Preface |
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xiii | |
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List of Symbols and Abbreviations |
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xvii | |
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Historical Development of Wastewater Collection and Treatment |
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1 | (24) |
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Water Supply and Wastewater Management in Antiquity |
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1 | (3) |
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Water Supply and Wastewater Management in the Medieval Age |
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4 | (3) |
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First Studies in Microbiology |
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7 | (4) |
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Wastewater Management by Direct Discharge into Soil and Bodies of Water -- The First Studies |
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11 | (1) |
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Mineralization of Organics in Rivers, Soils or by Experiment -- A Chemical or Biological Process? |
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12 | (2) |
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Early Biological Wastewater Treatment Processes |
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14 | (2) |
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The Cholera Epidemics -- Were They Caused by Bacteria Living in the Soil or Water? |
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16 | (1) |
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Early Experiments with the Activated Sludge Process |
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16 | (2) |
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Taking Samples and Measuring Pollutants |
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18 | (1) |
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Early Regulations for the Control of Wastewater Discharge |
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19 | (6) |
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20 | (5) |
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Wastewater Characterization and Regulations |
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25 | (18) |
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Volumetric Wastewater Production and Daily Changes |
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25 | (2) |
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27 | (7) |
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27 | (1) |
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28 | (1) |
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28 | (2) |
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30 | (2) |
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32 | (1) |
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32 | (1) |
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33 | (1) |
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34 | (1) |
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Methods for Measuring Dissolved Organic Substances as Total Parameters |
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34 | (4) |
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Biochemical Oxygen Demand |
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34 | (2) |
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36 | (1) |
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Total and Dissolved Organic Carbon |
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37 | (1) |
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38 | (5) |
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38 | (1) |
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38 | (1) |
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Legislation Concerning Discharge into Public Sewers |
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38 | (1) |
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Legislation Concerning Discharge into Waters |
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39 | (2) |
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41 | (1) |
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42 | (1) |
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43 | (26) |
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Some Remarks on the Composition and Morphology of Bacteria (Eubacteria) |
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43 | (2) |
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Proteins and Nucleic Acids |
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45 | (14) |
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45 | (1) |
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45 | (1) |
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46 | (1) |
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Proteins for Special Purposes |
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47 | (1) |
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47 | (3) |
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50 | (1) |
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50 | (4) |
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54 | (3) |
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57 | (1) |
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58 | (1) |
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59 | (10) |
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59 | (1) |
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59 | (1) |
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Catabolism of Using Glucose |
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60 | (1) |
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Aerobic Conversion by Prokaryotic Cells |
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60 | (5) |
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Anaerobic Conversion by Prokaryotic Cells |
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65 | (1) |
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66 | (1) |
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67 | (2) |
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Determination of Stoichiometric Equations for Catabolism and Anabolism |
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69 | (14) |
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69 | (1) |
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Aerobic Degradation of Organic Substances |
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70 | (6) |
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Degradation of Hydrocarbons Without Bacterial Decay |
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70 | (1) |
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Mineralization of 2,4-Dinitrophenol |
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71 | (3) |
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Degradation of Hydrocarbons with Bacterial Decay |
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74 | (2) |
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Measurement of O2 Consumption Rate ro,s and CO2 Production Rate rco,s |
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76 | (7) |
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78 | (3) |
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81 | (2) |
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Gas/Liquid Oxygen Transfer and Stripping |
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83 | (36) |
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83 | (3) |
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Mass Transfer Coefficients |
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86 | (4) |
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Definition of Specific Mass Transfer Coefficients |
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86 | (1) |
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87 | (3) |
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Measurement of Specific Overall Mass Transfer Coefficients KLa |
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90 | (5) |
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Absorption of Oxygen During Aeration |
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90 | (1) |
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90 | (1) |
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91 | (1) |
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Dynamic Method in Wastewater Mixed with Activated Sludge |
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92 | (1) |
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Desorption of Volatile Components During Aeration |
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93 | (2) |
