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Current Regulatory Considerations on Pharmaceutical Lyophilization Kumar Janoria, Ph.D. FDA/CDER/OPQ Office of Process & Facilities/Division of Process Assessment III www.fda.gov

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Page 1: Current Regulatory Considerations on Pharmaceutical ...islyophilization.org/wp-content/uploads/2016/11/Janoria-ISLFD-2016.pdf · Current Regulatory Considerations on Pharmaceutical

Current Regulatory Considerations on Pharmaceutical Lyophilization

Kumar Janoria, Ph.D.

FDA/CDER/OPQ

Office of Process & Facilities/Division of Process Assessment III

www.fda.gov

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Quiz What is a Primary Drying End Point in a lyophilization cycle? Options:

1. Point at which all of the free ice has been removed from all the vials and there are no concerns of collapse or melt back when the temperature is ramped up for secondary drying (desorption).

2. The reason our process takes so long and costs so much. 3. When a toothpick comes out clean after inserting into the center

of the cake. 4. There is no such thing called primary or secondary drying.

Temperatures can be continuously ramped up from freezing all the way to completion of lyophilization cycle.

www.fda.gov www.fda.gov

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3 www.fda.gov

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Disclaimer

• This presentation reflects the views of the

presenter and should not be construed to

represent FDA’s views or policies

• Word ‘should’ only means suggestion or

recommendation but is not required

• Opinions are based on small molecules review

perspective

www.fda.gov

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OPF’s Lyo Committee of Interest • Lyophilization is considered high-impact

manufacturing topic and therefore there is a need to develop common practices to ensure that appropriate and consistent evaluation will occur during manufacturing process assessment.

• Forum to gather information on freeze drying technology and manufacturing, establish applicable quality review standards, and Disseminate these findings to enhance submission quality and enable consistent review prActices.

www.fda.gov

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Expectations from Applicants

Demonstrate understanding of:

• Formulation

• Product

• Equipment

• Development of a lyo cycle specific to product

• Manufacturing process to achieve consistent batch to batch product

6 www.fda.gov

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Quality by Design (ICH Q8) • Quality Target Product Profile

• Critical Quality Attributes

• Risk Assessment: Linking Material Attributes and Process Parameters to Drug Product CQAs Critical Process Parameters

• Design Space

• Control Strategy

• Product Lifecycle Management and Continual Improvement

www.fda.gov

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Regulatory Considerations • Hold time and Equipment Compatibility

• Fill Volume/Fill Volume Tolerances

• Product Specific Characterization/Development Studies

• Establishing the Critical Process Parameters

• Establishing the end points for Primary and Secondary Drying

• Sampling Plan

• Critical Quality Attributes

• Scale-up

• Post Approval Lifecycle Perspective

8 www.fda.gov www.fda.gov

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Manufacturing Flow Chart

9

Compounding

Filtration

Filling and Partial Stoppering

Lyophilization and Full Stoppering

Sealing and Packaging

www.fda.gov www.fda.gov

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Hold time and Equipment Compatibility

• Product Stability after compounding (Bulk Hold) – Time – Temperature – Lighting – Inert Gas

• Compatibility with equipment train – Compounding Tank – Tubings – Pumps (Formulation contacting surfaces) – Filters

www.fda.gov www.fda.gov

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Fill Volume • Does USP <1151> Pharmaceutical Dosage Forms apply to lyophilized

drug products? • Example:

– 50mg/vial labeled drug upon reconstitution with 5mL diluent results in 10mg/mL.

– For a bulk concentration of 10mg/mL with recommended overfill per USP <1151> will result in 53mg/vial lyophilized product.

– What is the concentration achieved upon reconstituting with 5mL vs. 5.3 ml?- Accurate description in PI?

– Is this 6% overage or just acceptable overfill?

11 www.fda.gov www.fda.gov

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Fill Volume Tolerances

Parameters

Reference Product

[AMAZING®, 100

mg/vial]

Incredible HCl for

Injection,

100 mg /vial

Concentration of

bulk solution 25 mg/mL 50 mg/mL

Fill Volume

Filling range: 3.90 –

4.10 mL

target: 4.0 mL

1.90 – 2.10 mL

target: 2.0 mL

Calculated

Amount/vial 100mg± 2.5mg 100 mg ± 5 mg

12

• What is bulk solution in-process assay specification? Can

worst case combination of fill tolerance and in-process

assay result out of specification at release? www.fda.gov www.fda.gov

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Product Specific Characterization

• Studies: Freeze Drying Microscopy and Differential Scanning Calorimetry

• Amorphous Vs. Crystalline Vs. Metastable

• Annealing Vs. Non- Annealing

• Critical Temperatures: Glass Transition (Tg’), Eutectic (Teu), Collapse (Tc)

• Study Design (Ramp rates, Target Temperatures)

• Extrapolation of Information collected

13 www.fda.gov www.fda.gov

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Establishing the Critical Process Parameters

• Correlation of shelf temperature and chamber pressure and corresponding product temperature.

• Effect of critical process parameters on the powder properties.

