The world leader in serving science Shelly A. Parra Sr. Manager, Global Field Applications Optimizing downstream purification processes: New approaches and benefits to bioprocess chromatography
The world leader in serving science
Shelly A. Parra Sr. Manager, Global Field Applications
Optimizing downstream purification processes: New approaches and benefits to bioprocess chromatography
2
• Introduction to CaptureSelect™ Affinity Products and Services
• Principles & Advantages
• Introduction to POROS™ Chromatography:
• Principles, Product Attributes & Advantages
• Closing
Overview
3
Leading Capabilities for Every Step of the Bioprocess Workflow
Upstream Downstream
Cell line development and
media optimization
Mixing, cell culture, and fermentation
Harvest and collection Purification Bulk storage
and final fill
Microbial identification
Mycoplasma and viral detection
Sample prep and automation Analytical columns
QC and analysis Gibco™ Freedom™ CHO cell lines
Analytical services
Media optimization services
Gibco™ Media Express™
Cell culture media, feeds, supplements, and bioprocess liquids Single-use mixers, bioreactors, and fermentors
Bioprocess containers (BPCs)
Inflation and integrity test system
Harvest and separation products
Bioprocess containers (BPCs)
Single-use heat exchanger
Single-use aseptic sampling system
POROS™ chromatography resins
CaptureSelect™ affinity ligands and resins
Transfer assemblies
Residual DNA and protein tests
Storage and transport
BPCs, manifolds and containers
Single-use filling system
Acclimate™ freeze/thaw containment system
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Monoclonal antibodies
• mAb-based therapeutics continue to dominate even with new cell lines emerging
• More Mab Fragments, Fabs, ADCs • Dramatic increases in cell expression levels • Interest in continuous processing
Vaccines • Processes redesigned to be more responsive, more reproducible, with higher yields
Plasma • Interest in modernizing legacy processes
Biosimilars • More drugs coming off patent, need for shorter time to end-user
Gene Therapy • Growing interest in the area and the market expected to grow 15% CAGR
First in human • Speed to clinic is main product development driver
Ease of use • Major shift to disposables in downstream purification
Quality and efficiency
• Continued demand for highest quality resolution, capacity, salt tolerance and operation speed
• Consistent, reproducible material from batch to batch • Supply risk mitigation, cost minimization
Industry Trends Driving Growth in Downstream Purification
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Purification Overview - Optimizing downstream processes
Throughput Capacity
Resolution/Separation
Yield Balance Required
Development Time
Cost
Many Factors Influence Downstream Process Development
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BioProduction Solutions for Downstream Processing
POROS™ Ion Exchange • High performance cation and anion exchange
resins • Differentiated surface chemistries provide
unique selectivity
CaptureSelect™ Products and Services • Unique, tunable affinity ligands / resins • High purity in a single step
POROS™ Resins • MabCapture™ A Select resin • High performance Ion Exchange resins
Simplifying biomolecule purification and reducing COGs
Cell Culture Clarification
Capture/Affinity Chromatography
Viral Inactivation
Polish/Non-Affinity Chromatography
Viral Filtration
Formulation
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POROS™ Bulk Resins
• AFFINITY MabCapture™ A Select MabCapture™ A Heparin 50 µm AAV8/9
• ION EXCHANGE XQ XS HS50 HQ50 D50 PI50
POROS XS
>100 mg/mL Capacity
CaptureSelect™ Bulk Resins • ANTIBODY-BASED THERAPEUTICS
KappaXL FcXL IgG-CH1 IgA IgM
• PROTEIN THERAPEUTICS FSH HSA AAV8 & AAV9 Gonadotropin hGH
Services
• Custom Resin Development • CaptureSelect™ Affinity Ligand
Development
Pre-Packed Columns
• GoPure™ 1.2 cm Diameter Column • Atoll columns
Resins for bioprocessing at any scale
Affinity solutions from screening to final
manufacturing
Simplifying purification preparation and enabling custom affinity solutions
CaptureSelect™ Technology
Unique specificity
