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R E P R I N T F R O M
Implementing Process-Scale Adenovirus
Purification with a Single-Use Platform
Amélie Boulais, Nick Hutchinson,
and Fritjof Linz
The biopharmaceutical industry has
tended to adopt manufacturing platforms
to reduce both process development costs
and the time taken for new drugs to reach
the clinic. Platform processes are capable
of producing many similar products from
the same family with only minor adjust-
ments to operating parameters. This al-
lows companies to avoid having to “re-
invent the wheel” for every new product
that is in development while enabling
them to draw upon best practices identi-
fied from previous projects.
Biopharmaceutical companies can
implement recombinant viral vector plat-
forms with a completely single-use flow
path rather than installing stainless steel
equipment. Installing and qualifying sin-
gle-use technology is much easier, cheap-
er, and faster than multiple-use equip-
ment. It allows for closed system process-
ing that is vital when the viral vaccine is
too large for sterilization by filtration.
Single-use technologies improve vac-
cine safety by both reducing the risk of
product cross-contamination and batch-
to-batch contamination. Membrane ad-
sorbers are a single-use technology that
has proven effective in virus purification.
They have high capacities and give excel-
lent yields because the macroporous struc-
ture of the membrane allows the viruses
to enter the inner pore surface easily and
rapidly. The virus has access to all of the
ligands because of the absence of a steric
exclusion effect. The design of membrane
adsorbers is continuing to evolve.
Novel Membrane Chemistries
This tutorial describes the production
of adenovirus with the single-use plat-
form shown in Figure 1.
Sartorius Stedim Biotech (SSB) has as-
sembled the platform from existing and
proven technologies, available from lab
to production scale, that meet the qual-
ity requirements of the vaccine indus-
try. The approach has been successfully
demonstrated for the purification of an
Adenovirus serotype 5 vector, at the 20
L scale. It allows the complete purifica-
tion of the vaccine in one day. Table 1
shows the performance of the platform
straight-from-the-box and with minimal
optimization.
The process starts in the bioreac-
tor with the infection of HEK293 cells
grown in a serum-free media. The cell
concentration at infection was 1x106
cells/mL and a multiplicity of infection of
five. Performing a cell lysis step at the end
of the cell culture maximizes the yield of
virus particles from the bioreactor but
also releases large quantities of DNA.
EnablingViralVaccine Production
September 15, 2016
GENengnews.com
BIOPROCESSING
Tutorial
Amélie Boulais (amelie.boulais@sartorius-
stedim.com) is Process Development
Consultant, Integrated Solutions, Dr. Nick
Hutchinson works as technical content
manager, and Fritjof Linz, Ph.D., is vp,
purification, all at Sartorius Stedim Biotech.
Website: www.sartorius.com.
LeadingtheWayinLifeScienceTechnologies
Figure 1. A single-use platform process for viral vaccine production
Adding an endonuclease to the biore-
actor, such as DENARASE, digests the
released DNA and facilitates subsequent
purification operations.
The next step after the DNA digest
is to harvest the bioreactor. Electrostatic
interactions between virus particles and
diatomaceous earth depth filters can po-
tentially reduce the step yield so, if possi-
ble, we recommend manufacturers use a
polypropylene depth filter such as a Sar-
topure PP3 prefilter. This is constructed
from a fine microfiber fleece material
that improves clarification performance
and has a contained capsule format.
The clarification step should be com-
pleted using a suitable sterilizing-grade
filter capsule such as a Sartopore2 XLG.
Filter-sizing experiments may be required
at this stage of the process depending on
the bioreactor biomass concentration
and the amount of endonuclease added
to your specific process.
SSB recommends using the cassette
format for ultrafiltration steps in our
downstream platform process. These al-
low for simple scale-up while still deliv-
ering high yields (Table).
Ultrafiltration Step
During the first ultrafiltration step,
we advise manufacturers to use a mem-
brane with a nominal molecular weight
cut-off of 300 kDa. During the process
run we performed, the harvested Adeno-
virus was concentrated 10-fold and then
conditioned with 5 diafiltration volumes
of 50 mM Hepes, 150 mM NaCl, pH
7.5 for loading onto the subsequent
membrane adsorber step.
A 300 kDa PESU-membrane will re-
tain virus particles but will also allow the
removal of significant amounts of con-
taminating DNA and host cell proteins.
Figure 2 shows a chromatogram from
the Sartobind Q membrane adsorber
step used in the purification of the Ade-
novirus serotype 5 virus with a bind-and-
elute method. The flow rate was limited
by the standard chromatography hard-
ware to 1MV/min.
However, the step was still performed
in just 30 minutes. Under these condi-
tions, it was possible to achieve a bind-
ing capacity of 6 × 1012
virus particles/
mL of membrane and reduce the DNA
level more than 15-fold.
The elution pool from the Sartobind
Q membrane may require a subsequent
polishing step to capture the residual
nucleic acids. This step can be operated
in flowthrough mode with a Sartobind
STIC membrane adsorber. This is a weak
anion-exchanger with a unique primary
amine chemistry.
