except for the coating containing the conductive carbon black , the coated abrasive articles of the invention are constructed from conventional materials by a method which is well known in the art . the support member is typically coated with a first layer of binder adhesive , often referred to as a &# 34 ; make coat &# 34 ;, and then abrasive grains are applied . the abrasive grains may be oriented or may be applied to the support member without orientation , depending upon the requirements of the particular coated abrasive product . however , for use in wood finishing operations it is preferred that the abrasive grains be electrostatically applied so that a greater proportion of the grains have their longer axis more nearly perpendicular to the plane of the support member . alternatively , the first layer can be a slurry coat which comprises abrasive grains distributed throughout the adhesive binder . thereafter , the resulting adhesive / abrasive composite layer is then generally solidified or set sufficiently to retain the abrasive grains on the support member so that a second layer of binder adhesive , often referred to as a &# 34 ; size coat &# 34 ;, can be applied . the size coat further reinforces the coated abrasive product . optionally , an additional binder adhesive overcoat , often referred to as a &# 34 ; supersize coat &# 34 ;, which may contain grinding aids or other well known additives , can be applied over the size coat . once the final adhesive coating is solidified , the resulting coated abrasive product can be converted into a variety of conventional forms such as , for example , sheets , rolls , belts and discs . the conventional components forming the coated abrasive product of the invention may be selected from those typically used in this art . for example , the support member may be formed of paper , cloth , vulcanized fiber , polymeric film or any other suitable material currently known or which becomes available for this use in the future . the abrasive granules may be of any size and type conventionally utilized in the formation of coated abrasives such as , for example , flint , garnet , aluminum oxide , ceramic aluminum oxide , alumina zirconia , diamond , silicon carbide or mixtures thereof . preferably , the abrasive granules are selected from the group consisting of garnet , aluminum oxide , ceramic aluminum oxide , alumina zirconia and silicon carbide , and have a size ranging from about 16 grade ( average particle diameter of about 1320 ) to about 1200 grade ( average particle diameter of about 6 . 5 ). the bond system , which secures the abrasive granules to the support member , may be formed from urethane resins , phenolic reins , epoxy resins , acrylate resins , urea - formaldehyde resins , melamine - formaldehyde resins , glues or mixtures thereof . the bond system may also include other additives well known in the art such as fillers , grinding aids , coupling agents , dyes , wetting agents and surfactants . if the coated abrasive support member is cloth , is preferably has one or more binder adhesive layers which serve to seal the cloth and modify the final properties of the cloth . in general if the binder adhesive is present on the front surface of the support member beneath the abrasive coating , it is referred to as a &# 34 ; presize &# 34 ;. if it is present on the back surface of the support member on the opposite surface as the presize , it is referred to as a &# 34 ; backsize &# 34 ;. if the binder adhesive saturates the support member , it is referred to as a &# 34 ; saturant &# 34 ;. the coated abrasive product of the invention may also include such other modifications as are conventional in this art . for example , a coating of a pressure - sensitive adhesive may be applied to the nonabrasive side of the construction . at least one cured binder adhesive of the coated abrasive article of the invention is made conductive by incorporating carbon black aggregates into the formulation of at least one of the following : make coat , slurry coat , size coat , supersize coat , backsize coat , presize coat , and saturant . the carbon black useful in the present invention is an amorphous modification of carbon , typically formed by the partial combustion of hydrocarbons , which has an outermost oxidized atomic layer due to exposure to air . the carbon black aggregates can be added directly to the coating formulations . alternatively , the carbon black