EP0917828B1 - Procédé et dispositif de régulation de l'humidité de sortie du tabac - Google Patents

Procédé et dispositif de régulation de l'humidité de sortie du tabac Download PDF

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Publication number
EP0917828B1
EP0917828B1 EP98121560A EP98121560A EP0917828B1 EP 0917828 B1 EP0917828 B1 EP 0917828B1 EP 98121560 A EP98121560 A EP 98121560A EP 98121560 A EP98121560 A EP 98121560A EP 0917828 B1 EP0917828 B1 EP 0917828B1
Authority
EP
European Patent Office
Prior art keywords
tobacco
drum
water
throughflow
nozzle
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
EP98121560A
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German (de)
English (en)
Other versions
EP0917828A3 (fr
EP0917828A2 (fr
Inventor
Dietmar Franke
Fritz Schelhorn
Hans-Werner Fuchs
Harald Hofmann
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.)
British American Tobacco Germany GmbH
Original Assignee
British American Tobacco Germany GmbH
BAT Cigarettenfabriken GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by British American Tobacco Germany GmbH, BAT Cigarettenfabriken GmbH filed Critical British American Tobacco Germany GmbH
Publication of EP0917828A2 publication Critical patent/EP0917828A2/fr
Publication of EP0917828A3 publication Critical patent/EP0917828A3/fr
Application granted granted Critical
Publication of EP0917828B1 publication Critical patent/EP0917828B1/fr
Anticipated expiration legal-status Critical
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Classifications

    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/04—Humidifying or drying tobacco bunches or cut tobacco
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/06—Loosening tobacco leaves or cut tobacco

