Solid Dosage Processing

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    Introduction to Solid Dosage

    Processing

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    Stages of pharmaceutical manufacturing

    API

    Excipients

    PrimaryPackaging

    SecondaryPackaging

    API FinishedProduct

    Starting Materials

    (Chemicals)

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    Drug product manufacture

    Dosage Form

    Wet

    granulation

    milling

    blending

    Fluid Bed Dryer

    lubrication

    tableting

    coating

    imprintingProcess combines the drug andexcipients into the dosage form

    ExcipientsAPI

    crystallization

    filtration

    oven drying

    Dry granulation

    / milling

    Directcompression

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    Solid dosage processing

    Dosage forms Quality factors

    xcipients

    Particle properties

    Processing routes !nit operations

    Size reduction "milling#

    $lending

    Dry granulation "roll compaction#

    Wet granulation Drying

    %ablet compaction

    &oating

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    Solid dosage forms

    'ral %ablets

    (ozenges

    &he)able tablets ffervescent tablets

    *ulti+layer tablets

    *odified release

    &apsules

    ,ard gelatin

    Soft gelatin

    Po)ders

    Inhaled -erosol

    *etered dose inhalers

    Dry po)der inhalers

    Singh. aini "0110#. Dosage 2orms3 on+Parenteral. ncyclopedia of Pharmaceutical %echnology

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    Quality factors for solid dosage forms

    Functional quality factors

    -Disintegrates to desired size 4uic5ly-%he constituent particle size of the dosage form should dissolve and beabsorbed in the 6I tract at a pre+determined rate

    Physical quality factors

    -*ust not brea5 up on processing. pac5aging. transportation. dispensingor handling-Surface of tablet or capsule must be free of defects-*ust be stable under anticipated environmental conditions-,ave the same )eight and composition for each tablet or capsule

    Sensorial quality factors

    -asy and pleasant to s)allo)

    2ung and g "0117#. -I&h 8ournal. 9:";#.

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    *odels at different scales

    Scale Subject Problems

    nterprise $usiness process Sourcing. contractmanufacturing. capacity planning

    Plant Process synthesis. simulation.development

    6eneration of processalternatives. process optimization

    4uipment 4uipment selection.performance. sizing. costing

    *ixing. classification.granulation. milling

    &ontinuum 2lo) and handling of po)ders 6ranular flo)

    Particle Particle attributes3 composition.size distribution. density.strength. shape

    Interparticle forces. brea5age

    *olecule nantiomers and polymorphs.material properties

    Polymorph prediction. predictionof physical and chemicalproperties

    g "0110#. Po)der %echnology.

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    Product and process functions

    Product function

    Product property3 &ontent uniformity. dissolution. flo)ability. dust

    formation Particle Properties3 Particle size. particle shape. surface

    characteristics

    Process function

    Process parameters3 %ype of unit operation. operational

    parameters

    Product property = F(particle properties, formulation)

    Particle properties = F(process parameters, raw material/intermediate properties)

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    Particle properties

    Potential Impact

    Processing $ehavior

    Product Quality 2actors

    Property 2lo) $lending Wetting Drying *echanical Dissolution Stability

    Particle Size > > > > > > >

    Surface -rea > > > > > > >

    Particle Shape >

    Surface nergy > > >

    $ul5 Density > > >

    Pore Size > > >

    Internal 2riction > >

    Wall 2riction > >

    ,ygroscopicity > > >

    ,lina5 et al. 8ournal of Pharmaceutical Innovation. < "011=#

    Product property = F(particleproperties, formulation)

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    *ean particle size and flo)ability

    $odhmage. -? "011=#? &orrelation bet)een physical properties and flo)ability indicators for fine po)ders? *S%hesis. Department of &hemical ngineering. !niversity of Sas5atche)an?

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    Size distributions for various po)ders

    $odhmage. -? "011=#? &orrelation bet)een physical properties and flo)ability indicators for fine po)ders? *S%hesis. Department of &hemical ngineering. !niversity of Sas5atche)an?

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    Po)der flo) and tablet )eight variations

    ,ancoc5. $runo "011@#? Dosage 2orm Specific %ests? Short course on *aterial Properties. Purdue !niversity?

