EP1255457B1 - Method for improving the filling ability of tobacco - Google Patents
Method for improving the filling ability of tobacco Download PDFInfo
- Publication number
- EP1255457B1 EP1255457B1 EP01907496A EP01907496A EP1255457B1 EP 1255457 B1 EP1255457 B1 EP 1255457B1 EP 01907496 A EP01907496 A EP 01907496A EP 01907496 A EP01907496 A EP 01907496A EP 1255457 B1 EP1255457 B1 EP 1255457B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- tobacco
- compression
- weight
- carried out
- improving
- 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
Links
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
- A24B3/18—Other treatment of leaves, e.g. puffing, crimpling, cleaning
-
- 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
- A24B3/18—Other treatment of leaves, e.g. puffing, crimpling, cleaning
- A24B3/182—Puffing
Definitions
- the invention relates to a method for improving the Fillability of tobacco, such as cut tobacco leaves or ribs or tobacco additives, by treating the up to about 15% by weight of starting moisture Tobacco material with one of nitrogen and / or argon existing treatment gas at pressures from 50 to 1,000 bar followed by continuous or step-like compression from a continuous or step-like Decompression, the compression and Decompression steps in either an autoclave or with cascade-like switching in several autoclaves take place, and subsequent thermal aftertreatment of the discharged tobacco material.
- Such processes also known as INCOM inflation processes are known, have compared to the pressure treatment of Tobacco with carbon dioxide, ammonia or volatile organic gases proved to be advantageous.
- DE 31 19 330 A1 describes such an expansion process with Autoclaves prevailing working temperatures from 0 to 50 ° C, one to increase the filling capacity or Bloating degree the use of a tobacco material with a Moisture of up to 15% by weight and an aftertreatment with Provided water vapor. It was based on the fact that a lower tobacco moisture content of 10 to 15% by weight a desired stronger cooling of the discharge Leads tobacco material while relaxing.
- DE 34 14 625 C2 also discloses a cascade process, after which by various measures such as cooling the Treatment gas before loading the reactor, Cooling the autoclave or using a supercooled and liquefied treatment gas a low Working temperature in the impregnation of the tobacco causes shall be.
- the tobacco moisture can be arbitrary and for example in a range from 10 to 30% by weight lie, however it is explicitly demanded that the Autoclave temperature or its cooling water temperature is not May exceed 50 ° C.
- the invention is based, so far the task INCOM process to improve and with equally good or better values in terms of filling capacity or bloating effect those previously considered necessary and uneconomical cooling measures during compression avoid.
- the high pressure treatment was carried out in a laboratory autoclave a used content of 2 l performed.
- a Jacket for the circulation of liquid media was used for Setting the desired working temperatures.
- the Pressure build-up took place from below, the pressure decrease upwards.
- a compressor was used for adjustment the final pressure.
- a thermocouple measured the tobacco temperature in the upper segment of the tobacco fill.
- the laboratory device for thermal aftertreatment existed from a permeable conveyor belt Wire mesh, baffles to form the tobacco fleece in the desired width, a steam nozzle with slot-like Outlet opening and one arranged under the belt Dampfabsaugvorraum.
- the aftertreatment was carried out with Saturated steam.
- the tobacco samples were spread in flat plastic dishes and conditioned in a standard atmosphere at 21 ° C and 62% relative humidity.
- the filling capacities were determined using a Borgwaldt densimeter, and the specific volume in ml / g was converted to a nominal moisture of 12% by weight and a nominal temperature of 22 ° C.
- the experiments were carried out with tobacco moisture levels of 8, 12 and 14 and carried out as a comparison 18 wt .-%.
- the Working temperatures were set to 40 by thermostatting 60 and 80 ° C set.
- the final pressure was 700 bar, the Pressure reduction was carried out in a time interval of approximately 0.5 min carried out. All attempts were based on one uniform mixture of Virginia tobacco and the described aftertreatment method with saturated steam.
- T A means the tobacco temperature immediately before removal from the autoclave as the discharge temperature and ⁇ % the relative improvement in filling capacity or the degree of expansion.
