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Temperature dependence of hydrodynamic lengths

in the polystyrene-cyclohexane system

M. Adam and M. Delsanti

DPh-G/PSRM, CEN Saclay, B.P. 2, 91190 Gif sur Yvette, France (Reçu le 13 septembre 1979, révisé le 4 février, accepté le 3

mars

1980)

Résumé. 2014 Nous présentons des résultats expérimentaux sur le comportement dynamique du système polystyrène- cyclohexane en fonction de la température

au

voisinage du point 03B8 (0 ~ T 2014 03B8 30 °C). Il est trouvé que la

dépendance en température des rayons hydrodynamiques, RH et 03BEH, d’une chaine

en

régime dilué et d’un blob

en

régime semi-dilué sont respectivement :

RH~ (T - 03B8) 0,034±0,005 03BEH ~ (T - 03B8)-0,33±0,04.

Nous montrons que

ces

variations sont dues à la relative insensibilité des longueurs hydrodynamiques

aux

effets

de volume exclu. Les comportements observés semblent compatibles avec l’interprétation sur l’exposant dyna- mique apparent par Weill et des Cloizeaux.

Abstract.

2014

We present experimental data

on

the dynamic temperature behaviour of the polystyrene-cyclo-

hexane system in the neighbourhood of the 03B8 point (0 ~ T 2014 03B8 30 °C). It is found that the temperature depen-

dence of the hydrodynamic radii RH and 03BEH of

a

chain in dilute regime and

a

blob in semi-dilute regime

are res-

pectively :

RH ~ (T - 03B8)0.034±0.005 03BEH ~ (T - 03B8)-0.33±0.04 .

We show that these variations

are

due to the relative insensitivity of the hydrodynamic lengths to excluded volume effects. The behaviours observed

seem

compatible with the Weill-des Cloizeaux explanation

on

the apparent dynamic exponent.

Classification

Physics Abstracts

05.40

-

61.40

-

66.90

-

82.90

1. Introduction. - It has been shown, in the past few years, that the dynamic properties of dilute and semi-dilute polystyrene solutions can be deduced from the static properties if an effective dynamical.

exponent Va, smaller than the static exponent v, is introduced [1]. The aim of this study is to compare static and dynamic temperature scaling laws. The

static laws, deduced from an analogy, between criti-

cal phenomena and polymer systems, have been

verified by elastic neutron scattering [2]. Here we report the dynamic température scaling laws obtained

from Rayleigh light scattering experiments on poly- styrene-cyclohexane system.

In the first part we recall the static scaling laws

and their extension to dynamic temperature laws obtained with the help of phenomenological argu- ments. Then, we report expérimental results obtained

in well defined temperature concentration domains.

The specifications of these domains have been done

using theory and static experimental results [2].

The data are fitted to power laws [23], in order to

compare those results with :

-

previous static [2] and dynamic results [1],

-

scaling laws theory [2,17].

-

the different explanations on the dynamic

exponent v. (effective or real exponent [3, 4]).

Finally we discuss the comparison of our results

with the recent Weill-des Cloizeaux explanation [3]

of an effective exponent Va.

2. Theoretical considérations.

-

A polymer solu-

tion is considered [5] as :

-

dilute, if intermolecular interactions can be

neglected. In this case the characteristic length is R

the radius of gyration of the chain ;

- semi-dilute, if intermolecular interactions are

dominant. In a semi-dilute solution the chains inter- penetrate each other and the monomer concentra-

Article published online by EDP Sciences and available at http://dx.doi.org/10.1051/jphys:01980004107071300

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tion [6] is bigger than the overlap concentration c*

defined by : c* =- NjR3, where N is the number of statistical elements in a chain ;

-

concentrated, if the monomer concentration is of the order of magnitude of the solvent concentra- tion. We will not consider them, here.

2.1 DILUTE REGIME.

-

We consider an isolated chain of N statistical elements at a temperature T, above the 0 point. The 0 point corresponds to the temperature where intramolecular interactions vanish.

The mean distance between two monomers, separated by n statistical elements, has a Gaussian behaviour if

n ne and an excluded volume behaviour if n > n,,.

The n, value can be derived from an extension of the well known Flory equation of the expansion

factor [8] :

where 1 is the length of a statistical element and v the excluded volume parameter. The excluded volume interactions are dominant when a > 1 or

which leads to :

using a linear approximation in the neighbourhood

of the 0 point, v is proportional to the reduced tempe-

rature r

=

(T - 0)/0 [7].

