AU642241B2 - Process for the preparation of diorganopolysiloxanes having alkoxy end groups - Google Patents
Process for the preparation of diorganopolysiloxanes having alkoxy end groups Download PDFInfo
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- AU642241B2 AU642241B2 AU76081/91A AU7608191A AU642241B2 AU 642241 B2 AU642241 B2 AU 642241B2 AU 76081/91 A AU76081/91 A AU 76081/91A AU 7608191 A AU7608191 A AU 7608191A AU 642241 B2 AU642241 B2 AU 642241B2
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- 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
- C08G77/20—Polysiloxanes containing silicon bound to unsaturated aliphatic groups
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- 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
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- 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
- C08G77/14—Polysiloxanes containing silicon bound to oxygen-containing groups
- C08G77/18—Polysiloxanes containing silicon bound to oxygen-containing groups to alkoxy or aryloxy groups
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Abstract
Process for the preparation of diorganopolysiloxanes with alkoxy end groups in the presence of a catalyst chosen from sodium hydroxide and potassium hydroxide. Use of these diorganopolysiloxanes for the preparation of single-component polysiloxane compositions which are stable in storage in the absence of moisture and which crosslink to elastomer in the presence of moisture.
Description
COMMONWEALTH OF AUSTRA 2 2 4 FORM PATENTS ACT 1952 COMPLETE S P E C I F I CAT I ON FOR OFFICE USE: Class Int.Class Application Number: Lodged: ;j omplete Specification Lodged: Accepted: Published: .,Priority: Related Art: Name of Applicant: RHONE-POULENC CHIMIE "*Address of Applicant: 25, Quai Paul Doumer, 92408, Courbevoie, 'II* Cedex, France ,,.,Actual Inventor: Roger Cocco 0.
Address for Service: SHELSTON WATERS, 55 Clarence Street, Sydney Complete Specification for the Invention entitled: "PROCESS FOR THE PREPARATION OF DIORGANOPOLYSILOXANES HAVING ALKOXY END GROUPS" The following statement is a full description of this invention, including the best method of performing it known to us:- 1 PROCESS FOR THE PREPARATION OF DIORGANOPOLYSILOXANES HAVING ALKOXY END GROUPS The present invention relates to a process for the preparation of diorganopolysiloxanes having alkoxy end groups, termed PF (polymers containing functional groups) below, and to the use, of at least some of these, in particular as one of the essential constituents in single-component organopolysiloxane elastomer compositions which are stable on storage and .10 in the absence of moisture and which crosslink under *u atmospheric humidity at ambient temperature, which are termed compositions for cold-vulcanisable elastomer (CVE) compositions below.
It is known to prepare these PFs by reacting 0e S 15 a dialkoxysilane, a trialkoxysilane or a l tetraalkoxysilane with a diorganopolysiloxane oil comprising a hydroxyl group linked to the silicon atom at each end of its chain, but it is necessary to use a catalyst. Numerous patents have been filed claiming the use of catalysts specifically for this reaction for the introduction of functional groups.
US Patent 3,542,901 proposes an amine as the catalyst. This catalyst is effective but the reaction is fairly slow (for example 15 to 30 min at 60 0 C for fairly reactive alkoxysilanes such as Si(OCH) 4 or Vi Si
(OCH
3 3 With alkoxysilanes of low reactivity, it is necessary to make use of very much longer times, or to obtain only incomplete reactions. Now, it is known that the presence of residual silanols is generally adverse for the stability (see US 4,489,191-A and also French Patent Application Nos. 2,597,876 and 2,597,877).
Moreover, it is difficult to remove the amine completely, which may have an adverse effect on the stability of the composition on storage; it may also cause the appearance of yellowish discolorations, i either during storage of the mastic or on the crosslinked product.
10 It is for this reason that numerous other catalytic systems have been proposed. The following may be mentioned: potassium acetate US 3,504,051 diverse inorganic oxides FR 1,495,011 15 organic titanium derivatives US-A- 'S"r 4,111,890 titanate plus amine US 3,647,846 alkoxyaluminium chelate GB-A-2,144,758 N,N'-disubstituted hydroxylamine FR-A- 2,508,467 carboxylic acid plus amine FR 2,604,713 carbamates EP 0,210,402 organic compounds containing an oxime group FR 2,597,875.
Some of these catalysts are slightly more active than the amines, but it is nevertheless necessary to heat to 60-70°C in order to obtain times of 5 to 10 minutes for introduction of the functional groups. Moreover, these catalysts, or their residues, may have an adverse influence on the stability on storage; in particular in the presence of setting catalysts, as well as on the properties of the crosslinked products because it is difficult or impossible to remove them completely after reaction.
Patent Application FR 88.15312, filed on
S
S4 November 1988 in the name of the Applicant, also describes a process for the preparation of 10 diorganopolysilcxanes having alkoxy end groups using lithium oxide as the catalyst for the introduction of functional groups.
Another process for making oils containing functional groups (PF) consists in using mixed silanes I 15 having, in addition to the alkoxy groups, a watersoluble group such as an amido, amino, carbamate or oxime group, etc., if appropriate in the presence of a Sknown catalyst for the introduction of functional SS S groups and a polyalkoxysilane.
Processes of this type are described, in particular, in Patents US-A-3,697,568, US-A-3,896,079 and EP-A-69,256.
These processes are effective but necessitate the use of costly mixed silanes. Moreover, the organic products resulting from the water-soluble groups after reaction may have an adverse effect on the CVE composition (see pages 4 and 5 of French Patent FR-A- 2,543,562 on this subject).
