The present invention relates to silicone compositions which can be crosslinked by dehydrogenative condensation between reactive ≡SiH and ≡SiOH units and which employ an iridium complex as catalyst. It also relates to a preparation process relating thereto, to the crosslinked materials thus obtained and to the articles coated with or composed of these materials.
The invention thus relates to the field of the catalysis of dehydrogenative condensation reactions which make possible silicone polymerization/cross-linking. The reactive entities involved are monomers, oligomers and/or polymers of polyorganosiloxane (POS) nature.
The reactive units concerned in these entities are, on the one hand, the ≡SiH units and, on the other hand, the ≡SiOH units. Dehydrogenative condensation between these silicone reactive units and entities results in the formation of ≡Si—O—Si≡ bonds and in the release of hydrogen gas. This dehydrogenative condensation is an alternative to the polymerization/crosslinking routes known in the field of silicones, namely the ≡SiH/≡Si-alkenyl (vinyl) polyaddition route and the ≡SiOR/≡SiOR (with R=alkyl) polycondensation route. All these polymerization/crosslinking routes result in more or less polymerized and more or less crosslinked silicone products which can constitute products usable in multiple applications: adhesives, leaktightness products, pointing products, adhesion finishes, release coatings, foams, and the like.
The applications more particularly targeted by the invention are crosslinked silicone elastomer coatings of use as release coatings on various solid supports, for example flexible fibrous supports (made of paper or fabric, e.g.) or flexible nonfibrous supports, such as polymer films (polyester or polyolefin, e.g.) or alternatively supports made of aluminum or of any other metal, such as tin plate.
Another application to which the invention more especially relates is targeted at crosslinked silicone foams.
The dehydrogenative condensation reaction involves metal catalysts based on platinum, rhodium, palladium, ruthenium, boron or iridium, platinum catalysts being the most common (FR-B-1 209 131, U.S. Pat. No. 4,262 107, EP-A-1 167 424 and FR-A-2 806 930).
FR-B-1 209 131 discloses in particular the reaction between a silanol Ph2Si(OH)2 and a diorgano-siloxane [(Me2HSi)2O], with Me=methyl and Ph=phenyl, by dehydrogenative condensation in the presence of chloroplatinic acid (H2PtCl6.6H2O), which results in a polydiorganosiloxane possessing a D unit, —R2SiO2/2—, of dimethyl or diphenyl type. This reaction produces a rapid evolution of hydrogen.
U.S. Pat. No. 4,262,107 relates to a silicone composition of polyorganosiloxane (POS) type comprising more specifically a polydimethyldisiloxane possessing silanol ends and a crosslinking agent composed of a POS possessing ≡SiH units in the chain and possessing trimethylsilyl ends, a catalyst composed of a rhodium complex (RhCl3[(C8H17)2S]3), and a crosslinking inhibitor (for example, diethyl maleate, diethyl acetylenedi-carboxylate, triallyl isocyanurate or vinyl acetate).
EP-A-1 167 424 and US-A-2002/0013441 disclose the production of linear block silicone copolymers by dehydrogenative condensation of POS polymers possessing silanol ends and of aromatic POS possessing ≡SiH ends in the presence of a metal catalyst. Hydrosilylation catalysts are suitable and it is possible to employ the metals platinum, rhodium, palladium, ruthenium and iridium, preferably platinum, and compounds of these metals. The hydrosilylation catalyst is in particular a platinum complex, such as the Karstedt catalyst.
FR-A-2 806 930 relates to the use of boron derivatives of tris(pentafluorophenyl)borane type.
It would be of great usefulness to have available a broader panel of dehydrogenative condensation catalysts and in particular of catalysts which make it possible to optimize the kinetics of the reaction and the concentration/effectiveness of the catalyst ratio. An object of the invention is thus to provide novel dehydrogenative condensation catalysts which are particularly effective.
Another object of the invention is to provide catalysts with a lower cost price than platinum catalysts.
