6533b7d6fe1ef96bd1266621

RESEARCH PRODUCT

Desulfurization: Critical step towards enhanced selenium removal from industrial effluents

Nadia Morin-criniGrégorio CriniLucian C. StaicuLucian C. Staicu

subject

Environmental EngineeringHealth Toxicology and MutagenesisBarium Compoundschemistry.chemical_element02 engineering and technologyWastewater010501 environmental sciencesFerric Compounds01 natural sciencesSelenateSelenium pollutionWater PurificationSeleniumchemistry.chemical_compoundChlorides[CHIM.ANAL]Chemical Sciences/Analytical chemistryMetals HeavyEnvironmental ChemistryOrganic chemistrySulfateEffluentAnion Exchange ResinsComputingMilieux_MISCELLANEOUS0105 earth and related environmental sciencesIon exchangeSulfatesChemistryPublic Health Environmental and Occupational HealthGeneral MedicineGeneral Chemistry021001 nanoscience & nanotechnologyPollution6. Clean waterTrace ElementsFlue-gas desulfurization[ CHIM.POLY ] Chemical Sciences/Polymers[CHIM.POLY]Chemical Sciences/PolymersWastewater[ CHIM.ANAL ] Chemical Sciences/Analytical chemistry0210 nano-technologyWater Pollutants ChemicalSeleniumPower PlantsNuclear chemistry

description

Abstract Selenium (Se) removal from synthetic solutions and from real Flue Gas Desulfurization (FGD) wastewater generated by a coal-fired power plant was studied for the first time using a commercial iron oxide impregnated strong base anion exchange resin, Purolite ® FerrIX A33E. In synthetic solutions, the resin showed high affinity for selenate and selenite, while sulfate exhibited a strong competition for both oxyanions. The FGD wastewater investigated is a complex system that contains Se (∼1200 μg L −1 ), SO 4 2− (∼1.1 g L −1 ), Cl − (∼9.5 g L −1 ), and Ca 2+ (∼5 g L −1 ), alongside a broad spectrum of toxic trace metals including Cd, Cr, Hg, Ni, and Zn. The resin performed poorly against Se in the raw FGD wastewater and showed moderate to good removal of several trace elements such as Cd, Cr, Hg, and Zn. In FGD effluent, sulfate was identified as a powerful competing anion for Se, having high affinity for the exchange active sites of the resin. The desulfurization of the FGD effluent using BaCl 2 led to the increase in Se removal from 3% (non-desulfurized effluent) to 80% (desulfurized effluent) by combined precipitation and ion exchange treatment. However, complete desulfurization using equimolar BaCl 2 could not be achieved due to the presence of bicarbonate that acts as a sulfate competitor for barium. In addition to selenium and sulfate removal, several toxic metals were efficiently removed (Cd: 91%; Cr: 100%; Zn: 99%) by the combined (desulfurization and ion exchange) treatment.

10.1016/j.chemosphere.2016.12.132https://hal.archives-ouvertes.fr/hal-01664737