aggregates can be added to the coating formulations in the form of an aqueous dispersion . this latter method is preferred as the dispersion of the carbon black aggregates throughout the coating formulations is more easily accomplished if the carbon black aggregates are predispersed in an aqueous solution . generally , if a predispersed form is utilized , a greater percentage of carbon black aggregates may be present in the adhesive binder while maintaining the proper viscosity for coating . if the aggregates are not predispersed , the viscosity is higher , which may lead to difficulty in processing . furthermore , aqueous dispersions of carbon black aggregates are commercially available from sources such as cdi dispersions of newark , n . j . preferably carbon black aggregates , a dispersion aid , and a liquid dispersing medium such as water are mixed together until a homogeneous coating composition is achieved . more than one compatible dispersion aid may be used . this dispersion is then added to the adhesive binder . if the liquid dispersing medium is water , the dispersion aid can be an anionic or ionic surfactant . typical examples of surfactant dispersion aids include commercially available surfactants such as &# 34 ; daxad 11g &# 34 ; from w . r . grace of lexington , mass . ; &# 34 ; lomar pwa &# 34 ; and &# 34 ; nopcosperse a - 23 &# 34 ; from henkel corporation of ambler , pa . and &# 34 ; marasperse cbos - 4 &# 34 ; from daishowa chemicals inc . of rothschild , wis . the weight ratio of carbon black aggregates to dispersion aid preferably is in the range of 2 : 1 to 30 : 1 and more preferably in the range of 4 : 1 and 12 : 1 . if this ratio is too low or too high , the resulting viscosity may be too high . if the amount of dispersion aid is too great , unwanted recoagulation of the carbon black aggregates may occur . preferably , the dispersion contains 1 to 25 weight percent carbon black aggregates . the carbon black aggregate dispersion may be in an organic liquid instead of water . a dispersion aid which will be compatible with the particular organic liquid should then be employed . more than one compatible organic liquid may be used . it is preferred to use water as the dispersing medium to avoid the environmental concerns associated with organic liquids . as will be recognized by those skilled in the art , it is important to match the proper dispersion aid with the adhesive binder . if the dispersion aid and the adhesive binder are not compatible , the resulting coating composition may be too viscous . for example , an anionic dispersion aid is preferred with phenolic adhesive systems . one skilled in the adhesive binder art should be able to make such an assessment . in order to obtain good conductivity , the concentration of carbon black in the coating must be high enough to provide a continuous conductive pathway throughout the coating . since the conductivity of carbon black is isotropic ; that is , it does not rely on the juxtaposition of the carbon along a particular plane to yield a conductive path through the coating , the threshold concentration of carbon black required to provide a continuous conductive pathway throughout the coating is generally lower than the threshold concentration required for other conductive materials , such as graphite , in which the conduction is anisotropic . below the threshold concentration of carbon black there are only intermittent conductive pathways , formed by short chains of the amorphous carbon black aggregates , which is believed to explain the poor and / or erratic conductivity of coated abrasives articles containing low loadings of carbon black . preferably , the carbon black is present in a concentration sufficient to provide the binder adhesive layer which includes it with a surface resistivity of less than about 2000 kilo - ohms / cm , more preferably , less than about 500 kilo - ohms / cm , and most preferably , less than about 200 kilo - ohms / cm . the carbon black aggregates useful in the invention are formed of a multitude of smaller carbon black particles which are permanently fused together during the manufacturing process . generally these carbon black particles are nearly spherical with diameters ranging from about 15 nm to about 90 nm . preferably , the carbon black aggregate are composed of carbon black particles having an average particle size from 10 to 60 nm , more preferably from 10 to 40 nm . the amount of carbon black in