Landscapes
- Manufacture Of Tobacco Products (AREA)
Description
Die Erfindung betrifft ein Verfahren zur Verbesserung der Füllfähigkeit von Tabak, wie geschnittenen Tabakblättern oder -rippen bzw. Tabakzusatzstoffen, durch Behandlung des bis etwa 15 Gew.-% Ausgangsfeuchte aufweisenden Tabakmaterials mit einem aus Stickstoff und/oder Argon bestehenden Behandlungsgas bei Drücken von 50 bis 1.000 bar bei kontinuierlicher oder stufenartiger Kompression gefolgt von einer kontinuierlichen oder stufenartigen Dekompression, wobei die Kompressions- und Dekompressionsschritte in entweder einem Autoklaven oder bei kaskadenartiger Schaltung in mehreren Autoklaven erfolgen, und anschließende thermische Nachbehandlung des ausgetragenen Tabakmaterials.The invention relates to a method for improving the Fillability of tobacco, such as cut tobacco leaves or ribs or tobacco additives, by treating the up to about 15% by weight of starting moisture Tobacco material with one of nitrogen and / or argon existing treatment gas at pressures from 50 to 1,000 bar followed by continuous or step-like compression from a continuous or step-like Decompression, the compression and Decompression steps in either an autoclave or with cascade-like switching in several autoclaves take place, and subsequent thermal aftertreatment of the discharged tobacco material.
Derartige Verfahren, die auch als INCOM-Blähverfahren bekannt sind, haben sich gegenüber der Druckbehandlung von Tabak mit Kohlendioxid, Ammoniak oder flüchtigen organischen Gasen als vorteilhaft erwiesen. So beschreibt die DE 31 19 330 Al ein derartiges Blähverfahren mit im Autoklaven vorherrschenden Arbeitstemperaturen von 0 bis 50°C, wobei man zur Erhöhung der Füllfähigkeit oder des Blähgrades den Einsatz eines Tabakmaterials mit einer Feuchte von bis zu 15 Gew.-% und eine Nachbehandlung mit Wasserdampf vorsah. Hierbei wurde darauf abgestellt, daß eine geringere Feuchte des Tabaks von 10 bis 15 Gew.-% zu einer erwünschten stärkeren Abkühlung des auszutragenden Tabakmaterials beim Entspannen führt.Such processes, also known as INCOM inflation processes are known, have compared to the pressure treatment of Tobacco with carbon dioxide, ammonia or volatile organic gases proved to be advantageous. So describes DE 31 19 330 A1 describes such an expansion process with Autoclaves prevailing working temperatures from 0 to 50 ° C, one to increase the filling capacity or Bloating degree the use of a tobacco material with a Moisture of up to 15% by weight and an aftertreatment with Provided water vapor. It was based on the fact that a lower tobacco moisture content of 10 to 15% by weight a desired stronger cooling of the discharge Leads tobacco material while relaxing.
Ferner offenbart die DE 34 14 625 C2 ein Kaskadenverfahren, wonach durch verschiedenartigste Maßnahmen wie Kühlung des Behandlungsgases vor der Beaufschlagung des Reaktors, Kühlung des Autoklaven oder Einsatz eines unterkühlten und verflüssigten Behandlungsgases eine niedrige Arbeitstemperatur bei der Imprägnierung des Tabaks bewirkt werden soll. Zwar kann die Tabakfeuchte beliebig und beispielsweise in einem Bereich von 10 bis 30 Gew.-% liegen, jedoch wird ausdrücklich gefordert, daß die Autoklaventemperatur bzw. dessen Kühlwassertemperatur nicht 50 °C überschreiten darf.DE 34 14 625 C2 also discloses a cascade process, after which by various measures such as cooling the Treatment gas before loading the reactor, Cooling the autoclave or using a supercooled and liquefied treatment gas a low Working temperature in the impregnation of the tobacco causes shall be. The tobacco moisture can be arbitrary and for example in a range from 10 to 30% by weight lie, however it is explicitly demanded that the Autoclave temperature or its cooling water temperature is not May exceed 50 ° C.
Dieses wird auch gemäß DE 39 35 774 C2 in Zusammenhang mit einem kaskadenartigen Blähverfahren bestätigt, bei dem eine Umwälzung des Behandlungsgases über einen Kühler vorgesehen wird, um die erforderlichen tiefen Imprägniertemperaturen von 25 bzw. 45°C einzuhalten.This is also in connection with DE 39 35 774 C2 a cascade-like expansion process, in which a Circulation of the treatment gas is provided via a cooler to the required low impregnation temperatures of 25 or 45 ° C.
