Patent Application
20110183875
The present invention relates to vulcanisable guanidine-free mixtures containing ethylene acrylate (AEM), polyacrylate (ACM) and/or hydrogenated acrylonitrile (HNBR)-based rubber compounds having an improved scorch resistance, to vulcanisates, prepared by cross-linking this vulcanisable mixtures and their use in automotive, oil-field and/or off-shore applications.
The demand for high performance elastomers in automotive and industrial applications has considerably increased due to special requirements as well as the complex design of the automotive components. Novel materials are strongly requested, which fulfill these requirements as well as an improved scorch resistance.
Ethylene acrylate (AEM) elastomers and polyacrylate (ACM) elastomers comprising small amounts of a butene dioic acid monoalkyl ester cure-site monomer are widely used in the automotive industry due to their excellent resistance to lubricating oils and greases, heat and compression set resistance, mechanical toughness and their low brittle point. As such, they are well suited for gaskets and seals, various types of automotive hoses, spark plug boots and similar engine compartment rubber components.
Typically those products are produced by cross-linking a blend of the uncrosslinked (i.e. unvulcanized gum rubber) copolymer and a diamine curing agent along with various fillers and other additives in a press-curing step at sufficient time, temperature and pressure to achieve covalent chemical bonding.
A curative system consisting of an AEM-terpolymer, hexamethylene diamine carbamate (HMDC) as a curing agent in combination with a guanidine as an accelerator is well established. Different guanidine derivatives are in use depending on the intended application. This means that i.e. diphenyl guanidine (DPG) is preferred, if good flex resistance and elongation are required or di-o-tolylguanidine (DOTG), if the best compression set is requested.
HNBR-polymers can be vulcanized i.e. according to JP 2008-056793A. AEM- or ACM-based polymers can be vulcanized by using hexamethylene diamine carbamate (HMDC) as a curing agent in combination with guanidine as an accelerator.
Systems containing guanidine as an accelerator are well known, but these guanidines have been the subject to public debates for their hazardous potential. Guanidine raised questions concerning the medical and toxicological aspects in the workplace area. Several studies conducted with regard to the vulcanisation mechanisms with guanidine accelerators have shown that at elevated temperatures during vulcanisation, reaction products such as aromatic amines (e.g. aniline or o-toluidine) have to be considered.
JP A-50-45031 proposes an elastomer composition obtained by mixing hexamethylene diamine or hexamethylene diamine carbamate as a vulcaniser and 4,4′-methylenedianiline as an accelerator with an acrylate butenedioic acid monoester bipolymer or an ethylene-acrylate-butanedioic acid monoester terpolymer to achieve good compression set characteristics. The aromatic amine accelerator 4,4′-methylenedianiline in itself, like aniline or o-toluidine, is problematic due to its carcinogenic and toxicological potential. Some of these aromatic amines have been classified as unequivocally carcinogenic and are therefore included in the first category of the hazardous materials list for this reason. O-toluidine for example was classified as a category 1 carcinogen in the 2006 MAK and BAT Value List of the Deutsche Forschungsgemeinschaft (German Research Foundation). This listing is the basis for the legislative process of classifying substances according to their risk potential. Substances which are listed as carcinogen class 1 or which are known for releasing such a substance as a by-product during use should be avoided, as they might have a negative impact on human health and there is a high likelihood that they will be included in the list of substances that need special authorization under REACH. Extended studies focused on the noxious effects of o-toluidine on the human health have underlined the necessity of the development of less hazardous alternatives for this accelerator. O-toluidine is also released from rubbers that contain di-o-tolylguanidine (DOTG) as an accelerator only in small amounts.
Because of the aforementioned risks for human health with the guanidine based accelerator systems, alternative systems for accelerating the diamine cure have been introduced. One alternative system of vulcanisation accelerators is described in EP-A 2033989. This relates to a composition of vulcanisation accelerators, comprising
However, all guanidine replacements including the above-mentioned composition of vulcanisation accelerators show significantly less scorch safety. This on the other hand has unwanted implications on the processing of the compounds in the production plant.
An object of the present invention therefore was to provide an alternative accelerator system for the diamine crosslinking system, which does not contain guanidines and—at the same time—lead to a high scorch safety and thus lead to a manageable vulcanisation process.
