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US20060162733A1 - Process of reducing generation of benzo[a]pyrene during smoking - Google Patents

Process of reducing generation of benzo[a]pyrene during smoking Download PDF

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Publication number
US20060162733A1
US20060162733A1 US11/289,314 US28931405A US2006162733A1 US 20060162733 A1 US20060162733 A1 US 20060162733A1 US 28931405 A US28931405 A US 28931405A US 2006162733 A1 US2006162733 A1 US 2006162733A1
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US
United States
Prior art keywords
tobacco
process according
extraction
benzo
pyrene
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
Application number
US11/289,314
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English (en)
Inventor
Thomas McGrath
Stephen Haut
W. Chan
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.)
Philip Morris USA Inc
Original Assignee
Philip Morris USA Inc
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 Philip Morris USA Inc filed Critical Philip Morris USA Inc
Priority to US11/289,314 priority Critical patent/US20060162733A1/en
Assigned to PHILIP MORRIS USA INC. reassignment PHILIP MORRIS USA INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MCGRATH, THOMAS E., HAUT, STEPHEN A., CHAN, W. GEOFFREY
Publication of US20060162733A1 publication Critical patent/US20060162733A1/en
Abandoned legal-status Critical Current

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    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/24Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
    • A24B15/26Use of organic solvents for extraction
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/24Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/24Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
    • A24B15/241Extraction of specific substances
    • A24B15/246Polycyclic aromatic compounds

Definitions

  • a process for manufacturing a smoking article having reduced generation of benzo[a]pyrene (B[a]P) during smoking thereof comprises preparing a treated tobacco by contacting a tobacco material with an extraction solvent consisting essentially of methanol, ethanol, 1-propanol or 2-propanol; and incorporating the treated tobacco in a smoking article.
  • FIG. 1 depicts B[a]P yields from the 600° C. pyrolysis in Helium of solvent extracted bright tobacco (120 ml/min flow rate, 600° C./min heating rate, 10 min).
  • FIG. 2 depicts the effect of proline (0.4% w/w) and lipids on the yield of B[a]P from the 600° C. pyrolysis of a carbohydrate+lignin mixture.
  • the lipid mixture consists of oleic acid (1 mg), linoleic acid (2 mg), linolenic acid (3.5 mg), stigmasterol (0.8 mg, chlorogenic acid (8 mg) and solanesol (15 mg) dissolved in methanol.
  • PAHs polycyclic aromatic hydrocarbons
  • B[a]P Benzo[a]pyrene
  • a 5-ring PAH Benzo[a]pyrene
  • lipophilic tobacco components such as phytosterols, saturated aliphatic hydrocarbons, and terpenoid compounds were believed to be the major precursors of PAHs formed from a burning cigarette.
  • a number of solvent extracted tobaccos and individual tobacco components such as sterols, long-chain hydrocarbons, fatty acids, carbohydrates and polyphenols have been pyrolyzed at 600° C. in an effort to identify low temperature B[a]P precursors.
  • the yield of B[a]P obtained per gram of sample pyrolyzed has been normalized to the amount of each component present in tobacco.
  • the B[a]P yield from a mixture of selected tobacco lipophilic and cell wall components has also been investigated.
  • the pyrolysis setup used was described in McGrath, T. E. et al., J. Anal. Appl. Pyrol., 66 (2003) 51-70.
  • the experimental setup consisted of a 2.5 cm i.d. quartz tube placed inside a 30 cm long heated Carbolite furnace having an isothermal length of ca. 7 cm at a temperature of 600° C. Helium was used as the carrier gas at a flow rate of 120 cm 3 /min.
  • the residence time of gas phase pyrolysis products in the isothermal section of the reactor was calculated to be approximately 4 s at a furnace temperature of 600° C.
  • a fiber-glass filter placed in a housing assembly immediately at the end of the quartz tube on the exit side of the furnace was used to collect the product tar condensate.
  • the temperature of the sample in the heated quartz tube was measured using a chromel/alumel (K type) thermocouple. The thermocouple was also used to transport the ceramic boat containing the samples to and from the heated isothermal region
  • the hexane and ethyl acetate and methanol extracted samples were prepared using a Soxhlet extraction setup.
  • the water extracted sample was prepared by extracting a sample of bright lamina packed in a column with a continuous stream of deionized water at room temperature. Exhaustive extraction processes in hexane, ethyl acetate, methanol and water lead to about a 4, 16, 40 and 50% reduction in sample weight, respectively.
  • Oleic acid (99+%), linoleic acid (99%), stigmasterol (93%) and cholesterol (99+%) were purchased from Aldrich. Linolenic acid (90%, remainder linoleic acid) and D(+)-proline (99+%) were purchased from Acros. Chlorogenic acid (95+%) and solanesol (90+% from tobacco leaves) were obtained from Sigma. A mixture of: oleic acid (1 mg/g), linoleic acid (2 mg/g), linolenic acid (3.5 mg/g), stigmasterol (0.8 mg/g), chlorogenic acid (8 mg/g) and solanesol (15 mg/g) was prepared in methanol and added to a mixture of carbohydrates and lignin.
  • Avicel cellulose, xylan from birch wood, pectin from citrus fruits, and hydrolytic lignin were used as model tobacco cell wall components.
  • the Avicel cellulose sample was obtained from FCI and is a microcrystalline purified and depolymerized alpha-cellulose derived from fibrous plants (Avicel PH-102). It has an ash content of less than 0.007%.
  • the birchwood xylan (>95% xylose) sample was obtained from Fluka.
