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- W2414925203 abstract "Since distillation columns are major energy consumers, many studies have explored modifying conventional configurations to achieve process intensification by improving energy efficiency. In a conventional extractive distillation to separate a binary mixture that forms an azeotrope, the fresh feed enters an extractive column along with a heavy entrainer solvent. One key component goes overhead, and the other is recovered in a second column, with solvent recycled back to the extractive column. A recent paper proposed a new extractive distillation system in which the fresh feed is split between two columns. One key component is removed as a sidestream from the first column and the second is recovered in the distillate of the other column. Energy and total annual cost savings of 14% compared to a conventional system are claimed. The proposed new configuration is more complex and poses potential dynamic controllability problems. The purpose of this paper is to explore this issue." @default.
- W2414925203 created "2016-06-24" @default.
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- W2414925203 date "2016-09-01" @default.
- W2414925203 modified "2023-10-18" @default.
- W2414925203 title "Control comparison of conventional extractive distillation with a new split-feed configuration" @default.
- W2414925203 cites W2022878960 @default.
- W2414925203 doi "https://doi.org/10.1016/j.cep.2016.06.004" @default.
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