendicular to the longitudinal axis between successive turns of the helix, and the tube is provided with an oval-section wall with parallel fins extending tangentially and radially thereto, such that the fumes flow first from the boiler radially outward between gaps of the tangential and parallel fins of the helix turns towards the casing lateral wall, then secondly in a direction parallel to the longitudinal axis at the lateral wall, then thirdly radially inwardly from the lateral wall again between gaps of the tangential and parallel fins of the helix turns, whereby the successive gaps between the tangential and parallel fins of the helix turns define compulsory fume paths.
- EP 0 385 700 discloses a boiler installation comprising an outer casing, central catalytic burner tube, and extending around the burner tube, a heat-exchange unit comprising twin coils each in the form of an inner pipe provided with interior and exterior helical formations and an exterior pipe surrounding the inner pipe. Mains cold water is fed through the inner pipe and gets heat exchanged to it by heated water fed through the exterior pipe which is heated by the hot gases produced by the burner tube.
- the exterior pipe is provided with helical ribs for increasing the surface area exposed externally thereof.
- the aim of the present invention is to provide a heat exchanger with improved thermal efficiency that solves the drawbacks of the known art by increasing the thermal efficiency of the heat exchanger when compared to a conventional heat exchanger of the same dimensions.
- an object of the present invention consists of providing a heat exchanger that is structurally simple, easy to make and assemble, and at low cost.
- the heat exchanger with improved thermal efficiency comprises a container body 2, cylindrical with a circular end face, inside which a coiled duct 3 is accommodated which externally delimits a chamber 4 for the combustion of a combustible mixture 5 for heating the fluid or fluids to be heated 6, which circulate in the coiled duct 3, with the burned gases 7 produced by the combustion of the combustible mixture 5 by means of a burner cylinder 16 with a perforated surface 17.
- the burned gases 7, produced by the combustion of the combustible mixture 5 and defining a flow of hot fluid are sent forcibly onto the coiled duct 3 thus striking its outer surface in order to heat the fluid to be heated 6.
- the coiled duct 3 runs from an inlet mouth 8 to an outlet mouth 9, both outside the container body 2 and positioned, respectively, in the lower portion and in the upper portion of the container body 2.
- a plurality of fins 30 is provided which are defined on the outer surface of the coiled duct 3 and which run substantially along the entire longitudinal length of the coiled duct 3 in order to guide the hot fluid 7 along the coiled duct 3 with consequent increasing of the heat exchange between the hot fluid 7 and the fluid to be heated 6.
- the coiled duct 3 is substantially circular in transverse cross-section and the fins 30 run radially with respect to the circular transverse cross-section of the coiled duct 3, the whole being made in a single piece and without welds.
- the coiled duct 3 is divided internally, along a transverse cross-section, into a plurality of channels which are substantially parallel and independent of each other, each channel being crossed by a respective fluid to be heated 6.
- the coiled duct 3 is divided internally, along a transverse cross-section, into a main channel 31, which is coaxial to the coiled duct 3, and into a plurality of parallel secondary channels 32, which are mutually independent and radially external to the main channel 31.
- the fins 30 can trace a helical path with respect to the axis of the coiled duct 3.
- the coiled duct 3 can be divided into four channels 33 each of which is defined by a circular sector of the circular transverse cross-section of the coiled duct 3, for example, equal to one quarter of the circular transverse cross-section of the coiled duct 3.
- the coiled duct 3 can be arranged in proximity to, or even almost in direct contact with, substantially along all of its length, the outer walls 10 of the container body 2 and an element 11 for conveying the burned gases 7 in order to direct them to a discharge collection tank 20 and subsequently to a discharge tube 12 outside the container body 2.
- an air intake 14 is provided for forcibly injecting the combustible mixture 5, which can be for example a mixture of air and gas, by way of the above mentioned external fan means which consist, for example, in a fan outside the container body 2 which is not shown.
- the combustible mixture 5 is then sent into an intake chamber 15 which is annular in shape, is also defined at the upper face 13, and is connected with the burner cylinder 16.
- the intake chamber 15 is connected directly with the burner cylinder 16 which is defined by a permeable surface 17 and is cylindrical with a circular end face where the flame burns.
