Chapter 13

1 If the heat capacities were given in terms of mass (i.e., CPsm = J/g · K), then both FA0 and NA0 would have to be converted to mass:

2 Adapted from the problem by Ronald Willey, Seminar on a Nitroaniline Reactor Rupture. Prepared for SAChE, Center for Chemical Process Safety, American Institute of Chemical Engineers, New York (1994). Also see Process Safety Progress, vol. 20, no. 2 (2001), pp. 123–129. The values of ΔHRx and UA were estimated from the plant data of the temperature-time trajectory in the article by G. C. Vincent, Loss Prevention, 5, 46–52.

3 Value for k from J. M. Smith, Chemical Engineering Kinetics, 3rd ed. (New York: McGraw-Hill, 1981), p. 205. Note that ΔHRx and KC were calculated from values given in Perry’s Chemical Engineers’ Handbook, 6th ed. (New York: McGraw-Hill, 1984), pp. 3-147.

4 This example was coauthored by Professors Ronald J. Willey, Northeastern University, Michael B. Cutlip, University of Connecticut, and H. Scott Fogler, University of Michigan.

5 S. Abia, A. E. Humphrey, and N. F. Mills, Biochemical Engineering (New York: Academic Press, 1973).

..................Content has been hidden....................

You can't read the all page of ebook, please click here login for view all page.
Reset
3.227.239.9