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Chemical Engineering Thermodynamics

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

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

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Chemical Engineering Thermodynamics
1m³ of an ideal gas at 500 K and 1000 kPa expands reversibly to 5 times its initial volume in an insulated container. If the specific heat capacity (at constant pressure) of the gas is 21 J/mole . K, the final temperature will be

174 K
274 K
154 K
35 K

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Chemical Engineering Thermodynamics
The ammonia synthesis reaction represented by N₂ + 3H₂ ⇋ 2NH₃ ; ΔH = - 22.4 kcal, is

Exothermic
Isothermal
Adiabatic
Endothermic

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Chemical Engineering Thermodynamics
At constant temperature and pressure, for one mole of a pure substance, the ratio of the free energy to the chemical potential is

Zero
One
Infinity
Negative

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Chemical Engineering Thermodynamics
For an ideal solution, the value of activity co-efficient is

> 1
1
< 1

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

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

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