US3173481A - Heat exchanger - Google Patents

Heat exchanger Download PDF

Info

Publication number
US3173481A
US3173481A US225561A US22556162A US3173481A US 3173481 A US3173481 A US 3173481A US 225561 A US225561 A US 225561A US 22556162 A US22556162 A US 22556162A US 3173481 A US3173481 A US 3173481A
Authority
US
United States
Prior art keywords
tubes
core
fluid
exchanger
casing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US225561A
Inventor
Howard J Barkley
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Modine Manufacturing Co
Original Assignee
Modine Manufacturing Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Modine Manufacturing Co filed Critical Modine Manufacturing Co
Priority to US225561A priority Critical patent/US3173481A/en
Application granted granted Critical
Publication of US3173481A publication Critical patent/US3173481A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • 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
    • F28D7/16Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
    • F28D7/1684Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits having a non-circular cross-section
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • 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
    • Y10S165/405Extending in a longitudinal direction

Definitions

  • Heat exchangers having two separate and enclosed passes are well known in the art, such that the two fluids in the respective passes are completely contained for circulation through the exchanger.
  • the ethciency of an exchanger of this type is dependent upon the pressure drop of the fluid pressure in the exchanger, and accordingly it is important that the exchanger be built sufficiently sturdy to accommodate a desirable pressure and of course to also securely retain the fluids in their separate passes without leakage or impedance to flow.
  • Still another object of this invention is to provide a heat exchanger wherein the core of the exchanger comprising the usual tubes and tins are fxtured and physically size of the core within the limits of tolerance in the manufacture of a core.
  • Still a further object of this invention is to provide a heat exchanger with a core surrounded by a casing in. contact with the core and the entire assembly being arinthe art.
  • FIG. 1 is a top plan view of a fragment of a heat exchanger incorporating a preferred embodiment of this; invention, and with a part thereof broken away.
  • FIG. 2 is a side elevational view of the exchanger shown in FIG. 1.
  • FIG. 3 is a sectional view taken along the line 3 3 of FIG. 2 and with a corner of the View broken away.
  • FIG. 4 is a side elevational view of a fragment of a fin disposed within the exchanger shown.
  • FIG. 5 is a top plan View of the tin fragment shown in FIG. 4.
  • FIG. 6 is an end elevational v-iew of the tin fragment shown in FIG. 4.
  • This particular heat exchanger has application in theI oil cooler art and it will thus be described in connection with that art.
  • the exchanger is shown to include a plurality of tubes 10 extending through the length of theexchanger in a parallel and spaced-apart relation, and a;
  • header 11 is disposed at one end of the exchanger and a header 12 at the other end ofthe exchanger.
  • the headers 11 and 12 include end plates 13 which have openings therein of the shape of the tubes shown in FIG. 3 such that the tubes can of course project through the plates 13 and extend therebeyond as show-n in the :dotted lines in FIGS. 1 and 2. It will therefore be understood that the headers 11 and 12 conduct oil or other fluid into the tubes 10 for the passage between the headers, depending upon the direction of flow of the fluid. This therefore of course makes a fluid-tight and separate pass for the water or other fluid to flow through the exchanger.
  • Oil or other fluid will also be conducted through the exchanger through a second and separate pass which includes the tanks or headers 14 and 16 having the fittings 17 thereon.
  • a second and separate pass which includes the tanks or headers 14 and 16 having the fittings 17 thereon.
  • FIGS. 1 and 3 show two rows of iins 18 and an intermediate spacer plate 19 disposed in the space between every two successive tubes 10. Also, a single lin 18 is disposed at the outside surface of the outer tubes 10 as shown on lthe one side in FIGS. l and 3.
  • the particular conguration of tins shown is of a grid or strip type having two offset strips 21 and 22 which provide an intermediate opening 23 through which fluid can flow, and thus the oil, when used, will flow through the opening 23.
