TREA

PROCESS FOR THE PREPARATION OF HALOGENOALKYLDIALKYL CHLOROSILANE

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Information

  • Patent Application
  • 20080275264
  • Publication Number
    20080275264
  • Date Filed
    July 16, 2008
    15 years ago
  • Date Published
    November 06, 2008
    15 years ago
Information
Abstract
The present invention relates to a process for the preparation of 3-chloropropyldimethylchlorosilane by hydrosilylation reaction in a reaction medium comprising dimethylhydrochlorosilane and allyl chloride, in the presence of a catalytically effective amount of di-μ-chlorobis(η-1,5-cyclooctadiene)diiridium, the said process being characterized in that at least one auxiliary in the free or supported state selected from the group of compounds consisting of: (i) ketones,(ii) ethers,(iii) quinones,(iv) anhydrides,(v) unsaturated hydrocarbon compounds (UHC) having an aromatic nature and/or comprising at least one C═C double bond and/or at least one C≡C triple bond, it being possible for these unsaturated bonds to be conjugated or nonconjugated, the said UHCs being linear or cyclic (mono- or polycyclic), having from 4 to 30 carbon atoms, having from 1 to 8 ethylenic and/or acetylenic unsaturations and optionally comprising one or more heteroatoms,(vi) and their mixtures, is added to the reaction medium, with the condition according to which, when the auxiliary comprises one or more UHCs as defined above, then this (these) UHC(s) is (are) mixed with at least one other auxiliary other than a UHC.
Description

The present invention relates to a process for the preparation of haloalkyldialkylhalosilane.


More particularly, the present invention relates to a process for the preparation of 3-halopropyldimethylchlorosilane by hydrosilylation of dimethylhydrochlorosilane using allyl chloride and a catalyst based on a platinum ore metal, in particular iridium, and optional recovery of the said metal. The reaction involved in this example is as follows:







In this type of reaction, the amounts of platinum ore metal involved are often high with the aim of obtaining a satisfactory yield. Under these conditions, in order for the process to remain economically advantageous, it is necessary to recover the platinum ore metal in order to be able to reuse it as catalyst.


Another route for improving the economics of the process would be to optimize the activity of the catalyst. To do this, it is arranged for the degree of conversion (DC) of the hydrosilane (II) to be increased or, for a given DC, for the selectivity (S) of the catalyst to be significantly increased.


In the present account, the degree of conversion (DC) and the selectivity (S) correspond to the following definitions:






TT
=


number





of





moles





of





SiH





units





consumed


number





of





moles





of





SiH





units





or





of






(
II
)






introduced








S
=


number





of





moles





of






(
I
)



number





of





moles





of





SiH





units





or





of






(
II
)






introduced






The hydrosilylation of allyl chloride by dimethylhydrochlorosilane catalyzed by an iridium-based catalyst is disclosed in the following patent documents: JP-B-2938731 and JP-A-7126271. The catalysts disclosed in these patent documents are of the [Ir(diene)Cl]2 type and make possible access to full degrees of conversion (DC=100%) of the dimethylhydrochlorosilane with a good selectivity of the reaction (good yield YD of 3-chloropropyldimethylchlorosilane). However, these performances are achieved at the cost of very large amounts of catalyst.


EP-A-1 156 052 (=U.S. Pat. No. 6,359,161) and DE-A-10053037 (US-A-2002/0052520) disclose:







in the presence of free COD for increasing the yield:

    • EP-A-1 156 052: 4×10−3 mol of free COD per 1×10−4 mol of [Ir(COD)Cl]2:i.e. a ratio of 40,
    • versus DE-A-10053037: 9.2×10−4 mol of free COD per 4.5×10−6 mol of [Ir(COD)Cl]2:i.e. a ratio of 204.


BE-B-785343 (U.S. Pat. No. 3,798,252) discloses the hydrosilylation of allyl chloride by trichlorohydrosilane in the presence of chloroplatinic acid in solution in cyclohexanone (removal of water from the solution using Na2SO4). The ketone is combined with the platinum in order to improve the selectivity of the reaction.


In this state of the art, one of the essential objects of the present invention is to provide a means which makes it possible to optimise the activity of the iridium-based catalyst in comparison with what is taught in the prior art [in particular EP-A-1 156 052 (=U.S. Pat. No. 6,359,161) and DE-A-10053037 [US-A-2002/0052520].


