Methods for recovering acrylic acid

• US 6,252,110 B1
• Filed: 06/25/1998
• Issued: 06/26/2001
• Est. Priority Date: 06/25/1997
• Status: Expired due to Term

• Current Assignee: Nippon Shokubai Company Limited
• Original Assignee: Nippon Shokubai Company Limited
• Inventors: Takeda, Takahiro, Uemura, Masahiro, Ueoka, Masatoshi
• Primary Examiner(s): Shaver, Paul F.
• Application Number:
  US09/104,358
• Time in Patent Office: 1,097 Days
• Field of Search: 562/600, 562/598, 203/39, 203/75, 203/DIG.21
• US Class Current: 562/598
• CPC Class Codes: B01D 3/148 in combination with at least one evaporator
• CPC Class Codes: C07C 51/44 by distillation
• CPC Class Codes: C07C 51/487 by treatment giving rise to chemical modification by chemisorption C07C51/47
• CPC Class Codes: C07C 57/04 Acrylic acid; Methacrylic acid
• CPC Class Codes: Y10S 203/22 Accessories

Abstract

A method for recovering acrylic acid from high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid at high efficiency with stability which includes the steps of (1) introducing said high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid into an acrylic acid recovery column, distilling acrylic acid from the column top and recovering the same, (2) introducing bottom liquid A from said acrylic acid recovery column into a pyrolyzing tank to decompose the acrylic acid dimer in the bottom liquid A, and (3) recirculating at least a part of bottom liquid B from said pyrolyzing tank into the acrylic acid recovery column.

Claims

1. A method for recovering acrylic acid from high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid,

wherein the high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid is a bottom liquid obtained from a high boiling impurities separation column used in the process comprising contacting an acrylic acid-containing gas resulting from gas-phase catalytic oxidation of propylene and/or acrolein with water to trap the acrylic acid in the form of an aqueous acrylic acid solution, distilling the aqueous solution in an azeotropic separation column in the presence of an azeotropic solvent, and purifying the resultant crude acrylic acid obtained from the bottom part of said azeotropic separation column in said high boiling impurities separation column,

by a process which comprises

(1) introducing said high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid, into an acrylic acid recovery column and recovering acrylic acid as it is distilled off from the top of the column,

(2) introducing bottom liquid A from said acrylic acid recovery column into a pyrolyzing tank to decompose the acrylic acid dimer in the bottom liquid A, and then,

(3) recirculating at least a part of bottom liquid B from said pyrolyzing tank into the acrylic acid recovery column.

2. A method according to claim 1 in which the acrylic acid recovery column is a distillation column equipped with a thin film vaporizer.

3. A method according to claim 1 in which the pyrolyzing temperature is 120 to 220°

C.

4. A method according to claim 1, 2 or 3, in which the recirculated amount of the bottom liquid B from the pyrolyzing tank is 1 to 20 times that of the high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid.

6. A method according to claim 2 in which the pyrolyzing temperature is 120 to 220°

C.

5. A method for recovering acrylic acid from an acrylic acid recovery process comprising contacting an acrylic acid-containing gas obtained through gas-phase catalytic oxidation of propylene and/or acrolein with water to trap the acrylic acid in the form of its aqueous solution, distilling said aqueous acrylic acid solution in an azeotropic separation column in the presence of an azeotropic solvent, and purifying the crude acrylic acid obtained from the bottom part of said azeotropic separation column in a high boiling impurities separation column,

which method comprises recovering acrylic acid from said high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid as obtained from the bottom part of the high boiling impurities separation column, and

(1) introducing said high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid into an acrylic acid recovery column composed of a distillation column equipped with a thin film vaporizer, wherein conducting distillation under conditions of 10 to 100 mmHg and at the bottom temperature of the column of 60 to 120°

C., distilling acrylic acid off from the column top and recovering the same;

(2) introducing bottom liquid A from said thin film vaporizer into a pyrolyzing tank, whereat decomposing acrylic acid dimer in said bottom liquid A at temperatures of 120 to 220°

C.; and

thereafter

(3) recirculating at least a part of bottom liquid B of said pyrolyzing tank into said distillation column and/or thin film vaporizer, at a ratio of 1 to 20 times in volume to the high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid.

7. A method for recovering acrylic acid which consists essentially of recovering acrylic acid from high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid obtained from the bottom part of a high boiling impurities separation column, and

(1) introducing said high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid into an acrylic acid recovery column composed of a distillation column equipped with a thin film vaporizer, wherein conducting distillation under conditions of 10 to 100 mmHg and at the bottom temperature of the column of 60 to 120°

C., distilling acrylic acid off from the column top and recovering the same;

(2) introducing bottom liquid A from said thin film vaporizer into a pyrolyzing tank, whereat decomposing acrylic acid dimer in said bottom liquid A at temperatures of 120 to 220°

C.; and

thereafter

(3) recirculating at least a part of bottom liquid B of said pyrolyzing tank into said distillation column and/or thin vaporizer, at a ratio of 1 to 20 times in volume to the high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid.

8. A method for recovering acrylic acid from high boiling impurities containing acrylic acid diner, acrylic acid and maleic acid,

wherein the high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid is a bottom liquid obtained from a high boiling impurities separation column used in the process comprising contacting an acrylic acid-containing gas resulting from gas-phase catalytic oxidation of propylene and/or acrolein with water to trap the acrylic acid in the form of an aqueous acrylic acid solution, distilling the aqueous solution in an azeotropic separation column in the presence of an azeotropic solvent, and purifying the resultant crude acrylic acid obtained from the bottom part of said azeotropic separation column in said high boiling impurities separation column,

by a process which comprises

(1) introducing said high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid, into an acrylic acid recovery column operated under reduced pressure and at temperatures at the bottom part of the column ranging from 60 to 120°

C. and recovering acrylic acid as it is distilled off from the top of the column,

(2) introducing bottom liquid A from said acrylic acid recovery column into a pyrolyzing tank to decompose the acrylic acid dimer in the bottom liquid A, and then,

(3) recirculating at least a part of bottom liquid B from said pyrolyzing tank into the acrylic acid recovery column.

9. A method according to claim 8 in which the acrylic acid recovery column is a distillation column equipped with a thin film vaporizer.

10. A method according to claim 8 in which the pyrolyzing temperature is 120 to 220°

C.