EP1487901A1 - Verfahren zur herstellung von funktionalisierten polyorganosiloxanharzen durch redistribution in anwesenheit mindestens eines derivates einer trifluormethansulfonsäure - Google Patents
Verfahren zur herstellung von funktionalisierten polyorganosiloxanharzen durch redistribution in anwesenheit mindestens eines derivates einer trifluormethansulfonsäureInfo
- Publication number
- EP1487901A1 EP1487901A1 EP03725309A EP03725309A EP1487901A1 EP 1487901 A1 EP1487901 A1 EP 1487901A1 EP 03725309 A EP03725309 A EP 03725309A EP 03725309 A EP03725309 A EP 03725309A EP 1487901 A1 EP1487901 A1 EP 1487901A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- catalyst
- redistribution
- pos
- units
- resin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 229920005989 resin Polymers 0.000 title claims abstract description 81
- 239000011347 resin Substances 0.000 title claims abstract description 81
- 238000000034 method Methods 0.000 title claims abstract description 40
- ITMCEJHCFYSIIV-UHFFFAOYSA-N triflic acid Chemical class OS(=O)(=O)C(F)(F)F ITMCEJHCFYSIIV-UHFFFAOYSA-N 0.000 title description 10
- 239000003054 catalyst Substances 0.000 claims abstract description 30
- 230000003197 catalytic effect Effects 0.000 claims abstract description 11
- 125000000524 functional group Chemical group 0.000 claims abstract description 7
- 230000008569 process Effects 0.000 claims description 24
- 238000007306 functionalization reaction Methods 0.000 claims description 22
- 238000006243 chemical reaction Methods 0.000 claims description 20
- 239000003377 acid catalyst Substances 0.000 claims description 18
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 12
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000008096 xylene Substances 0.000 claims description 10
- 125000000217 alkyl group Chemical group 0.000 claims description 9
- 125000003118 aryl group Chemical group 0.000 claims description 9
- 239000012429 reaction media Substances 0.000 claims description 9
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 8
- 238000002360 preparation method Methods 0.000 claims description 8
- 125000003342 alkenyl group Chemical group 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 5
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 5
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 5
- 239000001257 hydrogen Substances 0.000 claims description 5
- 239000003960 organic solvent Substances 0.000 claims description 5
- 229920000570 polyether Polymers 0.000 claims description 5
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims description 5
- 239000004593 Epoxy Substances 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- 229910004283 SiO 4 Inorganic materials 0.000 claims description 4
- 125000000304 alkynyl group Chemical group 0.000 claims description 4
- 239000006229 carbon black Substances 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 150000004820 halides Chemical class 0.000 claims description 4
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 4
- 150000003573 thiols Chemical class 0.000 claims description 4
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims description 3
- 230000008030 elimination Effects 0.000 claims description 3
- 238000003379 elimination reaction Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 150000003463 sulfur Chemical class 0.000 claims description 3
- 150000001408 amides Chemical class 0.000 claims description 2
- 150000001412 amines Chemical class 0.000 claims description 2
- 238000009835 boiling Methods 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 230000003472 neutralizing effect Effects 0.000 claims description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims 1
- 239000000969 carrier Substances 0.000 claims 1
- 229910052717 sulfur Inorganic materials 0.000 claims 1
- 239000011593 sulfur Substances 0.000 claims 1
- KAKQVSNHTBLJCH-UHFFFAOYSA-N trifluoromethanesulfonimidic acid Chemical group NS(=O)(=O)C(F)(F)F KAKQVSNHTBLJCH-UHFFFAOYSA-N 0.000 claims 1
- 125000000008 (C1-C10) alkyl group Chemical group 0.000 abstract 1
- 229910020485 SiO4/2 Inorganic materials 0.000 abstract 1
- 238000010348 incorporation Methods 0.000 description 8
- 229920002050 silicone resin Polymers 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 210000002741 palatine tonsil Anatomy 0.000 description 6
- 238000006386 neutralization reaction Methods 0.000 description 5
- 125000004469 siloxy group Chemical group [SiH3]O* 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 3
- 229920002554 vinyl polymer Polymers 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- -1 alkyl silicate Chemical compound 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000009849 deactivation Effects 0.000 description 2
- 231100000584 environmental toxicity Toxicity 0.000 description 2
- 238000007210 heterogeneous catalysis Methods 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- ZXMGHDIOOHOAAE-UHFFFAOYSA-N 1,1,1-trifluoro-n-(trifluoromethylsulfonyl)methanesulfonamide Chemical group FC(F)(F)S(=O)(=O)NS(=O)(=O)C(F)(F)F ZXMGHDIOOHOAAE-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- UXJHQBVRZUANLK-UHFFFAOYSA-N azanylidyne(dichloro)-$l^{5}-phosphane Chemical compound ClP(Cl)#N UXJHQBVRZUANLK-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 238000007172 homogeneous catalysis Methods 0.000 description 1
- 125000001183 hydrocarbyl group Chemical group 0.000 description 1
- 238000006459 hydrosilylation reaction Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- GKTNLYAAZKKMTQ-UHFFFAOYSA-N n-[bis(dimethylamino)phosphinimyl]-n-methylmethanamine Chemical compound CN(C)P(=N)(N(C)C)N(C)C GKTNLYAAZKKMTQ-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 125000005375 organosiloxane group Chemical group 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000000135 prohibitive effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- UHUUYVZLXJHWDV-UHFFFAOYSA-N trimethyl(methylsilyloxy)silane Chemical compound C[SiH2]O[Si](C)(C)C UHUUYVZLXJHWDV-UHFFFAOYSA-N 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/06—Preparatory processes
- C08G77/08—Preparatory processes characterised by the catalysts used
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/06—Preparatory processes
- C08G77/10—Equilibration processes
Definitions
- POS resins silicone or polyorganosiloxane resins, hereinafter designated by POS resins.
