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Basic skill for ASPEN plus Liang Yu Department of Biological Systems Engineering Washington State University 01. 10. 2014
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Introduction Physical relationships Mass and energy balance Equilibrium relationships Rate correlations Predicts Stream flowrates, compositions, and properties Operating conditions Equipment sizes Economical analysis Energy analysis
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Start ASPEN plus
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Case study_Cumene Production Q = 0 Btu/hr Pdrop = 0 psi C6H6 + C3H6 = C9H12 Benzene Propylene Cumene (Isopropylbenzene) 90% Conversion of Propylene P = 1 atm Q = 0 Btu/hr Benzene: 40 lbmol/hr Propylene: 40 lbmol/hr T = 220 F P = 36 psia Use the SRK or RK-SOAVE Property Method Filename: CUMENE.BKP REACTOR FEED RECYCLE REAC-OUT COOL COOL-OUT SEP PRODUCT Goal: understand the basic knowledge of mass balance in the process
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Select template
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Components input_1 US Unit
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Components input_2 Click Next
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Unknown components input_1 Click
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Unknown components input_2
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Unknown components input_3 Click
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Unknown components input_4
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Unknown components input_5
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Unknown components input_6
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Select method_thermodynamics
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Another property method
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Calculate properties
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T vs. mole fraction_ Benzene and Propylene
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Simulation windows
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Select unit models_ RStoic
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Select unit models_ Heater and Flash2
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Click “Material” to link units
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Link the units_1
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Link the units_2
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Rearrange the flowsheet
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Save the case
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FEED input_1
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FEED input_2
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COOL input
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REACTOR input_1
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REACTOR input_2
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REACTOR input_3
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REACTOR input_4
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SEP input Unit
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Run the simulation
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Calculation is completed
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Stream results
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Click
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Stream results
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