US20170356691A1 - Swimming Pool Heat Exchangers And Associated Systems And Methods - Google Patents
Swimming Pool Heat Exchangers And Associated Systems And Methods Download PDFInfo
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- US20170356691A1 US20170356691A1 US15/617,760 US201715617760A US2017356691A1 US 20170356691 A1 US20170356691 A1 US 20170356691A1 US 201715617760 A US201715617760 A US 201715617760A US 2017356691 A1 US2017356691 A1 US 2017356691A1
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- tube assemblies
- heat exchanger
- tube
- swimming pool
- assemblies
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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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
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- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04H—BUILDINGS OR LIKE STRUCTURES FOR PARTICULAR PURPOSES; SWIMMING OR SPLASH BATHS OR POOLS; MASTS; FENCING; TENTS OR CANOPIES, IN GENERAL
- E04H4/00—Swimming or splash baths or pools
- E04H4/12—Devices or arrangements for circulating water, i.e. devices for removal of polluted water, cleaning baths or for water treatment
- E04H4/129—Systems for heating the water content of swimming pools
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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
- F24H1/0072—Special adaptations
-
- 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
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
- F28D1/05316—Assemblies of conduits connected to common headers, e.g. core type radiators
- F28D1/05333—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits
-
- 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
- F28F1/20—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 attachable to the 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
- F28F1/12—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
- F28F1/24—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 transversely
- F28F1/30—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 transversely the means being attachable to the element
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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
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
- F28F21/081—Heat exchange elements made from metals or metal alloys
- F28F21/085—Heat exchange elements made from metals or metal alloys from copper or copper alloys
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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
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
- F28F21/081—Heat exchange elements made from metals or metal alloys
- F28F21/086—Heat exchange elements made from metals or metal alloys from titanium or titanium alloys
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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
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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
- F28D7/06—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 having a single U-bend
-
- 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
- F28D7/16—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 in parallel spaced relation
- F28D7/1615—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 in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium
-
- 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
- F28D7/16—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 in parallel spaced relation
- F28D7/163—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 in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
-
- 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
- F28D7/16—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 in parallel spaced relation
- F28D7/1684—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 in parallel spaced relation the conduits having a non-circular cross-section
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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
- F28F1/02—Tubular elements of cross-section which is non-circular
- F28F1/04—Tubular elements of cross-section which is non-circular polygonal, e.g. rectangular
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2210/00—Heat exchange conduits
- F28F2210/08—Assemblies of conduits having different features
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2255/00—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes
- F28F2255/16—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes extruded
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2275/00—Fastening; Joining
- F28F2275/06—Fastening; Joining by welding
- F28F2275/067—Fastening; Joining by welding by laser welding
Definitions
- the present disclosure relates to swimming pool heat exchangers and associated systems and methods and, in particular, to heat exchangers including a plurality of titanium tubes with welded copper fins for improved heat transfer in swimming pool heater applications.
- heaters have been used over the years for heating fluids in applications such as residential heating systems and swimming pools. Although discussed herein with respect to water tube heat exchangers, fire tube heat exchangers have also been used in the industry. Most heaters include a heat exchanger disposed proximate a source of heat through which the fluid to be heated passes.
- the heat exchanger generally includes a metal conduit through which the fluid to be heated can pass and is positioned above a burning gas to absorb the heat of combustion and conduct it to the fluid passing through the conduit.
- the heat exchanger can be configured to maximize the exterior surface area exposed to the heat of combustion by using metal fins on the conduit.
- Gas-fired appliances with an air-to-liquid heat exchanger generally have a higher heat capacity than liquid-to-liquid heat exchangers.
- achieving adequate heat transfer using titanium tubes in the air-to-liquid heat exchanger of a gas-fired appliance has proven elusive in the swimming pool heater industry.
- One hurdle to attaining adequate heat transfer is the inability to extrude titanium into a tube with a substantial number of integrated fins.
- fins for a titanium tube cannot be extruded to the desired size for proper heat transfer.
- Some swimming pool heat exchangers include extruded fin tubes manufactured from either copper or cupro-nickel and have fin heights that cannot be manufactured out of titanium.
- Some manufacturers have welded stainless steel fins to stainless steel tubing. Some industries, such as boiler and fluid processing, have used fins of a dissimilar material than the tube welded to the titanium tubes. Some swimming pool heat exchangers include plate fin designs with tubes mechanically expanded into collars on the plates to bond the fins and tubes. However, such methods are unfeasible for use with titanium.
- swimming pool heat exchangers that include titanium tubes with welded copper fins that provide the desired amount of heat transfer and corrosion resistance in air-to-liquid applications.
- exemplary swimming pool heat exchangers include a housing and one or more tube assemblies disposed within the housing.
- Each of the tube assemblies includes an elongated titanium tube and at least one fin welded (e.g., laser welded) to an outer surface of the elongated titanium tube.
- any type of welding can be used to attach the fins to the outer surface of the titanium tube.
- the tube assemblies can include a plurality of fins individually welded in a spaced manner along the outer surface of the elongated titanium tube.
- the tube assemblies can each include one fin fabricated as a single material and defining a helical shape such that the inner surface of the helical fin is continuously welded along the outer surface of the elongated titanium tube.
- the elongated titanium tube and the welded fin(s) allow for corrosion resistance to swimming pool water while simultaneously allowing for improved heat transfer from the heat exchanger to the swimming pool water.
- the at least one fin can be a copper fin.
- the at least one fin can define a circular configuration.
- the elongated titanium tube can define a cylindrical configuration with an inner passage extending therethrough.
- the heat exchanger can include at least one tube sheet secured to ends of the one or more tube assemblies.
- the heat exchanger can include a column of the tube assemblies aligned along a central axis. In some embodiments, the heat exchanger can include a plurality of the tube assemblies staggered relative to each other. In some embodiments, the one or more tube assemblies can be of the same outer diameter. In some embodiments, the one or more tube assemblies can be of different outer diameters.
- the one or more tube assemblies can be arranged in, e.g., a U-shaped or cylindrical configuration, a flat configuration defining a single column of tube assemblies, a bent spiral configuration, a cylindrical configuration including a passage extending between the tube assemblies, an A-shaped configuration, a V-shaped configuration, a solid block configuration including multiple rows and columns of tube assemblies disposed adjacent to each other, combinations thereof, or the like.
- an exemplary method of heating swimming pool water includes introducing heated gas (or an alternative source) into one of the exemplary heat exchangers disclosed herein.
- the heated gas can be introduced into an area surrounding the one or more tube assemblies.
- the method includes introducing or circulating swimming pool water to the one or more tube assemblies of the heat exchanger to allow for heat transfer between the heated gas and the swimming pool water.
- the method includes adjusting a configuration of the one or more tube assemblies within the housing to adjust a heat transfer rate to the swimming pool water.
- an exemplary heat exchanger system includes a heat exchanger as disclosed herein, a gas source, and a swimming pool water source.
- the gas source can be fluidly connected to the heat exchanger and configured to supply heated gas (or an alternative source) to an area surrounding the one or more tube assemblies.
- the swimming pool water source can be fluidly connected to the heat exchanger and configured to supply swimming pool water to the one or more tube assemblies.
- FIG. 1 is a diagrammatic side view of an exemplary tube assembly of an exemplary heat exchanger according to the present disclosure.
- FIG. 2 is a diagrammatic front view of an exemplary tube assembly of FIG. 1 .
- FIG. 3 is a perspective view of a plurality of exemplary tube assemblies of FIG. 1 .
- FIG. 4 is a front view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 .
- FIG. 5 is a front view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 .
- FIG. 6 is a front view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 .
- FIG. 7 is a front view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 .
- FIG. 8 is a front view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 .
- FIG. 9 is a front view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 .
- FIG. 10 is a front view of an exemplary heat exchanger including one column of a plurality of tube assemblies of FIG. 1 .
- FIG. 11 is a front view of an exemplary heat exchanger including two columns of a plurality of tube assemblies of FIG. 1 .
- FIG. 12 is a front view of an exemplary heat exchanger including three columns of a plurality of tube assemblies of FIG. 1 .
- FIG. 13 is a front view of an exemplary heat exchanger including two columns of a plurality of differently sized tube assemblies of FIG. 1 .
- FIG. 14 is a front view of an exemplary heat exchanger including one staggered column of a plurality of tube assemblies of FIG. 1 .
- FIG. 15 is a front view of an exemplary heat exchanger including two staggered columns of a plurality of tube assemblies of FIG. 1 .
- FIG. 16 is a front view of an exemplary heat exchanger including three staggered columns of a plurality of tube assemblies of FIG. 1 .
- FIG. 17 is a front view of an exemplary heat exchanger including two staggered columns and one aligned column of a plurality of differently sized tube assemblies of FIG. 1 .
- FIG. 18 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a horizontal cylindrical configuration.
- FIG. 19 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a horizontal flat configuration.
- FIG. 20 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a vertical flat configuration.