- These functional MQ silicone resins can be liquid or solid at room temperature. They have been known for a very long time and are currently used in numerous applications such as, for example, in electrical insulating varnishes, heat-resistant coatings, encapsulation materials for semiconductor components, etc.
- the functional MQ POS resins (MM'Q) which are the subject of the present invention may also comprise siloxy units D and / or T, or even functionalized siloxy units D 'and / or T'.
- the main access routes to functional MQ resins are currently the condensation / hydrolysis processes from sodium silicate or alkyl silicate. (US-B-2,676,182, US-B-2,814,601, US-B-2,857,356, US-B-4,707,531). These techniques are not without drawbacks, in particular in terms of ease of implementation, cost and production of ecotoxic and / or dangerous effluents. However, there is an alternative, a priori attractive, to these condensation / hydrolysis techniques, namely the redistribution of POS oils in a POS resin comprising MQ motifs.
- Patent US-B-4,774,310 describes the preparation of functionalized Si-H resins by redistribution of tetramethyledisiloxane (M ′ 2 ) in an MQ resin in solution in an organic solvent, in the presence of triflic acid or perfluoroalkanesulfonic acid (TFOH) .
- the reaction medium is heated to a temperature between 50 and 100 ° C., then the triflic acid catalyst is neutralized with NaHCO 3 .
- the MM'Q resins thus obtained can react with organic or organosiloxane substances carrying an olefinic unsaturation (column 2 line 66 to column 3 line 3).
- This patent makes also a vague and general allusion to the supported acid catalysts (column 2 line 18).
- US Pat. No. 5,494,979 discloses the preparation of MQ resins functionalized with acrylate radicals, by redistribution of polydiorganosiloxane oils carrying D units and D acrylic units : MD acr late x D y M. This redistribution is carried out using a xylene solution of commercial MQ resin, using triflic acid as preferred acid catalyst.
- the POS MD acrylate x D y M used is as described in Example 2 of German patent n ° 3810140.
- This preparation of acrylate functionalized MQ resins also includes stages of neutralization, for example using sodium carbonate, then elimination of the solid residues by filtration.
- one of the essential objectives of the present invention is to provide an improved process for functionalizing silicone resins comprising M and Q siloxyl units, by redistribution using POSs carrying functional units or functionalization units ; this improved process should provide improvements in terms of ease of implementation, of significant increase in the functionalization rate of the redistributed resin as well as in the conversion rate of functional POS reagents, while keeping the cost of the process at the most low possible.
- Another essential objective of the invention is to provide a new acidic catalytic system useful or for the functionalization of silicone resins comprising M and Q units, by redistribution, by using a redistribution reagent constituted by a POS carrying functional or functionalization units, said catalytic system being endowed with properties such that it allows the improvement of the redistribution kinetics as well as of the yield and the transformation rate of the reaction, without inducing any complications on the methodological level or prohibitive increase in cost.
- Another essential objective of the invention is to significantly improve the catalysis, homogeneous or heterogeneous, of functionalization reactions of resins comprising M and Q siloxyl units by redistribution, by means of POS carrying functional or functionalization units.
- the improvement sought must be reflected in terms of the control, reliability and productivity of the corresponding industrial processes.
