the present exemplary embodiments relate to a toner for use in the printing and recording of images by electrophotographic and electrostatic processes . more particularly , the embodiments relate to a suspension polymerization process for producing wax containing toner . in various embodiments , there are provided toners and processes for the production and use thereof wherein the toner composition includes as a colorant an aqueous pigment concentrate dispersion . in other various embodiments , the wax used may be conventional waxes or aqueous dispersed waxes . the toner composition includes a binder resin that may be selected from any of a number of known resins . exemplary resin components include vinyl resins , including homopolymers or copolymers of two or more vinyl monomers ; and polymeric esterification products of a dicarboxylic acid and a diol comprising diphenol . these resins are polymerized during the present toner production process from suitable monomer components . exemplary vinyl monomers include styrene , p - chlorostyrene , unsaturated mono - olefins such as ethylene , propylene , buytlene , isobutylene , and the like ; saturated mono - olefins such as vinyl acetate , vinyl propionate and vinyl butyrate and the like ; vinyl esters such as esters of monocarboxylic acids , including methyl acrylate , ethyl acrylate , n - butylacrylate , isobutyl acrylate , dodecyl acrylate , n - octyl acrylate , phenyl acrylate , methyl methacrylate , ethyl methacrylate , and butyl methacrylate and the like ; acrylonitrile , methacrylonitrile , acrylamide , mixtures thereof ; and the like . examples of specific thermoplastic toner resins include styrene butadiene copolymers with a styrene content of from about 70 to about 95 weight percent . additionally , cross linked resins , including polymers , copolymers , and homopolymers of the aforementioned styrene polymers may be selected . also , waxes with a molecular weight of from about 300 to about 7 , 000 , such as polyethylene , polypropylene , paraffin waxes , polyamide waxes and various natural waxes can be included in or on the toner compositions as internal lubricants or fuser roll release agents . further , reactive extruded polyesters can be selected as the toner resin . the resin or resins are included in the toner composition disclosed herein in an amount of from about 60 % to about 90 % of the toner composition . preferably the resin component is included as from about 60 % to about 80 % of the total toner composition . in one embodiment , the resin particles may have a tg of from about 50 ° c . to about 75 ° c . and an acid number below 30 . the weight average molecular weight for the resin component may be between about 10 , 000 and about 100 , 000 . one or more pigments are included in the toner compositions of the present embodiments . these pigments may be in the form of conventional dry or wet - cake pigments or aqueous pigment dispersions . particularly well suited to the practice of the present embodiments are aqueous pigment concentrate dispersions , generally intended for use in liquid ink compositions or paints . suitable dispersions may contain an aqueous medium into which the desired pigment has been dispersed . the dispersion may further include a surfactant component , or a polymeric pigment stabilizer , such as a water soluble acrylic copolymer . these additional components may be added to stabilize the pigment particles and to improve dispersibility of the pigment during processing . other possible components of the dispersion include compounds such as propylene glycol , which may be included to enhance the viscosity of the pigment dispersion and to aid in pigment wetting . suitable aqueous pigment concentrate dispersions in accord with the foregoing include those available commercially from sun chemical , such as aquatone ® dispersions , flexiverse dispersions , sunsperse 6000 dispersions and moisture tone ® dispersions , as well as the dispersions available commercially from clariant , such as the hostafine dispersion products , among others . these dispersions generally include about 30 wt % solids to about 50 wt % solids pigment , and are included as from about 5 wt % to about 30 wt % of the toner composition . alternately , the aqueous pigment dispersion can be dried prior to its use in the toner production process . toners prepared using aqueous pigment dispersions may exhibit superior pigment dispersion compared to those prepared using dry or wet - cake pigments . examples of suitable dry pigments include carbon black like regal 330 ; magnetites , such as mobay magnetites m08029 , m08060 ; columbian magnetites ; mapico blacks and surface