Publications
2020
P. Gagnon, B. Goričar, Š. Peršič, U. Černigoj, A. Štrancar
Cell & Gene Therapy Insights 2020; 6(7), 1035–1046
Abstract:
One of the barriers to development of industrial purification platforms for large mRNA has been an inadequate selection of high-performing capture-purification tools. Hybridization-affinity uses a polythymidine (Oligo dT) ligand to base-pair with the polyadenine tail of mRNA. It can be used for capture but it cannot discriminate dsRNA (double-stranded) from ssRNA (single-stranded) and it supports only brief cleaning with 100 mM sodium hydroxide. Traditional anion exchangers elute only mRNA smaller than about 500 bases unless the columns are heated to 50–70°C. Hydrophobic interaction chromatography (HIC) and reverse phase chromatography (RPC) separate ssRNA from dsRNA and short transcripts, but their sensitivity to fouling by proteins and aggregates makes them better suited for polishing than for capture. Better capture options are needed to meet the needs of large clinical trials, scale-up, and manufacture of vaccines. Beyond that, a new spectrum of gene therapy treatments await. This article introduces two new capture options that both eliminate dsRNA, DNA, and proteins in a wash step, then provide high-resolution polishing of ssRNA in an elution gradient at ambient temperature. One represents a new class of anion exchangers. The other exploits hydrogen bonding. Both support prolonged exposure to 1 M sodium hydroxide. Easy transition to either HIC or RPC provides high-resolution orthogonal polishing.
2019
Calef Sánchez-Trasviña, Marco Rito-Palomares, and José González-Valdez
Advances in Polymer Technology, Volume 2019, December 12 2019, 10 pages
Abstract
PEGylated or polyethylene glycol-modified proteins have been used as therapeutic agents in different diseases. However, the major drawback in their procurement is the purification process to separate unreacted proteins and the PEGylated species. Several efforts have been done to separate PEGylation reactions by chromatography using different stationary phases and modified supports. In this context, this study presents the use of chromatographic monoliths modified with polyethylene glycol (PEG) to separate PEGylated Ribonuclease A (RNase A). To do this, Convective Interaction Media (CIM) Ethylenediamine (EDA) monolithic disks were PEGylated using three PEG molecular weights (1, 10, and 20 kDa). The PEGylated monoliths were used to separate PEGylated RNase A modified, as well, with three PEG molecular weights (5, 20, and 40 kDa) by hydrophobic interaction chromatography. Performance results showed that Bovine Serum Albumin (BSA) can bind to PEGylated monoliths and the amount of bound BSA increases when ammonium sulfate concentration and flow rate increase. Furthermore, when PEGylated RNase A was loaded into the PEGylated monoliths, PEG-PEG interactions predominated in the separation of the different PEGylated species (i.e., mono and di-PEGylated). It was also observed that the molecular weight of grafted PEG chains to the monolith impacts strongly in the operation resolution. Interestingly, it was possible to separate, for the first time, isomers of 40 kDa PEGylated RNase A by hydrophobic interaction chromatography. This technology, based on PEGylated monoliths, represents a new methodology to efficiently separate proteins and PEGylated proteins. Besides, it could be used to separate other PEGylated molecules of biopharmaceutical or biotechnological interest.
2018
Tsutomu Arakawa, Pete Gagnon
Journal of Pharmaceutical Sciences 107 (2018) 2297-2305
The concept of cosolvent exclusion was developed by a group of Timasheff's laboratory in 1970-1990 and is currently used widely to explain the effects of a variety of cosolvents on the stability and solubility of macromolecules. Not surprisingly, these concepts have had substantial influence in the fields of formulation, protein folding and unfolding, but they have perhaps more surprisingly found their way into the field of chromatography. A variety of excluded cosolvents have been used to enhance binding and resolution of proteins and other macromolecules in ion exchange, hydroxyapatite, affinity, and hydrophobic interaction chromatography. These cosolvents include salting-out salts, amino acids and polymers, and frequently polyethylene glycol (PEG). A new mode of chromatography, termed “steric exclusion chromatography,” was recently introduced. It employs hydroxylated solid phase surfaces. Steric exclusion of the PEG stabilizes the association of macromolecules with the solid phase. Elution is achieved by reducing the PEG concentration. Magnetic particles are also used in this chromatography. This review summarizes the concepts of preferential cosolvent exclusion and its applications in column chromatography.
