Chemical Engineering - Chemical Engineering Thermodynamics
Exercise : Chemical Engineering Thermodynamics - Section 10
- Chemical Engineering Thermodynamics - Section 1
- Chemical Engineering Thermodynamics - Section 2
- Chemical Engineering Thermodynamics - Section 3
- Chemical Engineering Thermodynamics - Section 4
- Chemical Engineering Thermodynamics - Section 5
- Chemical Engineering Thermodynamics - Section 6
- Chemical Engineering Thermodynamics - Section 7
- Chemical Engineering Thermodynamics - Section 8
- Chemical Engineering Thermodynamics - Section 9
- Chemical Engineering Thermodynamics - Section 10
- Chemical Engineering Thermodynamics - Section 11
36.
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
37.
For a thermodynamic system containing 'x' chemical species, the maximum number of phases that can co-exist at equilibrium is
38.
A reasonably general expression for vapour-liquid phase equilibrium at low to moderate pressure is Φi yi P = Yi xi fi° where, Φ is a vapor fugacity component, Yi is the liquid activity co-efficient and fi° is the fugacity of the pure component i. the Ki value (Yi = Ki xi) is therefore, in general a function of
39.
Standard temperature and pressure (S.T.P.) is
40.
Normal temperature and pressure (N.T.P.) corresponds to
Quick links
Quantitative Aptitude
Verbal (English)
Reasoning
Programming
Interview
Placement Papers