Surprisingly, it has now been found that guanidin-free vulcanisable mixtures containing ethylene acrylate (AEM), polyacrylate (ACM) and/or hydrogenated acrylonitrile (HNBR)-based rubbers and a mixture of certain accelerators and retarders achieve this objective.
The present invention therefore provides guanidine-free vulcanisable mixtures containing ethylene acrylate (AEM), polyacrylate (ACM) and/or hydrogenated acrylnitrile (HNBR)-based rubbers and at least one vulcanisation accelerator selected from a C1-C12 non aromatic amine, an amidine as well as salts and any mixtures thereof, and at least one retarder system comprising benzoic acid, salicylic acid, phthalic acid, phthalic acid anhydride and/or C6-C24-dicarboxylic acid (a), and/or carbodiimide (b) and/or a polycarbodiimide (c) and any mixtures of the above-mentioned retarders.
The polymers AEM, ACM and/or HNBR are well known in the art, either commercially available or may be produced by a person skilled in the art according to processes well described in the literature.
These known AEM-systems and/or ACM-systems, are for example disclosed in EP 1 378 539 A (ACM rubber systems), U.S. Pat. No. 2,599,123 (AEM rubber systems) and EP 1 499 670 A (AEM rubber systems), which are incorporated by reference into the present invention.
Furthermore, respective ACM rubbers are commercially available from Unimatec® under the trademark Noxtite® or from Zeon® under the trademark HY Temp® AR Polymer and respective AEM-rubbers are commercially available from DuPont under the trademark Vamac® Polymer.
Hydrogenated acrylonitrile (HNBR)-based rubbers according to the invention are described in EP 08022135.1 and EP 09164539.0.
In one preferred embodiment of the present invention the hydrogenated acrylonitrile (HNBR)-based polymer system is a vulcanisable polymer composition comprising
a polymer having a main polymer chain derived from
(ia) at least 25% to 95% by weight, preferably 25 to 85% by weight, more preferably 30 to 80% by weight, and particularly preferably 45 to 75% by weight, of at least one diene monomer, like i.e. 1,3-butadiene, isoprene, 2,3-dimethyl-1,3-butadiene, and 1,3-pentadiene based on the polymer, and
(ib) in the range of from 0.1 to 74.9% by weight, preferably 10 to 60% by weight, more preferably 15 to 55% by weight, particularly preferably 20 to 50% by weight, of an α,βethylenically unsaturated nitrile monomer, like i.e. acrylonitrile, α-alkylacrylonitril, with alkyl ═C1-C12-alkyl, and/or α-haloacrylonitriles, with halo ═F, Cl, Br and I, based on the polymer, and
(ic) in the range of from 0.1 to 20% by weight, preferably 0.5 to 20% by weight, more preferably 1 to 15% by weight, particularly preferably 1.5 to 10% by weight of at least one α,β-ethylenically unsaturated dicarboxylic acid monoester monomer, α,β-ethylenically unsaturated dicarboxylic acid monomer, α,β-ethylenically unsaturated dicarboxylic acid anhydride monomer or α,β-ethylenically unsaturated dicarboxylic acid diester as a third monomer,
wherein the sum of all monomer units mentioned under (ia), (ib) and (ic) is 100% by weight, as disclosed in EP 08022135.1 and EP 09164539.0, which are incorporated by reference into the present invention.
A particularly preferred polymer composition according to the present invention comprises:
(i) an optionally hydrogenated nitrile polymer derived from
The hydrogenated nitrile rubber may contain repeating units of other monomer units than those (ia), (ib) and (ic) which can be copolymerised with the various aforesaid monomer units, namely and in particular with the diene monomer, the αβ-ethylenically unsaturated nitrile monomer, the αβ-ethylenically unsaturated dicarboxylic acid monoester monomer. As such other monomers, αβ-ethylenically unsaturated carboxylate esters (other than αβ-ethylenically unsaturated dicarboxylic acid monoester), aromatic vinyl, fluorine-containing vinyl, αβ-ethylenically unsaturated monocarboxylic acid, and copolymerisable antiaging agent may be used.
