the invention relates to a latex polymer which acts in a resin formulation between an unsaturated polymer matrix and a reinforcing substrate . the term &# 34 ; polymer &# 34 ; is used broadly herein to mean either a copolymer or an overpolymer or a shell / core polymer . this polymer is made from 0 to 30 percent , and preferably 15 to 28 percent , and most preferably 20 to 25 percent styrene ; 55 to 97 percent , and preferably 65 to 80 percent , and most preferably 69 to 78 percent butadiene ; and 1 to 15 percent , and preferably 2 to 12 percent , and most preferably 3 to 10 percent by weight of an amine substituted alkyl acrylate , all percentages , based on the total weight of the monomers . if the polymer is a shell / core polymer , the shell is a copolymer of the amine substituted alkyl acrylate with the sbr . it is preferred that the amine substituted alkyl acrylate is present in at least 6 percent , and preferably at least about 3 percent of the monomer composition . the amine substituted alkyl acrylate has a general formula i ## str3 ## wherein r 1 is hydrogen , or alkyl having 1 to 4 carbon atoms , and preferably r 1 is hydrogen or methyl , and most preferably r 1 is methyl ; r 2 is an alkyl having from 1 to 8 carbon atoms , and preferably 2 to 4 carbon atoms , and r 3 and r 4 are the same or different and are hydrogen , aliphatic having 1 to 8 carbon atoms , or aromatic or aliphatic substituted aromatic having 6 to 8 carbon atoms , or together with the nitrogen are heterocyclic having 3 to 8 carbon atoms , or oxygen sulfur , and / or halogen derivatives of the same ; and preferably r 3 and r 4 are hydrogen or aliphatic having 1 to 4 carbon atoms where one may be hydrogen but not both ; and most preferably r 3 and r 4 are both ethyl , or r 3 is butyl and r 4 is hydrogen . methacrylate amino esters are preferred over acrylate amino esters , because they exhibit more favorable , higher combining ratios during copolymerization . increasing the number of carbon atoms in the groups attached to the nitrogen atom of the acrylic esters serves to decrease the rate of hydrolysis of the ester , especially in alkaline media . this is believed to be an advantage in the invention as practiced . specific examples of preferred acrylates include diethyl amino ethyl methacrylate , and monobutyl amino ethyl methacrylate . the polymers are latex polymers produced by emulsion polymerization when the random copolymer is produced , all monomers are charged at the same time to the reactor . when the shell - core polymer is produced , polymerization is first initiated with only the styrene and butadiene ; then the amine substituted alkyl acrylate is added at from about 32 to about 97 percent conversion of the core polymer and preferably from about 45 to about 60 percent conversion . suitable polymerization surfactants could be anionic surfactants including , for example , potassium oleate and sodium lauryl sulfate . nonionic and cationic surfactants as are known in the art could also be used . free radical catalysts such as an alkanoyl , aroyl , alkaroyl , or an aralkanoyl diperoxide , a monohydroperoxide , or an azo compound , a peroxy ester , a percarbonate , a persulfate , or any other suitable free radical - type initiator are used in an amount of from about 0 . 03 to about 0 . 3 parts per hundred parts monomer . examples of specific initiators include potassium persulfate , sodium persulfate , ammonium persulfate , benzoyl peroxide , lauroyl peroxide , diacetyl peroxide , cumene hydroperoxide , methyl ethyl ketone peroxide , diisopropylbenzene hydroperoxide , 2 , 4 - dichlorobenzoyl peroxide , naphthoyl peroxide , t - butyl perbenzoate , di - t - butyl perphthalate , isopropyl percarbonate , acetyl cyclohexane sulfonyl peroxide , disecondary butyl peroxydicarbonate , t - butyl peroxyneodecanoate , dinormal propyl peroxydicarbonate , azo - bisisobutyronitrile , alpha , alpha &# 39 ;- azodiisobutyrate , 2 , 2 &# 39 ; azo - bis -( 2 , 4 - dimethyl valeronitrile ), paramethane hydroperoxide , 4 - pinane