preliminary design space

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NIPTE-FDA Collaborative Case Study On Model-based Design Space Development Across Scales & with Stability Considerations. Preliminary Design Space. Define Target Product Profile (TPP). Derive Quality Attributes from TPP. Propose Manufacturing Process. Risk Analysis ( FMEA ). - PowerPoint PPT Presentation

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1

NIPTE-FDA Collaborative Case StudyOn Model-based Design Space Development

Across Scales & with Stability Considerations

Preliminary Design Space

2

QbD process

Define Target Product Profile (TPP)Derive Quality Attributes from TPP

Propose Manufacturing ProcessRisk Analysis (FMEA)

Risk Evaluation (Risk-based Classification)

Propose Parameters to Investigate (e.g., by DOE)

PROCESS DESIGN SPACE

3

Basic Processing SequenceRA Results

CPPs

5

Design Space Definition

• For each unit op establish functional relationships of CPP and CQA of input materials with CQA of output materials– e.g. disintegration time ~ compression force and

hydrophobicity• Establish interactions between unit ops

– e.g. hardness ~ PSD and compression force• Establish design space boundaries by propagating

backwards limits imposed on final product CQAs

6

Design Space Definition

courtesy: Dr. Steef. Boerrighter, Purdue University

7

Preliminary Design Space

• Considered– Degradation

• NMT 0.4 mole % lactam– Hardness

• NLT 3 kP– Weight variation

• 90 % - 110%• % RSD NMT 6%

• DS definition for 15 CPPs• Interactions were established for some CPPs

– one or more slides included to describe those interactions

• There were no significant interactions for few CPPs– ranges for those are shown in slide 18

8

Tablet Hardness ~ Intermediate CQA

Com

pres

sion

For

ce

Bulk density 0.52 kg/m3

1500

2000

2500

3000

Mea

n C

omp.

For

ce

Mean Hardness

280 290 300 310 320 330 340 350Median PS

1.5

2

2.5

3

3.5

4

4.5

5

Mea

n H

ardn

ess

Act

ual

1.5 2 2.5 3 3.5 4 4.5 5Mean Hardness Predicted

P<.0001 RSq=0.98 RMSE=0.1178

1500

2000

2500

3000

Mea

n C

omp.

For

ce

Mean Hardness

280 290 300 310 320 330 340 350Median PS

Bulk density 0.46 kg/m3

Median PSMedian PS

9

Tablet Hardness ~ Intermediate CQA

PAT application:Real time measurement

of bulk density and particle size

10

Tablet Hardness ~ Tabletting CPP

Min

Pun

ch G

ap

Press speed 63360 tab/hr

4.3

4.4

4.5

4.6

4.7

Min

Pun

ch G

ap

Tablet Hardness

3.55 3.6 3.65 3.7 3.75 3.8 3.85Compression height (mm)

4.3

4.4

4.5

4.6

4.7

Min

Pun

ch G

ap

Tablet Hardness

3.55 3.6 3.65 3.7 3.75 3.8 3.85Compression height (mm)

1

2

3

4

5

6

7

Table

tH

ard

ness

Act

ual

1 2 3 4 5 6 7Tablet Hardness Predicted

P<.0001 RSq=0.62 RMSE=0.6823

Press speed 21120 tab/hr

Comp. HeightComp. Height

11

Preliminary Tabletting Design Space

12

Blending

12

15 RPM, 50% 15 RPM, 80% 25 RPM, 50% 25 RPM, 80%0

0.002

0.004

0.006

0.008

0.01

0.012

0.014

0.016

0.018

STS

Significant increase in STS at extreme

conditions

13

Tablet Hardness ~ Drying CPP

EEF

0.2

0.25

0.3

0.35

0.4

0.45

EE

F

1500 2000 2500 3000Mean Comp. Force

0.2

0.25

0.3

0.35

0.4

0.45

EE

F

1500 2000 2500 3000Mean Comp. Force

End Moisture Target = 0.5%

End Moisture Target = 1%

Comp. Force Comp. Force

14

L0, D0 ~ Drying CPP

0.011

0.0115

0.012

0.0125

0.013

0.0135

0.014

0.0145

Gra

n In P

roc

Lacta

m A

ctu

al

0.011 0.012 0.013 0.014Gran In Proc Lactam Predicted

P=0.0816 RSq=0.65 RMSE=0.0007

0.009

0.01

0.011

0.012

0.013

0.014

0.015

Gra

n L

acta

mR

ate

Actu

al

0.009 0.010.011 0.013 0.015Gran Lactam Rate Predicted

P=0.0483 RSq=0.71 RMSE=0.0013

D0,

crys

tal d

amag

e

L 0, i

n-pr

oces

s la

ctam

X – Wet Massing TimeY – Water Content

15

Preliminary Drying Design Space

16

Tablet Hardness ~ Granulation CPP

WMT=60s

Wat

er C

onte

nt

4

4.5

5

5.5

6

Wat

er c

onte

nt

1500 2000 2500 3000Mean Comp. Force

4

4.5

5

5.5

6

Wat

er c

onte

nt

1500 2000 2500 3000Mean Comp. Force

WMT=0s

Comp. ForceComp. Force

17

Preliminary Granulation Design Space

18

Preliminary Design Space

• Granulation– Impeller speed

• 500 RPM• Fr 1.20

– Critical Fr determined for 4 L Gral at 250 RPM = 0.30

• Drying– End Product Target Temperature

• 25°C – 30°C• Blending

– 15 – 25 RPM– 60% – 80% fill ratio– # of rotations: 42-125

19

Summary

• Risk Assessment helps to identify CPP• Preliminary Design Space is defined by backward

propagation• Some PPs identified by RA are not critical in the

explored experimental domain• Preliminary Design Space is constructed for:

– Wet granulation– Fluidized bed drying– Blending– Tabletting

• Some interactions between unit ops were considered– Tabletting and intermediate CQA– Fluidized bed drying and tabletting– Wet granulation and tabletting

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