EP3719433A1 - Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide - Google Patents

Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide Download PDF

Info

Publication number
EP3719433A1
EP3719433A1 EP19020246.5A EP19020246A EP3719433A1 EP 3719433 A1 EP3719433 A1 EP 3719433A1 EP 19020246 A EP19020246 A EP 19020246A EP 3719433 A1 EP3719433 A1 EP 3719433A1
Authority
EP
European Patent Office
Prior art keywords
container
medium
heat exchanger
tube bundle
radial direction
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.)
Withdrawn
Application number
EP19020246.5A
Other languages
German (de)
English (en)
Inventor
Heinz Bauer
Manfred Steinbauer
Jürgen Spreemann
Florian Deichsel
Marcus Lang
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.)
Linde GmbH
Original Assignee
Linde GmbH
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 Linde GmbH filed Critical Linde GmbH
Priority to EP19020246.5A priority Critical patent/EP3719433A1/fr
Priority to CN202010160537.XA priority patent/CN111795590B/zh
Priority to RU2020111039A priority patent/RU2800696C2/ru
Priority to US16/834,029 priority patent/US11236945B2/en
Priority to EP20020143.2A priority patent/EP3719434B1/fr
Publication of EP3719433A1 publication Critical patent/EP3719433A1/fr
Priority to CY20221100037T priority patent/CY1124903T1/el
Withdrawn legal-status Critical Current

Links

Images

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
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02—Header boxes; End plates
    • F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00—Heat-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 flows in a continuous film, or trickles freely, over the conduits
    • F28D3/04—Distributing arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J5/00—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
    • F25J5/002—Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00—Heat-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 flows in a continuous film, or trickles freely, over the conduits
    • F28D3/02—Heat-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 flows in a continuous film, or trickles freely, over the conduits with 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
    • F28F25/00—Component parts of trickle coolers
    • F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
    • F28F27/02—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus for controlling the distribution of heat-exchange media between different channels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2280/00—Control of the process or apparatus
    • F25J2280/02—Control in general, load changes, different modes ("runs"), measurements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/32—Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0033—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for cryogenic applications
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0061—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
    • F28D2021/0064—Vaporizers, e.g. evaporators

