implementation of a robust manufacturing process for a ...the evolution of paste iv-1 as a...
TRANSCRIPT
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Implementation of a robust Manufacturing Process for a unique liquid formulated Alpha1
proteinase Inhibitor (Human), the recently FDA approved – GLASSIA®
Avi Baziz Kamada Ltd. Israel
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Contents: 1. Introduction 2. The shift 3. Company Strategic Mile Stones History 4. Engineering projects- Plant upgrade 5. Building QA Force and Regulatory Department 6. BLA, CMC, FDA audit, all the way to approval 7. Kamada Unique Purification Process- visiting card 8. Kamada Unique Purification Process - AAT 9. Main AAT Process steps 10. AAT- Main product attributes and advantages 11.Clinical pipeline 12. Next Generation (AAT) Inhaled
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The evolution of Paste IV-1 as a disposable raw material to … an important product for the manufacturing of a highly pure and
unique product The common product in market is lyophilized, mainly because of stability and shelf life constraint of a liquid protein solution. GLASSIA ® is the first liquid formulated product of it’s kind and is robust in a sense that the process is capable to utilize Cohn Fraction IV-1 as well as IV1+4 or even different Various suppliers (Plasma Fractionation sites), will be further detailed.
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Kamada Manufacturing
Facility
$30-$50
~$300
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Fraction IV or IV-1 From Human plasma
The shift
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Company Founded
• Company’s Foundation
• Flag Product - Albumin
• Strategy Change
Strategy Change
• Strategic agreements with the American Red-Cross (ARC)
IPO
• Israel’s First public BIO company
• Over 50% of company products are strategic
• Increasing investment in R&D
Entering the US Market
Sales and Marketing US & EU
• Pivotal clinical study ongoing
2012-2013
Inhaled AAT - US & Europe Clinical development & submission
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Engineering projects- Plant upgrade : Goal: System equipment and structure must reach the highest standards required by experienced Auditors.
• Three main upgrades between 2005 and 2009,
Construction and equipment. • Additional Expenses- Projects scope included Sewage
treatment Facility, software/ Hardware/ PLC and control system and validations
• End of project is defined Only when finishing all related Validations
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The Bet Kama Site (~4.5 Acres)
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TO Company • Leaned to Quality and Production • Integrated • Process directed activities • 300 employees • Continuing improvement
FROM Company • Leaned to Production and Quality • Tasks ambiance • Consequential directed activities • 100 employees • Preservation capabilities
HR, the key to success
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• Identifying of needs and corporate culture- GMP compliance, guidance and working • Qualified employee, fostering personal liability • organization structure • Working procedure (not SOP)- Team leaders, coordination between managers and departments. Synchronization of routine work depends first on will and drive of people, only than on good project plan
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Building QA Force and Regulatory Department
• Recruit and develop experienced QA & RA managers and staff
• Good Development Practice
– Ongoing Collaboration with R&D
– Establish Technology Transfer Procedures
– Continuous Training
• Establishing work teams and team work (Production; QA; QC; RA and R&D)
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BLA, CMC, FDA audit, all the way to approval
• Comprehensive Product Development Report by R&D
• Establishment of Two Major Projects
• Institute CPO Unit
• Perform Detailed Gap Analysis vs. BLA Chapters, Consultants references, Audits and inspections findings & cGMP Guidelines.
• Create a General Work Plan
• Generate a Detailed Work Plan
• Perform Internal Audits and Mock FDA Inspections as part of the detailed work plan
• Create Sub-teams Manage it as a Project, with
Engineering tools
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Unique, in house developed, patented process, based on
chromatographic purification.
Able to extract highly pure, stable, ready to use (Liquid),
specialty proteins (AAT, Albumin, Transferrin,
immunoglobulin and others).
Kamada Unique Purification Process- visiting card
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Kamada Unique Purification Process - AAT
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Kamada has the knowledge, experience and ability to adjust its manufacturing
process to :
- Assorted fraction pastes (Filter Press, Centrifuge)
- Various suppliers (Plasma Fractionation sites)
- Raw materials from different stages of fractionation (Fr IV or Fr IV-1)
- Final product, Liquid solution ready to use (injection or inhalation).