the coating composition required to form a continuous conductive pathway and lower the resistivity of the abrasive article to the range specified above depends upon the structure of the aggregate , the surface area of the aggregate , the surface chemistry of the aggregate and the size of the carbon black particles comprising the aggregate . for equal loadings of carbon black aggregates , reducing the size of the individual carbon black particles comprising the aggregates , while maintaining the other parameters constant , results in a reduction in the surface resistivity of the abrasive article . preferably , the size of the carbon black aggregates is less than 300 micrometers . more preferably , the size of the carbon black aggregates is in the range of 125 to 275 micrometers . a mixture of carbon black aggregates having 2 or more sizes of carbon black aggregates ( e . g ., a mixture of relatively large aggregates and relatively small aggregates ) may also be used . such mixtures would tend to provide a more efficient distribution of carbon black aggregates in the adhesive binder . the structure of carbon black aggregates refers to the size and configuration of the aggregate . high structure carbon blacks are composed of relatively highly branched aggregates while low structure carbon blacks are composed of relatively small compact aggregates . the structure of carbon black aggregates is characterized by the aggregate &# 39 ; s void volume . high structure carbon blacks contain more void space than low structure carbon blacks because their highly branched shape prevents close packing . one common way of quantifying structure is the dibutyl phthalate absorption test . this test measures the volume of dibutyl phthalate ( in ml ) absorbed by 100 g of carbon black , which is a measure of the amount of fluid required to fill the voids between aggregates . the dibutyl phthalate absorption can be used as a guide to structure level because , for a given surface area , the higher the structure , the higher the dibutyl phthalate absorption will be . for equal loadings of carbon black aggregates , increasing the structure of the carbon black aggregates used , while maintaining the other parameters constant , results in a reduction in the surface resistivity of the cured adhesive binder layer containing the carbon black aggregates . preferably the carbon black aggregates have a dibutyl phthalate absorption of from about 50 to 400 ml / 100 g , more preferably , from about 100 to 400 ml / 100 g . additionally , in the manufacturing process of all furnace type carbon blacks , chemisorbed oxygen complexes , such as carboxylic , quinonic , lactonic , and hydroxylic groups , form on the surface of the aggregates . these adsorbed molecules can be driven off by heating the carbon black aggregates to temperatures of about 950 c and are thus referred to as the volatile content . since these adsorbed molecules act as an electrically insulating layer on the surface of the carbon black aggregates , decreasing the volatile content of the carbon black aggregates used , while maintaining the other parameters constant , results in a reduction of the surface resistivity of the adhesive binder containing the carbon black aggregates . at volatile contents greater than about 4 percent by weight the carbon black aggregates are nonconductive . preferably the volatile content of the carbon black aggregates is less than about 3 percent by weight , more preferably , less than about 2 percent . the reduction in the surface resistivity of the adhesive binder containing the carbon black aggregates is also a function of the surface area of the carbon black aggregates used . for equal loadings of carbon black aggregates , increasing the surface area of the carbon black aggregates , while maintaining the other parameters constant , results in a reduction in the surface resistivity of the abrasive article . preferably the surface area of the carbon black aggregates is from about 100 to 1000 m 2 / g , more preferably , from about 130 to 1000 m 2 / g . preferably the total solid content of an uncured adhesive binder according to the present invention is in the range of 20 to 75 weight percent . more preferably the total solids content is in the range of 35 to 65 weight percent . in another aspect , preferably the viscosity of an uncured adhesive binder according to the present invention is in the range of 25 to 2000 cps . more preferably the