• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A novel tobacco product comprising tobacco containing gaseous carbon dioxide in an amount of at least 1 part of gaseous carbon dioxide per 100 parts of tobacco. The product, when rapidly heated is converted to expanded tobacco. An improved process for the expansion of tobacco is also provided which employs carbon dioxide as the expansion agent in a sequence of steps comprising: (1) contacting tobacco with carbon dioxide gas at a pressure of at least 250 psig for a time sufficient to impregnate the tobacco with the carbon dioxide gas to form a gaseous carbon dioxide- tobacco system, (2) releasing the pressure and (3) thereafter subjecting the carbon dioxide-treated tobacco to rapid heating conditions to remove the carbon dioxide and thereby expand the tobacco. The improvement in the above-described process comprising cooling the gaseous carbon dioxide and tobacco system in step (1) to a temperature close to the saturation temperature of carbon dioxide but not lower than -23 DEG C.
    公开号:SU1268091A3
    申请号:SU792748255
    申请日:1979-03-28
    公开日:1986-10-30
    发明作者:З.Де Ла Бурде Роджер；Е.Омент Патрик；В.Атш Фрэнсиз
    申请人:Филип Моррис Инкорпорейтед (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to the tobacco industry and can be used to increase the volume of tobacco. The aim of the invention is to improve the quality of tobacco. SUMMARY OF THE INVENTION The essence of the invention is that tobacco is placed in a carbon dioxide container in which pressure is applied. 17.6-56.2 MPa for 4 to 30 minutes until a mixture containing at least one part of dioxide is obtained. carbon per 100 parts of tobacco. At the same time, the pressure is quickly reduced to its atmospheric value and the resulting mixture of tobacco and carbon dioxide is heated to TOO-ZUS C to increase the volume of tobacco. To increase the amount of carbon dioxide remaining in tobacco with an increase in the volume of the latter, when carbon dioxide is supplied, the temperature is reduced to a temperature close to the saturation temperature of carbon dioxide (-23 ° C), which allows partial condensation of the latter inside tobacco. To this end, pre-snowing of tobacco with finely crushed dry ice (solid carbon dioxide) can be used, which combines cooling with the additional supply of carbon dioxide to tobacco and regulation of carbon dioxide supply to tobacco. You can also use the supply of cooled carbon dioxide in tobacco. Example 1. A sample weighing 400 g of light tobacco filler with a furnace content of 12.5% of volatile tobacco substances is placed in a high-pressure vessel such as an autoclave, from the tank containing carbon dioxide, the latter is fed under pressure until the pressure in the autoclave is approximately 56.2 MPa. The temperature is maintained above 30 ° C. to prevent the formation of liquid and solid carbon dioxide. The contact time of tobacco with carbon dioxide and the temperature was chosen such that the heat capacity of the process was 78.7 kcal / kg. Then, by releasing carbon dioxide from the autoclave, the pressure is brought to atmospheric pressure within 0.5 minutes, the tobacco is cooled to 2.2 ° C. The weight of the tobacco sample is increased by 2% due to carbon dioxide. The sample is then heated to 288 ° C for 5 minutes to increase the volume of the tobacco. The resulting tobacco sample contains 2.1% volatile matter. After equilibration at standard conditions at 23.9 ° C and a humidity of 60% (after 18 hours), the increase in volume is 11%. Example 2. A series of light tobacco samples is treated as in Example 1. The content of furnace volatile matter varies from 9 to 14.6%. Pressure - 56.2 ati. Indicators of an increase in the volume of tobacco during this lead, the price in the table. 1. Example 3. A series of light tobacco samples is treated as in Example 1 under conditions when the used COj does not form solid and liquid phases. Whether pressure of impregnation changed. The data obtained are given in table. 2 (missing values correspond to example 1). . . Example 4. A 400 g light tobacco filler sample with a furnace volatile content of 11.1% was placed in a high pressure vessel and passed a jet of COj to a pressure of 56.2 atm as in Example 1. The jet of CO was cooled to a temperature close to saturation. After 15 minutes holding for 0.5 minutes, the pressure is reduced. After that, the temperature of the tobacco is 37.8 ° C, and the weight increment due to C0 is 3.5%. The sample is then heated as in Example 1 of an increase in yI. After heating, the furnace volatile content is 1.9%. The balanced product has a cylindrical volume of 90.6 cm and a kiln volatile content of 10.8%, which corresponds to a corrected cylindrical volume of 89 cm, an increase in the degree of filling is 147% compared to the control. Example 5. A series of light tobacco samples are treated as in Example 4. Before relieving pressure, CO is cooled to a state close to saturation at three different pressures. The results are shown in Table. 3 (missing data correspond to example 1). Example 6. Repeat Example 4. But using thick shells of tobacco. Balanced sample
    after the increase in volume, it has a cylindrical volume of 92.4 cm with a furnace volatile content of 10.1%. The increase is 100% compared to the control.
