EP0768424B1 - Heated roll - Google Patents

Heated roll Download PDF

Info

Publication number
EP0768424B1
EP0768424B1 EP96115816A EP96115816A EP0768424B1 EP 0768424 B1 EP0768424 B1 EP 0768424B1 EP 96115816 A EP96115816 A EP 96115816A EP 96115816 A EP96115816 A EP 96115816A EP 0768424 B1 EP0768424 B1 EP 0768424B1
Authority
EP
European Patent Office
Prior art keywords
steam
discharge
set forth
heated roll
condensate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP96115816A
Other languages
German (de)
French (fr)
Other versions
EP0768424A2 (en
EP0768424A3 (en
Inventor
Heinz-Michael Dr. Zaoralek
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.)
Schwaebische Huettenwerke Automotive GmbH
Original Assignee
Schwaebische Huettenwerke Automotive GmbH
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 Schwaebische Huettenwerke Automotive GmbH filed Critical Schwaebische Huettenwerke Automotive GmbH
Publication of EP0768424A2 publication Critical patent/EP0768424A2/en
Publication of EP0768424A3 publication Critical patent/EP0768424A3/en
Application granted granted Critical
Publication of EP0768424B1 publication Critical patent/EP0768424B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F5/00Elements specially adapted for movement
    • F28F5/02Rotary drums or rollers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00Dryer section of machines for making continuous webs of paper
    • D21F5/02Drying on cylinders
    • D21F5/022Heating the cylinders
    • D21F5/028Heating the cylinders using steam
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F5/00Dryer section of machines for making continuous webs of paper
    • D21F5/02Drying on cylinders
    • D21F5/10Removing condensate from the interior of the cylinders
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21GCALENDERS; ACCESSORIES FOR PAPER-MAKING MACHINES
    • D21G1/00Calenders; Smoothing apparatus
    • D21G1/02Rolls; Their bearings
    • D21G1/0253Heating or cooling the rolls; Regulating the temperature
    • D21G1/0266Heating or cooling the rolls; Regulating the temperature using a heat-transfer fluid
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits

Definitions

  • the invention relates to the construction of steam-heated, preferably metallic, Rolls e.g. in paper machines, film drawing machines or the like machine equipment can be used.
  • the rollers often have to do this Purpose to be heated using liquid or gaseous heat transfer media Find.
  • such rollers are with a large number of axially parallel bores close to the periphery through which the Heat transfer medium is passed.
  • the invention deals with the embodiment of which is used as a heat carrier water vapor.
  • Such a roller is described in DE-A-43 13 379 by the applicant.
  • the one there Execution of the roller provides that through the peripheral holes conducted steam condenses at least partially in this, whereupon the condensate, centrifugal assisted to the ends of the peripheral bores at the roller ends flows and from there due to the vapor pressure or one to a drain pipe applied negative pressure through tubes or holes to the roller axis is where it will be derived from the roller through the drain line can.
  • a tube or bore is located at each end of the peripheral Holes.
  • the condensate control valve With a condensate control valve, the amount of runoff can be reduced Condensate can be controlled.
  • the heating power of the Determine roller is described in DE-A-43 13 379 by the applicant.
  • the differential pressure control system has a throttle valve in the outflow line, which has a certain differential pressure between the inflow line and the Discharge line of the roller maintained. Wants more steam to flow through the roller than intended, the pressure difference of the lines increases and the valve closes, and vice versa.
  • Flow control is e.g. on a throttle by measuring the pressure drop, the amount of overflow steam in the Discharge line determined and directly via an appropriately controlled throttle valve regulated.
  • peripheral heated steam-heated rolls Holes not reliable enough. Because either the common pressure difference for all drainage pipes of a peripherally drilled roller or the sum of the blow-through steam through all drainage pipes as well measured together, it can always happen that between Adjust the flow differences in the individual drainage pipes, which increase the Steam blowing through single or a group of tubes on the one hand and on the other hand, to overflow of one or more peripheral holes to lead.
  • DE 38 01 815 A1 discloses a device for removing condensate from a steam-heated drying cylinder.
  • the direction of rotation of the incoming steam is adjusted in a hollow drying cylinder by means of a suction mouthpiece provided on the inner cylinder wall so that the condensate collecting in a condensate riser pipe can be detached from the wall and transported away by the Coriolis force.
  • suction mouthpieces which must have relatively large dimensions because of the need to provide a large angular momentum, cannot be used in the limited space in the area of the entry points of the discharge pipes or bores of peripherally heated rollers.
  • the object of the invention is a, preferably temperature-controllable, steam-heated To propose roller, in which the removal of the resulting in the holes Condensate is reliably released in any operating condition.
  • discharge pipes or bores have at least one cross-sectional constriction and are thus designed are that they are a mixture, preferably swirling, of condensate and Cause steam.
  • a very small inner diameter can be provided at their ends near the peripheral bores, which is, for example, between 2 and 4 mm. This results in a strong increase in the flow rate of the condensate and the blowing steam, so that the resulting turbulence prevents the two media from segregating.
  • the free opening preferably has a cross-sectional area of 3 to about 12 mm 2 , in particular 3 to 7 mm 2 , and particularly preferably of about 3 mm 2 .
  • Twisting is also suitable for producing the necessary mixing Tube.
  • Such a discharge pipe is preferably designed such that the flow at least is turned sharply once.
  • An installation or the like can also be used for this purpose be provided.
  • Two peripheral bores can also be drilled through 2 connecting pipes or - channels are connected to the drain pipe or the drain hole through 1 common such pipe or a common such bore drained become.
  • Each of the above configurations according to the invention enables one each Roller to find individual operating point at which that in the peripheral Drilling condensate according to the given operating speed, the predetermined heating steam pressure and the set external differential pressure for the Total roller is reliably removed from the individual holes without the different holes influence each other excessively and without the The amount of total steam blowing through becomes uneconomically large.
  • the necessary cross-sectional narrowing of the discharge pipes and bores, the valves or internals in the pipes or bores also Operational risk because it can lead to constipation.
  • Carried with the steam Foreign bodies or even corrosion particles can enter the inlet openings The easier it is to lay drainage pipes or the narrowing points, the less are the respective free diameters.
  • the openings or meshes at most the diameter of the narrowest cross-section of the discharge pipes or holes accordingly. A foreign body that would be suitable for this Clogging the narrowest cross sections is stopped on the basket.
  • hot steam flows through the feed pipe 1 in the roll neck 2 on the one hand further through the steam channels 3 into the peripheral Bores 4 in the roller body 5, on the other hand through the central bore 6 in the roller body 5 to the other end of the roller, from there also through Steam channels to be introduced into peripheral holes.
  • Condensate that is in forms the peripheral holes (black arrows) from the holes 4 by means of of the steam pressure and flows to the end of the roll, either forward, i.e. with the steam flow direction, or backwards, against it, as in the Drawing shown.
  • the condensate collects in the collecting rooms 10 and passes from there, further under steam pressure, through the discharge pipes 7 into the Return pipe 8 through which it can leave the roller.
  • the drain pipes are provided at its outer end with a plug 9.
  • FIG. 2 shows, as a detail from FIG. 1, a discharge pipe 7 according to the prior art Technology.
  • FIG. 3 shows an embodiment of a discharge pipe 7 according to the invention, wherein the cross section of the tube 7 is narrowed.
  • FIG 4 a tube is shown with an inserted nozzle 12 instead of Pipe constriction.
  • Figure 5 shows a discharge pipe 7, which is twisted. Thereby a swirl of condensate and blow-by steam is achieved, so that a uniform drainage can take place.
  • FIG. 6 shows the arrangement of a sieve 11 in front of the discharge pipe 7.
  • the opening is to enable cleaning for the plug 9 so large that the screen 11 in and out can be.
  • Figure 7 shows an example of the dependencies between There is steam demand from the roller and blow-by steam.
  • the four re-enact it on the right, sloping curves show the drainage performance of the roller at various Differential vapor pressures (from above: 0.8 / 0.7 / 0.6 / 0.5 bar); the right slightly increasing lower curve corresponds to the steam throughput, each with increasing Blow-through steam as a percentage by weight.
  • the intersections of the curves are the stable operating points with a set differential pressure and given heating output. As can be seen, these are in the range between 5 and 20% blow-by steam.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Paper (AREA)
  • Drying Of Solid Materials (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Rolls And Other Rotary Bodies (AREA)

