EP0989231A2 - Controlling the moisture profile - Google Patents
Controlling the moisture profile Download PDFInfo
- Publication number
- EP0989231A2 EP0989231A2 EP99112923A EP99112923A EP0989231A2 EP 0989231 A2 EP0989231 A2 EP 0989231A2 EP 99112923 A EP99112923 A EP 99112923A EP 99112923 A EP99112923 A EP 99112923A EP 0989231 A2 EP0989231 A2 EP 0989231A2
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- European Patent Office
- Prior art keywords
- web
- fibrous web
- cylinder
- electromagnetic waves
- electrodes
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F5/00—Dryer section of machines for making continuous webs of paper
- D21F5/16—Drying webs by electrical heating
- D21F5/167—Microwave heating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
- F26B13/10—Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/32—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
- F26B3/34—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
- F26B3/347—Electromagnetic heating, e.g. induction heating or heating using microwave energy
Definitions
- the invention relates to a method and the associated devices for Moisture profiling of a fibrous web to be dried, in particular a paper, Cardboard or tissue web in machines for the production and / or finishing of the same.
- the fibrous webs are currently used for drying over heated cylinders guided. This complex process often results in an uneven distribution of the Moisture across the fibrous web. To correct this moisture cross profile certain zones additionally humidified or heated, the heating in the generally done inductively or by means of IR radiators and humidification with steam.
- the object of the invention is therefore a method that is as simple and precise as possible and to develop at least one corresponding device for moisture profiling.
- the object was achieved in that the fibrous web electromagnetic waves in the form of microwaves and / or high frequency waves is exposed. This is essentially due to the fact that the fibrous web is on at least one microwave transmitter and / or at least two with one High-frequency source connected electrodes of different polarity passed becomes.
- the high-frequency range lies approximately in the range between 10 and 300 MHz and the Microwave range between 300 MHz and 30 GHz. To ensure a uniform effect on the fibrous web, the Field energy of the electromagnetic waves across the fibrous web should also be possible be evenly distributed.
- the method is used in the areas where the fibrous web unites Has a dry content between 60 and 95%. On the one hand, these areas do not have to too much water to be heated and on the other hand is sufficient moisture to Absorption of the electromagnetic waves is present.
- the fibrous web is also supported in the area of electromagnetic waves. This stabilizes the Run of the fibrous web and reduces the risk of tearing. For this, the The fibrous web is guided over a rotating cylinder.
- the drying of the fibrous web at least predominantly by electromagnetic waves occur. Most of the time, however, the drying on conventional way, i.e. for example via heated cylinders, so that electromagnetic waves essentially only to compensate for Differences in moisture serve across the fibrous web.
- One or more waveguides are preferably used as the microwave transmitter Application, which are each connected to at least one microwave source and at least transversely to the fibrous web as evenly distributed as possible should. The result is a relatively even distribution of field energy Microwaves across the fibrous web.
- the fibrous web should have a microwaves rotating cylinder.
- the jacket of the cylinder or an outer coating of this jacket consist of a material that the Microwaves absorbed worse than the fibrous web. This is suitable for example Teflon.
- the thickness of the coating should be between 5 and 150 mm, are preferably between 10 and 50 mm.
- the course of the fibrous web can also be used alone or in addition to at least one sieve is supported, the material of which the microwaves are worse than the fibrous web absorbs.
- the electrodes should be in the form of Stick electrodes, capacitor plates and / or rotating cylinders.
- the fibrous web should rotate in the region of the electrodes Cylinder guided and preferably supported by a sieve.
- the preferably predominantly metallic Cylinder forms an electrode and on the with respect to the fibrous web opposite side at least one stick electrode and / or one Capacitor plate of different polarity is arranged. It is included as a protective measure an advantage if the cylinder has an electrically insulating outer coating. On the other hand, it is also possible that in the wrapping area of the cylinder there are at least two stick electrodes of different polarity, the High-frequency waves partially penetrate the fibrous web.
- FIG. 1 there is a microwave transmitter 2 along the looping area arranged outside the cylinder 3.
- the microwave transmitter 2 consists of a series of several across Path running waveguides with a rectangular cross-section, each with are connected to a microwave source. However, it is also possible that Arrange waveguide meandering. The resulting microwaves provide for the fact that the wetter parts of the fibrous web 1 are heated up more and thus are dried than the other areas. The result is a more even one Moisture cross profile.
- a shield 6 is arranged around the microwave transmitter 2, so that none Microwaves leave this device.
- the cylinder 3 is approximately 2 cm thick Coating 4 made of Teflon, which absorbs the microwaves less strongly than that Fibrous web 1. The thickness of the coating 4 ensures that the metallic Area of the cylinder 3 is as far away from the fibrous web 1, so that a the greatest possible field strength of the microwaves in the fibrous web 1 is guaranteed.
