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Subject: Re: Using Distillation Column Model in Inferentials CourseUse of temperature measurements to estimate compositions should work fine -actually without any need to know thermo - just using PLS or similar toregress steady-state data from simulations or from the real plant.We have used this on theoretical data on a pilot-plant column and on areal column. Please see these references:1. @ARTICLE{mejdell:91, author = "Mejdell, T. and Skogestad, S.", title = "Estimators for Ill-Conditioned Plants: High-Purity Distillation", journal = "Preprints ADCHEM '91", year = 1991, pages = 403-408, annote = {Estimation, Distillation columns, Large-scale systems, Data reduction, Kalman filters, Inferential control, Multivariate calibration, Input uncertainty, Robust control, Temperature control}2.@ARTICLE{mejdell:93-1, author = "Mejdell, T. and Skogestad, S.", title = "Output Estimation Using Multiple Secondary Measurements: High-Purity Distillation", author = "AIChE Journal", year = 1993, pages = 1641-1653}3. \item T. Mejdell and S. Skogestad, ``Estimation of Distillation Compositionsfrom Multiple Temperature Measurements using Partial-Least-SquaresRegression'', {\it Ind. Eng. Chem. Res.}, {\bf 30}, 12 , 2543-2555 (1991).4. \item T. Mejdell and S. Skogestad, ``Composition Estimator in a Pilot PlantDistillation Column using Multiple Temperatures'', {\it Ind. Eng. Chem. Res.},{\bf 30}, 12, 2555-2564 (1991).5.@Article{mejdell:94, author = {Mejdell, T. and Andersson, B-O.}, title = {Using Temperature Profile for Product Quality Estimation on a Distillation Column}, journal = {Reprinted from ISA Transactions}, year = 1994, volume = 33, pages = {27-34}, annote = {Estimation, Chemometrics, Process control, Distillation column} }
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