As additional αβ-ethylenically unsaturated carboxylate ester monomers (other than αβ-ethylenically unsaturated dicarboxylic acid monoester), for example, alkyl acrylate ester and alkyl methacrylate ester in which the carbon number of the alkyl group is 1-18 such as methyl acrylate, ethyl acrylate, propyl acrylate, butyl acrylate, n-dodecyl acrylate, methyl methacrylate, ethyl methacrylate and the like; alkoxyalkyl acrylate and alkoxyalkyl methacrylate in which the carbon number of the alkoxyalkyl is 2-12 such as methoxymethyl acrylate, methoxyethyl methacrylate and the like; cyanoalkyl acrylate and cyanoalkyl methacrylate in which the carbon number of the cyanoalkyl group is 2-12 such as α-αcyanoethyl acrylate, β-cyanoethyl acrylate, cyanobutyl methacrylate and the like; hydroxyalkyl acrylate and hydroxyalkyl methacrylate in which the carbon number of the hydroxyalkyl group is 1-12 such as 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, 3-hydroxypropyl acrylate and the like; fluorine-substituted benzyl group-containing acrylate and fluorine-substituted benzyl group-containing methacrylate such as fluorobenzyl acrylate, fluorobenzyl methacrylate and the like; fluoroalkyl group-containing acrylate and fluoroalkyl group-containing methacrylate such as trifluoroethyl acrylate, tetrafluoropropyl methacrylate and the like; unsaturated polycarboxylic acid polyalkyl ester such as dimethyl maleate, dimethyl fumarate, dimethyl itaconate, diethyl itaconate and the like; amino group-containing αβ-ethylenically unsaturated carboxylic acid ester such as dimethylaminomethyl acrylate, diethylaminoethyl acrylate and the like; and the like may be proposed.
The hydrogenation of the copolymer can take place in a manner known to a person skilled in the art. Suitable processes for the hydrogenation of nitrile rubbers are for example described in U.S. Pat. No. 3,700,637, DE-PS 2 539 132, EP-A 134023, DE-A 35 40 918, EP-A 298386, DE-A 35 29 252, DE-A 34 33 392, U.S. Pat. No. 4,464,515 and U.S. Pat. No. 4,503,196.
The process for the production of the aforesaid nitrile rubber is not restricted in particular. In general, a process in which the αβ-ethylenically unsaturated nitrile monomer, αβ-ethylenically unsaturated dicarboxylic acid monoester monomer, diene monomer or α-olefin monomer, and other monomers that can be copolymerized with these which are added in accordance with requirements, are copolymerised is convenient and preferred. As the polymerisation method, any of the well known emulsion polymerisation methods, suspension polymerisation methods, bulk polymerisation methods and solution polymerisation methods can be used, but the emulsion polymerisation method is preferred from the simplicity of the control of the polymerisation reaction. If the content of residual carbon-carbon double bonds in the copolymer obtained by copolymerisation is above the aforesaid range, hydrogenation (hydrogen addition reaction) of the copolymer may be performed. Such hydrogenation processes are not restricted in particular, and well known methods may be adopted.
All the AEM, ACM and HNBR polymers contain optionally at least one antioxidant, filler and/or cross-linking agent as a further component.
Accelerators according to the invention are chemical agents that accelerate the vulcanisation reaction like C1-C12-non-aromatic amines, amidine as well as salts and any mixtures thereof.
As a preferred embodiment of the present invention, the accelerator mixture comprises 1,8-diazabicyclo[5.4.0]undecene-7 (DBU) or 1,5-diazabicyclo[4.3.0]nonene-5 (DBN), 1,4-diazabicyclo-[2.2.2]octane (DABCO) 1,5,7-triazabicyclo[4.4.0]dec-5-ene (TBD) and/or 7-methyl-1,5,7-triazabicyclo[4.4.0]dec-5-ene (MTBD) and its derivatives as an amidine. From these, 1,8-diazabicyclo[5.4.0]undecene-7 is mostly preferred. All these amidines are commercially available products.
The compounds are well know and commercially available, i.e. 1,8-diazabicyclo[5.4.0]undecene-7 (DBU) is commercially available from BASF under the trade mark Lupragen® N700.
