FIELD OF THE INVENTION
[0001] This invention relates to a method for curing compositions that undergo a metathesis
reaction initiated by a metathesis catalyst, the method using a reaction control agent
for controlling the progress of the metathesis reaction and an elevated temperature
cure to complete the reaction. More specifically, the control agent slows the progress
of the metathesis reaction, and depending on the nature of the control agent, may
prevent completion of the reaction until the composition is exposed to temperatures
higher than the mixing temperature.
BACKGROUND OF THE INVENTION
[0002] Addition polymerizable silicone resins are widely used in many fields such as electronics,
health care and automotive applications. The polymerizable resins are cured as a two-part
system using a hydrosilation reaction. A platinum catalyst is used in one part, the
catalyst side, and a hydrogen terminated polydimethylsiloxane (HPDMS) in the other
part, the base side, while both sides contain vinyl terminated polydimethylsiloxanes
(PVDMS) resins. When these materials are cured at room temperature, they are referred
to as room temperature vulcanized (RTV). The most common RTV materials are typically
offered as a 10:1 ratio base/catalyst, such as RTV630 (GE Silicones), while some other
RTV materials are offered at a 1:1 ratio, such as RTV6428 (GE Silicones). Various
working times are required depending on the application from 2 minutes to several
hours and may involve a heat curing step above ambient temperature. The working time
is controlled with a retarder or inhibitor mixed with the catalyst component, such
as an amine or acetylenic compound.
[0003] Another class of addition polymerizable silicone resins are the liquid silicone rubber
(LSR) materials prepared through the liquid injection molding (LIM) process. The LSR
materials are cured at a temperature of 120°C-180°C in a mold injected to after mixing.
The mixture includes a retarder mixed with the catalyst component, such as an amine
or acetylenic compound, that allows the hydrosilation reaction to occur at the mold
temperature only.
[0004] Both the RTV and LSR types of formulations suffer from the shortcomings of the hydrosilation
mechanism. These shortcomings include: (1) deactivation of the platinum catalyst by
sulfur or other nucleophilic impurities; (2) high shrinkage, approximately 1%, due
to the high reduction of free volume upon polymerization; (3) high cost of platinum
metal needed for catalysis; (4) high cost of HPDMS and PVDMS resins; (5) requirement
of two different resins to be employed, namely vinyl and hydrogen terminated; (6)
undesirable hydrogen evolution from the decomposition of the hydrosiloxane cross-linkers
that typically are present in these systems; and (7) vinyl functionalized PDMS resins
have a low hydrocarbon content in the main chain after polymerization due to the presence
of only an ethyl spacer, which leads to a relatively high dielectric constant, which
is an undesirable property for some electronic applications.
[0005] A new type of polymerization system has been recently developed that may potentially
be used to replace addition-curable silicones and platinum catalysts in a wide variety
of applications to thereby avoid the shortcomings of the hydrosilation mechanism discussed
above. In this new metathesis reaction system, curing is achieved by a ring-opening
metathesis polymerization (ROMP) mechanism Metathesis is generally understood to mean
the metal catalyzed redistribution of carbon-carbon double bonds. The polymerizable
composition comprises a resin system that includes functionalities or groups that
are curable by ROMP together with a metathesis catalyst, such as a ruthenium carbene
complex. However, to efficiently utilize ROMP to prepare polymers, there is a need
for a method of curing in which the progress of the metathesis reaction is controlled
and proceeds to completion only upon the application of an elevated temperature, which
method is particularly useful for molding applications.
[0006] In addition to ROMP, other metathesis reaction systems utilize metathesis catalysts,
for example ring closing metathesis, acyclic diene metathesis polymerization, ring
opening metathesis and cross metathesis. There is further a need for a curing method
that controls the progress and completion of the reaction in these other metathesis
reaction systems.
[0007] In addition to silicone resins, another thermoset monomer type that is curable by
ROMP is the cycloolefins. These resins are usually molded, and there is thus a further
need for a curing method that controls the progress and completion of the metathesis
reaction for this monomer type.
SUMMARY OF THE INVENTION
[0008] The present invention provides a method of curing a composition that upon mixing
of its components undergoes a metathesis reaction, wherein the method includes mixing
of its components into the composition that control and catalyze the metathesis reaction,
but prevent completion of the reaction at the mixing temperature. The method includes
mixing together a metathesis-curable olefinic substrate, a ruthenium or osmium carbene
complex catalyst that is effective to initiate the metathesis reaction, such as ring-opening
metathesis polymerization (ROMP), and a reaction control agent for slowing the progress
of the reaction. The catalyst has the following structure:

wherein:
M is ruthenium or osmium,
X is an akylidene ligand with basicity higher than that of tricyclohexylphosphine
(PCy3),
X1 is a neutral electron donor ligand with a basicity lower than that of tricyclohexylphosphine,
X2 and X3 are either the same or different and are any anionic ligand, and R1 and R2 are either the same or different and are each independently hydrogen or a substituent
selected from the group consisting of C1-C20 alkyl, C2-C20 alkenyl, C2-C20 alkynyl, aryl, C1-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxycarbonyl, C1-C20 alkylthio, C1-C20 alkylsulfonyl and C1-C20 alkylsulfinyl, wherein each of the substituents is substituted or unsubstituted.
In an exemplary embodiment of the present invention, the catalyst has the following
structure:

wherein Ph is phenyl, X is an alkylidene, such as a saturated imidazolidene, having
a basicity (proton affinity) higher than tricyclohexylphosphine (PCy
3), and X
1 is a phosphine, phosphite, phosphinite, or phosphonite whose basicity is lower than
that of PCy
3. In a further exemplary embodiment, X
1 is a phosphine of the formula PR
3R
4R
5 where R
3, R
4, and R
5 are alkyl, aralkyl or aryl. The olefin-containing substrate, comprises one or a combination
of the following: a polymerizable telechelic siloxane-based polymer end-capped with
an olefin group curable by ROMP; a polymerizable siloxane-based polymer tethered and
end-capped with an olefin group curable by ROMP; a polymerizable tri-functional siloxane-based
oligomer or polymer end-capped with an olefin group curable by ROMP; and a polymerizable
quadri-functional siloxane-based oligomer or polymer end-capped with an olefin group
curable by ROMP.
[0009] The method uses a reaction control agent to slow the progress of the metathesis reaction.
The control agent allows the composition to be cured after a certain delayed time
after mixing (work time or pot life) and allows for acceleration of the rate of the
metathesis reaction toward completion only by heating to temperatures at least 30°C
above the mixing temperature at any time during the work time period. The control
agent, and the amount thereof, also allows for control of the viscosity build up rate
as the metathesis reaction proceeds, which is useful for many molding applications.
The reaction control agent is a hydrocarbon with one or more carbon-carbon double
bonds and/or triple bonds or a modified hydrocarbon with one or more Group 14 and/or
15 heteroatoms. These hydrocarbons may optionally further contain oxygen and/or sulfur
atoms and the heteroatoms may also be bonded to one or more hydrocarbon fragments
containing double bonds and/or triple bonds. Advantageously, the double and triple
bond groups are allyl (2-propenyl), vinyl (ethenyl), ethynyl or propargyl (2-propynyl)
groups. Also advantageously, the reaction control agent includes more than one double
or triple bond group. In an exemplary embodiment of the invention, the reaction control
agent is tetraallyl silane (TAS):

[0010] The catalyst and the reaction control agent are mixed with an olefinic substrate
to initiate the metathesis reaction with a controlled rate. By way of example, the
olefinic substrate may be a polysiloxane end-capped with cycloalkenyl groups that
are capable of undergoing a metathesis reaction. In yet another embodiment, norbornenylethyl
terminated and tethered polydimethylsiloxane resins are used.
DETAILED DESCRIPTION
[0011] The present invention provides a method of curing a composition by a metathesis reaction
wherein a ruthenium or osmium carbene complex is mixed together with a reaction control
agent to allow control of the progress of the metathesis reaction on an olefin-containing
substrate, and the composition is subjected to thermal activation to accelerate the
rate of the metathesis reaction to allow the reaction to proceed toward completion.
[0012] The catalysts useful in the method of the present invention include ruthenium or
osmium carbene complexes. The catalyst may have the following structure:

wherein:
M is ruthenium or osmium,
X is an alkylidene ligand with basicity higher than that of tricyclohexylphosphine
(PCy3),
X1 is a neutral electron donor ligand with a basicity lower than that of tricyclohexylphosphine,
X2 and X3 are either the same or different and are any anionic ligand, and
R1 and R2 are either the same or different and are each independently hydrogen or a substituent
selected from the group consisting of C1-C20 alkyl, C2-C20 alkynyl, C2-C20 alkynyl, aryl, C1-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxycarbonyl, C1-C20 alkylthio, C1-C20 alkylsulfonyl and C1-C20 alkylsulfinyl, wherein each of the substituents is substituted or unsubstituted.
[0013] One example of such catalyst, the parent benzylidene ruthenium complex 1, with the
following structure, exhibits good air and water stability:

wherein Ph is phenyl, and Cy is cyclohexyl.
The ring-opening metathesis activity and air stability of the parent complex 1 can
be increased by substituting an alkylidene ligand X, such as a saturated imidazolidine
ligand, for one of the tricyclohexylphosphine ligands, in accordance with the following
formula:

