Hydrogen gas, which is of potential interest
nationally as a clean fuel, can be generated by the reaction of
carbon (coal) and water:
C(s)+2H2O(g)→CO2(g)+2H2(g)C(s)+2H2O(g)→CO2(g)+2H2(g)
(2)Calorimetry reveals that this reaction
requires the input of 90.1kJ of
heat for every mole of
C(s)C(s)
consumed. By convention, when heat is absorbed during a reaction,
we consider the quantity of heat to be a positive number: in
chemical terms,
q>0q0
for an endothermic reaction. When heat is
evolved, the reaction is exothermic and
q<0q0
by convention.
It is interesting to ask where this input
energy goes when the reaction occurs. One way to answer this
question is to consider the fact that the reaction converts one
fuel,
C(s)C(s),
into another,
H2(g)H2(g).
To compare the energy available in each fuel, we can measure the
heat evolved in the combustion of each fuel with one mole of oxygen
gas. We observe that
C(s)+O2(g)→CO2(g)C(s)+O2(g)→CO2(g)
(3)produces 393.5kJ for one mole of carbon
burned; hence
q=-393.5kJq-393.5kJ.
The reaction
2H2(g)+O2(g)→2H2O(g)2H2(g)+O2(g)→2H2O(g)
(4)produces 483.6kJ for two moles of hydrogen gas
burned, so
q=-483.6kJq-483.6kJ.
It is evident that more energy is available from combustion of the
hydrogen fuel than from combustion of the carbon fuel, so it is not
surprising that conversion of the carbon fuel to hydrogen fuel
requires the input of energy.
Of considerable importance is the observation
that the heat input in Equation 2,
90.1kJ, is exactly equal to the
difference between the heat
evolved, -393.5kJ, in the combustion of carbon and the heat
evolved, -483.6kJ, in the combustion of hydrogen. This is not a
coincidence: if we take the
combustion of carbon and add to it the
reverse of the combustion of
hydrogen, we get
C(s)+O2(g)→CO2(g)C(s)+O2(g)→CO2(g)
2H2O(g)→2H2(g)+O2(g)2H2O(g)→2H2(g)+O2(g)
C(s)+O2(g)+2H2O(g)→CO2(g)+2H2(g)+O2(g)C(s)+O2(g)+2H2O(g)→CO2(g)+2H2(g)+O2(g)
(5)Canceling the
O2(g)O2(g)
from both sides, since it is net neither a reactant nor product,
Equation 5 is
equivalent to Equation 2. Thus, taking
the combustion of
carbon and "subtracting" the combustion of
hydrogen (or more accurately, adding the reverse of
the combustion of
hydrogen) yields Equation 2. And, the heat of the combustion of carbon
minus the heat of the combustion of
hydrogen equals the heat of Equation 2.
By studying many chemical reactions in this
way, we discover that this result, known as Hess'
Law, is general.
The heat of any reaction is equal to the
sum of the heats of reaction for any set of reactions which in sum
are equivalent to the overall reaction.
(Although we have not considered the
restriction, applicability of this law requires that all reactions
considered proceed under similar conditions: we will consider all
reactions to occur at constant pressure.)
A pictorial view of Hess' Law as applied to
the heat of Equation 2 is
illustrative. In Figure 1, the
reactants
C(s)+2H2O(g)C(s)+2H2O(g) are placed together in a box,
representing the state of the materials
involved in the reaction prior to the reaction. The products
CO2(g)+2H2(g)CO2(g)+2H2(g) are placed together in a second box representing the state
of the materials involved after the reaction. The reaction arrow
connecting these boxes is labeled with the heat of this reaction.
Now we take these same materials and place them in a third box
containing
C(s)C(s),
O2(g)O2(g),
and
2H2(g)2H2(g).
This box is connected to the reactant and product boxes with
reaction arrows, labeled by the heats of reaction in Equation 3 and Equation 4.
This picture of Hess' Law reveals that the
heat of reaction along the "path" directly connecting the reactant
state to the product state is exactly equal to the total heat of
reaction along the alternative "path" connecting reactants to
products via the intermediate state containing
C(s)C(s),
O2(g)O2(g),
and
2H2(g)2H2(g).
