"TIRE AND CROSSLINKABLE ELASTOMERIC COMPOSITION"
The present invention relates to a tire and to a crosslinkable elastomeric composition.
More in particular the present invention relates to a tire, including at least one structural element obtained by crosslinking a crosslinkable elastomeric composition comprising at least one elastomeric polymer grafted with at least one phenolic resin.
Moreover, the present invention also relates to a crosslinkable elastomeric composition comprising at least one elastomeric polymer grafted with at least one phenolic resin, as well as to a crosslinked manufactured article obtained by crosslinking said crosslinkable elastomeric composition. In the field of production of tires, it is known to use resins such as, for example, novolak-type or resol- type phenolic resins.
For example, in order to improve the abrasion resistance of the tire tread band to be used in heavy vehicles, it was proposed to introduce specific thermosetting resins in the polymeric base such as, for example, m-cresol-formaldehyde or phenolic resins, as described, for example, in the following Japanese
Patent Applications: JP 7-109381, JP 7-109382, or JP 7- 109383.
United States Patent US 5,026,762 relates to a rubber composition for use in tire treads which comprises :
(a) 100 parts by weight of a base rubber comprising a first rubber and a second rubber blended in a weight ratio of from 50:50 to 75:25, said first rubber containing natural rubber in an amount of at least 80% by weight, and said second rubber consisting essentially of a butadiene rubber; (b) from 55 to 90 parts by weight of a carbon black having an iodine adsorption of from 90 to 200 mg/g
and a dibutyl phthalate adsorption of from 100 to 140 ml/100 g; and
(c) from 1 to 10 parts by weight of a novolak-type tricresol-formaldehyde resin; said composition having a dynamic Young's modulus of not less than 8 MPa at 0° C.
The abovementioned rubber composition for tire treads is said to be useful for all-weather tires and to have a sufficient resistance to snow and ice skidding, to abrasion, to cracking and to crack growth and adequate durability.
United States Patent US 6,376,587 relates to a rubber composition for a tire tread comprising per 100 parts by weight of a diene based rubber component containing at least 50 parts by weight of styrene butadiene rubber: (1) 5 to 50 parts by weight of carbon black having a nitrogen absorption surface area of from 90 to 180 m2/g and a DBP absorption amount of from 100 to 170 ml/100 g; (2) 5 to 50 parts by weight of silica; (3) wherein the total amount of said carbon black and said silica is from 30 to 90 parts by weight; and (4) 5 to 20% by weight of a silane coupling agent relative to the blended amount of silica; (5) 1 to 15 parts by weight of a thermoplastic (novolak-type) phenolic resin; and (6) 5 to 20% by weight of hexamethylenetetramine relative to the blended amount of resin, wherein tan δ at 600C is lower than or equal to 0.14, tan δ at 00C is higher than or equal to 0.50, dynamic modulus E1 at 300C is higher than or equal to 1.2xlO7 pa, and tensile stress at 300% (M300) at 25°C is lower than or equal to 9.5 MPa. The abovementioned rubber composition is said to reduce the rolling resistance and to improve the fuel consumption without impairing the braking performance and the turning performance of an automobile on a wet road surface.
However, the Applicant has noticed that the use of the above disclosed phenolic resins in crosslinkable elastomeric compositions, may negatively affect their abrasion resistance. Consequently, the Applicant has faced the problem of providing a tire having high abrasion resistance combined with low rolling resistance.
The Applicant has now found that it is possible to obtain a tire having the above reported properties by using a crosslinkable elastomeric compositions comprising at least one elastomeric polymer grafted with at least one phenolic resin.
The tire so obtained shows high abrasion resistance combined with low rolling resistance. Furthermore, said tire show good mechanical properties (both static and dynamic) .
According to a first aspect, the present invention relates to a tire comprising at least one structural element including a crosslinked elastomeric material obtained by crosslinking a crosslinkable elastomeric composition comprising a crosslinkable elastomeric base comprising at least 30 phr, preferably of from 50 phr to 100 phr, of at least one elastomeric polymer grafted with at least one phenolic resin. The grafting of said at least one phenolic resin onto said at least one elastomeric polymer may be determined according to known techniques such as, for example, by FTIR analysis or 1H-NMR analysis: further details about said techniques will be disclosed in the examples which follow.
Preferably, said crosslinkable elastomeric base further comprises at least one second elastomeric polymer in an amount not higher than or equal to 70 phr, preferably of from 0 phr to 50 phr. For the purpose of the present description and of the claims which follow, the term "crosslinkable
elastomeric base" means any polymer or polymers mixture, either natural or synthetic, capable of assuming all the chemical-physical and mechanical properties typical of elastomeric polymers as a result of crosslinking with system known in the art such as, for example, a sulfur-based system or a peroxide-based system.
For the purposes of the present description and of the claims which follow, the term "phr" means the parts by weight of a given component of the elastomeric composition per 100 parts by weight of the elastomeric base .
For the purpose of the present description and of the claims which follow, except where otherwise indicated, all numbers expressing amounts, quantities, percentages, and so forth, are to be understood as being modified in all instances by the term "about". Also, all ranges include any combination of the maximum and minimum points disclosed and include any intermediate ranges therein, which may or may not be specifically enumerated herein.
According to one preferred embodiment, the tire comprises : a carcass structure of a substantially toroidal shape, having opposite lateral edges associated with respective right-hand and left-hand bead structures, said bead structures comprising at least one bead core and at least one bead filler; a belt structure applied in a radially external position with respect to said carcass structure; a tread band radially superimposed on said belt structure; a pair of sidewalls applied laterally on opposite sides with respect to said carcass structure; wherein said structural element is a tread band.
According to a further aspect, the present
invention also relates to a crosslinkable elastomeric composition comprising a crosslinkable elastomeric base comprising at least 30 phr, preferably of from 50 phr to 100 phr, of at least one elastomeric polymer grafted with at least one phenolic resin.
According to a further aspect, the present invention also relates to a crosslinked manufactured article obtained by crosslinking a crosslinkable elastomeric composition above disclosed. According to one preferred embodiment, said at least one phenolic resin is grafted directly onto the elastomeric polymer.
According to a further preferred embodiment, said at least one phenolic resin is grafted onto the elastomeric polymer through at least one functional group .
According to one preferred embodiment, said crosslinkable elastomeric composition further comprises from 0 phr to 120 phr, preferably from 20 phr to 90 phr, of at least one carbon black reinforcing filler.
According to one preferred embodiment, said elastomeric polymer grafted with at least one phenolic resin may have a weight average molecular weight (Mw) not lower than 80,000, preferably of from 100,000 to 1,000,000. Said weight average molecular weight (Mw) may be determined according to known techniques such as, for example, by gel permeation chromatography (GPC) .
According to a further preferred embodiment, said elastomeric polymer grafted with at least one phenolic resin may have a Mooney viscosity ML (1+4) not lower than 40, preferably of from 50 to 110. Said Mooney viscosity ML (1+4) may be determined according to Standard ASTM D1646-04 (at 1000C) .
