EP2771637A1 - Echangeur de chaleur à tube en polymère - Google Patents

Echangeur de chaleur à tube en polymère

Info

Publication number
EP2771637A1
EP2771637A1 EP12795120.0A EP12795120A EP2771637A1 EP 2771637 A1 EP2771637 A1 EP 2771637A1 EP 12795120 A EP12795120 A EP 12795120A EP 2771637 A1 EP2771637 A1 EP 2771637A1
Authority
EP
European Patent Office
Prior art keywords
heat exchanger
tubes
polymer
polyarylene sulfide
aromatic
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.)
Ceased
Application number
EP12795120.0A
Other languages
German (de)
English (en)
Inventor
Georgios S. Zafiris
John P. Wesson
Satyam Bendapudi
Brian L. Deperro
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.)
Carrier Corp
Original Assignee
Carrier Corp
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 Carrier Corp filed Critical Carrier Corp
Publication of EP2771637A1 publication Critical patent/EP2771637A1/fr
Ceased legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/06—Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material
    • F28F21/062—Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material the heat-exchange apparatus employing tubular conduits
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2255/00—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes
    • F28F2255/16—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes extruded

Definitions

  • the subject matter disclosed herein generally relates to heat exchangers and, more particularly, to heat exchangers having polymer tubes.
  • Heat exchangers are widely used in various applications, including but not limited to heating and cooling systems including hydronic fan coil units, heating and cooling in various industrial and chemical processes, heat recovery systems, and the like, to name but a few.
  • Many heat exchangers for transferring heat from one fluid to another fluid utilize one or more tubes through which one fluid flows while a second fluid flows around the tubes. Heat from one of the fluids is transferred to the other fluid by conduction through the tube wall.
  • Heat exchanger tubes may be made from a variety of materials, including metals such as aluminum or copper.
  • Metal heat exchanger tubes offer a number of different advantages, including high thermal conductivity and strength.
  • metal heat exchanger tubes also suffer from a number of problems.
  • metal heat exchanger tubes can be expensive and time-consuming to manufacture, are subject to corrosion from certain types of fluids, are and can impose limitations on the design of the heat exchanger due to the limitations of metal fabrication techniques.
  • Nylon plastic tubes have also been used for heat exchangers.
  • Plastic tube heat exchangers have not achieved widespread acceptance due to a number of problems such as low thermal conductivity and/or the necessity of high wall thicknesses in order to provide physical robustness to tubes under a wide variety of operating conditions such as high temperatures and/or pressures (e.g., in hydronic building heating systems, water temperatures can reach temperatures of 90°C and pressures of 3100 kPa).
  • Composite tubes have also been proposed that use plastic as part of the composite; however, such tubes can be expensive and difficult to manufacture, and composite tubes also may require high wall thicknesses to accommodate the various materials of the composite.
  • a heat exchanger includes a plurality of polymer tubes extending between and fluidly connecting an inlet manifold and an outlet manifold, thereby providing a flow path inside said tubes for a first fluid between the inlet manifold and the outlet manifold.
  • the tubes are configured to have space between the exterior surfaces thereof, thereby providing a fluid flow path for a second fluid through the space between the exterior surfaces of the tubes.
  • the tubes further comprise polyarylene sulfide, polyarylether ketone, aromatic polysulfone, aromatic polyetherimide, or blends thereof.
  • the tubes have a diameter of 1 mm to 10 mm and a wall thickness of 0.1 mm to 1 mm.
  • FIG. 1 is a schematic diagram depicting a front view of the tube portion of an exemplary heat exchanger
  • FIG. 2 is a schematic diagram depicting a top view of the tube portion of the exemplary heat exchanger of FIG. 1 ;
  • FIG. 3 is a schematic diagram depicting an end view of the tube portion of the exemplary heat exchanger of FIG. 1 ;
  • FIGS. 4A-C depict a schematic diagram of an exemplary heat exchanger known as a spiral heat exchanger
  • FIGS. 5A-B depict a schematic diagram of an exemplary heat exchanger known as a plate heat exchanger
  • FIG. 6 is a schematic diagram depicting a cross-sectional view of an exemplary tube structure having an integrated support
  • FIG. 7 is a schematic diagram depicting a cross-sectional view of an exemplary tube structure having an integrated support.