- Figures 2 and 3 show high frequency devices in which the run of the Fibrous web 1 is stabilized via a running, external sieve 5.
- the devices with a shield 6 for Provide high frequency waves.
- the fibrous web 1 is connected to a high-frequency source (HF) Electrodes of different polarity passed. This also leads to warming and drying the moist areas of the fibrous web 1 with the result a relatively uniform moisture cross profile.
- HF high-frequency source
- the metallic, rotating cylinder 3 itself forms one with the high-frequency source connected electrode 7.
- the electrode 7 of the other polarity is of a Capacitor plate formed, which is arranged in the wrapping area of the cylinder 3 is.
- the high-frequency waves penetrate the fibrous web 1, which the Arrangement makes it very effective. Because of the function of the cylinder 3 as an electrode 7 it should have an electrically insulating coating in the moist area Own fibrous web 1.
- all electrodes 7 are formed by stick electrodes in FIG. 3, which are arranged in the wrapping area of the cylinder 3.
- the one High-frequency source (HF) connected electrodes are polarized so that Adjacent stick electrodes always have different polarities. That I field forming between the electrodes 7 penetrates the fibrous web 1 at least partially, which also leads to the heating and drying of the damp areas the fibrous web 1 leads.
- HF High-frequency source
- the stick electrodes as well as the capacitor plate extend essentially across the fibrous web 1 and parallel to the cylinder 3.
- the devices can be in several places on a paper or coating machine be arranged. Furthermore, the entire drying process can will be realized. However, such devices are preferably for Moisture cross profile correction in dryer sections with conventionally heated Drying cylinders, which are wrapped in the fibrous web.
Abstract
Description
Die Erfindung betrifft ein Verfahren sowie die dazugehörigen Vorrichtungen zur Feuchteprofilierung einer zu trocknenden Faserstoffbahn, insbesondere einer Papier-, Karton- oder Tissuebahn in Maschinen zur Herstellung und/oder Veredelung derselben.The invention relates to a method and the associated devices for Moisture profiling of a fibrous web to be dried, in particular a paper, Cardboard or tissue web in machines for the production and / or finishing of the same.
Gegenwärtig werden die Faserstoffbahnen zur Trocknung über beheizte Zylinder geführt. Bei diesem aufwendigen Prozeß stellt sich oft eine ungleiche Verteilung der Feuchte quer zur Faserstoffbahn ein. Zur Korrektur dieses Feuchtequerprofils werden bestimmte Zonen zusätzlich befeuchtet oder beheizt, wobei die Beheizung im allgemeinen induktiv oder mittels IR-Strahler und die Befeuchtung mit Dampf erfolgt.The fibrous webs are currently used for drying over heated cylinders guided. This complex process often results in an uneven distribution of the Moisture across the fibrous web. To correct this moisture cross profile certain zones additionally humidified or heated, the heating in the generally done inductively or by means of IR radiators and humidification with steam.
Diese Korrekturmaßnahmen sind jedoch relativ ungenau. Außerdem ist das Messen und Regeln des Feuchteprofils sehr aufwendig.However, these corrective actions are relatively imprecise. It's also measuring and regulating the moisture profile is very complex.
Die Aufgabe der Erfindung ist es daher ein möglichst einfaches und genaues Verfahren sowie zumindest eine entsprechende Vorrichtung zur Feuchteprofilierung zu entwickeln.The object of the invention is therefore a method that is as simple and precise as possible and to develop at least one corresponding device for moisture profiling.
Erfindungsgemäß wurde die Aufgabe dadurch gelöst, daß die Faserstoffbahn elektromagnetischen Wellen in Form von Mikrowellen und/oder Hochfrequenzwellen ausgesetzt wird. Dies erfolgt im wesentlichen dadurch, daß die Faserstoffbahn an zumindest einem Mikrowellen-Sender und/oder an zumindest zwei mit einer Hochfrequenz-Quelle verbundenen Elektroden unterschiedlicher Polarität vorbeigeführt wird.According to the invention the object was achieved in that the fibrous web electromagnetic waves in the form of microwaves and / or high frequency waves is exposed. This is essentially due to the fact that the fibrous web is on at least one microwave transmitter and / or at least two with one High-frequency source connected electrodes of different polarity passed becomes.
Durch den Einsatz von elektromagnetischen Wellen ergibt sich eine selbstregulierende Wirkung, da feuchtere Stellen der Faserstoffbahn stärker getrocknet werden. Dies basiert auf der Tatsache, daß Wasser diese Wellen stärker absorbiert als das trockene Papier, d.h. deren Fasern.The use of electromagnetic waves results in a self-regulating Effect, since more moist parts of the fibrous web are dried more. This is based on the fact that water absorbs these waves more than the dry one Paper, i.e. whose fibers.
