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    Therm-O-Disc Inc. Product Engineering Dept

    Performance ImprovementSix W Project EPR 17340

    12D Pressure Release Thermal Sensor

    Engineering Analysis

    Changqi John Liu, Ph.D

    Created on 07/20/2005

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    Topics in This Presentation

    - Phase (1): Measurement

    Project Scope(1)

    Problem Statement

    Objective

    Team Members

    Physical Concept for 12D-Temp Control and Pressure Release Valve

    Major Output: TFD and Its Standard Deviation Target plan

    Cause and Effect Diagram Process Map Analysis

    Process Capability Analysis On 3/4/2005 At Project Start

    Process Capability Analysis on 04/21/05 and Results Analysis

    Improvement (1)-Blank Failure Analysis

    Improvement (2)-Second Stress Relief

    Improvement (3)-Stability Process

    DOE and Results analysis Process Optimization

    Confirmation test and results

    Conclusions

    Project Plan in Future Phase

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    Project Scope

    Problem Statement: 12D, Style 46338 Copeland Disc is a newlydeveloped Product. The first temp sorting reject rate is

    approximately to 450,000 PPM. Annual volume estimated to reach

    4.5 million in 2007. The high rate of first reject discs resulted in

    reworking labor increase by 6500 hour per year. The high rate of

    final scrap disc resulting in cost increased by $ 283,500 per year.

    Objective: By optimizing the process parameters to reduce first

    rejection scrapped discs by 10% by July 2005. This will yield about

    annually $97,600 cost saving per year. ( In long run, we will try to get

    scrap discs less than 150,000 PPM. If the final objective is reached it

    will generated about annually $189,000 cost reduction.

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    Team Members

    Changqi Liu: Sr. Project Engineer ( Mansfield ) Chen, Jianbang: Sr. Manufacture Engineer (

    China )

    Wu, Roy: Quality Engineer ( China )

    Zhang, Shear: Process Control Engineer ( China )

    Support Management Chua, Ck: Lean Manufacturing Manager

    Gurski, Mike: Engineering Manager

    Evans, Garry: Quality Control Manager

    Mansfield Support

    Born, Michael; Mueck, Jeff, Disc Dept

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    12D Disc with Different View Point

    Snap Action at Open/Close Temp

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    Disc Snap Open to Release the Pressure

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    Primary Metric

    Sigma vs. Date

    0

    1

    2

    3

    4

    5

    6

    7

    3/4/2005 4/3/2005 5/4/2005 6/3/2005 7/4/2005 8/4/2005 9/3/2005 10/4/2005 11/3/2005

    Date

    Sigma

    Projected

    Target

    Actual

    It should be here to get ~ 4.2 o F at the

    6 project completion

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    Objected Parameter

    S No Projected W Average* U S Limit L S Limit Z Level-U Z Level-L PPM-U PPM-L PPM-T FTY

    o F o F o F o F %

    1 6.50 275.0 268.0 278.0 0.46 1.08 322206 140757 462964 53.70

    2 6.00 275.0 268.0 278.0 0.50 1.17 308538 121673 430210 56.98

    3 5.50 275.0 268.0 278.0 0.55 1.27 292720 101557 394278 60.57

    4 5.00 275.0 268.0 278.0 0.60 1.40 274253 80757 355010 64.50

    5 4.50 275.0 268.0 278.0 0.67 1.56 252492 59907 312399 68.76

    6 4.00 275.0 268.0 278.0 0.75 1.75 226627 40059 266686 73.33

    7 3.50 275.0 268.0 278.0 0.86 2.00 195683 22750 218433 78.16

    8 3.00 275.0 268.0 278.0 1.00 2.33 158655 9815 168471 83.15

    9 2.50 275.0 268.0 278.0 1.20 2.80 115070 2555 117625 88.24

    10 2.00 275.0 268.0 278.0 1.50 3.50 66807 233 67040 93.30

    11 1.50 275.0 268.0 278.0 2.00 4.67 22750 2 22752 97.72

    12 1.00 275.0 268.0 278.0 3.00 7.00 1350 0 1350 99.87

    13 0.50 275.0 268.0 278.0 6.00 14.00 0 0 0 100.00

    * Normal Centeris 273o F, It is allowed theactualcentercontrol between272and275o F

