Chemical Engineering Thermodynamics
An ideal liquid refrigerant should

Both A and B
Have low specific heat
Not have a subatmospheric vapour pressure at the temperature in the refrigerator coils
Not have unduly high vapour pressure at the condenser temperature

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Chemical Engineering Thermodynamics
Gibbs-Duhem equation

Applies only to binary systems
Finds no application in gas-liquid equilibria involved in distillation
States that n₁dμ₁ + n₂dμ₂ + ....njdμj = 0, for a system of definite composition at constant temperature and pressure
None of these

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Chemical Engineering Thermodynamics
Steam undergoes isentropic expansion in a turbine from 5000 kPa and 400°C (entropy = 6.65 kJ/kg K) to 150 kPa) (entropy of saturated liquid = 1.4336 kJ/kg . K, entropy of saturated vapour = 7.2234 kJ/kg. K) The exit condition of steam is

Superheated vapour
Saturated vapour
Partially condensed vapour with quality of 0.1
Partially condensed vapour with quality of 0.9

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