- the burner cylinder 16 besides being connected at one end with the intake chamber 15 in order to introduce the combustible mixture 5 into the combustion chamber 4, has the opposite end closed by a thermally insulating disk 18.
- the conveyance element 11 can comprise a cylindrical hollow body with a circular end face, which is delimited in an upper region by the thermally insulating disk 18 and is connected, in proximity to the thermally insulating disk 18, with the discharge tube 12.
- the conveyance element 11 is accommodated in the container body 2 on the opposite side with respect to the burner cylinder 16 and has a lower opening which faces the lower end face 19 of the container body 2 for the transit of the burned gases 7 from the combustion chamber 4 to the discharge collection tank 20.
- the discharge collection tank 20 is arranged at the lower end face 19 of the container body 2 and is adapted to collect the liquids 21 produced by the condensation of the burned gases 7 in contact with the coiled duct 3.
- the discharge collection tank 20 is provided with an outward discharge connector 22 for the outflow of the liquids 21 from the container body 2 and with a discharge connector 23 for the outflow of the exhaust gases 7 by way of the outward discharge tube 12.
- the overall geometry of the heat exchanger 1 or some components can change, such as, for example, the discharge tube 12 which can be accommodated inside the container body 2.
- the coiled duct 3 remains unchanged.
- the combustible mixture 5, under the thrust of the fan means, is sent into the intake chamber 15 through the air intake 14 to then descend in the direction of the axis, i.e. parallel to the axis 25 of the heat exchanger 1, in the burner cylinder 16.
- the combustion occurs through the permeable surface 17 of the burner cylinder 16 and the burned gases 7 are directed into the combustion chamber 4.
- the burned gases 7 Due to the thrust generated by the fan means, the burned gases 7 are pushed towards the coiled duct 3 and guided into the helicoid grooves defined between one fin 30 and the next, thus completely striking the outer surface of the coiled duct 3 and yielding heat to it.
- the burned gases 7, again due to the thrust generated by the fan means, are pushed further downwards because they are compelled by their being guided into the helicoid grooves defined between one fin 30 and the next, and are then conveyed by the conveyance element 11 towards the lower end face 19 of the container body 2.
- any condensation 21 is collected on the bottom of the container body 2 in the discharge collection tank 20 and is then discharged by way of the connector 22, and the burned gases 7 flow outside by way of the discharge connector 23 and the discharge tube 12.
- this yield occurs thanks to the inner walls 34 or 35 of the coiled duct 3 which divide the channels 31, 32 and 33.
- the material from which the coiled duct 3 is made, for example aluminum or alloys thereof, through the inner walls 34 and 35 bring the heat yielded to the fins 30 right to the centre of the coiled duct 3.
- the heat exchanger with improved thermal efficiency fully achieves the intended aim and object in that the presence of the fins, specifically with helicoid twisting, on the outer surface of the coiled duct allows to guide the hot fluid, thus making it completely strike the outer surface of the coiled duct so as to optimise the heat exchange.
- a further advantage of the heat exchanger with improved thermal efficiency, according to the present invention consists in that it is structurally simple, easy to make and at low cost.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
- The present invention relates to a heat exchanger with improved thermal efficiency.
- In the field of heat exchangers and the like, for boilers to be used for heating sanitary water or water for central heating systems, the use is known of heat exchangers that are constituted, generally, by a metal container body inside which a combustion chamber is provided, which accommodates one or more coiled ducts inside which the fluids to be heated circulate.
- Usually, the combustible mixture, which is typically constituted by air and gas, is sent forcibly into the burner under the thrust of a fan and, after the combustion that occurs in an appropriate chamber, as a result of the thrust from the fan, the burned gases strike the duct by way of the spaces provided in the coiled duct, thus achieving the desired exchange of heat.
- Such known types of heat exchangers are not devoid of drawbacks, among which the fact that the burned gases cannot manage to strike the coiled duct completely and therefore the heat exchange has an effective efficiency that is not satisfactory.
- This drawback is even more pronounced when a plurality of coiled ducts are used in the same heat exchanger. The presence of a plurality of coiled ducts intertwined in each other and/or intercalated with each other, leads to evident fluidodynamic limits of the burned gases which should strike the ducts and to evident heat exchange limits between the outer duct and the inner duct.
