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Design of Experiment
methodology
ANOVA、FFD、CCD、Mixture Design
Response surface design
Kung, Chun-Hao
kch800721@gmail.com
Chemical engineering
department in NCKU
Central composite design
methods(CCD)
Mixture design
methods
Know
situation
Design of
experiment
Optimized
process
Flow chart
Response surface design
• Help you better understand and optimize your
response.
• Used to refine models after you have determined
important factors using factorial designs
Advantages of Response surface design
Factorial Points : Estimated main factor & interaction
Axial Points : Estimated pure quadratic form
Center Points : Estimated pure Error
→ Building a quadratic response surface
→ Resolves both main effects and interactions
Central composite design (CCD)
Common use
Level Temperature (℃) Annealing time (mins)
𝟐 120 5.0
1 115 6.5
0 100 10.0
-1 85 13.5
- 𝟐 80 15.0
8
Run Temp. Time Temp. Time
1 -1 -1 85 13.5
2 -1 1 85 6.5
3 1 -1 115 13.5
4 1 1 115 6.5
5 0 0 100 10
6 0 0 100 10
7 0 0 100 10
8 0 - 𝟐 100 15
9 0 𝟐 100 5
10 - 𝟐 0 80 10
11 𝟐 0 120 10
Design matrix
Reference: Michael Grätzel, Advanced Functional Materials, 24, 3250(2014)
Effect of Annealing Temperature on Film Morphology of Organic–Inorganic
Hybrid Pervoskite Solid-State Solar Cells
120℃
5 mins
15 mins
8𝟎℃
100℃
− 2: 100 − 115 − 100 × 1.414 =80
2: 100 + 115 − 100 × 1.414 = 120
run Temp. Time Voc (V) Jsc (mA/cm2) FF PCE (%)
1 80 10 0.77 7.07 0.72 3.89
2 85 13.5 0.72 10.30 0.59 4.44
3 85 6.5 0.25 12.98 0.37 1.23
4 100 15 0.78 13.86 0.72 7.77
5 100 10 0.78 11.99 0.73 6.78
6 100 5 0.81 6.63 0.73 3.92
7 115 13.5 0.71 12.80 0.66 5.99
8 115 6.5 0.72 13.18 0.71 6.72
9 120 10 0.71 11.42 0.68 5.50
Origin data-CCD
SAS-ANOVA
Source:11
DF: 10
變異數分析
來源 DF 和平方 平均值平方 F 值 Pr > F
模型 5 31.3531
0
6.27062 6.47 0.0306
誤差 5 4.84396 0.96879
已校正的
總計
10 36.1970
5
根 MSE 0.98427 R 平方 0.8662
應變平均值 5.43636 調整 R 平方 0.7324
變異係數 18.10534
Set regression equation
(model y1=x1 x2 t1 t2 t3 /noint selection=forward;)Commands :
proc : procedure
reg : regression
anova : calculate ANOVA
Y = a + bX1+c x2 + dx1
2+ ex2
2+ fx1x2
Parameters:11
參數估計值
變數 DF 參數
估計
標準
誤差
t 值 Pr > |t|
Intercept 1 6.78014 0.56827 11.93 <.0001
x1 1 1.16474 0.34802 3.35 0.0204
x2 1 -0.99064 0.34802 -2.85 0.0360
t1 1 -1.21157 0.41428 -2.92 0.0328
t2 1 -0.63640 0.41428 -1.54 0.1851
t3 1 0.98500 0.49214 2.00 0.1017
z=6.78+1.16*x-0.99*y-1.21*x2-0.63*y2+0.98.*x*y
Regression of PCE (%)
[x,y] = meshgrid(-2:0.01:2);
z=6.78014+(1.16474.*x)-(0.99064.*y)-(1.21157.*(x.^2))-(0.63640.*(y.^2))+(0.98500.*x.*y);
[C,h] = contour(x,y,z, [1,2,3,4,5,5.5,6,6.5,7,7.2]);
axis([-1.5,1.5,-1.5,1.5])
clabel(C,h);
1
1
2
2
3
3
4
4
4
4
5
5
5
5
5.5
5.5
5.5
5.5 5.5
5.5
6
6
6
6
6
6
6.5
6.5
6.5
6.5
6.5
7
7
7
7
7.2
Temperatuer(degree)
Annealingtime(mins)
85 100 115
6.5
10
13.5
-1.5 -1 -0.5 0 0.5 1 1.5
-1.5
-1
-0.5
0
0.5
1
1.5
12
Parameter Coefficient
Xtemp
1.16
Ytime
-0.99
XtempXtemp
-1.21
YtimeYtime
-0.63
XtempYtime
0.99
Main factor:
Interaction: Temp.-Time
90℃ 110℃
z=6.78+1.16*x-0.99*y-1.21*x2-0.63*y2+0.98.*x*y
>
Regression of PCE (%)
Mixture design method
Cl
BrI
14
 Model is fixed
 Algebra equation
 Time-consuming
 Model reduction
 SAS regression
 Interaction effect
 Save time
0.00 0.25 0.50 0.75 1.00
0.00
0.25
0.50
0.75
1.00
0.00
0.25
0.50
0.75
1.00
IBr
Cl
Binary Design (A) Ternary Design (B)
Modified mixture design methods
Advantages of mixture design
• Designs for these experiments are useful
because many product design and development
activities in industrial situations involve
formulations or mixtures.
