Process for purifying (meth)acrylic acid including a dividing-wall distillation column

Patent metadata

Field	Value
Publication number	US-10815182-B2
Application number	US-201816499887-A
Country	US
Kind code	B2
Filing date	Apr 3, 2018
Priority date	Apr 4, 2017
Publication date	Oct 27, 2020
Grant date	Oct 27, 2020

Abstract

The invention relates to the use of a column with a separating wall as a purification/finishing column in a (meth)acrylic acid recovery method based on the use of two distillation columns in the absence of external organic solvent. The method according to the invention improves the energy balance for the method while improving the technical quality of the (meth)acrylic acid recovered. The method according to the invention further produces polymer-grade (or glacial) (meth)acrylic acid compatible with the production of high-molecular weight acrylic acid polymers.

First claim

The invention claimed is:

1. A method for recovering purified (meth)acrylic acid, in the absence of organic solvent, from a gaseous reaction mixture comprising (meth)acrylic acid obtained by gaseous phase oxidation of a (meth)acrylic acid precursor, comprising at least the following steps:
a) subjecting the gaseous reaction mixture to a dehydration without using an azeotropic solvent in a first distillation column called a dehydration column having a top and a bottom, leading to a flow from the dehydration column top of which at least part is condensed and sent back to the dehydration column in the form of reflux, and to a flow from the dehydration column bottom of which at least part is sent back as reflux into a lower part of the dehydration column to form a recirculation loop;
b) sending at least in part the flow from the bottom of the dehydration column into a second distillation column called a finishing column having a top, a bottom, a top portion, a lower portion, a feed section, and a draw-off section, which separates a flow from the finishing column bottom containing heavy compounds, and a flow from the finishing column top containing light compounds, of which at least part is sent back to the dehydration column;

wherein:
i) the finishing column is equipped with a separating wall, the wall being connected with an upper dome of the finishing column in the top portion and not connected with the bottom of the finishing column in the lower portion, thereby separating the finishing column into two sections equipped with internal distillation elements that ensure gas-liquid contact, of which a lower space communicates with the space at the bottom of the column, and of which a headspace is separated into two sealed areas, said finishing column being fed in said feed section from a single side of the separating wall, and
ii) a gaseous flow rich in light compounds and comprising water is extracted at the top of the feed section, then recycled, after condensation, at least in part in a recirculation loop at the bottom of the dehydration column, and
iii) a flow of purified (meth)acrylic acid extracted in gaseous form from the finishing column at a top of a section located opposite to the feed section, is drawn off after condensation to form a condensed flow, part of the condensed flow being sent back as liquid reflux at a top of the draw-off section.

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

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

4. The method according to claim 1 wherein the (meth)acrylic acid precursor comprises carbon from a renewable source.

5. The method according to claim 1 wherein the finishing column is fed at a top at an upper tray of the feed section of the finishing column, and optionally, a portion of the gaseous flow that is extracted at the top of the feed section of the finishing column, is sent back after condensation into a feed flow of the finishing column.

6. The method according to claim 1 wherein the finishing column is fed at a point located lower than an upper tray of the feed section of the finishing column, and a portion of the gaseous flow that is extracted at a top of the feed section, is sent back after condensation as liquid reflux at the top of the feed section.

7. The method according to claim 1 wherein the feed section of the finishing column includes a number of theoretical trays inclusively between 5 and 20.

8. The method according to claim 1 wherein the draw-off section of the finishing column includes a number of theoretical trays inclusively between 2 and 20.

9. The method according to claim 1 wherein a lower space of the finishing column located under the separating wall is equipped with rectification elements representing between 1 and 5 theoretical trays.

10. The method according to claim 1 further comprising the introduction into the finishing column, of a chemical processing agent to reduce the residual aldehyde content.

11. The method according to claim 10 wherein the chemical processing agent for aldehydes is chosen from the group consisting of:
monoethanolamine, ethylene diamine, glycine, diethylenetriamine, dipropylenetriamine, ortho-, para-, and meta-phenylenediamine,
aniline, ortho-, para-, and meta-methylaniline,
hydrazine and its salts, hydrazine hydrate, hydrazine sulfate, hydrazine carboxylates, hydrazine hydrochloride, phenylhydrazine, 4-nitrophenylhydrazine, and 2,4-dinitrophenylhydrazine, aminoguanidine and its salts, aminoguanidine hydrogen carbonate, and
carboxylic acid hydrazides and their salts, hydrazides of formic, acetic, propionic, butanoic, pentanoic, maleic acids dihydrazides of adipic and succinic acids, urea and urea and hydrazine derivatives, semicarbazide and carbohydrazide and their salts;
alone or their mixtures in any proportions.

12. The method according to claim 10 wherein the chemical processing agent is introduced into a feed flow of the finishing column.

13. The method according to claim 10 wherein the chemical processing agent is introduced directly into the finishing column at a point located between the top and the bottom of the finishing column, lower than a tray where the column is fed.

14. The method according to claim 10 wherein a side draw of a gaseous flow comprising (meth)acrylic acid with intermediate quality is made from the draw-off section.

15. The method according to claim 1 further comprising an extra processing of purified (meth)acrylic acid by fractionated crystallization, or by distillation optionally in the presence of a compound reacting with residual aldehydes, leading to a polymer-grade (meth)acrylic acid quality.

16. A method for producing purified (meth)acrylic acid comprising the following steps:
A) subjecting at least one (meth)acrylic acid precursor to an oxidation in gaseous phase to form a gaseous reaction mixture comprising (meth)acrylic acid;
B) cooling the gaseous reaction mixture;
C) subjecting the cooled gaseous reaction mixture to the (meth)acrylic acid recovery method as defined according to claim 1 .

Assignees

• Arkema France

Inventors

• FAUCONET Michel Jean
• Tretjak Serge

Classifications

• C07C57/04

  Acrylic acid; Methacrylic acid · CPC title

• C07C51/44 Primary

  by distillation · CPC title

• C07C51/252

  of propene, butenes, acrolein or methacrolein · CPC title

• B01D9/004

  Fractional crystallisation; Fractionating or rectifying columns · CPC title

• B01D3/141

  where at least one distillation column contains at least one dividing wall · CPC title