Process for producing (meth) acrylic acid compound
View Patent ↗A process for producing a (meth)acrylic acid compound, which comprises distilling acrylic acid, methacrylic acid (these will hereinafter generally be referred to as “(meth)acrylic acid”) or an ester thereof (these will hereinafter generally be referred to as “a (meth)acrylic acid compound”) in a distillation column to obtain a purified (meth)acrylic acid compound, characterized in that in the course of operation of the distillation column including suspension and resumption of the operation, the distillation column is washed with water and, thereafter, inside washing with an organic solvent and/or azeotropic distillation in the presence of the organic solvent is conducted. In some cases, washing with alkaline water may be added prior to the washing with water. Washing of the distillation column for separating and purifying a crude (meth)acrylic acid compound, can be carried out easily. In particular, in a process for producing a (meth)acrylic acid compound, a substance used in a step before or after the distillation column can be utilized to recover a valuable substance, and the distillation column can be efficiently cleaned.
1. A process for producing a (meth)acrylic acid compound, comprising:
distilling (meth)acrylic acid or an ester thereof in a distillation column to obtain a purified (meth)acrylic acid compound,
wherein in the course of operation of the distillation column including suspension and resumption of the operation, the distillation column is washed with water and, thereafter, inside washing with an organic solvent and/or azeotropic distillation in the presence of the organic solvent is conducted.
2. A process for producing (meth)acrylic acid, comprising:
subjecting propylene, propane or isobutylene to vapor phase catalytic oxidation to obtain an oxidized reaction mixture,
absorbing the oxidized reaction product in water to obtain an aqueous solution containing (meth)acrylic acid,
concentrating the aqueous solution in the presence of an azeotropic agent, and
distilling the obtained (meth)acrylic acid in a distillation column to obtain purified (meth)acrylic acid,
wherein in the course of operation of the distillation column including suspension and resumption of the operation, the distillation column is washed with water and, thereafter, azeotropic distillation is conducted in the presence of the azeotropic agent.
3. A process for producing (meth)acrylic acid, comprising:
subjecting propylene, propane or isobutylene to vapor phase catalytic oxidation to obtain an oxidized reaction mixture,
absorbing the oxidized reaction product in water to obtain an aqueous solution containing (meth)acrylic acid,
concentrating the aqueous solution in the presence of an azeotropic agent, and
distilling the obtained (meth)acrylic acid in a distillation column to obtain purified (meth)acrylic acid,
wherein in the course of operation of the distillation column including suspension and resumption of the operation, the distillation column is preliminarily washed with water, then, with alkaline water and with water and, thereafter, azeotropic distillation is conducted in the presence of the azeotropic agent.
4. The process according to claim 1 , wherein the organic solvent has a water content of at most 2 wt %.
5. The process according to claim 1 , wherein the organic solvent is a (meth)acrylic acid compound, methanol, ethanol, butanol, benzene, toluene, methyl ethyl ketone, methyl isobutyl ketone, methyl n-butyl ketone, isopropyl acetate, diphenyl ether, biphenyl or a mixture thereof.
6. The process according to claim 1 , wherein the azeotropic distillation is conducted at a column top temperature of from 20 to 80° C. under a column top pressure of from 0.5 to 120 kPa.
7. The process according to claim 1 , wherein the azeotropic distillation is conducted in the presence of a polymerization inhibitor.
8. A process for producing a (meth)acrylic acid ester, comprising:
subjecting propylene, propane or isobutylene to vapor phase catalytic oxidation to obtain an oxidized reaction mixture,
absorbing the oxidized reaction product in water to obtain an aqueous solution containing (meth)acrylic acid,
concentrating the aqueous solution in the presence of an azeotropic agent, and
purifying the obtained (meth)acrylic acid in a distillation column and then reacting it with an alcohol to obtain an ester, and purifying the ester in a distillation column to obtain a purified (meth)acrylic acid ester,
wherein in the course of operation of the distillation column including suspension and resumption of the operation, the distillation column is washed with water and, thereafter, inside washing with an organic solvent and/or azeotropic distillation in the presence of the organic solvent is conducted.
9. A process for producing a (meth)acrylic acid ester, comprising:
subjecting propylene, propane or isobutylene to vapor phase catalytic oxidation to obtain an oxidized reaction mixture,
absorbing the oxidized reaction product in water to obtain an aqueous solution containing (meth)acrylic acid,
concentrating the aqueous solution in the presence of an azeotropic agent, and
purifying the obtained (meth)acrylic acid in a distillation column and then reacting it with an alcohol to obtain an ester, and purifying the ester in a distillation column to obtain a purified (meth)acrylic acid ester,
wherein in the course of operation of the distillation column including suspension and resumption of the operation, the distillation column is preliminarily washed with water, then, with alkaline water and with water and, thereafter, azeotropic distillation is conducted in the presence of an organic solvent.
10. The process according to claim 2 , wherein the azeotropic distillation is conducted at a column top temperature of from 20 to 80° C. under a column top pressure of from 0.5 to 120 kPa.
11. The process according to claim 2 , wherein the azeotropic distillation is conducted in the presence of a polymerization inhibitor.
12. The process according to claim 3 , wherein the azeotropic distillation is conducted at a column top temperature of from 20 to 80° C. under a column top pressure of from 0.5 to 120 kPa.
13. The process according to claim 3 , wherein the azeotropic distillation is conducted in the presence of a polymerization inhibitor.