Manufacturing process control with PAT - InfoScience · Manufacturing process control with PAT ......
Transcript of Manufacturing process control with PAT - InfoScience · Manufacturing process control with PAT ......
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Manufacturing process control with PATSubstitution of off-line HPLC & GC by in-line IR spectroscopy
Christian Lautz, F. Hoffmann-La Roche Ltd, Basel, SwitzerlandIFPAC-2015, January 25-28, Arlington,USA
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Many thanks to the team that made it possible!
Project coordinationA. BeyelerC. Lautz
CSV & ITH. DupyW. FreiP. Hänle
QC/QAR. HauckH.-G. Tölle
PATM. BetschartA. FehrC. Lautz
ManufacturingH. GasserA. GebertM. HaffnerA. Heuscher
WorkshopsMachine ShopElectricians
Project Team M. Cordon-FederspielR. DiodoneU. HoffmannC. MössnerB. Ruff
EngineeringJ. BlindH. KäserD. ÜberschlagV. Roux
Special thanks toP. ChalusG. Thurau
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Introduction
Feasibility study
Model development and validation
Manufacturing plant setup
Process qualification campaign
Model verification3
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Introduction
Feasibility study
Model development and validation
Manufacturing plant setup
Process qualification campaign
Model verification4
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Manufacturing process: Flow-chart
Reaction
Quench on sulfuric acid
Extractions Aqueousphases
API dissolved in toluene
5% NaHCO3 solutionWater
Concentration(54 °C, 20-220 mbar)
Reflux(78 °C, dissolve crusts)
Cooling to 60 °C
Concentrationadjustment
Ethanol
Reflux(78 °C, dissolve crusts)
Cooling to 60 °C
API dissolved in ethanolConcentration: 18%(m/m)
API dissolved in ethanolConcentration: 17%(m/m)
Seeding(1%(m/m) Form A)API
Concentrationadjustment (opt.)
Cooling to 41 °C (within 90 minutes)
Aging(41 °C, 1 h)
DilutionEthanol
Solvent exchange(54 °C, 260-330 mbar)
Ethanol, toluene
Ethanol Cooling to -10 °C (within 7 h)
Polishing filtration(1.2 m filter)
RinsingEthanol
Aqueousphase IPC
Distiller Crystallizer Release analysis
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Form B
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Manufacturing process: CPP & CQA
• IPC sampling– The concentration of the API and residual toluene is determined via IPC
sample (concentration is a critical process parameter, CPP)
• Seeding and crystallization– Crystallization of the desired polymorphic form A can only be achieved by
seeding; from the supersaturated solution the undesired form B is formed upon spontaneous crystallization (polymorphic form is a critical quality attribute, CQA)
Form A
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IPC sampling issues
• Sampling of the warm supersaturated solution into a glass bottle has the risk of undesired precipitation of the API in the sampling system or the bottle
• Crystallization may occur upon cooling during transport to QC lab or during sample preparation
• Heating the sample to bring the API in solution again is an undesired intervention to re-create a representative sample
• Two methods from one sample, HPLC for API concentration and GC for residual solvent determination
• In short: Assay determination with a higher probability of failures
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It is obvious……
An in-line PAT method couldovercome the problems related to sampling
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Challenges for the PAT method
• Choice of an adequate technology to deliver desired accuracy for IPC samples, and apply same technology for both concentration determinations
• Follow the distillation to its end point in the first reactor, and / or determine the concentrations after filtration and dilution in the second reactor?
