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US4172784A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the separation of cadmium (Cd++)-ions from sewage, waste water and aqueous solutions

Assignee: Evonik Operations GmbH
•
Filing: 1977-09-06
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Granted: 1979-10-30
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Expires: 1997-09-06
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Abstract

Abstract Cadmium (Cd ++ ) ions are separated from an effluent containing complexing agent such as nitrilotriacetic acid, ethylenediamine tetraacetic acid and/or diethylenetriamine pentaacetic acid, or their anionic salts by using an HS-containing triazine compound and Fe +++ ions in a quantity at least equal to the amount of complexing agent.

Inventors

  • 👤 Helmut Knorre
  • 👤 Gerhard Pohl
  • 👤 Klaus Stutzel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 10:59
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/52; C02F1/5272; C01; C01G; C01G11/00; C01G49/00; C01G49/02; C01G49/06; C02F1/72; C02F1/722; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/911; Y10S210/912

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 192 words
A process for the separation of cadmium (Cd ++ )-ions from aqueous liquids in which said cadmium ions are present as complexes of nitrilotriacetic acid, ethylenediamine tetraacetic acid and/or diethylenetriamino pentaacetic acid or their anionic salts, comprising contacting salt liquids with an HS-containing triazine compound of the general formula ##STR3## in which: R is hydrogen, the same or different alkyl with 1 to 3 carbons, --NR 1 R 2 or --OR 3 ; R 1 , r 2 and R 3 are hydrogen, the same or different alkyl with 1 to 6 carbons or phenyl; n is a whole number from 0 to 2; or a water-soluble salt thereof to precipitate said cadmium ions and wherein said compound is contacted in an amount such that at least one equivalent of mercapto or mercaptide groups is present per equivalent of cadmium ions the precipitation of the Cd +++ -ions takes place in the presence of an at least equivalent quantity of Fe +++ -ions, based on said complexing agent in said liquid, wherein said precipitation takes place at a pH value between 4 and 10, and separating the precipitate from the aqueous liquid.
Claim 2
Dependent Claim 192 words
A process for the separation of cadmium (Cd ++ )-ions from aqueous liquids in which said cadmium ions are present as complexes of nitrilotriacetic acid, ethylenediamine tetraacetic acid and/or diethylenetriamino pentaacetic acid or their anionic salts, comprising contacting salt liquids with an HS-containing triazine compound of the general formula ##STR3## in which: R is hydrogen, the same or different alkyl with 1 to 3 carbons, --NR 1 R 2 or --OR 3 ; R 1 , r 2 and R 3 are hydrogen, the same or different alkyl with 1 to 6 carbons or phenyl; n is a whole number from 0 to 2; or a water-soluble salt thereof to precipitate said cadmium ions and wherein said compound is contacted in an amount such that at least one equivalent of mercapto or mercaptide groups is present per equivalent of cadmium ions the precipitation of the Cd +++ -ions takes place in the presence of an at least equivalent quantity of Fe +++ -ions, based on said complexing agent in said liquid, wherein said precipitation takes place at a pH value between 4 and 10, and separating the precipitate from the aqueous liquid.
Claim 3
Dependent Claim 41 words
The process of claim 1 wherein the precipitation of the Cd ++ -ions takes place in the presence of a molar excess of Fe +++ -ions in the amount of 10 to 200%, based on the complexing agent in the liquid.
Claim 4
Dependent Claim 17 words
The process of claim 2 wherein said molar excess is in the amount of 50 to 100%.
Claim 5
Dependent Claim 21 words
The process of claim 1 wherein the required concentration of Fe +++ -ions in the liquid is determined by potentiometric means.
Claim 6
Dependent Claim 63 words
The process of claim 1 wherein filtration is used to separate the precipitate and subsequent to the precipitation and separation of the Cd ++ -ions, a Fe +++ -ion complex formed in the filtrate is oxidized by addition of hydrogen peroxide at a pH above 7, and the Fe +++ -ions are then precipitated and separated as a barely soluble Fe(OH) 3 .

References Cited (Backward Citations)

DE2240549A1 Cited
US3778368A Cited
US3816306A Cited
US3931007A Cited
JPS5110176A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-10-29 1983-04-30 1983-10-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-10-29 1987-04-30 1987-10-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-10-29 1991-04-30 1991-10-30 $7700.00 Window Closed / Lapsed

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