    W = 4.2 o F ~

    1st Sorting Yield to be 70%

    The target of the first phase is to obtain first sorting 70 %, final yield to 80%

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    Cause Effect Diagram

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    Process Flow Chart

    DPUHeat Treatment

    HT123

    BlankingB-3093-1

    DPUForming

    Auto Bumper

    DPUStress Relief

    SR 103

    DPU1st Thermal Cycle

    SR 105

    Bimetal RM StripRM 99033 MS-10

    DPU2nd Thermal Cycle

    SR 105

    Receiving Insp.MS-10, RMA-14-6

    Blanking Insp.QCW C10457

    Cleaning

    CL-355 & BF-603

    DeburringTM-701 & BF-605

    12DDisc Style No 46338

    Audit / In-Process

    QCW B-1425,12D

    701

    VA VA

    VAVA

    VA

    VAVA

    VA

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    Process Flow Chart (2)

    DPU

    3rd Thermal CycleSR 105

    DPU

    4th Thermal Cycle

    SR 105

    Tumbling or SR 103

    RFU

    Style No 46338

    Package

    Shipment

    4 Pot

    Sorting

    Yes

    No

    Cleaning

    CL - 355

    Dock Audit

    BF-609

    Inspection Audit

    QCW B1425

    12D Copeland Disc, Style 46338

    VA

    NVA

    VA VA

    VA

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    Process Mapping(1)-BlankingType o KPIVs(Xs) SPECs Gages KPOVS ( ys) Spec Data DPCT/WT RTY

    %

    CR Thickness MS-10, RM14-6 Digital Checker Thickness Unifor +/-I 0.D11

    C Grain Size MS-10, RM14-6 Optical Microscope Grain Size No. > 8

    C HES Hardness MS-10, RM14-6 Micro-Hardness Tester Hardness Value 210~260

    C LES Hardness MS-10, RM14-6 Micro-Hardness Tester Hardness Value 260~315

    C Cross Flatness MS-10, RM14-6 Special Tester Cross Curvature < 0.008"

    N Bonding Strength MS-10, RM14-6 Special Method, Visual De-layminated 0.005 1 Days CT 99.5

    C RM MS-10, RM14-6 Dimple Height B-3093

    N Cut MS-10, RM14-6 Visual Control Profile Hx B-3093

    N Layer MS-10, RM14-6 Visual Control Profile Hy B-3093

    CR Punches Dr. B-3093 Profilimeter Diameter D B-3093

    CR Setup BF-701 System Control Number Per Bag 320 o F 0.05 60 Min 95

    C Pieces/Bag BF 705 BF 701

    Vib. Frequency BF 706 Set

    Time BF 707 Timer Round Corner Radii 5E-04 45 Min 99.95

    Total 0.054 3 Days 94.6

    DPU

    Stamping

    Raw Material

    RM 99033

    Cleaning

    CL-355, BF603

    Heat Treatment

    Deburing

    Blank AuditCW-10457

    VA

    VA

    VA

    NVA

    Inspection

    MS-10, RM-14-6

    Store Room

    BF 605

    NVA

    VA

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    Process Mapping(2)-Calibration

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    PFMEA(1)

    Diff

    n

    FD/BFD f

    each disc res

    l

    in

    s

    andard deviati

    n wide

    Coolin

    Rate

    Chan

    ed

    Conveyernot s

    ooth to

    deliverDiscs are Wrapped

    Could not form the discFormin

    ability too low

    check every 20th lotToo Low Temp, EQ out ofControlchan

    e.

    Contact

    maintenan

    ce

    2

    84Metrology Instron1

    Too high Temp, EQ. Out of

    Control

    Forming ability

    ChangedForming conditions

    Heat

    Treatment

    4

    Disc equipment tooling wear.

    check Burr

    Punch tool is dull resulting in too

    much burrsharp edge

    Tooling

    needs

    grinding.

