US3419069A - Heat transfer apparatus having flexible plastic tubular elements arranged in a braided configuration - Google Patents

Heat transfer apparatus having flexible plastic tubular elements arranged in a braided configuration Download PDF

Info

Publication number
US3419069A
US3419069A US634631A US63463167A US3419069A US 3419069 A US3419069 A US 3419069A US 634631 A US634631 A US 634631A US 63463167 A US63463167 A US 63463167A US 3419069 A US3419069 A US 3419069A
Authority
US
United States
Prior art keywords
tubular elements
bundle
elements
fluid
heat transfer
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
US634631A
Inventor
Baker Thomas Bernard
Levy Stanley Burton
Ottolini Roland Frederick
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.)
Ametek Inc
Original Assignee
EI Du Pont de Nemours and Co
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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US634631A priority Critical patent/US3419069A/en
Priority to GB19714/68A priority patent/GB1199590A/en
Priority to FR1583962D priority patent/FR1583962A/fr
Application granted granted Critical
Publication of US3419069A publication Critical patent/US3419069A/en
Anticipated expiration legal-status Critical
Assigned to AMETEK, INC., A CORP. OF DE. reassignment AMETEK, INC., A CORP. OF DE. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: E.I. DU PONT DE NEMOURS AND COMPANY
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/0206Heat exchangers immersed in a large body of liquid
    • F28D1/0213Heat exchangers immersed in a large body of liquid for heating or cooling a liquid in a tank
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/06Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material
    • F28F21/062Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material the heat-exchange apparatus employing tubular conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2210/00Heat exchange conduits
    • F28F2210/10Particular layout, e.g. for uniform temperature distribution
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2255/00Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes
    • F28F2255/02Flexible elements

