The trend in the biopharmaceutical industry is changing from batch process to continuous process. For continuous biomanufacturing, traceability of the material is required by regulatory authorities.
Trang 1Journal of Chromatography A 1683 (2022) 463530
ContentslistsavailableatScienceDirect
journalhomepage:www.elsevier.com/locate/chroma
Narges Lalia,b, Peter Satzera,b, Alois Jungbauera,b,∗
a ACIB- Austrian Centre of Industrial Biotechnology, Krenngasse 37, Graz 8010, Austria
b Department of Biotechnology, University of Natural Resources and Life Sciences, Vienna, Austria
Article history:
Received 1 July 2022
Revised 19 September 2022
Accepted 21 September 2022
Available online 22 September 2022
Keywords:
Residence time distribution
Chromatography
Staphylococcal protein A
Periodic counter-current chromatography
Continuous
a b s t r a c t
The trend in the biopharmaceutical industry is changing from batch process to continuous process For continuous biomanufacturing, traceability of the material is required by regulatory authorities The recent ICH draft guideline Q13 on continuous manufacturing of drug substances and drug products requests an
“understanding of process dynamics as a function of input material attributes (e.g., potency, material flow properties), process conditions (e.g., mass flow rates) … One common approach is characterization
of residence time distribution (RTD) for the individual unit operations and integrated system.” Thus, it
is necessary to trace material through individual continuous unit operations and the integrated process The RTD of a process is obtained experimentally by injecting a pulse of an inert tracer into the inlet and measuring the broadening of the injected pulse in the outlet We investigated the RTD of three-column periodic counter-current chromatography (PCC) using staphylococcal protein A affinity chromatography, with a focus on how the material distributes over subsequent cycles A fluorescent-labeled antibody was used as the inert tracer under high salt concentration The tracer was injected once in each run but at different points of the loading phase We then analyzed the outlet of the column In the elution phase, regardless of the point of injection, we observed an even distribution of the tracer In the loading phase, a constant exchange between the antibody in the solid phase and the liquid phase was observed, meaning that sending the outlet of one chromatography column into another column to improve resin utilization causes higher residence time in the system for some portion of the material
© 2022 The Author(s) Published by Elsevier B.V This is an open access article under the CC BY license ( http://creativecommons.org/licenses/by/4.0/)
1 Introduction
The biopharmaceutical industry has recently become highly
interested in moving from batch process to continuous process,
though there are many challenges along the way, including the
traceabilityofmaterialthroughtheprocess.Traceabilityofthe
ma-terialisrequiredbyregulatoryauthoritiesforcontinuous
bioman-ufacturing.TherecentICHdraftguidelineQ13oncontinuous
man-ufacturingofdrugsubstancesanddrugproductsasksforthe
char-acterization of material flow in the continuous process and
rec-ommendsusingtheresidencetimedistribution(RTD)forthis
pur-pose The RTDis the probability distribution ofthe time a piece
of a substance is likely to spend in the reactor The most
com-monmethodofdeterminingtheRTDistomeasurethesystem
re-sponse foraninerttracer pulse[1].Theknowledge ofthis
distri-bution isimportantwhendesigning theprocess,aswell aswhen
∗ Corresponding author at: ACIB- Austrian Centre of Industrial Biotechnology,
Krenngasse 37, Graz 8010, Austria
E-mail address: alois.jungbauer@boku.ac.at (A Jungbauer)
theprocess isperformed, in ordertoget informationonstart-up andshut-down timing and samplingfrequency to determine the adequateprocessanalyticaltechnology(PAT)[2].Furthermore,the challengeofdefininganewbatchdefinitionforacontinuous bio-processwasaddressedbyRTDcharacterization[3,4].RTDneedsto
bedefinedfortheindividual unitoperationsandthenforthe in-tegratedprocess
RTDis measured through a tracer experiment, onlineprocess measurements of an appropriate product attribute, and/or pro-cessmodeling[3,5–8].RTDiscalculatedtheoreticallyusingamass transferequation,thoughinchromatographyitisquitechallenging becausethereareadsorptionanddesorptionkineticsinvolved Cur-rentunderstandingoftheadsorptionofantibodiesonporous pro-teinAaffinitychromatographybeadsisaporediffusion-controlled process[9–14].Thesaturationoftheporousbeadcanbedescribed
