Six Sigma 5 - Control
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Transcript of Six Sigma 5 - Control
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D M A I C
Control
Control
Six Sigma Road Map
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D M A I C
Control
QFDProcess Mapping
Measurement Systems
Benchmarking/Baselining
Yield & SigmaBasic Quality Tools
Design of Experiments
Brainstorm & Workout
Control Charts
Procedures
Training
ProductProduct
oror
ServiceService
1 Select CTQ Characteristics
2 Define Performance Standards
3 Validate Measurement System
4 Establish Product Capabili ty5 Define Performance Objectives
6 Identify Variation Sources
7 Screen Potential Causes
8 Discover Variable Relationships9 Establish Operating Tolerances
10 Validate Measurement System
11 Determine Process Capabil ity
12 Implement Process Controls
MMeasureeasure
IImprovemprove
CControlontrol
AAnalyzenalyze
StrategyStrategy CookbookCookbook Tools &Tools &
ConceptsConcepts
DDefineefine Define the problem Select cross-functional team Define team charter
Moving into the Control Phase
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Control
Control: Main Objectives/Deliverables
To make sure that ourprocess stays in control after the solution
has been implemented.
To quickly detect the out of control state and determine the
associatedspecial causes so that actions can be taken to correct
the problem before nonconformances are produced.
Develop and implement control system
Determine improved process capability
Given the planned capability for controlling the Xs, what will
be the new and improved capability for the process CTQ(s)?
Process Before
Improvement
LSL USL
Process After
Improvement
LSL USL
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Maintaining Control
Keep Xs within tolerance by using appropriate
controls (Risk Management, Mistake Proofing, etc.)
Apply control charts to Xs to monitor and control
variation.
Understand implications on existing quality plans due tomodification of current control systems.
Establish transition plan for maintaining control of
improved process (training plan, audit plan, etc.).
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What is a Process Control System? A process control system
strategy for maintaining the improved process performance
over time
identifies the specific actions and tools required for
sustaining the process improvements or gains
A control system may incorporate
Risk Management
Mistake-proofing devices
Statist ical process control (SPC)
Data collection plans
Ongoing measurements
Audit plans
Response or Action plans
Product drawings
Process documentation
Process ownership
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Control
Why is a Process
Control System Important? Defines the actions, resources, and responsibilit iesneeded to make sure the problem remains corrected and thebenefits from the solution continue to be realized.
Provides the methods and tools needed to maintain the
process improvement, independent of the current team.
Ensures that the improvements made have been
documented (often necessary to meet regulatoryrequirements).
Facilitates the solution's full-scale implementation by
promoting a common understanding of the process and plannedimprovements.
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Key Steps in
Developing a Process Control System1. Complete an implementation plan.
Plan and implement the solution and develop a method to controleach vital X or key sources of variation
Define all possible areas that may require action in order to
control the process X and then determine the appropriate course
ofaction to take
2. Develop a data collection plan to confirm that your solution
meets your improvement goals. Establish ongoing measurements needed for the project Y and
create a response plan to follow in case process performance falls
below established standards
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D M A I C
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3) Communicate your strategy.
Document the process and control plan to ensure process
standardization and the continuation of the solution's benefits
4) Train Personnel.
5) Run the new process and collect the data to confirm
your solution.
Key Steps (contd)
Th M i C t l M h i
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Three Main Control Mechanisms
Risk
Management
Risk
Management
SPCSPC
MistakeProofingMistakeProofing
Control
PotentialProblems
Avoid
PotentialProblems
D M A I C
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Determine the probability and impact of each riskpresented by the planned process change.
Link the probability and impact of occurrence to the risk,then determine the abatement action.
Assign ownership and determine timing for eachabatement action.
Risk Management
Recommended tool
Failure Modes & Effects Analysis (FMEA)
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Mistake Proofing Helps to sustain a solution by eliminating the possibility thatan X can be set outside the desired level or configuration...or
Warns the process operator before the X goes outside limitsso preventative action can be taken.
