| Preface |
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xi | |
| Editor |
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xiii | |
| Contributors |
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xv | |
| Section I Membrane Technology for Sustainable Development |
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1 Processing of Complex Industrial Effluents and Gaseous Mixtures through Innovative Membrane Technology |
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3 | (30) |
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4 | (2) |
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1.1.1 Impact of Industrial Effluents and Off-Gases on the Environment |
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4 | (1) |
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1.1.2 Mechanisms of Mass Transfer in Hydrostatic Pressure-Driven Membrane Process and Gas Permeation |
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5 | (1) |
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1.1.3 Objectives of the Work and Scope for Membrane Technology to Meet Challenges |
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6 | (1) |
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1.2 Case Study on Chloride Separation from Coke Oven Wastewater in Steel Industry |
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6 | (3) |
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1.2.1 Source of Chloride Effluent |
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6 | (1) |
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1.2.2 Synthesis of Nanofiltration Membrane |
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7 | (1) |
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1.2.3 Nanofiltration Process for Treatment of TATA Steel Industrial Effluent of 5 3/h Capacity |
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8 | (1) |
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1.3 Recovery of Dimethyl Sulfoxide Solvent from Pharmaceutical Effluent |
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9 | (4) |
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1.3.1 Source of Pharmaceutical Effluent |
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9 | (1) |
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1.3.2 Design and Commissioning of Electrodialysis Pilot Plant of Z500 L/batch/day |
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10 | (3) |
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1.4 Decolorization of Aqueous Sodium Thiocyanate Solution in Acrylic Fiber Industry |
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13 | (4) |
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1.4.1 Origin of Textile Effluent |
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13 | (1) |
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1.4.2 Depiction of Nanofiltration Process |
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13 | (1) |
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1.4.3 Design and Installation of Pilot Nanofiltration Plant of 6,000 L/batch/day |
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14 | (3) |
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1.5 Effluent Treatment for Chloralkali Industry |
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17 | (1) |
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1.6 Application of Ultrafiltration in Wastewater Treatment |
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17 | (3) |
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1.7 Separation of Industrial Off-Gases and Process Gas Mixtures |
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20 | (10) |
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1.7.1 Membranes for Gas Separation |
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20 | (1) |
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1.7.1.1 Poly(ether-block-amide) Membrane |
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20 | (1) |
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1.7.1.2 Silver tetrafluoroborate Loaded Pebax Membrane |
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20 | (1) |
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1.7.1.3 Cobalt(II) phthalocyanine Incorporated Pebax Membrane |
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21 | (1) |
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1.7.1.4 Matrimid Hollow Fiber Module |
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21 | (1) |
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1.7.1.5 Polysulfone Hollow Fiber Module |
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22 | (1) |
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1.7.1.6 Poly(ether ether ketone) Hollow Fiber Module |
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22 | (1) |
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1.7.1.7 Palladium Coated Ceramic Tubular Membrane |
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22 | (1) |
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1.7.2 Experimental Description of Laboratory Gas Separation Unit |
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22 | (1) |
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1.7.3 Membrane Performance for Gas Separation |
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23 | (1) |
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1.7.3.1 Separation of H2 and N2 |
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23 | (1) |
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1.7.3.2 Separation of CO2 and N2 |
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24 | (1) |
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1.7.3.3 Separation of O2 and N2 |
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24 | (1) |
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1.7.3.4 Recovery of Propylene from Refinery Fuel Gas Mixture |
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25 | (1) |
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1.7.3.5 Separation of Propane/Propylene Binary Gas Mixture |
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27 | (1) |
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1.7.3.6 Natural Gas Sweetening |
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27 | (3) |
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1.8 Conclusions and Future Perspectives |
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30 | (1) |
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30 | (3) |
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2 Comprehensive Process Solutions for Chemical and Allied Industries Using Membranes |
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33 | (22) |
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33 | (2) |
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2.2 Milestones on Industrial Applications of Membrane Technology in India |
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35 | (2) |
