Per- and polyfluoroalkyl substances (PFAS) are fluorinated and refractory pollutants that are ubiquitous in industrial wastewater. Photocatalytic destruction of such pollutants with catalysts such as TiO and ZnO is an attractive avenue for removal of PFAS, but refined forms of such photocatalysts are expensive. This study, for the first time, utilized milled unrefined raw mineral ilmenite, coupled to UV-C irradiation to achieve mineralization of the two model PFAS compounds perfluorooctanoic acid (PFOA) and perfluoro octane sulfonic acid (PFOS).
View Article and Find Full Text PDFThis case study assesses the valorization of industrial wastewater streams for bioenergy generation in an industrial munition facility. On-site pilot-scale demonstrations were performed to investigate the feasibility of algal growth in the target wastewater on a larger outdoor scale. An exploratory field study followed by an optimized one were carried out using two 1000 L open raceway ponds deployed within a greenhouse at an industrial munition facility.
View Article and Find Full Text PDFA novel Mg-based bimetal reagent (Mg/Cu) was used as an enhanced reductive system to degrade insensitive munition 2,4-dinitroanisole (DNAN), a contaminant found in energetic-laden waste. Degradation of DNAN was significantly impacted by dissolved oxygen and studied in anoxic and oxic bimetal systems (i.e.
View Article and Find Full Text PDFAmine-modified wheat straw (AMWS) has already been reported as a promising adsorbent for nitrate (NO) removal due to its cost-effectiveness and high efficiency. However, the NO removal mechanism has not been well understood, especially in the presence of co-existing ions. Here, the effect of co-existing anions on NO removal by AMWS was investigated and the underlying mechanisms were revealed using a combination of in-situ infrared (IR) spectroscopy and computational modeling.
View Article and Find Full Text PDFCarbonate precipitation, as part of the carbon dioxide (CO) mineralization process, is generally regarded as a high-temperature, high-pressure, and high-purity CO process. Typical conditions consist of temperatures around 120 °C and a pressure of 100 bar of pure CO, making the process costly. A major challenge facing carbonate precipitation is performing the reaction at low temperatures and low partial pressures of CO (p) such as 25 °C and CO flue gas concentration.
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