1 Introduction
The high compression of matter is of great importance in many science and engineering fields, such as inertial confinement fusion [
1,
2], high energy density physics [
3], high-pressure science [
4], Z-pinch experiments [
5,
6], and laboratory astrophysics [
7]. The method for compressing materials is divided mainly into dynamic impact compression and quasi-static compression. In inertial confinement fusion, an ultra-strong laser-driven shock wave is used to compress fusion fuel to 1 000 times solid density.
The thermodynamic quantities of a substance, such as temperature
T, pressure
p, and internal energy
U change with the change in density
ρ during the compression process. These changes are not only related to the equation of state (EOS) of the material being compressed, but also to the specific compression method selected. Taking shock compression [
8-
10] as an example, for a uniform gas system in the same initial state, the gas density can be compressed by a factor of three by applying a strong shock, or the same compression ratio can be achieved by sequentially loading two or more weaker shock waves. At the same final
ρ value, the
T and
p values obtained from multiple shocks will be significantly lower than those produced by a single shock. The quasi-static compression process can be regarded as a continuous compression of numerous weak shock waves; therefore, the increase in
T and
p values is the smallest of all the adiabatic methods.
Can we find another compression path in which the pressure increase is even slower than in a quasi-static compression? Previous theoretical work, conducted by Geyko
et al. [
11], studied the compression process of a spinning ideal gas and found that the
p-increase of the ideal gas in a spinning system during quasi-static adiabatic compression was lower than that in a stationary system, indicating the improved axial compressibility of spinning gas. The reason for this result is that the energy of external pdV work can be stored in the rotational kinetic energy
Er during compression, and the increase in
T for spinning gas is less than that of stationary gas.
The axial compression process of a spinning non-ideal gas with an EOS of virial expression was also studied, using theoretical analysis and numerical calculation methods. A nonrelativistic spinning gas with an angular velocity
ω was confined in a long cylinder with radius
R and length
L. In order to simplify the problem and obtain analytical results, the following three assumptions were adopted in the previous theoretical work of ideal gas conducted by Geyko
et al. [
11]: (i) the cylinder is long enough (
), so that end effects are negeligible, (ii) the wall of the cylinder is smooth, so that angular momentum is conserved during the compression process; and (iii) compression is a slow and adiabatic process, so that the gas always remains close to equilibrium. All the above assumptions in the previous work have been adopted in this work, so that it is possible to compare the compression behavior of non-ideal gas and ideal gas under the same condition.
The axial pressure of ideal gas in a cylinder will not be affected by the rotation of the system, as long as the temperature and average density remain the same [
11]. Unlike the behavior of ideal gas, it has been found that rotation causes the initial axial pressure of non-ideal gas to be higher than that of the corresponding stationary system. Nevertheless, the axial pressure of the spinning gas will be lower than that of the stationary gas when the compression ratio
η is large enough, since the temperature of the spinning gas increase at a slower rate during continuous compression. The behavior of pressure and temperature in gases with different forms of interaction potential energy were compared to illustrate the effect of gas models on gas compression characteristics. The results of this work ratify the conclusion that gas improved compressibility under axial compression.
When verifying the effect of spinning-induced compressibility improvement in real gases, consideration must be given to more complex situations, such as non-equilibrium processes in dynamic compression. Such verification work can be undertaken using numerical simulation methods, such as hydrodyanmic simulation [
12], discrete lattice Boltzmann methods [
13-
16], and molecular dynamics methods [
17].
In the remainder of this article, a theoretical analysis of the spinning non-ideal gas is presented in Section 2, the numerical results and discussion are in Section 3, and Section 4 presents a short summary of the entire work.
2 Theoretical analysis
The EOS of simple gases can be written in the form of a virial expansion [
18],
in which p is pressure, kB is the Boltzmann constant, T is temperature, n is particle number density, and B and C are the second and third virial coefficients, respectively. When the density of gas is not very high, the many-body interaction will be far weaker than the pair interaction in the system. Therefore, only the second virial term in the EOS is retained in this work and Eq. (1) can be simplified as,
Using isothermal approximation, we have
The balance between centrifugal force and the pressure difference dp obtained
The above equation demonstrates different asymptotic solutions for rare and dense limits. For the rare case (
), the term
in Eq. (4) can be ignored, and Eq. (4) becomes the same as the ideal gas equation, whose solution was given by Geyko
et al. [
11] and exhibits an exponential growth with
r2, as follows:
where n0 is the particle number density at . For the dense case (), the solution of Eq. (4) tends to
indicating a linear growth of with r2.
