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EQUILIBRIUM CONSTANTS, CHEMICAL AFFINITY, REACTION PROGRESS AND THE PHASE RULE

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Title: EQUILIBRIUM CONSTANTS, CHEMICAL AFFINITY, REACTION PROGRESS AND THE PHASE RULE


1
TOPIC 5
  • EQUILIBRIUM CONSTANTS, CHEMICAL AFFINITY,
    REACTION PROGRESS AND THE PHASE RULE

2
I. THE EQUILIBRIUM CONSTANT
3
DERIVATION OF THE EQUILIBRIUM CONSTANT
  • Consider the reaction aA bB ? cC
  • For each constituent we can write
  • ?A ?A? RT ln aA
  • ?B ?B? RT ln aB
  • ?C ?C? RT ln aC
  • But we now write
  • ?r? c?C - a?A - b?B
  • c(?C? RT ln aC) - a(?A? RT ln aA) - b(?B?
    RT ln aB)
  • (c?C - a?A - b?B) cRT ln aC - aRT ln aA -
    bRT ln aB
  • (c?C - a?A - b?B) RT ln aCc - RT ln aAa -
    RT ln aBb

4
  • In general notation, this is
  • we normally then write
  • so
  • At equilibrium we have

5
  • We call K the equilibrium constant. Because the
    standard states usually refer to pure substances,
    in which ? G, we often write this equation
  • The equilibrium constant is not a function of the
    composition of the system. It depends on
    temperature, and depending on the standard state
    chosen, pressure.
  • This is a remarkable equation, because it relates
    the free energy difference of the reactants and
    products in their standard states, with the
    activities of the constituents in their actual
    state!

The ai here are the activities at equilibrium!
6
CHANGE OF K WITH TEMPERATURE
  • Start with dG VdP - SdT
  • But ?rG ?rH - T?rS 0 at equilibrium, so
  • ?rS ?rH/T

7
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8
DOING THE INTEGRATION
  • CONSTANT ENTHALPY (?rCP 0)
  • This is the equation of a straight line with a
    slope of - ?rH/R on a plot of log K vs. 1/T.
  • CONSTANT HEAT CAPACITY

9
  • The previous equation can be rewritten in the
    form
  • log K a b/T c ln T
  • where

10
  • HEAT CAPACITY KNOWN (Maier-Kelley Expression)

11
How log KTr, ?rH and ?rCP contribute to the
variation of log K with temperature.
12
CHANGE OF K WITH PRESSURE
  • STANDARD STATE AT FIXED PRESSURE
  • If the standard state has a fixed pressure, then
  • and the equilibrium constant is independent of P.

and
13
  • VARIABLE PRESSURE STANDARD STATE
  • Integration is best accomplished by dividing up
    the free energy terms into separate terms for
    condensed phases, gases and solutes.
  • In general

14
  • For condensed phases, a constant volume
    approximation may be appropriate
  • For gases and supercritical fluids, the standard
    state is normally chosen as the ideal gas at the
    system temperature and one bar, so
  • However, if we have a variable pressure standard
    state (this is hardly ever used for gases), then

15
  • where Q is given by
  • For solutes, no general expression exists to
    substitute for the volume integral, so we write
  • So the general expression for the change in K
    with pressure is

16
II. HETEROGENEOUS AND OPEN SYSTEMS
17
THE CHEMICAL AFFINITY
  • For systems that are not in equilibrium, it would
    be convenient to have some quantitative measure
    of the degree to which the system is out of
    equilibrium. This measure is given by the
    affinity (A)
  • where ? is called the reaction progress variable.
    This variable takes on a value of 0 at the start
    of some spontaneous process and ends at some
    value, perhaps 1, in the equilibrium state.

18
  • The differential d? is therefore an increment of
    progress of any spontaneous reaction. For an
    irreversible process, we can therefore write
  • If we do not include the affinity term, then all
    we can write for an irreversible process is

19
  • Another way to understand the meaning of the
    affinity is to consider open systems. We have
    previously seen that at equilibrium in an open
    system, the chemical potentials of each component
    must be balanced in each and every phase. Let us
    consider a metastable state in which the chemical
    potentials are under some constraint and are not
    balanced. When we release this constraint, there
    will be a spontaneous, irreversible
    redistribution of potentials until equilibrium is
    obtained. Now let us imagine that this
    irreversible process takes place in very small
    increments, i.e., d?, in moles.