Description

Die Erfindung betrifft die Konstruktion von dampfbeheizten, vorzugsweise metallischen, Walzen, die z.B. in Papiermaschinen, Folienziehmaschinen oder ähnlichen maschinellen Einrichtungen eingesetzt werden. Die Walzen müssen häufig zu diesem Zweck erhitzt werden, wobei flüssige oder gasförmige Wärmeträger Verwendung finden. In einer besonderen Ausgestaltung sind derartige Walzen mit einer Vielzahl von achsparallelen, der Peripherie naheliegenden Bohrungen versehen, durch die der Wärmeträger geleitet wird. Hiervon behandelt die Erfindung die Ausgestaltung, bei der als Wärmeträger Wasserdampf verwendet wird.The invention relates to the construction of steam-heated, preferably metallic, Rolls e.g. in paper machines, film drawing machines or the like machine equipment can be used. The rollers often have to do this Purpose to be heated using liquid or gaseous heat transfer media Find. In a special embodiment, such rollers are with a large number of axially parallel bores close to the periphery through which the Heat transfer medium is passed. The invention deals with the embodiment of which is used as a heat carrier water vapor.

Eine solche Walze ist in der DE-A-43 13 379 der Anmelderin beschrieben. Die dortige Ausführung der Walze sieht vor, daß der durch die peripheren Bohrungen geleitete Dampf in diesen wenigstens teilweise kondensiert, worauf das Kondensat, fliehkraftunterstützt, zu den Enden der peripheren Bohrungen jeweils an den Walzenenden fließt und von dort auf Grund des Dampfdrucks oder eines an eine Abflußleitung angelegten Unterdrucks durch Röhren oder Bohrungen zur Walzenachse hingedrückt wird, von wo es durch die Abflußleitung aus der Walze abgeleitet werden kann. Eine solche Röhre oder Bohrung befindet sich jeweils an jedem Ende der peripheren Bohrungen. Dabei kann mit einem Kondensat-Regelventil die Menge des abfließenden Kondensats gesteuert werden. Somit läßt sich auch die Heizleistung der Walze bestimmen.Such a roller is described in DE-A-43 13 379 by the applicant. The one there Execution of the roller provides that through the peripheral holes conducted steam condenses at least partially in this, whereupon the condensate, centrifugal assisted to the ends of the peripheral bores at the roller ends flows and from there due to the vapor pressure or one to a drain pipe applied negative pressure through tubes or holes to the roller axis is where it will be derived from the roller through the drain line can. Such a tube or bore is located at each end of the peripheral Holes. With a condensate control valve, the amount of runoff can be reduced Condensate can be controlled. Thus, the heating power of the Determine roller.

Derartige Kondensat-Regelventile haben sich in vergleichbaren Einsätzen - wie z.B. bei der Dampfbeheizung von Plattenpressen - durchaus bewährt. Beim Einsatz in peripher gebohrten Walzen sind auf Grund der Besonderheiten des Betriebes jedoch Betriebsstörungen nicht völlig auszuschließen. Geringfügige Ungleichmäßigkeiten im Kondensatanfall oder, umlaufbedingt, in der Entwässerung der verschiedenen Ableitrohre oder -bohrungen führen dazu, daß Dampf durch die Ableitrohre oder -bohrungen durchblasen kann. Dies veranlaßt dann das Kondensat-Regelventil zu einer vorzeitigen Sperrung. Die weitere Entwässerung der Walze wird eingeschränkt und zuletzt unmöglich.Such condensate control valves have been used in comparable applications - e.g. for steam heating plate presses - well proven. When used in peripherally drilled rollers are due to the peculiarities of the operation Malfunctions cannot be completely ruled out. Minor irregularities in the Accumulation of condensate or, due to circulation, in the drainage of the various discharge pipes or holes result in steam through the exhaust pipes or holes can blow through. This then causes the condensate control valve to prematurely Blocking. The further drainage of the roller is restricted and last impossible.

