US3229762A - Welded heat exchanger - Google Patents

Welded heat exchanger Download PDF

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Publication number
US3229762A
US3229762A US363097A US36309764A US3229762A US 3229762 A US3229762 A US 3229762A US 363097 A US363097 A US 363097A US 36309764 A US36309764 A US 36309764A US 3229762 A US3229762 A US 3229762A
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Prior art keywords
heads
jacket
heating
heat exchanging
tubes
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Expired - Lifetime
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US363097A
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Vollhardt Frohmut
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Schmidtsche Heissdampf GmbH
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Schmidtsche Heissdampf GmbH
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Assigned to CIT GROUP/BUSINESS CREDIT, INC., THE reassignment CIT GROUP/BUSINESS CREDIT, INC., THE SECURITY AGREEMENT Assignors: OHIO ART COMPANY, THE AN OHIO CORPORATION
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F28F9/04—Arrangements for sealing elements into header boxes or end plates
    • F28F9/16—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling
    • F28F9/18—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
    • F28F9/182—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding the heat-exchange conduits having ends with a particular shape, e.g. deformed; the heat-exchange conduits or end plates having supplementary joining means, e.g. abutments
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/021—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers with heating tubes in which flows a non-specified heating fluid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/08—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being steam
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/005—Heat-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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/006—Tubular elements; Assemblies of tubular elements with variable shape, e.g. with modified tube ends, with different geometrical features
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00—Heat exchange conduits
    • F28F2210/02—Heat exchange conduits with particular branching, e.g. fractal conduit arrangements
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00—Heat exchange
    • Y10S165/355—Heat exchange having separate flow passage for two distinct fluids
    • Y10S165/40—Shell enclosed conduit assembly
    • Y10S165/427—Manifold for tube-side fluid, i.e. parallel
    • Y10S165/432—Manifold for tube-side fluid, i.e. parallel including a tube sheet
    • Y10S165/433—Tubes-tubesheet connection
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/4935—Heat exchanger or boiler making
    • Y10T29/49373—Tube joint and tube plate structure

