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Chemical Engineering Thermodynamics

Chemical Engineering Thermodynamics
The difference between isothermal compressibility and adiabatic compressibility for an ideal gas is

+ve
∞
-ve

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

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Chemical Engineering Thermodynamics
During a reversible isothermal expansion of an ideal gas, the entropy change is

+ve
-ve
∞

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Chemical Engineering Thermodynamics
Critical temperature is defined as the temperature above which a gas will

Never liquify however high the pressure may be
Not liquify (barring exceptions)
Immediately liquify
None of these

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Chemical Engineering Thermodynamics
Heat of reaction is

Dependent on both pressure and temperature
Dependent on pressure only
Dependent on temperature only
Independent of temperature changes

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Chemical Engineering Thermodynamics
Entropy change of mixing two liquid substances depends upon the

Both A and B
Quantity (i.e. number of moles)
Neither A nor B
Molar concentration

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