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Process for reducing the mercury content of industrial waste waters

Assignee: Hoechst AG
•
Filing: 1977-03-22
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Granted: 1978-08-22
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Expires: 1997-03-22
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Abstract

Abstract The invention deals with the reduction of the mercury content of industrial waste waters, especially those from a chlorine-alkali electrolysis using the amalgam process. According to the invention all mercury present in the waste water is converted to the form of Hg ++ ions by adding chlorine. Subsequently Fe ++ ions are added. The pH of the solution is raised until a redox potential of from - 0.1 to - 0.8 volts, relative to the normal hydrogen electrode, is obtained. The mercury precipitated and the iron oxide hydrate formed may be filtered from the waste water. Residual mercury contents in the filtrate of about 50 mg/m 3 may be obtained.

Inventors

  • 👤 Martin Krieg
  • 👤 Theo Olffers

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 18:21
CPC Classifications
C; C02; C02F; C02F9/00; C02F1/00; C02F1/72; C02F1/76; C02F2101/00; C02F2101/10; C02F2101/20; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/911; Y10S210/912; Y10S210/914

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 195 words
A process for reducing the mercury content of industrial waste waters to about only 50 mg/m 3 by precipitating the mercury compounds from the waste waters after having converted the total amount of mercury contained in such waters to the ionic bivalent oxidation state by adjusting first the waste water to a pH-value of 4.5 or less by the addition of hydrochloric acid or sulfuric acid, and then adding such an amount of chlorine, chlorinated water or sodium hypochlorite that a content of from 2 to 50 mg of active chlorine per liter waste water is present, which comprises subsequently adding to the waste water, pre-treated in this way, iron (II) ions until a content of from 0.1 to 1.5 g of such ions per liter of waste water is attained, then adjusting a redox potential of from -0.1 to -0.8 volts, relative to the normal hydrogen electrode by addition of a chemical agent increasing the pH selected from the group consisting of alkali lyes and calcium hydroxide thus reducing the bivalent mercury ions to insoluble mercury (I) salt, and precipitating it together with the iron oxide hydrates formed, and finally eliminating the precipitated products.
Claim 2
Dependent Claim 195 words
A process for reducing the mercury content of industrial waste waters to about only 50 mg/m 3 by precipitating the mercury compounds from the waste waters after having converted the total amount of mercury contained in such waters to the ionic bivalent oxidation state by adjusting first the waste water to a pH-value of 4.5 or less by the addition of hydrochloric acid or sulfuric acid, and then adding such an amount of chlorine, chlorinated water or sodium hypochlorite that a content of from 2 to 50 mg of active chlorine per liter waste water is present, which comprises subsequently adding to the waste water, pre-treated in this way, iron (II) ions until a content of from 0.1 to 1.5 g of such ions per liter of waste water is attained, then adjusting a redox potential of from -0.1 to -0.8 volts, relative to the normal hydrogen electrode by addition of a chemical agent increasing the pH selected from the group consisting of alkali lyes and calcium hydroxide thus reducing the bivalent mercury ions to insoluble mercury (I) salt, and precipitating it together with the iron oxide hydrates formed, and finally eliminating the precipitated products.
Claim 3
Dependent Claim 23 words
The process as claimed in claim 1, which comprises adjusting the redox potential and subsequently separating the precipitated products in an oxygen-free atmosphere.
Claim 4
Dependent Claim 22 words
The process as claimed in claim 1, wherein the waste waters stem from a chlorine-alkali electrolysis operating according to the amalgam process.

References Cited (Backward Citations)

US3847598A Cited
US3857704A Cited
US3764528A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-08-21 1982-02-20 1982-08-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-08-21 1986-02-20 1986-08-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-08-21 1990-02-20 1990-08-22 $7700.00 Window Closed / Lapsed

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