chromatography oct 2014
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Pharmaceu)calProcessDevelopment
Chromatography
DepartmentofChemicalEngineeringandChemicalTechnology
RichardEsco<,2014
Slide 2
PharmaceuticalProcess
DevelopmentChromatography
Content– History&Background– Types
• HPLC&uHPLC– Normalphase– ReversedPhase– Prepara)ve– SimulatedMovingBed– IonExchange– SizeExclusion
• GC– Packed– Capillary
• SuperCri)calFluid• ThinLayer• CapillaryElectrophoresis• Chiral
• Toillustratetherangeandscopeofthetechniques,instrumenta)onandapplica)ons.• Provideanapprecia)onoftheadvantagesandlimita)onsforuse‐op)misa)on.• TounderstandthesynergieswithengineeringprinciplesforTheore)calPlatesandScale‐up.
LectureAims:
Slide 3
PharmaceuticalProcess
DevelopmentChromatography‐HistoryTowritewithcolours‐literallytranslatedfromitsGreekrootschromaandgraphein.
1903‐ChromatographywasfirstdevelopedbytheRussianbotanistMikhailTswe<‐heproducedasepara)onofplantpigmentsusingacolumnofcalciumcarbonate
1927‐DrHeinrichWieland(NobelLaureate)“Uptonowwehavelearnedwithmuchefforttodis)ll,crystalliseandrecrystallise,andnowtheycomealongandjustpourthestuffthroughatube!”
1938‐IzmailovandShraiberimplementedTLC
1941‐ArcherJohnPorterMar)nandRichardLaurenceMillingtonSyngedevelopedliquid‐liquidpar))onchromatographysepara)ngvariousaminoacids
1944‐AJPMar)ncreatedpaperchromatography
1947‐FritzPriorandErikaCremerseparatedoxygen&carbondioxide‐gaschromatography
1952‐AJPMar)ndevelopedGas‐Liquidchromatography(NobelPrize)
1956‐J.J.VanDeemterintroducedtheequa)onwhichshowsthedependenceofthetheore)calplateheight(HETP)onthemobilephaselinearvelocity.OriginallyintroducedforGC,butithappensthatthesamephysicalprocessesoccursinHPLC.
1960‐JohnKnox(Edinburgh)introducedIon‐pairchromatography,reducedparametersandporousgraphi)ccarbon.
1963‐JCGiddingsusedsilicagelofsmallspecifiedpar)clestoachievehighresolu)onandspeed.
1966‐Hovarthcoined“HPLC”
1972‐Chemicallymodifiedsta)onaryphases(reversedphase)wereprepared
1973‐Merckintroducedsphericalpar)cles
Slide 4
PharmaceuticalProcess
DevelopmentChromatography‐Types
Thebasisofalltypesofchromatographyisthepar))onofthesamplecompoundsbetweenasta)onaryphaseandamobilephasewhichflowsoverand/orthroughthesta)onaryphase.Differentmechanismsfromdifferentcombina)onsofgaseous,solidorliquidphasesgiverisetothemaintypesofchromatography
•Adsorp)on•Par))on•IonExchange•SizeExclusion
Slide 5
PharmaceuticalProcess
DevelopmentChromatography‐Types
• Adsorp'onChromatographyusesasolidsta)onaryphaseeg,silicagel,ac)vatedcarbonandaliquidorgaseousmobilephase.Solutesareseparatedaccordingtotheirdifferentadsorp)oncharacteris)csontothesta)onaryphase.
• Par''onChromatographyisbasedonathinfilmformedonthesurfaceofasolidsupportbyaliquidsta)onaryphase.Solutesequilibratebetweenthemobilephaseandthesta)onaryliquidphase.
• IonExchangeChromatographyaresin(thesta)onarysolidphase)isusedtocovalentlya<achanionsorca)onsontoit.Soluteionsoftheoppositechargeinthemobileliquidphasearea<ractedtotheresinbyelectrosta)cforces.