Statics and regression
examples
16
17
Mixture design methodology
RegressionExperimental data Contour plot1. 2. 3.
SAS 9.3 MATLAB R2013a
0.00 0.25 0.50 0.75 1.00
0.00
0.25
0.50
0.75
1.00
0.00
0.25
0.50
0.75
1.00
IBr
Cl
Origin data
Ratio MACl MABr MAI Voc(V) Jsc (mA/cm2
) FF (%) PCE (%)
1 1 0 0 0.76 10.31 69% 5.42
2 0 1 0 0.97 5.54 71% 3.81
3 0 0 1 0.78 9.76 70% 5.38
4 0.33 0.333 0.333 0.86 11.54 66% 6.54
5 0.5 0.5 0 0.97 4.76 70% 3.23
6 0 0.5 0.5 0.92 5.97 66% 3.58
7 0.5 0 0.5 0.71 12.10 72% 6.12
8 0.67 0.17 0.17 0.73 12.37 71% 6.38
9 0.17 0.67 0.17 0.97 10.66 64% 6.54
10 0.17 0.17 0.67 0.85 11.46 77% 7.51
11 0.75 0.25 0 0.90 7.43 64% 4.32
12 0.25 0.75 0 0.96 7.68 57% 4.15
13 0.25 0 0.75 0.78 13.06 68% 6.89
14 0.75 0 0.25 0.80 9.93 72% 5.68
15 0 0.75 0.25 0.99 10.81 72% 7.71
16 0 0.25 0.75 0.82 10.05 73% 6.01
Forward selection
SAS Regression
run;
proc reg;
model y1=t1 t2 t3 t4 t5 t6 t7 t8 t9 t10 t11 t12 t13
/noint selection=forward;
proc anova;
前進選擇: 步驟 1 R 平方 = 0.6006 和 C(p) = 57.8286
前進選擇: 步驟 2 R 平方 = 0.8367 和 C(p) = 17.3612
前進選擇: 步驟 7 R 平方 = 0.9792 和 C(p) = 1.7387
Click run
Model reduction
Parameter Coefficient
X1 t1
X2 t2
X3 t3
X1X2 t4
X1X3 t5
X2X3 t6
X1X2X3 t7
X1X2(X1-X2) t8
X1X3(X1-X3) t9
X2X3(X2-X3) t10
X1X1X2X3 t11
X1X2X2X3 t12
X1X2X3X3 t13
SAS Regression-13 parameters
變異數分析
來源 DF R
2
平均值平方 F 值 Pr > F
模型 6 515.7 85.9 73.60 <.0001
誤差 10 11.8 1.2
未校正的總計 16 527.4
變
數
參數
估計
標準
誤差
第二型 SS F 值 Pr > F
t1 5.57799 0.77588 60.35377 51.69 <.0001
t2 4.53861 0.83794 34.25800 29.34 0.0003
t3 6.53751 0.73561 92.22951 78.98 <.0001
t4 -5.83005 4.15712 2.29666 1.97 0.1911
t7 64.07944 25.58609 7.32434 6.27 0.0312
t10 11.75880 7.90392 2.58452 2.21 0.1677
R 平方 = 0.9779 和 C(p) = -0.0183
Parameter Coefficient
X1 t1
X2 t2
X3 t3
X1X2 t4
X1X3 t5
X2X3 t6
X1X2X3 t7
X1X1X2X3 t11
X1X2X2X3 t12
X1X2X3X3 t13
SAS Regression-10 parameters
變異數分析
來源 DF 和
平方
平均值
平方
F 值 Pr > F
模型 6 513.8 85.6 63.28 <.0001
誤差 10 13.53 1.35
未校正的總計 16 527.4
變
數
參數
估計
標準
誤差
第二型 SS F 值 Pr > F
t1 5.26373 1.01318 36.52686 26.99 0.0004
t2 5.09614 0.83751 50.10738 37.03 0.0001
t3 5.81178 0.83751 65.16845 48.15 <.0001
t4 -6.08694 4.54785 2.42432 1.79 0.2104
t5 3.33659 4.54785 0.72845 0.54 0.4800
t7 59.03570 29.04160 5.59231 4.13 0.0695
R 平方 = 0.9743 和 C(p) = 2.7857
0
0.25
0.5
0.75
1 0
0.25
0.5
0.75
1
Cl
Br I
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
7.4
7.2
7
6.5
6
5
6 6.5
7
5
6.5
6
0
0.25
0.5
0.75
1 0
0.25
0.5
0.75
1
Cl
Br I
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
R 平方 = 0.9779 和 C(p) = -0.0183 R 平方 = 0.9743 和 C(p) = 2.7857
Different parameters compared
13 parameters 10 parameters
Contour plot- e.g. PCE
A=tril(meshgrid(0:0.001:1));
B=tril(meshgrid(1:-0.001:0)');
C=tril(1-A-B);
x=tril(0.5.*(1+C-B));
y=tril((3^0.5)*0.5.*A);
z=5.57799.*A +4.53861.*B+6.53751.*C -5.83005.*A.*B
+64.07944.*A.*B.*C+11.75880.*B.*C.*(B-C);
[C,h] = contourf(x,y,z,
[1,2,3,4,5,6,6.5,7,7.2,7.4,7.6],'LineWidth',1);
axis([0,1,0,1]);
clabel(C,h,'manual','fontsize',15);
hold on
plot([0.375,0.625],[0.6495,0.6495],'k:');
hold on
plot([0.25,0.75],[0.433,0.433],'k:');
hold on
plot([0.375,0.75],[0.6495,0],'k:');
hold on
plot([0.25,0.5],[0.433,0],'k:');
hold on
plot([0.125,0.25],[0.2165,0],'k:');
hold on
plot([0.125,0.875],[0.2165,0.2165],'k:');
hold on
plot([0.25,0.625],[0,0.6495],'k:');
hold on
plot([0.50,0.75],[0,0.433],'k:');
hold on
plot([0.75,0.875],[0,0.2165],'k:');
先建立矩
陣數列,
從0~1,
間格0.001
利用SAS迴歸得到的Eq.
