A novel phosphorus (P) adsorbent, ferrihydrite-modified diatomite (FHMD) was developed and characterized in this study. The FHMD was made through surface modification treatments, including NaOH treatment and ferrihydrite deposition on raw diatomite. In the NaOH treatment, surface SiO2 was partially dissolved in the NaOH solution. The dissolved Si contributed to form stable 2-line ferrihydrite, which deposited into the larger mesopores and macropores of the diatomite. The 2-line ferrihydrite not only deposited into the pores of the diatomite but also aggregated on the surface. Filling the larger mesopores and macropores of the diatomite and aggregation on the diatomite surface with 0.24 g Fe/g of 2-line ferrihydrite resulted in a specific surface area of 211.1 m2/g for the FHMD, which is an 8.5-fold increase over the raw diatomite (24.77 m2/g). The surface modification also increased the point of zero charge (pHPZC) values to 10 for the FHMD from 5.8 for the raw diatomite.<p> Effects of the formation process parameters such as concentrations of FeCl2, NaOH, and drying temperature on the formation mechanism and crystalline characteristics of FHMD were studied by using X-ray absorption near-edge structure (XANES) spectroscopy. The spectra were recorded in both the total electron yield (TEY) and the fluorescence yield (FY) modes to investigate the chemical nature of Fe and Si on the surface and in the bulk of ferrihydrite-modified diatomite, respectively. It was found that only the surface SiO2 was partially dissolved in the NaOH solution with stirring and heating, whereas the bulk of diatomite seemed to be preserved. The dissolved Si was incorporated into the structure of ferrihydrite to form the 2-line Si-containing ferrihydrite. The crystalline degree of ferrihydrite increased with the increasing FeCl2 concentration and the Brunauer-Emmett-Teller (BET) specific surface area of FHMD decreased with the increasing FeCl2 concentration. The NaOH solution of higher concentration partially dissolved more surface SiO2 and the crystalline degree of ferrihydrite decreased with the increase in NaOH concentration. The dehydroxylation on the surface of FHMD occurred in the high temperature calcination, causing an energy shift in the Si L-edge spectra to the high energy side and an increase in the crystalline degree of ferrihydrite. In this study, the optimal synthesis conditions for the FHMD with the least crystalline degree and the highest surface area were found to be as the follows: 100 mL of 0.5M FeCl2 solution, 6M NaOH solution and the drying temperature of 50 ºC.<p> Phosphorus adsorption behavior and adsorption mechanism of FHMD were investigated in the research. The Langmuir model best described the P adsorption data for FHMD. Because of increased surface area and surface charge, the maximum adsorption capacity of FHMD at pH 4 and pH 8.5 was increased from 10.2 mg P/g and 1.7 mg P/g of raw diatomite to 37.3 mg P/g and 13.6 mg P/g, respectively. Phosphorus showed the best affinity of adsorption onto FHMD among common anions. K-edge P XANES spectra demonstrate that P is not precipitated with Fe (III) of FHMD, but adsorbed on the surface layer of FHMD.<p> Phosphorus removal from lake water and limiting phosphorus release from sediment by FHMD was examined. Phosphorus removal from lake water proceeded primarily through P adsorption onto the surface of FHMD. When a dose of FHMD of 250 mg/L was applied to lake water, a total phosphorus (TP) removal efficiency of 88% was achieved and a residual TP concentration was 17.0 µg/L which falls within the oligotrophic TP range (3.0-17.7 µg/L). FHMD settled down to the bottom of the 43 cm high cylinder within 6 hours, which suggested that retention time of FHMD in the 5.5 m of Jackfish lake water column was close to the equilibrium time of P adsorption onto FHMD (72 hours). During the 30-day anoxic incubation period, TP concentrations in lake water treated by 400, 500 and 600 mg/L of FHMD showed a slight decrease and maximum TP concentrations remained at levels lower than 15 µg/L. The addition of FHMD resulted in a marked increase in Fe-P fraction, a pronounced decrease in labile-P and organic-P fractions, and stable Al-P, Ca-P and residual-P fractions. The effect of FHMD on limiting P release was comparable with those of the combination of FHMD and alum solutions with logarithmic ratios of Al to mobile P of 0.5 and 0.8. FHMD not only can effectively remove P from lake water but also keep a strong P-binding capacity under anoxic conditions and competition for P with alum at high amounts.