SlideShare a Scribd company logo
MerckMillipore.com
The life science business of Merck operates as MilliporeSigma in the U.S. and Canada.
Sherry Ashby Leon, Shannon Cleveland, Ravin Gami, Sal Giglia, Joseph Hersey, Nhung Nguyen, Andrew Koch, Songhua Liu
Merck, Bedford MA, USA
Introduction
Membrane-based prefilters are an important component of
many downstream operations. They are used to limit the
variability of process streams by removing plugging
contaminants thereby protecting sterilizing-grade filters and
other unit operations. Some prefilters contribute to process
safety by reducing bioburden in intermediate process steps
where sterilizing grade filters are not required.
Milligard® PES filters contain polyethersulfone (PES)
membranes of different pore sizes for efficient particle removal
from a broad range of process streams. These prefilters are
compatible with caustic sanitization, gamma irradiation,
autoclave and steam in place (SIP) sterilization methods. Table
1 lists the different pore sizes of Milligard® PES filters.
This poster summarizes throughput and bacterial retention
performance of Milligard® PES membranes in OptiScale®
capsules challenged with different streams. Throughput
capacity was determined either alone or with a downstream
sterilizing-grade filter.
© 2019 Merck KGaA, Darmstadt, Germany and/or its affiliates. All Rights Reserved. Merck, Millipore, the vibrant M, Milligard, OptiScale, Durapore, and
Millipore Express are trademarks of Merck KGaA, Darmstadt, Germany or its affiliates. All other trademarks are the property of their respective owners.
Detailed information on trademarks is available via publicly accessible resources.
MK_PS2745EN Ver 2.0 09/2019
Improve Process Efficiency in Bioprocess
Streams by Prefiltration Optimization and
Bioburden Reduction
Application
Milligard® PES
Filter
Bioburden Reduction
Particle &
Bioburden
Reduction
1.2/0.2 µm nominal
>6 LRV Brevundimonas
diminuta
1.2/0.45 µm >6 LRV Serratia marcescens
Particle
Reduction
1.2/0.8 µm NA
Table 1. Milligard® PES Filters
Methods
Throughput capacity studies
The streams used in these studies were selected to represent a
wide range of particle sizes and particle size distributions
(Figure 1); they were concentrated to achieve a high degree of
plugging (> 90% flux decay at < 1000 L/m2 of filtrate).
Throughput capacity of final sterilizing grade filters was
measured both with and without Milligard® PES prefilter
protection. The effect of different prefilter to final filter area
ratios on throughput capacity was explored at area ratios
ranging from 0.5:1 to 3:1. Tests were performed at both
constant pressure (10 psi) and constant flow (500 LMH final
filter) operating conditions. The experimental setup is
illustrated in Figure 2.
Figure 1. Particle size distributions of model streams
Bioburden reduction studies
Bioburden reduction was evaluated using Milligard® PES
1.2/0.2 µm nominal and 1.2/0.45 µm membrane in OptiScale®
capsules challenged at 2 psi with Soy peptone spiked with
Brevundimonas diminuta or Serratia marcescens. Retention of
these microorganisms was evaluated at different points of filter
plugging.
Figure 2. Experimental setup for throughput capacity tests
Results
Final filter protection and throughput
Figure 3 illustrates the throughput capacity of a Durapore®
0.22 µm filter alone, and paired with a Milligard ® PES 1.2/0.2
µm nominal prefilter. The capacity of the combined
prefilter/final filter train was almost 10 fold higher than that of
the sterilizing filter alone.
(b) 500 LMH constant flow(a) 10 psi constant pressure
0
500
1000
1500
2000
0 50 100
Throughput(L/m2offinalfilter)
Time (min)
with
prefilter
without
prefilter
0
5
10
15
20
25
30
0 500 1000 1500 2000
Presuure(psi)
Throughput (L/m2 of final filter)
without
prefilter
with
prefilter
The impact of prefiltration on final filter throughput capacity
for the 3 pore sizes of Milligard® PES filters, with 3 different
particle size distribution streams, and 2 types of final filters
(PVDF and PES) is summarized in Figure 4. These studies
were performed at constant pressure of 10 psi.
The magnitude of final filter throughput improvements was
dependent on the filter pore size, challenge feed, and the type
of sterilizing filter. As prefilters have lower unit costs than
sterilizing filters, any improvement in capacity due to prefilters
can result in dramatic improvements in filtration economics.
