Table 1. Streams and Cost Data for Case 1a.
| stream | Tin/°C | Tout/°C | FCp/kW·°C–1 | h/kW·m–2·°C–1 | 
|---|---|---|---|---|
| H1 | 327 | 40 | 100 | 0.5 | 
| H2 | 220 | 160 | 160 | 0.4 | 
| H3 | 220 | 60 | 60 | 0.14 | 
| H4 | 160 | 45 | 400 | 0.3 | 
| C1 | 100 | 300 | 100 | 0.35 | 
| C2 | 35 | 164 | 70 | 0.7 | 
| C3 | 85 | 138 | 350 | 0.5 | 
| C4 | 60 | 170 | 60 | 0.14 | 
| C5 | 140 | 300 | 200 | 0.6 | 
| HU | 330 | 250 | 100 | 0.5 | 
| CU | 15 | 30 | 160 | 0.5 | 
Area cost = 2000 + 70A $·year–1, A in m2. Hot utility (HU) cost = 60 $·kW–1·year–1. Cold utility (CU) cost = 6 $·kW–1·year–1.