Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures

Abstract The applicability of a fluidized‐bed reactor (FBR)‐based sulfate reducing bioprocess was investigated for the treatment of iron‐containing (40–90 mg/L) acidic wastewater at low (8°C) and high (65°C) temperatures. The FBRs operated at low and high temperatures were inoculated with cultures o...

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Published in:Biotechnology and Bioengineering
Main Authors: Sahinkaya, Erkan, Özkaya, Bestamin, Kaksonen, Anna H., Puhakka, Jaakko A.
Format: Article in Journal/Newspaper
Language:English
Published: Wiley 2006
Subjects:
Online Access:http://dx.doi.org/10.1002/bit.21195
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spelling crwiley:10.1002/bit.21195 2024-09-09T19:27:02+00:00 Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures Sahinkaya, Erkan Özkaya, Bestamin Kaksonen, Anna H. Puhakka, Jaakko A. 2006 http://dx.doi.org/10.1002/bit.21195 https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fbit.21195 https://onlinelibrary.wiley.com/doi/pdf/10.1002/bit.21195 en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor Biotechnology and Bioengineering volume 96, issue 6, page 1064-1072 ISSN 0006-3592 1097-0290 journal-article 2006 crwiley https://doi.org/10.1002/bit.21195 2024-07-11T04:35:35Z Abstract The applicability of a fluidized‐bed reactor (FBR)‐based sulfate reducing bioprocess was investigated for the treatment of iron‐containing (40–90 mg/L) acidic wastewater at low (8°C) and high (65°C) temperatures. The FBRs operated at low and high temperatures were inoculated with cultures of sulfate‐reducing bacteria (SRB) originally enriched from arctic and hot mining environments, respectively. Ethanol was supplemented as carbon and electron source for SRB. At 8°C, ethanol oxidation and sulfate reduction rates increased steadily and reached 320 and 265 mg/L·day, respectively, after 1 month of operation. After this point, the rates did not change significantly during 130 days of operation. Despite the complete ethanol oxidation and iron precipitation, the average sulfate reduction efficiency was 35 ± 4% between days 30 and 130 due to the accumulation of acetate. At 65°C, a rapid startup was observed as 99.9, 46, and 29% ethanol, sulfate, acetate removals, in respective order, were observed after 6 days. The feed pH was decreased gradually from its initial value of 6 to around 3.7 during 100 days of operation. The wastewater pH of 4.3–4.4 was neutralized by the alkalinity produced in acetate oxidation and the average effluent pH was 7.8 ± 0.8. As in the low temperature FBR, acetate accumulated. Hence, the oxidation of acetate is the rate‐limiting step in the sulfidogenic ethanol oxidation by thermophilic and psychrotrophic SRB. The sulfate reduction rate is three times and acetate oxidation rate is four times higher at 65°C than at 8°C. Biotechnol. Bioeng. 2007;96:1064–1072. © 2006 Wiley Periodicals, Inc. Article in Journal/Newspaper Arctic Wiley Online Library Arctic Biotechnology and Bioengineering 96 6 1064 1072
institution Open Polar
collection Wiley Online Library
op_collection_id crwiley
language English
description Abstract The applicability of a fluidized‐bed reactor (FBR)‐based sulfate reducing bioprocess was investigated for the treatment of iron‐containing (40–90 mg/L) acidic wastewater at low (8°C) and high (65°C) temperatures. The FBRs operated at low and high temperatures were inoculated with cultures of sulfate‐reducing bacteria (SRB) originally enriched from arctic and hot mining environments, respectively. Ethanol was supplemented as carbon and electron source for SRB. At 8°C, ethanol oxidation and sulfate reduction rates increased steadily and reached 320 and 265 mg/L·day, respectively, after 1 month of operation. After this point, the rates did not change significantly during 130 days of operation. Despite the complete ethanol oxidation and iron precipitation, the average sulfate reduction efficiency was 35 ± 4% between days 30 and 130 due to the accumulation of acetate. At 65°C, a rapid startup was observed as 99.9, 46, and 29% ethanol, sulfate, acetate removals, in respective order, were observed after 6 days. The feed pH was decreased gradually from its initial value of 6 to around 3.7 during 100 days of operation. The wastewater pH of 4.3–4.4 was neutralized by the alkalinity produced in acetate oxidation and the average effluent pH was 7.8 ± 0.8. As in the low temperature FBR, acetate accumulated. Hence, the oxidation of acetate is the rate‐limiting step in the sulfidogenic ethanol oxidation by thermophilic and psychrotrophic SRB. The sulfate reduction rate is three times and acetate oxidation rate is four times higher at 65°C than at 8°C. Biotechnol. Bioeng. 2007;96:1064–1072. © 2006 Wiley Periodicals, Inc.
format Article in Journal/Newspaper
author Sahinkaya, Erkan
Özkaya, Bestamin
Kaksonen, Anna H.
Puhakka, Jaakko A.
spellingShingle Sahinkaya, Erkan
Özkaya, Bestamin
Kaksonen, Anna H.
Puhakka, Jaakko A.
Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures
author_facet Sahinkaya, Erkan
Özkaya, Bestamin
Kaksonen, Anna H.
Puhakka, Jaakko A.
author_sort Sahinkaya, Erkan
title Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures
title_short Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures
title_full Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures
title_fullStr Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures
title_full_unstemmed Sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures
title_sort sulfidogenic fluidized‐bed treatment of metal‐containing wastewater at low and high temperatures
publisher Wiley
publishDate 2006
url http://dx.doi.org/10.1002/bit.21195
https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fbit.21195
https://onlinelibrary.wiley.com/doi/pdf/10.1002/bit.21195
geographic Arctic
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genre Arctic
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op_source Biotechnology and Bioengineering
volume 96, issue 6, page 1064-1072
ISSN 0006-3592 1097-0290
op_rights http://onlinelibrary.wiley.com/termsAndConditions#vor
op_doi https://doi.org/10.1002/bit.21195
container_title Biotechnology and Bioengineering
container_volume 96
container_issue 6
container_start_page 1064
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