[go: up one dir, main page]

EP0388793B1 - Method for making tobacco shreds - Google Patents

Method for making tobacco shreds Download PDF

Info

Publication number
EP0388793B1
EP0388793B1 EP90104900A EP90104900A EP0388793B1 EP 0388793 B1 EP0388793 B1 EP 0388793B1 EP 90104900 A EP90104900 A EP 90104900A EP 90104900 A EP90104900 A EP 90104900A EP 0388793 B1 EP0388793 B1 EP 0388793B1
Authority
EP
European Patent Office
Prior art keywords
tobacco
cut
bales
cutter
pressed
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
EP90104900A
Other languages
German (de)
French (fr)
Other versions
EP0388793A1 (en
Inventor
Manfred Dipl.-Ing. Lasch
Klaus-Georg Hackmack
Reinhard Dipl.-Ing. Liebe
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.)
Koerber AG
Original Assignee
Hauni Werke Koerber and Co KG
Koerber AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hauni Werke Koerber and Co KG, Koerber AG filed Critical Hauni Werke Koerber and Co KG
Priority to AT90104900T priority Critical patent/ATE99503T1/en
Publication of EP0388793A1 publication Critical patent/EP0388793A1/en
Application granted granted Critical
Publication of EP0388793B1 publication Critical patent/EP0388793B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00Preparing tobacco in the factory
    • A24B3/02Humidifying packed raw tobacco
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B7/00Cutting tobacco
    • A24B7/14Feeding or control devices for tobacco-cutting apparatus

Definitions

  • tobacco is dried relatively strongly, ie to a residual moisture content of about 8-11%, and is usually pressed for dispatch in cuboid or cylindrical bales or packages, although other forms of compression are also possible.
  • the tobacco can be pure pre-stripped leaf material (without substantial rib parts); the ribs removed before drying, which are processed separately and mixed into the leaf tobacco, can also be pressed and shipped in a dry state.
  • the pressed and relatively dry tobacco can also be stored for a long time in this condition. Should this relatively dry tobacco be used for smoking products, e.g. B. cigarettes are processed, it is necessary in the known processing methods, the individual sheets (or leaf pieces) or ribs (or rib pieces) in the pressed bale to separate and separate from each other.
  • the tobacco is compressed very strongly by means of converging press chains (one speaks of a "tobacco cake") before slices of fiber can be cut off on a mouthpiece by rotating knives.
  • the cut tobacco must then be dried again to the processing moisture of 12.5 to 13.5%, in which it is processed into cigarettes, for example on a cigarette machine.
  • the object on which the invention is based is to cut tobacco without a great deal of energy and equipment, and the process parameters can be selected such that good results are achieved with regard to the filling power of the cut tobacco produced.
  • this is achieved in that the tobacco is cut in a tobacco cutter at a humidity between 10% and 17% and a minimum temperature of ambient temperature (18 ° C to 25 ° C).
  • This cutting can be carried out in such a way that the pressed tobacco parts are not detached from one another beforehand, but rather that the tobacco, compressed into bales or pieces of bale, is fed to the tobacco cutter with its shipping moisture and room temperature and is processed by it to cut tobacco.
  • the tobacco can also be dissolved at a slightly elevated temperature and / or humidity before it is fed to the tobacco cutter.
  • the tobacco is used less because of dampening and drying processes that mechanically stress the tobacco and lead to an undesirable fiber shortening.
  • a very advantageous development of the invention is that the tobacco is fed to the tobacco cutter as tobacco pressed in bales or parts thereof and cut into cut tobacco without further moistening.
  • the tobacco pressed in bales or parts thereof can, however, also be heated to a temperature of at least 30 ° C., preferably at least 40 ° C., for example 40 ° C. to 50 ° C., before cutting, which further improves the cutting result.
  • very low moisture values i.e. at low shipping moisture values, and room temperature or very little elevated temperature, there is a loosening of the tobacco particles, e.g. B.
  • the tobacco leaves each other the risk of tobacco damage.
  • the tobacco to be cut must therefore be prepared if the pieces supplied do not exactly meet the aforementioned conditions.
  • the bales are broken up so far that the single sheets and / or smaller or larger lumps of them fill the baling chamber of the tobacco cutter between its chain in front of the cutting knives sufficiently homogeneously. If it was stated in the above that the heated tobacco should be loosened, after which the loosened tobacco is fed directly to the tobacco cutter, this means that the temperature drop during loosening and conveying to the tobacco cutter must not be so great that the Tobacco comes too cold in the tobacco cutter, because then the tobacco leaves in the tobacco cutter can be damaged by the pressing forces.
  • the tobacco Before loosening and cutting, the tobacco should therefore be warmed up to such an extent that it has a minimum temperature of 30 ° C in the tobacco cutter, but preferably about 40 ° C and above, for example between 40 ° C and 50 ° C. In this case, it is pliable enough to withstand the pressing forces.
  • the tobacco pressed in bales or parts thereof can advantageously be heated by exposure to microwaves or high-frequency electrical fields, as described in US Pat. No. 4,799,501. With such heating, the tobacco is not moistened at the same time. If it is desired to wet the tobacco when it is heated, which makes it even more supple and allows it to be dissolved at considerably lower temperatures, this is possible in a manner known per se and described, for example, by US Pat. No.
  • the energy required for heating and possibly drying is considerably less than when dampening to a relative humidity of 18% and above with conventional conditioning methods or when heating to high temperatures before cutting.
  • the plants for treating the tobacco with the optimal parameters according to the invention are not very expensive.
  • undesirable taste influences of the tobacco as a result of heating to high temperatures, which must be kept for a longer period of time to dry, are avoided and good values for the filling power of the tobacco are achieved.
  • Damping can be done by passing saturated steam or dry steam onto the dissolved tobacco, for example while this is being conveyed on a vibratory conveyor.
  • the steam can then be supplied from below.
  • the tobacco temperature can be around 60 ° C after steaming, but they can also be increased to around 90 ° C.
  • the warm and dry cut tobacco (leaf cut, rib cut, mixture of leaf and rib cut) leaving the tobacco cutter is, preferably immediately afterwards, d. H. before cooling, moistened, which can be done in a conventional manner in a wet drum, as z. B. is described in U.S. Patent 4,054,145 or 3,948,277.
  • the cut tobacco is moistened in a so-called steam tunnel, which has a vibrating feed channel with steam inlets and z. B. is described in US-PS 4 004 594 or GB-OS 2 138 666.
  • the tobacco moisture can be increased in order to minimize the energy expenditure until the further processing moisture (12 to 13.5%), which the tobacco has after cooling to room temperature and with which it is processed in cigarette machines. However, it can also be moistened to higher degrees of moisture (over 20%) in order to increase its filling power, after which it is dried down to the processing moisture.
  • the moistening preferably takes place immediately after cutting, so that the relatively dry but still warm cut tobacco reaches the moistening device before it has cooled down.
  • the tobacco fibers of different types or types of tobacco can be mixed with one another U.S. Patent 4,116,203 is suitable.
  • the advantage achieved by the invention is that a method is specified how bale-pressed tobacco can be processed into usable cut tobacco with minimal use of energy and equipment, without the extensive and energy-consuming dissolving, dampening and drying equipment being used were previously considered necessary. These systems change the taste of tobacco and reduce its size. If the tobacco is to be fed to the tobacco cutter in a dissolved form, which offers advantages for its operation, it is advantageously slightly warmed and / or moistened, for which reasonably priced systems are suitable. The energy consumption is also low.
  • the conditioning of the tobacco for loosening can be done with little energy and with simple systems, because it has been found that the tobacco leaves do not have to be completely detached from one another, but it is sufficient if the tobacco is loosely loosened so that the tobacco cutter's pressing space is at least approximately homogeneous is filled. If necessary, the tobacco can be fed to a steaming system before it is cut, in which its temperature and humidity are increased.
  • the heating to 40 ° C and 75 ° C was carried out by exposing the tobacco to microwaves. After cutting, the tobacco was brought to a moisture level of 12.04% and its filling power was determined in mm remaining height.
  • the following shows the relationship between the remaining height of the Borgwald densimeter and the cutting moisture or cutting temperature of the tobacco: Moisture content [%] Temperature [° C] Residual height [mm] (Borgwald densimeter) 8th 8th 40 36.04 8th 75 37.10 11 20th 34.26 11 40 38.23 11 75 38.26 13 20th 38.05 13 40 39.66 13 75 38.16 3.
  • Pressed raw Virginia tobacco tobacco leaves
  • a moisture content of 8.4% shipment moisture
  • the tobacco was cut with a condition of approx. 65 ° C. and a moisture content of 11.8% by means of a tobacco cutter from the applicant of the type KTH. After cutting, the tobacco was brought to a moisture of 13%, which corresponds approximately to the processing moisture at which cigarettes are made from the tobacco.
  • the residual height in the Borgwald densimeter was 36.31 mm at this humidity.
  • a similar hardness value was achieved after the leaves were separated from each other after dampening and heating and before cutting and were fed to the tobacco cutter in a loose formation.
  • a reference sample of the same tobacco which had been brought to the aforementioned condition of 65 ° C. and 11.8% moisture in the same way, was first subjected to a dissolving step in which the tobacco leaves were separated from one another. After dissolving, the tobacco was moistened in a conventional manner, namely by means of a so-called steam tunnel (US Pat. No. 4,004,594) to a moisture content of 21% and cut into tobacco fibers at room temperature. These fibers were heated in a HT vibration tunnel by the applicant (GB-OS 2 138 666) to a temperature of approx.

