(4) At a reaction temperature of 1000 K, when Cg = 1 mol/L, which one of the two products (i.e., D vs. U) has a higher formation rate? Explain your answer. (5) To promote the formation of D, should we use CSTR or PFR? Why? Assume that mass transfer is not limiting. (6) To promote the formation of D, should we operate the reaction at a higher or lower temperature? Why?

Why is it important to indicate the wavelength of light used in your experimental data and on the Beer's Law plot?

What can be said about the three distillate (s) and bottoms products that would be produced in any column that is designed and operated as shown?

in packed towers experiment, The Ergun equation is a fine starting point for typical use in helping size/design columns in a variety of applications, however it makes numerous assumptions and approximations in its derivation.  Can you name and explain (why) 2 regimes of operation where you clearly think the Ergun equation (at least the one we use in this class) would not be appropriate to use in column design?