[go: up one dir, main page]

US2729433A - Heat exchanger with removable tube banks - Google Patents

Heat exchanger with removable tube banks Download PDF

Info

Publication number
US2729433A
US2729433A US265253A US26525352A US2729433A US 2729433 A US2729433 A US 2729433A US 265253 A US265253 A US 265253A US 26525352 A US26525352 A US 26525352A US 2729433 A US2729433 A US 2729433A
Authority
US
United States
Prior art keywords
air
heat exchanger
bank
secured
shell
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
US265253A
Inventor
William F Berg
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.)
AO Smith Corp
Original Assignee
AO Smith Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by AO Smith Corp filed Critical AO Smith Corp
Priority to US265253A priority Critical patent/US2729433A/en
Application granted granted Critical
Publication of US2729433A publication Critical patent/US2729433A/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
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/0233Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with air flow channels
    • F28D1/024Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with air flow channels with an air driving element
    • 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0012Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
    • F28F27/02Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus for controlling the distribution of heat-exchange media between different channels
    • 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
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2280/00Mounting arrangements; Arrangements for facilitating assembling or disassembling of heat exchanger parts
    • F28F2280/02Removable elements
    • 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
    • Y10S165/092Heat exchange with valve or movable deflector for heat exchange fluid flow
    • Y10S165/109Heat exchange with valve or movable deflector for heat exchange fluid flow with by-pass of heat exchanger or heat exchanger section
    • Y10S165/11Bypass within or surrounds heat exchanger
    • Y10S165/113Bypass centrally located in heat exchanger

