2019

Exosomes fulfill a critical role as communicators among cells, with targeting and message content depending on their surface receptors and payload. This makes them obvious candidates for an extensive range of diagnostic, therapeutic applications and a need for a fast, robust and scalable purification procedure.

CIMmultusTM monolithic columns are designed to meet the special fractionation needs of very large biologics like exosomes.

We show examples of exosome purification from cell culture with CORNERSTONE Exosome Process Development Pack and analysis of exosomal vesicle populations by Image stream flow cytometry.

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This poster shows how Multi-Angle Light Scattering detector and Fluorescence detector couppled to PATfix analytical HPLC system can be used to track extracellular vesicles through purification process. Samples were analyzed by analytical size exclusion chromatography (SEC). On SEC cell culture components diffuze into pores of chromatographic media and are separated (mostly) based on size. Particles larger than the media pore size are excluded in the void peak. This peak represents extracellular vesicles including apoptosomes, microvesicles and exosomes as well as cell debris and aggregates.

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The increasing demand for messenger RNA (mRNA) as a therapeutic product requires larger production scales and more efficient extraction techniques. Fast and efficient way to purify poly-adenylated mRNA using affinity chromatography on CIMmultus™ Oligo dT column is presented.

The poly-adenylated tail of mRNA interacts with covalently bound oligo dT ligands in high-salt loading conditions, where electrostatic repulsion between negatively charged backbones of both, mRNA and oligo dT, are reduced and H-bonding in T-A base pair is emphasized. High salt concentration additionally screens out attractive electrostatic interactions between mRNA and other components in the process sample, thus facilitating aggregate reduction in purified product.

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One of the handicaps of working with bacteriophages is the long duration required to perform plaque assays. Plaque assays also impose questions about accuracy and precision relative to the scale and experience of the persons performing and interpreting them. This poster presents a pair of high precision, high accuracy chromatography-based assays that permit determination of phage concentration in less than 1 hour. Sensitivity of UV absorbance is poor because of the low concentration of phages. However, phage sensitivity is strongly amplified by monitoring the chromatogram with either fluorescence or MALS. Fluorescence works by measuring the fluorescence emission from tryptophan residues of the phage proteins. MALS works by passing a laser beam through the sample and reading the scatter produced when it encounters a particle. Larger species generate more scatter.

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Bacteriophages represent immense potential as therapeutic agents. Many of the most compelling applications of bacteriophages involve human therapy, some pertinent to gene therapy, others involving antibiotic replacement. In bacteriophage research and therapy, most applications ask for highly purified phage suspensions, as such it is crucial to reduce proteins, endotoxins, DNA and other contaminants. The most common technique for purification is ultracentrifugation using cesium chloride gradients. This technique is elaborate, cumbersome, expensive and difficult to scale-up.
Alternative techniques for purification are usually time consuming and affect phage recovery and/or viability. In this study we present efficient two-step chromatographic purification method with binding phages to a stationary phase - Convective Interaction Media (CIM®) monoliths. The aim of the study was to develop robust, fast and effective virus purification platform that can be used for several types of bacteriophages for any application. In this work bacterial lysate with bacteriophage T4 (host E.Coli) was used.

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Serotype 10 adeno-associated virus (AAVrh_10mCherry) was analysed on the PATfix™ HPLC system with the  CIMac™ AAV full/empty analytical column to estimate the ratio of empty and full AAV particles based on the peak area of the chromatogram given with three different detectors. AAV included a protein capsid containing single stranded DNA. CIMac™ AAV column consisted of a strong anion exchanger with QA chemistry (quaternary amine).

Poster was prepared by Blaz Goricar and presented at ISBioTech 9th Spring Meeting where it was awarded the first prize. Congratulations!

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2018

This poster presents fully scalable non-affinity purification strategy that has been proven to be effective for all AAV serotype tested to date. Cell lysate is directly subjected to column purification after removal of cell debris without requiring a concentration step using tangential flow filtration. The process consists of three chromatographic steps. Hydrophobic interaction chromatography on a CIMmultus OH monolith is used for initial virus capture and purification. Precipitating salts are used at 1.0–2.0 M to achieve virus binding. Most of the small molecule contaminants and proteins are eliminated in the flow-through. AAV co-elutes with a highly reduced population of contaminating proteins. DNA-protein complexes are very strongly retained and require NaOH for removal. Intermediate polishing is performed with a CIMmultus SO3 cation exchange monolith. The AAV fraction from the capture step is titrated to a pH value of 3.5—5.0 and diluted to binding conditions. Sugars and surfactants are added to suppress non-specific interactions with tubing and containers, and the product is eluted in a salt gradient. Final polishing is conducted on a CIMmultus QA anion exchange monolith which separates empty capsids from full capsids. This is achieved in a salt gradient at alkaline pH. For more information please refer to BIA Application note A048 (www.biaseparations.com/applications).

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Immunoaffinity columns using antibodies as ligands against mammalian proteins could be used for different applications in protein expression control and, if a standard available, for direct protein quantification in complex sample solutions. Additionally, these columns are ideal for polishing step of recombinant proteins, such as mammalian receptor Fc fusion proteins. Most importantly, such columns could extract a significant amount of a single membrane protein from native source, suitable for downstream analyses, such as mass spec analysis of their glycans. Immunoaffinity chromatographic monoliths against RAE-1 GPI anchored glycoprotein were developed (CIMmic HDZ - @RAE-1 column) as a part of Glycomet project with the main goal to analyze the antigen glycoprofile.

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Hydrazide-activated (HDZ) columns were proven to be a product of choice for making the most effective immunoaffinity columns. They take advantage of a special hydrazide linkage that binds antibodies through the carbohydrate residues on their Fc regions. This leaves the antigen-binding domains fully accessible to enable the most effective capture of desired target (Figure bellow).
CIMac™ HDZ monoliths make HDZ-immobilized antibody columns even more effective. Because of their large channel size and the efficiency of convective mass transport, they eliminate the long loading residence times that are required for affinity chromatography on porous particle columns. Flow rates of 5–10 column volumes per minute allow complete purifications in a few minutes, even when the source material contains a low concentration of antigen. The same performance is achieved whether a small peptide or a large bio-assemblage like a virus particle or extracellular vesicle is isolated. The combination of HDZ monoliths and the immobilization protocol offers a strong tool for fast antigen isolation from complex biological sample (plasma, lysate, etc.) and consequently sensitive antigen quantification. An example of CIMac™ HDZ application is a purification of fibrinogen from human plasma.

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Chromatography is a useful purification method for large biomolecules and virus manufacturing and it is easily scalable to large production volumes. Convective Interaction Media (CIM) monolithic columns constitute of large flow-through channels and consequently have high surface accessibility of binding sites. Preferences of CIM monolithic columns are flow independent performance, resulting in fast separation, concentration, purification, impurities removal, and analytics of biopharmaceuticals.
The aim of the study was to develop Influenza virus purification platform, which can be used for several virus strains. The main objective was to develop a process with as little as possible of intermediate steps, especially omitting Tangential Flow Filtration (TFF) or other sample pre-treatments with high host-cell DNA and protein removal, as well as to achieve high binding capacity of the Influenza virus per mL of monolithic support.

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During recombinant adeno associated virus (rAAV) downstream processing, a large amount of host-cell and product related impurities needs to be removed from the product. Succesful process on laboratory scale, such as Cesium chloride purification, lacks scalability when the process is due to be transfered to larger industrial scale. The aim of the study was to develop robust, fast and effective rAAV virus purification platform, which can be used for several AAV serotypes with various inserts. Lysed harvest and supernatant of rAAV9 were first captured and concentrated on CIMmultus™ OH column, followed by intermediate step on CIMmultus™ SO3 column and further polishing on CIMmultus™ QA column. Derived purity of industrial scale monolith purification product was compared to laboratory scale purification.

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CIM® chromatographic monoliths enable high 1) productivity of pDNA downstream process (DSP) due to high dynamic binding capacity for pDNA in small elution volumes and short chromatographic runs; 2) high resolution power due to convective-based mass transfer.

Sample displacement mode utilizes different relative binding affinities of components in a sample mixture and separates pDNA isoforms under overloading conditions - where sc pDNA isoform acts as a displacer of oc or linear pDNA isoform.

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2017

Production of high value biological therapeutics usually involves complex manufacturing processes with high process variability. Additionally, development of robust and reliable bioprocesses can be challenging. PAT aims to enhance bioprocess understanding and implies a holistic approach to ensure that quality is built into products by design. Efficient PAT therefore calls for fast and robust analytical techniques which enables to asses high quality information about critical quality attributes and key performance indicators as parallel as possible to the manufacturing process. PATfinder™ is unique HPLC system for routine gradient separations that enables every analytical task. Equipped with bio-inert ceramic pump heads is deliberately tailored to meet the demands of analytical applications covering wide range of biomolecules. Highly sensitive and fast multi-wavelength detector enables to detect component peaks even in very fast gradients.

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Preparative scale chromatographic separation of open-circular (oc) from supercoiled (sc) plasmid DNA (pDNA) isoforms has been already established on CIM® C4 with high ligand density (C4 HLD) monolithic columns with sample loading in 3.0 M ammonium sulphate (AS). The process requires high molarity of AS, increasing the overall cost of the process. Sample displacement chromatography (SDC) can be used as an alternative to decrease the AS concentration required during loading onto hydrophobic chromatographic supports. This study compares three chromatographic monoliths with different hydrophobic ligands on the surface (C4 HLD, pyridine and histamine) for the purification of different pDNA vectors in SD mode.

