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An EWMA control chart for the mean of individual streams in multiple stream processes

Gráfico de controle EWMA para as médias de fluxos individuais em processos multifluxo

Abstract:

In a multiple stream process (MSP) a product is manufactured in a number of streams in parallel. The traditional tool for monitoring MSPs, the group control chart (GCC), does not take into account that typically the value of the quality variable in each stream is the sum of a component common to all streams and an individual component, of the particular stream. This may render the GCC ineffective in detecting shifts in the mean of individual streams. Based on this two-components model, we propose an exponentially weighted moving average (EWMA) GCC to monitor the means of the individual streams components. We optimize its design (minimizing the ARL for given shifts in the mean of a stream) and compare their ARLs with the ones of other existing charts devised for two-components MSPs. For this comparison, we needed to obtain optimal designs of these previous charts too, which were not available in the literature; this is an additional contribution of our work. The ARLs of the charts were obtained by simulation, with a number of runs sufficiently large to ensure precise results. The results show that the proposed chart outperforms the previous ones, becoming thus recommended for the statistical control of MSPs.

Keywords:
Multiple stream processes; Group control chart; Components of variance; Exponentially weighted moving average

Resumo:

Em um processo de fluxo múltiplo (MSP) um produto é fabricado em vários fluxos em paralelo. A ferramenta tradicional para o monitoramento de MSPs é o gráfico de controle de grupo (GCG), que não leva em conta que tipicamente o valor da característica de qualidade em cada fluxo é a soma de um componente comum a todos os fluxos e um componente individual, do fluxo particular. Isso pode tornar o GCG ineficaz na detecção de mudanças na média de fluxos individuais. Com base neste modelo de dois componentes, propomos um GCG da média móvel ponderada exponencialmente (EWMA) para monitorar as médias dos componentes individuais dos fluxos. Otimizamos seu projeto (minimizando o ARL para determinados deslocamentos na média de um fluxo) e comparamos seus ARLs com os de outros gráficos destinados a MSPs de dois componentes. Para essa comparação, precisávamos obter os projetos ótimos também desses gráficos anteriores, que não estavam disponíveis na literatura; essa é uma contribuição adicional do nosso trabalho. Os ARLs dos gráficos foram obtidos por simulação, com um número de corridas suficientemente grande para garantir a precisão dos resultados. Estes mostram que o gráfico proposto supera os anteriores, tornando-se recomendado para o controle de MSPs.

Palavras-chave:
Processos Multifluxo; Gráfico de Controle de Grupo; Componentes da variância; Médias Móveis Exponencialmente Ponderadas

1 Introduction

Multiple stream processes (MSPs) are present in many industries, e.g. beverage, cosmetics and plastic industries, among others. They are characterized by the fact that the product, quality characteristics (quality variables) and specifications are the same in all streams, which ideally should have the same distribution, adjusted in the same target value and with the same spread. The first statistical process control (SPC) scheme specifically devised for MSPs was the group control chart (GCC), developed by the British during World War II and described by Boyd (1950)Boyd, B. F. (1950). Applying the group chart for and R. Industrial Quality Control, 3, 22-25.. The idea behind a GCC is to aggregate in one control chart the information from all streams, making easier the assessment of the process state. Concretely: at every sampling time, n measures of a quality variable are made in each stream and the averages and ranges of the observations in each stream are calculated; in the group X¯ control chart only the smallest and largest averages are plotted and compared with the control limits; if they fall within the control limits the process is considered to be in control. The group R chart is similar (for small sample sizes there is no lower control limit and only the largest range is plotted). For several decades this was the only procedure in the literature for monitoring multiple stream processes. Nelson (1986)Nelson, L. S. (1986). Control charts for multiple stream processes. Journal of Quality Technology, 18(4), 255-256. http://dx.doi.org/10.1080/00224065.1986.11979020.
http://dx.doi.org/10.1080/00224065.1986....
proposed a runs scheme to be used with group charts (with or without control limits): if a same stream yields the largest (or the smallest) reading more than r times in a row (where r is defined as a function of the number of streams of the process), this should be an indication that this particular stream has a higher (or lower) mean than the other ones.

