EP0752088A1 - Tube echangeur de chaleur pour chaudiere de chauffage - Google Patents

Tube echangeur de chaleur pour chaudiere de chauffage

Info

Publication number
EP0752088A1
EP0752088A1 EP95913118A EP95913118A EP0752088A1 EP 0752088 A1 EP0752088 A1 EP 0752088A1 EP 95913118 A EP95913118 A EP 95913118A EP 95913118 A EP95913118 A EP 95913118A EP 0752088 A1 EP0752088 A1 EP 0752088A1
Authority
EP
European Patent Office
Prior art keywords
outer tube
shells
tube
ribs
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.)
Granted
Application number
EP95913118A
Other languages
German (de)
English (en)
Other versions
EP0752088B1 (fr
Inventor
Wolfgang Kunkel
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.)
Hoval Interliz AG
Original Assignee
Hoval Interliz 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 Hoval Interliz AG filed Critical Hoval Interliz AG
Publication of EP0752088A1 publication Critical patent/EP0752088A1/fr
Application granted granted Critical
Publication of EP0752088B1 publication Critical patent/EP0752088B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081—Heat exchange elements made from metals or metal alloys
    • F28F21/084—Heat exchange elements made from metals or metal alloys from aluminium or aluminium alloys
    • 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
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00—Details
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00—Details
    • F24H9/0005—Details for water heaters
    • F24H9/001—Guiding means
    • F24H9/0026—Guiding means in combustion gas channels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • 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
    • F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
    • F28F21/081—Heat exchange elements made from metals or metal alloys
    • F28F21/082—Heat exchange elements made from metals or metal alloys from steel or ferrous alloys
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2275/00—Fastening; Joining
    • F28F2275/14—Fastening; Joining by using form fitting connection, e.g. with tongue and groove

Definitions

  • the invention relates to a heat exchanger tube for boilers, in particular for gas condensing boilers, according to the preamble of claim 1.
  • condensing boilers In, which mainly occur in boilers operated with gas firing, the combustion gases are cooled until the exhaust gas moisture condenses, in order to To exploit the heat of condensation.
  • the prerequisite for this is that the boiler is operated with a boiler temperature that is lower than the dew point temperature of the combustion gases at the end of the combustion gas path through the boiler.
  • the aim is to take the combustion gases through the water-cooled heat exchanger tubes of the boiler in a way that is as short as possible to reduce the combustion gases from the high inlet temperature, which can be around 850 ° C.
  • heat exchanger tubes which consist of a cylindrical, smooth-walled outer tube made of steel which is acid-corrosion-resistant against the exhaust gas condensate and an aluminum insert which is inserted into the outer tube and has a star-shaped cross section.
  • the outer tube must be made of steel in order to be able to weld at its ends into tube sheets or tube plates which separate the boiler water space surrounding the heat exchanger tubes on the one hand from the combustion chamber and on the other hand from the flue gas collector of the boiler .
  • the composite pipe made of steel outer pipe and aluminum Professional Lei nsatz can be acted upon with high gas inlet temperatures, since aluminum has a larger expansion coefficient than steel, so that the profile insert at its contact points with the outer tube with an increasing pressure with the outer tube in increasing temperature remains in contact with heat.
  • the heat transfer from the star-shaped aluminum profile insert to the steel outer tube is determined and limited by the fact that the profile insert only fits the outer tube on the comb surfaces of the radial arms of the profile insert touched, then the cross-section i are relatively thin-walled, a sufficient clearance Q uer plinth.
  • the invention has for its object to provide a heat exchanger tube of the type mentioned at the outset which enables an even greater heat transfer capacity from the combustion gases to the boiler and can be easily manufactured and further processed when installed in a boiler.
  • This object is achieved by the invention in the form of the heat exchanger tube obtained as a composite tube made of steel outer tubes and aluminum alloy profiles with the characterizing features of claim 1.
  • the tubular-shaped profile insert of the heat exchanger tube according to the invention can, on the one hand, be formed with a very large inner surface that absorbs heat from the combustion gases, preferably with ribs arranged in a comb-like manner on the inside of the two half-shells, and is above all in comparison to the known Sternprofi len with a much larger outer surface on the inside of the water-cooled steel outer tube, whereby the heat transfer performance from the combustion gases to the boiler water is significantly increased.
  • the shortness of the heat exchanger tube leads to the further essential advantage that the condensing boiler overall can be made shorter and thus space-saving when the heat exchanger tube is arranged vertically lower or when the heat exchanger tube is arranged horizontally.
  • the tubular body-shaped profile insert is divided into two half-shells and due to the formation of each half-shell with its ribs as one-sided open Profile easy and inexpensive to manufacture. For the production by extrusion, no so-called flying cores are required in the drawing die, which is therefore cheap and durable.
  • a particular advantage for the pus processing of the heat exchanger tube according to the invention or for its installation in a boiler has been found to be that when the outer tube is welded into a tube plate, thanks to the extremely large heat transfer contact surface and wr eable ability of Prof lmbies no destruction of the aluminum profile insert occurs when psychiatrist the end of the pro l ⁇ insert flush up to the tube plate in the ⁇ zoom ranges welded end of the outer tube.
  • the heat exchanger tube ⁇ therefore does not have with respect to the outer pipe ends bac staggered professional lmonenden herge ⁇ is to be, but can be used for installation in a boiler with a simple straight cut in the required length of manufactured long meter be separated.
  • the heat exchanger tube can be produced in a simple manner in such a way that the tube body has an outer diameter which is essentially corresponds to the inner diameter of the outer tube and is only so slightly smaller that the tube body can be easily pushed into the outer tube, and that the outer tube is then shaped by a permanent compression of the entire outer tube circumference, for example by a rolling or drawing process , is pressed radially and pressed against the aluminum mini-profi lei nsat z.
  • FIG. 1 shows an embodiment of the heat exchanger tube with an aluminum profile insert lying directly against the steel outer tube
  • FIG. 2 shows an embodiment for the type of FIG. 1 with a simple additional measure for enlarging the inner surface
  • FIG. 3 shows an embodiment with a profile insert which bears indirectly on the outer tube via an intermediate profile, in the manner of FIG. 1.
  • the heat exchanger tube shown in FIG. 1 consists of a cylindrical, smooth-walled outer tube 1 made of a corrosion-resistant chrome steel and a professional insert 2 made of aluminum.
  • the profile insert 2 is formed by a tubular body which is divided into two half-shells 3, 4 in a dividing plane running through the outer tube longitudinal axis.
  • the two half-shells 3, arcs 4 Trained with ribs 5 which extend in the longitudinal direction of the outer tube 1, and so in the clear Q uer4.000 of the tubular body protrude, that each Halb ⁇ cup 3, 4 with their ribs 5 open on one side Profiles so that the half-shells with their caps can be easily and cheaply produced with an extrusion tool or a drawing die without a so-called flying core.
  • the ribs 5, as the embodiment of FIG. 1 shows are arranged in a comb-like manner and perpendicular to the dividing plane on the inside of the two half-shells 3, 4, the ribs 5 of the two half-shells 3, 4 face each other in pairs and extend up to or at least close to the parting plane.
  • the two half-shells 3, 4 are formed with groove-shaped depressions 7 and rib-like projections 8, which are perpendicular to the parting plane and which the longitudinal edges in the Interlock like a labyrinth seal.
  • the sealing of the two joints between the half-shell longitudinal edges is important so that no gap arises, through which the exhaust gas or condensate penetrates between the tubular body of the professional insert 2 and the outer tube 1 and there leads to crevice corrosion.
  • the two half-shells, as illustrated in FIG. 1 are formed on one longitudinal edge with a groove-shaped depression and on the other longitudinal edge with a rib-like projection, the two half-shells can be of the same extruded profile in the required length be separated and fits one half shell rotated 180 ° in the longitudinal axis on the other half shell.
  • Figure 1 shows the heat exchanger tube for the sake of clarity in a not yet finalized state.
  • the longitudinal edges of the two half-shells interlocking with the recesses and projections are pressed together in such a gap-free manner and absolutely tightly against exhaust gas or condensate that a seam between the longitudinal edges of the half-shells cannot even be determined in a micro section of the cross section of the finished heat exchanger tube.
  • the gap-free compression of the outer tube and the profile insert on the contacting peripheral surfaces also prevents exhaust gas or condensate from penetrating between the outer tube and the profile insert on the end face of the heat exchanger tube installed in a boiler.
  • the extremely high heat transfer capability of the heat exchanger tube between the profile insert and the outer tube also has a surprisingly advantageous effect for the reverse heat flow when the heat exchanger tube ends are welded into tube sheets or tube plates of a boiler.
  • Welding tests have shown that even with a flush end face of the aluminum profile insert with the chrome steel outer tube, the aluminum is surprisingly not damaged or melted away, although the chrome outer tube with liquid welding material fuses with the tube plate of the boiler must be connected.
  • the exchanger tube can therefore be separated from the finished fabric of the exchanger tube in the lengths required for a boiler with a simple straight cut or saw cut or the like.
  • FIG. 2 shows an exemplary embodiment similar to FIG. 1, in which the tips of the ribs 5 arranged in a comb-like manner are at such a distance from one another Comply with the fact that a flat aluminum profile 9 can be inserted between the tips.
  • the rib length is so dimensioned that are pressed when joining the half-shells 3, 4 to the raw RK ⁇ rpe rförmi gen pro l ⁇ insert the comb tips with their the rib cross-section satisfied respective end faces and without a gap L of the low-profile 9, a reliable heat conductive contact between the flat profile and the ribs.
  • the contacting longitudinal edges of the two half-shells can also be designed such that they enclose the longitudinal edges of the flat profile and are clamped between them in a heat-conducting manner on the finished heat exchanger.
  • the heat-absorbing inner surface of the profile insert 2 can be enlarged again in a simple and cheap manner by a considerable amount in the order of 10% or more.
  • FIG. 3 shows an exemplary embodiment in which the aluminum professional insert 2 of the type of FIG. 1 does not directly touch the inside of the outer tube 1 with its outer side, but rather has an outer diameter which is significantly less than the inner diameter of the outer tube 1.
  • An annular cylindrical intermediate profile 10 made of aluminum is arranged in the annular space thus formed between the outer tube 1 and the profile insert 2.
  • This intermediate profile 10 consists of a tube wall, the entire outer circumference of which lies flush against the entire inner surface of the outer tube 1, and a number of ribs 11 arranged radially on the inside of the tube body, which extend to the outside of the profile Reach oil insert 2 and touch the outside of the profile insert flat and heat-conducting.
  • the intermediate profile 10 is similar to the inner profile insert 2 in a dividing plane running through the longitudinal axis of the outer tube and divided into two half-open profile profiles. parts, which can therefore also be produced with a simple drawing die without a flying core by extrusion of aluminum.
  • the intermediate professional 10 is designed in a similar way to the professional insert 2 described with reference to FIG. 1 with sealingly contacting or engaging longitudinal edges of the two intermediate professionals Ihten Iften.
  • the embodiment in FIG. 3 allows the total internal surface of the heat exchanger tube that can be touched and absorbed by the combustion gases to be increased by a good 100%. be increased.
  • the length of the heat exchanger tube can be shortened even further, in order to bring the combustion gases in a condensing boiler from an inlet temperature of, for example, 850 ° C. to an outlet temperature which is clearly below the dew point limit of the combustion gases cool down from, for example, 48 ° C.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Geometry (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Details Of Fluid Heaters (AREA)
  • Steam Or Hot-Water Central Heating Systems (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Air Supply (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

