T5 FILTRATION
BIOSEPARATION
Filtration
Overview of Filtration
Definition: Filtration is defined as the separation of solids from liquids by passing a suspension through a permeable medium that retains the particles.
Outcomes of Filtration:
Waste or Cake: The particles retained during the filtration process are referred to as waste or filter cake.
Filtrate: The filtered fluid that passes through is called filtrate.
Fluid State: The fluid can exist in either liquid or gas form.
Strategies in Product Recovery
Importance: Product recovery is one of the most critical aspects of industrial bioprocessing.
Scales of Operation:
Laboratory scale: 1-100 Litres.
Pilot scale: 100-10,000 Litres.
Industrial scale: 10,000-100,000 Litres.
Approach: There is no absolute rule for product recovery strategies; it depends on various factors.
Downstream Processing
Characteristics of Bioproducts:
Bioproducts are usually labile or sensitive, thus requiring controlled conditions to maintain their activity.
Conditions to consider:
pH
Temperature
Ionic strength
Operational Nuance: There is no unique, ideal operation or sequence that can be universally recommended. Each operation must be tailored to meet specific challenges and problems effectively.
Factors in Downstream Processing
Nature of the Product: Physical and chemical properties influence processing choices.
Concentration: Higher concentrations may lead to processing difficulties such as clogging and increased viscosity.
Stability: Bioproducts may be labile, and stability is crucial; this can encompass conditions like pH, temperature, etc.
Desire for Purity: Higher purity leads to increased costs.
End Use Considerations:
For medical applications, products must be free of pyrogenic materials.
Adherence to current good manufacturing practices (cGMP) is essential, along with addressing biosafety during production.
Filtration System Components
Different parts involved in a filtration process include:
Suspension: The mixture of solids and liquids before filtration.
Medium: The permeable substance through which the suspension is filtered.
Filtrate Flow (Q): The flow rate of the filtrate.
Driving Force: Pressure drop ($ riangle P$) is required to initiate the filtration process.
Filtration Examples and Descriptions
Slurry Composition Example:
10% solids, 90% liquid by weight.
Typical Outcomes of Filtration:
Filter-Cake: Composed of 25% liquid, 75% solids.
Filtrate: Contains approximately 0.01% solids.
Particle Size Comparison
Comparison Table (in µm and in. with US Mesh equivalent):
Beach Sand: >150 µm, >7 in., US Mesh: N/A
Granular Salt: 100 µm, 4 in., US Mesh: <80
Human Hair Diameter: 45-70 µm, 2-3 in., US Mesh: 325-200
White Blood Cells: 25 µm, 1 in., US Mesh: 550
Red Blood Cells: 8 µm, 0.3 in., US Mesh: 1750
Viruses: 0.008-0.1 µm, 0.0003-0.004 in., N/A
Aqueous Salt: <0.002 µm, <0.00008 in., N/A
Filtration Applications
Beyond Product Recovery: Filtration is used for handling heat-sensitive materials like antibiotics, antifungals, and vitamins, where high temperatures would cause denaturation.
Sterilization Methods:
Syringe filters for small volumes.
Sterilization of air involves pumping air through a sterilized filter to prevent contamination in aerobic cultures.
Filtration Equipment Classifications
Classification Criteria:
By Driving Force:
Gravity Filtration: Flow induced by hydrostatic head, e.g., water purification through sand.
Applied Forces: High pressure or vacuum to enhance filtration.
Classification by Filtration Mechanism
Cake Filtration: Solids accumulate on the filter’s surface, forming a cake that provides further filtration.
Clarifying Filtration: Solids are trapped within the pores of the filter medium.
Objective and Operating Cycles of Filtration
By Objective:
Dry Solids: Best achieved with cake filtration.
Filtrate: Best achieved with depth filtration.
By Operating Cycle:
Batch Filtration: Intermittent process.
Continuous Filtration: Ongoing; allows for cake removal continuously.
Nature of Solids in Filtration
Compressible vs Non-compressible: Different properties affecting filtration efficacy.
Examples include yeast for compressible cakes and sand or activated carbon for non-compressible cakes.
Types of Filtration
Depth Filtration: Constructed with a matrix (e.g., glass wool, filter paper) that traps particles within its structure.
Membrane/Absolute Filtration: Utilizes pores smaller than the filtered particles, applicable in ultrafiltration and reverse osmosis. This method is often more expensive.
Filtration Aids
Role and Functionality:
Aids in processes needing fine solid removal (<5 µm).
Applications include catalyst recovery, active pharmaceutical ingredients, and clarification of gray water.
Challenges with Fine Solids: Fine solids can lead to a rapid decline in filtration rates due to impermeable coatings on filters; pre-treatment with filter aids can address this issue.
Types of Filter Aids: Commonly, diatomite, perlite, and cellulose are used, requiring specific properties like rigidity and inertness.
Diatomite as a Filter Aid
Description: Contains microscopic silica skeletons of diatoms.
Processing: Mined, calcined, and milled to create various grades.
Advantages: Highly porous structure, inert in diverse applications.
Perlite as a Filter Aid
Description: Derived from volcanic rock, expanded through heating.
Advantages: Lower specific weight than diatomite, which reduces the amount needed for filtration.
Cellulose as a Filter Aid
Usage Characteristics: Less common due to higher costs and less filtration efficiency, but valuable for recovery processes and compatibility with hot caustics.
Relationship Between Particle Size and Filtration Efficiency
Particle size influences the ability to capture fine solids; smaller particles lead to improved clarity but increase resistance.
It’s critical to balance clarity with filtration efficiency, dictating optimal filter aid selection.
Filter Medium Characteristics
The composition of the filter medium is critical for functionality; it must effectively retain the filter aid while allowing liquid flow.
Types of Utilization for Filter Aids
Precoat: Involves establishing a layer of solids on the filter medium for improved filtration.
Body Feed: Involves mixing filter aids with the slurry feed to help develop a porous filter cake that promotes higher flow rates and improved clarity.
Filtration Systems with Filter Aids
Types of Systems:
Plate-and-frame filter presses.
Pressure leaf filters (horizontal and vertical).
Candle or tubular filters.
Nutsche filters.
Rotary vacuum drum filters.
Filter Press Functionality
Components: Consists of a frame, filter plates covered with cloth, and mechanisms for operations like opening and cleaning.
Operational Principle: Slurry is introduced and filtrate is extracted through cloths positioned within alternating plates, creating filter cakes that join when the framework fills up.
Advantages and Disadvantages of Filter Presses
Advantages:
Versatile for different materials and conditions.
Low maintenance costs with a compact footprint.
Effective in both cake and filtrate production.
Disadvantages:
Intermittent operation can lead to higher wear on cloths.
Labor-intensive processes may be required for maintenance.