Some further works on the monitoring of MSPs are Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
, Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
, Amin & Li, (2000)Amin, R. W., & Li, K. (2000). The MaxMin EWMA tolerance limits. International Journal of Quality & Reliability Management, 17(1), 27-41. http://dx.doi.org/10.1108/02656710010283351.
http://dx.doi.org/10.1108/02656710010283...
, Lanning et al. (2002)Lanning, J. W., Montgomery, D. C., & Runger, G. C. (2002). Monitoring a multiple stream filling operation using fractional samples. Quality Engineering, 15(2), 183-195. http://dx.doi.org/10.1081/QEN-120015851.
http://dx.doi.org/10.1081/QEN-120015851...
, Liu et al. (2008)Liu, X., Mackay, R. J., & Steiner, S. H. (2008). Monitoring multiple stream processes. Quality Engineering, 20(3), 296-308. http://dx.doi.org/10.1080/08982110802035404.
http://dx.doi.org/10.1080/08982110802035...
, Xiang & Tsung (2008)Xiang, L., & Tsung, F. (2008). Statistical monitoring of multi-stage processes based on engineering models. IIE Transactions, 40(10), 957-970. http://dx.doi.org/10.1080/07408170701880845.
http://dx.doi.org/10.1080/07408170701880...
, Meneces et al. (2008)Meneces, N. S., Olivera, S. A., Saccone, C. D., & Tessore, J. (2008). Statistical control of multiple-stream processes: a shewhart control chart for each stream. Quality Engineering, 20(2), 185-194. http://dx.doi.org/10.1080/08982110701241608.
http://dx.doi.org/10.1080/08982110701241...
& Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
. For a comprehensive literature review of this topic, which describes these works with some detail & includes other references, see Epprecht (2015)Epprecht, E. K. (2015). Statistical control of multiple-stream processes: a literature review. In S. Knoth & W. Schmid, (Eds.), Frontiers in statistical quality control 11 (p. 49-64). Springer International Publishing, Switzerland. http://dx.doi.org/10.1007/978-3-319-12355-4_4.
http://dx.doi.org/10.1007/978-3-319-1235...
.

Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
were pioneers in acknowledging the fact that many (if not most) MSPs have two separate sources of variation and thereby in such processes the value of the quality variable measured in time t in each stream should be represented by the sum of two random variables: a “mean level” common to all streams (and which may be stable or present some dynamics over time) plus an individual component responsible for the difference between the stream value and the common component value. This component will consist only of random variation about the common value, having null mean, in the case the process is in control and all streams are centered on the same value; on the other hand, a special cause affecting a stream may make the mean of its individual component differ from zero. An example of such a process is a filling process with a filling machine with many heads. The functioning of a common reservoir, pump and/or characteristics such as the density of the fluid are responsible for the common component level, while a clog or a fissure in some tube of one of the heads will affect only the output of that head. Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
have shown the inefficiency of the traditional GCCs (and of Nelson’s runs scheme) in signalling special causes affecting the mean of a particular stream. They proposed then a statistic (Rt) that is sensitive to such kind of changes: the difference between the largest and the smallest stream averages in time t. They have shown the effectiveness of this statistic and its superiority relative to the previous control schemes for MSPs. They also proposed and analyzed runs rules, CUSUM and EWMA versions of the chart.

For monitoring the means of the individual streams components under the two-component model Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
, based on a multivariate model and principal components decomposition, proposed a so-called S2 chart on a statistic which turns out to be proportional to the sample variance between streams: S2 equals m1 times the sample variance of the streams averages, where m is the number of streams; it can also be interpreted as the squared norm of the orthogonal projection of the multi-stream vector on the complementary subspace of the first principal component (which is the sample mean of all streams). This chart showed similar performance to the Rt chart in the case of shifts in one stream but outperforms the Rt chart when more than one stream shifts. A MEWMA version of the chart was also proposed and briefly analyzed.

Other work based on the two-component model of MSP was Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
. They proposed a residuals GCC where, in contrast with the classic GCC for the mean, the points plotted at each sampling time t are the smallest and the largest estimates of the individual streams components in time t rather than the smallest and the largest averages among all streams. This is a Shewhart-type GCC, and was shown to outperform the Shewhart-type versions of Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
Rt chart and Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
S2 chart in the detection of mean shifts in one individual stream.

However, as mentioned, Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
and Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
had proposed and analyzed also EWMA versions of their charts, which were much faster in signalling shifts of small and moderate sizes (2 standard deviations) than their Shewhart-type counterparts. The fact that the residuals GCC proposed by Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
outperformed the Shewhart-type versions of the charts of those authors raises the question whether an EWMA version of the residuals GCC might outperform the EWMA versions of those charts as well. This directly motivates the proposal and analysis of such an EWMA version of the residuals GCC, that is, an EWMA GCC on the smallest and the largest estimates of the individual streams components. The definition, optimization and performance analysis of such chart is the object of the present paper.

We give expressions for computation of the EWMA statistics and of the control limits for such control chart, detail its operation, and optimize its design (that is, we find the values of the control limits and of the EWMA smoothing constant that minimize the out-of-control ARL of the chart) for a variety of cases (combinations of number of streams, sample size and size of shift in the mean of a stream for which the average run length — ARL — should be minimized); we optimize, as well, in the same sense, the EWMA versions of Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
Rt chart and Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
S2 chart, for the sake of a fair performance comparison. To our knowledge, there was no optimization of the designs of the EWMA Rt and MEWMA S2 control charts in the literature. Then we obtain the ARL profiles (ARLs for a range of shifts in the mean of an individual stream) of the three control schemes, for comparing their performances. The ARLs were obtained through simulation, due to the prohibitive complexity of an analytical approach, but with a number of runs large enough to yield precise results. As will be seen, the proposed chart outperforms its predecessors.

