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US1833876A - Pipe coil heat exchange equipment - Google Patents

Pipe coil heat exchange equipment Download PDF

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Publication number
US1833876A
US1833876A US336370A US33637029A US1833876A US 1833876 A US1833876 A US 1833876A US 336370 A US336370 A US 336370A US 33637029 A US33637029 A US 33637029A US 1833876 A US1833876 A US 1833876A
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United States
Prior art keywords
pipe
heat exchange
exchange equipment
coil heat
pipe coil
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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
US336370A
Inventor
William H Mcgrath
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Standard Oil Development Co
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Standard Oil Development Co
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Publication date
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Priority to US336370A priority Critical patent/US1833876A/en
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Publication of US1833876A publication Critical patent/US1833876A/en
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Expired - Lifetime legal-status Critical Current

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    • 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
    • F28D7/08Heat-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 otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082Heat-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 otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • F28D7/085Heat-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 otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions
    • F28D7/087Heat-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 otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions assembled in arrays, each array being arranged in the same plane
    • 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
    • F28D7/02Heat-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 helically coiled
    • F28D7/026Heat-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 helically coiled the conduits of only one medium being helically coiled and formed by bent members, e.g. plates, the coils having a cylindrical 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
    • F28D7/08Heat-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 otherwise bent, e.g. in a serpentine or zig-zag

Definitions

  • This invention relates to improvements in tubular heat of the type inwhichbafllesamplacedinthefluidstream. Numerous forms ofsuch equipment have heretofore been proposed with a view to obtaining thorough tact of fluid with the tube walls. Principal objects of the present invention are to provide simple and efiective means comprising internal and external pi with baflle means in 've relation to the pipes. In a p erred form of the improvements described herein, the bullies are readily removable for cleaning.
  • FIG. 1 is a fragmentary perspective view showing the parts in withdrawn position
  • Fig. 3 is an end view of the inner pipe
  • Fig. 4 is a side .elevation of a preferred type of return bend
  • Fig. 5 is an end elevation of the same
  • Fig. 6 is a side elevation, partly in section, showing a horizontal arrangement of the exchanger
  • Fig. '7 is a diagrammatic side elevation showing the utilization of a vertical form of the equipment in connection with an oil still;
  • FIG. 8 is a view similar to Fig. 1, showing a modified form.
  • FIG. 1 denotes an outer pipe and 2 a smaller pipe therein.
  • Bafile 3 is of such size as to hold pipe 2 concentrically in pipe 1.
  • a helical baflle 4, mounted on a rod 5, is adapted to fit snugly in pipe 2.
  • the outer pipe 1 has an outwardly extendingannularflangefiatoneendandacorrespondingflange? atthe otherend.
  • Flange fiisrecemedatfi'onitsinner toreeeive lugs 8 formed at the end of inner pipe 2.
  • Flangesfiand'lhaveannulargrooves9 mixing and eflicient con to receive a correspondingl sha ton e 10 on a return bend 11.
  • portions 12, 12', on pipe 2 also have annular grooves 13, adapted to receive :1. correspondmgly shaped tongue 14 on return bend 11.
  • Bolt holes 16 may be provided in the 15 to corapgate with bolt holes 16' in flanges 6 m -i
  • rod 5 carryingbafle4isrunintopipe2andthenthis plpe is inserted in pipe lso that lugs 8 are seatedinrecessesfi'.
  • Returnbends 11 are next secured to adjacent sections. It will be seen that the assembly and disassembly are easily accomplished, which is a-great advantage, especially if the 'pment is to be used with oils or other liquywhich may foul the heat exchange surfaces and dictate frequent cleaning.
  • Fig. 6 I have illustrated the use of my device for simple conntercurrent heat exbetween two liquids.
  • the inlet for the Chang. e hqu d entering the Inner-pass is at 1'7.
  • Theqmd in the outer pass flows in the opposite Y direction and discharges at 18. While countereurrent flow is generally desirable, both liquids may of course flow in the same direction.
  • the equipment may be heated or cooled in any suitable way.
  • Fig. 7 shows the improved heat exchanger vertically and connected by a vapor line 19 to a still 20.
  • Feed oil is supplied to the still through line 21 which by branches and 23, respectively, to a terminal section 24 and an intermediate section 25 of the heat equipment.
  • Lines 26 and 26' convey the preheated oil to the still. Suitable valves are in the lines so that ge' flow of oil tdhrough the ex changer may regulated as eslred.
  • the feed oil passes through the inner pipes and the vapors and return bends detachably connecting adpass through the outer ipes.
  • Condensates jacent units, each bend having an annular may be taken off throug lines 27 and 28 to passage and an inner passage communicating suitable cooling coils 29 and 30. Any vapors with correspondin passages of the units.
  • a draw-off line 33 conveys condensate from the terminal section 24 into a line 34 which is connected with the draw-off lines 27, 28 and 31. Valves are provided in these lines to permit the routing of the condensate in any desired manner.
  • baflies in a true helical form but this is not an essential of the invention.
  • Any bafile means which will insure adequate mixing of the liquid passing through the tube and effective contact of the liquid with the tube walls may be used in the improved equipment.
  • bafiie is .shown in Fig. 8 in which plates 35 are mounted .on pipe 36 and have cut away portions 36 oppositely arranged to compel circuitous flow of liquid outward into contact with the tube walls.
  • Similar baffles 37, having cut away portions 37 are mounted on a rod 38 adapted for insertion in an inner pipe 39.
  • any other means may be provided which will permit the removal of the battles for cleaning.
  • Heat exchange equipment comprising an outer pipe, an inner pipe in spaced relation thereto, a return bend having outer and inner passageways detachably connected respectively to the outer and inner pipes, and baflie means operatively arranged with respect to both the inner and outer pipes.
  • Heat exchange equipment comprising a plurality of condenser units including pipes concentrically disposed to form an annular passage and an inner passage, a spiral baffle inthe a'nnular passage, a spiral baflie detachably supported in the inner passage, the inner pipe bemg suspended freely in the outer pipe,