    Example 7. A sample of LIGHT TObacco weighing 2 kg is treated with COj as in Example 4, then heated at 149 ° C for 5 minutes. The balanced product has a cylindrical volume of 85 cm.
    Example 8. Samples are treated according to example 5. But before contact with CO, tobacco sfé is cooled to a temperature slightly lower. The idtdric values were 92.92 and 87 cm, which corresponds to an increase in the degree of filling of 151% compared to the untreated control.
    Example .9. The sample is treated as in example 7, but at room temperature. The resulting product has no increase compared with the control.
    Example 10. For comparison, using CO; in the gaseous and liquid state 1.5 kg of light tobacco filler containing
    12.7% volatile substances are melted with liquid COj at a pressure of 56.2 atm, cooled to 19, and allowed to stand for 15 minutes. After that, drain excess fluid and relieve pressure. Weight gain is 23%. The material partially clumps together. Cylindrical volume 79 cm.
    Example 11. Gaseous COg, 15 min is treated with 1.2 kg of light tobacco filler at 19.6 pressure 56.2 MPa. The furnace volatile content is 13-, 3%. After depressurization, the percentage increase in weight is 3 due to CO adsorption. The material is free flowing and easy to handle. The cylindrical volume is 82 cm.
    Example 12. When processing tobacco according to example 1, the pressure is changed from 5.6 to 56.2 atm. The heat treatment temperature is 316 ° C. The optimal values of the volume increase were obtained with the values of the parameters corresponding to the proposed method.
    The invention provides an improvement in the quality of tobacco by increasing its volume.
    Table 1
    COj temperature before gas release, С
    The content of furnace volatile substances in tobacco, vol.%
    The temperature of the tobacco after release, ° C
    COJ retention on tobacco, vol.%
    The content of furnace volatile substances in the product after increasing the volume of tobacco, -06.%
    Cylindrical volume of the processed product, cm
    The content of furnace volatile substances in the treated product, about. %
    32.2
    31.7 14.6 10.3
    + 2.8
    -22.6 2.4 1.5
    1.8
    3.2
    94 74
    10.3
    11.3
    Corrected: cylinder, drichesky volume with the content of furnace volatile substances 11 06.%,
    Increasing the degree of filling, vol.% CO temperature before -17.7 Na 20 gas outflow, ° C Heat capacity, kcal / kg 78.7 Na 78 Temperature of tobacco after -13.9 Na 3, gas release, C Content of furnace volatile matter after volume increase, vol.% 2.2 1.9 Cylindrical volume 69 66 of the processed product, see Content of furnace volatile substances of the processed product, vol. % 10.7 11.5 Corrected cylindrical volume with the content of furnace volatile substances 66 69 11% by volume, cm Increase in the degree of filling 83 92% not, about. %
    Continued tabl, 1
    66
    88
    76
    144
    83
    111
    Table 2 0.6 19, 9 8.6--. 78 79 5.6- -16.7- -20.6 2.1 3.4 2.7 1.7 11.4 11.5 11.6 14 81
    COj temperature before gas injection, ° С
    Heat capacity before releasing COj, kcal / kg
    Tobacco temperature after
    vtuskan JI, with
    Retention of tobacco, vol.%
    Kiln content
    substances after magnification
    volume of tobacco, vol.%
    Cylindrical volume of the processed product, cm
    The content of furnace volatile substances processed product, o6.Z
    Adjusted cylindrical volume with the content of the furnace volatile substances 11 vol.%, Cm
    Increasing the degree of filling
    about.%
    Table 3
    2.2 80
    -18.3 2.4
    1.9
    71
    11.9
    78,117
    权利要求:
    Claims (4)
    [1]
    1. METHOD FOR INCREASING TOBACCO VOLUME by treating it with carbon dioxide gas under pressure, followed by its reduction, characterized in that, in order to improve the quality of tobacco, tobacco processing is carried out at a pressure of 17.6 -
    56.2 atm, followed by cooling to a temperature that ensures the preservation of carbon dioxide in a gaseous state, while treating the tobacco to obtain a mixture comprising at least one part of carbon monoxide per 100 parts of tobacco, and after reducing the pressure, the mixture is heated to remove gas.