  • the polymer tubes described herein are formed from a thermoplastic composition comprising polyarylene sulfide, polyarylether ketone, aromatic polysulfone, aromatic polyetherimide, or blends thereof.
  • polyarylene sulfide as used herein, includes any polyarylene sulfide- series resin (polyarylene thioether- series resin), and may be a homopolymer or copolymer having a polyarylene sulfide backbone having— (Ar— S— )— repeat units wherein Ar represents an arylene group.
  • Exemplary arylene groups include p- phenylene, m-phenylene, o-phenylene group, substituted phenylene groups (e.g., an alkylphenylene group having substituent(s) such as a C1-5 alkyl group, or an arylphenylene group having substituent(s) such as phenyl group), ⁇ , ⁇ '-diphenylenesulfone, p,p'-biphenylene, ⁇ , ⁇ '-diphenylene ether, and ⁇ , ⁇ '-diphenylenecarbonyl.
  • substituted phenylene groups e.g., an alkylphenylene group having substituent(s) such as a C1-5 alkyl group, or an arylphenylene group having substituent(s) such as phenyl group
  • ⁇ , ⁇ '-diphenylenesulfone p,p'-biphenylene
  • ⁇ , ⁇ '-diphenylene ether ⁇ ,
  • the polyarylene sulfide- series resin may be a homopolymer of a single repeat unit such as any of the above-mentioned repeat units, or may be a copolymer containing different repeat units such as any of the above- mentioned repeat units.
  • the polyarylene sulfide comprises at least 70 mol% p-phenylene sulfide repeat units.
  • the polyarylene sulfide comprises at least 90 mol% p-phenylene sulfide repeat units.
  • the polyarylene sulfide resin is a poly(p-phenylene sulfide) homopolymer.
  • the polyarylene sulfide resin may be obtained by allowing a relative low molecular weight of a linear polymer to crosslink with oxidation, or a high molecular weight polymer having a substantially linear structure which may be obtained by condensation polymerization from a bifunctional monomer.
  • a branched or crosslinked polyarylene sulfide resin obtained by a polymerization of the monomer in combination with a monomer having functional groups.
  • the polyarylene sulfide may be a polybiphenylene sulfide (PBPS), a polyarylene sulfide ketone (PPSK), a polybiphenylene sulfide sulfone (PPSS), or other polyarylene sulfide variants as known in the art.
  • the polyarylene sulfide can be blended or alloyed with an elastomer. Exemplary number average molecular weights of the polyphenylene sulfide- series resin can range from about 300 to 30 x 10 4 , more specifically about 400 to 10 x 10 4 .
  • the polyphenylene sulfide polymers are commercially available from Chevron Phillips Chemicals and Ticona Celanese under the brand names RYTON ® and FORTRON ® , respectively.
  • the polyphenylene sulfide polymer alloys and blends are commercially available from Chevron Phillips Chemicals under the brand name XTEL.
  • PAEK polyaryl ether ketones
  • PAEK resins include, but are not limited to, polyether ketones (PEK), polyether ether ketones (PEEK), polyether ketone ether ketone ketones (PEKEKK) and polyether ketone ketones (PEKK) and copolymers containing such groups as well as blends thereof.
  • the PAEK polymers may comprise monomer units containing an aromatic ring, usually a phenyl ring, a ketone group and an ether group in any sequence. Low levels, for example less than 10 mole %, of addition linking groups may be present as long as they do not fundamentally alter the properties of the PAEK resin.
  • PEEK is commercially available from Victrex Ltd. as VICTREX® PEEK.
  • PEKEKK resin is commercially available from BASF as ULTRAPEK .
  • Polyether ether ketone resins are also available under the GATONE TM and KETASPIRE ® trade names from Solvay Co. and Solvay Advanced Polymers.
  • the first resin component is a polymer selected from the group consisting of at least one of polyaryl ether ketones, polyaryl ketones, polyether ketones and polyether ether ketones.
  • Any of the PAEK polymers can be used which will have improved properties through blending with a second resin component according to the present invention. This encompasses the use of one or more polymers from any of the several classes of PAEK resins described herein or described in the references cited herein.
  • polyaryl ether ketones which are highly crystalline, with melting points above 300°C, can be used in blends according to the present invention.
  • Examples of these crystalline polyaryl ether ketones are shown in the structures (I), (II), (III), (IV) and (V) below.
  • polyaryl ether ketones The formation and properties of polyaryl ether ketones is well known in the art.
  • electrophilic aromatic substitution e.g., Friedel-Crafts catalyzed
  • aromatic diacyl halides with unsubstituted aromatic compounds such as diphenyl ether
  • a broad range of resins can be formed, for example, by the nucleophilic aromatic substitution reaction of an activated aromatic dihalide and an aromatic diol or salt thereof, as shown, for example, in US Patent 4,175,175.