The aim of the present invention is to propose catalysts for the introduction of functional groups which are very effective for obtaining straightchain diorganopolysiloxanes comprising at least one alkoxy group linked to a silicon atom at each end of their chain (polymers termed PF below or oils 6 containing functional groups).
a Another aim of the present invention is to propose catalysts for introducing functional groups 10 which enable PF to be obtained by carrying out the -reaction at ambient temperature, in particular using
CH
3 Si(OCH 3 3 CHz=CH-Si(OCH 3 3 or MeViSi(OCH 3 z as the agent for introducing functional groups (Me representing the methyl group -CH3 and Vi representing 15 the vinyl group -CH=CH 2 Another aim of the present invention is to propose catalysts for introducing functional groups which enable PF to be obtained, at ambient temperature, in a time of less than 15 minutes, advantageously of
S**
less than 10 minutes and preferably of 5 minutes or less, in particular using one of the abovementioned crosslinking agents as the crosslinking agent.
Another aim of the present invention is the use of inexpensive catalysts which are available commercially (in the chemical sector) and may be used, even in a large quantity, during the reaction for the introduction of functional groups.
Another aim of the present invention is to propose catalysts for introducing functional groups which may easily be neutralised at the end of the reaction for the introduction of functional groups, in particular by a silyl phosphate.
Another aim of the present invention is to propose catalysts for introducing functional groups which may be neutralised at the end of the reaction for the introduction of functional groups without there being any need for urgency in carrying out this 10 neutralisation, that is to say it is possible to start the neutralisation, for example, one hour after the reaction for the introduction of functional groups has been completed.
Another aim of the present invention is a 15 catalyst for introducing functional groups which, after its neutralisation and, if appropriate, the devolatilisation of the reaction mass at the end of the reaction for the introduction of functional groups, allows the preparation, using the PF obtained (containing the reaction product resulting from neutralisation of the catalyst), of compositions for cold-vulcanisable elastomers (CVE) which are stable on storage in the absence of moisture and which crosslink under atmospheric humidity at ambient temperature.
Such compositions have the advantage of not necessitating the use of compounds (scavengers) intended to remove the final traces of silanols, such as those described in Patent Nos. EP 69,256, EP 104,179 and FR 2,543,562.
A process for the preparation of linear diorganopolysiloxane containing at least one alkoxy group bound to a silicon atom at each end of its chain, comprising the step of reacting the following compounds 100 parts, by weight, of at least one linear diorganopolysiloxane containing an hydroxy group bound to a silicon atom at each end of its chain, 0.35 to 6 parts, by weight, of at least one polyalkoxysilane of formula:
(R
4 c (R 1 )aSi(OR 2 4 (1) 0.5 to 15 parts, by weight, of at least one alcohol, preferably methanol, in the presence of a catalytically effective amount of sodium hydroxide 15 or potassium hydroxide, wherein a is 0 or 1, or 2, wherein c is 0 or 1, or 2, wherein a c 0 or 1 or 2, wherein R represents a C 1 to C13 C. 13 20 saturated or unsaturated, substituted or unsubstituted, aliphatic, cycloalkane or aromatic monovalent hydrocarbon radical.
1. C 7 wherein R represents an aliphatic organic radical containing 1 to 8 carbon atoms, selected in particular from the alkyl radicals, alkylether radicals, alkylester radicals, alkylketone radicals, alkylcyano radicals, or an aralkyl radical containing 7 to 13 carbon atoms, and wherein if relevant more than one alkoxy group in the silane of 2 formula for R 2 may differ in the alkoxy groups, and wherein R 4 represents a substituted or unsubstituted, saturated or unsaturated, C 1 to C 13 aliphatic, cycloalkane or aromatic monovalent hydrocarbon radical, and wherein
R
4 may optionally be identical to R.
According to a variant of the invention, a process for the preparation of straight-chain diorganopolysiloxane comprising at least one alkoxy group linked to a silicon atom at each end of its chain has also been found, the said process being characterised in 20 that one mole of at least one diorganopolysiloxane comprising a hydroxyl group linked to a silicon atom at each end of its chain is reacted with 2 to 6 moles of at least one polyalkoxysilane of formula: *p S(R4) (Rl) Si(OR 2 (1) c a 4-(a+c) 25 in the presence of a catalytically effective amount of L sodium hydroxide or potassium hydroxide, 0 where a is 0 or 1, or 2, where c is 0 or 1, or 2, where a c 0 or 1 or 2, where R 1 represents a substituted or unsubstituted, saturated or unsaturated,
C
1 to C 13 aliphatic, cycloalkane or aromatic monovalent hydrocarbon radical, where R 2 represents an aliphatic organic radical having from 1 to 8 carbon atoms, 00 chosen, in particular, from alkyl radicals, 10 alkyl ether radicals, alkyl ester radicals, o alkyl ketone radicals, alkyl cyano radicals or an aralkyl radical having from 7 to 13 carbon atoms, it being understood that the alkoxy groups in the silane of formula (1) e 4 15 may each have a different meaning for R 2 or a.o. the same meaning, and where R 4 represents a substituted or unsubstituted, saturated or unsaturated,
C
1 to C 13 aliphatic, cycloalkane or aromatic monovalent hydrocarbon radical, it being possible for R 4 to be identical to R 1 These two variants exist because it has been found by the Applicant that during the introduction of functional groups into,the polydiorganosiloxanes by the alkoxysilanes, using strong alkaline catalysis, degradation reactions of the polymers, containing functional groups, which are obtained take place.
Following an in-depth kinetic study of these various 9 reactions involved, it has'been found that under certain conditions these adverse degradation reactions may be substantially slowed down.
Thus, the stronger the base used as catalyst the more it is the quantity of polyalkoxysilanes introduced, in synergism with the catalyst, which is a o predominant parameter in the degradation process of the Spolymers containing functional groups. It is for this reasqn that one mole of a diorganopolysiloxane 10 comprising a hydroxyl group linked to a silicon atom at a* each end of its chain is reacted with 2 to 6 moles of at least one polyalkoxysilane of formula knowing that only one of the alkoxy groups of a a polyalkoxysilane reacts with a silanol group of a *O a S 15 diorganopolysiloxane, which corresponds to one to three times the stoichiometric quantity.
