| Professor J. M. Coulson |
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xiii | |
| Preface to Sixth Edition |
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xv | |
| Preface to Fifth Edition |
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xvii | |
| Preface to Fourth Edition |
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xix | |
| Preface to Third Edition |
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xxi | |
| Preface to Second Edition |
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xxiii | |
| Preface to First Edition |
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xxv | |
| Acknowledgements |
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xxvii | |
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1 | (24) |
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1 | (1) |
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2 | (7) |
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The centimetre-gram-second (cgs) system |
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2 | (2) |
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The metre-kilogram-second (mks system) and the Systeme International d'Unites (SI) |
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4 | (1) |
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The foot-pound-second (fps) system |
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5 | (1) |
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The British engineering system |
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5 | (1) |
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Non-coherent system employing pound mass and pound force simultaneously |
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6 | (1) |
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6 | (1) |
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7 | (1) |
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8 | (1) |
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8 | (1) |
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9 | (3) |
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12 | (3) |
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15 | (5) |
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Redefinition of the length and mass dimensions |
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20 | (2) |
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Vector and scalar quantities |
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20 | (1) |
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Quantity mass and inertia mass |
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21 | (1) |
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22 | (1) |
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22 | (1) |
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22 | (3) |
| Part 1 Fluid Flow |
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25 | (354) |
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Flow of Fluids---Energy and Momentum Relationships |
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27 | (31) |
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27 | (1) |
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27 | (3) |
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30 | (9) |
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The incompressible fluid (liquid) |
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31 | (1) |
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31 | (3) |
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34 | (5) |
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39 | (9) |
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39 | (2) |
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Momentum changes in a fluid |
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41 | (3) |
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Energy of a fluid in motion |
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44 | (2) |
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46 | (1) |
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Constant flow per unit area |
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47 | (1) |
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47 | (1) |
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Pressure-volume relationships |
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48 | (2) |
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48 | (1) |
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48 | (2) |
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Rotational or vortex motion in a fluid |
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50 | (5) |
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52 | (2) |
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54 | (1) |
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55 | (1) |
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56 | (1) |
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56 | (2) |
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Flow of Liquids in Pipes and Open Channels |
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58 | (85) |
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58 | (1) |
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59 | (3) |
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60 | (1) |
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61 | (1) |
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62 | (41) |
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Shearing characteristics of a Newtonian fluid |
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62 | (1) |
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Pressure drop for flow of Newtonian liquids through a pipe |
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63 | (11) |
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Reynolds number and shear stress |
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74 | (1) |
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Velocity distributions and volumetric flowrates for streamline flow |
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75 | (7) |
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The transition from laminar to turbulent flow in a pipe |
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82 | (1) |
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Velocity distributions and volumetric flowrates for turbulent flow |
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83 | (4) |
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Flow through curved pipes |
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87 | (1) |
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Miscellaneous friction losses |
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87 | (6) |
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93 | (1) |
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94 | (9) |
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103 | (35) |
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Steady-state shear-dependent behaviour |
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105 | (8) |
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113 | (1) |
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114 | (4) |
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Characterisation of non-Newtonian fluids |
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118 | (2) |
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Dimensionless characterisation of viscoelastic flows |
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120 | (1) |
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Relation between rheology and structure of material |
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120 | (1) |
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Streamline flow in pipes and channels of regular geometry |
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121 | (15) |
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136 | (2) |
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The transition from laminar to turbulent flow |
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138 | (1) |
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138 | (1) |
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139 | (1) |
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140 | (3) |
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Flow of Compressible Fluids |
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143 | (38) |
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143 | (1) |
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Flow of gas through a nozzle or orifice |
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143 | (9) |
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144 | (3) |
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147 | (5) |
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Velocity of propagation of a pressure wave |
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152 | (2) |
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Converging-diverging nozzles for gas flow |
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154 | (4) |
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Maximum flow and critical pressure ratio |
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154 | (2) |
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The pressure and area for flow |
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156 | (2) |
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Effect of back-pressure on flow in nozzle |
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158 | (1) |
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158 | (16) |
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Energy balance for flow of ideal gas |
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159 | (1) |
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Isothermal flow of an ideal gas in a horizontal pipe |
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160 | (9) |
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Non-isothermal flow of an ideal gas in a horizontal pipe |
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169 | (1) |