  • the oil can thus flow along the plane of the iin 18 in either transverse direction, and it will of course at least partially flow through the openings 23 to give maximum heat exchange eiciency byyirtue of the turbulence created in the oil.
  • the significant feature of the fin is that it is of a type which is firm in the direction toward the tubes 10, and this feature is for a purpose mentioned hereinafter.
  • FIG. 3 particularly shows a casing 26 extending endlessly around the exchanger core which consists of the tubes 10 and tins 18. Further the casing 26 is shown to be in two parts 27 and 28 and these two parts are joined together at the joint portion designated 29. It will therefore be noted and understood that the inner surface extending endlessly around the casing 26 is in contact with the exchanger core at both the points of contact designated 31 on the tins 18, and also the points of contact designated 32 on the tubes and 33 on the tins 18.
  • the exchanger core presents a rectangular cross-sectional shape and the easing 26 presents a similar shape which is in snug and endless contact with the core.
  • the advantage is that the core can of course be assembled and the casing 26 can be disposed therearound :and lixtured tonto the core by moving the casing parts 27 and 28 toward each other and thus press the sides of the core inwardly and in lirm and snug contact throughout the width of the core, as viewed in FIG. 3.
  • the entire exchanger can be placed into a bonding bath for the well-known vibonding Ioperation so that all the points of Contact within the core and between the core and the casing 26 will be bonded together.
  • the casing 26 provides the means for containing the oil or like iiuid for passage along the iins 18, and also the casing 26 renders the entire assembly sturdy in that it is all an in tegral exchanger with the core bonded both internallyV and to the casing 26 for maximum strength.
  • the pressures within the exchanger can be raised to maximum quantities without distorting the exchanger and of course without requiring the wellknown eircularly shaped exchangers employed in, for instance, the toil cooler.
  • the arrangement is such that the tubes are provided with internal struts 35, and these struts of course provide for strength across the narrow portions of the tubes 10, and also the tubes 10 extend between the top side 34 and the bottom side 36 of the casing 26.
  • the rigid and set dimension of the tube 36 is employed in establishing the core dimen-v sion in the direction just mentioned, and the adjustability of the casing 26 between its sides 37 and 38 accommodate the core tolerance in that direction and also permit the snug lixturing and contacting of the core parts.
  • the exchanger is thus assembled with tube and fins comprising the core described, and these parts are enclosed Iby the casing 26, which of course has a necessary opening for accommodation of the headers 14 and 16 along ⁇ the casing wall 34.
  • the entire assembly is bonded so that all of the parts shown are attached to gether in one unit.
  • the tubes 10 are hat-tened' in their cross-sectional configuration and the struts ex tend between the flattened sides of the tubes for making; the tubes strong in the direction of the struts or supports 35. Also the ns 18 ⁇ are lstrong and resist forces and deiiection so that the entire core is arranged with the tins in abutment with the tiattened sides of the tubes and bonded thereto to render the core unitary in is construction from the casing side 37 to the casing side 38.
  • the flattened tubes with struts 35 'and the tins being bonded to the tubes all form a strong structure between the sides of the casing so that high internal uid pressures will not bulge the tubes 35 or distort the core.
  • a heat exchanger comprising a plurality of parallel and spaced-apart tubes having oppositely disposed open end portions, a header fluid-tightly attached to each of said open end portions for directing fluid through said tubes, a plurality of fins disposed between said tubes and being bonded thereto to form a core with said tubes and vbeing arranged for the ilow of uid over said tins, said tubes and said tins extending to common planes on opposite sides of said core, a casing fluid-tightly disposed in planular contact with both said tubes and said ins on said opposite sides and around the entire :periphery of said core endlessly in the direction transverse to the axes of said tubes and intermediate said headers and being bonded to said core and to said Iheaders for containment of the fluid tiowing over said fins and for strengthening said exchanger, and a uid inlet and a fluid outlet means on said casing for directing uid tlow through said core.