The phenolic resin may be introduced into the elastomeric polymer by means of processes known in the art such as, for example, the processes disclosed in
United States Patents US 2,227,797, or US 4,105,610.
According to one preferred embodiment, said phenolic resin may be grafted onto the elastomeric polymer by means of a process comprising: - feeding at least one elastomeric polymer, said elastomeric polymer optionally containing at least one functional group, and at least one phenolic resin, into at least one extruder comprising: a housing including at least one feed opening and a discharge opening, and at least one screw rotatably mounted in said housing; mixing and softening said mixture so as to obtain an elastomeric polymer grafted with at least one phenolic resin,- - discharge the elastomeric polymer obtained in the above step through the discharge opening. According to a further preferred embodiment, said phenolic resin may be grafted onto said elastomeric polymer by means of a process comprising: - feeding at least one elastomeric polymer, at least one functionalized monomer, and at least one phenolic resin, into at least one extruder comprising: a housing including at least one feed opening and a discharge opening, and at least one screw rotatably mounted in said housing,- mixing and softening said mixture so as to obtain an elastomeric polymer grafted with at least one phenolic resin,- discharging the elastomeric polymer obtained in the above step through the discharge opening.
Preferably, said processes may be carried out at a temperature of from 20°C to 3000C, more preferably of from 800C to 25O0C.
Preferably, said processes may be carried out for a time of from 10 seconds to 5 minutes, more preferably of from 30 seconds to 3 minutes.
Preferably, said extruder is a co-rotating twin- screw extruder.
Said elastomeric polymer grafted with at least one phenolic resin may be obtained in the form of a continuous ribbon or, alternatively, in the form of a subdivided product .
According to one preferred embodiment, said at least one phenolic resin may be selected, for example, from: - novolak-type phenolic resins or resol-type phenolic resins obtained from the reaction of a phenolic compound such as, for example, phenol, alkyl substituted phenol, arylalkyl or alkylaryl substituted phenol, resorcinol, alkyl substituted resorcinol, arylalkyl or alkylaryl substituted resorcinol, or mixtures thereof, with an aldehyde such as, for example, formaldehyde, p-formaldehyde, butyraldheyde, benzaldehyde, salicylaldheyde, acetaldehyde, propionaldehyde, crotonaldehyde, butyraldehyde, iso-butyraldehyde, n-valeraldehyde, crotonaldehyde, cinnamaldheyde, or mixtures thereof ; phenolic resins obtained from the reaction of alkyl substituted phenol and acetylene such as, for example, p-t-butylphenol-acetylene resin; substituted melamine resins such as, for example, N-substituted oxymethylmelamine resins; terpene phenolic resins obtained by alkylating phenolic compounds with terpene hydrocarbons. Novolak-type phenolic resins, resol-type phenolic resins, or mixtures thereof, are particularly preferred.
Specific examples of novolak-type phenolic resins, or resol-type phenolic resins, which may be advantageously used according to the present invention are: octylphenol-formaldehyde resin, octylphenol-
formaldehyde resin containing methylol groups, or mixture thereof .
Examples of phenolic resins which may be used according to the present invention and are available commercially are the products known under the name of SP-1068, SP-1045, from Schenectady International.
As disclosed above, said at least one phenolic resin is preferably grafted onto the elastomeric polymer through at least one functional group. According to one preferred embodiment, said at least one functional group may be selected, for example from: carboxylic groups; carboxylate groups; anhydride groups; ester groups, or mixtures thereof. Anhydride groups, carboxylic groups, are particularly preferred. The functional group may be introduced into the elastomeric polymer by means of processes known in the art such as, for example, during the production of the elastomeric polymer by co-polymerization with at least one corresponding functionalized monomer,- or by subsequent modification of the elastomeric polymer by grafting said at least one functionalized monomer, said grafting being optionally carried out in the presence of a free radical initiator (for example, an organic peroxide) . Preferably, said at least one functional group may be introduced into the elastomeric polymer by means of a process comprising: feeding at least one elastomeric polymer and at least one functionalized monomer into at least one extruder comprising: a housing including at least one feed opening and a discharge opening, and at least one screw rotatably mounted in said housing,- mixing and softening said mixture so as to obtain an elastomeric polymer including at least one functional group,- discharging the elastomeric polymer obtained in the
above step through the discharge opening. Further details about the above disclosed process may be found, for example, in International Patent Application WO 2005/118695. Functionalized monomers which may be advantageously used include, for example, monocarboxylic or dicarboxylic acids, or derivatives thereof, in particular salts, anhydrides or esters.
Examples of monocarboxylic or dicarboxylic acids, or derivatives thereof are: maleic acid, fumaric acid, citraconic acid, itaconic acid, acrylic acid, methacrylic acid, dithiodisuccinic acid, dithiodipropionic acid, and salts, anhydrides or esters derived therefrom, or mixtures thereof. Maleic anhydride, dithiodipropionic acid, are particularly preferred.
According to one preferred embodiment, the elastomeric polymer which may be utilized in the production of the elastomeric polymer grafted with at least one phenolic resin, may be selected from those commonly used in sulfur-crosslinkable elastomeric compositions, that are particularly suitable for producing tires, that is to say from elastomeric polymers or copolymers with an unsaturated chain having a glass transition temperature (T9) generally below 2O0C, preferably in the range of from O0C to -1100C. These polymers or copolymers may be of natural origin or may be obtained by solution polymerization, emulsion polymerization or gas-phase polymerization of one or more conjugated diolefins, optionally blended with at least one comonomer selected from monovinylarenes . Preferably, the obtained polymers or copolymers contain said at least one comonomer selected from monovinylarenes in an amount of not more than 60% by weight.
The conjugated diolefins generally contain from 4
to 12, preferably from 4 to 8 carbon atoms, and may be selected, for example, from the group comprising: 1,3- butadiene, isoprene, 2 , 3-dimethyl-l, 3-butadiene, 1,3- pentadiene, 1, 3-hexadiene, 3-butyl-l, 3-octadiene, 2-phenyl-1, 3 -butadiene, or mixtures thereof. 1,3- butadiene, isoprene, or mixtures thereof, are particularly preferred. Isoprene, 1, 3 -butadiene, are still particularly preferred.