  • Ar is independently a divalent aromatic radical selected from phenylene
  • X is independently -0-, -C(O)-, -O-Ar-C(O)-, -S-, -S0 2 - or a direct bond, and n is an integer of from 0 to about 10.
  • PAEK resins can be prepared by methods well known in the art.
  • One such method comprises heating a substantially equimolar mixture of at least one bisphenol, often reacted as its bis-phenolate salt, and at least one of either a dihalobenzoid compound or, in other cases, at least one halophenol compound may be reacted to form polymer.
  • mixtures of these compounds may be used.
  • hydroquinone can be reacted with a dihalo aryl ketone, such a dichloro benzophenone of difluoro benzophenone to form a polyaryl ether ketone.
  • dihydroxy aryl ketone such as dihydroxy benzophenone can be polymerized with aryl dihalides such as dichloro benzene to form PAEK resins.
  • dihydroxy aryl ethers such as dihydroxy diphenyl ether can be reacted with dihalo aryl ketones, such as difluoro benzophenone.
  • dihydroxy compounds with no ether linkages such as or dihydroxy biphenyl or hydroquinone may be reacted with dihalo compounds which may have both ether and ketone linkages, for instance bis-(dichloro phenyl) benzophenone.
  • diaryl ether carboxylic acids or carboxylic acid halides can be polymerized to form polyaryl ether ketones.
  • Examples of such compounds are diphenylether carboxylic acid, diphenyl ether carboxylic acid chloride, phenoxy-phenoxy benzoic acid, and mixtures thereof.
  • dicarboxylic acids or dicarboxylic acid halides can be condensed with diaryl ethers, for example iso- or tere- phthaloyl chlorides (or mixtures thereof) can be reacted with diphenyl ether, to form PAEK resins.
  • Polyaryl ether ketones may also be prepared by other processes.
  • One example is a process in which reactants such as: (a) a dicarboxylic acid; (b) at least one divalent aromatic radical and at least one mono aromatic dicarboxylic acid and, (c) combinations of (a) and (b), are reacted in the presence of a fluoroalkane sulfonic acid, particularly trifluoromethane sulfonic acid.
  • a fluoroalkane sulfonic acid particularly trifluoromethane sulfonic acid.
  • Additional polyaryl ether ketones may be prepared according to a process wherein aromatic diacyl compounds are polymerized with at least one aromatic compound and at least one mono acyl halide as described in, for example, US Patent 4,398,020.
  • PAEK resin weight average molecular weight (Mw) may vary from 5,000 to 150,000 g/mole, specifically from about 10,000 to 80,000 g/mole
  • Aromatic polysulfone as used herein includes any polymer having repeat units, a portion of which includes the structure (VI)
  • the aromatic polysulfone backbone can include a number of other connecting units, including an isopropylidene linkage that is part of the repeat unit of the well-known bisphenol A-based polysulfone.
  • polysulfone polysulfone
  • polyphenylenesulfone polyphenylenesulfone
  • polyethersulfone polyethersulfone
  • crosslinking or other functional groups and substituents can be included in the polymer structure to achieve target properties, as is known in the art.
  • Exemplary molecular weights for aromatic polysulfones can range from 40,000 to 80,000, more specifically 50,000 to 70,000.
  • Aromatic polyetherimide as used herein, includes any polymer that comprises repeat units of the formula (XI)
  • the polyimide, polyetherimide or polyetherimide sulfone may be a copolymer. Mixtures of the polyimide, polyetherimide or polyetherimide sulfone may also be employed.
  • the polyetherimide can be prepared by any of the methods well known to those skilled in the art, including the reaction of an aromatic bis(ether anhydride) of the formula (XII)
  • aromatic bis anhydrides examples include:
  • Another class of aromatic bis(ether anhydride)s included by formula (XII) above includes, but is not limited to, compounds wherein T is of the formula (XIV) (Formula XIV) and the ether linkages, for example, are preferably in the 3,3', 3,4', 4,3', or 4,4' positions, and mixtures thereof, and where Q is as defined above.
  • Any diamino compound may be employed.
  • suitable compounds are ethylenediamine, propylenediamine, trimethylenediamine, diethylenetriamine, triethylenetertramine, hexamethylenediamine, heptamethylenediamine, octamethylenediamine, nonamethylenediamine, decamethylenediamine, 1,12- dodecanediamine, 1,18-octadecanediamine, 3-methylheptamethylenediamine, 4,4- dimethylheptamethylenediamine, 4-methylnonamethylenediamine, 5- methylnonamethylenediamine, 2,5-dimethylhexamethylenediamine, 2,5- dimethylheptamethylenediamine, 2, 2-dimethylpropylenediamine, N-methyl-bis (3- aminopropyl) amine, 3-methoxyhexamethylenediamine, l,2-bis(3-aminopropoxy) ethane, bis(3-aminopropyl) sul
