US3144081A - Heat exchanger tube supports - Google Patents

Heat exchanger tube supports Download PDF

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US3144081A
US3144081A US178646A US17864662A US3144081A US 3144081 A US3144081 A US 3144081A US 178646 A US178646 A US 178646A US 17864662 A US17864662 A US 17864662A US 3144081 A US3144081 A US 3144081A
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tubes
channel members
shell
heat exchanger
side walls
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US178646A
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Edward J Skiba
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Brown Fintube Co
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Brown Fintube Co
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Priority to GB5659/63A priority patent/GB953309A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/007Auxiliary supports for elements
    • F28F9/013Auxiliary supports for elements for tubes or tube-assemblies
    • F28F9/0135Auxiliary supports for elements for tubes or tube-assemblies formed by grids having only one tube per closed grid opening
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/06Heat-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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/355Heat exchange having separate flow passage for two distinct fluids
    • Y10S165/40Shell enclosed conduit assembly
    • Y10S165/401Shell enclosed conduit assembly including tube support or shell-side flow director
    • Y10S165/416Extending transverse of shell, e.g. fin, baffle

Definitions

  • Such a heat exchanger embodies a plurality of hairpin shaped tubes enclosed in a shell of hairpin shape.
  • Each leg of the shell is of generally circular internal cross section and contains a bundle of straight tubes, consisting of the legs of the hairpin tubes, arranged in spaced parallel relation to each other.
  • Such heat exchangers often are of considerable length. It is important that the tubes in the bundle in each leg of the shell be firmly supported relatively to each other and to the shell, but the length of the heat exchanger often makes it impossible to support the tubes in each bundle from only the end at which they are connected to the shell. For this reason, at least one and preferably several spacing means should be located along the length of the bundle to provide the desired support to the tubes.
  • the spacing means should satisfy several criteria. It should properly space and secure the tubes relatively to each other. It should space and locate the tubes relatively to the shell. It should permit relative longitudinal movement between the tubes and the shell, as can occur due to differences in thermal expansion of the tubes and the shell. It should not impair heat transfer between the fluid in the tubes and the fluid outside of the tubes in the shell, and preferably should increase heat transfer. While performing the above functions, it should not substantially increase the pressure drop on the fluid passing through the shell, since this would increase pumping costs and provide other difliculties. In the event the fluid passing through the shell is of the type which can vaporize under the conditions to which it is subjected in the shell, the spacing means should allow the resultant vapors to pass freely through the shell without vapor binding.
  • a general object of the invention is the provision of strong, simple and economical spacing means which satisfies the above criteria and provides other advantages. More specific objects include the provision of such spacing means which can be readily manufactured and installed. Other objects include the provision of a heat exchanger embodying such spacing means.
  • FIGURE 1 is a side elevation with parts broken away of a preferred form of heat exchanger embodying the invention
  • FIGURE la is an enlarged section of the sealing means joining the inner tubes, shell tube, and fluid pipe at one end of one shell tube;
  • FIGURE 2 is a cross section to an enlarged scale of one leg of the heat exchanger shown in FIGURE 1, the view being taken as indicated by line 2-2 of FIGURE 1;
  • FIGURE 3 is a side elevation of a portion of a tube bundle of the heat exchanger to the same scale as FIG- URE 2;
  • FIGURE 4- is a perspective of a spacer embodying the invention.
  • a preferred form of heat exchanger embodying the invention comprises a pair of parallel external or shell tubes and 11. These tubes are connected at their rear ends to a return bend housing 12 having a rear opening surrounded by a flange 13 to which is bolted the cover 14 which closes the opening.
  • the shell tubes may be supported by frame members 15 or by any other convenient means.
  • the forward ends of the shell tubes 10 and 11 are provided with flanges 16 and 17, respectively, to which pipe-connecting fittings 18 and 19 are secured by bolts 21. Fluid is supplied to and discharged from the interior of the shell tubes through the connections 22 and 23 which are welded to the tubes 10 or 11 near the flanges 16 and 17.
  • the connection 23 is the inlet and connection 22 is the outlet, as indicated by the arrows. It will be understood, however, that the direction of flow through the shell tubes may be reversed if desired.
  • a plurality of hair pin tubes 25 are disposed in the shell tubes.
  • Each of illustrated tubes 25 comprises two bare straight sections or legs 26 connected by a return bend 27 within the return bend housing 12.
  • seven hairpin tubes are employed, the straight tube sections 26 being arranged in two bundles, one in each shell tube, so that there is one tube section 26' (see FIGURE 2) at the center of each bundle with its axis substantially coincident with that of the shell tube, and six outer tube sections equidistantly and equiangularly spaced around the central tube axis.
  • a greater or lesser number of tubes may be utilized without departing from the invention, although the outer hairpin tubes surrounding the inner tube or tubes are preferably even in number.
  • the forward ends of the tubes 26 in each bundle are fixed in a tube sheet 28 which is supported by a split locking ring 29, which is disposed in a groove in the tube sheet 28 and engages an inner flange 30 in the corresponding shell tube 10 or 11, against the force exerted by a sealing ring 31 that is engaged by the corresponding fitting 18 or 19.
  • Bolts 21 hold the fittings 18 and 19 in place and draw them against the sealing rings 31.
  • the rings 31 make sealing engagement with the adjacent tube sheet 28 and the adjacent flange 16 or 17 of the shell tube 10 or 11.
  • Pipes 32 and 33 connect the hairpin tubes to an external fluid system.
  • Pipe 32 connected to fitting 18 constitutes the inlet and pipe 33 connected to fitting 19 constitutes the outlet, thus providing for counterflow of the fluids in the illustrated heat exchanger.
  • the flow can be reversed if desired, and it will be evident that the connecting pipes 32 and 33 and the lateral connec tions 22 and 23 can be arranged to connect a plurality of heat exchanger units such as shown in FIGURE 1 in series or in multiple.