• MolecularorSizeExclusionChromatographyalsoknownasgelpermea)onorgelfiltra)on,thistypeofchromatographylacksanya<rac)veinterac)onbetweenthesta)onaryphaseandsolute.Theliquidorgaseousphasepassesthroughaporousgelwhichseparatesthemoleculesaccordingtotheirsize.Thesmallporesexcludethelargersolutemolecules,butallowsmallermoleculestoenterthegel,causingthemtoberetained.Thiscausesthelargermoleculestopassthroughthecolumnatafasterratethanthesmallerones.
Slide 6
PharmaceuticalProcess
DevelopmentChromatography‐Techniques
• HPLC&uHPLC– Normalphase(Polarsta)onaryphase&non‐polarmobilephase)
– ReversedPhase(Non‐polarsta)onaryphase&polarmobilephase)
– Prepara)ve(Columndiametersof2cm‐1m)
– SimulatedMovingBed(con)nuouscountercurrentchromatography)
– IonExchange(polymerphaseswhichexchangeionswithsolutes)
– SizeExclusion(eghighlycrosslinkedpolymethacrylatecolumns)
• GC– Packed(Carbowax‐PEG,Chromosorb‐diatomaceousearth)
– Capillary(CoatedegPEGorsiloxanes)• SuperCri)calFluid(Normalphasewithsupercri)calCO2+egMeOH)
• ThinLayer(sta)onaryphaseiscoatedonasolidsupportegglass)• CapillaryElectrophoresis(separatesionsbasedontheirelectrophore)cmobility
withtheuseofanappliedvoltage)
• Chiral(thesta)onaryphasecontainsasingleenan)omerofachiralcompound)
Slide 7
PharmaceuticalProcess
DevelopmentReversedPhase
• Thetechniqueofusingalkylchainscovalentlybondedtothesolidsupportcreatesahydrophobicsta)onaryphase,whichhasastrongeraffinityforhydrophobiccompounds.Theuseofahydrophobicsta)onaryphasecanbeconsideredtheopposite,or"reverse",ofnormalphasechromatography‐hencetheterm"reversedphasechromatography”
• Alkyl(R)bondedphasesaresilicabasedandarepreparedbyreac)ngthehydroxylgroupsonthesurfaceofthesilicawithorganicsilylchloridesorsilylesters.Anyremainingunreactedsilanolgroupsareblockedbysubsequentmethyla)onwithegtrimethylsilazane.
• Themostpopularcolumnisanoctadecylcarbonchain(C18)bondedsilica.ThisisfollowedbyC8bondedsilica,puresilica,cyanobondedsilicaandphenylbondedsilica.
• NotethatnotallC18columnshaveiden)calreten)onproper)es.Surfacefunc)onalisa)onofsilicacanbeperformedinamonomericorapolymericreac)onwithdifferentshort‐chainorganosilanesusedinasecondsteptocoverremainingsilanolgroups(end‐capping).Whiletheoverallreten)onmechanismremainsthesame,subtledifferencesinthesurfacechemistriesofdifferentsta)onaryphaseswillleadtochangesinselec)vity.
• Commonapplica)onsinclude:Materialpurityassessment,reac)onmonitoring,purifica)on,iden)fica)onofimpuri)es,andqualitycontrol.
