WO2024068779A1

WO2024068779A1 - Flavour material with improved thermal release for an aerosol-generating article

Info

Publication number: WO2024068779A1
Application number: PCT/EP2023/076785
Authority: WO
Inventors: Loïc DA COSTA; Céline Dominique Gaël GAMBS; Houxue HUANG; Emmanuel Gérard René ROUGET
Original assignee: Philip Morris Products S.A.
Priority date: 2022-09-29
Filing date: 2023-09-27
Publication date: 2024-04-04

Abstract

There is provided a flavour material (50) for use in an aerosol-generating article, wherein the flavourant is releasable from the flavour material upon heating the flavour material. The flavour material (50) comprises a polysaccharide matrix structure and a flavourant formulation dispersed within the polysaccharide matrix structure. The flavourant formulation is at least partly trapped within the polysaccharide matrix structure and releasable from the polysaccharide matrix structure upon heating of the flavour material. The flavour material comprises greater than 0.1 weight percent carbon particles, the carbon particles having a volume mean particle size of greater than 10 micrometres. Also provided is an aerosol-generating article (10) comprising the flavour material (50).

Description

FLAVOUR MATERIAL WITH IMPROVED THERMAL RELEASE FOR AN AEROSOLGENERATING ARTICLE

The present disclosure relates to a flavour material for use in an aerosol-generating article. Further, the present disclosure relates to aerosol-generating articles comprising one such flavour material.

Aerosol-generating articles in which an aerosol-generating substrate, such as for example a tobacco-containing substrate or a non-tobacco, nicotine-containing substrate, is heated rather than combusted, are known in the art. Typically, in such heated smoking articles an aerosol is generated by the transfer of heat from a heat source to a physically separate aerosol-generating substrate or material, which may be located in contact with, within, around, or downstream of the heat source. During use of the aerosol-generating article, volatile compounds are released from the aerosol-generating substrate by heat transfer from the heat source and are entrained in air drawn through the aerosol-generating article. As the released compounds cool, they condense to form an aerosol.

Several aerosol-generating devices for consuming aerosol-generating articles have been disclosed in the art. Such devices include, for example, electrically heated aerosol-generating devices in which an aerosol is generated by the transfer of heat from one or more electrical heater elements of the aerosol-generating device to the aerosol-generating substrate of an aerosolgenerating article. For example, electrically heated aerosol-generating devices have been proposed that comprise an internal heater blade which is adapted to be inserted into the aerosolgenerating substrate. As an alternative, inductively heatable aerosol-generating articles comprising an aerosol-generating substrate and a susceptor arranged within the aerosolgenerating substrate have been proposed by WO 2015/176898.

It has been proposed to include in aerosol-generating articles a source of flavour in addition to the aerosol-generating substrate. In effect, this practice was relatively common with conventional filter cigarettes, and a number of solutions have been described in the art for providing a flavourant at a location in a mouthpiece filter or in the rod of tobacco cut filler.

However, given how the aerosol is generated and delivered to the consumer in aerosolgenerating articles, ensuring a consistent flavour delivery during use may be difficult, and so a consumer may perceive fluctuations or a decrease in flavour intensity over time. Additionally, even prior to the aerosol-generating articles being used, some flavour species may be lost during certain production steps or during transportation and storage of the aerosol-generating articles.

It has previously been proposed to reduce the loss of volatile flavourants from smoking conventional filter cigarettes during storage through the encapsulation of the flavourant, for example in the form of a capsule or microcapsule containing a flavour formulation. The encapsulated flavour species can be released prior to or during smoking of the filter cigarette by breaking open the encapsulating structure, for example by manually crushing the structure. However, the encapsulated flavourant is typically released from the encapsulating structure in a single burst, and so one such solution might fail to provide a consistently intense flavour delivery during use of the article.

Therefore, a need is felt to provide flavour materials, as well as aerosol-generating articles containing flavour materials, that are associated with an enhanced flavour perception for the consumer, particularly towards the end of the use cycle of the aerosol-generating article.

The present disclosure relates to a flavour material for use in an aerosol-generating article, wherein a flavourant formulation is releasable from the flavour material upon heating the flavour material. The flavour material may comprise a matrix structure and a flavourant formulation dispersed within the matrix structure. The flavourant formulation is at least partly trapped within the matrix structure and is releasable from the matrix structure upon heating of the flavour material. The matrix structure may be a polysaccharide matrix structure. The flavour material may comprise greater than 0.1 weight percent of carbon particles. The carbon particles may have a volume mean particle size of greater than 10 micrometres.

According to a first aspect of the present invention, there is provided a flavour material for use in an aerosol-generating article; the flavour material comprising: a polysaccharide matrix structure; and a flavourant formulation dispersed within the polysaccharide matrix structure. The flavourant formulation is at least partly trapped within the polysaccharide matrix structure and is releasable from the polysaccharide matrix structure upon heating of the flavour material. The flavour material comprises greater than 0.1 weight percent carbon particles. The carbon particles have a volume mean particle size of greater than 10 micrometres.

As used herein with reference to the invention, the term “aerosol-generating article” is used to describe an article comprising an aerosol-generating substrate that is heated to generate an inhalable aerosol for delivery to a user.

As used herein with reference to the invention, the term “aerosol-generating substrate” is used to describe a substrate comprising aerosol-generating material that is capable of releasing upon heating volatile compounds that can generate an aerosol.

As used herein with reference to the invention, the term “aerosol” is used to describe a dispersion of solid particles, or liquid droplets, or a combination of solid particles and liquid droplets, in a gas. The aerosol may be visible or invisible. The aerosol may include vapours of substances that are ordinarily liquid or solid at room temperature as well as solid particles, or liquid droplets, or a combination of solid particles and liquid droplets. As used herein with reference to the invention, the term “aerosol-generating device” is used to describe a device that interacts with the aerosol-generating substrate of the aerosolgenerating article to generate an aerosol.

Aerosol-generating articles according to the invention have a proximal end through which, in use, an aerosol exits the aerosol-generating article for delivery to a user. The proximal end of the aerosol-generating article may also be referred to as the downstream end or mouth end of the aerosol-generating article. In use, a user draws directly or indirectly on the proximal end of the aerosol-generating article in order to inhale an aerosol generated by the aerosol-generating article.

Aerosol-generating articles according to the invention have a distal end. The distal end is opposite the proximal end. The distal end of the aerosol-generating article may also be referred to as the upstream end of the aerosol-generating article.

Components of aerosol-generating articles according to the invention may be described as being upstream or downstream of one another based on their relative positions between the proximal end of the aerosol-generating article and the distal end of the aerosol-generating article.

As used herein with reference to the invention, the term “longitudinal” is used to describe the direction between the upstream end and the downstream end of the aerosol-generating article. During use, air is drawn through the aerosol-generating article in the longitudinal direction.

As used herein with reference to the invention, the term “length” is used to describe the maximum dimension of the aerosol-generating article or a component of the aerosol-generating article in the longitudinal direction.

As used herein with reference to the invention, the term “transverse” is used to describe the direction perpendicular to the longitudinal direction. Unless otherwise stated, references to the “cross-section” of the aerosol-generating article or a component of the aerosol-generating article refer to the transverse cross-section.

As used herein with reference to the invention, the term “width” denotes the maximum dimension of the aerosol-generating article or a component of the aerosol-generating article in a transverse direction. Where the aerosol-generating article has a substantially circular crosssection, the width of the aerosol-generating article corresponds to the diameter of the aerosolgenerating article. Where a component of the aerosol-generating article has a substantially circular cross-section, the width of the component of the aerosol-generating article corresponds to the diameter of the component of the aerosol-generating article.

As used herein with reference to the invention, the term "hollow tubular element" is used to denote a generally cylindrical element having a lumen along a longitudinal axis thereof. The tubular portion may have a substantially circular, oval or elliptical cross-section. The lumen may have a substantially circular, oval or elliptical cross-section. In particular, the term "hollow tubular element" is used to denote an element defining at least one airflow conduit establishing an uninterrupted fluid communication between an upstream end of the hollow tubular element and a downstream end of the tubular element.

The inclusion of carbon based material - such as graphite, expanded graphite, graphene, etc. - in flavour materials in accordance with the present invention has been found to enhance flavour release, particularly at lower temperatures, with respect to flavour materials having comparable composition and structure, but lacking the carbon based material. Without wishing to be bound by theory, this is hypothesised to relate to an enhancement of the thermal conductivity of the flavour material, which may cause the flavourant formulation to be more promptly released from the polysaccharide matrix structure as a certain threshold temperature may be reached more quickly.

The improvement in flavour release is thought to be linked to a more even temperature distribution throughout the flavour material during use. With a greater proportion of the flavour material reaching a sufficiently high temperature to release flavour species from the matrix structure, a higher usage efficiency of the flavourant formulation is made possible.

The improved release of flavour species afforded by flavour material thermals in accordance with the present invention may also allow a heater configured to supply heat to an aerosol-generating article incorporating the flavour material to operate at a lower temperature and thus require less power.

By adjusting the amount and size of the carbon particles within the ranges that will be described in more detail below, it may be possible to control and fine-tune the flavour release enhancement. For example, a relatively narrow particle size distribution may provide a flavour material that is more homogenous in terms of thermal conductivity. This may mean that, during use, temperature gradients in the flavour material provided in different portions of an aerosolgenerating article that are exposed to the same heating profile are minimised.

In general, it has been recognised that use of a flavour material in an aerosol-generating article, wherein an aerosol-generating substrate is meant to be heated to generate the aerosol, presents different challenges and poses different constraints, compared with conditions encountered in the past with conventional cigarettes, wherein a substrate is combusted to generate a smoke. The inventors have found that by adjusting the relative proportions of the various ingredients in the formulation or by altering the composition of the matrix - for example, by selecting certain combinations of polysaccharides to form the matrix - or by doing both, it may advantageously be possible to finely tailor certain characteristics of the flavour material to specific needs associated with use in an aerosol-generating article. For example, the flavour release profile may be adjusted, such as to have the flavour released in more successive “waves” during use. As a result, the consumer may perceive flavour notes as more intense or lingering for longer during use. Thus, flavour materials in accordance with the present invention may offer a wider breadth of flavour profiles that were not accessible with the known flavour materials.

When a flavour material in accordance with the invention is incorporated in an aerosolgenerating article, such as for example a heat-not-burn article configured to generate an aerosol upon heating a tobacco-containing aerosol-generating substrate, puff-by-puff flavour release has been found to be generally more efficient.