Indem man hierbei das Dielektrikum Wasser einem elektrischen Feld aussetzt, kommt es zur Polarisation, also der Verschiebung von geladenen Teilchen aus der Ruhelage. Dabei entstehen Verluste, die zu einer Erwärmung des Wassers führen. Der Hochfrequenzbereich liegt etwa im Bereich zwischen 10 und 300 MHz und der Mikrowellenbereich zwischen 300 MHz und 30 GHz. Zur Gewährleistung einer gleichmäßigen Wirkung auf die Faserstoffbahn, sollte die Feldenergie der elektromagnetischen Wellen quer zur Faserstoffbahn möglichst auch gleichmäßig verteilt sein.By exposing the dielectric water to an electrical field it to polarization, i.e. the displacement of charged particles from the rest position. This results in losses that cause the water to heat up. The The high-frequency range lies approximately in the range between 10 and 300 MHz and the Microwave range between 300 MHz and 30 GHz. To ensure a uniform effect on the fibrous web, the Field energy of the electromagnetic waves across the fibrous web should also be possible be evenly distributed.
Anwendung findet das Verfahren in den Bereichen, wo die Faserstoffbahn einen Trockengehalt zwischen 60 und 95 % hat. In diesen Bereichen muß einerseits nicht zuviel Wasser erwärmt werden und ist aber andererseits ausreichend Feuchtigkeit zur Absorption der elektromagnetischen Wellen vorhanden.The method is used in the areas where the fibrous web unites Has a dry content between 60 and 95%. On the one hand, these areas do not have to too much water to be heated and on the other hand is sufficient moisture to Absorption of the electromagnetic waves is present.
Insbesondere bei hohen Geschwindigkeiten ist es von Vorteil, wenn die Faserstoffbahn auch im Bereich der elektromagnetischen Wellen gestützt verläuft. Dies stabilisiert den Lauf der Faserstoffbahn und verringert die Gefahr von Abrissen. Hierzu kann die Faserstoffbahn über einen rotierenden Zylinder geführt werden.Especially at high speeds, it is advantageous if the fibrous web is also supported in the area of electromagnetic waves. This stabilizes the Run of the fibrous web and reduces the risk of tearing. For this, the The fibrous web is guided over a rotating cylinder.
Je nach Art der Faserstoffbahn und/oder der Maschine ist es dabei durchaus möglich, daß die Trocknung der Faserstoffbahn zumindest überwiegend durch elektromagnetische Wellen erfolgt. Meistens wird jedoch die Trocknung auf konventionelle Weise, d.h. beispielsweise über beheizte Zylinder erfolgen, so daß elektromagnetische Wellen im wesentlichen nur zum Ausgleich von Feuchteunterschieden quer zur Faserstoffbahn dienen.Depending on the type of fibrous web and / or the machine, it is entirely possible that the drying of the fibrous web at least predominantly by electromagnetic waves occur. Most of the time, however, the drying on conventional way, i.e. for example via heated cylinders, so that electromagnetic waves essentially only to compensate for Differences in moisture serve across the fibrous web.
Als Mikrowellen-Sender kommen dabei vorzugsweise ein oder mehrere Hohlleiter zur Anwendung, die jeweils mit zumindest einer Mikrowellen-Quelle verbunden sind und wenigstens quer zur Faserstoffbahn möglichst gleichmäßig verteilt angeordnet sein sollten. Im Ergebnis entsteht eine relativ gleichmäßige Verteilung der Feldenergie der Mikrowellen quer zur Faserstoffbahn.One or more waveguides are preferably used as the microwave transmitter Application, which are each connected to at least one microwave source and at least transversely to the fibrous web as evenly distributed as possible should. The result is a relatively even distribution of field energy Microwaves across the fibrous web.
Zur Stützung sollte die Faserstoffbahn im Bereich der Mikrowellen über einen rotierenden Zylinder geführt werden.For support, the fibrous web should have a microwaves rotating cylinder.
Da die meist metallischen Zylinder zu einer Verringerung der Feldenergie der Mikrowellen in der Faserstoffbahn führen würden, sollte der Mantel des Zylinders oder eine äußere Beschichtung dieses Mantels aus einem Material bestehen, daß die Mikrowellen schlechter als die Faserstoffbahn absorbiert. Hierzu eignet sich beispielsweise Teflon. Die Stärke der Beschichtung sollte zwischen 5 und 150 mm, vorzugsweise zwischen 10 und 50 mm liegen.As the mostly metallic cylinders reduce the field energy of the Microwaves in the fibrous web would lead to the jacket of the cylinder or an outer coating of this jacket consist of a material that the Microwaves absorbed worse than the fibrous web. This is suitable for example Teflon. The thickness of the coating should be between 5 and 150 mm, are preferably between 10 and 50 mm.