Another object of the invention is to provide a panel of catalysts which are easy to prepare, so as to more readily present the catalyst which is the best suited to such and such a reaction and/or under such and such operating conditions.
Another object of the invention is to provide catalysts having moderate activation temperatures (mobilization of a small amount of energy for the catalysis of the dehydrogenative condensation: θ° C.<150° C.) and/or making possible better control of the evolution of hydrogen gas and of the quality of the polymerized product and/or of the crosslinked network, and/or, finally, making it possible to limit the side reactions.
Another essential object of the present invention is to provide ≡SiH/≡SiOH silicone compositions which can be polymerized or crosslinked by dehydrogenative condensation in the presence of such a catalyst.
Patent application PCT/FR02/01340, filed on 18 Apr. 2002 (and unpublished at the date of filing of the present application), discloses silicone compositions which crosslink by dehydrogenative condensation and which use, as catalyst, an iridium complex corresponding to the following formula (I′):
IrX(L)(L′)2
This patent application PCT/FR02/01340 cites in particular Vaska's complex IrCl(CO)(triphenyl-phosphine)2.
The objects set out above, and others, are achieved by the present invention, which relates first of all to a silicone composition which can be crosslinked by dehydrogenative condensation, this composition comprising:
characterized in that the catalytic complex -C- is an iridium complex obtained by reacting together:
the preferred ligands Σ′ are hydrocarbon groups comprising at least one unit
those of the latter type being the more preferred, such as, for example, cyclooctene;
it may be specified that the hydrocarbon groups can be linear, branched, aromatic or (poly)cyclic, can be optionally interrupted by one or more heteroatoms (e.g., O, S or N) and can comprise from 2 to 18 carbon atoms; they can be ligands comprising two of these units (preferably identical units) capable of bonding to the iridium atom (in this case, the two functionalities Σ′ are preferably provided by one and the same molecule connected to the iridium via its two electron-donating functional groups), for example a cyclic compound exhibiting two double bonds, e.g. 1,5-cyclooctadiene, or a diene exhibiting distant double bonds (“distant diene”). Thus, 1,5-cyclo-octadiene is a preferred form;
According to a preferred embodiment, the iridium complex is a dimeric complex (n=2) of following formula (I′):
in which Σ and Σ′ have the meanings given above, with the preferences indicated above with regard to the formula (I).
According to a specific embodiment, the catalytic complex —C— is obtained by reaction between:
According to a preferred embodiment, the dimeric iridium complex (I′) is bis(1,5-cyclooctadiene)di-iridium(I) dichloride of formula [IrCl(cycloocta-diene)]2. It is a commercial product.
According to a preferred embodiment, the ligand Σd is triphenylphosphine (TPP). By way of example, mention may also be made of tris(para-methoxyphenyl)phosphine.
According to a preferred embodiment, the catalytic complex —C— is the product of the mixing of bis(1,5-cyclooctadiene)diiridium(I) dichloride and of TPP.
As indicated below, the catalytic complex —C— is preferably obtained by reacting the abovementioned entities at ambient temperature, e.g. in the vicinity of 25° C., and in the open air, optionally in the presence of a solvent which makes it possible, if necessary, to dissolve the reactive entities. It is clearly understood that different reaction conditions can be applied in an equivalent way so as to obtain a conforming catalytic complex.
The use of such a catalytic complex —C— makes it possible to efficiently catalyze the dehydrogenative condensation reaction between ≡SiH and ≡SiOH siloxane entities under mild temperature conditions, generally at temperatures of less than 150° C., in particular of less than 100° C., and optionally at ambient temperature. Silicone networks or polymers are thus obtained in a few minutes, with variable ≡SiH/≡SiOH ratios.
The catalytic complexes carefully selected in accordance with the invention are effective and economic, in particular with regard to platinum-based catalysts.