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  • 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

- Nqv; 24, 1931.
w. H. M GRATH PIPE COIL HEAT EXCHANGE EQUIPMENT 2 SheetS-Sheet 1 anowbo'c Filed Jan. 31, 1929 7 :hi J i. 752$55572555.23!"- 5525 I252! 35!, FF
. u u E 4 NOV. 24, 1931. w, MCGRATH PIPE COIL HEAT EXCHANGE EQUIPMENT PM Nov. 24, 19:11
PATENT OFFICE UNITED STATES magmleomormamnmmassmuonmsrmm OIL nlmorm'r comm, A common OF DELAWARE rrracomrmarmenm ammrnuu anunamnnmmo.
This invention relates to improvements in tubular heat of the type inwhichbafllesamplacedinthefluidstream. Numerous forms ofsuch equipment have heretofore been proposed with a view to obtaining thorough tact of fluid with the tube walls. Principal objects of the present invention are to provide simple and efiective means comprising internal and external pi with baflle means in 've relation to the pipes. In a p erred form of the improvements described herein, the bullies are readily removable for cleaning.
The invention will be fully understood from the following description read in con; nection with the accompanying drawings, in which 7 Fig. 1 is a fragmentary perspective view showing the parts in withdrawn position;
Fig.2isaverticalsectionthroughthe outer and inner pipes;
Fig. 3 is an end view of the inner pipe;
Fig. 4 is a side .elevation of a preferred type of return bend;
Fig. 5 is an end elevation of the same;
Fig. 6 is a side elevation, partly in section, showing a horizontal arrangement of the exchanger;
Fig. '7 is a diagrammatic side elevation showing the utilization of a vertical form of the equipment in connection with an oil still; and
8 is a view similar to Fig. 1, showing a modified form.
Referring to the 1 denotes an outer pipe and 2 a smaller pipe therein. A helical baflle 1s secured to the pipe 2, preferably by welding, though it may be secured by removable means such as bolts and nuts. Bafile 3 is of such size as to hold pipe 2 concentrically in pipe 1. A helical baflle 4, mounted on a rod 5, is adapted to fit snugly in pipe 2.
The outer pipe 1 has an outwardly extendingannularflangefiatoneendandacorrespondingflange? atthe otherend. Flange fiisrecemedatfi'onitsinner toreeeive lugs 8 formed at the end of inner pipe 2. Flangesfiand'lhaveannulargrooves9 mixing and eflicient con to receive a correspondingl sha ton e 10 on a return bend 11. portions 12, 12', on pipe 2 also have annular grooves 13, adapted to receive :1. correspondmgly shaped tongue 14 on return bend 11. Itwillbenotedthatthercturnbendhasinner and outer "es 1, 2', correspondmg to pipes 1 and 2, so that liquids flowing H these pipes do not at any time come into direct contact with each other.
Flanges15onthereturnbendaresecured toflangesfiandtoflanges'Ton adjacentsectlons of pipes 1, by bolts and nuts or other readily removable means, not shown. Bolt holes 16 may be provided in the 15 to corapgate with bolt holes 16' in flanges 6 m -i In assembling theequi ment, rod 5 carryingbafle4isrunintopipe2andthenthis plpe is inserted in pipe lso that lugs 8 are seatedinrecessesfi'. Returnbends 11 are next secured to adjacent sections. It will be seen that the assembly and disassembly are easily accomplished, which is a-great advantage, especially if the 'pment is to be used with oils or other liquywhich may foul the heat exchange surfaces and necesitate frequent cleaning.
In Fig. 6 I have illustrated the use of my device for simple conntercurrent heat exbetween two liquids. The inlet for the Chang. e hqu d entering the Inner-pass is at 1'7. Theqmd in the outer pass flows in the opposite Y direction and discharges at 18. While countereurrent flow is generally desirable, both liquids may of course flow in the same direction. The equipment may be heated or cooled in any suitable way.