Definitions

  • the present invention relates to a heat exchanger or evaporating element of welded construction for wasteheat boilers, or similar heat exchangers, especially for heating by gaseous heating mediums at very high pressure.
  • An object of the invention is to provide a structure of heat exchanging tubes located in a shell or jacket with collecting or distributing heads placed on each of the ends of the shell or jacket serving as conductors for the heating medium back and forth between the heat exchanging tubes.
  • Means are well known in the prior art for forming the heating surfaces of boilers from individual evaporating elements which consist of a water enclosed or jacketed barrel through which a number of heating tubes extend.
  • the ends of the heating tubes are mounted in an upper and a lower tube head.
  • the heating medium is fed to the heating tubes through a hood or chamber, covering the tube heads and functioning as distributors, and is conducted away through a similar chamber serving as collector, which covers the other tube head.
  • Such heat exchanging elements are deficient for heating with gaseous heating media, which must be supplied at very high pressure, since both the chamber and the tube head are inadequate for such pressure loads.
  • the heating medium is a synthetic or ammonia gas which is under 300 to 500 atmospheric pressures and more, as is not uncommon in present high-pressure synthesis, and the medium should be cooled by heat exchanging, in which event the tangible heat of the gas should be utilized at the same time for the production of useful vapor, for example of pressure above atmospheres, then, first of all, the evaporating elements must be of such structure that there is adequate warranty that the high-pressure heating medium cannot break through in the area of the heat exchanger through which the cooling medium passes.
  • the instant invention compared to the prior, constructs the heads in one piece and of solid construction and are provided at their surfaces, which face the ends of the shell or jacket, with extensions machined from the solid material, for the connection of the heat exchanging tubes and with a suitably constructed connecting web for their connection with the shell or jacket as well as extensions at the side wall for the inflow and/ or outflow of the heating medium.
  • a further object is to provide bores piercing the extensions for the heat exchanging tubes and the bores for the inflow .and/ or outlet of the heating medium are so driven into the interior of the heads that the bores are directed towards each other.
  • a still further object is to provide a heat exchanging or evaporating element fully capable of the required high pressure loads because the heads themselves have no weldice ing seam and the only welding seams on the high-pressure side are the circumferential sea-ms of the tubes which connect the heat exchanging tubes with the extensions of the heads. Thus, there are only a few short welded joints. The longer connecting seams between the web of the heads and the ends of the shell or jacket are in an area of lower pressure.
  • a further advantageous development of the heat exchanging or evaporating elements of the present invention consists in that Y piece sets, which are known in the prior art, are provided as heat exchanging tubes. With this measure it is possible to reduce the number of the required circumferential seams of the tubes essentially without thereby reducing the potential heating surface for each element unit.
  • FIGURE 1 shows a side view of a heat exchanging element with parts in cross section
  • FIGURE 2 is a section on section line 2-2 of FIG- URE 1,
  • FIGURE 3 shows a portion of a cross-sectional view of the head according to FIGURE 1 on an enlarged scale
  • FIGURE 4 shows a diagrammatical view of a wasteheat boiler composed of the heat exchanging elements of the present invention.
  • the heat exchanging or evaporating element 1 consists of the shell or jacket 2 inside of which the heating tubes 3 are located.
  • the ends of the heating tubes 3 are connected to an upper and a lower head 4.
  • the heads 4 are placed on the ends of the shell or jacket 2 and are welded to the jacket, and form the collectors and distributors for the heating medium.
  • the heads 4 are of one piece and solid, e.g. they are machined from solid material. They are provided at their surfaces which face the interior of the jacket, with extensions 5 machined from the solid material.
  • the heating tubes 3 are welded to these extensions 5.
  • the latter are provided with a web 6 which is also machined from the head material.
  • the extensions 7 for the inlet and/ or outlet of the heating medium. These extensions 7, too, are machined from the solid head material.
  • the bores 8 are projected through the extensions 7 into the interior of the heads. Bores 9 advanced through the extensions 5 cut the bores 8 so that a connection between the extensions 7 and the extensions 5 and therefore between the heating tubes 3 is obtained.
  • the shell or jacket 2 is provided with the supply and delivery sockets 10 for the cooling medium.
  • the heating tubes 3 are developed as Y piece units 11, in which way the number of the required circumferential seams of the tubes is reduced to a minimum.
  • FIGURE 4 several of the heat exchanging elements are interchangeably connected with a waste-heat boiler.
  • the heating medium is supplied to the inlet 12, converted by the transfer tubes 13 from one heat exchanging element to the other and then conducted away through the outlet 14.
  • the cooling medium is supplied from a steam barrel 15 over a fall tube 16 to the heat exchanging elements 1 and is converted by the overflow tubes 17 from one heat exchanging element to the other.
  • the resulting steam mixture evaporates through the tube 18 into the steam barrel 15.
  • a heat exchanging or evaporating element of welded construction for waste-heat boilers or similar heat exchangers, especially for heating with gaseous heating media of very high pressure comprising a jacket, heat exchanging tubes located in said jacket conveying the heating medium, distributing heads located at both ends of said jacket serving as conductors of the heating medium to and from said heat exchanging tubes, said heads being of solid integral construction having at their surfaces facing the ends of said jacket, extensions machined from the solid construction of said heads for receiving the ends of said heating tubes, an integral cylindrical web upon said heads for connection with said jacket, additional extensions on a side wall of said heads integral with the material thereof for the inlet and outlet of the heating medium, bores which extend into said heads from said extensions for said heating tubes and bores which extend from said extensions for said inlet and outlet of the heating medium intersecting within said heads said first named bores.