At a temperature T > 8, one can visualize [9, 10]

the chain as being formed by a succession of N/nC

Gaussian subchains of size :

Since excluded volume effects exist only between subchains, the radius of gyration R of one isolated

chain is equal to :

From expressions (1) and (2) we obtain [2] :

In the temperature domain s > N-l/2, this law is valid because the number of subchains is very high (N/nC > 1). In the 0 domain z N- 1/2 the confor- mation of the chain is essentially Gaussian. The limit between these two behaviours is -r* = N-l/2 which will be called the cross-over temperature (see Fig. 1).

Now, we extend these results to the hydrodynamic

radius RH defined as :

where Do is the translational diffusion coefficients of the isolated chain and ’10 the viscosity of the solvent.

From an experimental point of view, it is known that :

Fig. 1.

-

Temperature concentration diagram : Region I) dilute system with excluded volume effect ; I’) dilute 0 domain ; II) semi-

dilute system with excluded volume effect ; II’) semi-dilute 0 domain.

-

for a Gaussian chain (0 temperature) RHO and Re

are proportional [11],

. -

when excluded volume effects are present (good solvent) RH is no longer proportional to R and RH = NVH 1 where vH is an effective dynamic expo- nent smaller than v [12].

For the dynamic behaviour, we have by analogy

with (3) :

The hydrodynamic radius, ’cH of a subchain (Gaus-

sian conformation) is proportional to rC. Taking the expressions (6), (2) and (1), we have in the tempe-

rature domain [13] r > -r* :

The value of the dynamic exponent vH, smaller than v,

implies that the hydrodynamic radius must increase

with the temperature more slowly than the radius of gyration. The thermal behaviour of RH can be

determined by quasi-elastic light scattering experi-

ments on a solution of finite monomer concentra- tion c c*, at a momentum transfer K such that

KR 1. The characteristic coherent time of the scattered light is [12, 14] :

D(c) is the diffusion coefficient of the coil at finite concentration. The experimental hydrodynamical I radius, RH(c), is deduced from the D(c) measurements from :

In the dilute regime, concentration dependence of

the diffusion coefficients, can be written as :

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By extrapolation to infinite dilution (c

-

0) we

obtain the hydrodynamic radius of an isolated chain.

The interaction parameter Q is given by [15, 6] :

m is the mass of monomer and v the specific volume

of the polymer which is a constant in the temperature

range investigated [16]. A2 is the second virial coeffi- cient and gf the hydrodynamic interaction parameter of the friction coefficient (see appendix). We demon-

strate in the appendix that the variation of ç with

the temperature is :

where Bi, B2, B3 are temperature independent posi-

tive factors (see appendix). Difference between hydro- dynamic and geometric expontnt implies that the sign of ç + vm must change at a finite, positive temperature so.

2.2 SEMI-DILUTE REGIME. - At a monomer con-

centration, c, higher than the overlap concentra-

tion c*, contact points exist between interpenetrated

chains. The average distance between adjacent contact points, ç, is independent of the polymerization index

of the chains and decreases with concentration [5].

The semi-dilute solution at a temperature T > 0

can be considered as a non interacting assembly of

small chains of size ç, called blobs, having N(ç)

statistical elements. One can visualize one blob as a

succession of N(ç)jnc Gaussian subchains with excluded volume effects between them. Using an

argument similar to the argument developed in

section 2.1, we deduce :

with the expressions of rC and ne as a function of the reduced temperature (1, 2) and the value of N (ç) :

we obtain [2] :

The size of the blob decreases with increasing tempe-

rature as it has been verified by elastic neutron scat-

tering experiments [2]. The expression (15) is meaning-

ful only if N(ç)/nc > 1, this leads (using (1), (14)

and (15)) to the condition r » r** where T**

=

cl’.

In the 0 domain r « T**, the blob is essentially

Gaussian (see Fig. 1).

Let us consider now the temperature behaviour of the hydrodynamic length ÇH [17] defined as :

where D(ç) is the diffusion coefficients of the blob and ’10 the viscosity of the solvent. From light scat- tering experiments [1, 18] it has been found that ÇH

is not proportional to ç and scales with N(ç) as :

Using an argument analogous to the one deve- loped in the dilute regime we found that :

Using expressions (1), (2), (14) and (15) we obtain :

Since vH is smaller than v, the hydrodynamic length Çu

must vary with temperature more rapidly than the

static length.

