EP0733871A1 - Heat transfer tube for a heat exchanger - Google Patents
Heat transfer tube for a heat exchanger Download PDFInfo
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- EP0733871A1 EP0733871A1 EP96103390A EP96103390A EP0733871A1 EP 0733871 A1 EP0733871 A1 EP 0733871A1 EP 96103390 A EP96103390 A EP 96103390A EP 96103390 A EP96103390 A EP 96103390A EP 0733871 A1 EP0733871 A1 EP 0733871A1
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- Prior art keywords
- ribs
- exchanger tube
- tube according
- troughs
- micro
- 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.)
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- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S165/00—Heat exchange
- Y10S165/51—Heat exchange having heat exchange surface treatment, adjunct or enhancement
- Y10S165/515—Patterned surface, e.g. knurled, grooved
Definitions
- the invention relates to an exchanger tube for a heat exchanger according to the features in the preamble of claim 1.
- the troughs formed in the ribs are produced by rolling.
- the material deformed from the ribs bulges into the channels at the front of the troughs.
- the bottoms of the troughs are at a distance from the canal bases.
- the known exchanger tube is produced by first producing the structure of the subsequent inner surface on one side on a metal strip in a two-stage rolling process, then forming the metal strip into a slot tube with an internal surface structure and then welding the slot edges.
- the two-stage rolling of the inner surface structure leads to high manufacturing costs.
- Several roller embossing tools are required, which affect the economy.
- the troughs of the ribs are created by rolling over an initially existing volume fraction of the ribs that were formed in the first rolling step. This former volume share of the ribs is only distributed in the immediate vicinity. However, a noteworthy reduction in the meter weight cannot be achieved.
- the invention is based on the object of creating an exchanger tube with an inner surface structure in which, on the one hand, the advantages of an equally good evaporation or condensation performance combined with a reduced fin weight are combined and, on the other hand, a one-step embossing process is used to produce the exchanger tube can.
- the core of the invention is formed by such an internal, rough surface structure, which has only rounded transitions and avoids sharp edges. Consequently, the rough surface structure can be produced in a particularly advantageous manner by roller embossing in a single step. This considerably reduces the expenditure on equipment.
- the surfaces of the ribs up to the channel soles are additionally provided with a targeted micro-roughness. This is particularly noticeable in the condensation and evaporation of refrigerants if the exchanger tube is integrated into a corresponding heat exchanger.
- the cross-sectional volume of the ribs has been reduced in favor of increasing the number of ribs. This makes it possible to enlarge the heat-exchanging surface structure and thus to improve the heat transfer. In this context, very slim ribs and thus narrow channels can also be created.
- the ribs rounded at the head have the particular advantage that when a heat exchanger tube is drawn into fins of a heat exchanger, in particular by widening by means of a tool moved through the heat exchanger tube, the head portions of the ribs are only insignificantly flattened, so that the formation of condensate films that are difficult to tear open is also effective is opposed. Nevertheless, the large number of projections, edges, tips and depressions which are advantageous for effective evaporation can be provided as vapor bubble nuclei by the micro-roughness due to the large fin surfaces, without the need for larger amounts of material.
- the surfaces of the fins can also be provided with a coarse structure corresponding to the inner structure of the exchanger tubes and / or with a micro-roughness.
- the invention is applied to exchanger tubes made of metal, but especially of copper or copper alloys.
- exchanger tubes can have, for example, a round or oval cross section.
- Round exchanger tubes preferably have an outside diameter of approximately 6 mm to 20 mm.
- the embodiment according to claim 2 provides that the central longitudinal planes of the troughs of adjacent ribs run in alignment.
- micro-roughness of the fin surfaces can be achieved in various ways. For example, a diffuse roughening by blasted corundum is conceivable. Notching of the rib surfaces in the form of linear micro-grooves is also conceivable (claim 3). These micro grooves then preferably extend parallel to one another. However, their longitudinal direction deviates from the longitudinal direction of the ribs.
- micro-roughness can moreover be formed according to claim 4 by intersecting micro-grooves which deviate from the longitudinal direction of the ribs.
- punctual depressions can also be provided. These can also be arranged in a line or cross shape at a distance one behind the other.
- microroughness can also be generated in various ways. A preferred variant is seen in the features of claim 5.
- the micro-roughness of the fin surfaces is produced by irradiation with hard particles, such as corundum, or by texturing using laser beams. It is possible to either process the starting material (sheet metal strip) already provided with the surface structure accordingly or to provide an embossing roller itself with the desired negative micro-roughness.
- the flank angle of the ribs can be 5 ° to 60 °, but preferably 10 ° to 40 °. In this way, a very slim rib contour can be produced.
- the distance between two adjacent ribs is 0.10 mm to 2.0 mm, preferably 0.26 mm to 0.6 mm.
- the height of the fins is appropriately between 0.03 mm and 1.0 mm, preferably 0.05 mm to 0.35 mm.
- the distance between two adjacent troughs of a rib is 0.2 mm to 4.0 mm, preferably 0.3 mm to 1.0 mm.
