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US5062956A Expired / Lapsed US ⏱️ 0.0 years remaining

Bioremediation of chromium (VI) contaminated aqueous systems by sulfate reducing bacteria

Assignee: Honeywell International Inc
•
Filing: 1990-03-20
•
Granted: 1991-11-05
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Expires: 2010-03-20
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Abstract

Abstract A method of reducing soluble Cr(VI) levels in aqueous wastes from 200 ppm or more to less than 1 ppm, particularly to less than 0.05 ppm, preferably to less than 0.01 ppm, uses fermentative sulfate-reudcing anaerobic bacteria to reduce Cr(VI) to Cr(III) and immobilize the latter as the extememly insoluble hydroxide. The process is readily adapted to operate continuously using a bioreactor containing sludge with sulfate-reducing anaerobic bacteria and operated as a chemostat.

Inventors

  • 👤 F. Stephen Lupton
  • 👤 Louis J. DeFilippi
  • 👤 James R. Goodman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 12:45
CPC Classifications
C; C22; C22B; C22B3/00; C22B3/18; C02; C02F; C02F3/00; C02F3/28; C02F2101/00; C02F2101/10; C02F2101/20; C02F2101/22; Y; Y02; Y02P; Y02P10/00; Y02P10/20; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/911; Y10S210/912; Y10S210/913; Y10S423/00; Y10S423/09; Y10S423/17

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 172 words
A method of reducing levels of Cr(VI) dissolved in a liquid aqueous residue resulting from chromium processing in amounts up to in excess of 200 ppm Cr(VI) said aqueous residue containing up to 5-10 wt. percent of dissolved salts comprising a) adjusting the pH of said aqueous residue to a value between about 6.5 and 9.5 by adding a neutralizing agent and thereby increasing the content of dissolved salts; b) adding to the pH adjusted residue (a) (1) a carbon source sufficient to sustain microbial growth, (2) a sulfate source sufficient to provide at least 10 millimoles sulfate per liter of said residue and (3) nutrients for sulfate-reducing anaerobic bacteria; c) diluting the aqueous residue of (b) to provide no more than 200 ppm of Cr(VI) per liter of diluted residue; d) contacting said diluted residue of (c) in the substantial absence of oxygen with sulfate-reducing anaerobic bacteria for a period of time sufficient to reduce the concentration of Cr(VI) to below about 0.05 ppm as chromium and to precipitate Cr(III) hydroxides.
Claim 2
Independent Claim 172 words
A method of reducing levels of Cr(VI) dissolved in a liquid aqueous residue resulting from chromium processing in amounts up to in excess of 200 ppm Cr(VI) said aqueous residue containing up to 5-10 wt. percent of dissolved salts comprising a) adjusting the pH of said aqueous residue to a value between about 6.5 and 9.5 by adding a neutralizing agent and thereby increasing the content of dissolved salts; b) adding to the pH adjusted residue (a) (1) a carbon source sufficient to sustain microbial growth, (2) a sulfate source sufficient to provide at least 10 millimoles sulfate per liter of said residue and (3) nutrients for sulfate-reducing anaerobic bacteria; c) diluting the aqueous residue of (b) to provide no more than 200 ppm of Cr(VI) per liter of diluted residue; d) contacting said diluted residue of (c) in the substantial absence of oxygen with sulfate-reducing anaerobic bacteria for a period of time sufficient to reduce the concentration of Cr(VI) to below about 0.05 ppm as chromium and to precipitate Cr(III) hydroxides.
Claim 3
Dependent Claim 21 words
The method of claim 1 where the pH is adjusted in (a) to a value between about 7.0 and about 8.5.
Claim 4
Dependent Claim 27 words
The method of claim 1 where the amount of Cr(VI) dissolved in the treated aqueous residue is less than about 0.01 ppm measured as chromium in (d).
Claim 5
Dependent Claim 140 words
A process for the continuous immobilization of Cr(VI) dissolved in resulting from chromium liquid aqueous residues processing resulting from chromium processing in amounts up to about 2000 ppm comprising transferring a portion of the liquid aqueous residue to a reservoir which maintains the pH of said aqueous residue at a value between about 6.5 and about 9.5, adding to the pH adjusted residue (a) a carbon source sufficient to sustain microbial growth, (b) a sulfate source sufficient to provide at least 10 millimols sulfate per liter of said residue, and optionally (c) nutrients for sulfate-reducing anaerobic bacteria, continuously delivering a portion of the pH adjusted liquid aqueous residue to a chemostat containing fermentative sulfate-reducing anaerobic bacteria in a sludge, and continuously removing as effluent an equal portion of treated aqueous residue containing less dissolved Cr(VI) than in the initial reside.
Claim 6
Dependent Claim 140 words
A process for the continuous immobilization of Cr(VI) dissolved in resulting from chromium liquid aqueous residues processing resulting from chromium processing in amounts up to about 2000 ppm comprising transferring a portion of the liquid aqueous residue to a reservoir which maintains the pH of said aqueous residue at a value between about 6.5 and about 9.5, adding to the pH adjusted residue (a) a carbon source sufficient to sustain microbial growth, (b) a sulfate source sufficient to provide at least 10 millimols sulfate per liter of said residue, and optionally (c) nutrients for sulfate-reducing anaerobic bacteria, continuously delivering a portion of the pH adjusted liquid aqueous residue to a chemostat containing fermentative sulfate-reducing anaerobic bacteria in a sludge, and continuously removing as effluent an equal portion of treated aqueous residue containing less dissolved Cr(VI) than in the initial reside.
Claim 7
Dependent Claim 22 words
The process of claim 4 where the pH is adjusted in said reservoir to a value between about 7.0 and about 8.5.
Claim 8
Dependent Claim 20 words
The process of claim 4 where the amount of Cr(VI) dissolved in said effluent is less than about 0.05 ppm.
Claim 9
Dependent Claim 20 words
The process of claim 4 where the amount of Cr(VI) dissolved in said effluent is less than about 0.01 ppm.

References Cited (Backward Citations)

US3941691A Cited
US4260491A Cited
US4468461A Cited
US4522723A Cited
US4701261A Cited
US4758344A Cited
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US4839052A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-11-04 1995-05-06 1995-11-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-11-04 1999-05-06 1999-11-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-11-04 2003-05-06 2003-11-05 $7700.00 Window Closed / Lapsed

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