The behaviour of ÇH can be determined from quasi-

elastic light scattering on a semi-dilute solution at c > c* and at a momentum transfer K such that K03BE « 1. The coherent characteristic time of the scattered light is :

from which we deduce the length ÇH by :

In the following section, we describe the experiments

which allow us to deduce the exponent values of the temperature laws.

3. Experknental procedure.

-

The dynamic lengths

are determined from spectral measurements of the

Rayleigh light scattered by cyclohexane-polystyrene

system, in the 35 to 65 °C range temperature, by light beating spectrometry.

Here we give the experimental conditions and the data processing used in order to determine 03BEH and RH,

we do not enter into the details of the light beating spectrometer which have been widely described in ref. [1].

3 .1 1 EXPERIMENTAL CONDITIONS. - The tempera-

ture regulation is achieved by a copper jacket regu- lated by a thermoresistance and ATNE monitor, within ± 0.01 °C. The copper jacket, in which the

optical cell containing the solution takes place, is

thermalized by a second chamber. The temperature is measured by mean of a thermocouple, in contact

with the cell, within an accuracy of ± 0.04 °C.

To investigate the thermal behaviour of RH and 03BEH,

it is necessary to carry out the experiments in well

defined regions. To this goal, it is useful to locate

the boundaries between the different regions, c*, s* and i**, given in the diagram (Fig. 1). The cross-

over temperature, i* and i**, are determined from

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the temperature concentration diagram drawn with

results obtained by neutron scattering experiments

in P.S. cyclohexane system [2]. It is found that : 01* m 3

x

103 M- 1/2 in the dilute regime ,

ei ** = N 35 c in the semi-dilute régime. (21)

M is the molecular weight of the macromolecule,

c the monomer concentration [6] in g/cm3. The

0 temperature in the polymer-solvent system studied

is equal to 35 I)C [19]. To define the dilute regime, it

is important to know the order of magnitude of the overlap concentration c*(t). We estimate that :

where cé and c*GS are the overlap concentrations at the 0 temperature and in a good solvent, respectively.

They are obtained using the following expression :

A is the Avogadro number, R; is the radius of gyration

found by intensity light scattering experiments [20].

The characteristics of the samples used are reported

in table I.

In order to observe macroscopic properties we

have performed the experiments at : KR gs 0.5 in the dilute régime,

and

in the semi-dilute régime.

We use an homodyne spectrometer in the dilute

régime, and an heterodyne spectrometer with sepa- rated beams in the semi-dilute regime [1].

3.2 DATA PROCFSSING.

-

As we deal with diffuse-

ing macroscopic process, the autocorrelation function of the scattered light intensity has an exponential profile with a characteristic time Tc inversely pro-

portional to K2. This allows to determine a diffusion coefficient D

=

T;lfK2.

The momentum transfer K is related to the scat-

tering angle 03C8, in the solution, by the relation :

À (4 880 À) is the wavelength of the incident beam and n is the refractive index of the solution. K has been determined from measurements in air of the

scattering angle, taking for the cyclohexane refrac-

tive index [21] :

under these conditions, we have obtained diffusion coefficients with an expérimental accuracy of 0.5 %

in the dilute regime and 1 % in the semi-dilute regime.

We have deduced RH and ÇH from D using expres- sions (9), (16) respectively and a temperature depen-

dence of the cyclohexane viscosity qo(T) established from a compilation of experimental results [22] :

the accuracy on No(t) is better than 1 %. This pro-

cessing gives RH(c --.> 0) and Ça within an accuracy

of 1.5 % and 2 %, respectively.

4. Results and discussions 4.1 DILUTE REGIME

-

The study of RH 1 as a function of the concentra-

tion, at a given temperature, shows that RH 1 varies

linearly with concentration (Fig. 2). From the expe- rimental results and the expression [6] :

we can deduce I?ï 1(t) and tp(T) defined in (5) and (9).

4 .1.1 Hydrodynamic radius RH at finite dilution.

