US20070185344A1 - Method of preparing halogenoalkyldialkyl chlorosilane - Google Patents

Method of preparing halogenoalkyldialkyl chlorosilane Download PDF

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Publication number
US20070185344A1
US20070185344A1 US10/561,223 US56122304A US2007185344A1 US 20070185344 A1 US20070185344 A1 US 20070185344A1 US 56122304 A US56122304 A US 56122304A US 2007185344 A1 US2007185344 A1 US 2007185344A1
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Prior art keywords
hal
formula
auxiliary
iii
uhc
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US10/561,223
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English (en)
Inventor
Nathalie Guennouni
Jean-Christopher Galland
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Rhodia Chimie SAS
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Rhodia Chimie SAS
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Assigned to RHODIA CHIMIE reassignment RHODIA CHIMIE ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: GALLAND, JEAN-CHRISTOPHE, GUENNOUNI, NATHALIE
Publication of US20070185344A1 publication Critical patent/US20070185344A1/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F7/00Compounds containing elements of Groups 4 or 14 of the Periodic Table
    • C07F7/02Silicon compounds
    • C07F7/08Compounds having one or more C—Si linkages
    • C07F7/12Organo silicon halides
    • C07F7/14Preparation thereof from optionally substituted halogenated silanes and hydrocarbons hydrosilylation reactions

Definitions

  • the present invention relates to a process for the preparation of haloalkyldialkylhalosilane.
  • 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:
  • 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.
  • DC degree of conversion
  • S selectivity
  • 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 Na 2 SO 4 ). The ketone is combined with the platinum in order to improve the selectivity of the reaction.
  • 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.
  • a 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) 3 X 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.).
  • the catalyst corresponds to the formula (I): [Ir(R 4 ) x (R 5 )] y (IV)
  • the ligands R 4 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-(R 2 R 3 )Si—H) and/or to increase the selectivity S for a given and fixed DC.
  • 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.
  • 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.
  • 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
  • this offers possibilities of easy recovery of the catalyst and thus of recycling the latter.
  • the auxiliary 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.
  • 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 .
  • 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.
  • the auxiliary is selected from the group consisting in particular of: cyclohexanone, 2-cyclohexen-1-one, isophorone, 2-benylidenecyplohexanone, 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-(vin
  • 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).
  • 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 .
  • the components of the mixture (vi), UHC/(i) and/or (ii) and/or (iii), are present in the reaction medium when the reaction begins.
  • the process according to the invention can be employed either continuously, semicontinuously or batchwise.
  • the product of formula (I) is 3-chloropropyldimethylchlorosilane
  • the product of formula (II) is dimethylhydrochlorosilane
  • the product of formula (III) is allyl chloride.
  • the invention relates to a catalytic system for the preparation of a haloalkyldialkylhalosilane of formula (I): Hal-(R 2 R 3 )Si—(CH 2 ) s -Hal by hydrosilylation reaction of a reaction medium comprising:
  • 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.
  • hydrosilylation auxiliaries The effect of the hydrosilylation auxiliaries is compared with a control reaction, where only di- ⁇ -chlorobis( ⁇ -1,5-cyclooctadiene)diiridium was used.
  • a control reaction where only di- ⁇ -chlorobis( ⁇ -1,5-cyclooctadiene)diiridium was used.
  • 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
  • the reaction medium is analyzed by gas chromatography calibrated with n-tetradecane.
  • 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.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Silicon Compounds (AREA)
US10/561,223 2003-06-17 2004-06-16 Method of preparing halogenoalkyldialkyl chlorosilane Abandoned US20070185344A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR0350222 2003-06-17
FR0350222A FR2856402B1 (fr) 2003-06-17 2003-06-17 Procede de preparation d'halogenoalkylchlorosilane
PCT/FR2004/001487 WO2004113354A2 (fr) 2003-06-17 2004-06-16 Procede de preparation d'halogenoalkyldialkyl-chlorosilane