Another essential object of the invention is to provide a process for the preparation of a haloalkyldialkylhalosilane of the above type which is effective, economical and easy to implement.


These objects, among others, are achieved by the invention, which relates, first, to a process for the preparation of a haloalkyldialkylhalosilane of formula (I):





Hal-(R2R3)Si—(CH2)s-Hal


by hydrosilylation reaction of a reaction medium comprising:

    • a silane of formula (II):





Hal-(R2R3)Si—H

    • and an alkenyl halide of formula (III):





CH═CH—(CH2)s-2Hal

    • in the presence of a catalytically effective amount of a hydrosilylation catalyst based on iridium in the oxidation state I or III,


      in which formulae (I), (II), (III):
    • the symbol Hal represents a halogen atom chosen from the chlorine, bromine and iodine atoms,
    • the symbols R2 et R3, which are identical or different, each represent a monovalent hydrocarbon group chosen from a linear or branched alkyl radical having from 1 to 6 carbon atoms and a phenyl radical, and
    • s represents an integer between 2 and 10 inclusive,


      the said process being characterized in that at least one auxiliary in the free or supported state selected from the group of compounds consisting of:
    • (i) ketones,
    • (ii) ethers,
    • (iii) quinones,
    • (iv) anhydrides,
    • (v) unsaturated hydrocarbon compounds (UHC) having an aromatic nature and/or comprising at least one C═C double bond and/or at least one C≡C triple bond, it being possible for these unsaturated bonds to be conjugated or nonconjugated, the said UHCs being linear or cyclic (mono- or polycyclic), having from 4 to 30 carbon atoms, having from 1 to 8 ethylenic and/or acetylenic unsaturations and optionally comprising one or more heteroatoms,
    • (vi) and their mixtures,


      is added to the reaction medium, with the condition according to which, when the auxiliary comprises one or more UHCs as defined above, then this (these) UHC(s) is (are) mixed with at least one other auxiliary other than a UHC.


In accordance with the present invention, the term “mixtures (vi)” of auxiliary compounds is understood in particular to mean:

    • (vi.1) any mixture of compounds (I) and/or (ii) and/or (iii) and/or (iv) and/or (v),
    • (vi.2) any compound having a molecule comprising at least two different chemical functional groups selected from the group consisting of the ketone, ether, anhydride, quinone, C═C and C≡C functional groups characteristic of the compounds (i) to (v),
    • (vi.3) any mixture of compounds (vi.2),
    • (vi.4) and any mixture based on at least one compound (i) to (v) and on at least one compound (vi.2).


According to a preferred form, use is made of a catalyst based on iridium in the oxidation state I, in the structure of which each iridium atom corresponds to the complex form of the Ir(L)3X type where the symbols L and X have the definitions given in the work “Chimie Organométallique” [Organométallic Chemistry] by Didier Astruc, published in 2000 by EDP Sciences (cf. in particular page 31 et seq.).


According to a more preferred form, the catalyst corresponds to the formula (IV):





[Ir(R4)x(R5)]y  (IV)

    • in which:
    • the symbol R4 represents either a monodentate ligand L, and in this case x=2, or a bidentate ligand (L)2, and in this case x=1, and
    • the symbol R5 represents either Hal as defined above, and in this case y=2, or a ligand of type LX, and in this case y=1.


Catalysts corresponding to the more preferred definition mentioned above in which:

    • R4 is a ligand comprising at least one C═C double bond and/or at least one C≡C triple bond, it being possible for these unsaturated bonds to be conjugated or nonconjugated, the said ligand being linear or cyclic (mono- or polycyclic), having from 4 to 30 carbon atoms, having from 1 to 8 ethylenic and/or acetylenic unsaturations and optionally comprising one or more heteroatoms, and
    • R5, in addition to Hal, can also represent a ligand LX, such as in particular a ligand derived from acetylacetone, from a β-ketoester, from a malonic ester or from an allyl compound,
    •  are highly suitable.


According to an even more preferred form, the catalyst corresponds to the formula (IV) where the symbol R5 of the catalyst represents Hal and y=2.


The ligands R4 of the preferred catalyst (IV) can be identical to or different from the UHCs (v) of the auxiliary.