Definitions

  • a heat transfer apparatus having a casing member surrounding at least one bundle of flexible plastic tubular elements, a substantial portion of each bundle comprising a first group of tubular elements arranged in a given pattern and interlaced in a substantially uniform manner with a second group of tubular elements arranged in symmetrically opposed pattern to provide a coherent flexible bundle, stable in size, and having a predetermined degree of packing and predetermined resistance to fluid flow through said bundle exteriorly of said elements which predetermined characteristics cooperate to provide a good heat transfer characteristics for the apparatus.
  • This invention relates generally to improved heat exchange, or heat transfer, apparatus; and more specifically to heat exchange apparatus having flexible plastic tubular elements in a particularly advantageous bundle arrangement.
  • 3,277,959 involves the use of interleaved tape elements spaced along a bundle of plastic tubular elements and bonded thereto.
  • the tape elements position the tubular elements, maintain them in a fairly compact bundle, and control, to some extent, fluid flow conditions exteriorly of the tubular elements in the bundle.
  • a third feature of this type as disclosed in prior copending application Ser. No. 598,070, filed Nov. 30, 1966 in the name of Robert Dilman Smith involves placing a bundle of plastic tubular elements in a foraminous casing member or sleeve to maintain a compact bundle configuration and desired fluid flow conditions in the bundle exteriorly of said elements.
  • the spaced tape elements bonded to the tubular elements prevent bending of the bundles during production, and use and will break loose or damage the tubular elements if excessive bending forces are encountered.
  • the tapes do not prevent the squeezing together and spreading apart of the flexible tubular elements between the spaced tape elements which has an adverse effect on fluid flow conditions and on the tubular elements.
  • the flexibility of the plastic tubular elements is used to provide a bundle of uniformly interlaced tubular elements which, without any additional structure or means, results in a coherent compact bundle in which uniform packing, resistance to flow, and spacing of the tubular elements are maintained uniformly along the bundle.
  • the bundle is flexible and rugged as required in assembly and operation of the heat exchange apparatus, and also accommodate thermal expansion of the elements in a more uniform and controlled manner.
  • bundles are provided in the preferred form of sleeve-like configurations it is possible without difficulty to assemble a number of sleeve-like bundles one inside the other and, if desired, to provide additional support and/or fluid flow for the bundle by positioning a substantially rigid support or a sparger member within the bundle as will be described in detail hereinafter.
  • FIGURE 1 is a partial isometric view of a preferred heat transfer arrangement embodying features of the invention with certain parts broken away to show the relationship of the component parts and features.
  • FIGURE 2 is a side elevational view, with certain parts broken away for a clearer showing, of a somewhat different heat transfer arrangement embodying features of the invention.
  • FIGURE 3 is an enlarged end view of the sparger and support member of the arrangement of FIGURE 2.
  • FIGURE 4 is a partial side elevational view of a bundle of tubular elements with the cooperating tube sheet member and a rigid support and sparger member associated therewith. The interlaced arrangement of the flexible tubular elements embodying the present inven tion is also shown in this figure.
  • FIGURE 5 is a partial enlarged detailed view of the preferred interlaced flexible tubular element arrangement of the invention, showing how the important angle of tubular element cross over or intersection is measured.
  • FIGURE 6 is a partial transverse cross sectional view of the arrangement of FIGURE 4 taken at line 66.
  • FIGURE 7 is a partial longitudinal cross sectional view of the sparger and support member of FIGURE 3.
  • FIGURE 8 is an enlarged partial side elevational view Of a heat exchange arrangement embodying features of the invention and similar to that of FIGURE 4, showing a modified arrangement in the tubular elements are interlaced With each other in groups of four.
  • FIGURES l, 4, 5 and 6 One preferred heat exchange arrangement or combina: tion embodying principles of this invention is shown in FIGURES l, 4, 5 and 6.
  • the apparatus shown in these figures comprises a casing member 10 formed by wall elements 11 of suitable material which define a chamber for a fluid the upper surface of which is indicated at 14.
  • the casing member is provided with fluid inlet means 12 and fluid outlet means 13.
  • An elongated compact bundle of a relatively large number of small thin-walled flexible plastic tubular elements T is positioned as shown to extend through at least a portion of a fluid in the chamber defined by wall elements 11.
  • Each end of the bundle 20 is provided with a header unit 21 which maintains free communication between the interiors of the tubular elements T and fluid supply conduit elements 23, 24, 25.
  • Suitable header unit arrangements are shown for example in U.S.
  • the tubular elements T of which there may be from about 500 to about 10,000 or more, may be formed of a composition, and in sizes, disclosed in the abovemen-tioned U.S. Patent No. 3,228,456.
  • the composition preferred is a polyfluorinated plastic such as a copolymer of tetrafluoroethylene and hexafluoropropylene with a thermal conductivity of about 0.1 B.t.u./hr./ft./F.
  • the tubular elements in the bundle are preferably in a size range between about 5 and 275 mils outside diameter with a wall thickness between about 0.5 and about 30.0 mils on centerlines spaced in an average of about 1.01- 2.00 diameters.
  • each sleeve comprises a first plurality of tubular elements positioned in a first helical pattern and an interengaged interlaced second plurality of tubular elements positioned in a second opposing helical pattern.
  • FIGURE 8 Another variation of an interlaced bundle is shown in FIGURE 8 in which the tubular elements are interlaced in the same general manner except that they are handled in groups of four elements. If the tubular elements are interwoven or braided together too tightly, a closed pattern with prohibitive resistance to fluid flow, unacceptable susceptability to plugging, and undesirable kinking of individual tubular elements is formed.
  • tubular elements are interwoven or braided together too loosely, the bundle loses its desired coherence and compactness; also, the position of the elements relative to each other to maintain a desired uniform packing packing and resistance to fluid flow through the bundle cannot be established or maintained. It has been determined that a controlling factor is the .angle of intersection formed where tubular elements of one plurality cross over the elements of the other plurality. For tubular elements in the size ranges discussed above, and particularly for tubular elements of about mils outside diameter, this angle is preferably maintained between about 10 and about 60. The measurement of this angle is shown in FIGURE 5 at angle ABC or 0.
  • interwoven bundles or sleeves are suitably accomplished on conventional well-known brading machinery with a few minor modifications obviously necessary to adapt them from small solid wires or yarns to the small hollow tubular elements utilized in the apparatus of this invention.
