Method of recovering (meth)acrylic acid
The present invention relates to a method of recovering (meth)acrylic acid and an apparatus used for the recovery method. The recovery method according to the present invention discharges each (meth)acrylic acid aqueous solution of different concentrations at a (meth)acrylic acid absorption tower, and uses an extraction solvent of a specific ratio in the step of extracting (meth)acrylic acid, thus enabling the operation of a continuous process of recovering (meth)acrylic acid that can secure a high (meth)acrylic acid recovery rate, and can simultaneously significantly reduce purification energy cost.
1. A method of recovering (meth)acrylic acid comprising the steps of:
A) contacting a mixed gas comprising (meth)acrylic acid, organic byproducts, and water vapor with water in a (meth)acrylic acid absorption tower to form an aqueous solution of (meth)acrylic acid;
B) discharging the (meth)acrylic acid aqueous solution of a first concentration, to the side part of the (meth)acrylic acid absorption tower;
C) discharging the (meth)acrylic acid aqueous solution of a second concentration, to the lowest part of the (meth)acrylic acid absorption tower;
B-1) contacting the (meth)acrylic acid aqueous solution of the first concentration discharged to the side part with an extraction solvent comprising a hydrophobic organic solvent in the (meth)acrylic acid extraction tower, to extract (meth)acrylic acid; and
D) distilling the (meth)acrylic acid extract obtained in step B-1) and the (meth)acrylic acid aqueous solution of the second concentration discharged in step C), through an azeotropic distillation process, to obtain (meth)acrylic acid,
wherein the first concentration has a lower (meth)acrylic acid concentration than the second concentration,
and the following Mathematical Formula 1 is satisfied:
Y 1= a×X 1 [Mathematical Formula 1]
wherein, in Mathematical Formula 1,
Y1 is an amount of the extraction solvent used in step B-1),
a is a ratio of the extraction solvent, and is equal to or greater than 2.5, and
X1 is an amount of water included in the (meth)acrylic acid aqueous solution of the first concentration.
2. The method of recovering (meth)acrylic acid according to claim 1 , wherein the (meth)acrylic acid aqueous solution of the first concentration is discharged at a point corresponding to the height of 40 to 99% from the highest part of the (meth)acrylic acid absorption tower to the lower position.
3. The method of recovering (meth)acrylic acid according to claim 1 , wherein the step of forming the (meth)acrylic acid aqueous solution is progressed under pressure of 1 to 1.5 bar and a temperature of 50 to 100° C.
4. The method of recovering (meth)acrylic acid according to claim 1 , wherein the (meth)acrylic acid aqueous solution of the first concentration comprises 40 wt % or less of (meth)acrylic acid.
5. The method of recovering (meth)acrylic acid according to claim 1 , wherein the (meth)acrylic acid aqueous solution of the second concentration comprises 60 wt % or more of (meth)acrylic acid.
6. The method of recovering (meth)acrylic acid according to claim 1 , wherein the (meth)acrylic acid aqueous solution of the first concentration discharged to the side part is discharged at a rate of 10 wt % to 50 wt %, based on the (meth)acrylic acid aqueous solution of the second concentration discharged to the lowest part.
7. The method of recovering (meth)acrylic acid according to claim 1 , wherein the following Mathematical Formula 2 is satisfied:
0.01≤ X 1/( X 1+ X 2)≤0.7 [Mathematical Formula 2]
wherein, in Mathematical Formula 2,
X1 is an amount of water in the (meth)acrylic acid aqueous solution of the first concentration, and
X2 is an amount of water in the (meth)acrylic acid aqueous solution of the second concentration.
8. The method of recovering (meth)acrylic acid according to claim 1 , wherein the following Mathematical Formula 3 is satisfied:
Y=b×X 2 [Mathematical Formula 3]
wherein, in Mathematical Formula 3,
Y is an amount of an azeotropic solvent used in step D),
b is an azeotropic ratio, and
X2 is an amount of water included in the (meth)acrylic acid aqueous solution of the second concentration.
9. The method of recovering (meth)acrylic acid according to claim 1 , wherein the extraction solvent used in step B-1) and the azeotropic solvent used in step D) are identical to each other, and the following Mathematical Formulas 4 and 5 are satisfied:
Y=Y 1+ Y 2 [Mathematical Formula 4]
Y 2> Y 1 [Mathematical Formula 5]
wherein, in Mathematical Formulas 4 and 5,
Y is the total amount of the azeotropic solvent used in step D),
Y1 is the amount of the extraction solvent used in step B-1), and
Y2 is the amount of the azeotropic solvent added in step D).