EP3966513A1 - Échangeur de chaleur à faisceau tubulaire comportant des modules/éléments intégrés constitués de surfaces déflectrices et de barrettes de guidage - Google Patents

Échangeur de chaleur à faisceau tubulaire comportant des modules/éléments intégrés constitués de surfaces déflectrices et de barrettes de guidage

Info

Publication number
EP3966513A1
EP3966513A1 EP20733340.2A EP20733340A EP3966513A1 EP 3966513 A1 EP3966513 A1 EP 3966513A1 EP 20733340 A EP20733340 A EP 20733340A EP 3966513 A1 EP3966513 A1 EP 3966513A1
Authority
EP
European Patent Office
Prior art keywords
heat exchanger
windows
exchanger according
bundle
bundle heat
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.)
Granted
Application number
EP20733340.2A
Other languages
German (de)
English (en)
Other versions
EP3966513B1 (fr
EP3966513C0 (fr
Inventor
Felix Streiff
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.)
Sulzer Management AG
Original Assignee
Sulzer Management AG
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 Sulzer Management AG filed Critical Sulzer Management AG
Publication of EP3966513A1 publication Critical patent/EP3966513A1/fr
Application granted granted Critical
Publication of EP3966513B1 publication Critical patent/EP3966513B1/fr
Publication of EP3966513C0 publication Critical patent/EP3966513C0/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • F28D7/085Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/06Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits having a single U-bend
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
    • F28D7/1615Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/421Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
    • B01F25/423Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components
    • B01F25/4233Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components using plates with holes, the holes being displaced from one plate to the next one to force the flow to make a bending movement
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • 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
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0022Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for chemical reactors
    • 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
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0052Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for mixers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F28F2009/222Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F28F2009/222Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F28F2009/224Longitudinal partitions
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F28F2009/222Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F28F2009/226Transversal partitions