In order to simplify the calculation and obtain the key dimensionless parameters of this problem, the dimensionless equation in Eq. (4) can be derived as
in which
nc is the critical number density of the system,
is dimensionless number density,
is dimensionless radius whose range is
,
ξ is the dimensionless second virial coefficient and
correspond to the ratio of spinning kinetic energy at the boundary to the thermal kinetic energy [
11]. Integration of Eq. (7) can be written as
where is the dimensionless number density at and should be determined using the equation of normalized condition equation:
The analytical solution of can be expressed as
where
is called the Lambert W function [
19] or the product log function, which is the inverse function of
. The distribution of
can be solved numerically by combining the simultaneous equations in Eq. (9) and Eq. (10). The non-uniform distribution of the number density will result in a non-uniform distribution of pressure, according to Eq. (2), and the average pressure on the two end faces of the cylinder (hereinafter referred to as “axial pressure”) can be expressed as follows:
Now we consider a small axial compression of the system, which causes the length of the cylinder to change from L to . The change in L will result in a corresponding change in ξ and , and the new value of ξ after compression can be obtained directly from Eq. (8) and written as
in which, and are the new values of the second virial coefficient and average number density, respectively, after small compression. The determined value of depends on the temperature after compression and the model of interaction between gas molecules, which is discussed in the following section.
The determination of new after compression is much more complicated, because the change in will be affected by both T and ω, while the change in T and ω should satisfy the conservation laws of angular momentum and energy during axial compression.
The total angular momentum of the system can be written as
and the conservation of angular momentum () can be written as
where and are the angular speed and dimensionless number density distribution after compression, respectively.
Before giving the energy conservation equation during compression, dicussing the relationship between the total energy E and the system’s state parameters is necessary. For an ideal gas, the internal energy U is only related to temperature T, so the total energy can be written as , where cv is the specific heat, the first term corresponds to the internal energy, and the second term corresponds to the rotational kinetic energy. However, for non-ideal gases, the internal energy of the system includes not only the kinetic energy of the thermal motion of the molecule Et but also the potential energy of the interaction between the molecule’s Ep.
Directly giving an analytical expression of Ep for non-ideal gas using the thermodynamic parameters of the system is difficult because only the relationship between p and the thermodynamic state quantities (n and T) are known. For adiabatic processes only (TdS = 0), dU = -pdV can be obtained, and the change in internal energy and pressure can be directly related to the equation . During the compression of spinning gas, although the total heat of the gas in the cylinder , heat conduction between different parts of the gas occurs due to the non-uniform distribution of , which makes the adiabatic conditions fail in the spinning system.
Modeling the form of Ep to continue the calculation is necessary. The simplest choice for potential energy models is to ignore Ep (), so that the internal energy of non-ideal gas exhibits the same form as the ideal gas. Considering that this model is too simplistic to reflect the influence of Ep on the compression process, we propose that the potential energy density of the system is equal to the virial pressure pv, as pv exhibits the same energy density dimension. Pressure can be divided into two parts: pt and pv, where is contributed by the thermal motion of the particles, and pv is contributed by the interaction between the particles, which can be obtained by . From this point on, the model of is qualitatively reasonable.
The conservation of energy during compression can be expressed as , where the work can be approximated by a trapezoidal integral as when compression is small, and dE corresponds to the change of energy during compression. Substituting specific expressions for each part, the expression of total energy is
and the conservation of energy can be rewritten as
Solving the simultaneous equations of Eqs. (15) and (17) using a iterative algorithm, the new value of and after compression can be determined. Meanwhile, the distribution of density and pressure can be obtained.
Since a continuous compression process with a large compression ratio η can be decomposed into a serious of small compression processes, the variation of each physical quantity during a continuous compression can be obtained through the cyclic calculation of the small compression process.
3 Numerical results and discussion
3.1 Compression with constant B
Strictly speaking, the second virial coefficient B is a function of temperature and will change with a change in T during compression. Here, for simplicity, we assume that B is a constant. The effect of temperature on B will be discussed in the following subsection.
The first significant difference between a spinning non-ideal gas and a spinning ideal gas is that the initial axial pressure in a non-ideal gas is affected by the density distribution. For an ideal gas, when temperature is uniform and determined, the average pressure
is only related to the average density and not to the density distribution in the r direction, as described in previous work [
11]. However, for a non-ideal gas, the virial part of the pressure
pv is proportional to
n2, and the non-uniform distribution of
in the rotating system will result in a larger average pressure as the second term in Eq. (12) if B is positive. That is to say, for virial gas under the same temperature and average density, a larger pressure is required to compress the spinning gas than to compress the static gas, and the spinning gas appears to be more difficult to compress when the compression is not started.
Here, the ratio of to is used to indicate the increase in pressure caused by rotation, in which and are the average axial pressure in the spinning and static system, respectively. The relationship between the pressure ratio and the two dimensionless parameters ξ and are shown in Fig. 1. It is found that, when ξ is constant, the value of increases as increases, indicating that a faster rotation leads to a greateer pressure difference. This phenomenon can be explained by the fact that faster rotation results in a greater inhomogeneity of density distribution, which could be derived from Eq. (11).
Meanwhile, the curve of the pressure ratio is not monotonous as ξ increases when is constant. It should be noted that there are two preconditions for the existence of pressure difference between spinning and static systems, one is the virial term in the pressure formula, and the other is the inhomogeneity of density distribution caused by rotation. The proportion of pv in the total pressure will increase as ξ increases, which causes an increase in . Although the density distribution non-uniformity will decrease with an increase of ξ, the same density difference leads to a greater pressure difference in the case when ξ is larger, which in turn reduces the value of . Under these two competing mechanisms, the curve reaches its maximum value when ξ is moderate.
Next, we study the differences in the pressure behavior of the spinning system and the static system during continuous compression. The change in pressure ratio with compression ratio η is illustrated in Fig. 2. When initial is the same, it is found that monotonically decreases with increasing η and is less than one when η is larger than a certain value, indicating that the axial pressure of spinning gas is lower and that spinning gas exhibits an improved compressibility in the latter stages of continuous compression. In addition, it has been found that the effect of compressibility improvement caused by rotation gradually decreases as ξ increases.
The main reason that in spinning gas increases at a slower rate than in static gas during the compression process is that part of the external pdV work can be stored in the rotational energy Er in the spinning system, making the temperature rise at a slower rate, as illustrated in Fig. 3. It can also be seen in Fig. 3 that the rise in temperature during compression is reduced as ξ increases. This result could be explained by the fact that a larger ξ means that the proportion of total energy that is potential energy is greater, and a larger part of the external pdV work is converted to Ep during compression.
The percentage of external pdV work converted to thermal, rotational kinetic, and potential energy during continuous compression, which were presented as , , and , respectively, are illustrated in Fig. 4 with a different initial and .
When is the same, it was found that and decrease as increases. While increases as increases. Meanwhile, when is the same, increases as increases, indicating that is positively related to the proportion of potential energy in the system energy. When the interaction of gas molecules is dominant (taking the example of a case with ), almost all of the pdV work is converted to potential energy, which explains why the temperature rise is so small, as illustrated in Fig. 3(c). Besides, both and decrease with an increase in the compression ratio during the compression process, as the value of ξ increases when η increases.
3.2 The effect of B(T)
According to the relevant theory of statistical physics [
18], the second virial coefficient B can be written as
where
is the potential energy of the pair interaction. Therefore,
B is not only a function of temperature, but it is also related to the form of the pair interaction in the system. Assuming that the pair interaction potential between gas molecules exhibits the form of
(
m>3), the analytical form of B(T) can be expressed as [
18]
where is the Gamma function. It has been found that B(T) is inversely proportional to the 3/m power of T, indicating that high temperatures will weaken the contribution of pair interactions between gas molecules to the virial component of pressure. The previously considered case, where B is constant, could be regarded as a case whose value of m tends to infinity.
The axial pressure ratio curves, during an adiabatic compression with different and a different form of B(T) are plotted in Fig. 5. The value of B is proportional to when m = 3 and the correlation between B and T weakens as m increases. Under the same initial conditions (, , and B0), the comparison of the axial pressure ratio curves with different forms of B(T) shows that will increase as m increases, indicating that the spin-induced compressibility improvement effect is more significant for gases with a larger m.
It should be noted that this does not mean that the smaller m is, the more difficult it is for the system to be compressed. The actual situation is just the opposite. If the temperature changes during the compression process are the same, the value of B in the gas with a smaller m will be less than that in the gas with a larger m, thereby making it easier for the gas to be compressed.
The suppression effect of B(T) on pressure works in both spinning and stationary gases. According to the previous calculation results, it is known that in the stationary system during the compression process is larger than that in the spinning system. Therefore, the suppression effect of B(T) on the pressure during compression is more obvious in the stationary system, resulting in a smaller and a larger pressure ratio in the gas with smaller m.
The effects of B(T) on the variation in temperature during compression are illustrated in Fig. 6. It has been found that the temperature ratio decreases monotonously as η increases in all cases, indicating that the temperature rise in spinning gas is slower than that in stationary gas. In addition, for gas with smaller m is less than that for gas with larger m, indicating that the suppression effect of B(T) on the temperature increase is more significant when m is smaller.
4 Summary
The compressive features of spinning non-ideal gas were investigated using theoretical analysis and numerical calculations. The interaction between the gas molecules causes the spinning gas and the stationary gas to exhibit different initial pressures at the same initial temperature. The analysis of non-ideal gases with various initial parameters in this study shows that, even if the initial pressure of the spinning gas is larger than that of the stationary gas, the temperature rise of the spinning gas is smaller than that of the stationary gas during a continuous quasi-static adiabatic axial compression. This ensures that, when the compression ratio is greater than a certain value, the pressure of the spinning gas is lower than that of stationary gas. The findings of this study verify the robustness of the spin-induced compressibility improvement effect in non-ideal gas. In addition, the effects of B(T) on pressure and temperature during compression were investigated.
The compression ratio considered in this work is based on the average density in the cylinder. For spinning gas, compression caused by centrifugal force along the radial direction is also present, so the highest density in the spinning gas is much larger than the average density nc. The corresponding physical picture is that a high-density shell structure is formed near the cylindrical surface. Compared with a uniform system, this shell structure exhibits a larger area density , and the increase in may correspond to a stronger particle stopping power. The high areal density is a key condition for inertial confinement fusion to achieve ignition. In addition, the device of the Z-pinch experiment is also cylindrical, and one of its goals is to compress high-temperature plasma to an extremely high density and areal density. The compressive feature of spinning gas may exhibits potential value for the design of the Z-pinch scheme.
Higher Education Press and Springer-Verlag GmbH Germany, part of Springer Nature 2020