It is very simple to test various iridium complex/ligand Σd pairs and to observe their properties and behavior. As is illustrated in the examples part, the preparation of the catalytic complex does not require a complex process or critical operating conditions. It is sufficient, for example, to prepare a mixture of an iridium complex and of a ligand Σd to be tested, optionally to dissolve this mixture in a solvent, such as toluene, in the case where the starting entities are in solid form, then to mix the combined product with a silicone composition comprising at least one POS A and one POS B according to the invention and optionally a crosslinking retarder, and to observe the crosslinking time at ambient temperature and/or at a higher temperature, e.g. under temperature conditions similar to the practical application desired. Phosphites and phosphines are, for example, chemical entities which are widely available. It is possible in particular to test combinations of ligands Σd and of iridium complexes which are commercially available, such as phosphites and phosphines and bis(1,5-cyclooctadiene)diiridium dichloride and (1,5-cyclooctadiene)(acetylacetonato)iridium. The incorporation, in the preparation of the silicone composition, of a simple stage for the preparation of the catalytic complex thus exhibits very obvious advantages, including the possibility of having available varied catalytic complexes suited to the circumstances (e.g., suited to the crosslinking duration and temperature conditions).
These catalytic complexes are in particular advantageous in preparing the elastomeric silicone networks under mild and economical conditions. The applications targeted in this case relate in particular to the adhesion resistance of paper, where it is desired to replace the current systems by less expensive systems, and silicone foams, where it is desired to control the evolution of hydrogen and the quality of the network. For the first application, it is preferable to control the diffusion of the hydrogen in order to prevent the formation of bubbles. For the second application, it is necessary to manage the size of the bubbles in order to optimize the properties of the final foam. These results are all the more significant as the reactivity of siloxane entities, in particular in forming nonlinear (crosslinked) products, is not very high if it is compared with that of hydrosilanes and alcohols in dehydrogenative condensation.
Quantitatively, use is made of 1 ppm to 1000 ppm, in particular of 1 ppm to 300 ppm, of iridium metal with respect to the body composed of the mixture of the oils possessing ≡SiH and ≡SiOH. When the present patent application deals with ranges, the limits are included.
The catalytic complex employs in particular from 0.5 to 10, especially from 0.5 to 5, more particularly from 0.5 to 2, mol of ligand Σd per 1 mol of Ir. Depending on the preferred embodiment of the invention, use is made of 0.75 to 1.5, in particular of 0.75 to 1.25 and better still of 1 mol of ligand Σd per 1 mol of Ir.
The siloxane entity -A- comprising reactive ≡SiH units is preferably chosen from the entities which have at least one unit of formula (II) and which are terminated by units of formula (III) or from the cyclic entities (generally comprising from 3 to 12 Si atoms) composed of units of formula (II), these formulae being represented below:
in which:
As regards the siloxane entities —B— comprising reactive ≡SiOH units, the selection is made in particular in the context of the invention of those which have at least one unit of formula (IV) and which are terminated by units of formula (V) or of cyclic entities (generally comprising from 3 to 12 Si atoms) which are composed of units of formula (IV), these formulae being represented below:
in which:
The entities of -A- and —B— type can also include, in their structure, “Q” or “T” units defined as indicated below:
with it being possible for R3 to represent one of the substituents provided for R1 or R2.
According to an advantageous embodiment of the invention, the polyorganosiloxanes -A- used comprise from 1 to 50 SiH units per molecule.
According to an advantageous embodiment of the invention, the polyorganosiloxanes —B— used comprise from 1 to 50 SiOH units per molecule.
According to a preferred embodiment, the poly-organosiloxanes -A- correspond to the general formula (VI):
in which:
According to a preferred embodiment, the poly-organosiloxanes —B— correspond to the general formula (VII):
in which:
The following compounds:
with a, b, c, d and e representing a number varying from:
in the polymer of formula S1:
in the polymer of formula S2:
in the polymer of formula S3:
The compounds of formula:
with 1≦f≦1200, preferably 50≦f≦400 and more preferably still 150≦f≦250,
are very particularly suitable in the invention as polyorganosiloxanes —B—.
