EP2173200B1 - Composition de tabac sans fumée, et procédés pour traiter le tabac destiné à y être utilisé - Google Patents

Composition de tabac sans fumée, et procédés pour traiter le tabac destiné à y être utilisé Download PDF

Info

Publication number
EP2173200B1
EP2173200B1 EP08796428.4A EP08796428A EP2173200B1 EP 2173200 B1 EP2173200 B1 EP 2173200B1 EP 08796428 A EP08796428 A EP 08796428A EP 2173200 B1 EP2173200 B1 EP 2173200B1
Authority
EP
European Patent Office
Prior art keywords
tobacco
formulation
product
microcapsules
percent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP08796428.4A
Other languages
German (de)
English (en)
Other versions
EP2173200A2 (fr
Inventor
John-Paul Mua
Luis Rosete Monsalud Jr.
Darrell Eugene Holton Jr.
James Neil Figlar
Paul Andrew Brinkley
David Neil Mcclanahan
Jack Gray Flinchum Jr.
Michael Francis Dube
Daniel Verdin Cantrell
Cynthia Stewart Stokes
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
RJ Reynolds Tobacco Co
Original Assignee
RJ Reynolds Tobacco Co
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=40149768&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP2173200(B1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority claimed from US11/781,604 external-priority patent/US7810507B2/en
Priority claimed from US11/781,666 external-priority patent/US8061362B2/en
Priority claimed from US11/781,641 external-priority patent/US7946295B2/en
Application filed by RJ Reynolds Tobacco Co filed Critical RJ Reynolds Tobacco Co
Priority to EP11157884.5A priority Critical patent/EP2377413B1/fr
Priority to EP10152287A priority patent/EP2179666B1/fr
Publication of EP2173200A2 publication Critical patent/EP2173200A2/fr
Application granted granted Critical
Publication of EP2173200B1 publication Critical patent/EP2173200B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/28Treatment of tobacco products or tobacco substitutes by chemical substances
    • A24B15/281Treatment of tobacco products or tobacco substitutes by chemical substances the action of the chemical substances being delayed
    • A24B15/283Treatment of tobacco products or tobacco substitutes by chemical substances the action of the chemical substances being delayed by encapsulation of the chemical substances
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B13/00Tobacco for pipes, for cigars, e.g. cigar inserts, or for cigarettes; Chewing tobacco; Snuff
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/183Treatment of tobacco products or tobacco substitutes sterilization, preservation or biological decontamination
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/28Treatment of tobacco products or tobacco substitutes by chemical substances
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/28Treatment of tobacco products or tobacco substitutes by chemical substances
    • A24B15/30Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances

Definitions

  • the present invention relates to tobacco, and in particular, to the use of tobacco in a smokeless form.
  • WO 2007/037962 A1 discloses a smokeless tobacco product including a powdered or granular smokeless tobacco formulation that is contained within a moisture-permeable packet or pouch. At least one capsule is disposed in the pouch.
  • 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. Tobacco also may be enjoyed in a so-called "smokeless" form. Particularly popular smokeless tobacco products are employed by inserting some form of processed tobacco or tobacco-containing formulation into the mouth of the user.
  • snuff smokeless tobacco product
  • 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.
  • Snus products available in the U.S.A. are marketed under the tradenames Camel Snus Frost, Camel Snus Original and Camel Snus Spice by R. J. Reynolds Tobacco Company.
  • Representative smokeless tobacco products also are marketed under the tradenames Oliver Twist by House of Oliver Twist A/S; Copenhagen, Skoal, SkoalDry, Rooster, Red Seal, Husky, and Revel by U.S. Smokeless Tobacco Co.; "taboka” by Philip Morris USA; and Levi Garrett, Peachy, Taylor's Pride, Kodiak, Hawken Wintergreen, Grizzly, Dental, Kentucky King, and Mammoth Cave by Conwood Sales Co., L.P. See also, for example, Bryzgalov et al., 1N1800 Life Cycle Assessment, Comparative Life Cycle Assessment of General Loose and Portion Snus (2005). In addition, certain quality standards associated with snus manufacture have been assembled as a so-called GothiaTek standard.
  • the present invention relates to a smokeless tobacco product as defined in the claims.
  • Processes for preparing a tobacco composition suitable for use in a smokeless tobacco product are also disclosed.
  • the product includes a smokeless tobacco formulation that can take various forms, 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.
  • the smokeless tobacco product is in the form of a tobacco formulation disposed within a moisture-permeable container.
  • the smokeless tobacco formulation preferably includes shredded, granular, or particulate particles of tobacco, and may include other ingredients, such as sweeteners, binders, colorants, pH adjusters, fillers, flavoring agents, disintegration aids, antioxidants, oral care additives, and preservatives.
  • the smokeless tobacco product includes at least one additive or ingredient disposed within a tobacco formulation, wherein the additive is in a form adapted to segregate, or otherwise create physical separation between, the additive and one or more other components of the tobacco formulation during normal conditions of storage and/or use.
  • the additive is in a form adapted to segregate, or otherwise create physical separation between, the additive and one or more other components of the tobacco formulation during normal conditions of storage and/or use.
  • the invention provides a smokeless tobacco product configured for insertion into the mouth of a user of the product, the tobacco product comprising a tobacco formulation in a form suitable for insertion into the mouth of a user and at least one additive contained within the tobacco formulation, the additive being present in a form that physically separates the additive from the tobacco formulation.
  • Suitable forms designed to accomplish such separation, and hence promote inhibition of interaction of selected components during handling and storage include encapsulated forms; strips, pellets, films, and the like having selected ingredients physically or chemically entrapped or suspended therein; and the like.
  • An encapsulated form is used to separate the additive, the encapsulated form including a wall or barrier structure defining an inner region or payload that contains the additive.
  • the invention includes a tobacco formulation including a plurality of microcapsules containing an additive designed to enhance the sensory characteristics of the product or add functional advantages to the product.
  • Use of additives in microencapsulated form can improve storage stability of the product, particularly the stability of the sensory profile of the product, and protect certain additives from degradation over time.
  • Microencapsulation can also insulate the user from undesirable sensory characteristics associated with the encapsulated ingredient, such as certain fillers, or provide a milder sensory experience by extending the release of certain flavorants over time.
  • Microencapsulation of water can allow the product to be produced, stored, and transported at a lower moisture level, which can reduce storage and transportation costs and improve storage stability of the product.
  • Exemplary additives that can be microencapsulated or otherwise segregated within a tobacco formulation include water, flavorants (e.g., sweeteners or tobacco-containing flavorants), binders, colorants, pH adjusters, buffering agents, fillers, disintegration aids, humectants, antioxidants, oral care ingredients, preservatives, and additives derived from herbal or botanical sources.
  • a representative microcapsule embodiment has an outer cover, shell, or coating that envelopes a liquid or solid core region, and in certain embodiments, the microcapsule can have a generally spherical shape.
  • the ability of the additive to interact with other components of the tobacco formulation is reduced or eliminated, which can enhance the storage stability of the resulting product.
  • the core region which typically releases the additive when the outer shell undergoes some type of physical destruction, breakage, or other loss of physical integrity (e.g., through dispersion, softening, crushing, application of pressure, or the like), thereby provides for altering the sensory properties of the smokeless tobacco product.
  • the outer shell of the microcapsules is designed to rupture during use or is water soluble under conditions of normal use, such as under conditions of at least about 45 weight percent moisture based on the total weight of the smokeless tobacco product.
  • the shell region is not intended to break down during use and, instead, maintains its integrity and does not release the contents of the core region.
  • the outermost moisture-permeable container preferably has the form of a pouch or bag, such as the type commonly used for the manufacture of snus products.
  • a smokeless tobacco product configured for insertion into the mouth of a user of the product
  • the tobacco product comprising a water-permeable pouch containing a tobacco formulation, the tobacco formulation comprising a tobacco material and a plurality of microcapsules dispersed within the tobacco material.
  • the microcapsules preferably comprise an outer shell encapsulating an internal payload comprising an additive, such as water, flavorants (e.g., sweeteners or tobacco-containing flavorants), binders, colorants, pH adjusters, buffering agents, oral care additives, fillers, disintegration aids, humectants, antioxidants, preservatives, additives derived from herbal or botanical sources, or mixtures thereof.
  • an additive such as water, flavorants (e.g., sweeteners or tobacco-containing flavorants), binders, colorants, pH adjusters, buffering agents, oral care additives, fillers, disintegration aids, humectants, antioxidants, preservatives, additives derived from herbal or botanical
  • a smokeless tobacco product configured for insertion into the mouth of a user of the product
  • the tobacco product comprising a water-permeable pouch containing a tobacco formulation, the tobacco formulation comprising a tobacco material and a plurality of microcapsules dispersed within the tobacco material, the plurality of microcapsules comprising an outer shell encapsulating an internal payload comprising an additive selected from the group consisting of water, a flavorant, and mixtures thereof.
  • Preferred microencapsulated flavorants include tobacco-containing flavorants, such as tobacco extracts or particulate tobacco material, sweeteners (e.g., sweeteners containing neotame), and vanillin (optionally in a complexed form).
  • the microencapsulated additive is water
  • the moisture content of the tobacco formulation prior to use is preferably less than about 20 weight percent based on the total weight of the formulation, more preferably less than about 15 weight percent, and most preferably less than about 10 weight percent.
  • the present invention provides a smokeless tobacco product comprising a water-permeable pouch containing a tobacco formulation, the tobacco formulation comprising a tobacco material and a plurality of microcapsules dispersed within the tobacco material, the plurality of microcapsules comprising an outer shell encapsulating an internal payload comprising a flavorant selected from a group consisting of a sweetener composition comprising neotame, a tobacco-containing flavorant, and mixtures thereof, wherein the microencapsulated flavorant is present in an amount of at least about 1 percent based on the weight of the dry tobacco formulation, and wherein the outer shell of the microcapsules is watersoluble under conditions of at least about 45 weight percent moisture, based on the total weight of the formulation.
  • the invention provides a smokeless tobacco product comprising a water-permeable pouch containing a tobacco formulation, the tobacco formulation comprising a tobacco material and a plurality of rupturable microcapsules dispersed within the tobacco material, the plurality of rupturable microcapsules comprising an outer shell encapsulating an internal payload comprising water, wherein the moisture content of the tobacco formulation prior to rupture of the microcapsules is no more than about 20 weight percent based on the total weight of the formulation.
  • a smokeless tobacco product comprising a water-permeable pouch containing a tobacco formulation, the tobacco formulation comprising a tobacco material and a plurality of microcapsules dispersed within the tobacco material, the plurality of microcapsules comprising an outer shell encapsulating an internal payload comprising an additive selected from the group consisting of a filler material, a buffering agent, an additive derived from an herbal or botanical source, and mixtures thereof.
  • Filler materials include vegetable fiber materials such as sugar beet fiber materials, oats or other cereal grain, bran fibers, starch, or other modified or natural cellulosic materials.
  • the microencapsulated filler material is typically present in an amount of at least about 5 percent based on the weight of the dry formulation.
  • Preferred buffering agents buffer within a pH range of about 6 to about 10
  • exemplary buffering agents include metal hydroxides, metal carbonates, metal bicarbonates, or mixtures thereof.
  • the microencapsulated buffering agent is typically present in an amount of at least about 1 percent based on the dry weight of the formulation.
  • additives derived from herbal or botanical sources suitable for use in the invention are often in the form of an oil or extract.
  • Exemplary compounds that can be present in such additives include minerals, vitamins, isoflavones, phytoesterols, allyl sulfides, dithiolthiones, isothiocyanates, indoles, lignans, flavonoids, polyphenols, and carotenoids.
  • the invention provides a smokeless tobacco product comprising a water-permeable pouch containing a tobacco formulation, the tobacco formulation comprising a tobacco material and a plurality of microcapsules dispersed within the tobacco material, the plurality of microcapsules comprising an outer shell encapsulating an internal payload comprising a filler material, wherein the outer shell of the microcapsules is non-water soluble under conditions of at least about 45 weight percent moisture, based on the total weight of the formulation.
  • the tobacco-containing portion e.g., extruded or shaped tobacco products, tobacco contained within a pouch, and the like
  • the tobacco-containing portion is intended to be placed in the mouth of the tobacco user, such that the tobacco formulation within the tobacco-containing portion may be enjoyed by the user.
  • the outer shell of the microcapsules within the tobacco-containing portion may be acted upon by moisture within the mouth of the user, broken, crushed, or otherwise acted upon to release its contents.
  • the outer moisture-permeable pouch if present, may be removed from the user's mouth for disposal.
  • that outer pouch when present, may be manufactured from a dissolvable or dispersible material, such that the tobacco formulation and the pouch may be ingested by the user. Residual components of the outer shell of the microcapsules may be dispersed within the mouth of the user for ingestion or remain within the used pouch for disposal.
  • Processes for preparing a tobacco composition suitable for use as a smokeless tobacco composition are provided. These processes can be characterized as including a heat treatment step that can be viewed as a type of pasteurization adapted to degrade, destroy, or denature at least a portion of the microorganisms within the tobacco composition.
  • the process comprises providing a mixture comprising water and a tobacco material having a high moisture content (e.g., in the form of a slurry), such as a mixture comprising at least about 75% by weight water, based on the total weight of the mixture.
  • the mixture is subjected to a heat treatment step for a time and at a temperature adapted to pasteurize the material (e.g., heating the mixture to a temperature of at least about 60°C for a time sufficient to pasteurize the tobacco material).
  • a temperature adapted to pasteurize the material e.g., heating the mixture to a temperature of at least about 60°C for a time sufficient to pasteurize the tobacco material.
  • an amount of a base is added to the mixture sufficient to raise the pH of the mixture to the alkaline pH range (i.e., above 7.0), thereby forming a pH-adjusted mixture.
  • sufficient base is added to raise the pH of the mixture to at least about 8.5.
  • the base addition step and thereafter it is preferable to continue heating the pH-adjusted mixture (e.g., to a temperature of at least about 60°C) for a time sufficient for the pH of the mixture to drop at least about 0.5 pH unit following the base addition step.
  • the pH-adjusted mixture e.g., to a temperature of at least about 60°C
  • the process can further include the step of adding a salt to the mixture prior to or during the heat treatment.
  • the salt addition step can comprise adding about 1 to about 5% by weight of sodium chloride, based on the dry weight of the tobacco material.
  • the mixture can be cooled (e.g., to a temperature of less than about 35°C).
  • a humectant can be added during or following the cooling step.
  • the pH of the mixture can be readjusted with additional base (e.g., to a pH of about 8.0 or less), and the mixture can be dried (e.g., to a moisture content of no more than about 15% by weight, based on the total weight of the dried tobacco material).
  • Flavorants, sweeteners, and additional moisture can be added to the dried tobacco material as desired (e.g., in an amount sufficient to raise the moisture content of the tobacco material to at least about 25% by weight).
  • the process includes: providing a slurry comprising water and a tobacco material, the slurry comprising at least about 80% by weight water, based on the total weight of the slurry; heating the slurry to a temperature of at least about 70°C for at least about 30 minutes (or other suitable time that effectively provides the desired treatment); adding an amount of a base to the slurry sufficient to raise the pH of the slurry to at least about 9.0, thereby forming a pH-adjusted slurry; continuing to heat the pH-adjusted slurry to a temperature of at least about 60°C for at least about 1.5 hours (or other suitable time that effectively provides the desired treatment); cooling the pH-adjusted slurry to about ambient temperature, the pH-adjusted slurry having a pH of at least about 8 at the time the cooling step begins; adding a humectant to the pH-adjusted slurry during or after the cooling step; and drying the pH-a
  • Yet another exemplary process for preparing a tobacco composition suitable for use as a smokeless tobacco composition is provided.
  • This process also includes a heat treatment step that can be viewed as a type of pasteurization treatment.
  • the process comprises providing a moist tobacco material having a first moisture content (e.g., having a moisture content of at least about 30% by weight, based on the total weight of the moist tobacco material), and heating the moist tobacco at a temperature (e.g., a temperature of at least about 85°C) and for a time sufficient to pasteurize the tobacco material while maintaining the moist tobacco material at the same approximate moisture level (i.e., the first moisture content) or higher (e.g., a moisture content at a level of at least about 30% by weight).
  • a first moisture content e.g., having a moisture content of at least about 30% by weight, based on the total weight of the moist tobacco material
  • a temperature e.g., a temperature of at least about 85°C
  • an amount of a base and water can be added to the moist tobacco material in an amount sufficient to raise the pH of the moist tobacco material to a pH in the alkaline pH range (e.g., at least about 8.7) and raise the moisture content of the tobacco material to a second moisture content (e.g., to at least about 40% by weight), thereby forming a pH-adjusted moist tobacco material.
  • a base and water can be added to the moist tobacco material in an amount sufficient to raise the pH of the moist tobacco material to a pH in the alkaline pH range (e.g., at least about 8.7) and raise the moisture content of the tobacco material to a second moisture content (e.g., to at least about 40% by weight), thereby forming a pH-adjusted moist tobacco material.
  • the process can include continuing to heat the pH-adjusted moist tobacco material at an elevated temperature (e.g., a temperature of at least about 55°C) for a time sufficient for the pH of the moist tobacco material to decrease to a lower level within the alkaline pH range (e.g., to drop to less than about 8.5) while maintaining the moisture content at the same approximate moisture level (i.e., the second moisture content) or higher (e.g., at least about 40% by weight).
  • an elevated temperature e.g., a temperature of at least about 55°C
  • a time sufficient for the pH of the moist tobacco material to decrease to a lower level within the alkaline pH range (e.g., to drop to less than about 8.5) while maintaining the moisture content at the same approximate moisture level (i.e., the second moisture content) or higher (e.g., at least about 40% by weight).
  • the tobacco material can then be dried under suitable conditions of time and temperature to reduce the moisture content of the tobacco material (e.g., at a temperature of at least about 35°C for a time sufficient to reduce the moisture content of the tobacco to less than about 35% by weight) while maintaining a pH in the alkaline range (e.g., at least about 7.6).
  • the process can further comprise the step of adding a sweetener composition to the dried tobacco material.
  • the moist tobacco material can comprise a mixture of a dry tobacco material having a moisture content of less than about 15% by weight and an aqueous solution of a salt, and such a mixture can be prepared by heating the dry tobacco material to an elevated temperature (e.g., at least about 60°C) and adding an aqueous salt solution (e.g., a sodium chloride solution) to the heated tobacco material.
  • an elevated temperature e.g., at least about 60°C
  • an aqueous salt solution e.g., a sodium chloride solution
  • the step of continuing to heat the pH-adjusted moist tobacco material comprises heating the pH-adjusted moist tobacco material at a temperature and moisture level sufficient to maintain a pH reduction rate of about 0.05 to about 0.15 pH units per hour.
  • a process for preparing a tobacco composition suitable for use as a smokeless tobacco composition comprising: providing a moist tobacco material comprising a mixture of a tobacco material and a salt solution, the moist tobacco material having a moisture content of about 30% to about 40% by weight, based on the total weight of the moist tobacco material; heating the moist tobacco to a temperature of at least about 90°C for at least about 1 hour (or other suitable time that effectively provides the desired treatment) to pasteurize the tobacco material while maintaining the moisture content at a level of about 30% to about 40% by weight; adding an amount of a base and water to the moist tobacco material sufficient to raise the pH of the slurry to at least about 8.7 and raise the moisture content to at least about 45% by weight, thereby forming a pH-adjusted moist tobacco material; continuing to heat the pH-adjusted moist tobacco material to a temperature of at least about 65°C for at least about 1 hour (or other suitable time that effectively provides the desired treatment) while
  • the smokeless tobacco product can include tobacco compositions in other forms and can include additives encapsulated or otherwise segregated from other components of the tobacco formulation using methods other than microencapsulation.
  • the tobacco product 10 includes a moisture-permeable container in the form of a pouch 12, which contains a solid tobacco filler material 14 of a type described herein.
  • the smokeless tobacco product also comprises a plurality of microcapsules 16 dispersed within the tobacco filler material 14, the microcapsules containing an additive such as described in greater detail below.
  • the tobacco product 10 includes a container pouch 20.
  • a preferred pouch comprises a moisture permeable mesh material.
  • the illustrated container pouch 20 is sealed closed along its length at an overlap region 22. The overlap region may be formed by sealing the bottom portion of one edge of the pouch 20 over the top portion of the opposite edge of the pouch (e.g., by heat sealing, suitable adhesive, or other suitable means).
  • a solid tobacco material 14 is disposed within the pouch 20, and a plurality of microcapsules 16 are dispersed within the tobacco material.
  • Also disposed within the pouch 20 is an optional larger spherical capsule 26.
  • the spherical capsule 26 has an outer shell 28 that contains an inner payload 30.
  • the tobacco product 10 includes a container pouch 34.
  • a preferred pouch comprises a moisture permeable mesh material.
  • the illustrated pouch 34 is sealed shut at its ends 36, 38 (e.g., by heat-sealing, a suitable adhesive, or other suitable sealing means).
  • a tobacco material 14 is contained within the pouch 34, and dispersed within the tobacco material are a plurality of microcapsules 16.
  • Also contained within the pouch 34 are two optional larger spherical capsules 40 and 42. Each of the spherical capsules 40, 42 has an outer shell 44, 46 that contains an inner payload 50, 52.
  • An optional dissolvable strip of a flavored material shown as a flavor sheet 56 is included in the pouch as well.
  • a strip of flavored material such as the flavor sheet 56 may be disposed in a pouch 34 without any larger capsules being present.
  • the tobacco product 10 includes an outer pouch 12 and an inner pouch 60.
  • Preferred pouches each comprise a moisture permeable mesh material, and the pouches 12, 60 are illustrated without showing a seam that may be present in pouches containing a flavor agent member such as a larger capsule (e.g., a macro-sized capsule), as well as pouches without larger capsules.
  • the outer pouch 12 forms a continuous container around a tobacco material 14 having microcapsules 16 dispersed therein.
  • the inner pouch 60 is disposed within the outer pouch 12 and is generally surrounded by the tobacco material 14, although the inner pouch 60 may also be in contact with, adhered to, or formed continuously with the outer pouch 12.
  • the inner pouch 60 contains a larger capsule 62 with an outer shell 66 and an inner payload 68. Although the inner pouch 60 is shown with interior space surrounding the capsule 62 for purposes of clarity in illustration, in preferred aspects of this embodiment the inner pouch 60 will be closely fitted around its contents.
  • the inner pouch may contain a flavor strip such as a dissolvable flavor strip (for example, a Cinnamon Oral Care Strip available in Listerine PocketPaks from Pfizer, Inc.).
  • the smokeless tobacco product of the invention can include at least one additive or ingredient of the tobacco composition in a form that physically separates or segregates, to a certain extent, the additive from one or more other components of the tobacco composition.
  • the functional advantage of such a separation can vary, but typically involves the minimization or elimination of chemical interaction between the additive and other components of the tobacco composition during conditions of normal storage and/or use. Separation of certain additives can thus enhance storage stability of the resulting tobacco product and/or preserve the desirable sensory characteristics of the product.
  • the means of separation can take various forms, including encapsulation of the additive or use of the additive in various forms such as beads, pellets, rods, films, strands, layered or laminate structures, sheets, strips, or other shaped items.
  • the additive can be dispersed within a matrix material and shaped into a desired form.
  • the additive can also be physically entrapped or encapsulated within a seam of a pouch housing the tobacco composition.
  • the additive is in an encapsulated form comprising an outer wall or barrier structure and an inner region containing the additive.
  • certain embodiments of the invention include a plurality of microcapsules, the microcapsules including an inner or core region encapsulated by an outer shell region.
  • 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.
  • the outer shell or coating of the microcapsules serves as a barrier between the payload and the tobacco composition of the smokeless tobacco product.
  • this barrier can be permanent, meaning it is intended to remain in place as a barrier during the life of the product, or temporary, meaning the barrier is designed to stop serving as a barrier, and thereby release the payload, under certain conditions of product use.
  • the additive in the core region is released when the outer shell undergoes some type of physical destruction, breakage, or other loss of physical integrity (e.g., through disintegration, softening, crushing, application of pressure, or the like), and thereby alters the sensory or functional properties of the smokeless tobacco product during use of the product.
  • the microcapsules may be incorporated within the pouch along with the tobacco formulation, and during use, contact of the microcapsules with moisture present in the user's mouth may cause the microcapsules to soften, lose their physical integrity, and release the additive within the user's mouth.
  • the microcapsules may be purposefully crushed by application of pressure to release the additive.
  • the shell is not designed to release the additive under conditions of normal use, such as in the case of microencapsulated filler materials.
  • 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.
  • the microcapsules undergo destruction during use of the product, and the contents of the microcapsules are introduced into the mouth of the user.
  • the contents of the microcapsules and substantial amounts of the tobacco formulation have been ingested by the human subject, and the pouch may be removed from the mouth of the human subject for disposal.
  • Exemplary types of additives that can be separated from other components of the tobacco formulation by encapsulation (e.g., included in the payload of microcapsules) or other techniques include water, flavorants, tobacco material (e.g., tobacco material in particulate form or in the form of a tobacco extract), organic and inorganic fillers (e.g., grains, processed grains, puffed grains, maltodextrin, dextrose, calcium carbonate, calcium phosphate, corn starch, lactose, manitol, xylitol, sorbitol, finely divided cellulose, and the like), binders (e.g., povidone, sodium carboxymethylcellulose and other modified cellulosic types of binders, sodium alginate, xanthan gum, starch-based binders, gum arabic, lecithin, and the like), pH adjusters or buffering agents (e.g., metal hydroxides, preferably alkali metal hydroxides such as sodium hydroxide and potassium hydro
  • Exemplary 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 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.
  • Flavorants may be natural or synthetic, and the character of these flavors imparted thereby may be described, without limitation, as fresh, sweet, herbal, confectionary, floral, fruity or spice.
  • 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, Leffingwell et al., Tobacco Flavoring for Smoking Products, R. J. Reynolds Tobacco Company (1972 ). Flavorings also may include components that are considered moistening, cooling or smoothening agents, such as eucalyptus.
  • These flavors may be provided neat (i.e., alone) or in a composite (e.g., spearmint and menthol, or orange and cinnamon).
  • Composite flavors may be combined in a single microcapsule as a mixture, or as separate components of separate microcapsules.
