Process for producing polymer-grade (meth)acrylic acid

1. A process for the recovery of polymer-grade (meth)acrylic acid, in the absence of organic solvent, from a gaseous reaction mixture comprising (meth)acrylic acid obtained by gas-phase oxidation of a precursor of the (meth)acrylic acid, comprising at least the following stages:

i) subjecting the gaseous reaction mixture to dehydration without using azeotropic or external organic solvent in a first distillation column, referred to as dehydration column having an upper part and a lower part, a temperature of the upper part being at least 40° C., said dehydration column operating at atmospheric pressure or greater pressure, resulting in a top stream, at least a portion of which is condensed and sent back to the dehydration column in the form of reflux, and in a bottom stream;

ii) subjecting the dehydration column bottom stream at least in part, to distillation in a second column, referred to as finishing column, resulting in a top stream comprising water and in a bottom stream comprising heavy compounds;

iii) recovering a purified polymer-grade (meth)acrylic acid stream by drawing off a sidestream from the finishing column;

wherein said process is carried out in the presence of at least one agent for the chemical treatment of aldehydes for reducing content of residual heavy aldehydes having a boiling point greater than that of (meth)acrylic acid and light aldehydes having a boiling point lower than that of (meth)acrylic acid;

wherein the finishing column is a column having a separating wall having two sides which is fed, on one side of the wall, with the dehydration column bottom stream and the drawing off of a sidestream of the purified (meth)acrylic acid stream is carried out in a section located on the other side of the separating wall;

wherein the agent for the chemical treatment of the heavy and light aldehydes is introduced into the finishing column at a level of a section located between the feed level of said finishing column and the level of a plate for drawing off a sidestream of purified (meth)acrylic acid; and

wherein a second drawing off is carried out in the gas phase on the finishing column, at a position located below the drawing off of a sidestream of the purified acrylic acid.

2. The process according to claim 1 , wherein the finishing column is a distillation column operating at a pressure below atmospheric pressure.

3. The process according to claim 1 wherein the purified (meth)acrylic acid stream obtained in stage iii) is drawn off in the form of a gaseous stream of polymer-grade (meth)acrylic acid.

4. The process according to claim 1 wherein the purified (meth)acrylic acid stream drawn off in stage iii) is subjected to an additional treatment by distillation using one or two distillation columns and the agent for the chemical treatment of the aldehydes is introduced during said additional treatment.

5. The process according to claim 1 wherein the agent for the chemical treatment of the aldehydes is chosen from the group consisting of:

amines,

aniline and aniline compounds,

hydrazine, hydrazine compounds, hydrazine salts, aminoguanidine and its salts

hydrazides, hydrazides of carboxylic acids and their salts, dihydrazides of adipic acid and succinic acid, urea and derivatives of urea and of hydrazine, and their salts;

alone or their mixtures in all proportions.

6. The process according to claim 1 wherein the precursor of the (meth)acrylic acid is acrolein, obtained by oxidation of propylene or by oxydehydrogenation of propane.

7. The process according to claim 1 wherein the precursor of the (meth)acrylic acid is methacrolein, obtained by oxidation of isobutylene and/or of tert-butanol or from oxydehydrogenation of butane and/or isobutane.

8. The process according to claim 1 wherein the precursor of the (meth)acrylic acid comprises carbon of renewable origin and is derived from glycerol, 3-hydroxypropionic acid or 2-hydroxypropionic acid.