By H. Scott Fogler
Nice constitution to make sure rules are essentially understood and will be appliedafter the of entirety of the booklet. this can be completed first via a dialogue ofcritical pondering and the way Socratic wondering is on the center of criticalthinking, through examples of severe considering questions, after which finallyexercises on severe considering. comprises extra insurance of business chemistrywith genuine reactors and genuine reactions and extends the wide variety of applicationsto which chemical response engineering ideas will be utilized. via theuse of an interactive CDROM that's gotten smaller wrapped with the textual content andcorresponding online page the ebook and source fabric is designed to addressdifferent pupil studying kinds in keeping with the Felder-Solomon LearningStyle Index. (e.g. global/sequential, active/reflective, verbal/visual andsensing/intuitive)
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Additional resources for Elements of chemical reaction engineering
ICM Kinetics Challenge 1 Performance # Example 1-1 Calculate the volume of a CSTR for the conditions used to figure the plug-lion reactor volume in Example E -1. Which volume i s larger. the PFR or the CSTR'? Explain why. Suggest two ways to work t h ~ sproblem ~ncorrec~ly. Calculate the rime ra reduce the number o f moles of A to 19 of its initial value in a constant-volume batch reactor for the reaction and data in Example 1 - 1 . \%'hat assumptions were made in the dcrivat~onof the design equation for: la) the batch reactor?
In this classical approach to chemical change, it is assumed that the total mass is neither created nor destroyed when n chemicill reaction occurs. The mass refemd to is the totar collective mass of a11 the different species in the system. However, when considering the individual species involved in a particular reaction, we do speak of the rate of disappearance of mass of a particular species. The ,artJ nf disoppeorolzce of n species, say species A, i s the trtrntber ($A mnlrc~ries[hot lose their chemical i d t w t i ~per ~rtrirt i r l l ~per ~rnirvc~iumefhrn~rghfhe breaking and slrbreqiienr re-forming of ckentical bonds drrring the course of the reartion.
Frnln Figure 15-12 of the Peters and Tirnmerhaus book. -in. pipe for single tube? and approximately 520 to $50 per square font of \usface area for fixed-tube sheet exchangers. A packed-bed (also called a hxed-bed) reactor is essentially a tubular renctor that is packed w~rhsolid satatyst panicles (Figure 1-1 3). eactionx. This reactor has the same difiicultiec with temperature conlrol a\ nther tubular reactors: in addition. he c:~lab\! On occasion. channeling of thc 24 Refe:enceChe1f sclu& Roblemr Mole Balances Chap.
Elements of chemical reaction engineering by H. Scott Fogler