US3656543A - Liquid metal heat exchanger - Google Patents

Liquid metal heat exchanger Download PDF

Info

Publication number
US3656543A
US3656543A US40036A US3656543DA US3656543A US 3656543 A US3656543 A US 3656543A US 40036 A US40036 A US 40036A US 3656543D A US3656543D A US 3656543DA US 3656543 A US3656543 A US 3656543A
Authority
US
United States
Prior art keywords
tube
tube sheet
funnel
heat exchanger
inlet
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
US40036A
Inventor
Walter Wolowodiuk
Tobias Stern
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.)
Foster Wheeler Inc
Original Assignee
Foster Wheeler Inc
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 Foster Wheeler Inc filed Critical Foster Wheeler Inc
Application granted granted Critical
Publication of US3656543A publication Critical patent/US3656543A/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
    • 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
    • F28D7/005Heat-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 for only one medium being tubes having bent portions or being assembled from bent tubes or being tubes having a toroidal configuration
    • 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
    • F28D7/163Heat-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 with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
    • F28D7/1669Heat-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 with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing the conduit assemblies having an annular shape; the conduits being assembled around a central distribution tube
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/007Auxiliary supports for elements
    • F28F9/013Auxiliary supports for elements for tubes or tube-assemblies
    • 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
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0054Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for nuclear applications
    • 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
    • F28F2009/222Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F28F2009/226Transversal partitions
    • 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
    • Y10S165/355Heat exchange having separate flow passage for two distinct fluids
    • Y10S165/40Shell enclosed conduit assembly
    • Y10S165/427Manifold for tube-side fluid, i.e. parallel
    • Y10S165/432Manifold for tube-side fluid, i.e. parallel including a tube sheet