Slide 8
PharmaceuticalProcess
DevelopmentInstrumenta)on‐HPLC
Agilent 1200
Slide 9
PharmaceuticalProcess
DevelopmentInstrumenta)on‐GC
Slide 10
PharmaceuticalProcess
DevelopmentExampleApplica)onGCSepara)onof3,4,5‐TrimethoxybenzaldehydeandImpuri)es
Column:25metres;,0.3mmIDfusedsilica,0.14umOV‐1701
Temperature:130oCisothermal
Slide 11
PharmaceuticalProcess
DevelopmentExampleApplica)on
GCSepara)onStandardMixtureofReferenceMaterialsusingFIDdetec)on
Slide 12
PharmaceuticalProcess
DevelopmentExampleApplica)onGCSepara)onofInsec)cidePermethrin
Slide 13
PharmaceuticalProcess
DevelopmentExampleApplica)onGCSepara)onofPharmaceu)calRawMaterialandIntermediates
Column:OV‐7Detector:FIDTemperature:180oCto270oC
andE/Zisomersof
Slide 14
PharmaceuticalProcess
DevelopmentExampleApplica)onGCSepara)onofOilofSassafras
Column:25meterby0.3mmIDfusedsilica, 0.14umpolyethyleneglycol20M
Temperature:60oCfor4mins,5OCperminto180oC
Detector:FID
Thisfragrantoilisdis)lledfromtherootbarkisextensivelyusedinthemanufactureofthecoarserkindsofperfume,andforscen)ngthecheapergradesofsoap.Theoilusedinperfumesisalsoextractedfromthefruits
Slide 15
PharmaceuticalProcess
DevelopmentExampleApplica)onGCSepara)onPolychlorinatedBiphenyls‐PCBs
100ppmofAroclor1015and1260
Column:OV‐73
Temperature:60oCto275oC
Detector:ElectronCapture
PCBswerewidelyusedasdielectricandcoolantfluids,forexampleintransformers,capacitors,andelectricmotorss
Slide 16
PharmaceuticalProcess
DevelopmentSimulatedMovingBed
Slide 17
PharmaceuticalProcess
DevelopmentCESimula)on
Slide 18
PharmaceuticalProcess
Development
• Many commercial instruments now perform both supercritical fluid chromatography and ultra high-performance/pressure liquid chromatography (uHPLC).
• This provides two orthogonal techniques and higher component selectivity.
• With operating pressures up to 600 bar (9000 psi) capability small particle HPLC and SFC can be used.
• Using gaseous CO2 as the mobile phase makes interfacing with mass spectrometers relatively straight forward.
Instrumenta)on‐SFC
Slide 19
PharmaceuticalProcess
Development
Slide 20
PharmaceuticalProcess
Development
• Theore)calAspects
– Efficiency‐reducedparametersandVanDeemterplots
– Resolu)on‐Theore)calPlates
– ColumnLoadingsandcycle)mes.
• Detectors
– FID,TCD,UV‐DA,MS,ECD,Fluorescence
• Quan)ta)on/Calibra)ons– ResponseFactors
– Rela)veResponseFactors
– InternalStandards
– StandardAddi)on
– Prepara)veScale‐up
H = A + B/u + Cu
h = H
dp
v =udp
Dm
Theore)calAspects
Slide 21
PharmaceuticalProcess
DevelopmentTheore)calAspectsReten)on
Compoundswillspendsome)meinthesta)onaryphase,andsome)meinthemobilephase.The)mespentbyanindividualmoleculeineachofthe2phasesiscalledthecapacityorreten)onfactork.Thera)oof)mespentinthe2phasesisequaltothera)oofthemassofthecompoundsinthe2phases.
k=)mespentinthesta)onaryphase=massinthesta)onaryphase)mespentinthemobilephase massinthemobilephase
Thera)ooftheconcentra)onofacompoundinthe2phasesiscalledthepar))oncoefficient(K)
K = molar concentration in the stationary phase
molar concentration in the mobile phase
ThefactorskandKarerelatedtoeachotherbasedonanotherparametercalledthephasera)oβ.
β = volumeofmobilephase volumeofsta)onaryphase k = K/βand
Whichshowsthatthemassra)oisafunc)onoftheconcentra)oninthetwophasesandtherela)vevolumeofthetwophases
Slide 22
PharmaceuticalProcess
DevelopmentTheore)calAspectsReten)on
The)meittakesforacompoundtotravelthroughthecolumn(fromwhenananalyteisinjectedtowhenitreachesthedetector)isknownasthereten'on'me(tr).Ifacompoundisnotretainedatall,itwills)lltake)metotravelthroughthecolumn.Therefore,inordertomakearela)onshipbetweenkandreten)on)me,anadjustmentmustbemadeforthistravel)me.
The)meittakesforanunretainedcompoundtotravelthroughthecolumnisouenknownasthedead'me(to).