  • a heat exchanger comprising a plurality of iiattened tubes disposed parallel land spaced apart and having open end portions, support means disposed within said tubes and connected between the flattened sides thereof for strengthening said tubes, -a header in fluid-flow communication with each of said open end portions, a plurality of tins disposed between said tubes at the attened sides thereof and being bonded thereto to present a unitary structure with said tubes and said support means, said tubes and said fins disposed with the two opposite edges of both being aligned along common planes to present a core with a predetermined rectangular cross-section dened by both said edges and by only said tins on sides of said rectangular cross-section intermediate said common planes, and a case ⁇ of said predetermined rectangular vcross-section and two parts disposed entirely between said headers in continuously snug and bonded contact with the rectangular periphery of said core and with said parts being bonded together for confining the iiow of fluid over said tins and being ⁇ adjustable along
  • a heat exchanger comprising a plurality of parallel and spaced-apart tubes having oppositely disposed open lend portions, a header huid-tightly attached to each of said open end portions for directing uid through said tubes, a plurality of fins disposed between said tuibes and being bonded thereto to form a core with said tubes and being arranged for the ow of uid over said tins, said tubes and said tins having equal lateral extents and both extending to one common plane on each opposite side of core, only said tins extending along the other opposite sides of said core, a casing disposed in planular contact with and bonded to both said tubes and said fins on the iirst said opposite sides of said core and bonded to said ns on the other said opposite sides of said core and extending around the entire periphery of ⁇ said core endlessly in the direction transverse to the axes of said tubes and I) .intermedia-te said headers and being fluid
  • a heat exchanger comprising a plurality of flattened tubes disposed parallel and spaced apart and having open end portions, two spaced-apart headers in fluid-How comfmunication with said open end portions, a plurality of tins disposed between said tubes at the flattened sides thereof and being
  • a heat exchanger comprising a plurality of parallel and spaced-apart tubes having liat sides and oppositcly disposed open end portions, a header fluid-tightly attached to each of said open end portions for directing fluid through said tubes, a plurality of tins disposed between said tubes on said flat sides thereof and being bonded thereto to form a core with said tubes and being arranged for the flow of fluid over said ns and with said core being of a predetermined cross-sectional shape, said tubes extending in side limits to one common plane on each of two opposite sides of said cross-sectional shape and with only said fins extending along the other two opposite sides, a casing of said cross-sectional shape and in two halves adjustably nestedV together and in contact with said tubes at said side limits on the tirst said opposite sides and with said casing being in contact with said tins on the other said opposite sides and being duid-tightly disposed in endless contact with the periphery of said core intermediate said headers and being bonded
  • a heat exchanger comprising a plurality of parallel and spaced-apart tubes having two oppositely disposed open end portions, a header fluid-tightly attached to each of said open end portions for directing uiid through said tubes, a plurality of fins disposed between said tubes and being bonded thereto to form a core with said tubes and being arranged for the ow of fluid over said fins, each of said tubes extending completely across said core between the outer limits of two opposite sides of said core and 'with said tubes being elongated in their extents between said opposite sides and being internally strutted for support in the two directions between said tubes, a two-piece casing iluidatightly disposed in endless Contact with the periphery of said core intermediate said headers and being bonded to said core and to said headers for containment of the uid owing over 'said tins and for strengthening said exchanger, the pieces of said 6 in said two directions to adju-st to said core in said two directions between said tubes prior to bond