Definitions

  • a funnel leading into a central downcomer separates [56] References cued cold incoming secondary liquid metal from the relatively hot UNITED STATES PATENTS Outgomg Secondary q metal- 3,490,521 1/1970 Byerley ..l65/161 9Claims,4Drawing Figures PATENTEDAER 18 1912 INVENTORS WALTER WOLOWOD/UK TOBIAS STERN BY ATTORNEY LIQIJW METAL HEAT EXCHANGER BACKGROUND OF THE NVEN'lION The invention described herein was made in the course of, or under, a contract with the United States Atomic Energy Commission.
  • a typical liquid metal suitable for this application is molten sodium.
  • the present invention overcomes drawbacks in the prior art, such as the difficulties mentioned above by providing heat exchange apparatus in which the tubes are readily accessible for maintenance and repair, and incorporating a thermal barrier to reduce thermal stresses as a result of temperature differences between the cold incoming secondary liquid metal and the remaining sodium in the apparatus.
  • FIG. 1 is an elevation view in section of a heat exchanger made in accordance with this invention
  • FIG. 2 is a view along 22 ofFIG. 1;
  • FIG. 3 is a sectional view showing in detail a portion of the heat exchanger of FIG. I.
  • FIG. 4 is a sectional view showing in detail another portion ofthe heat exchanger of FIG. 1.
  • heat exchanger consists of an outer cylindrical shell 12 forming a lower section of the heat exchanger 10 and having a curved bottom 14 having a primary outlet 16. Adjacent to the upper end of the shell 12 is a primary inlet 18 above which is a cylindrical upper section 22 which is provided on one side with a secondary outlet 24 in the lower portion thereof.
  • the upper section 22 is of larger diameter than the shell 12.
  • a secondary inlet 26 is located in section 22 at a location above that of secondary outlet 24.
  • the top of upper section 22 is closed off with an inverted hemispherical head 28 having a flange 32 which is bolted to a flange 34 of upper section 22. Inverted head 28 reduces the liquid metal content on the secondary side.
  • a flange 34 which forms the lower end of the upper section 22.
  • the flange 34 forms the support for a removable core 35 which is positioned within the section 22.
  • Clamping ring 36 holds in place an annular tube sheet 38 while bolts 42 spaced along ring 36 threaded into flange 34- hold the former in place.
  • a downcomer tube 44 which at the lower end thereof supports a lower annular tube sheet 46 from which extends an elliptical head 48 forming a collection compartment 52.
  • Spacer brackets 54 are provided for centering purposes.
  • the upper end 55 of downcomer tube 44- attaches to the lower face of the upper tube sheet 38 which in turn rests on flange 34.
  • a welded omega seal 56 is provided between the upper tube sheet 38 and the flange 36.
  • a funnel-like member 53 having a lower cylindrical portion which extends down into downcomer tube 44 and an upper portion which flares upwardly and outwardly is bolted at its peripheral marginal portion to a support ring 59 which is mounted on the inside wall of the upper section 22.
  • the lower portion of the funnel-like member 53 extends down into downcomer tube 44 to serve as a thermal barrier to reduce the thermai stresses in tube sheet 33 and also to reduce leakage of incoming cold secondary sodium into outgoing hot secondary sodium chambers.
  • a thin sleeve 69 (FIG. 3) made of stainless steel in its upper portion and of a material having a lower coefficient of expansion than stainless steel in its lower portion is posit oned snugly between the upper tube sheet 38 and the lower portion of member 58 to reduce further the leakage of secondary sodium.
  • a second flared member 61 located below the funnel member 58 is connected with that section through a cylindrical member 62 which extends from the outer edge of the section 6?. upwardly to the funnel member 58 as shown best perhaps in MG.
  • the upper funnel member 58 is thick enough to withstand the pressure of the secondary fluid and the lower flared member 61 is made thin enough to serve as a thermal barrier for the upper funnel 58.
  • Metallic thermal insulation 63 reduces the thermal gradient in the portion of the upper section 22 located between the secondary fluid outlet nozzle 24 and the support ring 59.
  • tube bundle 66 Connecting upper and lower tube sheets 38 and 46, respectively, is an annular assembly of tubes referred to as tube bundle 66, welded at both ends to their respective tube sheets.
  • Flow battles 63 also serve a tube supports.
  • the baffle arrangement is not a part of this invention, being part of an invention covered by U.S. application Ser. No. 8501, entitled Liquid Metal i-ieat Exchanger, filed Feb. 4, 1970 in the name of Walter Wolowodiuk, one of the inventors herein.
  • hot primary sodium enters through inlet 18, circulates around the tubes in bundle 66, filling the annular space around downcomer 44 and leaves through outlet 16 at the bottom of shell 12.
  • Single marked arrows show primary flow while double headed arrows show secondary flow.
  • Relatively cold secondary sodium enters through upper nozzle 26, flows downward through funnel-like member 58, downcomer tube 44, and into lower compartment 52. The sodium then passes up through tube sheet 46 into the tubes of bundle 66, through tube sheet 38 and out through nozzle 24.
  • the construction permits tube plugging without removing the tube bundle 66. This is accomplished by removing inverted hemispherical head 28 and the upper funnel-like member 58 with its associated lower member 64 which exposes upper tube sheet 38 for maintenance work. For the removal of bundle 66, ring 36 is unbolted and lifted out, omega seal 56 is cut and bundle 66 is lifted out of shell 12.
  • a liquid metal heat exchanger comprising:
  • a cylindrical shell having an upper section and a lower section
  • an axially disposed removable core means extending down into the lower section of said shell; said core means comprising a cylindrical tube extending down into said lower section and positioned so that the narrow part of said funnel communicates with said tube; a lower annular tube sheet mounted on the bottom of and surrounding said tube; a closure enclosing the bottom of said tube and lower tube sheet forming a lower compartment; an upper annular tube sheet encircling said tube and removably attached at its periphery to said shell; and a bundle of tubes extending between said upper and lower tube sheets to complete a flow path of secondary coolant flowing down through said funnel-shaped member, tube, lower compartment, and up through said bundle of tubes;
  • a secondary sodium inlet and a secondary sodium outlet in said upper section both being in the side wall of said upper section of said shell at a location laterally beyond the peripheries of said upper and lower annular tube sheets, said inlet being laterally beyond the periphery of said funnel-shaped member, said inlet directing fluid over said funnel-shaped member to flow downward through said tube, said outlet being disposed below said funnel-shaped member but above said upper tube sheet to direct secondary fluid coming out of said tube bundle out of said exchanger;
  • liquid metal heat exchanger defined in claim 1 wherein said means for suspending and clamping the top of said removable core means comprises an annular flange, said upper tube sheet being removably connected with said flange.
  • liquid metal heat exchanger defined in claim 4 further comprising a head, said head closing the top of said upper section and being bolted about its periphery to the top of said upper section.
  • a heat exchanger for placing two fluids in indirect heat exchange comprising: a shell; an intake in the side wall of said shell for a first of said fluids; an exhaust for said fluid positioned below said intake; a tube; a first annular tube sheet and a second annular tube sheet, said tube sheets encircling and being axially positioned with respect to said tube, said first tube sheet being closer to said intake than said second tube sheet; a tube bundle extending between said tube sheets; a chamber contiguous to said second tube sheet whereby said first fluid comes in through said intake, flows over said tube bundle outside of said chamber and exits at said exhaust, an inlet for a second of said fluids, said inlet being positioned laterally of said tube sheets, a funnel-like member for directing said second fluid from said inlet to said tube; an outlet for the second of said fluids, said outlet being between said first tube sheet and said funnel-like member, whereby said second fluid comes in through said inlet, passes through said funnel and said tube to said chamber, then passes through said tube bundle and out
  • the heat exchanger defined in claim 6 further comprising a clamping ring, said clamping ring being positioned over the outer peripheral marginal portion of said first tube sheet and bolted to said heat exchanger.

