Next Generation Biopharma Manufacturing Facilities

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    Next generation biopharma

    manufacturing facilitiesTrends for biotherapeutics and their production

    PABME, Dubai, April 29 2008Dr. Gnter Jagschies, Senior Director R&DStrategic Customer RelationsGE Healthcare Bio-Sciences ABUppsala, Sweden

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    Overview

    Pressure on pipeline efficiency and cost of treatment

    Focus on manufacturing efficiency and costs

    Varying API categories and production sources

    Widely varying production scales

    Switch from dedicated to multiproduct facilities

    Flexibility, agility, cost efficiency

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    Top selling biopharmaceuticals 2007

    FVIII, F VIIYesNovo Nordisk, Wyeth, Bayer, Baxter 4,518Clotting factors

    MabYesGenentech 5,527Rituxan / MabThera

    VaccineNoMerck&Co 1,481Gardasil

    MabYesMerck-Serono, BMS 1,439Erbitux

    Mab fragmentNoGenentech, Novartis 1,386Lucentis

    1,144

    >1,200

    2,439

    2,762

    3,000

    3,605

    4,114

    4,277

    4,862

    4,948

    5,275

    8,223

    10,926

    11,101

    US $ M

    MabYesAbbott Laboratories Humira

    Growth

    No

    Yes

    No

    No

    No

    Yes

    Partly

    Yes

    Yes

    Yes

    Partly

    No

    Yes

    Mammaliancells

    ErythropoietinAmgen, Roche, J&JEPOs

    MabJ&J, Schering-PloughRemicade

    Fc fusion proteinAmgen, WyethEnbrel

    rec hInsulinEli Lilly, Novo Nordisk, Sanofi-AventisInsulins

    LMW HeparinSanofi-AventisLovenox

    Glucocerebrosidase

    Mab

    Vaccine

    rec hGH

    Mab

    G-CSF

    Mab

    alpha/beta-Interferon

    Substance

    GenzymeCerezyme

    MedImmuneSynagis

    WyethPrevnar / Prevenar

    Pfizer, Novo Nordisk, Eli Lilly, SeronoGrowth hormones

    GenentechAvastin

    AmgenNeulasta / Neupogen

    GenentechHerceptin

    Schering-Plough, Roche, Biogen IdecBayer-Schering, Merck-Serono

    Interferons

    Companies countedBranded productProduct category

    Biopharma blockbusters 2007: US $ 82,3 billionMab blockbusters 2007: US $ 26,5 billion

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    Cost of treatment, example

    0

    5.000

    10.000

    15.000

    20.000

    25.000

    Today -10% -20% -30% -40% -75%

    Typical current level

    Level of new or

    established alternative

    ?

    ?

    ?

    Future level?

    Market forces:- Public health care systems- Shorter time to next innovation- Biosimilars

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    New(?) Challenges

    Flexibility

    AgilitySpeed

    Efficiency

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    Source: Genetic Engineering News, 2002

    20%

    32%

    6%

    6%

    3%

    13%

    20% Depreciation

    Labour

    Media

    other Raw Materials

    Protein A resin

    other Consumables

    Insurances, Taxes,

    Maintenance

    D

    C

    I,T,M

    RML

    M

    Production EconomicsOperating Costs in Mab Production

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    What is best-in-class performance?

    Best in class performance isfoundation for the future

    ac y u za on = -

    Cost = 15% CoS (100 USD/g)

    Process yield = 70-80%

    Product titer = 5 g/LTime = 10 day upstream

    2 days downstream

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    Mabs, rProteins, Vaccines, Cells, Genes

    2006 2004Pharmaceuticals Research & Manufacturing Association

    (PhRMA) clinical trials summary (2004-2006):Mabs: 76 160

    rProteins: 57 94

    @ success rate: 20% > 50 approvals by2012

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    Mabs and mammalian cells dominate(only products / API categories > US $ 1 billion included)

    26.500

    51.900

    3.920

    Mabs

    rProteins

    Vaccines

    51.484

    30.800

    Mammalian cells

    Other cells

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    Biopharma production challenges(Production volume and revenue map, 2006 data)

    Pharmacy list prices 2006, available packages:Arzneimittelkompendium (CH), MediMedia Gelbe ListePharmaindex (GER), RxUSA.com Pharmacy (USA)

    Annual global sales 2006: Annual reports 2006 Plasma products: Marketing Research Bureau 2004

    1

    10

    100

    1.000

    10.000

    100.000

    1.000.000

    10.000.000

    100.000.000

    0,01 0,10 1,00 10,00 100,00 1.000,00 10.000,00 100.000,00 1.000.000,00

    Annual production volume [kg]

    Pharmacypricevalue[USD/g,2006]

