By J R Backhurst, J H Harker, J.F. Richardson
This quantity within the Coulson and Richardson sequence in chemical engineering includes complete labored recommendations to the issues posed in quantity 1. while the most quantity includes illustrative labored examples through the textual content, this publication includes solutions to the tougher questions posed on the finish of every bankruptcy of the most text.
those questions are of either a customary and non-standard nature, and so will turn out to be of curiosity to either educational employees instructing classes during this quarter and to the prepared pupil. Chemical engineers in who're trying to find a typical method to a real-life challenge also will locate the ebook of substantial curiosity.
* a useful resource of data for the scholar learning the cloth contained in Chemical Engineering quantity 1
* A useful approach to studying - solutions are defined in complete
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Extra resources for Chemical engineering. Solutions to the problems in chemical engineering
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.
After a length l, the liquid is discharged into a tank. 5 Assume a fully developed flow with R/ u2 D 8 Re 1 . 15 m diameter to storage tanks situated 100 m away. The pressure drop along the pipe is 70 kN/m2 . The pipeline has to be repaired and it is necessary to pump the liquid by an alternative route consisting of 70 m of 200 mm pipe followed by 50 m of 100 mm pipe. If the existing pump is capable of developing a pressure of 300 kN/m2 , will it be suitable for use during the period required for the repairs?
12 What is a non-Newtonian fluid? Describe the principal types of behaviour exhibited by these fluids. 5 where a is the viscosity, and du/dr is the velocity gradient normal to the direction of motion. Show that the volumetric rate of streamline flow through a horizontal tube of radius a is: P 2 a5 5 2kl where P is the pressure drop over a length l of the tube. 123. 5 The fluid is therefore shear-thinning. 025 N s/m2 ). 002. From Fig. 0046. 32 m/s. 14 The relation between cost per unit length C of a pipeline installation and its diameter d is given by: C D a C bd where a and b are independent of pipe size.