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EP 1 750 070 A1 discloses a condensation gas-burning boiler with a heat exchanger through which combustion fumes and water flow, for producing hot water. A finned tube through which water flows is arranged inside a cylindrical casing, whereby the finned tube coils about the longitudinal axis of the casing to form a helix comprising a succession of adjacent turns each located adjacent the cylindrical lateral wall of the casing. A central deflecting disk is arranged to direct the fumes radially perpendicular to the longitudinal axis between successive turns of the helix, and the tube is provided with an oval-section wall with parallel fins extending tangentially and radially thereto, such that the fumes flow first from the boiler radially outward between gaps of the tangential and parallel fins of the helix turns towards the casing lateral wall, then secondly in a direction parallel to the longitudinal axis at the lateral wall, then thirdly radially inwardly from the lateral wall again between gaps of the tangential and parallel fins of the helix turns, whereby the successive gaps between the tangential and parallel fins of the helix turns define compulsory fume paths. -
EP 0 385 700 discloses a boiler installation comprising an outer casing, central catalytic burner tube, and extending around the burner tube, a heat-exchange unit comprising twin coils each in the form of an inner pipe provided with interior and exterior helical formations and an exterior pipe surrounding the inner pipe. Mains cold water is fed through the inner pipe and gets heat exchanged to it by heated water fed through the exterior pipe which is heated by the hot gases produced by the burner tube. The exterior pipe is provided with helical ribs for increasing the surface area exposed externally thereof. - The aim of the present invention is to provide a heat exchanger with improved thermal efficiency that solves the drawbacks of the known art by increasing the thermal efficiency of the heat exchanger when compared to a conventional heat exchanger of the same dimensions.
- Within this aim, an object of the present invention consists of providing a heat exchanger that is structurally simple, easy to make and assemble, and at low cost.
- In accordance with the invention, there is provided a heat exchanger as defined in the appended claims.
- Further characteristics and advantages of the invention will become better apparent from the description of a preferred, but not exclusive, embodiment of a heat exchanger with improved thermal efficiency, according to the invention, illustrated by way of non-limiting example in the accompanying drawings, wherein:
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Figure 1 shows a longitudinal sectional view of a heat exchanger with improved thermal efficiency, according to the invention; -
Figure 2 is a side elevation view of the coiled duct of the heat exchanger shown inFigure 1 ; -
Figure 3 is a plan view of the coiled duct of the heat exchanger shown inFigure 1 ; -
Figure 4 is a partial plan view of a first variation of the coiled duct shown inFigure 3 ; -
Figure 5 is a sectional view of the coiled duct shown inFigure 4 , taken along the line V-V; -
Figure 6 is a partial plan view of a second variation of the coiled duct shown inFigure 3 ; -
Figure 7 is a sectional view of the coiled duct shown inFigure 4 , taken along the line VII-VII; - With reference to the figures, the heat exchanger with improved thermal efficiency, generally indicated with the reference numeral 1, comprises a
container body 2, cylindrical with a circular end face, inside which acoiled duct 3 is accommodated which externally delimits achamber 4 for the combustion of acombustible mixture 5 for heating the fluid or fluids to be heated 6, which circulate in thecoiled duct 3, with the burnedgases 7 produced by the combustion of thecombustible mixture 5 by means of aburner cylinder 16 with a perforatedsurface 17. - By way of fan means, not shown, the burned
gases 7, produced by the combustion of thecombustible mixture 5 and defining a flow of hot fluid, are sent forcibly onto the coiledduct 3 thus striking its outer surface in order to heat the fluid to be heated 6. - More precisely, the
coiled duct 3 runs from aninlet mouth 8 to anoutlet mouth 9, both outside thecontainer body 2 and positioned, respectively, in the lower portion and in the upper portion of thecontainer body 2. - According to the invention, a plurality of
fins 30 is provided which are defined on the outer surface of thecoiled duct 3 and which run substantially along the entire longitudinal length of thecoiled duct 3 in order to guide thehot fluid 7 along thecoiled duct 3 with consequent increasing of the heat exchange between thehot fluid 7 and the fluid to be heated 6. - Advantageously, the
