Tangential Flow Filtration - TFF Processes For Hanvet By Tavis Tan This presentation is the work product of Pall Corporation and no portion of this presentation may be copied, published, performed, or redistributed without the express written authority of a Pall corporate officer. © 2017 Pall Corporation. 1 Do You Recall? General TFF System Configuration 2 2 Do You Recall? TFF Process Flowchart 3 3 TFF Process Overview Pre-Use Conditioning 1) INSTALL cassette with torque wrench MEASURE hold-up, minimum working volumes 2) FLUSH to remove storage agent 3) SANITIZE filter and system with NaOH solution 4) FLUSH to remove NaOH solution 5) MEASURE Normalized Water Permeability (NWP) To determine membrane cleaning effectiveness 6) INTEGRITY TEST To determine integrity of filter and system 7) CONDITION with buffer To condition filter for pH, ionic strength, temp 4 4 Pre Use Conditioning 1) Cassette Installation Torque Sequence 5 5 Pre Use Conditioning 1a) Hold-up & Minimum Working Volumes System Hold-up Volume – The total volume contained within the feed / retentate flow path Most of this volume is recoverable Minimum Working Volume – The system hold-up volume plus the minimum volume of liquid that must remain at the bottom of the feed vessel to prevent air from getting drawn into the system Limits maximum concentration achievable Increases with increase in cross flow rate Tank design affects minimum working volume 6 6 Pre Use Conditioning 2) Initial Flushing Objective : To remove bulk of storage agent (glycerin / sodium azide or NaOH) To remove additional foulants dissolved during storage (i.e. reused) 7 7 Pre Use Conditioning 3) Sanitization Typically accomplished by chemical mechanism in cassettes Objective : To lower the microbial population in the system To remove metabolites (proteins and sugars) which will promote microbial growth 8 8 3) Sanitization Sanitization Agents Chlorine – Bleach (sodium hypochlorite NaOCl) pH 6 – 8, 10 – 50 ppm Kills bacteria, spores, moulds, yeast and certain viruses Peracetic Acid – CH3C03H (Acetic acid + hydrogen peroxide) 100 - 300 ppm High biocidal effectiveness, good alternative to chlorine Sodium Hydroxide – NaOH pH > 12 Not as effective as chlorine but adequate in most cases 9 9 3) Sanitization Sterilization Complete destruction of microorganisms in the system using heat – Steam-in-place (SIP) – Wet autoclave at 121°C for 30 minutes Does not remove pyrogens and endotoxin NOTE: Most cassettes cannot be steamed! 10 10 Pre Use Conditioning 4) Post-Sanitization Flushing Objective : To remove all fluid extractables Removes all traces of sanitization agent Assures membrane is completely wetted before determining NWP Removal of extractables is time dependent – not volume dependent 11 11 Pre Use Conditioning 5) Measurement of NWP NWP t°C = Normalized Water Permeability Measure of the water filtrate flux rate as a function of transmembrane pressure at a given set temperature NWP 20°C = [ J (LMH) / TMP (psig) ] x tc where J = Filtrate flux rate TMP = Transmembrane Pressure tc = temperature correction factor 12 12 5) NWP Normalized Water Permeability Water Flux Rate (LMH) WP must be determined for "new" * membranes to establish the value against which recovery is measured. 60 * 40 20 WP is related to the pore diameter and number of pores / unit area of the membrane. * WP is temperature dependent. 5 10 15 TMP(psig) 13 13 5) NWP Water Permeability Example: Permeate Flux (LMH) Determining Membrane NWP Water Permeability = 110 LMH @ 10 psi = 11 LMH/psi NWP20°C = 11/10 X TCF Temperature Correction Factor = 1.109 (Correcting the water temperature from 16°C to 20°C) Temp = 16°C X 150 X 100 50 X 0 5 10 Normalised Water Permeability (NWP20°C) = 11 X 1.109 = 12.2 LMH 15 Transmembrane Pressure (psi) 14 14 5) NWP Temperature Correction Factor T oC 11 12 13 14 15 16 17 18 19 20 TCF20oC 1.271 1.235 1.202 1.169 1.139 1.109 1.081 1.053 1.027 1.000 T oC 21 22 23 24 25 26 27 28 29 30 TCF20oC 0.978 0.955 0.933 0.911 0.890 0.871 0.851 0.833 0.815 0.798 T oC 31 32 33 34 