An excess of polyakoxysilanes increases the rate of the degradation reactions; an excess of polyalkoxysilanes is understood to be an amount of these polyalkoxysilanes which is 3 times higher than the stoichiometric quantity. However, the degradation reactions may be distinctly slowed down when at least one alcohol, such as methanol, ethanol and propanol, individually or as a mixture, is present in the reaction mixture and its quantity is between 0.5 and parts by weight, preferably between 2 and 5 parts by weight, per 100 parts by weight of at least one polydiorganopolysiloxane.
In practice, an alcohol is used which has a boiling point of below or equal to 100 0
C.
Another aim of the present invention is the use of straight-chain diorganopolysiloxanes, in particular those comprising at least two alkoxy groups at each end of the chain, obtained by the process of the present invention for the preparation of single- Bcomponent polysiloxane compositions which are stable on storage in the absence of moisture and which crosslink 10 to form an elastomer in the presence of moisture.
**o More precisely, the diorganosiloxanes comprising at least one alkoxy group at each end of their chain have the formula: *appa a
R
1 a R R 1 a SR20)3-(a+c) Si 0 SiO Si -(0R 2 (2)
R
4 c R R 4 c nn 15 and the diorganopolysiloxane comprising a hydroxyl group at each end of its chain has the formula:
R
OH SiO--H (3) n where R 1
R
2 and R 4 have the same meaning as that given above for the silane of formula where the radicals R, which may be identical or es
*OP
0 0 10 o~o
S.
oS ue 0 oSore o 0 0P9 I* 0 eo.
S
7 different, represent monovalent hydrocarbon radicals having from 1 to 10 carbon atoms, which may be substituted by halogen at4oms or cyano groups; preferably, the radicals R are chosen from methyl, phenyl, vinyl and 3,3,3-trifluoropropyl radicals, where a is 0, or 1, or 2, where c 0, or 1, or 2, where a c 0, or 1, or 2, and where n has a value sufficient to confer on the polymers of formula and a viscosity of to 1,000,000 mPa s at 25°C, it being understood that the polysiloxane of formula may have an average formula in which the value of n is higher or lower than the value of n in the diorganopolysilaxanee reacting with the silane of formula The radicals R mentioned above comprise: alkyl and halogenoalkyl radicals having from 1 to carbon atoms, such as methyl, ethyl, propyl, isopropyl, butyl, pentyl, hexyl, 2-ethyl hexyl, octyl, decyl, 3,3,3-trifluoropropyl, 4,4,4trifluorobutyl or 4,4,4,3,3-pentafluorobutyl radicals, cycloalkyl and hajogenocycloalkyl radicals having from 1 to 10 carbon atoms, such as cyclopentyl, cyclohexyl, methylcyclohexyl, propylcyclohexyl, 2,3-difluorocyclobutyl or 3,4-difluoro-5methylcycloheptyl radicals, alkenyl radicals having from 2 to 4 carbon atoms, such as vinyl, allyl or but-2-enyl radicals, monocyclic aryl and halogenoaryl radicals having from 6 to 10 carbon atoms, such as phenyl, tolyl, xylyl, chlorophenyl, dichlorophenyl or trichlorophenyl radicals, and cyanoalkyl radicals in which the alkyl caains have from 2 to 3 carbon atoms, such as p-cyanoethyl and 10 -cyanopropyl radicals.
The following may be mentioned as specific examples of RzSiO units present in the alpha,omegadihydroxydiorganopolysiloxane of formula
(CH
3 SiO,
CH
3 (CHz=CH)SiO CH3
(CH
5 )zSiO, CFCHzCH 2
CH
3 )SiO NC-CHzCH 2 (CH) SiO NC-CH(CH) CHz (CHz=CH) SiO NC-CHzCH 2 CHz C 6 H) S i It must be understood that in the process according to the present invention a mixture consisting of alpha,omega-di(hydroxy)diorganopolysiloxane polymers which differ from one another in respect of the molecular weight and/or the nature of the groups linked to the silicon atoms may be used as polymer of formula It must also be mentioned that the polymer of formula may optionally comprise monoorganosiloxy RSiO 1 5 and/or SiO 2 units, in a proportion of at most 2% relative to the number of diorganosiloxy units R 2 SiO.
These alpha, omega-di( hydroxy) diorganopolysiloxane polymers are available commercially; in addition, they may be produced easily in accordance @6 00@ with techniques which are now well known.
Amongst the polyalkoxysilanes of formula
(R
4 )c(R')aSi(OR 2 4 which may be used in the process 10 according to the present invention, those listed below may be mentioned in particular: Si(OCH 3 4 0eS@S@ Si(OCH 2
CH
3 4 Si (OCH 2
CH
2
CH
3 4 15 (CH 3
O)
3 SiCH 3
(C
2
H
5 0) 3 SiCH 3
(CH
3 0) 3 SiCH
CH
2 0.00 o :(CzH 5 0) 3 SiCH CH 2
(CI
3 0) 3 SiCH 2 -CH CH 2
(CH
3 3 Si [CH 2
-(CH
3 )C CH,2
(C
2 1 5 0) 3 Si (OCH Si (OCH 2
-CH
2
-OCH
3 )4
CH
3 Si (OCH 2 -CI1 2
-OCH
3 3 CH2 CHSi(OCH 2
CH
2
CH
3 3 CHSSi(OCH 3
C
6
H
5 Si (OCH 2
-CH
2
-OCH
3 3
(CH
3
O)
3 Si [(CH 2 3 0 CH 2 CH CH 2 0 14 3 Si [(CH 2 2
CH
2 Cl] 3 Si 3 OOC C CHz] (CzHs) 3 Si (CH 2 3 N-i
N
(CzH 5 0) 3 Si (CH 2 2 CHzCl (CH30) 3 Si (CHz) 3
NH
z
(C
2 zH0) 3 Si (CHz) 3
NH
2
(CH
3
O)
3 Si (CHz) 3 NH (CH 2 2
NH
z 0' (C 2 zHO) 3 Si (CH) 3 NH (CH 2 )z -NH 1009 (CH30) 3 -Si(CHz) 3
SH
a 0 10
(CH
3
(CH
2 CH)Si(OCH 3 2 The most commonly used polyalkoxysilanes are: Si(OC 2 Hs) 4
CH
3 Si(OCH 3 3
CH
3 Si(OCzH) 3
(C
2
H
5 0) 3 Si(OCH3) CH 2 CH Si(OCH 3 3
CH
3 (CHz=CH)Si(OCH 3 2 CHz CH Si(OC 2 Hs) 3 15 With regard to the sodium hydroxide or potassium hydroxide used as the catalyst, both are widely available commercially; their formulae are, respectively, NaOH and KOH. When the reaction mixture does not contain alcohol, the sodium hydroxide or potassium hydroxide is preferably used as a solution in an alcohol, such as methanol or ethanol; the amount of alcohol present is then negligible. In general, a quantity of alcohol of between 2 and 4 times the quantity by weight of sodium hydroxida or potassium hydroxide is used.