Man hat versucht, die Kondensation des durchgeblasenen Dampfes in der Ausflußleitung zu beschleunigen, z.B. durch nicht isolierte Leitungen oder einen zusätzlichen Kondensator. Hierdurch wird dann bewirkt, daß das Kondensat-Regelventil wieder öffnet und Kondensat die Walze wieder verlassen kann. Es hat sich aber gezeigt, daß auch auf diesem Weg die völlig gleichmäßige Entwässerung aller peripheren Bohrungen nicht immer sichergestellt ist und einzelne Leitungen während des Betriebs dennoch mit kondensiertem Wasser gefüllt bleiben können. Dies führt zu einer ungleichmäßigen Beheizung der Walze und damit zu ihrer thermischen Verbiegung sowie zu Unwuchten des Walzenlaufs. Attempts have been made to condense the steam blown through the outflow line to accelerate, e.g. through non-insulated cables or an additional one Capacitor. This then causes the condensate control valve to operate again opens and condensate can leave the roller again. However, it has been shown that this way, too, the completely uniform drainage of all peripheral bores is not always ensured and individual lines during operation nevertheless can remain filled with condensed water. This leads to an uneven Heating of the roller and thus for its thermal bending as well Imbalance of the roller barrel.

Weiterhin wurde versucht, auf das Kondensat-Regelventil zu verzichten und stattdessen eine bestimmte Menge an Durchblasedampf zuzulassen. Damit ist der Vorteil verbunden, daß auch nicht kondensierbare Gase, welche in die Walze gelangt sind und die Wärmeübertragung behindern, wieder aus der Walze herausgeschleust werden. Systeme der Regelung der Durchblasedampfmenge sind z.B. für Trockenzylinder in Papiermaschinen bekannt. Man unterscheidet dabei Differenzdruckregelsysteme und Durchflußmengenregelsysteme.Furthermore, attempts have been made to dispense with the condensate control valve and instead to allow a certain amount of blow-by steam. That is the advantage connected that also non-condensable gases that have entered the roller and hinder the heat transfer, are ejected from the roller again. Blow-through steam control systems are e.g. for drying cylinders known in paper machines. A distinction is made between differential pressure control systems and flow control systems.

Das Differenzdruckregelsystem weist in der Ausflußleitung ein Drosselventil auf, welches einen bestimmten Differenzdruck zwischen der Einströmleitung und der Ausflußleitung der Walze aufrecht erhält. Will mehr Dampf durch die Walze strömen als beabsichtigt, steigt die Druckdifferenz der Leitungen und das Ventil schließt, sowie umgekehrt. Bei der Durchflußmengenregelung wird z.B. an einer Drossel durch Messung des Druckverlustes die Durchlaßmenge an Überblasedampf in der Ausflußleitung bestimmt und über ein entsprechend gesteuertes Drosselventil direkt geregelt.The differential pressure control system has a throttle valve in the outflow line, which has a certain differential pressure between the inflow line and the Discharge line of the roller maintained. Wants more steam to flow through the roller than intended, the pressure difference of the lines increases and the valve closes, and vice versa. Flow control is e.g. on a throttle by measuring the pressure drop, the amount of overflow steam in the Discharge line determined and directly via an appropriately controlled throttle valve regulated.

Auch diese beiden Systeme arbeiten bei dampfbeheizten Walzen der Bauart mit peripheren Bohrungen nicht zuverlässig genug. Da entweder die gemeinsame Druckdifferenz für alle Entwässerungsröhren einer peripher gebohrten Walze festgelegt wird oder die Summe des Durchblasedampfes durch alle Entwässerungsröhren ebenfalls gemeinsam gemessen wird, kann es immer wieder vorkommen, daß sich zwischen den einzelnen Entwässerungsröhren Durchflußunterschiede einstellen, die zum verstärkten Dampfdurchblasen bei einzelnen oder einer Gruppe von Röhren einerseits und zu einem Vollaufen von einzelnen oder mehreren peripheren Bohrungen andererseits führen.These two systems also work with peripheral heated steam-heated rolls Holes not reliable enough. Because either the common pressure difference for all drainage pipes of a peripherally drilled roller or the sum of the blow-through steam through all drainage pipes as well measured together, it can always happen that between Adjust the flow differences in the individual drainage pipes, which increase the Steam blowing through single or a group of tubes on the one hand and on the other hand, to overflow of one or more peripheral holes to lead.

Aus der DE 38 01 815 A1 ist eine Vorrichtung zum Abführen von Kondensat aus einem dampfbeheizten Trockenzylinder bekannt. Hier wird in einem hohlen Trockenzylinder mittels eines Saugmundstückes, das an der inneren Zylinderwandung vorgesehen ist, die Drehrichtung des einströmenden Dampfes so eingestellt, daß sich das in einem Kondensatsteigrohr ansammelnde Kondensat durch die Corioliskraft von der Wand ablöst und abtransportiert werden kann. Solche Saugmundstücke, die schon wegen der Notwendigkeit, einen großen Drehimpuls bereitzustellen, relativ große Abmessungen haben müssen, sind bei dem begrenzten Raum im Bereich der Eintrittsstellen der Ableitrohre oder -bohrungen von peripher beheizten Walzen nicht einsetzbar.DE 38 01 815 A1 discloses a device for removing condensate from a steam-heated drying cylinder. Here, the direction of rotation of the incoming steam is adjusted in a hollow drying cylinder by means of a suction mouthpiece provided on the inner cylinder wall so that the condensate collecting in a condensate riser pipe can be detached from the wall and transported away by the Coriolis force. Such suction mouthpieces, which must have relatively large dimensions because of the need to provide a large angular momentum, cannot be used in the limited space in the area of the entry points of the discharge pipes or bores of peripherally heated rollers.

Aufgabe der Erfindung ist es, eine, vorzugsweise temperaturregelbare, dampfbeheizte Walze vorzuschlagen, bei welcher die Entfernung des in den Bohrungen entstehenden Kondensats zuverlässig bei jedem Betriebszustand gelöst ist. The object of the invention is a, preferably temperature-controllable, steam-heated To propose roller, in which the removal of the resulting in the holes Condensate is reliably released in any operating condition.

