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Computers & chemical engineering, v.19 no.9, 1995년, pp.983 - 1005
Ricker, N.L. (Department of Chemical Engineering, BF-10, University of Washington, Seattle, WA 98195, U.S.A.) , Lee, J.H. (Department of Chemical Engineering Auburn University, U.S.A.)
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AbstractA nonlinear, mechanistic model of the Tennessee Eastman (TE) Plant-wide Challenge Process is derived for use in on-line monitoring and control The model has 26 states, 10 unmeasured disturbances and process parameters are estimated such that an equal number of model outputs match the corresp...
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