- FIG. 21 is a perspective view of an exemplary heat exchanger including a tube assemblies of FIG. 1 in a spiral configuration.
- FIG. 22 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a vertical cylindrical configuration.
- FIG. 23 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a flat A-shaped configuration.
- FIG. 24 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a flat slanted configuration.
- FIG. 25 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a solid block configuration.
- FIG. 26 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies of FIG. 1 in a flat slanted configuration.
- FIG. 27 is a block diagram of an exemplary heat exchanger system according to the present disclosure.
- exemplary heat exchangers including a plurality of tubes with welded fins (e.g., laser welded) are provided.
- the tubes can be smooth titanium tubes that include copper fins welded to the exterior surface to enhance heat transfer from hot combustion gases to swimming pool water flowing within the heat exchanger tubes of a gas-fired pool heater.
- the heat exchanger can include a single welded fin tube attached to a water circulating system suspended over a small source of heat.
- the exemplary heat exchangers achieve improved heat transfer by using titanium tubes with the welded copper fins in an air-to-liquid heat exchanger system with corrosion resistance (normally found in heat pump heat exchangers) and with a higher heat capacity of gas-fired appliances.
- the exemplary heat exchangers include titanium tubes in gas-fired swimming pool heaters to achieve corrosion resistance by isolating the swimming pool water within the titanium tubes, while maintaining the heat transfer characteristics of high-finned heat exchanger tubes.
- the fins are welded to the titanium tube to facilitate the higher heat transfer than normally achieved by the titanium tubes alone.
- the welded fins which provide a significant increase in surface area and are manufactured from a material with a higher thermal conductivity than titanium, thereby transferring the required amount of heat from a heat source, typically a burner, to swimming pool water inside of the titanium tube.
- the titanium tube in turn, is resistant to corrosion typically caused by exposure to swimming pool water.
- the exemplary heat exchangers can be used with any appliance that includes a heat exchanger configured to transfer heat from hot combustion gases to liquid where corrosion caused by the liquid is one of the primary concerns.
- the exemplary tubes and fins can be used in heaters for fluids, such as the heater for fluids disclosed in U.S. Pat. No. 6,026,804, incorporated herein by reference.
- the titanium tube can be expanded into the plate fins.
- such methods are generally performed with larger and more complicated processing machines.
- a plurality of titanium tubes can be arranged to form a heat exchanger and can be secured to one or more tube sheets to define the heat exchanger shape.
- the tube sheets provide a transition to the connected water system.
- different geometries, configurations or arrangements of the heat exchanger can be used, resulting in different tube arrangements within the geometry and different airflow paths through the tubes.
- varying sizes and/or numbers of the tubes can be used in flat horizontal or alternative configurations to differ airflow paths through the tubes.
- the material of the base tubing or the welded fins, or the geometry or arrangement of the fins relative to the tubes can be changed.
- Changing the fins e.g., the height, material, fin density on the tube, combinations thereof, or the like, can allow for heat transfer at different rates.
- the heat exchanger can be customized to adjust for the desired heat transfer rate.
- Changing the tube material can be used to accommodate for different types or sources of corrosion present in the heat exchanger system.
- each tube assembly 100 includes an elongated tube 102 , e.g., an extruded titanium tube defining a cylindrical configuration with an inner passage 103 extending therethrough configured to receive swimming pool water.
- the tube 102 can define a configuration other than cylindrical, e.g., square, rectangular, oval, or the like.
- the tube 102 can define an overall length 104 extending along a central longitudinal axis 106 .
- the tube 102 can define an outer diameter 108 with a wall thickness 110 . In some embodiments, the outer diameter 108 can be approximately 0.75 inches and the wall thickness 110 can be approximately 0.02 inches.
- the tube assembly 100 includes a plurality of fins 112 (e.g., copper fins) secured to an outer surface 116 of the tube 102 .
- the fins 112 can be welded (e.g., laser welded) to the outer surface 116 of the tube 102 .
- the entire circumferential inner diameter of the fins 112 can be laser welded to the outer surface 116 of the tube 102 .
- the fins 112 can define a substantially circular configuration with a diameter 114 .
- the diameter 114 of each fin 112 can be approximately, e.g., 40 mm, 50 mm, or the like.
- each fin 112 can define a thickness between approximately 0.015 inches to approximately 0.020 inches.
- the plurality of fins 112 can be fabricated as a single piece of material helically wound around the outer surface 116 of the tube 102 and welded along the entire contact surface of the inner surface of the fins 112 and the outer surface 116 of the tube 102 .
- the fins 112 can define different configurations, e.g., oval, rectangular, square, triangular, hexagonal, or the like.
- fins 112 having multiple different configurations can be secured to the outer surface 116 of the tube 102 .
- the fins 112 can define an asymmetrical configuration.
- the fins 112 can be spaced substantially uniformly relative to each other along the tube 102 . In some embodiments, the spacing between the fins 112 can be different. In some embodiments, the fins 112 can be welded to the tube 102 such that the fins 112 extend substantially perpendicularly relative to the longitudinal axis 106 . In some embodiments, the fins 112 can be welded to the tube 102 at non-perpendicular angles relative to the longitudinal axis 106 . The fins 112 can extend only along a partial length 118 of the overall length 104 of the tube 102 .
- proximal end 120 and the distal end 122 of the tube 102 can remain uncovered (e.g., without fins 112 ).
- a proximal length 124 and a distal length 126 of the tube 102 can remain uncovered or exposed.
- the proximal and distal lengths 124 , 126 can be substantially similar in dimension. In some embodiments, the proximal and distal lengths 124 , 126 can be different in dimension.
- FIG. 3 shows a plurality of tube assemblies 100 positioned adjacent to each other. As shown in FIG. 3 , the tube assemblies 100 can be aligned along the longitudinal axis 106 of each tube assembly 100 to form a substantially planar configuration of a heat exchanger. Alternative configurations or arrangements of the tube assemblies 100 will be discussed in greater detail below.
- FIGS. 4-9 show front views of exemplary heat exchangers 150 a - f with different configurations or arrangements of the tube assemblies 100 (referred to as primary tube assemblies 100 a and secondary tube assemblies 100 b ).
- the diameter of the tube assemblies 100 defines the diameter of the fins of each respective tube assembly 100 .
- the tube assemblies 100 a , 100 b can be arranged in a pattern relative to each other and secured on opposing sides (e.g., the proximal and distal ends 120 , 122 ) by endplates or tube sheets.
- FIGS. 4-9 show different sizes and arrangements of the tube assemblies 100 that can fit within the same structure 152 that defines a height 154 and a width 156 .
- the tube assemblies 100 can be used to fit within a structure 152 that defines the width 156 .
- the tube assemblies 100 of FIGS. 4-9 can include tube sheets disposed on each side of the tube assemblies 100 a , 100 b .
- the tube sheets can define a substantially rectangular configuration.
- the primary tube assemblies 100 a can be aligned along the horizontal central axis 130 .
- the primary tube assemblies 100 a can be spaced relative to each other to receive the secondary tube assemblies 100 b therebetween.
- the secondary tube assemblies 100 b can be disposed between the primary tube assemblies 100 a in a staggered or offset manner in a diagonal direction.
- the secondary tube assemblies 100 b are therefore aligned along their respective horizontal central axes, with the horizontal central axis of the secondary tube assemblies 100 b being offset from the horizontal central axis 130 of the primary tube assemblies 100 a .
- the heat exchanger 150 a can include six tube assemblies 100 a , 100 b .
- the fins of the tube assemblies 100 a , 100 b can be oriented substantially tangent relative to each other to avoid bypassed combustion gasses from escaping the heat exchanger.
- each of the tube assemblies 100 a , 100 b can be spaced relative to each other such that no tube assemblies 100 a , 100 b are positioned directly against each other.
- the fins of the tube assemblies 100 a , 100 b can be positioned adjacent to each other in an abutting relationship.
- the heat exchanger 150 b of FIG. 5 can be substantially similar in structure and function to the heat exchanger 150 a of FIG. 4 , except that seven tube assemblies 100 a , 100 b can be used.
- the outer diameter of the fins of the tube assemblies 100 a , 100 b can be dimensioned smaller than the tube assemblies 100 a , 100 b of FIG. 4 , allowing a greater number of tube assemblies 100 a , 100 b to fit within the same width 156 of the structure 152 .
- the heat exchanger 150 c of FIG. 6 can be substantially similar in structure and function to the heat exchanger of 150 a of FIG. 4 , except that ten tube assemblies 100 a , 100 b can be used.
- the outer diameter of the fins of the tube assemblies 100 a , 100 b can be dimensioned smaller than the tube assemblies 100 a , 100 b of FIGS. 4 and 5 , allowing a greater number of tube assemblies 100 a , 100 b to fit within the same width 156 of the structure 152 .
- the heat exchanger 150 d of FIG. 7 can be substantially similar in structure and function to the heat exchanger 150 a of FIG. 4 , except that sixteen tube assemblies 100 a , 100 b can be used.
- the outer diameter of the fins of the tube assemblies 100 a , 100 b can be dimensioned smaller than the tube assemblies 100 a , 100 b of FIGS. 4-6 , allowing a greater number of tube assemblies 100 a , 100 b to fit within the same width 156 of the structure 152 .
- the heat exchanger 150 e of FIG. 8 can be substantially similar in structure and function to the heat exchanger 150 a of FIG. 4 , except that fourteen tube assemblies 100 a , 100 b can be used.
- the outer diameter of the fins of the tube assemblies 100 a , 100 b can be dimensioned smaller than the tube assemblies 100 a , 100 b of FIGS. 4-6 , allowing a greater number of tube assemblies 100 a , 100 b to fit within the same width 156 of the structure 152 .
- the heat exchanger 150 f of FIG. 9 can be substantially similar in structure and function to the heat exchanger 150 a of FIG. 4 , except that twelve tube assemblies 100 a , 100 b can be used.
- the outer diameter of the fins of the tube assemblies 100 a , 100 b can be dimensioned smaller than the tube assemblies 100 a , 100 b of FIGS. 4-6 , allowing a greater number of tube assemblies 100 a , 100 b to fit within the same width 156 of the structure 152 .
- FIGS. 10-17 are front views of exemplary heat exchangers 200 a - h including a plurality of tube assemblies 100 arranged in different configurations.
- Each configuration provides a variation in heat transfer flow rates from the combustion gas to the swimming pool water.
- the different configurations result in varied heat transfer either by affecting the surface area in contact with the combustion gases (e.g., the number of rows and diameter of the tube assemblies 100 ) or by affecting the airflow pattern and distance the combustion gases stay in contact with the heat exchanger (e.g., staggered rows and diameter of the tube assemblies 100 ).
- FIG. 10 shows a heat exchanger 200 a that includes a single column 204 of tube assemblies 100 of the same size (e.g., four tube assemblies).
- the tube assemblies 100 can be arranged to align along a vertical central axis 202 .
- Air flow can enter the heat exchanger 200 a from, e.g., a first direction 206 substantially perpendicular to the vertical central axis 202 , a second direction 208 substantially aligned with the vertical central axis 202 , combinations thereof, or the like.
- FIG. 11 shows a heat exchanger 200 b that includes two columns 204 a , 204 b of tube assemblies 100 of the same size (e.g., each column including four tube assemblies).
- the tube assemblies 100 can be arranged such that four tube assemblies 100 are aligned along a first vertical central axis 202 a and four tube assemblies 100 are aligned along a second vertical central axis 202 b , the first and second vertical central axes 202 a , 202 b being spaced from each other.
- the two columns 204 a , 204 b of the tube assemblies 100 can be disposed adjacent to each other. Further, the adjacently positioned tube assemblies 100 can be aligned along horizontal central axes 210 a - d .
- Air flow can enter the heat exchanger 200 b from, e.g., a first direction 206 substantially perpendicular to the first and second vertical central axes 202 a , 202 b , a second direction 208 substantially aligned with the first and second vertical central axes 202 a , 202 b , combinations thereof, or the like.
- FIG. 12 shows a heat exchanger 200 c that includes three columns 204 a - c of tube assemblies 100 of the same size (e.g., each column including four tube assemblies).
- the tube assemblies 100 can be arranged such that four tube assemblies 100 are aligned along a first vertical central axis 202 a , four tube assemblies 100 are aligned along a second vertical central axis 202 b , and four tube assemblies 100 are aligned along a third vertical central axis 202 c , the vertical central axes 202 a , 202 b , 202 c being spaced from each other.
- the three columns 204 a - c of the tube assemblies 100 can be disposed adjacent to each other.
- Air flow can enter the heat exchanger 200 c from, e.g., a first direction 206 substantially perpendicular to the vertical central axes 202 a - c , a second direction 208 substantially aligned with the vertical central axes 202 a - c , combinations thereof, or the like.
- FIG. 13 shows a heat exchanger 200 d that includes two columns 204 a , 204 b of tube assemblies 100 a , 100 b of different sizes.
- the tube assemblies 100 a of the same size can be arranged such that four tube assemblies 100 a are aligned along a first vertical central axis 202 a , and two tube assemblies 100 b of a size different from the tube assemblies 100 a are aligned along a second vertical central axis 202 b .
- the first and second vertical central axes 202 a , 202 b are spaced from each other.
- the each tube assembly 100 b can be approximately double in diameter as compared to each tube assembly 100 a .
- the two columns 204 a , 204 b of the tube assemblies 100 a , 100 b can be disposed adjacent to each other.
- a horizontal central axis 212 a of one of the tube assemblies 100 b can be aligned between the horizontal central axes 210 a , 210 b of the tube assemblies 100 a .
- a horizontal central axis 212 b of the other tube assembly 100 b can be aligned between the horizontal central axes 210 c , 210 d of the tube assemblies 100 a .
- Air flow can enter the heat exchanger 200 d from, e.g., a first direction 206 substantially perpendicular to the vertical central axes 202 a , 202 b , a second direction 208 substantially aligned with the vertical central axes 202 a , 202 b , a third direction 214 substantially perpendicular to the vertical central axes 202 a , 202 b and opposing the first direction 206 , combinations thereof, or the like.
- FIG. 14 shows a heat exchanger 200 e that includes one staggered column 204 of tube assemblies 100 of the same size (e.g., the column including four tube assemblies).
- the tube assemblies 100 can be arranged such that every other tube assembly 100 is aligned along a first vertical central axis 202 a and a second vertical central axis 202 b , respectively.
- the first and second vertical central axes 202 a , 202 b are spaced from each other.
- Each of the adjacently positioned tube assemblies 100 can be staggered by an angle relative to horizontal central axes 210 a - d .
- the fins of the tube assemblies 100 can be disposed in a substantially tangent and abutting configuration.
- Air flow can enter the heat exchanger 200 e from, e.g., a first direction 206 substantially perpendicular to the vertical central axes 202 a , 202 b , a second direction 208 substantially aligned with the vertical central axes 202 a , 202 b , combinations thereof, or the like.
- FIG. 15 shows a heat exchanger 200 f that includes two staggered columns 204 a , 204 b of tube assemblies 100 of the same size (e.g., each column including four tube assemblies).
- the tube assemblies 100 can be arranged such that every other tube assembly 100 is aligned along a first to fourth vertical central axes 202 a - d , with two tube assemblies 100 aligned per vertical central axis 202 a - d .
- the vertical central axes 202 a - d are spaced from each other.
- Each of the adjacently positioned tube assemblies 100 can be staggered by an angle relative to horizontal central axes 210 a - d .
- the fins of the tube assemblies 100 can be disposed in a substantially tangent and abutting configuration.
- the fins of the tube assemblies 100 aligned along the horizontal central axes 210 a - d can abut each other.
- Air flow can enter the heat exchanger 200 f from, e.g., a first direction 206 substantially perpendicular to the vertical central axes 202 a - d , a second direction 208 substantially aligned with the vertical central axes 202 a - d , combinations thereof, or the like.
- FIG. 16 shows a heat exchanger 200 g that includes three staggered columns 204 a - c of tube assemblies 100 of the same size (e.g., each column including four tube assemblies).
- the tube assemblies 100 can be arranged such that every other tube assembly 100 is aligned along a first to sixth vertical central axes 202 a - f , with two tube assemblies 100 aligned per vertical central axis 202 a - f .
- the vertical central axes 202 a - f are spaced from each other.
- Each of the adjacently positioned tube assemblies 100 can be staggered by an angle relative to horizontal central axes 210 a - d .
- the fins of the tube assemblies 100 can be disposed in a substantially tangent and abutting configuration.
- the fins of the tube assemblies 100 aligned along the horizontal central axes 210 a - 3 can abut each other.
- Air flow can enter the heat exchanger 200 g from, e.g., a first direction 206 substantially perpendicular to the vertical central axes 202 a - f , a second direction 208 substantially aligned with the vertical central axes 202 a - f , combinations thereof, or the like.
- FIG. 17 shows a heat exchanger 200 h that includes one staggered column 204 a of tube assemblies 100 a of the same size (e.g., the column including four tube assemblies) and one column 204 b of tube assemblies 100 b sized differently than the tube assemblies 100 a .
- the tube assemblies 100 a can be arranged such that every other tube assembly 100 is aligned along a first vertical central axis 202 a and a second vertical central axis 202 b , respectively.
- the first and second vertical central axes 202 a , 202 b are spaced from each other.
- Each of the adjacently positioned tube assemblies 100 a can be staggered by an angle relative to horizontal central axes 210 a - f .
- the tube assemblies 100 b can be arranged such that the two tube assemblies 100 b are aligned along a third vertical central axis 202 c .
- the tube assemblies 100 b can be aligned with respective horizontal central axes 210 b , 210 e of two tube assemblies 100 a .