C1-C12-non aromatic amines, which can be used according to the invention are all primary, secondary or tertiary alkylamines, like i.e. diethylamine and dicyclohexylamine; butylamine and cyclohexylamine and/or dicyclohexylamine. In terms of safe production processes, amines having a higher flashing point than 100° C. are mostly preferred, like dicyclohexylamine. All the amines are commercially available products.
The vulcanisation accelerator may be contained in the composition according to the present invention in an amount of preferably 0.1 to 10 wt.-%, more preferably 0.5 to 8 wt.-% most preferably 1.0 to 5.0 wt.-%, in each case with respect to the total amount of the polymer in compositions according to the present invention.
A retarder is a chemical agent that slows down a rate determining step in a cascade of chemical reactions. For example, retarders are used to delay the onset of sulfur crosslinking (also known as curing or vulcanisation). A retarder can be useful during compound development as well as an additive to existing formulations to add a few minutes of processing safety (increase Mooney scorch time) to any kind of cure system.
In a preferred embodiment of the present invention, the retarder is used in an amount of from 0.1 to 7 wt.-%, preferably from 0.3 to 5 wt.-%, more preferably from 0.5 to 3 wt.-% based on the total amount of the polymer in compositions according to the present invention.
In one preferred embodiment of the present invention acids are used as retarders according to the invention. Acids (a) according to the invention are benzoic acid, salicylic acid, phthalic acid, phthalic acid anhydride and/or C6-C24-dicarboxylic acid. These acids are commercially available products.
In a further preferred embodiment of the present invention, the retarder is a carbodiimide (b).
If carbodiimides are used in combination with the aforementioned accelerators for example in acrylic polymers, the vulcanisation is delayed and the compound shows an improved scorch resistance.
The carbodiimide compounds used in the present invention, can be synthesized by commonly well known methods or are commercially available. The compound can be obtained, for example, by conducting a decarboxylation condensation reaction of various polyisocyanates using an organophosphorus compound or an organometallic compound as a catalyst at a temperature not lower than about 70° C., without using any solvent or using an inert solvent.
Examples of a monocarbodiimide compound included in the above-described carbodiimide compounds are dicyclohexylcarbodiimide, diisopropylcarbodiimide, dimethylcarbodiimide, diisobutylcarbodiimide, dioctylcarbodiimide, tert.-butylisopropylcarbodiimide, 2,6-diisopropylphenylencarbodiimide, diphenylcarbodiimide, di-tert.-butylcarbodiimide and di-β-naphthylcarbodiimide, and among them, dicyclohexylcarbodiimide or diisopropylcarbodiimide are particularly preferable in view of availability on an industrial scale.
In another embodiment of the present invention polycarbodiimides (c) are used. These polycarbodiimides are commercially available or can be produced by conventional production methods for polycarbodiimides [for example, the methods disclosed in U.S. Pat. No. 2,941,956; JP-B-47-33279, J. Org. Chem. 28, 2069-2075 (1963) and Chemical Review, 1981, Vol. 81, No. 4, pages 619 to 621].
The carbodiimide compound includes in particular 4,4′-dicyclohexylmethanecarbodiimide (degree of polymerization=2 to 20), tetramethylxylylenecarbodiimide (degree of polymerization=2 to 20), N,N-dimethylphenylcarbodiimide (degree of polymerization=2 to 20) and N,N′-di-2,6-diisopropylphenylencarbodiimide (degree of polymerization=2 to 20) and the like, and is not specifically limited as long as the compound has at least one carbodiimide group in a molecule.
Within the meaning of the present invention, suitable carbodiimides are in particular monomeric, dimeric or polymeric carbodiimides.
In the following, some aspects of the preferred carbodiimide compounds are described in detail.
In an preferred embodiment of the invention at least one sterically hindered carbodiimide is used as a retarder.
In another embodiment of the present invention the retarder is at least one monomeric or dimeric carbodiimide.
