EP0357907A1 - Heat exchanger - Google Patents
Heat exchanger Download PDFInfo
- Publication number
- EP0357907A1 EP0357907A1 EP19890112632 EP89112632A EP0357907A1 EP 0357907 A1 EP0357907 A1 EP 0357907A1 EP 19890112632 EP19890112632 EP 19890112632 EP 89112632 A EP89112632 A EP 89112632A EP 0357907 A1 EP0357907 A1 EP 0357907A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heat exchanger
- fluid
- outlet
- valve
- overflow pipe
- 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
Links
- 239000012530 fluid Substances 0.000 claims abstract description 44
- 239000002918 waste heat Substances 0.000 claims description 2
- 230000004048 modification Effects 0.000 abstract 1
- 238000012986 modification Methods 0.000 abstract 1
- 230000035515 penetration Effects 0.000 abstract 1
- 238000009413 insulation Methods 0.000 description 5
- 230000001914 calming effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
- F28F27/02—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus for controlling the distribution of heat-exchange media between different channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1884—Hot gas heating tube boilers with one or more heating tubes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B35/00—Control systems for steam boilers
- F22B35/007—Control systems for waste heat boilers
Definitions
- the invention relates to a heat exchanger, in particular waste heat steam generator, with heat exchanger tubes running between two end chambers, through which a fluid involved in the heat exchange flows and flowed against by another fluid supplied to the housing surrounding the heat exchanger tubes, and with one parallel to the chambers
- a heat exchanger of the type described above is known from DE-PS 28 46 455.
- the outlet-side chamber of the heat exchanger is separated by a partition running perpendicular to the heat exchanger tubes wall divided into an outflow and a mixing room.
- this mixing chamber the partial flow emerging from the heat exchanger tubes is mixed with the partial flow of the same fluid passing through the overflow tube, the respective proportions of the two partial flows being set by the position of the valve arrangement.
- This known embodiment has the disadvantage that the mixing of the two sub-streams is associated with a high pressure loss and that a relatively large mixing space must be provided in order to achieve a reasonably satisfactory mixing of the two sub-streams without it being possible to ensure that the out the fluid flow exiting the outlet connection of the heat exchanger does not consist of a hot core flow and a colder edge flow.
- the invention has for its object to provide a heat exchanger of the type described above, the mixing device formed at the outlet end of the overflow pipe guarantees low-loss and intensive mixing of the partial flows with a significantly reduced space requirement for the mixing section.
- the solution to this problem by the invention is characterized in that the outlet opening of the outlet-side heat exchanger chamber is formed on a collecting cone which interacts with the valve ring, and that the valve ring is provided with a conical outlet surface provided with a plurality of through-openings, the inclination of which The longitudinal axis of the heat exchanger corresponds approximately to the inclination of the collecting cone.
- a mixing device is created in which the partial flow emerging from the heat exchanger tubes is specifically fed through the collecting cone to the outlet opening of the end chamber, this partial flow passing through an annular flow cross section which is formed on the one hand by the wall of the collecting cone and on the other hand by the valve ring becomes.
- the partial flow of the same fluid that emerges from the overflow pipe is introduced into this partial flow directed towards the outlet opening by the inclination of the collecting cone. Since this outlet takes place from a conical outlet surface of the valve ring, the inclination of which to the longitudinal axis of the heat exchanger roughly corresponds to the inclination of the collecting cone, this results in intensive mixing of the two partial flows within a short mixing section.
- the conical outlet surface is provided with a large number of through openings which divide the fluid emerging from the overflow pipe into a large number of small flow threads, which are distributed over the annular flow cross section between the collecting cone and the conical outlet surface and are mixed into the partial flow coming from the heat exchanger pipes.
- the quantitative change in the two partial flows can - as is known - be carried out by adjusting the valve ring relative to the collecting cone on the one hand and the valve plate relative to the overflow pipe on the other hand, so that a predetermined outlet temperature of one of the two fluids participating in the heat exchange can be kept constant within narrow limits.
- the outlet-side chamber is formed by the collecting cone, the outlet opening of which is at the same time designed as an outlet connection of the heat exchanger. If a sufficiently large space is available and / or a type of calming zone is to be formed after the mixing section, the collecting cone can, according to a further feature of the invention, also be arranged within the outlet-side chamber, which in turn is provided with an outlet nozzle.
- the shortened heat exchanger shown in Fig.1 has a cylindrical housing 1, at one end of which an inlet chamber 2 with insulation 2a for the heat-emitting fluid F 1 is arranged.
- This fluid F1 is passed through heat exchanger tubes 3, which extend between the inlet chamber 2 and an outlet-side chamber 4.
- the cooled fluid F1 leaves the outlet chamber 4 through an outlet 4a.