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2.3 Membrane Development and Scale-Up |
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37 | (3) |
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2.4 Industrial Process Solutions |
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40 | (11) |
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40 | (2) |
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42 | (1) |
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43 | (5) |
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48 | (1) |
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2.4.5 Wastewater Treatment |
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48 | (1) |
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2.4.6 Ultrapure Water Production |
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49 | (2) |
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51 | (1) |
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52 | (3) |
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3 An Insight into Various Approaches toward Flux Enhancement and Fouling Mitigation of Membranes during Nano and Ultrafiltration |
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55 | (30) |
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55 | (1) |
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3.2 Principle and Mechanism |
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56 | (1) |
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3.3 Core Issues: Concentration Polarization and Membrane Fouling |
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57 | (1) |
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58 | (3) |
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3.4.1 Coagulation/Flocculation |
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58 | (2) |
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60 | (1) |
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60 | (1) |
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3.5 Imparting Fluid Instabilities |
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61 | (12) |
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3.5.1 Rotating Disk Module |
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62 | (4) |
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3.5.2 Turbulence Promoters and Secondary Flow |
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66 | (1) |
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3.5.3 Ultrasonic Irradiation |
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67 | (1) |
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3.5.4 Flow Reversal and Pulsating Flow |
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68 | (5) |
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3.6 Air Sparging and Gas Slug |
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73 | (2) |
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3.7 Membrane Surface Modification |
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75 | (1) |
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3.8 Conclusion and Future Outlook |
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76 | (1) |
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77 | (8) |
| Section II Water |
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4 Fabrication and Applications of Functionalized Membranes in Drinking Water Treatment |
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85 | (16) |
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85 | (2) |
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4.1.1 Different Classes of Membranes |
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85 | (1) |
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4.1.2 Utilities of Different Membranes in Water Treatment |
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85 | (1) |
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4.1.3 Organic and Inorganic Membranes |
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86 | (1) |
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4.1.4 Organic-Inorganic Mixed Matrix Membranes (MMMs) |
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86 | (1) |
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4.2 Synthesis and Fabrication of MMMs |
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87 | (1) |
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4.3 Application of Organic-Inorganic Mixed Matrix Membranes for Water Purification |
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88 | (8) |
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88 | (3) |
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4.3.2 Morphological, Mineralogical and Surface Roughness Variation |
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91 | (2) |
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4.3.3 Improvement in Membrane Inherent Properties |
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93 | (2) |
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4.3.4 Improvement in Specific Rejection Capability of Different Ions |
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95 | (1) |
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4.4 Cost Analysis of Mixed Matrix Membrane Processes |
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96 | (1) |
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97 | (1) |
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97 | (1) |
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98 | (3) |
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5 Design of Highly Compact and Cost-Effective Water Purification Systems for Promoting Rural and Urban Welfare |
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101 | (34) |
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102 | (2) |
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5.2 Overview of Water Purification Processes |
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104 | (3) |
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5.2.1 Chemical Coagulation and Flocculation |
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104 | (1) |
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105 | (1) |
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5.2.3 Ion Exchange Resins |
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105 | (1) |
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5.2.4 Disinfection by Chlorine, Ultraviolet Light and Ozonation |
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106 | (1) |
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106 | (1) |
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107 | (5) |
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5.3.1 Principle and Applications |
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109 | (1) |
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5.3.2 Nanofiltration of Ground/Surface Water Purification |