Definitions

  • Thisinvention relates to heat exchangers and more particularly toan air cooler having a plurality of heat transfer core sections which are arranged in the form of an annular bank or ring within the cooler.
  • An object ofthe present invention isto provide a heat exchanger wherein the heat transfer surfaces are in the form of a plurality of circularly disposed longitudinal tube units and the fluid to be heated or cooledis directed radially through the units.
  • Another object is to provide a heat exchanger having a large face area for a given cross sectional area of the heat exchanger.
  • Another object is to provide a gas to liquid heat exchanger which will effectively cool a large mass of gas without producing an appreciable pressure drop in the gas-being cooled.
  • Another object is to provide a heat exchanging apparatus wherein the temperature of the air being discharged from the apparatus may be conveniently controlled.
  • Still another object is to provide a heat exchanging apparatus having a plurality of independent heat transfer core sections which are removably secured to the exterior of the apparatus and may be readily withdrawn from the cooler for repair or cleaning.
  • a further object is to provide a simple and effective means of attaching a plurality of heat transfer core sections in the pattern of an annular bank, within a heat exchanger.
  • Another object is to provide heat transfer sections in a heat exchanger wherein all of thefittings for connections are disposed outside the shell of the unit for ready assembly and disassembly.
  • the present invention is directed to a barrel-shaped air cooler which comprises a generally cylindrical shell having suitable openings in opposite ends thereof for the entry and discharge of a-fluid'such as air.
  • the heat exchanging surface takes the form of an annular bank or ring which comprises a plurality of independent longitudinally disposed heat transfer core sections and is inwardly. spaced from the shell about the air inlet.
  • An end plate closes off the rear end of the heat transfer chamber and prevents the longitudinal passage of air therethrough.
  • the air enters the hollow interior of the annular bank through the inlet in the shell and is directed radially outwardly through the bank of core sections andis cooled as it passes therethrough. After cooling, the air passes longitudinallyin the annular space between the heat transfer bank and the shell, and then inwardly around the rear of the annulat bank to the discharge outlet in the shell.
  • a portion of the entering air may be by-passed directly through the hollow interior of the annular bank without passing radially through the heat exchanging core sections, and by varying the amount of by-passed air the temperature of the discharged air can be readily controlled.
  • an air cooler It is desirable for an air cooler to have a large face area per mass of air passing therethrough so as to keep 2,729,433 Fatented Jan. 3,, 1956 "ice the pressure drop of air passing through the cooler to a minimum. Ordinarily an increase, in face area is accomplished by increasing the cross sectional area or diameter of the cooler and this increased cooler size is frequently obiectionable for installation and economic reasons.
  • a greater heat transfer face area may he obtained for a given diameter shell than in an air cooler wherein the air passesstraight through a heat transfer surface disposed in a plane normal to the general flow of air or through a herringbone type cooler. Additional face area can be attained in the present barrel-type cooler without enlarging the diameter of the shell by. merely increasing the length of the heat transfer core sections.
  • Figure 1 is a front elevational view of the heat exchanger
  • Fig. 2 is a central vertical section of the heat exchanger
  • Fig. 3 is a fragmentary transverse section taken along line 3-3 of Fig. 2 showing the disposition of core sections within the annular bank;
  • Fig. 4 is a perspective of one of the frames of the annular heat transfer bank
  • Fig. 5 is a longitudinal section taken along line 5-5 of Figure 1 with a portion of the core section being shown in side elevation, and;
  • Fig. 6 is a longitudinal section taken along line 6-6 of Fig. 5 showing the structure of the core sections.
  • a fluid type heat exchanger having a hollow external casing or shell 1 which includes a generally cylindrical body section 2 and a generally conical end cap 3.
  • a pair of generally circular spider plates 4 and 5 are longitudinally spaced and secured edgewise by welding or the like to the inner surface of body section 2.
  • Front spider plate 4 is provided with an axial opening 6 through which a fluid to be heated or cooled, such as air, is admitted into the shell 1.
  • Plate4 is also provided with a plurality of circumferentially spaced generally rectangular flanged openings 7 which are spaced inwardly from the circumference of plate 4 and arranged about axial opening 6.
  • a flanged pipe connection 8 is welded within axial opening 6 and provides a means for attaching an air inlet pipe, not shown, to the heat exchanger.
  • the rear spider plate 5 is secured to the rear end of section 2 by a weld 9 and has a plurality of rectangular circumferentially spaced openings 10 adjacent its peripheral edge.
  • the plate 5 is formed with a central conical portion 11 directed toward the inlet opening 6 to aid in deflecting the incoming air radially outward through the tube units as will be described.
  • End cap 3 is provided with an outlet opening 12 for the discharge of cooled air.
  • a flanged pipe connection 23 is secured to cap 3 around opening 12 and provides a means for attaching an air discharge conduit, not shown, to cap 3.
  • a polygonal annular heat exchanging ring or bank 14 is disposed within shell 1 and spaced radially inward therefrom.
  • the hollow interior of the bank 14 registers with the axial opening 6 in the spider plate 4.
  • the heat exchanging bank 14 comprises, in general, a plurality of generally rectangular longitudinally disposed frames 15 which are secured in the form of a polygonal annulus or ring between spider. plates 4 and 5' and register witl openings 7 in plate 4, and a plurality of heat transfer core sections 16 which are inserted within shell 1 through openings 7 and are supported by, the respective frames 15.
  • each of the frames 15 includes four longitudinal angle iron guide bars 17, disposed to define a rectangular frame, and which are connected at their ends and central portions by a plurality of side plates 18 and cross ties 19 to provide a rigid integral structure.
  • Frames 15 are aligned behind the corresponding openings 7 in plate 4, and the side plates 18 at the ends of each frame are attached to the respective plates 4 and by angle brackets 20.
  • a pair of radial braces 21 extend outwardly from the central portion of each frame and are welded to the inner surface of shell 1.
  • a plurality of longitudinal sealing strips 22 are secured between the inner guide bars 17 of adjacent frames to seal off the space between frames to the passage of air.
  • the core sections 16 of heat transfer bank 14 which are supported by frames 15 include a cluster or bundle of longitudinally disposed tubes 23 within which a heating or cooling fluid, depending on the operation, is adapted to circulate.
  • Tubes 23 may be constructed of any material which has generally high thermal conductivity properties and which is able to withstand attack from the particular fluids employed in the heat exchanger.
  • Fins 24 may be constructed of any material having a high heat conductivity and which may be readily attached to tubes 23.
  • each core section 16 is provided with a plurality of transverse support plates 25.