A=tril(meshgrid(0:0.001:1)) B=tril(meshgrid(1:-0.001:0)');
x=tril(0.5.*(1+C-B)); y=tril((3^0.5)*0.5.*A);
C=tril(1-A-B);
z=5.58.*A +4.54.*B+6.54.*C -
5.83.*A.*B+64.08.*A.*B.*C+11.76.*B.*C.
*(B-C);
e.g. 0.5*(1+0.001-0.998) e.g. 3*0.5*0.001
Function
0
0.25
0.5
0.75
1 0
0.25
0.5
0.75
1
Cl
Br I
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
Contour plot- e.g. PCE
[C,h] = contourf(x,y,z, [1,2,3,4,5,6,6.5,7,7.2,7.4,7.6],'LineWidth',1);
axis([0,1,0,1]);
7
8
10
9
11
12
12.5
12.7
12
11
10
8
11
10
0
0.25
0.5
0.75
1 0
0.25
0.5
0.75
1
Cl
Br I
0 0.2 0.4 0.6 0.8 1
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
5
6
7
8
9
10
11
12
1
0.98
0.94
0.9
0.85
0.8
0.75
0.85
0.8
0
0.25
0.5
0.75
1 0
0.25
0.5
0.75
1
Cl
Br I
0 0.2 0.4 0.6 0.8 1
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0.7
0.75
0.8
0.85
0.9
0.95
1
0.6
0.65
0.68
0.7
0.75
0.8
0.850.9
0.55
0.7
0.7
0
0.25
0.5
0.75
1 0
0.25
0.5
0.75
1
Cl
Br I
0 0.2 0.4 0.6 0.8 1
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
0.55
0.6
0.65
0.7
0.75
0.8
0.85
0.6
0.6
0.65
0.65
0.68
0.68
0.7
0.75
0.8
0.85
0.9
0.75
0.7
0.55
0
0.25
0.5
0.75
1 0
0.25
0.5
0.75
1
IBr
Cl
5
6
6.5
7
7.2
7.2
7
6.5
6
5
6
6.5
0 0.2 0.4 0.6 0.8 1
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
1
1
2
3
4
5
6
7
JscVoc FF PCE
PCE=5.6*A +4.5*B+6.5*C -5.8*A*B+64.1*A*B*C+11.8*B*C*(B-C);
SAS Regression
Jsc=9.44 X1+6.58 X2+10.75 X3-6.69 X1X2+8.07 X1X3+91.79 X1X2X3+17.10X2X3(X2-X3)
Voc=0.76 X1+0.97 X2+0.77 X3+0.38 X1X2+0.20 X2X3+101.67X1X2X3+0.23X1X2(X1-X2)+0.38
X2X3(X2-X3)-112.78 X12X2X3-99.91 X1X2
2X3-95.62 X1X2X3
2
FF=0.70 X1+0.70 X2+0.71 X3-0.26 X1X2+0.36 X1X2(X1-X2)-3.92 X1X2
2X3+4.90X1X2X3
2
1
2
3
3
4
4
5
5
5
5
6
6
6
6
6
6.5
6.5
6.5
6.5
6.5
7
7
7
7.2
7.2
0
0.25
0.5
0.75
0
0.25
0.5
0.75
1
I
0 0.25 0.5 0.75 1
27
0.0 0.2 0.4 0.6 0.8 1.0
-16
-14
-12
-10
-8
-6
-4
-2
0
MAPbCl0.30
Br0.15
I0.55
MAPbCl0.30
Br0.35
I0.30
MAPbCl0.30
Br0.55
I0.15
Currentdensity(mA/cm
2
)
Voltage (V)
PCE Contour plot
run Cl Br I Voc Jsc FF PCE
0.30 0.55 0.15 0.97 9.94 0.70 6.77
0.30 0.35 0.35 0.92 14.07 0.73 9.47
0.30 0.15 0.55 0.75 12.67 0.68 6.52
Cl
IBr
Verification by J-V curve
FFD
(Full Factorial Design )
28
Factors and levels for the 23 Full Factorial Design
factors
levels
+ -
A, P3HT:PCBM concentration
(wt%)
2.5 1.5
B, rpm 600 1000
C, time (s) 60 40
Full Factorial Design
1.5wt% 600rpm 40s 600rpm 60s 1000rpm 40s 1000rpm 60s
VOC (V) 0.04 0.60 0.70 0.72
JSC (mA/cm2
) 2.94 7.22 1.21 1.03
FF 0.29 0.32 0.32 0.30
PCE (%) 0.03 2.83 0.27 0.22
R.P (Ω・cm2
)104
