The invention relates to silicone-azodicarbonamide mixtures, to processes for the production thereof and to the use thereof in rubber mixtures.
EP 2937351 discloses azocarbonyl-functionalized silanes of formula (R1)3-a(R2)aSi—R1—NH—C(O)—N═N—R4.
Also disclosed in KR20170049245 are alkyl-substituted azodicarbonamide compounds of formula R5—NH—C(O)—N═N—C(O)—NH—R5, wherein R5 is a linear or branched cyclic alkyl radical.
A disadvantage of the known silanes in the rubber mixtures is the low 300% modulus.
It is an object of the present invention to provide rubber mixtures containing silane-azodicarbonamide mixtures which show improvements in the 300% modulus relative to the known rubber mixtures.
The present invention provides a silane-azodicarbonamide mixture containing 5-95% by weight, preferably 5-50% by weight, particularly preferably 20-40% by weight, of azocarbonyl-functionalized silane of formula I based on the total amount of azocarbonyl-functionalized silane of formula I, silane of formula II and azodicarbonamide compound of formula III,
(R1)3-a(R2)aSi—R3—NH—C(O)—N═N—R4 (I),
0-90% by weight, preferably 20-60% by weight, particularly preferably 30-60% by weight, of silane of formula II based on the total amount of azocarbonyl-functionalized silane of formula I, silane of formula II and azodicarbonamide compound of formula III,
(R1)y(R2)3-ySi—R3—Sx—R3—Si(R1)y(R2)3-y (II) and
1-80% by weight, preferably 5-50% by weight, particularly preferably 15-40% by weight, of azodicarbonamide compound of formula III based on the total amount of azocarbonyl-functionalized silane of formula I, silane of formula II and azodicarbonamide compound of formula III,
R5—NH—C(O)—N═N—C(O)—NH—R5 (III),
wherein R1 are identical or different and represent C1-C10-alkoxy groups, preferably methoxy or ethoxy groups, phenoxy group or alkylpolyether group —O—(R6—O)r—R7 where R6 are identical or different and represent a branched, saturated or unsaturated, aliphatic, aromatic or mixed aliphatic/aromatic divalent C1-C30 hydrocarbon group, preferably —CH2—CH2—, r is an integer from 1 to 30, preferably 3 to 10, and R7 represents unsubstituted or substituted, branched or unbranched monovalent alkyl, alkenyl, aryl or aralkyl groups, preferably represents C13H27 alkyl group, R2 are identical or different and represent —OH, C6-C20-aryl groups, preferably phenyl, C1-C10-alkyl groups, preferably methyl or ethyl, C2-C20-alkenyl group, C7-C20-aralkyl group or halogen, preferably Cl,
R3 independently of one another represent —CH2—, —CH2CH2—, —CH2CH2CH2—, —C H2CH2CH2CH2—, —CH(CH3)—, —CH2CH(CH3)—, —CH(CH3)CH2—, —C(CH3)2—, —CH(C2H5)—, —CH2CH2CH(CH3)—, —CH(CH3)CH2CH2—, —CH2CH(CH3)CH2—, —CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2—, —CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2CH2- or
The azocarbonyl-functionalized silane of formula I may preferably be (CH3CH2O—)3Si-CH2—NH—CO—N═N-phenyl,
The silane of formula II may preferably be
The azodicarbonamide compound of formula III may preferably be
The silane-azodicarbonamide mixture may preferably contain an azocarbonyl-functionalized silane of formula I
(R1)3-a(R2)aSi—R3—NH—C(O)—N═N—R4 (I),
a silane of formula II
(R1)y(R2)3-ySi—R3—Sx—R3—Si(R1)y(R2)3-y (II) and
an azodicarbonamide compound of formula III
R5—NH—C(O)—N═N—C(O)—NH—R5 (III),
wherein a is 0, y is 3, x is 2 to 4, R1 is ethoxy, R3 is (CH2)3, R4 is phenyl, nitrophenyl or tert-butyl, R5 is a branched or unbranched alkyl radical, particularly preferably CH2—CH(C2H5)—(CH2)3—CH3.