Landscapes

  • Manufacture Of Tobacco Products (AREA)

Abstract

A method is described for making tobacco shreds from tobacco, particularly from tobacco leaves, which is supplied pressed into bales or parts thereof. <??>The invention resides in the fact that the tobacco is shredded in a tobacco shredder at a humidity of between 10% and 17% and a minimum temperature of ambient temperature (18 DEG C to 25 DEG C) without further processing.

Description

Verfahren zum Herstellen von Schnittabak aus Tabak, insbesondere aus Tabakblättern, der in Ballen oder Teilen davon gepreßt angeliefert wird.Process for producing cut tobacco from tobacco, in particular from tobacco leaves, which is delivered pressed in bales or parts thereof.

Tabak wird nach der Ernte relativ stark, d. h. auf eine Restfeuchte von etwa 8 - 11 % getrocknet und zum Versand gewöhnlich in quader- oder zylinderförmigen Ballen oder Paketen gepreßt, wobei auch andere Preßformen möglich sind. Bei dem Tabak kann es sich um reines vorentripptes Blattgut (ohne wesentliche Rippenanteile) handeln; die vor dem Trocknen entfernten Rippen, die getrennt weiterverarbeitet und dem Blattabak wieder zugemischt werden, können für sich ebenfalls in trockenem Zustand verpreßt und versandt werden. Der gepreßte und relativ trockene Tabak kann in diesem Zustand auch über längere Zeit gelagert werden.
Soll dieser relativ trockene Tabak zu Rauchprodukten, z. B. Zigaretten, verarbeitet werden, so ist es bei den bekannten Verarbeitungsverfahren erforderlich, die einzelnen Blätter (oder Blattstücke) bzw. Rippen (oder Rippenstücke) in den gepreßten Ballen wieder voneinander zu lösen und zu vereinzeln. Da die Blätter stark aneinanderhaften und sehr trocken sind, wodurch sie brüchig und sehr empfindlich gegen mechanische Einwirkungen sind, muß das Lösen schonend geschehen. Die heute überwiegend angewandte Methode des Lösens besteht darin, den Ballen in eine Vakuumkammer zu verbringen und durch einen oder mehrere Dorne, die in den Ballen getrieben werden, Dampf zuzuführen, der wegen des außen herrschenden Vakuums nach außen strömt und den Tabak erwärmt und befeuchtet, wodurch er geschmeidig wird, so daß die Blätter voneinander gelöst werden können. Diese Methode, die z. B. in der US-PS 3 372 703 beschrieben ist, ist apparativ aufwendig und erfordert zusätzlich einen beträchtlichen Energieaufwand. Anschließend an das zum Lösen erforderliche Feuchten auf ca. 12 bis 14 % Feuchte wird der Tabak bei konventionellen Verarbeitungsanlagen auf eine Schneidfeuchte von ca. 18 bis 23 % bei Tabakblättern und auf bis zu 30 % bei Rippen hochgefeuchtet und in einem Tabakschneider zu Schnittabak geschnitten. Hierbei wird der Tabak bei modernen Schneidern mittels konvergierender Preßketten sehr stark verdichtet (man spricht von einem "Tabakkuchen"), bevor an einem Mundstück von rotierenden Messern Scheiben aus Fasern abgeschnitten werden können. Der geschnittene Tabak muß dann wieder abgetrocknet werden bis auf die Verarbeitungsfeuchte von 12,5 bis 13,5 %, bei der er z.B. auf einer Zigarettenmaschine zu Zigaretten verarbeitet wird.
After the harvest, tobacco is dried relatively strongly, ie to a residual moisture content of about 8-11%, and is usually pressed for dispatch in cuboid or cylindrical bales or packages, although other forms of compression are also possible. The tobacco can be pure pre-stripped leaf material (without substantial rib parts); the ribs removed before drying, which are processed separately and mixed into the leaf tobacco, can also be pressed and shipped in a dry state. The pressed and relatively dry tobacco can also be stored for a long time in this condition.
Should this relatively dry tobacco be used for smoking products, e.g. B. cigarettes are processed, it is necessary in the known processing methods, the individual sheets (or leaf pieces) or ribs (or rib pieces) in the pressed bale to separate and separate from each other. Since the leaves stick together and are very dry, which makes them brittle and very sensitive to mechanical influences, they must be removed carefully. The method of loosening that is predominantly used today is to place the bale in a vacuum chamber and to supply steam through one or more mandrels which are driven in the bale, which flows outwards because of the external vacuum and warms and humidifies the tobacco, making it supple so that the leaves can be detached from each other. This method, the z. B. is described in US Pat. No. 3,372,703, is expensive in terms of equipment and additionally requires a considerable amount of energy. Subsequent to the moisture required for loosening to approx. 12 to 14% moisture, the tobacco in conventional processing systems is moistened to a cutting moisture of approx. 18 to 23% for tobacco leaves and up to 30% for ribs and cut into cut tobacco in a tobacco cutter. In modern tailors, the tobacco is compressed very strongly by means of converging press chains (one speaks of a "tobacco cake") before slices of fiber can be cut off on a mouthpiece by rotating knives. The cut tobacco must then be dried again to the processing moisture of 12.5 to 13.5%, in which it is processed into cigarettes, for example on a cigarette machine.