  • brading machinery with a few minor modifications obviously necessary to adapt them from small solid wires or yarns to the small hollow tubular elements utilized in the apparatus of this invention.
  • One example of a satisfactory arrangement generally suitable for forming the interlaced bundles of this invention is disclosed in Catalog 56 (ELF-20004-1M-l164) on Braiders of the New England Butt Co., 304 Pearl Street, Buffalo, R.I.
  • braided or interlaced bundles are formed with end portions in which the tubular elements are substantially parallel (not interlaced) to facilitate construction of the tube sheet TS (FIGURE 4) or end construction suitable for forming the necessary header arrangement of a heat exchange apparatus (such as disclosed in abovementioned U.S. Patents 3,228,456 and 3,277,959).
  • This is accomplished by periodically ceasing the braiding or interlacing action as a long length of bundles of tubular elements is being produced.
  • the configuration and/ or position of the bundle of tubular elements as a Whole can be controlled or maintained by the use of a rigid unit inserted within the bundle.
  • This unit may, if desired, be hollow and provided with suitable orifices 33 so fluid can be circulated through the unit into the bundle to improve fluid circulation and distribution within the bundle.
  • the unit 32 in a U-shaped configuration within the bundle maintains the bundle configuration and position.
  • Unit 32 is connected to conduit elbow elements 31 and to other conduits elements 30 and 33 through which fluid is supplied into the bundle interior as shown.
  • the tube bundle 20 and rigid supporting unit 32 are held in position relative to each other and relative to the wall elements 1 1 of the housing by means of a bracket assembly comprising elements 40, 42, and 43, all held in place by bolts 44 and 41.
  • the rigid unit controlling the position of the bundle and improving fluid circulation comprises a hollow radial portion 310 and a hollow axial portion 312 having perforations or orifices 313.
  • a fluid at one temperature is passed through the housing by means of inlet 12 and outlet 13, while a suitable fluid at a significantly different temperature is passed through the tubular elements T of bundle by means of conduit elements 23, 24, and header units 21 to cause transfer of heat between the two fluids.
  • a portion of the fluid at said one temperature may be circulated through the hollow rigid unit 32 and out of orifices 33 by means of supply conduit elements 33 and 30.
  • FIGURE 2 A modified version of heat transfer apparatus embodying principles of the invention is shown in FIGURE 2.
  • This version corresponds to a tube-in-shell heat exchanger arrangement similar to that shown in the above mentioned US. Patent No. 3,228,456.
  • braided or interlaced bundle of tubular elements similar to that shown in FIGURE 4 has been positioned in a shell or casing member 101 which is provided with inlet 105, outlet 106, and suitable header units 102 at each end thereof to permit circulation of fluid fro-m inlet 103 through the interiors of the tubular elements to the outlet 104.
  • suitable header constructions are disclosed in the above-mentioned US. Patents 3,228,456 and 3,277,- 959.
  • a rigid unit 401 can be mounted in cooperation with shell inlet 105 as shown in FIGURE 2 and in engagement with the bundle of tubular elements to help maintain the position of the bundle and improve the handling of fluid supplied into the bundle as shown, by means of openings 403 and 404- in hollow unit 401.
  • the enlarged showings of FIGURES 3 and 7 make the structure and function of this unit clear.
  • Unit 401 functions as shown in the preferred version of FIGURE 2 to receive a portion of the inlet stream to the shell in its hollow portion, and conduct this portion of the inlet stream directly into the central portion of the tube bundle where it is distributed through openings 403.
  • the other portion of the shell inlet stream passes through openings 404 directly into the shell outside of the hollow portion of unit 401.
  • FIGURE 7 The direction of shell inlet flow is generally indicated by the arrows in FIGURE 7.
  • the op eration of the FIGURE 2 version of the apparatus of the invention is believed to be apparent from the drawing; one fluid at a given temperature being passed within the casing member or shell 101 exteriorly of the tubular elements from inlet 105 to outlet 106 while a fluid at a different temperature is passed from header inlet 103 through the interiors of the tubular elements T to header outlet 104.
  • this invention provides a simplified arrangement in which the flexible tubular elements themselves act as spacing means to maintain the position of the elements relative to each other along the bundle, and establish a substantially uniform packing and resistance to fluid flow necessary for good heat exchange relation ships.
  • the invention provides a compact bundle which is also flexible and widely manipulatable in assembly, operation, and maintenance while preserving generally the important relationships of the tubular elements relative to each other.
  • the new arrangement of this invention results in a heat exchanger apparatus which is less susceptible to plugging of shellside fluid flow, less susceptible to tubular element kinking or damage, and also inherently possesses better and more uniform heat transfer characteristics.
  • An improved heat exchanger apparatus comprising in combination: a casing member, said casing member provided with structure defining a fluid-containing chamber, said apparatus further comprising a bundle of small diameter, thin-walled, flexible, tubular elements having continuously hollow interiors and formed of an organic polymeric composition, said bundle extending through at least a portion of said chamber to cooperate with a fluid contained in said chamber, said apparatus further comprising supporting means cooperating with said bundle to support said bundle in said chamber, conduit means operatively connected with the interiors of said tubular elements to circulate a fluid therethrough and establish a heat transfer relationship with a fluid in said chamber, said bundle having at least a substantial portion thereof comprising a first plurality of tubular elements arranged in a given pattern, and a second plurality of tubular elements arranged in a similar opposed pattern, said elements of each plurality being interlaced in a substantially uniform manner to provide a coherent flexible bundle substantially stable in size, the extent of interlacing and number of tubular elements being such that a predetermined degree of packing and a predetermined
  • the said supporting means comprises a substantially rigid reinforcing unit extending through said bundle and interengaged with said tubular elements to maintain the position of said bundle within desired limits in said chamber.
  • said supporting means comprises an elongated substantially rigid unit projecting into and extending along within the innermost sleeve arrangement for a substantial portion of the length of the bundle in order to positively maintain the position and configuration of the bundle Within desired limits, said unit comprising a fluid passageway therethrough and orifices connected therewith for handling fluid supplied into said bundle exteriorly of said tubular elements.

