simple shearing flows in polyisobutylene solutions · key words: bkz fiuid ; nonlin ear behavior;...

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--------------------------------------------- JOURNAL OF RE SEARCH of the Noti ona l Bur ea u of Standard s- A. Physics and Che mi stry Vo l. 75A, No. 1, Ja nuary- February 1971 Simple Shearing Flows in Polyisobutylene Solutions L J. Zapas and J. C. Phillips In s titu te for Bas ic Standards , National Bureau of Standards , Wash i ngton, D.C. 20234 (July 2, 1970) Meas ur ements of shea r str ess for va ri ous shearing fl ow histo ri es at 25 °C are co rr elated thr ough the BKZ elas ti c flu id theory. Th e data are on 10 perce nt P IB so lution in ce tane. Th e histo ri es in c lud e step n ,lilxa lioll . sud denly a ppli ed s\t'ady sll t'ar. shear in g A ow. rel ax ation a ft pr st('ady slwa r. Key words: BKZ fiuid ; nonl in ea r be hav ior; polyiso but ylene; s tr ess relaxa ti on; vi sc osit y. 1. Introduction In th is pap er we pr ese nt th e r es ults of a se ri es of exp e rim e nt s on a single s ampl e of polyis obut ylene solution s ubj ec ted to various histori es of s impl e sh ea r. Th e work -w as done as a part of a lar ger program to stud y th e a ppropriat eness of a fairly gene ral co nstitu- tive e quati on, the Bernstein, Ke ar sley, Zap as ( BKZ) el as tic fluid [11,1 in d esc ribin g a wide range of no n- lin ea r vi scoe la s ti c behavior for a ran ge of mate rial s. Thi s lar ger purp ose influen ce d bo th the choice of t es t mat erial and the choi ce of e xp e rim e nt s. In the first pla ce, the studi es were co nfined to a single sa mple so as to provid e a t es t of the co rr elations be tw ee n e xp eri- me nt s pr e di cted by the ass um ed co ns titutiv e e qu ation. Th e s ampl e wa s ch ose n to show esse ntiall y co mpl ete re lax ation within the tim e sca le of the e xp e rim e nt , sin ce ea rli e r s tudi es [2J had b ee n mad e on mat e r ial s with lon ge r relaxati on tim es . Th e deformation s ar e various hi stori es of s impl e she ar , b ec au se th ey ar e e xp e rim en tally c onv enie nt de formation s and bec au se th ey are co nvenie nt to analyz e in te rm s of the a ss um ed cons titutiv e e quation. Some meas urem e nt s of no rmal s tr es s es were mad e on this s ampl e, but we enc ount ered serious di sc re p- an ci es wh e n we a tt e mpt ed to c orrelat e th em with the she ar data. Thi s tr o ubl e ha s b ee n tra ce d to the r ece ntly dis co vered " press ur e hole e rror " [3J and the difficulty r esolv ed, but we hav e pos tpon ed public ation of th e norm al s tr ess data to avoid furth er dela y in the prese ntati on of the sh ea r s tr ess meas ur eme nt s. In th e c our se of th ese s tudi es so me meas ur eme nt e rr or s, customarily ignored, were fo und to be sur- pri singly large and so me co rr ec ti on methods were work ed o ut a nd ar e pr ese nt ed here. A ,p ecialized form of th e BKZ e la stic fluid was u se d in th is pap er to 1 Figures in bracke ts indicate the li terat ur e refere nces al the end of this paper. 408-434 0 - 71 -3 33 co rrelat e o ur e xp erime nt s with ve ry good su ccess . Alth ough this spec ial form is neither uniqu e nor ex ac t, it h as b ee n chose n to be co nsiste nt with a wide ran ge of phenome na b eyo nd that d esc ribed in this paper, and should be of co nside rabl e pr ac ti cal u se . 2. General Considerations Th e class of motions which we shall co nsid er will be limit ed to s impl e she arin g histori es . In the in co mpr ess ible iso thermal form of th e BKZ th eo ry [1 , 4J the valu e of the sh ea ring s tr ess at time t is given by the following r ela ti o n U(t) = (2. 1) -f ", W ,Jy(t) - Y(T) , t - T) (y (t ) - Y (T))d T where y( T) is th e am o unt of she ar at time T and W* is a fun ction of s train and time. 2 If W * is kn own, th e she arin g s tr ess a- (t) for any s impl e she arin g fl ow c an be c alculat ed thr ough eq (2.1). Of co ur se, th e form of W* is not sp ec ified by the th e or y and in ge ne ral th e fun ction W* mu st be dete rmin ed throu gh e xp e rim e nts. A good idea of th e function W * c an be obtain ed from e xaminin g a s in gle st ep s tre ss relaxation history in s impl e sh ear. In such a deformation the sh e arin rr his tory is given by: b for T < 0 Y(T) = y = co ns tant (2 .2) for T> O. By s ub s titutin g t" = t - T and (2.2) in (2.1), we get U(f) f '" -=- W*( y, t")dt" = W( y, t) y ( (2.3) :! Equ a tion (2. 1) is e qu ivalen t 10 e(1 (3. 11 ) of Bernstein :41 exce pt for a change uf notat ion. 1,1* of thi s t: qu at ioll is e q ual 10 - '2(U,,+ V, , ) of Be rn stein. and our a(/) is Bernsl t: in 's if l:!.

