CA2398951A1 - Method for improving the filling ability of tobacco - Google Patents
Method for improving the filling ability of tobacco Download PDFInfo
- Publication number
- CA2398951A1 CA2398951A1 CA002398951A CA2398951A CA2398951A1 CA 2398951 A1 CA2398951 A1 CA 2398951A1 CA 002398951 A CA002398951 A CA 002398951A CA 2398951 A CA2398951 A CA 2398951A CA 2398951 A1 CA2398951 A1 CA 2398951A1
- Authority
- CA
- Canada
- Prior art keywords
- tobacco
- compression
- treatment
- carried out
- continuous
- 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.)
- Abandoned
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
Landscapes
- Manufacture Of Tobacco Products (AREA)
Abstract
The invention relates to a method for improving the filling ability of tobacco, such as cut tobacco leaves, or ribs, or tobacco additives, whereby the tobacco material with an initial water content of up to 15 wt % is treated with a gas, comprising nitrogen and/or argon, at pressures from 50 to 1000 bar with a continuous, or staged compression, followed by a continuous or staged decompression, whereby the compression and decompression steps occur in, either an autoclave, or a cascade-like series of several autoclaves and, finally, a thermal after-treatment of the withdrawn tobacco material. The invention is characterised in that the compression is carried out at a working temperature of over 55 ~C, preferably from 60 to 90 ~C and the final water content of the tobacco is in the range of 8 to 14 wt. %.
Description
~cr/~P~o~ /oWzq METHOD FOR IMPROVING THE FILLING ABILITY
OF TOBACCO
The invention relates to a method for improving the fillabil-ity of tobacco, as cut tobacco leaves or ribs and/or tobacco additives, by treatment of the tobacco material, which initially has up to 15 wt.% moisture with a treatment gas con-sisting of nitrogen and/or argon at pressures of 50 to 1,000 bar with continuous or graduated compression followed by con-tinuous or graduated decompression, in which the compression or decompression stages take place in either an autoclave or with cascade-type switching in several autoclaves, followed by thermal after-treatment of the tobacco material discharged.
Methods of this kind, which are also known as INCOM expansion methods, have proved to be advantageous compared with the pressure treatment of tobacco with carbon dioxide, ammonia or volatile organic gases. Thus DE 31 19 330 A1 describes such an expansion method with operating temperatures of 0 to 50°C pre-vailing in the autoclave, wherein to increase the fillability or the degree of expansion, use of a tobacco material with moisture of up to 15 wt.% and after-treatment with water vapour was provided. In this case the aim was that lower moisture of the tobacco of 10 to 15 wt.% would lead to a desired greater cooling of the tobacco material to be dis-charged when the tension was released.
Furthermore, DE 34 14 625 C2 discloses a cascade method, according to which, by the most widely varying measures such as cooling of the treatment gas before loading of the reactor, cooling of the autoclaves or use of an undercooled and liquefied treatment gas, a low operating temperature is to be effected during impregnation of the tobacco. It is true that the tobacco moisture may lie anywhere, for instance within the range of 10 - 30 wt.%, however it is expressly required that the autoclave temperature and/or its cooling water temperature must not exceed 50°C.
OF TOBACCO
The invention relates to a method for improving the fillabil-ity of tobacco, as cut tobacco leaves or ribs and/or tobacco additives, by treatment of the tobacco material, which initially has up to 15 wt.% moisture with a treatment gas con-sisting of nitrogen and/or argon at pressures of 50 to 1,000 bar with continuous or graduated compression followed by con-tinuous or graduated decompression, in which the compression or decompression stages take place in either an autoclave or with cascade-type switching in several autoclaves, followed by thermal after-treatment of the tobacco material discharged.
Methods of this kind, which are also known as INCOM expansion methods, have proved to be advantageous compared with the pressure treatment of tobacco with carbon dioxide, ammonia or volatile organic gases. Thus DE 31 19 330 A1 describes such an expansion method with operating temperatures of 0 to 50°C pre-vailing in the autoclave, wherein to increase the fillability or the degree of expansion, use of a tobacco material with moisture of up to 15 wt.% and after-treatment with water vapour was provided. In this case the aim was that lower moisture of the tobacco of 10 to 15 wt.% would lead to a desired greater cooling of the tobacco material to be dis-charged when the tension was released.
Furthermore, DE 34 14 625 C2 discloses a cascade method, according to which, by the most widely varying measures such as cooling of the treatment gas before loading of the reactor, cooling of the autoclaves or use of an undercooled and liquefied treatment gas, a low operating temperature is to be effected during impregnation of the tobacco. It is true that the tobacco moisture may lie anywhere, for instance within the range of 10 - 30 wt.%, however it is expressly required that the autoclave temperature and/or its cooling water temperature must not exceed 50°C.
This is also confirmed according to DE 39 35 774 C2 in con-nection with a cascade-type expansion method, in which circu-lation of the treatment gas via a cooler is provided, in order to keep to the necessary low impregnation temperatures of 25 or 45°C.
Although good values have already been achieved with the aforementioned expansion methods with regard to increasing the fillability of tobacco and/or the degree of expansion, these are relatively expensive because of the necessary cooling of the autoclave or autoclaves and because of the additional cooling of the treatment gas.
The aim of the invention is to improve the existing INCOM
methods and with equally good or better values with regard to fillability or expansion effect, to avoid the uneconomical cooling measures during compression which have hitherto been regarded as necessary.
According to the invention a method of the type initially mentioned according to the preamble to the patent claim, is therefore proposed, which is characterised by the fact that the compression is carried out at a reactor temperature of above 55°C.
Surprisingly it has transpired that in the case of low tobacco moistures within the range of up to 15 wt.% the existing theory, which requires a low treatment temperature, does not lead to optimum expansion results. On the contrary, only by increasing the treatment temperature during compression was it possible to achieve surprisingly good values with regard to the expansion effect and/or fillability.
Furthermore, according to the method, this leads to the advantage, that the heat of compression does not have to be eliminated, and thus no additional cooling of the autoclave or autoclaves is necessary.
Although good values have already been achieved with the aforementioned expansion methods with regard to increasing the fillability of tobacco and/or the degree of expansion, these are relatively expensive because of the necessary cooling of the autoclave or autoclaves and because of the additional cooling of the treatment gas.
The aim of the invention is to improve the existing INCOM
methods and with equally good or better values with regard to fillability or expansion effect, to avoid the uneconomical cooling measures during compression which have hitherto been regarded as necessary.
According to the invention a method of the type initially mentioned according to the preamble to the patent claim, is therefore proposed, which is characterised by the fact that the compression is carried out at a reactor temperature of above 55°C.
Surprisingly it has transpired that in the case of low tobacco moistures within the range of up to 15 wt.% the existing theory, which requires a low treatment temperature, does not lead to optimum expansion results. On the contrary, only by increasing the treatment temperature during compression was it possible to achieve surprisingly good values with regard to the expansion effect and/or fillability.
Furthermore, according to the method, this leads to the advantage, that the heat of compression does not have to be eliminated, and thus no additional cooling of the autoclave or autoclaves is necessary.
In the following example, the method according to the invention is explained in comparison with the existing state of the art. The test results show the differing influence of the operating temperature on the degree of expansion for different tobacco moistures. According to the existing theory, in the case of tobacco moisture of 18 wt.%, increasing the operating temperature above 40°C leads to a deterioration in the expansion effect. On the other hand, in the case of tobacco moistures of below 15 wt.%, clear improvements appear if the high pressure treatment is carried out at operating temperatures of 60 and 80°C. Surprisingly the achievable degrees of expansion with low tobacco moisture and higher operating temperatures are even in some cases above the values achieved under conventional conditions.
Example The high pressure treatment was carried out in a laboratory autoclave with a used content of 2 1. A casing for circulation of liquid media was used to adjust the desired operating temperatures. The build-up of pressure was carried out from below, the reduction in pressure upwards. Several valves made the intended circuit diagrams possible. A compressor was used to adjust the final pressure. A thermocouple element measured the tobacco temperature in the upper tobacco filling section.
The laboratory device for thermal after-treatment consisted of a permeable wire gauze serving as a conveyor belt, baffles for formation of the tobacco mat in the desired width, a steam nozzle with slit-type outlet and a steam suction device arranged under the belt. The after-treatment was carried out with saturated steam.
The most important treatment parameters are shown by the following Table 1.
