As an assignment,


1) Repeat this simulation with different compounds and thermodynamics

Compounds:

Cold Stream: Toluene
Hot Stream: Styrene

Property Package: UNIFAC

2) Repeat this simulation with different feed conditions 

Cold Inlet Stream:

Mass Flow: 50000 kg/h
Mole Fraction(C7H8): 1
Mole Fraction(C8H8): 0
Temperature: 35 degree C 
Pressure: 6.5 bar

Hot Inlet Stream:

Mass Flow: 70000 kg/h
Mole Fraction(C7H8): 0
Mole Fraction(C8H8): 1
Temperature: 150 degree C 
Pressure: 3.5 bar

3) Repeat this simulation with different Heat Exchanger Properties

Flow type: Counter-Current
Cold Fluid Pressure Drop: 0.002 bar
Hot Fluid Pressure Drop: 0.025 bar


4) Repeat this simulation with different Shell & Tube Exchanger Properties

Type of Exchanger: 2-16 Shell & Tube Heat Exchanger
Total number of tubes: 1024
Tube Spacing: 75 mm
Tube Layout: Square
Thermal Conductivity of tube: 70 W/m K
Tube Roughness: 0.045 mm
Fouling Factor (tube side): 0 K m2/W
Tube Length: 5 m
External Diameter for tube: 60 mm
Tube thickness: 5 mm
Fouling Factor (shell side): 0 K m2/W
Shell Internal Diameter: 990.6 mm
Baffle Spacing : 250 mm
Baffle Cut: 25%
Fluid in Shell: Styrene