the present section details the preferred embodiments of the invention . these embodiments are set forth to illustrate the invention and aid in its understanding . since this disclosure is not a primer on inorganic oxides or tio 2 pigment production or their treatment or the design , manufacture or operation of treatment vessels , basic concepts known or readily determinable by those skilled in the field of tio 2 production have not been set forth in detail . concepts such as choosing appropriate manufacturing materials or solvents , or appropriate additives for the treatment process , or suitable conditions for operating the treatment process are known or readily determinable by those skilled in the industry . attention is directed to the appropriate texts and references known to those in the art field for details regarding these and other concepts that may be necessary in the practice of the invention . methods for treating tio 2 pigment with organosilicon compounds are well known in the prior art and are discussed in numerous references , including u . s . pat . nos . 2 , 488 , 440 ; 2 , 559 , 638 ; 4 , 061 , 503 ; and 4 , 151 , 154 , the dupont patents and u . s . pat . no . 5 , 653 , 794 by the present inventors . the teachings of these patents are incorporated into the present disclosure by reference . the subject invention provides a method for preparing a hydrophobic inorganic oxide by ( i ) mixing a reactive silane with an aqueous media under conditions so that the reactive silane substantially condenses and forms an aqueous reactive dispersion and ( ii ) mixing the resulting aqueous dispersion with a slurry of pigment and water under conditions so that the reactive dispersion chemically reacts with the inorganic oxide directly or upon subsequent heating or drying . suitable reactive silanes useful in the practice of the invention maybe represented by the formula : where r represents a nonhydrolyzable aliphatic , cycloaliphatic or aromatic group ( including a saturated or unsaturated branched or unbranched alkyl , aryl cycloalkyl or alkylaryl group ) having 1 to 20 carbon atoms , x represents a halogen and n = 1 or 2 . preferably , the reactive silane is an organochlorosilane , such as butyltrichlorosilane , isobutyltrichlorosilane , hexyltrichlorosilane , octyltrichlorosilane , octylmethyldichlorosilane , decyltrichlorosilane , dodecyltrichlorosilane , didecyldichlorosilane , dihexyldichlorosilane , dioctyldichlorosilane , octadecyltrichlorosilane or mixtures thereof . more preferably , the reactive silane is an organochlorosilane having an r group with 4 - 10 carbons and , in particular , 6 - 8 carbons . the most preferred organohalosilane is hexyltrichlorosilane . inorganic oxides appropriate for use in the present invention include those which have surface hydroxyls capable of condensing with reactive silanes or their hydrolyates or condensates . such inorganic oxides are represented by the rutile and anatase forms of titanium dioxide , kaolin and other clays , alumina , silica , aluminum trihydrate , zirconium oxide , zinc oxide , iron oxide , cadmium pigments , chromate pigments , chromium oxide pigments , glass fibers , glass flake , wollastonite and the like . preferred are standard pigment - grade titanium dioxides , regardless of whether they have been obtained from titanium tetrachloride or from titanium sulfate . the inorganic oxide can be an untreated inorganic oxide or an inorganic oxide whose surface has been treated by deposition thereon of phosphate , alumina , silica , zirconia and the like , using procedures known to practitioners in the field of inorganic oxide surface treatment . preferably , the inorganic oxide is titania or tio 2 pigment , whose surface is untreated or treated by deposition thereon of a hydrous phosphate , alumina , silica , zirconia or like - material . a preferred mode for practicing the claimed invention typically proceeds as follows . a reactive organohalosilane , such as hexyltrichlorosilane ( htcs ), is mixed with an aqueous media using a commercial type static mixer or emulsifier to form a dispersion that contains substantially the condensates of the silane . it is preferable to mix the silane with the aqueous media using a high speed emulsifier or agitator , such as an in - line rotor - stator mixer , in order to keep the resulting condensate well dispersed and to minimize any unreacted silane . although agitation is not critical , the agitation should be sufficient to avoid gelling of the silane , its condensates or the dispersion . the residence time of the dispersion in the mixer typcally is very short , 0 . 