Description

3,419,069 TUBULAR Dec. 31, 1968 1:3, BAKER ET AL HEAT TRANSFER APPARATUS HAVING FLEXIBLE PLASTIC ELEMENTS ARRANGED IN A BRAIDED CONFIGURATION Filed April 28. 1967 Sheet INVENTORS THOMAS BERNARD BAKER STANLEY BURTON LEVY ROLAND FREDERICK OTTOLINI ATTORNEY Dec. 31, 1968 115, B K ET AL HEAT TRANSFER APPARATUS HAVING FLEXIBLE PLASTIC TUBULAR ELEMENTS ARRANGED IN A BRAIDED CONFIGURATION Filed April 28, 1967 Sheet FIG.
INVENTORS THOMAS BERNARD BAKER STANLEY BURTON LEVY ROLAND FREDERICK OTTOLINI ATTORNEY United States Patent 3,419,069 HEAT TRANSFER APPARATUS HAVING FLEXIBLE PLASTIC TUBULAR ELE- MENTS ARRANGED IN A BRAIDED CONFIGURATION Thomas Bernard Baker and Stanley Burton Levy, Wilmington, and Roland Frederick Ottolini, Newark, Del., assignors to E. I. du Pont de Nemours and Company, Wilmington, Del., a corporation of Delaware Filed Apr. 28, 1967, Ser. No. 634,631 Claims. (Cl. 165--158) ABSTRACT OF THE DISCLOSURE A heat transfer apparatus having a casing member surrounding at least one bundle of flexible plastic tubular elements, a substantial portion of each bundle comprising a first group of tubular elements arranged in a given pattern and interlaced in a substantially uniform manner with a second group of tubular elements arranged in symmetrically opposed pattern to provide a coherent flexible bundle, stable in size, and having a predetermined degree of packing and predetermined resistance to fluid flow through said bundle exteriorly of said elements which predetermined characteristics cooperate to provide a good heat transfer characteristics for the apparatus.
Introduction This invention relates generally to improved heat exchange, or heat transfer, apparatus; and more specifically to heat exchange apparatus having flexible plastic tubular elements in a particularly advantageous bundle arrangement.
It is an object of the invention to provide novel and improved heat exchange apparatus combinations or arrangements having plastic components, especially flexible tubular elements, and components made of materials such as metals which arrangements perform effectively, reliably, and in addition, not only accommodate but utilize advantageously during their operation, the different properties of the plastic components under the desired operating conditions.
It is a further object to provide such novel and improved apparatus combinations which will overcome the problems, disadvantages, and deficiencies of early prior art flexible plastic tube heat exchange apparatus combinations as will be discussed hereinafter.
Other objects and advantages will be apparent from a consideration of the following specification, claims and accompanying drawings.
Background of the invention As indicated generally in US. Patent No. 3,228,456, heat exchange arrangements utilizing plastic tubular elements are known and have been found to be advantageous in many applications. Because of the use of small flexible plastic tubular elements, a number of special problems have been encountered, not only in designing and producing such arrangements, but also in their operation. Some of these problems involve the relatively low heat transfer coeflicients and the relatively high coeflicients of thermal expansion possessed by most plastic materials as compared with parts made of more conventional ma- 3,419,069 Patented Dec. 31, 1968 terials such as metals. Other problems relate to the different properties such as compressive strength, tensile strength, flexibility, and melting points of these plastic materials relative to the other materials used. Production and operating techniques as well as apparatus designs must be established such that the more conventional parts such as those still for-med of the usual metallic compositions can be shaped, formed, heated, and used While in cooperative association with the plastic parts to produce and operate economical, reliable, and effective heat exchange arrangements Wit-hout destroying or damaging the associated plastic parts by application of excessive forces, impacts, temperatures, or other conditions.
One problem involves maintaining uniform packing and resistance to fluid flow for the tube bundle in plastic tube heat exchange apparatus. This, in turn, has been related to the flexible nature of the small plastic tubes used in this type heat exchanger apparatus. The problem is aggravated at elevated operating temperatures at which considerable thermal expansion takes place and the tubes become even more flexible and limp. A number of special structural features have been needed and used in the past to try to solve these problems. One of such features as disclosed in prior US. Patent No. 3,228,456 involves the use of transverse rigid baflle members through which the plastic tubular elements extend for lateral support. The baflle members also are needed to provide the desired fluid flow conditions exteriorly of the tubular elements. A second of such features as disclosed in prior US. Patent No. 3,277,959 involves the use of interleaved tape elements spaced along a bundle of plastic tubular elements and bonded thereto. The tape elements position the tubular elements, maintain them in a fairly compact bundle, and control, to some extent, fluid flow conditions exteriorly of the tubular elements in the bundle. A third feature of this type as disclosed in prior copending application Ser. No. 598,070, filed Nov. 30, 1966 in the name of Robert Dilman Smith involves placing a bundle of plastic tubular elements in a foraminous casing member or sleeve to maintain a compact bundle configuration and desired fluid flow conditions in the bundle exteriorly of said elements.
However there are serious problems and disadvantages associated with each of the above prior art features. For example, threading the great multiplicity of small tubular elements through perforated transverse baffies as mentioned in the feature first mentioned is a prohibitive operation as to cost and time, and in addition does not prevent the squeezing together and spreading apart of the flexible tubular elements between the spaced transverse baflle members, which has an adverse effect on fluid flow conditions and on the tubular elements.
As to the second feature mentioned above, the spaced tape elements bonded to the tubular elements, prevent bending of the bundles during production, and use and will break loose or damage the tubular elements if excessive bending forces are encountered. In addition, the tapes do not prevent the squeezing together and spreading apart of the flexible tubular elements between the spaced tape elements which has an adverse effect on fluid flow conditions and on the tubular elements. The
bonding of spaced tape elements to the tubular elements tubular elements, does reduce the spreading apart of the tubular elements but still requires spacing means such as the tape elements to maintain the desired spacing between the tubular elements. Squeezing together of the tubular elements between the tape element positions still occurs and this feature represents a costly, and not entirely successful, way to provide a compact bundle with uniform spacing and resistance to fluid flow through the bundle.
In applicants improved arrangement embodying the present invention, the flexibility of the plastic tubular elements is used to provide a bundle of uniformly interlaced tubular elements which, without any additional structure or means, results in a coherent compact bundle in which uniform packing, resistance to flow, and spacing of the tubular elements are maintained uniformly along the bundle. In addition, the bundle is flexible and rugged as required in assembly and operation of the heat exchange apparatus, and also accommodate thermal expansion of the elements in a more uniform and controlled manner. Where the bundles are provided in the preferred form of sleeve-like configurations it is possible without difficulty to assemble a number of sleeve-like bundles one inside the other and, if desired, to provide additional support and/or fluid flow for the bundle by positioning a substantially rigid support or a sparger member within the bundle as will be described in detail hereinafter.