Because the flavourant formulation is at least partly trapped within the matrix until it is released upon heating, flavour materials in accordance with the present invention have been found to exhibit increased stability. For example, a significant reduction in losses of flavour species during storage, transportation, and so forth, has been observed, even under stress conditions. Coupled with the enhancement in flavour release, this makes for a particularly efficient use of flavourants and other ingredients of the flavour formulation.

In certain embodiments, the flavour material further comprises a carrier material. The polysaccharide matrix structure and the flavourant formulation trapped therein are supported by the carrier material, and the carrier material comprises the carbon particles.

This may be advantageous from a manufacturing viewpoint, as the carbon particles may be incorporated into the carrier material during manufacture of the carrier material itself.

In some embodiments, the carrier material is a carrier sheet material. As used herein, the term “sheet material” denotes a laminar material having a width and length substantially greater than the thickness thereof. For example, the carrier material may be a sheet of homogenised tobacco material or a sheet of a paper material. Advantageously, the carbon particles may be mixed with other constituents of the sheet material - for example, in the case of homogenised tobacco material, the carbon particles may be added to the slurry comprising tobacco particles from which the homogenised tobacco material is formed. Use of a homogenised tobacco material for manufacturing a flavour material in accordance with the present invention will be described in more detail below.

Embodiments wherein the carrier material is a carrier sheet material also have the advantage that the polysaccharide matrix structure and the flavourant formulation trapped therein may be deposited onto the carrier sheet material to form a flavour material that is, in effect, in sheet form and that can, as such, be cut into pieces having a predetermined average size (for example, a predetermined cut width or a predetermined cut length or both). This makes it easy to combine the flavour material with an aerosol-generating substrate in certain aerosol-generating articles, as will be described in more detail below.

In other embodiments, the carrier material may comprise a plurality of pieces cut from a sheet material, the pieces having a predetermined average size (for example, a predetermined cut width or a predetermined cut length or both). As an alternative, the carrier material may comprise a plurality of pieces cut from a naturally occurring plant material, preferably a plant leaf material (for example, tobacco lamina). In some embodiments, the carrier material may be tobacco cut filler.

In all the embodiments of the flavour material comprising a carrier material, the polysaccharide matrix structure trapping the flavourant formulation may be formed in situ on the carrier material. If this in situ formation step follows a manufacturing process from which the carrier material may is obtained, the in situ formation step may even be performed at a later date or at a different location.

Use of a carrier sheet material supporting polysaccharide matrix structure and the trapped flavourant formulation may have the added benefit that, by selecting and adjusting certain properties of the carrier sheet material (for example, its thickness) one may obtain a flavour material that is easier to form into a bobbin, and which can therefore be handled and processed more easily when the flavour material is incorporated into an aerosol-generating article. In view of a high speed automated manufacturing process, the increased structural strength provided by the carrier sheet material may be particularly beneficial.

At the same time, incorporating the carbon particles into a carrier sheet material may facilitate obtaining a homogenous distribution of the carbon particles per unit of surface area of carrier sheet material. Paired with the intimate contact between the polysaccharide matrix structure trapping the flavourant formulation and the carrier sheet material containing the carbon particles, this may ensure that an increase in thermal conductivity is exhibited homogenously across the flavour material. Advantageously, this may result in a particularly even temperature distribution throughout the flavour material in use.

This benefit is especially desirable if the carrier sheet material onto which the polysaccharide matrix structure trapping the flavourant formulation has been applied is cut or broken into smaller pieces for incorporation into an aerosol-generating article, as the various smaller pieces will tend to have similar flavour release profiles when exposed to a same heating profile.

As mentioned previously, in some preferred embodiments, the carrier sheet material may be in the form of a sheet of a homogenised tobacco material.

As used in the present specification, the term “homogenised tobacco material” encompasses any tobacco material formed by the agglomeration of particles of tobacco material. Sheets or webs of homogenised tobacco material are formed by agglomerating particulate tobacco obtained by grinding or otherwise powdering of one or both of tobacco leaf lamina and tobacco leaf stems. In addition, homogenised tobacco material may comprise a minor quantity of one or more of tobacco dust, tobacco fines, and other particulate tobacco by-products formed during the treating, handling and shipping of tobacco. The sheets of homogenised tobacco material may be produced by casting, extrusion, paper making processes or other any other suitable processes known in the art.

Sheets or webs of homogenised tobacco material for use in the invention may have a tobacco content of at least about 40 percent by weight on a dry weight basis, more preferably of at least about 60 percent by weight on a dry weight basis, more preferably or at least about 70 percent by weight on a dry basis and most preferably at least about 90 percent by weight on a dry weight basis.

Sheets or webs of homogenised tobacco material for use as the carrier sheet material may comprise one or more intrinsic binders, that is tobacco endogenous binders, one or more extrinsic binders, that is tobacco exogenous binders, ora combination thereof to help agglomerate the particulate tobacco. Alternatively, or in addition, sheets of homogenised tobacco material for use as the carrier sheet material may comprise other additives including, but not limited to, tobacco and non-tobacco fibres, aerosol-formers, humectants, plasticisers, flavourants, fillers, aqueous and non-aqueous solvents and combinations thereof.

Suitable extrinsic binders for inclusion in sheets or webs of homogenised tobacco material for use as the carrier sheet material are known in the art and include, but are not limited to: gums such as, for example, guar gum, xanthan gum, arabic gum and locust bean gum; cellulosic binders such as, for example, hydroxypropyl cellulose, carboxymethyl cellulose, hydroxyethyl cellulose, methyl cellulose and ethyl cellulose; polysaccharides such as, for example, starches, organic acids, such as alginic acid, conjugate base salts of organic acids, such as sodiumalginate, agar and pectins; and combinations thereof.

Suitable non-tobacco fibres for inclusion in sheets or webs of homogenised tobacco material for use as the carrier sheet material are known in the art and include, but are not limited to: cellulose fibres; soft-wood fibres; hard-wood fibres; jute fibres and combinations thereof. Prior to inclusion in sheets of homogenised tobacco material for use as the carrier sheet material, non- tobacco fibres may be treated by suitable processes known in the art including, but not limited to: mechanical pulping; refining; chemical pulping; bleaching; sulphate pulping; and combinations thereof.

Preferably, the sheets or webs of homogenised tobacco material comprise an aerosol former. As used herein, the term “aerosol former” describes any suitable known compound or mixture of compounds that, in use, facilitates formation of an aerosol and that is substantially resistant to thermal degradation at the operating temperature of the aerosol-generating article.

Suitable aerosol-formers are known in the art and include, but are not limited to: polyhydric alcohols, such as propylene glycol, triethylene glycol, 1 ,3-butanediol and glycerine; esters of polyhydric alcohols, such as glycerol mono-, di- or triacetate; and aliphatic esters of mono-, di- or polycarboxylic acids, such as dimethyl dodecanedioate and dimethyl tetradecanedioate. Preferred aerosol formers are polyhydric alcohols or mixtures thereof, such as propylene glycol, triethylene glycol, 1 ,3-butanediol and, most preferred, glycerine.

The sheets or webs of homogenised tobacco material may comprise a single aerosol former. Alternatively, the sheets or webs of homogenised tobacco material may comprise a combination of two or more aerosol formers.

The sheets or webs of homogenised tobacco material have an aerosol former content of greater than 10 percent on a dry weight basis. Preferably, the sheets or webs of homogenised tobacco material have an aerosol former content of greater than 12 percent on a dry weight basis. More preferably, the sheets or webs of homogenised tobacco material have an aerosol former content of greater than 14 percent on a dry weight basis. Even more preferably the sheets or webs of homogenised tobacco material have an aerosol former content of greater than 16 percent on a dry weight basis.

The sheets of homogenised tobacco material may have an aerosol former content of between approximately 10 percent and approximately 30 percent on a dry weight basis. Preferably, the sheets or webs of homogenised tobacco material have an aerosol former content of less than 25 percent on a dry weight basis.

In a preferred embodiment, the sheets of homogenised tobacco material have an aerosol former content of approximately 20 percent on a dry weight basis.

Sheets or webs of homogenised tobacco for use as the carrier sheet material in the flavour material of the present invention may be made by methods known in the art, for example the methods disclosed in International patent application WO-A-2012/164009 A2. In a preferred embodiment, sheets of homogenised tobacco material for use as the carrier sheet material are formed from a slurry comprising particulate tobacco, guar gum, cellulose fibres and glycerine by a casting process.

In other embodiments, the carrier sheet material may be in the form of a sheet of a nontobacco aerosol-generating material. For example, the carrier sheet material may be a sheet of sorbent non-tobacco material loaded with nicotine (for example, in the form of a nicotine salt) and an aerosol-former. Examples of such rods are described in the international application WO-A- 2015/082652. In addition, or as an alternative, the carrier sheet material may be a sheet of a homogenised non-tobacco plant material, such as an aromatic non-tobacco plant material.

In certain embodiments, the carrier sheet material may be in the form of a paper wrapper material. This has the benefit that the flavour material may be used as an alternative or in addition to conventional paper wrapper materials in the manufacture of an aerosol-generating article. Thus, the flavour material may be incorporated into the aerosol-generating article without significantly altering existing manufacturing processes and without requiring significant modifications of existing manufacturing apparatus. Preferably, the polysaccharide matrix structure comprises gellan gum and an emulsifier. The term “gellan gum” is used to identify a water-soluble anionic polysaccharide, which is produced by the bacterium Sphingomonas elodea. The repeating unit of the polymer is a tetrasaccharide, which consists of two residues of D-glucose and one of each residues of L- rhamnose and D-glucuronic acid. Gellan gum has been approved for food, non-food, cosmetic and pharmaceutical uses by authorities in many jurisdictions, such as Japan, USA, Canada, China, South Korea and the EU.

Two forms of gellan gum are known - namely, high acyl gellan gum and low acyl gellan gum - which differ by way of the degree/percent of substitution by O-acyl groups.

In flavour materials in accordance with the present invention, the gellan gum is preferably low acyl gellan gum. This is a gellan gum that is partly deacylated or fully deacylated. Its most common form is the fully deacylated one, with no detectable acyl groups, which is also called deacetylated gellan gum.

Use of low acyl gellan gum to form the polysaccharide matrix of a flavour material in accordance with the present invention is preferred because low acyl gellan gum is capable of forming gels at very low concentrations. Additionally, the texture of gellan gum based gels varies with the acyl content, low acyl gellan gum typically forming firmer, less elastic and more brittle gels compared with high acyl gellan gum.

In embodiments wherein the polysaccharide matrix structure comprises gellan gum and an emulsifier, a flavour material may advantageously be provided wherein a substantial fraction of the flavourant formulation is effectively trapped within the polysaccharide matrix structure. This is beneficial in that it improves the stability of the flavour material. Further, as it will be discussed in more detail below, it has an impact on how flavour species are released upon heating the flavour material, and so it may help tune a flavourant release profile during use.