A catalytically effective quantity of sodium hydroxide or potassium hydroxide is understood to be a quantity such that the rate of reaction is appreciably increased, in particular using CHSi(OCH 3 3
CH
2 =CH-Si(OCH 3 3 or MeViSi(OCH 3 as the agent for introducing functional groups. in the majority of cases, from 0.001 to 5 moles of sodium hydroxide or potassium hydroxide is used per I mole of silanol group -SiOH in the polydiorganoDolysiloxane of formula it being understood that in order to have 1 mole of -SiOH, 0.5 mole of polydiorganopolysiloxane of formula is needed.
The temperature of the reaction according to the present invention is preferably between -10 0 C and 90 0
C
and more preferably between 100C and 50 0
C.
The process according to the present invention is preferably carried out in the absence of moisture, for example in a closed reactor which is fitted with a stirrer and in which a vacuum has been produced and the air driven off has then been replaced by an anhydrous gas, for example nitrogen.
20 The reactants and the catalyst are charged into the reactor and when the reaction for the introduction of functional groups is complete the catalyst is neutralised and the reaction mass obtained is devolatilised in order to remove the alcohol formed during the reaction for the introduction of functional groups and the excess of agent for introducing functional groups (that is to say the silane of formula 16 Numerous products may be used to neutralise the catalyst for introducing functional groups (sodium hydroxide or potassium hydroxide), for example trichloroethyl phosphate or dimethylvinylsilyl acetate.
However, it is preferred to use a silyl phosphate, such as, for example, those described in French Patent
C
A2,410,004.
The devolatilisation is carried out, for example, under an absolute pressure of between 133 and 1 0 13332 pascals.
The patent application according to the present invention also relates to the use of diorganopolysiloxanes, in particular those comprising at least two alkoxy groups at each end of the chain, 15 obtained by the process of the present invention, for the preparation of single-component polysiloxane compositions which are stable on storage in the absence of moisture and which crosslink to form an elastomer in the presence of moisture.
These compositions are obtained by adding (by weight): 0 to 250 parts of inorganic fillers, 0 to 20 parts, preferably 0 to 10 parts, of at least one additive chosen from aminoorganosilanes, aminoorganopolysiloxanes and guanidinoorganosilanes simultaneously carrying, per molecule: at least one C 3 -C1 5 organic group linked by a SiC bond to the silicon atom and substituted by at least one amino radical or one guanidino radical, S(2i) and at least one C-Cs alkoxy radical or a C 3
-C
6 alkoxyalkyleneoxy radical, and an effective amount of condensation catalyst to 100 parts of the polymer, containing functional groups, to of formula obtained by the process of the present invention (containing the product from the neutralisation of sodium hydroxide or potassium 10- hydroxide).
An effective quantity of condensation catalyst is understood to be, for example, from 0.001 to 1 part by weight of at least one compound of a metal generally chosen from tin, titanium and zirconium and 15 their mixtures.
Condensation catalysts which may be used are tin monocarboxylates and dicarboxylates, such as tin 2ethylhexanoate, dibutyltin dilaurate or dibutyltin 0 diacetate (see the book by NOLL "Chemistry and technology of silicone", page 337, Academic Press, 1968 2nd edition).
The hexacoordinated chelates of tin or valency IV, such as those described in European Patent Application EP-A-147,323 and the Patent US-A 4,517,337, which are cited as reference, are particularly appropriate.
Condensation catalysts which are also preferred are those which are a mixture of a 18 diorganotin bis(p-diketonate) with an organic derivative of tin, also of valency IV, but free from any p-diketonato group and possessing at least one tin atom, each tin atom carrying two organic radicals bonded by a Sn-C bond, the other two valencies being satisfied by radicals chosen from organic or inorganic o 0 radicals bonded by a SnO or SnS bond, by halogen atoms, by hydroxyl groups and by oxygen atoms.
These organic derivatives of tin of valency 10 IV which are free from any p-diketonato group may be, in particular, tin salts of the formulae: AzSnR'6
R
6 SnO, AR zSnOSnR 6
,A
15 O-Q-O R6Sn SnR 6 2 O-Q-0 in which: R represents a Ci-C 2 hydrocarbon radical, which may or may not be halogenated, A represents an organic or inorganic radical bonded to the tin atom by a Sn-O or Sn-S bond, or a halogen atom, and Q represents a Cz-Cio alkylene radical.