The solution must have phosphate
ions added to it before it is loaded onto
this impurity capture step. Process de-
velopment engineers should perform
an optimization study to identify the
optimum phosphate concentration of
the load that will allow the membrane
adsorber membrane to remove nucleic
acids without binding the product and
reducing the yield.
In our experience with Adenovirus, a
loading buffer and load with a sodium
phosphate concentration of 250 mM
worked well, along with a loading ca-
pacity of 6.4 × 1013
virus particles/mL of
November 15, 2016 | GENengnews.com | Genetic Engineering & Biotechnology News	
Table. Processperformancetargetsachievedwithasingle-useviralvectorplatformat20Lscale
Unit Operation Step Yield (%)
Endonuclease Treatment 100
Clarification 98
Ultrafiltration 99
Bind and Elute Purification 78
Contaminant Capture Purification 85
Final Concentration and Diafiltration/Filtration 86
Overall Process Performance
Yield 55%
Final Host Cell Protein Concentration <20 mg/mL
Final DNA Concentration <10 ng/dose
Final Endonuclease Concentration <5 ng/mL
Figure 2. Typical
elution chromatogram
profile of Adenovirus
serotype 5 using
Sartobind Q membrane
adsorber for primary
purification step
(Equilibration: 50
mM Hepes, 200 mM
NaCl, pH 7.5; Wash: 50
mM Hepes, 200 mM
NaCl, pH 7.5; Isocratic
elution: 65% (v/v) of
50 mM Hepes pH 7.5,
1M NaCl. Strip: 50 mM
Hepes, pH 7.5, 1M NaCl)
membrane. The step reduced the DNA
concentration of the process stream to
0.7 ng DNA/dose, far below our target
of 10 ng DNA/dose.
The Sartobind STIC elution pool can
be concentrated, if required, and diafil-
tered with the formulation buffer in a
final ultrafiltration step. For this opera-
tion, SSB recommends a membrane with
a nominal molecular weight cut-off of
100 kDa.
Cassettes with stabilized cellulose
membrane are extremely hydrophilic to
limit fouling while maximizing the mem-
brane flux performance and product step
yield. Hydrosart cassettes were used dur-
ing the Adenovirus purification.
In conclusion, a single-use platform
is available for the purification of viral
vaccines and SSB has demonstrated its
application in an Adenovirus manufac-
turing process at the 20 L scale. It is flex-
ible and can be scale-up to 2,000 L in
a single-use format. The platform is a
preconfigured set of unit operations for
which SSB can recommend suitable op-
erating conditions.
The platform requires little addition-
al development work or capital expen-
diture but will allow drug developers
to establish manufacturing processes
quickly and reduce the time it takes to
reach the market with new viral vaccine
products.	
Genetic Engineering & Biotechnology News | GENengnews.com | November 15, 2016

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Single-Use Platform for Adenovirus Vaccine Purification

  • 1. R E P R I N T F R O M Implementing Process-Scale Adenovirus Purification with a Single-Use Platform Amélie Boulais, Nick Hutchinson, and Fritjof Linz The biopharmaceutical industry has tended to adopt manufacturing platforms to reduce both process development costs and the time taken for new drugs to reach the clinic. Platform processes are capable of producing many similar products from the same family with only minor adjust- ments to operating parameters. This al- lows companies to avoid having to “re- invent the wheel” for every new product that is in development while enabling them to draw upon best practices identi- fied from previous projects. Biopharmaceutical companies can implement recombinant viral vector plat- forms with a completely single-use flow path rather than installing stainless steel equipment. Installing and qualifying sin- gle-use technology is much easier, cheap- er, and faster than multiple-use equip- ment. It allows for closed system process- ing that is vital when the viral vaccine is too large for sterilization by filtration. Single-use technologies improve vac- cine safety by both reducing the risk of product cross-contamination and batch- to-batch contamination. Membrane ad- sorbers are a single-use technology that has proven effective in virus purification. They have high capacities and give excel- lent yields because the macroporous struc- ture of the membrane allows the viruses to enter the inner pore surface easily and rapidly. The virus has access to all of the ligands because of the absence of a steric exclusion effect. The design of membrane adsorbers is continuing to evolve. Novel Membrane Chemistries This tutorial describes the production of adenovirus with the single-use plat- form shown in Figure 1. Sartorius Stedim Biotech (SSB) has as- sembled the platform from existing and proven technologies, available from lab to production scale, that meet the qual- ity requirements of the vaccine indus- try. The approach has been successfully demonstrated for the purification of an Adenovirus serotype 5 vector, at the 20 L scale. It allows the complete purifica- tion of the vaccine in one day. Table 1 shows the performance of the platform straight-from-the-box and with minimal optimization. The process starts in the bioreac- tor with the infection of HEK293 cells grown in a serum-free media. The cell concentration at infection was 1x106 cells/mL and a multiplicity of infection of five. Performing a cell lysis step at the end of the cell culture maximizes the yield of virus particles from the bioreactor but also releases large quantities of DNA. EnablingViralVaccine Production September 15, 2016 GENengnews.com BIOPROCESSING Tutorial Amélie Boulais (amelie.boulais@sartorius- stedim.com) is Process Development Consultant, Integrated Solutions, Dr. Nick Hutchinson works as technical content manager, and Fritjof Linz, Ph.D., is vp, purification, all at Sartorius Stedim Biotech. Website: www.sartorius.com. LeadingtheWayinLifeScienceTechnologies Figure 1. A single-use platform process for viral vaccine production