The stages for achieving the objectives of this research are in Table 1.

Table 1
Stages of the research and objetives of each one.

The rest of this paper is organized as follows: Section 2 describes, as a background, the two-component model proposed by Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
and the statistics and charts proposed by them, by Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
and by Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
. Next, the EWMA chart we propose is described in Section 3. Then, in Section 4, we detail how the simulation was used for computing the ARLs of the three EWMA schemes considered. The design optimization problem is formally defined in Section 5, which also gives the optimal designs (the ones that give the minimum out-of-control ARL) found for the cases considered. Finally, the ARL profiles (ARL values for a range of shifts from 0.5 to 4 standard deviations) of the optimized charts and also of the residuals GCC are presented and compared in Section 6. Section 7 summarizes the conclusions of the analysis.

2 Background

As Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
, Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
and Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
, we consider here MSPs well represented by the following model:

x t i j = c t + e t i j (1)

where

xtij is the j-th observation of the quality variable x in the i-th stream in sampling time t;

i=1,2,,m, where m is the number of streams of the process, j=1,2,,n, where n is the sample size (number of observations taken from each stream at sampling time t), and t = 1, 2, 3, ... are the indexes of the successive samples of the process in the monitoring phase;

ct is a common component which represents the mean level of the process at time t; it may either be a constant value of have some dynamics, exhibit autocorrelation, and therefore in the greatest generality its evolution over time is a stochastic process;

etij is the j-th observation of the individual i-th stream component in sampling time t; we assume that when the process is in control, etij~N0,σ02;

and, as implicit in this definition, we assume that the values of etij are iid; independent between themselves and over time; we also assume that the variables c and e are independent. Still according to this definition, when the process is in control, at any time t all streams have the same expected value (they are either centered in a same fixed value, or the expected value wanders but at any given time it is the same for all streams), so the etij’s can be seen as realizations of the random noise at stream i. On the other hand, when one of the streams goes out of control, its mean shifts and its etij’s have no longer null mean.

In the particular case of only one observation per stream at each sampling time (n=1), the index j is dropped.

From this model, it follows that

V x t i j = V c t + V e t i j = V c t + σ 0 2 (2)

So, the classic X¯ group control chart (the traditional SPC tool for monitoring the mean of multiple stream processes), based on the m averages over j of the xtij’s of each stream, would have control limits width proportional to a total standard deviation of Vct+σ02/n. Then, unless the variance of the mean level, Vct, is small relative to the variance of the individual components (intra-stream variance) σ02, this chart would be quite insensitive to shifts in the mean of one (or some) of the individual stream components ei.

To overcome this problem, the three works cited that are based on this model of MSP propose monitoring separately the two components, c and e, with separate control charts. They also concurr in that, for controlling the mean level, ct should be estimated by the average of all the xtij’s in time t, and that this statistic should be monitored using an appropriate SPC technique according to the nature of ct — for example, a Shewhart, EWMA or CUSUM chart in case it exhibits no serial correlation, or some technique for monitoring autocorrelated processes otherwise. In any case, ct is treated as one variable and hence will be monitored using some established (well-known) univariate process control scheme. For this reason, all these works focus (as we do) exclusively on the monitoring of the individual streams components ei, i=1,2,,m.

Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
, considering individual observations per stream, proposed the statistic

R t = m a x x t i m i n x t i (3)

and analyzed a Shewhart-type control chart on Rt, as well as EWMA, CUSUM and runs rules versions of it. In case of more than one observation per stream at each sampling time, xti in Equation 3 should be replaced by the average (over j) of the n observations xtij (j = 1, 2, ..., n) in the stream. It is easy to see that in the second member of Equation 3 the mean level components (ct) of maxxti and of minxti cancel out, so the in-control standard deviation of Rt (and so the upper control limit for the Rt chart) is proportional to σ0, making the chart sensitive to shifts in the mean of a particular stream.

Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
proposed an S2 chart based on the statistic (in the notation of the present paper)

S 2 = σ 0 2 i = 1 m x t i x ¯ t i 2 (4)

where x¯ti is the average of the m streams in time t and σ02 is the in-control variance of xti (the same for all i), which, if not known, should be estimated from preliminary samples of the in-control process. Similarly to Rt, S2 filters out the mean level component and is sensitive to shifts in the mean of one or some streams. Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
also analyzed a MEWMA (Lowry et al., 1992Lowry, C. A., Woodall, W. H., Champ, C. W., & Rigdon, S. E. (1992). A multivariate exponentially weighted moving average control chart. Technometrics, 34(1), 46-53. http://dx.doi.org/10.2307/1269551.
http://dx.doi.org/10.2307/1269551...
) version of it. In this one, the values of each stream are separately smoothed (m EWMA values) and then combined in a S2 statistic (similarly to the usual MEWMA procedure for multivariate processes). The case of more than one observation per stream at each sampling time is also accomodated in a similar way as in Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
, by considering the averages of the n observations in stream i in time t, and replacing σ02 in Equation 4 by σ02/n.

In contrast with the Rt and the S2 charts, which are based on a single statistic, Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
proposed controlling the means of the individual streams components by a residuals group control chart, based on the differences (or residuals) between the subgroup averages and the estimate of the mean level rather than on the subgroup averages themselves. In sampling time t, n observations xtij (j=1,2,,n) are made at each stream i, i=1,2,,m. Next, the common component (mean level) in time t is estimated by the average of all observations in time t:

c t ^ = 1 n m i = 1 m j = 1 n x t i j (5)

and the differences (or residuals)

d t i j = x t i j c t ^ (6)

are calculated. Note that dtij is an estimator of the individual component etij. Then the average difference in each stream i is computed as

d ¯ t i = 1 n j = 1 n d t i j (7)

Alternatively, as can be seen by substituting Equation 6 in Equation 7, d¯ti can be computed by Equation 8

d ¯ t i = 1 n j = 1 n x t i j c t ^ (8)

The maximum and minimum of the m values of d¯ti are plotted in a GCC with control limits appropriately set for the desired false-alarm rate. For details, the reader is referred to Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
.

3 The EWMA group control chart proposed

We here propose an EWMA group control chart for the differences d¯ti (GEWMA-d¯ chart). At each sampling time, the sampling occurs exactly like in the case of the residuals GCC just described at the end of the previous section, and each d¯ti is calculated following the same steps (Equations 5, 6 and 7, or, alternatively, Equations 5 and 8). Then, each d¯ti is smoothed using the recursive Equation 9

Y t i = λ d ¯ t i + 1 λ Y t 1 i (9)

yielding m EWMA values, one for each stream. The smoothing constant λ0,1 is an implementation parameter of the chart whose value has to be chosen by its user. Given the assumption that, with the process in control, Eetij=0, it follows, as shown in Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
, that Ed¯ti=0 and this is the initial value for the EWMA statistic: Y0i=0. The maximum and the minimum Yti values in time t are plotted in a GCC with upper and lower control limits given by

U C L = k σ 0 λ 2 λ m 1 n m (10a)
L C L = k σ 0 λ 2 λ m 1 n m (10b)

where the control limit factor k is also an implementation parameter of the chart. A point outside the control limits is considered as evidence of a shift in the mean of the corresponding stream. Although only the extreme EWMA values are plotted, in case of a signal it is advisable to verify if the EWMA value of any other stream is outside the limits.

The expressions for the control limits were derived as follows. Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
have shown that, when the process is in control, the assumption that etij~N0,σ02 implies that every d¯ti is normally distributed with null mean and standard deviation equal to σ0m1/nm. As a consequence (using the welll-known relation between the standard deviation of a normal variable and the standard deviation of its exponentially smoothed value), the standard deviation of every Yti is Equation 11:

σ 0 λ 2 λ m 1 n m (11)

and the control limits (see Equations 10) are just set at k standard deviations of the (null) expected value of the differences. Since the successive values of EWMA statistics exhibit serial correlation, k cannot be determined simply as a quantile of the standard normal distribution but should rather be obtained by search as the value that, for the given number of streams of the process (m), sample size (n) and value of the smoothing constant λ, makes the in-control average run length match a specified ARL0 value. This will be explained in detail in the next section.

4 Design of the chart – performance measures and their computation

The best choice of smoothing constant and control limits for the EWMA chart proposed depends on the number of streams of the process m, on the sample size n, on the value specified for the in-control average run length (ARL0) and on the magnitude δ* (specified) of the shift in the mean of an individual stream that it is important to detect with minimum delay. Given m and n, the criterion we adopt for the design of the chart is to choose the values of λ and k that, with fixed in-control average run length ARL0 (specified), minimize the out-of-control run length (ARL1) for the relevant shift δ* specified. Minimization of the ARL1 (when possible) for a relevant shift specified, under the constraint of a specified ARL0, is a popular criterion for the design of a control chart.