asashrinking coremodelinwhichthe saturatingmigratedfrom theoutersurfaceofthebeadtothecore[15].Forsimplerunit op-erations, such ascontinuously stirring tank (CSTR) and plug flow reactor, the RTD function is fully solved for ideal cases [16] For morecomplicatedunit operationsorprocesses,RTDcan be
mea-https://doi.org/10.1016/j.chroma.2022.463530
0021-9673/© 2022 The Author(s) Published by Elsevier B.V This is an open access article under the CC BY license ( http://creativecommons.org/licenses/by/4.0/ )
Trang 2Fig 1 Schematic diagram of three-column periodic counter-current chromatography (PCC) in one cycle including six steps Steps 2, 4, and 6 show the main loading steps in
which two columns are in the loading phase and the other column is in the elution/regeneration step In these steps, the breakthrough of a column goes to the next column
to increase resin utilization Steps 1, 3, and 5 show the wash phase between the main loading steps
suredexperimentally by injectinga smallpulseofaninerttracer
andthentracingitintheoutlet.Theinerttracerneedstobe
iden-tical to the proteinof interest, butwe also need a difference by
which to detect the tracer Thus, finding an inerttracer is
chal-lenging
Antibodypurificationisperformedconventionallyby proteinA
affinity chromatography in batch mode; however, increasing
de-mandforantibodyproductslettheindustrymovefrombatch
pro-cessingtocontinuousprocessing.Abatchchromatographyprocess
isconvertedintoacontinuousprocessbyapplyingcounter-current
loading, also known as periodic counter-current chromatography
(PCC)[17].Thecombinationoffed-batchandcontinuouscaptureis
the mosteconomicalwaytoproduce monoclonalantibodies[18]
Thisshiftfrombatch tocontinuousprocessingleadstohigher
ca-pacity,higherquality,andlowerprices,buttheimprovedprocess
economicsisobtainedattheexpenseofcomplexity[18].TheRTD
of batch chromatographyislesschallengingbecause thematerial
is not transferred from one column to another, and the elution
is pooled and stirred Furthermore, we assume that the column
is fullyregenerated and the antibody is not left on the column
We assume a clean columnforevery batch Yet,in PCC ormany
continuous chromatography unit operations, part of the material
is transferredfromonecolumntothe nextcolumn, soitis more
challengingtotracethematerial
Labeling the monoclonalantibody with a fluorescent dye and
usingthefluorescentsignalfordetectionisamethodthathasbeen
widelyusedinchromatography,mainlyforconfocallaserscanning
microscopy(CLSM)imaging.Thequestionaroseastowhetherthe
labeled antibody has the exact properties of the unlabeled
anti-body because a slight difference may result in different binding
propertiesand/or displacementandthedangerofmisinterpreting
experimental results [19–22] Quantum dots may have a higher
sensitivity, butthereis lessexperience withthechromatographic
behavior ofsuch labeledproteins,anditisobviousthatthey also
introduceanaberrantchargetotheprotein[23].Despitethe
criti-cal aspectsoffluorescentlylabelingantibodies,themethodhasits
advantages: It isvery sensitive, anda variety offluorescent dyes
are readily available [24].This methodis cost-effectivecompared
to radiolabeling, and on-line scintillation counters are not
com-monlyusedinbioprocessinglaboratories
The goal ofthis work isto characterize the RTD ofprotein A chromatographyintheloadandelutionphases.First,we setup a methodtodemonstratethat thefluorescentlylabeled monoclonal antibody serves as an inerttracer, and then we determined the RTDofacounter-currentproteinAaffinitychromatographyrunby injectingthetraceratthestart,middle,andendofloading
Acommercialmonoclonalantibody(IgG2)wasusedasthe pro-tein ofinterest.Forthelast setofexperiments, another commer-cialmonoclonalantibody(IgG1)wasused.Chemicalsandreagents were purchasedfromMerck KGaAorSigmaAldrichunless other-wise stated All bufferswere filtered by a 0.22 μm filter(Merck KGaA)beforeuse.Afluorescentproteinlabelingkit(AlexaFluorTM 488)waspurchasedfromInvitrogen,anda10kDamembranefilter (MilliporeAmicon)wasusedduringthelabelingprocess
Fluorescent dyewas used to label the antibody The free dye wasremovedusinga10kDamembranefilter.Thedegreeof label-ing(DOL)wasdeterminedaccordingtothemanufacturer’s instruc-tions.TheDOLwasalways<1toensureminimallabeling.The fi-nalmonoclonalantibodylabeledwiththefluorescentdyewas re-ferredtoasthelabeledantibody