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Adiabatic flow of an ideal gas in a horizontal pipe |
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170 | (4) |
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174 | (1) |
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174 | (4) |
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178 | (1) |
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179 | (1) |
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179 | (2) |
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Flow of Multiphase Mixtures |
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181 | (51) |
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181 | (1) |
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Two-phase gas (vapour)-liquid flow |
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182 | (13) |
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182 | (1) |
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Flow regimes and flow patterns |
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183 | (3) |
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186 | (1) |
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Pressure, momentum, and energy relations |
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187 | (7) |
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194 | (1) |
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Flow of solids-liquid mixtures |
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195 | (18) |
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195 | (1) |
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Homogeneous non-settling suspensions |
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196 | (2) |
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198 | (1) |
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Coarse solids in horizontal flow |
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198 | (12) |
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Coarse solids in vertical flow |
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210 | (3) |
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Flow of gas-solids mixtures |
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213 | (13) |
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213 | (1) |
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214 | (9) |
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223 | (1) |
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224 | (2) |
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226 | (1) |
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227 | (2) |
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229 | (3) |
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Flow and Pressure Measurement |
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232 | (42) |
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232 | (1) |
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233 | (10) |
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233 | (1) |
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Pressure measuring devices |
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234 | (3) |
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Pressure signal transmission--the differential pressure cell |
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237 | (3) |
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Intelligent pressure transmitters |
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240 | (2) |
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242 | (1) |
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Measurement of fluid flow |
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243 | (29) |
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244 | (1) |
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Measurement by flow through a constriction |
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245 | (3) |
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248 | (6) |
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254 | (1) |
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255 | (1) |
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Pressure recovery in orifice-type meters |
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256 | (1) |
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Variable area meters---rotameters |
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257 | (4) |
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261 | (3) |
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Other methods of measuring flowrates |
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264 | (8) |
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272 | (1) |
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272 | (1) |
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272 | (2) |
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274 | (40) |
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Introduction---types of mixing |
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274 | (3) |
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Single-phase liquid mixing |
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274 | (1) |
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Mixing of immiscible liquids |
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274 | (1) |
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275 | (1) |
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275 | (1) |
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Gas--liquid--solids mixing |
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275 | (1) |
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275 | (1) |
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Miscellaneous mixing applications |
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276 | (1) |
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277 | (3) |
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277 | (2) |
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279 | (1) |
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Scale-up of stirred vessels |
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280 | (2) |
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Power consumption in stirred vessels |
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282 | (12) |
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282 | (6) |
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288 | (6) |
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Flow patterns in stirred tanks |
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294 | (4) |
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298 | (3) |
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301 | (9) |
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301 | (5) |
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306 | (1) |
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306 | (1) |
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307 | (3) |
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310 | (1) |
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Mixing in continuous systems |
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310 | (1) |
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311 | (1) |
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311 | (1) |
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312 | (2) |
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314 | (65) |
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314 | (1) |
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Pumping equipment for liquids |
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315 | (29) |
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316 | (5) |
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Positive-displacement rotary pumps |
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321 | (8) |
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329 | (15) |
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Pumping equipment for gases |
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344 | (14) |
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Fans and rotary compressors |
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344 | (2) |
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Centrifugal and turbocompressors |
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346 | (1) |
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The reciprocating piston compressor |
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347 | (1) |
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Power required for the compression of gases |
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347 | (11) |
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The use of compressed air for pumping |
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358 | (6) |
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358 | (6) |
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364 | (3) |
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Power requirements for pumping through pipelines |
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367 | (9) |
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368 | (6) |
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374 | (2) |
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376 | (1) |
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376 | (1) |
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377 | (2) |
| Part 2 Heat Transfer |
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379 | (192) |
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381 | (190) |
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381 | (1) |
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381 | (6) |
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Individual and overall coefficients of heat transfer |
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381 | (3) |
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Mean temperature difference |
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384 | (3) |