<p> The role of gypsum on stabilizing sediment and the optimum dose of gypsum were investigated. The effectiveness of gypsum in stabilizing sediment was proved by the fact that at the same agitation speed, turbidities and soluble reactive P (SRP) concentrations of samples treated with gypsum were much lower than those of sample without gypsum. The optimal thickness of the gypsum layer was found to be 0.8 cm.<p> Combined application of FHMD and gypsum to P control was investigated in the research. It was found in the 30-day incubation of lake water and sediment treated by FHMD and gypsum that no P release seemed to occur regardless of oxic or anoxic conditions. In order to investigate the 120-day effects of FHMD and gypsum on the P control under anoxic and agitation conditions a lab-scale artificial aquarium was established in an environmental chamber. Daily oscillation of a metal grid did not yield the sediment resuspension due to the gypsum stabilization. The combined application of FHMD and gypsum resulted in a 1 g/L increase in the SO42- concentration in the 120-day aquarium compared with that in the control aquarium; however it did not affect the total kjeldahl nitrogen (TKN) concentrations in both the control aquarium and the 120-day aquarium. The addition of FHMD and gypsum enhanced total alkalinity in the 120-day aquarium, thereby improving buffering capacity of lake water. Under anoxic conditions and sediment resuspension conditions, relative to a large increase in total P (TP) concentrations in the control aquarium, TP concentrations in the 120-day aquarium stayed relatively stable, fluctuating within the range of 9.1-13.3 µg/L. Relative to control sediment, Fe-P was significantly enhanced during the 60-day incubation; however, Fe-P did not appear to increase significantly in the second 60-day incubation. Labile-P and organic-P decreased with sediment depths in both control aquarium and test aquariums; however, Al-P, Ca-P and residue-P increased with sediment depth. Lower Al-P is observed in treatment aquariums than in control sediment.<p> As an effective P adsorbent, FHMD showed a high adsorption capacity as well as a significantly higher affinity for P than other anions. A combined application of FHMD and gypsum effectively reduced sediment resuspension and maintained TP levels within the oligotrophic range under anoxic conditions in the laboratory-scale artificial aquarium.

A novel phosphorus (P) adsorbent, ferrihydrite-modified diatomite (FHMD) was developed and characterized in this study. The FHMD was made through surface modification treatments, including NaOH treatment and ferrihydrite deposition on raw diatomite. In the NaOH treatment, surface SiO2 was partially dissolved in the NaOH solution. The dissolved Si contributed to form stable 2-line ferrihydrite, which deposited into the larger mesopores and macropores of the diatomite. The 2-line ferrihydrite not only deposited into the pores of the diatomite but also aggregated on the surface. Filling the larger mesopores and macropores of the diatomite and aggregation on the diatomite surface with 0.24 g Fe/g of 2-line ferrihydrite resulted in a specific surface area of 211.1 m2/g for the FHMD, which is an 8.5-fold increase over the raw diatomite (24.77 m2/g). The surface modification also increased the point of zero charge (pHPZC) values to 10 for the FHMD from 5.8 for the raw diatomite.<p> Effects of the formation process parameters such as concentrations of FeCl2, NaOH, and drying temperature on the formation mechanism and crystalline characteristics of FHMD were studied by using X-ray absorption near-edge structure (XANES) spectroscopy. The spectra were recorded in both the total electron yield (TEY) and the fluorescence yield (FY) modes to investigate the chemical nature of Fe and Si on the surface and in the bulk of ferrihydrite-modified diatomite, respectively. It was found that only the surface SiO2 was partially dissolved in the NaOH solution with stirring and heating, whereas the bulk of diatomite seemed to be preserved. The dissolved Si was incorporated into the structure of ferrihydrite to form the 2-line Si-containing ferrihydrite. The crystalline degree of ferrihydrite increased with the increasing FeCl2 concentration and the Brunauer-Emmett-Teller (BET) specific surface area of FHMD decreased with the increasing FeCl2 concentration. The NaOH solution of higher concentration partially dissolved more surface SiO2 and the crystalline degree of ferrihydrite decreased with the increase in NaOH concentration. The dehydroxylation on the surface of FHMD occurred in the high temperature calcination, causing an energy shift in the Si L-edge spectra to the high energy side and an increase in the crystalline degree of ferrihydrite. In this study, the optimal synthesis conditions for the FHMD with the least crystalline degree and the highest surface area were found to be as the follows: 100 mL of 0.5M FeCl2 solution, 6M NaOH solution and the drying temperature of 50 ºC.