Alle diese Verfahrensschritte vom Lösen über das Hochfeuchten bis zu dem Rücktrocknen sind energie- und kostenaufwendig.
Durch die GB-OS 2 141 319 ist es schon bekanntgeworden, anstelle von Vakuum-Feuchtanlagen Mikrowellen zum Lösen von Tabak zu verwenden, wobei die Haftungskräfte zwischen den Tabakteilen durch Erwärmen mittels der Mikrowellen verringert werden, doch werden auch bei diesem bekannten Verfahren die gelösten Tabakblätter auf Schneidfeuchte hochgefeuchtet, so daß der Schnitttabak anschließend ebenfalls wieder abgetrocknet werden muß. Es geht somit auch bei dem zuletzt erwähnten Verfahren Energie durch das Auffeuchten und Wiederabtrocknen verloren.
In der US-PS 4 799 501 ist ein Verfahren und eine Anlage zum Schneiden von Tabak beschrieben, wobei Ballen von relativ trockenem Tabak mittels Mikrowellen erwärmt und anschließend vor dem Abkühlen einem Tabakschneider zugeführt werden. Die Ballen (oder auch Ballenstücke davon) haben dabei die gleiche-Größe nach Breite und Höhe, wozu die meist größeren Versandballen erst in passende Teilstücke unterteilt werden müssen.
All of these process steps, from dissolving to high-humidification and back drying, are energy and cost-intensive.
From GB-OS 2 141 319 it has already become known to use microwaves for loosening tobacco instead of vacuum dampening systems, the adhesive forces between the tobacco parts being reduced by heating by means of the microwaves, but also in this known method the loosened tobacco leaves moistened to cutting moisture, so that the cut tobacco must then also be dried again. Thus, even in the last-mentioned process, energy is lost as a result of moistening and drying again.
US Pat. No. 4,799,501 describes a method and a plant for cutting tobacco, wherein bales of relatively dry tobacco are heated by means of microwaves and then fed to a tobacco cutter before cooling. The bales (or bale pieces thereof) have the same size in terms of width and height, for which purpose the mostly larger shipping bales first have to be divided into suitable sections.

