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Scaling behaviour of the fluid subclass near the liquid-gas critical point
Y. Garrabos
To cite this version:
Y. Garrabos. Scaling behaviour of the fluid subclass near the liquid-gas critical point. Journal de
Physique, 1986, 47 (2), pp.197-206. �10.1051/jphys:01986004702019700�. �jpa-00210196�
197
Scaling behaviour of the fluid subclass
near the liquid-gas critical point
Y. Garrabos
Laboratoire des Interactions Moléculaires et des Hautes Pressions, C.N.R.S., Université Paris-Nord, Avenue J. B. Clément, 93430 Villetaneuse, France
(Reçu le 25
mars1985, révisé le 20 septembre, accepté le 1 er octobre 1985)
Résumé.
2014Nous proposons des transformations d’échelle
nonuniverselles pour les deux variables physiques
mesurant les distances
aupoint critique liquide-vapeur d’un fluide pur le long de
sonisochore critique et de
sonisotherme critique. Après avoir effectué
cestransformations d’échelle,
nousobservons des comportements singu-
liers uniques pour tous les fluides purs proches de leur point critique liquide-vapeur.
Abstract.
2014Non-universal scale transformations
areproposed for the two relevant physical distances to the liquid-
gas critical point along the critical isochore and critical isotherm. These scale transformations allow
usto observe
an
identical singular behaviour for all pure fluids
neartheir liquid-gas critical point
J. Physique 47 (1986) 197-206 FTVRIER 1986,
Classification Physics Abstracts
64.60F
1. Introduction.
In
aprevious article [1], a phenomenological method
was developed to determine the asymptotic singular
behaviour for
apure fluid at equilibrium near its liquid-gas critical point. The following introduction
gives a brief account of the main assumptions and
results of the method before defining the singular scaling behaviour for the pure fluid subclass.
The basic input data are the four critical parameters
Pc, Tc, Pc. and y§. Pc, Tc and Pc are, respectively, the
critical pressure, temperature and density. y’c is the limiting slope at the liquid-gas critical point common
to the pressure along the critical isochore above the critical temperature and to the vapour-pressure curve below the critical temperature. These parameters define the location of the liquid-gas critical point
in the P, p, T diagram and of the tangent plane to the
characteristic surface f (P, p, T)
=0 at this point.
The basic input data are transformed into four
typical quantities as follows
m
is the molecular mass of the constitutive particle.
kB is the Boltzmann constant.
Thermodynamic properties and static correlation
functions of a known mass of
apure fluid are made dimensionless by expressing them in units of an
appropriate combination of and a (Eqs. (1) and (2)).
Pc and a are respectively an energy and a length
defined at the liquid-gas critical point.
As examples of interest for the notation used in the present study the order parameter, the ordering field
and the singular potential of the liquid-gas transition
are considered. The order parameter is related to the
density distance to the critical density while the ordering field is related to the distance to the chemical
potential on the critical isochore [2]. With our system of units, the dimensionless order parameter is given by
The dimensionless ordering field along the critical isotherm reads
where the chemical potential per particle p is the conjugate variable to the number density p/m. Jlc is the chemical potential per particle at the liquid-gas
critical point.
The dimensionless potential along the critical
isochore is given by [2]
where
Article published online by EDP Sciences and available at http://dx.doi.org/10.1051/jphys:01986004702019700
is the dimensionless relevant field related to the temperature distance to the critical temperature along
the critical isochore
Yc is the slope at the liquid-gas critical point of the
dimensionless potential given by equation (7). Zr
is the compressibility factor at the liquid-gas critical point.
Because of the way in which we use Yc and Zc,
we
recall brievely the two basic ideas of the pheno- menological method developed in reference [1].
We first obtain relations
where XlL) is the i-th non-universal leading amplitude
among the twelve amplitudes of the divergent pro-
perties of
agiven pure fluid in the approach to its liquid-gas critical point along the thermodynamic path (L) [2, 3].