- the bottoms of the troughs and the channel soles do not have to lie on one level.
- the minimum distance between the trough floors and the channel soles should then be at least 0.01 mm.
- FIG. 1 in FIG. 1 denotes a longitudinal section of a longitudinally welded exchanger tube for an otherwise not shown heat exchanger for the condensation and evaporation of refrigerants.
- the exchanger tube 1 which is circular in outer and inner cross section, has a smooth outer surface 2 and a structured inner surface 3.
- the exchanger tube 1 is placed in one of its own Outside diameter adapted opening inserted in the lamella and fixed by widening in the opening.
- an appropriately designed expansion tool is moved through the exchanger tube 1.
- the exchanger tube 1 has an outer diameter D of 9.52 mm.
- the exchanger tube 1 is produced from a sheet metal strip made of copper, which is flat on both sides and not shown.
- the sheet metal strip is subjected to a single-stage roller stamping process, one side of the sheet metal strip 4 remaining smooth (the later outer surface 2 of the exchanger tube 1) and the other side with a structured surface (the later inner side 3 of the exchanger tube 1) as shown in FIGS. 2 and 3 ) is provided. Only the edge regions 5 of the sheet metal strip 4 (FIG. 2) used for welding remain unstructured. After the roll embossing, the sheet metal strip 4 is formed into a slotted tube and then welded along the longitudinal seam and divided into lengths.
- both the head regions 10 of the ribs 7 and the transitions 11 from the flanks 8 to the channel soles 12 are rounded.
- the cross-sectional volume of the ribs 7 is smaller than the cross-sectional volume of the channels 13 between the ribs 7.
- each rib 7 is provided with a sinusoidal ridge shape when viewed in longitudinal section. Because of this sinusoidal wave crest of the ribs 7 in their longitudinal directions LR, transverse troughs 14 are formed in the ribs 7. As FIG. 2 shows in this connection, troughs 14 of adjacent ribs 7 are arranged one behind the other at an angle ⁇ of 45 ° to the longitudinal axis 6 of the exchanger tube 1. The angle ⁇ enclosed between the longitudinal direction LR of the ribs 7 and the central longitudinal planes MLE of the troughs 14 is 90 °. The distance A1 between two troughs 14 adjacent in the longitudinal direction of a rib 7 is 0.50 mm (FIGS. 2 and 5) and the distance A2 of the trough bottoms 15 from the channel soles 12 is 0.01 mm. The troughs 14 have a depth T1 of 0.25 mm (FIGS. 4 and 5).
- the microroughness 16 is produced directly during the roll embossing.
- the embossing roller has been provided with a negative diffuse surface structure by means of irradiation with corundum, which then ensures the generation of the surface structure on the later inner surface 3 of the exchanger tube 1.
- the exchanger tube 1 illustrated in FIG. 1 has a significantly better heat transfer coefficient k '(W / mK) compared not only to an exchanger tube with a smooth inner surface, but also to an internally grooved exchanger tube.
- FIGS. 6 and 7 drawn up on the basis of comparative investigations without additional explanations (FIG. 6 —condensation, FIG. 7 — evaporation).
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- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Geometry (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Shaping Metal By Deep-Drawing, Or The Like (AREA)
- Laser Beam Processing (AREA)
- Pressure Welding/Diffusion-Bonding (AREA)
Abstract
Description
Die Erfindung betrifft ein Austauscherrohr für einen Wärmeaustauscher gemäß den Merkmalen im Oberbegriff des Anspruchs 1.The invention relates to an exchanger tube for a heat exchanger according to the features in the preamble of
Ein derartiges Austauscherrohr zählt durch die US-PS 53 32 034 zum Stand der Technik. Hierbei weisen sowohl die Rippen als auch die von den Rippen seitlich begrenzten Kanäle jeweils einen trapezförmigen Querschnitt auf. Das Querschnittsvolumen der Rippen ist etwa halb so groß wie das Querschnittsvolumen der Kanäle bemessen.Such an exchanger tube is part of the prior art through US Pat. No. 5,332,034. Both the ribs and the channels laterally delimited by the ribs each have a trapezoidal cross section. The cross-sectional volume of the ribs is approximately half the size of the cross-sectional volume of the channels.
Die in den Rippen ausgeformten Mulden werden durch Walzen hergestellt. Hierbei wölbt sich das aus den Rippen verformte Material stirnseitig der Mulden in die Kanäle hinein. Die Böden der Mulden liegen im Abstand zu den Kanalsohlen.The troughs formed in the ribs are produced by rolling. The material deformed from the ribs bulges into the channels at the front of the troughs. The bottoms of the troughs are at a distance from the canal bases.
Die Herstellung des bekannten Austauscherrohrs erfolgt dadurch, daß zunächst in einem zweistufigen Walzprozeß die Struktur der späteren inneren Oberfläche einseitig an einem Metallband erzeugt, anschließend das Metallband zu einem Schlitzrohr mit innenliegender Oberflächenstruktur umgeformt wird und danach die Schlitzkanten verschweißt werden.The known exchanger tube is produced by first producing the structure of the subsequent inner surface on one side on a metal strip in a two-stage rolling process, then forming the metal strip into a slot tube with an internal surface structure and then welding the slot edges.