Provided that the siloxane entities -A- and —B— are oligomers or polymers, they can be described as indicated below.
The POS -A- can be linear (e.g. (VI)), branched or cyclic. For economic reasons, its viscosity is preferably less than 100 mPa·s at 25° C.; the identical or different organic radicals are preferably methyl, ethyl and/or phenyl. When the POS is linear, the hydrogen atoms of the ≡SiH functional groups are bonded directly to the silicon atoms situated at the chain end(s) and/or in the chain.
Mention may be made, as example of linear constituent -A-, of polymethylhydrosiloxanes comprising trimethylsiloxyl and/or hydrodimethylsiloxy ends.
Mention may be made, among cyclic polymers, of those corresponding to the following formulae:
[OSi(CH3)H]4; [OSi(CH3)H]5; [OSi(CH3)H]3; [OSi(CH3)H]8; [OSi(C2H5)H]3.
Mention may be made, as concrete examples of branched polymers, of:
The constituent —B— can exhibit a viscosity which can reach 200 000 mPa·s. For economic reasons, a constituent having a viscosity generally of the order of 20 to 10 000 mPa·s is chosen.
The identical or different organic groups generally present in the α,ω-hydroxylated oils or gums are the methyl, ethyl, phenyl or trifluoropropyl radicals. Preferably, at least 80% by number of said organic groups are methyl groups bonded directly to the silicon atoms. In the context of the present invention, preference is given more especially to α,ω-bis(hydroxy)polydimethylsiloxanes.
The —B— entities can comprise resins possessing silanol functional groups exhibiting, per molecule, at least one of the R′SiO0.5 unit (M unit) and R′2SiO unit (D unit), in combination with at least one of the R′SiO0.5 unit (T unit) and SiO2 unit (Q unit). The R′ radicals generally present are methyl, ethyl, isopropyl, tert-butyl and n-hexyl. Mention may be made, as examples of resins, of the resins MQ(OH), MDQ(OH), TD(OH) and MDT(OH).
It is possible to employ solvents for the POS -A- or —B—, so as to adjust the viscosity of the composition. Mention may be made, as examples of such conventional solvents for silicone polymers, of solvents of aromatic type, such as xylene and toluene, saturated aliphatic solvents, such as hexane, heptane, White Spirit®, tetrahydrofuran and diethyl ether, or chlorinated solvents, such as methylene chloride and perchloroethylene. In the context of the present invention, it will be preferable, however, not to use a solvent.
The respective amounts of siloxane entities -A- and —B— are also determining in order to be able to satisfactorily carry out the dehydrogenative condensation of the composition according to the invention.
Thus, the ≡SiH/≡SiOH ratio is advantageously between 1 and 100, preferably between 2 and 50 and more preferably still between 2 and 25.
The composition according to the invention can also comprise at least one crosslinking inhibitor or retarder -D-. Such a constituent is generally used to confer a degree of pot life on the ready-for-use composition. By varying, on the one hand, the nature of the catalytic combination and its concentration in the composition (which results in a given crosslinking rate) and, on the other hand, the nature of the retarder and its concentration, it is possible to adjust the pot life. The activity of the catalytic combination is restored by heating (thermal activation). The retarder is preferably chosen from acetylenic alcohols (ethynylcyclohexanol: ECH) and/or diallyl maleates and/or triallyl isocyanurates and/or dialkyl maleates (diethyl maleates) and/or dialkyl alkynedicarboxylates (diethyl acetylenedicarboxylate) or alternatively from polyorganosiloxanes, advantageously cyclic and substituted by at least one alkenyl, tetramethylvinylcyclotetrasiloxane being particularly preferred, or alkylated maleates.