Description

Jan. 18, 1966 F. VOLLHARDT 3,2
WELDED HEAT EXCHANGER Filed April 28, 1964 2 Sheets-Sheet 1 @mulim m FIG. I
Fiohmul Val/hard! INVENTOR I 4 ATTORN EYS Jan. 18, 1966 VQLLHARDT 3,229,762
WELDED HEAT EXCHANGER Filed April 28, 1964 2 Sheets-Sheeo 2 III" L IIIHH F rohmuf Val/hard! INVENTOR ATTORNEYS United States Patent 3,229,762 WELDED HEAT EXCHANGER Frohmut Vollhardt, Gottingen, Germany, assignor to Schmidtsche Heissdampf-Gesellschaft m.b.H., Kassel- Wilhelmshohe, Germany Filed Apr. 28, 1964, Ser. No. 363,097
Claims priority, application Germany, May 25, 1963,
Sch 33,326 2 Claims. (Cl. 165-157) The present invention relates to a heat exchanger or evaporating element of welded construction for wasteheat boilers, or similar heat exchangers, especially for heating by gaseous heating mediums at very high pressure.
An object of the invention is to provide a structure of heat exchanging tubes located in a shell or jacket with collecting or distributing heads placed on each of the ends of the shell or jacket serving as conductors for the heating medium back and forth between the heat exchanging tubes.
Means are well known in the prior art for forming the heating surfaces of boilers from individual evaporating elements which consist of a water enclosed or jacketed barrel through which a number of heating tubes extend. The ends of the heating tubes are mounted in an upper and a lower tube head. In most of these known constructions, the heating medium is fed to the heating tubes through a hood or chamber, covering the tube heads and functioning as distributors, and is conducted away through a similar chamber serving as collector, which covers the other tube head.
Such heat exchanging elements are deficient for heating with gaseous heating media, which must be supplied at very high pressure, since both the chamber and the tube head are inadequate for such pressure loads. For instance, if the heating medium is a synthetic or ammonia gas which is under 300 to 500 atmospheric pressures and more, as is not uncommon in present high-pressure synthesis, and the medium should be cooled by heat exchanging, in which event the tangible heat of the gas should be utilized at the same time for the production of useful vapor, for example of pressure above atmospheres, then, first of all, the evaporating elements must be of such structure that there is adequate warranty that the high-pressure heating medium cannot break through in the area of the heat exchanger through which the cooling medium passes. Such a penetration of the heating medium certainly leads to a complete destruction of the heat exchanger. For this reason, large welding seams should be avoided in the structure of the evaporating elements. This requirement may not be easily met by prior constructions of heat exchangers so that those of the usual construction are unsuitable. It is a further object of the invention to remedy the above disadvantages.
The instant invention compared to the prior, constructs the heads in one piece and of solid construction and are provided at their surfaces, which face the ends of the shell or jacket, with extensions machined from the solid material, for the connection of the heat exchanging tubes and with a suitably constructed connecting web for their connection with the shell or jacket as well as extensions at the side wall for the inflow and/ or outflow of the heating medium.
A further object is to provide bores piercing the extensions for the heat exchanging tubes and the bores for the inflow .and/ or outlet of the heating medium are so driven into the interior of the heads that the bores are directed towards each other.
A still further object is to provide a heat exchanging or evaporating element fully capable of the required high pressure loads because the heads themselves have no weldice ing seam and the only welding seams on the high-pressure side are the circumferential sea-ms of the tubes which connect the heat exchanging tubes with the extensions of the heads. Thus, there are only a few short welded joints. The longer connecting seams between the web of the heads and the ends of the shell or jacket are in an area of lower pressure.
Through appropriate arrangement of the extensions and the bores on the heads it is easily possible to arrange the inlet as well as the outlet of the heating medium at one head, which presents a great freedom in the installment of the evaporating elements for their interchanging with the heating surface groups of a waste-heat boiler.
A further advantageous development of the heat exchanging or evaporating elements of the present invention consists in that Y piece sets, which are known in the prior art, are provided as heat exchanging tubes. With this measure it is possible to reduce the number of the required circumferential seams of the tubes essentially without thereby reducing the potential heating surface for each element unit.