- the heat-absorbing fluid F2 is supplied to the housing 1 surrounding the heat exchanger tubes 3 through a nozzle 1a. It acts on the heat exchanger tubes from the outside and, after being heated, leaves the housing 1 through a connector 1b.
- the inlet chamber 2 and the outlet-side chamber 4 are connected to one another parallel to the heat exchanger tubes 3 by an overflow tube 5, which is provided with insulation 5a.
- an overflow tube 5 which is provided with insulation 5a.
- a valve arrangement is formed, which is shown enlarged in Figures 2 and 3.
- This valve arrangement comprises a valve plate 6, with which the flow cross section of the overflow pipe 5 can be completely closed in one end position and which is arranged on a valve rod 7.
- a valve ring 8 is also attached, which is flowed through by the fluid F 1 leaving the overflow pipe 5 and which closes an outlet opening 9 in the other end position of the valve arrangement, which is formed in a collecting cone 10.
- This collecting cone 10 is arranged in the outlet-side chamber 4 in such a way that the outlet openings of all the heat exchanger tubes 3 open out inside the collecting cone 10. In this way, the collection cone 10 and its outlet opening 9 flows through the entirety of that portion of the fluid F 1 that exits the heat exchanger tubes 3.
- the valve rod 7 is actuated by a servomotor 11 which is arranged on the outside of the outlet-side chamber 4.
- a servomotor 11 which is arranged on the outside of the outlet-side chamber 4.
- the valve rod 7 can be transferred into two end positions and all intermediate positions.
- the valve plate 6 closes the entire cross section of the overflow pipe 5.
- the heat-emitting fluid F 1 flows through the heat exchanger pipes 3; it enters the collecting cone 10 and leaves it through the outlet opening 9.
- the valve plate 6 releases the flow cross section of the overflow pipe 5, whereas the valve ring 8 rests on the collecting cone 10 in an area which surrounds the outlet opening 9.
- the heat exchanger tubes 3 are closed on their outlet side by the backwater; the heat-emitting fluid F1 flows completely through the overflow pipe 5 and passes through the interior of the valve ring 8 into the outlet opening 9. Since the overflow pipe 5 is provided with insulation 5a, heat exchange between the heat-emitting fluid F1 and the heat-absorbing fluid F2 is in this end position almost prevented.
- valve assembly described above can therefore be used to control either the outlet temperature of the fluid F1 or the fluid F2 within narrow limits.
- valve ring 8 In order to bring about a thorough mixing of that portion of the heat-emitting fluid F 1 that emerges from the heat exchanger tubes 3 with the portion that leaves the overflow tube 5, the valve ring 8 is provided with a conical outlet surface 8 a, which is provided with a plurality of through openings 8 b Inclination to the longitudinal axis of the heat exchanger corresponds approximately to the inclination of the collecting cone 10 to this longitudinal axis of the heat exchanger. In this way - as can be seen in FIGS. 2 and 3 - good mixing of the two partial flows is produced before they leave the outlet opening 9 of the collecting cone 10.
- the partial quantity emerging from the overflow pipe 5 is bundled through the through openings 8b in the manner of a shower Partial stream injected, which emerges from the collecting cone 10. In this way it is prevented that 9 strands of the heat-emitting fluid F 1 emerge from the outlet opening at very different temperatures.
- the outlet-side chamber 4 is therefore only provided to make the flow more uniform, without mixing of the two partial flows of the heat-emitting fluid F 1 taking place in this outlet-side chamber 4.
- valve arrangement in the exemplary embodiment according to FIG. 3 corresponds to the valve arrangement in the first exemplary embodiment according to FIGS. 1 and 2.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Multiple-Way Valves (AREA)
Abstract
Description
Die Erfindung betrifft einen Wärmetauscher, insbesondere Abhitze-Dampferzeuger, mit zwischen zwei endseitigen Kammern verlaufenden Wärmetauscherrohren, die von einem am Wärmeaustausch beteiligten Fluid durchströmt und von einem anderen, dem die Wärmetauscherrohre umgebenden Gehäuse zugeführten Fluid angeströmt werden, sowie mit einem die Kammern parallel zu den Wärmetauscherrohren verbindenden Überströmrohr, durch das insbesondere zur Aufrechterhaltung einer vorgebbaren Austrittstemperatur eines der beiden Fluids ein veränderlicher Teilstrom des zwischen den Kammern strömenden Fluids unter wesentlicher Vermeidung des Wärmeaustauschs mit dem anderen Fluid hindurchführbar ist und das zur Veränderung seines Strömungsquerschnitts mit einer Ventilanordnung versehen ist, die einen den Strömungsquerschnitt des Überströmrohres in der einen Endstellung der Ventilanordnung verschließenden Ventilteller und einen mit dem Ventilteller über eine Ventilstange verbundenen Ventilring umfaßt, der von dem das Überströmrohr verlassenden Fluid durchströmt wird und in der anderen Endstellung der Ventilanordnung eine in der austrittsseitigen Kammer ausgebildete Öffnung für das aus den Wärmetauscherrohren austretende Fluid verschließt.The invention relates to a heat exchanger, in particular waste heat steam generator, with heat exchanger tubes running between two end chambers, through which a fluid involved in the heat exchange flows and flowed against by another fluid supplied to the housing surrounding the heat exchanger tubes, and with one parallel to the chambers Overflow pipe connecting heat exchanger tubes, through which a variable partial flow of the fluid flowing between the chambers can be passed, in particular to maintain a predeterminable outlet temperature of one of the two fluids, while essentially avoiding heat exchange with the other fluid, and which is provided with a valve arrangement for changing its flow cross-section, one the flow cross-section of the overflow pipe in the one end position of the valve arrangement closing valve plate and connected to the valve plate via a valve rod en comprises a valve ring through which the fluid leaving the overflow pipe flows and in the other end position of the valve arrangement closes an opening formed in the outlet-side chamber for the fluid emerging from the heat exchanger tubes.