Definitions

  • the invention relates to a heat exchanger and a method for operating such a heat exchanger.
  • Coiled heat exchangers are e.g. used in natural gas liquefaction plants.
  • a first fluid medium is applied as a refrigerant to the shell side and evaporates by means of a falling film. This evaporation can lead to a so-called maldistribution over the tube bundle, so that some tubes receive too much refrigerant, other tubes too little.
  • the tube side i.e. the media carried in the tube bundle
  • the first medium or the refrigerant on the shell side can also be regulated in order to compensate for a maldistribution.
  • valves arranged in the jacket space or on the tube bundle, as well as moving parts inside the heat exchanger can only be implemented with comparatively great effort.
  • the present invention is therefore based on the object of specifying a heat exchanger and a corresponding method for indirect heat transfer, which enables a particularly continuous shift of the area-related task of the first medium in a radial direction of the tube bundle and so low the cost of additional instrumentation as possible.
  • the distribution arms for applying the tube bundle with the liquid phase of the first medium have at least one first container and at least one second container separate from the first container, the first container being in flow connection with the annular channel so that the liquid phase of the first medium can be introduced from the annular channel into the at least one first container and can be distributed from there via outlet openings of the first container to a first region of the tube bundle, and the at least one second container is in flow connection with the collecting container, so that the liquid phase of the first medium can be introduced from the collecting container into the at least one second container and can be distributed from there to a second region of the tube bundle via outlet openings of the second container.
  • the distribution arms can each be designed in the shape of a sector of a circle. Furthermore, between two adjacent distribution arms in the circumferential direction of the jacket or the core tube can be separated by a gap through which the tubes of the tube bundle can be passed (e.g. towards the connection pieces provided on the jacket).
  • the heat exchanger has at least one first controllable valve, via which the ring channel can be charged with the first medium, and / or that the heat exchanger has at least one second controllable valve via which the collecting container of the core tube with the first medium can be loaded.
  • the ring channel is in flow connection with a first inlet arranged on the jacket, so that the first medium can be introduced into the ring channel via the first inlet, the first valve in particular being arranged upstream of the first inlet.
  • the collecting container of the core tube is in flow connection with a second inlet arranged on the jacket, so that the first medium can be introduced into the collecting container via the second inlet, the second valve in particular being arranged upstream of the second inlet.
  • the first container and the second container can be charged simultaneously with variable mass flows of the first medium by appropriately setting the valves.
  • the first container and the second container are arranged above the tube bundle that by setting the two valves the amount of liquid phase applied to the tube bundle per area and time in a radial direction of the Tube bundle is changeable or adjustable.
  • one embodiment of the invention provides that the arrangement of the outlet openings of the first and the second container is designed so that radially different amounts of liquid can be adjusted.
  • the second container can have outlet openings which are located further inward in the radial direction than the outlet openings of the first container.
  • the second container only have outlet openings for an inner half of the tube bundle, while the first container only has outlet openings for the outer half of the tube bundle.
  • the said amount can be changed or adjusted in the radial direction of the tube bundle so that the said amount increases monotonically towards the outside in a radial direction of the tube bundle or outwards decreases monotonously.
  • one embodiment of the invention provides that the at least one first container is formed by a first distribution arm of the liquid distributor, and that the at least one second container is formed by a second distribution arm of the liquid distributor.
  • the at least one first container is formed by a first area of a distribution arm
  • the at least one second container is formed by a second area of the distribution arm that is separate from the first area
  • the two regions run next to one another in the radial direction along which the distributor arm extends.
  • the two areas are fluidically separated from one another by a partition wall of the distributor arm that extends in the radial direction.
  • the two areas are opposite one another in the radial direction along which the distributor arm extends.
  • it can furthermore be provided according to one embodiment that the two areas are separated from one another by a partition wall extending in a circumferential direction of the core tube.
  • Another aspect of the present invention relates to a method for performing an indirect heat transfer between at least a first fluid medium and a second fluid medium using a heat exchanger according to the invention, wherein the second medium is introduced into the tube bundle, and wherein a first mass flow of the first medium over the ring channel is introduced into the at least one first container, and wherein (in particular at the same time) a second mass flow of the first medium is introduced into the at least one second container via the collecting container, the two mass flows being set (e.g. using the said valves), in order to change the amount of the liquid phase of the first medium applied to the tube bundle per area and time via the outlet openings of the at least one first container and the outlet openings of the at least one second container in the radial direction of the tube bundle put.
  • the two mass flows of the first medium are set such that the said amount of the liquid phase of the first medium increases monotonically towards the outside in a radial direction of the tube bundle or decreases monotonously towards the outside.