  • Plates 25 are formed with a plurality of suitable circular openings which receive tubes 23.
  • the corner extremities of each plate 25 are provided with projection or legs 26 which are adapted to engage the respective guide bars 17 of frame 15 so that the core section 16 may slide easily into position within frame 15.
  • the tubes 23 are secured at the front and rear end of core section 16 to a front tube plate 27 and a rear tube plate 28 respectively.
  • Plates 27 and 28 are generally rectangular in shape and provided with a plurality of suitable openings within which the respective ends of tubes 23 are secured, by either welding, brazing, soldering or the like, depending on the metals employed.
  • Plates 27 are of greater size than the respective rectangular openings 7 in plate 4 so that the outer periphery of plates 27 will bear against plate 4 when core sections 16 are inserted into the annular heat transfer bank 14 through the openings 7.
  • each core section 16 is enclosed by a plurality of side plates 29 which are secured by welding to the respective tube plates 27 and 28 and to the support plates 25.
  • Side plates 29 serve to seal 011 the space between core sections 16 to the passage of air and direct the air radially outward through the sections 16. It may be desirable to provide plates 29 with suitable expansion joints, not shown, to compensate for expansions of the plates 29 during operation of the heat exchanger.
  • a generally rectangular header box 30 is secured by welding to the outer face of front tube plate 27 and serves to distribute the cooling liquid or water to and from tubes 23.
  • a rib 31 divides header box 30 into two chambers, an inlet chamber 32 and an outlet chamber 33.
  • a fitting 34 is secured within a suitable opening in the outer face of header box 30 and establishes communication between chamber 32 and a suitable source of cooling liquid, and a second fitting 35 similarly provides communication between outlet chamber 33 and a suitable drain system. These fittings are all located outside of shell 1.
  • a header cap 36 is secured to the rear tube plate 28 and defines a return chamber 37.
  • Water entering inlet chamber 32 through fitting 34 passes through the tubes 23 in the inner half of the bundle to return chamber 37 and thence is returned through the tubes in the outer half 4 of the bundle to the outlet chamber 33.
  • the core sections 16 are inserted into shell 1 through openings 7 to comprise the heat transfer bank 14.
  • Legs 26 ride on guide bars 17 of frame 15 and each core section is pushed inwardly until the peripheral edge of tube plate 27 bears against spider plate 4.
  • a plurality of bolts 38 serve to secure the peripheral edge of each plate 27 to plate 4.
  • each core section 16 is not attached to any member but merely rest on the frame 15 and is free to float with the expansion and contraction of the core section during operation of the heat exchanger.
  • Each core section 16 is independently mounted within bank 14 with the respective tube plates 27 of each core section being removably secured to plate 4 by bolts 38.
  • each core section may be readily removed from the bank for cleaning or repair without disturbing the remaining core sections or altering the apparatus by merely unfastening bolts 38.
  • the air to be cooled enters the hollow interior of the bank 14 through opening 6 in spider plate 4 and is directed radially outward through the core sections 16 of the bank and across the finned tubes 23. Heat is transferred from the air to the cooling medium within tubes 23. The cooled air then passes longitudinally within the annular space between the bank 14 and the body section 2 through openings 10 and is discharged from the shell through outlet 12.
  • a valving arrangement is provided to permit any desired amount of the entering air to pass directly through shell 1 without passing through the core sections 16. This is accomplished by providing end plate 11 with a plurality of generally rectangular circumferentially spaced openings 39 and a plurality of hinged, adjustable valves or flaps 40 to close said openings. The valves 40, when open, permit air to pass longitudinally through annulus 14 to the discharge outlet 12.
  • a plurality of generally rectangular hinged flaps 41 are employed to control the flow of air through opening 10 in rear spider plate 5.
  • Flaps 40 and 41 may be operated manually by ropes or chains or electrically or by any other desired means.
  • flaps 40 and 41 may be preferred to operate corresponding radial flaps 40 and 41 together. That is, as flaps 40 in end plate 11 are opened to allow air to by-pass core sections 16, flaps 41 are closed to reduce the flow of air through the core sections. Thus when flaps 40 are completely open, flaps 41 are entirely closed and all the air will by-pass the core sections. Conversely when end plate flaps 40 are closed, flaps 41 are open and all the air will be directed across the core sections.
  • the present invention provides a maximum face area for a given shell diameter and thereby 7 reduces the pressure loss of the air passing through the unit.
  • the present invention may be adapted for use in large or small installations and will function elfectively to cool great or small masses of air. Furthermore, the temperature of the air being discharged from the unit may be accurately controlled through use of the by-pass valves 40 and 41.
  • the air or gas to be cooled enters opening 6 in shell 1 and passes radially outward across the core sections 16, and is discharged through opening 12.
  • the apparatus will operate with equal effectiveness if the air is introduced into shell 1 through opening 12 and passes radially inward across core sections 16 and is dis- 14 having equal or unequal cross sectional areas may be employed within a given shell and arranged therein in a parallel relation, in series, i n a staggered relation or in any desired configuration to effect the heat transfer for a given operation.
  • the exchanger can still remain in operation if it is necessary to remove one or more units for repair or cleaning purposes.
  • a heat transfer apparatus comprising a generally cylindrical casing having a centrally disposed fluid inlet opening at one end and a centrally disposed fluid outlet opening at the other end, an annular member secured at its periphery to said casing and located adjacent said outlet opening, an inner set of circumferentially spaced openings disposed in said annular member to provide for passage of untreated fluid through said member, an outer set of circumferentially spaced openings disposed outwardly from the first set to provide for passage of treated fluid through said annular member, closure means pivoted to said annular member adjacent both said first and said second spaced openings to permit opening and closing of said openings and thereby control the flow of treated and untreated fluid through the outlet and the temperature of the fluid discharged from the apparatus, a pair of longitudinally spaced spider plates assembled with said casing, longitudinally extending frame members of generally rectangular shape assembled annularly and secured at their respective ends to said spider plates to provide a plurality of independent frame members spaced annularly about the inside of said casing and removed inwardly from the cas
  • the sealing strip comprises a longitudinally disposed strip secured to the inner adjacent frame members and extending therebetween to seal off the space between the core units to the passage of fluid and thereby effectively direct fluid across the core units, and a pair of radial braces extending outwardly from the central portion of each frame and secured to the inner surface of the casing to strengthen the central portion of said frames.

