WO2020128971A1 - Procédé de blanchiment de tabac - Google Patents

Procédé de blanchiment de tabac Download PDF

Info

Publication number
WO2020128971A1
WO2020128971A1 PCT/IB2019/061129 IB2019061129W WO2020128971A1 WO 2020128971 A1 WO2020128971 A1 WO 2020128971A1 IB 2019061129 W IB2019061129 W IB 2019061129W WO 2020128971 A1 WO2020128971 A1 WO 2020128971A1
Authority
WO
WIPO (PCT)
Prior art keywords
tobacco
pulp
tobacco material
whitened
smokeless
Prior art date
Application number
PCT/IB2019/061129
Other languages
English (en)
Inventor
David Neil Mcclanahan
Michael David DAVIS
Original Assignee
R. J. Reynolds Tobacco Company
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 R. J. Reynolds Tobacco Company filed Critical R. J. Reynolds Tobacco Company
Priority to MX2021007533A priority Critical patent/MX2021007533A/es
Priority to JP2021535697A priority patent/JP2022514100A/ja
Priority to CA3124297A priority patent/CA3124297A1/fr
Priority to EP19836840.9A priority patent/EP3897230A1/fr
Publication of WO2020128971A1 publication Critical patent/WO2020128971A1/fr

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
    • A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18—Treatment of tobacco products or tobacco substitutes
    • A24B15/28—Treatment of tobacco products or tobacco substitutes by chemical substances
    • A24B15/42—Treatment of tobacco products or tobacco substitutes by chemical substances by organic and inorganic substances
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18—Treatment of tobacco products or tobacco substitutes
    • A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B13/00—Tobacco for pipes, for cigars, e.g. cigar inserts, or for cigarettes; Chewing tobacco; Snuff
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18—Treatment of tobacco products or tobacco substitutes
    • A24B15/28—Treatment of tobacco products or tobacco substitutes by chemical substances
    • A24B15/287—Treatment of tobacco products or tobacco substitutes by chemical substances by inorganic substances only
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18—Treatment of tobacco products or tobacco substitutes
    • A24B15/28—Treatment of tobacco products or tobacco substitutes by chemical substances
    • A24B15/30—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances
    • A24B15/32—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances by acyclic compounds
    • 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
    • A24B3/04—Humidifying or drying tobacco bunches or cut tobacco