0.00083 278.8 71.68 99.72
R.S (Ω・cm2
) 1.88 2.23 7.36 1.15
Run A B C Voc (V) Jsc (mA/cm2) FF PCE (%)
1 - + - 0.04 2.94 0.29 0.03
2 - + + 0.60 7.22 0.65 2.83
3 - - - 0.70 1.21 0.32 0.27
4 - - + 0.72 1.03 0.30 0.22
factors + -
A, concentration (wt%) 2.5 1.5
B, revolution (rpm) 600 1000
C , time (s) 60 40
2.5wt% 600rpm 40s 600rpm 60s 1000rpm 40s 1000rpm 60s
VOC (V) 0.60 0.58 0.60 0.70
JSC (mA/cm2
) 7.54 9.11 9.40 1.90
FF 0.54 0.60 0.63 0.40
PCE (%) 2.46 3.18 3.53 0.53
R.P (Ω・cm2
)104
0.88 40.91 143.42 168.52
R.S (Ω・cm2
) 2.05 2.80 2.27 7.39
5 + + - 0.60 7.54 0.54 2.46
6 + + + 0.58 9.11 0.60 3.18
7 + - - 0.60 9.40 0.63 3.53
8 + - + 0.70 1.90 0.40 0.53
factors + -
A, concentration (wt%) 2.5 1.5
B, revolution (rpm) 600 1000
C , time (s) 60 40
Run A B C Voc (V) Jsc (mA/cm2) FF PCE (%)
1 - + - 0.04 2.94 0.29 0.03
2 - + + 0.60 7.22 0.65 2.83
3 - - - 0.70 1.21 0.32 0.27
4 - - + 0.72 1.03 0.30 0.22
5 + + - 0.60 7.54 0.54 2.46
6 + + + 0.58 9.11 0.60 3.18
7 + - - 0.60 9.40 0.63 3.53
8 + - + 0.70 1.90 0.40 0.53
factors + -
A, concentration (wt%) 2.5 1.5
B, revolution (rpm) 600 1000
C , time (s) 60 40
Design matrix
Run A B C AB BC AC ABC PCE
1 - + - - - + + 0.03
2 - + + - + - - 2.83
3 - - - + + + - 0.27
4 - - + + - - + 0.22
5 + + - + - - - 2.46
6 + + + + + + + 3.18
7 + - - - + - + 3.53
8 + - + - - + - 0.53
effect estimate
A 1.59
B 0.99
C 0.12
AB -0.20
BC 1.64
AC -1.26
ABC 0.22
The estimate of A =
(
𝟐.𝟒𝟔+𝟑.𝟏𝟖+𝟑.𝟓𝟑+𝟎.𝟓𝟑
𝟒
) - (
𝟎.𝟎𝟑+𝟐.𝟖𝟑+𝟎.𝟐𝟕+𝟎.𝟐𝟐
𝟒
) = 1.59
Calculate the estimate

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Design of experiment methodology

  • 1. Design of Experiment methodology ANOVA、FFD、CCD、Mixture Design Response surface design Kung, Chun-Hao kch800721@gmail.com Chemical engineering department in NCKU
  • 5. • Help you better understand and optimize your response. • Used to refine models after you have determined important factors using factorial designs Advantages of Response surface design
  • 6. Factorial Points : Estimated main factor & interaction Axial Points : Estimated pure quadratic form Center Points : Estimated pure Error → Building a quadratic response surface → Resolves both main effects and interactions Central composite design (CCD)