Bioproduction Purification Products and Services
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• Introduction to CaptureSelect™ Affinity Products and Services
• Principles & Advantages
• Introduction to POROS™ Chromatography:
• Principles, Product Attributes & Advantages
• Closing
Overview
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Purification Can Be More Efficient
Non-Affinity Capture
Polish 1
Polish 2
Polish 3
Polish 4
Polish 5
Affinity Capture
Polish 1
Polish 2
80% reduction in purification time
Cell culturefeed
Purifiedproduct
CaptureSelect™ solution • Enabling a platform approach
for biomolecules through selectivity /specificity • High purity in single step
• Reduction of process steps • Higher yields, reduced costs
• Mild elution conditions • To retain biological activity of
target
• Efficient clearance of HCP, DNA, virus • High selectivity in capture step
Simplify recombinant protein
purification
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• Technology based on single-domain [VHH] antibody fragments • Combining antibody based selectivity and process robustness
• Unique screening technology for target specificity, mild elution & stability • Animal origin free (AOF) production process in yeast • Safe and well tolerated by humans
• Products in commercial purification processes (US and EU)
CaptureSelect affinity ligands
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EL
CaptureSelect affinity purification
Load Load Load EL EL EL Load
Purified sample Complex Impurities Immobilized Ligand Purification target Impurities
Binding Mild Elution
Principle
Results
• One-step selectivity to meet customer challenges • Antibody based target specificity → performance independent of feed stock
EL Load Load EL
Proven platform for product specific affinity solutions
rh GH rh G-CSF rh IgG1 Toxin rhFIX pdFIX
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CaptureSelect™ technology platform
Proven platform for development of product specific affinity solutions
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Bioprocess Products
Affinity resins for
large scale cGMP
purification
Custom Ligand Design
Tailored solutions on POROS® resin or Agarose
Antibody Toolbox®
Small scale antibody
purification
Protein Purification
Small scale protein
purification
C-tag Small, inert affinity tag
HPLC affinity
columns
Rapid analysis
and purification
- Supporting Bioprocess
resins
Biotin Conjugated
Ligands
Assay dev. or sample
prep
Bioprocess •First approved gene therapy product purified using CaptureSelect™
•First approved FVIII biobetter purified by CaptureSelect™
•Full portfolio of products for antibody formats, biosimilars and biobetters
Services • Customized affinity solutions - target specific - process compatible - scalable • Selective purification of post translational modified protein
Research • Unique TAG system for purification of EPEA tagged proteins
• Complete offering for purification of any antibody format from any source
CaptureSelect product map and formats
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Broad range of target molecules covered (RUO and cGMP)
• Antibodies • Human IgG, IgA, IgM • Multi-species IgG • Human specific • Mouse and Rat specific • Fab fragment
− CH1 − LC-kappa/lambda
• Fc fragments and Fc-fusions
• Non-Antibody targets (recombinant and plasma derived) • Blood factors: FI, FII, FVII, FVIII, FIX, vWF, • Proteins: HSA, AAT, tPA, ATIII, TF, Fib, ApoA1, ApoH • Hormones; G-CSF, FSH, hGH, hCG, GM-CSF, Insulin • Viruses: AAV serotypes, Adenovirus, Influenza • Affinity Tags: C-Tag (EPEA)
CH3
CH1
CH2
VH
CL
VL
CH3
CH1
CH2
VH
CL
VL
CH4
CH1
CH2
VH
CL
VL
CH3
CH3
CH1
CH2
VH
CL
VL
www.thermofisher.com..captureselect-affinity-products.html
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Antibody and antibody fragment purification
Fab fragment
Fc fragment
KappaXL - Human CL-kappa (all) - Generic: 100 % Fab-k coverage - Mild elution
FcXL - Human IgG-Fc (CH3) - All IgG subclasses: IVIG - Mild elution
IgG-CH1 / CH1-XL* - Unique selectivity - Generic: all Fab-k/l - No binding to free LCs - All IgG subclasses: IVIG
Caution: For manufacturing, processing, or repacking.
