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Specialist Group on ANAEROBIC DIGESTION Newsletter - IWA

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Sulfate reducing biological processes in biofilms for metal precipitati<strong>on</strong><br />

by Marisol Gallegos García (mgg@ipicyt.edu.mx)<br />

Instituti<strong>on</strong>:<br />

Instituto Potosino de Investigación Científica y Tecnológica.<br />

División de Ciencias Ambientales.<br />

Camino a la Presa San José 2055. Lomas 4ª Sección.<br />

San Luis Potosí, SLP. México. 78216<br />

Supervisors:<br />

Dr. Elías Razo-Flores<br />

Dra. Mª. Lourdes Berenice Celis-García<br />

Abstract:<br />

The envir<strong>on</strong>ment c<strong>on</strong>taminati<strong>on</strong> by heavy metals is an important matter due to its negative impact over the<br />

public health, the envir<strong>on</strong>ment and the ec<strong>on</strong>omy. Sulfate reducti<strong>on</strong> has become and alternative for the treatment<br />

of wastewaters that c<strong>on</strong>tain heavy metals. The general objective of this work was to study the applicati<strong>on</strong> of<br />

biological sulfate reducti<strong>on</strong> processes in biofilm reactors for metal precipitati<strong>on</strong> and recovery of the metal<br />

sulfides in <strong>on</strong>e step. First of all, the competence between methanogens and sulfate reducers was studied in an<br />

UASB reactor that was operated for over 240 days, for the development of sulfate reducing biomass from a<br />

methanogenic granular sludge. The chemical oxygen demand (COD) removed by sulfate reducti<strong>on</strong> was 20% and<br />

the total sulfide c<strong>on</strong>centrati<strong>on</strong> reached in the reactor was 310 mg/L. The specific sulfate reducing and<br />

methanogenic activities of the granular sludge pointed out to the development of sulfate reducing bacteria<br />

(SRB). The presence of SRB that oxidize incompletely the substrate to acetate, allowed the permanence of<br />

methanogens that were not limited by substrate, and in c<strong>on</strong>sequence were not completely displaced by the SRB<br />

at the end of reactor operati<strong>on</strong>. Afterwards, a down-flow fluidized bed reactor (DFFB) was proposed for the<br />

precipitati<strong>on</strong> and recovery of metals. The DFFB reactor was operated c<strong>on</strong>tinuously during 320 days and<br />

precipitati<strong>on</strong> efficiencies over 99.0% of Fe, Zn and Cd were obtained. The recovered metal sulfides amounted to<br />

90% of the theoretical mass expected to be precipitated; pyrite (FeS), sphaleryte (ZnS) and greenockite (CdS)<br />

predominated in the precipitate. The metal loading rate did not affect the reactor performance even at pH values<br />

as low as 5.0. The COD removal efficiency was close to 54%, which suggested an incomplete substrate<br />

oxidati<strong>on</strong> by the immobilized SRB, this was c<strong>on</strong>firmed by the high c<strong>on</strong>centrati<strong>on</strong> of acetate in the effluent and<br />

the absence of alkalinity producti<strong>on</strong>. Finally, the development of a sulfate reducing biofilm able to oxidize<br />

completely the substrate was studied. To achieve this, a selecti<strong>on</strong> pressure by substrate was used; three different<br />

assays were carried out in the DFFB reactor that was fed with a mixture of acetate/lactate with the following<br />

ratios <strong>on</strong> a COD basis: 50/50, 80/20 and 90/10 during 21 days. The best biofilm performance in terms of COD<br />

removal efficiency (71%) and sulfide producti<strong>on</strong> rate (2.9 mg H 2 S/L-h) was obtained with the biofilm developed<br />

in the experiment with the 90/10 acetate/lactate ratio. With this biofilm, the reactor was operated c<strong>on</strong>tinuously<br />

110 days. When the pH in the fed was decreased to 4.0, any inhibitory effect was observed over the SRB, as the<br />

reactor performance showed which achieved COD and sulfate removal efficiencies of 80 and 42%, respectively.<br />

The alkalinity produced by the complete oxidati<strong>on</strong> of the substrate neutralized the influent pH, and maintained a<br />

pH of 7.0 within the reactor. This work is the first to report the precipitati<strong>on</strong> and recovery of metals as metal<br />

sulfides in <strong>on</strong>e step and the development, in a short period of time, of a SRB biofilm able to oxidize completely<br />

the substrate.<br />

Link to Thesis: http://www.ipicyt.edu.mx/storage-sipicyt/materialbiblioteca/GallegosGarc%edaMarisol.pdf<br />

List of publicati<strong>on</strong>s:<br />

Gallegos-García, M., et al. (2009). Precipitati<strong>on</strong> and recovery of metal sulfides from metal c<strong>on</strong>taining acidic<br />

wastewater in a sulfidogenic down-flow fluidized bed reactor. Biotechnol Bioeng. 102, 91-99.<br />

doi.wiley.com/10.1002/bit.22049<br />

Gallegos-García, M., et al. (2008). Competencia por sustrato durante el desarrollo de Biomasa sulfato reductora<br />

a partir de un lodo metanogénico en un reactor UASB. Sometido, a la Revista Internaci<strong>on</strong>al de<br />

C<strong>on</strong>taminación Ambiental.<br />

Gallegos-García, M., et al. (In preparati<strong>on</strong>). Formati<strong>on</strong> of a sulfate-reducing biofilm of complete oxidati<strong>on</strong> of the<br />

substrate for the treatment of a synthetic effluent with sulfate.<br />

<strong>IWA</strong> <str<strong>on</strong>g>Specialist</str<strong>on</strong>g> <str<strong>on</strong>g>Group</str<strong>on</strong>g> <strong>on</strong> Anaerobic Digesti<strong>on</strong><br />

18 June 2009 <strong>Newsletter</strong>

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