We are separating a mixture of light hydrocarbons in a stripping column. The saturated liquid feed is 35.0 mol% n-butane, 45.0 mol% n-pentane, and 20.0 mol% n-hexane. The feed rate is 100.0 kmol/h, and it is at 7.0 bar. The column is also at 7.0 bar, has a partial reboiler, and CMO can be assumed valid. The bottoms product is 98.2 mol% n-hexane, and the boilup ratio is . Find bottoms flow rate B, distillate flow rate D, and mole fractions of distillate and bottoms.