In the case of charts with memory such as EWMA and CUSUM charts, there are two possible scenarios to be considered for the definition of the ARLs, especially regarding ARL1: in the zero-state scenario, the process is already out of control when the monitoring starts; in the steady-state scenario, when the monitoring starts the process is in control and only after some time a special cause brings the process to an out-of-control state. The scenario has an impact on the ARL1 because in the steady-state scenario when the special cause occurs the effect of the initial value of the EWMA statistic has already dissipated whereas in the zero-state scenario it is present. The result is that the zero-state ARL1 is larger than the steady-state ARL1. However, the differences are not usually substantial, as the great bulk of literature on the performance of EWMA charts has shown.

We considered only the steady-state ARL1. The reason is that, even in case the monitoring starts with the process out of control, as soon as there is an alarm, the process should be investigated, the special cause eliminated, and when the monitoring is resumed, the process will be in control. The process should then be in control every time the monitoring is resumed after an alarm (including eventual false alarms), so the zero-state scenario is a transient situation, if it ever occurs.

The analytical computation of the ARLs (either in control or out of control) of the proposed chart is not only quite complex but would be prohibitively computer intensive. For univariate EWMA charts it is still feasible to use, for example (and most often) Markov chain models. With multiple stream processes, however, the d¯ti values of different streams are correlated (the proof is given in Epprecht et al., 2011aEpprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
), which makes the different Yti values cross-correlated, too. The Markov chain model for more than two simultaneous EWMA charts of cross-correlated variables is extremely time consuming to compute (see, for example, Epprecht et al., 2011bEpprecht, E. K., de Luna, M. A., & Aparisi, F. (2011b). Joint EWMA charts for multivariate process control: markov chain and optimal design. International Journal of Production Research, 49(23), 7151-7169. http://dx.doi.org/10.1080/00207543.2010.537383.
http://dx.doi.org/10.1080/00207543.2010....
). For this reason, we resorted to simulation.

In order to guarantee accurate simulation results, we used 10,000 runs for obtaining each ARL estimate. This guarantees a standard error of less than 1% of the SDRL (standard deviation of the run length). The SDRL, in turn, is always smaller than the ARL. Indeed, in the case Shewhart-type charts, whose run lengths follow a geometric distribution, SDRL=ARLARL1<ARL. The run length distributions of EWMA charts are less skewed and will have SDRL<ARLARL1<ARL. This means that standard error of the ARL estimates would of less than 1% of the estimate. In each simulation run, values were generated for every etij (ct was kept constant and equal to zero, without loss of generality, because the charting procedure filters it out completely; as a result, the simulated xtij’s coincide with the etij’s; see Equation 1). At each simulated sampling time t, c^t was calculated by Equation 5; next, Equations 8 and 9 were applied for each stream i, and the EWMA values (Yd¯ti) were compared with the control limits.

To obtain the steady-state ARL1’s, a “warm-up” period of 50 samples (from t=1 to t=50) was allowed before inserting the simulated mean shift in one of the streams. In case of an alarm during the first 50 samples, the run was disconsidered and the “warm-up” period restarted (with Y0i=0 for all streams).

The EWMA versions of the charts proposed by Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
and Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
were also simulated for purposes of performance comparison. The same series of xtij values generated in each simulation run was used for all the three schemes.

With EWMA charts, the ARL0 constraint fixes the relationship between the smoothing constant λ and the control limits width factor k; so, given the former, the latter is uniquely determined (see for example Crowder, 1989Crowder, S. V. (1989). Design of Exponentially Weighted Moving Average Schemes. Journal of Quality Technology, 21(3), 155-162. http://dx.doi.org/10.1080/00224065.1989.11979164.
http://dx.doi.org/10.1080/00224065.1989....
, for curves of k×λ — also called iso-ARL0 curves — for the univariate EWMA chart for monitoring the process mean). In the case of the GEWMA-d¯ chart, this relation will depend also on the number of streams (m). For illustration, Figure 1 shows the GEWMA-d¯ iso-ARL0 curves for m=20 streams, for 3 different ARL0 values. These curves were obtained by simulation and search: discretizing the range of possible values for λ, for each value of λ considered, a univariate search was conducted for the value of k that yielded the desired ARL0 (computed by simulation). The dots on the curves in the Figure are the points λ,k thus obtained. Other points in the curve can be obtained by linear interpolation. So, each curve contains all points λ,k that give a same ARL0. These curves are helpful in the stage of optimization of the chart, described in detail the next section. In summary, given the specified ARL0, the goal is to find the pair λ,k in the respective curve that yields the shortest ARL1 for a shift of interest in the mean in one stream.