Ten among the twelve equations (9) are predicted by the renormalization group theory (RG), [3] in the
form of ten universal ratios between the twelve ampli-
tudes X i(L). This prediction verifies the two-scale factor universality hypothesis for the (d, n) univer- sality class [4] (d and n are respectively the dimension
of space and order parameter). For the fluid subclass belonging to the (d
=3, n
=1) universality class,
universal ratios [5] may be rearranged [1] to read
where XJL) is one of the ten amplitudes related to ,+
and Dc selected as independent quantities. ,+ is the amplitude of the correlation length divergence along
the critical isochore in the one-phase region. DC is the asymptotic shape amplitude of the critical isotherm for the field conjugate to the order parameter. Taking
into account equations (10), two among equations (9)
are undetermined. In reference [1],
wehave assumed that these two equations relate separately ,+ and Dc
to the characteristic parameters Yc and Z, as follows [1]
v =
0.63 and 6
=4.815 are two universal critical exponents [6] associated with,ç+ and Dc respectively.
Hence, YG and FG are two phenomenological cons-
tants with the same numerical values for all pure
fluids, so that [1]
As a next step, the method presented in reference [1]
defines Yr and Z, as non-universal scale factors for the
measure of the physical distance to the liquid-gas
critical point of any pure fluid along its critical isochore and critical isotherm respectively.
The basic idea of (RG) is to assume analytical
relations between the relevant renormalized fields t * and h* for the 3-dimensional 0" model, and the corresponding physical fields of the system (S) [7].
We develop an approach analogous to the theoretical
one. We allow analytical relations between the relevant rescaled fields å1J* and AH* for the fluid subclass
scaling behaviour, and the reduced physical fields
iand Ah for each member of this subclass. These scale transformations read as follows
where T and Ah are respectively defined by eq uations (8)
and (6). We postulate that the exponenta y and
zhave the same numerical values for all pure fluids.
In reference [1], we only gave the explicit scale
transformation along the critical isochore. When the rescaled thermodynamic potential A-.i’* along the
critical isochore above the critical temperature is identified with AS defined by equation (7), we find again the form of equation (11) using the numerical
value y
=1 for the exponent y in equation (15).
The main purpose of the present work is to complete
these scale transformations by the phenomenological assignment of the numerical value
z= - 3/2 to the exponent
z.In section 2 we determine leading contributions to the fluid subclass scaling behaviour. They are entirely
defined by our choice for numerical values of the exponents y and
zand the constants YG and FG.
In section 3, we present the scaling behaviour of the rescaled isothermal susceptibility along the critical
isochore above the critical temperature using experi-
mental results for several pure fluids. Some interesting qualitative features are observed beyond the range of
validity of the asymptotic scaling behaviour.
In the same way, section 4 deals with rescaled form of the top of the liquid-gas coexistence curve below the critical temperature.
We conclude that the fluid subclass scaling beha-
viour can be governed by the same non-universal Y,,
and Zr scale factors at least up to the first order of the
non-analytical corrections in the Wegner expan- sion [8, 9].
2. Leading contributions to the scaling behaviour.
To formulate the scaling behaviour of the rescaled singular property X* we assume that
where Y* (L) is a function which only depends on the scaling distance Ax* to the liquid-gas critical point along the thermodynamic path (L).
The analogy between our phenomenological ap-
proach and the (RG) fundamental one requires an
asymptotic scaling behaviour which is entirely charac-
199
terized by the two scale transformations proposed
in the introduction
Equations (18) and (19) define the scaling distances
Ax* along the critical isochore and critical isotherm
respectively. Thus, leading amplitudes of the non- analytical contribution to equations (17) are inferred
from equations (11) to (14).
For instance, we consider the asymptotic shape
for the critical isotherm given by the scaling form
where 3cD is assumed to have the same numerical value for all pure fluids. AX* is the rescaled order parameter related to the dimensionless one by
Now,
werecall that the following asymptotic shape
of the critical isotherm
is assigned to each pure fluid [2]. When equations (19)
and (21) are substituted into equation (20) and the
result compared with equation (22), we obtain again equation (12). The relationship between the leading amplitude 3D and the phenomenological constant FG, (Eq. (14)), is given by
Applying the same reasoning to the scaling beha-
viour of the correlation length along the critical isochore above the critical temperature we find
where 3’ is the corresponding leading amplitude.