Ein Wärmetauscher der voranstehend beschriebenen Art ist aus der DE-PS 28 46 455 bekannt. Bei dieser bekannten Ausführung wird die austrittsseitige Kammer des Wärmetauschers durch eine senkrecht zu den Wärmetauscherrohren verlaufende Trenn wand in einen Ausströmraum und einen Mischraum unterteilt. In diesem Mischraum wird der aus den Wärmetauscherrohren austretende Teilstrom mit dem das Überströmrohr passierenden Teilstrom desselben Fluids gemischt, wobei die jeweiligen Anteile der beiden Teilströme durch die Stellung der Ventilanordnung eingestellt werden.A heat exchanger of the type described above is known from DE-PS 28 46 455. In this known embodiment, the outlet-side chamber of the heat exchanger is separated by a partition running perpendicular to the heat exchanger tubes wall divided into an outflow and a mixing room. In this mixing chamber, the partial flow emerging from the heat exchanger tubes is mixed with the partial flow of the same fluid passing through the overflow tube, the respective proportions of the two partial flows being set by the position of the valve arrangement.
Diese bekannte Ausführung hat den Nachteil, daß die Vermischung der beiden Teilströme mit einem hohen Druckverlust verbunden ist und daß ein verhältnismäßig großer Mischraum vorgesehen werden muß, um eine einigermaßen zufriedenstellende Vermischung der beiden Teilströme zu erzielen, ohne daß hierbei sichergestellt werden kann, daß der aus dem Austrittstutzen des Wärmetauschers austretende Fluidstrom nicht aus einer heißen Kernströmung und einer kälteren Randströmung besteht.This known embodiment has the disadvantage that the mixing of the two sub-streams is associated with a high pressure loss and that a relatively large mixing space must be provided in order to achieve a reasonably satisfactory mixing of the two sub-streams without it being possible to ensure that the out the fluid flow exiting the outlet connection of the heat exchanger does not consist of a hot core flow and a colder edge flow.
Der Erfindung liegt die Aufgabe zugrunde, einen Wärmetauscher der eingangs beschriebenen Art zu schaffen, dessen am austrittsseitigen Ende des Überströmrohres ausgebildete Mischeinrichtung eine verlustarme und intensive Vermischung der Teilströme bei erheblich verringertem Raumbedarf für die Mischstrecke garantiert.The invention has for its object to provide a heat exchanger of the type described above, the mixing device formed at the outlet end of the overflow pipe guarantees low-loss and intensive mixing of the partial flows with a significantly reduced space requirement for the mixing section.
Die Lösung dieser Aufgabenstellung durch die Erfindung ist dadurch gekennzeichnet, daß die Austrittsöffnung der austrittsseitigen Wärmetauscherkammer an einem Sammelkonus ausgebildet ist, der mit dem Ventilring zusammenwirkt, und daß der Ventilring mit einer kegelförmigen, mit einer Vielzahl von Durchtrittsöffnungen versehenen Austrittsfläche versehen ist, deren Neigung zur Wärmetauscherlängsachse etwa der Neigung des Sammelkonus entspricht.The solution to this problem by the invention is characterized in that the outlet opening of the outlet-side heat exchanger chamber is formed on a collecting cone which interacts with the valve ring, and that the valve ring is provided with a conical outlet surface provided with a plurality of through-openings, the inclination of which The longitudinal axis of the heat exchanger corresponds approximately to the inclination of the collecting cone.