Wenngleich mit den oben erwähnten Blähverfahren bereits gute Werte hinsichtlich der Erhöhung der Füllfähigkeit von Tabak bzw. des Blähgrades erzielt werden, sind sie wegen der erforderlichen Kühlung des oder der Autoklaven und wegen der zusätzlichen Kühlung des Behandlungsgases verhältnismäßig aufwendig.Already with the above-mentioned expansion processes good values in terms of increasing the filling capacity of Tobacco or the degree of swelling are achieved, they are because the required cooling of the autoclave (s) and because of the additional cooling of the treatment gas relatively expensive.
Der Erfindung liegt die Aufgabe zugrunde, die bisherigen INCOM-Verfahren zu verbessern und bei gleich guten oder besseren Werten hinsichtlich Füllfähigkeit oder Bläheffekt die bislang für erforderlich gehaltenen und unwirtschaftlichen Kühlmaßnahmen bei der Kompression zu vermeiden.The invention is based, so far the task INCOM process to improve and with equally good or better values in terms of filling capacity or bloating effect those previously considered necessary and uneconomical cooling measures during compression avoid.
Erfindungsgemäß wird daher ein Verfahren der eingangs erwähnten Art gemäß Oberbegriff Patentanspruch vorgeschlagen, das dadurch gekennzeichnet ist, daß die Kompression bei einer Reaktortemperatur von über 55°C durchgeführt wird.According to the invention is therefore a method of the beginning mentioned type according to the preamble claim proposed, which is characterized in that the Compression at a reactor temperature above 55 ° C is carried out.
Überraschenderweise hat sich gezeigt, daß im Fall niedriger Tabakfeuchten im Bereich von bis 15 Gew.-% die bisherige Lehre, die eine tiefe Behandlungstemperatur fordert, nicht zu optimalen Blähergebnissen führt. Vielmehr konnten erst durch Erhöhung der Behandlungstemperatur bei der Kompression erstaunlich gute Werte hinsichtlich des Bläheffektes bzw. der Füllfähigkeit erzielt werden.Surprisingly, it has been shown that in the case lower Tobacco moisture in the range of up to 15 wt .-% the previous one Teaching that requires a low treatment temperature is not leads to optimal blowing results. Rather, only by increasing the treatment temperature at the Compression astonishingly good values in terms of Bloating effect or the filling ability can be achieved.
Dieses führt weiterhin verfahrensmäßig zu dem Vorteil, daß die Kompressionswärme nicht abgeführt werden muß, also keine zusätzliche Kühlung des oder der Autoklaven erforderlich ist.In terms of procedure, this also leads to the advantage that the heat of compression does not have to be dissipated, that is no additional cooling of the autoclave (s) is required.
Im folgenden Beispiel wird das erfindungsgemäße Verfahren im Vergleich zum bisherigen Stand der Technik erläutert. Die Versuchsergebnisse zeigen den für verschiedene Tabakfeuchten unterschiedlichen Einfluß der Arbeitstemperatur auf den Blähgrad. Gemäß der bisherigen Lehre führt im Fall einer Tabakfeuchte von 18 Gew.-% eine Erhöhung der Arbeitstemperatur über 40°C zu einer Verschlechterung des Bläheffekts. Dagegen zeigen sich bei Tabakfeuchten von unter 15 Gew.-% deutliche Verbesserungen, wenn die Hochdruckbehandlung bei Arbeitstemperaturen von 60 und 80 °C durchgeführt wird. Erstaunlicherweise liegen die erzielbaren Blähgrade bei niedriger Tabakfeuchte und höheren Arbeitstemperaturen sogar teilweise über den unter konventionellen Bedingungen erhaltenen Werten. The process according to the invention is shown in the following example compared to the prior art explained. The test results show that for different Tobacco moisture different influence of Working temperature to the degree of swelling. According to the previous one In the case of a tobacco moisture content of 18% by weight, a lesson is taught Increase the working temperature above 40 ° C to one Worsening of the bloating effect. In contrast, show up in Tobacco moisture content of less than 15% by weight, significant improvements, if the high pressure treatment at working temperatures of 60 and 80 ° C is carried out. Amazingly, they are achievable degrees of swelling at low tobacco moisture and higher working temperatures even partially above values obtained under conventional conditions.