Diese Aufgabe wird gelöst, indem die Ableitrohre oder -bohrungen mindestens eine Querschnittsverengung aufweisen und damit so ausgebildet sind, daß sie eine Vermischung, vorzugsweise Verwirbelung, von Kondensat und Dampf verursachen.This object is achieved in that the discharge pipes or bores have at least one cross-sectional constriction and are thus designed are that they are a mixture, preferably swirling, of condensate and Cause steam.

Dazu kann an ihren den peripheren Bohrungen naheliegenden Enden ein sehr kleiner innerer Durchmesser vorgesehen sein, der z.B. zwischen 2 und 4 mm liegt. Dadurch wird eine starke Erhöhung der Strömungsgeschwindigkeit des Kondensates und des durchblasenden Dampfes erzielt, so daß die sich ergebende Turbulenz die Entmischung der beiden Medien verhindert. Die freie Öffnung weist vorzugsweise eine Querschnittsfläche von 3 bis etwa 12 mm2, insbesondere 3 bis 7 mm2, und besonders bevorzugt von etwa 3 mm2 auf.For this purpose, a very small inner diameter can be provided at their ends near the peripheral bores, which is, for example, between 2 and 4 mm. This results in a strong increase in the flow rate of the condensate and the blowing steam, so that the resulting turbulence prevents the two media from segregating. The free opening preferably has a cross-sectional area of 3 to about 12 mm 2 , in particular 3 to 7 mm 2 , and particularly preferably of about 3 mm 2 .

In den, vorzugsweise durchgehenden, Ableitrohren oder -bohrungen, die an den Enden der peripheren Bohrungen dazu dienen sollen, das Kondensat zur Walzenmitte abzuleiten, findet eine Vermischung des Kondensats und des mit einströmenden Durchblasedampfes statt. Das Kondensat bleibt nicht mehr, gezwungen von der hohen Fliehkraft, am Umfang zurück, während der Durchblasedampf schnell zur Walzenachse strömt. Die einzelnen peripheren Bohrungen werden auf diese Weise gleichmäßig entwässert.In the, preferably continuous, discharge pipes or bores connected to the Ends of the peripheral bores are intended to serve the condensate to the center of the roll a mixture of the condensate and the inflowing Blow-by steam instead. The condensate no longer remains, forced by the high centrifugal force, back on the circumference, while the blow-by steam quickly Roll axis flows. The individual peripheral holes are made in this way evenly drained.

Eine vergleichbare Wirkung hat die Einsetzung von Düsen an den zum Walzenumfang weisenden Enden der Ableitrohre oder -bohrungen. Sie führen ebenfalls zu einer verstärkten Vermischung von Kondensat und Durchblasedampf im weiteren Verlauf der Rohre oder Bohrungen.The insertion of nozzles on the circumference of the roller has a comparable effect pointing ends of the discharge pipes or bores. They also lead to one increased mixing of condensate and blow-by steam in the further course of the pipes or holes.

Ebenso geeignet, die notwendige Vermischung zu erzeugen, ist eine Verwindung der Rohre.Twisting is also suitable for producing the necessary mixing Tube.

Vorzugsweise ist solch ein Ableitungsrohr so ausgebildet, daß die Strömung wenigstens einmal scharf umgelenkt wird. Hierzu kann auch ein Einbau oder dergleichen vorgesehen sein.Such a discharge pipe is preferably designed such that the flow at least is turned sharply once. An installation or the like can also be used for this purpose be provided.

Es können auch zwei periphere Bohrungen, die durch 2 Verbindungsrohre oder - kanäle mit dem Ableitungsrohr oder der Ableitungsbohrung verbunden sind, durch 1 gemeinsames solches Rohr oder eine gemeinsame solche Bohrung entwässert werden.Two peripheral bores can also be drilled through 2 connecting pipes or - channels are connected to the drain pipe or the drain hole through 1 common such pipe or a common such bore drained become.

Möglich ist auch der Einbau von zusätzlichen, an einer oder mehreren Stellen der Rohre oder Bohrungen angebrachten Strömungshindernissen.It is also possible to install additional ones at one or more points Pipes or holes attached to flow obstacles.

Jede der vorstehenden erfindungsgemäßen Ausgestaltungen ermöglicht es, einen je Walze individuellen Betriebspunkt zu finden, bei welchem das in den peripheren Bohrungen anfallende Kondensat entsprechend der gegebenen Beriebsdrehzahl, dem vorgegebenen Heizdampfdruck und dem eingestellten äußeren Differenzdruck für die Gesamtwalze zuverlässig aus den einzelnen Bohrungen entfernt wird, ohne daß sich die verschiedenen Bohrungen übermäßig gegenseitig beeinflussen und ohne daß die Menge des insgesamt durchblasenden Dampfes unwirtschaftlich groß wird. Hierbei hat es sich als vorteilhaft erwiesen, als Maximalwert zehn Gewichtsprozente kondensierten Dampf nicht zu überschreiten. Mehr als 20 Gewichtsprozente liegen außerhalb sinnvoller Betriebsführung. Trägt man die "Entwässerungsleistung" und den "Kondensatanfall" bzw. den "Dampfdurchsatz" pro Stunde für einen derartigen Betriebspunkt eines einzelnen Entwässerungsrohres oder einer einzelnen Entwässerungsbohrung am Ende einer peripheren Bohrung in einem Diagramm auf der y-Achse und den Prozentanteil Durch- oder Überblasedampf auf der x-Achse auf, so ergeben sich im Falle der erfindungsgemäßen Ausgestaltung der Walzen zwei Kurven, die sich im Bereich zwischen über 5 % und unter 20 % Überblasedampfanteil schneiden.Each of the above configurations according to the invention enables one each Roller to find individual operating point at which that in the peripheral Drilling condensate according to the given operating speed, the predetermined heating steam pressure and the set external differential pressure for the Total roller is reliably removed from the individual holes without the different holes influence each other excessively and without the The amount of total steam blowing through becomes uneconomically large. Here it has proven to be advantageous to condense ten percent by weight as the maximum value Steam not to be exceeded. More than 20 percent by weight are outside sensible management. If you wear the "drainage performance" and the "Condensate accumulation" or the "steam throughput" per hour for such an operating point of a single drain pipe or drain hole at the end of a peripheral hole in a diagram on the y axis and the percentage of blow-by or blow-by steam on the x-axis, the result is in the case of the configuration of the rollers according to the invention, two curves which are in the Cut the area between over 5% and under 20% overblowing steam.

