The author regrets that the following errors occurred in the above paper: In Table 1 (p. 3122) b should read -0.6246 instead of 0.6246 for carbon monoxide and 0.0704 instead of 0.1899 for nitric oxide. K should read 0.0050 instead of 0.0000 for cyanogen. Line 6, Table 1 (p. 3122) should read Oxygen?
Separation synthesis of multicomponent feed streams into multicomponent product streams
โ Scribed by C. A. Floudas
- Publisher
- American Institute of Chemical Engineers
- Year
- 1987
- Tongue
- English
- Weight
- 826 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
โฆ Synopsis
The synthesis problem of separation sequences that separate several multicomponent feed streams into several desired multicomponent product streams is addressed. A superstructure is proposed for this separation problem that has embedded all the alternative separation configurations of interest. This superstructure, which has as separator units the separation tasks that are defined for each separation breakpoint, involves options for series and/or parallel sequences, as well as stream splitting, mixing, and bypassing. Formulating and solving this superstructure as a nonlinear programming problem that has as unknowns the stream interconnections, results in an optimal separation sequence. This sequence, which may involve fewer separator units than those included in the superstructure, is shown to be a realistic and practical one. The synthesis approach is illustrated with four example problems.
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