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US4804528A Expired / Lapsed US ⏱️ 0.0 years remaining

Stripping and recovery of dichromate in electrolytic chlorate systems

Assignee: Aker Solutions Canada Inc
•
Filing: 1988-01-12
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Granted: 1989-02-14
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Expires: 2008-01-12
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Abstract

Abstract A process for removing dichromates from chlorate-rich solutions containing hypochlorite and dichromate ions and produced by the electrolysis of brine. The dichromate is reduced in a two-stage process by the addition of ammonia under controlled conditions of pH and temperature to a mixed di- and trivalent chromium hydroxide which is precipitated from solution and removed. The process provides an economical method of recovering chromium from electrolytically produced chlorate solutions.

Inventors

  • 👤 Ian H. Warren

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 21:51
CPC Classifications
C; C01; C01B; C01B11/00; C01B11/12; C01B11/14; C01B11/145; C25; C25B; C25B1/00; C25B1/01; C25B1/24; C25B1/26; C25B1/265; C25B15/00; C25B15/08; C25B15/085; Y; Y10; Y10S; Y10S204/00; Y10S204/13; Y10S210/00; Y10S210/902; Y10S210/911; Y10S210/912; Y10S210/913

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 134 words
A process for the removal of dichromate from a solution containing chlorate, hypochlorite and dichromate ions by the reduction of the hexavalent chromium of said dichromate to mixed di- and trivalent chromium in the form of a hydroxide precipitate which process comprises effecting said reduction in two stages comprising (a) adding ammonia to said solution and treating said solution at a pH greater than 8.5 at a temperature of greater than 60° C. with said ammonia to effect production of said hydroxide precipitate; said ammonia and said hypochlorite being present in sufficiently excessive amounts to permit the production of said hydroxide precipitate; and (b) adjusting the pH of the resultant solution to below 8.5 at a temperature of greater than 40° C. to effect substantially complete precipitation of said di- and trivalent chromium hydroxide.
Claim 2
Dependent Claim 134 words
A process for the removal of dichromate from a solution containing chlorate, hypochlorite and dichromate ions by the reduction of the hexavalent chromium of said dichromate to mixed di- and trivalent chromium in the form of a hydroxide precipitate which process comprises effecting said reduction in two stages comprising (a) adding ammonia to said solution and treating said solution at a pH greater than 8.5 at a temperature of greater than 60° C. with said ammonia to effect production of said hydroxide precipitate; said ammonia and said hypochlorite being present in sufficiently excessive amounts to permit the production of said hydroxide precipitate; and (b) adjusting the pH of the resultant solution to below 8.5 at a temperature of greater than 40° C. to effect substantially complete precipitation of said di- and trivalent chromium hydroxide.
Claim 3
Dependent Claim 51 words
A process as claimed in claim 1 wherein said solution during stage (a) has a pH greater than 10.5 and a temperature selected from the range 75° C.-85° C., and during stage (b) has a pH selected from the range 6.5-7.5 and a temperature selected from the range 75° C.-85° C.
Claim 4
Dependent Claim 25 words
A process as claimed in claim 2 wherein any ammonia remaining in said solution after stage (a) is removed under vacuum prior to stage (b).
Claim 5
Dependent Claim 34 words
A process as claimed in claim 3 wherein the pH of the solution in stage (a) is adjusted by the addition of sodium hydroxide and in stage (b) by the addition of hydrochloric acid.
Claim 6
Dependent Claim 40 words
A process as claimed in any one of claims 1 to 4 wherein said solution comprising chlorate, hypochlorite and dichromate ions is a solution comprising sodium chlorate and sodium chloride produced by the electrolysis of brine in an electrolytic cell.

References Cited (Backward Citations)

SE218495C1 Cited
US3843769A Cited
JPS5521508A Cited
US4259297A Cited
US4560546A Cited
US4477318A Cited
US4680126A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-02-14 1992-08-15 1993-02-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-02-14 1996-08-15 1997-02-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-02-14 2000-08-15 2001-02-14 $7700.00 Window Closed / Lapsed

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