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Received December 5, 2016
Accepted April 25, 2017
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Sparse probabilistic principal component analysis model for plant-wide process monitoring
State Key Lab of Industrial Control Technology, Institute of Industrial Control Technology, Zhejiang University, Hangzhou, 310027, P. R. China
jliang@iipc.zju.edu.cn
Korean Journal of Chemical Engineering, August 2017, 34(8), 2135-2146(12), 10.1007/s11814-017-0119-9
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Abstract
In the industrial monitoring process, probabilistic principal component analysis (PPCA) is a popular algorithm for reducing the dimension. However, the principal components (PCs) are not easy to interpret and its preserved number cannot be determined automatically. In this paper, we propose a sparse PPCA (SPPCA) to improve the interpretability by adding a prior and introducing sparsification to the loading matrix of PPCA. An expectation-maximization (EM) algorithm is used to obtain the parameters of the probabilistic formulation, and the dimensionality of the latent variable space can be automatically determined during the iterative process. With the sparse representation, a process monitoring strategy is then developed with the construction of several partial PPCA models. Case studies of SPPCA to a numerical case and Tennessee Eastman (TE) benchmark process demonstrate its feasibility and efficiency.
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References
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Jiang Q, Yan X, Korean J. Chem. Eng., 31(11), 1935 (2014)
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Kim D, Lee IB, Chemom. Intell. Lab. Syst., 67, 109 (2003)
Choi SW, Park JH, Lee IB, Comput. Chem. Eng., 28(8), 1377 (2004)
Chen T, Sun Y, Control Eng. Practice, 17, 469 (2009)
Ge ZQ, Song ZH, AIChE J., 56(11), 2838 (2010)
Vines SK, J. R. Stat. Soc. Ser. C-Applied Stat., 49, 441 (2000)
Jolliffe IT, Trendafilov NT, Uddin M, J. Comput. Graph. Stat., 12, 531 (2003)
Zou H, Hastie T, Tibshirani R, J. Comput. Graph. Stat., 15, 265 (2006)
Xie L, Lin XZ, Zeng JS, Ind. Eng. Chem. Res., 52(49), 17475 (2013)
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Guan Y, Dy JG, AISTATS, 5, 185 (2009)
Koyejo O, Ghosh J, Khanna R, Poldrack RA, NIPS, 676 (2014).
Khanna R, Ghosh J, Poldrack R, Koyejo OO, AISTATS, 38, 453 (2015)
Latouche P, Mattei PA, Bouveyron C, Chiquet J, J. Multivariate Anal., 146, 177 (2014)
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Qin SJ, Valle S, Piovoso MJ, J. Chemometr., 15, 715 (2001)
Choi SW, Lee IB, J. Process Control, 15(3), 295 (2005)
Zhang Y, Zhou H, Qin SJ, Chai T, IEEE T. Ind. Inform., 6, 3 (2010)
Wang B, Jiang Q, Yan X, Korean J. Chem. Eng., 31(6), 930 (2014)
Bishop CM, NIPS, 11, 382 (1998)
Bishop CM, Springer-Verlag, New York (2006).
Martin EB, Morris AJ, J. Process Control, 6(6), 349 (1996)
Chen Q, Wynne RJ, Goulding P, Sandoz D, Control Eng. Practice, 8, 531 (2000)
Chen Q, Kruger U, Leung ATY, Control Eng. Practice, 12, 267 (2004)
Downs JJ, Vogel EF, Comput. Chem. Eng., 17, 245 (1993)
Grbovic M, Li WC, Xu P, Usadi AK, Song LM, Vucetic S, J. Process Control, 22(4), 738 (2012)
Ge ZQ, Song ZH, Ind. Eng. Chem. Res., 52(5), 1947 (2013)