Additionally, from a manufacturing viewpoint, a stable polysaccharide matrix structure comprising gellan gum and an emulsifier can be formed by supplying heat to the starting reagents without requiring the use of cross-linking agents. In fact, by kneading and emulsifying the flavour formulation and gellan gum in a heated aqueous bath, the polysaccharide-coated flavourant can be brought to an emulsified state which is then substantially preserved after drying and cooling. Advantageously, this allows for a significant amount of flavourant to be provided in an immobilised state within the polysaccharide matrix, and so a flavour material with a high flavourant content may be provided.

Preferably, the emulsifier is lecithin. Use of lecithin as the emulsifier is advantageous in that it is commonly available and generally recognised as being non-toxic. Like gellan gum, lecithin is commonly used in the food industry as an additive, and has been approved for such use by both the USA Food and Drug Administration and the EU authorities. As such, the pairing of gellan gum and lecithin is especially adapted to be included in a flavour material destined for human use.

Preferably, where the polysaccharide matrix comprises gellan gum and an emulsifier, the gellan gum makes up from 5 percent by weight to 99.9 percent by weight of the flavour material on a dry weight basis.

More preferably, the gellan gum makes up at least 7 percent by weight of the flavour material on a dry weight basis, even more preferably at least 10 percent by weight of the flavour material on a dry weight basis.

The gellan gum preferably makes up for up to 80 percent by weight of the flavour material on a dry weight basis, more preferably up to 60 percent by weight of the flavour material on a dry weight basis, even more preferably up to 40 percent by weight of the flavour material on a dry weight basis, particularly preferably up to 30 percent by weight of the flavour material on a dry weight basis.

In some embodiments, the gellan gum makes up from 5 percent by weight to 80 percent by weight of the flavour material on a dry weight basis, preferably from 5 percent by weight to 60 percent by weight of the flavour material on a dry weight basis, more preferably from 5 percent by weight to 40 percent by weight of the flavour material on a dry weight basis, even more preferably from 5 percent by weight to 30 percent by weight of the flavour material on a dry weight basis.

In other embodiments, the gellan gum makes up from 10 percent by weight to 80 percent by weight of the flavour material on a dry weight basis, preferably from 10 percent by weight to 60 percent by weight of the flavour material on a dry weight basis, more preferably from 10 percent by weight to 40 percent by weight of the flavour material on a dry weight basis, even more preferably from 10 percent by weight to 30 percent by weight of the flavour material on a dry weight basis.

The emulsifier may make up from 0.01 percent by weight to 2 percent by weight of the flavour material on a dry weight basis. Preferably, the emulsifier makes up from 0.02 percent by weight to 2 percent by weight of the flavour material on a dry weight basis. More preferably, the emulsifier makes up from 0.05 percent by weight to 2 percent by weight of the flavour material on a dry weight basis. Even more preferably, the emulsifier makes up from 0.1 percent by weight to 2 percent by weight of the flavour material on a dry weight basis.

In preferred embodiments, emulsifier is lecithin and makes up from 0.01 percent by weight to 2 percent by weight of the flavour material on a dry weight basis. Preferably, lecithin makes up from 0.02 percent by weight to 2 percent by weight of the flavour material on a dry weight basis. More preferably, lecithin makes up from 0.05 percent by weight to 2 percent by weight of the flavour material on a dry weight basis. Even more preferably, lecithin makes up from 0.1 percent by weight to 2 percent by weight of the flavour material on a dry weight basis.

In certain embodiments, the polysaccharide matrix structure comprises gellan gum as the sole polysaccharide.

In other embodiments, the polysaccharide matrix structure comprises gellan gum in combination with at least a further polysaccharide selected from the group consisting of guar, tamarind gum, sodium alginate, xanthan gum, sodium carboxymethyl cellulose, and hydroxypropyl methyl cellulose.

Flavour materials according to the invention wherein the polysaccharide matrix structure comprises gellan gum in combination with one or more of the polysaccharides listed above have been found to provide different flavourant release profiles upon heating. For example, in embodiments wherein the polysaccharide matrix structure comprises gellan gum in combination with another one of the polysaccharides listed above, a flavourant release profile characterised by two distinct peaks at two different temperatures has been observed. Without wishing to be bound by theory, it is hypothesised that this is due to a different strength of interaction between the flavourant and each polysaccharide in the matrix structure, and may also have to do with each polysaccharide undergoing thermal decomposition at slightly different temperatures.

Because different combinations of polysaccharides in the matrix structure will generally lead to slightly different flavourant release profiles when the flavour material is heated, embodiments wherein gellan gum is combined with one or more of the other polysaccharides listed above may advantageously be used to fine-tune the flavourant release during use of an aerosol-generating article containing the flavour material. Additionally, different flavour materials, each containing a polysaccharide matrix structure comprising a different combination of polysaccharides, may be used in combination in a single aerosol-generating article to further adjust and control flavourant delivery during a whole use cycle of the aerosol-generating article. For example, incorporating in a single aerosol-generating article different flavour materials according to the invention, wherein the different flavour materials are adapted to release most of the flavourant at different temperature or at different times during the use cycle may help maintain an overall flavour delivery substantially consistent throughout.

In embodiments of the flavour material wherein the matrix structure comprises gellan gum in combination with at least one of the additional polysaccharides listed above, the at least one additional polysaccharide may make up at least 0.01 percent by weight of the flavourant delivery material on a dry weight basis. Preferably, the at least one additional polysaccharide makes up at least 0.1 percent by weight of the flavourant delivery material on a dry weight basis. More preferably, the at least one additional polysaccharide makes up at least 1.0 percent by weight of the flavourant delivery material on a dry weight basis. Even more preferably, the at least one additional polysaccharide makes up at least 2.0 percent by weight of the flavourant delivery material on a dry weight basis. In particularly preferred embodiments, the at least one additional polysaccharide makes up at least 5 percent by weight of the flavourant delivery material on a dry weight basis.

In embodiments of the flavour material wherein the matrix structure comprises gellan gum in combination with at least one of the additional polysaccharides listed above, the at least one additional polysaccharide may make up 80 percent by weight or less of the flavourant delivery material on a dry weight basis. Preferably, the at least one additional polysaccharide makes up 35 percent by weight or less of the flavourant delivery material on a dry weight basis. More preferably, the at least one additional polysaccharide makes up 25 percent by weight or less of the flavourant delivery material on a dry weight basis. Even more preferably, the at least one additional polysaccharide makes up 15 percent by weight or less of the flavourant delivery material on a dry weight basis.

In some embodiments, the at least one additional polysaccharide makes up from 1.0 percent to 35 percent by weight or less of the flavourant delivery material on a dry weight basis, preferably from 2.0 percent to 35 percent by weight or less of the flavourant delivery material on a dry weight basis, more preferably from 5.0 percent to 35 percent by weight or less of the flavourant delivery material on a dry weight basis.

In other embodiments, the at least one additional polysaccharide makes up from 1.0 percent to 25 percent by weight or less of the flavourant delivery material on a dry weight basis, preferably from 2.0 percent to 25 percent by weight or less of the flavourant delivery material on a dry weight basis, more preferably from 5.0 percent to 25 percent by weight or less of the flavourant delivery material on a dry weight basis.

In further embodiments, the at least one additional polysaccharide makes up from 1.0 percent to 15 percent by weight or less of the flavourant delivery material on a dry weight basis, preferably from 2.0 percent to 15 percent by weight or less of the flavourant delivery material on a dry weight basis, more preferably from 5.0 percent to 15 percent by weight or less of the flavourant delivery material on a dry weight basis.

The flavour material may comprise at least 0.01 percent by weight of a flavourant on a dry weight basis. Preferably, the flavour material comprises at least 1 percent by weight of a flavourant on a dry weight basis. More preferably, the flavour material comprises at least 5 percent by weight of a flavourant on a dry weight basis. Even more preferably, the flavour material comprises at least 10 percent by weight of a flavourant on a dry weight basis.

In certain embodiments, the flavour material comprises at least 20 percent by weight of a flavourant on a dry weight basis, preferably at least 25 percent by weight of a flavourant on a dry weight basis, more preferably at least 30 percent by weight of a flavourant on a dry weight basis. The flavour material may up to 90 percent by weight of a flavourant on a dry weight basis. Preferably, the flavour material may up to 85 percent by weight of a flavourant on a dry weight basis. More preferably, the flavour material may up to 80 percent by weight of a flavourant on a dry weight basis. Even more preferably, the flavour material may up to 75 percent by weight of a flavourant on a dry weight basis.

In certain preferred embodiments, the flavour material comprises from 20 percent by weight to 80 percent by weight of a flavourant on a dry weight basis, preferably from 25 percent by weight to 80 percent by weight of a flavourant on a dry weight basis, more preferably from 30 percent by weight to 80 percent by weight of a flavourant on a dry weight basis.

In other preferred embodiments, the flavour material comprises from 20 percent by weight to 75 percent by weight of a flavourant on a dry weight basis, preferably from 25 percent by weight to 75 percent by weight of a flavourant on a dry weight basis, more preferably from 30 percent by weight to 75 percent by weight of a flavourant on a dry weight basis.

Suitable flavourants for inclusion in the flavour formulation of a flavour material in accordance with the present invention include, but are not limited to:

Suitable flavourants for inclusion in the flavour formulation of a flavour material in accordance with the present invention include, but are not limited to, menthol, limonene, and eugenol.

Menthol is a monoterpenoid, which may be made synthetically or obtained from the oils of peppermint or other mints. It imparts minty, cool flavour notes.

Limonene is a cyclic monoterpene, and is typically found in the oil of citrus fruit peels. It is also a component of the aromatic resins of numerous coniferous and broadleaved trees. It imparts citrusy flavour notes.

Eugenol is an allyl chain-substituted guaiacol, and is commonly found in the essential oils of clove, nutmeg, cinnamon, basil and bay leaf. It imparts spicy, clove-like flavour notes.

The inventors have found that menthol and limonene can be fairly easily trapped and immobilised within the polysaccharide matrix, and so flavour materials containing a flavour formulation containing menthol, limonene or mixtures thereof exhibit very good stability.

In preferred embodiments, the flavourant formulation comprises menthol.

The flavour material may comprise at least 0.01 percent by weight of a menthol on a dry weight basis. Preferably, the flavour material comprises at least 1 percent by weight of a menthol on a dry weight basis. More preferably, the flavour material comprises at least 5 percent by weight of a menthol on a dry weight basis. Even more preferably, the flavour material comprises at least 10 percent by weight of a menthol on a dry weight basis. In certain embodiments, the flavour material comprises at least 20 percent by weight of a menthol on a dry weight basis, preferably at least 25 percent by weight of a menthol on a dry weight basis, more preferably at least 30 percent by weight of a menthol on a dry weight basis.