viscosity is in the range of 100 to 1000 cps , and most preferably in the range of 100 to 750 cps . the present invention is further illustrated by the following nonlimiting examples wherein all parts and percentages are by weight unless otherwise specified . in these examples carbon black aggregates were mixed throughout a binder resin coating formulation by an air driven stirrer equipped with a propeller blade ( commercially available from gast manufacturing corp . ), and the resulting mixture was coated onto a sanding belt . the coating was then cured in a forced air oven . the sanding belts were then installed on an oakley model d semi - automatic single belt sander ( the oakley company ; bristol , tenn . ), and used to sand wood or wood - like products . the use of abrasive having the inventive adhesive binder layer comprising carbon black aggregate yielded a noticeable increase in the amount of dust removed by the exhaust system . a silicon carbide , y weight , cloth sanding belt , 15 cm × 762 cm , was made using a filled phenolic resole make coat and grade 120 ( average particle size of about 116 micrometers ) silicon carbide abrasive particles . a size coat adhesive was prepared according to the following steps : a ) adding about 10 . 9 parts ethylene glycol monoethyl ether to about 89 . 1 parts water ; b ) adding 503 grams of a sodium naphthalene sulfonate / formaldehyde copolymer dispersing agent ( daxad llg ; w . r . grace & amp ; co . ; lexington , ma ) to 6281 grams of the mixture prepared in step ( a ), while stirring ; c ) adding the mixture for step ( b ) to 7725 grams of a phenolic resole ( phenolic resin having a phenol to formaldehyde ratio of about 1 : 2 and a solids content of 76 percent ), while stirring ; and d ) adding 493 grams of carbon black aggregates having a volatile content of 1 . 2 percent , a surface area of 1000 m 2 / g , and a dibutyl phthalate absorption of 370 ml / 100 g , and composed of carbon black particles having an average particle size of about 35 nm ( printex xe - 2 ; degussa ; frankfurt , west germany ) to the mixture from step ( c ), while stirring ; and the size coat adhesive binder was applied to the silicon carbide coated belt described above . after the size coat had cured , the surface resistivity of the cured size coat was measured by placing the probes of an ohmmeter ( beckman industrial digital multimeter , model 4410 ) onto the surface of the cured size coat 1 . 0 cm apart . this yielded a surface resistivity value of 21 . 7 ± 6 . 1 kilo - ohms / cm . the surface of a grade 100 ( average particle size of about 15 micrometers ), silicon carbide , e weight paper sanding belt having a hide glue make coat and an unfilled phenolic resole size coat , 15 cm × 762 cm , was made conductive by applying a conductive supersize coating , wherein the supersize coat adhesive was prepared according to the following steps : a ) adding 18 parts of a dispersing agent ( daxad 11g ) to 61 . 2 parts water , while stirring ; b ) adding 19 . 8 parts of the dispersing agent / water mixture prepared in step ( a ) to 601 . 1 parts water , while stirring ; c ) adding 157 . 7 parts ethylene glycol monoethyl ether to the mixture from step ( b ), while stirring ; d ) adding 40 . 5 parts of carbon black aggregates having a volatile content of 1 . 5 percent , a surface area of 254 m 2 / g , and a dibutyl phthalate absorption of 185 ml / 100 g , and composed of carbon black particles having an average particle size of 35 nm ( vulcan xc - 72r ; cabot corp . ; boston , mass .) to the mixture from step ( c ), while stirring ; e ) repeating steps ( b ) and ( c ) 3 times ( to provide a mixture comprising 662 . 3 parts water , 157 . 7 parts ethylene glycol monoethyl ether , 18 parts dispersing agent , and 162 parts carbon black ); f ) adding about 11 . 1 parts ethylene glycol monoethyl ether to about 88 . 