Page 107 - Applied Process Design For Chemical And Petrochemical Plants Volume II

96 Applied Process Design for Chemical and Petrochemical Plants

PRODUCT ST BEAUS
OVERHEAD RATE = 89.797 ll0L.S LI UID
0.0 ioLs VABoa
BOILTOMS BATE = 10.203 MOLS LIQUID
SUH OF PRODUCTS = 100.300 MOLS

1 85.00 0.39 44.898 0.0 0.0
2 102.86 0.46 44,898 134.695 0.0
3 120.71 0.52 44.898 134.695 0.0
4 138.57 0.59 44.898 134.695 0-0
5 156.43 0.66 144.898 134.695 0.0
6 174.29 0.73 144.898 134.695 0.0
7 192.14 0.79 144.898 134.695 0.0
8 210.00 0.86 10.203 134.695 0.0
STAGE NO. 1 ...*-I OVERHEAD CONDESSES.
TEMPERATURE = 81.75 DEG-F
PBESSURE = 0.39 PSIA

3.693787E-02 0.579909E-(31 0.8356649+01 0.62300 53.68U 0.0 0.0
0.8055913-01 0.111028E+00 O.l37623E+Ol 7.23397 130.356 0.0 0.0
0.893344E+00 0.829924E+OO 0.929G18E+00 d0.21964 7422.723 0.0 0.0
0.180887E-01 0.10167OE-02 0.562068E-01 1.62431 120.329 0.0 0.0
0.106980E-02 3.384860E-04 0.359752E-01 0.09607 13.850 0.0 0.0
0.608310E-07 0.566475E-09 0.9312352-02 0.00001 0.001 0.0 0.0
1.003030 0.999998 89.79700 7740.937 0.0 0.0
EBTAALPY, BTU/'JNIT Pi03 = 2318.02881 26.890 20467,7891 24 4.03 7
CONDENSEE !!EAT JUTY = 2499393.0 LIT3
----- ( E = 0,530000 )
LI UID REFLUX------
---
--- 81.55 I3EG.F.----
NOLs----
___- LBS----
1 N-SEXANE 0.31150 26.842
2 WATER 3.61698 65.178
3 EPICHLOROBY DRIH 40.10982 371 1,361
4 GLYCIDOL 0.81216 60.165
5 GIA 0.04803 6.925
6 ?ICY 0.00000 0.030
44.89850 3670.471
ENTHALPY, BTU/UNIT PLCh = 2318.02881 26.890

INTERNAL STREAMS LEAVING STAGE
0 702365E-03 0 693785--02 0.9877763+01 0.03330 2.611 0.93450 80.525
0: 4388 18E-01 0' 805594;-0 1 0.183580E+0 1 1.89314 34.114 10.85099 195-53 5
0 738175"+00 O:d93351E+OO 0.121019E+Ol 31.84622 2946.731 120.33041 11134.172
O:,I96167~+00 C 180890E-01 0 922004F-01 8.46386 627.003 2,43651 180.496
0. L 1 04 94E-0 1 0: 10698 1 E-02 0: 508 22 Si- 0 1 0.90811 130.922 0.14410 20.775
0 462302E-05 0.6083163-07 0.131582E-01 0.00020 0.032 0.00001 0.001
1: ooocoi) 1.000007 43.14185 37111,413 334,69550 116i1.500
ENTHALPY, BTU/UNIT PLOW = 2358-33 154 34,112 20873.9062 242.14 1

STAGE TEHPERATURE = 115.04 DEG. P
PRESSURE = 0.52 PSIA

0.3 7 9 42 1 E- 0 3 0.4 9 1 4 2 7E- 0 2 0.12 9 5 1 9 E + 0 2 0.01563 1.347 0.65330 56,295
O.ZU5430E-01 0.686564E-01 0-2797353+01 1.01098 18.21~ 9-12711 164-47 1
0.470701E+00 0.842987E+OO 0.179083E+01 19.38924 1794.086 112.06575 10369.441
0.414043E+00 0.7588733-01 0.183279I?+OO 17.05534 1263.460 10.08837 747.346
0.9026253-01
0.00020
0.476
0.15U139E-05
0.033
0.711249E-04 0.7553773-02 0.836849E-01 3.7 18 12 536-04 1 1.00419 144.774
0.216712E-01
0.00293
1.000000 1.000000 41.19226 3613.627 132,93881 11482.352
ENTHALPY, BTU/UUIT FLOW = 4063.29980 46,318 21326,8906 296.916