BMPRAC CT
Lecture 1: Introduction to Biomanufacturing
Biomanufacturing Processes
Biopharmaceutical Analysis
Biomanufacturing Practices
Quality Operations
Quality Assurance
Quality Control
Specifications and Testing
Laboratory Testing
Production Operations
Cell Culture
Reactor Design and Operations
Mixing Operations
Excess Deaths
Definition: Differences between observed deaths and expected deaths during a period, factoring in age distribution and population trends.
Age-Standardized Death Rate (ADR)
Adjusts the death rates of a population to a standard age distribution for accurate comparisons across populations or timeframes.
Morbidity vs. Mortality
Morbidity: State of being unhealthy.
Mortality: Number of deaths in a population.
Disability-Adjusted Life Years (DALY)
A measure of the burden of disease.
DALY = YLL + YLD
YLL: Years of life lost due to premature death.
YLD: Years lived with disability.
Factors Influencing Disease Susceptibility
Lifestyle choices, genetics, age, gender, environment.
Types of Medical Care
Curative Care
Preventative Care
Palliative Care
Biopharmaceuticals
Definition: Biotherapeutics that treat acute/chronic diseases, produced from macromolecules like proteins, DNA, RNA.
Production Sources
Eukaryotic and prokaryotic cells; isolated from natural sources or synthetically made.
Comparison: Biopharmaceuticals vs Pharmaceuticals
Biopharmaceuticals:
Large biomolecules, expensive, fewer side effects, may be personalized.
Pharmaceuticals:
Small chemical drugs, cheaper, mainly manufactured by chemical means.
Biopharmaceutical Manufacturing Processes
Stage 1: Upstream Processing
Objective: Cultivate cells/enzyme reactions to produce products (e.g., CHO, BHK cells).
Stage 2: Downstream Processing
Objective: Recovery, purification, and stabilization of products (e.g., cell separation).
Page 2: Biopharmaceutical Manufacturing Operations
Bioreactors
Function: Culture cells, providing optimal growth environments.
Volume: Ranges from 25ml to 10,000l.
Seed Trains
Important for preparing cell inoculum for production bioreactors.
Dispensing and Buffer Preparation
Dispensing
Involves precise weighing, measuring, and packaging of materials.
Necessary for consistency and quality throughout production.
Key activities in media/buffer prep: mixing, pH adjustment, quality control, documentation, sterilization.
Approved APIs
Sources: Mammalian (CHO, BHK), Human, Bacterial (E. coli).
Cell Banking
Protects against contamination and catastrophic loss.
Types of cell banks: R&D, Master, Working, End-of-Production.
Genetic stability maintained through sub-culturing from Master to Working Cell Banks.
Page 3: Seed Train and Bioreactor Functionality
Seed Train Objectives
Main Objective: Generate a large number of viable cells quickly.
Secondary Objective: Identify potential production issues early.
Terminology
N-culture in production; prior steps in the seed train termed N-X.
Clean-in-Place (CIP)
Utilizes detergents/disinfectants, rinses, and sprays for thorough cleaning.
Steps: Detergent wash, water rinse, acid rinse, water rinse to neutral pH.
Steam-in-Place (SIP)
Employs steam or sterilized solutions for sterilization.
Maintains positive pressure to prevent contamination.
Bioreactor Functioning
Overview of how fresh medium supports cell growth and product generation.
Page 4: Bioreactor Operation Modes
Batch Culture
High substrate concentrations, longer turnaround times.
Growth Curve Phases:
Lag Phase: Cells adapt.
Exponential Phase: Constant doubling rate.
Stationary Phase: Growth slows due to nutrient depletion.
Death Phase: Cell death exceeds growth rate.
Disadvantages: High substrate levels lead to low biomass yield and prolonged turnaround times.
Fed-Batch Cultures
Begin as a batch culture, slow feeding of nutrients maintains low substrate concentrations leading to higher cell and product concentration.
Continuous Cultures
Constant nutrient feed; cells grow and produce continuously while effluent is removed.
Types of continuous bioreactors: Chemostat, Perfusion.
Page 5: Perfusion Cultures and Substrate Management
Perfusion Cultures
Continuous culture allows for cell recycling, maintaining high cell concentrations in the bioreactor.
Substrate Management
Low substrate concentrations facilitate respiration rather than fermentation, yielding higher product formation.
Page 6: Bioreactor Designs and Components
Stirred-Tank Bioreactors
Key components include a cylindrical tank, impellers, sparger.
Common materials: stainless steel, single-use plastics, glass.
Control of pH
Established through deadbands to maintain operational stability and prevent over-reaction.
Action taken when pH exceeds limits: acid or alkali added accordingly.
Single-Use Bioreactors
Advantages: Reduced labor, risk of contamination, easy disposal.
Disadvantages: Less efficient mixing, dependence on specific vendors, high costs.
Page 7: Bioreactor Operations and Monitoring
Dissolved Oxygen Monitoring
Crucial for cell respiration; controlled through DO probes and systems.
Air flow and stirrer speed adjustments to maintain optimum levels.
Foam Control
Proteins create foam; antifoams used to destabilize and manage excess foam, but must be controlled to prevent large bubble formation.
Page 8: Additional Monitoring Systems
Conductivity and Antifoam Control Systems
Systems detect foam levels and adjust antifoam addition to maintain operational efficiency.
pH Control
Use of deadbands to mitigate over-addition of agents and maintain desired pH levels.
Page 9: Batch Culture Kinetics
Cell Growth in Batch Bioreactor
Biomass and product yield assessments using the Monod model for fermentation kinetics.
Exponential Phase Characteristics
Cells exhibit auto-catalytic growth behavior, doubling at a constant rate, leading to exponential cell concentration increases.
Page 10: Monod Model and Specific Growth Rates
Monod Model
Describes growth rate implications based on substrate concentrations.
Specific Growth Rate (µ)
Influenced by various factors: substrate availability, temperature, presence of inhibitors.
Biomass Yield
Calculates efficiency in biomass production.
The yield is expressed as a ratio of biomass produced to substrate consumed.