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Chemical Engineering Thermodynamics

Chemical Engineering Thermodynamics
dW and dq are not the exact differential, because q and W are

Intensive properties
Extensive properties
Path functions
State functions

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Chemical Engineering Thermodynamics
"The fugacity of a gas in a mixture is equal to the product of its mole fraction and its fugacity in the pure state at the total pressure of the mixture". This is

The statement as per Gibbs-Helmholtz
Called Lewis-Randall rule
Henry's law
None of these

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Chemical Engineering Thermodynamics
Sublimation temperature of dry ice (solid CO₂) is __________ °C.

-273
-78
5
0

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Chemical Engineering Thermodynamics
The expression for entropy change given by, ΔS = nR ln (V₂/V₁) + nCv ln (T₂/T₁) is valid for

Cooling of a substance
Reversible isothermal volume change
Simultaneous heating and expansion of an ideal gas
Heating of a substance

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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
0.5 RT
2 RT
-2 RT ln 0.5

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Chemical Engineering Thermodynamics
For a multicomponent system, the term chemical potential is equivalent to the

Partial molar free energy
Molar free energy change
Molar free energy
Molal concentration difference

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