Polyolefin mimic polyester copolymers
US-2024218116-A1 · Jul 4, 2024 · US
US9353043B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9353043-B2 |
| Application number | US-201514620579-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 12, 2015 |
| Priority date | Feb 18, 2014 |
| Publication date | May 31, 2016 |
| Grant date | May 31, 2016 |
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In a process for preparing (meth)acrylic esters (E) of polyalkoxy-containing alcohols which comprises reacting polyalkoxy-containing alcohols (P) of formula (I) where R 1 is hydrogen, a hydroxyl group or a straight-chain or branched, saturated or unsaturated alcohol of 1 to 30 carbon atoms, R 2 and R 3 are each independently H or methyl, and m and n are each independently an integer between 0 and 100, with the proviso that m and n cannot both be 0, with a (meth)acrylic anhydride (A) in the presence of at least one basic catalyst (K) having a pK B value of not more than 7.0 and of at least one sterically hindered polymerization inhibitor, the reaction mixture is quenched with a C 1 -C 6 alkanol after the reaction has ended.
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We claim: 1. A process for preparing a (meth)acrylic ester (E) of a polyalkoxy-containing alcohol, the process comprising reacting a polyalkoxy-containing alcohol (P) of formula (I) wherein R 1 is hydrogen, a hydroxyl group or a straight-chain or branched, saturated or unsaturated alcohol of 1 to 30 carbon atoms, R 2 and R 3 are each independently H or methyl, and m and n are each independently an integer between 0 and 100, with the proviso that m and n cannot both be 0, with a (meth)acrylic anhydride (A) in the presence of a basic catalyst (K) having a pK B value of not more than 7.0 and of a sterically hindered polymerization inhibitor, wherein the reaction mixture is quenched with a C 1 -C 6 alkanol after the reaction has ended. 2. The process according to claim 1 , wherein R 2 and R 3 are each hydrogen in formula (I). 3. The process according to claim 1 , wherein m and n in formula (I) are each independently integers in the range from 5 to 90. 4. The process according to claim 3 , wherein m and n in formula (I) are each independently integers in the range from 5 to 50. 5. The process according to claim 1 , wherein the substituent R 1 is a straight-chain, saturated or unsaturated primary alcohol of 6 to 22 carbon atoms. 6. The process according to claim 1 , wherein the basic catalyst (K) has a pK B value of not more than 3.0. 7. The process according to claim 6 , wherein the basic catalyst is selected from the group consisting of alkali metal and alkaline earth metal hydroxides and inorganic salts. 8. The process according to claim 7 , wherein the basic catalyst is lithium hydroxide, sodium hydroxide, potassium hydroxide, magnesium hydroxide or calcium hydroxide. 9. The process according to claim 7 , wherein the inorganic salt comprises at least one anion selected from the group consisting of carbonate (CO 3 2− ), bicarbonate (HCO 3− ), phosphate (PO 4 3− ), hydrogenphosphate (HPO 4 2− ), dihydrogenphosphate (H 2 PO 4− ), sulfate (SO 4 2− ), sulfite (SO 3 2− ) and carboxylate (R 4 —COO—), where R 4 is C 1 -C 18 alkyl; C 2 -C 18 alkyl optionally interrupted by an oxygen atom, a sulfur atom, a substituted or unsubstituted imino group, or any combination thereof; or C 6 -C 14 aryl. 10. The process according to claim 9 , wherein the inorganic salt is selected from the group consisting of Li 3 PO 4 , K 3 PO 4 , Na 3 PO 4 , K 2 CO 3 and Na 2 CO 3 and also hydrates thereof. 11. The process according to claim 1 , wherein the amount of (meth)acrylic anhydride (A) is reacted at not more than 1.35 mol per mole of the polyalkoxy-containing alcohol (P). 12. The process according to claim 11 , wherein the amount of (meth)acrylic anhydride (A) is reacted at not more than 1.15 mol per mole of the polyalkoxy-containing alcohol (P). 13. The process according to claim 1 wherein the sterically hindered polymerization inhibitor does not degrade during the course of the reaction. 14. The process according to claim 13 , wherein the sterically hindered polymerization inhibitor is selected from the group consisting of 2,6-di-tert-butylphenol, 2,6-di-tert-butyl-4-methylphenol and phenothiazine. 15. The process according to claim 1 , wherein the C 1 -C 6 alkanol is selected from the group consisting of methanol, ethanol, propanol and isopropanol. 16. The process according to claim 15 , wherein the C 1 -C 6 alkanol is selected from the group consisting of methanol and ethanol. 17. The process according to claim 1 , wherein the quench time is up to 2 h, but not less than 30 minutes. 18. The process according claim 1 , wherein the C 1 -C 6 alkanol is added to the reaction medium in amounts of up to 5 wt %, based on total reaction medium. 19. A method for producing a dispersion, comprising employing a (meth)acrylic ester (E) of a polyalkoxy-containing alcohol as a monomer or comonomer.
Diluents or solvents · CPC title
acyclic · CPC title
Phenols; Phenolates · CPC title
Alkali metals, alkaline earth metals, beryllium, magnesium, copper, silver, gold, zinc, cadmium, mercury, manganese, or compounds thereof {(C08G63/823 takes precedence)} · CPC title
by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds · CPC title
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