  • the Figure 1 shows in connection with the Figure 2 an embodiment of a heat exchanger 1 according to the invention, which makes it possible to counteract a maldistribution of a first medium M (eg a refrigerant) guided in a jacket space 3 onto a tube bundle 5 of the heat exchanger 1.
  • a first medium M eg a refrigerant
  • the heat exchanger 1 has in detail a jacket 2 which surrounds the jacket space 3, a core tube 4 which extends in the jacket space 3 and on which the tubes 50 of the tube bundle 5 are wound, the tube bundle 5 for receiving at least one fluid second medium M ' is designed so that heat can be transferred indirectly between the first medium M and the at least one second medium M '.
  • the core tube 4 serves in particular as the core or carrier of the tube bundle, the individual tubes 50 being wound onto the horizontally arranged core tube 4 with spacers in between.
  • the core tube 4 extends along the vertical and preferably carries at least part of the load on the tubes 50 of the tube bundle 5.
  • the individual tubes 50 are preferably wound on or around the core tube 4, at least in sections, in a helical manner.
  • Such a heat exchanger is therefore also referred to as a wound heat exchanger 1.
  • the heat exchanger 1 has a - in relation to the vertical or longitudinal axis z of the core tube 4 - arranged above the tube bundle 5 in the jacket space 3 liquid distributor 6 for subjecting the tube bundle 5 with a liquid phase F of the first medium M
  • the liquid distributor 6 from Core tube 3 has distribution arms 60 protruding in the radial direction R, which can be configured in the shape of a sector of a circle, for example in the plan view along the longitudinal axis z (see also FIG Figures 2 to 4 ).
  • the distributor arms 60 each have a base 60g and side walls 60d extending from the respective base 60g, which, starting from the core tube 4, extend outward to the annular channel 61.
  • the liquid distributor 6 preferably has an annular channel 61 extending or encircling above the distributing arms 60 in a circumferential direction U of the casing 2 and also a collecting container 62 formed by the core tube 4, the annular channel 61 and the collecting container 62 each for collecting the first medium M, which is in particular a two-phase mixture, are formed.
  • the first medium M can be calmed and degassed in the collecting container 62 and in the annular channel 61 or later in the containers 60a, 60b or areas 60a, 60b, so that ultimately a liquid phase F of the first medium or refrigerant M via the distribution arms 60 can be distributed over the tube bundle 5.
  • the distribution arms 60 form at least one first container 60a and at least one second container 60b separate from the first container 60a, the at least one first container 60a being in flow connection with the annular channel 61 so that the liquid phase F des first medium M can be introduced from the annular channel 61 into the at least one first container 60a and from there can be distributed via outlet openings 600 of a bottom 60g of the at least one first container 60a to a first area 5a of the tube bundle 5, and the at least one second container 60b is in flow connection with the collecting container 62 so that the liquid phase F of the first medium M can be introduced from the collecting container 62 into the at least one second container 60b and from there via outlet openings 601 of a bottom 60g of the at least one second container 60b to a second area 5b of the tube bundle 5 is distributable.
  • the liquid distributor 6 has several (here for example four) distribution arms 60, two distribution arms 60 opposite one another in the radial direction R each forming a first container 60a, which is fluidically separated from the collecting container 62 or from the core tube 4 (for example through a wall section 60f of the core tube 4) and is fed with the liquid phase F of the first medium M only from the outside via the ring channel 61, for example through an opening 61a of an inner wall 61c of the ring channel 61 Figure 2
  • the inner wall 61c lies opposite an outer circumferential wall 61b of the annular channel 61, both walls extending from a base 61d of the annular channel 61.
  • the ring channel 61 can also be attached to the jacket 2 so that, for example, the outer wall 61b can be formed by the jacket 2.
  • two further distribution arms 60 opposite one another in the radial direction R each form a second container 60b, the respective second container 60b, in contrast to the respective first container 60a, being fluidically separated from the annular channel 61 (e.g. by a section 60e of the inner wall 61c of the annular channel 61) and is only fed with the liquid phase of the F of the first medium M from the inside via the collecting container 62 or the core tube 4.
  • a wall of the core tube 4 can each have a corresponding opening 4a.
  • the containers 60a, 60b are each assigned to an area 5a or 5b of the upper side of the tube bundle 5 (cf. Fig. 1 ), so that the distribution of the liquid phase F on the tube bundle 5 can be influenced by different liquid delivery to the areas 5a, 5b.
  • the first and second containers 60a, 60b allow different liquid levels and thus also different volume flows.
  • the arrangement of the outlet openings 600, 601 of the first and second containers 60a, 60b can be designed such that radially different amounts of liquid can be set.
  • the second containers 60b connected to the core tube 4 can have outlet openings 601 which are located further inward in the radial direction R than the outlet openings 600 of the first container 60a.
  • the second containers 60b only have outlet openings 601 for an inner half of the tube bundle 5 and the first containers 60a connected to the annular channel 61 can only have outlet openings 600 for the outer half of the tube bundle 5.
  • the outlet openings 600, 601 can here also be varied in size or an overlap of the outlet openings 600 of the first container 60a with the outlet openings 601 of the second container 60b with respect to the radial direction can be provided.
  • the ring channel 61 can be charged with the first medium M via a first valve 7 and via the subsequent first inlet or connector 9, so that a corresponding mass flow of the first medium M into the ring channel 61 and the first Container or distribution arms 60a can be regulated accordingly.
  • the collecting container 62 can be charged with the first medium M via a second valve 8 and via the subsequent second inlet or connection 10, which is provided centrally above the collecting container 62 on the jacket 2, so that a corresponding mass flow of the first medium M in the collecting container 62 or the second container or distribution arms 60b can also be regulated accordingly.
