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US2160898A - Heat exchange apparatus for rectifying columns - Google Patents

Heat exchange apparatus for rectifying columns Download PDF

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Publication number
US2160898A
US2160898A US196192A US19619238A US2160898A US 2160898 A US2160898 A US 2160898A US 196192 A US196192 A US 196192A US 19619238 A US19619238 A US 19619238A US 2160898 A US2160898 A US 2160898A
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oxygen
air
heat exchange
coils
coil
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US196192A
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Peff Peter
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J5/00Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
    • F25J5/002Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
    • 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
    • Y10S62/00Refrigeration
    • Y10S62/902Apparatus
    • Y10S62/903Heat exchange structure

Definitions

  • This invention relates generally to improvements in heat exchange apparatus for use in rectifying columns for distilling atmospheric gases; and the invention has reference, morexparticu- -1arly, to a novel construction of heat exchange means adapted to form part of a rectifying column wherein air under pressure is rapidly cooled down, then expanded and liquefied, and thereupon distilled to separate its oxygen and m nitrogen components for discharge from the column.
  • air is first suitably purified and then compressed to a high pressure (usually from 500 to 3000 pounds),
  • the high pressure air admitted into the rectifying column at relatively high temperature must first be rapidly cooled down. It is an object of this invention to pro- 25 vide a simply constructed but highly eflicient heat exchange apparatus'through which the ingoing and downflowing air initially passes, and by means of which the, relatively cold outgoing and up-flowing oxygen and nitrogen gases, being discharged from the rectifying column, may be effectively utilized to absorb or extract heat from the counter-flowing ingoing air.
  • the novel heat exchange apparatus includes relatively and adjaeently grouped tubular air con- 5 duit coils and a tubular oxygen conduit coil, to-
  • This invention has for a further object to provide a novel construction and relative dispositional arrangement of a plurality of concentrically related air tube coils, each comprising a single helical tube, and an oxygen tube coil comprising a plurality of helical tubes in' parallel, with certain of the air tube coils being positioned 55 at one side or inwardly of said oxygen tube coil while. the others of' the air tube coils are positioned at the opposite or outer side of said oxygen tube coil, thus assuring that substantially equal heat exchange effect is exerted by the intermediately disposed oxygen tube coil upon the out- 5 lying air tube coils.
  • Fig. 1 is a vertical longitudinal sectional view of a heat exchange apparatus according to this invention, portions of the air tube coils and inter- 15 Q mediate oxygen tube coil being shown in elevation; and Fig. 2 is a transverse or horizontal sectional view of said heat exchange apparatus.
  • the novel heat exchange apparatus is mounted within the upper end ofa rectifying column which is not shown except for a portion of its top end wall, which is indicated by the reference character I. 1
  • the heat exchange apparatus per se comprises an external cylindrical jacket or casing 2 having a top flange 3, which is secured by bolts 4, or
  • the means for conducting the ingoing airv through the heat exchange. apparatus comprises a series of air conduit coils in relatively concentrically spaced relation 'to extend downwardly through the housing chamber 1.
  • Each coil comprises a single helical tube, the helices of which are of such pitch as to provide some free space therebetween so as to permit flow movement of nitrogen between adjacent helices of the respective conduit coils.
  • the means for conducting the outgoing oxygen through the heat exchange apparatus comprises an oxygen conduit coil to extend upwardly through the housing chamber 1.
  • This oxygen conduit coil comprises a plurality of helical tubes disposed in parallel relation in vertical plane, the helices of the same being of such pitch that free space is provided between vertically adjacent tubes so as to permit flow movement of nitrogen therebetween.
  • the oxygen conduit coil comprises four tubes 9, I0, ii and 52 disposed in parallel in vertical plane; it will be understood, however, that a greater or lesser number of such tubes may be optionally employed.
  • the lower intake ends of these tubes 8, it, it and i2 are connected with a suitable intake header E3, to which is connected the oxygen delivery pipe it which leads from the source of oxygen gas within the rectifying column interior.
  • the air conduit coils are respectively designated by the reference characters ll, l8, l9 and 20. These air conduit coils run parallel one to another and in concentric relation, and comprise an inner group consisting of the tubes I1 and I8, disposed inwardly of and concentric to the oxygen conduit coil, and an outer group consisting of the tubes l9 and 20, disposed outwardly of and also concentric to the oxygen conduit coil. While four air conduit coils are shown in the drawing, it will be understood that more or less than this number may be employed, and, likewise, more than one oxygen conduit coil may be employed, according to the size of the heat exchange apparatus required for a given size and capacity of rectifying column with which it is associated.
  • the upper or intake ends of the respective air conduit coils are connected with a suitable intake header 2
  • the lower outlet ends of said respective air conduit coils are connected with a suitable outlet header 23, to which is connected the air delivery pipe 24 for delivering the cooled compressed airto the expansion valve (not shown) through which it is, in turn, delivered into the rectifying column for liquefication and distillation.
  • the comparatively cold nitrogen gas which is formed within and rises through the rectifying column, flows through the member 8 upwardly through the spaces intermediate the coil runs as well as between the helices of the individual coils, thus contacting the walls of the air conduit tubes so as to materially aid in the transfer of heat therethrough from the air flowing downwardly through said air conduit coils.
  • Any suitable form of nitrogen'outlet means, as 26, is connected in communication with the upper end of said housing chamber 1.
  • said oxygen conduit coil comprises a plurality of tubes having their helices parallelin vertical plane.
  • Heat exchange apparatus for the purposes described, comprising means to provide an annular housing chamber arranged to receive, for outgoing movement therethrough, nitrogen gas discharged from a rectifying column, an up-flow.
  • oxygen conduit coil extending through said housing chamber interior to conduct outgoing oxygen for discharge from said rectifying column
  • said oxygen conduit coil comprising a plurality of tubes having their helices parallel in vertical plane, header means with which the inlet ends and outlet ends of said tubes respectively connect, a series of air conduit coils each comprising a single tube extending through said housing chamber interior to conduct ingoing compressed air to-the interior of said rectifying column, said air and oxygen conduit coils being arranged in concentric closely spaced relation, with some of the air conduit coils inwardly and some outwardly disposed relative to saidoxygen conduit coil, all

