Fluorinated polymer and use thereof in the preparation of hydrophilic membranes (vi)
US-2015375181-A1 · Dec 31, 2015 · US
US9751982B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9751982-B2 |
| Application number | US-201214352247-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 16, 2012 |
| Priority date | Oct 19, 2011 |
| Publication date | Sep 5, 2017 |
| Grant date | Sep 5, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to compositions of polyether polyol resins (hydroxyfunctional oligo or poly ether) comprising a mixture of α,α-branched alkane carboxylic glycidyl esters derived from butene oligomers characterized in that the sum of the concentration of the blocked and of the highly branched isomers is maximum 55%, preferably below 40%, and most preferably below 30% weight on total composition.
Opening claim text (preview).
We claim: 1. A process to prepare a composition of polyether polyol resin comprising reacting at least one polyol having at least three hydroxyl groups and a composition of α,α-branched alkane carboxylic glycidyl esters from butene oligomers, comprising a glycidyl ester mixture of neo-acids derived from a dimer or trimer of butene having both blocked isomers and highly branched isomers wherein a sum of a concentration of blocked isomers and the concentration of highly branched isomers is a maximum of 55 wt % based on the weight of the composition of α,α-branched alkane carboxylic glycidyl esters, wherein the highly branched isomers are isomers of neo-acids having at least 5 methyl groups. 2. The process of claim 1 , wherein the composition of α,α-branched alkane carboxylic glycidyl esters is based on a neononanoic acid mixture wherein the sum of the concentration of the blocked and of the highly branched isomers is a maximum of 55 wt % based on the total weight of the composition. 3. The process of claim 2 wherein the composition of α,α-branched alkane carboxylic glycidyl esters comprises 2,2-dimethyl heptanoic acid glycidyl ester, or 2-methyl 2-ethyl hexanoic acid glycidyl ester or 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl esters. 4. The process of claim 2 wherein the composition of α,α-branched alkane carboxylic glycidyl esters comprises 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount below 40 wt % based on the total weight of the composition. 5. The process of claim 4 wherein the mixture of α,α-branched alkane carboxylic glycidyl esters comprises 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount below 30 wt % based on the total weight of the composition. 6. The process of claim 4 wherein the mixture of α,α-branched alkane carboxylic glycidyl esters comprises 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount below or equal to 25 wt % based on the total weight of the composition. 7. The process of claim 2 wherein the composition of α,α-branched alkane carboxylic glycidyl esters comprises 2-methyl 2-ethyl hexanoic acid glycidyl ester in an amount above 10 wt % based on the total weight of the composition. 8. The process of claim 7 wherein the mixture of α,α-branched alkane carboxylic glycidyl esters comprises 2-methyl 2-ethyl hexanoic acid glycidyl ester in an amount above 30 wt % based on the total weight of the composition. 9. The process of claim 7 wherein the mixture of α,α-branched alkane carboxylic glycidyl esters comprises 2-methyl 2-ethyl hexanoic acid glycidyl ester in an amount above 45 wt % based on the total weight of the composition. 10. The process of claim 2 wherein the composition of α,α-branched alkane carboxylic glycidyl esters comprises 2,2-dimethyl heptanoic acid glycidyl ester, 2-methyl 2-ethyl hexanoic acid glycidyl ester and 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount above 40 wt % based on the total weight of the composition. 11. The process of claim 10 wherein the mixture of α,α-branched alkane carboxylic glycidyl esters comprises 2,2-dimethyl heptanoic acid glycidyl ester, 2-methyl 2-ethyl hexanoic acid glycidyl ester and 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount above 55 wt % based on the total weight of the composition. 12. The process of claim 10 wherein the mixture of α, 60 -branched alkane carboxylic glycidyl esters comprises 2,2-dimethyl heptanoic acid glycidyl ester, 2-methyl 2-ethyl hexanoic acid glycidyl ester and 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount above 65 wt % based on the total weight of the composition. 13. The process of claim 2 wherein the composition of α,α-branched alkane carboxylic glycidyl esters comprises 2,2-dimethyl heptanoic acid glycidyl ester in an amount of 1 to 15 wt %, 2-methyl 2-ethyl hexanoic acid glycidyl ester in an amount of 40 to 70 wt % and 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount of 8 to 32 wt % based on the total weight of the composition. 14. The process of claim 2 wherein the composition of α,α-branched alkane carboxylic glycidyl esters comprises 2,2-dimethyl heptanoic acid glycidyl ester in an amount of 2 to 10 wt %, 2-methyl 2-ethyl hexanoic acid glycidyl ester in an amount of 47 to 61 wt % and 2-methyl 2-ethyl 3-methyl pentanoic acid glycidyl ester stereoisomers in an amount of 10 to 25 wt % based on the total weight of the composition. 15. The process of claim 2 wherein the sum of the concentration of the blocked isomers and of the highly branched isomers is below 40 wt % based on the total weight of the composition. 16. The process of claim 2 wherein the sum of the concentration of the blocked isomers and of the highly branched isomers is below 30 wt % based on the total weight of the composition. 17. The process of claim 1 wherein the polyether polyol resin composition has a number average molecular weight (Mn) lower than 4500 Dalton according the polystyrene standard or has an hydroxyl value above 120 mg KOH/g on solids. 18. The process of claim 1 , wherein the sum of the concentration of the blocked isomers and of the highly branched isomers is below 40 wt % based on the total weight of the composition. 19. The process of claim 1 , wherein the sum of the concentration of the blocked isomers and of the highly branched isomers is below 30 wt % based on the weight of the composition. 20. The process of claim 1 wherein the mixture of α,α-branched alkane carboxylic glycidyl esters is derived from butene oligomers. 21. A binder composition useful for a coating application with a low VOC and comprising the polyether polyol resin composition from the process of claim 1 . 22. A metal or plastic substrate coated with a coating composition comprising the binder composition of claim 21 . 23. A polyester-ether resin comprising the reaction product of the polyether polyol resin composition from the process of claim 1 and dimethylol propionic acid.
Of metal · CPC title
Composite [nonstructural laminate] · CPC title
Polyalkylene oxides · CPC title
Coating compositions based on polyethers obtained by reactions forming an ether link in the main chain (based on polyacetals C09D159/00; based on epoxy resins C09D163/00; based on polythioether-ethers C09D181/02; based on polyethersulfones C09D181/06); Coating compositions based on derivatives of such polymers · CPC title
containing aliphatic hydroxyl groups · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.