Es hat sich zusätzlich gezeigt, daß eine erfindungsgemäße Ausgestaltung der Ableitrohre oder -bohrungen zu einer automatischen Einstellung des Gleichgewichts zwischen dem Kondensatspiegel in der peripheren Bohrung und dem durchtretenden Überblasedampf führt. Nimmt der Anteil an Überblasedampf aus einem beliebigen Grund zu, sinkt die Entwässerungsleistung des Rohres. Der Kondensatspiegel in der peripheren Bohrung steigt und drosselt den Anteil an Überblasedampf. Bei einem Zuviel an Kondensatabfuhr in einer peripheren Bohrung sinkt umgekehrt der Kondensatspiegel und die Öffnung des Entwässerungsrohres wird für einen verstärkten Durchsatz von Überblasedampf freigegeben.It has also been shown that an embodiment of the discharge pipes according to the invention or holes for automatic balance adjustment between the condensate level in the peripheral hole and the penetrating Blown steam leads. The proportion of overblown steam takes from any Reason, the drainage performance of the pipe drops. The condensate level in the peripheral bore increases and throttles the proportion of blow-by steam. At a Conversely, too much condensate drainage in a peripheral borehole drops the condensate level and the opening of the drainage pipe is reinforced for a Blown steam released.

Bei hohen Dampfdrücken und kleineren Walzenabmessungen können Verhältnisse eintreten, in denen das Gleichgewicht erst bei unerwünscht großen Überblasedampfanteilen erreicht wird. Eine Begrenzung des Überblasedampfanteils außerhalb der Walze, z.B. durch eine Dampfmengenregelung, ist jedoch nicht sinnvoll, weil dann wieder die eingangs beschriebenen Verhältnisse der ungleichmäßigen Entwässerung der peripheren Rohre eintreten. Es kann in einem derartigen Fall demgegenüber sinnvoll sein, zwei oder auch mehr periphere Bohrungen in Gruppen zusammenzufassen und jeweils auf jeder Seite mit nur einem Ableiterohr oder einer Ableitebohrung zu versehen. Durch den verdoppelten bzw. vervielfachten Durchsatz kommt es dann wieder zu der angestrebten Vermischung von Kondensat und Durchblasedampf. Es sind dabei Gruppen mit möglichst wenigen peripheren Bohrungen zu bilden, um im Falle eines Walzenstops das Zusammenfließen von Kondensat im unteren Bereich der Walze zu verhindern.At high steam pressures and smaller roller dimensions, conditions can occur occur in which the equilibrium only with undesirably large overblowing steam proportions is achieved. A limitation of the amount of overblown steam outside the Roller, e.g. by regulating the amount of steam, however, does not make sense because then again the conditions of the uneven drainage described at the beginning of the peripheral tubes. In contrast, it can be useful in such a case be to combine two or more peripheral holes in groups and on each side with only one drain pipe or one drain hole Mistake. It then comes through the doubled or multiplied throughput back to the desired mixing of condensate and blow-by steam. It groups with as few peripheral holes as possible are to be formed in order to In the event of a roller stop, condensate flows together in the lower area of the To prevent roller.

Allerdings stellen die erforderlichen Querschnittsverengungen der Ableitungsrohre und -bohrungen, die Ventile oder Einbauten in den Rohren oder Bohrungen auch ein Betriebsrisiko dar, weil es zu Verstopfungen kommen kann. Mit dem Dampf mitgeführte Fremdkörper oder auch Korrosionspartikel können die Eintrittsöffnungen der Entwässerungsrohre oder die Verengungsstellen um so leichter verlegen, je geringer die jeweiligen freien Durchmesser sind. In einer bevorzugten Ausgestaltung wird darum an der dem äußeren Umfang zugewandten Seite der Ableitungsrohre oder - bohrungen ein Korb oder eine Rückhalteeinrichtung angeordnet, deren Öffnungen oder Maschen höchstens dem Durchmesser des engsten Querschnitts der Ableitungsrohre oder -bohrungen entsprechend. Ein Fremdkörper, der geeignet wäre, diese engsten Querschnitte zu verstopfen, wird an dem Korb aufgehalten. Da der Korb oder die Rückhalteeinrichtung viele solcher Öffnungen haben, bedarf es auch vieler Fremdkörper, ehe eine Verstopfung herbeigeführt wird. Eine weitere Sicherheit ergibt sich dadurch, daß jede periphere Bohrung zwei solcher Rohre oder Bohrungen, nämlich an beiden Enden, aufweist. Wenn dennoch über eine längere Betriebszeit das Auftreten derartiger Fremdkörper nicht ausgeschlossen werden kann, empfiehlt es sich, die in der erwähnten DE-A-43 13 379 konstruktionsbedingten Verschlüsse als Service-Öffnungen auszuführen, die auf einfache Weise geöffnet und wieder verschlossen werden können. Durch derartige Service-Öffnungen können dann die Körbe bzw. Rückhalteeinrichtungen gewartet werden, ohne daß größere Eingriffe an der Walze, wie z.B. die Demontage der Walzenzapfen, erforderlich ist. Auch ist es bei bestimmten Walzengestaltungen dann möglich, Ableitungsrohre auszuwechseln, wenn diese wegen der hohen Kondensatgeschwindigkeiten bei längerer Betriebszeit Kavitationsschäden aufweisen sollten.However, the necessary cross-sectional narrowing of the discharge pipes and bores, the valves or internals in the pipes or bores also Operational risk because it can lead to constipation. Carried with the steam Foreign bodies or even corrosion particles can enter the inlet openings The easier it is to lay drainage pipes or the narrowing points, the less are the respective free diameters. In a preferred embodiment therefore on the side of the discharge pipes facing the outer circumference or bores arranged a basket or a restraint, the openings or meshes at most the diameter of the narrowest cross-section of the discharge pipes or holes accordingly. A foreign body that would be suitable for this Clogging the narrowest cross sections is stopped on the basket. Because the basket or the restraint device has many such openings, many are required Foreign objects before constipation is brought about. Another security results the fact that each peripheral bore two such pipes or bores, namely at both ends. If nevertheless over a longer period of operation The occurrence of such foreign bodies cannot be excluded, it is recommended itself, which in the aforementioned DE-A-43 13 379 construction-related closures as Execute service openings that are easily opened and closed again can be. The baskets can then be opened through such service openings or retention devices are maintained without major intervention on the Roller, e.g. disassembly of the roll neck is required. It is also at certain roller designs then possible to replace drain pipes if this due to the high condensate velocities caused by cavitation damage over long periods of operation should have.