• Choice of probe technology for potential distillation (gas bubbles) and / or crystallization (encrustation on probe)
• For GMP sampling in manufacturing– Computer System Validation and (laboratory) instrument qualification– PAT method validation
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Introduction
Feasibility study
Model development and validation
Manufacturing plant setup
Process qualification campaign
Model verification10
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Laboratory feasibility study
• IR was chosen as primary technology for a laboratory feasibility study due to the ruggedness of ATR probes to gas bubbles and (non-sticking) particles
• Transmission NIR spectroscopy was chosen as secondary technology, since it is more sensitive to gas bubbles (for probes with a horizontal slit)
• Quantitative chemometric models were developed for IR and NIR spectroscopy from the same set of calibration standards
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PAT method development
• Instrument– Mettler Toledo iC45m IR spectrometer equipped with HC22 ATR probe and
2 m AgX optical fiber; resolution 4 cm-1 with 256 scans per spectrum
• Sample preparation and measurement– Generic samples prepared from pure substances API, toluene and ethanol;
randomized amounts to avoid collinearity• API: 15.0–30.0%(m/m)• Toluene: 0-5.0%(m/m)
– 45 samples, measured at 55 °C in a thermostat (100 ml glass bottles with magnetic stirrer bar)
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IR method development results: API
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IR method development results: Toluene
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140 200 260 320 380 440 500
Conc
entr
atio
n [ %
(m/m
) ]
Time [ min ]
API (IR)
API (HPLC)
Toluene (IR)
Toluene (GC)
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Technical scale-up: 50 L reactor
* Outside the calibrated model range
Time [ min ]
API (IR)[ %(m/m) ]
API (HPLC)[ %(m/m) ]
Toluene (IR)[ %(m/m) ]
Toluene (GC)[ %(m/m) ]
142 21.5 19.9 24.1* 30.3*
234 20.8 20.4 13.8* 15.8*
324 22.6 22.9 5.4 5.2
444 23.0 23.3 1.1 0.9
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Assessment of feasibility study results
• Quantitative IR models were successfully applied in technical scale-up for monitoring and in-line concentration determination
– “Real” production process (50 L scale) can be monitored with models derived from generic samples prepared from pure components
– Agreement between off-line analyses and in-line measurements– Successful preliminary test of validation based on a reduced number of
separate samples (robustness; linearity, accuracy, precision)
• Agreement to introduce an in-line spectroscopic concentration measure-ment in manufacturing for process qualification campaign
– Final chemometric models will also be based on generic samples from pure compounds since (only) this allows for necessary sample variability
– HPLC & GC analysis will not be used as basis for model development
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Technical setup in manufacturingM
M
ATEX environment
Vertical slit NIR probe
ATEX NIRspectrometer
Non-ATEX environment
Bottom valve with ATR IR probe
ATEX IR spectrometer
Data visualisation for IR:Laptop in control room
Crystallizer
Distiller
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Introduction
Feasibility study
Model development and validation
Manufacturing plant setup
Process qualification campaign
Model verification18
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IR method development and validation for GMP use
• Instrument– Mettler Toledo ReactIR 45P IR spectrometer, equipped with custom-made
ATR probe (90 cm length, 6.3 mm diameter) and 2.5 m AgX optical fiber – Instrument qualification and CSV successfully completed
• Concentration ranges– API: 10.9 – 25.4%(m/m)
• Specification: 15.3 – 18.7%(m/m); 17.0%(m/m) as target value– Toluene: 0 – 5.0%(m/m)
• Specification: max. 2.0%(m/m)– Cyclohexane: 0 – 1.3%(m/m) (denaturant in ethanol from solvent recovery)
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IR method development and validation for GMP use
• Calibration samples / cross validation– 4 batches API, 2 qualities ethanol– 1 quality toluene and cyclohexane– 60 samples
• Robustness samples / external test-set validation– Mutual self-influence of analytes as well as influence of temperature, water,
cyclohexane and unidentified side products (from mother-liquor residue) tested
– 3 batches API, 3 qualities ethanol– 1 quality toluene, cyclohexane, water, mother liquor residue– 23 samples
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IR method development and validation for GMP use
• Validation samples / external test-set validation– 1 batch API, 1 quality ethanol and toluene– Linarity, accuracy, precision and LOQ for toluene; no intermediate precision– 39 samples
• Samples measured at 54 – 66 °C in a thermostat (100 ml glass bottles with magnetic stirrer bar) with 256 scans per spectrum; resolution 4 cm-1
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IR method development results: Raw spectra
