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Relevant bibliographies by topics / Catalytic wet peroxide oxidation

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Journal articles

Academic literature on the topic 'Catalytic wet peroxide oxidation'

Author: Grafiati

Published: 4 June 2021

Last updated: 26 April 2022

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Journal articles on the topic "Catalytic wet peroxide oxidation"

1

Sanabria, Nancy R., Rafael Molina, and Sonia Moreno. "Development of Pillared Clays for Wet Hydrogen Peroxide Oxidation of Phenol and Its Application in the Posttreatment of Coffee Wastewater." International Journal of Photoenergy 2012 (2012): 1–17. http://dx.doi.org/10.1155/2012/864104.

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This paper focuses on the use of pillared clays as catalysts for the Fenton-like advanced oxidation, specifically wet hydrogen peroxide catalytic oxidation (WHPCO). This paper discusses the limitations on the application of a homogeneous Fenton system, development of solid catalysts for the oxidation of phenol, advances in the synthesis of pillared clays, and their potential application as catalysts for phenol oxidation. Finally, it analyzes the use of pillared clays as heterogeneous Fenton-like catalysts for a real wastewater treatment, emphasizing the oxidation of phenolic compounds present

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2

Garcia-Costa, Alicia L., Juan A. Zazo, and Jose A. Casas. "Microwave-assisted catalytic wet peroxide oxidation: Energy optimization." Separation and Purification Technology 215 (May 2019): 62–69. http://dx.doi.org/10.1016/j.seppur.2019.01.006.

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3

Jiao, Zhaojie, Guilin Zhou, Haidong Zhang, Yu Shen, Xianming Zhang, and Xu Gao. "Degrading quinoline wastewater by catalytic wet peroxide oxidation." DESALINATION AND WATER TREATMENT 124 (2018): 256–66. http://dx.doi.org/10.5004/dwt.2018.22727.

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4

Pariente, M. I., J. A. Melero, F. Martínez, J. A. Botas, and A. I. Gallego. "Catalytic wet hydrogen peroxide oxidation of a petrochemical wastewater." Water Science and Technology 61, no. 7 (2010): 1829–36. http://dx.doi.org/10.2166/wst.2010.875.

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Continuous Catalytic Wet Hydrogen Peroxide Oxidation (CWHPO) for the treatment of a petrochemical industry wastewater has been studied on a pilot plant scale process. The installation, based on a catalytic fixed bed reactor (FBR) coupled with a stirred tank reactor (STR), shows an interesting alternative for the intensification of a continuous CWHPO treatment. Agglomerated SBA-15 silica-supported iron oxide (Fe2O3/SBA-15) was used as Fenton-like catalyst. Several variables such as the temperature and hydrogen peroxide concentration, as well as the capacity of the pilot plant for the treatment

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5

Quintanilla, Asunción, and Macarena Munoz. "Editorial Catalysts: Special Issue on Trends in Catalytic Wet Peroxide Oxidation Processes." Catalysts 9, no. 11 (2019): 918. http://dx.doi.org/10.3390/catal9110918.

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6

Liou, Rey-May, Shih-Hsiung Chen, Cheng-Hsien Huang, et al. "Catalytic wet peroxide oxidation of p-nitrophenol by Fe (III) supported on resin." Water Science and Technology 62, no. 8 (2010): 1879–87. http://dx.doi.org/10.2166/wst.2010.370.

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FeIII supported on resin (FeIII-resin) as an effective catalyst for peroxide oxidation was prepared and applied for the degradation of p-nitrophenol (PNP). Catalytic wet peroxide oxidation (CWPO) experiments with hydrogen peroxide as oxidant were performed in a batch rector with p-nitrophenol as the model pollutant. Under given conditions (PNP concentration 500 mg/L, H2O2 0.1 M, 80°C, resin dosage 0.6% g/mL), p-nitrophenol was almost completely removed, corresponding to an 84% of COD removal. It was found that the reaction temperature, oxidant concentration. and initial pH of solution signific

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7

Xu, Jun Qiang, Fang Guo, Jun Li, Xiu Zhi Ran, and Yan Tang. "Synthesis of the Cu/Flokite Catalysts and their Performances for Catalytic Wet Peroxide Oxidation of Phenol." Advanced Materials Research 560-561 (August 2012): 869–72. http://dx.doi.org/10.4028/www.scientific.net/amr.560-561.869.

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The supported Cu/Flokite catalysts were prepared by conventional incipient wetness impregnation. The catalysis oxidation degradation of phenol was carried out in heterogeneous catalyst and H2O2 process. The results indicated that the reaction system with catalyst and hydrogen peroxide was more benefit to degradation of phenol. When the phenol initial concentration was 100 mg/L, the phenol removal over the 2.5%Cu -2.5% Fe/Flokite catalyst could reach 96%. The peroxide catalytic oxidation process over the enhanced heterogeneous catalyst would be a novel technique for the treatment of phenol wast

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8

Hosseini, S. A., Kh Farhadi, S. Siahkamari, and B. Azizi. "Catalytic wet peroxide oxidation of phenol over ZnFe2O4 nano spinel." Canadian Journal of Chemistry 95, no. 1 (2017): 87–94. http://dx.doi.org/10.1139/cjc-2016-0220.

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The catalytic wet peroxide oxidation of phenol was investigated over ZnFe2O4 nano spinels under different conditions designed by the experimental design. ZnFe2O4 nano oxide was synthesized by the sol-gel combustion method and characterized by X-ray diffraction, Fourier transform infrared spectroscopy, and scanning electron microscope techniques. The mean particle size was determined to be around 80–90 nm. The experiments were designed by the Box–Behnken type of response surface methodology by considering four process variables: CH2O2 (mol L−1), ZnFe2O4 amount (g), temperature (°C), and reactio

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9

Sanabria, Nancy R., Yury M. Peralta, Mardelly K. Montañez, Nelson Rodríguez-Valencia, Rafael Molina, and Sonia Moreno. "Catalytic oxidation with Al–Ce–Fe–PILC as a post-treatment system for coffee wet processing wastewater." Water Science and Technology 66, no. 8 (2012): 1663–68. http://dx.doi.org/10.2166/wst.2012.410.

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The effluent from the anaerobic biological treatment of coffee wet processing wastewater (CWPW) contains a non-biodegradable compound that must be treated before it is discharged into a water source. In this paper, the wet hydrogen peroxide catalytic oxidation (WHPCO) process using Al–Ce–Fe–PILC catalysts was researched as a post-treatment system for CWPW and tested in a semi-batch reactor at atmospheric pressure and 25 °C. The Al–Ce–Fe–PILC achieved a high conversion rate of total phenolic compounds (70%) and mineralization to CO2 (50%) after 5 h reaction time. The chemical oxygen demand (COD

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10

Hong, Fang, Guo Min Cao, Xiao Dan Shuai, and Mei Sheng. "Catalytic Wet Peroxide Oxidation of Epoxy Resin Wastewater for Reusing." Advanced Materials Research 788 (September 2013): 263–67. http://dx.doi.org/10.4028/www.scientific.net/amr.788.263.

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To remove the organic compounds from epoxy resin wastewater which contains high concentration sodium chloride, a catalytic wet peroxide oxidation (CWPO) process was applied to treat it. The effect of different reaction conditions on total organic carbon (TOC) removal efficiency was evaluated, and the experimental results showed that the optimal H2O2 dosage, Fe2+ dosage, temperature, and pH were 0.735 M, 0.027 M, 90oC and 3.0, respectively. Multiple additive methods of H2O2 and Fe2+ significantly enhanced TOC removal than the one step addition. The TOC value of treated wastewater was lower than

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