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Chemical Engineering Thermodynamics

Chemical Engineering Thermodynamics
The first law of thermodynamics is a restatement of the law of conservation of

Energy
Momentum
None of these
Mass

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Chemical Engineering Thermodynamics
One mole of nitrogen at 8 bar and 600 K is contained in a piston-cylinder arrangement. It is brought to 1 bar isothermally against a resisting pressure of 1 bar. The work done (in Joules) by the gas is

4988.4
4364.9
10373
30554

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Chemical Engineering Thermodynamics
When liquid and vapour phases of one component system are in equilibrium (at a given temperature and pressure), the molar free energy is

More in vapour phase
Same in both the phases
More in liquid phase
Replaced by chemical potential which is more in vapour phase

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Chemical Engineering Thermodynamics
In a homogeneous solution, the activity co-efficient of a component depends upon the

Temperature
Composition
Pressure
All of these

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Chemical Engineering Thermodynamics
Co-efficient of performance for a reversed Carnot cycle working between temperatures T₁ and T₂ (T₁ > T₂) is

(T₁ - T₂)/T₁
T₁/(T₁ - T₂)
(T₁ - T₂)/T₂
T₂/(T₁ - T₂)

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

Extensive properties
State functions
Intensive properties
Path functions

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