5.4 Phase diagrams of binary systems Φ min =1, F max =3 C=2, F=2-Φ+2=4-Φ Predict by phase law: Three dimentional diagram T, P, x Intercepting plane graph---two dimentional diagrams T, P, x (T, x) p, (P, x) T or (T, P) x
Contents Liquid-liquid Miscible Partly-miscible Immiscible Liquid-solid Water-salt Solid-solid
5.4.1 Phase diagram of miscible binary systems Ideal mixed systems: Two components both follow Raoult’s Law. ( ) T, P-x, A+B
( ) T, P-y, A+B
( ) T, P-x-y xAxA Liquid P Vapour Φ=2 F=2-2+1=1(P) liquid Liquid/ Vapour A is more volatile than BB is more volatile than A
( ) P T-x
x1x1x1x1 d T3 d’ x2 TA*TA* x3x4 T c T2 c’ a a’ b T1 b’ A B TB*TB* x1x1x1x1 T1T1T1T1 x2x2x2x2 T2T2T2T2 x3x3x3x3 T3T3T3T3 x2x2x2x2 x3x3x3x3 x4x4x4x4 A The composition variation in the distillation process How would it be in an closed system?
P-x , liquid(upper line)- gas(lower line) Getting T-x phase diagram from P-x Relating P-x and T-x phase diagram T-x , gas(upper line)-liquid(lower line)
The Lever rule C, total amount of the systems DE ( tie line ) isothermal
Phase equilibrium variation at constant temperature ---the level rule
The principle of distillation Simple distillationT T 1 T T2 Separate a volatile liquid from a non-volatile solute or solid
Theoretical plates: the number of effective vaporization and condensation steps that are required to achieve a condensate of given composition from a given distillate Fractional distillation
Non-ideal solutions
P-x and T-x phase diagrams of non-ideal miscible binary systems
Azeotropes Low-boiling azeotrope
351.28K , Low-boiling azeotrope
The maximum azeotropic point High boiling azeotropes K HCl
Homework Y: P161 17, 18 A: P (a), 8.6(a) Preview: Y: 5.5,5.6, 5.7 A:8.5, 8.6