Vapor mole fraction 1.000 9.914e-005 1.000

Enth MJ/h -27802. -36898. 4221.5

Tc C 182.3337 193.6704 53.1923

Pc bar 59.7316 55.9544 66.4611

Std. sp gr. wtr = 1 0.777 0.790 0.634

Std. sp gr. air = 1 1.452 1.509 0.953

Degree API 50.6709 47.6972 91.5735

Average mol wt 42.0440 43.7075 27.5966

Actual dens kg/m3 3.3750 748.7028 1.3862

Actual vol m3/h 2675.6489 11.2438 441.5150

Std liq m3/h 11.6258 10.6610 0.9648

Std vap 0 C m3/h 4814.0321 4316.9537 497.0762

- - Vapor only - -

Molar flow kmol/h 214.7813 0.0191 22.1774

Mass flow kg/h 9030.2640 0.8245 612.0215

Average mol wt 42.0440 43.1813 27.5966

Actual dens kg/m3 3.3750 2.1534 1.3862

Actual vol m3/h 2675.6489 0.3829 441.5150

Std liq m3/h 11.6258 0.0011 0.9648

Std vap 0 C m3/h 4814.0321 0.4280 497.0762

Cp kJ/kg-K 1.3184 1.2668 1.4954

Z factor 0.9602 0.9715 0.9865

Visc n-s/m2 9.200e-006 8.694e-006 8.148e-006

Th cond W/m-K 0.0139 0.0124 0.0150

- - Liquid only - -

Molar flow kmol/h 192.5847

Mass flow kg/h 8417.4137

Average mol wt 43.7076

Actual dens kg/m3 775.0227

Actual vol m3/h 10.8609

Std liq m3/h 10.6599

Std vap 0 C m3/h 4316.5259

Cp kJ/kg-K 2.5655

Z factor 0.0037

Visc n-s/m2 0.0002163

Th cond W/m-K 0.1817

Surf. tens. N/m 0.0209

CHEMCAD 6.2.0 Page 10

Simulation: Midterm Kenzhegaliyeva E. N Date: 10/17/2012 Time: 06:10:18

FLOW SUMMARIES:

Stream No. 1 2 3 4

Stream Name

Temp C 20.0000* 14.7261 14.7261 1040.1475

Pres bar 4.0000* 2.0000 2.0000 1.8000

Enth MJ/h -3101.6 -7755.6 -7755.6 -8028.1

Vapor mass frac. 0.00000 0.00000 0.00000 1.0000

Total kmol/h 103.6382 422.3827 422.3827 218.3436

Total kg/h 2283.0000 9427.9670 9427.9670 9144.9121

Total std L m3/h 3.1281 13.0442 13.0442 11.7633

Total std V m3/h 2322.91 9467.14 9467.14 4893.88

Flowrates in kg/h

Acetylene 1349.9576 5740.4152 5740.4152 532.7983

Water 933.0422 3603.0115 3603.0115 72.7517

Acetaldehyde 0.0000 84.5396 84.5396 8539.3619

Stream No. 5 7 8

Stream Name

Temp C 38.9700 24.8061 -30.3893

Pres bar 2.0000 1.2000 1.0000

Enth MJ/h -27802. -36898. 4221.5