EP2299227B1 - Röhrenwärmetauscher - Google Patents

Röhrenwärmetauscher Download PDF

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Publication number
EP2299227B1
EP2299227B1 EP10171888.0A EP10171888A EP2299227B1 EP 2299227 B1 EP2299227 B1 EP 2299227B1 EP 10171888 A EP10171888 A EP 10171888A EP 2299227 B1 EP2299227 B1 EP 2299227B1
Authority
EP
European Patent Office
Prior art keywords
tube
heat exchanger
tubular heat
product
juice
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.)
Active
Application number
EP10171888.0A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP2299227A3 (de
EP2299227A2 (de
Inventor
Roland Feilner
Jörg Zacharias
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.)
Krones AG
Original Assignee
Krones 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 Krones AG filed Critical Krones AG
Priority to PL10171888T priority Critical patent/PL2299227T3/pl
Publication of EP2299227A2 publication Critical patent/EP2299227A2/de
Publication of EP2299227A3 publication Critical patent/EP2299227A3/de
Application granted granted Critical
Publication of EP2299227B1 publication Critical patent/EP2299227B1/de
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/34Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely
    • F28F1/36Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending obliquely the means being helically wound fins or wire spirals
    • 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
    • F28D7/10Heat-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 one within the other, e.g. concentrically
    • F28D7/106Heat-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 one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40Tubular 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/42Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/42Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
    • F28F1/424Means comprising outside portions integral with inside portions
    • F28F1/426Means comprising outside portions integral with inside portions the outside portions and the inside portions forming parts of complementary shape, e.g. concave and convex
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • 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
    • F28D2021/0042Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for foodstuffs
    • 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
    • F28D2021/0098Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for viscous or semi-liquid materials, e.g. for processing sludge
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers

Definitions

  • the invention relates to a tubular heat exchanger specified in the preamble of claim 1 species and an inner and / or jacket tube of such a tubular heat exchanger.
  • Out DE 102 56 232 B4 is a tubular heat exchanger, according to the preamble of claim 1, for the UHT treatment of milk and dairy products for sterilization known.
  • the jacket tube is a smooth tube.
  • the inner tubes are tantdrallrohre, in which the multi-course mutually opposing swirls intersect at angles between 25 ° and 35 ° along the tube axis, ie with helix angles between 65 ° and 55 °. This angle range is specially adapted to milk and milk products, which are very prone to build up on the contacted surface. Therefore, the swirls are additionally electrochemically polished. The combination of the two measures results in an optimal inhibition of the buildup of milk and milk products and thus in long life of the tube heat exchanger up to a required cleaning cycle.
  • helix angles of 45 ° which are to be regarded as optimal in terms of heat transfer, but which lead to milk and milk products to an inadmissibly strong formation of deposits. Inclination between 25 ° and 35 ° and the additional surface treatment are therefore an optimum for milk and milk products in terms of inhibiting the product-specific formation of deposits, however, as well as the usual helix angle of 45 ° to the tube axis, an unfavorable relationship between the achieved increase in heat transfer and excessive Increase of the pressure loss in the flow.
  • Out DE 600 19 635 T2 is a tube heat exchanger for the treatment of juices with fibers and / or particles known in which simply twisted inner and / or outer tubes are used.
  • the helix angle is shown at about 45 °, while the helix angle in the jacket tube at about 75 °, in each case based on the tube axis, is shown.
  • this tubular heat exchanger it is disadvantageous that, in order to increase the heat transfer, it is necessary to accept very high pressure loss with a constant flow area and the boundary layer of the flow is excited to strong rotation at the swirlings extending at the same helix angle to the pipe axis. This requires very high, possibly for the product disadvantageous, delivery pressure for the treatment of the product in the tubular heat exchanger.
  • the invention has for its object to provide a tubular heat exchanger of the type mentioned above and a use of such a tubular heat exchanger, which allow optimally short residence times and small heat exchanger surfaces in the processing of juices or juicy food products with medium to high viscosity despite only moderate delivery pressure.
  • the propensity for product batch formation is of secondary importance to juices and juice-like food products, since when using cross-twist tubes with the indicated shallow helix angles it is primarily important that pulp, fibers or particles as constituents of the juices or juice-like food products are not used because of the shallow helix angles Suspending and collecting tend, but quickly washed away. Furthermore, such a cleaning up to a hygienic condition is possible.
  • the tube heat exchanger is particularly well suited for the thermal treatment of juices or juice-like food products with viscosities> about 5 mPas, wherein the product may contain pulp, fibers or particles.
  • each swirl in the axial section of the tube has a trough-like depression with mutual, approximately wedge-shaped ribs in cross section, between which a swirl depth between approximately 0.8 mm to 1.2 mm exists in the depression.
  • the interaction between the relatively shallow helix angles and the moderate swirl depth results even at moderate delivery pressure in an optimal ratio for juices and juicy food products of medium to high viscosities between the increase in heat transfer and the resulting increase in pressure loss.
  • the recesses and the ribs are located on the product-contactable surface.
  • the width seen in the direction of the tube axis in the depression is a multiple of the twist depth. It should be between about 5.0 and 20.0 mm.
  • the depressions are relatively wide depressions, at the limiting ribs components of the product are rapidly flushed, and also a hygienic cleaning, e.g. for a product change.
  • both multistage swirls cover the entire surface of the pipe surface.
  • the jacket tube with several cross-spiral inner tubes forms a module of the tubular heat exchanger.
  • This module can extend over 3.0, 6.0 m or more and, suitably, is combined in series to treat the product in the multi-module tubular heat exchanger.
  • a heat transfer medium is used in the flow channel between the jacket tube and the inner tubes.
  • the respective cross-spiral inner tube has the depressions of the swirls on the outside or the inside, for example, depending on which pipe surface the product flows along.
  • the used swirls on the inner and outer tube surfaces in the flows are effective.
  • module M of a tubular heat exchanger W for the thermal treatment of juices or juicy food products with medium to high viscosities, for example, a viscosity of more than about 5 mPas consists of a jacket tube 1 and at least one inside the jacket tube 1 at a distance from the inner wall of the jacket tube
  • the module M is combined in the tube heat exchanger W, for example, with other, similar or similar modules not shown, to form a treatment section of a certain conveying length.
  • the product is treated either by a recuperative process, ie product by product separated by, for example, the inner tube 2, or by a method in which a heat transfer medium (steam or water) is used, the heat transfer medium is separated from the product by, for example, the respective Inner tube 2.
  • a recuperative process ie product by product separated by, for example, the inner tube 2
  • a method in which a heat transfer medium steam or water
  • the respective method is, preferably, operated in countercurrent or in direct current.
  • the jacket tube 1 in Fig. 1 is designed as a cross-twist tube with substantially mutually symmetrical to the tube axis X crossing,
  • D1, D2 wherein the twist angle ⁇ to the tube axis X between 18 ° to 23 ° and the angle of attack ⁇ 67 ° and 72 ° to the tube axis.
  • the funneldrallrohr for example similar to that in Fig. 4 shown formed with pointing to the tube interior recesses 3.
  • the respective inner tube 2 is also a Buchdrallrohr with substantially mutually symmetrical to the tube axis X crossing multi-speed swirls and helix angles ⁇ between 18 ° and 23 °.
  • the jacket tube 1 is a smooth tube.
  • each inner tube 2 contained in the jacket tube 1 is a Buchdrallrohr with each other substantially symmetrical to the tube axis X crossing, Distance to twist D1, D2 and helix angles a1 between 18 ° and 23 ° to the tube axis X.
  • the twists D1, D2 are more common, so that despite the relatively steep angle of attack (helix angle a1 between 18 ° and 23 °) the entire Pipe surface offers the product above all the heat transfer intensifying macrostructures, and is achieved between the increase in heat transfer and the pressure loss caused by the swirls an optimum.
  • Fig. 4 illustrates the macrostructures formed by the intersecting swirls D1, D2 of the respective funneldrallrohres as the inner tube 2, which are present on the inside and the outside of the tube.
  • Fig. 4 lie the tube axis X facing in the axial direction successively trough-like depressions 3, which are each bounded by substantially wedge-shaped ribs 5 and have a twist depth T between 0.8 mm and 1.2 mm.
  • the width B of each recess 3 is a multiple of the twist depth T, preferably between 5.0 mm and 20.0 mm.
  • a rounded tip 4 is provided corresponding to the recess 3, which is bounded in the axial direction by approximately V-shaped grooves 6.
  • the ribs 5 and the grooves 6 could be rounded, for example, with regard to a good cleanability of the tube.
  • the ribs 5 and the grooves 6 extend as well as the wells 3 and the crests 4 at the helix angle ⁇ , ⁇ 1 helical and periodically crossing each other over the entire inner or outer pipe surface.
  • FIG Fig. 5 is a funneldrallrohr as a jacket or inner tube 1, 2 indicated, in which the recesses 3 on the outside of the tube (ie the tube axis X facing away) are present.
  • the twist depth T is between 0.8 mm and 1.2 mm.
  • the helix angles ⁇ , ⁇ 1 are between 18 ° and 23 ° to the tube axis X.
  • the in Fig. 5 shown cross-twist tube is suitably used as the inner tube 2, for example, if the product flows between the jacket tube 1 and the outside of the inner tube 2. If a heat transfer medium is used, which flows in the flow channel between the jacket tube 1 and each inner tube 2, the cross-twist tube is expediently analogous to the inner tube 2 Fig. 4 educated.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
EP10171888.0A 2009-09-08 2010-08-04 Röhrenwärmetauscher Active EP2299227B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL10171888T PL2299227T3 (pl) 2009-09-08 2010-08-04 Rurowy wymiennik ciepła