Figure 3. Effect of Milligard® PES 1.2/0.2 µm nominal filters
on capacity of Durapore® 0.22 µm filter: (a) 10 psi constant
pressure (b) 500 LMH (final filter) constant flow.
Figure 4. Final filter capacity improvement by prefiltration. %
improvement is compared to stand-alone final sterilizing filter:
(a) Durapore® 0.22 µm (PVDF) final filter; (b) Millipore
Express® SHF (PES) final filter.
(a) Durapore® 0.22 µm (PVDF) final filter
(b) Millipore Express® SHF (PES) final filter
Optimization of area ratio
Increasing prefilter area will often improve final filter capacity.
Optimizing the prefilter to final filter area ratio can result in a
cost-effective filtration solution. Figure 5 shows an example of
the capacity benefit of different area ratios. A theoretical model
is available for efficient system sizing and optimization.
0
500
1000
1500
2000
2500
3000
0 1 2 3 4
Throughput(L/m2finalfilter)
Area Ratio (Pre/Final Filter)
Model
Data
Millipore
Express®
SHF only
Figure 5. Effect of prefilter (Milligard® PES 1.2/0.2 µm
nominal) to final filter (Millipore Express® SHF) area ratio on
throughput capacity in Soy peptone at 10 psi constant
pressure.
Particle removal by prefilters
Prefilters protect final filters and other unit operations by
removing particles that would otherwise plug or contaminate
downstream unit operations. Particle removal capability was
quantified by measuring cumulative concentration of particles of
different sizes in the Soy peptone challenge and filtrate solutions
after processing through Milligard® PES filters. Most particles in
this solution are smaller than 1.0 µm in size, with the highest
concentration being at approximately 0.2 µm in diameter (Figure
1). Figure 6 shows that all Milligard® PES filters retained over
90% of the particles between 0.2 µm and 1.0 µm.
Figure 6. Soy peptone particle retention by Milligard® PES
filters.
Bioburden reduction
Prefilters can provide an increased level of process safety by
reducing bioburden. Milligard® PES 1.2/0.2 µm nominal filters
have been validated to demonstrate >6 log B. diminuta
retention while the Milligard® PES 1.2/0.45 µm filters have been
validated to demonstrate >6 log retention of S. marcescens.
Figure 7 shows microorganism retention by ‘stand alone’
Milligard® PES 1.2/0.2 µm nominal and Milligard® PES 1.2/0.45
µm filters in the absence of a final sterilizing filter. The
microorganism challenge level was > 107 cfu/cm2 and filtrate
grab samples were collected at different points of filter plugging.
As would be expected based on a retention mechanism based on
size exclusion, microorganism retention was robust (no
breakthrough) under all conditions.
Figure 7. Log reduction values (LRV) as a function of filter
plugging. (a) Milligard® PES 1.2/0.2 µm nominal filters
challenged with B. diminuta; (b) Milligard® PES 1.2/0.45 µm
filters challenged with S. marcescens. Data points indicate results
from individual OptiScale® 25 devices; arrows indicate complete
retention.
Summary
Milligard® PES filters are available in a range of pore sizes for
processing different streams, are compatible with multiple
sterilization methods, and have been validated to reduce
bioburden. These filters:
• Dramatically improve the throughput capacity of both PVDF
and PES sterilizing-grade filters, significantly improving
filtration economics.
• Efficiently remove particulates from process streams.
• Can be used ‘stand-alone’ to provide sustained bioburden
reduction even under conditions of extreme filter plugging.
(a) Milligard® PES 1.2/0.2
µm nominal filter retention
of B. diminuta
(b) Milligard® PES
1.2/0.45 µm filter
retention of S. marcescens
To quantify the particle removal capability of the prefilters,
particle concentrations and size distributions of the challenge
stream feeds and filtrates were measured using an optical
particle counter (Liquilaz SO2).