Landscapes

  • 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

Jan. 3, 1956 w. F. BERG HEAT EXCHANGER WITH REMOVABLE TUBE BANKS 3 Sheets-Sheet 1 Filed Jan. '7, 1952 INI-ENTOR. WzZlzam EBerg QWMQ /JQJW ATTORNEYS.
Jan. 3, 1956 W. F. BERG HEAT EXCHANGER WITH REMOVABLE TUBE BANKS Filed Jan. 7, 1952 3 Sheets-Sheet 2 7 /6 l9 Z/ [I J f /5 000000 o 29 00000 0 Q2 17 0 0 0 0 00 J l I I I I Z6 24 I9 Z5 Z5 Z6 w 0 IN VEN TOR.
William EBezfg W Q M AT TORNEYS.
Jan. 3, 1956 w. F. BERG HEAT EXCHANGER WITH REMOVABLE TUBE BANKS 3 Sheets-Sheet 3 Filed Jan. 7, 1952 ZNVENTOR. William RBerg gnaw/9 M ATTORNEYS.
United States Patent HEAT EXCHANGER WITH REMOVABLE TUBE BANKS William F. Berg, Eimhurst, N. Y., assignor to A. 0. Smith Corporation, Milwaukee, Wis, a corporation York Application January 7, 1952, Serial No. 265,253
3 Claims. (Cl. 257-241) Thisinvention relates to heat exchangers and more particularly toan air cooler having a plurality of heat transfer core sections which are arranged in the form of an annular bank or ring within the cooler.
An object ofthe present invention isto provide a heat exchanger wherein the heat transfer surfaces are in the form of a plurality of circularly disposed longitudinal tube units and the fluid to be heated or cooledis directed radially through the units.
Another object is to provide a heat exchanger having a large face area for a given cross sectional area of the heat exchanger.
Another object is to provide a gas to liquid heat exchanger which will effectively cool a large mass of gas without producing an appreciable pressure drop in the gas-being cooled.
Another object is to provide a heat exchanging apparatus wherein the temperature of the air being discharged from the apparatus may be conveniently controlled.
Still another object is to provide a heat exchanging apparatus having a plurality of independent heat transfer core sections which are removably secured to the exterior of the apparatus and may be readily withdrawn from the cooler for repair or cleaning.
A further object is to provide a simple and effective means of attaching a plurality of heat transfer core sections in the pattern of an annular bank, within a heat exchanger.
Another object is to provide heat transfer sections in a heat exchanger wherein all of thefittings for connections are disposed outside the shell of the unit for ready assembly and disassembly.
' The present invention is directed to a barrel-shaped air cooler which comprises a generally cylindrical shell having suitable openings in opposite ends thereof for the entry and discharge of a-fluid'such as air. The heat exchanging surface takes the form of an annular bank or ring which comprises a plurality of independent longitudinally disposed heat transfer core sections and is inwardly. spaced from the shell about the air inlet. An end plate closes off the rear end of the heat transfer chamber and prevents the longitudinal passage of air therethrough. The air enters the hollow interior of the annular bank through the inlet in the shell and is directed radially outwardly through the bank of core sections andis cooled as it passes therethrough. After cooling, the air passes longitudinallyin the annular space between the heat transfer bank and the shell, and then inwardly around the rear of the annulat bank to the discharge outlet in the shell.
By providing the end plate with adjustable valves or flaps, a portion of the entering air may be by-passed directly through the hollow interior of the annular bank without passing radially through the heat exchanging core sections, and by varying the amount of by-passed air the temperature of the discharged air can be readily controlled.
It is desirable for an air cooler to have a large face area per mass of air passing therethrough so as to keep 2,729,433 Fatented Jan. 3,, 1956 "ice the pressure drop of air passing through the cooler to a minimum. Ordinarily an increase, in face area is accomplished by increasing the cross sectional area or diameter of the cooler and this increased cooler size is frequently obiectionable for installation and economic reasons.
By providing the heat transfer surfaces in the form of an annular bank a greater heat transfer face area may he obtained for a given diameter shell than in an air cooler wherein the air passesstraight through a heat transfer surface disposed in a plane normal to the general flow of air or through a herringbone type cooler. Additional face area can be attained in the present barrel-type cooler without enlarging the diameter of the shell by. merely increasing the length of the heat transfer core sections.
Other objects and advantages will appear in the course of the following description.
in the drawings:
Figure 1 is a front elevational view of the heat exchanger;
Fig. 2 is a central vertical section of the heat exchanger;
Fig. 3 is a fragmentary transverse section taken along line 3-3 of Fig. 2 showing the disposition of core sections within the annular bank;
Fig. 4 is a perspective of one of the frames of the annular heat transfer bank;
Fig. 5 is a longitudinal section taken along line 5-5 of Figure 1 with a portion of the core section being shown in side elevation, and;
Fig. 6 is a longitudinal section taken along line 6-6 of Fig. 5 showing the structure of the core sections.
Referring to the drawings there is shown a fluid type heat exchanger having a hollow external casing or shell 1 which includes a generally cylindrical body section 2 and a generally conical end cap 3.
A pair of generally circular spider plates 4 and 5 are longitudinally spaced and secured edgewise by welding or the like to the inner surface of body section 2.
Front spider plate 4 is provided with an axial opening 6 through which a fluid to be heated or cooled, such as air, is admitted into the shell 1. Plate4 is also provided with a plurality of circumferentially spaced generally rectangular flanged openings 7 which are spaced inwardly from the circumference of plate 4 and arranged about axial opening 6.
A flanged pipe connection 8 is welded within axial opening 6 and provides a means for attaching an air inlet pipe, not shown, to the heat exchanger. I
The rear spider plate 5 is secured to the rear end of section 2 by a weld 9 and has a plurality of rectangular circumferentially spaced openings 10 adjacent its peripheral edge. The plate 5 is formed with a central conical portion 11 directed toward the inlet opening 6 to aid in deflecting the incoming air radially outward through the tube units as will be described.