Usingthedead)me,thereten)onfactor(k)foracompoundcanberelatedtothereten)on)me.
k = (tr – to)/ to Wheretr=thereten)on)meofthecompound,andto=thedead)me
Selec)vityα α =k2
k1
Slide 23
PharmaceuticalProcess
Development
Alsoknownascolumnefficiency,thenumberoftheore)calplatesisamathema)calconceptanditisanindirectmeasureofpeakwidthforapeakataspecificreten)on)me.
Theore)calAspectsNumberofTheore)calPlates(N)
N = 5.54 tR
wh
2
N=numberoftheore)calplatestr=reten)on)mewh=peakwidthathalfheight()me)
Acolumnwithahighnumberoftheore)calplateswillhaveanarrowerpeakatagivenreten)on)methanacolumnwithalowerNnumber.
Highcolumnefficiencyisbeneficialsincelesspeaksepara)on(meaningloweralpha,α‐selec)vity)isrequiredtocompletelyresolvecomponents.Onsta)onaryphaseswherethealphas(α)aresmall,more efficient columns are needed. Column efficiency is a func)on of the column dimensions(diameter, length and film thickness), the type of carrier gas and its flow rate or average linearvelocity, and the compound and its reten)on. For column comparison purposes, the number oftheore)calplatespermeter(N/m)isouenused.
Slide 24
PharmaceuticalProcess
Development
Anothermeasureofcolumnefficiencyistheheightequivalenttoatheore)calplate‐Handusuallyreportedinmillimeters.Theshortereachtheore)calplate,themoreplatesare"contained"inanylengthofcolumn.This,ofcourse,translatestomoreplatespermeterandahighercolumnefficiency.
Theore)calAspectsHeightEquivalenttoaTheore)calPlate(H)
H = L
N
N=numberoftheore)calplatesL =Lengthofcolumn(mm)
Slide 25
PharmaceuticalProcess
Development
Thehighertheresolu)on,thelesstheoverlapbetweentwopeaks.Separa)onisonlythedistanceor)mebetweentwopeakmaxima(alpha,α).Resolu)ontakesintoconsidera)onbothalpha(α)andthewidthofthepeaks.Itiscalculatedusingeitheroftheequa)onsbelow.Baselineresolu)onusuallyoccursatresolu)onnumberof1.50;however,thereisnovisiblebaselinebetweenthetwopeaks.Numbersgreaterthan1.50indicatethereisbaselinebetweenthepeaksandnumberslessthan1.50indicatethereissomedegreeofco‐elu)on.
Theore)calAspectsResolu)on‐R
R = 1.18 t
R2 - t
R1
wh1
+ wh2
R = 2 t
R2 - t
R1
wb1
+ wb2
tR1 = retention time of first peaktR2 = retention time of second peakWh1 = peak width at half height of first peak (time)Wh2 = peak width at half height of second peak (time)Wb1 = peak width at base pf first peak (time)Wb2 = peak width at base of second peak (time)
Slide 26
PharmaceuticalProcess
DevelopmentResolu)onandEfficiency
Resolu)onisrelatedtothesepara)onorcolumnefficiencyandalsotheselec)vity(α).
