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Page 1: Dynamics of immature mAb glycoform secretion during CHO cell … · groups are exploring the manufacture of Man5 mAb glycoforms to reduce product glycan variability and capitalise

General rights Copyright and moral rights for the publications made accessible in the public portal are retained by the authors and/or other copyright owners and it is a condition of accessing publications that users recognise and abide by the legal requirements associated with these rights.

Users may download and print one copy of any publication from the public portal for the purpose of private study or research.

You may not further distribute the material or use it for any profit-making activity or commercial gain

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Dynamics of immature mAb glycoform secretion during CHO cell cultureAn integrated modelling framework

Jimenez del Val, Ioscani; Fan, Yuzhou; Weilguny, Dietmar

Published in:Biotechnology Journal

Link to article, DOI:10.1002/biot.201400663

Publication date:2016

Document VersionPeer reviewed version

Link back to DTU Orbit

Citation (APA):Jimenez del Val, I., Fan, Y., & Weilguny, D. (2016). Dynamics of immature mAb glycoform secretion during CHOcell culture: An integrated modelling framework. Biotechnology Journal, 11(5), 610-623.https://doi.org/10.1002/biot.201400663

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This article has been accepted for publication and undergone full peer review but has not been through the copyediting, typesetting, pagination and proofreading process, which may lead to differences between this version and the Version of Record. Please cite this article as doi: 10.1002/biot.201400663. Submitted: 11-May-2015 Revised: 09-Oct-2015 Accepted: 23-Dec-2015 This article is protected by copyright. All rights reserved.

ResearchArticle

DynamicsofimmaturemAbglycoformsecretionduringCHOcellculture:Anintegratedmodelling

framework

IoscaniJimenezdelVal1

YuzhouFan2,3

DietmarWeilguny3

1 SchoolofChemicalandBioprocessEngineering,UniversityCollegeDublin,Belfield,Dublin4,

Ireland.

2 NetworkEngineeringofEukaryoticCellFactories,DepartmentofSystemsBiology,Technical

UniversityofDenmark,2800Kgs.Lyngby,Denmark.

3 SymphogenA/S,Pederstrupvej93,2750Ballerup,Denmark.

Correspondence:Dr.IoscaniJimenezdelVal,SchoolofChemicalandBioprocessEngineering,

UniversityCollegeDublin,Belfield,Dublin4,Ireland.

Email:[email protected]

Keywords:Dynamicglycosylationmodel, insilicoglycoengineering,CHOcells,pharmaceutical

bioprocessing,therapeuticproteinglycosylation

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Abbreviations:CS,couplingstrategy;Man9,ninemannoseglycan;Man5,fivemannoseglycan;

GE,glycosylationenzymes;NS,nucleotidesugars; ,cellspecificproductivity;CD,cellculture

dynamics model; GlycoModel, glycosylation model; GA, Golgi apparatus; ER, endoplasmic

reticulum;ERGIC, ER‐Golgi intermediate compartment;COPI, coat protein complex I;COPII,

coatproteincomplexII;GRP,Golgiresidentprotein;ManI,α‐1,2mannosidaseI(EC3.2.1.113);

GnTI, α‐1,3 N‐acetylglucosaminyl transferase I (EC 2.4.1.101); ManII, α‐1,3/ α‐1,6

mannosidaseII(EC3.2.1.113);GnTII,α‐1,6N‐acetylglucosaminyltransferaseII(EC2.4.1.143);

FucT,α‐1,6 fucosyltransferase (EC 2.4.1.68);GalT, β‐1,4 galactosyltransferase (EC 2.4.1.38);

SiaT,α‐1,6sialyltransferase(EC2.4.99.1)

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Abstract

Ensuring consistent glycosylation‐associated quality of therapeutic monoclonal antibodies

(mAbs)hasbecomeapriorityinpharmaceuticalbioprocessinggiventhatthedistributionand

composition of the carbohydrates (glycans) bound to these molecules determines their

therapeutic efficacy and immunogenicity. However, the interaction between bioprocess

conditions,cellularmetabolismandtheintracellularprocessofglycosylationremainstobefully

understood. To gain further insight into these interactions, we present a novel integrated

modellingplatformthat linksdynamicvariations inmAbglycosylationwithcellularsecretory

capacity. Two alternativemechanistic representations of howmAb specific productivity ( )

influencesglycosylationarecompared.Inthefirst,mAbglycosylationismodulatedbythelinear

velocitywithwhichsecretorycargotraversestheGolgiapparatus.Inthesecond,glycosylation

isinfluencedbyvariationsinGolgivolume.Withinourmodellingframework,bothmechanisms

accurately reproduce experimentally‐observed dynamic changes in mAb glycosylation. In

addition, anoptimisation‐basedstrategyhasbeendeveloped to estimate the concentrationof

glycosylationenzymesrequiredtominimisemAbglycoformvariability.Ourresultssuggestthat

the availability of glycosylation machinery relative to cellular secretory capacity may play a

crucialrole inmAbglycosylation. Inthefuture, themodelling frameworkpresentedheremay

aidinselectingandengineeringcelllinesthatensureconsistentmAbglycosylation.

1. Introduction

Monoclonal antibodies (mAbs) have emerged as the highest‐selling products of the

pharmaceutical industry [1].Thisunprecedentedcommercial successcanbeattributed to the

efficacy with which this class of protein therapeutics treat a multitude of life‐threatening

illnesses, including several types of cancer and autoimmune disorders [2]. All commercially‐

availablemAbscontain twoconsensusasparagine‐linked(N‐linked)glycosylationsiteson the

Cγ2 domains of their constant fragment (Fc) [3]. The monosaccharide composition and

distribution of the carbohydrates (glycans) bound to these sites has beenwidely reported to

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influence thesafety [4]and therapeuticefficacyofmAbs [3]. In turn,variations inbioprocess

conditionshavebeenshowntoheavilyimpactthedistributionofglycansboundtotherapeutic

glycoproteins [5]. Mathematical modelling, in turn, has emerged as an instrument that can

provide furtherqualitativeandquantitative insight into themechanismsbywhichbioprocess

conditionsinfluencetherapeuticproteinglycosylation[6,7].

Until recently,dynamicdata formAbglycoformdistribution throughout cell culturehasbeen

sparinglyavailableintheliterature.However,withthedevelopmentofrobust,high‐throughput

methodsformAbglycanprofiling[8‐10],asolidknowledgebaseonmAbglycosylationdynamics

isbeinggenerated[9‐13].Interestingly,themajorityofthesereportspresentsimilarqualitative

trends, where mAbs with less processed glycans accumulate towards the end of culture. In

particular,thechangesthathavemostcommonlybeenreportedinvolvereducedgalactosylation

[9,11] andincreasedsecretionofhigh‐mannoseglycans(inparticular, theMan5glycan)[10,

13]. These reportshighlight thedynamicnatureofmAbglycosylationduring cell culture and

open the possibility of utilising dynamic glycan distribution data to further understand the

interplay between cell culture conditions, cell line characteristics and therapeutic protein

glycosylation.