coiled duct 3 is substantially circular in transverse cross-section and thefins 30 run radially with respect to the circular transverse cross-section of thecoiled duct 3, the whole being made in a single piece and without welds. - In order to be able to simultaneously or selectively heat a plurality of
fluids 6 such as, for example, water intended for the sanitary plumbing system of a building or for the central heating system of the same building, thecoiled duct 3 is divided internally, along a transverse cross-section, into a plurality of channels which are substantially parallel and independent of each other, each channel being crossed by a respective fluid to be heated 6. - More specifically, the
coiled duct 3 is divided internally, along a transverse cross-section, into amain channel 31, which is coaxial to thecoiled duct 3, and into a plurality of parallelsecondary channels 32, which are mutually independent and radially external to themain channel 31. - In this way, it is possible to obtain five channels of which one, the
main channel 31, is crossed by a first fluid to be heated 6 and four, thesecondary channels 32, having a transverse cross-section that is substantially equal to one quarter of the transverse cross-section of the region outside themain channel 31, i.e. equal to one quarter of the circular rim, are crossed by a second fluid to be heated 6. - In a first possible variation of the
coiled duct 3, thefins 30 can trace a helical path with respect to the axis of thecoiled duct 3. - In a second possible variation of the
coiled duct 3, thecoiled duct 3 can be divided into fourchannels 33 each of which is defined by a circular sector of the circular transverse cross-section of thecoiled duct 3, for example, equal to one quarter of the circular transverse cross-section of thecoiled duct 3. - With a helicoid fin structure of the
coiled duct 3, thecoiled duct 3 can be arranged in proximity to, or even almost in direct contact with, substantially along all of its length, theouter walls 10 of thecontainer body 2 and anelement 11 for conveying the burnedgases 7 in order to direct them to adischarge collection tank 20 and subsequently to adischarge tube 12 outside thecontainer body 2. - At the
upper face 13 of thecontainer body 2, anair intake 14 is provided for forcibly injecting thecombustible mixture 5, which can be for example a mixture of air and gas, by way of the above mentioned external fan means which consist, for example, in a fan outside thecontainer body 2 which is not shown. - The
combustible mixture 5 is then sent into anintake chamber 15 which is annular in shape, is also defined at theupper face 13, and is connected with theburner cylinder 16. - In more detail, the
intake chamber 15 is connected directly with theburner cylinder 16 which is defined by apermeable surface 17 and is cylindrical with a circular end face where the flame burns. - The
burner cylinder 16, besides being connected at one end with theintake chamber 15 in order to introduce thecombustible mixture 5 into thecombustion chamber 4, has the opposite end closed by a thermally insulatingdisk 18. - Advantageously, the
conveyance element 11 can comprise a cylindrical hollow body with a circular end face, which is delimited in an upper region by the thermally insulatingdisk 18 and is connected, in proximity to the thermally insulatingdisk 18, with thedischarge tube 12. - Conveniently, the
conveyance element 11 is accommodated in thecontainer body 2 on the opposite side with respect to theburner cylinder 16 and has a lower opening which faces thelower end face 19 of thecontainer body 2 for the transit of the burnedgases 7 from thecombustion chamber 4 to thedischarge collection tank 20. - Moreover, the
discharge collection tank 20 is arranged at thelower end face 19 of thecontainer body 2 and is adapted to collect theliquids 21 produced by the condensation of the burnedgases 7 in contact with thecoiled duct 3. - The
discharge collection tank 20 is provided with anoutward discharge connector 22 for the outflow of theliquids 21 from thecontainer body 2 and with adischarge connector 23 for the outflow of theexhaust gases 7 by way of theoutward discharge tube 12. - In a possible variation of the heat exchanger 1, the overall geometry of the heat exchanger 1 or some components can change, such as, for example, the
discharge tube 12 which can be accommodated inside thecontainer body 2. In any case, thecoiled duct 3 remains unchanged. - Operation of the heat exchanger according to the present invention is as follows.
