Industrial Fluid Properties
IFPSC
Simulation Collective
 

Fluid Properties Simulation Challenge Problem Sets


The chemical names are linked to information defining that chemical.


Problem Set 1. Vapor Liquid Equilibria

Part a) Determine the Px curve for a mixture of dimethyl ether and propylene at -20 °C (253.15 K)with explicit pressures for x=0, 0.2, 0.4, 0.6, 0.8, 1.0 and the pressure at 20 °C (293.15 K) for x=0.5

Part b) Determine the pressure and composition of the azeotropic point for a mixture of nitroethane and propylene glycol monomethyl ether at 80 °C (353.15 K)and at 40 °C (313.15 K), and the bubble point pressure for x=0.2 (nitroethane) and x=0.5

Problem Set 2. Prediction of density

The task is to determine the density of the following fluids at the specified conditions. Benchmarks are provided for part a, water.

part # system State Point 1 State Point 2
a water 0.1 MPa, 293 K (998.24 kg/m3) 2.0 MPa, 423 K (918.01 kg/m3)
b Cyclohexane 0.1 MPa, 300 K 20 MPa, 400 K
c Isopropanol 0.1 MPa, 298.15 K 5 MPa, 400 K
d Diethanol amine 0.1 MPa, 330 K 5 MPa, 400 K
e 1,2,3-trichloropropane 0.1 MPa, 290 K 1.5 MPa, 400 K
f Triethylene glycol 0.1 MPa, 310 K 2 MPa, 280 K
g Pyridine 0.1 MPa, 298 K 10 MPa, 375 K
h Water + choline chloride (Aqueous choline chloride) 0.1 MPa, 298 K, 20% choline Cl by weight 1 MPa, 305 K, 10% choline Cl by weight
i Water + methanol (50:50 by mass fraction) 0.1 MPa, 325 K 10 MPa, 400 K

 

Problem Set 3. Prediction of Viscosity

The task is to determine the shear viscosity of the following fluids at the specified conditions.

part # system State Point 1
a N-nonane 0.1 MPa, 300 K
b Isopropanol 0.1 MPa, 300 K
c N-nonane + Isopropanol (0.5 mole fraction) 0.1 MPa, 300 K
d N-nonane + Isopropanol (0.75 mole fraction isopropanol) 0.1 MPa, 300 K