  • 8. Level Temperature (℃) Annealing time (mins) 𝟐 120 5.0 1 115 6.5 0 100 10.0 -1 85 13.5 - 𝟐 80 15.0 8 Run Temp. Time Temp. Time 1 -1 -1 85 13.5 2 -1 1 85 6.5 3 1 -1 115 13.5 4 1 1 115 6.5 5 0 0 100 10 6 0 0 100 10 7 0 0 100 10 8 0 - 𝟐 100 15 9 0 𝟐 100 5 10 - 𝟐 0 80 10 11 𝟐 0 120 10 Design matrix Reference: Michael Grätzel, Advanced Functional Materials, 24, 3250(2014) Effect of Annealing Temperature on Film Morphology of Organic–Inorganic Hybrid Pervoskite Solid-State Solar Cells 120℃ 5 mins 15 mins 8𝟎℃ 100℃ − 2: 100 − 115 − 100 × 1.414 =80 2: 100 + 115 − 100 × 1.414 = 120
  • 9. run Temp. Time Voc (V) Jsc (mA/cm2) FF PCE (%) 1 80 10 0.77 7.07 0.72 3.89 2 85 13.5 0.72 10.30 0.59 4.44 3 85 6.5 0.25 12.98 0.37 1.23 4 100 15 0.78 13.86 0.72 7.77 5 100 10 0.78 11.99 0.73 6.78 6 100 5 0.81 6.63 0.73 3.92 7 115 13.5 0.71 12.80 0.66 5.99 8 115 6.5 0.72 13.18 0.71 6.72 9 120 10 0.71 11.42 0.68 5.50 Origin data-CCD
  • 10. SAS-ANOVA Source:11 DF: 10 變異數分析 來源 DF 和平方 平均值平方 F 值 Pr > F 模型 5 31.3531 0 6.27062 6.47 0.0306 誤差 5 4.84396 0.96879 已校正的 總計 10 36.1970 5 根 MSE 0.98427 R 平方 0.8662 應變平均值 5.43636 調整 R 平方 0.7324 變異係數 18.10534 Set regression equation (model y1=x1 x2 t1 t2 t3 /noint selection=forward;)Commands : proc : procedure reg : regression anova : calculate ANOVA Y = a + bX1+c x2 + dx1 2+ ex2 2+ fx1x2 Parameters:11
  • 11. 參數估計值 變數 DF 參數 估計 標準 誤差 t 值 Pr > |t| Intercept 1 6.78014 0.56827 11.93 <.0001 x1 1 1.16474 0.34802 3.35 0.0204 x2 1 -0.99064 0.34802 -2.85 0.0360 t1 1 -1.21157 0.41428 -2.92 0.0328 t2 1 -0.63640 0.41428 -1.54 0.1851 t3 1 0.98500 0.49214 2.00 0.1017 z=6.78+1.16*x-0.99*y-1.21*x2-0.63*y2+0.98.*x*y Regression of PCE (%) [x,y] = meshgrid(-2:0.01:2); z=6.78014+(1.16474.*x)-(0.99064.*y)-(1.21157.*(x.^2))-(0.63640.*(y.^2))+(0.98500.*x.*y); [C,h] = contour(x,y,z, [1,2,3,4,5,5.5,6,6.5,7,7.2]); axis([-1.5,1.5,-1.5,1.5]) clabel(C,h);
  • 12. 1 1 2 2 3 3 4 4 4 4 5 5 5 5 5.5 5.5 5.5 5.5 5.5 5.5 6 6 6 6 6 6 6.5 6.5 6.5 6.5 6.5 7 7 7 7 7.2 Temperatuer(degree) Annealingtime(mins) 85 100 115 6.5 10 13.5 -1.5 -1 -0.5 0 0.5 1 1.5 -1.5 -1 -0.5 0 0.5 1 1.5 12 Parameter Coefficient Xtemp 1.16 Ytime -0.99 XtempXtemp -1.21 YtimeYtime -0.63 XtempYtime 0.99 Main factor: Interaction: Temp.-Time 90℃ 110℃ z=6.78+1.16*x-0.99*y-1.21*x2-0.63*y2+0.98.*x*y > Regression of PCE (%)
  • 14. 14  Model is fixed  Algebra equation  Time-consuming  Model reduction  SAS regression  Interaction effect  Save time 0.00 0.25 0.50 0.75 1.00 0.00 0.25 0.50 0.75 1.00 0.00 0.25 0.50 0.75 1.00 IBr Cl Binary Design (A) Ternary Design (B) Modified mixture design methods
  • 15. Advantages of mixture design • Designs for these experiments are useful because many product design and development activities in industrial situations involve formulations or mixtures.
