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Chemical Engineering Thermodynamics

Chemical Engineering Thermodynamics
During Joule-Thomson expansion of gases

Temperature remains constant
Entropy remains constant
Enthalpy remains constant
None of these

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Chemical Engineering Thermodynamics
Air enters an adiabatic compressor at 300K. The exit temperature for a compression ratio of 3, assuming air to be an ideal gas (Y = Cp/Cv = 7/5) and the process to be reversible, is

300(35/7)
300(33/7)
300(33/5)
300(32/7)

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Chemical Engineering Thermodynamics
For water at 300°C, it has a vapour pressure 8592.7 kPa and fugacity 6738.9 kPa Under these conditions, one mole of water in liquid phase has a volume of 25.28 cm³ and that in vapour phase in 391.1 cm³.Fugacity of water (in kPa) at 9000 kPa will be

7058.3
9000
6738.9
6753.5

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Chemical Engineering Thermodynamics
At absolute zero temperature, all substances have the same

Heat capacity
None of these
Crystalline structure
Entropy

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Chemical Engineering Thermodynamics
The accentric factor of a materical, 'ω', is defined as ω = -log10(Prsat)Tr⁻¹ = 0.7, where, Prsat = reduced vapor pressure, Tr = reduced temperature. The value of accentric factor is always

< 3
< 1
> 2
> 1

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Chemical Engineering Thermodynamics
The root mean square speed of molecules of a gas is equal to (where, m = mass of the molecule K = Boltzman's constant, T = absolute temperature)

√(6KT/m)
√(2KT/m)
3KT/m
√(3KT/m)

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