Example The high pressure treatment was carried out in a laboratory autoclave with a used content of 2 1. A casing for circulation of liquid media was used to adjust the desired operating temperatures. The build-up of pressure was carried out from below, the reduction in pressure upwards. Several valves made the intended circuit diagrams possible. A compressor was used to adjust the final pressure. A thermocouple element measured the tobacco temperature in the upper tobacco filling section.
The laboratory device for thermal after-treatment consisted of a permeable wire gauze serving as a conveyor belt, baffles for formation of the tobacco mat in the desired width, a steam nozzle with slit-type outlet and a steam suction device arranged under the belt. The after-treatment was carried out with saturated steam.
The most important treatment parameters are shown by the following Table 1.
Table 1 High ressure Thermal after-treatment treatment Gas supply from below Steaming about 10 kg/h ca acit Gas outlet a wards Slit nozzle about 8 mm Tobacco 300 g Slit width about 160 mm antit Tobacco PVC pipe/ Transport about 5 cm/s container perforated bottom The tobacco samples were spread out in flat plastic trays and conditioned in the standard climate at 21°C and 62% relative humidity. The fillabilities were determined using a Borgwaldt density meter, and the specific volume in ml/g converted for a nominal moisture of 12 wt.% and a nominal temperature of 22°C.
From the data of the untreated comparison/base specimens and the expanded specimens, the relative improvement in fillability, which is also described as the degree of expansion, can be calculated according to the following formula, in which FH means the fillability of the base and FE
means the fillability of the expanded tobacco:
d °s = (Ffi - FH) * loo% / FB
The tests were carried out with tobacco moistures of 8, 12 and 14 and 18 wt.% as a comparison. The operating temperatures were adjusted by thermostatic control to 40, 60 and 80°C. The final pressure amounted to 700 bar, the pressure reduction was carried out in a time interval of approx. 0.5 min. All the tests were based on a uniform mixture of Virginia tobaccos and the after-treatment method with saturated steam described.
The results of the tests are represented in the following Table 2, and those of the comparative test in the following Table 2a. In the tables T" means the tobacco temperature immediately before removal from the autoclave as discharge temperature and O % means the relative improvement in fillability and/or degree of expansion.
From the data of the untreated comparison/base specimens and the expanded specimens, the relative improvement in fillability, which is also described as the degree of expansion, can be calculated according to the following formula, in which FH means the fillability of the base and FE
means the fillability of the expanded tobacco:
d °s = (Ffi - FH) * loo% / FB
The tests were carried out with tobacco moistures of 8, 12 and 14 and 18 wt.% as a comparison. The operating temperatures were adjusted by thermostatic control to 40, 60 and 80°C. The final pressure amounted to 700 bar, the pressure reduction was carried out in a time interval of approx. 0.5 min. All the tests were based on a uniform mixture of Virginia tobaccos and the after-treatment method with saturated steam described.
The results of the tests are represented in the following Table 2, and those of the comparative test in the following Table 2a. In the tables T" means the tobacco temperature immediately before removal from the autoclave as discharge temperature and O % means the relative improvement in fillability and/or degree of expansion.
Table 2 Operating temperatureTobaccomoisture8Tobaccomoisturel2Tobaccomoisturel4 C urt.% vvt.% urt.%
TA oC a % TA oC D % TA oC D
Table 2a Operating temperature ° C Tobacco moisture 18 wt.~°
TA o C 0 Comparison of the above tables clearly shows the positive effect o~ higher operating temperatures of 60 and 80°C on the improvement of fillability, if tobacco with moistures of less than 15 wt.s is used.
TA oC a % TA oC D % TA oC D
Table 2a Operating temperature ° C Tobacco moisture 18 wt.~°
TA o C 0 Comparison of the above tables clearly shows the positive effect o~ higher operating temperatures of 60 and 80°C on the improvement of fillability, if tobacco with moistures of less than 15 wt.s is used.
Claims (3)
1. Method for improving the fillability of tobacco, as cut tobacco leaves or ribs and/or tobacco additives, by treatment of the tobacco material, which has up to approx. 15 wt.%
initial moisture with a treatment gas consisting of nitrogen and/or argon at pressures of 50 to 1,000 bar with continuous or graduated compression followed by continuous or graduated decompression, the compression or decompression stages being carried out in either one autoclave or with cascade-type switching in several autoclaves, followed by thermal after-treatment of the tobacco material discharged, characterised in that the compression is carried out at an operating temperature above 55°C.
initial moisture with a treatment gas consisting of nitrogen and/or argon at pressures of 50 to 1,000 bar with continuous or graduated compression followed by continuous or graduated decompression, the compression or decompression stages being carried out in either one autoclave or with cascade-type switching in several autoclaves, followed by thermal after-treatment of the tobacco material discharged, characterised in that the compression is carried out at an operating temperature above 55°C.
