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Combined biologic removal of sulphate for tanning industrial wastewaters

dc.contributor.authorDi Berardino, Santino
dc.date.accessioned2010-04-08T10:49:33Z
dc.date.available2010-04-08T10:49:33Z
dc.date.issued2009-08-08
dc.description.abstractA biologic pretreatment technology of mixed tanneries wastewater, suitable for sulphate-rich industrial wastewaters, has been studied, in order to eliminate chemical precipitation and improve removal efficiency of the relevant pollutants. It couples an anaerobic reactor with an aerobic sulphide oxidant (ASO) step, where H2S2 is partially oxidized to elemental sulphur, and includes a recirculation system. The proposed solution provided Methanogenic Archae (MA) and Sulphate Reducing Bacteria (SRB) coexistence and controlled inhibition by partial oxidation of hydrogen sulphide.. The removal effiency of the anaerobic reactor was quite dependent on temperature and hydaulic retention time (HRT). COD removal varied between 32-68 % and sulphate removal (20-60%), referred to the mixture of the industrial effluent diluted with 50% of recirculation, at an Organic Load (OL) ranging from 0.5 to 1.5 kg CODM³ d⁻¹ and HRT from 1 to 5 days. The entire biologic pretreatment (AHF+ASO) resulted much more efficient and COD removal increased to 64-82% being less dependent on temperature variations. This process removed also a significant part (85%) of Chromium (Cr⁺³), by sorption into the biologic sludge. This two step biologic pretreatment, ensured better removal of relevant parameters than conventional chemical precipitation, avoided addition of chemical products, minimized excess sludge production, and also removed hydrogen sukphide and sulphate, resulting in a favorable alternative solution. The effluent from this stage was submitted to a sequencing batch nitrification/denitrification step, to improve the removal of the relevenat parameters. The average removal efficiency of entire process was appreciable and better than the conventional solution: COD = 88%, Sulphate = 68% and Nitrogen (kjeldahl) = 92%, chromium (Cr⁺³=96%). However, the presence of non degradable organic compounds delivered in the effluent from syntetic tanning, were hard to remove completely and did not allow fulfilling the severe standards for wastewater discharge in water course in terms of COD, Nitrogen (kjeldahl) and color. This requires and additional polishing steppt
dc.identifier.citationDi Berardino, Santino. Combined biologic removal of sulphate for tanning industrial wastewater. In: 12th IWA Sludge Conference - Sustainable Management of Water & Wastewater Sludge, Harbin, China, August 8-10, 2009, 6p.pt
dc.identifier.urihttp://hdl.handle.net/10400.9/597
dc.language.isoengpt
dc.subjectTanneries wastewater treatmentpt
dc.subjectAnaerobic digestionpt
dc.subjectBiogas productionpt
dc.subjectSulphate reductionpt
dc.subjectSulphide removalpt
dc.subjectThiobacteriapt
dc.titleCombined biologic removal of sulphate for tanning industrial wastewaterspt
dc.typeconference object
dspace.entity.typePublication
oaire.citation.conferencePlaceHarbin-Chinapt
oaire.citation.title12th IWA Sludge Conference - Sustainable Management of Water & Wastewater Sludgept
person.familyNameDi Berardino
person.givenNameSantino
person.identifier.orcid0000-0002-1286-4178
person.identifier.ridP-4062-2015
person.identifier.scopus-author-id55188504700
rcaap.rightsopenAccesspt
rcaap.typeconferenceObjectpt
relation.isAuthorOfPublication5b05d792-bc63-4b68-98ee-540c213f19ff
relation.isAuthorOfPublication.latestForDiscovery5b05d792-bc63-4b68-98ee-540c213f19ff

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