A catalytic oxidation process of olive oil mill wastewaters using hydrogen peroxide and copper

2010 ◽  
Vol 23 (1-3) ◽  
pp. 187-193 ◽  
Author(s):  
S. De Rosa ◽  
A. Siciliano
Keyword(s):  
Hydrogen Peroxide ◽  
Olive Oil ◽  
Catalytic Oxidation ◽  
Oxidation Process

scholarly journals Optimization of isopropyl alcohol degradation by microwave-induced catalytic oxidation process

2019 ◽  
Vol 9 (3) ◽  
pp. 213-224
Author(s):  
Quynh Thi Phuong Tran ◽  
Chi-Hsu Hsieh ◽  
Tung-Yu Yang ◽  
Hsin-hsin Tung
Keyword(s):  
Hydrogen Peroxide ◽  
Catalytic Oxidation ◽  
Working Conditions ◽  
Isopropyl Alcohol ◽  
Oxidation Process ◽  
Removal Rate ◽  
Response Variability ◽  
Manufacturing Industries ◽  
Independent Variables ◽  
Central Composite

Abstract Isopropyl alcohol (IPA) is a common waste solvent from the semiconductor and optoelectronic manufacturing industries. The current study assesses the feasibility of microwave-induced catalytic oxidation process for synthetic IPA wastewater. The effect of three independent variables, including oxidant (hydrogen peroxide), initial IPA concentration, and dosage of catalyst (granular activated carbon, GAC) on the IPA removal efficiency, were investigated and optimized by response surface methodology based on central composite design. The estimated optimal working conditions were as follows: [H2O2] <0.132 M, GAC dosage = 108–123 g/L, and initial [IPA] = 0.038–0.10 M. The findings indicated that the dosage of GAC and the initial IPA concentration strongly affected the overall IPA removal. The values of R2 = 0.9948 and adjusted R2 = 0.9901 demonstrated that the response variability could be explained by the model expressing a satisfactory quadratic fit. Finally, the H2O2/GAC/MW process showed a faster and higher IPA removal rate than other processes tested.

Hydrogen Peroxide/Iron Oxide -Induced Catalytic Oxidation of Organic Compounds

2002 ◽  
Vol 5 (2) ◽  
Author(s):  
Mirat D. Gurol ◽  
Shu-Sung Lin
Keyword(s):  
Hydrogen Peroxide ◽  
Iron Oxide ◽  
Catalytic Oxidation ◽  
Organic Compounds ◽  
Oxidation Process ◽  
Heterogeneous Catalytic ◽  
Oxidation Of Organic Compounds

AbstractThis paper describes a novel heterogeneous catalytic oxidation process involving the use of hydrogen peroxide (H

Wet hydrogen peroxide catalytic oxidation of olive oil mill wastewaters using Cu-zeolite and Cu-pillared clay catalysts

2007 ◽  
Vol 124 (3-4) ◽  
pp. 240-246 ◽  
Author(s):  
Girolamo Giordano ◽  
Siglinda Perathoner ◽  
Gabriele Centi ◽  
Salvatore De Rosa ◽  
Teresa Granato ◽  
...  
Keyword(s):  
Hydrogen Peroxide ◽  
Olive Oil ◽  
Catalytic Oxidation ◽  
Pillared Clay ◽  
Clay Catalysts

Advanced Treatment of Coking Wastewater by Oxidation Process Using Pyrite and Hydrogen Peroxide

2013 ◽  
Vol 726-731 ◽  
pp. 2521-2525
Author(s):  
Zhi Yong Zhang ◽  
De Li Wu
Keyword(s):  
Hydrogen Peroxide ◽  
Oxidation Process ◽  
Low Cost ◽  
Oxygen Demand ◽  
Utilization Efficiency ◽  
Advanced Treatment ◽  
Coking Wastewater ◽  
Second Stage ◽  
Potential Alternative ◽  
High Utilization

Coking wastewater is a kind of recalcitrant wastewater including complicate compositions. Advanced treatment of coking wastewater by Fenton-Like reaction using pyrite as catalyst was investigated in this paper. The results show that the chemical oxygen demand (COD) of coking wastewater decreased significantly by method of coagulation combined with two-stage oxidation reaction. COD of wastewater can decrease from 250mg/l to 45mg/l after treatment, when 2g/L pyrite was used in each stage oxidation and the dosage of hydrogen peroxide (H2O2) is 0.2ml/l for first stage treatment, 0.1ml/l for second stage treatment respectively. The pyrite is effective to promote Fenton-Like reaction with low cost due to high utilization efficiency of H2O2, moreover, catalyst could be easily recovered and reused. The Fenton-Like reaction might be used as a potential alternative to advanced treatment of recalcitrant wastewater.

Phenolic Wastewater Treatment by Microwave-Induced H2O2-Fe (III)-Cu (II)/γ-Al2O3 Catalytic Oxidation Process

2013 ◽  
Vol 777 ◽  
pp. 101-105
Author(s):  
Jie Zhang ◽  
Wei Qian Pan ◽  
Tong Zheng ◽  
Peng Wang
Keyword(s):  
Catalytic Oxidation ◽  
Oxidation Process ◽  
Synthetic Wastewater ◽  
Reaction Rate Constants ◽  
Toc Removal ◽  
First Order Kinetics ◽  
Phenolic Pollutants ◽  
Phenolic Wastewater ◽  
Ph Range ◽  
Induction Stage

To achieve efficient removal of phenolic pollutants in water, the catalyst of Fe (III)-Cu (II)/γ-Al2O3 was prepared. In the presence of Fe (III)-Cu (II)/γ-Al2O3, microwave-induced hydrogen peroxide (H2O2) catalytic oxidation process was conducted for the treatment of synthetic wastewater containing PNP, a representative of phenolic pollutants. Effectiveness of the process and factors influencing PNP removal were investigated and results showed microwave-induced H2O2-Fe (III)-Cu (II)/γ-Al2O3 process could achieve 99.41% PNP removal percentage, corresponding to 77.9% TOC removal in a given condition. The process remained effective in the 2-8 pH range with high reusability of Fe (III)-Cu (II)/γ-Al2O3 catalyst. The kinetics study showed microwave-induced H2O2-Fe (III)-Cu (II)/γ-Al2O3 process could be divided into microwave induction stage and catalytic oxidation stage, both of which fitted first-order kinetics, with reaction rate constants of 0.0453 min-1 and 4.7552 min-1 respectively.

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