  • the amount of liquid phase F that is applied along the radial direction R of the tube bundle 5 to the tube bundle 5 or the areas 5a, 5b can be varied in order to counteract a maldistribution of the liquid phase F in the jacket space 3.
  • the distribution arms 60 are therefore fed from the outside via the annular channel 61 (first container 60a) or from the inside via the collecting container 62 provided in the core tube 4 (second container 60b) in order to vary the liquid discharge to the tube bundle 5 in the radial direction R if necessary . to adjust.
  • Figure 3 shows an alternative embodiment of the liquid distributor 6, wherein the at least one first container 60a is formed by a first area 60a of a distribution arm 60, and wherein the at least one second container 60b is formed by a second area 60b of the same distribution arm 60 which is fluidically separated from the first area 60a is.
  • the two areas 60a, 60b in the radial direction R, along which the distribution arm 60 extends, run next to one another from the core tube 4 to the jacket 2, the two areas 60a, 60b preferably extending through one in the radial direction R.
  • Partition 60c of the distributor arm 60 are fluidically separated from one another.
  • the first area 60a is again supplied with the liquid phase F of the first medium M from the outside via the ring channel 61, in particular via an opening 61a in the inner wall 61c of the ring channel 61 Wall section 60f of core tube 4 is fluidically separated from core tube 4 or collecting container 62.
  • the at least one second region 60b is supplied with the liquid phase F of the first medium M from the collecting container 62 via an opening 4a of the core tube 4 and is e.g. Fluidically separated from the annular channel 61 by a section 60e of the inner wall 61c of the annular channel 61.
  • annular channel 61 is variably supplied with the liquid phase F via the first valve 7
  • the collecting container 62 is variably supplied with the liquid phase F of the first medium M via the second valve 8.
  • the valves 7, 8 By appropriately setting the valves 7, 8 or regulating the two mass flows of the first medium M in the annular channel 61 or in the collecting container, the amount of liquid phase F, which along the radial direction R of the tube bundle 5 on the tube bundle 5 or The areas 5a, 5b given up are varied in order to counteract a maldistribution of the liquid phase F in the jacket space 3.
  • the outlet openings 600, 601 of the first and second containers 60a, 60b are designed such that radially different amounts of liquid can be set.
  • the second containers 60b connected to the core tube 4 can have outlet openings 601 which are located further inward in the radial direction R than the outlet openings 600 of the first container 60a.
  • the second containers 60b only have outlet openings 601 for an inner half of the tube bundle 5 and the first containers 60a connected to the annular channel 61 can only have outlet openings 600 for the outer half of the tube bundle 5 (see above).
  • Fig. 4 shows a further variant of a heat exchanger 1 according to the invention, the at least one first and the at least one second area 60a, 60b again being formed by a distributor arm, in which case, in contrast to FIG Figure 3 the partition wall 60c, which separates the two areas 60a, 60b from one another in terms of flow, extends in the circumferential direction U of the jacket 2 or of the core tube 4, so that the two areas 60a, 60c extend in the radial direction R, along which the distribution arm extends from the core tube to the jacket 2, are opposite one another.
  • the first area is supplied with the liquid phase F via an opening 61a in the inner wall 61c of the annular channel
  • the second area 60b is supplied with the liquid phase F from the collecting container 62 via an opening 4a in the core tube 4.
  • the outlet openings 600 of the first container 60a lie further outside in the radial direction R than the outlet openings 601 of the second container 60b.
  • the ring channel 61 is according to FIG Figure 4 variably supplied with the liquid phase F via the first valve 7, whereas the collecting container 62 is variably supplied with the liquid phase F of the first medium M via the second valve 8.
  • the amount of liquid phase F that is flowing along the radial direction R of the tube bundle 5 onto the tube bundle 5 or the areas 5a, 5b abandoned are varied in order to counteract a maldistribution of the liquid phase F in the shell space 3. If e.g. If the mass flow of the first medium M in the collecting container 62 is increased or decreased in the annular channel 61, more liquid F is applied to the tube bundle 5 via the inner second areas 60b than via the outer first areas 60a.
  • liquid distributor according to the invention it is possible to react optimally to any influence on the part of the process and to counteract a maldistribution on the shell side, so that the overall performance of the heat exchanger is improved.
  • the two areas 60a, 60b can also be implemented via a divided ring channel 61 (e.g. two semicircular ring channels or two concentric ring channels) or a divided core tube 4 (e.g. concentric core tube plugged into one another or core tube divided in diameter).
  • the distribution arms 60 can also have any other spatial separation.
  • more than two valves or containers can be used to adjust the liquid distribution in the radial direction of the tube bundle.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
EP19020246.5A 2019-04-02 2019-04-02 Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide Withdrawn EP3719433A1 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP19020246.5A EP3719433A1 (fr) 2019-04-02 2019-04-02 Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide
CN202010160537.XA CN111795590B (zh) 2019-04-02 2020-03-09 用于实现不同液体装载的盘管式换热器的可控液体分配器
RU2020111039A RU2800696C2 (ru) 2019-04-02 2020-03-17 Управляемый распределитель жидкости змеевикового трубчатого теплообменника для реализации различных жидкостных нагрузок
US16/834,029 US11236945B2 (en) 2019-04-02 2020-03-30 Controllable liquid distributor of a coiled-tube heat exchanger for realizing different liquid loadings
EP20020143.2A EP3719434B1 (fr) 2019-04-02 2020-03-31 Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide
CY20221100037T CY1124903T1 (el) 2019-04-02 2022-01-14 Ρυθμιζομενος διανομεας υγρου ενος σπειροειδους εναλλακτη θερμοτητας για την εφαρμογη διαφορετικων φορτιων υγρου

