US3683656A - Heat exchanger apparatus and method of making the same - Google Patents

Heat exchanger apparatus and method of making the same Download PDF

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US3683656A
US3683656A US22491A US3683656DA US3683656A US 3683656 A US3683656 A US 3683656A US 22491 A US22491 A US 22491A US 3683656D A US3683656D A US 3683656DA US 3683656 A US3683656 A US 3683656A
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diameter
fin
tube
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tubular blank
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Carl M Lewis
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Trane US Inc
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Assigned to TRANE COMPANY THE reassignment TRANE COMPANY THE MERGER (SEE DOCUMENT FOR DETAILS). EFFECTIVE 12/1/83 WISCONSIN Assignors: A-S CAPITAL INC., A CORP OF DE (CHANGED TO), TRANE COMPANY THE, A CORP OF WI (INTO)
Assigned to AMERICAN STANDARD INC., A CORP OF DE reassignment AMERICAN STANDARD INC., A CORP OF DE MERGER (SEE DOCUMENT FOR DETAILS). EFFECTIVE 12/28/84 DELAWARE Assignors: A-S SALEM INC., A CORP. OF DE (MERGED INTO), TRANE COMPANY, THE
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21CMANUFACTURE OF METAL SHEETS, WIRE, RODS, TUBES OR PROFILES, OTHERWISE THAN BY ROLLING; AUXILIARY OPERATIONS USED IN CONNECTION WITH METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL
    • B21C37/00Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape
    • B21C37/06Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape of tubes or metal hoses; Combined procedures for making tubes, e.g. for making multi-wall tubes
    • B21C37/15Making tubes of special shape; Making tube fittings
    • B21C37/20Making helical or similar guides in or on tubes without removing material, e.g. by drawing same over mandrels, by pushing same through dies ; Making tubes with angled walls, ribbed tubes and tubes with decorated walls
    • B21C37/207Making helical or similar guides in or on tubes without removing material, e.g. by drawing same over mandrels, by pushing same through dies ; Making tubes with angled walls, ribbed tubes and tubes with decorated walls with helical guides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21DWORKING OR PROCESSING OF SHEET METAL OR METAL TUBES, RODS OR PROFILES WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21D53/00Making other particular articles
    • B21D53/02Making other particular articles heat exchangers or parts thereof, e.g. radiators, condensers fins, headers
    • B21D53/06Making other particular articles heat exchangers or parts thereof, e.g. radiators, condensers fins, headers of metal tubes
    • 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
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00Metal working
    • Y10T29/49Method of mechanical manufacture
    • Y10T29/4935Heat exchanger or boiler making
    • Y10T29/49377Tube with heat transfer means
    • Y10T29/49378Finned tube
    • Y10T29/49382Helically finned