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Page 1: Simple shearing flows in polyisobutylene solutions · Key words: BKZ fiuid ; nonlin ear behavior; polyisobutylene; stress relaxati on; ... examining a single step stress relaxation

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JOURNAL OF RE SEARC H of the No tiona l Bureau of Standards- A. Physics and Chemistry Vo l. 75A, No. 1, Ja nuary- February 1971

Simple Shearing Flows in Polyisobutylene Solutions

L J. Zapas and J. C. Phillips

Institute for Basic Standards, National Bureau of Standards, Wash ington, D.C. 20234

(July 2, 1970)

M easure me nt s o f shea r s tress for va rious shea ring fl ow hi s tori es a t 25 °C are correlated through th e BKZ elas ti c flu id th eo ry. The da ta a re on 10 pe rcent P IB so luti on in ce ta ne . Th e hi stori es inc lude ~ in g l t · step ~ trt' ss n ,lil xa lioll . sud de nly appli ed s\t' ad y s ll t'ar. ~ l l'ady shea r in g Aow. ~ Ir t->ss relax ation a ft pr s t('ady s lwa r.

Ke y word s : BKZ fiuid ; nonlin ea r be hav ior; polyiso but yle ne ; s tress re laxa ti on ; vi scos it y.

1. Introduction

In th is pape r we prese nt the res ults of a seri es of experiment s on a sin gle sample of polyisobutylene solution subjected to vario us hi s tori es of s imple shea r. The work -was done as a part of a larger program to study th e a ppropriate ness of a fairly gene ral cons titu ­tive equation , th e Bern stein , Kearsley, Zapas (BKZ) elas tic fluid [11,1 in d escribin g a wide ra nge of non­lin ear viscoelas ti c be havior for a range of ma terials. This larger purpose influ e nced both th e c hoice of tes t materi al and th e choice of experime nts. In th e firs t place, th e s tudi es were confined to a single sampl e so as to provide a test of the correla tions between experi­me nts predic ted by the assumed cons titutive equa tion. The sampl e was chosen to show essentially comple te relaxa tion within the time scale of the experiment , since earli e r s tudies [2J had been made on mate r ial s with longe r relaxation tim es. The d eformations are various hi s tories of simple s hear, because they are experimen tally conveni ent deformation s and becau se they are co nvenient to analyze in term s of the assumed cons titutiv e equation.

Some me asureme nts of normal stresses were made on thi s sample, but we encountered se rious di screp­ancies whe n we a tte mpted to correlate them with th e shear data. Thi s trouble has been traced to the recently disco vered " press ure hole e rror" [3J and the diffic ulty resolved , but we have postponed publication of the norm al stress da ta to a void furthe r delay in the prese ntatio n of th e shear stress measure ments.

In th e course of th ese s tudies some measurement errors, cus tomarily ignored , were found to be s ur­prisingly la rge a nd some correct ion me thods were worked out a nd are presented here . A , pecialized form of th e BKZ elasti c fluid was used in th is pape r to

1 Figures in brackets ind ica te t he li te ra ture refere nces a l the end of t his pape r.

408-434 0 - 71 - 3

33

correlate our expe r iments with very good s uccess. Although thi s s pec ial fo rm is ne ithe r uniqu e nor exac t , it has been c hosen to be consis te nt with a wide range of phe nomena beyond that described in thi s pa per , and should be of conside rable prac ti cal use.

