in general , a confectionery product composition according to the present invention typically comprises a water - soluble bulk portion , a water - insoluble chewable polymer system portion , and flavoring agents . the water - soluble portion dissipates with a portion of the flavoring agent over a period of time during chewing . the polymer system portion is retained in the mouth throughout the chew . to a certain degree , the polymer system fully corresponds to a conventional gum base , both with respect to manufacturing , ingredients and to a certain degree release . the main difference is found in composition and textural properties of the polymer system . the polymer system is the masticatory substance of the confectionery product according to the invention , which imparts the chew characteristics to the final product . the polymer system typically defines the release profile of flavours , and sweeteners and plays a significant role in the final product . the insoluble portion of the confectionery product typically may contain any combination of pvac &# 39 ; s , plasticizers , waxes , softeners , fillers and other optional ingredients such as colorants and antioxidants . further elastomers or high molecular weight pvac &# 39 ; s may be applied in the polymer system to a very limited degree without compromising the desired toffee - like texture . the composition of the polymer system formulations can vary substantially depending on the particular product to be prepared and on the desired masticatory and other sensory characteristics of the final product . the amount of elastomers and in particular high molecular weight elastomers should be kept very low or preferably be completely omitted according to the invention . according to a preferred embodiment the polymer system and the final confectionery product should be substantially free of elastomer . however , when used , e . g . for the purpose of making the polymer system robust elastomers may provide the rubbery , cohesive nature to the confectionery product which varies depending on this ingredient &# 39 ; s chemical structure and how it may be compounded with other ingredients . elastomers suitable for use in the polymer system of the present invention may include natural or synthetic types . the elastomer may be any water - insoluable polymer known in the art , and includes those polymers utilized for chewing gum and bubble gum listed in food and drug administration , cfr , title 21 , section 172 , 615 , as “ masticatory substances of natural vegetable origin ” and “ masticatory substances , synthetic ”. useful natural elastomers include natural rubber such as smoked or liquid latex and guayule , natural gums such as jelutong , lechi caspi , perillo , sorva , massaranduba balata , massaranduba chocolate , nispero , rosidinha , chicle , gutta percha , gutta kataiu , niger gutta , tunu , chilte , chiquibul , gutta hang kang . useful synthetic elastomers include high molecular weight elastomers such as butadiene - styrene copolymers , polyisobutadiene and isobutylene - isoprene copolymers , low molecular weight elastomers such as polybutene , polybutadiene and polyisobutylene , vinyl polymeric elastomers such as polyvinyl acetate , polyethylene , vinyl copolymeric elastomers such as vinyl acetate / vinyl laurate , vinyl acetate / vinyl stearate , ethylene / vinyl acetate , polyvinyl alcohol or mixtures thereof butadiene - styrene type elastomers , or sbr as they may be called , typically are copolymers of from about 20 : 80 to 60 : 40 styrene : butadiene monomers . the ratio of these monomers affects the elasticity of the sbr as evaluated by mooney viscosity . as the styrene : butadiene ratio decreases , the mooney viscosity decreases . the structure of sbr typically consists of straight chain 1 , 3 - butadiene copolymerized with phenylethylene ( styrene ) and provides the non - linear molecular nature of these elastomers . the average molecular weight of sbr is & lt ; 600 , 000 g / mole . isobutylene - isoprene type elastomers , or butyl as they may be called , have molar percent levels of isoprene ranging from 0 . 2 to 4 . 0 . similar to sbr , as the isoprene : isobutylene ratio decreases , so does the elasticity , measured by mooney viscosity . the structure of butyl rubber typically consists of branched 2 - methyl - 1 , 3 - butadiene ( isoprene ) copolymerized with branched 2 - methylpropene ( isobutylene ), and , as with sbr , this type of structure is non - linear in nature . the average molecular weight of sbr is in the range from 150 , 000 g / mole to 1 , 000 , 000 g / mole . polyisobutylene , or pm as they may be called , type elastomers are polymers of 2 - methylpropene and , as with sbr and butyl , are non - linear in nature . the low molecular weight elastomers provide soft chew characteristics to the polymer system and still provide the elastic qualities as do the other elastomers . average molecular weights may range from about 30 , 000 to 120 , 000 g / mole and the penetration may range from about 4 millimeters to 20 millimeters . the higher the penetration , the softer the pm . similar to the sbr and butyl , the high molecular weight elastomers provide elasticity the gum . average molecular weight may range from 120 , 000 to 1 , 000 , 000 g / mole . again , if used at all , the molecular weight should be relatively low . the main components of the polymer system according to the invention is vinyl polymer ( s ). vinyl polymeric and copolymeric type elastomers provide tack resistance , vary the chew characteristics of the product