The flavour material may up to 90 percent by weight of a menthol on a dry weight basis. Preferably, the flavour material may up to 85 percent by weight of a menthol on a dry weight basis. More preferably, the flavour material may up to 80 percent by weight of a menthol on a dry weight basis. Even more preferably, the flavour material may up to 75 percent by weight of a menthol on a dry weight basis.

In certain preferred embodiments, the flavour material comprises from 20 percent by weight to 80 percent by weight of a menthol on a dry weight basis, preferably from 25 percent by weight to 80 percent by weight of a menthol on a dry weight basis, more preferably from 30 percent by weight to 80 percent by weight of a menthol on a dry weight basis.

In other preferred embodiments, the flavour material comprises from 20 percent by weight to 75 percent by weight of a menthol on a dry weight basis, preferably from 25 percent by weight to 75 percent by weight of a menthol on a dry weight basis, more preferably from 30 percent by weight to 75 percent by weight of a menthol on a dry weight basis.

Preferably, the carbon particles consist of one or more of: graphite particles, expanded graphite particles and graphene particles. In a preferred embodiment, the carbon particles consist of one or both of expanded graphite particles and graphene particles.

Advantageously, particles such as those listed above, particularly graphite and expanded graphite, may have a high thermal conductivity and a low density, and so they may be able to substantially improve the thermal conductivity of the flavour material without significantly increasing the density of the flavour material. This may be advantageous in that an increase in density may increase the weight, and therefore the transport costs, for a given volume of the flavour material itself. Equally, an increase in density may potentially have a proportional impact on transport costs when the flavour material is incorporated into an aerosol-generating article.

Additionally, particles such as those listed above have the benefit that they may be inductively heated, and so heat may be supplied directly within a flavour material in accordance with the present invention when the flavour material is exposed to an electromagnetic field generated by an induction coil.

Preferably, the carbon particles have a volume mean particle size from 30 micrometres to 150 micrometres.

As used herein, the term “volume mean particle size” may refer to a mean calculated using the equation below, where d[4,3] is the volume mean particle size and d is the particle size.

In other words, the volume mean particle size may refer to a mean calculated by dividing the sum of the particle sizes to the fourth power by the sum of the particle sizes to the third power.

Surprisingly, the inventors have found these relatively small particle size ranges to be particularly effective at increasing the thermal conductivity of a flavour material, particularly when the flavour material is in the form of or comprises a sheet. In addition, these relatively small particle sizes may advantageously result in a more homogeneous distribution of thermal conductivity, and in a sheet having a more even thickness than if larger particle sizes were used.

In embodiments wherein the carbon particles are comprised within a carrier sheet material supporting the polysaccharide structure trapping the flavour formulation, it may also be easier to mix particles in this size range with the similarly sized particles used to manufacture the carrier sheet material, such as in the case of a sheet of homogenised tobacco material or other plant material.

The carbon particles may have a particle size distribution having a D10 particle size, a D50 particle size, and a D90 particle size. In such a particle size distribution, 10% of the particles have a particle size which is less than or equal to the D10 particle size and 90% of the particles have a particle size which is less than or equal to the D90 particle size. The D50 particle size is the median particle size so 50% of the particles have a particle size which is less than or equal to the D50 particle size.

The D90 particle size may be less than or equal to 50, 40, 30, 25, 20, 15, 10, 8, 5, or 3 times the D10 particle size. The D90 particle size may be greater than or equal to 2, 3, 5 or 8 times the D10 particle size.

The D90 particle size may be between 3 and 50, 3 and 40, 3 and 30, 3 and 25, 3 and 20, 3 and 15, 3 and 10, 3 and 8, 3 and 5, 5 and 50, 5 and 40, 5 and 30, 5 and 25, 5 and 20, 5 and 15, 5 and 10, 5 and 8, 8 and 50, 8 and 40, 8 and 30, 8 and 25, 8 and 20, 8 and 15, 8 and 10, 10 and 50, 10 and 40, 10 and 30, 10 and 25, 10 and 20, 10 and 15, 15 and 50, 15 and 40, 15 and 30, 15 and 25, 15 and 20 times the D10 particle size.

Preferred particle size distributions may have a D90 particle size between 3 and 25, or 3 and 15, times the D10 particle size. Particularly preferred particle size distributions may have a D90 particle size between 5 and 20, or 5 and 10, times the D10 particle size.

In certain preferred embodiments, in a flavour material according to the present invention the carbon particles have a particle size distribution with a D90 particle size and a D10 particles size, and the D90 particle size is no more than 25 or 15 times the D10 particle size.

A compromise must be made in relation to the particle size distribution. A tighter particle size distribution may advantageously provide a more uniform thermal conductivity throughout the flavour material. This is because there will be less variation in particle size in different locations in the flavour material. This may advantageously allow for more efficient usage of the flavourant formulation throughout the flavour material. However, a tighter particle size distribution may disadvantageously be more difficult and expensive to achieve. The inventors have found that the particle size distributions described above may provide an optimal compromise between these two factors.

Desired D10 and D90 particle sizes may be obtained by sieving. Sieving may therefore be used to obtain a narrow particle size distribution where desired.

The D10 particle size of the carbon particles may be greater than or equal to 1 , 2, 3, 5, 10, 20, 30, 35, 50, 75, 100, 150, 200, 250, 500, or 900 microns. Each of the carbon particles may have a particle size of greater than or equal to 1 , 2, 3, 5, 10, 20, 30, 35, 50, 75, 100, 150, 200, 250, 500, or 900 microns.

The D10 particle size of the carbon particles may be less than or equal to 1000, 900, 500, 200, 100, 150, 100, 75, 50, 35, 30, 20, 10, 5, 3 or 2 microns. Each of the carbon particles may have a particle size of less than or equal to 1000, 900, 500, 200, 100, 150, 100, 75, 50, 35, 30, 20, 10, 5, 3 or 2 microns.

The D90 particle size of the carbon particles may be less than or equal to 1000, 900, 500, 200, 100, 150, 100, 75, 50, 35, 30, 20, 10, 5, 3 or 2 microns. Each of the carbon particles may have a particle size of less than or equal to 1000, 900, 500, 200, 100, 150, 100, 75, 50, 35, 30, 20, 10, 5, 3 or 2 microns.

The D90 particle size of the carbon particles may be greater than or equal to 1 , 2, 3, 5, 10, 20, 30, 35, 50, 75, 100, 150, 200, 250, 500, or 900 microns. Each of the carbon particles may have a particle size of greater than or equal to 1 , 2, 3, 5, 10, 20, 30, 35, 50, 75, 100, 150, 200, 250, 500, or 900 microns.

One or both of a D50 particle size and a volume mean particle size of the carbon particles may be greater than or equal to 1 , 2, 3, 5, 10, 20, 30, 35, 50, 75, 100, 150, 200, 250, 500, or 900 microns.

One or both of a D50 particle size and a volume mean particle size of the carbon particles may be less than or equal to 1000, 900, 500, 200, 100, 150, 100, 75, 50, 35, 30, 20, 10, 5, 3 or 2 microns.

One or both of a D50 particle size and a volume mean particle size of the carbon particles may be between 1 and 1000, preferably between 10 and 200, more preferably between 30 and 150, or even more preferably between 50 and 75 microns. Alternatively, or in addition, each of the carbon particles may have a particle size of between 1 and 1000, preferably between 10 and 200, more preferably between 30 and 150, or even more preferably between 50 and 75 microns.

Surprisingly, the inventors have found these relatively small particle size ranges to be particularly effective at increasing the thermal conductivity of a flavour material in accordance with the present invention, particularly in those embodiments wherein the flavour material comprises a carrier sheet material supporting the polysaccharide matrix trapping the flavour formulation. In addition, these relatively small particle sizes may advantageously result in a more homogeneous carrier sheet material in terms of thermal conductivity, and in a carrier sheet material having a more even thickness than if larger particle sizes were used. It may also be easier to mix particles in this size range with the similarly sized particles used in some manufacturing processes for forming the carrier sheet material.

The carbon particles may have a volume mean particle size of greater than or equal to 1 , 2, 3, 5, 10, 20, 30, 35, 50, 75, 100, 150, 200, 250, 500, or 900 microns.

It may be particularly preferable that the volume mean particle size of the carbon particles is greater than 10 microns.

The carbon particles may have a volume mean particle size of less than or equal to 1000, 900, 500, 200, 100, 150, 100, 75, 50, 35, 30, 20, 10, 5, 3 or 2 microns.

The carbon particles may have a volume mean particle size of between 1 and 1000, 10 and 200, 30 and 150, or 50 and 75 microns. These volume mean particle size ranges may be particularly preferable where the flavour material comprises, or is in the form of, a sheet.

The carbon particles may have a volume mean particle size at least 2, 3, 5, 8, 10, 15, or 20 times the number mean particle size.

It may be particularly preferable that the thermally conductive particles are, or comprise, graphite particles.

The graphite particles may have a particle size distribution with a D10 particle size of between 5 and 20, for example 10 and 14, microns, for example around 12 microns. The graphite particles may have a particle size distribution with a D50 particle size of between 25 and 45 microns, for example around 35 microns. The graphite particles may have a particle size distribution with a D90 particle size of between 45 and 75 microns, for example around 55 microns. Advantageously, such particles are commercially available and have been found by the inventors to provide a significant increase in the thermal conductivity of flavour materials.

It may be particularly preferable that the thermally conductive particles are, or comprise, expanded graphite particles.

The expanded graphite particles may have a particle size distribution with a D10 particle size of between 5 and 20, for example 9 and 12, microns, for example around 10.5 microns. The expanded graphite particles may have a particle size distribution with a D50 particle size of between 15 and 25 microns, for example around 20 microns. The expanded graphite particles may have a particle size distribution with a D90 particle size of between 46 and 66 microns, for example around 56 microns. Advantageously, such particles are commercially available and have been found by the inventors to provide a significant increase in the thermal conductivity of flavour materials. The expanded graphite particles may also advantageously reduce the overall density of the flavour material.

Each of the carbon particles may have three mutually perpendicular dimensions. A largest dimension of these three dimensions may be no more than 10, 8, 5, 3, or 2 times larger than a smallest dimension of these three dimensions. A largest dimension of these three dimensions being no more than 10, 8, 5, 3, or 2 times larger than a second largest dimension of these three dimensions. Each of these three dimensions may be substantially equal. Each of the carbon particles may be substantially spherical.