    1

    05Deburr operator1Vibration time too short2

    Disc operation effected

    by

    Edge burr exceeds

    .001"Deburring

    3

    present

    Contact

    maintenan

    ce

    3

    24

    Q.A. Visual

    Inspection2

    Cleaning process has poor

    filtration.4

    Disc oil and

    contaminationOil or contaminationCleaning

    2

    dia. and profile.operate correctlyout ofspecification

    81

    Press operator

    checks1Tooling d imensions incorrect8Disc willnotBlank D imensionBlanking1

    Recomme

    nded

    Action(s)

    R

    P

    N

    D

    e

    t

    Current Process

    ControlsO

    c

    c

    Potential Cause(s)/ Mechanism(s)

    ofFailureS

    e

    v

    Potential Effect(s) of

    Failure

    PotentialFailure

    Mode(s)

    Process

    Function

    Requirements

    Item

    #

    JIHGFEDCBA

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    Improvement (1)

    Effect of RM and Blanking

    RM Thickness Uniformity Parameter Uniformity Blank Number of Blank Disc Per Bag

    HY Lesson Failure Analysis

    Large Number Risk

    Low Yield Disc Unstable

    It is not the HT and Cleaning Process that depend the Numberof Blank Per Bag.

    It is Major the RM Parameter variation to Determine the

    Number Per Bag Blank Number Should be Optimized, A Plan was sent to China

    plant to do tests Yield vs. Number of Blank per Bag

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    Improvement(2)

    Second Time Stress Relief

    Second Time Stress Relief was done in China

    Plant which was originally used to correct the

    bad HY blank. After the blank was corrected, it is

    still being used in production.

    To increase the stability of disc.

    It can be get more upper and lower limit

    from 268/276 to 268/278 in process. It is proved to increase the life cycles also.

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    Process Analysis Step by Step on

    4/21/05

    PRA AsFed AS-SR As-1stC As-2ndC As-3rdC As-4thC 1stST

    o F

    Average 297.73 276.49 272.45 273.48 275.49 275.37 276.09

    Stdev 7.69 7.24 5.87 7.14 6.14 5.10 4.98

    Max 301.10 290.20 285.30 287.40 288.70 286.90 287.10

    Min 294.50 264.40 258.70 257.80 265.20 267.30 267.80

    Range 6.60 25.80 26.60 29.60 23.50 19.60 22.30

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    Process Capability at 4/25/05

    284280276272268264

    LSL U SL

    Process Data

    Sample N 120

    StDev(With in) 5.25000

    StDev(O veral l) 5.12431

    LSL 267.00000

    Target *

    U SL 283.00000

    Sample Mean 273.40000

    P otential (Within) C apability

    C PU 0.61

    C pk 0.41

    Lower C L 0.33

    Upper C L 0.49

    C C pk 0.51

    C p

    O verall C apability

    P p 0.52

    Lower C L 0.45Upper C L 0.59

    P P L 0.42

    P P U

    0.51

    0.62

    P pk 0.42

    Lower C L 0.34

    Upper C L 0.50

    C pm *

    Lower C L

    Lower C L

    *

    0.44

    Upper C L 0.57

    C PL 0.41

    O bserve d P erformance

    PP M < LSL 125000.00

    PPM > USL 25000.00

    PPM Tota l 150000.00

    Exp. Within Performance

    PPM < LSL 111413.06

    PPM > USL 33731.92

    PPM Tota l 145144.98

    Exp. O v erall Performance

    PPM < LSL 105842.15

    PPM > USL 30505.13

    PPM Total 136347.28

    W ithin

    O v erall

    Process Capability For 12 D 463 38 Disc Thermal Sensor(using 95.0% confidence)

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    Plan in Improvement Phase

    Blank Number Optimization: WAs formed vs. numberof blanks per bag (1500, 1750, 2000, 2250pieces/bag)

    HT Temp Optimization

    Use Appropriated HT System to get the right Open andDifferential ( 275/100 o F) Special for 12D 46338

    Punch Effect and Optimization

    SR and Stability Optimization

    Combination Effect DOE Test To get best two levels for above four factors to do the

    design of experimental

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    Improvement (3)

    Design Experiment Analysis

    Affecting Factors HT Temp, Time, Temp Creasing, Cooling Rate, Number per

    container

    Forming Conditions Penetration 1 and Penetration II

    Punch effect: Spherical Radium of 1st Punch

    SR Temp, Time, Temp Increasing Rate, Cooling Rate Number Per

    Basket

    Thermal Cycles

    Cycle time, Temp, Number Per Basket

    If each factor takes 2 levels, it will be 215 tests. It is too many

    tests to be performable. We need a Blocking Method.

