Process for purification of anhydrous hydrogen chloride gas

• US 6,719,957 B2
• Filed: 04/17/2002
• Issued: 04/13/2004
• Est. Priority Date: 04/17/2002
• Status: Expired due to Term

• Current Assignee: Covestro LLC (Covestro AG)
• Original Assignee: Bayer AG, Bayer Corporation (Bayer AG)
• Inventors: Weymans, Guenther, Brady, Bill L. Jr., Steffens, Friedhelm, Keggenhoff, Berthold
• Primary Examiner(s): NGUYEN, NGOC YEN M
• Application Number:
  US10/124,795
• Publication Number:
  US 20030196764A1
• Time in Patent Office: 727 Days
• Field of Search: 423/488, 423/240.R, 423/245.1, 423/481
• US Class Current: 423/488
• CPC Class Codes: B01D 53/002 by condensation
• CPC Class Codes: C01B 7/0706 of hydrogen chloride

Abstract

High boiling contaminants such as chloro-aromatic compounds are removed from a gas by compressing the gas containing the contaminant, cooling the compressed gas to reduce the temperature of the gas to at least 20° C. above the outlet temperature of a second cooling stage but above the freezing point of the highest melting compound in the first cooling stage, further cooling the gas in a second cooling stage to at least −20° C., returning cooled gas from the second cooling stage to the first cooling stage, and recovering condensate streams which contain the contaminant compound from the first and second cooling stages. An apparatus suitable for carrying out this process is also disclosed. The process of the present invention is particularly useful for removing chloro-aromatic compounds from anhydrous hydrogen chloride gas.

Claims

1. A process for the purification of hydrogen chloride gas containing contaminants having a boiling point higher than 100°

C. comprising

a) compressing hydrogen chloride gas containing a contaminant,

b) feeding the compressed hydrogen chloride gas to a first cooling stage in which the temperature of the compressed gas is reduced to at least 20°

C. above that of a second cooling stage, thereby generating a first condensate stream and a cooled hydrogen chloride gas stream,

c) feeding the cooled hydrogen chloride gas stream from the first cooling stage to a second cooling stage in which the temperature of the feed is reduced to at least −

20°

C., thereby generating a second condensate stream and a second cooled hydrogen chloride gas stream,

d) returning the second cooled hydrogen chloride gas stream to the first cooling stage as cooling medium, and

e) removing the first and second condensate streams.

2. The process of claim 1 in which the contaminant to be removed from the hydrogen chloride gas is a chlorinated aromatic compound.

3. The process of claim 2 in which the hydrogen chloride gas containing a chlorinated aromatic compound is compressed from a pressure of from 1 to 5 bar absolute to a pressure of from 8 to 20 bar absolute in step a).

4. The process of claim 2 in which the temperature of the compressed gas is reduced to a temperature of from 0 to −

20°

C. in the first cooling stage.

5. The process of claim 4 in which the temperature of the gas feed is reduced to a temperature of from −

15 to −

30°

C. in the second cooling stage.

6. The process of claim 2 in which the temperature of the gas feed is reduced to a temperature of from −

15 to −

30°

C. in the second cooling stage.

7. The process of claim 1 in which the condensates from the first and second cooling stages are combined.

8. The process of claim 1 in which in which the condensates from the first and second cooling stages are transferred to an evaporating stage in which from 50 to 95% by weight of the condensate is evaporated.

9. The process of claim 8 in which evaporated condensate is fed to the second cooling stage at its upstream side.

10. The process of claim 8 in which the condensate from the evaporating stage is transferred to a vessel in which from 10-30% by weight of the condensate is evaporated.

11. The process of claim 1 in which the condensate from the second cooling stage is transferred to a vessel at a pressure of from 1 to 5 bar absolute where it is heated to evaporate from 50 to 95% by weight of the condensate.

12. The process of claim 8 in which the evaporated condensate is fed to a compressor on its suction side.

13. The process of claim 8 in which any liquid remaining after evaporation is removed from the vessel and disposed of.

14. The process of claim 2 in which o-dichlorobenzene and/or mono-chlorobenzene are the contaminants to be removed.