The carbon particles may comprise at least 10, 20, 50, 100, 200, 500, or 1000 particles.

In a flavour material in accordance with the present invention, the carbon particles make up from 0.01 percent by weight to 10 percent by weight of the flavour material on a dry weight basis.

In some embodiments, the flavour material further comprises a polyol having the formula CnH2n+20n.

The term “polyol” is used herein to describe an organic compound comprising two or more hydroxyl groups. Polyols containing two, three, and four hydroxyl groups may also be referred to as diols, triols, and tetrols, respectively.

Preferred polyols for inclusion in a flavour material in accordance with the present invention include glycerol, sorbitol, xylitol, mannitol, and erythritol.

The incorporation of a polyol in the flavour material has a beneficial effect on its pliability. This may make the flavour material easier to handle and given a predetermined form, which may facilitate its incorporation into an aerosol-generating article.

Preferably, in embodiments where the flavour material comprises a polyol as described above, the polyol makes up from 0.01 percent by weight to 20 percent by weight of the flavour material on a dry weight basis. More preferably, the polyol makes up from 0.01 percent by weight to 15 percent by weight of the flavour material on a dry weight basis. Even more preferably, the polyol makes up from 0.01 percent by weight to 10 percent by weight of the flavour material on a dry weight basis.

In some embodiments, the flavour material comprises fibres, preferably cellulose fibres.

The incorporation of fibres, especially cellulose fibres, may advantageously improve the tensile strength of the flavour material, particularly when it is provided in sheet form. This facilitates the manufacturing process, both of the flavour material itself and of an aerosolgenerating article including the flavour material. The benefit is felt especially in those embodiments wherein the polysaccharide matrix trapping the flavourant formulation is not supported by a carrier material. In embodiments of the flavour material comprising cellulose fibres, the cellulose fibres may make up at least 0.01 percent by weight of the flavour material on a dry weight basis. Preferably, the cellulose fibres make up at least 0.05 percent by weight of the flavour material on a dry weight basis. More preferably, the cellulose fibres make up at least 0.5 percent by weight of the flavour material on a dry weight basis. Even more preferably, the cellulose fibres make up at least 1.0 percent by weight of the flavour material on a dry weight basis. In particularly preferred embodiments, the cellulose fibres make up at least 2.0 percent by weight of the flavour material on a dry weight basis.

The cellulose fibres may make up 10 percent by weight or less of the flavour material on a dry weight basis. Preferably, the cellulose fibres make up 8.0 percent by weight or less of the flavour material on a dry weight basis. More preferably, the cellulose fibres make up 7.0 percent by weight or less of the flavour material on a dry weight basis. Even more preferably, the cellulose fibres make up 5.0 percent by weight or less of the flavour material on a dry weight basis.

In some embodiments, the fibres make up from 0.01 percent by weight to 10 percent by weight of the flavour material on a dry weight basis. Preferably, the fibres make up from 0.01 percent by weight to 8.0 percent by weight of the flavour material on a dry weight basis. More preferably, the fibres make up from 0.01 percent by weight to 7.0 percent by weight of the flavour material on a dry weight basis. Even more preferably, the fibres make up from 0.01 percent by weight to 5 percent by weight of the flavour material on a dry weight basis.

In other embodiments, the fibres make up from 1.0 percent by weight to 10 percent by weight of the flavour material on a dry weight basis. Preferably, the fibres make up from 1 .0 percent by weight to 8.0 percent by weight of the flavour material on a dry weight basis. More preferably, the fibres make up from 1 .0 percent by weight to 7.0 percent by weight of the flavour material on a dry weight basis. Even more preferably, the fibres make up from 1 .0 percent by weight to 5 percent by weight of the flavour material on a dry weight basis.

In further embodiments, the fibres make up from 2.0 percent by weight to 10 percent by weight of the flavour material on a dry weight basis. Preferably, the fibres make up from 2.0 percent by weight to 8.0 percent by weight of the flavour material on a dry weight basis. More preferably, the fibres make up from 2.0 percent by weight to 7.0 percent by weight of the flavour material on a dry weight basis. Even more preferably, the fibres make up from 2.0 percent by weight to 5 percent by weight of the flavour material on a dry weight basis.

In some embodiments, a flavour material in accordance with the present invention may comprise a salt of calcium or a salt of magnesium or both, such as calcium chloride or calcium lactate.

In embodiments where the flavour material comprises a salt of calcium or a salt of magnesium or both, the salt or salts make up from 0.01 percent by weight to 10 percent by weight on a dry weight basis. Preferably, the salt or salts make up from 0.01 percent by weight to 5 percent by weight on a dry weight basis.

In embodiments where the flavour material comprises a citrate salt, the citrate salt makes up from 0.01 percent by weight to 5 percent by weight on a dry weight basis. Preferably, the citrate salt makes up from 0.01 percent by weight to 1 percent by weight on a dry weight basis.

A flavour material in accordance with the present invention may generally comprise water. This is because the flavour material will generally be manufactured by combining the various compounds described above in an aqueous bath. After drying, the water content will be reduced, but may generally be non-null.

Thus, a flavour material in accordance with the present invention may comprise from 0.01 percent by weight to 10 percent by weight of water, preferably from 0.01 percent by weight to 8 percent by weight of water, more preferably from 0.01 percent by weight to 6 percent by weight of water, even more preferably from 0.01 percent by weight to 4 percent by weight of water.

In some embodiments, the flavour material comprises from 0.5 percent by weight to 10 percent by weight of water, preferably from 0.01 percent by weight to 8 percent by weight of water, more preferably from 0.5 percent by weight to 6 percent by weight of water, even more preferably from 0.5 percent by weight to 4 percent by weight of water.

In other embodiments, the flavour material comprises from 1.0 percent by weight to 10 percent by weight of water, preferably from 1.0 percent by weight to 8 percent by weight of water, more preferably from 1 .0 percent by weight to 6 percent by weight of water, even more preferably from 1 .0 percent by weight to 4 percent by weight of water.

In further embodiments, the flavour material comprises from 1.5 percent by weight to 10 percent by weight of water, preferably from 1.5 percent by weight to 8 percent by weight of water, more preferably from 1 .5 percent by weight to 6 percent by weight of water, even more preferably from 1.5 percent by weight to 4 percent by weight of water.

Flavour materials in accordance with the present invention can be prepared by different routes.

A method of manufacturing a flavour material in accordance with the present invention may comprise a first step of preparing an aqueous composition comprising a flavour formulation, a polysaccharide and an emulsifier; a second step of casting the aqueous composition over a substantially flat support surface; a third step of letting the aqueous composition jellify on the support surface; a fourth step of drying the jellified aqueous composition. The dried flavour material may subsequently be removed from the support surface. The support surface may be a metallic plate.

Another method of manufacturing a flavour delivery in accordance with the present invention may comprise a first step of preparing an aqueous composition comprising a flavour formulation, a polysaccharide and an emulsifier; a second step of casting the aqueous composition over a carrier sheet material lying on a substantially flat support surface; a third step of letting the aqueous composition jellify on the carrier sheet material; a fourth step of drying the jellified aqueous composition and the carrier sheet material. The dried flavour material wherein the carrier sheet material supports a polysaccharide matrix trapping the flavour formulation may subsequently be removed from the support surface.

A further method of manufacturing a flavour delivery in accordance with the present invention may comprise a first step of preparing an aqueous composition comprising a flavour formulation, a polysaccharide and an emulsifier; a second step of spraying the aqueous composition over a carrier sheet material (for example, homogenised tobacco material) lying on a substantially flat support surface; a third step of letting the aqueous composition jellify on the carrier sheet material; a fourth step of drying the jellified aqueous composition and the carrier sheet material. The dried flavour material wherein the carrier sheet material supports a polysaccharide matrix trapping the flavour formulation may subsequently be removed from the support surface.

The present disclosure relates to an aerosol-generating article comprising a flavour material, wherein a flavourant formulation is releasable from the flavour material upon heating the flavour material. The flavour material may comprise a matrix structure and a flavourant formulation dispersed within the matrix structure. The flavourant formulation is at least partly trapped within the matrix structure and is releasable from the matrix structure upon heating of the flavour material. The matrix structure may be a polysaccharide matrix structure. The flavour material may comprise greater than 0.1 weight percent of carbon particles. The carbon particles may have a volume mean particle size of greater than 10 micrometres.

According to a second aspect of the present invention, there is provided an aerosolgenerating article comprising a flavour material, wherein the flavourant is releasable from the flavour material upon heating the flavour-delivery material. The flavour material comprises a polysaccharide matrix structure; and a flavourant formulation dispersed within the polysaccharide matrix structure. The flavourant formulation is trapped within the polysaccharide matrix structure and releasable from the polysaccharide matrix structure upon heating of the flavour material. The flavour material comprises greater than 0.1 weight percent carbon particles, the carbon particles having a volume mean particle size of greater than 10 micrometres.

As will be apparent from the foregoing description of flavour materials in accordance with the present invention, by incorporating one such flavour material in an aerosol-generating article it is advantageously possible to provide a new range of aerosol-generating articles capable of delivering flavour to a consumer in a more consistent and controlled manner. Additionally, because the flavourant formulation is at least partly trapped within the matrix until it is released when heat is supplied to the aerosol-generating article during use, losses of flavour species during storage and transportation of the aerosol-generating articles can be greatly reduced. Coupled with the enhancement in flavour release, this makes for a particularly efficient use of flavourants and other ingredients of the flavour formulation.

Aerosol-generating articles in accordance with the present invention have been found to provide a more efficient release of flavour species during use compared with corresponding aerosol-generating articles containing an equivalent flavour material not including carbon particles in line with the foregoing description. In particular, release of flavour species has been observed to remain consistently higher and to vary less significantly from one puff to the next.

In certain embodiments, in aerosol-generating articles in accordance with the present invention the flavour material further comprises a carrier sheet material, wherein the polysaccharide matrix structure and the flavourant formulation are supported by the carrier sheet material, and wherein the carrier sheet material comprises the carbon particles.

The carrier sheet material provides a support for the polysaccharide matrix structure trapping the flavourant formulation, and so by adjusting the composition and geometry of the carrier sheet material it may be possible to facilitate manufacturing of the aerosol-generating article.

In certain embodiments, the aerosol-generating article comprises a rod of aerosolgenerating substrate; a downstream section provided downstream of the rod of aerosolgenerating substrate and extending to a mouth end of the aerosol-generating article; optionally an upstream section provided downstream of the rod of aerosol-generating substrate and extending to a distal end of the aerosol-generating article. The flavour material is provided in at least one of the rod of aerosol-generating substrate; the downstream section; and the optional upstream section.