Die der Erfindung zugrundeliegende Aufgabe besteht darin, das Schneiden von Tabak ohne großen Aufwand an Energie und Anlagen durchzuführen, wobei die Verfahrensparameter so gewählt werden können, daß gute Ergebnisse bezüglich der Füllkraft des erzeugten Schnittabaks erzielt werden.
Gemäß der Erfindung wird dies dadurch erreicht, daß der Tabak bei einer Feuchte zwischen 10 % und 17 % und einer Mindesttemperatur von Umgebungstemperatur (18 °C bis 25 °C) in einem Tabakschneider geschnitten wird.
Dieses Schneiden kann derart erfolgen, daß kein vorheriges Lösen der gepreßten Tabakteile voneinander stattfindet, sondern daß der Tabak in Ballen oder Ballenstücken verpreßt mit seiner Versandfeuchte und Raumtemperatur dem Tabakschneider zugeführt wird und von diesem zu Schnittabak verarbeitet wird. Wie anschließend noch ausgeführt wird, kann aber bei etwas erhöhter Temperatur und/oder Feuchte der Tabak auch gelöst werden, bevor er dem Tabakschneider zugeführt wird. Dies hat insofern Vorteile, als der Betrieb des Tabakschneiders unproblematischer wird.
Gute Ergebnisse beim Schneiden erhält man dann, wenn der Tabak bei einer Feuchte zwischen 11 % und 16 %, bevorzugt zwischen 13% und 16 %, z.B. ca. 14 %, in einem Tabakschneider geschnitten wird.
Eine sehr vorteilhafte Feuchtekondition des Tabaks beim Schneiden besteht darin, ihm die Feuchte zu verleihen, die der Tabak bei der weiteren Verarbeitung in Zigarettenmaschinen aufweisen soll. Es sind dies Feuchtewerte zwischen 12,5 und 13,5 %, die in Ausnahmefällen geringfügig unter- bzw. überschritten werden können. Der Tabak läßt sich bei solchen Feuchtewerten sehr gut direkt, also ohne das bisher für erforderlich gehaltene Auffeuchten auf Werte zwischen 18 bis 23 % Feuchtegehalt, schneiden. Bei dieser sehr vorteilhaften Schneidfeuchte, die im Bereich der Verarbeitungsfeuchte liegt, entfällt der bisher erforderlich gewesene Feucht- und Trocknungsschritt. Außerdem wird der Tabak weniger beansprucht, da Auffeucht- und Trocknungsvorgänge entfallen, die den Tabak naturgemäß mechanisch belasten und zu einer unerwünschten Faserverkürzung führen. Wie schon ausgeführt, besteht eine sehr vorteilhafte Weiterbildung der Erfindung darin, daß der Tabak als in Ballen oder Teilen davon gepreßter Tabak dem Tabakschneider zugeführt und ohne weitere Auffeuchtung zu Schnittabak geschnitten wird.
Der in Ballen oder Teilen davon gepreßte Tabak kann allerdings vor dem Schneiden auch auf eine Temperatur von mindestens 30 °C, bevorzugt mindestens 40 °C, z.B. 40 °C bis 50 °C, erwärmt werden, was das Schneidergebnis noch verbessert. Bei sehr niedrigen Feuchtewerten, also bei geringen Versandfeuchtewerten, und Raumtemperatur oder ganz wenig erhöhter Temperatur besteht beim Lösen der Tabakteilchen, z. B. der Tabakblätter, voneinander die Gefahr der Tabakbeschädigung. Unter den vorgeschilderten Bedingungen ist es daher vorteilhaft, den Tabak in gepreßter Form, d. h. als Versandballen oder Stücken davon dem Tabakschneider zuzuführen. Es ist dann für die Qualität des Schnitttabaks wichtig, daß die zugeführten Stücke etwa gleiche Abmessungen haben und den Tabakschneider zumindest annähernd über seine Breite ausfüllen, damit die sogenannten Preßketten, die konisch zu einem Preßkanal divergieren, gut und gleichmäßig ausgefüllt sind. Der zu schneidende Tabak muß also, falls die zugeführten Stücke nicht genau den vorgenannten Bedingungen genügen, vorbereitet werden. Eine Verbesserung in dieser Hinsicht bringt eine weitere Ausgestaltung der Erfindung, bei der der Tabak unmittelbar nach einem Erwärmungsvorgang einem Löseschritt unterzogen wird und der gelöste Tabak unmittelbar nach dem Lösen einem Tabakschneider zugeführt wird, in dem er zu Schnittabak geschnitten wird.
Es hat sich gezeigt, daß ein ausreichendes Lösen des gepreßten Tabaks bei viel geringeren Feuchte- und Temperaturwerten erfolgen kann, als bisher angenommen wurde. Bei einer Versandfeuchte von 11 % kann schon bei einer Erwärmung auf 30 °C ausreichend gelöst werden, wobei die Lösequalität mit zunehmender Temperatur besser wird. Unter dem Begriff "Lösen" des Tabaks in dem erwärmten Ballen oder einem Teilstück davon wird nicht verstanden, daß alle oder die ganz überwiegende Zahl der Blätter von den benachbarten Blättern gelöst werden müssen. Dies kann zwar der Fall sein, doch genügt für die Erfindung, daß die Ballen soweit aufgelöst werden, daß die Einzelblätter und/oder kleinere oder größere Klumpen davon den Preßraum des Tabakschneiders zwischen dessen Kette vor den Schneidmessern ausreichend homogen ausfüllen. Wenn im vorigen ausgeführt wurde, daß ein Lösen des erwärmten Tabaks erfolgen soll, wonach der gelöste Tabak unmittelbar dem Tabakschneider zugeführt wird, so wird darunter verstanden, daß der Temperaturabfall während des Lösens und des Förderns zu dem Tabakschneider nicht so groß werden darf, daß der Tabak zu kalt in den Tabakschneider kommt, weil dann die Tabakblätter in dem Tabakschneider durch die Preßkräfte beschädigt werden können. Der Tabak sollte vor dem Lösen und Schneiden daher so weit aufgewärmt werden, daß er im Tabakschneider eine Mindesttemperatur von 30 °C, möglichst aber von ca. 40 °C und darüber, z.B. zwischen 40 °C und 50 °C, aufweist. In diesem Fall ist er geschmeidig genug, um den Preßkräften standzuhalten.
Das Erwärmen des in Ballen oder Teilen davon gepreßten Tabaks kann vorteilhaft durch Beaufschlagung mit Mikrowellen oder elektrischen Hochfrequenzfeldern erfolgen, wie dies in der US-PS 4 799 501 beschrieben ist. Bei einer derartigen Erwärmung wird der Tabak nicht gleichzeitig gefeuchtet.
Ist es erwünscht, den Tabak beim Erwärmen auch zu feuchten, wodurch er noch geschmeidiger wird und das Lösen bei erheblich niedrigeren Temperaturen möglich ist, so ist dies dadurch möglich, daß in an sich bekannter und z.B. durch die US-PS 3 372 703 beschriebener Weise durch Hohldorne Dampf in das Innere der sich im Vakuum befindlichen Ballen geführt wird. Der nach außen in Richtung des Vakuums strömende Dampf erwärmt und feuchtet dabei die Tabakblätter, so daß die Ballen entweder ohne Lösevorgang direkt im Tabakschneider geschnitten werden können oder die Blätter nach dem Lösen dem Tabakschneider zugeführt werden.
Ein besonders guter Kompromiß zwischen Anlagen- und Energieaufwand und Qualität des Schnittabaks erzielt man dann, wenn der in Ballen oder Teilen davon gepreßte Tabak auf eine Temperatur zwischen 30 °C und 60 °C, vorzugsweise zwischen 40 °C und 50 °C erwärmt wird, und auf eine Feuchte zwischen 13 % und 15 %, vorzugsweise von ca. 14 % gefeuchtet wird. Bei diesen Parametern ist der Energieaufwand zum Erwärmen und evtl. Abtrocknen erheblich geringer als bei einem Auffeuchten auf relative Feuchtwerte von 18 % und darüber bei üblichen Konditionierungsverfahren oder bei einem Erwärmen auf hohe Temperaturen vor dem Schneiden.
Außerdem sind die Anlagen zum Behandeln des Tabaks bei den optimalen Parametern gemäß der Erfindung wenig aufwendig. Schließlich werden unerwünschte geschmackliche Beeinflussungen des Tabaks infolge Erwärmens auf hohe Temperaturen, die zum Abtrocknen auch noch längere Zeit gehalten werden müssen, vermieden und gute Werte der Füllkraft des Tabaks erreicht.
The object on which the invention is based is to cut tobacco without a great deal of energy and equipment, and the process parameters can be selected such that good results are achieved with regard to the filling power of the cut tobacco produced.
According to the invention, this is achieved in that the tobacco is cut in a tobacco cutter at a humidity between 10% and 17% and a minimum temperature of ambient temperature (18 ° C to 25 ° C).
This cutting can be carried out in such a way that the pressed tobacco parts are not detached from one another beforehand, but rather that the tobacco, compressed into bales or pieces of bale, is fed to the tobacco cutter with its shipping moisture and room temperature and is processed by it to cut tobacco. As will be explained below, the tobacco can also be dissolved at a slightly elevated temperature and / or humidity before it is fed to the tobacco cutter. This has advantages in that the operation of the tobacco cutter becomes less problematic.
Good cutting results are obtained if the tobacco is cut in a tobacco cutter at a moisture content between 11% and 16%, preferably between 13% and 16%, for example approx. 14%.
A very advantageous moisture condition of the tobacco when cutting is to give it the moisture that the tobacco should have during further processing in cigarette machines. These are moisture values between 12.5 and 13.5%, which in exceptional cases can be slightly below or exceeded. With such moisture values, the tobacco can be cut very well directly, that is, without the damping previously thought necessary, to values between 18 and 23% moisture content. With this very advantageous cutting moisture, which is in the range of the processing moisture, the previously required dampening and drying step is eliminated. In addition, the tobacco is used less because of dampening and drying processes that mechanically stress the tobacco and lead to an undesirable fiber shortening. As already stated, a very advantageous development of the invention is that the tobacco is fed to the tobacco cutter as tobacco pressed in bales or parts thereof and cut into cut tobacco without further moistening.
The tobacco pressed in bales or parts thereof can, however, also be heated to a temperature of at least 30 ° C., preferably at least 40 ° C., for example 40 ° C. to 50 ° C., before cutting, which further improves the cutting result. At very low moisture values, i.e. at low shipping moisture values, and room temperature or very little elevated temperature, there is a loosening of the tobacco particles, e.g. B. the tobacco leaves, each other the risk of tobacco damage. Under the conditions outlined above, it is therefore advantageous to feed the tobacco to the tobacco cutter in a compressed form, ie as a shipping bale or pieces thereof. It is then important for the quality of the cut tobacco that the pieces fed have approximately the same dimensions and fill the tobacco cutter at least approximately over its width, so that the so-called press chains, which diverge conically into a press channel, are filled well and evenly. The tobacco to be cut must therefore be prepared if the pieces supplied do not exactly meet the aforementioned conditions. An improvement in this respect is brought about by a further embodiment of the invention in which the tobacco is subjected to a dissolving step immediately after a heating process and the dissolved tobacco is fed to a tobacco cutter immediately after being loosened, in which it is cut into cut tobacco.
It has been shown that sufficient release of the pressed tobacco can take place at much lower moisture and temperature values than was previously assumed. With a shipping moisture content of 11%, heating to 30 ° C is sufficient can be solved, the soldering quality gets better with increasing temperature. The term "loosening" of the tobacco in the heated bale or a part thereof does not mean that all or most of the leaves have to be released from the neighboring leaves. Although this may be the case, it is sufficient for the invention that the bales are broken up so far that the single sheets and / or smaller or larger lumps of them fill the baling chamber of the tobacco cutter between its chain in front of the cutting knives sufficiently homogeneously. If it was stated in the above that the heated tobacco should be loosened, after which the loosened tobacco is fed directly to the tobacco cutter, this means that the temperature drop during loosening and conveying to the tobacco cutter must not be so great that the Tobacco comes too cold in the tobacco cutter, because then the tobacco leaves in the tobacco cutter can be damaged by the pressing forces. Before loosening and cutting, the tobacco should therefore be warmed up to such an extent that it has a minimum temperature of 30 ° C in the tobacco cutter, but preferably about 40 ° C and above, for example between 40 ° C and 50 ° C. In this case, it is pliable enough to withstand the pressing forces.
The tobacco pressed in bales or parts thereof can advantageously be heated by exposure to microwaves or high-frequency electrical fields, as described in US Pat. No. 4,799,501. With such heating, the tobacco is not moistened at the same time.
If it is desired to wet the tobacco when it is heated, which makes it even more supple and allows it to be dissolved at considerably lower temperatures, this is possible in a manner known per se and described, for example, by US Pat. No. 3,372,703 through hollow mandrels steam is led into the interior of the bales in a vacuum. The steam flowing outwards in the direction of the vacuum warms and humidifies the tobacco leaves so that the bales can either be cut directly in the tobacco cutter without loosening or the leaves can be fed to the tobacco cutter after loosening.
A particularly good compromise between plant and energy expenditure and the quality of the cut tobacco is achieved if the tobacco pressed in bales or parts thereof is heated to a temperature between 30 ° C and 60 ° C, preferably between 40 ° C and 50 ° C, and is moistened to a moisture between 13% and 15%, preferably of about 14%. With these parameters, the energy required for heating and possibly drying is considerably less than when dampening to a relative humidity of 18% and above with conventional conditioning methods or when heating to high temperatures before cutting.
In addition, the plants for treating the tobacco with the optimal parameters according to the invention are not very expensive. Finally, undesirable taste influences of the tobacco as a result of heating to high temperatures, which must be kept for a longer period of time to dry, are avoided and good values for the filling power of the tobacco are achieved.