Theeffectofchangingtheseparameterscanbeeasilyassessedusingtheequa)on:
k2 = retention factor of second peak
Selec)vity α =k2
k1
R = N
4
- 1
k2
k2 + 1
α
α
Slide 27
PharmaceuticalProcess
DevelopmentExample1
2 3
)me tR1 tR2 tR3
N = 5.54 tR
wh
2
t0
Wh1
Wh2
Wh3
Average N = 6931
(104) (146) (152)
(3.7)
(3.7)
(4.0)
(61.5)
N1 = 5.54
104
3.7
2
= 4377
N2 = 5.54
146
3.7
2
= 8626
N3 = 5.54
152
4.0
2
= 7791
Slide 28
PharmaceuticalProcess
DevelopmentExample1
2 3
t0
)me tR1 tR2 tR3
Wh1
Wh2
Wh3
(104) (146) (152)
(3.7)
(3.7)
(4.0)
R = 1.18 t
R3 - t
R2
wh3
+ wh2
R = 1.18 152 - 146
4.0 + 3.7
=0.78
(61.5)
Slide 29
PharmaceuticalProcess
DevelopmentExample1
2 3
t0
)me tR1 tR2 tR3
Wh1
Wh2
Wh3
(104) (146) (152)
(3.7)
(3.7)
(4.0)
(61.5)
α
1.47
1.37
= 1.07=
k2
= 152 - 61.5
61.5
= 1.47
R = 6921
4 1.07 - 1
1.07
1.47
1.47 + 1
=0.80
α =k2
k1
R = N
4
- 1
k2
k2 + 1
α
α
k1
= 146 - 61.5
61.5
= 1.37
Slide 30
PharmaceuticalProcess
DevelopmentExample1
2 3
t0
)me tR1 tR2 tR3
Wh1
Wh2
Wh3
(104) (146) (152)
(3.7)
(3.7)
(4.0)
(61.5)
=1.5forbaselineresolu)on
1.5 = N
4 1.07 - 1
1.07
1.47
1.47 + 1
N = 24,068
R = N
4
- 1
k2
k2 + 1
α
α
Slide 31
PharmaceuticalProcess
DevelopmentTheore)calAspectsVanDeemterrela)onship
H = L
N
ThevalueofHdependsprimarilyonfourfactors,1)thevelocityofthemobilephase,2)mul)pathdiffusion,3)thediffusionofthecompoundinthemobilephase,and4)thetransferofthecompoundbetweenthesta)onaryphaseandthemobilephase.Forcolumnspackedwithpar)cles(HPLCcolumns),thesefactorscanbeexpressedbythefollowingformula
H = A + B/u + (Cs + Cm) u
u is the average linear mobile phase velocity,A is a constant expressing diffusion due to non uniformity of the packing.B is a constant expressing the longitudinal diffusion coefficient in the mobile phaseCs is the mass transfer term in the stationary phaseCm is the mass transfer term in the mobile phase
Slide 32
PharmaceuticalProcess
Development
TheATerm
Inpackedcolumns,peak‐broadeningistheresultofanumberoffactors.Asmoleculesoftheanalytemovethroughthecolumn,theytakemanydifferentpathsaroundthepackedpar)cles.Someofthesepathsareundoubtedlylongerthanotherssoasthemoleculesmovethroughthecolumn,theytendtospreadout.Theamountofspreadingisaffectedbythenatureofthecolumnmaterialandhowwellthecolumnispacked.Thisfactorisgenerallypropor)onaltothepar)clesizeofthepackingmaterial.Thisfactormustbetakenintoaccountforpackedcolumns,butforcapillarycolumns,thistermisnotneededsincetherearenopar)cles
12
Flow
Direction
Pathways of two molecules
during elution. Distance traveled
by molecule 1 is longer than
that traveled by molecule 2, thus
molecule 1 will take longer to
elute.
Theore)calAspects
Slide 33
PharmaceuticalProcess
DevelopmentTheore)calAspects
TheLongitudinalDiffusionTermB/u
Longitudinaldiffusionalsocontributestopeakbroadening.Inthisprocess,analytesdiffusefromareasofhighconcentra)ontomorediluteareainfrontofandbehindthemovingband.Thedegreeoflongitudinaldiffusionisreducedtosomeextentbythepackingmaterial.Atlowveloci)eslongitudinaldiffusionhasanega)veeffectonresolu)on,butthiseffectisnegligibleathigherveloci)es.Thistermisveryimportantingaschromatographyasdiffusioncoefficientsingassesareordersofmagnitudehigherthaninliquids.Inliquidchromatography,thistermistypicallyclosetozerorela)vetotheotherterms.
TheMassTransferTermsCu.
Themasstransfertermrelatestothefactthatequilibriumbetweenthemobileandsta)onaryphasesisneverrealisedinachromatographycolumn.Ittakes)meforanalytesinthemobilephasetomoveintothesta)onaryphase.Becausenoequilibriumisreached,someoftheanalytesaresweptaheadoftheofthemainband.Italsotakes)meformoleculestomoveoutofthesta)onaryphase,andsomeoftheanalytesmoleculeswillbeleubehindbytherapidlymovingmobilephase.Likethelongitudinalterm,themasstransfertermisbasedondiffusion.However,longitudinaldiffusiontakesplaceparalleltothedirec)onofflow,andthereforeisinverselyrelatedtothemobilephaseflowrate,whilemasstransferdiffusiontakesplaceperpendiculartotheflowrate.Asaconsequence,thefasterthemobilephasemoves,theless)methereisforequilibriumbetweenthephasesandthemasstransfereffectonpeakbroadeningisdirectlyrelatedtomobilephasevelocity.
