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Exam on Separation Processes - Spring 2005 - MIT
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Spring 2005 EXAM 1 Wednesday, March 2, 2005
ln P=A−
where P is in atmospheres and T is in Kelvins.
Component z A D
C 3 0.25 9.816 2260 C 4 0.40 9.922 2696 C 5 0.35 10.173 3141
a) Determine whether the mixture is a subcooled liquid, a mixture of vapor and liquid, or a superheated vapor.
b) It is desired to bring the mixture to its bubble point (saturated liquid). If temperature is maintained at 100°C, to what total pressure must the mixture be subjected to reach the bubble point?
c) If pressure is maintained at 15 atmospheres, to what temperature must the mixture be adjusted to reach the bubble point? An answer within a few degrees centigrade is acceptable.
a) What are the minimum reflux ratio and minimum number of stages required to effect this separation?
b) If we were to design a distillation column with a partial reboiler and total condenser to operate at 1.2 times the minimum reflux ratio, how many stages, in addition to the reboiler, are needed? What is the optimum location for the feed?
We wish to determine if we can use an existing distillation column that is no longer being used for its original purpose. The column is equipped with a total condenser, a partial reboiler, and ten plates above the reboiler. There are only two possible locations at which the feed can be introduced without making modifications to the column. These locations are plate 5, counting up, and directly into the reboiler. The reboiler is equipped with steam coils that are capable of vaporizing up to 85 pound-mol/hour of the liquid in the reboiler. Although the column is not what you would design, we would like to determine whether the column can be used, as is, to make the desired product. You are asked to consider two cases, the feed introduced at plate 5 and the feed introduced into the reboiler.
c) The feed is introduced at plate 5 (not likely to be the optimum location) and the reflux ratio is set to four. Show the operating lines for this reflux ratio and show the equilibrium stages stepped off on a McCabe-Thiele diagram with the feed on plate 5 and a total of ten plates plus a reboiler. Can the column be operated at this reflux ratio? Does the reboiler have adequate capacity? It is acceptable to make a distillate that is purer in component A than specified.
d) The feed is introduced directly into the reboiler. Can the column now be operated at a reflux ratio of four? Demonstrate the validity of your answer graphically or algebraically. What is the lowest reflux ratio at which this column can be operated? Does the reboiler have adequate capacity at this reflux ratio?