2. Method according to claim 1, characterised in that the compression is carried out at an operating temperature of 60 to 90°C.
3. Method according to claim 1, characterised in that the initial moisture of the tobacco material lies within the range 8 to 14 wt.%.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10006425A DE10006425C1 (en) | 2000-02-14 | 2000-02-14 | Process for improving the fillability of tobacco |
DE10006425.6 | 2000-02-14 | ||
PCT/EP2001/001229 WO2001058288A1 (en) | 2000-02-14 | 2001-02-05 | Method for improving the filling ability of tobacco |
Publications (1)
Publication Number | Publication Date |
---|---|
CA2398951A1 true CA2398951A1 (en) | 2001-08-16 |
Family
ID=7630805
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002398951A Abandoned CA2398951A1 (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 US US10/182,733 patent/US20030089376A1/en not_active Abandoned
- 2001-02-05 CA CA002398951A patent/CA2398951A1/en not_active Abandoned
- 2001-02-05 PL PL357298A patent/PL193100B1/en unknown
- 2001-02-05 EA EA200200856A patent/EA004085B1/en not_active IP Right Cessation
- 2001-02-05 EP EP01907496A patent/EP1255457B1/en not_active Expired - Lifetime
- 2001-02-05 SK SK1332-2002A patent/SK13322002A3/en unknown
- 2001-02-05 DE DE50100335T patent/DE50100335D1/en not_active Expired - Lifetime
- 2001-02-05 IL IL15079001A patent/IL150790A0/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 CZ CZ20023079A patent/CZ20023079A3/en unknown
- 2001-02-05 AT AT01907496T patent/ATE243438T1/en not_active IP Right Cessation
- 2001-02-05 AU AU2001235450A patent/AU2001235450A1/en not_active Abandoned
- 2001-02-05 HU HU0204461A patent/HUP0204461A2/en unknown
- 2001-02-05 ES ES01907496T patent/ES2202277T3/en not_active Expired - Lifetime
- 2001-02-05 EE EEP200200448A patent/EE200200448A/en unknown
- 2001-02-05 KR KR1020027010639A patent/KR20020075430A/en not_active Application Discontinuation
- 2001-02-05 CN CN01805011A patent/CN1404366A/en active Pending
- 2001-02-05 JP JP2001557410A patent/JP2003525035A/en not_active Withdrawn
- 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 |
---|---|
EP1255457B1 (en) | 2003-06-25 |
US20030089376A1 (en) | 2003-05-15 |
UA72316C2 (en) | 2005-02-15 |
AU2001235450A1 (en) | 2001-08-20 |
NO20023782L (en) | 2002-08-09 |
DE50100335D1 (en) | 2003-07-31 |
SK13322002A3 (en) | 2003-02-04 |
BR0108282A (en) | 2002-10-29 |
ES2202277T3 (en) | 2004-04-01 |
EA200200856A1 (en) | 2003-06-26 |
ATE243438T1 (en) | 2003-07-15 |
PL193100B1 (en) | 2007-01-31 |
HUP0204461A2 (en) | 2003-04-28 |
JP2003525035A (en) | 2003-08-26 |
EA004085B1 (en) | 2003-12-25 |
AR027419A1 (en) | 2003-03-26 |
PL357298A1 (en) | 2004-07-26 |
KR20020075430A (en) | 2002-10-04 |
DE10006425C1 (en) | 2001-08-16 |
CZ20023079A3 (en) | 2003-03-12 |
NO20023782D0 (en) | 2002-08-09 |
EE200200448A (en) | 2003-12-15 |
CN1404366A (en) | 2003-03-19 |
EP1255457A1 (en) | 2002-11-13 |
IL150790A0 (en) | 2003-02-12 |
WO2001058288A1 (en) | 2001-08-16 |
BG107105A (en) | 2003-05-30 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FZDE | Discontinued |