Process for the reduction of carbochlorination residue

• US 5,569,440 A
• Filed: 09/14/1994
• Issued: 10/29/1996
• Est. Priority Date: 09/14/1994
• Status: Expired due to Fees

• Current Assignee: Teledyne Industries Incorporated (Teledyne Technologies Incorporated)
• Original Assignee: Teledyne Industries Incorporated (Teledyne Technologies Incorporated)
• Inventors: Sommers, James A.
• Primary Examiner(s): BOS, STEVEN J
• Application Number:
  US08/305,555
• Time in Patent Office: 776 Days
• Field of Search: 423/79, 423/492, 423/60
• US Class Current: 423/79
• CPC Class Codes: C01G 25/04 Halides

Abstract

An improved carbochlorination process for the production of volatile metal chlorides is disclosed. When chlorine gas contacts a metal oxide or a mixed metal oxide in a reaction zone in the presence of carbon at elevated temperatures, an undesirable carbochlorination residue forms containing carbon in the reaction zone. After the build-up of a carbochlorination residue in the reaction zone occurs, the volume of the carbochlorination residue in the reaction zone is reduced by periodically introducing just chlorine and metal oxide or mixed metal oxide reactants into the reaction zone without introducing any additional carbon. These components react with a portion of the carbon in the carbochlorination residue so as to reduce the amount of the residue.

Claims

1. In a carbochlorination process for the production of volatile metal chlorides wherein chlorine gas contacts zirconium oxides in a reaction zone in the presence of carbon at elevated temperatures and builds up a carbochlorination residue containing carbon in the reaction zone, the improvement comprising reducing the volume of the carbochlorination residue in the reaction zone by periodically introducing, after the build up of a carbochlorination residue in the reaction zone, zirconium oxide or zircon into the reaction zone without introducing any carbon, to thereby react the carbon in the carbochlorination residue with the zirconium oxide or zircon.

2. The process of claim 1, wherein after the periodic introduction of zirconium oxide or zircon sand into the reaction zone the carbochlorination reaction is continued.

3. The process of claims 1 or 2, wherein the reaction zone is maintained at a temperature of from about 900°

C. to about 1200°

C.

4. The process of claims 1 or 2, wherein the zirconium oxide is baddeleyite.