Increased secretion of under‐processed mAb glycoforms during cell culture is particularly

relevant in the context of pharmaceutical bioprocessing. The Man5 glycoform has been

associatedwithdecreasedserumhalf‐life[14,15]andcompromisedeffectorfunctionactivation

of mAbs [3, 16]. Furthermore, antibodies bearing this glycan have been associated with

detrimental inflammatory responses in humans [17]. Despite these findings, several research

groups are exploring the manufacture of Man5 mAb glycoforms to reduce product glycan

variabilityandcapitaliseon increasedantibodydependent cellular cytotoxicity (ADCC)which

mayresultfromtheabsenceofcorefucoseonMan5glycoforms[13].Reducedgalactosylation,

in turn, has been associatedwith decreased complement activation [18]. Given the influence

immatureglycoformshaveonthetherapeuticefficacyofmAbs,understandingthedynamicsof

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their secretion during cell culture is highly relevant towards developing next‐generation

therapeuticglycoproteinmanufacturingprocesses.

As reviewedrecently [6], severalmathematicalmodelshavebeendeveloped to represent the

protein glycosylation process [19‐24]. Of these, themodels formulated by Umaña and Bailey

[24],KrambeckandBetenbaugh [19],Hossler et al. [20]anddelVal et al. [21] are single‐cell

models where glycosylation is assumed to be independent of extracellular conditions, cell

growth and recombinant protein productivity. The remaining models have built upon their

predecessors by coupling the glycosylation process with cellular metabolism and bioreactor

culturedynamics.TheworkbyOhadiandcollaborators[22]couplestheglycosylationmodelof

Hossleretal.[20]withamodelforCHOcellgrowthandmetabolismandanabbreviatedmodel

fornucleotideandnucleotidesugar(NS)biosynthesis.Similarly,themodelbyJedrzejewskietal.

uses the glycosylationmodel of del Val et al. [21] and integrates it into a framework for cell

culture dynamics and a detailed dynamic model for NS metabolism [23]. In essence, both

coupledmodelssoughttodescribelimitationstomAbglycosylationintermsofthedependency

betweenextracellularnutrient availability and intracellularNSconcentrations, andbothhave

been shown to reproduce experimentally‐observed glycan distributions accurately. Because

both models create a direct link between readily‐measurable bioprocess conditions and

recombinantproductglycosylation,theyhavebeenidentifiedasthemostamenableforinsilico

glycoengineeringinthecontextofpharmaceuticalbioprocessing[6].

Despite successfully coupling cellular metabolism with mAb glycosylation, both of these

integratedmodelsdonot specifywhether therateof recombinantproteinsecretion ( )was

considered to influenceproteinglycosylation. Indeed,both theseprocesses (proteinsecretion

and glycosylation) are mediated by Golgi apparatus (GA) dynamics [25, 26] and, thus, are

inextricablylinkedtooneanother.TherelationshipbetweenGAdynamics, andglycosylation

is presented in Figure 1. Crucially, the mechanisms described in Figure 1 define the rate at

whichsecretorycargoenters (and leaves) theGolgi space,andhowthesedynamics influence

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themorphologyandresidentproteincontentoftheGA.Inordertomathematicallymodelthe

interplay between and protein glycosylation, two alternative representations of Golgi

dynamicsareconsideredinthiswork:

i. CS1: Increased (compared to baseline levels – Figure 1A)may occur due to secretory

cargotraversingtheGolgiapparatus(GA)athigherrates[27,28].Thiswouldreducethe

retention time of glycoproteins within the GA, and thus, decrease the extent of

glycosylationreactionstherein[20](Figure1B).

ii. CS2:Increased couldalsoarisefromanenlargedsecretory(Golgi)apparatus[29,30].In

thiscase, ifglycosylationenzyme(GE)expressionlevelsweretoremainunchanged,their

availability within a larger GA would be diluted (Figure 1C). In turn, lower GE

concentrationswouldhaveanegativeimpactontherateofglycosylationreactions.

Interestingly,moststudieswhereincreased hasbeeninduced(e.g.byreducingtemperature

[31‐34] or by adding supplements such as sodium butyrate [34‐37]) report variable

consequences on glycosylation and have generally attributed them to pleiotropic effects

associatedwithcellcyclearrest.However,severalpublicationshavelinkedincreasedsecretory

capacity( )withreducedglycoformcomplexity[32,38,39].Ofthese,therecentpublicationby

Fanetal.[39]integratesexperimentaldataforintracellularNSavailability,mAbglycoprofiling

and comparative and quantitative proteomics to conclude that a likely cause for increased

secretion of immature glycoforms (particularly hypogalactosylated and Man5 glycans) is

reducedglycosylationmachineryrelativetocellularsecretorycapacity.

In light of the possible correlation between and glycan processing, we propose a novel

modelling framework where the influence of recombinant protein secretion rate is

mechanistically linked to the glycosylation processwithin theGA. The two interpretations of

howincreasedsecretorycapacity influences theglycosylationprocesswithinGolgi (described

asiandii,aboveandpresentedinFigure1)arecomparedinthiswork.Usingtheexperimental

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datareportedbyFanetal.[39],wepresentacomprehensivestrategytoestimatetheunknown

parameters of our model. Once parameterised, the model quantitatively reproduces the

experimentally‐observed increase in immature mAb glycoform secretion at higher rates of

product secretion. Results from our modelling framework suggest that availability of

glycosylationmachinery relative tomAb specific productivitymay indeed be responsible for

increased secretion of under‐processed glycans during CHO cell culture. Additional

optimisation‐based calculations within our modelling framework indicate that a ~3‐fold

increaseintheexpressionof functionalN‐acetylglucosaminyltransferaseI(GnTI–theenzyme

responsible for the transition from high mannose to hybrid and complex glycans) should

maintainsecretionofMan5glycansatbaselinelevels.Themodellingstrategypresentedinthis

work provides additional insight into cellular processeswhichmay negatively impact glycan

processing. Thus, it has potential applications in refining selection and glycoengineering

strategies to identify and generate cell lines that are capable of producing consistent and

optimalmAbglycoforms.

2. Mathematicalmodeldevelopment

2.1. Experimentaldatacalculations

Threedistinctphasesofculturewereobservedintheexperimentaldatausedforthiswork[39].