A may be chosen from the group comprising: S(i) monocarboxylate radicals of formula
R
7 COO, R 7 being a CI-C 20 hydrocarbon radical, which may or may not be halogenated, (2i) dicarboxylate radicals of formula coo-
SCOO-
bonded to a single tin atom or to two tin atoms, leading to the two formulae:
/COO
0e*o G SnR 6 2 oocoo G000 SSn62 SnR 6 2 coo C0-SnR 6 2 0300 R 7
COO
in which G1 represents a divalent C 1
-C
15 hydrocarbon 7 R70COGICOO, in which R 7 and G have the meaning given, respectively, under and (2i).
The above tin salts are well known and are described, in particular, in the NOLL publication mentioned above, the Patents US-A-3,186,963 and 3,862,919, Belgian Patent 842,305 and British Patent GB-A-1,289,900, which are cited as reference.
The inorganic fillers are used in an amount of from 0 to 250 parts, preferably from 5 to 200 parts, per 100 parts of PF of formula These fillers may be in the form of very finely divided products, the average particle diameter of which is less than 0.1 micrometre. These fillers include silicas produced by combustion and silicas produced by precipitation; their BET specific surface aee e area is generally larger than 40 m 2 /g.
400 S 10 These fillers may also be in the form of more coarsely divided products having an average particle diameter of more than 0.1 micrometre. The following may be mentioned as examples of such fillers: ground quartz, diatomaceous silicas, calcium carbonate, calcine clay, titanium oxide of the rutile type, iron, zinc, chromium, zirconium and magnesium oxides, the various forms of alumina (hydrated or nonhydrated), 0 boron nitride, l.thopone, barium metaborate, barium sulphate and glass microspheres; their specific surface area is generally less than 30 m 2 /g.
These fillers may have been surface-modified by treatment with the various organosilicon compounds customarily used for this application. Thus, these organosilicon compounds may be organochlorosilanes, diorganocyclopolysiloxanes, hexaorganodisiloxanes, hexaorganodisilazanes or diorganocyclopolysiloxanes (French Patent FR-A-1,126,884, FR-A-1,136,885, FR-A- 1,236,505; British Patent GB-A-1,024,234). In the 21 majority of cases, the treated fillers contain from 3 to 30% of their weight of organosilicon compounds.
The fillers may consist of a mixture of several types of fillers of different particle sizes; thus, for example, they may consist of 30 to 70% of finely divided silicas having a BET specific surface 0 area of greater than 40 m 2 /g and 70 to 30% of more o,.o coarsely divided silicas having a specific surface area ga* Oof less than 30 m2/g.
10 In order to improve, in particular, the adherence of the CVEs, the compositions according to the invention may optionally also contain from 0 to 20 parts, preferably from 1 to 15 parts, of at least 4 one additive chosen from aminoorganosilanes, S 15 aminoorganopolysiloxanes and guanidineorganosilanes simultaneously carrying, per molecule: S(i) at least one C 3 -C15 organic group bonded .by a SiC bond to the silicon atom and substituted by at least one amino radical or one guanidino radical, S(2i) and at least one C 1
-C
5 alkoxy radical or one C 3 -Cgalkoxyalkylene radical.
These additives and their modes of use are described, in particular, in the patents US-A-2,574,311, US-A-2,832,754, US-A-2,930,809, US-A-2,971,864, US-A-3,341,563, U3-A-3,686,375 and US-A-4,180,642.
Amongst these additives, the silanes of formnula:
H
2 N (CHZ) 3 Si (0C 2
H
5 3 HZN (CH 2 3 Si (OCH 3 3
H
2 N (CH 2 ?NH (CH 2 3 S i (CH 3 3 may be mentioned in particular.
Particularly suitable adherence promoters are the silanes of formula: 3 -Si N 0 in which Y is an alkyl or alkoxy'radical having from 1 to 4 carbon atoms inclusive, at least two of the radicals Y being alkoxy radicals, which may be iS' identical or different, are chosen from a hydrogen atom and an alkyl radical having from 1 to 3 carbon atoms ~SbSinclusive and m is an integer between 3 and inclusive.
Silanes which may be mentioned are:
(CH
3 O)3Si(CH2)3 N 0 gama-morpoL-I 1.opropyltr imetho xys ilane
(C
3 CH2O)3Si(CHZ)3 N 0 gaima-morpholinopropyltriethoxys ilane.
These products and the process for their preparation are described by John L. SPEIER, J. Org.
Chem. vol. 36, No. 21, 1971, page 3, 120.
In the text which follows and in the foregoing text, unless specifically indicated to the contrary, the percentages and the parts are by weight.
The following examples illustrate the invention, without restricting its scope.
In these examples: 6 Mn is the number-average molecular mass, and 00 q is the viscosity expressed in mPa s.
4%V-) 8 EXAMPLE 1
C.
0 10 100 g of an a,w-dihydroxypolydimethylsiloxane *01 having a viscosity n of 175,000 mPa s at 25°C and a Mn of 75,000 and containing 450 ppr of hydroxyl groups (0.0026 SiOH units per 100 g of polymer) are introduced into a reactor.
Anhydrous nitrogen is also introduced into 0 this reactor and, with stirring, 1 g (0.0067 mol) of vinyltrimethoxysilane and 0.0160 g (0.0004 mol) of sodium hydroxide of formula NaOH are introduced at am ambient temperature The mixture is allowed to react for 1 hour at a temperature of 25°C and is then neutralised with 0.218 g of silyl phosphate which has a phosphoric acid equivalent content of 12.5% and is prepared in accordance with Example 2 of French Patent 2,410,004.
After devolatilisation of the alcohol formed (under 16 x 133.32 pascals), an oil is obtained which has a viscosity q of 178,000 mPa s at 25°C. 'H NMR, 2Si NMR and IR analyses show that'this oil is devoid of silanol groups and that it has a structure of formula: CH3 2 -Si-0 -SiO Si-(OCH 3 2 Vi CH3 Vi An intermediate determination shows that after a reaction time of 7 minutes there are already no o longer any silanol groups.
