the binder composition of the present invention is formed by placing a xerogellant , desirably in powder form , in an appropriately sized container and adding sufficient water so that the xerogellant is fully hydrated ( swollen ) to a gel . this step may take up to an hour or more depending upon the xerogellant used . while any material meeting the definition of a xerogellant may be utilized , exemplary xerogellants include sodium carboxymethyl cellulose , derivatives of sodium carboxymethyl cellulose , poly ( acrylic acid ) salts , ( ethylene oxide ), acrylonitrile - grafted starch , hydrolyzed polyacrylonitrile , poly ( vinyl alcohol - sodium acrylate ) and polyisobutylene - co - disodium maleate . one xerogellant is a starch grafted sodium polyacrylate which may be obtained from hoechst celanese corporation under the trade designation sanwet im5000p . once the xerogellant has completely swelled , it is transferred to a blender , for example a waring blender , and mixed at a high speed until it is in a liquified form . those in the art will recognize that it may be necessary to add a small amount of additional water to achieve a liquified state . it is to the liquified xerogellant that the water dispersible polymer , the elastomeric latex emulsion and the plasticizing agent are added . next , the water dispersible polymer , the elastomeric latex emulsion and the plasiticzing agent are added to the liquified xerogellant and all four components are thoroughly mixed at low speed in , for example , a blender . typically additional water is added at this stage to assist in the blending operation . desirably , the water dispersible polymer may be added to the hydrated xerogellant as an aqueous dispersion . while any water dispersible polymer may be utilized , exemplary water dispersible polymers include such polymers chosen from the group including relatively high molecular weight amorphous polyesters that disperse directly in water without the assistance of organic cosolvents , suractants , or amines . this water dispersibiity is attributable , in large part , to the presence of ionic substituents attached to the polymer chain , illustrated below . ## str1 ## a = an aromatic dicarboxylic acid moiety g = an aliphatic or cycloaliphatic glycol residue while only two of the aromatic dicarboxylic acid moieties shown above have sodiosuifo ( so 3 - na + ) substituents , on the average , there are five to eight ionic sodiosulfo substituents per molecule . this type of polymer is available form the eastman kodak co . of rochester , n . y . under the trade designation eastman aq . in particular , eastman aq 55d and aq 38d . the &# 34 ; d &# 34 ; represents the fact that the polymer is in a dispersed form . the number refers to the dry glass transition temperature , in degrees centigrade , of the polymer . alternatively , the water dispersible polymer may be selected from the group including acrylic polymers , polyoxides , vinyl polymers , cellulose derivatives , starch derivatives , polysaccahrides , proteins and copolymers thereof . while any suitable elastomeric latex emulsion may be utilized , exemplary elastomeric latex emulsions may be obtained from the b . f . goodrich co ., specialty polymers & amp ; chemicals division under the trade designation hystretch , for example hystretch v - 60 . hystretch v - 60 elastomeric latex emulsions typically are a blend of about 50 % latex , about 50 % water , less than about 0 . 01 % acrylamide , less than about 1 . 0 % ammonium hydroxide , less than about 0 . 01 % ethyl acrylate , less than about 0 . 1 % formaldehyde and less than about 0 . 0025 % n - methylolacrylamide . u . s . pat . no . 5 , 056 , 960 to marienfeld has described hystretch v - 60 as an aqueous dispersion based on an elastomeric , fully saturated , acrylic terpolymer . while any suitable plasticizing agent may be utilized , exemplary plasticizing agents include glycerin , sorbitol , glucidol , sucrose , ethylene glycol , propylene glycol , diethylene glycol , polyethylene glycol , acid amides , dimethyl acetamide , dimethyl sulfoxide , methyl pyrrolidene and tetramethylene suifone . one exemplary plasticizing agent is glycerin which may be obtained from fischer scientific of fairtown , n . j ., under the trade designation g - 33 - 1 . the resultant binder composition contains : ( 1 ) from about 10 to about 40 weight percent of the water dispersible polymer ; ( 2 ) from about 10 to about 40 weight percent of the elastomeric latex emulsion ; ( 3 ) from about 20 to about 40 weight percent of the xerogellant ; and ( 4 ) from about 5 to about 20 weight percent of the plasticizing agent in an aqueous solution . for example , the resultant binder composition may contain : ( 1 ) from about 20 to about 40 weight percent of the water dispersible polymer ; ( 2 ) from about 20 to about 40 weight percent of the elastomeric latex emulsion ; ( 3 ) from about 20 to about 40 weight percent of the xerogellant ; and ( 4 ) from about 10 to about 20 weight percent of the plasticizing agent in an aqueous solution . more particularly , the resultant binder composition may contain : ( 1 ) from about 20 to about 35 weight percent of the water dispersible polymer ; ( 2 ) from about 20 to about 35 weight percent of the elastomeric latex emulsion ; ( 3 ) from about 20 to about 35 weight percent of the xerogellant ; and ( 4 ) from about 10 to about 15 weight percent of the plasticizing agent in an aqueous solution . even more particularly , the resultant binder composition may contain : ( 1 ) from about 25 to about 30 weight percent of the water dispersible polymer ; ( 2 ) from about 25 to about 30 weight percent of the elastomeric latex emulsion ; ( 3 ) from about 25 to about 30 weight percent of the xerogellant ; and ( 4 ) from about 10 to about 15 weight percent of the plasticizing agent in an aqueous solution . as will be discussed in more detail hereinafter , the binder composition may be applied by either spraying processes or dipping processes . generally speaking , the percent of the four components in the aqueous solution should be tailored to the application process which is to be utilized . for example , when it is desired to apply the binder composition by dipping , the percent of the four components in solution is usually greater than 1 percent . more particularly , the percent of the four components in solution may be greater than 1 . 1 percent . even more particularly , the percent of the four components in solution may be greater than 1 . 25 percent if the binder composition is to be applied by dipping . yet even more particularly , the percent of the four components in solution may be greater than 2 percent if the binder composition is to be applied by dipping . if the binder composition is to be applied by spraying processes , the percent of the four components in solution may be less than 1 percent . for example , the percent of the four components in solution may be less than 0 . 50 percent if the binder composition is to be applied by spraying . even more particularly , the percent of the four components in solution may be less than 0 . 25 percent if the binder composition is to be applied by spraying . once the binder composition has been formulated as described above it is transferred to an appropriate spraying mechanism or dipping trough , depending upon the method of application of the composition . at this point a coherent wet - laid or dry - laid ( air - laid ) fibrous web prepared by conventional methods is provided . these webs are coherent in that they are self - supporting and may be relatively easily handled so long as they are handled with care . moreover , these conventional webs will disintegrate or fall apart when placed in water and aggitated . however , these conventional webs have very low tensile strength and will readily tear apart . application of the binder by either the spraying or dipping process is then carried out in conventional manner . once the wet - laid or dry ( air ) laid web has had the binder applied it is allowed to dry in conventional manner . once dry , the coherent webs exhibit improved tensile strength when compared to the tensile strength of the untreated wet - laid or dry - laid webs . for example , the tensile strength of the fibrous web may be increased by at least 25 percent as compared to the tensile strength of the untreated web not containing the binder . more particularly , the tensile strength of the fibrous web may be increase by at least 100 percent as compared to the tensile strength of the untreated web not containing the binder . even more particularly , the tensile strength of the fibrous web may be increased by at least 500 percent as compared to the tensile strength of the untreated web not containing the binder . yet even more particularly , the tensile strength of the fibrous web may be increase by at least 1 , 000 percent as compared to the tensile strength of the untreated web not containing the binder . a desirable feature of the present invention is that the improvement in tensile strength is effected where the amount of binder present , &# 34 ; add - on &# 34 ;, in the resultant hydrodisintegratable fibrous web represents only a small portion , by weight , of the entire web . for example , the binder componets typically are from about 0 . 20 to about 15 percent , by weight , of the dry web . more particularly , the binder components may be from about 0 . 20 to about 10 percent , by weight , of the dry web . even more particularly , the binder components may be from about 0 . 30 to about 5 percent , by weight , of the web . importantly , the resultant coherent fibrous webs have the ability to rapidly &# 34 ; fall apart &# 34 ; or disintegrate when placed in water and aggitated . thus , this material may be effectively utilized in disposable products which may be placed in a toilet and flushed away . in some embodiments it may be desirable to employ various additives such as antioxidants , antistatic agents , blowing agents , compatibilizers , flame retardants , heat stabilizers , impact modifiers , lubricants , ultraviolet stabilizers , processing aids , surfactants , dispersants , slip agents , etc ., as fabricating agents or as modifiers depending on the specific properties which would be desirable to have in the final product . the use of surfactants can further enhance the rate of hydrodisintegration of the coherent fibrous web . exemplary surfactants which can be utilized in the invention are ( 1 ) anionic surfactants such as carboxylic acids and salts , sulfonic acids and salts , sulfuric acid esters and salts , phosphoric and polyphosphoric acid esters and salts ; ( 2 ) non - ionic surfactants such as ethoxylated alcohols , ethoxylated alhylphenols , ethoxylated carboxylic esters and ethoxylated carboxylic amides ; ( 3 ) cationic surfactants such as oxygen free amines , oxygen containing amines , amide linked amines and quaternary ammonium salts ; and ( 4 ) amphoteric surfactants such as imidazolinium derivatives , amino acids and their derivatives in which the nitrogen atom is protonated and alkylketaimes . the surfactants may be added so that they form from at least about 0 . 01 to about 0 . 10 weight percent of the coherent fibrous web . for example , the surfactants may form from at least about 0 . 03 to about 0 . 08 weight percent of the coherent fibrous web . more particularly , the surfactants may form from at least about 0 . 05 to about 0 . 06 weight percent of the coherent fibrous web . those of skill in the art will readily recognize that the hydrodisintegratable coherent web may be formed by other methods . the invention will now be described with respect to certain specific embodiments thereof . three binder compositions were prepared in accordance with the present invention . one to be applied by spraying on wet - laid webs , one to be applied to wet - laid webs by dipping and one to be applied onto air - laid webs by dipping . for the spraying application , about 0 . 1 gram of xerogellant , sanwet im5000p , was added to a 100 milliliter beaker with 80 milliliters of water . the xerogellant was allowed to swell ( hydrate ) for about one ( 1 ) hour . thereafter , the hydrated xerogellant was transferred to a waring blender 7011 model 31bl92 and mixed at high speed for about one ( 1 ) minute until the gel was liquified . at this point seventy ( 70 ) additional milliliters of water , 0 . 4 grams of water dispersible polymer ( aq55d ), 0 . 225 grams of elastomeric latex emuslion ( hystretch v - 60 ) and 0 . 045 grams of plasticizing agent ( glycerin ) were added . because the aq55d is only 25 % solids , only 0 . 1 gram of these solids were actually added . because the hystretch v - 60 is only 50 % solids , only 0 . 11 gram of these solids were actually added . thus , the resultant binder composition had 0 . 355 grams of total solids in 150 milliliters of water . this is a 0 . 24 % solution . for the dipping of wet - laid webs application , about 1 gram of xerogellant , sanwet im5000p , was added to a 100 milliliter beaker with 80 milliliters of water . the xerogellant was allowed to swell ( hydrate ) for about one ( 1 ) hour . thereafter , the hydrated xerogellant was transferred to a waring blender 7011 model 31bl92 and mixed at high speed for about one ( 1 ) minute until the gel was liquified . at this point one hundred and seventy ( 170 ) additional milliliters of water , 4 grams of water dispersible polymer ( aq55d ), 2 grams of elastomeric latex emuslion ( hystretch v - 60 ) and 0 . 45 gram of plasticizing agent ( glycerin ) were added . because the aq55d is only 25 % solids , only 1 gram of these solids were actually added . because the hystretch v - 60 is only 50 % solids , only 1 gram of these solids were actually added . thus , the resultant binder composition had 3 . 45 grams of total solids in 250 milliliters of water . this is a 1 . 38 % solution . for the dipping of air - laid webs application , about 0 . 5 gram of xerogellant , sanwet im5000p , was added to a 100 milliliter beaker with 80 milliliters of water . the xerogellant was allowed to swell ( hydrate ) for about one ( 1 ) hour . thereafter , the hydrated xerogellant was transferred to a waring blender 7011 model 31bl92 and mixed at high speed for about one ( 1 ) minute until the gel was liquified . at this point eighty ( 80 ) additional milliliters of water , 2 grams of water dispersible polymer ( aq55d ), 1 gram of elastomeric latex emuslion ( hystretch v - 60 ) and 0 . 225 gram of plasticizing agent ( glycerin ) were added . because the aq55d is only 25 % solids , only 0 . 5 gram of these solids were actually added . because the hystretch v - 60 is only 50 % solids , only 0 . 5 gram of these solids were actually added . thus , the resultant binder composition had 1 . 724 grams of total solids in 160 milliliters of water . this is a 1 . 