IE57155B1 - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
IE57155B1
IE57155B1 IE115186A IE115186A IE57155B1 IE 57155 B1 IE57155 B1 IE 57155B1 IE 115186 A IE115186 A IE 115186A IE 115186 A IE115186 A IE 115186A IE 57155 B1 IE57155 B1 IE 57155B1
Authority
IE
Ireland
Prior art keywords
inner shell
water
heat exchanger
heat
chamber
Prior art date
Application number
IE115186A
Other versions
IE861151L (en
Original Assignee
Thermocatalytic Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Thermocatalytic Corp filed Critical Thermocatalytic Corp
Priority to IE115186A priority Critical patent/IE57155B1/en
Publication of IE861151L publication Critical patent/IE861151L/en
Publication of IE57155B1 publication Critical patent/IE57155B1/en

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

THERMOCATALYTIC CORP, A CORPORATION ORGANISED AND EXISTING UNDER THE LAMS OF THE STATE OF HEM YORK, UNITED STATES OF AMERICA, OF 129, HILLSIDE AVENUE, WILLISTON PARK, NEW YORK 11596, UNITED STATES OF AMERICA.
Price 90p The present invention relates to a heat exchanger for a radiant heated water boiler.
In prior United States Patent Specification No. 4, 442,799, a radiant heated-water boiler is disclosed having a heat exchanger comprising a cylindrical shell, in which a gas fired combustion element concentrically disposed. The combustion element is connected to a heat source, such as a gas/air mixture, which ignites the combustion element, the ignited gases passing through the element into the surrounding hollow shell. Disposed at a clearance position, about the combustion element is a helically coiled tube, through which water is pumped, which water thus absorbs the heat from the combustion element.
While this construction is highly effective and more efficient than those heat exchange arrangements previously known, several disadvantages have become known. For example, the use of a helically coiled tube increases the cost of the heat exchanger due to its complexity, labour intensiveness, and cost of basic raw material, such as the copper needed for the tube. In addition, the exchange of heat is based solely on radiation and convection impinging on the tube to heat the water in the tube. Further, only a limited through-put of water is possible, since the water has to pass serially through - 2 the spiral tube.
According to the present invention, there is provided a heat exchanger for a radiant heated water boiler comprising a pair of concentrically arranged cylindrical shells connected at each end to define therebetween a chamber for holding water, an inlet for the supply of water to said chamber extending through the outer shell at a lower end and an outlet for the discharge of water from the chamber at the upper end, a combustion element extending into the inner shell from said upper end providing a source of heat radiating outwardly therefrom against the inner shell, said inner shell comprising a corrugated wall formed with a single continuous helix extending substantially from said inlet to said.outlet and a porous plug arranged in the lower end of said inner shell to regulate the exhaust of said heat source flowing downwardly along the interior surface of said inner shell.
A heat exchanger of such construction can be simpler in construction than those known heretofore and can provide improved efficiency in operation because heat transfer is effective by conduction as well as by convection.
The invention will be more fully appreciated from the following detailed description of the presently preferred embodiment, reference being made to the accompanying drawing in which : 2o Fig. 1 is a partial section through the length of the heat exchanger : Fig. 2 is a transverse section through the heat exchanger taken along line 2-2 of Fig. 1; and Fig. 3 is an enlarged portion of the helical corrugated inner shell.
As seen in Figs. 1 and 2, the heat exchanger generally depicted by numeral 10, comprises and outer cylindrical shell 12 and an inner cylindrical shell 14, concentrically spaced from each other. The upper end of the inner shell 14 is flared outwardly to form a radial flange 16 adapted to overlay a corresponding flanged end 18 of the outer shell. Secured to the flange 18 of the outer shell is a cap 20 which holds the inner shell 14 in a fixed position. The lower end of the inner shell comprises a smooth cylindrical footing 22 which is force fit with an 0-ring seal 24 seated in an annular - 3 groove 26 formed in a radially inwardly directed flange 28 at the lower most end of the outer shell 12. In this manner, the inner shell 14 is sealed at its lower end by the O-ring 24, and at its upper end by the cap 20, so that it extends concentrically within the outer shell 12, defining therewith a closed annular chamber 30 along its entire length, in which water to be heated may be located.
An inlet 32 is provided for cooled water passes through the outer shell 12 adjacent its lower end and an outlet 34 for heated-water passes adjacent its upper end. ί 10 The present invention differs from the prior device in providing a double shell heat exchanger, the inner shell being formed of a single metallic cylinder, which as will be described has a distinctive configuration. As seen in the Figs. 1-3, the inner shell 14 comprises a single wall 42 in which a single corrugation, accordion-like along the longitudinal axis, and consisting of a continuous helix from one end to the other Is formed. Thus, both the outer and inner surfaces of the wall 42 in longitudinal section have continuous undulations : the outer surface helix 44 being completely In contact with the water in the chamber 30; the inner surface helix 46 being completely open for impingement of the Incendiary gas and its radiation B.
Concomitantly, the outer helix 44 provides an upward helically path F for the water flow, with a long dwelling time in the chamber, while the inner helix 46 simultaneously provides a helical counter-current downward path G for the exhaust gases.
A porous combustion element 36 Is appropriately mounted in a central clearance position within the inner shell and communicates through a supply duct 38 passing through the cap 22 with a source of combustible gas, which is forced under pressure, arrow A into the combustion element 36 and through the porosity of its wall construction so that it radiates radially therefrom as noted by the arrows individually and collectively designated B. 3θ As understood, and as described in detail in the referred-to U.S.
Patent Specification No. 4,442,799, the operation of the combustion element 36 * contemplates Igniting the combustion gases with the result that at, or near, the periphery of the surface of element 36 there Is the referred-to combustion j reaction that is manifested by Incandescence. As a result, the radially - 4 flowing exhaust gases B are at an elevated temperature with which it is highly desirable to effectuate a heat transfer to a flowing heat exchange fluid, such as water.
To the above end, the heat exchanger 10 also includes a source of water that is pumped though a pipe or conduit (not shown) into the inlet 32 such that a continuous stream of water exits through the outlet 34 after a sufficient period of dwelling time within the chamber 30 such that its temperature is significantly elevated as compared with the temperature at which it entered, A plug 40, made of ceramic porous material is forced, fitted or otherwise mounted tightly within the inner shell at the lower or remote end from the combustion element, so as to prevent the rapid escape of the incendiary exhaust gases from the inner shell 14. The plug 40 on the other hand regulates the escape of the gas, while at the same time acting to cool the gas prior to its escape. In cooling the incendiary gas, the plug 40, itself becomes hot and glows, at its tip, adding to the heat within the inner shell. The gas is cooled as it passes around the plug 40 and exits through the open lower end 22 of the inner shell, as seen by arrow E.
Although the structure described is different from that described in US Patent Specification No. 4,442, 799, the basic operation of the heat exchanger is similar so that further details of the combustion element, plug, and water flow will be apparent to those skilled in this art.
As has already been noted, the present invention differs from the prior device in providing a double shell heat exchanger, the inner shell being formed of a single metallic cylinder, which as described has a distinctive configuration. As seen in Figs. 1-3, it will be recognised that during operation the fluid flow rate is such that the entire chamber 30 formed between the inner and outer shells is filled with the fluid, passing in contact with the outer surface of the helically corrugated inner shell, effecting heat conduction, with the entire surface. Simultaneously, the inner surface of the corrugated inner shell provides an enlarged area against which the radiant heat may impinge. As a result the entire body of water in the chamber 30 is subject to heat transfer at all times. - 5 Among other noteworthy advantages obtained by the present invention are the following : The construction of the heat exchanger has been simplified by the use of a relatively large dimensioned inner shell rather than the small diameter helical tube; the surface adjacent to the radiant combustion element has been Increased significantly due to the accordion-like corrugated surface and therefore more radiant heat Is transferred to the fluid ι being heated, and similarly, the surface against which the water resides Is also increased by the accordion-like structure: heat transfer occurs due to both convection and conduction and the transfer is more direct because the 4 water surfaces are correspondingly in direct contact with the heating media; during operation, there is turbulent helical flow of the radiant and exhaust J gases which increases heat transfer, as seen in Fig. 2 where it is clear that the water helix spirals radially in one direction while the gas helix sprials radially in the other direction, so that the water and gas in adjacent axial 15 layers is in constant movement with respect to each other; the fluid to be heated takes a helical flow pattern and is thus turbulent, thereby reducing the effect of the insulating boundary layer generally caused in smooth helical tubes, and provides a higher heat transfer; and heat transfer is also enhanced by the fluid flow counter to the radiant heat and exhaust gases.
The advantages enumerated above are in large measure obtained because of the increased surface space for both water and gas contact, providing an increased dwell time under conditions of heat transfer, while simultaneously providing means for directing the flow of liquid and Incendiary gas in counterflow direction.
Preferably, the heat exchanger is completed by enclosing the outer shell with a layer of insulation abutting the outer surface of the outer shell 12. A surrounding decorative housing, not shown, may be provided.

Claims (2)

CLAIMS :
1. A heat exchanger for a radiant heated water boiler comprising a pair of concentrically arranged cylindrical shells connected at each end to define therebetween a chamber for holding 5 water, an inlet for the supply of water to said chamber extending through the outer shell at a lower end and an outlet for the discharge 4 of water from the chamber at the upper end, a combustion element extending into the inner shell from said upper end providing a source Ί of heat radiating outwardly therefrom against the inner shell, said J 10 inner shell comprising a corrugated wall formed with a single continuous helix extending substantially from said inlet to said outlet and a porous plug arranged in the lower end of said inner shell to regulate the exhaust of said heat source flowing downwardly along the interior surface of said inner shell. 15
2. A heat exchanger for a radiant heated water boiler . substantially as herein described with reference to the accompanying drawing.
IE115186A 1986-05-01 1986-05-01 Heat exchanger IE57155B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
IE115186A IE57155B1 (en) 1986-05-01 1986-05-01 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IE115186A IE57155B1 (en) 1986-05-01 1986-05-01 Heat exchanger

Publications (2)

Publication Number Publication Date
IE861151L IE861151L (en) 1987-11-01
IE57155B1 true IE57155B1 (en) 1992-05-06

Family

ID=11022716

Family Applications (1)

Application Number Title Priority Date Filing Date
IE115186A IE57155B1 (en) 1986-05-01 1986-05-01 Heat exchanger

Country Status (1)

Country Link
IE (1) IE57155B1 (en)

Also Published As

Publication number Publication date
IE861151L (en) 1987-11-01

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