COMPARATIVE EXAMPLE 2 The procedure is as in Example 1, changing only the amount of vinyltrimethoxysilane introduced: a 5 g (0.034 mol), that is to say in excess.
After a reaction time of 1 hour at a temperature of 25 0 C, it is found that the silanol groups have disappeared, but the viscosity of the polymer obtained is no higher than 15,000 mPa s at 25 0
C.
The degradation reactions of the polymer containing functional groups have substantially reduced the viscosity of the latter.
EXAMPLE 3 The procedure is as in Example 1, replacing the sodium hydroxide introduced by 0.0080 g (0.00014 mol) of potassium hydroxide, of formula KOH, and neutralising the potassium hydroxide, after a reaction time of 1 hour, with 0.076 g of silyl phosphate (12.5% expressed as phosphoric acid).
The oil obtained has a viscosity r of 120,000 mPa s at 'H NMR, "Si NMR and IR analyses show that this oil is devoid of silanol groups.
COMPARATIVE EXAMPLE 4 S* The procedure is as in Example 1, replacing o the sodium hydroxide by 0.0080 g (0.00014 mol) of potassium hydroxide and changing the amount of 10 vinyltrimethoxysilane: 2.5 g(0.017 mol), that is to say in excess; and the potassium hydroxide being neutralised, after a reaction time of 1 hour, with 0.076 g of silyl phosphate (12.5% expressed as g phosphoric acid).
S 15 After a reaction time of 1 hour at a temperature of 25 0 C, it is found that the silanol groups have disappeared, but the viscosity of the polymer obtained is 20,000 mPa s at 25 0
C.
The degradation reactions of the polymer containing functional groups have substantially reduced the viscosity of the latter.
EXAMPLE The procedure is as in Comparative Example 4, adding 2.5 g (0.017 mpl) of methanol to the reaction mixture.
After a reaction time of 1 hour, the polymer obtained has a viscosity q of 140,000 mPa s at 25 0 C and the polymer is devoid of silanol groups.
26 EXAMPLE 6 The procedure is as in Example 1, introducing: 100 g of c,w-dihydroxypolydimethylsiloxane, 2.5 g (0.017 mol) of vinyltrimethoxysilane (excess), 6 0.016 g (0.0004 mol) of sodium hydroxide, and 2.5 g (0.078 mol) of methanol.
S.
The mixture is allowed to react for 1 hour 10 and is then neutralised.
After devolatilisation of the excess vinyltrimethoxysilane and the alcohol, an oil is obtained which has a viscosity q of 128000 mPa s at 25°C and a number-average molecular mass Mn 73,000.
15 1 H NMR, 29Si NMR and IR analyses show that the introduction of functional groups into this oil is complete: absence of silanol groups.
SCOMPARATIVE EXAMPLE 7 The procedure is as in Example 6, not introducing methanol; there is therefore an excess of vinyltrimethoxysilane, this excess not being compensated for by the presence of at least one volatile alcohol.
After a reaction time of 1 hour at a temperature of 25 0 C, it is found that the silanol groups have disappeared, but the viscosity of the polymer obtained at 25 0 C is 50,000 mPa s, which is confirmed by the number-average molecular mass of said polymer: Mn 59,000.
COMPARATIVE EXAMPLE 8 The procedure is as in Example 1, using the following amounts of reagents: 100 g of a,w-dihydroxypolydimethylsiloxane S*oo 5 g (0.034 mol) of vinyltrimethoxysilane (excess), 6. and S- 0.0110 g (0.0002 mol) of potassium hydroxide After a reaction time of 1 hour at 25"C, the
*S
10 -mixture is neutralised with 0.107 g of silyl phosphate (12.5% of phosphoric acid).
The polymer obtained has a viscosity r of 6400 mPa s at EXAMPLE 9 15 The procedure is as in Comparative Example 8, adding 5 g (0.034 mol) of methanol to the reaction mixture.
After a reaction time of 1 hour, the polymer obtained has a viscosity r of 104,000 mPa s at 25°C and is devoid of silanol groups.
COMPARATIVE EXAMPLE The procedure is as in Example 1, using the following amounts of reagents: 100 g of a,w-dihydroxypolydimethylsiloxane, 2.5 g (0.017 mol) of vinyltrimethoxysilane (excess), and 0.0110 g (0.002 mol) of potassium hydroxide.
After a reaction time of 1 hour at 25 0 C, the mixture is neutralised with 0.107 g of silyl phosphate (12.5% of phosphoric acid).
The polymer obtained has a viscosity r of 20,000 mPa s at EXAMPLE 11 0* The procedure is as in Comparative Example adding 2.5 g (0.054 iwol) of ethanol, of formula
C
2
H
5 OH, to the reaction mixture.
*0 The polymer obtained has a viscosity 1 of 92,000 mPa s at 25°C and is devoid of silanol groups.
EXAMPLE 12 The procedure is as in Comparative Example o 10, adding 5 g (0.083 mol) of propan-2-ol to the reaction mixture.