In the drawings:
FIGURE 1 is a partial isometric view of a preferred heat transfer arrangement embodying features of the invention with certain parts broken away to show the relationship of the component parts and features.
FIGURE 2 is a side elevational view, with certain parts broken away for a clearer showing, of a somewhat different heat transfer arrangement embodying features of the invention.
FIGURE 3 is an enlarged end view of the sparger and support member of the arrangement of FIGURE 2.
FIGURE 4 is a partial side elevational view of a bundle of tubular elements with the cooperating tube sheet member and a rigid support and sparger member associated therewith. The interlaced arrangement of the flexible tubular elements embodying the present inven tion is also shown in this figure.
FIGURE 5 is a partial enlarged detailed view of the preferred interlaced flexible tubular element arrangement of the invention, showing how the important angle of tubular element cross over or intersection is measured.
FIGURE 6 is a partial transverse cross sectional view of the arrangement of FIGURE 4 taken at line 66.
FIGURE 7 is a partial longitudinal cross sectional view of the sparger and support member of FIGURE 3.
FIGURE 8 is an enlarged partial side elevational view Of a heat exchange arrangement embodying features of the invention and similar to that of FIGURE 4, showing a modified arrangement in the tubular elements are interlaced With each other in groups of four.
One preferred heat exchange arrangement or combina: tion embodying principles of this invention is shown in FIGURES l, 4, 5 and 6. The apparatus shown in these figures comprises a casing member 10 formed by wall elements 11 of suitable material which define a chamber for a fluid the upper surface of which is indicated at 14. The casing member is provided with fluid inlet means 12 and fluid outlet means 13. An elongated compact bundle of a relatively large number of small thin-walled flexible plastic tubular elements T is positioned as shown to extend through at least a portion of a fluid in the chamber defined by wall elements 11. Each end of the bundle 20 is provided with a header unit 21 which maintains free communication between the interiors of the tubular elements T and fluid supply conduit elements 23, 24, 25. Suitable header unit arrangements are shown for example in U.S. Patents 3,228,456 and 3,277,959 mentioned above. The tubular elements T of which there may be from about 500 to about 10,000 or more, may be formed of a composition, and in sizes, disclosed in the abovemen-tioned U.S. Patent No. 3,228,456. The composition preferred is a polyfluorinated plastic such as a copolymer of tetrafluoroethylene and hexafluoropropylene with a thermal conductivity of about 0.1 B.t.u./hr./ft./F. The tubular elements in the bundle are preferably in a size range between about 5 and 275 mils outside diameter with a wall thickness between about 0.5 and about 30.0 mils on centerlines spaced in an average of about 1.01- 2.00 diameters.
As best shown in FIGURES 4, 5 and 6, the position of the tubular elements relative to each other, the packing of the tubular elements, and their resistance to fluid flow are controlled solely by the interengagement and interlacing of the flexible tubular elements with each other. A braided arrangement, as shown in FIGURES 4, 5 and 6 is preferred in which a plurality of braided sleeves are assembled one inside the other to form the bundle. Generally speaking, each sleeve comprises a first plurality of tubular elements positioned in a first helical pattern and an interengaged interlaced second plurality of tubular elements positioned in a second opposing helical pattern. In the preferred interlaced pattern shown in the drawings a tubular element of one plurality proceeds in an over two and under two pattern of interweaving relative to the tubular elements of the second opposing plurality, with the interwoven position of any element being offset by one element with respect to its adjacent tubular elements of the same plurality. Another variation of an interlaced bundle is shown in FIGURE 8 in which the tubular elements are interlaced in the same general manner except that they are handled in groups of four elements. If the tubular elements are interwoven or braided together too tightly, a closed pattern with prohibitive resistance to fluid flow, unacceptable susceptability to plugging, and undesirable kinking of individual tubular elements is formed. On the other hand, if the tubular elements are interwoven or braided together too loosely, the bundle loses its desired coherence and compactness; also, the position of the elements relative to each other to maintain a desired uniform packing packing and resistance to fluid flow through the bundle cannot be established or maintained. It has been determined that a controlling factor is the .angle of intersection formed where tubular elements of one plurality cross over the elements of the other plurality. For tubular elements in the size ranges discussed above, and particularly for tubular elements of about mils outside diameter, this angle is preferably maintained between about 10 and about 60. The measurement of this angle is shown in FIGURE 5 at angle ABC or 0.
Formation of the interwoven bundles or sleeves is suitably accomplished on conventional well-known brading machinery with a few minor modifications obviously necessary to adapt them from small solid wires or yarns to the small hollow tubular elements utilized in the apparatus of this invention. One example of a satisfactory arrangement generally suitable for forming the interlaced bundles of this invention is disclosed in Catalog 56 (ELF-20004-1M-l164) on Braiders of the New England Butt Co., 304 Pearl Street, Providence, R.I. Preferably, braided or interlaced bundles are formed with end portions in which the tubular elements are substantially parallel (not interlaced) to facilitate construction of the tube sheet TS (FIGURE 4) or end construction suitable for forming the necessary header arrangement of a heat exchange apparatus (such as disclosed in abovementioned U.S. Patents 3,228,456 and 3,277,959). This is accomplished by periodically ceasing the braiding or interlacing action as a long length of bundles of tubular elements is being produced.
As shown in FIGURES 1, 4 and 6, the configuration and/ or position of the bundle of tubular elements as a Whole can be controlled or maintained by the use of a rigid unit inserted within the bundle. This unit may, if desired, be hollow and provided with suitable orifices 33 so fluid can be circulated through the unit into the bundle to improve fluid circulation and distribution within the bundle. Specifically, in FIGURE 1 the unit 32 in a U-shaped configuration within the bundle maintains the bundle configuration and position. Unit 32 is connected to conduit elbow elements 31 and to other conduits elements 30 and 33 through which fluid is supplied into the bundle interior as shown. As further illustrated in FIGURE 1, the tube bundle 20 and rigid supporting unit 32 are held in position relative to each other and relative to the wall elements 1 1 of the housing by means of a bracket assembly comprising elements 40, 42, and 43, all held in place by bolts 44 and 41. In FIGURE 4 the rigid unit controlling the position of the bundle and improving fluid circulation comprises a hollow radial portion 310 and a hollow axial portion 312 having perforations or orifices 313.