Acetylenic alcohols (see, for example, FR-B-1 528 464 and FR-A-2 372 874) are the preferred retarders. They are in particular those corresponding to the following formula:
R1—(R2)C(OH)—C≡CH
in which:
Said alcohols are preferably chosen from those exhibiting a boiling point of greater than 250° C. Mention may be made, as examples, of:
These α-acetylenic alcohols are commercial products.
Such a retarder is present in particular in a proportion of 3000 ppm at most, preferably in a proportion of 100 to 2000 ppm, with respect to the total weight-of the compounds -A- and —B—.
The composition according to the invention can also comprise one or more POS resins -E-. These resins are well known branched POS oligomers or polymers which are commercially available. They are present in the form of solutions, preferably siloxane solutions. They exhibit, in their structure, at least two different units chosen from those of formula R*3SiO0.5 (M unit), R*2SiO (D unit), R*SiO1.5 (T unit) and SiO2 (Q unit), at least one of these units being a T or Q unit.
The R* radicals are identical or different and are chosen from linear or branched C1-C6 alkyl radicals, C2-C4 alkenyl radicals, the phenyl radical or the 3,3,3-trifluoropropyl radical. Mention may be made, for example, as R* alkyl radicals, of the methyl, ethyl, isopropyl, tert-butyl and n-hexyl radicals and, as R* alkenyl radicals, of the vinyl radical. It should be understood that, in the POS resins -E- of the abovementioned type, for a portion of them, the R* radicals are alkenyl radicals.
Mention may be made, as examples of branched organopolysiloxane oligomers or polymers -E-, of MQ resins, MDQ resins, TD resins and MDT resins, it being possible for the alkenyl functional groups to be carried by the M, D and/or T units. Mention may be made, as examples of resins -E- which are particularly well suited, of the vinylated MDQ or MQ resins having a content by weight of vinyl groups of between 0.2 and 10% by weight, these vinyl groups being carried by the M and/or D units.
This structuring resin -E- is advantageously present in a concentration of between 10 and 70% by weight with respect to the combined constituents of the composition, preferably between 30 and 60% by weight and more preferably still between 40 and 60% by weight.
The composition according to the invention can also comprise a filler —F—, preferably an inorganic filler, chosen from siliceous or nonsiliceous materials.
When siliceous materials are concerned, they can act as reinforcing or semi-reinforcing filler. The reinforcing siliceous fillers are preferably chosen from colloidal silicas, fumed and precipitated silica powders, or their mixtures. Semi-reinforcing siliceous fillers, such as diatomaceous earths or ground quartz, can also be employed. These powders exhibit a main particle size generally of less than 0.1 μm and a specific surface BET of greater than 50 m2/g, preferably between 100 and 300 m2/g.
As regards nonsiliceous organic materials, they can be involved as semi-reinforcing or bulking inorganic filler. Examples of these nonsiliceous fillers, which can be used alone or as a mixture, are carbon black, titanium dioxide, aluminum oxide, alumina hydrate, expanded vermiculite, zirconia, a zirconate, unexpanded vermiculite, calcium carbonate, zinc oxide, mica, talc, iron oxide, barium sulfate and slaked lime. These fillers have a particle size generally of between 0.001 and 300 μm and a BET specific surface of less than 100 m2/g.
In practice but without implied limitation, the filler employed is a silica.
The filler can be treated using any appropriate compatibilizing agent and in particular hexamethyldi-silazane. For further details in this regard, reference may be made, for example, to patent FR-B-2 764 894.
With regard to the weight, it is preferable to employ an amount of filler of between 5 and 30%, preferably between 7 and 20%, by weight, with respect to the combined constituents of the preparation.
Naturally, the composition can be enriched using all kinds of additives, depending upon the final applications targeted.