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109 | (3) |
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112 | (4) |
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5.4.1 Principle and Mechanism of Mass Transfer |
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113 | (1) |
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5.4.2 Fluoride Contamination of Ground Water |
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114 | (1) |
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5.4.3 Laboratory Experiments on Separation of Fluoride from Drinking Water |
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115 | (1) |
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5.4.4 Experimental Procedure for Reverse Osmosis System |
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115 | (1) |
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5.4.5 Equations for Calculation of Operating Parameters |
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116 | (1) |
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116 | (1) |
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5.4.5.2 Rejection Efficiency |
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116 | (1) |
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5.4.5.3 Water Recovery (%) |
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116 | (1) |
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5.5 Analytical Procedures |
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116 | (2) |
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116 | (1) |
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5.5.2 Potable Quality Analysis by H2S Vial Method |
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117 | (1) |
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5.5.3 Analysis for E. Coli and Total Coliform Bacteria |
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118 | (1) |
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5.6 Effect of Operating Parameters |
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118 | (1) |
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5.6.1 Effect of Feed Pressure on Pure Water Flux |
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118 | (1) |
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5.6.2 Flux and Rejection for Synthetic Fluoride Feed |
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118 | (1) |
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5.7 Defluoridation in Rural Areas |
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119 | (4) |
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5.7.1 Methods for Treatment of Reject Stream for Water Recycle for Safe Disposal |
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122 | (1) |
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123 | (1) |
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5.9 Ultrafiltration for Purification of Surface Water |
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124 | (6) |
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5.9.1 Hollow Fiber Membranes for Surface Water Treatment |
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124 | (2) |
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5.9.2 Hand Pump Operated Ultrafiltration Membrane Systems |
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126 | (1) |
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5.9.2.1 Submerged Membrane Module with Suction Mode of Operation |
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127 | (1) |
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5.9.2.2 External Membrane Module for Positive Hydrostatic Feed Pressure |
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127 | (3) |
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5.10 Concentration Polarization and Fouling |
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130 | (1) |
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5.11 Membrane Cleaning and Storage |
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130 | (1) |
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130 | (1) |
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131 | (1) |
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131 | (4) |
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6 Ceramic Membrane Based Community Model Plants for Arsenic Decontamination from Ground Water and Quality Drinking Water Supply |
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135 | (20) |
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136 | (1) |
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136 | (1) |
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6.1.2 Permissible Limits of Arsenic Content in Drinking Water |
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136 | (1) |
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6.2 Nature of the Problem on Arsenic Contamination in Ground Water |
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137 | (1) |
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6.2.1 Arsenic Contamination in Ground Water-Arsenic Speciation |
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137 | (1) |
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6.2.2 Co-Contaminants in Ground Water |
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138 | (1) |
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6.3 Technologies for Arsenic Removal in Drinking Water |
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138 | (1) |
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6.3.1 Conventional Technologies for Arsenic Removal |
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138 | (1) |
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6.3.2 Shortcomings of Conventional Technologies |
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139 | (1) |
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6.4 Membrane-Based Processes for Decontamination of Arsenic |
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139 | (2) |
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6.4.1 High-Pressure Membrane Processes |
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139 | (1) |
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6.4.2 Low-Pressure Point-of-Use (POU) Systems |
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140 | (1) |
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6.5 Ceramic Membrane-Based Process for Decontamination of Arsenic |
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141 | (1) |
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6.6 Hybrid Process for Decontamination of Arsenic Using Low-Cost Ceramic Membrane |
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142 | (5) |
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6.6.1 Adsorbent Preparation and Selection |
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142 | (1) |
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6.6.2 Bench Scale Studies Under Cross-Flow Microfiltration Conditions Using Ceramic Membrane |