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    DOE Analysis

    In this phase, the DOE will focus on SR andThermal Cycles

    Factors selected

    Number of Disc Per Container SR - Temp

    Thermal Cycle Temp and Cycle Times

    Altogether four factors, Each factor has two

    levels, The Complete tests are 24. It still toomany. we will take 8 tests

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    Table I Factors and Levels Being Selected

    Factor Level Low (Code: -1) Level High (Code: +1) Factor Code

    Stress Relief Temp 550 o F / 20 Min. 700 o F / 20 Min. A

    Disc # per Basket 250 Per Container 500 Per Container B

    Cycle Number 2 Cycles 4 Cycles C

    Cycle Temp 310 o F/10 Min 550 o F /10 Min D

    StdOrder RunOrder SR T Disc No Cycle No TC Tem

    4 1 1 1 -1 -1

    1 2 -1 -1 -1 -1

    5 3 -1 -1 1 1

    6 4 1 -1 1 -13 5 -1 1 -1 1

    7 6 -1 1 1 -1

    2 7 1 -1 -1 1

    8 8 1 1 1 1

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    Planned Tests

    Run No SR Temp Disc No PerB Cycle No. C- Temp

    1 550F/20 Min 250 2 310F/10 Min

    2 550F/20 Min 500 4 310F/10 Min

    3 550F/20 Min 250 4 550F/10 Min

    4 700F/20 Min 500 4 550F/10 Min

    5 700F/20 Min 250 2 550F/10 Min

    6 550F/20 Min 500 2 550F/10 Min

    7 700F/20 Min 250 4 310F/10 Min

    8 700F/20 Min 500 2 310F/10 Min

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    Test Results

    Run I Run II Run III Run IV

    TFD BFD TFD BFD TFD BFD TFD BFD

    Average 297.1 185.2 293.0 184.0 294.1 181.4 294.0 187.6

    Stdev 6.62 5.20 6.59 4.95 6.87 5.13 7.24 4.41

    Max 306.7 195.3 309.3 195.3 309.7 195.1 313.3 195.6

    Min 282.4 175.2 280.5 169.3 283.7 174.3 284.6 180.6

    Range 24.3 20.1 28.8 26.0 26.0 20.8 28.7 15.0

    RUN V RUN VI Run VII Run VIII

    TFD BFD TFD BFD TFD BFD TFD BFD

    Average 275.6 174.9 276.9 176.5 276.8 175.5 274.9 175.7

    Stdev 4.88 4.15 4.85 5.40 6.85 4.35 6.43 6.04

    Max 285.9 188.0 286.5 195.8 292.8 184.2 286.7 195.3

    Min 265.2 168.2 268.3 167.7 264.4 168.8 263.1 164.5

    Range 20.7 19.8 18.2 28.1 28.4 15.4 23.6 30.8

    30 pieces of samples were taken to do stat check

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    TFD Stdev

    Run No SR Disc No TC No TC Temp Stdev

    o F Pieces Cycles o F o F

    1 550 250 2 310 5.28

    2 550 250 4 550 5.483 550 500 2 550 5.12

    4 550 500 4 310 5.99

    5 700 250 2 550 3.58

    6 700 250 4 310 4.09

    7 700 500 2 310 4.81

    8 700 500 4 550 5.58

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    Main Effect on The Results

    MeanofResults

    1-1

    5.50

    5.25

    5.00

    4.75

    4.50

    1-1

    1-1

    5.50

    5.25

    5.00

    4.75

    4.50

    1-1

    SR T Disc No

    Cycle No T C T em

    Main Effects Plot (data means) for Results

    High Temp will resulting in a lower Standard Deviation

    Less number of discs in a container will result in a lower Stdev

    Less thermal cycles will result in a lower Stdev

    Thermal Cycles Temp will not be of large effect

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    Interaction

    SR T

    1-1 1-1 1-1

    6

    5

    4

    Disc No

    6

    5

    4

    Cycle No

    6

    5

    4

    TC Tem

    SR T

    -1

    1

    Di

    -1

    1

    Cycl

    -1

    1

    InteractionPlot (datameans) for Results

    When SR temp at high level, 250 disc discs in a container willresult in a lower standard deviation