[0014] The ligands X may be 4,5-dihydroimidazol-2-ylidenes, which have the following general
structure:

[0015] These substituted alkylidene ligands X have a basicity or proton affinity higher
than that of tricyclohexylphosphine, which is believed to contribute to the higher
activity and higher air stability. A derivative of complex
1 containing the alkylidene 1,3-bis(2,4,6-trimethylphenyl)-imidazol-2-ylidene (sIMES)
ligand is shown here:

wherein Mes is mesityl (2,4,6 trimethylphenyl). Other 4,5-dihydroimidazol-2-ylidenes
can also be used to afford ruthenium carbene complexes
3 and
4 having the following structures:

wherein Mes is mesityl, Ph is phenyl, and Cy is cyclohexyl.
[0016] To achieve a longer working time (pot life) and improve compatibility with reaction
control agents, tricyclohexylphosphine (PCy
3) is substituted with a neutral electron donor ligand X
1 with a lower basicity (as expressed by the pKa) or proton affinity than PCy
3 as shown below:

[0017] Examples of compound types that can be used as neutral electron donor ligands are:
phosphines, phosphites, phosphinites or phosphonites. In an exemplary embodiment,
X
1 is a phosphine of the formula PR
3R
4R
5 where R
3, R
4, and R
5 are alkyl, aralkyl or aryl, with a basicity lower than that of PCy
3. In a further exemplary embodiment, R
3, R
4, and R
5 are n-butyl, such that X
1 is tri-n-butylphosphine (PBu
3), and X is sIMES as shown below as structure 5:

[0018] The method further comprises mixing a reaction control agent with the catalyst and
olefinic substrate. After mixing of the composition components, the catalyst initiates
the metathesis reaction while the control agent slows the progress of the metathesis
reaction, and thereby allows for an increase in the time period before cure, or before
the metathesis reaction proceeds to completion or to a desired extent short of completion.
The length of this time period, also called work time or pot life, is controlled by
preventing completion of the reaction until the composition is heated to a temperature
at least 30EC above the mixing temperature. By way of example, the composition components
may be mixed at ambient temperature, followed by heat curing at 60EC or greater, such
as 100EC or 150EC. By way of further example, the composition components may be mixed
at sub-ambient temperatures (at least 30°C below ambient), followed by raising the
temperature to at least ambient to complete the reaction. The reaction control agent
also allows for control of the viscosity build up as the metathesis reaction proceeds,
which is useful for many molding applications.
[0019] The reaction control agent is an organic compound that falls within two categories.
The first category of control agents includes modified hydrocarbons with one or more
heteroatoms selected from Group 14 or 15 of the periodic table. Group 14 currently
includes C, Si, Ge, Sn, and Pb, though C is understood to be excluded by definition
of a heteroatom. Group 15 currently includes N, P, As, Sb and Bi. A heteroatom is
understood to refer to an atom other than carbon or hydrogen in an organic compound.
The modified hydrocarbon may optionally further contain oxygen or sulfur atoms. Also,
optionally, the heteroatoms may be bonded to one or more hydrocarbon fragments containing
a double or triple bond, for example, allyl, vinyl, ethynyl and propargyl-containing
fragments. Examples of modified hydrocarbons with Group 14 heteroatoms include 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane
and 5-(trimethylsilyl)-1,3 cyclopentadiene. Examples of modified hydrocarbons with
Group 15 heteroatoms include 4-vinyl pyridine, triphenyl phosphine and tricyclohexyl
phosphine. Another example of modified hydrocarbons with Group 14 heteroatoms include
those having carbon-carbon double bonds and/or triple bonds and one or more central
Group 14 atoms, and can further contain, in the case of silicon as the central atom(s),
oxygen atoms connected to silicon to form siloxane bonds. In this embodiment, the
reaction control agent has the structure shown below:

wherein:
G is selected from the group consisting of L3,

and

L is a hydrocarbon fragment containing a double or triple bond;
L1-L9 are each independently selected from the group consisting of L, alkyl, aryl, aralkyl
or haloalkyl;
A is a Group 14 heteroatom;
n = 0-20; and
m = 0-20.
Of the Group 14 atoms, which include Si, Ge, Sn and Pb (excluding C), the central
atom is advantageously Si, Ge or Sn, and more advantageously Si.
[0020] In one embodiment, G=L
3 such that the reaction control agent is a tetracoordinated compound having at least
one substituent group L that is a hydrocarbon fragment containing a double or triple
bond. Allyl and vinyl groups are hydrocarbon fragments containing a double bond, for
example, and alkynyl groups, such as propargyl and ethynyl groups, are hydrocarbon
fragments containing a triple bond, for example.
For the other substituent groups L
1, L
2, L
3, if not a hydrocarbon fragment containing a double or triple bond, then the substituent
group is an alkyl, aryl, aralkyl or haloalkyl group, which are essentially inert to
the metathesis reaction. Thus, it is the hydrocarbon fragment containing the double
or triple bond that determines the extent of the retardation of the metathesis reaction,
such that a greater number of such hydrocarbon fragments would be expected to achieve
longer working times than similar structures containing fewer of such hydrocarbon
fragments. An exemplary inert substituent is the methyl group. Examples of control
agents of this embodiment include tetraallylsilane, tetraallylstannane, allyltrimethyl
silane, ethynyltrimethyl silane, tetravinylsilane, and vinyl trimethylsilane.
[0021] In the embodiment where G is defined as:

the central atom A is Si, such that the reaction control agent contains a straight
chain siloxane compound in which the ends of the chain are capped by hydrocarbon fragments
containing a double or triple bond. The substituent groups within the chain (i.e.,
L
1, L
2, L
4, L
5, L
6, L
7) may also be hydrocarbon fragments containing double or triple bonds or may be an
inert substituent including alkyl, aryl, aralkyl or haloalkyl groups. By way of example,
where A is silicon and n=0, a disiloxane compound is formed, such as divinyltetramethyldisiloxane.
[0022] In the embodiment where G is:

a structure is formed having a chain of single-bonded Group 14 atoms where the ends
of the chain are capped by hydrocarbon fragments containing a double or triple bond.
As with the previous embodiment, the substituent groups within the chain (i.e., L
1, L
2, L
8, L
9) may be either the hydrocarbon fragment with the double or triple bond or may be
an inert alkyl, aryl, aralkyl or haloalkyl group. Where m=2, for example, a 3 atom
chain is formed with 2 hydrocarbon fragment double or triple bond end groups and 6
L
1-L
9 substituent groups.
[0023] The second category of reaction control agents include hydrocarbons containing one
or more double or triple bond functional groups, for example, allyl, vinyl, ethynyl
or propargyl groups. The hydrocarbon may optionally further contain sulfur and/or
oxygen atoms. Examples of these hydrocarbons include trimethylolpropane diallyl ether,
diallyl phthalate, glyoxyl bis(diallyl acetal), pentaerythritol triacrylate and C
14 diol dimethacrylate.
[0024] In the method of the present invention, the metathesis reaction is initiated upon
mixing of the composition components, but the progress of the reaction is slowed by
the presence of the reaction control agent. While the composition remains at the mixing
temperature, the metathesis reaction proceeds slowly and the viscosity build up is
gradual. Upon exposing the composition to an elevated temperature at least 30°C greater
than the mixing temperature, the catalyst is further activated to accelerate the rate
of the metathesis reaction and allow the metathesis reaction to proceed toward completion.
However, if the composition remains at the mixing temperature beyond a certain time,
the catalyst may become deactivated, such that it no longer has the potency to complete
the metathesis reaction upon application of the elevated temperature. Thus, in the
method of the present invention, exposure to the elevated temperature is carried out
prior to deactivation of the catalyst. The time at which the catalyst will deactivate
will vary for different reaction control agents. The hardness after the elevated temperature
curing step is indicative of the potency of the catalyst. A hardness of 0 after the
elevated temperature curing step indicates that a complete deactivation of the catalyst
occurred prior to the heat treatment.
[0025] The method further comprises mixing the catalyst and control agent with an olefin-containing
substrate (compound or mixture of compounds), such as a cycloolefin-containing compound
or mixture of compounds or an acyclic olefin-containing compound or mixture of compounds,
to initiate the metathesis reaction, such as ROMP. Advantageously, for a composition
curable by ROMP, the compound or mixture of compounds comprises at least one cyclic
olefin functionalized majority (> 50%) siloxane oligomer or polymer that is telechelic,
tethered, tri-functional and/or quadri-functional. The compound or mixture of compounds
curable by ROMP comprises one or a combination of the following: a polymerizable telechelic
siloxane-based polymer end-capped with an olefin group curable by ROMP; a polymerizable
siloxane-based polymer tethered and end-capped with an olefin group curable by ROMP;
a polymerizable tri-functional siloxane-based oligomer or polymer end-capped with
an olefin group curable by ROMP; and a polymerizable quadri-functional siloxane-based
oligomer or polymer end-capped with an olefin group curable by ROMP. The olefin groups
may be cycloalkenyl groups, for example norbornenyl or norbornenylethyl groups. The
cycloalkenyl functionalized PDMS resins that are cured via ROMP have a higher hydrocarbon
content than the vinyl functionalized PDMS resins that are used in hydrosilation reactions.
The higher hydrocarbon content leads to a lower dielectric constant, which is desirable
for many electronic applications.
[0026] In addition to the above category of oligomers and polymers, the olefin-containing
substrate may comprise any other cycloalkenyl-functionalized oligomers or polymers
that may undergo polymerization via ROMP mechanism, such as reactive cycloolefins.
Acyclic olefin-functionalized compounds that may undergo acyclic diene metathesis
polymerization are also contemplated.
[0027] The method of the present invention contemplates forming a catalyst paste and a base
paste that upon mixture with one another, form a curable paste/paste system in which
the metathesis reaction proceeds. Generally, in this system, the catalyst paste comprises
the metathesis catalyst for initiating polymerization, and a solvent for the catalyst
that is miscible or dispersible with the base paste and that does not interfere with
the metathesis reaction. The solvent may be, for example, 3-phenyl-heptamethyl-trisiloxane.
Another exemplary solvent is a partially phenyl substituted poly(dimethylsiloxane),
such as Dow Corning fluid 556. The base paste generally comprises the olefin-containing
substrate that is curable via ROMP or other metathesis reaction, and the reaction
control agent. The composition may further include filler systems and/or optional
additives suitable for the particular application, such as pigments or surfactants,
that do not interfere with the reaction.
[0028] The method of the present invention may be used to replace curing methods using the
hydrosilation reaction system of platinum catalysts and dual resin systems. The metathesis
reaction is a homo-reaction using a single resin system, which simplifies the formulation,
for example using the NBE-functionalized PDMS resins in combination with a ruthenium
carbene complex catalyst. The method of the present invention enables easy formulation
and curing of RTV materials, for example, a material similar to RTV6428 (GE Silicones,
Waterford, NY), as set forth in Example 1 below, because the viscosity range and working
time characteristics are similar to those materials.
[0029] The reaction control agent is incorporated into the base paste, to slow the ROMP
mechanism upon mixing of the catalyst paste and base, thereby increasing the working
time of the resin before cure, and to prevent completion of the ROMP mechanism in
the absence of an elevated temperature above the mixing temperature. While numerous
retarders are known for use with the platinum catalysts in the hydrosilation mechanism,
unexpectedly, some of the most common of them are not effective with the ruthenium
carbene catalysts in the ROMP mechanism. However, tetraallyl silane (TAS), for example,
has been found to provide significantly increased working time, particularly with
catalyst 5. Similarly, other modified hydrocarbon compounds having a Group 14 or 15
heteroatom and optionally one or more carbon-carbon double and/or triple bonds have
also been found to be effective, as explained further, below, as well as hydrocarbons
without the Group 14 or 15 heteroatom but containing one or more double and/or triple
bonds.
EXAMPLE
[0030] Resins 1 and 2 were formulated to provide similar properties to that of the commercial
RTV silicon marketed by GE, referred to as RTV6428. While RTV6428 is mixed with a
1:1 base/catalyst ratio, Resins 1 and 2 were mixed with a 10:1 ratio. A telechelic
polydimethylsiloxane (PDMS) end-capped with norbornenylethyl groups was used in the
base paste, with n=243 as shown below:

[0031] The base paste formulation is provided below in Table 1:
TABLE 1
| Base Paste Composition (wt.%) |
| PDMS resin end-capped with norbornenylethyl groups |
71 |
| Hexamethyldisilazane treated Crystalline silica |
9 |
| Sub-micron hydrophobic Silica |
20 |
| Total |
100 |
[0032] The catalyst used in the catalyst paste is PCy
3 substituted ruthenium carbene complex (2) for Resin 1 and the PBu
3 substituted ruthenium carbene complex (5) for Resin 2, each obtained from Materia,
Inc., Pasadena, California. The catalyst component was formulated by dissolving it
in a partially phenyl substituted polymethylsiloxane, in particular, Dow Corning Fluid
556. The catalyst paste formulation is provided in Table 2:
TABLE 2
| Test Catalyst Paste Composition (wt.%) |
| Dow Corning Fluid 556 |
36.05 |
| Calcium Silicate Wollastonite (2-10µm) |
53.70 |
| Sub-micron Silica |
10 |
| Catalyst Complex 2 or 5 |
0.25 |
| Total |
100 |
[0033] The base paste and catalyst paste were mixed at ambient temperature. The physical
properties for Resins 1 and 2 and the commercial RTV6428 composition are provided
in Table 3. Also provided in Table 3 are the properties of two other 10:1 commercial
RTV materials, RTV630, marketed by GE Silicones (Waterford, NY) and V-2330 marketed
by Rhodia (Troy, NY).
TABLE 3
| Physical Property Comparison of Short Working Time Silicones |
| |
RTV6428 |
RTV630 |
V-2330 |
Resin 1 |
Resin 2 |
| Catalyst |
Pt-based |
Pt-based |
Pt-based |
2 |
5 |
| Mixing Ratio |
1:1 |
10:1 |
10:1 |
10:1 |
10:1 |
| Viscosity of Base (Pa.s) |
0.88 |
113 |
14.8 |
19.6 |
19.6 |
| Working Time WT (h,m,s) |
1m, 34s |
2h, 30m |
10m |
1m, 28s |
~ 10-30m |
| Set time ST (h,m,s) |
2m, 43s |
6h, 30m |
1h, 10m |
3m, 20s |
5h, 30m |
| Tensile Strength (MPa) |
3.57
(0.30) |
6.27
(0.18) |
2.89
(0.77) |
3.47
(0.40) |
2.16
(0.36) |
| Elongation (%) |
85
(6) |
299
(24) |
325
(52) |
244
(16) |
235
(4) |
| Hardness, Shore A (100°C) |
62 |
54 |
29 |
37 |
36 |
| Tear Strength (N/mm) |
3.3
(0.4) |
12.3
(2.2) |
12.37
(0.51) |
5.49
(0.06) |
4.62
(0.47) |
[0034] The Resin 1 and RTV6428 compositions provide similar working times and set times,
as well as tensile strength. The compositions have different elongation, hardness
and tear strength, which may be attributed to the type of filler and the extent of
filler loading. The data in Table 3 suggests that catalyst
5 is far more sluggish at room temperature than catalyst
2, but affords materials with the same hardness. Thus, a straight chain C
4 alkyl phosphine is less active than a cyclic C
6 alkyl phosphine, such that longer working times may be achieved by limiting the phosphine
ligands to acyclic C
1-C
5 alkyls. Thus, for applications desiring longer working times, a composition of the
invention containing ruthenium carbene complex
5 having the tributylphosphine ligand provides advantageous results compared to a composition
containing complex
2. However, the RTV630 composition still provides longer work and set times than Resin
2.
[0035] By using reaction control agents in the formulation, it is believed that longer working
times, up to several hours, can be achieved at room temperature prior to curing at
elevated temperature. Also, some reaction control agents may be used to allow deactivation
only below 120°C to enable the composition's use as an LSR material. As discussed
in the Background of the Invention, RTV and LSR materials cured by the hydrosilation
reaction used a retarder mixed with the catalyst component, such as an amine or acetylenic
compound, to control the working time and/or to allow the hydrosilation reaction to
occur at the mold temperature only. Some of the retarders used with the hydrosilation
mechanism were investigated to determine their effectiveness as reaction control agents
with the ROMP mechanism, specifically compounds
11,14 and
15 in Table 4 below. Resin 2 containing catalyst
5 with the tributylphosphine ligand was used as the control resin, with 0% retarder.
In each of the test resins, 0.14 mg/g concentration of reaction control agent was
added to the base paste, and the weight percent of the resin was reduced by an equivalent
amount. Unexpectedly, it was found that the commonly used retarders listed above for
hydrosilation are ineffective in ROMP-cured RTV and LSR materials. However, one reaction
control agent, specifically tetraallyl silane (TAS) at a concentration of 0.14 mg/g,
had a remarkable effect on the working time, delaying it from about 31 minutes (Resin
2) to about 4½ hours. The working time at room temperature (RT) and the Shore A hardness
after thermal treatment of the cured resins is provided in Table 4. Working time was
determined by inserting a plastic stick into the paste and measuring the time at which
the stick was no longer able to manipulate the paste and at which the stick could
be removed from the paste without any appreciable amount of paste adhering to the
stick.
TABLE 4
| Reaction Control Agent (RCA) |
RCA Mol. Wt. |
RCA mm/g resin |
Working Time WT (RT)** |
Shore A Hardness (after oven cure*) |
| Control-Resin 2 |
-- |
-- |
~ 10-30 min |
35 |
| Tetravinyl silane (2) |
136.77 |
0.00102 |
~ 1 h |
28 |
| 1,5,7-Tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane (3) |
344.66 |
0.00041 |
~ 30 min |
30 |
| Vinyltrimethylsilane (4) |
100.24 |
0.00140 |
~ 40 min |
38 |
| Vinylpentamethyldisiloxane (5) |
174.39 |
0.00080 |
~ 50 min |
37 |
| Tetraallyl silane (TAS, 6) |
192.37 |
0.00073 |
~4h 30min |
36 |
| Divinyltetramethyldisiloxane (7) |
186.4 |
0.00075 |
~ 30 min |
35 |
| Ethynyl TriMethylSilane (8) |
98.22 |
0.00143 |
~ 14 min |
37 |
| Allyl TriPhenylSilane (9) |
300.48 |
0.00047 |
~ 18 min |
36 |
| PentaErythritol Triacrylate (10) |
298.3 |
0.00047 |
~ 12 min |
37 |
| 1-Ethynyl-1-CycloHexanol (11) |
124.18 |
0.00113 |
~ 17 min |
0 |
| C14 Diol Dimethacrylate (12) |
338.49 |
0.00041 |
~10 min |
38 |
| Pyridine (13) |
79.1 |
0.00177 |
~ 20 min |
36 |
| TriEthylAmine (14) |
101.1 |
0.00138 |
~ 12 min |
38 |
| Benzotriazole (15) |
119.1 |
0.00118 |
~ 1h 30 min |
8 |
*Cured in oven at 100°C for one hour after the onset of working time. A zero value
for hardness indicates a failure of the paste to cure, thereby indicating deactivation
of the catalyst.
** Because the working time was tested by a manual method, the results are only accurate
to +/- 10% of the value of the WT given, and the results are particularly inaccurate
in the case of quick curing compositions, such as the control resin. |
With the exception of TAS
(6), some of the known retarders had little to no effect on slowing the ROMP reaction
and some even appeared to act as weak accelerators. Not only did the addition of a
small quantity of TAS drastically increase the working time, but it did so without
affecting the hardness of the cured resin. Benzotriazole, commonly used with the hydrosilation
reaction, was not effective due to its inability to harden (cure) even after exposure
to elevated temperature for one hour. From the results of Table 4, it would appear
that structures containing multiple allyl groups are more effective than analog structures
containing multiple vinyl groups.
[0036] Some of the reaction control agents from Table 4 were also tested at a higher concentration
of 0.7 mg/g, to further investigate their effect on slowing the progress of the metathesis
reaction. The results are shown below in Table 5. Again, Resin 2 was used, substituting
the reaction control agent for an equivalent amount of the PDMS resin.
TABLE 5
| Reaction Control Agent (RCA) |
RCA Mol. Wt. |
RCA mm/g resin |
Working Time WT (RT) |
Shore A Hardness (after oven cure*) |
| Control-Resin 2 |
-- |
-- |
~ 10-30 min |
35 |
| Tetraallyl silane (TAS, 6) |
192.37 |
0.00364 |
~48 h |
25** |
| Ethynyl TriMethylSilane (8) |
98.22 |
0.00713 |
~ 40 min |
36 |
| Allyl TriPhenylSilane (9) |
300.48 |
0.00233 |
~ 70 min |
35 |
| PentaErythritol Triacrylate (10) |
298.3 |
0.00235 |
~ 50 min |
36 |
| C14 Diol Dimethacrylate (12) |
338.49 |
0.00207 |
~ 35 min |
37 |
* Material was placed in an oven at 100°C for one hour after the onset of working
time.
** For TAS, Shore A hardness at 24 h is 34 at 100°C and 35 at 150°C. Shore A hardness
at 48h is 35 at 150°C. |
Again, the TAS
(6) reaction control agent has a remarkable effect on the ROMP reaction by catalyst
5, slowing it considerably, to provide a working time with the resin of 48 hours.
[0037] Given the remarkable effectiveness of the TAS control agent with catalyst
5, additional testing was performed. In particular, the TAS structure contains a central
tetracoordinated silicon atom with the substituent groups being hydrocarbon fragments
containing a double bond. Analog vinyl structures were also tested to further investigate
the effect of the double bond. Potential reaction control agents were investigated
having less than 4 allyl or vinyl substituents with the remaining substituents being
inert groups, such as methyl. Similarly, hydrocarbon fragments containing a triple
bond rather than a double bond were also investigated, in particular ethynyl and propargyl
(2-propynyl) groups, which are examples of alkynyl groups. In addition to silicon
as the central atom, tin was also tested to investigate the effectiveness of other
Group 14 central atoms, wherein Group 14 refers to the 1988 IUPAC system for identifying
groups in the periodic table. Group 14 includes silicon, germanium, tin and lead (excluding
carbon).
In addition to a sole central atom, straight chain groups containing Group 14 atoms
are also contemplated, in particular, siloxane chains and single-bonded Group 14 chains
end functionalized with the hydrocarbon fragments. Modified hydrocarbons containing
Group 14 heteroatoms, as well as Group 15 heteroatoms, were also tested with the double
and/or triple bond groups being optional. These modified hydrocarbons also include
sulfur or oxygen atoms as an optional heteroatom. Hydrocarbons containing double and/or
triple bond groups were also investigated without having the Group 14 or 15 atom.
Sulfur and oxygen were optional components for these hydrocarbons, as well. The compounds
containing various functional groups that may act as reaction control agents were
tested at the same molar concentration (0.036 mm/g) in order to keep the molar ratio
of control agent to catalyst constant at 24.3. The results are provided in Table 6.
TABLE 6
| Reaction Control Agent |
Working Time WT (RT) |
Shore A after 100°C for 1 hour at WT |
| Control—Resin 2 |
~10-30 min |
35 |
| Vinyl Compounds |
| Tetravinyl silane (2) |
2 h |
26 |
| 1,3,5,7-Tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane (3) |
40 min |
26 |
| Vinyltrimethylsilane (4) |
1h |
36 |
| Vinylpentamethyldisiloxane (5) |
10 min |
37 |
| Divinyltetramethyldisiloxane (7) |
5 h |
32 |
| 5-(Trimethylsilyl)-1,3 cyclopentadiene |
15 min |
37 |
| Allyl Compounds |
| Tetraallyl silane (TAS, 6) |
48 hrs |
35 |
| Allyltrimethyl silane |
1hr |
35 |
| Tetraallyl stannane |
~25 hrs |
32 |
| Trimethylolpropane diallyl ether |
27 min |
31 |
| Diallyl phthalate |
24h |
27 |
| Glyoxal bis(diallyl acetal) |
~20 h |
35 |
| Acrylate and Methacrylate Compounds |
| PentaErythritol Triacrylate (10) |
50 min |
34 |
| C14 Diol Dimethacrylate (12) |
35 min |
36 |
| Ebecryl® 350 Silicon Dimethacrylate* |
35 min |
36 |
| Alkynyl Compounds |
| Ethynyltrimethyl silane (8) |
2 hrs, 20 min |
30 |
| Propargyltrimethyl silane |
~26 hrs |
36 |
| Amines |
| N,N,N',N'-Tetraallyl Ethylenediamine |
~66 h |
0 |
| 4,4'-Bipyridyl |
40 min |
40 |
| Pyridine (13) |
30min |
35 |
| 4-Vinyl pyridine |
2h 30min |
36 |
| Quinazoline |
20 min |
39 |
| Quinoline |
30 min |
37 |
| Ebecryl® P-115 Acrylated amine* |
20 min |
36 |
| 4-Dimethylaminopyridine (DMAP) |
40 min |
39 |
| Phosphines |
| TriPhenyl Phosphine |
~20 h |
34 * |
| Tricyclohexyl Phosphine |
~20 h |
39 * |
| *UCB Chemicals, Smyrna, GA |
[0038] As the results of Table 6 show, the control agent TAS
(6) containing multiple allyl groups is the most efficient at slowing the metathesis
reaction. However, there were a broad variety of compound types tested as reaction
control agents, as listed in Table 6. Comparing the results of the ethynyl- and propargyl-trimethyl
silanes to the vinyl- and allyl-trimethyl silanes, it would appear that in analog
structures triple bonds may be more efficient at slowing the metathesis reaction than
corresponding double bonds. In general terms, with the silane series, the propargyl
(2-propynyl) functional group is the strongest followed by the allyl group (2-propenyl),
while the vinyl group is the weakest.
The presence of more than one unsaturated group in the silane derivative also increases
the control effect, as indicated by comparing the results obtained by tetraallyl silane
with the results obtained by allyltrimethylsilane. Substituting the Si atom in the
TAS with another Group 14 atom, such as Sn, to afford tetraallylstannane also gives
substantial reaction slowing. Good retarding activity is obtained in the case of diallyl
phthalate and glyoxal bis(diallyl acetal), indicating that oxygen bonded allyl groups
can also be effective. Aside from the vinyl group-containing 4-vinyl pyridine, which
has a weak effect, the amines did not seem to have an effect, even with the presence
of an allyl group, as was the case with N,N,N'N'-tetraallyl ethylenediamine, where
the composition could not be cured. However, it is noted that further testing is needed
to determine whether the catalyst was deactivated upon mixing with the reaction control
agent or whether there is a delayed time after mixing at which the catalyst deactivates,
such that elevated cure can be achieved, in accordance with the method of the present
invention, prior to expiration of that delayed time. The acrylates had only a weak
effect, which is believed to be due to the electron withdrawing effect of the carbonyl
attached to the double bond. The two phosphines tested have a significant slowing
effect on the metathesis reaction even though they do not contain any unconjugated
double or triple bonds. It may be inferred in this case that the phosphines can act
as substitute ligands on the metal atom of the catalyst and therefore operate under
a separate mechanism for modifying the rate of reaction than what is described for
the other compound types above.
[0039] Based on the above, it can be expected that a Group 14 tetra-coordinate central atom
bonded to hydrocarbon fragments containing double bonds will have high retarding activity,
and this activity will be increased in the order 2-propynyl > 2-propenyl » ethynyl
> ethenyl (vinyl). Also the retarding activity will be higher for higher numbers of
unsaturated groups present. Group 15 tri-coordinate compounds, such as phosphines,
appear to have substantial retarding activity even in the absence of unconjugated
double bonds. It can be inferred then that in the general case of phosphines, arsines
and stibines there is an electron pair available on the heteroatom which is expected
to act as an electron donor to the metal center and therefore affect its reactivity
to metathesis.
[0040] We also measured the viscosity of the paste mixture containing TAS as it varied with
time after mixing at ambient temperature. The hardness was measured at each time interval,
after curing for 1 hr. at 100°C. The results are shown in Table 7.
TABLE 7
| Time |
Viscosity (Pa.s) |
Shore A Hardness (100°C) |
| Immediately After Mixing |
26 |
25 |
| 24h After Mixing |
28 |
34 |
| 48h After Mixing |
119 |
25 |
| 96h After Mixing |
190 |
0 |
Control (no TAS)
Immediately After Mixing |
11 |
36 |
[0041] From the data in Table 7, it can be concluded that the viscosity build up with TAS
is gradual and that the mixture can only be cured by heat within a certain time window.
In other words, the metathesis reaction must be completed by heat curing before the
catalyst loses its potency to metathesize the olefinic substrate, i.e., before the
catalyst deactivates. In the case of TAS, the catalyst deactivates at some period
between 48 and 96 hrs. after mixing. This can be of an advantage for an LSR or RTV
application since residual material will not cure inside the dosing equipment, which
would be undesirable.
[0042] Potential uses for compositions of the present invention include automotive applications,
electric/electronics applications, electro and appliances, medical applications, textile
applications, and other miscellaneous applications. By way of example and not limitation,
automotive applications may include: distributor caps, cable bushings, loudspeaker
covers, housing seals, bellows, plug seals, spark plug boots, vent flaps, grommets
for weather packs, central door locker membranes, o-rings, gaskets, bushings, boots,
and combined elements with thermoplastics. By way of example and not limitation, electric/electronics
applications may include: sockets for antennas, terminals, plug connections, conductors
(overvoltage), insulators (high voltage), housing seals, reinforced insulating hoses,
vibration dampers (collectors), switch membrane covers (damp room switches), watch
seals, insulating parts for hot adhesive guns, key pads for computers and telephones,
anode caps, insulators and surge arresters, diaphragms, grommets, cable seals, and
covers for switches. By way of example and not limitation, electro and appliance applications
may include: small seals, cable bushings, reinforced insulating hoses, lamp seals,
appliance feet, membranes, o-rings, diffuser for hair dryers, gaskets for faucets,
gaskets for pressure cookers, detergent seals for dish washers, parts for coffee and
espresso machines, coated glass fiber hoses for electric stoves, and water diffuser
for shower bath. By way of example and not limitation, medical applications may include:
seals for medical appliances, syringe plungers, breast nipple protectors, base plates
(dental), inflating bellows, catheters, instrument mats, sterilization mats, o-rings
for dialysers, earplugs, pipette nipples, catheter holders, cannula protection sleeves,
nose clamps, valves and bellows for respirators, baby bottle nipples, baby pacifiers,
stoppers, respiratory masks, Foley catheters, electrodes, parts for dental applications,
and parts for medical equipment. By way of example and not limitation, textile applications
may include: textile coating for conveyor belts, tents, compensators and technical
applications, sleeves for electrical and heat insulation, heat reflecting fabrics
for steel worker's coats, airbag coating, and printing inks. By way of example and
not limitation, miscellaneous applications may include: swimming goggles, snorkels
and mouthpieces for snorkels, elements for sport shoes, diving masks, swimming caps,
respiratory devices, photocopier rolls and butcher's gloves. All of the foregoing
are intended to be exemplary uses for the compositions of the present invention and
are not intended to limit the invention in any way.
1. A method of curing a composition by a metathesis reaction, comprising the steps of:
(a) mixing an olefin-containing substrate, a metal carbene complex catalyst and a
reaction control agent at a mixing temperature to form a mixture,
wherein the catalyst is effective to initiate the metathesis reaction upon mixing,
and
wherein the reaction control agent is present in an amount sufficient to slow the
progress of the metathesis reaction and to prevent the metathesis reaction from proceeding
to completion in the absence of an elevated temperature above the mixing temperature,
and
wherein the olefin-containing substrate includes at least one oligomer or polymer
selected from the group consisting of: a telechelic siloxane-based oligomer or polymer
end-capped with olefin groups curably by the metathesis reaction, a siloxane-based
oligomer or polymer tethered and end-capped with olefin groups curable by the metathesis
reaction, a tri-functional siloxane-based oligomer or polymer end-capped with olefin
groups curable by the metathesis reaction, and a quadri-functional siloxane-based
oligomer or polymer end-capped with olefin groups curable by the metathesis reaction,
and
wherein the metal carbene complex catalyst has the structure:

wherein:
M is ruthenium or osmium,
X is an alkylidene ligand with basicity higher than that of tricyclohexylphosphine
(PCy3),
X1 is a neutral electron donor ligand with a basicity lower than that of tricyclohexylphosphine,
X2 and X3 are either the same or different and are any anionic ligand, and
R1 and R2 are either the same or different and are each independently hydrogen or a substituent
selected from the group consisting of C1-C20 alkyl, C2-C20 alkenyl, C1-C20 alkynyl, aryl, C1-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxycarbonyl, C1-C20 alkylihio, C1-C20 alkylsulfonyl and C1-C20 alkylsultinyl, wherein each of the substituents is substituted or unsubstituted;
and
wherein the reaction control agent is selected from the group consisting of:
1) modified hydrocarbons containing at least one heteroatom selected from Group 14
and 15 of the periodic table, and optionally containing one or more oxygen atoms,
sulfur atoms, or both, and wherein the at least one heteroatom is optionally bonded
to one or more hydrocarbon fragments containing a double or triple bond, and
2) hydrocarbons containing one or more double or triple bond functional groups, and
optionally containing one or more oxygen atoms, sulfur atoms, or both; and
(b) prior to deactivation of the catalyst, exposing the mixture to the elevated temperature
of at least 30°C greater than the mixing temperature to accelerate the rate of the
metathesis reaction to allow the reaction to proceed toward completion.
2. The method of claim 1 wherein the at least one oligomer or polymer has a > 50% majority
siloxane backbone functionalized with the olefin groups curable by the metathesis
reaction, and
wherein the metal carbene complex catalyst has the formula:

wherein Ph is phenyl, X is an alkylidene ligand having a basicity higher than that
of tricyclohexylphosphine (PCy
3), and X
1 is a phosphine, phosphite, phosphinite or phosphonite having a basicity lower than
that of PCy
3.
3. The method of either of claims 1 or 2 wherein the substrate comprises a polysiloxane
tethered and end-capped with cycloalkenyl groups capable of undergoing a metathesis
reaction.
4. The method of either of claims 1 or 2 wherein the substrate comprises a polysiloxane
end-capped with cycloalkenyl groups capable of undergoing a metathesis reaction.
5. The method of either of claims 3 or 4 wherein the cycloalkenyl groups are norbornenyl
groups.
6. The method of either of claims 3 or 4 wherein the cycloalkenyl groups are norbomenylethyl
groups.
7. The method of claim 2 wherein X1 is a phosphine of the formula PR3R4R5 wherein R3, R4, and R5 are each an alkyl, aralkyl or aryl.
8. The method of claim 7 wherein X1 is a phosphine of the formula PR3R4R5
wherein R3, R4, and R5 are each n-butyl.
9. The method of claim 1 wherein R1 is phenyl and R2 is hydrogen.
10. The method of any of claims 1-9 wherein the X has the structure:

wherein Mes is mesityl and R' is hydrogen or phenyl.
11. The method of any of claims 1-9 wherein the X has the structure:

wherein Mes is mesityl.
12. The method of any of claims 1-9 wherein the catalyst has the structure:

wherein Bu is butyl, Ph is phenyl and Mes is mesityl.
13. The method of any of claims 1-12 wherein the mixing step includes a group 2) reaction
control agent, and the one or more functional groups are selected from an allyl group,
a vinyl group, an ethynyl group or a propargyl group.
14. The method of claim 13 wherein the group 2) reaction control agent includes at least
two functional groups.
15. The method of claim 13 wherein the group 2) reaction control agent includes at least
three functional groups.
16. The method of claim 13 wherein the group 2) reaction control agent further includes
one or more oxygen atoms, sulfur atoms, or both.
17. The method of claim 13 wherein the group 2) reaction control agent is diallyl phthalate
or glyoxal bis(diallyl acetal).
18. The method of any of claims 1-12 wherein the mixing step includes a group 1) reaction
control agent containing a Group 14 heteroatom.
19. The method of claim 18 wherein the group 1) reaction control agent further includes
one or more oxygen atoms, sulfur atoms, or both.
20. The method of claim 18 wherein the group 1) reaction control agent further includes
one or more hydrocarbon fragments containing a group selected from an allyl group,
a vinyl group, an ethynyl group or a propargyl group.
21. The method of claim 18 wherein the group 1) reaction control agent is tetraallylsilane,
tetraallylstannane, tetravinylsilane, tetraallylgermane, divinyltetramethyldisiloxane,
allyltrimethylsilane, ethynyltrimethylsilane, or vinyltrimethylsilane.
22. The method of claim 18 wherein the group 1) reaction control agent has the structure:

wherein:
G is selected from the group consisting of: L
3,

and

L is a hydrocarbon fragment containing a double or triple bond,
L
1 -L
9 are each independently selected from the group consisting of L, alkyl, aryl, aralkyl
or haloalkyl,
A is a Group 14 heteroatom,
n = 0-20, and
m = 0-20.
23. The method of any of claims 1-12 wherein the mixing step includes a group 1) reaction
control agent containing a Group 15 heteroatom.
24. The method of claim 23 wherein the group 1) reaction control agent further includes
one or more oxygen atoms, sulfur atoms, or both.
25. The method of claim 23 wherein the group 1) reaction control agent further includes
one or more hydrocarbon fragments containing a group selected from an allyl group,
a vinyl group, an ethynyl group or a propargyl group.
26. The method of claim 23 wherein the group 1) reaction control agent is 4-vinyl pyridine,
triphenyl phosphine or tricyclohexyl phosphine.
27. The method of any of claims 1-26 wherein the mixing step is at ambient temperature
and the exposing step is at the elevated temperature of at least 60°C.
28. The method of claim 27 wherein the exposing step is at the elevated temperature of
at least 100°C.
29. The method of any of claims 1-26 wherein the mixing step is at a temperature at least
30°C below ambient and the exposing step is at the elevated temperature of at least
ambient temperature.
1. Verfahren zum Härten einer Zusammensetzung durch eine Metathesereaktion, das die folgenden
Schritte beinhaltet:
(a) Mischen eines olefinhaltigen Substrats, eines Metallcarben-Komplex-Katalysators
und eines Reaktionslenkungsmittels bei einer Mischtemperatur, um ein Gemisch zu bilden,
wobei der Katalysator die Metathesereaktion nach dem Mischen einleitet, und
wobei das Reaktionslenkungsmittel in einer Menge vorliegt, die ausreicht, um das Fortschreiten
der Metathesereaktion zu verlangsamen und zu verhindern, dass die Metathesereaktion
in Abwesenheit einer erhöhten Temperatur über der Mischtemperatur bis zur Vollendung
fortfährt, und
wobei das olefinhaltige Substrat wenigstens ein Oligomer oder Polymer enthält, das
ausgewählt ist aus der Gruppe bestehend aus: einem telechelen Oligomer oder Polymer
auf Siloxanbasis, "endcapped" mit Olefingruppen, die durch die Metathesereaktion härtbar
sind, einem Oligomer oder Polymer auf Siloxanbasis, verbunden und endcapped mit Olefingruppen,
die durch die Metathesereaktion härtbar sind, einem trifunktionellen Oligomer oder
Polymer auf Siloxanbsis, endcapped mit Olefingruppen, die durch die Metathesereaktion
härtbar sind, und einem tetrafunktionellen Oligomer oder Polymer auf Siloxanbasis,
endcapped mit Olefingruppen, die durch die Metathesereaktion härtbar sind, und
wobei der Metallcarben-Komplex-Katalysator die folgende Struktur hat:

wobei:
M Ruthenium oder Osmium ist,
X ein Alkylidenligand mit einer höheren Basizität als Tricyclohexylphosphin (PCy3) ist,
X1 ein neutraler Elektronendonatorligand mit einer geringeren Basizität als der von
Tricyclohexylphosphin ist,
X2 und X3 entweder gleich oder unterschiedlich und ein beliebiger anionischer Ligand sind,
und
R1 und R2 entweder gleich oder unterschiedlich und jeweils unabhängig Folgendes sind: Wasserstoff
oder ein Substituent, ausgewählt aus der Gruppe bestehend aus C1-C20-Alkyl, C2-C20-Alkenyl, C2-C20-Alkynyl, Aryl, C1-C20-Carboxylat, C1-C20-Alkoxy, C2-C20-Alkenyloxy, C2-C20-Alkynyloxy, Aryloxy, C2-C20-Alkoxycarbonyl, C1-C20-Alkylthio, C1-C20-Alkylsulfonyl und C1-C20-Alkylsulfinyl, wobei jeder der Substituenten substituiert oder nichtsubstituiert
ist; und
wobei das Reaktionslenkungsmittel ausgewählt ist aus der Gruppe bestehend aus:
1) modifizierten Kohlenwasserstoffen, die wenigstens ein Heteroatom enthalten, das
ausgewählt ist aus der Gruppe 14 und 15 der Tabelle des Periodensystems, und optional
ein oder mehrere Sauerstoffatome, Schwefelatome oder beides enthalten, und wobei das
wenigstens eine Heteroatom optional an ein oder mehrere Kohlenwasserstofffragmente
gebunden ist, die eine Doppel- oder Dreifachbindung enthalten, und
2) Kohlenwasserstoffen, die eine oder mehrere funktionelle Gruppen mit Doppel- oder
Dreifachbindung enthalten und optional ein oder mehrere Sauerstoffatome, Schwefelatome
oder beides enthalten; und
b) vor der Deaktivierung des Katalysators das Aussetzen des Gemischs der erhöhten
Temperatur von wenigstens 30°C über der Mischtemperatur, um die Geschwindigkeit der
Metathesereaktion zu beschleunigen, damit die Reaktion zur Vollendung hin fortfahren
kann.
2. Verfahren nach Anspruch 1, wobei das wenigstens eine Oligomer oder Polymer ein Rückgrat
hat, das mehrheitlich (>50 %) aus Siloxan besteht, funktionalisiert mit den Olefingruppen,
die durch die Metathesereaktion härtbar sind, und
wobei der Metallcarben-Komplex-Katalysator die folgende Formel hat:

wobei Ph Phenyl ist, X ein Alkylidenligand mit einer höheren Basizität als die von
Tricyclohexylphosphin (PCy
3) ist und X
1 ein Phosphin, Phosphit, Phosphinit oder Phosphonit mit einer geringeren Basizität
als die von PCy
3 ist.
3. Verfahren nach Anspruch 1 oder 2, wobei das Substrat ein Polysiloxan umfasst, gebunden
und endcapped mit Cycloalkenylgruppen, die eine Metathesereaktion durchlaufen können.
4. Verfahren nach Anspruch 1 oder 2, wobei das Substrat ein Polysiloxan umfasst, endcapped
mit Cycloalkenylgruppen, die eine Metathesereaktion durchlaufen können.
5. Verfahren nach Anspruch 3 oder 4, wobei die Cycloalkenylgruppen Norbornenylgruppen
sind.
6. Verfahren nach Anspruch 3 oder 4, wobei die Cycloalkenylgruppen Norbornenylethylgruppen
sind.
7. Verfahren nach Anspruch 2, wobei X1 ein Phosphin der Formel PR3R4R5 ist, wobei R3, R4 und R5 jeweils ein Alkyl, Aralkyl oder Aryl sind.
8. Verfahren nach Anspruch 7, wobei X1 ein Phosphin der Formel PR3R4R5 ist, wobei R3, R4 und R5 jeweils n-Butyl sind.
9. Verfahren nach Anspruch 1, wobei R1 Phenyl ist und R2 Wasserstoff ist.
10. Verfahren nach einem der Ansprüche 1-9, wobei das X die folgende Struktur hat:

wobei Mes Mesityl und R' Wasserstoff oder Phenyl ist.
11. Verfahren nach einem der Ansprüche 1-9, wobei das X die folgende Struktur hat:

wobei Mes Mesityl ist.
12. Verfahren nach einem der Ansprüche 1-9, wobei der Katalysator die folgende Struktur
hat:

wobei Bu Butyl ist, Ph Phenyl ist und Mes Mesityl ist.
13. Verfahren nach einem der Ansprüche 1-12, wobei der Mischschritt ein Reaktionslenkungsmittel
der Gruppe 2) beinhaltet und die eine oder mehreren funktionellen Gruppen ausgewählt
sind aus einer Allylgruppe, einer Vinylgruppe, einer Ethynylgruppe oder einer Propargylgruppe.
14. Verfahren nach Anspruch 13, wobei das Reaktionslenkungsmittel der Gruppe 2) wenigstens
zwei funktionelle Gruppen enthält.
15. Verfahren nach Anspruch 13, wobei das Reaktionslenkungsmittel der Gruppe 2) wenigstens
drei funktionelle Gruppen enthält.
16. Verfahren nach Anspruch 13, wobei das Reaktionslenkungsmittel der Gruppe 2) ferner
ein oder mehrere Sauerstoffatome, Schwefelatome oder beides enthält.
17. Verfahren nach Anspruch 13, wobei das Reaktionslenkungsmittel der Gruppe 2) Diallylphthalat
oder Glyoxal-bis(diallylacetal) ist.
18. Verfahren nach einem der Ansprüche 1-12, wobei der Mischschritt ein Reaktionslenkungsmittel
der Gruppe 1) mit einem Heteroatom der Gruppe 14 beinhaltet.
19. Verfahren nach Anspruch 18, wobei das Reaktionslenkungsmittel der Gruppe 1) ferner
ein oder mehrere Sauerstoffatome, Schwefelatome oder beides enthält.
20. Verfahren nach Anspruch 18, wobei das Reaktionslenkungsmittel der Gruppe 1) ferner
ein oder mehrere Kohlenwasserstofffragmente enthält, die eine Gruppe enthalten, die
ausgewählt ist aus einer Allylgruppe, einer Vinylgruppe, einer Ethynylgruppe oder
einer Propargylgruppe.
21. Verfahren nach Anspruch 18, wobei das Reaktionslenkungsmittel der Gruppe 1) Tetraallylsilan,
Tetraallylstannan, Tetravinylsilan, Tetraallylgerman, Divinyltetramethyldisiloxan,
Allyltrimethylsilan, Ethynyltrimethylsilan oder Vinyltrimethylsilan ist.
22. Verfahren nach Anspruch 18, wobei das Reaktionslenkungsmittel der Gruppe 1) die folgende
Struktur hat:

wobei:
G ausgewählt ist aus der Gruppe bestehend aus: L
3,

und

L ein Kohlenwasserstofffragment ist, das eine Doppel-oder Dreifachbindung enthält,
L
1-L
9 jeweils unabhängig ausgewählt sind aus der Gruppe bestehend aus L, Alkyl, Aryl, Aralkyl
oder Haloalkyl,
A ein Gruppe-14-Heteroatom ist,
n = 0-20 und
m = 0-20.
23. Verfahren nach einem der Ansprüche 1-12, wobei der Mischschritt ein Reaktionslenkungsmittel
der Gruppe 1) mit einem Heteroatom der Gruppe 15 beinhaltet.
24. Verfahren nach Anspruch 23, wobei das Reaktionslenkungsmittel der Gruppe 1) ferner
ein oder mehrere Sauerstoffatome, Schwefelatome oder beides enthält.
25. Verfahren nach Anspruch 23, wobei das Reaktionslenkungsmittel der Gruppe 1) ferner
ein oder mehrere Kohlenwasserstofffragmente enthält, die eine Gruppe enthalten, die
ausgewählt ist aus einer Allylgruppe, einer Vinylgruppe, einer Ethynylgruppe oder
einer Propargylgruppe.
26. Verfahren nach Anspruch 23, wobei das Reaktionslenkungsmittel der Gruppe 1) 4-Vinylpyridin,
Triphenylphosphin oder Tricyclohexylphosphin ist.
27. Verfahren nach einem der Ansprüche 1-26, wobei der Mischschritt bei Umgebungstemperatur
und der Aussetzungsschritt bei der erhöhten Temperatur von wenigstens 60°C erfolgt.
28. Verfahren nach Anspruch 27, wobei der Aussetzungsschritt bei der erhöhten Temperatur
von wenigstens 100°C erfolgt.
29. Verfahren nach einem der Ansprüche 1-26, wobei der Mischschritt bei einer Temperatur
von wenigstens 30°C unter Umgebungstemperatur und der Aussetzungsschritt bei der erhöhten
Temperatur von wenigstens Umgebungstemperatur erfolgt.
1. Procédé de durcissement d'une composition par réaction de métathèse, comprenant les
étapes de :
(a) mélange d'un substrat contenant une oléfine, d'un catalyseur complexe métal carbène
et d'un agent de contrôle de réaction à une température de mélange afin de former
un mélange,
dans lequel le catalyseur est efficace pour lancer la réaction de métathèse au moment
du mélange, et
dans lequel l'agent de contrôle de réaction est présent dans une quantité suffisante
pour ralentir la progression de la réaction de métathèse et empêcher la réaction de
métathèse de se poursuivre jusqu'à son terme en l'absence d'une température élevée
au-dessus de la température de mélange, et
dans lequel le substrat contenant une oléfine comporte au moins un oligomère ou un
polymère sélectionné dans le groupe consistant en : un oligomère ou polymère à base
de siloxane téléchélique terminé par des groupes oléfine durcissable par la réaction
de métathèse, un oligomère ou polymère à base de siloxane fixé et terminé par des
groupes oléfine durcissable par la réaction de métathèse, un oligomère ou polymère
à base de siloxane trifonctionnel terminé par des groupes oléfine durcissable par
la réaction de métathèse, et un oligomère ou polymère à base de siloxane quadri-fonctionnel
terminé par des groupes oléfine durcissables par la réaction de métathèse, et
dans lequel le catalyseur complexe métal carbène a la structure :