CH3
CH2
VL
CH1 CL
CH2
VH VL
CH3
Glycosylation site
Protein A - Human IgG-Fc (CH2-CH3) - Low IgG3 affinity: no IVIG
* CH1-XL currently available for RUO, BioProcess resin expected Sept 2017
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• Improved version of the KappaSelect ligand • Same binding specificity and epitope • Improved elution characteristics • Improved stability (50 mM NaOH for cleaning)
CaptureSelect KappaXL
Elution
Strip pH 2.0 Elution
Strip pH 2.0
KappaXL KappaSelect
Elution with 100 mM Glycine pH 3.5
Column: 0.4 ml, 2 cm bed height Load: 12 ml 1 mg/ml Human IgG Running buffer: PBS pH 7.4 Flow: 150 cm/h Elution: buffers are indicated Strip buffer: PBS pH 2.0
Elution buffer KappaXL elution
(%)
Kappa Select Elution
(%)
20 mM citric acid pH 3.0 100 74
20 mM citric acid pH 3.5 99 35
20 mM citric acid pH 4.0 82 5
100 mM glycine pH 3.5 98 48
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Targeting CH3 as a platform for mAbs and Fc fusions
Binding specificity
Human IgG, Fc fusion proteins from recombinant sources, and plasma IgG/IVIG
Matrix and particle size
Aldehyde-activated agarose, 65 μm
Dynamic binding capacity
30 g IgG per liter of matrix (column: 10 cm bed height, 150 cm/h, polyclonal IgG )
Elution buffer • 20 mM citric acid or acetic acid, pH 3 to 4 • 20 mM sodium acetate, 1.0 M MgCl2, 40% (v/v) propylene glycol, pH 5 to 6
Purification of human IgG1 monoclonal; efficient clearance of product-related impurities using FcXL • Mild elution, making it suitable for Fc fusion
proteins • Human-specific, no binding to bovine
antibodies • Excellent scalability • Non-animal-derived
L FT Wash Elution
FcXL ProtA
Product-related impurities observed in the elution fraction of ProtA purification are mainly present in the flow-through using FcXL
Caution: For manufacturing, processing, or repacking.
• CaptureSelect FcXL • Combining high specificity and mild elution for the purification of mAbs and Fc-
fusions
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• CaptureSelect IgG-CH1 (CH1-XL) • Purification of Fabs from CHO cells containing over-expressed light chains and light chain
dimers
Targeting CH1 as a Platform for Antibody Fab Fragments
• Purifies all subclasses of human IgG • Purifies all antibody fragments
(kappa/lambda) • No free light chain binding (only correctly
assembled Fabs)
A true platform for Fab fragments
VH
Affi Capt Sel GP6 053b(1291298174)001:10_UV1_280nm Affi Capt Sel GP6 053b(1291298174)001:10_Cond Affi Capt Sel GP6 053b(1291298174)001:10_pH Affi Capt Sel GP6 053b(1291298174)001:10_Fractions Affi Capt Sel GP6 053b(1291298174)001:10_Logbook
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High purity of the Fab, no light chain in the eluate
Eluate Marker
CH-1
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CaptureSelect CH1-XL
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Flow through
Elution Strip
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Elution
Strip
Polyclonal Fab
IVIG
CaptureSelect CH1-XL - Improved binding capacity - Elution with standard buffers at
pH 4.0 - Available as RUO resin - Resin suitable for cGMP Sept
2017
10
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18 17
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Human Ivig Human Fab
Dyn
amic
bin
ding
cap
acity
(g/l)
Dynamic binding capacity at 5% breakthrough
IgG-CH1
CH1-XL
- Column volume: 1 ml - Column dimensions: 5/50 mm - Flow: 0.5 ml/min (150 cm/hour) - Residence time: 2 minutes - Equilibration buffer: PBS pH 7.4 - Elution buffer: 50 mM Sodium Acetate pH 4.0 - Strip buffer: 100 mM Glycine pH 2.0
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CaptureSelect™ Bioprocess Resins: Ab and Ab fragments
Caution: For manufacturing, processing, or repacking.