API Toluene
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IR method development results: APIP
redi
cted
- A
PI
Cross validation (model)Test-set validation
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IR method development results: API
• Cross validation results– Spectral range: 1100 – 1700 cm-1
– 1st derivative as data pretreatment– Principal components: 3– RMSECV: 0.07%(m/m)– Mahalanobis Distance: 1.66 ± 0.80
• Test-set validation results– RMSEP: 0.24%(m/m)– Acceptance criterion RMSEP: ≤0.8%(m/m)– Mahalanobis Distance: 1.58 ± 0.51– Mahalanobis Distance limit (MDL): 4.7
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IR method development results: Toluene
Cross validation (model)Test-set validation
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IR method development results: Toluene
• Cross validation results– Spectral range: 700 – 800 cm-1
– 1st derivative as data pretreatment– Principal components: 2– RMSECV: 0.08%(m/m)– Mahalanobis Distance: 1.31 ± 0.85
• Test-set validation results– RMSEP: 0.07%(m/m)– Acceptance criterion RMSEP: ≤0.5%(m/m)– Mahalanobis Distance: 1.23 ± 0.56– Mahalanobis Distance limit (MDL): 4.4
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First IR model application: Laboratory distillation
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0 50 100 150 200 250 300 350
Conc
entr
atio
n [ %
(m/m
) ]
Time [ min ]
API (IR)
API (HPLC)
Toluene (IR)
Toluene (GC)
Time [ min ]
API (HPLC)[ %(m/m) ]
API (IR)[ %(m/m) ] MD Toluene (GC)
[ %(m/m) ]Toluene (IR)[ %(m/m) ] MD
284 17.5 17.4 1.57 0.38 0.35 2.33
326 16.6 16.2 1.61 0.38 0.38 2.28
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Introduction
Feasibility study
Model development and validation
Manufacturing plant setup
Process qualification campaign
Model verification28
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Setup of NIR spectrometer and probe in plant
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Setup of IR spectrometer and probe in plant
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Setup of IR spectrometer and probe in plant
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Setup of IR spectrometer and probe in plant
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Setup of IR spectrometer and probe in plant
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Introduction
Feasibility study
Model development and validation
Manufacturing plant setup
Process qualification campaign
Model verification34
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The spectroscopic limitations in manufacturing
• Background measurement with clean probe after installation– Empty reactor, dry and under nitrogen– Measurement possible only once before first batch due to (potential)
encrustation, thus valid/used throughout the whole campaign
• Stepwise control process established for IR spectrometer to ensure correct functionality of the spectroscopic GMP measurement
– Full set of functional tests before setup in plant– Slightly reduced set of functional tests after setup in plant, before first batch– SST before every plant batch– Full set of functional tests after removal from plant and return to laboratory
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The first manufacturing batch: Complete processDistiller (NIR) & Crystallizer (IR)
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Tolu
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[ %(m
/m) ]
API [
%(m
/m) ]
Time [ h ]
Distillation & crystallization overview
Seeding at 41 °C
Start of ramp to -10 °C
Addition rate decreased
Vessel transfer (NIR → IR)
Stepwise dilution
Changes in stirrer speed
Specification for toluene can be reached without problems during solvent exchange
Every following batch showed crusts on probe after seeding
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The first manufacturing batch: IR data for APICrystallizer
0.0
0.5
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18.0
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Mah
alan
obis
Dis
tanc
e (M
D)
API [
%(m
/m) ]
Time [ h ]
Rinse with 200 kg ethanol
50 kg ethanol from spray ring
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1.6
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Mah
alan
obis
Dis
tanc
e (M
D)
API [
%(m
/m) ]
Time [ min ]
Sample at 60 °C:
API = 17.46% (m/m)MD = 1.81
Start cooling to 41 °C
50 kg ethanol from spray ring
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The first manufacturing batch: GMP IR data for APICrystallizer
Sensitivity of the Mahalanobis Distance on temperature change becomes evident
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The results overview: Technical batches
Batch SampleGMP IR value
PolymorphYield
[ %(m/m) ] MD [ % ]
1Toluene <1.0 1.3
A 86.4API 17.5 1.8
2Toluene <1.0 1.3
A 86.1API 17.1 1.8
3Toluene 1.3 1.0
A 89.3API 17.2 1.6
4Toluene <1.0 1.1
A 89.3API 17.5 1.7
5Toluene 1.3 0.9
A 88.9API 17.3 1.6
All specifications and limits are met
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The results overview: Process qualification batches
Batch SampleGMP IR value