End cap 3 is provided with an outlet opening 12 for the discharge of cooled air. A flanged pipe connection 23 is secured to cap 3 around opening 12 and provides a means for attaching an air discharge conduit, not shown, to cap 3.
A polygonal annular heat exchanging ring or bank 14 is disposed within shell 1 and spaced radially inward therefrom. The hollow interior of the bank 14 registers with the axial opening 6 in the spider plate 4. The heat exchanging bank 14 comprises, in general, a plurality of generally rectangular longitudinally disposed frames 15 which are secured in the form of a polygonal annulus or ring between spider. plates 4 and 5' and register witl openings 7 in plate 4, and a plurality of heat transfer core sections 16 which are inserted within shell 1 through openings 7 and are supported by, the respective frames 15.
As shown in Fig. 4 each of the frames 15 includes four longitudinal angle iron guide bars 17, disposed to define a rectangular frame, and which are connected at their ends and central portions by a plurality of side plates 18 and cross ties 19 to provide a rigid integral structure.
Frames 15 are aligned behind the corresponding openings 7 in plate 4, and the side plates 18 at the ends of each frame are attached to the respective plates 4 and by angle brackets 20.
To further secure frames 15, a pair of radial braces 21 extend outwardly from the central portion of each frame and are welded to the inner surface of shell 1.
A plurality of longitudinal sealing strips 22 are secured between the inner guide bars 17 of adjacent frames to seal off the space between frames to the passage of air.
The core sections 16 of heat transfer bank 14 which are supported by frames 15 include a cluster or bundle of longitudinally disposed tubes 23 within which a heating or cooling fluid, depending on the operation, is adapted to circulate. Tubes 23 may be constructed of any material which has generally high thermal conductivity properties and which is able to withstand attack from the particular fluids employed in the heat exchanger.
To increase the effective heat transfer area of core sections 16 of a plurality of longitudinally spaced transverse fins 24 are secured to tubes 23. Fins 24 may be constructed of any material having a high heat conductivity and which may be readily attached to tubes 23.
To support the tubes 23 over their length each core section 16 is provided with a plurality of transverse support plates 25. Plates 25 are formed with a plurality of suitable circular openings which receive tubes 23. The corner extremities of each plate 25 are provided with projection or legs 26 which are adapted to engage the respective guide bars 17 of frame 15 so that the core section 16 may slide easily into position within frame 15.
The tubes 23 are secured at the front and rear end of core section 16 to a front tube plate 27 and a rear tube plate 28 respectively. Plates 27 and 28 are generally rectangular in shape and provided with a plurality of suitable openings within which the respective ends of tubes 23 are secured, by either welding, brazing, soldering or the like, depending on the metals employed.
Plates 27 are of greater size than the respective rectangular openings 7 in plate 4 so that the outer periphery of plates 27 will bear against plate 4 when core sections 16 are inserted into the annular heat transfer bank 14 through the openings 7.
The sides of each core section 16 are enclosed by a plurality of side plates 29 which are secured by welding to the respective tube plates 27 and 28 and to the support plates 25. Side plates 29 serve to seal 011 the space between core sections 16 to the passage of air and direct the air radially outward through the sections 16. It may be desirable to provide plates 29 with suitable expansion joints, not shown, to compensate for expansions of the plates 29 during operation of the heat exchanger.
A generally rectangular header box 30 is secured by welding to the outer face of front tube plate 27 and serves to distribute the cooling liquid or water to and from tubes 23. A rib 31 divides header box 30 into two chambers, an inlet chamber 32 and an outlet chamber 33. The tubes 23 in the inner half of the bundle register with inlet chamber 32 while the tubes in the outer half of the bundle register with outlet chamber 33. A fitting 34 is secured within a suitable opening in the outer face of header box 30 and establishes communication between chamber 32 and a suitable source of cooling liquid, and a second fitting 35 similarly provides communication between outlet chamber 33 and a suitable drain system. These fittings are all located outside of shell 1.
A header cap 36 is secured to the rear tube plate 28 and defines a return chamber 37. Water entering inlet chamber 32 through fitting 34 passes through the tubes 23 in the inner half of the bundle to return chamber 37 and thence is returned through the tubes in the outer half 4 of the bundle to the outlet chamber 33. By providing chambers 32, 33 and 37 with ribs similar to rib 31 the number of passes that the water makes through the core section 16 can be correspondingly increased. The number of passes required depends on the type of operation in which the heat exchanger is employed.
The core sections 16 are inserted into shell 1 through openings 7 to comprise the heat transfer bank 14. Legs 26 ride on guide bars 17 of frame 15 and each core section is pushed inwardly until the peripheral edge of tube plate 27 bears against spider plate 4. A plurality of bolts 38 serve to secure the peripheral edge of each plate 27 to plate 4.
The inner or rear end of each core section 16 is not attached to any member but merely rest on the frame 15 and is free to float with the expansion and contraction of the core section during operation of the heat exchanger.
Each core section 16 is independently mounted within bank 14 with the respective tube plates 27 of each core section being removably secured to plate 4 by bolts 38. Thus each core section may be readily removed from the bank for cleaning or repair without disturbing the remaining core sections or altering the apparatus by merely unfastening bolts 38.