Fig. 7 shows the improved heat exchanger vertically and connected by a vapor line 19 to a still 20. Feed oil is supplied to the still through line 21 which by branches and 23, respectively, to a terminal section 24 and an intermediate section 25 of the heat equipment. Lines 26 and 26' convey the preheated oil to the still. Suitable valves are in the lines so that ge' flow of oil tdhrough the ex changer may regulated as eslred.
In the installation shown, the feed oil passes through the inner pipes and the vapors and return bends detachably connecting adpass through the outer ipes. Condensates jacent units, each bend having an annular may be taken off throug lines 27 and 28 to passage and an inner passage communicating suitable cooling coils 29 and 30. Any vapors with correspondin passages of the units.
leaving the terminal section 24 pass through a line 31 into a cooling coil 32. A draw-off line 33 conveys condensate from the terminal section 24 into a line 34 which is connected with the draw-off lines 27, 28 and 31. Valves are provided in these lines to permit the routing of the condensate in any desired manner.
I prefer to use baflies in a true helical form but this is not an essential of the invention. Any bafile means which will insure adequate mixing of the liquid passing through the tube and effective contact of the liquid with the tube walls may be used in the improved equipment. For example, one alternative form of bafiie is .shown in Fig. 8 in which plates 35 are mounted .on pipe 36 and have cut away portions 36 oppositely arranged to compel circuitous flow of liquid outward into contact with the tube walls. Similar baffles 37, having cut away portions 37 are mounted on a rod 38 adapted for insertion in an inner pipe 39.
Instead of the arrangement shown for installing the baflles, any other means may be provided which will permit the removal of the battles for cleaning.
The construction described is preferred but it will be understood that various changes and alternative arrangements may be made within the scope of the appended claims, in which it is my intention to claim all novelty inherent in the invention as broadly as the prior art permits.
I claim:
1. Heat exchange equipment comprising an outer pipe, an inner pipe in spaced relation thereto, a return bend having outer and inner passageways detachably connected respectively to the outer and inner pipes, and baflie means operatively arranged with respect to both the inner and outer pipes.
2. Heat exchange equipment comprising a plurality of condenser units including pipes concentrically disposed to form an annular passage and an inner passage, a spiral baffle in the annular passage, a spiral bafiie detachably supported in the inner passage, the inner pipe being detachably supported in the outer pipe, and return bends detachably connecting adjacentunits, each 'bend having an annular passage and an inner passage communicating with the corresponding passages of the units.
3. Heat exchange equipment comprising a plurality of condenser units including pipes concentrically disposed to form an annular passage and an inner passage, a spiral baffle inthe a'nnular passage, a spiral baflie detachably supported in the inner passage, the inner pipe bemg suspended freely in the outer pipe,
WIL IAM H. MoGRATH. o
US336370A 1929-01-31 1929-01-31 Pipe coil heat exchange equipment Expired - Lifetime US1833876A (en)