- the tube assemblies 100 b can be disposed along horizontal central axes that are parallel to (but not aligned with) the horizontal central axes 210 a - f ).
- the fins of the tube assemblies 100 a , 100 b can be disposed in a substantially tangent and abutting configuration.
- Air flow can enter the heat exchanger 200 h from, e.g., a first direction 206 substantially perpendicular to the vertical central axes 202 a - c , a second direction 208 substantially aligned with the vertical central axes 202 a - c , a third direction 214 substantially perpendicular to the vertical central axes 202 a - c and opposing the first direction 206 , combinations thereof, or the like.
- FIGS. 18-26 show perspective views of exemplary heat exchangers 250 a - i including tube assemblies 100 in different configurations.
- the tube assemblies 100 can have a substantially round cross-section (such as the tube assemblies of FIGS. 1-17 ).
- FIG. 18 shows a heat exchanger 250 a including a plurality of tube assemblies 100 stacked and aligned relative to each other, and bent into a substantially U-shaped, tear-shaped or horizontal cylindrical configuration.
- the tube assemblies 100 can extend in a direction substantially aligned with horizontal.
- the ends of the tube assemblies 100 can be disposed adjacent to each other and secured to a single tube sheet 252 .
- a passage 254 is formed between the tube assemblies 100 and extends the height of the heat exchanger 250 a . Air flow can enter into the passage 254 from above 256 and below 258. Air flow can enter/exit the heat exchanger 250 a in opposing directions 260 , 262 perpendicular to the tube assemblies 100 .
- FIG. 19 shows a heat exchanger 250 b including a plurality of tube assemblies 100 aligned relative to each other and forming a substantially horizontal flat configuration (e.g., a single row of tube assemblies 100 ).
- the tube assemblies 100 can extend in a direction substantially aligned with horizontal.
- the ends of the tube assemblies 100 can be aligned and secured to tube sheets 252 a , 252 b on opposing sides of the tube assemblies 100 .
- Air flow can enter/exit the heat exchanger 250 b in opposing directions 256 , 258 perpendicular to the tube assemblies 100 .
- FIG. 20 shows a heat exchanger 250 c including a plurality of tube assemblies 100 aligned relative to each other and forming a substantially vertical flat configuration (e.g., a single column of tube assemblies 100 ).
- the tube assemblies 100 in the vertical configuration can be aligned substantially perpendicular to the alignment of the horizontal configuration, and substantially perpendicular to horizontal.
- the ends of the tube assemblies 100 can be aligned and secured to tube sheets 252 a , 252 b on opposing sides of the tube assemblies 100 .
- Air flow can enter/exit the heat exchanger 250 c in opposing directions 256 , 258 perpendicular to the tube assemblies 100 .
- FIG. 21 shows a heat exchanger 250 d including a single tube assembly 100 curved into a spiral configuration.
- the tube assembly 100 can be bent into a spiral shape with the ends of the tube assembly 100 being secured to tube sheets 252 a , 252 b sized for only a single tube assembly 100 .
- the spiral configuration results in a passage 254 formed between the tube assembly 100 components and extending the height of the heat exchanger 250 d .
- Air flow can enter/exit the heat exchanger 250 d in opposing directions 256 , 258 perpendicular to the tube assembly 100 , via a direction 260 passing through the passage 254 , combinations thereof, or the like.
- FIG. 22 shows a heat exchanger 250 e including a plurality of tube assemblies 100 disposed adjacent to each other and curved into a vertical cylindrical configuration (e.g., a curved single row of tube assemblies 100 extending substantially perpendicularly to horizontal).
- a passage 254 is formed between the tube assemblies 100 and extends the height of the heat exchanger 250 e .
- the ends of the tube assemblies 100 can be aligned and secured to tube sheets 252 a , 252 b .
- Air flow can enter/exit the heat exchanger 250 e in opposing directions 256 , 258 perpendicular to the tube assemblies 100 , via a direction 260 passing through the passage 254 , combinations thereof, or the like.
- FIG. 23 shows a heat exchanger 250 f including a plurality of tube assemblies 100 a , 100 b aligned and formed into a substantially flat A-shaped or upside down V-shaped configuration.
- the heat exchanger 250 f includes a first flat group of tube assemblies 100 a and a second flat group of tube assemblies 100 b that are joined at one central tube assembly 100 .
- the first and second flat group of tube assemblies 100 a , 100 b connect at the central tube assembly 100 and extend in opposing directions to form an angle 264 therebetween (e.g., between approximately 30° and approximately 90°, or the like).
- Each of the tube assemblies 100 a , 100 b can extend substantially parallel to horizontal.
- the ends of the tube assemblies 100 a , 100 b can be aligned and secured to tube sheets 252 a , 252 b on opposing sides of the tube assemblies 100 a , 100 b .
- Air flow can enter/exit the heat exchanger 250 f via direction 256 perpendicular to the second flat group of tube assemblies 100 b , direction 258 perpendicular to the first flat group of tube assemblies 100 a , via direction 260 perpendicular to the central tube assembly 100 , combinations thereof, or the like.
- FIG. 24 shows a heat exchanger 250 g including a plurality of tube assemblies 100 aligned and formed into a flat slanted configuration (e.g., a single row of tube assemblies 100 each extending substantially parallel to horizontal, with the combined row of tube assemblies 100 being slanted relative to horizontal).
- the tube assemblies 100 can be disposed adjacent to each other and aligned into a flat configuration, and the heat exchanger 250 g can be slanted by an angle 264 (e.g., between approximately 30° and approximately 90°) relative to a horizontal plane 266 .
- the ends of the tube assemblies 100 can be aligned and secured to tube sheets 252 a , 252 b on opposing sides of the tube assemblies 100 . In the orientation of FIG.
- the tube sheets 252 a , 252 b are at the sides of the heat exchanger 250 g .
- Air flow can enter/exit the heat exchanger 250 g via direction 256 parallel to the horizontal plane 266 , via direction 258 perpendicular to the horizontal plane 266 , combinations thereof, or the like.
- FIG. 25 shows a heat exchanger 250 h including a plurality of tube assemblies 100 aligned and formed into a solid block configuration.
- the tube assemblies 100 can be disposed adjacent to each other in multiple rows and columns to form the solid block configuration.
- Each of the tube assemblies 100 can extend substantially parallel to horizontal. It should be understood that a variety of shapes can be formed by varying the number of rows and columns of the heat exchanger 250 h .
- the ends of the tube assemblies 100 can be aligned and secured to tube sheets 252 a , 252 b on opposing sides of the tube assemblies 100 . Air flow can enter/exit the heat exchanger 250 h via direction 256 perpendicular to the tube assemblies 100 .
- FIG. 26 shows a heat exchanger 250 i including a plurality of tube assemblies 100 aligned and formed into a flat slanted configuration (e.g., a single row of aligned tube assemblies 100 , with each tube assembly 100 extending at an angle relative to horizontal).
- the tube assemblies 100 can be disposed adjacent to each other and aligned into a flat configuration, and the heat exchanger 250 i can be slanted by an angle 264 (e.g., between approximately 30° and approximately 90°) relative to a horizontal plane 266 .
- the ends of the tube assemblies 100 can be aligned and secured to tube sheets 252 a , 252 b on opposing sides of the tube assemblies 100 . In the orientation of FIG.
- the tube sheets 252 a , 252 b are substantially at the top and bottom of the heat exchanger 250 i .
- the tube sheets 252 a , 252 b can be substantially perpendicular to the ends of the tube assemblies 100 , and angled relative to the horizontal plane 266 .
- Air flow can enter/exit the heat exchanger 250 i via direction 256 parallel to the horizontal plane 266 , via direction 258 perpendicular to the horizontal plane 266 , combinations thereof, or the like.
- FIG. 27 is a block diagram of an exemplary heat exchanger system 300 .
- the heat exchanger system 300 can include at least one of the exemplary heat exchangers 302 described herein.
- the heat exchanger 302 includes one or more tube assemblies 304 .
- the heat exchanger 302 can be disposed within a heater housing 306 .
- a gas source 308 can be fluidly connected to the heater housing 306 and/or the heat exchanger 302 to introduce heated gas into an area surrounding the tube assemblies 304 .
- a water circulating system or source 310 can be fluidly connected to the heater housing 306 to introduce swimming pool water into the tube assemblies 304 . Due to the heated gas surrounding the tube assemblies 304 , the swimming pool water can be heated to the desired temperature.
- the titanium structure of the elongated tubes with the copper fins welded to the tubes provides for corrosion resistance by isolating the swimming pool water within the tubes, while allowing for improved heat transfer to the swimming pool water.
Abstract
Description
- The present application claims the priority benefit of U.S. Provisional Application No. 62/348,186, filed Jun. 10, 2016, which is hereby incorporated by reference in its entirety for all purposes.