Der Lauf der Faserstoffbahn kann jedoch auch für sich allein oder in Ergänzung von wenigstens einem Sieb unterstützt werden, dessen Material die Mikrowellen schlechter als die Faserstoffbahn absorbiert.However, the course of the fibrous web can also be used alone or in addition to at least one sieve is supported, the material of which the microwaves are worse than the fibrous web absorbs.
Im Falle des Einsatzes von Hochfrequenzwellen sollten die Elektroden die Form von Stabelektroden, Kondensatorplatten und/oder rotierende Zylindern haben.In the case of using high frequency waves, the electrodes should be in the form of Stick electrodes, capacitor plates and / or rotating cylinders.
Auch hierbei sollte die Faserstoffbahn im Bereich der Elektroden über einen rotierenden Zylinder geführt und vorzugsweise von einem Sieb gestützt sein.Here too, the fibrous web should rotate in the region of the electrodes Cylinder guided and preferably supported by a sieve.
Dabei ist es möglich, daß der vorzugsweise überwiegend metallisch ausgeführte Zylinder eine Elektrode bildet und auf der bezüglich der Faserstoffbahn gegenüberliegenden Seite zumindest eine Stabelektrode und/oder eine Kondensatorplatte anderer Polarität angeordnet ist. Als Schutzmaßnahme ist es dabei von Vorteil, wenn der Zylinder eine elektrisch isolierende, äußere Beschichtung besitzt. Es ist andererseits jedoch auch möglich, daß im Umschlingungsbereich des Zylinders zumindest zwei Stabelektroden verschiedener Polarität vorhanden sind, deren Hochfrequenzwellen teilweise die Faserstoffbahn durchdringen.It is possible that the preferably predominantly metallic Cylinder forms an electrode and on the with respect to the fibrous web opposite side at least one stick electrode and / or one Capacitor plate of different polarity is arranged. It is included as a protective measure an advantage if the cylinder has an electrically insulating outer coating. On the other hand, it is also possible that in the wrapping area of the cylinder there are at least two stick electrodes of different polarity, the High-frequency waves partially penetrate the fibrous web.
Unabhängig von der Art der Wellen, die auch kombiniert miteinander eingesetzt werden können, sollten diese Vorrichtungen eine elektromagnetische Abschirmung gegenüber der Umwelt besitzen.Regardless of the type of shaft, which can also be used in combination these devices should be shielded from electromagnetic interference own the environment.
Nachfolgend soll die Erfindung an mehreren Ausführungsbeispielen näher erläutert
werden. In den beigefügten Zeichnungen zeigt:
Alle Figuren zeigen einen Querschnitt durch einen Zylinder 3 mit der
erfindungsgemäßen Vorrichtung, wobei die Faserstoffbahn 1 den größten Teil des
Umfangs des rotierenden Zylinders 3 umschlingt. Der Zylinder 3 ist hierbei nicht separat
beheizt.All figures show a cross section through a
Gemäß Figur 1 ist entlang des Umschlingungsbereiches ein Mikrowellen-Sender 2
außerhalb des Zylinders 3 angeordnet.According to FIG. 1, there is a
Der Mikrowellen-Sender 2 besteht aus einer Aneinanderreihung von mehreren quer zur
Bahnlaufrichtung verlaufenden Hohlleitern mit rechteckigem Querschnitt, die jeweils mit
einer Mikrowellen-Quelle verbunden sind. Es ist dabei jedoch auch möglich, die
Hohlleiter mäanderförmig anzuordnen. Die davon ausgehenden Mikrowellen sorgen
dafür, daß die feuchteren Stellen der Faserstoffbahn 1 stärker erwärmt und damit
getrocknet werden als die übrigen Bereiche. Im Ergebnis entsteht ein vergleichmäßigtes
Feuchtequerprofil.The
Um den Mikrowellen-Sender 2 ist eine Abschirmung 6 angeordnet, so daß keine
Mikrowellen diese Vorrichtung verlassen. Der Zylinder 3 besitzt eine ca. 2 cm dicke
Beschichtung 4 aus Teflon, welche die Mikrowellen weniger stark absorbiert als die
Faserstoffbahn 1. Die Stärke der Beschichtung 4 sorgt dafür, daß der metallische
Bereich des Zylinders 3 möglichst weit weg von der Faserstoffbahn 1 liegt, so daß eine
möglichst große Feldstärke der Mikrowellen in der Faserstoffbahn 1 gewährleistet ist.A
Zur Stabilisierung des Laufes der Faserstoffbahn 1 dient ein mitlaufendes, bezüglich der
Oberfläche des Zylinders 2 außen liegendes Sieb 5, welches ebenfalls aus einem
Material besteht, das die Mikrowellen weniger stark absorbiert als die Faserstoffbahn 1.For the stabilization of the run of the
Die Figuren 2 und 3 zeigen Hochfrequenzvorrichtungen bei denen der Lauf der
Faserstoffbahn 1 über ein mitlaufendes, außenliegendes Sieb 5 stabilisiert wird.
