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Publication numberUS2650802 A
Publication typeGrant
Publication dateSep 1, 1953
Filing dateSep 8, 1948
Priority dateSep 19, 1947
Publication numberUS 2650802 A, US 2650802A, US-A-2650802, US2650802 A, US2650802A
InventorsHuet Andre
Original AssigneeHuet Andre
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Countercurrent heat exchanger
US 2650802 A
Abstract  available in
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)


Patented Sept. 1, 1953 2,650,802 COUNTERCURRENT HEAT EXCHANGER Andr Huet, Paris, France Application September 8, 1948, Serial No. 48,179 In France September 19, 1947 1 Claim. 1

This invention relates to an improved countercurrent heat exchanger having a tube bundle traversed interiorly as by water and disposed in a stream of hot gases so that the warmer gases first encounter tubes traversed by the warmed water and that the coolest gases subsequently contact tubes traversed by the coolest water.

In particular the present invention contemplates that the tubes of the tube bundle which constitute the heat exchanger are disposed with respect to one another so that while retaining the principle of counter-flow the water inside the tubes flows nevertheless in the tube bundle as a whole in the same general sense as the gases. For example, in the case of the application of the invention to an economizer of a water tube boiler the tubes of the economizer are disposed in the usual manner on the path of the rising hot gases, but they are associated among themselves to realize an internal circulation in such fashion that the discharge tubes of the economizer which contain the hottest water are in contact with the hottest portion of the rising gases while the admission tubes of the economizer which contain the coldest water are in contact with the coolest gases, all in realizing a circulation of the water which permits it to rise as it becomes heated.

As an example of carrying out this disposition, if an economizer had only two rows of tubes, each of these two rows of tubes would be constituted by a distinct multi-looped element made up of several parallel tubes interconnected by return bends and the discharge branches of the elements would constitute the first row of tubes reached by the hot rising gases, while the admission branches would constitute the second row of tubes which are located after the first in the direction of gas fiow and the plane of each looped element would be slightly inclined from the horizontal plane to permit the discharge branch to be elevated slightly above the admission branch. The branch tubes of each element themselves may have a continuous slight slope favoring the flow of steam bubbles in case of vaporization.

To conveniently direct the current of hot gases the tubes are preferably provided with tangential fins conforming to my earlier application, serial No. 748,561, filed May 16, 1947, now Patent No. 2,578,136, granted December 11, 1951, with the distinction that the fins of the several tubes of any particular looped element do not contact each other but are disposed in such fashion as to come in contact, or substantially in contact, with the fins of the tubes of another element in a manner to guide the passage of exterior gas,

all in oifering a staggered disposition of tubes to the streams of gases which produces in the flow of gases the successive effects of dilation, of compression, and of change of direction assuring the optimum heat exchange.

The invention will be best understood upon consideration of the following description when read in conjunction with the accompanying drawing in which:

Figure 1 is a schematic vertical sectional view of part of a water tube boiler equipped with an economizer embodying the invention.

Figure 2 is a view on a larger scale of part of the economizer shown in Figure 1.

Figure 3 illustrates in plan view one of the double-looped elements making up the economizer.

. Fig. 4 is a diagrammatic plan view showing the manner in which the looped elements are connected to the inlet and outlet headers.

In the case for example of a Water tube boiler of which half is represented at the right of the axis of symmetry X-X in Figure l the inclined bundle of water tubes H3 rises from the lower drum IE to the upper drum it. The economizer designated as a whole by numeral i5 is placed at the outlet side of this tube bundle in the path AB of the hot gases from the furnace. The tubes forming the economizer lie in rows parallel to the general direction of the axes of the tubes 10 as one sees in the drawing. The economizer which has been shown comprises four rows of tubes but the number could be different.

The economizer is made up of double-looped elements 20 such as is shown in Figure 3 and consisting of four parallel tubes H to 24 con nected for series flow therethrough by return bends, connecting adjacent ends of the tubes. When an element is mounted, its plane is slightly inclined from the horizontal following the line D-D in Figure 2. The cold water coming from the distributor 25 passes successively through the branches 2 I, 22, 23 and 24 of the element and the hot water is discharged into exits through the collecting header 26.

With the arrangement embodying the invention it may be seen that all the inlet branches 2 I, Zia, 2 lb, and 210 of the several elements 26 in the economizer make up the fourth row of tubes, that is to say the furthest from the hot gases A, the elements 22, 22a, 22b, and 22c-make up the third row; the elements 23, 23a, 23b and 230 the second; and the elements 24, 24a, 24b and 240 the first, that is to say the row nearest to the water tubes H] which is contacted by the hottest gases 3 A. Thus, as has already been explained the economizer functions in countercurrent but, because of the inclination of the elements in planes parallel to the line DD of Figure 2, the water which traverses the branches 2| to 24 of each element rises within that element from the level of tube 2| to the level of tube 24, Figure 2, as it is heated, which favors the circulation within the element.

