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Statistics for Materials Engineers

MATLS 3J03

© KevinDunn,2013

Instructor: Tim Dietrich

Overall revision number: 19 (January 2013)

(2)

Design resolution

What is “Resolution” ?

The length of the shortest word in the defining relation.

I 27−4 example: shortest word = 3 letters: 27III−4 design

I main effects confounded with 2-factor interactions

I 28−5 example: shortest word = 4 letter: 28−5 IV design

I main effects confounded with 3-factor interactions

I 25−1 half-fraction design

I four factors as standard factorial

I factorE = ABCD, soI = ABCDE

I it is a 25V−1design

(3)

Design resolution

Resolution: shows how clearly effects are separated

I Let main effects = 1

I Two-factor interactions = 2

I Three-factor interactions = 3

Resolution V designs

I 5−1 = 4: main effects confounded with 4-factor interactions

I 5−2 = 3: 2-fi confounded with 3-fi

I 5−3 = 2: 3-fi confounded with 2-fi

Aim for a higher resolution, but accept a lower resolution initially, in order to test more factors

(4)

Design resolution

Resolution III designs

I Used for: Excellent for initial screening

I Type of confounding?

Resolution IV designs

I Used for: Learning about and understanding a system (characterization)

I Type of confounding?

Resolution V designs and full factorial designs

I Used for: Optimizing a process, understanding complex effects

I To develop high-accuracy models

(5)

Design resolution

(6)

Saturated designs - screening

I Resolution III design

I Screen many factors

I Good for evaluating a new system

I Lab-scale work

I New product development

I Transfer from the lab to plant scale

(7)

Saturated design example

1. Create X andy matrices from the table

2. Solve forb

3. Plot Pareto plot of main effects (they are highly confounded)

4. Usual assumption: high order interactions are small

(8)

Saturated design example

I A,CandG are significant

I E: fairly small

I βbE→E + AC + BG + DF

I could be due to main effectE I or due toAC, and/orBGand/or

DFinteractions

I FactorsB,D andFare not important

I If we remove them, we are left with 4 factors, in 8 runs

I This automatically becomes a

resolution IV design

I The coefficients for other terms will not change(Why?)

Next experiments: focus onA,C,G and their interactions. Maybe keepE, but it is small enough that it is likely negligible.

(9)

Saturated designs: note

I Fraction factorials: 2k−p runs

I for integersk andp: 4,8,16,32,64,128, . . . I Plackett and Burman designs are for screening also:

I multiples of 4: 12,16,20,24,28, . . .runs

I Box and Bisgaard paper: “What can you find out from 12 experimental runs?”

(10)

Foldover: de-aliasing

I Experiments are not a one-shot operation; always run sequential experiments

I How should we work with fractional factorials?

I highly confounded; but say one factor Cis important

I switch the sign ofC: fromCto−C

I Also switch the signs of the terms that depend on it:

I e.g. ifD = ABC,

I then: D=AB(−C) =−ABC

I repeat the fractional set of experiments

I combine the results of both fractions: theXandy will have

double the number of rows

I it unconfoundsC: this main effect will be estimated on its own, and have no confounding associated with it

Switching the sign of a factor will de-alias its main effect and all its associated two-factor interactions.

(11)

Foldover: removing 2-fi confounding

I Run another fraction, but switch all the signs in the design table

I i.e. letA=−A, letB=−B, etc

I Also switch the signs of the terms that are generated from it (see previous slide)

I Run another fractional factorial

I Combine both sets of experiments

I All 2-fi will be removed from the main effects; will still be confounded with higher order interactions

(12)

Projectivity

Fractional factorials collapse to full factorials when effects are insignificant.

Projectivity= P = resolution - 1 = highest number of factors which can form a full factorial, that are embedded in your fractionated set of experiments.

(13)

Example (previous exam/test)

You are developing a new product, but struggling to get product stability (measured in days), to the required level. Aim for stability above 50 days. Four factors considered:

I A = monomer concentration: 30% or 50% I B = acid concentration: low or high

I C= catalyst level: 2% or 3% I D = temperature: 393K or 423K Experiments in standard order:

(14)

Example (continued)

1. How was the experimented generated?

2. What is the defining relationship?

3. What will be aliased withA; with D and withBC?

4. Describe the aliasing structure (resolution)?

5. What is the model’s intercept; main effect for A; and for the AD interaction?

(15)

Example (continued)

If the least squares model is:

y= 29.5−5.75xA−3.75xB −1.25xC + 0.75xD+ 0.50xAxB + 1.0xAxC −1.0xAxD

what is the predicted stability when operating at:

I monomer concentration of 25%

I low acid concentration

I 1.5% catalyst level

I a temperature of 408 K

(16)

Response surface methods

Objective for theresponse surface method (RSM): achieve the best response using sequential experimentation.

Wasn’t the COST approach also sequential experimentation?

Different to COST: We are going to change multiple variables at a time!

(17)

George E. P. Box: he pioneered RSM

G. E. P. Box and K. B. Wilson (1951): “On the Experimental Attainment of Optimum Conditions”,Journal of the Royal Statististical Society.B 13, 1 - 45.

[Photo credit: JMP/SAS]

I October 1919 to 28 March 2013

I “... essentially, all models are

wrong, but some are useful”

(18)

Single-variable case

We could have got to optimum faster if we had used quadratic (or spline) approximations.

(19)

Single-variable case

This coincides with the COST approach:

I take exploratory steps of γi towards an optimum

I refit the model once we plateau

I repeat

We are going to do exactly the same, but withmultiple variables. Key points:

1. use the model to optimize with

2. stop once you detect the “model” is inadequate

3. the rebuild/refit it

(20)

Analogy for finding the optimum

(21)

Motivation: an example from reactor design

I Reactor inlet temperature,T, and pressure, P can be adjusted I Leads to different responses,y = methanol yield, for different

combinations of T andP

I What if we did not have a reliable “first-principles” model?