PolymorphYield
[ %(m/m) ] MD [ % ]
6Toluene 1.2 1.0
A 91.9API 18.0 1.7
7Toluene 1.1 1.0
A 91.9API 17.9 1.7
8Toluene 1.3 0.9
A 91.2API 17.5 1.6
All specifications and limits are met
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Assessment of PAT results from process qualification campaign
• No sampling necessary any more
• Direct in-line determination of two parameters from one IR spectrum– Residual toluene concentration after solvent exchange (off-line: GC)– API concentration prior to seeding (off-line: HPLC)
• Quantitative results in minutes, significantly reduced cycle time
• Control of API concentration within specification (CPP) to ensure precipitation of desired polymorph after seeding (CQA)
• 8 batches produced in Jan./Feb. 2014 with good results / reproducibility
• First validated spectroscopic PAT method for small molecule API manufacturing in Basel
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Introduction
Feasibility study
Model development and validation
Manufacturing plant setup
Process qualification campaign
Model verification42
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IR method verification after the campaign
• Sample preparation and measurement– Verification samples / external test-set validation
• 1 batch API (campaign batch 2), 1 quality ethanol and toluene• 24 samples
– Samples measured at 60 °C in a thermostat (100 ml glass bottles with magnetic stirrer bar) with 256 scans per spectrum; resolution 4 cm-1
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11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26
Pred
icte
d AP
I [ %
(m/m
) ]
Actual API [ %(m/m) ] 44
IR method verification results: API
Cross validation (model)Test-set validationTest-set verification
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IR method verification results: API
• Test-set validation results– RMSEP: 0.24%(m/m)– Acceptance criterion RMSEP: ≤0.8%(m/m)– Mahalanobis Distance: 1.58 ± 0.51– Mahalanobis Distance limit (MDL): 4.7
• Test-set verification results– RMSEP: 0.30%(m/m)– Mahalanobis Distance: 1.63 ± 0.54
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-0.9
-0.8
-0.7
-0.6
-0.5
-0.4
-0.3
-0.2
-0.1
0.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400
Pred
icte
d -A
ctua
l API
[ %
(m/m
) ]
Sample number
Limit: RMSEP ≤ 0.8%(m/m)
Limit: RMSEP ≤ 0.8%(m/m)
46
IR method verification results: API predictions
Cross validation (model)Test-set validationTest-set verification
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0.0
0.5
1.0
1.5
2.0
2.5
3.0
3.5
4.0
4.5
5.0
0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400
Mah
alan
obis
Dis
tanc
e A
PI
Sample number
Limit: Mahalanobis Distance ≤ 4.7
47
IR method verification results: API MD
Cross validation (model)Test-set validationTest-set verification
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0.0
0.5
1.0
1.5
2.0
2.5
3.0
3.5
4.0
4.5
5.0
0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0
Pred
icte
d To
luen
e [ %
(m/m
) ]
Actual Toluene [ %(m/m) ] 48
IR method verification results: Toluene
Cross validation (model)Test-set validationTest-set verification
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IR method verification results: Toluene
• Test-set validation results– RMSEP: 0.07%(m/m)– Acceptance criterion RMSEP: ≤0.5%(m/m)– Mahalanobis Distance: 1.23 ± 0.56– Mahalanobis Distance limit (MDL): 4.4
• Test-set verification results– RMSEP: 0.12%(m/m)– Mahalanobis Distance: 1.25 ± 0.57
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-0.55-0.50-0.45-0.40-0.35-0.30-0.25-0.20-0.15-0.10-0.050.000.050.100.150.200.250.300.350.400.450.500.55
0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400
Pred
icte
d -A
ctua
l Tol
uene
[ %
(m/m
) ]
Sample number
Limit: RMSEP ≤ 0.5%(m/m)
Limit: RMSEP ≤ 0.5%(m/m)
50
IR method verification results: Toluene predictions
Cross validation (model)Test-set validationTest-set verification
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0.0
0.5
1.0
1.5
2.0
2.5
3.0
3.5
4.0
4.5
5.0
0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400
Mah
alan
obis
Dist
ance
Tolu
ene
Sample number
Limit: Mahalanobis Distance ≤ 4.4
51
IR method verification results: Toluene MD
Cross validation (model)Test-set validationTest-set verification
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The next (potential) steps
• PAT QC samples can now be handled by the production groups – Streamline efforts and procedures to simplify ease of use for shift workers– Intermediate reactor cleaning for longer campaigns
• Process automation in manufacturing – Control of distillation, transfer, dilution, IPC up to seeding point– NIR: Two probes on one spectrometer with multiplexer, long fibers possible– IR: One spectrometer and probe necessary per reactor, limited fiber length– Connection of spectrometer(s) to plant DCS (PAQ necessary)
• Method lifecycle– Introduce F-Ratio as secondary quality criterion with acceptance limits
derived from the process qualification campaign
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Doing now what patients need next
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