Mit dieser erfindungsgemäßen Ausbildung wird eine Mischeinrichtung geschaffen, bei der der aus den Wärmetauscherrohren austretende Teilstrom durch den Sammelkonus gezielt der Austrittsöffnung der endseitigen Kammer zugeführt wird, wobei dieser Teilstrom einen ringförmigen Strömungsquerschnitt passiert, der einerseits durch die Wand des Sammelkonus und andererseits durch den Ventilring gebildet wird. In diesen durch die Neigung des Sammelkonus gezielt zur Austrittsöffnung gerichteten Teilstrom wird derjenige Teilstrom desselben Fluids eingeleitet, der aus dem Überströmrohr austritt. Da dieser Austritt aus einer kegelförmigen Austrittsfläche des Ventilringes erfolgt, deren Neigung zur Wärmetauscherlängsachse etwa der Neigung des Sammelkonus entspricht, ergibt sich eine intensive Vermischung der beiden Teilströme innerhalb einer kurzen Mischstrecke. Zu diesem Zweck ist die kegelförmige Austrittsfläche mit einer Vielzahl von Durchtrittsöffnungen versehen, die das aus dem Überströmrohr austretende Fluid in eine Vielzahl kleiner Strömungsfäden aufteilt, die verteilt über den ringförmigen Strömungsquerschnitt zwischen Sammelkonus und kegelförmiger Austrittsfläche in den aus den Wärmetauscherrohren kommenden Teilstrom eingemischt werden. Es erfolgt somit sowohl eine intensive als auch eine verlustarme Durchmischung der beiden Teilströme innerhalb einer sehr kurzen Mischstrecke, so daß für den Mischvorgang nur ein geringer Raumbedarf besteht.With this embodiment according to the invention, a mixing device is created in which the partial flow emerging from the heat exchanger tubes is specifically fed through the collecting cone to the outlet opening of the end chamber, this partial flow passing through an annular flow cross section which is formed on the one hand by the wall of the collecting cone and on the other hand by the valve ring becomes. The partial flow of the same fluid that emerges from the overflow pipe is introduced into this partial flow directed towards the outlet opening by the inclination of the collecting cone. Since this outlet takes place from a conical outlet surface of the valve ring, the inclination of which to the longitudinal axis of the heat exchanger roughly corresponds to the inclination of the collecting cone, this results in intensive mixing of the two partial flows within a short mixing section. For this purpose, the conical outlet surface is provided with a large number of through openings which divide the fluid emerging from the overflow pipe into a large number of small flow threads, which are distributed over the annular flow cross section between the collecting cone and the conical outlet surface and are mixed into the partial flow coming from the heat exchanger pipes. This results in both intensive and low-loss mixing of the two partial flows within a very short mixing section, so that the mixing process takes up little space.
Die mengenmäßige Veränderung der beiden Teilströme kann - wie bekannt - durch eine Verstellung einerseits des Ventilringes gegenüber dem Sammelkonus und andererseits des Ventiltellers gegenüber dem Überströmrohr erfolgen, so daß eine vorgegebene Austrittstemperatur eines der beiden am Wärmeaustausch teilnehmenden Fluids innerhalb enger Grenzen konstant gehalten werden kann.The quantitative change in the two partial flows can - as is known - be carried out by adjusting the valve ring relative to the collecting cone on the one hand and the valve plate relative to the overflow pipe on the other hand, so that a predetermined outlet temperature of one of the two fluids participating in the heat exchange can be kept constant within narrow limits.
Bei einer bevorzugten Weiterbildung der Erfindung wird die austrittseitige Kammer durch den Sammelkonus gebildet, dessen Austrittsöffnung zugleich als Austrittstutzen des Wärmetauschers ausgeführt ist. Sofern ein ausreichend großer Raum zur Verfügung steht und/oder nach der Mischstrecke eine Art Beruhigungszone ausgebildet werden soll, kann der Sammelkonus gemäß einem weiteren Merkmal der Erfindung auch innerhalb der austrittseitigen Kammer angeordnet sein, die ihrerseits mit einem Austrittstutzen versehen ist.In a preferred development of the invention, the outlet-side chamber is formed by the collecting cone, the outlet opening of which is at the same time designed as an outlet connection of the heat exchanger. If a sufficiently large space is available and / or a type of calming zone is to be formed after the mixing section, the collecting cone can, according to a further feature of the invention, also be arranged within the outlet-side chamber, which in turn is provided with an outlet nozzle.
Auf der Zeichnung sind zwei Ausführungsbeispiele des erfindungsgemäßen Wärmetauschers dargestellt, und zwar zeigen:
- Fig. 1 einen Längsschnitt durch ein Ausführungsbeispiel eines schematisch dargestellten Wärmetauschers,
- Fig. 2 eine vergrößerte Darstellung der Ventilanordnung nach Fig.1 und
- Fig. 3 eine der Fig.2 entsprechende Darstellung einer zweiten Ausführungsform.