Außerdem sind auch hier die Vorrichtungen mit einer Abschirmung 6 für die
Hochfrequenzwellen versehen. Figures 2 and 3 show high frequency devices in which the run of the
Fibrous
Die Faserstoffbahn 1 wird jedoch an mit einer Hochfrequenz-Quelle (HF) verbundenen
Elektroden unterschiedlicher Polarität vorbeigeführt. Dies führt ebenfalls zur Erwärmung
und Trocknung der feuchten Bereiche der Faserstoffbahn 1 mit dem Ergebnis
eines relativ gleichmäßigen Feuchtequerprofil.However, the
In Figur 2 bildet der metallische, rotierende Zylinder 3 selbst eine mit der Hochfrequenz-Quelle
verbundene Elektrode 7. Die Elektrode 7 der anderen Polarität wird von einer
Kondensatorplatte gebildet, die im Umschlingungsbereich des Zylinders 3 angeordnet
ist. Die Hochfrequenzwellen durchdringen dabei die Faserstoffbahn 1, was die
Anordnung sehr wirksam macht. Wegen der Funktion des Zylinders 3 als Elektrode 7
sollte er eine elektrisch isolierende Beschichtung im Bereich der feuchten
Faserstoffbahn 1 besitzen.In FIG. 2, the metallic, rotating
Im Gegensatz hierzu werden in Figur 3 alle Elektroden 7 von Stabelelektroden gebildet,
die im Umschlingungsbereich des Zylinders 3 angeordnet sind. Die mit einer
Hochfrequenz-Quelle (HF) verbundenen Elektroden sind dabei so gepolt, daß
benachbarte Stabelektroden immer unterschiedliche Polarität aufweisen. Das sich
zwischen den Elektroden 7 ausbildende Feld durchdringt dabei die Faserstoffbahn 1
zumindest teilweise, was ebenfalls zur Erwärmung und Trocknung der feuchten Stellen
der Faserstoffbahn 1 führt.In contrast to this, all
Die Stabelektroden wie auch die Kondensatorplatte erstrecken sich im wesentlichen
quer zur Faserstoffbahn 1 und parallel zum Zylinder 3.The stick electrodes as well as the capacitor plate extend essentially
across the
Die Vorrichtungen können an mehreren Stellen einer Papier- oder Streichmaschine angeordnet sein. Desweiteren kann damit auch der gesamte Trocknungsvorgang realisiert werden. Vorzugsweise befinden sich derartige Vorrichtungen jedoch zur Feuchtequerprofilkorrektur in Trockenpartien mit konventionell beheizten Trockenzylindern, die von der Faserstoffbahn umschlungen sind.The devices can be in several places on a paper or coating machine be arranged. Furthermore, the entire drying process can will be realized. However, such devices are preferably for Moisture cross profile correction in dryer sections with conventionally heated Drying cylinders, which are wrapped in the fibrous web.
Claims (20)
die Faserstoffbahn (1) elektromagnetischen Wellen in Form von Mikrowellen und/oder Hochfrequenzwellen ausgesetzt wird.Method for moisture profiling a fibrous web (1) to be dried in machines for producing and / or finishing the same, characterized in that
the fibrous web (1) is exposed to electromagnetic waves in the form of microwaves and / or high-frequency waves.
die Feldenergie der elektromagnetischen Wellen quer zur Faserstoffbahn (1) möglichst gleichmäßig verteilt ist.A method according to claim 1, characterized in that
the field energy of the electromagnetic waves is distributed as evenly as possible across the fibrous web (1).
die elektromagnetischen Wellen bei einem Trockengehalt der Faserstoffbahn (1) zwischen 60-95 % zum Einsatz kommen.A method according to claim 1 or 2, characterized in that
the electromagnetic waves are used when the dry matter content of the fibrous web (1) is between 60-95%.
die Faserstoffbahn (1) zumindest im Bereich der elektromagnetischen Wellen gestützt verläuft.Method according to one of the preceding claims, characterized in that
the fibrous web (1) runs at least in the region of the electromagnetic waves.