35 36 37 38 39 40 15 TCF20oC 0.781 0.765 0.749 0.734 0.719 0.705 0.692 0.678 0.665 0.653 T oC 41 42 43 44 45 46 47 48 49 50 15 TCF20oC 0.641 0.629 0.618 0.607 0.596 0.586 0.576 0.566 0.556 0.547 5) NWP When to Determine NWP Immediately after initial pre-conditioning? One or two days after initial pre-conditioning After a full cleaning regime? After the first process run? 16 16 5) NWP Cross Flow vs DP CF is directly related to DP with filtrate closed and constant viscosity Changes in DP for same CF may indicate – cassette compression – or that there may be a blockage in the feed ports to the cassette – or there has been a change in fluid viscosity 17 17 Pre Use Conditioning 6) Integrity Test Purpose: To assure proper assembly and membrane / membrane element integrity Techniques used: – Pressure Hold (Qualitative) – For system integrity – Air Diffusion (Quantitative) – For membrane integrity Use mass flow meters for fast, 18 accurate determination 18 Pre Use Conditioning 6) Integrity Test System Configuration M ass Flow meter Cassette Hardware Air Source Integrity Inlet Valv e Feed Test Profile Retentate Filtrate Pump Integrity Outlet Valv e Waste 19 19 Pre Use Conditioning 7) Buffer / Temperature Conditioning Ensure buffer is in suitable conditions: – Ionic strength – pH – Temperature Prevent possible precipitation when product is added to TFF system Remove air that can block pores and reduce flux rate Prevent micro bubbles (shear) Prevent contraction or expansion caused by changes in temperature 20 20 TFF Process Overview Processing 8) OPTIMIZE processing To determine operating parameters 9) CONCENTRATE To reduce sample volume 10) DIAFILTER (or exchange buffer) To reduce salt concentration 11) RECOVER product To maximize recovery of product from the system 21 21 Processing TFF Process Optimization 1) Planning 2) Pre and Post Use Conditioning 3) Optimization 4) Concentration 5) Diafiltration 6) Product Recovery 22 22 TFF Process Optimization 1) Planning Clearly establish process objectives Trial considerations – Establish volume to be used for trial – Membrane area to volume ratio Approximate to full scale process – Concentration factor required Hold-up volume and dilution – Diafiltration requirements? – Product stability (e.g. temperature) 23 23 TFF Process Optimization 1) Planning Identify and obtain required materials, TFF equipment and cassettes – Select correct platform – Select membrane rating/MWCO – Determine area to be used for trial – Acquire appropriate volume of sample Sample should be truly representative of product Measure actual volume used Assay sample for mass balance – Have additional cassettes available in case? – Consider large scale process and process requirements (e.g. SIP) 24 24 TFF Process Optimization 1) Planning Equipment requirements – Pump – Hold-up/Min working volumes Know it and minimize it – Correct range of instruments – Calibrated instrumentation Pressure gauges Thermometer – Temperature control? – Flowmeter? – Use spreadsheet if possible 25 25 TFF Process Optimization Flux vs Transmembrane Pressure GEL LAYER MEMBRANE CONTROLLED REGION CONTROLLED REGION Filtrate Flux Rate WATER PROCESS FLUID CONSTANT CF (D P) WHERE CF = CROSS FLOW VELOCITY OPTIMAL Transmembrane Pressure 26 26 TFF Process Optimization Optimum conditions for selected Crossflow for concentration step... Permeate Flux Rate (LMH) Flux Vs TMP 50.00 1.25 40.00 1.00 30.00 0.75 20.00 0.50 10.00 0.25 0.00 0.00 0.50 1.00 1.50 0.00 2.00 Transmembrane Pressure Process Flux Differential Pressure 27 27 TFF Process Optimization Process Sample Concentrate sample at "optimized" conditions Measure Flux vs. Concentration Factor Sample both retentate and permeate Perform diafiltration as required Recover Product Measure product recovery 28 28 TFF Process Optimization TFF System Configuration -- Concentration Recirculation 29 29 TFF Process Optimization TFF System Configuration -- Diafiltration Recirculation 30 30 TFF Process Optimization Optimal Concentration (CD) to Perform Diafiltration CD = CG = 1.0 e CG 2.7183 = 0.368 CG Filtrate Flux Rate (LMH) 100 90 80 70 K 60 50 40 CG 30 20 10 0 1 2 3 4 5 6 7 8 9 10 20 Concentration Factor 31 31 TFF Process Optimization Diafiltration Volume, VD Each VD is a volume of buffer equal to the volume of process solution present in the process reservoir and circulation loop at the start of the diafiltration. To predict the number of diafiltration volumes required to “wash out” a target percentage of a permeable molecule, (refer to chart). Note: Concentration can affect performance of the diafiltration in 2 ways – 1. Process flux – 2. Transmission of permeable molecules Increase in conc = increase in resistance of flow through membrane Increase in resistance = decrease in permeate flow rate (process flux, J) In some apps, conc of retained molecules at the membrane surface can result in difficulty for smaller permeable species to pass through membrane. Passage or Transmission, T = Cpermeate/Cfeed 32 ; T(%) = T x 100 32 TFF Process Optimization Diafiltration Volume, VD 2x concentrate 33 33 TFF Process Optimization Determining the Number of Diafiltration Volumes J = Cp/Cf = T% Constant Volume Diafiltration 0 % Permeable solids recovered in filtrate Passage/Transmission % of molecule 40 60 10 80 90 20 94 96 98 30 % Passage 100 99 0 1 2 3 4 60 80 5 6 7 40 50 8 9 10 11 12 Diafiltration Volumes E.g. T% = 10%, 1X VD = 10% permeable; 2X VD = 15% permeable T% = 50%, 1X VD = 45% permeable; 2X VD = 68% permeable T% = 100%, 1X VD = 70% permeable; 2x VD = 88% permeable, etc. 34 34 13 14 A Comparison of Different Concentration And Diafiltration Combinations Used For The Processing Of Albumin System Size 10m 2 Batch Vol. (L) Protein Conc. % Filt. Rate (L/Hr) Avg. Rate (L/Hr) Perm. Vol. (L) Filt. Time (Hr) CASE A 1) Initial 2) Conc. 5X 3) Diafilt. 5X TOTALS 1000 200 200 5 25 25 940 140 160 460 150 800 1000 1800 1.7 6.7 8.4 CASE B 1) Initial 2) Diafilt. 5X 3) Conc. 5X TOTALS 1000 1000 200 5 5 25 940 1060 160 1000 520 5000 800 5800 5.0 1.5 6.5 CASE C 1) Initial 2) Conc. 2X 3) Diafilt. 5X 4) Conc. 2.5X TOTALS 1000 500 500 200 5 10 10 25 940 600 680 160 740 640 370 500 2500 300 3300 0.7 3.9 0.8 5.4 Source: Scale-up Considerations for Membrane Processes R.S. Tutunjian, Bio/Technology Inc. 3, July 85 35 35 TFF Process Optimization 6) Product Recovery Close filtrate Recirculate concentrate for ~15 min. Displace / Collect concentrate Minimum volume buffer recirculation Displace / Collect remaining sample Actual recovery procedure has to be optimized for each process 36 36 Gel Layer Represents a high concentration of PRODUCT at the membrane surface Represents a significant percentage of total PRODUCT Accounts for a significant loss of PRODUCT if not properly recovered. 37 37 Summary of UF Optimization protocol 1) Measure sample activity and volume 2) Measure NWP and DP vs. CFF for water 3) Determine air integrity and system hold-up volume Buffer condition before adding sample 4) Generate Flux vs. TMP curve at selected CFF – Measure passage and recovery – Evaluate Flux vs. Passage – Repeat Flux vs. TMP at different CFF if results are not optimal 38 38 Summary of UF Optimization protocol 5) Concentrate Sample at optimal TMP – Measure Flux vs Concentration Factor – Measure product passage – Concentrate beyond required factor 6) Add required diafiltration volumes – Measure Flux vs Diafiltration Volumes 7) Recover product 8) Determine optimal cleaning protocol 39 39 TFF Process Overview Post-Use Conditioning 12) FLUSH with buffer (optional) To remove easily removed foulants prior to introducing chemicals 13) CLEAN in place (CIP) with NaOH solution 14) FLUSH to remove NaOH solution 15) MEASURE NWP To determine membrane cleaning effectiveness 16) STORE cassette in NaOH solution To ensure filter remains wet To prevent microbial growth 40 40 Post Use Conditioning Reasons for Cleaning Allow for reuse of cassettes (economics) Maintain efficient productivity by removing fouling materials from the membrane Maintain a clean and sanitary system by removing microorganisms and their metabolites Prevent contamination of subsequent production batches! 