2. General Considerations

Th e class of motions whi ch we shall consider will be limited to simple s he aring hi s tori es .

In th e in compressible isothe rmal form of th e BKZ th eory [1 , 4J th e value of th e shearing s tress a t time t is given by th e followin g relation

U(t ) = (2. 1)

-f ", W ,Jy ( t ) - Y(T) , t - T) (y ( t ) - Y (T))dT

where y ( T) is th e amount of shear at time T and W* is a fun c tion of s train and time.2 If W * is kn own , the shearin g s tress a- (t ) for a ny simple shearing fl ow can be calculated through eq (2.1). Of course, the form of W* is not s pecified by the theory and in general the fun ction W* must be determined through experiments.

A good idea of the function W * can be obtained from examining a single step stress relaxation history in simple shear. In s uch a deformation the shearin rr his tory is given by: b

for T < 0

Y(T) = y = constant (2 .2)

for T> O.

By subs tituting t" = t - T and (2.2) in (2.1), we get

U (f ) f '" -=- W*( y , t")dt" = W( y , t ) y (

(2.3)

:! Equa tion (2. 1) is equ ivalen t 10 e(1 (3. 11 ) of Be rn ste in :41 except for a c hange uf no tat ion. 1,1* of thi s t:quat ioll is eq ual 10 - '2(U,,+ V, , ) of Be rn s te in . a nd our a(/) is Be rn s l t: in 's ifl:!.

Page 2: Simple shearing flows in polyisobutylene solutions · Key words: BKZ fiuid ; nonlin ear behavior; polyisobutylene; stress relaxati on; ... examining a single step stress relaxation

where W ( t) = a W (y , t)

* y, at (2.4)

and

W(y, co) = 0.

In this paper we shall refer to W as the relaxation function . From (2.3) it follows that W or W* may be obtained from single step stress relaxation measure­ments in shear at different strains and from this the stress for any simple shearing flow history may be predicted. This approach is similar to the one used for simple extension histories [2].

Bernstein [51 has shown that the function

( a In W(y, t) ) ?t' ( y, [) = W ( y, [) 1 + a In y (2.5)

may also be obtained from experiments of suddenly applied steady shear. Thus, in principle, we should be able to obtain W(y, t) from a series of experi­ments , and then proceed to check the BKZ theory by comparing measured and predicted stress for simple shearing histories.

Of course, one can never realize experimentally these shearing histories exactly as assumed. From some of the experiments which approximated suddenly applied constant rate of shear history, discussed in section 6, we were able to get a rough approximation of the relaxation function . Applying corrections which will be discussed later using an iterative scheme, we recalculated a function W which is consistent with all our experiments which include measurements of viscosity as a function of the rate of shear, stress relaxation after shear (for different rates of shear), measurement of stress as a function of time for sud­denly applied steady shear, and single step stress relaxation experiments. These results, we felt , justi­fied the use of an expression for W(y, I) which can describe all our experiments and which is a special form of a more detailed expression consistent with the behavior of other materials and other deformations, VIZ:

W(y, [) = G([) ( 1 + 0.145 IY1 ) 1 + ~y2 o + 0.06y2) 5/ 2

(2.6)

where G (I) is the s hear stress relaxation modulus. ~ It is evident that th ere are many other forms which are consistent with our experimental data. Our motiva­tion for choosing form (2.6) is its relative simplicity and its consistency with a strain potential fun ction [1]. Furthermore, form (2.6) is useful in process control engineering since an immediate translation from the linear to the nonlinear behavior can be made as a

3 Notice that (; (t). the s hear re laxat ion modulus, is the limit of relaxation function W (y . 1) as y goes to ze ro.

34

function of temperature , molecular weight, and concentration.

3. Experimental

The data reported in this paper were obtained on a 10-percent solution of polyisobutylene (vistanex L- lOO, Enjay Chemical CO.)4 in cetane. A Weissenberg Rheogoniometer was used to shear the sample be­tween a flat plate (7.5 cm diameter) and a cone such that the angle of the gap was 0.0268 radians . The cone was at the bottom and was connected to the driving shaft. The plate was at the top and was connected to a torsion bar which was used to measure the torque. For most of the experiments a torsion bar of lis -in diam eter was I

used. The stress-time measurements and the dynamic response were recorded on an oscillograph.