PhaseIischaracterisedbycultureat37°Candoccursbetween0and5days(0to120h).Phase

IIisdefinedascultureat33.5°Candspansfromdays5to9(120to216h).Finally,PhaseIIIis

cultureat33.5°Cwithstationarycellgrowthandwasobservedfromday9(216h)untiltheend

of culture. Estimates for average values of net specific growth rate ( ), specific glucose

uptakerate( )andspecificmAbsecretion( )wereobtainedfromtheexperimentaldataby

calculating theslopeof thecumulativeproduction/uptakeof eachspecieswithrespect to the

integralviablecellnumber[31].DetailsonthesecalculationsarepresentedinSupplementary

Section1.

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2.2. IntegratedmathematicalmodelformAbglycosylation

AnintegratedmodeltodescribethedynamicsofmAbglycosylationthroughoutcellculturewas

formulated by coupling an unsegregated and unstructured cell culture dynamics (CD)model

withthemodelforintracellularmAbglycosylation(GlycoModel)describedbydelValetal.[21].

A schematic representation of themodelling strategy employed in this work is presented in

Figure 2. The assumptions underlying all models integrated in this work are presented in

Supplementary Section 2. All simulations, optimisations and parameter estimations were

performedwithgPROMSModelBuilder4.1.0(www.psenterprise.com/gproms)[40].

2.2.1. Cellculturedynamicsmodel

Anunsegregatedandunstructuredcellculturedynamicsmodelwasdevelopedtorepresentcell

growthanddeath,glucoseuptake,lactatesecretionanduptake,aswellasmAbproduction.The

CDmodelmaterialbalancesweredefinedasEquations1through6.

Eq.1

Eq.2

Eq.3

Eq.4

, , Eq.5

Eq.6

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Thespecific rates forcellgrowth( ) [41], celldeath( ) [42],glucoseuptake( ), lactate

consumption ( , ), lactate secretion ( , ) and mAb specific productivity ( ) were

definedasEqs.7–12.

,,

Eq.7

,,

, Eq.8

1/ ,

Eq.9

, / Eq.10

,1/ ,

Eq.11

/ Eq.12

ThefundamentalcriterionfordevelopmentoftheCDcomponentwastogeneratethesimplest

modelpossiblethatcouldcapturecellgrowthandmAbproductivityaccurately,giventhatthese

variablesarethekeyinputsfortheGlycoModel.DetailsontheassumptionsunderlyingtheCD

modelarepresentedinSupplementarySection2.

TheCDmodelcontainsthetenkineticparameterslistedinSupplementaryTableST1.Giventhe

distinct behaviour of cell culture at 37°C and 33.5°C, two sets of parameters, one for each

temperature,weredefined [31]. Parameter values for theCDmodelwere obtained using the

maximumlikelihoodparameterestimationactivityavailableingPROMS4.1.0,wherethevalues

fortheunknownphysicalandvariancemodelparametersareobtainedsothattheprobabilityof

themodel predicting the experimental values ismaximised [40]. Data for viable cell density,

deadcelldensity,extracellularglucose,lactateandproductwereusedforparameterestimation.

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2.2.2. Glycosylationmodel(GlycoModel)

Thethreeequationsdefiningthemainfeaturesoftheglycosylationmodelusedinthisworkare

presentedasEq.13–Eq.15[21].

,

. .

Eq.13

,12

, Eq.14

,

, / , / 1, / , / , / , /

∑, /

. ., / , / , /

Eq.15

Eq.13representsthematerialbalancesofmaturingcisternaeflowingthroughaGolgispaceof

length z(Figure 2B). There, the inlet of secretory cargo into the Golgi is determined by the

concentrationofglycan ( )at 0multipliedby ,whichrepresents the linearvelocity

with which the secretory cargo traverses the Golgi space. GRP recycling is represented by

defining the distribution of these species along the Golgi space length as three‐parameter

normal functions (Eq. 14), where , represents the peak enzyme concentration, , the

localization of the peak concentration and , the breadth of enzyme concentration. Eq. 15 is

presented as an example of the rate expressions included in the GlycoModel. The reaction

network considered in this model was developed to represent mAb Fc glycosylation and

consistsof77glycanslinkedthrough95reactionscatalysedbyeightenzymes[21].

Given that intracellular availability ofNSswasnot reported to control secretion of immature

glycans in thedatasetused for thiswork [39], their concentration in theGAwasassumed to

remain constant throughout culture. Golgi concentration of UDP‐GlcNAc and UDP‐Gal was

derived from the day 5 (120h) values reported for this dataset. These data were selected

because they were the lowest observed concentrations for both NSs during culture. Even at

theselowabundances,therespectiveenzymes(GnTI,GnTIIandGalT)wouldbesaturatedwith

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NSsaccordingtotheliteraturevaluesfor , (dissociationconstantsofNSsfromtheenzymes)

[43‐45]. All considered values for Golgi NS concentrations, along with their derivation are

presentedinSupplementarySection3andTableST2.

2.2.3. Modelcouplingstrategy

In contrast to previous integrated models, the work presented herein defines a direct

mechanistic link between mAb and the intracellular process of glycosylation (Eq. 16). In

addition,Eq.17hasbeendefinedtorepresenttheaccumulationofmAbglycoform i( )in

the extracellular environment as a function of the glycanmolar fraction at the exit of Golgi,

, [22,23].

9 2 Eq.16

, Eq.17

In Eq. 16, the linear velocitywithwhich secretory cargo traverses theGolgi space ( ), Golgi

volume ( ) and the concentration of Man9 glycoform entering the Golgi space

( 9 )areallproportionalto .GiventhatoneofthemajorfunctionsoftheERGICisto

concentratesecretorycargopriortoitstransporttotheGA[46],andthatthecargocontentsat

the inlet of the Golgi space are determined by the number of secretory vesicles that fuse to

generatenew cisterna [25, 30], it is possible to assume that the value for 9 remains

relativelyconstant.Thisparameter’svaluewasobtainedwithEq.16usinga 12.3

(the highest experimentally observed [39]), 0.045 (as derived from the Golgi

retentiontimereportedpreviously[21,24]),andanaveragemAbmolecularweight( )of

150kDa. This calculation yields a value of 9 100 . It is worth noting that the

highest observedintheconsideredexperimentaldataset[39]wasusedforthiscalculationtoAcc

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ensure theobtainedvalue for 9 is consistentwith those reportedpreviously [19‐21,

23,24].

As discussed in Section 1, and may vary [28, 29], thus potentially impacting Golgi

dynamicsand,consequently,glycosylation.Withtheseconsiderations,two“couplingstrategies”

havebeendefinedtoisolatetheinfluenceeachofthesevariableshasonthedynamicsofmAbFc

glycosylation. In the first coupling strategy, is assumed to remain constant,while the

variablewhichcontrolsGolgidynamics is . In thesecondcouplingstrategy, isassumed to

remainconstantwhile varies,thuscontrollingGolgidynamics.