- In particular, it is necessary to emphasise that the heat exchange between the fluid to be heated 6 and the burned
gases 7, which in the drawings occurs in counter-current, is favoured by the presence of thefins 30. - The
combustible mixture 5, under the thrust of the fan means, is sent into theintake chamber 15 through theair intake 14 to then descend in the direction of the axis, i.e. parallel to theaxis 25 of the heat exchanger 1, in theburner cylinder 16. - The combustion occurs through the
permeable surface 17 of theburner cylinder 16 and the burnedgases 7 are directed into thecombustion chamber 4. - Due to the thrust generated by the fan means, the burned
gases 7 are pushed towards thecoiled duct 3 and guided into the helicoid grooves defined between onefin 30 and the next, thus completely striking the outer surface of thecoiled duct 3 and yielding heat to it. - The burned
gases 7, again due to the thrust generated by the fan means, are pushed further downwards because they are compelled by their being guided into the helicoid grooves defined between onefin 30 and the next, and are then conveyed by theconveyance element 11 towards thelower end face 19 of thecontainer body 2. - More specifically, the geometry of the
coiled duct 3, by being contained between the walls of thecontainer body 2 and of theconveyance element 11, forces the burnedgases 7 to cross the helicoid grooves defined between thefins 30 thus considerably increasing the thermal efficiency. - As mentioned above, any
condensation 21 is collected on the bottom of thecontainer body 2 in thedischarge collection tank 20 and is then discharged by way of theconnector 22, and the burnedgases 7 flow outside by way of thedischarge connector 23 and thedischarge tube 12. - In this manner, the calorific power possessed by the burned
gases 7 is yielded to the fluids to be heated 6. - More precisely, this yield occurs thanks to the
inner walls coiled duct 3 which divide thechannels coiled duct 3 is made, for example aluminum or alloys thereof, through theinner walls fins 30 right to the centre of thecoiled duct 3. - Therefore, if one or more of the
channels gases 7 and the fluid to be heated 6 which crosses at least one of thechannels - In practice it has been found that the heat exchanger with improved thermal efficiency, according to the present invention, fully achieves the intended aim and object in that the presence of the fins, specifically with helicoid twisting, on the outer surface of the coiled duct allows to guide the hot fluid, thus making it completely strike the outer surface of the coiled duct so as to optimise the heat exchange.
- A further advantage of the heat exchanger with improved thermal efficiency, according to the present invention, consists in that it is structurally simple, easy to make and at low cost.
- The heat exchanger with improved thermal efficiency, thus conceived, is susceptible of numerous modifications and variations, all of which are within the scope of the appended claims.
- Moreover, all the details may be substituted by other, technically equivalent elements.
- In practice the materials employed, provided they are compatible with the specific use, and the dimensions and the contingent shapes, may be any according to requirements and to the state of the art.
- The disclosures in Italian Patent Application No.
MI2009A001983 - Where technical features mentioned in any claim are followed by reference signs, those reference signs have been included for the sole purpose of increasing the intelligibility of the claims and accordingly, such reference signs do not have any limiting effect on the interpretation of each element identified by way of example by such reference signs.
Claims (8)
- A heat exchanger (1) with improved thermal efficiency, comprising a containment body (2) crossed by a forced flow of hot fluid (7) and at least one coiled duct (3) crossed internally by at least one fluid to be heated (6), said at least one coiled duct (3) being accommodated inside said containment body (2) and being struck by said hot fluid (7) in order to heat said at least one fluid to be heated (6), the heat exchanger (1) further comprising a plurality of fins (30), which are provided on the outer surface of said at least one coiled duct (3) and run substantially along the entire longitudinal length of said at least one coiled duct (3) in order to guide said hot fluid (7) along said at least one coiled duct (3) so as to increase the heat exchange between said at least one hot fluid (7) and said fluid to be heated (6), said fins (30) tracing a helical path with respect to the axis of said at least one coiled duct (3), characterized in that said at least one coiled duct (3) is arranged in proximity to, or even almost in direct contact with, substantially along all of its length, the outer walls (10) of said container body (2) and an element (11) for conveying the burned gases (7) in order to direct them to a discharge collection tank (20) and subsequently to a discharge tube (12) outside the container body (2), wherein the geometry of said at least one coiled duct (3), by being contained between the walls of the container body (2) and of the conveyance element (11) forces the burned gases (7) to cross the helicoid grooves defined between the fins (30) for increasing the thermal efficiency.