  • 17. 17 Mixture design methodology RegressionExperimental data Contour plot1. 2. 3. SAS 9.3 MATLAB R2013a 0.00 0.25 0.50 0.75 1.00 0.00 0.25 0.50 0.75 1.00 0.00 0.25 0.50 0.75 1.00 IBr Cl
  • 18. Origin data Ratio MACl MABr MAI Voc(V) Jsc (mA/cm2 ) FF (%) PCE (%) 1 1 0 0 0.76 10.31 69% 5.42 2 0 1 0 0.97 5.54 71% 3.81 3 0 0 1 0.78 9.76 70% 5.38 4 0.33 0.333 0.333 0.86 11.54 66% 6.54 5 0.5 0.5 0 0.97 4.76 70% 3.23 6 0 0.5 0.5 0.92 5.97 66% 3.58 7 0.5 0 0.5 0.71 12.10 72% 6.12 8 0.67 0.17 0.17 0.73 12.37 71% 6.38 9 0.17 0.67 0.17 0.97 10.66 64% 6.54 10 0.17 0.17 0.67 0.85 11.46 77% 7.51 11 0.75 0.25 0 0.90 7.43 64% 4.32 12 0.25 0.75 0 0.96 7.68 57% 4.15 13 0.25 0 0.75 0.78 13.06 68% 6.89 14 0.75 0 0.25 0.80 9.93 72% 5.68 15 0 0.75 0.25 0.99 10.81 72% 7.71 16 0 0.25 0.75 0.82 10.05 73% 6.01
  • 19. Forward selection SAS Regression run; proc reg; model y1=t1 t2 t3 t4 t5 t6 t7 t8 t9 t10 t11 t12 t13 /noint selection=forward; proc anova; 前進選擇: 步驟 1 R 平方 = 0.6006 和 C(p) = 57.8286 前進選擇: 步驟 2 R 平方 = 0.8367 和 C(p) = 17.3612 前進選擇: 步驟 7 R 平方 = 0.9792 和 C(p) = 1.7387 Click run Model reduction
  • 20. Parameter Coefficient X1 t1 X2 t2 X3 t3 X1X2 t4 X1X3 t5 X2X3 t6 X1X2X3 t7 X1X2(X1-X2) t8 X1X3(X1-X3) t9 X2X3(X2-X3) t10 X1X1X2X3 t11 X1X2X2X3 t12 X1X2X3X3 t13 SAS Regression-13 parameters 變異數分析 來源 DF R 2 平均值平方 F 值 Pr > F 模型 6 515.7 85.9 73.60 <.0001 誤差 10 11.8 1.2 未校正的總計 16 527.4 變 數 參數 估計 標準 誤差 第二型 SS F 值 Pr > F t1 5.57799 0.77588 60.35377 51.69 <.0001 t2 4.53861 0.83794 34.25800 29.34 0.0003 t3 6.53751 0.73561 92.22951 78.98 <.0001 t4 -5.83005 4.15712 2.29666 1.97 0.1911 t7 64.07944 25.58609 7.32434 6.27 0.0312 t10 11.75880 7.90392 2.58452 2.21 0.1677 R 平方 = 0.9779 和 C(p) = -0.0183
  • 21. Parameter Coefficient X1 t1 X2 t2 X3 t3 X1X2 t4 X1X3 t5 X2X3 t6 X1X2X3 t7 X1X1X2X3 t11 X1X2X2X3 t12 X1X2X3X3 t13 SAS Regression-10 parameters 變異數分析 來源 DF 和 平方 平均值 平方 F 值 Pr > F 模型 6 513.8 85.6 63.28 <.0001 誤差 10 13.53 1.35 未校正的總計 16 527.4 變 數 參數 估計 標準 誤差 第二型 SS F 值 Pr > F t1 5.26373 1.01318 36.52686 26.99 0.0004 t2 5.09614 0.83751 50.10738 37.03 0.0001 t3 5.81178 0.83751 65.16845 48.15 <.0001 t4 -6.08694 4.54785 2.42432 1.79 0.2104 t5 3.33659 4.54785 0.72845 0.54 0.4800 t7 59.03570 29.04160 5.59231 4.13 0.0695 R 平方 = 0.9743 和 C(p) = 2.7857
  • 22. 0 0.25 0.5 0.75 1 0 0.25 0.5 0.75 1 Cl Br I 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 7.4 7.2 7 6.5 6 5 6 6.5 7 5 6.5 6 0 0.25 0.5 0.75 1 0 0.25 0.5 0.75 1 Cl Br I 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 R 平方 = 0.9779 和 C(p) = -0.0183 R 平方 = 0.9743 和 C(p) = 2.7857 Different parameters compared 13 parameters 10 parameters
  • 23. Contour plot- e.g. PCE A=tril(meshgrid(0:0.001:1)); B=tril(meshgrid(1:-0.001:0)'); C=tril(1-A-B); x=tril(0.5.*(1+C-B)); y=tril((3^0.5)*0.5.*A); z=5.57799.*A +4.53861.*B+6.53751.*C -5.83005.*A.*B +64.07944.*A.*B.*C+11.75880.*B.*C.*(B-C); [C,h] = contourf(x,y,z, [1,2,3,4,5,6,6.5,7,7.2,7.4,7.6],'LineWidth',1); axis([0,1,0,1]); clabel(C,h,'manual','fontsize',15); hold on plot([0.375,0.625],[0.6495,0.6495],'k:'); hold on plot([0.25,0.75],[0.433,0.433],'k:'); hold on plot([0.375,0.75],[0.6495,0],'k:'); hold on plot([0.25,0.5],[0.433,0],'k:'); hold on plot([0.125,0.25],[0.2165,0],'k:'); hold on plot([0.125,0.875],[0.2165,0.2165],'k:'); hold on plot([0.25,0.625],[0,0.6495],'k:'); hold on plot([0.50,0.75],[0,0.433],'k:'); hold on plot([0.75,0.875],[0,0.2165],'k:'); 先建立矩 陣數列, 從0~1, 間格0.001 利用SAS迴歸得到的Eq.