The silane-azodicarbonamide mixture may contain further additives or consist solely of azocarbonyl-functionalized silane of formula I, silane of formula II and azodicarbonamide compound of formula III. Additives may be for example: solvents, for example methanol, ethanol, propanol, butanol, cyclohexanol, N,N-dimethylformamide, dimethyl sulfoxide, pentane, hexane, cyclohexane, heptane, octane, decane, toluene, xylene, acetone, acetonitrile, carbon tetrachloride, chloroform, dichloromethane, 1,2-dichloromethane, tetrachloroethylene, diethyl ether, methyl tert-butyl ether, methyl ethyl ketone, tetrahydrofuran, dioxane, pyridine or methyl acetate, amines of general formula IV
R8—NH2 (IV),
wherein R8 represents a branched or unbranched, saturated or unsaturated, aliphatic or cyclic monovalent C1-C30-hydrocarbon group, preferably C1-C20-, particularly preferably C1-C10-, very particularly preferably C2-C8-, especially preferably CH(CH3)2, CH2CH(CH3)2, C(CH3)3, CH2C(CH3)3, CH2CH2CH(CH3)2, CH2CH(CH3) CH2CH3, CH2CH(CH2CH3)2, CH2CH2CH(CH2CH2CH3)CH2CH2CH2CH3, CH2CH(CH2CH3)CH2CH2CH2CH3, or a substituted or unsubstituted aryl group, preferably phenyl,
(R9)3-aa(R10)aaSi—R11—NH2 (V),
The silane-azodicarbonamide mixture according to the invention may comprise oligomers that form as a result of hydrolysis and condensation of the silanes of formula I and/or silanes of formula II.
The silane mixture according to the invention may be in a form applied to a carrier, for example wax, polymer or carbon black. The silane-azodicarbonamide mixture according to the invention may be in a form applied to a silica, wherein the bonding may be physical or chemical.
The present invention further provides a process for producing the silane-azodicarbonamide mixture according to the invention which is characterized in that it comprises mixing 5-95% by weight, preferably 5-50% by weight, particularly preferably 20-40% by weight, of azocarbonyl-functionalized silane of formula I based on the total amount of azocarbonyl-functionalized silane of formula I, silane of formula II and azodicarbonamide compound of formula III,
(R1)3-a(R2)aSi—R3—NH—C(O)—N═N—R4 (I),
0-90% by weight, preferably 20-60% by weight, particularly preferably 30-60% by weight, of silane of formula II based on the total amount of azocarbonyl-functionalized silane of formula I, silane of formula II and azodicarbonamide compound of formula III,
(R1)y(R2)3-ySi—R3—Sx—R3—Si(R1)y(R2)3-y (II) and
1-80% by weight, preferably 5-50% by weight, particularly preferably 15-40% by weight, of azodicarbonamide compound of formula III based on the total amount of azocarbonyl-functionalized silane of formula I, silane of formula II and azodicarbonamide compound of formula III,
R5—NH—C(O)—N═N—C(O)—NH—R5 (III),
The blending may be carried out after production of the individual components or else during production of the individual components at various suitable points. The blending of the azocarbonyl-functionalized silane of formula I and the silane of formula II may be carried out during production of the azodicarbonamide compound of formula III.
The process according to the invention may be performed with exclusion of air. The process according to the invention may be performed under a protective gas atmosphere, for example under argon or nitrogen, preferably under nitrogen.
The blending may preferably be carried out by mixing with a stirrer.
The process according to the invention may be performed at standard pressure, elevated pressure or reduced pressure. Preferably, the process according to the invention may be performed at standard pressure.
Elevated pressure may be a pressure of 1.1 bar to 100 bar, preferably of 1.1 bar to 50 bar, particularly preferably of 1.1 bar to 10 bar and very particularly preferably of 1.1 to 5 bar.
Reduced pressure may be a pressure of 1 mbar to 1000 mbar, preferably 250 mbar to 1000 mbar, more preferably 500 mbar to 1000 mbar.
The process according to the invention may be performed at between 0° C. and 100° C., preferably between 10° C. and 50° C., particularly preferably between 10° C. and 35° C.