1 % solution . in each case the entire solution was mixed on low speed in the blender for about thirty ( 30 ) seconds . in the spraying application the resultant solution was transferred to a small amber bottle attached to a chromist ( trademark ) sprayer model number 51901 sold by gelman sciences of ann arbor , mich . for spray application . in the dipping applications , the resultant solution was poured into a pyrex dish and covered until the samples were treated . the wet - laid webs used in these experiments were generally composed of three ( 3 ) denier , one - half inch length polyester obtained from mini fibers corp . of johnson , tex . and abaca pulp . more specifically , about 60 %, by weight , polyester , about 40 %, by weight , abaca pulp and about 0 . 125 %, by weight , of a wet strength resing ( parez nc631 ) obtained from american cyanamid corp . of wayne n . j . these webs were manufactured by the kimberly - clark corp at its lee mill in lee mass . their basis weight was approximately 27 grams per square meter . the air - laid webs used in these experiments were generally composed of 100 % polyester fibers obtained from the mini fiber corp . of johnson , tex . with a polyvinyl alcohol binder . the pvoh binder represented about 0 . 5 %, by weight , add - on of the webs . the binder is available under the trade designation grade 523 airvol from air products & amp ; chemicals , inc . of allentown , pa . more specifically , the polyester fibers had an average denier of three ( 3 ) and an average lenght of one - half ( 1 / 2 ) inch . the webs were made at clemson univ ., clemson s . c . on rando web air laying equipment . their basis weight was approximately 45 grams per square meter . samples of the webs to have binder applied in accordance with the present invention were cut to three ( 3 ) inch by seven ( 7 ) size . each sample was weighed before binder application and after the binder had been applied and the web dried . drying was accomplished by hand blotting and the sample being hung in a hood at ambient temperature overnight . if the binder application was accomplished by dipping the airlaid webs were supported by a screen during the actual dipping phase . in the case of spraying , the webs were sprayed directly . the dried webs were tested for machine direction ( md ) tensile strength using an instron materials testing machine model number 1122 . the guage length was set at three ( 3 ) inches and the cross head speed was twelve 12 inches per minute . peak load was recorded for each sample tested , including the control webs . percent increase in strength was calculated as : ( treated tensile strength -- control tensile strength divided by control tensile strength ) times 100 . the results of these examples are recorded in table i , below . table i__________________________________________________________________________ binder percent control treated increasesample type of conc . add on tensile tensile in strengthweb application ( percent ) ( by wt .) ( grams ) ( grams ) ( percent ) __________________________________________________________________________wetlaid spray . 24 0 . 30 1295 1755 35 . 52wetlaid spray . 24 1 . 30 1295 2506 93 . 51wetlaid spray . 24 1 . 60 1295 2983 130 . 35wetlaid spray . 24 1 . 90 1295 2019 55 . 91wetlaid dip saturation 1 . 38 4 . 90 1295 3293 154 . 29wetlaid dip saturation 1 . 38 5 . 10 1295 5314 310 . 35wetlaid dip saturation 1 . 38 5 . 90 1295 5763 345 . 02wetlaid dip saturation 1 . 38 9 . 90 1295 6860 429 . 73wetlaid dip saturation 1 . 38 7 . 50 1295 5243 304 . 86airlaid dip saturation 1 . 10 6 . 90 160 . 8 1825 1034 . 95airlaid dip saturation 1 . 10 7 . 50 160 . 8 1461 808 . 58airlaid dip saturation 1 . 10 2 . 20 160 . 8 1340 733 . 33airlaid dip saturation 1 . 10 13 . 50 160 . 8 2047 1173 . 01__________________________________________________________________________ all of the samples were also subjected to the shake test as defined above . all of the samples formed in accordance with the present invention , fell apart into generally individual fibers in less than thirty ( 30 ) seconds . while the control samples had accomplished this objective in about ten ( 10 ) seconds , the significant improvement in tensile strength of the samples of the present invention as compared to that of the control samples allows the samples of the present invention to be utilized in commercial applications . moreover , the fact that the samples of the present invention had fallen apart in under thirty seconds is believed to make them suitable for use in products which may be flushed down the toilet . it is to be understood that variations and modifications of the present invention may be made without departing from the scope of the invention . it is also to be understood that the scope of the present invention is not to be interpreted as limited to the specific embodiments disclosed herein , but only in accordance , with the appended claims when read in light of the foregoing disclosure .