Fluoropolyether compound, and lubricant and magnetic disc comprising same
US-2015371672-A1 · Dec 24, 2015 · US
US9758619B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9758619-B2 |
| Application number | US-201214234577-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 15, 2012 |
| Priority date | Aug 25, 2011 |
| Publication date | Sep 12, 2017 |
| Grant date | Sep 12, 2017 |
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Ethylene carbonate is polymerized by itself or together with another cyclic monomer such as 1,2-propylene oxide in the presence of a double metal cyanide catalyst. Most of the ethylene carbonate adds to the chain to form a terminal carbonate group, which decarboxylates to produce a hydroxyethyl group at the end of the polymer chain. The polymerization of more ethylene carbonate onto the chain end results in the formation of poly(ethyleneoxy) units. Therefore, the process provides a method for making poly(ethyleneoxy) polymers without the need to polymerize ethylene oxide. The process is useful for making polyethers that are useful as water-absorbable polymers, surfactants and as raw materials for polyurethanes. The process is also useful for increasing the primary hydroxyl content of a polyether.
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What is claimed is: 1. A process for preparing a polyether containing ether-linked ethyleneoxy units, comprising copolymerizing a mixture of 5-35 weight-% ethylene carbonate and 65-95 weight-% 1,2-propylene oxide, based on the combined weight of the ethylene carbonate and 1,2-propylene oxide, wherein the ethylene carbonate is dissolved in the 1,2-propylene oxide prior to being polymerized, in the presence of an initiator compound having one or more oxyalkylatable groups and a double metal cyanide catalyst and in the substantial absence of ethylene oxide, wherein 80 to 98% of the ethyleneoxy units are ether-linked. 2. The process of claim 1 wherein the oxyalkylatable groups are hydroxyl, primary amino or secondary amino groups, or a mixture of any two or more of such groups. 3. The process of claim 2 wherein the oxyalkylatable groups are hydroxyl groups. 4. The process of claim 3 wherein the initiator contains from 2 to 8 hydroxyl groups per molecule and has a hydroxyl equivalent weight of from 70 to 2500. 5. The process of claim 3 wherein the initiator is a polyether that has a hydroxyl equivalent weight of from 500 to 2000. 6. The process of claim 1 wherein carbon dioxide is removed at least once during the polymerization. 7. The process of claim 1 , wherein the product contains carbonate groups. 8. The process of claim 1 , wherein the product contains terminal poly(ethyleneoxy) groups. 9. The process of claim 8 , which contains terminal primary hydroxyl groups. 10. The process of claim 1 , further comprising continuing the polymerization in the presence of ethylene carbonate alone or together with up to 25% by weight of 1,2-propylene oxide to introduce terminal poly(ethyleneoxy) groups and increase the primary hydroxyl content of the polyether.
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