Process for purifying aniline from gas phase hydrogenations

Patent metadata

Field	Value
Publication number	US-9233910-B2
Application number	US-201113878190-A
Country	US
Kind code	B2
Filing date	Oct 17, 2011
Priority date	Oct 21, 2010
Publication date	Jan 12, 2016
Grant date	Jan 12, 2016

Abstract

The invention relates to a process for purifying aniline produced by gas-phase hydrogenation of nitrobenzene, by fractional condensation of the crude reaction product obtained in gaseous form so that at least two liquid process products, a partial condensate (PK) and a total condensate (TK), are obtained.

First claim

The invention claimed is:

1. A process for producing aniline by gas-phase hydrogenation of nitrobenzene and subsequent purification of the aniline, comprising:
obtaining a gaseous crude reaction product, which is subjected to fractional condensation such that at least two liquid process products are obtained, wherein the at least two liquid process products include at least one partial condensate (PK) and a total condensate (TK),
carrying out a condensation leading to the formation of PK at a temperature that is higher than the condensation temperature leading to the formation of TK,
passing a product stream originating from PK and a product stream originating from TK into a distillation column comprising at least two sections, comprising at least one stripping section and at least one rectifying section,
introducing the product stream originating from PK into a lower section of the distillation column between a lowermost stripping section and a section which follows, and introducing the product stream originating from TK into a top portion of the distillation column above an uppermost rectifying section, and
withdrawing distilled aniline in a side stream between the lowermost stripping section and the uppermost rectifying section of the distillation column.

2. The process according to claim 1 , wherein:
the condensation leading to the formation of PK is carried out at a temperature from 60° C. to 160° C., and
the condensation leading to the formation of TK is carried out at a temperature from 25° C. to 90° C.

3. The process according to claim 2 , wherein:
product stream originating from PK is a partial condensate obtained in fractional condensation, and
product stream originating from TK is an organic phase which is obtained by phase separation of TK and/or a process product comprising TK into an aqueous phase and an organic phase.

4. The process according to claim 2 , wherein:
product stream originating from PK is an organic phase which is obtained after mixing PK and/or a process product comprising PK with aqueous base solution and subsequent phase separation into an aqueous phase and an organic phase, and
product stream originating from TK is an organic phase which is obtained after mixing TK and/or a process product comprising TK with aqueous base solution and subsequent phase separation into an aqueous phase and an organic phase.

5. The process according to claim 1 , wherein:
product stream originating from PK is a partial condensate obtained in a fractional condensation, and
product stream originating from TK is an organic phase which is obtained by phase separation of TK and/or a process product comprising TK into an aqueous phase and an organic phase.

6. The process according to claim 5 , wherein aniline withdrawn from the distillation column in a side stream is mixed with aqueous base solution, and an aniline depleted of acidic impurities is obtained by phase separation.

7. The process according to claim 1 , wherein:
product stream originating from PK is an organic phase which is obtained after mixing PK and/or a process product comprising PK with aqueous base solution and subsequent phase separation into an aqueous phase and an organic phase, and
product stream originating from TK is an organic phase which is obtained after mixing TK and/or a process product comprising TK with aqueous base solution and subsequent phase separation into an aqueous phase and an organic phase.

8. The process according to claim 7 , wherein:
PK and/or the process product comprising PK is mixed, before, during and/or after mixing with aqueous base solution, in a single- or multi-stage process with water and/or with a stream A comprising at least 50% by mass water, based on the total mass of stream A.

9. The process according to claim 8 , wherein:
stream A comprising at least 50% by mass water is an aqueous phase which is obtained after mixing TK and/or a process product comprising TK with aqueous base solution and subsequent phase separation into an aqueous phase and an organic phase.

10. The process according to claim 7 , wherein:
the organic phase obtained after mixing TK and/or a process product comprising TK with aqueous base solution and subsequent phase separation is washed in a single- or multi-stage process with water and/or with a stream B comprising at least 50% by mass water, based on the total mass of stream B.

11. The process according to claim 10 , wherein:
stream B comprising at least 50% by mass water is a liquid condensate stream of gas phase removed at a top portion of the distillation column and/or a process product comprising a liquid condensate stream of gas phase removed at the top portion of the distillation column.

12. The process according to claim 11 , wherein
the process product comprising the liquid condensate stream of the gas phase removed at the top portion of the distillation column is obtained
by adding an aniline-water azeotropic mixture,
obtained by introducing into a water stripper an aqueous phase obtained by phase separation after mixing PK and/or a process product comprising PK with aqueous base solution,
to total condensate of gas phase removed at a top portion of the distillation column.

13. The process according to claim 7 , wherein:
TK and/or process product comprising TK is mixed, before, during and/or after mixing with aqueous base solution, in a single- or multi-stage process with water and/or with a stream B comprising at least 50% by mass water, based on the total mass of stream B.

14. The process according to claim 13 , wherein
stream B comprising at least 50% by mass water is a process product comprising liquid condensate stream of gas phase removed at a top portion of the distillation column.

15. The process according to claim 14 , wherein:
the process product comprising the liquid condensate stream of the gas phase removed at the top portion of the distillation column is obtained
by adding an aniline-water azeotropic mixture,
obtained by introducing into a water stripper an aqueous phase obtained by phase separation after mixing PK and/or a process product comprising PK with aqueous base solution,

to total condensate of gas phase removed at a top portion of the distillation column.

16. The process according to claim 7 , wherein the aqueous base solution comprises a solution of an alkali metal hydroxide and/or alkaline earth metal hydroxide.

Assignees

• Lehner Peter
• Sommer Knut
• Moussa Amgad Salah
• Bayer Ip Gmbh

Inventors

• Lehner Peter
• Sommer Knut
• Moussa Amgad Salah

Classifications

• C07C209/86 Primary

  Separation · CPC title

• C07C209/84 Primary

  Purification · CPC title

• C07C211/46

  Aniline · CPC title