20
  • If we compare the two expressions
  • we see that
  • or
  • To see what this means, we need a relationship
    between dn and d?.
  • Because reactants and products in a reaction are
    related by fixed stoichiometries, changes in
    their number of moles are related by the
    following

21
  • The only natural cause of changes in the number
    of moles is a spontaneous or irreversible
    reaction such as we are now considering. Thus, it
    seems natural to write
  • It thus follows that

22
  • For example, if we have the reaction
  • A ? 5B
  • we would write
  • This relation allows us to make a connection
    between the reaction progress and the chemical
    potentials. Starting with
  • we now sum over all constituents to get

23
  • But we have and
  • so it follows that
  • Now, the criterion of equilibrium is
  • So it is clear that A 0 is another way of
    expressing the criterion of equilibrium. That is,
    at equilibrium, the chemical affinity will be
    zero there is no drive towards equilibrium,
    because the system is already there!

24
  • For example, for the reaction O2 2H2 ? 2H2O
  • A ?O2 2?H2 - 2?H2O
  • In a metastable mixture of O2 and H2, A is the
    amount by which the chemical potentials could be
    lowered by spontaneous reaction upon release of
    the metastable constraint. The chemical affinity
    is the driving force of the reaction. The
    driving force becomes zero when ?O2 2?H2
    2?H2O.
  • Another relation can be derived starting with
  • ?i ?i RT ln ai

25
  • where
  • but
  • so
  • From what we have done, we can expect that we
    have the following relations

26
THE PHASE RULE
  • Let us consider a closed system that has C
    components and P phases. In this system, the
    compositions of each of the phases are potential
    variables, for a total of P(C-1) compositional
    variables (there are only C-1 compositional
    variables for each phase, because the sum has to
    total 100). In addition, temperature and
    pressure are variables. So the total number of
    variables are P(C-1) 2.
  • At the same time, at equilibrium, we have for
    each component, P - 1 constraints of the type
  • ?i1 ?i2 ?i3 ?i4 ?iP
  • This gives us a total of C(P-1) constraints.

27
  • If we define the number of degrees of freedom (F)
    as
  • F of variables - of constraints
  • we can then write
  • F P(C-1) 2 - C(P - 1)
  • F PC - P 2 - CP C
  • F C 2 - P
  • This expression is known as the Gibbs phase rule.
    It is an amazingly powerful relationship, but
    care must be taken in its application. Recall
    that the components are defined as the minimum
    number of mathematical entities required to
    express the compositions of all phases in the
    system. The choice of components is arbitrary,
    and they need not correspond to actual chemical
    entities.

28
CHOICE OF COMPONENTS
  • Example 1 Consider the system containing
    forsterite (Mg2SiO4), enstatite (Mg2Si2O6) and
    quartz (SiO2).
  • In this case, only two components are required to
    fully describe the compositions of all the
    phases.
  • Valid Component Choices
  • 1) Mg2SiO4, SiO2 2) Mg2SiO4, Mg2Si2O6 3) MgO,
    SiO2 4) Si2O4, MgO 5) Mg2Si2O6, -SiO2 etc.
  • Invalid Component Choices
  • 1) Mg, Si 2) Mg, Si, O 3) Mg2SiO4
  • F C 2 - P 2 2 - 3 1
  • So the system is univariant.

29
  • Example 2 Consider a system composed of the
    phases dolomite (CaMg(CO3)2), quartz (SiO2),
    diopside (CaMgSi2O6) and carbon dioxide vapor
    (CO2).
  • Only three components are required to describe
    this system. One valid choice is CaMgO2, CO2 and
    SiO2.
  • Note that Ca and Mg do not give rise to separate
    components because they occur in the same ratio
    wherever they occur.
  • F C 2 - P 3 2 - 4 1
  • so this system is also univariant.

30
  • Example 3 Consider a system containing calcite,
    dolomite, quartz, and a single fluid containing
    H2O and CO2.
  • In this system, five components are required to
    describe the system. One valid choice is CaO,
    MgO, SiO2, H2O, and CO2.
  • F C 2 - P 5 2 - 4 3
  • This system is a trivariant one. If the vapor
    phase formed two immisicible fluid phases, then
    the system would have one more phase, and one
    less degree of freedom and would be divariant.
  • F C 2 - P 5 2 - 5 2

31
  • Example 4 Consider a system containing garnet
    ((Fe,Mg)3Al2(SiO4)3), cordierite
    ((Fe,Mg)2Al4Si5O18), spinel ((Fe,Mg)Al2O4),
    olivine ((Fe,Mg)2SiO4), quartz (SiO2) and
    orthopyroxene ((Fe,Mg)2Si2O6).
  • This one is a bit tricky. If Fe and Mg substitute
    for one another ideally in each of these phases,
    i.e., there is no differential partitioning of Fe
    and Mg, then they behave as a single component,
    so we have three components (Fe,Mg)O, Al2O3, and
    SiO2. This system has F 3 2 - 6 -1 and
    cannot be in equilibrium. If Fe or Mg prefer one
    phase to the others, then they are separate
    components and C 4. In this case F 4 2 - 6
    0 and the system is invariant.