Definitions

  • the invention relates to bundled heat exchangers with assemblies (which can be designed as built-in elements, but do not have to) consisting of deflection surfaces and guide webs in the outer space according to the preamble of claim 1.
  • baffles are often used instead of baffles.
  • deflection surfaces is used to make it clear that their applicability is not limited to heat exchangers made of a metallic material.
  • the bundles can consist of tubes through which a heat exchange medium (for example a heating or cooling medium which heats or cools the product circulating in the outer space) is passed.
  • a heat exchange medium for example a heating or cooling medium which heats or cools the product circulating in the outer space
  • other heat exchange elements such as electric heating rods, electric heating coils and the like, combined into bundles, can also be used. can be used.
  • tubes or “tube bundles” are used in the following, although after what has been said it should be understood that other elongated heat exchange elements such as heating rods are also meant.
  • baffles or baffles is used to guide the flow by guiding the flow of the fluid in the outer space partly across and partly parallel to the pipes.
  • These sheets have bores corresponding to the pipe division, are perpendicular to the pipes and have segment-shaped windows for the axial passage of the fluid.
  • Other known embodiments consist alternately of discs and rings. They are installed as standard in turbulent (low-viscosity fluids) and laminar (viscous fluids) flow.
  • VDI Heat Atlas (6th edition), Sections Gg5 and Ob7.
  • each mixing element or pipe coil bundle requires its own collector for the heat transfer medium.
  • the pressure loss on the heat carrier side in the pipes is high because of the long lines and many pipe bends. Different lengths of the coils lead to uneven distribution of the flows on the heat transfer side and can in turn cause maldistribution on the product side.
  • the object of the invention is to create a tube bundle heat exchanger, mixer heat exchanger or mixing reactor of the type mentioned at the outset which avoids the disadvantages of the prior art. This object is achieved by the characterizing features of claim 1.
  • the tube bundle heat exchanger according to the invention is particularly suitable for viscous products and can be manufactured very cheaply.
  • products can be heated, cooled, evaporated or exothermic reactions carried out with simultaneous, intensive mixing.
  • With low axial backmixing and low pressure loss it has no moving parts.
  • the formation of maldistribution is prevented and the fixtures are, if necessary, easily accessible for cleaning from the outside.
  • the apparatus is also very easy to scale.
  • the arrangement and the number of elongated (axially aligned) pipes (or other heat exchange elements) through which there is a flow can be freely selected.
  • Fig. 2 is a perspective view of the same
  • FIG. 3 shows a view of the entry side of an installation element according to FIG. 1,
  • FIG. 5 shows a view of the entry side of an installation element in an alternative
  • FIG. 17 is a perspective view of the embodiment according to FIGS. 9-16.
  • the product flows in the shell space of a tube bundle heat exchanger known per se with an inlet 2 and an outlet 3 for the product in the outer space 6.
  • An inlet 4 and an outlet 5 are provided for the heat transfer medium that is in the tubes 7 flows.
  • the baffles (or baffles) 8 that are usually present, which are perpendicular to the tubes or to the axis of the heat exchanger and have bores 7 'for the tubes, are modified so that they have two or more windows 12, 13 for the axial Leave the passage of the product from the inlet side to the outlet side of the deflection surface open.
  • At least one guide bar 10 or 11 is attached to the entry and exit side. These guide webs run parallel to the tubes and subdivide the cross section of the tube bundle into sections of approximately the same size. If necessary, the deflection surfaces can also be set at an angle to the heat exchanger or pipe axis, see reference number 9.
  • the guide webs 10, 11 on the entry side and exit side of the deflection surfaces are preferably 90 ° to one another.
  • the direction of flow of the partial flows transversely to the pipes on the outlet side is again opposite on both sides of the guide web 11.
  • Deflection surfaces with windows and crossing guide bars each form a built-in element A or B.
  • the guide bars 1 1, 10 'of built-in elements (A, B) following one another in the flow direction preferably intersect at 90 °. Closed partial areas 8, 8 'and windows 12, 12' and 13, 13 'of successive built-in elements A, B alternate.
  • each built-in element is divided into partial flows and mixed in such a way that in each built-in element at least one doubling of the number of layers (with two partial flows or one guide bar on the inlet and outlet side) with simultaneous intensive heat transfer.
  • the number of layers formed increases exponentially from inlet to outlet with the number of built-in elements following one another in the direction of flow. This process could be demonstrated on the basis of tests with rapidly hardening, tough polyester resin.
  • the mixing is intensified by turbulence.
  • the axial distance between successive deflection surfaces preferably corresponds to the height of two guide webs without any distances between them. The installation can, however, also take place at intervals or shortened with guide bars pushed into one another.
  • the deflection surfaces can also have several windows 25, 26, 27 and several pairs of guide bars (21, 22 and 23, 24). It is also possible that the number of guide bars on the entry side and on the exit side, or their height, is different. This increases the intensity of the mixing, but also increases the effort and pressure loss.
  • the flow path in the outer space is lengthened by the guide webs according to the invention. This also increases the flow velocity around the pipes and the heat transfer. The intensive mixing also prevents axial back mixing. The greater the number of successive assemblies / built-in elements in the heat exchanger and thus the slimmer the apparatus, the narrower the residence time distribution will be, analogous to a cascade of stirred tanks.
  • all of the previously known deflection plates (or surfaces) for heat exchangers do not cause any mixing in the case of laminar flow or viscous products.
  • the heat transfer is only improved, due to the better cross flow to the pipes.
  • the product flow is only diverted, but not divided and mixed.
  • FIG. 1 shows, by way of example, built-in elements A, B according to the invention from a deflection surface and associated guide bars in a U-tube heat exchanger with an extendable tube bundle.
  • the jacket 1 of the apparatus is shown axially cut open a little in front of the center or in front of the outlet-side guide web 11 of an installation element, while the installation elements are shown in the view.
  • a built-in element consists of closed partial areas, windows and associated guide bars on the entry and exit side.
  • the built-in elements can be loosely or wholly or partially firmly connected to the pipes by soldering, welding or gluing.
  • the individual parts of a built-in element are also at least partially connected in this way.
  • the internals are, as is customary with normal baffles, connected to one another and to the apparatus by holding rods. It is also possible to produce sub-elements, consisting of a guide bar and closed sub-areas, from sheet metal by bending.
  • the arrangement shown with U-tubes is only an example.
  • the built-in elements are also suitable for all other tube bundle heat exchangers such as those with permanently installed, straight tubes and tube sheets or for multi-thread devices. Non-circular (e.g. square or rectangular) apparatus cross-sections would also be possible.
  • electric heating rods or heating coils can also be used.
  • FIG. 2 shows a three-dimensional representation of a bundle of pipes 7 with built-in elements according to the invention which comprise windows 12, 13, closed partial surfaces 8 and guide webs 10, 11. Closed partial areas and windows of successive built-in elements each cover one another and successive guide webs preferably cross at an angle of 90 °.
  • FIG. 3 shows a view of the entry side of an installation element A according to the invention with a deflection surface 8 and two guide webs 10, 11 as well as two windows 12, 13 and bores 7 'in the closed partial surfaces for the pipes.
  • the area of the window normally corresponds approximately to the closed partial area. However, it is also possible to make the windows much smaller or in a different shape, such as slots or bores, in order to generate special flow effects or an additional pressure loss or to prevent the formation of strands.
  • 4 shows the view of the inlet side of a built-in element B according to the invention following in the direction of flow with a deflection surface 8 'and two guide webs 10', 11 'and two windows 12', 13 'and bores 7' for the pipes.
  • the closed partial areas and the windows are offset with respect to the preceding installation element shown in FIG. 3.
  • FIG. 5 shows a view of the entry side of an installation element according to the invention with a deflecting surface 8 with bores 7 'for the pipes and two guide webs 10, 11 and two windows 12, 13, the windows being one significantly smaller area than the deflection surface and have any shape.
  • FIG. 6 again shows the view of the entry side of another installation element according to the invention with a deflection surface 8 and four guide webs 21, 22, 23, 24 as well as three windows 25, 26, 27 and bores 7 'for the pipes.
  • FIG. 7 shows the view of the entry side of an installation element according to the invention with a deflection surface 8 and with only one guide bar 10 on the entry side, two guide bars 23, 24 and three windows 25, 26, 27 and bores 7 'for the pipes.
  • FIG. 8 is the view of the entry side of an installation element according to the invention, which follows an installation element in front of it according to FIG. 7, with a deflection surface 8 'and with only one guide web 10' on the entry side two guide webs 23 ', 24' and three Windows 25 ', 26', 27 'and holes 7' for the pipes.
  • the windows are each offset from the windows with respect to the element according to FIG. 7, so that no direct, axial passage is possible if the elements are arranged one after the other in the direction of flow.
  • FIGS. 9 to 17 are not all shown on the same scale.
  • the jacket 1 is omitted for reasons of illustration.
  • 9 is a plan view of the tube bundle of the heat exchanger with the deflection surfaces, windows and guide webs according to the invention.
  • the heat exchange medium heat or coolant
  • the guide webs are provided here with the reference numerals 10a to 10e.
  • Further guide bars 10a ', 10a "to 10e', 10e” are located at an angle of 90 ° to this, these guide bars each being at right angles with deflecting surfaces 8a ', 8a “; 8b '; 8c ', 8c “; 8d '; 8e ', 8e “are connected.
  • the reference symbols 8a ', 8a "; 8b '; 8c ', 8c “; 8d '; 8e ', 8e denote partial areas that have openings or bores for pipes to pass through.
  • the deflection surfaces are also through window 12a '; 12b ', 12b “; 12c '; 12d ', 12d "; 12e 'interrupted.
  • the geometry of the deflection surfaces and the windows cut out in them alternate from deflection surface to deflection surface, as will be explained in more detail below.
  • FIG. 10 shows the same structure as FIG. 9, but this time shown in the direction of the arrow X in FIG.
  • FIG. 11 is a plan view from the direction of the arrow XI in FIG. 9 with the marked sections XII-XII and XIII-XIII, which can be found in FIGS. 12 and 13, respectively.
  • Sections XIV-XIV, XV-XV and XVI-XVI are also indicated in FIG. 9. These sections are shown in FIGS. 14, 15 and 16, respectively.
  • the sections show the successive deflection surfaces, each of which has a complementary geometry to the previous (or next) deflection surface in order to ensure optimal mixing of the product to be mixed.
  • the deflecting surface shown in FIG. 14 has (covering) partial surfaces 8a, 8a ′′ which divert the flow of the product and have only one bore for a pipe. In between there is the (open) window 12a ‘, which offers no resistance to the flow and is only crossed by two pipes.
  • the turning surface shown in Fig. 15 is complementary to the turning surface of Fig. 14, i.
  • FIG. 17 finally shows a perspective illustration of the tube bundle heat exchanger described with reference to FIGS. 9 to 16, the arrow 28 indicating the direction of flow of the product (cf. FIG. 9).
  • this figure is not provided with reference numerals, but these emerge from FIGS. 9 to 16.
  • the assemblies or built-in elements and their components such as deflection surfaces and guide bars can be manufactured from steel and welded in a manner known per se. However, cast parts can also be used. Finally, production from plastics is also possible, e.g. in injection molding or additive manufacturing such as 3D printing.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