0%
20%
40%
60%
80%
100%
Particle sizes 0.2-1.0 µm
ParticleRetention
Milligard® PES 1.2/0.2 µm nominal
Milligard® PES 1.2/0.45 µm
Milligard® PES 1.2/0.8 µm
0
200
400
600
800
1000
1200
1400
1600
Soy Peptone Whey Soy T
CapacityIncreasebyPrefiltration
(%)
Milligard® PES 1.2/0.2 µm nominal
Milligard® PES 1.2/0.45 µm
Milligard® PES 1.2/0.8 µm
0
50
100
150
200
250
300
350
400
Soy Peptone Whey Soy T
CapacityIncreasebyPrefiltration(%)
Milligard® PES 1.2/0.2 µm nominal
Milligard® PES 1.2/0.45 µm
Milligard® PES 1.2/0.8 µm
0
2
4
6
8
10
0 20 40 60 80 100
LRV
% Flow Decay
0
2
4
6
8
10
0 20 40 60 80 100
LRV
% Flow Decay

More Related Content

PDF
White Paper: Explore Versatility with SPTFF
PDF
Reducing Contamination Risk and Improving Product Recovery During Final Steri...
PDF
Filtration Strategies for Optimal Development and Purification of a FMD Virus...
PDF
Reducing Contamination Risk and Improving Product Recovery During Final Steri...
PDF
Millipak® Final Fill Filters
PPT
Tx Single Use Seminar Jun09
PDF
Ultrafiltration Diafiltration Process Development of High Concentration Visco...
PDF
Selection, sizing, and operation of bioprocess filtration trains for optimal ...
White Paper: Explore Versatility with SPTFF
Reducing Contamination Risk and Improving Product Recovery During Final Steri...
Filtration Strategies for Optimal Development and Purification of a FMD Virus...
Reducing Contamination Risk and Improving Product Recovery During Final Steri...
Millipak® Final Fill Filters
Tx Single Use Seminar Jun09
Ultrafiltration Diafiltration Process Development of High Concentration Visco...
Selection, sizing, and operation of bioprocess filtration trains for optimal ...

What's hot (18)

PDF
Optimization of Tangential Flow Filtration Applications and Scale Up Consider...
PDF
Pellicon 2
PDF
Implementing and Managing Pre-use Post-sterilization Integrity Testing (PUPSIT)
PDF
Normal Flow Filtration: Design and Scale Up
PDF
Potential Impact of Draft Annex 1 on Sterilizing Filtration
PDF
Find your filter. What’s best for your process?
PDF
A hands on guide to ultrafiltration1
PDF
Normal Flow Filtration: Design and Scale Up
PDF
Pellicon 3 biomax membrane
PDF
Parvovirus Filtration Best Practices - 25 Years of Hands-On Experience
PDF
Inline Flocculation for Harvest and Perfusate Clarification
PDF
Membrane Chromatography Solutions for Single-Use, Intensified mAb Purification
PDF
Process Development for Continuous Flow-Through Polishing Purification for mA...
PDF
Millipak® Final Fill Filters Reduce Contamination Risks and Simplify Filtrati...
PDF
Single-Pass Tangential Flow Filtration (SPTFF) Theory and Practice
PDF
A Cost Analysis and Evaluation of Perfused Seed Train Scenarios Through Proce...
PPTX
Implementing a Fully Single-Use, Integrated mAb Biosimilars Purification Plat...
PDF
An Efficient and cGMP-friendly Solution to Diafiltration for Intensified or C...
Optimization of Tangential Flow Filtration Applications and Scale Up Consider...
Pellicon 2
Implementing and Managing Pre-use Post-sterilization Integrity Testing (PUPSIT)
Normal Flow Filtration: Design and Scale Up
Potential Impact of Draft Annex 1 on Sterilizing Filtration
Find your filter. What’s best for your process?
A hands on guide to ultrafiltration1
Normal Flow Filtration: Design and Scale Up
Pellicon 3 biomax membrane
Parvovirus Filtration Best Practices - 25 Years of Hands-On Experience
Inline Flocculation for Harvest and Perfusate Clarification
Membrane Chromatography Solutions for Single-Use, Intensified mAb Purification
Process Development for Continuous Flow-Through Polishing Purification for mA...
Millipak® Final Fill Filters Reduce Contamination Risks and Simplify Filtrati...
Single-Pass Tangential Flow Filtration (SPTFF) Theory and Practice
A Cost Analysis and Evaluation of Perfused Seed Train Scenarios Through Proce...
Implementing a Fully Single-Use, Integrated mAb Biosimilars Purification Plat...
An Efficient and cGMP-friendly Solution to Diafiltration for Intensified or C...
Ad

Similar to Improve Process Efficiency in Bioprocess Streams by Prefiltration Optimization and Bioburden Reduction (20)

PDF
Cell Culture Media Filtration – Filter Selection and Sizing
PDF
Selection, sizing, and operation of bioprocess filtration trains for optimal ...