Eine Bedämpfung kann durch Aufleiten von Sattdampf oder trockenem Dampf auf den gelösten Tabak erfolgen, beispielsweise während dieser auf einem Schwingförderer gefördert wird. Der Dampf kann dann von unten zugeführt werden. Die Tabaktemperaturan können nach dem Bedämpfen bei ca. 60 °C liegen, sie können aber auch bis ca. 90 °C erhöht werden.Damping can be done by passing saturated steam or dry steam onto the dissolved tobacco, for example while this is being conveyed on a vibratory conveyor. The steam can then be supplied from below. The tobacco temperature can be around 60 ° C after steaming, but they can also be increased to around 90 ° C.

Der warm und trocken den Tabakschneider verlassende Schnittabak (Blattschnitt, Rippenschnitt, Gemisch von Blatt- und Rippen - schnitt) wird, vorzugsweise unmittelbar anschließend, d. h. vor dem Abkühlen, gefeuchtet, was in an sich bekannter Weise in einer Feuchttrommel geschehen kann, wie sie z. B. in der US-PS 4 054 145 oder 3 948 277 beschrieben ist. Gemäß einer besonders vorteilhaften Weiterbildung der Erfindung wird der Schnittabak in einem sogenannten Dämpftunnel gefeuchtet, der einen vibrierenden Förderkanal mit Dampfeinlässen aufweist und z. B. in der US-PS 4 004 594 oder der GB-OS 2 138 666 beschrieben ist. Die Tabakfeuchte kann zwecks Minimierung des Energieaufwandes bis zur Weiterverarbeitungsfeuchte (12 bis 13,5 %) erhöht werden, die der Tabak nach dem Abkühlen auf Raumtemperatur hat und mit der er in Zigarettenmaschinen weiterverarbeitet wird. Er kann aber auch zwecks Erhöhung seiner Füllkraft auf höhere Feuchtegrade (über 20 %) gefeuchtet werden, wonach er auf die Weiterverarbeitungsfeuchte herabgetrocknet wird. Die Befeuchtung findet vorzugsweise unmittelbar nach dem Schneiden statt, so daß der relativ trockene, aber noch warme Schnittabak zur Feuchteinrichtung gelangt, bevor er abgekühlt ist.The warm and dry cut tobacco (leaf cut, rib cut, mixture of leaf and rib cut) leaving the tobacco cutter is, preferably immediately afterwards, d. H. before cooling, moistened, which can be done in a conventional manner in a wet drum, as z. B. is described in U.S. Patent 4,054,145 or 3,948,277. According to a particularly advantageous development of the invention, the cut tobacco is moistened in a so-called steam tunnel, which has a vibrating feed channel with steam inlets and z. B. is described in US-PS 4 004 594 or GB-OS 2 138 666. The tobacco moisture can be increased in order to minimize the energy expenditure until the further processing moisture (12 to 13.5%), which the tobacco has after cooling to room temperature and with which it is processed in cigarette machines. However, it can also be moistened to higher degrees of moisture (over 20%) in order to increase its filling power, after which it is dried down to the processing moisture. The moistening preferably takes place immediately after cutting, so that the relatively dry but still warm cut tobacco reaches the moistening device before it has cooled down.

Nach beendeter Behandlung können die Tabakfasern unterschiedlicher Tabakarten oder -sorten, auch Blattabak und Rippentabak, miteinander gemischt werden, wozu sich eine Anlage entsprechend der US-PS 4 116 203 eignet.After the treatment has been completed, the tobacco fibers of different types or types of tobacco, including leaf tobacco and rib tobacco, can be mixed with one another U.S. Patent 4,116,203 is suitable.

Der mit der Erfindung erzielte Vorteil besteht darin, daß ein Verfahren angegeben wird, wie in Ballen gepreßter Tabak mit minimalem Energie- und Anlageneinsatz zu brauchbarem Schnitttabak verarbeitet werden kann, ohne daß die umfangreichen und energieaufwendigen Löse-, Feucht- und Trocknungsanlagen verwendet werden, die bisher für erforderlich gehalten wurden. Diese Anlagen verändern den Tabak geschmacklich und reduzieren ihn in seiner Größe.
Soll der Tabak in gelöster Form dem Tabakschneider zugeführt werden, was für dessen Betrieb Vorteile bietet, so wird er vorteilhaft geringfügig erwärmt und/oder aufgefeuchtet, wozu sich preiswerte Anlagen eignen. Der Energieaufwand ist ebenfalls dabei gering. Die Konditionierung des Tabaks zum Lösen kann mit geringem Energieaufwand und mit einfachen Anlagen erfolgen, weil sich herausgestellt hat, daß die Tabakblätter nicht vollständig voneinander gelöst werden müssen, sondern es genügt, wenn der Tabak grob gelöst wird, damit der Preßraum des Tabakschneiders zumindest annähernd homogen gefüllt ist.
Im Bedarfsfall kann der Tabak vor dem Schneiden einer Bedämpfungsanlage zugeführt werden, in der seine Temperatur und Feuchte erhöht wird.
The advantage achieved by the invention is that a method is specified how bale-pressed tobacco can be processed into usable cut tobacco with minimal use of energy and equipment, without the extensive and energy-consuming dissolving, dampening and drying equipment being used were previously considered necessary. These systems change the taste of tobacco and reduce its size.
If the tobacco is to be fed to the tobacco cutter in a dissolved form, which offers advantages for its operation, it is advantageously slightly warmed and / or moistened, for which reasonably priced systems are suitable. The energy consumption is also low. The conditioning of the tobacco for loosening can be done with little energy and with simple systems, because it has been found that the tobacco leaves do not have to be completely detached from one another, but it is sufficient if the tobacco is loosely loosened so that the tobacco cutter's pressing space is at least approximately homogeneous is filled.
If necessary, the tobacco can be fed to a steaming system before it is cut, in which its temperature and humidity are increased.

