Open channels have been used in the pulp and paper industry for fibre
suspension containment, tree log transport, spillage and storage tank
overflows and effluent removal. Open channels could have other uses su
ch as in steep bleaching, but no engineering design data or methods ha
ve been proposed in the technical literature. Flow data were obtained
in four rectangular channels for water and a bleached pine kraft fibre
suspension at pulp concentrations ranging from 0.5 to 2.25 per cent w
hen flowing in channels of various widths at slopes ranging from 1 deg
rees to 10 degrees. Various flow mechanisms were deduced from visual o
bservations and are described. A logarithmic resistance formula simila
r to the Prantl-Karman-Nikuradse equations for pipe Row was used succe
ssfully to model the flow resistance. Linear correlations were obtaine
d at each fibre concentration, channel width and slope. Coefficients i
n the equation were found to be a function of pulp concentration, chan
nel slope, width and surface roughness. The equation provides a basis
for open channel design.