Suchergebnisse

Intro -- Foreword -- Preface -- Prologue -- Contents -- About the Editors -- Contributors -- Part I: Climate Change: Introduction, Models, Scenarios, Impact, and Scientific Evidence -- 1 Introduction to Climate Change Mitigation and Adaptation -- Introduction -- Climate Change -- Most Recent IPCC Updates -- The Greenhouse Effect -- Anthropogenic Climate Change -- Effects of Climate Change -- Impact of Climate Change Mitigation Actions -- Climate Change Adaptation Versus Climate Change Mitigation -- Climate Change and the Public -- What´s Next? -- Motivation -- Why This Book Is Needed -- Audience of the Handbook -- Scope -- References -- 2 Global Climate Change and Greenhouse Gases Emissions in Terrestrial Ecosystems -- Introduction: Global Climate Change and Soil Greenhouse Gases Emissions -- Soil Greenhouse Gases Emissions -- Soil CO2 Emission -- Soil CH4 Emission -- Soil N2O Emission -- Measurement Methods of Soil Greenhouse Gases Emissions -- Soil Chamber Methods -- Closed Static Chamber -- Closed Dynamic Chamber -- Open Dynamic Chamber -- Micrometeorological Methods - Eddy Covariance Technique -- Advantages and Disadvantages of the Measurement Methods -- Research Approaches of Global Climate Change and Soil Greenhouse Gases Emissions: Laboratory Incubation, Field Experiment, Met... -- Laboratory Incubation -- Field Experiment -- Meta-Analysis -- Biogeochemical and Ecosystem Modeling -- The DNDC Model -- Dynamic Land Ecosystem Model (DLEM) -- Impacts of Global Climate Change on Soil Greenhouse Gases Emissions: Case Studies -- Laboratory Incubation and Field Experiment -- Laboratory Incubation -- Field Experiment -- Meta-Analysis -- Biogeochemical and Ecosystem Modeling -- Site and Stand Levels -- Regional and Global Scales -- Closing Remarks and Future Research -- Cross-References -- References.

AbstractWorldwide, there is a continuous need to develop alternative treatment methods to replace conventional processes for textile wastewater. In this regard, Fenton oxidation, with the potential of hydroxyl radical production, is an efficient method. Nevertheless, pH dependence, high chemical consumption and sludge production are a few aspects that limit its wide application. Therefore, to overcome these limits, integration of Fenton oxidation with other advanced oxidation processes is considered a viable option. Therefore, in this study, Ultrasonic‐assisted Fenton oxidation was investigated to observe the increase in degradation efficiency of Fenton oxidation. For this purpose, low frequency ultrasonic water bath was used and malachite green dye was used as a model pollutant. Central composite design was used for experimental design, and [OP]ini, OP:Fe+2 (wt/wt), H2O2:Fe+2 (wt/wt) and pH were used as control factors. Based on experimental results, maximum of 97.5% Chemical Oxidation Demand (COD) reduction was obtained at the process conditions of [OP]ini: 100 mg/L, OP:Fe+2: 50, H2O2:Fe+2: 1.5 and pH:3. Furthermore, 10 times reduction in the consumption of hydrogen peroxide was obtained. According to Pareto analysis, organic pollutant (OP) in interaction with OP is the most significant while pH was identified as the least. The process followed pseudo‐first order kinetics (k = 0.0196 min−1) with electrical energy order of 26.21 kWh/m3 and the maximum energy consumption per COD removal of 0.8 kJ/COD, lower than those available in the literature. The results suggested that US‐assisted Fenton oxidation could be considered as an efficient method for treating the recalcitrant wastewater.