1996
DOI: 10.1016/s0016-2361(96)00166-4
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Rheological behaviour of multiphase slurries for combustion applications

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Cited by 4 publications
(3 citation statements)
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“…A linear shear stress−shear rate relationship with an initial shear stress threshold is found for both of the surfactants. This clearly indicates non-Newtonian , characteristics of the water suspension of the coal samples in the weight concentration range of 55−64.8%. The linear plot with an initial intercept as shown in a representative plot (panels a−c of Figure ) also indicates that these fluids belong to Bingham plastic fluids obeying eq τ = τ 0 + γ η where τ and γ denote shear stress and applied shear rate, respectively.…”
Section: Resultsmentioning
confidence: 71%
“…A linear shear stress−shear rate relationship with an initial shear stress threshold is found for both of the surfactants. This clearly indicates non-Newtonian , characteristics of the water suspension of the coal samples in the weight concentration range of 55−64.8%. The linear plot with an initial intercept as shown in a representative plot (panels a−c of Figure ) also indicates that these fluids belong to Bingham plastic fluids obeying eq τ = τ 0 + γ η where τ and γ denote shear stress and applied shear rate, respectively.…”
Section: Resultsmentioning
confidence: 71%
“…14 In the presence of both surfactants, the fly ash–water slurry shows a linear relation between shear stress and shear rate with an early shear yield stress value, indicating a non-Newtonian Bingham plastic fluid in a solid weight fraction range of 50–64%. 27,28 The slurry follows the equation of the Bingham plastic modelwhere γ and τ indicate the applied shear rate and shear stress, respectively. τ 0 is the yield stress, and η is defined as the Bingham viscosity.…”
Section: Resultsmentioning
confidence: 99%
“…On the measurement of shear stress, varying the shear rate of the fly ash–water slurry containing different solid weight ratios of fly ash in the presence of 0.017 g/ cc saponin, we have compared the flow characteristic of slurry with CTAB, a commercial dispersant . In the presence of both surfactants, the fly ash–water slurry shows a linear relation between shear stress and shear rate with an early shear yield stress value, indicating a non-Newtonian Bingham plastic fluid in a solid weight fraction range of 50–64%. , The slurry follows the equation of the Bingham plastic model where γ and τ indicate the applied shear rate and shear stress, respectively. τ 0 is the yield stress, and η is defined as the Bingham viscosity.…”
Section: Resultsmentioning
confidence: 99%