The chamber enclosing the cone-plate assembly was kept at a temperature of 25.0 °C ± 0.1 0c. Ambient temperature was controlled at 25.0 °C ± 0.5 °C . An ambient temperature 3 degrees below the chamber temperature caused a noticeable change in the curve of viscosity versus rate of shear at high rates of shear. The zero shear viscosity at this temperature varies about 5 percent per degree.

Periodically, degradation checks were made on samples of 10-percent PIB by ta}<ing viscosity versus rate of shear data. No changes were observed over a 2 year period.

4 . Behavior at Small Deformations

It is clear from eq (2.6) that the shear relaxation modulus , G(l), plays an important role in our curve fitting scheme. Since stress relaxation measurements cannot be carried out using deformations small enough to yield an infinitesimal modulus, this is ordinarily obtained by some sort of extrapolation procedure. An alternate method, adopted here , is to calculate a curve from measured values of the dynamic modulus , G' (w) [6]. We employed the conversion scheme given by Marvin [7],

G(t) = G' (w) I llw=t

(4.1)

using an approximation technique similar to the famil­iar derivative schemes [61 for the relaxation spectrum, H (T). Even though we must depend on extrapolation for values of H ( T) at small T, the effect on G ([) is slight.

Figure 1 shows the dynamic data and figure 2 the derived values of G ([). The dotted portion of figure 2 represents values extrapolated to times smaller than

~Cert a in comm erc ial equipment , instrum ent s. or ma te rial s are identified in thi s paper in order to adequat e ly spec ify the experiment a l procedure. In no case does s uch identifica· tion imply recommendation or e ndorseme nt by the .'Jational Bureau of S tandards . nor does it imply that the mat erial or equipment identified is necessarily the best avail able fo r th e purpose.

Page 3: Simple shearing flows in polyisobutylene solutions · Key words: BKZ fiuid ; nonlin ear behavior; polyisobutylene; stress relaxati on; ... examining a single step stress relaxation

11' z 3' '<:9

'------.J 2 <.9 o --' g

'"" if)

(5 IL.

I ,i I ~

<.9 o --'

o

O~--~~--------O~--------~----------~2

LOG L(J,d F I GUHE L: Dynamic morlnlu s C ' (w ) oll d dyna miti v iscosity 'Y/ ' (w )

./or a 10·percent PIB (L- IOO ) solution ill cetane.

Solid c ircles arc (h e calcula ted va lues from cqs (4 .2) and (4.3).

3 --- ---.....

2

N

~I z

<3 ~o o ..J

-I

-2

-....... ............ ............ ,

F IGUHE 2: S hea r relaxation modulus , C( l ), ./or a 10'percellt PIB (L- IOO ) solut ion ill cetane.

The do lt ed POri ion shows the ex tra pula ted region.

(l /w) for the highest measured freque ncy. As a critical chec k on both th e convers ion and the extrapolation , we calc ulated C'( w) and 1) '( w ) from th e well known relation s [6 1

C' ( w ) = w L: IC (l ) sin wi dIn I (4.2)

1)' ( w) = f ""oc lC ( t) cos wl dIn l , (4.3)

35

where 1)' (w) is the dynami c viscosity. The solid circles in figure 1 repres ent these valu es, which agree with the measured curve. For values of w hi gh er than 10 S- l

the integrals in (4.2) and (4.3) de pe nd strongly on the extrapolated region of C (t) . Some of the values of C(t) calculated from (4.1) are give n in table 1.