    HSA, plasma

    Huminsulin

    Rituxan/MabThera

    HumalogAvastin

    IVIG, plasma

    EnbrelHumira

    RemicadeHerceptin

    SynagisPulmozyme

    NeulastaReoPro

    Aranesp

    ReFacto

    Neupogen

    BeneFIX

    KogenateAvonex

    PegaSysRebif

    NovoSeven

    Humatrope

    Xolair

    Advate

    Coagulation factor VIII EPO, Factor IX, VII, interferonsl HGH, low dose antibodiesn High dose antibodies, fusion proteins Insulinsr Plasma proteins

    Most future Mabswill require annual

    capacity of 100-500 kg

    Some Mabswill require annual

    capacity of 1-5 tons

    Insulins

    1-5 tons

    Plasma proteins50-500 tons

    Most rProteinswill require annualcapacity of 1-10 kg

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    The challenge is the supply of vaccines

    Capacity Time

    0

    500

    1000

    1500

    2000

    2500

    milliondoses

    2006 PandemicPlanning

    There is a huge gap between the expecteddemand and the current capacity Most countries are looking for in-country

    domestic solutions WHO is driving local capacity build up

    20102004 WHO

    Currently the manufacturing timeis ~6-9 months Need of faster supply less than 3 months

    production time Difficult and time consuming to scale up with

    old technology

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    The vaccine landscape is changing and is

    moving to new manufacturing methodsEgg-basedproductiontechnology

    Cell Culture-basedproductiontechnology

    Cell Freeproductiontechnology

    System Eggs Mammalian Cells Insect and Bacterial Cells Recomb Cells

    Lead Times 6-9 months ~6 months ~3 months Days?Maturity On the market New on the market In 2-4 years time -

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    Many facilities have

    brand new installations and up to 25year old installations, running with newand old processes.

    dedicated one-product or multi-product setups.

    a degree of mismatch betweencurrent bioreactor output and DSP line

    dimensions chosen at the time of facilitydesign.

    limited flexibility!

    Large / modern biopharma facilities

    Genentech, Oceanside, CA

    Image: Boehringer Ingelheim GmbH

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    Production setup: 6 fermentors 1 DSP

    Mab Cell Culture(6x 2.000 L, 5 g/L)

    Cell Removal

    Capture(1x 120 cm , 30 cm height)

    Polishing 1(1x 80 cm , 25 cm height)

    Polishing 2(1x 60 cm , 23 cm height)

    UF/DFFormulation

    Virus Removal

    Virus Inactivation

    Mab Cell Culture(6x 15.000 L, 5 g/L)

    Cell Removal

    Capture(1x 160 cm , 40 cm height)

    Polishing 1(1x 160 cm , 42 cm height)

    Polishing 2(1x 140 cm , 30 cm height)

    UF/DFFormulation

    Virus Removal

    Virus Inactivation

    - 313 L bed volume- 40 g/L capacity- one cycle

    - 780 L bed volume- 40 g/L capacity- three cycles

    10-ton/yr

    scenario

    1-ton/yr

    scenario

    - 125 L bed volume- 100 g/L capacity- one cycle

    - 62 L bed volume- 200 g/L capacity- one cycle

    - 850 L bed volume- 100 g/L capacity- one cycle

    - 425 L bed volume- 200 g/L capacity- one cycle

    10 kg/batch126 batches

    80% yield

    75 kg/batch168 batches

    80% yield

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    Chromatography

    CD = 80cmCD = 100cmCD = 120cmCD = 140cmCD = 160cmCD = 180cm

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    Stainless steel space

    Disposables space

    Emerging production scenariosMore companies will have more than one product in production, many of them small in scale

    Batches / product / year(scale: 1-170 with six-pack of bioreactors)

    Bioreactorvolume

    (scale:525000L)

    Scale limit for many single-usecomponents: 1000 L

    Large number of batchesfavors re-use strategies

    10 100

    10

    100

    1000

    10000

    cGMP fully dedicated facility(500-3.000 kg per product)

    cGMP clinical manufacturing(2-30 kg per product)

    cGMP multi-product facility(10-500 kg per product)cGMP multi-product facility

    (10-500 kg per product)cGMP multi-product facility(10-500 kg per product)

    Non-GMP pilot facility(10-500 g per product)

    High product titers smaller installationsproduce largequantities

    How much of GMP productionwill reach the disposable space?

    Product ion sc enar ios n eed tocon sider higher degrees of f lexibi l i ty

    High product titers fewer batches producelarge quantities

    Lab bench designsused to be a

    production transferissue.

    Now the issue is

    with stainless steel

    engineer ing habi ts!

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    Reality checkHow many products are sharing facility capacity?

