rubber mixtures according to the present invention may obviously also contain known rubber fillers and rubber auxiliary substances as well as crosslinkers . constituent ( a ) in rubber mixtures according to the present invention are double bond - containing rubbers which are called r rubbers according to din / iso 1629 . these rubbers have a double bond in the main chain . the following , for example , are included among these : nr : natural rubber ir : polyisoprene sbr : styrene / butadiene rubber br : polybutadiene rubber sibr : styrene / isoprene / butadiene rubber nbr : nitrile rubber iir : butyl rubber biir : brominated isobutylene / isoprene copolymers with bromine contents of 0 . 1 - 10 wt . % ciir : chlorinated isobutylene / isoprene copolymers with chlorine ontents of 0 . 1 - 10 wt . % hnbr : hydrogenated or partially hydrogenated nitrile rubber snbr : styrene / butadiene / acrylonitrile rubber cr : polychloroprene enr : epoxidized natural rubbers or mixtures thereof x - nbr : carboxylated nitrile rubber x - sbr : carboxylated styrene / butadiene copolymers . however , double bond - containing rubbers are also understood to be those rubbers which are called m rubbers according to din / iso 1629 and have , apart from a saturated main chain , double bonds in the side chains . epdm , for example , is included here . double bond - containing rubbers of the types mentioned above to be used in rubber mixtures according to the present invention may obviously be modified by those functional groups which react with zinc peroxide and which enable improvement of the linkage of crosslinked rubber particles to the surrounding rubber matrix in the vulcanized state . preferred uncrosstinked rubbers are those which are functionalized by hydroxyl , carboxyl , amino , amide and / or epoxide groups . the introduction of functional groups may take place directly during polymerization , by copolymerization with suitable comonomers , or after polymerization by polymer modification . the introduction of such functional groups by polymer modification is known and is described , for example , in m . l . hallensleben “ chemisch modifizierte polymere ” in houben - weyl methoden der organischen chemie , 4th edition , “ makromolekulare stoffe ”, part 1 - 3 ; georg thieme verlag stuttgart , new york , 1987 ; p . 1994 - 2024 , de - a 2 653 144 , ep - a 464 478 , ep - a 806 452 and de - a 198 32 459 . 6 . the amount of functional groups in the rubbers is generally 0 . 05 to 25 wt . %, preferably 0 . 1 to 10 wt . %. constituent ( b ) in rubber mixtures according to the present invention are crosslinked rubber particles , so - called rubber gels or microgels , which are obtained by appropriate crosslinking of the following rubbers : nr : natural rubber , br : polybutadiene , abr : butadiene / c 1 - 4 alkyl acrylate copolymers , ir : polyisoprene , sbr : tyrene / butadiene copolymers with styrene contents of 1 - 60 , preferably 5 - 50 wt . %, sibr : styrene / isoprene / butadiene rubber , x - sbr : carboxylated styrene / butadiene copolymers , fkm : fluorinated rubbers , acm : acrylate rubbers , nbr : olybutadiene / acrylonitrile copolymers with acrylonitrile contents of - 60 , preferably 10 - 50 wt . %, x - nbr : arboxylated nitrile rubbers , enr : poxidized natural rubber , cr : olychloroprene , iir : obutylene / isoprene copolymers with isoprene contents of 0 . 5 - 10 wt . %, biir : brominated isobutylene / isoprene copolymers with bromine contents of 0 . 1 - 10 wt . %, ciir : hlorinated isobutylene / isoprene copolymers with chlorine contents of 0 . 1 - 10 wt . %, hnbr : partially and fully hydrogenated nitrile rubbers , epm : ethylene / propylene copolymers , epdm : ethylene / propylene / diene terpolymers , eam : ethylene / acrylate copolymers , evm : ethylene / vinylacetate copolymers , co and eco : epichlorhydrin rubbers , q : silicone rubbers , au : polyesterurethane polymers , eu : polyetherurethane polymers . rubber particles to be used according to the present invention normally have particle diameters of 5 to 1000 nm , preferably 10 to 600 nm ( data relating to diameter in accordance with din 53 206 ). due to the crosslinking , they are ( almost ) insoluble and are swellable in suitable precipitating agents , e . g . toluene . the ( insoluble ) gel fraction of the rubber particles generally amounts to 80 to 100 wt . %, preferably 90 to 100 wt . %. the swelling index of the rubber particles ( ql ) in toluene is about 1 to 15 , preferably 1 to 10 . ql = the   swelling   index   ql   is   defined   as : wet   weight   of   toluene  -  containing   gel dry   weight   of   gel . to determine the gel content and the swelling index , 250 mg of gel is swollen in 25 ml of toluene for 24 hours with shaking . the ( insoluble ) gel fraction is centrifuged off at 20 , 000 rpm and weighed ( wet weight of toluene - containing gel ) and then dried to constant weight at 70 ° c . and weighed again ( dry weight of gel ). the preparation of crosslinked rubber particles ( rubber gels ) to be used from parent rubbers of the types mentioned above is known in principle and is described , for example , in u . s . pat . no . 5 , 395 , 891 and ep - a 981 000 49 . in addition , it is possible to enlarge the particle size of the rubber particles by agglomeration . the preparation of silica / rubber hybrid gels by coagglomeration is also described , for example in de - a 199 39 865 . 8 . obviously , the crosslinked rubber particles , like the previously mentioned uncrosslinked double bond - containing rubbers , may also be modified by suitable functional groups which , as mentioned above , are able to react with zinc oxide and / or cause an improvement in the linkage of the rubber particles to the surrounding rubber matrix in the vulcanized state . more preferably , modified crosslinked rubber particles which are modified by hydroxyl , carboxyl , amino , amido or by epoxide groups at the surface and which are present in the ranges of amounts mentioned above , are used in rubber mixtures according to the present invention the modification of crosslinked rubber particles ( rubber gels ) and the introduction of the previously mentioned functional groups are also known to a person skilled in the art and are described , for example , in de - a 199 19 459 . 9 , de - a 199 29 347 . 3 , de - a 198 34 804 . 5 . only modification of the corresponding rubbers or rubber gels in aqueous dispersion using appropriate polar monomers which enable the introduction of a hydroxyl , amino , amido , carboxyl and / or epoxide group is mentioned at this point . constituent ( c ) in the rubber mixtures are peroxides of metals from groups ia , ib , iia and iib of the periodic system of elements . preferred metal peroxides are : sodium peroxide , calcium peroxide , barium peroxide and zinc peroxide , wherein zinc peroxide is particularly preferred . these peroxides may be used in the pure form or in a desensitized form . conventional desensitizing agents are the oxides , hydroxides and carbonates of the corresponding metals . commercial zinc peroxide from riedel - de haen contains , e . g . in addition to about 55 wt . % zinc peroxide , also additional zinc oxide and small amounts of zinc carbonate and zinc hydroxide . rubber mixtures according to the present invention may contain , in addition to mixture constituents ( a ), ( b ) and ( c ), also further fillers and / or rubber auxiliary substances and / or crosslinkers . particularly suitable fillers for preparing rubber mixtures and vulcanizates according to the present invention are e . g . : carbon blacks . the carbon blacks to be used here are prepared by the lamp black , furnace black or channel black process and have bet surface areas of 20 - 200 m 2 / g such as e . g . : saf , isaf , iisaf , haf , fef or gpf carbon blacks . silicas , prepared e . g . by precipitation of solutions of silicates or flame hydrolysis of silicon halides with specific surface areas of 5 - 1000 , preferably 20 - 400 m 2 / g ( bet surface area ) and primary particle sizes of 5 - 400 nm . the silicas may also optionally be present as mixed oxides with other metal oxides such as al , mg , ca , ba , zn and ti oxides . synthetic silicates such as aluminum silicate , alkaline earth silicates , such as magnesium silicate or calcium silicate , with bet surface areas of 20 - 400 m 2 / g and primary particle diameters of 5 - 400 nm . thermoplastic fillers such as polyethylene , polypropylene , polytetrafluoroethylene , syndiotactic 1 , 2 - polybutadiene , trans - 1 , 4 - polybutadiene , syndiotactic polystyrene and polycarbonate . suitable rubber auxiliary substances are e . g . : reaction accelerators , antioxidants , heat stabilizers , light stabilizers , ozone stabilizers , processing auxiliary substances , plasticizers , tackifiers , blowing agents , colorants , pigments , waxes , resins , extenders , organic acids , delayers , metal oxides and filler activators such as , for example , triethanolamine , polyethylene glycol , hexanetriol and bis -( triethoxysilylpropyl )- tetrasulfide . the rubber auxiliary substances are used in conventional amounts , which are governed , inter alia , by the intended application . conventional amounts are e . g . amounts of 0 . 1 - 50 parts by wt ., with respect to the amount of rubber ( a ) used . crosslinkers which may be used are sulfur , sulfur donors , peroxides or crosslinking agents such as , for example , diisopropenylbenzene , dinvinylbenzene , divinylether , divinylsulfone , diallyl phthalate , triallyl cyanurate , triallyl isocyanurate , 1 , 2 - polybutadiene , n , n ′- m - phenylenemaleic imide and / or triallyl trimellitate . in addition , suitable compounds are the acrylates and methacrylates of polyhydric , preferably 2 to 4 - hydric , c 2 to c 10 alcohols such as ethylene glycol , propanediol - 1 , 2 - butanediol , hexanediol , polyethylene glycol with 2 to 20 , preferably 2 to 8 oxyethylene units , neopentyl glycol , bisphenol - a , glycerine , trimethylolpropane , pentaerythritol , sorbitol with unsaturated polyesters of aliphatic diols and polyols and also maleic acid , fumaric acid and / or itaconic acid . rubber mixtures according to the present invention may also contain vulcanization accelerators . examples of suitable vulcanization accelerators are e . g . mercaptobenzthiazoles and - sulfenamides , guanidines , thiurams , dithiocarbamates , thioureas , thiocarbonates and dithiophosphates . the vulcanization accelerators , sulfur and sulfur donors or peroxides or other cross - linking agents such as , for example , dimeric 2 , 4 - toluylidene diisocyanate (= desmodur ® tt ) or 1 , 4 - bis - 1 - ethoxyhydroquinone (= crosslinker 30 / 10 ) are used in amounts of 0 . 1 - 40 parts by wt ., preferably 0 . 1 - 10 parts by wt ., with respect to the total amount of rubber . rubber mixtures according to the present invention are prepared by mixing the individual components in suitable equipment such as rollers , internal mixers or also mixer extruders . preferred mixing temperatures are about 50 - 180 ° c . the use of pre - produced mixtures of individual components e . g . in the form of master batches , is also possible . the preparation of gel / rubber master batches is performed , for example , in the latex state by mixing latices of the uncrosslinked rubbers and rubber gels . isolation of the master batch components prepared in this way can be performed in the conventional way by evaporation , precipitation or freeze - coagulation . suitable master batches and also rubber formulations according to the present invention can be obtained directly by mixing other components , such as fillers or phenol resins , into the latex mixture and then working this up . vulcanization of rubber mixtures according to the present invention is performed at temperatures of 100 - 250 ° c ., preferably 130 - 180 ° c ., optionally under a pressure of 10 - 200 bar . the rubber mixtures are suitable in particular for producing industrial rubber articles and tire components . the following may be mentioned by way of example : roller coverings , coverings for conveyer belts , belts , spinnerets , seals , centres for golf balls , soles of shoes , beading mixtures , tire carcasses , subtread mixtures and tire sidewalls . the mixtures are particularly suitable for producing reinforced sidewalls for tires with emergency running properties (“ inserts for run flat tires ”). the rubber gel used for the trials is prepared in accordance with u . s . pat . no . 5 , 395 , 891 by crosslinking polybutadiene latices by means of dicumyl peroxide . characteristic data for the rubber gel are summarized in the table below : diameter of density of dcp latex latex gel gel amount particles d 50 particles content qi tg gel type [ phr ] [ nm ] [ g / cm 3 ] [%] [%] [° c .] a br 1 . 0 116 0 . 9349 97 7 . 4 − 66 . 5 the following mixtures were prepared and the properties of the corresponding vulcanizates were determined . it is shown that the product of the modulus at 100 % extension and the elongation at break ( s 100 × d ) and also the tear strength are improved by adding zinc peroxide . the mixing viscosity is not significantly worsened by adding zinc peroxide . mixture no : 1 2 3 4 5 natural rubber 1 ) 100 100 100 100 100 gel a 60 60 60 60 60 carbon black n 330 2 2 2 2 2 koresin 2 ) 4 4 4 4 4 rhenopol l 3 ) 4 4 4 4 4 zinc oxide 5 0 0 0 0 stearic acid 2 2 2 2 2 tmq 4 ) 1 . 5 1 . 5 1 . 5 1 . 5 1 . 5 6ppd 5 ) 2 . 5 2 . 5 2 . 5 2 . 5 2 . 5 sulfur 5 2 . 5 2 . 5 2 . 5 1 . 5 cbs 6 ) 2 2 2 1 1 . 8 zinc peroxide 7 ) ( ca . 55 %) 0 9 . 1 18 . 2 9 . 1 18 . 2 to characterize the properties of the uncrosslinked compounds , the following quantities were determined : mooney viscosity ml 1 + 4 ( 100 ° c . ), mooney relaxation mr 30 and mooney scorch at ( 130 ° c .). mixture no : 1 2 3 4 5 ml 1 + 4 ( 100 ° c .) [ me ] 23 . 0 25 . 7 26 . 8 28 . 2 26 . 0 mr 30 [%] 1 . 3 1 . 9 3 . 4 3 . 5 3 . 5 ms ( 130 ° c .) 30 . 0 31 . 0 the vulcanization behavior of the mixtures is tested in a rheometer at 160 ° c . in accordance with din 53 529 with the aid of a monsanto rheometer mdr 2000 e . characteristic data such as f a , f max , t 50 and t 90 were determined in this way . these are defined , according to din 53 529 , part 3 , as follows : mixture no : 1 2 3 4 5 f a [ dnm ] 0 . 9 0 . 9 1 . 0 1 . 0 0 . 9 t 50 [ min .] 4 . 2 5 . 6 6 . 0 6 . 2 6 . 4 t 90 [ min .] 6 . 1 8 . 8 9 . 3 9 . 5 9 . 8 f max [ dnm ] 17 . 4 15 . 5 15 . 8 12 . 8 12 . 3 on the basis of the compounds mentioned above , the following test results are obtained after 15 min vulcanization time at 165 ° c . : mixture no : ° 1 2 3 4 5 tensile strength [ mpa ] 8 . 8 11 . 9 9 . 8 17 . 5 17 . 0 elongation at break [%] 255 285 260 425 430 modulus at 50 % extension [ mpa ] 1 . 0 1 . 0 1 . 1 0 . 9 0 . 8 modulus at 100 % extension [ mpa ] 2 . 0 1 . 9 2 . 0 1 . 5 1 . 4 modulus at 300 % extension [ mpa ] — — — 8 . 7 8 . 3 shore a hardness , 23 ° c . 57 57 59 53 53 shore a hardness , 70 ° c . 57 57 58 53 52 rebound resilience , 23 ° c . [%] 67 70 67 63 63 rebound resilience , 70 ° c . [%] 83 81 75 72 72 goodrich flexometer δ t [° c .] 3 . 8 2 . 6 2 . 6 7 . 5 5 . 7 goodrich flexometer t [° c .] 102 . 3 101 . 0 103 . 6 108 . 8 108 . 2 tan δ / 60 ° c . — — 0 . 021 0 . 032 0 . 0 s 100 × d 510 542 520 638 602 although the invention has been described in detail in the foregoing for the purpose of illustration , it is to be understood that such detail is solely for that purpose and that variations can be made therein by those skilled in the art without departing from the spirit and scope of the invention except as it may be limited by the claims .