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A method is proposed for the direct determination of the rate of shear-shearing stress curve of a fluid from data obtained in concentric cylinder viscometers. The method involves the use of a viscometer in which the ratio of outer to inner cylinder radii can be varied. It is further shown that to a close approximation two such radius ratios are sufficient to define the flow curve. Data for two non-Newtonian systems are presented to show that the proposed method is valid.
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Krieger et al. (1952) studied this question.
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