1929
DOI: 10.1007/bf01496959
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Ueber die rechnerische Darstellung des Strukturgebietes der Viskosität

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Cited by 143 publications
(58 citation statements)
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“…[15] The viscous behavior of the disperse system may be described by the consistency K and the flow index n in a power law according to the Ostwald-de-Waele model. [17] However, slurries used for RPC manufacturing are commonly characterized by the presence of a yield point. The Ostwald-de-Waele model does not take a yield point into account as with the Bingham equation, for example, which, on the contrary, is not able to approximate a nonNewtonian, or shear thinning fluid.…”
Section: Rheological Behaviormentioning
confidence: 99%
“…[15] The viscous behavior of the disperse system may be described by the consistency K and the flow index n in a power law according to the Ostwald-de-Waele model. [17] However, slurries used for RPC manufacturing are commonly characterized by the presence of a yield point. The Ostwald-de-Waele model does not take a yield point into account as with the Bingham equation, for example, which, on the contrary, is not able to approximate a nonNewtonian, or shear thinning fluid.…”
Section: Rheological Behaviormentioning
confidence: 99%
“…[19] The exponent n indicates Newtonian behavior for n ¼ 1 and decreases with increasing pseudoplastic (shear thinning) behavior to n << 1. None of the investigated slurries exhibited a thixotropic behavior.…”
Section: Rheological Investigationsmentioning
confidence: 99%
“…94,138,[334][335][336] This shear-thinning behavior was described by a power law or Ostwald-de Waele relationship as shown in Eq. (17), 147,337 where g is viscosity, c is shear rate, and K and n are fitting parameters. K is known as the flow consistency index, giving the viscosity at a shear rate of 1 s…”
Section: A Suspension Viscositymentioning
confidence: 99%