Definitions

  • a shell-and-tube heat exchanger is shown having a bundle of tubes each of which is provided with exter- [2l] Appl. No.: 22,491 nal helical fins except inland portions adjacent tube sheets and supports.
  • the tubes are constructed by first 52 us. (:1 ..'...72/911, 72/100, 29/1573 AH rolling grooves into the tube and reducing the tube 51 1m. (:1.
  • This invention relates to heat exchanger apparatus and the method of making the same. More particularly this invention relates to shell-and-tube type heat exchangers and specifically the tubes thereof and the method of making them.
  • the finning dies are only useful in those transition areas where the finning dies are first engaged with the heat exchanger tube.
  • the sizing die is simultaneously disengaged from the tube thereby yielding an area which is not sized. Therefore, the finning dies must be of such configuration as to form fins of a diameter no greater than the land portions except in those transition areas where the finning dies are first engaged with the heat exchanger tube surface.
  • the instant invention contemplates a different method of reducing the diameter of the finned portions.
  • the fins are reduced in diameter without materially shortening their protruding extent.
  • the reduction in fin diameter may be accomplished entirely along the finned portions of the tube rather than just in the transition areas heretofore described.
  • FIG. 1 is a vertical section through a shell and tube type heat exchanger having tubes therein constructed in accordance with the teachings of this invention
  • FIG. 2 is a section taken at line 2-2 of FIG. 3 which illustrates the apparatus and method for forming heat exchanger tubes in accordance with the teachings of this invention.
  • FIG. 3 is a section taken at line 3-3 of FIG. 2.
  • FIG. 1 of the drawings it will be seen that-shell and tube type heat exchanger 10 has a cylindrical shell with tube sheets 12 at each end thereof.
  • An appropriate tube support 13 may be located intermediate tube sheets 12 for supporting heat exchanger tubes 14 therebetween.
  • Tube sheets 12 and tube support 13 are provided with apertures 15 in which thetubes 14 are received.
  • Each tube 14 has a plurality of integrally helically finned portions 16 axially nonextensive with the land portions 17.
  • the land portions 17 are positioned to be axially coextensive with the tube sheets and tube supports for the purpose of establishing a good support at tube sheet 13 and a good seal at tube sheets 12. If desired the tubes 14 may be roll expanded slightly within the tube sheets to provide the desired seal.
  • the shell-and-tube heat exchanger 10 is provided with inlet 18 such as for the ingress of a liquid refrigerant and an outlet 19 such as for the egress of a gaseous refrigerant.
  • the heat exchanger also has inlet and outlet headers 20 and 21 communicating with the interior of tubes 14 for passing a second heat exchange fluid such as water therethrough in heat exchange relationship with the heat exchange fluid passing external to heat exchanger tubes 14.
  • the fins may be formed on heat exchanger tubes 14 by a fin forming head 22 shown in FIGS. 2 and 3.
  • Head 22 is comprised of an annular member 31 having provision for supporting a set of three circumferentially spaced leading roll assemblies 23, 24 and 25 and a set of three circumferentially spaced trailing roller assemblies'26, 27 and 28.
  • the roller assemblies 23, 24 and 25 are generally similar in construction.
  • Roller assembly 23 has a U-shaped frame 29 which is mounted for radial adjustment with respect to tube 14 in a groove 30 of annular member 31.
  • An arbor 32 extends between and is joumaled at the ends of the legs of U-shape frame 29.
  • Arbor 32 carries a set of roller dies 33 for grooving tube 14 and roll extruding fins 42 up from the surface of tube 14. Arbor 32 is disposed at a slight skew so that the dies 33 thread themselves and advance along tube 14. A screw adjustment 34 is provided for moving frame 29 and thus dies 33 radially inwardly and outwardly with respect to tube 14.
  • Each trailing roller assembly also has a U-shaped frame 35 supported in a groove 36 in annular member 31.
  • An arbor 37 is joumaled at the ends of the legs of U-shaped member 35 and supports a training roller 38.
  • the roller 38 of trailing roller assembly 26 is somewhat smaller in diameter and is provided with a curved surface 39 adapted to contact and apply pressure to the lateral side of the fins 42 thereby bending them over in a common direction toward one end of the tube 14.
  • a screw adjustment 40 is provided to adjust the position of U-shaped members 35 and thus each roller 38 radially inwardly and outwardly with respect to tube 14 in grooves 36.
  • a mandrel 41 may be disposed within tube 14 or may be disposed in axially fixed relationship with fin forming head 22.
  • a tubular blank 14 is inserted into annular member 31 a distance beyond roller dies 33 sufiicient to provide for the land portions of the tube adjacent one end of the tube.
  • the tube then is advanced axially with respect to the fin forming head in the direction shown by the vectors in FIG. 2 and rotated with respect to the fin forming head 22 in the direction shown by the vectors in FIG. 3.
  • roller dies 33 are brought into engagement with the surface of tube 14 by adjustment of screws 34 whereby an erect fin 42 is formed which extends substantially beyond the diameter or profile a of the unfinned or land portions of tube 14.