(22)

2-variable example

I Current baseline:

I T = 325 K

I S = 0.75 g.L−1

I profit =$407 per day

I Example worked out on the board

(23)

2-variable example

Questions:

I how “wide” should the initial factorial be?

I should it be a fractional or full factorial?

I how do you deal with more than 2 variables?

I how do you deal with integer variables?

I how large should steps be?

Both experiment 6 and 7 were wasteful.

(24)

2-variable example

(25)

2-variable example

(26)

2-variable example

Adding second order effects; use a central composite design.

I CCD design: full factorial + axial points + center points

(27)

2-variable example

Add quadratic terms to model: ˆ

y=b0+bTxT +bSxS +bTSxTxS +bTTxT2 +bSSxS2

y = Xb+e

              y8 y9 y10 y11 y6 y13 y14 y15 y16               =              

1 −1 −1 +1 +1 +1 1 +1 −1 −1 +1 +1 1 −1 +1 −1 +1 +1 1 +1 +1 +1 +1 +1

1 0 0 0 0 0

1 0 −1.41 0 0 2 1 1.41 0 0 2 0 1 0 1.41 0 0 2 1 −1.41 0 0 2 0

(28)

2-variable example

I The next experiment is based on the contour plot output, i.e.

I T(17)≈343 K

I S(17)≈1.60 g.L−1

I yˆ(17)= $736

I yactual(17) = $738

(29)

General approach for RSM

1. Start at baseline; run full or fractional factorial

I yˆ=b0+bAxA+bBxB+. . .+bABxAxB+bACxAxC+. . .

2. Main effects usually greater than 2-factor interaction 3. Estimate path of steepest ascent (or descent):

I ∂yˆ

∂xA

=bA

∂yˆ

∂xB

=bB

∂yˆ

∂xC

=bC . . .

I Move bA units inxA;and bB units inxB;andbC units inxC

etc

I These are coded units. Unscale to real-world units!

I Implement a portion of the full step, e.g. only 25% if full step is too large.

4. Make several sequential steps until response levels off

I e.g. y6= 600;y7 = 800,y8 = 825,y9 = 750

(30)

General approach for RSM

5. Use a new factorial at the previous peak (e.g. at they8 point)

I perhaps add other factors

I flip signs on binary factors

6. Repeat steps 1 to 5, until linear model is insufficient

I Curvature shows up

I 2-factor interactions similar or greater than main effects

I Contour plots will show this clearly

7. Estimate (calculate) a quadratic model

I Use a central composite design; uses 3-levels per factor

I Add quadratic terms to model, e.g. . . .+bAAxA2+bBBxB2+. . .

8. Draw contour plots (surfaces) and move to next optimum

(31)

What is the response variable

I Single y is not always feasible

I Use y = “total costs”, or y = “net profit”

I Superimpose contour surfaces

Page 579 of the Hill and Hunter review article - reference in the notes.

(32)

Evolutionary operation (EVOP)

I Similar concept to RSM

I Processes are not constant, the optimum is shifting

I heat-exchanger fouling

I build-up inside reactors and tubing

I catalyst deactivation

I slowly varying disturbances

I Iterative hunt for the process optimum:

I make small perturbations within daily production

I use replicate runs and average

I move along the response surface

(33)

General approach for experimentation

I Box: “The best time to run an experiment is after the experiment”

I Box: “To find out what happens when you interfere with a system, you must interfere with it, not passively observe it.”

I Box: “Discovering the unexpected is more important than confirming the known”

I Box: “Do not spend more than 20% to 25% of your time and budget on your first group of experiments”

Phase 1: screening runs

Phase 2: sequential experiments to augment screening Phase 3: optimizing; RSM and full factorials

Phase 4: maintain the optimum, search for better optima

(34)

Mistakes, missing values, and constraints

I If you do not, or cannot, reach −1 or +1:

I Use a least squares model, with the coded values actually used in the experiment. E.g.:

I −1 corresponds to 425K, and +1 corresponds to 475K

I experiment ran at 455K, instead of 475K

I then use 455−450

(475−425)/2= 0.2 in theXmatrix

I (see the next slide)

I You lose some orthogonality in theXmatrix

I Missing values

I main effects estimate multiple times (so we have built-in redundancy already)

I drop out insignificant terms, e.g. a 2-fi, and estimate fewer parameters

(35)

Handling of constraints

I New runs are not independent; lost orthogonality

(36)

Optimal designs

I What is sub-optimal about our existing designs? Nothing!

I Use optimal designs when:

I constraints are complex (plane constraints;k ≥3)

I estimating a non-standard model

I running a reduced number of experiments

I have more than 2-levels per factor

I want to add experiments to existing runs

(37)

Optimal designs

Computer-based approach:

1. User specifies the model (i.e. the parameters)

2. Computer finds all possible combinations (grid approach)

I user can augment this list, called candidate points

I center-points added

3. User specifies number of experiments

4. Computer iteratively selects the “optimal” set Optimality criteria:

I A-optimal: minimizes trace

(XTX)−1

I D-optimal: maximizes det(XTX)

I G-optimal: minimize maximum variance of ˆy

I V-optimal: minimize average variance of ˆy

(38)

Optimal designs

I A full factorial design, 2k is already A-, D- G- and V-optimal.

I D-optimal designs work well; used most often.

(39)

Mixture designs

I Fine chemicals, pharmaceuticals, food manufacturing, and polymer processing

I There are screening and optimization designs for mixtures also

I Constraint for mixtures: P

ixi = 1 I Cannot be changed independently

References

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