Product Target applications Uniqueness
CaptureSelect™ KappaXL Human IgG and Fab fragments thereof containing a kappa light chain
Mild elution for fragments and antibodies
CaptureSelect™ FcXL
Human IgG antibodies, Fc-fusion proteins CH3 binding domain, mild elution
CaptureSelect™ IgG-CH1 and CH1-XL
Human IgG antibodies and Fab fragments thereof
CH1 binding domain, no free light chain binding for fragments
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Pipeline of affinity products
CaptureSelect™ affinity products for purification of: Therapeutic proteins (non-mAb) & viruses Antibody types
Bioprocess cGMP
FSH, Human Albumin, hCG AAV8, AAV9,
KappaXL FcXL
IgG-CH1
Stage 5: RUO products
hGH, tPA Antithrombin III, Fibrinogen,
Transferrin, ApoH, C1-Inh
IgA, IgM CH1-XL
Stage 4: Lead Selection
Prothrombin, GM-CSF Exotoxin A (PE)
IgG-CH2
Stage 3: Prototype Resins
Insulin, EPO Adenovirus (Adv5), Flu (HA)
IgE, Free LC-kappa
Stage 2: Lead Screening
TSH, IFNa/b, hIL2, Protein C, FV, FX, FXI, FXII, FXIII, FH, vWF,
Lentivirus (VSV-G)
Rabbit IgG, Anti-Idiotypes
Stage 1: Library Construction DNAse Free LC-lambda,
scFv, IgY, Mouse IgG
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Analytical Products Supporting Bioprocess Resins
Leakage ELISAs
• Reagents for a sandwich ELISA to detect leached ligand in the elution fractions of the CaptureSelect bioprocess affinity resins
• Available for all
CaptureSelect based bioprocess resins
HPLC columns
• Prepacked POROS CaptureSelect Affinity Columns for rapid quantitation of immunoglobulins, fusion proteins, Fabs, and bispecific antibodies
• Applications include titer determination and small scale purification
Conjugated ligands
• Biotinylated ligands for use in a range of analytical assays
• Applications include Capture ELISA, Western blot, Gyros’ Gyrolab®-based immunoassays, and label-free detection platforms
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• Introduction to CaptureSelect™ Affinity Products and Services
• Principles & Advantages
• Introduction to POROS™ Chromatography:
• Principles, Product Attributes & Advantages
• Case Studies • Closing
Overview
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• Polystyrene-Divinylbenzene Backbone • Rigid, Incompressible • Easy Handling • Robust Chemical Stability
• Perfusion Chromatography • Pore Structure with Large Throughpores • Unlocks Interior of Bead • Increased Convective Flow, Reduced Diffusional Limitations • Improved Mass Transfer, More Efficient Purification
• 50 Micron Particle Size • Superior Resolution • Excellent Pressure-Flow Properties • Fully Scalable
POROS™ Chromatography Resin: Product attributes
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BSA
DB
C, 5
% (m
g/m
l)
Flow Rate (cm/hr)
POROS XQ POROS HQ50 POROS PI50 Q Sepharose™ FFFormat
Column: 0.46cmDx 20cmL
Load Condition: 10 mg/mL BSA in 20mM Tris, pH 8.0
Maintain high dynamic binding capacity over a large flow rate
range
High Performance Resins Enable Increased Productivity
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POROS™ Chromatography Resin: Principles • Architecture of bead conserves mass transfer at high flows
POROS®
10 cm Bed
Agarose
10 cm Bed
Theoretical Transition
Reprinted from: Hahn, R., Comparison of Protein A Affinity Sorbents, J. of Chromatography B (2003) 790, 35-51. Fig 3 with permission from Elsevier (10)
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POROS™ Chromatography Resin: Elution Efficiency
• POROS resin improves elution volume versus typical process resin
POROS®
Diffusive
Reprinted from: Hahn, R., Comparison of Protein A Affinity Sorbents, J. of Chromatography B (2003) 790, 35-51. Fig 8 with permission from Elsevier (10)
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Superior Resolution Enables Higher Yield and Purity
500cm/H
300cm/H
Conventional resins lose resolution as flow rate increases
POROS resins maintain resolution as flow rate increases
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POROS™ AEX Separation Compared to Conventional Chromatography Resin
Conventional Resin Loses Resolution as Flow Rate Increases
Format Column: 0.46cmDx 20cmL, 3.32ml Gradient: 0 – 50%B, 10 CV Buffer A: 20 mM Tris, pH 8.0 Buffer B: 20 mM Tris/ 1.0M NaCl, pH 8.0 Sample:
Transferrin 5mg/mL, pI 5.6 Chicken Ovalbumin 10mg/mL, pI 4.6 Soybean Trypsin Inhibitor 4mg/ml, pI 4.5
Total Protein Loaded: 4.4 mg, 1.3mg/ml
