Process for preparing polyether alcohols with DMC catalysts using compounds bearing SiH groups as additives
View Patent ↗Process for preparing polyether alcohols by polymerization by means of double metal cyanide catalysts (DMC catalysts), characterized in that, before or during the polymerization, one or more, optionally mixed additives consisting of compounds having one or more hydridic hydrogen atoms bonded to one silicon atom are added to the reaction mixture.
1. Process for preparing polyether alcohols with elevated polydispersity by polymerization by means of double metal cyanide catalysts (DMC catalysts), characterized in that, before or during the polymerization, one or more additives, optionally mixed, consisting of compounds having one or more hydrogen atoms bonded to one silicon atom as Si—H additive are added to the starting reaction mixture comprising the OH-functional starting compound and the DMC catalyst.
2. Process according to claim 1 , characterized in that, the polydispersity Mw/Mn of the produced polyetherols is higher compared to a polyether produced without the Si—H-additive under otherwise same reaction conditions.
3. Process according to claim 1 , characterized in that, the polydispersity of the produced polyetherols is at least 10 percent higher if compared to a process which is performed without the Si—H-additives.
4. Process according to claim 1 , characterized in that, the absolute value of the polydispersity Mw/Mn is at least 0.1 higher if compared to a process which is performed without the Si—H-additives.
5. Process for preparing polyether alcohols according to claim 1 , characterized in that the Si—H additive has the formula (I)
R′″ a H b Si (I),
where
R′″ is one or more identical or different radicals selected from linear or branched, saturated, mono- or polyunsaturated, alkyl, alkoxy, alkylsilyl, aryl, alkylaryl or arylalkyl radicals having 1 to 40 carbon atoms or haloalkyl groups having 1 to 20 carbon atoms,
a is an integer of 1 to 3,
b is an integer of 1 to 3,
with the proviso that the sum of a and b is equal to 4 and at least one hydrogen atom bonded to a silicon atom is present in the molecule.
6. Process for preparing polyether alcohols according to claim 2 , characterized in that the silicon-hydrogen compounds of the formula (I) used are monomethyl, dimethyl- and trimethylsilane, monoethyl-, diethyl-, triethylsilane, monopropyl-, dipropyl-, tripropylsilane, monophenyl-, diphenyl-, triphenylsilane, phenylmethyl- and phenylethylsilane, phenyldimethyl- and phenyldiethylsilane, monoethoxy-, dimethoxy- and trimethoxysilane and monoethoxy-, diethoxy-, and triethoxysilane, dimethylmethoxysilane, methyldimethoxysilane or tris(trimethylsilyl)silane.
7. Process for preparing polyether alcohols according to claim 1 , characterized in that the additives used are hydrosiloxanes or polyorganosiloxanes of the general formula (II)
in which
R is one or more identical or different radicals selected from linear or branched, saturated, mono- or polyunsaturated alkyl, alkoxy, aryl, alkylaryl or arylalkyl radicals having 1 to 40 carbon atoms, or haloalkyl groups having 1 to 20 carbon atoms, or siloxy groups and triorganosiloxy groups,
where
R′ and R″ are each independently H or R,
x is an integer of 0 to 600,
y is an integer of 0 to 100,
with the proviso that at least one hydrogen atom bonded to a silicon atom is present in the molecule.
8. Process for preparing polyether alcohols according to claim 1 , characterized in that polyether alcohols of the formulae (Va) or (Vb)
R 1 —[(CR 6 R 2 —CR 5 R 3 —O) n H] (Va)
or R 1 —[(CR 5 R 3 —CR 6 R 2 —O) n H] m
R 1 —[(CHR 2 —CH(CH 2 OR 4 )—O) n H] m (Vb)
or R 1 —[(CH(CH 2 OR 4 )—CHR 2 —O) n H] m
where R 1 is either a hydroxyl radical or a radical having at least one carbon atom,
m is 1 to 8 and
n is 1 to 12 000, and
R 2 or R 3 , and R 5 or R 6 , are identically or else independently H or a saturated or optionally mono- or polyunsaturated, optionally mono- or polyvalent hydrocarbon radical which may also have further substitution; where the R 5 and R 6 radicals are each a monovalent hydrocarbon radical,
are prepared.
9. Process according to claim 1 for preparing polyether alcohols of the formulae (Va) or (Vb)
R 1 —[(CR 6 R 2 —CR 5 R 3 —O) n H] m (Va)
or R 1 —[(CR 5 R 3 —CR 6 R 2 —O) n H] m
R 1 —[(CHR 2 —CH(CH 2 OR 4 )—O) n H] m (Vb)
or R 1 —[(CH(CH 2 OR 4 )—CHR 2 —O) n H] m
and mixtures thereof, where R 1 is either a hydroxyl radical or a radical having at least one carbon atom,
m is 1 to 8 and
n is 1 to 12 000,
by polymerizing alkylene oxides of the formula (IIIa) or (IIIb)
where R 2 or R 3 , and R 5 or R 6 are the same or are independently H or a saturated or optionally mono- or polyunsaturated, optionally mono- or polyvalent hydrocarbon radical which may also have further substitution, where the R 5 and R 6 radicals are each a monovalent hydrocarbon radical and the hydrocarbon radical may be bridged cycloaliphatically via the fragment Y; where Y may be a methylene bridge having 0, 1 or 2 methylene units or glycidyl compounds such as glycidyl ethers and/or glycidyl esters of the general formula (IIIb)
whose at least one glycidyloxypropyl group is bonded via an ether or ester function R 4 to a linear or branched alkyl radical having 1 to 24 carbon atoms, an aromatic or cycloaliphatic radical, onto starter compounds R 1 —H (IV) where R 1 is either a hydroxyl radical or a radical having at least one carbon atom.
10. Process for preparing polyetherols of the formulae (Va) or (Vb) according to claim 1 , characterized in that at least one of the two R 2 and R 3 radicals in formula (IIIa) is hydrogen.
11. Process for preparing polyether alcohols according to claim 1 , characterized in that alkylene oxides of the formula (IIa) or (IIb) used are ethylene oxide, propylene oxide, 1,2- or 2,3-butylene oxide, isobutylene oxide, 1,2-dodecene oxide, styrene oxide, cyclohexene oxide, epichlorohydrin, 2,3-epoxy-1-propanol or vinylcyclohexene oxide, or mixtures thereof.
12. Process according to claim 1 , characterized in that, the polyetheralcohols having an average molecular masses of below 8.000 g/mol and based on starting alcohols like allyl alcohol, hexenole, butanol, octanol, decanol, dodecanol, stearyl alcohol, 2-ethylhexanol, isononanol, ethylene glycol, propylene glycol, di-, tri- and polyethylene glycol, 1,2-propylen glycol, di- and polypropylene glycol, 1,4-butandiol, 1,6-hexandiol, trimethylol propan and/or glycerol, have polydispersities of higher than or equal to 1.2.
13. Process according to claim 1 , characterized in that, the polyetheralcohols having an average molecular masses of higher than 8.000 g/mol have polydispersities of higher than or equal to 1.4.
14. Preparation of polyurethanes using polyether alcohols of the formulae (Va) and (Vb), obtained by a process according to claim 1 .
15. Preparation of polyether siloxanes using polyether alcohols of the formulae (Va) and (Vb), obtained by a process according to claim 1 .
16. Preparation of surface-active substances or surfactants using polyether alcohols of the formulae (Va) and (Vb), obtained by a process according to claim 1 .