The iridium-based catalyst can be supported, as is disclosed, for example, in U.S. Pat. No. 6,177,585 and GB-A-1 526 324.


The catalytic system used in accordance with the process according to the invention makes it possible to reduce the amount of catalyst necessary for the achievement of a full degree of conversion DC of the silane of formula (II): (Hal-(R2R3)Si—H) and/or to increase the selectivity S for a given and fixed DC.


This catalytic system is advantageously composed:

    • of an organometallic catalyst based on iridium in the oxidation state I or III,
    • of one or more auxiliaries each introduced in a minimum amount of 20 mol % with respect to the metal.


This or these auxiliaries can be used in the liquid or solid form. Provided that they are liquid, they can be introduced in an amount such that, in the reaction medium, they, in addition to acting as hydrosilylation promoter, act as solvent for the reaction.


The fact of being able to be employed in liquid form is a very major operational advantage for the process of the invention.


The possible function of solvent of the auxiliary can also make it possible, in particular when it is a heavy solvent (namely, a solvent having a boiling point at atmospheric pressure which is greater than that of the compound of formula (I), such as, for example, a polyether), to improve the stability of the reaction medium and thus the safety of the process. In addition, this offers possibilities of easy recovery of the catalyst and thus of recycling the latter.


When the auxiliary is in the free state, it can be introduced into the reaction medium according to a molar ratio, with respect to the iridium metal, of at least 0.2, preferably of at least 1. Depending on the nature of the ligands, a molar ratio of greater than 10 and even of greater than 100 can more preferably be chosen.


In the case where the auxiliary comprises at least one compound selected from the group of the UHCs (v), taken by themselves or as mixtures with one another, the concentration of catalyst (preferably IV) is such that the iridium/silane of formula (II) molar ratio is less than or equal to 400×10−6, preferably less than or equal to 200×10−6 and more preferably still less than or equal to 50×10−6.


Reference may be made, as examples of suitable ketones (i), to those defined in U.S. Pat. No. 3,798,252 et in PL-A-176036, PL-A-174810, PL-A-145670 and JP-A-75024947.


Reference may be made, as examples of suitable ethers (ii), to those defined in U.S. Pat. No. 4,820,674 and in JP-A-52093718.


Advantageously, the auxiliary is selected from the group consisting in particular of: cyclohexanone, 2-cyclohexen-1-one, isophorone, 2-benzylidenecyclohexanone, 3-methylene-2-norbornanone, 4-hexen-3-one, 2-allylcyclohexanone, 2-oxo-1-cyclohexanepropionitrile, 2-(1-cyclohexenyl)cyclohexanone, monoglyme, ethylene glycol divinyl ether, ethyl ether, benzoquinone, phenylbenzoquinone, maleic anhydride, allyl succinic anhydride, 3-benzylidene-2,4-pentadione, phenothiazine, (methylvinyl)cyclotetrasiloxane (vinylated D4), 4-phenyl-3-butyn-2-one, 1,3-butadiene, 1,5-hexadiene, 1,3-cyclohexadiene, 1,5-cyclooctadiene (COD), 1,5,9-cyclododecatriene, divinyltetramethylsiloxane (DVTMS), norbornadiene and their mixtures.


According to a preferred embodiment of the invention, the auxiliary is a mixture (vi) comprising at least one UHC (v), preferably COD, and at least one ketone (i), preferably cyclohexanone, and/or at least one ether (ii) and/or at least one quinone (iii).


In this preferred embodiment of the process according to the invention, the concentration of catalyst, preferably of formula (IV), is such that the iridium/silane of formula (II) molar ratio is less than or equal to 100×10−6, preferably less than or equal to 60×10−6, and more preferably still is between 40×10−6 and 1×10−6.


According to a procedure specific to this preferred embodiment, the components of the mixture (vi), UHC/(i) and/or (ii) and/or (iii), are present in the reaction medium when the reaction begins.


Mention will be made, as examples of iridium complexes of formula (IV) which are especially well suited, of those corresponding to the even more preferred form, in the formula of which the symbol R4 is a ligand chosen from 1,3-butadiene, 1,5-hexadiene, 1,3-cyclohexadiene, 1,5-cyclooctadiene (COD), 1,5,9-cyclododecatriene, divinyltetramethylsiloxane and norbornadiene.