9 parts water ; g ) adding 2746 grams of the ethylene glycol monoethyl ether / water mixture from step ( f ) to 1941 grams of a melamine - formaldehyde resin ( mf - 405 ; btl specialty resins corp . ; warren , n . j . ), while stirring ; h ) adding 2147 grams of kaolin to the mixture from step ( g ), while stirring ; i ) adding 8120 grams of the mixture from step ( e ) to the mixture from step ( h ), while stirring ; and after curing the supersize coating , the surface resistivity of the abrasive belt was measured as described in example 1 and found to be less than 100 kilo - ohms / cm . this belt and a similar belt having no supersize coating and having a measured surface resistivity of greater than 20 , 000 kilo - ohms / cm were used to sand red oak workpieces on an oakley model d single belt sander with a belt speed of 1670 surface meters per minute ( smpm ) ( 5500 surface feet per minute ( sfpm )). when using the belt having the conductive supersize coating no electrical shocks were experienced by the operator from the steel stop used to limit the workpiece &# 39 ; s movement , and dust accumulation on the workpiece and on the sanding machine were greatly reduced . in contrast , when using the similar belt having no conductive supersize coating the operator experienced many shocks and dust accumulation was greatly increased . additionally , an ammeter was connected to the steel stop used to limit the workpiece &# 39 ; s movement and to ground in order to check for measurable current flow . using the nonconductive belt resulted in a current flow of from 0 . 4 to 2 . 2 microamps . in contrast , the use of the abrasive belt having the conductive supersize coating produced no measurable current flow . two silicon carbide , e weight paper , sanding belts ( 15 cm × 762 cm ) were made using a phenolic resole make coat and grade p180 ( average particle size of about 78 micrometers ) silicon carbide abrasive particles . to one belt was applied a standard nonconductive resole size coating . to the other was applied a carbon black containing conductive coating prepared according to the following steps : ( a ) adding 1 part ethylene glycol monoethyl ether to 9 parts water ; ( b ) adding 940 grams of the mixture from step ( a ) to 3790 grams of a phenolic resole ( as described in example 1 ), while stirring ; ( c ) adding 2648 grams of calcium carbonate ( average size of about 16 micrometers ) to the mixture from step ( b ), while mixing ; ( d ) adding 2622 grams of an aqueous dispersion comprising carbon black aggregates ( prepared as described in steps ( a ) through ( e ) of example 2 ) to the mixture from step ( c ); and after the size coatings had cured , both belts were evaluated on the same red oak workpiece using an oakley model d single belt as described in example 1 . the testing period for each belt was 45 minutes . cut tests indicated nearly identical performance . the red oak dust concentration was measured on the operator and on the machine at a point just past the workpiece and adjacent to the exhaust by gravimetric analysis using nucleopore membrane filters having a pore size of 0 . 8 micrometers ( commercially available from nucleopore corp . of pleasanton , calif .). for the standard nonconductive belt , the concentration of dust at the operator was 1 . 7 mg / m 3 and at the point just past the workpiece it was 170 mg / m 3 . for the abrasive belt having the conductive size coating , the values were 1 . 1 mg / m 3 and 75 . 6 mg / m 3 , respectively . the surface of a grade p150 ( average particle size of about 97 micrometers ), aluminum oxide , f weight paper sanding belt ( 15 cm × 762 cm ) having a calcium carbonate filled phenolic resole make coat was made conductive by applying to it and curing an unfilled phenolic resole size coating prepared according to the following steps : ( b ) adding 160 grams of the mixture from step ( a ) to 5850 grams of a phenolic resin ( as described in example 1 ), while stirring ; ( c ) adding 4290 grams of an aqueous dispersion comprising carbon black aggregates ( prepared as described in steps ( a ) through ( e ) of example 1 ) to the mixture from step ( b ); and this formulation , when cured , was 13 . 5 percent by weight carbon black . the surface resistivity of the sanding belt was determined , as described in example 1 , to be less than 150 kilo - ohms / cm . the surface of a grade p150 , aluminum oxide , sanding belt , as described in example 4 , was overcoated with the size coating composition of example 4 with the exception that an equal amount of graphite particles having an average particle size of 5 micrometers ( commercially available from dixon ticonderoga co . of lakehurst , n . j .) was substituted for the carbon black aggregates . this formulation , when cured , yielded a surface resistivity of over 20 , 000 kilo - ohms / cm . the surface of a grade p150 , aluminum oxide , sanding belt , as described in example 4 , was made conductive by applying a filled phenolic resole size coating prepared as described in example 