The partial molar enthalpies of a species in a simple binary mixture can sometimes be approximated by the following expressions
a) For these expressions, show that b1 must equal b2 .
b) For these expressions, show that the enthalpy of mixing per
mole of solution at constant temperature and pressure is given
by
c) If N1 moles of species 1 and N2 moles of species 2, both initially at a temperature of Ti , are adiabatically mixed at constant pressure, show that the final temperature is equal to
where CP,1
and CP,2 are the constant molar isobaric heat capacities
of species 1 and 2, respectively.
The enthalpy of mixing (also called heat of mixing) is the heat that is taken up or released upon mixing of two (non-reacting) chemical substances. When the enthalpy of mixing is positive, mixing is endothermic while negative enthalpy of mixing signifies exothermicmixing.
Enthalpy of mixing
We know that in an ideal system ΔG=ΔH−TΔSΔG=ΔH−TΔS, but this equation can also be applied to the thermodynamics of mixing and solved for the enthalpy of mixing so that it reads
ΔmixH=ΔmixG+TΔmixS(1.15)(1.15)ΔmixH=ΔmixG+TΔmixS
Plugging in our expressions for ΔmixGΔmixG (Equation 1.101.10) and ΔmixSΔmixS (Equation 1.141.14) , we get
ΔmixH=nRT(x1lnx1+x2lnx2)+T[−nR(x1lnx1+x2lnx2)]=0(1.16)(1.16)ΔmixH=nRT(x1lnx1+x2lnx2)+T[−nR(x1lnx1+x2lnx2)]=0
This result makes sense when considering the system. The molecules of ideal gas are spread out enough that they do not interact with one another when mixed, which implies that no heat is absorbed or produced and results in a ΔmixHΔmixH of zero. Figure 2 illustrates how TΔmixSTΔmixS and ΔmixGΔmixG change as a function of the mole fraction so that ΔmixHΔmixH of a solution will always be equal to zero (this is for the mixing of two ideal gasses).
I can go on but the details require statistical thermodymics modelling of enthalpy of mixing.
The partial molar enthalpies of a species in a simple binary mixture can sometimes be approximated...
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The molar volume in cm^3/mol of a binary liquid mixture at T and P is given by:V~ = 120 x1 + 70 x2 + (15 x1 + 8 x2) x1 x2a.) Find expressions for the partial molar volumes of species 1 and 2 at T and P.b.) Show that when these expressions are combined in accord with Eqn 11.11 the given equation for V~ is recovered.c.) Show that these expressions satisfy Eqn 11.14, the Gibbs-Duhem equation.d.) Show that at constant...
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