- 1 shows a longitudinal section through an embodiment of a schematically illustrated heat exchanger,
- Fig. 2 is an enlarged view of the valve assembly of Fig.1 and
- 3 a representation corresponding to FIG. 2 of a second embodiment.
Der in Fig.1 verkürzt dargestellte Wärmetauscher hat ein zylindrisches Gehäuse 1, an dessen einem Ende eine mit einer Isolierung 2a versehene Eintrittskammer 2 für das wärmeabgebende Fluid F₁ angeordnet ist. Dieses Fluid F₁ wird durch Wärmetauscherrohre 3 geführt, die sich zwischen der Eintrittskammer 2 und einer austrittseitigen Kammer 4 erstrecken. Das abgekühlte Fluid F₁ verläßt die austrittseitige Kammer 4 durch einen Austrittstutzen 4a. Das wärmeaufnehmende Fluid F₂ wird dem die Wärmetauscherrohre 3 umgebenden Gehäuse 1 durch einen Stutzen 1a zugeführt. Es beaufschlagt die Wärmetauscherrohre von außen und verläßt nach seiner Aufheizung das Gehäuse 1 durch einen Stutzen 1b.The shortened heat exchanger shown in Fig.1 has a
Die Eintrittskammer 2 und die austrittseitige Kammer 4 sind miteinander parallel zu den Wärmetauscherrohren 3 durch ein Überströmrohr 5 verbunden, das mit einer Isolierung 5a versehen ist. Am austrittseitigen Ende dieses Überströmrohres 5 ist eine Ventilanordnung ausgebildet, die vergrößert in den Figuren 2 und 3 dargestellt ist.The
Diese Ventilanordnung umfaßt einen Ventilteller 6, mit dem in der einen Endstellung der Strömungsquerschnitt des Überströmrohres 5 vollständig verschlossen werden kann und der an einer Ventilstange 7 angeordnet ist. An dieser Ventilstange 7 ist weiterhin ein Ventilring 8 befestigt, der von dem das Überströmrohr 5 verlassenden Fluid F₁ durchströmt wird und der in der anderen Endstellung der Ventilanordnung eine Austrittsöffnung 9 verschließt, die in einem Sammelkonus 10 ausgebildet ist. Dieser Sammelkonus 10 ist derart in der austrittseitigen Kammer 4 angeordnet, daß die Austrittsöffnungen sämtlicher Wärmetauscherrohre 3 innerhalb des Sammelkonus 10 münden. Auf diese Weise wird der Sammelkonus 10 und seine Austrittsöffnung 9 von der Gesamtheit desjenigen Anteils des Fluids F₁ durchströmt, das aus den Wärmetauscherrohren 3 austritt.This valve arrangement comprises a
Die Ventilstange 7 wird von einem Stellmotor 11 betätigt, der auf der Außenseite der austrittseitigen Kammer 4 angeordnet ist. Mittels dieses Stellmotors 11 kann die Ventilstange 7 in zwei Endstellungen und sämtliche Zwischenstellungen überführt werden. In der einen Endstellung verschließt der Ventilteller 6 den gesamten Querschnitt des Überströmrohres 5. In dieser Endstellung strömt das wärmeabgebende Fluid F₁ insgesamt durch die Wärmetauscherrohre 3; es gelangt in den Sammelkonus 10 und verläßt diesen durch die Austrittsöffnung 9. In der anderen Endstellung gibt der Ventilteller 6 den Strömungsquerschnitt des Überströmrohres 5 frei, wogegen der Ventil ring 8 am Sammelkonus 10 in einem Bereich anliegt, der die Austrittsöffnung 9 umgibt. Auf diese Weise werden die Wärmetauscherrohre 3 auf ihrer Austrittsseite durch den Rückstau verschlossen; das wärmeabgebende Fluid F₁ strömt vollständig durch das Überströmrohr 5 und gelangt durch das Innere des Ventilringes 8 in die Austrittsöffnung 9. Da das Überströmrohr 5 mit einer Isolierung 5a versehen ist, wird in dieser Endstellung ein Wärmeaustausch zwischen dem wärmeabgebenden Fluid F₁ und dem wärmeaufnehmenden Fluid F₂ nahezu verhindert.The
Durch die Zwischenstellungen, die stufenlos zwischen diesen beiden voranstehend beschriebenen Endstellungen mittels des Stellmotors 11 über die Ventilstange 7 eingestellt werden können, kann diejenige Teilmenge vorbestimmt werden, die am Wärmeaustausch teilnimmt, wogegen die andere Teilmenge nahezu vom Wärmeaustausch ausgeschlossen wird. Die voranstehend beschriebene Ventilanordnung kann demzufolge dazu benutzt werden, entweder die Austrittstemperatur des Fluids F₁ oder des Fluids F₂ in engen Grenzen zu regeln.Due to the intermediate positions, which can be continuously adjusted between these two end positions described above by means of the
