IP Library Granted Patent US 7,041,849
Granted Patent B2
US 7,041,849 · App. 10/845,571 · Granted May 9, 2006

Method of recovering polymerization inhibitor and method of producing acrylic acid

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Quick Facts
Patent No.
US 7,041,849
App. No.
10/845,571
Granted
May 9, 2006
Kind
B2
Abstract

In an acrylic acid production process which comprises the step of producing acrylic acid by catalytic vapor-phase oxidation of propane, propylene, and/or acrolein; and purifying the acrylic acid produced in the step of producing with distillation in the presence of the polymerization inhibitor for preventing polymerization of the acrylic acid, a viscosity at 20° C. of the bottoms which comprises the polymerization inhibitor, discharged in the step of purifying, is adjusted to 2 Pa·s (2,000 cP) or less and the polymerization inhibitor is extracted using an aqueous medium. According to the method, in an acrylic acid production process, an extraction operation for recovery of the polymerization inhibitor can be continuously conducted in a stable manner.

Claims (29)

1. A method of recovering a polymerization inhibitor from a liquid that comprises the polymerization inhibitor,

the liquid being discharged in an acrylic acid production process,

the acrylic acid producing process comprising the steps of: producing acrylic acid by catalytic vapor-phase oxidation of propane, propylene, and/or acrolein; and purifying the acrylic acid produced in the step of producing with distillation in the presence of the polymerization inhibitor for preventing polymerization of the acrylic acid,

the liquid being a residue discharged in the step of purifying,

wherein the method comprises the steps of:

adjusting a viscosity at 20° C. of the liquid to 2Pa·s (2,000 cP) or less; and

extracting the polymerization inhibitor from the liquid by using an aqueous medium.

2. The method according to claim 1 , wherein the method further comprises the step of heating the liquid before extracting the polymerization inhibitor from the liquid by using the aqueous medium.

3. The method according to claim 1 , wherein the method further comprises the step of volatilizing at least a part of a volatile substance in an aqueous solution comprising the polymerization inhibitor obtained by extraction by heating and/or decompressing the aqueous solution.

4. The method according to claim 2 , wherein the method further comprises the step of volatilizing at least a part of a volatile substance in an aqueous solution comprising the polymerization inhibitor obtained by extraction by heating and/or decompressing the aqueous solution.

5. The method according to claim 3 , wherein the method further comprises the step of heating a liquid after the volatilization of at least a part of the volatile substance in the presence of an acid catalyst, cooling the liquid after the heating, and subjecting the cooled liquid to solid-liquid separation.

6. The method according to claim 4 , wherein the method further comprises the step of heating a liquid after the volatilization of at least a part of the volatile substance in the presence of an acid catalyst, cooling the liquid after the heating, and subjecting the cooled liquid to solid-liquid separation.

7. The method according to claim 1 , wherein the method further comprises the step of recycling the polymerization inhibitor extracted by using the aqueous medium by sending the extracted inhibitor to the acrylic acid production process.

8. The method according to claim 2 , wherein the method further comprises the step of recycling the polymerization inhibitor extracted by using the aqueous medium by sending the extracted inhibitor to the acrylic acid production process.

9. The method according to claim 3 , wherein the method further comprises the step of recycling the polymerization inhibitor extracted by using the aqueous medium by sending the extracted inhibitor to the acrylic acid production process.

10. The method according to claim 4 , wherein the method further comprises the step of recycling the polymerization inhibitor extracted by using the aqueous medium by sending the extracted inhibitor to the acrylic acid production process.

11. The method according to claim 5 , wherein the method further comprises the step of recycling the polymerization inhibitor extracted by using the aqueous medium by sending the extracted inhibitor to the acrylic acid production process.

12. The method according to claim 6 , wherein the method further comprises the step of recycling the polymerization inhibitor extracted by using the aqueous medium by sending the extracted inhibitor to the acrylic acid production process.

13. The method according to claim 2 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

14. The method according to claim 3 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

15. The method according to claim 4 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

16. The method according to claim 5 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

17. The method according to claim 6 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

18. The method according to claim 7 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

19. The method according to claim 8 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

20. The method according to claim 9 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

21. The method according to claim 10 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

22. The method according to claim 11 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

23. The method according to claim 12 , wherein the heating of the liquid before the extraction of the polymerization inhibitor using the aqueous medium is for thermally decomposing an acrylic acid oligomer in the liquid.

Assignments (2)
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →
MERGER Recorded Sep 4, 2017
From: MITSUBISHI CHEMICAL CORPORATION
To: MITSUBISHI RAYON CO., LTD.
Reel/Frame 043750/0207 →