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Heat transfer by conduction |
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387 | (27) |
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Conduction through a plane wall |
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387 | (3) |
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Thermal resistances in series |
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390 | (2) |
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Conduction through a thick-walled tube |
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392 | (1) |
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Conduction through a spherical shell and to a particle |
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392 | (2) |
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Unsteady state conduction |
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394 | (18) |
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Conduction with internal heat source |
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412 | (2) |
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Heat transfer by convection |
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414 | (24) |
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Natural and forced convection |
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414 | (1) |
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Application of dimensional analysis to convection |
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415 | (2) |
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Forced convection in tubes |
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417 | (9) |
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Forced convection outside tubes |
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426 | (7) |
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Flow in non-circular sections |
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433 | (1) |
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Convection to spherical particles |
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434 | (1) |
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435 | (3) |
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Heat transfer by radiation |
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438 | (33) |
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438 | (1) |
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Radiation from a black body |
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439 | (2) |
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Radiation from real surfaces |
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441 | (6) |
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Radiation transfer between black surfaces |
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447 | (11) |
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Radiation transfer between grey surfaces |
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458 | (7) |
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465 | (6) |
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Heat transfer in the condensation of vapours |
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471 | (11) |
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Film coefficients for vertical and inclined surfaces |
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471 | (3) |
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Condensation on vertical and horizontal tubes |
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474 | (2) |
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476 | (2) |
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Condensation of mixed vapours |
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478 | (4) |
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482 | (14) |
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482 | (2) |
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484 | (2) |
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Heat transfer coefficients and heat flux |
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486 | (4) |
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Analysis based on bubble characteristics |
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490 | (2) |
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492 | (2) |
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494 | (2) |
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Heat transfer in reaction vessels |
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496 | (7) |
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496 | (3) |
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499 | (2) |
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Time required for heating or cooling |
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501 | (2) |
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Shell and tube heat exchangers |
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503 | (37) |
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503 | (3) |
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506 | (4) |
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Mean temperature difference in multipass exchangers |
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510 | (7) |
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517 | (6) |
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Pressure drop in heat exchangers |
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523 | (3) |
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526 | (8) |
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Heat exchanger performance |
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534 | (1) |
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535 | (5) |
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540 | (15) |
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540 | (8) |
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548 | (2) |
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550 | (1) |
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550 | (3) |
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Scraped-surface heat exchangers |
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553 | (2) |
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555 | (6) |
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Heat losses through lagging |
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555 | (2) |
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Economic thickness of lagging |
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557 | (1) |
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Critical thickness of lagging |
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557 | (4) |
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561 | (1) |
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562 | (4) |
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566 | (5) |
| Part 3 Mass Transfer |
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571 | (90) |
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573 | (88) |
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573 | (2) |
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Diffusion in binary gas mixtures |
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575 | (18) |
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Properties of binary mixtures |
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575 | (1) |
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Equimolecular counterdiffusion |
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576 | (1) |
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Mass transfer through a stationary second component |
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577 | (4) |
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Diffusivities of gases and vapours |
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581 | (5) |
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586 | (1) |
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General case for gas-phase mass transfer |
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587 | (1) |
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588 | (1) |
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589 | (1) |
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Unsteady-state mass transfer |
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590 | (3) |
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Multicomponent gas-phase systems |
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593 | (3) |
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Molar flux in terms of effective diffusivity |
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593 | (1) |
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Maxwell's law of diffusion |
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594 | (2) |
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596 | (3) |
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Liquid phase diffusivities |
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597 | (2) |
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Mass transfer across a phase boundary |
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599 | (27) |
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600 | (2) |
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602 | (12) |
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The film-penetration theory |
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614 | (3) |
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Mass transfer to a sphere in a homogenous fluid |
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617 | (1) |
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Other theories of mass transfer |
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618 | (1) |
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618 | (1) |
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Mass transfer coefficients |
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619 | (2) |
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Countercurrent mass transfer and transfer units |