  • the polyetherimide resin comprises structural units according to formula (XI) wherein each R is independently p-phenylene or m-phenylene or a mixture thereof and T is a divalent radical of the formula (XV) (Formula XV)
  • polyetherimides include those disclosed in US Patents 3,847,867, 3,852,242, 3,803,085, 3905,942, 3,983,093, and 4,443,591, the disclosures of which are incorporated herein by reference in their entirety.
  • Polyimides, polyetherimides and polyetherimide sulfones may have a melt index of about 0.1 to about 10 grams per minute (g/min), as measured by American Society for Testing Materials (ASTM) D1238 at 340 to about 370°C, using a 6.6 kilogram (kg) weight.
  • ASTM American Society for Testing Materials
  • the polyetherimide resin has a weight average molecular weight (Mw) of about 10,000 to about 150,000 grams per mole (g/mole), as measured by gel permeation chromatography, using a polystyrene standard. In another embodiment the polyetherimide has Mw of 20,000 to 60,000. Such polyetherimide resins typically have an intrinsic viscosity greater than about 0.2 deciliters per gram (dl/g), or, more specifically, about 0.35 to about 0.7 dl/g as measured in m-cresol at 25 °C. Examples of some polyetherimides useful in blends described herein are listed in ASTM D5205 "Standard Classification System for Polyetherimide (PEI) Materials”.
  • the composition can be further modified, if desired, by including one or more additives often used with thermoplastic polymers, some of which may serve to beneficially affect the chemical and physical properties.
  • additives often used with thermoplastic polymers, some of which may serve to beneficially affect the chemical and physical properties.
  • examples are mineral fillers, including clay, reinforcing agents, for example, glass fibers, flakes or spheres, plasticizers, flame retardants, stabilizers, antioxidants, colorants, processing aids, and the like as known in the art.
  • the resin composition includes a nanoparticle additive for enhancing the thermal conductivity of the composition.
  • additives include aluminum nanoflakes or carbon nanoparticles, with particle sizes ranging from about 10 nm to about 250 nm, more specifically about 50 nm to about 200 nm, and even more specifically from about 50 nm to about 100 nm.
  • the resin compositions used in the present invention can be prepared and/or formed into tubes by a variety of methods involving intimate admixing of the materials with any additional additives desired in the formulation. Suitable procedures include solution blending and melt blending. Because of the availability of melt blending equipment in commercial polymer processing facilities, melt processing procedures may be readily used. Examples of equipment used in such melt compounding methods include: co-rotating and counter-rotating extruders, single screw extruders, disc-pack processors and various other types of extrusion equipment. In some instances, the compounded material exits the extruder through appropriately- shaped holes in a die and the resulting tubes are cooled by air or by passing through a water bath. The cooled tubes can then be cut to an appropriate length.
  • rapid cooling of the tubes can result in low levels of crystallinity that adversely impact physical properties (e.g., dimensional stability) of the polymer tube.
  • the above-described polymer compositions can be adjusted by post-production processing such as annealing at elevated temperatures to produce target crystallinities or other properties. Annealing temperatures can range from about 80°C to about 180°C.
  • Exemplary polymer compositions for which such annealing may be used include polyphenylene sulfides and/or polyarylether ketones, with which annealing can be used to produce target crystallinities of about 10% to about 85% (more specifically about 30% to about 80%), and the annealing temperature can vary with the choice of polymer (e.g., useful annealing temperatures for polyphenylene sulfides can range from about 80°C to about 130°C.
  • Annealing can be carried out with conventional heat sources such as radiant or convective heat sources either on-line with the tube extrusion process or off-line at some point in time after the tubes have been manufactured.
  • FIG. 1 An exemplary heat exchanger is shown in schematic diagram form in FIG. 1.
  • FIG. 1 depicts a heat exchanger 10 such as for use in a typical fan coil heat exchanger unit.
  • a bank of tubes 12 extends between end plates 14 and 16.
  • Tube supports 18 are disposed at positions between the end plates and have openings therein through which the tubes 12 pass.
  • Inlet plenum 20 having inlet 22 receives a first fluid (e.g., water, ethylene glycol, or the like), which flows through the tubes 12 and out into an outlet plenum 24, from where it flows through outlet 25 and out of the heat exchanger.