TABLE 1. Shear relaxation modulus /or 10 percent Vistanex L- l 00 (in cetane) at 25 °C

t (; ( t ) t (; (t) (s ) (Nlm") (5 ) (Nlm ")

1 x 10- ' 2. 1 J x 10" 3 X 10 - 1 3.85 X 10' 2 X 10 - 5 1.98 X 10" 5 X 10- 1 2.02 x lO' S x 10 - 5 1.78 x 10"· 8 X 10 - ' 1.05 x 10' 1 x 10- ' 1.6 1 x 10 " 1.0 7.8 2 x 10- 4 1.45 x 10" 2. 0 2.57 5 x 10- ' 1. 16 x 10" 3.0 1.1 7 I x 10- " 9. 5 X 10" 4.6 4. 1 x 10- '

:1 x 10- " 7.4 X 10" 8. 0 7.9 X 10- " 5 x 10- " 5.2 X 10" 10. 0 4.0 X 10- " I X 10- 2 3 .8 X 10' 1.4 X 10 ' 1.2 X 10- ' 2 x 10 - " 2 .85 X LO" 1.8 x 10' 3.9 x 10 - " 5 x 10- " 1.8 X 10" :1.0 x 10' 2.0 x 10 - " 1 X 10- ' 1.08 x 10' 3.0 X 10 ' 9.87 x 10- ' :1 x 10- ' 5. 92 x 10'

5. Single Step Stress Relaxation in Shear

In secti on 2 th e definition of a s ingle s te p s tress relaxation his tory in simple shear was given in whi ch the s te p is in s tantaneou s. In practice , it takes a finite t ime to reach th e desired deformation, and it can be shown that the m easured s tress is an upper bound of the s tress relaxati on fun ction. At long tim es the differ­ence be tween the relaxation fun ction a nd th e bound becom es s mail. With a knowledge of th e actual s train hi story, on e can es timate thi s difference and obtain a better bound for th e relaxation fun c tion.

With the history

Y(T) = O, T :;;; O

Y(T) =1. T , 0 :;;; T :;;; tl (5.1) II

Y(T) = y (I) = y , II :;;; T :;;; I

where tl is the tim e required to reach the maximum strain , eq (2 .1) becomes

Since the quantity given by the integral in (5.2) is nega­

tive , r:r(l ) is an upper bound of W (y , t). Since - W *( y , t) Y

is a monotone nonincreasing func tion of t, the ratio of

Page 4: Simple shearing flows in polyisobutylene solutions · Key words: BKZ fiuid ; nonlin ear behavior; polyisobutylene; stress relaxati on; ... examining a single step stress relaxation

a-(t) /W(y, t) goes to unity at high values of t. y For values of y such that

a condition satisfied in the stress relaxation data reo ported here, it can be shown [81 that a- (I + t l ) /y for 1 ~/ I is a lower bound of W(y, t).o

An example of the two bounds and the function W(y, I) is shown in figure 3 for y=0.2 andt l = 0.03 S.

The values of W (y , t) are the values that we used to correlate our different experiments. We see that even for values of 1 = 10 II the upper bound is high. The average of the two bounds gives agreement to within 1 perce nt. In the example in figure 3, a very good approximation of W (y, t) can be obtained by averaging the time of the two bounds, viz,

In our experiments the strains were induced through a shaft of the rheogoniometer normally used for sinus­oidal deformation histories. The motion of the cone was monitored with a transducer. The deformations were obtained by using a springloaded lever arm to drive . the shaft through part of a cycle. This arrange­ment allowed us to obtain strains up to y = l.8. By using only a part of the sinusoidal deformation , we could obtain a motion of the cone very close to a ramp function. The time required to reach the maximum strain was of the order of 0.01 to 0.05 S.

r;;--o E "­Z

<.!)

o J

W(~,t)

-2 - I LOG(t,s)

(j( 1+ 1,/2)

~

o

FIGURE 3: Bounds ujW(y . I) jor y = O.2 (Ina I, = 0.03 s .

.~ This is equivalent to taking the relaxation from the instant of reaching the final shear va lu e.

36

Unfortunately, in our experimental system there is another complication due to the motion of the upper platen. The true strain at any time t is more nearly

g(t) - a-~t) where f( is a constant depending on the

stiffness of the torsion bar and the geometry of the cone and plate, and g(t) is the nominal strain at t cal­culated from the motion of the cone. With a stiffer torsion bar the error due to the motion of the upper plate would be smaller but small stresses could not be measured with enough precision. If the motion of the cone is monitored, one can calculate the error due to the motion of the plate. In our measurements the error in the stress at the early times was 6 percent.

Figure 4 shows a plot of W ( y, I) versus y in which both corrections were made. The isochrones at the early times are in very good agreement with eq (2.6) which corresponds with the lines. To the extent that the isochrones are parallel in this type of a plot , i.e., superposition occurs by a vertical translation, one can justify the representation of W (y, t) as a product of the stress relaxation modulus and a function of shear, y, i.e., eq (2.6).