Monovinylarenes which may optionally be used as comonomers generally contain from 8 to 20, preferably from 8 to 12 carbon atoms, and may be selected, for example, from: stirene; 1-vinylnaphthalene; 2- vinylnaphthalene; various alkyl, cycloalkyl, aryl, alkylaryl or arylalkyl derivatives of stirene such as, for example, α-methylstirene, 3-methylstirene, 4-propylstirene, 4-cyclohexylstirene, 4-dodecylstirene, 2-ethyl-4-benzylstirene, 4-p-tolylstirene, 4- (4- phenylbutyl) stirene, or mixtures thereof. Stirene is particularly preferred. Preferably, the elastomeric polymer may be selected, for example, from: cis-1 , 4-polyisoprene
(natural or synthetic), 3 , 4-polyisoprene, polybutadiene
(in particular polybutadiene with a high 1,4-cis content) , optionally halogenated isoprene/isobutene copolymers, 1 , 3-butadiene/acrylonitrile copolymers, stirene/1, 3 -butadiene copolymers, stirene/isoprene/1, 3- butadiene copolymers, stirene/1, 3- butadiene/acrylonitrile copolymers, or mixtures thereof . Alternatively, elastomeric polymer of one or more monoolefins with an olefinic comonomer and at least one diene, or derivatives thereof, may be used. The monoolefins may be selected from: ethylene and α- olefins generally containing from 3 to 12 carbon atoms, such as, for example, propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, or mixtures thereof. The following
are preferred: copolymers between ethylene and an α- olefin, optionally with a diene; isobutene homopolymers or copolymers thereof with small amounts of a diene, which are optionally at least partially halogenated. The diene generally contains from 4 to 20 carbon atoms and is preferably selected from: 1, 3 -butadiene, isoprene, 1, 4-hexadiene, 1 , 4-cyclohexadiene, 5- ethylidene-2-norbornene, 5-methylene-2-norbornene, vinylnorbornene, or mixtures thereof. Among these, the following are particularly preferred: ethylene/propylene/diene copolymers (EPDM) ; polyisobutene; butyl rubbers; halobutyl rubbers, in particular chlorobutyl or bromobutyl rubbers; or mixtures thereof . Elastomeric polymers functionalized by reaction with suitable terminating agents or coupling agents may also be used. In particular, elastomeric polymers obtained by anionic polymerization in the presence of an organometallic initiator (in particular an organolithium initiator) may be functionalized by reacting the residual organometallic groups derived from the initiator with suitable terminating agents or coupling agents such as, for example, imines, carbodiimides, alkyltin halides, substituted benzophenones, alkoxysilanes or aryloxysilanes (see, for example, European Patent EP 451,604, or United States Patents US 4,742,124, or US 4,550,142).
As disclosed above, the crosslinkable elastomeric base, may further comprises at least one second elastomeric polymer. Said elastomeric polymer may be selected, for example, from: cis-1 , 4-polyisoprene (natural or synthetic), 3,4- polyisoprene, polybutadiene (in particular polybutadiene with a high 1,4-cis content), optionally halogenated isoprene/isobutene copolymers, 1 , 3-butadiene/acrylonitrile copolymers,
stirene/1, 3 -butadiene copolymers, stirene/isoprene/1, 3 -butadiene copolymers, stirene/1 , 3 -butadiene/acrylonitrile copolymers, or mixtures thereof; - ethylene/propylene copolymers (EPR) or ethylene/propylene/diene copolymers (EPDM) ; polyisobutene; butyl rubbers; halobutyl rubbers, in particular chlorobutyl or bromobutyl rubbers; or mixtures thereof; or mixtures thereof.
As disclosed above, said crosslinkable elastomeric composition may further comprise at least one carbon black reinforcing filler.
According to one preferred embodiment, the carbon black reinforcing filler which may be used in the present invention may be selected from those having a surface area of not less than 20 m2/g (determined by CTAB absorption as described in Standard ISO 6810:1995) . At least one additional reinforcing filler may advantageously be added to the above disclosed crosslinkable elastomeric composition, in an amount generally of from 0 phr to 120 phr, preferably of from 20 phr to 90 phr. The reinforcing filler may be selected from those commonly used for crosslinked manufactured products, in particular for tires, such as, for example, silica, alumina, aluminosilicates, calcium carbonate, kaolin, or mixtures thereof. Silica is particularly preferred. The silica which may be used in the present invention may generally be a pyrogenic silica or, preferably, a precipitated silica, with a BET surface area (measured according to Standard ISO 5794/1:2005) of from 50 m2/g to 500 m2/g, preferably of from 70 m2/g to 200 m2/g.
When a reinforcing filler comprising silica is
present, the crosslinkable elastomeric composition may advantageously incorporate a silane coupling agent capable of interacting with the silica and of linking it to the elastomeric polymer during the vulcanization. According to one preferred embodiment, said silane coupling agent may be selected, for example, from those having at least one hydrolizable silane group which may be identified, for example, by the following general formula (I) : (R)3Si-CnH2n-X (I) wherein the groups R, which may be equal or different from each other, are selected from: alkyl, alkoxy or aryloxy groups or from halogen atoms, on condition that at least one of the groups R is an alkoxy or aryloxy group; n is an integer of from 1 to 6, extremes included; X is a group selected from: nitroso, mercapto, amino, epoxide, vinyl, imide, chloro, -(S)1nCnH2n-Si-(R)3, or -S-COR, wherein m and n are integers of from 1 to 6, extremes included, and the groups R are defined as above.
Among the silane coupling agents that are particularly preferred are bis (3-triethoxysilyl- propyl) tetrasulphide, bis (3-triethoxysilylpropyl) - disulphide, or mixtures thereof. Said coupling agents may be used as such or as a suitable mixture with an inert filler (for example, carbon black) so as to facilitate their incorporation into the crosslinkable elastomeric base.
According to one preferred embodiment, said silane coupling agent is present in the crosslinkable elastomeric composition in an amount of from 0 phr to 10 phr, preferably of from 0.5 phr to 5 phr.
The crosslinkable elastomeric composition above disclosed may be vulcanized according to known techniques, in particular with sulfur-based vulcanizing systems commonly used for elastomeric polymers. To this
end, in the composition, after one or more stages of thermomechanical processing, a sulfur-based vulcanizing agent is incorporated together with vulcanization accelerators. In the final processing stage, the temperature is generally kept below 1500C and preferably below 13O0C, so as to avoid any unwanted pre-crosslinking phenomena.
The vulcanizing agent most advantageously used is sulfur, or molecules containing sulfur (sulfur donors) , with accelerators and activators known to those skilled in the art .
Activators that are particularly effective are zinc compounds, and in particular ZnO, ZnCO3, zinc salts of saturated or unsaturated fatty acids containing from 8 to 18 carbon atoms, such as, for example, zinc stearate, which are preferably formed in situ in the elastomeric composition from ZnO and fatty acid, and also BiO, PbO, Pb3O4, PbO2, or mixtures thereof.
Accelerators that are commonly used may be selected, for example, from: dithiocarbamates, guanidine, thiourea, thiazoles, sulphenamides, thiurams, amines, xanthates, or mixtures thereof.
Said crosslinkable elastomeric composition may comprise other commonly used additives selected on the basis of the specific application for which the composition is intended. For example, the following may be added to said elastomeric composition: antioxidants, anti-ageing agents, plasticizers, adhesives, anti-ozone agents, modifying resins, waxes, fibres (for example Kevlar pulp), or mixtures thereof.