5 to 1 second , although longer times may be used . the dispersion is aged ( usually in the mixer or in a process line or batch mixer downstream ) for about 1 second to about 120 seconds , preferably for around 20 seconds . longer aging times can be used if sufficient agitation is present . it is also preferred to maintain a ph value above or equal to about nine to aid in driving the conversion of the silane toward condensates of the silane . although a high ph value of around 9 is preferred , it is contemplated that the invention may be practiced at lower ph values also , even ph values of 1 - 2 . at lower ph values , there may be less conversion of the silane to its condensates but a reactive dispersion would still be formed . it is also contemplated that the invention will be practiced at the ph value that results from mixing the silane with the aqueous media ; that is , no adjustment of the ph is made . it is also contemplated that the dispersion that results from mixing the silane with the aqueous media may be heated to aid in conversion of the silane to its condensates . the temperature to which the dispersion may be heated will be determined , for the most part , by the type of equipment that is available . typically the dispersion may be heated to 70 - 90 ° c . the resulting aqueous dispersion is added over a period of time to a reactor containing a slurry of tio 2 pigment and water . the pigment slurry should be sufficiently agitated such : that the reactive dispersion is rapidly mixed into the bulk of the pigment slurry . the amount of aqueous dispersion added to the reactor is such so as to result in a concentration of organosilicon coating on the final pigment in the range of about 0 . 1 to about 5 . 0 weight percent based on the weight of the pigment . after the dispersion is mixed with the pigment slurry , the entire mass is allowed to come to an equilibrium ph and consequently a uniform viscosity . the ph is then raised to flocculate the organically treated pigment and to facilitate filtration and washing of the pigment . typically , additions of an alkali source , such as sodium hydroxide , are used to raise the ph up to a value of about 7 - 10 ph ( although lower ph values may be used , including values as low as about 4 ). the slurry is aged for about 30 to 60 minutes to assure a uniform mixture . additional adjustments may be made to the ph during or after aging . the pigment is then separated , washed until the oxide has a electrical resistivity of at least 3000 ohms , dewatered , sufficiently dried , collected and micronized . following micronizing , the treated pigment can be used for dispersion into a plastic material , such as a polyolefin material , typically polyethylene . the pigments of the present invention have shown excellent dispersion properties in plastics and do not degrade the lacing resistance properties of the resulting pigmented plastic films . the hydrophobic pigment products of this invention offer processibility in polymer composites as least as good as pigments prepared according to prior art procedures ; that is , the dispersibility of the products of the present invention in polymers is at least as good as prior art pigments and the lacing resistance of the resulting polymer composites containing the products of the present invention is as good as prior art polymer composites . representative polymers in which the products of the present invention may be used include , but are not limited to , polymers of ethylenically unsubstituted monomers , including polyethylene , polypropylene , polybutylene and copolymers of ethylene with alpha - olefins containing 4 to 12 carbon atoms or vinyl acetate ; vinyl homopolymers , acrylic homopolymers and copolymers , polyamides , polycarbonates , polystyrenes , acrylonitrile - butadiene - styrenes , polyethers and the like . the following examples set forth preferred embodiments of the invention . these embodiments are merely illustrative and are not intended to , and should not be construed to , limit the claimed invention in any way . a slurry of tio 2 and water was prepared in the following manner . sufficient standard tio 2 was added to a 150 gallon tank and diluted with water to obtain a tio 2 slurry containing 192 pounds of tio 2 at a concentration of 350 grams / liter . the tank was equipped with two orthogonal 9 ″ bow tie mixers . the slurry was heated to , and maintained at , about 70 ° c . by directly injecting steam . the initial ph of the slurry was about 2 . 5 . next , about 837 . 7 grams of hexyl trichlorosilane ( htcs ) were pumped into the tank over 45 minutes . the htcs was directed onto the slurry surface about midway between the tank center and the outer wall . the ph of the slurry dropped to about 1 . 5 after addition of the htcs . the htcs treated slurry was very fluid and apparently well mixed . the ph of the slurry was adjusted to 7 . 9 with about 1080 ml of a 50 % sodium hydroxide solution . significantly , the slurry viscosity increased noticeably as the ph rose above about 4 . 5 . at a ph of about 7 . 9 , the slurry was mixed well in the center of the tank , but there was virtually no motion in the slurry near the walls of the tank . a brookfield viscosity of a sample of the slurry was about 1200 cps . the slurry was aged at 70 ° c . and a ph of about 7 . 9 with mixing for about 45 minutes . after about 35 minutes of aging at these conditions the viscosity decreased to 400 cps . at the end of the aging period the ph had equilibrated to about 7 . 4 . the ph was readjusted to about 8 . 5 and the slurry further aged for 20 minutes with stirring , still at 70 ° c . the brookfield viscosity measurement at the end of the second aging period was 320 cps . the htcs treated tio 2 slurry was filtered and washed using a rotary vacuum filter . the collected filter cake was oven dried at 110 ° c . for about 12 hours . portions of the dried filter cake were forced through an 8 mesh sieve and steam micronized at 500 ° f . lacing evaluations were conducted by measuring the relative size and number of holes generated in a film sample laid out on a dark surface , and the pigment gave excellent lacing resistance with a rating of 1 . 1 . example 1 was prepared in a manner similar to comparative example 1 except that a dispersion of about 2 . 3 % htcs in aqueous media was first prepared and reacted for approximately 2 . 4 minutes ( see below ) before introducing the resulting dispersion into the tio 2 slurry . as in the comparative example , a suitable tio 2 slurry was added to a 150 gallon tank ( 32 inch diameter ) and diluted to obtain a tio 2 slurry containing 190 pounds of tio 2 at a concentration of 350 grams / liter . the tank was equipped with two orthogonal 9 ″ bow tie mixers , and the slurry was heated to and maintained at 70 ° c . by direct injection of steam . the initial ph of the slurry was about 2 . 5 . hcts was reacted with water in a continuous flow arrangement to form the dispersion . a 2000 ml beaker was equipped with an ultraturrax ® model t - 45 high speed disperser operated at its highest speed . the htcs flow rate was 19 . 2 grams / minute , and the water flow rate was 825 . 4 grams / minutes . this provided a residence time of 2 . 4 minutes . the aqueous dispersion formed from the htcs and water was allowed to overflow into the tank containing the tio 2 slurry in this manner over 43 minutes . the ph of the slurry was about 1 . 6 after addition of the dispersion , and the organically treated slurry was fluid and mixed well . the ph of the slurry was adjusted to 8 . 2 with 1450 ml of 50 % sodium hydroxide solution , in contrast to example 1 , the viscosity did not increase noticeably as the ph was raised above about 4 . 5 as evidenced by the motion of the slurry in the tank . at a ph of 8 . 2 , the brookfield viscosity of a sample of the slurry removed from the tank was measured to be about 470 cps . the slurry was aged at 70 ° c . with mixing for 60 minutes . at the end of the aging period the ph had decreased to about 7 . 8 and the viscosity was measured to be about 500 cps . the organically treated tio 2 slurry was filtered and washed using a rotary vacuum filter . the filter cake was oven dried at 110 ° c . for about 12 hours . portions of the dried filter cake were forced through an 8 mesh sieve and steam micronized at 500 ° f . lacing evaluations were conducted , by measuring the relative size and number of holes generated in a film sample laid out on a dark surface and the product displayed excellent lacing resistance with ratings of 1 . 2 and 1 . 