IPC분류정보
국가/구분 |
United States(US) Patent
등록
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국제특허분류(IPC7판) |
|
출원번호 |
US-0223752
(2002-08-19)
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발명자
/ 주소 |
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출원인 / 주소 |
- R. J. Reynolds Tobacco Company
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대리인 / 주소 |
DLA Piper Rudnick Gray Cary US LLP
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인용정보 |
피인용 횟수 :
65 인용 특허 :
47 |
초록
▼
Tobaccos are cured in a manner so as to provide tobaccos having extremely low tobacco specific nitrosamine (TSNA) contents. Harvested Virginia tobacco is subjected to flue-curing so as to provide flue-cured tobacco. During the curing processing steps, contact of the tobacco with nitric oxide gases,
Tobaccos are cured in a manner so as to provide tobaccos having extremely low tobacco specific nitrosamine (TSNA) contents. Harvested Virginia tobacco is subjected to flue-curing so as to provide flue-cured tobacco. During the curing processing steps, contact of the tobacco with nitric oxide gases, such as those produced as combustion products of propane burning heating units, is avoided. Tobacco in curing barns is not subjected to direct-fire curing techniques, but rather, heat for tobacco curing can be provided by heat exchange or electrical heating methods.
대표청구항
▼
1. A method for preparing cured Virginia tobacco that has a TSNA content below 2 ppm, based on the dry weight of cured tobacco, comprising the steps of:providing a barn with an air circulation device and a heat exchange unit; putting harvested green Virginia tobacco in the barn; producing heated air
1. A method for preparing cured Virginia tobacco that has a TSNA content below 2 ppm, based on the dry weight of cured tobacco, comprising the steps of:providing a barn with an air circulation device and a heat exchange unit; putting harvested green Virginia tobacco in the barn; producing heated air and nitric oxide gases through the act of burning a propane or diesel fuel in the heat exchange unit; preventing substantially all of the nitric oxide gases from contacting the harvested tobacco and from causing a chemical reaction therewith; circulating the heated air with the aid of the air circulation device, through the barn for at least about 120 hours in the absence of substantially all of the nitric oxide gases to produce cured tobacco while preventing formation of TSNA in the cured tobacco that would otherwise be formed by the chemical reaction; ascertaining the nitric oxide content in the barn while the heated air is being circulated there through: and determining that the TSNA content of the cured tobacco is below 2 ppm. 2. The method of claim 1, wherein the temperature of the heated air is about 35° C. to about 75° C.3. The method of claim 1, wherein the heated air is circulated for less than about 200 hours.4. The method of claim 1, wherein the step of circulating heated air comprises a yellowing treatment step, a leaf drying treatment step, and a midrib drying treatment.5. The method of claim 4, wherein the yellowing treatment step comprises circulating air heated to about 35° C. to about 40° C. for about 24 to about 72 hours.6. The method of claim 4, wherein the yellowing treatment step comprises circulating air heated to about 35° C. to about 40° C. for about 36 to about 60 hours.7. The method of claim 4, wherein during the yellowing treatment step, ambient air is introduced into the barn.8. The method of claim 4, wherein the leaf drying treatment step comprises circulating air heated to about 40° C. to about 57° C. for about 48 hours.9. The method of claim 4, wherein during the leaf drying treatment step, ambient air is introduced into the barn.10. The method of claim 9, wherein the amount of ambient air introduced into the barn during the leaf drying stage is greater than the amount of ambient air introduced into the barn during the yellowing stage.11. The method of claim 4, wherein the midrib drying treatment step comprises circulating air heated to about 57° C. to about 75° C. for about 48 hours.12. The method of claim 4, wherein during the midrib drying treatment step, heated air is recirculated within the barn.13. The method of claim 1, wherein the step of circulating heated air is performed for about 5 days to about 8 days.14. The method of claim 1, wherein the step of circulating heated air is performed for about 6 days to about 7 days.15. The method of claim 1, wherein the temperature of the heated air does not exceed about 90° C.16. The method of claim 15, wherein the temperature of the heated air does not exceed about 85° C.17. The method of claim 15, wherein the temperature of the heated air does not exceed about 80° C.18. The method of claim 4, wherein the relative humidity in the barn is about 85 percent during the yellowing treatment step.19. The method of claim 4, wherein the relative humidity in the barn is lower during leaf drying and midrib drying treatment steps compared to the yellowing treatment step.20. The method of claim 1, wherein the level of nitric oxide gases present in the barn during cure period does not exceed that normally present in non-polluted, ambient, environmental air.21. The method of claim 1, wherein the level of nitric oxide gases present in the barn during cure period is less than 0.1 kilogram of nitric oxide.22. The method of claim 1, wherein the level of nitric oxide gases present in the barn during cure period is less than 0.01 kilogram of nitric oxide.23. The method of claim 1, wherein the level of nitric oxide gases present in the barn at any time during cure period is about equal to the amount in ambient, environmental air.24. The method of claim 1, wherein the level of nitric oxide gases present in the barn at any time during cure period is less than the amount in ambient, environmental air.25. The method of claim 1, wherein the barn is further equipped with a means for removing nitric oxide gases from the atmosphere within the barn.26. The method of claim 25, wherein the means is selected from the group consisting of a catalytic conversion unit, scrubber, absorbent material, and selective filtration material.27. The method of claim 1, wherein the cured tobacco comprises sugar contents of about 12 to about 20 percent, based on the dry weight of the cured tobacco.28. The method of claim 1, wherein the TSNA content of cured tobacco is than less than 1.5 ppm, based on the dry weight of the cured tobacco.29. The method of claim 1, wherein the TSNA content of cured tobacco is less than 1 ppm, based on the dry weight of the cured tobacco.30. The method of claim 1, wherein the TSNA content of cured tobacco is less than 0.5 ppm, based on the dry weight of the cured tobacco.31. The method of claim 1, wherein the TSNA content of cured tobacco is undetectable.32. The method of claim 1, wherein the harvested green Virginia tobacco is not pre-treated.33. The method of claim 1, wherein the barn is a bulk barn.34. The method of claim 1, wherein the step of producing heated air and nitric oxide gas comprises the act of burning a propane fuel in the heat exchange unit.
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