Page 366 - Elements of Chemical Reaction Engineering Ebook

Chap. 6 Supplementary Reading 337
Given a batch reactor with A a a D, calculatie the
B
composition after 6.5 h. [lst Ed. P9-111
Chlorination of benzene to monochlorobenzene and dichlorobenzene
in a CSTR. [lst Ed. P9-141
Determine the number of independent reactions in the oxidation of
munonia. [lst Ed. P9-171
Oxidation of formaldehyde:
1
HCHO + 20, " > HCOOH

2HCHO " > HCOOCH, [2ndEd.P9-13Bl

Continuation of CDP6-H.
HCOOH " > CO2+H2

HCOOH k4 @O+H20 t2ndEkl. p9-14~1

CLIP6 JB Continuation of CDP6-H and I:
HCOOCH, k4 > CH30H + HCOOH [2nd Ed. P9-15,]
Design a reactor for the alkylation of benzene with propylene to max-
imize the selectivity of isopropylbenzene. [Proc. 2nd Joint China/USA
Chem. Eng. Con$ Ill, 51, (199711.
Reactions between paraffins and olefins to form highly brancheld par-
affins are carried out in a slurry reactor to increase the octane nimber
in gasoline. [Chem. Eng. Sci. 51, 10, 2053 (1996)l.
Design a reaction system to maximize the production of alkyl chlo-
ride. [lst Ed. P9-191
Design a reaction system to maximize the selectivity of p-xylene from
methanol and toluene over a HZSM-8 zeolite catalyst. [2nd Ed. 13-17]
Oxidation of propylene to acrolein (Chem. Eng. Sei. 51,2189 (1'996)).

SUPPLEMENTARY READING

1. Selectivity, reactor schemes, and staging for multiple reactions, together with eval-
uation of the corresponding design equations, are presented in

DENBIGH, K. G., and J. C. R. TURNER, Chemical Reactor Theory, 2nd ed. Cam-
bridge: Cambridge University Press, 1971, Chap. 6.
O.,
LEVENSPIEL, Chemical Reaction Engineering, 2nd ed. New York Wiley,
1972, Chap. 7.
Some example problems on reactor design for multiple reactions are presented in
HOUGEN, 0. A., and K. M. WATSON, Chemical Pracess Principles, 1% 3:
Kinetics and Catalysis. New York: Wiley, 1947. Chap. XVIII.