Definitions

  • the present invention relates to products made or derived from tobacco, or that otherwise incorporate tobacco, and are intended for human consumption.
  • Cigarettes, cigars and pipes are popular smoking articles that employ tobacco in various forms.
  • Such smoking articles are used by heating or burning tobacco, and aerosol (e.g., smoke) is inhaled by the smoker.
  • aerosol e.g., smoke
  • tobacco also may be enjoyed in a so-called“smokeless” form.
  • smokeless tobacco products are employed by inserting some form of processed tobacco or tobacco-containing formulation into the mouth of the user.
  • smokeless tobacco product is referred to as“snuff.”
  • Representative types of moist snuff products are manufactured in Europe, particularly in Sweden, by or through companies such as Swedish Match AB, Fiedler & Lundgren AB, Gustavus AB, Skandinavisk Tobakskompagni A/S, and Rocker Production AB.
  • Smokeless tobacco products available in the U.S.A. are marketed under the tradenames CAMEL Snus, CAMEL Orbs, CAMEL Strips and CAMEL Sticks by R. J.
  • the present disclosure provides a method of processing a tobacco material to modify the color of the tobacco material, specifically to provide a tobacco material that is lightened in color (i.e.,“whitened”) ⁇
  • the whitened tobacco material can be used in smokeless tobacco materials to give materials adapted for oral use with a whitened appearance.
  • the method can include (i) extracting a tobacco material with an aqueous solution to provide a tobacco solids material and a tobacco extract; (ii) treating the tobacco solids material with a caustic wash to provide a tobacco pulp; (iii) bleaching the tobacco pulp with a solution comprising a strong base, an oxidizing agent, or a combination thereof to provide a bleached tobacco pulp; and (iv) drying the bleached tobacco pulp to provide the whitened tobacco material.
  • the bleached tobacco pulp can be dried to a moisture content of less than about 30 percent moisture on a wet basis.
  • the whitened tobacco material is characterized by an International Organization for Standardization (ISO) brightness of at least about 55%, at least about 60%, at least about 65%, or at least about 70%.
  • ISO International Organization for Standardization
  • the tobacco input material comprises lamina, stems, or a combination thereof.
  • the tobacco input material can include Rustica stems and/or Burley stems.
  • the tobacco input material comprises at least about 90% by weight roots, stalks, or a combination thereof.
  • the method can further include milling the tobacco material before the extraction step such that the milled tobacco material is able to pass through a screen of 18 or 16 U.S. sieve size.
  • the method can further include hydrolyzing the tobacco pulp with an acid prior to step (ii).
  • the acid can be sulfuric acid, hydrochloric acid, citric acid, or a combination thereof.
  • the method can further comprise dewatering the tobacco material, for example using at least one of a screw press and a basket centrifuge, following steps (i), (ii) and or step (iii).
  • the aqueous solution used to extract the tobacco material in step (i) can comprise a chelating agent.
  • the aqueous solution can include ethylenediaminetetraacetic acid (EDTA) and or diethylenetriamine pentaacetic acid (DTP A).
  • EDTA ethylenediaminetetraacetic acid
  • DTP A diethylenetriamine pentaacetic acid
  • the molar ratio of aqueous solution to the tobacco material in the extraction step (i) is from about 4:1 to about 16: 1.
  • the step of treating the tobacco solid material with a caustic wash is done at atmospheric pressure.
  • the caustic wash comprises at least one strong base.
  • the caustic wash can comprise sodium hydroxide.
  • the methods described herein can further comprise mixing the tobacco solids material with a wood pulp prior to step (ii). In certain embodiments, the methods described herein can further comprise mixing the tobacco solids material with a wood pulp after step (ii).
  • the bleaching step (iii) comprises treatment with a strong base and an oxidizing agent, and wherein the molar ratio of the amount of strong base to the amount of oxidizing agent is from about 1 : 1 to about 1 : 100, or from about 1 :5 to about 1 :50.
  • the bleaching step (iii) comprises treatment with one or more of peracetic acid, sodium hydroxide, and hydrogen peroxide.
  • the bleaching step (iii) further comprises treatment with one or more stabilizers in addition to an oxidizing agent.
  • the stabilizers can be selected from the group consisting of magnesium sulfate, sodium silicate, and combinations thereof.
  • the method further includes neutralizing the bleached pulp material to a pH in the range of about 5 to about 11 prior to step (iv).
  • the method further includes incorporating the whitened tobacco material within a smokeless tobacco product.
  • the whitened tobacco material can be milled before incorporating the tobacco material into a tobacco product to a size in the range of about 10 mm to about 0.1 mm.
  • the smokeless tobacco product can further include one or more additional components selected from the group consisting of flavorants, fillers, binders, pH adjusters, buffering agents, colorants, disintegration aids, antioxidants, humectants, and preservatives.
  • the smokeless tobacco product can include a water-permeable pouch containing the whitened tobacco material.
  • the smokeless tobacco product can further include one or more additional components selected from the group consisting of flavorants, fillers, binders, pH adjusters, buffering agents, colorants, disintegration aids, antioxidants, humectants, and preservatives.
  • the invention includes, without limitation, the following embodiments.
  • Embodiment 1 A method of preparing a whitened tobacco material for use in a smokeless tobacco product, comprising: (i) extracting a tobacco material with an aqueous solution to provide a tobacco solids material and a tobacco extract; (ii) treating the tobacco solids material with a caustic wash to provide a tobacco pulp; (iii) bleaching the tobacco pulp with a solution comprising a strong base, an oxidizing agent, or a combination thereof to provide a bleached tobacco pulp; and (iv) drying the bleached tobacco pulp to provide the whitened tobacco material.
  • Embodiment 2 The method of Embodiment 1, further comprising milling the tobacco material such that the milled tobacco material is able to pass through a screen of 18 U.S. sieve size.
  • Embodiment 3 The method of any of Embodiments 1-2, wherein the step of treating the tobacco solid material with a caustic wash is done at atmospheric pressure.
  • Embodiment 4 The method of any of Embodiments 1-3, wherein the caustic wash comprises at least one strong base.
  • Embodiment 5 The method of any of Embodiments 1-4, wherein the caustic wash comprises sodium hydroxide.
  • Embodiment 6 The method of any of Embodiments 1-5, wherein the bleached tobacco pulp is dried to a moisture content of less than about 30 percent moisture on a wet basis.
  • Embodiment 7 The method of any of Embodiments 1-6, further comprising hydrolyzing the tobacco pulp with an acid prior to step (ii).
  • Embodiment 8 The method of Embodiment 7, wherein the acid is sulfuric acid, hydrochloric acid, citric acid, or a combination thereof.
  • Embodiment 9 The method of any of Embodiments 1-8, further comprising dewatering the tobacco material using at least one of a screw press and a basket centrifuge following steps (i), (ii) and/or step (iii).
  • Embodiment 10 The method of any of Embodiments 1-9, wherein the bleaching step (iii) comprises treatment with one or more of peracetic acid, sodium hydroxide, and hydrogen peroxide.
  • Embodiment 11 The method of any of Embodiments 1-10, wherein the bleaching step (iii) further comprises treatment with one or more stabilizers in addition to an oxidizing agent.
  • Embodiment 12 The method of Embodiment 11, wherein the stabilizers are selected from the group consisting of magnesium sulfate, sodium silicate, and combinations thereof.
  • Embodiment 13 The method of any of Embodiments 1-12, wherein the bleaching step (iii) comprises treatment with a strong base and an oxidizing agent, and wherein the molar ratio of the amount of strong base to the amount of oxidizing agent is from about 1 : 1 to about 1 : 100.
  • Embodiment 14 The method of any of Embodiments 1-13, wherein the molar ratio of the amount of strong base to the amount of oxidizing agent is from about 1:5 to about 1:50.
  • Embodiment 15 The method of any of Embodiments 1-14, further comprising neutralizing the bleached pulp material to a pH in the range of about 5 to about 11 prior to step (iv).
  • Embodiment 16 The method of any of Embodiments 1-15, further comprising milling the whitened tobacco material following step (iv) to a size in the range of approximately 5 mm to about 0.1 mm.
  • Embodiment 17 The method of any of Embodiments 1-16, wherein the aqueous solution used to extract the tobacco material in step (i) comprises a chelating agent.
  • Embodiment 18 The method of Embodiment 17, wherein the chelating agent comprises one or more of EDTA and DTPA.
  • Embodiment 19 The method of any of Embodiments 1-18, wherein the molar ratio of aqueous solution to the tobacco material in the extraction step (i) is from about 4: 1 to about 16: 1.
  • Embodiment 20 The method of any of Embodiments 1-19, wherein the tobacco material comprises lamina, stems, or a combination thereof.
  • Embodiment 21 The method of any of Embodiments 1-20, wherein the tobacco material comprises Rustica stems.
  • Embodiment 22 The method of any of Embodiments 1-21, wherein the tobacco material comprises at least about 90% by weight roots, stalks, or a combination thereof.
  • Embodiment 23 The method of any of Embodiments 1-22, further comprising mixing the tobacco solids material with a wood pulp prior to step (ii).
  • Embodiment 24 The method of any of Embodiments 1-23, wherein the whitened tobacco material is characterized by an International Organization for Standardization (ISO) brightness of at least about 60%.
  • ISO International Organization for Standardization
  • Embodiment 25 The method of any of Embodiments 1-24, further comprising incorporating the whitened tobacco material within a smokeless tobacco product.
  • Embodiment 26 The method of Embodiments 25, wherein the smokeless tobacco product further comprises one or more additional components selected from the group consisting of flavorants, fillers, binders, pH adjusters, buffering agents, colorants, disintegration aids, antioxidants, humectants, and preservatives.
  • additional components selected from the group consisting of flavorants, fillers, binders, pH adjusters, buffering agents, colorants, disintegration aids, antioxidants, humectants, and preservatives.
  • Embodiment 27 A smokeless tobacco product incorporating the whitened tobacco material prepared according to the method of any of Embodiments 1-26.
  • Embodiment 28 The smokeless tobacco product of Embodiment 27, comprising a water-permeable pouch containing the whitened tobacco material.
  • Embodiment 29 The smokeless tobacco product of any of Embodiments 26-27, further comprising one or more additional components selected from the group consisting of flavorants, fillers, binders, pH adjusters, buffering agents, colorants, disintegration aids, antioxidants, humectants, and preservatives.
  • additional components selected from the group consisting of flavorants, fillers, binders, pH adjusters, buffering agents, colorants, disintegration aids, antioxidants, humectants, and preservatives.
  • FIG. 1 is a front perspective view illustrating a pouched product according to an embodiment
  • Figure 2 is a flow chart illustrating the general steps for preparing a whitened tobacco material according to an embodiment.
  • the tobacco product 10 includes a moisture-permeable container in the form of a pouch 20, which contains a solid tobacco filler material 15 comprising a whitened tobacco material of a type described herein.
  • the smokeless tobacco product also may optionally comprise, in certain embodiments, a plurality of microcapsules dispersed within the tobacco filler material 15, the microcapsules containing a component (e.g., a flavorant) such as described in greater detail below.
  • a component e.g., a flavorant
  • the tobacco product 10 is typically used by placing one pouch containing the tobacco formulation in the mouth of a human subject/user.
  • saliva in the mouth of the user causes some of the components of the tobacco formulation to pass through the water-permeable pouch and into the mouth of the user.
  • the pouch preferably is not chewed or swallowed.
  • the user is provided with tobacco flavor and satisfaction, and is not required to spit out any portion of the tobacco formulation.
  • substantial amounts of the tobacco formulation and the contents of the optional microcapsules and have been ingested by the human subject and the pouch may be removed from the mouth of the human subject for disposal.
  • the pouch materials can be designed and manufactured such that under conditions of normal use, a significant amount of the tobacco formulation contents permeate through the pouch material prior to the time that the pouch undergoes loss of its physical integrity.
  • the present disclosure provides a whitened tobacco composition, smokeless tobacco products incorporating such whitened tobacco compositions, and methods for preparing a whitened tobacco composition and for incorporating such compositions within smokeless tobacco products.
  • the term“whitened” refers to a composition comprising a tobacco material that has been treated to remove some degree of color therefrom.
  • a“whitened” tobacco material that is treated according to the methods described herein is visually lighter in hue than an untreated tobacco material.
  • the whitened tobacco composition of the invention can be used as a component of a smokeless tobacco composition, such as loose moist snuff, loose dry snuff, chewing tobacco, pelletized tobacco pieces, extruded or formed tobacco strips, pieces, rods, or sticks, finely divided ground powders, finely divided or milled agglomerates of powdered pieces and components, flake-like pieces, molded processed tobacco pieces, pieces of tobacco-containing gum, rolls of tape-like films, readily water-dissolvable or water-dispersible films or strips, or capsule-like materials.
  • a smokeless tobacco composition such as loose moist snuff, loose dry snuff, chewing tobacco, pelletized tobacco pieces, extruded or formed tobacco strips, pieces, rods, or sticks, finely divided ground powders, finely divided or milled agglomerates of powdered pieces and components, flake-like pieces, molded processed tobacco pieces, pieces of tobacco-containing gum, rolls of tape-like films, readily water-dissolv
  • tobaccos that can be employed include flue-cured or Virginia (e.g., K326), burley, sun-cured (e.g., Indian Kumool and Oriental tobaccos, including Katerini, Prelip, Komotini, Xanthi and Yambol tobaccos), Maryland, dark, dark-fired, dark air cured (e.g., Passanda, Cubano, Jatin and Bezuki tobaccos), light air cured (e.g., North Wisconsin and Galpao tobaccos), Indian air cured, Red Russian and Rustica tobaccos, as well as various other rare or specialty tobaccos and various blends of any of the foregoing tobaccos.
  • flue-cured or Virginia e.g., K326)
  • burley sun-cured
  • Indian Kumool and Oriental tobaccos including Katerini, Prelip, Komotini, Xanthi and Yambol tobaccos
  • Maryland dark, dark-fired
  • dark air cured e.g., Passanda, Cubano, Ja
  • Nicotiana species include N. tabacum, N. rustica, N. alata, N. arentsii, N. excelsior, N. forgetiana, N. glauca, N. glutinosa, N. gossei, N.
  • N. clevelandii N. cordifolia, N. corymbosa, N. fragrans, N. goodspeedii, N. linearis, N. miersii, N. nudicaulis, N. obtusifolia, N. occidentalis subsp. Hersperis, N. pauciflora, N. petunioides, N. quadrivalvis,
  • N. repanda N. rotundifolia, N. solanifolia, and N. spegazzinii.
  • Nicotiana species can be derived using genetic -modification or crossbreeding techniques (e.g., tobacco plants can be genetically engineered or crossbred to increase or decrease production of components, characteristics or attributes). See, for example, the types of genetic modifications of plants set forth in US Pat. Nos. 5,539,093 to Fitzmaurice et al.; 5,668,295 to Wahab et al.; 5,705,624 to Fitzmaurice et al.;
  • the tobacco materials are those that have been appropriately cured and aged.
  • Especially preferred techniques and conditions for curing flue-cured tobacco are set forth in Nestor et al., Beitrage Tabakforsch. hit., 20 (2003) 467-475 and US Pat. No. 6,895,974 to Peele, which are incorporated herein by reference.
  • Representative techniques and conditions for air curing tobacco are set forth in Roton et al., Beitrage Tabakforsch. Ink, 21 (2005) 305-320 and Staaf et al., Beitrage Tabakforsch. Int, 21 (2005) 321-330, which are incorporated herein by reference. Certain types of unusual or rare tobaccos can be sun cured.
  • the Nicotiana species can be selected for the content of various compounds that are present therein. For example, plants can be selected on the basis that those plants produce relatively high quantities of one or more of the compounds desired to be isolated therefrom. In certain embodiments, plants of the Nicotiana species (e.g., Galpao commun tobacco) are specifically grown for their abundance of leaf surface compounds. Tobacco plants can be grown in greenhouses, growth chambers, or outdoors in fields, or grown hydroponically.
  • Nicotiana species e.g., Galpao commun tobacco
  • the plant of the Nicotiana species can be employed. For example, virtually all of the plant (e.g. , the whole plant) can be harvested, and employed as such. Alternatively, various parts or pieces of the plant can be harvested or separated for further use after harvest. For example, the flower, leaves, stem, stalk, roots, seeds, and various combinations thereof, can be isolated for further use or treatment.
  • the tobacco material subjected to the treatments set forth herein is Rustica stems in milled form.
  • the post-harvest processing of the plant or portion thereof can vary. After harvest, the plant, or portion thereof, can be used in a green form (e.g. , the plant or portion thereof can be used without being subjected to any curing process). For example, the plant or portion thereof can be used without being subjected to significant storage, handling or processing conditions. In certain situations, it is advantageous for the plant or portion thereof be used virtually immediately after harvest.
  • a plant or portion thereof in green form can be refrigerated or frozen for later use, freeze dried, subjected to irradiation, yellowed, dried, cured (e.g., using air drying techniques or techniques that employ application of heat), heated or cooked (e.g., roasted, fried or boiled), or otherwise subjected to storage or treatment for later use.
  • the harvested plant or portion thereof can be physically processed.
  • the plant or portion thereof can be separated into individual parts or pieces (e.g., the leaves can be removed from the stems, and/or the stems and leaves can be removed from the stalk).
  • the harvested plant or individual parts or pieces can be further subdivided into parts or pieces (e.g., the leaves can be shredded, cut, comminuted, pulverized, milled or ground into pieces or parts that can be characterized as filler-type pieces, granules, particulates or fine powders).
  • the plant, or parts thereof can be subjected to external forces or pressure (e.g., by being pressed or subjected to roll treatment).
  • the plant or portion thereof can have a moisture content that approximates its natural moisture content (e.g., its moisture content immediately upon harvest), a moisture content achieved by adding moisture to the plant or portion thereof, or a moisture content that results from the drying of the plant or portion thereof.
  • a moisture content that approximates its natural moisture content e.g., its moisture content immediately upon harvest
  • a moisture content achieved by adding moisture to the plant or portion thereof e.g., a moisture content achieved by adding moisture to the plant or portion thereof
  • a moisture content that results from the drying of the plant or portion thereof e.g., powdered, pulverized, ground or milled pieces of plants or portions thereof can have moisture contents of less than about 25 weight percent, often less than about 20 weight percent, and frequently less than about 15 weight percent.
  • Tobacco compositions intended to be used in a smokeless form such as that in Figure 1 may incorporate a single type of tobacco (e.g., in a so-called“straight grade” form).
