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However, heavy crude oil emulsion exhibits either Newtonian behaviour at high shear rate or a shear thinning rheological behaviour at low shear rate (McKibben et al. 2000; Al-Roomi et al. 2004).
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Rheological testing revealed Newtonian-like response to shear below 10 s−1 and pseudoplastic behavior at higher shear.
At low shear rate, both materials show a Newtonian behaviour, while at high shear rate, the viscosity linearly decreases as a non-Newtonian fluid described in Carreau model [34].
The melt rheological behaviour of a low molecular weight tri-block copolymer revealed a low melt viscosity at high shear rates, and a high viscosity at low shear rates.
At high shear rate, they reveal shear-thinning behavior, which is the apparent viscosity reduction by increasing shear rate.
At high shear rate, it reveals shear-thinning behavior (i.e., apparent viscosity reduction by increasing shear rate).
All PUAE solutions exhibited non-Newtonian shear-thinning pseudoplastic behaviour that was accurately described by the Carreau model but was better fit by the power-law model at high shear rates (≥1/s), which demonstrated that the variation in the apparent viscosity dependence was greater at higher concentrations and shear rates.
Shear thinning at high shear rate overcomes injection problems.
PV was measured at high shear rate (200/s) and low shear rate (50/s).
According to Fig. 3, gellan gum demonstrates high viscosity at low shear rate, but low viscosity at high shear rate.
The dispersions with the graphite particles are shear thinning at low shear rates and approach a constant dynamic viscosity at high shear rates.
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