2.2.3.1. CouplingStrategy1(CS1):variablelinearvelocitythroughGolgi

Here,theinletandoutletratesofsecretorycargotraversingtheGolgispace(thelinearvelocity

throughGolgi)areassumedtobeequalandproportionalto .Thisassumptionissupportedby

experimental evidence where variable transport rates between the ER and Golgi have been

observed in living cells [28]. Moreover, anterograde dynein/dynactin‐mediated vesicle

transporthasalsobeenobservedtooccuratvariablerates[27].Afundamentalconsequenceof

theinletandoutletratesbeingequalisthatnochangesinthevolumeofGolgiareassumedto

occur, regardless of changes in . In addition, we assume that COPI vesicle‐mediated

retrogradetransportofGRPsforrecyclingoccursatasufficientlyhighratethatensuresaquasi‐

steadystateconcentrationofresidentproteinswithinGolgiwhennochangeinresidentprotein

expressionoccurs.Havingdefinedthevaluesfor , and 9 , wasmade

afunctionofthe calculatedbytheCDmodelandwaslinkedtotheGlycoModelthroughEq.

13.

2.2.3.2. CouplingStrategy2(CS2):variableGolgivolume

CS2assumesthattherateatwhichsecretorymaterialleavestheGolgispaceisnotequaltothat

atwhichitarrives.Asaconsequence,increasedtransportfromERGICtotheGolgispaceresults

in an accumulation of Golgi structures, which in turn, leads to increased volume of the GA.

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Increasedproductsecretionisachievedbyalargervolumeofsecretorycomponentsleavingthe

GAataconstantrate.Thisbehaviourissupportedbyexperimentalevidencewherethevolume

ofERandGolgihasbeenobservedtoincreaseuponinducedsynthesisofarecombinantprotein

[29] and adetailed studywhere increased expression of secretorypathway componentswas

observed at very high (>100pg/cell/day), while the secretion rate ( ) was observed to

remainrelativelyconstant[34].

ChangesinGolgivolumewereimplementedbydefiningthedilutionfunctionpresentedinEq.

18.There,variationsin arecalculatedbasedonthe fromtheCDmodelusingEq.16

while assuming constant and 9 . The baseline Golgi volume ( , ), was

defined by solving Eq. 16 using constant values for 0.045 [21, 23] and

9 100 ,alongwitha 5.6

,asderivedfromtheexperimentaldata for

Phase I of culture. This value of was used, given it was the lowest observed in the

experimental dataset considered for this work [39]. The resulting , was

1.15 10 , which is within the same order of magnitude of Golgi volumes assumed in

previousmodels[19‐21,24].

,

Eq.18

Considering thatno large variations inGRPexpression (neither enzymesorNS transporters)

were reported for our considered dataset [39], the concentrations of glycosylation enzymes

(GE)withinGolgi(Eq.14)weremultipliedbythedilutioncoefficient(Eq.18)torepresent ‐

associatedvariationsinGolgivolume.Animportantadditionalconsiderationwasthatincreases

in Golgi volume were assumed to be irreversible within the timeframes associated with

transientreductionsin .Themechanismunderlyingthisassumptionisthattheredistribution

of secretory machinery from Golgi to other components of the pathway occurs over longer

periodsoftimewhencomparedtotheshort‐livedreductionsinproductsecretion.

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DespitetheassumedchangesinGolgivolume,theconcentrationofNSsandsecretorycargoin

this organelle are assumed to remain constant. As discussed previously, the reported

concentrationsofNSs(evenwhenconsideringmaximalGolgivolumedilution)wereobserved

tosaturatetheirrespectiveenzymes.Inturn,theconcentrationofsecretorycargowasassumed

constantgiventhedependencebetweencis‐Golgicisternaformationandthecargocapacityof

COPII‐coatedvesicles.ForallsimulationswithCS2, and 9 wereassumedtoremain

constantandequalto0.045 and100 ,respectively.

2.2.4. GlycoModelparameterestimation

Estimation of the unknown parameters in both CSs was performed in a series of sequential

stepsbasedonpreviousreports[21]:

• Step1:ThefractionofmAbglycoformi( )secretedduringthecellcultureintervalbetween

288 and336 was calculatedwith Eq. 19 using themAb glycan distributions reported at

each time point ( , and , , respectively) and the corresponding mAb titres

( and ).A fullderivationofEq.19 is available inFanet al. [39] and is

alsopresentedinSupplementarySection4ofthiswork.

, , Eq.19

• Step2:TheparametersdefiningthedistributionandconcentrationoftheGnTI,ManII,GnTII

andFucTglycosylationenzymes(GEs)alongtheGolgispace( , and inEq.14)were

estimated by obtaining the minimum amount of enzyme necessary to achieve the

distribution obtained from Step 1, while also considering a 12.3

. For this

estimation, the values for , were kept at the nominal (literature) values shown in

Supplementary Table ST3 (Suppl. Section 5). The interval between288 and336 was

selected for these estimations because it presented the highest , and thus, excludedAcc

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secretion of other high mannose glycans (Man9‐Man6) that were not observed

experimentally[39].

• Step3:Withtheparametersobtained inStep2, thedistributionandconcentrationofGalT

andSiaTwereestimatedbyobtainingtheminimumamountofenzymerequiredtoachieve

1%oftheG2FS1(Figure2)glycoform.

• Step4:With thedistributionof allGEsdefined throughSteps2and3, three , s forGalT

(eachaccountingfortheglycanbranchspecificityreportedforthisglycosyltransferase[45])

andone forSiaTwereestimatedusingexperimentally‐deriveddata for themAbglycoform

distribution determined during Phase I of culture and a corresponding value for of

5.6pg/cell/day(PhaseI).Thisglycoformdistributionwasusedfor , estimationbecauseit

presented thehighest fractionof galactosylated and sialylated glycoforms, thus facilitating

accurateandrobustestimatesfortheparameters.

Steps 2 and 3 were performed using the built‐in multiple‐shooting control vector

parametrization algorithm available in gPROMS 4.1.0 (www.psenterprise.com/gproms) [40].

