Z2-5464 — Annual report 2013
1.
Catalytic wet air oxidation of bisphenol A model solution in a trickle-bed reactor over titanate nanotube-based catalysts

Titanate nanotube-based catalysts were prepared via alkaline hydrothermal synthesis route followed by heat-treatment at different temperatures, ranging from 300 to 700 °C. The resulting metal-free solids were then applied as a catalyst in a three-phase trickle-bed reactor, where catalytic wet air oxidation (CWAO) reactions of model aqueous Bisphenol A (BPA) solution were performed. It was observed in the given range of operating conditions that BPA undergoes both non-catalytic as well as catalytic oxidation routes, while the latter is far more pronounced. At 210 °C and in the presence of 0.5 g of titanate nanotube-based catalyst, which was annealed at 600 °C, a complete BPA removal was obtained. From TOC point of view, approximately 70% conversion was achieved indicating the persistence of refractory intermediates of lower carboxylic acids.

COBISS.SI-ID: 5149722
2.
Titanate nanotubes as a novel catalyst for removal of toxicity and estrogenicity of bisphenol A in the CWAO process

Catalytic wet air oxidation (CWAO) of aqueous bisphenol A (BPA) solution was studied in a continuous-flow trickle-bed reactor in the presence of titanate nanotube-based catalysts. These active metal-free solids were prepared by alkaline hydrothermal synthesis followed by heat treatment at temperatures ranging from 300 to 700 °C, so that they would have varying physicochemical properties. The aim of the study was to investigate the removal efficiency of titanate nanotube-based catalysts used in the CWAO process to remove toxicity and estrogenicity of BPA at a very short space time of 0.6 min•gCAT•g−1. In addition, noncatalytic BPA degradation in the presence of inert SiC particles was also performed. As a result, significantly higher estrogenicity and toxic effects of the liquid-phase sample compared to the catalytic oxidation experiments were observed. Complete removal of estrogenicity and high reduction of toxicity from aqueous solution were achieved at 210 °C over 0.5 g of catalyst that had been annealed at 600 °C.

COBISS.SI-ID: 5312282
3.
Removal of bisphenol A and its oxidation products from aqueous solutions by sequential catalytic wet air oxidation and biodegradation

Model aqueous solution of bisphenol A (BPA) of 10 mg L–1 was treated in a continuous and sequential catalytic wet air oxidation (CWAO)/aerobic bioreactor (BR) system. Wet oxidation with titanate nanotube-based catalyst resulted in nearly complete removal of BPA () 99 %) at a very short space time of 0.3 min•gCAT•g–1. The main identified oxidation products in the CWAO effluent were acetic acid, formic acid and p-hydroxyacetophenone (p-HAP). All of these compounds were consequently and efficiently removed in the BR system at a hydraulic residence time (HRT) of 7.2 h. Although apparent toxicity of the CWAO effluent was found higher than of the initial BPA solution, the former could be successfully detoxified through aerobic biodegradation. The combined system thus presents a potential treatment process for the efficient removal of BPA and its oxidative derivatives from wastewaters.

COBISS.SI-ID: 5262106