Das zweistufige Walzen der inneren Oberflächenstruktur führt zu einem hohen Fertigungsaufwand. Es sind mehrere Walzprägewerkzeuge erforderlich, welche die Wirtschaftlichkeit beeinträchtigen. Die Mulden der Rippen entstehen durch Überwalzen eines zunächst vorhandenen Volumenanteils der im ersten Walzschritt ausgeprägten Rippen. Dieser ehemalige Volumenanteil der Rippen wird nur in die unmittelbare Nachbarschaft verteilt. Eine nennenswerte Verringerung des Metergewichts kann aber nicht erreicht werden.The two-stage rolling of the inner surface structure leads to high manufacturing costs. Several roller embossing tools are required, which affect the economy. The troughs of the ribs are created by rolling over an initially existing volume fraction of the ribs that were formed in the first rolling step. This former volume share of the ribs is only distributed in the immediate vicinity. However, a noteworthy reduction in the meter weight cannot be achieved.
Ferner kann es aufgrund der Ebenflächigkeit der Kopfseiten und der Flanken der Rippen im praktischen Einsatz zur Bildung von schwer aufreißbaren, die Kondensation verzögernden Kondensatfilmen kommen, so daß sich Sperrschichten mit wärmeisolierenden Eigenschaften bilden. Für die Verdampfung stehen nur wenige Kanten als Dampfblasenkeime zur Verfügung.Furthermore, due to the flatness of the top sides and the flanks of the ribs in practical use, it is possible to form condensate films which are difficult to tear open and which delay condensation, so that barrier layers with heat-insulating properties are formed. Only a few edges are available as vapor bubble nuclei for evaporation.
Der Erfindung liegt ausgehend vom Stand der Technik die Aufgabe zugrunde, ein Austauscherrohr mit einer inneren Oberflächenstruktur zu schaffen, bei welcher sich einerseits die Vorteile einer gleichermaßen guten Verdampfungs- bzw. Kondensationsleistung bei reduziertem Rippengewicht verbinden und andererseits zur Herstellung des Austauscherrohrs ein einstufiges Prägeverfahren angewendet werden kann.Based on the prior art, the invention is based on the object of creating an exchanger tube with an inner surface structure in which, on the one hand, the advantages of an equally good evaporation or condensation performance combined with a reduced fin weight are combined and, on the other hand, a one-step embossing process is used to produce the exchanger tube can.
Die Lösung dieser Aufgabe besteht nach der Erfindung in den im kennzeichnenden Teil des Anspruchs 1 aufgeführten Merkmalen.This object is achieved according to the invention in the features listed in the characterizing part of
Kern der Erfindung bildet eine solche innere grobe Oberflächenstruktur, die nur gerundete Übergänge aufweist und scharfe Kanten vermeidet. Folglich kann in besonders vorteilhafter Weise die grobe Oberflächenstruktur durch Walzprägen in einer einzigen Stufe erzeugt werden. Der apparatetechnische Aufwand wird dadurch erheblich gesenkt.The core of the invention is formed by such an internal, rough surface structure, which has only rounded transitions and avoids sharp edges. Consequently, the rough surface structure can be produced in a particularly advantageous manner by roller embossing in a single step. This considerably reduces the expenditure on equipment.
Ferner ist es jetzt hinsichtlich der Intensivierung des Wärmeübergangs zwischen dem in dem Austauscherrohr strömenden Fluid und der groben Oberflächenstruktur von Vorteil, daß die Oberflächen der Rippen bis hin zu den Kanalsohlen zusätzlich mit einer gezielten Mikrorauhigkeit versehen werden. Dies macht sich insbesondere bei der Kondensation und Verdampfung von Kältemitteln bemerkbar, wenn das Austauscherrohr in einen entsprechenden Wärmeaustauscher eingegliedert wird. Das Querschnittsvolumen der Rippen ist zugunsten der Erhöhung der Rippenanzahl verringert worden. Hierdurch ist es möglich, die wärmeaustauschende Oberflächenstruktur zu vergrößern und somit den Wärmeübergang zu verbessern. Auch können in diesem Zusammenhang sehr schlanke Rippen und damit schmale Kanäle erzeugt werden. Die kopfseitig gerundeten Rippen haben insbesondere den Vorteil, daß beim Einziehen eines Austauscherrohrs in Lamellen eines Wärmeaustauschers, insbesondere durch Aufweiten mittels eines durch das Austauscherrohr bewegten Werkzeugs, die Kopfpartien der Rippen nur unwesentlich abgeplattet werden, so daß hiermit auch der Bildung von schwer aufreißbaren Kondensatfilmen wirksam entgegengetreten wird. Dennoch kann durch die Mikrorauhigkeit aufgrund der großen Rippenoberflächen die für eine effektive Verdampfung vorteilhafte große Anzahl von Vorsprüngen, Kanten, Spitzen und Vertiefungen als Dampfblasenkeime bereitgestellt werden, ohne daß hierfür größere Materialmengen erforderlich sind.Furthermore, with regard to the intensification of the heat transfer between the fluid flowing in the exchanger tube and the coarse surface structure, it is now advantageous that the surfaces of the ribs up to the channel soles are additionally provided with a targeted micro-roughness. This is particularly noticeable in the condensation and evaporation of refrigerants if the exchanger tube is integrated into a corresponding heat exchanger. The cross-sectional volume of the ribs has been reduced in favor of increasing the number of ribs. This makes it possible to enlarge the heat-exchanging surface structure and thus to improve the heat transfer. In this context, very slim ribs and thus narrow channels can also be created. The ribs rounded at the head have the particular advantage that when a heat exchanger tube is drawn into fins of a heat exchanger, in particular by widening by means of a tool moved through the heat exchanger tube, the head portions of the ribs are only insignificantly flattened, so that the formation of condensate films that are difficult to tear open is also effective is opposed. Nevertheless, the large number of projections, edges, tips and depressions which are advantageous for effective evaporation can be provided as vapor bubble nuclei by the micro-roughness due to the large fin surfaces, without the need for larger amounts of material.