  • 2. Adding an endonuclease to the biore- actor, such as DENARASE, digests the released DNA and facilitates subsequent purification operations. The next step after the DNA digest is to harvest the bioreactor. Electrostatic interactions between virus particles and diatomaceous earth depth filters can po- tentially reduce the step yield so, if possi- ble, we recommend manufacturers use a polypropylene depth filter such as a Sar- topure PP3 prefilter. This is constructed from a fine microfiber fleece material that improves clarification performance and has a contained capsule format. The clarification step should be com- pleted using a suitable sterilizing-grade filter capsule such as a Sartopore2 XLG. Filter-sizing experiments may be required at this stage of the process depending on the bioreactor biomass concentration and the amount of endonuclease added to your specific process. SSB recommends using the cassette format for ultrafiltration steps in our downstream platform process. These al- low for simple scale-up while still deliv- ering high yields (Table). Ultrafiltration Step During the first ultrafiltration step, we advise manufacturers to use a mem- brane with a nominal molecular weight cut-off of 300 kDa. During the process run we performed, the harvested Adeno- virus was concentrated 10-fold and then conditioned with 5 diafiltration volumes of 50 mM Hepes, 150 mM NaCl, pH 7.5 for loading onto the subsequent membrane adsorber step. A 300 kDa PESU-membrane will re- tain virus particles but will also allow the removal of significant amounts of con- taminating DNA and host cell proteins. Figure 2 shows a chromatogram from the Sartobind Q membrane adsorber step used in the purification of the Ade- novirus serotype 5 virus with a bind-and- elute method. The flow rate was limited by the standard chromatography hard- ware to 1MV/min. However, the step was still performed in just 30 minutes. Under these condi- tions, it was possible to achieve a bind- ing capacity of 6 × 1012 virus particles/ mL of membrane and reduce the DNA level more than 15-fold. The elution pool from the Sartobind Q membrane may require a subsequent polishing step to capture the residual nucleic acids. This step can be operated in flowthrough mode with a Sartobind STIC membrane adsorber. This is a weak anion-exchanger with a unique primary amine chemistry. The solution must have phosphate ions added to it before it is loaded onto this impurity capture step. Process de- velopment engineers should perform an optimization study to identify the optimum phosphate concentration of the load that will allow the membrane adsorber membrane to remove nucleic acids without binding the product and reducing the yield. In our experience with Adenovirus, a loading buffer and load with a sodium phosphate concentration of 250 mM worked well, along with a loading ca- pacity of 6.4 × 1013 virus particles/mL of November 15, 2016 | GENengnews.com | Genetic Engineering & Biotechnology News Table. Processperformancetargetsachievedwithasingle-useviralvectorplatformat20Lscale Unit Operation Step Yield (%) Endonuclease Treatment 100 Clarification 98 Ultrafiltration 99 Bind and Elute Purification 78 Contaminant Capture Purification 85 Final Concentration and Diafiltration/Filtration 86 Overall Process Performance Yield 55% Final Host Cell Protein Concentration <20 mg/mL Final DNA Concentration <10 ng/dose Final Endonuclease Concentration <5 ng/mL Figure 2. Typical elution chromatogram profile of Adenovirus serotype 5 using Sartobind Q membrane adsorber for primary purification step (Equilibration: 50 mM Hepes, 200 mM NaCl, pH 7.5; Wash: 50 mM Hepes, 200 mM NaCl, pH 7.5; Isocratic elution: 65% (v/v) of 50 mM Hepes pH 7.5, 1M NaCl. Strip: 50 mM Hepes, pH 7.5, 1M NaCl)
  • 3. membrane. The step reduced the DNA concentration of the process stream to 0.7 ng DNA/dose, far below our target of 10 ng DNA/dose. The Sartobind STIC elution pool can be concentrated, if required, and diafil- tered with the formulation buffer in a final ultrafiltration step. For this opera- tion, SSB recommends a membrane with a nominal molecular weight cut-off of 100 kDa. Cassettes with stabilized cellulose membrane are extremely hydrophilic to limit fouling while maximizing the mem- brane flux performance and product step yield. Hydrosart cassettes were used dur- ing the Adenovirus purification. In conclusion, a single-use platform is available for the purification of viral vaccines and SSB has demonstrated its application in an Adenovirus manufac- turing process at the 20 L scale. It is flex- ible and can be scale-up to 2,000 L in a single-use format. The platform is a preconfigured set of unit operations for which SSB can recommend suitable op- erating conditions. The platform requires little addition- al development work or capital expen- diture but will allow drug developers to establish manufacturing processes quickly and reduce the time it takes to reach the market with new viral vaccine products. Genetic Engineering & Biotechnology News | GENengnews.com | November 15, 2016