Answers are grounded in this paper and cite their sources.
Flow experiments give an equation relating to S in terms of measurable quantities, where is the inter-granular porosity of the bed, and S is the envelope surface area of the granules in 1 cm 3 of bed. Heywood's shape factors for the granules give a second equation relating to S. Using the two equations and S can be determined uniquely. If the tortuosity factor be taken to be π/2 in the equations given previously (Jones 1956), connecting the friction factor λ and the Reynolds number (Re), then λ = 16/(Re) for granular beds, as for long straight tubes.
No takes yet. Share an insight, caveat, or question.
Jones et al. (1961) studied this question.
Synapse has enriched 10 related papers. Consider them for comparative context: