q1r iterative procedure furnish good approximate expressions and we shall proceed on that assumption. Actually we shall be content here with only the first step in that procedure and therefore we calculate Aa@ )4y and insert it into (7.16)4,5,6. In this calculation in order to simplify the resulting expressions we use the equations (7.16)1,2,3 in the form (7.20) v’,, = 0, h,,, T*’ 1 E$ = 0, u, T*p 1 E,fl = O, as is appropriate
t&
for the first iterative step. Thus we obtain
=g
(nm2- Cy)[h;hp,y,,)]. 3
2
(U=C qP 6TB,
f T,a - 4 VU,,, c
)I
(7.21)
In obtaining (7.21)2, we have used the relation (A. 11) from the Appendix. Among these first iterates the equations (7.21),,2 are easily recognized as the relativistic versions of the laws of Navier-Stokes and Fourier respectively that were first derived by Eckart. This interpretation identifies the coefficients of the square brackets as viscosity p and heat conductivity K. We must recall that in relativity the expression h;( l/T T,, - l/c2 tY’Uor,y) plays the role of the “thermodynamic force” for heat conduction. The equation (7.21), relates the dynamic pressure to the divergence of
RELATIVISTIC
THERMODYNAMICS
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209
velocity and the coefficient of ,U6,a must be interpreted as the bulk viscosity v of the gas. If we introduce the state functions (4) we obtain more specific forms for p, K and v viz. /l=471yu=471y--
m6c7
I
15TB3 6*o -m6c7 D3
3T=&
4.0
+ -;nkTG 3
+ k nmk(y + 5G - yG2) 4
(7.22) nm2c2
+3j@
l-f-+&-G= Y2 Y
The second members of these equations refer to the non-degenerate limit a + co. Note that the relations (7.22) offer a possibility to determine the unknown functions BT(n, T), B,(n, T) and B,(n, T) from measurements of viscosity, heat conductivity and bulk viscosity. We conclude that extended thermodynamics contains Eckart’s ordinary thermodynamics as an approximation. 7.6. Comparison with older Theories of Extended Thermodynamics, notably the Theories of Miiller [2] and Israel [3]
Miiller’s paper was written when linear irreversible thermodynamics’ was the only systematic thermodynamic theory of non-equilibrium and it was within this theory that he derived his results. We change the notation of Miiller’s equations ([2] 6.28) through ([2] 6.30) so as to make it conform to the notation of the present paper and write these equations in the form
qr = KTh”P II=
LT T ,a--tUYJ,, c2
+ kjm + MD,, - Nt,,P>.,
(7.23)
-v[U~,~ + Gil+ Mqq,].
k stands for U”R*,. Israel’s equations ([3] 14) are identical to these except for notation. Comparison of (7.21) and (7.23) shows that Miller’s and Israel’s results differ from Eckart’s by the terms with the coefficients A, B, C and M, N. Nothing specific can be said about these 5 coefficients from thermodynamic arguments even if we wish the equations (7.23) to apply to an ideal gas. In particular, there is no relation between the five coefficients A through N and the thermal and caloric equations of state of a degenerate gas. It is tempting to assume that the 9 equations (7.23) of the old theories corres’ Sometimes called TIP for thermodynamics or irreversible processes.
