By Richardson J.F., Backhurst J.R., Harker J.H.
Quantity five is a set of suggestions to the issues within the new (3rd) version of quantity 2. it's been written at the same time with the education of the recent variation of quantity 2 and vast reference has been made to the equations and assets of knowledge in that quantity in any respect levels. during this feel the e-book is complementary to quantity 2. The operating all through is in SI devices
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Additional resources for Solutions To The Problems In Coulson & Richardson's Chemical Engineering
39. If a mixture of equal volumes of the two particles is fluidised, what is the relation between the voidage and fluid velocity if it is assumed that complete segregation is obtained? Solution The variation of the index n with flow conditions is fully discussed in Chapters 5 and 6 of Volume 2. The ratio uc /u0 is in general, dependent on the Reynolds number, voidage, and the ratio of particle diameter to that of the containing vessel. 2, the drag force is attributable entirely to skin friction, and at high velocities when Re > 500 skin friction becomes negligible and in these regions the ratio uc /u0 is independent of Re.
24(1 + e)2 − 9e] and: This relationship is plotted in Figure 6a. 6 Voidage e Figure 6a. 6 Obtain a relationship for the ratio of the terminal falling velocity of a particle to the minimum fluidising velocity for a bed of similar particles. It may be assumed that Stokes’ Law and the Carman-Kozeny equation are applicable. 4? Solution In a fluidised bed the total frictional force must be equal to the effective weight of bed. 7 . 3 of Chapter 4. 5, which agrees with the solution to that problem. 7 A packed bed consisting of uniform spherical particles of diameter 3 mm and density 4200 kg/m3 , is fluidised by means of a liquid of viscosity 1 mN s/m2 and density 1100 kg/m3 .
1. 3 kN/m2 and 293 K. 6 kg/m2 s, what is the pressure drop across the column? In making calculations, Carman’s method should be used. By how much may the liquid flow rate be increased before the column floods? 46) To take account fully of the liquid flow, reference 56 in Chapter 4 of Volume 2 provides a correction factor which depends on the liquid flowrate and the Raschig size. 18 may be used to calculate the liquid flowrate which would cause the column to flood. 2 m in diameter and 9 m tall, is packed with 25 mm Raschig rings, and used for the vacuum distillation of a mixture of isomers of molecular mass 155 kg/kmol.
Solutions To The Problems In Coulson & Richardson's Chemical Engineering by Richardson J.F., Backhurst J.R., Harker J.H.