US20160334137A1 - Condensing boiler - Google Patents
Condensing boiler Download PDFInfo
- Publication number
- US20160334137A1 US20160334137A1 US15/152,917 US201615152917A US2016334137A1 US 20160334137 A1 US20160334137 A1 US 20160334137A1 US 201615152917 A US201615152917 A US 201615152917A US 2016334137 A1 US2016334137 A1 US 2016334137A1
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- Prior art keywords
- fumes
- collection chamber
- chamber
- fume collection
- fume
- 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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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
- F24H9/0036—Dispositions against condensation of combustion products
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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
- F24H1/24—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
- F24H1/263—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 with a dry-wall combustion chamber
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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
- F24H1/24—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
- F24H1/28—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 including one or more furnace or fire tubes
- F24H1/285—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 including one or more furnace or fire tubes with the fire tubes arranged alongside the combustion chamber
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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
-
- 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
- F24H1/44—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with combinations of two or more of the types covered by groups F24H1/24 - F24H1/40 , e.g. boilers having a combination of features covered by F24H1/24 - F24H1/40
- F24H1/445—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with combinations of two or more of the types covered by groups F24H1/24 - F24H1/40 , e.g. boilers having a combination of features covered by F24H1/24 - F24H1/40 with integrated flue gas condenser
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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
- F24H8/00—Fluid heaters characterised by means for extracting latent heat from flue gases by means of condensation
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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
- F24H9/0015—Guiding means in water channels
- F24H9/0021—Sleeves surrounding heating elements or heating pipes, e.g. pipes filled with heat transfer fluid, for guiding heated liquid
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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
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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
- F24H9/12—Arrangements for connecting heaters to circulation pipes
- F24H9/13—Arrangements for connecting heaters to circulation pipes for water heaters
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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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
- F28D21/0003—Recuperative heat exchangers the heat being recuperated from exhaust gases
- F28D21/0005—Recuperative heat exchangers the heat being recuperated from exhaust gases for domestic or space-heating systems
- F28D21/0007—Water heaters
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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
- F28D7/12—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 the surrounding tube being closed at one end, e.g. return type
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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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0012—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form
- F28D9/0018—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form without any annular circulation of the heat exchange media
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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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
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- 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
- F28F1/08—Tubular elements crimped or corrugated in longitudinal section
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2200/00—Heat sources or energy sources
- F24D2200/16—Waste heat
- F24D2200/18—Flue gas recuperation
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
Definitions
- the present invention relates to a condensing boiler.
- condensing boilers have an outer enclosure that defines a chamber containing the water to be heated and which accommodates internally a burner constituted by a combustion chamber associated with a burner and connected to a plurality of fume tubes, which exchange heat with the water to be heated, in order to allow the transmission of sensible heat and latent heat from the fumes to the water, and which lead into a fume collection chamber connected to a stack.
- a condensing device usually constituted by a coil, inside which water passes through and outside which the fumes flow over, the function of which is to also recover the latent heat from any residual water vapor in the fumes exiting from the fume tubes.
- the aim of the present invention is to provide a condensing boiler that is capable of reaching high yield levels by way of recovering most of the latent heat available in the combustion fumes.
- Another object of the present invention is to provide a condensing boiler that has a condensing device which for the same space occupation with respect to conventional condensing devices has a greater heat exchange surface.
- Another object of the present invention is to provide a condensing boiler that is simple to provide in terms of construction, so that it can be competitive from a merely economic viewpoint as well.
- FIG. 1 is a longitudinal cross-sectional view of a condensing boiler according to the invention
- FIG. 2 is a schematic front elevation view of a condensing device present in the boiler according to the invention.
- FIG. 3 is an enlarged longitudinal cross-sectional view of a portion of the boiler according to the invention.
- a condensing boiler generally indicated with the reference numeral 1 , comprises an outer enclosure 2 , for example substantially cylindrical, inside which is defined a chamber 3 for containing the water to be heated.
- the containment chamber 3 is provided with an inlet 3 a , which can be connected to a duct 5 for the return of cold water, originating for example from a heating system or from the water mains, and an outlet 3 b , which can be connected to a duct 6 for the delivery of hot water, which arrives, for example, in the heating system or in the household water system.
- a combustion chamber 7 which is associated with a burner 8 .