The , values were obtained using the maximum likelihood parameter estimation activity

available in the same software package which has been briefly described in the CD model

section.Unlessstatedotherwise,allotherparametersforGolgienzymelocalisation( , )and

enzymekinetics( , , , )wereconsideredtobethesameasthoseusedbydelValetal.[21]

and are presented in Supplementary Tables ST3 and ST5 (Suppl. Section 7). All estimations

were performed on stand‐alone, steady‐state versions of the GlycoModel.Wemust highlight

that theonlyrequireddata inputs forestimationofallGlycoModelparameterswere themAb

glycan distributions secreted during the initial and final phases of culture, along with the

correspondingvaluesfor foreachphase.Acc

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3. Results

3.1. Culturedynamicsmodelperformance█Whatarethemajorresults?█

TheestimatedparametersfortheCDmodelarepresentedinSupplementaryTableST4(Suppl.

Section 6) and simulation results with the obtained parameters are compared with the

experimentaldatainFigure3.TheultimatepurposeoftheCDmodelwastoprovideanaccurate

representationofcellgrowthandmAbproductivitygiventhatthesewerethecriticalvariables

usedforcouplingwiththeGlycoModel.AscanbeseeninFigure3,theseculturevariableswere

capturedaccuratelyandshowgoodagreementwiththeexperimentaldataacrossallphasesof

culture.

3.1.1. GlycoModel enzyme distribution estimation█What are the major

results?█

Thedistributionandconcentrationofglycosylationenzymes(GEs)alongtheGolgispacewere

estimatedasdescribedinSection2.2.4.TheestimatedGEdistributionparametersforCS1and

CS2 are presented in Supplementary Table ST5 (Suppl. Section 7) and the resulting profiles

alongtheGolgispaceareshowninFigures4A(CS1)and4B(CS2).Althoughtheconcentrations

divergeinmagnitude(particularlyforManI,GnTIIandFucT),theirlocalisationanddistribution

are similar to those reported previously [21]. The estimated enzyme profiles show high co‐

localisationoftheManIandGnTIenzymes,a fairlynarrowprofileforFucTandrelatively low

abundancesoftheGalTandSiaTenzymesforbothcouplingstrategies.

Themaindifferencesbetweentheenzymeprofilesestimated forbothCSsare forManI,GnTII

and FucT. With the exception of GnTII, the profiles are narrower and the peak enzyme

concentrationishigherforCS1,whichislikelyduetotheassumptionsunderlyingeachmodel.

In CS1, the higher linear velocities of secretory cargo through Golgi reduce the time the

glycoproteinsubstratesareexposedtotheGEstherein.Inordertocompensateforthisreduced

reactiontime,higherpeakenzymeconcentrationswereestimatedand,becauseatotalenzyme

(integral over theGolgi space)minimisation criterionwas included, thewidth of the profiles

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wasestimatedtobenarrower.ItispossiblethatthistrendwasnotobservedforGnTIIbecause

theturnoverrateconsideredforthisenzymeisthehighestoftheglycosyltransferaseenzymes

includedforthereactionnetwork(SupplementaryTableST3).Analogously,thelowestturnover

ratecorrespondstoFucT,andthismaybethereasonwhytheprofileforthisenzymepresents

suchahighpeakconcentration.Conversely,theenzymedistributionsforCS2presentlowerand

broaderprofiles.Inthiscase,theholdingtimewithinGolgiremainsconstantbecausethelinear

velocity through Golgi is assumed to remain constant, and thus, lower peak enzyme

concentrationsareabletoachievethesamereactionconversions.

For both coupling strategies, the profiles for GalT and SiaTwere found to be similar. This is

likelyduetothelowvaluesforG2FandG2FS1assumedfortheirestimation.Itisworthnoting

that, although these profiles provide sufficient activity to satisfy the constraints defined for

parameterestimation,availabilityoftheseenzymesislikelytobehigherinvivo.Specifically,the

relativelylowgalactosylationandsialylationofmAbglycanshascommonlybeenattributedto

limitedaccessofGalTandSiaTtotheglycanspresentwithinthecrystallisablefragmentofmAbs

due to steric constraints [47]. Thus, the limited secretion of galactosylated and sialylated

glycanswouldbeinfluencedmoreheavilybytheaffinityoftheenzymesfortheglycans( , )

thanenzymeavailability.

3.1.2. GlycoModel , estimationandintegratedmodelsimulationresults█What

arethemajorresults?█

Oncetheparametersforenzymeconcentrationanddistributionwereobtained,thedissociation

constantsoftheglycoproteinsfromtheGEs( , )wereestimatedasdescribedinsection2.2.4.

The obtained parameters, along with the respective confidence intervals, are presented in

SupplementaryTableST6(Suppl.Section8).Simulationresultsforbothintegratedmodels(CS1

andCS2)obtainedwiththeestimatedCD,enzymeand , parametersarecomparedwiththe

experimentaldatareportedbyFanetal.[39]inFigures4C‐4H.There,itcanbeseenthatbothAcc

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coupling strategies follow very similar trends and reproduce the dynamic glycoform

distributiondatawell.

Ofparticularrelevancetothisworkisthatbothcouplingstrategiesarecapableofreproducing

the shift from a distribution of relativelymaturemAb glycoforms during the initial phase of

culture to onewith considerablyhigherproportionsofMan5andhypogalactosylated glycans

towards the end of culture. Specifically, both coupling strategies predict an increase in the

fractionofMan5glycoformfrom2.9%at120hofcultureto21%,at336h(Figure4C).Similarly,

the fractions of G1F glycoform (both on theα‐1,6 andα‐1,3 arms of the biantennary glycan

structure) were predicted to drop from 20% to 10% (Figure 4F) and from 9% to 4%,

respectively(Figure4G).

Thelargestdeviationsbetweenmodelandexperimentareobservedfortherelativeamountof

Man5 present observed during phase III of culture (Figure 4A). Both coupling strategies

underestimate the fraction of Man5 at 288h by approximately 2.2%. Additionally, smaller

deviationscanbeseenforthefractionofgalactosylatedglycansduringPhaseIIIofculture.Both

couplingstrategiesoverestimategalactosylationbybetween1%and2%duringthelatephases

ofculture.Iftheprecipitousdropinglycancomplexityindeedoccursduetoincreased ,then

underestimationofMan5andoverestimationofgalactosylationtowardstheendofculturemay

possiblybedue toexternaleffects thathavenotbeenconsidered in themodel.Suchexternal

effectscouldbedepletionofMn2+(whichisaknowncofactorforbothGnTIandGalT[10,48]),

orinhibitionofenzymeactivityduetoaccumulationofmetabolites,suchasammoniaorlactate

[49],towardsthelatterstagesofculture.

3.1.3. Man5secretionminimisation█Whatarethemajorresults?█

Considering that a likely cause for the observed increased secretion of Man5 is insufficient

availabilityofGnTIrelativetoincreasedsecretorycapacity[39],bothCSmodelswereusedto

determine thedegreeofGnTIoverexpression thatwouldkeepMan5 secretion to its baseline

levels(priortothetemperatureshift).Inordertodoso,anoptimisationfunctionwasdefinedto

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obtain the amount of GnTI required to maintain Man5 secretion below 2% (baseline level).

