EP2779849B1 - Smokeless tobacco product comprising tobacco-derived pectin component - Google Patents

Smokeless tobacco product comprising tobacco-derived pectin component Download PDF

Info

Publication number
EP2779849B1
EP2779849B1 EP12795236.4A EP12795236A EP2779849B1 EP 2779849 B1 EP2779849 B1 EP 2779849B1 EP 12795236 A EP12795236 A EP 12795236A EP 2779849 B1 EP2779849 B1 EP 2779849B1
Authority
EP
European Patent Office
Prior art keywords
tobacco
pectin
smokeless
product
smokeless tobacco
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
EP12795236.4A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP2779849A1 (en
Inventor
Gong Chen
Margarette Elisa Lovette
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
Application filed by RJ Reynolds Tobacco Co filed Critical RJ Reynolds Tobacco Co
Publication of EP2779849A1 publication Critical patent/EP2779849A1/en
Application granted granted Critical
Publication of EP2779849B1 publication Critical patent/EP2779849B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • A24B15/30Treatment of tobacco products or tobacco substitutes by chemical substances by organic 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
    • A24B15/24Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts

Definitions

  • the present disclosure relates to products made or derived from tobacco, or that otherwise incorporate tobacco, and are intended for human consumption.
  • the disclosure relates to compositions or formulations incorporating tobacco, and that are intended to be employed in a smokeless form.
  • Cigarettes, cigars, and pipes are popular smoking articles that employ tobacco in various forms. Such smoking articles are employed by heating or burning tobacco to generate aerosol (e.g., smoke) that may be inhaled by the smoker. Tobacco may also 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. See for example, the types of smokeless tobacco formulations, ingredients, and processing methodologies set forth in US Pat. Nos. 1,376,586 to Schwartz ; 3,696,917 to Levi ; 4,513,756 to Pittman et al. ; 4,528,993 to Sensabaugh, Jr. et al.
  • Exemplary smokeless tobacco products that have been marketed include those referred to as CAMEL Snus, CAMEL Orbs, CAMEL Strips and CAMEL Sticks by R. J.
  • the present disclosure relates to a smokeless tobacco product configured for insertion into the mouth of a user and processes for preparing a smokeless tobacco composition suitable for use in a smokeless tobacco product.
  • the smokeless tobacco composition incorporates a pectin component derived from tobacco or a tobacco material.
  • Various properties can be imparted to the tobacco product by the tobacco-derived pectin material and such properties can be impacted, for example, by selection of the pectin source (e.g., which part or parts of the tobacco material is used), the techniques used to extract and isolate the pectin, and by any intentional or unintentional modification of the pectin structure.
  • the tobacco-derived pectin can provide various attributes to the smokeless tobacco product.
  • the pectin may provide some degree of integrity to the smokeless tobacco product.
  • the smokeless tobacco product may, in certain embodiments, be held together in whole or in part by the pectin component. Further, incorporation of tobacco-derived pectin within a smokeless tobacco product can give a product having a higher content of tobacco-derived components.
  • a smokeless tobacco product configured for insertion into the mouth of a user, the smokeless tobacco product comprising a tobacco material and a binder component, the binder component comprising a tobacco-derived pectin material in accordance with claim 1.
  • the tobacco-derived pectin material is the only binder component therein.
  • the smokeless tobacco product can be extruded.
  • the smokeless tobacco product can be, for example, in the form of a pill, pellet, tablet, coin, bead, ovoid, obloid, cube, film, flake, stick, foam, or gel.
  • the smokeless tobacco product is dissolvable.
  • the smokeless tobacco product comprises greater than about 3% by weight of the tobacco-derived pectin material or greater than about 4% by weight of tobacco-derived pectin material.
  • the smokeless tobacco product further comprises one or more components selected from the group consisting of flavorants, sweeteners, salts, fillers, fats, emulsifiers, gelling agents, disintegration aids, compressability aids, colorants, humectants, pH adjusters, buffering agents, oral care additives, preservatives, syrups, and mixtures thereof.
  • the tobacco material is in particulate form with an average particle size of less than about 50 microns.
  • the invention provides a smokeless tobacco product comprising a tobacco material (e.g., a milled tobacco material or an aqueous tobacco extract) in an amount of 20 to 50 dry weight percent; a tobacco-derived pectin material in an amount of 2 to 10 dry weight percent; one or more fillers (e.g., at least one rice-derived filler material) in an amount of 10 to 40 dry weight percent; one or more sweeteners (e.g., at least one sugar alcohol) in any amount of 5 to 15 dry weight percent; and at least one flavorant in an amount up to 5 dry weight percent.
  • the product may further include an additional binder component, such as a natural gum.
  • a method of preparing a smokeless tobacco product comprising: extracting pectin from a first tobacco material to form a tobacco-derived pectin material; combining the tobacco-derived pectin material with a second tobacco material to form a smokeless tobacco composition; and incorporating the resulting composition into a smokeless tobacco product (e.g., by forming the composition into a desired product shape such as by extrusion).
  • the extracting step is conducted with an aqueous solution.
  • the aqueous solution comprises one or more components selected from the group consisting of surfactants, co-solvents, enzymes, and pH adjusters.
  • the extracting step comprises mixing a cured tobacco material with an aqueous solution of oxalic acid and/or ammonium oxalate and collecting an aqueous extract.
  • the extracting step further comprises adding a second solvent to the aqueous extract to effect precipitation of a pectin material and collecting the precipitated pectin material.
  • the method further comprises treating the first tobacco material with a pectin releasing agent prior to the extracting step.
  • the first tobacco material comprises tobacco stem, tobacco lamina, or a combination thereof. In some embodimetns, the first tobacco material is a cured tobacco material.
  • the method comprises mixing a cured first tobacco material with an aqueous solution of oxalic acid and/or ammonium oxalate and collecting an aqueous extract. In certain embodiments, the method further comprises combining the extracted pectin with a second tobacco material to produce a smokeless tobacco product.
  • the present invention can provide smokeless tobacco compositions suitable for oral use.
  • the smokeless tobacco compositions generally include a tobacco material, one or more pectin components, and optionally one or more additional components as described herein.
  • at least one pectin component is derived from tobacco.
  • the products of the disclosure incorporate some form of a plant of the Nicotiana species, and most preferably, those compositions or products incorporate some form of tobacco.
  • the selection of the Nicotiana species can vary; and in particular, the selection of the types of tobacco or tobaccos may vary.
  • Tobaccos that can be employed include flue-cured or Virginia (e.g., K326), burley, sun-cured (e.g., Indian Kurnool and Oriental tobaccos, including Katerini, Prelip, Komotini, Xanthi and Yambol tobaccos), Maryland, dark, dark-fired, dark air cured (e.g., Passanda, Cubano, Jatin and Bezuki tobaccos), light air cured (e.g., North Wisconsin and Galpao tobaccos), Indian air cured, Red Russian and Rustica tobaccos, as well as various other rare or specialty tobaccos.
  • flue-cured or Virginia e.g., K326)
  • burley sun-cured
  • Nicotiana species include N. tabacum, N.
  • Nicotiana species can be derived using genetic-modification or crossbreeding techniques (e.g., tobacco plants can be genetically engineered or crossbred to increase or decrease production of components, characteristics or attributes). See, for example, the types of genetic modifications of plants set forth in US Pat. Nos. 5,539,093 to Fitzmaurice et al. ; 5,668,295 to Wahab et al. ; 5,705,624 to Fitzmaurice et al. ; 5,844,119 to Weigl ; 6,730,832 to Dominguez et al. ; 7,173,170 to Liu et al. ; 7,208,659 to Colliver et al. and 7,230,160 to Benning et al. ; US Patent Appl. Pub. No. 2006/0236434 to Conkling et al. ; and PCT WO 2008/103935 to Nielsen et al.
  • tobaccos can be subjected to alternative types of curing processes, such as fire curing or sun curing.
  • harvested tobaccos that are cured are then aged.
  • tobaccos used for the preparation of tobacco compositions or products most preferably incorporate components of tobaccos that have been cured and aged.
  • tobacco materials used in the present invention can be subjected to additional processing prior to use, such as fermentation, bleaching, and the like.
  • At least a portion of the plant of the Nicotiana species can be employed in an immature form. That is, the plant, or at least one portion of that plant, can be harvested before reaching a stage normally regarded as ripe or mature. As such, for example, tobacco can be harvested when the tobacco plant is at the point of a sprout, is commencing leaf formation, is commencing flowering, or the like.
  • At least a portion of the plant of the Nicotiana species can be employed in a mature form. That is, the plant, or at least one portion of that plant, can be harvested when that plant (or plant portion) reaches a point that is traditionally viewed as being ripe, over-ripe or mature.
  • Oriental tobacco plants can be harvested, burley tobacco plants can be harvested, or Virginia tobacco leaves can be harvested or primed by stalk position.
  • the tobacco material may be cased and dried, and then ground to the desired form.
  • the tobacco material formulation 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.
  • Nonaqueous casing components may be applied to the tobacco in amounts of about 1 percent to about 15 percent, based on the dry weight of the tobacco.
  • the tobacco material is typically used in a form that can be described as particulate (i.e., shredded, ground, granulated, or powder form).
  • the manner by which the tobacco material is provided in a finely divided or powder type of form may vary.
  • plant parts or pieces are comminuted, ground or pulverized into a particulate form using equipment and techniques for grinding, milling, or the like.
