Hollow Fiber Bioreactors: Single-Use. Perfusion. Scalable. Continuous Manufacturing.

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Bioreactors and BioServices for the Life of your Proteins Hollow Fiber Bioreactors: Single-Use. Perfusion. Scalable. Continuous Manufacturing. Presented by: Scott Waniger Vice President, BioServices BPI West: Oakland, California March 14, 2016

Bioreactors and BioServices for the Life of your Proteins Hollow Fiber Bioreactors: Single-Use. Perfusion. Scalable. Continuous Manufacturing. Presented by: Scott Waniger Vice President, BioServices BPI West: Oakland, California March 14, 2016

Cell Culture Company Provider of Bioreactors and BioServices Manufactures automated single-use perfusion bioreactor systems and disposables Provides custom manufacturing of mammalian and insect cell lines and expressed proteins to producers of human and animal healthcare products Minneapolis-based since 1981 Formerly known as Biovest International, Inc. Pioneered Hollow Fiber Bioreactor platform Spun-off as Cell Culture Company January 2016 33,000 sq. ft. facility Corporate Offices Bioreactor system and disposables manufacturing operations GMP BioServices compliant manufacturing 3

Cell Culture Company Our Mission: Cell Culture Company strives to revolutionize the quality, scalability and predictability of diagnostic and therapeutic mammalian protein production. We provide automated single-use perfusion bioreactor systems and custom development and manufacturing (CDMO) services for the human and animal healthcare industry. Delivering innovative and scalable GMP custom mammalian cell and protein production solutions and services from pre-clinical to commercial in mg to kg quantities. We re about achieving superior results for our customers. Delivering value through the: Improvement of cell health quality, resulting in homogeneous protein expression produced through the use of a homeostatic system Decreasing production risk as a result of using closed, parallel systems Increasing speed to market due to reduced upstream validation requirements Reducing capital expenditures, labor, facilities and materials costs delivering increased protein per square foot of production space 4

Hollow Fiber Cell Culture Bioreactors Key Initiatives: Cell culture on artificial capillaries: an approach to tissue growth in vitro October 1972 Knazek RA, Gullino PM, Kohler PO, Dedrick RL. Scalable technology from R&D to Manufacturing Scale Single Use Automated Perfusion Bioreactor Systems Licensed FDA Injectable Diagnostic Imaging Biologic (ProstaScint ) Clinical trial Support 4 Phase III Clinical Trials (currently an anti-pd-1 mab) 23 Phase I/II Clinical Trials Primary upstream manufacturing platform for large scale( >2 gram) IVD products 5

6 Hollow Fiber Cell Culture Bioreactors

Hollow Fiber: Perfusion Cell Culture Fiber bundle encased in clear case IntraCapillary Space = ICS - Inside the fibers ExtraCapillary Space= ECS Outside the fibers 7

8 Electron Micrograph of a single fiber

Hollow Fiber: Perfusion Cell Culture Hollow fiber material is a semipermeable membrane composed of cellulose acetate: 35-60 kda MWCO Small nutrients freely exchange between ICS & ECS Cells and products are retained in ECS volume 9

EM photos of cells on fibers Suspension Hybridoma Culture Adherent CHO Culture 10

Nuclear Magnetic Resolution (NMR) images of cell growth in a Hollow Fiber Bioreactor Day 1 Day 2 Day 5 A high-resolution, diffusion weighted image of the bioreactor at 1, 2, and 5 days post-inoculation with a hybridoma cell line. The cell mass appears bright/white and shows homogenous distribution. 11

C3 Manufactures & Distributes Hollow Fiber Bioreactors Research Scale Protein Pilot Scale Protein Large Scale Protein Commercial Scale Protein HF Primer AcuSyst-MAXIMIZER AcuSyst XCELLERATOR HF MicroBrx AutovaxID AcuSyst XCELLERATOR R&D Pre- Clinical Phase I Phase II Phase III Commercial 12