  • rollers 38 are adjusted radially inwardly to engagement with the sides of fins 42 by adjustment screws 40.
  • the roller 38 of roller assembly 26 which is provided with the curved surface 39 applies lateral pressure on the erect fin 42 thereby causing it to be bent over and reduced to a diameter d which is equal to or less than diameter a.
  • roller dies 33 are adjusted radially outwardly with respect to tube 14 by means of screw adjustments 34 until roller dies 33 no longer engage the surface of tube 14.
  • rollers 38 continue to bend over the remaining fins until rollers 38 approach the land area at which point rollers 38 are adjusted radially outwardly by means of screw adjustments 40 so that rollers 38 also clear the surface 17 of tube 14.
  • screw adjustments 40 so that rollers 38 also clear the surface 17 of tube 14.
  • roller dies 33 form slight grooves in the surface of tube 14 and reduce its diameter sufficiently so that the internal surface of tube 14 contacts mandrel 41. Further advancement of tube 14 through dies 33 causes the material between the grooves to be extruded outwardly substantially beyond the original diameter of the tube whereby a relatively erect and high fin is produced.
  • This fin upon coming in contact with surface 39 of a roller 38 is bent over by application of lateral pressure at the side' of the fins thereby reducing the diameter of the fins to less than about the original outer tube diameter a.
  • the original tube diameter, the land diameter or tube sheet or support aperture diameter a is substantially greater than the sum of the fin root diameter b and twice the fin height or protrusion curvilinear length 0 and equal to or greater than the bent fin outer diameter.
  • an exemplary evaporator tube of approximately 0.750 inch diameter and having about 0.035 inch high fins with a fin density of about 35 fins per inch it is possible by the use of the invention disclosed herein to either increase the fin height by about 25 percent or increase the tube internal cross-sectional area by about 6 percent without increases in the original tube diameter, the land diameter or tube sheet or support aperture diameter. Variations will, of course, exist for tubes of different diameter, fin height, fin density etc.
  • a method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank having a generally circular cross-section of a predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter; reducing the diameter of said fully developed helical fin to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step and to a diameter less than said aperture predetermined diameter by applying lateral force to one side of the helix of said helical fin axially of said tubular blank to cause said helical fin to bend over and thereby be reduced in diameter.
  • a method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank of generally circular crosssection of predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of only a portion of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter and leaving at least one'unfinned land portion; reducing the diameter of the fully developed finned portion to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step, to less than said aperture predetermined diameter, and to about the diameter of said land portion by bending said helical fin over; and from the step of extruding the helical fin to the step of bending the fin over, maintaining the inner diameter-of the span of tubular blank with the extruded bent over fin at substantially the inner diameter of said span existing immediately following the extruding
  • a method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank of generally circular crosssectiori of predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of only a portion of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter and leaving at least one unfinned land portion; reducing the diameter of the finned portion to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step, to less than said aperture predetermined diameter, and to about the diameter of said land portion by applying sufficient lateral force to one side of the helix of said helical fin axially of said tubular blank to cause said helical fin to bend over and thereby be reduced in diameter to about the diameter of said land portion; and from the step of extruding the helical fin to the step
  • a method of providing a tubular blank of a predetermined outer diameter with an extended heat transfer surface in the form of integral helical fins and adapted to be supported in a tube support aperture of predetermined diameter including the steps of: applying radially inward pressure on the outer surfaceof said tubular blank along a helicoidal path to thereby displace the material of said tubular blank causing a general reducing in outer diameter of the tubular blank and a helicoidal groove to be formed in the surface thereof; applying suflicient laterial pressure to the sides of said groove to displace the material between convolutions of said groove radially outward substantially beyond said predetermined diameter thereby forming a fully developed helicoidal fin having a diameter larger than said predetermined outer diameter and greater than s d a erture redetermined di ete a d a l ing sufiicieiit lateral?