  • the plant material 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 or less than about 5 weight percent.
  • the tobacco material is employed in the form of parts or pieces that have an average particle size less than 50 microns.
  • the average particle size of the tobacco particles may be less than or equal to about 25 microns.
  • the tobacco particles may be sized to pass through a screen mesh. If desired, air classification equipment may be used to ensure that small sized tobacco particles of the desired sizes, or range of sizes, may be collected. If desired, differently sized pieces of granulated tobacco may be mixed together.
  • At least a portion of the tobacco material employed in the tobacco composition or product can have the form of an extract.
  • Tobacco extracts can be obtained by extracting tobacco using a solvent having an aqueous character such as distilled water or tap water.
  • aqueous tobacco extracts can be provided by extracting tobacco with water, such that water insoluble pulp material is separated from the aqueous solvent and the water soluble and dispersible tobacco components dissolved and dispersed therein.
  • the tobacco extract can be employed in a variety of forms.
  • the aqueous tobacco extract can be isolated in an essentially solvent free form, such as can be obtained as a result of the use of a spray drying or freeze drying process, or other similar types of processing steps.
  • the aqueous tobacco extract can be employed in a liquid form, and as such, the content of tobacco solubles within the liquid solvent can be controlled by selection of the amount of solvent employed for extraction, concentration of the liquid tobacco extract by removal of solvent, addition of solvent to dilute the liquid tobacco extract, or the like.
  • Exemplary techniques for extracting components of tobacco are described in US Pat. Nos. 4,144,895 to Fiore ; 4,150,677 to Osborne, Jr. et al. ; 4,267,847 to Reid ; 4,289,147 to Wildman et al .; 4,351,346 to Brummer et al. ; 4,359,059 to Brummer et al.
  • the relative amount of tobacco material within the smokeless tobacco composition is at least 20 percent, on a dry weight basis of the composition, and including all sources of tobacco including tobacco components and any tobacco-derived components such as binders. In certain instances, the amounts of other components within the smokeless tobacco composition may exceed about 40 percent, on a dry weight basis.
  • the range of tobacco material within the smokeless tobacco composition is 20 to 50 dry weight percent.
  • the tobacco material may, in certain embodiments, be subjected to thermal or convection heating to control the moisture content thereof prior to incorporating it within a smokeless tobacco product according to the present invention.
  • the tobacco material formulation may be oven-dried, in warmed air at temperatures of about 40°C to about 95°C for a length of time appropriate to attain the desired moisture content.
  • the tobacco material formulation maybe dried for about 12 hours to about 24 hours at about 54°C to about 60°C.
  • 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 tobacco material formulation may be prepared, followed by irradiation or pasteurization, and then flavoring ingredient(s) may be applied to the formulation. Representative processes are set forth in US Pat. Pub. Nos. 2009/0025738 to Mua et al ; 2009/0025739 to Brinkley et al. ; and 2011/0247640 to Beeson et al.
  • the smokeless tobacco products of the present invention comprise a binder component that includes pectin.
  • pectin refers to a complex group of polysaccharides principally comprising 1,4-linked ⁇ -D-galactosyluronic acid residues. Typically, pectin comprises at least about 65% such subunits.
  • the acid groups present on these residues can be free acids, combined as a methyl ester, or in salt form (e.g., as sodium, potassium, calcium, or ammonium salts).
  • the molecular weight of pectin can vary; for example, the number average molecular weight can be from about 60 Da to about 13,0000 Da, and can vary based on origin and extraction conditions.
  • pectic polysaccharides include polygalacturonan (comprising linear galacturonic acid subunits), rhamnogalacturonan I (RG1, comprising alternating rhamnose and galacturonic acid subunits), and rhamnogalacturonan II (RG2, a complex, highly branched polysaccharide).
  • Pectin is often characterized in terms of its "hairy” and “smooth" regions. Hairy regions of pectin are portions of the molecule that are very flexible and which may comprise many neutral sugar molecules, such as rhamnose, galactose, arabinose, and/or other sugars, in a highly branched structure. Smooth regions of pectin are portions of the molecule that comprise primarily homogalacturonic acid.
  • Pectin is found in most plants, for example, in the cell walls (where the pectin acts as a binder to hold the cell walls together).
  • the amount and characteristics of pectin in different plants can vary significantly.
  • pectin from different tissues of the plant and pectin present in the plant at different stages of development can exhibit different characteristics.
  • the arrangement and amounts of various monosaccharide derivative units, the degree of esterification, and the polymer lengths of the heteropolysaccharides can vary significantly.
  • pectin within a given pectin sample can depend on the extraction method. For example, commercial extraction of pectin often causes extensive degradation of the neutral sugar-containing sidechains of the polysaccharide. In other words, most extraction methods result in the destruction of many of the hairy regions of the pectin, leaving mainly smooth galacturonic acid regions, with only a few neutral sugar units attached to and/or in the main linear chain. These neutral sugar units remaining can vary in nature and location on the pectin chain and can influence the properties of pectin.
  • a given sample of pectin can comprise some degree of pectin derivatives.
  • pectin derivatives can be naturally occurring in the pectin sample or the sample can be treated in some way to promote formation of one or more pectin derivatives.
  • Pectin derivatives include, but are not limited to, protopectin, pectinic acid, esterified pectin, wherein one or more carboxylic acid groups are methylated, pectin salts, and/or pectic acid. Esterification is common, and the degree of esterification typically determines the degree of reactivity of the pectin or derivative thereof with calcium and other cations.
  • Pectin as extracted generally has greater than about 50% of its acidic functionalities esterified, and is thus sometimes classified as "high methyl ester (HM) pectin.” Modification of the extraction process (e.g., extended hydrolysis) or continued acid treatment will typically give a "low methyl ester (LM) pectin,” with less than about 50% methyl ester groups. Pectin can be treated, in some embodiments, during and/or following extraction and isolation of the pectin to alter the degree of esterification. For example, in certain embodiments, controlled removal of methoxy groups (i.e., de-esterification) is done to convert HM pectin to LM pectin.
  • methoxy groups i.e., de-esterification
  • This conversion can be accomplished, for example, with pectin methylesterases and/or via extended hydrolysis. Some pectins are treated during manufacture with ammonia to produce amidated pectins. Some pectins are partially or completely converted to salts (e.g., by modifying the carboxyl groups of the D-galactopyranosyluronic acid residues).
  • smokeless tobacco products comprise pectin derived from tobacco.
  • tobacco-derived pectin refers to a pectin material extracted or isolated from a tobacco plant or portion thereof, and such material is understood to have a variable level of purity with respect to pectin and, accordingly, can include other components extracted or isolated from tobacco in addition to pectin.
  • the method by which pectin is derived from a tobacco material can vary.
  • the pectin can be derived from any part of a tobacco plant or portion thereof (e.g., leaves, seeds, flowers, stalks, roots, and/or stems).
  • the pectin is derived from tobacco lamina and/or stem. Pectin from various locations of the tobacco plant can be kept separate, or pectin from various locations within the tobacco plant can be combined and processed and/or used in combination according to the present invention. In some embodiments, the tobacco material is cured prior to the process of isolating the pectin therefrom.
  • tobacco is treated so as to provide the pectin contained therein in a more usable (e.g., more concentrated) form.
  • the pectin can be isolated from tobacco or tobacco materials using any suitable method.
  • one or more extraction processes are used to first isolate the pectin into an extraction solvent.
  • tobacco or a tobacco material is first extracted (e.g., with water or an aqueous solution of one or more reagents).
  • the temperature of the water and the time for which the tobacco or tobacco material remains in contact with the water can vary.
  • the mixture is heated. For example, it may be heated to about 50 °C, about 75 °C, or about 100 °C.
  • the mixture is agitated.
  • the pH of the solution can vary, but in certain embodiments, the extraction solvent is acidic.
  • a processing aid is added to facilitate the extraction.
  • a processing aid is any agent that facilitates the extraction of the pectin into the extraction solvent.
  • suitable processing aids include, but are not limited to, mineral acids and enzymes.
  • the processing aid selected can affect the structure of the pectin; for example, use of enzymes typically results in shorter, branched segments.
  • Various other additives can be used in the extraction process, including, but not limited to, surfactants and co-solvents.
  • oxalic acid and/or ammonium oxalate i.e., oxalic acid or a salt thereof
  • the extraction conditions and the amount of time for which the tobacco remains in contact with the extraction solvent can impact the properties of the pectin (e.g., the degree of esterification).
  • the remaining solids are typically separated and the resulting solution is clarified.
  • the separation of solids from solution and clarification can be accomplished via various methods as described herein (e.g., filtration, including ultrafiltration, centrifugation, and/or distillation) to give an extract.
  • multiple clarification steps are conducted.
  • the extracted mixture is concentrated. Concentration can occur before and/or after the separation of solids, but is commonly done after the separation of solids.
  • the extract is typically further processed to further isolate the pectin from other compounds present in the extract.
  • the pectin can be precipitated from the clarified solution.