While only estimating , , an inherent assumption in this strategy is that all

overexpressedGnTIlocalisesinthesameregionofGolgi.

Theresultingenzymeprofilesforeachcouplingstrategyarecomparedwiththeoriginalonesin

Figure 5A and 5C. There, the increase in GnTI concentration is apparent, although the

localisationandwidthof theestimatedprofilesaresimilar to thoseobtainedprior toenzyme

overexpression.Throughthisstrategy,theobtained , valueswerefoundtobe0.93

for CS1 and 0.84 for CS2 (Supplementary Section 9). With these values, the total

concentrationsofGnTIwithin theGolgispace(the integralof over the lengthofGolgi)

were calculated tobe1.82 (CS1) and 1.98 (CS2), thus representinga3‐fold increase in

GnTI concentration compared to the original (highMan5 secretion) values for each coupling

strategy.

Thesimulatedend‐pointglycoformdistributionsforbothcouplingstrategiesafterinsilicoGnTI

overexpression are presented in Figures 5B and 5C. There, it can be seen that Man5 is

maintained at the desired low levels and that reduced secretion of this glycoform results in

higheraccumulationofmoreprocessedglycans,inparticularG0FandG1F.Specifically,Man5is

predictedtodecreasefrom21%to1.6%(CS1)and21%to1.5%(CS2);G0Fincreasesfrom56%

to69%forbothcouplingstrategies;andthefractionofG1Fgoesfrom14.3%(CS1)and14.7%

(CS2) to 17.2% and 17.8%, respectively. Dynamic profiles obtained with in silico GnTI

overexpressionarepresentedinSupplementaryFiguresS3andS4.

These results highlight the insilico glycoengineering capabilities of our integratedmodelling

frameworkandsimultaneouslyprovideadditionalevidence insupportofaschemewherethe

availability of glycosylation machinery relative to cellular secretory capacity influences the

glycosylationprocess.Acc

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4. Discussion

4.1. Modelformulation█Whatarethemajorresultsandconclusions?█

Basedonpreviousexperimentalwork,ourmotivationtodevelopthemodelpresentedherewas

to provide mechanistic links between variations in and the glycosylation process so that

dynamicchangesinmAbglycoformsecretionduringCHOcellculturecouldbedescribed.Akey

property of the experimental data used for this work was that expression of glycosylation

machinerywasnotobservedtovaryatdifferentspecificproductivities[39].Thisallowedusto

target theabundanceof glycosylationmachinery relative to cellular secretory capacity as the

likelymechanism causingdecreased glycanprocessing. Indoing so, an obvious alternative –

thatglycosylationenzymeactivitymaybecompromisedbylowtemperatureculture–wasnot

considered. This phenomenonwas not examined given that, to our knowledge, there are no

reports associating reducedGnTI activitywith lower temperatures. Indeed, animal and plant

GnTIhasbeen reported tohaveabroad rangeof temperatureoptimaspanning from25°C to

50°C[50],althoughstudiescitedthereinrefertorecombinantversionstheenzymeproducedin

E.coli.

Inparalleltothis,GnTIactivityhasbeenreportedtobenegativelyaffectedbyaccumulationof

ammonia during cell culture in a pH(Lactate)‐dependent manner [49]. We speculate that

deviationsbetweenmodelandexperimentobservedduringPhaseIIIofculturemaybedueto

theseeffects,whichwerenotincludedinourmodellingframework.Anadditionallimitationto

ourmodel is that,becauseNSavailability isassumed to remainunchanged,adirect linkwith

cellularmetabolismisnotprovided.

However,theintegratedmodellingstrategypresentedhereismodular.Thus,theCDmodelcan

be exchanged for more detailed descriptions of culture dynamics that include cellular

metabolismand cell populationdynamics [51, 52].More specifically, detailedCDmodels that

includeadetaileddescriptionofNSmetabolism[23]couldbereadilycoupledtotheGlycoModel

via andtheNStransportfunctions(fromthecytosoltoGolgi)thatarealreadyavailableinthe

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GlycoModel[21].Wemusthighlightthat,despitenotincludingadditionalmetaboliceffects,the

majorshifttoMan5andhypogalactosylatedglycansecretion(reportedbetweenPhasesIandII

[39]) was reproduced accurately by both integrated models, indicating that may indeed

impactrecombinantproteinglycosylation.

Indevelopingthetwocouplingstrategies,weaimedtoidentifywhichprocesswasmostlikelyto

generate the variations in mAb glycoform secretion observed in the experimental data. As

discussed extensively throughout themanuscript, CS1 assumes that determines the linear

rateofsecretorycargothroughtheGA.Insupportofthisassumptionispreviousworkwhere

Golgi dynamics havebeen visualised in living cells [28] andwhere the rate atwhichdynein‐

dynactin mediated transport of secretory vesicles has been found to be variable [27].

Furthermore, a mechanism whereby increased expression of GEs leads to higher COPII

assemblyand,consequentlytoincreasedGolgivolumehasbeenobservedexperimentally[30].

The proteomic data obtained for the considered experimental dataset found no significant

increaseinGEsorproteinsinvolvedinCOPII‐vesicleformationatdifferent s[39],suggesting

thatdenovosynthesisofGolgicomponentsmaynothavebeenprevalentduringculture.

TheabovefindingscontrastwithpreviousworkthathasobservedincreasedexpressionofCOPI

and COPII proteins in cell lines that present higher specific productivity [53]. Increased

expression of COPII proteins, in particular, could result in higher denovo synthesis of Golgi

componentsand,possibly, leadto increasedGolgivolume[30], thusfavouringthemechanism

depictedbyCS2.Inaddition,secretionkineticshavebeenreportedtoremainrelativelyconstant

while an overall increase in secretory pathway components was observed during culture of

hyper‐productiveCHOcells treatedwithsodiumbutyrateundermildhypothermicconditions

[34]. In line with these findings, increases in Golgi volume during synthesis of recombinant

proteinshasbeenobserved[29].However,whileusingthesamemethodsfordeterminingGolgi

volume, recent reports have found no correlation between the size of Golgi and increased

specificproductivity[54].Inconjunction,theaboveseeminglyconflictingfindingssuggestthat

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bothmechanisms(variable orvariable )couldoccursimultaneouslyandprevalenceof

oneovertheothermaybecelllinedependent.