Figure 1
k×λcurves for the GEWMA-d¯ chart for 20 streams

For a fair performance comparison of the (optimized) EWMA-d¯ chart with Mortell & Runger’s (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
EWMA-Rt chart and Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
MEWMA-S2 chart, we must use the optimal designs of these charts too. As a prerequisite to the optimization, we determined, in the same way, iso-ARL0 curves for the EWMA-Rt and the MEWMA-S2 charts. Figures 2 and 3 exhibit the curves for 20-stream processes and 3 different ARL0 values. Curves for other numbers of streams are given in Simões (2010)Simões, B. F. T. (2010). Controle estatístico de processos multicanal (Tese de doutorado). Pontifícia Universidade Católica do Rio de Janeiro - PUC-Rio, Rio de Janeiro. and are available upon request. To the best of our knowledge, there is no work in the literature that gives the k×λ curves for these charts.

Figure 2
k×λ curves for the EWMA-Rt chart for 20 streams
Figure 3
k×λ curves for the MEWMA S2 chart for 20 streams

5 Optimal designs

With m, n, ARL0 and δ* given, we obtain the best design for the GEWMA-d¯ chart solving the following optimization problem (Equation 12):

M i n A R L 1 δ * , θ (12)

subject to (Equation 13)

A R L δ = 0, θ = A R L 0 (13)

where:

δ=μ1μ0/σ0 is a shift in the in-control mean of an individual stream component ei, represented in standard deviation units; note that, as we assume that the in-control mean of any individual stream component is zero (that is, Eetij=0), δ=μ1/σ0.

δ* is the smallest shift in the mean of the individual component of a stream that is considered relevant to detect with minimum delay (for which ARL1 should be minimized);

θ represents the set of parameters of the chart: θ=n,m,kλ, where the notation kλ indicates that, given the desired ARL0, k is uniquely determined by the respective iso-ARL0 curve as a function of λ, as just seen in the preceding section.

With k thus determined as a function of λ, and with n and m as input data, λ becomes the only decision variable, so the optimal solution can be found by any univariate search method. We chose to use the Golden Section Search method (Kiefer, 1953Kiefer, J. (1953). Sequential minimax search for a maximum. Proceedings of the American Mathematical Society, 4(3), 502-506. http://dx.doi.org/10.1090/S0002-9939-1953-0055639-3.
http://dx.doi.org/10.1090/S0002-9939-195...
), programmed in MatlabTM. For each value of λ, the ARL1 for the δ* specified was obtained by simulation. The search was considered to have converged when the last interval was smaller than 0.005. This termination criterion was based on previous observation that the ARL1 as a function of λ is quite flat around the minimum. The midpoint of the last interval was then considered to be the optimal solution.

The optimal values of λ and k, under the constraint of ARL0 = 200, are shown in the columns with headings λ* and k* of Table 2 (for n = 1) and Table 3 (for n = 4), for m = 5, 10 and 20 streams and δ*= 0.5, 1.0 and 2.0. Larger values of δ* were not considered because EWMA schemes are devised for the detection of small to moderate changes in the process parameters. Optimal designs for other numbers of streams in the process (namely, m = 2, 3 and 15) and also for other ARL0 values (ARL0 = 100 and 370.4) can be found in Simões (2010)Simões, B. F. T. (2010). Controle estatístico de processos multicanal (Tese de doutorado). Pontifícia Universidade Católica do Rio de Janeiro - PUC-Rio, Rio de Janeiro. and can be obtained by request to the first author.

Table 2
Optimal designs (λ* and k*) and ARL profiles, for ARL0 = 200.0 and n = 1.
Table 3
Optimal designs (λ* and k*) and ARL profiles, for ARL0 = 200.0 and n = 4.

As seen in these tables, we also optimized the designs of the EWMA-Rt and MEWMA-S2 charts (for the same values of m, n, δ* and ARL0), for the purposes of performance comparison (which is the subject of the next section). The optimization problem statement and the solution method are the same for all charts; only the monitoring statistic and control limits differ. The monitoring statistics of the EWMA-Rt and MEWMA S2 charts were described in Section 2. We now describe how their control limits are related to k, for full understanding of their designs in Tables 2 and 3.

Note that these charts have only one (upper) control limit (UCL), because their statistics are positive and only increases in their expected values indicate out-of-control situations. The UCL of the EWMA-Rt chart is given by Equation 14

U C L = d 2 + k d 3 λ 2 λ σ 0 n (14)

Where, again, k denotes the control limit factor, and d2 and d3 are the mean and standard deviation of the relative range for normal data, which are tabulated in many statistical and SPC books. Note that, here, the “sample size” to which d2 and d3 correspond is the number of streams, m, rather than the number of observations per stream, n, in time t.

In the case of the MEWMA S2 chart, k is the very control limit (that is, UCL = k), because when the process is in control the MEWMA statistic (Wt) has unit variance. Indeed, in sampling time t, the statistic is (using our notation for consistency) (Equation 15)

W t = n 2 λ σ 0 2 λ i = 1 m Z t i Z ¯ t 2 (15)

where Zti is the exponentially smoothed value of the i-th stream and Z¯t is the sample average (over i) of the Zti’s. Since the variance of i=1mZtiZ¯t2 is σ02/nλ/2λ, Wt has unit variance.