Using classic methods of protein purification (precipitation, ion-exchange columns, ultra filtration, diafiltration ,filtration…).
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Main AAT Process steps
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Pretreatment
Heat treatment
Precipitation
Centrifugation or filter press for removal of insoluble materials
Protein purification
Chromatography purification steps ultrafilteration / diafiltration steps
Viral elimination steps (nanofiltration)
Viral inactivation steps (solvent / detergent treatment)
Final polishing step
DS
Final 0.2µ sterile filtration
DP
Formulation
Aseptic filling
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AAT- Main product attributes and advantages
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1. Batch continues production
2. Each batch started with 100 to 200 kg of paste (Reference, without FA) and finished as a concentrated liquid DS
3. Tight bio-burden limits all along the process
4. Extremely high safety standards (two viral inactivation steps).
5. significant High yields
6. High specific activity –Avr. 0.9
7. Distribution of molecular size- MT 90%.
8. 2% Active Alpha-1 Proteines Inhibitor ready to use
9. Stabilizer and preservative free
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The Next Generation (AAT) Inhaled
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• In Phase 2-3 in the EU
• Current production capacity MT 1,000 patients by IV
• production capacity MT 4,000 patients by Inhalation
• AAT process as other IP are protected under patents in EU,
North America…
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Thanks
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Appendices Topics mentioned along the presentation
o New controlled Facility Layout plans- Manufacturing area (partial) o List of required Validation protocols (Partial) o Before- After, illustration o General Layouts- after reconstruction o Kamada Product Line o Alpha-1 Antitrypsin (AAT), Augmentation Therapy o Additional Indications o AAT Potential Market o Intellectual Property
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Drawing. No. Title
D-20001/96 Layout
D-1131/00 CD Production Area Pressure Cascade
D-1132/00 Production Layout & Room Classification
D-1134/00 CD Production Area – Dirty Equipment Flow
D-1135/00 CD Personnel Flow Into Prod. Areas
D-1101/03 Process Flow in Prod. Area AAT Drug Substance/Product
D-1101/05 IgG Process
D-01001/96 Parenteral Drug Process
D-1141/00 CD Production Area - Clean Equipment Flow
D-11300/96 CD Production Area – HVAC AC- 2203
CD Production Area – HVAC AC- 2204
CD Production Area – HVAC AC- 2205
CD Production Area – HVAC AC- 2206
CD Production Area – HVAC AC- 2207
CD Production Area – HVAC AC- 2256
CD Production Area – HVAC AC- 2284
New controlled Facility Layout plans- Manufacturing area (partial)
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Machine / System CC URS DQ IQ OQ
AC-2203 (Pretreatment Area) - - + + +
AC-2204 (Filling Suite 1) + + + + +
AC-2205 (Filling suite 2 ) + + + + +
AC-2206 (Buffers) + + + + +
AC-2207 (Controlled corridors & Peripherals, Prep. Room, Gowning Areas) + + + + +
AC-2208 (Second Viral Elimination Room) + + + + +
AC-2209 (Gowning to filling rooms) + + + + +
AC-2256 (First Viral Elimination Room) + + + + +
AC-2284 (General Production Room) + + + + +
Clean Room Facility Monitoring System - - + + +
New Autoclave (ACL-1402) + + + + +
New Depyrogenation Oven (SO-1403) + + + + +
Existing Autoclave (ACL-2005) - - + + +
Vessel (T-56) + + + + +
Vessel (T-57) + + + + +
Vessel (T-59) + + + + +
Vessel (T-60) + + + + +
Vessel (T-61) + + + + +
Vessel (T-70) + + + + +
Vessel (T-71) + + + + +
Vessel (T-72) + + + + +
Vessel (T-73) + + + + +
Vessel (T-63) 80L + + + + +
Vessel 80 L( T-93) + + + + +
Vessel 80L (T-64) + + + + +
Vessel 80 L (T-94) + + + + +
Vessel (T-99) 250L + + + + +