For the purpose of further improving the processability, a plasticizer generally selected from mineral oils, vegetable oils, synthetic oils, or mixtures thereof, such as, for example, aromatic oil, naphthenic oil, phthalates, soybean oil, or mixtures thereof, may be added to said crosslinkable elastomeric
composition. The amount of plasticizer generally ranges from 0 phr to 70 phr, preferably from 3 phr to 30 phr.
The above disclosed crosslinkable elastomeric composition may be prepared by mixing together the crosslinkable elastomeric base with the reinforcing filler and with the other additives optionally present according to techniques known in the art . The mixing may be carried out, for example, using an open mixer of open-mill type, or an internal mixer of the type with tangential rotors (Banbury) or with interlocking rotors (Intermix) , or in continuous mixers of Ko-Kneader type (Buss) , or of co-rotating or counter-rotating twin- screw type.
The present invention will now be illustrated in further detail by means of a number of illustrative embodiments, with reference to the attached Fig. 1-2:
Fig. 1 is a view in cross section of a portion of a tire made according to the invention;
Fig. 2 is a schematic diagram of a production plant for producing an elastomeric polymer grafted with at least one phenolic resin according to the process of the present invention.
"a" indicates an axial direction and "r" indicates a radial direction. For simplicity, Fig. 1 shows only a portion of the tire, the remaining portion not represented being identical and symmetrically arranged with respect to the radial direction "r" .
The tire (100) comprises at least one carcass ply
(101) , the opposite lateral edges of which are associated with respective bead structures comprising at least one bead core (102) and at least one bead filler (104) . The association between the carcass ply
(101) and the bead core (102) is achieved here by folding back the opposite lateral edges of the carcass ply (101) around the bead core (102) so as to form the so-called carcass back-fold (101a) as shown in Fig. 1.
Alternatively, the conventional bead core (102) may¬ be replaced with at least one annular insert formed from rubberized wires arranged in concentric coils (not represented in Fig. 1) (see, for example, European Patent Applications EP 928,680, or EP 928,702). In this case, the carcass ply (101) is not back-folded around said annular inserts, the coupling being provided by a second carcass ply (not represented in Fig. 1) applied externally over the first. The carcass ply (101) generally consists of a plurality of reinforcing cords arranged parallel to each other and at least partially coated with a layer of a crosslinked elastomeric composition. These reinforcing cords are usually made of textile fibres, for example rayon, nylon or polyethylene terephthalate, or of steel wires stranded together, coated with a metal alloy (for example copper/zinc, zinc/manganese, zinc/molybdenum/cobalt alloys and the like) .
The carcass ply (101) is usually of radial type, i.e. it incorporates reinforcing cords arranged in a substantially perpendicular direction relative to a circumferential direction. The core (102) is enclosed in a bead (103) , defined along an inner circumferential edge of the tire (100), with which the tire engages on a rim (not represented in Fig. 1) forming part of a vehicle wheel. The space defined by each carcass back- fold (101a) contains a bead filler (104) wherein the bead core (102) is embedded. An antiabrasive strip
(105) is usually placed in an axially external position relative to the carcass back-fold (101a) .
A belt structure (106) is applied along the circumference of the carcass ply (101) . In the particular embodiment in Fig. 1, the belt structure
(106) comprises two belt strips (106a, 106b) which incorporate a plurality of reinforcing cords, typically metal cords, which are parallel to each other in each
strip and intersecting with respect to the adjacent strip, oriented so as to form a predetermined angle relative to a circumferential direction. On the radially outermost belt strip (106b) may optionally be applied at least one zero-degree reinforcing layer (106c), commonly known as a "0° belt", which generally incorporates a plurality of reinforcing cords, typically textile cords, arranged at an angle of a few degrees relative to a circumferential direction, and coated and welded together by means of a crosslinked elastomeric composition.
A sidewall (108) is also applied externally onto the carcass ply (101) , this sidewall extending, in an axially external position, from the bead (103) to the end of the belt structure (106) .
A tread band (109) , which may be made according to the present invention, whose lateral edges are connected to the sidewalls (108) , is applied circumferentially in a position radially external to the belt structure (106) . Externally, the tread band (109) has a rolling surface (109a) designed to come into contact with the ground. Circumferential grooves which are connected by transverse notches (not represented in Fig. 1) so as to define a plurality of blocks of various shapes and sizes distributed over the rolling surface (109a) are generally made in this surface (109a) , which is represented for simplicity in Fig. 1 as being smooth.
A tread underlayer (111) is placed between the belt structure (106) and the tread band (109) .
As represented in Fig. 1, the tread underlayer (111) may have uniform thickness.
Alternatively, the tread underlayer (111) may have a variable thickness in the transversal direction. For example, the thickness may be greater near its outer edges than at a central zone.
In Fig. 1, said tread underlayer (111) extends over a surface substantially corresponding to the surface of development of said belt structure (106) . Alternatively, said tread underlayer (111) extends only along at least one portion of the development of said belt structure (106) , for instance at opposite side portions of said belt structure (106) (not represented in Fig. 1) .
A strip made of elastomeric material (110) , commonly known as a "mini-sidewall", may optionally be present in the connecting zone between the sidewalls
(108) and the tread band (109) , this mini-sidewall generally being obtained by co-extrusion with the tread band and allowing an improvement in the mechanical interaction between the tread band (109) and the sidewalls (108) . Alternatively, the end portion of the sidewall (108) directly covers the lateral edge of the tread band (109) .
In the case of tubeless tires, a rubber layer (112) generally known as a liner, which provides the necessary impermeability to the inflation air of the tire, may also be provided in a radially internal position relative to the carcass ply (101) .
The process for producing the tire according to the present invention may be carried out according to techniques and using apparatus that are known in the art, as described, for example, in European Patents EP 199,064, or in United States Patent US 4,872,822, or US 4,768,937, said process including manufacturing the crude tire and subsequently moulding and vulcanizing the crude tire.
With reference to Fig. 2, the production plant
(200) includes an extruder (201) suitable for carrying out the process for the preparation of the elastomeric polymer grafted with at least one phenolic resin according to the present invention. As schematically
shown in Fig. 2, by means of feed hopper (206) the extruder (201) is fed with the compounds necessary for producing said grafted elastomeric polymer. Preferably, the extruder is a co-rotating twin screw extruder. According to one embodiment, a previously made elastomeric polymer containing at least one functional group (such as, for example, a functional group derived from maleic anhydride or dithiodipropionic acid) (202) and a phenolic resin (203) , are fed to the extruder through a feed hopper (206) . Alternatively, the compounds may be fed to the extruder (201) through different feed hoppers (not represented in Fig. 2) .