  • one means by which the pectin can be precipitated is to mix the concentrated solution with a reagent to precipitate the pectin, including, but not limited to, alcohol (e.g., ethanol and/or isopropanol), protein-containing solution, and/or detergent-containing solution.
  • the derivatives may precipitate readily from the clarified solution without the addition of any reagent, or may require the addition of one or more reagent to ensure the precipitation of pectin and various pectin derivatives that may be present in a given sample.
  • the precipitation may be conducted at reduced temperatures. For example, the mixture may be cooled to around 0 °C (e.g., around 5 °C) to promote precipitation of the pectin.
  • the resulting solid precipitate is then separated from the solution (e.g., by filtration or centrifugation). The precipitate is then commonly washed and dried.
  • the purity of the tobacco-derived pectin can vary, although it is preferably relatively high. Purity as intended herein refers to the content of both pectin and pectin derivatives as described above.
  • the tobacco-derived pectin sample is typically at least about 50% pure, at least about 60% pure, at least about 70% pure, at least about 80% pure, at least about 85% pure, at least about 90% pure, at least about 95% pure, at least about 98% pure, or at least about 99% pure.
  • the pectin comprises less than about 20% non-tobacco-derived material, less than about 15% non-tobacco-derived material, less than about 10% non-tobacco-derived material, less than about 5% non-tobacco-derived material, less than about 2% non-tobacco derived material, less than about 1% non-tobacco-derived material, or less than about 0.5% non-tobacco derived material.
  • various agents can be added at certain stages in the extraction and/or isolation processes to modify the pectin.
  • the present invention is intended to cover not only the isolation and use of pure pectin derived from tobacco, but also pectin derivatives produced therefrom, either naturally or synthetically.
  • the pectin-containing precipitate described above can be washed with a salt-containing or alkali-containing solvent to convert pectin in part or in whole to salt form.
  • the precipitate is treated with ammonia to produce some degree of amidated pectin.
  • pectin is extracted as taught by U.S. Patent Appl. Publ. No. 2012/141648 to Morton et al. , wherein pectin is extracted by means of a pectin extraction apparatus in which a dried plant pulp component is contacted with an extraction buffer (e.g., a solution of about 10% acetic acid and about 10 mM ethylenediaminetetraacetic acid (EDTA)), and the separated extract is precipitated by the addition of ethanol.
  • fine tobacco powder is cooked in an alkaline pH adjusted solution at elevated temperatures relative to ambient to release pectin, which can subsequently be separated and/or used according to the invention. Such treatment also can provide desirable sensory attributes to the tobacco material. See, for example, U.S. Pat. Nos. 5,099,864 to Young et al. ; 5,339,838 to Young et al. ; and 5,501,237 to Young et al. .
  • tobacco or a tobacco material e.g., tobacco shreds, scraps, dust, or fines
  • tobacco or a tobacco material is treated prior to extraction to effectuate the release of pectins.
  • pectins in tobacco often comprise protopectins, comprising calcium and magnesium salts of partially esterified and acetylated polymers of galacturonic acid.
  • a reagent such as an alkali metal carbonate, with a chelating agent (e.g., EDTA), or with an acid (e.g., HCl, phosphoric acid) to break the protopectin crosslinks and release the tobacco pectins.
  • a chelating agent e.g., EDTA
  • an acid e.g., HCl, phosphoric acid
  • pectin releasing agents are also intended to be encompassed within the methods of the invention.
  • DAP diammonium hydrogen phosphate
  • the form of the pectin derived from the tobacco or tobacco material and used in smokeless tobacco products can vary.
  • the tobacco-derived pectin is used in dried solid form directly as produced by the extraction process.
  • the dried solid is ground into a powder or granules of varying particle size.
  • the pectin component when provided in a powder or granulated form, is typically employed in the form of parts or pieces that have an average particle size less than about 50 microns. According to some aspects, the average particle size of the pectin component may be about 25 microns or less.
  • the pectin is used in solution.
  • the pectin component is admixed with one or more other components of the smokeless tobacco product before being combined with the remaining ingredients to make up the smokeless tobacco products of the invention.
  • the tobacco-derived pectin can provide various functions within the smokeless tobacco products of the present invention.
  • Pectin is commonly used as a gelling agent and thus can perform thickening, binding, and/or stabilizing functions within the smokeless tobacco products.
  • the tobacco-derived pectin can act as a binder.
  • a binder generally acts to help maintain the form and/or structure of a material.
  • a binder may help to facilitate the formation of a tobacco-containing product into the desired form. In some embodiments, it may provide a level of structural integrity to the formed product.
  • the tobacco-derived pectin may be added in addition to one or more other binders, or may be used as the sole binder. In some embodiments, it may be useful as a binder for certain reconstituted tobacco compositions.
  • pectin has been incorporated as a binder within an insulating material for a fuel element of a smoking article with conductive aerosol chamber, as described in U.S. Pat. No. 5,105,831 to Banerjee et al. .
  • pectin-containing reconstituted tobacco materials have been developed, and are described for example, in U.S. Pat. Nos. 3,386,449 to Hind ; 3,420,241 to Hind et al. ; 3,529,602 to Hind et al. ; 3,353,541 to Hind et al.
  • Pectin can also be used as a source of dietary fiber.
  • the tobacco-derived pectin provided herein is sufficient to fulfill the intended function of a binder in smokeless tobacco products.
  • the tobacco-derived pectin may be, and is preferably sufficient to provide a cohesive tobacco composition.
  • the tobacco-derived pectin may function to hold the smokeless tobacco product together in use.
  • the tobacco-derived pectin provides a degree of structural integrity in a solid tobacco composition.
  • the tobacco-derived pectin may provide some level of film-forming capability or control.
  • one or more additional binders e.g., povidone, sodium carboxymethylcellulose and other modified cellulosic types of binders, sodium alginate, xanthan gum, starch-based binders, gum arabic, gellan gum, lecithin, and the like
  • additional binders e.g., povidone, sodium carboxymethylcellulose and other modified cellulosic types of binders, sodium alginate, xanthan gum, starch-based binders, gum arabic, gellan gum, lecithin, and the like
  • the use 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.
  • the tobacco-derived pectin binder may be employed in amounts sufficient to provide the desired physical attributes and physical integrity to the smokeless tobacco composition.
  • the smokeless tobacco composition can comprise greater than 2%, greater than about 3%, greater than about 4%, greater than about 5%, greater than about 6%, greater than about 7%, greater than about 8%, greater than about 9%, or 10% of tobacco-derived pectin, based on the total dry weight of the smokeless tobacco composition or product.
  • a representative amount of binder is between 2% and 10% tobacco-derived pectin by total dry weight of the smokeless tobacco product.
  • the total amount of binder within the composition will not exceed about 45% of the total dry weight of the composition.
  • the smokeless tobacco product can comprise, for example, 2% by weight, about 3% by weight, about 4% by weight, about 5% by weight, about 6% by weight, about 7% by weight, about 8% by weight, about 9% by weight, or 10% by weight of tobacco-derived pectin.
  • the one or more additional binders where employed in the smokeless tobacco products of the invention, include a natural gum.
  • a natural gum refers to polysaccharide materials of natural origin that are useful as thickening or gelling agents.
  • Representative natural gums derived from plants, which are typically water soluble to some degree, include xanthan gum, guar gum, gum arabic, ghatti gum, gum tragacanth, karaya gum, locust bean gum, gellan gum, and combinations thereof.
  • tobacco-derived pectin can afford a smokeless tobacco product having a higher degree of tobacco-derived components.
  • Replacing and/or supplementing traditional binders with tobacco-derived pectin in smokeless tobacco products can, in some embodiments, provide the smokeless tobacco product with various characteristics, some of which are improved over those of smokeless tobacco products employing traditional binders.
  • smokeless tobacco products employing tobacco-derived pectin exhibit increased rigidity over smokeless tobacco products employing traditional binders.
  • Increased rigidity can, in some embodiments, be quantified. However, in some embodiments, the increased rigidity is simply evaluated by feel of the product (e.g., by trying to bend/flex the product).
  • smokeless tobacco products employing tobacco-derived pectin exhibit reduced tackiness as compared to smokeless tobacco products employing traditional binders.
  • the reduction in tackiness can, in some embodiments, be quantified. In some embodiments, the reduction in tackiness is simply evaluated by feel of the product.
  • smokeless tobacco products comprising tobacco-derived pectin as a binder rather than commercially available pullulan binder exhibit increased rigidity and/or reduced tackiness. Pullulan and smokable products incorporating pullulan are discussed in more detail for example, in US Pat. Pub. No. 2007/0137668 to Borschke et al.
  • the tobacco material and tobacco-derived pectin binder can be combined in any manner known in the art, such as by simply mixing the two components together using conventional mixing apparatuses.
  • the tobacco material and tobacco-derived pectin ingredients can also be processed, blended, formulated, combined and mixed with other materials or ingredients. See, for example, those representative components, combination of components, relative amounts of those components and ingredients relative to tobacco, and manners and methods for employing those components, set forth in US Pat. Pub. Nos. 2007/0062549 and 2007/0186941 to Holton, et al.
  • the additional ingredients can be artificial, or can be obtained or derived from herbal or biological sources.
