By Charles G. Hill
Some of the most acclaimed books within the box, Introduction to Chemical Engineering Kinetics and Reactor Design presents an introductory textual content concentrating on chemical kinetics and reactor for chemical engineering scholars. This new moment variation is totally revised and up to date to incorporate lots of intellectually stimulating difficulties (more than eighty% are new) encompassing quite a lot of chemical engineering subject matters, together with such new components as organic structures and nano expertise.
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Extra info for Introduction to Chemical Engineering Kinetics and Reactor Design
Since several of these variables may change from location to location within the reactor under consideration, knowledge of the relationships between these variables and the conversion rate is needed if one is to be able to integrate the appropriate material balance equations over the reactor volume. It is important to note that in many situations of practical engineering importance, the rate of reaction observed is not identical with the intrinsic chemical reaction rate evaluated using the bulk fluid properties.
We start by treating constant-volume systems that lead to closed-form solutions and then proceed to the complications present in variable-volume systems. We have chosen to place a “V” to the right of certain equation numbers in this section to emphasize to the reader 25 that these equations are not general but are restricted to constant volume systems. The use of ξ∗ , the extent of reaction per unit volume in a constant volume system, will also emphasize this restriction. 8) V In graphical form, the preceding two equations imply that for first-order reactions, plots of lnCA versus time will be linear with a slope equal to − k and an intercept equal to lnCA0 .
The exit gases leave at a pressure of 4 atm. The data follow. 3 Mean heat capacity (Cp ) over the temperature range of interest [cal∕(mol⋅∘ C)] Standard states are taken as the gases at unit fugacity. Ideal gas behavior may be assumed. Do not use any thermochemical data other than those given above. Remember to allow for the variation in the heat of reaction with temperature. What would be the potential advantages and disadvantages of increasing the operating pressure to 8 atm or to 40 atm? You may again assume ideal gas behavior to determine effluent compositions and temperatures for these cases.
Introduction to Chemical Engineering Kinetics and Reactor Design by Charles G. Hill