  • 24. A=tril(meshgrid(0:0.001:1)) B=tril(meshgrid(1:-0.001:0)'); x=tril(0.5.*(1+C-B)); y=tril((3^0.5)*0.5.*A); C=tril(1-A-B); z=5.58.*A +4.54.*B+6.54.*C - 5.83.*A.*B+64.08.*A.*B.*C+11.76.*B.*C. *(B-C); e.g. 0.5*(1+0.001-0.998) e.g. 3*0.5*0.001 Function
  • 25. 0 0.25 0.5 0.75 1 0 0.25 0.5 0.75 1 Cl Br I 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 Contour plot- e.g. PCE [C,h] = contourf(x,y,z, [1,2,3,4,5,6,6.5,7,7.2,7.4,7.6],'LineWidth',1); axis([0,1,0,1]);
  • 26. 7 8 10 9 11 12 12.5 12.7 12 11 10 8 11 10 0 0.25 0.5 0.75 1 0 0.25 0.5 0.75 1 Cl Br I 0 0.2 0.4 0.6 0.8 1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 5 6 7 8 9 10 11 12 1 0.98 0.94 0.9 0.85 0.8 0.75 0.85 0.8 0 0.25 0.5 0.75 1 0 0.25 0.5 0.75 1 Cl Br I 0 0.2 0.4 0.6 0.8 1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0.7 0.75 0.8 0.85 0.9 0.95 1 0.6 0.65 0.68 0.7 0.75 0.8 0.850.9 0.55 0.7 0.7 0 0.25 0.5 0.75 1 0 0.25 0.5 0.75 1 Cl Br I 0 0.2 0.4 0.6 0.8 1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 0.55 0.6 0.65 0.7 0.75 0.8 0.85 0.6 0.6 0.65 0.65 0.68 0.68 0.7 0.75 0.8 0.85 0.9 0.75 0.7 0.55 0 0.25 0.5 0.75 1 0 0.25 0.5 0.75 1 IBr Cl 5 6 6.5 7 7.2 7.2 7 6.5 6 5 6 6.5 0 0.2 0.4 0.6 0.8 1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 1 2 3 4 5 6 7 JscVoc FF PCE PCE=5.6*A +4.5*B+6.5*C -5.8*A*B+64.1*A*B*C+11.8*B*C*(B-C); SAS Regression Jsc=9.44 X1+6.58 X2+10.75 X3-6.69 X1X2+8.07 X1X3+91.79 X1X2X3+17.10X2X3(X2-X3) Voc=0.76 X1+0.97 X2+0.77 X3+0.38 X1X2+0.20 X2X3+101.67X1X2X3+0.23X1X2(X1-X2)+0.38 X2X3(X2-X3)-112.78 X12X2X3-99.91 X1X2 2X3-95.62 X1X2X3 2 FF=0.70 X1+0.70 X2+0.71 X3-0.26 X1X2+0.36 X1X2(X1-X2)-3.92 X1X2 2X3+4.90X1X2X3 2
  • 27. 1 2 3 3 4 4 5 5 5 5 6 6 6 6 6 6.5 6.5 6.5 6.5 6.5 7 7 7 7.2 7.2 0 0.25 0.5 0.75 0 0.25 0.5 0.75 1 I 0 0.25 0.5 0.75 1 27 0.0 0.2 0.4 0.6 0.8 1.0 -16 -14 -12 -10 -8 -6 -4 -2 0 MAPbCl0.30 Br0.15 I0.55 MAPbCl0.30 Br0.35 I0.30 MAPbCl0.30 Br0.55 I0.15 Currentdensity(mA/cm 2 ) Voltage (V) PCE Contour plot run Cl Br I Voc Jsc FF PCE 0.30 0.55 0.15 0.97 9.94 0.70 6.77 0.30 0.35 0.35 0.92 14.07 0.73 9.47 0.30 0.15 0.55 0.75 12.67 0.68 6.52 Cl IBr Verification by J-V curve
  • 29. Factors and levels for the 23 Full Factorial Design factors levels + - A, P3HT:PCBM concentration (wt%) 2.5 1.5 B, rpm 600 1000 C, time (s) 60 40 Full Factorial Design
  • 30. 1.5wt% 600rpm 40s 600rpm 60s 1000rpm 40s 1000rpm 60s VOC (V) 0.04 0.60 0.70 0.72 JSC (mA/cm2 ) 2.94 7.22 1.21 1.03 FF 0.29 0.32 0.32 0.30 PCE (%) 0.03 2.83 0.27 0.22 R.P (Ω・cm2 )104 0.00083 278.8 71.68 99.72 R.S (Ω・cm2 ) 1.88 2.23 7.36 1.15 Run A B C Voc (V) Jsc (mA/cm2) FF PCE (%) 1 - + - 0.04 2.94 0.29 0.03 2 - + + 0.60 7.22 0.65 2.83 3 - - - 0.70 1.21 0.32 0.27 4 - - + 0.72 1.03 0.30 0.22 factors + - A, concentration (wt%) 2.5 1.5 B, revolution (rpm) 600 1000 C , time (s) 60 40