  • exemplary types of ingredients 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, vanillin, ethylvanillin glucoside, mannose, galactose, lactose, and the like), artificial sweeteners (e.g., sucralose, saccharin, aspartame, acesulfame K, neotame and the like), organic and inorganic fillers (e.g., grains, processed grains, puffed grains, maltodextrin, dextrose, calcium carbonate, calcium phosphate, corn starch, lactose, sugar alcohols such as isomalt, mannitol, xylitol, or sorbitol, finely
  • the sweetener component of the smokeless tobacco products of the present invention can be any sweetener, in natural or artificial form or as a combination of artificial and natural sweeteners.
  • sugar i.e., sucrose
  • sucralose, maltodextrin, or corn syrup is the primary sweetener ingredient.
  • both sucrose and corn syrup are used in the smokeless tobacco products.
  • Other exemplary sweeteners are sugar alcohols.
  • Sugar alcohols are polyols derived from monosaccharides or disaccharides that have a partially or fully hydrogenated form.
  • Exemplary sugar alcohols have between about 4 and about 20 carbon atoms and include erythritol, arabitol, ribitol, isomalt, maltitol, dulcitol, iditol, mannitol, xylitol, lactitol, sorbitol, and combinations thereof (e.g., hydrogenated starch hydrolysates).
  • a representative amount of sweetener may make up at least 5 percent, often at least about 10% of the total dry weight of the composition. The amount of sweetener within the composition will not exceed 15 percent, of the total dry weight of the composition.
  • a syrup is employed in amounts sufficient to provide chewiness and retard solubilization, or otherwise provide desired flavor attributes to the smokeless tobacco composition.
  • a representative amount of syrup e.g., corn syrup
  • the smokeless tobacco compositions of the disclosure also include at least one filler ingredient.
  • sugar alcohols are particularly advantageous as filler components in certain products of the disclosure because such materials contribute some sweetness and do not disrupt the chewable characteristics which may be desired in the final product.
  • a fondant filler is used.
  • Fondant fillers typically comprise sugar, corn syrup, and water.
  • One exemplary fondant filler composition consists of sugar, corn syrup, water, albumen, algin, citric acid, vanillin, sodium propionate, and potassium sorbate.
  • a filler component often fulfills multiple functions, such as enhancing certain organoleptic properties such as texture and mouthfeel, enhancing cohesiveness or compressibility of the product, and the like.
  • a representative amount of filler, whether an organic and/or inorganic filler, may make up at least 10 percent, based on the total dry weight of the composition. The amount of filler within the composition will not exceed 40%, and frequently will not exceed about 30 percent of the total dry weight of the composition.
  • the filler component includes one or more rice-derived fillers, such as rice starch or rice flour or combinations thereof.
  • one or more fats are added.
  • the fat may function, for example, as a processing aid and/or to optimize the appearance of the smokeless tobacco product.
  • pre-melted fat such as partially hydrogenated soybean oil can be included in the composition.
  • a "flavorant” or “flavoring agent” is any flavorful or aromatic substance capable of altering the sensory characteristics associated with the smokeless tobacco composition.
  • Exemplary sensory characteristics that can be modified by the flavorant include, taste, mouthfeel, moistness, coolness/heat, and/or fragrance/aroma.
  • the flavorants can be natural or synthetic, and the character of these flavors can be described as, without limitation, fresh, sweet, herbal, confectionary, floral, fruity or spice.
  • flavors include, but are not limited to, vanilla, coffee, chocolate, cream, mint (e.g., mint oil), spearmint, menthol, peppermint, wintergreen, lavender, cardamon, nutmeg, cinnamon, clove, cascarilla, sandalwood, honey, jasmine, ginger, anise, sage, licorice, lemon, orange, apple, peach, lime, cherry, and strawberry.
  • Flavorants utilized in the disclosure also can 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). In some instances, the flavorant may be provided in a spray-dried form or a liquid form. Flavorants are typically present in an amount of about 0.5 to 5 dry weight percent, often about 1 to 5 dry weight percent, and most often about 2 to 5 dry weight percent.
  • a salt e.g., sodium chloride, flour salt
  • a representative amount of salt is at least about 0.5 dry weight percent or at least about 1.0 dry weight percent or at least about 1.5 dry weight percent, but will typically may make up less than about 5 percent of the total dry weight of the composition (e.g., about 0.5 to about 4 dry weight percent).
  • a humectant e.g., glycerin
  • the humectant may be employed in amounts sufficient to provide desired moisture attributes to the smokeless tobacco composition. Further, in some instances, the humectant may impart desirable flow characteristics to the smokeless tobacco composition for depositing in a starch mould.
  • a representative amount of humectant is at least about 0.5 dry weight percent or at least about 1.0 dry weight percent or at least about 1.5 dry weight percent, but will typically make up less than about 5 percent of the total dry weight of the composition (e.g., about 0.5 to about 4 dry weight percent).
  • 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 buffering agent is typically present in an amount less than about 1 percent based on the dry weight of the formulation.
  • Such additional ingredients may be provided in a powder or granulated form for mixing with the tobacco material formulation, or otherwise may be provided in liquid form.
  • the ingredients when provided in a powder or granulated form is employed in the form of parts or pieces that have an average particle size less than 50 microns. According to some aspects, the average particle size of the additive may be about 25 microns or less.
  • the moisture content of the additives provided in a powder or granulated form may vary. Most preferably, the moisture content of the additive provided in a powder or granulated form is less than about 10 weight percent, and may be less than about 5 percent, and is often less than about 2.5 weight percent.
  • the additive may be admixed with any component or with the tobacco material in, for example, a Hobart mixer with a paddle prior to adding any liquid additives.
  • the resultant mixture may still have a relatively low moisture content of less than about 10 weight percent, and may be less than about 5 percent, and is often less than about 2.5 weight percent.
  • the relative amounts of the various additive components within the smokeless tobacco product may vary.
  • the aforementioned types of ingredients can be employed together (e.g., as ingredient formulations) or separately (e.g., individual additive components can be added at different stages involved in the preparation of the final tobacco product).
  • the relative amounts of the various components within the smokeless tobacco formulation may vary, and typically are selected so as to provide the desired sensory and performance characteristics to the tobacco product.
  • the aforementioned types of additives may be encapsulated as provided in the final product or composition. Exemplary encapsulated additives are described, for example, in WO 2010/132444 A2 to Atchley .
  • any of the above-noted classes of ingredients for the smokeless tobacco composition of the disclosure can be derived from tobacco material by subjecting at least a portion of a tobacco plant (e.g., leaves, seeds, flowers, stalks, roots, or stems) to a separation process, which typically can include multiple sequential extraction steps, in order to isolate desired components of the tobacco material.
  • a separation process typically can include multiple sequential extraction steps, in order to isolate desired components of the tobacco material.
  • Exemplary separation processes include chromatography, distillation, filtration, recrystallization, solvent-solvent partitioning, cold pressing, solvent extraction (e.g., using solvents such as water, alcohols or hydrocarbons such as heptane or hexane), or a combination thereof.
  • solvents such as water, alcohols or hydrocarbons such as heptane or hexane
  • the resulting isolated tobacco component can be chemically transformed prior to use in the compositions of the disclosure.
  • Exemplary chemical transformations include hydrogenation, esterification, transesterification, isomeric conversion, acetal formation, acetal decomposition, acid/base reaction, hydrolysis, thermal treatment, enzymatic treatment, and combinations of such steps.
  • Techniques for preparing tobacco isolates for use in the compositions of the disclosure are set forth, for example, in U.S. Pat. Pub. Nos. 2011/0174323 to Coleman, III et al. , and U.S. Publ. No. 2011/259353 to Coleman, III et al.
  • Examples of the types of compounds that may be present in the tobacco isolate include hydrocarbons, cellulose, alcohols, aldehydes, ketones, carboxylic acids, amino acids, esters, lactones, anhydrides, carbohydrates (e.g., reducing sugars), phenols, quinones, ethers, nitriles, amines, amides, imides, plastid pigments, proteins, coenzyme-Q, pectin, starch, lignin, and lipids. Additional examples are described as natural tar diluents in PCT WO 2007/012980 to Lipowicz , which is incorporated by reference herein in its entirety.
  • a smokeless tobacco ingredient prepared from a tobacco isolate will vary depending on the composition of the isolate, which can vary in part based on the extraction process employed, the portion of the tobacco plant involved, the type of chemical transformation utilized, and the like.
  • Certain tobacco isolates can provide sugars, fillers, binders, disintegration or compressibility aids, or flavorants for the smokeless tobacco composition of the disclosure.
  • Representative smokeless tobacco compositions may incorporate tobacco in an amount of about 30-40 weight percent and tobacco-derived pectin as described herein in an amount of about 4 weight percent, based on the total dry weight of the smokeless tobacco composition.
  • the smokeless tobacco composition comprises about 36 weight percent milled tobacco, about 4 weight percent tobacco-derived pectin, about 14 weight percent rice starch, about 6 weight percent rice flour, about 7 weight percent maltitol powder, and about 3 weight percent flavoring compounds, based on the total dry weight of the smokeless tobacco composition, wherein the remainder comprises one or more colorants, sweeteners, fillers, binders, pH adjusters, and salts.