Abstract

A liquid metal heat exchanger providing for a single pass of primary liquid metal and two passes of secondary liquid metal consisting of a removable core suspended at the top by an annular tube sheet clamped by a bolted ring for convenient removal. A funnel leading into a central downcomer separates cold incoming secondary liquid metal from the relatively hot outgoing secondary liquid metal.

Description

0 United States Patent [151 3,656,543 Wolowodiuh et a1. [45] Apr. 18, 1972 [54] LIQUID METAL HEAT EXCHANGER 1,990,251 2/1935 Potter ..l65/75 x 3 059 908 10/1962 Fox et al.... ..165/74 [72] Inventors: Walter Wolowodruk New Provldence;
Tobias stem, Rockaway, both of Ni 3,325,374 6/1967 Margen ..l22/32 X [73] Assignee: Foster Wheeler Corporation, Livingston, FOREIGN PATENTS OR APPLICATIONS 835,266 5/1960 Great Britain ..l76/65 [22] Filed: May 25, 1970 P I E Ch 1 S k l rzmary xammerares u a0 [21] Appl' 40,036 Attorney-Roland A. Anderson 52 use: ..165/74,165/l58, 176/65, 7] TR 51 I Cl A liquid metal heat exchanger providing for a single pass of 58 F ld lllll IIIIIIIIIIIIIIIIIIIIIIIIII 15g 161 P mary liquid metal and two passes of secondary liquid metal 1 1e 0 /32 i consisting of a removable core suspended at the top by an annular tube sheet clamped by a bolted ring for convenient removal. A funnel leading into a central downcomer separates [56] References cued cold incoming secondary liquid metal from the relatively hot UNITED STATES PATENTS Outgomg Secondary q metal- 3,490,521 1/1970 Byerley ..l65/161 9Claims,4Drawing Figures PATENTEDAER 18 1912 INVENTORS WALTER WOLOWOD/UK TOBIAS STERN BY ATTORNEY LIQIJW METAL HEAT EXCHANGER BACKGROUND OF THE NVEN'lION The invention described herein was made in the course of, or under, a contract with the United States Atomic Energy Commission.
In the development of liquid metal fast breeder reactors, it is necessary to produce effective and reliable heat exchange apparatus for the transfer of heat from the primary liquid metal reactor coolant to suitable secondary liquid metal. A typical liquid metal suitable for this application is molten sodium.
Among the difficulties involved in the design and development of suitable heat exchange apparatus are those having to do with conducting maintenance operations in a liquid sodium environment, absorbing stresses induced by thermal gradients, and others which will become apparent from the description of this invention.
SUMMARY OF THE INVENTION The present invention overcomes drawbacks in the prior art, such as the difficulties mentioned above by providing heat exchange apparatus in which the tubes are readily accessible for maintenance and repair, and incorporating a thermal barrier to reduce thermal stresses as a result of temperature differences between the cold incoming secondary liquid metal and the remaining sodium in the apparatus.
It is thus one of the objects of this invention to provide an improved heat exchanger with improved maintenance and repair features and reduced thermal stresses.
BRIEF DESCRIPTION OF THE DRAWING FIG. 1 is an elevation view in section of a heat exchanger made in accordance with this invention;
FIG. 2 is a view along 22 ofFIG. 1;
FIG. 3 is a sectional view showing in detail a portion of the heat exchanger of FIG. I; and
FIG. 4 is a sectional view showing in detail another portion ofthe heat exchanger of FIG. 1.
DESCRIPTION OF THE PREFERRED EMBODIMENT Referring to the figures, heat exchanger consists of an outer cylindrical shell 12 forming a lower section of the heat exchanger 10 and having a curved bottom 14 having a primary outlet 16. Adjacent to the upper end of the shell 12 is a primary inlet 18 above which is a cylindrical upper section 22 which is provided on one side with a secondary outlet 24 in the lower portion thereof. The upper section 22 is of larger diameter than the shell 12. A secondary inlet 26 is located in section 22 at a location above that of secondary outlet 24. The top of upper section 22 is closed off with an inverted hemispherical head 28 having a flange 32 which is bolted to a flange 34 of upper section 22. Inverted head 28 reduces the liquid metal content on the secondary side.
It will be seen that at the top of the lower section 12 is a flange 34 which forms the lower end of the upper section 22. The flange 34 forms the support for a removable core 35 which is positioned within the section 22. Clamping ring 36 holds in place an annular tube sheet 38 while bolts 42 spaced along ring 36 threaded into flange 34- hold the former in place.
Extending down into lower section 12 is a downcomer tube 44 which at the lower end thereof supports a lower annular tube sheet 46 from which extends an elliptical head 48 forming a collection compartment 52. Spacer brackets 54 are provided for centering purposes.
The upper end 55 of downcomer tube 44- attaches to the lower face of the upper tube sheet 38 which in turn rests on flange 34. A welded omega seal 56 is provided between the upper tube sheet 38 and the flange 36.
A funnel-like member 53 having a lower cylindrical portion which extends down into downcomer tube 44 and an upper portion which flares upwardly and outwardly is bolted at its peripheral marginal portion to a support ring 59 which is mounted on the inside wall of the upper section 22. The lower portion of the funnel-like member 53 extends down into downcomer tube 44 to serve as a thermal barrier to reduce the thermai stresses in tube sheet 33 and also to reduce leakage of incoming cold secondary sodium into outgoing hot secondary sodium chambers. A thin sleeve 69 (FIG. 3) made of stainless steel in its upper portion and of a material having a lower coefficient of expansion than stainless steel in its lower portion is posit oned snugly between the upper tube sheet 38 and the lower portion of member 58 to reduce further the leakage of secondary sodium.
A second flared member 61 located below the funnel member 58 is connected with that section through a cylindrical member 62 which extends from the outer edge of the section 6?. upwardly to the funnel member 58 as shown best perhaps in MG.
The upper funnel member 58 is thick enough to withstand the pressure of the secondary fluid and the lower flared member 61 is made thin enough to serve as a thermal barrier for the upper funnel 58. Metallic thermal insulation 63 reduces the thermal gradient in the portion of the upper section 22 located between the secondary fluid outlet nozzle 24 and the support ring 59.