When the process is in control, Wt is distributed as a chi-squared variable with m1 degrees of freedom; this is why the values of k for this MEWMA chart in Tables 2 and 3 increase noticeably with m. In Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
, in the expression of Wt the factor that appears pre-multiplying the summation is σ02λ/2λ, which is clearly a typo.

The column k* of Tables 2 and 3 gives also), in one row for each pair (m, n), the control limit factor k of the Shewhart-type residuals GCC of Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
. The control limits for this chart are set at ±kσ0m1/mn. Note that this expression corresponds to Equations 10a and 10b in the particular case λ=1. Indeed, the Shewhart chart can be seen as a particular case of an EWMA chart with λ=1. With λ thus fixed (and considering n given), the constraint on ARL0 determines uniquely the value of k, so (unlike with the EWMA charts) there is no possibility of optimizing the Shewhart chart for a given δ*; this is why for this chart the values of δ* are left blank and there is only one value of k for each pair (m, n), while for the EWMA charts λ*, k* and the ARL1 profile depend on the value of δ* besides of the values of (m, n).

6 Performance analysis

Tables 2 and 3 show also the steady-state ARL1 profiles (steady-state ARL1 values for a range of shifts in the mean of one stream) of the GEWMA-d¯ chart, the residuals GCC of Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
, the EWMA-Rt chart of Mortell & Runger (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
and the MEWMA-S2 chart of Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
, for process with 5, 10 and 20 streams, and for the cases of 1 and 4 observations per stream. The ARLs for the shifts for which the charts were optimized δ* are in bold. Recall that, being a Shewhart-type chart, the residuals GCC with fixed n and ARL0 constraint does not admit optimization. Tables of ARL profiles of the EWMA charts for m = 2, 3 and 15 and also for ARL0 = 100 and 370.4 are available upon request to the first author. For ARL profiles of the residuals GCC, refer to Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
.

It can be seen that the GEWMA-d¯ chart outperforms the other EWMA charts practically always: the ARL reduction relative to the MEWMA-S2 chart is smaller (but consistent), while the reduction relative to the EWMA-Rt chart is substantial. The only exception was with n = 1 and δ*=0.5. In this case, for shifts of 4 standard deviations, the ARL of the EWMA-Rt chart was between 5% and 6% smaller. Nevertheless, given the two-component nature of the process variance (see Equation 2), we may expect that a shift of 0.5 standard deviations of the individual component (i.e., 0.5σ0) is likely to be substantially smaller in terms of the total standard deviation and, as a result, not typically relevant, so that in most practical situations the charts should be optimized for shifts larger than δ*=0.5.

The residuals GCC was considered just for completeness and for reference, since it was expected that its EWMA counterpart (the GEWMA-d¯ chart), and also the other EWMA charts, yielded much lower ARL1 values. As a matter of fact, the residuals GCC, with n = 1, outperforms the GEWMA-d¯ chart for δ4 (and for δ3 in the case of δ*=0.5 with m = 10 and 20). With n = 4, in the case δ*=0.5 or 1.0, the residuals GCC outperforms the GEWMA-d¯ chart for δ2; in the case δ*=2.0, the GEWMA-d¯ chart is always the most efficient of all charts considered. Note that EWMA charts are devised for quicker detection of small and moderate shifts; for large shifts it is natural that Shewhart-type charts provide shorter ARLs (being, nevertheless, much slower in the detection of small and moderate shifts). So the GEWMA-d¯ chart achieves its objective, being, for the detection of small and moderate shifts, the most efficient among the EWMA charts considered. The comparison with the residuals GCC was useful to show in which situations (for which sizes of shift) each one is preferable.

To provide a general picture of the quantitative improvement attained with the new chart, Figure 4 shows the ARL curves of the three charts with n=1 for the case of 20 streams, optimized for δ*=0.5. For a better visualization, due to the large variation in the magnitude of the ARLs with the mean shifts, the figure was split into two parts with different vertical scales, one for shifts up to 1.5 standard deviations and the other for shifts from 1.5 to 4.0 standard deviations.

Figure 4
ARL1 profiles for n = 1 (m = 20 streams, ARL0 = 200.0, optimized for δ = 0.5).

Figure 5 is similar to Figure 4, now for the case of subgroups of size n=4 per stream. The same pattern can be observed. The GEWMA-d¯ chart uniformly outperforms the other EWMA charts: it slightly outperforms the MEWMA-S2 chart and substantially outperforms the EWMA-Rt chart. They are outperformed by the residuals GCC only for the largest shifts.