Die Hochdruckbehandlung wurde in einem Laborautoklaven mit einem genutzten Inhalt von 2 l durchgeführt. Eine Ummantelung zur Zirkulation flüssiger Medien diente zur Einstellung der gewünschten Arbeitstemperaturen. Der Druckaufbau erfolgte von unten, der Druckabbau nach oben. Mehrere Ventile ermöglichten die beabsichtigten Schaltungsschemata. Ein Kompressor diente zur Einstellung des Enddruckes. Ein Thermoelement maß die Tabaktemperatur im oberen Segment der Tabakschüttung.The high pressure treatment was carried out in a laboratory autoclave a used content of 2 l performed. A Jacket for the circulation of liquid media was used for Setting the desired working temperatures. The Pressure build-up took place from below, the pressure decrease upwards. Several valves enabled the intended Circuit schematics. A compressor was used for adjustment the final pressure. A thermocouple measured the tobacco temperature in the upper segment of the tobacco fill.
Die Laborvorrichtung zur thermischen Nachbehandlung bestand aus einem als Transportband dienenden durchlässigen Drahtgewebe, Leitblechen zur Ausbildung des Tabakvlieses in der gewünschten Breite, einer Dampfdüse mit schlitzartiger Austrittsöffnung und einer unter dem Band angeordneten Dampfabsaugvorrichtung. Die Nachbehandlung erfolgte mit Sattdampf.The laboratory device for thermal aftertreatment existed from a permeable conveyor belt Wire mesh, baffles to form the tobacco fleece in the desired width, a steam nozzle with slot-like Outlet opening and one arranged under the belt Dampfabsaugvorrichtung. The aftertreatment was carried out with Saturated steam.
Die wichtigsten Behandlungsparameter sind der folgenden
Tabelle 1 zu entnehmen.
Die Tabakproben wurden in flachen Plastikschalen
ausgebreitet und im Normklima bei 21°C und 62% relativer
Feuchte konditioniert. Die Füllfähigkeiten wurden mit Hilfe
eines Borgwaldt-Densimeters bestimmt, und das spezifische
Volumen in ml/g auf eine Sollfeuchte von 12 Gew.-% und eine
Solltemperatur von 22°C umgerechnet. Aus den Daten des
unbehandelten Vergleichs bzw. Basis und den expandierten
Mustern errechnet sich die auch als Blähgrad bezeichnete
relative Füllfähigkeitsverbesserung nach der folgenden
Formel, in welcher FB die Füllfähigkeit der Basis und FE
die Füllfähigkeit des expandierten Tabaks bedeuten:
Die Versuche wurden mit Tabakfeuchten von 8, 12 und 14 sowie als Vergleich 18 Gew.-% durchgeführt. Die Arbeitstemperaturen wurden durch Thermostatisierung auf 40, 60 und 80°C eingestellt. Der Enddruck betrug 700 bar, der Druckabbau wurde in einem Zeitintervall von etwa 0,5 min durchgeführt. Alle Versuche basierten auf einer einheitlichen Mischung aus Virginiatabaken und der beschriebenen Nachbehandlungsmethode mit Sattdampf.The experiments were carried out with tobacco moisture levels of 8, 12 and 14 and carried out as a comparison 18 wt .-%. The Working temperatures were set to 40 by thermostatting 60 and 80 ° C set. The final pressure was 700 bar, the Pressure reduction was carried out in a time interval of approximately 0.5 min carried out. All attempts were based on one uniform mixture of Virginia tobacco and the described aftertreatment method with saturated steam.
Die Ergebnisse der Versuche sind in der folgenden
Tabelle 2, die des Vergleichsversuchs in der folgenden
Tabelle 2a dargestellt. In den Tabellen bedeuten TA die
Tabaktemperatur unmittelbar vor der Entnahme aus dem
Autoklaven als Austragstemperatur und Δ % die relative
Füllfähigkeitsverbesserung bzw. den Blähgrad.
8 Gew.-%
12 Gew.-%
14 Gew.-%
8% by weight
12% by weight
14% by weight
Der Vergleich der obigen Tabellen zeigt deutlich den positiven Effekt höherer Arbeitstemperaturen von 60 und 80°C auf die Füllfähigkeitsverbesserung, wenn Tabak mit Feuchten von unter 15 Gew.-% eingesetzt wird.The comparison of the above tables clearly shows that positive effect of higher working temperatures of 60 and 80 ° C on the improvement in filling capacity when using tobacco Moisture of less than 15 wt .-% is used.