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Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2549687A (en) * 1947-11-21 1951-04-17 Duriron Co Heat exchanger
US2693026A (en) * 1950-02-17 1954-11-02 Modine Mfg Co Method of making concentric tubes with radial fins
US2872915A (en) * 1956-02-02 1959-02-10 Bowen William Spencer Solar energy apparatus
US3071159A (en) * 1958-04-19 1963-01-01 Coraggioso Corrado Bono Heat exchanger tube
US3920068A (en) * 1973-06-22 1975-11-18 Dorr Oliver Inc Concentric double-pipe horizontal heat exchanger for fiber containing fluids
US4915164A (en) * 1988-06-27 1990-04-10 Harper Jr William H Heat exchanger
US6715285B2 (en) 2001-01-04 2004-04-06 Mandi Company Stirling engine with high pressure fluid heat exchanger
EP1719964A1 (en) * 2004-02-06 2006-11-08 Daikin Industries, Ltd. Heat exchanger for hot water supply
US8162040B2 (en) 2006-03-10 2012-04-24 Spinworks, LLC Heat exchanging insert and method for fabricating same
US20130079166A1 (en) * 2010-11-12 2013-03-28 Jingfu Wang Hollow transmission shaft
US20140083667A1 (en) * 2012-09-27 2014-03-27 Tai-Her Yang Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline And Transferring Heat To Exterior Through Outer Periphery Of Pipeline
US8755682B2 (en) 2012-07-18 2014-06-17 Trebor International Mixing header for fluid heater
CN105043140A (en) * 2015-08-06 2015-11-11 江门市顺恩牛奶有限公司 Liquid spiral type sleeve heat exchange device
EP3287730A1 (en) * 2016-08-25 2018-02-28 Bosch Termoteknik Isitma ve Klima Sanayi Ticaret Anonim Sirketi Heat exchanger
US10782072B2 (en) * 2014-04-16 2020-09-22 Enterex America LLC Counterflow helical heat exchanger

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2549687A (en) * 1947-11-21 1951-04-17 Duriron Co Heat exchanger
US2693026A (en) * 1950-02-17 1954-11-02 Modine Mfg Co Method of making concentric tubes with radial fins
US2872915A (en) * 1956-02-02 1959-02-10 Bowen William Spencer Solar energy apparatus
US3071159A (en) * 1958-04-19 1963-01-01 Coraggioso Corrado Bono Heat exchanger tube
US3920068A (en) * 1973-06-22 1975-11-18 Dorr Oliver Inc Concentric double-pipe horizontal heat exchanger for fiber containing fluids
US4915164A (en) * 1988-06-27 1990-04-10 Harper Jr William H Heat exchanger
US6715285B2 (en) 2001-01-04 2004-04-06 Mandi Company Stirling engine with high pressure fluid heat exchanger
EP1719964A4 (en) * 2004-02-06 2013-11-06 Daikin Ind Ltd Heat exchanger for hot water supply
EP1719964A1 (en) * 2004-02-06 2006-11-08 Daikin Industries, Ltd. Heat exchanger for hot water supply
US8162040B2 (en) 2006-03-10 2012-04-24 Spinworks, LLC Heat exchanging insert and method for fabricating same
US20130079166A1 (en) * 2010-11-12 2013-03-28 Jingfu Wang Hollow transmission shaft
US8715094B2 (en) * 2010-11-12 2014-05-06 Shandong Zhongtai New Energy Group Co., Ltd Hollow transmission shaft
EP2587076A4 (en) * 2010-11-12 2016-09-28 Shandong Zhongtai New Energy Group Co Ltd Hollow transmission shaft
US8755682B2 (en) 2012-07-18 2014-06-17 Trebor International Mixing header for fluid heater
US20140083667A1 (en) * 2012-09-27 2014-03-27 Tai-Her Yang Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline And Transferring Heat To Exterior Through Outer Periphery Of Pipeline
US9719733B2 (en) * 2012-09-27 2017-08-01 Tai-Her Yang Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline
US10119769B2 (en) 2012-09-27 2018-11-06 Tai-Her Yang Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline
US10782072B2 (en) * 2014-04-16 2020-09-22 Enterex America LLC Counterflow helical heat exchanger
CN105043140A (en) * 2015-08-06 2015-11-11 江门市顺恩牛奶有限公司 Liquid spiral type sleeve heat exchange device
EP3287730A1 (en) * 2016-08-25 2018-02-28 Bosch Termoteknik Isitma ve Klima Sanayi Ticaret Anonim Sirketi Heat exchanger

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