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Chemical Engineering Thermodynamics

Chemical Engineering Thermodynamics
The partial molar enthalpy of a component in an ideal binary gas mixture of composition Z, at a temperature T and pressure P, is a function only of

T
T and P
T, P and Z
T and Z

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Chemical Engineering Thermodynamics
An ideal liquid refrigerant should

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

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Chemical Engineering Thermodynamics
The equation Tds = dE - PdV applies to

Single phase fluid of constant composition
Both B and C
Single phase fluid of varying composition
Open as well as closed systems

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Chemical Engineering Thermodynamics
Fugacity is a measure of the

Escaping tendencies of the same substance in different phases of a system
Behaviour of ideal gases
Relative volatility of a mixture of two miscible liquids
None of these

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Chemical Engineering Thermodynamics
The theoretical minimum work required to separate one mole of a liquid mixture at 1 atm, containing 50 mole % each of n- heptane and n- octane into pure compounds each at 1 atm is

-RT ln 0.5
2 RT
-2 RT ln 0.5
0.5 RT

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Chemical Engineering Thermodynamics
Equation which relates pressure, volume and temperature of a gas is called the

None of these
Gibbs Duhem equation
Ideal gas equation
Equation of state

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MORE MCQ ON Chemical Engineering Thermodynamics

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