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP19020246.5A EP3719433A1 (fr) 2019-04-02 2019-04-02 Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide

Publications (1)

Publication Number Publication Date
EP3719433A1 true EP3719433A1 (fr) 2020-10-07

Family

ID=66091838

Family Applications (2)

Application Number Title Priority Date Filing Date
EP19020246.5A Withdrawn EP3719433A1 (fr) 2019-04-02 2019-04-02 Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide
EP20020143.2A Active EP3719434B1 (fr) 2019-04-02 2020-03-31 Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP20020143.2A Active EP3719434B1 (fr) 2019-04-02 2020-03-31 Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide

Country Status (3)

Country Link
US (1) US11236945B2 (fr)
EP (2) EP3719433A1 (fr)
CY (1) CY1124903T1 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116379520A (zh) * 2023-05-09 2023-07-04 北京纵力能源科技服务有限公司 一种中央空调冷却系统水量均衡器

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2511642A2 (fr) * 2011-04-14 2012-10-17 Linde Aktiengesellschaft Echangeur thermique doté d'un réglage de liquide supplémentaire dans l'espace d'enveloppe
DE102012016500A1 (de) * 2012-08-21 2013-08-22 Linde Aktiengesellschaft Wärmeübertrager und Verfahren zum Verteilen einer flüssigen Phase auf ein Rohrbündel eines Wärmeübertragers
EP3367033A1 (fr) * 2017-02-24 2018-08-29 Linde Aktiengesellschaft Échangeur thermique et procédé de distribution d'une phase liquide dans un échangeur thermique
EP3367034A1 (fr) * 2017-02-24 2018-08-29 Linde Aktiengesellschaft Échangeur thermique et procédé de distribution d'une phase liquide dans un échangeur thermique

