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Introduction to Unit Operations: Fundamental Concepts |
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1 | (10) |
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1 | (1) |
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1 | (1) |
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Transformation and Commercialization of Agricultural Products |
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2 | (1) |
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Flow Charts and Description of Some Food Processes |
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2 | (1) |
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Steady and Unsteady States |
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3 | (1) |
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Discontinuous, Continuous, and Semicontinuous Operations |
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3 | (3) |
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Unit Operations: Classification |
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6 | (3) |
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Momentum Transfer Unit Operations |
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7 | (1) |
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Mass Transfer Unit Operations |
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8 | (1) |
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Heat Transfer Unit Operations |
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8 | (1) |
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Simultaneous Mass-Heat Transfer Unit Operations |
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8 | (1) |
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Complementary Unit Operations |
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9 | (1) |
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Mathematical Setup of the Problems |
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9 | (2) |
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Unit Systems: Dimensional Analysis and Similarity |
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11 | (32) |
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Magnitude and Unit Systems |
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11 | (6) |
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11 | (1) |
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12 | (1) |
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12 | (1) |
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International Unit System (IS) |
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13 | (1) |
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14 | (1) |
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15 | (2) |
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17 | (6) |
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18 | (2) |
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Dimensional Analysis Methods |
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20 | (1) |
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20 | (2) |
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22 | (1) |
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Method of Differential Equations |
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22 | (1) |
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23 | (20) |
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24 | (1) |
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25 | (1) |
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25 | (1) |
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25 | (1) |
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25 | (5) |
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30 | (13) |
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Introduction to Transport Phenomena |
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43 | (10) |
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43 | (1) |
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Transport Phenomena: Definition |
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44 | (1) |
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Circulation Regimes: Reynolds' Experiment |
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45 | (3) |
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Mechanisms of Transport Phenomena |
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48 | (5) |
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49 | (1) |
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50 | (1) |
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50 | (1) |
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50 | (1) |
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51 | (2) |
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Molecular Transport of Momentum, Energy, and Mass |
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53 | (12) |
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53 | (1) |
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Momentum Transport: Newton's Law of Viscosity |
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53 | (2) |
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Energy Transmission: Fourier's Law of Heat Conduction |
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55 | (2) |
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Mass Transfer: Fick's Law of Diffusion |
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57 | (4) |
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General Equation of Velocity |
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61 | (4) |
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65 | (24) |
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65 | (1) |
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65 | (5) |
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Mollier's Psychrometric Diagram for Humid Air |
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70 | (5) |
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Psychrometric Chart sT - X |
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70 | (4) |
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Psychrometric Chart X - T |
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74 | (1) |
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75 | (2) |
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Adiabatic Saturation of Air |
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77 | (12) |
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80 | (9) |
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Rheology of Food Products |
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89 | (54) |
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89 | (1) |
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90 | (3) |
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Elastic Solids and Newtonian Fluids |
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93 | (2) |
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95 | (1) |
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Rheological Classification of Fluid Foods |
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96 | (1) |
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97 | (2) |
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99 | (8) |
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99 | (4) |
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103 | (4) |
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107 | (6) |
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113 | (1) |
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Effect of Concentration on Viscosity |
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114 | (4) |
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Structural Theories of Viscosity |
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114 | (1) |
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115 | (2) |
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Combined Effect: Temperature--Concentration |
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117 | (1) |
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118 | (3) |
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118 | (1) |
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118 | (1) |
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118 | (2) |
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120 | (1) |
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121 | (1) |
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Mechanical Model of the Bingham's Body |
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121 | (1) |
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Rheological Measures in Semiliquid Foods |
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121 | (22) |
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123 | (1) |
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123 | (1) |
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Concentric Cylinders Viscometers |
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123 | (3) |
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Plate--Plate and Cone--Plate Viscometers |
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126 | (2) |
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128 | (2) |
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130 | (2) |
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132 | (1) |
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Back Extrusion Viscometry |
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132 | (3) |
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Squeezing Flow Viscometry |
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135 | (1) |
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136 | (1) |
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136 | (1) |
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137 | (1) |
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137 | (1) |
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137 | (1) |
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138 | (5) |
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Transport of Fluids through Pipes |
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143 | (62) |
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143 | (1) |
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Circulation of Incompressible Fluids |
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144 | (16) |
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Criteria for Laminar Flow |
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144 | (3) |
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147 | (2) |
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149 | (4) |
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153 | (2) |
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Flow in Noncylindrical Piping |
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155 | (2) |
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Universal Velocity Profile |
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157 | (3) |
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Macroscopic Balances in Fluid Circulation |
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160 | (6) |
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160 | (1) |
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161 | (1) |
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162 | (3) |
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Mechanical Energy Balance |
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165 | (1) |
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166 | (13) |
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166 | (1) |
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Calculation of Friction Factors |
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167 | (1) |
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Flow under Laminar Regime |
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168 | (2) |
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Flow under Turbulent Regime |
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170 | (3) |
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Minor Mechanical Energy Losses |
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173 | (2) |
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175 | (1) |
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175 | (4) |
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179 | (7) |
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Calculation of Velocity and Circulation Flow Rate |
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179 | (2) |
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Calculation of Minimum Diameter of Piping |
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181 | (1) |
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182 | (1) |
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182 | (1) |
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183 | (1) |
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184 | (2) |
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186 | (19) |
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Characteristics of a Pump |
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186 | (1) |
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187 | (1) |
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188 | (1) |
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188 | (1) |
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Net Positive Suction Head: Cavitation |
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189 | (1) |
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Installation Point of a Pump |
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190 | (1) |
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191 | (1) |
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191 | (1) |
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191 | (2) |
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193 | (12) |
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Circulation of Fluid through Porous Beds: Fluidization |
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205 | (30) |
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205 | (1) |
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Darcy's Law: Permeability |
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205 | (1) |
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206 | (4) |
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206 | (1) |
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207 | (3) |
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Equations for Flow through Porous Beds |
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210 | (6) |
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Laminar Flow: Equation of Kozeny--Carman |
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210 | (2) |
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Turbulent Flow: Equation of Burke--Plummer |
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212 | (1) |
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Laminar-Turbulent Global Flow: Equations of Ergun and Chilton--Colburn |
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213 | (3) |
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216 | (19) |
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Minimal Velocity of Fluidization |
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218 | (1) |
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219 | (1) |
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219 | (1) |
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220 | (1) |
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Minimal Porosity of Fluizidation |
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220 | (1) |
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221 | (1) |
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222 | (13) |
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235 | (30) |
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235 | (1) |
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Fundamentals of Filtration |
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235 | (6) |
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Resistance of the Filtering Cake |
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236 | (3) |
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Filtering Medium Resistance |
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239 | (1) |
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Total Filtration Resistance |
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240 | (1) |
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241 | (1) |
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Filtration at Constant Pressure Drop |
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241 | (3) |
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Filtration at Constant Volumetric Flow |
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244 | (1) |
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245 | (3) |
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248 | (1) |
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Optimal Filtration Conditions at Constant Pressure |
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248 | (2) |
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Rotary Vacuum Disk Filter |
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250 | (15) |
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253 | (12) |
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Separation Processes by Membranes |
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265 | (44) |
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265 | (5) |
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267 | (2) |
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Polarization by Concentration |
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269 | (1) |
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Mass Transfer in Membranes |
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270 | (4) |
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270 | (1) |
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Simultaneous Diffusion and Capillary Flow Model |
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270 | (1) |
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Simultaneous Viscous and Friction Flow Model |
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271 | (1) |
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Preferential Adsorption and Capillary Flow Model |
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272 | (1) |
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Model Based on the Thermodynamics of Irreversible Processes |
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273 | (1) |
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Models for Transfer through the Polarization Layer |
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274 | (6) |
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274 | (5) |
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279 | (1) |
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280 | (7) |
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280 | (3) |
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Polarization Layer by Concentration |
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283 | (1) |
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Influence of Different Factors |
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284 | (1) |
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284 | (1) |
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285 | (2) |
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287 | (1) |
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287 | (6) |
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288 | (1) |
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Concentration Polarization Layer |
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289 | (2) |
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Influence of Different Factors |
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291 | (1) |
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291 | (1) |
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292 | (1) |
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293 | (1) |
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Design of Reverse Osmosis and Ultrafiltration Systems |
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293 | (5) |
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294 | (3) |
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297 | (1) |
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Operative Layout of the Modules |
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298 | (11) |
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298 | (1) |
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299 | (1) |
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Two Stages with Recirculation |
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300 | (1) |
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301 | (8) |
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Thermal Properties of Food |
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309 | (12) |
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309 | (2) |
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311 | (2) |
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313 | (3) |
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316 | (5) |
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319 | (2) |
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Heat Transfer by Conduction |
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321 | (46) |
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Fundamental Equations in Heat Conduction |
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321 | (4) |
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321 | (3) |
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324 | (1) |
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325 | (1) |
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Heat Conduction under Steady Regime |
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325 | (14) |
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Monodimensional Heat Conduction |
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326 | (1) |
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327 | (2) |
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329 | (3) |
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332 | (2) |
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Bidimensional Heat Conduction |
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334 | (2) |
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336 | (1) |
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337 | (1) |
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Tridimensional Heat Conduction |
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337 | (2) |
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Heat Conduction under Unsteady State |
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339 | (28) |
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Monodimensional Heat Conduction |
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339 | (1) |
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340 | (7) |
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Numerical and Graphical Methods |
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347 | (4) |
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Bi- and Tridimensinal Heat Conduction: Newman's Rule |
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351 | (1) |
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352 | (15) |
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Heat Transfer by Convection |
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367 | (100) |
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367 | (1) |
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Heat Transfer Coefficients |
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367 | (11) |
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367 | (3) |
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370 | (1) |
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371 | (2) |
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Convection in Non-Newtonian Fluids |
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373 | (1) |
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374 | (4) |
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Concentric Tube Heat Exchangers |
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378 | (6) |
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378 | (1) |
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378 | (4) |
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382 | (1) |
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Calculation of Individual Coefficients |
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383 | (1) |
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Calculation of Head Losses |
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384 | (1) |
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Shell and Tube Heat Exchangers |
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384 | (12) |
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385 | (3) |
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Calculation of the True Logarithmic Mean Temperature Difference |
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388 | (1) |
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Calculation of Individual Coefficients |
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389 | (1) |
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Coefficients for the Inside of the Tubes |
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390 | (2) |
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Coefficients on the Side of the Shell |
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392 | (3) |
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Calculation of Head Losses |
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395 | (1) |
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395 | (1) |
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Head Losses on the Shell Side |
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395 | (1) |
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Plate-Type Heat Exchangers |
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396 | (13) |
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399 | (2) |
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401 | (1) |
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Calculation of the True Logarithmic Mean Temperature Difference |
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402 | (1) |
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Calculation of the Heat Transfer Coefficients |
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403 | (3) |
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Calculation of Head Losses |
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406 | (1) |
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407 | (2) |
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Extended Surface Heat Exchangers |
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409 | (6) |
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411 | (1) |
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412 | (2) |
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Calculation of Extended Surface Heat Exchangers |
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414 | (1) |
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Scraped Surface Heat Exchangers |
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415 | (2) |
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Agitated Vessels with Jacket and Coils |
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417 | (1) |
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Individual Coefficient inside the Vessel |
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417 | (1) |
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Individual Coefficient inside the Coil |
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418 | (1) |
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Individual Coefficient in the Jacket |
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418 | (1) |
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418 | (49) |
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425 | (42) |
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Heat Transfer by Radiation |
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467 | (24) |
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467 | (1) |
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468 | (1) |
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468 | (1) |
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468 | (1) |
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469 | (1) |
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469 | (5) |
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469 | (2) |
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Monochromatic Properties: Kirchhoff's Law |
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471 | (1) |
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472 | (2) |
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474 | (4) |
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Definition and Calculation |
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474 | (1) |
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Properties of View Factors |
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475 | (3) |
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Exchange of Radiant Energy between Surfaces Separated by Nonabsorbing Media |
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478 | (4) |
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Radiation between Black Surfaces |
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479 | (1) |
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Radiation between a Surface and a Black Surface Completely Surrounding It |
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479 | (1) |
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Radiation between Black Surfaces in the Presence of Refractory Surfaces: Refractory Factor |
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480 | (1) |
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Radiation between Nonblack Surfaces: Gray Factor |
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481 | (1) |
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Coefficient of Heat Transfer by Radiation |
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482 | (2) |
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Simultaneous Heat Transfer by Convection and Radiation |
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484 | (7) |
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485 | (6) |
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Thermal Processing of Foods |
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491 | (44) |
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491 | (1) |
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491 | (11) |
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492 | (1) |
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493 | (1) |
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Thermal Death Time Constant z |
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493 | (4) |
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497 | (1) |
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498 | (3) |
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501 | (1) |
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Effect of Temperature on Rate and Thermal Treatment Parameters |
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501 | (1) |
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Treatment of Canned Products |
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502 | (6) |
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502 | (3) |
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Methods to Determine Lethality |
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505 | (1) |
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505 | (1) |
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506 | (2) |
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Thermal Treatment in Aseptic Processing |
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508 | (27) |
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510 | (1) |
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Dispersion of Residence Times |
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511 | (2) |
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Distribution Function E under Ideal Behavior |
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513 | (3) |
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Distribution Function E under Nonideal Behavior |
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516 | (3) |
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Application of the Distribution Models to Continuous Thermal Treatment |
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519 | (2) |
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521 | (14) |
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Food Preservation by Cooling |
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535 | (38) |
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535 | (2) |
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537 | (4) |
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538 | (2) |
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Equivalent Molecular Weight of Solutes |
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540 | (1) |
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Thermal Properties of Frozen Foods |
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541 | (2) |
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541 | (1) |
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541 | (1) |
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542 | (1) |
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543 | (6) |
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Design of Freezing Systems |
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549 | (1) |
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550 | (1) |
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Refrigeration Mechanical Systems |
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551 | (4) |
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555 | (1) |
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556 | (17) |
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Systems with Two Compressors and One Evaporator |
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559 | (2) |
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Systems with Two Compressors and Two Evaporators |
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561 | (2) |
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563 | (10) |
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573 | (52) |
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573 | (1) |
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Mixing of Two Air Streams |
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574 | (1) |
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Mass and Heat Balances in Ideal Dryers |