  • the segregated additive such as an additive in the payload of the microcapsules
  • is a tobacco-based flavorant composition such as a flavorant comprising particulate tobacco material or a tobacco extract (e.g., an aqueous tobacco extract in solid form).
  • a tobacco-based flavorant composition such as a flavorant comprising particulate tobacco material or a tobacco extract (e.g., an aqueous tobacco extract in solid form).
  • a microencapsulated flavorant can provide the smokeless tobacco formulation with extended release flavor characteristics. Some forms of smokeless tobacco formulations deliver a strong sensory profile. By microencapsulating a portion of the tobacco material in the formulation, a milder sensory experience can be achieved.
  • Microencapsulation of a tobacco flavorant can also extend the sensory experience by providing a slow continuous release of tobacco flavor over time as the product resides in the mouth.
  • Preferred microencapsulated tobacco flavorants will provide extended release of the tobacco flavorant under conditions of normal use of the smokeless tobacco product, such as under conditions of a 45% or greater moisture level, based on the total weight of the smokeless tobacco product.
  • Extracts useful as components of the tobacco formulation can be employed. Extracts can be used in solid form (e.g., spray-dried or freeze-dried form), in liquid form, in semi-solid form, or the like.
  • Exemplary tobacco extracts and extraction techniques are set forth, for example, in US Pat. Nos. 4,150,677 to Osborne, Jr. et al. ; 4,967,771 to Fagg et al. ; 5,005,593 to Fagg et al. ; 5,148,819 to Fagg ; and 5,435,325 to Clapp et al. .
  • Various tobacco extraction and reconstitution methodologies are set forth in US Pat. Nos.
  • Suitable known reconstituted tobacco processing techniques such as paper-making techniques or casting-type processes, can be employed. See, for example, the types of paper-making processes set forth in US Pat. Nos. 3,398,754 to Tughan ; 3,847,164 to Mattina ; 4,131,117 to Kite ; 4,270,552 to Jenkins ; 4,308,877 to Mattina ; 4,341,228 to Keritsis ; 4,421,126 to Gellatly ; 4,706,692 to Gellatly ; 4,962,774 to Thomasson ; 4,941,484 to Clapp ; 4,987,906 to Young ; 5,056,537 to Brown ; 5,143,097 to Sohn ; 5,159,942 to Brinkley et al.
  • the segregated additive such as an additive in the payload of the microcapsules, comprises vanillin as a flavorant.
  • vanillin as a flavorant.
  • the microencapsulated vanillin can be in the form of a complexed vanillin that releases vanillin over time, such as ethylvanillin glucoside.
  • the microencapsulated vanillin will provide extended release of vanillin during conditions of normal use, such as under conditions of a 45% or greater moisture level.
  • the segregated additive such as an additive in the payload of the microcapsules
  • SUCRASWEET® is a combination of neotame, acesulfame potassium, and maltitol. It is possible for certain sweeteners, particularly sweeteners containing neotame, to exhibit a lack of stability under certain conditions, such as basic pH. Certain sweeteners can chemically breakdown to form byproducts that can alter the sensory characteristics of the smokeless tobacco formulation in an undesirable manner, such as by increasing bitterness.
  • microencapsulated sweetener flavorant By microencapsulating such sweeteners, breakdown of the sweetener flavorant can be reduced or avoided and the desired sensory profile of the smokeless tobacco product can be preserved for a longer period of time.
  • the microencapsulated sweetener flavorant will provide a continuous and extended release of flavorant and exhibit water-solubility during conditions of normal use, such as under conditions of a 45% or greater moisture level.
  • the segregated additive such as an additive in the payload of the microcapsules
  • water which serves to increase the moisture level of the smokeless tobacco product.
  • the microencapsulated water preferably provides a rapid release of water.
  • the outer shell of the microcapsules in this embodiment are preferably designed to rupture during use, such as by crushing of the microcapsules by the user, thereby resulting in rapid release of water in the product at any time during or before use of the product.
  • microencapsulated water is particularly suitable for tobacco formulations having a moisture content, prior to use (e.g., during storage), of less than about 20 weight percent, frequently less than about 15 weight percent, and often less than about 10 weight percent, based on the total weight of the tobacco formulation.
  • a typical moisture content range for the tobacco formulation in this embodiment is about 5 to about 20 weight percent.
  • the additive can also be in the form of isolated components (e.g., oils or extracts) from botanical or herbal sources, such as potato peel, grape seed, ginseng, gingko biloba, Saint John's Wort, saw palmetto, green tea, black tea, black cohosh, cayenne, chamomile, cranberry, echinacea, garlic, evening primrose, feverfew, ginger, goldenseal, hawthorn, kava, licorice, milk thistle, uva ursi, or valerian.
  • botanical or herbal sources such as potato peel, grape seed, ginseng, gingko biloba, Saint John's Wort, saw palmetto, green tea, black tea, black cohosh, cayenne, chamomile, cranberry, echinacea, garlic, evening primrose, feverfew, ginger, goldenseal, hawthorn, kava, licorice, milk thistle, uva ursi, or vale
  • Additives such as the oils and extracts noted above, often include compounds from various classes known to provide certain bioactive effects, such as minerals, vitamins, isoflavones, phytoesterols, allyl sulfides, dithiolthiones, isothiocyanates, indoles, lignans, flavonoids, polyphenols, and carotenoids.
  • Exemplary compounds found in these types of extracts or oils include ascorbic acid, peanut endocarb, resveratrol, sulforaphane, beta-carotene, lycopene, lutein, co-enzyme Q, carnitine, quercetin, kaempferol, and the like.
  • the oil or extract additives used in the present invention may comprise, without limitation, any of the compounds and sources set forth herein, including mixtures thereof.
  • Certain additives of this type are sometimes referred to as dietary supplements, nutraceuticals, "phytochemicals” or "functional foods”.
  • These types of additives are sometimes defined in the art as encompassing substances typically available from naturally-occurring sources (e.g., plant materials) that provide one or more advantageous biological effects (e.g., health promotion, disease prevention, or other medicinal properties), but are not classified or regulated as drugs.
  • the microencapsulated additive can add advantageous biological functions to the product, such as immune system boosting effects, antioxidant effects, and the like. Microencapsulation can increase the probability that the bioactive additive will remain in an active form until the product is used. In preferred embodiments, the microencapsulated bioactive additive will provide a continuous and extended release of the additive and exhibit water-solubility during conditions of normal use, such as at a 45% or greater moisture level.
  • the segregated additive such as an additive in the payload of the microcapsules, may comprise a buffering agent, such as sodium bicarbonate and/or sodium carbonate.
  • a buffering agent such as sodium bicarbonate and/or sodium carbonate.
  • Suitable buffering agents typically buffer at a pH of at least about 6.0, often at least about 7.0, and frequently at least about 7.5.
  • Suitable buffering agents typically buffer at a pH of less than about 10.0, often less than about 9.5, and frequently less than about 9.0.
  • a microencapsulated buffering agent that provides extended release can aid in maintaining the product pH in a desired range, which results in a more consistent sensory profile for the product and extends shelf-life.
  • the microencapsulated buffering agent will release buffering agent as the temperature of the product exceeds a certain temperature threshold (e.g., about 80°F or about 27°C) or when the product pH decreases to an undesirably low level (e.g., 7.3 or less).
  • a segregated additive such as an additive in the payload of the microcapsules, is a filler and comprises a vegetable fiber material. Certain filler materials can impart less desirable sensory characteristics to the smokeless tobacco product.
  • certain fillers may have a grainy or mealy texture or taste. Microencapsulation, or otherwise achieving physical separation, of the filler can serve to minimize the effect of the sensory characteristics of the filler on the overall sensory profile of the smokeless tobacco product. In this manner, fillers can be advantageously employed when a milder product taste is desired without imparting any taste off-notes.
  • a particularly preferred filler is FIBREX® brand filler available from International Fiber Corporation, which is a fiber material derived from sugar beets.
  • Other suitable filler materials include oats or other cereal grain, bran fibers, starch, or other modified or natural cellulosic materials.
  • the microencapsulated filler is in a non-water soluble form under conditions of normal use, such as at a moisture level of 45% or greater by weight.
  • the outer shell of the microcapsules it is preferable for the outer shell of the microcapsules to lose physical integrity under conditions of normal use in the mouth of the user, such as under conditions of relatively high moisture (e.g., above 45% moisture based on the total weight of the smokeless tobacco product). In other embodiments, it is preferably for the outer shell of the microcapsules to lose physical integrity when the smokeless tobacco product reaches a certain pH, such as a pH at or below about 7.3, or a certain temperature, such as at or above about 27°C.
  • the microcapsules are designed to rupture when acted upon by physical force or pressure by the user, either through pressure applied by hand prior to insertion of the product in the mouth or through pressure applied after the product is inserted into the oral cavity (e.g., pressure applied by the tongue or teeth).
  • the microcapsule payload can have a form that can vary.
  • the payload has the form of a liquid or gel, although the payload can be in the form of a solid (e.g., a crystalline material or a dry powder).
  • the payload is a mixture of the additive (e.g., a flavoring agent) and a diluting agent or carrier (e.g., water).
  • a preferred diluting agent is a triglyceride, such as a medium chain triglyceride, and more particularly a food grade mixture of medium chain triglycerides. See, for example, Radzuan et al., Porim Bulletin, 39, 33-38 (1999 ).
  • the amount of additive and diluting agent within the microcapsule may vary. In some instances, the diluting agent may be eliminated altogether, and the entire payload can be composed of the additive. Alternatively, the payload can be almost entirely comprised of diluting agent, and only contain a very small amount of relatively potent additive.
  • the composition of the mixture of additive and diluting agent is in the range of about 5 percent to about 99 percent additive, and more preferably in the range of about 5 to about 75 percent additive, and most preferably in the range of about 10 to about 25 percent additive, by weight based on the total weight of the payload, with the balance being diluting agent. The exact amount of additive will depend on several factors including the additive type and the desired sensory profile of the product.
  • the crush strength of the microcapsules is sufficient to allow for normal handling and storage without significant degree of premature or undesirable breakage. Providing capsules that possess both suitable integrity during storage and the ability to rupture or otherwise break down at the time of use can be determined by experimentation, depending upon factors such as capsule size and type, and is a matter of design choice. See, for example, U.S. Pat. Pub. No. 2007/0068540 to Thomas et al. , which is incorporated herein by reference.
  • An exemplary microcapsule may include an outer shell incorporating a material such as wax, gelatin, cyclodextrin, or alginate, and an inner payload incorporating an aqueous or non-aqueous liquid (e.g., a solution or dispersion of at least one flavoring ingredient within water or an organic liquid such as an alcohol or oil; or a mixture of water and a miscible liquid like alcohol or glycerin).
  • aqueous or non-aqueous liquid e.g., a solution or dispersion of at least one flavoring ingredient within water or an organic liquid such as an alcohol or oil; or a mixture of water and a miscible liquid like alcohol or glycerin.
  • a plurality of such microcapsules may be incorporated within the pouch along with the tobacco formulation; and during use of the product, a crushing or other physical destruction of the microcapsules may allow the microcapsules to release the additive contained therein to provide suitable moistening of components of the tobacco formulation, as well as provide other functional benefits such as enhanced taste.
  • a suitable number of capsules having outer shells comprising a food grade waxy substance and an inner payload comprising water may be incorporated within a pouch such that, upon rupture of those capsules, sufficient water is released to provide a desired moistening effect upon the tobacco formulation.
  • microcapsules used in the smokeless tobacco product of the invention may be uniform or varied in size, weight, and shape, and such properties of the microcapsules will depend upon the desired properties of the smokeless tobacco product.
  • a representative microcapsule is generally spherical in shape.
  • suitable microcapsules may have other types of shapes, such as generally rectilinear, oblong, elliptical, or oval shapes.
  • Exemplary microcapsules may have diameters of less than about 100 microns, such as microcapsules having diameters in the range of about 1 to about 40 microns, or about 1 micron to about 20 microns.
  • the number of microcapsules incorporated into the smokeless tobacco product can vary, depending upon factors such as the size of the microcapsules, the character or nature of the additive in the payload, the desired attributes of the smokeless tobacco product, and the like.
  • the number of microcapsules incorporated within smokeless tobacco product can exceed about 5, can exceed about 10, can exceed about 20, can exceed about 40, and can even exceed about 100. In certain embodiments, the number of capsules can be greater than about 500, and even greater than about 1,000.
  • the total weight of the microcapsules contained within the smokeless tobacco product may vary, but is typically greater than about 10 mg, often greater than about 20 mg, and can be greater than about 30 mg.
  • the total weight of the microcapsules is typically less than about 200 mg, often less than about 100 mg, and can be less than about 50 mg.
  • the relative weight of the microcapsules in the pouch may vary. Typically, the dry weight of the tobacco within the smokeless tobacco product is greater than the weight provided by microcapsule components. However, the weight of microcapsule components can range from about 10 percent to about 75 percent, often about 20 percent to about 50 percent, based on the combined weight of microcapsule components and dry weight of tobacco.
  • microcapsules of different sizes and/or of different types may be incorporated within the product.
  • different microcapsules may be incorporated into the product to provide desired properties (e.g., mouthfeel, flavor, other sensory effect), and/or to provide release of encapsulated components at different times during the use of the product.
  • a first flavoring ingredient may be released from a first set of microcapsules upon initial introduction of the product to a user's mouth, and a second flavoring ingredient, contained in a second set of microcapsules, may not be released until a later time (e.g., a semi-soluble coating of the second capsules takes longer to rupture than the coating of the first capsule set).
  • microcapsules of the invention can be formed using any microencapsulating technology known in the art.
  • the microcapsules can be formed using any of various chemical encapsulation techniques such as solvent evaporation, solvent extraction, organic phase separation, interfacial polymerization, simple and complex coacervation, in-situ polymerization, liposome encapsulation, and nanoencapsulation.
  • chemical encapsulation techniques such as solvent evaporation, solvent extraction, organic phase separation, interfacial polymerization, simple and complex coacervation, in-situ polymerization, liposome encapsulation, and nanoencapsulation.
  • physical methods of encapsulation could be used, such as spray coating, pan coating, fluid bed coating, annular jet coating, spinning disk atomization, spray cooling, spray drying, spray chilling, stationary nozzle coextrusion, centrifugal head coextrusion, or submerged nozzle coextrusion.
  • Coacervation is a colloid phenomenon that begins with a solution of a colloid in an appropriate solvent. Depending on the nature of the colloid, various changes can bring about a reduction of the solubility of the colloid. As a result of this reduction, a significant portion of the colloid can be separated out into a new phase, thus forming a two phase system, with one being rich and the other being poor in colloid concentration.
  • the colloid-rich phase in a dispersed state appears as amorphous liquid droplets called coacervate droplets. Upon standing, these coalesce into one clear homogenous colloid-rich liquid layer, known as the coacervate layer, which can be deposited so as to produce the wall material of the resultant microcapsules.
  • Simple coacervation can be effected either by mixing two colloidal dispersions, one having a high affinity for water, or it can be induced by adding a strongly hydrophilic substance such as alcohol or sodium sulfate.
  • a water soluble polymer is concentrated in water by the action of a water miscible, non-solvent for the emerging polymer (e.g., gelatin) phase.
  • Ethanol, acetone, dioxane, isopropanol and propanol are exemplary solvents that can cause separation of a coacervate such as gelatin, polyvinyl alcohol, or methyl cellulose.
  • Phase separation can be effected by the addition of an electrolyte such as an inorganic salt to an aqueous solution of a polymer such as gelatin, polyvinyl alcohol, or carboxymethylcellulose.
  • Complex coacervation can be induced in systems having two dispersed hydrophilic colloids of opposite electric charges. Neutralization of the overall positive charges on one of the colloids by the negative charge on the other is used to bring about separation of the polymer-rich complex coacervate phase.
  • the gelatingum arabic (gum acacia) system is one known complex coacervation system.
  • Organic phase separation is sometimes more simply referred to as "water-in-oil" microencapsulation.
  • the polar core is dispersed into an oily or nonpolar continuous medium.
  • the wall material is then dissolved in this continuous medium.
  • the outer wall or shell material and solvents used to form the microcapsules of the invention can vary.
  • Classes of materials that are typically used as wall or shell materials include proteins, polysaccharides, starches, waxes, fats, natural and synthetic polymers, and resins.
  • Exemplary materials for use in the microencapsulation process used to form the microcapsules include gelatin, acacia (gum arabic), polyvinyl acetate, potassium alginate, carob bean gum, potassium citrate, carrageenan, potassium polymetaphosphate, citric acid, potassium tripolyphosphate, dextrin, polyvinyl alcohol, povidone, dimethylpolysiloxane, dimethyl silicone, refined paraffin wax, ethylcellulose, bleached shellac, modified food starch, sodium alginate, guar gum, sodium carboxymethylcellulose, hydroxypropyl cellulose, sodium citrate, hydroxypropylmethylcellulose, sodium ferrocyanide, sodium polyphosphates, locust bean gum, methylcellulose, sodium trimetaphosphate, methyl ethyl cellulose, sodium tripolyphosphate, microcrystalline wax, tannic acid, petroleum wax, terpene resin, tragacanth, polyethylene, xanthan gum, and polyethylene glycol
  • Microcapsules are commercially available, and exemplary types of microcapsule technologies are of the type set forth in Gutcho, Microcapsules and Microencapsulation Techniques (1976 ); Gutcho, Microcapsules and Other Capsules Advances Since 1975 (1979 ); Kondo, Microcapsule Processing and Technology (1979 ); Iwamoto et al., AAPS Pharm. Sci. Tech. 2002 3(3): article 25 ; U.S. Pat. Nos. 3,550,598 to McGlumphy ; 4,889,144 to Tateno et al. ; 5,004,595 to Cherukuri et al. ; 5,690,990 to Bonner ; 5,759,599 to Wampler et al.
  • microcapsules are available from sources such as Microtek Laboratories of Dayton, Ohio.
  • Exemplary types of commercially available microencapsulating techniques include those marketed under the trade names ULTRASEALTM and PERMASEALTM available from Givaudan headquartered in Vernier, Switzerland.
  • embodiments of the smokeless tobacco product may include larger capsules containing any of the additives described herein for use in microcapsules.
  • Exemplary smaller spherical capsules have diameters of at least about 0.5 mm, generally at least about 1 mm, often at least about 2 mm, and frequently at least about 3 mm.
  • Exemplary larger spherical capsules have diameters of less than about 6 mm, and often less than about 5 mm.
  • Exemplary smaller individual capsules weigh at least about 5 mg, often at least about 15 mg, and frequently at least about 25 mg.
  • Exemplary larger individual capsules weigh less than about 75 mg, generally less than about 65 mg, and often less than about 55 mg.
  • capsules are of the type commercially available as “Momints” by Yosha! Enterprises, Inc. and “Ice Breakers Liquid Ice” from The Hershey Company. Representative types of capsules also have been incorporated in chewing gum, such as the type of gum marketed under the tradename "Cinnaburst” by Cadbury Adams USA. Representative types of capsules and components thereof also are set forth in US Pat. Nos. 3,339,558 to Waterbury ; 3,390,686 to Irby, Jr. et al. ; 3,685,521 to Dock ; 3,916,914 to Brooks et al. ; 4,889,144 to Tateno et al. 6,631,722 to MacAdam et al.
  • the capsules may be colored, provided with smooth or rough surfaces, have rigid or pliant shells, have brittle or durable shells, or other desired features or characters.
  • the smokeless tobacco product can include other flavorants in the form of beads, pellets, rods, strands, sheets, strips, or other shaped items designed to deliver a pre-determined, concentrated amount of a flavoring ingredient to the user.
  • Such forms typically include a carrier material (i.e., a matrix material) and a flavorant dispersed therein, and allow for controlled delivery of the flavorant.
  • a carrier material i.e., a matrix material
  • flavorant dispersed therein i.e., a matrix material
  • representative types of materials and ingredients useful for the manufacture of essentially water insoluble flavored beads, strands or pellets may be found within the filters of cigarettes available as Camel Dark Mint, Camel Mandarin Mint, Camel Spice Crema, Camel Izmir Stinger, Camel Spice Twist, Camel Mandalay Lime and Camel Aegean Spice by R. J. Reynolds Tobacco Company.
  • At least one flavored strip, piece or sheet of flavored water dispersible or water soluble material may be disposed within each pouch as shown in FIG. 3 .
  • 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 .
  • At least one larger capsule may be enclosed within a small moisture permeable mesh pouch that is in turn contained within the outer mesh container of the smokeless tobacco product.
  • the tobacco formulation within the pouch may be segregated from at least one of the capsules also contained within that pouch, as shown in FIG. 4 .
  • the tobaccos may include types of tobaccos such as flue-cured tobacco, burley tobacco, Oriental tobacco, Maryland tobacco, dark tobacco, dark-fired tobacco, dark air cured (e.g., passanda, cubano, jatin and bezuki tobaccos) or light air cured (e.g., North Wisconsin and galpoa tobaccos), and Rustica tobaccos, as well as other rare or specialty tobaccos.
  • types of tobaccos such as flue-cured tobacco, burley tobacco, Oriental tobacco, Maryland tobacco, dark tobacco, dark-fired tobacco, dark air cured (e.g., passanda, cubano, jatin and bezuki tobaccos) or light air cured (e.g., North Wisconsin and galpoa tobaccos), and Rustica tobaccos, as well as other rare or specialty tobaccos.
  • Descriptions of various types of tobaccos, growing practices, harvesting practices and curing practices are set forth in Tobacco Production, Chemistry and Technology, Davis et al. (Eds.) (1999 ). See, also
  • 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. Int., 20 (2003) 467-475 and U.S. Pat. No. 6,895,974 to Peele .
  • Representative techniques and conditions for air curing tobacco are set forth in Roton et al., Beitrage Tabakforsch. Int., 21 (2005) 305-320 and Staaf et al., Beitrage Tabakforsch.
  • Tobacco products of the present invention may incorporate a single type of tobacco (e.g., in a so-called "straight grade" form).
  • the tobacco within a tobacco product 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 within a tobacco product also may have a so-called "blended" form.
  • the tobacco within a tobacco product 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).
  • a representative blend may incorporate about 30 to about 70 parts burley tobacco (e.g., lamina, or lamina and stem), and about 30 to about 70 parts flue cured tobacco (e.g., stem, lamina, or lamina and stem) on a dry weight basis.
  • exemplary tobacco blends incorporate about 75 parts flue-cured tobacco, about 15 parts burley tobacco, and about 10 parts Oriental tobacco; or about 65 parts flue-cured tobacco, about 25 parts burley tobacco, and about 10 parts Oriental tobacco; or about 65 parts flue-cured tobacco, about 10 parts burley tobacco, and about 25 parts Oriental tobacco; on a dry weight basis.
  • the tobacco material can have the form of processed tobacco parts or pieces, cured and aged tobacco in essentially natural lamina or stem form, a tobacco extract, extracted tobacco pulp (e.g., using water as a solvent), or a mixture of the foregoing (e.g., a mixture that combines extracted tobacco pulp with granulated cured and aged natural tobacco lamina).
  • the tobacco that is used for the tobacco product most preferably includes tobacco lamina, or tobacco lamina and stem mixture. Tobacco mixtures incorporating a predominant amount of tobacco lamina, relative to tobacco stem, are preferred. Most preferably, the tobacco lamina and stem are used in an unextracted form, that is, such that the extractable portion (e.g., the water soluble portion) is present within the unextractable portion (e.g., the tobacco pulp) in a manner comparable to that of natural tobacco provided in a cured and aged form. Most preferably, the tobacco is not provided in a reconstituted form, extruded form, or any form that has resulted from extraction and recombination of components of that tobacco.
  • 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)
  • the tobacco product optionally may incorporate tobacco that has been fermented. See, also, the types of tobacco processing techniques set forth in PCT WO 05/063060 to Atchley et al. .
  • the tobacco material may be cased and dried, and then ground to the desired form.
  • the tobacco material may be cased with an aqueous casing containing components such as sugars (e.g., fructose, glucose, and sucrose), humectants (e.g., glycerin and propylene glycol), flavoring ingredients (e.g., cocoa and licorice), and the like.
  • Non-aqueous casing components preferably are applied to the tobacco in amounts of about 1 percent to about 15 percent, based on the dry weight of the tobacco.
  • the tobacco used for the manufacture of the tobacco product preferably is provided in a shredded, ground, granulated, fine particulate, or powder form.
  • 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 Tyler mesh, generally are sized to pass a screen of about 20 Tyler mesh, often are sized to pass through a screen of about 50 Tyler mesh, frequently are sized to pass through a screen of about 60 Tyler mesh, may even be sized to pass through a screen of 100 Tyler mesh, and further may be sized so as to pass through a screen of 200 Tyler mesh.
  • 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 Tyler mesh, but not through a 60 Tyler mesh. If desired, differently sized pieces of granulated tobacco may be mixed together.
  • the very finely divided tobacco particles or pieces suitable for snus products have a particle size greater than -8 Tyler mesh, often -8 to +100 Tyler mesh, frequently -18 to +60 Tyler mesh.
  • 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 relative amount of tobacco within the tobacco formulation may vary.
  • the amount of tobacco within the tobacco formulation is at least about 25 percent or at least about 30 percent, on a dry weight basis of the formulation.
  • the amounts of other components within the tobacco formulation may exceed about 40 percent, on a dry weight basis.
  • a typical range of tobacco material within the formulation is about 30 to about 40 weight percent.