Definitions

  • the invention relates to a method and a device for regulating the Initial moisture content of a dissolving / conditioning and optionally a sauce drum processed tobacco.
  • a dissolving / conditioning and optionally the dissolving / conditioning / sauce drum the function, to loosen the raw tobacco delivered in bale form, to sauce and for the others Prepare process steps in tobacco preparation.
  • Special embodiments such drums are for example from WO 90/13231, EP-B-0 424 501 and EP-A-0 471 513.
  • FIG. 5 of EP-A-0 471 513 A typical embodiment is shown in Fig. 5 of EP-A-0 471 513, wherein the water nozzles are in the entry area of the drum and as two-substance nozzles are trained to apply a mixture of water and steam. It will sought that the tobacco, for example, when leaving the drum Output moisture has from about 12% to about 16.5%, the exact value depends on the subsequent process steps of tobacco preparation.
  • the invention is therefore based on the object, a method and a To provide device in which the disadvantages mentioned above do not occur and where in particular the initial moisture content of the tobacco is at an optimal value can be adjusted.
  • the advantages achieved with the invention are based on the use of a two-stage water entry, namely once in the inlet area of the drum and on the other hand in the outlet area.
  • the target value for the water flow rate in the The inlet area of the drum is calculated depending on the target value for the tobacco output moisture, which in turn is dependent on the following Process steps depends, and on the actual values for that of the drum supplied tobacco mass flow, the tobacco inlet moisture and the steam flow rate.
  • a water flow rate is therefore used in the inlet area of the drum, which is tailored to the procedure, but is not yet strictly according to the Target value for the tobacco output moisture is aimed. This is only done by means of a second Water entry in the outlet area of the drum is set exactly, the target value this second water entry from the target and actual value for the tobacco outlet moisture is calculated. Only in the second stage is there in a way Fine-tuning the regulation of the tobacco outlet moisture, so that one with high Accuracy receives a value for the subsequent process steps of Preparation of tobacco is optimal.
  • the water flow rate for the Water supply in the outlet area of the drum by comparison with the actual value adjusted for the amount of water sprayed to the lowest possible Obtain deviations from the target value for the tobacco source moisture.
  • the sauce that may be added to the drum also contains water in extreme cases up to about 90%, according to a preferred embodiment when calculating the water flow rate for the inlet area of the drum the target value for the flow of the sauce fed into the drum is taken into account, in order to avoid excessive deviations or fluctuations here too.
  • the calculation of the water flow rate for the Inlet area of the drum through a formula that defines the main influencing parameters considered, namely the target value for the tobacco source moisture, the Actual value for the tobacco mass flow, the actual value for the input moisture of the tobacco, the actual value for the steam flow and finally possibly the Target value for the sauce flow.
  • the cutting frequency the slicer determined by the belt scale, so that with high uniformity A constant tobacco mass flow is supplied to the drum.
  • a first light barrier that sits at the beginning of the impact belt and at the slicer actuates an empty message.
  • the two nozzles are two-substance nozzles trained who inject a two-component mixture of water and steam. there both the amount of steam supplied and the amount of water supplied recorded and adjusted to the respective target values in order to be too strong here Exclude fluctuations to a large extent.
  • the sauce is also expediently introduced in the discharge area arranged two drum nozzle for a sauce / steam mixture.
  • the drum is equipped with a "pneumatic Blade "that rinses contaminants from the surface of the drum, the too inhomogeneous process conditions and especially too strong Fluctuations in heat transfer can result.
