the effect of the particle size distribution on non-newtonian turbulent ...

Preamble
n' apparent flow behaviour index
N number <strong>of</strong> items
p mixing length factor
pressure Pa
q ratio <strong>of</strong> solid to liquid oscillation amplitude
Q volumetric flow rate <strong>of</strong> slurry m 3 /s
r radius at a point in <strong>the</strong> pipe m
correlation coefficient
R radius <strong>of</strong> <strong>the</strong> pipe m
Re Reynolds number
S relative density
u point velocity m/s
u+ dimensionless velocity
V average slurry velocity m/s
V. shear velocity m/s
X unknown quantity
abscissa value
y distance from <strong>the</strong> pipe wall m
y+ dimensionless wall distance
y ordinate value
et proportional to
shape factor
shear stress ratio