In the adhesion resistance application on flexible supports (paper or polymer film), the composition can comprise an adhesion adjusting system selected from known systems. Those disclosed in French patent FR-B-2 450 642, patent U.S. Pat. No. 3,772,247 or European patent application EP-A-0 601 938 may be concerned. Mention may be made, as examples, of the adjusting systems based:
Other functional additives of this composition can be stabilizing agents, bactericides, photosensitizers, fungicides, corrosion inhibitors, antifreeze agents, wetting agents, antifoaming agents, synthetic latexes, colorants or acidifying agents.
Mention may also be made, among conventional additives, of adhesion promoters, such as, for example, those comprising at least one alkoxylated organosilane, at least one epoxidized organosilicon compound and at least one metal chelate and/or one metal alkoxide, for example VTMO (VinylTriMethoxySilane), GLYMO (GLYcidoxypropyltriMethOxysilane) or TBT (tert-butyl titanate).
This composition can be a solution or an emulsion. In the latter case, it can then comprise at least one surfactant and optionally at least one agent for fixing the pH, such as HCO3−/CO32− and/or H2PO4−/HPO42−.
Another subject matter of the present invention is the use of a catalytic iridium complex as defined in the present application as dehydrogenative condensation catalyst for a silicone composition which crosslinks by dehydrogenative condensation, this composition being moreover defined in the present application.
A further subject matter of the present invention is the catalytic complexes capable of being obtained in accordance with the invention by reacting at least one iridium complex as defined above and at least one ligand as defined above.
According to yet another of its aspects, the present invention relates to a process for polymerizing and/or crosslinking a composition as defined above. This process is characterized in that a dehydrogenative condensation is carried out between said compounds -A- and —B— and in that said dehydrogenative condensation is initiated by thermal activation of the catalytic complex —C—. The catalytic complex according to the invention can be prepared in a first stage by mixing the abovementioned entities, as described above.
According to another alternative form of the invention, the invention relates to a process for the preparation of a branched polyorganosiloxane comprising at least two polyorganosiloxane chains connected to one another via an Si—O—Si siloxyl group in which a dehydrogenative condensation reaction is carried out between an organosiloxane monomer, oligomer or polymer A′ comprising reactive ≡SiH units and an organosiloxane monomer, oligomer or polymer B′ comprising reactive ≡SiOH units, characterized in that said dehydrogenative condensation reaction is carried out in the presence of the catalytic complex C defined as above or according to one of claims 1 to 15 and is optionally initiated by thermal activation. According to a preferred form, the ≡SiH/≡SiOH ratio is greater than 1.
The catalytic complex can either be added to the mixture of the compounds A and B, for example of the polymers of the S1 or S2 or S3 type with a polymer of the S4 type, or, preferably, be mixed beforehand with the compound B, for example the polymer of the S4 type, before being brought into contact with the compound A, for example the polymer S1 or S2 or S3. Generally, the mixtures are prepared with stirring at ambient temperature.
The catalytic complex can be employed as is or in solution in a solvent.
The catalytic complex solution can, for example, be used to prepare a bath with the monomer(s), oligomer(s) and/or polymer(s) to be polymerized and/or crosslinked by dehydrogenative condensation, so that the concentration of the catalytic complex(es) present is between 0.01 and 5% by weight in said bath and preferably between 0.05 and 0.5%.
The solvents which can be used can in particular be esters, ethers, aromatic solvents, water in the form of traces, carbonates and hindered alcohols. Mention may be made, for the alcohols, of isopropylbenzyl alcohol or benzyl alcohol. Mention may be made, for the ethers, of di(n-butyl) ether. Mention may be made, for the esters, of dibutyl maleate, dimethyl ethylmalonate, methyl salicylate, dioctyl adipate, butyl tartrate, ethyl lactate, n-butyl lactate or isopropyl lactate. Other solvents are toluene and tetrahydrofuran.
The silicone composition according to the invention, which can be used in particular as coating base for the preparation of release coatings possessing a water-repellant nature, is prepared using means and according to mixing methodologies well known to a person skilled in the art, whether compositions, with or without solvents, or emulsions are involved.