où :
M représente le ruthénium ou l'osmium,
X représente un ligand alkylidène d'une basicité supérieure à celle de la tricyclohexylphosphine
(PCy3),
X1 représente un ligand donneur d'électrons neutre d'une basicité inférieure à celle
de la tricyclohexylphosphine,
X2 et X3 sont soit identiques, soit différents et représentent n'importe quel ligand anionique,
et
R1 et R2 sont soit identiques, soit différents et représentent chacun indépendamment de l'hydrogène
ou un substituant sélectionné dans le groupe consistant en C1-C20 alkyle, C2-C20 alkényle, C2-C20 alkynyle, aryle, C1-C20 carboxylate, C1-C20 alkoxy, C2-C20 alkenyloxy, C2-C20 alkynyloxy, aryloxy, C2-C20 alkoxycarbonyle, C1-C20 alkylthio, C1-C20 alkylsulfonyle et C1-C20 alkylsulfinyle, dans lequel chacun des substituants est substitué ou non substitué
; et
dans lequel l'agent de contrôle de réaction est sélectionné dans le groupe consistant
en
1) hydrocarbures modifiés contenant au moins un hétéroatome sélectionné dans le Groupe
14 et 15 du tableau périodique, et contenant optionnellement un ou plusieurs atomes
d'oxygène, atomes de soufre, ou les deux, et dans lequel l'au moins un hétéroatome
est optionnellement lié à un ou plusieurs fragments d'hydrocarbure contenant une liaison
double ou triple, et
2) hydrocarbures contenant un ou plusieurs groupes fonctionnels à liaison double ou
triple, et contenant optionnellement un ou plusieurs atomes d'oxygène, atomes de soufre,
ou les deux ; et
3) avant la désactivation du catalyseur, l'exposition du mélange à la température
élevée d'au moins 30°C de plus que la température de mélange afin d'accélérer la vitesse
de la réaction de métathèse et permettre à la réaction de se poursuivre jusqu'à son
terme.
2. Procédé selon la revendication 1, dans lequel l'au moins un oligomère ou polymère
a un squelette de siloxane majoritaire > 50% fonctionnalisé avec les groupes oléfine
durcissable par la réaction de métathèse, et
dans lequel le catalyseur complexe métal carbène a la formule :

où Ph représente le phényle, X représente un ligand alkylidène d'une basicité supérieure
à celle de la tricyclohexylphosphine (PCy
3), et X
1 représente une phosphine, un phosphite, un phosphinite ou un phosphonite d'une basicité
inférieure à celle de la PCy
3.
3. Procédé selon la revendication 1 ou 2, dans lequel le substrat comprend un polysiloxane
fixé et terminé par des groupes cycloalkényle capable de subir une réaction de métathèse.
4. Procédé selon la revendication 1 ou 2, dans lequel le substrat comprend un polysiloxane
terminé par des groupes cycloalkényle capables de subir une réaction de métathèse.
5. Procédé selon la revendication 3 ou 4, dans lequel les groupes cycloalkényle sont
des groupes norbornényle.
6. Procédé selon la revendication 3 ou 4, dans lequel les groupes cycloalkényle sont
des groupes norbornényléthyle.
7. Procédé selon la revendication 2, dans lequel X1 représente une phosphine de la formule PR3R4R5, où R3, R4 et R5 représentent chacun un alkyle, aralkyle ou aryle.
8. Procédé selon la revendication 7, dans lequel X1 représente une phosphine de la formule PR3R4R5, où R3, R4 et R5 représentent chacun un n-butyle.
9. Procédé selon la revendication 1, dans lequel R1 représente le phényle et R2 l'hydrogène.
10. Procédé selon l'une quelconque des revendications 1 à 9, dans lequel-X a la structure
:

où Mes représente le mésityle et R
1 représente l'hydrogène ou le phényle.
11. Procédé selon l'une quelconque des revendications 1 à 9, dans lequel X a la structure
:

où Mes représente le mésityle.
12. Procédé selon l'une quelconque des revendications 1 à 9, dans lequel le catalyseur
a la structure :

où Bu représente le butyle, Ph le phényle et Mes le mésityle.
13. Procédé selon l'une quelconque des revendications 1 à 12, dans lequel l'étape de mélange
comporte un agent de contrôle de réaction du groupe 2), et les un ou plusieurs groupes
fonctionnels sont sélectionnés dans un groupe allyle, un groupe vinyle, un groupe
éthynyle ou un groupe propargyle.
14. Procédé selon la revendication 13, dans lequel l'agent de contrôle de réaction de
groupe 2) comporte au moins deux groupes fonctionnels.
15. Procédé selon la revendication 13, dans lequel l'agent de contrôle de réaction de
groupe 2) comporte au moins trois groupes fonctionnels.
16. Procédé selon la revendication 13, dans lequel l'agent de contrôle de réaction de
groupe 2) comporte en outre un ou plusieurs atomes d'oxygène, atomes de soufre ou
les deux.
17. Procédé selon la revendication 13, dans lequel l'agent de contrôle de réaction de
groupe 2) est du phtalate de diallyle ou du glyoxal bis(diallyle acétal).
18. Procédé selon l'une quelconque des revendications 1 à 12, dans lequel l'étape de mélange
comporte un agent de contrôle de réaction de groupe 1) contenant un hétéroatome de
Groupe 14.
19. Procédé selon la revendication 18, dans lequel l'agent de contrôle de réaction de
groupe 1) comporte en outre un ou plusieurs atomes d'oxygène, atomes de soufre, ou
les deux.
20. Procédé selon la revendication 18, dans lequel l'agent de contrôle de réaction de
groupe 1) comporte en outre un ou plusieurs fragments d'hydrocarbure contenant un
groupe sélectionné parmi un groupe allyle, un groupe vinyle, un groupe éthynyle ou
un groupe propargyle.
21. Procédé selon la revendication 18, dans lequel l'agent de contrôle de réaction de
groupe 1) est un tétraallylsilane, tétraallylstannane, tétravinylsilane, tétraallylgermane,
divinyltétraméthyldisiloxane, allyltriméthylsilane, éthynyltriméthylsilane ou vinyltriméthylsilane.
22. Procédé selon la revendication 18, dans lequel l'agent de contrôle de réaction de
groupe 1) a la structure :

où
G est sélectionné dans le groupe consistant en : L
3,

et
L est un fragment d'hydrocarbure contenant une liaison double ou triple,
L
1 à L
9 sont chacun sélectionnés indépendamment dans le groupe consistant en L, alkyle, aryle,
aralkyle ou haloalkyle,
A est un hétéroatome de Groupe 14,
N = 0 à 20, et
M = 0 à 20.
23. Procédé selon l'une quelconque des revendications 1 à 12, dans lequel l'étape de mélange
comporte un agent de contrôle de réaction de groupe 1) contenant un hétéroatome de
Groupe 15.
24. Procédé selon la revendication 23, dans lequel l'agent de contrôle de réaction de
groupe 1) comporte en outre un ou plusieurs atomes d'oxygène, atomes de soufre, ou
les deux.
25. Procédé selon la revendication 23, dans lequel l'agent de contrôle de réaction de
groupe 1) comporte en outre un ou plusieurs fragments d'hydrocarbure contenant un
groupe sélectionné dans un groupe allyle, un groupe vinyle, un groupe éthynyle ou
un groupe propargyle.
26. Procédé selon la revendication 23, dans lequel l'agent de contrôle de réaction de
groupe 1) est une 4-vinyle pyridine, une triphényle phosphine ou une tricyclohexylephosphine.
27. Procédé selon l'une quelconque des revendications 1 à 26, dans lequel l'étape de mélange
s'effectue à température ambiante et l'étape d'exposition s'effectue à la température
élevée d'au moins 60°C.
28. Procédé selon la revendication 27, dans lequel l'étape d'exposition s'effectue à la
température élevée d'au moins 100°C.
29. Procédé selon l'une quelconque des revendications 1 à 26, dans lequel l'étape de mélange
s'effectue à une température d'au moins 30°C en dessous de la température ambiante
et l'étape d'exposition s'effectue à la température élevée d'au moins la température
ambiante.