    When 2 cyclic number was taken with the high ST temp, it will

    help to reduce the stdev

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    Analysis of Variance for Results (coded units)

    Source DF Seq SS Adj SS Adj MS F P

    Main Effects 4 3.7040 3.7040 0.9260 * *

    2-Way Interactions 3 0.8157 0.8157 0.2719 * *

    Residual Error 0 * * *

    Total 7 4.5197

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    Estimated Effects and Coefficients for Results

    (coded units)

    Term Effect Coef

    Constant 4.9913

    SR T -0.9525 -0.4763

    Disc No 0.7675 0.3837

    Cycle No 0.5875 0.2938

    TC Tem -0.1025 -0.0513

    SR T*Disc No 0.5925 0.2963

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    Effect of Factors

    Term

    Effect

    AC

    D

    AD

    C

    AB

    B

    A

    3.53.02.52.01.51.00.50.0

    3.306Factor

    TC Tem

    Name

    A S R T

    B Disc N o

    C C y cle N o

    D

    Pare to Chart of the Effects(response is Results, Alpha = .05)

    Lenth's PSE = 0.87825

    Thermal Cycle Temp (D) effect is small

    AC and AD effect are small either

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    Factorial Fit: Results versus SR T, Disc No,

    Cycle No

    After taking away the thermal temp factor:Estimated Effects and Coefficients for Results (coded units)

    Term Effect Coef SE Coef T P

    Constant 4.9913 0.07490 66.64 0.000SR T -0.9525 -0.4763 0.07490 -6.36 0.008

    Disc No 0.7675 0.3837 0.07490 5.12 0.014

    Cycle No 0.5875 0.2938 0.07490 3.92 0.029

    SR T*Disc No 0.5925 0.2962 0.07490 3.96 0.029

    S = 0.211847 R-Sq = 97.02% R-Sq(adj) = 93.05%

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    Main Effect Factors

    Term

    Standardized Effect

    C

    AB

    B

    A

    76543210

    3.182 Factor NameA SR T

    B Disc No

    C C ycle No

    Pareto Chart of the Standardized Effects(response is Results, Alpha = .05)

    The main factors of the A SR Temp, B - Disc Number per container,

    C Number of thermal cycles

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    Residuals

    Residual

    Percent

    0.40.20.0-0.2-0.4

    99

    90

    50

    10

    1

    Fitted Value

    Residual

    5.55.04.54.03.5

    0.2

    0.1

    0.0

    -0.1

    -0.2

    Residual

    F

    requency

    0.20.10.0-0.1-0.2

    1.00

    0.75

    0.50

    0.25

    0.00

    Observation Order

    Residual

    87654321

    0.2

    0.1

    0.0

    -0.1

    -0.2

    Normal Probability Plot of the Residuals Residuals Versus the Fitted Values

    Hist og ram o f t he R esid uals R esid uals Versus t he Ord er o f t he Dat a

    Residual Plots for Results

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    Analysis of Variance for Results (coded units)

    Source DF Seq SS Adj SS Adj MS F P

    Main Effects 3 3.6829 3.6829 1.22765 27.35 0.011

    2-Way Interactions 1 0.7021 0.7021 0.70211 15.64 0.029

    Residual Error 3 0.1346 0.1346 0.04488

    Total 7 4.5197

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    Effect Equation Obtained

    = 4.9913 0.476TSR+ 0.384NDisc + 0.2938NCycles +0.296TSRNDisc

    Optimized Process Conditions

    SR Temp (TSR) 700o F/ 20Min

    Number of Disc (NDisc) 250 Pieces Per Container Thermal Cycles (NCycles) 2 Cycles

    Thermal Cycle Temp 550 o F /20 Min

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    Confirmation Test & More Improvement