made from these bases having vinyl polymers and offer hydrophilic properties beneficial to sensory perception of the final confectionery products . for vinyl copolymeric types , the amount of vinyl laurate , vinyl stearate , or ethylene present in the vinyl laurate / vinyl acetate ( vlna ), vinyl stearate / vinyl acetate ( vsna ), or ethylene / vinyl acetate ( eva ) copolymers respectively typically ranges from about 10 to about 60 percent by weight of the copolymer . average molecular weights of these polymers may range from about 2 , 000 g / mole to about 100 , 000 g / mole . the vinyl polymers as polyvinyl alcohol and polyvinyl acetate having an average molecular weight from about 8 , 000 g / mole to about 65 , 000 g / mole . elastomer plasticizers vary the firmness of the polymer system . their specificity on polymer inter - molecular chain breaking ( plasticizing ) along with their varying softening points cause varying degrees of finished confectionery product firmness and compatibility when used in the polymer system . particular useful plasticizers according to the present invention are triacetin , acetylated mono - and di - and triglycerides of short chain fatty acids , acetylated mono - and di - and triglycerides of medium chain fatty acids , acetylated monoglycerides of long chain fatty acids , methyl ester of rosin , low molecular weight pvac . the plasticizers used may be of one type or of combinations of more than one type . typically , the ratios of one to the other are dependent on each respective softening point , the effect on flavor release , and the respective degree of tack they cause to the gum . petroleum waxes aid in the curing of the finished confectionery product made from the polymer system as well as improve shelf - life and texture . wax crystal size influence the release of flavor . those waxes high in iso - alkanes have a smaller crystal size than those waxes high in normal - alkanes , especially those with normal - alkanes of carbon numbers less than 30 . the smaller crystal size allows slower release of flavor since there is more hindrance of the flavor &# 39 ; s escape from this wax versus a wax having larger crystal sizes . the compatability of polymer systems made using normal - alkanic waxes is less when compared to polymer systems made with iso - alkanic waxes . petroleum wax ( refined paraffin and microcrystalline wax ) and paraffin wax is composed of mainly straight - chained normal - alkanes and branched iso - alkanes . the ratio of normal - alkanes to iso - alkanes varies . the normal - alkanic waxes typically have carbon chain lengths & gt ; c - 18 but the lengths are not predominantly longer than c - 30 . the branched and ring structures are located near the end of the chain for those waxes that are predominantly normal - alkanic . the viscosity of normal - alkanic waxes is & lt ; 10 mm2 / s ( at 100 . degree . c .) and the combined number average molecular weight is & lt ; 600 g / mole . the iso - alkanic waxes typically have carbon lengths that are predominantly greater than c - 30 . the branched chains and ring structures are located randomly along the carbon chain in those waxes that are predominantly iso - alkanic . the viscosity of iso - alkanic waxes is greater than 10 mm2 / s ( at 100 . degree . c .) and the combined number average molekylar weight is & gt ; 600 g / mole . synthetic waxes are produced by means atypical of petroleum wax production and thus are not considered petroleum wax . the synthetic waxes may include waxes containing branched alkanes and copolymerized with monomers such as but not limited to propylene and polyethylene and fischer tropsch type waxes . polyethylene wax is a synthetic wax containing alkane units of varying lengths having attached thereto ethylene monomers . the natural waxes may include rice bran wax , bees &# 39 ; wax , carnauba wax or candelilla wax . the selection of softeners has an influence on the softness of the base . softeners modify the texture , cause the hydrophobic and hydrophilic components of the base to be miscible , and may further plasticize the synthetic polymers of the polymer system . the emulsifiers , which belong to the group of softeners , provide the polymer system with water - binding properties , which confer to the polymer system a pleasant smooth surface and reduce its adhesive properties . softeners suitable for use in the polymer system include triglycerides of non - hydrogenated , partially hydrogenated and fully hydrogenated vegetable oils and tallow , cocoa butter and degreased cocoa powder and in addition to these the emulsifiers . the group of triglycerides include cottonseed , palm , palm kernel , coconut , safflower , rapeseed , sunflower , tallow , soybean , cocoa butter , medium chained triglycerides and the like . the caproic , caprylic , capric , myristic , lauric and palmitic fatty acids of the triglycerides tend to plasticize the synthetic elastomers more than triglycerides containing predominantly stearic fatty acid . to the group of emulsifiers belong the monoglycerides , diglycerides , acetylated mono and diglycerides , distilled mono - and diglycerides , glycerol monostearate , propylene glycol monostearate , na -, k -, mg - and ca - stearates , glycerol triacetate , fatty acid monoglycerides ( e . g . stearic , palmitic , oleic and linoleic acids ), lactic acid esters and acetic acid esters of mono - and diglycerides , sugar esters of edible fatty acids also referred to as sucrose polyesters including those disclosed in wo 00 / 25598 , lecithin and hydroxylated