CHM 5414 Lecture Notes
29 October 1996
Your browser must support super and subscripts to view this page!
Heating It Up
Flames are even more fascinating than soap bubbles. The ancients were so
enamored of Fire that they elevated it to one of the four elements (earth,
air, fire, water). In fact, that philosophy persisted through the
Phlogiston theory of conflagration up until only a couple of hundred years ago!
But even knowing the dance of fuel and oxidizer, exothermicity and buoyancy,
doesn't dash the wonder of flame. That couldn't be 'cause all us chemists are closet
pyromaniacs, could it?
In flames, heat and work play off against one another in a most satisfying way
which leads us below to general expressions for adiabatic processes!
In the last lecture, we found that the energy of an ideal gas depended not on its pressure
but on its temperature. Compressed or exanded in thermal contact with surroundings, ideal gases
have fixed energy. They are worked upon or do work, but that work is exactly compensated for
by heat transfer:
dE = q + w = 0 or q=-w
It's easy to imagine the work involved as -PextdV, but the "heat transferred" doesn't
change the gas's appearance; instead it bumps molecular microstates up or down their quantum
energy level ladders invisibly save for instruments which measure temperature.
Let's imagine a non-isothermal process; temperature is now permitted to change, and
there must be some sensitivity of thermodynamic values to that like:
dE = (E/T)V dT = CV dT
We've chatted about CV before from a statistical mechanical point of view.
It's magnitude reflects the number of ways a system can hide energy (available degrees
of freedom) as the temperature increases. If few modes are available in the partition
function sense, the temperature can shoot up with trivial energy additions. (Hey, it's reciprocal;
if dE is insensitive to dT due to a small CV, then dT is super-sensitive to dE, right?)
On the other hand, we know that z increases with temperature, making additional states (and indeed
entire modes) turn active. At solid state temperatures, only the phonon (solid vibration) modes are active.
At liquid state temperatures (T>trans), those phonons have become cramped translations, and rotations have
started to become active. By gas temperatures, both translations and rotations are fully active (T>rot),
and vibrations are slowly beginning to turn on. "Fully active" means that the energy is as
expected from the Equipartition Theorem, ½RT for each available mode (a full RT for each
vibration since it incorporates both kinetic and potential energies). So for a rigid
3-d polyatomic gas, 3 translations + 3 rotations yields <E>=3RT which tells us CV
in that T range will be about 3R. (All of this for a mole, of course; CV is an extensive variable just
like E.)
Just for jollies, a monatomic gas has no rotations, so its CV is expected to be about
(3/2)RT around room temperature.
We could, of course, calculate CV from z as we have E by simply differentiating the
statistical mechanical expression for molar E with respect to T (at constant V).
CV = 2 RT (ln z/T)V + RT²(²ln z/T²)V,P
but that's not terribly practical. Instead, we usually take advantage of the fact that at room
temperature, we're still waiting for the vibrations to get interested (T<vib),
so CV is changing only rather slowly with T. Indeed, the variation is fit to a T polymial
usually of the form:
CV = a + bT + c/T²
Those parameters aren't fundamental in any way; this is just curve-fitting here. But it is
a particularly simple curve, easily integrated:
dE = T1T2 a + bT + c/T² dT = aT + ½bT² - c(1/T)
As chemists, we're more enthusiastic for dH which also has a temperature dependence. But while
dE=q-PdV measures qV, dH=q+VdP measures qP, and we're not surprised that it's
temperature dependence,
dH = (H/T)P dT = CP dT
bears the P subscript. It too is very weakly T dependent at room temperature (for the
same reason), and gets expanded into the very same polynomial, with different coefficients; so
dH = a'T + ½b'T² - c'(1/T)
and it's fair to ask how CV and CP relate. The answer's easy for an ideal gas.
dH=dE+d(PV)=dE+nRdT, so CP=CV+R. Your mileage may vary if you're not ideal.
Why do we want to know this???
Because the interesting chemical reactions are either exothermic, providing lots of q, or
endothermic, requiring some q, and almost never thermoneutral. Therefore, either the reactants
or the products are obliged to absorb the reaction q, and the resultant dT may influence the
equilibria. This is important to know, if we're making our livelihood off chemical produce. :-)
Just as we can find the H ° of
our favorite reaction:
a A + b B c C + d D
as
H° = c Hf°(C) + d Hf°(D) - a Hf°(A) - b Hf°(B)
so to can we define a
CP = c CP(C) + d CP(D) - a CP(A) - b CP(B)
which permits us to evaluate H
at something other than standard temperature. If the CP heat capacities are really
constant over the temperature difference from 25°C to T, then each H
varies by its own CPT.
And the nonstandard temperature H we seek is:
H(T) = H ° + CPT
and similarly with E if we use CV.
But what of S?
It too must be temperature dependent via, say, dH=TdS+VdP,
which for isobaric (fixed pressure) processes (for which H is famous), means
dS=(dH)/T=CP(1/T)dT. And for reasonably constant CP,
dS=CPd lnT or S=CPln(T2/T1).
And if we were masochistic, we could now find the temperature dependence of
A
(using CV, of course) and that for G
as well (using CP).
But while Cwhatever is
critical for evaluating thermo energy/entropy changes at different temperatures
via Hess's Law, a variant of it is interesting characterizing the second
great class of thermodynamic processes:
Adiabatic Processes
Instead of perfect thermal coupling (isothermal) of system to surroundings,
adiabatic processes require perfect insulation! This is greeted with greater
suspicion; after all, doesn't everything have some finite, even if tiny,
heat conductivity? Thermos bottles don't keep coffee hot forever.