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142 | (1) |
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6.6.3 Adsorption Studies Under Dynamic Condition Using Arsenic-Spiked Tap Water |
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143 | (2) |
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6.6.4 Adsorption Capacity Under Cross-Flow Condition |
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145 | (1) |
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6.6.5 Effect of Dynamic Membrane Formation during Cross-Flow Microfiltration Experiments Using Natural Ground Water |
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146 | (1) |
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6.6.6 Role of Dynamic Membrane Formation on Removal of Arsenic |
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146 | (1) |
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6.6.7 Findings of Bench Scale Trial |
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147 | (1) |
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6.7 Pilot Plant Trials for Treatment of Arsenic Contaminated Natural Ground Water |
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147 | (4) |
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6.7.1 Performance Evaluation for Production of Quality Drinking Water |
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148 | (2) |
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6.7.2 Sustainability of the Technology |
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150 | (1) |
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151 | (1) |
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151 | (1) |
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152 | (3) |
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7 Forward Osmosis: An Efficient and Economical Alternative for Water Reclamation and Concentration of Food Products & Beverages |
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155 | (20) |
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7.1 Introduction and Background |
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155 | (4) |
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156 | (1) |
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7.1.2 Commercial Adoption |
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156 | (1) |
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7.1.3 Technical Background |
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157 | (2) |
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7.2 Key Membranes and Desired Properties for FO |
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159 | (1) |
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7.3 Concentration Polarization |
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160 | (5) |
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7.3.1 External Concentration Polarization (ECP) |
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160 | (2) |
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162 | (1) |
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7.3.3 Internal Concentration Polarization |
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163 | (1) |
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7.3.4 Model for Concentrative Internal Concentration Polarization |
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163 | (1) |
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7.3.5 Model for Dilutive Internal Concentration Polarization (DICP) |
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164 | (1) |
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7.4 Forward Osmosis Membrane Properties |
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165 | (2) |
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7.4.1 TFC-FO Membrane Structure and Modification |
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166 | (1) |
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7.4.2 Hydrophilic TFC-FO Membranes for Enhanced Antifouling Properties |
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167 | (1) |
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7.5 Forward Osmosis Membrane Module Configurations: Advantages and Disadvantages |
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167 | (2) |
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169 | (1) |
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170 | (1) |
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170 | (5) |
| Section III Health |
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8 Low-Cost Production of Anti-Diabetic and Anti-Obesity Sweetener from Stevia Leaves by Diafiltration Membrane Process |
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175 | (16) |
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175 | (2) |
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8.1.1 History of Stevia Glycosides |
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176 | (1) |
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8.1.2 Botanical Description of the Plant |
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176 | (1) |
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8.2 Applications of Stevia |
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177 | (1) |
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8.2.1 Milk and Food Products |
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177 | (1) |
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8.2.2 Essential Oil and Fatty Acids |
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178 | (1) |
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8.2.3 Health Benefits of Stevia |
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178 | (1) |
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8.3 Separation Processes for Stevia Isolation |
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178 | (1) |
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8.4 Role of Membranes in Stevia Glycosides Isolation |
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179 | (1) |
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8.4.1 Important Equations |
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179 | (1) |
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180 | (1) |
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180 | (1) |
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8.7 Case Study 1: Bench Scale Experimental Trials |
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181 | (3) |
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8.7.1 Performance of Ceramic Tubular Microfiltration Module |
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181 | (1) |
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8.7.2 Performance of Ultrafiltration Based Diafiltration Process |
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182 | (1) |
