Removal of phosgene from off-gases

• US 5,200,163 A
• Filed: 10/30/1991
• Issued: 04/06/1993
• Est. Priority Date: 12/13/1990
• Status: Expired due to Term

• Current Assignee: BASF AG (BASF SE)
• Original Assignee: BASF AG (BASF SE)
• Inventors: Kahl, Thomas M., Henkelmann, Jochem, Schwarz, Wolfgang, Troetsch-Schaller, Irene, Franzischka, Wolfgang, Hupfer, Leopold
• Primary Examiner(s): Straub, Gary P.
• Assistant Examiner(s): LUND, VALERIE A
• Application Number:
  US07/785,288
• Time in Patent Office: 524 Days
• Field of Search: 423/240 R, 423/481, 423/488, 55/71
• US Class Current: 423/240.00R
• CPC Class Codes: B01D 53/70 Organic halogen compounds

Abstract

To remove phosgene from off-gases, the former is reacted in a washing zone with a liquid which contains or is composed of compounds of the formula ##STR1## where R₁ and R₂ are identical or different and are each aliphatic or cycloaliphatic alkyl of 1 to 8 carbons, or R₁ and R₂ are --(CH₂)_n -- where n is 4 or 5, R₃ is hydrogen or aliphatic or cycloaliphatic alkyl of 1 to 6 carbon atoms, or R₁ or R₂ and R₃ are --(CH₂)_m -- where m is 3, 4 or 5.

The liquid can be regenerated by the addition of water, and the regenerated liquid can be returned to the washing zone.

Claims

1. In a process for removing phosgene from off-gases by washing with a liquid, the improvement which comprises:

reacting the phosgene contained by the off-gas in a washing zone with a wash liquid which consists essentially of at least one compound of the formula ##STR9## where R₁ and R₂ are identical or different and are selected from the group consisting of alkyl of 1 to 8 carbons and cycloalkyl of 5 to 8 carbon atoms, or R₁ and R₂ when taken together may also represent --(CH₂)_n -- where n is 4 or 5, and R₃ is selected from the group consisting of hydrogen, alkyl of 1 to 6 carbon atoms and cycloalkyl of 5 to 6 carbon atoms, or R₁ or R₂ when taken individually together with R₃ may also represent --(CH₂)_m -- where m is 3, 4 or 5, to form a Vilsmeier salt; and

further reacting said salt with water to form an off gas containing HCl with the phosgene removed.

2. A process as claimed in claim 1, wherein the wash liquid is extracted from the washing zone, water is added to the wash liquid, and the extracted wash liquid is returned to the washing zone.

3. A process as claimed in claim 1, wherein said wash liquid contains an inert aprotic solvent.

4. A process as claimed in claim 1, wherein the washing treatment is carried out at a temperature of at least 20°

C. below the boiling point of the wash liquid.

5. A process as claimed in claim 1, wherein said washing zone includes a column in which the off-gas containing phosgene is introduced near the bottom end and the wash liquid is introduced at the top end of said column such that a phosgene-free off-gas is removed at the top end of said column, and wash liquid collected at the bottom of the column is recycled to the top end of the column to maintain the absorption of phosgene while preventing hydrolysis of the wash liquid.

6. A process as claimed in claim 5, wherein the amount of water added to the wash liquid is about 1 mol, plus any loss of water stripped from the wash liquid by the off-gas, per mol of phosgene washed out.

7. A process as claimed in claim 5, wherein the washing treatment is carried out at a temperature of at least 20°

C. below the boiling point of the wash liquid.