lecithin , most of these may contain triglyceride levels less than 2 percent by weight from their manufacturing processing . the softeners including the emulsifiers may be used alone or at least two or more in combination . generally , according to the invention , the amount of fillers should be kept low in the final confectionery product and preferably completely avoided in order to maintain the desired toffee - like textural properties . fillers used in polymer system modify the texture of the polymer system and aid in processing . particle size has an effect on cohesiveness , density and processing characteristics of the polymer system and its compounding . the smaller the particle size , the more dense and cohesive the final polymer system . also , by selecting fillers based on their particle size distribution , initial mass compounding may be varied , thus allowing alteration of the compounding characteristics of the initial mass during polymer system processing and ultimately the final chew characteristics of gums made from these polymer systems . fillers suitable for use in the polymer system include magnesium and calcium carbonate , ground limestone and silicate types such as magnesium and aluminum silicate , kaolin and clay , aluminium oxide , silicium oxide , talc , as well as titanium oxide , mono -, di - and tricalcium phosphate , sodium sulphate , cellulose polymers such as ethyl , methyl and wood or mixtures thereof . talc filler may be used in the polymer system and confectionery product of the present invention that may come in contact with or employ acid flavors or provide an acidic environment needed to prevent degradation of an artificial sweetener by reacting with calcium carbonate type fillers . mean particle size for calcium carbonate and talc fillers typically range from about 0 . 1 micron to about 15 microns . the fillers may also include natural organic fibres such as fruit vegetable fibres , grain , rice , cellulose and combinations thereof . function and list of other optional ingredients such as antioxidants , colorants and flavorants antioxidants prolong shelf - life and storage of polymer system , finished confectionery product or their respective components including fats and flavor oils . antioxidants suitable for use in polymer system include butylated hydroxyanisole . ( bha ), butylated hydroxytoluene ( bht ), betacarotenes , tocopherols , acidulants such as vitamin c , propyl gallate , other synthetic and natural types or mixtures thereof . flavorants and colorants impart characteristics or remove or mask undesired characteristics . colorants may typically include fd & amp ; c type lakes , plant extracts , fruit and vegetable extracts and titanium dioxide flavorants may typically include cocoa powder , heat - modified amino acids and other vegetable extracts . polymer systems are typically prepared by adding an amount of the high molecular weight pvac , low molecular weight pvac and plasticizer to a heated ( 10 . degree . c .- 120 . degree . c .) sigma blade mixer with a front to rear speed ratio of from about 1 . 2 : 1 to about 2 : 1 , the higher ratio typically being used for polymer system which requires more rigorous compounding of its medium / high molecular weight polymers . the initial amounts of ingredients comprising the initial mass may be determined by the working capacity of the mixing kettle in order to attain a proper consistency and by the degree of compounding desired to break down the although slight amount of medium / high molecular weight polymers and increase chain branching . the longer the time of compounding , the use of lower molecular weight or softening point polymer system ingredients , the lower the viscosity and firmness of the final polymer system . compounding typically begins to be effective once the ingredients have massed together . anywhere from 15 minutes to 90 minutes may be the length of compounding time . preferably , the time of compounding is from 20 minutes to about 60 minutes . after the initial ingredients have massed homogeneously and compounded for the time desired , the balance of the polymer system ingredients are added in a sequential manner until a completely homogeneous molten mass is attained . typically , any remainder of the polymer system components are added within 60 minutes after the initial compounding time . typical polymer system processing times may vary from about 0 . 5 to about 4 hours , preferably from about 0 . 5 to 1 . 5 hours , depending on the formulation . the final mass temperature when dumped may be between 70 . degree . c . and 130 . degree . c . and preferably between 100 . degree . c . and 120 . degree . c . the completed molten mass is emptied from the mixing kettle into coated or lined pans , extruded or cast into any desirable shape and allowed to cool and solidify . those skilled in the art will recognize that many variations of the above - described procedure may be followed . a polymer system according to an embodiment of the invention is prepared by a method corresponding to the method typically applied for gum base mixing . the applied method involved mixing in a z - blade mixer . the polymer system comprises the following components : it should be noted that extruding of the polymer system may advantageously be applied within the scope of the invention . a confectionery product is mixed on the basis of the polymer system of example 1 . the mixing is performed by a method corresponding to the method typically applied for mixing of gum base together with the hydrophilic chewing gum components . the confectionery product comprised : confectionery products having the shape of an ellipsoid and having a weight of approximately 1 . 