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POROS HQ 50 Conventional Resin
Abs
orba
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280n
m (m
AU
)
Abs
orba
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280n
m (m
AU
) Volume (ml) Volume (ml)
____ 100 cm/hr
____ 300 cm/hr
____ 500 cm/hr
____ 100 cm/hr
____ 300 cm/hr
____ 500 cm/hr
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Implementing POROS™ Resins at Scale: Cleanability and scalability
• Robust chemical stability • pH: 1-14
• 5N NaOH • 2M Acetic Acid • 1M HCl
• Ionic Strength: 0-5M salt • Solvents
• Water • 0-100% alcohols • Acetonitrile • Other organic solvents
• Additives • Urea, Guanidine • Ethylene Glycol • Detergents
• Excellent pressure-flow properties
Pressure Flow Curve for POROS 50 HSPacked 3bar in 21cmD Glass Column with SS frits
0.0
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2.5
3.0
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Flow Rate (cm/hr)
Pres
sure
(bar
)
19cm Bed Height
29 cm Bed Height
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Implementing POROS™ Resins at Scale: Improved column lifetime
Cleaning Protocol 20CV: Tris-HCl, pH 8.2
4CV: 0.2N HCl, 1M NaCl
2CV: Tris-HCl
4CV: 0.5N NaOH, 50% Isopropanol
2CV: Tris-HCl
4CV: 5% Acetic Acid, 1M NaCl
POROS HQ50 Cleaning Study
0
20
40
60
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100
0 30 60 90 130Cycle Number
% R
ecov
ery
Robust stability allows for effective cleaning and strong reuse performance
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Classical Antibody Purification Ligands Protein A, G, and A/G
• Protein A
• 85% of market–chemical tolerance, easier elution • Binds Fc region at CH2-CH3 sites and binds to VH3 • Does not bind IgG3
• Protein G
• Binds Fc region at CH2-CH3 sites and to the CH1 region
• Poor binding to Ig subtypes (e.g., IgA, IgM, IgE, etc.)
• Protein A/G
• Combines five Fc binding domains from Protein A and two from Protein G
• Combined specificity of Protein A and G for a one- resin-fits-all solution
Utilized for multispecies antibody purification from a wide range of sample sources
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Thermo Scientific™ POROS™ MabCapture™ Select resins Combining speed and selectivity for a more efficient purification
Capacity
Resolution
Productivity
Bead
Protein A: >35 mg/mL Protein G: >12 mg/mL Protein A/G: 20 mg/mL
Optimized 45 µm particle for improved impurity clearance, better yield
Maintains high binding capacity at high flow rates
Incompressible bead with robust physical stability, low backpressure
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IEX Resin
Mode of Operation Key Applications
Cation Exchange
(CEX)
Bind/elute Polish of many biomolecules (mAb, VLP/viruses, fusion proteins, high pI recombinant proteins)
Overload/ Flow through
Polish for mAb by binding impurities under normal B/E conditions: impurity removal (aggregates, HCP, DNA, viruses)
Anion Exchange
(AEX)
Bind/elute Polish of many biomolecules (low pI recombinant proteins, DNA, viruses, plasmids)
Flow through Polish for mAb: binds impurities (DNA, viruses, HCP, aggregates, endotoxin)
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SP Sepharose
Volume (mL)
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m (m
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Capto S
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POROS XS vs. Capto S
POROS XS is the only CEX resin to successfully combine superior capacity, salt tolerance & resolution
Format
Column: 1cmD x 20cmL; Buffer A: 20mM MES, 25mM NaCl pH 6.2; Buffer B: 20mM MES, 1M NaCl pH 6.2; Gradient: 10% B – 50% B 7.5CV; Flow Rate: 300cm/H; Sample: Chymotrypsinogen; Cytochrome C; Lysozyme
POROS XS Chromatography Resin Setting standards in resolution and capacity
C5
Cap
acity
(mg/
ml)
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Capacity of Cation Exchange Resins 100 mM NaCl, pH 4.5, 300 cm/H
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SP Sepharo
POROS XS vs. GigaCap S
Volume (mL)
Abs
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m (m
AU
)
POROS XS
Gigacap S
, p ,
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C5
Cap
acit
y (m
g/m
l)
Capacity of Cation Exchange Resins 40 mM NaCl, pH 5.0, 300 cm/H
Global Adoption
36
Run 1 – pH 5.5 Run 2 – pH 5.0 Run 3 – pH 4.5
• Large particle size resin lacks resolution capability • Peak cutting required to separate monomer and aggregate • Decreased product yield