Mention will be made, as specific examples of iridium complexes (IV) which are even better suited, of the following catalysts:

  • di-μ-chlorobis(η-1,5-hexadiene)diiridium,
  • di-μ-bromobis(η-1,5-hexadiene)diiridium,
  • di-μ-iodobis(η-1,5-hexadiene)diiridium,
  • di-μ-chlorobis(η-1,5-cyclooctadiene)diiridium,
  • di-μ-bromobis(η-1,5-cyclooctadiene)diiridium,
  • di-μ-iodobis(η-1,5-cyclooctadiene)diiridium,
  • di-μ-chlorobis(η-2,5-norbornadiene)diiridium,
  • di-μ-bromobis(η-2,5-norbornadiene)diiridium,
  • di-μ-iodobis(η-2,5-norbornadiene)diiridium.


The process according to the invention can be employed either continuously, semicontinuously or batchwise.


These three operating methods are suitable in particular when the catalyst, preferably IV, is used in a homogeneous liquid medium, according to a preferred arrangement of the invention and as disclosed in JP-B-2 938 731 and EP-A-1 156 052.


Preferably, the product of formula (I) is 3-chloropropyldimethylchlorosilane, the product of formula (II) is dimethylhydrochlorosilane and the product of formula (III) is allyl chloride.


According to another of its aspects, the invention relates to a catalytic system for the preparation of a haloalkyldialkylhalosilane of formula (I):





Hal-(R2R3)Si—(CH2)s-Hal


by hydrosilylation reaction of a reaction medium comprising:

    • a silane of formula (II):





Hal-(R2R3)Si—H

    • and an alkenyl halide of formula (III):





CH═CH—(CH2)s-2Hal


in which formulae:

    • the symbol Hal represents a halogen atom chosen from the chlorine, bromine and iodine atoms,
    • the symbols R2 et R3, which are identical or different, each represent a monovalent hydrocarbon group chosen from a linear or branched alkyl radical having from 1 to 6 carbon atoms and a phenyl radical, and
    • s represents an integer between 2 and 10 inclusive, characterized in that it comprises:
      • 1—a hydrosilylation catalyst based on iridium in the oxidation state I, in the structure of which each iridium atom corresponds to the complex form of the Ir(L)3X type where the symbols L and X have the definitions given in the work “Chimie Organométallique” [Organometallic Chemistry] by Didier Astruc, published in 2000 by EDP Sciences (cf. in particular page 31 et seq.), this catalyst preferably corresponding to the formula:





[Ir(R4)x(R5)]y  (IV)

      • in which:
    • the symbol R4 represents either a monodentate ligand L, and in this case x=2, or a bidentate ligand (L)2, and in this case x=1, and
    • the symbol R5 represents either Hal, Hal representing a halogen atom chosen from chlorine, bromine and iodine atoms, and in this case y=2, or a ligand of type LX, and in this case y=1,
      • 2- and at least one auxiliary in the free or supported state selected from the group of compounds consisting of:
        • (i) ketones,
        • (ii) ethers,
        • (iii) quinones,
        • (iv) anhydrides,
        • (v) unsaturated hydrocarbon compounds (UHC) having an aromatic nature and/or comprising at least one C═C double bond and/or at least one C≡C triple bond, it being possible for these unsaturated bonds to be conjugated or nonconjugated, the said UHCs being linear or cyclic (mono- or polycyclic), having from 4 to 30 carbon atoms, having from 1 to 8 ethylenic and/or acetylenic unsaturations and optionally comprising one or more heteroatoms,
        • (vi) and their mixtures,


          with the condition according to which, when the auxiliary comprises one or more UHCs as defined above, then this (these) UHC(s) is (are) mixed with at least one other auxiliary other than a UHC.







EXAMPLES

The following examples illustrate the invention without limiting the scope thereof. They have the object of evaluating catalytic systems: [di-μ-chlorobis(η-1,5-cyclooctadiene)diiridium+hydrosilylation auxiliary(ies)] in the reaction for the hydrosilylation of allyl chloride by dimethylhydrochlorosilane.


The tests are carried out in parallel reactors.


Each reactor is equipped with a magnetic stirrer, with a reflux condenser and with a thermometer. The heat-exchange fluid is brought to a temperature of −35° C., which makes it possible to obtain a material balance always greater than 95% by weight.