The invention also relates to a process for producing at least one release coating on a support, preferably a flexible support, characterized in that it comprises the application, to this support, of a composition as defined above, preferably employing POS -A- and —B— as defined above, and then ensuring that crosslinking occurs.
In accordance with this process, the compositions can be applied using devices used on industrial machines for coating paper, such as a roll coating head, e.g. a five-roll coating head, or air knife or smoothing rod systems, on flexible supports or materials and then cured by moving through appropriate heating devices, such as tunnel ovens heated at 70-200° C.; the passage time in these ovens depends on temperature; it is generally of the order of 5 to 15 seconds at a temperature of the order of 100° C. and of the order of 1.5 to 3 seconds at a temperature of the order of 180° C.
Said compositions can be deposited on any flexible material or substrate, such as paper of various types (e.g., supercalendered, coated or glassine), board, cellulose sheets, metal sheets or plastic films (polyester, polyethylene, polypropylene, and the like).
The amounts of compositions deposited can be of the order of 0.5 to 2 g per m2 of surface to be treated, which corresponds to the deposition of layers of the order of 0.5 to 2 μm.
The materials or supports thus coated can subsequently be brought into contact with any adhesive material, e.g. rubber, acrylic or other, which is sensitive to pressure. The adhesive material is then easily detachable from said support or material.
The flexible supports coated with a release silicone film can, for example, be:
Another subject matter of the invention is a process for producing at least one article made of crosslinked silicone foam, characterized in that it comprises the stage of crosslinking a composition as defined above, while preferably employing the POS A and POS B as defined above, while ensuring that at least a portion of the hydrogen gas formed is not discharged from the reaction medium.
The compositions according to the invention are of use in the field of release coatings on paints, the encapsulation of electrical and electronic components, or coatings for textiles, and in the field of the sheathing of optical fibers.
Another subject matter of the invention is any coating obtained by crosslinking a composition comprising siloxane entities -A- possessing reactive SiH units, e.g. of S1, S2 or S3 type, as are defined above, and siloxane entities —B—, e.g. of S4 type, as are defined above. These coatings can be of varnish, adhesive coating, release coating and/or ink type.
The invention is also targeted at:
Another subject matter of the present invention is the resins or polymers capable of being obtained from the compositions described above.
The invention will now be described in more detail using nonlimiting implementational examples.
A mixture of silicone oils is prepared from the following reactive oils:
Furthermore, the desired amounts of iridium complex (IrClCod]2 and of ligand Σd are weighed out in a 30 ml flask equipped with a magnetic stirrer and are then diluted with a small amount of sulfur-free toluene (0.5 ml). The necessary amount of the preformed mixture of silicone oils is added to this solution. The time measurements begin at this point, at the same time as the magnetic stirring begins.
After stirring at ambient temperature, the setting (crosslinking) time is measured. The conditions and the results are combined in table 1.
A mixture of silicone oils is prepared from the following reactive oils:
Furthermore, the desired amounts of iridium complex [IrClCod]2 are weighed out in a 30 ml flask equipped with a magnetic stirrer and are then diluted with a small amount of sulfur-free toluene (0.5 ml). After stirring for 10 minutes, the necessary amount of the preformed mixture of silicone oils is added to this solution. The time measurements begin at this point, at the same time as the magnetic stirring begins.
After stirring at ambient temperature, the setting (crosslinking) time is measured.
The conditions and the result are combined in table 1.
*NC: No crosslinking after stirring at a.t. for 6 h
It should be clearly understood that the invention defined by the appended claims is not limited to the specific embodiments indicated in the description above but encompasses the alternative forms thereof which depart neither from the scope nor from the spirit of the present invention.
Number | Date | Country | Kind |
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03/07908 | Jun 2003 | FR | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/FR04/01616 | 6/25/2004 | WO | 5/10/2006 |