By J R Backhurst, J H Harker, J.F. Richardson

ISBN-10: 075064950X

ISBN-13: 9780750649506

This quantity within the Coulson and Richardson sequence in chemical engineering includes complete labored strategies to the issues posed in quantity 1. when the most quantity includes illustrative labored examples through the textual content, this ebook comprises solutions to the tougher questions posed on the finish of every bankruptcy of the most text.These questions are of either a customary and non-standard nature, and so will turn out to be of curiosity to either educational employees educating classes during this region and to the prepared scholar. Chemical engineers in who're searching for a customary technique to a real-life challenge also will locate the ebook of substantial interest.* a useful resource of knowledge for the scholar learning the fabric contained in Chemical Engineering quantity 1* A precious approach to studying - solutions are defined in complete

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**Additional resources for Chemical Engineering: Solutions Volume 1**

**Sample text**

Annual charges are a fraction ˇ of the capital cost. Obtain an expression for the optimum pipe diameter on a minimum cost basis for a fluid of density and viscosity flowing at a mass rate of G. Assume that the fluid is in turbulent flow and that the Blasius equation is applicable, that is the friction factor is proportional to the Reynolds number to the power of minus one quarter. Indicate clearly how the optimum diameter depends on flowrate and fluid properties. Solution The total annual cost of a pipeline consists of a capital charge plus the running costs.

03 Ns/m2 . 03 D 4220 For a smooth pipe, Fig. 0048 for this value of Re. 3 m diameter pipeline. As a result of frictional heating, the temperature of the oil is 20 deg K higher at the refinery end than at the terminal end of the pipe and the viscosity has fallen to one half its original value. What is the ratio of the pressure gradient in the pipeline at the refinery end to that at the terminal end? Viscosity of oil at terminal D 90 mNs/m2 . Density of oil (approximately constant) D 960 kg/m3 . Flowrate of oil D 20,000 tonne/day.

0005 respectively. From Fig. 6 kN/m2 In addition, there will be a small pressure drop at the junction of the two pipes although this has been neglected in this solution. Thus the existing pump is satisfactory for this duty. 11 Explain the phenomenon of hydraulic jump which occurs during the flow of a liquid in an open channel. 5 m/s and a depth of 75 mm. Calculate, from first principles, the corresponding velocity and depth after the jump. 9. 12 What is a non-Newtonian fluid? Describe the principal types of behaviour exhibited by these fluids.

### Chemical Engineering: Solutions Volume 1 by J R Backhurst, J H Harker, J.F. Richardson

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