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    xcipients

    %o aid in the processing of the drug delivery system during its

    manufactureA

    %o protect. support. or enhance stability. bioavailability or patient

    acceptabilityA

    %o assist in product identificationA %o enhance any other attribute of the overall safety. effectiveness. or

    delivery of the drug during storage or use?

    xcipients are substances. other than the active drugsubstance. or finished dosage form. that have been

    appropriately evaluated for safety and are included in

    drug delivery systems3

    !SP. 6eneral Information &hapter B

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    xcipient functions

    Component Function Examples

    2illers Increase size and )eight of finaldosage form

    *icrocrystallinecellulose. sucrose

    $inders Promote particle aggregation Pregelatinized starch.hydroxypropyl

    methylcelluloseDisintegrants Promote brea5 do)n of aggregates Sodium starch glycolate

    2lo) -ids Eeduce interaction bet)een particles %alc

    (ubricants Eeduce interactions bet)een particlesand surfaces of processing e4uipment

    *agnesium stearate

    Surfactants Promotes )etting Sodium lauryl sulfate.Polysorbate

    *odifiedEelease-gents

    Influences the release of active ,ydroxypropylmethylcellulose.Surelease.

    ,lina5 "011;#

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    *ost popular excipients

    *agnesium stearate "lubricant#

    (actose "compression aid#

    *icrocrystalline cellulose

    "compression aid#

    Starch "corn# "compression aid#

    Silicon dioxide "glidant# Stearic acid "lubricant#

    Sodium starch glycollate "disintegrant#

    6elatin "binder#

    %alc "film coating adFuvant. glidant#

    Sucrose "s)eetener. coating#

    &alcium stearate "lubricant#

    Povidone "binder#

    Pre+gelatinized starch "binder#

    ,ydroxypropylmethylcellulose "film

    coating. binder#

    'P- products "film coats and dyes#

    &rosscarmelose sodium "disintegrant#

    ,ydroxypropylcellulose "binder. film

    coating#

    thylcellulose "enteric coating#

    Dibasic calcium phosphate

    "compression aid#

    &rospovidone "disintegrant#

    Shellac and 6laze "coating agent#

    International pharmaceutical excipients council of the americas.

    http3//)))?ipecamericas?org/public/fa4s?html

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    Processing routes

    2ill die

    &oating. Pac5aging etc??

    &ompress %ablet

    Direct Compression

    DrugDiluent

    6lidant

    Disintegrant

    (ubricant

    Dry Granulation

    Disintegrant

    6lidant

    (ubricant

    DrugDiluent

    (ubricant

    *ixing

    &ompression

    &omminution

    Screening

    *ixing

    *ixing

    Wetting

    6ranulation

    Drying

    Screening

    *ixing

    DrugDiluent

    $inder

    Solvent

    Disintegrant

    6lidant

    (ubricant

    Wet Granulation

    ther !outes

    2luidized bed granulation

    xtrusion / rotary granulation

    "ablet

    Compression

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    !nit operations

    Process function

    Process parameters3 %ype of unit operation. operational parameters

    %ype of unit operation Size reduction "*illing#

    $lending

    Dry granulation "Eoll compaction#

    Wet granulation

    Drying

    %ablet compression

    &oating

    Particle properties = F(processparameters, feed/intermediate properties)

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    !nit operations

    Size reduction "milling#

    -dvantages and disadvantages

    2orces in milling

    *illing e4uipment "dry milling#

    *edia mills ")et milling#

    *ill selection

    nergy re4uirements

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    Particle size reduction

    *ixing is more uniform if ingredients are roughly the same size

    *illing of )et granules can promote uniform and efficient drying

    Increased surface area can improve dissolution rate and bioavailablity

    Improved content uniformity of dosage units

    xcessive heat generation can lead to degradation. change in

    polymorphic form

    Increase in surface energy can lead to agglomeration

    *ay result in excessive production of fines or overly broad particle

    size distribution

    $enefits

    Disadvantages

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    2orces in milling

    Shear "cutting forces#

    &ompression "crushing

    forces#

    Impact "high velocitycollision#

    6riffith theory % G %ensile stress

    H G Houngs modulus

    J G Surface energy

    c G fault length

    YT

    c

    =

    Eumpf "

