IP Library › Granted Patent US 12,441,676
Granted Patent B2
US 12,441,676 · App. 17/923,885 · Granted Oct 14, 2025

Process for preparing acrylic acid

Inventors: Hyebin Kim (Daejeon, KR); Mi Kyung Kim (Daejeon, KR); Eunkyo Kim (Daejeon, KR); Joon Ho Shin (Daejeon, KR)
Assignee: LG Chem, Ltd.
C07C57/04
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Quick Facts
Patent No.
US 12,441,676
App. No.
17/923,885
Granted
Oct 14, 2025
Kind
B2
Abstract

The present application relates to a process for producing acrylic acid.

Claims (22)

1. A process for producing acrylic acid, the process comprising:

(1) separating a first low-boiling-point material including acetaldehyde (ACHO) and a first high-boiling-point material including acrylic acid (AA) by cooling a reaction product of a bio-raw material;

(2) separating a condensed second low-boiling-point material including acetaldehyde (ACHO) and a second high-boiling-point material including acrylic acid (AA) by compressing the first low-boiling-point material including acetaldehyde (ACHO);

(3) separating a first incompressible material and a third low-boiling-point material including acetaldehyde (ACHO) by adding a second absorbent to the condensed second low-boiling-point material including acetaldehyde (ACHO) and cooling thereof; and

(4) purifying the first high-boiling-point material including acrylic acid (AA) to obtain acrylic acid.

2. The process for producing acrylic acid of claim 1 , further comprising a process of adding a first absorbent during cooling the reaction product of the bio-raw material of the step (1).

3. The process for producing acrylic acid of claim 2 , wherein the first absorbent comprises a material having a boiling point difference of 20° C. or higher compared to a normal boiling point (NBP) of the acrylic acid (AA) and a boiling point difference of 50° C. or higher compared to a normal boiling point (NBP) of the acetaldehyde (ACHO).

4. The process for producing acrylic acid of claim 1 , wherein the second absorbent comprises a material having a boiling point which is 20° C. or higher than a normal boiling point (NBP) of the acetaldehyde (ACHO).

5. The process for producing acrylic acid of claim 1 , wherein the step (1) is performed by using a cooling tower; and

wherein the cooling tower has a cooling temperature of higher than or equal to 10° C. and lower than or equal to 150° C. and an inner pressure of greater than or equal to 0.5 bar and less than or equal to 5.0 bar.

6. The process for producing acrylic acid of claim 2 , wherein the first absorbent is included in an amount to make the acrylic acid (AA) included in the first low-boiling-point material of the step (1) to be 1 parts by weight or less with respect to 100 parts by weight of acrylic acid included in the reaction product of the bio-raw material.

7. The process for producing acrylic acid of claim 1 , wherein the step (3) is performed by using an absorption tower; and

wherein the absorption tower has a temperature of higher than or equal to 0° C. and lower than or equal to 150° C. and an inner pressure of greater than or equal to 0.5 bar and less than or equal to 10.0 bar.

8. The process for producing acrylic acid of claim 1 , wherein the second absorbent is included in an amount to make the acetaldehyde (ACHO) included in the first incompressible material of the step (3) to be 1 parts by weight or less with respect to 100 parts by weight of acetaldehyde included in the reaction product of the bio-raw material.

9. The process for producing acrylic acid of claim 1 , further comprising a step of circulating the second high-boiling-point material including acrylic acid (AA) of the step (2) to the step (1).

10. The process for producing acrylic acid of claim 1 , wherein the step (2) is performed by using a compressor; and

wherein the compressor has a discharge pressure of greater than or equal to 1.2 bar and less than or equal to 10.0 bar.

11. The process for producing acrylic acid of claim 1 , further comprising a step of separating the third low-boiling-point material including acetaldehyde (ACHO) into acetaldehyde and the second absorbent.

12. The process for producing acrylic acid of claim 11 , wherein the step of separating the third low-boiling-point material is performed by using a separation tower; and

wherein the separation tower has a temperature of higher than or equal to 10° C. and lower than or equal to 200° C. and an inner pressure of greater than or equal to 0.3 bar and less than or equal to 10.0 bar.

13. The process for producing acrylic acid of claim 1 , wherein the second absorbent has a temperature of higher than or equal to −5° C. and lower than or equal to 20° C.

14. The process for producing acrylic acid of claim 11 , wherein purity of the acetaldehyde is 95% or greater, and a recovery rate thereof based on the reaction product of the bio-raw material is 95% or greater.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 7, 2022
From: KIM, HYEBIN; KIM, MI KYUNG; KIM, EUNKYO; SHIN, JOON HO
To: LG CHEM, LTD.
Reel/Frame 061680/0832 →
Priority Claims (1)
KR 10-2020-0167623 · Dec 3, 2020 · national
Continuity (1)
Related Publication 20230271914A1 · Aug 31, 2023
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