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8.7.3 Performance of Hydrophilized Polyamide Nanofiltration Membrane |
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183 | (1) |
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8.8 Case Study 2: Pilot Scale Experimental Trials |
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184 | (2) |
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8.8.1 Extraction of Stevia by Ultrafiltration |
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184 | (1) |
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8.8.2 Concentration of Stevia by Nanofiltration |
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185 | (1) |
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9 Operation and Maintenance Costs |
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186 | (2) |
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10 Conclusions and Future Scope |
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188 | (1) |
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188 | (1) |
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189 | (2) |
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9 Microfiltration Membranes: Fabrication and Application |
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191 | (22) |
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192 | (1) |
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9.2 Membrane Materials and Trade-Offs |
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193 | (2) |
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193 | (1) |
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9.2.2 Polymeric Membranes |
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194 | (1) |
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9.2.3 Polymeric vs. Ceramic Membranes |
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195 | (1) |
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9.2.4 Polymer-Ceramic Composite Membranes |
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195 | (1) |
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9.3 General Methods of Preparation of Microfiltration Membranes |
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195 | (3) |
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9.3.1 Ceramic Membrane Preparation Techniques |
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195 | (1) |
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9.3.2 Materials for Ceramic Membranes |
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196 | (1) |
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9.3.3 Important Parameters Influencing Ceramic Membrane Structure |
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196 | (1) |
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9.3.4 Structural Material |
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197 | (1) |
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9.3.5 Pore Forming Material |
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197 | (1) |
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197 | (1) |
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9.3.7 Sintering Temperature |
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198 | (1) |
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9.4 Characterization Techniques |
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198 | (4) |
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9.4.1 Characterization Techniques for Membranes |
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198 | (1) |
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199 | (1) |
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9.4.3 Average Pore Size and Pore Size Distribution |
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199 | (1) |
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9.4.4 Porosity and Structural Density |
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200 | (1) |
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9.4.5 Liquid Permeation Characterization |
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201 | (1) |
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9.4.6 Gas Transport Characteristics |
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201 | (1) |
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9.5 Applications of Microfiltration Membranes |
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202 | (7) |
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9.5.1 Treatment of Oily Wastewater Using Ceramic Membrane |
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203 | (1) |
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9.5.1.1 Effect of Trans-Membrane Pressure on Flux |
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204 | (1) |
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9.5.1.2 Effect of Trans-Membrane Pressure on Oil Separation |
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204 | (1) |
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9.5.1.3 Identification of Flux Decline Mechanism |
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204 | (2) |
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9.5.2 Clarification of Sweet Lemon Juice by Microfiltration |
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206 | (1) |
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9.5.2.1 Juice Preparation and Pretreatment |
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207 | (1) |
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9.5.2.2 Microfiltration Studies |
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207 | (1) |
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9.5.2.3 Effect of Operating Pressure on Permeate Flux |
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208 | (1) |
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9.5.3 Separation of Bio-Molecules, Proteins, and Bacteria by Microfiltration |
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209 | (1) |
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9.5.4 Pretreatment of Drinking Water |
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209 | (1) |
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209 | (1) |
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210 | (3) |
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10 Hemodialysis Membranes for Treatment of Chronic Kidney Disease: State-of-the-Art and Future Prospects |
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213 | (20) |
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214 | (3) |
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214 | (1) |
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10.1.2 Kidney Dysfunction |
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214 | (1) |
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215 | (1) |
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216 | (1) |
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10.2 Hemodialysis Membranes |