L'invention concerne un tube échangeur de chaleur qui comprend un tube extérieur (1) cylindrique à paroi lisse, en acier, dans lequel est inséré un profilé (2) en aluminium. Ce profilé se compose de deux demi-coques (3, 4) qui s'emboîtent au niveau de leurs bords longitudinaux par le biais de cavités (7) se présentant sous forme de rainures et de parties saillantes (8) se présentant sous forme de nervures. Les deux demi-coques (3, 4) comportent des ailettes (5) longitudinales sur leur face intérieure, orientées de manière à ce que chaque demi-coque constitue, de par ses ailettes, un profilé ouvert d'un côté.
EP95913118A 1994-03-24 1995-03-15 Tube echangeur de chaleur pour chaudiere de chauffage Expired - Lifetime EP0752088B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE9405062U 1994-03-24
DE9405062U DE9405062U1 (de) 1994-03-24 1994-03-24 Wärmetauscherrohr für Heizkessel
PCT/EP1995/000957 WO1995025937A1 (fr) 1994-03-24 1995-03-15 Tube echangeur de chaleur pour chaudiere de chauffage

Publications (2)

Publication Number Publication Date
EP0752088A1 true EP0752088A1 (fr) 1997-01-08
EP0752088B1 EP0752088B1 (fr) 1997-11-26

Family

ID=6906491

Family Applications (1)

Application Number Title Priority Date Filing Date
EP95913118A Expired - Lifetime EP0752088B1 (fr) 1994-03-24 1995-03-15 Tube echangeur de chaleur pour chaudiere de chauffage

Country Status (26)

