A stream of hot dry nitrogen flows through a process unit that contains liquid acetone. A substantial portion of the acetone vaporizes and is carried off by the nitrogen. The combined gases leave the recovery unit at 205C and 1.10 bar and enter a condenser in which a portion of the acetone is liquefied. The remaining gas leaves the condenser at 283.15k10.0C and 60.0bar. The partial pressure of acetone in the feed to the condenser is 0.150 bar, and that in the effluent gas from the condenser is 0.379 bar. Assume ideal gas behavior. Calculate for a basis of 1.00m3 of gas fed to the condenser the mass of acetone condensed (kg) and the volume of gas leaving the condenser (m3)