EP0627607B1 - Echangeur de chaleur chauffé par la vapeur - Google Patents

Echangeur de chaleur chauffé par la vapeur Download PDF

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Publication number
EP0627607B1
EP0627607B1 EP94105670A EP94105670A EP0627607B1 EP 0627607 B1 EP0627607 B1 EP 0627607B1 EP 94105670 A EP94105670 A EP 94105670A EP 94105670 A EP94105670 A EP 94105670A EP 0627607 B1 EP0627607 B1 EP 0627607B1
Authority
EP
European Patent Office
Prior art keywords
tubes
heating
feed
conduit
heat exchanger
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP94105670A
Other languages
German (de)
English (en)
Other versions
EP0627607A3 (fr
EP0627607A2 (fr
Inventor
Ulrich Alfred Martin
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.)
Wieland Werke AG
Original Assignee
Wieland Werke 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 Wieland Werke AG filed Critical Wieland Werke AG
Publication of EP0627607A2 publication Critical patent/EP0627607A2/fr
Publication of EP0627607A3 publication Critical patent/EP0627607A3/fr
Application granted granted Critical
Publication of EP0627607B1 publication Critical patent/EP0627607B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • F28D7/02Heat-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
    • F28D7/024Heat-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

Definitions

  • the invention relates to a steam-heated Heat exchanger, especially for the condensate side Regulation of heat transfer, with a one steam-heated heating system, by one secondary Heating medium flows through the housing, the upstream lying end to a return and downstream End of a flow for the secondary heating medium is connectable, and with heating steam in parallel and in Flow through countercurrent to the secondary heating medium Heating pipes connected to one at the upstream end Steam flow and at the downstream end to one Condensate return are connected, the housing from a series of parallel from the secondary heating medium flowed through jacket tubes, in each of which one of the Heating pipes is arranged, the flow side through a Jacket pipes common secondary flow line for the secondary heating medium and its wall through are led outside to the common steam flow.
  • the jacket pipes have a first Embodiment radially from its end protruding pipe socket through which the secondary Heating medium can flow into or out of the jacket tube.
  • the front sides of the casing pipes are on the flow side fluid-tight against the steam supply line sealed.
  • the Pipe socket expanded to connecting flanges, which at mutually coupled jacket tubes one with these form an integral secondary flow line.
  • the Flanges are again at a distance from the end of the Jacket pipes arranged.
  • the jacket pipes are on the front also fluid-tight in this embodiment sealed and the outflow of the secondary heating medium takes place in the radial direction.
  • a cooling of the primary Heating medium through the secondary heating medium takes place only if the primary heating medium in the heating pipe is at a distance areas from the end of the casing tube reached be washed by the secondary heating medium.
  • the heating pipes are all in one housing arranged and with their ends on two tube plates connected, of which the flow tube in the upper housing part arranged laterally in the housing wall is, while the condensate-side tube plate is the housing closes at the bottom and from a condensate collector separates.
  • the heating pipes are helically coiled, the slope of the turns from top to bottom so that the heat-exchanging surface towards Steam entry to the condensate outlet increases accordingly.
  • Such heat exchangers have become common in practice proven; the heat exchanger is easy to control and there are none at all steam pressures Sounds. However, the manufacture of one Heat exchanger very complex and expensive.
  • the advantage achieved by the invention initially exists in that the heating pipes are led through the flow line are because it ensures that the heating pipes on Steam enters through the jacket pipes and the Secondary heating medium flowing through the flow line very much to be cooled well and heat pockets from the current of the secondary heating medium is not detected and flushed through, cannot arise. This ensures that in Heat exchanger no bubbling, crackling or cracking noises can result from overheating on the secondary side.
  • the heating pipes in the area the mouth of the casing tube in the secondary Flow line and within the secondary flow line themselves have the smallest possible heat exchange surface, in particular are smooth-walled. You therefore give in this Area less heat and this heat can be from which the Secondary heating medium flowing through the flow line can be easily removed.
  • the narrowed mouth area of the casing tube from a short axial connecting piece formed by the casing tube merges with an outwardly convex shell.
  • the arrangement be such that parallel to the secondary flow line on their of the Jacket side facing away from a steam flow line to which the runs across the secondary Flow pipe connected through heating pipes connected are.
  • the heat exchanging surface of the in the Flow pipe trending heating pipe sections is then optimally small and the heat given off to the secondary Heating medium in the flow pipe correspondingly low.
  • the structure of the invention Heat exchanger has the further advantage that the secondary Flow and return line just like that Steam supply line and the condensate manifold either with one of their two or with theirs both ends of the line to the flow and return for the secondary heating medium or to the common steam flow and the common condensate return can be connected.
  • the one with the secondary supply and return lines, the Steam supply line and the condensate manifold prefabricated and pre-assembled heat exchangers very versatile connection options to the primary-side energy supply system and that secondary-side energy consumer system.
  • FIG 1 shows a heat exchanger according to the invention in Longitudinal section, Figure 2 in plan view.
  • each casing tube 1 is at the upstream end 1 ′′ a return, not shown, and downstream not lying end 1 'to yourself shown advance of the secondary Energy consumer system for the secondary heating medium in way to be described further below connected.
  • Heating pipe 2 for passing the heating steam or Condensate, with all heating pipes 2 from heating steam in parallel and flows in countercurrent to the secondary heating medium will.
  • the heating pipes 2 are at the upstream end 2 '' to a steam supply, which is itself not shown and at the downstream end 2 'to a likewise in the Drawing not shown condensate return primary power supply system connected.
  • the jacket tubes 1 are in the region of their mouth 4 in the secondary flow line 3 narrowed in cross section, wherein this narrowed mouth area in detail by one short axial connector 7 and in the transition from this connecting piece 7 to the cylindrical part of the Jacket tube 1 from an outwardly convex Shell section 8 formed.
  • This narrowing leads to an increase in the flow rate of the secondary Heating medium and thus for a good cooling of the Mouth area and the cross section of the flow line 3 penetrating sections 6 of the heating tubes 2.
  • the heating tubes 2 are then in their Mouth area of the jacket tubes 1 straight and smooth-walled section 6 helical coiled, with the outer coil diameter equal to that Inner diameter of the casing tube 1.
  • a displacer 9 which is designed in the exemplary embodiment as a tube that on return-side end 1 '' of the casing tube 1 on the end face closed, at the flow end 1 'but at the front is open and that prevents the flow of the secondary heating medium through the otherwise free interior the coiled tubing takes place.
  • they are Heating pipes 2 in the coiled area with finned pipes closely coiled tube coils.
  • the casing tubes 1 are through one side piece 10 attached to one next to each Jacket tubes 1 running common secondary Return line 11 for the secondary heating medium connected.
  • this return line 11 takes place Connection of all jacket pipes 1 to the common return of the cooled secondary heating medium from the secondary Energy consumer system, this connection optional at one of the two ends of the return line 11 or both ends of the line can be done. Also the connection of the secondary lead of the energy consumer system takes place over the secondary pipes common to all jacket pipes Flow line 3, the connection in turn to one of the both ends of this flow line 3 or on both of them Ends can be made simultaneously.
  • the condensate ends 2 'of the heating tubes 2 are each axially through the end wall of its casing tube 1 passed through and with a common Condensate manifold 12 connected in detail not shown in the figure to the Condensate return from the primary energy supply system is to be connected.

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)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Claims (8)