Country Link
US (1) US6070657A (fr)
EP (1) EP0752088B1 (fr)
JP (1) JP3016866B2 (fr)
KR (1) KR100217265B1 (fr)
CN (1) CN1120347C (fr)
AT (1) ATE160628T1 (fr)
AU (1) AU678713B2 (fr)
CA (1) CA2186270C (fr)
CZ (1) CZ286145B6 (fr)
DE (2) DE9405062U1 (fr)
DK (1) DK0752088T3 (fr)
EE (1) EE03318B1 (fr)
ES (1) ES2112055T3 (fr)
FI (1) FI107835B (fr)
GR (1) GR3026039T3 (fr)
HR (1) HRP950131B1 (fr)
HU (1) HU220435B (fr)
LV (1) LV12025B (fr)
NO (1) NO303151B1 (fr)
NZ (1) NZ282800A (fr)
PL (1) PL178916B1 (fr)
RU (1) RU2125219C1 (fr)
SK (1) SK281996B6 (fr)
TR (1) TR28643A (fr)
UA (1) UA26941C2 (fr)
WO (1) WO1995025937A1 (fr)

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EP2781873A4 (fr) * 2011-11-14 2015-10-07 Sung-Hwan Choi Tuyau d'échange de chaleur et méthode de fabrication de celui-ci
EP3040638A1 (fr) 2015-07-23 2016-07-06 Hoval Aktiengesellschaft Tuyau de transfert de chaleur et chaudiere dotee d'un tel tuyau de transfert de chaleur
EP1617139B1 (fr) 2004-07-13 2016-08-31 UNICAL AG S.p.A. Conduite dans une chaudière à tubes de fumées

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1617139B1 (fr) 2004-07-13 2016-08-31 UNICAL AG S.p.A. Conduite dans une chaudière à tubes de fumées
EP2781873A4 (fr) * 2011-11-14 2015-10-07 Sung-Hwan Choi Tuyau d'échange de chaleur et méthode de fabrication de celui-ci
EP3040638A1 (fr) 2015-07-23 2016-07-06 Hoval Aktiengesellschaft Tuyau de transfert de chaleur et chaudiere dotee d'un tel tuyau de transfert de chaleur
EP3301378A1 (fr) 2015-07-23 2018-04-04 Hoval Aktiengesellschaft Tuyau de transfert de chaleur et chaudière dotée d'un tel tuyau de transfert de chaleur
EP3040638B1 (fr) * 2015-07-23 2018-05-09 Hoval Aktiengesellschaft Tuyau de transfert de chaleur et chaudiere dotee d'un tel tuyau de transfert de chaleur

Also Published As

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HRP950131A2 (en) 1997-02-28
NO303151B1 (no) 1998-06-02
DK0752088T3 (da) 1998-08-10
CN1144558A (zh) 1997-03-05
CA2186270C (fr) 2000-06-13
FI963772A0 (fi) 1996-09-23
SK281996B6 (sk) 2001-10-08
AU2070895A (en) 1995-10-09
ES2112055T3 (es) 1998-03-16
DE9405062U1 (de) 1994-05-26
EE03318B1 (et) 2000-12-15
PL178916B1 (pl) 2000-06-30
KR100217265B1 (ko) 1999-09-01
NO963993L (no) 1996-09-23
TR28643A (tr) 1996-12-16
JPH09507708A (ja) 1997-08-05
PL316389A1 (en) 1997-01-06
CZ261396A3 (en) 1996-12-11
FI107835B (fi) 2001-10-15
HRP950131B1 (en) 2000-10-31
FI963772A (fi) 1996-09-23
JP3016866B2 (ja) 2000-03-06
EP0752088B1 (fr) 1997-11-26
GR3026039T3 (en) 1998-04-30
DE59501046D1 (de) 1998-01-08
HU220435B (hu) 2002-01-28
SK116596A3 (en) 1998-10-07
NZ282800A (en) 1997-03-24
HUP9774653A2 (en) 1997-01-28
CZ286145B6 (cs) 2000-01-12
LV12025A (lv) 1998-04-20
WO1995025937A1 (fr) 1995-09-28
US6070657A (en) 2000-06-06
ATE160628T1 (de) 1997-12-15
HU9602608D0 (en) 1996-11-28
RU2125219C1 (ru) 1999-01-20
AU678713B2 (en) 1997-06-05
CA2186270A1 (fr) 1995-09-28
KR970701851A (ko) 1997-04-12
UA26941C2 (uk) 1999-12-29
LV12025B (lv) 1998-07-20
CN1120347C (zh) 2003-09-03
NO963993D0 (no) 1996-09-23

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