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The design of hydraulic systems of slurry transport demands a special attention due to coarse particles present a settling behavior inside the pipes. In this situation, the transport velocity should have order of magnitude sufficient to promote the suspension and the transport of particles, avoiding the solids deposition at the bottom of pipe. The transport of mineral slurries containing coarse particles was the primary goal of the thesis. A survey of the available literature was done and through the experimental tests could be possible to raise a data bank in order to develop a new best fit correlation for the critical velocity (VC) which included the particle shape effect, through the sphericity function. VC could be defined as the minimum velocity where a moving bed of particles takes place at the bottom of the horizontal pipe and it is slightly above the deposition velocity VD, which could be characterized by a bed of stationary particles at the bottom of pipe. The research was conducted using two recirculating pipe test rigs with transparent PVC pipe of 25.4mm and 50.8mm internal diameter with slurry concentrations from 8% up to 27% by volume. The material used was apatite and hematite concentrates and quartz mineral, clustered in two classes of size range (-0.297+0.210mm; -0.149+0.105mm), where the variables were: i) Head losses per meter of horizontal pipe (ΔP/L), ii) Mean transport velocity (V), iii) solids distribution profile, iv) particle shape effect, through the sphericity function (ψ), v) density of particles and liquid, vi) Volumetric concentration of slurries, vii) particles size and viii) pipe diameter. The critical velocity (VC), for each studied condition, was visually determined through the transparent sections of the pipes. The results have yielded a new semi empirical model to predict the critical velocity, yielding a deviation of less than 10% from the observed values of experimental data for VC.

Modelagem da velocidade crítica de transporte de polpas minerais contendo partículas grossas.