treated magnetites ; pfizer magnetites cb4799 , cb5300 , cb5600 , mcx6369 ; bayer magnetites , bayferrox 8600 , 8610 ; northern pigments magnetites , np - 604 , np - 608 ; magnox magnetites tmb - 100 , or tmb - 104 ; and the like . as color pigments , there can be selected cyan , magenta , yellow , red , green , brown , or blue pigments or mixtures thereof . specific examples of pigments include phthalocyanine heliogen blue l6900 , d6840 , d7080 , d7020 , pylam oil blue , pylam oil yellow , pigment blue 1 available from paul uhlich & amp ; company , inc ., pigment violet 1 , pigment red 48 , lemon chrome yellow dcc 1026 , e . d . toluidine red and bon red c available from dominion color corporation , ltd ., toronto , ontario , novaperm yellow fgl , hostaperm pink e from hoechst , cinquasia magenta available from e . i . dupont de nemours & amp ; company , and the like . generally , colored pigments that can be selected are cyan , magenta , or yellow pigments , and mixtures thereof . examples of magenta materials that may be selected as pigments include , for example , 2 , 9 - dimethyl - substituted quinacridone and anthraquinone dye identified in the color index as ci 60710 , ci dispersed red 15 , diazo dye identified in the color index as ci 26050 , ci solvent red 19 , and the like . illustrative examples of cyan materials that may be used as pigments include copper tetra ( octadecyl sulfonamido ) phthalocyanine , x - copper phthalocyanine pigment listed in the color index as ci 74160 , ci pigment blue , and anthrathrene blue , identified in the color index as ci 69810 , special blue x - 2137 , and the like ; while illustrative examples of yellow pigments that may be selected are diarylide yellow 3 , 3 - dichlorobenzidene acetoacetanilides , a monoazo pigment identified in the color index as ci 12700 , ci solvent yellow 16 , a nitrophenyl amine sulfonamide identified in the color index as foron yellow se / gln , ci dispersed yellow 33 , 2 , 5 - dimethoxy - 4 - sulfonanilide phenylazo - 4 ′- chloro - 2 , 5 - dimethoxy acetoacetanilide , and permanent yellow fgl . colored magnetites , such as mixtures of mapico black , and cyan components may also be selected as pigments with the process of the present invention . these pigments may be used as dry powder or in the wet cake form . as discussed above , the pigment should be included in the toner composition in an amount of from about 5 wt % to about 15 wt % of the toner composition [ the pigment is included up to 15 % which can be derived from 30 % of pigment dispersion . in addition to the pigment , the toner composition may also include other colorants which may be any of the known pigments suitable for use in toner and developer compositions . though pigments are generally a more preferred colorant because of their light fast properties and the water content , some dye colorants may also be used . these additional colorants may be added to achieve special colors and / or to increase color density . specifically , the additional colorant should be suitable for use with the recited or suggested resin component , and also compatible with the remaining components of the toner composition . charge control agents may be added to the toner for the purpose of making the toner product either more electronegative or more electropositive . whether the toner needs to be made more electronegative or more electropositive is determined by several factors . some of these include the electronegativity of the remaining toner components as combined , i . e ., different colorants and resins may impart different charge characteristics to the toner composition . also , the carrier , if one will be used , must be considered , as many carrier materials impart a charge to the toner composition . further , the machine in which the toner is used may impart some charge to the toner , as will the operation thereof . the purpose of the charge control agent component of the toner is to stabilize the toner with respect to electrical charge and thus avoid problems of print quality , color balance , and fogging , which are associated with too much or too little charge on the toner particles . charge control agents may be selected from quaternary salts , metal and non - metal dyes , chromium , cobalt and zinc complexes , nigrosines , positive and negative colorless polymers , metal chelates , and quaternary amines , depending on the particular requirements of the complete toner composition . examples of suitable commercially available charge control agents include the following : s - 34 , s - 40 , e - 82 , e - 81 , e - 84 , e - 87 , e - 88 and e - 89 , all manufactured by orient chemicals , and trh , t - 77 , t - 95 , and tns - 2 , all manufactured by hodogaya chemical co . charge control agents offered by basf , hoechst / clariant , zeneca and others may also be found to be suitable . these and other similar commercially available charge control agents may be selected . generally , the charge control agent is included in the toner composition as up to about 10 % thereof , based on the weight of the toner . the wax component to be used in the toner is preferably composed of at least one wax selected from the group consisting of polyolefin waxes , carnauba wax , candelilla wax , hydrogenated jojoba oil , rice wax , hydrogenated lanolin , meadowfoam oil , and derivatives thereof . preferably , the polyolefin waxes include low molecular weight waxes such as polypropylenes and polyethylenes , such as epolene n - 15 commercially available from eastman chemical products , inc ., and similar waxes . the commercially available polyethylenes may have a molecular weight of from about 300 g / mol to about 3000 g / mol , while the commercially available polypropylenes utilized for the toner compositions of the present invention may have a molecular weight of from about 4 , 000 g / mol to about 7 , 000 g / mol . low molecular weight wax materials are present in the toner composition of the present invention in various amounts , however , generally these waxes are present in the toner composition in an amount of from about 0 wt % to about 15 wt %, and preferably in an amount of from about 5 wt % to about 10 wt %, based on the weight of the toner . as with the case of the pigment component , the wax component added to the toner composition may be in the form of a conventional wax or as an aqueous wax dispersion . particularly well suited to the practice of the present embodiments are aqueous wax dispersions . suitable dispersions may contain an aqueous medium into which the desired wax has been dispersed as colloidal wax particles . the dispersion may further include a particulate stabilizer component , or a polymeric wax stabilizer . these additional components may be added to stabilize the wax particles and to improve dispersibility of the wax during processing . other possible components of the dispersion include compounds such as propylene glycol , which may be included to enhance the viscosity of the wax dispersion and to aid in wax wetting . suitable aqueous wax dispersions may be made by dispersing a functionalized wax in an aqueous medium under shear and , optionally , with the application of heat . these dispersions generally include about 30 wt % solids to about 50 wt % solids wax . commercial aqueous wax dispersions include unithox ® series of ethoxylate molecules from baker petolite ®. the unithox ethoxylate molecules have both the hydrophilic alkane segments and hydrophobic ethylene oxide segments and are thus amphophilic and self - emulsifying . these properties are useful in helping to disperse a wide range of materials within the toner particles such pigments , resins , waxes , and charge control agents . plasticizers may also be included in the toner compositions . useful plasticizers include both very low viscosity plasticizers and polymeric plasticizers that are liquid at room temperature . these low viscosity plasticizers can be used alone or as part of a mixture of low viscosity plasticizers . typical examples of useful plasticizers include dimethylphthalate , dibutylphthalate , tributylphosphate , butylstearate , ethyleneglycolbutyletheracetate , diethyleneglycolethyletheracetate , and diethyleneglycolbutyletheracetate . the amount of plasticier included in the toner is preferably from about 0 wt % to about 5 wt %, based on the toner composition . the toner of the present invention may further include external additives employed for the purpose of enhancing flowability of the toner product . the additive used may be a single component additive or may be a specific combination of additives , the combined use of which produces a special performance effect of the toner product . additives may be selected from silicas , metal stearates , fluoropolymer powders , fine polymer powders , rare earth oxides , waxes , conductive particles , magnetite , carbon , and titanates , and other like compounds . post additive treatment agents , such as flowability enhancers of the type used in this toner product , result in deagglomeration of the toner particles in use , and enhanced stability during storage of the toner product . in selecting a flowability enhancing additive to be added to the toner product during a post - treatment step , it is important to consider these parameters : anti - caking ; flowability ; electrostatic