Abstract:Abstract. A 1-x A x BO 3 belongs to the perovskite oxides of the ABO 3 structure. In this study, nanoparticles of La 0.5 Ca 0.5 FeO 3 were fabricated by sol-gel citrate technique. A series of common analytical techniques were used to characterize the crystallinity, morphology, specific surface area, and grain size of the nanopowders. These properties were characterised by means of XRD, SEM, EDX and FTIR. The calculated particles size using the Scherrer's formula was about 20 nm. Moreover, the family of perovsk… Show more
“…Perovskite oxides with ABO 3 structure have been reported to be promising catalysts for oxidative removal of organic dyes in aqueous solution [11][12][13], owing to their high hydrothermal stability as well as the unique properties such as controllable oxygen vacancy and oxidation state of B-site cation, and the ability to accommodate various metal ions without destroying the matrix structure [14,15]. For example, the iron ions, which are the major components of the traditional Fenton catalyst, can be located in perovskite framework like LaFeO 3 and used as solid catalyst for M A N U S C R I P T A C C E P T E D ACCEPTED MANUSCRIPT 4 RhB oxidation [16,17].…”
On the mechanism of oxidative degradation of rhodamine B over LaFeO 3 catalysts supported on silica materials: Role of support, Microporous and Mesoporous Materials (2015),
AbstractThis work aims to investigate the role of silica support in the catalytic oxidation of rhodamine B (RhB) over LaFeO 3 -Silica composites. Four LaFeO 3 -Silica composites using mesoporous silica (SBA-15, SBA-16, MCF) and nano-sized silica powder (NSP) as supports are prepared. XRD, N 2 physisorption isotherms and TEM results show that pure LaFeO 3 phase, with particle size of 15-20 nm, is prepared and the texture of supports remains unchanged after the deposition of LaFeO 3 .Catalytic results show that, besides the function to disperse LaFeO 3 on the surface, the support plays two important roles in the reaction: one is to absorb RhB from solution to the pores of support, and the other is to transport RhB from the pores to the active site, both influence the catalytic efficiency. Thus the non-porous NSP with negligible capacity for RhB adsorption is the worst, and the MCF with considerable capacity for RhB adsorption and the strongest ability to transport RhB to the active site is the best support of LaFeO 3 for RhB oxidation. SBA-15 and SBA-16, although show considerable or even higher capacity for RhB adsorption relative to MCF, their contribution to the reaction is less due to the low efficiency of transporting RhB to the active site. On these bases, the role of silica support in RhB oxidation conducted over LaFeO 3 -Silica composite is proposed.
“…Perovskite oxides with ABO 3 structure have been reported to be promising catalysts for oxidative removal of organic dyes in aqueous solution [11][12][13], owing to their high hydrothermal stability as well as the unique properties such as controllable oxygen vacancy and oxidation state of B-site cation, and the ability to accommodate various metal ions without destroying the matrix structure [14,15]. For example, the iron ions, which are the major components of the traditional Fenton catalyst, can be located in perovskite framework like LaFeO 3 and used as solid catalyst for M A N U S C R I P T A C C E P T E D ACCEPTED MANUSCRIPT 4 RhB oxidation [16,17].…”
On the mechanism of oxidative degradation of rhodamine B over LaFeO 3 catalysts supported on silica materials: Role of support, Microporous and Mesoporous Materials (2015),
AbstractThis work aims to investigate the role of silica support in the catalytic oxidation of rhodamine B (RhB) over LaFeO 3 -Silica composites. Four LaFeO 3 -Silica composites using mesoporous silica (SBA-15, SBA-16, MCF) and nano-sized silica powder (NSP) as supports are prepared. XRD, N 2 physisorption isotherms and TEM results show that pure LaFeO 3 phase, with particle size of 15-20 nm, is prepared and the texture of supports remains unchanged after the deposition of LaFeO 3 .Catalytic results show that, besides the function to disperse LaFeO 3 on the surface, the support plays two important roles in the reaction: one is to absorb RhB from solution to the pores of support, and the other is to transport RhB from the pores to the active site, both influence the catalytic efficiency. Thus the non-porous NSP with negligible capacity for RhB adsorption is the worst, and the MCF with considerable capacity for RhB adsorption and the strongest ability to transport RhB to the active site is the best support of LaFeO 3 for RhB oxidation. SBA-15 and SBA-16, although show considerable or even higher capacity for RhB adsorption relative to MCF, their contribution to the reaction is less due to the low efficiency of transporting RhB to the active site. On these bases, the role of silica support in RhB oxidation conducted over LaFeO 3 -Silica composite is proposed.
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