A process for stripping and drying a starting organic material, comprising: a) introducing the starting organic material into an upper contact zone of a column that has an upper contact zone and a lower contact zone, and allowing the starting organic material to travel downwardly through the column, through the upper contact zone and then through the lower contact zone to a bottom section of the column; b) introducing 0.0002 to 0.02 kg of superheated steam per kg of starting organic material into the upper contact zone of the column and above the lower contact zone of the column such that the superheated steam moves upwardly through the upper contact zone, where it contacts the starting organic material and removes impurities therefrom, and then to a top section of the column; c) introducing 0.0001 to 0.003 kg of nitrogen or argon per kg of starting organic material into the lower contact zone of the column such that the nitrogen or argon moves upwardly through the lower contact zone where it contacts a portion of the organic material and removes moisture from therefrom, then moves upwardly through the upper contact zone where it contacts another portion of organic material, and then moves to a top section of the column; d) removing the steam and the nitrogen or argon from the top section of the column above the upper contact zone; and e) removing the stripped and dried organic material from the bottom section of the column below the lower contact zone; wherein the starting organic material is a liquid polyether having a molecular weight of from 500 to 10,000, or is a crude polymer polyol, that contains from 50 to 5,000 ppm of volatile organic impurities and up to 50,000 ppm of water, and the stripped and dried organic material contains up to 10 ppm of volatile organic compounds and up to 200 ppm of water. a) introducing the starting organic material into an upper contact zone of a column that has an upper contact zone and a lower contact zone, and allowing the starting organic material to travel downwardly through the column, through the upper contact zone and then through the lower contact zone to a bottom section of the column; b) introducing 0.0002 to 0.02 kg of superheated steam per kg of starting organic material into the upper contact zone of the column and above the lower contact zone of the column such that the superheated steam moves upwardly through the upper contact zone, where it contacts the starting organic material and removes impurities therefrom, and then to a top section of the column; c) introducing 0.0001 to 0.003 kg of nitrogen or argon per kg of starting organic material into the lower contact zone of the column such that the nitrogen or argon moves upwardly through the lower contact zone where it contacts a portion of the organic material and removes moisture from therefrom, then moves upwardly through the upper contact zone where it contacts another portion of organic material, and then moves to a top section of the column; d) removing the steam and the nitrogen or argon from the top section of the column above the upper contact zone; and e) removing the stripped and dried organic material from the bottom section of the column below the lower contact zone;