AnHPLCsystem(DionexUltimate3000HPLCsystem)and an-alytical protein A affinity chromatography column were used to determine the antibody concentration and fluorescence intensity The HPLC systemwas equippedwith a diode array detectorand fluorescent detector(ThermoFisher Scientific) The analytical col-umnwasaPOROSA20μmcolumn(2.1× 30mm,0.1ml; Ther-moFisher Scientific) The equilibration buffer was 50 mM phos-phatebuffercontaining150mMNaCl(pH7.0).Theelution buffer was100mMglycinebuffer(pH2.5).Thesampleinjectionwas20
Trang 3N Lali, P Satzer and A Jungbauer Journal of Chromatography A 1683 (2022) 463530
Fig 2 Batch mode condition equivalent to one column in counter-current chro-
matography (PCC) The blue area indicates the product bound to resin in a column
The brown area indicates the unbound product leaving the column a) Full break-
through curve The blue area shows the maximum resin capacity, which is equal to
the equilibrium binding capacity (EBC) b) Conventional load volume in batch mode
until 10% of breakthrough (DBC10) c) The batch mode loading volume is equivalent
to the PCC loading volume, and the load is up to 70% of breakthrough d) The batch
mode chromatography up to 70% breakthrough, which reproduces the RTD in one
column in PCC The dashed line shows the switches between different steps in one
cycle For example, column 2 from Fig 1 : Section 1 shows the material bound to
column 2 from column 3 in the previous wash step (step 1 in Fig 1 ), and Section
2 shows the material bound to column 2 from the breakthrough of column 1 (step
2 in Fig 1 ), Section 3 shows the material bound to column 2 in the main loading
step (step 3 in Fig 1 ), Section 4 shows the material moved out of column 2 and
loaded into column 3 (step 4 in Fig 1 ), and Section 5 shows the material moved
out of column 2 and loaded into column 1 (step 5 in Fig 1 ) Area V is equal to area
I and area IV is equal to area II
μl The UV signal at 280 nm (UV280) was monitored and used
to determinetheantibody concentration,andthefluorescent
sig-nal was monitored and used to determine the labeled antibody
concentration The results were evaluated and quantified using
Chromeleon7software(ThermoFisherScientific)
For continuous chromatography, three-column PCC was used
(Fig.1) OnePCCcycleconsistsofsixsteps Steps2,4,and6are
the mainloading steps,inwhichtwo columnsare intheloading
phase and one columnisin the elution/regeneration phase
Dur-ing thesesteps,theinlet goestoa columnandthebreakthrough
of that column goes to the next column, so resin utilization in-creases.There is a UV detector betweenthe two columnsin the loadingphase tomonitorthe breakthroughcurve Steps1,3,and
5 are thewash steps betweenthe main loadingsteps The wash buffergoestothefullyloaded columnandsendsthewashbuffer together with the remaining product to a freshcolumn to avoid losingtheproduct.Thesestepsareonlyaslongasthewashphase aftertheloadingphase(Fig.1)
The system was an ÄKTA Avant chromatography system equippedwithextravalvesandasecondUVdetector.Extratubing wasaddedwhennecessary,andtheflowpathwaschangedto pro-duceathree-columnPCCsystemasexplainedbyGomis-Fonsetal [20].Mab SelectSuRe(Cytiva)resin waspackedintoTricorn5/50 columns,andthecolumnvolumeforthethreecolumnswas1ml The equilibration/load/wash buffer was20 mM phosphatebuffer containing150mMNaCl(pH7.4).Theelutionbufferwas100mM acetate buffer (pH3.0) For some experiments, we increased the NaClto500mMintheequilibration/load/washbufferandelution buffer Chromatographyphasesincludedequilibration,load, wash, andelutionphases.Theflowratewas0.4ml/min
In the PCC experiments, loading time/volume was calculated basedona preliminaryexperimentandmonitoredby thesecond
UV detector,which wasplaced afterthefirstcolumninthemain loadingphases[25].Loading time/volumewasbased onreaching 70% ofthe final breakthrough signal [25].The UV280 was moni-toredduringtheelutionphase.FortheRTDmeasurement,0.5ml
oflabeledantibodywasinjectedduringtheloadingphaseusinga sampleloopintheinjectionvalve.Allelutionpeakswerecollected
in0.5mlor1mlfractionsandanalyzedforantibodyconcentration andlabeledantibodyconcentration
The basic principle of many continuous chromatography unit operationsis to increase the loadamount to maximize the resin utilizationby recyclingtheoutletofthecolumntoavoid decreas-ing the yield [17] We used a batch chromatography experiment
toreproducetheresultsfromonlyonecolumninPCC,which ap-pliesto differentcontinuouschromatographyprocesses,including PCC.Thebatchchromatographywassetupbyprolongingtheload phase up to 70% of the final breakthrough (Fig 2) Figs 1 and
2showthat in onecolumn in PCC,bound material camefrom the two previous steps (andcolumn), andtheunboundproduct goes intothenexttwosteps(andcolumn);therefore,itmakestheRTD