With the above and other objects which will become apparent from the detailed description below, a preferred modification of the invention is shown in the drawings, in which:
FIGURE 1 shows a side view of a heat exchanging element with parts in cross section,
FIGURE 2 is a section on section line 2-2 of FIG- URE 1,
FIGURE 3 shows a portion of a cross-sectional view of the head according to FIGURE 1 on an enlarged scale, and
FIGURE 4 shows a diagrammatical view of a wasteheat boiler composed of the heat exchanging elements of the present invention.
The heat exchanging or evaporating element 1 consists of the shell or jacket 2 inside of which the heating tubes 3 are located. The ends of the heating tubes 3 are connected to an upper and a lower head 4. The heads 4 are placed on the ends of the shell or jacket 2 and are welded to the jacket, and form the collectors and distributors for the heating medium.
The heads 4 are of one piece and solid, e.g. they are machined from solid material. They are provided at their surfaces which face the interior of the jacket, with extensions 5 machined from the solid material. The heating tubes 3 are welded to these extensions 5.
For the welding of the shell or jacket 2 with the heads 4, the latter are provided with a web 6 which is also machined from the head material. At the side wall of the heads 4 are the extensions 7 for the inlet and/ or outlet of the heating medium. These extensions 7, too, are machined from the solid head material. The bores 8 are projected through the extensions 7 into the interior of the heads. Bores 9 advanced through the extensions 5 cut the bores 8 so that a connection between the extensions 7 and the extensions 5 and therefore between the heating tubes 3 is obtained.
The shell or jacket 2 is provided with the supply and delivery sockets 10 for the cooling medium.
The heating tubes 3 are developed as Y piece units 11, in which way the number of the required circumferential seams of the tubes is reduced to a minimum.
In FIGURE 4, several of the heat exchanging elements are interchangeably connected with a waste-heat boiler. The heating medium is supplied to the inlet 12, converted by the transfer tubes 13 from one heat exchanging element to the other and then conducted away through the outlet 14. The cooling medium is supplied from a steam barrel 15 over a fall tube 16 to the heat exchanging elements 1 and is converted by the overflow tubes 17 from one heat exchanging element to the other. The resulting steam mixture evaporates through the tube 18 into the steam barrel 15.
Through the selection of certain definite sizes of the various heat exchanging elements, it may be possible to assemble comprehensive performance data for waste-heat boilers and gas coolers by interchanging groups of elements in the assembly of groupings of prefabricated machine parts.
It is thought that the invention and its advantages will be understood from the foregoing description and it is apparent that various changes may be made in the form, construction and arrangement of the parts without departing from the spirit and scope of the invention or sacrificing its material advantages, the form hereinbefore described and illustrated in the drawings being merely a preferred embodiment thereof.
I claim:
1. A heat exchanging or evaporating element of welded construction for waste-heat boilers or similar heat exchangers, especially for heating with gaseous heating media of very high pressure, comprising a jacket, heat exchanging tubes located in said jacket conveying the heating medium, distributing heads located at both ends of said jacket serving as conductors of the heating medium to and from said heat exchanging tubes, said heads being of solid integral construction having at their surfaces facing the ends of said jacket, extensions machined from the solid construction of said heads for receiving the ends of said heating tubes, an integral cylindrical web upon said heads for connection with said jacket, additional extensions on a side wall of said heads integral with the material thereof for the inlet and outlet of the heating medium, bores which extend into said heads from said extensions for said heating tubes and bores which extend from said extensions for said inlet and outlet of the heating medium intersecting within said heads said first named bores.
2. A heat exchanging or evaporating element as set forth in claim 1 wherein said heating tubes comprise two parallel pipe lengths united at both ends to form common throats.
References Cited by the Examiner UNITED STATES PATENTS 1,894,987 1/1933 Fusco 1 172 X 1,924,900 8/1933 Armacost 172 X 2,911,200 11/1959 Gardner et al 165173 X 3,176,761 4/1965 Anderson et al. 165l75 X FOREIGN PATENTS 421,152 12/1909 France.
ROBERT A. OLEARY, Primary Examiner.
N. R. WILSON, Assistant Examiner.