Mistake proofing can be used alone or with either riskmanagement or statistical process control to sustain a solution.
D M A I C
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Control charts can be used to monitor Xs and quicklydetect a change in the process due to special cause
variation.
Very helpful when your Xs cannot be mistake proofed or
easily controlled within the required tolerance range.
Statistical Process Control
Tool we will look at Shewhart control charts,
as an introduction to SPC
D M A I C
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Introduction to Statistical Process Control (SPC)
(Recommended reference: Montgomery, Doug (2001).Introduction to StatisticalQuality Control, 4th edition, John Wiley & Sons, New York, NY.)
From Montgomery:
SPC a powerful collection of problem-solving tools useful in
achieving process stability and improving capability through
the reduction of variability.
SPC can be applied to any process. Its seven major tools (often
referred to as the magnificent seven) are:
Histogram or stem-and-leaf display
Check sheet
Pareto chart Cause-and-effect diagram
Control chart
Scatter diagram
Defect concentration
diagram
Focus of
remaininglectures
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Concepts/definitions:
Common cause variability Inherent or natural variability in a
process, which is the cumulative effect of essentially unavoidable
causes.
Assignable cause or special cause variability - above and
beyond the natural process variability. In a manufacturing process,this often comes from improperly adjusted machines, operator error
or defective raw material. This may result in a shift in the process
mean, an increase in the process variability, or both.
Statistical process control charts are used to detect the presence
of an assignable causes, by detecting a shift in the mean of
the parameter being monitored, an increase in its variance,or both.
D M A I C
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Statistical basis of the Control Chart
Sample number or time
Sam
plequalitycharacteristic
Upper control limit (UCL)Usually center line + 3s, where
s is the standard error of the
quality characteristic being plotted.
Lower control limit (LCL)Usually center line - 3s, where
s is the standard error of the
quality characteristic being plotted.
Center line avg value of the
sample quality characteristicwhen the process is in control
When the process is in control, all points should fall within the UCL
and LCL, in an essentially random pattern.
D M A I C
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D M A I C
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Relationship between control charts and hypothesis testing
Some similarities:
Suppose the sample quality characteristic being plotted (vertical axis) is
. If the current value of plots between the control limits, then we conclude
that the process mean is in control; that is, it is equal to some value 0 . Ifexceeds either limit, we conclude that the process mean is out of control; that
is, it is equal to some value 1 0.
Type I and II errors apply to performance of control charts- Type I error is concluding that an in-control process is out of control
- Type II error is concluding that in out-of-control process is in control
Some differences:
When testing statistical hypothesis, usually check for validity of
assumptions. Control charts are used to check for departure from an assumed
state.
Assignable cause can result in different types of shifts in process parameters
(e.g. sustained shift or abrupt temporary shift or steady drift).
X
X
X
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D M A I C
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Samplequalitycharacteristic Upper control limit (UCL)
Lower control limit (LCL)
Center line
Detect a process shift and correct it, before it ever exceeds the
specification limits (ie results in unacceptable quality)
Controlling the process parameter within specification/tolerance
Upper specification limit (USL)
Lower specification limit (LSL)
Sample number or time
D M A I C
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Process improvement using a control chart
ProcessProcess
Measurement SystemMeasurement System
Input Output
Detect assignable cause
Identify root cause
of the problem
Implement
corrective action
Verify and
follow up
D M A I C
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Guide to Univariate Process Monitoring and Control
Continuous or Discrete data?
Sample size Data type
ContinousDiscrete (attribute)
Shift sizeto detect
n>1 n=1fraction Defects (count)
large small large small large small large small
SXRX,, Cusum
EWMACusumEWMA
CusumEWMA
Using p
Cusum
EWMAUsing c,u;
time between
events
cu
pnp
X (individuals)
MR
Shift sizeto detect
Shift sizeto detect
Shift sizeto detect
Assumption: Process data is not autocorrelated
Shewhart control chartsDr. Walter Shewhart, Bell Labs, 1920s
(
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Sensitizing rules for Shewhart control charts
1. One or more points outside of the control limits.2. Two of 3 consecutive points outside the 2-sigma warning limits but still
inside the control limits.
