14.2 Adiabatic phase transformation 303
shall start with that problem because it has much in common with diffusion and may be
used to demonstrate important principles.
14.2 Adiabatic phase transformation
Foraprocess taking place under adiabatic and isobaric conditions, dQ = 0 and dP = 0,
we have from the first law
dH = d(U + PV) = dU + PdV + V dP = dQ + V dP = 0. (14.1)
Forasystem which is closed to exchange of matter as well as heat we also have dN
i
=
0 and it is convenient to use the combined law in the following form obtained from
Eqs (14.1) and a generalized form of Eq. (1.72)
T · d
ip
S = T dS + V dP + µ
i
dN
i
− dH = T dS. (14.2)
It should be emphasized that here we have not represented T · d
ip
S with the driving force
Ddξ because the reaction is not isothermal. The condition for a reversible reaction is
d
ip
S = 0 and thus dS = 0. In order for the reaction to proceed with a measurable rate it
is necessary that d
ip
S > 0 and thus dS > 0.
A homogeneous reaction (e.g. a spontaneous reaction between molecules in a gas)
occurs gradually in the whole system and one can usually presume that it has proceeded
to the same extent ξ in all parts of the system. It is evident that such a reaction can occur
under adiabatic and isobaric conditions. The situation is different for a heterogeneous
reaction which takes place by nucleation and growth. Let us examine the simple case of a
sharp phase transformation which goes to completion instantaneously at any point as an
interface passes by. The extent of reaction can be measured as the fraction of the system
which has undergone the transformation. Thus, ξ would go from 0 to 1. Alternatively,
ξ can be given as the number of atoms in the transformed part. Let us suppose that this
reaction can occur under adiabatic conditions. Due to the heat of transformation, this
should mean that the transformed part of the system is at a different temperature than
the rest and heat would thus flow between the different parts unless the transformation is
extremely rapid and leaves no time for the flow of heat. Such high transformation rates
are not very common. An explosion may come close. We may thus conclude that the
transformation in a material cannot normally be truly adiabatic even if it occurs inside
a thermally insulated system. Before considering the effect of the heat transfer we shall
nevertheless examine the conditions for a hypothetical transformation which is truly
adiabatic. Since we realize that the transformation will cause a change of temperature
we must start by defining the thermal properties.
Let us consider a unary system with two phases, α and β, and let us suppose that the
difference in their heat capacities, C
p
,isindependent of temperature. Then the differ-
ences in molar enthalpy H
m
and in entropy S
m
at any temperature are independent of
temperature but may vary with pressure. The equilibrium temperature at a given pressure
will be T
e
= H
m
/S
m
. Schematic T, P and H
m
, P phase diagrams are given in Fig. 14.1.
The boundary between α and α + β is denoted α/β because it represents α in equilibrium