Um eine gute Durchmischung derjenigen Teilmenge des wärmeabgebenden Fluids F₁, die aus den Wärmetauscherrohren 3 austritt, mit der Teilmenge zu bewirken, die das Überströmrohr 5 verläßt, ist der Ventilring 8 mit einer kegelförmigen, mit einer Vielzahl von Durchtrittsöffnungen 8b versehenen Austrittsfläche 8a versehen, deren Neigung zur Wärmetauscherlängsachse etwa der Neigung des Sammelkonus 10 zu dieser Wärmetauscherlängsachse entspricht. Auf diese Weise wird - wie in den Figuren 2 und 3 zu erkennen - eine gute Durchmischung der beiden Teilströme erzeugt, bevor diese die Austrittsöffnung 9 des Sammelkonus 10 verlassen. Die aus dem Überströmrohr 5 austretende Teilmenge wird durch die Durchtrittsöffnungen 8b in der Art einer Dusche in den gebündelten Teilstrom eingedüst, der aus dem Sammelkonus 10 austritt. Auf diese Weise wird verhindert, daß aus der Austrittsöffnung 9 Strähnen des wärmeabgebenden Fluids F₁ mit sehr unterschiedlicher Temperatur austreten. Beim Ausführungsbeispiel nach den Figuren 1 und 2 ist die austrittseitige Kammer 4 deshalb lediglich zur Vergleichmäßigung der Strömung vorgesehen, ohne daß in dieser austrittseitigen Kammer 4 eine Vermischung der beiden Teilströme des wärmeabgebenden Fluids F₁ stattfindet.In order to bring about a thorough mixing of that portion of the heat-emitting
Durch die intensive Vermischung der beiden Teilströme des Fluids F₁ im Bereich der Austrittsöffnung 9 ist es möglich, gemäß der Ausführungsform nach Fig.3 vollständig auf die austrittseitige Kammer 4 zu verzichten und den Austrittstutzen 4a unmittelbar an die Austrittsöffnung 9 anzuschließen, wie dies Fig.3 zeigt. Ansonsten entspricht die Ventilanordnung beim Ausführungsbeispiel nach Fig.3 der Ventilanordnung des ersten Ausführungsbeispiels gemäß den Figuren 1 und 2.Due to the intensive mixing of the two partial flows of the
- F₁ wärmeabgebendes FluidF₁ heat releasing fluid
- F₂ wärmeaufnehmendes FluidF₂ heat absorbing fluid
- 1 Gehäuse1 housing
- 1a Stutzen1a nozzle
- 1b Stutzen1b nozzle
- 2 Eintrittskammer2 entry chamber
- 2a Isolierung2a insulation
- 3 Wärmetauscherrohr3 heat exchanger tube
- 4 austrittseitige Kammer4 exit chamber
- 4a Austrittstutzen4a outlet connection
- 5 Überströmrohr5 overflow pipe
- 5a Isolierung5a insulation
- 6 Ventilteller6 valve plates
- 7 Ventilstange7 valve rod
- 8 Ventilring8 valve ring
- 8a Austrittsfläche8a exit surface
- 8b Durchtrittsöffnung8b passage opening
- 9 Austrittsöffnung9 outlet opening
- 10 Sammelkonus10 collecting cone
- 11 Stellmotor11 servomotor
Claims (3)
dadurch gekennzeichnet,
daß die Austrittsöffnung (9) an einem Sammelkonus (10) ausgebildet ist, der mit dem Ventilring (8) zusammenwirkt, und daß der Ventilring (8) mit einer kegelförmigen, mit einer Vielzahl von Durchtrittsöffnungen (8b) versehenen Austrittsfläche (8a) versehen ist, deren Neigung zur Wärmetauscherlängsachse etwa der Neigung des Sammelkonus (10) entspricht.1. Heat exchanger, in particular waste heat steam generator, with heat exchanger tubes running between two end chambers, through which a fluid involved in the heat exchange flows and flowed against by another fluid supplied to the housing surrounding the heat exchanger tubes, and with a fluid connecting the chambers parallel to the heat exchanger tubes Overflow pipe, through which a variable partial flow of the fluid flowing between the chambers can be passed, in particular to maintain a predeterminable outlet temperature of one of the two fluids, while essentially avoiding heat exchange with the other fluid, and which is provided with a valve arrangement for changing its flow cross-section, which has a flow cross-section of the overflow pipe in the one end position of the valve arrangement closing valve plate and a valve ring connected to the valve plate via a valve rod, which of the fluid flowing through the overflow pipe and in the other end position of the valve arrangement closes an opening formed in the outlet-side chamber for the fluid emerging from the heat exchanger pipes,
characterized,
that the outlet opening (9) is formed on a collecting cone (10) which cooperates with the valve ring (8), and that the valve ring (8) is provided with a conical outlet surface (8a) provided with a plurality of through openings (8b) , whose inclination to the heat exchanger longitudinal axis corresponds approximately to the inclination of the collecting cone (10).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19883830248 DE3830248C1 (en) | 1988-09-06 | 1988-09-06 | |