Description

March 16, 1965 H. J. BARKLEY 3,173,481
HEAT EXCHANGER Filed Sept. 24, 1962 lmmllli IN1/wrom HOWARD BARKLEY A By: MM] @4MM/VJ @QTTORNEY United States Patent O 3,173,481 HEAT EXCHANGER Howard J. Barkley, Racine, Wis., assigner to Modine Manufacturing Company, Racine, Wis., a corporation of Wisconsin Filed Sept. 24, 1962, Ser. No. 225,561 6 Claims. (Cl. 165-160) This invention relates to a heat exchanger, and more particularly it relates to an exchanger wherein two uids are employed :for operation and both lluids have separate and enclosed passes.
Heat exchangers having two separate and enclosed passes are well known in the art, such that the two fluids in the respective passes are completely contained for circulation through the exchanger. The ethciency of an exchanger of this type is dependent upon the pressure drop of the fluid pressure in the exchanger, and accordingly it is important that the exchanger be built sufficiently sturdy to accommodate a desirable pressure and of course to also securely retain the fluids in their separate passes without leakage or impedance to flow.
Accordingly, it is an object of this invention to provide a heat exchanger which accommodates a high internal pressure in both the fluids flowing through `the exchanger.
Still another object of this invention is to provide a heat exchanger wherein the core of the exchanger comprising the usual tubes and tins are fxtured and physically size of the core within the limits of tolerance in the manufacture of a core.
Still a further object of this invention is to provide a heat exchanger with a core surrounded by a casing in. contact with the core and the entire assembly being arinthe art.
Other objects an-d advantages will become apparent upon reading the following description in light of the: accompanying drawings wherein:
FIG. 1 is a top plan view of a fragment of a heat exchanger incorporating a preferred embodiment of this; invention, and with a part thereof broken away.
FIG. 2 is a side elevational view of the exchanger shown in FIG. 1.
FIG. 3 is a sectional view taken along the line 3 3 of FIG. 2 and with a corner of the View broken away.
FIG. 4 is a side elevational view of a fragment of a fin disposed within the exchanger shown.
FIG. 5 is a top plan View of the tin fragment shown in FIG. 4.
FIG. 6 is an end elevational v-iew of the tin fragment shown in FIG. 4.
This particular heat exchanger has application in theI oil cooler art and it will thus be described in connection with that art. Thus the exchanger is shown to include a plurality of tubes 10 extending through the length of theexchanger in a parallel and spaced-apart relation, and a;
.40 ranged so that the core and casing can be all bonded together in one bonding operation, such as that well known header 11 is disposed at one end of the exchanger and a header 12 at the other end ofthe exchanger. The headers 11 and 12 include end plates 13 which have openings therein of the shape of the tubes shown in FIG. 3 such that the tubes can of course project through the plates 13 and extend therebeyond as show-n in the :dotted lines in FIGS. 1 and 2. It will therefore be understood that the headers 11 and 12 conduct oil or other fluid into the tubes 10 for the passage between the headers, depending upon the direction of flow of the fluid. This therefore of course makes a fluid-tight and separate pass for the water or other fluid to flow through the exchanger.
Oil or other fluid will also be conducted through the exchanger through a second and separate pass which includes the tanks or headers 14 and 16 having the fittings 17 thereon. Thus it will of course be seen that the oil can pass between the headers 14 and 16 and through the exchanger in the spaces between the tubes 10 and thereby the usual exchange of heat will occur as the lluids move4 through their respective passes in the well-known manner.
The spaces between the tubes 10 are shown to be occupied by tins 18 which are of a serpentine shape and rolled or punched to be of the offset strip form providing for eicient heat exchange between the iins 18 and the tubes 10. Thus FIGS. 1 and 3, for instance, show two rows of iins 18 and an intermediate spacer plate 19 disposed in the space between every two successive tubes 10. Also, a single lin 18 is disposed at the outside surface of the outer tubes 10 as shown on lthe one side in FIGS. l and 3.
The particular conguration of tins shown is of a grid or strip type having two offset strips 21 and 22 which provide an intermediate opening 23 through which fluid can flow, and thus the oil, when used, will flow through the opening 23. With this type of iin 18, the oil can thus flow along the plane of the iin 18 in either transverse direction, and it will of course at least partially flow through the openings 23 to give maximum heat exchange eiciency byyirtue of the turbulence created in the oil. However, the significant feature of the fin is that it is of a type which is firm in the direction toward the tubes 10, and this feature is for a purpose mentioned hereinafter.