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2017
V.Rajamanickam, D.Wurm, C.Slouka, C.Herwig, O.Spadiut
Anal Bioanal Chem (2016)
The bacterium Escherichia coli is a well-studied recombinant host organism with a plethora of applications in biotechnology. Highly valuable biopharmaceuticals, such as antibody fragments and growth factors, are currently being produced in E. coli. However, the high metabolic burden during recombinant protein production can lead to cell death, consequent lysis, and undesired product loss. Thus, fast and precise analyzers to monitor E. coli bioprocesses and to retrieve key process information, such as the optimal time point of harvest, are needed. However, such reliable monitoring tools are still scarce to date. In this study, we cultivated an E. coli strain producing a recombinant single-chain antibody fragment in the cytoplasm. In bioreactor cultivations, we purposely triggered cell lysis by pH ramps. We developed a novel toolbox using UV chromatograms as fingerprints and chemometric techniques to monitor these lysis events and used flow cytometry (FCM) as reference method to quantify viability offline. Summarizing, we were able to show that a novel toolbox comprising HPLC chromatogram fingerprinting and data science tools allowed the identification of E. coli lysis in a fast and reliable manner. We are convinced that this toolbox will not only facilitate E. coli bioprocess monitoring but will also allow enhanced process control in the future
Sebastijan Peljhan, Tina Jakop, Dunja Šček, Vid Skvarča, Blaž Goričar, Romina Žabar, Nina Mencin. Electrophoresis 2017 July 20
The plasma-derived IgG used either for diagnostic purpose or intravenous application (in form of IVIG) in various medical therapies is certainly gaining more and more attention on annual basis. Different manufacturing processes are used to isolate immunoglobulins from human plasma. However, a quest for alternative paths in IgG isolation not only requires development of the most efficient isolation process, but also a rapid and reliable analytics to track the purification. Fast and reliable fingerprint based method for characterization of IgG prepared from Cohn I+II+III paste is presented in this paper. The fingerprint method bases on partial separation of proteins in linear gradient on CIMacTM quaternary amine, strong anion exchange group (QA) 0.1 mL column. Partial separation of proteins does not allow simple quantitative analysis of the samples during the IgG isolation from Cohn I+II+III fraction paste, but very accurate qualitative information about the composition of the sample can be obtained in less than 5 min. From the differences in the chromatograms of various samples, the ratio between IgG and impurities in each sample can be easily assessed. The method is suitable for input material control, in-line monitoring of the downstream processing, final control of the products, as well as in stability studies and enables taking fast and accurate decisions during fractionation process.
Antonio M. Munoz, Paul Yourik, Vaishnavi Rajagopal, Jagpreet S. Nanda, Jon R. Lorsch, Sarah E. Walker
RNA Biology, 2017, VOL. 14, NO. 2, 188–196
In vitro studies of translation provide critical mechanistic details, yet purification of large amounts of highly active eukaryotic ribosomes remains a challenge for biochemists and structural biologists. Here, we present an optimized method for preparation of highly active yeast ribosomes that could easily be adapted for purification of ribosomes from other species. The use of a nitrogen mill for cell lysis coupled with chromatographic purification of the ribosomes results in 10-fold-increased yield and less variability compared with the traditional approach, which relies on sedimentation through sucrose cushions. We demonstrate that these ribosomes are equivalent to those made using the traditional method in a host of in vitro assays, and that utilization of this new method will consistently produce high yields of active yeast ribosomes.
Attachments
2015
D. Buzzi, A. Štrancar
Chimica Oggi-Chemistry Today; Vol 33(1) January/February 2015
The importance of the monitoring of a process all along its steps by means of PAT has been defined by FDA in 2002. How can be defined the product quality and what are the parameters that should be checked by means of different analysis techniques, being focused in particular on the application of high pressure liquid chromatography techniques (HPLC) as high value tool for the process monitoring. From the first introduction of Process Analytical Technology to the "state of the art": how can be PAT implemented in order to ensure the final product quality.
P. Kramberger, U. Lidija, A. Štrancar
Human Vaccines & Immunotherapeutics, 11:4 (2015) 1010-1021
Downstream processing of nanoplexes (viruses, virus-like particles, bacteriophages) is characterized by complexity of the starting material, number of purification methods to choose from, regulations that are setting the frame for the final product and analytical methods for upstream and downstream monitoring. This review gives an overview on the nanoplex downstream challenges and chromatography based analytical methods for efficient monitoring of the nanoplex production.