  • the moisture content of the tobacco formulation prior to use by a consumer of the formulation may vary. Typically, the moisture content of the tobacco formulation, 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. Certain types of tobacco formulations have moisture contents, prior to use, of less than about 15 weight percent, frequently less than about 10 weight percent, and often less than about 5 weight percent. For certain tobacco products, such as those incorporating snus-types of tobacco compositions, the moisture content may exceed 20 weight percent, and often may exceed 30 weight percent. For example, a representative snus-type product may possess a tobacco composition exhibiting a moisture content of about 25 weight percent to about 50 weight percent, preferably about 30 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, mixers available as FKM130, FKM600, FKM1200, FKM2000 and FKM3000 from Littleford Day, Inc., Plough Share types of mixer cylinders, and the like.
  • 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 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 9, and often will not exceed about 8.5.
  • a representative tobacco formulation exhibits a pH of about 6.8 to about 8.2.
  • 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 tobacco parts or pieces may be irradiated, or those parts and pieces may be pasteurized, or otherwise subjected to controlled heat treatment.
  • the component materials may be irradiated, or those component materials may be pasteurized, or otherwise subjected to controlled heat treatment.
  • a formulation may be prepared, followed by irradiation or pasteurization, and then flavoring ingredient(s) may be applied to the formulation.
  • the tobacco formulation can be irradiated or pasteurized after the tobacco formulation has been incorporated within a moisture-permeable packet or pouch (e.g., so as to provide individual containers of snus-type smokeless tobacco product.
  • the present invention relates to a tobacco treatment process.
  • the process involves heat treatment of tobacco used in the preparation of a tobacco formulation suitable for use as a smokeless tobacco formulation.
  • the process involves subjecting tobacco material, which most preferably is in moist form, to heat treatment.
  • the heat treatment 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 heat treatment which is provided by subjecting the tobacco material to a sufficiently high temperature for a sufficient length of time, has the ability to alter the overall character or nature of the tobacco material to a desired degree.
  • the heat treatment can be used to provide a desired color or visual character to the tobacco material, desired sensory properties to the tobacco material, or a desired physical nature or texture to the tobacco material.
  • the heat treatment causes the tobacco material to experience a treatment characteristic of a pasteurization type of treatment.
  • certain types and amounts of spores, mold, microbes, bacteria, and the like can be rendered inactive, or the enzymes generated thereby can be denatured or otherwise rendered inactive.
  • Certain components that are rendered inactive, or are otherwise effectively reduced in number, are biological agents (e.g., enzymes) that have the capability of promoting formation of tobacco-specific nitrosamines.
  • Pasteurization techniques are set forth, for example, on the websites of the U.S. Food and Drug Administration and the U.S. Department of Agriculture.
  • 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. It is preferably to avoid excessively high heat treatment temperatures, such as temperatures at or above the boiling point of water. However, the temperature of the heat treatment step can be characterized as elevated, meaning the temperature is greater than room temperature (i.e., greater than 25°C).
  • the methods and equipment used to accomplish the heat treatment can vary. 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 processes of the invention set forth below can be performed using equipment known in the art such as various mixing apparatus, including various jacketed mixing apparatus capable of heating the contents of the mixer, as well as stirring or agitating the contents of the mixer.
  • Exemplary mixing vessels include mixers available from Scott Equipment Company, Littleford Day, Inc., Lödige Process Technology, and the Breddo Likwifier Division of American Ingredients Company.
  • Examples of 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 U.S. Patent No. 4,882,128 to Hukvari et al. ).
  • Preferred mixers allow for direct steam injection into the contents of the mixer. All process steps noted below can be conducted while the tobacco material is being stirred or agitated.
  • the pressure within the mixing vessel during the process can be atmospheric pressure or elevated pressure (e.g., about 0.69 bar to 69 bars (about 10 psig to about 1,000 psig).)
  • the moisture content of the moist tobacco material subjected to heat treatment is at least about 30 percent, often is at least about 35 percent, and frequently is at least about 40 percent, based on the total weight of the tobacco formulation being subjected to heat treatment.
  • the tobacco material can be moisturized by addition of aqueous fluids, such as steam, liquid tap water, aqueous solutions of sodium chloride, and the like.
  • the moist tobacco material is contacted with a basic material (e.g., sodium carbonate, sodium bicarbonate, or a mixture thereof) in order to raise the pH to the alkaline pH range.
  • a basic material e.g., sodium carbonate, sodium bicarbonate, or a mixture thereof
  • the moisture content of the tobacco material is at least about 30 percent, often is at least about 35 percent, and frequently is at least about 40 percent, based on the total weight of the tobacco formulation.
  • the tobacco material is cooled somewhat prior to addition of the basic material thereto (e.g., the tobacco can be cooled to below about 75°C, frequently below about 65°C, and often below about 55°C).
  • the tobacco mixture is allowed to interact with the basic material while that tobacco material experiences a sufficiently high moisture level until the pH of the tobacco material drops to about 8 pH units. Then, the tobacco material is cooled and dried.
  • Exemplary flavorant compositions include various top dressing and casing compositions, including those compositions described in US Pat. Nos. 5,121,757 to White et al. ; 5,370,139 to Shu et al. ; 5,318,050 to Gonzalez-Parra et al. ; 5,343,879 to Teague ; 5,413,122 to Shu et al. ; 5,962,662 to Shu et al. ; 6,048,404 to White ; 6,298,858 to Coleman, III, et al. ; 6,325,860 to Coleman, III ; 6,428,624 to Coleman, III, et al.
  • the invention provides various processes for preparing a tobacco material for use in a smokeless tobacco product.
  • the methods of the invention involve heat treatment of the tobacco and adjustment of the pH of the tobacco in a manner adapted for improving the storage stability of the sensory characteristics of the smokeless tobacco product.
  • a tobacco material in a desired form e.g., shredded or particulate form
  • the tobacco material may comprise a blend of various tobacco types, such as a blend of various tobacco lamina materials (e.g., flue-cured lamina, Oriental lamina, and the like) and various stem materials (e.g., Rustica stem, Kurnool stem, Indian Sun-Cured stem, and the like).
  • the blend of tobacco materials is typically provided at a low moisture level, such as about 5 to about 15% by weight (e.g., about 10-12% by weight) based on the total weight of the tobacco material.
  • the tobacco material is preferably combined with a salt material, and the salt material is preferably in aqueous solution form.
  • an aqueous sodium chloride solution is added to the tobacco material and the resulting mixture typically has a moisture content of about 30 to about 50% by weight, often about 30 to about 40% by weight (e.g., 35% by weight).
  • the tobacco material can be heated while the sodium chloride or other salt material is added in order to aid thorough mixing of the salt solution with the tobacco material.
  • the heating can comprise heating the tobacco material to a temperature of at least about 60°C, typically about 60°C to about 65°C.
  • the moist tobacco material with optional salt component is then subjected to a heat treatment step, which involves heating the tobacco material for a time and at a temperature sufficient to pasteurize the tobacco as described above.
  • exemplary heating temperatures include temperatures of about 85°C or higher, such as about 85°C to about 100°C, more typically about 90°C to about 95°C.
  • the time of exposure to the pasteurization temperature can vary, but is typically at least about 1 hour, such as about 1 hour to about 3 hours.
  • the heating of the tobacco is conducted by both raising the jacket temperature of the mixer holding the tobacco material and direct steam injection into the tobacco material. The steam injection will also typically result in an increase in moisture content of the tobacco during the heating step.
  • the moisture content of the tobacco material is maintained during the heating step at essentially a constant moisture level or is allowed to rise slightly, such as a level of at least about 30% by weight, such as about 30% to about 40% by weight (e.g., about 35% by weight).
  • the tobacco is maintained in a relatively moist condition during the heating step.
  • the tobacco material is typically cooled prior to addition of a base intended to raise the pH of the material.
  • the temperature of the tobacco material is typically reduced to about 60°C to about 65°C.
  • a base is then added to the tobacco material and thoroughly mixed with the tobacco material.
  • the base can be any material capable of raising the pH of the tobacco material to an alkaline pH range (e.g., about 9 to about 10).
  • Exemplary bases include alkali metal hydroxides, alkali metal carbonates, alkali metal bicarbonates, and mixtures thereof.
  • Specific base materials that can be used include sodium carbonate, potassium carbonate, sodium bicarbonate, potassium bicarbonate, sodium hydroxide, potassium hydroxide, and mixtures thereof.
  • the base is typically added in the form of an aqueous solution and the base addition step typically results in an increase of moisture content of the tobacco material.
  • sufficient base is added to the tobacco material to result in a tobacco material pH of at least about 8.7, such as a pH of about 8.7 to about 10.
  • the final moisture content is often about 40% to about 55% by weight, frequently about 45% to about 50% by weight.
  • the resulting moist, pH-adjusted tobacco material is heated at an elevated temperature, such as a temperature of at least about 55°C, often at a temperature range of about 55°C to about 95°C, more often about 65°C to about 75°C.
  • an elevated temperature such as a temperature of at least about 55°C, often at a temperature range of about 55°C to about 95°C, more often about 65°C to about 75°C.
  • the moisture level of the tobacco material is held relatively constant or allowed to rise slightly in order to promote the continued reaction between the tobacco material and the base.
  • the moisture level of the tobacco material is preferably maintained at a level of at least about 40% by weight, and typically about 40% to about 55% by weight, frequently about 45% to about 50% by weight.
  • the mixing vessel containing the tobacco material is typically not vented to atmosphere, although a small flow of filtered air can be allowed to pass through the head space of the mixer to remove ammonia that forms as the base reacts with acidic materials in the tobacco material.
  • the heating step following base addition will typically continue for at least about 1 hour, and often will continue for about 1 to about 3 hours. During this step, it is preferable to allow the pH to drop to below about 8.5, such as about 8.0 to about 8.5 (e.g., about 8.1, about 8.2, about 8.3, about 8.4, or about 8.5).
  • about 8.0 to about 8.5 e.g., about 8.1, about 8.2, about 8.3, about 8.4, or about 8.5.
  • the rate of pH reduction is maintained at about 0.05 to about 0.15 pH units per hour, more typically about 0.08 to about 0.10 pH units per hour (e.g., about 0.09 pH units per hour).
  • the moist tobacco material is dried by continued heating of the tobacco material while the mixing vessel is allowed to vent such that water vapor is removed.
  • This step typically involves heating the tobacco material at a moderate elevated temperature, such as at a temperature of at least about 35°C, frequently at a temperature of about 35°C to about 70°C, more often about 55°C to about 65°C.
  • the length of the drying step can vary, but is typically about 20 to about 24 hours.
  • the final moisture content of the tobacco material following drying is often less than about 35% by weight, such as about 25% to about 35% by weight, frequently about 25% to about 30% by weight. It is advantageous to maintain the pH of the material during the drying step in the range of about 7.6 to about 8.2.
  • the tobacco material is initially mixed with a large excess of water to form a mixture having a relatively high moisture content, which can be characterized as a slurry, prior to heat treatment.
  • the slurry typically comprises at least about 75% by weight of water, and often at least about 80% by weight of water. In one embodiment, the tobacco material slurry comprises about 75% to about 95% by weight water.
  • the slurry is mixed with a salt material, such as an aqueous solution of sodium chloride.
  • the salt material is typically added in amount of about 1 to about 8% by weight (e.g., about 1 to about 3% by weight) of the tobacco material, based on the dry weight of the tobacco material.
  • the slurry is heated in order to pasteurize the tobacco material.
  • the heating step typically comprises heating the tobacco material slurry to a temperature of at least about 60°C, such as a temperature of about 60°C to about 100°C, more often about 70°C to about 90°C (e.g., about 75°C).
  • the time of heating can vary, but will typically be at least about 30 minutes, such as about 30 minutes to about 1 hour.
  • a base material is added.
  • the base material is typically in the form of an aqueous solution and the base can be any basic material such as those materials set forth above.
  • the base is added in an amount of about 3 to about 11% by weight based on the dry weight of the tobacco material.
  • Sufficient base is added to raise the pH of the slurry to an alkaline pH range, such as at least about 8.5, and typically at least about 9.0.
  • An exemplary pH range for the slurry following base addition is about 8.5 to about 11, more frequently about 9 to about 10.
  • the slurry is agitated and heated to an elevated temperature, such as a temperature of at least about 60°C, for a period of time sufficient to allow the pH of the slurry to drop at least about 0.5 pH units.
  • the time of heating will typically be at least about 1.5 hours, such as a range of about 1.5 hours to about 3.0 hours.
  • the temperature of the heating step will typically range from about 70°C to about 95°C.
  • the final pH of the slurry following this heating step will typically be in the range of about 8.0 to about 8.5 (e.g., about 8.1, about 8.2, about 8.3, about 8.4, or about 8.5).
  • the slurry can be cooled to ambient temperature, such as a temperature below about 35°C.
  • a humectant such as glycerol, propylene glycol, or sugar alcohol (e.g., maltitol syrup) can be added.
  • the tobacco material is then dried.
  • the drying step involved casting the slurry onto a belt (e.g., a stainless steel belt) and passing the tobacco through a drying zone operated at a temperature of about 85°C to about 285°C.
  • the typical resident time of the tobacco material in the drying zone is about 2 to about 5 minutes.
  • the belt speed through the drying zone or tunnel can range from about 25 to about 55 feet/min.
  • the final moisture content of the dried tobacco material is typically about 5 to about 15% by weight, often about 10 to about 12% by weight.
  • Tobacco material drying techniques are set forth, for example, in U.S. Pat. Nos. 4,941,484 to Clapp et al. ; 5,005,593 to Fagg et al. ; and 5,234,008 to Fagg .
  • a smokeless tobacco formulation is prepared using tobacco treated in a similar manner to that for a paper process reconstituted tobacco, such as described in US Pat Nos. 5,159,942 and 5,445,169 to Brinkley .
  • tobacco is subjected to an aqueous extraction at an elevated temperature in order to separate the tobacco material into a solids portion and an extract portion, wherein the extract portion typically has a relatively low solids content (e.g., about 3-6% solids).
  • the time and temperature of the extraction can vary, but typically the temperature is at least about 60°C, such as a temperature of about 60°C to about 100°C, more often about 70°C to about 90°C (e.g., about 75°C), and the time is typically about 30 minutes to about 1.5 hours.
  • the aqueous solution used to extract the tobacco material typically contains a salt and a base material, such as about 3 to about 8% by weight of a salt (e.g., sodium chloride) and about 1 to about 5% by weight of a base (e.g., sodium hydroxide), based on the weight of the tobacco.
  • a salt e.g., sodium chloride
  • a base e.g., sodium hydroxide
  • the extract is then preferably cooled down (e.g., cooled to about 65°C) and optionally neutralized by addition of a base (e.g., about 3.5% sodium hydroxide and about 3.5 % potassium carbonate by weight of tobacco).
  • a base e.g., about 3.5% sodium hydroxide and about 3.5 % potassium carbonate by weight of tobacco.
  • the pH of the extract can changes from about 9.0-9.5 to about 8.0-8.5.
  • the extract can be concentrated to form a concentrated extract with a relatively high solids content, such as about 30-35% solids, via vacuum evaporation, for example.
  • the concentrated extract is optionally mixed with a humectant (e.g., about 6% glycerin), and then added back to the extracted solids portion.
  • the resulting tobacco material can be dried to reduce the moisture content, such as to about 10 to about 12% moisture.
  • the drying step can be accomplished, for example, using a forced air oven at a temperature of about 85°C to about
  • the tobacco material is allowed to intimately mix with the base material in a moist environment for a time sufficient to encourage significant interaction between the base and acidic species within the tobacco. Significant drying of the tobacco is prevented until sufficient contact between the tobacco and base has occurred.
  • the above processes lead to greater storage stability of the sensory characteristics of the smokeless tobacco products formed using the tobacco materials treated according to these processes, and in particular, it is believed that greater pH storage stability of the final product can be achieved using the processes of the invention.
  • the resulting tobacco material can be mixed with additional flavorants, including sweeteners.
  • additional flavorants including sweeteners.
  • Various flavorants and water can be added as necessary to adjust flavor and moisture content such that the tobacco material exhibits the desired final moisture range for the product, which can vary as noted above.
  • the moisture content of the tobacco composition is raised to at least about 25% by weight in this step.
  • a typical toasting process which can occur either before or after the above-described heat treatment processes, comprises heating a relatively dry tobacco material (e.g., having a moisture content of about 5% to about 20% by weight) at an elevated temperature (about 85°C to about 300°C) for a time sufficient to toast the tobacco material, such as a period of about 1 to about 3 hours.
  • a relatively dry tobacco material e.g., having a moisture content of about 5% to about 20% by weight
  • an elevated temperature about 85°C to about 300°C
  • the tobacco can be mixed with a base and/or sugars (e.g., glucose, fructose, sucrose, high fructose corn syrup, caramel, rhamnose, or mixtures thereof), or sugar alcohols (e.g., maltitol, mannitol, xylitol, sorbitol, or mixtures thereof), prior to heating in order to promote Maillard reactions during heating.
  • sugars e.g., glucose, fructose, sucrose, high fructose corn syrup, caramel, rhamnose, or mixtures thereof
  • sugar alcohols e.g., maltitol, mannitol, xylitol, sorbitol, or mixtures thereof
  • Exemplary toasting conditions are set forth, for example, in U.S. Pat. Nos. 4,534,372 to White and 4,596,259 to White et al. .
  • the tobacco used for the manufacture of the tobacco product also can be processed, blended, formulated, combined and mixed with other materials or ingredients, including non-encapsulated amounts of any of the additives that can be used in the microcapsules discussed herein.
  • the tobacco composition can incorporate salts, sweeteners, binders, colorants, pH adjusters, fillers, oral care additives, flavoring agents, 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 PCT application WO2007/037962 .
  • the relative amounts of the various components within the tobacco formulation may vary.
  • the amounts presented herein are total amounts of each type of additive, and can represent both encapsulated (or otherwise separated forms) and non-encapsulated components.
  • the smokeless tobacco products of the invention can include any of the various amounts of additive solely in the form of a microencapsulated or otherwise separated additive, solely in the form of a non-encapsulated additive, or in the form of a mixture of encapsulated and non-encapsulated additive.
  • a sweetener is most preferably employed in amounts sufficient to provide desired flavor attributes to the tobacco formulation.
  • a representative amount of sweetener whether an artificial sweetener and/or natural sugar, may make up at least about 1 percent to at least about 3 percent, of the total dry weight of the formulation.
  • the amount of sweetener within the formulation will not exceed about 40 percent, often will not exceed about 35 percent, and frequently will not exceed about 30 percent, of the total dry weight of the formulation.
  • a tobacco-containing microencapsulated (or otherwise separated) additive such as particulate tobacco or a tobacco extract, is preferably present in an amount sufficient to provide desired flavor attributes to the tobacco formulation.
  • the tobacco-containing microencapsulated additive is often present in an amount of at least about 5 percent of the total dry weight of the formulation, more typically at least about 10 percent.
  • the amount of tobacco-containing microencapsulated additive is typically less than about 50 weight percent, often less than about 40 weight percent, and frequently less than about 30 weight percent of the total dry weight of the formulation.
  • Embodiments of the invention including microencapsulated (or otherwise separated) water typically include an amount of water in microencapsulated form of at least about 10 percent, typically at least about 15 percent, and frequently at least about 20 percent, based on the total weight of the formulation.
  • the amount of microencapsulated water is typically less than about 35 percent, often less than about 30 percent, and frequently less than about 25 percent.
  • An additive derived from an herbal or botanical source is preferably employed in amounts sufficient to provide desired functional attributes to the tobacco formulation and the amount will vary depending on the desired function and the type of herbal or botanical source.
  • a representative amount of additive is at least about 1 percent to at least about 3 percent, of the total dry weight of the formulation.
  • the amount of additive within the formulation will not exceed about 40 percent, often will not exceed about 35 percent, and frequently will not exceed about 30 percent, of the total dry weight of the formulation.
  • a binder may be employed in amounts sufficient to provide the desired physical attributes and physical integrity to the tobacco formulation.
  • a representative amount of binder may make up at least about 1 percent to at least about 3 percent of the total dry weight of the formulation.
  • the amount of binder within the formulation will not exceed about 20 percent of the total dry weight of the formulation.
  • the amount of binder within a desirable formulation will not exceed about 15 percent, and frequently will not exceed about 10 percent, of the total dry weight of the formulation.
  • a disintegration aid may be 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., by undergoing swelling upon contact with water).
  • a representative amount of disintegration aid may make up at least about 1 percent to at least about 10 percent of the total dry weight of the formulation.
  • the amount of disintegration aid within the formulation will not exceed about 50 percent, and frequently will not exceed about 30 percent, of the total dry weight of the formulation.
  • a colorant may be employed in amounts sufficient to provide the desired visual attributes to the tobacco formulation.
  • a representative amount of colorant may make up at least about 1 percent to at least about 3 percent, of the total dry weight of the formulation.
  • the amount of colorant within the formulation will not exceed about 30 percent, and frequently will not exceed about 10 percent, of the total dry weight of the formulation.
  • a filler preferably is employed in amounts sufficient to provide control of desired physical attributes and sensory attributes to the tobacco formulation.
  • a representative amount of filler may make up at least about 5 percent to at least about 15 percent, of the total dry weight of the formulation.
  • the amount of filler within the formulation will not exceed about 60 percent, and frequently will not exceed about 40 percent, of the total dry weight of the formulation.
  • a buffering or pH adjusting agent may be employed in the tobacco formulation.
  • a representative amount of buffering or pH adjusting agent may make up at least about 1 percent to at least about 3 percent of the total dry weight of the formulation.
  • the amount of buffering or pH adjusting agent within the formulation will not exceed about 10 percent, and frequently will not exceed about 5 percent, of the total dry weight of the formulation.
  • a non-sweetener flavorant preferably is employed in amounts sufficient to provide desired sensory attributes to the tobacco formulation.
  • a representative amount of flavorant e.g., vanillin
  • the amount of flavoring ingredient will not exceed about 15 percent, and frequently will not exceed about 5 percent, of the total dry weight of the formulation.
  • a salt may be employed in amounts sufficient to provide desired sensory attributes to the tobacco formulation.
  • a representative amount of salt may make up at least about 1 percent to at least about 3 percent of the total dry weight of the formulation.
  • the amount of salt within the formulation will not exceed about 10 percent, and frequently does not exceed about 5 percent, of the total dry weight of the formulation.
  • An antioxidant may be employed in the tobacco formulation.
  • a representative amount of antioxidant may make up at least about 1 percent to at least about 3 percent, of the total dry weight of the formulation.
  • the amount of antioxidant within the formulation will not exceed about 25 percent, and frequently will not exceed about 10 percent, of the total dry weight of the formulation.
  • a preservative may be employed in the tobacco formulation.
  • a representative amount of preservative may make up at least about 0.1 percent to at least about 1 percent, of the total dry weight of the formulation.
  • the amount of preservative within the formulation will not typically exceed about 5 percent, and frequently will not exceed about 3 percent, of the total dry weight of the formulation.
  • the tobacco formulation can incorporate at least one oral care ingredient (or mixture of such ingredients) that provides the ability to inhibit tooth decay or loss, inhibit gum disease, relieve mouth pain, whiten teeth or otherwise inhibit tooth staining, elicit salivary stimulation, inhibit breath malodor, freshen breath, or the like.
  • oral care ingredient or mixture of such ingredients
  • effective amounts of ingredients such as thyme oil, eucalyptus oil and zinc (e.g., such as the ingredients of formulations commercially available as ZYTEX® from Discus Dental) can be incorporated into the formulation.
  • exemplary ingredients that can be incorporated in desired effective amounts within tobacco-containing formulations can include those that are incorporated within the types of oral care compositions set forth in Takahashi et al., Oral Microbiology and Immunology, 19(1), 61-64 (2004 ); US Pat. No. 6,083,527 to Thistle ; and US Pat. Appl. Pub. Nos. 2006/0210488 to Jakubowski and 2006/02228308 to Cummins et al.
  • Other exemplary ingredients of tobacco containing-formulation include those contained in formulations marketed as MALTISORB® by Roquette and DENTIZYME® by NatraRx.
  • a representative amount of oral care additive is at least about 1 percent, often at least about 3 percent, and frequently at least about 5 percent of the total dry weight of the formulation.
  • the amount of oral care additive within the formulation will not typically exceed about 30 percent, often will not exceed about 25 percent, and frequently will not exceed about 20 percent, of the total dry weight of the formulation.