DE3830248 | 1988-09-06 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0357907A1 true EP0357907A1 (en) | 1990-03-14 |
EP0357907B1 EP0357907B1 (en) | 1991-11-13 |
Family
ID=6362368
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19890112632 Expired - Lifetime EP0357907B1 (en) | 1988-09-06 | 1989-07-11 | Heat exchanger |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0357907B1 (en) |
DE (1) | DE3830248C1 (en) |
ES (1) | ES2027812T3 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0617230A1 (en) * | 1993-03-26 | 1994-09-28 | Haldor Topsoe A/S | Waste heat boiler |
EP0690262A1 (en) * | 1994-06-29 | 1996-01-03 | Haldor Topsoe A/S | Waste heat boiler |
WO1999064806A1 (en) * | 1998-06-08 | 1999-12-16 | Alstom Uk Ltd. | Heat exchanger |
WO2004083761A1 (en) * | 2003-03-17 | 2004-09-30 | Tuchenhagen Dairy Systems Gmbh | Device for inflowing in the stream area of a tube carrier plate of a heat exchanges provided with a tube bundle |
EP1793189A2 (en) * | 2005-12-01 | 2007-06-06 | Alstom Technology Ltd | Waste heat boiler |
WO2007068343A1 (en) * | 2005-12-13 | 2007-06-21 | Tuchenhagen Dairy Systems Gmbh | Device for influencing the flow in the region of a tube support plate of a tubular heat exchanger |
WO2012041344A1 (en) | 2010-09-30 | 2012-04-05 | Haldor Topsoe A/S | Waste heat boiler |
WO2013167180A1 (en) | 2012-05-09 | 2013-11-14 | Haldor Topsøe A/S | Waste heat boiler with bypass and mixer |
WO2021141484A1 (en) * | 2020-01-10 | 2021-07-15 | Citech Energy Recovery System Malaysia Sdn Bhd | Heat exchanger |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1303092A (en) * | 1970-08-29 | 1973-01-17 | ||
GB1333980A (en) * | 1972-07-28 | 1973-10-17 | Clarke Chapman John Thompson L | Boiler |
DE2846455B1 (en) * | 1978-10-23 | 1979-10-31 | Borsig Gmbh | Tube bundle heat exchanger with a constant outlet temperature of one of the two media |
-
1988
- 1988-09-06 DE DE19883830248 patent/DE3830248C1/de not_active Expired - Lifetime
-
1989
- 1989-07-11 EP EP19890112632 patent/EP0357907B1/en not_active Expired - Lifetime
- 1989-07-11 ES ES89112632T patent/ES2027812T3/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1303092A (en) * | 1970-08-29 | 1973-01-17 | ||
GB1333980A (en) * | 1972-07-28 | 1973-10-17 | Clarke Chapman John Thompson L | Boiler |
DE2846455B1 (en) * | 1978-10-23 | 1979-10-31 | Borsig Gmbh | Tube bundle heat exchanger with a constant outlet temperature of one of the two media |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5452686A (en) * | 1993-03-26 | 1995-09-26 | Haldor Topsoe A/S | Waste heat boiler |
EP0617230A1 (en) * | 1993-03-26 | 1994-09-28 | Haldor Topsoe A/S | Waste heat boiler |
EP0690262A1 (en) * | 1994-06-29 | 1996-01-03 | Haldor Topsoe A/S | Waste heat boiler |
US5852990A (en) * | 1994-06-29 | 1998-12-29 | Haldor Topsoe A/S | Waste heat boiler |
WO1999064806A1 (en) * | 1998-06-08 | 1999-12-16 | Alstom Uk Ltd. | Heat exchanger |
US6302191B1 (en) | 1998-06-08 | 2001-10-16 | Alstom Uk Limited | Heat exchanger |
WO2004083761A1 (en) * | 2003-03-17 | 2004-09-30 | Tuchenhagen Dairy Systems Gmbh | Device for inflowing in the stream area of a tube carrier plate of a heat exchanges provided with a tube bundle |
EP1793189A3 (en) * | 2005-12-01 | 2013-04-17 | Alstom Technology Ltd | Waste heat boiler |
EP1793189A2 (en) * | 2005-12-01 | 2007-06-06 | Alstom Technology Ltd | Waste heat boiler |
WO2007068343A1 (en) * | 2005-12-13 | 2007-06-21 | Tuchenhagen Dairy Systems Gmbh | Device for influencing the flow in the region of a tube support plate of a tubular heat exchanger |
US20090205813A1 (en) * | 2005-12-13 | 2009-08-20 | Tuchenhagen Dairy Systems Gmbh | Device for influencing the flow in the region of a tube support plate of a tube bundle heat exchanger |
US9127893B2 (en) | 2005-12-13 | 2015-09-08 | Gea Tds Gmbh | Device for influencing the flow in the region of a tube support plate of a tube bundle heat exchanger |
WO2012041344A1 (en) | 2010-09-30 | 2012-04-05 | Haldor Topsoe A/S | Waste heat boiler |
