2009
DOI: 10.1007/s11431-008-0283-6
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Rheological responses of fumed silica suspensions under steady and oscillatory shear

Abstract: Rheological experiments under steady and oscillatory shear were conducted for fumed silica suspensions in polyethylene glycol. Under steady shear the shear-thinning and thickening response were exhibited and the flow exponent N was determined. With the increase of concentration the flow exponent N showed a rapid increase, and it increased dramatically when the discontinuous shear-thickening took place. Oscillatory shear experiments were conducted at constant frequency and constant amplitude strain, respectivel… Show more

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Cited by 20 publications
(4 citation statements)
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“…From the literature, for fumed silica dispersions, it was explained that weak steric repulsive force and Brownian motion prevent further association of fumed silica aggregates at very low shear rates [73]. The viscosity of the suspension decreased by increasing shear rate because some of the agglomerations were disrupted and the orientation of fumed silica particles aligns with the direction of the shear flow [10,73,121].…”
Section: Discussionmentioning
confidence: 99%
“…From the literature, for fumed silica dispersions, it was explained that weak steric repulsive force and Brownian motion prevent further association of fumed silica aggregates at very low shear rates [73]. The viscosity of the suspension decreased by increasing shear rate because some of the agglomerations were disrupted and the orientation of fumed silica particles aligns with the direction of the shear flow [10,73,121].…”
Section: Discussionmentioning
confidence: 99%
“…From the literature, for fumed silica dispersions, it was explained that weak steric repulsive force and Brownian motion prevent further association of fumed silica aggregates at very low shear rates [73]. The viscosity of the suspension decreased by increasing shear rate because some of the agglomerations were disrupted and the orientation of fumed silica particles aligns with the direction of the shear flow [10,73,121].…”
Section: Discussionmentioning
confidence: 99%
“…The flow index n indicates the departure from Newton model and n = 1, n [ 1 and n \ 1 exhibit Newtonian, shear-thickening and shear-thinning behavior, respectively [25,26]. For n = 1, K becomes the dynamic viscosity g. Table 1 shows the values of the fitting parameters K and n, and the regression coefficient R 2 .…”
Section: Rheological Behavior and Spinnability Of The Precursor Solmentioning
confidence: 99%