Process for removing mercury from brine sludges
AssigneeStauffer Chemical Company
InventorsJulian E. Blanch, Helmut W. Majewski
Life of this patent
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Abstract
The mercury content of electrolysis cell brine sludge is reduced by sequentially: (1) acidifying the sludge to a pH below 2.5 and (2) leaching the sludge with aqueous hypochlorite solvent. The mercury content removed from the sludge may optionally be isolated from the solvent and reused as mercury cathode for brine electrolysis.
Claims19
A process for reducing the mercury content of mercury cathode brine electrolysis cell sludge containing minor concentrations of mercury by sequentially:
- (1) acidifying said sludge to a pH below 2.5, and (2) leaching said sludge with aqueous hypochlorite solvent of a pH above 5 until the mercury content is less than 0.75 part per million by weight based on the weight of sludge wet cake after leaching.
A process for recovering and concentrating the mercury content of mercury cathode brine electrolysis cell sludge containing minor concentrations of mercury by sequentially:
- (1) acidifying said sludge to a pH below 2.5, (2) leaching said sludge with aqueous hypochlorite solvent at a pH above 5, (3) separating said solvent from the leached sludge, and (4) isolating the major part of the mercury content of said separated solvent.
In an improved process for making elemental chlorine and sodium-mercury amalgam by the electrolysis of brine in a mercury cathode electrolysis cell wherein depleted brine from said cell is treated with alkali-metal carbonate or alkali-metal hydroxide to precipitate impurities as clarifier sludge, said sludge containing minor concentrations of mercury, separating said sludge from said brine for disposal outside the cell, and adding to the electrolysis cell metallic mercury in amount at least equal to the mercury retained by said separated clarifier sludge;
- the improvement which comprises:
- recovering the mercury content of said sludge by sequentially:
- (1) acidifying said sludge with hydrochloric acid to a pH below 2.5, (2) leaching said sludge with aqueous hypochlorite solvent at a pH above 5, (3) separating said solvent from the leached sludge, (4) isolating the major part of the mercury content of said separated solvent, (5) converting the insolubilized mercury to metallic mercury or chloride of mercury, and (6) returning said metallic mercury to a cathode of a mercury cathode brine electrolysis cell.
In an improved process for making elemental chlorine and sodium-mercury amalgam by the electrolysis of brine in a mercury cathode electrolysis cell wherein depleted brine is reconcentrated by contact with solid sodium chloride and returned to said electrolysis cell, said contact with sodium chloride resulting in the accumulation of insoluble impurities as saturator sludge, said sludge containing minor concentrations of mercury, separating said sludge from said brine for disposal outside the cell, and adding to the electrolysis cell metallic mercury in amount at least equal to the mercury retained by said saturator sludge;
- the improvement which comprises:
- recovering the mercury content of said sludge by sequentially:
- (1) acidifying said sludge with hydrochloric acid to a pH below 2.5, (2) leaching said sludge with aqueous hypochlorite solvent at a pH above 5, (3) separating said solvent from the leached sludge, (4) isolating the major part of the mercury content of said separated solvent, (5) converting the insolubilized mercury to metallic mercury or chloride of mercury, and (6) returning said metallic mercury to a cathode of a mercury cathode brine electrolysis cell.
Dependencies are inferred from the claim text.