Up to this point in this book, almost all of the distillation columns considered were operated continuously. These columns are fed continuously and produce product streams continuously.
KeywordsCapacity Factor Reflux Ratio Relative Volatility Total Reflux Luenberger Observer
These keywords were added by machine and not by the authors. This process is experimental and the keywords may be updated as the learning algorithm improves.
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- Block, B. (1961). Batch distillation of binary mixtures provides versatile process operation. Chem. Eng. 68, 87–93.Google Scholar
- Boston, J. F., Britt, H. I., Jirapongphan, S., and Shah, V. B. (1981). Foundations of computer aided chemical process design. New York: Engineering Foundation.Google Scholar
- Coates, J. and Pressburg, B. S. (1961). How to analyse the calculations for batch rectifications in tray columns. Chem. Eng. 68, 131–136.Google Scholar
- Holland, C. D. and Liapis, A. I. (1983). Computer methods for solving dynamic separation problems. New York: McGraw-Hill.Google Scholar
- Meadows, E. L. (1963). Muhicomponent batch distillation calculations on a digital computer. Chem. Eng. Prog. Symp. Ser. 45, 59, 48. AIChE, New York.Google Scholar
- Muhrer, C. A., Grassi, V. G., and Silowka, W. (1990). Process improvements in batch distillation through dynamic simulation. AIChE Annual Meeting, Chicago.AIChE, New York.Google Scholar
- Robinson, C. S. and Gilliland, E. R. (1950). Elements of fractional distillation. New York: McGrawHill.Google Scholar
- Van Dongen, D. B. and Doherty, M. F. (1985). On the dynamics of distillation processes IV —Batch distillation.Chem. Eng. Sci. 11, 2087–2093.Google Scholar
© Van Nostrand Reinhold 1992