| Foreword |
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ix | |
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1 | (20) |
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1.1 Procedure in Heat Exchanger Design |
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2 | (10) |
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1.2 Information about Heat Exchangers |
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12 | (9) |
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18 | (1) |
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19 | (2) |
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2 Calculations of the Temperature Differences LMTD and CMTD |
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21 | (16) |
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2.1 Logarithmic Mean Temperature Difference for Ideal Countercurrent Flow |
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21 | (1) |
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2.2 Corrected Temperature Difference for Multipass Heat Exchanger |
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22 | (7) |
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2.3 Influence of Bypass Streams on LMTD |
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29 | (1) |
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2.4 Mean Weighted Temperature Difference |
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30 | (2) |
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2.5 Determination of the Heat Exchanger Outlet Temperatures |
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32 | (5) |
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References and Further Reading |
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35 | (2) |
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3 Calculations of the Heat Transfer Coefficients and Pressure Losses in Convective Heat Transfer |
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37 | (28) |
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3.1 Tube-Side Heat Transfer Coefficient |
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41 | (1) |
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3.2 Shell-Side Heat Transfer Coefficient |
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42 | (7) |
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3.3 Comparison of Different Calculation Models |
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49 | (2) |
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3.4 Pressure Loss in Convective Heat Exchangers |
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51 | (5) |
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3.5 Heat Exchanger Design with Heat Exchanger Tables |
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56 | (9) |
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63 | (1) |
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References and Further Reading |
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63 | (2) |
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4 Geometrical Heat Exchanger Calculations |
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65 | (10) |
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65 | (3) |
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4.2 Tube-Side Calculations |
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68 | (2) |
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4.3 Shell-Side Calculations |
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70 | (5) |
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5 Dimensionless Characterization Number for the Heat Transfer |
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75 | (4) |
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5.1 Reynolds Number Re for the Characterization of the Flow Condition |
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75 | (1) |
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5.2 Prandtl Number Pr, Peclet Number Pe, and Temperature Conductivity a |
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75 | (1) |
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5.3 Nusselt Number Nu for the Calculation of the Heat Transfer Coefficient |
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76 | (1) |
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5.4 Stanton Number St for the Calculation of the Heat Transfer Coefficient |
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76 | (1) |
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5.5 Colburn Factor JC for the Calculation of the Heat Transfer Coefficient |
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77 | (1) |
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5.6 Kern Factor JK for the Calculation of the Heat Transfer Coefficient |
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77 | (1) |
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5.7 Graßhof Number Gr for the Calculation of the Heat Transfer Coefficient in Natural Convection |
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78 | (1) |
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78 | (1) |
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6 Overall Heat Transfer Coefficient and Temperature Profile |
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79 | (12) |
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6.1 Calculation of the Overall Heat Transfer Coefficient |
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79 | (5) |
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6.2 Calculation of the Temperature Gradient in a Heat Exchanger |
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84 | (2) |
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86 | (2) |
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6.4 Calculation of the Heat Transfer Coefficient from the Overall Heat Transfer Coefficient |
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88 | (3) |
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89 | (1) |
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89 | (2) |
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7 Chemical Engineering Calculations |
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91 | (14) |
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7.1 Vapor Pressure Calculations |
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91 | (2) |
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7.2 Equilibrium between the Liquid and the Vapor Phase |
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93 | (1) |
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7.3 Bubble Point Calculation |
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94 | (1) |
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7.4 Dew Point Calculation |
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95 | (1) |
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7.5 Calculation of Dew and Bubble Lines of Ideal Binary Mixtures |
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95 | (2) |
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97 | (2) |
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7.7 Condensation or Flash Curve of Binary Mixtures |
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99 | (2) |
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7.8 Calculation of Nonideal Binary Mixtures |
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101 | (2) |
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7.9 Flash Calculations for Multicomponent Mixtures |
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103 | (2) |
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104 | (1) |
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105 | (42) |
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Construction Types of Condensers |
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106 | (1) |
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8.1 Condenser Construction Types |
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106 | (5) |
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8.2 Heat Transfer Coefficients in Isothermal Condensation |
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111 | (11) |
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8.3 Comparison of Different Calculation Models |
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122 | (3) |
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8.4 Condensation of Vapors with Inert Gas |
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125 | (4) |
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8.5 Condensation of Multicomponent Mixtures |
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129 | (6) |
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135 | (12) |
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145 | (1) |
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145 | (2) |
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147 | (34) |
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148 | (1) |
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9.2 Evaporator Construction Types |
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149 | (9) |
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9.3 Design of Evaporators for Nucleate Boiling |
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158 | (14) |
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9.4 Design of Falling Film Evaporators |
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172 | (9) |
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179 | (2) |
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10 Design of Thermosiphon Reboilers |
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181 | (48) |
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10.1 Thermal Calculations |
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182 | (2) |
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10.2 Calculation of the Heat Transfer Coefficient |
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184 | (7) |
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10.3 Calculation of the Two-Phase Density and the Average Density in the Reboiler |
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191 | (2) |
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10.4 Flow Velocity WReb in the Reboiler |
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193 | (1) |
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10.5 Determination of the Required Height H1 for the Thermosiphon Circulation or the Maximum Allowable Pressure Loss ΔPmax in Thermosiphon Circulation |
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194 | (9) |
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10.6 Design of Riser and Downcomer Diameter |
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203 | (3) |
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10.7 Calculation of the Pressure Losses in the Thermosiphon Circulation |
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206 | (6) |
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10.8 Calculation of the Required Reboiler Length or Area for the Heating up to the Boiling Temperature and for the Evaporation in Vertical Thermosiphon Evaporators |
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212 | (3) |
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10.9 Required Heating Length for Vertical Thermosiphon Reboilers According to Fair |
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215 | (3) |
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10.10 Calculation of the Pressure and Boiling Point Increase by Means of the Liquid Height H1 |
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218 | (3) |
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10.11 Average Overall Heat Transfer Coefficient for Heating + Vaporizing |
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221 | (1) |
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10.12 Calculation of the Vapor Fraction x of the Two-Phase Mixture in a Vertical Reboiler |
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221 | (1) |
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10.13 Thermosiphon Reboiler Design Example |
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222 | (7) |
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226 | (3) |
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11 Double Pipe, Helical Coil, and Cross Flow Heat Exchanger |
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229 | (18) |
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11.1 Double Pipe and Multipipe Heat Exchangers |
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229 | (8) |
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11.2 Helical Coil Heat Exchanger |
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237 | (4) |
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241 | (6) |
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244 | (1) |
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245 | (2) |
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12 Finned Tube Heat Exchangers |
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247 | (18) |
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12.1 Why Finned Tube Heat Exchangers? |
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247 | (2) |
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12.2 What Parameters Influence the Effectiveness of Finned Tubes? |
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249 | (2) |
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12.3 Finned Tube Calculations |
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251 | (8) |
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12.4 Application Examples |
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259 | (6) |
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264 | (1) |
| Index |
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265 | |
