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DRAFT Achieving intensification and flexibility in virus purification with state- of - the- art chromatography tools Authors: Mochao Zhao, Melissa Vandersluis Abstract Vaccines greatly reduce disease, disability, death, and inequity worldwide. They even permitted total eradication of Small Pox. However, most vaccines available today are still manufactured with the original process technologies in complex and capital-intensive facilities. The labor-intensive, low-yield and low throughput processes, and the lack of manufacturing flexibility, diminish affordability for developing countries, forcing manufacturers to address the problem by supplying these markets with subsidized products and/or non-sustainable prices. Advancements in vaccines manufacturing would benefit both global health and the industry. Needs for better processes Viruses, widely known for their prophylactic use as vaccines in the biotechnology world, are also gaining popularity in therapeutic fields. Viral vectors are being used as delivery vehicles in more than two-thirds of gene therapy clinical trials. Oncolytic virotherapies, with 2 commercially available and 48 currently in clinical pipelines, represent the next potential breakthrough therapeutic modalities for cancer treatment. However, despite of the proven success of viral vaccines or therapeutic promises of emerging gene and viral therapies, there are still multiple barriers to extending the access to these products around the world. The lack of breakthroughs in manufacturing technology is one of them. While current viral vaccine manufacturing methods are in some cases effective for small-scale production, these methods share several critical shortcomings: they are too slow, too complicated, lack robustness, and require expensive specialized facilities and equipment for large-scale production. The lack of modern, efficient production technology is restricting progress on several fronts (bb). Due to high capital and development costs and the low product profitability created by high manufacturing costs and limits on product pricing, niche vaccine opportunities are seen as financially risky, with low probability of breakeven or profitability. Promising new vaccines developed from large viruses remain undeveloped due to the lack of viable processing capabilities to handle the large viruses. Likewise, progress in development of oncolytic virotherapies is limited because large doses of highly purified material are required, but efficient manufacturing processes are lacking (cc). Meanwhile, viral vectors have been widely exploited for gene delivery approaches, further increasing the demand for large-scale production of highly purified viral material. In all cases, progress is directly limited by gaps in manufacturing technologies.

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Page 1: Achieving intensification and flexibility in virus purification with … · 2017. 10. 9. · Achieving intensification and flexibility in virus purification with state-of-the-art

DRAFT

Achieving intensification and flexibility in virus purification with state-of-the-art chromatography tools

Authors:MochaoZhao,MelissaVandersluis

Abstract Vaccinesgreatlyreducedisease,disability,death,andinequityworldwide.TheyevenpermittedtotaleradicationofSmallPox.However,mostvaccinesavailabletodayarestillmanufacturedwiththeoriginalprocesstechnologiesincomplexandcapital-intensivefacilities.Thelabor-intensive,low-yieldandlowthroughputprocesses,andthelackofmanufacturingflexibility,diminishaffordabilityfordevelopingcountries,forcingmanufacturerstoaddresstheproblembysupplyingthesemarketswithsubsidizedproductsand/ornon-sustainableprices.Advancementsinvaccinesmanufacturingwouldbenefitbothglobalhealthandtheindustry.

Needs for better processes Viruses,widelyknownfortheirprophylacticuseasvaccinesinthebiotechnologyworld,arealsogainingpopularityintherapeuticfields.Viralvectorsarebeingusedasdeliveryvehiclesinmorethantwo-thirdsofgenetherapyclinicaltrials.Oncolyticvirotherapies,with2commerciallyavailableand48currentlyinclinicalpipelines,representthenextpotentialbreakthroughtherapeuticmodalitiesforcancertreatment.However,despiteoftheprovensuccessofviralvaccinesortherapeuticpromisesofemerginggeneandviraltherapies,therearestillmultiplebarrierstoextendingtheaccesstotheseproductsaroundtheworld.Thelackofbreakthroughsinmanufacturingtechnologyisoneofthem.Whilecurrentviralvaccinemanufacturingmethodsareinsomecaseseffectiveforsmall-scaleproduction,thesemethodsshareseveralcriticalshortcomings:theyaretooslow,toocomplicated,lackrobustness,andrequireexpensivespecializedfacilitiesandequipmentforlarge-scaleproduction.Thelackofmodern,efficientproductiontechnologyisrestrictingprogressonseveralfronts(bb).Duetohighcapitalanddevelopmentcostsandthelowproductprofitabilitycreatedbyhighmanufacturingcostsandlimitsonproductpricing,nichevaccineopportunitiesareseenasfinanciallyrisky,withlowprobabilityofbreakevenorprofitability.Promisingnewvaccinesdevelopedfromlargevirusesremainundevelopedduetothelackofviableprocessingcapabilitiestohandlethelargeviruses.Likewise,progressindevelopmentofoncolyticvirotherapiesislimitedbecauselargedosesofhighlypurifiedmaterialarerequired,butefficientmanufacturingprocessesarelacking(cc).Meanwhile,viralvectorshavebeenwidelyexploitedforgenedeliveryapproaches,furtherincreasingthedemandforlarge-scaleproductionofhighlypurifiedviralmaterial.Inallcases,progressisdirectlylimitedbygapsinmanufacturingtechnologies.