Connecting upper and lower tube sheets 38 and 46, respectively, is an annular assembly of tubes referred to as tube bundle 66, welded at both ends to their respective tube sheets. Flow battles 63 also serve a tube supports. The baffle arrangement is not a part of this invention, being part of an invention covered by U.S. application Ser. No. 8501, entitled Liquid Metal i-ieat Exchanger, filed Feb. 4, 1970 in the name of Walter Wolowodiuk, one of the inventors herein. A plurality of inner and outer spaced tie rods 72 and 74 respectively, having sleeves interconnect the flow baffles by welding and bolting as shown in FIG. 2 to obtain a more rigid structure.
in the operation of heat exchanger 16, hot primary sodium enters through inlet 18, circulates around the tubes in bundle 66, filling the annular space around downcomer 44 and leaves through outlet 16 at the bottom of shell 12. Single marked arrows show primary flow while double headed arrows show secondary flow. Relatively cold secondary sodium enters through upper nozzle 26, flows downward through funnel-like member 58, downcomer tube 44, and into lower compartment 52. The sodium then passes up through tube sheet 46 into the tubes of bundle 66, through tube sheet 38 and out through nozzle 24.
In the arrangement described, the construction permits tube plugging without removing the tube bundle 66. This is accomplished by removing inverted hemispherical head 28 and the upper funnel-like member 58 with its associated lower member 64 which exposes upper tube sheet 38 for maintenance work. For the removal of bundle 66, ring 36 is unbolted and lifted out, omega seal 56 is cut and bundle 66 is lifted out of shell 12.
What is claimed is:
l. A liquid metal heat exchanger comprising:
a cylindrical shell having an upper section and a lower section;
a funnel-shaped member in said upper section, said member being removably attached at the periphery thereof to said upper section;
an axially disposed removable core means extending down into the lower section of said shell; said core means comprising a cylindrical tube extending down into said lower section and positioned so that the narrow part of said funnel communicates with said tube; a lower annular tube sheet mounted on the bottom of and surrounding said tube; a closure enclosing the bottom of said tube and lower tube sheet forming a lower compartment; an upper annular tube sheet encircling said tube and removably attached at its periphery to said shell; and a bundle of tubes extending between said upper and lower tube sheets to complete a flow path of secondary coolant flowing down through said funnel-shaped member, tube, lower compartment, and up through said bundle of tubes;
means in said upper section f! suspending and clamping the top of said removable core means at the periphery of said upper tube sheet;
a secondary sodium inlet and a secondary sodium outlet in said upper section, said inlet and outlet both being in the side wall of said upper section of said shell at a location laterally beyond the peripheries of said upper and lower annular tube sheets, said inlet being laterally beyond the periphery of said funnel-shaped member, said inlet directing fluid over said funnel-shaped member to flow downward through said tube, said outlet being disposed below said funnel-shaped member but above said upper tube sheet to direct secondary fluid coming out of said tube bundle out of said exchanger; and
a primary sodium inlet in the upper portion of said lower section said primary sodium inlet being laterally beyond said bundle of tubes and said lower tube sheet, and a primary sodium outlet below said lower chamber.
2. The liquid metal heat exchanger defined in claim 1 wherein said means for suspending and clamping the top of said removable core means comprises an annular flange, said upper tube sheet being removably connected with said flange.
3. The liquid metal heat exchanger defined in claim 2 wherein said means for suspending and securing the top of said removable core means further comprises a clamping ring bolted to said flange, said clamping ring clamping said upper tube sheet between said ring and said flange.
4. The liquid metal heat exchanger defined in claim 3 wherein said upper tube sheet is supported upon the top of said cylindrical tube.
5. The liquid metal heat exchanger defined in claim 4 further comprising a head, said head closing the top of said upper section and being bolted about its periphery to the top of said upper section.
6. A heat exchanger for placing two fluids in indirect heat exchange comprising: a shell; an intake in the side wall of said shell for a first of said fluids; an exhaust for said fluid positioned below said intake; a tube; a first annular tube sheet and a second annular tube sheet, said tube sheets encircling and being axially positioned with respect to said tube, said first tube sheet being closer to said intake than said second tube sheet; a tube bundle extending between said tube sheets; a chamber contiguous to said second tube sheet whereby said first fluid comes in through said intake, flows over said tube bundle outside of said chamber and exits at said exhaust, an inlet for a second of said fluids, said inlet being positioned laterally of said tube sheets, a funnel-like member for directing said second fluid from said inlet to said tube; an outlet for the second of said fluids, said outlet being between said first tube sheet and said funnel-like member, whereby said second fluid comes in through said inlet, passes through said funnel and said tube to said chamber, then passes through said tube bundle and out said outlet, said funnel-like member and said first tube sheet being removably secured at their peripheries to said shell to permit access to said tube bundle by moving said funnel and then said first tube sheet and attached tube bundle axially out of said shell.
7. The heat exchanger defined in claim 6 further comprising a support ring, the peripheral marginal portion of said funnellike member being bolted to said ring.
8. The heat exchanger defined in claim 6 further comprising a clamping ring, said clamping ring being positioned over the outer peripheral marginal portion of said first tube sheet and bolted to said heat exchanger.
9. The heat exchanger defined in claim 8 wherein said tube and said tube bundle are substantially vertically disposed with said first tube sheet at a higher elevation than said second tube sheet, said funnel-shaped member having a lower cylindrical portion extending down into said tube, said first tube sheet having an inner marginal portion resting on the top of said tube.

Claims (9)

1. A liquid metal heat exchanger comprising: a cylindrical shell having an upper section and a lower section; a funnel-shaped member in said upper section, said member being removably attached at tHe periphery thereof to said upper section; an axially disposed removable core means extending down into the lower section of said shell; said core means comprising a cylindrical tube extending down into said lower section and positioned so that the narrow part of said funnel communicates with said tube; a lower annular tube sheet mounted on the bottom of and surrounding said tube; a closure enclosing the bottom of said tube and lower tube sheet forming a lower compartment; an upper annular tube sheet encircling said tube and removably attached at its periphery to said shell; and a bundle of tubes extending between said upper and lower tube sheets to complete a flow path of secondary coolant flowing down through said funnel-shaped member, tube, lower compartment, and up through said bundle of tubes; means in said upper section for suspending and clamping the top of said removable core means at the periphery of said upper tube sheet; a secondary sodium inlet and a secondary sodium outlet in said upper section, said inlet and outlet both being in the side wall of said upper section of said shell at a location laterally beyond the peripheries of said upper and lower annular tube sheets, said inlet being laterally beyond the periphery of said funnel-shaped member, said inlet directing fluid over said funnel-shaped member to flow downward through said tube, said outlet being disposed below said funnel-shaped member but above said upper tube sheet to direct secondary fluid coming out of said tube bundle out of said exchanger; and a primary sodium inlet in the upper portion of said lower section said primary sodium inlet being laterally beyond said bundle of tubes and said lower tube sheet, and a primary sodium outlet below said lower chamber.
2. The liquid metal heat exchanger defined in claim 1 wherein said means for suspending and clamping the top of said removable core means comprises an annular flange, said upper tube sheet being removably connected with said flange.
3. The liquid metal heat exchanger defined in claim 2 wherein said means for suspending and securing the top of said removable core means further comprises a clamping ring bolted to said flange, said clamping ring clamping said upper tube sheet between said ring and said flange.
4. The liquid metal heat exchanger defined in claim 3 wherein said upper tube sheet is supported upon the top of said cylindrical tube.
5. The liquid metal heat exchanger defined in claim 4 further comprising a head, said head closing the top of said upper section and being bolted about its periphery to the top of said upper section.
6. A heat exchanger for placing two fluids in indirect heat exchange comprising: a shell; an intake in the side wall of said shell for a first of said fluids; an exhaust for said fluid positioned below said intake; a tube; a first annular tube sheet and a second annular tube sheet, said tube sheets encircling and being axially positioned with respect to said tube, said first tube sheet being closer to said intake than said second tube sheet; a tube bundle extending between said tube sheets; a chamber contiguous to said second tube sheet whereby said first fluid comes in through said intake, flows over said tube bundle outside of said chamber and exits at said exhaust, an inlet for a second of said fluids, said inlet being positioned laterally of said tube sheets, a funnel-like member for directing said second fluid from said inlet to said tube; an outlet for the second of said fluids, said outlet being between said first tube sheet and said funnel-like member, whereby said second fluid comes in through said inlet, passes through said funnel and said tube to said chamber, then passes through said tube bundle and out said outlet, said funnel-like member and said first tube sheet being removably secured at their peripheries to said shell to permit access to said tube bundle by moving said funnel and then said first tube sheet and attached tube bundle axially out of said shelL.
7. The heat exchanger defined in claim 6 further comprising a support ring, the peripheral marginal portion of said funnel-like member being bolted to said ring.
8. The heat exchanger defined in claim 6 further comprising a clamping ring, said clamping ring being positioned over the outer peripheral marginal portion of said first tube sheet and bolted to said heat exchanger.
9. The heat exchanger defined in claim 8 wherein said tube and said tube bundle are substantially vertically disposed with said first tube sheet at a higher elevation than said second tube sheet, said funnel-shaped member having a lower cylindrical portion extending down into said tube, said first tube sheet having an inner marginal portion resting on the top of said tube.
US40036A 1970-05-25 1970-05-25 Liquid metal heat exchanger Expired - Lifetime US3656543A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US4003670A 1970-05-25 1970-05-25