Die Erfindung wird im folgenden anhand von Ausführungsbeispielen näher erläutert.
1. Roh-Burley-Tabak (Tabakblätter) mit einem Feuchtegehalt von 8,5, 11 (Versandfeuchte) und 14 % wurde in gepreßtem Zustand mit einem Tabakschneider der Anmelderin vom Typ KTH geschnitten. Die Temperaturen beim Schneiden betrugen ca. 20 °C, 40 °C und 75 °C. Die Erwärmung auf 40 °C und 75 °C wurde durch Beaufschlagung des Tabaks mit Mikrowellen vorgenommen.
Nach dem Schneiden wurde der Tabak auf eine Feuchte von 15,64 % gefeuchtet und seine Füllkraft in einem üblichen in der tabakverarbeitenden Industrie weitverbreiteten Borgwald-Densimeter in mm Resthöhe ermittelt.
Im folgenden findet sich der Zusammenhang zwischen mm Resthöhe des Borgwald-Densimeters und Schneidfeuchte bzw. Schneidtemperatur des Tabaks: Feuchtegehalt [%] Temperatur [°C] Resthöhe [mm] (Borgwald-Densimeter) 8,5 8,5 40 34,27 8,5 75 38,63 11 20 36,20 11 40 40,44 11 75 39,23 14 20 39,65 14 40 42,75 14 75 39,57
2. Roh-Virginia-Tabak (Tabakblätter) mit einem Feuchtegehalt von 8 %, 11 % (Versandfeuchte) und 13 % wurde ebenfalls in gepreßtem Zustand in einem Tabakschneider der Anmelderin vom Typ KTH geschnitten. Die Temperaturen beim Schneiden betrugen ebenfalls 20 °C, 40 °C und 75 °C. Die Erwärmung auf 40 °C und 75 °C wurde durch Beaufschlagung des Tabaks mit Mikrowellen vorgenommen. Nach dem Schneiden wurde der Tabak auf eine Feuchte von 12,04 % gebracht und seine Füllkraft in mm Resthöhe ermittelt.
Im folgenden findet sich der Zusammenhang zwischen mm Resthöhe des Borgwald-Densimeters und Schneidfeuchte bzw. Schneidtemperatur des Tabaks: Feuchtegehalt [%] Temperatur [°C] Resthöhe [mm] (Borgwald-Densimeter) 8 8 40 36,04 8 75 37,10 11 20 34,26 11 40 38,23 11 75 38,26 13 20 38,05 13 40 39,66 13 75 38,16
3.Gepreßter Roh-Virginia-Tabak (Tabakblätter) mit einem Feuchtegehalt von 8,4 % (Versandfeuchte) wurde von Raumtemperatur dadurch erwärmt und gefeuchtet, daß seinem Inneren, während er sich in einem Vakuum befand, Dampf durch einen Hohldorn zugeleitet wurde. Der Tabak wurde mit einer Kondition von ca. 65 °C und 11,8 % Feuchtegehalt mittels eines Tabakschneiders der Anmelderin vom Typ KTH geschnitten. Nach dem Schneiden wurde der Tabak auf eine Feuchte von 13 % gebracht, die etwa der Verarbeitungsfeuchte entspricht, bei der aus dem Tabak Zigaretten hergestellt werden. Die Resthöhe im Borgwald-Densimeter war bei dieser Feuchte 36,31 mm.
The invention is explained in more detail below on the basis of exemplary embodiments.
1. Raw Burley tobacco (tobacco leaves) with a moisture content of 8.5, 11 (shipping moisture) and 14% was cut in the pressed state with a tobacco cutter from the applicant of the KTH type. The cutting temperatures were approx. 20 ° C, 40 ° C and 75 ° C. The heating to 40 ° C and 75 ° C was carried out by exposing the tobacco to microwaves.
After cutting, the tobacco was moistened to a moisture content of 15.64% and its filling power was determined in a standard Borgwald densimeter in mm, which is widely used in the tobacco processing industry.
The following shows the relationship between the remaining height of the Borgwald densimeter and the cutting moisture or cutting temperature of the tobacco: Moisture content [%] Temperature [° C] Residual height [mm] (Borgwald densimeter) 8.5 8.5 40 34.27 8.5 75 38.63 11 20th 36.20 11 40 40.44 11 75 39.23 14 20th 39.65 14 40 42.75 14 75 39.57
2. Raw Virginia tobacco (tobacco leaves) with a moisture content of 8%, 11% (shipping moisture) and 13% was also cut in the pressed state in a tobacco cutter from the applicant of the KTH type. The temperatures when cutting were also 20 ° C, 40 ° C and 75 ° C. The heating to 40 ° C and 75 ° C was carried out by exposing the tobacco to microwaves. After cutting, the tobacco was brought to a moisture level of 12.04% and its filling power was determined in mm remaining height.
The following shows the relationship between the remaining height of the Borgwald densimeter and the cutting moisture or cutting temperature of the tobacco: Moisture content [%] Temperature [° C] Residual height [mm] (Borgwald densimeter) 8th 8th 40 36.04 8th 75 37.10 11 20th 34.26 11 40 38.23 11 75 38.26 13 20th 38.05 13 40 39.66 13 75 38.16
3. Pressed raw Virginia tobacco (tobacco leaves) with a moisture content of 8.4% (shipping moisture) was warmed and moistened from room temperature by supplying steam to it inside while in a vacuum, through a hollow mandrel. The tobacco was cut with a condition of approx. 65 ° C. and a moisture content of 11.8% by means of a tobacco cutter from the applicant of the type KTH. After cutting, the tobacco was brought to a moisture of 13%, which corresponds approximately to the processing moisture at which cigarettes are made from the tobacco. The residual height in the Borgwald densimeter was 36.31 mm at this humidity.