Where the flavour material comprises a carrier sheet material as described above, the carrier sheet material may be a sheet of homogenised tobacco material. In those embodiments, the aerosol-generating article may comprise a rod of aerosol-generating substrate; a downstream section provided downstream of the rod of aerosol-generating substrate and extending to a mouth end of the aerosol-generating article; optionally an upstream section provided downstream of the rod of aerosol-generating substrate and extending to a distal end of the aerosol-generating article; and the flavour material may be provided in the rod of aerosol-generating substrate.

Incorporation of a flavour material in accordance with the present invention in an aerosolgenerating article may be carried out according to one of several routes.

For example, pieces of the flavour material may be mixed with solid particles of an aerosolgenerating material, such as cut tobacco, to form the rod of aerosol-generating substrate of an aerosol-generating article. As an alternative, or additionally, pieces of the flavour material may be provided at other locations within the aerosol-generating article, such as locations along the downstream section of the aerosol-generating article. The downstream section of the aerosol-generating article may comprise multiple components, and so the flavour material may be incorporated into any one of such components.

As a further alternative, a flavour material comprising a carrier sheet material in the form of a paper wrapper may be used as a plug wrap for the rod of aerosol-generating article alone or in combination with another paper wrapper.

This list of possible arrangements is not meant to be exhaustive, and it will be apparent that different placements of a flavour material in an aerosol-generating article may be possible, provided that during use of the aerosol-generating article the flavour material is supplied with enough heat to release the flavour formulation from the polysaccharide matrix.

An aerosol-generating article containing a flavour material in accordance with the present invention may be used in combination with an aerosol-generating device, such as a hand-held electrical heater configured to supply heat in a controlled manner to the aerosol-generating article. This is so, by heating the aerosol-generating substrate and the flavour material, a flavour-enriched aerosol can be delivered to a consumer.

As such, aerosol-generating articles according to the invention find particular application in aerosol-generating systems comprising an aerosol-generating device having a heating chamber into which the aerosol-generating article according to the second aspect of the invention is received such that heat can be supplied to the aerosol-generating substrate. This may be achieved by providing one or more heating elements arranged about the periphery of the heating chamber, the one or more heating elements being heated resistively or inductively. Alternatively, this may also be achieved by way of a resistively heated blade-shaped component of the aerosolgenerating device, which is inserted into the aerosol-generating substrate when the aerosolgenerating article is inserted into the heating chamber.

According to yet another alternative, a susceptor element may be provided within the aerosol-generating substrate, and the aerosol-generating device may have an inductor for producing an alternating or fluctuating electromagnetic field. When the aerosol-generating article engages with the aerosol-generating device, the fluctuating electromagnetic field produced by the inductor induces a current in the susceptor element, causing the susceptor element to heat up. The electrically-operated aerosol-generating device may be capable of generating a fluctuating electromagnetic field having a magnetic field strength (H-field strength) of between 1 and 5 kilo amperes per metre (kA m), preferably between 2 and 3 kA/m, for example about 2.5 kA/m. The invention is defined in the claims. However, below there is provided a non-exhaustive list of non-limiting examples. Any one or more of the features of these examples may be combined with any one or more features of another example, embodiment, or aspect described herein.

Example Ex1 : A flavour material for use in an aerosol-generating article, wherein the flavourant is releasable from the flavour material upon heating the flavour material; the flavour material comprising: a polysaccharide matrix structure; and a flavourant formulation dispersed within the polysaccharide matrix structure, wherein the flavourant formulation is at least partly trapped within the polysaccharide matrix structure and releasable from the polysaccharide matrix structure upon heating of the flavour material; and greater than 0.1 weight percent carbon particles, the carbon particles having a volume mean particle size of greater than 10 micrometres.

Example Ex2: A flavour material according to Ex1 further comprising a carrier sheet material, wherein the polysaccharide matrix structure and the flavourant formulation are supported by the carrier sheet material, and wherein the carrier sheet material comprises the carbon particles.

Example Ex 3: A flavour material according to Ex2, wherein the carrier sheet material is one of a sheet of homogenised tobacco material, a sheet of non-tobacco aerosol-generating material, a paper wrapper material.

Example Ex4: A flavour material according to any one of the preceding Examples, wherein the polysaccharide matrix structure comprises gellan gum and an emulsifier.

Example Ex 5: A flavour material according to Example Ex 4, wherein the emulsifier is lecithin.

Example Ex6: A flavour material according to Example Ex 4 or Ex5, wherein the polysaccharide matrix structure comprises gellan gum as the sole polysaccharide or gellan gum in combination with at least a further polysaccharide selected from the group consisting of guar, tamarind gum, sodium alginate, xanthan gum, sodium carboxymethyl cellulose, and hydroxypropyl methyl cellulose.

Example Ex7: A flavour material according to any one of Examples Ex 4, Ex5, and Ex6, wherein the gellan gum makes up from 5 percent by weight to 99.9 percent by weight of the flavour material on a dry weight basis.

Example Ex8: A flavour material according to any one of the preceding claims, further comprising a polyol having the formula C_nH2n+2O_n.

Example Ex9: A flavour material according to Example Ex8, wherein the polyol is selected from the group consisting of glycerol, sorbitol, xylitol, mannitol, and erythritol. Example Ex10: A flavour material according to Example Ex8 or Ex9, wherein the polyol makes up from 0.01 percent by weight to 20 percent by weight of the flavour material on a dry weight basis.

Example Ex 11 : A flavour material according to any one of the preceding Examples, wherein the carbon particles consist of one or more of: graphite particles, expanded graphite particles and graphene particles.

Example Ex12: A flavour material according to any one of the preceding claims, wherein the carbon particles have a volume mean particle size from 30 micrometres to 150 micrometres.

Example Ex13: A flavour material according to any one of the preceding claims, wherein the carbon particles have a particle size distribution with a D90 particle size and a D10 particles size, wherein the D90 particle size is no more than 25 or 15 times the D10 particle size.

Example Ex14: A flavour material according to any one of the preceding claims, wherein the carbon particles make up from 0.01 percent by weight to 10 percent by weight of the flavour material on a dry weight basis.

Example Ex15: A flavour material according to any one of the preceding claims further comprising fibres.

Example Ex16: A flavour material according to Example Ex 15, wherein the fibres make up from 0.01 percent by weight to 10 percent by weight of the flavour material on a dry weight basis.

Example Ex17: A flavour material according to any one of the preceding claims comprising from 0.01 percent by weight to 80 percent by weight of menthol on a dry weight basis.

Example Ex18: An aerosol-generating article comprising a flavour material according to any one of Examples Ex1 to Ex17.

Example Ex19: An aerosol-generating article comprising a flavour material, wherein the flavourant is releasable from the flavour material upon heating the flavour-delivery material; the flavour material comprising: a polysaccharide matrix structure; and a flavourant formulation dispersed within the polysaccharide matrix structure, wherein the flavourant formulation is trapped within the polysaccharide matrix structure and releasable from the polysaccharide matrix structure upon heating of the flavour material; and wherein the flavour material comprises greater than 0.1 weight percent carbon particles, the carbon particles having a volume mean particle size of greater than 10 micrometres, wherein flavour material further comprises a carrier sheet material, wherein the polysaccharide matrix structure and the flavourant formulation are supported by the carrier sheet material, and wherein the carrier sheet material comprises the carbon particles.

Example Ex20: An aerosol-generating article according to Example Ex 18 or Ex19, the article comprising: a rod of aerosol-generating substrate; a downstream section provided downstream of the rod of aerosol-generating substrate and extending to a mouth end of the aerosol-generating article; optionally an upstream section provided downstream of the rod of aerosol-generating substrate and extending to a distal end of the aerosol-generating article; wherein the flavour material is provided in at least one of the rod of aerosol-generating substrate; the downstream section; and the optional upstream section.

Example Ex 21 : An aerosol-generating article according to Example Ex19, wherein the carrier sheet material is a sheet of homogenised tobacco material; wherein the aerosol-generating article comprises a rod of aerosol-generating substrate; a downstream section provided downstream of the rod of aerosol-generating substrate and extending to a mouth end of the aerosol-generating article; optionally an upstream section provided downstream of the rod of aerosol-generating substrate and extending to a distal end of the aerosol-generating article; wherein the flavour material is provided in the rod of aerosol-generating substrate.

Examples will now be further described with reference to the figures in which:

Figure 1 shows a schematic side cross-sectional view of an aerosol-generating article in accordance with the present invention comprising a flavour material in the rod of aerosolgenerating substrate;

Figure 2 shows a scanning electron microscope image of the flavour material used in the aerosol-generating article of Figure 1 ; and

Figure 3 shows a scanning electron microscope image of another flavour material in accordance with the present invention.

An aerosol-generating article 10 in accordance with the present invention is shown in Figure 1. The aerosol-generating article 10 shown in Figure 1 comprises a rod 12 of aerosol-generating substrate and a downstream section 14 at a location downstream of the rod 12 of aerosolgenerating substrate. Further, the aerosol-generating article 10 comprises an upstream section 16 at a location upstream of the rod 12 of aerosol-generating substrate.

A ventilation zone 60 is provided at a location downstream of the rod 12 of aerosolgenerating substrate.

In more detail, in the embodiment of Figure 1 , the downstream section 14 comprises a mouthpiece element 18 and a hollow section 20. The hollow section 20 comprises an aerosolcooling element 22 comprising a hollow tubular element and the ventilation zone 60, which comprises a plurality of openings formed through a wall of the hollow tubular element. The aerosol-cooling element 22 is positioned immediately downstream of the rod 12 of aerosolgenerating substrate. As shown in the drawing of Figure 1 , an upstream end of the aerosolcooling element 22 abuts a downstream end of the rod 12 of aerosol-generating substrate. The mouthpiece element 18 is positioned immediately downstream of the aerosol-cooling element 22. As shown in the drawing of Figure 1 , an upstream end of the mouthpiece element 18 abuts a downstream end of the aerosol-cooling element 22. The mouthpiece element 18 comprises a plug 24 of low-density filtration material. The rod 12 comprises an aerosol-generating substrate in the form of a gathered sheet of homogenised tobacco material. However, other types of tobacco-containing substrate, such as a tobacco cut filler, can replace the gathered sheet of homogenised tobacco material.

The upstream section 16 comprises a cylindrical plug 26 of compressed and plasticised cellulose acetate circumscribed by a wrapper 28. The plug 26 of the upstream section 16 has a length of about 5 millimetres.

Further, the aerosol-generating article comprises a flavour material 50. In more detail, a plurality of pieces of a flavour material in sheet form are dispersed within the rod 12. The flavour material 50 is of the type described in detail above.

Examples of suitable formulations for the flavour material 50 and processes for forming the flavour material 50 are set out below.

Preparation A - Flavour material comprising a menthol formulation trapped in a gellan gum polysaccharide matrix

100 g of water are heated to about 60 degrees Celsius and 3.0 g of gellan gum are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 80 to 85 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin, 1.1 g of graphite and 8.0 g of menthol are added to the mixture. The flavourcontaining mixture is homogenized for 3 minutes. Subsequently, the resulting aqueous composition is cast on a metallic tray, left to jellify and dried in a still oven at 65 degrees Celsius. A flavour material in sheet form is obtained.

Preparation B - Flavour material comprising a menthol formulation trapped in a gellan gum r polysaccharide matrix

100 g of water are heated to about 60 degrees Celsius and 1.0 g of gellan gum are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 80 to 85 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin, 1.1 g of graphite and 8.0 g of menthol are added to the mixture. The flavourcontaining mixture is homogenized for 3 minutes. Subsequently, 2.0 g of guar are added to the mixture, which is then homogenised again for another 3 minutes. Subsequently, the resulting aqueous composition is cast on a metallic tray, left to jellify and dried in a still oven at 75 degrees Celsius. A flavour material in sheet form is obtained.

Preparation C - Flavour material comprising a menthol formulation trapped in a gellan gum accharide matrix supported on a carrier sheet material (paper wrapper)

100 g of water are heated to about 60 degrees Celsius and 3.0 g of gellan gum are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 80 to 85 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin and 8.0 g of menthol are added to the mixture. The flavour-containing mixture is homogenized for 3 minutes. Subsequently, the resulting aqueous composition is cast on a paper wrapper comprising graphite particles located on a metallic tray, left to jellify and dried in a still oven at 65 degrees Celsius. A flavour material comprising a layer of gellan gum matrix trapping the menthol formulation immobilised on the graphite-containing paper wrapper is obtained.

Preparation D - Flavour material comprising a menthol formulation trapped in a gellan gum polysaccharide matrix supported on a carrier sheet material (homogenised tobacco material)

100 g of water are heated to about 60 degrees Celsius and 3.0 g of gellan gum are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 80 to 85 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin and 8.0 g of menthol are added to the mixture. The flavour-containing mixture is homogenized for 3 minutes. Subsequently, the resulting aqueous composition is cast on a sheet of homogenised tobacco material comprising graphite particles located on a metallic tray, left to jellify and dried in a still oven at 65 degrees Celsius. A flavour material comprising a layer of gellan gum matrix trapping the menthol formulation immobilised on the graphite-containing homogenised tobacco material is obtained.

Preparation E - Flavour material comprising a menthol formulation trapped in a gellan gum - guar polysaccharide matrix supported on a carrier sheet material (homogenised tobacco material)

100 g of water are heated to about 60 degrees Celsius and 1.0 g of gellan gum are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 80 to 85 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin and 8.0 g of menthol are added to the mixture. The flavour-containing mixture is homogenized for 3 minutes. Subsequently, 2.0 g of guar are added to the mixture, which is then homogenised again for another 3 minutes. Subsequently, the resulting aqueous composition is cast on on a sheet of homogenised tobacco material comprising graphite particles and located on a metallic tray, left to jellify and dried in a still oven at 65 degrees Celsius. A flavour material comprising a layer of gellan gum I guar matrix trapping the menthol formulation immobilised on the graphite-containing homogenised tobacco material is obtained. Preparation F - Flavour material comprising a menthol formulation trapped in a qellan gum - alginate matrix supported on a carrier sheet material (homogenised tobacco material)

100 g of water are heated to about 60 degrees Celsius and 2.0 g of gellan gum and 0.5 g of alginate are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 90 to 95 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin and 8.0 g of menthol are added to the mixture. The flavour-containing mixture is homogenized for 3 minutes. Subsequently, 2.0 g of guar are added to the mixture, which is then homogenised again for another 3 minutes. Subsequently, the resulting aqueous composition is cast on on a sheet of homogenised tobacco material comprising graphite particles and located on a metallic tray, left to jellify and dried in a still oven at 65 degrees Celsius. A flavour material comprising a layer of gellan gum I alginate matrix trapping the menthol formulation immobilised on the graphite-containing homogenised tobacco material is obtained.

Preparation G - Aerosol-generating article comprising a flavour material produced according to Preparation A

An amount of flavour material produced according to Preparation A making up for an overall content of menthol of 5 mg was added to the rod of a commercially available aerosol-generating article (HEET® by Philip Morris Products S.A.).

Comparative Preparation A - Flavour material comprising a menthol formulation trapped in a gellan gum polysaccharide matrix supported on a carrier sheet material (homogenised tobacco material)

100 g of water are heated to about 60 degrees Celsius and 3.0 g of gellan gum are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 80 to 85 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin and 8.0 g of menthol are added to the mixture. The flavour-containing mixture is homogenized for 3 minutes. Subsequently, the resulting aqueous composition is cast on a sheet of homogenised tobacco material free of graphite particles and located on a metallic tray, left to jellify and dried in a still oven at 65 degrees Celsius. A flavour material comprising a layer of gellan gum matrix trapping the menthol formulation immobilised on the graphite-free homogenised tobacco material is obtained.

Comparative Preparation B - Flavour material comprising a menthol formulation trapped in a qellan gum - guar polysaccharide matrix supported on a carrier sheet material (homogenised tobacco material)

100 g of water are heated to about 60 degrees Celsius and 1.0 g of gellan gum are added to the water bath. The resulting mixture is homogenized and heated to a temperature in the range from 80 to 85 degrees Celsius and kept at this temperature for 5 minutes. The mixture is subsequently cooled down to a temperature in the range from 70 to 75 degrees Celsius and 0.1 g of lecithin and 8.0 g of menthol are added to the mixture. The flavour-containing mixture is homogenized for 3 minutes. Subsequently, 2.0 g of guar are added to the mixture, which is then homogenised again for another 3 minutes. Subsequently, the resulting aqueous composition is cast on on a sheet of homogenised tobacco material free of particles and located on a metallic tray, left to jellify and dried in a still oven at 65 degrees Celsius. A flavour material comprising a layer of gellan gum I guar matrix trapping the menthol formulation immobilised on the graphite- free homogenised tobacco material is obtained.

Comparative Preparation C - Aerosol-generating article comprising a flavour material produced according to Comparative Preparation A

An amount of flavour material produced according to Comparative Preparation A making up for an overall content of menthol of 5 mg was added to the rod of a commercially available aerosol-generating article (HEET® by Philip Morris Products S.A.)

Morphologic characterisation

Figure 2 shows a scanning electron microscope (SEM) image of the flavour material 50 produced in accordance with Preparation E embedded in a wax. It can be seen from the image that the internal structure of the flavour material includes a matrix 52 with a plurality of small pockets 54 adapted to trap the flavour composition, the pockets 54 being dispersed through the matrix 52. The pockets are relatively uniformly distributed through the material and are relatively consistent in size. The flavour material 50 further comprises a carrier sheet material 56 in the form of a sheet of homogenised tobacco material containing graphite particles, the carrier sheet material 56 supporting the matrix 52. The SEM technology does not allow for the graphite particles to be distinguished from the remainder of the carrier sheet material.

Figure 3 shows a SEM image of a flavour material 150 produced in accordance with Preparation A embedded in a wax. It can be seen from the image that the internal structure of the flavour material includes a matrix 52 with a plurality of small pockets 54 adapted to trap the flavour composition, the pockets 54 being dispersed through the matrix 52. The domains are relatively uniformly distributed through the material and are relatively consistent in size. In contrast to the flavour material 50 of Figure 2, the flavour material 150 does not comprise a carrier sheet material supporting the matrix, and carbon particles are embedded in the matrix structure. The SEM technology does not allow for the graphite particles to be distinguished from the remainder of the matrix structure.

Thermogravimetric analysis

The flavour release profile of the flavour material produced according to the Preparations above may be analysed in a thermogravimetric analysis (TGA). The TGA test is carried out using a thermogravimetric machine coupled to a mass spectrometer, or similar TGA equipment. In the analysis the flavour material is heated from 25 degrees Celsius to 400 degrees Celsius in an inert nitrogen atmosphere with the temperature being increased at a rate of 15 degrees Celsius per minute and with an air flow of 60 ml per minute. As the temperature is increased, the release of menthol is assessed by detecting the menthol molecules by way of a specific ion representative of menthol.

Data collected carrying out TGA tests on flavour materials in accordance with the invention can be compared with data collected carrying out an equivalent TGA test on the flavourant formulation alone (e.g. pure menthol). One such comparison may provide some information about release mechanisms and dynamics, which may be help fine tune a flavourant release profile when the flavour material is incorporated in an aerosol-generating article.

When heated in the thermogravimetric analysis described, pure menthol was released unimodally between 50 degrees Celsius and 166 degrees Celsius, with a maximum around 138 degrees Celsius.

By contrast, when heated in the thermogravimetric analysis described, the flavour material produced according to Preparation E was found to provide a multi modal release of menthol. A first fraction (about 57 percent) of the menthol was released between 62 degrees Celsius and 239 degrees Celsius, with a local maximum at about 194 degrees Celsius. A second fraction (about 24 percent) of the menthol was released between 240 degrees Celsius and 305 degrees Celsius with a local maximum at about 252 degrees Celsius. A third fraction (about 19 percent) of the menthol was released between 305 degrees Celsius and 387 degrees Celsius with a local maximum at about 344 degrees Celsius.

Release of the first fraction of menthol with a maximum just below 200 degrees Celsius may suggest that some of the menthol formulation is solubilised or relatively weakly immobilised within the flavour material. On the other hand, release of the second fraction of menthol with a maximum around 250 degrees Celsius - a temperature associated with gellan gum thermal degradation - may support the hypothesis that a significant portion of the menthol formulation is trapped within the matrix structure, and has some stronger interaction with the gellan gum in the matrix structure. Release of the third fraction of menthol at even higher temperatures may suggest that the menthol formulation interacts in a different manner with the guar in the matrix structure.

The same TGA test was carried out on a flavour material prepared in accordance with Preparation D. This flavour material was found to provide a bimodal release of menthol. A first, small fraction (about 9 percent) of the menthol was released between about 68 degrees Celsius and about 148 degrees Celsius, with a local maximum around 125 degrees Celsius. A second, much more significant fraction (about 91 percent) of the menthol was released between 230 degrees Celsius and 245 degrees Celsius, with a local maximum at around 242 degrees Celsius. Release of the first fraction of menthol around 130 degrees Celsius may suggest that a small portion of the menthol formulation contained in the flavour material is not immobilised. On the other hand, the greater part of the menthol formulation contained in the flavour material being released at higher temperatures appears to suggest a stronger interaction with the gellan gum, which results in an effective immobilisation.