3 , which , when cured , was filled to 52 weight percent overall ( 45 % calcium carbonate , 7 % carbon black ). this adhesive binder formulation , when cured , provided the sanding belt with a surface resistivity of less than 100 kilo - ohms / cm . the surface of a grade p150 , aluminum oxide , sanding belt , as described in example 4 , was overcoated with the size coating composition of example 6 with the exception that an equal amount of graphite particles having an average particle size of 5 micrometers ( commercially available from dixon ticonderoga co .) was substituted for the carbon black aggregates . this formulation , when cured , yielded a surface resistivity of over 20 , 000 kilo - ohms / cm . the grade p150 , aluminum oxide , sanding belts prepared in examples 4 - 7 were mounted on an oakley model d - 1 single belt sander , operating at 1670 surface meters per minute ( smpm ) ( 5500 surface feet per minute ( sfpm )) and under a constant 4 . 55 kg ( 10 lb .) load , and used to sand red oak workpieces for a period of 30 minutes . a 40 . 6 cm × 59 . 7 cm aluminum plate was placed between the end of the workpiece and the outlet dust hood . this plate was used both to collect the wood dust that would normally fall onto the sanding table during the test period and to measure the current generated by the electrostatically charged dust . the amount of dust collected was weighed after each test period , and current measurements were made by connecting an ammeter between the plate and a ground . for each belt tested , the total mass of wood stock removed by sanding was divided by the mass of dust collected on the aluminum plate to generate a dimensionless dust efficiency factor ( def ). thus , high values of the def indicate that the production of dust uncollected by the exhaust system was low ; that is , the abrasive belt having the conductive size coat was efficient in keeping static electricity to a minimum . the results of these tests are shown below in table 1 for the belts of examples 4 - 7 . two representative test runs are shown for each example . table 1______________________________________ current generatedexample no . def ( microamps ) ______________________________________4 a ) 94 . 1 . 03 -. 054 b ) 87 . 7 . 05 -. 075 a ) 16 . 0 1 . 35 - 1 . 405 b ) 16 . 4 . 67 - 1 . 346 a ) 74 . 2 . 03 -. 046 b ) 85 . 5 . 05 -. 067 a ) 8 . 3 1 . 37 - 1 . 597 b ) 13 . 5 . 55 -. 69______________________________________ in all cases , as can be seen from the data in table 1 , carbon black is much more efficient in reducing the amount of dust than graphite containing size coats . in order to test the performance of a coated abrasive having a conductive supersize coat with a second non - conductive zinc stearate supersize coating , a grade p180 ( average particle size of about 78 micrometers ), aluminum oxide , f weight paper abrasive article was first fabricated using a hide glue make coat and urea - formaldehyde size coat . the abrasive article was then overcoated with a urea - formaldehyde supersize coating solution which contained 13 . 9 percent by weight of the carbon black aggregates used in example 2 . the surface resistivity was measured at less than 100 kilo - ohms / cm . the abrasive article was then coated with a 12 . 6 % solution of zinc stearate in water . the coated abrasive article was then converted into belts 15 . 2 cm × 762 cm . when tested on the oakley sander ( as described in example 1 ), the amount of wood dust observed on the sanding table and on the workpiece after test completion was remarkably reduced with respect to the amount of dust observed when using a non - conductive belt . the back surface of a grade p150 ( average particle size of about 97 micrometers ), aluminum oxide , e weight paper sanding belt ( 15 cm × 762 cm ) having a hide glue make coat and a calcium carbonate filled phenolic resole size coat was made conductive by applying thereto a backsize coat formulation which was prepared according to the following steps : ( a ) adding 198 . 6 grams of water to 166 . 4 grams of urea - formaldehyde ( durite al8405 ; borden chemical ; ontario , canada ), while stirring ; ( b ) adding 191 . 9 grams of an aqueous dispersion of carbon black aggregates having a volatile content of 1 . 5 percent , a surface area of 254 m 2 / g , and a dibutyl phthalate absorption of 185 ml / 100 g , and composed of carbon black particles having an average size of 30 nm ( bs 10795 ; cdi dispersions ; newark , n . j .) to the mixture from step ( a ), while stirring ; ( c ) adding 2 . 