15 The polymer obtained has a viscosity r of 85,000 mPa s at 25°C and is devoid of silanol groups.
oe
Claims (17)
1. A process for the preparation of linear diorganopolysiloxane containing at least one alkoxy group bound to a silicon atom at each end of it chain, comprising the step of reacting the following compounds 100 parts, by weight, of at least one linear diorganopolysiloxane containing an hydroxy group bound to a silicon atom at each end of its chain, 0.35 to 6 parts, by weight, of at least one polyalkoxysilane of formula: (R4 c(R) aSi(OR2 (1) to 15 parts, by weight, of at least one alcohol, in the presence of a catalytically effective amount of sodium hydroxide or potassium hydroxide, wherein a is 0 or i, or 2, wherein c is 0 or 1, or 2, wherein a c 0 or 1 or 2, 1 wherein R represents a C 1 to C 1 3 saturated or unsaturated, substituted or 20 unsubstituted, aliphatic, cycloalkane or aromatic monovalent hydrocarbon radical. S. S1. oRA 30 wherein R 2 represents an aliphatic organic radical containing 1 to 8 carbon atoms, selected in particular from the alkyl radicals, alkylether radicals, alkylester radicals, alkylketone radicals, alkylcyano radicals, or an aralkyl radical containing 7 to 13 carbon atoms, and wherein if relevant more than one alkoxy group in the silane of 2 formula for R may differ in the alkoxy groups, and wherein R 4 represents a substituted or unsubstituted, saturated or unsaturated, C 1 to C 13 aliphatic, cycloalkane or aromatic monovalent hydrocarbon radical, and wherein 4 1 R may optionally be identical to R.
2. A process according to claim 1 wherein the aromatic monovalent hydrocarbon radical can further comprise an i oepoxy, a primary, a secondary or tertiary amine mercapto group.
3. A process according to claim 1, wherein the quantity of at least one alcohol is between 2 and 5 parts by weight.
4. A process according to claim 1 comprising the steps 0 of reacting one mole of at least one diorganopolysiloxane comprising a hydroxyl group linked to a silicon atom at each end of its chain with 2 to 6 moles of at least one ^c^1/ 31 polyalkoxysilane of formula in the presence of a catalytically effective quantity of sodium hydroxide or potassium hydroxide.
A process according to claim 4, wherein the sodium hydroxide or potassium hydroxide is in solution in an alcohol.
6. A process according to any one of the preceding claims wherein from 0.001 to 5 moles of sodium hydroxide or potassium hydroxide are used per one mole of silanol group =SiOH in the diorganopolysiloxane.
7. A process according to any one of the preceding claims, wherein the temperature is from -10 0 C and +90 0 C.
8. A process according to claim 7 wherein the temperature is from +100C to 50 0 C.
9. A process according to claim 1 wherein the alcohol is methanol.
A process according to any one of the preceding claims, wherein the linear diorganopolysiloxane comprising at least one alkoxy group at each end of the chain has the formula: SI a i a a 2 2 (R 0 Si 0 -SiO Si (OR 14 11 4 15 c c (2) n C. and wherein the straight-chain diorganopolysiloxane comprising a hydroxyl group at each end of its chain has the formula 20 R 1 OH H S R 25 R n CC mm -32- wherein the radicals R, which may be identical or different, represent monovalent hydrocarbon radicals having from 1 to 10 carbon atoms, which may be optionally substituted by halogen atoms or cyano groups, and wherein n has a value sufficient to confer on the diorganopolysiloxanes of formula and a viscosity of 25 to 1,000,000 mPa s at 25 0 C.
11. A process according to claim 10 wherein the radical R in the formulae and is chosen from methyl, phenyl, vinyl and trifluropropyl radicals.
12. A process according to any one of the preceding claims, wherein the polyalkoxysilane of formula is chosen from methyltrimethoxysilane, methyltriethyoxy- silane, vinyltrimethoxysilane, tetraethoxysilane, vinyltriethoxysilane and methylvinyldimethoxysilane.
13. A process according to any one of claims 10 to 12 wherein the step of reacting the product of formula (1) and the product of formula for the introduction of ii.. functional groups is complete in less than 10 minutes.
14. A process according to claim 10 wherein at the end S: of the reaction, for the introduction of functional a groups, between the product of formula and the 9* product of formula the sodium hydroxide or potassium 0 a 5 hydroxide used is neutralised.
15. A process according to claim 14 characterised in that the sodium hydroxide or potassium hydroxide is A 4 .neutralised by silyl phosphate. /I 33
16. The product obtained according to one of claims 14 to 15 for the preparation of single-component polysiloxane compositions which are stable on storage in the absence of moisture and which crosslink to form an elastomer in the presence of moisture.
17. A process for the preparation of straight-chain diorganopolysiloxane substantially as herein described with reference to any one of the examples, excluding the comparative examples. DATED 27th July, 1993 RHONE-POULENC CHIMIE Attorney: IAN T. ERNST Fellow Institute of Patent Attorneys of Australia of SHELSTON WATERS e 9 o 9 o
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9005756A FR2661680B1 (en) | 1990-05-02 | 1990-05-02 | PROCESS FOR THE PREPARATION OF DIORGANOPOLYSILOXANES WITH ALCOXY TERMINAL GROUPS. |
FR9005756 | 1990-05-02 |
Publications (2)
Publication Number | Publication Date |
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AU7608191A AU7608191A (en) | 1991-11-07 |
