Chemical Engineering: Solutions to the Problems in Volumes 2 - download pdf or read online

By J H Harker

ISBN-10: 0750656395

ISBN-13: 9780750656399

ISBN-10: 1417502037

ISBN-13: 9781417502035

Richardson et al give you the scholar of chemical engineering with complete labored options to the issues posed in Chemical Engineering quantity 2 ''Particle know-how and Separation Processes'' fifth version, and Chemical Engineering quantity three ''Chemical and Biochemical Reactors & method Control'' third version. while the most volumes includes illustrative labored examples during the textual content, this e-book comprises solutions to the tougher questions posed on the finish of every bankruptcy of the most texts. those questions are of either a regular and non-standard nature, and so will turn out to be of curiosity to either educational employees educating classes during this quarter and to the willing pupil. Chemical engineers in who're trying to find a typical technique to a real-life challenge also will locate the ebook of substantial curiosity. * includes absolutely labored recommendations to the issues posed in Chemical Engineering Volumes 2 and three * allows the reader to get the utmost make the most of utilizing Volumes 2 and three * a really powerful approach to studying

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Additional info for Chemical Engineering: Solutions to the Problems in Volumes 2 & 3

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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.

It may be assumed that Stokes’ Law is applicable, and the effect of added mass of the liquid moved with each sphere may be ignored. 18 A binary suspension consists of equal masses of spherical particles of the same shape and density whose free falling velocities in the liquid are 1 mm/s and 2 mm/s, respectively. 2. As sedimentation proceeds, a sharp interface forms between the clear liquid and suspension consisting only of small particles, and a second interface separates the suspension of fines from the mixed suspension.

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. 3 kN/m2 . Obtain an expression for the pressure drop on the assumption that this is not appreciably affected by the liquid flow and may be calculated using a modified form of Carman’s equation. 125 kg/m2 . 4 m3 /kmol. 5. 71)3 = 909G′ kg/m3 ρ/P = ρs /Ps where subscript s refers to the still. 22 m in diameter and 9 m high, and packed with 25 mm Raschig rings, is used for the vacuum distillation of a mixture of isomers of molecular mass 155 kg/kmol.

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Chemical Engineering: Solutions to the Problems in Volumes 2 & 3 by J H Harker

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