A. G. Lopes
FBP-461, Food and Bioproducts Processing (2014)
As the biopharmaceutical industry matures, the trend towards increased flexibility and productivity, faster time tomarket and greater profitability are driving the replacement of traditional stainless steel equipment by single-use technology (SUT). The use of SUT in the biopharmaceutical industry can significantly impact the manufacturing process efficiency by reducing capital costs, improving plant flexibility, reducing start-up times and costs, and elim-inating both non-value added process steps and the risk of cross-contamination. In addition it significantly reduces process liquid waste, labour costs and on-site quality and validation requirements. This paper reviews the current status of the technology and the impact of SUT in the biopharmaceutical industry, with the aim of identifying the challenges and limitations that still need to be addressed for further adoption of these technologies. Even tough SUT has a multitude of systems available, its components and assemblies have little standardisation as well as alack of harmonised tests and procedures among suppliers, with an array of guidelines from a variety of sourcesand no critical limits have been established. In addition, the use of SUT has new validation requirements such as leachables and extractables, suppliers’ qualification and SUT lot-to-lot variability. The lack of expertise in these areas and the new training requirements when using SUT also need to be addressed. To date the majority of the avail-able literature regarding SUT is found in trade journals where typically suppliers are the main contributors. There is still a lack of engagement of the academic community, which contributes to very limited scientific proof from independent peer-reviewed research to support performance of SUT. This is particularly the case during operation and integrity testing of SUT, during for example on-site testing, transport and disposal. Another area where no work has been undertaken concerns conceptual approaches for facility clean-room requirement and appropriate layout design using SUT. Investment in novel technologies, research, standardisation and training is paramount for further development and implementation of SUTs across all sectors of the biopharmaceutical industry.
2014
F. W. Krainer, R. Pletzenauer, L. Rossetti, C. Herwig, A. Glieder, O. Spadiut
Protein Expression and Purification 95 (2014) 104–112
The plant enzyme horseradish peroxidase (HRP) is used in several important industrial and medical applications, of which especially biosensors and diagnostic kits describe an emerging field. Although there is an increasing demand for high amounts of pure enzyme preparations, HRP is still isolated from the plant as a mixture of different isoenzymes with different biochemical properties. Based on a recent next generation sequencing approach of the horseradish transcriptome, we produced 19 individual HRP isoenzymes recombinantly in the yeast Pichia pastoris. After optimizing a previously reported 2-step purification strategy for the recombinant isoenzyme HRP C1A by substituting an unfavorable size exclusion chromatography step with an anion exchange step using a monolithic column, we purified the 19 HRP isoenzymes with varying success. Subsequent basic biochemical characterization revealed differences in catalytic activity, substrate specificity and thermal stability of the purified HRP preparations. The preparations of the isoenzymes HRP A2A and HRP A2B were found to be highly interesting candidates for future applications in diagnostic kits with increased sensitivity.
F. W. Krainer, R. Pletzenauer, L. Rossetti, C. Herwig, A. Glieder, O. Spadiut
Protein Expression and Purification 95 (2014) 104–112
The plant enzyme horseradish peroxidase (HRP) is used in several important industrial and medical applications, of which especially biosensors and diagnostic kits describe an emerging field. Although there is an increasing demand for high amounts of pure enzyme preparations, HRP is still isolated from the plant as a mixture of different isoenzymes with different biochemical properties. Based on a recent next generation sequencing approach of the horseradish transcriptome, we produced 19 individual HRP isoenzymes recombinantly in the yeast Pichia pastoris. After optimizing a previously reported 2-step purification strategy for the recombinant isoenzyme HRP C1A by substituting an unfavorable size exclusion chromatography step with an anion exchange step using a monolithic column, we purified the 19 HRP isoenzymes with varying success. Subsequent basic biochemical characterization revealed differences in catalytic activity, substrate specificity and thermal stability of the purified HRP preparations. The preparations of the isoenzymes HRP A2A and HRP A2B were found to be highly interesting candidates for future applications in diagnostic kits with increased sensitivity.
2013
A. A. Shukla, U. Gottschalk
Trends in Biotechnology (2012) 1-8
The manufacture of protein biopharmaceuticals is conducted under current good manufacturing practice (cGMP) and involves multiple unit operations for upstream production and downstream purification. Until recently, production facilities relied on the use of relatively inflexible, hard-piped equipment including large stainless steel bioreactors and tanks to hold product intermediates and buffers. However, there is an increasing trend towards the adoption of single-use technologies across the manufacturing process. Technical advances have now made an end-to-end single-use manufacturing facility possible, but several aspects of single-use technology require further improvement and are continually evolving. This article provides a perspective on the current state-of-the-art in single-use technologies and highlights trends that will improve performance and increase the market penetration of disposable manufacturing in the future.