  • the present invention provides supporting and spacing devices 40 for supporting the tubes 26 in proper position with respect to each other and with respect to the surrounding shell tubes and 11.
  • FIG. URE 4 there are several supporting devices 40 disposed along the length of the bundle of the straight tube sections 26 in each of the shell tubes.
  • One of the supporting devices 40 is shown separately in perspective in FIG- URE 4 and is shown in place and to an enlarged scale in FIGURES 2 and 3.
  • each supporting device or spacer 40 comprises a central member 41 in the form of a short tubular member which is adapted to be mounted on and preferably fixed to the central tube section 26 of the bundle of tubes in each shell tube.
  • the central member 41 supports a set of identical channel members 42 equally spaced about the member 41.
  • a second set of smaller channel members 43 is also mounted on central member 41, the members 43 being alternately disposed relative to members 42.
  • Each channel member 42 is formed of a piece of sheet metal bent to have two diverging side wall44 connected at the bottom to a narrow base 45 fixed, as by welding, to the exterior of central member 41.
  • Each side wall 44 is wide enough to extend from the outer surface of member 41 to the inner surface of the shell tube 10 or 11.
  • Each smaller channel member 43 of the other group is also formed of a piece of sheet metal bent to have two identical side walls 46 joined to a narrow base 47 fixed as by welding to the exterior of central member 41.
  • the side walls 46 of each member 43 are considerably narrower than the side walls 44 of members 42. The outer edges of side walls 46 being located close to, and preferably in contact with the outer surfaces of the side walls 44 of the channel members 42.
  • the cross sectional shape of the channel members 43 is identical to the cross sectional shape of the channel members 42 up to the point where the side walls 44 of channel members 42 are engaged by the outer edges of the side walls 46 of channel members 43. This is shown in FIGURE 2.
  • the channel members 43, and the lower portions of the alternately disposed channel members 42 thus provide identical V- shaped bearing surfaces which contact the straight lengths 26 of the outer tubes in a bundle when the spacer is mounted in place with its central member 41 surrounding the central tube 26'.
  • the outer tubes are preferably held in contact with these surfaces by a band or strap 50 located adjacent to the spacer, as shown in FIGURES 1, 2 and 3.
  • This band or strap may be any conventional type of metal strapping applied in a conventional manner and hence requires no further description.
  • Spacers of the kind described above may be readily manufactured by preforming strips of metal into long channel members having the cross sections of members 42 and 43, and fixing these long channel-shaped members in the proper alternating relationship on a central tubular member approximately as long as the channel members and having the cross section of member 41 by welding the narrow bottom walls of such channel-shaped members to the outer surface of the central tubular member, preferably in accordance with the method and apparatus disclosed in J. W. Brown, Jr. Patents 2,298,249 and 2,298,250 issued October 6, 1942. The long welded assembly is then cut into short spacer members 40 of the desired length.
  • the desired number of spacers 40 are slid onto the central straight tube section 26' of each bundle, arranged in the proper and preferably uniformly spaced relation, and if desired are welded to such tube section as shown in FIGURE 2. Thereafter, the straight sections 26 of the outer tubes in the bundle are positioned within the channel members 42 and 43 as shown in FIGURE 2, and the straps 50 are applied. The tube sheet 28 at each end of the tube bundle is then mounted and fixed in place, and the heat exchanger is assembled in the usual manner. During assembly the outer edges of the wide channel members 42 engage the shells 1t) and 11 and facilitate sliding the tube bundles into the shells.
  • the outer tubes are firmly and accurately located relatively to each other and to the central tube by their engagement with the side walls 44 and 46 of the channel members 42 and 43 of the spacers 40, against which side walls they are held by the straps 50 adjacent each spacer.
  • the outer edges of the side walls 44 of the wide channel members 42 engage the inner surfaces of the shells and accurately locate the bundles as a whole relatively to the shells.
  • the walls 44 of channel members 42 and the walls 46 of channel members 43 provide addition heat exchange surfaces which increase transfer of heat between fluid flowing inside of the tubes 25 and the fluid flowing outside of the tubes and inside of the shells.
  • the spacing and heat transfer functions of the spacers 40 are provided without substantially increasing the pressure drop on the fluid flowing through the shell outside of the tubes, since all extended surfaces of the spacer are parallel to the direction of fluid flow.
  • These geometrical relationships of the parts of the spacer also permit vapors which might arise from vaporizing type shell fluids to pass freely through the heat exchanger without vapor binding, as could occur with transverse plate type supports. All of these desirable results can be achieved at relatively low cost.
  • the spacers themselves are rugged and have long life.
  • the side walls 44 and 46 of channel members 42 and 43 are flat; this is preferable since it not only facilitates the forming of the channel members on relatively simple equipment but also because it promotes heat transfer by providing space between each channel member and the surface portion of each outer tube which is nearest the central tube.
  • the lower portion of each channel member can be made to conform to the outer surface of the tube, or can be made of other configurations than shown. It is desirable, however, that the portions of the various channel members which contact the tubes be identical so as to provide for the desired equidistant and equiangular spacing of outer tubes of identical cross section in the bundle.
  • the number of wide channel members 42 should be equal to the number of the narrow channel members 43, since they are alternately disposed; this means that there is an even number of channel shaped bearing surfaces available for supporting outer tubes in a bundle.
  • the number of wide members 42 and of narrow members 43 may, of course, be an odd or even number, but the total number of members 42 and 43 should be an even number which is determined by the number of tubes which it is desired to support by the spacer.
  • spacer is formed of sheet metal parts welded to a central member, it is apparent that it may be formed of other materials and in other manners.
  • spacers of the invention have been disclosed as used in hairpin type heat exchangers having bare tubes, they may be employed to support and space tubes in a bundle in other types of heat exchangers. Moreover, they may be used to support finned tubes in hairpin or other type heat exchangers, as by engaging bare portions of such tubes.