-

The expansion factor Rai RH, varies by less than 8 % (see Table II) in the temperature range investigated :

Assuming a power law [23], in the domain T/T* > 1.4,

the best fit gives [24] :

The variation of RH/RHO, in the domain i/i* > 1.4

(domain 1 in figure 1) as a function of 0-r is repre-

Table I.

-

Characteristics of the samples used where the symbols have their usual meaning. cGS*, is calculated

using of the expression (23) where Rp is the radius of polystyrene-dissolved in benzene [20].

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Fig. 2.

-

Variation of the inverse of the apparent hydrodynamic

radius

as a

function of the

monomer

concentration, in the dilute

regime, at T

=

38.5 OC. Representative

error

bar is shown.

Table II.

-

RH and ÇH experimental values obtained

at various temperature.

sented on a log-log scale in figure 3. The aH exponent value is confirmed by the representation used in figure 4 :

has a constant value for i/I* > 1.1, but a decreasing

value for i/i* 1, which means that in the 0 domain the results cannot be described by a power law. We

can note that the cross-over temperature i* coincides with the value determined from eq. (21). The expo- nent aH found is much smaller than the exponent

a

=

0.2 predicted for the geometric expansion ; hydrodynamic AND GEOGMETRIC /LENGTH are not proper-

hydrodynamic and tional. This result is in geometric length are agreement with ref. not propor- [25] where

the ratio RJR is measured as a function of tempera-

ture in polystyrene-cyclohexane solution. RJR is

found to decrease as the temperature increases.

From the expression (7) and the experimental value aH,

we deduce an effective dynamic exponent vH

=

0.52.

The exponent value obtained is smaller than v(0.6)

and vH(o.55) obtained in very good solvent [1, 12].

The very low relative variation of RH compared to

the experimental accuracy does not allow us to rely

Fig. 3.

-

Variation of the hydrodynamie expansion factor

as a

function of the temperature, Ot >- 10 0(; (log-log scale).

-

Full

line is the best fit of the experimental points ;

----

Dotted line represents the theoretical expansion factor of geometric length

which bas been calculated using arbitrary R/Ro

==

RJR, at

0r

=

10 °C.

Fig. 4.

-

Verification of the température power law of the hydro- dynamic expansion factor, in dilute regime.

on the exponent value obtained from this experiment.

The important point is that the hydrodynamic

radius is relatively insensitive to the excluded volume effects compared to the geometric length.

4.1.2 Concentration dependence of the hydrody-

namic radius.

-

In the temperature range investi-

gated (0 °C Or 27 °C), the parameter

is negative and increases as the reduced temperature increases. The variation of Ç(i) with temperature is given in figure 5.

In the 0 domain T T*, the Q variation with the reduced température can be considered as being

linear. In the demain T > T*, experimental data are compared with calculated values obtained using

eq. (12) with : :

-

the exponent value found previously vH = 0.52,

-

and v

=

0.92 cm3/g found by densitometry [16].

The constant factor B2 and B3 are ajusted by means

of least square fit.

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Fig. 5.

-

Variation with temperature of the absolute value of the interaction parameter 0. Full line corresponds to the theore- tical values obtained from expression (12).

The interaction parameter Ç and the excluded volume effects increase as the temperature increases.

Ç is negative in the neighbourhood of the 0 point

and positive for a good solvent [1, 12, 26] and it

becomes equal to zero at a temperature ()to = 35°C

much higher than the 0 temperature [25]. This change

of sign of the parameter indicates that the thermo-

dynamic factor NA2 is not proportional to the hydro- dynamic parameter Qf. This fact confirms that R and RH do not have the same temperature dependence (see appendix).

4.2 SEMI-DILUTE REGIME.

-

The measurement of

ÇH, at a given concentration (c = 4 Co*), as a function

of the temperature, shows that ÇH decreases as the temperature increases (see Table II). The results obtained in the region i/1** > 5.5 are plotted on a log-log scale as a function of the reduced tempera-

ture (Fig. 6). It is found that [24] :

Fig. 6.

-

Variation of the relative hydrodynamic length ÇH/ÇH6 in

semi-dilute regime

as a

function of the temperature, 01 a 18.4 OC

(log-log scale). Full line is the best fit of the experimental points ;

---

Dotted line is the variation of geometric length which

has been calculated using arbitrary (/(o

=

ÇH/ÇH6 at 0r = 18.4 OC.

