Confidence interval and tests on process capability ratios • Note that Cˆp or Cˆpk is a simply point estimate. It is more necessary to report the Home Page Title Page JJ II J I Page 1 of 37 confidence interval for PCR. Go Back Full Screen Close Quit • For the “first generation” ratio Cp, replace σ by S, Cˆp = (U SL − LSL)/(6S), the 100(1 − α)% confidence interval is: Home Page Title Page s Cˆp χ21−α/2,n−1 n−1 s ≤ Cp ≤ Cˆp χ2α/2,n−1 n−1 JJ II J I Page 2 of 37 . Go Back Full Screen Close Quit Example. Suppose U SL = 62, LSL = 38, n = 20, CL ≈ T = (U SL + LSL)/2 and S = 1.75, then the point estimate of Home Page Title Page Cp is JJ II J I Page 3 of 37 62 − 38 Cˆp = = 2.29, 6 × 1.75 Go Back Full Screen Close Quit and the 95% confidence interval on Cp is r 2.29 r 8.91 32.85 ≤ Cp ≤ 2.29 , 19 19 1.57 ≤ Cp ≤ 3.01, Home Page Title Page JJ II J I Page 4 of 37 where χ20.975,19 = 8.91 and χ20.025,19 = 32.85. Go Back Full Screen Close Quit This confidence interval seems wider (small sample). • Use S rather than R/d2 to estimate σ and Home Page Title Page the process must be in statistical in control. Otherwise, S and R/d2 could be very dif- JJ II J I Page 5 of 37 Go Back ferent. Full Screen Close Quit • For Cpk and Cpm, the approx. 100(1 − α)% confidence interval on Cpk is Home Page s Cˆpk 1 − Zα/2 1 1 ≤ C + pk 2 ˆ 9nCpk 2(n − 1) s 1 1 ˆ ≤ Cpk 1 + Zα/2 . + 2 9nCˆpk 2(n − 1) Title Page JJ II J I Page 6 of 37 Go Back Full Screen Close Quit Example. n = 20 from stable process id used to estimate Cpk with Cˆpk = 1.33. Home Page Title Page Then an approx. 95% confidence interval on Cpk is JJ II J I Page 7 of 37 Go Back Full Screen Close Quit r 1.33 1 − 1.96 1 1 + 2 9 × 20 × 1.33 2 × 19 ≤ Cpk ≤ r 1.33 1 + 1.96 Home Page Title Page 1 1 + 2 9 × 20 × 1.33 2 × 19 , JJ II J I Page 8 of 37 Go Back or 0.99 ≤ Cpk ≤ 1.67. Full Screen Close Quit It could be very wider since from 0.99 < 1 Home Page (bad case ) to 1.67 (good case). • Small sample is main reason. Title Page JJ II J I Page 9 of 37 Go Back Full Screen Close Quit • For Cpc, we estimate E|X − T | by c = Pn 1 i=1 |xi − T |, it leads to the estimator n Home Page Title Page U SL − LSL ˆ p Cpc = . 6c π/2 JJ II J I Page 10 of 37 Go Back Full Screen Close Quit A 100(1 − α)% confidence interval for E|X − T | is approx. given as follows: Home Page Title Page sc c ± tα/2,n−1 √ , n JJ II J I Page 11 of 37 Go Back Full Screen Close Quit where s2c 1 = n−1 n X (|xi − T | − c)2 i=1 n X 1 [ |xi − T |2 − nc2]. = n − 1 i=1 Home Page Title Page JJ II J I Page 12 of 37 Go Back Full Screen Close Quit Thus, a 100(1 − α)% confidence interval for Cpc is Home Page Title Page Cˆpc 1+ tα/2,n−1sc √ c n ≤ Cpc ≤ Cˆpc 1− tα/2,n−1sc . √ c n JJ II J I Page 13 of 37 Go Back Full Screen Close Quit Testing hypothesis about PCRs Consider the hypothesis testing problem: Home Page Title Page H0 : Cp = Cp0(target value), H1 : Cp > Cp0. JJ II J I Page 14 of 37 Go Back Full Screen Close Quit Here we may define in advance Cp(High) [Cp (Low)] as a process capability that we Home Page Title Page would like to accept [reject] with prob. 1− α [1 − β]. JJ II J I Page 15 of 37 Go Back Full Screen Close Quit Table 7-5 gives Cp(H)/Cp(L) and Home Page C/Cp(L) for varying sample sizes and α = β = 0.05 or α = β = 0.10. Title Page JJ II J I Page 16 of 37 Go Back Full Screen Close Quit Home Page Title Page JJ II J I Page 17 of 37 Go Back Full Screen Close Quit See also the following figure. Actually, q C/Cp(L) = 1/ χ2α,n−1/(n − 1). Home Page Title Page JJ II J I Page 18 of 37 Go Back Full Screen Close Quit Home Page Title Page JJ II J I Page 19 of 37 Go Back Full Screen Close Quit Home Page Title Page JJ II J I Page 20 of 37 Go Back Full Screen Close Quit Example. A supplier is told to demonstrate that his process capability exceeds Cp = 1.33. Thus, he want to test H0 : Cp = 1.33, H1 : Cp > 1.33. Home Page Title Page JJ II J I Page 21 of 37 Go Back Full Screen Close Quit If Cp is below 1.33, there will be a high prob. of detecting this (90%), whereas if Home Page Title Page Cp exceeds 1.66, there will be a high prob. of judging the process capable (90%). JJ II J I Page 22 of 37 Go Back Full Screen Close Quit It means α = 0.10, β = 0.10 and Cp(H) = 1.66, Cp(L) = 1.33, Cp(H)/Cp(L) = 1.25. Home Page Form Table 7-5, we get n = 70 and C/Cp(L) = 1.10 and C = 1.33 × 1.10 = Title Page JJ II J I Page 23 of 37 Go Back 1.46. Full Screen Close Quit Process performance indices AIAG(Automotive Industry Action Home Page Group) recommended process capability indices Cp and Cpk when the process is in Title Page JJ II J I Page 24 of 37 control with σˆ = R/d2. Go Back Full Screen Close Quit When the process is not in control, AIAG use process performance indices: Pp and Ppk , Pˆp = (U SL − LSL)/(6S), Pˆpk is similar. S and R/d2 is quite different in this Home Page Title Page JJ II J I Page 25 of 37 case. Go Back Full Screen Close Quit Process capability analysis using a control chart Home Page • Histograms, PP, PCR summarize the performance of process. They do not address Title Page JJ II J I Page 26 of 37 the issue of statistical control. Go Back Full Screen Close Quit • Control chart should be regard as the primary technique. Home Page Title Page Bottle bursting strength. Sample size 5 for each subgroup. JJ II J I Page 27 of 37 Go Back Full Screen Close Quit R chart: U CL = D4R = 2.115 × 77.3 = 163.49, CL = R = 77.3, LCL = D3R = 0. Home Page Title Page JJ II J I Page 28 of 37 Go Back Full Screen Close Quit x chart: U CL = x + A2R = 264.06 + 0.577 × 77.3 = 308.66, CL = x = 264.06, LCL = x − A2R = 264.06 − 0.577 × 77.3 = 219.46. Home Page Title Page JJ II J I Page 29 of 37 Go Back Full Screen Close Quit µˆ = 264.06 and σˆ = R/d2 = 77.3/2.326 = 33.23. Then, the one-side PCR is estimated by Home Page Title Page µ − LSL 264.06 − 200 ˆ = = 0.64. Cpl = 3ˆ σ 3 × 33.23 JJ II J I Page 30 of 37 Go Back This process capability is inadequate. Full Screen Close Quit • Although a process is in control, but operating at a an unacceptable level. Home Page • Control chart can be used as monitoring device or logbook or show the effect Title Page JJ II J I Page 31 of 37 of changes. Go Back Full Screen Close Quit • Process is out-of-control, it is unsafe to estimate the process capability. Stable Home Page process is needed. Process capability analysis using de- Title Page JJ II J I Page 32 of 37 signed experiments Go Back Full Screen Close Quit Control charts and tabular methods • 2 σtotal = 2 σproduct + 2 σgage . Home Page Title Page JJ II J I Page 33 of 37 Go Back Full Screen Close Quit Measuring gage capability. See Figure 7-13. The std. of measurement error σgage can be estimated by σgage = R/d2 = 1.0/1.128 = 0.887. Home Page Title Page JJ II J I Page 34 of 37 Go Back Full Screen Close Quit Home Page Title Page JJ II J I Page 35 of 37 Go Back Full Screen Close Quit Usually 6σgage is a good estimate of gage capability: 6σgage = 6 × 0.887 = 5.32. Home Page Title Page JJ II J I Page 36 of 37 Go Back Full Screen Close Quit • P/T ratio ( precision-to-tolerance band): P 6ˆ σgage = . T U SL − LSL Home Page Title Page For example 7-7, we have P/T = 6 × JJ II J I 0.887/(60 − 5) = 0.097. Page 37 of 37 Go Back Full Screen Close Quit
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