Progress since EPSRC Centre feasibility April, 2015 Purification Solutions for Biotherapeutic Manufacturing Find out more: www.puridify.com Puridify’s anatomy of innovation Unmet need O. Hardick starts doctoral research program Project idea conceived at BBRSC BRIC workshop 2008 First patent application for the technology O. Hardick starts enterprise fellowship to consider next steps Puridify founded and wins 1st OneStart competition Puridify begins operations at Stevenage Biocatalyst Further capital raised key employees appointed Venture Capital raised for commercialisation 2015 Not for distribution 1 Chromatography: Critical purification step A critical tool in part of the $153bn biotechnology market Chromatography reagent market: $5bn (18% CAGR)1 1. Global Markets for Reagents for Chromatography, BCC Research, September 2012 Not for distribution 2 Technology: Bead resin is outdated Porous Bead Resin Old vs New • Expensive – costs $10m • Economical – uses 10x less reagent • Slow – relies on diffusion • Fast – can use convective flow • Variable – column packing issues • Robust – fixed structure & screening • Outdated - next gen drugs too large • Flexible – suitable for next gen drugs • Large – takes up lots of space • Small – small clean room footprint Not for distribution 3 FibroSelect: Advantage of nanofibres in bind-elute Bead Resin FibroSelect Membrane Monolith Pore diffusion = limiting High porosity Limited surface area High porosity Prone to fouling : deadend channels Optimal surface areapore size Deadend structure Focus is marcomolecular Pore size: 15-40nm Pore size: 0.2-2.0µm Pore size: 0.2-0.5µm Pore size: 2µm Capture area: 40m2/g Capture area: 10m2/g Capture area: 2m2/g Capture area:1-200m2/g Not for distribution 4 FibroSelect: Allows low pressure operations ∇ Membrane A; Membrane B; ⊙ Membrane C; ◊ FibroSelect Low pressure at high flowrate maximises productivity Not for distribution 5 Binding capacity (mg/ml) FibroSelect: Strong performance at all flowrates Cation Exchange o Anion Exchange □ Flowrate (cm/hr) Not for distribution 6 Recent Progress 10mL DEAE cartridge 400mL/min, BSA load until 10% BT 1400 90 80 1200 UV absorbance 60 800 UV absorbance 50 600 Conductivity 40 400 30 200 Conductivity (mS/cm) 70 1000 20 0 10 -200 0 0 100 200 300 400 500 600 700 800 Volume (ml) High throughput screening Research optimisation Pilot purification Solid structure also allows uniform performance over scales Not for distribution 7 Recent growth in recombinant vaccines • Move away from egg vaccine production • Growth of focus on preventative strategies for non-infectious diseases such as Parkinson’s disease and therapeutic use such as cancer • Requirement to shorten time to market with outbreaks like Ebola, Flu variants, SARS and other sources of potential epidemics • Cost of goods and scalability for global populations • Veterinary vaccines: foot & mouth, avian influenza Not for distribution 8 Desirable adsorption surface properties • Surface area - Capture capacity • Porosity - Pressure drop and access to surface area • Stability - chemical, biological & physical • Hydrophilicity - (can be introduced) • Functional groups for modification • ROBUSTNESS - reproducible in fabrication and operation Developed for mAb purification, applied to viral vectors Not for distribution 9 Desirable adsorption surface properties Not for distribution 10 Macromolecular Biomolecule Purification 100 nm Size and labile nature of AV make them difficult to purify Not for distribution 11 Infectivity of the product Filled Empty • Adenovirus has a complex maturation cycle, with mixed subtype batches leading to lower therapeutic efficacy • Much is yet to be understood about the positive or negative adjuvant effect caused due to the ratio of infective vs non-infective viral capsids • Utilisation of diverse ligand library and buffer conditions will be required in IEX setting to separate adeno subtypes Future potential to control infectivity of viral particles Not for distribution 12 FibroSelect: Simple plug and play technology 1. Truly disposable operation: Lifetime of FibroSelect unit (number of cycles) used in a single sitting makes disposable operation economic 2. Increased throughput: Rapid cycling increases grams of therapeutic purified, per hour, per litre of adsorbent 3. Flexible operation Smaller, disposable FibroSelect units are better suited to the new generation of smaller, geographically local, multi product, manufacturing facilities 4. Robustness of operation No column packing, easier to predict performance, using well trusted materials and purification chemistries Enabling new process operations without changing underlying purification principals with the support of the bioindustry Not for distribution 13 Thank you ----- .com Not for distribution 14