- the combustion chamber 7 is, for example, delimited laterally by a cylindrical wall 9 , which separates it from the chamber 3 containing the water to be heated, and is, conveniently, positioned substantially coaxially to the outer enclosure 2 .
- the burner 8 is, conveniently, arranged at one longitudinal end 7 a of the combustion chamber 7 , which, at its opposite end, is closed by a deflection wall 7 b which deflects the fumes produced by the flame generated by the burner 8 , so as to make them turn toward the end 7 a of the combustion chamber where the burner 8 is located.
- a tubular element 10 positioned substantially coaxial to the burner 8 , which laterally confines the flame produced by the burner 8 and defines, with the cylindrical wall 9 , an annular interspace 11 , into which the fumes redirected by the deflection wall 7 b are channeled and directed toward the end 7 a of the combustion chamber 7 .
- the tubular element 10 can, advantageously, have a corrugated shape structure in order to increase the turbulence of the fumes.
- the combustion chamber 7 is connected to a plurality of heat exchange tubes 12 , which pass through the containment chamber 3 and lead, with an outlet end 12 a thereof, into a fume collection chamber 13 , which is, conveniently, arranged, with respect to the chamber 3 for containing the water to be heated, at the opposite end to the burner 8 . While the fumes flow over the heat exchange tubes 12 they transfer sensible heat and part of the latent heat to the water present in the containment chamber 3 .
- the combustion chamber 7 has, for example, one or more ports 13 which are connected with a fume redirection chamber 14 , which channels the fumes into the heat exchange tubes 12 and is defined, substantially, between a delimiting end wall 15 of the chamber 3 containing the water to be heated and a door 16 , which is passed through, axially, by the burner 8 and can be opened in order to allow inspection of the combustion chamber.
- a fume redirection chamber 14 which channels the fumes into the heat exchange tubes 12 and is defined, substantially, between a delimiting end wall 15 of the chamber 3 containing the water to be heated and a door 16 , which is passed through, axially, by the burner 8 and can be opened in order to allow inspection of the combustion chamber.
- the collection chamber 13 for the fumes originating from the heat exchange tubes 12 is substantially cylindrical and is connected to a stack 17 for evacuating the fumes to outside the boiler.
- a condensing device 18 for the fumes arriving in the fume collection chamber 13 , which makes it possible to recover any residual latent heat in the fumes before they exit into the atmosphere through the stack 17 .
- the stack 17 is provided with an intake 17 a which is arranged substantially coaxially to the fume collection chamber 13 .
- the condensing device 18 comprises at least one fume cooling element 19 which is substantially annular and is arranged substantially coaxially to the fume collection chamber 13 in order to be skimmed radially, on its outer surface, by a flow of fumes that arrive from the heat exchange tubes 12 and are directed toward the intake 17 a of the stack 17 .
- the (or each) cooling element 19 is substantially a self-contained closed loop and, more precisely, substantially toroidal or “doughnut” shaped with its axis arranged substantially coaxially to the axis of the fume collection chamber 13 .
- the condensing device 18 has a plurality of cooling elements 19 which are arranged so as to face each other and are substantially mutually coaxial, so as to define, between the cooling elements 19 , a plurality of regions 20 for channeling the fumes each one of which is intended to be crossed radially by a flow of the fumes that is directed from the outer perimetric edge 19 a of the cooling elements 19 toward the axis of the fume collection chamber 13 .
- each cooling element 19 defined inside each cooling element 19 is a flow cavity 21 for a heat exchange fluid, which makes it possible to exchange heat with the fumes that brush against the cooling elements 19 so as to recover at least some of the residual latent heat.
- each cooling element 19 has, conveniently in the lower part thereof, at least one intake port 22 a which is connected with its flow cavity 21 and is connected, by way of a bypass duct 23 , to the cold water return duct 5 and, in the upper part thereof, at least one outlet port 22 b , which is connected to the containment chamber 3 , in order to enable the water that has entered the flow cavity 21 of the cooling elements 19 and been heated by the combustion fumes arrived in the fume collection chamber 13 to reach, in turn, through the containment chamber 3 , the hot water delivery duct 6 .
- the outlet ends 12 a of the heat exchange tubes 12 are distributed around the axis of the fume collection chamber 13 along a circumference and the outer perimetric edge 19 a of the cooling elements 19 has a smaller diameter than the circumference along which the outlet ends 12 a of the heat exchange tubes 12 are distributed, so as to ensure the radial flow of the fumes from the heat exchange tubes 12 to the stack 17 through the channeling regions 20 defined between the cooling elements 19 .