The effect of the hydrosilylation auxiliaries is compared with a control reaction, where only di-μ-chlorobis(η-1,5-cyclooctadiene)diiridium was used. For this control test, an intentionally low amount of catalyst was introduced in order to obtain a degree of conversion of the corresponding SiH functional groups of the order of 50%.


The dimethylhydrochlorosilane, with a purity of 99% by weight, is added by running onto a heel, composed of the allyl chloride (1.05 mol. eq./silane) and of the catalytic system


[di-μ-chlorobis(η-1,5-cyclooctadiene)diiridium+hydrosilylation auxiliary(ies)] heated to 35° C. The silane is run in via a syringe driver at a flow rate of 1.3 ml/minute. The temperature of the reaction medium is not regulated.


The reaction medium is analyzed by gas chromatography calibrated with n-tetradecane.


I: Hydrosilylation Auxiliaries Used Alone:

1.1—Effect of the Ketones (i):














TABLE I







Ketone/
Ir/ClMe2SiH




Ex-

Ir molar
molar ratio
DC
S


ample
Ketone
ratio
(×10−6)
(%)
(%)




















1
None
0
235
94
76


2
Cyclohexanone
100
235
80
91


3
None
0
130
50
82


4
2-Cyclohexen-1-one
91
133
44
91


5
2-Allylcyclohexanone
100
133
41
92


6
2-(1-Cyclohexenyl)-
137
132
51
90



cyclohexanone


7
3-Benzylidene-2,4-
1.2
131
59
81



pentadione


8
3-Benzylidene-2,4-
115
134
42
92



pentadione









1.2—Effect of the Ethers (ii):














TABLE II








Ir/ClMe2SiH






Ether/Ir
molar ratio


Example
Ether
molar ratio
(×10−6)
DC (%)
S (%)




















3
None
0
130
50
82


9
Monoglyme
109
131
60
81


10
Monoglyme
260
136
45
86


11
Ethyl ether
740
134
60
89









1.3—Effect of the Quinones (iii):














TABLE III








Ir/ClMe2SiH






Quinone/Ir
molar ratio


Example
Quinone
molar ratio
(×10−6)
DC (%)
S (%)




















3
None
0
130
50
82


12
Benzoquinone
93
141
40
94


13
Phenylbenzo-
1.1
137
51
84



quinone









1.4—Effect of the Anhydrides (iv):














TABLE IV








Ir/ClMe2SiH




Ex-

Anhydride/Ir
molar ratio


ample
Anhydride
molar ratio
(×10−6)
DC (%)
S (%)




















3
None
0
130
50
82


14
Allyl succinic
103
133
47
87



anhydride


15
Maleic anhydride
1.7
131
43
84









1.5—Effect of the UHC Auxiliaries (v):














TABLE V








Ir/ClMe2SiH






R4/Ir
molar ratio


Example
UHC (v)
molar ratio
(×10−6)
DC (%)
S (%)




















3
None
0
130
50
82


16
Vinylated D4
104
135
48
86


17
Phenothiazine
1.1
132
55
83









II: Combination of Hydrosilylation Auxiliaries
II.1—Combination of Cyclohexanone and of 1,5-Cyclooctadiene (1,5-COD):














TABLE VI





Ex-
Ir/ClMe2SiH
DC
S
Cyclohexanone/Ir
1,5-COD/Ir


ample
(×10−6)
(%)
(%)
molar ratio
molar ratio







18
51
21
70
—
—


19
49
15
82
189
—


  20(1)
50
29
85
—
135


21
51
94
96
170
110






(1)full conversion of the SiH functional groups can be obtained in the presence of free 1,5-COD only if a greater concentration of [IrCODCl]2 is introduced into the medium.






II.2—Combination of Ethyl Ether and of 1,5-Cyclooctadiene (1,5-COD):














TABLE VII






Ir/ClMe2SiH


Ethyl ether/Ir
1,5-COD/Ir


Example
(×10−6)
DC (%)
S (%)
molar ratio
molar ratio




















18
51
21
70
—
—


   20 (1)
50
29
85
—
135


22
51
100
98
100
148






(1) full conversion of the SiH functional groups can be obtained in the presence of free 1,5-COD only if a greater concentration of [IrCODCl]2 is introduced into the medium.