This exponent value is bigger than the value

b

=

0.25 ± 0.01 determined by neutron scattering in

the same temperature domain [2]. The hydrodynamic length 03BEH is not proportional to the geometric length ç.

In figure 7 we present the experimental results over

the whole temperature range investigated. We see

that ÇHjÇH8 has two different behaviours, the quantity

the temperature r**exp = 4 z**, where ÇH reaches an asymptotic behaviour, is in agreement with the cor- responding value obtained for 03BE by elastic neutron scattering experiments [2], but is much bigger than

the temperature i** determined from eq. (21). Now, using expression (18) and the experimental value bH,

we found that the effective dynamic exponent vH is

equal to 0.54. The discrepancy between the exponent values found for the geometric length03BE and the hydrodynamic length ÇH is due to the insensitivity

of ÇH to the excluded volume effects.

Fig. 7.

-

Verification of the temperature power law of hydro- dynamic length in semi-dilute regime.

The different values of vH and v lead to opposite

effects on RH and ÇH’ RH varies more slowly than R

with temperature and ÇH varies more rapidly than j

with temperature.

4.3 DISCUSSION ON THE DYNAMIC EXPONENT. -

The existence of an effective dynamic exponent vH smaller than the static exponent v allows us to explain

the temperature behaviour of the dynamic quantities.

Let us relate our results with the Weill-des Cloizeaux [3a] (W.D.C.) interpretation of the appa- rent exponent vH.

They (W.D.C.) calculate the radius of gyration (R - Ny) and the hydrodynamic radius (RH - NVH)

of a chain taking as for hypothesis the Gaussian

conformation of the chain at shorter distances, they

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determine the effective exponents v(Nlnc) and vu(Njne).

At a low Nln,, value, vH is found to be smaller than v.

As Njne increases v reaches its asymptotic value [27]

(0.6) more rapidly than vH.

This treatment can be extended to the calculation of the effective temperature exponents if one notes : - ne is proportional to t - 2 in the neighbourhood of the 0 point,

-

the blob is analogous to an isolated chain of size ç with N (ç)- cç 3 statistical elements.

In figure 8 we give the variation of the effective temperature exponents a, aH, b and bH as a function

of J Njne. In the dilute regime, for the temperature

range 1 T/T* 4 (or 1 BNlnc 4) where the experiments have been performed, the effective tem-

perature exponent varies between 0 and 0.1; the

mean value correspond roughly to the exponent determined experimentally (aH

=

0.034). From figure 8, [28] we observe that the exponent - bH

decreases very rapidly and reaches a minimum value

(-bH= -0.3) at JN(ç)/nc = 2.5 and then increases very slowly with N(ç)jne (- bH

= -

0.29 for

J N(ç)jne

=

5). Experiments, in semi-dilute regime,

have been perforrned in the temperature range 1 T/T*exp* 3 ’ which corresponds, making an over estimation, to 1 JN(ç)jne 3. In this tempera-

ture domain bH is approximately a constant bH= 0.3

which must be compared to the value determined

experimentally bH

=

0.33 [29]. We can note that, in order to determine vh from bH we must know thé

v corresponding value, because using the asymptotic

value v

=

0.6 one over estimates the exponent value vH.

This discussion leads to the conclusion that the

explanation given by Weill and des Cloizeaux is in

qualitative agreement with our experimental results.

The main problem aroused by W.D.C. calculation

Fig. 8.

-

Variation of the temperature exponents,

a

and aH in dilute regime, b and bH in semi-dilute régime

as a

function of

Q which is equal to i/1* in dilute régime and approximately equal to i/i** in semi-dilute regime.

lies in its basic assumption : does the local Gaussian conformation exist ?

This assumption is verified in a 0 solvent ; but there is no experimental evidence of its validity in a good solvent.

By elastic neutron scattering the size rc of the

Gaussian conformation, in polystyrene-cyclohexane

solution near 0 temperature, has been measured [30].

rc decreases as the temperature increases and becomes

equal to the statistical length (1

=

10 À) when

Since benzene, at room temperature is a better solvent than cyclohexane at 57 °C for polystyrene (Rbenzene > Rcyclohexane 570) the local Gaussian confor- mation does not exist in the system polystyrene-

benzene. This observation casts some doubt on the

validity of W.D.C. calculation and we believe that direct experimental confirmations are indispensable.

One of these, could be, to find some polymer solvent

systems where this cross-over effect is negligible, in

order to verify that vH could indeed reach the asymp- totic value (0.6).