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The Solution Resides in Innovation State-of-the-artvirusproductionprocessesandtechnologiesholdthepromiseofenablingproductionofnewvaccinesaswellasviralvectorplatformsforotherapplications,whilealsostreamliningandstrengtheningcurrentprocesses.Thesetechnologies,manyofwhicharebeingusedsuccessfullyinmodernbiotherapeuticsmanufacturing,canalsocreatedramaticcostandproductivityimprovementsforvirusmanufacturing(dd).

Anewgenerationofhigh-productivity,disposableprocessingtechnologiesgreatlysimplifyproductionarchitectureandreducefacilityfootprint.Inupstreamprocesses,stainlesssteelbioreactorsandmicro-carriersarebeingreplacedbymicrofibers(ex.iCELLis)thatcanachievecelldensityupto150millioncells/mL(ee,ff).Thenextgenerationfixed-bedcontinuousperfusionbioreactorsdevelopedbyUnivercellscanreachhighcelldensitywith50-70%volumereduction(gg).Withreducedbioreactorsize,mediausageaswellasfacilitydesignandcostcanbesignificantlyimproved.Indownstreamprocesses,advancementsinchromatographytechnologysuchasaffinitymediaspecificallyforviruscaptureandsingle-usehigh-productivitymembranechromatographyofferseveralperformanceandcostadvantagesoverthetraditionalpurificationtechniques.Withapowerfulcapturetool,theprocessarchitecturecanbesimplifiedwithfewerunitoperationsyetstillmaintaincriticalqualityattributes,leadingtosignificantcostsavingsaslessspace,utilities,andlabourarerequired.Single-use,high-throughputmembranecolumnsfurtherreducevalidation,cleaning,andstorage-relatedexpenseswhileimprovingproductivityviahighbindingcapacitiesandfastflowrates.Theeaseofscalabilityofchromatographycolumnsalsoenablessmoothproductiontransitionfromthelabbenchtothemanufacturingsite.Whencombined,newsingle-use,highproductivityprocesstechnologiescanovercomethemanufacturingconstraintsthathavelimitedmorewidespreadproliferationofvaccineuse,whilealsoopeningdoorstopromisingnewvaccinesandviral-basedtreatments.Replacingtraditionallarge,inflexibleandcomplexstainlesssteeloperationswithsmallfootprintfacilitiesenablesquickbatch-to-batchturnoverandrapidchangeoverbetweendifferentproducts.Thesmaller,morecompactprocessarchitectureallowsvirusestobeprocessedinsmallfacilitiesacrossmultiplegeographies,withthepromiseofeventuallyplacingproductionproximatetothepointofcare.Inaddition,simplified,smallfootprintprocessesenableflexibleprocessingwhichallowanewlevelofagilityforrespondingtochangesindemandandhandlingmulti-productmanufacturing.

Acornerstoneofthenewpurificationtechnologiesishighproductivitymembranechromatography,astate-of-the-arttechnologythatcombineshighbindingcapacityandrapidmasstransfertoimprovepurificationthroughput.High-productivitymembranechromatographywithcommonmodalities(ex.cationexchange,anionexchange,ormixed-mode)havebeenavailableandimplementedinmanybiotherapeuticsmanufacturingprocess.Insomecases,suchmembraneswithhighselectivitycandeliversufficientpuritylevelinasinglestep,makingsingle-steppurificationaviablesolution.Inaddition,affinitychromatographycanbecombinedwithmembranechromatographytoreplacemanypurificationunitsforhighlyintensifiedandproductiveprocesses.Threecasesstudiesofprocessintensificationusingstate-of-the-artchromatographytoolsarediscussedbelow.

Case Study 1: Newcastle Disease Virus single step purification using HD-Q Inthisexample,engineeredNewcastleDiseaseVirus(NDV)producedforoncolyticvirotherapyisamplifiedinembryonatedeggsandpurifiedfromtheallantoicfluid.Theconventionalcentrifugation-

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basedpurificationmethodresultsinlowvirusrecovery(12%-35%)andonlypartialremovalofimpurities(upto6.3mghostcellproteinleftafterTFFandUC)(hh).

Thisconventionalpurificationschemeisslow,non-scalable,labor-intensiveandalsoleadstolowproductivity,non-optimalprocesseconomics,andhighfailureratesinamanufacturingenvironment.Consequently,themanufacturersofNDVforoncolytictherapywilllikelysufferfromthehighcostofgoodsandinabilitytoreliablymeetmarketdemand.Thisapproachforcesatradeoffbetweenproductpurityandproductrecovery.