41 41 Post Use Conditioning Selection of Cleaning Agent Cleaning agents selected: – Based on combination of effectiveness and compatibility – With the membrane, membrane device and the process Need to determine and identify: – Type of fouling agents Likely contaminants in product or solutions – Membrane type and device / system Compatibility of cleaning agent with system – Application requirements Compatibility of cleaning agent with process 42 42 Post Use Conditioning Types of Cleaning Agents - Acids Type Foulant Conditions Nitric Acid HNO3 Phosphoric H3PO4 Citric Acid Mineral scale 0.1N, 35-45oC, pH 1 0.1N, 35-45oC, pH 1 1%, 35-45oC, pH1 Inorganics Nucleic Acids Iron 43 43 Post Use Conditioning Types of Cleaning Agents – Alkalis, Oxidizers Type Foulant Conditions Sodium Hydroxide Proteins, enzymes, vaccines, bacterial cells / lysates, polysaccharides, organic colloids, pyrogens, lipids 0.1-0.5 N NaOH, 35-45oC, pH > 13 Sodium Hydroxide / Sodium Hypochloride Inorganics Nucleic Acids 0.3-0.5 N NaOH, 200-400 ppm NaOCl, 35-45oC, pH>12 44 44 Post Use Conditioning Types of Cleaning Agents - Surfactants Type Foulant Conditions Sodium Dodecyl Sulfate (SDS) Triton X 100 Tween 80 Precipitated proteins bacterial cells / lysates, polysaccharides, lipids, oils, antifoams 0.1% 35-45oC, pH 4-9 45 45 Post Use Conditioning Critical Cleaning Process Parameters The goal is to determine – the minimum time – the minimum concentration of cleaning agent required to assure effective, reliable, repeatable, efficient and economic cleaning 46 46 Post Use Conditioning Critical Cleaning Process Parameters Time Cleaning Agent Concentration Temperature Flow Rate – Fluid Velocity Water Quality 47 47 Post Use Conditioning: Critical Cleaning Process Parameter Time – For a given cleaning agent, concentration and solution temperature, the minimum cleaning solution contact time must be determined. – Typical time frame: 30 - 120 minutes – Longer is not better Temperature Increasing temperature will: Decrease strength of foulant / surface bonds Increase solubility of foulant Increase hydrolysis and oxidation rates Typical range: 25- 45°C 48 48 Post Use Conditioning: Critical Cleaning Process Parameters Crossflow Requirements – To reduce boundary layer effects, it is essential to maintain adequate shear at liquid/surface interface. – For cleaning, use 1 ½ - 2X CFF rate used for processing – Minimum velocity (pipe) of 3 m/s will generate flow in the turbulent range 49 49 Post Use Conditioning: Critical Cleaning Process Parameters Water Quality Pharmaceutical grade Water For Injection (WFI) Water used for cleaning and making up cleaning solutions should be of equivalent quality to the water used in the process. 50 50 Post Use Conditioning: Membrane Recovery Ability to show recovery of “new” membrane NWP after cleaning is an accepted measure of membrane recovery Cassettes can be dissected and membrane surfaces analyzed for remaining contaminants (destructive) 51 51 Post Use Conditioning: Determine Cleaning Effectiveness The target for effective cleaning is to recover the initial water permeability of the membrane. NWP (after cleaning) Membrane Recovery = --------------------------------- x 100% NWP (initial) Typical recovery should exceed 80%. NWP = Water Permeability at 20°C 52 52 Post Use Conditioning: Storage of Membrane Cassettes Prevent polymeric membrane from drying out Prevent microbial growth during storage Cassettes should be stored in a suitable agent, in a closed, sealed container at temperatures between 4 –20°C 53 53 Post Use Conditioning: Storage of Membrane Cassettes Agent Condition Water Time Frame 1 day max Sodium Hydroxide 0.05 – 0.1 N < 6 months* Sodium Azide Glycerol 0.05 – 0.1% 15-20% < 1 year * It is recommended that storage agents be flushed out and replaced at least every 6 months. 54 54 Post Use Conditioning: Cleaning Validation Provide documented evidence that the cleaning procedure assures the equipment is suitably clean In order to protect the product’s identify, safety, purity, and potency. 