2

-2

FIGURE 4: Isochrones oIW(y. t) versus y.

The lines indicate the calc ulated behavior from eq (2.6).

6. Suddenly Applied Constant Rate of Shear

With our experimental arrangement we found that we could not obtain an instantaneous constant rate of shear. For that reason we monitored and measured the motion of the cone with a transducer during the early part of the shearing. The monitoring arrangement prevented the use of the temperature control chamber. Therefore, the measurements were done at room tem-

- - - -- -----~- J

Page 5: Simple shearing flows in polyisobutylene solutions · Key words: BKZ fiuid ; nonlin ear behavior; polyisobutylene; stress relaxati on; ... examining a single step stress relaxation

t =22.2 sec-I

~~.--~o---o~II~.~1 ----I

2

~ 5.56

~---~-~ ----o~

b ...... _oe' d~~~

,.,0/

-2

/ /

/ p/

.if ,if'

-I o LOG (t. 5)

F,G UHE 5: Th e .sohd lin es represent th e stress calcillated/or a suddenly applied rute o./"shear/or the rates o./"shear indicated.

The open c ircles are experim ental da ta, a nd the so lid c ircl es are ca lculat ed va lu es using th e tru e hi story of th e motio n.

perature. Since it took about 20 s to complete a run, the temperature variation was no more than ± 0.5 °C at 25 °C.

For these runs, due to the limitations of the tran s­ducer, we co uld monitor strain s only up to y = 0.4. On repeating an experiment, differen t strain histories were invariably obtained (over the early part of the time scale); thi s was probably caused by differing positions of the gear teeth. So, from each series of repetitive run s, we selected the one with the least de viation from a con stant rate of shear.

Using eq (2. 1) with the history

y( T) = 0, T< O (6. 1)

Y(T)= YT,T ~ O ; y =constant

we obtain 6

where Y = y~ and y is the rate of shear. In figure 5 we show the data as obtained. The lines represent the prediction of (6_2) and (2.6) which assume a suddenly applied steady shear (for the rates of shear indicated), and the black solid circles are values calculated from (2.1) and (2.6) usin g the tru e hi story of the motion. The agreeme nt is very good. The in ertia of the upper platen and assembly was not corrected for. We es timated for y = 22.2 s - I that the inertial effect caused an error of

6Througho ut the pape r we s hall use the not ation a tn If to re present the de rivat ive of a In 'Y

In III wilh respect to the d erivative of the logar ithm of the firs t argument.

37

less than 2 perce nt. Figure 5 shows at high rates of shear an overshoot of the s tress cr(t) as it approaches its limitin g valu e.

From eq (6.2) the maximum value of the stress should occur whe n

a In W(y, l ) =- 1 a In y . (6.3)

Our empirical form of W ( y , t) , eq (2.6), sati sfies thi s condition at y = 2.44.

In table 2 we show the strain s at which the maximum of the stress occurs from oth er data. 7 Middleman's data [9] were estimated from the published graphs. The data of the more conce ntrated polyisobutylene solu­tion s were obtained in our laboratory. The zero shear viscosities at 25 °C were 4460 poise for the 15_1 percent concentration and 17,760 poise for the 19.3-percent concentration_ Assuming the principle of reduced variables with respect to concentration to be valid [10], we see that the rates of shear reported in table 2 for the higher concentrations will be 8 times as high when reduced to 10-percent concentration, for which the zero shear viscosity is 540 poise.8

The position of this overshoot can be used to study the error caused by the motion of the upper platen. It is easy to show this error by experiments with torsion bars of different diameters. In figure 6 we show the data obtained from a 15.1 percent solution at a nominal

' If eq (2.6) is correc t for all concentra tions. the max imum of the stress must occur at the same valu e of y.

II The reduced rat e of shea r Yli is given as

where TJi is the ze ro shea r viscosit y at concent ration (." 1 .

