pat in freeze drying

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    Application of PAT in Freeze-Drying of Biopharmaceuticals

    Rakhi B. Shah, Ph.D .U.S. Food and Drug Administration

    Disclaimer: The views expressed in this presentation are the personalopinions of the speaker and do not necessarily represent the views of FDA

    AAPS National Biotech Conference 2010

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    Overview

    Process Analytical Technology (PAT)

    Freeze-drying

    Application of PAT in freeze drying

    Case study

    Conclusion

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    Process Analytical Technology

    A fundamental element of PAT is to increaseprocess understanding and control and to verifyproduct quality prior to release.

    PAT offers the possibility to increase productquality consistency and to reduce product riskthrough increased process knowledge andunderstanding optimized process control with theuse of PAT tools

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    Reducing Product Variability

    Process(or Process Step)

    DesignSpace

    Monitoring of Parametersor Attributes

    Process Controls/PAT

    InputProcess

    Parameters

    InputRaw materials

    Product(or Intermediate)

    ProductVariability

    ReducedProductVariability

    ProcessVariability

    Nasr, FDA

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    Freeze-DryingLow-temperature drying process

    Convert solut ions of heat-labile materials into sol ids

    Heat and mass transfer

    Steps in freeze-drying:i. Freezing: water converted to ice and the solutes are crystallized or

    transformed into solid

    ii. Primary drying: ice crystals removed by sublimation under vacuum

    iii. Secondary drying: drying under vacuum where most of theunfrozen water is removed by desorption.

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    Heat Transfer MeasurementsThermocouples

    positioned bottom-center in the vial

    -less robust ,difficult tohandle , sterilityproblems-Used mainly inlaboratory scale

    Pikal et al., 2002; Scheind & Giessler, 2008; Chouvene et al., 2005; Schneid, SP Industries Webinar, 2009

    wireless battery-freetemperature sensors

    sterilizable and can be usedin both laboratory andmanufacturing scale optimal comparability of temperature profi les for scale up

    Resistance thermaldetectors

    TEMPRIS TM+ Reliable, easy tosterilize- s ize , accuratepositioning is difficult,limited validity due tomeasurement of temperature averageprimarily inmanufacturing scale

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    Mass Transfer MeasurementsMicrobalance

    Determines the loss of weight of a sample vial during freeze drying byintermittent or continuous weighing information about sublimationrate and process step endpoints

    for research and development

    Mayeresse & Veillon, 2006; Schneid, SP Industries Webinar, 2009

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    Pressure MeasurementsCapacitance Manometer Thermal conductivity

    sensor (Pirani)

    Independent of the type of gas

    Dependent on type of gas, calibrated for aspecific gas (usuallyN2 )

    Dew point sensor

    Determinationof concentrationof water vapor in a gas

    Roy and Pikal, 1989; Jennings and Duan, 1995; Schneid, SP Industries Webinar, 2009

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    Mass Spectrometer Plasma emissionspectroscopy

    Measures water vapor, N2 alsoany additionalresidualsolvents,volatil es, etc

    Lyotrack TM:Spectroscopicmeasurement of water concentration in thechamber atmosphereusing a cold plasmasource connected to thechamber

    Manometric TemperatureMeasurement (MTM)

    Pressure Rise Testsare performedperiodically by rapidclosing (

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    Tunable Diode Laser Absorption Spectroscopy

    NIR-spectroscopic method for the determination of trace concentrations of a gasNo contact to the product

    Use in sterile processes (manufacturing) and in all scales of freeze dryers

    Eg: SMART TM freeze dryer

    www.tdlas.com ; Schneid, SP Industries Webinar, 2009

    Pressure Measurements

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    Spectroscopic Techniques

    Near infra-red: for residual moisture measurements in vials throughcontinuous measurements dur ing secondary drying

    Raman: for determination of physical product characteristi cs

    Only one vial monitoredfor research and development

    Near infra red/Raman Spectroscopy

    Brulls et al., 2003;Liu; Bai et al., 2005; Lin & Hsu, 2005, Schneid, SP Industries Webinar, 2009De Beer et al., 2007; Romero-Torres et al., 2007

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    Tools for Process DevelopmentFourier Transform Infra Red Spectroscopy Nuclear Magnet ic Resonance

    Determination of secondary structure anddynamics of proteins during f reeze-drying

    Kumar, et al., 2009; Bhuyan and Udgaonkar, 1999

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    Tools for Process DevelopmentFreeze-drying microscopy

    Lyostat TM

    Differential ScanningCalorimetery

    X-ray Diffraction

    Determination of crtical temperatures(Collapse/Eutectic) for opt imized

    process

    Determination of crystalline-amorphous transitions

    Taylor and Zhai, , ;Hatley and Franks, 1991; Pyne and Suryanarayanan, 2001

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    A Case Study

    Use of Near Infra-Red (NIR) to determine moisturecontent for Freeze-Drying Unit Operation

    Design

    Analyze Control

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    Design

    Noncontact probes buil t into the chamber through gaps made in the door of the freeze dryer chamber

    Placement of sensor depends upon measurement attr ibute: NIR for residual moisture content and cake quality placed at the bottomof the vial

    Calibration is set up with various levels of mois ture content of the productanalyzed with NIR. Calibration can be performed on-line or off-line andvalidation test samples are also run on the NIR instrument.

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    Analyze

    Principal Component Analysis (PCA) tocharacterize raw materials and processvariables

    Parti al Least Square (PLS) regression toinvestigate the linkages betweenspectral information and other sourcesof data. Sometimes done after pretreatment (2 nd derivative or normalization of spectral data)

    Build robust prediction model.Determine accuracy, precis ion, errors of

    calibration and prediction

    Y = f{x}+error

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    ControlFeed incoming data into the computer

    Pretreatment of data (if needed) done automatically by chemometric software

    Calculate observed Y and compare with expected Y

    Continuous feedback control is set

    If obtained Y is on target, no need to change operating parametersIf outside the range, operating parameters are adjusted

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    Drying Curve

    Drying time

    % w

    a t e r

    Design space

    Knowledge space

    Operating range

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    Summary

    Improve process control and deliver more consistentproduct quality and achieve higher operationalefficiency by use of PAT in biotech Freeze-dryingprocess

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    Questions?

    [email protected]