FIG. 3 particularly shows a casing 26 extending endlessly around the exchanger core which consists of the tubes 10 and tins 18. Further the casing 26 is shown to be in two parts 27 and 28 and these two parts are joined together at the joint portion designated 29. It will therefore be noted and understood that the inner surface extending endlessly around the casing 26 is in contact with the exchanger core at both the points of contact designated 31 on the tins 18, and also the points of contact designated 32 on the tubes and 33 on the tins 18. Thus the exchanger core presents a rectangular cross-sectional shape and the easing 26 presents a similar shape which is in snug and endless contact with the core.
With the arrangement described, the advantage is that the core can of course be assembled and the casing 26 can be disposed therearound :and lixtured tonto the core by moving the casing parts 27 and 28 toward each other and thus press the sides of the core inwardly and in lirm and snug contact throughout the width of the core, as viewed in FIG. 3. With this snug assembly, the entire exchanger can be placed into a bonding bath for the well-known vibonding Ioperation so that all the points of Contact within the core and between the core and the casing 26 will be bonded together. lt will therefore be seen that the casing 26 provides the means for containing the oil or like iiuid for passage along the iins 18, and also the casing 26 renders the entire assembly sturdy in that it is all an in tegral exchanger with the core bonded both internallyV and to the casing 26 for maximum strength. By virtue of this arrangement, the pressures within the exchanger can be raised to maximum quantities without distorting the exchanger and of course without requiring the wellknown eircularly shaped exchangers employed in, for instance, the toil cooler.
It will therefore be noted that the arrangement is such that the tubes are provided with internal struts 35, and these struts of course provide for strength across the narrow portions of the tubes 10, and also the tubes 10 extend between the top side 34 and the bottom side 36 of the casing 26. Thus the rigid and set dimension of the tube 36 is employed in establishing the core dimen-v sion in the direction just mentioned, and the adjustability of the casing 26 between its sides 37 and 38 accommodate the core tolerance in that direction and also permit the snug lixturing and contacting of the core parts.
The exchanger is thus assembled with tube and fins comprising the core described, and these parts are enclosed Iby the casing 26, which of course has a necessary opening for accommodation of the headers 14 and 16 along `the casing wall 34. Thus the entire assembly is bonded so that all of the parts shown are attached to gether in one unit.
It will therefore be noted that the tubes 10 are hat-tened' in their cross-sectional configuration and the struts ex tend between the flattened sides of the tubes for making; the tubes strong in the direction of the struts or supports 35. Also the ns 18 `are lstrong and resist forces and deiiection so that the entire core is arranged with the tins in abutment with the tiattened sides of the tubes and bonded thereto to render the core unitary in is construction from the casing side 37 to the casing side 38. That is, the flattened tubes with struts 35 'and the tins being bonded to the tubes, all form a strong structure between the sides of the casing so that high internal uid pressures will not bulge the tubes 35 or distort the core.
What is claimed is:
1. A heat exchanger comprising a plurality of parallel and spaced-apart tubes having oppositely disposed open end portions, a header fluid-tightly attached to each of said open end portions for directing fluid through said tubes, a plurality of fins disposed between said tubes and being bonded thereto to form a core with said tubes and vbeing arranged for the ilow of uid over said tins, said tubes and said tins extending to common planes on opposite sides of said core, a casing fluid-tightly disposed in planular contact with both said tubes and said ins on said opposite sides and around the entire :periphery of said core endlessly in the direction transverse to the axes of said tubes and intermediate said headers and being bonded to said core and to said Iheaders for containment of the fluid tiowing over said fins and for strengthening said exchanger, and a uid inlet and a fluid outlet means on said casing for directing uid tlow through said core.
2. A heat exchanger comprising a plurality of iiattened tubes disposed parallel land spaced apart and having open end portions, support means disposed within said tubes and connected between the flattened sides thereof for strengthening said tubes, -a header in fluid-flow communication with each of said open end portions, a plurality of tins disposed between said tubes at the attened sides thereof and being bonded thereto to present a unitary structure with said tubes and said support means, said tubes and said fins disposed with the two opposite edges of both being aligned along common planes to present a core with a predetermined rectangular cross-section dened by both said edges and by only said tins on sides of said rectangular cross-section intermediate said common planes, and a case `of said predetermined rectangular vcross-section and two parts disposed entirely between said headers in continuously snug and bonded contact with the rectangular periphery of said core and with said parts being bonded together for confining the iiow of fluid over said tins and being `adjustable along said common planes prior to bonding.