210
LIU,
MtiLLER,
AND
RUGGERI
pond to the 9 independent equations (2.2)3 or (7.16)4,5,6 of the present theory when the representation (4.3)2 is introduced. And indeed that assumption is valid, even though only approximately. Insertion of (4.3), into the equations (7.16)4,5,6 gives after some calculation
c2(nm2 -
t
Cy) h;ht
I
(7.24)
where the brackets ( ) and ( } in (7.24)2,3 are equal to the corresponding brackets in (7.21),,,. The equations (7.24) are approximate, because in their derivation all terms of the general form flUp,,, nn,,, 17e,,, qa Up,,, qorn,y, qae,?, tcap> Up,,, t<,,g,,, tcor8>e,, have been ignored. Such terms would have been ignored by Miiller and Israel, if in fact they had appeared in their work, because they would have considered them as non-linear. Comparison of (7.23) and (7.24) reveals strong similarities between the two sets of equations. There is one difference though which makes the equations (7.24) of the present theory superior to the equations (7.23) of the old theories. Indeed, in (7.24) all coefficients in the square brackets are explicitly known to within one function of a single variable, see (7.7). Thus, while the old theories contain the eight unknown functions ~1,rc, v, A, B, C, M and N of two variables each, the present theory contains only three unknown functions of two variables, viz. B;, B,, B, plus one unknown function of a single variable. In addition, of course, the new theory contains a number of explicit non-linear terms which had formerly never appeared. Another difference between the sets (7.23) and (7.24) is only apparent. The factors of qcm,sj and - t<,~>,8 in (7.23),,2 and the factors of n,, and qb,a in (7.23),,, are the same ones while this is not obvious for the corresponding factors in (7.24). However, the alternative forms of A; and A! given in (7.8),,, guarantee the same relation between those pairs of factors as in (7.23).
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Inspection
THERMODYNAMICS
211
OF GASES
of the equations (7.24) shows that the three coefficients
71 5c3-~~m2-~)~~=4~~2m6~~
--
3
B.4
c2 c; --= 6 B;
D,
A4
BJ,.,
’
2m6c7
-4ny 7
(7.25)
0; e12.1
z2,2
z2,2
z2,3
I A;*
B;
are to be considered as relaxation times for t<“‘), q” and 17 respectively. Note that the inequalities (7.9) ensure the positivity of these relaxation times. The second members in (7.25) are derived by use of (7.7) and (7.8). 7.7. The Non-Relativistic Limit for a Non-Degenerate Gas
The non-relativistic theory of extended thermodynamics with 14 variables has been formulated by Kremer C7.183. In that theory the variables are given by nonrelativistic moments of up to fourth order. It is therefore not obvious how the present theory, which uses only first and second order moments, is related to the non-relativistic one. Dreyer & Weiss C7.193 have investigated this question and they have found complete agreement between the weakly relativistic limit y B 1 of the present theory and Kremer’s non-relativistic theory. In the process of comparing the two theories Dreyer & Weiss were able to determine the orders of magnitude of the functions B;, B, and B, that remain unknown in the present paper. They grouped all quantities according to their “relativistic order of magnitude” as O(y), O(l), 0(1/y) etc. and they found that in case of the non-degenerate gas we have’ (i) B;isofO(l) (ii) B, is of O( 1)
(iv) CT tends to -6--
m2 1
(7.26)
kTy
z Kremer’s theory contains two arbitrary constants which we have taken to be zero in (26), because they vanish in the kinetic theory of gases.
212
LIU,
MijLLER,
AND
RUGGERI
From (i) it might seem that the bulk viscosity v in (7.22) were of O(l), but this is not so. In fact, on the contrary, the factor of l/B; in (7.22) is of @(l/y*) so that v vanishes in the non-relativistic case as is to be expected for an ideal gas. The viscosity and the heat conductivity are both of U(1) as can be seen from (ii), (iii) and (7.22). APPENDIX
A.l. Evaluation of Entropy Principle, The vector h’* that determines V”, of the Lagrange multipliers 5, /i, corresponding constitutive function transformations i.e. we must have
The general solution of this functional
Symmetry Conditions and Trace Condition
Y@ and A@? according to (5.7), is a function and ,Z’,,. By the principle of relativity the must be isotropic with respect to arbitrary
equation is given by the representation
A=0
where ,4cA)= (ZA),Bns has been defined with Z$ = gaS and where the coefficients yA may be Rnctions of the scalars <, GA=A”AkA)(A=O,
1, 2, 3), Qi= (Zi+‘)OLa (i= 1, 2, 3).