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Oxygen Transfer Rate, Energy Consumption and Efficiency in Large-scale Plants |
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95 | (13) |
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95 | (1) |
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95 | (1) |
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Power Consumption and Efficiency |
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96 | (2) |
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98 | (1) |
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98 | (1) |
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The Simple Plug Flow Model |
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99 | (2) |
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Proposed Model of the American Society of Civil Engineers |
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101 | (2) |
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103 | (1) |
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103 | (3) |
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Power Consumption and Efficiency |
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106 | (1) |
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106 | (2) |
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Dimensional Analysis and Transfer of Models |
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108 | (11) |
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108 | (1) |
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Power Consumption of a Stirred, Non-aerated Tank -- A Simple Example |
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109 | (3) |
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Description of Oxygen Transfer, Power Consumption and Efficiency by Surface Aerators Using Dimensionless Numbers |
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112 | (1) |
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Application of Dimensionless Numbers for Surface Aeration |
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113 | (2) |
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115 | (2) |
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117 | (2) |
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Aerobic Wastewater Treatment in Activated Sludge Systems |
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119 | (32) |
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119 | (1) |
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Kinetic and Reaction Engineering Models With and Without Oxygen Limitation |
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119 | (19) |
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119 | (1) |
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With High Initial Concentration of Bacteria |
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119 | (3) |
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With Low Initial Concentration of Bacteria |
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122 | (1) |
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122 | (3) |
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Completely Mixed Activated Sludge Reactor |
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125 | (1) |
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125 | (1) |
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Mean Retention Time, Recycle Ratio and Thickening Ratio as Process Parameters |
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126 | (2) |
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128 | (2) |
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130 | (2) |
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Completely Mixed Tank Cascades With Sludge Recycle |
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132 | (2) |
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Flow Reactor With Axial Dispersion |
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134 | (2) |
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Stoichiometric and Kinetic Coefficients |
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136 | (1) |
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137 | (1) |
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Retention Time Distribution in Activated Sludge Reactors |
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138 | (6) |
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Retention Time Distribution |
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138 | (2) |
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140 | (1) |
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Completely Mixed Tank Cascade |
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140 | (1) |
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Tube Flow Reactor With Axial Dispersion |
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141 | (1) |
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Comparison Between Tank Cascades and Tube Flow Reactors |
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142 | (2) |
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Technical Scale Activated Sludge Systems for Carbon Removal |
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144 | (7) |
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146 | (3) |
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149 | (2) |
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Aerobic Treatment with Biofilm Systems |
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151 | (18) |
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151 | (1) |
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Biofilm Reactors for Wastewater Treatment |
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152 | (6) |
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152 | (2) |
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Submerged and Aerated Fixed Bed Reactors |
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154 | (2) |
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156 | (2) |
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Mechanisms for Oxygen Mass Transfer in Biofilm Systems |
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158 | (1) |
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Models for Oxygen Mass Transfer Rates in Biofilm Systems |
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159 | (10) |
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159 | (1) |
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Mass Transfer Gas/Liquid is Rate-limiting |
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159 | (1) |
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Mass Transfer Liquid/Solid is Rate-limiting |
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160 | (1) |
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Biological Reaction is Rate-limiting |
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160 | (1) |
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Diffusion and Reaction Inside the Biofilm |
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160 | (3) |
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Influence of Diffusion and Reaction Inside the Biofilm and of Mass Transfer Liquid/Solid |
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163 | (1) |
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Influence of Mass Transfer Rates at Gas Bubble and Biofilm Surfaces |
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164 | (1) |
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164 | (2) |
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166 | (3) |
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Anaerobic Degradation of Organics |
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169 | (26) |
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Catabolic Reactions -- Cooperation of Different Groups of Bacteria |
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169 | (7) |
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169 | (1) |
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169 | (1) |
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169 | (2) |
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171 | (1) |
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171 | (2) |
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Regulation of Acetogenics by Methanogenics |
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173 | (2) |
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Sulfate and Nitrate Reduction |
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175 | (1) |
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Kinetics -- Models and Coefficients |
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176 | (6) |
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176 | (1) |
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Hydrolysis and Formation of Lower Fatty Acids by Acidogenic Bacteria |
