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Shear-flow coupling tests were performed through shear displacement control at a shearing speed of 0.1 mm/min.
The processing conditions that contributed to an optimum gel setting were found at sago starch of level of 7.69%, sugar of 30.29%, and shearing speed of 45.86 rpm.
A three-factor three-level Box–Behnken design was adopthree-factor three-levelneous effecthree-factor three-levelvariaBox Behnkensago starch andesign5% sugar) and one processing variable (shearing speed of mixer at 20–50 rpm) on textural and rheological properties of gels.
DNA quantity and purity was assayed (via Nanodrop 1000) prior to and after DNA size reduction using a Hydroshear (Genome Solutions/Digilab) with a standard orifice set to maximal possible shearing speed (13) for 20 cycles (maximal shearing speed varies with individual orifice).
At large shearing speed, ek increases.
Moreover, the composites were also prepared by using melt compounding under the different shearing speed of extruder via our custom-built high-shear extruder.
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The faster shear speed setting produced much smaller fragments with the average length being ~1.9 kb.
The contents of stevioside and rebaudioside A in fluid extract increased with the drug size, but decreased at high shearing speeds and solvent to drug ratio, while their yields decreased at higher temperature and were not affected by turbo speed.
The fluctuating parts of the two types of energy increase with increasing shear speed.
The magnitude and recurrence time of stress drop decreased with increasing shear speed for a given particle size, however, they increased with increase of particle size at the same shear speed.
The frictional instabilities (stress drops) were constrained not only by the shear speed but also by the particle size.
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