    Group I SR 700 F/20 Min, 250 pieces/PC ;2 Cycles/Air Cooling, 550 F/10 Min

    Group II SR 700 F/20 Min, 250 pieces/PC 2 SR ;

    2 Cycles/Air Cooling, 550 F/10 Min

    To See if 2 times of SR will improve the Sigma

    Group III SR 700 F/20Min, 250 Pieces/PC;

    4 Cycles, 310F/10 Min

    Sorting Oil heating and Cooling

    Group IV SR 700 F/20Min, 250 Pieces/PC-2 SR ;4 Cycles , 310F/10 Min

    Sorting Oil Heating and Cooling,

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    Confirmation Test Results

    Test 1 Test 2 Test 3 Test 4

    TFD BFD TFD BFD TFD BFD TFD BFD

    Averag

    e 274.30 174.17 271.45 174.07 270.94 173.08 271.27 174.85

    Stdev 4.03 3.81 3.59 2.89 2.43 2.78 3.92 4.03

    Max 280.30 178.50 282.60 180.10 277.60 177.30 282.70 189.90

    Min 263.30 164.40 264.60 169.60 265.90 166.10 263.70 166.80

    Range 17.00 14.10 18.00 10.50 11.70 11.20 19.00 23.10

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    Primary Metric

    Sigma vs. Date

    0

    1

    2

    3

    4

    5

    6

    7

    3/4/2005 4/3/2005 5/4/2005 6/3/2005 7/4/2005 8/4/2005 9/3/2005 10/4/2005 11/3/2005

    Date

    Sigma

    Projected

    Target

    Actual

    We are here W ~ 5 o F

    Objective ~ 4.2 o F on 7/20/05

    We have now reached: < 4 o F

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    Projected Parameters

    S No Projected W Average* U S Limit L S Limit Z Level-U Z Level-L PPM-U PPM-L PPM-T Yield

    o F o F o F o F %

    1 6.50 275.0 268.0 278.0 0.46 1.08 322206 140757 462964 53.70

    2 6.00 275.0 268.0 278.0 0.50 1.17 308538 121673 430210 56.98

    3 5.50 275.0 268.0 278.0 0.55 1.27 292720 101557 394278 60.57

    4 5.00 275.0 268.0 278.0 0.60 1.40 274253 80757 355010 64.50

    5 4.50 275.0 268.0 278.0 0.67 1.56 252492 59907 312399 68.76

    6 4.00 275.0 268.0 278.0 0.75 1.75 226627 40059 266686 73.33

    7 3.50 275.0 268.0 278.0 0.86 2.00 195683 22750 218433 78.16

    8 3.00 275.0 268.0 278.0 1.00 2.33 158655 9815 168471 83.15

    9 2.50 275.0 268.0 278.0 1.20 2.80 115070 2555 117625 88.24

    10 2.00 275.0 268.0 278.0 1.50 3.50 66807 233 67040 93.30

    11 1.50 275.0 268.0 278.0 2.00 4.67 22750 2 22752 97.72

    12 1.00 275.0 268.0 278.0 3.00 7.00 1350 0 1350 99.87

    13 0.50 275.0 268.0 278.0 6.00 14.00 0 0 0 100.00

    * Normal Centeris 273F, It is allowed theactualcentercontrol between272and275o F

    When < 4 o F,

    1st sorting Yield will be ~ 75%

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    Conclusions

    By Optimizing the Stability Conditions as below: SR 700 o F / 20 Min. 250 pieces/Per Condition

    2 Thermal Cycle with temp as 550 o F /10 Min.

    It is able to improve the performance:

    The first Sorting yield increased from 50 % to 75% The final yield will be more than 80%.

    This corresponds to an approx labor saving of 4000hrs.

    The 10% yield improvement corresponds to a costreduction of approx. $80,000 per year. ( 4 milliondiscs per year in production )

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    Future Works

    Effect of the blank number on the Forming Effect of Punch Spherical Radius on the

    Forming

    Second Phase ImprovementTarget: 10-15% improvement

    TFD Stdev Target should be < 1.75 o F

    Third Phase Improvement Long Run

    Maximum is about 19.9 % of improvement

    TFD Stdev Target should be < 1 o F