9 grams of aqueous aluminum chloride ( 28 % solids ) to the mixture from step ( b ), while stirring ; and after curing the coating , the surface resistivity of the back surface was less than 50 kilo - ohms / cm . the grade p150 , aluminum oxide , sanding belt of example 9 and a belt identical in all respects except that it did not have the conductive coating were mounted on an oakley model d single belt sander , operating at 1760 smpm ( 5500 and under a constant 4 . 55 kg ( 10 lb .) load , and used to sand red oak workpieces for a period of 21 minutes . the dust efficiency factor was measured for each belt by the method described above for the belts of examples 4 - 7 . the belt of example 9 having the conductive size coat had a def of 25 . 4 and the nonconductive belt had a def of 3 . 0 . additionally , the belt of example 9 having the conductive size coat removed about 10 percent more stock and had an abrading surface that was remarkably cleaner than that of the nonconductive belt . 3785 grams of an aqueous carbon black dispersion ( prepared as described in steps ( a ) through ( e ) of example 2 ) this make adhesive was applied to a f weight paper backing to provide an average wet add - on weight of 45 grams / square meter . immediately afterwards , grade p150 aluminum oxide abrasive grains were projected into the make coat to provide an average add - on weight of 134 grams / square meter . the resulting composite was precured for 25 minutes at 88 ° c . the surface resistivity of this unsized coated abrasive was measured in the same manner as example 1 and the value was less than 200 kilo - ohms / cm . a calcium carbonate filled resole phenolic resin size adhesive was applied over the abrasive grains to provide an average add - on wet weight of 76 grams / square meter . the size adhesive was cured and the resulting coated abrasive was converted into 15 cm × 762 cm endless belts . the surface resistivity of the cured size coat was determined , as described in example 1 , to be greater than 20 , 000 kilo - ohms / cm . a control belt was prepared in the same manner as example 10 except it did not contain carbon black aggregates in the make adhesive . the dust efficiency factor of the example 10 and the control were tested in the same manner as example 4 except the test length was reduced to 21 minutes . the results are shown below in table 2 . the data indicate the construction having a make coat comprising carbon black aggregates was much more efficient in reducing the amount of dust than a conventional construction . a y weight sateen polyester cloth was saturated with a phenolic / latex solution and then partially cured until the treated cloth was dry to the touch . next a presize coating composition containing the carbon black aggregates was knife coated on the abrasive side of the cloth to provide an average add - on wet weight of 117 grams / square meter . the presize coating composition was prepared by thoroughly mixing : 3905 grams of aerofene 72155 - w - 55 phenolic resin ( ashland chemical company ; columbus , ohio ); 3065 grams of hycar nitrile latex 1571 ( bf goodrich company ; cleveland , ohio ); and 3030 grams of a carbon black aggregate dispersion ( prepared as described in steps ( a ) through ( e ) of example 2 ). the presize coating composition was partially cured until the treated cloth was dry to the touch . a backsize coating composition was then applied to the non - abrasive side of the cloth , i . e . opposite the presize . the backsize coating composition consisted of a phenolic / latex resin and was partially cured in the same manner as the saturant . next , a conventional make adhesive , abrasive grain and the size adhesive were applied to the treated backing in a traditional manner to form the coated abrasive . the make and size adhesives were conventional calcium carbonate filled resole phenolic resins . the abrasive grain was grade 120 silicon carbide . after the size adhesive was applied , the construction was fully cured for 10 hours at 95 ° c . two controls , control - b and control - c , were prepared in the same manner as example 11 but with the following exceptions . the presize coating composition used to prepare control - b did not contain carbon black aggregates . the presize for control - c , which contained graphite rather than carbon black aggregates , was prepared by thoroughly mixing : 868 grams of graphite ( lonza k6 ; lonza inc . ; fair lawn , n . j .). the example 11 , control - b , and control - c abrasive articles were converted into 15 cm x 762 cm endless belts . the cut performance of these belts were evaluated as described in example 2 . the def as defined in example 7 of each construction , was also determined . the data are provided below in table 3 . table 3______________________________________example no . cut , grams dust , grams def______________________________________11 393 4 98 . 