The process according to the invention may be performed in a solvent, for example methanol, ethanol, propanol, butanol, cyclohexanol, N,N-dimethylformamide, dimethyl sulfoxide, pentane, hexane, cyclohexane, heptane, octane, decane, toluene, xylene, acetone, acetonitrile, carbon tetrachloride, chloroform, dichloromethane, 1,2-dichloroethane, tetrachloroethylene, diethyl ether, methyl tert-butyl ether, methyl ethyl ketone, tetrahydrofuran, dioxane, pyridine or methyl acetate, or a mixture of the aforementioned solvents. The process according to the invention may preferably be performed without solvent.
The volatile secondary components may be separated by distillation.
The distillative purification may be carried out either before or after mixing of the azocarbonyl-functionalized silane of formula I, the silane of formula II and the azodicarbonamide compound of formula III. The distillative purification may preferably be carried out after the blending of the azocarbonyl-functionalized silane of formula I, the silane of formula II and the azodicarbonamide compound of formula III.
The distillative purification may be performed in a batch process or via a thin-film evaporator.
The distillative purification may be performed with exclusion of air. The process may be performed under a protective gas atmosphere, for example under argon or nitrogen, preferably under nitrogen.
The distillative purification may be performed at standard pressure or reduced pressure. The process according to the invention may preferably be performed under reduced pressure.
Reduced pressure may be a pressure of 1 mbar to 1000 mbar, preferably 10 mbar to 200 mbar, particularly preferably 20 mbar to 1000 mbar.
The distillative purification may be performed at between 20° C. and 100° C., preferably between 20° C. and 80° C., particularly preferably between 30° C. and 60° C.
The invention further provides a rubber mixture comprising
(R1)3-a(R2)aSi—R3—NH—C(O)—N═N—R4 (I),
(R1)y(R2)3-ySi—R3—Sx—R3—Si(R1)y(R2)3-y (II) and
R5—NH—C(O)—N═N—C(O)—NH—R5 (III),
The rubber may preferably be a diene rubber, particularly preferably natural rubber, polyisoprene, polybutadiene, styrene-butadiene copolymers, isobutylene/isoprene copolymers, butadiene/acrylonitrile copolymers, ethylene/propylene/diene copolymers (EPDM), partly hydrogenated or fully hydrogenated NBR rubber.
Rubber used may be natural rubber and/or synthetic rubbers. Preferred synthetic rubbers are described for example in W. Hofmann, Kautschuktechnologie [Rubber Technology], Genter Verlag, Stuttgart 1980. They may include:
In a preferred embodiment, the rubbers may be sulfur-vulcanizable. For the production of car tyre treads it is in particular possible to use anionically polymerized S—SBR rubbers (solution SBR) with a glass transition temperature above −50° C., and also mixtures of these with diene rubbers. It is particularly preferably possible to use S—SBR rubbers whose butadiene portion has more than 20% by weight vinyl fraction. It is very particularly preferably possible to use S—SBR rubbers whose butadiene portion has more than 50% by weight vinyl fraction.
It is preferably possible to use mixtures of the abovementioned rubbers which have an S—SBR content of more than 50% by weight, preferably more than 60% by weight.
The rubber may be a functionalized rubber, where the functional groups may be amine and/or amide and/or urethane and/or urea and/or aminosiloxane and/or siloxane and/or silyl and/or alkylsilyl, for example N,N-bis(trimethylsilyl)aminopropylmethyldiethoxysilane or methyltriphenoxysilane, and/or halogenated silyl and/or silane sulfide and/or thiol and/or hydroxyl and/or ethoxy and/or epoxy and/or carboxyl and/or tin, for example tin tetrachloride or dibutyldichlorotin, and/or silanol and/or hexachlorodisiloxane and/or thiocarboxy and/or nitrile and/or nitroxide and/or amido and/or imino and/or urethane and/or urea and/or dimethylimidazolidinone and/or 2-methyl-2-thiazoline and/or 2-benzothiazoleacetonitrile and/or 2-thiophenecarbonitrile and/or 2-(N-methyl-N-3-trimethoxysilylpropyl)thiazoline and/or carbodiimide and/or N-substituted aminoaldehyde and/or N-substituted aminoketone and/or N-substituted aminothioaldehyde and/or N-substituted aminothioketone and/or benzophenone and/or thiobenzophenone with amino group and/or isocyanate and/or isothiocyanate and/or hydrazine and/or sulfonyl and/or sulfinyl and/or oxazoline and/or ester groups.
The rubber mixture according to the invention may contain at least one filler.
Fillers usable for the rubber mixtures according to the invention include the following fillers:
It is possible with preference to use amorphous silicas prepared by precipitation from solutions of silicates, with BET surface areas of 20 to 400 m2/g, more preferably 100 m2/g to 250 m2/g, in amounts of 5 to 150 parts by weight, based in each case on 100 parts of rubber.
With very particular preference, it is possible to use precipitated silicas as filler.
The fillers mentioned may be used alone or in a mixture.
The rubber mixtures according to the invention may contain 5 to 150 parts by weight of filler and 0.1 to 30 parts by weight, preferably 2 to 25 parts by weight, particularly preferably 5 to 20 parts by weight, of the silane-azodicarbonamide mixture according to the invention, wherein the parts by weight are based on 100 parts by weight of rubber.
The silane-azodicarbonamide mixture according to the invention may be used as adhesion promoters between inorganic materials, for example glass beads, glass shards, glass surfaces, glass fibres, or oxidic fillers, preferably silicas such as precipitated silicas and formed silicas, and organic polymers, for example thermosets, thermoplastics or elastomers, or as crosslinking agents and surface modifiers for oxidic surfaces.
The silane-azodicarbonamide mixture according to the invention can be used as coupling reagents in filled rubber mixtures, examples being tyre treads, industrial rubber articles or footwear soles.
The rubber mixtures according to the invention may comprise further rubber auxiliaries, such as reaction accelerators, ageing stabilizers, heat stabilizers, light stabilizers, antiozonants, processing aids, plasticizers, resins, tackifiers, blowing agents, dyes, pigments, waxes, extenders, organic acids, retarders, metal oxides, and activators such as diphenylguanidine, triethanolamine, polyethylene glycol, alkoxy-terminated polyethylene glycol alkyl-O—(CH2—CH2—O)yi-H with y1=2-25, preferably y1=2-15, more preferably y1=3-10, most preferably y1=3-6, or hexanetriol, that are familiar to the rubber industry.
The rubber auxiliaries may be used in familiar amounts determined inter alia by factors including the intended use. Customary amounts may, for example, be amounts of 0.1% to 50% by weight based on rubber. Crosslinkers used may be peroxides, sulfur or sulfur donor substances. The rubber mixtures according to the invention may further comprise vulcanization accelerators. Examples of suitable vulcanization accelerators may be mercaptobenzothiazoles, sulfenamides, thiurams, dithiocarbamates, thioureas and thiocarbonates. The vulcanization accelerators and sulfur may be used in amounts of 0.1% to 10% by weight, preferably 0.1% to 5% by weight, based on 100 parts by weight of rubber.
The rubber mixtures according to the invention can be vulcanized at temperatures of 100° C. to 200° C., preferably 120° C. to 180° C., optionally at a pressure of 10 to 200 bar. The blending of the rubbers with the filler, optionally rubber auxiliaries and the silane-azodicarbonamide mixtures may be carried out in known mixing units, such as rollers, internal mixers and mixing extruders.
The rubber mixtures according to the invention can be used for production of moulded articles, for example for the production of tyres, especially pneumatic tyres or tyre treads, cable sheaths, hoses, drive belts, conveyor belts, roller coverings, footwear soles, sealing rings and damping elements.
Advantages of the silane-azodicarbonamide mixtures according to the invention are improved stress values and a more balanced result in rebound resilience measurements in rubber mixtures.
Si 69™ (bis-[3-(triethoxysilyl)-propyl]-tetrasulfide) from Evonik Operations GmbH is employed as example 1.