- the cooling elements 19 define axially a channel 23 for merging the flows of the fumes that pass through the channeling regions 20 , which is facing the intake 17 a of the stack 17 and laterally delimited by the inner perimetric edges of the cooling elements 19 .
- each one of the cooling elements 19 is connected, with its intake port 22 a , to an intake manifold 25 , by way of a respective intake duct 25 a , and, with its outlet port 22 b , to an outlet manifold 26 , by way of a respective discharge duct 26 a.
- the intake manifold 25 is connected to the bypass duct 23 , while the outlet manifold 26 is connected to a connecting duct 27 which leads into the containment chamber 3 .
- the intake ducts 25 a and the discharge ducts 26 a pass through a wall of the fume collection chamber 13 , passing through adapted openings in which there are, advantageously, sealing gaskets 31 which prevent the egress of the fumes from such collection chamber.
- the fume collection chamber 13 there can be, between the set of cooling elements 19 and the walls arranged at the axial ends of the fume collection chamber 13 , two circular gaskets 32 which prevent the fumes from flowing directly toward the stack 17 without passing through the channeling regions 20 defined between pairs of cooling elements 19 .
- the cooling elements 19 have, in the axial direction, a substantially flattened shape structure.
- the cooling elements 19 have, conveniently, a narrowed portion 19 c proximate to their outer perimetric edge 19 a and an enlarged portion 19 d proximate to the corresponding inner perimetric edge 19 b , so as to create a variation in the passage cross-section of the channeling regions 20 that produces a variation in speed of the radial flows of fumes that pass through them, with an increase in the turbulence and, therefore, in the heat exchange coefficient of the fumes.
- cooling elements 19 can be, advantageously, made from a respective pair of annular and mutually facing plates 28 .
- Each one of the plates 28 has, at points that are mutually diametrically opposite, tabs 29 a and 29 b , which protrude from the outer perimetric edge.
- the respective plates 28 are first mutually welded at their inner and outer perimetric edges, at the edges of their tabs 29 a and 29 b and in localized points 30 of their surface and, subsequently, they are deformed by inflation by way of a pressurized gas that is blown into the space present between the plates 28 through the intake ports 22 a and/or the outlet ports 22 b , which were previously provided.
- the cold water originating from the return duct 5 enters the containment chamber 3 through the inlet 3 a.
- the burner 8 generates a flame that extends inside the tubular element 10 , producing combustion fumes that flow through the combustion chamber until they reach the deflection wall 17 b , which redirects them and channels them along the annular interspace 11 , so that they can begin to exchange heat with the water present in the containment chamber 3 .
- the fume redirection chamber 14 which directs them into the heat exchange tubes 12 .
- combustion fumes flow over the heat exchange tubes 12 , they transfer not only sensible heat but also some of the latent heat to the water contained in the containment chamber 3 .
- the water thus heated exits the containment chamber 3 from the outlet 3 b and enters the delivery duct 6 .
- the flow cavity 21 defined inside the cooling elements 19 receives, through the corresponding intake duct 25 a connected to its intake port 22 a , cold water originating from the return duct 5 , by way of the bypass duct 23 and the intake manifold 25 .
- the combustion fumes that exit from the heat exchange tubes 12 are channeled into the channeling regions 20 defined between the cooling elements 19 .
- the combustion fumes transfer any residual latent heat to the water that is flowing inside the flow cavity 21 of the cooling elements 19 .
- the fumes After flowing through the channeling regions 20 , the fumes enter the merging channel 23 , through which they reach the intake 17 a of the stack 17 , so that they can be evacuated into the atmosphere.
- the water that flows through the flow cavity 21 of the cooling elements 19 and which is heated by the residual latent heat transferred from the combustion fumes exits from the cooling elements 19 through the relative outlet ports 22 b and reaches, by way of the discharge ducts 26 a , the outlet manifold 26 , from which it is sent, by way of connecting duct 27 , into the containment chamber 3 , so as to be reunited with the water fed by the return duct 5 .
- the invention is capable of fully achieving the set aim in that the peculiar condensing device according to the invention with which the boiler is provided enables a high recovery of the latent heat of the fumes with perceptible increase in the yield of the boiler.