  • the tobacco within a tobacco composition may be composed solely of flue-cured tobacco (e.g., all of the tobacco may be composed, or derived from, either flue-cured tobacco lamina or a mixture of flue-cured tobacco lamina and flue-cured tobacco stem).
  • the tobacco comprises or is composed solely of sun-cured milled Rustica stems (i.e., N. rustica stems).
  • the tobacco within a tobacco composition also may have a so- called“blended” form.
  • the tobacco within a tobacco composition of the present invention may include a mixture of parts or pieces of flue-cured, burley (e.g., Malawi burley tobacco) and Oriental tobaccos (e.g., as tobacco composed of, or derived from, tobacco lamina, or a mixture of tobacco lamina and tobacco stem).
  • burley e.g., Malawi burley tobacco
  • Oriental tobaccos e.g., as tobacco composed of, or derived from, tobacco lamina, or a mixture of tobacco lamina and tobacco stem.
  • Portions of the tobaccos within the tobacco product may have processed forms, such as processed tobacco stems (e.g., cut-rolled stems, cut-rolled-expanded stems or cut-puffed stems), or volume expanded tobacco (e.g., puffed tobacco, such as dry ice expanded tobacco (DIET)).
  • processed tobacco stems e.g., cut-rolled stems, cut-rolled-expanded stems or cut-puffed stems
  • volume expanded tobacco e.g., puffed tobacco, such as dry ice expanded tobacco (DIET)
  • DIET dry ice expanded tobacco
  • the tobacco product optionally may incorporate tobacco that has been fermented.
  • the starting tobacco material can include tobacco stems.
  • stem refers to the long thing part of a tobacco plant from which leaves or flowers grow, and can include the leaves, lamina, and/or flowers.
  • stalks and/or roots can be separated into individual pieces (e.g., roots separated from stalks, and/or root parts separated from each other, such as big root, mid root, and small root parts) or the stalks and roots may be combined.
  • “stalk” is meant the stalk that is left after the leaf (including stem and lamina) has been removed.“Root” and various specific root parts useful according to the present invention may be defined and classified as described, for example, in Mauseth, Botany: An Introduction to Plant Biology: Fourth Edition, Jones and Bartlett Publishers (2009) and Glimn-Lacy et al., Botany Illustrated, Second Edition, Springer (2006), which are incorporated herein by reference.
  • the harvested stalks and/or roots are typically cleaned, ground, and dried to produce a material that can be described as particulate (i.e., shredded, pulverized, ground, granulated, or powdered).
  • stalks and/or roots can also refer to stalks and/or roots that have undergone an extraction process to remove water soluble materials.
  • the cellulosic material (i.e., pulp) remaining after stalks and/or root materials undergo an extraction process can also be useful in the present invention.
  • the tobacco material may comprise material from any part of a plant of the Nicotiana species
  • the majority of the material can comprise material obtained from the stems, stalks and or roots of the plant.
  • the tobacco material comprises at least about 90%, at least about 92%, at least about 95%, or at least about 97% by dry weight of at least one of the stem material, the stalk material and the root material of a harvested plant of the Nicotiana species.
  • the tobacco material used in the present invention is typically provided in a shredded, ground, granulated, fine particulate, or powder form.
  • the tobacco whitening process described herein can include optionally milling a tobacco material.
  • the tobacco is employed in the form of parts or pieces that have an average particle size less than that of the parts or pieces of shredded tobacco used in so-called“fine cut” tobacco products.
  • the very finely divided tobacco particles or pieces are sized to pass through a screen of about 18 or 16 U.S. sieve size, generally are sized to pass a screen of about 20 U.S. sieve size, often are sized to pass through a screen of about 50 U.S.
  • sieve size frequently are sized to pass through a screen of about 60 U.S. sieve size, may even be sized to pass through a screen of 100 U.S. sieve size, and further may be sized so as to pass through a screen of 200 U.S. sieve size.
  • U.S. Sieve Series two scales commonly used to classify particle sizes are the U.S. Sieve Series and Tyler Equivalent. Sometimes these two scales are referred to as Tyler Mesh Size or Tyler Standard Sieve Series.
  • U.S. sieve size is referred to in the present application.
  • air classification equipment may be used to ensure that small sized tobacco particles of the desired sizes, or range of sizes, may be collected.
  • the tobacco material is in particulate form sized to pass through an 18 or 16 U.S.
  • the tobacco is provided with an average particle size of about 0.2 to about 2 mm, about 0.5 to about 1.5 mm, about 0.2 to about 1.0 mm, or about 0.75 to about 1.25 mm (e.g., about 1 mm).
  • the manner by which the tobacco is provided in a finely divided or powder type of form may vary.
  • tobacco parts or pieces are comminuted, ground or pulverized into a powder type of form using equipment and techniques for grinding, milling, or the like.
  • the tobacco is relatively dry in form during grinding or milling, using equipment such as hammer mills, cutter heads, air control mills, or the like.
  • tobacco parts or pieces may be ground or milled when the moisture content thereof is less than about 15 weight percent to less than about 5 weight percent.
  • the tobacco material can be processed to provide it in the desired form before and/or after being subjected to the whitening and/or clarification processes described herein.
  • the type of tobacco material that is treated i.e., subjected to the processes described herein is selected such that it is initially visually lighter in color than other tobacco materials to some degree.
  • one optional step of the method described herein comprises screening various tobacco materials and selecting one or more of the tobacco materials based on their visual appearance (i.e., their“lightness,” or“whiteness”).
  • this screening step can, in some embodiments, comprise a visual screening wherein certain tobacco materials (e.g., certain tobacco types) are selected that are visually lighter in hue than other tobacco materials.
  • the screening can be conducted by means of an automated operation that selects certain tobacco materials based on predetermined characteristics (e.g., having a lightness above a given threshold value).
  • optical instruments e.g., spectrophotometer/spectroreflectometer
  • optical sorting equipment can be used for this purpose.
  • Such equipment is available, for example, from Autoelrepho® Products, A Z Technology, Hunter Lab, X- Rite, SpecMetrix, and others.
  • the tobacco material can be treated to extract a soluble component of the tobacco material therefrom.
  • this first treatment step can comprise a solvent extraction at operation 105 comprising contacting the tobacco material with a solvent (e.g., water) for a time and at a temperature sufficient to cause the extraction of one or more components of the tobacco material into the solvent, and separating the extract from the residual tobacco solid material.
  • a solvent e.g., water
  • “Tobacco solid material” as used herein is the solid, residual tobacco material that remains after the liquid component (i.e., tobacco extract) is removed from the material in step 105.
  • tobacco extract refers to the isolated components of a tobacco material that are extracted from solid tobacco pulp by a solvent that is brought into contact with the tobacco material in an extraction process in step 105.
  • the solvent is added to the tobacco material and the material is soaked for a given period of time (e.g., about 1 h); the pulp is then filtered to give a tobacco solid material and the solvent and any solubles contained therein are filtered off to give a tobacco extract.
  • the solvent used for extraction of the tobacco material can vary.
  • the solvent comprises a solvent having an aqueous character, such as distilled water and/or tap water.
  • the solvent can have one or more additives and may contain, for example, organic and or inorganic acids, bases, or salts, pH buffers, surfactants, or combinations thereof and may comprise minor amounts of one or more organic solvents (e.g., various alcohols, polyols, and or humectants).
  • the solvent comprises sodium hydroxide (NaOH) (e.g., as a 5% NaOH solution in water).
  • the solvent can comprise an organic solvent, such as an alcohol (e.g., ethanol, isopropanol, etc.), which can be used alone or in combination with an aqueous solvent.
  • the extraction comprises adding a large excess of one or more solvents to the tobacco material so as to produce a slurry (comprising, for example, 50-90% by weight of the solvent), although the amount of solvent can vary.
  • the solvent can be at room temperature or at an elevated temperature.
  • the solvent can be heated at a temperature of between about room temperature and about 120 °C, preferably about room temperature and about 110 °C (e.g., about 100 °C, about 80 °C, about 60 °C, about 40 °C, or about 20 °C).
  • the particulate or powder tobacco material can be combined with water to form a moist aqueous material (e.g., in the form of a suspension or slurry) and the resulting material is typically heated to effectuate extraction of various compounds.
  • the water used to form the moist material can be pure water (e.g., tap water or deionized water) or a mixture of water with suitable co-solvents such as certain alcohols.
  • the amount of water added to form the moist material can be at least about 50 weight percent, or at least about 60 weight percent, or at least about 70 weight percent, based on the total weight of the moist material. In some cases, the amount of water can be described as at least about 80 weight percent or at least about 90 weight percent.
  • the tobacco material can be extracted with water and at least one chelating agent which is capable of removing transition metals from the tobacco material.
  • Chelating agents are useful to remove certain metals from the tobacco material that could cause yellowing, and thus interfere with the whitening process.
  • the tobacco material can be extracted with an aqueous solution comprising ethylenediaminetetraacetic acid (EDTA).
  • EDTA ethylenediaminetetraacetic acid
  • the chelating agent can comprise diethylenetriamine pentaacetic acid (DTP A).
  • the chelating agent(s) can be present in an amount of about 0.01 to about 1.0 dry weight percent, about 0.05 to about 0.5 dry weight percent, or about 0.1 to about 0.2 dry weight percent, based on the total dry weight of the tobacco material.
  • the amount of time for which the tobacco material remains in contact with the solvent can vary.
  • the tobacco material is in contact with the solvent for about thirty minutes to about six hours (e.g., about 1 hour, about 2 hours, about 3 hours, about 4 hours, about 5 hours, or about 6 hours), although shorter and longer time periods can be used.
  • the amount of time can depend, for example, on the temperature of the solvent. For example, less time may be required to extract the tobacco material using solvent at a higher temperature than that required to extract the tobacco material with room temperature or cold solvent.
  • the extraction process provides a tobacco solid material and a tobacco extract.
  • the number of extraction steps can vary.
  • the tobacco pulp is extracted one or more times, two or more times, three or more times, four or more times, or five or more times.
  • the solvent used for each extraction can vary.
  • one or more extractions are conducted using hot water; and in a final extraction, the extraction is conducted using a basic solution (e.g., a 5% NaOH solution).
  • a basic solution e.g., a 5% NaOH solution
  • the tobacco solid material is filtered and the solvent and solubles are removed from the tobacco solid material.
  • the extracts obtained from each extraction can be combined and clarified, as described in U.S. Pat. No.
  • the tobacco pulp is generally isolated from the tobacco extract, for example, by filtration or centrifugation, although these methods are not intended to be limiting.
  • the tobacco pulp can be isolated from the extract by means of distillation (e.g., steam distillation) of the tobacco mixture (e.g., the tobacco slurry).
  • the process of filtration can comprise passing the liquid through one or more filter screens to remove selected sizes of particulate matter. Screens may be, for example, stationary, vibrating, rotary, or any combination thereof. Filters may be, for example, press filters or pressure fdters.
  • the filtration method used can involve microfiltration, ultrafiltration, and/or nanofiltration.
  • a filter aid can be employed to provide effective filtration and can comprise any material typically used for this purpose.
  • some common filter aids include cellulose fibers, perlite, bentonite, diatomaceous earth, and other silaceous materials.
  • alternative methods can also be used, for example, centrifugation or settling/sedimentation of the components and siphoning off of the liquid. See, for example, the processes and products described in U.S. Pat. App. Pub. Nos. 2012/0152265 to Dube et al. and 2012/0192880 to Dube et al., herein incorporated by reference in their entireties.
  • the extracted solid components can be used as the starting tobacco material in various embodiments of the whitening process described herein.
  • the tobacco material can be hydrolyzed with at least one acid, as illustrated at operation 110 of Fig. 2, for example.
  • Steam- or water-based pre-hydrolysis of the tobacco material prior to pulping, for example, can reduce the amount of chemicals necessary in a bleaching operation. Any form of hydrolysis known in the art can be used.
  • a salt of a weak acid or a weak base (or both) can be dissolved in water in a hydrolysis process.
  • tobacco materials can undergo enzymatic hydrolysis.
  • the tobacco material can be hydrolyzed with sulfuric acid, hydrochloric acid, or any other mineral or organic acid.
  • Pulps can be produced from raw materials either mechanically or chemically.
  • refiner mechanical pulping techniques can be used to produce tobacco pulp.
  • raw tobacco materials can be chipped, and then fed between refiners where the chips are made into fibers between revolving metal disks, for example. See, e.g., the mechanical pulping equipment and processes disclosed in U.S. Pat. Nos. 4,421,595 to Huusari and 7,237,733 to Vikman, WO 2010/023363, CA 1074606, and CN 201268810, all of which are herein incorporated by reference in their entireties.
  • raw tobacco material can be pretreated (i.e., extracted) with water for several hours before undergoing the pulping process.
  • the weight ratio of water to tobacco material can be approximately 10: 1 to about 4: 1.
  • Pretreating the tobacco material e.g., stalk and or root materials
  • the pretreated mixture can then be drained to about a 20% consistency.
  • the term“consistency” is defined as the percentage of solids in a mixture.
  • This pretreated tobacco material can then be refined at atmospheric pressure with a plurality of passes through a machine that can chip the stalk. See, for example, the machines discussed in U.S. Pat. Nos. 3,661,192 to Nicholson et al.; 3,861,602 to Smith et al; 4,135,563 to Maucher; and 5,005,620 to Morey, each of which is incorporated by reference herein.
  • a chemical pulping process can be used to pulp and delignify the tobacco biomass at operation 115.
  • a chemical pulping process separates lignin from cellulose fibers by dissolving lignin in a cooking liquor such that the lignin, which binds the cellulose fibers together, can be washed away from the cellulose fibers without seriously degrading the cellulose fibers.
  • Soda pulping involves cooking raw material chips in a sodium hydroxide cooking liquor.
  • the kraft process evolved from soda pulping and involves cooking raw material chips in a solution of sodium hydroxide and sodium sulfide.
  • the acidic sulfite process involves using sulfurous acid and bisulfate ion in the cook.
  • the kraft process is the most commonly used method for chemical wood pulping; however, the soda process can also be used to produce some hardwood pulps. Any chemical pulping process, including, but not limited to the three examples listed above, can be used to produce a tobacco pulp from raw tobacco materials.
  • a cooking liquor can comprise a strong base.
  • a strong base refers to a basic chemical compound (or combination of such compounds) that is able to deprotonate very weak acids in an acid-base reaction.
  • strong bases that can be useful in the present invention include, but are not limited to one or more of sodium hydroxide, potassium hydroxide, sodium carbonate, sodium bicarbonate, potassium carbonate, potassium bicarbonate, ammonium hydroxide, ammonium bicarbonate, and ammonium carbonate.
  • the weight of the strong base can be greater than about 5%, greater than about 25%, or greater than about 40% of the weight of the tobacco input.
  • the weight of the strong base can be less than about 60% or less than about 50% of the weight of the tobacco input. In still further embodiments, the weight of the strong base can be from about 5% to about 50%, or from about 30% to about 40% of the weight of the tobacco input. Various other chemicals and weight ratios thereof can also be employed to chemically pulp the tobacco input in other embodiments.
  • chemically pulping a tobacco input can include heating the tobacco input and the strong base. Heating the tobacco input and the strong base can be conducted to increase the efficacy of the chemical pulping. In this regard, an increase in either cooking temperature or time will result in an increased reaction rate (rate of lignin removal).
  • the method of producing a tobacco-derived pulp can include one or more additional operations. See, e.g., U.S. Patent Appl. Pub. No. 2013/0276801 to Byrd Jr. et al., herein incorporated by reference in its entirety.
  • the tobacco input can undergo further processing steps prior to pulping and/or the delignification method can include additional treatment steps (e.g., drying the tobacco input, or depithing the tobacco input).
  • these additional steps can be conducted to remove pith (which comprises lignin) from the tobacco input and/or tobacco pulp manually, and thus reduce the amount of chemicals necessary to delignify the tobacco input during a chemical pulping process, for example.
  • Mixing water with the tobacco pulp to form a slurry and filtering the slurry can be conducted, for example, to remove certain materials, such as pith, parenchyma, and tissue from the tobacco pulp.
  • Anthraquinone can be employed in a chemical pulping method in an attempt to provide a higher yield by protecting carbohydrates from the strong base during delignification, for example.
  • Other processing steps known in the pulping and delignification field can be employed in forming tobacco pulp from the raw tobacco input.
  • a wood pulp is added to the solid tobacco materials and/or the tobacco pulp during the overall bleaching processes described herein. It is noted that wood pulp can be introduced into the bleaching process at any of the steps described herein.
  • the methods described herein can further comprise mixing the tobacco solids material with a wood material prior to pulping such that the wood material is also pulped.
  • the methods described herein can further comprise mixing the tobacco pulp with a wood pulp after the pulping process.
  • the wood pulp is a bleached pulp material and can be added after the solid tobacco materials have been pulped and bleached. If unbleached wood pulp is used, an additional caustic extraction step may be required, or the wood pulp can need to be added to the tobacco pulp before the step of bleaching.
  • the wood pulp can be market available wood pulp. In certain embodiments, the wood pulp can be market available wood pulp.
  • the wood pulp can be a bleached hardwood pulp.
  • the wood pulp added to the processes described herein can be added in an amount of about 1 to about 20 wt. %, or about 5 to about 15 wt. %, based on the total weight of the pulp used (i.e., the total weight of tobacco pulp and wood pulp used).
  • the wood pulp can be added in an amount of at least about 1 wt. %, at least about 5 wt. %, or at least about 10 wt. %, based on the total weight of the pulp used.
  • the wood pulp can be added in an amount of no more than about 5 wt. %, no more than about 10 wt. %, no more than about 15 wt. %, or no more than about 20 wt. %, based on the total weight of the pulp used.
  • Tobacco pulp that has been provided and isolated following the extraction and pulping steps can be whitened in certain embodiments according to any means known in the art, as shown in step 120 of Figure 2. It is noted that in certain embodiments, a combination of tobacco pulp and wood pulp may undergo a whitening step or any other process step described herein; however, for convenience, the following description refers only to tobacco pulp.
  • whitening methods using various bleaching or oxidizing agents and oxidation catalysts can be used.
  • Example oxidizing agents include peroxides (e.g., hydrogen peroxide), chlorite salts, chlorate salts, perchlorate salts, hypochlorite salts, ozone, ammonia, and combinations thereof.
  • Example oxidation catalysts are titanium dioxide, manganese dioxide, and combinations thereof. Processes for treating tobacco with bleaching agents are discussed, for example, in US Patent Nos. 787,611 to Daniels, Jr.; 1,086,306 to Oelenheinz; 1,437,095 to Delling; 1,757,477 to Rosenroch; 2,122,421 to Hawkinson; 2,148,147 to Baier; 2,170,107 to Baier; 2,274,649 to Baier; 2,770,239 to Prats et ak; 3,612,065 to Rosen; 3,851,653 to Rosen; 3,889,689 to Rosen; 3,943,945 to Rosen; 4,143,666 to Rainer; 4,194,514 to Campbell; 4,366,823, 4,366,824, and 4,388,933 to Rainer et ak; 4,641,667 to Schmekel et ak; and 5,713,376 to Berger; and PCT WO 96/31255 to Giolvas, all of
  • tobacco pulp is whitened using a caustic reagent and/or an oxidizing agent.
  • the tobacco pulp is whitened using both a caustic reagent and an oxidizing agent.
  • the caustic reagent and oxidizing agent can be provided separately or can be combined.
  • the caustic reagent can vary and can be, for example, any strong base, including but not limited to, an alkaline metal hydroxide, alkaline earth metal hydroxide, or mixture thereof.
  • the caustic reagent is sodium hydroxide or potassium hydroxide.
  • Alternative reagents that can be used include, but are not limited to, ammonium hydroxide, sodium carbonate, potassium carbonate, ammonia gas, and mixtures thereof.
  • the caustic reagent is generally provided in solution form (e.g., in aqueous solution) and the concentration of the caustic reagent in the solution can vary. Also, the amount of caustic reagent used in the methods of the present invention can vary.
  • the caustic reagent is provided in an amount of between about 1% and about 50% dry weight basis (e.g., between about 1% and about 40% or between about 1% and about 30%) by weight of the (dry) tobacco pulp.
  • the caustic reagent can be provided in an amount of about 2%, about 5%, about 7%, about 10%, or about 25% by weight of the (dry) tobacco pulp. It is noted that the quantity of caustic reagent required may, in certain embodiments, vary as a result of the strength of the caustic reagent.
  • more caustic reagent may, in some embodiments, be required where the caustic reagent is a weaker base, whereas less caustic reagent may, in some embodiments, be required where the caustic reagent is a strong base.
  • the oxidizing agent i.e., oxidant or oxidizer
  • oxidant or oxidizer can be any substance that readily transfers oxygen atoms and/or gains electrons in a reduction/oxidation (redox) chemical reaction.
  • Peroxides e.g., hydrogen peroxide, peracetic acid
  • any oxidizing reagent including, but not limited to; other oxides (including nitrous oxide, silver oxide, chromium trioxide, chromate, dichromate, pyridinium chlorochromate; and osmium tetroxide); oxygen ((3 ⁇ 4); ozone (O3) ; fluorine (F 2 ); chlorine (Cl 2 ); and other halogens; hypochlorite, chlorite, chlorate, perchlorite, and other halogen analogues thereof; nitric acid; nitrate compounds; sulfuric acid; persulfuric acids; hydroxyl radicals; manganate and permanganate compounds (e.
  • the oxidizing reagent used according to the invention is chlorine-free. In certain embodiments, the oxidizing reagent is provided in aqueous solution form.
  • the amount of oxidizing agent used in the methods of the present invention can vary. For example, in certain embodiments, the oxidizing agent is provided in a weight amount of about one to fifty times the weight of the (dry) tobacco pulp. For example, in some embodiments, the oxidizing agent is provided in a weight amount about equal to the weight of the (dry) tobacco pulp, about 1.3 times the weight of the (dry) tobacco pulp, about 1.5 times the weight of the (dry) tobacco pulp, about 2 times the weight of the (dry) tobacco pulp, or about 5 times the weight of the (dry) tobacco pulp.
  • the bleaching process can further include treatment with one or more stabilizers in addition to an oxidizing agent.
  • the stabilizer can be selected from the group consisting of magnesium sulfate, sodium silicate, and combinations thereof.
  • the stabilizer(s) can be present in an amount of about 0.01 to about 3.0 dry weight percent, about 0.1 to about 2.5 dry weight percent, or about 0.5 to about 2.0 dry weight percent, based on the total dry weight of the tobacco material pulp.
  • the tobacco pulp is brought into contact with the caustic reagent and/or oxidizing agent for a period of time.
  • the tobacco material can be brought into contact with the caustic reagent and oxidizing reagent simultaneously, or can be brought into contact with the caustic reagent and oxidizing reagent separately.
  • the oxidizing reagent is added to the tobacco material and then the caustic reagent is added to the tobacco material such that, after addition, both reagents are in contact with the tobacco material simultaneously.
  • the caustic reagent is added to the tobacco material and then the oxidizing reagent is added to the tobacco material such that, after addition, both reagents are in contact with the tobacco material simultaneously.
  • the molar ratio of the caustic reagent to oxidizing agent can vary.
  • the molar ratio of NaOH to hydrogen peroxide is from about 1: 1 to about 1:100, preferably from about 1:5 to about 1:50, and more preferably from about 1 : 10 to about 1:25.
  • the molar ratio of NaOH to hydrogen peroxide is between about 1:20 and about 1:25.
  • the time for which the tobacco material is contacted with the caustic reagent and/or oxidizing agent can vary.
  • the time for which the tobacco material is contacted with the caustic reagent and/or oxidizing agent is that amount of time sufficient to provide a tobacco pulp material with a lightened color as compared to the untreated tobacco material.
  • the tobacco material is contacted with the caustic reagent and or oxidizing agent overnight.
  • the time period is a period of at least about 10 minutes, typically at least about 20 minutes, more often at least about 30 minutes.
  • the time period is a period of no more than about 10 hours, no more than about 8 hours, no more than about 6 hours, no more than about 4 hours, no more than about 2 hours, or no more than about 1 hour.
  • the tobacco material can be heated during treatment with the caustic reagent and/or oxidizing agent. Generally, heating the tobacco material accelerates the whitening process. Where the tobacco material is heated during treatment, sufficient color lightening is typically achieved in less time than in embodiments wherein the tobacco material is unheated during treatment.
  • the temperature and time of the heat treatment process will vary, and generally, the length of the heat treatment will decrease as the temperature of the heat treatment increases.
  • the mixture of tobacco material, caustic reagent, and/or oxidizing agent can be heated at a temperature of between room temperature and about 100 °C (e.g., about 90 °C or about 80 °C). Preferably, the mixture is heated between room temperature and about 75 °C.
  • the heating can be accomplished using any heating method or apparatus known in the art.
  • the heating can be carried out in an enclosed vessel (e.g., one providing for a controlled atmospheric environment, controlled atmospheric components, and a controlled atmospheric pressure), or in a vessel that is essentially open to ambient air.
  • the temperature can be controlled by using a jacketed vessel, direct steam injection into the tobacco, bubbling hot air through the tobacco, and the like.
  • the heating is performed in a vessel also capable of providing mixing of the composition, such as by stirring or agitation.
  • Example mixing vessels include mixers available from Scott Equipment Company, Littleford Day, Inc., Lodige Process Technology, and the Breddo Likwifier Division of American Ingredients Company.
  • vessels which provide a pressure controlled environment include high pressure autoclaves available from Berghof/ America Inc. of Concord, California, and high pressure reactors available from The Parr Instrument Co. (e.g., Parr Reactor Model Nos. 4522 and 4552 described in US Patent No. 4,882,128 to Hukvari et al.).
  • the pressure within the mixing vessel during the process can be atmospheric pressure or elevated pressure (e.g., about 10 psig to about 1,000 psig).
  • the heating process is conducted in a microwave oven, a convection oven, or by infrared heating.
  • Atmospheric air, or ambient atmosphere is the preferred atmosphere for carrying out the optional heating step of the present invention.
  • heating can also take place under a controlled atmosphere, such as a generally inert atmosphere. Gases such as nitrogen, argon and carbon dioxide can be used.
  • a hydrocarbon gas e.g., methane, ethane or butane
  • a fluorocarbon gas also can provide at least a portion of a controlled atmosphere in certain embodiments, depending on the choice of treatment conditions and desired reaction products.
  • the bleached tobacco pulp before drying the bleached tobacco pulp, can be treated with an acid to neutralize the tobacco pulp after the bleaching process to a pH in the range of about 5 to about 11 (as illustrated at operation 125 of Fig. 2, for example), such as about 6 to about 10.
  • the bleached tobacco pulp can be treated with sulfuric acid, hydrochloric acid, citric acid, or any combination thereof. Other acids known in the art can also be used to neutralize the bleached tobacco pulp.
  • the pH of the bleached tobacco pulp can be approximately 7.
  • the treated tobacco pulp is generally filtered (i.e., isolated from the caustic reagent and/or oxidizing reagent) and dried (as illustrated at operation 130 of Fig. 2, for example) to give a whitened tobacco pulp material.
  • the tobacco pulp can be dried to a moisture level of about 1-30%, about 5-20%, or about 10-15% moisture on a wet basis.
  • the whitened tobacco material can optionally be milled a size in the range of approximately about 5 mm to about 0.1 mm, or about 1 mm to about 0.1 mm. In certain embodiments, the whitened tobacco material can be milled to a size of less than about 10 mm, less than about 5 mm, less than about 2 mm, or less than about 1 mm.
  • the whitened tobacco material can have an ISO brightness of at least about 50%, at least about 60%, at least about 65%, at least about 70%, at least about 75%, or at least about 80%.
  • the whitened tobacco material described herein can have an ISO brightness in the range of about 50% to about 90%, about 55% to about 75%, or about 60% to about 70%.
  • ISO brightness can be measured according to ISO 3688:1999 or ISO 2470-1:2016.
  • the whitened tobacco pulp thus produced can be characterized as lightened in color (e.g.,“whitened”) in comparison to the untreated tobacco pulp.
  • Visual and/or instrumental assessments such as those previously described can be used to verily and, if desired, quantify the degree of lightening achieved by way of the presently described method of the invention.
  • Assessment of the whiteness of a material generally requires comparison with another material.
  • the extent of lightening can be quantified, for example, by spectroscopic comparison with an untreated tobacco sample (e.g., untreated tobacco pulp).
  • White colors are often defined with reference to the International Commission on
  • Illumination's CIE's
  • the whitened tobacco pulp can, in certain embodiments, be characterized as closer on the chromaticity diagram to pure white than untreated tobacco pulp.
  • the tobacco materials discussed in the present invention can be treated and/or processed in other ways before, after, or during the process steps described above.
  • the tobacco materials can be irradiated, pasteurized, or otherwise subjected to controlled heat treatment.
  • Such treatment processes are detailed, for example, in US Pat. Pub. No. 2009/0025738 to Mua et al, which is incorporated herein by reference.
  • tobacco materials can be treated with water and an additive capable of inhibiting reaction of asparagine to form acrylamide upon heating of the tobacco material (e.g., an additive selected from the group consisting of lysine, glycine, histidine, alanine, methionine, glutamic acid, aspartic acid, proline, phenylalanine, valine, arginine, compositions incorporating di- and trivalent cations, asparaginase, certain non-reducing saccharides, certain reducing agents, phenolic compounds, certain compounds having at least one free thiol group or functionality, oxidizing agents, oxidation catalysts, natural plant extracts (e.g., rosemary extract), and combinations thereof), and combinations thereof.
  • an additive selected from the group consisting of lysine, glycine, histidine, alanine, methionine, glutamic acid, aspartic acid, proline, phenylalanine, valine, arginine, compositions incorporating di- and trivalent
  • the whitened tobacco material can be incorporated within a smokeless tobacco product according to the present invention.
  • the tobacco product can include one or more additional components in addition to the whitened tobacco material as described above.
  • the whitened tobacco material can be processed, blended, formulated, combined and or mixed with other materials or ingredients, such as other tobacco materials or flavorants, fillers, binders, pH adjusters, buffering agents, salts, sweeteners, colorants, oral care additives, disintegration aids, antioxidants, humectants, and preservatives. See, for example, those representative components, combination of components, relative amounts of those components and ingredients relative to tobacco, and manners and methods for employing those components, set forth in US Pat. Pub.
  • the relative amount of whitened tobacco material within the smokeless tobacco product may vary.
  • the amount of whitened tobacco material within the smokeless tobacco product is at least about 10%, at least about 25%, at least about 50%, at least about 60%, at least about 70%, at least about 80%, or at least about 90% on a dry weight basis of the formulation.
  • a typical range of tobacco material within the formulation is about 10 to about 99%, more often about 50 to about 99% by weight on a dry basis.
  • the whitened tobacco material used for the manufacture of the smokeless tobacco products of the invention preferably is provided in a ground, granulated, fine particulate, or powdered form.
  • the whitened tobacco material may be subjected to processing steps that provide a further grinding for further particle size reduction.
  • the whitening processes of the present invention generally provide a whitened tobacco material with a decreased amount of high molecular weight compounds, leading to more interstitial room and thus higher possible water content in smokeless tobacco materials produced therefrom than those from unwhitened tobacco materials.
  • the smokeless tobacco products produced according to the invention provide for faster nicotine release than products produced from unwhitened tobacco materials.
  • Example flavorants that can be used are components, or suitable combinations of those components, that act to alter the bitterness, sweetness, sourness, or saltiness of the smokeless tobacco product, enhance the perceived dryness or moistness of the formulation, or the degree of tobacco taste exhibited by the formulation.
  • Flavorants may be natural or synthetic, and the character of the flavors imparted thereby may be described, without limitation, as fresh, sweet, herbal, confectionary, floral, fruity, or spicy.
  • flavors include, but are not limited to, vanilla, coffee, chocolate/cocoa, cream, mint, spearmint, menthol, peppermint, wintergreen, eucalyptus, lavender, cardamon, nutmeg, cinnamon, clove, cascarilla, sandalwood, honey, jasmine, ginger, anise, sage, licorice, lemon, orange, apple, peach, lime, cherry, strawberry, and any combinations thereof. See also, Leffmgwell et al., Tobacco Flavoring for Smoking Products, R. J. Reynolds Tobacco Company (1972), which is incorporated herein by reference. Flavorings also may include components that are considered moistening, cooling or smoothening agents, such as eucalyptus.
  • Types of flavorants include salts (e.g., sodium chloride, potassium chloride, sodium citrate, potassium citrate, sodium acetate, potassium acetate, and the like), natural sweeteners (e.g., fructose, sucrose, glucose, maltose, mannose, galactose, lactose, and the like), artificial sweeteners (e.g., sucralose, saccharin, aspartame, acesulfame K, neotame, and the like); and mixtures thereof.
  • salts e.g., sodium chloride, potassium chloride, sodium citrate, potassium citrate, sodium acetate, potassium acetate, and the like
  • natural sweeteners e.g., fructose, sucrose, glucose, maltose, mannose, galactose, lactose, and the like
  • artificial sweeteners e.g., sucralose, saccharin, aspartame, acesulfame K,
  • the amount of flavorants utilized in the tobacco composition can vary, but is typically up to about 10 dry weight percent, and certain embodiments are characterized by a flavorant content of at least about 1 dry weight percent, such as about 1 to about 10 dry weight percent. Combinations of flavorants are often used, such as about 0.1 to about 2 dry weight percent of an artificial sweetener, about 0.5 to about 8 dry weight percent of a salt such as sodium chloride and about 1 to about 5 dry weight percent of an additional flavoring.
  • Example filler materials include vegetable fiber materials such as sugar beet fiber materials (e.g., FIBREX® brand filler available from International Fiber Corporation), oats or other cereal grain (including processed or puffed grains), bran fibers, starch, or other modified or natural cellulosic materials such as microcrystalline cellulose. Additional specific examples include com starch, maltodextrin, dextrose, calcium carbonate, calcium phosphate, lactose, manitol, xylitol, and sorbitol.
  • vegetable fiber materials such as sugar beet fiber materials (e.g., FIBREX® brand filler available from International Fiber Corporation), oats or other cereal grain (including processed or puffed grains), bran fibers, starch, or other modified or natural cellulosic materials such as microcrystalline cellulose. Additional specific examples include com starch, maltodextrin, dextrose, calcium carbonate, calcium phosphate, lactose, manitol, xylito
  • the amount of filler, where utilized in the tobacco composition can vary, but is typically up to about 20 dry weight percent, and certain embodiments are characterized by a filler content of up to about 10 dry weight percent, up to about 5 dry weight percent or up to about 1 dry weight percent. Combinations of fillers can also be used.
  • Typical binders can be organic or inorganic, or a combination thereof.
  • Representative binders include povidone, sodium carboxymethylcellulose and other modified cellulosic materials, sodium alginate, xanthan gum, starch-based binders, gum arabic, pectin, carrageenan, pullulan, zein, and the like.
  • the amount of binder utilized in the tobacco composition can vary, but is typically up to about 30 dry weight percent, and certain embodiments are characterized by a binder content of at least about 5 dry weight percent, such as about 5 to about 30 dry weight percent.
  • Preferred pH adjusters or buffering agents provide and/or buffer within a pH range of about 6 to about 10, and example agents include metal hydroxides, metal carbonates, metal bicarbonates, and mixtures thereof. Specific example materials include citric acid, sodium hydroxide, potassium hydroxide, potassium carbonate, sodium carbonate, and sodium bicarbonate.
  • the amount of pH adjuster or buffering material utilized in the tobacco composition can vary, but is typically up to about 5 dry weight percent, and certain embodiments can be characterized by a pH adjuster/buffer content of less than about 0.5 dry weight percent, such as about 0.05 to about 0.2 dry weight percent. Particularly in embodiments comprising an extract clarified by distillation, the pH may be lowered by the addition of one or more pH adjusters (e.g., citric acid).
  • a colorant may be employed in amounts sufficient to provide the desired physical attributes to the tobacco formulation.
  • Example colorants include various dyes and pigments, such as caramel coloring and titanium dioxide.
  • the amount of colorant utilized in the tobacco composition can vary, but is typically up to about 3 dry weight percent, and certain embodiments are characterized by a colorant content of at least about 0.1 dry weight percent, such as about 0.5 to about 3 dry weight percent.
  • Example humectants include glycerin and propylene glycol.
  • the amount of humectant utilized in the tobacco composition can vary, but is typically up to about 5 dry weight percent, and certain
  • embodiments can be characterized by a humectant content of at least about 1 dry weight percent, such as about 2 to about 5 dry weight percent.
  • ingredients such as preservatives (e.g., potassium sorbate), disintegration aids (e.g., microcrystalline cellulose, croscarmellose sodium, crospovidone, sodium starch glycolate, pregelatinized com starch, and the like), and/or antioxidants can also be used.
  • preservatives e.g., potassium sorbate
  • disintegration aids e.g., microcrystalline cellulose, croscarmellose sodium, crospovidone, sodium starch glycolate, pregelatinized com starch, and the like
  • antioxidants e.g., antioxidants
  • such ingredients, where used are used in amounts of up to about 10 dry weight percent and usually at least about 0.1 dry weight percent, such as about 0.5 to about 10 dry weight percent.
  • a disintegration aid is generally employed in an amount sufficient to provide control of desired physical attributes of the tobacco formulation such as, for example, by providing loss of physical integrity and dispersion of the various component materials upon contact of the formulation with water (e.g
  • any of the components described above can be added in an encapsulated form (e.g., in the form of microcapsules), the encapsulated form a wall or barrier structure defining an inner region and isolating the inner region permanently or temporarily from the tobacco composition.
  • the inner region includes a payload of an additive either adapted for enhancing one or more sensory characteristics of the smokeless tobacco product, such as taste, mouthfeel, moistness, coolness/heat, and/or fragrance, or adapted for adding an additional functional quality to the smokeless tobacco product, such as addition of an antioxidant or immune system enhancing function. See, for example, the subject matter of US Pat. Appl. Pub. No. 2009/0025738 to Mua et ak, which is incorporated herein by reference.
  • Representative tobacco formulations may incorporate about 80% to about 95% percent whitened tobacco material, about 0.1% to about 5% artificial sweetener, about 0.5% to about 2% salt, about 1% to about 5% flavoring, about 1% to about 5% humectants (e.g., propylene glycol), and up to about 10% pH adjuster or buffering agent (e.g., sodium bicarbonate or citric acid), based on the total dry weight of the tobacco formulation.
  • pH adjuster or buffering agent e.g., sodium bicarbonate or citric acid
  • the components of the tobacco composition can be brought together in admixture using any mixing technique or equipment known in the art.
  • the optional components noted above which may be in liquid or dry solid form, can be admixed with the whitened tobacco material in a pretreatment step prior to mixture with any remaining components of the composition or simply mixed with the whitened tobacco material together with all other liquid or dry ingredients.
  • Any mixing method that brings the tobacco composition ingredients into intimate contact can be used.
  • a mixing apparatus featuring an impeller or other structure capable of agitation is typically used.
  • Example mixing equipment includes casing drums, conditioning cylinders or dmms, liquid spray apparatus, conical-type blenders, ribbon blenders, mixers available as FKM130, FKM600, FKM1200, FKM2000 and FKM3000 from Littleford Day, Inc., Plough Share types of mixer cylinders, and the like.
  • the overall mixture of various components with the whitened tobacco material may be relatively uniform in nature. See also, for example, the types of methodologies set forth in US Pat. No. 4,148,325 to Solomon et ak; US Pat. No. 6,510,855 to Korte et ak; and US Pat. No. 6,834,654 to Williams, each of which is incorporated herein by reference. Manners and methods for formulating snus- type tobacco formulations will be apparent to those skilled in the art of snus tobacco product production.
  • the moisture content of the smokeless tobacco product prior to use by a consumer of the formulation may vary.
  • the moisture content of the product, as present within the pouch prior to insertion into the mouth of the user is less than about 55 weight percent, generally is less than about 50 weight percent, and often is less than about 45 weight percent.
  • the moisture content may exceed 20 weight percent, and often may exceed 30 weight percent.
  • a representative snus-type product may possess a tobacco composition exhibiting a moisture content of about 20 weight percent to about 50 weight percent, preferably about 20 weight percent to about 40 weight percent.
  • the manner by which the moisture content of the formulation is controlled may vary.
  • the formulation may be subjected to thermal or convection heating.
  • the formulation may be oven-dried, in warmed air at temperatures of about 40°C to about 95°C, with a preferred temperature range of about 60°C to about 80°C for a length of time appropriate to attain the desired moisture content.
  • tobacco formulations may be moistened using casing drums, conditioning cylinders or drums, liquid spray apparatus, ribbon blenders, or mixers.
  • moist tobacco formulations such as the types of tobacco formulations employed within snus types of products, are subjected to pasteurization or fermentation. Techniques for pasteurizing/heat treating and/or fermenting snus types of tobacco products will be apparent to those skilled in the art of snus product design and manufacture.
  • the acidity or alkalinity of the tobacco formulation can vary.
  • the pH of that formulation is at least about 6.5, and preferably at least about 7.5.
  • the pH of that formulation will not exceed about 11, or will not exceed about 9, and often will not exceed about 8.5.
  • a representative tobacco formulation exhibits a pH of about 6.8 to about 8.2 (e.g., about 7.8).
  • a representative technique for determining the pH of a tobacco formulation involves dispersing 5 g of that formulation in 100 ml of high performance liquid chromatography water, and measuring the pH of the resulting suspension/solution (e.g., with a pH meter).
  • the whitened tobacco material and any other components noted above are combined within a moisture-permeable packet or pouch that acts as a container for use of the tobacco.
  • the composition/construction of such packets or pouches, such as the container pouch 20 in the embodiment illustrated in Figure 1, may be varied.
  • Suitable packets, pouches or containers of the type used for the manufacture of smokeless tobacco products are available under the tradenames CatchDry, Ettan, General, Granit, Goteborgs Rape, Grovsnus White, Metropol Kaktus, Mocca Anis, Mocca Mint, Mocca Wintergreen, Kicks, Probe, Prince, Skruf, Epok, and TreAnkrare.
  • the tobacco formulation may be contained in pouches and packaged, in a manner and using the types of components used for the manufacture of conventional snus types of products.
  • the pouch provides a liquid-permeable container of a type that may be considered to be similar in character to the mesh-like type of material that is used for the construction of a tea bag.
  • Components of the loosely arranged, granular tobacco formulation readily diffuse through the pouch and into the mouth of the user.
  • Snus types of products can be manufactured using equipment such as that available as SB 51-1/T, SBL 50 and SB 53-2/T from Merzmaschinen GmBH.
  • Snus pouches can be provided as individual pouches, or a plurality of pouches (e.g., 2, 4, 5, 10, 12, 15, 20, 25 or 30 pouches) can connected or linked together (e.g., in an end-to-end manner) such that a single pouch or individual portion can be readily removed for use from a one-piece strand or matrix of pouches.
  • a pouch may, for example, be manufactured from materials, and in such a manner, such that during use by the user, the pouch undergoes a controlled dispersion or dissolution.
  • Such pouch materials may have the form of a mesh, screen, perforated paper, permeable fabric, or the like.
  • pouch material manufactured from a mesh-like form of rice paper, or perforated rice paper may dissolve in the mouth of the user.
  • the pouch and tobacco formulation each may undergo complete dispersion within the mouth of the user during normal conditions of use, and hence the pouch and tobacco formulation both may be ingested by the user.
  • pouch materials may be manufactured using water dispersible film forming materials (e.g., binding agents such as alginates, carboxymethylcellulose, xanthan gum, pullulan, and the like), as well as those materials in combination with materials such as ground cellulosics (e.g., fine particle size wood pulp).
  • Preferred pouch materials though water dispersible or dissolvable, may be designed and manufactured such that under conditions of normal use, a significant amount of the tobacco formulation contents permeate through the pouch material prior to the time that the pouch undergoes loss of its physical integrity.
  • flavoring ingredients, disintegration aids, and other desired components may be incorporated within, or applied to, the pouch material.
  • a nonwoven web can be used to form an outer water-permeable pouch which can be used to house a composition adapted for oral use.
  • each pouch may vary. In smaller embodiments, the dry weight of the material within each pouch is at least about 50 mg to about 150 mg. For a larger embodiment, the dry weight of the material within each pouch preferably does not exceed about 300 mg to about 500 mg.
  • each pouch/container may have disposed therein a flavor agent member, as described in greater detail in US Pat. No. 7,861,728 to Holton, Jr. et al, which is incorporated herein by reference. If desired, other components can be contained within each pouch.
  • At least one flavored strip, piece or sheet of flavored water dispersible or water soluble material may be disposed within each pouch along with or without at least one capsule.
  • flavored water dispersible or water soluble material e.g., a breath-freshening edible film type of material
  • Such strips or sheets may be folded or crumpled in order to be readily incorporated within the pouch. See, for example, the types of materials and technologies set forth in US Pat. Nos. 6,887,307 to Scott et al. and 6,923,981 to Leung et al.; and The EFSA Journal (2004) 85, 1-32; which are incorporated herein by reference.
  • the smokeless tobacco product can be packaged within any suitable inner packaging material and/or outer container. See also, for example, the various types of containers for smokeless types of products that are set forth in US Pat. Nos. 7,014,039 to Henson et al.; 7,537,110 to Kutsch et al.; 7,584,843 to Kutsch et al.; D592,956 to Thiellier; D594,154 to Patel et al.; and D625,178 to Bailey et al.; US Pat. Pub. Nos.
  • Products of the present disclosure may be packaged and stored in much the same manner that conventional types of smokeless tobacco products are packaged and stored.
  • a plurality of packets or pouches may be contained in a container used to contain smokeless tobacco products, such as a cylindrical container sometimes referred to as a“puck”.
  • the container can be any shape, and is not limited to cylindrical containers.
  • Such containers may be manufactured out of any suitable material, such as metal, molded plastic, fiberboard, combinations thereof, etc.
  • moist tobacco products e.g., products having moisture contents of more than about 20 weight percent
  • may be refrigerated e.g., at a temperature of less than about 10° C, often less than about 8 °C, and sometimes less than about 5 °C).
  • relatively dry tobacco products e.g., products having moisture contents of less than about 15 weight percent
  • Various smokeless tobacco products disclosed herein are advantageous in that they provide a composition that is non-staining, or is staining to a lesser degree than products comprising only unwhitened tobacco materials. These products thus are desirable in reducing staining of teeth and clothing that may come in contact therewith. It is noted that even the spent (used) product is lighter in color than traditional spent (used) oral tobacco products. Further, the products may have enhanced visual appeal by virtue of their whitened color.
  • Embodiments of the present disclosure are more fully illustrated by the following examples, which are set forth to illustrate aspects of the present disclosure and are not to be construed as limiting thereof.
  • g means gram
  • L means liter
  • mL means milliliter
  • Da means daltons. All weight percentages are expressed on a dry basis, meaning excluding water content, unless otherwise indicated.
  • a bleached tobacco material was produced using tobacco plants as raw material. 1.1 lbs of milled N. rustica stem tobacco material (milled to a particle size of about 18-60 US mesh was soaked in 15.4 lbs of water and 2.4g of EDTA for 1 hour. The soaked tobacco material was then pressed and drained (i.e., dewatered) using a screw press.
  • the drained and pressed tobacco material was then treated with a caustic wash. Specifically, 10 lbs of 2.5% NaOH was added to the pressed tobacco material. The tobacco material and caustic wash mixture was held at about 210°F (about 100°C) for about 90 minutes. The tobacco material in the NaOH wash was then drained and pressed to provide a tobacco pulp and residual liquid extract.
  • the tobacco pulp (1.34 lbs) was then mixed with a bleaching solution comprising 2L water, 15 grams NaOH, and 45 grams of sodium silicate (NaSiCh).
  • a bleaching solution comprising 2L water, 15 grams NaOH, and 45 grams of sodium silicate (NaSiCh).
  • 0.9 lbs of 35% hydrogen peroxide was added to the mixture and the mixture was cooked for 60 minutes.
  • the cooked mixture was allowed to sit for 30 mins, and then it was neutralized with HC1 to bring the mixture to a pH of about 9. Finally the mixture was dried.
  • a bleaching solution comprising 2L water, 15 grams NaOH, and 45 grams of sodium silicate (NaSiCh).
  • a bleached tobacco material was produced using tobacco plants as raw material. 1.1 lbs of finely milled burley stem tobacco material (milled to a particle size of about 18-60 US mesh) was soaked in 15.4 lbs of water and 2.4g of EDTA for 1 hour. The soaked tobacco material was then pressed and drained in a screw press.
  • the drained and pressed tobacco material was then treated with a caustic wash. Specifically, 10 lbs of 2.5% NaOH was added to the pressed tobacco material. The tobacco material and caustic wash mixture was held at about 210°F (about 100°C) for about 90 minutes. The tobacco material in the NaOH wash was then drained and pressed to provide a tobacco pulp and residual liquid extract.
  • the bleaching was conducted by two-stage high-consistency bleaching with peracetic acid followed by hydrogen peroxide (P).
  • a first bleaching solution comprising 4.5L of water and 50g of peracetic acid for 90 minutes.
  • the pH of the mixture after the addition of the peracetic acid was about 5.2.
  • 7.0g of NaOH was added and the new pH was about 6.8.
  • an additional 6.0g of NaOH was added to the mixture and the pH was about 8.0.
  • the final pH of the tobacco pulp after the bleaching with the peracetic acid was about 8.2.
  • the pulp was then pressed and drained in a screw press.
  • a second bleaching solution comprising 2L water, 15 grams NaOH, 15 grams of magnesium sulfate ( gSO ) and 45 grams of sodium silicate (NaSiCh).
  • 0.9 lbs of 35% hydrogen peroxide was added to the mixture and the mixture was cooked for 60 minutes. The cooked mixture was allowed to sit for 30 mins, and then it was neutralized with HC1 to bring the mixture to a pH of about 9. Finally the mixture was dried.
  • a bleached tobacco material was produced using tobacco plants as raw material.
  • the dry weight recipe of the resulting pulp, which has no added wood pulp, is shown in Table 1 below.
  • tobacco biomass was extracted with hot water. About 75 lbs. of milled Rustic stem was weighed out. About 600 lbs. of hot water (about 212°F) was added to a tank. An agitator was turned on in the tank, it was ensured that the discharge valve on the tank was closed, and the milled Rustica stem was added to the tank. Next, about 187.5 g of EDTA was weighed out and added to the tank. The steam drain on the tank was opened and steam was applied to the tank. Once the temperature of the liquid in the tank reached about 180-215°F, the contents of the tank were mixed for 50 mins while steam was still being added to the tank. After 50 minutes, the steam into the tank was cut off. The contents of the tank were then mixed for an additional 10 minutes.
  • the liquid in the tank was discharged and the remaining Rustica stem was rinsed and drained using a basket centrifuge.
  • Alternative dewatering equipment can also be used.
  • a screw press was used for recipes that included wood pulp, while a basket centrifuge was used for recipes with no added wood pulp.
  • the tobacco biomass was caustically extracted.
  • About 600 lbs. of water was added to the tank.
  • An agitator was turned on in the tank and it was ensured that the discharge valve on the tank was closed.
  • About 37.5 lbs. of sodium hydroxide powder was measured and added to the tank.
  • the steam drain on the tank was opened and steam was applied to the tank. Once the temperature of the liquid in the tank reached about 200-215°F, the contents of the tank were then held at about 212°F and mixed for about 90 mins while steam was still being added to the tank. After 90 minutes, the steam into the tank was cut off.
  • About 50.0 lbs. of citric acid powder was then measured and slowly added to the tank. The contents of the tank were then mixed for an additional 10 minutes.
  • the pH of the contents of the tank was measured and adjusted until the pH was in the range of about 9.0 to about 10.5.
  • the liquid in the tank was discharged and the remaining tobacco cake was rinsed and drained using a basket centrifuge. About 100 lbs. of water can be used to rinse the residual pulp and the rinsing and dewatering steps can be repeated if necessary.
  • the tobacco biomass was subjected to a peroxide bleaching process.
  • the discharge valve of the tank is closed and about 600 lbs. of hot water (about 180°F) was added to the tank.
  • the steam drain on the tank was opened and steam was applied to the tank.
  • the agitator for the tank was turned on.
  • the rinsed and dewatered tobacco cake was then added to the tank.
  • About 22.5 lbs. of sodium hydroxide powder was measured and added to the tank.
  • About 7.5 lbs. of 40% sodium silicate was measured and added to the tank.
  • About 127.5 lbs. of 36% peroxide was measured and added to the tank.
  • a pump at 20 psi was run to the tank for about 1 minute with the ball valve wide open and then flushed with about 12 gallons of water.
  • the steam drain on the tank was opened and steam was applied to the tank. Once the temperature of the liquid in the tank reached about 165°F, the liquid began to foam. About 30 grams (or more) of defoamer can be added as necessary to keep the foam contained in the tank. After the temperature of the liquid in the tank reached about 180°F, the steam was turned off and the contents of the tank were mixed for about 30-60 mins. Next, about 34.0 lbs. of citric acid powder was measured and added to the tank. The contents of the tank were then allowed to mix for about 10 minutes. The pH of the contents of the tank was then measured and adjusted until the pH was in the range of about 10.0 to about 10.75.
  • the liquid in the tank was discharged and the remaining tobacco cake was rinsed and drained using a screw press and/or centrifuge. About 100 lbs. of water can be used to rinse the residual pulp and the rinsing and dewatering steps can be repeated if necessary.
  • the final tobacco cake can be dried to a moisture content of about 10- 15% moisture.
  • a bleached tobacco material was produced using tobacco plants as raw material.
  • the dry weight recipe of the resulting pulp, which has wood pulp added, is shown in Table 2 below.
  • Example 3 The extraction and bleaching processes used above in Example 3 were also used for bleaching the tobacco biomass with the added wood pulp. However, as noted above, a screw press was used for dewatering/drying the pulp at various points in the process instead of a basket centrifuge.
  • Example 3 Two samples of bleached tobacco pulp according to Example 3 (no added wood pulp) were tested and had an ISO brightness of 67.6% and 63.8%.
  • Example 4 One sample of bleached tobacco pulp according to Example 4 (with added wood pulp) was tested and had an ISO brightness of 70.1%.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture Of Tobacco Products (AREA)