Preferably at least one dimeric carbodiimid or a polycarbodiimide of the formula (II)
—R′—(N═C═N—R)n—R″ (I)
In a first preferred embodiment of this mode, R represents an aromatic or an aralkylene radical, which, in the case of an aromatic or an aralkylene residue, in at least one ortho-position, preferably in both ortho-positions to the aromatic carbon atom which carries the carbodiimide group, carries aliphatic and/or cycloaliphatic substituents with at least 2 C-atoms, preferably branched or cyclic aliphatic radicals with at least 3 C-atoms, more preferably isopropyl residues.
In particular those carbodiimides of the general formula (I) or (II) are preferred in which the ortho-positions to the aromatic carbon atom which carries the carbodiimide group are substituted by isopropyl and in which the para-positions to the aromatic carbon atom which carries the carbodiimide group are also substituted by isopropyl.
In a further preferred embodiment of the polymeric carbodiimides, R represents an aromatic residue, which is bonded by a C1- to C8-alkyl moiety, preferably a C1 to C4-moiety, with the carbodiimide group.
Furthermore, polymeric aliphatic carbodiimides can be used, for example on the basis of isophorone diamine which is for example commercially available by Nisshinbo.
In this mode of the present invention the carbodiimide is preferably represented by the general formula (II)
in which R1
in which the residues R1 and R4 represent independently from each other a linear branched C2- to C20-cycloalkyl residue, a C6- to C15-aryl residue or a C6 to C15-aralkyl residue.
It is preferred that the residues R1 to R4 are C2- to C20-alkyl or C2- to C20-cycloalkyl residues.
It is further preferred that the residues R1 to R4 are C2 to C20-alkyl residues.
In the present invention, C2- to C20-alkyl and C2- to C20-cycloalkyl stands preferably for ethyl, propyl, isopropyl, sec.-butyl, tert.-butyl, cyclohexyl and/or dodecyl, whereby the residue isopropyl is in particular preferred.
In the present invention, C6- to C15-aryl and C6- to C15-aralkyl stand preferably for phenyl, tolyl, benzyl or naphthyl.
Especially preferred is the use of one monomeric carbodiimide according to formula (III)
The polycarbodiimides (c) used as retarders are commercially available products, for example from Rhein Chemie Rheinau GmbH under the tradenames Stabaxol® P, Stabaxol® P100, Stabaxol® P200 and Stabaxol® P400. Furthermore, respective carbodiimides are commercially available from Raschig under the tradenames Stabilisator 2000, 9000 and 11000.
Alternatively they can be prepared according to methods well known by persons skilled in the art.
To prepare the carbodiimides and/or polycarbodiimides of the general formulas (I)-(II), its mono- or diisocyanates can be condensed as starting compounds at elevated temperatures, for example at 40 to 200° C., in the presence of catalysts with the release of carbon dioxide. Suitable methods are described in DE-A-11 30 594 and in FR 1 180 370.
The polymeric carbodiimides of the general formula (II) may be terminal reacted with isocyanate compounds.
The carbodiimides may also be used as a mixture of different carbodiimides.
In a further embodiment of the present invention, it is also possible that a mixture of different carbodiimides is used. In case a mixture of different carbodiimides is used, the used carbodiimides may be selected from the group consisting of monomeric, dimeric and polymeric carbodiimides. In respect of the monomeric, dimeric and polymeric carbodiimides, it is referred to the explanations above.
Furthermore, it is preferred that the used carbodiimides have a reduced content of free isocyanates. Preferred carbodiimides have a reduced content of free isocyanates lower than 1 wt.-%.
The system according to the present invention is not only understood as a composition in the classical way of understanding, as the definition of a system according to the present invention also comprises the combined or separate use of the system of accelerators and of the retarders in the preparation of polymers at any time during the vulcanisation process of the rubbers.
In one preferred embodiment of the present invention the carbodiimides are used as a mixture of at least two different carbodiimides as a retarder.
The vulcanisation accelerators according to the above-mentioned invention may be deposited on at least one particulate filler such as precipitated and fumed silica, carbon black or other inorganic mineral, or may be used as a polymer bound material.
In another preferred embodiment of the present invention the vulcanisable mixtures further comprise a filler selected from the group consisting of silica, carbon black, clay, talc, aluminum hydroxide, calcium carbonate, and magnesium carbonate.
In another preferred embodiment of the present invention the vulcanisable mixtures further comprise additives selected from the group consisting of dispersants and plasticizers.
Optionally the vulcanisable polymer composition according to the present invention may further comprise one or more additional vulcanizing agents besides the diamine crosslinking agent. Such additional vulcanisation systems are well known in the art and the choice thereof is within the purview of a person skilled in the art.
In one embodiment, an organic peroxide (e.g., dicumyl peroxide or 2,2′-bis(tert-butylperoxy diisopropyl-benzene) may be used as additional vulcanizing agent in the polymer composition according to the present invention.
In another embodiment, sulfur or another conventional sulfur-containing vulcanizing agent or even mixtures thereof may be used as additional vulcanizing agent(s) in the polymer composition according to the present invention. Suitable additional sulfur-containing vulcanizing agents are commercially available, e.g. Vulkacit® DM/C (benzothiazyl disulfide), Vulkacit® Thiuram MS/C (tetramethyl thiuram monosulfide), and Vulkacit® Thiuram/C (tetramethyl thiuram disulfide). It may be suitable to even add a further peroxide to such sulfur-based vulcanizing agents like e.g. zinc peroxide.
In another preferred embodiment of the present invention the vulcanisable mixtures further comprise at least one additional polymer as a binding material, selected from the group consisting of acrylate rubber (ACM), ethylene acrylate rubber (AEM), ethylene propylene diene terpolymer (EPDM), ethylene propylene copolymer (EPM), ethylene vinyl acetate (EVM), ethylene methyl acrylate (EMA), acrylnitrile-diene copolymer (NBR), hydrogenated acrylnitrildiene copolymer (HNBR) and a mixture thereof.
The present invention further provides a process for preparing vulcanisates according to the invention characterized in that, ethylene acrylate (AEM), polyacrylate (ACM) and/or hydrogenated acrylonitrile (HNBR)-based rubbers and at least one vulcanisation accelerator selected from an amine, an amidine as well as salts and any mixtures of the above-mentioned accelerators and at least one retarder system comprising (a) an acid, preferably benzoic acid, salicylic acid, phthalic acid, phthalic acid anhydride and/or C6-C24-dicarboxylic acid, and/or (b) a carbodiimide, and/or (c) a polycarbodiimide and any mixtures of the above-mentioned retarders are cross-linked by using a curative system based on an polyamine, preferably a diamine or a diamine carbamate, such as i.e.
Among these, an aliphatic polyamine is preferred, and hexamethylene diamine carbamate is particularly preferred.
The content of the polyamine crosslinking agent in the vulcanisable polymer composition is in the range of from 0.2 to 20 parts by weight, preferably in the range of from 0.5 to 10 party by weight, more preferably of from 1.0 to 5 parts by weight based on 100 parts by weight of the polymer.
In such process for preparing the polymer vulcanisates the mixing of the ethylene acrylate (AEM), polyacrylate (ACM) and/or hydrogenated acrylonitrile (HNBR)-based rubbers, the polyamine crosslinking agent, and at least one vulcanisation accelerator selected from an non aromatic amine, an amidine, as well as salts and any mixtures thereof and at least one retarder system comprising (a) an benzoic acid, salicylic acid, phthalic acid, phthalic acid anhydride and/or C6-C24-dicarboxylic acid, and/or (b) a carbodiimide and/or (c) a polycarbodiimide and optionally the antioxidant, the filler and other conventional additives may be performed in any conventional manner known in the art. For example, all components may be admixed on a two-roll rubber mill or in an internal mixer.
Thus, the polymer composition is mixed and prepared in a conventional manner and the temperature during mixing is maintained as is known in the art. Temperatures in the range of from 80 to 130° C. have proven to be typically applicable, always depending on the specific type of rubber used and other components as chosen.
In a typical embodiment of the present process it is then preferred to heat the polymer composition to form the rubber vulcanisates using conventional procedures also well known in the art. Preferably, the vulcanisable rubber composition is heated to a temperature in the range of from about 130° to about 200° C., preferably from about 140° to about 190° C., more preferably from about 150° to about 180° C. Preferably, the heating is conducted for a period of from about 1 minute to about 15 hours, more preferably from about 5 minutes to about 30 minutes.