4.2. Integrated model performance █What are the major results and

conclusions?█

Intermsofreproducingthedynamicchangesinglycoformdistributionduringculture,bothCSs

perform similarly well. The reason behind this is that they both present two alternative

mechanisms that result in the same phenomenon. In both cases, impaired glycan processing

with increased is defined to occur due to reduced exposure of secretory cargo to the GEs

withinGolgi.InCS1,reducedexposureoccursduetolowerGolgiholdingtimesassociatedwith

variationsin ,whileCS2representsreducedexposurebyconsideringthattheGEsarediluted

througha ‐inducedincreaseinGolgivolume.Giventhesimilaritiesinmodelperformance,the

current framework cannot identifywhichmechanism controls the process for this particular

cellline.

Regardlessofthecontrollingmechanism,wemusthighlightthatadequatemodelperformance

supports the hypothesis that availability of glycosylation machinery relative to cell specific

productivityistheunderlyingcausebehindsecretionoflessprocessedmAbglycoformsupona

shift to increased . In particular, estimation of the glycosylation enzyme distribution

parameters was performed using a steady‐state version of the GlycoModel utilising a single

data‐point (corresponding to the time interval between 288h and 336h). With the obtained

parameters, the changes in described by the CD model (which was parameterised

independently) generated the experimentally‐observed shift to increased Man5 secretion

without any additional input. This was observed for both coupling strategies, and in itself,

indicates that the relationshipbetween andavailabilityof glycosylationmachinery interact

toquantitativelyreproducethedynamicchangesobservedinmAbglycoformsecretion.Acc

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With these results and previous experimental evidence, it is possible to conclude that the

relativeabundanceofglycosylationmachineryrelativetocellularsecretorycapacitymayplaya

key role in the glycosylation process. To our knowledge, this has not been confirmed

experimentally, although specific productivity has been identified to potentially influence

recombinant protein glycosylation [32, 38, 39]. Contrastingly, several reportswhere product

glycosylation has beenmonitored under high productivity conditions (temperature shift and

sodiumbutyrate treatment) have not found significant impacts on product glycosylation [33,

37].

Taking these findings into consideration and linking themwith the results of our modelling

framework,itispossiblethatthecorrelationbetween andreducedglycanprocessinghasnot

beenmore broadly established due to cell line‐specific variations. A shift to secretion of less

processedglycanswouldonlybeobservedifglycosylationmachineryissufficientlyavailableat

low s, but becomes limiting at higher productivities. If the baseline levels of glycosylation

machineryarehighenoughtocopewithhigher s,thedistributionofsecretedglycanswould

remainrelativelyunchanged.Itwouldbeinterestingtoseeifthesepropertiesareobservedina

celllinethatexhibitsverysimilardynamictrendsinMan5secretionduringculture[10].

Industrially, the ramifications of this hypothesis would extend to cell‐line selection and

bioprocessoptimisation.Acelllinewithrelativelylowbaselinelevelsof,forexample,GnTImay

be selected for further development, given that, under the examined conditions, it produces

acceptablelevelsofMan5.However,whenculturedunderconditionsthatincreaseproductivity,

an undesired shift to higherMan5 glycoform secretionmay occur due to limitations in GnTI

availabilityrelativetoahigher .Fromthisperspective,monitoringexpressionofdifferentGEs

relativetospecificproductivityduringearlystagesofbioprocessdevelopmentmayproveuseful

in reducing the probability of encountering shifts in glycosylation‐associated quality during

latterstagesofbioprocessdevelopment.Acc

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ResultsobtainedwiththeinsilicoGnTIoverexpressionstrategydescribedinthisworkprovide

additional support for thehypothesis that correlates variations in withdecreased secreted

glycancomplexity.WhilesimulatingoverexpressionofGnTI,enoughofthisenzymeisprovided

tomaintainahighenoughrateofMan5processingevenatthehighest values.Thus,secretion

ofthisimmaturemAbglycoformisminimised.AlthoughtheresultsobtainedfrominsilicoGnTI

overexpressionareyettobeexperimentallyconfirmed,suchacomputationalstrategycouldbe

used toestimate theexpression levelsofGEsrequired tomaintaincertainproductglycoform

distributionatpredefinedlevelsofproductivity.This,inturn,couldaidincell‐lineselectionand

engineeringduringearlystagesofbioprocessdevelopment.

In conclusion, the modelling framework presented herein is the first to provide a detailed

mechanistic link describing how cell specific productivity may impact monoclonal antibody

glycosylation.Thiscomputationaltoolcouldaidincelllineselectionandengineeringduringthe

early stages of bioprocess development, and if linkedwithmore detailedmodels for cellular

metabolism,couldbeemployedtocontrolpharmaceuticalbioprocessestoensureproductionof

therapeuticproteinswithconsistentandoptimalglycosylationprofiles.

Acknowledgments

Wewould like to thankDrMikaelRørdamAndersen, ProfMichael JBetenbaugh andDrCleo

Kontoravdi forproviding theexperimentaldataused for thiswork.ThegPROMScode for the

GlycoModel was kindly provided by Dr Cleo Kontoravdi. IJV would also like to thank Prof

MohamedAlRubeai,DrCleoKontoravdiandDrSarantosKyriakopoulosforfruitfuldiscussions

on theworkpresented in thismanuscript.YFwas fundedbySymphogenA/Sand theDanish

Agency for Science, Technology and Innovationunder the Industrial PhD grant – Symphogen

01/2012‐12/2014.

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ConflictofInterest

Theauthorsdeclarenofinancialorcommercialconflictofinterest.

Notationandsymbols

• :netspecificgrowthrate• :specificmAbsecretionrate• :specificglucoseconsumptionrate• , :numberofcellsaccumulateduptotime • , :amountofmAbaccumulateduptotime • , :cumulativeamountofglucoseconsumeduptotime • :integralviablecellnumberattime • :fractionofmAbglycoform secretedoveraspecifiedtimeinterval• :liquidvolumeinthecellcultureflask• :viablecelldensity• :deadcelldensity• :glucoseconcentration• :lactateconcentration• :antibody(product)concentration• :volumetricflowrateoffeed• :volumetricflowrateofsampleremovedfromflask• :specificgrowthrate• :specificdeathrate• , :specificlactatesecretionrate• , :specificlactateconsumptionrate• , :maximumspecificgrowthrate• , :maximumspecificdeathrate• :Cellularcarryingcapacity• , :Monodconstantforgrowthonglucose• , :inversesaturationconstantforthespecificdeathrate• ⁄ :yieldcoefficientofcellsfromglucose• ⁄ :yieldcoefficientoflactatefromglucoseconsumption• ⁄ :yieldcoefficientofcellsfromlactateconsumption• , :Monodconstantforlactateconsumption• :mAbglycoform • :Nucleotidesugar (UDP‐GlcNAc,GDP‐Fuc,UDP‐GalorCMP‐Neu5Ac)• :Nucleotideby‐productk(UDP,GDPorCMP)• :linearvelocityofsecretorycargothroughtheGolgiapparatus• :normalizedaxialcoordinateoftheGolgiapparatus

