Page 105 - Separation process engineering
P. 105

C. Derivations

                        C1. Determine the effect of pressure on the temperature, separation and diameter of a flash drum.
                        C2. Solve the Rachford-Rice equation for V/F for a binary system.

                        C3. Assume that vapor pressure can be calculated from the Antoine equation and that Raoult’s law
                             can be used to calculate K values. For a binary flash system, solve for the drum pressure if drum
                             temperature and V/F are given.
                        C4. Derive Eq. (2-24) and show that it is correct.

                        C5. Choosing to use V/F to develop the Rachford-Rice equation is conventional but arbitrary. We
                             could also use L/F, the fraction remaining liquid, as the trial variable. Develop the Rachford-Rice
                             equation as f(L/F).

                        C6. In flash distillation a liquid mixture is partially vaporized. We could also take a vapor mixture
                             and partially condense it. Draw a schematic diagram of partial condensation equipment. Derive
                             the equations for this process. Are they different from flash distillation? If so, how?
                        C7. Plot Eq. (2-40) vs. V/F for Example 2-2 to illustrate that convergence is not as linear as the
                             Rachford-Rice equation.

                        C8. Show how to use a temperature composition diagram to solve a binary flash distillation problem
                             when the drum temperature, feed mole fraction, drum pressure, and feed rate are specified. Show
                             how to determine x, y, L, and V.

                        C9. For a vapor-liquid-liquid flash distillation, derive Eqs. (2-62) and (2-63) and the equations that
                             allow calculation of all the mole fractions once V/F and L              /F are known.
                                                                                              liquid_1
                    D. Problems

                    *Answers to problems with an asterisk are at the back of the book.
                       D1.* We are separating a mixture of methanol and water in a flash drum at 1 atm pressure. Equilibrium
                             data are listed in Table 2-7.

                             a. Feed is 60 mol% methanol, and 40% of the feed is vaporized. What are the vapor and liquid
                               mole fractions and flow rates? Feed rate is 100 kmol/h.

                             b. Repeat part a for a feed rate of 1500 kmol/h.
                             c. If the feed is 30 mol% methanol and we desire a liquid product that is 20 mol% methanol, what
                               V/F must be used? For a feed rate of 1000 lbmol/h, find product flow rates and compositions.

                             d. We are operating the flash drum so that the liquid mole fraction is 45 mol% methanol. L = 1500
                               kmol/h, and V/F = 0.2. What must the flow rate and composition of the feed be?
                             e. Find the dimensions of a vertical flash drum for Problem 2.D1c.

                                                                                3
                                                        3
                                Data: ρ  = 1.00 g/cm , ρ    m,L  = 0.7914 g/cm , MW  = 18.01, MW  = 32.04. Assume vapors are
                                                                                                         m
                                        w
                                                                                        w
                                ideal gas.
                             f. If z = 0.4, p = 1 atm, and T drum  = 77°C, find V/F, x , and y .
                                                                                                 m
                                                                                        m
                             g. If F = 50 mol/h, z = 0.8, p = 1 atm, and y  = 0.892 mole fraction methanol, find V, L, and x .
                                                                             m
                                                                                                                                      m
                                Table 2-7. Vapor-liquid equilibrium data for methanol water (p = 1 atm) (mol%)
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