In a further embodiment the present invention relates to a polymer vulcanisate obtainable by the process mentioned before.
In another preferred embodiment of the present invention diamine or a diamine carbamate are used as a curative system.
The present invention further provides for use of the inventive vulcanisate for automotive, oil-field and/or off-shore applications.
The present invention is described in more detail by reference to the following examples, without being limited to them.
The vulcanisable mixtures presented in Table 1 show a comparative evaluation of a series of three compounds, prepared with a vulcanisation system comprising a vulcanisation agent, hexamethylene diamine carbamate and Rhenogran® DOTG (di-orto-tolyl-guanidine) or Rhenogran® XLA (according to EP-A 2033989) as different accelerators selected from the group in combination with or without Stabaxol® I as a retarder.
The ingredients for the compounds A, B, C and D in phr are summarized in Table 1
The respective polymer compositions were blended in a laboratory internal mixer GUMIX 2 IM, type Banburry, with 40 RPM and a 70% filling factor, using an upside down procedure. The dump temperature registered was 100° C. In order to obtain good homogeneous mixes, the mixing process was further continued on the laboratory open mill Rubicon (roll distance: 150 mm, roll width: 320 mm) with a friction of 1:1.25 at 40° C. for 6 min. The polymer compositions were press-cured in slabs of 13.5 cm×13.5 cm at 180° C. in a hydraulic press Agila, type PE 100, at 100 bar, and then post-cured at 175° C. for four hours at ambient pressure.
The Mooney viscosity of the compounds was determined at 100° C. while the Mooney scorch measurement was conducted at 120° C. Both studies were performed in accordance with DIN 53523. The vulcanisation process was measured at 180° C. in accordance with DIN 53529. The processing and curing characteristics of the compounds A-C are reported in Table 2.
It can be clearly seen from the test results that blend C and D, which are according to the invention show results comparable to blend A. Blend A contains the hazardous di-o-tolyl-guandine.
The Mooney scorch of compound C is significantly improved compared to compound B (monomeric carbodiimides used), which is an important practical advantage in some conventional applications of the compounds. Compound D also shows some improvement, while is not as significant as with compound C.
It can also be seen quite clearly that the combination of accelerator Rhenogran® XLA-60 with the retarder Stabaxol® I or alternatively Benzopic acid leads to a fast but manageable curing time (t90-t10), which offers an opportunity for cost reductions in the production of rubber articles.
Direct comparison of compound B with C, or D, all containing Rhenogran® XLA-60 as an accelerator, reveals the significant improvement regarding scorch safety at T5 [min] which was achieved in example C by adding Stabaxol® I, and in example D by adding benzoic acid as a retarder.
Table 3 shows the ingredients for the compounds E, F and G in phr (Example 3).
The nitrile rubber “NBR1” used as starting basis for the hydrogenation to obtain “HNBR1” contained repeating units of acrylonitrile, butadiene and a termonomer in the amounts given in the following Table A and had the Mooney Viscosity also mentioned in Table A, further details are disclosed in EP 09164539.0.
A 12% total solids solution of NBR 1 in monochlorobenzene (“MCB”) as solvent was charged into a high pressure reactor and heated to 138° C. while being agitated at 600 rpm. Once the temperature was stabilized a solution of Wilkinson's catalyst and triphenylphosphine (“TPP”) as co-catalyst were introduced and hydrogen was introduced into the vessel to reach a pressure of 85 bar. The reaction was agitated for 4 hrs at which time the hydrogen pressure was released and the reactor cooled to room temperature (˜22° C.). The polymer solution was then removed from the reactor and coagulated using either steam or alcohol methods known in the art. The isolated polymer was then dried.
As can be deduced from the Moving-Die-Rheometer—results given in Table 4, vulcanisation kinetics are slowed down by the application of Stabaxol®. As this measurement is performed at 180° C., the differences are not as pronounced as in the former test, where the measurement was carried out at 120° C. Nevertheless, the results again clearly indicate the retarder function of Stabaxol I. TS 2 and T50 are shifted to longer vulcanisation times.
| Number | Date | Country | Kind |
|---|---|---|---|
| 09169333.3 | Sep 2009 | EP | regional |