Ein ähnlicher Härtewert wurde erreicht, nachdem die Blätter nach dem Feuchten und Erwärmen und vor dem Schneiden voneinander gelöst worden waren und in lockerer Formation dem Tabakschneider zugeführt worden waren.
Eine Referenzprobe des gleichen Tabaks, die in der gleichen Weise auf die vorgenannte Kondition von 65 °C und 11,8 % Feuchte gebracht worden war, wurde zunächst einem Löseschritt unterzogen, bei dem also die Tabakblätter voneinander getrennt wurden. Nach dem Lösen wurde der Tabak in konventioneller Weise, nämlich mittels eines sogenannten Dämpftunnels (US-PS 4 004 594) auf 21 % Feuchtegehalt hochgefeuchtet und bei Raumtemperatur zu Tabakfasern geschnitten. Diese Fasern wurden in einem HT-Vibrationstunnel der Anmelderin (GB-OS 2 138 666) auf eine Temperatur von ca. 90 °C erwärmt und dabei noch geringfügig weitergefeuchtet und in einem handelsüblichen Gleichstromtrockner auf den Weiterverarbeitungs-Feuchtegehalt von 13 % heruntergetrocknet. Die Resthöhe im Borgwald-Densimeter betrug 34,97 mm.
Es muß betont werden, daß der Verarbeitungsprozeß der Referenzprobe, den die Anmelderin bisher als bestgeeigneten vertrieben hat, gegenüber dem vorbeschriebenen Verfahren gemäß der Erfindung drei zusätzliche Anlagenteile erfordert, nämlich eine Vorrichtung zum Hochfeuchten von 11,8 % auf ca. 21 %, einen HT-Tunnel zum Erwärmen und gleichzeitigen Expandieren des Tabaks sowie eine Gleichstromtrocknungstrommel zum Abtrocknen auf Verarbeitungsfeuchte von 13 %. Diese zusätzlichen Anlagenteile sind aufwendig und erfordern beträchtlichen Energieeinsatz. Außerdem wird der Tabak durch die Förder- und Behandlungsvorgänge mechanisch beansprucht.
A similar hardness value was achieved after the leaves were separated from each other after dampening and heating and before cutting and were fed to the tobacco cutter in a loose formation.
A reference sample of the same tobacco, which had been brought to the aforementioned condition of 65 ° C. and 11.8% moisture in the same way, was first subjected to a dissolving step in which the tobacco leaves were separated from one another. After dissolving, the tobacco was moistened in a conventional manner, namely by means of a so-called steam tunnel (US Pat. No. 4,004,594) to a moisture content of 21% and cut into tobacco fibers at room temperature. These fibers were heated in a HT vibration tunnel by the applicant (GB-OS 2 138 666) to a temperature of approx. 90 ° C and were slightly further moistened and dried down to a further processing moisture content of 13% in a commercially available direct current dryer. The remaining height in the Borgwald densimeter was 34.97 mm.
It has to be emphasized that the processing of the reference sample, which the applicant has hitherto sold as the most suitable, requires three additional system parts compared to the previously described method according to the invention, namely a device for high humidification from 11.8% to approx. 21%, an HT -Tunnel for heating and expanding the tobacco at the same time as well as a DC drying drum for drying to processing moisture of 13%. These additional parts of the system are complex and require considerable energy input. In addition, the tobacco is mechanically stressed by the extraction and treatment processes.

Claims (16)

  1. Method of producing cut tobacco from tobacco, in particular from tobacco leaves, which is supplied pressed in bales or parts thereof, characterized in that the tobacco is cut at a moisture level of between 10% and 17% and a minimum temperature of ambient temperature (18°C to 25°C) in a tobacco cutter.
  2. Method according to Claim 1, characterized in that the tobacco, which has a moisture level of between 11% and 16%, is cut into cut tobacco in a tobacco cutter.
  3. Method according to Claim 2, characterized in that the tobacco is supplied to the tobacco cutter as tobacco pressed in bales or parts thereof and is cut into cut tobacco without moistening.
  4. Method according to one or more of the preceding claims, characterized in that the tobacco pressed in bales or parts thereof is heated to a temperature of at least 30°C before cutting.
  5. Method according to Claim 4, characterized in that the tobacco is subjected to a loosening step directly after heating, and in that the loosened tobacco is supplied directly to the tobacco cutter, in which it is cut into cut tobacco.
  6. Method according to one or more of the preceding claims, characterized in that the tobacco is heated to a temperature of 40°C or above before cutting.
  7. Method according to one or more of Claims 4 to 6, characterized in that the tobacco pressed in bales or parts thereof is heated by the action of microwaves or electrical high-frequency fields thereon.
  8. Method according to one or more of Claims 4 to 6, characterized in that the tobacco is additionally moistened during heating.
  9. Method according to Claim 8, characterized in that the tobacco pressed in bales or parts thereof is heated and moistened in that steam is preferably passed through a hollow mandrel into the interior of the bales which are in a vacuum.
  10. Method according to one or more of the preceding claims, characterized in that the tobacco pressed in bales or parts thereof is heated to a temperature between 30°C and 60°C, preferably between 40°C and 50°C, e.g. to approximately 40°C, and is brought to a moisture level of between 13% and 16%, preferably 14%.
  11. Method according to one or more of Claims 5 to 10, characterized in that the tobacco is steamed after loosening for the purpose of increasing its temperature and relative moisture level and is then supplied to the tobacco cutter.
  12. Method according to one or more of the preceding claims, characterized in that the cut tobacco leaving the tobacco cutter is preferably moistened directly afterwards.
  13. Method according to Claim 12, characterized in that the cut tobacco is moistened to processing moisture level.
  14. Method according to Claim 12, characterized in that the cut tobacco is moistened substantially beyond the processing moisture level and is then dried to processing moisture level again.
  15. Method according to one or more of Claims 12 to 14, characterized in that for moistening the cut tobacco is acted upon by steam while it runs through a vibrating channel.
  16. Method according to one or more of Claims 12 to 14, characterized in that the cut tobacco is moistened in a moisture drum.
EP90104900A 1989-03-18 1990-03-15 Method for making tobacco shreds Expired - Lifetime EP0388793B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT90104900T ATE99503T1 (en) 1989-03-18 1990-03-15 PROCESS FOR MAKING CUT TOBACCO.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3908937 1989-03-18
DE3908937A DE3908937A1 (en) 1989-03-18 1989-03-18 METHOD FOR PRODUCING CUT TOBACCO

Publications (2)

Publication Number Publication Date
EP0388793A1 EP0388793A1 (en) 1990-09-26
EP0388793B1 true EP0388793B1 (en) 1994-01-05

Family

ID=6376662

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90104900A Expired - Lifetime EP0388793B1 (en) 1989-03-18 1990-03-15 Method for making tobacco shreds

Country Status (6)

Country Link
US (1) US5143095A (en)
EP (1) EP0388793B1 (en)
JP (1) JPH02273167A (en)
AT (1) ATE99503T1 (en)
DE (2) DE3908937A1 (en)
ES (1) ES2048349T3 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103704865A (en) * 2013-12-30 2014-04-09 红塔烟草(集团)有限责任公司 Technology for cigarette production

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5148820A (en) * 1989-09-18 1992-09-22 British-American Tobacco Company Limited Processing of tobacco leaves
US5720735A (en) * 1997-02-12 1998-02-24 Dorros; Gerald Bifurcated endovascular catheter
DE19756217A1 (en) * 1997-12-17 1999-07-01 Bat Cigarettenfab Gmbh Process for the treatment of fine tobacco
US6595216B1 (en) * 2001-03-20 2003-07-22 Brown & Williamson Tobacco Corporation Method of cutting sheets of reconstituted tobacco
CA2488334C (en) 2002-06-13 2010-12-07 Johns Hopkins University 24-sulfoximine vitamin d3 compounds
PL368498A1 (en) * 2004-06-14 2005-12-27 International Tobacco Machinery Poland Ltd. Method and appliance for processing plant material, particularly tobacco
DE102004043833B4 (en) * 2004-09-08 2006-10-05 Hauni Primary Gmbh Plant of the tobacco processing industry
DE102004045040A1 (en) * 2004-09-15 2006-03-30 Hauni Primary Gmbh Preparation and provision of tobacco
DE102006038622B4 (en) * 2006-08-17 2008-08-28 Hauni Maschinenbau Ag Processing of tobacco products consisting of tobacco products
CN101694435B (en) * 2009-06-23 2011-02-16 中国烟草总公司郑州烟草研究院 Method and device for measuring crushing degree of tobacco shreds
DE102010028501B4 (en) 2010-05-03 2014-02-13 Hauni Maschinenbau Ag Device for conditioning tobacco
PL2608685T3 (en) 2010-08-24 2014-11-28 Hauni Maschinenbau Gmbh Device for the treatment of tobacco
CN102048234A (en) * 2010-12-02 2011-05-11 云南省烟草农业科学研究院 Tobacco leaf weighing and curing method
CN104041932B (en) * 2013-03-11 2015-12-02 贵州中烟工业有限责任公司 The treating apparatus of tobacco leaf and processing method
DE102017120169A1 (en) 2017-09-01 2019-03-07 Hauni Maschinenbau Gmbh Drum of the tobacco processing industry for treating tobacco
CN116326801A (en) * 2023-03-17 2023-06-27 湖北中烟工业有限责任公司 Shredded tobacco, its preparation method and cigarette