WO2013167180A1 (en) | 2012-05-09 | 2013-11-14 | Haldor Topsøe A/S | Waste heat boiler with bypass and mixer |
CN104285117A (en) * | 2012-05-09 | 2015-01-14 | 赫多特普索化工设备公司 | Waste heat boiler with bypass and mixer |
CN104285117B (en) * | 2012-05-09 | 2016-06-08 | 赫多特普索化工设备公司 | There is the waste heat boiler of bypass and mixing tank |
EA026857B1 (en) * | 2012-05-09 | 2017-05-31 | Хальдор Топсёэ А/С | Waste heat boiler with bypass and mixer |
US9739474B2 (en) | 2012-05-09 | 2017-08-22 | Haldor Topsoe A/S | Waste heat boiler with bypass and mixer |
WO2021141484A1 (en) * | 2020-01-10 | 2021-07-15 | Citech Energy Recovery System Malaysia Sdn Bhd | Heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
ES2027812T3 (en) | 1992-06-16 |
EP0357907B1 (en) | 1991-11-13 |
DE3830248C1 (en) | 1990-01-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE1294820B (en) | Flow throttle, consisting of at least one pair of coaxial, successively flowed through cylindrical vortex chambers | |
EP0357907B1 (en) | Heat exchanger | |
DE2111204C3 (en) | Spin-on filter | |
EP1189127B1 (en) | Thermostatic valve | |
DE19543960C2 (en) | Spray arm for a coating device | |
EP0273231B1 (en) | Regulating device, in particular for an ammoniac converter | |
DE3338063A1 (en) | Sanitary water delivery device with water heater and tap | |
DE3020557A1 (en) | Oil cooler for IC-engine - has deflection guides at inlet and outlets of flow channels to circulate before return | |
DE4423240C1 (en) | Thermostat valve with hollow cylindrical plug | |
DE3140687A1 (en) | Tubular heat exchanger | |
DE3490578C2 (en) | Device for circulating boiler media | |
DE19650086C1 (en) | Heat transmitter for gas-fluid heat exchange | |
DE2153719B2 (en) | HEAT TRANSFER DEVICE | |
EP3822569B1 (en) | Heat exchanger | |
EP0898100A2 (en) | Multiple way mixing valve | |
EP1466716A1 (en) | Device to distribute melted plastic material | |
DE681545C (en) | Thermostatic mixer | |
DE3304353A1 (en) | Hollow fibre dialyser | |
DE822400C (en) | Plate heat exchanger | |
DE2645278A1 (en) | PROCESS, EQUIPMENT AND SYSTEM FOR REHEATING OF A VISCOSE LIQUID FUEL | |
DE2947163C2 (en) | Method and device for the continuous cooling of wires heated to high temperatures | |
DE2334381A1 (en) | DEVICE FOR THE PRODUCTION OF CURLED FEEDS | |
DE1937735C (en) | Device for mixing two media whose temperatures differ greatly from one another | |
DE4109101A1 (en) | INSTALLATION FOR MIXING CHAMBERS OF FLOW TECHNICAL PLANTS | |
DE2421327C3 (en) | Exhaust pipe for a multi-disc rotary piston engine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19900113 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): BE ES IT NL |
|
17Q | First examination report despatched |
Effective date: 19910305 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE ES IT NL |
|
ITF | It: translation for a ep patent filed | ||
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2027812 Country of ref document: ES Kind code of ref document: T3 |
|
PLBI | Opposition filed |
Free format text: ORIGINAL CODE: 0009260 |
|
26 | Opposition filed |
Opponent name: MAN GUTEHOFFNUNGSHUETTE AG Effective date: 19920812 |
|
NLR1 | Nl: opposition has been filed with the epo |
Opponent name: MAN GUTEHOFFNUNGSHUTTE AG |
|
PLBN | Opposition rejected |
Free format text: ORIGINAL CODE: 0009273 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: OPPOSITION REJECTED |
|
27O | Opposition rejected |
Effective date: 19930828 |
|
NLR2 | Nl: decision of opposition | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19960723 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 19960729 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19960730 Year of fee payment: 8 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19970712 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19970731 |
|
BERE | Be: lapsed |
Owner name: BALCKE-DURR A.G. Effective date: 19970731 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19980201 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 19980201 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 19980811 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20050711 |