  • Representative tobacco formulations may incorporate about 25 to about 60 percent tobacco, about 1 to about 5 percent artificial sweetener, about 1 to about 5 percent colorant, about 10 to about 60 percent organic and/or inorganic filler, about 5 to about 20 percent disintegrating aid, about 1 to about 5 percent binder, about 1 to about 5 percent pH-adjusting/buffering agent, flavoring ingredient in an amount of up to about 10 percent, preservative in an amount up to about 2 percent, and salt in an amount up to about 5 percent, based on the total dry weight of the tobacco formulation.
  • the particular percentages and choice of ingredients will vary depending upon the desired flavor, texture, and other characteristics.
  • the manner by which the various components of the tobacco formulation are combined may vary.
  • the various components of the formulation may be contacted, combined, or mixed together in conical-type blenders, mixing drums, ribbon blenders, or the like.
  • the overall mixture of various components with the powdered tobacco components may be relatively uniform in nature. See also, for example, the types of methodologies set forth in U.S. Pat. Nos. 4,148,325 to Solomon et al. ; 6,510,855 to Korte et al.; and 6,834,654 to Williams . Manners and methods for formulating snus-type tobacco formulations will be apparent to those skilled in the art of snus tobacco product production.
  • the tobacco composition most preferably is provided in a form that is characteristic of a snus type of product as described with reference to the accompanying drawings
  • the tobacco composition also can have the form of loose moist snuff, loose dry snuff, chewing tobacco, pelletized tobacco pieces, extruded tobacco strips or pieces, finely divided ground powders, finely divided or milled agglomerates of powdered pieces and components, flake-like pieces (e.g., that can be formed by agglomerating tobacco formulation components in a fluidized bed), molded processed tobacco pieces (e.g., formed in the general shape of a coin, cylinder, bean, cube, or the like), pieces of tobacco-containing gum, products incorporating mixtures of edible material combined with tobacco pieces and/or tobacco extract, products incorporating tobacco (e.g., in the form of tobacco extract) carried by a solid inedible substrate, and the like.
  • loose moist snuff loose dry snuff
  • chewing tobacco pelletized tobacco pieces, extrude
  • the tobacco composition can have the form of compressed tobacco pellets, multi-layered extruded pieces, extruded or formed rods or sticks, compositions having one type of tobacco formulation surrounded by a different type of tobacco formulation, rolls of tape-like films, readily water-dissolvable or water-dispersible films or strips (see, for example, US Pat. Appl. Pub. No. 2006/0198873 to Chan et al. ), or capsule-like materials possessing an outer shell (e.g., a pliable or hard outer shell that can be clear, colorless, translucent or highly colored in nature) and an inner region possessing tobacco or tobacco flavor (e.g., a Newtoniam fluid or a thixotropic fluid incorporating tobacco of some form).
  • an outer shell e.g., a pliable or hard outer shell that can be clear, colorless, translucent or highly colored in nature
  • an inner region possessing tobacco or tobacco flavor e.g., a Newtoniam fluid or a thixotropic fluid incorporating tobacco of
  • Processed tobacco compositions such as compressed tobacco pellets can be produced by compacting granulated tobacco and associated formulation components, compacting those components in the form of a pellet, and optionally coating each pellet with an overcoat material.
  • Exemplary granulation devices are available as the FL-M Series granulator equipment (e.g., FL-M-3) from Vector Corporation and as WP 120V and WP 200VN from Alexanderwerk, Inc.
  • Exemplary compaction devices such as compaction presses, are available as Colton 2216 and Colton 2247 from Vector Corporation and as 1200i, 2200i, 3200, 2090, 3090 and 4090 from Fette Compacting.
  • Devices for providing outer coating layers to compacted pelletized tobacco formulations are available as CompuLab 24, CompuLab 36, Accela-Cota 48 and Accela-Cota 60 from Thomas Engineering.
  • Processed tobacco compositions can be manufactured using a wide variety of extrusion techniques.
  • multi-layered tobacco pellets can be manufactured using co-extrusion techniques (e.g., using a twin screw extruder).
  • co-extrusion techniques e.g., using a twin screw extruder
  • successive wet or dry components or component mixtures can be placed within separate extrusion hoppers.
  • Steam, gases (e.g., ammonia, air, carbon dioxide, and the like), and humectants e.g., glycerin or propylene glycol
  • the various components are processed so as to be very well mixed, and hence, come in complete contact with each other.
  • Multilayered materials can have the general form of films, and alternatively, multi-layered generally spherical materials can possess various layers extending from the inside outward.
  • Certain tobacco compositions can incorporate tobacco as the major component thereof.
  • those compositions do not, to any substantial degree, leave any residue in the mouth of the user thereof.
  • those compositions do not provide the user's mouth with slick or slimy sensation (e.g., due to overly high levels of binding agents).
  • Tobacco materials during processing, can be treated with pH adjusters or other suitable agents, so that natural pectins within the tobacco material can be released. Release of natural tobacco pectin can act to reduce the amount of additional gums/hydrocolloids, cellulose-derived, or starch-based binders needed to aid in desired sheet or film tensile strength qualities.
  • fine tobacco powder is cooked in an alkaline pH adjusted solution at elevated temperatures relative to ambient.
  • Such treatment also can provide desirable sensory attributes to the tobacco material. See, for example, US Pat. Nos. 5,099,864 to Young et al. ; 5,339,838 to Young et al. ; and 5,501,237 to Young et al. .
  • a representative type of tobacco formulation possesses an outer shell and an inner region in the form of a tobacco formulation.
  • a representative outer shell can be provided by providing a liquid mixture of alginates (e.g., sodium alginates available as Kelvis, Kelgin and Mannucol from International Specialty Products Corp.), rice starch, sucralose, glycerin and flavoring agent (e.g., mint flavor) in water so as to provide a liquid mix exhibiting a Brookfield viscosity at 25°C of about 20,000 to about 25,000 centipoise.
  • alginates e.g., sodium alginates available as Kelvis, Kelgin and Mannucol from International Specialty Products Corp.
  • rice starch e.g., a starch
  • sucralose e.g., glycerin
  • flavoring agent e.g., mint flavor
  • That viscous mixture can be used to form a sheet that can be formed into an outer layer (e.g., using a Villaware Imperia Pasta Machine, Dough Roller 150 equipped with a Villaware Ravioli Attachment for Imperia 150-25, each of which is available through Imperia Trading Company) or semi-circular shells that can be combined (e.g., by exposure to heat) to form an outer layer.
  • an outer layer e.g., using a Villaware Imperia Pasta Machine, Dough Roller 150 equipped with a Villaware Ravioli Attachment for Imperia 150-25, each of which is available through Imperia Trading Company
  • semi-circular shells that can be combined (e.g., by exposure to heat) to form an outer layer.
  • such a viscous mixture can be suitably dried by heating at about 60°C for about 1 hour. Inside that outer shell can be incorporated a wide variety of tobacco formulations.
  • One representative tobacco formulation used as the inner region of such a is a dry or moist mixture of granulated or milled tobacco material that can be mixed with other ingredients, such as flavoring agents, humectants, fillers, pH adjusters, dispersion aids, and the like.
  • One representative tobacco formulation has the form of a gel or soft gel. That tobacco formulation can be provided by mixing granulated or milled tobacco material, kappa-carageenan, Kelvis-type sodium alginate, propylene glycol and flavoring agent (e.g., menthol and cinnamon) in water, such that the moisture content of the formulation is about 40 to about 50 weight percent.
  • One representative tobacco formulation has the form of a fluid.
  • That tobacco formulation can be provided by mixing granulated or milled tobacco material, glycerin, propylene glycol, kappa-carageenan, carboxymethycellulose available as Ticalose 1500 from TIC Gums and micro-crystalline cellulose (e.g., Ticacel HV from TIC Gums) in water, such that the moisture content of the formulation is about 60 to about 70 weight percent.
  • the tobacco in the form of a pellet or other processed form, it may be desirable to treat the tobacco material in the smokeless tobacco product with a bleaching or oxidizing agent in order to alter the color of the tobacco material.
  • a bleaching or oxidizing agent in order to alter the color of the tobacco material.
  • Exemplary bleaching agents include hydrogen peroxide, ozone, and ammonia. Processes for treating tobacco with bleaching agents are discussed, for example, in US Pat. Nos. 787,611 to Daniels, Jr.
  • the type of pouch used to contain the tobacco formulation can vary, and in fact, in certain embodiments, a pouch may be unnecessary.
  • tobacco formulations having the form of a tobacco pellet or other processed form already sized for individual use may not require containment in the form of a pouch. Instead, the pellets or other processed forms of the tobacco formulation could be simply packaged in an outer container without using a pouch to divide the tobacco formulation into individual serving sizes.
  • Suitable packets, pouches or containers of the type used for the manufacture of smokeless tobacco products are available under the tradenames "taboka,” CatchDry, Ettan, General, Granit, Goteborgs Rape, Grovsnus White, Metropol Kaktus, Mocca Anis, Mocca Mint, Mocca Wintergreen, Kicks, Probe, Prince, Skruf, TreAnkrare, Camel Snus Original, Camel Snus Frost and Camel Snus Spice.
  • 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 or fleece 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.
  • an exemplary pouch may be manufactured from materials, and in such a manner, such that during use by the user, the pouch is 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.
  • exemplary 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 toss of its physical integrity.
  • flavoring ingredients, disintegration aids, and other desired components may be incorporated within, or applied to, the pouch material.
  • 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, which may be suitably modified with a capsule insertion apparatus of the general type set forth in U.S. Pat. Pub. No. 2007/0068540 to Thomas et al.
  • 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.
  • the pouches containing the tobacco formulation are preferably packaged in an outer container that is sealed tightly, and is composed of a suitable material, such that the atmospheric conditions within that sealed package are modified and/or controlled. That is, the sealed package can provide a good barrier that inhibits the passage of compositions such as moisture and oxygen therethrough.
  • the atmosphere within the sealed package can be further modified by introducing a selected gaseous species (e.g., nitrogen, argon, or a mixture thereof) into the package prior to sealing.
  • a selected gaseous species e.g., nitrogen, argon, or a mixture thereof
  • the present invention can involve the use of equipment, materials, methodologies and process conditions that are suitably modified in order to provide the packaging and controlled atmospheric conditions for the tobacco products that are packaged pursuant thereto.
  • the atmosphere within the packaging materials can be modified in a variety of ways. For example, a significant amount of the atmosphere within the package can be removed (e.g., by using vacuum packaging types of techniques), or the atmosphere within the package can be altered in a controlled manner (e.g., by using gas flushing types of techniques).
  • the controlled or modified atmospheres within packaged tobacco products of the present invention can vary.
  • tobacco product is vacuum packed or flushed so as to have a controlled or modified atmosphere (e.g., even if the atmosphere is controlled in a manner such that the atmospheric pressure within the sealed package is at a positive pressure relevant to ambient atmospheric pressure)
  • atmospheric conditions within the package are controlled such that a significant amount, and most preferably virtually all of the oxygen present within with package, is removed from that package prior to the time that the package is sealed. That is, less than about 8 percent, and often less than about 6 percent, of the weight of the controlled atmosphere initially present with a sealed outer package is composed of oxygen.
  • the atmosphere present within the package preferably can possess less than about 5 percent oxygen, and most preferably between about 1 percent oxygen and about 5 percent oxygen, based on the weight of the controlled atmosphere initially present within that sealed package.
  • a gaseous species e.g., a selected gas or mixture of gases
  • a significant amount, and most preferably virtually all, of the atmosphere within the sealed package is provided by the desired gaseous species.
  • gaseous species include nitrogen, argon, carbon dioxide, and the like (e.g., high purity gases that are greater than about 99 percent pure, by weight).
  • the atmosphere to which the tobacco product incorporates a relatively high level of a desired gaseous species (e.g., oxygen) in order to introduce the effects of "gas shock" to the tobacco product can be desirable for the introduction of "oxygen shock” for purposes of inhibiting enzymatic discoloration, preventing anaerobic fermentation reactions, and inhibiting aerobic and anaerobic microbial growth).
  • a controlled atmosphere containing an amount of oxygen such that the level of oxygen in that atmosphere greater than about 25 percent by weight, often greater than about 30 percent by weight, can provide conditions suitable for introduction of oxygen shock.
  • Representative equipment useful for carrying out process steps associated with the packaging processes described herein is available from Winpak Ltd. (e.g., systems identified as LD32, L25, L18 and L12); as Linium 300 Series horizontal flow wrapping systems from Doboy Inc. (e.g., Linium Model Nos. 301, 302, 303, 304 or 305); as Hiwrap 504 systems available from Hitech Systems s.r.l.; and as the types of systems available from Rovemamaschinen GmbH.
  • Preferred equipment provides a wrapping material that provides a seal that does not allow passage of gases or moisture therethrough (e.g., a seal that might be considered as "air tight").
  • the pouches containing the tobacco formulation can be packaged within a sealed hard container that serves as the outermost package or container.
  • a representative hard container is the short, rounded edge, generally cylindrical container traditionally used for the marketing of snus types of products. See, for example, the types of representative snuff-box types of designs set forth in PCT WO 2005/016036 to Bjorkholm .
  • Other types of containers that can be suitably modified are plastic or metal type containers set forth in US Pat. No. 7,014,039 to Henson et al. See, also, the types of hard containers used for the commercial distribution of Camel Snus by R. J.
  • the type of container used for the "toboka” product can be adapted to possess a slidable tip lid (e.g., that slides generally parallel to the longitudinal axis of the container) in order that the container can be opened and closed.
  • the container can have an accordion or bellows type of design; and as such, the container can be extended open for filling with smokeless tobacco product during production, and then contracted after filling of the container is complete.
  • containers can be equipped with suitable seals or grommets, such that when an opened container is re-shut, a good seal is provided.
  • the hard container In use, the hard container is opened, the outer package is opened, a pouch is removed therefrom, and the pouch is enjoyed by the consumer.
  • the hard container is manually resealed, and additional pouches are removed from that container by the consumer as desired.
  • the amount of tobacco formulation incorporated within each sealed outer package can vary.
  • loose tobacco composition can be incorporated into an outer package, the package is sealed, and that loose tobacco can be used as loose snuff or chewing tobacco when the outer package is opened.
  • tobacco composition contained within a snus-type pouch or packet is incorporated within the outer package, the package is sealed, and the snus-type product can be used when the outer package is opened.
  • the amount of tobacco formulation within each individual portion is such that there is at least about 50 mg, often at least about 150 mg, and frequently at least about 250 mg, of dry weight tobacco; and less than about 700 mg, often less than about 500 mg, and frequently less than about 300 mg, of dry weight tobacco.
  • snus-type smokeless tobacco products can have the form of so-called "portion snus.”
  • the amount of tobacco formulation within each pouch is between about 100 mg and about 400 mg.
  • One exemplary snus-type product possesses about 1 g of a tobacco formulation having a moisture content of about 35 weight percent; which tobacco formulation is contained in a sealed fleece pouch having an overall length of about 30 mm, a width of about 16 mm, and a height of about 5 mm, wherein the length of the compartment area of that pouch is about 26 mm due to a seal of about 2 mm width at each end of that pouch.
  • Another exemplary snus-type product possesses about 0.5 g of a tobacco formulation having a moisture content of about 35 weight percent; which tobacco formulation is contained in a sealed fleece pouch having an overall length of about 26 mm, a width of about 12 mm, and a height of about 5 mm, wherein the length of the compartment area of that pouch is about 22 mm due to a seal of about 2 mm width at each end of that pouch.
  • Products of the present invention 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 cylindrical container.
  • moist tobacco products e.g., products having moisture contents of more than about 20 weight percent
  • moist tobacco products 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
  • a moist tobacco formulation suitable for use as a snus type of smokeless tobacco product is provided in the following manner.
  • a pre-blend of several lamina components is made and metered into an AeroFlex Model A115 flexible screw conveyor (Vac-U-Max Company, Belleville, NJ).
  • the flexible screw feeder discharges directly to a Fitzmill Comminutor hammer mill (Fitzpatrick, Elmhurst IL) utilizing a concave with 0.125 inch diameter holes.
  • the milled lamina is then pneumatically conveyed to a Rotex Model 44 screener (Rotex Corporation, Cincinnati, OH) with 2 screens - an 18 Tyler mesh and a 60 Tyler mesh.
  • the material that does not pass through the 18 mesh screen is conveyed back into the infeed hopper for further milling and the material passing the 60 mesh is discarded.
  • the material that passes the 18 mesh and is retained on the 60 mesh is gravity discharged into a container for further use in the process.
  • a plurality of stem fractions (Rustica, Kurnool, and Indian Sun Cured) is milled separately to the same size as the lamina using the same equipment noted above.
  • the tobacco is heated by passing heated water at 97°C through the water jacket on the Scott Mixer to obtain a tobacco temperature of 65°C prior to applying the first casing.
  • Mixer shaft speed is 73 rpm during the heating step.
  • Sodium chloride and water are placed in a Breddo Likwifier Model LORWW mixer and mixed for a minimum time of 3 minutes.
  • the casing is then pumped into the mixer via an ARO air operated Diaphragm pump at a flow rate of 4 gpm.
  • the casing is introduced into the Scott Mixer via a Spraying Systems Corporation Model 1 ⁇ 2GD SS-16 hydraulic atomizing nozzle.
  • the mixer speed is 73 rpm and the tobacco temperature is controlled at 65°C during this step by applying either hot water or chilled water to the mixer water jacket.
  • the mixer runs for a minimum of 10 minutes to ensure proper mixing of the first casing and the tobacco.
  • Tobacco moisture at the end of this step is 35.95% with a pH of 5.30.
  • the temperature set point on the water jacket is raised to 88°C to minimize condensation during the heating phase.
  • Steam is directly injected into the Scott mixer via two nozzles, one mounted on each end of the vessel. The steam is injected to raise and maintain the tobacco temperature to at least 93°C and is held at this temperature for a minimum of 60 minutes.
  • Mixer speed is 10 rpm during this step.
  • Tobacco moisture at the end of this step is 40.23% with a pH of 5.22.
  • the tobacco is cooled to 65°C prior to applying the second casing.
  • the cooling step is accomplished by both evaporative and convective cooling.
  • a fan is utilized to introduce filtered room air at ambient temperature into the Scott Mixer in order to evaporatively cool the tobacco and chilled water at a temperature of 3°C is introduced to the water jacket to also cool the tobacco.
  • Mixer speed is 10 rpm during this step.
  • a second casing solution comprising water and sodium carbonate is placed in a Breddo Likwifier Model LORWW mixer and mixed for a minimum time of 3 minutes.
  • the casing is then pumped into the mixer via an ARO air operated Diaphragm pump at a flow rate of 4 gpm.
  • the casing is introduced into the Scott Mixer via a Spraying Systems Corporation Model 1 ⁇ 2 GD SS-16 hydraulic atomizing nozzle.
  • the mixer speed is 73 rpm and the tobacco temperature is controlled at 65°C during this step by applying either hot water or chilled water to the mixer water jacket.
  • the mixer runs for a minimum of 5 minutes to ensure proper mixing of the second casing and the tobacco.
  • the tobacco moisture at the end of this step is 51.62% with a pH of 8.72.
  • the Scott mixer After addition of the second casing, the Scott mixer is held at a constant 71°C temperature for 2 hours using the water jacket. A small flow of filtered air is passed through the Scott Mixer to purge the head space. Mixer speed is 10 rpm during this step. Tobacco moisture at the end of this step is 49.36% with a pH of 8.34.
  • the batch is dried at a constant 38°C for a period of 20 hours by passing hot water at 54°C through the water jacket and passing filtered air through the Scott Mixer.
  • Mixer speed is 10 rpm during this step.
  • Tobacco moisture at the end of this step is 31.08% with a pH of 7.90.
  • the tobacco After drying, the tobacco is cooled to 29°C prior to applying the third casing by passing chilled water at 3°C through the water jacket. Mixer speed is 10 rpm during this step. Tobacco moisture at the end of this step is 30.85% with a pH of 7.89.
  • the third casing solution which comprises a sweetener, is placed in a Breddo Likwifier Model LORWW mixer and mixed for a minimum time of 3 minutes.
  • the casing is then pumped into the mixer via an ARO air operated Diaphragm pump at a flow rate of 4 gpm.
  • the casing is introduced into the Scott Mixer via a Spraying Systems Corporation Model 1 ⁇ 2 GD SS-16 hydraulic atomizing nozzle.
  • Mixer speed is 73 rpm and the tobacco temperature is controlled at 29°C during this step by passing chilled water through the mixer water jacket.
  • the mixer runs for a minimum of 15 minutes to ensure proper mixing of the third casing and the tobacco.
  • Tobacco moisture at the end of this step is 34.23% with a pH of 7.87.
  • the tobacco After applying the third casing, the tobacco is maintained at 29°C by passing chilled water at 3°C through the water jacket. Mixer speed is 10 rpm during this step. Tobacco moisture at the end of this step is 34.23% with a pH of 7.87.
  • a top dressing flavorant material is placed in a pressurized blow pot.
  • the top dressing is then pumped into the mixer via air pressure on the blow pot at a flow rate of 4 gpm.
  • the top dressing is introduced into the Scott Mixer via a Spraying Systems Corporation Model 1 ⁇ 2 GD SS-16 hydraulic atomizing nozzle.
  • Mixer speed is 73 rpm and the tobacco temperature is controlled at 29°C during this step by passing chilled water through the mixer water jacket.
  • the mixer runs for a minimum of 15 minutes to ensure proper mixing of the top dressing and the tobacco.
  • Tobacco moisture at the end of this step is 36.53% with a pH of 7.84.
  • the resulting product is stored at 3°C and is ready for pouching.
  • a moist tobacco formulation suitable for use as a snus type of smokeless tobacco product is provided in the following manner.
  • a dry, milled tobacco material blend as set forth in Example 1 is provided.
  • water can be provided in the form of water at ambient temperature or heated.
  • the water can incorporate ingredients dispersed or dissolved therein.
  • a solution of sodium chloride dissolved in water can be added to the dry tobacco mixture in an amount sufficient to achieve an amount of sodium chloride in the tobacco material of about 1 to about 8% by weight, based on the dry weight of the tobacco.
  • sufficient water is added to the tobacco mixture such that the tobacco mixture is in slurry form and has a moisture content of 1 weight part tobacco to about 4 to about 10 weight parts waters (e.g., 1 part tobacco:4 to 5 part water).
  • the tobacco material slurry is heated to about 75°C and mixed at a speed of 24 rpm. Then, the convective and conductive heating of the tobacco mixture is complemented by the addition of steam to the mixture. In particular, steam is blown into contact with the tobacco mixture using nozzles present in the mixer. The temperature of the mixture is held at about 75°C for about 30 minutes to about 45 minutes, while still being mixed at 24 rpm.
  • the moisture content of the tobacco slurry can be controlled during steam treatment by control of the jacket temperature. For example, lowering the jacket temperature during steam treatment can increase the moisture content of the tobacco mixture.
  • a base such as potassium or sodium hydroxide
  • potassium hydroxide is added to the tobacco slurry in the form of an aqueous solution.
  • concentration of potassium hydroxide of about 6% to about 8% by weight, based on the dry weight to of the tobacco.
  • the mixture is maintained at an elevated temperature of about 75°C for about 1.5 hours to 3 hours. During that period, the pH of the mixture drops to about 8.2 to about 8.3.
  • the tobacco slurry is cooled to ambient temperature and, during cooling, glycerol is added in an amount of about 3 to about 8%, based on the dry weight of the tobacco.
  • the resulting mixture is cast onto a hot aluminum or stainless steel belt and dried to a moisture content of about 10-12% by weight by passing the tobacco material through a drying zone operated at a temperature of 85°C to 285°C.
  • the resulting dried tobacco material is placed within a mixer and water and a sweetener are added in order to raise the moisture level to at least about 30% by weight.
  • a final top dressing flavorant is sprayed onto the moist tobacco.
  • the resulting tobacco is cooled to ambient temperature, stored at 3°C, and is ready for pouching.
  • a moist tobacco formulation suitable for use as a snus type of smokeless tobacco product is provided in the following manner.
  • Tobacco is treated in a similar manner to that for a paper process reconstituted tobacco, such as described in US Pat Nos. 5,159,942 and 5,445,169 to Brinkley , with some modification.
  • Tobacco (1 part) is subjected to an aqueous extraction (11 parts water) at 75° C for about 45 min by mixing at 24 rpm, and the solids/fibers are separated by centrifugation from the weak extract (about 3-6% solids).
  • the aqueous solution used to extract the tobacco contains about 3.5 % salt (sodium chloride) and about 1% base (sodium hydroxide) by weight of tobacco.
  • the weak extract is cooled down to about 65°C and then neutralized by addition of a base (e.g., about 3.5% sodium hydroxide and about 3.5 % potassium carbonate by weight of tobacco), while mixing at a speed of 10 rpm for about 1.5 h or more.
  • a base e.g., about 3.5% sodium hydroxide and about 3.5 % potassium carbonate by weight of tobacco
  • the pH of the extract changes from about 9.2 to about 8.2, after which the weak extract is concentrated to an about 30-35% solids strong extract via vacuum evaporation.
  • the strong extract is mixed with about 6% glycerin humectant, and then added back to the extracted fibers, before being dried to about 10 to about 12% moisture in a forced air oven (at a temperature of about 85 to about 100° C).
  • the resulting dried tobacco material is placed within a mixer and water and a sweetener are added in order to raise the moisture level to at least about 30% by weight.
  • a final top dressing flavorant is sprayed onto the moist tobacco.
  • the resulting tobacco is cooled to ambient temperature, stored at 3°C, and is ready for pouching.