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Description

June 6, 1939. P. PEFF 2,160,898
HEAT EXCHANGE APPARATUS FOR RECT IFYING COLUMNS Filed Match 16, 1938 III! NITROGE'N ange INVENTOR. Mex" 5y,
ATTORNEY;
Patented June 6, 1939 PATENT OFFICE HEAT EXCHANGE APPARATUS FOR RECTIFYIN G COLUMNS Peter Peif, West Orange, N. J. Application March 16, 1938, Serial-N0. 198,192
3 Claims.
This invention relates generally to improvements in heat exchange apparatus for use in rectifying columns for distilling atmospheric gases; and the invention has reference, morexparticu- -1arly, to a novel construction of heat exchange means adapted to form part of a rectifying column wherein air under pressure is rapidly cooled down, then expanded and liquefied, and thereupon distilled to separate its oxygen and m nitrogen components for discharge from the column.
In the -rectifying of atmospheric gases, air is first suitably purified and then compressed to a high pressure (usually from 500 to 3000 pounds),
and after being dried is admitted into a rectifying column wherein it is expanded to approximately atmospheric pressure and liquefied and thereupon distilled to separatethe oxygen and nitrogen.
Preparatory to the expansion, liquefication and distillation processes, the high pressure air admitted into the rectifying column at relatively high temperature must first be rapidly cooled down. It is an object of this invention to pro- 25 vide a simply constructed but highly eflicient heat exchange apparatus'through which the ingoing and downflowing air initially passes, and by means of which the, relatively cold outgoing and up-flowing oxygen and nitrogen gases, being discharged from the rectifying column, may be effectively utilized to absorb or extract heat from the counter-flowing ingoing air. To this end the novel heat exchange apparatus includes relatively and adjaeently grouped tubular air con- 5 duit coils and a tubular oxygen conduit coil, to-
gether with spacing means whereby the respective coil groups are maintained in uniformly laterally spaced relation concentrically, to provide passage space for the outgoing and up-flowing movement of nitrogen gas, and so that this relatively cold nitrogen gas may contact with the external surfaces of the air tube coils for additional heat exchange effect, while at the same time the uniformly distributed passage space thus provided for said nitrogen gas will assure continuous flow thereof with a minimum of restriction.
This invention has for a further object to provide a novel construction and relative dispositional arrangement of a plurality of concentrically related air tube coils, each comprising a single helical tube, and an oxygen tube coil comprising a plurality of helical tubes in' parallel, with certain of the air tube coils being positioned 55 at one side or inwardly of said oxygen tube coil while. the others of' the air tube coils are positioned at the opposite or outer side of said oxygen tube coil, thus assuring that substantially equal heat exchange effect is exerted by the intermediately disposed oxygen tube coil upon the out- 5 lying air tube coils.
Other objects of this invention, not at this time more particularly enumerated, will be understood from the following detailed description or the same; I
An illustrative embodiment of this invention is shown in the accompanying drawing, in which:
Fig. 1 is a vertical longitudinal sectional view of a heat exchange apparatus according to this invention, portions of the air tube coils and inter- 15 Q mediate oxygen tube coil being shown in elevation; and Fig. 2 is a transverse or horizontal sectional view of said heat exchange apparatus.
Similar characters of reference are employed in said above mentioned views, to indicate correo sponding parts.
The novel heat exchange apparatus is mounted within the upper end ofa rectifying column which is not shown except for a portion of its top end wall, which is indicated by the reference character I. 1
The heat exchange apparatus per se comprises an external cylindrical jacket or casing 2 having a top flange 3, which is secured by bolts 4, or
' other suitable fastening means, to the rectifying column top wall I, so as to depend therefrom.- Suitably secured to said top flange 3 to extend therefrom axially downward within the interior of said jacket or casing 2 is a cylindrical spool 5, the lower free end of which is closed by a bot- 5 tom cap or end wall'i; By this arrangement, an annular housing chamber 1 is provided, intermediate said jacket or casing 2 and said spool 5, within which the coil groups of the apparatus are concentrically arranged to extend downward- 40 ly therethrough. The lowernend of said jacket or casing 2 is open to communication with the interior of the rectifying column, any suitable means of connection being provided, such as indicated illustratively by the connecting member 8. The means for conducting the ingoing airv through the heat exchange. apparatus comprises a series of air conduit coils in relatively concentrically spaced relation 'to extend downwardly through the housing chamber 1. Each coil comprises a single helical tube, the helices of which are of such pitch as to provide some free space therebetween so as to permit flow movement of nitrogen between adjacent helices of the respective conduit coils.