Abstract

A shell-and-tube heat exchanger is shown having a bundle of tubes each of which is provided with external helical fins except in land portions adjacent tube sheets and supports. The tubes are constructed by first rolling grooves into the tube and reducing the tube diameter, then roll extruding fins up from the surface of decreased diameter to a diameter larger than the land portions of the tube and larger than the tube apertures in the tube sheets and supports of the heat exchanger, and finally rolling portions of the fins partially over toward an adjacent fin in a common axial direction to reduce the outer diameter of the fins so that the tube can be passed through the tube apertures of the tube sheets and supports. The rolling over of the fins is accomplished by applying lateral pressure on the fins through the use of a trailing roll-over die. Means is provided for radially withdrawing the groove forming and fin extruding dies from the surface of the tube without an equal withdrawal of the trailing roll-over die whereby all fins exceeding the desired diameter may be bent over to establish the desired fin diameter.

Description

United States Patent 1151 3,683,656 Lewis 1451 Aug. 15, 1972 [54] HEAT EXCHANGER APPARATUS AND Primary Examiner-Richard .I. Herbst METHOD OF MAKING THE SAME AttorneyArthur 0. Andersen and Carl M Lewis [72] Inventor: Carl M. Lewis, c/o The Trane Co.,
LaCrosse, Wis. 54 01 ABSTRACT [22] i 25 70 A shell-and-tube heat exchanger is shown having a bundle of tubes each of which is provided with exter- [2l] Appl. No.: 22,491 nal helical fins except inland portions adjacent tube sheets and supports. The tubes are constructed by first 52 us. (:1 ..'...72/911, 72/100, 29/1573 AH rolling grooves into the tube and reducing the tube 51 1m. (:1. ..B2ld 53/06 diameter, roll extruding fins p from the Surface [58] Field of S h, 29/]57 3 57 3 A, 57 3 of decreased diameter to a diameter larger than the 72 93 land portions of the tube and larger than the tube apertures in the tube sheets and supports of the heat [56] References Cited exchanger, and finally rolling portions of the fins partially over toward an adjacent fin in a common axial UNITED STATES PATENTS direction to reduce the outer diameter of the fins so 2 362 694 11/1944 11111 ..29/157.3 A the tube be Peesed hreugh the tube apertures 3 383 892 5/1968 Brothen ..72/9s ef the tube Sheets and suPPefls- The Yelling ever 0f 2 978 797 4/1961 Ekelund ..29/157.3 A the fins is eeeempliehed by applying lateral Pressure 3,174,319 3/1965 Koyana at a]. 29/1573 A on the fins through the use of a trailing roll-over die. 3 602 027 8/1971 Klug et al. ..72/98 Means is Pmided fer radially withdrawing the greeve forming and fin extruding dies from the surface of the FOREIGN PATENTS OR APPLICATIONS tube without an equal withdrawal of the trailing rollover die whereby all fins exceeding the desired diamel27,873 6/1948 Austraha ..29/l57.3A ter may be bent Over to establish the desired fin diameter.
4 Claims, 3 Drawing Figures HEAT EXCHANGER APPARATUS AND METHOD OF MAKING THE SAME This invention relates to heat exchanger apparatus and the method of making the same. More particularly this invention relates to shell-and-tube type heat exchangers and specifically the tubes thereof and the method of making them.
It is now common practice to provide integral helical fins on heat exchanger tubes which are installed in shell-and-tube type heat exchangers. The tube sheets and tube supports insuch heat exchangers have apertures through which the heat exchanger tubes are inserted during installation. In certain types of heat exchangers, such as refrigerant evaporators, it is common practice to provide the tubes with an integral external helical fin in those areas intermediate the tube sheets and tube supports. A land or unfinned portion is generally left in the area of contact with the tube sheets and tube supports. Because the tubes are normally finned prior to installation within such a heat exchanger, it is common practice to form fins which have a diameter substantially no greater than the diameter of the land portions or diameter of the tube apertures within the tube sheets and supports. This is accomplished by forming the fins substantially entirely into the tube rather than by extruding the fins out from the original surface of the tube. However, it must be recognized that in forming the fins substantially entirely into the tube, the tube internal diameter is materially reduced thereby increasing its resistance to fluid flow therethrough.
It has been recognized, such as in U.S. Pat. No. 3 ,383,892, that in forming helical fins in this manner on the external surface of heat exchanger tubes, a transition condition may exist wherein the fins may extend radially beyond the land portions of the tube in those areas where the finning dies are first engaged with the tube surface. By providing a fin sizing die on the fin forming roller assembly it is possible to shorten the fins in this transition area thereby permitting the tube to be inserted through the apertures within the tube sheets and tube supports of a shell-and-tube type heat exchanger. The device as disclosed in this patent has the disadvantage of shortening the heat exchanger fins. Furthermore, it is only useful in those transition areas where the finning dies are first engaged with the heat exchanger tube. Thus note that as the finning dies are disengaged from the tube, the sizing die is simultaneously disengaged from the tube thereby yielding an area which is not sized. Therefore, the finning dies must be of such configuration as to form fins of a diameter no greater than the land portions except in those transition areas where the finning dies are first engaged with the heat exchanger tube surface.
The instant invention contemplates a different method of reducing the diameter of the finned portions. In the instant invention the fins are reduced in diameter without materially shortening their protruding extent. Furthermore, the reduction in fin diameter may be accomplished entirely along the finned portions of the tube rather than just in the transition areas heretofore described. Thus it is possible to reduce the diameter of integral helical fins which generally throughout their longitudinal extend along a heat exchanger tube protrude beyond the profile of the land portions of said tube. This is accomplished in the instant invention by rolling grooves into the tube and reducing the tube diameter, then roll extruding the fins up from the surface of decreased diameter to a diameter larger than that of the land portions of the tube and larger than that of the tube apertures in the tube sheets and supports, and finally bending over the outer portions of the fins toward an adjacent fin in a common axial direction to reduce the outer diameter of the fins so that the tube can be passed through the tube apertures of the tube sheets and tube supports,
