Search

Refractory pollutants often exist in wastewater after photocatalysis. Here, experiments, gas chromatography-mass spectrometry (GC–MS) analysis and density functional theory (DFT) simulations were used to explain the different levels of photocatalytic degradation of organics in papermaking wastewater associated with two photocatalytic processes with the goal of improving environmental sustainability. The photocatalytic experiments of flocculation and SBR effluents of papermaking wastewater were studied in a reactor with nano-TiO2 colloid, followed by GC–MS analysis, and the different degradation levels of organics were explained based on DFT adsorption and photocatalysis simulations. The experimental results show that the total COD removal rates were 65.8% and 90.8% for the flocculation-photocatalysis and SBR-photocatalysis processes, and the resin acids and fatty acids in wastewater were classified as easily degradable pollutants and esters as refractory pollutants. The adsorption and photocatalysis simulations show that compared with dehydroabietic acid and pentadecanoic acid, the adsorption of glycerol monostearate by nano-TiO2 colloid is difficult, the reaction pathways for photocatalysis are complex and the band gap of TiO2 photocatalyst after adsorption is wide. The experimental and simulation results indicate that the different degradation levels are attributed to the difficulty of the adsorption and photocatalytic reactions of glycerol monostearate compared with the reactions of the other two easily degradable pollutants. Thus, the different photocatalytic degradation levels of organic pollutants in the two photocatalytic processes of papermaking wastewater indicate that sustainable photocatalytic technology could be applied to different types of industrial wastewater.

Under microwave irradiation, raw sludge was pyrolyzed mainly by evaporation of water, with a weight loss ratio of 84.8% and a maximum temperature not exceeding 200 °C. High-temperature pyrolysis of SiC sludge could be realized, with a weight loss ratio of 93.4% and a final pyrolysis temperature of 1131.7 °C. Variations between the electric field intensity distribution are the main reason for the differences of pyrolysis efficiencies. HFSS simulation showed that the electric field intensity of the raw sludge gradually decreased from 2.94 × 10 4 V/m to 0.88 × 10 4 V/m when pyrolysis ends, while that of SiC sludge decreased from 3.73 × 10 4 V/m at the beginning to 1.28 × 10 4 V/m, then increased to 4.03 × 10 4 V/m. The electromagnetic effect is the main factor (r ≥ 0.91) influencing the temperature increase and weight loss of raw sludge. Both the electromagnetic effect and heat conduction effect influenced temperature rise and weight loss of SiC sludge, but the former’s influence was comparatively larger.

International audience; Adding catalyst could improve the yields and qualities of bio-gas and bio-oil, and realize the oriented production. Results showed that the catalytic gas-production capacities of CaO were higher than those of Fe2O3, and the bio-gas yield at 800°C reached a maximum of 35.1%. Because the polar cracking active sites of CaO reduced the activation energy of the pyrolysis reaction and resulted in high catalytic cracking efficiencies. In addition, the quality of bio-oil produced by CaO was superior to that by Fe2O3, although the bio-oil yield of CaO was relatively weak. The light bio-fuel oriented catalytic pyrolysis could be realized when adding different catalysts. At 800°C, CaO was 45% higher than Fe2O3 in aspect of H2 production while Fe2O3 was 103% higher than CaO in aspect of CH4 production. Therefore, CaO was more suitable for H2 production and Fe2O3 was more suitable for CH4 production.