A consequence of our observation of Hess' Law is therefore that the
net heat evolved or absorbed during a reaction is independent of
the path connecting the reactant to product. (This statement is
again subject to our restriction that all reactions in the
alternative path must occur under constant pressure
conditions.)
A slightly different view of Figure 1 results from beginning at the
reactant box and following a complete circuit through the other
boxes leading back to the reactant box, summing the net heats of
reaction as we go. We discover that the net heat transferred (again
provided that all reactions occur under constant pressure) is
exactly zero. This is a statement of the conservation of energy:
the energy in the reactant state does not depend upon the processes
which produced that state. Therefore, we cannot extract any energy
from the reactants by a process which simply recreates the
reactants. Were this not the case, we could endlessly produce
unlimited quantities of energy by following the circuitous path
which continually reproduces the initial reactants.
By this reasoning, we can define an energy
function whose value for the reactants is independent of how the
reactant state was prepared. Likewise, the value of this energy
function in the product state is independent of how the products
are prepared. We choose this function,
HH, so that
the change in the function,
ΔH=Hproducts−HreactantsΔHHproductsHreactants,
is equal to the heat of reaction
qq under
constant pressure conditions.
HH, which we
call the enthalpy, is a state
function, since its value depends only on the state of
the materials under consideration, that is, the temperature,
pressure and composition of these materials.
The concept of a state function is somewhat
analogous to the idea of elevation. Consider the difference in
elevation between the first floor and the third floor of a
building. This difference is independent of the path we choose to
get from the first floor to the third floor. We can simply climb up
two flights of stairs, or we can climb one flight of stairs, walk
the length of the building, then walk a second flight of stairs. Or
we can ride the elevator. We could even walk outside and have a
crane lift us to the roof of the building, from which we climb down
to the third floor. Each path produces exactly the same elevation
gain, even though the distance traveled is significantly different
from one path to the next. This is simply because the elevation is
a "state function." Our elevation, standing on the third floor, is
independent of how we got to the third floor, and the same is true
of the first floor. Since the elevation thus a state function, the
elevation gain is independent of the path.
Now, the existence of an energy state function
HH is of
considerable importance in calculating heats of reaction. Consider
the prototypical reaction in Figure 2(a), with reactants
RR being
converted to products
PP. We wish to
calculate the heat absorbed or released in this reaction, which is
ΔHΔH.
Since HH is a
state function, we can follow any path from
RR to
PP and
calculate
ΔHΔH
along that path. In Figure 2(b), we
consider one such possible path, consisting of two reactions
passing through an intermediate state containing all the atoms
involved in the reaction, each in elemental form. This is a useful
intermediate state since it can be used for any possible chemical
reaction. For example, in Figure 1,
the atoms involved in the reaction are C, H, and O, each of which
are represented in the intermediate state in elemental form. We can
see in Figure 2(b) that the
ΔHΔH
for the overall reaction is now the difference between the
ΔHΔH
in the formation of the products
PP from the
elements and the
ΔHΔH
in the formation of the reactants
RR from the
elements.
The
ΔHΔH
values for formation of each material from the elements are thus of
general utility in calculating
ΔHΔH
for any reaction of interest. We therefore define the
standard formation reaction for reactant
RR,
aselements in standard state→Relements in standard state→R
and the heat involved in this reaction is the
standard enthalpy of formation, designated
by
ΔHf°ΔHf°.
The subscript
ff, standing
for "formation," indicates that the
ΔHΔH
is for the reaction creating the material from the elements in
standard state. The superscript ° indicates that the reactions occur
under constant standard pressure conditions of 1 atm. From Figure 2(b), we see that the heat of any reaction can
be calculated from
ΔHf°=ΔHf°products−ΔHf°reactantsΔHf°
ΔHf°products
ΔHf°reactants
(6)Extensive tables of
ΔHf°ΔHf° have
been compiled and published. This allows us to calculate with
complete confidence the heat of reaction for any reaction of
interest, even including hypothetical reactions which may be
difficult to perform or impossibly slow to react.
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