Im folgenden wird eine erfindungsgemäße Ausgestaltung einer peripher gebohrten Walze anhand der Zeichnungen in Figuren 1 bis 7 beschrieben:

Figur 1
zeigt dabei einen Teil einer Walze, den Zapfenbereich einer Seite, in einer perspektivischen Schnittdarstellung;
Figur 2
zeigt als Ausschnitt von Fig. 1 ein Ableitungsrohr nach dem bisherigen Stand der Technik;
Figur 3
zeigt eine erfindungsgemäße Ausgestaltung eines Ableitungsrohres mit einem Innenmaß von ca. 2 - 4 mm;
Figur 4
zeigt eine erfindungsgemäße Ausgestaltung eines Ableitungsrohres mit einer Düse zur Verwirbelung des Kondensats mit dem Überblasedampf;
Figur 5
zeigt eine mögliche Ausgestaltung, bei welcher die Verwirbelung durch eine Verwindung des Ableitungsrohres erreicht wird;
Figur 6
zeigt ein erfindungsgemäß ausgestaltetes Ableitungsrohr mit einem Sieb; und
Figur 7
zeigt im Diagramm den Dampfbedarf und die Kondensatabfuhr einer erfindungsgemäßen Walze.
An embodiment of a peripherally drilled roller according to the invention is described below with reference to the drawings in FIGS. 1 to 7:
Figure 1
shows part of a roller, the pin region of one side, in a perspective sectional view;
Figure 2
shows a detail of Figure 1, a drain pipe according to the prior art;
Figure 3
shows an embodiment of a discharge pipe according to the invention with an internal dimension of about 2-4 mm;
Figure 4
shows an embodiment of a discharge pipe according to the invention with a nozzle for swirling the condensate with the blow-by steam;
Figure 5
shows a possible embodiment in which the swirl is achieved by twisting the discharge pipe;
Figure 6
shows an inventive discharge pipe with a sieve; and
Figure 7
shows in the diagram the steam requirement and the condensate drainage of a roller according to the invention.

Wie in Figur 1 zu sehen, strömt heißer Dampf (weiße Pfeile) durch das Zuleitungsrohr 1 im Walzenzapfen 2 einerseits weiter durch die Dampfkanäle 3 in die peripheren Bohrungen 4 im Walzenkörper 5, andererseits durch die zentrale Bohrung 6 im Walzenkörper 5 zum anderen Ende der Walze, um von dort ebenfalls durch Dampfkanäle in periphere Bohrungen eingeleitet zu werden. Kondensat, das sich in den peripheren Bohrungen bildet (schwarze Pfeile) wird aus den Bohrungen 4 mittels des Dampfdrucks herausgedrängt und fließt zum Walzenende, entweder vorwärts, d.h. mit der Dampfströmungsrichtung, oder rückwärts, gegen diese, wie in der Zeichnung dargestellt. Das Kondensat sammelt sich in den Sammelräumen 10 und gelangt von dort, weiter unter Dampfdruck, durch die Ableitungsrohre 7 in das Rücklaufrohr 8, durch das es die Walze verlassen kann. Die Ableitungsrohre sind an ihrem äußeren Ende mit Verschlußstopfen 9 versehen.As can be seen in Figure 1, hot steam (white arrows) flows through the feed pipe 1 in the roll neck 2 on the one hand further through the steam channels 3 into the peripheral Bores 4 in the roller body 5, on the other hand through the central bore 6 in the roller body 5 to the other end of the roller, from there also through Steam channels to be introduced into peripheral holes. Condensate that is in forms the peripheral holes (black arrows) from the holes 4 by means of of the steam pressure and flows to the end of the roll, either forward, i.e. with the steam flow direction, or backwards, against it, as in the Drawing shown. The condensate collects in the collecting rooms 10 and passes from there, further under steam pressure, through the discharge pipes 7 into the Return pipe 8 through which it can leave the roller. The drain pipes are provided at its outer end with a plug 9.

Figur 2 zeigt, als Ausschnitt aus Figur 1, ein Ableitungsrohr 7 nach dem Stand der Technik.FIG. 2 shows, as a detail from FIG. 1, a discharge pipe 7 according to the prior art Technology.

Figur 3 zeigt eine erfindungsgemäße Ausgestaltung eines Ableitungsrohres 7, wobei der Querschnitt des Rohres 7 verengt ist.FIG. 3 shows an embodiment of a discharge pipe 7 according to the invention, wherein the cross section of the tube 7 is narrowed.

In Figur 4 ist ein Rohr dargestellt mit einer eingesetzten Düse 12 anstelle der Rohrverengung. Figur 5 zeigt ein Ableitungsrohr 7, welches verwunden ist. Dadurch wird eine Verwirbelung von Kondensat und Durchblasedampf erreicht, so daß eine gleichmäßige Entwässerung stattfinden kann. In Figure 4, a tube is shown with an inserted nozzle 12 instead of Pipe constriction. Figure 5 shows a discharge pipe 7, which is twisted. Thereby a swirl of condensate and blow-by steam is achieved, so that a uniform drainage can take place.

In Figur 6 ist die Anordnung eines Siebes 11 vor dem Ableitungsrohr 7 dargestellt. Zur Ermöglichung der Reinigung ist bei Verwendung eines Siebes 11 die Öffnung für den Verschlußstopfen 9 so groß ausgeführt, daß das Sieb 11 ein- und ausgeführt werden kann.FIG. 6 shows the arrangement of a sieve 11 in front of the discharge pipe 7. When using a sieve 11, the opening is to enable cleaning for the plug 9 so large that the screen 11 in and out can be.

