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CTG SIX SIGMA Final.pdf - Chemtool

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PURPOSE<br />

• The purpose of this presentation is to<br />

demonstrate the Six Sigma Techniques<br />

and capabilities of the <strong>Chemtool</strong>, Inc.<br />

Container Technology Group (<strong>CTG</strong>).<br />

• The presentation follows a typical<br />

aluminum can plant cupper lube trial. The<br />

trial material in this case is NuSol 177-M.<br />

• The tear-off rate during the trial improved<br />

from 0.147/10,000 to 0.128/10,000, a<br />

12.5% improvement.


Was the Tear-off Rate Improvement<br />

Statistically Significant?<br />

• Tear-off rate for seven (7) days<br />

preceding the trial – 0.147/10,000.<br />

• Tear-off rate for seven (7) day trial<br />

period – 0.128/10,000.<br />

Test and CI for Two Proportions (C1A vs. 177M)<br />

Sample X N Sample p<br />

C1A 758 52348754 0.0000147<br />

177M 648 50466446 0.0000128<br />

Difference = p (1) - p (2)<br />

Estimate for difference: 1.639595E-06<br />

95% lower bound for difference: 4.409649E-07<br />

Test for difference = 0 (vs > 0): Z = 2.25<br />

P-Value = 0.012<br />

Yes! The<br />

Improvement is<br />

Statistically<br />

Significant!


Plant Concerns with NuSol 177M<br />

• The following issues typically might be<br />

raised as negatives to NuSol use:<br />

• pH instability<br />

• Tramp oil instability (concentration variation)<br />

• Inconsistent cup lube weights<br />

• Variation in top wall concentricity<br />

These issues are addressed with “data driven”<br />

answers on the following pages.


DID NUSOL 177M IMPROVE COOLANT<br />

pH STABILITY AND CAPABILITY?<br />

• NuSol 177M makes up<br />

at a pH of ~8.6.<br />

• The coolant pH<br />

increased to ~ 9.0<br />

• Yes!<br />

Coolant pH<br />

was “more stable and<br />

capable” with NuSol<br />

177M vs. competitive<br />

material (C pk 0.80 vs.<br />

0.44)


% TRAMP OIL IN THE COOLANT<br />

CHANGED DURING THE TRIAL<br />

• The chart shows a<br />

decease in % tramp oil.<br />

• Simultaneously the %<br />

177M increased.<br />

• The total oil remained<br />

constant until a plant<br />

addition.<br />

• Anecdotally, the same<br />

phenomena occurs with<br />

the competition material<br />

(increased % cupper =<br />

decreased % tramp).


DID NUSOL 177M DESTABILIZE<br />

THE % TRAMP OIL?<br />

• <strong>Chemtool</strong> Crystal Lake<br />

lab analysis showed the<br />

% of gear oil and cupper<br />

lube were constant.<br />

• The in-use test method<br />

gave inaccurate results.<br />

• NO! % Tramp oil<br />

was not destabilized by<br />

NuSol 177M!<br />

• A more accurate test<br />

method was developed &<br />

rolled out to the<br />

customer.<br />

NuSol 177-M<br />

1.0<br />

0.5<br />

0.0<br />

% NuSol 177-M in Oil Split (BRIX)<br />

NuSol 177-M = 5.26558 - 0.0652284 Brix<br />

S = 0.0120906 R-Sq = 99.9 % R-Sq(adj) = 99.9 %<br />

65 70 75 80<br />

Brix


DID NUSOL 177M IMPACT CUP<br />

LUBE WEIGHT CONSISTENCY?<br />

Cupper One Comparison<br />

Lube<br />

177M<br />

X<br />

Mean<br />

15.631<br />

13.714<br />

S.D.<br />

3.488<br />

4.261<br />

Min.<br />

6<br />

-12<br />

Cupper Two Comparison<br />

Lube<br />

177M<br />

X<br />

Mean<br />

16.167<br />

15<br />

S.D.<br />

2.924<br />

3.383<br />

Min.<br />

8<br />

8<br />

Max.<br />

26<br />

20<br />

Max.<br />

27<br />

27<br />

Range<br />

20<br />

32<br />

Range<br />

19<br />

19<br />

• No! Cup Lube<br />

weights were MORE<br />

consistent during the<br />

trial (lower S.D.), but<br />

the competitor<br />

inconsistency was<br />

likelydue to mechanical<br />

issues identified bt<br />

<strong>Chemtool</strong>.<br />

• Defective solenoids on<br />

both application units.<br />

(Replaced).<br />

• Lube supply not<br />

touching bottom of coil<br />

on cupper one<br />

(Repaired).


WHAT IMPACT TOP WALL CONCENTRICITY<br />

DID NUSOL 177M HAVE?<br />

CONCENTRICITY DATA SUMMARY<br />

Variable<br />

Mean<br />

TrMean<br />

StDev<br />

Minimum<br />

Maximum<br />

Range<br />

Other<br />

0.006046<br />

0.006045<br />

0.000111<br />

0.0056<br />

0.00646<br />

0.00086<br />

177M<br />

0.006053<br />

0.006053<br />

0.000109<br />

0.00567<br />

0.00644<br />

0.00077<br />

None! The<br />

concentricity results are<br />

“Statistically Similar.”


CUP MAT CONVEYOR ISSUES<br />

• DATA IMPUT<br />

• Unusually, the cupper conveyor system with more<br />

mechanical issues had fewer tear-offs<br />

• Six Sigma correlation made with “line stops” and<br />

tear-off rates (p-value)<br />

• <strong>SIX</strong> <strong>SIGMA</strong> CORRELATION INVESTGATION<br />

• CUP conveyor run on line stops<br />

• Cups are rubbed “dry”<br />

• Cups are dumped after one (1) hour stops<br />

• Explanation of why the cupper with less line stops<br />

has lower tear-off rates (lube loss)<br />

• PROPOSED CORRECTIVE ACTION<br />

• Cup conveyor “auto-stop” with line back-up (No lube<br />

loss)


CONCLUSIONS<br />

• ADDITIONAL ISSUES IDENTIFIED<br />

• Metal trial<br />

• Cup Conveyor<br />

• Cup lube application failure<br />

• <strong>SIX</strong> <strong>SIGMA</strong> DATA ANSWERS<br />

• Improved or equal performance in cup lube<br />

weights, coolant pH, % coolant tramp oil,<br />

and top wall concentricity!<br />

• Statistically Significant 12.5%<br />

IMPROVEMENT in Tear-off rate in spite<br />

of mechanical and metal issues!


QUOTATIONS<br />

• “The goal is to transform data<br />

into information, and information<br />

into insight.” Carly Fiona<br />

• “As Luce reminded me, he said,<br />

without data, , without facts, the<br />

discussion….is just another<br />

opinion.”<br />

• “When you cannot measure,<br />

when you cannot express in<br />

numbers, your knowledge is of a<br />

meager and unsatisfactory kind:<br />

(Lord Kelvin)

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