We insert (A.2) into the equations (5.7),,,,, and apply the requirement that 7@ and AaBy be symmetric as well as the requirement (2.3)2 on the trace of 4. These requirements severely limit the generality of the coefficient functions ya in (A.2). In fact, if we are interested to have & to within third order terms in g the coefficients ?A must be calculated so as to contain C in up to (3 - A)th order and these read
Y*=r*+ac,G
ar,
1 a*r, ar3 ar2 YI=rl+~G’+Z~G:+dC,G,+~r,Q, ar,
1 a*r,
ar,
i
(A.31
i
Yo=ro+ac,G’+Z~G:+acoG,+4r2Q,
1 a*r, p-C:+ +zaG:,
a*r, -G,G,+~G,+t~G,Q~+~r,e*, aG; 0
0
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213
where the rA are functions of 5 and GO which can be shown to satisfy the differential equations.
&
(G;T,)
=f
(m*c*G;r,)
0
&(G~r2)=$z2c2G;r,)
(A.41
0
j$ (GV,)=-$(m*c*G;r,) 0
In conclusion we may say that the constitutive functions for ha, v*, T”fl and AaBy are now specific except for the unknown function r,(<, Go) and functions of < which emerge as constants in the integration of (A.4). A.2. Determination
of rA
The evaluation of the entropy principle was much simplified by the choice of the Lagrange multipliers 5, ,4’ and ,PB as variables. However, since these multipliers have no a priori significance, we should much prefer to state our results in terms of the original variables V”, T”fl of Chapter 2 or, even better, in terms of the suggestive variables n, e, Z7, qp, t(““> of Chapter 3. The first step in that transformation is effected by equating
(A.51
to the equilibrium
expressions implied
by (5.7),,2,j and (A.2), (A.3), viz.
are /ialE.
are hOLIE=- tag+2GOdco
>
214
LIU,
It follows by some calculation
MijLLER,
AND
RUGGERI
that we have
which identifies &,/c as the reciprocal of the absolute temperature T. Moreover, we obtain an interpretation of the equilibrium values of the Lagrange multipliers t 1E, /i a 1E in terms of IX and T, namely
(A.81 The second part of (A.7) follows from (7.4),. We conclude that g IE is closely related to the Gibbs free energy g = l/n(e +p) - Ts and to the variable a which occurs in the equilibrium state functions (7.4),. Finally the comparison of (A.5) and (A.6) gives
adGo at
q/Gko
= cn,
=o
ar, -- c3 co @)= JG,3 I7
e
z-o= -p
(A.9)
=x’
r,= -2 %
nm2 - Cy)
3&
of which the latter two equations imply an integrability
condition
for Cy, viz.
‘(e+p).
(A.ll)
The key to the further treatment, and indeed to the whole procedure of this paper is the observation that the knowledge of n(a, T), p(a, T) and Cy(a, T) from equilibrium statistical mechanics (see (7.4),,,,d) allows us to calculate r. and f1 from (A.9)3 and (A.10)2. The remaining functions r2 and r3 may then be calculated integrating (A.4). Frequent use of the recurrence relations (7.6) finally provides the solutions To(a, T) = 47ty q
m4c5J4,0
Tl(a, T) = 47cy 2
m6c7z6&,
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THERMODYNAMICS
215
OF GASES
+pw+w 2 y6
-
y*
(A.12)
The functions A(a), B(a) emerge as constants of integration. A.3. Constitutive Relation for Aa@ as a Linear Function of II, qa and t<@) Insertion of rA from (A.12) into the formulae (A.3) for ya and insertion of those into the representation (A.2) gives h’” and by differentiation we obtain AaPY according to (5.7). However, there is a drawback, because the AmBythus calculated is still a function of the Lagrange multipliers 5, /i, and Z,,. To be sure, in the previous section we have identified the equilibrium values of the Lagrange multipliers and we obtained
So now we have to calculate non-equilibrium values of the Lagrange multipliers. We shall be forced to limit the attention to linear departures from equilibrium and write
(A.13)
The quantities x, Aa, 1, a(@), ca and c are considered so small that products may be neglected. A’, cra and a(@) are normal to V and o(OLB>is trace-less. We write (5.7),., with (A.2) and obtain with (3.2) and (3.10) and by dropping non-linear terms in C:
+ 22
(nYPyn, 0
595/169/l-15
+ A!rYAy).
