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US4012297A Expired / Lapsed US ⏱️ 0.0 years remaining

Mercury recovery and recycle process

Assignee: BASF Corp
•
Filing: 1976-01-16
•
Granted: 1977-03-15
•
Expires: 1996-01-16
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Abstract

Abstract In the process of producing chlorine and caustic soda employing mercury amalgam electrolytic cells, mercury losses occur in both solid and liquid plant waste streams. This invention provides for an integrated system in which mercury is extracted from plant waste streams, the waste streams are discharged, and the mercury recovered by electro-reduction in the plant electrolytic cells.

Inventors

  • 👤 Edward Nicholas Balko
  • 👤 William Francis Schmitt
  • 👤 Shyam Dattatreya Argade

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 12:03
CPC Classifications
C; C01; C01D; C01D3/00; C01D3/14; C01D3/16; C25; C25B; C25B1/00; C25B1/01; C25B1/34; C25B1/36

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 206 words
A process for the purification of solids and liquid waste streams from a mercury amalgam chlorine plant employing an aqueous brine stream containing metallic mercury and soluble and insoluble mercury salts comprising a. purifying said brine stream by adding sodium carbonate and sodium hydroxide to precipitate therefrom, b. separating said mercury and mercury salts from the brine stream and reacting said mercury and mercury salts with sulfuric acid, c. adjusting the pH of the slurry resulting from the reaction of step (b) from about 6.0 to 9.0 and oxidizing all of said metallic mercury and insoluble mercury salts present into soluble mercury salts, with an amount of oxidant sufficient thereto, d. filtering the slurry and washing the solids whereupon the solids are removed, e. removing residual oxidant, adjusting the pH of the solution from about 2.5 to about 6.0 and precipitating the mercury contained therein by adding an amount of sulfide source sufficient thereto, f. filtering off the mercury sulfide and allowing the filtrate to be discharged, g. dispersing said mercury sulfide in a brine solution, adjusting the pH to about 8 to 10, oxidizing the mercury forming soluble mercuric chloride, h. combining the brine solution of step (g) with said brine stream of step (a).
Claim 2
Dependent Claim 206 words
A process for the purification of solids and liquid waste streams from a mercury amalgam chlorine plant employing an aqueous brine stream containing metallic mercury and soluble and insoluble mercury salts comprising a. purifying said brine stream by adding sodium carbonate and sodium hydroxide to precipitate therefrom, b. separating said mercury and mercury salts from the brine stream and reacting said mercury and mercury salts with sulfuric acid, c. adjusting the pH of the slurry resulting from the reaction of step (b) from about 6.0 to 9.0 and oxidizing all of said metallic mercury and insoluble mercury salts present into soluble mercury salts, with an amount of oxidant sufficient thereto, d. filtering the slurry and washing the solids whereupon the solids are removed, e. removing residual oxidant, adjusting the pH of the solution from about 2.5 to about 6.0 and precipitating the mercury contained therein by adding an amount of sulfide source sufficient thereto, f. filtering off the mercury sulfide and allowing the filtrate to be discharged, g. dispersing said mercury sulfide in a brine solution, adjusting the pH to about 8 to 10, oxidizing the mercury forming soluble mercuric chloride, h. combining the brine solution of step (g) with said brine stream of step (a).
Claim 3
Dependent Claim 19 words
The process of claim 1 wherein the filtrate from step (d) is combined with other plant liquid waste streams.
Claim 4
Dependent Claim 12 words
The process of claim 1 wherein the oxidant employed is sodium hypochlorite.
Claim 5
Dependent Claim 12 words
The process of claim 1 wherein the oxidant employed is chlorine gas.
Claim 6
Dependent Claim 12 words
The process of claim 1 wherein the oxidant employed is hypochlorous acid.

References Cited (Backward Citations)

US3801480A Cited
US3785942A Cited
US3755110A Cited
US3691037A Cited
US3836442A Cited
US3895938A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-03-14 1980-09-13 1981-03-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-03-14 1984-09-13 1985-03-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-03-14 1988-09-13 1989-03-15 $7700.00 Window Closed / Lapsed

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