  • a heat exchanger comprising an elongated shell; a bundle of elongated heat exchange tubes located in said shell, said tubes being spaced from each other and disposed substantially parallel to each other and to said shell and substantially equiangularly spaced around a central axis; and a spacer engaging said tubes and said shell to locate said tubes with respect to said shell and to each other, comprising a first set of outwardly opening channel members of substantially identical cross section extending longitudinally along and spaced substantially equiangularly about said axis, each of said channel members having outwardly diverging sidewalls, a second set of channel members alternately disposed between the channel members of said first set and extending longitudinally along and disposed substantially equiangularly around said axis, each of said channel members of said second set being of substantially identical cross section and having outwardly diverging sidewalls, the sidewalls of the channel members of said second set terminating adjacent to sidewalls of adjacent channel members of said first set, and means for locating said channel members with respect to each other
  • a heat exchanger comprising an elongated shell; a plurality of elongated heat exchange tubes of generally circular substantially identical cross section located in said shell in substantially parallel relation and substantially equidistantly and equiangularly spaced from an axis extending longitudinally of said shell; and a spacer engaging said tubes and said shell to locate said tubes with respect to said axis and said shell comprising a first set of channel members of substantially identical cross section extending longitudinally along and spaced substantially equidistantly and equiangularly about said axis, each of said channel members having sidewalls formed of sheet material, a second set of channel members of substantially identical cross section alternately disposed between said channel members of aid first set and extending longitudinally along and spaced substantially equidistantly and equiangularly about said axis, each of said channel members of said second set having outwardly diverging sidewalls formed of sheet material and having their outermost edges in close proximity to adjacent sidewalls of adjacent channel members of said first set, the side
  • a heat exchanger comprising an elongated shell; a bundle of elongated heat exchange tubes located in said shell, said tubes being disposed substantially parallel to each other and to said shell and substantially equidistantly and equiangularly spaced around a central axis; and a spacer engaging said tubes and said shell to locate said tubes with respect to said axis and said shell comprising a tubular central member, a first set of channel members of substantially identical cross section extending longitudinally along and spaced equiangularly around said central member, each of said channel members having outwardly diverging side walls, and a second set of channel members alternately disposed between the channel members of said first set and extending longitudinally along and disposed equiangularly around said central member, each of said channel members of said second set being of substantially identical cross section and having outwardly diverging side walls, the side walls of the channel members of the second set terminating adjacent to side walls of adjacent channel members of the first set, each channel member receiving and supporting one of said heat exchanger tubes to locate
  • a heat exchanger comprising an elongated shell; a bundle of elongated heat exchange tubes located in said shell, said tubes being spaced from each other and disposed substantially parallel to each other and to said shell and substantially equidistantly and equiangularly spaced around a central axis; a spacer engaging said tubes and said shell to locate said tubes in said shell comprising a tubular central member, a first set of channel members of substantially identical cross section extending longitudinally along said central member and spaced equiangularly around said central member, each of said channel members having outwardly diverging side walls, and a second set of channel members alternately disposed between the channel members of said first set and extending longitudinally along and disposed equiangularly around said central member, each of said channel members of said second set being of substantially identical cross section and having outwardly diverging side walls, the side Walls of the channel members of the second set terminating adjacent to the side walls of adjacent channel members of the first set, the side walls of said channel members of said first and second
  • a heat exchanger comprising an elongated shell; a plurality of elongated heat exchange tubes of generally circular substantially identical cross section located in said shell in substantially parallel relation and substantially equidistantly and equiangularly spaced from an axis extending longitudinally of said shell; a plurality of spacers disposed at spaced locations along said bundle, each of said spacers engaging said tubes and said shell to locate said tubes in said shell comprising a central member, a first set of channel members of substantially identical cross section supported from and around said central member at locations equidistantly and equiangularly spaced from said axis, each of said channel members having side walls formed of sheet material, and a second set of channel members of substantially identical cross section alternately disposed between said channel members of said first set, supported from and around said central member at locations equidistantly and equiangularly spaced from said axis, each of said channel members.
  • a hairpin type heat exchanger comprising an elongated shell of hairpin shape having two straight legs; a plurality of elongated hairpin-shaped heat exchange tubes defining two bundles of straight tube sections each of which bundles is disposed longitudinally in one of the legs of the shell, the tubes in each bundle being of generally circular cross section with one of said tubes located centrally of the bundle and others of substantially identical cross section located in substantially parallel relation to and substantially equidistantly and equiangularly spaced from the axis of the central tube; spacers engaging said tubes in said shell legs to locate said tubes, each of said spacers comprising a tubular central member mounted coaxially on the central tube in a bundle, a first set of channel members of substantially identical cross section supported from and around said central member at locations equidistantly and equiangularly spaced from its axis, each of said channel members having outwardly diverging sheet metal side walls, a second set of channel members of substantially identical cross section alternately disposed between said channel members of said
  • a spacer for locating an even number of elongated members of generally circular substantially identical cross section with their axes in substantially parallel relation and substantially equidistantly and equiangularly spaced from the axis of the spacer comprising a central member having an axis coincident with the axis of the spacer; a first set of channel members of substantially identical cross section supported from said central member at locations therearound equidistantly and equiangularly spaced from the axis of the spacer, each of said channel members having side walls formed of sheet material; a second set of channel members of substantially identical cross section, alternately disposed between said channel members of said first set and supported from and around said central member at locations equidistantly and equiangularly spaced from the axis of said spacer, each of said channel members of said second set having out- Wardly diverging side Walls formed of sheet material the outermost edges of which side Walls are located in close proximity to adjacent side walls of adjacent channel members of said

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

Aug. 11, 1964 E. J. SKIBA HEAT EXCHANGER TUBE SUPPORTS Filed March 9, 1962 INVENTOR.
