Higher functional polyether carbonate polyols obtained using branching molecules

Patent metadata

Field	Value
Publication number	US-9957354-B2
Application number	US-201414915687-A
Country	US
Kind code	B2
Filing date	Sep 1, 2014
Priority date	Sep 5, 2013
Publication date	May 1, 2018
Grant date	May 1, 2018

Abstract

The present invention relates to a method for producing higher functional polyether carbonate polyols, said method preferably comprising the steps of ([alpha]) providing a DMC catalyst and; ([alpha][alpha]) a suspending agent that does contain any H-functional groups and/or ([alpha][beta]) an H-functional starter compound ([beta]) adding carbon dioxide and at least one alkylene oxide ([gamma]) adding carbon dioxide and at least two alkylene oxides, wherein these alkylene oxides can be the same as or different from the alkylene oxide or alkylene oxides added in step ([beta]), and ([delta]) adding carbon dioxide and at least one alkylene oxide, wherein this alkylene oxide or these alkylene oxides can be the same as or different from the alkylene oxides added in steps ([beta]) and ([gamma]), at least one of the alkylene oxides in step ([gamma]) having an epoxy functionality of >=2 and, in addition, in the case that no H-functional starter compound is provided in ([alpha]), step ([delta]) includes the addition of an H-functional starter compound.

First claim

The invention claimed is:

1. A process for preparing polyethercarbonate polyols of relatively high functionality comprising reacting at least two alkylene oxides and carbon dioxide with H-functional starter compounds in the presence of a double metal cyanide catalyst, comprising the steps of
(α) initially introducing a double metal cyanide catalyst and
(αα) a suspension medium that contains no H-functional groups, and/or
(αβ) an H-functional starter compound,

(γ) metering in carbon dioxide and at least two alkylene oxides and
(δ) metering in carbon dioxide and at least one alkylene oxide, wherein the alkylene oxide(s) are identical or different from the alkylene oxides metered in step (γ),
wherein at least one of the alkylene oxides in step (γ) having an epoxy functionality of ≥2 is selected from the group consisting of BAGE bisphenol A diglycidyl ether and DED 1,2,9,10-diepoxydecane, and
wherein, if no H-functional starter compound was introduced in step (α), step (δ) comprises the metering of an H-functional starter compound.

2. The process as claimed in claim 1 , further comprising step (β) between step (α) and step (γ):
(β) metering in carbon dioxide and at least one alkylene oxide,
and wherein at least two alkylene oxides metered in step (γ) are identical or different from the alkylene oxide or alkylene oxides metered in step (β), and wherein the alkylene oxide(s) metered in step (δ) are identical or different from the alkylene oxides metered in step (β) and (γ).

3. The process as claimed in any of claims 1 , wherein the polyethercarbonate polyol according to formula (Ia) has an e/f ratio of 2:1 to 1:20,

4. The process as claimed in claim 1 , wherein at least one of the alkylene oxides having an epoxy functionality of ≥2 in step (γ) is a compound of formula (I),

where X1 is a chemical bond or a di- or multivalent, heteroatom-containing or non-heteroatom-containing C5-C22 aliphatic, aromatic, araliphatic or cycloaliphatic radical and n is an integer ≥1.

5. The process as claimed in claim 1 , wherein at least one of the alkylene oxides having an epoxy functionality of ≥2 in step (γ) is a compound of formula (II),

where X2 and X3 independently of one another are a chemical bond or are heteroatom-containing or non-heteroatom-containing C5-C22 aliphatic, aromatic, araliphatic or cycloaliphatic radicals.

6. The process as claimed in claim 1 , wherein at least one of the alkylene oxides having an epoxy functionality of ≥2 in step (γ) is a compound of formula (III),

where X4 is a di- or polyvalent, heteroatom-containing or non-heteroatom-containing C5-C22 aliphatic, aromatic, araliphatic or cycloaliphatic radical and n is an integer ≥1.

7. The process as claimed in claim 1 , wherein the addition of the alkylene oxide or oxides having an epoxy functionality of ≥2 in step (γ) is concluded before 50 mol% of the total amount of alkylene oxides has been added.

8. The process as claimed in claim 1 , wherein at least the step (δ) is carried out continuously.

9. The process as claimed in claim 1 , comprising continuously metering an H-functional starter compound in step (δ).

10. The process as claimed in claim 1 , comprising discontinuously metering an H-functional starter compound in step (δ).

11. The process as claimed in claims 1 , wherein the polyethercarbonate polyol of relatively high functionality is reacted, in an additional process step, with di- and/or polyisocyanates.

12. A polyethercarbonate polyol of relatively high functionality, obtained by the process as claimed in claim 1 .

13. A crosslinked polyethercarbonate polymer obtained by the process as claimed in claim 11 .

14. A article comprising the crosslinked polyethercarbonate polymer as claimed in claim 13 wherein the article is a thermoset solids, viscoelastic foams or coatings.

15. The process as claimed in claim 1 , wherein the at least one of the alkylene oxides in step (γ) having an epoxy functionality of ≥2 is added before more than half of the total alkylene oxides has been added.

16. The process as claimed in claim 1 , wherein the at least one of the alkylene oxides in step (γ) having an epoxy functionality of ≥2 is added before more than a quarter of the total alkylene oxides has been added.

Assignees

• Covestro Deutschland Ag

Inventors

• Müller Thomas E
• Gürtler Christoph
• Subhani Muhammad A
• Köhler Burkhard
• Leitner Walter

Classifications

• C08G65/2663 Primary

  Metal cyanide catalysts, i.e. DMC's · CPC title

• C08G64/34

  and cyclic ethers · CPC title

• C08G65/2696

  characterised by the process or apparatus used · CPC title

• C08G65/2603

  the other compounds containing oxygen · CPC title

• C08G18/44

  Polycarbonates · CPC title