  • the pectin sample was obtained from Sigma and has a galacturonic and methoxy content of 81% and 8.6%, respectively.
  • D-glucose was used as a model tobacco sugar. The D-glucose sample was obtained from Acros and is 99+% reagent grade.
  • a mixture of cellulose, hemicellulose, pectin, glucose, and lignin was made up with the following component ratios of 1:1:1: 1:0.3, respectively.
  • the resulting mixture is denoted as Carbo-Lig Mix throughout the rest of the text.
  • the samples also contained smaller amounts of Calcium.
  • a sample of tobacco or model tobacco compound to be pyrolyzed was placed in a ceramic boat that initially rested in an unheated section of the quartz tube outside of the heated furnace.
  • a tar trap assembly was placed on the exit side of the furnace. After the furnace had reached the desired set temperature, for example, 600° C., the sample was pushed to the isothermal region in the furnace and pyrolyzed for a total of 10 minutes.
  • the boat was pulled back to the unheated section of the quartz tube and the remaining solid residue was allowed to cool to room temperature.
  • the fiber-glass filter was removed, placed in an amber screw capped vial, and the washings from the pad housing assembly walls was added to the vial. A total solvent level of 5 mL of methanol was used and the vial was left to stir overnight on a shaker.
  • the quartz tube was cleaned in air at a temperature of 650° C.
  • the tar fractions collected were analyzed by GC-MS using an Agilent 6890 GC equipped with an Agilent 5973 quadrupole MSD analyzer operating in the single ion mode (SIM).
  • the yield of B[a]P was calculated using a calibration curve obtained from the analysis of standard solutions of B[a]P ranging from 10 to 1000 ng/ml.
  • B[a]P Yield Component (ng/g) (ng/g) Sterols Stigmasterol b ( ⁇ 0.8 mg/g) 1200 0.9 Isoprenoid Solanesol (20-40 mg/g) ND 0 Fatty Acids Oleic acid ( ⁇ 1 mg/g) 80 0.08 Linoleic acid ( ⁇ 2 mg/g) 175 0.35 Linolenic acid ( ⁇ 4 mg/g) 335 1.34 Carbohydrates Cellulose ( ⁇ 100 mg/g) 970 60 Hemicellulose ( ⁇ 100 mg/g) 976 60 Pectin ( ⁇ 100 mg/g) 100 10 Glucose ( ⁇ 140 mg/g) 786 98 Polyphenols Lignin ( ⁇ 40 mg/g) 934 18 Chlorogenic acid ( ⁇ 8 mg/g) ND ND not detected.
  • a carbohydrate+lignin mixture (Carbo-Lig mix) was pryolyzed in the presence of an amino acid (proline) and a mixture of tobacco lipid components. 0.4% w/w of D(+)-proline was physically mixed with the Carbo-Lig mix.
  • the lipid mixture consisted of oleic acid (1 mg/g), linoleic acid (2 mg/g), linolenic acid (3.5 mg/g), stigmasterol (0.8 mg/g), chlorogenic acid (8 mg/g) and solanesol (15 mg/g).
  • the amounts of amino acid and lipids added are consistent with the amount of each component present in bright tobacco. As shown in FIG.
  • Extraction of bright tobacco lamina with hexane and ethyl acetate removes lipophilic components of tobacco but does not lead to a decrease in B[a]P formed.
  • Extraction with methanol decreases the B[a]P yield by 35% whereas extraction with water significantly increases the yield of B[a]P.
  • the methanol extraction process appears to remove low temperature B[a]P precursors while extraction with water appears to concentrate B[a]P precursors on a per gram of material basis. From the individual tobacco components pyrolyzed at 600° C., only the tobacco carbohydrates and cell wall components such as glucose, cellulose, hemicellulose and lignin appear to contribute significantly to the formation of B[a]P.
  • Extraction of tobacco can also reduce generation of B[a]P during smoking.
  • the extraction with the methanol, ethanol, 1-propanol or 2-propanol is preferably carried out on tobacco which has not been subjected to a prior extraction with acetone.
  • the extraction is preferably carried out using a single solvent selected from the group consisting of methanol, ethanol, 1-propanol and 2-propanol.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacture Of Tobacco Products (AREA)
US11/289,314 2004-12-01 2005-11-30 Process of reducing generation of benzo[a]pyrene during smoking Abandoned US20060162733A1 (en)