Claims (3)
- A method for improving the filling capacity of tobacco, such as cut tobacco leaves or ribs or tobacco additives, by treating the tobacco material that has an initial moisture content of up to roughly 15 % by weight with a treatment gas comprising nitrogen and/or argon at pressures of 50 to 1,000 bar during a continuous or staged compression, followed by a continuous or staged decompression, whereby the compression and decompression steps occur in either an autoclave or, in the case of a cascade-type circuit, in several autoclaves, and subsequent thermal aftertreatment of the discharged tobacco material,
characterised in that the compression is carried out at a working temperature of above 55°C. - A method according to Claim 1,
characterised in that compression is carried out at a working temperature of 60 to 90°C. - A method according to Claim 1,
characterised in that the initial moisture content of of the tobacco material lies in the range from 8 to 14 % by weight.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10006425 | 2000-02-14 | ||
DE10006425A DE10006425C1 (en) | 2000-02-14 | 2000-02-14 | Process for improving the fillability of tobacco |
PCT/EP2001/001229 WO2001058288A1 (en) | 2000-02-14 | 2001-02-05 | Method for improving the filling ability of tobacco |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1255457A1 EP1255457A1 (en) | 2002-11-13 |
EP1255457B1 true EP1255457B1 (en) | 2003-06-25 |
Family
ID=7630805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP01907496A Expired - Lifetime EP1255457B1 (en) | 2000-02-14 | 2001-02-05 | Method for improving the filling ability of tobacco |
Country Status (23)
Country | Link |
---|---|
US (1) | US20030089376A1 (en) |
EP (1) | EP1255457B1 (en) |
JP (1) | JP2003525035A (en) |
KR (1) | KR20020075430A (en) |
CN (1) | CN1404366A (en) |
AR (1) | AR027419A1 (en) |
AT (1) | ATE243438T1 (en) |
AU (1) | AU2001235450A1 (en) |
BG (1) | BG107105A (en) |
BR (1) | BR0108282A (en) |
CA (1) | CA2398951A1 (en) |
CZ (1) | CZ20023079A3 (en) |
DE (2) | DE10006425C1 (en) |
EA (1) | EA004085B1 (en) |
EE (1) | EE200200448A (en) |
ES (1) | ES2202277T3 (en) |
HU (1) | HUP0204461A2 (en) |
IL (1) | IL150790A0 (en) |
NO (1) | NO20023782D0 (en) |
PL (1) | PL193100B1 (en) |
SK (1) | SK13322002A3 (en) |
UA (1) | UA72316C2 (en) |
WO (1) | WO2001058288A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10046124C1 (en) * | 2000-09-15 | 2002-07-04 | Reemtsma H F & Ph | Process for improving the fillability of tobacco |
DE10229451A1 (en) | 2002-07-01 | 2004-01-15 | Reemtsma Cigarettenfabriken Gmbh | Process for improving the fillability of tobacco |
CN104336752A (en) * | 2013-08-06 | 2015-02-11 | 李计红 | Method for improving tobaccos |
CN111728258B (en) * | 2020-07-13 | 2022-05-03 | 广西中烟工业有限责任公司 | Pretreatment process for shredding tobacco flakes |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3119330C2 (en) * | 1981-05-15 | 1983-06-01 | H.F. & Ph.F. Reemtsma Gmbh & Co, 2000 Hamburg | Process for improving the filling capacity of tobacco |
US4531529A (en) * | 1982-10-04 | 1985-07-30 | R. J. Reynolds Tobacco Company | Process for increasing filling capacity of tobacco |
DE3414625A1 (en) * | 1983-04-21 | 1984-10-25 | H.F. & Ph.F. Reemtsma Gmbh & Co, 2000 Hamburg | Process for improving the filling properties of tobacco |