W 8044mm,
mmce/mwm United States Patent 3,144,081 HEAT EXCHANGER TUEE SUPPORTS Edward J. Slriha, Rocky River, Ohio, assignor to Brown Eintuhe Company, Elyria, Ohio, a corporation of Ohio Filed Mar. 9, 1962, Ser. No. 178,646 7 (Ilaims. (Cl. 165-162) This invention relates to heat exchangers, and more particularly to the tubes of multiple tube heat exchangers. The invention is described herein as applied to a heat exchanger of the hairpin type, in which use the invention provides exceptional advantages.
Such a heat exchanger embodies a plurality of hairpin shaped tubes enclosed in a shell of hairpin shape. Each leg of the shell is of generally circular internal cross section and contains a bundle of straight tubes, consisting of the legs of the hairpin tubes, arranged in spaced parallel relation to each other. Such heat exchangers often are of considerable length. It is important that the tubes in the bundle in each leg of the shell be firmly supported relatively to each other and to the shell, but the length of the heat exchanger often makes it impossible to support the tubes in each bundle from only the end at which they are connected to the shell. For this reason, at least one and preferably several spacing means should be located along the length of the bundle to provide the desired support to the tubes.
The spacing means should satisfy several criteria. It should properly space and secure the tubes relatively to each other. It should space and locate the tubes relatively to the shell. It should permit relative longitudinal movement between the tubes and the shell, as can occur due to differences in thermal expansion of the tubes and the shell. It should not impair heat transfer between the fluid in the tubes and the fluid outside of the tubes in the shell, and preferably should increase heat transfer. While performing the above functions, it should not substantially increase the pressure drop on the fluid passing through the shell, since this would increase pumping costs and provide other difliculties. In the event the fluid passing through the shell is of the type which can vaporize under the conditions to which it is subjected in the shell, the spacing means should allow the resultant vapors to pass freely through the shell without vapor binding.
A general object of the invention is the provision of strong, simple and economical spacing means which satisfies the above criteria and provides other advantages. More specific objects include the provision of such spacing means which can be readily manufactured and installed. Other objects include the provision of a heat exchanger embodying such spacing means.
Further objects and advantages of the invention Will be apparent from the following description of a preferred form, reference being made to the accompanying drawings in which,
FIGURE 1 is a side elevation with parts broken away of a preferred form of heat exchanger embodying the invention;
FIGURE la is an enlarged section of the sealing means joining the inner tubes, shell tube, and fluid pipe at one end of one shell tube;
FIGURE 2 is a cross section to an enlarged scale of one leg of the heat exchanger shown in FIGURE 1, the view being taken as indicated by line 2-2 of FIGURE 1;
FIGURE 3 is a side elevation of a portion of a tube bundle of the heat exchanger to the same scale as FIG- URE 2; and
FIGURE 4- is a perspective of a spacer embodying the invention.
As shown in FIGURES 1 and 2 of the drawings, a preferred form of heat exchanger embodying the invention comprises a pair of parallel external or shell tubes and 11. These tubes are connected at their rear ends to a return bend housing 12 having a rear opening surrounded by a flange 13 to which is bolted the cover 14 which closes the opening. The shell tubes may be supported by frame members 15 or by any other convenient means. The forward ends of the shell tubes 10 and 11 are provided with flanges 16 and 17, respectively, to which pipe-connecting fittings 18 and 19 are secured by bolts 21. Fluid is supplied to and discharged from the interior of the shell tubes through the connections 22 and 23 which are welded to the tubes 10 or 11 near the flanges 16 and 17. In the form of the heat exchanger shown in the drawing, the connection 23 is the inlet and connection 22 is the outlet, as indicated by the arrows. It will be understood, however, that the direction of flow through the shell tubes may be reversed if desired.
To provide a path for another fluid or commodity to flow in heat exchange relation to the fluid or commodity within the shell tubes, a plurality of hair pin tubes 25 are disposed in the shell tubes. Each of illustrated tubes 25 comprises two bare straight sections or legs 26 connected by a return bend 27 within the return bend housing 12. In the form of the invention shown in the drawings, seven hairpin tubes are employed, the straight tube sections 26 being arranged in two bundles, one in each shell tube, so that there is one tube section 26' (see FIGURE 2) at the center of each bundle with its axis substantially coincident with that of the shell tube, and six outer tube sections equidistantly and equiangularly spaced around the central tube axis. A greater or lesser number of tubes may be utilized without departing from the invention, although the outer hairpin tubes surrounding the inner tube or tubes are preferably even in number. As shown in FIGURES 1 and 1a, the forward ends of the tubes 26 in each bundle are fixed in a tube sheet 28 which is supported by a split locking ring 29, which is disposed in a groove in the tube sheet 28 and engages an inner flange 30 in the corresponding shell tube 10 or 11, against the force exerted by a sealing ring 31 that is engaged by the corresponding fitting 18 or 19. Bolts 21 hold the fittings 18 and 19 in place and draw them against the sealing rings 31. The rings 31 make sealing engagement with the adjacent tube sheet 28 and the adjacent flange 16 or 17 of the shell tube 10 or 11. Thus, there are fluid tight connections between the interiors of pipes 32 and 33 connected to fittings 18 and 19 and the interiors of hairpin tubes 25, and the spaces within the shell tubes 19 and 11 and surrounding the hairpin tubes are also sealed at the forward end of the heat exchanger, by the rings 31. This type of connection is dis closed in detail and claimed in the copending application of John W. Brown, Jr. and John W. Nevins, Serial No. 32,349, filed May 27, 1960, and owned by the assignee of the present application. Any convenient sealing means may be employed, however, inasmuch as the sealing means forms no part of the present invention.
Pipes 32 and 33 connect the hairpin tubes to an external fluid system. Pipe 32 connected to fitting 18 constitutes the inlet and pipe 33 connected to fitting 19 constitutes the outlet, thus providing for counterflow of the fluids in the illustrated heat exchanger. Obviously the flow can be reversed if desired, and it will be evident that the connecting pipes 32 and 33 and the lateral connec tions 22 and 23 can be arranged to connect a plurality of heat exchanger units such as shown in FIGURE 1 in series or in multiple.