3’ and go are the basic independent variables for the twelve amplitudes of the fluid subclass scaling beha-
viour as ç+ and DC are the basic ones for the twelve
amplitudes of the non-universal behaviour of each member of this subclass. Consequently, the ampli-
tude 3(’) for any leading contribution to the function
Y*
onequation (17) is obtained by the universal form
while the universal equation (10) allows to calculate
XIL) from +’ and DC.
According to the assessment of the status of the fluid critical behaviour made by Levelt Sengers and Sengers [2], Sengers [10] and Moldover [11], the
isothermal compressibility and the shape of the top of the coexistence curve are properties for which experimental thermodynamic data in a more conven-
tional range and experimental optical data sufficiently
close to the liquid-gas critical point are available for
several fluids [2, 10-12]. In the next sections, a compa- rison is made using these data to test the validity of
our phenomenological conjecture presented here.
3. Scaling behaviour of the isothermal susceptibility.
In agreement with phenomenological equation (17),
the asymptotic scaling behaviour of the rescaled isothermal susceptibility S*T on the critical isochore above the critical temperature will be given by the scaling form
where y
=1.24 is the universal critical exponent [6].
The numerical value of the leading amplitude 3c is
determined by equation (25), so that
where Rx
=1.7, R
=Rç+ .(Rc)-l/d, (with R4+
=0.27
and Rc
=0.066, R
=0.668) are theoretical universal ratios [5]. Using results obtained by equations (24), (23), (13) and (14), we find
The relationship between the rescaled isothermal
susceptibility, 8*
=[1(Afl*)/I(AR*)], and the
dimensionless isothermal susceptibility, XT
=[ð(åm)/ð(åh)]T’ reads
In equation (29), X, follows from the reduction process of the isothermal compressibility, "T=p-l(ðp/ðP)T’
using Pc and a as proper units,
sothat
Thus the rescaled isothermal susceptibility on the
critical isochore above the critical temperature can be written in
amore convenient form as
since the isothermal compressibility is usually reduced by the critical pressure (K* T = xT PJ [2].
When the experimental values of the product Z, xT are plotted as a function of the scaling distance Yet, then the scaling equation (26) predicts that the
different curves K*(T) for each pure fluid should all collapse onto one single curve.
A plot of these experimental data for several pure fluids is shown in figure 1. Two distinct ranges on A-G*
are apparent depending on whether either the optical
or
the thermodynamic data are considered [10-12].
A detailled discussion of these experimental ranges
is given in references [10] and [11].
Fig. 1.
-Scaled isothermal susceptibility data for different pure fluids
as afunction of the scaling distance Yc
ialong the
critical isochore above the critical temperature (see text). Inset shows fitted results of K* T
versus ifor Xe, H20 and He using
the scaled equation of state of Levelt Sengers et al. [12]. For references and detailed discussion of original experiments
seereferences [2, 10-12].
The results of interferrometric measurements obtain- ed from gradient profiles in Xe, C02 and SF6 show
a single scaled behaviour in agreement with the
phenomenological asymptote (Eqs. (26) and (28)).
With our numerical value assigned to the phenome- nological constant 3ð, we recall that the leading amplitude determinations for each of the three pure fluids above are within the error of the results obtained
by interferometric measurements (see Table III in
Ref. [1]). The experimental precision in this asymptotic
range is about 10 %. Furthermore, these experi-
ments have shown that the fluid critical exponents are
approaching those for the theoretical model. Nearest to the liquid-gas critical point, the amplitude agree- ment is then a convincing test for the asymptotic cha-
racter of our scaling behaviour.
In figure 1, results of thermodynamic measurements
are of special interest in view of the qualitative scaling
201
behaviour in the range far from the liquid-gas critical point. Applying the previous scale transformations to
horizontal and vertical axes respectively, the different
plots of K*(,r) for eleven pure fluids fall on the single
dotted line as shown in figure 1. To clarify the effects of scale transformations we have represented in the
inset the variation of K; as a function of i for Xe, H20
and He. Xe was selected as a simple fluid, H20 as a polar fluid and He as a quantum fluid for their signi-
ficant differences in numerical value of x and Z, scale
factors. Instead of the experimental data it is conve-
nient to use the empirical scaled equation of state of
Levelt Sengers et ale [12] with the effective value of critical exponents (yeffective
=1.19).
