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Chapter 1 Reverse osmosis |
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1 | (6) |
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1 | (3) |
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1.2 Definition and Osmotic Pressure |
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4 | (1) |
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5 | (2) |
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Chapter 2 SWRO desalination plants |
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7 | (30) |
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7 | (1) |
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8 | (2) |
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9 | (1) |
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9 | (1) |
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10 | (8) |
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2.3.1 Dissolved air flotation |
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10 | (3) |
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2.3.2 Dual media nitration |
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13 | (2) |
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2.3.3 Membrane-based pretreatment |
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15 | (2) |
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17 | (1) |
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18 | (3) |
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18 | (1) |
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2.4.2 Energy-recovery device |
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19 | (2) |
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21 | (2) |
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23 | (8) |
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2.6.1 RO pass configuration |
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24 | (2) |
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2.6.2 SWRO system configuration |
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26 | (3) |
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2.6.3 BWRO system configuration |
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29 | (2) |
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31 | (3) |
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2.7.1 Stabilization and corrosion control |
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32 | (1) |
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32 | (1) |
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2.7.3 Alkalinity adjustment |
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32 | (1) |
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2.7.4 Hardness (CaCO3) adjustment |
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33 | (1) |
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33 | (1) |
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2.7.6 Aeration and degasification |
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33 | (1) |
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34 | (3) |
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2.8.1 Conventional discharge strategy |
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34 | (1) |
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2.8.2 Discharge to injection wells |
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34 | (1) |
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2.8.3 Discharge to offshore galleries and trenches |
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34 | (1) |
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2.8.4 Zero liquid discharge (ZLD) |
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35 | (1) |
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2.8.5 Dilution of concentrate using forward osmosis process |
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35 | (2) |
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Chapter 3 Energy consumption in SWRO operation |
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37 | (18) |
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3.1 Membrane Transport Mechanism in a Small-Scale System |
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37 | (11) |
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3.1.1 Solution--diffusion theory |
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37 | (2) |
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3.1.2 Permeate resistance |
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39 | (1) |
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3.1.3 Concentration polarization |
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40 | (2) |
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42 | (6) |
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3.2 Membrane Transport Mechanism in Module-Scale Operation |
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48 | (3) |
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3.3 Energy Consumption Model in the RO Process |
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51 | (4) |
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Chapter 4 Recent trends in the SEC of SWRO |
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55 | (18) |
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4.1 SWRO Plants Worldwide |
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55 | (1) |
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55 | (1) |
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55 | (1) |
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56 | (1) |
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4.2 Increasing Large-Scale SWRO Applications |
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56 | (8) |
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4.3 Using ERDs with High Energy Efficiency |
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64 | (1) |
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4.4 Increasing Product Water Quantity |
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65 | (1) |
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4.5 Improving Product Water Quality |
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66 | (1) |
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4.6 Applying Multiple Pretreatment Methods for Harmful Algal Blooms |
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67 | (3) |
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4.7 Performing Retrofitting and Expansion |
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70 | (1) |
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4.8 Utilizing Renewable Energy |
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71 | (2) |
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Chapter 5 Factors affecting the SEC of SWRO plants |
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73 | (12) |
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5.1 Specific Energy Consumption of Pre- and Post-Treatment |
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73 | (1) |
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74 | (2) |
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74 | (1) |
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74 | (1) |
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5.2.3 Overall feed conditions |
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75 | (1) |
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76 | (2) |
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76 | (1) |
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77 | (1) |
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78 | (4) |
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78 | (2) |
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80 | (2) |
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5.5 Summary and Future Directions |
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82 | (3) |
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Chapter 6 Advanced technologies for a low-energy SWRO process |
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85 | (66) |
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6.1 Theoretical Energy Calculation of the SWRO Process |
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85 | (10) |
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6.1.1 Exergy analysis for theoretical minimum energy |
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85 | (6) |
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6.1.2 Analysis of future directions for low-energy SWRO |
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91 | (3) |
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6.1.3 Maximum available margin for low-energy SWRO |
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94 | (1) |
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6.2 Minimizing Irreversibility in a High-Pressure Pump |
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95 | (12) |
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95 | (3) |
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98 | (1) |
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99 | (2) |
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101 | (4) |
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6.2.5 Energy comparison of minimizing irreversibility in HPP |
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105 | (2) |
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6.3 Reducing the Osmotic Pressure of Seawater |
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107 | (10) |
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6.3.1 Split partial single pass |
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107 | (2) |
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6.3.2 FO and reverse osmosis (RO) hybrid process |
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109 | (3) |
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6.3.3 Draw solution-assisted RO |
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112 | (2) |
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6.3.4 Energy comparison of reducing the osmotic pressure of seawater |
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114 | (3) |
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6.4 Osmotic Energy Recovery in Concentrate Streams |
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117 | (8) |
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6.4.1 Pressure retarded osmosis |
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117 | (3) |
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6.4.2 Reverse electrodialysis |
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120 | (4) |
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6.4.3 Osmotic energy recovery in a concentrate stream |
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124 | (1) |
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6.5 Improvement of RO Membranes |
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125 | (26) |
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6.5.1 Introduction of novel building blocks |
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126 | (1) |
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6.5.2 RO membrane surface modification |
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126 | (1) |
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6.5.3 Biomimetic RO membranes |
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127 | (1) |
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6.5.4 Inorganic RO membranes |
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128 | (1) |
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6.5.5 Mixed matrix RO membranes |
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129 | (2) |
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Chapter 7 Concluding remarks and epilogue |
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131 | (1) |
Acknowledgments |
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132 | (1) |
References |
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133 | (26) |
Index |
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159 | |