Since the length of the heat exchanger and hence the length of the shell tubes 10 and 11 and the straight sections 26 of the hairpin tubes are great in comparison to the diameters of the tubes, lengths of 20 or more feet with shell tubes of four inches or less in diameter and hairpin tubes of A; inch outside diameter being not uncommon, the tubes in the tube bundles, if unsupported except at the tube sheets, will bend and sag and in many cases will touch each other as well as the wall of the shell tube, resulting in a decrease in heat exchange efficiency, a possible increase .in pressure drop and generally less efficient operation of the exchanger. In order to eliminate these difliculties, the present invention provides supporting and spacing devices 40 for supporting the tubes 26 in proper position with respect to each other and with respect to the surrounding shell tubes and 11. In the illustrated embodiment there are several supporting devices 40 disposed along the length of the bundle of the straight tube sections 26 in each of the shell tubes. One of the supporting devices 40 is shown separately in perspective in FIG- URE 4 and is shown in place and to an enlarged scale in FIGURES 2 and 3.
As illustrated in the drawings, each supporting device or spacer 40 comprises a central member 41 in the form of a short tubular member which is adapted to be mounted on and preferably fixed to the central tube section 26 of the bundle of tubes in each shell tube. The central member 41 supports a set of identical channel members 42 equally spaced about the member 41. A second set of smaller channel members 43, identical to each other, is also mounted on central member 41, the members 43 being alternately disposed relative to members 42.
Each channel member 42 is formed of a piece of sheet metal bent to have two diverging side wall44 connected at the bottom to a narrow base 45 fixed, as by welding, to the exterior of central member 41. Each side wall 44 is wide enough to extend from the outer surface of member 41 to the inner surface of the shell tube 10 or 11. Each smaller channel member 43 of the other group is also formed of a piece of sheet metal bent to have two identical side walls 46 joined to a narrow base 47 fixed as by welding to the exterior of central member 41. The side walls 46 of each member 43 are considerably narrower than the side walls 44 of members 42. The outer edges of side walls 46 being located close to, and preferably in contact with the outer surfaces of the side walls 44 of the channel members 42.
In the preferred embodiment, the cross sectional shape of the channel members 43 is identical to the cross sectional shape of the channel members 42 up to the point where the side walls 44 of channel members 42 are engaged by the outer edges of the side walls 46 of channel members 43. This is shown in FIGURE 2. The channel members 43, and the lower portions of the alternately disposed channel members 42 thus provide identical V- shaped bearing surfaces which contact the straight lengths 26 of the outer tubes in a bundle when the spacer is mounted in place with its central member 41 surrounding the central tube 26'. The outer tubes are preferably held in contact with these surfaces by a band or strap 50 located adjacent to the spacer, as shown in FIGURES 1, 2 and 3. This band or strap may be any conventional type of metal strapping applied in a conventional manner and hence requires no further description.
Spacers of the kind described above may be readily manufactured by preforming strips of metal into long channel members having the cross sections of members 42 and 43, and fixing these long channel-shaped members in the proper alternating relationship on a central tubular member approximately as long as the channel members and having the cross section of member 41 by welding the narrow bottom walls of such channel-shaped members to the outer surface of the central tubular member, preferably in accordance with the method and apparatus disclosed in J. W. Brown, Jr. Patents 2,298,249 and 2,298,250 issued October 6, 1942. The long welded assembly is then cut into short spacer members 40 of the desired length. Although the outer edges of the narrow walls 46 of channel members 43 also could be welded to the wide outer side walls 44 of the channel members 42, this is not necessary as a practical matter because these edges are wedged in place by the forces developed between these edges and 4 the outer surfaces of side walls 44 when the side walls of members 42 and 43 are urged toward the central member 41 by the forces exerted on the side walls by the tubes 26 when the spacer is in place in the heat exchanger.
In the assembly of a heat exchanger embodying spacers 40, the desired number of spacers 40 are slid onto the central straight tube section 26' of each bundle, arranged in the proper and preferably uniformly spaced relation, and if desired are welded to such tube section as shown in FIGURE 2. Thereafter, the straight sections 26 of the outer tubes in the bundle are positioned within the channel members 42 and 43 as shown in FIGURE 2, and the straps 50 are applied. The tube sheet 28 at each end of the tube bundle is then mounted and fixed in place, and the heat exchanger is assembled in the usual manner. During assembly the outer edges of the wide channel members 42 engage the shells 1t) and 11 and facilitate sliding the tube bundles into the shells.
In the assembled heat exchanger the outer tubes are firmly and accurately located relatively to each other and to the central tube by their engagement with the side walls 44 and 46 of the channel members 42 and 43 of the spacers 40, against which side walls they are held by the straps 50 adjacent each spacer. As illustrated in FIG- URE 2, the outer edges of the side walls 44 of the wide channel members 42 engage the inner surfaces of the shells and accurately locate the bundles as a whole relatively to the shells. The walls 44 of channel members 42 and the walls 46 of channel members 43 provide addition heat exchange surfaces which increase transfer of heat between fluid flowing inside of the tubes 25 and the fluid flowing outside of the tubes and inside of the shells. Moreover, the spacing and heat transfer functions of the spacers 40 are provided without substantially increasing the pressure drop on the fluid flowing through the shell outside of the tubes, since all extended surfaces of the spacer are parallel to the direction of fluid flow. These geometrical relationships of the parts of the spacer also permit vapors which might arise from vaporizing type shell fluids to pass freely through the heat exchanger without vapor binding, as could occur with transverse plate type supports. All of these desirable results can be achieved at relatively low cost. The spacers themselves are rugged and have long life.
In the illustrated embodiment, the side walls 44 and 46 of channel members 42 and 43 are flat; this is preferable since it not only facilitates the forming of the channel members on relatively simple equipment but also because it promotes heat transfer by providing space between each channel member and the surface portion of each outer tube which is nearest the central tube. However, if desired, the lower portion of each channel member can be made to conform to the outer surface of the tube, or can be made of other configurations than shown. It is desirable, however, that the portions of the various channel members which contact the tubes be identical so as to provide for the desired equidistant and equiangular spacing of outer tubes of identical cross section in the bundle.