5. Conclusion.

-

From these experiments, done in

the neighbourhood of the 0 temperature on PS- cyclohexane system, we conclude : that the hydro- dynamic radius RH of a chain is relatively insensitive to changes in the segment distribution arising from

excluded volume effects [31]. This conclusion can be

extended, in the semi-dilute regime, to the hydro- dynamic length of a blob 03BEH.

The concentration and molecular weight depen-

dence Of 03BEH and RH, at the 0 temperature, have not been verified but the temperature exponents found, suggest that, 03BEH c-’ and RH - Mû.5. This last point is in agreement with experiments done at the

0 point [11]. Our results are in qualitative agreement with an explanation of anomalous dynamic expo- nents by cross-over effects. But those experimental

results (Table II) allow any theoretical approach on

the problem of dynamic exponents, to be verified.

Acknowledgments.

-

The authors wish to thank J. P. Cotton, C. Bagnuls, J. des Cloizeaux, G. Weill and G. Jannink for hepful discussions ; F. Geiessler and A. M. Heicht for their advices regarding various experimental aspects. We thank M. Daoud for sending his preprint.

Appendix.

-

Let us recall the expression of the

interaction parameter ç [6, 15] :

.

Here we relate, the second virial coefficients A 2 and

the hydrodynamic interactions parameter Qf, to the

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macromolecular parameters in order to calculate the thermal behaviour of e.

In the domain i > i*, A 2 is proportional to the

volume occupied by one chain [8, 5], with eq. (4),

we have :

.

In the 0 domain i i*, A2 is proportional to the

excluded volume parameter [8] which is a linear

function of the reduced temperature

Q f is defined [6, 15] by :

where fo and f (c) are the frictional coefficients of a

chain at infinite and finite dilution, respectively. To

evaluate Qf let us select a chain amongst the other and détermine its effective friction coeffcient f (c) :

the additional friction coefficients bf(c) is due to the macroscopic incrément of the viscosity bn due to the

presence of the other chains :

03B2 is a numerical factor which is no longer equal to 6 7c

since the size of the selected chain is equal the size

of the other chains [32]. &, is related by definition [6, 8]

to the intrinsic viscosity M by :

Using the expressions (A . 4)-(A . 7) we obtain :

It has been shown [33] that :

where il (characteristic time of the first mode of the

chain) is the time required by a chain to diffuse on

a distance equal to its size [34] R :

Using (A. 8), (A. 9) and (A 10) we find that

In the domain i > T* using the thermal behaviour

proposed for RH, R, A2 and the expression of e

(eqs. (4), (7), (A . 2) and (A 1», we have :

In the 0 domaine 1:*, a temperature expansion

can be made :

Factors BI, B2, B3 and v are independent of the

reduced temperature. The specific volume v can be

considered as a constant in the temperature range

experimentally investigated [16]. Bi is proportional

to the intrinsic viscosity (positive factor), thus at the

0 point e + vm is negative. B2 and B3 are positive

and respectively proportional to N3Y-l and to N"H-".

The reduced temperature io at which e + vm vanishes

is molecular weight dependent (To - N-1/2).

Références and notes

[1] ADAM, M., DELSANTI, M., Macromolecules 10 (1977) 1229.

DELSANTI, M., Thesis, Université de Paris Sud (1978).

[2] DAOUD, M., JANNINK, G., J. Physique 37 (1976) 973.

COTTON, J. P., NIERLICH, N., BOUÉ, F., DAOUD, M., FARNOUX, B., JANNINK, G., DUPLESSIX, R. and PICOT, C., J. Chem.

Phys. 65 (1976) 1101.

[3a] WEILL, G. and

DES

CLOIZEAUX, J., J. Physique 40 (1979) 99.

[3b] AKCASU, A. Z., HAN, C. C., Macromolecules 12 (1979) 276.

[4] JASNOW, D., MOORE, M. A., J. Physique Lett. 38 (1977) L-467.