Auch die Oberflächen der Lamellen können bei Bedarf mit einer Grobstruktur entsprechend der Innenstruktur der Austauscherrohre und/oder mit einer Mikrorauhigkeit versehen werden.If necessary, the surfaces of the fins can also be provided with a coarse structure corresponding to the inner structure of the exchanger tubes and / or with a micro-roughness.
Die Anwendung der Erfindung erfolgt bei Austauscherrohren aus Metall, insbesondere aber aus Kupfer oder Kupferlegierungen. Derartige Austauscherrohre können z.B. einen runden oder ovalen Querschnitt besitzen. Runde Austauscherrohre weisen bevorzugt einen Außendurchmesser von etwa 6 mm bis 20 mm auf.The invention is applied to exchanger tubes made of metal, but especially of copper or copper alloys. Such exchanger tubes can have, for example, a round or oval cross section. Round exchanger tubes preferably have an outside diameter of approximately 6 mm to 20 mm.
Grundsätzlich ist es erfindungsgemäß vorstellbar, daß die Mittellängsebenen der Mulden zwar parallel zueinander, jedoch in Längsrichtung der Rippen zueinander versetzt verlaufen.Basically, it is conceivable according to the invention that the central longitudinal planes of the troughs run parallel to one another, but are offset in the longitudinal direction of the ribs.
Die Ausführungsform gemäß Anspruch 2 sieht demgegenüber vor, daß die Mittellängsebenen der Mulden benachbarter Rippen fluchtend verlaufen.In contrast, the embodiment according to
Die Mikrorauhigkeit der Rippenoberflächen kann auf verschiedene Art und Weise verwirklicht werden. So ist beispielsweise eine diffuse Aufrauhung durch gestrahlten Korund denkbar. Vorstellbar ist ferner eine Kerbung der Rippenoberflächen in Form von linienförmigen Mikrorillen (Anspruch 3). Diese Mikrorillen erstrecken sich dann bevorzugt parallel zueinander. Ihre Längsrichtung weicht jedoch von der Längsrichtung der Rippen ab.The micro-roughness of the fin surfaces can be achieved in various ways. For example, a diffuse roughening by blasted corundum is conceivable. Notching of the rib surfaces in the form of linear micro-grooves is also conceivable (claim 3). These micro grooves then preferably extend parallel to one another. However, their longitudinal direction deviates from the longitudinal direction of the ribs.
Die Mikrorauhigkeit kann darüberhinaus entsprechend Anspruch 4 durch sich kreuzförmig schneidende, von der Längsrichtung der Rippen abweichende Mikrorillen gebildet sein.The micro-roughness can moreover be formed according to
Statt durchgehender Mikrorillen können aber auch punktuelle Vertiefungen vorgesehen werden. Diese können ebenfalls linienförmig oder kreuzförmig im Abstand hintereinander angeordnet sein.Instead of continuous micro grooves, punctual depressions can also be provided. These can also be arranged in a line or cross shape at a distance one behind the other.
Auch die Erzeugung der Mikrorauhigkeit kann auf verschiedene Art und Weise erfolgen. Eine bevorzugte Variante wird hierbei in den Merkmalen des Anspruchs 5 gesehen. Hier wird die Mikrorauhigkeit der Rippenoberflächen durch eine Bestrahlung mit Hartpartikeln, wie z.B. Korund, oder durch eine Texturierung mittels Laserstrahlen hergestellt. Dabei ist es möglich, entweder das bereits mit der Oberflächenstruktur versehene Ausgangsmaterial (Blechband) entsprechend zu bearbeiten oder eine Prägewalze selber mit der gewünschten negativen Mikrorauhigkeit zu versehen.The microroughness can also be generated in various ways. A preferred variant is seen in the features of
Auch eine Profilgebung der Prägewalze durch Funkenerodieren ist möglich.Profiling the embossing roller by spark eroding is also possible.