DE3334736A1 (en) * | 1983-09-26 | 1985-04-04 | Kohlensäure-Werke Rud. Buse GmbH & Co, 5462 Bad Hönningen | METHOD FOR PRODUCING LOW NICOTINE TOBACCO BY HIGH PRESSURE EXTRACTION |
US5065774A (en) * | 1989-08-18 | 1991-11-19 | R. J. Reynolds Tobacco Company | Process for expanding tobacco under moderate conditions |
DE3935774C2 (en) * | 1989-10-24 | 1996-06-20 | Peter Dr Theissing | Process to improve the temperature profile during the bloating of tobacco |
US5483977A (en) * | 1993-06-14 | 1996-01-16 | R. J. Reynolds Tobacco Company | Tobacco expansion processes and apparatus |
-
2000
- 2000-02-14 DE DE10006425A patent/DE10006425C1/en not_active Expired - Fee Related
-
2001
- 2001-02-05 JP JP2001557410A patent/JP2003525035A/en not_active Withdrawn
- 2001-02-05 EP EP01907496A patent/EP1255457B1/en not_active Expired - Lifetime
- 2001-02-05 US US10/182,733 patent/US20030089376A1/en not_active Abandoned
- 2001-02-05 CN CN01805011A patent/CN1404366A/en active Pending
- 2001-02-05 EA EA200200856A patent/EA004085B1/en not_active IP Right Cessation
- 2001-02-05 ES ES01907496T patent/ES2202277T3/en not_active Expired - Lifetime
- 2001-02-05 HU HU0204461A patent/HUP0204461A2/en unknown
- 2001-02-05 AU AU2001235450A patent/AU2001235450A1/en not_active Abandoned
- 2001-02-05 EE EEP200200448A patent/EE200200448A/en unknown
- 2001-02-05 SK SK1332-2002A patent/SK13322002A3/en unknown
- 2001-02-05 CZ CZ20023079A patent/CZ20023079A3/en unknown
- 2001-02-05 BR BR0108282-5A patent/BR0108282A/en not_active Application Discontinuation
- 2001-02-05 WO PCT/EP2001/001229 patent/WO2001058288A1/en not_active Application Discontinuation
- 2001-02-05 CA CA002398951A patent/CA2398951A1/en not_active Abandoned
- 2001-02-05 KR KR1020027010639A patent/KR20020075430A/en not_active Application Discontinuation
- 2001-02-05 PL PL357298A patent/PL193100B1/en unknown
- 2001-02-05 IL IL15079001A patent/IL150790A0/en unknown
- 2001-02-05 AT AT01907496T patent/ATE243438T1/en not_active IP Right Cessation
- 2001-02-05 DE DE50100335T patent/DE50100335D1/en not_active Expired - Lifetime
- 2001-02-14 AR ARP010100651A patent/AR027419A1/en unknown
- 2001-05-02 UA UA2002097456A patent/UA72316C2/en unknown
-
2002
- 2002-08-09 NO NO20023782A patent/NO20023782D0/en not_active Application Discontinuation
- 2002-09-13 BG BG107105A patent/BG107105A/en unknown
Also Published As
Publication number | Publication date |
---|---|
CZ20023079A3 (en) | 2003-03-12 |
EA200200856A1 (en) | 2003-06-26 |
EE200200448A (en) | 2003-12-15 |
AR027419A1 (en) | 2003-03-26 |
SK13322002A3 (en) | 2003-02-04 |
DE10006425C1 (en) | 2001-08-16 |
UA72316C2 (en) | 2005-02-15 |
WO2001058288A1 (en) | 2001-08-16 |
BR0108282A (en) | 2002-10-29 |
NO20023782L (en) | 2002-08-09 |
JP2003525035A (en) | 2003-08-26 |
ES2202277T3 (en) | 2004-04-01 |
CN1404366A (en) | 2003-03-19 |
PL357298A1 (en) | 2004-07-26 |
EP1255457A1 (en) | 2002-11-13 |
ATE243438T1 (en) | 2003-07-15 |
BG107105A (en) | 2003-05-30 |
NO20023782D0 (en) | 2002-08-09 |
US20030089376A1 (en) | 2003-05-15 |
AU2001235450A1 (en) | 2001-08-20 |
KR20020075430A (en) | 2002-10-04 |
IL150790A0 (en) | 2003-02-12 |
DE50100335D1 (en) | 2003-07-31 |
HUP0204461A2 (en) | 2003-04-28 |
CA2398951A1 (en) | 2001-08-16 |
EA004085B1 (en) | 2003-12-25 |
PL193100B1 (en) | 2007-01-31 |
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