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217 | (1) |
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10.2.1 Dialyzer Size and Efficiency |
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218 | (1) |
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10.2.2 Reuse of Dialyzers |
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218 | (1) |
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10.3 History of Dialysis Process |
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218 | (1) |
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10.4 Hemodialysis Module Design |
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219 | (3) |
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10.4.1 Design of Dialysis Cartridge |
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219 | (1) |
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10.4.2 Mechanism of Dialysis |
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220 | (1) |
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10.4.3 Parameters Influencing Hemodialysis |
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221 | (1) |
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221 | (1) |
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10.4.3.2 OF Coefficient (KUF) |
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221 | (1) |
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10.4.3.3 Mass Transfer Coefficient (k0A) |
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221 | (1) |
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10.4.3.4 Dialysis Adequacy (Kt/V) |
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221 | (1) |
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10.4.3.5 Transport Mechanisms |
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221 | (1) |
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10.4.4 Features of Hemodialysis Fibers |
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221 | (1) |
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222 | (1) |
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222 | (2) |
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10.5.1 Efficient Casting Machine for Spinning Hollow Fibers |
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222 | (1) |
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10.5.2 Spinneret for Dialysis Fibers |
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223 | (1) |
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10.6 Drawbacks of Hemodialysis |
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224 | (1) |
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10.7 Emerging Trends in Dialysis Research |
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225 | (2) |
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10.7.1 Heparinization of Fibers |
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225 | (1) |
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10.7.1.1 Progress on Antithrombogenic Continuous Hemofilter |
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225 | (1) |
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10.7.2 Biocompatible Membranes |
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226 | (1) |
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10.7.3 Innovative Membranes |
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226 | (1) |
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226 | (1) |
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10.7.5 A Bioartificial Kidney System |
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227 | (1) |
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10.7.5.1 Artificial Membrane for Bioartificial Tubule Devices |
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227 | (1) |
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10.7.5.2 Formation of Tubular Epithelial Cells-Monolayer |
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227 | (1) |
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227 | (1) |
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228 | (5) |
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11 Design of Cost-Effective Membrane Devices for Production of Potable Alkaline Ionized Water |
|
|
233 | (20) |
|
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|
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|
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|
|
233 | (3) |
|
|
|
234 | (1) |
|
11.1.2 Alkaline Water: Health Benefits |
|
|
234 | (2) |
|
11.1.3 Principle of Electrolytic Ionization of Water |
|
|
236 | (1) |
|
11.2 State-of-the-Art Water Electrolysis and Electrolyzers |
|
|
236 | (1) |
|
11.3 Design of Device for Alkaline Ionized Water Production |
|
|
237 | (6) |
|
11.3.1 Operating Mechanism of AIW Device |
|
|
237 | (1) |
|
11.3.2 Membrane Synthesis |
|
|
237 | (1) |
|
11.3.2.1 Synthesis of Nonporous Cation Exchange Membrane |
|
|
238 | (1) |
|
11.3.2.2 Synthesis of Flat Sheet Ultrafiltration Membrane |
|
|
238 | (1) |
|
11.3.2.3 Synthesis of Hollow Fiber Ultrafiltration Membrane |
|
|
239 | (1) |
|
11.3.3 Design and Operation of Electrolyzers |
|
|
240 | (1) |
|
11.3.3.1 Table Top Electrolyzer |
|
|
240 | (1) |
|
11.3.3.2 Batch Electrolyzer |
|
|
241 | (1) |
|
11.3.3.3 Continuous Electrolyzer |
|
|
242 | (1) |
|
11.4 Performance of Electrolyzers |
|
|
243 | (3) |
|
11.4.1 Table Top Electrolyzer |
|
|
243 | (1) |
|
11.4.2 Batch Electrolyzer |
|
|
244 | (1) |
|
11.4.3 Continuous Hollow Fiber Based Electrolyzer |
|
|
245 | (1) |
|
|
|
246 | (2) |
|
|
|
248 | (1) |
|
|
|
249 | (4) |
| Section IV Membrane Process Design |
|
|
12 Mass Transfer Modeling in Hollow Fiber Liquid Membrane Separation Processes |
|
|
253 | (26) |
|
|
|
|
|
|
|
|
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253 | (3) |
|
12.2 Theory of Solute Transport in Liquid Membranes |
|
|
256 | (1) |
|
12.3 Mass Transfer Modeling in Hollow Fiber Contactors |
|
|
257 | (16) |
|
12.3.1 Diffusive Mass Transport Model |
|
|
257 | (1) |
|
12.3.1.1 Diffusional-Kinematic Mass Transport Model |
|
|
259 | (1) |
|
12.3.1.2 Mixed Kinetic Mass Transport Model |
|
|
260 | (2) |
|
12.3.2 Flow and Mass Transfer Model |
|
|
262 | (1) |
|
12.3.2.1 1-D Flow and Mass Transfer Models |
|
|
263 | (1) |
|
12.3.2.2 2-D Flow and Mass Transfer Models |
|
|
264 | (2) |
|
12.3.3 Computational Fluid Dynamics (CFD) Based Models |
|
|
266 | (1) |
|
12.3.3.1 CFD Case Studies of Solvent Extraction Processes |
|
|
270 | (3) |
|
12.4 Conclusions and Future Perspective |
|
|
273 | (1) |
|
|
|
274 | (2) |
|
|
|
276 | (3) |
|
13 Design of Membrane Systems Using Computational Fluid Dynamics and Molecular Modeling |
|
|
279 | (20) |
|
|
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|
|
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|
|
279 | (1) |
|
13.2 Overview of Molecular Modeling and CFD in Membrane Processes |
|
|
280 | (14) |
|
13.2.1 Optimization of Pressure Driven Processes |
|
|
280 | (3) |
|
|
|
283 | (4) |
|
|
|
287 | (3) |
|