inPCCrathercomplicated
Theprolonged loadingphase inbatch chromatographyisused
asanequivalenttocharacterizethe PCC(Fig.2) Forexample,for column 2 (Figs 1 and 2), there are different sections of loaded material: Section 1 shows the material bound to column2 from column3 in the previous washstep (step), Section 2 shows the material bound to column2from the breakthroughof column1 (step 2),Section 3 showsthematerial bound tocolumn2 inthe main loading step (step 3), Section 4 showsthe material moved outofcolumn2andloadedintocolumn3(step4),andSection5
showsthe material moved out ofcolumn 2andloaded into col-umn1(step 5).Bytracing thematerialinthesesections,we pre-dictthematerialflowinathree-columnPCC.Theadvantageofthis experimentisthatfractionationoftheoutletofonecolumninthe loadingphaseispossible
The same ÄKTA Avant chromatography system was used but
inthe conventionalflow pathequipped withoneofthe columns mentionedin2.4.basedonreaching70%ofthefinalbreakthrough signal.UV280wasmonitoredduringtheelutionphase.FortheRTD measurement,0.5mloflabeledantibodywasinjectedduringthe loadingphaseusingasampleloopintheinjectionvalve.The
Trang 4out-Fig 3 Two elution peaks in PCC Left, with conventional protein A buffer Right, with 500 mM of all buffers Blue bars show the unlabeled antibody concentration Green
bars show the labeled antibody concentration In the elution peak with conventional buffers, the retention time of the labeled antibody is longer than that of the unlabeled antibody In the elution peak with high salt buffer, the retention time of the labeled antibody is equal to that of the unlabeled antibody
Fig 4 Three consecutive elution peaks in a PCC experiment Blue bars show the unlabeled antibody concentration Green bars show the labeled antibody concentration The
labeled antibody was injected at the start of the loading phase corresponding to the first elution peak, but it was detectable in the next two elution peaks after injection
letofallphaseswascollectedin0.5mlor1mlfractionsand
an-alyzed byanalytical HPLC forantibodyconcentration andlabeled
antibodyconcentration
A Leica TCS SP8-STED laser (point) scanning confocal
micro-scope wasused Fluorescentlylabeled antibodywasused for
im-age acquisition (green) The microscope was equipped with the
StimulatedEmissionDepletion(STED)module,whichoffersspatial
super-resolution fluorescence imaging The electronics and
soft-waremodulewere fromPicoQuant(Germany).ForAlexa488dye,
the excitation wavelength was490 nm andemission wavelength
520nm
Achannelslide(ibidiGmbH)withaheightof0.2mmwas con-nectedtoasyringepump,onefilterfromaTricorn5filterkit (Cy-tiva)wasplaced intotheoutletoftheLuer connection,andresin beadswerelooselypackedintothechannel,producinga microcol-umn.Thesyringepumpwasusedtorunthemicrocolumnwiththe samesuperficial velocity.Themicrocolumn wasplaced underthe microscopeandan image wasdetected every 10s.A chromatog-raphy run was performedunder the microscope, including equi-libration, loading (unlabeled) antibody, loading labeled antibody, loading(unlabeled) antibody,wash,andelution Duringthe load-ing,theunlabeledantibody,equalto40%oftheresincapacity,was loadedintotheresinfirst.Next,thelabeledantibody,equalto40%
oftheresincapacity,andtheunlabeledantibody, equalto40%of
Trang 5N Lali, P Satzer and A Jungbauer Journal of Chromatography A 1683 (2022) 463530
Fig 5 Injection of labeled antibody at the end of the loading phase The blue line shows the unlabeled antibody concentration The green line shows the labeled antibody
concentration
resincapacity,wereloaded.Intotal,theamountwasequalto120%
oftheresincapacity
3 Result and discussion
During the PCC experiments with three protein A affinity
columns,0.5mloffluorescent-labeledantibodywasinjectedeither
atthestart,themiddle,ortheendoftheloadingphase.The
un-labeled and labeledantibody concentrationsin the elution peaks
show that, when conventional buffers (lower salt concentration)
were used,regardlessofthepointofinjection,the average
reten-tion time ofthelabeled antibodieswaslonger thanthat of
unla-beledantibody(Fig.3).Thissuggeststhat,underthiscondition,the
affinity ofthelabeled antibodywashigherthanthatofunlabeled
antibody.Inaddition,thismeansthatthefluorescentlylabeled
an-tibodydoesnotactasaninerttracer.Thefluorescentdyewas
pre-viouslydemonstratedtoaltertheretentiontimeofthelabeled
an-tibody becauseitleadstoslightdifferencesinhydrophobicityand
charge However, thisdifferenceinretentiontime waseliminated
byincreasingthesaltconcentration[21]