True. There's even a physical law due to Isaac Newton on the subject called
Newton's Law of Cooling (equally applicable to heating). It states that
the rate of cooling (heating) is directly proportional to the current
T
between system and surroundings, regardless of the thermal conductivity
coefficients! While it's meaningless to approach adiabaticity by minimizing
the very T
we seek to establish, Newton's Law suggests that, if a rate is
involved, simply look to extremely short processes as necessarily
adiabatic since time is required to bleed away heat.
The astute among you will realize that Newton's Law refers only to thermal
conduction (through matter) not convection (through matter transport) or
via radiation. Photons are a good deal more prompt than any other heat
transfer mechanism, but they're remarkably inefficient. Radiative
cooling is truly lethargic.
What has this to do with approaching adiabatic processes? We might look to
rapid ones. Explosions come to mind, if one is of the mad scientist brand
of chemist. Mea culpa. Mea culpa. Mea maxima culpa.
Not only are explosions rapid, effectively trapping their exothermicity
among the products, but they're also over before the (typically gaseous products have begun
to expand. So they've not yet done Pressure-Volume work, and E
is the interesting quantity since it equates to heat at V=0.
If we imagine instantaneous completion of an explosion, the products must
distribute the enormous exothermicity among themselves. And Hess encourages
us to imagine that the reaction proceeds at 25°C releasing E°
after which that E°
is reabsorbed by all the products (and anything else in the vicinity...unreacted
reagents, non-reactive diluents, etc.) until the temperature has risen to
accommodate it all. Since for exothermicity, E<0,
the appropriate relation is:
E° = - [ c CV(C) + d CV(D) ] T
or
Texplosion = 298°K - E°/[sum of product CV]
Similarly, but with less justification, a flame temperature might be
approximated as:
Tflame = 298°K - H ° / [sum of product CP]
since the flame products do expand against atmospheric pressure while reacting.
A few trials with these expression convince one that adiabaticity is wildly
overestimated. The oxyacetylene torch, for example, is calculated to be hotter
than the photosphere of the sun! Sure. Still comparisons of even these
hopelessly approximate temperatures are useful to rank real flame temperatures.
Adiabatic Expansion
Isothermal expansions have been covered in the previous notes. If they could
be imagined carried out reversibly, the Pext would have to be
Pinternal -
at all points in the process. That makes Pext=nRT/V for an ideal gas
undergoing isothermal expansion.
P = constant×V -1 along an isotherm
giving rise to the hyperbola in the chart at right. But an adiabatic expansion
cannot take those paths; the energy the gas loses to Pressure-Volume work is
not made up by heat transfer since that is presumed to be impossible. Thus
the internal energy and the temperature of the ideal gas must decline. While
the adiabatic expansion might begin at point A, it must end at point B on a
different isotherm.
The black curve in the figure at the left is an adiabat for a monatomic gas.
Clearly it falls more steeply than V -1. The
adiabatic expansion starts at V=2 L where the adiabat crosses the 373 K
isotherm in this example, and it ends at V=6.3 L where it crosses the 173 K
isotherm. Life would be simpler if it dropped from 373 K
to 173 K
at constant Vinitial
then slid down the 173 K isotherm.
The reason that's easier is that E=0
along the isotherm but changes by CVT
along the fixed V path.
But both paths reach the same (final) state! And the adiabat gets there by
doing work on the atmosphere in an amount we can imagine to be reversible.
We can equate this reversible work with the CVT
and learn how V relates to T under adiabatic expansion.
We imagine the process proceeding in baby steps along each isotherm over
which the adiabat passes; that is, we drop a little (CVdT),
then slide a little (-PdV), repeated in small increments, shadowing the
adiabat with infinitesimal drops and slides. Along the adiabat steps, dE=-PdV;
along the drop/slide alternate, dE=CVdT+0. Since they get the same
place, they must be equal:
nCV dT = - nRT dV/V
CV dT/T = - R dV/V
CV ln(T2/T1) = + R ln(V1/V2)
ln(T2/T1) = (R/CV) ln(V1/V2)
ln(T2/T1) = ln(V1/V2)R/CV
(T2/T1) = (V1/V2)R/CV
or
T2V2R/CV = T1V1R/CV = const = T VR/CV
Sustitution of the ideal gas equation into this formula and recognition that
CP = CV+R for an ideal gas gives two further adiabatic
relations:
P / TCP/R = constant
and the one we need:
P VCP/CV = constant
or, given the values expected for heat capacities of an ideal monatomic gas,
CP/CV=(5/2)÷(3/2)=5/3, the black adiabat above is
the equation P=const/V5/3 which does indeed fall faster than
1/V.
Return to the CHM 5414 Lecture Notes or Go To Next or Previous Lectures.
Chris Parr
University of Texas at Dallas
Programs in Chemistry, Room BE3.506
P.O. Box 830688 M/S BE2.6 (for snailmail)
Richardson, TX 75083-0688
Voice: (972) 883-2485
Fax: (972) 883-2925
BBS: (972) 883-2168 (HST) or -2932 (V.32bis)
Internet: parr@utdallas.edu (Click on that address to send Dr. Parr e-mail.)
Last modified 10 August 1998.