By R. K. Sinnott (Auth.)
This second version of Coulson & Richardson's vintage Chemical Engineering textual content offers an entire replace and revision of Volume 6: An advent to Design. It offers a revised and up to date creation to the method and systems for method layout and method apparatus choice and layout for the chemical procedure and allied industries. It comprises fabric on circulation sheeting, piping and instrumentation, mechanical layout of kit, costing and undertaking overview, protection and loss prevention. the cloth on security and loss prevention and environmental defense has been revised to hide present systems and laws. strategy integration and using warmth pumps has been incorporated within the bankruptcy on strength utilisation. extra fabric has been further on warmth move gear; agitated vessels are actually lined and the dialogue of fired warmers and plate warmth exchangers prolonged. The appendices were prolonged to incorporate a working laptop or computer software for strength balances, illustrations of apparatus specification sheets and warmth exchanger tube format diagrams.
This 2d version will proceed to supply undergraduate scholars of chemical engineering, chemical engineers in and chemists and mechanical engineers, who've to take on difficulties bobbing up within the procedure industries, with a worthy textual content on how a whole strategy is designed and the way it has to be outfitted into the surroundings
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Extra info for Coulson and Richardson's Chemical Engineering. Chemical Engineering Design
Select the boundary round any stage so as to reduce the number of unknown streams to as few as possible. 4. 14). 4 Selection of system boundaries and organisation of the solution. Short stop Monomer water Catalyst Polymer Filter Dryer Reactor Recovery column Recycle monomer Effluent The diagram shows the main steps in a process for producing a polymer. From the following data, calculate the stream flows for a production rate of 10,000 kg/h. 5 kg/ 1000 kg unreacted monomer Filter, wash water approx.
WHITWELL, J. C. and TONER, R. K. Conservation of Mass and Energy (McGraw- Hill, 1969). WILLIAMS, E. T. and JAckson, R. C. Stoichiometry for Chemical Engineers (McGraw-Hill, 1958). Advanced texts HENLEY, E. J. and ROSEN, E. M. (1969) Material and Energy Balance Computations (Wiley). MYERs, A. L. and SEIDER, W. D. (1976) Introduction to Chemical Engineering and Computer Calculations (Prentice-Hall). 20.
If the acetone concentration in the feed suddenly rises to 1000 ppm, due to a spill in the process plant, and stays at that level for half an hour, will the limit of 200 ppm in the effluent discharge be exceeded? Solution Capacity 500 m 3 4 5000 kg / h I00— I00 --y ( ? ) p pm 000 ppm Basis: increment of time Dt. To illustrate the general solution to this type of problem, the balance will be set up in terms of symbols for all the quantities and then actual values for this example substituted. Let, Material in the tank = M, Flow-rate = F, Initial concentration in the tank = Co , Concentration at time t after the feed concentration is increased = C, Concentration in the effluent feed = C 1 , Change in concentration over time increment Dt = DC, Average concentration in the tank during the time increment = Cap.