Page 6: Simple shearing flows in polyisobutylene solutions · Key words: BKZ fiuid ; nonlin ear behavior; polyisobutylene; stress relaxati on; ... examining a single step stress relaxation

,.----, NE "-z . ::-b ~

0 0 ....J

3

-2 -I LOG (t. 5)

o )a"

• %tIl ... 0.35"

o

FIG URE 6: Stress versus ti me, /Ising different torsion iwrs for the same nominal rate of shear of 22 .'1.1 - 1 applied at t = O, for a {s./· percent solution of PIS in cetane.

rate of shear of 22.2 s - I. The open circles show the data obtained with a 0.125-in torsion bar. The solid circles are data obtained with a 0.25-in bar and the black triangles, with a 0.35-in bar. The histories of the motion of the cone for all the runs were almost identi­cal, so that a direct comparison can be made of the effect of the motion of the upper platen. The maximum occurs at t = 0.11 s for the 0.25-in and 0.35-in bars and at t = 0.16 s for the 0.125-in bar.

TABLE 2. Values of l' at which the maximum of the shearing stress occurs for the designated rates of shear

15.1 percent 19.3 percent Middleman's y Vistanex L- I00 Vistanex L- I00 Data on Polyiso-

(in cetane) (in cetane) butylene BASF at 25 °C a t 25 °C B- 50 at 23.9 °C

0.0048 ...... . ..... 2.45 .012 .. .... . .... . 2.4 .024 ...... ... ... 2.3

1.77 2 .. 55 2.55 ...... 5.56 2.55 2.55 ......

ILl 2.5 2.5 ..... . 22.2 2.5 2.55 .... ..

7. Steady State Shearing Flow

In the previous section we examined the stress from suddenly applied constant rate of shear. After a certain time, as can be observed, the shearing stress reaches a limiting value independent of time. The viscosity, 1) (y), which is the ratio of this shearing stress to the rate of shear, is given by

In figure 7 we show the experimental values of viscosity as the open circles. The solid circles are the values 1

calculated from (7.1) and (2.6). In the same figure we show the dynamic viscosity 1)' (w) . We observe that the two curves cannot be superposed by a shift along the horizontal axis .

8. Stress Relaxation After Steady Shear

In this history the material is initially sheared at a constant rate of shear y until the shearing stress is independent of time. The motion stops at time we call zero, and we observe the subsequent decay of the stress as a function of time. The strain history at time 7 is given by

1'(7) = "'7+1'0 ,

1' ( 7) = Yo ,

7 :s 0

7 ;;': O.

From (2.1) and the conditions of (8.1) we obtain 9

(8.1)

In figure 8 and figure 9 we show the experimental results with the open circles and the calculated results with the solid circles. The experimental points fall slightly higher than the calculated values, as the motion of the upper platen would lead one to expect.

At the limit of zero rate of shear, (8.2) reduces to

Differentiating (8.3) with respect to t we get

_ a-(t) = C(t) . l'

(8.3)

(8.4)

In principle we can obtain C(t) from this limit, but this method is not an accurate one. Since in the previ­ous section we mentioned the errors due to the motion of the upper platen, it is interesting to look at an example where these errors are very pronounced. From (8.3) using an integration by parts we obtain

] IX 1'" ~ a(t)dt = C(t)tdt . l' 0 0

(8.5)

From eq (4.2) by taking the limit as w goes to zero , we get

. C'(W) IX hm --2-= C(t)tdt w--+O W 0

(8.6)

(7.1) 9 For brevit y, when Wappears in an int egra l withou t it s argu ments, it is unders tood tha t they are the same as for the preceding W.

38

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3

r\(W)

-I 2

FI GU RE 7: The viscosity as a fun ction of rate of shear.

The open c ircles are ex pe rim ental da ta, and the so lid circles a re calcula ted values. Th e d yna mic viscosity is a lso shown for comparison.

0

0-b :::::.

b l!l 0 ...J

-I

-2 -I LOG (I, s)

FI GU RE 8: St re~s relaxation after steody shear, for rates of shear y = O.S56 s- '(I ), y= 1. 77 s- '(li) , and y= 11.1 s- '(II/ ).

The open c ircles arc experi mental data , and the solid circles are calcula tcc!.

and from (8.5) and (8.6) we obtain

1 f oe G' (w) -: cr (t)dt = lim --.,-' y 0 w --> O w-

(8.7)

In figure 10 we show a plot of

y L" cr ( t ) cit

39

0

.£ b ;::,.

b l!l lZl 9-1

0

-2 -I o LOG (I, s)

FIGURE 9: Stres> relaxation a}ier steady sil ear, for rate; of shear y= 0.177 5- '(1 V), y= 1.11 s- ' (V), and y= 5.56 s- ' (VI).