The means for conducting the outgoing oxygen through the heat exchange apparatus comprises an oxygen conduit coil to extend upwardly through the housing chamber 1. This oxygen conduit coil comprises a plurality of helical tubes disposed in parallel relation in vertical plane, the helices of the same being of such pitch that free space is provided between vertically adjacent tubes so as to permit flow movement of nitrogen therebetween. As illustrated in the drawing, the oxygen conduit coil comprises four tubes 9, I0, ii and 52 disposed in parallel in vertical plane; it will be understood, however, that a greater or lesser number of such tubes may be optionally employed. The lower intake ends of these tubes 8, it, it and i2 are connected with a suitable intake header E3, to which is connected the oxygen delivery pipe it which leads from the source of oxygen gas within the rectifying column interior. The upper outlet ends of said tubes 9, l0, H and G2 are, in similar manner, connected with a suitable outlet header i5, to which is connected the oxygen discharge pipe is through which the oxygen gas generated within the rectifying column is finally discharged for delivery to a suitable gas holder (not shown). The advantage of the multiple parallel tube form of the oxygen conduit coil .is that it assures less resistance to the free and reasonably rapid flow of the oxygen as which is at a comparatively low pressure.
The air conduit coils are respectively designated by the reference characters ll, l8, l9 and 20. These air conduit coils run parallel one to another and in concentric relation, and comprise an inner group consisting of the tubes I1 and I8, disposed inwardly of and concentric to the oxygen conduit coil, and an outer group consisting of the tubes l9 and 20, disposed outwardly of and also concentric to the oxygen conduit coil. While four air conduit coils are shown in the drawing, it will be understood that more or less than this number may be employed, and, likewise, more than one oxygen conduit coil may be employed, according to the size of the heat exchange apparatus required for a given size and capacity of rectifying column with which it is associated. The upper or intake ends of the respective air conduit coils are connected with a suitable intake header 2|, to which is connected the air delivery pipe 22 through which the dry compressed air is delivered to the rectifying column. The lower outlet ends of said respective air conduit coils are connected with a suitable outlet header 23, to which is connected the air delivery pipe 24 for delivering the cooled compressed airto the expansion valve (not shown) through which it is, in turn, delivered into the rectifying column for liquefication and distillation.
From the above description and the accompanying drawing, it will be clear that the air conduit coils and the oxygen conduit coil are relatively disposed in mutually spaced concentric relation. In order to maintain the concentric spacing uniform between the successive coils, so that spaces around and between adjacent helices thereof are freely opento the flow of nitrogen around and contiguous thereto,v vertically extending spacing strips 25 are engaged between the coil runs, and also between the sides of the jacket or casing wall 2 and spool wall 5 and the coils respectively adjacent to these walls.
The comparatively cold nitrogen gas, which is formed within and rises through the rectifying column, flows through the member 8 upwardly through the spaces intermediate the coil runs as well as between the helices of the individual coils, thus contacting the walls of the air conduit tubes so as to materially aid in the transfer of heat therethrough from the air flowing downwardly through said air conduit coils. Any suitable form of nitrogen'outlet means, as 26, is connected in communication with the upper end of said housing chamber 1.
It will be obvious that various changes could be made in the above described constructions, and that apparently widely different embodiments of this invention could be made without departing from the scope thereof. It is therefore intended that all matter contained in the above description or shown in the accompanying drawrel tending through said housing chamber interior to conduct outgoing oxygen for discharge from said rectifying column, said air and oxygen conduit coils being arranged in concentric closely spaced relation with some of the air conduit coils disposed inwardly of and adjacent to and some outwardly of and adjacent to the oxygen conduit coil, all arranged so that nitrogen gas may flow contiguous to and in contact with all air and oxygen conduit coils, and spacer means to maintain said coil runs uniformly spaced concentricallyto provide passages for the flow movement of nitrogen therebetween and contiguous thereto.
2. In heat exchange apparatus as defined in claim 1, wherein said oxygen conduit coil comprises a plurality of tubes having their helices parallelin vertical plane.
. 3. Heat exchange apparatus for the purposes described, comprising means to provide an annular housing chamber arranged to receive, for outgoing movement therethrough, nitrogen gas discharged from a rectifying column, an up-flow.
oxygen conduit coil extending through said housing chamber interior to conduct outgoing oxygen for discharge from said rectifying column, said oxygen conduit coil comprising a plurality of tubes having their helices parallel in vertical plane, header means with which the inlet ends and outlet ends of said tubes respectively connect, a series of air conduit coils each comprising a single tube extending through said housing chamber interior to conduct ingoing compressed air to-the interior of said rectifying column, said air and oxygen conduit coils being arranged in concentric closely spaced relation, with some of the air conduit coils inwardly and some outwardly disposed relative to saidoxygen conduit coil, all
arranged so that nitrogen gas may flow contiguous to and in contact with all said air and oxygen conduit coils, header means with which the inlet and outlet ends of said air conduit coil tubes respectively connect, and spacer means to maintain said coil runs uniformly spaced concentrically to provide passages for the flow movement of nitrogen therebetween and contiguous thereto.
. PETER. PEFF.
US196192A 1938-03-16 1938-03-16 Heat exchange apparatus for rectifying columns Expired - Lifetime US2160898A (en)

