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For this model, there are two inputs (no-slip holdup and Froude Number), and three outputs (Beggs and Brill Parameters a, b and c) which are associated with a particular flow regime. After the prediction of a, b and c, the slip Hold-up is calculated, which is one of the basic parameters of pressure drop calculation. Pressure drop in two-phase flow is a major design variable, governing the pumping power required to transport two-phase fluids and also governing the recirculation rate in natural circulation systems. ... Perhaps the most widely used of these corrections to the homogeneous model is the correlation of Beggs and Brill (1973), which corrects the. Two Phase Flow - Beggs & Brill Method Pipe Roughness Gas Flowrate m 3 /h Nm 3 /h @ 1 atm, 0 C Flowing Temperature Deg C Inlet Pressure bar psi Deg F SCFM @ 14.7 PSI, 60 F Density Kg/m 3 lb/ft 3 Viscosity cP lb/ft.s. Beggs and Brill correlation. Calculate the Z factor with the Brill - >Beggs</b> correlation. z.BeggsBrill ( pres.pr, temp.pr, tolerance = 1e-13, verbose = FALSE).
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