Abstract
A condensing boiler, which comprises an outer enclosure, which defines a chamber for containing water to be heated and accommodates a combustion chamber which is connected to a plurality of heat exchange tubes which lead into a fume collection chamber which is connected to a fume evacuation stack; a condensing device for the fumes is arranged in the fume collection chamber; the stack has an intake which is arranged substantially coaxially to the fume collection chamber and the condensing device comprises at least one fume cooling element which has a substantially annular shape and is arranged substantially coaxially to the fume collection chamber.
Description
- The present invention relates to a condensing boiler.
- Nowadays in household heating systems and systems for producing household hot water, “condensing” boilers are widespread. In these boilers the fumes produced by combustion are cooled until at least a part of the water vapor contained therein condenses, with consequent transfer to the water from the fumes not only of sensible heat but also of latent heat of condensation.
- Typically, condensing boilers have an outer enclosure that defines a chamber containing the water to be heated and which accommodates internally a burner constituted by a combustion chamber associated with a burner and connected to a plurality of fume tubes, which exchange heat with the water to be heated, in order to allow the transmission of sensible heat and latent heat from the fumes to the water, and which lead into a fume collection chamber connected to a stack.
- In order to seek to obtain higher yields, within the fume collection chamber there can be a condensing device, usually constituted by a coil, inside which water passes through and outside which the fumes flow over, the function of which is to also recover the latent heat from any residual water vapor in the fumes exiting from the fume tubes.
- Although conventional condensing devices make a positive contribution to increasing the level di efficiency of condensing boilers, they have not, however, been found to be fully satisfactory in exchanging heat between water and fumes.
- In particular, current condensing devices have a high space occupation but a relatively small heat exchange surface.
- The aim of the present invention is to provide a condensing boiler that is capable of reaching high yield levels by way of recovering most of the latent heat available in the combustion fumes.
- Within this aim another object of the present invention is to provide a condensing boiler that has a condensing device which for the same space occupation with respect to conventional condensing devices has a greater heat exchange surface.
- Another object of the present invention is to provide a condensing boiler that is simple to provide in terms of construction, so that it can be competitive from a merely economic viewpoint as well.
- This aim and these and other objects which will become better apparent hereinafter are achieved by a condensing boiler, according to the invention, as defined in appended claim 1.
- Further characteristics and advantages of the invention will become better apparent from the description of a preferred, but not exclusive, embodiment of the condensing boiler, according to the invention, which is illustrated by way of non-limiting example in the accompanying drawings wherein:
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FIG. 1 is a longitudinal cross-sectional view of a condensing boiler according to the invention; -
FIG. 2 is a schematic front elevation view of a condensing device present in the boiler according to the invention; -
FIG. 3 is an enlarged longitudinal cross-sectional view of a portion of the boiler according to the invention. - With reference to the figures, a condensing boiler, according to the invention, generally indicated with the reference numeral 1, comprises an
outer enclosure 2, for example substantially cylindrical, inside which is defined achamber 3 for containing the water to be heated. - In particular, the
containment chamber 3 is provided with aninlet 3 a, which can be connected to a duct 5 for the return of cold water, originating for example from a heating system or from the water mains, and anoutlet 3 b, which can be connected to aduct 6 for the delivery of hot water, which arrives, for example, in the heating system or in the household water system. - Also accommodated inside the
outer enclosure 2 is acombustion chamber 7, which is associated with aburner 8. - The
combustion chamber 7 is, for example, delimited laterally by acylindrical wall 9, which separates it from thechamber 3 containing the water to be heated, and is, conveniently, positioned substantially coaxially to theouter enclosure 2. - The
burner 8 is, conveniently, arranged at onelongitudinal end 7 a of thecombustion chamber 7, which, at its opposite end, is closed by adeflection wall 7 b which deflects the fumes produced by the flame generated by theburner 8, so as to make them turn toward theend 7 a of the combustion chamber where theburner 8 is located. - Inside the
combustion chamber 7 there can conveniently be atubular element 10, positioned substantially coaxial to theburner 8, which laterally confines the flame produced by theburner 8 and defines, with thecylindrical wall 9, anannular interspace 11, into which the fumes redirected by thedeflection wall 7 b are channeled and directed toward theend 7 a of thecombustion chamber 7. - The
tubular element 10 can, advantageously, have a corrugated shape structure in order to increase the turbulence of the fumes. - The
combustion chamber 7 is connected to a plurality ofheat exchange tubes 12, which pass through thecontainment chamber 3 and lead, with anoutlet end 12 a thereof, into afume collection chamber 13, which is, conveniently, arranged, with respect to thechamber 3 for containing the water to be heated, at the opposite end to theburner 8. While the fumes flow over theheat exchange tubes 12 they transfer sensible heat and part of the latent heat to the water present in thecontainment chamber 3. - As illustrated, at its
end 7 a, thecombustion chamber 7 has, for example, one ormore ports 13 which are connected with afume redirection chamber 14, which channels the fumes into theheat exchange tubes 12 and is defined, substantially, between adelimiting end wall 15 of thechamber 3 containing the water to be heated and adoor 16, which is passed through, axially, by theburner 8 and can be opened in order to allow inspection of the combustion chamber. - Conveniently, the
collection chamber 13 for the fumes originating from theheat exchange tubes 12 is substantially cylindrical and is connected to astack 17 for evacuating the fumes to outside the boiler. - In particular, arranged inside the
fume collection chamber 13 is acondensing device 18 for the fumes arriving in thefume collection chamber 13, which makes it possible to recover any residual latent heat in the fumes before they exit into the atmosphere through thestack 17. - According to the invention, the
stack 17 is provided with anintake 17 a which is arranged substantially coaxially to thefume collection chamber 13. - Also according to the invention, the
condensing device 18 comprises at least onefume cooling element 19 which is substantially annular and is arranged substantially coaxially to thefume collection chamber 13 in order to be skimmed radially, on its outer surface, by a flow of fumes that arrive from theheat exchange tubes 12 and are directed toward theintake 17 a of thestack 17. - More specifically, as illustrated, the (or each)
cooling element 19 is substantially a self-contained closed loop and, more precisely, substantially toroidal or “doughnut” shaped with its axis arranged substantially coaxially to the axis of thefume collection chamber 13. - Preferably, the
condensing device 18 has a plurality ofcooling elements 19 which are arranged so as to face each other and are substantially mutually coaxial, so as to define, between thecooling elements 19, a plurality ofregions 20 for channeling the fumes each one of which is intended to be crossed radially by a flow of the fumes that is directed from the outerperimetric edge 19 a of thecooling elements 19 toward the axis of thefume collection chamber 13. - In more detail, defined inside each
cooling element 19 is aflow cavity 21 for a heat exchange fluid, which makes it possible to exchange heat with the fumes that brush against thecooling elements 19 so as to recover at least some of the residual latent heat. - In particular, each
cooling element 19 has, conveniently in the lower part thereof, at least oneintake port 22 a which is connected with itsflow cavity 21 and is connected, by way of abypass duct 23, to the cold water return duct 5 and, in the upper part thereof, at least oneoutlet port 22 b, which is connected to thecontainment chamber 3, in order to enable the water that has entered theflow cavity 21 of thecooling elements 19 and been heated by the combustion fumes arrived in thefume collection chamber 13 to reach, in turn, through thecontainment chamber 3, the hotwater delivery duct 6. - Advantageously, the outlet ends 12 a of the
heat exchange tubes 12 are distributed around the axis of thefume collection chamber 13 along a circumference and the outerperimetric edge 19 a of thecooling elements 19 has a smaller diameter than the circumference along which the outlet ends 12 a of theheat exchange tubes 12 are distributed, so as to ensure the radial flow of the fumes from theheat exchange tubes 12 to thestack 17 through the channelingregions 20 defined between thecooling elements 19. - Conveniently, the
cooling elements 19 define axially achannel 23 for merging the flows of the fumes that pass through the channelingregions 20, which is facing theintake 17 a of thestack 17 and laterally delimited by the inner perimetric edges of thecooling elements 19. - As illustrated, each one of the
cooling elements 19 is connected, with itsintake port 22 a, to anintake manifold 25, by way of arespective intake duct 25 a, and, with itsoutlet port 22 b, to anoutlet manifold 26, by way of arespective discharge duct 26 a. - In particular, the
intake manifold 25 is connected to thebypass duct 23, while theoutlet manifold 26 is connected to a connectingduct 27 which leads into thecontainment chamber 3. - Conveniently, the
intake ducts 25 a and thedischarge ducts 26 a pass through a wall of thefume collection chamber 13, passing through adapted openings in which there are, advantageously, sealinggaskets 31 which prevent the egress of the fumes from such collection chamber. - Conveniently, inside the
fume collection chamber 13 there can be, between the set ofcooling elements 19 and the walls arranged at the axial ends of thefume collection chamber 13, twocircular gaskets 32 which prevent the fumes from flowing directly toward thestack 17 without passing through the channelingregions 20 defined between pairs ofcooling elements 19. - Advantageously, the
cooling elements 19 have, in the axial direction, a substantially flattened shape structure. - More specifically, the
cooling elements 19 have, conveniently, a narrowedportion 19 c proximate to their outerperimetric edge 19 a and an enlargedportion 19 d proximate to the corresponding innerperimetric edge 19 b, so as to create a variation in the passage cross-section of thechanneling regions 20 that produces a variation in speed of the radial flows of fumes that pass through them, with an increase in the turbulence and, therefore, in the heat exchange coefficient of the fumes. - For completeness, it should be noted that the
cooling elements 19 can be, advantageously, made from a respective pair of annular and mutually facingplates 28. - Each one of the
plates 28 has, at points that are mutually diametrically opposite,tabs - In the
tabs cooling element 19, theintake port 22 a and theoutlet port 22 b of thecooling elements 19 are respectively provided. - In order to provide each
cooling element 19, therespective plates 28 are first mutually welded at their inner and outer perimetric edges, at the edges of theirtabs points 30 of their surface and, subsequently, they are deformed by inflation by way of a pressurized gas that is blown into the space present between theplates 28 through theintake ports 22 a and/or theoutlet ports 22 b, which were previously provided. - Operation of the condensing boiler according to the invention is the following.
- The cold water originating from the return duct 5 enters the
containment chamber 3 through theinlet 3 a. - The
burner 8 generates a flame that extends inside thetubular element 10, producing combustion fumes that flow through the combustion chamber until they reach the deflection wall 17 b, which redirects them and channels them along theannular interspace 11, so that they can begin to exchange heat with the water present in thecontainment chamber 3. - Once the fumes have flowed through the
annular interspace 11 they enter, through theconnection ports 13, thefume redirection chamber 14 which directs them into theheat exchange tubes 12. - While the combustion fumes flow over the
heat exchange tubes 12, they transfer not only sensible heat but also some of the latent heat to the water contained in thecontainment chamber 3. - The water thus heated exits the
containment chamber 3 from theoutlet 3 b and enters thedelivery duct 6. - When the combustion fumes reach the end of
outlet 12 a of theheat exchange tubes 12, they enter thefume collection chamber 13 and encounter thecooling elements 19. - The
flow cavity 21 defined inside thecooling elements 19 receives, through thecorresponding intake duct 25 a connected to itsintake port 22 a, cold water originating from the return duct 5, by way of thebypass duct 23 and theintake manifold 25. - In order to reach the
stack 17, the combustion fumes that exit from theheat exchange tubes 12 are channeled into the channelingregions 20 defined between thecooling elements 19. - By radially flowing through the channeling
regions 20 from the outerperimetric edge 19 a of thecooling elements 19 toward the axis of thefume collection chamber 13, the combustion fumes transfer any residual latent heat to the water that is flowing inside theflow cavity 21 of thecooling elements 19. - After flowing through the channeling
regions 20, the fumes enter themerging channel 23, through which they reach theintake 17 a of thestack 17, so that they can be evacuated into the atmosphere. - The water that flows through the
flow cavity 21 of thecooling elements 19 and which is heated by the residual latent heat transferred from the combustion fumes exits from thecooling elements 19 through therelative outlet ports 22 b and reaches, by way of thedischarge ducts 26 a, theoutlet manifold 26, from which it is sent, by way of connectingduct 27, into thecontainment chamber 3, so as to be reunited with the water fed by the return duct 5. - In practice it has been found that the invention is capable of fully achieving the set aim in that the peculiar condensing device according to the invention with which the boiler is provided enables a high recovery of the latent heat of the fumes with perceptible increase in the yield of the boiler.
- All the characteristics of the invention, indicated above as advantageous, convenient or similar, may also be missing or be substituted by equivalent characteristics.