L'invention concerne un échangeur de chaleur à faisceau tubulaire comportant des éléments intégrés constitués de barrettes de guidage, de fenêtres et de barrettes de guidage. Lesdits éléments intégrés permettent d'obtenir un mélange permanent dans le courant de produit pendant le transfert de chaleur, ce qui empêche une mauvaise répartition et le rétromélange axial. En même temps, la voie d'écoulement est prolongée, et le transfert de chaleur se trouve ainsi amélioré. Le produit s'écoule à l'extérieur (6) d'un échangeur de chaleur à faisceau tubulaire (1) comportant une entrée (2) et une sortie (3) pour le produit, et une entrée (4) et une sortie (5) pour l'échangeur de chaleur dans les tubes (7). Les déflecteurs (ou surfaces déflectrices) (8) contenus dans un échangeur de chaleur à faisceau tubulaire sont modifiés de façon à laisser ouvertes des fenêtres (12, 13) et de telle sorte qu'au moins une barrette de guidage (10) ou (11) est montée sur le côté entrée et le côté sortie de la surface déflectrice. Lesdites barrettes de guidage s'étendent parallèlement aux axes des tubes, et se croisent. Le courant est divisé sur le côté entrée par les barrettes de guidage, et guidé dans des directions opposées aux fenêtres, où il sort ensuite sur des côtés opposés des barrettes de sortie, et est dévié.
EP20733340.2A 2019-05-28 2020-05-26 Échangeur de chaleur à faisceau tubulaire comportant des modules/éléments intégrés constitués de surfaces déflectrices et de barrettes de guidage Active EP3966513B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH00696/19A CH716236A2 (de) 2019-05-28 2019-05-28 Rohrbündel-Wärmeübertrager mit Einbauelementen aus Umlenkflächen und Leitstegen.
PCT/EP2020/064519 WO2020239734A1 (fr) 2019-05-28 2020-05-26 Échangeur de chaleur à faisceau tubulaire comportant des modules/éléments intégrés constitués de surfaces déflectrices et de barrettes de guidage

