packed columns;
structured packings in distillation;
performance modeling;
scale-up in packed column;
D O I:
10.1080/00986440214995
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Scale-up of laboratory data for distillation with structured packings is considered. Organic mixtures were rectified in a column with elements of laboratory-scale gauze packing at atmospheric and reduced pressure. The composition was virtually constant for each system and pressure. The correlation of height of the transfer unit for laboratory data is much better assuming a non-negligible resistance in the liquid phase, an important difference compared with available models for commercial columns. Results were compared with data for gauze and corrugated sheet packings in literature to obtain the ratio between efficiencies in both scales. Two equations are proposed for predicting performance of pilot plants with both types of structured packings.