2control - b 409 38 10 . 8control - c 369 3 123______________________________________ the data show the improvement in def by incorporating carbon black aggregates into the presize coating . example 12 was prepared as follows . one hundred and twenty - five grams of ethylene glycol monoethyl ether was added to 500 grams of water . carbon black aggregates ( as described in example 1 ) was added to the ethylene glycol monoethyl ether / water mixture , while stirring , until a thick paste resulted . the total amount of carbon black added was 52 . 7 grams . five hundred and forty - seven grams of the thick paste was added to 390 grams of a phenolic resole ( as described in example 1 ), while stirring . the viscosity of the resulting adhesive binder , as determined using a brookfield model lvtdv - ii viscometer ( brookfield engineering laboratories , inc . ; stoughton , mass . ), using a number 2 spindle at 30 rpm , was 50 cps at a temperature of 50 ° c . a control adhesive binder , control - d , was prepared as follows . thirty - one and one - half grams of carbon black aggregates ( as described in example 1 ) was added to 777 grams of a phenolic resole ( as described in example 1 ) while stirring . the viscosity of the control - d adhesive , as determined with the brookfield viscometer , using a number 3 spindle , at 6 rpm was 16 , 100 cps at a temperature of 55 ° c . a 2 . 5 micrometer ( 0 . 01 inch ) thick film of the example 12 and control - d adhesives were knife coated onto glass microscope slides . the films were cured according to the following heating schedule : 25 °→ 66 ° c . ( 150 ° f .) at about 2 . 7 ° c ./ min 66 ° c . for about 0 . 5 hours 66 °→ 88 ° c . ( 190 ° f .) at about 2 . 2 ° c ./ min 88 ° c . for about 0 . 75 hours 88 °→ 104 ° c . ( 220 ° f .) at about 1 . 1 ° c ./ min 104 ° c . for about 1 hour . the amount of carbon black present in the cured example 12 and control - d adhesives were 12 . 5 and 5 . 1 percent , respectively . the surface resistivity of the cured example 12 and control - d adhesives were determined , as described in example 1 , to be less than 50 kilo - ohms / cm and greater than 20 , 000 kilo - ohms / cm , respectively . example 13 describes a preferred method for preparing an adhesive binder according to the present invention . this example was prepared according to the following steps : ( a ) adding 18 grams of a dispersing agent ( daxad llg ) to 61 . 2 grams of water , while stirring ; ( b ) adding 19 . 8 grams of the dispersing agent / water mixture from step ( a ) to 601 . 1 grams of water , while stirring ; ( c ) adding 157 . 7 grams of ethylene glycol monoethyl ether to the mixture from step ( b ); ( d ) adding 40 . 5 grams of carbon black aggregates ( as described in example 1 ) to the mixture from step ( c ); ( e ) repeating steps ( b ) and ( c ) 3 times ( to provide a mixture comprising 662 . 3 grams of water , 157 . 7 grams of ethylene glycol monoethyl ether , 18 grams of dispersing agent , and 162 grams of carbon black aggregates ); ( f ) adding the mixture for step ( e ) to 568 grams of a phenolic resole ( as described in example 1 ), while stirring ; and the viscosity of the resulting adhesive binder was determined as described in example 12 using a number 2 spindle . the viscosity at 30 rpm was 140 cps at a temperature of 40 ° c . the adhesive binder was coated onto a glass slide and cured as described in example 12 . the surface resistivity of the cured adhesive binder , as determined by the method described in example 1 , was less than 50 kilo - ohms / cm . the amount of carbon black present in the cured adhesive binder was 12 . 4 percent . various modifications and alterations of this invention will become apparent to those skilled in the art without departing from the scope of this invention , and it should be understood that this invention is not to be unduly limited to the illustrative embodiments set forth herein .