Interne Untersuchungen haben ergeben, daß es zur Erzielung einer gleichermaßen guten Kondensations- und Verdampfungsleistung entsprechend Anspruch 6 vorteilhaft ist, wenn die Tiefe der Mikrorauhigkeit 0,075 mm oder geringer bemessen wird.Internal investigations have shown that to achieve an equally good condensation and evaporation performance according to
Nach Anspruch 7 kann der Flankenwinkel der Rippen 5° bis 60°, vorzugsweise jedoch 10° bis 40°, betragen. Auf diese Weise ist eine sehr schlanke Rippenkontur herstellbar.According to
Der Verlauf der Rippen relativ zur Längsachse des Austauscherrohrs erfolgt gemäß den Merkmalen des Anspruchs 8 unter einem Winkel von 1° bis 89°, vorzugsweise 20° bis 55°.The course of the ribs relative to the longitudinal axis of the exchanger tube takes place according to the features of
Ferner ist es im Rahmen der Erfindung sinnvoll, wenn nach Anspruch 9 der zwischen der Längsrichtung der Rippen und den Mittellängsebenen der Mulden eingeschlossene Winkel 90° und kleiner bemessen ist.Furthermore, it makes sense within the scope of the invention if the angle enclosed between the longitudinal direction of the ribs and the central longitudinal planes of the troughs is 90 ° and smaller.
Gemäß Anspruch 10 ist es vorteilhaft, wenn der Abstand zweier benachbarter Rippen 0,10 mm bis 2,0 mm, vorzugsweise 0,26 mm bis 0,6 mm, beträgt.According to
Die Höhe der Rippen wird je nach Rohrdurchmesser entsprechend Anspruch 11 zweckmäßig zwischen 0,03 mm bis 1,0 mm, vorzugsweise 0,05 mm bis 0,35 mm, bemessen.Depending on the tube diameter, the height of the fins is appropriately between 0.03 mm and 1.0 mm, preferably 0.05 mm to 0.35 mm.
Desweiteren ist es nach der Erfindung von Vorteil, wenn nach Anspruch 12 der Abstand zweier benachbarter Mulden einer Rippe 0,2 mm bis 4,0 mm, vorzugsweise 0,3 mm bis 1,0 mm, beträgt.Furthermore, it is advantageous according to the invention if, according to
Die Böden der Mulden und die Kanalsohlen müssen gemäß Anspruch 13 nicht auf einer Ebene liegen. Der minimale Abstand der Muldenböden von den Kanalsohlen sollte dann mindestens 0,01 mm betragen.The bottoms of the troughs and the channel soles do not have to lie on one level. The minimum distance between the trough floors and the channel soles should then be at least 0.01 mm.
Entsprechend den Merkmalen des Anspruchs 14 ist es aber auch denkbar, daß die Muldenböden und die Kanalsohlen in derselben Ebene liegen.According to the features of
Die Erfindung ist nachfolgend anhand von in den Zeichnungen dargestellten Ausführungsbeispielen näher erläutert. Es zeigen:
Figur 1- in der Perspektive einen Längenabschnitt eines Austauscherrohrs;
Figur 2- in der Draufsicht einen Längenabschnitt eines strukturierten Blechbands;
Figur 3- in der Perspektive den Ausschnitt III der
Figur 2; Figur 4- in vergrößerter Darstellung einen vertikalen Querschnitt entlang der Linie IV-
IV der Figur 2; Figur 5- einen vertikalen Längsschnitt entlang der Linie V-V der Figur 4 und die
Figuren 6 und 7- anhand von Diagrammen einen Leistungsvergleich an Wärmeaustauschern in Koaxialbauweise mit verschiedenen Rohrausführungen.
- Figure 1
- in perspective a length section of an exchanger tube;
- Figure 2
- in plan view a length section of a structured sheet metal strip;
- Figure 3
- in perspective the section III of Figure 2;
- Figure 4
- in an enlarged view a vertical cross section along the line IV-IV of Figure 2;
- Figure 5
- a vertical longitudinal section along the line VV of Figure 4 and
- Figures 6 and 7
- Based on diagrams, a performance comparison of heat exchangers in coaxial design with different pipe designs.
Mit 1 ist in der Figur 1 ein Längenabschnitt eines längsnahtgeschweißten Austauscherrohrs für einen ansonsten nicht näher dargestellten Wärmeaustauscher zur Kondensation und Verdampfung von Kältemitteln bezeichnet.1 in FIG. 1 denotes a longitudinal section of a longitudinally welded exchanger tube for an otherwise not shown heat exchanger for the condensation and evaporation of refrigerants.