die Trocknung der Faserstoffbahn (1) zumindest überwiegend durch die elektromagnetischen Wellen erfolgt.Method according to one of the preceding claims, characterized in that
the fibrous web (1) is at least predominantly dried by the electromagnetic waves.
die Trocknung der Faserstoffbahn (1) nur zu einem geringen Teil über die elektromagnetischen Wellen erfolgt und vorzugsweise zum Ausgleich von Feuchteunterschieden quer zur Faserstoffbahn (1) dient. Method according to one of claims 1 to 4, characterized in that
the fibrous web (1) is only dried to a small extent via the electromagnetic waves and is preferably used to compensate for moisture differences across the fibrous web (1).
die Faserstoffbahn (1) an zumindest einem Mikrowellen-Sender (2) vorbeigeführt wird.Device for carrying out the method according to one of the preceding claims, characterized in that
the fibrous web (1) is guided past at least one microwave transmitter (2).
der Mikrowellen-Sender (2) aus einem oder mehreren Hohlleitern besteht, die jeweils mit zumindest einer Mikrowellen-Quelle verbunden sind.Apparatus according to claim 7, characterized in that
the microwave transmitter (2) consists of one or more waveguides, each of which is connected to at least one microwave source.
die Hohlleiter quer zur Faserstoffbahn (1) möglichst gleichmäßig verteilt sind.Apparatus according to claim 8, characterized in that
the waveguides are distributed as evenly as possible across the fibrous web (1).
die Faserstoffbahn (1) im Bereich eines Mikrowellen-Senders (2) über einen rotierenden Zylinder (3) geführt wird.Device according to one of claims 7 to 9, characterized in that
the fibrous web (1) is guided in the area of a microwave transmitter (2) via a rotating cylinder (3).
der Mantel des Zylinders (3) oder eine äußere Beschichtung (4) dieses Mantels aus einem Material besteht, welches die Mikrowellen schlechter als die Faserstoffbahn (1) absorbiert.Apparatus according to claim 10, characterized in that
the jacket of the cylinder (3) or an outer coating (4) of this jacket consists of a material which absorbs the microwaves less well than the fibrous web (1).
die Dicke der äußeren Beschichtung (4) zwischen 5 und 150 mm, insbesondere zwischen 10 und 50 mm liegt.Device according to claim 11, characterized in that
the thickness of the outer coating (4) is between 5 and 150 mm, in particular between 10 and 50 mm.
der Lauf der Faserstoffbahn (1) von wenigstens einem Sieb (5) unterstützt wird, dessen Material die Mikrowellen schlechter als die Faserstoffbahn (1) absorbiert.Device according to one of claims 7 to 12, characterized in that
the run of the fibrous web (1) is supported by at least one sieve (5), the material of which absorbs the microwaves worse than the fibrous web (1).
die Faserstoffbahn (1) an zumindest zwei mit einer Hochfrequenz-Quelle verbundenen Elektroden (7) unterschiedlicher Polarität vorbeigeführt wird. Device according to one of the preceding claims, characterized in that
the fibrous web (1) is guided past at least two electrodes (7) of different polarity connected to a high-frequency source.
die Elektroden die Form von Stabelektroden, Kondensatorplatten und/oder rotierenden Zylindern (3) haben.Device according to claim 14, characterized in that
the electrodes are in the form of stick electrodes, capacitor plates and / or rotating cylinders (3).
die Faserstoffbahn (1) im Bereich der Elektroden (7) über einen rotierenden Zylinder (3) geführt und vorzugsweise von einem Sieb (5) gestützt ist.Apparatus according to claim 14 or 15, characterized in that
the fibrous web (1) is guided in the region of the electrodes (7) over a rotating cylinder (3) and is preferably supported by a sieve (5).
der vorzugsweise überwiegend metallisch ausgeführte Zylinder (3) eine Elektrode (7) bildet und auf der bezüglich der Faserstoffbahn (1) gegenüberliegende Seite zumindest eine Stabelektrode und/oder eine Kondensatorplatte anderer Polarität angeordnet ist.Device according to claim 15 or 16, characterized in that
the preferably predominantly metallic cylinder (3) forms an electrode (7) and at least one rod electrode and / or a capacitor plate of a different polarity is arranged on the side opposite the fibrous web (1).
der Zylinder (3) eine elektrisch isolierende, äußere Beschichtung besitzt.Apparatus according to claim 17, characterized in that
the cylinder (3) has an electrically insulating, outer coating.
im Umschlingungsbereich des Zylinders (3) zumindest zwei Stabelektroden verschiedener Polarität vorhanden sind, deren Hochfrequenzwellen teilweise die Faserstoffbahn (1) durchdringen.Apparatus according to claim 16, characterized in that
At least two rod electrodes of different polarity are present in the wrapping area of the cylinder (3), the high-frequency waves of which partially penetrate the fibrous web (1).