2-Phenyl-N-(3-(triethoxysilyl)propyl)diazenecarboxamide produced according to EP 2 937 351, example 7, is employed as example 2.
2-Ethylhexylamine and pentane were cooled to 0° C. in a 2 L flask with stirrer and reflux condenser. Diisopropyl diazodicarboxylate (DIAD) was slowly added while the temperature was maintained at 0° C. The mixture was stirred for a further 30 min at this temperature and then stirred for two to three hours at 20° C. The crude product N,N-bis(2-ethylhexyl)azodicarbonamide was obtained as a solution in pentane and isopropanol. The reaction conversion was monitored by HPLC analysis. The solvent was removed in vacuo and the product obtained as a deep-red solid in >=70% purity (determined by 1H-NMR analysis).
2-Ethylhexylamine (291 g, 2.25 mol) and pentane (122 g, 1.69 mol) were cooled to 5° C. in a 2 L flask with stirrer and reflux condenser. Diisopropyl diazodicarboxylate (DIAD) (227 g, 1.16 mol) was slowly added while the temperature was maintained at 5° C. The mixture was stirred for a further 30 min at 0° C. and then stirred for two to three hours at 20° C. The resulting solution of N,N-bis(2-ethylhexyl)azodicarbonamide was subsequently divided and a quarter of this solution (126.0 g, 60% in iPrOH/pentane, 0.28 mol) admixed with Si 69™ (95 g, 0.18 mol) und 2-phenyl-N-(3-(triethoxysilyl)propyl)diazenecarboxamide (128 g, 0.36 mol). The reaction solution was stirred at 20° C. for 5 min. Pentane was distilled off at 40° C. and 500 mbar, before a vacuum of 20 mbar was applied at 40-60° C. with stirring and pentane and iPrOH were removed by distillation. The distilled mixed product was analyzed by NMR and GC.
Si 69: 30% (1H-NMR, DMSO-d6)
2-Phenyl-N-(3-(triethoxysilyl)propyl)diazenecarboxamide: 40% (1H-NMR, DMSO-d6)
N,N-bis(2-ethylhexyl)azodicarbonamide: 30% (1H-NMR, DMSO-d6)
Isopropanol: 0.3% (GC)
The materials used are listed in table 1.
The formulation used for the rubber mixtures is specified in table 2. The unit phr means parts by weight based on 100 parts of the raw rubber used.
Mixture production is described in table 3.
The elastomer mixtures were produced with a GK 1.5 E internal mixer from Harburg Freudenberger Maschinenbau GmbH. Test methods used for the mixtures and vulcanizates thereof were effected according to table 4.
It is apparent from table 5 that the vulcanizates of the inventive mixtures 1-11 comprising the inventive silane-azodicarbonamide mixtures exhibit a markedly improved 300% stress value compared to the comparative mixtures 1-3.
Inventive mixtures 4 and 11 are identical to examples 1-3 in terms of composition. Inventive mixture 4 was produced during mixing by addition of the individual components examples 1-3 to the internal mixer, while in the case of inventive mixture 11 a premixture of examples 1-3 is added. Similar results are obtained irrespective of whether the silane-azodicarbonamide mixture is produced as a premixture or produced during mixing.
The materials used are listed in table 1.
The formulation used for the rubber mixtures is specified in table 6. The unit phr means parts by weight based on 100 parts of the raw rubber used.
Mixture production is described in table 3.
The elastomer mixtures were produced with a GK 1.5 E internal mixer from Harburg Freudenberger Maschinenbau GmbH. Test methods used for the mixtures and vulcanizates thereof were effected according to table 7. The vulcanizates were produced in a vulcanizing press at 150° C. with a hot time of 30 min.
It is apparent from table 8 that the vulcanizates of the inventive mixtures 12 and 13 comprising the inventive silane-azodicarbonamide mixture exhibit a markedly improved 300% stress value compared to the comparative mixture 4. The Mooney viscosity is additionally significantly lower.
Number | Date | Country | Kind |
---|---|---|---|
21203839.2 | Oct 2021 | EP | regional |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2022/077957 | 10/7/2022 | WO |