Das im Außen- und Innenquerschnitt kreisrunde Austauscherrohr 1 besitzt eine glatte äußere Oberfläche 2 und eine strukturierte innere Oberfläche 3. Zur Festlegung des Austauscherrohrs 1 in einer ggf. von mehreren zueinander parallel verlaufenden Austauscherrohren 1 durchsetzten Lamelle eines Wärmeaustauschers wird das Austauscherrohr 1 in eine an seinen Außendurchmesser angepaßte Öffnung in der Lamelle eingeführt und durch Aufweiten in der Öffnung festgelegt. Zu diesem Zweck wird ein entsprechend ausgebildetes nicht näher dargestelltes Aufweitwerkzeug durch das Austauscherrohr 1 verlagert.The
Beim Ausführungsbeispiel besitzt das Austauscherrohr 1 einen Außendurchmesser D von 9,52 mm.In the exemplary embodiment, the
Die Herstellung des Austauscherrohrs 1 erfolgt aus einem nicht näher dargestellten beidseitig ebenen Blechband aus Kupfer. Das Blechband wird einem einstufigen Walzprägevorgang unterworfen, wobei entsprechend der Darstellung der Figuren 2 und 3 eine Seite des Blechbands 4 glatt bleibt (die spätere äußere Oberfläche 2 des Austauscherrohrs 1) und die andere Seite mit einer strukturierten Oberfläche (die spätere Innenseite 3 des Austauscherrohrs 1) versehen wird. Lediglich die dem Verschweißen dienenden Randbereiche 5 des Blechbands 4 (Figur 2) bleiben unstrukturiert. Nach dem Walzprägen wird das Blechband 4 zu einem Schlitzrohr eingeformt und dann längsnahtgeschweißt sowie auf Länge abgeteilt.The
Die Struktur der inneren Oberfläche 3 des Austauscherrohrs 1 wird anschließend anhand der Figuren 2 bis 5 näher erläutert.The structure of the
Sie umfaßt unter einem Winkel α von 45° zur Längsachse 6 des Austauscherrohrs 1 verlaufende parallele Rippen 7 (Figuren 2 und 3) mit geneigten Flanken 8 (Figuren 3 und 4). Der Flankenwinkel β der Rippen 7 beträgt beim Ausführungsbeispiel 20° und der Abstand A zweier benachbarter Rippen 7 0,35 mm (Figuren 2 und 4). Ihre Höhe H beläuft sich auf 0,30 mm (Figur 4). Der die Rippen 7 im Fußbereich verbindende Basisabschnitt 9 hat eine Dicke D1 von 0,30 mm (Figur 5).It comprises at an angle α of 45 ° to the
Ferner ist aus den Figuren 3 und 4 zu erkennen, daß sowohl die Kopfbereiche 10 der Rippen 7 als auch die Übergänge 11 von den Flanken 8 auf die Kanalsohlen 12 gerundet sind. Das Querschnittsvolumen der Rippen 7 ist kleiner als das Querschnittsvolumen der Kanäle 13 zwischen den Rippen 7 bemessen.It can also be seen from FIGS. 3 and 4 that both the
Wie insbesondere die Figuren 3 und 5 veranschaulichen, ist jede Rippe 7 im Längsschnitt gesehen mit einem sinusförmigen Kammverlauf versehen. Aufgrund dieses sinusförmigen Wellenkamms der Rippen 7 in ihren Längsrichtungen LR werden in den Rippen 7 quer verlaufende Mulden 14 gebildet. Wie in diesem Zusammenhang die Figur 2 zeigt, sind Mulden 14 benachbarter Rippen 7 in einem Winkel γ von 45° zur Längsachse 6 des Austauscherrohrs 1 fluchtend hintereinander angeordnet. Der zwischen der Längsrichtung LR der Rippen 7 und den Mittellängsebenen MLE der Mulden 14 eingeschlossene Winkel δ beträgt 90°. Der Abstand A1 zweier in Längsrichtung einer Rippe 7 benachbarter Mulden 14 0,50 mm (Figuren 2 und 5) und der Abstand A2 der Muldenböden 15 von den Kanalsohlen 12 beträgt 0,01 mm. Die Mulden 14 haben eine Tiefe T1 von 0,25 mm (Figuren 4 und 5).As particularly illustrated in FIGS. 3 and 5, each
Wie die Figur 5 in bewußt übertriebener Darstellung anhand des Wellenkamms der Rippen 7 erkennen läßt, sind die Oberflächen 8, 10, 11 der Rippen 7, d.h. die Kopfbereiche 10, die Flanken 8 und die Übergänge 11 von den Flanken 8 auf die Kanalsohlen 12, ggf. aber auch die Kanalsohlen 12, mit einer Mikrorauhigkeit 16 versehen, deren Tiefe T 0,005 mm beträgt.As can be seen in FIG. 5 in a deliberately exaggerated representation based on the wave crest of the
Die Herstellung der Mikrorauhigkeit 16 erfolgt beim Ausführungsbeispiel unmittelbar beim Walzprägen. Dazu ist die Prägewalze mittels einer Bestrahlung durch Korunde mit einer negativen diffusen Oberflächenstruktur versehen worden, die dann die Erzeugung der Oberflächenstruktur an der späteren inneren Oberfläche 3 des Austauscherrohrs 1 gewährleistet.In the exemplary embodiment, the
Aufgrund der strukturierten inneren Oberfläche 3 hat das in Figur 1 veranschaulichte Austauscherrohr 1 im Vergleich nicht nur zu einem Austauscherrohr mit einer glatten inneren Oberfläche, sondern auch zu einem innen gerillten Austauscherrohr einen wesentlich besseren Wärmedurchgangskoeffizienten k' (W/mK).Due to the structured
Dieser Sachverhalt ist aus den aufgrund vergleichender Untersuchungen erstellten Diagrammen gemäß den Figuren 6 und 7 ohne zusätzliche Erläuterungen erkennbar (Figur 6 -Kondensation, Fig. 7 - Verdampfung).This fact can be seen from the diagrams according to FIGS. 6 and 7 drawn up on the basis of comparative investigations without additional explanations (FIG. 6 —condensation, FIG. 7 — evaporation).