hydroperoxide , and the like . initiation may also be by uv or other radiation . the polymerization is generally run in a 1000 - 3500 gallon batch reactor at a temperature of about 10 ° c . to about 50 ° c . and a pressure of about 50 psi to about 60 psi to about 100 percent conversion . optimally , the polymerization product is a latex having a particle size of about 40 to about 140 nm , and preferably 80 to about 130 nm . the polymer is usually at a concentration of about 40 percent in the latex . the resin / latex adhesive is prepared by mixing the adhesion promoting latex with a resin . in the preferred case , the resin is a resorcinol formaldehyde ( rf ) resin . it is believed that the latex polymer of the present invention will be effective in promoting adhesion in any resin formulation wherein styrene / butadiene / vinyl pyridine has been effective in promoting adhesion . examples of other such suitable resins include acrylic polymers , phenol polysulfide polymers and copolymers from formaldehyde and hydroxy benzenes such as xylenols and cresols . the dry solids ratio of latex polymer to resorcinol - formaldehyde ( l / rf ratio ) is from about 1 to about 10 , and preferably from about 1 to about 7 , and most preferably from about 2 to about 5 . the most preferable latex / resin ratio may vary depending on the reinforcing substrate , the resin , and the unsaturated polymer matrix to which it must be adhered . the reinforcing substrate is dipped into the resin / latex adhesive and the excess is removed . the coated substrate is dried , and then cured at 150 ° c . to about 250 ° c ., and preferably from about 175 ° to about 230 ° c . for 30 seconds to 10 minutes , depending on the temperature , and preferably from about 1 to about 4 minutes . the treated substrate is then embedded into the unsaturated polymer which already contains curing agents , etc . this composite is then cured under pressure at a temperature of from about 100 ° to about 200 ° c ., and preferably from about 130 ° to about 180 ° c . for 10 to about 30 minutes , depending on the temperature , and the thickness of the composite . suitable substrates include cords , fibers and textiles made of cotton , rayon , silk , wool , polyester such as poly ( ethylene terephthalate ), aliphatic and aromatic polyamides such as nylon 66 and poly ( phenylene terephthalamide ), carbon , glass and steel . as is well known , some of the reinforcing substrates give best results if pretreated , before coating with the resinlatex composition of this invention , e . g ., poly ( ethylene terephthalate ) &# 34 ; polyester &# 34 ;, i . e ., fibers treated with a polyisocyanate as taught in u . s . pat . nos . 3 , 307 , 966 and 3 , 226 , 276 which are incorporated herein by reference as if fully set forth herein . examples of preferred substrates include those commonly used to reinforce rubber such as rayon , nylon , polyester , glass , and &# 34 ; kevlar &# 34 ; ( a poly ( phenylene terephthalamide ) sold by du pont de nemours , inc .) the unsaturated polymer matrices include , for example , polymers made from butadiene , styrene , isoprene , isobutylene , acrylonitrile , ethylene / propylene , chloroprene , derivatives of the same , and other such polymers . the resin latex formulation promotes adhesion between the substrate and an unsaturated polymer matrix . by &# 34 ; unsaturated polymer &# 34 ; in this instance it is meant a polymer having unsaturation in the backbone or pendant groups and not aromaticity . this is most generally olefinic unsaturation . it is believed that the adhesion promoter of the present invention is broadly applicable for use with all sorts of polymers having olefinic unsaturation . examples of specifically preferred unsaturated polymers include styrene / butadiene , natural rubber or polyisoprene , polychloroprene , butadiene / isobutylene copolymer , and ethylene / propylene / butadiene terpolymers . the adhesion promoter of the present invention results in excellent adhesion as measured by astm test d - 2138 . in this test , adhesive failure can occur at two interfaces : between the substrate and the rfl , and between the rfl and the elastomeric matrix . in addition , cohesive failure may occur in the substrate , the rfl or the elastomeric matrix . traditionally , by excellent adhesion , it is meant not only that the failure load is high but also that primary failure does not occur at either interface nor does it occur cohesively in the rfl . in such a situation then , interfacial bond strengths as well as the cohesive strength of the rfl are greater than the cohesive strengths of either the substrate or the elastomeric matrix . in all these examples , failure in the astm d2138 test occurred primarily within the elastomeric matrix . this means that adhesion between the elastomer matrix and the rfl , adhesion between the textile substrate and the rfl , and the cohesive strength of the rfl are all greater than the measured and reported adhesion value . the invention will be better understood by reference to the following examples . a random terpolymer of butadiene , styrene , and diethylaminoethylmethacrylate ( deam ) was prepared using the recipe in table i . table i______________________________________ingredient parts______________________________________butadiene 70 . 0styrene 20 . 0deam 10 . 0potassium oleate 5 . 0potassium hydroxide 0 . 05trisodium phosphate ( na . sub . 3 po . sub . 4 . 12h . sub . 2 o ) 0 . 5sodium bicarbonate 0 . 2sodium hydrosulfite ( na . sub . 2 s . sub . 2 o . sub . 4 ) 0 . 1dispersing agent 1 . 5t - dodecyl mercaptan 0 . 36sodium persulfate 0 . 35water 140 . 00______________________________________ aqueous stock solutions were prepared with one or more of the following ingredients : potassium oleate , potassium hydroxide , trisodium phosphate , sodium bicarbonate , sodium hydrosulfite , and sodium persulfate . all stock solutions and the water were purged with dry nitrogen gas before use . potassium oleate , potassium hydroxide , trisodium phosphate , sodium bicarbonate , dispersing agent , some distilled water , styrene and deam were all charged into the batch reactor . the reactor was sealed and the butadiene gas was introduced . sodium hydrosulfite was added and the reactor was introduced into a constant temperature water bath at 50 ° c . and the contents were continuously stirred . after 10 minutes , t - dodecyl mercaptan was added , and 30 minutes later , sodium persulfate was added . after about 30 hours , 90 percent or more of the monomers had been converted to polymer . the reactor was removed from the bath and the contents ( sbr - deam latex ) were removed . a butadiene - styrene - vinylpyridine ( sbr - vp ) latex was prepared using the recipe in table i , except that 2 - vinylpyridine ( vp ) was substituted for deam . rfl formulations were prepared with sbr - deam and sbr - vp latices using the formulation in table ii . table ii______________________________________ wet dry______________________________________part aresorcinol - formaldehyde resin ( 70 %) 14 . 24 9 . 97ammonia ( 28 %) 28 . 94 -- sodium hydroxide 0 . 28 0 . 28acrylic latex ( 37 %) 29 . 05 10 . 75water 145 . 53 -- part blatex ( 41 %) ( sbr - deam or sbr - vp ) 166 . 66 68 . 33natural rubber latex ( 62 %) 12 . 35 7 . 66water 48 . 51 -- part cformalin ( 37 %) 8 . 14 3 . 01water 31 . 41 -- total 485 . 11 100 . 00______________________________________ part a was first prepared . although commercial resorcinol - formaldehyde ( rf ) resin was used in this case , it is well known that rf resin can be prepared in - situ by reacting resorcinol with formaldehyde . the use of the acrylic latex , to protect the sbr type latex from environmental attack , has been documented by solomon in u . s . pat . no . 3 , 968 , 295 which is incorporated herein by reference as if set forth herein . part b was then prepared . the addition of natural rubber latex to the formulation is not necessary for rfls prepared from sbr - deam to act as effective adhesion promoters . part a was then added to part b and was well mixed . part c was prepared and was added to the mixture of parts a and b . the rfl was then used within 24 hours . rfl - a was prepared using the formulation in table ii . rfl - b was prepared in a similar way to rfl - a but without the acrylic or the natural rubber latices . as is well known in the art , textiles made with poly ( ethylene terephthalate ) ( pet ) fibers have to be treated with an ie coating prior to rfl treatment . the ie formulation in table iii was used for this purpose . table iii______________________________________ingredient parts______________________________________phenol - blocked methylene bis ( phenyliso - 3 . 56cyanate ) adduct of glycerol and epichlorohydrin 1 . 34anionic surfactant 0 . 10water 95 . 00______________________________________ nylon 6 , 6 ( 840 / 2 denier ) tire cords were dipped into a bath containing the rfl - a mixture , the excess rfl was removed , and the cords were dried for 2 minutes at 150 ° c . the dried cords were then baked for 1 minute at 220 ° c . rayon ( 1650 / 3 denier ) tire cords were treated with the rfl - b mixture using the above procedure . pet ( 1000 / 2 denier ) cords were first dipped into the ei mixture , the excess mixture was removed , and the cords were dried for 2 minutes at 150 ° c . the dried cords were than baked for 1 minute at 240 ° c . they were then treated with the rfl mixture as outlined above . the following unsaturated polymer matrices were used for the preparation of h - adhesion test samples . these polymer compounds are typical of those used in tires and other industrial rubber products . ______________________________________ingredient parts______________________________________compound anatural rubber 60 . 00styrene - butadiene rubber 40 . 00zinc oxide 2 . 00stearic acid 0 . 75oil 15 . 75carbon black 60 . 00phenol formaldehyde resin 2 . 50morpholinothiobenzothiazole sulfenamide 0 . 90sulfur 2 . 71compound bnatural rubber 60 . 00styrene - butadiene rubber 20 . 00cis - polybutadiene 20 . 00zinc oxide 2 . 00stearic acid 1 . 50oil 10 . 00carbon black 55 . 00morpholinothiobenzothiazole sulfenamide 1 . 00sulfur 3 . 56______________________________________ h - adhesion test samples were prepared and tested according to astm d - 2138 . the results obtained are shown in table iv . table iv______________________________________ adhesionfiber cord rfl polymer latex mean ± polymer denier type compound type std . dev . ______________________________________rayon 1650 / 3 b compound sbr - vp 34 . 3 ± 1 . 3 arayon 1650 / 3 b compound sbr - deam 31 . 2 ± 1 . 6 anylon 840 / 2 a compound sbr - vp 33 . 8 ± 3 . 2 bnylon 840 / 2 a compound sbr - deam 33 . 6 ± 1 . 5 bpet 1000 / 2 a compound sbr - vp 31 . 5 ± 2 . 6 apet 1000 / 2 a compound sbr - deam 29 . 6 ± 2 . 7 a______________________________________ these results show that sbr - deam latex , in an rfl formulation , provides excellent adhesion between typical tire reinforcement materials and unsaturated polymer compounds . the level of adhesion is comparable to that obtained with the sbr - vp latex that is typically used today . a terpolymer of butadiene , styrene , and diethylaminoethylmethacrylate ( deam ) was prepared using the recipe in table v . table v______________________________________ingredient parts______________________________________butadiene 70 . 0styrene 20 . 0deam 10 . 0surfactant a 3 . 0surfactant b 2 . 0potassium hydroxide 0 . 05trisodium phosphate 0 . 5sodium bicarbonate 0 . 2sodium hydrosulfite 0 . 1dispersing agent 1 . 5t - dodecyl mercaptan 0 . 36sodium persulfate 0 . 35water 132 . 