M. Li, Y. X. Qiu
Vaccine 31 (2013) 1264-1267
An effective downstream bio-processing of vaccine products requires complete chemical knowledge of the contaminants that may arise from a given vector expression system. Whether the vaccine is made from the traditional egg-based or the new cell-cultured process, it is the expression system that determines the types of impurities that need to be identified and removed from the vaccine product.
There are mechanical and chemical factors that can either reduce the yield or render a vaccine product to be irreversibly inactive. The choice of equipment and solvents is therefore important in minimizing product loss, and for maintaining an efficient and optimized manufacturing process.
The frequent out-of-specification, irreproducible data and inefficiency in the manufacturing of biologics were the basis for FDA to propose the “cGMP for the 21st Century” initiative in the year of 2000. Effective 2004, the concept of quality by design (QbD) has been imposed in the manufacturing of biologics. To facilitate the implementation of QbD FDA has encouraged the use of process analytical technology (PAT). Further, FDA believes that an optimized manufacturing scheme requires one to identify and to control the variables that can negatively affect the yield and quality of the desired product, and PAT can reveal wrongful data and alert the operator for immediate correction during processing.
M. Bartolini, I. W. Wainer, C. Bertucci, V. Andrisano
Journal of Pharmaceutical and Biomedical Analysis 73 (2013) 77-81
Adenosine nucleotides are involved as substrates or co-factors in several biochemical reactions, catalyzed by enzymes, which modulate energy production, signal transduction and cell proliferation. We here report the development and optimization of an ion exchange liquid chromatography (LC) method for the determination of ATP, ADP and AMP. This method is specifically aimed at the determination of the ATP-ase activity of human heat shock protein 90 (Hsp90), a molecular chaperone that has emerged as target enzyme in cancer therapy. Separation of the three nucleotides was achieved in a 15-min run by using a disk shaped monolithic ethylene diamine stationary phase of small dimensions (2 mm × 6 mm i.d.), under a three-solvent gradient elution mode and UV detection at 256 nm. The described direct LC method resulted highly specific as a consequence of the baseline separation of the three adenosine nucleotides and could be applied to the determination of the enzymatic activity of ADP/ATP generating or consuming enzymes (such as kinases). Furthermore, comparison of the LOD and LOQ values of the LC method with those obtained with the malachite green assay, which is one of the most used indirect screening methodologies for ATP-ase activity, showed that the LC method has a similar range of application without presenting the drawbacks related to contamination by inorganic phosphate ions and glycerol, which are present in Hsp90 commercial samples.
F. Ibrahim, C. Andre, R. Aljhni, T. Gharbi, Y. C. Guillaume
Journal of Molecular Catalysis B: Enzymatic 94 (2013) 136-140
Acetylcholinesterase (AChE) is a serine protease that hydrolyzes the neurotransmitter acetylcholine. Here, the effects of hydroxyl radical (OH•) and nitric oxide (NO) on AChE activity were studied using a biochromatographic process. The enzyme was immobilized on an ethylenediamine (EDA) monolithic convective interaction media (CIM) disk. The AChE enzymatic mechanism was demonstrated from the chromatographic peak shape. A decrease in AChE activity was observed for each concentration of NO, while OH• dot radical formation led to an increase in the rate of enzymatic catalysis. Michaelis–Menten and Lineweaver–Burk plots were obtained in the presence or absence of the free radicals and their effects on Km and Vmax were evaluated. Our results indicated classical deactivation/activation kinetics without significant influence on the rate of substrate binding. The variation in transition state energies (ΔΔGES) induced by the free radicals indicated that a conformational change was occurring in the active site, while changes in the binding site were negligible. These results clearly demonstrate the direct role of OH• dot and NO on AChE activity and confirm the role they may play in Alzheimer's disease.
H. G. Schwelberger, J. Feurle, F. Ahrens
Journal of Neural Transmission 120 (2013) 983-986
Diamine oxidase (DAO) was purified to homogeneity from human seminal plasma by consecutive chromatographic fractionation on heparin-sepharose, phenyl-sepharose, CIM-QA, and Superdex 200. Human seminal plasma DAO behaves electrophoretically similar to DAO proteins from other human tissues and has very similar enzymatic properties with histamine and aliphatic diamines being the preferred substrates as well as significant conversion of polyamines. The cellular source and functional importance of DAO in human semen remain to be determined.