Publications (1)

Publication Number Publication Date
US3656543A true US3656543A (en) 1972-04-18

Family

ID=21908741

Family Applications (1)

Application Number Title Priority Date Filing Date
US40036A Expired - Lifetime US3656543A (en) 1970-05-25 1970-05-25 Liquid metal heat exchanger

Country Status (5)

Country Link
US (1) US3656543A (en)
CA (1) CA919163A (en)
DE (1) DE2122054A1 (en)
FR (1) FR2090262B1 (en)
GB (1) GB1346111A (en)

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3784443A (en) * 1970-08-07 1974-01-08 Commissariat Energie Atomique Device for the leak-tight assembly of heat exchangers in nuclear reactors
US3896873A (en) * 1972-05-01 1975-07-29 Atomic Energy Commission Heat exchanger with a removable tube section
DE2913444A1 (en) * 1978-04-06 1979-10-18 Belleli Ind Mecc COUNTERFLOW HEAT EXCHANGER WITH TWO FIXED PIPE PLATES
US4312703A (en) * 1977-05-13 1982-01-26 B. V. Neratoom Nuclear reactor installation
US5785114A (en) * 1996-02-23 1998-07-28 Westinghouse Electric Corporation Integral hydrogen cooler assembly for electric generators
US20030102111A1 (en) * 2001-12-03 2003-06-05 Brinck Joseph A. Heat exchanger
US20030196781A1 (en) * 2002-04-23 2003-10-23 Wanni Amar S. Heat exchanger with floating head
WO2005075065A1 (en) * 2004-01-28 2005-08-18 Shell Internationale Research Maatschappij B.V. Heat-exchanger for carrying out an exothermic reaction
US20070175612A1 (en) * 2003-10-02 2007-08-02 Behr Gmbh & Co. Kg Charge intercooler for a motor vehicle
US20070199887A1 (en) * 2004-03-08 2007-08-30 Anne Boer Filter System With Filter Means Retractable Into A Housing
US20070228328A1 (en) * 2004-04-26 2007-10-04 Merck Patent Gmbh As-Indacen Derivatives
US20070254965A1 (en) * 2004-03-08 2007-11-01 Shell Oil Company Gas Distributor for a Reactor
US20110079747A1 (en) * 2009-10-02 2011-04-07 Mcwhorter Edward Milton Direct current simplex generator
US8148164B2 (en) 2003-06-20 2012-04-03 Roche Diagnostics Operations, Inc. System and method for determining the concentration of an analyte in a sample fluid
US8377707B2 (en) 2003-06-20 2013-02-19 Roche Diagnostics Operations, Inc. System and method for determining an abused sensor during analyte measurement
US8663442B2 (en) 2003-06-20 2014-03-04 Roche Diagnostics Operations, Inc. System and method for analyte measurement using dose sufficiency electrodes
US20170211887A1 (en) * 2016-01-22 2017-07-27 Fulton Group N.A., Inc. Tube configuration for a heat exchanger, heat exchanger including the tube configuration, fluid heating system including the same, and methods of manufacture thereof
US20190137192A1 (en) * 2014-09-05 2019-05-09 2078095 Ontario Limited Heat recovery apparatus and method
US11441850B2 (en) * 2020-01-24 2022-09-13 Hamilton Sundstrand Corporation Integral mounting arm for heat exchanger
US11453160B2 (en) 2020-01-24 2022-09-27 Hamilton Sundstrand Corporation Method of building a heat exchanger
US11460252B2 (en) 2020-01-24 2022-10-04 Hamilton Sundstrand Corporation Header arrangement for additively manufactured heat exchanger
US11703283B2 (en) 2020-01-24 2023-07-18 Hamilton Sundstrand Corporation Radial configuration for heat exchanger core
US11859832B2 (en) 2021-06-22 2024-01-02 2078095 Ontario Limited Gray water heat recovery apparatus and method