00______________________________________ this recipe is similar to that in table i except that potassium oleate has been replaced by surfactant a . surfactant a is an ammonium salt of sulfated nonylphenoxy poly ( ethyleneoxy ) ethanol . this formulation uses an additional surfactant -- surfactant b , which is ammoniumlauryl sarcosinate . the polymerization procedure is almost exactly the one described in example 1 . the only difference is that surfactant b is added during polymerization in two steps : one - half the quantity at about 8 percent conversion and the other half after reaction is almost complete ( greater than 95 percent conversion ). an rfl ( rfl - c ) was prepared using a formulation similar to that in table ii in example 1 , the only difference being that the only latex used was either sbrdeam or sbr - vp . in other words , the amount of natural rubber solids in the formulation shown in table ii in example 1 was replaced with either sbr - deam solids or sbr - vp solids , depending on which latex was being used in the formulation . the sbr - vp used in this experiment was manufactured by the bfgoodrich company and is sold under the brand name goodrite 2528 × 10 . 1260 / 2 nylon 6 , 6 tire cords were treated with rfl - c and embedded in compound b . 1000 / 2 denier pet tire cords were treated with ie and rfl - c mixtures and embedded in compound a . the procedures are described in example 1 . table vi shows the results of the h - adhesion test ( astm d - 2138 ). table vi______________________________________ adhesionfiber cord rfl polymer latex mean ± polymer denier type compound type std . dev . ______________________________________pet 1000 / 2 c compound sbr - vp 25 . 3 ± 1 . 7 apet 1000 / 2 c compound sbr - deam 27 . 6 ± 2 . 1 anylon 1260 / 2 c compound sbr - vp 38 . 5 ± 2 . 4 bnylon 1260 / 2 c compound sbr - deam 34 . 4 ± 1 . 5 b______________________________________ these results again indicate that adhesion obtained with sbr - deam latex in an rfl formulation is comparable to that obtained with commercially available sbr - vp latex . a core - shell sbr - deam latex was prepared using the formulation in table v . the core - shell structure was created by initially introducing only 2 . 5 parts of deam into the reactor . the rest ( 7 . 5 parts ) was added at about 70 percent conversion . in this case , the core and the shell are composed of sbr - deam polymer ; the concentration of deam in the shell is much greater than that in the core . preparation of the rfl , treatment of 1600 / 2 pet tire cord , adhesion sample preparation and testing were all the same as in example 2 . the adhesion results obtained are shown in table vii . table vii______________________________________ adhesionfiber cord rfl polymer latex mean ± polymer denier type compound type std . dev . ______________________________________pet 1600 / 2 c compound sbr - vp 32 . 9 ± 2 . 8 apet 1600 / 2 c compound sbr - deam 29 . 7 ± 1 . 3 a______________________________________ these results indicate that adhesion obtained with core - shell sbr - deam latex , in an rfl formulation is also comparable to that obtained with sbr - vp latex . a core - shell sbr - deam latex was prepared using a formulation similar to that in table v ; the only exceptions were that the levels of butadiene and deam were 72 . 0 and 3 . 69 parts respectively . the core - shell structure was created by introducing all of the deam into the reactor at 49 percent conversion . thus , the resulting latex particles are expected to contain a core of sbr polymer which is covered with a shell of sbr - deam polymer . preparation of the rfl , treatment of 1600 / 2 pet tire cord , adhesion sample preparation and testing were all the same as in example 2 . the adhesion results obtained are shown in table viii . table viii______________________________________ adhesionfiber cord rfl polymer latex mean ± polymer denier type compound type std . dev . ______________________________________pet 1600 / 2 c compound sbr - vp 32 . 9 ± 2 . 8 apet 1600 / 2 c compound sbr - deam 30 . 9 ± 3 . 0 a______________________________________ these results indicate that adhesion obtained with core - shell sbr - deam latex , which contains only about 3 . 8 percent deam in the polymer is also comparable to that obtained with commercially available sbr - vp latex . while in accordance with the patent statutes , the best mode and preferred embodiment has been set forth , the scope of the invention is not limited thereto , but rather by the scope of the attached claims .