- Another objective targeted through the improvement of the catalytic system is to improve the quality of the functionalized MQ resins obtained, while optimizing safety and minimizing the ecotoxic impact of the industrial processes considered.
- Another essential objective of the invention is to provide a process for the functionalization of MQ silicone resins by redistribution, in which the efficiency of incorporation of the functionalization POS (M ′ 2 ) is significantly increased compared to those obtained by known methods.
- Another essential objective of the invention is to provide a process for functionalizing MQ silicone resins by redistribution using POS for functionalization which process offers the possibility of controlling the rate of functionalities introduced as well as the location of these functions on the resin.
- Another essential objective of the invention is to propose a process for functionalizing MQ type silicone resins by redistribution, this process being capable of being applied to a wide variety of chemical functions, so as to be able to produce a wide variety of resins Functional MQs suitable for multiple applications, from a raw material constituted by a resin core at the periphery of which are chosen chemical functions.
- Ci-Cio or a C 8 -C 12 aryl the radicals Y being identical or different from each other and representing a functional group Y, by redistribution of POS resins using POSf carrying functional units M 'and / or D' and / or T ', as defined above, in the presence of an acid catalyst, said process being characterized in that at least one catalyst of the following formula (I) is used:
- ⁇ m is an integer greater than or equal to 1;
- the acid catalyst must be liquid under the conditions of use.
- acids whose acidity measured in the gas phase is greater than that of sulfuric acid, therefore in terms of ⁇ G ⁇ 302 Kcal / mole.
- (CF 3 SO 2 ) 2 NH ⁇ G 292 Kcal / mole
- (C 4 F 9 SO 2 ) 2 NH ⁇ G 284 Kcal / mole.
- one of the essential constituent means of the invention relates to the catalytic system formed by three particular classes ( ⁇ ) (i), I (ii) and (I) (iii) of triflic acid derivatives.
- the use of this catalytic system makes it possible to obtain incorporation yields in POS carrying functional units (for example M ′) greater than 50%, preferably 60% and more preferably still 70%, to be compared with yields obtained. in the processes according to the prior art capping at 30%.
- the catalytic system according to the invention is also remarkable in terms of kinetics.
- redistribution can be easily stopped by neutralization of the acid catalyst using a base (for example NaHCO 3 , Na 2 CO 3 , CaCO 3 ...) and / or by deactivation by heat.
- a base for example NaHCO 3 , Na 2 CO 3 , CaCO 3 .
- Neutralization is all the easier since the residual acidity is here clearly lower compared to that obtained after traditional redistribution catalysis.
- neutralization has the advantage that the final reaction medium is not aggressive with respect to the functionalized MQ silicone resins. The stability of the latter at temperature and storage is all the better.
- This process also makes it possible to control the functionalization rate of the MQ resin, or even the location of its functions on the resin.
- a core of MQ resin which constitutes a convenience
- a mixture of catalysts comprising at least one catalyst of formula (I) as defined above and at least catalyst of the following formula (F):
- Y is advantageously chosen from the group comprising:
- the starting MQ resins can be either non-functionalized, or already functionalized.
- MQ resins are commercial products, for example of formula (M x Q y ) z with x between 0.5 and 1 and including between 0 and 1
- the MQ resins already functionalized are in particular those obtained by the process in accordance with the present invention from non-functionalized starting MQ resins or by the process of synthesis from sodium silicate described in US Pat. No. 2,676,182.
- the starting MQ resin is in the form of a solution in an organic solvent such as, for example, xylene or toluene.
- the POSf of formulas (IN.l), (IN.2), (LV.3) correspond respectively to disiloxanes, linear polyorganosiloxanes and cyclic oligoorganosiloxanes.
- POSf are for example M 2 , M 2 V V i 1 , MD X M, MD x D ' y M, M'D x D' y M ', MD x DV V i I y M, M Vi D x D Vi y M vi , M'D X M ', M Vi D x M vi , D x . Vi D y .
- the acid catalyst of formula (I) (i) or (ii) or (iii) that the fluorinated chain C ra F 2n ⁇ + 1 can be lengthened so as to increase the acidity of the catalyst, and subsequently its efficiency.
- the chosen catalyst has a melting point below the reaction temperature so that the catalyst is in the liquid state during the reaction.
- the concentration of acid catalyst (I) is advantageously between 1 ppm and 2% relative to the starting resin.
- the mass ratio catalyst (P / inert support (preferably carbon black) is preferably between 0.1 and 10, preferably is of the order of 1.
- the catalysis can be homogeneous or heterogeneous.
- the catalyst being in this case dissolved in the reaction medium.
- the catalyst is, at least in part, absorbed on an inert support which may for example be carbon black or silica.