Claims (1)

1. HEAT EXCHANGING OR EVAPORATING ELEMENT OF WELDED CONSTRUCTION FOR WASTE-HEAT BOILERS OR SIMILAR HEAT EXCHANGERS, ESPECIALLY FOR HEATING WITH GASEOUS HEATING MEDIA OF VERY HIGH PRESSURE, COMPRISING A JACKET, HEAT EXCHANGING TUBES LOCATED IN SAID JACKET CONVEYING THE HEATING MEDIUM, DISTRIBUTING HEADS LOCATED AT BOTH ENDS OF SAID JACKET SERVING AS CONDUCTORS OF THE HEATING MEDIUM TO AND FROM SAID HEAT EXCHANGING TUBES, SAID HEADS BEING OF SOLID INTEGRAL CONSTRUCTION HAVING AT THEIR SURFACES FACING THE ENDS OF SAID JACKET, EXTENSIONS MACHINED FROM THE SOLID CONSTRUCTION OF SAID HEADS FOR RECEIVING THE ENDS OF SAID HEATING TUBES, AN INTEGRAL CYLINDRICAL WEB UPON SAID HEADS FOR CONNECTION WITH SAID JACKET, ADDITIONAL EXTENSIONS ON A SIDE WALL OF SAID HEADS INTEGRAL
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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3443548A (en) * 1968-01-23 1969-05-13 Vogt & Co Inc Henry High temperature and high pressure steam generator
US4588026A (en) * 1979-06-11 1986-05-13 Raytheon Company Coiled heat exchanger
US5775412A (en) * 1996-01-11 1998-07-07 Gidding Engineering, Inc. High pressure dense heat transfer area heat exchanger
US20050028964A1 (en) * 2003-08-04 2005-02-10 Cleland James M. Cold plate for beer dispensing tower
US7051797B2 (en) * 2000-04-11 2006-05-30 Bronswerk Heat Transfer B.V. Heat exchanger
US20080219086A1 (en) * 2007-03-09 2008-09-11 Peter Mathys Apparatus for the heat-exchanging and mixing treatment of fluid media
US20130206374A1 (en) * 2010-03-15 2013-08-15 The Trustees Of Dartmouth College Geometry of heat exchanger with high efficiency
CN108627025A (en) * 2018-05-28 2018-10-09 张化机（苏州）重装有限公司 A kind of inlet tube structure of condensate water pot
US20180328673A1 (en) * 2017-05-12 2018-11-15 The Boeing Company Hollow Lattice Thermal Energy Storage Heat Exchanger
US20190145318A1 (en) * 2017-11-14 2019-05-16 The Boeing Company Dendritic heat exchangers and methods of utilizing the same
US10612867B2 (en) 2018-02-21 2020-04-07 The Boeing Company Thermal management systems incorporating shape memory alloy actuators and related methods
EP3734041A1 (en) * 2017-11-14 2020-11-04 The Boeing Company Dentritic heat exchanger and methods of utilizing the same
US11118838B2 (en) * 2019-02-20 2021-09-14 Hamilton Sundstrand Corporation Leaf-shaped geometry for heat exchanger core
US11143170B2 (en) 2019-06-28 2021-10-12 The Boeing Company Shape memory alloy lifting tubes and shape memory alloy actuators including the same
US11168584B2 (en) 2019-06-28 2021-11-09 The Boeing Company Thermal management system using shape memory alloy actuator
US11415377B2 (en) * 2019-12-23 2022-08-16 Hamilton Sundstrand Corporation Two-stage fractal heat exchanger
US11525438B2 (en) 2019-06-28 2022-12-13 The Boeing Company Shape memory alloy actuators and thermal management systems including the same

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR421152A (en) * 1909-12-13 1911-02-16 Valentin Purrey Methodical temperature exchanger
US1894987A (en) * 1930-07-11 1933-01-24 Rudolph V Fusco Service water heater
US1924900A (en) * 1932-07-16 1933-08-29 Superheater Co Ltd Symmetrical heating unit
US2911200A (en) * 1957-03-28 1959-11-03 Griscom Russell Co Heat exchanger tube sheet joint construction
US3176761A (en) * 1962-10-29 1965-04-06 North American Aviation Inc Heat exchanger