  • FIGS. 1 and 2 generally by reference number 10 indicated plant is used to process the delivered in the form of tobacco bales 12 Raw tobacco for the further process steps in tobacco preparation and has, seen in the conveying direction of the tobacco bales 12, a conveyor belt 14 on which the individual tobacco bales 12, which are released from their packaging, lie in a row.
  • the conveyor belt 14 transports the tobacco bales 12 to one in the tobacco industry referred to as "slicer" cutting device 16, in which the Tobacco bale 12 by a vertically movable cutting knife 18 in individual Portions are divided.
  • the cut front, such as disc or cuboid area 20 of each tobacco bale 12 falls down onto a baffle 22, which brings this tobacco slice 20 to a belt scale 24, which weighs the tobacco slice and the belt speed the tobacco mass flow in kg per Hour determined, so that 20 for each cut tobacco slice current tobacco mass flow value.
  • the tobacco slice 20 arrives at an entry channel 26 for a rotating release conditioning and optionally sauce drum 28, which over a two-fluid nozzle 30, which is located in the entry area of the drum 28, in the illustrated embodiment in the input end wall 32 of the drum 28, Water and steam is supplied, the amount of water sprayed so is set that the tobacco is dissolved and processed for transport.
  • Another two-substance nozzle 34 is located in the discharge hood 36 of the drum 28 and also sprayed a mixture of water and motive steam on the dissolved Tobacco particles that are discharged from the drum 28.
  • the amount of water sprayed on the outlet should have a uniform outlet moisture guarantee the tobacco that is used for further processing.
  • nozzle 38 for the introduction of sauce and steam, which is used in the case that the drum 28 also as a sauce drum should serve.
  • the three nozzles 30, 34 and 38 are steamed from supplied to a common line 40 which is connected to the nozzles.
  • the drum has a recirculating air duct 42, into which steam from the line 40 is sprayed. This will change the temperature of the drum set.
  • a hood heater is installed, which as Steam heat exchanger is designed to condense sauce and water at the To prevent discharge hood 36.
  • a "pneumatic blade” is provided in the upper area of the drum, namely, a pipe 52 provided with outlet nozzles, which is fed with compressed air.
  • the compressed air blown out cyclically from the nozzles approx. Every three minutes releases Contaminants from the inner wall of the drum 28, so that no sauce and Tobacco deposits can occur. Due to the rotation of the drum, the entire cylindrical inner surface of the drum in the region of the discharge end cleaned so that no contamination can occur there.
  • the drum 28 is inclined downwards inclined so that the loosened, conditioned and possibly with sauce Tobacco can fall down on a discharge chute 46 that the tobacco one Conveyor belt 48 and thus the further process steps of tobacco preparation supplies.
  • a first sensor 54 for the actual value of the input moisture which is located above the belt scale 24 and the Moisture of the tobacco slices 20 lying on the belt scale 24 with one of the in the Tobacco industry techniques determined.
  • the belt scale 24 determines the actual value of the tobacco mass flow.
  • the regulation of the tobacco mass flow takes place with the help of the belt scale 24.
  • the belt scale 24 can run faster or slower. So the drum 28 a practically constant tobacco mass flow fed.
  • the actual value determined by the belt weigher 24 and fed to the drum 28 Tobacco mass flow is also used to calculate the water flow rate on the drum entry that is sprayed from the nozzle 30, i.e., this Water flow rate depends on the current tobacco mass flow.
  • Light barrier 50 is provided, which determines whether a tobacco slice 20 on the Band 22 is or not. If the light barrier 50 signals an empty message, see above is the next cut tobacco slice 20 on a slicer 16 Tilting device 53 released. If the second light barrier is empty 51 at the end of the impact belt 22, the speed of the impact belt 22 is increased, to close the gap between tobacco layers 20, thereby creating a Seamless allocation of the belt scale 24 is guaranteed.
  • the cutting frequency of the slicer knife 18 through the belt scale 24 determines, i.e. if the tobacco mass flow falls below the target value, it will Slicer knife 18 moves faster to increase tobacco slices 20 per unit time to produce.