In operation of the apparatus of FIGURE 1, a fluid at one temperature is passed through the housing by means of inlet 12 and outlet 13, while a suitable fluid at a significantly different temperature is passed through the tubular elements T of bundle by means of conduit elements 23, 24, and header units 21 to cause transfer of heat between the two fluids. In order to improve the fluid flow through the bundle 20 exteriorly of the tubular elements, a portion of the fluid at said one temperature may be circulated through the hollow rigid unit 32 and out of orifices 33 by means of supply conduit elements 33 and 30.
A modified version of heat transfer apparatus embodying principles of the invention is shown in FIGURE 2. This version corresponds to a tube-in-shell heat exchanger arrangement similar to that shown in the above mentioned US. Patent No. 3,228,456. In this version, braided or interlaced bundle of tubular elements similar to that shown in FIGURE 4 has been positioned in a shell or casing member 101 which is provided with inlet 105, outlet 106, and suitable header units 102 at each end thereof to permit circulation of fluid fro-m inlet 103 through the interiors of the tubular elements to the outlet 104. Suitable header constructions are disclosed in the above-mentioned US. Patents 3,228,456 and 3,277,- 959. If desired, a rigid unit 401 can be mounted in cooperation with shell inlet 105 as shown in FIGURE 2 and in engagement with the bundle of tubular elements to help maintain the position of the bundle and improve the handling of fluid supplied into the bundle as shown, by means of openings 403 and 404- in hollow unit 401. The enlarged showings of FIGURES 3 and 7 make the structure and function of this unit clear. Unit 401 functions as shown in the preferred version of FIGURE 2 to receive a portion of the inlet stream to the shell in its hollow portion, and conduct this portion of the inlet stream directly into the central portion of the tube bundle where it is distributed through openings 403. The other portion of the shell inlet stream passes through openings 404 directly into the shell outside of the hollow portion of unit 401. The direction of shell inlet flow is generally indicated by the arrows in FIGURE 7. The op eration of the FIGURE 2 version of the apparatus of the invention is believed to be apparent from the drawing; one fluid at a given temperature being passed within the casing member or shell 101 exteriorly of the tubular elements from inlet 105 to outlet 106 while a fluid at a different temperature is passed from header inlet 103 through the interiors of the tubular elements T to header outlet 104.
It is believed that the preceding description indicates that a novel improved heat exchanger apparatus has been provided in accordance with the objects of the invention.
Compared with the above-mentioned prior art heat exchanger combinations, this invention provides a simplified arrangement in which the flexible tubular elements themselves act as spacing means to maintain the position of the elements relative to each other along the bundle, and establish a substantially uniform packing and resistance to fluid flow necessary for good heat exchange relation ships. The invention provides a compact bundle which is also flexible and widely manipulatable in assembly, operation, and maintenance while preserving generally the important relationships of the tubular elements relative to each other. The new arrangement of this invention results in a heat exchanger apparatus which is less susceptible to plugging of shellside fluid flow, less susceptible to tubular element kinking or damage, and also inherently possesses better and more uniform heat transfer characteristics.
Although certain preferred embodiments of the invention have been described in detail in accordance with the Patent Law, many variations and modifications within the spirit of the invention will be obvious to those skilled in the art and all such are considered to fall within the scope of the following claims.
What is claimed is:
1. An improved heat exchanger apparatus comprising in combination: a casing member, said casing member provided with structure defining a fluid-containing chamber, said apparatus further comprising a bundle of small diameter, thin-walled, flexible, tubular elements having continuously hollow interiors and formed of an organic polymeric composition, said bundle extending through at least a portion of said chamber to cooperate with a fluid contained in said chamber, said apparatus further comprising supporting means cooperating with said bundle to support said bundle in said chamber, conduit means operatively connected with the interiors of said tubular elements to circulate a fluid therethrough and establish a heat transfer relationship with a fluid in said chamber, said bundle having at least a substantial portion thereof comprising a first plurality of tubular elements arranged in a given pattern, and a second plurality of tubular elements arranged in a similar opposed pattern, said elements of each plurality being interlaced in a substantially uniform manner to provide a coherent flexible bundle substantially stable in size, the extent of interlacing and number of tubular elements being such that a predetermined degree of packing and a predetermined resistance to fluid flow through said bundle exteriorly of said tubular elements, is provided to maintain said heat transfer relationship at effective levels.
2. The improved apparatus of claim 1 in which the tubular elements of one plurality cross over the engaged tubular elements of the other plurality to form included angles of intersection of between about 10 and 60.
3. The improved apparatus of claim 2 in which said first and second pluralities of tubular elements are arranged in symmetrically opposed patterns and are interwoven in a regular pattern to provide a braided bundle.
4. The improved apparatus of claim 3 in which said bundle comprises a number of layers each having interlaced pluralities of tubular elements.
5. The improved apparatus of claim 4 in which said layers are in the form of hollow sleeve arrangements of graduated sizes each positioned within sleeve arrangement of larger size to form a compact stable bundle.
6. The improved apparatus of claim 5 in which said bundle is elongated in form with end portions and the tubular elements at said end portions are substantially parallel and free of interlacing.
7. The improved apparatus of claim 1 in which the said supporting means comprises a substantially rigid reinforcing unit extending through said bundle and interengaged with said tubular elements to maintain the position of said bundle within desired limits in said chamber.
8. The improved apparatus of claim 7 in which said unit comprises a fluid passageway therethrough and orifices connected therewith for handling fluid supplied into said bundle exteriorly of said tubular elements.
9. The improved apparatus of claim 8 in which said unit is engaged and coextensive with a significant portion of the length of said bundle to maintain the desired position of the bundle and improved fluid circulation along said portion of the bundle length.
10. The improved apparatus of claim 5 in which said supporting means comprises an elongated substantially rigid unit projecting into and extending along within the innermost sleeve arrangement for a substantial portion of the length of the bundle in order to positively maintain the position and configuration of the bundle Within desired limits, said unit comprising a fluid passageway therethrough and orifices connected therewith for handling fluid supplied into said bundle exteriorly of said tubular elements.
ROBERT A. OLEARY, Primal Examiner.
10 A. W. DAVIS, JR., Assistant Examiner.
U.S. Cl. X.R.
US634631A 1967-04-28 1967-04-28 Heat transfer apparatus having flexible plastic tubular elements arranged in a braided configuration Expired - Lifetime US3419069A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US634631A US3419069A (en) 1967-04-28 1967-04-28 Heat transfer apparatus having flexible plastic tubular elements arranged in a braided configuration
GB19714/68A GB1199590A (en) 1967-04-28 1968-04-25 Tubular Heat Exchanger
FR1583962D FR1583962A (en) 1967-04-28 1968-04-26