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR421152A (en) * 1909-12-13 1911-02-16 Valentin Purrey Methodical temperature exchanger
US1894987A (en) * 1930-07-11 1933-01-24 Rudolph V Fusco Service water heater
US1924900A (en) * 1932-07-16 1933-08-29 Superheater Co Ltd Symmetrical heating unit
US2911200A (en) * 1957-03-28 1959-11-03 Griscom Russell Co Heat exchanger tube sheet joint construction
US3176761A (en) * 1962-10-29 1965-04-06 North American Aviation Inc Heat exchanger

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3443548A (en) * 1968-01-23 1969-05-13 Vogt & Co Inc Henry High temperature and high pressure steam generator
US4588026A (en) * 1979-06-11 1986-05-13 Raytheon Company Coiled heat exchanger
US5775412A (en) * 1996-01-11 1998-07-07 Gidding Engineering, Inc. High pressure dense heat transfer area heat exchanger
US7051797B2 (en) * 2000-04-11 2006-05-30 Bronswerk Heat Transfer B.V. Heat exchanger
US20050028964A1 (en) * 2003-08-04 2005-02-10 Cleland James M. Cold plate for beer dispensing tower
WO2005016815A1 (en) * 2003-08-04 2005-02-24 Cleland Sales Corporation Coil basket
US7363962B2 (en) 2003-08-04 2008-04-29 Cleland Sales Corporation Cold plate for beer dispensing tower
US20080219086A1 (en) * 2007-03-09 2008-09-11 Peter Mathys Apparatus for the heat-exchanging and mixing treatment of fluid media
US8794820B2 (en) * 2007-03-09 2014-08-05 Sulzer Chemtech Ag Apparatus for the heat-exchanging and mixing treatment of fluid media
US20130206374A1 (en) * 2010-03-15 2013-08-15 The Trustees Of Dartmouth College Geometry of heat exchanger with high efficiency
US9134072B2 (en) * 2010-03-15 2015-09-15 The Trustees Of Dartmouth College Geometry of heat exchanger with high efficiency
US20180328673A1 (en) * 2017-05-12 2018-11-15 The Boeing Company Hollow Lattice Thermal Energy Storage Heat Exchanger
US11747094B2 (en) * 2017-05-12 2023-09-05 The Boeing Company Hollow lattice thermal energy storage heat exchanger
CN109779762B (en) * 2017-11-14 2022-11-11 波音公司 Dendritic heat exchanger and method of using same
US20190145318A1 (en) * 2017-11-14 2019-05-16 The Boeing Company Dendritic heat exchangers and methods of utilizing the same
CN109779762A (en) * 2017-11-14 2019-05-21 波音公司 Dendroid heat exchanger and the method for utilizing it
US10619570B2 (en) * 2017-11-14 2020-04-14 The Boeing Company Dendritic heat exchangers and methods of utilizing the same
EP3734041A1 (en) * 2017-11-14 2020-11-04 The Boeing Company Dentritic heat exchanger and methods of utilizing the same
US11060480B2 (en) 2017-11-14 2021-07-13 The Boeing Company Sound-attenuating heat exchangers and methods of utilizing the same
US10612867B2 (en) 2018-02-21 2020-04-07 The Boeing Company Thermal management systems incorporating shape memory alloy actuators and related methods
CN108627025A (en) * 2018-05-28 2018-10-09 张化机（苏州）重装有限公司 A kind of inlet tube structure of condensate water pot
CN108627025B (en) * 2018-05-28 2023-11-21 张化机（苏州）重装有限公司 Inlet pipe structure of condensate water tank
US11118838B2 (en) * 2019-02-20 2021-09-14 Hamilton Sundstrand Corporation Leaf-shaped geometry for heat exchanger core
US11143170B2 (en) 2019-06-28 2021-10-12 The Boeing Company Shape memory alloy lifting tubes and shape memory alloy actuators including the same
US11168584B2 (en) 2019-06-28 2021-11-09 The Boeing Company Thermal management system using shape memory alloy actuator
US11525438B2 (en) 2019-06-28 2022-12-13 The Boeing Company Shape memory alloy actuators and thermal management systems including the same
US11415377B2 (en) * 2019-12-23 2022-08-16 Hamilton Sundstrand Corporation Two-stage fractal heat exchanger

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