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• , :stoichiometriccoefficientofglycoform inreaction • :reactionrate • :concentrationofenzyme alongtheaxialcoordinateofGolgi• , :parameterdescribingthepeakconcentrationofenzyme withinGolgi• , :parameterdefiningthelocationofthepeakconcentrationofenzyme withinGolgi• :parameterdefiningthewidthoftheconcentrationprofileofenzyme • , :turnoverrateforenzyme • , / :dissociationconstantofmAbglycoform fromenzyme • , / :dissociationconstantofnucleotidesugar fromenzyme • :competingmAbglycoformsubstratesforthesameenzyme• , / :dissociationconstantofcompetingmAbglycoform fromenzyme • , / :inhibitionconstantofby‐product onenzyme • :mAbglycoformwithadditionalsugarresidueadded• , / :dissociationconstantofmAbglycoform 1 fromenzyme • 9 :concentrationoftheMan9mAbglycoformattheinletofGolgi 0 • :meanmAbmolecularweight• :volumeoftheGolgiapparatus• , :volumeoftheGolgiapparatusatbaselineproductivity• , :molarfractionofmAbglycoform attheoutletofGolgi 1

• :glycosylationenzymedilutionfactor

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FigureLegends

Figure1.MechanismsrelatingGolgiglycosylationwith [25,26]

A) Secretory cargo ( ) is transported from the endoplasmic reticulum (ER) to the ER‐Golgi

intermediatecompartment(ERGIC)viaCOPII‐coatedvesicles(step1).TheERGICconcentrates

thesecretorycargoandaidsinsortingGolgiresidentproteins( )(step2).Thesecretorycargo

isthentransportedfromERGICtotheinletoftheGolgispace,where,ifcisternalmaturationis

considered,thevesiclesfusetogenerateanewGolgicompartment(step3).Thenewlyformed,

cargo‐containing cisternawill thenprogress forwardalong theGolgi spacewhile theprotein‐

bound glycans are processed by the glycosylation enzymes (GEs). Upon traversing the Golgi

space,thecargoistransportedtothecytoplasmicmembraneforsecretion(step5).Thiswork

considers two distinct mechanisms to describe changes along the secretory pathway in the

eventofincreasedspecificproductivity.Inthefirst(CS1),higherproductionofsecretorycargo

is assumed to increase the linear velocity ( )withwhich the cisternaeprogress through the

Golgispace.TherateofCOPI‐vesiclemediatedretrogradetransportisalsoassumedtoincrease

so that Golgi resident proteins (nucleotide sugar transporters and GEs) are maintained at

relativelyconstantvalueswithinGolgi(B).Thesecondmechanism(CS2)assumesthatthelinear

rate with which cisternae migrate through Golgi remains unchanged. Because of this, more

anterogradeCOPII‐coatedvesiclesaccumulateattheproximalsideoftheGolgispaceandfuseto

generate larger cisternae, thus causing an overall increase inGolgi volume and a consequent

dilutionofresidentproteinstherein(C).

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Figure2.Modeldevelopmentstrategy

The model development strategy employed in this work is presented (A), where an

unstructuredandunsegregatedmodelforcellculturedynamicsiscoupledtoasingle‐cellmodel

formAbFcglycosylationviathespecificproductivityoftherecombinantproduct( )through

thetwocouplingstrategies(CS1andCS2)presentedinFigure1.Asimplifiedreactionnetwork

detailingtheglycansobservedinthisworkisalsoshown(B).ThemAb‐boundMan9glycoform

enterstheGolgiapparatus(GA)fromtheendoplasmicreticulum(ER)andundergoesaseriesof

enzymatically‐catalysed reactions where monosaccharides are cleaved off or added to the

glycan structure. Once the glycoprotein cargo traverses the GA, it is assumed to be secreted

from the cell. The dashed tube surrounding the reaction network represents the Golgi space

through which the cisternae carrying the secretory cargo flow [21]. Notation for all

oligosaccharides is shownbelowthe correspondingstructuresand thenamesof theenzymes

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whichcatalyseeachglycosylationreactionarepresentedabovethearrows.Themetabolicco‐

substratesforthemonosaccharideadditionreactions(nucleotidesugars)areshownbelowthe

arrows (UDP‐GlcNAc, GDP‐Fuc, UDP‐Gal and CMP‐Neu5Ac). Structures and glycosidic bond

configurationsfortheMan9glycanenteringtheGA(C)andacomplex,biantennary,sialylated

andfucosylatedoligosaccharidestructure(D)arealsoshown.

Figure3.Cellculturedynamics

A)Experimentaldataforviablecelldensity( ),deadcelldensity( ),B)mAbtitre( ),C)

extracellular glucose concentration ( ) and D) extracellular lactate ( ) are compared with

simulation results (lines). The dashed grey lines indicate the three distinct culture phases

defined in thiswork. Phase I is culture at 37°C, Phase II is culture at 33.5°C andPhase III is

stationarygrowthat33.5°C.Theerrorbarsincludedwiththeexperimentaldatacorrespondto

onestandarddeviationofduplicateexperiments.

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Figure4.Comparisonofmodelcouplingstrategies

The estimated distribution of GEs (ManI, GnTI, ManII, GnTII, FucT, GalT and SiaT) along the

normalised length of Golgi for coupling strategies CS1 and CS2 are presented in A and B,

respectively. Glycoform distribution simulation results obtained after , estimation for CS1

andCS2(solidanddashedlines,respectively)arecomparedwiththeexperimentaldata( )in

C‐H.DataforthesixmajorobservedmAbFc‐boundglycansispresented:Man5(A),A1G0F(B),

G0F(C),G1(1,6)F(D),G1(1,3)F(E)andG2F(F).Thedashedgreylinesmarkthethreephasesof

culturementionedthroughoutthemanuscript.

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Figure5.InsilicominimisationofMan5secretion

The GnTI profile that was found to minimise secretion of Man5 glycans (dashed line) is

compared with the high Man5 enzyme distribution for CS1 (A). The end‐point glycoform

distributioncalculatedforCS1withnomodificationtoGnTIavailability(solidbars)iscompared

withtheoneobtained for insilicoGnTIoverexpression(beltedpattern) in(B).Thesamedata

correspondingtoCS2ispresentedin(C)and(D).Duetodifferencesinscale,theaxisontheleft

of each bar chart corresponds to the Man5 and G0F glycans and the axis on the right

correspondstotheremainingfiveglycans.

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