E. Maksimova, E. Vlakh, E. Sinitsyna, T. Tennikova
J. Sep. Sci. 2013, 36, 3741–3749
Ultrashort monolithic columns (disks) were thoroughly studied as efficient stationary phases for precipitation–dissolution chromatography of synthetic polymers. Gradient elution mode was applied in all chromatographic runs. The mixtures of different flexible chain homopolymers, such as polystyrenes, poly(methyl methacrylates), and poly(tert-butylmethacrylates) were separated according to their molecular weights on both commercial poly(styrene-co divinylbenzene).
disks (12 id × 3 mm and 5 × 5 mm) and lab-made monolithic columns (4.6 id × 50 mm) filled with supports of different hydrophobicity. The experimental conditions were optimized to reach fast and highly efficient separation. It was observed that, similar to the separation of monoliths of other classes of (macro)molecules (proteins, DNA, oligonucleotides), the length of column did not affect the peak resolution.
A comparison of the retention properties of the poly(styrene-co-divinylbenzene) diskshaped monoliths with those based on poly(lauryl methacrylate-co-ethylene dimethacrylate), poly(butyl methacrylate-co-ethylene dimethacrylate), and poly(glycidyl methacrylate-co-ethylene dimethacrylate) supports demonstrated the obvious effect of surface chemistry on the resolution factor. Additionally, the results of the discussed chromatographic mode on the fast determination of the molecular weights of homopolymers used in this study were compared to those established by SEC on columns packed with sorbent beads of a similar nature to the monoliths.
Roy N D‘Souza, Ana M Azevedo, M Raquel Aires-Barros, Nika Lendero Krajnc, Petra Kramberger, Maria Laura Carbajal, Mariano Grasselli, Roland Meyer & Marcelo Fernández-Lahore
Vol. 1, No. 5, Pharmaceutical Bioprocessing (2013)
Downstream processing is currently the major bottleneck for bioproduct generation. In contrast to the advances in fermentation processes, the tools used for downstream processes have struggled to keep pace in the last 20 years. Purification bottlenecks are quite serious, as these processes can account for up to 80% of the total production cost. Coupled with the emergence of new classes of bioproducts, for example, virus-like particles or plasmidic DNA, this has created a great need for superior alternatives. In this review, improved downstream technologies, including aqueous two-phase systems, expanded bed adsorption chromatography, convective flow systems, and fibre-based adsorbent systems, have been discussed. These adaptive methods are more suited to the burgeoning downstream processing needs of the future, enabling the cost-efficient production of new classes biomaterials with a high degree of purity, and thereby hold the promise to become indispensable tools in the pharmaceutical and food industries.
2012
J. Lee, H. T. Gan, S. M. Abdul Latiff , C. Chuah, W. Y. Lee, Y.-S. Yang, B. Loo, S. K. Ng, P. Gagnon
Journal of Chromatography A, 1270 (2012) 162-170
We introduce a chromatography method for purification of large proteins and viruses that works by capturing them at a non-reactive hydrophilic surface by their mutual steric exclusion of polyethylene glycol (PEG). No direct chemical interaction between the surface and the target species is required. We refer to the technique as steric exclusion chromatography. Hydroxyl-substituted polymethacrylate monoliths provide a hydrophilic surface and support convective mass transport that is unaffected by the viscosity of the PEG. Elution is achieved by reducing PEG concentration. Selectivity correlates with molecular size, with larger species retained more strongly than smaller species. Retention increases with PEG size and concentration. Salts weaken retention in proportion to their concentration and Hofmeister ranking. Retention is enhanced near the isoelectric point of the target species. Virus binding capacity was measured at 9.9 × 1012 plaque forming units per mL of monolith. 99.8% of host cell proteins and 93% of DNA were eliminated. Mass recovery exceeded 90%. IgM capacity was greater than 60 mg/mL. 95% of host cell proteins were eliminated from IgM produced in protein-free media, and mass recovery was up to 90%. Bioactivity was fully conserved by both viruses and antibodies. Process time ranged from less than 30 min to 2 h depending on the product concentration in the feed stream.
P. Gagnon
Journal of Chromatography A, 1221 (2012) 57-70(2012) 57-70
This article reviews technology trends in antibody purification. Section 1 discusses non-chromatography methods, including precipitation, liquid–liquid extraction, and high performance tangential flow filtration. The second addresses chromatography methods. It begins with discussion of fluidized and fixed bed formats. It continues with stationary phase architecture: diffusive particles, perfusive particles, membranes and monoliths. The remainder of the section reviews recent innovations in size exclusion, anion exchange, cation exchange, hydrophobic interaction, immobilized metal affinity, mixed-mode, and bioaffinity chromatography. Section 3 addresses an emerging trend of formulating process buffers to prevent or correct anomalies in the antibodies being purified. Methods are discussed for preventing aggregate formation, dissociating antibody-contaminant complexes, restoring native antibody from aggregates, and conserving or restoring native disulfide pairing.