- The present disclosure relates to swimming pool heat exchangers and associated systems and methods and, in particular, to heat exchangers including a plurality of titanium tubes with welded copper fins for improved heat transfer in swimming pool heater applications.
- Various types of heaters have been used over the years for heating fluids in applications such as residential heating systems and swimming pools. Although discussed herein with respect to water tube heat exchangers, fire tube heat exchangers have also been used in the industry. Most heaters include a heat exchanger disposed proximate a source of heat through which the fluid to be heated passes. The heat exchanger generally includes a metal conduit through which the fluid to be heated can pass and is positioned above a burning gas to absorb the heat of combustion and conduct it to the fluid passing through the conduit. To increase the efficiency of heat transfer, the heat exchanger can be configured to maximize the exterior surface area exposed to the heat of combustion by using metal fins on the conduit.
- Different materials of construction for heat exchangers have been used. The advantages of using titanium tubing with swimming pool water to avoid corrosion has been well documented, and titanium tubing has been widely used in mechanical heating appliances (e.g., heat pumps). In particular, titanium has been successfully used with mechanical heating appliances due to the heat exchanger being used for a liquid-to-liquid heat transfer and, compared to gas-fired appliances, a relatively low amount of heat to be transferred into the swimming pool water.
- Gas-fired appliances with an air-to-liquid heat exchanger generally have a higher heat capacity than liquid-to-liquid heat exchangers. However, achieving adequate heat transfer using titanium tubes in the air-to-liquid heat exchanger of a gas-fired appliance has proven elusive in the swimming pool heater industry. One hurdle to attaining adequate heat transfer is the inability to extrude titanium into a tube with a substantial number of integrated fins. Although the extrusion process is widely used with copper and cupro-nickel in the industry, fins for a titanium tube cannot be extruded to the desired size for proper heat transfer. Some swimming pool heat exchangers include extruded fin tubes manufactured from either copper or cupro-nickel and have fin heights that cannot be manufactured out of titanium.
- Some manufacturers have welded stainless steel fins to stainless steel tubing. Some industries, such as boiler and fluid processing, have used fins of a dissimilar material than the tube welded to the titanium tubes. Some swimming pool heat exchangers include plate fin designs with tubes mechanically expanded into collars on the plates to bond the fins and tubes. However, such methods are unfeasible for use with titanium.
- Thus, a need exists for swimming pool heat exchangers that include titanium tubes with welded copper fins that provide the desired amount of heat transfer and corrosion resistance in air-to-liquid applications. These and other needs are addressed by the swimming pool heat exchangers and associated systems and methods of the present disclosure.
- In accordance with embodiments of the present disclosure, exemplary swimming pool heat exchangers are provided that include a housing and one or more tube assemblies disposed within the housing. Each of the tube assemblies includes an elongated titanium tube and at least one fin welded (e.g., laser welded) to an outer surface of the elongated titanium tube. In some embodiments, any type of welding can be used to attach the fins to the outer surface of the titanium tube. In some embodiments, the tube assemblies can include a plurality of fins individually welded in a spaced manner along the outer surface of the elongated titanium tube. In some embodiments, the tube assemblies can each include one fin fabricated as a single material and defining a helical shape such that the inner surface of the helical fin is continuously welded along the outer surface of the elongated titanium tube. The elongated titanium tube and the welded fin(s) allow for corrosion resistance to swimming pool water while simultaneously allowing for improved heat transfer from the heat exchanger to the swimming pool water.
- The at least one fin can be a copper fin. The at least one fin can define a circular configuration. The elongated titanium tube can define a cylindrical configuration with an inner passage extending therethrough. The heat exchanger can include at least one tube sheet secured to ends of the one or more tube assemblies.
- In some embodiments, the heat exchanger can include a column of the tube assemblies aligned along a central axis. In some embodiments, the heat exchanger can include a plurality of the tube assemblies staggered relative to each other. In some embodiments, the one or more tube assemblies can be of the same outer diameter. In some embodiments, the one or more tube assemblies can be of different outer diameters. In some embodiments, the one or more tube assemblies can be arranged in, e.g., a U-shaped or cylindrical configuration, a flat configuration defining a single column of tube assemblies, a bent spiral configuration, a cylindrical configuration including a passage extending between the tube assemblies, an A-shaped configuration, a V-shaped configuration, a solid block configuration including multiple rows and columns of tube assemblies disposed adjacent to each other, combinations thereof, or the like.
- In accordance with embodiments of the present disclosure, an exemplary method of heating swimming pool water is provided. The method includes introducing heated gas (or an alternative source) into one of the exemplary heat exchangers disclosed herein. In particular, the heated gas can be introduced into an area surrounding the one or more tube assemblies. The method includes introducing or circulating swimming pool water to the one or more tube assemblies of the heat exchanger to allow for heat transfer between the heated gas and the swimming pool water. The method includes adjusting a configuration of the one or more tube assemblies within the housing to adjust a heat transfer rate to the swimming pool water.
- In accordance with embodiments of the present disclosure, an exemplary heat exchanger system is provided that includes a heat exchanger as disclosed herein, a gas source, and a swimming pool water source. The gas source can be fluidly connected to the heat exchanger and configured to supply heated gas (or an alternative source) to an area surrounding the one or more tube assemblies. The swimming pool water source can be fluidly connected to the heat exchanger and configured to supply swimming pool water to the one or more tube assemblies.
- Other objects and features will become apparent from the following detailed description considered in conjunction with the accompanying drawings. It is to be understood, however, that the drawings are designed as an illustration only and not as a definition of the limits of the invention.
- To assist those of skill in the art in making and using the disclosed heat exchangers and associated systems and methods, reference is made to the accompanying figures, wherein:
-
FIG. 1 is a diagrammatic side view of an exemplary tube assembly of an exemplary heat exchanger according to the present disclosure. -
FIG. 2 is a diagrammatic front view of an exemplary tube assembly ofFIG. 1 . -
FIG. 3 is a perspective view of a plurality of exemplary tube assemblies ofFIG. 1 . -
FIG. 4 is a front view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 . -
FIG. 5 is a front view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 . -
FIG. 6 is a front view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 . -
FIG. 7 is a front view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 . -
FIG. 8 is a front view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 . -
FIG. 9 is a front view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 . -
FIG. 10 is a front view of an exemplary heat exchanger including one column of a plurality of tube assemblies ofFIG. 1 . -
FIG. 11 is a front view of an exemplary heat exchanger including two columns of a plurality of tube assemblies ofFIG. 1 . -
FIG. 12 is a front view of an exemplary heat exchanger including three columns of a plurality of tube assemblies ofFIG. 1 . -
FIG. 13 is a front view of an exemplary heat exchanger including two columns of a plurality of differently sized tube assemblies ofFIG. 1 . -
FIG. 14 is a front view of an exemplary heat exchanger including one staggered column of a plurality of tube assemblies ofFIG. 1 . -
FIG. 15 is a front view of an exemplary heat exchanger including two staggered columns of a plurality of tube assemblies ofFIG. 1 . -
FIG. 16 is a front view of an exemplary heat exchanger including three staggered columns of a plurality of tube assemblies ofFIG. 1 . -
FIG. 17 is a front view of an exemplary heat exchanger including two staggered columns and one aligned column of a plurality of differently sized tube assemblies ofFIG. 1 . -
FIG. 18 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a horizontal cylindrical configuration. -
FIG. 19 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a horizontal flat configuration. -
FIG. 20 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a vertical flat configuration. -
FIG. 21 is a perspective view of an exemplary heat exchanger including a tube assemblies ofFIG. 1 in a spiral configuration. -
FIG. 22 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a vertical cylindrical configuration. -
FIG. 23 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a flat A-shaped configuration. -
FIG. 24 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a flat slanted configuration. -
FIG. 25 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a solid block configuration. -
FIG. 26 is a perspective view of an exemplary heat exchanger including a plurality of tube assemblies ofFIG. 1 in a flat slanted configuration. -
FIG. 27 is a block diagram of an exemplary heat exchanger system according to the present disclosure. - In accordance with embodiments of the present disclosure, exemplary heat exchangers including a plurality of tubes with welded fins (e.g., laser welded) are provided. The tubes can be smooth titanium tubes that include copper fins welded to the exterior surface to enhance heat transfer from hot combustion gases to swimming pool water flowing within the heat exchanger tubes of a gas-fired pool heater. In some embodiments, the heat exchanger can include a single welded fin tube attached to a water circulating system suspended over a small source of heat. The exemplary heat exchangers achieve improved heat transfer by using titanium tubes with the welded copper fins in an air-to-liquid heat exchanger system with corrosion resistance (normally found in heat pump heat exchangers) and with a higher heat capacity of gas-fired appliances. In particular, the exemplary heat exchangers include titanium tubes in gas-fired swimming pool heaters to achieve corrosion resistance by isolating the swimming pool water within the titanium tubes, while maintaining the heat transfer characteristics of high-finned heat exchanger tubes.
- By using titanium tubes with fins welded to the exterior made from copper or another material, heat transfer far above what titanium tubes can achieve alone can be accomplished while still offering the corrosion resistance needed in the portion of the heat exchanger in direct contact with swimming pool water. In particular, rather than using extruded or expanded fins as normally done in the swimming pool heater industry, the fins are welded to the titanium tube to facilitate the higher heat transfer than normally achieved by the titanium tubes alone. The welded fins, which provide a significant increase in surface area and are manufactured from a material with a higher thermal conductivity than titanium, thereby transferring the required amount of heat from a heat source, typically a burner, to swimming pool water inside of the titanium tube. The titanium tube, in turn, is resistant to corrosion typically caused by exposure to swimming pool water. This heat transfer is aided by the fact that the entire length of fin is welded to the tube, resulting in a permanent thermal bond between the titanium tube and the fins. The bond would not be permanent if the fin was only attached at the endpoints or only by mechanical means. Therefore, the thermal bond between the titanium tube and the fins results in an improved attachment between the components.
- Although discussed herein with respect to gas-fired swimming pool heaters, it should be understood that the exemplary heat exchangers can be used with any appliance that includes a heat exchanger configured to transfer heat from hot combustion gases to liquid where corrosion caused by the liquid is one of the primary concerns. In some embodiments, the exemplary tubes and fins can be used in heaters for fluids, such as the heater for fluids disclosed in U.S. Pat. No. 6,026,804, incorporated herein by reference. In some embodiments, rather than laser welding, the titanium tube can be expanded into the plate fins. However, such methods are generally performed with larger and more complicated processing machines.
- A plurality of titanium tubes can be arranged to form a heat exchanger and can be secured to one or more tube sheets to define the heat exchanger shape. The tube sheets provide a transition to the connected water system. In some embodiments, different geometries, configurations or arrangements of the heat exchanger can be used, resulting in different tube arrangements within the geometry and different airflow paths through the tubes. In some embodiments, varying sizes and/or numbers of the tubes can be used in flat horizontal or alternative configurations to differ airflow paths through the tubes.
- In some embodiments, the material of the base tubing or the welded fins, or the geometry or arrangement of the fins relative to the tubes can be changed. Changing the fins, e.g., the height, material, fin density on the tube, combinations thereof, or the like, can allow for heat transfer at different rates. Thus, by changing characteristics of the fins welded to the tubes, the heat exchanger can be customized to adjust for the desired heat transfer rate. Changing the tube material can be used to accommodate for different types or sources of corrosion present in the heat exchanger system.
- With reference to
FIGS. 1 and 2 , diagrammatic side and front views of anexemplary tube assembly 100 of an exemplary heat exchanger are provided. It should be understood that the heat exchanger can include one or more of thetube assemblies 100 arranged in various configurations depending on the heat transfer rate desired for the system. Eachtube assembly 100 includes anelongated tube 102, e.g., an extruded titanium tube defining a cylindrical configuration with aninner passage 103 extending therethrough configured to receive swimming pool water. In some embodiments, thetube 102 can define a configuration other than cylindrical, e.g., square, rectangular, oval, or the like. Thetube 102 can define anoverall length 104 extending along a centrallongitudinal axis 106. Thetube 102 can define anouter diameter 108 with awall thickness 110. In some embodiments, theouter diameter 108 can be approximately 0.75 inches and thewall thickness 110 can be approximately 0.02 inches. - The
tube assembly 100 includes a plurality of fins 112 (e.g., copper fins) secured to anouter surface 116 of thetube 102. Thefins 112 can be welded (e.g., laser welded) to theouter surface 116 of thetube 102. In particular, rather than only a partial welding, the entire circumferential inner diameter of thefins 112 can be laser welded to theouter surface 116 of thetube 102. In some embodiments, thefins 112 can define a substantially circular configuration with adiameter 114. In some embodiments, thediameter 114 of eachfin 112 can be approximately, e.g., 40 mm, 50 mm, or the like. In some embodiments, eachfin 112 can define a thickness between approximately 0.015 inches to approximately 0.020 inches. In some embodiments, the plurality offins 112 can be fabricated as a single piece of material helically wound around theouter surface 116 of thetube 102 and welded along the entire contact surface of the inner surface of thefins 112 and theouter surface 116 of thetube 102. Although illustrated as substantially circular, in some embodiments, thefins 112 can define different configurations, e.g., oval, rectangular, square, triangular, hexagonal, or the like. In some embodiments,fins 112 having multiple different configurations can be secured to theouter surface 116 of thetube 102. For example, rather than being symmetrical relative to the vertical and horizontalcentral axes FIG. 2 , thefins 112 can define an asymmetrical configuration. - In some embodiments, the
fins 112 can be spaced substantially uniformly relative to each other along thetube 102. In some embodiments, the spacing between thefins 112 can be different. In some embodiments, thefins 112 can be welded to thetube 102 such that thefins 112 extend substantially perpendicularly relative to thelongitudinal axis 106. In some embodiments, thefins 112 can be welded to thetube 102 at non-perpendicular angles relative to thelongitudinal axis 106. Thefins 112 can extend only along apartial length 118 of theoverall length 104 of thetube 102. In particular, theproximal end 120 and thedistal end 122 of thetube 102 can remain uncovered (e.g., without fins 112). For example, aproximal length 124 and adistal length 126 of thetube 102 can remain uncovered or exposed. In some embodiments, the proximal anddistal lengths distal lengths -
FIG. 3 shows a plurality oftube assemblies 100 positioned adjacent to each other. As shown inFIG. 3 , thetube assemblies 100 can be aligned along thelongitudinal axis 106 of eachtube assembly 100 to form a substantially planar configuration of a heat exchanger. Alternative configurations or arrangements of thetube assemblies 100 will be discussed in greater detail below. -
FIGS. 4-9 show front views of exemplary heat exchangers 150 a-f with different configurations or arrangements of the tube assemblies 100 (referred to asprimary tube assemblies 100 a andsecondary tube assemblies 100 b). The diameter of thetube assemblies 100 defines the diameter of the fins of eachrespective tube assembly 100. Thetube assemblies distal ends 120, 122) by endplates or tube sheets. In particular,FIGS. 4-9 show different sizes and arrangements of thetube assemblies 100 that can fit within thesame structure 152 that defines aheight 154 and awidth 156. For example, different sizes and combinations of thetube assemblies 100 can be used to fit within astructure 152 that defines thewidth 156. It should be understood that thetube assemblies 100 ofFIGS. 4-9 can include tube sheets disposed on each side of thetube assemblies - In the embodiment of
FIG. 4 , theprimary tube assemblies 100 a can be aligned along the horizontalcentral axis 130. Theprimary tube assemblies 100 a can be spaced relative to each other to receive thesecondary tube assemblies 100 b therebetween. In particular, thesecondary tube assemblies 100 b can be disposed between theprimary tube assemblies 100 a in a staggered or offset manner in a diagonal direction. Thesecondary tube assemblies 100 b are therefore aligned along their respective horizontal central axes, with the horizontal central axis of thesecondary tube assemblies 100 b being offset from the horizontalcentral axis 130 of theprimary tube assemblies 100 a. As an example, theheat exchanger 150 a can include sixtube assemblies tube assemblies tube assemblies tube assemblies tube assemblies - The
heat exchanger 150 b ofFIG. 5 can be substantially similar in structure and function to theheat exchanger 150 a ofFIG. 4 , except that seventube assemblies tube assemblies tube assemblies FIG. 4 , allowing a greater number oftube assemblies same width 156 of thestructure 152. - The
heat exchanger 150 c ofFIG. 6 can be substantially similar in structure and function to the heat exchanger of 150 a ofFIG. 4 , except that tentube assemblies tube assemblies tube assemblies FIGS. 4 and 5 , allowing a greater number oftube assemblies same width 156 of thestructure 152. - The
heat exchanger 150 d ofFIG. 7 can be substantially similar in structure and function to theheat exchanger 150 a ofFIG. 4 , except that sixteentube assemblies tube assemblies tube assemblies FIGS. 4-6 , allowing a greater number oftube assemblies same width 156 of thestructure 152. - The
heat exchanger 150 e ofFIG. 8 can be substantially similar in structure and function to theheat exchanger 150 a ofFIG. 4 , except that fourteentube assemblies tube assemblies tube assemblies FIGS. 4-6 , allowing a greater number oftube assemblies same width 156 of thestructure 152. - The
heat exchanger 150 f ofFIG. 9 can be substantially similar in structure and function to theheat exchanger 150 a ofFIG. 4 , except that twelvetube assemblies tube assemblies tube assemblies FIGS. 4-6 , allowing a greater number oftube assemblies same width 156 of thestructure 152. -
FIGS. 10-17 are front views of exemplary heat exchangers 200 a-h including a plurality oftube assemblies 100 arranged in different configurations. Each configuration provides a variation in heat transfer flow rates from the combustion gas to the swimming pool water. In particular, the different configurations result in varied heat transfer either by affecting the surface area in contact with the combustion gases (e.g., the number of rows and diameter of the tube assemblies 100) or by affecting the airflow pattern and distance the combustion gases stay in contact with the heat exchanger (e.g., staggered rows and diameter of the tube assemblies 100). For example,FIG. 10 shows aheat exchanger 200 a that includes asingle column 204 oftube assemblies 100 of the same size (e.g., four tube assemblies). Thetube assemblies 100 can be arranged to align along a verticalcentral axis 202. Air flow can enter theheat exchanger 200 a from, e.g., afirst direction 206 substantially perpendicular to the verticalcentral axis 202, asecond direction 208 substantially aligned with the verticalcentral axis 202, combinations thereof, or the like. -
FIG. 11 shows aheat exchanger 200 b that includes twocolumns tube assemblies 100 of the same size (e.g., each column including four tube assemblies). Thetube assemblies 100 can be arranged such that fourtube assemblies 100 are aligned along a first verticalcentral axis 202 a and fourtube assemblies 100 are aligned along a second verticalcentral axis 202 b, the first and second verticalcentral axes columns tube assemblies 100 can be disposed adjacent to each other. Further, the adjacently positionedtube assemblies 100 can be aligned along horizontal central axes 210 a-d. Air flow can enter theheat exchanger 200 b from, e.g., afirst direction 206 substantially perpendicular to the first and second verticalcentral axes second direction 208 substantially aligned with the first and second verticalcentral axes -
FIG. 12 shows aheat exchanger 200 c that includes threecolumns 204 a-c oftube assemblies 100 of the same size (e.g., each column including four tube assemblies). Thetube assemblies 100 can be arranged such that fourtube assemblies 100 are aligned along a first verticalcentral axis 202 a, fourtube assemblies 100 are aligned along a second verticalcentral axis 202 b, and fourtube assemblies 100 are aligned along a third verticalcentral axis 202 c, the verticalcentral axes columns 204 a-c of thetube assemblies 100 can be disposed adjacent to each other. Further, the adjacently positionedtube assemblies 100 can be aligned along horizontal central axes 210 a-d. Air flow can enter theheat exchanger 200 c from, e.g., afirst direction 206 substantially perpendicular to the verticalcentral axes 202 a-c, asecond direction 208 substantially aligned with the verticalcentral axes 202 a-c, combinations thereof, or the like. -
FIG. 13 shows aheat exchanger 200 d that includes twocolumns tube assemblies tube assemblies 100 a of the same size can be arranged such that fourtube assemblies 100 a are aligned along a first verticalcentral axis 202 a, and twotube assemblies 100 b of a size different from thetube assemblies 100 a are aligned along a second verticalcentral axis 202 b. The first and second verticalcentral axes tube assembly 100 b can be approximately double in diameter as compared to eachtube assembly 100 a. The twocolumns tube assemblies central axis 212 a of one of thetube assemblies 100 b can be aligned between the horizontalcentral axes tube assemblies 100 a. Similarly, a horizontalcentral axis 212 b of theother tube assembly 100 b can be aligned between the horizontalcentral axes tube assemblies 100 a. Air flow can enter theheat exchanger 200 d from, e.g., afirst direction 206 substantially perpendicular to the verticalcentral axes second direction 208 substantially aligned with the verticalcentral axes third direction 214 substantially perpendicular to the verticalcentral axes first direction 206, combinations thereof, or the like. -
FIG. 14 shows aheat exchanger 200 e that includes one staggeredcolumn 204 oftube assemblies 100 of the same size (e.g., the column including four tube assemblies). Thetube assemblies 100 can be arranged such that everyother tube assembly 100 is aligned along a first verticalcentral axis 202 a and a second verticalcentral axis 202 b, respectively. The first and second verticalcentral axes tube assemblies 100 can be staggered by an angle relative to horizontal central axes 210 a-d. The fins of thetube assemblies 100 can be disposed in a substantially tangent and abutting configuration. Air flow can enter theheat exchanger 200 e from, e.g., afirst direction 206 substantially perpendicular to the verticalcentral axes second direction 208 substantially aligned with the verticalcentral axes -
FIG. 15 shows aheat exchanger 200 f that includes two staggeredcolumns tube assemblies 100 of the same size (e.g., each column including four tube assemblies). Thetube assemblies 100 can be arranged such that everyother tube assembly 100 is aligned along a first to fourth verticalcentral axes 202 a-d, with twotube assemblies 100 aligned per verticalcentral axis 202 a-d. The verticalcentral axes 202 a-d are spaced from each other. Each of the adjacently positionedtube assemblies 100 can be staggered by an angle relative to horizontal central axes 210 a-d. The fins of thetube assemblies 100 can be disposed in a substantially tangent and abutting configuration. For example, the fins of thetube assemblies 100 aligned along the horizontal central axes 210 a-d can abut each other. Air flow can enter theheat exchanger 200 f from, e.g., afirst direction 206 substantially perpendicular to the verticalcentral axes 202 a-d, asecond direction 208 substantially aligned with the verticalcentral axes 202 a-d, combinations thereof, or the like. -
FIG. 16 shows aheat exchanger 200 g that includes three staggeredcolumns 204 a-c oftube assemblies 100 of the same size (e.g., each column including four tube assemblies). Thetube assemblies 100 can be arranged such that everyother tube assembly 100 is aligned along a first to sixth verticalcentral axes 202 a-f, with twotube assemblies 100 aligned per verticalcentral axis 202 a-f. The verticalcentral axes 202 a-f are spaced from each other. Each of the adjacently positionedtube assemblies 100 can be staggered by an angle relative to horizontal central axes 210 a-d. The fins of thetube assemblies 100 can be disposed in a substantially tangent and abutting configuration. For example, the fins of thetube assemblies 100 aligned along the horizontal central axes 210 a-3 can abut each other. Air flow can enter theheat exchanger 200 g from, e.g., afirst direction 206 substantially perpendicular to the verticalcentral axes 202 a-f, asecond direction 208 substantially aligned with the verticalcentral axes 202 a-f, combinations thereof, or the like. -
FIG. 17 shows aheat exchanger 200 h that includes one staggeredcolumn 204 a oftube assemblies 100 a of the same size (e.g., the column including four tube assemblies) and onecolumn 204 b oftube assemblies 100 b sized differently than thetube assemblies 100 a. Thetube assemblies 100 a can be arranged such that everyother tube assembly 100 is aligned along a first verticalcentral axis 202 a and a second verticalcentral axis 202 b, respectively. The first and second verticalcentral axes tube assemblies 100 a can be staggered by an angle relative to horizontal central axes 210 a-f. Thetube assemblies 100 b can be arranged such that the twotube assemblies 100 b are aligned along a third verticalcentral axis 202 c. Thetube assemblies 100 b can be aligned with respective horizontalcentral axes tube assemblies 100 a. In some embodiments, thetube assemblies 100 b can be disposed along horizontal central axes that are parallel to (but not aligned with) the horizontal central axes 210 a-f). The fins of thetube assemblies heat exchanger 200 h from, e.g., afirst direction 206 substantially perpendicular to the verticalcentral axes 202 a-c, asecond direction 208 substantially aligned with the verticalcentral axes 202 a-c, athird direction 214 substantially perpendicular to the verticalcentral axes 202 a-c and opposing thefirst direction 206, combinations thereof, or the like. -
FIGS. 18-26 show perspective views of exemplary heat exchangers 250 a-i includingtube assemblies 100 in different configurations. Although illustrated as substantially square or rectangular in cross-section, in some embodiments, thetube assemblies 100 can have a substantially round cross-section (such as the tube assemblies ofFIGS. 1-17 ). For example,FIG. 18 shows aheat exchanger 250 a including a plurality oftube assemblies 100 stacked and aligned relative to each other, and bent into a substantially U-shaped, tear-shaped or horizontal cylindrical configuration. Thetube assemblies 100 can extend in a direction substantially aligned with horizontal. The ends of thetube assemblies 100 can be disposed adjacent to each other and secured to asingle tube sheet 252. Due to the curved shape of thetube assemblies 100, apassage 254 is formed between thetube assemblies 100 and extends the height of theheat exchanger 250 a. Air flow can enter into thepassage 254 from above 256 and below 258. Air flow can enter/exit theheat exchanger 250 a in opposingdirections tube assemblies 100. -
FIG. 19 shows aheat exchanger 250 b including a plurality oftube assemblies 100 aligned relative to each other and forming a substantially horizontal flat configuration (e.g., a single row of tube assemblies 100). Particularly, thetube assemblies 100 can extend in a direction substantially aligned with horizontal. The ends of thetube assemblies 100 can be aligned and secured totube sheets tube assemblies 100. Air flow can enter/exit theheat exchanger 250 b in opposingdirections tube assemblies 100. -