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    *illing e4uipment K screen mills

    &ritical parameters for a conical screen mill Screen ,ole Size/Shape

    Impeller %ype

    Impeller &learance

    Speed

    valuate impact on aspirin granulation Particle size reduction

    *illing time and energy re4uirements

    'verall milling performance

    Milling Work Index = i!e reduction / Milling work

    Milling "ime Index = i!e reduction / Milling time

    $yers. Pec5 "

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    *illing e4uipment K screen mills

    Screen hole size has largest impact on particle size

    reduction. milling time and energy re4uirements

    *illing )or5 index significantly lo)er for smaller screenhole sizes

    Impeller type has largest effect on overall milling

    performance

    Impeller clearance not significant at small clearances *illing )or5 index lo)er at higher mill speeds

    Deflection of material a)ay from screens

    $yers. Pec5 "

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    *illing e4uipment K impact mills

    Significant )ear on surfaces

    ,ammer mills

    *edium to coarse size reduction

    Peripheral speed 01+;1 m/sec

    Pin mills

    Peripheral speed up to 011 m/sec &apable of fine grinding

    &an be used to mill stic5y materials

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    *illing e4uipment K Fet mill

    Superfine to colloid size reduction

    &an be used for heat sensitive products

    Different configurations Panca5e "spiral# Fet mill

    2ines exit from center

    (oop/oval Fet mill 2ines exit from top

    'pposing Fet mills Particles impact each other in opposing Fets

    2luidized bed Fet mill Particles are Fetted to)ards center "lo) )ear on e4uipment#

    2ixed/moving target Fet mills Particles impact on surface of target ")ear can be significant#

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    *illing e4uipment K stirred media mill

    &ritical parameters

    -gitator speed

    2eed rate

    Size of beads

    $ead charge

    Density of beads

    Design of blades *ill chamber

    Eesidence time

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    *ill selection

    Wibo)o and g "

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    nergy based analysis K ball mill

    *acroscale energy+size relationships "&hen et al?. 0119# &alculate specific energy for a given size reduction

    2unctional form derived from theoretical considerations

    Eittingers model

    nergy re4uired for particle size reduction is proportional to the area of ne)surface created

    Lic5s model nergy re4uired to brea5 a particle is proportional to the ratio of the particle

    volume before reduction to the volume after reduction

    &hen et al? "0119#. 8 Pharm Sci. :7"9#.

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    nergy based analysis K ball millLic5s (a),igh loading

    (o) fre4uencyEolling attrition

    Eittingers (a)(o) loading

    ,igh fre4uency

    Impact fragmentation

    1

    FP

    R

    xx

    k t=

    +

    exp( )p F Kx x k t=

    -ttrition

    2ragmentation

    Size Eeduction of MK(actose *onohydrate in a $all *ill

    &hen et al? "0119#. 8 Pharm Sci. :7"9#.

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    !nit operations

    $lending

    $lending e4uipment

    Impact of size difference

    Eadial vs axial mixing

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    $lending K convective mixingEibbon $lenders 'rbiting Scre) $lenders

    Planetary $lenders

    ,orizontal Double -rm $lenders

    2orberg $lenders

    Nertical ,igh Intensity *ixers

    ,orizontal ,igh Intensity *ixers

    Diffusion *ixers )ith Intensifier/-gitator

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    Size difference and mixing uniformity

    &ampbell and $auer "

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    *ixing in a bin blender K axial mixing

    Sudah et al? "0110#. Po)der %echnology.

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    *ixing in a bin blender K radial mixing

    Sudah et al? "0110#. Po)der %echnology.