Thus, the PCC experiments were performed again with
in-creased salt concentration: 500 mM NaCl in the
equilibra-tion/load/wash and elution buffer Under highsalt concentration,
regardless ofthepoint ofinjection, theaverage retentiontime of
the labeledantibodywasequalto thatofthe unlabeledantibody
(Fig.3).Therefore,weconcludethatthelabeledantibodywas
con-sidered an inert tracer under high salt concentration conditions
In addition, theresults indicatethat any section ofthe inlet
dis-tributesequallyintheelutionpeak.Forthisreason,allfurther
ex-perimentswereperformedunderhighsaltconcentrations
By increasing the NaCl concentration in the equilibra-tion/load/washandelutionbufferto500mM,wehadthelabeled antibodyasaninerttracer.However,thelabeledantibodywas un-expectedlydetectedinthenextelutionpeaks(Fig.4),whichmeans thatthelabeledmaterialthatwasalreadyloadedintoonecolumn wastransferredduringtheloadingphasetothenextcolumn Fur-therinvestigationofthiseffectrequiredfractionationandanalysis
oftheoutletofonecolumninPCC.Thelimitationwasthat,inthe PCC process, the outlet of one column goes directly to the next column,socollecting theoutletofonecolumn(Fig.1,step2, be-tween column1 andcolumn2) interrupts the wholeprocess To overcomethischallenge,a batchchromatographyexperimentwas setupwiththeconditionsmentionedin2.5torepresenttheRTD
ofonecolumninthePCC
Asexplainedin2.5,batch chromatographywithalonger load-ing volume can be representative of the RTD of each column in continuouschromatography (Fig 2) Batchmode chromatography wasperformed to better understand the RTDduring the loading phase.Thepulseinjectionwasperformedduringtheloadingphase butatdifferentpointsoftheloadingphase
Injectionattheendoftheloadingphase showedthatthe an-tibody bound to the resin more than expected When the tracer wasinjected atthe point of60% breakthrough,we expected 60%
oflabeledantibodytoleavetheresinand40%tobindtotheresin; thus,this40%wouldbefoundintheelutionpeak However,only 20%ofinjectedlabeledantibodymovedoutofthecolumnduring theloadingphaseand80%wasintheelutionpeak(Fig.5)
Trang 6Fig 6 Injection of labeled antibody at the start of the loading phase The blue line shows the unlabeled antibody concentration The green line shows the labeled antibody
concentration
Fig 7 Injection of labeled antibody at the start of the loading phase, fully overloading the column until reaching a full breakthrough and continuing to load until 220 CV
The blue line shows the unlabeled antibody concentration The green line shows the labeled antibody concentration
Whenthetracerwasinjectedatthestartoftheloadingphase,
itstartedleavingthecolumntogetherwithanexcessofunlabeled
antibodyinthebreakthrough.Theinitialassumptionwasthatthe
tracer isbound totheresinuntiltheelutionphase.However,10%
oftheinjectedmaterialmovedoutofthecolumnduringthe
load-ingandwashphase(Fig.6)
HIC analytical chromatographyand CEX analytical chromatog-raphywereperformed(datanotshown)toidentifythedifferences between the labeled and unlabeledantibodies The labeled anti-bodyisslightlymorehydrophobic.AntibodyproteinAinteraction
isdominatedbyhydrophobicinteractions[26,27].Thus,amore
Trang 7hy-N Lali, P Satzer and A Jungbauer Journal of Chromatography A 1683 (2022) 463530
drophobic tracer binds stronger, but we observed that a certain
fractionexitsthecolumneventhoughitshouldremaininside
Weconcludethatthedesorptionreactionbecomesmore
signif-icantespeciallywhentheresinisoverloadedandtheconcentration
ofantibodyishighinthesolidphase.Weassumethatconstant
ex-changebetweentheantibodyinthe liquidphaseandsolidphase
isoccurring.Thedesorptionisdetectabletoalesserextentin
con-ventionalbatchchromatographywhentheloadingvolumeisupto
10%ofbreakthrough.Inthatcase,theresinisnotfullyloaded,and
the desorbed product getsadsorbed againonto the unused fresh
resinfurtherinthesamecolumn Althoughthedesorptionratein
batchchromatographyisusuallyconsiderednegligible,previous
re-searchhasshownthattheoveralladsorptionrateisacombination
ofthe adsorption/desorptionrate[28].The loadamount ishigher
ineachcolumninPCC,sothedesorptionrateismorepronounced
whenitcomestocontinuouschromatography
Following the pulseinjection in batch chromatography
(injec-tion atthestartofthe loadingphase), anexperimentwassetup
to investigateif the tracer can be completely removed fromthe
column by prolonging the loading phase andadding more
unla-beled antibody The assumption wasthat, if we loadmore
unla-beledantibody,theconstantexchangebetweentheliquidandsolid
phasewouldleadtolosingthelabeledantibodyduringtheloading
phase.Weloadedacolumnuntilfull breakthroughandcontinued