- The individual characteristics set out in reference to general teachings or to specific embodiments may all be present in other embodiments or may substitute characteristics in such embodiments.
- The invention, thus conceived, is susceptible of numerous modifications and variations, all of which are within the scope of the appended claims.
- In practice the materials employed, provided they are compatible with the specific use, and the dimensions and shapes, may be any according to requirements.
- Moreover, all the details may be substituted by other, technically equivalent elements.
- The disclosures in Italian Patent Application No. VR2015A000081 (102015902350753) from which this application claims priority are incorporated herein by reference.
Claims (10)
1. A condensing boiler comprising an outer enclosure defining internally a chamber for containing water to be heated, which is provided with an inlet which can be connected to a duct for the return of cold water and with an outlet which can be connected to a duct for the delivery of hot water, and accommodating internally a combustion chamber, which is associated with a burner and is connected to a plurality of heat exchange tubes which pass through said containment chamber and lead, with an outlet end thereof, into a fume collection chamber, which is substantially cylindrical and is connected to a fume evacuation stack, inside said fume collection chamber there being a condensing device for the fumes that arrive in said fume collection chamber, wherein said stack has an intake which is arranged substantially coaxially to said fume collection chamber and in that said condensing device comprises at least one fume cooling element which has a substantially annular shape and is arranged substantially coaxially to said fume collection chamber in order to be skimmed radially on its outer surface by a flow of the fumes that arrive from said heat exchange tubes and are directed toward the intake of said stack.
2. The boiler according to claim 1 , wherein said at least one cooling element is provided internally with a flow cavity for a heat exchange fluid.
3. The boiler according to claim 1 , wherein said at least one cooling element has at least one intake port which is connected, by way of a bypass duct, to said cold water return duct, and at least one outlet port which is connected to said containment chamber.
4. The boiler according to claim 1 , wherein the outlet ends of said heat exchange tubes are distributed around an axis of said fume collection chamber along a circumference, said at least one cooling element having an outer perimetric edge which has a smaller diameter than said circumference.
5. The boiler according to claim 4 , wherein said condensing device has a plurality of cooling elements which are arranged so as to face each other and are substantially mutually coaxial, so as to define, between said cooling elements, a plurality of regions for channeling the fumes each one of which is intended to be crossed radially by a flow of the fumes that is directed from the outer perimetric edge of said cooling elements toward the axis of said fume collection chamber.
6. The boiler according to claim 5 , wherein said cooling elements define axially a channel for merging flows of the fumes that pass through said channeling regions.
7. The boiler according to claim 3 , wherein each one of said cooling elements is connected, with its intake port, to an intake manifold by way of a respective intake duct, and by way of its outlet port to an outlet manifold, by way of a respective discharge duct, said intake manifold being connected to said bypass duct and said outlet manifold by way of a connecting duct which leads into said containment chamber.
8. The boiler according to claim 4 , wherein said cooling elements have a narrowed portion proximate to their outer perimetric edge and an enlarged portion proximate to a corresponding inner perimetric edge.
9. The boiler according to claim 1 , wherein said fume collection chamber is arranged, with respect to said containment chamber, on an opposite side with respect to said burner.
