Solution Manual for Transport Processes and Separation Process Principles Fifth Edition Christie John Geankoplis A. Allen Hersel Daniel Lepek Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.2-1) Eq. (1.3-4) k 353.2 °C 273.15 °C 80.05 80 C = = + = = ° Eq. (1.3-2)    °C 80.0 1/1.8 F 32 F 176°F = = ° ° =  Eq. (1.3-3) °R °F 460 176 460 °R 636°R = + = + = Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.2-2) Eq. (1.3-2)       °C 1 1.8 °F 32 1/1.8 155 32 68.33°C = = =   Eq. (1.3-4) K °C 273.15 68.33 273.15 341.5K = + = + = Eq. (1.3-3) °R °F 460 155 460 615°R = + = + = Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.3-1)           2 2 MW O 32.00, MW N 28.02 MW air 0.21 32.00 0.79 28.02 28.9 kg / kg mol      Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.3-2) 2 2 MW 28.01 32.00 44.01 56.0 kg 2CO O 2CO moles CO 2.00 kg mol 28.01kg/kg mol + = =      2 2 2 moles O 1.00, 1.00 32.00 32.0kg O 2.00 44.0 88.0Kg CO    Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.3-3) Gas g MW g mol mol/sec N 2 20 28.02 0.7138 0.1648 mol/sec O 2 83 32.00 2.5938 0.5990 CO 2 45 44.01 1.0225 0.2362 Total 148 g 4.330/g mol 1.0000 34.2g/g mol 148g Average mol wt 34.2 kg/kg mol 4.3301g mol = = Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.3-4) Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.3-5) Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.4-1) P = 2.4 mm Hg From Appendix A.1 1 atm = 760 mm Hg 3 2.4 mm Hg P 3.16 10 atm 760 mm Hg/atm     1 atm = 33.90 × 12 in. H 2 O (at 4°C) 2 2 in.H O 2.4 P atm 33.90 12 1.285in.H O 760 atm          1 μm = 10 −3 mm 3 2.4 mm P 2, 400 μm Hg 10 mm/ μm    1 atm = 1.01325 × 10 5 Pa 5 2.4 Pa P atm 1.01325 10 320 Pa 760 atm          Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.4-2) V 1 = 65.0 ft 3 , T 1 = 460 + 90 = 550 °R, T 2 = 460 + 65 = 525 °R From Appendix A.1, 1 atm = 14.696 psia p 1 = 29.0 + 14.696 = 43.696 psia, p 2 = 75.0 + 14.696 = 89.696 psia p 1 = 43.696/14.696 = 2.975 atm, p 2 = 89.696/14.696 = 6.104 atm Eq. (1.4-2)     3 1 2 1 2 2.975 p V V 65.0 30.24ft p 6.104    R = 0.7302 ft 3 · atm/lb mol · °R, MW of N 2 = 28.01 Eq. (1.4-1)       n pV/RT 2.975 65.0 / 0.7302 550 0.4815lb mol    Density, r = 0.4815 ( ) 28.01 ( ) / 30.24 = 0.446lb m /ft 3 Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.5-1) Basis: 10 000 kg/a feed Total balance 10 000 = S + W Solids balance 0.38 (10 000) = 0.745 + (0)W 2 W 10000 5135 4865kg H O/d    S 5135kg/d of 74%solution  Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.5-2) Basis: 1000 kg/h “dry” fish cake Solids balance     0.20 W S 0 0.60 1000 W 3000 kg/h wet cake feed    Total balance 2 W S 1000 3000 S 1000 S 2000 kg H O/h      Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.5-3) Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028. (1.5-4) Ancillary material to Geankoplis, et al., Transport Processes and Separation Process Principles, 5/E, ISBN: 9780134181028.