foranexcessivelylongloadingvolume(220CV).Duringthe
load-ing phase, 65% of the tracer moved out of the column, andthe
concentrationoflabeledantibodyintheflowthroughdecreasedas
theoverallconcentrationinthecolumndecreased(Fig.7).This
ex-perimentconfirmedthatthereisaconstantexchangebetween
an-tibodiesintheliquidandsolidphases
To confirmthis unexpectedexchange, CLSMimaging was
per-formed tovisualizetheeffect(Fig.8) CSLMhasbeenused
previ-ouslywhentheexacttransportmechanismisstillunresolved[29]
Thebeadswereplacedinthemicrochannelandthe
chromatogra-phyrun performedunderthemicroscope, includingequilibration,
loadingunlabeledantibody,loadinglabeledantibody,loading
unla-beled antibody,wash,andelution(seeSection 2.6).Thebeadsare
loaded withunlabeledantibodyuntil 40%ofthebinding capacity
isreached Theunlabeledantibodyisnotvisible(Fig.8B) The
la-beled antibody,equalto40%ofthebindingcapacity,wasthen
in-jected,followedbyloadingtheunlabeledantibody,equalto40%of
thebinding capacity(Fig.8D).TheCLMSimagesshowthat,when
thelabeledantibodywasadded,itstartedtobindfromthesurface
of theresin even though the antibodywasalready bound tothe
resin.Thisbehaviorisexpectedforaporediffusion-limitedprocess
[30–32].The labeledantibody should surpass thebound fraction,
butit isboundatthesurface Theeffect becameeven more
pro-nouncedwhentheunlabeledantibodywasloadedagainontopof
thelabeledantibody.Thegreenfractionmigratedfromthesurface
area towardsthecoreofthebeads(Fig.8,avideoofthis
experi-mentincludingtheloadingphaseandelutionphaseisavailablein
the onlinesupplementary material) We assume that the
adsorp-tionisnot fullybasedona porediffusion-limitedprocess;itmay
be a combinationof solidandporediffusion.Therefore,a certain
portionoflabeled tracerremains onthesurfaceandconstant
ex-changebetweenliquidandsolidphasesoccurs
Fig 8 Resin beads under the microscope in a microcolumn A: Fresh resin Beads
are shown in black and white B: Unlabeled antibody was loaded (which is not vis- ible) C and D: Labeled antibody was loaded (green) E: Unlabeled antibody was loaded (not visible) Please see the video of this process online in the supplemen- tary material
Trang 8Fig 9 Pulse injection in batch chromatography using IgG1 The blue line shows the unlabeled antibody concentration The green line shows the labeled antibody concen-
tration
Tovalidatepreviousresults,thelastsetofexperimentswas
per-formed usingan antibodyofsubclass1andthesamefluorescent
dye.Intwoseparateexperiments,onepulseoftracerwasinjected
at the start and the end of the loading phase The experiments
wereperformedinbatchmodeasdescribedin2.5
Whenthelabeledmaterialwasinjectedatthestartofthe
load-ing phase, only91% werefound in theelution peakeven though
thehypothesiswastofind100%ofinjectedmaterialintheelution
peak When the labeled material was injected at the end ofthe
loadingphase,62%werefoundintheelutionpeakeventhoughthe
hypothesiswastofind35%ofinjectedmaterialintheelutionpeak
(asitwasinjectedat65%ofbreakthrough)(Fig.9).Theresults
val-idatethepreviousexperimentswithIgG2,thoughtheconstant
ex-change occurred to a lesserextent The reason is that the
bind-ing affinity of IgG1towardprotein Aresin is higherthan that of
IgG2, solessexchangewasobservedbetweentheliquidandsolid
phases.However,theexchangeisstillsignificant
The dyebinding siteon theantibodyisimportantandcan
in-dicateifitisaffectingtheproteinAbinding.Inourcase,weused
mab SelectSure, which is composed of four mutatedZ-domains
[33].It is a myththat the Z-domain derived fromstaphylococcal
protein Aexclusivelybinds totheFc-domainofantibodybecause
theelution pHisindependentoftheantibodysubclass[34].Bach
et al.investigatedthebinding behavior of15 differentantibodies
of subclass IgG1and IgG2 andfound a secondary interaction by
incubation of the F(ab’)2 fragments for all of them The weaker
secondary interaction also suggestsa constant exchange between
bound andfreeantibodies[35].Thisobservationcorroboratesour
findings
4 Conclusion
We conclude that a fluorescent-labeledantibody serves as an
inert tracer in protein A affinity chromatography for
determin-ing the RTD only when it is performed at a high salt
concen-tration When we usethe fluorescent-labeledantibodyunderthe
mentioned conditions,anysection of theinlet distributesequally
through the elution peak, meaning that the ratio of labeled and
unlabeled antibodies remains the same throughout the elution
peak Although the constant exchange of antibodiesbetweenthe
liquid andsolid phase in the loadingphase complicates the RTD