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US634631A US3419069A (en) 1967-04-28 1967-04-28 Heat transfer apparatus having flexible plastic tubular elements arranged in a braided configuration

Publications (1)

Publication Number Publication Date
US3419069A true US3419069A (en) 1968-12-31

Family

ID=24544595

Family Applications (1)

Application Number Title Priority Date Filing Date
US634631A Expired - Lifetime US3419069A (en) 1967-04-28 1967-04-28 Heat transfer apparatus having flexible plastic tubular elements arranged in a braided configuration

Country Status (3)

Country Link
US (1) US3419069A (en)
FR (1) FR1583962A (en)
GB (1) GB1199590A (en)

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2010138A1 (en) * 1968-06-04 1970-02-13 Du Pont
US3529664A (en) * 1969-04-23 1970-09-22 Du Pont End structure for thermoplastic tubing
DE2126248A1 (en) * 1970-05-26 1971-12-02 E.I. du Pont de Nemours and Co., Wilmington, Del. (V.StA.) Plant and process for the heat exchange of liquids
US3804160A (en) * 1970-05-26 1974-04-16 Du Pont Fluid heat exchange system
US3805881A (en) * 1971-08-17 1974-04-23 Du Pont Fluid heat exchange system
US3863712A (en) * 1970-08-14 1975-02-04 Frank T Smith Liquid heat exchange system
DE2441333A1 (en) * 1973-08-30 1975-03-27 Teijin Ltd DEVICE FOR TREATMENT OF FLUIDS AND METHOD FOR MANUFACTURING THE SAME
DE2536494A1 (en) * 1975-08-16 1977-02-24 Bayer Ag Hollow fibre bundle for osmotic separations - with fibres arranged in spiral formation around a core, and in cartridge form
WO1981000297A1 (en) * 1979-07-11 1981-02-05 Du Pont Apparatus with expandable tube bundle
US4256178A (en) * 1977-02-17 1981-03-17 Maschinenfabrik Augsburg-Nurnberg Aktiengesellschaft Coaxial heat exchanger and method for constructing a heat exchanger
US4271900A (en) * 1978-06-28 1981-06-09 E. I. Du Pont De Nemours And Company Apparatus with expandable tube bundle
WO1981002705A1 (en) * 1980-03-24 1981-10-01 Baxter Travenol Lab Forming diffusion membrane units with joined capillary membrane tubes
US4484624A (en) * 1978-11-06 1984-11-27 Akzo Nv Apparatus for transferring heat by means of hollow filaments, and its use in various heating systems
US4588026A (en) * 1979-06-11 1986-05-13 Raytheon Company Coiled heat exchanger
DE3508382A1 (en) * 1985-03-08 1986-09-11 Akzo Gmbh, 5600 Wuppertal DEVICE FOR THE TRANSFER OF HEAT AND / OR FABRIC WITH THE AID OF CAVE THREADS
DE3614339A1 (en) * 1986-04-28 1987-10-29 Akzo Gmbh HEAT EXCHANGER AND METHOD FOR PRODUCING HEAT EXCHANGER
DE3614342A1 (en) * 1986-04-28 1987-10-29 Akzo Gmbh HEAT AND / OR FABRIC EXCHANGER AND METHOD FOR PRODUCING HEAT AND / OR FABRIC EXCHANGER
WO1995026488A1 (en) * 1994-03-28 1995-10-05 Minntech Corporation Wound heat exchanger oxygenator
US5472044A (en) * 1993-10-20 1995-12-05 E. I. Du Pont De Nemours And Company Method and apparatus for interacting a gas and liquid on a convoluted array of tubes
US6390187B1 (en) * 1998-12-29 2002-05-21 Valeo Thermique Moteur Heat exchanger with flexible tubes
US20160109197A1 (en) * 2014-10-15 2016-04-21 Hamilton Sundstrand Corporation Prevention of cooling flow blockage

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA971554A (en) * 1970-08-14 1975-07-22 Robert D. Smith Liquid heat exchange system
DE3216877C1 (en) * 1982-05-03 1983-11-03 Donald Dipl.-Ing. 1000 Berlin Herbst Heat exchange element that can be built into a housing

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3315740A (en) * 1965-01-14 1967-04-25 Du Pont Flexible plastic tube bundle and method of making
US3363680A (en) * 1966-07-21 1968-01-16 Du Pont Plastic tube heat exchanger with novel header construction

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3315740A (en) * 1965-01-14 1967-04-25 Du Pont Flexible plastic tube bundle and method of making
US3363680A (en) * 1966-07-21 1968-01-16 Du Pont Plastic tube heat exchanger with novel header construction

Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3526274A (en) * 1968-06-04 1970-09-01 Du Pont Cross flow box cooler unit
FR2010138A1 (en) * 1968-06-04 1970-02-13 Du Pont
US3529664A (en) * 1969-04-23 1970-09-22 Du Pont End structure for thermoplastic tubing
DE2126248A1 (en) * 1970-05-26 1971-12-02 E.I. du Pont de Nemours and Co., Wilmington, Del. (V.StA.) Plant and process for the heat exchange of liquids
US3804160A (en) * 1970-05-26 1974-04-16 Du Pont Fluid heat exchange system
US3863712A (en) * 1970-08-14 1975-02-04 Frank T Smith Liquid heat exchange system
US3805881A (en) * 1971-08-17 1974-04-23 Du Pont Fluid heat exchange system
DE2441333A1 (en) * 1973-08-30 1975-03-27 Teijin Ltd DEVICE FOR TREATMENT OF FLUIDS AND METHOD FOR MANUFACTURING THE SAME
DE2536494A1 (en) * 1975-08-16 1977-02-24 Bayer Ag Hollow fibre bundle for osmotic separations - with fibres arranged in spiral formation around a core, and in cartridge form
US4256178A (en) * 1977-02-17 1981-03-17 Maschinenfabrik Augsburg-Nurnberg Aktiengesellschaft Coaxial heat exchanger and method for constructing a heat exchanger
US4271900A (en) * 1978-06-28 1981-06-09 E. I. Du Pont De Nemours And Company Apparatus with expandable tube bundle
US4484624A (en) * 1978-11-06 1984-11-27 Akzo Nv Apparatus for transferring heat by means of hollow filaments, and its use in various heating systems
US4588026A (en) * 1979-06-11 1986-05-13 Raytheon Company Coiled heat exchanger
WO1981000297A1 (en) * 1979-07-11 1981-02-05 Du Pont Apparatus with expandable tube bundle
WO1981002705A1 (en) * 1980-03-24 1981-10-01 Baxter Travenol Lab Forming diffusion membrane units with joined capillary membrane tubes
US4346006A (en) * 1980-03-24 1982-08-24 Baxter Travenol Laboratories, Inc. Diffusion membrane units with adhered semipermeable capillaries
DE3508382A1 (en) * 1985-03-08 1986-09-11 Akzo Gmbh, 5600 Wuppertal DEVICE FOR THE TRANSFER OF HEAT AND / OR FABRIC WITH THE AID OF CAVE THREADS
US4867233A (en) * 1986-04-28 1989-09-19 Akzo N.V. Heat exchanger and method of making heat exchangers
DE3614342A1 (en) * 1986-04-28 1987-10-29 Akzo Gmbh HEAT AND / OR FABRIC EXCHANGER AND METHOD FOR PRODUCING HEAT AND / OR FABRIC EXCHANGER
US4834930A (en) * 1986-04-28 1989-05-30 Akzo N.V. Method for the manufacture of apparatus for the transfer of heat and/or mass
DE3614339A1 (en) * 1986-04-28 1987-10-29 Akzo Gmbh HEAT EXCHANGER AND METHOD FOR PRODUCING HEAT EXCHANGER
US5472044A (en) * 1993-10-20 1995-12-05 E. I. Du Pont De Nemours And Company Method and apparatus for interacting a gas and liquid on a convoluted array of tubes
WO1995026488A1 (en) * 1994-03-28 1995-10-05 Minntech Corporation Wound heat exchanger oxygenator
US5706889A (en) * 1994-03-28 1998-01-13 Minntech Corporation Wound heat exchanger oxygenator
US5718869A (en) * 1994-03-28 1998-02-17 Minntech Corporation Wound heat exchanger oxygenator
US6390187B1 (en) * 1998-12-29 2002-05-21 Valeo Thermique Moteur Heat exchanger with flexible tubes
US20160109197A1 (en) * 2014-10-15 2016-04-21 Hamilton Sundstrand Corporation Prevention of cooling flow blockage
US10415903B2 (en) * 2014-10-15 2019-09-17 Hamilton Sundstrand Corporation Prevention of cooling flow blockage

Also Published As

Publication number Publication date
GB1199590A (en) 1970-07-22
FR1583962A (en) 1969-12-12

Similar Documents

Publication Publication Date Title
US3419069A (en) Heat transfer apparatus having flexible plastic tubular elements arranged in a braided configuration
US3277959A (en) Plastic tube heat exchanger and process of making
US3438434A (en) Subdivided heat exchanger tube bundle assembly providing longitudinally distributed fluid bypass and distributing channels
US3526274A (en) Cross flow box cooler unit
US514338A (en) Surface condenses
US3265124A (en) Coated graphite products
US4570679A (en) Conduction of low temperature fluid
EP0412177B1 (en) Static mixing device
JP3986557B2 (en) Heating element
US3243170A (en) Tower packing units
NO142460B (en) HOLDER FOR ROOMS IN A HEAT EXCHANGE
CN101711183A (en) Filling-material structure of fluid contacting column and preparation method thereof
US3127200A (en) Sayag
US3195627A (en) Heat exchangers
US3582045A (en) Polymer intermingler
JPS61153388A (en) Heat exchange device
US3330336A (en) Heat exchanger tubes with longitudinal ribs
US469731A (en) Boiler-tube
DE1601162B2 (en) PIPE REACTOR FOR PERFORMING ENDO AND EXOTHERMAL REACTIONS WITH FORCED CIRCULATION OF THE HEAT TRANSFER MEDIUM
US2376349A (en) Loosely dumped filling body
US2744813A (en) Catalytic furnace
US3770051A (en) Apparatus for heat treatment of synthetic fibre yarn
DK157707B (en) TUBES-HEAT EXCHANGE
US1713456A (en) Heat-exchange coil
US3307621A (en) Heat transfer apparatus

Legal Events

Date Code Title Description
AS Assignment

Owner name: AMETEK, INC., 410 PARK AVENUE, NEW YORK, NEW YORK

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:E.I. DU PONT DE NEMOURS AND COMPANY;REEL/FRAME:004589/0577

Effective date: 19860602