Articles comprising copolyesters produced with germanium catalyst
US-2024376258-A1 · Nov 14, 2024 · US
US2016229787A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016229787-A1 |
| Application number | US-201415029376-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 17, 2014 |
| Priority date | Oct 17, 2013 |
| Publication date | Aug 11, 2016 |
| Grant date | — |
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Methods and systems for producing alkyl hydroxyalkanoate from hydroxy carboxylic acid recovery bottoms. The methods generally comprise the steps of obtaining a hydroxy carboxylic acid recovery bottom, adding a mono-alcohol to the hydroxy carboxylic acid recovery bottom to obtain a first mixture, heating the first mixture in the presence of a catalyst to form a reaction product, distilling the reaction product, and recovering an alkyl hydroxyalkanoate fraction.
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1 . A method for producing an alkyl hydroxyalkanoate, comprising: a) obtaining a hydroxyalkanoate containing composition, comprising: (i) at least 40 percent by weight hydroxyalkanoate equivalents; (ii) greater than 0 and less than 45 percent by weight free hydroxyalkanoates; (iii) at least 1 percent by weight saccharide equivalents; and (iv) less than 15 percent by weight water; b) mixing a mono-alcohol in a molar ratio of from about 1.1 to 1.0 to about 10.0 to 1.0 of mono-alcohol to hydroxyalkanoate equivalents present in the hydroxyalkanoate containing composition to obtain a first mixture; c) heating the first mixture to form a reaction product; d) distilling the reaction product and recovering an alkyl hydroxyalkanoate fraction comprising: (i) at least 90 percent by weight alkyl hydroxyalkanoate; (ii) less than 1 percent by weight hydroxyalkanoic acid; (iii) less than 1 percent by weight water; and (iv) less than 0.5 percent by weight saccharide equivalents. 2 . The method of claim 1 , wherein step (d) further comprises separating the reaction product into a first fraction enriched in the mono-alcohol and water, and a second fraction enriched in the alkyl hydroxyalkanoate, wherein the alkyl hydroxyalkanoate fraction is recovered from the second fraction. 3 . The method of claim 1 , wherein step (d) comprises: a first step to provide a first fraction enriched in water and mono-alcohol and a second fraction enriched in the alkyl hydroxyalkanoate and the saccharide equivalents; and a second step to fractionate the second fraction into a saccharide equivalents enriched fraction, and the alkyl hydroxyalkanoate fraction. 4 - 5 . (canceled) 6 . The method of claim 1 , wherein step (d) comprises: a first step to provide a first fraction enriched in water, mono-alcohol, and alkyl hydroxyalkanoate and a second fraction enriched in saccharide equivalents; and a second step to fractionate the first fraction into a water and mono-alcohol enriched fraction and the alkyl hydroxyalkanoate fraction. 7 . The method of claim 1 , wherein the first mixture is heated to a temperature of from about 50° C. to about 300° C. 8 - 10 . (canceled) 11 . The method of claim 1 , wherein the pressure in step (e) ranges from 1 atm to 100 atm. 12 - 13 . (canceled) 14 . The method of claim 1 , wherein the hydroxyalkanoate containing composition comprises at least 50 percent by weight of hydroxyalkanoate equivalents. 15 - 16 . (canceled) 17 . The method of claim 1 , wherein the hydroxyalkanoate containing composition comprises between 0.5 and 40 percent free hydroxyalkanoates. 18 - 21 . (canceled) 22 . The method of claim 1 , wherein the hydroxyalkanoate containing composition comprises at least 2 percent by weight saccharide equivalents. 23 - 24 . (canceled) 25 . The method of claim 1 , wherein the hydroxyalkanoate containing composition comprises less than 15 percent by weight water. 26 - 28 . (canceled) 29 . The method of claim 1 , wherein a pressure below atmospheric pressure is utilized during step (d) to recover the alkyl hydroxyalkanoate fraction. 30 - 33 . (canceled) 34 . The method of claim 1 , wherein percent yield of alkyl hydroxyalkanoate from hydroxyalkanoate equivalents is greater than 50%. 35 - 37 . (canceled) 38 . The method of claim 1 , wherein percent yield of alkyl hydroxyalkanoate from hydroxyalkanoate equivalents is greater than 90%. 39 . (canceled) 40 . The method of claim 1 , wherein the hydroxyalkanoate containing composition is selected from the group consisting of 2-carbon hydroxyalkanoates, 3-carbon hydroxyalkanoates, 4-carbon hydroxyalkanoates, 5-carbon hydroxyalkanoates and mixtures thereof. 41 . The method of claim 1 , wherein percent recovery of alkyl hydroxyalkanoate from hydroxyalkanoate equivalents is greater than 50%. 42 - 46 . (canceled) 47 . The method of claim 1 , wherein the alkyl hydroxyalkanoate fraction comprises less than 0.1 by weight saccharide equivalents. 48 . (canceled) 49 . The method of claim 1 , wherein the hydroxyalkanoate is hydroxypropionate. 50 . The method of claim 49 , wherein the hydroxyalkanoate is lactic acid. 51 . (canceled) 52 . The method of claim 1 , wherein the alkyl hydroxyalkanoate is alkyl hydroxypropionate. 54 . The method of claim 1 , wherein the alkyl hydroxyalkanoate is ethyl lactate. 55 - 56 . (canceled)
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