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Monoclonal Antibody Separation: Lucentis from Genentech
Author
Dinh, JustingHeck, Greg
Lynam, Phillip
Mar, Diane
Marshall, Kevin J.
Mischel, Nolan
Olson, Jared R.
Ramirez, Adrian Z.
Date
2012Type
ThesisDepartment
Chemical and Materials Engineering
Degree Level
Honors Thesis
Degree Name
Chemical Engineering
Abstract
This design project focuses on the bioseparation of Lucentis (Genentech Inc.), a
humanized anti-VEGF-A monoclonal antibody fragment used to treat macular
degeneration. Vascular endothelial growth factor, VEGF, promotes blood vessel growth
in the wet form of macular degeneration. These fragile blood vessels easily break and
lead to bleeding within the macula, which causes a gradual loss of sight. Anti-VEGF-A
suppresses the growth of blood vessels by binding to VEGF.
The process design begins with a 1000 L batch of fermented culture. The cell
culture fluid contains approximately 5 g/L of antibody and 20 to 25 % of cell material.
The goal is to produce a final purified solution of 10-30 g/L antibody at 99 % purity.
The bioprocesses to be investigated include: fermentation, homogenization,
centrifugation, chromatography (HIC and cation exchange) and membrane utrafiltration.
Alternative cases will also be explored in which the chromatography steps are replaced
with G-Protein and immobilized metal chromatography.
The project objective is to assemble these various separation steps into a process
capable of separating and purifying the target antibody from the cell culture fluid. The
final product is an aqueous solution of the pure antibody in a formulation solution. The
key aspect of this study is the optimization of both purity and step yield for each process
step. Experimentally, the presence and separation of Lucentis was confirmed through
ELISA, SDS PAGE and mass spectroscopy. A base case of HIC and IEX was assumed.
HIC was inconclusive and requires further testing to determine the parameters necessary
for separation. IEX was found to successfully purify the concentrate. However, the
Lucentis sample requires pretreatment and salt removal before feed into the
IEX. Promising alternative cases include IMAC and Affinity G Protein which yielded
the highest degree of purification experimentally with approximately 62.7% of Lucentis
eluted in the protein sample. However, these base cases are limited due to the cost of the
method, although preliminary economic analysis suggests that IMAC may be
economically feasible.
All downstream separation processes include a report on theory, experimental
results and design, operational parameters, and sizing estimations and economic analysis
for industrial operation. The economic analysis includes operational costs and raw
material costs. An understanding of the mechanisms of separation, experimental results
and economic analysis are presented in a final report and a poster.
Permanent link
http://hdl.handle.net/11714/358Additional Information
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