The number of wide channel members 42 should be equal to the number of the narrow channel members 43, since they are alternately disposed; this means that there is an even number of channel shaped bearing surfaces available for supporting outer tubes in a bundle. The number of wide members 42 and of narrow members 43 may, of course, be an odd or even number, but the total number of members 42 and 43 should be an even number which is determined by the number of tubes which it is desired to support by the spacer.
While the illustrated spacer is formed of sheet metal parts welded to a central member, it is apparent that it may be formed of other materials and in other manners. Furthermore, while the spacers of the invention have been disclosed as used in hairpin type heat exchangers having bare tubes, they may be employed to support and space tubes in a bundle in other types of heat exchangers. Moreover, they may be used to support finned tubes in hairpin or other type heat exchangers, as by engaging bare portions of such tubes.
Various changes and modifications in the invention will be apparent to those skilled in the art. It is therefore to be understood that the patent is not limited to the preferred form of the invention disclosed herein or in any manner other than by the scope of the appended claims.
I claim:
1. A heat exchanger comprising an elongated shell; a bundle of elongated heat exchange tubes located in said shell, said tubes being spaced from each other and disposed substantially parallel to each other and to said shell and substantially equiangularly spaced around a central axis; and a spacer engaging said tubes and said shell to locate said tubes with respect to said shell and to each other, comprising a first set of outwardly opening channel members of substantially identical cross section extending longitudinally along and spaced substantially equiangularly about said axis, each of said channel members having outwardly diverging sidewalls, a second set of channel members alternately disposed between the channel members of said first set and extending longitudinally along and disposed substantially equiangularly around said axis, each of said channel members of said second set being of substantially identical cross section and having outwardly diverging sidewalls, the sidewalls of the channel members of said second set terminating adjacent to sidewalls of adjacent channel members of said first set, and means for locating said channel members with respect to each other, each channel member receiving and supporting one of said heat exchange tubes to locate said tubes substantially equiangularly about said axis, and the sidewalls of said channel members in said first set engaging said shell to locate said spacer and said tubes with respect to said shell.
2. A heat exchanger comprising an elongated shell; a plurality of elongated heat exchange tubes of generally circular substantially identical cross section located in said shell in substantially parallel relation and substantially equidistantly and equiangularly spaced from an axis extending longitudinally of said shell; and a spacer engaging said tubes and said shell to locate said tubes with respect to said axis and said shell comprising a first set of channel members of substantially identical cross section extending longitudinally along and spaced substantially equidistantly and equiangularly about said axis, each of said channel members having sidewalls formed of sheet material, a second set of channel members of substantially identical cross section alternately disposed between said channel members of aid first set and extending longitudinally along and spaced substantially equidistantly and equiangularly about said axis, each of said channel members of said second set having outwardly diverging sidewalls formed of sheet material and having their outermost edges in close proximity to adjacent sidewalls of adjacent channel members of said first set, the sidewalls of said channel members of said first set extending outwardly beyond the edges of said channel members of said second set, said channel members of said first and second sets having substantially identical lower portions up to the portions of the walls which are in close proximity, and means for locating said channel members with respect to each other, the lower portion of each of said channel members receiving and bearing against one of said heat exchanger tubes so that all said tubes are located with their axes in substantially parallel relation and substantially equidistantly and equiangularly spaced from said first axis, and the outwardly extending sidewalls of said first set of channel members engaging said shell to locate said spacer and said tubes and said shell.
3. A heat exchanger comprising an elongated shell; a bundle of elongated heat exchange tubes located in said shell, said tubes being disposed substantially parallel to each other and to said shell and substantially equidistantly and equiangularly spaced around a central axis; and a spacer engaging said tubes and said shell to locate said tubes with respect to said axis and said shell comprising a tubular central member, a first set of channel members of substantially identical cross section extending longitudinally along and spaced equiangularly around said central member, each of said channel members having outwardly diverging side walls, and a second set of channel members alternately disposed between the channel members of said first set and extending longitudinally along and disposed equiangularly around said central member, each of said channel members of said second set being of substantially identical cross section and having outwardly diverging side walls, the side walls of the channel members of the second set terminating adjacent to side walls of adjacent channel members of the first set, each channel member receiving and supporting one of said heat exchanger tubes to locate said tubes substantially equidistantly and equiangularly from said central axis, and the side walls of said channel members in said first set engaging said shell to locate said spacer and said tubes with respect to said shell.
4. A heat exchanger comprising an elongated shell; a bundle of elongated heat exchange tubes located in said shell, said tubes being spaced from each other and disposed substantially parallel to each other and to said shell and substantially equidistantly and equiangularly spaced around a central axis; a spacer engaging said tubes and said shell to locate said tubes in said shell comprising a tubular central member, a first set of channel members of substantially identical cross section extending longitudinally along said central member and spaced equiangularly around said central member, each of said channel members having outwardly diverging side walls, and a second set of channel members alternately disposed between the channel members of said first set and extending longitudinally along and disposed equiangularly around said central member, each of said channel members of said second set being of substantially identical cross section and having outwardly diverging side walls, the side Walls of the channel members of the second set terminating adjacent to the side walls of adjacent channel members of the first set, the side walls of said channel members of said first and second sets receiving and supporting one of said heat exchanger tubes to locate said tubes substantially equidistantly and equiangularly from said central axis and the side walls of said channel members in said first set engaging said shell to locate said spacer and said tubes in said shell; and means surrounding said bundle of tubes for holding said tubes in contact with the side walls of the channel members in which the tubes are disposed.
