Method of reprocessing alkanesulfonic acid

Patent metadata

Field	Value
Publication number	US-10214485-B2
Application number	US-201615774722-A
Country	US
Kind code	B2
Filing date	Nov 8, 2016
Priority date	Nov 10, 2015
Publication date	Feb 26, 2019
Grant date	Feb 26, 2019

Abstract

The invention relates to a method of reprocessing alkanesulfonic acid employed in a chemical process as an agent, catalyst or solvent and comprising the steps of:
(a) removing an alkanesulfonic acid-comprising stream from a reaction mixture generated in the chemical process, (b) feeding the alkanesulfonic acid-comprising stream into a melt crystallization as the starting melt to form crystals of the alkanesulfonic acid, of hydrates of the alkanesulfonic acid or of a mixture of both suspended in mother liquor, (c) performing a solid-liquid separation to remove the crystals from the mother liquor, (d) optionally washing the crystals to remove mother liquor adhering to the crystals, (e) recycling the washed or unwashed crystals removed from the mother liquor into the chemical process.

First claim

The invention claimed is:

1. A method of reprocessing alkanesulfonic acid employed in a chemical process as an agent, catalyst or solvent, the method comprising:
(a) removing an alkanesulfonic acid-comprising stream from a reaction mixture generated in the chemical process,
(b) feeding the alkanesulfonic acid-comprising stream into a melt crystallization as a starting melt to form crystals of the alkanesulfonic acid, of hydrates of the alkanesulfonic acid or of a mixture of both suspended in a mother liquor,
(c) performing a solid-liquid separation to remove the crystals from the mother liquor,
(d) optionally washing the crystals to remove the mother liquor adhering to the crystals, and
(e) recycling the washed or unwashed crystals removed from the mother liquor into the chemical process.

2. The method according to claim 1 , wherein the reaction mixture in (a) is biphasic and the alkanesulfonic acid-comprising stream is removed from the reaction mixture by phase separation.

3. The method according to claim 1 , wherein the mother liquor after removal of the crystals in (c) and/or the mother liquor generated in (b) are at least partly recycled into the melt crystallization in (b).

4. The method according to claim 1 , wherein
the alkanesulfonic acid-comprising stream before being fed into the melt crystallization in (b) is distilled to remove low boilers,
the low boilers are drawn off at the top of a distillation column,
a material stream comprising the alkanesulfonic acid, high boilers and residual low boilers is withdrawn at the bottom of the distillation column, and
the stream comprising the alkanesulfonic acid, the high boilers and the residual low boilers is fed to the melt crystallization in (b).

5. The method according to claim 4 , wherein the mother liquor after removal of the crystals in (c) and/or the mother liquor generated in (b) are at least partly recycled into the melt crystallization or into the distillation column for removing low boilers.

6. The method according to claim 1 , wherein the crystals from (c) or from (d) are fed to a distillation for water removal.

7. The method according to claim 1 , wherein the mother liquor after removal of the crystals in (c) and/or the mother liquor generated in (b) are at least partly fed to a high boilers removal in which the alkanesulfonic acid is removed by evaporation.

8. The method according to claim 7 , wherein the alkanesulfonic acid removed by evaporation is recycled into the chemical process.

9. The method according to claim 8 , wherein the alkanesulfonic acid removed by evaporation is at least partially condensed before being recycled into the chemical process.

10. The method according to claim 7 , wherein
the mother liquor after removal of the high boilers is partially condensed to obtain a condensed portion and an uncondensed portion,
the condensed portion is recycled into a distillation for removing the low boilers or into the melt crystallization in (b), and
the uncondensed portion is discharged from the process as low boilers.

11. The method according to claim 1 , wherein the alkanesulfonic acid is methanesulfonic acid.

12. The method according to claim 1 , wherein the chemical process is an alkylation or an esterification reaction.

13. The method according to claim 1 , wherein the chemical process is an alkylation of salicylic acid or of substituted or unsubstituted aromatics.

14. The method according to claim 13 , wherein the chemical process is production of linear alkylbenzene from benzene or substituted benzene with an olefin in the presence of the alkanesulfonic acid as a catalyst.

15. The method according to claim 1 , wherein the melt crystallization is a suspension crystallization or a layer crystallization.

Assignees

• Basf Se

Inventors

• Spielmann Jan
• Koch Michael
• Wortmann Juergen
• Weiguny Sabine
• Ruether Feelly
• Sengpiel Robert

Classifications

• C07C303/44 Primary

  Separation; Purification · CPC title

• C07C309/04

  containing only one sulfo group · CPC title