Table 3. Streams and Cost Data for Case 2a.
stream | Tin/°C | Tout/°C | FCp/kW·°C–1 | h/kW·m–2·°C–1 |
---|---|---|---|---|
H1 | 180 | 75 | 30 | 2 |
H2 | 280 | 120 | 60 | 1 |
H3 | 180 | 75 | 30 | 2 |
H4 | 140 | 40 | 30 | 1 |
H5 | 220 | 120 | 50 | 1 |
H6 | 180 | 55 | 35 | 2 |
H7 | 200 | 60 | 30 | 0.4 |
H8 | 120 | 40 | 100 | 0.5 |
C1 | 40 | 230 | 20 | 1 |
C2 | 100 | 220 | 60 | 1 |
C3 | 40 | 190 | 35 | 2 |
C4 | 50 | 190 | 30 | 2 |
C5 | 50 | 250 | 60 | 2 |
C6 | 90 | 190 | 50 | 1 |
C7 | 160 | 250 | 60 | 3 |
HU | 325 | 325 | 1 | |
CU | 25 | 40 | 2 |
Area cost = 8000 + 500A0.75 $·year–1, A in m2. HU cost = 80 $·kW–1·year–1. CU cost = 10 $·kW–1·year–1.