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2517694C2 (en) * 1975-04-22 1985-01-03 Hochtemperatur-Reaktorbau GmbH, 4600 Dortmund Heat exchangers with a circular or hexagonal cross-section with a number of tube bundles
FR2460273A1 (en) * 1979-06-29 1981-01-23 Inst Francais Du Petrole Recovering oil from tanks of submerged ship - uses alternate compressed air and water cycles to fill and discharge bell connected to surface
FR2524686A1 (en) * 1982-04-02 1983-10-07 Novatome HEAT AND RADIATION PROTECTION DEVICE FOR AN INTERMEDIATE HEAT EXCHANGER DRAINING IN A NUCLEAR REACTOR TANK
CN114136125B (en) * 2021-11-29 2022-11-15 无锡齐为金属科技有限公司 Double-tube heat exchange tube

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1990251A (en) * 1933-04-17 1935-02-05 Westinghouse Electric & Mfg Co Heat exchange apparatus
GB835266A (en) * 1955-07-08 1960-05-18 Gen Electric Improvements relating to nuclear reactors
US3059908A (en) * 1959-09-29 1962-10-23 Iii Thomas H Fox Heat exchanger
US3325374A (en) * 1963-07-19 1967-06-13 Atomenergi Ab Compact nuclear reactor and integral heat exchanger arrangement
US3490521A (en) * 1968-03-12 1970-01-20 Westinghouse Electric Corp Tube and shell heat exchanger

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1990251A (en) * 1933-04-17 1935-02-05 Westinghouse Electric & Mfg Co Heat exchange apparatus
GB835266A (en) * 1955-07-08 1960-05-18 Gen Electric Improvements relating to nuclear reactors
US3059908A (en) * 1959-09-29 1962-10-23 Iii Thomas H Fox Heat exchanger
US3325374A (en) * 1963-07-19 1967-06-13 Atomenergi Ab Compact nuclear reactor and integral heat exchanger arrangement
US3490521A (en) * 1968-03-12 1970-01-20 Westinghouse Electric Corp Tube and shell heat exchanger