  • the remainder can, in one embodiment, comprise titanium dioxide, xylitol, sorbitol, calcium carbonate, maltodextrin, xanthan gum, sodium hydroxide, and sodium chloride.
  • 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 smokeless tobacco composition are combined may vary.
  • the various components of the smokeless tobacco composition may be contacted, combined, or mixed together in conical-type blenders, mixing drums, ribbon blenders, or the like, such as a Hobart mixer.
  • 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 .
  • the smokeless tobacco product can be provided in any suitable predetermined shape or form.
  • the smokeless tobacco product is provided in the form having a general shape of a pill, pellet, tablet, coin, bead, ovoid, obloid, cube, film, flake, stick, foam, gel, or the like.
  • the shape is determined by the shape of the mold in which the product is formed. Individual compositions can be sized such that they fit entirely in the user's mouth, or such that they fit only partially in the mouth. Thus, the preferred dimensions can vary.
  • Shapes such as, for example, rods and cubes can be formed by first extruding the material through a die having the desired cross-section (e.g., round or square) and then optionally cutting the extruded material into desired lengths.
  • Techniques and equipment for extruding tobacco materials are set forth in US Pat. Nos. 3,098,492 to Wursburg ; 4,874,000 to Tamol et al. ; 4,880,018 to Graves et al. ; 4,989,620 to Keritsis et al. ; 5,072,744 to Luke et al. ; 5,829,453 to White et al. ; and 6,182,670 to White et al.
  • Exemplary extrusion equipment suitable for use include food or gum extruders, or industrial pasta extruders such as Model TP 200/300 available from Emiliomiti, LLC of Italy.
  • a single machine may be capable of achieving multiple steps of the processes described herein, such as, for example, kneader systems available from Buss AG.
  • the smokeless tobacco product can be dried or moistened to reach the final desired moisture level.
  • the moisture content of the smokeless tobacco product prior to use by a consumer can vary.
  • the moisture content of the smokeless tobacco product, as present within a single unit of product prior to insertion into the mouth of the user is within the range of about 5 to about 20 weight percent, often about 8 to about 15 weight percent, more often about 10 to about 13 weight percent, based on the total weight of the product unit, but may vary depending upon the specific form of the smokeless tobacco product.
  • the acidity or alkalinity of the smokeless tobacco product which is often characterized in terms of pH, 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 9.5, and often will not exceed about 9.0.
  • a representative tobacco formulation exhibits a pH of about 6.8 to about 8.8 (e.g., about 7.4 to about 8.2).
  • a representative technique for determining the pH of a smokeless 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).
  • compositions of the present invention may be dissolvable.
  • dissolvable refers to compositions having aqueous-soluble components that interact with moisture in the oral cavity and enter into solution, thereby causing gradual consumption of the product.
  • the dissolvable smokeless tobacco product is capable of lasting in the user's mouth for a given period of time until it completely dissolves. Dissolution rates of the present smokeless tobacco products can vary over a wide range, from less than about 1 minute to about 60 minutes.
  • fast release compositions typically dissolve and/or release the active component in less than about 2 minutes, often less than about 1 minute (e.g., less than about 50 seconds, less than about 40 seconds, less than about 30 seconds, or less than about 20 seconds). Dissolution can occur by any means, such as melting, mechanical disruption (e.g., chewing), enzymatic or other chemical degradation, or by disruption of the interaction between the components of the product.
  • the products can be meltable as discussed, for example, in US Publ. No. 2012/037175 to Cantrell et al.
  • the compositions do not dissolve during the smokeless tobacco product's residence in the user's mouth.
  • the smokeless tobacco composition may be coated with a coating substance.
  • a glazing or anti-sticking coating substance such as, for example, CAPOL 410 (available from Centerchem, Inc.), maybe applied to the smokeless tobacco composition to provide free-flowing properties.
  • Outer coatings can also help to improve storage stability of the smokeless tobacco products of the present disclosure as well as improve the packaging process by reducing friability and dusting.
  • Devices for providing outer coating layers to the products of the present disclosure include pan coaters and spray coaters, and particularly include the coating devices available as CompuLab 24, CompuLab 36, Accela-Cota 48 and Accela-Cota 60 from Thomas Engineering.
  • An exemplary outer coating comprises a film-forming polymer, such as a cellulosic polymer, an optional plasticizer, and optional flavorants, colorants, salts, sweeteners or other additives of the types set forth herein.
  • the coating compositions are usually aqueous in nature and can be applied using any pellet or tablet coating technique known in the art, such as pan coating.
  • Exemplary film-forming polymers include cellulosic polymers such as methylcellulose, hydroxypropyl cellulose (HPC), hydroxypropyl methylcellulose (HPMC), hydroxyethyl cellulose, and carboxy methylcellulose.
  • Exemplary plasticizers include aqueous solutions or emulsions of glyceryl monostearate and triethyl citrate. Exemplary coating compositions and methods of application are described in U.S. Publ. No. 2012/055494 to Hunt et al.
  • products can also be formed with multiple different formulations having different properties in the same product unit.
  • two different compositions could be coextruded to form a product with different characteristics across its cross-section.
  • Such a process could be used to provide a product with two different compositions featuring different dissolution rates such that a first portion of the product dissolves at a first rate (e.g., a faster rate) and a second portion dissolves at a second, slower rate.
  • the tobacco component of the smokeless tobacco composition can be replaced or supplemented with other suitable botanical components such as, for example, tea particulates, coffee particulates, herbal particulates, spice particulates and/or combinations thereof.
  • suitable botanical components such as, for example, tea particulates, coffee particulates, herbal particulates, spice particulates and/or combinations thereof.
  • the particulates may be typically provided in a powder form, which may be extracted from an appropriate botanical source.
  • Products of the present disclosure can be packaged and stored in any suitable packaging. See, for example, the various types of containers for smokeless types of products that are set forth in US Pat. Nos. 7,014,039 to Henson et al. ; 7,537,110 to Kutsch et al. ; 7,584,843 to Kutsch et al. ; D592,956 to Thiellier and D594,154 to Patel et al. ; US Pat. Pub. Nos. 2008/0173317 to Robinson et al. ; 2009/0014343 to Clark et al. ; 2009/0014450 to Bjorkholm ; 2009/0250360 to Bellamah et al.
  • Approximately 363 kg (800 pounds) of air-cured burley tobacco (lamina and stem) are processed to extract and dry the pectin component as follows. To about 6532 kg (14,400 pounds) of well water is added about 36.3 kg (80 pounds) of oxalic acid and about 36.3 kg (80 pounds) of ammonium oxalate. The resulting mixture is agitated until the oxalic acid and ammonium oxalate are dissolved to form a solution. The tobacco is added to the solution and the resulting mixture is heated at about 95 - 98 °C for about 90 minutes. The tobacco is removed from the mixture by filtration (additionally or alternatively, centrifugation can be used). The resulting liquid is collected once it has reached a desired level of clarity. It may be necessary to repeat the filtration/centrifugation steps two or more times to achieve the desired level of clarity. The liquid is then concentrated under vacuum until the product comprises approximately 9-11% solids.
  • Ethanol is added to the concentrated material in an amount of 1.2 times the amount of the concentrate by weight to give a dilute concentrate.
  • the dilute concentrate is cooled to between about 5 and 7 °C.
  • the dilute concentrate is centrifuged to isolate the solid material that has formed.
  • the solid material is rinsed in 50% ethanol in water (v/v) and then in 100% ethanol and the rinsed solid is isolated by centrifugation.
  • the combined solid material is dried in a tray dryer under full vacuum, with hot water circulation at 55 °C in a jacket of the dryer. After a minimum of 6 hours, the sample is removed and tested to ensure that it comprises less than 5% moisture by weight. If the sample does not meet this requirement, it is further dried to give the isolated pectin product. Based on the original 800 g of tobacco material, 30 g of pectin product was isolated, in the form of a dark brown powder.
  • the dark brown powder is used in a dissolvable smokeless tobacco formulation typically comprising a tobacco blend and pullulan binder. Instead of the pullulan binder, the dark brown powder isolated as described above is used.
  • the smokeless tobacco formulation comprises about 36 weight percent milled tobacco, about 4 weight percent of the dark brown powder (pectin component), about 14 weight percent rice starch, about 6 weight percent rice flour, about 7 weight percent maltitol powder, and about 3 weight percent flavoring compounds, based on the total dry weight of the smokeless tobacco composition.
  • the formulation also includes minor amounts of titanium dioxide, xylitol, sorbitol, calcium carbonate, maltodextrin, xanthan gum, sodium hydroxide, and sodium chloride.
  • the resulting smokeless tobacco product was evaluated by informal sensory evaluations. The evaluations noted no discernable differences related to mouth-feel, color, or other visual attributes for the experimental finished product as opposed to the control product.
  • the trial product containing tobacco-derived pectin exhibits reduced stick tackiness and increased rigidity as compared to the control material during processing. Both of these characteristics are considered positive attributes for this type of formulation.
EP12795236.4A 2011-11-18 2012-11-16 Smokeless tobacco product comprising tobacco-derived pectin component Active EP2779849B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US13/299,621 US20130125904A1 (en) 2011-11-18 2011-11-18 Smokeless tobacco product comprising pectin component
PCT/US2012/065480 WO2013074903A1 (en) 2011-11-18 2012-11-16 Smokeless tobacco product comprising tobacco - derived pectin component