Figur 7 schließlich zeigt an einem Beispiel auf, welche Abhängigkeiten zwischen Dampfbedarf der Walze und Durchblasedampf bestehen. Darin stellen die vier nach rechts abfallenden Kurven die Entwässerungsleistungen der Walze bei verschiedenen Differenz-Dampfdrücken (von oben: 0,8/0,7/0,6/0,5 bar) dar; die nach rechts leicht ansteigende untere Kurve entspricht dem Dampfdurchsatz, jeweils mit ansteigendem Anteil Durchblasedampf in Gewichtsprozenten. Die Schnittstellen der Kurven sind die stabilen Betriebspunkte bei eingestelltem Differenzdruck und gegebener Heizleistung. Wie ersichtlich, liegen diese im Bereich zwischen 5 und 20 % Durchblasedampf.Figure 7 shows an example of the dependencies between There is steam demand from the roller and blow-by steam. The four re-enact it on the right, sloping curves show the drainage performance of the roller at various Differential vapor pressures (from above: 0.8 / 0.7 / 0.6 / 0.5 bar); the right slightly increasing lower curve corresponds to the steam throughput, each with increasing Blow-through steam as a percentage by weight. The intersections of the curves are the stable operating points with a set differential pressure and given heating output. As can be seen, these are in the range between 5 and 20% blow-by steam.

Claims (10)

  1. A steam-heated roll comprising preferably peripheral, at least approximately axially parallel drilled passages (4) for heat supply and removal and, running radially from the latter to the roll center, discharge tubes or drilled passages (7) for condensate dewatering,
    characterized in that
    said discharge tubes or drilled passages (7) comprise at least one cross-sectional constriction and are thus configured so that they cause a mixing or swirling of condensate and steam.
  2. The steam-heated roll as set forth in claim 1, characterized in that said cross-sectional constriction is formed by a nozzle or restriction aperture (12) inserted in the tube.
  3. The steam-heated roll as set forth in any of the preceding claims, characterized in that said discharge tube (7) is rendered tortuous, comprising preferably at least one sharp fitting or the like, deflecting the flow.
  4. The steam-heated roll as set forth in any of the preceding claims, characterized in that said preferably full-length discharge tubes or drilled passages (7) comprise at said cross-sectional constrictions a free opening of between 3 and roughly 12 mm2, preferably between 3 and 7 mm2, particularly 3 mm2.
  5. The steam-heated roll as set forth in any of the preceding claims, characterized in that at least two peripheral drilled passages (4) are connected by means of connecting tubes or passageways to a discharge tube or a discharge drilled passage (7) and are dewatered thereby.
  6. The steam-heated roll as set forth in any of the preceding claims, characterized in that maximally a quarter of said peripheral drilled passages (4) are connected by means of connecting tubes or passageways to a discharge tube or a discharge drilled passage (7) and are dewatered thereby.
  7. The steam-heated roll as set forth in any of the preceding claims, characterized in that in the direction of flow upstream of said discharge tubes or drilled passages (7) a strainer or sieve (11) is arranged, the openings of which are smaller than or equal to the smallest diameters in said discharge tube or discharge drilled passage (7).
  8. The steam-heated roll as set forth in any of the preceding claims, characterized in that opposite the outer end of said discharge tube or drilled passages (7) openings are incorporated and are closed off by releasable closure means (9).
  9. The steam-heated roll as set forth in any of the preceding claims, characterized in that said opening is so large that said strainer (11) or the complete discharge tube (7) can be removed therethrough.
  10. A method of controlling the steam flow through and the condensate discharge from a steam-heated roll as set forth in any of the preceding claims, characterized in that the pressure difference between inlet and outlet of the steam for each peripheral drilled passage (4) is controlled depending on the desired heating capacity, vapor pressure and/or rotary speed of the roll so that the percentage of overblow steam at the condensate exit is less than 20 percent by weight, preferably between 5 and 15 percent by weight.
EP96115816A 1995-10-13 1996-10-02 Heated roll Expired - Lifetime EP0768424B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19538236A DE19538236A1 (en) 1995-10-13 1995-10-13 Heating roller
DE19538236 1995-10-13

Publications (3)

Publication Number Publication Date
EP0768424A2 EP0768424A2 (en) 1997-04-16
EP0768424A3 EP0768424A3 (en) 1998-05-13
EP0768424B1 true EP0768424B1 (en) 2000-06-14

Family

ID=7774825

Family Applications (1)

Application Number Title Priority Date Filing Date
EP96115816A Expired - Lifetime EP0768424B1 (en) 1995-10-13 1996-10-02 Heated roll

Country Status (5)