3. A heat exchanger comprising a plurality of parallel and spaced-apart tubes having oppositely disposed open lend portions, a header huid-tightly attached to each of said open end portions for directing uid through said tubes, a plurality of fins disposed between said tuibes and being bonded thereto to form a core with said tubes and being arranged for the ow of uid over said tins, said tubes and said tins having equal lateral extents and both extending to one common plane on each opposite side of core, only said tins extending along the other opposite sides of said core, a casing disposed in planular contact with and bonded to both said tubes and said fins on the iirst said opposite sides of said core and bonded to said ns on the other said opposite sides of said core and extending around the entire periphery of `said core endlessly in the direction transverse to the axes of said tubes and I) .intermedia-te said headers and being fluid-tightly bonded to said core and to said headers for containment of the fluid tiowing over said iins and for strengthening said exchanger, and a fluid inlet means and a fluid outlet means on said casing for directing tiuid ilow through said core.
4. A heat exchanger comprising a plurality of flattened tubes disposed parallel and spaced apart and having open end portions, two spaced-apart headers in fluid-How comfmunication with said open end portions, a plurality of tins disposed between said tubes at the flattened sides thereof and being |bonded thereto, said tubes and said iins disposed to present a core with a rectangular crosssection by said tubes land said tins being coextensive on the first two opposite sides and with said core having only said tins on the other two opposite sides, a rectangular case of two parts disposed entirely in the space between said headers and in endless bonded Contact `along all said sides of said core, said parts being overlapped and movable toward and away from each other and said attened sides along said first two opposite sides prior to bonding .to adjust to said core size at said other two opposite sides :and thereby abut said tins, and header means in fluidiiow communication with said case for directing fluid over said core.
5. A heat exchanger comprising a plurality of parallel and spaced-apart tubes having liat sides and oppositcly disposed open end portions, a header fluid-tightly attached to each of said open end portions for directing fluid through said tubes, a plurality of tins disposed between said tubes on said flat sides thereof and being bonded thereto to form a core with said tubes and being arranged for the flow of fluid over said ns and with said core being of a predetermined cross-sectional shape, said tubes extending in side limits to one common plane on each of two opposite sides of said cross-sectional shape and with only said fins extending along the other two opposite sides, a casing of said cross-sectional shape and in two halves adjustably nestedV together and in contact with said tubes at said side limits on the tirst said opposite sides and with said casing being in contact with said tins on the other said opposite sides and being duid-tightly disposed in endless contact with the periphery of said core intermediate said headers and being bonded to said core and to said headers for containment of the tiuid owing over said ns and for strengthening said exchanger, and header means in iiuid-iiow communication with said oasing for directing liuid over `said core.
6. A heat exchanger comprising a plurality of parallel and spaced-apart tubes having two oppositely disposed open end portions, a header fluid-tightly attached to each of said open end portions for directing uiid through said tubes, a plurality of fins disposed between said tubes and being bonded thereto to form a core with said tubes and being arranged for the ow of fluid over said fins, each of said tubes extending completely across said core between the outer limits of two opposite sides of said core and 'with said tubes being elongated in their extents between said opposite sides and being internally strutted for support in the two directions between said tubes, a two-piece casing iluidatightly disposed in endless Contact with the periphery of said core intermediate said headers and being bonded to said core and to said headers for containment of the uid owing over 'said tins and for strengthening said exchanger, the pieces of said 6 in said two directions to adju-st to said core in said two directions between said tubes prior to bonding.
References Cited by the Examiner UNITED STATES PATENTS 1,673,409 6/28 Kelley 165-148 1,830,375 11/31 Shoop 16S-183 2,499,901 3/50 Brown 165-160 2,686,957 8/54 Koerper 16S-152 2,804,284 8/57 Otten 165-160 2,877,000 3/59 Person 16S-159 CHARLES SUKALO, Primary Examiner.
casing being movable toward and away from each other 15 FREDERCK L MATTESON JR ExFlmiW