PDF
Cell Culture Media Filtration – Filter Selection and Sizing
PDF
Filtration Strategies for Optimal Development and Purification of a FMD Virus...
PDF
Find your filter. What’s best for your process?
PDF
Improved Product Recovery Using Blow-down and Millipak® Final Fill Filters
PDF
Sterile Filtration
PDF
Parvovirus Filtration Best Practices - 25 Years of Hands-On Experience
PDF
Tinospora cordifolia – AS BIOADSORBENT FOR REMOVAL OF FLUORIDE FROM WATER
PPT
liqui cel product overview
PPTX
Millipak Final Fill Filtration Presentation
PPTX
Implementing a Fully Single-Use, Integrated mAb Biosimilars Purification Plat...
PPTX
MEMBRANE FILTRATION PRESENTATION.pptx ppt
PDF
Membrane Bio reactor-2015 study material
PDF
Waste Water Treatment plant
PDF
Depth Filter flyer - final
PDF
Dannenberg waste waterfilter brochure
PDF
Dannenberg waste waterfilter brochure
PDF
Removal of Fluoride From Drinking Water Using Tea Waste as Adsorbent
PDF
EPM Module 5.pdf
Cell Culture Media Filtration – Filter Selection and Sizing
Selection, sizing, and operation of bioprocess filtration trains for optimal ...
Cell Culture Media Filtration – Filter Selection and Sizing
Filtration Strategies for Optimal Development and Purification of a FMD Virus...
Find your filter. What’s best for your process?
Improved Product Recovery Using Blow-down and Millipak® Final Fill Filters
Sterile Filtration
Parvovirus Filtration Best Practices - 25 Years of Hands-On Experience
Tinospora cordifolia – AS BIOADSORBENT FOR REMOVAL OF FLUORIDE FROM WATER
liqui cel product overview
Millipak Final Fill Filtration Presentation
Implementing a Fully Single-Use, Integrated mAb Biosimilars Purification Plat...
MEMBRANE FILTRATION PRESENTATION.pptx ppt
Membrane Bio reactor-2015 study material
Waste Water Treatment plant
Depth Filter flyer - final
Dannenberg waste waterfilter brochure
Dannenberg waste waterfilter brochure
Removal of Fluoride From Drinking Water Using Tea Waste as Adsorbent
EPM Module 5.pdf
Ad

More from Merck Life Sciences (20)

PDF
Launch of our new Titanium Dioxide Alternative
PDF
The Viscosity Reduction Platform: Viscosity-reducing excipients for improveme...
PDF
Use of Excipients in Downstream Processing to Improve Protein Purification
PDF
Exploring the protein stabilizing capability of surfactants against agitation...
PDF
The Viscosity Reduction Platform: Viscosity Reducing Excipients for Protein F...
PDF
Characterization of monoclonal antibodies and Antibody drug conjugates by Sur...
PDF
The Role of BioPhorum Extractables Data in the Effective Adoption of Single-U...
PDF
The Future of Pharma- and Biopharmaceutical Audits
PDF
Moving your Gene Therapy from R&D to IND: How to navigate the Regulatory Land...
PDF
Identity testing by NGS as a means of risk mitigation for viral gene therapies
PDF
Latest advancements of melt based 3D printing technologies for oral drug deli...
PDF
CAR-T Manufacturing Innovations that Work - Automating Low Volume Processes a...
PDF
Viral safety of biologics: What's changing with the ICH Q5A revision?
PDF
Improve Operational Efficiency by Over 30% with Product, Process, & Systems A...
PDF
Insights from a Global Collaboration Accelerating Vaccine Development with an...
PDF
Risk-Based Qualification of X-Ray Sterilization for Single-Use Systems
PDF
Rapid replication competent adenovirus (rRCA) detection: Accelerate your lot ...
PDF
The High Intensity Sweeteners Neotame and Sucralose: 2 Ways to ace the Patien...
PDF
The Developability Classification System (DCS): Enabling an Optimized Approac...
PDF
How to Accelerate and Enhance ADC Therapies
Launch of our new Titanium Dioxide Alternative
The Viscosity Reduction Platform: Viscosity-reducing excipients for improveme...
Use of Excipients in Downstream Processing to Improve Protein Purification
Exploring the protein stabilizing capability of surfactants against agitation...