II.3—Combination of Benzoquinone and of 1,5-Cyclooctadiene (1,5-COD):














TABLE VIII









Benzo-




Ir/ClMe2SiH


quinone/Ir
1,5-COD/Ir


Example
(×10−6)
DC (%)
S (%)
molar ratio
molar ratio




















18
51
21
70
—
—


   20 (1)
50
29
85
—
135


23
50
100
97
51
110






(1) full conversion of the SiH functional groups can be obtained in the presence of free 1,5-COD only if a greater concentration of [IrCODCl]2 is introduced into the medium.






III: Example 2.4
Repetition of Example 2.1 with Regulation of the Temperature

92.48 g of allyl chloride (1.194 mol), 0.011 g of catalyst [Ir(COD)Cl]2 where COD=1,5-cyclooctadiene (2.829×10−5 mol), and also COD (0.611 g, 5.648 mmol) and cyclohexanone (1.067 g, 10.9 mmol), are charged to a 500 ml four-necked glass flask equipped with a stirrer and surmounted by a reflux condenser. The mixture is stirred in order to completely dissolve the catalytic system.


The dimethylhydrochlorosilane, with a purity of 99% by weight, is introduced into the reaction medium via a peristaltic pump. 107.15 g (1.117 mol) thereof are introduced over 2 hours 30 minutes. The flow rate for introduction is adjusted in order to maintain the temperature of the reaction medium between 20 and 25° C., taking into account the high exothermicity of the reaction. The reaction medium is kept stirred for 20 minutes after the end of the introduction of the dimethylhydrochlorosilane.


At the end of this period of 20 minutes, a sample is withdrawn for analysis. The results are as follows:


DC of the dimethylhydrochlorosilane=99.8%,


S for chloropropyldimethylchlorosilane=98.3% (by analysis by gas chromatography).

