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Thermodynamics of Wet, Saturated & Superheated Vapor. P M V Subbarao Professor Mechanical Engineering Department I I T Delhi. Insearch of Simple Pfaffian Substance …. Specific Volume of Wet Mixture. More Properties of Wet Mixture.
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Thermodynamics of Wet, Saturated & Superheated Vapor P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Insearch of Simple Pfaffian Substance …..
Let Y be any extensive property and let y be the corresponding intensive property, Y/m, then
Vapour Dome • Saturated Liquid Line and Saturated vapour line intersect at the critical point and form what is often called the “vapour dome.” Water Critical Point:
Vapour • Temperature of the substance is higher than the saturation temperature at a given pressure. • Pressure of the substance is lower than the saturation pressure at a given temperature. • Molecules of substance move in random paths. • Weak inter-molecular forces. • Occupy entire volume of the container : No free surface. • Very low density • Highly compressible.
p-v-T Relations for Vapour Phase • At high Temperature and low pressure pv is constant at a given temperature. • This nature is called Ideal gas behaviour of gases. T1 T2
Behaviour of Vapour • = interatomic potential, Joules. • r = separation of molecules, nm (mean Free path). • r = equivalent “hard sphere” radius of molecule (overlap of electron clouds). • At high T, high p, collisions in the repulsive part of – positive deviations from constancy. • At low T, moderate p, collisions in the attractive portion of – negative deviations from constancy.
The specific volume of A vapour: • v = f (p,T) P – v- T Relation • Greatest need for EoS of saturated and superheated steam. • R and a are constants. • The is called as Rankine’s Equation of state, 1849.
The specific volume of A vapour: • v = f (p,T) P – v- T Relation • Callender’s Characteristic Equation for saturated and superheated vapours. • R and b are constants. • c is a function of temperature and itis called as co-aggregation volume.
Van der Waals EOS • One of the oldest but most extensively used of the EOS of non ideal gases • Any EOS model must reproduce graphs such as that of the previous • a, b are the Van der Waals constants for the particular gas; • for water: a = 0.5658 J-m3/mole2; b = 3.049x10-5m3/mole,
JO H A N N E S D . V A N D E R W A A L SThe equation of state for gases and liquidsNobel Lecture, December 12, 1910 I intend to discuss in sequence: (1) the broad outlines of my equation of state and how I arrived at it; (2) what my attitude was and still is to that equation; (3) how in the last four years I have sought to account for the discrepancies which remained between the experimental results and this equation; (4) how I have also sought to explain the behaviour of binary and ternary mixtures by means of the equation of state.
Van der Waals EOS • a, b are the Van der Waals constants for the particular gas; • for water: a = 0.5658 J-m3/mole2; b = 3.049x10-5 m3/mole,
Compressibility Factor • The deviation from ideal gas behaviour can also be expressed by compressibility factor, Z. • The ratio of volume of real gas, Vreal to the ideal volume of that gas, Vperfect calculated by ideal gas equation is known as compressibility factor.
Compact description of non-ideality: the compressibility factor, Z 1 as p 0 (ideality) Z < 1 at low T, moderate p (point A) Z > 1 at high p, high T (point B)
Generalized Compressibility Chart Reduced Temperature TR = T/Tc Reduced Pressure pR= p/pc
VdW EOS & Compressibility • arepresents the attractive part of the potential; with b = 0, the VdW EOS gives a smaller v for the same T than the ideal gas • brepresents the repulsive portion of the potential; with a= 0, the VdW EOS gives a larger v for the same T than the ideal gas • The VdW EOS is easily expressed in the forms p(T,v) or T(p,v). • For the v(T,p) form, or, equivalently, Z(p,T):
The ideal gas equation of state may be written several ways.