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Critical Process Parameters Powder Properties

loading

cooling rate

primary and secondary drying

conditions

• temperatures

• durations

• pressure

structure

cake appearance

water content

Assay

impurities

reconstitution time

www.fda.gov www.fda.gov

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Establishing the End Points for Primary and Secondary Drying

• Thermocouples

• Pirani Gauge vs. Capacitance Manometer

• Dew Point

• TDLAS

• Pressure rise test

• Sampling plan (moisture content)

15 www.fda.gov www.fda.gov

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Typical Lyophilization Cycle Graph

A typical graph shows the shelf temperature (–), average product temperature as measured by the

thermocouples (...), capacitance manometer (C) and Pirani gauge (P) over the course of the run.

Reference: Quality by design: Impact of formulation variables and their interactions on quality attributes of a lyophilized

monoclonal antibody. International Journal of Pharmaceutics 438 (2012) 167– 175

16 www.fda.gov www.fda.gov

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Sampling plan • To adequately capture the variation or uniformity

• Edge Effect

17

1.6 1.4 1 1 1.4 1 1 1.8 1.8 1 1.4 1.8 1 1.4 1.6

1 1 1.2 1 1.4 1 1 1.6 1.6 1 1.4 1.6 1.2 1 1

0.8 1 1.8 1.8 1.4 2.4 1.8 2.4 2.4 1.8 1.4 2.4 1.8 1 0.8

1.2 1.4 1.2 1.8 1.2 1.8 3.6 2.4 2.4 3.2 2.8 2.4 1.2 1.4 1.2

1.2 1 2.4 1.8 1.6 2.2 2.6 4 3.6 2.6 1.6 2.4 2.4 1 1.2

0.8 1.2 1.2 1.2 1.4 2.2 2.4 4.6 4.6 2.8 3.6 4.6 1.2 1.2 0.8

1.8 0.8 2.2 1.6 1.4 1.6 2 2.6 2.6 2 1.4 2.6 2.2 0.8 1.8

1 1 1 1.8 2 1.2 3.6 1.8 3.6 3.6 2 1.8 1 1 1

1.8 1.6 1.2 0.8 1.2 1.2 1.8 1.4 1.4 1.8 1.2 1.4 1.2 1.6 1.8

1.2 1.4 1.4 1.2 1.6 1 1.6 2.2 2.2 1.6 1.6 2.2 1.4 1.4 1.2

1 1 2.4 1.8 1 1.8 1 1

Example of Edge effect: Variation in moisture content across the shelf due to edge effect.

• Process development vs. Routine testing

www.fda.gov www.fda.gov

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Critical Quality Attributes • Residual Moisture Content (using appropriate Moisture testing

method)

• Appearance of Lyophilized Cake

• Assay (Loss due to sublimation)

• Reconstitution Time (Method consistency)

18 www.fda.gov www.fda.gov

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Scale-up • Scale-up factor

• Same dryer vs. larger dryer

• Partial load vs. full load

• Equipment capabilities (Ramp rate, lowest chamber pressure, lowest shelf temperature)

• Sampling Plan

19 www.fda.gov www.fda.gov

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Post Approval Lifecycle Perspective

0

20

40

60

80

100

120

140

0 1 2 3 4 5 6

Ave

rage

nu

mb

er o

f su

pp

lem

ents

file

d

(ND

A+A

ND

A)

Time for submission post approval (years)

Post approval of ANDA/NDA: Number of Supplements Vs. Filing Time The information is based on total 125 applications with 103 ANDAs and 22 NDAs. There were total of

453 supplements filed of which 360 are ANDA supplements and 93 are NDA supplements. A descending

trend of filed supplements was noted with the number of years post approval of the ANDA or the NDA.

www.fda.gov www.fda.gov

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21 21

1%

5%

32%

26%

18%

2%

16%

Change Type All

ComponentComposition

Container Closure

Labeling

Manufacturing Process

Manufacturing Site

Miscellaneous

Specifications

1%

0% Container Closure

36%

17%

25%

4%

17%

Change Type-NDA

1%

6%

31%

28%

17%

2% 15%

Change Type-ANDA

Post Approval Lifecycle Perspective

The information is based on total 125 applications with 103 ANDAs and 22 NDAs. There were total of

453 supplements filed of which 360 are ANDA supplements and 93 are NDA supplements. The

supplements were divided into 7 categories based on the proposed change type. The categories were

created based on the “Guidance for Industry: Changes to an approved NDA or ANDA”.

www.fda.gov www.fda.gov

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Commonly Used Terms • Lyophilization

• Freeze Drying

• Lyophilizer

• Choked flow

• Freeze Drying

Microscope

• DSC

• Tg’/Tc/Teu/Tg

• Freezing

• Ice Nucleation

• Annealing

• Vacuum

• Sublimation

• Condensation

• Condenser

(Temperature)

• Ramp rate and

Hold times

• Shelf vs. Product

Temperature

• Thermocouple

• Vapor pressure

• Pressure Gauge

• Primary Drying

• Cake Resistance

• Secondary Drying

• Collapse

• Melt back

• Pressure rise Test

• Drying End Points

• Lyo recipe

• Cake/powder

Appearance

22 www.fda.gov www.fda.gov

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Acknowledgements • Naiqi Ya

• Edwin Jao

• David Doleski

• Robert Iser

• Lane Christensen

• Abi D’Sa

• Steve Rhieu

• Vani Mathur

23

• Akshata Nevrekar

• David Anderson

• Geoff Wu

• Abhishek Sahay

• Niles Ron

• David Awotwe-Otoo

• Charu Srinivasan

• Cyrus Agarabi

www.fda.gov www.fda.gov