  • a third transducer 58 is connected to a central feed 60 for the steam connected and determines the current actual value for the Steam mass flow.
  • the actual value for the tobacco mass flow, the actual value for the input moisture and the actual value for the steam mass flow is transferred to a computer 62, the one from the instantaneous values of these actual values and two process parameters on the other hand, namely the target value for the sauce flow and the target value for the tobacco outlet moisture, the target value for the water flow rate calculated, which is given to a first controller 64.
  • the first controller 64 receives the output signal of a fourth Transducer 66 connected to a first water feed 68 for the Two-substance nozzle 30 is connected.
  • the controller 64 processes the target and the actual value for the water flow rate in the usual way and produces a Control signal for a water flow valve 70, which is in the water supply line 72 to the two-substance nozzle 30 between the first water feed 68 and the fourth sensor 66 is located.
  • the factor A contained in this formula is in the range of 0.4 to 1 and has the Purpose, the influence of the amount of steam on the amount of water on the process and on to adapt the system 10.
  • the differences in the Condensation of steam on tobacco is taken into account, a characteristic of the following Influencing variables depends on: drum temperature, tobacco temperature, amount of steam and Airflow profile in the drum. Based on empirical data can be considered this parameter the factor A can be set.
  • the value for the factor B is in the range from 0.6 to 0.8 and assumes that the calculated amount of water is about 60 to 80% of the total amount of water in the Process corresponds.
  • the remaining amount of water i.e. 20% to 40% of the total amount of water, serves as a work area for regulating the initial moisture at the tobacco discharge, which takes place via the two-substance nozzle 34 in the discharge area.
  • the sauce flow rate should still be considered as the sauce also contains water.
  • the water content of commercially available sauces is in the range from 50% to almost 100% and is taken into account by the factor C, whose Numerical value is between 0.5 and almost 1.
  • the actual value of the initial moisture content of the tobacco is included on the conveyor belt 48 a fifth transducer 74 determined, the output signal to one second controller 76 is given, which also the target value for the Tobacco outlet moisture receives, as can be seen from Figure 3.
  • the second controller 76 processes the two signals in the usual manner in accordance with one of the known control mechanisms and generates a target value for the water flow in the discharge area, which is passed to a third controller 78, the the actual value of the water supply to the two-substance nozzle 34 from a sixth Sensor 80 receives, which is in the water line 82 between a second water feed 84 for the discharge area and the two-substance nozzle 34 located.
  • the third controller 78 controls a flow control valve 86 that between the second water feed 84 and the transducer 80 is arranged.
  • the actual values for the tobacco mass flow match Steam flow rate and the tobacco inlet moisture set the target value for the water flow rate constantly on, so that taking into account the target value for the Tobacco exit moisture, among others, from the following process steps and depends on the type of tobacco used, and possibly on the target value the optimum water flow rate for the sauce flow can be calculated can, from which in turn in the first controller 64 an optimal target value for the Amount of water is regulated, which at the inlet of the drum 28 by means of Two-substance nozzle 30 is sprayed onto the tobacco in the drum 28. Doing so automatically takes into account the mass of steam supplied to the system.
  • the amount of water for the two-substance nozzle 34 is controlled by a cascade control 76 78 determines, the tobacco outlet moisture via the guide controller 76 is settled.
  • the sauce flow rate is separated by a control circuit, not shown regulated.
  • control circuit in the recirculation air duct injected amount of steam adjusted to the temperature of the drum 28 on a to keep the specified target value.

