Continuous sulfidogenic wastewater treatment with iron sulfide sludge oxidation and recycle

This study evaluated the technical feasibility of packed-bed sulfidogenic bioreactors dosed with ferrous chloride for continuous wastewater treatment over a 450-day period. In phase I, the bioreactors were operated under different combinations of carbon, iron, and sulfate mass loads without sludge r...

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Veröffentlicht in:Water research (Oxford) 2017-05, Vol.114, p.210-217
Hauptverfasser: Deng, Dongyang, Lin, Lian-Shin
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description This study evaluated the technical feasibility of packed-bed sulfidogenic bioreactors dosed with ferrous chloride for continuous wastewater treatment over a 450-day period. In phase I, the bioreactors were operated under different combinations of carbon, iron, and sulfate mass loads without sludge recycling to identify optimal treatment conditions. A COD/sulfate mass ratio of 2 and a Fe/S molar ratio of 1 yielded the best treatment performance with COD oxidation rate of 786 ± 82 mg/(L⋅d), which resulted in 84 ± 9% COD removal, 94 ± 6% sulfate reduction, and good iron retention (99 ± 1%) under favorable pH conditions (6.2–7.0). In phase II, the bioreactors were operated under this chemical load combination over a 62-day period, during which 7 events of sludge collection, oxidation, and recycling were performed. The collected sludge materials contained both inorganic and organic matter with FeS and FeS2 as the main inorganic constituents. In each event, the sludge materials were oxidized in an oxidizing basin before recycling to mix with the wastewater influent. Sludge recycling yielded enhanced COD removal (90 ± 6% vs. 75 ± 7%), and better effluent quality in terms of pH (6.8 ± 0.1 vs. 6.5 ± 0.2), iron (0.7 ± 0.5 vs. 1.9 ± 1.7 mg/L), and sulfide-S (0.3 ± 0.1 vs. 0.4 ± 0.1 mg/L) removal compared to the baseline operation without sludge recycling during phase II. This process exhibited treatment stability with reasonable variations, and fairly consistent sludge content over long periods of operation under a range of COD/sulfate and Fe/S ratios without sludge recycling. The bioreactors were found to absorb recycling-induced changes efficiently without causing elevated suspended solids in the effluents. [Display omitted] •COD/sulfate = 2 (mass) and Fe/S = 1 (molar) resulted in favorable treatment.•Recycling oxidized sludge enhanced the treatment performance.•Evidence suggested co-existence of FeS and FeS2 in the bioreactor sludge.•Consistent solid content and VSS/TSS ratio of the sludge during long-term operation.
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Sludge recycling yielded enhanced COD removal (90 ± 6% vs. 75 ± 7%), and better effluent quality in terms of pH (6.8 ± 0.1 vs. 6.5 ± 0.2), iron (0.7 ± 0.5 vs. 1.9 ± 1.7 mg/L), and sulfide-S (0.3 ± 0.1 vs. 0.4 ± 0.1 mg/L) removal compared to the baseline operation without sludge recycling during phase II. This process exhibited treatment stability with reasonable variations, and fairly consistent sludge content over long periods of operation under a range of COD/sulfate and Fe/S ratios without sludge recycling. The bioreactors were found to absorb recycling-induced changes efficiently without causing elevated suspended solids in the effluents. 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Sludge recycling yielded enhanced COD removal (90 ± 6% vs. 75 ± 7%), and better effluent quality in terms of pH (6.8 ± 0.1 vs. 6.5 ± 0.2), iron (0.7 ± 0.5 vs. 1.9 ± 1.7 mg/L), and sulfide-S (0.3 ± 0.1 vs. 0.4 ± 0.1 mg/L) removal compared to the baseline operation without sludge recycling during phase II. This process exhibited treatment stability with reasonable variations, and fairly consistent sludge content over long periods of operation under a range of COD/sulfate and Fe/S ratios without sludge recycling. The bioreactors were found to absorb recycling-induced changes efficiently without causing elevated suspended solids in the effluents. [Display omitted] •COD/sulfate = 2 (mass) and Fe/S = 1 (molar) resulted in favorable treatment.•Recycling oxidized sludge enhanced the treatment performance.•Evidence suggested co-existence of FeS and FeS2 in the bioreactor sludge.•Consistent solid content and VSS/TSS ratio of the sludge during long-term operation.