Page 29 - Process simulation and control using Aspen

22 PROCESS SIMULATION AND CONTROL USING ASPEN

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£1 fo. * r " 3 5l<»amT»blf[
r rjj 1 - 3
50 0 2000 200 0
i f. nr i ion oo ion on
Vapo* Froc 0016 0 000 1 000
Mote Flow fcmot/hi 220 462 1 Tf 971 42 492
Mas* Ftow b/h. 15906 41* 13312.698 2593 716
v . l:...- Flow culler 1039 561 382.439 3008 065
lE.Hh»lpy MMBtu/hi 16 583 1243? 2 236
Mole Flow bmolVIv
C3H8 22 046 9 275 12 771
NC4H10 44092 30124 13 969
66139 56 242 9 896
N.C6H14 eeies 82 329 5856
(V Mixw pMto! SoiMralof* { Heal Enchangon | Column* | Re»cto.. \ P-eume Chongeij \ Mo puMw* | So§*. | Um. Models )
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STREAMS ' FVwh2 Flaih3 D>came> 3ep Sep2
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For H*e, press Fi " "" C.\- .g Pol<tou\Ajper. PK» 11,1 ! NUM i - .. . . Av,4,>:-
* Start}} Aspen Pkn - Simulatl_
FIGURE 1.29

If we click on Stream Table button, the results table takes a place in the Process
Flowsheet Window, as shown in Figure 1.30.

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Fie Edt View Data Tocfc Run Fevaheet Librvy Whdow Help
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1

F L V
Temptntuit F 50 0 200 0 200.0
Pttiiun pri 15 00 100 00 100.00
V*poi Fnc 0 .018 0 000 1000
HoUFtow fcrnoVhi 220462 177 971 42 492
fcftu 15906 414 13312 698 2593 716
VokuntFlw 1639 561 382439 3008 065
EnlhJpy MMBtu/hi -16583 -12.499 -2236
Hole Flw
C3H8 22 046 9 275 12 771
-
H-C4H10 44 092 30 124 13569
K-C5H12 66139 56 242 9996
H-C6H14 88 185 82.329 5 856
Mok Trie
C3K8 0 . 100 0053 0 301
HX4HI0 0 .200 0 169 0329
.
H-C5H12 OJOO 0 316 0233
H-C6H14 0 400 0 463 0 138
.
r
Mm/Spitlan Sflpntms { HeatEicchangeit { Cdum | Reactori | PrMtue Chmgeii j Mmpdalai | Soldi j Use. Models j
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C:V.oF<*lefs\A»penMu»n.l
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FIGURE 1.30