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- W4313231669 abstract "Over the last fifteen years, immense progress has been made in the research of pressure-swing batch distillation. The challenge lies in the fact that certain pressure-sensitive azeotropic mixtures cannot be separated in a regular open batch mode, with an acceptable outcome. Throughout most of this text, findings are to contradict previously grounded facts. Acetone-methanol separation by pressure-swing batch distillation in a mixed double system consisted of a regular and inverted double column is a process under the investigations. In this work, a complete global solution to the optimal control problem in form of a sequential synthesis of controlled trajectories, is derived. During this study, the optimal reflux strategy through cyclic operation was extended to the separation of a non-ideal minimum boiling azeotrope of industrial significance. The influence of the liquid ratio and tank volume on the control pattern and energy requirement are evaluated as well." @default.
- W4313231669 created "2023-01-06" @default.
- W4313231669 creator A5078750464 @default.
- W4313231669 date "2022-12-29" @default.
- W4313231669 modified "2023-09-28" @default.
- W4313231669 title "Pressure-driven batch distillation optimal control for acetone-methanol separation" @default.
- W4313231669 doi "https://doi.org/10.26434/chemrxiv-2022-r30p2" @default.
- W4313231669 hasPublicationYear "2022" @default.
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