Figure 5
ARL1 profiles for n = 4 (m = 20 streams, ARL0 = 200.0, optimized for δ = 0.5).

6 Conclusions

Our objective, as stated in the Introduction section of this paper, was to propose of an EWMA group control chart (GCC) on the smallest and the largest estimates of the individual streams components of a MSP, optimize it and and analyze its performance. This chart is the EWMA counterpart of Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
Shewhart-type residuals GCC. For this, we would first need to define the computation of the EWMA statistic to use, the calculation of the chart parameters, and describe its operation. Our motivation was the expectation that such a chart might be faster in detecting small and moderate shifts in the mean of individual streams of the process than the EWMA versions of Mortell & Runger’s (1995)Mortell, R. R., & Runger, G. C. (1995). Statistical process control of multiple stream processes. Journal of Quality Technology, 27(1), 1-12. http://dx.doi.org/10.1080/00224065.1995.11979554.
http://dx.doi.org/10.1080/00224065.1995....
Rt chart (EWMA-Rt) and Runger et al. (1996)Runger, G. C., Alt, F. B., & Montgomery, D. C. (1996). Controlling multiple stream processes with principal components. International Journal of Production Research, 34(11), 2991-2999. http://dx.doi.org/10.1080/00207549608905074.
http://dx.doi.org/10.1080/00207549608905...
S2 chart (MEWMA-S2). So a second objective was to compare the performances of the proposed chart with the previous ones, in equivalent conditions. This required optimizing all the charts for a variety of situations and for different sizes of shift in the mean of an individual stream, compute their ARLs and compare them side by side. The objective of the optimization was to obtain the design that yields the shortest out-of-control ARL (ARL1) possible for a given shift (specified), subject to a constraint on the value of ARL0.

We succeeded in achieving all these objectives, and named our chart the GEWMA-d¯ chart. The comparative performance analysis confirmed our expectations: for the detection of shifts in the mean of the individual component of a single stream, the GEWMA-d¯ chart has shown to outperform, in virtually all the cases analyzed, the EWMA-Rt and MEWMA-S2 charts. Its ARLs were smaller than the ones of the latter and dramatically smaller than the ones of the former.

The only exception observed was when the charts are used with a sample size of 1 and are optimimized for a shift of 0.5 standard deviations. In this case, and only for very large shifts (of the order of 4 or more standard deviations), the ARL of the EWMA-Rt chart was smaller. Nevertheless, given the two-component nature of the process variance, we may expect that a shift of 0.5 standard deviations of the individual component is likely not be typically relevant and that in most practical situations the charts should be optimized for shifts larger than this value. In this case, the proposed chart uniformly outperforms the other two. The differences in performance (i.e., the advantages of the proposed chart) increase with the number of streams.

For signalling larger shifts (of the order of 3 or more standard deviations), the Shewhart-type residuals GCC of Epprecht et al. (2011a)Epprecht, E. K., Barbosa, L. F. M., & Simões, B. F. T. (2011a). SPC of multiple stream processes – a chart for enhanced detection of shifts in one stream. Produção, 21(2), 242-253. http://dx.doi.org/10.1590/S0103-65132011005000022.
http://dx.doi.org/10.1590/S0103-65132011...
is the fastest chart; this was expected since the EWMA charts are devised for protection against small and moderate shifts and Shewhart charts tend to be faster against larger shifts.

An additional contribution of this work are the optimal designs obtained for the EWMA-Rt and MEWMA-S2 charts, which had not been given in the previous literature.

As a conclusion, the GEWMA-d¯ chart is recommended for the monitoring of small and moderate shifts of the mean of individual streams, being in this case the fastest of the charts considered.

Acknowledgements

The authors have been partly supported by the CNPq (Brazilian Concil for the Scientific and Technological Development), project numbers 140933/2006-9, 302326/2008-1 and 308677/2015-3. They are grateful to the anonymous reviewers whose comments contributed to improve the quality of this paper.

  • Financial support: CNPq (Conselho Nacional de Desenvolvimento Científico e Tecnológico), project numbers 140933/2006-9, 302326/2008-1 and 308677/2015-3.
  • How to cite: Simões, B. F. T., & Epprecht, E. K. (2021). An EWMA control chart for the mean of individual streams in multiple stream processes. Gestão & Produção, 28(3), e062. https://doi.org/10.1590/1806-9649-2021v28e062

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  • Xiang, L., & Tsung, F. (2008). Statistical monitoring of multi-stage processes based on engineering models. IIE Transactions, 40(10), 957-970. http://dx.doi.org/10.1080/07408170701880845
    » http://dx.doi.org/10.1080/07408170701880845

Publication Dates

  • Publication in this collection
    12 July 2021
  • Date of issue
    2021

History

  • Received
    12 Sept 2020
  • Accepted
    18 Jan 2021
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