A mathematical model which describes the nonsteady state heat and mass transfer operations durmg the freeze drymg process IS presented With the use of tins model the problem of operating a freeze dryer to obtam a fixed final mmsture content m mmlmum trme IS formulated as an optImaI control problem R
Optimal control of a freeze Dryer—II: Dynamic analysis
✍ Scribed by R.J. Litchfield; A.I. Liapis
- Book ID
- 103006556
- Publisher
- Elsevier Science
- Year
- 1982
- Tongue
- English
- Weight
- 729 KB
- Volume
- 37
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
The unsteady state model and Lagrangian equations of the freeze-drying process presented in Part 1[4],
havebeen solved for non-fat reconstituted milk and turkey, using the control strategies presented in[4]; the results were then used to evaluate the coefficients representing the necessary conditions of optimality. The results for non-fat reconstituted milk confirm the results of the quasi-steady state analysis[4], except for a time segment very close to t =O. Simulations with turkey breast showed similar results at low pressures, but it was found that at higher pressures the assumed control policies which were based on a quasi-steady state analysis[l], were not optimal
The non-steady state results indicate that for turkey, intermediate rather than maximum, pressure control policies were optimal for cases (a) and (b) in [4]. However, in practice these optimal pressure policies might produce only minor improvements in drying time when compared with a near optimal policy. It was also found that changes in the interface constraint affected drying times only marginally, but that large heaters operating under optimal control had a pronounced effect on the drying time.
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