determination, the adsorption process is a combination of solid
and porediffusion,which explainsthe exchange ofmaterial
dur-ing loading Thisalso suggeststhat, in thiscase, we have an
ex-tremelywideRTD.Inthecaseofthecirculationofproductin
con-tinuouschromatography unit operation, such asPCC,the circula-tionofproductinthesystemincreasestheaverageresidencetime
Narges Lali: Execution of experiments, design of the exper-iments, drafting of the manuscript, interpretation of the data
Peter Satzer:designoftheexperiments,interpretationofthedata:
Alois Jungbauer:Conceptualization,Resources,Writing Review& Editing,Supervision,Fundingacquisition
Declaration of Competing Interest
Theauthorsdeclarethattheyhavenoknowncompeting finan-cialinterestsorpersonalrelationshipsthatcouldhaveappearedto influencetheworkreportedinthispaper
Acknowledgments
This work was supported by the European Union’s Horizon
2020research andinnovationprogramundergrantagreementno 635557
Supplementary material associated with this article can be found,intheonlineversion,atdoi:10.1016/j.chroma.2022.463530
References
[1] O Levenspiel, Chemical Reaction Engineering, 3rd ed., Wiley, New York, 1999 ed[Online] Available: http://app.knovel.com/web/toc.v/cid:kpCREE0 0 05 [2] W Engisch, F Muzzio, Using residence time distributions (rtds) to address the traceability of raw materials in continuous pharmaceutical manufacturing, J Pharm Innov 11 (2016) 64–81, doi: 10.1007/s12247-015- 9238- 1
[3] N Lali, A Jungbauer, P Satzer, Traceability of products and guide for batch def- inition in integrated continuous biomanufacturing, J Chem Technol Biotech- nol (2021), doi: 10.1002/jctb.6953
[4] "GUIDANCE DOCUMENT quality considerations for continuous manufac- turing issued by: office of medical products and tobacco, center for drug evaluation and research document Nr FDA-2019-d-0298 February 2019." https://www.fda.gov/regulatory-information/search-fda-guidance-documents/ quality- considerations- continuous- manufacturing (accessed
[5] J Sencar, N Hammerschmidt, A Jungbauer, Modeling the residence time dis- tribution of integrated continuous bioprocesses, Biotechnol J 15 (8) (2020) e20 0 0 0 08 Aug, doi: 10.10 02/biot.2020 0 0 0 08
[6] S Mun, Y Xie, N.-H.L Wang, Residence time distribution in a size-exclusion SMB for insulin purification, AlChE J 49 (8) (2003) 2039–2058, doi: 10.1002/ aic.690490814
[7] S Pawlowski, N Nayak, M Meireles, C.A.M Portugal, S Velizarov, J.G Crespo, CFD modelling of flow patterns, tortuosity and residence time distribution in monolithic porous columns reconstructed from X-ray tomography data, Chem Eng J 350 (2018) 757–766 2018/10/15/, doi: 10.1016/j.cej.2018.06.017
Trang 9N Lali, P Satzer and A Jungbauer Journal of Chromatography A 1683 (2022) 463530
[8] M.A Teeters, I Quiñones-García, Evaluating and monitoring the packing behav-
ior of process-scale chromatography columns, J Chromatogr A 1069 (1) (2005)
53–64 2005/03/25/, doi: 10.1016/j.chroma.2005.02.051
[9] Y.N Sun, et al., Comparison of protein A affinity resins for twin-column contin-
uous capture processes: process performance and resin characteristics, J Chro-
matogr A 1654 (2021) 462454 Sep 27, doi: 10.1016/j.chroma.2021.462454
[10] C.-.S Chen, N Yoshimoto, S Yamamoto, Prediction of the performance of
capture chromatography processes of proteins and its application to the re-
peated cyclic operation optimization, J Chem Eng Jpn 53 (11) (2020) 689–
697, doi: 10.1252/jcej.20we116
[11] W Krepper, P Satzer, B.M Beyer, A Jungbauer, Temperature dependence of an-
tibody adsorption in protein A affinity chromatography, J Chromatogr A 1551
(2018,) 59–68 May 25, doi: 10.1016/j.chroma.2018.03.059
[12] E.X Perez-Almodovar, G Carta, IgG adsorption on a new protein A adsorbent
based on macroporous hydrophilic polymers I Adsorption equilibrium and
kinetics, J Chromatogr A 1216 (47) (2009) 8339–8347 Nov 20, doi: 10.1016/j
chroma.2009.09.017
[13] J.T McCue, G Kemp, D Low, I Quiñones-Garcı ´a, Evaluation of protein-A chro-
matography media, J Chromatogr A 989 (1) (2003) 139–153, doi: 10.1016/
s0 021-9673(03)0 0 0 05-0
[14] R Hahn, P Bauerhansl, K Shimahara, C Wizniewski, A Tscheliessnig, A Jung-
bauer, Comparison of protein A affinity sorbents: II Mass transfer properties, J
Chromatogr A 1093 (1) (2005) 98–110 20 05/11/04/, doi: 10.1016/j.chroma.20 05
07.050
[15] J Weinberg, S Zhang, G Crews, E Healy, G Carta, T Przybycien, Polyclonal
and monoclonal IgG binding on protein A resins-evidence of competitive bind-
ing effects, Biotechnol Bioeng 114 (8) (2017) 1803–1812 Aug, doi: 10.1002/bit