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    !nit operations

    Dry granulation "roll compaction#

    &ritical parameters

    8ohansons theory

    2eed system Impact of granulation on flo) properties

    Wet granulation

    *onitoring li4uid addition Drying

    2luidised bed dryer

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    Eoll compaction

    &ritical parameters Eoll speed and pressure

    ,orizontal and vertical

    feed speed. deaeration

    Eoll diameter and

    surface

    -dvantages Improve po)der flo)

    Eeduce segregation

    potential

    o moisture addition.

    drying

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    8ohansons theory

    Slip Eegion

    ip Eegion

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    8ohansons theory

    Slip region

    ip region

    Hu et al? "01

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    8ohansons theory K nip angle

    $indhumadhavan et al? "011;#. &hem ng Sci. =1"

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    8ohansons theory + stress profile

    $indhumadhavan et al? "011;#. &hem ng Sci. =1"

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    ff? angle of friction and pea5 pressure

    "8ohansons theory#

    ff? -ngle of

    2riction

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    ff? angle of friction and nip angle

    "8ohansons theory#

    ff? -ngle of

    2riction

    ip -ngle

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    ffect of lubrication on friction properties

    Hu et al? "01

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    ffect of lubrication on pea5 roll pressure

    Hu et al? "01

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    ffect of lubrication on nip angle

    Hu et al? "01

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    2alzone et al? "

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    Impact of feed and roll speed on granule properties

    *ean particle

    size

    ,ydrous (actose

    ,

    ,2alzone et al? "

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    ffect of entrained air on feeding and discharging

    8ohanson "

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    &haracterization of flo)ability

    ,ausner ratio G tapped density / bul5 density xcellent

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    Eoll compaction and flo) properties

    Soares et al? "011;#.Dry granulation and compression of spray dried plant extracts. --PSPharmSci%ech

    $efore

    &ompaction

    "poor#

    -fter

    &ompaction

    "excellent#

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    ,igh shear )et granulation

    -dvantages Improve flo)

    Improve uniformity Increase bul5 density

    nhance resistance to

    segregation

    &ritical parameters -mount of binder

    Eate of addition %ime of granulation

    Speed

    Mixer Blade

    Bowl

    Chopper Blade

    Discharge

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    Wet granulation K monitoring li4uid addition

    8orgensen et al? "0119#. 8 Pharm Sci. :7":#. 0070+0097

    "-# 1?09 ml/g

    Impeller %or4ue for MK(actose *onohydrate/*&& granulation

    " 1?9@ ml/g

    agglomeration

    "$# 1?7= ml/g

    nucleation

    "D# 1?;7 ml/g

    agglomerate gro)th

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    Wet granulation K monitoring li4uid addition

    8orgensen et al? "0119#. 8 Pharm Sci. :7":#. 0070+0097

    "-# 1?09 ml/g

    "< min#

    S* of MK(actose *onohydrate/*&& granules

    " 1?9@ ml/g

    "0 min#

    agglomeration

    "$# 1?7= ml/g

    "

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    2luid bed drying

    Air Flow

    Inlet FilterCondensorSteamDamper

    Damper Outlet Filter

    Air Flow

    Product

    Temperature

    Inlet

    Temperature

    OutletTemperature

    From

    ranulator

    To !ill

    Dr"in# $one

    Filter %a#

    Air Flow

    &etainin#

    Screein

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    !nit operations

    %ablet compaction

    Eelative density and compaction pressure

    &oating 'bFectives

    &ritical parameters

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    Eotary tablet press

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    Eelative density changes in manufacture of tablets

    ,ancoc5 et al? "0119#. Pharm %ech. -pril 0117. =9+C1

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    4uivalence of tablets made )ith different presses

    ,ancoc5 et al? "0119#. Pharm %ech. -pril 0117. =9+C1

    P ti

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    Pan coating

    $enefits

    *as5 taste &hemical barrier

    &ontrolled release

    -ppearance

    &ritical Parameters

    -ir flo) Spray

    Drum dynamics Eotational speed

    2ill fraction

    Air'!oisture

    Dr" Air

    &otation

    %a((le

    Spra" )o**le

    Air Flow

    Inlet FilterSteamInlet

    Temperature

    Inlet Air

    Outlet AirOutlet Filter

    Outlet

    Temperature

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    Eeferences

    "#eory and Practice of Industrial P#armacy. (?(achman et al? "eds# "