Abstract

L'invention concerne un procédé de préparation de matière de tabac blanchie, le procédé comprenant les étapes consistant à (i) extraire une matière de tabac avec une solution aqueuse pour obtenir une matière solide de tabac et un extrait de tabac ; (ii) traiter la matière solide de tabac avec un lavage caustique pour obtenir une pâte de tabac ; (iii) blanchir la pâte de tabac avec une solution comprenant une base forte, un agent oxydant ou une combinaison de ceux-ci pour obtenir une pâte de tabac blanchie ; et (iv) sécher la pâte de tabac blanchie pour obtenir la matière de tabac blanchie. L'invention concerne également un produit de tabac sans fumée incorporant une matière de tabac blanchie. Le produit de tabac sans fumée peut être une formulation de type tabac humide contenue dans un sachet fermé hermétiquement.
PCT/IB2019/061129 2018-12-20 2019-12-19 Procédé de blanchiment de tabac WO2020128971A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
MX2021007533A MX2021007533A (es) 2018-12-20 2019-12-19 Metodo para blanquear tabaco.
JP2021535697A JP2022514100A (ja) 2018-12-20 2019-12-19 タバコを白色化する方法
CA3124297A CA3124297A1 (fr) 2018-12-20 2019-12-19 Procede de blanchiment de tabac
EP19836840.9A EP3897230A1 (fr) 2018-12-20 2019-12-19 Procédé de blanchiment de tabac

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US16/227,742 US20200196658A1 (en) 2018-12-20 2018-12-20 Method for whitening tobacco
US16/227,742 2018-12-20

Publications (1)

Publication Number Publication Date
WO2020128971A1 true WO2020128971A1 (fr) 2020-06-25

Family

ID=69167870

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2019/061129 WO2020128971A1 (fr) 2018-12-20 2019-12-19 Procédé de blanchiment de tabac

Country Status (7)

Country Link
US (1) US20200196658A1 (fr)
EP (1) EP3897230A1 (fr)
JP (1) JP2022514100A (fr)
CA (1) CA3124297A1 (fr)
MX (1) MX2021007533A (fr)
TW (1) TW202033109A (fr)
WO (1) WO2020128971A1 (fr)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023007440A1 (fr) 2021-07-30 2023-02-02 Nicoventures Trading Limited Substrat de génération d'aérosol comprenant de la cellulose microcristalline
WO2023084499A1 (fr) 2021-11-15 2023-05-19 Nicoventures Trading Limited Produits présentant des caractéristiques sensorielles améliorées
WO2024079722A1 (fr) 2022-10-14 2024-04-18 Nicoventures Trading Limited Produits en sachet contenant des capsules
WO2024089588A1 (fr) 2022-10-24 2024-05-02 Nicoventures Trading Limited Produits en forme de sachet
WO2024095163A1 (fr) 2022-11-01 2024-05-10 Nicoventures Trading Limited Composition orale comprenant un agent d'ajustement de ph encapsulé
WO2024095164A1 (fr) 2022-11-01 2024-05-10 Nicoventures Trading Limited Produits à charge sphérique

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB201817864D0 (en) * 2018-11-01 2018-12-19 Nicoventures Trading Ltd Aerosolisable formulation
US20210229882A1 (en) * 2019-04-08 2021-07-29 Nicholas J. Singer Dissolvable and edible paper and film for food products
JP2022547977A (ja) 2019-09-11 2022-11-16 ニコベンチャーズ トレーディング リミテッド タバコを白色化するための代替方法
US11369131B2 (en) 2019-09-13 2022-06-28 Nicoventures Trading Limited Method for whitening tobacco
US11903406B2 (en) 2019-09-18 2024-02-20 American Snuff Company, Llc Method for fermenting tobacco
US11937626B2 (en) * 2020-09-04 2024-03-26 Nicoventures Trading Limited Method for whitening tobacco
WO2022132018A1 (fr) * 2020-12-16 2022-06-23 Liw Innovation Ab Nouvelle composition de poudre
JPWO2023119517A1 (fr) * 2021-12-22 2023-06-29
WO2023194959A1 (fr) 2022-04-06 2023-10-12 Nicoventures Trading Limited Produits en sachet avec liant thermoscellable
WO2024069544A1 (fr) 2022-09-30 2024-04-04 Nicoventures Trading Limited Substrat de tabac reconstitué pour dispositif de distribution d'aérosol
WO2024069542A1 (fr) 2022-09-30 2024-04-04 R. J. Reynolds Tobacco Company Procédé de formation de tabac reconstitué

Citations (162)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US787611A (en) 1903-06-17 1905-04-18 American Cigar Company Treating tobacco.
US1086306A (en) 1912-11-11 1914-02-03 Theodor Oelenheinz Process of bleaching tobacco-leaves.
US1376586A (en) 1918-04-06 1921-05-03 Schwartz Francis Tobacco-tablet
US1437095A (en) 1920-06-01 1922-11-28 August Wasmuth Process of bleaching tobacco
US1757477A (en) 1927-07-11 1930-05-06 Rosenhoch Samuel Process and device for ozonizing tobacco
US2122421A (en) 1937-07-30 1938-07-05 Du Pont Tobacco treatment
US2148147A (en) 1933-12-30 1939-02-21 Degussa Process for bleaching tobacco
US2170107A (en) 1935-01-28 1939-08-22 Degussa Process for bleaching tobacco
US2274649A (en) 1935-01-28 1942-03-03 Degussa Process for bleaching tobacco
US2770239A (en) 1952-02-04 1956-11-13 Prats Jose Romero Process of treating tobacco
US3612065A (en) 1970-03-09 1971-10-12 Creative Enterprises Inc Method of puffing tobacco and reducing nicotine content thereof
US3661192A (en) 1969-12-08 1972-05-09 Nicholson Mfg Co Peripheral chipper for round log sections
US3696917A (en) 1970-09-10 1972-10-10 Elaine G Levi Tobacco pouch closure
US3851653A (en) 1972-10-11 1974-12-03 Rosen Enterprises Inc Method of puffing tobacco and reducing nicotine content thereof
US3861602A (en) 1973-07-06 1975-01-21 Morbark Ind Inc Brush chipper
US3889689A (en) 1971-12-20 1975-06-17 Rosen Enterprise Inc Method of treating tobacco with catalase and hydrogen peroxide
US3943940A (en) 1974-09-13 1976-03-16 Isao Minami Method of removing nicotine in smoking and a smoking filter to be used therefor
US3943945A (en) 1971-09-20 1976-03-16 Rosen Enterprises, Inc. Process for preparation of reconstituted tobacco sheet
US4135563A (en) 1976-03-15 1979-01-23 Maucher Walter H Apparatus for reducing fiber material to chip form
US4143666A (en) 1975-08-15 1979-03-13 Philip Morris Incorporated Smoking material
US4144895A (en) 1974-03-08 1979-03-20 Amf Incorporated Solvent extraction process
US4148325A (en) 1975-08-18 1979-04-10 British-American Tobacco Company Limited Treatment of tobacco
US4150677A (en) 1977-01-24 1979-04-24 Philip Morris Incorporated Treatment of tobacco
US4194514A (en) 1976-09-27 1980-03-25 Stauffer Chemical Company Removal of radioactive lead and polonium from tobacco
CA1074606A (fr) 1977-06-08 1980-04-01 Llewellyn E. Clark Methode de thermo-mecanique pour la fabrication de la pate a papier et appareil servant a cette fin
US4267847A (en) 1978-05-12 1981-05-19 British-American Tobacco Company Limited Tobacco additives
US4289147A (en) 1979-11-15 1981-09-15 Leaf Proteins, Inc. Process for obtaining deproteinized tobacco freed of nicotine and green pigment, for use as a smoking product
US4340073A (en) 1974-02-12 1982-07-20 Philip Morris, Incorporated Expanding tobacco
US4351346A (en) 1980-03-08 1982-09-28 B.A.T. Cigaretten-Fabriken Gmbh Process for the preparation of aromatic substances
US4359059A (en) 1980-03-08 1982-11-16 B.A.T. Cigaretten-Fabriken Gmbh Process for the preparation of aromatic substances
US4366823A (en) 1981-06-25 1983-01-04 Philip Morris, Incorporated Process for expanding tobacco
US4366824A (en) 1981-06-25 1983-01-04 Philip Morris Incorporated Process for expanding tobacco
US4388933A (en) 1981-06-25 1983-06-21 Philip Morris, Inc. Tobacco stem treatment and expanded tobacco product
US4421595A (en) 1979-01-12 1983-12-20 Yhtyneet Paperitehtaat Oy Jylhavaara Process for preparing thermomechanical pulp with heat recovery
US4506682A (en) 1981-12-07 1985-03-26 Mueller Adam Clear tobacco aroma oil, a process for obtaining it from a tobacco extract, and its use
US4513756A (en) 1983-04-28 1985-04-30 The Pinkerton Tobacco Company Process of making tobacco pellets
US4528993A (en) 1982-08-20 1985-07-16 R. J. Reynolds Tobacco Company Process for producing moist snuff
US4589428A (en) 1980-02-21 1986-05-20 Philip Morris Incorporated Tobacco treatment
US4605016A (en) 1983-07-21 1986-08-12 Japan Tobacco, Inc. Process for preparing tobacco flavoring formulations
US4607479A (en) 1983-12-14 1986-08-26 Svenska Tobaks Ab Apparatus for packaging given quantities of snuff
US4624269A (en) 1984-09-17 1986-11-25 The Pinkerton Tobacco Company Chewable tobacco based product
US4631899A (en) 1983-09-20 1986-12-30 Hermann Kruger's EFTF. A/S Method of dispensing a metered quantity of snuff and of packaging the individual, metered quantities of snuff
US4641667A (en) 1983-12-09 1987-02-10 B.A.T. Cigarettenfabriken Gmbh Process of preparing nicotine N'-oxide and smoking products containing it
US4660577A (en) 1982-08-20 1987-04-28 R.J. Reynolds Tobacco Company Dry pre-mix for moist snuff
US4716911A (en) 1986-04-08 1988-01-05 Genencor, Inc. Method for protein removal from tobacco
US4727889A (en) 1986-12-22 1988-03-01 R. J. Reynolds Tobacco Company Tobacco processing
US4882128A (en) 1987-07-31 1989-11-21 Parr Instrument Company Pressure and temperature reaction vessel, method, and apparatus
US4887618A (en) 1988-05-19 1989-12-19 R. J. Reynolds Tobacco Company Tobacco processing
US4941484A (en) 1989-05-30 1990-07-17 R. J. Reynolds Tobacco Company Tobacco processing
US4967771A (en) 1988-12-07 1990-11-06 R. J. Reynolds Tobacco Company Process for extracting tobacco
US4986286A (en) 1989-05-02 1991-01-22 R. J. Reynolds Tobacco Company Tobacco treatment process
US4987907A (en) 1988-06-29 1991-01-29 Helme Tobacco Company Chewing tobacco composition and process for producing same
US4991599A (en) 1989-12-20 1991-02-12 Tibbetts Hubert M Fiberless tobacco product for smoking and chewing
US5005620A (en) 1990-04-17 1991-04-09 Morbark Industries, Inc. Drum-type wood chipper
US5005593A (en) 1988-01-27 1991-04-09 R. J. Reynolds Tobacco Company Process for providing tobacco extracts
US5018540A (en) 1986-12-29 1991-05-28 Philip Morris Incorporated Process for removal of basic materials
US5060669A (en) 1989-12-18 1991-10-29 R. J. Reynolds Tobacco Company Tobacco treatment process
US5065775A (en) 1990-02-23 1991-11-19 R. J. Reynolds Tobacco Company Tobacco processing
US5074319A (en) 1990-04-19 1991-12-24 R. J. Reynolds Tobacco Company Tobacco extraction process
US5092352A (en) 1983-12-14 1992-03-03 American Brands, Inc. Chewing tobacco product
US5099862A (en) 1990-04-05 1992-03-31 R. J. Reynolds Tobacco Company Tobacco extraction process
US5121757A (en) 1989-12-18 1992-06-16 R. J. Reynolds Tobacco Company Tobacco treatment process
US5131414A (en) 1990-02-23 1992-07-21 R. J. Reynolds Tobacco Company Tobacco processing
US5131415A (en) 1991-04-04 1992-07-21 R. J. Reynolds Tobacco Company Tobacco extraction process
US5148819A (en) 1991-08-15 1992-09-22 R. J. Reynolds Tobacco Company Process for extracting tobacco
US5167244A (en) 1990-01-19 1992-12-01 Kjerstad Randy E Tobacco substitute
US5197494A (en) 1991-06-04 1993-03-30 R.J. Reynolds Tobacco Company Tobacco extraction process
US5230354A (en) 1991-09-03 1993-07-27 R. J. Reynolds Tobacco Company Tobacco processing
US5234008A (en) 1990-02-23 1993-08-10 R. J. Reynolds Tobacco Company Tobacco processing
US5243999A (en) 1991-09-03 1993-09-14 R. J. Reynolds Tobacco Company Tobacco processing
US5259403A (en) 1992-03-18 1993-11-09 R. J. Reynolds Tobacco Company Process and apparatus for expanding tobacco cut filler
US5301694A (en) 1991-11-12 1994-04-12 Philip Morris Incorporated Process for isolating plant extract fractions
US5318050A (en) 1991-06-04 1994-06-07 R. J. Reynolds Tobacco Company Tobacco treatment process
US5343879A (en) 1991-06-21 1994-09-06 R. J. Reynolds Tobacco Company Tobacco treatment process
US5346734A (en) 1993-04-16 1994-09-13 Bethanie K. Wydick Perforated latex oral pouch for loose snuff
US5360022A (en) 1991-07-22 1994-11-01 R. J. Reynolds Tobacco Company Tobacco processing
US5387416A (en) 1993-07-23 1995-02-07 R. J. Reynolds Tobacco Company Tobacco composition
US5435325A (en) 1988-04-21 1995-07-25 R. J. Reynolds Tobacco Company Process for providing tobacco extracts using a solvent in a supercritical state
US5445169A (en) 1992-08-17 1995-08-29 R. J. Reynolds Tobacco Company Process for providing a tobacco extract
US5539093A (en) 1994-06-16 1996-07-23 Fitzmaurice; Wayne P. DNA sequences encoding enzymes useful in carotenoid biosynthesis
WO1996031255A1 (fr) 1995-04-07 1996-10-10 George Giolvas Procede et appareil pour l'elimination des constituants nocifs des cigarettes et du tabac avant leur consommation
US5668295A (en) 1990-11-14 1997-09-16 Philip Morris Incorporated Protein involved in nicotine synthesis, DNA encoding, and use of sense and antisense DNAs corresponding thereto to affect nicotine content in transgenic tobacco cells and plants
US5705624A (en) 1995-12-27 1998-01-06 Fitzmaurice; Wayne Paul DNA sequences encoding enzymes useful in phytoene biosynthesis
US5713376A (en) 1996-05-13 1998-02-03 Berger; Carl Non-addictive tobacco products
US5844119A (en) 1994-12-21 1998-12-01 The Salk Institute For Biological Studies Genetically modified plants having modulated flower development
US5908032A (en) 1996-08-09 1999-06-01 R.J. Reynolds Tobacco Company Method of and apparatus for expanding tobacco
US6131584A (en) 1999-04-15 2000-10-17 Brown & Williamson Tobacco Corporation Tobacco treatment process
US6162516A (en) 1995-10-11 2000-12-19 Derr; Dedric M. System and method for protecting oral tissues from smokeless tobacco
US6298859B1 (en) 1998-07-08 2001-10-09 Novozymes A/S Use of a phenol oxidizing enzyme in the treatment of tobacco
US6510855B1 (en) 2000-03-03 2003-01-28 Brown & Williamson Tobacco Corporation Tobacco recovery system
US6668839B2 (en) 2001-05-01 2003-12-30 Jonnie R. Williams Smokeless tobacco product
US20040020503A1 (en) 2001-05-01 2004-02-05 Williams Jonnie R. Smokeless tobacco product
US6730832B1 (en) 2001-09-10 2004-05-04 Luis Mayan Dominguez High threonine producing lines of Nicotiana tobacum and methods for producing
US20040118422A1 (en) 2002-12-19 2004-06-24 Swedish Match North Europe Ab Tobacco dough and a method for its manufacture
US6772767B2 (en) 2002-09-09 2004-08-10 Brown & Williamson Tobacco Corporation Process for reducing nitrogen containing compounds and lignin in tobacco
WO2004095959A1 (fr) 2003-04-29 2004-11-11 Swedish Match North Europe Ab Produit tabac sans fumee oral et son procede de production
US6834654B2 (en) 2001-05-01 2004-12-28 Regent Court Technologies, Llc Smokeless tobacco product
US20050061339A1 (en) 2001-12-21 2005-03-24 Henri Hansson Tobacco and/or tobacco substitute composition for use as a snuff in the oral cavity
US6887307B1 (en) 1999-07-22 2005-05-03 Warner-Lambert Company, Llc Pullulan film compositions
WO2005041699A2 (fr) 2003-11-03 2005-05-12 U.S. Smokeless Tobacco Company Tabac sans fumee aromatise et procedes de fabrication de ce tabac
US6895974B2 (en) 1999-04-26 2005-05-24 R. J. Reynolds Tobacco Company Tobacco processing
WO2005063060A1 (fr) 2003-12-22 2005-07-14 U.S. Smokeless Tobacco Company Procede de traitement pour compositions de tabac ou de tabac a priser
US6923981B2 (en) 1998-09-25 2005-08-02 Warner-Lambert Company Fast dissolving orally consumable films
US6953040B2 (en) 2001-09-28 2005-10-11 U.S. Smokeless Tobacco Company Tobacco mint plant material product
US20050244521A1 (en) 2003-11-07 2005-11-03 Strickland James A Tobacco compositions
US20060037623A1 (en) 2004-08-23 2006-02-23 Lawrence Robert H Jr Nicotiana diversity
US7014039B2 (en) 2003-06-19 2006-03-21 R.J. Reynolds Tobacco Company Sliding shell package for smoking articles
US7025066B2 (en) 2002-10-31 2006-04-11 Jerry Wayne Lawson Method of reducing the sucrose ester concentration of a tobacco mixture
US7032601B2 (en) 2001-09-28 2006-04-25 U.S. Smokeless Tobacco Company Encapsulated materials
US20060191548A1 (en) 2003-11-07 2006-08-31 Strickland James A Tobacco compositions
US20060236434A1 (en) 2000-08-30 2006-10-19 North Carolina State University Methods and compositions for tobacco plants with reduced nicotine
US20070062549A1 (en) 2005-09-22 2007-03-22 Holton Darrell E Jr Smokeless tobacco composition
US7208659B2 (en) 2001-05-02 2007-04-24 Conopco Inc. Process for increasing the flavonoid content of a plant and plants obtainable thereby
US7230160B2 (en) 2001-03-08 2007-06-12 Michigan State University Lipid metabolism regulators in plants
US7237733B2 (en) 2002-11-18 2007-07-03 M-Real Oyj Method and apparatus for producing mechanical fibers
US20070186941A1 (en) 2006-02-10 2007-08-16 Holton Darrell E Jr Smokeless tobacco composition
US20070186942A1 (en) 2006-01-31 2007-08-16 U. S. Smokeless Tobacco Company Tobacco Articles and Methods
US20080029110A1 (en) 2006-02-10 2008-02-07 R. J. Reynolds Tobacco Company Smokeless Tobacco Composition
US20080029116A1 (en) 2006-08-01 2008-02-07 John Howard Robinson Smokeless tobacco
US7337782B2 (en) 2004-08-18 2008-03-04 R.J. Reynolds Tobacco Company Process to remove protein and other biomolecules from tobacco extract or slurry
US20080173317A1 (en) 2006-08-01 2008-07-24 John Howard Robinson Smokeless tobacco
US20080196730A1 (en) 2004-07-02 2008-08-21 Radi Medical Systems Ab Smokeless Tobacco Product
US20080209586A1 (en) 2007-02-23 2008-08-28 U.S. Smokeless Tobacco Company Novel tobacco compositions and methods of making
US20080245377A1 (en) 2007-04-04 2008-10-09 R.J. Reynolds Tobacco Company Cigarette comprising dark-cured tobacco
US20080305216A1 (en) 2007-06-08 2008-12-11 Philip Morris Usa Inc. Capsule clusters for oral consumption
US20090014343A1 (en) 2007-05-07 2009-01-15 Philip Morris Usa Inc. Pocket-size hybrid container for consumer items
US20090014450A1 (en) 2003-08-18 2009-01-15 Gustavus Ab Snuff-box lid
US20090025738A1 (en) 2007-07-23 2009-01-29 R. J. Reynolds Tobacco Company Smokeless Tobacco Composition
US20090065013A1 (en) 2006-04-28 2009-03-12 Swedish Match North Europe Ab moist snuff non-tobacco composition and a method for producing thereof
USD592956S1 (en) 2008-02-08 2009-05-26 Philip Morris Usa Inc. Container
US7537110B2 (en) 2005-06-02 2009-05-26 Philip Morris Usa Inc. Container for consumer article
USD594154S1 (en) 2007-11-13 2009-06-09 R.J. Reynolds Tobacco Company Container with bottom compartment
US7556047B2 (en) 2003-03-20 2009-07-07 R.J. Reynolds Tobacco Company Method of expanding tobacco using steam
CN201268810Y (zh) 2008-09-25 2009-07-08 杨明学 一种秸秆机械制浆机
US7584843B2 (en) 2005-07-18 2009-09-08 Philip Morris Usa Inc. Pocket-size hand-held container for consumer items
US20090223989A1 (en) 2008-03-04 2009-09-10 R.J. Reynolds Tobacco Company Dispensing Container
US20090230003A1 (en) 2008-02-08 2009-09-17 Philip Morris Usa Inc. Pocket-sized container
US20090250360A1 (en) 2007-11-30 2009-10-08 Philip Morris Usa Inc. Pocket-size container for consumer items
US20090266837A1 (en) 2008-04-25 2009-10-29 R. J. Reynolds Tobacco Company Dispensing Container
US20090293889A1 (en) 2007-11-28 2009-12-03 Philip Morris Usa Inc. Smokeless compressed tobacco product for oral consumption
WO2010023363A1 (fr) 2008-08-29 2010-03-04 Upm-Kymmene Corporation Procédé et appareil pour la fabrication d’une pâte mécanique
US20100084424A1 (en) 2006-12-12 2010-04-08 John Gelardi Container with pivoting cover
US20100133140A1 (en) 2008-12-01 2010-06-03 Bailey Ryan A Dual cavity sliding dispenser
USD625178S1 (en) 2009-04-16 2010-10-12 R.J. Reynolds Tobacco Company, Inc. Container with hinged insert
US20100264157A1 (en) 2009-04-16 2010-10-21 R.J. Reynolds Tobacco Company Dispensing container for metered dispensing of product
US20100291245A1 (en) 2008-12-08 2010-11-18 Philip Morris Usa Inc. Soft, chewable and orally dissolvable and/or disintegrable products
WO2010132444A2 (fr) 2009-05-11 2010-11-18 U.S. Smokeless Tobacco Company Llc Procédé et dispositif pour aromatiser du tabac sans fumée
US20100300463A1 (en) 2009-06-02 2010-12-02 R.J. Reynolds Tobacco Company Thermal treatment process for tobacco materials
US20110048434A1 (en) 2009-06-02 2011-03-03 R. J. Reynolds Tobacco Company Thermal treatment process for tobacco materials
US20110139164A1 (en) 2009-12-15 2011-06-16 R. J. Reynolds Tobacco Company Tobacco Product And Method For Manufacture
US20110168712A1 (en) 2010-01-12 2011-07-14 R.J. Reynolds Tobacco Company Dispensing container
US20110204074A1 (en) 2010-02-23 2011-08-25 R.J. Reynolds Tobacco Company Dispensing container
US20110247640A1 (en) 2010-04-08 2011-10-13 R. J. Reynolds Tobacco Company Smokeless Tobacco Composition Comprising Tobacco-Derived Material and Non-Tobacco Plant Material
US20120067361A1 (en) 2009-04-03 2012-03-22 X-International Aps Plant fiber product and method for its manufacture
US20120152265A1 (en) 2010-12-17 2012-06-21 R.J. Reynolds Tobacco Company Tobacco-Derived Syrup Composition
US20120192880A1 (en) 2011-01-28 2012-08-02 R. J. Reynolds Tobacco Company Tobacco-derived casing composition
US20130206153A1 (en) * 2012-02-13 2013-08-15 R.J. Reynolds Tobacco Company Whitened tobacco composition
US20130276801A1 (en) 2012-04-19 2013-10-24 North Carolina State University Method for producing microcrystalline cellulose from tobacco and related tobacco product
US8991403B2 (en) 2009-06-02 2015-03-31 R.J. Reynolds Tobacco Company Thermal treatment process for tobacco materials
US20170020183A1 (en) 2014-04-04 2017-01-26 X-International Aps Tobacco Raw Material
WO2018083114A1 (fr) * 2016-11-02 2018-05-11 Winnington Ab Substance de tabac défibré
US20180266053A1 (en) * 2017-03-20 2018-09-20 R.J. Reynolds Tobacco Company Tobacco-derived nanocellulose material