The Viscosity Reduction Platform: Viscosity Reducing Excipients for Protein F...
Characterization of monoclonal antibodies and Antibody drug conjugates by Sur...
The Role of BioPhorum Extractables Data in the Effective Adoption of Single-U...
The Future of Pharma- and Biopharmaceutical Audits
Moving your Gene Therapy from R&D to IND: How to navigate the Regulatory Land...
Identity testing by NGS as a means of risk mitigation for viral gene therapies
Latest advancements of melt based 3D printing technologies for oral drug deli...
CAR-T Manufacturing Innovations that Work - Automating Low Volume Processes a...
Viral safety of biologics: What's changing with the ICH Q5A revision?
Improve Operational Efficiency by Over 30% with Product, Process, & Systems A...
Insights from a Global Collaboration Accelerating Vaccine Development with an...
Risk-Based Qualification of X-Ray Sterilization for Single-Use Systems
Rapid replication competent adenovirus (rRCA) detection: Accelerate your lot ...
The High Intensity Sweeteners Neotame and Sucralose: 2 Ways to ace the Patien...
The Developability Classification System (DCS): Enabling an Optimized Approac...
How to Accelerate and Enhance ADC Therapies

Recently uploaded (20)

PPT
OPIOID ANALGESICS AND THEIR IMPLICATIONS
PPTX
CEREBROVASCULAR DISORDER.POWERPOINT PRESENTATIONx
PPTX
JUVENILE NASOPHARYNGEAL ANGIOFIBROMA.pptx
DOC
Adobe Premiere Pro CC Crack With Serial Key Full Free Download 2025
PDF
Handout_ NURS 220 Topic 10-Abnormal Pregnancy.pdf
PPT
ASRH Presentation for students and teachers 2770633.ppt
PPTX
neonatal infection(7392992y282939y5.pptx
PPTX
post stroke aphasia rehabilitation physician
PPTX
Pathophysiology And Clinical Features Of Peripheral Nervous System .pptx
PPTX
ACID BASE management, base deficit correction
PPTX
Respiratory drugs, drugs acting on the respi system
PPTX
NEET PG 2025 Pharmacology Recall | Real Exam Questions from 3rd August with D...
PPTX
Imaging of parasitic D. Case Discussions.pptx
PDF
Therapeutic Potential of Citrus Flavonoids in Metabolic Inflammation and Ins...
PDF
Human Health And Disease hggyutgghg .pdf
PPTX
CME 2 Acute Chest Pain preentation for education
PPTX
SKIN Anatomy and physiology and associated diseases
PPT
genitourinary-cancers_1.ppt Nursing care of clients with GU cancer
PPTX
POLYCYSTIC OVARIAN SYNDROME.pptx by Dr( med) Charles Amoateng
PPT
Copy-Histopathology Practical by CMDA ESUTH CHAPTER(0) - Copy.ppt
OPIOID ANALGESICS AND THEIR IMPLICATIONS
CEREBROVASCULAR DISORDER.POWERPOINT PRESENTATIONx
JUVENILE NASOPHARYNGEAL ANGIOFIBROMA.pptx
Adobe Premiere Pro CC Crack With Serial Key Full Free Download 2025
Handout_ NURS 220 Topic 10-Abnormal Pregnancy.pdf
ASRH Presentation for students and teachers 2770633.ppt
neonatal infection(7392992y282939y5.pptx
post stroke aphasia rehabilitation physician
Pathophysiology And Clinical Features Of Peripheral Nervous System .pptx
ACID BASE management, base deficit correction
Respiratory drugs, drugs acting on the respi system
NEET PG 2025 Pharmacology Recall | Real Exam Questions from 3rd August with D...
Imaging of parasitic D. Case Discussions.pptx
Therapeutic Potential of Citrus Flavonoids in Metabolic Inflammation and Ins...
