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 = ( Partial E/ Partial 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> Theta 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> Theta 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 ( Partial ln z/ Partial T)V + RT²( Partial ²ln z/ Partial 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< Theta 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 =  integral T1T2 a + bT + c/T² dT = a Delta T + ½b Delta T² - c Delta (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 = ( Partial H/ Partial 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' Delta T + ½b' Delta T² - c' Delta (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  Delta H ° of our favorite reaction:

a A + b B  arrow right c C + d D

as
 Delta H° = c  Delta Hf°(C) + d  Delta Hf°(D) - a  Delta Hf°(A) - b  Delta Hf°(B)

so to can we define a
 Delta CP = c CP(C) + d CP(D) - a CP(A) - b CP(B)

which permits us to evaluate  Delta 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  Delta H varies by its own CP Delta T. And the nonstandard temperature  Delta H we seek is:

 Delta H(T) =  Delta H ° +  Delta CP Delta T


and similarly with  Delta E if we use CV.

But what of  Delta 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  Delta S=CPln(T2/T1). And if we were masochistic, we could now find the temperature dependence of  Delta A (using CV, of course) and that for  Delta G as well (using CP).

But while  Delta 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  Delta T between system and surroundings, regardless of the thermal conductivity coefficients! While it's meaningless to approach adiabaticity by minimizing the very  Delta 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  Delta E is the interesting quantity since it equates to heat at  Delta 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  Delta E° after which that  Delta 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,  Delta E<0, the appropriate relation is:

 Delta E° = - [ c CV(C) + d CV(D) ]  Delta T

or

Texplosion = 298°K -  Delta E°/[sum of product CV]

Similarly, but with less justification, a flame temperature might be approximated as:

Tflame = 298°K -  Delta 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

Ideal Gas Isotherm Chart Isothermal expansions have been covered in the previous notes. If they could be imagined carried out reversibly, the Pext would have to be Pinternal - epsilon 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.

Adiabat Between Isotherms 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  Delta E=0 along the isotherm but changes by CV Delta T 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 CV Delta T 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.