Cited By (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3784443A (en) * 1970-08-07 1974-01-08 Commissariat Energie Atomique Device for the leak-tight assembly of heat exchangers in nuclear reactors
US3896873A (en) * 1972-05-01 1975-07-29 Atomic Energy Commission Heat exchanger with a removable tube section
US4312703A (en) * 1977-05-13 1982-01-26 B. V. Neratoom Nuclear reactor installation
DE2913444A1 (en) * 1978-04-06 1979-10-18 Belleli Ind Mecc COUNTERFLOW HEAT EXCHANGER WITH TWO FIXED PIPE PLATES
US5785114A (en) * 1996-02-23 1998-07-28 Westinghouse Electric Corporation Integral hydrogen cooler assembly for electric generators
US20030102111A1 (en) * 2001-12-03 2003-06-05 Brinck Joseph A. Heat exchanger
US20030196781A1 (en) * 2002-04-23 2003-10-23 Wanni Amar S. Heat exchanger with floating head
US6736199B2 (en) * 2002-04-23 2004-05-18 Exxonmobil Research And Engineering Company Heat exchanger with floating head
EP1357344A3 (en) * 2002-04-23 2007-04-25 ExxonMobil Research and Engineering Company Heat exchanger with floating head
US8148164B2 (en) 2003-06-20 2012-04-03 Roche Diagnostics Operations, Inc. System and method for determining the concentration of an analyte in a sample fluid
US8859293B2 (en) 2003-06-20 2014-10-14 Roche Diagnostics Operations, Inc. Method for determining whether a disposable, dry regent, electrochemical test strip is unsuitable for use
US8663442B2 (en) 2003-06-20 2014-03-04 Roche Diagnostics Operations, Inc. System and method for analyte measurement using dose sufficiency electrodes
US8586373B2 (en) 2003-06-20 2013-11-19 Roche Diagnostics Operations, Inc. System and method for determining the concentration of an analyte in a sample fluid
US8377707B2 (en) 2003-06-20 2013-02-19 Roche Diagnostics Operations, Inc. System and method for determining an abused sensor during analyte measurement
US8298828B2 (en) 2003-06-20 2012-10-30 Roche Diagnostics Operations, Inc. System and method for determining the concentration of an analyte in a sample fluid
US20070175612A1 (en) * 2003-10-02 2007-08-02 Behr Gmbh & Co. Kg Charge intercooler for a motor vehicle
US8225849B2 (en) * 2003-10-02 2012-07-24 Behr Gmbh & Co. Kg Charge intercooler for a motor vehicle
WO2005075065A1 (en) * 2004-01-28 2005-08-18 Shell Internationale Research Maatschappij B.V. Heat-exchanger for carrying out an exothermic reaction
CN100540132C (en) * 2004-01-28 2009-09-16 国际壳牌研究有限公司 Be used to carry out the slurry-phase reactor of exothermic reaction
US8246915B2 (en) 2004-01-28 2012-08-21 Shell Oil Company Heat-exchanger for carrying out an exothermic reaction
AU2005210164B2 (en) * 2004-01-28 2008-04-03 Shell Internationale Research Maatschappij B.V. Heat-exchanger for carrying out an exothermic reaction
US7448601B2 (en) 2004-03-08 2008-11-11 Shell Oil Company Gas distributor for a reactor
US20070254965A1 (en) * 2004-03-08 2007-11-01 Shell Oil Company Gas Distributor for a Reactor
US20070199887A1 (en) * 2004-03-08 2007-08-30 Anne Boer Filter System With Filter Means Retractable Into A Housing
US20070228328A1 (en) * 2004-04-26 2007-10-04 Merck Patent Gmbh As-Indacen Derivatives
US20110079747A1 (en) * 2009-10-02 2011-04-07 Mcwhorter Edward Milton Direct current simplex generator
US11306978B2 (en) * 2014-09-05 2022-04-19 2078095 Ontario Limited Heat recovery apparatus and method
US20190137192A1 (en) * 2014-09-05 2019-05-09 2078095 Ontario Limited Heat recovery apparatus and method
US20170211887A1 (en) * 2016-01-22 2017-07-27 Fulton Group N.A., Inc. Tube configuration for a heat exchanger, heat exchanger including the tube configuration, fluid heating system including the same, and methods of manufacture thereof
US11441850B2 (en) * 2020-01-24 2022-09-13 Hamilton Sundstrand Corporation Integral mounting arm for heat exchanger
US11453160B2 (en) 2020-01-24 2022-09-27 Hamilton Sundstrand Corporation Method of building a heat exchanger
US11460252B2 (en) 2020-01-24 2022-10-04 Hamilton Sundstrand Corporation Header arrangement for additively manufactured heat exchanger
US11703283B2 (en) 2020-01-24 2023-07-18 Hamilton Sundstrand Corporation Radial configuration for heat exchanger core
US11752691B2 (en) 2020-01-24 2023-09-12 Hamilton Sundstrand Corporation Method of building a heat exchanger
US11859832B2 (en) 2021-06-22 2024-01-02 2078095 Ontario Limited Gray water heat recovery apparatus and method

Also Published As

Publication number Publication date
CA919163A (en) 1973-01-16
GB1346111A (en) 1974-02-06
FR2090262A1 (en) 1972-01-14
DE2122054A1 (en) 1972-01-13
FR2090262B1 (en) 1975-02-21

Similar Documents

Publication Publication Date Title
US3656543A (en) Liquid metal heat exchanger
US3242981A (en) Nuclear reactor heat exchangers
GB1292777A (en) Heat exchange apparatus for cooling gases
NO138919B (en) HEAT EXCHANGER FOR COOLING HOT GASES
US3134432A (en) Heat exchanger
US4036294A (en) Heat exchanger assembly designed as a longitudinal counterflow device
JPH0250398B2 (en)
US3033773A (en) Solid gas suspension nuclear fuel assembly
US4377552A (en) Nuclear reactor exchanger
US4101377A (en) Fast neutron reactor
GB1424858A (en) Flow distribution for heat exchangers
US3662718A (en) Sodium heated steam generator
US3306351A (en) Heat exchanger for cooling cracked gases by multiple media
GB1060220A (en) Improvements in heat exchangers adapted for generation of vapour from liquid
US3112735A (en) Liquid metal heated vapor generator
US3267906A (en) Compact heat source and heat exchanger
GB1466476A (en) Heat exchanger
US4786463A (en) Emergency heat exchanger for cooling the primary fluid of a nuclear reactor, and a process for assembling this heat exchanger
US3908756A (en) Tube-in-shell heat exchangers
FR2106620B1 (en)
US3930537A (en) Heat exchanger
US4585053A (en) Heat exchanger for reactor core and the like
US3504737A (en) Heat exchangers
US2930592A (en) Heat exchangers
JPS6337880B2 (en)