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/FR2004/001487 A-371-Of-International WO2004113354A2 (fr) 2003-06-17 2004-06-16 Procede de preparation d'halogenoalkyldialkyl-chlorosilane

Related Child Applications (1)

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US12/173,968 Continuation US7884225B2 (en) 2003-06-17 2008-07-16 Process for the preparation of halogenoalkyldialkyl chlorosilane

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US20070185344A1 true US20070185344A1 (en) 2007-08-09

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US10/561,223 Abandoned US20070185344A1 (en) 2003-06-17 2004-06-16 Method of preparing halogenoalkyldialkyl chlorosilane
US12/173,968 Expired - Fee Related US7884225B2 (en) 2003-06-17 2008-07-16 Process for the preparation of halogenoalkyldialkyl chlorosilane

Family Applications After (1)

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US12/173,968 Expired - Fee Related US7884225B2 (en) 2003-06-17 2008-07-16 Process for the preparation of halogenoalkyldialkyl chlorosilane

Country Status (9)

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US (2) US20070185344A1 (de)
EP (1) EP1633761B1 (de)
JP (1) JP4510011B2 (de)
CN (1) CN100448882C (de)
AT (1) ATE394406T1 (de)
DE (1) DE602004013583D1 (de)
ES (1) ES2305834T3 (de)
FR (1) FR2856402B1 (de)
WO (1) WO2004113354A2 (de)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102007011158A1 (de) * 2007-03-07 2008-09-11 Wacker Chemie Ag Iridiumkatalysiertes Herstellungsverfahren für siliciumorganische Verbindungen
JP5455937B2 (ja) * 2008-03-06 2014-03-26 ダウ・コーニング・コーポレイション ハロアルキルアルコキシシランおよびハロアルキルハロシランの製造方法
CN108291030B (zh) 2015-12-07 2021-01-05 美国陶氏有机硅公司 使用铱络合物催化剂氢化硅烷化羧酸烷基酯和氢封端的有机硅氧烷寡聚物的方法和组合物
WO2017154846A1 (ja) * 2016-03-09 2017-09-14 国立研究開発法人産業技術総合研究所 イリジウム錯体等を用いたアリル化合物のヒドロシリル化によるシリル化合物の製造方法
JP7252142B2 (ja) 2017-06-26 2023-04-04 ダウ シリコーンズ コーポレーション 脂肪族不飽和アルコキシシラン及び水素末端オルガノシロキサンオリゴマーをヒドロシリル化して、イリジウム触媒を使用してポリオルガノシロキサンを官能化するのに有用なアルコキシシリル末端ポリマーを調製する方法
US10723843B2 (en) * 2017-07-20 2020-07-28 Dow Silicones Corporation Process for preparing platinum organosiloxane complexes using an enone additive
WO2019040383A1 (en) 2017-08-22 2019-02-28 Dow Silicones Corporation DOUBLE CURING ADHESIVE COMPOSITION AND METHODS OF PREPARATION AND USE
CN110577485B (zh) * 2018-06-11 2022-11-04 武汉大学 一种降樟脑衍生的[2,2,1]-桥环烯酮类化合物及其合成方法和应用
JP2021178786A (ja) * 2020-05-13 2021-11-18 信越化学工業株式会社 ジメチルクロロシラン化合物の製造方法

