Process Systems Engineering
Conceptual design of distillation processes for mixtures with distillation boundaries: I. Computational assessment of split feasibility
Article first published online: 26 JUL 2010
DOI: 10.1002/aic.12378
Copyright © 2010 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Brüggemann, S. and Marquardt, W. (2011), Conceptual design of distillation processes for mixtures with distillation boundaries: I. Computational assessment of split feasibility. AIChE J., 57: 1526–1539. doi: 10.1002/aic.12378
Publication History
- Issue published online: 5 MAY 2011
- Article first published online: 26 JUL 2010
- Accepted manuscript online: 26 JUL 2010 12:00AM EST
- Manuscript Accepted: 10 JUL 2010
- Manuscript Revised: 25 MAY 2010
- Manuscript Received: 30 JUL 2007
- Abstract
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- Cited By
Keywords:
- design (process simulation);
- distillation;
- mathematical modeling;
- process synthesis;
- simulation;
- process
Abstract
Geometric design methods for the conceptual design of azeotropic distillation processes are fast and efficient tools for the economic screening of different process alternatives. This two-part series presents a fully automated conceptual design method for finding an optimal recycle policy for the separation of mixtures with distillation boundaries. It does not require visualization and graphical inspection of residue curve or pinch maps and is, hence, not limited to ternary mixtures. The first part introduces a fully computational geometric split feasibility test based on bifurcation analysis. This bifurcation-based feasibility test can be used as a valuable stand-alone tool for the assessment of different separation options. It is also one of the core elements of the recycle optimization discussed in the second part of this series. © 2010 American Institute of Chemical Engineers AIChE J, 2011

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