AU642241B2 true AU642241B2 (en) | 1993-10-14 |
Family
ID=9396418
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU76081/91A Ceased AU642241B2 (en) | 1990-05-02 | 1991-04-26 | Process for the preparation of diorganopolysiloxanes having alkoxy end groups |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0457693B1 (en) |
JP (1) | JPH0791388B2 (en) |
AT (1) | ATE102234T1 (en) |
AU (1) | AU642241B2 (en) |
BR (1) | BR9101766A (en) |
DE (1) | DE69101262T2 (en) |
ES (1) | ES2062729T3 (en) |
FR (1) | FR2661680B1 (en) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
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CA2081447C (en) * | 1990-04-26 | 1997-08-19 | Gerhard Staiger | Organo(poly)siloxanes containing terminal siloxane units having organyloxy and hydrogen groups |
DE4022661A1 (en) * | 1990-07-17 | 1992-01-23 | Bayer Ag | METHOD FOR PRODUCING POLY (DIORGANOSILOXANES) WITH ALKOXY END GROUPS |
DE4207212A1 (en) * | 1992-03-06 | 1993-09-09 | Bayer Ag | METHOD FOR PRODUCING ORGANYLOXY END-STOPPED POLYSILOXANS |
JPH07126391A (en) * | 1993-09-07 | 1995-05-16 | Shin Etsu Chem Co Ltd | Epoxidized organopolysiloxane |
DE19533915A1 (en) * | 1995-09-13 | 1997-03-20 | Bayer Ag | Process for the preparation of poly (diorganosiloxanes) with diorganyloxyorganylsilyl or triorganylsilyl end groups, crosslinkable mixtures containing poly (diorganosiloxanes) with diorganyloxyorganylsilyl or triorganyloxysilyl end groups and their use |
US5837784A (en) * | 1996-06-12 | 1998-11-17 | Dow Corning Corporation | Method of making alkoxylated organosilicone resins and the resins produced thereby |
JP2001114896A (en) * | 1999-10-13 | 2001-04-24 | Shin Etsu Chem Co Ltd | Method for producing end hydrolyzable group blocked organopolysiloxane |
JP4399066B2 (en) * | 1999-10-29 | 2010-01-13 | 東レ・ダウコーニング株式会社 | Process for producing amino group-containing organopolysiloxane |
JP4231974B2 (en) * | 1999-11-17 | 2009-03-04 | 信越化学工業株式会社 | Process for producing organooxy-terminated organopolysiloxane |
JP2002030149A (en) * | 2000-07-18 | 2002-01-31 | Shin Etsu Chem Co Ltd | Method of producing organopolysiloxane containing mercapto group and releasing agent, lubricant, and glossing agent using the organopolysiloxane |
US6818721B2 (en) * | 2002-12-02 | 2004-11-16 | Rpo Pty Ltd. | Process for producing polysiloxanes and use of the same |
FR2882760B1 (en) * | 2005-03-04 | 2007-04-20 | Rhodia Chimie Sa | ORGANOPOLYSILOXANE COMPOSITIONS CURING IN ELASTOMERS FROM AMBIENT TEMPERATURE IN THE PRESENCE OF MOISTURE |
FR2900153B1 (en) | 2006-04-21 | 2008-07-18 | Rhodia Recherches & Tech | PROCESS FOR CONDENSING SILYLATED PATTERNS USING CARBENE TYPE CATALYST |
DE102007034711A1 (en) | 2007-07-25 | 2009-01-29 | Wacker Chemie Ag | Process for the preparation of organosilicon-containing organosilicon compounds |
JP4255088B1 (en) * | 2008-06-06 | 2009-04-15 | 鈴鹿富士ゼロックス株式会社 | Hybrid composition |
WO2014098189A1 (en) | 2012-12-21 | 2014-06-26 | 日本山村硝子株式会社 | Organic-inorganic hybrid prepolymer, organic-inorganic hybrid material, and element sealing structure |
DE102015216598A1 (en) * | 2015-08-31 | 2017-03-02 | Wacker Chemie Ag | Process for the preparation of organosilicon-containing organosilicon compounds |
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BE533700A (en) * | ||||
US2634252A (en) * | 1949-05-25 | 1953-04-07 | Dow Corning | Method of polymerizing organosiloxanes with alkoxides and alcohol-hydroxide complexes |
FR1495011A (en) * | 1966-08-10 | 1967-09-15 | Midland Silicones Ltd | Process for the preparation of organopolysiloxanes with alkoxylated substituents linked to silicon |
JPS53118500A (en) * | 1977-03-25 | 1978-10-16 | Toray Silicone Co Ltd | Production of organic functional polysiloxane |
DE3106186A1 (en) * | 1981-02-19 | 1982-09-09 | Wacker-Chemie GmbH, 8000 München | METHOD FOR PRODUCING ORGANOPOLYSILOXANS AND USE OF THIS ORGANOP |
DE3523206A1 (en) * | 1985-06-28 | 1987-01-02 | Bayer Ag | METHOD FOR PRODUCING POLY (DIORGANOSILOXANES) WITH ALKOXY END GROUPS |
CA1327207C (en) * | 1987-08-27 | 1994-02-22 | Jeffrey Hayward Wengrovius | Polyalkoxysilyl-terminated polydiorganosiloxanes, methods for their preparation, and room temperature vulcanizable compositions containing them |
FR2638752B1 (en) * | 1988-11-04 | 1992-07-24 | Rhone Poulenc Chimie | PROCESS FOR THE PREPARATION OF DIORGANOPOLYSILOXANES WITH ALCOXY TERMINAL GROUPS |
-
1990
- 1990-05-02 FR FR9005756A patent/FR2661680B1/en not_active Expired - Lifetime
-
1991
- 1991-03-26 JP JP3084362A patent/JPH0791388B2/en not_active Expired - Fee Related
- 1991-04-23 ES ES91420133T patent/ES2062729T3/en not_active Expired - Lifetime
- 1991-04-23 DE DE69101262T patent/DE69101262T2/en not_active Expired - Fee Related
- 1991-04-23 AT AT91420133T patent/ATE102234T1/en not_active IP Right Cessation
- 1991-04-23 EP EP91420133A patent/EP0457693B1/en not_active Expired - Lifetime
- 1991-04-26 AU AU76081/91A patent/AU642241B2/en not_active Ceased
- 1991-04-30 BR BR919101766A patent/BR9101766A/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
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AU7608191A (en) | 1991-11-07 |
JPH0791388B2 (en) | 1995-10-04 |
EP0457693A1 (en) | 1991-11-21 |
EP0457693B1 (en) | 1994-03-02 |
FR2661680B1 (en) | 1992-07-24 |
JPH04227731A (en) | 1992-08-17 |
FR2661680A1 (en) | 1991-11-08 |
ATE102234T1 (en) | 1994-03-15 |
DE69101262T2 (en) | 1994-08-25 |
BR9101766A (en) | 1991-12-17 |
ES2062729T3 (en) | 1994-12-16 |
DE69101262D1 (en) | 1994-04-07 |
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