It is thus an object of this invention to provide a method of reducing the diameter of an external integral helical fin on a heat exchanger tube to or less than the diameter of the unfinned portions of the heat exchanger tube or to or less than the diameter of the apertures in tube sheets or tube supports through which the tube must be inserted.
It is a further object of this invention to provide a method of increasing the internal diameter of a tube without increasing the diameter of the external helical fins thereon beyond the diameter of the land portions thereof or the diameter of the apertures within the tube sheets or tube supports through which the tube must be inserted.
It is a further object of this invention to provide a heat exchanger tube of increased internal diameter.
And it is still a further object of this invention to provide a heat exchanger tube with increased fin surface for a given fin density and height and a given land diameter.
Other objects and advantages will become apparent as this specification proceeds to describe the invention with reference to the drawings in which;
FIG. 1 is a vertical section through a shell and tube type heat exchanger having tubes therein constructed in accordance with the teachings of this invention, and
FIG. 2 is a section taken at line 2-2 of FIG. 3 which illustrates the apparatus and method for forming heat exchanger tubes in accordance with the teachings of this invention, and
FIG. 3 is a section taken at line 3-3 of FIG. 2.
Now referring to FIG. 1 of the drawings it will be seen that-shell and tube type heat exchanger 10 has a cylindrical shell with tube sheets 12 at each end thereof. An appropriate tube support 13 may be located intermediate tube sheets 12 for supporting heat exchanger tubes 14 therebetween. Tube sheets 12 and tube support 13 are provided with apertures 15 in which thetubes 14 are received.
Each tube 14 has a plurality of integrally helically finned portions 16 axially nonextensive with the land portions 17. The land portions 17 are positioned to be axially coextensive with the tube sheets and tube supports for the purpose of establishing a good support at tube sheet 13 and a good seal at tube sheets 12. If desired the tubes 14 may be roll expanded slightly within the tube sheets to provide the desired seal.
The shell-and-tube heat exchanger 10 is provided with inlet 18 such as for the ingress of a liquid refrigerant and an outlet 19 such as for the egress of a gaseous refrigerant. The heat exchanger also has inlet and outlet headers 20 and 21 communicating with the interior of tubes 14 for passing a second heat exchange fluid such as water therethrough in heat exchange relationship with the heat exchange fluid passing external to heat exchanger tubes 14.
The specific details of the heat exchanger tubes 14 and their method of construction will be more clearly understood by reference to FIGS. 2 and 3.
The fins may be formed on heat exchanger tubes 14 by a fin forming head 22 shown in FIGS. 2 and 3. Head 22 is comprised of an annular member 31 having provision for supporting a set of three circumferentially spaced leading roll assemblies 23, 24 and 25 and a set of three circumferentially spaced trailing roller assemblies'26, 27 and 28. The roller assemblies 23, 24 and 25 are generally similar in construction. Roller assembly 23 has a U-shaped frame 29 which is mounted for radial adjustment with respect to tube 14 in a groove 30 of annular member 31. An arbor 32 extends between and is joumaled at the ends of the legs of U-shape frame 29. Arbor 32 carries a set of roller dies 33 for grooving tube 14 and roll extruding fins 42 up from the surface of tube 14. Arbor 32 is disposed at a slight skew so that the dies 33 thread themselves and advance along tube 14. A screw adjustment 34 is provided for moving frame 29 and thus dies 33 radially inwardly and outwardly with respect to tube 14.
Each trailing roller assembly also has a U-shaped frame 35 supported in a groove 36 in annular member 31. An arbor 37 is joumaled at the ends of the legs of U-shaped member 35 and supports a training roller 38. The roller 38 of trailing roller assembly 26 is somewhat smaller in diameter and is provided with a curved surface 39 adapted to contact and apply pressure to the lateral side of the fins 42 thereby bending them over in a common direction toward one end of the tube 14. A screw adjustment 40 is provided to adjust the position of U-shaped members 35 and thus each roller 38 radially inwardly and outwardly with respect to tube 14 in grooves 36. It should be appreciated that in the case of a single lead fin, only one of rollers 38 need have a curve surface 39 although more than one of rollers 38 could have a curved surface 39. In the case of a multiple lead fin, it may be necessary that the complete bend-over operation for a single fin be performed by a single roller. The screw adjustments 34 and 40 are independent whereby U-shaped frame 29 and thus roller dies 33 may be withdrawn from the surface of tube 14 without affecting the operation of rollers 38. This enables all the fins 42 of tube 14 to be bent over despite their location on the tube 14.
In order to operate the fin forming head a mandrel 41 may be disposed within tube 14 or may be disposed in axially fixed relationship with fin forming head 22. In any event, a tubular blank 14 is inserted into annular member 31 a distance beyond roller dies 33 sufiicient to provide for the land portions of the tube adjacent one end of the tube. The tube then is advanced axially with respect to the fin forming head in the direction shown by the vectors in FIG. 2 and rotated with respect to the fin forming head 22 in the direction shown by the vectors in FIG. 3. Simultaneously the roller dies 33 are brought into engagement with the surface of tube 14 by adjustment of screws 34 whereby an erect fin 42 is formed which extends substantially beyond the diameter or profile a of the unfinned or land portions of tube 14. When the fins have advanced to rollers 38, rollers 38 are adjusted radially inwardly to engagement with the sides of fins 42 by adjustment screws 40. The roller 38 of roller assembly 26 which is provided with the curved surface 39 applies lateral pressure on the erect fin 42 thereby causing it to be bent over and reduced to a diameter d which is equal to or less than diameter a. As the roller dies 33 approach an intended land portion 17, roller dies 33 are adjusted radially outwardly with respect to tube 14 by means of screw adjustments 34 until roller dies 33 no longer engage the surface of tube 14. However, rollers 38 continue to bend over the remaining fins until rollers 38 approach the land area at which point rollers 38 are adjusted radially outwardly by means of screw adjustments 40 so that rollers 38 also clear the surface 17 of tube 14. The same procedure may be used in forming the second finned portion of tube 14.