    [2]
    2. The method according to p. 1, characterized in that the treatment with carbon dioxide is carried out at a pressure of 28.1-56.2 ati.
    [3]
    3. The method according to PP. 1 and 2, which consists in the fact that the heating of the resulting mixture is carried out at 100 - 370 ° C.
    [4]
    4. The method according to PP. 1-3, characterized in that the pressure is reduced by reducing it to atmospheric pressure.
    SU, B , 1268091 AZ
    类似技术:
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    同族专利:
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US1789435A|1929-01-28|1931-01-20|American Mach & Foundry|Expanding tobacco|
    US2344106A|1939-07-14|1944-03-14|Larus & Brother Company Inc|Method of and apparatus for treating tobacco|
    US3771533A|1970-08-31|1973-11-13|Philip Morris Inc|Process for puffing tobacco|
    AU450553B2|1970-12-21|1974-07-11|Philip Morris Incorporated|Process for puffing tobacco|
    GB1375820A|1970-12-21|1974-11-27|
    IT1031068B|1974-02-05|1979-04-30|Airco Inc|METHOD AND EQUIPMENT FOR THE EXPANSION OF OR GANIC SUBSTANCES|
    US4340073A|1974-02-12|1982-07-20|Philip Morris, Incorporated|Expanding tobacco|DE3119330C2|1981-05-15|1983-06-01|H.F. & Ph.F. Reemtsma Gmbh & Co, 2000 Hamburg|Process for improving the filling capacity of tobacco|
    JPS642118Y2|1981-05-25|1989-01-18|
    JPS58137284U|1982-03-09|1983-09-14|
    US4460000A|1982-06-14|1984-07-17|The Boc Group, Inc.|Vacuum and gas expansion of tobacco|
    US4531529A|1982-10-04|1985-07-30|R. J. Reynolds Tobacco Company|Process for increasing filling capacity of tobacco|
    DE3414625C2|1983-04-21|1988-02-11|H.F. & Ph.F. Reemtsma Gmbh & Co, 2000 Hamburg, De|
    US4528994A|1983-12-16|1985-07-16|Brown & Williamson Tobacco Corporation|Tobacco treating process|
    US4630619A|1983-12-16|1986-12-23|Brown & Williamson Tobacco Corp.|Process for treating tobacco|
    US4791942A|1986-08-01|1988-12-20|The American Tobacco Company|Process and apparatus for the expansion of tobacco|
    CA1328064C|1987-07-27|1994-03-29|Masao Kobari|Apparatus for expanding material for foodstuffs, favorite items and the like|
    DE3841915C1|1988-12-13|1990-05-10|Laszlo Dr. Basel Ch Egri|Tobacco heat treatment plant - incorporates drums with wetting jets and revolving blades|
    CA2005332A1|1988-12-13|1990-06-13|Laszlo Egri|Method of and apparatus for expanding tobacco|
    JPH0330660A|1989-06-19|1991-02-08|R J Reynolds Tobacco Co|Method for expanding tobacco material|
    US5251649A|1991-06-18|1993-10-12|Philip Morris Incorporated|Process for impregnation and expansion of tobacco|
    SK139993A3|1992-12-17|1994-09-07|Philip Morris Prod|Method of impregnation and expanding of tobacco and device for its performing|
    GB201221207D0|2012-11-26|2013-01-09|British American Tobacco Co|Treatment of tobacco material|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/891,468|US4258729A|1978-03-29|1978-03-29|Novel tobacco product and improved process for the expansion of tobacco|
    US05/891,290|US4235250A|1978-03-29|1978-03-29|Process for the expansion of tobacco|
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