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176 | (1) |
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Transformation of Lower Fatty Acids by Acetogenic Bacteria |
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177 | (2) |
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Transformation of Acetate and Hydrogen into Methane |
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179 | (1) |
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180 | (2) |
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182 | (2) |
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184 | (11) |
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184 | (1) |
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185 | (2) |
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Upflow Anaerobic Sludge Blanket |
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187 | (1) |
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Anaerobic Fixed Bed Reactor |
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188 | (2) |
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Anaerobic Rotating Disc Reactor |
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190 | (1) |
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Anaerobic Expanded and Fluidized Bed Reactors |
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191 | (1) |
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192 | (1) |
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193 | (2) |
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Biodegradation of Special Organic Compounds |
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195 | (28) |
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195 | (1) |
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196 | (8) |
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Chlorinated n-Alkanes, Particularly Dichloromethane and 1,2-Dichloroethane |
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196 | (1) |
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Properties, Use, Environmental Problems and Kinetics |
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196 | (2) |
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Treatment of Wastewater Containing DCM or DCA |
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198 | (2) |
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200 | (1) |
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Properties, Use and Environmental Problems |
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200 | (1) |
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Principles of Biological Degradation |
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200 | (2) |
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Treatment of Wastewater Containing Chlorobenzenes |
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202 | (1) |
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203 | (1) |
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204 | (2) |
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Properties, Use, Environmental Problems and Kinetics |
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204 | (2) |
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Treatment of Wastewater Containing 4-NP or 2,4-DNT |
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206 | (1) |
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Polycyclic Aromatic Hydrocarbons and Mineral Oils |
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206 | (5) |
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Properties, Use and Environmental Problems |
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206 | (1) |
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207 | (2) |
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209 | (1) |
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209 | (2) |
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PAHs Dissolved in n-Dodecane Standard Emulsion |
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211 | (1) |
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211 | (6) |
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Properties, Use and Environmental Problems |
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211 | (2) |
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Production of Azo Dyes in the Chemical Industry -- Biodegradability of Naphthalene Sulfonic Acids |
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213 | (2) |
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Biodegradation of Azo Dyes |
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215 | (1) |
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Direct Aerobic Degradation |
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215 | (1) |
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Anaerobic Reduction of Azo Dyes |
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215 | (1) |
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Aerobic Degradation of Metabolites |
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216 | (1) |
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Treatment of Wastewater Containing the Azo Dye Reactive Black 5 |
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216 | (1) |
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217 | (6) |
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218 | (5) |
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Biological Nutrient Removal |
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223 | (44) |
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223 | (4) |
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Biological Nitrogen Removal |
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227 | (17) |
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The Nitrogen Cycle and the Technical Removal Process |
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227 | (1) |
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228 | (1) |
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Nitrifying Bacteria and Stoichiometry |
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228 | (3) |
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Stoichiometry and Kinetics of Nitrification |
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231 | (4) |
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Parameters Influencing Nitrification |
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235 | (2) |
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237 | (1) |
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Denitrifying Bacteria and Stoichiometry |
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237 | (2) |
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Stoichiometry and Kinetics of Denitrification |
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239 | (1) |
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Parameters Influencing Denitrification |
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240 | (2) |
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Nitrite Accumulation During Nitrification |
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242 | (1) |
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New Microbial Processes for Nitrogen Removal |
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243 | (1) |
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Biological Phosphorus Removal |
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244 | (6) |
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Enhanced Biological Phosphorus Removal |
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244 | (1) |
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Kinetic Model for Biological Phosphorus Removal |
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245 | (1) |
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245 | (1) |
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246 | (1) |
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247 | (1) |
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Results of a Batch Experiment |
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248 | (1) |
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Parameters Affecting Biological Phosphorus Removal |
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249 | (1) |
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Biological Nutrient Removal Processes |
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250 | (7) |
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250 | (1) |
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Nitrogen Removal Processes |
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250 | (2) |
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Chemical and Biological Phosphorus Removal |
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252 | (1) |
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Processes for Nitrogen and Phosphorus Removal |
