Page 249 - Elements of Chemical Reaction Engineering 3rd Edition

Chap. 4 CD-ROM Material 221
B. Solution to California Registration Exam Problem
C. Ten Types of Home Problems: 20 Solved Problems
5. Analogy of CRE Algorithms to a Menu in a Fine French Restaurant
6. Algorithm for Gas Phase Reaction
e Living Example Problems
J. Example 4-7 Pressure Drop with Reaction-Numerical Solution
2. Example 4-8 Dehydrogenation in a Spherical Reactor
3. Example 4-9 Working in Terms of Molar Flow Rate in a PFR
4. Example 4-10 Membrane Reactor
5. Example 4-11 Isothermal Semibatch Reactor with a Second-order Reaction
e Professional Reference Shelf
1. Time to Reach Steady State for a 1st Order Reaction in a CSTR
2. Recycle Reactors
3. Crifiquing Journal Articles
e FAQ [Frequently Asked Questions]- In UpdatesFAQ icon section
a Additional Homework Problems

A sinister gentlemen is interested in producing methyl perchlorate in
a batch reactor. The reactor has a strange and unsettling rate law [2nd
Ed. P4-281
(Ecological Engineering) A much more complicated version of Prob-
lem 4-17 uses actual pond (CSTR) sizes and flow rates in modeling
the site with CSTRs for the Des Plaines River experimental wetlands
site (EW3) in order to degrade atrazine.
The rate of binding ligands ta receptors is studied in this app1ic:ation
of reaction kinetics to bioengineering. The time to bind 50% of the
ligands to the receptors is required. [2nd Ed. P4-341
A batch reactor is used for the bromination of p-chlorophenyl islopro-
pyl ether. Calculate the batch reaction time. [Znd Ed. P4-291
California Professional Engineers Exam Problem in which the reaction
B-t-H, --+ A
is carried out in a batch reactor. [2nd Ed. P4-151
The gas-phase reaction
A+2B ---+ 2D
has the rate law -rA = 2.5C),WB. Reactor volumes of PFRs and
CSTRs are required in this multipart problem. [2nd Ed. P4-211
What type and arrangement of jlow reactors should you use for a
decomposition reaction with the rate law -rA = k,C),’,/( 1 + k,CA)?
[2nd Ed. P4-141
Verify that the liquid-phase reaction of 5,6-benzoquinoline with
hydrogen is pseudo-first-order. [2nd Ed. P4-71
The liquid-phase reaction
2A-t-B e
C+D
is carried out in a semibatch reactor. Plot the conversion, volume, and
species concyntration as a function of time. Reactive distillatioln is
also considered in part (e). [2nd Ed. P4-271
Designed to reinforce the basic CRE principles through very straight
forward calculations of CSTR and PFR volumes and a batch reactor