FIG. 20 shows aheat exchanger 250 c including a plurality oftube assemblies 100 aligned relative to each other and forming a substantially vertical flat configuration (e.g., a single column of tube assemblies 100). In particular, thetube assemblies 100 in the vertical configuration can be aligned substantially perpendicular to the alignment of the horizontal configuration, and substantially perpendicular to horizontal. The ends of thetube assemblies 100 can be aligned and secured totube sheets tube assemblies 100. Air flow can enter/exit theheat exchanger 250 c in opposingdirections tube assemblies 100. -
FIG. 21 shows aheat exchanger 250 d including asingle tube assembly 100 curved into a spiral configuration. In particular, thetube assembly 100 can be bent into a spiral shape with the ends of thetube assembly 100 being secured totube sheets single tube assembly 100. The spiral configuration results in apassage 254 formed between thetube assembly 100 components and extending the height of theheat exchanger 250 d. Air flow can enter/exit theheat exchanger 250 d in opposingdirections tube assembly 100, via adirection 260 passing through thepassage 254, combinations thereof, or the like. -
FIG. 22 shows aheat exchanger 250 e including a plurality oftube assemblies 100 disposed adjacent to each other and curved into a vertical cylindrical configuration (e.g., a curved single row oftube assemblies 100 extending substantially perpendicularly to horizontal). In particular, due to the cylindrical configuration of thetube assemblies 100, apassage 254 is formed between thetube assemblies 100 and extends the height of theheat exchanger 250 e. The ends of thetube assemblies 100 can be aligned and secured totube sheets heat exchanger 250 e in opposingdirections tube assemblies 100, via adirection 260 passing through thepassage 254, combinations thereof, or the like. -
FIG. 23 shows aheat exchanger 250 f including a plurality oftube assemblies heat exchanger 250 f includes a first flat group oftube assemblies 100 a and a second flat group oftube assemblies 100 b that are joined at onecentral tube assembly 100. The first and second flat group oftube assemblies central tube assembly 100 and extend in opposing directions to form anangle 264 therebetween (e.g., between approximately 30° and approximately 90°, or the like). Each of thetube assemblies tube assemblies tube sheets tube assemblies heat exchanger 250 f viadirection 256 perpendicular to the second flat group oftube assemblies 100 b,direction 258 perpendicular to the first flat group oftube assemblies 100 a, viadirection 260 perpendicular to thecentral tube assembly 100, combinations thereof, or the like. -
FIG. 24 shows aheat exchanger 250 g including a plurality oftube assemblies 100 aligned and formed into a flat slanted configuration (e.g., a single row oftube assemblies 100 each extending substantially parallel to horizontal, with the combined row oftube assemblies 100 being slanted relative to horizontal). In particular, thetube assemblies 100 can be disposed adjacent to each other and aligned into a flat configuration, and theheat exchanger 250 g can be slanted by an angle 264 (e.g., between approximately 30° and approximately 90°) relative to ahorizontal plane 266. The ends of thetube assemblies 100 can be aligned and secured totube sheets tube assemblies 100. In the orientation ofFIG. 24 , thetube sheets heat exchanger 250 g. Air flow can enter/exit theheat exchanger 250 g viadirection 256 parallel to thehorizontal plane 266, viadirection 258 perpendicular to thehorizontal plane 266, combinations thereof, or the like. - While the above configurations were formed from a single column of
tube assemblies 100,FIG. 25 shows aheat exchanger 250 h including a plurality oftube assemblies 100 aligned and formed into a solid block configuration. In particular, thetube assemblies 100 can be disposed adjacent to each other in multiple rows and columns to form the solid block configuration. Each of thetube assemblies 100 can extend substantially parallel to horizontal. It should be understood that a variety of shapes can be formed by varying the number of rows and columns of theheat exchanger 250 h. The ends of thetube assemblies 100 can be aligned and secured totube sheets tube assemblies 100. Air flow can enter/exit theheat exchanger 250 h viadirection 256 perpendicular to thetube assemblies 100. -
FIG. 26 shows aheat exchanger 250 i including a plurality oftube assemblies 100 aligned and formed into a flat slanted configuration (e.g., a single row of alignedtube assemblies 100, with eachtube assembly 100 extending at an angle relative to horizontal). In particular, thetube assemblies 100 can be disposed adjacent to each other and aligned into a flat configuration, and theheat exchanger 250 i can be slanted by an angle 264 (e.g., between approximately 30° and approximately 90°) relative to ahorizontal plane 266. The ends of thetube assemblies 100 can be aligned and secured totube sheets tube assemblies 100. In the orientation ofFIG. 26 , thetube sheets heat exchanger 250 i. Thetube sheets tube assemblies 100, and angled relative to thehorizontal plane 266. Air flow can enter/exit theheat exchanger 250 i viadirection 256 parallel to thehorizontal plane 266, viadirection 258 perpendicular to thehorizontal plane 266, combinations thereof, or the like. -
FIG. 27 is a block diagram of an exemplaryheat exchanger system 300. Theheat exchanger system 300 can include at least one of theexemplary heat exchangers 302 described herein. Theheat exchanger 302 includes one ormore tube assemblies 304. Theheat exchanger 302 can be disposed within aheater housing 306. Agas source 308 can be fluidly connected to theheater housing 306 and/or theheat exchanger 302 to introduce heated gas into an area surrounding thetube assemblies 304. A water circulating system orsource 310 can be fluidly connected to theheater housing 306 to introduce swimming pool water into thetube assemblies 304. Due to the heated gas surrounding thetube assemblies 304, the swimming pool water can be heated to the desired temperature. As noted above, the titanium structure of the elongated tubes with the copper fins welded to the tubes provides for corrosion resistance by isolating the swimming pool water within the tubes, while allowing for improved heat transfer to the swimming pool water. - While exemplary embodiments have been described herein, it is expressly noted that these embodiments should not be construed as limiting, but rather that additions and modifications to what is expressly described herein also are included within the scope of the invention. Moreover, it is to be understood that the features of the various embodiments described herein are not mutually exclusive and can exist in various combinations and permutations, even if such combinations or permutations are not made express herein, without departing from the spirit and scope of the invention.
Claims (20)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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US15/617,760 US20170356691A1 (en) | 2016-06-10 | 2017-06-08 | Swimming Pool Heat Exchangers And Associated Systems And Methods |
CA2970160A CA2970160A1 (en) | 2016-06-10 | 2017-06-09 | Swimming pool heat exchangers and associated systems and methods |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201662348186P | 2016-06-10 | 2016-06-10 | |
US15/617,760 US20170356691A1 (en) | 2016-06-10 | 2017-06-08 | Swimming Pool Heat Exchangers And Associated Systems And Methods |
Publications (1)
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US20170356691A1 true US20170356691A1 (en) | 2017-12-14 |
Family
ID=60572408
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US15/617,760 Abandoned US20170356691A1 (en) | 2016-06-10 | 2017-06-08 | Swimming Pool Heat Exchangers And Associated Systems And Methods |
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US (1) | US20170356691A1 (en) |
AU (1) | AU2017203940A1 (en) |
CA (1) | CA2970160A1 (en) |
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US20180135915A1 (en) * | 2016-11-11 | 2018-05-17 | Johnson Controls Technology Company | Finned heat exchanger u-bends, manifolds, and distributor tubes |
US20220127870A1 (en) * | 2018-07-25 | 2022-04-28 | Hayward Industries, Inc. | Compact Universal Gas Pool Heater And Associated Methods |
CN114867971A (en) * | 2019-10-04 | 2022-08-05 | 里姆制造公司 | Heat exchanger tube and tube assembly arrangement |
US20220316823A1 (en) * | 2021-03-30 | 2022-10-06 | Rheem Manufacturing Company | Corrosion prevention for heat exchanger devices and pool heaters |
US11739980B2 (en) * | 2018-08-23 | 2023-08-29 | Purpose Co., Ltd. | Heat exchanging unit, heat exchanging apparatus, and hot water supply system |
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- 2017-06-08 US US15/617,760 patent/US20170356691A1/en not_active Abandoned
- 2017-06-09 AU AU2017203940A patent/AU2017203940A1/en not_active Abandoned
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US20180135915A1 (en) * | 2016-11-11 | 2018-05-17 | Johnson Controls Technology Company | Finned heat exchanger u-bends, manifolds, and distributor tubes |
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CN114867971A (en) * | 2019-10-04 | 2022-08-05 | 里姆制造公司 | Heat exchanger tube and tube assembly arrangement |
US11499747B2 (en) * | 2019-10-04 | 2022-11-15 | Rheem Manufacturing Company | Heat exchanger tubes and tube assembly configurations |
US20220316823A1 (en) * | 2021-03-30 | 2022-10-06 | Rheem Manufacturing Company | Corrosion prevention for heat exchanger devices and pool heaters |
Also Published As
Publication number | Publication date |
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CA2970160A1 (en) | 2017-12-10 |
AU2017203940A1 (en) | 2018-01-04 |
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