Publications (3)

Publication Number Publication Date
EP3966513A1 true EP3966513A1 (fr) 2022-03-16
EP3966513B1 EP3966513B1 (fr) 2024-07-17
EP3966513C0 EP3966513C0 (fr) 2024-07-17

Family

ID=71103336

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20733340.2A Active EP3966513B1 (fr) 2019-05-28 2020-05-26 Échangeur de chaleur à faisceau tubulaire comportant des modules/éléments intégrés constitués de surfaces déflectrices et de barrettes de guidage

Country Status (7)

Country Link
US (1) US12050065B2 (fr)
EP (1) EP3966513B1 (fr)
JP (1) JP2022535693A (fr)
KR (1) KR20220012323A (fr)
CN (1) CN113950604A (fr)
CH (1) CH716236A2 (fr)
WO (1) WO2020239734A1 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH717390A2 (de) * 2020-05-06 2021-11-15 Streiff Felix Baugruppen/Einbauelemente aus Umlenkflächen mit Trennstegen für den Einbau in Rohre/Kanäle oder in den Mantelraum von Rohrbündel-Wärmetauschern.

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Publication number Priority date Publication date Assignee Title
US1505429A (en) * 1922-04-08 1924-08-19 Whitlock Coil Pipe Company Heat-exchange apparatus
US3400758A (en) * 1966-05-16 1968-09-10 United Aircraft Prod Helical baffle means in a tubular heat exchanger
CH493811A (de) * 1967-09-06 1970-07-15 Basf Ag Wärmetauschvorrichtung
DE2839564C2 (de) 1978-09-12 1982-10-21 Hoechst Ag, 6000 Frankfurt Vorrichtung mit Zu- und Abfuhr von Wärme und zum Mischen von flüssigen Medien
US5217066A (en) * 1992-08-10 1993-06-08 Enfab, Inc. Integral heat exchanger and method of construction
EP0749776B1 (fr) * 1995-06-21 2001-01-24 Sulzer Chemtech AG Mélangeur avec corps en forme de tube
EP0998973A1 (fr) * 1998-10-27 2000-05-10 Balcke-Dürr Energietechnik GmbH Réacteur à faisceau de tubes refroidis
DE50003420D1 (de) 1999-07-07 2003-10-02 Fluitec Georg Ag Winterthur Vorrichtung für den Wärmetausch
DE50200013D1 (de) * 2002-03-22 2003-07-31 Sulzer Chemtech Ag Winterthur Rohrmischer mit einem longitudinalen Einbaukörper
DE10223788C1 (de) * 2002-05-29 2003-06-18 Lurgi Ag Wärmetauscher
US20090301699A1 (en) * 2008-06-05 2009-12-10 Lummus Novolent Gmbh/Lummus Technology Inc. Vertical combined feed/effluent heat exchanger with variable baffle angle
US20140262172A1 (en) * 2013-03-14 2014-09-18 Koch Heat Transfer Company, Lp Tube bundle for shell-and-tube heat exchanger and a method of use
DE102013004934A1 (de) * 2013-03-22 2014-09-25 Gkn Sinter Metals Holding Gmbh Rohrbündelrekuperator an einem Sinterofen sowie Wärmeübertragungsverfahren mit einem Sinterofen und mit einem Rohrbündelrekuperator
EP3029407A1 (fr) * 2014-12-02 2016-06-08 Borgwarner Emissions Systems Spain, S.L.U. Déflecteur rainuré pour un échangeur de chaleur
DE102015013516B4 (de) * 2015-10-20 2018-01-18 Frank Brucker Rohrbündelwärmeübertrager und Fertigungsverfahren für Rohrbündelwärmeübertrager
DK3415852T3 (da) * 2016-08-05 2024-02-05 Obshestvo S Ogranichennoi Otvetstvennostu Reinnolts Lab Skal- og rørkondensator og varmevekslingsrør til en skal- og rørkondensator (varianter)

Also Published As

Publication number Publication date
US20220236014A1 (en) 2022-07-28
JP2022535693A (ja) 2022-08-10
WO2020239734A1 (fr) 2020-12-03
CH716236A2 (de) 2020-11-30
EP3966513B1 (fr) 2024-07-17
EP3966513C0 (fr) 2024-07-17
CN113950604A (zh) 2022-01-18
US12050065B2 (en) 2024-07-30
KR20220012323A (ko) 2022-02-03

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