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New vaccines against Influenza A are required each year to keep up with the most virulent evolving strains. This highlights a need for predictive analytical tools that can aid purification process development and validation. Rapid and reliable quantification of Influenza A virus is therefore of the utmost importance for enabling good yields and controlling the costs of the downstream processing. Here we demonstrate the ability of monolithic chromatography media to produce process predictive profiles that can document ability to remove impurities and obtain high product recoveries.

CIMac™ Analytical Columns are short bed high performance monolithic columns offering all the advantages of CIM® monolithic technology. Their small volume and short column length allow the operation at high volumetric flow rates enabling to receive the information about the product quantity and purity in just a few minutes. Hence, the CIMac™ Analytical Columns can be effectively used for the in-process and final control of various samples from different purification process steps.

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2016

Adeno-associated virus (AAV) vectors of various serotypes are considered to have high potential for gene therapy applications. Currently, manufacturing of AAV vectors faces the challenge of co-production of incompletely formed particles lacking a recombinant viral genome. Empty capsids increase the dose of total AAV administered for efficient transduction and are thought to cause unwanted immunological reactions against the virus.Removal of empty capsids during manufacturing, as well as analysis of empty/full AAV particle content is therefore a critical requirement for any AAV production process. This poster demonstrates how CIMmultus™ QA monolithic columns can be used to remove empty AAV capsids from the product chromatographically in a single step.

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Productivity of the downstream bioprocessing depends among others on the efficiency of chromatographic step. One of the crucial chromatographic parameters is dynamic binding capacity (DBC) for certain biomolecule. DBC could be tailored with changing the surface area of convective pores by tailoring the surface of pre-polymerized monoliths using graft or block polymerization of polymer brushes. Grafted CIM monoliths have already been prepared via Radical Polymerization (RP) and successfully characterized (1).

Recently, the implementation and optimization of Controlled Radical Polymerization (CRP) for grafting of large pore monoliths (average diameter 6 μm ) resulted in polymethacrylate-based ionic exchanger with at least 5 times higher DBC compared to non-grafted 6 μm monoliths, while preserving high permeability. The main goal of our study was to chromatographically characterize novel grafted ion-exchanging monoliths (CIM gDEAE and CIM gSO3) to see whether novel columns still retain flow independent chromatographic properties of non-grafted monoliths.

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The upstream and downstream monoclonal antibody (mAb) bioprocessing makes them susceptible to physical and chemical modifications. In the biotechnological production process of mAbs, structural variations may arise due to some enzymatic activity. Antibody charge variants have gained considerable attention in the biotechnology industry due to their potential influence on stability and biological activity and cation-exchange chromatography (CEX) is one of the typical approaches for mAb charge variant analyses. We tested several CEX columns under different conditions and the best column for isotype separation was weak cation-exchanging CIMac COOH chromatographic monolith in pH gradient. We have proven a flow independent separation of mAb charge variants and in this way, a resolution comparable to classical CEX particulate-based analytical columns was achieved in only 6 min analysis time.

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To ensure the desired chromatographic characteristics of the CIM® monolithic column at large scales, monolith microstructure morphology, pore size distribution, porosity and surface ligand density should be uniform. To demonstrate the uniformity of large chromatographic monoliths we have developed new testing procedures. By fabricating smaller columns (disks) from different random  positions of larger monolith, non-cGMP compliant chromatographic testing can be applied on the same polymerization batch without affecting the cGMP compliance of large-scale chromatographic monolith. Each individual disk was thoroughly tested and the results were compared to the properties of the large monolith.

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Since plasmid DNA (pDNA) as a pharmaceutical product has stringent requirements of purity and efficacy, one or more chromatographic steps are often used in the downstream processing train. High ligand density butyl-modified (C4 HLD) monolithic support is currently used in a polishing step of a pDNA purification process (1) and is mainly focused to supercoiled (sc) pDNA isoform separation from the open circular (oc) and linear pDNA isoform as well as for removal of remaining gDNA and RNA. The goal of the study was to compare the productivities of two variations of the polishing chromatographic process employing monoliths – classical bind-elute (BE) versus recently described (2) sample displacement purification (SDP). Classical purification requires high concentration of ammonium sulphate (AS) during loading step and elution is then achieved by descending AS gradient. SDP utilises different relative binding affinities of components in a sample mixture and separates pDNA isoforms under overloading conditions, where sc pDNA isoform acts as a displacer of oc or linear pDNA isoform.

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