Slide 34
PharmaceuticalProcess
Development
Forhighresolu)on,thesediffusionfactorsshouldbeminimized(plateheightshouldbesmall).Thereisamop)mumatminimumH.TheVanDeemterplotshowsthattheeffectofthevariousband‐broadeningparametersonplateheight.Peakbroadeningduetomul)pathdiffusionisrela)velyconstantoverthenormalrangeofmobilephaseveloci)es,whilepeakbroadeningduetomobilephasemasstransferincreaseswithmobilephasevelocity.Onthecontrary,peakbroadeningduetolongitudinaldiffusionishighatlowveloci)esandhasalessereffectasmobilephasevelocityincreases.Theoveralleffectisthatthereisanintermediatevelocitythatyieldsthesmallestplateheightandhencethehighestresolu)on.However,intheinterestofspeedofanalysis,recommendedveloci)esareouensetsomewhathigherthatthis.
Linear Velocity, u
Pla
te H
eig
ht,
H
Multipath Term, A
Mass Transfer (both), Cu
Longitudinal diffusion, B/u
A + B/u + Cu
Theore)calAspects
Slide 35
PharmaceuticalProcess
Development
Decreasingpar)clesizehasbeenobservedtolimittheeffectofflowrateonpeakefficiencysmallerpar)cleshaveshorterdiffusionpathlengths,allowingasolutetotravelinandoutofthepar)clefaster.Thereforetheanalytespendsless)meinsidethepar)clewherepeakdiffusioncanoccur.No)cethatasthepar)clesizedecreases,thecurvebecomesfla<er,orlessaffectedbyhighercolumnflowrates.Smallerpar)clesizesyieldbe<eroverallefficiencies,orlesspeakdispersion,acrossamuchwiderrangeofusableflowrates,butmuchhigherbackpressures
Theore)calAspects
Slide 36
PharmaceuticalProcess
DevelopmentTheore)calAspectsGiddingsintroduceddimensionlessparametersforHandalsoforthelinearvelocityu.Dimensionlessparametersallowthedirectcomparisonoftheefficiencydifferentcolumnspackedwithdifferentpar)clesizepackingmaterials.Accordingtothetheory,awellpackedcolumnshouldhaveareducedplateheight(h)intherangeof2‐3atareducedvelocity(v)ofabout3.
ReducedmobilephasevelocityvAdimensionlessmeasureofthemobilephasevelocitycomparedtodiffusionintothepores.
h = H
dp
v =udp
Dm
H=heightequivalentofatheore)calplate(µm)dp=meanpar)clesize(µm)
u=linearvelocityofthemobilephasedp =par)clediameterDM=diffusioncoefficientofthesoluteinthemobilephase.
Withtheseparameters,anempiricalformoftheVanDeemterequa)onwasderivedbyProfJohnKnox(Edinburgh,1960)
h = B
v+ Av
1/ 3 + Cvh = 2
Slide 37
PharmaceuticalProcess
Development
Slide 38
PharmaceuticalProcess
Development
GCThermalConduc/vityDetector(TCD)
TheTCDisatrulyuniversaldetector.Itconsistsofaheatedsensorinathermostatedchamber,throughwhichtheeffluentflows.Heliumisusuallyusedasacarriergas,asithasthehighestthermalconduc)vityofanygas,exceptforhydrogen.Asthepeakselute,thethermalconduc)vityofthegasinthechamberchanges.Thischangestheheatflowfromtheheatedsensor,throughthegas,tothewalls.Sincethesensorisbeingheatedataconstantrate,itbecomesho<erasthethermalconduc)vityoftheeffluentdrops.Thechangeintemperatureofthesensingwirefilamentorthermistorchangesitsresistance.
