Process and apparatus for purification of acrylic acid

Patent metadata

Field	Value
Publication number	US-10213706-B2
Application number	US-201515520038-A
Country	US
Kind code	B2
Filing date	Jul 30, 2015
Priority date	Oct 24, 2014
Publication date	Feb 26, 2019
Grant date	Feb 26, 2019

Abstract

A process and an apparatus for the purification of a crude acrylic acid composition containing maleic anhydride as an impurity comprising the following steps: (a) carrying out at least one dynamic melt crystallization stage (14, 14a, 14b, 14c, 14d) with the crude acrylic acid composition to prepare a first purified acrylic acid composition and a first residue containing at least 3.5% by weight maleic anhydride, (b) adding a solvent (26) which is capable of dissolving maleic anhydride to the first residue in an amount that the weight ratio of the solvent to the maleic anhydride is 0.3 or more to prepare a ratio-adjusted residue and (c) carrying out at least one further dynamic melt crystallization stage and/or at least one static melt crystallization stage (18, 18a, 18b) with the ratio-adjusted residue to prepare a second purified acrylic acid composition and a second residue.

First claim

The invention claimed is:

1. An apparatus ( 10 ) for the purification of a crude acrylic acid composition containing maleic anhydride as an impurity being configured for carrying out a melt crystallization process comprising the steps of:
(a) carrying out at least one dynamic melt crystallization stage ( 14 , 14 a , 14 b , 14 c , 14 d ) with the crude acrylic acid composition to prepare a first purified acrylic acid composition and a first residue containing at least 3.5% by weight maleic anhydride,
(b) adding a solvent ( 26 ) which is capable of dissolving maleic anhydride to the first residue in an amount that the weight ratio of the solvent to the maleic anhydride is 0.3 or more to prepare a ratio-adjusted residue, and
(c) carrying out at least one further dynamic melt crystallization stage and/or at least one static melt crystallization stage ( 18 , 18 a , 18 b ) with the ratio-adjusted residue to prepare a second purified acrylic acid composition and a second residue,
wherein the apparatus ( 10 ) comprises:
a first melt crystallization section ( 12 ) for (a) carrying out at least one dynamic melt crystallization stage ( 14 , 14 a , 14 b , 14 c , 14 d ) with the crude acrylic acid composition to prepare a first purified acrylic acid composition and a first residue, wherein the first melt crystallization section ( 12 ) has an inlet for the crude acrylic acid composition, an outlet for the first purified acrylic acid composition and an outlet for the first residue, wherein the outlet for the first purified acrylic acid composition and the outlet for the first residue may be the same,
means ( 26 ) for (b) adding a solvent to the first residue and for adjusting a predetermined weight ratio of the solvent to the first residue to prepare a ratio-adjusted residue and
a second melt crystallization section ( 16 ) for (c) carrying out at least one further dynamic melt crystallization stage or at least one static melt crystallization stage ( 18 , 18 a , 18 b ) with the first residue to prepare a second purified acrylic acid composition and a second residue, wherein the second melt crystallization section ( 16 ) has an inlet being arranged downstream of the means ( 26 ) for introducing the solvent to the first residue and the inlet being in fluid communication with the outlet for the first purified acrylic acid composition.

2. The apparatus ( 10 ) of claim 1 , wherein the at least one dynamic melt crystallizer ( 14 ) is a falling film crystallizer.

3. The apparatus ( 10 ) of claim 1 , wherein the means ( 26 ) for introducing the solvent comprise a piping for supplying the solvent, a control valve and a flow meter.

4. The apparatus ( 10 ) of claim 1 , wherein the apparatus ( 10 ) does not comprise any separation means for separating a precipitated maleic anhydride from the crude acrylic acid composition or from the first residue.

5. A process for the purification of a crude acrylic acid composition containing maleic anhydride as an impurity, the process comprising the steps of:
(a) carrying out at least one dynamic melt crystallization stage ( 14 , 14 a , 14 b , 14 c , 14 d ) with the crude acrylic acid composition to prepare a first purified acrylic acid composition and a first residue containing at least 3.5% by weight maleic anhydride,
(b) adding a solvent ( 26 ) which is capable of dissolving maleic anhydride to the first residue in an amount that the weight ratio of the solvent to the maleic anhydride is 0.3 or more to prepare a ratio-adjusted residue and
(c) carrying out at least one further dynamic melt crystallization stage and/or at least one static melt crystallization stage ( 18 , 18 a , 18 b ) with the ratio-adjusted residue to prepare a second purified acrylic acid composition and a second residue,

wherein at least one of steps (a), (b), or (c) is performed in the apparatus of claim 1 .

6. The process of claim 5 , wherein the concentration of maleic anhydride in the first residue prepared in step (a) is at least 4% by weight based on 100% by weight of the first residue.

7. The process of claim 5 , wherein the weight ratio of the solvent to the maleic anhydride in step (b) is adjusted to a range of from 0.3 to 2.0.

8. The process of claim 5 , wherein the solvent is water.

9. The process of claim 5 , wherein the second purified acrylic acid composition obtained in step (c) ( 18 , 18 a , 18 b ) is at least partially recycled ( 30 ) to the dynamic melt crystallization of step (a) ( 14 , 14 a , 14 b , 14 c , 14 d ).

10. The process of claim 5 , wherein two to four dynamic melt crystallization stages ( 14 a , 14 b , 14 c , 14 d ) are used to prepare the first purified acrylic acid composition and the first residue in step (a) and wherein one to three static melt crystallization stages ( 18 a , 18 b ) are carried out with the ratio-adjusted residue in step (c).

11. The process of claim 10 , wherein at least one of the dynamic melt crystallization stages ( 14 a , 14 b , 14 c , 14 d ) of step (a) is carried out as falling film crystallization.

12. The process of claim 5 , wherein the crude acrylic acid composition is produced from propylene.

13. The process of claim 5 , wherein the crude acrylic acid composition is obtained by a synthesis process comprising at least one fermentation step.

14. The process of claim 5 , wherein no additional solvent is added to the crude acrylic acid composition before it is subjected to step (a).

15. The process of claim 5 , wherein in steps (a) to (c) no separation of a precipitated maleic anhydride by a separation means from the crude acrylic acid composition or from the first residue is conducted.

Assignees

• Sulzer Chemtech Ag

Inventors

• Schäfer Matthias
• Kuszlik Andrzej
• Lippuner Florian
• Engstler Herbert

Classifications

• B01D9/00

  Crystallisation (crystallisation directly from the vapour phase B01D7/02; making single crystals C30B {; crystallisation as part of the Bayer process also classified in C01F7/14}) · CPC title

• C07C57/04

  Acrylic acid; Methacrylic acid · CPC title

• C07C51/43 Primary

  by change of the physical state, e.g. crystallisation · CPC title

• B01D9/0059 Primary

  General arrangements of crystallisation plant, e.g. flow sheets · CPC title