32
  • Example 5 Consider the system containing the
    phases calcite (CaCO3), fluorite (CaF2),
    fluocerite (LaF3), bastnäsite (LaCO3F), parisite
    (CaLa2(CO3)3F2) and synchysite (CaLa(CO3)2F). How
    many components are required to describe this
    system?
  • This one is also tricky. It would seem that F-
    and CO32- should be separate components. However,
    there are charge-balance requirements that tie
    these together as a single component. It takes 3
    components to describe this system. One choice
    is CaCO3, LaCO3F and F2(CO3)-1. The latter is an
    example of an exchange operator component, in
    which 2 F- are exchanged for one CO32-.

33
APPLICATION OF THE PHASE RULE TO PHASE
DIAGRAMS THE Al2SiO5 SYSTEM
34
PHASE RULE FOR OPEN SYSTEMS
  • The activities of mobile components in an open
    system are not controlled by the phases in the
    system they are controlled by some external
    factor. Therefore, there is an additional
    constraint on each of the mobile components, and
    the degrees of freedom should be reduced
    accordingly.
  • F C 2 - P - M
  • where C number of total components and M the
    number of mobile components.
  • This version of the phase rule explains why
    increased metasomatism tends to reduce the number
    of minerals in a rock.

35
TYPES OF COMPONENTS(AFTER KORZHINSKII, 1959)
  • Trace components Usually chosen as elements and
    occur at very low concentrations in the minerals
    of a system (e.g., V, Cr, Co in a granite). They
    are not an essential part of any phase. Their
    concentrations can very over a range without
    affecting the number of phases.
  • Accessory components Components that occur
    almost entirely in a single phase. For example
    TiO2 in rutile, titanite or ilmenite P2O5 in
    apatite ZrO2 in zircon. In each case, the
    presence of the component causes a phase to
    exist, but no net increase in the degrees of
    freedom occurs.

36
  • Isomorphous components These are components that
    substitute freely for one another on various
    lattice sites. If the substitution its truly
    ideal, in other words, the mineral properties are
    unaffected by substitution, then the two
    components behave as one and can be considered a
    single component.
  • Excess components Those that occur in the pure
    form, and also in some or all of the other phases
    of the system. For example SiO2 occurs in all
    silicates and also in the form of quartz. Because
    the activity of SiO2 is fixed by the presence of
    quartz, it is often possible to neglect SiO2 as a
    component in the counting of components.

37
  • Determinative components All those that do not
    fit into any of the above categories. They are
    therefore the set of independent components that
    control which phases will occur and how much.
    These are the components used to plot diagrams
    showing phase relations.

38
MINERALOGICAL PHASE RULE
  • Natural systems would normally have at least two
    degrees of freedom, e.g., temperature and
    pressure, in other words F ? 2. This allows us to
    write the mineralogical phase rule as
  • P ? C
  • this simply states that the number of minerals
    one would find in a rock in equilibrium is
    limited by the number of components.

39
BUFFERED SYSTEMS
  • Buffered system - a system in which the presence
    of a certain number of phases fixes all the
    properties of the system at a given temperature
    and pressure. In other words, the activities of
    all the components are fixed if temperature and
    pressure are specified.
  • The phase rule can help us to identify buffered
    systems.
  • For example, consider a rock containing both
    gypsum (CaSO42H2O) and anhydrite (CaSO4). This
    is a two-component, two-phase system, so F C
    2 - P 2 2 - 2 2.

40
  • This is a divariant system, and if we fix
    temperature and pressure, and gypsum and
    anhydrite remain in equilibrium, the the activity
    of H2O is fixed according to
  • CaSO42H2O ? CaSO4 2H2O
  • The equilibrium constant for this reaction can be
    written
  • Because the solids are pure, their activities are
    unity, so
  • and the activity of water is fixed!

41
  • Of course, any component can be buffered in
    theory. Consider a rock containing only
    forsterite and enstatite. This is a two-component
    system which will fix silica activity when P and
    T are specified.
  • Mg2SiO4 SiO2 ? Mg2Si2O6
  • Because enstatite and forsterite are pure phases,
    their activities are unity. However, this is not
    the case for the activity of silica.
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