Publications (2)

Publication Number Publication Date
EP2779849A1 EP2779849A1 (en) 2014-09-24
EP2779849B1 true EP2779849B1 (en) 2018-06-20

Family

ID=47279091

Family Applications (1)

Application Number Title Priority Date Filing Date
EP12795236.4A Active EP2779849B1 (en) 2011-11-18 2012-11-16 Smokeless tobacco product comprising tobacco-derived pectin component

Country Status (5)

Country Link
US (1) US20130125904A1 (ja)
EP (1) EP2779849B1 (ja)
JP (1) JP6324897B2 (ja)
CN (1) CN103997919A (ja)
WO (1) WO2013074903A1 (ja)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2824755C (en) 2011-09-23 2018-01-16 Kt Corporation Method for deriving a merge candidate block and device using same
US10130120B2 (en) * 2013-03-15 2018-11-20 Altria Client Services Llc Use of pectin or other anionic polymers in the stabilization and controlled release of nicotine in oral sensorial tobacco products or nicotine containing non-tobacco oral sensorial products
CA2896378A1 (en) * 2013-04-18 2014-10-23 The Hershey Company Comestible containing finely ground demulcent
US20140356295A1 (en) 2013-06-03 2014-12-04 R.J. Reynolds Tobacco Company Cosmetic compositions comprising tobacco seed-derived component
US10357054B2 (en) * 2013-10-16 2019-07-23 R.J. Reynolds Tobacco Company Smokeless tobacco pastille
CN103519341B (zh) * 2013-10-23 2015-06-03 红塔烟草(集团)有限责任公司 一种低果胶含量的造纸法再造烟叶片基及其制备方法
CN103948164B (zh) * 2014-05-19 2016-08-24 川渝中烟工业有限责任公司 口含烟提取液及其制备方法和口含烟
CN105747267A (zh) * 2014-12-17 2016-07-13 贵州中烟工业有限责任公司 一种含化型无烟气烟草制品及其制备方法
CN105167166B (zh) * 2015-07-21 2017-05-17 中国烟草总公司广东省公司 一种含有烟草全组分提取物的口含烟及其制备方法
US11612183B2 (en) * 2015-12-10 2023-03-28 R.J. Reynolds Tobacco Company Protein-enriched tobacco composition
US10744140B2 (en) * 2016-08-01 2020-08-18 Power Supplements, Llc Synergistic nutraceutical beverage formulations providing enhanced thermogenesis, mental clarity, and stamina while minimizing adrenaline and dopamine concentration perturbations associated with withdrawal
WO2018100688A1 (ja) * 2016-11-30 2018-06-07 日本たばこ産業株式会社 喫煙物品用香料含有シートおよびそれを含む喫煙物品
US20180368472A1 (en) * 2017-06-21 2018-12-27 Altria Client Services Llc Encapsulated ingredients for e-vaping devices and method of manufacturing thereof
CN107319622A (zh) * 2017-06-29 2017-11-07 滁州卷烟材料厂 一种烟叶的加工处理方法
PL3984379T3 (pl) * 2020-10-15 2023-12-18 Jt International Sa Sposób wytwarzania arkusza RTB zawierającego wyrób tytoniowy
WO2022259702A1 (ja) * 2021-06-11 2022-12-15 日本たばこ産業株式会社 たばこ製剤
KR102616657B1 (ko) * 2021-09-06 2023-12-20 주식회사 케이티앤지 물리성이 향상된 향료 시트, 이를 포함하는 흡연 물품 및 이들의 제조 방법
KR20230048194A (ko) * 2021-10-01 2023-04-11 주식회사 케이티앤지 표면 거칠기가 향상된 향료 시트, 이를 포함하는 흡연 물품 및 이들의 제조 방법