- The heat exchanger (1) according to claim 1, characterized in that said at least one coiled duct (3) substantially has a circular transverse cross-section and in that said fins (30) run radially with respect to said circular transverse cross-section.
- The heat exchanger (1) according to one or more of the preceding claims, characterized in that said at least one coiled duct (3) is divided internally, along a transverse cross-section, into a plurality of channels (33) which are substantially parallel and independent of each other, each channel being crossed by a respective fluid to be heated (6).
- The heat exchanger according to claim 3, characterized in that each one of said channels (33) is formed by a circular sector of the circular transverse cross-section of said at least one coiled duct (3).
- The heat exchanger (1) according to one or more of the preceding claims, characterized in that it comprises four of said channels (33) having a transverse cross-section that is substantially equal to one quarter of the circular transverse cross-section of said at least one coiled duct (3).
- The heat exchanger (1) according to one or more of claims 1 and 2, characterized in that said at least one coiled duct (3) is divided internally, along a transverse cross-section, into a main channel (31), which is coaxial to said at least one coiled duct (3), and into a plurality of parallel secondary channels (32), which are mutually independent and radially external to said main channel (31), said main channel (31) and said secondary channels (32) being crossed respectively by a first fluid to be heated (6) and by a second fluid to be heated (6).
- The heat exchanger (1) according to claim 6, characterized in that each one of said secondary channels (32) is formed by an annular sector of said at least one coiled duct (3).
- The heat exchanger (1) according to one or more of claims 6 and 7, characterized in that it comprises four of said secondary channels (32) having a transverse cross-section that is substantially equal to one quarter of the transverse cross-section of the region outside said main channel (31) of said at least one coiled duct (3).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITMI2009A001983A IT1396923B1 (en) | 2009-11-12 | 2009-11-12 | HEAT EXCHANGER WITH INCREASED THERMAL EFFICIENCY. |
PCT/EP2010/066277 WO2011057895A1 (en) | 2009-11-12 | 2010-10-27 | Heat exchanger with improved thermal efficiency |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2499437A1 EP2499437A1 (en) | 2012-09-19 |
EP2499437B1 true EP2499437B1 (en) | 2018-05-02 |
Family
ID=42167572
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10768981.2A Active EP2499437B1 (en) | 2009-11-12 | 2010-10-27 | Heat exchanger with improved thermal efficiency |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2499437B1 (en) |
IT (1) | IT1396923B1 (en) |
WO (1) | WO2011057895A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102015015335A1 (en) * | 2015-11-26 | 2017-06-01 | Linde Aktiengesellschaft | Latent heat storage, method and heating arrangement |
CN114659393B (en) * | 2022-03-23 | 2023-07-18 | 江苏庆峰工程集团有限公司 | Heat exchange system |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0385700A1 (en) * | 1989-02-28 | 1990-09-05 | Michael John Nunnerley | Heat exchange unit, heat exchange system, method of improving heat exchange efficiency, and refrigeration circuit |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2209325C3 (en) * | 1970-05-18 | 1978-08-03 | Noranda Metal Industries Inc., Bellingham, Wash. (V.St.A.) | Heat exchange tube |
AU3338500A (en) * | 1999-03-31 | 2000-10-16 | Asea Brown Boveri Limited | Heat exchanger |
EP1750070B1 (en) * | 2005-08-05 | 2012-05-30 | ELBI International S.p.A. | Gas boiler provided with a heat exchanger with finned tube and method of producing the same |
-
2009
- 2009-11-12 IT ITMI2009A001983A patent/IT1396923B1/en active
-
2010
- 2010-10-27 EP EP10768981.2A patent/EP2499437B1/en active Active
- 2010-10-27 WO PCT/EP2010/066277 patent/WO2011057895A1/en active Application Filing
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0385700A1 (en) * | 1989-02-28 | 1990-09-05 | Michael John Nunnerley | Heat exchange unit, heat exchange system, method of improving heat exchange efficiency, and refrigeration circuit |
Also Published As
Publication number | Publication date |
---|---|
IT1396923B1 (en) | 2012-12-20 |
WO2011057895A8 (en) | 2011-07-07 |
WO2011057895A1 (en) | 2011-05-19 |
EP2499437A1 (en) | 2012-09-19 |
ITMI20091983A1 (en) | 2011-05-13 |
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