- the method according to the invention can be defined by other methodological characteristics, and in particular in that it comprises the following essential steps:
- the organic solvent preferably xylene and toluene
- MQ starting POS resin solution
- the functionalization process by redistribution according to the invention makes it possible in particular to graft Si-H and / or Si-alkenyl (preferably vinyl) units, onto MQ resins. Since these H or alkenyl functions are reactive functions, among others, it is possible, in accordance with the invention, to carry out a second functionalization according to a hydrosilylation mechanism, so as to fix covalently on the MQ resin already functionalized, a second functional segment.
- reaction atmosphere be free of humidity.
- neutral gas for example argon or nitrogen.
- the reaction pressure is advantageously normal and the reaction temperature can range from room temperature (25 ° C for example) to a temperature of 150 ° C or more.
- the redistribution is stopped by deactivating the catalyst.
- an acid catalyst in this case triflic acid or its derivatives
- deactivation can take place using a basic neutralizer, such as for example sodium carbonate Na 2 CO 3 or sodium bicarbonate NaHCO 3 .
- Neutralization is all the more necessary when it is a homogeneous catalysis since in such a case, unlike heterogeneous catalysis, the catalyst is not removed at the end of the reaction.
- the redistributed and functionalized resin obtained is subjected to at least one other redistribution / functionalization, using POSs carrying functional patterns.
- the invention also relates to a catalytic system useful for the preparation of functionalized polyorganosiloxane (POS) resins and comprising units M: (R 3 SiO ⁇ / 2 ), Q: (SiO 42 ) and M ': (Y a R 3.
- ⁇ m is an integer greater than or equal to 1;
- ⁇ n is an integer equal to 1 or 2 and A represents OH, NH2 or NH with:
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Silicon Polymers (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0203771 | 2002-03-26 | ||
| FR0203771A FR2837826B1 (fr) | 2002-03-26 | 2002-03-26 | Procede de preparation de resines polyorganosiloxane fonctionnalisees par redistribution en presence d'au moins un derive d'acide triflique |
| PCT/FR2003/000889 WO2003080711A1 (fr) | 2002-03-26 | 2003-03-20 | Procede de preparation de resines polyorganosiloxane fonctionnalisees par redistribution en presence d'au moins un derive d'acide triflique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP1487901A1 true EP1487901A1 (de) | 2004-12-22 |
Family
ID=27839205
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP03725309A Withdrawn EP1487901A1 (de) | 2002-03-26 | 2003-03-20 | Verfahren zur herstellung von funktionalisierten polyorganosiloxanharzen durch redistribution in anwesenheit mindestens eines derivates einer trifluormethansulfonsäure |
Country Status (6)
| Country | Link |
|---|---|
| US (2) | US7402647B2 (de) |
| EP (1) | EP1487901A1 (de) |
| CN (1) | CN100339418C (de) |
| AU (1) | AU2003227851A1 (de) |
| FR (1) | FR2837826B1 (de) |
| WO (1) | WO2003080711A1 (de) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2837826B1 (fr) * | 2002-03-26 | 2005-10-28 | Rhodia Chimie Sa | Procede de preparation de resines polyorganosiloxane fonctionnalisees par redistribution en presence d'au moins un derive d'acide triflique |
| FR2837825B1 (fr) * | 2002-03-26 | 2005-02-25 | Rhodia Chimie Sa | Procede de preparation de resines polyorganosiloxane fonctionnalisees par redistribution en presence d'acide triflique et/ou d'au moins l'un de ses derives et de charge inerte non basique |
| JP7389061B2 (ja) | 2018-08-24 | 2023-11-29 | ダウ シリコーンズ コーポレーション | ヒドロキシル末端ポリジオルガノシロキサンの縮合重合のため方法 |
| CN112469769B (zh) | 2018-08-24 | 2022-07-08 | 美国陶氏有机硅公司 | 用于羟基封端的聚二有机硅氧烷的缩合聚合的方法 |
Family Cites Families (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2676182A (en) | 1950-09-13 | 1954-04-20 | Dow Corning | Copolymeric siloxanes and methods of preparing them |
