
- •Vapor mole fraction 0.0000 0.0000 0.0000 0.1137
- •Visc n-s/m2 1.026e-005
- •Visc n-s/m2 0.002530 0.001115 0.001648 0.0003499
- •Vapor mole fraction 0.3340 1.000 0.0000
- •Visc n-s/m2 1.019e-005 9.971e-006
- •Visc n-s/m2 0.0003460 0.0002928
- •Vapor mass frac. 0.00000 0.00000 0.00000 0.066746
- •Vapor mass frac. 0.21030 1.0000 0.00000
- •Input Output Input Output
- •Input Output
- •Vapor mole fraction 0.0000 0.0000 0.0000 0.1137
- •Visc n-s/m2 1.026e-005
- •Visc n-s/m2 0.002530 0.001115 0.001648 0.0003499
- •Vapor mole fraction 0.3340 1.000 0.0000
- •Visc n-s/m2 1.019e-005 9.971e-006
- •Visc n-s/m2 0.0003460 0.0002928
- •Vapor mass frac. 0.00000 0.00000 0.00000 0.066746
- •Vapor mass frac. 0.21030 1.0000 0.00000
Vapor mole fraction 0.3340 1.000 0.0000
Enth MJ/h -66582. -53813. -8354.7
Tc C 314.7275 314.5653 316.2905
Pc bar 85.2486 85.2405 85.7908
Std. sp gr. wtr = 1 0.907 0.900 0.971
Std. sp gr. air = 1 2.305 2.384 1.767
Degree API 24.5614 25.6882 14.2008
Average mol wt 66.7566 69.0421 51.1794
Actual dens kg/m3 6.7032 4.3112 851.6128
Actual vol m3/h 1720.0601 2412.0883 1.3280
Std liq m3/h 12.7165 11.5519 1.1646
Std vap 0 C m3/h 3871.1899 3375.8851 495.3037
- - Vapor only - -
Molar flow kmol/h 57.6960 150.6174
Mass flow kg/h 2424.7478 10398.9391
Average mol wt 42.0263 69.0421
Actual dens kg/m3 1.4188 4.3112
Actual vol m3/h 1708.9939 2412.0883
Std liq m3/h 2.6286 11.5519
Std vap 0 C m3/h 1293.1771 3375.8851
Cp kJ/kg-K 1.6574 1.7211
Z factor 0.9843 0.9610
Visc n-s/m2 1.019e-005 9.971e-006
Th cond W/m-K 0.0189 0.0209
- - Liquid only - -
Molar flow kmol/h 115.0198 22.0983
Mass flow kg/h 9105.1723 1130.9782
Average mol wt 79.1618 51.1794
Actual dens kg/m3 822.7966 851.6128
Actual vol m3/h 11.0661 1.3280
Std liq m3/h 10.0878 1.1646
Std vap 0 C m3/h 2578.0131 495.3037
Cp kJ/kg-K 2.3175 2.7661
Z factor 0.0038 0.0049
Visc n-s/m2 0.0003460 0.0002928
Th cond W/m-K 0.1321 0.1442
Surf. tens. N/m 0.0196 0.0171
CHEMCAD 6.3.1 Page 18
Simulation: Lab 4 Date: 11/16/2012 Time: 16:36:22
FLOW SUMMARIES:
Stream No. 1 2 3 4
Stream Name
Temp C 25.0000* 25.0000* 24.9999 87.4631
Pres bar 1.0000* 1.0000* 1.0000 1.0000
Enth MJ/h -26931. -41252. -68183. -68183.
Vapor mass frac. 0.00000 0.00000 0.00000 0.066746
Total kmol/h 82.2956 90.4201 172.7158 172.7158
Total kg/h 6100.0000 5430.0000 11530.0000 11529.9203
Total std L m3/h 7.4800 5.1506 12.6306 12.7165
Total std V m3/h 1844.55 2026.64 3871.19 3871.19
Flowrates in kg/h
N-Butanol 6100.0000 0.0000 6100.0000 98.1202
Acetic Acid 0.0000 5430.0000 5430.0000 814.5000
Water 0.0000 0.0000 0.0000 1421.6446
N-Butyl Acetate 0.0000 0.0000 0.0000 8927.7220
Dibutyl Ether (t 0.0000 0.0000 0.0000 267.9340
Stream No. 5 6 7
Stream Name
Temp C 90.0000 127.9078 128.9688
Pres bar 1.0000 2.0000 2.0000
Enth MJ/h -66582. -53813. -8354.7