Scalable Technology 1X 2X AcuSyst-Xcellerator 13 20X

Case Studies Study 1: Scalable Technology that reduces the need to validate during scale up C3 s Hollow Fiber Perfusion technology allows for a 20-fold expansion of bioreactor capacity Cell substrate (cartridge) space does not change in form fit size function or size Scale up occurs by connecting multiple cartridges in parallel Study 2: Continuous Protein Expression Manufacturing In vivo-like cell environment supports cells at >10 9 cells per ml of space No seed train Steady state metabolic activity Long lasting protein expression production 14

Case Study 1: Data Table Bioreactor System No. of 2.1 m 2 Cartridges No. of Culture Days Grams of IgG Liters of Supernatant Cell Line A (Shaker Flask titer 0.02 g/l) Titer g/l IgG Production mgs/day/cartridge AutovaxID 1 30 9.0 3.0 3.00 300 Maximizer 2 60 40.8 16.0 2.55 340 Xcellerator 10 37 111.0 43.0 2.58 300 Cell Line B (Shaker Flask titer 0.01 g/l) AutovaxID 1 30 3.5 3.0 1.16 116 Maximizer 2 62 13.0 16.0 0.81 105 Maximizer 2 30 6.1 8.0 0.76 102 Maximizer 2 60 17.0 16.0 1.06 142 Maximizer 2 30 7.5 3.3 2.27 125 Maximizer 2 60 14.0 16.0 0.88 117 Maximizer 2 60 17 15.0 1.14 143 Xcellerator 10 60 70 50.0 1.40 117 Cell Line C (Shaker Flask titer 0.005 g/l) Xcellerator 10 47 8 32.9 0.25 18 Xcellerator 10 94 21 66.4 0.31 22 Xcellerator 10 51 11 36.7 0.31 22 Xcellerator 10 51 11 36.1 0.30 21 Xcellerator 10 55 10 38.5 0.27 19 Xcell 6 82 12 35.4 0.32 23 Cell Line D (Shaker Flask titer 0.008 g/l) Xcellerator 10 85 81 62 1.32 96 Xcellerator 10 69 62 50 1.24 90 Cell Line E (Shaker Flask titer 0.008 g/l) Maximizer 2 48 10 11 0.95 104 Xcellerator 10 21 91 38 2.39 433 15

mg of IgG/day/cartridge Case Study 1: Scalable Production Cell Line A Normalized Production Rate 400 300 300 340 300 200 100 0 ONE CARTRIDGE AUTOVAXID TWO CARTRIDGE MAXIMIZER TEN CARTRIDGE XCELLERATOR 16

mg of IgG/day/cartridge Case Study 1: Scalable Production Cell Line B Normalized Production Rate 150 100 116 105 102 142 125 117 143 117 50 0 ONE CARTRIDGE AUTOVAXID TWO CARTRIDGE MAXIMIZER TWO CARTRIDGE MAXIMIZER TWO CARTRIDGE MAXIMIZER TWO CARTRIDGE MAXIMIZER TWO CARTRIDGE MAXIMIZER TWO CARTRIDGE MAXIMIZER TEN CARTRIDGE XCELLERATOR 17

mg of IgG/day/cartridge Case Study 1: Scalable Production Cell Line C Normalized Production Rate 25 20 18 22 22 21 19 23 15 10 5 0 TEN CARTRIDGE XCELLERATOR TEN CARTRIDGE XCELLERATOR TEN CARTRIDGE XCELLERATOR TEN CARTRIDGE XCELLERATOR TEN CARTRIDGE XCELLERATOR SIX CARTRIDGE XCELLERATOR 18

mg of IgG/day/cartridge Case Study 1: Scalable Production Cell Line D Normalized Production Rate 100 80 60 40 20 0 TEN CARTRIDGE XCELLERATOR 90 94 TEN CARTRIDGE XCELLERATOR 19

mg of IgG/day/cartridge Case Study 1: Media Optimization 500 400 300 200 100 Cell Line E Normalized Production Rate: Tissue Culture Media Comparison of RPMI-1640 vs. C3 High Density Media 104 433 0 TWO CARTRIDGE MAXIMIZER (RPMI-1640 + NUTRIDOMA) TEN CARTRIDGE XCELLERATOR (C3 HIGH DENSITY MEDIA + NUTRIDOMA) 20