5. A heat exchanger comprising an elongated shell; a plurality of elongated heat exchange tubes of generally circular substantially identical cross section located in said shell in substantially parallel relation and substantially equidistantly and equiangularly spaced from an axis extending longitudinally of said shell; a plurality of spacers disposed at spaced locations along said bundle, each of said spacers engaging said tubes and said shell to locate said tubes in said shell comprising a central member, a first set of channel members of substantially identical cross section supported from and around said central member at locations equidistantly and equiangularly spaced from said axis, each of said channel members having side walls formed of sheet material, and a second set of channel members of substantially identical cross section alternately disposed between said channel members of said first set, supported from and around said central member at locations equidistantly and equiangularly spaced from said axis, each of said channel members. of said second set having outwardly diverging side walls formed of sheet material and having their outermost edges in close proximity to adjacent side walls of adjacent channel members of said first set, the side walls of said channel members of said first set extending outwardly beyond the edges of said channel members of said second set, said channel members of said first and second sets having substantially identical lower portions up to the portions of the walls thereof which are in close proximity, the lower portion of each of said channel members receiving and bearing against one of said heat exchanger tubes so that all said tubes are located with their axes in substantially parallel relation and substantially equidistantly and equiangularly spaced from said first axis, and the outwardly extending side walls of said first set of channel members engage said shell to locate said spacer and said tubes in said shell; and means holding each of said tubes against the lower portion of the channel member of said spacer which receives said tube.
6. A hairpin type heat exchanger comprising an elongated shell of hairpin shape having two straight legs; a plurality of elongated hairpin-shaped heat exchange tubes defining two bundles of straight tube sections each of which bundles is disposed longitudinally in one of the legs of the shell, the tubes in each bundle being of generally circular cross section with one of said tubes located centrally of the bundle and others of substantially identical cross section located in substantially parallel relation to and substantially equidistantly and equiangularly spaced from the axis of the central tube; spacers engaging said tubes in said shell legs to locate said tubes, each of said spacers comprising a tubular central member mounted coaxially on the central tube in a bundle, a first set of channel members of substantially identical cross section supported from and around said central member at locations equidistantly and equiangularly spaced from its axis, each of said channel members having outwardly diverging sheet metal side walls, a second set of channel members of substantially identical cross section alternately disposed between said channel members of said first set, supported from and around said central member at locations equidistantly and equiangularly spaced from its axis, each of said channel members of said second set having outwardly diverging sheet metal side walls the outermost edges of which are in close proximity to the side walls of adjacent channel members of said first set, the side walls of said channel members of said first set extending outwardly beyond the edges of said channel members of said second set, said channel members of said first and second sets having substantially identical lower portions up to the portions of the walls thereof which are in close prox- ,imity, the lower portion of each of said channel members receiving and bearing against one of said heat exchanger tubes other than said central tube in a bundle so that all said tubes are located with their axes in substantially parallel relation and substantially equidistantly and equiangularly spacedfrom the axis of said central tube and the outwardly extending side walls of said first set of channel members engage said shell to locate said spacer and said tubes in said shell; and means holding each of said tubes of a bundle against the lower portion of the channel member of said spacer which receives said tube.
7. A spacer for locating an even number of elongated members of generally circular substantially identical cross section with their axes in substantially parallel relation and substantially equidistantly and equiangularly spaced from the axis of the spacer, said spacer comprising a central member having an axis coincident with the axis of the spacer; a first set of channel members of substantially identical cross section supported from said central member at locations therearound equidistantly and equiangularly spaced from the axis of the spacer, each of said channel members having side walls formed of sheet material; a second set of channel members of substantially identical cross section, alternately disposed between said channel members of said first set and supported from and around said central member at locations equidistantly and equiangularly spaced from the axis of said spacer, each of said channel members of said second set having out- Wardly diverging side Walls formed of sheet material the outermost edges of which side Walls are located in close proximity to adjacent side walls of adjacent channel members of said first set, the side walls of said channel members of said first set extending outwardly a substantial distance beyond the edges of said channel members of said second set, said channel members of said first and second sets having lower portions which are substantially identical in cross section up to the portions thereof at which their side walls are in close proximity, said channel members of said first and second sets being adapted to bear against the elongated members of generally circular cross section.
References Cited in the file of this patent UNITED STATES PATENTS 1,767,652 Daley June 24, 1930 2,804,284 Otten Aug. 27, 1957 FOREIGN PATENTS 480,574 Great Britain Feb. 24, 1938 600,592 Canada June 28, 1960

Claims (1)

1. A HEAT EXCHANGER COMPRISING AN ELONGATED SHELL; A BUNDLE OF ELONGATED HEAT EXCHANGE TUBES LOCATED IN SAID SHELL, SAID TUBES BEING SPACED FROM EACH OTHER AND DISPOSED SUBSTANTIALLY PARALLEL TO EACH OTHER AND TO SAID SHELL AND SUBSTANTIALLY EQUIANGULARLY SPACED AROUND A CENTRAL AXIS; AND A SPACER ENGAGING SAID TUBES AND SAID SHELL TO LOCATE SAID TUBES WITH RESPECT TO SAID SHELL AND TO EACH OTHER, COMPRISING A FIRST SET OF OUTWARDLY OPENING CHANNEL MEMBERS OF SUBSTANTIALLY IDENTICAL CROSS SECTION EXTENDING LONGITUDINALLY ALONG AND SPACED SUBSTANTIALLY EQUIANGULARLY ABOUT SAID AXIS, EACH OF SAID CHANNEL MEMBERS HAVING OUTWARDLY DIVERGING SIDEWALLS, A SECOND SET OF CHANNEL MEMBERS ALTERNATELY DISPOSED BETWEEN THE CHANNEL MEMBERS OF SAID FIRST SET AND EXTENDING LONGITUDINALLY ALONG AND DISPOSED SUBSTANTIALLY EQUIANGULARLY AROUND SAID AXIS, EACH OF SAID CHANNEL MEMBERS OF SAID SECOND SET BEING OF SUBSTANTIALLY IDENTICAL CROSS SECTION AND HAVING OUTWARDLY DIVERGING SIDEWALLS, THE SIDEWALLS OF THE CHANNEL MEMBERS OF SAID SECOND SET TERMINATING ADJACENT TO SIDEWALLS OF ADJACENT CHANNEL MEMBERS OF SAID FIRST SET, AND MEANS FOR LOCATING SAID CHANNEL MEMBERS WITH RESPECT TO EACH OTHER, EACH CHANNEL MEMBER RECEIVING AND SUPPORTING ONE OF SAID HEAT EXCHANGE TUBES TO LOCATE SAID TUBES SUBSTANTIALLY EQUIANGULARLY ABOUT SAID AXIS, AND THE SIDEWALLS OF SAID CHANNEL MEMBERS IN SAID FIRST SET ENGAGING SAID SHELL TO LOCATE SAID SPACER AND SAID TUBES WITH RESPECT TO SAID SHELL.
