Simultaneous synthesis of distillation trains and heat exchanger networks
✍ Scribed by Miguel A. Isla; Jaime Cerdá
- Publisher
- Elsevier Science
- Year
- 1987
- Tongue
- English
- Weight
- 983 KB
- Volume
- 42
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
A new mathematical formulation for the optimal synthesis of heat-integrated distillation systems that accounts for constrained heat matches between columns and the rest of the process is presented. The definition of temperature intervals commonly used by heat exchanger network synthesis procedures is embedded in the proposed formulation that can be regarded as a generalization of the network flow model of Cerd& and Westerberg (1983, Chem. Engng Sci. 38, 1723) under conditions of variable stream temperatures. The minimization of the total flow-sheet utility cost has been chosen as the design target. The problem has been represented through a mixed-integer linear program. By performing the search with a standard branch-and-bound technique the global optimality of the solution found is guaranteed. Three case studies involving the separation ofa ternary mixture by distillation have been solved. The consideration of the rest of the process produces in two of them new distillation train designs costing less overall.
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