charge ; stability ; coefficient of friction ; transfer efficiency ; photoreceptor release properties ; hydrophobicity ; storage stability ; and others . the indication of these characteristics generally requires inorganic compounds of fine particle size and high surface areas . these additives are often treated to render them hydrophobic in order to overcome the drawbacks associated with their conventionally hydrophillic nature . for example , as the post additive to be employed in production of a toner in keeping with the present invention there may be used a hydrophobic silica fine powder in combination with a hydrophobic titanium oxide powder . preferably , the titanium oxide powder is a silane treated powder . other suitable external additives , or post additives , may include but are not limited to the use of aluminum oxide ; zinc oxide ; cerium oxide ; strontium titanate ; iron oxide ; ferrite powder ; calcium carbonate ; copper oxide ; barium sulfate ; lithopone ; metal salts of fatty acids ; powdered fluoropolymers ; polytetrafluoroethylene ; polyethylene powder ; carbon black ; silicon carbide ; silicon nitride ; and powdered or fine particle polymers . various methods may be used to produce the present toner compositions . in one embodiment , the pigment of the appropriate color may be added to a high intensity mixer along with the remaining toner components , including resin , wax , charge control agent , additional pigment and plasticizer . when using a conventional wax , one proposed process involves ( 1 ) forming an organic dispersion of pigment , wax , vinyl monomer ( typically styrene and acrylics ), initiator , charge control agent ; ( 2 ) forming an aqueous phase of water and particulate stabilizer ; ( 3 ) dispersing the organic dispersion into the aqueous phase under high shear to give a suspension of organic droplets ; ( 4 ) subjecting the suspension to polymerization conditions to form toner particles ; ( 5 ) washing and drying the wet toner particles to give the final dried toner particles . when using an aqueous wax dispersion containing a functionalized wax , one proposed process involves ( 1 ) forming an organic dispersion of pigment , functionalized wax , conventional wax ( optional ), vinyl monomer ( typically styrene and acrylics ), initiator , charge control agent ; ( 2 ) forming an aqueous phase of water , colloidal wax particles and particulate stabilizers ( the aqueous wax dispersion ); ( 3 ) dispersing the organic dispersion into the aqueous phase under high shear to give a suspension of organic droplets ; ( 4 ) subjecting the suspension to polymerization conditions to form toner particles ; ( 5 ) washing and drying the wet toner particles to give the final dried toner particles . in the first described process using a conventional wax additive , the organic dispersion is created by mixing together the pigment ( which may be in the form of a dried pigment dispersion from an aqueous pigment dispersion concentrate or as a conventional particulate or cake form ), the wax , the monomer , initiator , and charge control agent ( if used ). an aqueous phase of particulate stabilizer mixed in water is then added to the mixture and the resulting mixture sheared at a high rate . in one embodiment , the initiator is added to the monomer and dissolved therein . the monomer or monomer mixture is then added to the reaction vessel along with the aqueous dispersion with high shearing agitation to obtain a suspension of monomer droplets . the heavy shearing forces reduce the size of the monomer droplets and during this time an equilibrium is reached . the size of the droplets is stabilized or limited by the suspending agent complex which coats their surfaces . the mixture is then heated and stirred in the reaction vessel to polymerize the monomer droplets . the resulting polymer particles are isolated by filtration and can , if desired , be slurried with water to remove water - soluble impurities and free suspending agent complex . alternately , upon achieving a suspension of toner particles in the desired size range , the reaction mixture may be allowed to cool , either at ambient temperature or by immersion in cold water , and the toner particles can be recovered by filtration . the particles may be further washed with a low boiling hydrocarbon solvent to remove the paraffin solvents , and then vacuum dried , leaving dry color toner powder . any suitable mixing equipment may be employed for mixing the components . an example of such equipment is a vessel equipped with an impeller - type agitator and a means of heating the content of the vessel . the temperature selected should ensure fluid - like behavior of the mixture . while any suitable temperature may be employed , preferred temperatures are in the range of at least about 100 ° c . to about 200 ° c . any suitable organic medium which does not interfere with the polymerization of the monomer , water mixable or low boiling points may be employed . exemplary solvents include ethyl acetate , tetrahydrofuran , n , n - dimethyl formamide , acetone , n - methyl pyrrolidone , sulfolane ethylene glycol , and the like . the organic dispersion may further include a surfactant which may be a non - ionic , a cationic or an anionic surfactant . examples of such surfactants include copolymers of vinylpyrrolidonone , alkylated maleic acid copolymers , polymers containing ethylene oxide moieties , polymers containing propylene oxide moieties and sodium dodecylsulfate . the surfactant may be present in the organic dispersion in an amount of from about 0 . 2 wt % to about 15 wt %, based on the amount of organic phase present , while from about 1 wt % to about 10 wt % based on the amount of organic phase present is typical . the mean particle size by volume of a toner in keeping with this processing may range from about 3 microns to about 15 microns , as measured on a coulter multisizer , depending upon the application and the requirements of the imaging machine in which the toner will be used . the resulting fine powder toner may be passed through an air classifier to selectively remove the ultra - fine particles , usually those of 5 microns or smaller , which may be detrimental to the xerographic imaging process . the toner powder thus produced may then be post treated by blending the powder , as in a high intensity blender , with a combination of post additives , such as hydrophobic silane treated silica fine powder and hydrophobic silane treated titanium oxide powder . of course , a single post additive agent may also be used . the skilled artisan will be able to determine what post additive or post additive combination will best suit the intended toner product . treatment with the post additives may produce a toner powder with optimum flow properties for use in the intended printer / copier machine . although conventional dry pigments may be used in the present invention , it has been noted that certain advantages may be realized for a toner prepared from an aqueous pigment concentrate dispersion over that prepared from a dry pigment include a higher degree of pigment dispersion , a higher color density at an equal pigment loading , a reduced pigment loading at a desired color density , narrower particle size distribution and charge distribution . a reduced pigment loading is advantageous in reducing the amount of pigment exposed on the surface of a toner particle and thus narrowing the charge distribution . a reduced pigment loading should reduce fine particles of less than 3 microns and thus narrow the particle size distribution . a higher degree of pigment dispersion becomes advantageous for the preparation of smaller size toner particles ( 5 - 8 microns ) which are needed for the new generation of high resolution laser printers and copiers . the use of an aqueous pigment concentrate dispersion becomes the method of choice for achieving the smaller size toner particles that show high color density , narrow charge distribution and particle size distribution . this example uses an aqueous pigment dispersion concentrate with a conventional wax material . the aqueous pigment concentrate bfd - 1121 pigment blue , which contains 30 . 8 % pigment , 60 % water and 9 . 2 % acrylic polymer pigment stabilizer and available commercially from sun chemical , was used . the following materials were charged into a henschel high intensity mixer : bfd - 1121 concentrate ( 200 g ), a styrene butyl acrylate copolymer resin ( 60 g ), trh ( 10 g ), a charge control agent available commercially from orient chemicals , ceralub p - 40 ( 20 g ), a polypropylene wax available commercially from shamrock technologies , inc ., and cabosil m - 5 silica fine powder ( 4 g ), available commercially from cabot corporation . the foregoing components were blended in the mixer for 10 minutes at 2 , 000 rpm . the resulting blend was allowed to settle and excess water was decanted . the solid paste was then transferred to a warner & amp ; pfleiderer zsk - 30 twin - screw extruder and compounded at 150 ° c . at 400 rpm and at about 64 % torque to form a pigment / wax / resin mixture . the mixture was passed through the extruder once more to make sure complete removal of water . into a 250 milliliter polypropylene bottle was added styrene ( 70 g ), butyl methacrylate ( 60 g ), a solution of 50 wt % of a styrene - n - butylmethacrylate resin in styrene ( 30 g ), and the pigment / wax / resin mixture ( 48 g ). the resulting mixture was shaken overnight with a burrel wrist action shaker until the resin dissolved . aibn 2 , 2 ′- azo - bisisobutyronitrile ( 1 . 