die Vorrichtung eine elektromagnetische Abschirmung (6) besitzt.Device according to one of claims 7 to 19, characterized in that
the device has an electromagnetic shield (6).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19841638A DE19841638A1 (en) | 1998-09-11 | 1998-09-11 | Moisture profiling |
DE19841638 | 1998-09-11 |
Publications (2)
Publication Number | Publication Date |
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EP0989231A2 true EP0989231A2 (en) | 2000-03-29 |
EP0989231A3 EP0989231A3 (en) | 2001-04-25 |
Family
ID=7880651
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP99112923A Withdrawn EP0989231A3 (en) | 1998-09-11 | 1999-07-05 | Controlling the moisture profile |
Country Status (3)
Country | Link |
---|---|
US (2) | US6425190B1 (en) |
EP (1) | EP0989231A3 (en) |
DE (1) | DE19841638A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6736935B2 (en) | 2002-06-27 | 2004-05-18 | Kimberly-Clark Worldwide, Inc. | Drying process having a profile leveling intermediate and final drying stages |
WO2004083523A1 (en) * | 2003-03-21 | 2004-09-30 | Saueressig Gmbh + Co. | Production method for an absorbent fibre product and corresponding absorbent fibre product |
CN109631546A (en) * | 2018-11-12 | 2019-04-16 | 芜湖顺成电子有限公司 | A kind of spiral electric wire drying unit |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10305598A1 (en) * | 2003-02-11 | 2004-08-19 | Voith Paper Patent Gmbh | Material web moisture content determination method, e.g. a paper or card web, whereby an infrared moisture sensor is used that is mounted on a beam so that it can be moved over the whole web width |
DE10319724A1 (en) * | 2003-05-02 | 2005-01-20 | Voith Paper Patent Gmbh | Process to increase the dry matter content in a wet paper web by exposure to microwave energy |
DE10347587A1 (en) * | 2003-10-14 | 2005-05-19 | Voith Paper Patent Gmbh | Papermaking assembly drying station or smoothing drum for wet web of carton, paper or tissue sets up oscillation in drying or smoothing station |
FI20051096A (en) * | 2005-10-31 | 2007-05-01 | Savcor Process Oy | Procedure in a wet portion of a paper machine, cardboard machine or other similar forming machine |
DE102008038215A1 (en) * | 2008-08-18 | 2010-02-25 | Siemens Aktiengesellschaft | Method and device for drying a paper web |
DE102008062320B3 (en) * | 2008-12-15 | 2010-04-15 | Siemens Aktiengesellschaft | Drying chamber for the dielectric drying of a material, in particular a paper web |
ATE529568T1 (en) * | 2008-12-23 | 2011-11-15 | Tecnerga S R L | SYSTEM FOR ADJUSTING AND CONTROLLING THE WATER CONTENT OF PAPER DURING THE PRODUCTION CYCLE |
US9481777B2 (en) | 2012-03-30 | 2016-11-01 | The Procter & Gamble Company | Method of dewatering in a continuous high internal phase emulsion foam forming process |
CN108518951B (en) * | 2018-03-27 | 2019-11-05 | 宁波雯泽纺织品有限公司 | Textile processing drying equipment |
CN114608294B (en) * | 2020-12-07 | 2023-09-08 | 辛集市祥光绒布有限公司 | Large-scale vertical cloth drying device |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU445577B2 (en) * | 1968-06-14 | 1974-02-08 | Ford Russell George | Process and apparatus for moisture contents de-peaking and equalization |
US3952421A (en) * | 1974-10-18 | 1976-04-27 | Chemetron Corporation | Dielectric heating arrangement for drying a continuously moving web of material |
DE3445615A1 (en) * | 1984-12-14 | 1986-06-19 | Maschinenfabrik Horst Kabus GmbH, 7085 Bopfingen | Method for drying webs made of paper, textile or the like |
WO1992012291A1 (en) * | 1991-01-07 | 1992-07-23 | Sven Gunnar Nygren | Controlling moisture content in a paper-making process |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE697509C (en) * | 1936-06-11 | 1940-10-16 | Siemens Schuckertwerke Akt Ges | Drying device for paper webs on paper machines |
DE691038C (en) * | 1937-07-01 | 1940-05-15 | Siemens Schuckertwerke Akt Ges | Device for drying paper webs and similar material webs |