Each flow (202) and (203), is fed to the feed hopper (206) by means of different metering devices (205) . Preferably said metering devices are loss-in- weight gravimetric feeders. Alternatively, each flow
(202) and (203) , may be fed to the feed hopper (206) by means of the same metering device (205) (not represented in Fig. 2) . Alternatively, the phenolic resin (203) , may be in a molten state and may be injected to the extruder (201) by means of a gravimetrically controlled feeding pump (not represented in Fig. 2) .
Alternatively, the elastomeric polymer, the at least one functionalized monomer (such as, for example, maleic anhydride or dithiodipropionic acid) and the phenolic resin, may be fed to the extruder (201) through a feed hopper (206) by means of a metering device (205) (not represented in Fig. 2) . Fig. 2 shows also a degassing unit schematically indicated by reference sign (208) from which a flow of the gases possibly generated during extrusion (207) exits .
The resulting elastomeric polymer grafted with at least one phenolic resin (210) is discharged from the extruder (201), e.g. in the form of a continuous
strand, by pumping it through an extruder die (209) and is conveyed to a cooling device (211) . A gear pump (not represented in Fig. 2) may be provided before said extruder die (209) . After cooling, the resulting elastomeric polymer including at least one phenolic resin may be granulated by means of a grinding device (not represented in Fig. 2) .
Alternatively, the elastomeric polymer grafted with at least one phenolic resin (210) is discharged from the extruder (201) in the form of a subdivided product by pumpimg it through an extruder die (209) which may be provided with a perforated die plate equipped with knives (not represented in Fig. 2) . The obtained subdivided product may be, e.g. in a granular form, with an average diameter of the granules generally of from 0.5 mm to about 3 mm, preferably of from 1 mm to 2 mm, and a length generally of from about 1 mm to 4 mm, preferably of from 1.5 mm to 3 mm.
The present invention will be further illustrated below by means of a number of preparation examples, which are given for purely indicative purposes and without any limitation of this invention. EXAMPLE 1 Preparation of the elastomeric polymer grafted with phenolic resin in a twin-screw extruder
The amounts of the components used are given in Table 1 (the amounts of the various components are given in phr) .
TABLE 1
IR-g-MAH: functionalized cis-1, 4-polyisoprene
obtained as below disclosed; phenolic resin: octylphenol-formaldehyde resin (SP-
1068 - Schenectady International) . (a) Preparation of IR-g-MAH The cis-l-4-polyisoprene (SKI3
Nizhnekamskneftechim Export) was obtained in the form of granules having an average particles size diameter of about 3 mm - 20 mm, by means of a rubber grinder. The so obtained granules (100 phr) and maleic anhydride (2 phr) , also in a granular form, were fed to the feed hopper of a co-rotating twin-screw extruder having a nominal screw diameter of 40 mm and a L/D ratio of 48. The maximum temperature in the extruder was 2200C. The extrusion head was kept at a temperature of 1000C. The obtained elastomeric polymer was discharged from the extruder in the form of a continuous strand, was cooled at room temperature (230C) in a cooling device and granulated. A sample of the obtained elastomeric polymer was subjected to FTIR analysis below disclosed in order to evaluate the presence of the grafted maleic anhydride. FTIR analysis
A sample of the elastomeric polymer (0.5 g) was placed in a wire netting and compressed, at 15 tons, for 5 min, at 700C, in a Carver Laboratory press, to obtain a supported thin layer of the elastomeric polymer. Subsequently, the obtained supported thin layer of the elastomeric polymer, was put in a ASE 100 Accelerated Solvent Extractor from Dionex in order to extract the non-grafted maleic anhydride. The extraction was carried out in an acetone solution, at a temperature of 1200C, at a pressure of 1500 psi, for a time of 20 min.
Subsequently, the extracted elastomeric polymer was dissolved in a dichloromethane solution to obtain a viscous solution which was spread onto a sodium
chloride lamina. The spread lamina was heated, at 5O0C, for 30 min, under vacuum, to obtain a supported thin film of the elastomeric polymer.
The obtained supported thin film of the elastomeric polymer, was subjected to FTIR analysis which was carried out by means of a Perkin-Elmer Spectrum One FTIR Spectrometer. The presence of a band at 1700 cm"1 confirms the grafting of maleic anhydride. (b) Grafting of phenolic resin The functionalized cis-1, 4-polyisoprene (IR-g-MAH) obtained as above disclosed and the phenolic resin were fed to the feed hopper of a co-rotating twin-screw extruder having a nominal screw diameter of 40 mm and a L/D ratio of 48. The maximum temperature in the extruder was 1800C. The extrusion head was kept at a temperature of 900C.
The obtained elastomeric polymer was discharged from the extruder in the form of a continuous strand, was cooled at room temperature (230C) in a cooling device and granulated. A sample of the obtained elastomeric polymer was subjected to FTIR analysis below disclosed in order to evaluate the presence of the grafted phenolic resin. FTIR analysis A sample of the elastomeric polymer (0.5 g) was placed in a wire netting and compressed, at 15 tons, for 5 min, at 7O0C, in a Carver Laboratory press, to obtain a supported thin layer of the elastomeric polymer. Subsequently, the obtained supported thin layer of the elastomeric polymer, was put in a ASE 100
Accelerated Solvent Extractor from Dionex in order to extract the non-grafted phenolic resin. The extraction was carried out in an acetone solution, at a temperature of 1200C, at a pressure of 1500 psi, for a time of 20 min.
Subsequently, the extracted elastomeric polymer was dissolved in a dichloromethane solution to obtain a viscous solution which was spread onto a sodium chloride lamina. The spread lamina which was heated, at 50°C, for 30 min, under vacuum, to obtain a supported thin layer of the elastomeric polymer.
The obtained supported thin layer of the elastomeric polymer, was subjected to FTIR analysis which was carried out by means of a Perkin-Elmer Spectrum One FTIR Spectrometer. The presence of a band at 1700 cm"1 confirms the grafting of maleic anhydride, while the presence of a broad band at 1250 cm"1 - 1260 cm"1 confirms the grafting of phenolic resin. EXAMPLES 2-4 Preparation of the elastomeric compositions
The elastomeric compositions given in Table 2 were prepared as follows (the amounts of the various components are given in phr) .
All the components, except accelerator (TBBS), retardant (PVI) , and sulfur, were mixed together in an internal mixer (model Pomini PL 1.6) for about 5 min (1st Step) . As soon as the temperature reached 145+50C, the elastomeric composition was discharged. The accelerator (TBBS) , retardant (PVI) , and sulfur, were then added and mixing was carried out in an open roll mixer (2nd Step) .
TABLE 2
(*) : comparative.