10. The boiler according to claim 5 , further comprising circular gaskets which act between said cooling elements and walls arranged at axial ends of said fume collection chamber, in order to prevent the fumes from flowing directly toward the stack without passing through said channeling regions.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITVR20150081 | 2015-05-12 | ||
ITVR2015A000081 | 2015-05-12 |
Publications (1)
Publication Number | Publication Date |
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US20160334137A1 true US20160334137A1 (en) | 2016-11-17 |
Family
ID=53794455
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/152,917 Abandoned US20160334137A1 (en) | 2015-05-12 | 2016-05-12 | Condensing boiler |
Country Status (2)
Country | Link |
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US (1) | US20160334137A1 (en) |
EP (1) | EP3093579A1 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140224191A1 (en) * | 2013-02-12 | 2014-08-14 | Lester James Thiessen | Burner Tube Heat Exchanger for a Storage Tank |
US20140245972A1 (en) * | 2013-02-12 | 2014-09-04 | Lester James Thiessen | Heat Exchanger for an Oil Storage Tank |
US20180031276A1 (en) * | 2016-07-28 | 2018-02-01 | Brendan Kemp Boiler Design Limited | Condensing boiler |
CN109084478A (en) * | 2018-09-27 | 2018-12-25 | 山西崇光科技有限公司 | It is a kind of for solving the flue gas check device of condensing boiler smoke backflow |
US20190093922A1 (en) * | 2017-09-25 | 2019-03-28 | I.C.I. Caldaie S.P.A. | Boiler |
US20190323706A1 (en) * | 2016-06-07 | 2019-10-24 | Cleaver-Brooks, Inc. | Burner with Adjustable End Cap and Method of Operating Same |
Families Citing this family (3)
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CN107421110A (en) * | 2017-08-18 | 2017-12-01 | 德清县德沃工业设备安装有限公司 | A kind of gas fired-boiler |
CN111023569A (en) * | 2019-11-07 | 2020-04-17 | 赵素真 | Circulating condensation boiler |
CN114392578A (en) * | 2022-02-14 | 2022-04-26 | 马传钊 | Boiler condensate water recovery equipment |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3838975A (en) * | 1973-05-18 | 1974-10-01 | Universal Oil Prod Co | Thermal incinerator with heat recuperation |
US5611299A (en) * | 1992-03-10 | 1997-03-18 | Varga; Zeljko | Boiler with reduced NOX emission |
US20090056647A1 (en) * | 2006-01-11 | 2009-03-05 | Viessmann Werke Gmbh & Co., Kg | Boiler |
US20110185985A1 (en) * | 2010-02-03 | 2011-08-04 | Farshid Ahmady | Fluid heating apparatus |
US20130125838A1 (en) * | 2010-08-12 | 2013-05-23 | Kyungdong Navien Co., Ltd. | Latent heat exchanger in condensing boiler |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3413968A1 (en) * | 1984-03-31 | 1985-10-10 | Didier-Werke Ag, 6200 Wiesbaden | Device for combustion support for an oil burner or gas burner |
FR2565334A1 (en) * | 1984-06-01 | 1985-12-06 | Deleage Sa | Condensation boiler using a dry process |
-
2016
- 2016-05-10 EP EP16168903.9A patent/EP3093579A1/en not_active Withdrawn
- 2016-05-12 US US15/152,917 patent/US20160334137A1/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3838975A (en) * | 1973-05-18 | 1974-10-01 | Universal Oil Prod Co | Thermal incinerator with heat recuperation |
US5611299A (en) * | 1992-03-10 | 1997-03-18 | Varga; Zeljko | Boiler with reduced NOX emission |
US20090056647A1 (en) * | 2006-01-11 | 2009-03-05 | Viessmann Werke Gmbh & Co., Kg | Boiler |
US20110185985A1 (en) * | 2010-02-03 | 2011-08-04 | Farshid Ahmady | Fluid heating apparatus |
US20130125838A1 (en) * | 2010-08-12 | 2013-05-23 | Kyungdong Navien Co., Ltd. | Latent heat exchanger in condensing boiler |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140224191A1 (en) * | 2013-02-12 | 2014-08-14 | Lester James Thiessen | Burner Tube Heat Exchanger for a Storage Tank |
US20140245972A1 (en) * | 2013-02-12 | 2014-09-04 | Lester James Thiessen | Heat Exchanger for an Oil Storage Tank |
US10773880B2 (en) * | 2013-02-12 | 2020-09-15 | Viro Rentals, Inc. | Burner tube heat exchanger for a storage tank |
US20190323706A1 (en) * | 2016-06-07 | 2019-10-24 | Cleaver-Brooks, Inc. | Burner with Adjustable End Cap and Method of Operating Same |
US11933491B2 (en) * | 2016-06-07 | 2024-03-19 | The Cleaver-Brooks Company, LLC | Burner with adjustable end cap and method of operating same |
US20180031276A1 (en) * | 2016-07-28 | 2018-02-01 | Brendan Kemp Boiler Design Limited | Condensing boiler |
US10760820B2 (en) * | 2016-07-28 | 2020-09-01 | Bkbd Limited | Condensing boiler |
US20190093922A1 (en) * | 2017-09-25 | 2019-03-28 | I.C.I. Caldaie S.P.A. | Boiler |
CN109084478A (en) * | 2018-09-27 | 2018-12-25 | 山西崇光科技有限公司 | It is a kind of for solving the flue gas check device of condensing boiler smoke backflow |
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