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  • Manufacture Of Tobacco Products (AREA)
  • Manufacturing Of Cigar And Cigarette Tobacco (AREA)

Claims (12)

  1. Procédé de régulation de l'humidité de sortie du tabac traité par un tambour (28) d'ouverture/conditionnement et éventuellement de sauçage, présentant les caractéristiques suivantes :
    dans la zone d'entrée du tambour (28) on pulvérise, à travers une première buse (30), un débit d'eau qui est régulé en fonction de la valeur de consigne de l'humidité de sortie du tabac et des valeurs réelles du débit massique du tabac, le débit de vapeur et l'humidité d'entrée du tabac ; et
    dans la zone de sortie du tambour (28), on pulvérise, à travers une deuxième buse (34), un débit d'eau dont la valeur de consigne est calculée en fonction de la valeur de consigne et de la valeur réelle de l'humidité de sortie du tabac.
  2. Procédé selon la revendication 1, caractérisé en ce que le débit d'eau pour la deuxième buse (34) est régulé par comparaison avec la valeur réelle de la quantité d'eau pulvérisée, et/ou en ce que le débit d'eau pour la deuxième buse (34) est régulé par comparaison entre l'humidité de sortie de consigne et l'humidité de sortie réelle du tabac.
  3. Procédé selon l'une des revendications 1 ou 2, caractérisé en ce que le calcul du débit d'eau pour la première buse (30) s'effectue en tenant compte de la valeur de consigne du débit de la sauce envoyée au tambour (28), et en ce qu'en particulier le débit d'eau dans la zone d'entrée du tambour (28) est calculé au moyen de la formule suivante : QW = (M2- M1 100% - M2 QT - QD · A - QS · C) · B
    Qw =
    débit d'eau
    M2 =
    humidité de sortie de consigne
    M1 =
    humidité d'entrée réelle
    QT =
    flux massique de tabac
    QD =
    quantité de vapeur réelle
    QS =
    quantité de sauce
    le facteur A se situant entre 0,4 et 1
    le facteur B se situant entre 0,6 et 0,8 et
    le facteur C entre 0,5 et 1,0.
  4. Procédé selon l'une des revendications précédentes, caractérisé en ce que le flux massique de tabac envoyé au tambour (28) est régulé au moyen d'une bascule courroie (24) qui est placée entre le tambour (28) et un slicer (16) monté en amont du tambour (28) pour la réalisation de portions de tabac (20) en forme de tranches, et en ce que la fréquence de coupe du slicer (16) est déterminée par la bascule courroie (24), une barrière photoélectrique (50) prévue entre le slicer (16) et la bascule courroie (24) actionnant le slicer (16).
  5. Procédé selon l'une des revendications précédentes, caractérisé en ce qu'on pulvérise au moyen de la première buse (30) et/ou au moyen de la deuxième buse (34), un mélange à deux substances d'eau et de vapeur, tandis que la sauce est pulvérisée au moyen d'une buse (38) disposée dans la zone de sortie du tambour (28) et qui est conformée en buse pour deux substances, pour un mélange sauce/vapeur.
  6. Procédé selon l'une des revendications 1 à 5, caractérisé en ce que la température du tambour (28) est régulée par injection de vapeur dans un canal de circulation d'air du tambour (28), et/ou en ce que le capot de sortie (36) du tambour (28) est chauffé par un échangeur de chaleur à vapeur, tandis que la porte du capot de sortie (36) est chauffée électriquement.
  7. Dispositif pour la régulation de l'humidité de sortie du tabac traité par un tambour (28) d'ouverture/conditionnement et éventuellement de sauçage, présentant les caractéristiques suivantes :
    un calculateur (62) pour calculer une valeur de consigne du débit d'eau pulvérisé à travers une première buse (30) dans la zone d'entrée du tambour (28), à partir des valeurs réelles du flux massique de tabac, du débit de vapeur et de l'humidité d'entrée du tabac ; et à partir de la valeur de consigne de l'humidité de sortie du tabac ; et
    un régulateur (78) pour la quantité d'eau pulvérisée à travers une deuxième buse (34) dans la zone de sortie du tambour (28) en fonction de la valeur de consigne et de la valeur réelle de l'humidité de sortie du tabac.
  8. Dispositif selon la revendication 7, caractérisé en ce qu'un régulateur (76) est monté en circuit avec le régulateur (78) comme régulateur de conduite.
  9. Dispositif selon l'une des revendications 7 ou 8, caractérisé en ce qu'en amont du tambour (28) est montée une bascule courroie (24) pour amener un flux massique constant de tabac au tambour (28), en ce que la bascule courroie (24) est placée entre le tambour (28) et un slicer (16) pour réaliser des portions de tabac (20) en forme de tranches, une première barrière photoélectrique (50), disposée derrière le slicer (16), actionnant le slicer (16).
  10. Dispositif selon la revendication 9, caractérisé par une deuxième barrière photoélectrique (51), disposée derrière le slicer (16), pour l'occupation sans vides de la bascule courroie (24).
  11. Dispositif selon l'une des revendications 7 à 10, caractérisé par un autre régulateur (64) destiné à déterminer le débit d'eau envoyé à la première buse (30), à partir de la valeur de consigne calculée et de la valeur réelle du débit d'eau, et/ou par un autre régulateur (76) destiné à calculer une valeur de consigne du débit d'eau envoyé à la deuxième buse (34) à partir de la valeur de consigne et de la valeur réelle de l'humidité de sortie du tabac.
  12. Dispositif selon l'une des revendications 7 à 11, caractérisé par une lame pneumatique (52) prévue dans le tambour (28).
EP98121560A 1997-11-20 1998-11-18 Procédé et dispositif de régulation de l'humidité de sortie du tabac Expired - Lifetime EP0917828B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19751525A DE19751525C2 (de) 1997-11-20 1997-11-20 Verfahren und Vorrichtung zur Regelung der Ausgangsfeuchte von Tabak
DE19751525 1997-11-20