AL-NOAIMI, G. F., MARTINEZ-MEKLER, G. C., WILSON, C. A.,

J. Physique Lett. 39 (1978) L-373.

[5] DAOUD, M., COTTON, J. P., FARNOUX, B., JANNINK, G., SARMA, G., BENOIT, H., DUPLESSIX, R., PICOT, C.,

DE

GENNES,

P. G., Macromolecules 8 (1975) 804.

[6] The

monomer

concentration, c, in section 2 and appendix is expressed in

monomer

number by unity volume (cm-3),

in the section 3 and 4 is expressed in

monomer mass

by unity volume (g/cm3). If A

=

constant x B and the

constant is dimensionless,

we

will write A ~ B. A ~ B

means

A proportional to B.

[7] This definition of 03C4 is different from the

one

introduced by Flory [8]

03C4

= (T-03B8/T) However, in the small values of 03C4

here investigated there is

no

appreciable numerical diffe-

rence

between the two definitions.

[8] FLORY, J. P., Principles of Polymer Chemistry (Cornell) 1953.

[9] FARNOUX, B., BOUÉ, F., COTTON, J. P., DAOUD, M., JANNINK, G., NIERLICH, N.,

DE

GENNES, P. G., J. Physique 39 (1978)

77.

[10] DAOUD, M., Thesis, Université de Paris VI (1977).

[11] KING, T. A., KNOX, A., LEE, W. I. and MCADAM, J. D. G., Polymer 14 (1973) 151.

FROST, R. A., CAROLINE, D., Macromolecules 10 (1977) 616.

[12] ADAM, M., DELSANTI, M., J. Physique 37 (1976) 1045.

[13] DAOUD, M. and JANNINK, G., J. Physique 39 (1978) 331.

[14] See for instance :

CUMMINS, H. Z., PIKE, E. R., Photon correlation and light beating spectroscopy (Plenum press, New York) 1973.

[15] YAMAKAWA, H., Modern theory of polymer solutions (Harper

and Row, New York) 1971.

[16] FRANÇOIS, J., CANDAU, F., BENOIT, H., Polymer 15 (1974) 618.

[17] DE GENNES, P. G., Macromolecules 9 (1976) 587.

[18] ADAM, M., DELSANTI, M. and JANNINK, G., J. Physique Lett.

37 (1976) L-53.

[19] STRAZIELLE, C. and BENOIT, H., Macromolecules 8 (1975) 203.

[20] DECKER, D., Thesis, Strasbourg (1968).

(9)

[21] TIMMERMANS, J., Physics chemical constants of pure organic compounds (Elsevier Amsterdam) 1950.

[22] Lange’s Handbook of chemistry, J. A. Dean (Mc Graw Hill book Cy) 1973.

Handbook of chemistry and physics, 59th Edition (RC Weast

CRC Press).

BRUNET, J. and GUBBINS, K. E., Trans. Faraday Soc. 65 (1969)

1255.

Polymer Handbook, Brandrup, J., Immergut, E. H. (1975).

[23] Since the analytical expression proposed in ref. [3b] does not

allow the authors to obtain

a

quantitative agreement We fit

our

data by power laws.

[24] A variation of 1 °C in the 03B8 value give

no

appreciable change in the exponent value (6 %).

[25] ALLEN, G., VASUDEVAN, P., HAWKINS, E. Y., KING, T. A., J.

Chem. Soc. Faraday Trans. II 73 (1977) 449.

[26] BAILEY, D., KING, T. A., PINDER, D. N., Chem. Phys. 12 (1976)

161.

KING, T. A., KNOX, A., MCADAM, J. D. G., Polymer 14 (1973)

293.

[27] A

more

accurate value for

03BD

is 0.588 (see ref. [4]).

[28] After this paper

was

written,

we

received

a

preprint by M.

Daoud giving similar theoretical results

on

the thermal behaviour in semi-dilute range.

[29] One

can

remark that the maximum theoretical value of bH (using

03BD =

0.6) is smaller than the experimental value.

[30] FARNOUX, B., BOUÉ, F., COTTON, J. P., DAOUD, M., JANNINK, G., NIERLICH, M.,

DE

GENNES, P. G., J. Physique 39 (1978) 77.

[31] KRIGBAUM, W. R. and CARPENTER, D. K., J. Phys. Chem. 59 (1955) 1166.

[32] LI, J. C. M., CHANG, P., J. Chem. Phys. 23 (1954) 518.

[33] FERRY, J. D., Viscoelastic properties of polymers (Wiley, New York) 1961.

[34] LANDAU, L. D., LIFSHITZ, E. M., Mécanique des fluides (Mir

Moscou) 1961.

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