5 determined on two portions of the product . thus , compared to the direct addition of htcs to the tio 2 slurry , addition of the dispersion of htcs and water to the tio 2 slurry yielded a mixture with significantly lower brookfield viscosity , hence , easier processibility . the product was prepared according to the method of example 1 with the exception that 630 . 3 grams of htcs was reacted with water in the continuous flow emulsifier unit such that a 1 . 5 % dispersion was formed , with a 2 . 0 minute residence time , before overflowing into 180 pounds of tio 2 in a 350 grams / liter slurry . brookfield viscosities before and after aging the organically treated slurry were 410 and 500 cps , respectively . the finished product yielded a lacing resistance value of 1 . 1 . the product was prepared according to the method of example 2 except that 125 . 5 grams of 85 % phosphoric acid were added to 203 pounds of tio 2 prior to addition of the dispersion . 552 . 7 grams of htcs were reacted with water in the continuous flow unit to form a 2 . 0 % dispersion , with a 4 . 1 minute residence time , before overflowing into the tio 2 slurry . the ph at the end of the addition period of the htcs / water reaction products was 1 . 6 , and the brookfield viscosity was measured as 470 cps . the ph of the mixture was adjusted to 7 . 8 using 50 % sodium hydroxide and the mixture aged for 60 minutes at 70 ° c . following the 60 minute age , the ph was 7 . 7 and the brookfield viscosity was measured as 490 cps . the ph was adjusted to 8 . 7 using 50 % sodium hydroxide solution , and the product was finished according to example 2 . the finished product gave a lacing resistance value of 1 . 2 . 50 % tio 2 : 50 % polyethylene concentrates were prepared using a haake rheocord 9000 computer controlled torque rheometer . 125 g of tio 2 and 125 g of ldpe 722 manufactured by dow chemical company were dry blended and added to the 75 ° c . preheated chamber with rotors running at 50 rpm . one minute after addition of the tio 2 / ldpe mixture , the chamber temperature was raised to 105 ° c . frictional heat generated by mixing was used to drive the rate of incorporation of the tio 2 into the ldpe until a steady state mixture was achieved . the hot concentrate was removed from the mixing chamber and then placed into a cumberland crusher to obtain finely granulated 50 % concentrate samples . high temperature stability , or lacing resistance , is an important property of inorganic oxides used in polyethylene film applications . lacing is believed to be a measure of concentrate volatility at specific weight percent pigment loadings and processing temperatures . lacing tests were conducted on 50 % tio 2 concentrate samples prepared according to the method described above . the concentrates were conditioned for 48 hours at 23 ° c . and 50 % relative humidity . the concentrates were then let down into the ldpe 722 to achieve a 20 % loading of tio 2 in the final film . lacing evaluations were run on a 1 ″ extruder equipped with a slot die for fabricating cast films . a temperature profile of 625 ° f . die , 515 f clamp ring , 415 ° f . zone 3 , 350 ° f . zone 2 , 300 ° f . zone 1 was used . the screw speed was set at about 90 rpm . a 25 . 4 cm . polished chrome chill roll was used to cool and transport the films and was set to maintain a 75 mm film thickness . the chill roll distance from the die lips was about 22 mm and the temperature was about 27 ° c . after the tio 2 / ldpe mix was placed in the hopper , the material was allowed to run until the appearance of white in the clear film was first noted . to ensure the concentration of tio 2 in the film had stabilized , a two minute time interval was allowed before observations were recorded and a film sample taken . the extruder was then purged with ldpe until the film returned to clear . lacing performance was ranked by counting the relative size and number of holes generated in a film sample laid out on a dark surface . a 1 . 0 - 3 . 0 rating system was used . a rating of 1 was given to films with no lacing , 2 was given to films showing the onset of lacing and 3 was given to films with extreme lacing . increments of 0 . 1 were used to give some indication of relative performance between the samples . upon reading the present disclosure , including the above examples , alternative constructions and embodiments will become obvious to those skilled in the art . these variations are considered to be fully within the scope and spirit of the invention . the subject invention is only limited by the claims which follow and their equivalents .