There will be seen in FIG. 2 that in the process just described, roller dies 33 form slight grooves in the surface of tube 14 and reduce its diameter sufficiently so that the internal surface of tube 14 contacts mandrel 41. Further advancement of tube 14 through dies 33 causes the material between the grooves to be extruded outwardly substantially beyond the original diameter of the tube whereby a relatively erect and high fin is produced. This fin, upon coming in contact with surface 39 of a roller 38 is bent over by application of lateral pressure at the side' of the fins thereby reducing the diameter of the fins to less than about the original outer tube diameter a. Thus it will be seen that the original tube diameter, the land diameter or tube sheet or support aperture diameter a is substantially greater than the sum of the fin root diameter b and twice the fin height or protrusion curvilinear length 0 and equal to or greater than the bent fin outer diameter. On an exemplary evaporator tube of approximately 0.750 inch diameter and having about 0.035 inch high fins with a fin density of about 35 fins per inch it is possible by the use of the invention disclosed herein to either increase the fin height by about 25 percent or increase the tube internal cross-sectional area by about 6 percent without increases in the original tube diameter, the land diameter or tube sheet or support aperture diameter. Variations will, of course, exist for tubes of different diameter, fin height, fin density etc.
Having now described the preferred method and apparatus for practicing my invention, 1 contemplate that many changes may be made without departing from the scope or spirit of my invention and I accordingly desire to be limited only by the claims.
I claim:
1. A method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank having a generally circular cross-section of a predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter; reducing the diameter of said fully developed helical fin to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step and to a diameter less than said aperture predetermined diameter by applying lateral force to one side of the helix of said helical fin axially of said tubular blank to cause said helical fin to bend over and thereby be reduced in diameter.
2. A method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank of generally circular crosssection of predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of only a portion of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter and leaving at least one'unfinned land portion; reducing the diameter of the fully developed finned portion to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step, to less than said aperture predetermined diameter, and to about the diameter of said land portion by bending said helical fin over; and from the step of extruding the helical fin to the step of bending the fin over, maintaining the inner diameter-of the span of tubular blank with the extruded bent over fin at substantially the inner diameter of said span existing immediately following the extruding step.
3. A method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank of generally circular crosssectiori of predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of only a portion of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter and leaving at least one unfinned land portion; reducing the diameter of the finned portion to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step, to less than said aperture predetermined diameter, and to about the diameter of said land portion by applying sufficient lateral force to one side of the helix of said helical fin axially of said tubular blank to cause said helical fin to bend over and thereby be reduced in diameter to about the diameter of said land portion; and from the step of extruding the helical fin to the step of bending the fin over, maintaining the inner diameter of the span of tubular blank with the extruded bent over fin at substantially the inner diameter of said span existing immediately following the extruding step.
4. A method of providing a tubular blank of a predetermined outer diameter with an extended heat transfer surface in the form of integral helical fins and adapted to be supported in a tube support aperture of predetermined diameter including the steps of: applying radially inward pressure on the outer surfaceof said tubular blank along a helicoidal path to thereby displace the material of said tubular blank causing a general reducing in outer diameter of the tubular blank and a helicoidal groove to be formed in the surface thereof; applying suflicient laterial pressure to the sides of said groove to displace the material between convolutions of said groove radially outward substantially beyond said predetermined diameter thereby forming a fully developed helicoidal fin having a diameter larger than said predetermined outer diameter and greater than s d a erture redetermined di ete a d a l ing sufiicieiit lateral? pressure to one i de of saiii gr t e to cause said helicoidal fin to be bent over sufiiciently to reduce the diameter of said fin to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the step of fully developing the helical fin, to less than said aperture predetermined diameter, to about said predetermined outer diameter; and from the step of fully developing the helical fin to the step of bending the fin over, maintaining the inner diameter of the span of tubular blank with the fully developed and bent over fin at substantially the inner diameter of said span existing immediately following the step of fully developing the helical fin.