13.2.4 Membrane Bioreactor |
|
|
290 | (2) |
|
13.2.5 Other Membrane Processes |
|
|
292 | (2) |
|
|
|
294 | (1) |
|
|
|
295 | (4) |
| Section V Energy |
|
|
14 Carbon-Polymer Nanocomposite Membranes as Electrolytes for Direct Methanol Fuel Cells |
|
|
299 | (18) |
|
|
|
|
|
14.1 Introduction to Direct Methanol Fuel Cells |
|
|
299 | (3) |
|
14.1.1 Challenges in DMFC |
|
|
300 | (1) |
|
14.1.2 Membrane Electrolytes in DMFC |
|
|
300 | (2) |
|
14.2 Functionalized Carbon Nanoadditives in PEMs |
|
|
302 | (2) |
|
14.2.1 Carbon Nanotube Based Composite Membranes |
|
|
302 | (1) |
|
14.2.2 Fullerene Based Composite Membranes |
|
|
303 | (1) |
|
14.2.3 Carbon Nanofiber Based Membranes |
|
|
303 | (1) |
|
14.3 Different Functionalization Routes for Additives |
|
|
304 | (2) |
|
14.3.1 Characterization of Functionalized Additives |
|
|
305 | (1) |
|
14.4 Fabrication of Composite Membranes |
|
|
306 | (1) |
|
14.5 Effect of Functionalized Additives on Membrane Properties |
|
|
306 | (7) |
|
14.5.1 Physico-Chemical Properties |
|
|
306 | (3) |
|
14.5.2 Ion Exchange Capacity and Water Uptake |
|
|
309 | (1) |
|
14.5.3 Proton Conductivity and Methanol Permeability |
|
|
310 | (1) |
|
14.5.4 Oxidative Stability |
|
|
311 | (1) |
|
14.5.5 Fuel Cell Polarization Studies |
|
|
312 | (1) |
|
|
|
313 | (1) |
|
|
|
314 | (1) |
|
|
|
314 | (3) |
|
15 Bioethanol Production in a Pervaporation Membrane Bioreactor |
|
|
317 | (18) |
|
|
|
|
|
|
|
|
|
|
|
317 | (1) |
|
15.2 Production and Consumption Scenario of Bioethanol |
|
|
318 | (1) |
|
15.3 Lignocellulose as Feedstock for Bioethanol Production |
|
|
319 | (1) |
|
15.4 Bioethanol Production from Lignocellulosic Feedstock |
|
|
319 | (1) |
|
|
|
320 | (2) |
|
15.5.1 Types of Fermentation Processes |
|
|
320 | (1) |
|
15.5.2 Fermentation with Immobilized Yeast |
|
|
321 | (1) |
|
15.6 Membrane Bioreactor (MBR) Systems |
|
|
322 | (1) |
|
15.7 Theory of Pervaporation (PV) |
|
|
322 | (1) |
|
15.8 Pervaporation Membranes for Extraction of Ethanol from Aqueous Solutions |
|
|
323 | (1) |
|
15.9 Bioethanol Production in MBR |
|
|
324 | (5) |
|
15.10 Economic Assessment of the Integrated Fermentation-Pervaporation Process |
|
|
329 | (1) |
|
|
|
329 | (1) |
|
|
|
330 | (5) |
|
16 Recovery of Value-Added Products in Process Industries through Membrane Contactors |
|
|
335 | (16) |
|
|
|
|
|
|
|
|
|
335 | (3) |
|
16.2 Introduction to Membrane Contactor Systems |
|
|
338 | (4) |
|
16.2.1 Liquid-Liquid Membrane Contactors |
|
|
338 | (4) |
|
16.2.2 Membrane Distillation |
|
|
342 | (1) |
|
16.2.2.1 Flux and Selectivity Calculations |
|
|
342 | (1) |
|
16.3 Indigenous Membranes and Commercial Modules Investigated for Separation of Chemical Entities |
|
|
342 | (1) |
|
16.4 Results and Discussion |
|
|
343 | (3) |
|
16.4.1 Case Study 1: Reactive Extraction of Carboxylic Acids Using Indigenous Liquid-Liquid Membrane Contactor System |
|
|
343 | (1) |
|
16.4.1.1 Reactive Extraction of Levulinic Acid from Industrial Effluent Using Microporous Polyvinyl Chloride Membrane |
|
|
343 | (1) |
|
16.4.1.2 Reactive Extraction of Acrylic Acid from Synthetic Solution Using Ultraporous Polyvinylidene Fluoride (PVDF)/Polyvinylpyrrolidone (PVP) Blend Membrane |
|
|
344 | (1) |
|
16.4.2 Case Study 2: Recovery of Hexane Volatile Solvent from Sunflower Oil Miscella Using Ultraporous PVC Membrane by Vacuum Membrane Distillation |
|
|
345 | (1) |
|
16.4.2.1 Effect of Downstream Pressure on Membrane Selectivity and Total Flux |
|
|
345 | (1) |
|
16.5 Conclusions and Future Prospects |
|
|
346 | (1) |
|
|
|
347 | (1) |
|
|
|
347 | (1) |
|
|
|
348 | (3) |
|
17 Recent Research Trends in Polymer Nanocomposite Proton Exchange Membranes for Electrochemical Energy Conversion and Storage Devices |
|
|
351 | (24) |
|
|
|
M. Sri Abirami Saraswathi |
|
|
|
|
|
|
|
|
351 | (3) |
|
17.2 Veracities of Nafion in Fuel Cell and VRFB Environments |
|
|
354 | (1) |
|
17.3 Need for Developing Polymer Nanocomposite Membranes |
|
|
355 | (14) |
|
17.3.1 Polymer Nanocomposite Membranes for PEMFC and DMFC Applications |
|
|
356 | (1) |
|
17.3.1.1 PFSA Based Nanocomposite Membranes |
|
|
356 | (1) |
|
17.3.1.2 Sulfonated Hydrocarbon Polymer Based Nanocomposite Membranes with Inorganic Oxides |
|
|
360 | (6) |
|
17.3.2 Polymer Nanocomposite Membranes for VRFB Applications |
|
|
366 | (1) |
|
17.3.2.1 Tailored Nafion Based Nanocomposite Membranes for VRFB Applications |
|
|
366 | (1) |
|
17.3.2.2 Sulfonated Hydrocarbon Polymer Based Nanocomposite Membranes for VRFB Applications |
|
|
367 | (2) |
|
|
|
369 | (1) |
|
|
|
370 | (1) |
|
|
|
370 | (5) |
|
18 Polyion Complex Membranes for Polymer Electrolyte Membrane and Direct Methanol Fuel Cell Applications |
|
|
375 | (22) |
|
|
|
|
|
|
|
|
|
376 | (1) |
|
18.2 Challenges Facing Fuel Cells |
|
|
377 | (1) |
|
18.3 Research Trends in Polymer Electrolyte Membranes for PEMFC and DMFC |
|
|
377 | (1) |
|
18.4 Types of Interactions in Acid-Base Blend Membranes |
|
|
378 | (2) |
|
18.4.1 Dipole-Dipole/van der Waals Interactions |
|
|
379 | (1) |
|
18.4.2 Hydrogen-Bonding Interaction Blend Membranes |
|
|
379 | (1) |
|
18.4.3 Ionically Cross-Linked Acid-Base Blends and Acid-Base Ionomers |
|
|
379 | (1) |
|
18.4.4 Covalently Cross-Linked Blends |
|
|
379 | (1) |
|
18.4.5 Covalently and Ionically Cross-Linked Blends |
|
|
379 | (1) |
|
18.5 Membrane Synthesis by Solution Casting and Solvent Evaporation Method |
|
|
380 | (1) |
|
18.6 Membrane Characterization |
|
|
381 | (1) |
|
18.6.1 Analytical Characterization |
|
|
381 | (1) |
|
18.6.2 Physico-Chemical Characterization |
|
|
381 | (1) |
|
18.6.2.1 Ion Exchange Capacity (IEC) and Sorption Studies |
|
|
381 | (1) |
|
18.6.2.2 Proton Conductivity |
|
|
381 | (1) |
|
18.6.2.3 Methanol Permeability |
|
|
382 | (1) |
|
18.7 Recent Trends in Acid-Base Blend Membranes |
|
|
382 | (6) |
|
|
|
383 | (1) |
|
18.7.2 SPEEK-Based Blend Membrane |
|
|
384 | (1) |
|
|
|
385 | (3) |
|
18.8 Molecular Dynamics Simulation Study for Acid-Base Blend Membranes |
|
|
388 | (3) |
|
18.8.1 Construction of MD Simulation |
|
|
389 | (1) |
|
18.8.1.1 Diffusion Coefficient and Ion-Conductivity |
|
|
389 | (1) |
|
18.8.1.2 Radial Distribution Function (RDF) |
|
|
390 | (1) |
|
|
|
391 | (1) |
|
|
|
391 | (6) |
| Section VI Environment |
|
|
19 Integrated Membrane Technology for Promoting Zero Liquid Discharge in Process Industries |
|
|
397 | (20) |
|
|
|
|
|
|
|
|
|
397 | (1) |
|
19.2 Current Status of Membrane Processes for Industrial Growth |
|
|
398 | (1) |
|
19.3 Membrane Process Integration for Industrial Sustainability |
|
|
399 | (2) |
|
19.4 Breakthrough Advancements of Membrane Processes in Industries |
|
|
401 | (4) |
|
|
|
402 | (1) |
|
19.4.2 Pressure-Retarded Osmosis |
|
|
403 | (1) |
|
19.4.3 Continuous Electro-Deionization |
|
|
404 | (1) |
|
|
|
404 | (1) |
|
19.5 Membrane Technology for Facilitating Zero Liquid Discharge (ZLD) in Industries |
|
|
405 | (3) |
|
19.5.1 Conventional Zero Liquid Discharge Systems |
|
|
405 | (1) |
|