</description><subject>Bioreactors</subject><subject>COD oxidation rate</subject><subject>COD/sulfate</subject><subject>Fe/S</subject><subject>Iron</subject><subject>Sewage - chemistry</subject><subject>Sludge recycle</subject><subject>Sulfides</subject><subject>Sulfidogenic</subject><subject>Waste Disposal, Fluid</subject><subject>Waste Water</subject><subject>Wastewater treatment</subject><issn>0043-1354</issn><issn>1879-2448</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNp9kMtOwzAQRS0EouXxBwhlySZh_EjibJBQxUtCYgMrFpZrT4qrNAHbofTvMWphyWoWc-5czSHkjEJBgVaXy2Kto8dQMKB1AawAIffIlMq6yZkQcp9MAQTPKS_FhByFsAQAxnhzSCZMMtEwyqbkdTb00fXjMIYsjF3r7LDA3plsrUPE1IA-Sy06rrCP2drFt8z5od-xmIVutAvMhi9ndXRpoXubeTQb0-EJOWh1F_B0N4_Jy-3N8-w-f3y6e5hdP-ZGgIx5xUA20tRVC9aWEu28tvNSagCs2pJTbnRbamZpJcu6pszQkvKGMyaokLzR_JhcbO----FjxBDVygWDXad7TH-ppITXjHNeJlRsUeOHEDy26t27lfYbRUH9aFVLtdWqfrQqYCppTbHzXcM4X6H9C_16TMDVFsD056dDr4Jx2Bu0LsmIyg7u_4ZvZ8iL9g</recordid><startdate>20170501</startdate><enddate>20170501</enddate><creator>Deng, Dongyang</creator><creator>Lin, Lian-Shin</creator><general>Elsevier Ltd</general><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope><orcidid>https://orcid.org/0000-0002-5578-4768</orcidid></search><sort><creationdate>20170501</creationdate><title>Continuous sulfidogenic wastewater treatment with iron sulfide sludge oxidation and recycle</title><author>Deng, Dongyang ; Lin, Lian-Shin</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c408t-620898c76f0dd58edb7db58a00e6f5313caf5a2d16857712c15139322414839a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Bioreactors</topic><topic>COD oxidation rate</topic><topic>COD/sulfate</topic><topic>Fe/S</topic><topic>Iron</topic><topic>Sewage - chemistry</topic><topic>Sludge recycle</topic><topic>Sulfides</topic><topic>Sulfidogenic</topic><topic>Waste Disposal, Fluid</topic><topic>Waste Water</topic><topic>Wastewater treatment</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Deng, Dongyang</creatorcontrib><creatorcontrib>Lin, Lian-Shin</creatorcontrib><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><jtitle>Water research (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Deng, Dongyang</au><au>Lin, Lian-Shin</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Continuous sulfidogenic wastewater treatment with iron sulfide sludge oxidation and recycle</atitle><jtitle>Water research (Oxford)</jtitle><addtitle>Water Res</addtitle><date>2017-05-01</date><risdate>2017</risdate><volume>114</volume><spage>210</spage><epage>217</epage><pages>210-217</pages><issn>0043-1354</issn><eissn>1879-2448</eissn><abstract>This study evaluated the technical feasibility of packed-bed sulfidogenic bioreactors dosed with ferrous chloride for continuous wastewater treatment over a 450-day period. In phase I, the bioreactors were operated under different combinations of carbon, iron, and sulfate mass loads without sludge recycling to identify optimal treatment conditions. A COD/sulfate mass ratio of 2 and a Fe/S molar ratio of 1 yielded the best treatment performance with COD oxidation rate of 786 ± 82 mg/(L⋅d), which resulted in 84 ± 9% COD removal, 94 ± 6% sulfate reduction, and good iron retention (99 ± 1%) under favorable pH conditions (6.2–7.0). In phase II, the bioreactors were operated under this chemical load combination over a 62-day period, during which 7 events of sludge collection, oxidation, and recycling were performed. The collected sludge materials contained both inorganic and organic matter with FeS and FeS2 as the main inorganic constituents. In each event, the sludge materials were oxidized in an oxidizing basin before recycling to mix with the wastewater influent. Sludge recycling yielded enhanced COD removal (90 ± 6% vs. 75 ± 7%), and better effluent quality in terms of pH (6.8 ± 0.1 vs. 6.5 ± 0.2), iron (0.7 ± 0.5 vs. 1.9 ± 1.7 mg/L), and sulfide-S (0.3 ± 0.1 vs. 0.4 ± 0.1 mg/L) removal compared to the baseline operation without sludge recycling during phase II. This process exhibited treatment stability with reasonable variations, and fairly consistent sludge content over long periods of operation under a range of COD/sulfate and Fe/S ratios without sludge recycling. The bioreactors were found to absorb recycling-induced changes efficiently without causing elevated suspended solids in the effluents. [Display omitted] •COD/sulfate = 2 (mass) and Fe/S = 1 (molar) resulted in favorable treatment.•Recycling oxidized sludge enhanced the treatment performance.•Evidence suggested co-existence of FeS and FeS2 in the bioreactor sludge.•Consistent solid content and VSS/TSS ratio of the sludge during long-term operation.</abstract><cop>England</cop><pub>Elsevier Ltd</pub><pmid>28249212</pmid><doi>10.1016/j.watres.2017.02.048</doi><tpages>8</tpages><orcidid>https://orcid.org/0000-0002-5578-4768</orcidid><oa>free_for_read</oa></addata></record>
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subjects Bioreactors
COD oxidation rate
COD/sulfate
Fe/S
Iron
Sewage - chemistry
Sludge recycle
Sulfides
Sulfidogenic
Waste Disposal, Fluid
Waste Water
Wastewater treatment
title Continuous sulfidogenic wastewater treatment with iron sulfide sludge oxidation and recycle
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