The air to be cooled enters the hollow interior of the bank 14 through opening 6 in spider plate 4 and is directed radially outward through the core sections 16 of the bank and across the finned tubes 23. Heat is transferred from the air to the cooling medium within tubes 23. The cooled air then passes longitudinally within the annular space between the bank 14 and the body section 2 through openings 10 and is discharged from the shell through outlet 12.
To control the temperature of the air being discharged through outlet 12 a valving arrangement is provided to permit any desired amount of the entering air to pass directly through shell 1 without passing through the core sections 16. This is accomplished by providing end plate 11 with a plurality of generally rectangular circumferentially spaced openings 39 and a plurality of hinged, adjustable valves or flaps 40 to close said openings. The valves 40, when open, permit air to pass longitudinally through annulus 14 to the discharge outlet 12.
In addition a plurality of generally rectangular hinged flaps 41 are employed to control the flow of air through opening 10 in rear spider plate 5.
Flaps 40 and 41 may be operated manually by ropes or chains or electrically or by any other desired means.
It may be preferred to operate corresponding radial flaps 40 and 41 together. That is, as flaps 40 in end plate 11 are opened to allow air to by-pass core sections 16, flaps 41 are closed to reduce the flow of air through the core sections. Thus when flaps 40 are completely open, flaps 41 are entirely closed and all the air will by-pass the core sections. Conversely when end plate flaps 40 are closed, flaps 41 are open and all the air will be directed across the core sections.
By arranging the heat transfer core sections in the shape of a ring or annulus the present invention provides a maximum face area for a given shell diameter and thereby 7 reduces the pressure loss of the air passing through the unit.
The present invention may be adapted for use in large or small installations and will function elfectively to cool great or small masses of air. Furthermore, the temperature of the air being discharged from the unit may be accurately controlled through use of the by- pass valves 40 and 41.
As described, the air or gas to be cooled enters opening 6 in shell 1 and passes radially outward across the core sections 16, and is discharged through opening 12. However the apparatus will operate with equal effectiveness if the air is introduced into shell 1 through opening 12 and passes radially inward across core sections 16 and is dis- 14 having equal or unequal cross sectional areas may be employed within a given shell and arranged therein in a parallel relation, in series, i n a staggered relation or in any desired configuration to effect the heat transfer for a given operation.
The exchanger can still remain in operation if it is necessary to remove one or more units for repair or cleaning purposes.
Various embodiments of the invention may be employed within the scope of the following claims.
I claim:
1. A heat transfer apparatus comprising a generally cylindrical casing having a centrally disposed fluid inlet opening at one end and a centrally disposed fluid outlet opening at the other end, an annular member secured at its periphery to said casing and located adjacent said outlet opening, an inner set of circumferentially spaced openings disposed in said annular member to provide for passage of untreated fluid through said member, an outer set of circumferentially spaced openings disposed outwardly from the first set to provide for passage of treated fluid through said annular member, closure means pivoted to said annular member adjacent both said first and said second spaced openings to permit opening and closing of said openings and thereby control the flow of treated and untreated fluid through the outlet and the temperature of the fluid discharged from the apparatus, a pair of longitudinally spaced spider plates assembled with said casing, longitudinally extending frame members of generally rectangular shape assembled annularly and secured at their respective ends to said spider plates to provide a plurality of independent frame members spaced annularly about the inside of said casing and removed inwardly from the casing wall to provide a longitudinal passage between the casing and frames extending the length of the casing to the outer set of spaced openings, the exit end of each frame member being secured to said annular member and the entry end of each frame being secured to the entry end of the casing, means to seal off the longitudinal passage at the entry end of the casing, heat exchange core units removably disposed in each frame and with each unit being independent of the other units, baffle means extending centrally from said annular memher and toward the inlet opening to direct a portion of the fluid entering the casing radially across said units, and a longitudinally extending strip secured to the inner portion of adjacent frame members and extending between said adjacent frame members to seal off the passage of fluid between the core units and effectively direct the fluid across the core units.
2. The apparatus of claim 1, and a pair of radial braces extending outwardly from the central portion of each frame member and secured to the inner surface of the casing to strengthen the central portion of said frames.
3. The apparatus of claim 1 in which the sealing strip comprises a longitudinally disposed strip secured to the inner adjacent frame members and extending therebetween to seal off the space between the core units to the passage of fluid and thereby effectively direct fluid across the core units, and a pair of radial braces extending outwardly from the central portion of each frame and secured to the inner surface of the casing to strengthen the central portion of said frames.
References Cited in the file of this patent UNITED STATES PATENTS 1,737,189 Haber Nov. 26, 1929 1,784,956 Benjamin Dec. 16, 1930 2,038,002 Ris Apr. 21, 1936 2,336,840 Brehob Dec. 14, 1943 2,421,371 Budlane June 3, 1947 2,423,175 Churchill et a1. June 1, 1947 2,521,866 Ott Sept. 11, 1950 2,615,687 Simons Oct. 28, 1952 2,650,073 Holm Aug. 25, 1953
US265253A 1952-01-07 1952-01-07 Heat exchanger with removable tube banks Expired - Lifetime US2729433A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US265253A US2729433A (en) 1952-01-07 1952-01-07 Heat exchanger with removable tube banks