Claims (1)

1. A HEAT EXCHANGER COMPRISING A PLURALITY OF PARALLEL AND SPACED-APART TUBES HAVING OPPOSITELY DISPOSED OPEN END PORTIONS, A HEADER FLUID-TIGHTLY ATTACHED TO EACH OF SAID OPEN END PORTIONS FOR DIRECTING FLUID THROUGH SAID TUBES, A PLURALITY OF FINS DISPOSD BETWEEN SAID TUBES AND BEING BONDED THERETO TO FORM A CORE WITH SAID TUBES AND BEING ARRANGED FOR THE FLOW OF FLUID OVER SAID FINS, SAID TUBES AND SAID FINS EXTENDING TO COMMON PLANES ON OPPOSITE SIDES OF SAID CORE, A CASING FLUID-TIGHTLY DISPOSED IN PLANAR CONTACT WITH BOTH SAID TUBES AND SAID FINS ON SAID OPPOSITE SIDES AND AROUND THE ENTIRE PERIPHERY OF SAID CORE ENDLESSLY IN THE DIRECTION TRANSVERSE TO THE AXES OF SAID TUBES AND INTERMEDIATE SAID HEADERS AND BEING BONDED TO SAID CORE AND TO SAID HEADERS FOR CONTAINMENT OF THE FLUID FLOWING OVER SAID FINS AND FOR STRENGTHENING SAID EXCHANGER, AND A FLUID INLET AND A FLUID OUTLET MEANS ON SAID CASING FOR DIRECTING FLUID FLOW THROUGH SAID CORE.
US225561A 1962-09-24 1962-09-24 Heat exchanger Expired - Lifetime US3173481A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US225561A US3173481A (en) 1962-09-24 1962-09-24 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US225561A US3173481A (en) 1962-09-24 1962-09-24 Heat exchanger

Publications (1)

Publication Number Publication Date
US3173481A true US3173481A (en) 1965-03-16

Family

ID=22845354

Family Applications (1)

Application Number Title Priority Date Filing Date
US225561A Expired - Lifetime US3173481A (en) 1962-09-24 1962-09-24 Heat exchanger

Country Status (1)

Country Link
US (1) US3173481A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3732919A (en) * 1970-07-01 1973-05-15 J Wilson Heat exchanger
US5238469A (en) * 1992-04-02 1993-08-24 Saes Pure Gas, Inc. Method and apparatus for removing residual hydrogen from a purified gas
FR2827949A1 (en) * 2001-07-26 2003-01-31 Denso Corp EXHAUST GAS EXCHANGER
WO2004065874A1 (en) * 2003-01-23 2004-08-05 Behr Gmbh & Co. Kg Device for exchanging heat
US20060102321A1 (en) * 2002-07-25 2006-05-18 Shuko Shincho Heat exchanger
US20060254757A1 (en) * 2005-05-10 2006-11-16 Kamsma Hubertus R Intermediate cooler for air-conditioning refrigerant
US20070017661A1 (en) * 2003-10-20 2007-01-25 Behr Gmbh & Co, Kg Heat exchanger
US20110162826A1 (en) * 2008-06-26 2011-07-07 Paul Garret Heat exchanger and casing for the exchanger
CN109724432A (en) * 2017-10-30 2019-05-07 翰昂汽车零部件有限公司 Heat exchanger for internal combustion engine

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1673409A (en) * 1926-03-12 1928-06-12 Winchester Repeating Arms Co Heat-interchange apparatus
US1830375A (en) * 1930-04-04 1931-11-03 Shoop Gertrude Heat exchange article
US2499901A (en) * 1946-08-31 1950-03-07 Brown Fintube Co Fin tube assembly
US2686957A (en) * 1951-08-17 1954-08-24 Smith Corp A O Method of manufacturing heat exchanger sections
US2804284A (en) * 1953-04-03 1957-08-27 Griscom Russell Co Heat exchanger
US2877000A (en) * 1955-09-16 1959-03-10 Int Harvester Co Heat exchanger