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Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2508247A (en) * 1945-09-25 1950-05-16 Research Corp Heat interchanger
US2553469A (en) * 1946-12-26 1951-05-15 Gulf Oil Corp Method for fractional distillation
US2633717A (en) * 1949-09-29 1953-04-07 Joy Mfg Co Rectification column
US2817950A (en) * 1951-01-20 1957-12-31 Philips Corp Hot-gas reciprocating engine construction
US2895303A (en) * 1956-05-17 1959-07-21 Little Inc A Purification of low-boiling gases
US3055641A (en) * 1960-05-03 1962-09-25 United Aircraft Corp Heat exchanger
US3130779A (en) * 1958-05-05 1964-04-28 Huet Andre Light boiler for nuclear energy installation
US3384166A (en) * 1966-07-07 1968-05-21 Gen Motors Corp Multi-tube annular heat exchanger
US3403727A (en) * 1965-04-30 1968-10-01 Linde Ag Crossflow countercurrent heat exchanger with inner and outer-tube sections made up of closely packed coaxially nested layers of helicoidally wound tubes
US3448792A (en) * 1966-11-07 1969-06-10 Hooker Chemical Corp Thermal convection condenser and method of use
US3526273A (en) * 1968-07-31 1970-09-01 Borg Warner Heat exchanger
US4243097A (en) * 1975-08-27 1981-01-06 Shell Oil Company Waste heat boiler
US4272667A (en) * 1978-07-10 1981-06-09 Edward Golowacz Electric fluid heating apparatus employing stackable heat transfer modules
US4462463A (en) * 1982-04-21 1984-07-31 Gorham Jr Robert S Triple pass heat exchanger
US5419392A (en) * 1993-02-10 1995-05-30 Maruyama; Noboru Heat exchanging apparatus
US5568835A (en) * 1995-07-25 1996-10-29 The Babcock & Wilcox Company Concentric heat exchanger having hydraulically expanded flow channels
US5845704A (en) * 1997-05-16 1998-12-08 Flowserve Management Company Heat exchanger baffle design
US6076597A (en) * 1997-12-31 2000-06-20 Flowserve Management Company Helical coil heat exchanger with removable end plates
US20050115699A1 (en) * 2002-01-21 2005-06-02 Thierry Nuris Coil for coolant circulation, method for making same and reactor comprising same
US20190137185A1 (en) * 2016-05-12 2019-05-09 Linde Aktiengesellschaft Coiled heat exchanger having inserts between the shroud and the last pipe layer