Family Cites Families (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2737789A (en) * 1954-02-05 1956-03-13 Alonzo W Ruff Evaporative refrigerant condenser
US3256932A (en) * 1963-01-03 1966-06-21 Babcock & Wilcox Co Heat exchanger tube arrangement
US3395676A (en) * 1966-07-05 1968-08-06 Babcock & Wilcox Co Vapor generator
US3666423A (en) * 1969-11-26 1972-05-30 Texaco Inc Heat exchange apparatus
SE400119B (sv) * 1974-09-02 1978-03-13 Munters Ab Carl Sett att forhindra dimbildning vid evaporativa kylare, och anordning for genomforande av settet
DE2534442A1 (de) * 1975-08-01 1977-02-10 Linde Ag Waermeaustauscher in spiralblechbauart
US4201262A (en) * 1978-08-07 1980-05-06 Goldstein Stanley A Cooler for chilling a working fluid
NL8002172A (nl) * 1980-04-15 1981-11-16 Shell Int Research Reactor voor exotherme reacties.
CH658198A5 (de) * 1983-01-04 1986-10-31 Sulzer Ag Fluessigkeitsverteiler in einer stoff- und waermeaustauschkolonne.
CH660308A5 (de) * 1983-03-01 1987-04-15 Sulzer Ag Vorrichtung zur fluessigkeitsverteilung in einer stoff- und waermeaustauschkolonne.
US5181537A (en) * 1989-12-12 1993-01-26 Conoco Inc. Outlet collectors that are rate insensitive
DE4301712A1 (de) * 1993-01-22 1994-07-28 Linde Ag Anlage und Verfahren zur Tieftemperaturzerlegung von Luft und Flüssigkeitsverteiler für eine Stoffaustauschsäule
CA2206847C (fr) * 1994-12-14 2005-06-28 Shuzo Nomura Echangeur de chaleur
US20050077029A1 (en) * 2002-10-03 2005-04-14 Jose Morales Cervantes Heat exchanger for fermentation tank
DE102004040974A1 (de) * 2004-08-24 2006-03-02 Linde Ag Gewickelter Wärmetauscher
DE102007019816A1 (de) * 2007-04-26 2008-10-30 Linde Ag Sammler-Verteiler-Kombination
DE102010056023A1 (de) * 2010-12-23 2012-06-28 Linde Aktiengesellschaft Kolonne
DE102011017030A1 (de) * 2011-04-14 2012-10-18 Linde Ag Wärmetauscher mit Kernrohr und Ringkanal
AU2012201620B2 (en) * 2011-04-14 2015-04-30 Linde Aktiengesellschaft Heat exchanger with sections
DE102011117588A1 (de) * 2011-11-03 2013-05-08 Linde Aktiengesellschaft Einrichtung zur Herstellung eines Phasenkontaktes zwischen einer flüssigen und einer gasförmigen Phase, insbesondere Stoffaustauschkolonne
US9766024B2 (en) * 2012-10-09 2017-09-19 Linde Aktiengesellschaft Method for controlling a temperature distribution in a heat exchanger
EP2818821B1 (fr) * 2013-06-27 2016-02-03 Linde Aktiengesellschaft Echangeur de chaleur enroulé avec alimentation par tuyau central
US20160209118A1 (en) * 2015-01-16 2016-07-21 Air Products And Chemicals, Inc. Shell-Side Fluid Distribution in Coil Wound Heat Exchangers
EP3430338B1 (fr) * 2016-03-16 2019-12-18 Linde Aktiengesellschaft Dispositif de separation pour un fluide caloporteur enroule destine a separer une phase gazeuse d'une phase liquide d'un milieu a deux phases achemine cote enveloppe
EP3428563A1 (fr) * 2017-07-10 2019-01-16 Linde Aktiengesellschaft Soutirage/injection de gaz destiné à influencer la migration radiale de liquide
EP3447425A1 (fr) * 2017-08-22 2019-02-27 Linde Aktiengesellschaft Aménagements dans un échangeur de chaleur enroulé permettant la réduction d'écoulement turbulent de gaz

