Recovery of sodium fluoride and other chemicals from spent carbon liners

• US 4,113,831 A
• Filed: 10/02/1975
• Issued: 09/12/1978
• Est. Priority Date: 10/02/1975
• Status: Expired due to Term

• Current Assignee: National Fluoride and Chemical Corporation
• Original Assignee: National Fluoride and Chemical Corporation
• Inventors: Orth, Richard D., Orth, George Otto Jr.
• Primary Examiner(s): Vertiz, O. R.
• Assistant Examiner(s): Langel, Wayne A.
• Application Number:
  US05/618,958
• Time in Patent Office: 1,076 Days
• Field of Search: 423/184, 423/185, 423/630, 423/499, 423/122, 423/129, 423/127, 423/116, 423/119, 423/120, 423/121
• US Class Current: 423/119
• CPC Class Codes: C01B 32/05 Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
• CPC Class Codes: C01D 3/02 Fluorides
• CPC Class Codes: C01F 7/04 Preparation of alkali metal aluminates; Aluminium oxide or hydroxide therefrom C01F7/028 takes precedence
• CPC Class Codes: C25C 3/08 Cell construction, e.g. bottoms, walls, cathodes

Abstract

Floride and aluminum values, as well as carbon, are recovered from waste cathode liner material from aluminum electrolytic cells by leaching of the liner at ambient temperature with a caustic solution, followed by precipitation of sodium fluoride by saturating the leach liquor with a compound which suppresses the solubility of sodium fluoride in the leach liquor. Ammonia is a preferred compound. Aluminum compounds, as well as the carbon values, are also recovered. Treating chemicals used in the process are recycled. The process is essentially a closed-cycle process with substantially no discharge of effluent.

Claims

1. A method for recovering the fluoride and aluminum contained in used cathode carbon liner from electrolytic cells used in the refining of aluminum, comprising:

extracting crushed liner material containing fluoride and aluminum with a caustic solution in an extraction zone to yield an extraction solution containing solubilized sodium aluminate and sodium fluoride,

adding a solubility suppressant to the extraction solution containing the sodium fluoride which suppresses the solubility of the fluoride and causes precipitation of sodium fluoride,

recovering the sodium fluoride from the extraction solution,

contacting the remaining extraction solution containing the sodium aluminate with carbon dioxide to precipitate the aluminum as aluminum hydrates, leaving a residual solution containing sodium carbonate, and

regenerating the caustic solution from the residual solution for recycle to the extraction zone by adding calcium hydroxide to the residual solution.

2. The method of claim 1 wherein the solubility suppressant is ammonia.

3. The method of claim 1 wherein the solubility suppressant is one selected from the group consisting of monohydric or polyhydric alcohols having from one to four carbon atoms, primary and secondary amines, sodium salts and acetone.

4. The method of claim 1 wherein the solubility suppressant is ammonia and the extraction solution is saturated with ammonia in an absorption zone to precipitate sodium fluoride from the extraction solution and wherein the extraction solution containing ammonia is heated to drive off the ammonia for recovery utilizing heat generated by absorption of ammonia in the extraction solution.

5. A method for recovering the fluoride and aluminum contained in used cathode carbon liner from electrolytic cells used in the refining of aluminum, comprising:

extracting crushed liner material with an aqueous caustic solution in an extraction zone to yield an extraction solution containing solubilized sodium aluminate and sodium fluoride,

saturating the extraction solution with ammonia in an absorption zone to precipitate sodium fluoride,

recovering the sodium fluoride from the extraction solution,

contacting the extracting solution containing sodium aluminate with carbon dioxide to precipitate the aluminum as aluminum hydrates,

recovering the ammonia from the extraction solution for recycle to the absorption zone, and

recovering the caustic in the extraction solution for recycle to the extraction zone.

6. The method of claim 5 wherein the aqueous extraction solution contains 1-5% by weight sodium hydroxide.

7. A method for recovering the fluoride and aluminum contained in spent cathode carbon liner from electrolytic cells used in the refining of aluminum, comprising:

extracting the fluoride contained in crushed carbon liner by subjecting the crushed liner to continuous, multistage, countercurrent extraction with a caustic solution at ambient temperature, to yield an extraction solution containing solubilized sodium aluminate and sodium fluoride,

saturating the extraction solution with ammonia in an absorption zone to precipitate sodium fluoride,

recovering the sodium fluoride from the extraction solution,

contacting the extraction solution containing sodium aluminate with carbon dioxide to precipitate the aluminum as aluminum hydrates,

recovering the ammonia from the extraction solution for recycle to the absorption zone, and

recovering the caustic in the extraction solution for recycle to the extraction zone.