5 gram were formed of the resulting above - described mix . the resulting confectionery product appeared as a chewing gum but the textural properties were comparable to the texture of toffee . the release of sweetener and flavor were impressing and in good harmony with the toffee - like product . a confectionery product is mixed on the basis of the polymer system of example 1 . the mixing is performed by a method corresponding to method typically applied for mixing of gum base together with the hydrophilic chewing gum components . the confectionery product comprised : confectionery products having the shape of an ellipsoid and having a weight of approximately 1 . 5 gram were formed of the resulting above - described mix . the resulting confectionery product appeared as a chewing gum but the textural properties were comparable to the texture of toffee . the release of sweetener and flavor were impressing and in good harmony with the toffee - like product . it was furthermore observed that the confectionery product required a little more plasticizer compared to example 2 . this is due to the fact that the lemon flavor and the associated acid tends to act as a significant supplementary plasticizer to the specifically applied triacetin . a confectionery product is mixed on the basis of the polymer system of example 1 . the mixing is performed by a method corresponding to method typically applied for mixing of gum base together with the hydrophilic chewing gum components . the confectionery product comprised : confectionery products having the shape of an ellipsoid and having a weight o f approximately 1 . 5 gram were formed of the resulting above - described mix . the resulting confectionery product appeared as a chewing gum but the textural properties were comparable to the texture of toffee . the release of sweetener and flavor were impressing and in good harmony with the toffee - like product . again , it was found advantageous to apply a little more plasticizer compared to example 2 for the same reasons as in example 3 . a confectionery product is mixed on the basis of the polymer system of example 1 . the mixing is performed by a method corresponding to method typically applied for mixing of gum base together with the hydrophilic chewing gum components . the confectionery product comprised : confectionery products having the shape of an ellipsoid and having a weight of approximately 1 . 5 gram were formed of the resulting above - described mix . the resulting confectionery product appeared as a chewing gum but the textural properties were comparable to the texture of toffee . the release of sweetener and flavor were impressing and in good harmony with the toffee - like product . again , it was found advantageous to apply a little more plasticizer compared to example 2 for the same reasons as in example 3 . a confectionery product is mixed on the basis of the polymer system of example 1 . the mixing is performed by a method corresponding to method typically applied for mixing of gum base together with the hydrophilic chewing gum components . the confectionery product comprised : confectionery products having the shape of an ellipsoid and having a weight of approximately 1 . 5 gram were formed of the resulting above - described mix . the resulting confectionery product appeared as a chewing gum but the textural properties were comparable to the texture of toffee . the release of sweetener and flavor were impressing and in good harmony with the toffee - like product . the confectionery products of example 2 - 6 were coated by a hard coating comprising xylitol . the confectionery products of example 4 and 5 were coated by a soft coating . the specifically applied soft coating is chocolate . it is noted that other soft coat materials may also be applied within the scope of the invention . in an advantageous embodiment of the invention , chocolate may be applied as a coating , a product module or center filling as the polymer system has proved robust to such quite aggressive plasticizing component , which typically tends to dissolve conventional chewing gum formulations . by evaluation it was noted that the desired toffee - character may be effectively supported and / or improved by the combination of toffee - like confectionery product according to the invention and chocolate . further layers of coatings may also be applied within the scope of the invention . it is noted that the confectionery product may be manufactured in several different ways within the scope of the invention , including well - known two processes or e . g . by extruding . it is moreover noted that the shape , size and weight may vary significantly according to the current desired properties of the product . various shapes may thus e . g . include round , ellipsoid , square , multimodular , ring - formed , etc . one particular interesting variant is a center - filled confectionery structure . the polymer system applied according to the invention has thus proved quite resistant to e . g . fat - based ingredients such as chocolate both prior to or subsequent to the chewing .
the invention relates to a chewable tablet including a polymer system , tobacco powder , flavor and sweetener , at least about 70 % by weight of the polymer system being polyvinyl acetate and less than 10 % by weight of the polymer system being polymer having a molecular weight of greater than about 50000 g / mol .