IR: cis-1, 4-polyisoprene (SKI3 - Nizhnekamskneftechim
Export) ;
Vulcan® 1345: carbon black (Cabot Corp.); IR-g-MAH: functionalized cis-1, 4-polyisoprene obtained as disclosed in Example 1; Elastomeric polymer of Example 1: elastomeric polymer grafted with phenolic resin obtained as disclosed in Example 1 ; Wax: composition of microcrystalline wax (Antilux®
654 - Lanxess) ; phenolic resin: octylphenol- formaldehyde resin (SP-1068
- Schenectady International) ;
Polyplastol* 6: mixture of zinc salts of fatty acids (palmitic acid, stearic acid and oleic acid being present in major amount) (Great Lakes Chemical Corp . ) ; 6-PPD (antioxidant): N- (1, 3-dimethylbutyl) -N' -p- phenylenediamine; TMQ (anti-ageing): polymerized 2, 2 , 4-trimethyl-l, 2- dihydroquinoline (Vulcanox® HS/LG - Lanxess) ; TBBS (accelerator) : N-t-butyl-2-benzothiazyl- sulfenamide (Vulkacit8 NZ/ECG - Lanxess) ;
PVI (retardant) : N- (cyclohexylthio)phthalimide (Santogard PVI - Flexsys) .
The static mechanical properties according to
Standard ISO 37:1994 were measured on samples of the abovementioned elastomeric compositions vulcanized at
1510C, for 30 min. The results obtained are given in
Table 3.
Table 3 also shows the dynamic mechanical properties, measured using an Instron dynamic device in the traction-compression mode according to the following methods. A test piece of the crosslinked elastomeric composition (vulcanized at 151°C, for 30 min) having a cylindrical form (length = 25 mm,- diameter = 12 mm) , compression-preloaded up to a 10% longitudinal deformation with respect to the initial length, and kept at the prefixed temperature (230C,
700C, or 1000C) for the whole duration of the test, was submitted to a dynamic sinusoidal strain having an amplitude of ±3.5% with respect to the length under pre-load, with a 100 Hz frequency. The dynamic mechanical properties are expressed in terms of dynamic elastic modulus (E') and Tan delta (loss factor) values.
The Tan delta value is calculated as a ratio between viscous modulus (E") and elastic modulus (E') . Finally, Table 3 also show the DIN abrasion: the data (expressed in mm3) correspond to the amount of
elastomeric composition removed by operating under the standard conditions given in DIN standard 53516.
TABLE 3
*: comparative.
EXAMPLE 5
Preparation of the elastomeric polymer grafted with phenolic resin in a twin-screw extruder
The amounts of the components used are given in Table 4 (the amounts of the various components are given in phr) .
TABLE 4
SBR-g-MAH: functionalized solution styrene/1,3- butadiene copolymer obtained as below disclosed; phenolic resin: octylphenol-formaldehyde resin
(SP-1068 - Schenectady International) . (a) Preparation of S-SBR-g-MAH
The preparation of S-SBR-g-MAH was carried out as disclosed in Example 1 above reported, the only differences being the following: solution styrene/1 , 3 -butadiene copolymer having a styrene content of 36% by weight and a vinyl content of 27.5% by weight, with respect to the total copolymer weight, and containing 37.5 phr of aromatic oil (HP752 - Japan Synthetic Rubber) : 100 phr; maleic anhydride: 3 phr; extrusion head: kept at a temperature of 8O0C. A sample of the obtained elastomeric polymer was subjected to FTIR analysis below disclosed in order to evaluate the presence of the grafted maleic anhydride. FTIR analysis
A sample of the elastomeric polymer (0.5 g) was placed in a wire netting and compressed, at 15 tons, for 5 min, at 700C, in a Carver Laboratory press, to obtain a supported thin layer of the elastomeric polymer. Subsequently, the obtained supported thin layer of the elastomeric polymer, was put in a ASE* 100
Accelerated Solvent Extractor from Dionex in order to extract the non-grafted maleic anhydride. The extraction was carried out in a toluene :ethanol (30:70)
solution, at a temperature of 1300C, at a pressure of 1500 psi, for a time of 20 min.
Subsequently, the extracted elastomeric polymer was dissolved in a dichloromethane solution to obtain a viscous solution which was spread onto a sodium chloride lamina. The spread lamina was heated, at 500C, for 30 min, under vacuum, to obtain a supported thin layer of the elastomeric polymer.
The obtained supported thin layer of the elastomeric polymer, was subjected to FTIR analysis which was carried out by means of a Perkin-Elmer Spectrum One FTIR Spectrometer. The presence of a band at 1700 cm"1 confirms the grafting of maleic anhydride. (b) Grafting of phenolic resin The grafting of phenolic resin onto the functionalized solution stryrene-1, 3 -butadiene copolymer (S-SBR-g-MAH) obtained as above disclosed was carried out as disclosed in the Example 1 above reported. A sample of the obtained elastomeric polymer was subjected to FTIR analysis below disclosed in order to evaluate the presence of the grafted phenolic resin. FTIR analysis
A sample of the elastomeric polymer (0.5 g) was placed in a wire netting and compressed, at 15 tons, for 5 min, at 70°C, in a Carver Laboratory press, to obtain a supported thin layer of the elastomeric polymer. Subsequently, the obtained supported thin layer of the elastomeric polymer, was put in a ASE 100 Accelerated Solvent Extractor from Dionex in order to extract the non-grafted phenolic resin. The extraction was carried out in a toluene :ethanol (30:70) solution, at a temperature of 13O0C, at a pressure of 1500 psi, for a time of 20 min. Subsequently, the extracted elastomeric polymer was dissolved in a dichloromethane solution to obtain a
viscous solution which was spread onto a sodium chloride lamina. The spread lamina was heated, at 500C, for 30 min, under vacuum, to obtain a supported thin layer of the elastomeric polymer. The obtained supported thin layer of the elastomeric polymer, was subjected to FTIR analysis which was carried out by means of a Perkin-Elmer Spectrum One FTIR Spectrometer. The presence of a band at 1700 cm"1 confirms the grafting of maleic anhydride, while the presence of a broad band at 1250 cm"1 - 1260 cm"1 confirms the grafting of phenolic resin. EXAMPLES 6-8 Preparation of the elastomeric compositions
The elastomeric compositions given in Table 5 were prepared as follows (the amounts of the various components are given in phr) .
All the components, except accelerators (CBS and DPG80) and sulfur, were mixed together in an internal mixer (model Pomini PL 1.6) for about 5 min (1st Step) . As soon as the temperature reached 145±5°C, the elastomeric composition was discharged. The accelerator (CBS and DPG80) and sulfur, were then added and mixing was carried out in an open roll mixer (2nd Step) .
TABLE 5
(*) : comparative.