Country Link
US (1) US6039681A (en)
EP (1) EP0768424B1 (en)
JP (1) JPH09133125A (en)
CA (1) CA2187056A1 (en)
DE (2) DE19538236A1 (en)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI106054B (en) * 1999-03-29 2000-11-15 Valmet Corp Thermo roll for a paper / cardboard machine or finishing machine and process for making the thermo roll
US5899264A (en) * 1997-09-17 1999-05-04 Marquip, Inc. Steam supply and condensate removal apparatus for heated roll
DE19747555A1 (en) 1997-10-28 1999-04-29 Voith Sulzer Papiertech Patent Heated and / or coolable cylinder
DE19756152C2 (en) * 1997-12-17 2002-06-27 Voith Paper Patent Gmbh Steam heated roller
DE19809080C2 (en) * 1997-12-17 2003-08-14 Voith Paper Patent Gmbh Steam heated roller
EP0942097A1 (en) * 1998-03-05 1999-09-15 Walzen Irle GmbH Heat exchanger
DE19819072C1 (en) * 1998-04-29 1999-08-19 Voith Sulzer Papiertech Patent Steam heated roller for finishing paper web surfaces
US6161303A (en) * 1998-10-29 2000-12-19 Voith Sulzer Papiertechnik Patent Gmbh Pressing apparatus having chamber end sealing
FI105115B (en) * 1998-12-02 2000-06-15 Valmet Corp Heated roller
EP1029976B1 (en) * 1999-02-17 2002-07-24 Walzen Irle GmbH Roller
US6619471B1 (en) 2000-10-25 2003-09-16 Surface Engineering Associates, Inc. Furnace roller
AU2001249015A1 (en) * 2000-10-25 2002-05-06 Surface Engineering Associates, Inc. Furnace roller
FI20002885A0 (en) * 2000-12-29 2000-12-29 Santasalo Powermet Oy Method for making the roll end of a roll of a paper or board machine or a finishing machine and a roll, in particular a heated roll
DE10207505B4 (en) * 2002-02-22 2015-07-30 Shw Casting Technologies Gmbh roller
DE10230037B9 (en) * 2002-07-04 2004-10-21 Voith Paper Patent Gmbh Heating roller and process for its manufacture
DE10235142A1 (en) * 2002-08-01 2004-02-19 Shw Casting Technologies Gmbh Roller for thermally pressure treating strip-like media, such as paper or fleece, in a multiple roller calender comprises a base body made from tempered forged steel or alloyed cast iron
DE10239559B4 (en) 2002-08-28 2016-09-29 Shw Casting Technologies Gmbh Roller for the thermomechanical treatment of a sheet-like medium
DE10351515A1 (en) * 2003-11-05 2005-06-09 Voith Paper Patent Gmbh Roller for thermal treatment of a material web
DE102005000795A1 (en) * 2005-01-05 2006-07-13 Voith Paper Patent Gmbh Apparatus and method for producing and / or refining a fibrous web
DE102005000782A1 (en) * 2005-01-05 2006-07-20 Voith Paper Patent Gmbh Drying cylinder for use in the production or finishing of fibrous webs, e.g. paper, comprises heating fluid channels between a supporting structure and a thin outer casing
US8602955B2 (en) * 2009-03-17 2013-12-10 Andritz Bricmont Inc. Furnace roller assembly
JP5890270B2 (en) * 2012-07-20 2016-03-22 株式会社日立パワーソリューションズ Drilled roll and roll press equipment
CN106945347B (en) * 2017-04-19 2023-08-18 云南全心包装印刷有限公司 Stable energy-saving steam compression roller and steam energy-saving circulating system using same
KR102201075B1 (en) * 2019-01-10 2021-01-11 에스 알 씨 주식회사 Roller for forming corrugated paper by external surface steam circulation
CN114396781B (en) * 2021-12-01 2023-02-21 泰州印染机械有限公司 High-efficiency energy-saving double-layer steam drying cylinder

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3721016A (en) * 1969-08-04 1973-03-20 Int Paper Co Method of removing condensate from a rotary dryer
US4194299A (en) * 1978-04-11 1980-03-25 Sca Development Aktiebolag Condensate discharging device
DE3801815A1 (en) * 1988-01-22 1989-08-03 Voith Gmbh J M DEVICE FOR DRAINING CONDENSATE FROM A STEAM-HEATED DRY CYLINDER OR THE LIKE MEANING OF A ROTATING SIPHON
DE4313379C2 (en) * 1993-04-23 1998-11-05 Schwaebische Huettenwerke Gmbh Heating roller

Also Published As

Publication number Publication date
DE19538236A1 (en) 1997-04-17
CA2187056A1 (en) 1997-04-14
EP0768424A2 (en) 1997-04-16
JPH09133125A (en) 1997-05-20
DE59605433D1 (en) 2000-07-20
EP0768424A3 (en) 1998-05-13
US6039681A (en) 2000-03-21

Similar Documents

Publication Publication Date Title
EP0768424B1 (en) Heated roll
EP3479982B1 (en) Cooling roll
DE3327179A1 (en) EVAPORATOR
EP0629739B1 (en) Headbox for a paper machine
DE1942157A1 (en) Air-cooled condenser
DE4313379C2 (en) Heating roller
DE2927977A1 (en) HEAT EXCHANGER
EP0093203A1 (en) Installation for the removal of solid impurities from cooling water for power stations, etc.
AT405685B (en) HEAT EXCHANGER
DE9306176U1 (en) Heating roller
EP1157755A2 (en) Nozzle manifold for the cooling or descaling of metallic elongated material, in particular of rolling stock
WO2002006575A1 (en) Method and device for continuously treating synthetic fibers in a heat exchange chamber
DE60010410T2 (en) Management device for circulating in a heat exchanger solid
DE10117989C1 (en) Steam creating system, for heating by exhaust gas, has two or more water/steam circuits, each with at least one evaporator device
DE102007012527A1 (en) Fluid exchanging device, has distributor connecting directly to fluid tube, in which total fluid flow is partitioned into partial flows flowing into assigned delay assembly and leaking out into fluid tank in retarded manner
DE10001297A1 (en) Spring loaded water spray valve has angled jets to spray onto vertical plates and with the rate of spraying determined by the number of jets opened through the water pressure
DE60011305T2 (en) DEVICE FOR CARRYING OUT PHYSICAL AND / OR CHEMICAL PROCESSES, FOR EXAMPLE A HEAT EXCHANGE
DE3818819C2 (en) Heat transfer device
DE202011110778U1 (en) Conduit branch piece for downpipes
DE3535315A1 (en) Apparatus for carrying away condensate from a steam-heated drying cylinder
DE3315250A1 (en) Device for flow distribution in heat exchangers
DE3513286A1 (en) DRY CYLINDER THAT IS HEATABLE
DE2830608C2 (en) Cooling water injection for an adjustable throttle for steam
DE202019002014U1 (en) Water bath evaporator and process plant
DE29719007U1 (en) Device for injecting steam into flowing water for the purpose of heating the water

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

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): DE FI GB IT SE

17P Request for examination filed

Effective date: 19970620

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): DE FI GB IT SE

17Q First examination report despatched

Effective date: 19980826

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

ITF It: translation for a ep patent filed

Owner name: BARZANO' E ZANARDO MILANO S.P.A.

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): DE FI GB IT SE

GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 20000615

REF Corresponds to:

Ref document number: 59605433

Country of ref document: DE

Date of ref document: 20000720

EN Fr: translation not filed
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20020923

Year of fee payment: 7

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20020925

Year of fee payment: 7

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20031002

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20031003

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20031002

EUG Se: european patent has lapsed
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;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.

Effective date: 20051002

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FI

Payment date: 20051014

Year of fee payment: 10

Ref country code: DE

Payment date: 20051014

Year of fee payment: 10

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20061002

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20070501