Thedetectorislimitedbyitsrela)velylowsensi)vity,comparedtootherdetectors,andusuallyhasafairlylargedeadvolume.Itis,therefore,notverysuitableforcapillarywork.
Detectors
Slide 39
PharmaceuticalProcess
Development
GCFlameIoniza/onDetector(FID)
TheFIDisnearlyuniversallysensi)vetoorganiccompounds,andshowsgoodsensi)vityandexcellentlinearity.Thecolumneffluentisfedintoaflamefueledbyhydrogen,withaforcedairflow.Apoten)alofseveralhundredvoltsisimposedbetweenthe)poftheflameburnerandthecollectorwhichsurroundstheflame.Asthesamplecomponentsburn,theyproduceaburstofions.Theseproducea)nycurrentbetweentheflame)pandthecollector.
TheFIDdetectorhasanumberofadvantages.Theresponseisroughlypropor)onaltothenumberofcarbonatomsintheflameatany)me.Thedetectorisinsensi)vetoinorganicgases,water,carbondioxide,sulfurdioxide,nitrogenoxidesandothernon‐combus)blegases.Thedetectorhasaverywidelinearrange,overabout7ordersofmagnitude,hasalowdeadvolumeofabout1ml.
Detectors
Slide 40
PharmaceuticalProcess
Development
Ultraviolet(UV)detectorsarefairlygeneralinapplica)on,sincemostorganiccompoundsabsorbatsomewavelengthsintheUVspectrum.However,theuseofwavelengthsbelow210nmisusuallynotuseableforanalysisbecausemostsolventswhichwouldbeusedaseluentswouldalsoabsorbintheseareas.TheresponseofthisdetectordependsonBeer'sLaw,andthereforegivesalinearresponseover4‐5ordersofmagnitude.Thedetec)onlimitsvarywidely,dependingonthesamplecomponentanditsex)nc)oncoefficientatthewavelengthbeingused.Inthemostfavorablecases,1ngorlessofacompoundmaybedetected.
DetectorsHPLC
Othercommonlyuseddetectorsinclude
Refrac)veIndexFluorescenceElectrochemicalMassSpec
Slide 41
PharmaceuticalProcess
DevelopmentQuan)ta)onData from chromatograms may be used to obtain the relative or absolute concentration of components in amixture, providing good resolution is achieved. The Peak area, from integration of the detector signal duringelution of a component, is proportional to the amount of that component in the sample. However, the responseof a detector varies from one compound to another; for example, the HPLC ultraviolet detector depends onabsorption of electromagnetic radiation, the spectra of the components and the detection wavelength used.
There are four principal methods for obtaining quantitative information:
1. Normalising peak areas2. Internal standards3. External standards4. Standard addition methods.
1. Normalising peak areas is simply the area of an individual peak calculated as a percentage of the total areasrecorded for all peaks in the chromatogram.
Slide 42
PharmaceuticalProcess
DevelopmentQuan)ta)on2. The internal standard method is a variation on the above, and is recommended for accurate quantitative work.
It eliminates the need for accurate injections since a reference standard is included in each sample analysed.An internal standard is selected which has a retention time such that it is eluted in a suitable 'gap' in thechromatogram.
The procedure involves analysing a test mixture sample containing known amounts of each component plus apredetermined amount of the internal standard (I.S.) to calculate the Response factor RF.