55 55 Post Use Conditioning: Validation of Membrane Recovery Need to demonstrate the ability to effectively and consistently clean the membrane of all residual matter, after each process run, back to its initial “unused” condition. Single-use eliminates the need to clean and go through the process of cleaning validation 56 56 For an Effective Cleaning Protocol – need to establish Cleaning agent(s) – Mode of Cleaning: hydrolysis, oxidation, solubilization, emulsification, enzymatic digestion,etc. Conditions – Contact time, temp, volume, conc., etc. When does cleaning protocol start? Post cleaning procedure – Flushing to remove all traces of cleaning agents – Storage 57 57 Post Use Conditioning: Objective Targets for Cleaning The target for effective cleaning is to recover the initial water permeability (NWP) of the membrane. The target for consistent cleaning is to reproduce the effective cleaning over repeated cycles. 58 58 Post Use Conditioning: Cleaning Study – Case Study Materials – Omega 10KD membrane – Centrasette Screen Channel Cassette Foulant: 1% BSA /PBS buffer Process Conditions – Steady state 2-hour process cycles at 25 psig TMP – 2-hour cleaning cycle at given conditions Procedure – SOP direct from Pall Cassette Care & Use Manual 59 59 Post Use Conditioning: Cleaning Study – Case Study A: None Cleaning Agents Legend B: 0.1N NaOH A= None - 1% BSA Recirc. B= 0.1N NaOH @ CFF=0.6 B2: 0.1N NaOH B2= 0.1N@ CFF=0.6 C= 0.5N NaOH C: 0.5N NaOH D= 0.1N + 200ppm OCl D: 0.1N NaOH + 200ppm OCl Membrane Cleaning Recovery Centrasette 10KD Cassette OS010C06 Lot# 38075001 Figure 1A: Measured NWP results before and after cleaning for 4 consecutive recirculation cycles with 1% BSA 12 11 NWP (LMH/psig) 10 B B 9.48 9.25 D 9.55 9 B B B 8.65 8.8 8.75 9.1 B 8 B 6.9 C B 7.15 6.8 7 B2 6.95 6.55 6 5 4 3 2 4.6 4.65 A A 4.85 A 3.3 A 1 2 3 Cycle Run 60 4 60 JJR0599C13 Post Use Conditioning: Cleaning Study – Case Study Membrane Cleaning Recovery Centrasette 10KD Cassette OS010C06 Lot# 38075001 A: None B: 0.1N NaOH B2: 0.1N NaOH @ CFF=0.6 C: 0.5N NaOH D: 0.1N NaOH + 200ppm OCl Cleaning Agents Legend A= None - 1% BSA Recirc. B= 0.1N NaOH B2= 0.1N@ CFF=0.6 C= 0.5N NaOH D= 0.1N + 200ppm OCl Figure 1B: % Recovery before and after cleaning for 4 consecutive recirculation cycles with 1% BSA 98 100 % Membrane Recovery 90 B 101 91 B B 96 93 D B 80 73 70 B 75 72 C B B 60 50 49 40 A 73 69 B 51 49 A A 35 30 A 20 10 0 1 2 Cycle Run 61 3 4 61 JJR0699C01 Post Use Conditioning: Cleaning Study – Case Study A: None Cleaning Agents Legend B: 0.1N NaOH A= None - 1% BSA Recirc. B= 0.1N NaOH B2: 0.1N NaOH @ CFF=0.6 B2= 0.1N@ CFF=0.6 C= 0.5N NaOH C: 0.5N NaOH D= 0.1N + 200ppm OCl D: 0.1N NaOH + 200ppm OCl Membrane Cleaning Recovery Centrasette 10KD Cassette OS010C06 Lot# 38075001 12 Figure 2A: Measured NWP results before and after cleaning for 3 consecutive recirculation cycles with 1% D 11 D D 9.65 10 D 9.75 9.45 9.1 NWP (LMH/psig) 9 8 B 6.8 7 B2 C 6.95 6.55 6 5 4 3.3 3.55 3 A A A 2 A 2.35 2 1 4 5 Cycle Runs 62 6 7 JJR0599C13 62 Post Use Conditioning: Cleaning Study – Case Study Membrane Cleaning Recovery Centrasette 10KD Cassette OS010C06 Lot# 38075001 A: None Cleaning Agents Legend B: 0.1N NaOH A= None - 1% BSA Recirc. B2: 0.1N NaOH @ CFF=0.6 B= 0.1N NaOH B2= 0.1N@ CFF=0.6 C:C= 0.5N 0.5N NaOH NaOH D= 0.1N + 200ppm OCl D: 0.1N NaOH + 200ppm OCl Figure 2B: % Recovery before and after cleaning for 3 consecutive recirculation cycles with 1% BSA 102 100 96 90 % Membrane Recovery 103 100 D D D D 80 70 60 50 40 30 37 35 A A 25 21 20 A A 10 0 4 5 Cycle Run 63 6 7 JJR0699C01 63 Post Use Conditioning: Cleaning Summary Cleaning is a critical part of the production process It is necessary to demonstrate that a cleaning protocol is effective and consistent A cleaning study should document the effect of changes in the cleaning process variables: – Cleaning agent concentration – Time – Temperature – Fluid Velocity 64 64 Thank You Tavis Tan