Aggregate Separation on a Non-POROS Resin
37
Run 1 – pH 5.5 Run 2 – pH 5.0 Run 3 – pH 4.5
High resolution POROS Resin provides improved separation
Aggregate Separation on POROS XS
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• Optimization of baseline separation • Gradient can be optimized to step elution • Improved product yield due to efficient separation of
monomer and aggregate
Optimization of Aggregate Separation on POROS XS
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POROS Anion Exchange Resin Offerings
POROS®
Resin
Type of AEX
Resin Surface Chemistry
BSA Binding Capacity (mg/mL)
AEX Applications
D50 Weak Dimethylaminopropyl 90 Bind/Elute: Protein, virus, plasmid DNA purification
Flow Through:
Trace impurity removal by binding impurities (DNA,
viruses, HCP, aggregates, endotoxin)
PI50 Weak Polyethyleneimine (Mixed Amine) 80
HQ50 Strong Quaternized
polyethyleneimine (Mixed Amine)
75
XQ Strong Fully quaternized amine >140
• A full range of weak and strong anion exchange resins with unique surface chemistries, that provide unique selectivity
40
POROS XQ is a strong AEX resin that successfully combines superior capacity, salt tolerance & resolution
POROS XQ Strong AEX Chromatography Resin Novel solution for high capacity and resolution
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BSA
DBC,
5%
(mg/
ml)
Capacity of strong AEX resins at various salt conditions
POROS® XQNuvia™ QCapto™ QEshmuno™ QFractogel® TMAECapto™ Q Impres
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Volume (ml)
POROS® XQ Capto™ Q
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POROS® XQ Capto™ Q Impres
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POROS® XQ Fractogel® TMAE
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A high performance resin can provide advantages for flow through chromatography
POROS resins allow high linear velocity, so allows high volumetric flow with smaller diameter/volume columns and less buffer (or much faster processing time)
Flow Through with soft gels can require large diameter/large volume columns to permit reasonable volumetric flow.
Resin Type Linear Flow
Rate (cm/hr)
Column Diameter
(cm)
Bed Height (cm)
Column Volume
(L)
Volumetric Flow Rate
(L/min)
Column Volume
Reduction (%)
1000 L Load Time
Reduction (%)
Soft Gel 200 100 10 78.5 26.5
POROS 1000 45 10 15.9 26.5 80%
POROS 1000 100 10 75.8 130.8 80%
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Yun (Kenneth) Kang, Rajesh Ambat, Troii Hall, Matthew D Sauffer, Stanley Ng,Martha L Healy-Fried, Julia Lee, Josaih C Adaelu, William D Holmes, Warren Emery, Behnam Shanehsaz, Amy Huebner, Bo Qi, Richard Chen, Michael Barry, Dale L Ludwig & Paul Balderes, Pharmaceutical Bioprocessing, Vol. 3, No. 8, Pages 477-487 , DOI 10.4155/pbp.15.28
POROS™ XQ Case Study: Mab polish in 2-step process
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Purpose: To design a scalable AEX flow through polish step for acidic/neutral antibodies (pI≤8.0) that had proved challenging using conventional strong AEX resins (QFF). Goal was to maximize impurity clearance (HCP, host DNA, leached ProA, and HMW aggregates) and product yield by utilizing POROS XQ, a salt tolerant strong AEX resin and to optimize to a 2-step purification process: Protein A>AEX FT Process Details:
• 7 Mabs tested • Loading Capacity: 100-300 mg of protein /ml of resin • Study format:
• HTP Screening: 96 well plates, 40 µl resin volume in 270 µl working volume • Development: 1.1cmD x 5.3cmL, 5ml columns • Pilot: 14cmD x 18.5cmL, 2.9L
POROS™ XQ Case Study: Mab polish in 2-step process
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POROS™ XQ Case Study: Mab polish in 2-step process
Data from Kang, Yun (Kenneth), et al (Eli Lilly) “Development of an acidic/neutral antibody flow-through polishing step using salt tolerant anion exchange chromatography”, Pharmaceutical Bioprocess (2015), V8 (8), pages 477-487, DOI 10.4155/pbp.15.28
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POROS™ XQ Case Study: Mab polish in 2-step process
• POROS XQ increased flexibility when designing the purification scheme and eliminated the need for load dilution and diafiltration steps allowing for a more efficient and cost effective process
Data from Kang, Yun (Kenneth), et al (Eli Lilly) “Development of an acidic/neutral antibody flow-through polishing step using salt tolerant anion exchange chromatography”, Pharmaceutical Bioprocess (2015), V8 (8), pages 477-487, DOI 10.4155/pbp.15.28
