Appendix 5A: Tray Efficiency Models


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Appendix 5A: Tray Efficiency Models
Appendix 5A: Tray Efficiency Models
Point Efficiency Most of the theoretical models developed to predict tray efficiency start from the estimation of the local or point efficiency EOG defined in agreement with the tray sketch in Fig. 5A-1. The assumptions commonly adopted are that the liquid composition changes only with the coordinate z, x = f(z), and vapor composition changes both with z and
Citation
Alessandro Brambilla: Distillation Control and Optimization: Operation Fundamentals through Software Control. Appendix 5A: Tray Efficiency Models, Chapter (McGraw-Hill Professional, 2014), AccessEngineering Export