| Robust Dynamic Principal Component Analysis for Process Performance Monitoring | ||||
| Daniel Castro-Rodriguez1, Gary Montague2 and Elaine Martin2, (1)School of Chemical Engineering and Advanced Materials., University of Newcastle upon Tyne., Merz Court. University of Newcastle upon Tyne, Newcastle upon Tyne, NE1 7RU, United Kingdom, (2)School of Chemical Engineering and Advanced Materials, University of Newcastle upon Tyne., Merz Court. University of Newcastle upon Tyne, Newcastle upon Tyne, NE1 7RU, United Kingdom
Research into a raft of multivariate statistical process control methodologies for linear, non-linear, steady-state and dynamic, batch and continuous systems has been widely reported in the literature over the past two decades [1,2,4]. As a consequence of the on-line, real time implementation of these technologies, it is possible to detect changes in process behavior that may otherwise not have been identified if univariate statistical process control methodologies had been applied. In particular for dynamic systems, the univariate methods of CUSUM and EWMA and their multivariate counterparts, MCUSUM and MEWMA are not applicable for systems that comprise a large number of highly correlated variables [1]. This limitation has materialized in the development of methodologies formulated around the statistical projection techniques of principal component analysis and projection to latent structures. Consequently, the most commonly implemented monitoring metrics are those of Hotelling's T2 and the squared prediction error [1,2,4].
More recently, to address the dynamic nature of processes, Ku et al. [5] proposed dynamic principal component analysis (DPCA). A data matrix is formulated, similar to that used in time series modelling, and PCA is then applied to the augmented matrix. However a fundamental issue is the sensitivity of the projection based methods to the presence of outliers. A consequence of this additional complication is that a number of robust principal component analysis approaches have been proposed including a methodology proposed by Hubert et al. [3]. The concept is based on projection pursuit and the minimum covariance determinant. More specifically, the robust principal component analysis approach is as follows. First a measure of the level to which an observation is categorised as an outlier is quantified according to:
where
If this distance is smaller than
In the reported research, robust and dynamic principal component analysis are combined thereby drawing together the dynamic nature of the process and the potential presence of outliers. The approach is tested using a simulation of a multivariate autoregressive system and on a polyvinyl acetate CSTR where known faults are introduced. In the case of the polyvinyl acetate CSTR several faults are introduced. The faults pertain to disturbances in the temperatures of the feed and of the cooling water, changes in the flows of feed and initiator, disturbances in the controller setpoint, a step change of 10% in the magnitude of the initiator density and also a 10% step change in the monomer volume fraction. All faults materialise in significant changes in the molecular weight of the product. The analysed variables are the flow rates of feed and initiator, the temperatures of the reactor, the feed and cooling water and the output of the controller. All these variables are measurable with instrumentation present in any plant. The two metrics, Hotelling's T2 and the SPE obtained from the application of PCA, robust PCA, dynamic PCA and the proposed robust dynamic DPCA are used to determine the presence of faults.
References
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