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US20060283469A1 (en) * 2005-06-01 2006-12-21 Philip Morris Usa Inc. Tobacco with an increased level of natural tar diluents
US20070092636A1 (en) * 2005-10-24 2007-04-26 3M Innovative Properties Company Method of making light emitting device having a molded encapsulant
US20070141739A1 (en) * 2005-10-24 2007-06-21 3M Innovative Properties Company Method of making light emitting device having a molded encapsulant
WO2008108889A1 (fr) 2006-10-18 2008-09-12 R.J.Reynolds Tobacco Company Article à fumer contenant du tabac
US20120125354A1 (en) * 2010-11-18 2012-05-24 R.J. Reynolds Tobacco Company Fire-Cured Tobacco Extract and Tobacco Products Made Therefrom
WO2013148810A1 (fr) 2012-03-28 2013-10-03 R. J. Reynolds Tobacco Company Article à fumer incorporant un substrat conducteur
US8881737B2 (en) 2012-09-04 2014-11-11 R.J. Reynolds Tobacco Company Electronic smoking article comprising one or more microheaters
US8910640B2 (en) 2013-01-30 2014-12-16 R.J. Reynolds Tobacco Company Wick suitable for use in an electronic smoking article
US8910639B2 (en) 2012-09-05 2014-12-16 R. J. Reynolds Tobacco Company Single-use connector and cartridge for a smoking article and related method
US9078473B2 (en) 2011-08-09 2015-07-14 R.J. Reynolds Tobacco Company Smoking articles and use thereof for yielding inhalation materials
US9220302B2 (en) 2013-03-15 2015-12-29 R.J. Reynolds Tobacco Company Cartridge for an aerosol delivery device and method for assembling a cartridge for a smoking article
US9277770B2 (en) 2013-03-14 2016-03-08 R. J. Reynolds Tobacco Company Atomizer for an aerosol delivery device formed from a continuously extending wire and related input, cartridge, and method
US9423152B2 (en) 2013-03-15 2016-08-23 R. J. Reynolds Tobacco Company Heating control arrangement for an electronic smoking article and associated system and method
US9451791B2 (en) 2014-02-05 2016-09-27 Rai Strategic Holdings, Inc. Aerosol delivery device with an illuminated outer surface and related method
US9491974B2 (en) 2013-03-15 2016-11-15 Rai Strategic Holdings, Inc. Heating elements formed from a sheet of a material and inputs and methods for the production of atomizers
US9597466B2 (en) 2014-03-12 2017-03-21 R. J. Reynolds Tobacco Company Aerosol delivery system and related method, apparatus, and computer program product for providing control information to an aerosol delivery device via a cartridge
US9609893B2 (en) 2013-03-15 2017-04-04 Rai Strategic Holdings, Inc. Cartridge and control body of an aerosol delivery device including anti-rotation mechanism and related method
US9833019B2 (en) 2014-02-13 2017-12-05 Rai Strategic Holdings, Inc. Method for assembling a cartridge for a smoking article
US9839237B2 (en) 2013-11-22 2017-12-12 Rai Strategic Holdings, Inc. Reservoir housing for an electronic smoking article
US9839238B2 (en) 2014-02-28 2017-12-12 Rai Strategic Holdings, Inc. Control body for an electronic smoking article
US9854841B2 (en) 2012-10-08 2018-01-02 Rai Strategic Holdings, Inc. Electronic smoking article and associated method
US9877510B2 (en) 2014-04-04 2018-01-30 Rai Strategic Holdings, Inc. Sensor for an aerosol delivery device
US9918495B2 (en) 2014-02-28 2018-03-20 Rai Strategic Holdings, Inc. Atomizer for an aerosol delivery device and related input, aerosol production assembly, cartridge, and method
US9924741B2 (en) 2014-05-05 2018-03-27 Rai Strategic Holdings, Inc. Method of preparing an aerosol delivery device
US9974334B2 (en) 2014-01-17 2018-05-22 Rai Strategic Holdings, Inc. Electronic smoking article with improved storage of aerosol precursor compositions
US10004259B2 (en) 2012-06-28 2018-06-26 Rai Strategic Holdings, Inc. Reservoir and heater system for controllable delivery of multiple aerosolizable materials in an electronic smoking article
US10031183B2 (en) 2013-03-07 2018-07-24 Rai Strategic Holdings, Inc. Spent cartridge detection method and system for an electronic smoking article
US10117460B2 (en) 2012-10-08 2018-11-06 Rai Strategic Holdings, Inc. Electronic smoking article and associated method
US10172387B2 (en) 2013-08-28 2019-01-08 Rai Strategic Holdings, Inc. Carbon conductive substrate for electronic smoking article
US10238145B2 (en) 2015-05-19 2019-03-26 Rai Strategic Holdings, Inc. Assembly substation for assembling a cartridge for a smoking article
US10405579B2 (en) 2016-04-29 2019-09-10 Rai Strategic Holdings, Inc. Methods for assembling a cartridge for an aerosol delivery device, and associated systems and apparatuses
US10575558B2 (en) 2014-02-03 2020-03-03 Rai Strategic Holdings, Inc. Aerosol delivery device comprising multiple outer bodies and related assembly method
US10888119B2 (en) 2014-07-10 2021-01-12 Rai Strategic Holdings, Inc. System and related methods, apparatuses, and computer program products for controlling operation of a device based on a read request
WO2021009730A1 (fr) 2019-07-18 2021-01-21 R. J. Reynolds Tobacco Company Absorbeurs d'énergie thermique destinés à la production de produits permettant de chauffer du tabac
US11229239B2 (en) 2013-07-19 2022-01-25 Rai Strategic Holdings, Inc. Electronic smoking article with haptic feedback
US11666098B2 (en) 2014-02-07 2023-06-06 Rai Strategic Holdings, Inc. Charging accessory device for an aerosol delivery device and related system, method, apparatus, and computer program product for providing interactive services for aerosol delivery devices
US11696604B2 (en) 2014-03-13 2023-07-11 Rai Strategic Holdings, Inc. Aerosol delivery device and related method and computer program product for controlling an aerosol delivery device based on input characteristics
US12285042B2 (en) 2013-03-12 2025-04-29 Rai Strategic Holdings, Inc. Electronic smoking article having a vapor-enhancing apparatus and associated method
US12369632B2 (en) 2013-03-14 2025-07-29 Rai Strategic Holdings, Inc. Electronic smoking article with improved storage and transport of aerosol precursor compositions

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