Page 268 - Design and Operation of Heat Exchangers and their Networks
P. 268

3200
                                            3900
                                                   1220
                                                 3040
                                                      520
                                                        120
                                                 112
                                               120
                                            155
                                                      40
                                                        20
                                                   60
                                                 2800
                                               3200
                                            3550
                                                   200
                                                        –
                                                      0
                                                 1020
                                                      120
                                                   520
                                               240
                                                        –
                                            0
                                                   1020
                                                 240
                                            350
                                                      520
                                                        –
                                               0
                                                  780
                                                240
                                   2005), Δt min ¼5K.  (kW)  H c  (°C)  t c  (kW)  H h  (kW)  O  (kW)  I  (kW)  D  –  –  3700  350  200   150  Optimal design of heat exchanger networks  257
                                                      400
                                            350
                                                   500
                                                        –
                                   al.,
                                   et
                                   (Ravagnani  (kW)  ΔH h  150  350  400  2600  200  0  –
                                   H2C2_175R  (kW)
                                   for  ΔH c  0  700  160  1820  700  400  –
                                   table
                                   Problem  (°C)  t h  175  160  125  117  65  45
                                   6.4  t,              –
                                   Table  SN  1  2  3  4  5  6  7
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