<p> Phosphorus adsorption behavior and adsorption mechanism of FHMD were investigated in the research. The Langmuir model best described the P adsorption data for FHMD. Because of increased surface area and surface charge, the maximum adsorption capacity of FHMD at pH 4 and pH 8.5 was increased from 10.2 mg P/g and 1.7 mg P/g of raw diatomite to 37.3 mg P/g and 13.6 mg P/g, respectively. Phosphorus showed the best affinity of adsorption onto FHMD among common anions. K-edge P XANES spectra demonstrate that P is not precipitated with Fe (III) of FHMD, but adsorbed on the surface layer of FHMD.<p> Phosphorus removal from lake water and limiting phosphorus release from sediment by FHMD was examined. Phosphorus removal from lake water proceeded primarily through P adsorption onto the surface of FHMD. When a dose of FHMD of 250 mg/L was applied to lake water, a total phosphorus (TP) removal efficiency of 88% was achieved and a residual TP concentration was 17.0 µg/L which falls within the oligotrophic TP range (3.0-17.7 µg/L). FHMD settled down to the bottom of the 43 cm high cylinder within 6 hours, which suggested that retention time of FHMD in the 5.5 m of Jackfish lake water column was close to the equilibrium time of P adsorption onto FHMD (72 hours). During the 30-day anoxic incubation period, TP concentrations in lake water treated by 400, 500 and 600 mg/L of FHMD showed a slight decrease and maximum TP concentrations remained at levels lower than 15 µg/L. The addition of FHMD resulted in a marked increase in Fe-P fraction, a pronounced decrease in labile-P and organic-P fractions, and stable Al-P, Ca-P and residual-P fractions. The effect of FHMD on limiting P release was comparable with those of the combination of FHMD and alum solutions with logarithmic ratios of Al to mobile P of 0.5 and 0.8. FHMD not only can effectively remove P from lake water but also keep a strong P-binding capacity under anoxic conditions and competition for P with alum at high amounts.<p> The role of gypsum on stabilizing sediment and the optimum dose of gypsum were investigated. The effectiveness of gypsum in stabilizing sediment was proved by the fact that at the same agitation speed, turbidities and soluble reactive P (SRP) concentrations of samples treated with gypsum were much lower than those of sample without gypsum. The optimal thickness of the gypsum layer was found to be 0.8 cm.<p> Combined application of FHMD and gypsum to P control was investigated in the research. It was found in the 30-day incubation of lake water and sediment treated by FHMD and gypsum that no P release seemed to occur regardless of oxic or anoxic conditions. In order to investigate the 120-day effects of FHMD and gypsum on the P control under anoxic and agitation conditions a lab-scale artificial aquarium was established in an environmental chamber. Daily oscillation of a metal grid did not yield the sediment resuspension due to the gypsum stabilization. The combined application of FHMD and gypsum resulted in a 1 g/L increase in the SO42- concentration in the 120-day aquarium compared with that in the control aquarium; however it did not affect the total kjeldahl nitrogen (TKN) concentrations in both the control aquarium and the 120-day aquarium. The addition of FHMD and gypsum enhanced total alkalinity in the 120-day aquarium, thereby improving buffering capacity of lake water. Under anoxic conditions and sediment resuspension conditions, relative to a large increase in total P (TP) concentrations in the control aquarium, TP concentrations in the 120-day aquarium stayed relatively stable, fluctuating within the range of 9.1-13.3 µg/L. Relative to control sediment, Fe-P was significantly enhanced during the 60-day incubation; however, Fe-P did not appear to increase significantly in the second 60-day incubation. Labile-P and organic-P decreased with sediment depths in both control aquarium and test aquariums; however, Al-P, Ca-P and residue-P increased with sediment depth. Lower Al-P is observed in treatment aquariums than in control sediment.<p> As an effective P adsorbent, FHMD showed a high adsorption capacity as well as a significantly higher affinity for P than other anions. A combined application of FHMD and gypsum effectively reduced sediment resuspension and maintained TP levels within the oligotrophic range under anoxic conditions in the laboratory-scale artificial aquarium.