The branches of each element of the economizer are provided with tangential fins of the type described in my aforementioned Patent No. 2,578,136. As seen in Figure 2 the elements 29 are disposed so that their component tubes are staggered with respect to those of the adjacent elements and the fins come into contact with the fins of the elements situated not immediately below but two rows below, the fin 30 of the tube 23 in the first element, Figure 2, coming in contact with the fin 3| of the tube 222; in the second element above etc, so as to present sinuous channels C-C to the gases flowing in the general direction of the arrow A across the staggered arrangement of tubes, the general direction of channels C-C being that of the flow A. This arrangement produces in the gases the successive effects of dilation and of contraction, as well as change of direction, which assures the optimum of heat exchange. It is obvious that an economizer construction embodying the invention could have tubes that do not carry fins, or carry fins arranged in ordinary manner.

The invention is applicable equally to economizers whatever be their location within the boiler and more generally to all heat exchangers.

What I claim is:

In a heat exchange bank positioned to intercept an ascending stream of fluid which approaches the bank obliquely from one side of the bank below the latter; said bank comprising a plurality of individual looped elements disposed in superposed relation in parallel planes located generally transverse of general direction of flow of the fluid stream flowing through the bank and each consisting of a number of similarly spaced parallel tube lengths located in a row inclined 4 lightly from the horizontal and having their contiguous ends interconnected by return bends for series fluid flow from an inlet tube at one end of the row to an outlet tube at the end of the row from which the stream of fluid approaches the bank with said superposed elements progressively offset in a direction toward the approaching fluid stream by increments substantially equal to one half the tube spacing in each row to stagger said tubes and dispose the several outlet tubes in a row inclined substantially from the vertical at that side of said bank from which the ascending fluid approaches and confronting the stream of fluid approaching the bank; inlet and outlet headers to which the lowest and highest tubes respectively of each element are connected; and longitudinally extending fins projecting from said tubes at substantially diametrically spaced points and so oriented vertically that the distal ends of flns on the respective tubes in alternate rows aline and are substantially in contact to form vertical flow directing bafiles within said bank causing the fluid stream to change from a direction of flow normal to the plane of the outlet tubes of said elements and ascend substantially vertically through the back to contact different tube lengths of the respective rows forming each successively encountered element as the stream ascends through the bank.


References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 767,187 Wadham Aug. 9, 1904 1,757,621 De Lorenzi May 6, 1930 1,827,201 Kerr Oct. 13, 1931 1,884,777 Lucke Oct. 25, 1932 2,167,333 Foss July 25, 1939 2,277,921 McCullough et a1. Mar. 31, 1942 2,444,908 Bailey et al July 13, 1948 FOREIGN PATENTS Number Country Date 432,342 France Oct. 3, 1911

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US767187 *Jun 6, 1903Aug 9, 1904Robert WadhamApparatus for transmission of heat.
US1757621 *Oct 1, 1927May 6, 1930Int Comb Eng CorpEconomizer
US1827201 *Oct 5, 1928Oct 13, 1931Babcock & Wilcox CoEconomizer with overlapping plates
US1884777 *Apr 21, 1928Oct 25, 1932Babcock & Wilcox CoLongitudinal flow economizer
US2167333 *Jul 20, 1937Jul 25, 1939B F Sturtevant CoHeat exchanger
US2277921 *Sep 11, 1939Mar 31, 1942Bohn Aluminium & Brass CorpHeat exchange unit
US2444908 *Jun 6, 1946Jul 13, 1948Babcock & Wilcox CoFluid heat exchange installation
FR432342A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3111168 *Nov 14, 1955Nov 19, 1963Huet AndreHeat exchangers
US3251665 *May 31, 1963May 17, 1966Pittsburgh Plate Glass CoMethod for the production of glass fibers
US3384165 *Feb 3, 1966May 21, 1968Du PontHeat exchanger
US3975229 *Jan 10, 1972Aug 17, 1976Jackson Morden AFlameless reboiler for reconcentrating liquid desiccant
US4004965 *May 24, 1976Jan 25, 1977Maloney-Crawford Tank CorporationVertical flameless reboiler for reconcentrating liquid desiccant
US4226279 *Aug 15, 1978Oct 7, 1980Foster Wheeler Energy CorporationMethod of suppressing formation of heat exchange fluid particles into standing waves
US5799724 *Jul 22, 1997Sep 1, 1998The Babcock & Wilcox CompanyTrapezoidal deflectors for heat exchanger tubes
US7686072 *Feb 5, 2007Mar 30, 2010Riello S.P.A.Heat exchanger and methods of producing the same
U.S. Classification165/165, 122/367.3, 165/183, 165/160, 122/420, 165/DIG.451, 165/176, 165/172
International ClassificationF28F1/14, F22D1/10
Cooperative ClassificationF22D1/10, Y10S165/451, F28F1/14
European ClassificationF22D1/10, F28F1/14