Process for the continuous production of polyoxyalkylene polyols
The invention relates to a process for producing a polyoxyalkylene polyol, comprising depositing an alkylene oxide onto an H-functional starter substance in the presence of a double metal cyanide (DMC) catalyst, wherein the alkylene oxide is dosed at the mass flow rate m(alkylene oxide), the H-functional starter substance is dosed at the mass flow rate m(starter substance), and the double metal cyanide (DMC) catalyst is dosed in a dispersant at the mass flow rate m(DMC) continuously into the reactor with the reaction volume V during the reaction, and the resulting reaction mixture is continuously removed from the reactor, and wherein the quotient of the sum of the mass flow rates Σ{dot over (m)} of {dot over (m)}(alkylene oxide), {dot over (m)}(starter substance) and {dot over (m)}(DMC) to give the reaction volume V in the steady state is greater than or equal to 1200 g/(h·L).
1. A process for preparing a polyoxyalkylene polyol comprising addition of an alkylene oxide onto an H-functional starter substance in the presence of a double metal cyanide (DMC) catalyst;
wherein the alkylene oxide with a mass flow {dot over (m)}(alkviene oxide), the H-functional starter substance with a mass flow {dot over (m)}(starter substance) and the double metal cyanide (DMC) catalyst in a dispersion medium with a mass flow {dot over (m)}(DMC) are during the reaction continuously metered into a reactor having a reaction volume V and the resulting reaction mixture is continuously removed from the reactor;
and wherein the quotient of the sum of the mass Σ{dot over (m)}, composed of {dot over (m)}(alkylene oxide), {dot over (m)}(starter substance) and {dot over (m)}(DMC), and the reaction volume V in the steady state is not less than 1200 g/(h·L).
2. The process as claimed in claim 1 , wherein the quotient of the sum of the mass flows Σ{dot over (m)}, composed of {dot over (m)}(olkylene oxide), {dot over (m)}(starter substance) and {dot over (m)}(DMC), and the reaction volume V in the steady state is not less than 1500 g/(h·L).
3. The process as claimed in claim 1 , wherein the quotient of the sum of the mass flows Σ{dot over (m)}, composed of {dot over (m)}(alkylene oxide), {dot over (m)}(starter substance) and {dot over (m)}(DMC), and the reaction volume V in the steady state is not more than 4000 g/(h·L).
4. The process as claimed in claim 1 , wherein the reaction volume V is identical to the reactor volume V R .
5. The process as claimed in claim 1 , wherein the polyoxyalkylene polyol comprises a polyether polyol.
6. The process as claimed in claim 1 , wherein the concentration of the double metal cyanide (DMC) catalyst is 50 ppm or less, based on the sum of alkylene oxide, H-functional starter substance, dispersion medium and double metal cyanide (DMC) catalyst.
7. The process as claimed in claim 1 , wherein the double metal cyanide (DMC) catalyst is obtained by reaction of an aqueous solution of a cyanide-free metal salt, an aqueous solution of a metal cyanide salt, an organic complex ligand and a complex-forming component.
8. The process as claimed in claim 7 , wherein the complex-forming component is a polyether polyol having a number-average molecular weight of ≥500 g/mol, wherein the number-average molecular weight is calculated from the determined OH number.
9. The process as claimed in claim 7 , wherein the organic complex ligand comprises one or more of dimethoxyethane, tert-butanol, 2-methyl-3-buten-2-ol, 2-methyl-3-butyn-2-ol, ethylene glycol mono-tert-butyl ether and 3-methyl-3-oxetanemethanol.
10. The process as claimed in claim 1 , wherein the H-functional starter substance comprises one or more of ethylene glycol, propylene glycol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol , 2-methylpropane-1,3-diol, neopentyl glycol, 1,6-hexanediol, diethylene glycol, dipropylene glycol, glycerol, trimethylolpropane and di- and trifunctional polyether polyols.
11. The process as claimed in claim 1 , wherein the dispersion medium is the same as the H-functional starter substance.
12. The process as claimed in claim 1 , wherein the alkylene oxide is ethylene oxide, propylene oxide or a mixture of ethylene oxide and propylene oxide.
13. The process as claimed in claim 1 , wherein the reaction temperature is 130° C. to 170° C.
14. The process as claimed in claim 1 , wherein the reaction mixture continuously outflowing from the reactor is continuously transferred into a postreactor to reduce the content of free alkylene oxide.
15. The process as claimed in claim 1 , wherein the quotient of the sum of the mass flows Σ{dot over (m)}, composed of {dot over (m)}(olkylene oxide), {dot over (m)}(starter substance) and {dot over (m)}(DMC), and the reaction volume V in the steady state is 1200 g/(h·L) to 4000 g/(h·L).