3. Four of 5 consecutive points beyond the 1-sigma limits.
4. A run of 8 consecutive points on one side of the center line.5. Six points in a row steadily increasing or decreasing.
6. Fifteen points in a row in zone C.
7. Fourteen points in a row alternating up and down.
8. Eight points in a row on both sides of the center line with none in zone C.9. An unusual or nonrandom pattern in the data.
10. One or more points near a warning or control limit.
estern
lectric
ules
+ 1 s.e.
-1 s.e.
Zone C
-2 s.e.
+ 2 s.e.
+ 3 s.e.
-3 s.e.
D M A I C
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Guide to Univariate Process Monitoring and Control
Continuous or Discrete data?
Sample size Data type
Continuous Discrete (attribute)
Shift sizeto detect
n>1 n=1fraction Defects (count)
large small large small large small large small
SXRX,, Cusum
EWMACusumEWMA
CusumEWMA
Using p
Cusum
EWMAUsing c,u;
time between
events
cu
pnp
X (individuals)
MR
Shift sizeto detect
Shift sizeto detect
Shift sizeto detect
Assumption: Process data is not autocorrelated
Shewhart control chartsDr. Walter Shewhart, Bell Labs, 1920s
(
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Control
Shewhart control charts for a continuous Y or X
Need to monitor both the mean and variability of the variable (Y
or X).
Assume n > 1, for every sample collected over time
Monitor to control the process mean ( chart)
Monitor S (sample std dev) or R (sample range) to control the
process variability. (S chart or R chart)
Typically use an S chart if n >10-12 or if n varies from sample to
sample.
R chart is more commonly used than an S chart.
X X
D M A I C
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Constructing the and R chartsX
Statistical basis:
Assume that X, the process parameter to be monitored, is normallydistributed with mean and std deviation , both known.
Assume that we are collecting m samples of size n from the processover time. The sample data can be summarized by and
ri for i= 1, m.
Therefore,
ix
=+
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Control
Typically, and are unknown, so they must be estimated fromthe sample data.
Unbiased estimator for is mix
m
xi
i ,...,1,1
==
Unbiased estimator for is , where
and d2 is listed for various sample sizes in Appendix Table VI of
Montgomerys SQC book (reference given in Control 2.ppt).
2d
R miRm
Ri
i ,...,1,1
==
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Constructing the chartX
Centerline = X
LCL =
=
ndRX2
3nd
RX2
3+UCL =
=RAX 2 RAX 2+
Where A2 is found in Appendix Table VI.
See Piston ring example from handout (Montgomery, pages 213-215).
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C l
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Constructing the and R charts in MinitabX
Piston ring example:
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Select
Xbar-R
chart
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C t l
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D M A I C
C t l
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252015105Subgroup 0
74.015
74.005
73.995
73.985
SampleM
ean
X=74.00
3.0SL=74.01
-3.0SL=73.99
0.05
0.04
0.03
0.02
0.01
0.00SampleR
ange
R=0.02324
3.0SL=0.04914
-3.0SL=0.00E+
Xbar/R Chart for x1-x5
Minitab output:
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P-chart example (with Minitab)
See example 6-1 in Montgomery, pages 288-290 of handout.
N=50 for each of the 30 samplesSampl e Di
num1 122 153 8
4 105 46 77 168 99 1410 1011 512 6
13 1714 1215 22
16 817 1018 5
19 1320 1121 2022 1823 2424 1525 926 1227 7
28 1329 930 6
Sampl e Di
num
D M A I C
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Minitab input:
D M A I C
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Since our n was constant for all samples,it can be entered as a constant here.
D M A I C
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Control
3020100
0.5
0.4
0.3
0.2
0.1
0.0
Sample Number
Proportion
P Chart for Di
1
1
P=0.2313
3.0SL=0.4102
-3.0SL=0.05243
Minitab output: