Production of acrylic acid
US-2015353466-A1 · Dec 10, 2015 · US
US9309180B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9309180-B2 |
| Application number | US-201414650089-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 14, 2014 |
| Priority date | Jan 16, 2013 |
| Publication date | Apr 12, 2016 |
| Grant date | Apr 12, 2016 |
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Method for producing acrylic acid by dehydration of a C 3 hydroxycarboxylic acid, characterized in that dehydration is achieved by contacting, at a temperature of more than 150° C., the hydroxycarboxylic acid with a mixture which is liquid at this temperature and comprises at least one metal salt of a C 3 hydroxycarboxylic acid, and water.
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What is claimed is: 1. A method for producing acrylic acid by the dehydration of a C 3 hydroxycarboxylic acid, comprising the step of contacting the C 3 hydroxycarboxylic acid with a liquid mixture at a temperature of more than 150° C., wherein the liquid mixture comprises at least one alkali metal salt or alkaline earth metal salt of a C 3 hydroxycarboxylic acid, and water. 2. The method as claimed in claim 1 , wherein the temperature of the mixture is from 160° C. to 300° C. 3. The method as claimed in claim 1 , wherein the hydroxycarboxylic acid metal salt is produced using a metal carbonate or one or more metal salts of formula (I) M z+ x H 3-x*z PO 4 z*x− (I) where x=1 or 2, z=1 or 2 and M=metal, with the proviso that when z=2, x=1 wherein the metal is an alkali metal or alkaline earth metal. 4. The method as claimed in claim 1 , wherein the hydroxycarboxylic acid to be dehydrated and the hydroxycarboxylic acid on which the hydroxycarboxylic acid metal salt is based are identical. 5. The method as claimed in claim 1 , wherein the mixture comprises at least one polymerization inhibitor. 6. The method as claimed in claim 5 , wherein the fraction of the sum total of polymerization inhibitors in the liquid mixture is from 0.05% to 2.5% by mass. 7. The method as claimed in claim 1 , wherein the pressure above the liquid mixture is below 500 mbar. 8. The method as claimed in claim 1 , wherein the contacting of the hydroxycarboxylic acid to be dehydrated and the mixture is performed such that the hydroxycarboxylic acid is introduced into the mixture. 9. The method as claimed in claim 8 , wherein the introduction of the hydroxycarboxylic acid to be dehydrated into the liquid mixture is performed via an introduction point disposed no less than 5% and no more than 75% below the surface of the mixture based on the total height of the liquid at this point. 10. The method as claimed in claim 1 , wherein the employed C 3 hydroxycarboxylic acid to be dehydrated is selected from 3-hydroxypropionic acid and lactic acid. 11. The method as claimed in claim 5 , wherein the polymerization inhibitor is selected from hydroquinone and p-methoxyphenol. 12. The method as claimed in claim 5 , wherein the fraction of the sum total of polymerization inhibitors in the liquid mixture is from 0.1% to 0.5% by mass. 13. The method as claimed in claim 1 , wherein the pressure above the liquid mixture is from 50 to 100 mbar. 14. A method for producing a superabsorbent polymer comprising a step of producing a monomer component containing an acrylic acid made by dehydration of a C 3 hydroxycarboxylic acid, wherein the dehydration is achieved by contacting, at a temperature of more than 150° C., a hydroxycarboxylic acid with a liquid mixture at this temperature and comprises at least one metal salt of a C 3 hydroxycarboxylic acid, and water. 15. The method as claimed in claim 14 , wherein the employed C 3 hydroxycarboxylic acid to be dehydrated is selected from 3-hydroxypropionic acid and lactic acid.
by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups {(C07C51/36 - C07C51/373 take precedence)} · CPC title
Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof · CPC title
Acrylic acid; Methacrylic acid · CPC title
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