data processing system adapted to a vapour recompression distillation unit is described. It is shown that it allows the identification of mass transfer parameters of the distillation column, of heat exchange of the boiler-condenser, of manometric and flow coefficients of compressor and of its isentr
Dynamic version of steady state optimizing control of a distillation column by trial method
✍ Scribed by Y. Sawaragi; T. Takamatsu; K. Fukunaga; E. Nakanishi; H. Tamura
- Publisher
- Elsevier Science
- Year
- 1971
- Tongue
- English
- Weight
- 664 KB
- Volume
- 7
- Category
- Article
- ISSN
- 0005-1098
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✦ Synopsis
Brief Paper Dynamic Version of Steady State Optimizing Control of a Distillation Column by Trial Method* Version dynamique de la commande optimalisante en rrgime &abli d'une colonne distiller par la m&hode d'exploration Dynamische Variante einer den station/iren Zustand optimierenden Regelung einer Destillationskolonne auf empirischem Wege ~HHaMrrqecKa~ Bepcn~ OnTnMn3rtpytoI~ero ynpaBJIeHrta ~HCTHJLrlfllBtOHHOH KOJ-IOHHOI4 yCTaHOBI4BI//eMC~ COCTOIIHHH MeTO
📜 SIMILAR VOLUMES
## Abstract A Petlyuk distillation column, considering equilibrium and non‐equilibrium stage models, was studied. Rigorous simulations were conducted using Aspen Plus™ RATEFRAC Module for the separation of ternary mixtures. According to the equilibrium model, the energy‐efficient design of the Petl