Claims (4)

1. A method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank having a generally circular cross-section of a predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter; reducing the diameter of said fully developed helical fin to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step and to a diameter less than said aperture predetermined diameter by applying lateral force to one side of the helix of said helical fin axially of said tubular blank to cause said helical fin to bend over and thereby be reduced in diameter.
2. A method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank of generally circular cross-section of predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of only a portion of said tubular blank to a diameter grEater than said predetermined outer diameter and greater than said aperture predetermined diameter and leaving at least one unfinned land portion; reducing the diameter of the fully developed finned portion to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step, to less than said aperture predetermined diameter, and to about the diameter of said land portion by bending said helical fin over; and from the step of extruding the helical fin to the step of bending the fin over, maintaining the inner diameter of the span of tubular blank with the extruded bent over fin at substantially the inner diameter of said span existing immediately following the extruding step.
3. A method of making a heat exchanger tube adapted to be supported in a tube support aperture of predetermined diameter comprising the steps of: providing a tubular blank of generally circular cross-section of predetermined outer diameter which is no greater than said aperture predetermined diameter; forming an extended heat transfer surface by extruding a fully developed helical fin up from the outer surface of only a portion of said tubular blank to a diameter greater than said predetermined outer diameter and greater than said aperture predetermined diameter and leaving at least one unfinned land portion; reducing the diameter of the finned portion to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the extruding step, to less than said aperture predetermined diameter, and to about the diameter of said land portion by applying sufficient lateral force to one side of the helix of said helical fin axially of said tubular blank to cause said helical fin to bend over and thereby be reduced in diameter to about the diameter of said land portion; and from the step of extruding the helical fin to the step of bending the fin over, maintaining the inner diameter of the span of tubular blank with the extruded bent over fin at substantially the inner diameter of said span existing immediately following the extruding step.
4. A method of providing a tubular blank of a predetermined outer diameter with an extended heat transfer surface in the form of integral helical fins and adapted to be supported in a tube support aperture of predetermined diameter including the steps of: applying radially inward pressure on the outer surfaceof said tubular blank along a helicoidal path to thereby displace the material of said tubular blank causing a general reducing in outer diameter of the tubular blank and a helicoidal groove to be formed in the surface thereof; applying sufficient laterial pressure to the sides of said groove to displace the material between convolutions of said groove radially outward substantially beyond said predetermined diameter thereby forming a fully developed helicoidal fin having a diameter larger than said predetermined outer diameter and greater than said aperture predetermined diameter; and applying sufficient lateral pressure to one side of said groove to cause said helicoidal fin to be bent over sufficiently to reduce the diameter of said fin to a diameter less than the outer diameter of said fully developed helical fin existing immediately following the step of fully developing the helical fin, to less than said aperture predetermined diameter, to about said predetermined outer diameter; and from the step of fully developing the helical fin to the step of bending the fin over, maintaining the inner diameter of the span of tubular blank with the fully developed and bent over fin at substantially the inner diameter of said span existing immediately following the step of fully developing the helical fin.
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Cited By (13)

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DE2803365A1 (en) * 1977-01-26 1978-07-27 Zaklad Doswiadczalny Przy Zakl METHOD AND APPARATUS FOR MANUFACTURING CROSS-FIBED PIPES
DE2735762A1 (en) * 1977-08-09 1979-02-22 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
DE2758527A1 (en) * 1977-12-28 1979-07-05 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
EP0012382A1 (en) * 1978-12-06 1980-06-25 Zaklad Doswiadczalny przy Zakladach Urzadzen Chemicznych "Metalchem" Rolling mill for manufacturing finned tubes
US4313248A (en) * 1977-02-25 1982-02-02 Fukurawa Metals Co., Ltd. Method of producing heat transfer tube for use in boiling type heat exchangers
EP0121252A2 (en) * 1983-03-31 1984-10-10 Zaklady Urzadzen Chemicznych METALCHEM im. Wladyslawa Planetorza A method of rolling transverse ribbed tubes and a set of tools for rolling transverse ribbed tubes
US4612791A (en) * 1984-06-19 1986-09-23 Zaklady Urzadzen Chemicznych Metalchem Method and apparatus for rolling transversely ribbed bimetallic pipes
FR2590816A1 (en) * 1985-12-02 1987-06-05 Carrier Corp PROCESS AND APPARATUS FOR MANUFACTURING EXTENDED EXTERIOR SURFACE TUBES WITH MULTI-HELICOIDAL FIN FLOWS, ESPECIALLY FOR HEAT EXCHANGER EVAPORATOR TUBES
GB2218359A (en) * 1988-05-13 1989-11-15 Mars Di Renzo Giovanni Tomezzo Manufacturing finned tubes
US4901553A (en) * 1987-06-03 1990-02-20 Sumitomo Metal Industries, Ltd. Method of manufacturing a finned tube
WO1990010513A1 (en) * 1989-03-13 1990-09-20 Belorussky Politekhnichesky Institut Machine tool for cutting out transverse ribs on a rectangular cross-section element for heat exchanger
US6382311B1 (en) 1999-03-09 2002-05-07 American Standard International Inc. Nucleate boiling surface
US6427767B1 (en) 1997-02-26 2002-08-06 American Standard International Inc. Nucleate boiling surface

