Process for preparation of highly pure, non-yellowing methacrylic acid
View Patent ↗This invention relates to a process of preparing highly pure, non-yellowing (meth)acrylic acid necessary for high-tech applications requiring long-tem color stability in the presence of amines. Process for the preparation of highly pure, non-yellowing (meth)acrylic acid comprising the steps: f) Condensation of a (meth)acrylic acid-containing gas phase obtained via a gas phase oxidation process of a C4-compound to generate an aqueous (meth)acrylic acid solution g) Separation of the (meth)acrylic acid from the aqueous (meth)acrylic acid solution to obtain crude (meth)acrylic acid h) Rectification of the crude (meth)acrylic acid to obtain pure (meth)acrylic acid via a sidestream outlet of the rectification column i) Treatment of the pure (meth)acrylic acid generated in step c) with an ion exchange resin j) Distillation of the (meth)acrylic acid generated in step d).
1. A process for preparing highly pure, non-yellowing (meth)acrylic acid, comprising:
a) condensing a (meth)acrylic acid-containing gas phase obtained via a gas phase oxidation process of a C4-compound to generate an aqueous (meth)acrylic acid solution;
b) separating the (meth)acrylic acid from the aqueous (meth)acrylic acid solution to obtain crude (meth)acrylic acid;
c) rectifying the crude (meth)acrylic acid in a rectification column to obtain pure (meth)acrylic acid via a sidestream outlet of the rectification column;
d) treating the pure (meth)acrylic acid generated in c) with an ion exchange resin; and
e) distilling the (meth)acrylic acid generated in d).
2. The process of claim 1 , wherein b) comprises extracting the aqueous (meth)acrylic acid solution via an organic solvent followed by a thermal separation process to obtain the crude (meth)acrylic acid.
3. The process of claim 1 , wherein the crude (meth)acrylic acid introduced into c) exhibits an APHA value according to DIN ISO 6271 of 100-250.
4. The process of claim 1 , wherein in c) the amount of pure (meth)acrylic acid removed via the sidestream outlet in a defined time interval is 40-80% of the amount of crude (meth)acrylic acid introduced into the rectification column in the same time interval.
5. The process of claim 1 , wherein the ion exchange resin is dried prior to use.
6. The process of claim 1 , wherein d) is carried out continuously.
7. The process of claim 1 , wherein the treating in d) is carried out at a temperature of 30-100° C.
8. The process of claim 1 , wherein a weight ratio of ion-exchange resin to pure (meth)acrylic acid is 0.1-10%.
9. The process of claim 1 , wherein a residence time of pure (meth)acrylic acid within d) is 1-100 min.