  1. Echangeur de chaleur chauffé à la vapeur, notamment pour la régulation du transfert thermique côté condensats, avec un corps comportant un circuit de chauffage chauffé à la vapeur, traversé par un fluide de chauffage secondaire, qui est connecté à son extrémité amont à un retour et à son extrémité aval à une arrivée pour le fluide secondaire et avec des tubes de chauffage (2) parcourus par la vapeur de chauffage parallèlement et à contre-courant par rapport au fluide de chauffage secondaire, lesquels tubes de chauffage sont connectés à leur extrémité amont (2") à une arrivée de vapeur et à leur extrémité aval (2') à un retour des condensats, le corps étant formé d'une série de tubes-enveloppes (1) parcourus en parallèle par le fluide de chauffage secondaire, dans chacun desquels est disposé un des tubes de chauffage (2) qui, côté arrivée, est connecté extérieurement à l'arrivée de vapeur commune, à travers une conduite d'arrivée secondaire (3) secondaire pour le liquide de chauffage secondaire commune aux tubes enveloppes (1) et à travers la paroi de ladite conduite, caractérisé par le fait que les tubes-enveloppes (1) débouchent avec leur extrémité de tube (1') côté arrivée, ouverte au niveau de sa face frontale, dans la conduite d'arrivée (3) secondaire, par le fait que les tubes de chauffage (1), côté arrivée, communiquent à travers l'embouchure (4) formée côté face frontale du tube-enveloppe (1) concerné avec la conduite d'arrivée (3) secondaire et que les tubes-enveloppes (1), dans la région de leur embouchure (4) dans la conduite d'arrivée (3) secondaire présentent une section transversale rétrécie.
  2. Echangeur de chaleur selon la revendication 1, caractérisé par le fait que les tubes de chauffage (2), dans la région de l'embouchure (4) du tube-enveloppe (1) dans la conduite d'arrivée secondaire (3) et à l'intérieur de la conduite d'arrivée secondaire (3) elle-même, présentent une surface d'échange thermique aussi réduite que possible, notamment présentent des parois lisses.
  3. Echangeur de chaleur selon la revendication 1 ou 2, caractérisé par le fait que la région d'embouchure rétrécie du tube-enveloppe (1) est formée par un court tronçon de liaison (7) axial auquel le tube-enveloppe (1) se raccorde par un tronçon en forme de coque (8) bombé convexe en direction de l'extérieur.
  4. Echangeur de chaleur selon une des revendications 1 à 3, caractérisé par le fait qu'une conduite d'arrivée de vapeur (5) est disposé parallèlement à la conduite d'arrivée secondaire (3), du côté de celle-ci éloigné des tubes-enveloppes (1), conduite à laquelle sont connectés les tubes de chauffage (2) qui traversent la conduite d'arrivée secondaire (3).
  5. Echangeur de chaleur selon une des revendications 1 à 4, caractérisé par le fait que dans le tube-enveloppe (1), à distance de l'embouchure (4) des tubes-enveloppes dans la conduite d'arrivée secondaire (3), les tubes de chauffage (2) sont enroulés en hélice, le diamètre d'enroulement extérieur étant égal au diamètre intérieur du tube-enveloppe (1), un élément formant barrage (9) étant disposé dans l'espace intérieur de l'hélice.
  6. Echangeur de chaleur selon la revendication 5, caractérisé par le fait que les tubes de chauffage (2), dans la région enroulée en hélice sont conformés en tubes à ailettes à spires jointives.
  7. Echangeur de chaleur selon une des revendications 1 à 6, caractérisé par le fait que les tubes-enveloppes (1), à leur extrémité amont (1"), sont connectés chacun par un tronçon (10) latéral à une conduite de retour (11) commune pour le fluide de chauffage secondaire, qui s'étend à côté des tubes-enveloppes (1) et par le fait que les extrémités côté condensat (2') des tubes de chauffage (2) traversent axialement la paroi frontale de leur tube-enveloppe (1) et sont connectées à un collecteur de condensats (12) commun.
  8. Echangeur de chaleur selon la revendication 7, caractérisé par le fait que les conduites d'arrivée et de retour secondaires (3, 11) ainsi que la conduite d'arrivée de vapeur (5) et le collecteur de condensats (12) peuvent être connectés de manière sélective par l'une de leurs deux extrémités ou par leurs deux extrémités à l'arrivée et au retour pour le fluide de chauffage secondaire et à l'arrivée de vapeur commune et au retour de condensats commun.
EP94105670A 1993-06-02 1994-04-13 Echangeur de chaleur chauffé par la vapeur Expired - Lifetime EP0627607B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4318240A DE4318240C2 (de) 1993-06-02 1993-06-02 Dampfbeheizter Wärmeübertrager
DE4318240 1993-06-02