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575 | (2) |
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Continuous Dryer without Recirculation |
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575 | (1) |
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Continuous Dryer with Recirculation |
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576 | (1) |
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577 | (7) |
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577 | (3) |
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Constant Rate Drying Period |
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580 | (2) |
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Falling Rate Drying Period |
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582 | (1) |
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582 | (2) |
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584 | (10) |
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585 | (2) |
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587 | (1) |
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587 | (2) |
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Discontinuous Dryers with Air Circulation through the Bed |
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589 | (3) |
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592 | (2) |
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594 | (10) |
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595 | (3) |
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598 | (2) |
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Two-Fluid Pneumatic Atomizers |
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600 | (2) |
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Interaction between Droplets and Drying Air |
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602 | (1) |
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602 | (2) |
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604 | (10) |
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607 | (1) |
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Primary and Secondary Drying Stages |
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607 | (1) |
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Simultaneous Heat and Mass Transfer |
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607 | (7) |
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614 | (11) |
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614 | (1) |
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615 | (1) |
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616 | (1) |
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616 | (1) |
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617 | (1) |
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618 | (7) |
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625 | (46) |
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|
625 | (1) |
|
Heat Transfer in Evaporators |
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626 | (6) |
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Enthalpies of Vapors and Liquids |
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627 | (2) |
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|
629 | (2) |
|
Heat Transfer Coefficients |
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631 | (1) |
|
Single Effect Evaporators |
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632 | (2) |
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634 | (6) |
|
Recompression of Released Vapor |
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634 | (1) |
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634 | (2) |
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636 | (1) |
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637 | (1) |
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638 | (2) |
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Multiple-Effect Evaporators |
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640 | (9) |
|
Circulation Systems of Streams |
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640 | (1) |
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640 | (2) |
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642 | (1) |
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642 | (1) |
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|
642 | (1) |
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|
643 | (2) |
|
Resolution of the Mathematical Model |
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|
645 | (1) |
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|
646 | (1) |
|
Iterative Method when there is Boiling Point Rise |
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|
647 | (1) |
|
Iterative Method when there is No Boiling Point Rise |
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|
648 | (1) |
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|
649 | (22) |
|
Natural Circulation Evaporators |
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|
649 | (1) |
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|
649 | (1) |
|
Short Tube Horizontal Evaporator |
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|
649 | (1) |
|
Short Tube Vertical Evaporator |
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|
650 | (1) |
|
Evaporator with External Calandria |
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|
651 | (1) |
|
Forced Circulation Evaporators |
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|
651 | (1) |
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|
652 | (2) |
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|
654 | (1) |
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|
654 | (17) |
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|
671 | (52) |
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|
671 | (1) |
|
Liquid--Vapor Equilibrium |
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|
671 | (7) |
|
Partial Pressures: Laws of Dalton, Raoult, and Henry |
|
|
674 | (2) |
|
|
676 | (1) |
|
Enthalpy Composition Diagram |
|
|
677 | (1) |
|
Distillation of Binary Mixtures |
|
|
678 | (4) |
|
|
678 | (2) |
|
|
680 | (2) |
|
Continuous Rectification of Binary Mixtures |
|
|
682 | (20) |
|
Calculation of the Number of Plates |
|
|
684 | (1) |
|
|
684 | (3) |
|
Solution of the Mathematical Model: Method of McCabe--Thiele |
|
|
687 | (4) |
|
|
691 | (1) |
|
Minimum Reflux Relationship |
|
|
691 | (3) |
|
Number of Plates for Total Reflux |
|
|
694 | (1) |
|
Multiple Feed Lines and Lateral Extraction |
|
|
694 | (3) |
|
|
697 | (1) |
|
|
698 | (3) |
|
|
701 | (1) |
|
Discontinuous Rectification |
|
|
702 | (4) |
|
Operation with Constant Distillate Composition |
|
|
702 | (3) |
|
Operation under Constant Reflux Ratio |
|
|
705 | (1) |
|
|
706 | (17) |
|
|
708 | (15) |
|
|
723 | (50) |
|
|
723 | (1) |
|
|
724 | (2) |
|
|
726 | (6) |
|
|
727 | (1) |
|
Basic Mass Transfer Equations |
|
|
727 | (1) |
|
Diffusion in the Gas Phase |
|
|
728 | (1) |
|
Diffusion in the Liquid Phase |
|
|
729 | (1) |
|
|
729 | (3) |
|
|
732 | (23) |
|
|
732 | (1) |
|
|
733 | (1) |
|
|
733 | (3) |
|
|
736 | (2) |
|
Selection of Packing Type: Calculation of the Column Diameter |
|
|
738 | (2) |
|
Packing Static Characteristics |
|
|
740 | (1) |
|
Packing Dynamic Characteristics |
|
|
741 | (1) |
|
Determination of Flooding Rate |
|
|
742 | (2) |
|
Determination of Packing Type |
|
|
744 | (1) |
|
Calculation of the Column Height |
|
|
745 | (1) |
|
|
746 | (3) |
|
|
749 | (2) |
|
Calculation of the Number of Transfer Units |
|
|
751 | (3) |
|
Calculation of the Height of the Transfer Unit |
|
|
754 | (1) |
|
|
755 | (18) |
|
|
758 | (15) |
|
|
773 | (50) |
|
|
773 | (1) |
|
Solid--Liquid Equilibrium |
|
|
774 | (8) |
|
Retention of Solution and Solvent |
|
|
776 | (1) |
|
Triangular and Rectangular Diagrams |
|
|
777 | (1) |
|
|
777 | (4) |
|
|
781 | (1) |
|
|
782 | (17) |
|
|
782 | (4) |
|
Multistage Concurrent System |
|
|
786 | (6) |
|
Continuous Countercurrent Multistage System |
|
|
792 | (7) |
|
Solid--Liquid Extraction Equipment |
|
|
799 | (7) |
|
|
800 | (1) |
|
Fixed-Bed Multistage Systems |
|
|
801 | (1) |
|
|
801 | (3) |
|
Other Types of Extractors |
|
|
804 | (2) |
|
Applications to the Food Industry |
|
|
806 | (17) |
|
|
810 | (13) |
|
Adsorption and Ionic Exchange |
|
|
823 | (32) |
|
|
823 | (1) |
|
|
823 | (1) |
|
|
823 | (1) |
|
|
824 | (4) |
|
|
824 | (3) |
|
Ionic Exchange Equilibrium |
|
|
827 | (1) |
|
|
828 | (1) |
|
|
828 | (1) |
|
|
829 | (1) |
|
|
829 | (5) |
|
|
830 | (1) |
|
|
831 | (1) |
|
Countercurrent Multiple Contact |
|
|
832 | (2) |
|
|
834 | (2) |
|
|
836 | (19) |
|
Fixed-Bed Columns with Phase Equilibrium |
|
|
837 | (1) |
|
|
837 | (1) |
|
|
838 | (4) |
|
Calculation of Height of Exchange Zone in an Adsorption Column |
|
|
842 | (2) |
|
Calculation of Height of Exchange Zone in an Ionic Exchange Column |
|
|
844 | (2) |
|
|
846 | (9) |
References |
|
855 | (10) |
Appendix |
|
865 | (10) |
Index |
|
875 | |