Landscapes

  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Toxicology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Molecular Biology (AREA)
  • Manufacture Of Tobacco Products (AREA)

Claims (9)

  1. Produit de tabac sans fumée configuré pour insertion dans la bouche d'un utilisateur du produit, le produit de tabac comprenant une poche perméable à l'eau contenant une formulation de tabac, la formulation de tabac comprenant une matière de tabac et une pluralité de microcapsules dispersées au sein de ladite matière de tabac, la pluralité de microcapsules comprenant une enveloppe externe encapsulant une charge utile interne, l'enveloppe externe des microcapsules étant apte à se rompre de manière que la rupture de l'enveloppe externe expose la charge utile à la matière de tabac, et la charge utile interne comprenant une matière de charge et un aromatisant contenant du tabac, la matière de charge comprenant une matière de fibre végétale.
  2. Produit de tabac sans fumée selon la revendication 1, dans lequel la charge utile des microcapsules comprend de la vanilline sous une forme complexe.
  3. Produit de tabac sans fumée selon la revendication 1, dans lequel la matière de charge comprend une matière de fibre de betterave à sucre.
  4. Produit de tabac sans fumée selon l'une des revendications 1 à 3, dans lequel la charge utile des microcapsules comprend un agent tampon.
  5. Produit de tabac sans fumée selon la revendication 4, dans lequel l'agent tampon tamponne au sein d'une plage de pH d'environ 6 à environ 10.
  6. Produit de tabac sans fumée selon l'une des revendications 1 à 5, dans lequel l'aromatisant contenant du tabac comprend un extrait de tabac ou une matière de tabac particulaire.
  7. Produit de tabac sans fumée selon l'une des revendications 1 à 6, dans lequel la charge utile des microcapsules comprend, en outre, un édulcorant comprenant du néotame.
  8. Produit de tabac sans fumée selon l'une des revendications 1 à 7, dans lequel la charge utile des microcapsules comprend, en outre, un additif dérivé d'une source botanique ou aux herbes.
  9. Produit de tabac sans fumée selon l'une des revendications 1 à 8, dans lequel l'enveloppe externe des microcapsules est soluble dans l'eau dans des conditions d'au moins environ 45 % d'humidité, sur la base du poids total du produit de tabac sans fumée.
EP08796428.4A 2007-07-23 2008-07-22 Composition de tabac sans fumée, et procédés pour traiter le tabac destiné à y être utilisé Active EP2173200B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP11157884.5A EP2377413B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP10152287A EP2179666B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US11/781,604 US7810507B2 (en) 2006-02-10 2007-07-23 Smokeless tobacco composition
US11/781,666 US8061362B2 (en) 2007-07-23 2007-07-23 Smokeless tobacco composition
US11/781,641 US7946295B2 (en) 2007-07-23 2007-07-23 Smokeless tobacco composition
PCT/US2008/070755 WO2009015142A2 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée, et procédés pour traiter le tabac destiné à y être utilisé

Related Child Applications (5)

Application Number Title Priority Date Filing Date
EP10152287A Division EP2179666B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP10152287A Division-Into EP2179666B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP11157884.5A Division EP2377413B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP11157884.5A Division-Into EP2377413B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP10152287.8 Division-Into 2010-02-01

Publications (2)

Publication Number Publication Date
EP2173200A2 EP2173200A2 (fr) 2010-04-14
EP2173200B1 true EP2173200B1 (fr) 2017-11-15

Family

ID=40149768

Family Applications (3)

Application Number Title Priority Date Filing Date
EP11157884.5A Active EP2377413B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP10152287A Revoked EP2179666B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP08796428.4A Active EP2173200B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée, et procédés pour traiter le tabac destiné à y être utilisé

Family Applications Before (2)

Application Number Title Priority Date Filing Date
EP11157884.5A Active EP2377413B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages
EP10152287A Revoked EP2179666B1 (fr) 2007-07-23 2008-07-22 Composition de tabac sans fumée et procédé pour le traitement du tabac pour de tels usages

Country Status (5)

Country Link
EP (3) EP2377413B1 (fr)
JP (1) JP5339635B2 (fr)
CN (1) CN101873809B (fr)
DK (1) DK2377413T3 (fr)
WO (1) WO2009015142A2 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023084499A1 (fr) * 2021-11-15 2023-05-19 Nicoventures Trading Limited Produits présentant des caractéristiques sensorielles améliorées
WO2023187412A1 (fr) * 2022-04-01 2023-10-05 Nicoventures Trading Limited Produit comprenant un récipient perméable et un extrait séché à partir d'un matériau végétal et ses utilisations
WO2024194187A1 (fr) * 2023-03-17 2024-09-26 Philip Morris Products S.A. Sachet à usage oral comprenant un matériau d'arôme immobilisé à l'intérieur d'une matrice polysaccharidique

