00243 qeba09294a7c4e7be519dcac12e96db

00243 qeba09294a7c4e7be519dcac12e96db



Statistical Process Monitoring with Integrated Moving Average Noise 245

The approach of monitoring forecast errors has reemerged recently in the ąuality improvement literaturę. Alwan and Roberts (1988) plot 1-step forecasts on a ‘fcpecial cause” chart with no control limits and plot forecast errors on a ‘bommon cause” chart with ‘3-sigma” control limits. MacGregor (1988) outlines the essential concepts of process monitoring using control charts and process adjustment (control) using dynamie input-output models with time series errors. He suggests using control charts Tor analyzing control system performance and as diagnostic tools in control schemes.” Vander Wiel et al. (1992) successfully implemented this approach to control and monitor the batch polymerization process introduced in Example 2 above. After reducing the process variability using a minimum variance adjustment algorithm they monitored forecast errors using a CUSUM chart. Others who suggest monitoring forecast errors are Montgomery and Friedman (1989), Montgomeiy and Mastrangelo (1991) and Box and Kramer (1992). Superville and Adams (1994) give a convincing argument against using ARLs to select control charts to monitor forecast errors. They suggest using the probability of signaling by a fixed number of periods beyond the change point instead.

In addition, several papers have appeared demonstrating that positive autocorrelation can dramatically inerease false alarm rates for various monitoring schemes. Goldsmith and Whitfield (1961) were the first to study the effect of autocorrelation on ARLs for CUSUM charts. Additional studies have been reported by Johnson and Bagshaw (1974), Bagshaw and Johnson (1975) and Vasilopoulos and Stamboulis (1978).

Integrated Moving Averages and Level Shifts

Industrial data that tends to wander can often be modeled as a first order integrated moving average (IMA). The IMA model provides a reasonable fit to both the laser power data in Figurę 1 and the viscosity data in Figurę 2. Other ARIMA models may fit slightly better, but the IMA is not a bad choice. Box and Kramer (1992) and MacGregor (1988) place special importance on the IMA model because it fits reasonably well to data from a wide variety of industrial and economic processes. IMAs are often used to model stochastic disturbances in automatic control applications because the popular proportional-integral controller is optimal for first order input-output systems with IMA disturbances, A huge number of successful feedback loops under PI control in a wide rangę of applications is evidence that IMA approximations to correlated disturbances are useful.

We will define a process N, (t = 0,1,2,...) as a first order IMA if


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