26286
[16] H.S Fogler, Elements of Chemical Reaction Engineering (in English), 2006
[17] A Jungbauer, Continuous downstream processing of biopharmaceuticals,
Trends Biotechnol 31 (8) (2013) 479–492 Aug, doi: 10.1016/j.tibtech.2013.05
011
[18] A.L Cataldo, D Burgstaller, G Hribar, A Jungbauer, P Satzer, Economics and
ecology: modelling of continuous primary recovery and capture scenarios for
recombinant antibody production, J Biotechnol 308 (2020) 87–95 Jan 20,
doi: 10.1016/j.jbiotec.2019.12.001
[19] C.A Teske, R Simon, A Niebisch, J Hubbuch, Changes in retention behavior of
fluorescently labeled proteins during ion-exchange chromatography caused by
different protein surface labeling positions, Biotechnol Bioeng 98 (1) (2007)
193–200 Sep 1, doi: 10.1002/bit.21374
[20] J Gomis-Fons, N Andersson, B Nilsson, Optimization study on periodic
counter-current chromatography integrated in a monoclonal antibody down-
stream process, J Chromatogr A 1621 (2020) 461055 Jun 21, doi: 10.1016/j
chroma.2020.461055
[21] C.A Teske, M Schroeder, R Simon, J Hubbuch, Protein-labeling effects in con-
focal laser scanning microscopy, J Phys Chem B 109 (28) (2005) 13811–13817
Jul 21 + , doi: 10.1021/jp050713
[22] C.A Teske, E von Lieres, M Schroder, A Ladiwala, S.M Cramer, J.J Hubbuch,
Competitive adsorption of labeled and native protein in confocal laser scan-
ning microscopy, Biotechnol Bioeng 95 (1) (2006) 58–66 Sep 5, doi: 10.1002/
bit.20940
[23] U Resch-Genger, M Grabolle, S Cavaliere-Jaricot, R Nitschke, T Nann, Quan- tum dots versus organic dyes as fluorescent labels, Nat Methods 5 (9) (2008) 763–775 Sep, doi: 10.1038/nmeth.1248
[24] S Vira, E Mekhedov, G Humphrey, P.S Blank, Fluorescent-labeled antibodies: balancing functionality and degree of labeling, Anal Biochem 402 (2) (2010) 146–150 Jul 15, doi: 10.1016/j.ab.2010.03.036
[25] R Godawat, K Brower, S Jain, K Konstantinov, F Riske, V Warikoo, Periodic counter-current chromatography – design and operational considerations for integrated and continuous purification of proteins, Biotechnol J 7 (12) (2012) 1496–1508 Dec, doi: 10.10 02/biot.20120 0 068
[26] M Salvalaglio, L Zamolo, V Busini, D Moscatelli, C Cavallotti, Molecular mod- eling of protein A affinity chromatography, J Chromatogr A 1216 (50) (2009) 8678–8686 2009/12/11/, doi: 10.1016/j.chroma.2009.04.035
[27] W.L DeLano, M.H Ultsch, A.M de Vos, J.A Wells, Convergent solutions to binding at a protein-protein interface, Science 287 (5456) (20 0 0) 1279–1283, doi: 10.1126/science.287.5456.1279
[28] L Yang, J.D Harding, A.V Ivanov, N Ramasubramanyan, D.D Dong, Effect of cleaning agents and additives on Protein A ligand degradation and chromatog- raphy performance, J Chromatogr A 1385 (2015) 63–68 Mar 13, doi: 10.1016/j chroma.2015.01.068
[29] J Hubbuch, T Linden, E Knieps, J Thömmes, M.-.R Kula, Mechanism and ki- netics of protein transport in chromatographic media studied by confocal laser scanning microscopy: part II Impact on chromatographic separations, J Chro- matogr A 1021 (1) (2003) 105–115 20 03/12/22/, doi: 10.1016/j.chroma.20 03.08
092 [30] M Zhu, G Carta, Protein adsorption equilibrium and kinetics in multimodal cation exchange resins, Adsorption 22 (2) (2016) 165–179 2016/02/01, doi: 10 1007/s10450-015-9735-z
[31] E.X Perez-Almodovar, Y Wu, G Carta, Multicomponent adsorption of mono- clonal antibodies on macroporous and polymer grafted cation exchangers, J Chromatogr A 1264 (2012) 48–56 2012/11/16/, doi: 10.1016/j.chroma.2012.09
064 [32] T Liu, J.M Angelo, D.-.Q Lin, A.M Lenhoff, S.-.J Yao, Characterization
of dextran-grafted hydrophobic charge-induction resins: structural proper- ties, protein adsorption and transport, J Chromatogr A 1517 (2017) 44–53 2017/09/29/, doi: 10.1016/j.chroma.2017.07.090
[33] M Linhult, et al., Improving the tolerance of a protein a analogue to re- peated alkaline exposures using a bypass mutagenesis approach, Proteins Struct Funct Bioinf 55 (2) (2004) 407–416 2004/05/01doi: 10.1002/prot.10616, doi: 10.1002/prot.10616
[34] S Ghose, M Allen, B Hubbard, C Brooks, S.M Cramer, Antibody vari- able region interactions with Protein A: implications for the development
of generic purification processes, Biotechnol Bioeng 92 (6) (2005) 665–673 2005/12/2010.1002/bit.20729, doi: 10.1002/bit.20729
[35] J Bach, N Lewis, K Maggiora, A.J Gillespie, L Connell-Crowley, Differential binding of heavy chain variable domain 3 antigen binding fragments to pro- tein a chromatography resins, J Chromatogr A 1409 (2015) 60–69 2015/08/28/, doi: 10.1016/j.chroma.2015.06.064