Human Health And Disease hggyutgghg .pdf
CME 2 Acute Chest Pain preentation for education
SKIN Anatomy and physiology and associated diseases
genitourinary-cancers_1.ppt Nursing care of clients with GU cancer
POLYCYSTIC OVARIAN SYNDROME.pptx by Dr( med) Charles Amoateng
Copy-Histopathology Practical by CMDA ESUTH CHAPTER(0) - Copy.ppt

Improve Process Efficiency in Bioprocess Streams by Prefiltration Optimization and Bioburden Reduction

  • 1. MerckMillipore.com The life science business of Merck operates as MilliporeSigma in the U.S. and Canada. Sherry Ashby Leon, Shannon Cleveland, Ravin Gami, Sal Giglia, Joseph Hersey, Nhung Nguyen, Andrew Koch, Songhua Liu Merck, Bedford MA, USA Introduction Membrane-based prefilters are an important component of many downstream operations. They are used to limit the variability of process streams by removing plugging contaminants thereby protecting sterilizing-grade filters and other unit operations. Some prefilters contribute to process safety by reducing bioburden in intermediate process steps where sterilizing grade filters are not required. Milligard® PES filters contain polyethersulfone (PES) membranes of different pore sizes for efficient particle removal from a broad range of process streams. These prefilters are compatible with caustic sanitization, gamma irradiation, autoclave and steam in place (SIP) sterilization methods. Table 1 lists the different pore sizes of Milligard® PES filters. This poster summarizes throughput and bacterial retention performance of Milligard® PES membranes in OptiScale® capsules challenged with different streams. Throughput capacity was determined either alone or with a downstream sterilizing-grade filter. © 2019 Merck KGaA, Darmstadt, Germany and/or its affiliates. All Rights Reserved. Merck, Millipore, the vibrant M, Milligard, OptiScale, Durapore, and Millipore Express are trademarks of Merck KGaA, Darmstadt, Germany or its affiliates. All other trademarks are the property of their respective owners. Detailed information on trademarks is available via publicly accessible resources. MK_PS2745EN Ver 2.0 09/2019 Improve Process Efficiency in Bioprocess Streams by Prefiltration Optimization and Bioburden Reduction Application Milligard® PES Filter Bioburden Reduction Particle & Bioburden Reduction 1.2/0.2 µm nominal >6 LRV Brevundimonas diminuta 1.2/0.45 µm >6 LRV Serratia marcescens Particle Reduction 1.2/0.8 µm NA Table 1. Milligard® PES Filters Methods Throughput capacity studies The streams used in these studies were selected to represent a wide range of particle sizes and particle size distributions (Figure 1); they were concentrated to achieve a high degree of plugging (> 90% flux decay at < 1000 L/m2 of filtrate). Throughput capacity of final sterilizing grade filters was measured both with and without Milligard® PES prefilter protection. The effect of different prefilter to final filter area ratios on throughput capacity was explored at area ratios ranging from 0.5:1 to 3:1. Tests were performed at both constant pressure (10 psi) and constant flow (500 LMH final filter) operating conditions. The experimental setup is illustrated in Figure 2. Figure 1. Particle size distributions of model streams Bioburden reduction studies Bioburden reduction was evaluated using Milligard® PES 1.2/0.2 µm nominal and 1.2/0.45 µm membrane in OptiScale® capsules challenged at 2 psi with Soy peptone spiked with Brevundimonas diminuta or Serratia marcescens. Retention of these microorganisms was evaluated at different points of filter plugging. Figure 2. Experimental setup for throughput capacity tests Results Final filter protection and throughput Figure 3 illustrates the throughput capacity of a Durapore® 0.22 µm filter alone, and paired with a Milligard ® PES 1.2/0.2 µm nominal prefilter. The capacity of the combined prefilter/final filter train was almost 10 fold higher than that of the sterilizing filter alone. (b) 500 LMH constant flow(a) 10 psi constant pressure 0 500 1000 1500 2000 0 50 100 Throughput(L/m2offinalfilter) Time (min) with prefilter without prefilter 0 5 10 15 20 25 30 0 500 1000 1500 2000 Presuure(psi) Throughput (L/m2 of final filter) without prefilter with prefilter The impact of prefiltration on final filter throughput capacity for the 3 pore sizes of Milligard® PES filters, with 3 different particle size distribution streams, and 2 types of final filters (PVDF and PES) is summarized in Figure 4. These studies were performed at constant pressure of 10 psi. The magnitude of final filter throughput improvements was dependent on the filter pore size, challenge feed, and the type of sterilizing