2-8 Fold HMW Clearance
1-9 Fold HCP Clearance
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Viral Clearance on POROS™ XQ resin with increasing conductivity
• POROS XQ resin provides excellent viral clearance for both model viruses under typical FT/Wash conditions as well as increased conductivity
• Viral clearance with higher salt concentrations allows for increased flexibility when designing a purification scheme − Minimizes need for load dilution and diafiltration steps − Allows for more efficient and cost effective processes
Load Conductivity
Load Capacity (IgG/ml of
resin)
POROS XQ
XmuLV Log10 Reduction
MMV Log10 Reduction
5 mS/cm 500 >4.31 ± 0.12 >5.10 ± 0.09
10 mS/cm 500 > 4.39 ± 0.14 1.61 ± 0.23
15 mS/cm 500 3.46 ± 0.29 0.19 ± 0.28
Study Conditions Column Format: 0.46cmD x 20 cmL Flow Rate: 300 cm/hr Protein Load: 5 mg/ml Polyclonal IgG Buffer System: 20 mM Bis-Tris Propane, pH 7.0
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• “POROS XQ is compatible with multivalent buffers which would provide a practical alternative to traditional AEX resins”
• “Unique salt tolerant nature of POROS XQ allows it to be compatible with most Pro A elution buffers eliminating the need for pre-AEX buffer exchange or inline dilution. In addition, wider operating ranges can be defined relative to traditional Q chromatography, which is likely to result in greater process robustness and manufacturing flexibility."
• “Utilization of XQ Chromatography enabled development of a two-column mAb purification platform, able to meet product purity targets for all antibodies evaluated in the study”
POROS™ XQ Provides Value
Data from Kang, Yun (Kenneth), et al (Eli Lilly) “Development of an acidic/neutral antibody flow-through polishing step using salt tolerant anion exchange chromatography”, Pharmaceutical Bioprocess (2015), V8 (8), pages 477-487, DOI 10.4155/pbp.15.28
• Residual HMW ≤1.5% highlighted in Red
• Yield ≥ 90% in Blue • Overlap shading
indicates “sweet spot”
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SITUATION OUR RESPONSE VALUE DELIVERED
• Large column volumes and long cycle times
• Goal = increase productivity of anion exchange (AEX) flow through step
• POROS HQ • Optimized AEX format • Technical support for
process optimization, column packing and lifetime
10 fold Cycle time reduction
More cost effective Optimized process
2.5X protein load Robust viral clearance & product quality
Case Study: POROS HQ in Short Bed/High Flow Format
Data from Shen, Yuyi et al, (Xoma) “An Optimized Approach for AEX Polish Chromatography to Drive Productivity and Decrease Cost of Goods”, Poster Presentation, BPI, Boston, MA Oct 2014
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POROS™ Quality Testing
• CQA testing designed to model how customers use the material
• Statistical process control to monitor manufacturing processes
• Outsourced testing: bioburden analysis, catalyst and OH polymer SEC testing • All contract labs have been qualified and approved
PROCESS STEP
Size Distribution
Fines Measurement FTIR Extractables
/ Leachates
Pore mode
Protein
Capacity Separation Endotoxin Bioburden
Base Polymer ● ● ●
Product Intermediate ● ●
Final Product ● ● ● ● ● ● ● ●
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• Robust, Defined, Proven Quality System − ISO 9001:2008 & ISO 13485:2003 Certified
> Last Registrar Audit – September 2015
− Process Media Products Backed by a Drug Master File since 2001
− Facility and Quality Systems Routinely Audited by Customers
− Products Used in Multiple FDA/EMEA Approved Therapeutic Processes
− Products being evaluated and incorporated into new processes by existing and new customers
POROS Quality Systems
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Your Partner for Purification
Enabling, purification solutions that simplify processes and reduce COGs
Superior performance compared to other resins
Novel affinity and IEX solutions Established reputation for affinity
purification of recombinant proteins including biosimilars
Established reputation for process and product-related impurity removal
State-of-the-art manufacturing and robust quality
Global support
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A solution that’s fits your needs
PHARMACEUTICAL GRADE REAGENT. FOR MANUFACTURING AND LABORATORY USE ONLY.
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