RF=((Ax)(Cis))/((Ais)(Cx))
Where:Ax=AreaofthecompoundofinterestCx=Concentra)onofthecompoundAis=AreaoftheinternalstandardCis=Concentra)onoftheinternalstandard
Oncetheresponsefactorisknown,analysisofanunknownmixtureisachievedbyaddinganaccuratelyknownamountofinternalstandardandthencarryingoutthechromatography.The concentration of each component iscalculated using the equation above, rearranged to give
Cx=(Ax/AIS)x(CIS/RF)
Slide 43
PharmaceuticalProcess
Development
3. External Standard Method
Automated sample injection systems and multiport injection valves(HPLC) have good reproducibility so that a series of injections can bemade with a variation in sample volume of < 1 %. A set of standardmixtures containing known concentrations of the analytes is analysedand their peak areas recorded. A calibration graph of area versusconcentration can be drawn for each analyte to confirm a linear detectorresponse and from which the amount of the analyte in a mixture can bedetermined
Quan)ta)on
Concentra)on
4.StandardAddi'on.Thestandardsolu)on(solu)onofknownconcentra)onofanalyte)isaddedtotheunknownsolu)on.Atypicalprocedureinvolvespreparingseveralsolu)onscontainingthesameamountofunknown,butdifferentamountsofstandard.Forexample,five25mLvolumetricflasksareeachfilledwith10mLoftheunknown.Thenthestandardisaddedindifferingamounts,suchas0,1,2,3,and4mL.Theflasksarethendilutedtothemarkandmixedwell.
Theideaofthisprocedureisthatthetotalconcentra)onoftheanalyteisthecombina)onoftheunknownandthestandard,andthatthetotalconcentra)onvarieslinearly.Ifthesignalresponseislinearinthisconcentra)onrange,thenaplotsimilartothatshownisgenerated
Slide 44
PharmaceuticalProcess
DevelopmentScale‐up
Onceadesiredanaly)calsepara)onhasbeenachieved,aloadingstudyisouenperformedtodeterminethecapacityofthepackingmaterialandthescale‐upfactorcalculated:
Scale - up factor = Diameter Prep( )2
X Length Prep
Diameter Analytical( )2 X Length Analytical
Thisfactorisusedtocalculatetheprepara)vecolumnloading,egforcolumnsofthesamelengthbutwith3.9and19mmIDa24mgloadingcanbeusedfroma1mganaly)calloading
Theequivalentflowraterequiredforthesamelinearvelocityiscalculatedfrom:
Flow Rate Prep( ) = Flow Rate Anal( ) X Diameter Prep( )2
Diameter Anal( )2
Slide 45
PharmaceuticalProcess
DevelopmentScale‐upPrepara)vechromatographyisgenerallycarriedoutundermassand/orvolumeoverloadedcondi)onsinordertoincreasetheproductthroughput.Involumeoverloading,thesampleconcentra)onismaintainedinthelinearregionoftheisothermandthevolumeisincreasedun)lthethroughputisop)mized.Inmassoverloading,thesampleconcentra)onisincreasedbeyondthelinearadsorp)onregion,resul)nginasymmetricbandprofiles,withself‐sharpeningfrontsandtailingrearboundaries.Acombina)onofvolumeandmassoverloadingiscommonlyusedtomaximisethroughputinprepara)veelu)onchromatography.
Slide 46
PharmaceuticalProcess
DevelopmentChromatography
• Tounderstandthebasicprinciplesofthedifferentmajortypesofcommonlyusedchromatographictechniquesandhowtoassesschromatographicperformance.
• Tobeabletoapplytheore)calconsidera)onstoprac)calexamples,forexample– Useandselec)onofquan)ta)veprocedures.– Scale‐updecisionsandprocedures.
LearningOutcomes
ExampleQues)ons:
• ExplaintheA,BandCtermsoftheVanDeemterequa)onandhowyoucancomparetheperformanceofdifferentHPLCcolumnspackedwithdifferentpar)clesizematerialswiththeore)calvalues.
• Foragivensepara)oncharacterisethechromatographicperformanceintermsofN,Rsanda.
• Describehowyouwouldcalculatetherela)veresponsefactorforcomponentB.• Inscalingupthesepara)onfroman4.5mmidanaly)caltoa76.2mmid
prepara)vecolumn;fromthegivendatawhatflowratewouldyouuse;b)whatsamplemass/columnloadingwouldyouuse?
FurtherReadingsugges)ons:
PRINCIPLESANDPRACTICEOFCHROMATOGRAPHY,RaymondP.W.Sco<,Chrom‐EdBookSeries‐on‐lineIntroduc)ontoModernLiquidChromatography,LloydR.Snyder,JosephJ.KirklandandJohnW.Dolan
Slide 47
PharmaceuticalProcess
Development
• Semba BioSciences
Acknowledgement
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