filter. As prefilters have lower unit costs than sterilizing filters, any improvement in capacity due to prefilters can result in dramatic improvements in filtration economics. Figure 3. Effect of Milligard® PES 1.2/0.2 µm nominal filters on capacity of Durapore® 0.22 µm filter: (a) 10 psi constant pressure (b) 500 LMH (final filter) constant flow. Figure 4. Final filter capacity improvement by prefiltration. % improvement is compared to stand-alone final sterilizing filter: (a) Durapore® 0.22 µm (PVDF) final filter; (b) Millipore Express® SHF (PES) final filter. (a) Durapore® 0.22 µm (PVDF) final filter (b) Millipore Express® SHF (PES) final filter Optimization of area ratio Increasing prefilter area will often improve final filter capacity. Optimizing the prefilter to final filter area ratio can result in a cost-effective filtration solution. Figure 5 shows an example of the capacity benefit of different area ratios. A theoretical model is available for efficient system sizing and optimization. 0 500 1000 1500 2000 2500 3000 0 1 2 3 4 Throughput(L/m2finalfilter) Area Ratio (Pre/Final Filter) Model Data Millipore Express® SHF only Figure 5. Effect of prefilter (Milligard® PES 1.2/0.2 µm nominal) to final filter (Millipore Express® SHF) area ratio on throughput capacity in Soy peptone at 10 psi constant pressure. Particle removal by prefilters Prefilters protect final filters and other unit operations by removing particles that would otherwise plug or contaminate downstream unit operations. Particle removal capability was quantified by measuring cumulative concentration of particles of different sizes in the Soy peptone challenge and filtrate solutions after processing through Milligard® PES filters. Most particles in this solution are smaller than 1.0 µm in size, with the highest concentration being at approximately 0.2 µm in diameter (Figure 1). Figure 6 shows that all Milligard® PES filters retained over 90% of the particles between 0.2 µm and 1.0 µm. Figure 6. Soy peptone particle retention by Milligard® PES filters. Bioburden reduction Prefilters can provide an increased level of process safety by reducing bioburden. Milligard® PES 1.2/0.2 µm nominal filters have been validated to demonstrate >6 log B. diminuta retention while the Milligard® PES 1.2/0.45 µm filters have been validated to demonstrate >6 log retention of S. marcescens. Figure 7 shows microorganism retention by ‘stand alone’ Milligard® PES 1.2/0.2 µm nominal and Milligard® PES 1.2/0.45 µm filters in the absence of a final sterilizing filter. The microorganism challenge level was > 107 cfu/cm2 and filtrate grab samples were collected at different points of filter plugging. As would be expected based on a retention mechanism based on size exclusion, microorganism retention was robust (no breakthrough) under all conditions. Figure 7. Log reduction values (LRV) as a function of filter plugging. (a) Milligard® PES 1.2/0.2 µm nominal filters challenged with B. diminuta; (b) Milligard® PES 1.2/0.45 µm filters challenged with S. marcescens. Data points indicate results from individual OptiScale® 25 devices; arrows indicate complete retention. Summary Milligard® PES filters are available in a range of pore sizes for processing different streams, are compatible with multiple sterilization methods, and have been validated to reduce bioburden. These filters: • Dramatically improve the throughput capacity of both PVDF and PES sterilizing-grade filters, significantly improving filtration economics. • Efficiently remove particulates from process streams. • Can be used ‘stand-alone’ to provide sustained bioburden reduction even under conditions of extreme filter plugging. (a) Milligard® PES 1.2/0.2 µm nominal filter retention of B. diminuta (b) Milligard® PES 1.2/0.45 µm filter retention of S. marcescens To quantify the particle removal capability of the prefilters, particle concentrations and size distributions of the challenge stream feeds and filtrates were measured using an optical particle counter (Liquilaz SO2). 0% 20% 40% 60% 80% 100% Particle sizes 0.2-1.0 µm ParticleRetention Milligard® PES 1.2/0.2 µm nominal Milligard® PES 1.2/0.45 µm Milligard® PES 1.2/0.8 µm 0 200 400 600 800 1000 1200 1400 1600 Soy Peptone Whey Soy T CapacityIncreasebyPrefiltration (%) Milligard® PES 1.2/0.2 µm nominal Milligard® PES 1.2/0.45 µm Milligard® PES 1.2/0.8 µm 0 50 100 150 200 250 300 350 400 Soy Peptone Whey Soy T CapacityIncreasebyPrefiltration(%) Milligard® PES 1.2/0.2 µm nominal Milligard® PES 1.2/0.45 µm Milligard® PES 1.2/0.8 µm 0 2 4 6 8 10 0 20 40 60 80 100 LRV % Flow Decay 0 2 4 6 8 10 0 20 40 60 80 100 LRV % Flow Decay