  • a first fluid e.g., water, ethylene glycol, or the like
  • FIG. 2 depicts a top view of the heat exchanger 10, and shows the flow of a second fluid (e.g., air) between the tubes of the tube bank.
  • FIG. 3 depicts an end view of the heat exchanger 10 taken at a cross-section through or at the end plate 14. End plate 14 has a number of holes 26 therein that receive the tubes 12.
  • the tubes are sealingly attached to the end plate by conventional techniques, including but not limited to the use of an adhesive, laser welding, ultrasonic welding, or other thermoplastic welding techniques such as magnetic induction or microwave welding performed by magnetic induction or microwave heating of metal particle additives in the tube and/or end plate polymer compositions.
  • FIGS. 4A and 4B depict side and end views, respectively, of a spiral heat exchanger 40 having a continuous spiral tube 12' with inlet 42 and outlet 44. Heat transfer fluid enters the spiral tube 12' at inlet 42 at the perimeter of the spiral and exits outlet 44 at the center of the spiral while air to be heated or cooled by the heat transfer fluid is directed in a perpendicular direction across the spiral tube 12'.
  • Multiple spiral heat exchangers may be stacked in modular fashion as shown in FIG. 4C.
  • FIG. 5A schematically depicts a plate heat exchanger 50 having heat transfer tubes 12", inlet portion 52, and outlet portion 54. The plate heat exchanger is distinguished from the heat exchanger of FIG.
  • tubes 12" have a rectangular cross-section, and in that the entire assembly 50 can be injection molded in a single injection molding shot process.
  • Multiple plate heat exchangers may be stacked in modular fashion as shown in FIG. 5B having two end modules 50' and one or more middle modules 50".
  • stacked heat exchanger modules have gaskets between them and are fastened together with adhesive or with mechanical connections such as a threaded nut and bold connector or other known connectors.
  • modules on each end of the stack include a solid end wall as part of their injection molded structure.
  • the polymer tubes 12 may have different cross-sectional configurations, including but not limited to circular, ovular, elliptical, square, or rectangular. Tubes with ovular or elliptical cross-sections can have a cross- sectional aspect ratio of greater than 1 and less than or equal to 4.
  • the wall thickness of the tubes can range from about 0.1 mm to about 1 mm, and more specifically from about 0.2 mm to about 0.5 mm.
  • the diameter of circular tubes can range from about 1 mm to about 10 mm, and more specifically from about 2 mm to about 5 mm, and ovular or elliptical tubes can be sized to have cross-sectional areas equivalent to circular tubes with such diameters.
  • Tubes can be formed using conventional extrusion techniques that are well-known in the art and do not require further detailed explanation herein.
  • the liquid carrying channels can be of rectangular cross-section and of the above sizes and wall thicknesses, and are formed by injection molding along with the manifolds in one injection molding shot, such as for the plate heat exchanger of FIG. 5.
  • a composition comprising the above- described polyarylene sulfide, polyarylether ketone, aromatic polysulfone, aromatic polyetherimide polymers is co-extruded as one or more layers in a multi-layer tube.
  • a multi-layer tube also includes a barrier layer such as a fluoropolymer (e.g., polyvinylidene fluoride (PVDF), ethylene tetrafluoroethylene (ETFE), perflouroalkoxy (PFA) resins, or polytetrafluoroethylene (PTFE).
  • PVDF polyvinylidene fluoride
  • ETFE ethylene tetrafluoroethylene
  • PFA perflouroalkoxy
  • PTFE polytetrafluoroethylene
  • adhesion of some fluoropolymers to adjacent layer(s) of a multi-layer tube structure can be enhanced through the inclusion of tie layers of adhesion-promoting polymers adjacent to the fluoropolymer layer(s) (e.g., PFA or ETFE, or polymer blends containing a fluoropolymer and one or more other polymers compatible with both the fluoropolymer and the adjacent polymer layers).
  • tie layers of adhesion-promoting polymers adjacent to the fluoropolymer layer(s) e.g., PFA or ETFE, or polymer blends containing a fluoropolymer and one or more other polymers compatible with both the fluoropolymer and the adjacent polymer layers.
  • the tubes can be extruded with integrated supports.
  • Such supports can provide strength and integrity to the tube, and may be particularly useful for non-circular cross-section tubes.
  • Integrated supports can be of any cross-sectional shape, including circular or rectangular, and can be internal or external to the tube. Internal supports may extend part way across the diameter of the tube or may be a web structure that extends completely across the tube diameter.
  • FIG. 4 internal support structure
  • FIG. 5 external support structure