Family Cites Families (137)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1376586A (en) 1918-04-06 1921-05-03 Schwartz Francis Tobacco-tablet
US3098492A (en) 1960-11-25 1963-07-23 Nat Starch Chem Corp Method of making tobacco product
US3353541A (en) 1966-06-16 1967-11-21 Philip Morris Inc Tobacco sheet material
US3386449A (en) 1966-06-16 1968-06-04 Philip Morris Inc Method of making a reconstituted tobacco sheet
US3411515A (en) * 1967-04-28 1968-11-19 Philip Morris Inc Method of preparing a reconstituted tobacco sheet employing a pectin adhesive
US3420241A (en) 1967-04-28 1969-01-07 Philip Morris Inc Method of preparing a reconstituted tobacco sheet employing a pectin adhesive
US3529602A (en) * 1969-02-27 1970-09-22 Philip Morris Inc Tobacco substitute sheet material
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
US3746012A (en) 1972-01-17 1973-07-17 Philip Morris Inc Method of making expanded reconstituted tobacco
GB1489761A (en) 1974-03-08 1977-10-26 Amf Inc Process of treating tobacco
GB1550835A (en) 1975-08-18 1979-08-22 British American Tobacco Co Treatment of tobacco
US4150677A (en) 1977-01-24 1979-04-24 Philip Morris Incorporated Treatment of tobacco
US4267847A (en) 1978-05-12 1981-05-19 British-American Tobacco Company Limited Tobacco additives
US4289147A (en) 1979-11-15 1981-09-15 Leaf Proteins, Inc. Process for obtaining deproteinized tobacco freed of nicotine and green pigment, for use as a smoking product
US4589428A (en) 1980-02-21 1986-05-20 Philip Morris Incorporated Tobacco treatment
DE3009031C2 (de) 1980-03-08 1983-04-21 B.A.T. Cigaretten-Fabriken Gmbh, 2000 Hamburg Verfahren zur Herstellung von Aromastoffen für Rauchprodukte
DE3009032C2 (de) 1980-03-08 1983-11-24 B.A.T. Cigaretten-Fabriken Gmbh, 2000 Hamburg Verfahren zur Herstellung von Aromastoffen für Rauchprodukte
IN158943B (ja) 1981-12-07 1987-02-21 Mueller Adam
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
US4874000A (en) 1982-12-30 1989-10-17 Philip Morris Incorporated Method and apparatus for drying and cooling extruded tobacco-containing material
US4989620A (en) 1982-12-30 1991-02-05 Philip Morris Incorporated Method and apparatus for coating extruded tobacco-containing material
US4513756A (en) 1983-04-28 1985-04-30 The Pinkerton Tobacco Company Process of making tobacco pellets
JPS6024172A (ja) 1983-07-21 1985-02-06 日本たばこ産業株式会社 たばこ用香料の製造方法
US5092352A (en) 1983-12-14 1992-03-03 American Brands, Inc. Chewing tobacco product
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
US5105831A (en) 1985-10-23 1992-04-21 R. J. Reynolds Tobacco Company Smoking article with conductive aerosol chamber
US4880018A (en) 1986-02-05 1989-11-14 R. J. Reynolds Tobacco Company Extruded tobacco materials
US4716911A (en) 1986-04-08 1988-01-05 Genencor, Inc. Method for protein removal from tobacco
US4727889A (en) 1986-12-22 1988-03-01 R. J. Reynolds Tobacco Company Tobacco processing
US5018540A (en) 1986-12-29 1991-05-28 Philip Morris Incorporated Process for removal of basic materials
US5005593A (en) 1988-01-27 1991-04-09 R. J. Reynolds Tobacco Company Process for providing tobacco extracts
US5435325A (en) 1988-04-21 1995-07-25 R. J. Reynolds Tobacco Company Process for providing tobacco extracts using a solvent in a supercritical state
US4887618A (en) 1988-05-19 1989-12-19 R. J. Reynolds Tobacco Company Tobacco processing
US4987907A (en) 1988-06-29 1991-01-29 Helme Tobacco Company Chewing tobacco composition and process for producing same
US4967771A (en) 1988-12-07 1990-11-06 R. J. Reynolds Tobacco Company Process for extracting tobacco
US4986286A (en) 1989-05-02 1991-01-22 R. J. Reynolds Tobacco Company Tobacco treatment process
US4941484A (en) 1989-05-30 1990-07-17 R. J. Reynolds Tobacco Company Tobacco processing
GB8914508D0 (en) 1989-06-23 1989-08-09 British American Tobacco Co Improvements relating to the making of smoking articles
US5121757A (en) 1989-12-18 1992-06-16 R. J. Reynolds Tobacco Company Tobacco treatment process
US5060669A (en) 1989-12-18 1991-10-29 R. J. Reynolds Tobacco Company Tobacco treatment process
US4991599A (en) 1989-12-20 1991-02-12 Tibbetts Hubert M Fiberless tobacco product for smoking and chewing
US5099864A (en) 1990-01-05 1992-03-31 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US5131414A (en) 1990-02-23 1992-07-21 R. J. Reynolds Tobacco Company Tobacco processing
US5065775A (en) 1990-02-23 1991-11-19 R. J. Reynolds Tobacco Company Tobacco processing
US5234008A (en) 1990-02-23 1993-08-10 R. J. Reynolds Tobacco Company Tobacco processing
US5099862A (en) 1990-04-05 1992-03-31 R. J. Reynolds Tobacco Company Tobacco extraction process
US5074319A (en) 1990-04-19 1991-12-24 R. J. Reynolds Tobacco Company Tobacco extraction process
US5668295A (en) 1990-11-14 1997-09-16 Philip Morris Incorporated Protein involved in nicotine synthesis, DNA encoding, and use of sense and antisense DNAs corresponding thereto to affect nicotine content in transgenic tobacco cells and plants
US5131415A (en) 1991-04-04 1992-07-21 R. J. Reynolds Tobacco Company Tobacco extraction process
US5197494A (en) 1991-06-04 1993-03-30 R.J. Reynolds Tobacco Company Tobacco extraction process
US5318050A (en) 1991-06-04 1994-06-07 R. J. Reynolds Tobacco Company Tobacco treatment process
US5343879A (en) 1991-06-21 1994-09-06 R. J. Reynolds Tobacco Company Tobacco treatment process
US5360022A (en) 1991-07-22 1994-11-01 R. J. Reynolds Tobacco Company Tobacco processing
US5148819A (en) 1991-08-15 1992-09-22 R. J. Reynolds Tobacco Company Process for extracting tobacco
US5243999A (en) 1991-09-03 1993-09-14 R. J. Reynolds Tobacco Company Tobacco processing
US5230354A (en) 1991-09-03 1993-07-27 R. J. Reynolds Tobacco Company Tobacco processing
US5501237A (en) 1991-09-30 1996-03-26 R. J. Reynolds Tobacco Company Tobacco reconstitution process
US5301694A (en) 1991-11-12 1994-04-12 Philip Morris Incorporated Process for isolating plant extract fractions
US5445169A (en) 1992-08-17 1995-08-29 R. J. Reynolds Tobacco Company Process for providing a tobacco extract
US5339838A (en) 1992-08-17 1994-08-23 R. J. Reynolds Tobacco Company Method for providing a reconstituted tobacco material
US5387416A (en) 1993-07-23 1995-02-07 R. J. Reynolds Tobacco Company Tobacco composition
US5539093A (en) 1994-06-16 1996-07-23 Fitzmaurice; Wayne P. DNA sequences encoding enzymes useful in carotenoid biosynthesis
US5637785A (en) 1994-12-21 1997-06-10 The Salk Institute For Biological Studies Genetically modified plants having modulated flower development
US5829453A (en) 1995-06-09 1998-11-03 R. J. Reynolds Tobacco Company Low-density tobacco filler and a method of making low-density tobacco filler and smoking articles therefrom
US5705624A (en) 1995-12-27 1998-01-06 Fitzmaurice; Wayne Paul DNA sequences encoding enzymes useful in phytoene biosynthesis
US6906172B2 (en) 1998-03-10 2005-06-14 Large Scale Biology Corporation Flexible processing apparatus for isolating and purifying viruses, soluble proteins and peptides from plant sources
US6298859B1 (en) 1998-07-08 2001-10-09 Novozymes A/S Use of a phenol oxidizing enzyme in the treatment of tobacco
ATE342994T1 (de) 1998-08-11 2006-11-15 Biosource Tech Inc Verfahren zur gewinnung von proteinen aus der interstitiellen flüssigkeit von pflanzen
US6131584A (en) 1999-04-15 2000-10-17 Brown & Williamson Tobacco Corporation Tobacco treatment process
US6805134B2 (en) 1999-04-26 2004-10-19 R. J. Reynolds Tobacco Company Tobacco processing
US6371126B1 (en) 2000-03-03 2002-04-16 Brown & Williamson Tobacco Corporation Tobacco recovery system
CA2420724A1 (en) 2000-08-30 2002-03-07 North Carolina State University Transgenic plants containing molecular decoys that alter protein content therein
ATE546535T1 (de) 2001-03-08 2012-03-15 Univ Michigan State Lipidstoffwechsel-regulatoren in pflanzen
MXPA03010006A (es) 2001-05-01 2005-03-07 Regent Court Technologies Llc Producto de tabaco sin humo.
US6668839B2 (en) 2001-05-01 2003-12-30 Jonnie R. Williams Smokeless tobacco product
US20040020503A1 (en) 2001-05-01 2004-02-05 Williams Jonnie R. Smokeless tobacco product
US7208659B2 (en) 2001-05-02 2007-04-24 Conopco Inc. Process for increasing the flavonoid content of a plant and plants obtainable thereby
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
US6817970B2 (en) 2002-06-17 2004-11-16 Large Scale Biology Corporation Centrifuge for extracting interstitial fluid
US6772767B2 (en) 2002-09-09 2004-08-10 Brown & Williamson Tobacco Corporation Process for reducing nitrogen containing compounds and lignin in tobacco
US7025066B2 (en) 2002-10-31 2006-04-11 Jerry Wayne Lawson Method of reducing the sucrose ester concentration of a tobacco mixture
SE0301244D0 (sv) 2003-04-29 2003-04-29 Swedish Match North Europe Ab Smokeless tobacco product user package
US7014039B2 (en) 2003-06-19 2006-03-21 R.J. Reynolds Tobacco Company Sliding shell package for smoking articles
SE527350C8 (sv) 2003-08-18 2006-03-21 Gallaher Snus Ab Lock till snusdosa
TWI343791B (en) 2003-11-03 2011-06-21 Us Smokeless Tobacco Co Flavored smokeless tobacco and methods of making
JP4931596B2 (ja) 2003-11-07 2012-05-16 ユーエス スモークレス タバコ カンパニー リミテッド ライアビリティ カンパニー タバコ組成物
US8627828B2 (en) 2003-11-07 2014-01-14 U.S. Smokeless Tobacco Company Llc Tobacco compositions
WO2005063060A1 (en) 2003-12-22 2005-07-14 U.S. Smokeless Tobacco Company Conditioning process for tobacco and/or snuff compositions
US20080196730A1 (en) 2004-07-02 2008-08-21 Radi Medical Systems Ab Smokeless Tobacco Product
US7337782B2 (en) 2004-08-18 2008-03-04 R.J. Reynolds Tobacco Company Process to remove protein and other biomolecules from tobacco extract or slurry
US7798153B2 (en) 2004-08-23 2010-09-21 Us Smokeless Tobacco Co. Nicotiana Kawakamii smokeless tobacco
US7650891B1 (en) 2004-09-03 2010-01-26 Rosswil Llc Ltd. Tobacco precursor product
WO2007012980A1 (en) 2005-06-01 2007-02-01 Philip Morris Products S.A. Tobacco with an increased level of natural tar dilutents
US7537110B2 (en) 2005-06-02 2009-05-26 Philip Morris Usa Inc. Container for consumer article
US7584843B2 (en) 2005-07-18 2009-09-08 Philip Morris Usa Inc. Pocket-size hand-held container for consumer items
US20070062549A1 (en) 2005-09-22 2007-03-22 Holton Darrell E Jr Smokeless tobacco composition
US7861728B2 (en) 2006-02-10 2011-01-04 R.J. Reynolds Tobacco Company Smokeless tobacco composition having an outer and inner pouch
US20070137668A1 (en) 2005-12-15 2007-06-21 Borschke August J Smoking articles and wrapping materials therefor
US7819124B2 (en) 2006-01-31 2010-10-26 U.S. Smokeless Tobacco Company Tobacco articles and methods
US7810507B2 (en) 2006-02-10 2010-10-12 R. J. Reynolds Tobacco Company Smokeless tobacco composition
SE529886C2 (sv) 2006-04-28 2007-12-18 Swedish Match North Europe Ab En ny metod för framställning av en fuktsnuskomposition som inte innehåller tobak
US7946296B2 (en) * 2006-05-26 2011-05-24 Philip Morris Usa Inc. Dissolvable tobacco film strips and method of making the same
US20080029117A1 (en) 2006-08-01 2008-02-07 John-Paul Mua Smokeless Tobacco
DE602007010944D1 (de) * 2006-08-01 2011-01-13 Reynolds Tobacco Co R Rauchloser tabak
US20080029116A1 (en) 2006-08-01 2008-02-07 John Howard Robinson Smokeless tobacco
US20080173317A1 (en) 2006-08-01 2008-07-24 John Howard Robinson Smokeless tobacco
JP2008125498A (ja) * 2006-11-27 2008-06-05 Tetsuro Asao タバコ葉の製造方法
EP2089294A4 (en) 2006-12-12 2010-01-20 Meadwestvaco Corp PACKING WITH ROTATABLE LID
JP5780702B2 (ja) 2007-02-23 2015-09-16 ユーエス スモークレス タバコ カンパニー リミテッド ライアビリティ カンパニー タバコ組成物および作製法
US8186360B2 (en) 2007-04-04 2012-05-29 R.J. Reynolds Tobacco Company Cigarette comprising dark air-cured tobacco
US8393465B2 (en) 2007-05-07 2013-03-12 Philip Morris Usa Inc. Pocket-size hybrid container for consumer items
WO2009004488A2 (en) 2007-06-08 2009-01-08 Philip Morris Products S.A. Capsule clusters for oral consumption
US7946295B2 (en) 2007-07-23 2011-05-24 R. J. Reynolds Tobacco Company Smokeless tobacco composition
EP2179666B1 (en) * 2007-07-23 2012-08-29 R.J.Reynolds Tobacco Company Smokeless Tobacco Compositions And Methods For Treating Tobacco For Use Therein
US8061362B2 (en) 2007-07-23 2011-11-22 R. J. Reynolds Tobacco Company Smokeless tobacco composition
USD594154S1 (en) 2007-11-13 2009-06-09 R.J. Reynolds Tobacco Company Container with bottom compartment
US8336557B2 (en) 2007-11-28 2012-12-25 Philip Morris Usa Inc. Smokeless compressed tobacco product for oral consumption
US7878324B2 (en) 2007-11-30 2011-02-01 Philip Morris Usa Inc. Pocket-size container for consumer items
US20090230003A1 (en) 2008-02-08 2009-09-17 Philip Morris Usa Inc. Pocket-sized container
USD592956S1 (en) 2008-02-08 2009-05-26 Philip Morris Usa Inc. Container
US8033425B2 (en) 2008-03-04 2011-10-11 R.J. Reynolds Tobacco Company Dispensing container
US7946450B2 (en) 2008-04-25 2011-05-24 R.J. Reynolds Tobacco Company Dispensing container
CN101406318B (zh) * 2008-11-21 2011-07-13 深圳烟草工业有限责任公司 接近烟草甜的能明显增加卷烟甜韵的甜味功能聚类物制剂
US9248935B2 (en) 2008-12-01 2016-02-02 R.J. Reynolds Tobacco Company Dual cavity sliding dispenser
US9155772B2 (en) * 2008-12-08 2015-10-13 Philip Morris Usa Inc. Soft, chewable and orally dissolvable and/or disintegrable products
US9167835B2 (en) * 2008-12-30 2015-10-27 Philip Morris Usa Inc. Dissolvable films impregnated with encapsulated tobacco, tea, coffee, botanicals, and flavors for oral products
US8863755B2 (en) * 2009-02-27 2014-10-21 Philip Morris Usa Inc. Controlled flavor release tobacco pouch products and methods of making
US9167847B2 (en) * 2009-03-16 2015-10-27 Philip Morris Usa Inc. Production of coated tobacco particles suitable for usage in a smokeless tobacoo product
JP2012526553A (ja) 2009-05-11 2012-11-01 ユーエス スモークレス タバコ カンパニー リミテッド ライアビリティ カンパニー 無煙タバコに香味を付けるための方法およびデバイス
US20110139164A1 (en) 2009-12-15 2011-06-16 R. J. Reynolds Tobacco Company Tobacco Product And Method For Manufacture
US8955523B2 (en) 2010-01-15 2015-02-17 R.J. Reynolds Tobacco Company Tobacco-derived components and materials
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