A comparison between the menthol release profiles of flavour materials prepared according to Preparations E and D demonstrates that adjusting the composition of the polysaccharide matrix - for example, using gellan gum alone or in combination with another polysaccharide - may help fine tune flavour delivery when the flavour material is incorporated in an aerosol-generating article. In particular, it may be possible to control at what temperature flavour release is initiated and around what temperature flavour release is maximised. Additionally, flavour materials which, like the ones prepared according to Preparations E and D, have different flavour release profiles with local maxima at different temperatures, may be combined in a single aerosol-generating articles to provide an even broader range of flavour delivery options to the consumer.

The same TGA test was carried out on a flavour material prepared in accordance with Comparative Preparation B, which differs from the flavour material prepared according to Preparation E only in that the carrier sheet of homogenised tobacco material does not include the graphite particles. Like the flavour material prepared according to Preparation E, when heated in the thermogravimetric analysis described, the flavour material produced according to Comparative Preparation B was found to provide a multi modal release of menthol. A first fraction (about 41 percent) of the menthol was released in the lower temperature range, then a second fraction (about 34 percent) and a third fraction (about 25 percent) of the menthol were released in the higher temperature intervals.

A comparison between the menthol release profile of Preparation E and Comparative Preparation B suggests that the inclusion of the carbon particles in the flavour material tends to enhance the thermal release of menthol at lower temperatures. In particular, a shift of about 5 degrees Celsius towards lower temperatures was observed, the local maximum associated with release of the first fraction of menthol being observed at about 199 degrees Celsius for the flavour material produced in accordance with Comparative Preparation B.

Additional tests carried out under isothermal conditions have confirmed that, especially at lower temperatures, the flavour material produced in accordance with Preparation E releases significantly more menthol than the flavour delivery produced in accordance with Comparative Preparation B. At 150 degrees Celsius, the flavour material produced in accordance with Preparation E released about 1.73 times as much menthol as the flavour delivery produced in accordance with Comparative Preparation B. At 180 degrees Celsius, the flavour material produced in accordance with Preparation E released about 1 .5 times as much menthol as the flavour delivery produced in accordance with Comparative Preparation B. This appears to confirm that supply of heat is made more effective by the presence of the carbon particles, presumably as they enhance heat transfer by conduction and facilitate a more homogenous temperature distribution throughout the flavour material. As a consequence, a greater portion of the menthol is brought more quickly to a condition wherein it is released from the flavour material.

The same TGA test described above was carried out on a flavour material prepared in accordance with Comparative Preparation A, which differs from the flavour material prepared according to Preparation D only in that no graphite particles are included in the favour delivery material. Like the flavour material prepared according to Preparation D, when heated in the thermogravimetric analysis described, the flavour material produced according to Comparative Preparation A was found to provide a bimodal release of menthol.

The menthol release profile of Preparation D was compared with the menthol release profile of Comparative Preparation A by plotting the cumulative amount of menthol released by each flavour material side by side. The results of this comparison suggest that the inclusion of the carbon particles in the flavour material tends to enhance the thermal release of menthol. In particular, a shift of about 5 degrees Celsius or more towards lower temperatures for the flavour material produced according to Preparation D was observed. For example, 40 percent of the menthol contained in the flavour material produced according to Preparation D had been released when the flavour material reached 240 degrees Celsius, whereas the flavour material produced according to Comparative Preparation A only reached the same 40 percent release threshold at 245 degrees Celsius. Similarly, 60 percent of the menthol contained in the flavour material produced according to Preparation D had been released when the flavour material reached 243 degrees Celsius, whereas the flavour material produced according to Comparative Preparation A only reached the same 40 percent release threshold at about 249 degrees Celsius.

Thermal stability

The thermal stability under stress conditions of a flavour material in accordance with the present invention may be assessed by ageing the flavour material at a constant temperature and monitoring its weight loss over time. To this purpose samples of the flavour material cut into regular and homogenously sized pieces are weighed and distributed in a series of Schott glass open bottles. The samples are aged in a laboratory oven set at 50 degrees Celsius for a period of two weeks. For the flavour material produced in accordance with Preparation E, a weight loss of about 24 percent was measured at the end of the test. It is hypothesised that such weight loss value accounts not only for some migration of flavour species, but also for losses of humidity and glycerol, and so it is considered to be satisfactory. Puff-by-puff flavour delivery assessment

Flavour delivery of an aerosol-generating article incorporating a flavour material in accordance with the present invention may be assessed by heating the aerosol-generating article in a commercially available, compatible heating device and measuring the menthol delivered at the mouth end of the article with every puff. In more detail, the products released with each puff from the aerosol-generating article heated by the heating device may be analysed using Proton Transfer Mass Spectrometry (PTR-MS).

The puff-by-puff menthol delivery of an aerosol-generating article produced in accordance with Preparation G was compared with the puff-by-puff delivery release of an aerosol-generating article produced in accordance with Comparative Preparation C under the same test conditions. It was observed that with each puff a larger amount of menthol was released from the Preparation G article than from the Comparative Preparation C article. Further, while the amount of menthol released with the second puff and each consecutive puff from the Comparative Preparation C article fluctuated between about 0.04 mg/puff and 0.09 mg/puff, the amount of menthols released with the second puff and each consecutive puff from the Preparation G article was more remained more consistently between about 0.09 mg/puff and about 0.11 mg/puff.

For the purpose of the present description and of the appended claims, except where otherwise indicated, all numbers expressing amounts, quantities, percentages, and so forth, are to be understood as being modified in all instances by the term "about". Also, all ranges include the maximum and minimum points disclosed and include any intermediate ranges therein, which may or may not be specifically enumerated herein. In this context, therefore, a number A is understood as A ± 5% of A. Within this context, a number A may be considered to include numerical values that are within general standard error for the measurement of the property that the number A modifies. The number A, in some instances as used in the appended claims, may deviate by the percentages enumerated above provided that the amount by which A deviates does not materially affect the basic and novel characteristic(s) of the claimed invention. Also, all ranges include the maximum and minimum points disclosed and include any intermediate ranges therein, which may or may not be specifically enumerated herein.

Claims

1. A flavour material for use in an aerosol-generating article, wherein the flavourant is releasable from the flavour material upon heating the flavour material; the flavour material comprising: a polysaccharide matrix structure; and a flavourant formulation dispersed within the polysaccharide matrix structure, wherein the flavourant formulation is at least partly trapped within the polysaccharide matrix structure and releasable from the polysaccharide matrix structure upon heating of the flavour material; and greater than 0.1 weight percent carbon particles, the carbon particles having a volume mean particle size of greater than 10 micrometres.

2. A flavour material according to claim 1 further comprising a carrier sheet material, wherein the polysaccharide matrix structure and the flavourant formulation are supported by the carrier sheet material, and wherein the carrier sheet material comprises the carbon particles.

3. A flavour material according to claim 2, wherein the carrier sheet material is one of a sheet of homogenised tobacco material, a sheet of non-tobacco aerosol-generating material, a paper wrapper material.

4. A flavour delivery according to any one of the preceding claims, wherein the polysaccharide matrix structure comprises gellan gum and an emulsifier.

5. A flavour material according to claim 4, wherein the polysaccharide matrix structure comprises gellan gum as the sole polysaccharide or gellan gum in combination with at least a further polysaccharide selected from the group consisting of guar, tamarind gum, sodium alginate, xanthan gum, sodium carboxymethyl cellulose, and hydroxypropyl methyl cellulose; wherein the gellan gum preferably makes up from 5 percent by weight to 99.9 percent by weight of the flavour material on a dry weight basis.

6. A flavour material according to any one of the preceding claims, further comprising a polyol having the formula C_nH2n+2O_n, wherein the polyol is selected from the group consisting of glycerol, sorbitol, xylitol, mannitol, and erythritol or wherein the polyol makes up from 0.01 percent by weight to 20 percent by weight of the flavour material on a dry weight basis or both.

7. A flavour material according to any one of the preceding claims, wherein the carbon particles consist of one or more of: graphite particles, expanded graphite particles and graphene particles.

8. A flavour material according to any one of the preceding claims, wherein the carbon particles have a volume mean particle size from 30 micrometres to 150 micrometres.

9. A flavour material according to any one of the preceding claims, wherein the carbon particles have a particle size distribution with a D90 particle size and a D10 particles size, wherein the D90 particle size is no more than 25 or 15 times the D10 particle size.

10. A flavour material according to any one of the preceding claims, wherein the carbon particles make up from 0.01 percent by weight to 10 percent by weight of the flavour material on a dry weight basis.

11. A flavour material according to any one of the preceding claims further comprising fibres, preferably the fibres making up from 0.01 percent by weight to 10 percent by weight of the flavour material on a dry weight basis.

12. An aerosol-generating article comprising a flavour material, wherein the flavourant is releasable from the flavour material upon heating the flavour-delivery material; the flavour material comprising: a polysaccharide matrix structure; and a flavourant formulation dispersed within the polysaccharide matrix structure, wherein the flavourant formulation is trapped within the polysaccharide matrix structure and releasable from the polysaccharide matrix structure upon heating of the flavour material; and wherein the flavour material comprises greater than 0.1 weight percent carbon particles, the carbon particles having a volume mean particle size of greater than 10 micrometres.

13. An aerosol-generating article according to claim 12, wherein the flavour material further comprises a carrier sheet material, wherein the polysaccharide matrix structure and the flavourant formulation are supported by the carrier sheet material, and wherein the carrier sheet material comprises the carbon particles.

14. An aerosol-generating article according to claim 12 or 13 comprising: a rod of aerosolgenerating substrate; a downstream section provided downstream of the rod of aerosolgenerating substrate and extending to a mouth end of the aerosol-generating article; optionally an upstream section provided downstream of the rod of aerosol-generating substrate and extending to a distal end of the aerosol-generating article; wherein the flavour material is provided in at least one of the rod of aerosol-generating substrate; the downstream section; and the optional upstream section.

15. An aerosol-generating article according to claim 13, wherein the carrier sheet material is a sheet of homogenised tobacco material; wherein the aerosol-generating article comprises a rod of aerosol-generating substrate; a downstream section provided downstream of the rod of aerosol-generating substrate and extending to a mouth end of the aerosol-generating article; optionally an upstream section provided downstream of the rod of aerosol-generating substrate and extending to a distal end of the aerosol-generating article; wherein the flavour material is provided in the rod of aerosol-generating substrate.