Azeotropic distillation in a middle vessel batch column. 3: Model validation
- Massachusetts Inst. of Tech., Cambridge, MA (United States)
A dimensional time model of the middle vessel batch distillation column (MVC) is developed in the ABACUSS process modeling environment, and simulations are conducted to validate the theoretical insights developed for the operation of the MVC based on a warped time model of the MVC. The qualitative dynamics of the MVC operated in the presence of linear separation boundaries are validated via simulations conducted on the ternary azeotropic mixture of acetone, chloroform, and methanol. It is also shown via simulation that the separation results obtained from a column with significant but reasonable amounts of holdup on the trays are not significantly different from a column in which holdup in the trays is assumed to be negligible. Theoretical operating policies for separating the azeotrope of acetone and chloroform using benzene as a batch entrainer are also validated using the ABACUSS model. Finally, the authors explore the advantages and disadvantages of different feasible operating policies for separating a mixture of acetone, benzene, and chloroform completely into its constituent pure components.
- Sponsoring Organization:
- USDOE, Washington, DC (United States); Massachusetts Inst. of Tech., Cambridge, MA (United States)
- DOE Contract Number:
- FG02-94ER14447
- OSTI ID:
- 345352
- Journal Information:
- Industrial and Engineering Chemistry Research, Vol. 38, Issue 4; Other Information: PBD: Apr 1999
- Country of Publication:
- United States
- Language:
- English
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