Publications (3)

Publication Number Publication Date
EP0917828A2 EP0917828A2 (fr) 1999-05-26
EP0917828A3 EP0917828A3 (fr) 2000-01-12
EP0917828B1 true EP0917828B1 (fr) 2002-06-19

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EP98121560A Expired - Lifetime EP0917828B1 (fr) 1997-11-20 1998-11-18 Procédé et dispositif de régulation de l'humidité de sortie du tabac

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US (2) US6155269A (fr)
EP (1) EP0917828B1 (fr)
DE (1) DE19751525C2 (fr)

Families Citing this family (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE60120665T2 (de) * 2000-02-16 2007-05-31 Japan Tobacco Inc. Verfahren zur herstellung von geschnittenem tabak und herstellungssystem dafür
ITTV20010086A1 (it) * 2001-07-02 2003-01-02 Garbuio Spa Macchina per il trattamento del tabacco
CN1305418C (zh) * 2002-03-14 2007-03-21 日本烟草产业株式会社 原料的湿度调节方法和湿度调节机
WO2005063060A1 (fr) 2003-12-22 2005-07-14 U.S. Smokeless Tobacco Company Procede de traitement pour compositions de tabac ou de tabac a priser
PL376849A1 (pl) * 2005-08-31 2007-03-05 International Tobacco Machinery Poland Spółka Z Ograniczoną Odpowiedzialnością Sposób i urządzenie do obróbki termicznej materiałów sypkich, zwłaszcza pochodzenia roślinnego
PL2537072T3 (pl) 2010-02-17 2014-05-30 Hauni Maschinenbau Gmbh Urządzenie do wstępnej obróbki tytoniu w przemyśle tytoniowym i sposób eksploatacji urządzenia
EP2417860A1 (fr) * 2010-08-11 2012-02-15 Köhl Maschinenbau AG Dispositif et procédé de séparation de parties de balles d'un produit comprimé
EP2608685B1 (fr) * 2010-08-24 2014-06-04 Hauni Maschinenbau AG Dispositif pour le traitement du tabac
WO2012130823A1 (fr) 2011-03-30 2012-10-04 Basf Se Concentrés en suspension
WO2012146598A1 (fr) 2011-04-28 2012-11-01 Basf Se Procédé de préparation de 4-amino-2,4-dihydro-[1,2,4]triazole-3-thiones 2-substituées
WO2012146535A1 (fr) 2011-04-28 2012-11-01 Basf Se Procédé pour la préparation de 2,4-dihydro-[1,2,4]triazole-3-thiones 2-substituées
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CN103099301B (zh) * 2011-11-14 2015-02-04 中烟机械技术中心有限责任公司 烟块松散分区回潮系统及工艺
CN102551188B (zh) * 2011-12-31 2014-04-02 贵州烟叶复烤有限责任公司 烟叶梗头打叶处理工艺
CN103202526B (zh) * 2012-01-11 2015-03-11 湖北中烟工业有限责任公司 用于大惯性系统烟片回潮机的加水离散调节方法
DE102012207531A1 (de) * 2012-05-07 2013-11-07 Hauni Maschinenbau Ag Verfahren und Vorrichtung zum Lösen, Konditionieren und Soßieren von Tabak
CN102813276A (zh) * 2012-09-12 2012-12-12 云南烟草科学研究院 一种白肋烟及香料烟润叶加料装置
BR102012026524A2 (pt) * 2012-10-16 2014-09-30 Souza Cruz Sa Equipamento para tratamento de tabaco ou de outro material a granel sensível a danos mecânicos
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CN114376254B (zh) * 2020-10-19 2023-05-12 湖南中烟工业有限责任公司 烟草回潮筒内空气含水率测量装置、方法及回潮筒
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CN114532564A (zh) * 2022-03-24 2022-05-27 河南中烟工业有限责任公司 基于主成分分析策略的松散回潮出口烟丝含水率控制方法
CN114831330B (zh) * 2022-05-23 2023-07-25 红云红河烟草(集团)有限责任公司 一种制丝车间松散回潮工序智能加水模型的建立方法
CN115005477A (zh) * 2022-05-24 2022-09-06 山东中烟工业有限责任公司 一种烟用超级回潮机出口水分控制装置和工作方法