  • 31. 2.5wt% 600rpm 40s 600rpm 60s 1000rpm 40s 1000rpm 60s VOC (V) 0.60 0.58 0.60 0.70 JSC (mA/cm2 ) 7.54 9.11 9.40 1.90 FF 0.54 0.60 0.63 0.40 PCE (%) 2.46 3.18 3.53 0.53 R.P (Ω・cm2 )104 0.88 40.91 143.42 168.52 R.S (Ω・cm2 ) 2.05 2.80 2.27 7.39 5 + + - 0.60 7.54 0.54 2.46 6 + + + 0.58 9.11 0.60 3.18 7 + - - 0.60 9.40 0.63 3.53 8 + - + 0.70 1.90 0.40 0.53 factors + - A, concentration (wt%) 2.5 1.5 B, revolution (rpm) 600 1000 C , time (s) 60 40
  • 32. Run A B C Voc (V) Jsc (mA/cm2) FF PCE (%) 1 - + - 0.04 2.94 0.29 0.03 2 - + + 0.60 7.22 0.65 2.83 3 - - - 0.70 1.21 0.32 0.27 4 - - + 0.72 1.03 0.30 0.22 5 + + - 0.60 7.54 0.54 2.46 6 + + + 0.58 9.11 0.60 3.18 7 + - - 0.60 9.40 0.63 3.53 8 + - + 0.70 1.90 0.40 0.53 factors + - A, concentration (wt%) 2.5 1.5 B, revolution (rpm) 600 1000 C , time (s) 60 40 Design matrix
  • 33. Run A B C AB BC AC ABC PCE 1 - + - - - + + 0.03 2 - + + - + - - 2.83 3 - - - + + + - 0.27 4 - - + + - - + 0.22 5 + + - + - - - 2.46 6 + + + + + + + 3.18 7 + - - - + - + 3.53 8 + - + - - + - 0.53 effect estimate A 1.59 B 0.99 C 0.12 AB -0.20 BC 1.64 AC -1.26 ABC 0.22 The estimate of A = ( 𝟐.𝟒𝟔+𝟑.𝟏𝟖+𝟑.𝟓𝟑+𝟎.𝟓𝟑 𝟒 ) - ( 𝟎.𝟎𝟑+𝟐.𝟖𝟑+𝟎.𝟐𝟕+𝟎.𝟐𝟐 𝟒 ) = 1.59 Calculate the estimate

Notes de l'éditeur

  1. 因此我參考了上述了文獻 設計了一個實驗矩陣 以中心點加熱溫度100℃10分鐘做為零階 接著軸點上的溫度變化從80到120度,加熱時間從5到15分鐘 以這個實驗設計矩陣去做實驗 Michael Grätzel, Advanced Functional Materials Volume 24, pages 3250–3258 (2014)
  2. 藉由上述的數據,帶入迴歸可以得到這張二次回歸曲線圖 從圖上很明顯地可以看到有一個最佳的效率範圍,大約落在90~110度區間, 為了瞭解究竟溫度與時間對於目標值效率的影響 可以從迴歸後得到二次方程式的係數來分析數值 數值的大小以及正負代表對於目標值的貢獻程度 從這個表上來看, 溫度的主效應系數大於時間 也意味著溫度對於效率的影響程度較大 同時溫度與時間的交互作用對於目標值屬於正回饋的貢獻 在此也就意味著溫度與時間的兩者效應,對於效率彼此會有交互作用 所以,從這個統計上的意義,可以得到一個推論 溫度的影響因子比加熱時間還來的重要 同時,兩者具有交互作用 z=6.78+(1.16.*x)-(0.99.*y)-(1.21.*(x.^2))-(0.63.*(y.^2))+(0.98.*x.*y);
  3. 而為了能有效率的分析複雜的三成份系統,在此我使用了改良式的混合實驗設計法 這方法是結合了Design A與Design B的特性 Design A主要是探討兩成分效應 而Design B為了解三成份的效應 因為這兩個Model都是固定的,10個數據點10項,無法回歸,必須解代數方程式 所以實驗室提出了改良式混合實驗設計法 結合了Design A 與Design B與特性 變成16個數據點,而係數只有13項 因此可以藉由回歸的方式來獲得較準確的Model 同時藉由統計分析,也可以了解三成分混合系統的交互作用 Scheffe分別提出錐體配置設計(simplex lattice design,design A)及錐體中心點設計(simplex-centroid design,design B)兩種各十點實驗配置的方法。 數據點要多於項數,才得以回歸
  4. 而研究的步驟可大略分為三步 第一步是取得三角圖上16個不同混合比例的元件數據 接下來再利用SAS軟體回歸這些數據並得到回歸方程式 再把回歸式利用繪圖軟體MATLAB畫成三角等高線圖以利分析與觀察。
  5. 接下來我取了三個確認點來確認效率的三角圖是否具有意義 首先我把氯的比例視為定值0.30,碘與溴的混合比例加起來為0.7 因此可以得到如表格所示的混合比例 從數據上可以看到,隨著溴的比例增高,Voc的確跟著增加 然而,碘的含量提升,卻並未使電流密度有跟著一致上升,反而是產生了一最大值 而效率,再三者特性的加乘效應下,在混合比例為0.3:0.35:0.35可得到一個最佳的效率值為9.47% 而這些效率值,也正好落在我所迴歸出來三角圖,證明其是具有意義的 接著,再從J-V curve上也可以明顯地看到這三個條件的特性有所不同 因此除了統計上的結果外,後續我也做了儀器分析來近一步的佐證