Publications (3)

Publication Number Publication Date
EP0627607A2 EP0627607A2 (fr) 1994-12-07
EP0627607A3 EP0627607A3 (fr) 1996-03-20
EP0627607B1 true EP0627607B1 (fr) 1998-09-30

Family

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Application Number Title Priority Date Filing Date
EP94105670A Expired - Lifetime EP0627607B1 (fr) 1993-06-02 1994-04-13 Echangeur de chaleur chauffé par la vapeur

Country Status (4)

Country Link
EP (1) EP0627607B1 (fr)
AT (1) ATE171776T1 (fr)
DE (2) DE4318240C2 (fr)
DK (1) DK0627607T3 (fr)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10303570B4 (de) * 2003-01-30 2007-02-01 Helmut Bälz GmbH Wärmetauschereinrichtung zur Erzeugung von Warm- oder Heißwasser
CN107869925B (zh) * 2017-03-21 2019-01-18 山东大学 一种含有不凝气体的多管式稳流装置的管壳式换热器
CN107894178B (zh) * 2017-03-21 2019-02-12 山东大学 一种稳流装置间距变大的可凝结汽体的换热器
CN107869924B (zh) * 2017-03-21 2019-01-18 山东大学 一种汽相可冷凝的多管式稳流装置的管壳式换热器
CN107869926B (zh) * 2017-03-21 2019-01-18 山东大学 一种稳流装置尺寸逐渐变小的可凝结汽体换热器
CN107869927B (zh) * 2017-03-21 2019-01-18 山东大学 一种稳流装置长度变化的不可凝气体管式换热器
CN107966052B (zh) * 2017-04-21 2019-03-08 青岛金玉大商贸有限公司 一种长度变化的可冷凝的多孔式稳流装置换热器
CN107976094B (zh) * 2017-04-21 2019-04-02 青岛金玉大商贸有限公司 一种长度变化的不可凝气体多孔式稳流装置换热器
CN107966051B (zh) * 2017-04-21 2019-04-02 青岛金玉大商贸有限公司 一种间距变化的可冷凝的多孔式稳流装置换热器
CN107976093B (zh) * 2017-04-21 2019-03-29 青岛金玉大商贸有限公司 一种间距变化的不可凝气体多孔式稳流装置换热器
CN107966053B (zh) * 2017-04-21 2019-03-08 青岛金玉大商贸有限公司 一种可冷凝的多孔式稳流装置换热器
CN107966050B (zh) * 2017-04-21 2019-03-29 青岛金玉大商贸有限公司 一种含有不凝气体的多孔式稳流装置换热器
CN112022046B (zh) * 2019-06-04 2024-09-13 青岛海尔洗碗机有限公司 一种洗碗机套管换热装置及洗碗机

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE7733614U1 (fr) * 1900-01-01 Viessmann, Hans, 3559 Battenberg
DE1119883B (de) * 1955-08-12 1961-12-21 Helmut Baelz Ges Fuer Patentve Stehender dampfbeheizter Waermetauscher mit schraubenfoermig eng gewundenen Heizrohren
NL237150A (fr) * 1958-03-17
IT8223093U1 (it) * 1982-10-04 1984-04-04 Ferroli Ind Riscaldamento S P A Scambiatore di calore-gas in particolare per impianti di riscaldamento centralizzato con servizio di fornitura di acqua calda ad usi igienico-sanitari.
DE3310375A1 (de) * 1983-03-22 1984-09-27 Franz 7505 Ettlingen Gärtner Waermetauscher

Also Published As

Publication number Publication date
DE4318240C2 (de) 1998-05-20
EP0627607A3 (fr) 1996-03-20
ATE171776T1 (de) 1998-10-15
DE4318240A1 (de) 1994-12-08
DE59406993D1 (de) 1998-11-05
EP0627607A2 (fr) 1994-12-07
DK0627607T3 (da) 1999-02-08

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