Thus, in order to connect our phenomenological single scaled asymptotic behaviour of S*T with scaled results inferred from conventional thermodynamic
measurements in a wider range, we propose to modify equation (26) in the following way
where we assume that the first confluent amplitude ac’)+ has the same numerical value for all pure fluids.
L1
=0.5 is the theoretical universal exponent [13, 6].
Indeed, as was noted by Sengers [10], past experience
has shown the necessity to use Wegner expansion [8]
for pure fluids in order to reconcile the optical data
with those obtained in conventional ranges. The quali-
tative scaled behaviour represented by the dotted
curve in figure 1 is an illustration of the effect of
Wegner expansion terms which make substantial contribution to the departure from the leading scaling
contribution (dash-dotted line on Fig. 1). Unfortuna- tely, the amplitudes of the Wegner correction terms
depend in a complicated way on the non-universal
constants appearing in the theory [8, 9]. These cons-
tants are related to the two relevant scaling fields
which vanish at the liquid-gas critical point and to
others irrelevant scaling fields approaching
afinite
value at this same point. In the present status of the theoretical development, the dependence of Wegner amplitudes on the non-universal scale factors of real systems is not known.
Consequently, in view of the two-scale factor
universality, the meaning of our phenomenological hypothesis expressed by equation (32) is clear : we
assume that only the non-universal scale factors Yr
and Zc govern the asymptotic scaling behaviour as
well
asthe first correction-to-scaling behaviour of critical fluids. Thus, the ratio agl Irk is
acharacteristic number for the fluid subclass.
A comparison between experimental results of KT for six pure fluids and the calculated values from
equation (32) with the amplitude õgl
=0.7 selected
by iteration is presented in figure 2. The range of
Fig. 2.
-Plot of the isothermal compressibility deviations
as afunction of T - T. for Xe, SF6, C02, C2H4, H20 and He.
The base line
arecalculated from the phenomenological scaled equation (32) for Yc r 0.05 and by the empirical equation Zc K T Pc = 0.1683 (Yr T)- 1.16665 in the range 0.1 Y, T 0.5 (see text). The value of T - T, for each pure fluid
corres-ponding to Y,
T =0.1 is represented by
avertical bar superimposed
onthe logarithmic scale of the horizontal axis of tem- perature distances. Full
curves1 to 9, experimental data fitted by non-analytical expansions defined from the numerical values of table I. The dotted
curves areasymptotic extrapolations from the full
curveswhen the value of the critical exponent is the RG theoretical
one(7
= 1.24); 0 [15]; 2022, T = Tc + 0.6677 K : reference temperature of [15] with xT
= 19.64 (MPa)-l ;
D [20] ; A [26] ; +, reference temperatures of [18] with data listed in table II ; 0, Q, v, 8, x , 0, tempe-
rature distances in the practical range 0.1 Yc 0.5 (see text) with data listed in table III.
applicability of equation (32) is limited to Yc ’t ;5 0.05.
This equation reproduces the experimental data of
Xe [14, 18], SF6 [14, 18-22], C02 [14, 18, 23, 24], C2H4 [18, 25-27], H20 [10, 12, 18, 28] and He [10, 12, 18, 29-31] which are reported in tables I and II.
Curves 1, 2 and 3 show that interferometric mea- surements of the asymptotic behaviour for Xe, SF6
and C02 are very well represented by equation (32).
As previously pointed out, the asymptotic behaviour
of these curves confirms that the leading amplitudes
scaled with Y, and Z, indeed attain the proposed single value of 3+C equation (28), with differences which do not exceed 3 %. Note for these three fluids that the recent light-scattering measurements [15, 19, 23],
curves 4, 5 and 6, are in agreement with our pheno- menological predictions from equation (32). Thus, the
connection with reference temperatures from critical temperature defined by table II are correctly carried
out. These reference temperatures are chosen suffi-
ciently distant to the critical temperature for accurate determination of xT from P, p, T measurements by
a
graphical method [18]. Xe, SF6 and C02 data are
a careful test of our postulate about the single ampli-
tude value for the first Wegner correction term.