Family Cites Families (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1063941A (en) * 1963-11-18 1967-04-05 Korber Kurt Method of and apparatus for drying tobacco or similar foliate material
DE1813620C3 (de) * 1968-12-10 1974-08-08 Fa. Wilh. Quester, 5000 Koeln Vorrichtung zum Konditionieren von Tabak mittels einer umlaufenden Trommel
DE1932906C3 (de) * 1969-06-28 1979-02-08 Hauni-Werke Koerber & Co Kg, 2050 Hamburg Anordnung zum Vereinigen von im schwankenden Mengenstrom gefördertem Tabak mit Zusätzen
DE2019369C3 (de) * 1970-04-22 1980-08-28 Hauni-Werke Koerber & Co Kg, 2050 Hamburg Verfahren zum Trocknen von Tabak und Trocknungsförderer
DE2135637C3 (de) * 1971-07-16 1980-05-29 Hauni-Werke Koerber & Co Kg, 2050 Hamburg Verfahren und Vorrichtung zum Zusetzen einer Beimischung zu Tabak
US3785765A (en) * 1972-02-17 1974-01-15 Imasco Ltd Rotary tobacco dryer
US3787985A (en) * 1972-08-14 1974-01-29 Industrial Nucleonics Corp Dryer control system and method
DE2240682C2 (de) * 1972-08-18 1983-09-01 Hauni-Werke Körber & Co KG, 2050 Hamburg Verfahren und Vorrichtung zum Feuchten von Tabak
US4045657A (en) * 1973-06-07 1977-08-30 Svenska Tobaks Aktiebolaget Method of facilitating exact evaluation or control of the processing of a product mass, and apparatus for carrying said method into effect
US3905123A (en) * 1973-10-15 1975-09-16 Industrial Nucleonics Corp Method and apparatus for controlling a tobacco dryer
DE2747232B2 (de) * 1977-10-21 1980-05-08 Fa. Wilh. Quester, 5000 Koeln Regelungsverfahren zur kontinuierlichen Behandlung von Schüttgütern zur Veränderung ihrer physikalischen Eigenschaften
DE3001734A1 (de) * 1980-01-18 1981-07-23 Hauni-Werke Körber & Co KG, 2050 Hamburg Trommel zum behandeln von tabak
DE3223223A1 (de) * 1981-07-07 1983-01-27 Hauni-Werke Körber & Co KG, 2050 Hamburg Steueranordnung fuer trommeltrockner
US4513759A (en) * 1981-07-07 1985-04-30 Hauni-Werke Korber & Co. Kg Apparatus for expelling moisture from tobacco or the like
EP0095866A1 (fr) * 1982-06-02 1983-12-07 Amf Incorporated Dispositif d'alimentation et de coupe du tabac
JPS6024171A (ja) * 1983-07-21 1985-02-06 日本たばこ産業株式会社 たばこの調湿機における水分および温度の制御装置
JPS6054028B2 (ja) * 1983-12-23 1985-11-28 日本たばこ産業株式会社 たばこ用乾燥調和装置
US4730627A (en) * 1986-11-28 1988-03-15 R. J. Reynolds Tobacco Company Method and apparatus for treating particulate material
GB8910279D0 (en) * 1989-05-04 1989-06-21 Gbe International Plc Improvements in or relating to apparatus for treating tobacco
JP3019219B2 (ja) * 1989-08-07 2000-03-13 株式会社木原製作所 葉たばこ乾燥機における湿度制御装置
GB8924885D0 (en) * 1989-11-03 1989-12-20 Gbe International Plc Improvements in or relating to rotary treatment cylinders
US5103842A (en) * 1990-08-14 1992-04-14 Philip Morris Incorporated Conditioning cylinder with flights, backmixing baffles, conditioning nozzles and air recirculation
NZ270418A (en) 1994-02-07 1997-09-22 Eisai Co Ltd Polycyclic triazole & imidazole derivatives, antifungal compositions
GB9602080D0 (en) 1996-02-02 1996-04-03 Pfizer Ltd Pharmaceutical compounds
EP0829478A3 (fr) 1996-09-09 1998-03-25 F. Hoffmann-La Roche Ag Dérivés de N-benzylimidazolium et N-benzyltriazolium, leur préparation et leur utilisation comme agents anti-fongiques et anti-mycotiques
KR20010005792A (ko) 1997-03-31 2001-01-15 다케다 야쿠힌 고교 가부시키가이샤 아졸 화합물, 이의 제조 방법 및 용도
WO1999033846A2 (fr) 1997-12-31 1999-07-08 The University Of Kansas Remedes contenant des precurseurs hydrosolubles d'amines secondaires et tertiaires, et leurs procedes d'obtention

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EP0917828A3 (fr) 2000-01-12
US20010000095A1 (en) 2001-04-05
US6155269A (en) 2000-12-05
US6502581B2 (en) 2003-01-07
EP0917828A2 (fr) 1999-05-26
DE19751525C2 (de) 2003-02-13
DE19751525A1 (de) 1999-06-02

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