US4338200A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the removal of heavy metals from aqueous liquids
Assignee: Akzo NV
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Filing: 1980-07-30
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Granted: 1982-07-06
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Expires: 2000-07-30
Abstract
Abstract The invention relates to a process for the removal of heavy metal ions, particularly chromium, lead and/or zinc ions, from aqueous liquids by precipitation wherein the aqueous liquid containing the heavy metal ions and an aqueous liquid containing a base which precipitates the heavy metal ions in the form of their hydroxide or basic salt are added simultaneously to an amount of water at a pH between 5 and 10 and a temperature between 60° and 100° C. and the pH and the temperature are maintained in the specified ranges during the precipitation.
Inventors
- 👤 Foeke Zeijlstra
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 17:26
CPC Classifications
C; C02; C02F; C02F9/00; C02F1/00; C02F1/52; C02F1/5236; C02F1/5245; C02F1/66; C02F2101/00; C02F2101/10; C02F2101/20; C02F2101/22; C02F2209/00; C02F2209/02; C02F2209/06; C10; C10M; C10M2215/00; C10M2215/22; C10M2215/221; C10M2215/225; C10M2215/226; C10M2215/24; C10M2215/30; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/911; Y10S210/912; Y10S210/913
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
198 words
A process for homogeneously precipitating heavy metal ions selected from the group consisting of chromium ions, zinc ions, and lead ions from aqueous liquids containing same consisting essentially of separately but simultaneously adding (1) an aqueous liquid containing said heavy metal ions in the form of a heavy metal salt selected from the group consisting of chromium sulphate, zinc sulphate, and lead sulphate and (2) an aqueous liquid containing a base that precipitates the heavy metal ion of said heavy metal salt in the form of its hydroxide or basic salt to a quantity of water that (a) is being stirred, (b) has a pH between 5 and 10, and (c) is at a temperature ranging from about 60° C. to about 100° C. to cause homogeneous precipitation of the heavy metal hydroxide or basic salt, wherein the pH of the resulting solution is maintained between 6 and 8 by adjusting the rates of addition of aqueous liquid (1) and aqueous liquid (2) and wherein the temperature is held within the range from about 60° C. to about 100° C. during the homogeneous precipitation, and separating the precipitated heavy metal hydroxide or basic salt from the resulting solution.
Claim 2
Dependent Claim
198 words
A process for homogeneously precipitating heavy metal ions selected from the group consisting of chromium ions, zinc ions, and lead ions from aqueous liquids containing same consisting essentially of separately but simultaneously adding (1) an aqueous liquid containing said heavy metal ions in the form of a heavy metal salt selected from the group consisting of chromium sulphate, zinc sulphate, and lead sulphate and (2) an aqueous liquid containing a base that precipitates the heavy metal ion of said heavy metal salt in the form of its hydroxide or basic salt to a quantity of water that (a) is being stirred, (b) has a pH between 5 and 10, and (c) is at a temperature ranging from about 60° C. to about 100° C. to cause homogeneous precipitation of the heavy metal hydroxide or basic salt, wherein the pH of the resulting solution is maintained between 6 and 8 by adjusting the rates of addition of aqueous liquid (1) and aqueous liquid (2) and wherein the temperature is held within the range from about 60° C. to about 100° C. during the homogeneous precipitation, and separating the precipitated heavy metal hydroxide or basic salt from the resulting solution.
Claim 3
Dependent Claim
28 words
Process according to claim 1 wherein the heavy metal salts are selected from the group consisting of chromium sulfate and zinc sulphate and the base is a hydroxide.
Claim 4
Dependent Claim
20 words
Process according to claim 1 wherein the heavy metal salt is lead sulphate and the base is a carbonate solution.
Claim 5
Dependent Claim
15 words
Process according to claim 1 wherein the temperature is maintained between 75° and 90° C.
Claim 6
Dependent Claim
37 words
Process according to claim 1 wherein the rate of addition of the aqueous liquid containing the heavy metal ions is in the range of about 0.1 to about 5 liters per second per m 3 reaction mixture.
Claim 7
Dependent Claim
160 words
A process for homogeneously precipitating chromium ions from aqueous liquids containing same consisting essentially of separately but simultaneously adding (1) an aqueous liquid containing said chromium ions in the form of chromium acetate and (2) an aqueous liquid containing a base that precipitates the chromium ion in the form of its hydroxide or basic salts to a quantity of water that (a) is being stirred, (b) has a pH between 5 and 10, and (c) is at a temperature ranging from about 60° C. to about 100° C. to cause homogeneous precipitation of the chromium hydroxide or basic salt, wherein the pH of the resulting solution is maintained between 8 and 10 by adjusting the rates of addition of aqueous liquid (1) and aqueous liquid (2) and wherein the temperature is held within the range from about 60° C. to about 100° C. during the homogeneous precipitation, and separating the precipitated chromium hydroxide or basic salt from the resulting solution.
Claim 8
Dependent Claim
160 words
A process for homogeneously precipitating chromium ions from aqueous liquids containing same consisting essentially of separately but simultaneously adding (1) an aqueous liquid containing said chromium ions in the form of chromium acetate and (2) an aqueous liquid containing a base that precipitates the chromium ion in the form of its hydroxide or basic salts to a quantity of water that (a) is being stirred, (b) has a pH between 5 and 10, and (c) is at a temperature ranging from about 60° C. to about 100° C. to cause homogeneous precipitation of the chromium hydroxide or basic salt, wherein the pH of the resulting solution is maintained between 8 and 10 by adjusting the rates of addition of aqueous liquid (1) and aqueous liquid (2) and wherein the temperature is held within the range from about 60° C. to about 100° C. during the homogeneous precipitation, and separating the precipitated chromium hydroxide or basic salt from the resulting solution.
Claim 9
Dependent Claim
15 words
Process according to claim 6 wherein the pH 5 is maintained between 7 and 7.5.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-07-05 | 1986-01-04 | 1986-07-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-07-05 | 1990-01-04 | 1990-07-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-07-05 | 1994-01-04 | 1994-07-06 | $7700.00 | Window Closed / Lapsed |