Claims
  • 1-12. (canceled)
  • 13. A method for the preparation of a haloalkyldialkylhalosilane of formula (I): Hal-(R2R3)Si—(CH2)s-Hal  (I)
  • 14. The method as defined by claim 13, said catalyst comprising iridium in the oxidation state 1, in the structure of which each iridium atom corresponds to the complex form of the Ir(L)3X type wherein the symbols L and X have the definitions given in the text “Chimie Organométallique” [Organometallic Chemistry] by Didier Astruc, published in 2000 by EDP Sciences (cf. page 31 et seq.).
  • 15. The method as defined by claim 14, said catalyst having the formula: [Ir(R4)x(R5)]y  (IV)in which:the symbol R4 represents either a monodentate ligand L, and in this case x=2, or a bidentate ligand (L)2 and in this case x=1, andthe symbol R5 represents either Hal, which represents a halogen atom selected from the group consisting of chlorine, bromine and iodine atoms, and in this case y=2, or a ligand of type LX, and in this case y=1.
  • 16. The method as defined by claim 15, wherein the formula (IV): R4 is a ligand comprising at least one C═C double bond and/or at least one C≡C triple bond, it being possible for these unsaturated bonds to be conjugated or nonconjugated, the said ligand being linear or cyclic (mono- or polycyclic), having from 4 to 30 carbon atoms, having from 1 to 8 ethylenic and/or acetylenic sites of unsaturation and optionally comprising one or more heteroatoms, andR5, in addition to Hal, can also represent a ligand LX derived from acetylacetone, from a β-ketoester, from a malonic ester or from an allyl compound.
  • 17. The method as defined by claim 13, wherein the auxiliary is introduced into the reaction medium in the free state and in a molar ratio, with respect to the iridium metal, of at least 0.2.
  • 18. The method as defined by claim 13, wherein the auxiliary comprises at least one compound selected from the group consisting of the UHCs (v) or mixture thereof and the concentration of catalyst is such that the iridium/silane of formula (II) molar ratio is less than or equal to 400×10−6.
  • 19. The method as defined by claim 13, wherein the auxiliary is selected from the group consisting of: cyclohexanone, 2-cyclohexen-1-one, isophorone, 2-benzylidenecyclohexanone, 3-methylene-2-norbornanone, 4-hexen-3-one, 2-allylcyclohexanone, 2-oxo-1-cyclohexanepropionitrile, 2-(1-cyclohexenyl)cyclohexanone, monoglyme, ethylene glycol divinyl ether, ethyl ether, benzoquinone, phenylbenzoquinone, maleic anhydride, allyl succinic anhydride, 3-benzylidene-2,4-pentadione, phenothiazine, (methylvinyl)cyclotetrasiloxane (vinylated D4), 4-phenyl-3-butyn-2-one, 1,3-butadiene, 1,5-hexadiene, 1,3-cyclohexadiene, 1,5-cyclooctadiene (COD), 1,5,9-cyclododecatriene, divinyltetramethylsiloxane (DVTMS), norbornadiene and mixtures thereof.
  • 20. The method as defined by claim 13, wherein the auxiliary is a mixture (vi) comprising at least one UHC (v) and at least one ketone (i) and/or at least one ether (ii) and/or at least one quinone (iii).
  • 21. The method as defined by claim 20, wherein the concentration of catalyst is such that the iridium/silane of formula (II) molar ratio is less than or equal to 100×10−6.
  • 22. The method as defined by claim 20, wherein the components of the mixture (vi), UHC/(i) and/or (ii) and/or (iii), are present in the reaction medium when the reaction is initiated.
  • 23. The method as defined by claim 13, wherein the product of formula (I) is 3-chloropropyldimethylchlorosilane, the product of formula (II) is dimethylhydrochlorosilane and the product of formula (III) is allyl chloride.
  • 24. A catalytic system for the preparation of a haloalkyldialkylhalosilane of formula (I): Hal-(R2R3)Si—(CH2)s-Hal  (I)by hydrosilylation reaction of a reaction medium comprising: a silane of formula (II): Hal-(R2R3)Si—H  (II)and an alkenyl halide of formula (III): CH═CH—(CH2)s-2Hal  (III)in which formulae: the symbol Hal represents a halogen atom selected from the group consisting of chlorine, bromine and iodine atoms,the symbols R2 et R3, which may be identical or different, are each a monovalent hydrocarbon radical selected from the group consisting of a linear or branched alkyl radical having from 1 to 6 carbon atoms and a phenyl radical, ands is an integer ranging from 2 to 10 inclusive, and which comprises:(1) a hydrosilylation catalyst based on iridium in the oxidation state 1, in the structure of which each iridium atom corresponds to the complex form of the Ir(L)3X type wherein the symbols L and X have the definitions given in the text “Chimie Organométallique” [Organometallic Chemistry] by Didier Astruc, published in 2000 by EDP Sciences, or having the formula: [Ir(R4)x(R5)]y  (IV)in which: the symbol R4 represents either a monodentate ligand L, and in this case x=2, or a bidentate ligand (L)2 and in this case x=1, andthe symbol R5 represents either Hal, Hal representing a halogen atom selected from the group consisting of chlorine, bromine and iodine atoms, and in this case y=2, or a ligand of type LX, and in this case y=1, and(2) at least one auxiliary in the free or supported state selected from the group of compounds consisting of:(i) ketones,(ii) ethers,(iii) quinones,(iv) anhydrides,(v) unsaturated hydrocarbon compounds (UHC) whether aromatic and/or comprising at least one C═C double bond and/or at least one C≡C triple bond, it being possible for these unsaturated bonds to be conjugated or nonconjugated, the said UHCs being linear or cyclic (mono- or polycyclic), having from 4 to 30 carbon atoms, having from 1 to 8 ethylenic and/or acetylenic sites of unsaturation and optionally comprising one or more heteroatoms, and(vi) mixtures thereof,
  • 25. The method as defined by claim 17, said molar ratio being at least 1.
  • 26. The method as defined by claim 17, said molar ratio being at least 100.
  • 27. The method as defined by claim 18, said molar ratio being less than or equal to 200×10−6.
  • 28. The method as defined by claim 18, said molar ratio being less than or equal to 50×10−6.
  • 29. The method as defined by claim 21, said molar ratio being less than or equal to 60×10−6.
  • 30. The method as defined by claim 21, said molar ratio ranging from 40×10−6 to 1×10−6.
  • 31. The method as defined by claim 20, said mixture comprising COD and cyclohexanone.
Priority Claims (1)
Number Date Country Kind
030222 Jun 2003 FR national
Continuations (1)
Number Date Country
Parent 10561223 Feb 2007 US
Child 12173968 US