Families Citing this family (94)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
HUE027645T2 (en) 2005-01-07 2016-10-28 Regeneron Pharma IGF-1 fusion proteins and therapeutic applications
GB2469838A (en) * 2009-04-29 2010-11-03 British American Tobacco Co Treated tobacco
RU2536214C2 (ru) 2009-05-11 2014-12-20 Ю.С. Смоуклис Тобэкоу Компани Ллк Способ и устройство для ароматизации бездымного табака
US8944072B2 (en) * 2009-06-02 2015-02-03 R.J. Reynolds Tobacco Company Thermal treatment process for tobacco materials
CN102821625B (zh) 2010-03-26 2016-11-23 菲利普莫里斯生产公司 具有耐热片材的发烟制品
AR081743A1 (es) * 2010-03-26 2012-10-17 Philip Morris Prod Fabricacion de capsulas de nucleo/caparazon de diferentes geometrias y tratamiento a partir de las mismas
US9993019B2 (en) * 2010-03-26 2018-06-12 Philip Morris Usa Inc. Method for making particle of a hydrophobic additive and a polysaccharide coating and tobacco products containing particle of a hydrophobic additive and a polysaccharide coating
US8268370B2 (en) * 2010-03-26 2012-09-18 Philip Morris Usa Inc. Solid oral sensorial products including stain inhibitor
EP2552245B1 (fr) 2010-03-26 2018-11-14 Philip Morris Products S.A. Inhibition de l'irritation sensorielle pendant la consommation de produits de tabac non fumables
US9039839B2 (en) 2010-04-08 2015-05-26 R.J. Reynolds Tobacco Company Smokeless tobacco composition comprising tobacco-derived material and non-tobacco plant material
CA2796346C (fr) 2010-04-14 2018-10-02 Altria Client Services Inc. Produit de tabac sans fumee preforme
CN102905565B (zh) * 2010-05-21 2016-08-24 环球蒸汽商标公司 制备用于电吸烟设备的烟草提取物的方法
RU2580483C2 (ru) 2010-08-05 2016-04-10 Олтриа Клайент Сервисиз Инк. Материал с табаком, спутанным со структурными волокнами
WO2012019035A2 (fr) 2010-08-05 2012-02-09 Frank Scott Atchley Produits, systèmes et procédés composites à base de tabac sans fumée
US9155321B2 (en) * 2010-08-11 2015-10-13 R.J. Reynolds Tobacco Company Meltable smokeless tobacco composition
US10028520B2 (en) * 2010-09-02 2018-07-24 R.J. Reynolds Tobacco Company Apparatus for manufacturing a smokeless tobacco product incorporating an object, and associated method
US9675102B2 (en) * 2010-09-07 2017-06-13 R. J. Reynolds Tobacco Company Smokeless tobacco product comprising effervescent composition
US9775376B2 (en) * 2010-12-01 2017-10-03 R.J. Reynolds Tobacco Company Smokeless tobacco pastille and moulding process for forming smokeless tobacco products
US9204667B2 (en) * 2010-12-01 2015-12-08 R.J. Reynolds Tobacco Company Smokeless tobacco pastille and injection molding process for forming smokeless tobacco products
AU2011338226B2 (en) 2010-12-10 2015-12-24 Altria Client Services Inc. Smokeless tobacco packaging system and method
RU2443330C1 (ru) * 2011-01-27 2012-02-27 Олег Иванович Квасенков Способ получения некурительного изделия из махорки
RU2452312C1 (ru) * 2011-02-18 2012-06-10 Олег Иванович Квасенков Способ получения некурительного изделия из махорки
RU2452315C1 (ru) * 2011-02-18 2012-06-10 Олег Иванович Квасенков Способ получения некурительного изделия из махорки
RU2451470C1 (ru) * 2011-02-21 2012-05-27 Олег Иванович Квасенков Способ получения некурительного изделия из махорки
RU2445871C1 (ru) * 2011-05-05 2012-03-27 Олег Иванович Квасенков Способ получения некурительного изделия из табака
RU2445872C1 (ru) * 2011-05-05 2012-03-27 Олег Иванович Квасенков Способ получения некурительного изделия из табака
US9474303B2 (en) * 2011-09-22 2016-10-25 R.J. Reynolds Tobacco Company Translucent smokeless tobacco product
US20130125904A1 (en) * 2011-11-18 2013-05-23 R.J. Reynolds Tobacco Company Smokeless tobacco product comprising pectin component
CN102524944B (zh) * 2012-01-19 2013-08-21 湖北中烟工业有限责任公司 一种专用于改善重组烟叶外观的颜色调节剂及其制备方法
US20130255702A1 (en) * 2012-03-28 2013-10-03 R.J. Reynolds Tobacco Company Smoking article incorporating a conductive substrate
WO2013146926A1 (fr) * 2012-03-28 2013-10-03 日本たばこ産業株式会社 Procédé de production d'une matière pour tabac, matière pour tabac à usage oral, et produit pour tabac à usage oral
WO2013146952A1 (fr) * 2012-03-30 2013-10-03 日本たばこ産業株式会社 Procédé de traitement de tabac
USD729974S1 (en) 2012-04-11 2015-05-19 British American Tobacco (Investments) Limited Oral tobacco
USD784604S1 (en) 2012-04-11 2017-04-18 British American Tobacco (Investments) Limited Oral tobacco
GB2501092A (en) * 2012-04-11 2013-10-16 British American Tobacco Co Oral tobacco product
USD784602S1 (en) 2012-04-11 2017-04-18 British American Tobacco (Investments) Limited Oral tobacco
USD784603S1 (en) 2012-04-11 2017-04-18 British American Tobacco (Investments) Limited Oral tobacco
WO2013192413A1 (fr) * 2012-06-20 2013-12-27 Mishra Munmaya K Granulés comprenant des lipides de tabac sans fumée
CN102940307B (zh) * 2012-11-19 2016-06-08 湖南中烟工业有限责任公司 一种用于口含型烟草制品的缓释碱性微胶囊及其制备方法和应用
GB201302485D0 (en) 2013-02-13 2013-03-27 British American Tobacco Co Tobacco Treatment
US9661876B2 (en) * 2013-03-14 2017-05-30 R.J. Reynolds Tobacco Company Sugar-enriched extract derived from tobacco
PT2991510T (pt) * 2013-05-02 2019-12-18 Jt Int Sa Material vaporizável
JP6129964B2 (ja) * 2013-06-19 2017-05-17 日本たばこ産業株式会社 たばこ原料の製造方法
GB201314917D0 (en) 2013-08-21 2013-10-02 British American Tobacco Co Treated Tobacco and processes for preparing the same, Devices including the same and uses thereof
US11503853B2 (en) * 2013-09-09 2022-11-22 R.J. Reynolds Tobacco Company Smokeless tobacco composition incorporating a botanical material
EP3051965B1 (fr) * 2013-10-03 2018-12-05 Philip Morris Products S.a.s. Produit de type tabac emballé comprenant du tabac pasteurisé
CN103494317A (zh) * 2013-10-08 2014-01-08 红塔烟草(集团)有限责任公司 一种基于新鲜烟叶制备的无烟气烟草制品
US10357054B2 (en) * 2013-10-16 2019-07-23 R.J. Reynolds Tobacco Company Smokeless tobacco pastille
EP3062639A1 (fr) * 2013-10-30 2016-09-07 Philip Morris Products S.A. Pasteurisation du tabac
GB201319288D0 (en) * 2013-10-31 2013-12-18 British American Tobacco Co Tobacco Material and Treatment Thereof
GB201319291D0 (en) * 2013-10-31 2013-12-18 Investments Ltd Tobacco Material and treatment thereof
CN103549648B (zh) * 2013-11-11 2016-08-17 云南烟草科学研究院 一种新型压片型无烟烟草制品及其制备方法
US9375033B2 (en) * 2014-02-14 2016-06-28 R.J. Reynolds Tobacco Company Tobacco-containing gel composition
CN103815541B (zh) * 2014-02-21 2016-09-21 湖北中烟工业有限责任公司 三层烟用水胶囊及其制备方法
CN103815542B (zh) * 2014-02-21 2016-09-21 湖北中烟工业有限责任公司 四层烟用水胶囊及其制备方法
US10239089B2 (en) 2014-03-14 2019-03-26 Altria Client Services Llc Product portion enrobing process and apparatus
EP3957190B1 (fr) 2014-03-14 2024-08-21 Altria Client Services LLC Produits de tabac sans fumée gainés de polymères
CN106659182B (zh) * 2014-06-27 2021-03-02 Wm.雷格利Jr.公司 含有钾盐的风味组合物
EP2976950A1 (fr) * 2014-07-21 2016-01-27 JT International S.A. Procédé de production d'un produit de tabac sans fumée en portions
JP6727128B2 (ja) * 2014-10-24 2020-07-22 日本たばこ産業株式会社 口腔用たばこ組成物及びその製造方法
MX2017007751A (es) * 2014-12-17 2017-09-05 Philip Morris Products Sa Pasteurizacion de tabaco cortado fino.
US20170280764A1 (en) * 2014-12-19 2017-10-05 Swedish Match North Europe Ab An oral smokeless moist snuff product
JP6001108B2 (ja) * 2015-02-02 2016-10-05 エクス−インターナショナル・エピエス 植物繊維製品およびその製造方法
CN104770861A (zh) * 2015-02-11 2015-07-15 贵州中烟工业有限责任公司 一种口含型无烟气烟草制品及其制备方法
CN104824823B (zh) * 2015-03-13 2017-11-28 广东中烟工业有限责任公司 提升再造烟叶感官质量的方法
CN106136314A (zh) * 2015-04-01 2016-11-23 上海烟草集团有限责任公司 一种烟碱可调节烟嘴
EP3280278B1 (fr) 2015-04-08 2019-05-29 Swedish Match North Europe AB Procédé de production d'un produit de tabac sans fumée en sachet comprenant un traitement thermique
US10881133B2 (en) 2015-04-16 2021-01-05 R.J. Reynolds Tobacco Company Tobacco-derived cellulosic sugar
US10532046B2 (en) * 2015-12-03 2020-01-14 Niconovum Usa, Inc. Multi-phase delivery compositions and products incorporating such compositions
US10499684B2 (en) 2016-01-28 2019-12-10 R.J. Reynolds Tobacco Company Tobacco-derived flavorants
GB201603866D0 (en) * 2016-03-07 2016-04-20 British American Tobacco Co Smokeless oral tobacco product and preperation thereof
EP4052592A1 (fr) * 2016-04-19 2022-09-07 Altria Client Services LLC Application d'une particule d'arôme dans le filtre d'un article à fumer pour distribuer un arôme
CN107912809A (zh) * 2016-10-10 2018-04-17 湖南中烟工业有限责任公司 一种电子烟烟液胶囊
CN106579538B (zh) * 2016-12-14 2018-05-11 湖北中烟工业有限责任公司 一种袋装口含烟及其制备方法
US11091446B2 (en) 2017-03-24 2021-08-17 R.J. Reynolds Tobacco Company Methods of selectively forming substituted pyrazines
EP3643184A4 (fr) * 2017-08-02 2021-05-05 Japan Tobacco, Inc. Procédé de production de liquide goût tabac, et liquide goût tabac
GB201713129D0 (en) * 2017-08-16 2017-09-27 British American Tobacco Investments Ltd Flour system
CN109757776A (zh) * 2017-11-09 2019-05-17 翟颖君 加热抽吸获取咖啡或茶中植物碱和香味物质的方法及产品
CN111035047A (zh) * 2018-10-15 2020-04-21 上海新型烟草制品研究院有限公司 一种口含烟制品
GB201817864D0 (en) * 2018-11-01 2018-12-19 Nicoventures Trading Ltd Aerosolisable formulation
GB201903083D0 (en) * 2019-03-07 2019-04-24 Nicoventures Trading Ltd Tobacco processing method
US11877590B2 (en) 2019-03-27 2024-01-23 Fiedler & Lundgren Ab Smokeless tobacco composition
US11730187B2 (en) 2019-05-08 2023-08-22 Gamot Global Pte. Ltd. Use of isothiocyanate in smokeless tobacco products
US11826462B2 (en) 2019-12-09 2023-11-28 Nicoventures Trading Limited Oral product with sustained flavor release
US11793230B2 (en) 2019-12-09 2023-10-24 Nicoventures Trading Limited Oral products with improved binding of active ingredients
US11969502B2 (en) 2019-12-09 2024-04-30 Nicoventures Trading Limited Oral products
US11872231B2 (en) 2019-12-09 2024-01-16 Nicoventures Trading Limited Moist oral product comprising an active ingredient
US11617744B2 (en) * 2019-12-09 2023-04-04 Nico Ventures Trading Limited Moist oral compositions
CN113925191B (zh) * 2020-06-29 2023-03-31 上海烟草集团有限责任公司 一种含茶口含烟及其制备方法
JP7235872B2 (ja) * 2020-07-06 2023-03-08 日本たばこ産業株式会社 口腔用たばこ製品
KR102525023B1 (ko) * 2020-08-14 2023-04-24 주식회사 케이티앤지 토스트엽을 포함하는 판상엽 시트 및 그의 제조방법, 그리고 상기 판상엽 시트를 포함하는 비연소형 흡연물품
EP4420534A1 (fr) 2021-10-20 2024-08-28 Sunsho Pharmaceutical Co., Ltd. Produit de tabac sans fumée à usage oral et capsule molle utilisée dans celui-ci
CN114403491B (zh) * 2022-02-18 2023-06-27 上海烟草集团有限责任公司 一种再造烟叶外观改善剂及其制备方法与应用
CN115015453A (zh) * 2022-06-15 2022-09-06 河南中烟工业有限责任公司 一种检测口用型无烟气烟草制品中甜味剂的前处理方法