- 1 -1 -
- AustauscherrohrExchanger tube
- 2 -2 -
- äußere Oberfläche v. 1outer surface v. 1
- 3 -3 -
- innere Oberfläche v. 1inner surface v. 1
- 4 -4 -
- BlechbandMetal strip
- 5 -5 -
- Randbereiche v. 4Marginal areas v. 4th
- 6 -6 -
- Längsachse v. 1Longitudinal axis v. 1
- 7 -7 -
- RippenRibs
- 8 -8th -
- Flanken v. 7Flanks v. 7
- 9 -9 -
- Basisabschnitt v. 4Base section v. 4th
- 10 -10 -
- Kopfbereiche v. 7Head areas v. 7
- 11 -11 -
- Übergänge v. 8 auf 12Transitions v. 8 on 12
- 12 -12 -
- KanalsohlenChannel soles
- 13 -13 -
- Kanälechannels
- 14 -14 -
- MuldenHopper
- 15 -15 -
- MuldenbödenTrough floors
- 16 -16 -
- MikrorauhigkeitMicro roughness
- A -A -
-
Abstand zweier benachbarter Rippen 7Distance between two
adjacent ribs 7 - A1 -A1 -
-
Abstand zweier benachbarter MLE auf einer Rippe 7Distance between two adjacent MLE on a
rib 7 - A2 -A2 -
- Abstand v. 12 zu 15Distance from 12 to 15
- D -D -
- Außendurchmesser v. 1Outer diameter of 1
- D1 -D1 -
- Dicke v. 9Thickness v. 9
- H -H -
- Höhe v. 7Height of 7
- LR -LR -
- Längsrichtung v. 7Longitudinal direction v. 7
- MLE-MLE-
-
Mittellängsebenen direkt benachbarter Mulden 14 auf verschiedenen Rippen 7Middle longitudinal planes of directly
adjacent troughs 14 ondifferent ribs 7 - T -T -
- Tiefe v. 16Depth of 16
- T1 -T1 -
- Tiefe v. 14Depth of 14
- α -α -
- Winkel zw. 6 u. 7Angle between 6 u. 7
- β -β -
- Flankenwinkel v. 7Flank angle v. 7
- γ -γ -
- Winkel zw. 6 u. MLEAngle between 6 u. MLE
- δ -δ -
- Winkel zw. LR u. MLEAngle between LR and MLE
Claims (15)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19510124A DE19510124A1 (en) | 1995-03-21 | 1995-03-21 | Exchanger tube for a heat exchanger |
DE19510124 | 1995-03-21 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0733871A1 true EP0733871A1 (en) | 1996-09-25 |
EP0733871B1 EP0733871B1 (en) | 2000-02-02 |
Family
ID=7757210
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96103390A Expired - Lifetime EP0733871B1 (en) | 1995-03-21 | 1996-03-05 | Heat transfer tube for a heat exchanger |
Country Status (9)
Country | Link |
---|---|
US (1) | US5682946A (en) |
EP (1) | EP0733871B1 (en) |
JP (1) | JPH08327273A (en) |
AT (1) | ATE189518T1 (en) |
DE (2) | DE19510124A1 (en) |
DK (1) | DK0733871T3 (en) |
ES (1) | ES2143102T3 (en) |
GR (1) | GR3033193T3 (en) |
PT (1) | PT733871E (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0819908A3 (en) * | 1996-07-19 | 1999-06-09 | Alcan Alluminio S.p.A. | Rolled section for the realization of heat exchangers and relevant production method |
EP1202018A3 (en) * | 2000-10-27 | 2004-04-07 | Alcoa Inc. | Micro-textured heat transfer surfaces |
EP1734327A1 (en) * | 2005-06-17 | 2006-12-20 | Behr GmbH & Co. KG | Heat exchanger in particular sorption, or reaction heat exchanger and/or heat pipe. |
EP2554292A1 (en) * | 2011-08-05 | 2013-02-06 | Witzenmann GmbH | Conduit element with surface structure and method for production and use of such a conduit element |
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DE19612470A1 (en) * | 1996-03-28 | 1997-10-02 | Km Europa Metal Ag | Exchanger tube |
US5785088A (en) * | 1997-05-08 | 1998-07-28 | Wuh Choung Industrial Co., Ltd. | Fiber pore structure incorporate with a v-shaped micro-groove for use with heat pipes |
US6182743B1 (en) | 1998-11-02 | 2001-02-06 | Outokumpu Cooper Franklin Inc. | Polyhedral array heat transfer tube |
US6176301B1 (en) | 1998-12-04 | 2001-01-23 | Outokumpu Copper Franklin, Inc. | Heat transfer tube with crack-like cavities to enhance performance thereof |
AU6563500A (en) * | 1999-07-14 | 2001-01-30 | Fitr Gesellschaft Fur Innovation Im Tief- Und Rohrleitungsbau Weimar M.b.H. | Conduits and conduit elements for transporting flowable media |