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2508247A (en) * 1945-09-25 1950-05-16 Research Corp Heat interchanger
US2553469A (en) * 1946-12-26 1951-05-15 Gulf Oil Corp Method for fractional distillation
US2633717A (en) * 1949-09-29 1953-04-07 Joy Mfg Co Rectification column
US2817950A (en) * 1951-01-20 1957-12-31 Philips Corp Hot-gas reciprocating engine construction
US2895303A (en) * 1956-05-17 1959-07-21 Little Inc A Purification of low-boiling gases
US3130779A (en) * 1958-05-05 1964-04-28 Huet Andre Light boiler for nuclear energy installation
US3055641A (en) * 1960-05-03 1962-09-25 United Aircraft Corp Heat exchanger
US3403727A (en) * 1965-04-30 1968-10-01 Linde Ag Crossflow countercurrent heat exchanger with inner and outer-tube sections made up of closely packed coaxially nested layers of helicoidally wound tubes
US3384166A (en) * 1966-07-07 1968-05-21 Gen Motors Corp Multi-tube annular heat exchanger
US3448792A (en) * 1966-11-07 1969-06-10 Hooker Chemical Corp Thermal convection condenser and method of use
US3526273A (en) * 1968-07-31 1970-09-01 Borg Warner Heat exchanger
US4243097A (en) * 1975-08-27 1981-01-06 Shell Oil Company Waste heat boiler
US4272667A (en) * 1978-07-10 1981-06-09 Edward Golowacz Electric fluid heating apparatus employing stackable heat transfer modules
US4462463A (en) * 1982-04-21 1984-07-31 Gorham Jr Robert S Triple pass heat exchanger
US5419392A (en) * 1993-02-10 1995-05-30 Maruyama; Noboru Heat exchanging apparatus
US5568835A (en) * 1995-07-25 1996-10-29 The Babcock & Wilcox Company Concentric heat exchanger having hydraulically expanded flow channels
US5845704A (en) * 1997-05-16 1998-12-08 Flowserve Management Company Heat exchanger baffle design
US6076597A (en) * 1997-12-31 2000-06-20 Flowserve Management Company Helical coil heat exchanger with removable end plates
US6102106A (en) * 1997-12-31 2000-08-15 Flowserve Management Company Method of servicing a helical coil heat exchanger with removable end plates
US20050115699A1 (en) * 2002-01-21 2005-06-02 Thierry Nuris Coil for coolant circulation, method for making same and reactor comprising same
US7549462B2 (en) * 2002-01-21 2009-06-23 Rhodia Polyamide Intermediates Coil for coolant circulation, method for making same and reactor comprising same
US20190137185A1 (en) * 2016-05-12 2019-05-09 Linde Aktiengesellschaft Coiled heat exchanger having inserts between the shroud and the last pipe layer
US10914526B2 (en) * 2016-05-12 2021-02-09 Linde Aktiengesellschaft Coiled heat exchanger having inserts between the shroud and the last pipe layer

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