The open ci rcles are experim ental data , and the solid ci rcles are calculated.

versus y using different torsion bars. The error intro­duced by the motion of the platen is very dramatic.

9. Discussion

The good agreem ent be tween th e ex pe rim e ntal data and the calculated values shows the validity of the BKZ theory even for mate rials whe re the sh ear r elaxation modulus falls very qui c kly. The relatively

Page 8: Simple shearing flows in polyisobutylene solutions · Key words: BKZ fiuid ; nonlin ear behavior; polyisobutylene; stress relaxati on; ... examining a single step stress relaxation

<D o -'

o

-2 -I LOG (~,5- 1 )

DIA. IN ~ 1/32

• 1/16

o 1/8 -0- 1/4

o

FIG URE 10. Varialion oj'Y f. x a(t)dl as a ./unclion oj' y using eli/ {)

./erelll lorsioll !Jars, where a(t) is the measured slress ({Iier Ihe cessalion o/sleady shear.

simple form that we used to represe nt the function W(y, t) seems to describe the behavior adequately, at least within the range of shearing deformations of our experiments. The separation of W(y, t) into a product of two functions, one of time and one of strain, i.e., W(y, t) =G(t)Wu(y), may be an oversimplifica­tion. Although a more co mplicated form of W(y, t) gave us be tter agreement, we felt that the uncertainty in our experimental data did not justify its use.

Our purpose in this paper is not to establish a unique form of W (y, t), but rather to show how a wide variety of measurements from differe nt shear histori es can be related. Indeed , we know that the behavior of plasti cized PVC is not consistent with a W(y, t) which is a product of a function of strain and a function of time. Experiments on normal stresses are more critically depe ndent on the values of W (y, t) at long times and large strains. For instance , the first normal stress differe nce, <TII(t)-<TZ2(t), for a suddenly

applied constant rate of shear, given by eq (6.1), can be calculated from [4]

<TII(t)-<TZZ(t)=y2 L W(yg, 0 (2+aa\:~)gdr

(9.1)

In general, if the function W is such that at high values of y we have

a In W < -2 a In y

(9 .2)

then the maximum of <TII(t)-<TZZ(t) will occur at time tl/l for which

a In W( 1'tl/l' tl/') a In y

-2.

For longe r times <TII(t) -<Tzz(t) will tend to level to a lower value. This behavior of the first normal stress difference is roughly similar to that of the shear stress. There are clear differen ces however; a comparison of eq (9.1) with eq (6.2) shows that th e overshoot for the shearing stress, if it occurs, must do so at an earlier time than tl/l. It may well be possible , however , to find a form of W(y, t) co mpatible with the shear s tress data of thi s paper which never satisfies the co ndition (9.2) for any value of y_

1 O. References

[1 1 Bernstein . B .. Kearsley. E. A., and Zapas. L. .J., Trans. Soc. Rheo!. 7, 391-410 (1963).

12J Zapas, L. J., and Craft, T., J. Res. Na t. Bur. Stand. (U.S.), 69A Whys. and Chem.), No.6, 541 - 546 (1965).

[3J Broadbent, .J. M., Kaye, A., Lodge, A. S. , and Vale, D. G., Nature 217,55 (1968).

[4J Bernstein, B .. Acta. Mechanica, II , 10 . 4, 329--3S4 (1966). lSI Bernstein , B. , and Fosdick, R. L. , Rh eo logica Acta 9, 106 (1970). 161 Fe rry, J. D., Viscoelastic Properties of Polymers (John Wiley,

New York , 1961). 171 Marvin, R. S., Phys. Rev. 86,644 (1952). [81 Zapas, L. .I ., and Marv in , R. S., A Correction for a Non·Zero

Loading Time in Stress Relaxation (in preparation). [9 1 Middleman , S., Trans. Soc. Rheol. 13,123 (1969).

I IOJ DeWitt , T. W., Markov itz, H. , Padden , F . .I ., and Zapa s, L..J. , J. Colloid Sci. 10,174- 188 (1955).

(paper 75Al - 648)

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