S-SBR: solution styrene/l , 3 -butadiene copolymer having a styrene content of 36% by weight and a vinyl content of 27.5% by weight, with respect to the total copolymer weight and containing 37.5 phr of aromatic oil (HP752 - Japan Synthetic Rubber) ;
STR20: natural rubber (SRI Trang Agroindustry) ;
BR: polybutadiene (Europrene Neocis - Polimeri Europa) ;
HV 3396: carbon black (Columbian);
S-SBR-g-MAH: functionalized solution styrene/1,3- butadiene copolymer obtained as disclosed in Example 5;
Elastomeric polymer of Example 5 : elastomeric polymer grafted with a phenolic resin obtained as disclosed in Example 5 ;
X50Sβ: silane coupling agent comprising 50% by weight of carbon black and 50% by weight of bis (3-triethoxysilylpropyl) tetrasulphide (Degussa-
Hϋls) ; PolyplastolΦ 6 : mixture of zinc salts of fatty acids
(palmitic acid, stearic acid and oleic acid being present in major amount) (Great Lakes Chemical
Corp . ) ;
ZeosilΦ MP 1165: silica (Rhodia) ; Wax: composition of microcrystalline wax (Antilux®
654 - Lanxess) ; TMQ (anti-ageing): polymerized 2, 2 , 4-trimethyl-l, 2- dihydroquinoline (VulcanoχΦ HS/LG - Lanxess) ; phenolic resin: octylphenol-formaldehyde resin (SP-1068
- Schenectady International) ;
6-PPD (antioxidant): N- (1 , 3-dimethylbutyl) -N' -p- phenylenediamine;
CBS (accelerator) : N-cyclohexyl-2-benzothiazyl- sulphenamide (Vulkacit* CZ/C - Lanxess) ; DPG80 (accelerator) : diphenyl guanidine (Rhenogran®
DPG80 - Rhein Chemie) . The static mechanical properties according to Standard ISO 37:1994 were measured on samples of the abovementioned elastomeric compositions vulcanized at 1700C, for 10 min. The results obtained are given in Table 6. Table 6 also shows the dynamic mechanical properties, measured using an Instron dynamic device in
the traction-compression mode according to the following methods. A test piece of the crosslinked elastomeric composition (vulcanized at 17O0C, for 10 min) having a cylindrical form (length = 25 mm; diameter = 12 mm) , compression-preloaded up to a 10% longitudinal deformation with respect to the initial length, and kept at the prefixed temperature (230C, 700C, or 1000C) for the whole duration of the test, was submitted to a dynamic sinusoidal strain having an amplitude of ±3.5% with respect to the length under pre-load, with a 100 Hz frequency. The dynamic mechanical properties are expressed in terms of dynamic elastic modulus (E') and Tan delta (loss factor) values. The Tan delta value is calculated as a ratio between viscous modulus (E") and elastic modulus (E') .
Finally, Table 6 also show the DIN abrasion: the data (expressed in mm3) correspond to the amount of elastomeric composition removed by operating under the standard conditions given in DIN standard 53516.
TABLE 6
*: comparative.
EXAMPLE 9
Preparation of the elastomeric polymer grafted with phenolic resin in a twin-screw extruder
The amounts of the components used are given in Table 7 (the amounts of the various components are given in phr) .
TABLE 7
SBR-g-MAH: functionalized solution styrene/l, 3- butadiene copolymer obtained as below disclosed; phenolic resin: octylphenol-formaldehyde resin containing methylol groups (SP-1045 - Schenectady International) .
(a) Preparation of S-SBR-g-MAH
The preparation of the S-SBR-g-MAH was carried as disclosed in Example 1 above reported, the only- differences being the following: solution styrene/l , 3 -butadiene having a styrene content of 25% by weight and a vinyl content of 47% by weight, with respect to the total copolymer weight, and containing 37.5 phr of TDAE oil (SE
SLR-4630 - Dow Chemical) : 100 phr; maximum temperature in the extruder: 1800C; extrusion head: kept at a temperature of 800C.
A sample of the obtained elastomeric polymer was subjected to FTIR analysis. The FTIR analysis was carried out as disclosed in Example 5 above reported.
The presence of a band at 1700 cm"1 confirms the grafting of maleic anhydride.
(b) Grafting of phenolic resin The grafting of phenolic resin onto the functionalized solution styrene/l, 3 -butadiene copolymer (S-SBR-g-MAH) obtained as above disclosed was carried out as disclosed in Example 1 above reported the only difference being the following: - extrusion head: kept at a temperature of 8O0C.
A sample of the obtained elastomeric polymer was subjected to FTIR analysis. The FTIR analysis was carried out as disclosed in Example 5 above reported. The presence of a band at 1700 cm"1 confirms the grafting of maleic anhydride, while the presence of a broad band at 1250 cm"1 - 1260 cm"1 confirms the grafting of phenolic resin. EXAMPLES 10-12 Preparation of the elastomeric compositions The elastomeric compositions given in Table 8 were prepared as follows (the amounts of the various components are given in phr) .
All the components, except accelerator (CBS, DPG80) and sulfur, were mixed together in an internal mixer (model Pomini PL 1.6) for about 5 min (1st Step) . As soon as the temperature reached 145±5°C, the elastomeric composition was discharged. The accelerators (CBS and DPG80) and sulfur, were then added and mixing was carried out in an open roll mixer (2nd Step) .
TABLE 8
(*) : comparative.
S-SBR: solution styrene/1, 3 -butadiene copolymer, having a styrene content of 25% by weight and a vinyl content of 47% by weight, with respect to the total copolymer weight, and containing 37.5 phr of TDAE oil (SE SLR-4630 - Dow Chemical) ;
STR20: natural rubber (SRI Trang Agroindustry) ;
BR: polybutadiene (Europrene Neocis - Polimeri Europa) ;
HV 3396: carbon black (Columbian);
S-SBR-g-MAH: functionalized solution styrene/1,3- butadiene copolymer obtained as disclosed in Example 9;
Elastomeric polymer of Example 9: elastomeric polymer grafted with a phenolic resin obtained as disclosed in Example 9;
X50SΦ: silane coupling agent comprising 50% by weight of carbon black and 50% by weight of bis (3-triethoxysilylpropyl) tetrasulphide (Degussa-
Hϋls) ; Polyplastol 6: mixture of zinc salts of fatty acids
(palmitic acid, stearic acid and oleic acid being present in major amount) (Great Lakes Chemical
Corp . ) ;
Zeosile MP 1165: silica (Rhodia) ; Wax: composition of microcrystalline wax (Antilux
654 - Lanxess) ; TMQ (anti-ageing): polymerized 2 , 2 , 4-trimethyl-l, 2- dihydroquinoline (Vulcanox® HS/LG - Lanxess) ; phenolic resin: octylphenol-formaldehyde resin containing methylol groups (SP-1045 - Schenectady
International) ; 6-PPD (antioxidant): N- (1, 3-dimethylbutyl) -N' -p- phenylenediamine ; CBS (accelerator) : N-cyclohexyl-2-benzothiazyl- sulphenamide (Vulkacit CZ/C - Lanxess) ;
DPG80 (accelerator) : diphenyl guanidine (Rhenogran® DPG80 - Rhein Chemie) .
The static mechanical properties, the dynamic mechanical properties, as well as the DIN abrasion, were measured as disclosed in Example 5 above reported. The results obtained are given in Table 9.