    Products above one metric tonper year may still require oneor more dedicated facilities

    Multiple product facilities willbe dominating the future

    Flexibility in the design is bestprotection against uncertaintyin planning

    Genentech manufacturing backgrounder (www.gene.com, 2006)

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    LEAN chromatography - summaryClassic step (1st generation tools)

    Improved step (use of up-to-date tools)

    Value adding work

    Non-value adding work

    Required non-value adding work

    Optional:Waste removed

    Single-useoperation

    Resin preparation*) Packing andre-packing*)

    Excessive equilibration volume &)

    Excessive elution volume &)

    Excessive process time &) &) not optimized

    Run

    CIP and storage #)Equilibration Load Wash Elution Strip

    Inefficientwash step &)

    Resin Preparation*)

    Run

    CIP and storage #)Equilibration Load Wash Elution Strip

    Packing andre-packing*)

    Excessive equilibrationvolume &)

    Excessive elutionvolume &)

    &) not yet optimized

    Inefficientwash step &)

    ReadyToProcessTM

    pre-packed

    pre-qualifiedpre-sanitized

    PreDictorTM plates(HTPD)

    Fast,low cost

    optimization(LEAN & SixSigma)

    AxiChromTM

    Faster procedureLess failure Modern resins

    Higher capacityand flow, longer

    lifetime

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    Influenza vaccine production capacity buildup with disposables to save time

    Traditional Flu Vaccine Production Facility Commissioning & Validation:

    Build Facility

    Validate Equipment

    Commission Facility

    Validate Process

    Build Facility

    Validate Equipment

    Commission Facility

    Validate Process

    Time Saved

    Saving ~60%

    in time

    Disposable Insect Cell Culture-Based Flu Vaccine Production:

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    flexibel planning

    flexible location

    minimal capital investment

    minimal process development

    minimal distribution and storage local policies/relationships

    local human capital

    Our vision . . .the future is a modular, self-supporting, disposable production plant

    Fast deployableproductioncapacity

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    Process economy gains overall DSPUse of modern resins: combined effect of capacity, flow, and lifetime

    10,911,8

    19,2

    37,4

    0

    5

    10

    15

    20

    25

    30

    35

    40

    Classic process Protein A update Protein A 3-step

    model process

    Protein A 2-step

    model process

    Downstream

    costcontribution[USD/g]

    0

    20

    40

    60

    80

    100

    120

    DSPprocesstime[h]

    Cost savings with modern resins up to 70%Process time down to 2 days from 5 days

    2-step process: additional indirect gains fromspace and tankage requirements

    Working volume 10,000 LTiter 5 g/LYield 79%

    (Sepharose Fast Flowresins)

    (MabSelect SuRe/CaptoS/ CaptoQ)

    (MabSelect SuRe/Sepharose Fast Flow)

    (MabSelect SuRe/Captoadhere)

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    Process improvements

    FacilityLow utilization Intense

    Efficiency gains directly visible at management levelEfficiency gains hardly visible at management level

    Investment in improvement pays off quicklyHesitant to invest in improvement

    Equipment performance on critical pathExisting equipment, performance tolerance

    Staff is a scarce resource, tough prioritizationStaff is available and has spare time

    Intense facility utilizationLow facility utilization

    Can be nothing Can be millions

    Cost driven management Extra production time creates the opportunity to run more batches.

    In a facility that produces several Mab products at a cost of $ 100M 70% of the costs may beconsidered fixed. At 5 days batch time up to 70 batches of 25 kg each could be run. One additionalbatch would reduce the cost per batch with $ ~15K. The savings amount to $ 1M / yr.

    Revenue driven management At a commercial value of $ 2.000/gram, one extra batch of 25 kg of product would be

    worth $ 50M of extra revenue.

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    Conclusions

    Monoclonal antibodies Improved processes with modern production tools and LEAN design are

    requirements to remain competitive and meet treatment cost challenges

    Insulin Diabetes is a growing challenge all over Asia. Local production will be a need

    and a business opportunity

    Plasma proteins Advanced healthcare is a growing need all over Asia. Again, local collection of

    human plasma and fractionation is a business opportunity

    Vaccines Vaccination carries the hope for cure instead of chronic treatment. Infectious

    disease is a global threat (e.g., pandemic influenza). Short lead times of just afew months require fast deployment of production where the outbreak is.

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    Thank you

    GE Healthcare Bio-Sciences AB, a General Electric company.

    GE Healthcare Bio-Sciences AB

    Bjrkgatan 30751 84 UppsalaSweden

    Capto, MabSelect, and Sepharose are trademarks of GE Healthcare companies. Biacore is atrademark of Biacore AB.GE, imagination at work and GE monogram are trademarks of General Electric Company.

    All goods and services are sold subject to the terms and conditions of sale of the company within GEHealthcare which supplies them. GE Healthcare reserves the right, subject to any regulatory andcontractual approval, if required, to make changes in specifications and features shown herein, ordiscontinue the product described at any time without notice or obligation. Contact your local GEHealthcare representative for the most current information.

    2007 General Electric Company All rights reserved.

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