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5424470A (en) * 1994-10-27 1995-06-13 Dow Corning Corporation Unsaturated ketones as accelerators for hydrosilation
US5449802A (en) * 1994-12-27 1995-09-12 Dow Corning Corporation Acetylenic alcohols and ethers as accelerators for hydrosilation
US5481016A (en) * 1995-04-17 1996-01-02 Dow Corning Corporation Alcohols and silated alcohols as accelerators for hydrosilation
US5486637A (en) * 1995-04-17 1996-01-23 Dow Corning Corporation Unsaturated alcohols as accelerators for hydrosilation
US5493045A (en) * 1995-06-26 1996-02-20 Dow Corning Corporation Ene-yne unsaturated compounds as accelerators for hydrosilation
US5616763A (en) * 1996-01-29 1997-04-01 Dow Corning Corporation Aldehydes as accelerators for hydrosilation
US5756796A (en) * 1997-05-19 1998-05-26 Dow Corning Corporation Method for preparation of alkenylsilanes
US5756795A (en) * 1996-12-30 1998-05-26 Dow Corning Corporation Unsaturated accelerators for hydrosilation
US20010053861A1 (en) * 2000-05-15 2001-12-20 Yoichi Tonomura Preparation of halopropyldimethylchlorosilanes
US20020052520A1 (en) * 2000-10-26 2002-05-02 Andreas Bauer Preparation of organosilanes
US6500977B1 (en) * 2001-11-27 2002-12-31 Dow Corning Corporation Process for producing organosilanes
US20060167296A1 (en) * 2002-08-09 2006-07-27 Nathalie Guennouni Method of preparing halogenoalkyldialkyl chlorosilane

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2938731B2 (ja) * 1993-10-28 1999-08-25 信越化学工業株式会社 ハロプロピルジメチルクロロシランの製造方法およびその合成用の触媒
FR2833265B1 (fr) * 2001-12-06 2006-02-10 Rhodia Chimie Sa Procede d'obtention de monoorganoxysilane polysulfures
DE10232663C1 (de) * 2002-07-18 2003-10-16 Wacker Chemie Gmbh Kontinuierliche Herstellung von Organosilanen

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5424470A (en) * 1994-10-27 1995-06-13 Dow Corning Corporation Unsaturated ketones as accelerators for hydrosilation
US5449802A (en) * 1994-12-27 1995-09-12 Dow Corning Corporation Acetylenic alcohols and ethers as accelerators for hydrosilation
US5481016A (en) * 1995-04-17 1996-01-02 Dow Corning Corporation Alcohols and silated alcohols as accelerators for hydrosilation
US5486637A (en) * 1995-04-17 1996-01-23 Dow Corning Corporation Unsaturated alcohols as accelerators for hydrosilation
US5493045A (en) * 1995-06-26 1996-02-20 Dow Corning Corporation Ene-yne unsaturated compounds as accelerators for hydrosilation
US5616763A (en) * 1996-01-29 1997-04-01 Dow Corning Corporation Aldehydes as accelerators for hydrosilation
US5756795A (en) * 1996-12-30 1998-05-26 Dow Corning Corporation Unsaturated accelerators for hydrosilation
US5756796A (en) * 1997-05-19 1998-05-26 Dow Corning Corporation Method for preparation of alkenylsilanes
US20010053861A1 (en) * 2000-05-15 2001-12-20 Yoichi Tonomura Preparation of halopropyldimethylchlorosilanes
US20020052520A1 (en) * 2000-10-26 2002-05-02 Andreas Bauer Preparation of organosilanes
US6500977B1 (en) * 2001-11-27 2002-12-31 Dow Corning Corporation Process for producing organosilanes
US20060167296A1 (en) * 2002-08-09 2006-07-27 Nathalie Guennouni Method of preparing halogenoalkyldialkyl chlorosilane
US7307180B2 (en) * 2002-08-09 2007-12-11 Rhodia Chimie Method of preparing halogenoalkyldialkyl chlorosilane

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Publication number Publication date
US20080275264A1 (en) 2008-11-06
US7884225B2 (en) 2011-02-08
DE602004013583D1 (de) 2008-06-19
ES2305834T3 (es) 2008-11-01
EP1633761A2 (de) 2006-03-15
ATE394406T1 (de) 2008-05-15
JP2006527742A (ja) 2006-12-07
CN1820013A (zh) 2006-08-16
FR2856402B1 (fr) 2005-08-26
CN100448882C (zh) 2009-01-07
EP1633761B1 (de) 2008-05-07
WO2004113354A2 (fr) 2004-12-29
WO2004113354A3 (fr) 2005-03-17
FR2856402A1 (fr) 2004-12-24
JP4510011B2 (ja) 2010-07-21

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