Page 165 - Process simulation and control using Aspen
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152 PROCKSS SIMULATION AND CONTROL USING ASPEN
As the distillation tower descibed in the problem statement, it is appropriate to
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choose CDUIOF PetroFrac model. Then place it in the flowsheet window. Adding all
incoming and outgoing streams and renaming the streams as well as block, the process
flow diagram takes the shape as shown in Figure 3.65.
L'Mi- 111" A KM* 1W mm m 31* 1Mb -jM«.
FIGURE 3.65
Configuring settings
Click Next to continue the simulation (see Figure 3.66). In the Title field, enter
'
Simulation of a Petroleum Refining Column'. Open the Accounting sheet keeping
untouched the other global defaults set by Aspen Plus.
t.
r
k - . <i.i-?-ir-Q-ii'-i?--i i.-r
<UbM . »»No M - -o- Ut- W» W.
FIGURE 3.66
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