DE694637C (en) * | 1937-09-03 | 1940-08-05 | Siemens Schuckertwerke Akt Ges | Device for heating, in particular drying, of wood, paper or similar objects in an electrical field |
US2319174A (en) * | 1942-06-23 | 1943-05-11 | Fred K H Levey Co Inc | Method of and apparatus for printing |
GB1027589A (en) * | 1964-06-04 | 1966-04-27 | Fitchburg Paper | Drying travelling webs |
DE1959116A1 (en) * | 1969-11-25 | 1971-05-27 | Boehmer Eisenwerk Kg | Aufrueckvorrichtung for rail car |
US4188731A (en) * | 1976-08-25 | 1980-02-19 | Rauskolb Fred W | Method and apparatus for eliminating wet streaks in fibrous sheets or webs by infra-red radiation |
DE2816551C3 (en) | 1978-04-17 | 1981-11-26 | SIEMENS AG AAAAA, 1000 Berlin und 8000 München | Drying control on a paper machine |
FI74062C (en) * | 1985-12-12 | 1987-12-10 | Imatran Voima Oy | FOERFARANDE OCH ANORDNING FOER MINSKNING HOEGFREKVENT ELENERGI AV FUKTIGHETSDIFFERENSERNA HOS EN ROERLIG BANA MEDELST. |
US4738752A (en) * | 1986-08-12 | 1988-04-19 | Beloit Corporation | Heated extended nip press apparatus |
FI80099C (en) * | 1986-10-31 | 1990-04-10 | Imatran Voima Oy | FOERFARANDE OCH ANORDNING FOER TORKNING AV ROERLIGT BANMATERIAL. |
US5064979A (en) * | 1990-08-07 | 1991-11-12 | W. R. Grace & Co.-Conn. | Microwave air float bar for drying a traveling web |
ATE129067T1 (en) * | 1990-12-17 | 1995-10-15 | Per Erik Gustafsson | ARRANGEMENT FOR GENERATING ENERGY AND METHOD FOR USE OF THE SAME. |
DE4121203A1 (en) * | 1991-06-27 | 1993-01-14 | Alfred Linden | Varnished paper and cardboard dryer - has hollow conductors to deliver microwave energy to moving material across its line of travel |
FI103820B1 (en) * | 1993-11-30 | 1999-09-30 | Valmet Paper Machinery Inc | Procedures for drying a paper web and drying parts for paper machine |
JP3077879B2 (en) * | 1994-02-15 | 2000-08-21 | インターナショナル・ビジネス・マシーンズ・コーポレ−ション | Apparatus and method for applying microwave energy to a web-type quantified processing material |
US5659972A (en) * | 1995-10-06 | 1997-08-26 | Avery Dennison Corporation | Apparatus and method for drying or curing web materials and coatings |
US5863613A (en) * | 1996-12-20 | 1999-01-26 | Ppg Industries, Inc. | Apparatus and method for spray painting of an article |
-
1998
- 1998-09-11 DE DE19841638A patent/DE19841638A1/en not_active Withdrawn
-
1999
- 1999-07-05 EP EP99112923A patent/EP0989231A3/en not_active Withdrawn
- 1999-09-10 US US09/393,690 patent/US6425190B1/en not_active Expired - Fee Related
-
2001
- 2001-09-18 US US09/954,053 patent/US6463677B2/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU445577B2 (en) * | 1968-06-14 | 1974-02-08 | Ford Russell George | Process and apparatus for moisture contents de-peaking and equalization |
US3952421A (en) * | 1974-10-18 | 1976-04-27 | Chemetron Corporation | Dielectric heating arrangement for drying a continuously moving web of material |
DE3445615A1 (en) * | 1984-12-14 | 1986-06-19 | Maschinenfabrik Horst Kabus GmbH, 7085 Bopfingen | Method for drying webs made of paper, textile or the like |
WO1992012291A1 (en) * | 1991-01-07 | 1992-07-23 | Sven Gunnar Nygren | Controlling moisture content in a paper-making process |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6736935B2 (en) | 2002-06-27 | 2004-05-18 | Kimberly-Clark Worldwide, Inc. | Drying process having a profile leveling intermediate and final drying stages |
WO2004083523A1 (en) * | 2003-03-21 | 2004-09-30 | Saueressig Gmbh + Co. | Production method for an absorbent fibre product and corresponding absorbent fibre product |
US7758722B2 (en) | 2003-03-21 | 2010-07-20 | Saueressig Gmbh + Co. | Production method for an absorbent fiber product and corresponding absorbent fiber product |
CN109631546A (en) * | 2018-11-12 | 2019-04-16 | 芜湖顺成电子有限公司 | A kind of spiral electric wire drying unit |
Also Published As
Publication number | Publication date |
---|---|
US20020043004A1 (en) | 2002-04-18 |
US6425190B1 (en) | 2002-07-30 |
EP0989231A3 (en) | 2001-04-25 |
DE19841638A1 (en) | 2000-03-16 |
US6463677B2 (en) | 2002-10-15 |
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