| US2814601A (en) | 1954-04-29 | 1957-11-26 | Dow Corning | Organopolysiloxane adhesive and pressure-sensitive adhesive tape containing same |
| DE1017883B (de) | 1954-07-08 | 1957-10-17 | Fellows Gear Shaper Co | Schalt- und Vorschubeinrichtung fuer Zahnradherstellungsmaschinen |
| CA1091380A (en) * | 1975-03-07 | 1980-12-09 | Mark W. Siefken | Polymerization of silanes |
| US4020043A (en) | 1975-03-07 | 1977-04-26 | Minnesota Mining And Manufacturing Company | Vulcanizable alkoxysilyl capped polymer composition |
| US4222952A (en) * | 1979-06-25 | 1980-09-16 | Union Carbide Corporation | Siloxane bond rearrangement effected by solid perfluorinated polymers containing pendant sulfonic acid groups |
| US4448927A (en) * | 1983-03-14 | 1984-05-15 | Dow Corning Corporation | Method of polymerizing oligomers of polydiorganosiloxane in the presence of filler |
| JPS61195129A (ja) | 1985-02-22 | 1986-08-29 | Toray Silicone Co Ltd | 有機けい素重合体の製造方法 |
| GB8615862D0 (en) | 1986-06-28 | 1986-08-06 | Dow Corning Ltd | Making siloxane resins |
| DE3810140C1 (de) | 1988-03-25 | 1989-10-05 | Th. Goldschmidt Ag, 4300 Essen, De | |
| US4929691A (en) * | 1989-03-28 | 1990-05-29 | Dow Corning Corporation | Liquid silicone resin compositions |
| DE4116014A1 (de) * | 1991-05-16 | 1992-11-26 | Wacker Chemie Gmbh | Verfahren zur herstellung von organo(poly)siloxanen |
| US5494979A (en) | 1993-03-26 | 1996-02-27 | Th. Goldschmidt Ag | Abhesive coating composition with an additive, which affects the degree of abhesiveness |
| JPH07228701A (ja) * | 1994-02-18 | 1995-08-29 | Toray Dow Corning Silicone Co Ltd | ケイ素原子結合水素原子含有シリコーン樹脂の製造方法 |
| EP0797612B1 (de) * | 1994-12-12 | 1999-01-13 | Hüls Silicone Gesellschaft mit beschränkter Haftung | Verfahren zur herstellung von im wesentlichen cyclenfreien polyorgano-siloxanen und organofunktionellen siloxanen |
| US5510430A (en) | 1995-03-31 | 1996-04-23 | General Electric Company | Method of functionalizing organosiloxane condensation products |
| FR2802540B1 (fr) * | 1999-12-17 | 2002-05-24 | Rhodia Chimie Sa | Procede de preparation de polyorganosiloxanes par polymerisation catalysee par un systeme catalytique a base d'acide triflique ou de derives de l'acide triflique |
| JP4965033B2 (ja) * | 2001-06-29 | 2012-07-04 | 東レ・ダウコーニング株式会社 | 液状アルコキシシリル官能性シリコーン樹脂、その製造方法および硬化性シリコーン樹脂組成物 |
| FR2837826B1 (fr) * | 2002-03-26 | 2005-10-28 | Rhodia Chimie Sa | Procede de preparation de resines polyorganosiloxane fonctionnalisees par redistribution en presence d'au moins un derive d'acide triflique |
| FR2837825B1 (fr) * | 2002-03-26 | 2005-02-25 | Rhodia Chimie Sa | Procede de preparation de resines polyorganosiloxane fonctionnalisees par redistribution en presence d'acide triflique et/ou d'au moins l'un de ses derives et de charge inerte non basique |
-
2002
- 2002-03-26 FR FR0203771A patent/FR2837826B1/fr not_active Expired - Fee Related
-
2003
- 2003-03-20 US US10/509,071 patent/US7402647B2/en not_active Expired - Fee Related
- 2003-03-20 EP EP03725309A patent/EP1487901A1/de not_active Withdrawn
- 2003-03-20 CN CNB038097958A patent/CN100339418C/zh not_active Expired - Fee Related
- 2003-03-20 AU AU2003227851A patent/AU2003227851A1/en not_active Abandoned
- 2003-03-20 WO PCT/FR2003/000889 patent/WO2003080711A1/fr not_active Ceased
-
2008
- 2008-06-19 US US12/142,384 patent/US20080255322A1/en not_active Abandoned
Non-Patent Citations (1)
| Title |
|---|
| See references of WO03080711A1 * |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2003227851A1 (en) | 2003-10-08 |
| CN1649939A (zh) | 2005-08-03 |
| FR2837826A1 (fr) | 2003-10-03 |
| US7402647B2 (en) | 2008-07-22 |
| US20050239987A1 (en) | 2005-10-27 |
| WO2003080711A1 (fr) | 2003-10-02 |
| US20080255322A1 (en) | 2008-10-16 |
| FR2837826B1 (fr) | 2005-10-28 |
| CN100339418C (zh) | 2007-09-26 |
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