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE835127C (en) * 1950-01-21 1952-03-27 Wilhelm Quester Maschinenfabri Process for keeping tobacco products warm for further processing
GB1089361A (en) * 1964-01-22 1967-11-01 Desmond Walter Molins Improvements relating to tobacco processing
US3372703A (en) * 1966-06-13 1968-03-12 American Mach & Foundry Tobacco moistener
DE2135637C3 (en) * 1971-07-16 1980-05-29 Hauni-Werke Koerber & Co Kg, 2050 Hamburg Method and device for adding an admixture to tobacco
DE2240682C2 (en) * 1972-08-18 1983-09-01 Hauni-Werke Körber & Co KG, 2050 Hamburg Method and device for moistening tobacco
DE2402538C2 (en) * 1974-01-19 1985-05-09 Hauni-Werke Körber & Co KG, 2050 Hamburg Method and device for conditioning tobacco
DE2540411C2 (en) * 1975-09-11 1986-02-20 Hauni-Werke Körber & Co KG, 2050 Hamburg Method and apparatus for producing a tobacco mixture
US4582070A (en) * 1983-04-07 1986-04-15 Brown & Williamson Tobacco Corporation Tobacco treating process
CH662478A5 (en) * 1983-04-23 1987-10-15 Hauni Werke Koerber & Co Kg METHOD AND DEVICE FOR BLOWING TOBACCO.
US4600024A (en) * 1983-06-15 1986-07-15 Hallmark Fabricators Inc Tobacco separation pretreatment system
US4615343A (en) * 1983-09-03 1986-10-07 Hauni-Werke Korber & Co. Kg. Device for compressing tobacco in tobacco comminuting machines
DE3603193A1 (en) * 1986-02-03 1987-08-06 Hauni Werke Koerber & Co Kg METHOD AND SYSTEM FOR PRODUCING CUT TOBACCO FROM RELATIVELY DRY TOBACCO

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103704865A (en) * 2013-12-30 2014-04-09 红塔烟草(集团)有限责任公司 Technology for cigarette production

Also Published As

Publication number Publication date
US5143095A (en) 1992-09-01
EP0388793A1 (en) 1990-09-26
DE3908937A1 (en) 1990-09-20
DE59004071D1 (en) 1994-02-17
JPH02273167A (en) 1990-11-07
ES2048349T3 (en) 1994-03-16
ATE99503T1 (en) 1994-01-15

Similar Documents

Publication Publication Date Title
EP0388793B1 (en) Method for making tobacco shreds
EP0388673B1 (en) Method and apparatus for making tabacco shreds from relatively dry tabacco
DE2714995C3 (en) Production of cellulosic) material with improved digestibility for ruminants
EP1353572B1 (en) Method for the treatment of tobacco
DE69428563T2 (en) Process for the preparation of a cigarette filler mixture
DE3603193A1 (en) METHOD AND SYSTEM FOR PRODUCING CUT TOBACCO FROM RELATIVELY DRY TOBACCO
DE2931313A1 (en) PROCESS FOR REFINING A TOBACCO BY-PRODUCT MATERIAL AND THE PRODUCT OBTAINED THEREFORE
DE2657550C2 (en) Process for the manufacture of a filler for cigarette and pipe tobacco
DE2841874A1 (en) METHOD FOR REDUCING THE MOISTURE CONTENT OF EXPANDED TOBACCO
DE60120665T2 (en) METHOD FOR THE PRODUCTION OF SLICED TOBACCO AND MANUFACTURING SYSTEM THEREFOR
DE3414625C2 (en)
DE2402658A1 (en) METHOD OF EXPANSION OF TOBACCO USING MICROWAVES
DE69402316T2 (en) TREATMENT OF SMOKING MATERIAL
DE3421102A1 (en) METHOD AND DEVICE FOR REORDERING EXPANDED TOBACCO
DE3782384T2 (en) APPLICATION OF A LIQUID FOAM ADDITIVE TO A TOBACCO FILLING.
DE2731932A1 (en) DEVICE AND METHOD FOR EVEN WETTING WHOLE TOBACCO STICKS
DE2731931C2 (en)
CH682039A5 (en)
DE19543262C2 (en) Process and plant for the treatment of tobacco leaves for the production of cut tobacco
EP0845218B1 (en) Method and apparatus for the treatment of tobacco ribs for producing tobacco cut filler
DE1432585A1 (en) Method for treating tobacco in the manufacture of tobacco articles, in particular cigarettes
DE1532041A1 (en) Process for reconstituting tobacco
DE1297015B (en) Process for the production of shaped tobacco bodies, in particular tobacco foils, from an aqueous tobacco pulp
DE3822785A1 (en) Method and arrangement for preparing green tobacco
DE4143416C2 (en) Process for preparing and preserving feed materials and / or moist crops and device for carrying out this process

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: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IT LI LU NL SE

17P Request for examination filed

Effective date: 19901219

17Q First examination report despatched

Effective date: 19911227

ITF It: translation for a ep patent filed
GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE DK ES FR GB GR IT LI LU NL SE

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

Ref country code: NL

Effective date: 19940105

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 19940105

Ref country code: DK

Effective date: 19940105

Ref country code: BE

Effective date: 19940105

REF Corresponds to:

Ref document number: 99503

Country of ref document: AT

Date of ref document: 19940115

Kind code of ref document: T

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

Effective date: 19940117

REF Corresponds to:

Ref document number: 59004071

Country of ref document: DE

Date of ref document: 19940217

ET Fr: translation filed
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

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

Effective date: 19940331

NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
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
EAL Se: european patent in force in sweden

Ref document number: 90104900.7

REG Reference to a national code

Ref country code: CH

Ref legal event code: PUE

Owner name: HAUNI MASCHINENBAU AKTIENGESELLSCHAFT

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

REG Reference to a national code

Ref country code: ES

Ref legal event code: PC2A

Owner name: HAUNI MASCHINENBAU AG.

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

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

Ref country code: GB

Payment date: 19960219

Year of fee payment: 7

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

Ref country code: FR

Payment date: 19960226

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: 19960304

Year of fee payment: 7

Ref country code: AT

Payment date: 19960304

Year of fee payment: 7

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

Ref country code: ES

Payment date: 19960307

Year of fee payment: 7

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

Ref country code: DE

Payment date: 19960424

Year of fee payment: 7

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

Ref country code: CH

Payment date: 19960521

Year of fee payment: 7

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

Ref country code: GB

Effective date: 19970315

Ref country code: AT

Effective date: 19970315

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

Ref country code: SE

Effective date: 19970316

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

Ref country code: ES

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

Effective date: 19970317

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

Ref country code: LI

Effective date: 19970331

Ref country code: CH

Effective date: 19970331

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

Effective date: 19970315

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

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

Ref country code: FR

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

Effective date: 19971128

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

Ref country code: DE

Effective date: 19971202

EUG Se: european patent has lapsed

Ref document number: 90104900.7

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 19990201

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: 20050315