Page 109 - Applied Process Design For Chemical And Petrochemical Plants Volume II

98 Applied Process Design for Chemical and Petrochemical Plants

STAGE NU. a (XELIOILER ----- LIQUID STXEAM IS BOTTOAS PRODUCT)
TEBPERATURE = 224.68 DEL P
PRESSURE = 0.86 PSIA

INTEaYAL STREABS LEAVING STAGI(
0.45098OE-08 0.20UA98E-06 0-5109833+02 0.00000 O.OO@ 0~00002 0.002
0.2991 933-05 0.6601 95E-04 0.220665E+02 0.03053 0.001 0.00805 0.145
0.324473E-03 0.393227E-02 0.121192E+02 0.00331 0.306 0.47541 44.360
9.9084193-02 0.477594E-01 0.5257623+01 0.09269 h. fi66 5.82269 43 1.344
0.9 j9133E+OO 0.934957E+00 O.P95584E+00 5.58198 1381.033 113.98735 16433.555
0,514552E-01 0.1327581-01 0.25009.3Et00 0.52500 b5.370 1.61904 263.27.1
1.000000 0.999995 10.20300 1473.976 121.91722 17172.676
ENTHALPY, BTU/UNIT PLOY = 15248.2773 105.550 35206.3750 2U9.9U7

REBOILER HEAT DUTY = 2573009.0 BTU
CONDENSER dEAT DUTY= 2499393.0 BTU

OVERALL COHPONENT BALANCES (MOLS) ---- BEPOfE FINAL POBCING ----

IN OUT Iii/OUT

0.62300 0.62300 1.00000000
7.23400 7.23400 1.00000000
80.22301 80.22293 1.00000000
1.71700 1.71700 1.00000000
9.67800 9.67804 0.99999583
0.52500 0.52500 0.99999529
99.99998 99.99995 1.00000000

NOBHALIZED PRODUCT STBEANS ---- AFTER COMPONENT BALANCES FOaCEJ ----

STAGE NO. 1 ...... OVERXEAD CONDENSER
TEHPEBATURP = 81.75 DEG-F
PRESSURE = 0.39 PSIA

COHPOMENT
0.62300 0.693787E-02 53.684 0.653506E-02 0.0 0-0 0.0 0.0
7.23397 0.80559 1 E- 0 1 130.356 0.168398E-01 0.0 0.0 0.0 0.0
80.21964 0.8933453+00 7422.723 0.958892E+00 0.0 0.0 0.0 0.0
0.0
120.329 0.155445E-01
1.62431 0.180887E-01
0.09606 3.10698OE-02 13.850 0.17891UE-02 0.0 0.0 0.0 0.0
0.0
0.0
0.0
0.000'51 0.6083073-07 0.001 0.114746E-06 0.0 0.0 0.0 0.0
89.79697 7740.937 0.0 0.0
STAGE NO. 6 (RZBOILER)
TEHPERATOBE = 224.68 DEG.
PRESSURE = 0.86 PSIA

C OH POI ENT
1 0 00000 0 4009893-08 0.000 0.239 18 1 E- 08 0.0 0.0 0-0 0.0
2 0: 00003 0: 299 19 1 E-35 0.00 1 0.3732 00E-06 0.0 0.0 0.0 0.0
iz :N 3.00331 0.324474E-03 6.866 0.465829Y-02 0.0 0.0 0.0 9.0
0.0
0.306 3.207826E- 03
0.09269 0.908423E-02
0.0
0.0
0.0
5 9.58194 0.939133E+00 1381.427 0.937216E+00 0.0 0.0 0.0 0-0
6 3.52493 0.514551E-01 85.363 0,579180E-01 0.0 0.0 0.0 0.0
10.20296 1473.969 0.0 0.0