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

L'invention porte sur un échangeur de chaleur à tube en polymère, qui comprend une pluralité de tubes en polymère s'étendant entre un collecteur d'entrée et un collecteur de sortie et raccordés fluidiquement à ces collecteurs, en créant ainsi un trajet d'écoulement à l'intérieur desdits tubes pour un premier fluide entre le collecteur d'entrée et le collecteur de sortie. Les tubes sont conçus pour présenter un espace libre entre leurs surfaces extérieures, en créant ainsi un trajet d'écoulement de fluide pour un second fluide à travers l'espace entre les surfaces extérieures des tubes.
EP12795120.0A 2011-10-26 2012-10-26 Echangeur de chaleur à tube en polymère Ceased EP2771637A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201161551738P 2011-10-26 2011-10-26
PCT/US2012/062063 WO2013063359A1 (fr) 2011-10-26 2012-10-26 Echangeur de chaleur à tube en polymère

Publications (1)

Publication Number Publication Date
EP2771637A1 true EP2771637A1 (fr) 2014-09-03

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Country Status (4)

Country Link
US (1) US20140262183A1 (fr)
EP (1) EP2771637A1 (fr)
CN (1) CN103890533A (fr)
WO (1) WO2013063359A1 (fr)

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US20140262183A1 (en) 2014-09-18
CN103890533A (zh) 2014-06-25

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