Case Studies Study 1: Scalable Technology that reduces the need to validate during scale up C3 s Hollow Fiber Perfusion technology allows for a 20-fold expansion of bioreactor capacity Cell substrate (cartridge) space does not change in form fit size or function Multiple cartridges are connected in parallel Study 2: Continuous Protein Expression Manufacturing In vivo-like cell environment supports cells at >10 9 cells per ml of space No seed train Steady state metabolic activity Long lasting protein expression production 21

Case Study 2: Operator Requirements to Support a 90-Day Xcellerator Culture (~ 1,600 L stirred tank equiv.) Disposable bioreactor assembly installation = 2 hours Inoculation preparation (thaw to seed ~10 8 ) = 6 hours Daily bioreactor support = 1 hour/day Total operator time for 90 day perfusion culture = 98 hours Product Output: 100-200x concentration based on standard suspension culture environment (stirred tank requires additional concentration step) Cell culture supernatant passes through a sterilizing grade 0.2 micron filter to yield cell-free supernatant Proceed immediately to downstream processing 22

Case Study 2: No Seed Train Culture Day 6 Culture Day 8 Culture Day 10 Culture Day 12 Culture Day 14 Culture Day 16 23

g/l Case Study 2: Steady State Metabolic Control: Cell Line D, 84 and 69 day cultures ph 7.5 7.3 7.1 6.9 6.7 6.5 0 10 20 30 40 50 60 70 80 90 100 Culture Day 5 Glucose and Lactate Concentrations Glucose Glucose Lactate Lactate 4 3 2 1 0 0 10 20 30 40 50 60 70 80 90 100 Culture day 24

Case Study 2: 100+ Day Consistent and Continuous Protein Expression Perfusion Hollow Fiber Bioreactor; IgG production rate* 14 Culture 1 Culture 2 Culture 3 Culture 4 Culture 5 Culture 6 12 10 8 GRAMS PER WEEK 6 4 2 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 CULTURE WEEK *Cell Line IgG titer in shake flask = 5 mg/l 25

Case Study 2: 100+ Day Consistent and Continuous Protein Expression Perfusion Hollow Fiber Bioreactor; IgG production rate* 14 Culture 1 Culture 2 Culture 3 Culture 4 Culture 5 Culture 6 12 10 8 GRAMS PER WEEK 6 4 2 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 CULTURE WEEK *Cell Line IgG titer in shake flask = 5 mg/l 26

Perfusion Hollow Fiber and Batch/Fed-Batch System and Process Features Perfusion Hollow Fiber Batch/Fed-Batch Support mammalian cell culture expression system Yes Yes Single Use Yes Yes Closed System Yes Yes Supported in market for 30+ years Yes Yes Maintains Metabolic Homeostasis for 60+ days (ph, glucose, lactate, l-glutamine, oxygen) Concurrent product concentration Continuous Manufacture of Expressed Proteins Linear Scalability Yes Yes (100-200X) Yes Yes (same cartridge size in parallel) No No (requires further downstream processing) No (requires ATF modification) No (each scale expansion requires validation) Seed Train Required No Yes 27

What environment is best for your cells production? Consider Thinking Outside the Wave. Consider Thinking Outside the Tank. 28

and consider Automated Perfusion Hollow Fiber Bioreactors for your protein expression needs Improved cell health quality, resulting in homogeneous protein expression produced through the use of a homeostatic system Decreased production risk as a result of using our closed, parallel systems Increased speed to market due to reduced upstream validation requirements Reduced capital expenditures, labor, facilities and materials costs delivering increased protein per square foot of production space 29

C3 s BioServices and Hollow Fiber Perfusion Bioreactor Platform Key Initiatives: Serviced over 1,700 labs globally Expanded and worked with over 2,650 different cell lines Manufactured a licensed FDA therapeutic imaging biologic Supported manufacturing for 4 phase III clinical trials Currently supporting anti-pd-1 mab at CMO 23 Phase I/II clinical trials Hollow Fiber Perfusion Bioreactors are The primary platform for large scale (>2 g/year) IVD mab products 30

Bioreactors and BioServices for the Life of your Proteins Hollow Fiber Perfusion Bioreactors: Please stop by booth #505 for more information Presented by: Scott Waniger Vice President, BioServices BPI West: Oakland, California March 14 2016