Family Cites Families (167)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US509864A (en) * 1893-12-05 Lubricator
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
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
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
DE1553786B1 (de) 1964-12-09 1970-04-30 Payer Lux Scherkopf fuer Trockenrasierapparate
US3390686A (en) 1965-12-21 1968-07-02 American Tobacco Co Tobacco smoke filter element
US3353541A (en) 1966-06-16 1967-11-21 Philip Morris Inc Tobacco sheet material
US3398754A (en) 1966-06-27 1968-08-27 Gallaher Ltd Method for producing a reconstituted tobacco web
US3339558A (en) 1966-10-28 1967-09-05 Haskett Barry F Smoking article and filter therefor containing vitamin a
US3550598A (en) 1967-08-15 1970-12-29 James H Mcglumphy Reconstituted tobacco containing adherent encapsulated flavors and other matter
US3483874A (en) 1967-11-29 1969-12-16 Philip Morris Inc Process for the treatment of tobacco
US3612065A (en) 1970-03-09 1971-10-12 Creative Enterprises Inc Method of puffing tobacco and reducing nicotine content thereof
US3685521A (en) 1970-06-16 1972-08-22 H 2 O Filter Corp The Cigarette holder containing actuated carbon and frangible capsule
US3696917A (en) 1970-09-10 1972-10-10 Elaine G Levi Tobacco pouch closure
US3760815A (en) 1971-01-06 1973-09-25 Philip Morris Inc Preparation of reconstituted tobacco
US3889689A (en) 1971-12-20 1975-06-17 Rosen Enterprise Inc Method of treating tobacco with catalase and hydrogen peroxide
GB1400278A (en) 1972-06-06 1975-07-16 British American Tobacco Co Smoking articles
US3851653A (en) 1972-10-11 1974-12-03 Rosen Enterprises Inc Method of puffing tobacco and reducing nicotine content thereof
US3847164A (en) 1973-10-11 1974-11-12 Kimberly Clark Co Method of making reconstituted tobacco having reduced nitrates
US4034764A (en) 1975-08-15 1977-07-12 Philip Morris Incorporated Smoking material and method for its preparation
GB1550835A (en) 1975-08-18 1979-08-22 British American Tobacco Co Treatment of tobacco
US4194514A (en) 1976-09-27 1980-03-25 Stauffer Chemical Company Removal of radioactive lead and polonium from tobacco
US4131117A (en) 1976-12-21 1978-12-26 Philip Morris Incorporated Method for removal of potassium nitrate from tobacco extracts
US4150677A (en) 1977-01-24 1979-04-24 Philip Morris Incorporated Treatment of tobacco
US4270552A (en) 1977-10-04 1981-06-02 Brown & Williamson Tobacco Corporation Process and apparatus for producing paper reconstituted tobacco
US4308877A (en) 1978-03-06 1982-01-05 Kimberly-Clark Corporation Method of making reconstituted tobacco having reduced nitrates
US4341228A (en) 1981-01-07 1982-07-27 Philip Morris Incorporated Method for employing tobacco dust in a paper-making type preparation of reconstituted tobacco and the smoking material produced thereby
US4421126A (en) 1981-06-04 1983-12-20 Philip Morris Incorporated Process for utilizing tobacco fines in making reconstituted 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
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
US4534372A (en) 1983-08-22 1985-08-13 R. J. Reynolds Tobacco Company Smoking product
US4596259A (en) 1983-08-22 1986-06-24 R. J. Reynolds Tobacco Company Smoking material and method for its preparation
DK149920C (da) 1983-09-20 1987-05-18 Krueger S Eftf A S Hermann Fremgangsmaade ved portionering af snus og emballering af de enkelte snusportioner
DE3344554A1 (de) 1983-12-09 1985-06-20 B.A.T. Cigaretten-Fabriken Gmbh, 2000 Hamburg Rauchprodukt, enthaltend nicotin-n' -oxid
US5092352A (en) 1983-12-14 1992-03-03 American Brands, Inc. Chewing tobacco product
SE450566B (sv) 1983-12-14 1987-07-06 Svenska Tobaks Ab Anordning for att portionsforpacka snus
US4674519A (en) 1984-05-25 1987-06-23 Philip Morris Incorporated Cohesive tobacco composition
US4624269A (en) 1984-09-17 1986-11-25 The Pinkerton Tobacco Company Chewable tobacco based product
US4706692A (en) 1985-12-30 1987-11-17 Philip Morris Incorporated Method and apparatus for coating reconstituted tobacco
US5004595A (en) 1986-12-23 1991-04-02 Warner-Lambert Company Multiple encapsulated flavor delivery system and method of preparation
FR2613713B1 (fr) 1987-04-07 1989-08-04 Roquette Freres Procede de preparation de diacetals d'alditols, notamment du dibenzylidene-sorbitol, en milieu aqueux
KR910000142B1 (ko) 1987-05-29 1991-01-21 니혼 다바고 상교오 가부시기가이샤 담배용 필터
US4882128A (en) 1987-07-31 1989-11-21 Parr Instrument Company Pressure and temperature reaction vessel, method, and apparatus
US4821749A (en) 1988-01-22 1989-04-18 R. J. Reynolds Tobacco Company Extruded tobacco materials
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
US6056992A (en) 1988-06-02 2000-05-02 Campbell Soup Company Encapsulated additives
US4987907A (en) 1988-06-29 1991-01-29 Helme Tobacco Company Chewing tobacco composition and process for producing same
US4962774A (en) 1988-11-16 1990-10-16 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US4967771A (en) 1988-12-07 1990-11-06 R. J. Reynolds Tobacco Company Process for extracting tobacco
US4972854A (en) 1989-05-24 1990-11-27 Philip Morris Incorporated Apparatus and method for manufacturing tobacco sheet material
US4941484A (en) 1989-05-30 1990-07-17 R. J. Reynolds Tobacco Company Tobacco processing
US4987906A (en) 1989-09-13 1991-01-29 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US5056537A (en) 1989-09-29 1991-10-15 R. J. Reynolds Tobacco Company Cigarette
US5101839A (en) 1990-08-15 1992-04-07 R. J. Reynolds Tobacco Company Cigarette and smokable filler material therefor
US5121757A (en) 1989-12-18 1992-06-16 R. J. Reynolds Tobacco Company Tobacco treatment process
US5099864A (en) * 1990-01-05 1992-03-31 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US5167244A (en) 1990-01-19 1992-12-01 Kjerstad Randy E Tobacco substitute
US5234008A (en) 1990-02-23 1993-08-10 R. J. Reynolds Tobacco Company Tobacco processing
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
US5327917A (en) 1990-08-15 1994-07-12 R. J. Reynolds Tobacco Company Method for providing a reconstituted tobacco material
US5962662A (en) 1990-12-20 1999-10-05 R.J. Reynolds Tobacco Company Method for producing a flavorful and aromatic composition for use in smoking articles
US5143097A (en) 1991-01-28 1992-09-01 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US5131415A (en) 1991-04-04 1992-07-21 R. J. Reynolds Tobacco Company Tobacco extraction process
JP3159724B2 (ja) 1991-04-19 2001-04-23 フロイント産業株式会社 シームレスカプセル製造方法および装置
US5186948A (en) 1991-05-28 1993-02-16 Freund Inphachem Inc. Apparatus for manufacturing seamless capsules
US5318050A (en) 1991-06-04 1994-06-07 R. J. Reynolds Tobacco Company Tobacco treatment process
US5159942A (en) 1991-06-04 1992-11-03 R. J. Reynolds Tobacco Company Process for providing smokable material for a cigarette
US5343879A (en) 1991-06-21 1994-09-06 R. J. Reynolds Tobacco Company Tobacco treatment process
US5203354A (en) 1991-06-28 1993-04-20 Philip Morris Incorporated Restructured tobacco dryer
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
US5501237A (en) 1991-09-30 1996-03-26 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US5413122A (en) 1992-02-18 1995-05-09 R. J. Reynolds Tobacco Company Method of providing flavorful and aromatic compounds
US5759599A (en) 1992-03-30 1998-06-02 Givaudan Roure Flavors Corporation Method of flavoring and mechanically processing foods with polymer encapsulated flavor oils
JP3681410B2 (ja) 1992-04-09 2005-08-10 フィリップ・モーリス・プロダクツ・インコーポレイテッド 再構成タバコシート及びその製造法及び使用法
US5339838A (en) 1992-08-17 1994-08-23 R. J. Reynolds Tobacco Company Method for providing a reconstituted tobacco material
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
US5325877A (en) 1993-07-23 1994-07-05 R. J. Reynolds Tobacco Company Tobacco reconstitution process
AU675573B2 (en) 1993-09-30 1997-02-06 British-American Tobacco Company Limited Improvements relating to tobacco smoke filter elements
US5370139A (en) 1993-10-14 1994-12-06 R. J. Reynolds Tobacco Company Tobacco treatment process
US5690990A (en) 1994-03-04 1997-11-25 Arnhem, Inc. Process for encapsulating the flavor with colloid gel matrix
US5533530A (en) 1994-09-01 1996-07-09 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US6117455A (en) 1994-09-30 2000-09-12 Takeda Chemical Industries, Ltd. Sustained-release microcapsule of amorphous water-soluble pharmaceutical active agent
GR1002575B (el) 1995-04-07 1997-02-06 Μεθοδος και συσκευη αφαιρεσεως βλαπτικων ουσιων εκ των σιγαρεττων προ της καταναλωσεως.
WO1997013419A2 (fr) 1995-10-11 1997-04-17 Derr Dedric M Systeme et methode de protection des muqueuses de la bouche contre le tabac a chiquer
US5598866A (en) 1995-11-06 1997-02-04 Nelson; Cliff H. Portable well testing apparatus
JP3759986B2 (ja) 1995-12-07 2006-03-29 フロイント産業株式会社 シームレスカプセルおよびその製造方法
US5997691A (en) 1996-07-09 1999-12-07 Philip Morris Incorporated Method and apparatus for applying a material to a web
US6591841B1 (en) 1996-08-01 2003-07-15 Jackie Lee White Method of providing flavorful and aromatic tobacco suspension
BR9711875A (pt) 1996-10-09 1999-08-24 Givaudan Roure Int Processo para a prepara-Æo de contas como aditivo alimenticio ou de tabaco
JP3881699B2 (ja) 1996-10-09 2007-02-14 ジボーダン―ルール(アンテルナシヨナル)ソシエテ アノニム 食品添加剤としてのビーズの製造方法
US6039901A (en) 1997-01-31 2000-03-21 Givaudan Roure Flavors Corporation Enzymatically protein encapsulating oil particles by complex coacervation
US6106875A (en) 1997-10-08 2000-08-22 Givaudan Roure (International) Sa Method of encapsulating flavors and fragrances by controlled water transport into microcapsules
US6045835A (en) 1997-10-08 2000-04-04 Givaudan Roure (International) Sa Method of encapsulating flavors and fragrances by controlled water transport into microcapsules
US6048404A (en) 1998-05-07 2000-04-11 R.J. Reynolds Tobacco Company Tobacco flavoring components of enhanced aromatic content and method of providing same
US6596298B2 (en) 1998-09-25 2003-07-22 Warner-Lambert Company Fast dissolving orally comsumable films
US6083527A (en) 1998-11-05 2000-07-04 Thistle; Robert Breath mint with tooth decay and halitosis prevention characteristics
US6298858B1 (en) 1998-11-18 2001-10-09 R. J. Reynolds Tobacco Company Tobacco flavoring components of enhanced aromatic content and method of providing same
US6428624B1 (en) 1998-12-07 2002-08-06 R. J. Reynolds Tobacco Co. Method of providing flavorful and aromatic compounds
US6805134B2 (en) 1999-04-26 2004-10-19 R. J. Reynolds Tobacco Company Tobacco processing
US6216706B1 (en) 1999-05-27 2001-04-17 Philip Morris Incorporated Method and apparatus for producing reconstituted tobacco sheets
ZA200003120B (en) 1999-06-30 2001-01-02 Givaudan Roure Int Encapsulation of active ingredients.
DE60020716T2 (de) 1999-07-22 2005-12-15 Warner-Lambert Co. Llc Filmbildende zusammensetzungen aus pullulan
EP1240883A4 (fr) 1999-12-20 2007-05-30 Chugai Pharmaceutical Co Ltd Procede de fabrication de gelules sans raccord
US6325860B1 (en) 2000-02-15 2001-12-04 R. J. Reynolds Tobacco Company Method of providing flavorful and aromatic compounds in absence of reducing sugars
US6371126B1 (en) 2000-03-03 2002-04-16 Brown & Williamson Tobacco Corporation Tobacco recovery system
US6695924B1 (en) 2000-07-25 2004-02-24 Michael Francis Dube Method of improving flavor in smoking article
US6834654B2 (en) 2001-05-01 2004-12-28 Regent Court Technologies, Llc Smokeless tobacco product
US6612429B2 (en) 2001-06-22 2003-09-02 Brown & Williamson Tobacco Corporation Flip open package with microencapsulated flavor release
KR20030009800A (ko) 2001-07-24 2003-02-05 김진희 담배맛 변경이 가능한 담배
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
CN1167364C (zh) * 2001-10-25 2004-09-22 南京大学 纳米孔香烟助燃降害添加剂
AU2002340407A1 (en) * 2001-11-09 2003-05-26 Vector Tobacco Inc. Method and composition for mentholation of charcoal filtered cigarettes
FR2832632B1 (fr) 2001-11-26 2004-04-23 Mane Fils V Capsule a solubilisation et liberation du contenu rapides
AU2002360097A1 (en) 2001-12-21 2003-07-09 Galenica Ab Tobacco and/or tobacco substitute composition for use as a snuff in the oral cavity
US6949256B2 (en) 2002-01-18 2005-09-27 Banner Pharmacaps, Inc. Non-gelatin capsule shell formulation
US7025066B2 (en) 2002-10-31 2006-04-11 Jerry Wayne Lawson Method of reducing the sucrose ester concentration of a tobacco mixture
EP1572164A2 (fr) 2002-12-18 2005-09-14 Pain Therapeutics, Inc. Formes posologiques orales comprenant des agents actifs au plan therapeutique dans des noyaux a liberation lente et des revetements de capsule en gelatine a liberation immediate
US20040118422A1 (en) 2002-12-19 2004-06-24 Swedish Match North Europe Ab Tobacco dough and a method for its manufacture
US20040173228A1 (en) 2003-03-04 2004-09-09 R. J. Reynolds Tobacco Company Method for producing flavorful and aromatic compounds from tobacco
SE0301244D0 (sv) 2003-04-29 2003-04-29 Swedish Match North Europe Ab Smokeless tobacco product user package
US7293564B2 (en) 2003-06-11 2007-11-13 R. J. Reynolds Tobacco Company Method for chemically modifying tobacco during curing
US7014039B2 (en) 2003-06-19 2006-03-21 R.J. Reynolds Tobacco Company Sliding shell package for smoking articles
US7836895B2 (en) 2003-06-23 2010-11-23 R. J. Reynolds Tobacco Company Filtered cigarette incorporating a breakable capsule
US7784083B2 (en) 2003-07-08 2010-08-24 Panasonic Corporation Receiving/generating section information for multimedia contents based on level of performance
CN100508976C (zh) 2003-07-24 2009-07-08 史密丝克莱恩比彻姆公司 口腔溶解薄膜
SE527350C8 (sv) 2003-08-18 2006-03-21 Gallaher Snus Ab Lock till snusdosa
US7115085B2 (en) 2003-09-12 2006-10-03 R.J. Reynolds Tobacco Company Method and apparatus for incorporating objects into cigarette filters
BRPI0415682A (pt) 2003-11-03 2006-12-19 Us Smokeless Tobacco Co tabaco sem fumaça aromatizado e métodos de fabricação
US8469036B2 (en) 2003-11-07 2013-06-25 U.S. Smokeless Tobacco Company Llc Tobacco compositions
US8627828B2 (en) 2003-11-07 2014-01-14 U.S. Smokeless Tobacco Company Llc Tobacco 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
US20060228308A1 (en) 2004-02-26 2006-10-12 Cummins Barry W Oral health care drink and method for reducing malodors
US20050196437A1 (en) 2004-03-02 2005-09-08 Bednarz Christina A. Hard capsules
EP1593376A1 (fr) 2004-05-04 2005-11-09 Warner-Lambert Company LLC Gélules de pullulane ameliorées
US8408216B2 (en) 2004-12-22 2013-04-02 Philip Morris Usa Inc. Flavor carrier for use in smoking articles
US10285431B2 (en) 2004-12-30 2019-05-14 Philip Morris Usa Inc. Encapsulated flavorant designed for thermal release and cigarette bearing the same
US7578298B2 (en) 2005-02-04 2009-08-25 Philip Morris Usa Inc. Flavor capsule for enhanced flavor delivery in cigarettes
US20060210488A1 (en) 2005-03-19 2006-09-21 Jakubowski Henryk P Teeth whitening candy with tartar removal and breath freshening properties
EA012674B1 (ru) 2005-04-29 2009-12-30 Филип Моррис Продактс С.А. Табачный продукт в пакетиках
US7878962B2 (en) 2005-05-03 2011-02-01 Philip Morris Usa Inc. Cigarettes and filter subassemblies with squeezable flavor capsule and methods of manufacture
WO2006136197A1 (fr) 2005-06-21 2006-12-28 V. Mane Fils Produit a fumer comprenant une capsule cassante, capsule cassante et procede de fabrication de cette capsule
PL1906775T3 (pl) 2005-06-21 2010-01-29 V Mane Fils Urządzenie do palenia zawierające łamliwą kapsułkę, łamliwa kapsułka i sposób wytwarzania wymienionej kapsułki
WO2006136199A1 (fr) 2005-06-21 2006-12-28 V.Mane Fils Article pour fumeur contenant une capsule frangible, capsule frangible et procede de fabrication associe
EP1754419A1 (fr) 2005-08-15 2007-02-21 Philip Morris Products S.A. Dispositif pour la liberation de liquide dans un article à fumer
US20070062549A1 (en) 2005-09-22 2007-03-22 Holton Darrell E Jr Smokeless tobacco composition
ES2446242T3 (es) * 2005-09-22 2014-03-06 R. J. Reynolds Tobacco Company Composición de tabaco sin humo
US7479098B2 (en) 2005-09-23 2009-01-20 R. J. Reynolds Tobacco Company Equipment for insertion of objects into smoking articles
PL1942753T3 (pl) 2005-11-01 2009-10-30 Philip Morris Products Sa Wyrób tytoniowy z ręcznie uwalnianym środkiem zapachowym
US8053008B2 (en) 2005-11-21 2011-11-08 Philip Morris Usa Inc. Method of manufacturing flavor pouches
US8685478B2 (en) 2005-11-21 2014-04-01 Philip Morris Usa Inc. Flavor pouch

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023084499A1 (fr) * 2021-11-15 2023-05-19 Nicoventures Trading Limited Produits présentant des caractéristiques sensorielles améliorées
WO2023187412A1 (fr) * 2022-04-01 2023-10-05 Nicoventures Trading Limited Produit comprenant un récipient perméable et un extrait séché à partir d'un matériau végétal et ses utilisations
WO2024194187A1 (fr) * 2023-03-17 2024-09-26 Philip Morris Products S.A. Sachet à usage oral comprenant un matériau d'arôme immobilisé à l'intérieur d'une matrice polysaccharidique

Also Published As

Publication number Publication date
WO2009015142A8 (fr) 2010-01-28
EP2173200A2 (fr) 2010-04-14
EP2179666B1 (fr) 2012-08-29
EP2179666A2 (fr) 2010-04-28
WO2009015142A2 (fr) 2009-01-29
CN101873809A (zh) 2010-10-27
EP2377413B1 (fr) 2017-03-01
DK2377413T3 (en) 2017-05-01
EP2377413A1 (fr) 2011-10-19
EP2179666A3 (fr) 2010-09-22
JP5339635B2 (ja) 2013-11-13
CN101873809B (zh) 2014-11-12
WO2009015142A3 (fr) 2009-08-27
JP2010534475A (ja) 2010-11-11

Similar Documents

Publication Publication Date Title
US10219537B2 (en) Smokeless tobacco composition
EP2173200B1 (fr) Composition de tabac sans fumée, et procédés pour traiter le tabac destiné à y être utilisé
US7810507B2 (en) Smokeless tobacco composition
US7946295B2 (en) Smokeless tobacco composition
DK2173200T3 (en) Smokeless tobacco compositions and methods of treating tobacco for use therein
EP1926401B1 (fr) Composition de tabac qui ne se fume pas
US7861728B2 (en) Smokeless tobacco composition having an outer and inner pouch
US20070062549A1 (en) Smokeless tobacco composition
US20210169790A1 (en) Fleece for oral product with releasable component
EP4072331A1 (fr) Produits en sachet

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20100128

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA MK RS

DAX Request for extension of the european patent (deleted)
RIN1 Information on inventor provided before grant (corrected)

Inventor name: CANTRELL, DANIEL, VERDIN

Inventor name: MCCLANAHAN, DAVID, NEIL

Inventor name: MUA, JOHN-PAUL

Inventor name: HOLTON, DARRELL, EUGENE JR.

Inventor name: FIGLAR, JAMES, NEIL

Inventor name: BRINKLEY, PAUL, ANDREW

Inventor name: MONSALUD, LUIS, ROSETE JR.

Inventor name: DUBE, MICHAEL, FRANCIS

Inventor name: FLINCHUM, JACK, GRAY JR.

Inventor name: STOKES, CYNTHIA, STEWART

17Q First examination report despatched

Effective date: 20101230

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

INTG Intention to grant announced

Effective date: 20170529

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

Ref country code: GB

Ref legal event code: FG4D

Ref country code: AT

Ref legal event code: REF

Ref document number: 945395

Country of ref document: AT

Kind code of ref document: T

Effective date: 20171115

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

Effective date: 20171221

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602008052994

Country of ref document: DE

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2659715

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20180319

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20171115

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 945395

Country of ref document: AT

Kind code of ref document: T

Effective date: 20171115

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180215

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180216

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180215

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 11

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602008052994

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20180817

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180722

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20180731

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180731

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180731

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180722

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180731

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180722

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20080722

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171115

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180315

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230504

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20230808

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20240530

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20240611

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20240611

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20240612

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20240604

Year of fee payment: 17

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DK

Payment date: 20240712

Year of fee payment: 17