O presente trabalho trata do desenvolvimento um novo material, diatomita modificada por ferro, como ativador dos oxidantes persulfato de sódio e peróxido de hidrogênio para degradar poluentes prioritários (fenantreno e antraceno), diesel e o poluente emergente ácido perfluoroctanóico (PFOA). Os objetivos deste estudo foram comparar esse novo método com métodos convencionais de ativação para esses oxidantes; e estudar, estatisticamente, a relação ótima entre a quantidade deste material e a concentração de oxidante para a degradação dos contaminantes. A diatomita bruta e as diatomitas modificadas (CAT-5 e CAT-20) foram caracterizadas por diferentes técnicas. Os principais resultados da caracterização mostraram que os materiais são amorfos e que a concentração de ferro foi 4%, 17% e 25% para diatomita bruta, CAT-5 e CAT-20, respectivamente. Os resultados mostraram que os materiais modificados apresentaram significativa atividade catalítica para ativar os oxidantes e degradar os poluentes, sendo a CAT-5 a mais reativa. Resultados satisfatórios foram obtidos utilizando 45 g L-1 de persulfato de sódio com 2,5 g de diatomita modificada (CAT-5), com degradação de 87% e 96% de fenantreno e antraceno, respectivamente, em 168 horas de tratamento. Para o tratamento de solo arenoso contaminado com diesel, os melhores resultados foram obtidos utilizando 41 g L-1 de persulfato de sódio e 1,56 g de CAT-5, obtendo decaimento de 91% de carbono total em 146 horas. A eficiência da decomposição de PFOA mostra que a reatividade dos sistemas seguiu a ordem: peróxido de hidrogênio em altas concentrações > peróxido de hidrogênio em paralelo com persulfato > persulfato alcalino, ambos ativados com CAT-5, atingindo 86%, 69% e 48%, respectivamente, após 6 horas de reação. / The present work deals with the development of a new materials, modified diatomite by iron, as an activator of the oxidants sodium persulfate and hydrogen peroxide to degrade priority pollutants (phenantherene and anthracene), diesel and emerging pollutant perfluorooctanoic acid (PFOA). The aims of this study were to compare this new method with traditional activation method for these oxidants; and to study, statistically, the optimal ratio between the quantity of the material and the concentration of oxidant to the degradation of contaminants. The raw and modified materials were characterized by different techniques. The main characterization results showed that materials are amorphous, and that the iron concentrations were 4,78%, 17,65% and 25% for the raw diatomite, CAT-5 and CAT-20, respectively. The results showed that the modified material showed significant catalytic activity to activate the oxidants and to degrade pollutants, with CAT-5 being the most reactive. Satisfactory results were obtained using 2,5 g of modified diatomite (CAT-%) with sodium persulfate at 45 g L-1, with degradation of 87% and 96% of phenanthrene and anthracene, respectively, in 168 hours of treatment. For the treatment of sandy soil contaminated with diesel, the best result was obtained using 41 g L-1 of sodium persulfate sodium and 1,56 g of CAT-5, resulting in a decrease of 91% of total carbon present in diesel. The PFOA decomposition efficiency for the systems shows that hydrogen peroxide at high concentrations > hydrogen peroxide-activated persulfate > alkaline-activated persulfate, both with CAT-5, achieving 83%, 69% and 48% , respectively, after 6 hours of reaction.