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253 | (1) |
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Different Levels of Performance |
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253 | (2) |
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255 | (2) |
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Membrane Bioreactors (MBR) |
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257 | (1) |
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Phosphorus and Nitrogen Recycle |
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257 | (10) |
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257 | (1) |
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258 | (1) |
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259 | (3) |
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262 | (5) |
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Modelling of the Activated Sludge Process |
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267 | (24) |
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Why We Need Mathematical Models |
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267 | (1) |
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Models Describing Carbon and Nitrogen Removal |
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268 | (3) |
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268 | (1) |
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Carbon Removal and Bacterial Decay |
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269 | (1) |
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Carbon Removal and Nitrification Without Bacterial Decay |
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270 | (1) |
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Models for Optimizing the Activated Sludge Process |
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271 | (20) |
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271 | (1) |
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Modelling the Influence of Aeration on Carbon Removal |
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272 | (3) |
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Activated Sludge Model 1 (ASM 1) |
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275 | (8) |
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283 | (2) |
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More Complicated Models and Conclusions |
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285 | (1) |
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286 | (2) |
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288 | (3) |
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Membrane Technology in Biological Wastewater Treatment |
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291 | (40) |
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291 | (2) |
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293 | (8) |
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Membrane Characteristics and Definitions |
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293 | (3) |
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Mass Transport Through Non-porous Membranes |
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296 | (4) |
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Mass Transport Through Porous Membranes |
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300 | (1) |
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Mass Transfer Resistance Mechanisms |
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301 | (7) |
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301 | (1) |
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Mass Transfer Resistances |
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302 | (1) |
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Concentration Polarization Model |
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303 | (3) |
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Solution--diffusion Model and Concentration Polarization |
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306 | (2) |
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The Pore Model and Concentration Polarization |
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308 | (1) |
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Performance and Module Design |
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308 | (10) |
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308 | (1) |
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Design and Configuration of Membrane Modules |
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309 | (1) |
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309 | (4) |
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313 | (1) |
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314 | (1) |
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314 | (1) |
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Membrane Fouling and Cleaning Management |
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315 | (1) |
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Types of Fouling Processes |
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315 | (1) |
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Membrane Cleaning Strategies |
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316 | (2) |
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318 | (13) |
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Final Treatment (Behind the Secondary Clarifier) |
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318 | (1) |
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Membrane Bioreactors in Aerobic Wastewater Treatment |
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319 | (4) |
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Membrane Bioreactors and Nutrient Removal |
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323 | (1) |
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324 | (3) |
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327 | (4) |
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Production Integrated Water Management and Decentralized Effluent Treatment |
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331 | (24) |
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331 | (2) |
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Production Integrated Water Management in the Chemical Industry |
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333 | (13) |
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Sustainable Development and Process Optimization |
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333 | (1) |
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333 | (1) |
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334 | (2) |
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Production of Naphthalenedisufonic Acid |
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336 | (2) |
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Methodology of Process Improvement |
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338 | (1) |
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Minimization of Fresh Water Use |
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339 | (1) |
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Description of the Problem |
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339 | (1) |
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The Concentration/Mass Flow Rate Diagram and the Graphical Solution |
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340 | (4) |
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The Network Design Method |
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344 | (2) |
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Decentralized Effluent Treatment |
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346 | (9) |
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Minimization of Treated Wastewater |
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346 | (1) |
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Description of the Problem |
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346 | (1) |
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Representation of Treatment Processes in a Concentration/Mass Flow Rate Diagram |
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347 | (2) |
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The Lowest Wastewater Flow Rate to Treat |
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349 | (1) |
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Processes for Decentralized Effluent Treatment |
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349 | (1) |
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350 | (4) |
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354 | (1) |
Subject Index |
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355 | |