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050056294A1 (en) * 2002-11-19 2005-03-17 Wanna Joseph T. Modified reconstituted tobacco sheet
BR112017003770B1 (pt) * 2014-09-30 2022-02-08 Philip Morris Products S.A. Material de tabaco homogeneizado, método de produção de material de tabaco homogeneizado e artigo gerador de aerosol compreendendo o dito material

Patent Citations (170)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US787611A (en) 1903-06-17 1905-04-18 American Cigar Company Treating tobacco.
US1086306A (en) 1912-11-11 1914-02-03 Theodor Oelenheinz Process of bleaching tobacco-leaves.
US1376586A (en) 1918-04-06 1921-05-03 Schwartz Francis Tobacco-tablet
US1437095A (en) 1920-06-01 1922-11-28 August Wasmuth Process of bleaching tobacco
US1757477A (en) 1927-07-11 1930-05-06 Rosenhoch Samuel Process and device for ozonizing tobacco
US2148147A (en) 1933-12-30 1939-02-21 Degussa Process for bleaching tobacco
US2274649A (en) 1935-01-28 1942-03-03 Degussa Process for bleaching tobacco
US2170107A (en) 1935-01-28 1939-08-22 Degussa Process for bleaching tobacco
US2122421A (en) 1937-07-30 1938-07-05 Du Pont Tobacco treatment
US2770239A (en) 1952-02-04 1956-11-13 Prats Jose Romero Process of treating tobacco
US3661192A (en) 1969-12-08 1972-05-09 Nicholson Mfg Co Peripheral chipper for round log sections
US3612065A (en) 1970-03-09 1971-10-12 Creative Enterprises Inc Method of puffing tobacco and reducing nicotine content thereof
US3696917A (en) 1970-09-10 1972-10-10 Elaine G Levi Tobacco pouch closure
US3943945A (en) 1971-09-20 1976-03-16 Rosen Enterprises, Inc. Process for preparation of reconstituted tobacco sheet
US3889689A (en) 1971-12-20 1975-06-17 Rosen Enterprise Inc Method of treating tobacco with catalase and hydrogen peroxide
US3851653A (en) 1972-10-11 1974-12-03 Rosen Enterprises Inc Method of puffing tobacco and reducing nicotine content thereof
US3861602A (en) 1973-07-06 1975-01-21 Morbark Ind Inc Brush chipper
US4340073A (en) 1974-02-12 1982-07-20 Philip Morris, Incorporated Expanding tobacco
US4144895A (en) 1974-03-08 1979-03-20 Amf Incorporated Solvent extraction process
US3943940A (en) 1974-09-13 1976-03-16 Isao Minami Method of removing nicotine in smoking and a smoking filter to be used therefor
US4143666A (en) 1975-08-15 1979-03-13 Philip Morris Incorporated Smoking material
US4148325A (en) 1975-08-18 1979-04-10 British-American Tobacco Company Limited Treatment of tobacco
US4135563A (en) 1976-03-15 1979-01-23 Maucher Walter H Apparatus for reducing fiber material to chip form
US4194514A (en) 1976-09-27 1980-03-25 Stauffer Chemical Company Removal of radioactive lead and polonium from tobacco
US4150677A (en) 1977-01-24 1979-04-24 Philip Morris Incorporated Treatment of tobacco
CA1074606A (fr) 1977-06-08 1980-04-01 Llewellyn E. Clark Methode de thermo-mecanique pour la fabrication de la pate a papier et appareil servant a cette fin
US4267847A (en) 1978-05-12 1981-05-19 British-American Tobacco Company Limited Tobacco additives
US4421595A (en) 1979-01-12 1983-12-20 Yhtyneet Paperitehtaat Oy Jylhavaara Process for preparing thermomechanical pulp with heat recovery
US4289147A (en) 1979-11-15 1981-09-15 Leaf Proteins, Inc. Process for obtaining deproteinized tobacco freed of nicotine and green pigment, for use as a smoking product
US4589428A (en) 1980-02-21 1986-05-20 Philip Morris Incorporated Tobacco treatment
US4359059A (en) 1980-03-08 1982-11-16 B.A.T. Cigaretten-Fabriken Gmbh Process for the preparation of aromatic substances
US4351346A (en) 1980-03-08 1982-09-28 B.A.T. Cigaretten-Fabriken Gmbh Process for the preparation of aromatic substances
US4366824A (en) 1981-06-25 1983-01-04 Philip Morris Incorporated Process for expanding tobacco
US4388933A (en) 1981-06-25 1983-06-21 Philip Morris, Inc. Tobacco stem treatment and expanded tobacco product
US4366823A (en) 1981-06-25 1983-01-04 Philip Morris, Incorporated Process for expanding tobacco
US4506682A (en) 1981-12-07 1985-03-26 Mueller Adam Clear tobacco aroma oil, a process for obtaining it from a tobacco extract, and its use
US4528993A (en) 1982-08-20 1985-07-16 R. J. Reynolds Tobacco Company Process for producing moist snuff
US4660577A (en) 1982-08-20 1987-04-28 R.J. Reynolds Tobacco Company Dry pre-mix for moist snuff
US4513756A (en) 1983-04-28 1985-04-30 The Pinkerton Tobacco Company Process of making tobacco pellets
US4605016A (en) 1983-07-21 1986-08-12 Japan Tobacco, Inc. Process for preparing tobacco flavoring formulations
US4631899A (en) 1983-09-20 1986-12-30 Hermann Kruger's EFTF. A/S Method of dispensing a metered quantity of snuff and of packaging the individual, metered quantities of snuff
US4641667A (en) 1983-12-09 1987-02-10 B.A.T. Cigarettenfabriken Gmbh Process of preparing nicotine N'-oxide and smoking products containing it
US4607479A (en) 1983-12-14 1986-08-26 Svenska Tobaks Ab Apparatus for packaging given quantities of snuff
US5092352A (en) 1983-12-14 1992-03-03 American Brands, Inc. Chewing tobacco product
US4624269A (en) 1984-09-17 1986-11-25 The Pinkerton Tobacco Company Chewable tobacco based product
US4716911A (en) 1986-04-08 1988-01-05 Genencor, Inc. Method for protein removal from tobacco
US4727889A (en) 1986-12-22 1988-03-01 R. J. Reynolds Tobacco Company Tobacco processing
US5018540A (en) 1986-12-29 1991-05-28 Philip Morris Incorporated Process for removal of basic materials
US4882128A (en) 1987-07-31 1989-11-21 Parr Instrument Company Pressure and temperature reaction vessel, method, and apparatus
US5005593A (en) 1988-01-27 1991-04-09 R. J. Reynolds Tobacco Company Process for providing tobacco extracts
US5435325A (en) 1988-04-21 1995-07-25 R. J. Reynolds Tobacco Company Process for providing tobacco extracts using a solvent in a supercritical state
US4887618A (en) 1988-05-19 1989-12-19 R. J. Reynolds Tobacco Company Tobacco processing
US4987907A (en) 1988-06-29 1991-01-29 Helme Tobacco Company Chewing tobacco composition and process for producing same
US4967771A (en) 1988-12-07 1990-11-06 R. J. Reynolds Tobacco Company Process for extracting tobacco
US4986286A (en) 1989-05-02 1991-01-22 R. J. Reynolds Tobacco Company Tobacco treatment process
US4941484A (en) 1989-05-30 1990-07-17 R. J. Reynolds Tobacco Company Tobacco processing
US5121757A (en) 1989-12-18 1992-06-16 R. J. Reynolds Tobacco Company Tobacco treatment process
US5060669A (en) 1989-12-18 1991-10-29 R. J. Reynolds Tobacco Company Tobacco treatment process
US4991599A (en) 1989-12-20 1991-02-12 Tibbetts Hubert M Fiberless tobacco product for smoking and chewing
US5167244A (en) 1990-01-19 1992-12-01 Kjerstad Randy E Tobacco substitute
US5065775A (en) 1990-02-23 1991-11-19 R. J. Reynolds Tobacco Company Tobacco processing
US5131414A (en) 1990-02-23 1992-07-21 R. J. Reynolds Tobacco Company Tobacco processing
US5234008A (en) 1990-02-23 1993-08-10 R. J. Reynolds Tobacco Company Tobacco processing
US5099862A (en) 1990-04-05 1992-03-31 R. J. Reynolds Tobacco Company Tobacco extraction process
US5005620A (en) 1990-04-17 1991-04-09 Morbark Industries, Inc. Drum-type wood chipper
US5074319A (en) 1990-04-19 1991-12-24 R. J. Reynolds Tobacco Company Tobacco extraction process
US5668295A (en) 1990-11-14 1997-09-16 Philip Morris Incorporated Protein involved in nicotine synthesis, DNA encoding, and use of sense and antisense DNAs corresponding thereto to affect nicotine content in transgenic tobacco cells and plants
US5131415A (en) 1991-04-04 1992-07-21 R. J. Reynolds Tobacco Company Tobacco extraction process
US5318050A (en) 1991-06-04 1994-06-07 R. J. Reynolds Tobacco Company Tobacco treatment process
US5197494A (en) 1991-06-04 1993-03-30 R.J. Reynolds Tobacco Company Tobacco extraction process
US5343879A (en) 1991-06-21 1994-09-06 R. J. Reynolds Tobacco Company Tobacco treatment process
US5360022A (en) 1991-07-22 1994-11-01 R. J. Reynolds Tobacco Company Tobacco processing
US5148819A (en) 1991-08-15 1992-09-22 R. J. Reynolds Tobacco Company Process for extracting tobacco
US5243999A (en) 1991-09-03 1993-09-14 R. J. Reynolds Tobacco Company Tobacco processing
US5230354A (en) 1991-09-03 1993-07-27 R. J. Reynolds Tobacco Company Tobacco processing
US5301694A (en) 1991-11-12 1994-04-12 Philip Morris Incorporated Process for isolating plant extract fractions
US5259403A (en) 1992-03-18 1993-11-09 R. J. Reynolds Tobacco Company Process and apparatus for expanding tobacco cut filler
US5445169A (en) 1992-08-17 1995-08-29 R. J. Reynolds Tobacco Company Process for providing a tobacco extract
US5346734A (en) 1993-04-16 1994-09-13 Bethanie K. Wydick Perforated latex oral pouch for loose snuff
US5387416A (en) 1993-07-23 1995-02-07 R. J. Reynolds Tobacco Company Tobacco composition
US5539093A (en) 1994-06-16 1996-07-23 Fitzmaurice; Wayne P. DNA sequences encoding enzymes useful in carotenoid biosynthesis
US5844119A (en) 1994-12-21 1998-12-01 The Salk Institute For Biological Studies Genetically modified plants having modulated flower development
WO1996031255A1 (fr) 1995-04-07 1996-10-10 George Giolvas Procede et appareil pour l'elimination des constituants nocifs des cigarettes et du tabac avant leur consommation
US6162516A (en) 1995-10-11 2000-12-19 Derr; Dedric M. System and method for protecting oral tissues from smokeless tobacco
US5705624A (en) 1995-12-27 1998-01-06 Fitzmaurice; Wayne Paul DNA sequences encoding enzymes useful in phytoene biosynthesis
US5713376A (en) 1996-05-13 1998-02-03 Berger; Carl Non-addictive tobacco products
US5908032A (en) 1996-08-09 1999-06-01 R.J. Reynolds Tobacco Company Method of and apparatus for expanding tobacco
US6298859B1 (en) 1998-07-08 2001-10-09 Novozymes A/S Use of a phenol oxidizing enzyme in the treatment of tobacco
US6923981B2 (en) 1998-09-25 2005-08-02 Warner-Lambert Company Fast dissolving orally consumable films
US6131584A (en) 1999-04-15 2000-10-17 Brown & Williamson Tobacco Corporation Tobacco treatment process
US6895974B2 (en) 1999-04-26 2005-05-24 R. J. Reynolds Tobacco Company Tobacco processing
US6887307B1 (en) 1999-07-22 2005-05-03 Warner-Lambert Company, Llc Pullulan film compositions
US6510855B1 (en) 2000-03-03 2003-01-28 Brown & Williamson Tobacco Corporation Tobacco recovery system
US20060236434A1 (en) 2000-08-30 2006-10-19 North Carolina State University Methods and compositions for tobacco plants with reduced nicotine
US7230160B2 (en) 2001-03-08 2007-06-12 Michigan State University Lipid metabolism regulators in plants
US20040020503A1 (en) 2001-05-01 2004-02-05 Williams Jonnie R. Smokeless tobacco product
US6834654B2 (en) 2001-05-01 2004-12-28 Regent Court Technologies, Llc Smokeless tobacco product
US6668839B2 (en) 2001-05-01 2003-12-30 Jonnie R. Williams Smokeless tobacco product
US7208659B2 (en) 2001-05-02 2007-04-24 Conopco Inc. Process for increasing the flavonoid content of a plant and plants obtainable thereby
US7173170B2 (en) 2001-09-10 2007-02-06 Reynolds Technologies, Inc. High threonine producing lines of Nicotiana tobacum and methods of producing
US6730832B1 (en) 2001-09-10 2004-05-04 Luis Mayan Dominguez High threonine producing lines of Nicotiana tobacum and methods for producing
US7032601B2 (en) 2001-09-28 2006-04-25 U.S. Smokeless Tobacco Company Encapsulated materials
US6953040B2 (en) 2001-09-28 2005-10-11 U.S. Smokeless Tobacco Company Tobacco mint plant material product
US20050061339A1 (en) 2001-12-21 2005-03-24 Henri Hansson Tobacco and/or tobacco substitute composition for use as a snuff in the oral cavity
US6772767B2 (en) 2002-09-09 2004-08-10 Brown & Williamson Tobacco Corporation Process for reducing nitrogen containing compounds and lignin in tobacco
US7025066B2 (en) 2002-10-31 2006-04-11 Jerry Wayne Lawson Method of reducing the sucrose ester concentration of a tobacco mixture
US7237733B2 (en) 2002-11-18 2007-07-03 M-Real Oyj Method and apparatus for producing mechanical fibers
US20040118422A1 (en) 2002-12-19 2004-06-24 Swedish Match North Europe Ab Tobacco dough and a method for its manufacture
US7556047B2 (en) 2003-03-20 2009-07-07 R.J. Reynolds Tobacco Company Method of expanding tobacco using steam
WO2004095959A1 (fr) 2003-04-29 2004-11-11 Swedish Match North Europe Ab Produit tabac sans fumee oral et son procede de production
US7014039B2 (en) 2003-06-19 2006-03-21 R.J. Reynolds Tobacco Company Sliding shell package for smoking articles
US20090014450A1 (en) 2003-08-18 2009-01-15 Gustavus Ab Snuff-box lid
US20050115580A1 (en) 2003-11-03 2005-06-02 Quinter Phillip F. Flavored smokeless tobacco and methods of making
WO2005041699A2 (fr) 2003-11-03 2005-05-12 U.S. Smokeless Tobacco Company Tabac sans fumee aromatise et procedes de fabrication de ce tabac
US20060191548A1 (en) 2003-11-07 2006-08-31 Strickland James A Tobacco compositions
US20050244521A1 (en) 2003-11-07 2005-11-03 Strickland James A Tobacco compositions
US7694686B2 (en) 2003-12-22 2010-04-13 U.S. Smokeless Tobacco Company Conditioning process for tobacco and/or snuff compositions
WO2005063060A1 (fr) 2003-12-22 2005-07-14 U.S. Smokeless Tobacco Company Procede de traitement pour compositions de tabac ou de tabac a priser
US20080196730A1 (en) 2004-07-02 2008-08-21 Radi Medical Systems Ab Smokeless Tobacco Product
US7337782B2 (en) 2004-08-18 2008-03-04 R.J. Reynolds Tobacco Company Process to remove protein and other biomolecules from tobacco extract or slurry
US20060037623A1 (en) 2004-08-23 2006-02-23 Lawrence Robert H Jr Nicotiana diversity
US7537110B2 (en) 2005-06-02 2009-05-26 Philip Morris Usa Inc. Container for consumer article
US7584843B2 (en) 2005-07-18 2009-09-08 Philip Morris Usa Inc. Pocket-size hand-held container for consumer items
US20070062549A1 (en) 2005-09-22 2007-03-22 Holton Darrell E Jr Smokeless tobacco composition
US20070186942A1 (en) 2006-01-31 2007-08-16 U. S. Smokeless Tobacco Company Tobacco Articles and Methods
US20080029110A1 (en) 2006-02-10 2008-02-07 R. J. Reynolds Tobacco Company Smokeless Tobacco Composition
US7861728B2 (en) 2006-02-10 2011-01-04 R.J. Reynolds Tobacco Company Smokeless tobacco composition having an outer and inner pouch
US20070186941A1 (en) 2006-02-10 2007-08-16 Holton Darrell E Jr Smokeless tobacco composition
US20090065013A1 (en) 2006-04-28 2009-03-12 Swedish Match North Europe Ab moist snuff non-tobacco composition and a method for producing thereof
US20080029116A1 (en) 2006-08-01 2008-02-07 John Howard Robinson Smokeless tobacco
US20080173317A1 (en) 2006-08-01 2008-07-24 John Howard Robinson Smokeless tobacco
US20100084424A1 (en) 2006-12-12 2010-04-08 John Gelardi Container with pivoting cover
WO2008103935A2 (fr) 2007-02-23 2008-08-28 U.S. Smokeless Tobacco Company Nouvelles compositions de tabac et leurs procédés de fabrication
US20080209586A1 (en) 2007-02-23 2008-08-28 U.S. Smokeless Tobacco Company Novel tobacco compositions and methods of making
US20080245377A1 (en) 2007-04-04 2008-10-09 R.J. Reynolds Tobacco Company Cigarette comprising dark-cured tobacco
US20090014343A1 (en) 2007-05-07 2009-01-15 Philip Morris Usa Inc. Pocket-size hybrid container for consumer items
US20080305216A1 (en) 2007-06-08 2008-12-11 Philip Morris Usa Inc. Capsule clusters for oral consumption
US20110315154A1 (en) 2007-07-23 2011-12-29 R. J. Reynolds Tobacco Company Smokeless tobacco composition
US20090025738A1 (en) 2007-07-23 2009-01-29 R. J. Reynolds Tobacco Company Smokeless Tobacco Composition
USD594154S1 (en) 2007-11-13 2009-06-09 R.J. Reynolds Tobacco Company Container with bottom compartment
US20090293889A1 (en) 2007-11-28 2009-12-03 Philip Morris Usa Inc. Smokeless compressed tobacco product for oral consumption
US20090250360A1 (en) 2007-11-30 2009-10-08 Philip Morris Usa Inc. Pocket-size container for consumer items
USD592956S1 (en) 2008-02-08 2009-05-26 Philip Morris Usa Inc. Container
US20090230003A1 (en) 2008-02-08 2009-09-17 Philip Morris Usa Inc. Pocket-sized container
US20090223989A1 (en) 2008-03-04 2009-09-10 R.J. Reynolds Tobacco Company Dispensing Container
US20090266837A1 (en) 2008-04-25 2009-10-29 R. J. Reynolds Tobacco Company Dispensing Container
WO2010023363A1 (fr) 2008-08-29 2010-03-04 Upm-Kymmene Corporation Procédé et appareil pour la fabrication d’une pâte mécanique
CN201268810Y (zh) 2008-09-25 2009-07-08 杨明学 一种秸秆机械制浆机
US20100133140A1 (en) 2008-12-01 2010-06-03 Bailey Ryan A Dual cavity sliding dispenser
US20100291245A1 (en) 2008-12-08 2010-11-18 Philip Morris Usa Inc. Soft, chewable and orally dissolvable and/or disintegrable products
US20120067361A1 (en) 2009-04-03 2012-03-22 X-International Aps Plant fiber product and method for its manufacture
US20100264157A1 (en) 2009-04-16 2010-10-21 R.J. Reynolds Tobacco Company Dispensing container for metered dispensing of product
USD625178S1 (en) 2009-04-16 2010-10-12 R.J. Reynolds Tobacco Company, Inc. Container with hinged insert
WO2010132444A2 (fr) 2009-05-11 2010-11-18 U.S. Smokeless Tobacco Company Llc Procédé et dispositif pour aromatiser du tabac sans fumée
US20100300463A1 (en) 2009-06-02 2010-12-02 R.J. Reynolds Tobacco Company Thermal treatment process for tobacco materials
US20110048434A1 (en) 2009-06-02 2011-03-03 R. J. Reynolds Tobacco Company Thermal treatment process for tobacco materials
US8991403B2 (en) 2009-06-02 2015-03-31 R.J. Reynolds Tobacco Company Thermal treatment process for tobacco materials
US20110139164A1 (en) 2009-12-15 2011-06-16 R. J. Reynolds Tobacco Company Tobacco Product And Method For Manufacture
US20110168712A1 (en) 2010-01-12 2011-07-14 R.J. Reynolds Tobacco Company Dispensing container
US20110204074A1 (en) 2010-02-23 2011-08-25 R.J. Reynolds Tobacco Company Dispensing container
US20110247640A1 (en) 2010-04-08 2011-10-13 R. J. Reynolds Tobacco Company Smokeless Tobacco Composition Comprising Tobacco-Derived Material and Non-Tobacco Plant Material
US20120152265A1 (en) 2010-12-17 2012-06-21 R.J. Reynolds Tobacco Company Tobacco-Derived Syrup Composition
US20120192880A1 (en) 2011-01-28 2012-08-02 R. J. Reynolds Tobacco Company Tobacco-derived casing composition
US20130206153A1 (en) * 2012-02-13 2013-08-15 R.J. Reynolds Tobacco Company Whitened tobacco composition
US9420825B2 (en) 2012-02-13 2016-08-23 R.J. Reynolds Tobacco Company Whitened tobacco composition
US20130276801A1 (en) 2012-04-19 2013-10-24 North Carolina State University Method for producing microcrystalline cellulose from tobacco and related tobacco product
US20170020183A1 (en) 2014-04-04 2017-01-26 X-International Aps Tobacco Raw Material
US20170112183A1 (en) 2014-04-04 2017-04-27 X-International Aps Tobacco Raw Material
WO2018083114A1 (fr) * 2016-11-02 2018-05-11 Winnington Ab Substance de tabac défibré
US20180266053A1 (en) * 2017-03-20 2018-09-20 R.J. Reynolds Tobacco Company Tobacco-derived nanocellulose material

Non-Patent Citations (8)

* Cited by examiner, † Cited by third party
Title
"Tobacco Production, Chemistry and Technology", 1999
GLIMN-LACY ET AL.: "Botany Illustrated", 2006, SPRINGER
GOODSPEED, THE GENUS NICOTIANA, (CHONICA BOTANICA, 1954
LEFFINGWELL ET AL.: "Tobacco Flavoring for Smoking Products", 1972, R. J. REYNOLDS TOBACCO COMPANY
MAUSETH: "Botany: An Introduction to Plant Biology", 2009, JONES AND BARTLETT PUBLISHERS
NESTOR ET AL., BEITRAGE TABAKFORSCH. INT., vol. 20, 2003, pages 467 - 475
STAAF ET AL., BEITRAGE TABAKFORSCH. INT., vol. 21, 2005, pages 321 - 330
THE EFSA JOURNAL, vol. 85, 2004, pages 1 - 32

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023007440A1 (fr) 2021-07-30 2023-02-02 Nicoventures Trading Limited Substrat de génération d'aérosol comprenant de la cellulose microcristalline
WO2023084499A1 (fr) 2021-11-15 2023-05-19 Nicoventures Trading Limited Produits présentant des caractéristiques sensorielles améliorées
WO2024079722A1 (fr) 2022-10-14 2024-04-18 Nicoventures Trading Limited Produits en sachet contenant des capsules
WO2024089588A1 (fr) 2022-10-24 2024-05-02 Nicoventures Trading Limited Produits en forme de sachet
WO2024095163A1 (fr) 2022-11-01 2024-05-10 Nicoventures Trading Limited Composition orale comprenant un agent d'ajustement de ph encapsulé
WO2024095164A1 (fr) 2022-11-01 2024-05-10 Nicoventures Trading Limited Produits à charge sphérique

Also Published As

Publication number Publication date
US20200196658A1 (en) 2020-06-25
MX2021007533A (es) 2021-08-05
EP3897230A1 (fr) 2021-10-27
TW202033109A (zh) 2020-09-16
CA3124297A1 (fr) 2020-06-25
JP2022514100A (ja) 2022-02-09

Similar Documents

Publication Publication Date Title
US20200196658A1 (en) Method for whitening tobacco
US11166486B2 (en) Whitened tobacco composition
US11369131B2 (en) Method for whitening tobacco
US11805804B2 (en) Alternative methods for whitening tobacco
US20210068448A1 (en) Method for whitening tobacco
US10342251B2 (en) Smokeless tobacco composition comprising tobacco-derived material and non-tobacco plant material
US11937626B2 (en) Method for whitening tobacco

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 19836840

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2021535697

Country of ref document: JP

Kind code of ref document: A

Ref document number: 3124297

Country of ref document: CA

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2019836840

Country of ref document: EP

Effective date: 20210720