I'm going through the exercises in a Thermodynamics book, just to revise and build my intuition. Right now, I'm working on:

Show that for a quasistatic adiabatic process in a perfect gas, with constant specific heats:

$$PV^\gamma = \left[\text{constant}\right]$$

with $\gamma = \frac{C_P}{C_V}$

where $P$ is pressure, $V$ is volume, and $C_V$ is the constant-volume heat capacity.

I'm not looking for the answer, just for a hint (I'm stuck and want to find the solution myself).

So those are my thoughts:

  • perfect gas means: $PV = RT$, ($R$ is the universal gas constant)
  • adiabatic means: $\mathrm{d}Q = 0$, ($Q$ for heat)
  • since there is no heat exchange, the process is reversible
  • reversible means: $\mathrm{d}W = -P \, \mathrm{d}V$, ($W$ is for work)
  • heat capacity is defined as $C_\text{V} = \left( \frac{\mathrm{d}Q}{\mathrm{d}T} \right)_V$, respectively $C_\text{P} = \left( \frac{\mathrm{d}Q}{\mathrm{d}T} \right)_\text{P}$

If I draw a $PV$ diagram for this situation, it looks like this:

Now I want to show that $PV^\gamma=\left[\text{const}\right]$ by going from $\text{State 1}$ to $\text{State 2}$ in the $PV$ diagram.

I've started like this: $$ W ~=~ -\int_{V_1}^{V_2}P \, \mathrm{d}V ~=~ -\int_{V_1}^{V_2} \frac{RT}{V} \mathrm{d}V ~=~ RT \ln{\left(\frac{V_2}{V_2}\right)} $$

This leads me into the wrong direction though. I thought about using $R = C_P - C_V$ here, but it doesn't seem to work. Any suggestions?

Please just give me a hint, not the solution.

  • 2
    $\begingroup$ You have to use $dU=c_V dT$. The answer can be found in any book. $\endgroup$
    – jinawee
    Feb 10, 2014 at 16:07
  • 6
    $\begingroup$ NB: "since there is no heat exchange, the process is reversible". This is not true as far as I'm aware. The mixing of different substances is irreversible, but does not correspond to heat exchange. (On the flip side, there do exist plenty of reversible processes that involve heat exchange). When we talk about adiabatic expansions/compressions, we typically mean an expansion which is both a) reversible and b) involves no heat exchange. The key point is that the latter on its own does not imply the former. $\endgroup$
    – gj255
    Feb 10, 2014 at 17:30
  • $\begingroup$ Try applying the first law of thermodynamics to get some expression with $C_p$ and/or $C_v$ and then use the definition of gamma & the ideal gas equation. $\endgroup$
    – xasthor
    Feb 18, 2017 at 13:31

4 Answers 4


You have to equal the expression for $\mathrm{d}E$ given by the first law of thermodynamics with the expression that you get if you isolate $\mathrm{d}E$ from $C_V=\left(\frac{\partial E}{\partial T}\right)_V$. Then integrate both sides. With this you should be able to reach the final answer.

A more detailed explanation can be found here. Note that the solutions in the link are also done by me, and Studydrive is a free-access website.

  • $\begingroup$ Is study drive a free-access site, or is it a subscription service? (It might be useful to mention that for those who are not knowledgeable on it) $\endgroup$
    – Kyle Kanos
    Nov 19, 2016 at 19:00

From the first law of thermodynamics, you have:

$$\Delta U = q + w$$

As $q$ is zero, $$\mathrm{d}U = -P \, \mathrm{d}V$$

Now put $\mathrm{d}U = C_v \, \mathrm{d}T$ (molar heat capacity at constant volume).

Therefore, $$C_v \, \mathrm{d}T = -P \, \mathrm{d}V$$

Using the ideal gas equation, substitute $P$ by $\frac{RT}{V}$.

$$-\frac{RT}{V} \mathrm{d}V = C_v \, \mathrm{d}T$$

Integrating the equation, you get $$ \begin{align} \int_{V_1}^{V_2} -\frac{RT}{V} \mathrm{d}V & = \int_{T_1}^{T_2} C_v \, \mathrm{d}T \\[10px] \frac{RT}{V} \ln \left(\frac{V_1}{V_2}\right) & = C_v \left(T_2 - T_1 \right) \end{align} $$

  • $\begingroup$ You can integrate differential equations only. $\Delta$ signifies a finite change whereas $d$ signifies an infinitely small change (differential change). An equation containing $\Delta$ cannot be integrated. $\endgroup$
    – Yashas
    Feb 18, 2017 at 14:28

The mathematical condition you're missing is work = -change in internal energy (which you mentioned as dQ = 0).

dU is ideally written as n*Cv(dT).

take n=1 (for simplicity), equate PdV to -dU, bring in R = Cv (gamma - 1) (same thing as you mentioned), and integrate it. It will be of a logarithmic form with a ton of constants.

Hope this helps. Good Luck!


Before the hint, some conceptual issues:

since there is no heat exchange, the process is reversible

Not necessarily. An adiabatic process is irreversible if either (1) it is not carried out extremely slowly (quasi statically) or (2) mechanical friction is present. To be reversible it must be carried out quasi statically and without friction.

reversible means: $\mathrm{d}W = -P \, \mathrm{d}V$, ($W$ is for work)

Not necessarily. Only if the system is always in mechanical equilibrium with the surroundings so that the $P$ is both the gas and external pressure. That requires the process be carried out slowly. Otherwise $P$ is the external pressure only and the work is irreversible.

heat capacity is defined as $C_\text{V} = \left( > \frac{\mathrm{d}Q}{\mathrm{d}T} \right)_V$, respectively $C_\text{P} = > \left( \frac{\mathrm{d}Q}{\mathrm{d}T} \right)_\text{P}$

These are not the definitions of the heat capacities. The specific heat capacities are defined in terms of the specific internal energy and enthalpy, as follows:

$$c_{v}=\biggl (\frac{\partial u}{\partial T}\biggr)_v$$

$$c_{p}=\biggl (\frac{\partial h}{\partial T}\biggr)_P$$

Now, the hint. Your equation for a reversible adiabatic process is for an ideal gas. For an ideal gas, and only an ideal gas $du=c_{v}dT$ regardless of the process. Use this together with the ideal gas equation, the reversible work equation, and the first law, and you can derive the equation.

Hope this helps.


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