Non-Patent Citations (1)

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

Also Published As

Publication number Publication date
JP2014533505A (ja) 2014-12-15
US20130125904A1 (en) 2013-05-23
JP6324897B2 (ja) 2018-05-16
WO2013074903A1 (en) 2013-05-23
EP2779849A1 (en) 2014-09-24
CN103997919A (zh) 2014-08-20

Similar Documents

Publication Publication Date Title
EP2779849B1 (en) Smokeless tobacco product comprising tobacco-derived pectin component
US11666083B2 (en) Meltable smokeless tobacco composition
EP2645885B1 (en) Smokeless tobacco pastille and moulding process for forming smokeless tobacco products
EP2645886B1 (en) Smokeless tobacco pastille and injection molding process for forming smokeless tobacco products
EP2779850B1 (en) Smokeless tobacco products with starch component
US20130263870A1 (en) Smokeless tobacco pastille and moulding process for forming smokeless tobacco products
US20230255257A1 (en) Meltable smokeless tobacco composition

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: 20140617

AK Designated contracting states

Kind code of ref document: A1

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

DAX Request for extension of the european patent (deleted)
GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

INTG Intention to grant announced

Effective date: 20180109

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

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 1009933

Country of ref document: AT

Kind code of ref document: T

Effective date: 20180715

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602012047693

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: NL

Ref legal event code: MP

Effective date: 20180620

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

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: 20180920

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: 20180620

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: 20180620

REG Reference to a national code

Ref country code: NO

Ref legal event code: T2

Effective date: 20180620

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

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

Ref country code: RS

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: 20180620

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: 20180620

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: 20180921

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: 20180620

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 1009933

Country of ref document: AT

Kind code of ref document: T

Effective date: 20180620

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: 20180620

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

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: 20180620

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: 20181020

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: 20180620

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: 20180620

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: 20180620

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: 20180620

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: 20180620

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

Ref country code: ES

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: 20180620

Ref country code: IT

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: 20180620

Ref country code: SM

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: 20180620

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602012047693

Country of ref document: DE

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: 20190321

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

Ref country code: DK

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: 20180620

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 602012047693

Country of ref document: DE

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20181116

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

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: 20180620

Ref country code: LU

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

Effective date: 20181116

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20181130

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: 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: 20180620

Ref country code: LI

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

Effective date: 20181130

Ref country code: CH

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

Effective date: 20181130

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

Ref country code: FR

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

Effective date: 20181130

Ref country code: IE

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

Effective date: 20181116

Ref country code: DE

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

Effective date: 20190601

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: 20181130

Ref country code: AL

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: 20180620

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

Ref country code: GB

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

Effective date: 20181116

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: 20181116

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: 20180620

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

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: 20180620

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: 20121116

Ref country code: MK

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

Effective date: 20180620

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: 20180620

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: SE

Payment date: 20230912

Year of fee payment: 12

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

Ref country code: NO

Payment date: 20231108

Year of fee payment: 12