US178646A 1962-03-09 1962-03-09 Heat exchanger tube supports Expired - Lifetime US3144081A (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4265301A (en) * 1976-04-06 1981-05-05 Anderson James H Heat exchanger support construction
US4285396A (en) * 1979-01-25 1981-08-25 Wachter Associates, Inc. Steam generator tube support system
US4286549A (en) * 1979-12-03 1981-09-01 Foster Wheeler Energy Corporation Steam generator support system
US4456058A (en) * 1982-11-30 1984-06-26 Brown Fintube Company Heat exchanger tube support
US5449037A (en) * 1993-12-08 1995-09-12 Brown Fintube Corporation Heat exchanger tube spacer, separator, and support
US5472047A (en) * 1993-09-20 1995-12-05 Brown Fintube Mixed finned tube and bare tube heat exchanger tube bundle
US20060108108A1 (en) * 2004-11-19 2006-05-25 Naukkarinen Olli P Spirally wound, layered tube heat exchanger and method of manufacture
US20060108107A1 (en) * 2004-11-19 2006-05-25 Advanced Heat Transfer, Llc Wound layered tube heat exchanger
US20090014151A1 (en) * 2007-07-11 2009-01-15 Andreas Capelle Exhaust gas heat exchanger with an oscillationattenuated bundle of exchanger tubes
CN103968691A (en) * 2014-05-27 2014-08-06 高秀志 Longitudinal flow shell pass heat exchanger
US20180266769A1 (en) * 2015-01-19 2018-09-20 Daikin Industries, Ltd. Heat exchanger and method of manufacturing same
US11187471B2 (en) * 2017-06-28 2021-11-30 Holtec International Heat exchanger for severe service conditions

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Publication number Priority date Publication date Assignee Title
US1767652A (en) * 1927-04-23 1930-06-24 Bell & Gossett Co Tube assembly for heat-transfer devices
GB480574A (en) * 1937-07-06 1938-02-24 New Engine Company Ltd Improvements in regenerators for use with external combustion air or gas engines
US2804284A (en) * 1953-04-03 1957-08-27 Griscom Russell Co Heat exchanger
CA600592A (en) * 1960-06-28 K. Davies David Heat exchange apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA600592A (en) * 1960-06-28 K. Davies David Heat exchange apparatus
US1767652A (en) * 1927-04-23 1930-06-24 Bell & Gossett Co Tube assembly for heat-transfer devices
GB480574A (en) * 1937-07-06 1938-02-24 New Engine Company Ltd Improvements in regenerators for use with external combustion air or gas engines
US2804284A (en) * 1953-04-03 1957-08-27 Griscom Russell Co Heat exchanger

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4265301A (en) * 1976-04-06 1981-05-05 Anderson James H Heat exchanger support construction
US4285396A (en) * 1979-01-25 1981-08-25 Wachter Associates, Inc. Steam generator tube support system
US4286549A (en) * 1979-12-03 1981-09-01 Foster Wheeler Energy Corporation Steam generator support system
US4456058A (en) * 1982-11-30 1984-06-26 Brown Fintube Company Heat exchanger tube support
US5472047A (en) * 1993-09-20 1995-12-05 Brown Fintube Mixed finned tube and bare tube heat exchanger tube bundle
US5449037A (en) * 1993-12-08 1995-09-12 Brown Fintube Corporation Heat exchanger tube spacer, separator, and support
US7546867B2 (en) 2004-11-19 2009-06-16 Luvata Grenada Llc Spirally wound, layered tube heat exchanger
US20060108108A1 (en) * 2004-11-19 2006-05-25 Naukkarinen Olli P Spirally wound, layered tube heat exchanger and method of manufacture
US20060108107A1 (en) * 2004-11-19 2006-05-25 Advanced Heat Transfer, Llc Wound layered tube heat exchanger
WO2007076314A2 (en) 2005-12-21 2007-07-05 Luvata Grenada Llc Spirally wound, layered tube heat exchanger and method of manufacture
US20090014151A1 (en) * 2007-07-11 2009-01-15 Andreas Capelle Exhaust gas heat exchanger with an oscillationattenuated bundle of exchanger tubes
US8387684B2 (en) * 2007-07-11 2013-03-05 Visteon Global Technologies, Inc. Exhaust gas heat exchanger with an oscillationattenuated bundle of exchanger tubes
DE102008002430C5 (en) 2007-07-11 2018-03-22 Hanon Systems Exhaust gas heat exchanger with vibration-damped exchanger tube bundle
CN103968691A (en) * 2014-05-27 2014-08-06 高秀志 Longitudinal flow shell pass heat exchanger
US20180266769A1 (en) * 2015-01-19 2018-09-20 Daikin Industries, Ltd. Heat exchanger and method of manufacturing same
US11054187B2 (en) * 2015-01-19 2021-07-06 Daikin Industries, Ltd. Heat exchanger and method of manufacturing same
US11187471B2 (en) * 2017-06-28 2021-11-30 Holtec International Heat exchanger for severe service conditions

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