Thenewsingle-stepmembranechromatographymethodforpurifyingengineeredNDVisfast,scalable,andachieveshighvirusrecovery(78.1%)with>99%purity(hh).

FigureYY:

Case Study 2: Influenza Single-Step purification using affinity membrane

Inthisexample,affinitymembraneswereemployedtopurifyinfluenzavaccinefromallantoicfluidharvest.

Theaffinitymembrane’shighproductivityenabledprocessintensification,resultinginsuccessfulpurificationinasinglestep:targetpurity,highcapacity,andhighrecoveryareallachieved(99.9%HCPclearance(3LRV),87%yield,and30-foldconcentration)(aa).Theprototypeaffinitymembranesachievedperformanceequaltoorexceedingcommercialaffinityresins.

Theaffinitymembrane’shighproductivityenables100Xsmallercolumns(comparedtocommercialresins)forsamebatchsize.Inthisexample,a500mLmembranecolumncanpurifyallantoicfluidharvestfrom1Millionembryonatedchickeneggsin1shift(8h,average104HAU/mL@5mL/egg).

FigureXX:Comparisonofinfluenzapurificationusingaffinityresinsandaffinitymembranes.Productivitycalculationsarebasedonahypotheticalloadof200columnvolumes(CV)plus20CVforadditionalequilibrationandcleaningstepsforeachproduct.

ImpurityClearance Productivity

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Media BC(HAU/mL) Recovery Virusin

FTFlowrate(CV/min)

CycleTime(min)

Productivity(HAU/L.h)

AffinityResin#1 1x106 96% 2% 0.7 315 1.9E+08

AffinityResin#2 7x105 87% 4% 1 220 1.9E+08

AffinityResin#3 2x105 74% NA 2.9 76 1.6E+08

PrototypeH15 2x106 81% 10% 33 7 1.8E+10

PrototypeX40 2x106 95% 3.6% 33 7 1.8E+10

Case Study 3: Modelling a VLP-based vaccine process Avaccinemanufacturerre-engineereditstraditionalvaccinepurificationprocessforVLP-basedvaccines,enabledlargelybythepowerofaffinitymembraneperformance.Thenewmembrane-basedprocessaccomplishedthepurificationinthreeunitoperations,ascomparedtothirteenoperationsinthebaselineprocess.Thesimplifiedprocessresultedinmuchgreaterproductrevoery(lessproductloss),whichfurtherenableddownsizingoftherequiredupstreamoperations.Thisupstreamdownsizingenabledtheadoptionofsimpler,single-usebioreactors.Thenewprocessmodelsignificantlyreducedthecapitalinvestmentrequired,whilealsoimprovingcostperdose,processreliabilityandplantfootprint(CANWEQUANTIFYANYOFTHESECAPITALANDCOSTIMPROVEMENTS??).

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(modellingslidesbelowmaybeeliminatedforfinalsubmission)

Conclusion Thehighproductivityandcost-efficiencyofthesingle-usechromatographymembraneprocessenablefavorableprocesseconomicscomparedtothelabor-andcapital-intensivereferenceprocesses.The

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simplifiedarchitectureofthemembraneprocess,combinedwithpotentiallyfullycontinuousandclosed(aseptic)operation,shouldenablemanufacturinginatrulyflexible,lowcostandsmallfootprintfacility.Thehighthroughputmembranepurificationprocesscanimprovecurrentegg-basedvirusprocesses,andwillalsomarryperfectlywithimproved,high-throughputupstreamprocess(ex.adaptNDVstraintocellcultureandimplementintoascalablemanufacturingstrategyusingPalliCELLisreactor).

References (aa)R.Jacquemart,WorldVaccineCongress(Washington,DC,2017)

(bb)A.Pralong,H.L.Levine,J.Lilja,A.Gaasvik,andH.Hummel,Eng.LifeSci.14(3),244-253(2014)

(cc)S.J.Russell,K.Peng,andJ.C.Bell,NatBiotechnol.30(7),658-670(2012)

(dd)R.Jacquemart,M.Vandersluis,M.Zhao,K.Sukhija,N.Sidhu,andJ.Stout,ComputationalandStructuralBiotechnologyJournal14,309-318(2016)

(ee)R.Rajendran,R.Lingala,S.K.Vuppu,B.O.Bandi,E.Manickam,S.R.Macherla,S.Dubois,N.Havelange,andK.Maithal,AMBExpress4(25)(2014)

(ff)PallLifeSciences,“iCELLisBioreactors,”ApplicationNote(2016)

(gg)Univercells,“Single-useperfusiontechwillcutcostofvaccineproduction,saysUnivercells,”PressRelease(2016)

(hh)R.Jacquemart,M.Zhao,X.Shang,J.Stout,L.A.Santry,K.Matuszewska,B.W.Bridle,J.J.Petrik,andS.K.Wootton,WorldVaccineCongressEurope(Barcelona,2016)