19.5.2 Hybrid Zero Liquid Discharge Systems |
|
|
406 | (1) |
|
19.5.2.1 ZLD Combined with Reverse Osmosis |
|
|
407 | (1) |
|
19.5.2.2 ZLD Combined with Electrodialysis |
|
|
407 | (1) |
|
19.5.2.3 ZLD Combined with Membrane Distillation |
|
|
407 | (1) |
|
19.6 Potential of Membrane Technology Toward ZLD |
|
|
408 | (1) |
|
19.7 Advancements and Scope of Membrane Technology for ZLD |
|
|
408 | (1) |
|
19.8 Emerging Trends in State-of-the-Art ZLD Systems |
|
|
408 | (1) |
|
19.9 Computational Aspects in Membrane Processes |
|
|
409 | (3) |
|
19.9.1 Simulation of Spiral Wound Membranes |
|
|
410 | (1) |
|
19.9.2 Simulation of Hollow Fiber Membranes |
|
|
411 | (1) |
|
19.9.3 Design of Membrane Systems |
|
|
412 | (1) |
|
|
|
412 | (1) |
|
|
|
413 | (4) |
|
20 Electromembrane Processes in Water Purification and Energy Generation |
|
|
417 | (26) |
|
|
|
Jogi Ganesh Dattatreya Tadimeti |
|
|
|
|
|
|
|
|
417 | (1) |
|
|
|
418 | (2) |
|
20.3 Ion Exchange Membranes |
|
|
420 | (2) |
|
20.4 Mathematical Representation of Various Fluxes in Electrodialysis Process |
|
|
422 | (1) |
|
20.5 Current-Voltage Characteristics |
|
|
423 | (1) |
|
|
|
423 | (1) |
|
|
|
424 | (1) |
|
20.5.3 Over Limiting Region |
|
|
424 | (1) |
|
20.6 Concentration Polarization |
|
|
424 | (1) |
|
20.7 LCD Determination and Parameters Influencing LCD |
|
|
425 | (1) |
|
20.8 Mass Transfer Enhancement in Electrodialysis |
|
|
426 | (1) |
|
20.9 Facilitation of Electrodialysis |
|
|
427 | (2) |
|
20.10 Role of Mathematical Modeling in Electrodialysis |
|
|
429 | (1) |
|
20.11 Challenges and Proposed Remedies in Electrodialysis |
|
|
430 | (1) |
|
20.12 Applications of Electrodialysis |
|
|
431 | (2) |
|
20.13 Bipolar Membrane Electrodialysis (EDBPM) |
|
|
433 | (1) |
|
20.14 Bipolar Membrane Preparation and Characterization |
|
|
434 | (1) |
|
20.15 Bipolar Membrane Applications |
|
|
435 | (1) |
|
20.16 Capacitive Deionization |
|
|
435 | (1) |
|
20.17 Energy Generation through Reverse Electrodialysis |
|
|
436 | (1) |
|
|
|
437 | (1) |
|
|
|
438 | (5) |
|
21 Adsorption-Membrane Filtration Hybrid Process in Wastewater Treatment |
|
|
443 | (18) |
|
|
|
|
|
|
|
|
|
443 | (1) |
|
|
|
444 | (4) |
|
21.2.1 Adsorption Kinetics |
|
|
446 | (1) |
|
21.2.2 Adsorption Isotherms |
|
|
447 | (1) |
|
|
|
448 | (1) |
|
21.4 Adsorption-Membrane Hybrid Process |
|
|
449 | (7) |
|
21.4.1 Adsorption-Membrane Filtration Hybridization Scheme |
|
|
449 | (1) |
|
21.4.1.1 First Scheme: Adsorption-Submersed Membrane Filtration |
|
|
449 | (1) |
|
21.4.1.2 Second Scheme: Coupling of Adsorption Process with Membrane Filtration |
|
|
450 | (1) |
|
21.4.1.3 Third Scheme: PAC Dynamic Membrane |
|
|
451 | (2) |
|
21.4.2 Effect of Adsorption Process on Hybrid Process |
|
|
453 | (1) |
|
21.4.3 Effect of Membrane Process on Hybrid Process |
|
|
453 | (1) |
|
21.4.4 Application of Adsorption-Membrane Filtration Hybrid Process |
|
|
454 | (1) |
|
21.4.5 Extension of Adsorption-Membrane Hybrid Process |
|
|
454 | (2) |
|
21.5 Conclusions and Future Scope |
|
|
456 | (1) |
|
|
|
457 | (1) |
|
|
|
457 | (4) |
|
22 Layer-by-Layer (Lbl) Coated Multilayer Membranes in Dye House Effluent Treatment |
|
|
461 | (16) |
|
|
|
|
|
|
|
Charuvila T. Aravindakumar |
|
|
|
|
461 | (1) |
|
22.2 Water Consumption in the Textile Sector |
|
|
462 | (1) |
|
22.3 Overview of Textile Processing and Major Pollutants |
|
|
463 | (1) |
|
22.4 Natural vs. Synthetic Dyes |
|
|
463 | (1) |
|
22.5 Treatment Methods for Textile Wastewater |
|
|
464 | (1) |
|
22.6 Membrane Separation Processes |
|
|
465 | (2) |
|
22.6.1 Microfiltration in Textile Effluent Treatment |
|
|
465 | (1) |
|
|
|
466 | (1) |
|
22.7 Layer-by-Layer (LbL) Assembly |
|
|
467 | (1) |
|
22.8 Materials in LbL Assembly |
|
|
468 | (1) |
|
22.9 LbL Assembled MF Membranes for Textile Dye Removal |
|
|
469 | (4) |
|
22.10 Conclusions and Future Prospects |
|
|
473 | (1) |
|
|
|
473 | (4) |
|
23 Membrane Technology-A Sustainable Approach for Environmental Protection |
|
|
477 | (18) |
|
|
|
|
|
|
|
|
|
477 | (2) |
|
23.2 Brief about Membrane Technology |
|
|
479 | (1) |
|
23.3 Application of Membrane Technology in Environmental Protection |
|
|
480 | (10) |
|
23.3.1 Municipal Wastewater Treatment |
|
|
480 | (1) |
|
23.3.2 Pharmaceutical Waste Treatment |
|
|
481 | (1) |
|
23.3.3 Heavy Metal Removal from Ground Water |
|
|
482 | (1) |
|
|
|
483 | (2) |
|
23.3.5 Tannery and Dye Waste Treatment |
|
|
485 | (1) |
|
23.3.6 Application in Paper and Pulp Industries |
|
|
486 | (1) |
|
23.3.7 Dairy Wastewater Treatment |
|
|
487 | (1) |
|
23.3.7.1 Case Study on Application of Membrane Technology in Dairy Effluent Treatment |
|
|
488 | (2) |
|
23.4 Advanced Membrane Separation Process for Treatment of Different Waste Streams |
|
|
490 | (1) |
|
|
|
490 | (5) |
|
24 Processing of Dairy Industrial Effluent and Kitchen Wastewater by Integration of Microbial Action with Membrane Processes |
|
|
495 | (22) |
|
|
|
|
|
|
|
|
|
496 | (1) |
|
24.2 Membrane Filtration Technology |
|
|
496 | (1) |
|
24.2.1 Membrane Characteristics |
|
|
496 | (1) |
|
24.2.2 Classification of Membranes |
|
|
497 | (1) |
|
24.3 Potential of Membrane Filtration When Combined with Biological Process |
|
|
497 | (1) |
|
24.4 Challenges Facing MBR and MFC Technologies |
|
|
498 | (1) |
|
24.5 Types of Membrane Bioreactors |
|
|
499 | (3) |
|
24.5.1 Submerged/Immersed MBR |
|
|
499 | (1) |
|
24.5.2 Side-Stream/External MBR |
|
|
500 | (1) |
|
24.5.3 Advancements in MBR Process |
|
|
500 | (1) |
|
24.5.4 Microbial Consortia Used in MBR |
|
|
501 | (1) |
|
|
|
502 | (2) |
|
24.6.1 Design and Working of Microbial Fuel Cell (MFC) |
|
|
502 | (1) |
|
24.6.2 Advantages in MFC Process |
|
|
503 | (1) |
|
24.6.3 Microbial Consortia Used in MFC |
|
|
503 | (1) |
|
24.7 Experimental Case Study with Kitchen Wastewater |
|
|
504 | (1) |
|
24.7.1 Collection of Kitchen Wastewater |
|
|
504 | (1) |
|
24.7.2 Preparation of Inoculums |
|
|
504 | (1) |
|
24.7.3 Description of Submerged/Internal MBR (SMBR) |
|
|
504 | (1) |
|
24.8 Experimental Case Study on Dairy Industrial Effluent |
|
|
504 | (3) |
|
24.8.1 Collection of Dairy Industrial Effluent |
|
|
504 | (1) |
|
24.8.2 Preparation of Inoculums |
|
|
504 | (2) |
|
24.8.3 Description of Side-Stream/External MBR (SSMBR) |
|
|
506 | (1) |
|
24.8.4 Description of Laboratory MFC Unit for Treatment of Kitchen Wastewater |
|
|
506 | (1) |
|
24.9 Sampling and Analytical Methods |
|
|
507 | (1) |
|
24.10 Membrane Fouling and Its Prevention |
|
|
507 | (1) |
|
24.11 Results and Discussion |
|
|
508 | (3) |
|
24.11.1 Treatment of Kitchen Wastewater and Dairy Effluent |
|
|
508 | (1) |
|
24.11.2 Case Study on Kitchen Wastewater |
|
|
509 | (1) |
|
24.11.3 Case Study on Dairy Effluent |
|
|
510 | (1) |
|
24.11.4 Color Removal from Kitchen Wastewater and Dairy Effluent |
|
|
510 | (1) |
|
24.11.5 Treatment of Kitchen Wastewater by MFC |
|
|
511 | (1) |
|
|
|
511 | (1) |
|
|
|
512 | (3) |
|
|
|
515 | (2) |
| Index |
|
517 | |