TABLE 9
(*) comparative. EXAMPLE 13
Preparation of the elastomeric polymer grafted with phenolic resin in a twin-screw extruder
The amounts of the components used are given in Table 10 (the amounts of the various components are given in phr) .
TABLE 10
S-SBR-g-DTDP: functionalized solution styrene/1,3- butadiene copolymer obtained as below disclosed; phenolic resin: octylphenol-formaldehyde resin (SP-1068
- Schenectady International) . (a) Preparation of S-SBR-g-DTDP
The preparation of S-SBR-g-DTDP was carried out as disclosed in Example 1 above reported, the only differences being the following: solution styrene/1, 3 -butadiene copolymer having a styrene content of 36% by weight and a vinyl content of 27.5% by weight, with respect to the total copolymer weight, and containing 37.5 phr of aromatic oil (HP752 - Japan Synthetic Rubber) : 100 phr; dithiodipropionic acid: 3 phr; maximum temperature in the extruder: 1800C; extrusion head: kept at a temperature of 800C. A sample of the obtained elastomeric polymer was subjected to 1H-NMR analysis below disclosed in order to evaluate the presence of the grafted dithiodipronic acid .
1H-NMR analysis A sample of the elastomeric polymer (0.5 g) was placed in a wire netting and compressed, at 15 tons, for 5 min, at 700C, in a Carver Laboratory press, to obtain a supported thin layer of the elastomeric polymer. Subsequently, the obtained supported thin layer of the elastomeric polymer, was put in a ASE* 100 Accelerated Solvent Extractor from Dionex in order to
extract the non-grafted dithiodipropionic acid. The extraction was carried out in a toluene :ethanol (30:70) solution, at a temperature of 13O0C, at a pressure of 1500 psi, for a time of 20 min. Subsequently, the extracted elastomeric polymer was dissolved in a dichloromethane solution and subsequently treated with a diazomethane in order to perform the esterification (methylation) of the acid group . The obtained compound was subjected to proton nuclear magnetic resonance (1H-NMR) analysis which was carried out on Bruker 400 MHz instruments operating at the following conditions:
CDCl3 solution; - temperature of 25°C;
64 scans with a delay of 3 sec.
The grafting of dithiodipropionic acid was confirmed by the presence of signals at 2.95 ppm (α) , 2.80 ppm (β) and 3.7 ppm (γ) [-SCH2 (β) CH2 (α) -COOCH3 (γ) ]. (b) Grafting of phenolic resin
The grafting of phenolic resin onto the functionalized solution styrene/1 , 3 -butadiene copolymer
(S-SBR-g-DTDP) obtained as above disclosed, was carried out as disclosed in Example 1 above reported, the only difference being the following: extrusion head: kept at a temperature of 800C.
A sample of the obtained elastomeric polymer was subjected to 1H-NMR analysis below disclosed in order to evaluate the presence of the grafted phenolic resin. 1H-NMR analysis
A sample of the elastomeric polymer (0.5 g) was placed in a wire netting and compressed, at 15 tons, for 5 min, at 700C, in a Carver Laboratory press, to obtain a supported thin layer of the elastomeric polymer. Subsequently, the obtained supported thin layer of the elastomeric polymer, was put in a ASE® 100
Accelerated Solvent Extractor from Dionex in order to extract the non-grafted phenolic resin. The extraction was carried out in a toluene rethanol (30:70) solution, at a temperature of 1300C, at a pressure of 1500 psi, for a time of 20 min.
Subsequently, the extracted elastomeric polymer was dissolved in a dichloromethane solution and subsequently treated with a diazomethane in order to perform the esterification (methylation) of the acid group.
The obtained compound was subjected to proton nuclear magnetic resonance (1H-NMR) analysis which was carried out on Bruker 400 MHz instruments operating at the following conditions: - CDCl3 solution; temperature of 250C;
64 scans with a delay of 3 sec.
The grafting of dithiodipropionic acid was confirmed by the presence of signals at 2.95 ppm (α) , 2.80 ppm (β) and 3.7 ppm (γ) [-SCH2 (β) CH2 (α) -COOCH3 (γ) ], while the grafting of the phenolic resin was confirmed by the presence of a signal at 3.8 ppm [methylene (-CH2-) group linked to phenolic group) . EXAMPLES 14-16 Preparation of the elastomeric compositions
The elastomeric compositions given in Table 11 were prepared as follows (the amounts of the various components are given in phr) .
All the components, except accelerator (CBS, DPG80) and sulfur, were mixed together in an internal mixer
(model Pomini PL 1.6) for about 5 min (1st Step). As soon as the temperature reached 145±5°C, the elastomeric composition was discharged. The accelerators (CBS and DPG80) and sulfur, were then added and mixing was carried out in an open roll mixer
(2nd Step) .
TABLE 11
(*) : comparative.
S-SBR: solution styrene/1 , 3 -butadiene copolymer having a styrene content of 36% by weight and a vinyl content of 27.5% by weight, with respect to the total copolymer weight, and containing 37.5 phr of aromatic oil (HP752 - Japan Synthetic Rubber) ;
STR20: natural rubber (SR Trang Agroindustry) ;
BR: polybutadiene (Europrene Neocis - Polimeri Europa) ;
HV 3396: carbon black (Columbian);
S-SBR-g-DTDP: functionalized solution styrene/1,3- butadiene copolymer obtained as disclosed in Example 13;
Elastomeric polymer of Example 13: elastomeric polymer grafted with dithiodipropionic acid obtained as disclosed in Example 13; DTDP: dithiodipropionic acid; X50S : silane coupling agent comprising 50% by weight of carbon black and 50% by weight of bis (3-triethoxysilylpropyl) tetrasulphide (Degussa-
Hϋls) ;
Polyplastol0 6 : mixture of zinc salts of fatty acids (palmitic acid, stearic acid and oleic acid being present in major amount) (Great Lakes Chemical
Corp . ) ;
Zeosil 1165: silica (Rhodia) ;
Wax: composition of microcrystalline wax (Antilux" 654 - Lanxess) ;
TMQ (anti-ageing): polymerized 2 , 2 , 4-trimethyl-l, 2- dihydroquinoline (Vulcanox* HS/LG - Lanxess) ; phenolic resin: octylphenol-formaldehyde resin (SP-1068
- Schenectady International) ; 6-PPD (antioxidant): N- (1, 3-dimethylbutyl) -N' -p- phenylenediamine; CBS (accelerator) : N-cyclohexyl-2-benzothiazyl- sulphenamide (Vulkacit CZ/C - Lanxess) ;
DPG80 (accelerator) :diphenyl guanidine (Rhenogran® DPG80 - Rhein Chemie) .
The static mechanical properties, the dynamic mechanical properties, as well as the DIN abrasion, were measured as disclosed in Example 5 above reported. The results obtained are given in Table 12.
TABLE 12
( * ) comparat ive .