22.5-5. steam stripping and number of trays. a relatively nonvolatile hydrocarbon oil contains 4.0 mol % propane and is being stripped by direct superheated steam in a stripping tray tower to reduce the propane content to 0.2%. the temperature is held constant at 422 k by internal heating in the tower at 2.026 × 105 pa pressure. a total of 11.42 kg mol of direct steam is used for 300 kg mol of total entering liquid. the vapor–liquid equilibria can be represented by y = 25x, where y is mole fraction propane in the steam and x is mole fraction propane in the oil. steam can be considered as an inert gas and will not condense. plot the operating and equilibrium lines and determine the number of theoretical trays needed. ans. 5.6 theoretical trays (stepping down from the tower top)