US6254631B1 (en) | 1999-09-23 | 2001-07-03 | Intratherapeutics, Inc. | Stent with enhanced friction |
FR2837270B1 (en) * | 2002-03-12 | 2004-10-01 | Trefimetaux | GROOVED TUBES FOR REVERSIBLE USE FOR HEAT EXCHANGERS |
EP1845327B1 (en) * | 2002-06-10 | 2008-10-29 | Wolverine Tube Inc. | Method of manufacturing a heat transfer tube |
US8573022B2 (en) * | 2002-06-10 | 2013-11-05 | Wieland-Werke Ag | Method for making enhanced heat transfer surfaces |
US7311137B2 (en) * | 2002-06-10 | 2007-12-25 | Wolverine Tube, Inc. | Heat transfer tube including enhanced heat transfer surfaces |
US20040099409A1 (en) * | 2002-11-25 | 2004-05-27 | Bennett Donald L. | Polyhedral array heat transfer tube |
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US20060112535A1 (en) * | 2004-05-13 | 2006-06-01 | Petur Thors | Retractable finning tool and method of using |
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JP4554557B2 (en) * | 2006-06-13 | 2010-09-29 | トヨタ自動車株式会社 | Cooler |
CN100547339C (en) * | 2008-03-12 | 2009-10-07 | 江苏萃隆精密铜管股份有限公司 | A kind of intensify heat transfer pipe and preparation method thereof |
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CN103851945B (en) * | 2012-12-07 | 2017-05-24 | 诺而达奥托铜业(中山)有限公司 | Internal threaded pipe with rough internal surface |
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US9638413B2 (en) | 2014-03-05 | 2017-05-02 | Progreen Labs, Llc | Treatment device of a heating system |
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US9593857B2 (en) | 2014-03-07 | 2017-03-14 | ProGreen Labs, LLC. | Heating system |
USD1009227S1 (en) | 2016-08-05 | 2023-12-26 | Rls Llc | Crimp fitting for joining tubing |
JP6663899B2 (en) * | 2017-11-29 | 2020-03-13 | 本田技研工業株式会社 | Cooling system |
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- 1996-03-05 DK DK96103390T patent/DK0733871T3/en active
- 1996-03-05 ES ES96103390T patent/ES2143102T3/en not_active Expired - Lifetime
- 1996-03-05 DE DE59604338T patent/DE59604338D1/en not_active Expired - Lifetime
- 1996-03-05 AT AT96103390T patent/ATE189518T1/en active
- 1996-03-05 EP EP96103390A patent/EP0733871B1/en not_active Expired - Lifetime
- 1996-03-12 JP JP8054811A patent/JPH08327273A/en active Pending
- 1996-03-18 US US08/617,466 patent/US5682946A/en not_active Expired - Lifetime
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Cited By (5)
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---|---|---|---|---|
EP0819908A3 (en) * | 1996-07-19 | 1999-06-09 | Alcan Alluminio S.p.A. | Rolled section for the realization of heat exchangers and relevant production method |
EP1202018A3 (en) * | 2000-10-27 | 2004-04-07 | Alcoa Inc. | Micro-textured heat transfer surfaces |
US6925711B2 (en) | 2000-10-27 | 2005-08-09 | Alcoa Inc. | Micro-textured heat transfer surfaces |
EP1734327A1 (en) * | 2005-06-17 | 2006-12-20 | Behr GmbH & Co. KG | Heat exchanger in particular sorption, or reaction heat exchanger and/or heat pipe. |
EP2554292A1 (en) * | 2011-08-05 | 2013-02-06 | Witzenmann GmbH | Conduit element with surface structure and method for production and use of such a conduit element |
Also Published As
Publication number | Publication date |
---|---|
ES2143102T3 (en) | 2000-05-01 |
GR3033193T3 (en) | 2000-08-31 |
EP0733871B1 (en) | 2000-02-02 |
DK0733871T3 (en) | 2000-07-24 |
US5682946A (en) | 1997-11-04 |
PT733871E (en) | 2000-06-30 |
DE59604338D1 (en) | 2000-03-09 |
DE19510124A1 (en) | 1996-09-26 |
ATE189518T1 (en) | 2000-02-15 |
JPH08327273A (en) | 1996-12-13 |
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