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102009040558A DE102009040558A1 (de) 2009-09-08 2009-09-08 Röhrenwärmetauscher

Publications (3)

Publication Number Publication Date
EP2299227A2 EP2299227A2 (de) 2011-03-23
EP2299227A3 EP2299227A3 (de) 2016-12-07
EP2299227B1 true EP2299227B1 (de) 2018-09-19

Family

ID=43242416

Family Applications (1)

Application Number Title Priority Date Filing Date
EP10171888.0A Active EP2299227B1 (de) 2009-09-08 2010-08-04 Röhrenwärmetauscher

Country Status (8)

Country Link
US (1) US20110056663A1 (pl)
EP (1) EP2299227B1 (pl)
CN (1) CN102012177A (pl)
BR (1) BRPI1003318A2 (pl)
DE (1) DE102009040558A1 (pl)
ES (1) ES2691257T3 (pl)
HU (1) HUE041374T2 (pl)
PL (1) PL2299227T3 (pl)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011006653A1 (de) 2011-04-01 2012-10-04 Krones Aktiengesellschaft Getränkeerhitzungssystem mit integrierter Verbrennungsanlage und Verfahren zum Erhitzen von Getränken
RU2548332C1 (ru) * 2013-10-08 2015-04-20 Николай Григорьевич Гладков Теплообменник
CN104713405B (zh) * 2015-03-04 2016-08-17 东南大学 一种正三角形排列的对涡排阵列换热装置
RU2622340C1 (ru) * 2016-07-15 2017-06-14 Федеральное государственное бюджетное образовательное учреждение высшего образования "Юго-Западный государственный университет" (ЮЗГУ) Вихревой теплообменный элемент
RU2672229C1 (ru) * 2017-10-17 2018-11-12 Федеральное государственное бюджетное образовательное учреждение высшего образования " Юго-Западный государственный университет" (ЮЗГУ) Вихревой теплообменный элемент

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US1797014A (en) * 1923-11-12 1931-03-17 Edgar B Nichols Milk-treatment tank
US1918966A (en) * 1930-06-20 1933-07-18 Gen Chemical Corp Apparatus for treating gas
US2080537A (en) * 1935-12-06 1937-05-18 Cherry Burrell Corp Processing vat
US2353912A (en) * 1940-04-23 1944-07-18 Elmer H Berryman Means for homogenizing and heat-treating fluids
US2413360A (en) * 1940-10-02 1946-12-31 Walter Maguire Company Inc Heat exchanger
US2589262A (en) * 1946-06-12 1952-03-18 Hydrocarbon Research Inc Heat exchanger
DE1539323A1 (de) * 1966-06-08 1969-10-02 Siemens Ag Thermogenerator
US3850231A (en) * 1973-05-24 1974-11-26 Combustion Eng Lmfbr intermediate heat exchanger
DE9403913U1 (de) * 1994-03-09 1994-05-05 Gea Finnah Gmbh Rohrbündel-Wärmetauscher
JPH0842982A (ja) * 1994-05-17 1996-02-16 Hde Metallwerk Gmbh 高効率型毛管式熱交換器
US5992512A (en) * 1996-03-21 1999-11-30 The Furukawa Electric Co., Ltd. Heat exchanger tube and method for manufacturing the same
US6273180B1 (en) * 1998-12-23 2001-08-14 L'air Liquide, Societe Anonyme Pour L'etude Et L'eploitation Des Procedes Georges Claude Heat exchanger for preheating an oxidizing gas
SE518089C2 (sv) 1999-10-26 2002-08-27 Tetra Laval Holdings & Finance Anordning vid en tubvärmeväxlare
DE10156374C1 (de) * 2001-11-16 2003-02-27 Wieland Werke Ag Beidseitig strukturiertes Wärmeaustauscherrohr und Verfahren zu dessen Herstellung
DE10210016B9 (de) * 2002-03-07 2004-09-09 Wieland-Werke Ag Wärmeaustauschrohr mit berippter Innenoberfläche
DE10256232B4 (de) * 2002-12-02 2004-10-21 Tuchenhagen Dairy Systems Gmbh Vorrichtung zur Verlängerung der Standzeit von Rohrbündel-Wärmeaustauschern in indirekt beheizten UHT-Anlagen für Nahrungsmittel
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Also Published As

Publication number Publication date
US20110056663A1 (en) 2011-03-10
DE102009040558A1 (de) 2011-03-10
EP2299227A3 (de) 2016-12-07
PL2299227T3 (pl) 2019-06-28
HUE041374T2 (hu) 2019-05-28
EP2299227A2 (de) 2011-03-23
CN102012177A (zh) 2011-04-13
ES2691257T3 (es) 2018-11-26
BRPI1003318A2 (pt) 2012-05-29

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