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US2362694A (en) * 1942-02-02 1944-11-14 Calumet And Hecla Cons Copper Method of manufacturing tubes for heat exchange devices
US2978797A (en) * 1954-02-22 1961-04-11 Svenska Metallverken Ab Tubular finned metal sections and manufacture thereof
US3174319A (en) * 1962-01-05 1965-03-23 Nihon Kentetsu Company Ltd Method and apparatus for manufacturing integrally finned tubing
US3383892A (en) * 1965-08-13 1968-05-21 Anaconda American Brass Co Manufacture of integrally finned tubing
US3602027A (en) * 1969-04-01 1971-08-31 Trane Co Simultaneous finning and reforming of tubular heat transfer surface

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US2362694A (en) * 1942-02-02 1944-11-14 Calumet And Hecla Cons Copper Method of manufacturing tubes for heat exchange devices
US2978797A (en) * 1954-02-22 1961-04-11 Svenska Metallverken Ab Tubular finned metal sections and manufacture thereof
US3174319A (en) * 1962-01-05 1965-03-23 Nihon Kentetsu Company Ltd Method and apparatus for manufacturing integrally finned tubing
US3383892A (en) * 1965-08-13 1968-05-21 Anaconda American Brass Co Manufacture of integrally finned tubing
US3602027A (en) * 1969-04-01 1971-08-31 Trane Co Simultaneous finning and reforming of tubular heat transfer surface

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2378584A1 (en) * 1977-01-26 1978-08-25 Zaklad Doswiadczalny Przy Zakl PROCESS FOR MANUFACTURING TRANSVERSAL FINNED TUBES AND TOOL FOR MANUFACTURING SUCH TUBES
US4153982A (en) * 1977-01-26 1979-05-15 Zaklad Doswiadczaln przy Zakladach Urzadzen Chemicznych "Metalchem" Method and apparatus for forming cross ribbed pipes
DE2803365A1 (en) * 1977-01-26 1978-07-27 Zaklad Doswiadczalny Przy Zakl METHOD AND APPARATUS FOR MANUFACTURING CROSS-FIBED PIPES
US4313248A (en) * 1977-02-25 1982-02-02 Fukurawa Metals Co., Ltd. Method of producing heat transfer tube for use in boiling type heat exchangers
DE2735762A1 (en) * 1977-08-09 1979-02-22 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
DE2758527A1 (en) * 1977-12-28 1979-07-05 Wieland Werke Ag FIBER TUBE AND THE METHOD AND DEVICE FOR THE PRODUCTION THEREOF
EP0012382A1 (en) * 1978-12-06 1980-06-25 Zaklad Doswiadczalny przy Zakladach Urzadzen Chemicznych "Metalchem" Rolling mill for manufacturing finned tubes
EP0121252A3 (en) * 1983-03-31 1987-05-27 Zaklady Urzadzen Chemicznych Metalchem Im. Wladyslawa Planetorza A method of rolling transverse ribbed tubes and a set of tools for rolling transverse ribbed tubes
EP0121252A2 (en) * 1983-03-31 1984-10-10 Zaklady Urzadzen Chemicznych METALCHEM im. Wladyslawa Planetorza A method of rolling transverse ribbed tubes and a set of tools for rolling transverse ribbed tubes
US4612791A (en) * 1984-06-19 1986-09-23 Zaklady Urzadzen Chemicznych Metalchem Method and apparatus for rolling transversely ribbed bimetallic pipes
FR2590816A1 (en) * 1985-12-02 1987-06-05 Carrier Corp PROCESS AND APPARATUS FOR MANUFACTURING EXTENDED EXTERIOR SURFACE TUBES WITH MULTI-HELICOIDAL FIN FLOWS, ESPECIALLY FOR HEAT EXCHANGER EVAPORATOR TUBES
US4901553A (en) * 1987-06-03 1990-02-20 Sumitomo Metal Industries, Ltd. Method of manufacturing a finned tube
US4959985A (en) * 1987-06-03 1990-10-02 Sumitomo Metal Industries Ltd. Method of manufacturing metallic tube with spiral fin
GB2218359A (en) * 1988-05-13 1989-11-15 Mars Di Renzo Giovanni Tomezzo Manufacturing finned tubes
GB2218359B (en) * 1988-05-13 1992-10-21 Mars Di Renzo Giovanni Tomezzo A method of manufacturing finned tubes having a high heat exchange factor.
WO1990010513A1 (en) * 1989-03-13 1990-09-20 Belorussky Politekhnichesky Institut Machine tool for cutting out transverse ribs on a rectangular cross-section element for heat exchanger
US6427767B1 (en) 1997-02-26 2002-08-06 American Standard International Inc. Nucleate boiling surface
US6382311B1 (en) 1999-03-09 2002-05-07 American Standard International Inc. Nucleate boiling surface

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