Select Chapter >> | TOC | Preface | 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 | 13 | 14 | 15 | 16 | 17 | 18 | Appendices |
Chapter 13: Unsteady State Nonisothermal Reactor Design
Additional Homework Problems
CDP13-BC
A heat exchanger and a controller are to be
added to the ammonium nitrate reactor discussed in Problem P9-3 from the 4th edition of Elements of Chemical Reaction Engineering. The reactor
temperature is to be controlled by manipulating the coolant flow rate,
in the heat exchanger. The ambient temperature at the time the controller
is turned on is 970°R. The product of the heat-transfer coefficient
and heat-exchanger area is UA = 10,000 Btu/h |
||
The controller is to be a PI controller with an integral
time, ![]() |
||
For each of the following three cases, plot the reactor temperature and mass in the reactor, M, as a function of time. [Hint: First show that the energy balance can be written as | ||
![]() |
||
(a) Consider Mconstant at 300 lb. |
||
![]() |
||
The set-point of the mass in the tank is 325 lb.
|