Principle
To understand the concept of diabatic phenomena, first
Boyle’s law is
applied to the simple set-up of Fig. 1.

Fig. 1
The amount of
gas in both compartments together is p·Va + p·Vb which
holds with the closed valve (at time zero, t0) as well as after
equilibration of the pressures (at time t) when the valve has been opened. So,
it holds that:
pa, 0·Va + pb, 0·Vb
= pt·(Va + Vb). (1)
With given pa, 0, pb, 0, Va
and Vb at t0,
pt can be calculated. When Vb =
jVa and pb, 0 = kpa, 0 then pt
becomes:
pt = pa(1+jk)/(1+j). (2)
However, this is only true when the temperature T in
the whole system remains constant during the whole process of pressure
equilibration, i.e. the process is isotherm or diabatic. When this is not the
case, then the left compartment cools down and the right one heats up. For more
info about this adiabatic process, see Adiabatic Compression and expansion.
Another condition is that the gas is ideal, i.e. the
particles do not interact and they have no size. When pressures (so densities)
are low, both conditions apply well and (1), which is actually based on Boyle’s
law (see Gas Laws),
can be used. When they do not hold, the Van der Waals corrections are
necessary.
Application
Innumerous in science, technology and so indirectly in
medicine, e.g. in breathing apparatus and especially in pulmonology.
The Van der Waals corrections are used for mass
calculations of commercials gases in high-pressure tanks e.g. applied in
medicine, especially with the expensive helium.
More Info
The Van der Waals correction has two constants a and b (Table 1). The
correction factor “a” is needed for
the interaction between the gas particles (attraction coefficient), and a
correction factor “b” for the volume
occupied by the gas particles.
Table 1.
|
Molecule, |
Van der Waals
constants |
|
|
atom |
a |
b |
|
or mixture |
103J.m3/kmol2 |
10-3m3/kmol |
|
He |
3,5 |
22 |
|
H2 |
25 |
26 |
|
O2 |
140 |
31 |
|
N2 |
140 |
39 |
|
CO2 |
360 |
44 |
|
H2O |
550 |
30.5 |
|
air |
140 |
37.4 |
b of air interpolated from weighed b’s
of O2 and N2
According to Van der
Waals:
(p + an2/Vm2)
(Vm-nb) = nRT, (3a)
where Vm the total volume and n the number of kmoles in the volume V. They increase and reduce
pressure, respectively. Table 1 gives for some gases the numerical values of
the two constants. When a and b are zero, then the van der Waals
equation degenerates to Boyle's law. To calculate p, (3) can be rewritten:
p = nRT/(Vm-nb) - an2/Vm2, (3b)
With normal temperatures and pressures of about 100
bar or more, the Van der Waals correction makes sense. For instance, a tank
filled with air 300 bar and 290 K comprises 7.8% less. (assumed that aair = 37.4x10-3).
At 200 bar the interaction effect dominates the particle-volume-effect, but at
300 bar the situation is reversed. The p-V diagram of Fig. 2 also illustrates
the rather complex behavior of the correction. Since Boyle’s law is independent
of the type of particles, the straight line of Boyle (log-log diagram) holds
for both air and helium.

Fig. 2
Comparison of p/V relation according to the Law of Boyle and according
to the Van der Waals equation for air and He. The curves are calculated for n = 0.1 kmol and T = 300 K (1E4 = 10!4).
The Van der Waals curve of He shows already strong deviations (about
10%) from Boyle’s law at 100 bar, since the interaction effect is weak compared
to the particle-volume-effect. The p-V curve approaches the straight Boyle line
from above, but the air-curve first crosses the Boyle line and then approaches
the line from below. For low pressures the Boyle line is the asymptote for the
Van der Waals curves. The rather surprising behavior of the Van der Waals
equation is due to the fact that it is a cubic equation in n and in V.
For very precise calculations in gas mixtures at
pressures beyond 50 bar, this correction is even not precise enough. Then, the
theory of virial coefficients, taking also into account the (first and higher
order) interactions between the types of particles in a mixture (), is applied
(see textbooks of physics).