Carboxylic acid recovery from magnesium carboxylate mixture
The invention is directed to a method for recovering carboyxlic acid from an magnesium carboxylate containing aqueous mixture, including the steps of: contacting the aqueous mixture with an acidic ion exchanger, thereby forming a carboxylic acid mixture and an ion exchanger loaded with magnesium ions; contacting the ion exchanger loaded with magnesium ions with a hydrochloric acid solution, thereby forming a magnesium chloride solution; and thermally decomposing the magnesium chloride solution at a temperature of at least 300° C., thereby forming magnesium oxide (MgO) and hydrogen chloride (HCl).
1. Method for recovering carboyxlic acid from a magnesium carboxylate containing aqueous mixture, comprising the steps of
contacting the aqueous mixture with an acidic ion exchanger, thereby forming a carboxylic acid mixture and an ion exchanger loaded with magnesium ions; and
contacting the ion exchanger loaded with magnesium ions with a hydrochloric acid solution, thereby forming a magnesium chloride solution; and
thermally decomposing the magnesium chloride solution at a temperature of at least 300° C., thereby forming magnesium oxide (MgO) and hydrogen chloride (HCl),
wherein at least part of the carboxylic acid mixture is fed back to the aqueous mixture.
2. Method according to claim 1 , further comprising
dissolving the HCl in water, thereby obtaining a HCl solution; and
bringing the MgO in contact with water, thereby obtaining Mg(OH) 2 .
3. Method according to claim 2 , wherein the HCl solution is recycled for use in contacting the ion exchanger loaded with magnesium ions.
4. Method according to claim 1 , wherein MgO and/or Mg(OH) 2 is recycled for use in a fermentation process.
5. Method according to claim 1 , wherein the ion exchanger loaded with magnesium ions is washed with water before contacting it with the hydrochloric acid solution.
6. Method according to claim 1 , wherein the acidic ion exchanger is strongly acidic and comprises one or more sulphonic acid and/or phosphonic acid groups.
7. Method according to claim 1 , wherein the acidic ion exchanger is a solid acidic ion exchanger.
8. Method according to claim 1 , wherein the ion exchange step is conducted in an ion exchange column.
9. Method according to claim 1 , wherein the ion exchange step is conducted in a fluidized bed or a simulated moving bed of polymeric ion exchange resin beads.
10. Method according to claim 1 , wherein the acidic ion exchanger is a liquid acidic ion exchanger.
11. Method according to claim 10 , wherein the acidic ion exchanger is an organic compound comprising one or more sulphonic acid and/or phosphonic acid groups, wherein the acidic ion exchanger is optionally dissolved in a hydrophobic solvent.
12. Method according to claim 1 , wherein the carboxylic acid is selected from the group consisting of lactic acid, succinic acid, propionic acid, 3-hydroxypropionic acid, hydroxybutyric acid, citric acid, fumaric acid, itaconic acid, adipic acid, acrylic acid, levulinic acid, maleic acid, terephtalic acid, 2,5-furandicarboxylic acid, lactylic acids and fatty acids.
13. Method according to claim 1 , wherein at least 99 wt. % of the aqueous mixture is in liquid or dissolved form, based on the total weight of the aqueous mixture.
14. Method according to claim 1 ,
wherein contacting the aqueous mixture with the acidic cation exchanger is conducted at a temperature of at least 40° C.