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1673409A (en) * 1926-03-12 1928-06-12 Winchester Repeating Arms Co Heat-interchange apparatus
US1830375A (en) * 1930-04-04 1931-11-03 Shoop Gertrude Heat exchange article
US2499901A (en) * 1946-08-31 1950-03-07 Brown Fintube Co Fin tube assembly
US2686957A (en) * 1951-08-17 1954-08-24 Smith Corp A O Method of manufacturing heat exchanger sections
US2804284A (en) * 1953-04-03 1957-08-27 Griscom Russell Co Heat exchanger
US2877000A (en) * 1955-09-16 1959-03-10 Int Harvester Co Heat exchanger

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3732919A (en) * 1970-07-01 1973-05-15 J Wilson Heat exchanger
US5238469A (en) * 1992-04-02 1993-08-24 Saes Pure Gas, Inc. Method and apparatus for removing residual hydrogen from a purified gas
USRE35725E (en) * 1992-04-02 1998-02-10 Saes Pure Gas, Inc. Method and apparatus for removing residual hydrogen from a purified gas
FR2827949A1 (en) * 2001-07-26 2003-01-31 Denso Corp EXHAUST GAS EXCHANGER
US7267160B2 (en) * 2002-07-25 2007-09-11 T.Rad Co., Ltd. Heat exchanger
US20060102321A1 (en) * 2002-07-25 2006-05-18 Shuko Shincho Heat exchanger
WO2004065874A1 (en) * 2003-01-23 2004-08-05 Behr Gmbh & Co. Kg Device for exchanging heat
US20060048759A1 (en) * 2003-01-23 2006-03-09 Behr Gmbh & Co. Kg Device for exchanging heat
US7571718B2 (en) 2003-01-23 2009-08-11 Behr Gmbh & Co. Kg Device for exchanging heat
US20070017661A1 (en) * 2003-10-20 2007-01-25 Behr Gmbh & Co, Kg Heat exchanger
US20060254757A1 (en) * 2005-05-10 2006-11-16 Kamsma Hubertus R Intermediate cooler for air-conditioning refrigerant
US20110162826A1 (en) * 2008-06-26 2011-07-07 Paul Garret Heat exchanger and casing for the exchanger
CN102138052B (en) * 2008-06-26 2014-02-26 法雷奥热系统公司 Heat exchanger and housing for the exchanger
US9599412B2 (en) * 2008-06-26 2017-03-21 Valeo Systemes Thermiques Heat exchanger and casing for the exchanger
CN109724432A (en) * 2017-10-30 2019-05-07 翰昂汽车零部件有限公司 Heat exchanger for internal combustion engine
CN109724432B (en) * 2017-10-30 2020-12-15 翰昂汽车零部件有限公司 Heat exchanger for internal combustion engine

Similar Documents

Publication Publication Date Title
US4815534A (en) Plate type heat exchanger
US4285397A (en) Heat-exchangers with plate-like heat exchange elements
US3596495A (en) Heat transfer device and method of making
US2752128A (en) Heat exchange structure
US2039593A (en) Heat transfer coil
US3907028A (en) Concentric cylinder heat exchanger
US2782009A (en) Heat exchangers
US2959400A (en) Prime surface heat exchanger with dimpled sheets
US3734177A (en) Heat exchanger
US3552488A (en) Plate-fin heat exchanger
US3173481A (en) Heat exchanger
GB1278308A (en) An improved heat exchanger
US3825061A (en) Leak protected heat exchanger
US2858112A (en) Heat exchanger
US3731736A (en) Plate and fin heat exchanger
US3894581A (en) Method of manifold construction for formed tube-sheet heat exchanger and structure formed thereby
US3113615A (en) Heat exchanger header construction
US3074480A (en) Heat exchanger
JPS60263088A (en) Heat exchanger
US4373578A (en) Radiator with heat exchanger
KR100354729B1 (en) Manufacturing method of flat heat exchanger and press tool used in manufacturing method
US2539870A (en) Crossflow heat exchanger
US2093256A (en) Heat exchange element
US3024003A (en) Heat exchanger
US3515207A (en) Fin configuration for fin and tube heat exchanger