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US265253A US2729433A (en) 1952-01-07 1952-01-07 Heat exchanger with removable tube banks

Publications (1)

Publication Number Publication Date
US2729433A true US2729433A (en) 1956-01-03

Family

ID=23009678

Family Applications (1)

Application Number Title Priority Date Filing Date
US265253A Expired - Lifetime US2729433A (en) 1952-01-07 1952-01-07 Heat exchanger with removable tube banks

Country Status (1)

Country Link
US (1) US2729433A (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2938712A (en) * 1955-05-03 1960-05-31 Svenska Flaektfabriken Ab Air preheater
US3012547A (en) * 1955-04-21 1961-12-12 Westinghouse Electric Corp Unitized steam generator
US3031563A (en) * 1959-05-25 1962-04-24 Turbine Equipment Company Multiple pass electric heater for fluids
US3155158A (en) * 1960-03-25 1964-11-03 English Electric Co Ltd Header type tubular heat exchanger
US3187808A (en) * 1962-05-23 1965-06-08 American Schack Company Inc High temperature recuperator
US3259177A (en) * 1962-07-11 1966-07-05 Gea Luftkuehler Happel Gmbh Liquid cooler and control therefor
US3373802A (en) * 1964-12-07 1968-03-19 Reymersholms Gamla Ind Ab Heat exchanger with removable tube groups of decreasing flow area
US3435890A (en) * 1966-04-22 1969-04-01 Babcock & Wilcox Ltd Heat exchanger
US3447598A (en) * 1967-05-12 1969-06-03 Pullman Inc Air cooled heat exchanger
US3991821A (en) * 1974-12-20 1976-11-16 Modine Manufacturing Company Heat exchange system
US4253516A (en) * 1978-06-22 1981-03-03 Westinghouse Electric Corp. Modular heat exchanger
US4299273A (en) * 1977-09-14 1981-11-10 Sulzer Brothers Ltd. Heat exchanger, especially recuperator for high temperature reactors
US4592416A (en) * 1985-04-29 1986-06-03 The Air Preheater Company, Inc. Modular tubular heat exchanger
US6735953B1 (en) * 1997-12-22 2004-05-18 Allied Signal Inc. Turbomachine-driven environmental control system
US20050252645A1 (en) * 2002-06-28 2005-11-17 Methanol Casale S.A. Multiservice heat exchange unit
US20070023173A1 (en) * 2005-07-27 2007-02-01 Nelson John A Heat exchanger
US20080128580A1 (en) * 2006-05-17 2008-06-05 Wilson Rickey A Polygon Tumble Assembler
US20110139410A1 (en) * 2009-12-16 2011-06-16 Lennox International, Inc. Floating Coil Heat Exchanger
US10739078B2 (en) 2015-01-15 2020-08-11 A Markussen Holding As Heat exchanger

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1737189A (en) * 1923-10-31 1929-11-26 Haber Eugen Heat exchanger
US1784956A (en) * 1924-07-28 1930-12-16 Edward O Benjamin Distilling apparatus and method
US2038002A (en) * 1934-05-08 1936-04-21 Griscom Russell Co Heat exchanger
US2336840A (en) * 1942-07-04 1943-12-14 Gen Electric Radiator arrangement
US2421371A (en) * 1944-04-29 1947-06-03 Herman Nelson Corp Heat exchanger
US2423175A (en) * 1943-11-15 1947-07-01 Churchill John Adrian Heat exchange apparatus
US2521866A (en) * 1946-09-09 1950-09-12 Oran W Ott Air-heating furnace with automatically controlled air by-pass for preventing condensation
US2615687A (en) * 1948-01-03 1952-10-28 American Blower Corp Heat exchanger
US2650073A (en) * 1949-06-25 1953-08-25 Air Preheater Combined regenerator and precooler for gas turbine cycles