(A.14)
216
LIU,
MtiLLER,
AND
RUGGERI
On the right hand side we introduce (A.13), dropping all non-linear terms in 1, A”, i, o
4ny 27 zz -- 3 ‘=G4m”c7
0; 6 I,,,
I,,, I ’
1 12,1 I,,2 D; 6 I2,2 12,,I ’
(A.15)
In the next step we calculate a linear constitutive relation for A,,, as follows. We write the linear part of (5.7), with the coefficients yA inserted from Section A.l. Thus we obtain
+
+g= (A,A&JS
+ Ll,n,c,,n~ + flyAaCpsA~).
(A.16)
0
We insert (A.13) with (A.15) and, again dropping all non-linear terms, we arrive at an explicit expression for A,,, which contains but one unknown function of a single variable, viz. A(a). Comparison of that expression for A.,, with the representation (4.3), identifies the coefficients C;, C3 and Cg. The results have been listed in Chapter 7, see (7.7).
RELATIVISTIC
THERMODYNAMICS
OF GASES
217
A.4 The Entropy-Entropy
Flux Vector and the Entropy Production The equations ( 5.7)1,2,3 may be combined in the form dh’” = V= d[ + T@ d/i, + A@ dC,
By use of (5.3) this relation entropy-entropy flux vector
(A.17)
may be converted into a differential
dh*= -
form for h”, the (A.18)
We replace Vu and 7’@ by their decompositions (3.2) and (3.10) and insert the representations (4.3)* and (4.3), for AmByand h”. Moreover we introduce the linear expressions (A.1 3) with (A.1 5) for r, /i, and L’,,. In this manner we obtain a differential form in dZ7, dq” and dtCru> on both sides of (A.18). Comparison of coefficients then identifies the coefficients A; through Ai in (4.3),. The results have been listed in Chapter 7, see (7.8). Thus we have obtained explicit expressions for the entropy density (A.19) and the entropy flux (A.20)
Note that the entropy density contains non-equilibrim contributions which are quadratic in U, q” and t<@). The coefficients A;‘, AT and Ai of these terms will be shown to be negative by the hyperbolic argument of Section A.5 below, thus ensuring that the entropy assumes its maximum in equilibrium. Note also that the entropy flux is not just equal to the heat flux divided by temperature, rather it contains two quadratic contributions. The residual inequality (5.7), can be written more explicitly by use of the linear representation (4.3), and of the decompositions (A.13),. We obtain for the entropy production ;=
12B;on-2B,o”q,-B,~(“P>t(,B>
20
(A.21)
or by use of (A.15)
n2
+ - 3 B4 z4,0 Tg--4%ol+y--mc 4zyD3
15 B, 1 tt 20 2m c 4rty Z6.0 (A.22)
218
LIU, MULLER, ANLI RUGGERI
We conclude that there are three “mechanisms” for entropy production. One is related to the dynamic pressure, one to heat flux and one to shear stress. For the entropy production to be non-negative the coefficients By, B,, and B, must satisfy the inequalities that were listed in (7.9), . Inspection of (A.22) confirms this statement. AS. Some Consequences of Hyperbolicity In the requirement (6.7) of hyperbolicity we replace I/*, Fp and A’/? by their representations (3.2), (3.10) and (4.3),. Also we introduce the linear expressions (13) with (15) for 5, /1, and C,,. In this manner the left hand side of the inequality (6.7) becomes a quadratic form in the variations an, 6T, 6U”, SIT, 6qP, &(P”). Since the inequality must hold for arbitrary values of these variations, the coefficients of (&I)~, (6T)2, @If)‘, 6q’dq,Jt<“‘> 6t<,,> must be positive. This requirement leads to the conditions that have been listed in (7.9),, if we make use of the explicit form (7.8) for the coefficients A$, A? and A:. However, the conditions (7.9), do not exhaust all consequences of the requirement of hyperbolicity. Indeed, some of the remaining consequences impose bounds on the values of rc, qa and t<@) in terms of values of n and T. As long as we stay close to equilibrium, these constraints will be satisfied but they cannot hold far from equilibrium. This situation is not different from the non-relativistic case investigated in [ 171.