5 g ), vazo 52 2 , 2 ′- azo - bis ( 2 , 4 - dimethyl valeronitrile ) ( 1 . 5 g ), were then added to the mixture , which was subsequently homogenized with a brinkmann homogenizer with a 20 tsm generator at 8 , 000 rpm for 1 minute to provide a pigment dispersion . an aqueous phase was prepared by mixing water ( 100 g ), ludox hs - 30 ( 11 g , a dispersion of 30 wt % silica in water available from aldrich ), polyvinylamine ( 0 . 06 g ), 2 . 5 wt % sodium dichromate solution ( 1 . 7 g ), sodium chloride ( 2 g ). the aqueous phase was homogenized ( 8 , 000 rpm ) and a portion of the pigment dispersion ( 80 g ) was then added . homogenization was continued for 10 seconds to provide an o / w ( oil - in - water ) suspension . the resulting mixture was then transferred into a 2 liter reaction kettle equipped with mechanical stirrer and condenser . a non - ionic surfactant solution ( 1 killogram , 2 % pluronic l43 weight average molecular weight 1 , 850 ) was then added to the aforementioned mixture . the resulting mixture was the heated at 75 ° c . for 16 hours , at 85 ° c . for 5 hours , and then transferred into a 4 liter beaker . the resulting toner was then washed with water ( 10 × 3l ) and 0 . 1 n koh solution ( 2 × 3l ), sieved through a combination of 425 and 250 microns sieves , and freeze dried to provide a toner . this example used an aqueous pigment dispersion concentrate with an aqueous dispersible wax , unithox ® 450 ethoxylate available from baker petrolite and a conventional wax . the following materials were charged into a henschel high intensity mixer : bfd - 1121 pigment concentrate ( 200 g ), unithox ® 450 ( 20 g ), a styrene butyl acrylate copolymer resin ( 60 g ), trh ( 10 g ), a charge control agent available commercially from orient chemicals , ceralub p - 40 ( 20 g ), a polypropylene wax available commercially from shamrock technologies , inc ., and cabosil m - 5 silica fine powder ( 4 g ), available commercially from cabot corporation . the foregoing components were blended in the mixer for 10 minutes at 2 , 000 rpm . the resulting blend was allowed to settle and excess water is decanted . the solid paste was then transferred to a warner & amp ; pfleiderer zsk - 30 twin - screw extruder and compounded at 150 ° c . at 400 rpm and at about 64 % torque to a pigment / wax / resin mixture . the mixture was passed through the extruder once more to make sure complete removal of water . into a 250 milliliter polypropylene bottle was added styrene ( 70 g ), butyl methacrylate ( 60 g ), a solution of 50 wt % of a styrene - n - butylmethacrylate resin in styrene ( 30 g ), and the pigment / wax / resin mixture ( 48 g ). the resulting mixture was shaken overnight with a burrel wrist action shaker until the resin is dissolved . aibn 2 , 2 ′- azo - bisisobutyronitrile ( 1 . 5 g ), vazo 52 2 , 2 ′- azo - bis ( 2 , 4 - dimethyl valeronitrile ) ( 1 . 5 g ), were then added to the mixture , which was subsequently homogenized with a brinkmann homogenizer with a 20 tsm generator at 8 , 000 rpm for 1 minute to provide a pigment dispersion . an aqueous phase was prepared by mixing water ( 100 g ), ludox hs - 30 ( 11 g , a dispersion of 30 wt % silica in water available from aldrich ), polyvinylamine ( 0 . 06 g ), 2 . 5 wt % sodium dichromate solution ( 1 . 7 g ), sodium chloride ( 2 g ). the aqueous phase is homogenized ( 8 , 000 rpm ) and a portion of the pigment dispersion ( 80 g ) was then added . homogenization was continued for 10 seconds to provide an o / w ( oil - in - water ) suspension . the resulting mixture was then transferred into a 2 liter reaction kettle equipped with mechanical stirrer and condenser . a non - ionic surfactant solution ( 1 killogram , 2 percent pluronic l43 weight average molecular weight 1 , 850 ) was then added to the aforementioned mixture . the resulting mixture was the heated at 75 ° c . for 16 hours , at 85 ° c . for 5 hours , and then transferred into a 4 liter beaker . the resulting toner was then washed with water ( 10 × 3 l ) and 0 . 1 n koh solution ( 2 × 3 l ), sieved through a combination of 425 and 250 microns sieves , and freeze dried to provide a toner . it is to be understood that the inventive aspects of the formulation as presented herein are equally applicable to all color toner formulations , and it is intended that the invention should be construed in keeping with and afforded the full breadth of coverage of the appended claims .