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621 | (5) |
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Mass transfer and chemical reaction |
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626 | (8) |
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626 | (5) |
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631 | (3) |
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Mass transfer and chemical reaction in a catalyst pellet |
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634 | (12) |
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636 | (2) |
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638 | (4) |
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642 | (2) |
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Mass transfer and chemical reaction with a mass transfer resistance external to the pellet |
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644 | (2) |
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Practical studies of mass transfer |
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646 | (8) |
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The j-factor of Chilton and Colburn for flow in tubes |
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646 | (3) |
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Mass transfer at plane surfaces |
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649 | (2) |
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Effect of surface roughness and form drag |
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651 | (1) |
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Mass transfer from a fluid to the surface of particles |
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651 | (3) |
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654 | (1) |
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655 | (1) |
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656 | (5) |
| Part 4 Momentum, Heat and Mass Transfer |
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661 | (128) |
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663 | (31) |
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663 | (5) |
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668 | (2) |
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The streamline portion of the boundary layer |
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670 | (5) |
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The turbulent boundary layer |
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675 | (6) |
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675 | (2) |
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677 | (4) |
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Boundary layer theory applied to pipe flow |
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681 | (4) |
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681 | (1) |
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Application of the boundary-layer theory |
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682 | (3) |
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The boundary layer for heat transfer |
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685 | (6) |
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685 | (1) |
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685 | (2) |
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Heat transfer for streamline flow over a plane surface---constant surface temperature |
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687 | (3) |
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Heat transfer for streamline flow over a plane surface---constant surface heat flux |
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690 | (1) |
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The boundary layer for mass transfer |
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691 | (1) |
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692 | (1) |
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692 | (1) |
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692 | (2) |
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Momentum, Heat, and Mass Transfer |
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694 | (44) |
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694 | (2) |
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Transfer by molecular diffusion |
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696 | (4) |
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696 | (1) |
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696 | (1) |
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696 | (1) |
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697 | (1) |
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698 | (1) |
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699 | (1) |
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700 | (6) |
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The nature of turbulent flow |
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701 | (1) |
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Mixing length and eddy kinematic viscosity |
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702 | (4) |
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Universal velocity profile |
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706 | (7) |
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706 | (1) |
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707 | (1) |
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707 | (1) |
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Velocity profile for all regions |
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708 | (1) |
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708 | (1) |
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Laminar sub-layer and buffer layer thicknesses |
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709 | (1) |
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Variation of eddy kinematic viscosity |
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710 | (1) |
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Approximate form of velocity profile in turbulent region |
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711 | (1) |
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Effect of curvature of pipe wall on shear stress |
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712 | (1) |
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Friction factor for a smooth pipe |
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713 | (2) |
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Effect of surface roughness on shear stress |
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715 | (2) |
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Simultaneous momentum, heat and mass transfer |
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717 | (3) |
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720 | (15) |
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Simple form of analogy between momentum, heat and mass transfer |
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720 | (3) |
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Mass transfer with bulk flow |
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723 | (2) |
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Taylor-Prandtl modification of Reynolds analogy for heat transfer and mass transfer |
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725 | (2) |
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Use of universal velocity profile in Reynolds analogy |
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727 | (2) |
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Flow over a plane surface |
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729 | (2) |
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731 | (4) |
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735 | (1) |
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735 | (1) |
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735 | (3) |
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Humidification and Water Cooling |
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|
738 | (51) |
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738 | (1) |
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739 | (7) |
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739 | (3) |
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742 | (1) |
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Adiabatic saturation temperature |
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|
743 | (3) |
|
Humidity data for the air--water system |
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|
746 | (10) |
|
Temperature-humidity chart |
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749 | (2) |
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751 | (5) |
|
Determination of humidity |
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|
756 | (3) |
|
Humidification and dehumidification |
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|
759 | (3) |
|
Methods of increasing humidity |
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|
759 | (2) |
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761 | (1) |
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762 | (17) |
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762 | (3) |
|
Design of natural-draught towers |
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|
765 | (2) |
|
Height of packing for both natural and mechanical draught towers |
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|
767 | (5) |
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|
|
772 | (1) |
|
Temperature and humidity gradients in a water cooling tower |
|
|
773 | (1) |
|
Evaluation of heat and mass transfer coefficients |
|
|
774 | (4) |
|
|
|
778 | (1) |
|
Systems other than air-water |
|
|
779 | (6) |
|
|
|
785 | (1) |
|
|
|
786 | (1) |
|
|
|
787 | (2) |
| Appendix |
|
789 | (36) |
|
A1. Tables of physical properties |
|
|
790 | (16) |
|
|
|
806 | (9) |
|
A3. Mathematical tables Fold-out charts |
|
|
815 | (10) |
| Problems |
|
825 | (44) |
| Index |
|
869 | |