With the addition of the deviation plots in the case of C2H4, H20 and He obtained in the temperature
range of thermodynamic data, figure 2 shows clearly
that the maximum difference is about the error in the
experimental determination of xT. For example,
curves 9a and 9b in the He case are an illustration of the typical scatter in experimental results for these
properties. In the same way, it is interesting to observe
Table I.
-Literature results for the fit of the isothermal compressibility data by non-analytical expansions (line 1).
The numbers in the first column are those of the corresponding deviation curves represented in figure 2
onthe expe- rimental temperature range for each pure fluid (see text).
Table II.
-Reference temperatures from the critical temperature where
ourdeterminations [18] by
agraphical
method of the isothermal compressibility data are obtained from accurate P, p, T measurements. These data referred
by the symbol in the first column have been compared to the values calculated by equation (32), see figure 2 and text.
203
Table III.
-Temperature distances to the critical temperature in the range defined by 0.1 - Yc
’t0.5 (see text).
The experimental isothermal compressibility data referred by the symbol in the first column have been compared
to the calculated values obtained from the practical relation Z, Pc KT
=0.1683 (Yc t)-1.16665, see figure 2.
the plots presented for C2H4 where our equation (32)
is a better representation than the fundamental
equation proposed by Levelt Sengers et ale [25] for the
results of accurate Douslin and Harrison measure- ments.
Moreover the validity of the single scaled behaviour
seems to have a more extended range than those of
validity of equation (32). A comparison between experimental results of table III and the calculated values from the empirical equation
in the range 0.1 Y, T - 0.5 is also presented in figure 2. The plot reveal a good agreement interesting
for practical purposes
orif a Wegner expansion with
sufficient number of terms is used for the representa- tion of the single scaled behaviour beyond the value
V, T
=0.05.
The choice of the six pure fluids is significant for
their differences in the non-universal scale factors.
Moreover, four decades in T - Teare covered in
figure 2 by the plot of deviations of isothermal com-
pressibility data. Thus we conclude that the scale transformations are acceptable in order to observe the single scaled behaviour for all pure fluids with equa- tion (32) as a good approximation to this single
behaviour in the range Yc i 0.05.
4. Scaling behaviour of the coexistence curve.
In order to describe the two-phase region of pure fluids it is convenient to substitute the following new variable
instead of the rescaled order parameter defined by equation (21)
where the dimensionless difference åmLV is given by
PL and pv are the liquid and vapour densities. In
addition, we define the practical difference
where densities are reduced by pc. Using equations (34)
and (35) the rescaled variable Aflfv is obtained as
On the basis of equation (17), the asymptotic equation for the liquid-gas coexistence curve is
where P
=0.325 is the universal critical exponent [6].
The numerical value of the leading amplitude 5p is
determined from the following relation
where the two ratios in the bracket were defined in
equation (27). We find
z .nn.
In figure 3, we show that the scaling plots of
Z c 112 Ap* versus Yc i I obtained from results of
Fig. 3.
-Scaled liquid-gas coexistence data for different pure fluids
as afunction of the scaling distances I Yc i to the critical
point (see text and legend of figure 1 for details).
interferrometric measurements in Xe, C02 and SF6,
can indeed be projected onto. the single asymptotic
curve predicted by equations (37) and (39). This result supports our hypothesis for the fluid subclass scaling
behaviour. In that case, the phenomenological deter-
mination of the leading amplitude is within the expe- rimental precision of 5 % (see Table III in Ref. [1]).
When the ranges far from the liquid-gas critical point are investigated, the scaled thermodynamic
behaviour of åJK,iv shown in figure 3 is similar to the scaled thermodynamic behaviour found for 8; (see Fig. 1). In order to make a quantitative illustration of scale transformations in that region
wefit again the
curves åp:t(l ’t 1) for Xe, H20 and He with the effective value of the critical exponent (effective
=0.355) [12].
Likewise, using the same arguments as in the previous section, we propose to modify equation (37) as follows
where the first confluent amplitude i1i) has the same
numerical value for all pure fluids. The value of i1i) is
related to ac(1), by the theoretical universal ratio
(’)Ia-1) [32]. However the coexistence curve data for pure fluids have the resolution to determine i1B 1) rather
accurately. This complicated task would require inter- comparison between optical results and density data
on