2019
DOI: 10.1016/j.cherd.2019.04.023
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Process intensification in multicomponent distillation: A review of recent advancements

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Cited by 60 publications
(27 citation statements)
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References 82 publications
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“…This configuration has two reboilers at DE and E as well as two condensers at ABC and A , thereby allowing the heat duty to be generated and removed by heat exchangers operated at milder temperature levels. These observations demonstrate that, for most industrial applications, building the FTC configuration is not a reasonable first choice …”
Section: Case Study—ngl Recovery and Fractionationmentioning
confidence: 98%
“…This configuration has two reboilers at DE and E as well as two condensers at ABC and A , thereby allowing the heat duty to be generated and removed by heat exchangers operated at milder temperature levels. These observations demonstrate that, for most industrial applications, building the FTC configuration is not a reasonable first choice …”
Section: Case Study—ngl Recovery and Fractionationmentioning
confidence: 98%
“…A number of recently published review/perspectives papers on PI, process synthesis, and reactive dividing wall columns have highlighted the tremendous potential of PI, and indicate a very high level of interest in PI because of the promise of significant improvements in the current state of the art in energy efficient operations as well as the possibility to discover truly innovative and novel solutions for new processing routes. They also confirm that the goals of smart manufacturing, sustainable production, circular economy could be realized through appropriate application of PI solutions.…”
Section: Perspectivesmentioning
confidence: 99%
“…Therefore, PI as a topic has been attracting much attention from industry as well as academia. Also, process systems engineering (PSE) has been closely related to the developments within PI as recent reviews on PI indicate. But what is PI, or, how can it be achieved?…”
Section: Introductionmentioning
confidence: 99%
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“…However, adopting tray‐by‐tray based unit models for large distillation network superstructures can often lead to intractable optimization problems. Consequently, most superstructure‐based approaches 7,19,20 have employed the Underwood equations, 21,22 due to their reasonable accuracy and simplicity.…”
Section: Introductionmentioning
confidence: 99%