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Rheology complex viscosity

Further examinations showed the temperature dependence of the structure by employing combined/hyphenated temperature-dependent measurements. By combination of T-WAXS, T-SAXS [133], temperature-dependent F solid state NMR, rheology (complex viscosity as function of temperature/frequency) [134] as well as dielectric spectroscopy [135] proved the probability of the model and the change of the structure with temperature. [Pg.259]

Viscous Hquids are classified based on their rheological behavior characterized by the relationship of shear stress with shear rate. Eor Newtonian Hquids, the viscosity represented by the ratio of shear stress to shear rate is independent of shear rate, whereas non-Newtonian Hquid viscosity changes with shear rate. Non-Newtonian Hquids are further divided into three categories time-independent, time-dependent, and viscoelastic. A detailed discussion of these rheologically complex Hquids is given elsewhere (see Rheological measurements). [Pg.427]

Generally, the rheology of polymer melts depends strongly on the temperature at which the measurement is carried out. It is well known that for thermorheological simplicity, isotherms of storage modulus (G (co)), loss modulus (G"(complex viscosity (r (co)) can be superimposed by horizontal shifts along the frequency axis ... [Pg.284]

Viseometry and rheology Intrinsic viscosity [t ] can be related to complex size via MHKS, a coefihcient... [Pg.170]

Upon mixing and injection of the caprolactam monomer streams into the rheological instrument, polymerization was initiated and continued, whereas simultaneously monitoring the complex viscosity and other rheological parameters of the polymerizing system. The maximum measurable complex viscosity levels were achieved in about 100 s or less, depending on temperature. [Pg.56]

Fig. 32 Shear-rheological behavior at 240°C of 10, and 20wt% SBM. (a) Complex viscosity as function of frequency... Fig. 32 Shear-rheological behavior at 240°C of 10, and 20wt% SBM. (a) Complex viscosity as function of frequency...
FIG. 15.46 Viscosity, 77, and first normal stress difference, Nh of Vectra 900 at 310 °C as functions of shear rate, according to Langelaan and Gotsis (1996). The first normal stress coefficient, Yi, is estimated from N, by the present author. ( ) Capillary rheometer ( ) and ( ) cone and plate rheometer ( ) complex viscosity rj (A) non-steady state values of the cone and plate rheometer. Courtesy Society of Rheology. [Pg.584]

Figure 4.17. Linear melt-state rheological properties as a function of oscillatory frequency (a) storage modulus, G and (b) loss modulus, G" (c) Dependence of complex viscosity on temperature for ABS nanocomposites. Reprinted with permission from ref (68). Figure 4.17. Linear melt-state rheological properties as a function of oscillatory frequency (a) storage modulus, G and (b) loss modulus, G" (c) Dependence of complex viscosity on temperature for ABS nanocomposites. Reprinted with permission from ref (68).
The principle rheological properties which reflect the polymer process dynamics are the loss modulus (C), storage modulus (G"), dynamic complex viscosity (n ), and tan delta parameters. In simplified form the loss modulus describes the viscous or fluid component of viscosity. That is, how easily the molecules can move past each other. The storage modulus describes the elastic or network entanglement structure of the polymers. It is, therefore, sensitive to cross linking, reaction formation and the elastomeric modifiers. The complex dynamic viscosity is the combined effect of both moduli discussed. It, therefore. [Pg.190]

In addition to relationships between apparent viscosity and dynamic or complex viscosity, those between first normal stress coefficient versus dynamic viscosity or apparent viscosity are also of interest to predict one from another for food processing or product development applications. Such relationships were derived for the quasilinear co-rotational Goddard-Miller model (Abdel-Khalik et al., 1974 Bird et al., 1974, 1977). It should be noted that a first normal stress coefficient in a flow field, V i(y), and another in an oscillatory field, fri(ct>), can be determined. Further, as discussed below, (y) can be estimated from steady shear and dynamic rheological data. [Pg.127]

Figure 5.20 Steady-state viscosity T] y) and dynamic complex viscosity rj u)) as functions of reduced shear rate (j>r) or frequency cox), for a 1.5% w/v solution of the associative thickener described in the caption to Fig. 5-18. (From Annable et al. 1993, with permission from the Journal of Rheology.)... Figure 5.20 Steady-state viscosity T] y) and dynamic complex viscosity rj u)) as functions of reduced shear rate (j>r) or frequency cox), for a 1.5% w/v solution of the associative thickener described in the caption to Fig. 5-18. (From Annable et al. 1993, with permission from the Journal of Rheology.)...
PLA The viscosity functions of PLA show the relative stability of the PLA pellets and of the as-spun fibers during rheological measurements. The differences between both functions of the complex viscosity show a low thermal degradation... [Pg.204]

Dynamic shear rheology involves measuring the resistance to dynamic oscillatory flows. Dynamic moduli such as the storage (or solid-like) modulus (G ), the loss (or fluid-like) modulus (G"), the loss tangent (tan 8 = G"IG ) and the complex viscosity ( / ) can all be used to characterize deformation resistance to dynamic oscillation of a sinusoidally imposed deformation with a characteristic frequency of oscillation (o). [Pg.171]

The complex viscosity as a function of frequency, maximum strain and temperature is generally determined with one rheometer. Standard ASTM 4440-84/90 defines the measurement of rheological parameters of polymer samples using dynamic oscillation. This standard reiterates the importance of determining the linear viscoelastic region prior to performing dynamic frequency sweeps. [Pg.341]

For the step from the 3D-rheology to the 2D-state, to the surface rheology, it is best to use the vector treatment for describing the complex variables of strain s , stress complex viscosity T , complex shear modulus G , respectively, ri and G are viscoelastic vectors. The relating vector treatment for strain in a shear deformation is shown in Fig. 3.7. [Pg.77]

The rheological behavior of these materials is still far from being fully understood but relationships between their rheology and the degree of exfoliation of the nanoparticles have been reported [73]. An increase in the steady shear flow viscosity with the clay content has been reported for most systems [62, 74], while in some cases, viscosity decreases with low clay loading [46, 75]. Another important characteristic of exfoliated nanocomposites is the loss of the complex viscosity Newtonian plateau in oscillatory shear flow [76-80]. Transient experiments have also been used to study the rheological response of polymer nanocomposites. The degree of exfoliation is associated with the amplitude of stress overshoots in start-up experiment [81]. Two main modes of relaxation have been observed in the stress relaxation (step shear) test, namely, a fast mode associated with the polymer matrix and a slow mode associated with the polymer-clay network [60]. The presence of a clay-polymer network has also been evidenced by Cole-Cole plots [82]. [Pg.588]


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