O presente trabalho trata do desenvolvimento um novo material, diatomita modificada por ferro, como ativador dos oxidantes persulfato de sódio e peróxido de hidrogênio para degradar poluentes prioritários (fenantreno e antraceno), diesel e o poluente emergente ácido perfluoroctanóico (PFOA). Os objetivos deste estudo foram comparar esse novo método com métodos convencionais de ativação para esses oxidantes; e estudar, estatisticamente, a relação ótima entre a quantidade deste material e a concentração de oxidante para a degradação dos contaminantes. A diatomita bruta e as diatomitas modificadas (CAT-5 e CAT-20) foram caracterizadas por diferentes técnicas. Os principais resultados da caracterização mostraram que os materiais são amorfos e que a concentração de ferro foi 4%, 17% e 25% para diatomita bruta, CAT-5 e CAT-20, respectivamente. Os resultados mostraram que os materiais modificados apresentaram significativa atividade catalítica para ativar os oxidantes e degradar os poluentes, sendo a CAT-5 a mais reativa. Resultados satisfatórios foram obtidos utilizando 45 g L-1 de persulfato de sódio com 2,5 g de diatomita modificada (CAT-5), com degradação de 87% e 96% de fenantreno e antraceno, respectivamente, em 168 horas de tratamento. Para o tratamento de solo arenoso contaminado com diesel, os melhores resultados foram obtidos utilizando 41 g L-1 de persulfato de sódio e 1,56 g de CAT-5, obtendo decaimento de 91% de carbono total em 146 horas. A eficiência da decomposição de PFOA mostra que a reatividade dos sistemas seguiu a ordem: peróxido de hidrogênio em altas concentrações > peróxido de hidrogênio em paralelo com persulfato > persulfato alcalino, ambos ativados com CAT-5, atingindo 86%, 69% e 48%, respectivamente, após 6 horas de reação. / The present work deals with the development of a new materials, modified diatomite by iron, as an activator of the oxidants sodium persulfate and hydrogen peroxide to degrade priority pollutants (phenantherene and anthracene), diesel and emerging pollutant perfluorooctanoic acid (PFOA). The aims of this study were to compare this new method with traditional activation method for these oxidants; and to study, statistically, the optimal ratio between the quantity of the material and the concentration of oxidant to the degradation of contaminants. The raw and modified materials were characterized by different techniques. The main characterization results showed that materials are amorphous, and that the iron concentrations were 4,78%, 17,65% and 25% for the raw diatomite, CAT-5 and CAT-20, respectively. The results showed that the modified material showed significant catalytic activity to activate the oxidants and to degrade pollutants, with CAT-5 being the most reactive. Satisfactory results were obtained using 2,5 g of modified diatomite (CAT-%) with sodium persulfate at 45 g L-1, with degradation of 87% and 96% of phenanthrene and anthracene, respectively, in 168 hours of treatment. For the treatment of sandy soil contaminated with diesel, the best result was obtained using 41 g L-1 of sodium persulfate sodium and 1,56 g of CAT-5, resulting in a decrease of 91% of total carbon present in diesel. The PFOA decomposition efficiency for the systems shows that hydrogen peroxide at high concentrations > hydrogen peroxide-activated persulfate > alkaline-activated persulfate, both with CAT-5, achieving 83%, 69% and 48% , respectively, after 6 hours of reaction.