Vessel 250L( T-69) + + + + +
Vessel (T-92) 300L + + + + +
Vessel 300L( T-62) + + + + +
Vessels screen - - + + +
Heating/cooling system for vessels + + + + +
Uniformity of filling vials - - + + +
Media Fill - - + + +
Filling Machine 1 + + + + +
Filling Machine 2 + + + + +
Gowning Validation - - + + +
Nitrogen System + + + + +
Oil Free Compressed Air System + + + + +
Clean Steam Production and Distribution System + + + + +
WFI Distribution System + + + + +
RO Distribution System + + + + +
NaOH Distribution System + + + + +
List of required Validation protocols (Partial)
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General Layouts- after reconstruction
Southern Building Northern Building
Central Building
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Kamada Product Line Category Product
Respiratory
Intravenous AAT (Glassia®) – Alpha 1 Deficiency
A1- AAT (IH) for Alpha 1 deficiency*
B1- AAT (IH) for Bronchiectasis*
C1 – AAT (IH) for Cystic Fibrosis*
Diabetes D1 – AAT (IV)
Immunoglobulins
KamRAB
KamRho- D IM
KamRho -D IV
Varitect **
Hepatect **
Megalotect**
Pentaglobin **
Critical Care
IVIG**
Heparin sodium injection **
Heparin Lock Flush
Kamacaine
Kamacaine Adrenaline
Protosol
Snake antiserum*
Albumin**
Coagulation Factors
Factor IX**
Factor VIII, VWF**
Additional Specialty Proteins Human Transferrin (Diag.)
Human Transferrin (Pharm.) * * Under development
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Alpha-1 Antitrypsin (AAT)
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• Protein derived from human plasma (fraction IV)
• Indicated for chronic treatment of genetically deficient alpha 1 patients
• Regulates the activity of Neutrophil Elastase (NE) - excess of which may
cause chronic inflammatory state, lung tissue damage and decrease in lung
function
• Treatment with AAT controls the excess NE activity by restoring the
enzyme/inhibitor balance
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AAT
AAT
AAT
AAT
AAT
AAT
AAT
Augmentation Therapy
Alpha 1 Patient
Healthy or treated patient
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Additional Indications
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Diseases related to
inactive AAT
COPD, Diabetes, IBD
Vasculitis, Wegener’s
Panniculitis
Diseases with
overwhelming inflammation
Sinusitis, Bronchiectasis
Cystic Fibrosis, IBD
Chronic Infections
Diabetic Foot
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AAT Potential Market
• 1: 2,500 potential patients world-wide
• ~100,000 in the US
• ~100,000 in the EU
• Current market
• 5,000 identified and treated
• 6,000 identified, 1,000 treated
• ~$500 Million
• significant growth of the AATD market
• potential and additional indications
• Baxter is the leading company in the US specializing in identification of
new patients
• Average cost of therapy is $100,000 / patient / year
• Orphan indication to support premium pricing
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Intellectual Property
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PATENT: “Large Scale Preparation of Alpha1 Proteinase Inhibitor and Use Thereof “ Granted: USA, EU, Australia
PATENT: “Method for purification of alpha1 proteinase inhibitor”
Granted: USA
PATENT: “Ultrapure Transferrin for Pharmaceutical Compositions “ Granted: USA
PENDING PATENT: “Large Scale Preparation of Alpha1 Proteinase Inhibitor and Use Thereof“
National stage: Israel, Canada, Argentina
PENDING PATENT: “Pulmonary Delivery of Alpha1 Proteinase Inhibitor” National stage: USA, EU, Australia, Canada, Israel, Mexico, Brazil, Russia
PENDING PATENT: “Alpha1 Antitrypsin for Treating Exacerbation Episodes of Pulmonary
Diseases” National stage: USA, EU, Australia, Canada, Israel, Mexico, Brazil, Russia
ORPHAN DRUG DESIGNATIONS in US and EU for inhaled AAT for:
AAT Deficiency, CF and Bronchiectasis indications (Bronchiectasis only in the US)