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2511642A2 (fr) * 2011-04-14 2012-10-17 Linde Aktiengesellschaft Echangeur thermique doté d'un réglage de liquide supplémentaire dans l'espace d'enveloppe
DE102012016500A1 (de) * 2012-08-21 2013-08-22 Linde Aktiengesellschaft Wärmeübertrager und Verfahren zum Verteilen einer flüssigen Phase auf ein Rohrbündel eines Wärmeübertragers
EP3367033A1 (fr) * 2017-02-24 2018-08-29 Linde Aktiengesellschaft Échangeur thermique et procédé de distribution d'une phase liquide dans un échangeur thermique
EP3367034A1 (fr) * 2017-02-24 2018-08-29 Linde Aktiengesellschaft Échangeur thermique et procédé de distribution d'une phase liquide dans un échangeur thermique

Also Published As

Publication number Publication date
EP3719434B1 (fr) 2021-12-15
RU2020111039A (ru) 2021-09-17
CY1124903T1 (el) 2023-01-05
US11236945B2 (en) 2022-02-01
EP3719434A1 (fr) 2020-10-07
US20200318912A1 (en) 2020-10-08
CN111795590A (zh) 2020-10-20

Similar Documents

Publication Publication Date Title
DE102005001952A1 (de) Rohrbündelreaktor zur Durchführung exothermer oder endothermer Gasphasenreaktionen
EP2511642A2 (fr) Echangeur thermique doté d'un réglage de liquide supplémentaire dans l'espace d'enveloppe
EP3719434B1 (fr) Distributeur de fluide réglable d'un échangeur de chaleur enroulé permettant de réaliser des différentes charges de fluide
EP3128278B1 (fr) Amenee et extraction d'ecoulements tubulaires par temperature intermediaire pour des echangeurs de chaleur a bobines
WO2014135672A1 (fr) Colonne servant à mettre en œuvre des processus de transfert de matière sous forme gazeuse/liquide
WO2017167458A1 (fr) Echangeur de chaleur à spirales
EP0027984A2 (fr) Réacteur à eau bouillante
DE10051523A1 (de) Vorrichtung zur Verteilung einer Flüssigkeit in einer Gegenstrom-Kolonne
WO2016131787A1 (fr) Échangeur de chaleur à faisceau tubulaire muni d'éléments de faisceau tubulaire agencés séquentiellement
EP3367033A1 (fr) Échangeur thermique et procédé de distribution d'une phase liquide dans un échangeur thermique
DE102013202790A1 (de) Wärmeübertrager
EP3600588B1 (fr) Fond pour une colonne d'échange de matière
DE1117804B (de) Vorrichtung zur kontinuierlichen Desodorisation und destillativen Neutralisation von OElen und Fetten
WO2020207626A1 (fr) Conception d'entretoise et ensemble formant entretoise servant à réduire une répartition erronée radiale dans un échangeur de chaleur enroulé
DE2609571C2 (de) Abblaseeinrichtung zur Überdruckbegrenzung bei Kernkraftwerken, insbesondere bei Siedewasser-Kernkraftwerken
DE102016103719B4 (de) Vorrichtung zur Fluidführung
EP0481573A1 (fr) Dispositif pour réduction de pression d'un média à gaz
EP0408836B1 (fr) Appareil pour constituer un milieu conditionné dans des conteneurs
DE2752486A1 (de) Einlaufverteiler fuer ein anschwemm- kesselfilter
DE102017208319A1 (de) Radialstromeinsatzvorrichtung zum Vorgeben wenigstens eines radialen Strömungspfades in einem Schüttungsreaktor sowie Montageverfahren und Verwendung
DE102012005569A1 (de) Wärmetauscher mit Sektionen
DE102012002526A1 (de) Flüssigkeitsverteiler
DE4444891C2 (de) Verfahren und Vorrichtung zum Betreiben einer Rektifikation in stark variierenden Lastbereichen
WO2020007503A1 (fr) Stabilisation de faisceau de tubes pour échangeurs de chaleur enroulés
DE850503C (de) Verfahren zum Betrieb von Verdichtern mit mindestens einem einer Stufe nachgeschalteten Kuehler und Verdichter zum Ausueben dieses Verfahrens

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN PUBLISHED

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20210408