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1737189A (en) * 1923-10-31 1929-11-26 Haber Eugen Heat exchanger
US1784956A (en) * 1924-07-28 1930-12-16 Edward O Benjamin Distilling apparatus and method
US2038002A (en) * 1934-05-08 1936-04-21 Griscom Russell Co Heat exchanger
US2336840A (en) * 1942-07-04 1943-12-14 Gen Electric Radiator arrangement
US2423175A (en) * 1943-11-15 1947-07-01 Churchill John Adrian Heat exchange apparatus
US2421371A (en) * 1944-04-29 1947-06-03 Herman Nelson Corp Heat exchanger
US2521866A (en) * 1946-09-09 1950-09-12 Oran W Ott Air-heating furnace with automatically controlled air by-pass for preventing condensation
US2615687A (en) * 1948-01-03 1952-10-28 American Blower Corp Heat exchanger
US2650073A (en) * 1949-06-25 1953-08-25 Air Preheater Combined regenerator and precooler for gas turbine cycles

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3012547A (en) * 1955-04-21 1961-12-12 Westinghouse Electric Corp Unitized steam generator
US2938712A (en) * 1955-05-03 1960-05-31 Svenska Flaektfabriken Ab Air preheater
US3031563A (en) * 1959-05-25 1962-04-24 Turbine Equipment Company Multiple pass electric heater for fluids
US3155158A (en) * 1960-03-25 1964-11-03 English Electric Co Ltd Header type tubular heat exchanger
US3187808A (en) * 1962-05-23 1965-06-08 American Schack Company Inc High temperature recuperator
US3259177A (en) * 1962-07-11 1966-07-05 Gea Luftkuehler Happel Gmbh Liquid cooler and control therefor
US3373802A (en) * 1964-12-07 1968-03-19 Reymersholms Gamla Ind Ab Heat exchanger with removable tube groups of decreasing flow area
US3435890A (en) * 1966-04-22 1969-04-01 Babcock & Wilcox Ltd Heat exchanger
US3447598A (en) * 1967-05-12 1969-06-03 Pullman Inc Air cooled heat exchanger
US3991821A (en) * 1974-12-20 1976-11-16 Modine Manufacturing Company Heat exchange system
US4299273A (en) * 1977-09-14 1981-11-10 Sulzer Brothers Ltd. Heat exchanger, especially recuperator for high temperature reactors
US4253516A (en) * 1978-06-22 1981-03-03 Westinghouse Electric Corp. Modular heat exchanger
US4592416A (en) * 1985-04-29 1986-06-03 The Air Preheater Company, Inc. Modular tubular heat exchanger
US6735953B1 (en) * 1997-12-22 2004-05-18 Allied Signal Inc. Turbomachine-driven environmental control system
US20050252645A1 (en) * 2002-06-28 2005-11-17 Methanol Casale S.A. Multiservice heat exchange unit
US20070023173A1 (en) * 2005-07-27 2007-02-01 Nelson John A Heat exchanger
US20080128580A1 (en) * 2006-05-17 2008-06-05 Wilson Rickey A Polygon Tumble Assembler
US8056229B2 (en) * 2006-05-17 2011-11-15 Babcock & Wilcox Power Generation Group, Inc. Method of manufacturing a tubular support structure
US20110139410A1 (en) * 2009-12-16 2011-06-16 Lennox International, Inc. Floating Coil Heat Exchanger
US10739078B2 (en) 2015-01-15 2020-08-11 A Markussen Holding As Heat exchanger

Similar Documents

Publication Publication Date Title
US2729433A (en) Heat exchanger with removable tube banks
US2499901A (en) Fin tube assembly
US2411097A (en) Heat exchanger
US3483920A (en) Heat exchangers
US2730337A (en) Heat exchanger
US2372079A (en) Heat exchanger
US3033534A (en) Toroidal heat exchangers
US2236976A (en) Method of making heat exchangers
US3306351A (en) Heat exchanger for cooling cracked gases by multiple media
US2418191A (en) Heat exchanger
US3746083A (en) Heat-exchanger
US2360094A (en) Heat exchanger
US3507323A (en) Tube heat exchanger
CN104457343B (en) A kind of tubular arc heat exchange plate type heat-exchanger rig
US3734176A (en) Heat exchanger assembly having a common fluid box
US1916768A (en) Heat exchanger
WO1982000343A1 (en) Heat exchanger for flowing media
US3628508A (en) Waste-heat boilers and like gas/liquid heat transfer systems
RU2206851C1 (en) Shell-and-plate heat exchanger (modofocations)
US2452391A (en) Heat exchanger
US2806676A (en) Heat transfer apparatus
US3348610A (en) Heat exchangers for cooling fresh cracked gases or the like
US2729432A (en) Large capacity heat exchanger
US3244225A (en) Heat exchanger
US1813057A (en) Apparatus for heat exchanging