ACKNOWLEDGMENT One of the authors (I-S.L.) gratefully acknowledges the support of the Humboldt Foundation.
REFERENCES 1. C. ECKART, The Thermodynamics of Irreversible Processes III: Relativistic Theory of the Simple Fluid. Phys. Rev. 58 (1940). 2. I. MOLLER, Zur Ausbreitungsgeschwindigkeit von Storungen in kontinuierlichen Medien. Dissertation TH Aachen (1966). 3. W. ISRAEL, Nonstationary Irreversible Thermodynamics: A Causal Relativistic Theory. Annuls of Physics 100 (1976). 4. I-SHIH LIU, Method of Lagrange Multipliers for Exploitation of Lagrange Multipliers. Arch. Rational Mech. Anal. 46 (1972). 5. T. RUGGERI, Symmetric hyperbolic system of conservative equations for a viscous-heat conducting fluid. Acta Mech. 47 (1983). 6. N. A. CHERNIKOV, The Relativistic Gas in the Gravitational Field. Acta Phys. Polonica 23 (1963). 7. N. A. CHERNIKOV, Equilibrium Distribution of the Relativistic Gas. Actn Phys. Polonica 26 (1964). 8. N. A. CHERNIKOV, Microscopic Foundation of Relativistic Hydrodynamics. Acra Phys. Polonica 27 (1964). 9. C. MARLE, Sur l’l?tablissement des Equations de I’Hydrodynamique des Fluides Relativistes Dissipatives. Ann. Inst. Henri PoincarC 10 (1969).
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10. G. M. KREMER, Zur erweiterten Thermodynamik idealer und dichter Gase. Disserration TU Berlin (1985). 11. K. 0. FRIEDRICHS AND P. D. LAX, Systems of Conservation Equations with a Convex Extension. Proc. Nat. Acad. Sci. 68 (1971). 12. G. F. SMITH, On Isotropic Integrity Bases. Arch. Rarional Mech. Anal. 18 (1965). 13. C. C. WANG, A New Representation Theorem for Isotropic Functions: Answer to Professor G. F. Smith’s Criticism of my Paper on Representations for Isotropic Functions. Part I: Scalar Valued Isotropic Functions. Arch. Rational Mech. Anal. 36 (1970); Part II: Vector Valued Isotropic, Symmetric Tensor Valued Isotropic, Skew-Symmetric Tensor Valued Isotropic Functions, ibid. 14. F. J~TTNER, Das Maxwell’sche Gesetz der Geschwindigkeitsverteilung in der Relativitatstheorie. Annalen der Physik 34 ( 1911). 15. F. J~~TTNER, Die relativistische Quantentheorie des idealen Gases. Zeitschriff 1: Physik 47 (1928), 542.
16. W. DREYER, Statistical Mechanics of a Relativistic Gas in Non-Equilibrium (in preparation). 17. I-SHIH Ltu AND I. MILLER, Extended Thermodynamics of Classical and Degenerate Ideal Gases. Arch. Rational Anal. 83 (1983). 18. G. M. KREMER, Extended Thermodynamics of a Gas with 14 Moments (in preparation). 19. W. DREYER AND W. WEISS, The Classical Limit of Relativistic Extended Thermodynamics (in preparation).