High‐throughput mAb expression and purification platform based on transient CHO

A high‐cell‐density transient transfection system was recently developed in our laboratory based on a CHO‐GS‐KO cell line. This method yields monoclonal antibody titers up to 350 mg/L from a simple 7‐day process, in volumes ranging from 2 mL to 2 L. By performing transfections in 24‐deep‐well plates, a large number of mAbs can be expressed simultaneously. We coupled this new high‐throughput transfection process to a semiautomated protein A purification process. Using a Biomek FX^p liquid handling robot, up to 72 unique mAbs can be simultaneously purified. Our primary goal was to obtain >0.25 mg of purified mAb at a concentration of >0.5 mg/mL, without any concentration or buffer‐exchange steps. We optimized both the batch‐binding and the batch elution steps. The length of the batch‐binding step was important to minimize mAb losses in the flowthrough fraction. The elution step proved to be challenging to simultaneously maximize protein recovery and protein concentration. We designed a variable volume elution strategy based on the average supernatant titer. Finally, we present two case studies. In the first study, we produced 56 affinity maturation mAb variants at an average yield of 0.33 ± 0.05 mg (average concentration of 0.65 ± 0.10 mg/mL). In a second study, we produced 42 unique mAbs, from an early‐stage discovery effort, at an average yield of 0.79 ± 0.31 mg (average concentration of 1.59 ± 0.63 mg/mL). The combination of parallel high‐yielding transient transfection and semiautomated high‐throughput protein A purification represents a valuable mAb drug discovery tool. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:239–247, 2015     

Selective high throughput protein quantification based on UV absorption spectra

The application of high throughput experimentation (HTE) in protein purification process development has created an analytical bottleneck. Recently, a new label‐free and non‐invasive methodology for analyzing multicomponent protein mixtures by means of spectral measurements was presented. Analytics based on the methodology was shown to increase analytical throughput for selective protein quantification significantly, however this was only demonstrated for one particular protein combination. In this work, the possibilities and limitations of the analytical method are investigated further. Principal component analysis (PCA) was performed on a broad range of absorption spectra to investigate their common characteristics and differences. The PCA was used both for cluster analysis and to define a measure for spectral similarity. For binary protein combinations, the calibration precision was shown to decrease exponentially with the defined spectral similarity factor. Knowledge of this correlation can be used to determine a priori whether a calibration will be successful or not. Calibration robustness was investigated by applying the analytics to liquid chromatography performed in HTE mode. Further it was shown, that a spectral difference of 0.6% was sufficient to sucessfully preform a spectral based calibration of two IgG1 monoclonals. Biotechnol. Bioeng. 2013; 110: 448–460. © 2012 Wiley Periodicals, Inc.     

A heme fusion tag for protein affinity purification and quantification

We report a novel affinity‐based purification method for proteins expressed in Escherichia coli that uses the coordination of a heme tag to an L ‐histidine‐immobilized sepharose (HIS) resin. This approach provides an affinity purification tag visible to the eye, facilitating tracking of the protein. We show that azurin and maltose binding protein are readily purified from cell lysate using the heme tag and HIS resin. Mild conditions are used; heme‐tagged proteins are bound to the HIS resin in phosphate buffer, pH 7.0, and eluted by adding 200–500 mM imidazole or binding buffer at pH 5 or 8. The HIS resin exhibits a low level of nonspecific binding of untagged cellular proteins for the systems studied here. An additional advantage of the heme tag‐HIS method for purification is that the heme tag can be used for protein quantification by using the pyridine hemochrome absorbance method for heme concentration determination.     

High‐throughput screening techniques for rapid PEG‐based precipitation of IgG4 mAb from clarified cell culture supernatant

Locating optimal protein precipitation conditions for complex biological feed materials is problematic. This article describes the application of a series of high‐throughput platforms for the rapid identification and selection of conditions for the precipitation of an IgG₄ monoclonal antibody (mAb) from a complex feedstock using only microliter quantities of material. The approach uses 96‐microwell filter plates combined with high‐throughput analytical methods and a method for well volume determination for product quantification. The low material, time and resource requirements facilitated the use of a full factorial Design of Experiments (DoE) for the rapid investigation into how critical parameters impact the IgG₄ precipitation. To aid the DoE, a set of preliminary range‐finding studies were conducted first. Data collected through this approach describing Polyethylene Glycol (PEG) precipitation of the IgG₄ as a function of mAb concentration, precipitant concentration, and pH are presented. Response surface diagrams were used to explore interactions between parameters and to inform selection of the most favorable conditions for maximum yield and purification. PEG concentrations required for maximum yield and purity were dependant on the IgG₄ concentration; however, concentrations of 14 to 20% w/v, pH 6.5, gave optimal levels of yield and purity. Application of the high‐throughput approach enabled 1,155 conditions to be examined with less than 1 g of material. The level of insights gained over such a short time frame is indicative of the power of microwell experimentation in allowing the rapid identification of appropriate processing conditions for key bioprocess operations. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Characterization and design of chemically selective cationic displacers using a robotic high‐throughput screen

A robotic high‐throughput displacer screen was developed and employed to identify chemically selective displacers for several protein pairs in cation exchange chromatography. This automated screen enabled the evaluation of a wide range of experimental conditions in a relatively short period of time. Displacers were evaluated at multiple concentrations for these protein pairs, and DC‐50 plots were constructed. Selectivity pathway plots were also constructed and different regimes were established for selective and exclusive separations. Importantly, selective displacement was found to be conserved for multiple protein pairs, demonstrating the technique to be applicable for a range of protein systems. Although chemically selective displacers were able to separate protein pairs that had similar retention in ion exchange but different surface hydrophobicities, they were not able to distinguish protein pairs with similar surface hydrophobicities. This corroborates that displacer‐protein hydrophobic interactions play an important role for this class of selective displacers. Important functional group moieties were established and efficient displacers were identified. These results demonstrate that the design of chemically selective displacers requires a delicate balance between the abilities to displace proteins from the resin and to bind to a selected protein. The use of robotic screening of displacers will enable the extension of chemically selective displacement chromatography beyond hydrophobic displacer‐protein interactions to other secondary interactions and more selective displacement systems. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

High‐throughput cell quantification assays for use in cell purification development – enabling technologies for cell production

High‐throughput screening (HTS) technology is gaining increasing importance in downstream process development of cell‐based products. The development of such HTS‐technologies, however, is highly dependent on the availability of robust, accurate, and sensitive high‐throughput cell quantification methods. In this article, we compare state‐of‐the‐art cell quantification methods with focus on their applicability in HTS‐platforms for downstream processing of cell‐based products. Sensitivity, dynamic range, and precision were evaluated for four methods that differ in their respective mechanism. In addition, we evaluated the performance of these methods over a range of buffer compositions, medium densities, and viscosities, representing conditions found in many downstream processing methods. We found that CellTiter‐Glo? and flow cytometry are excellent tools for high‐throughput cell quantification. Both methods have broad working ranges (3–4 log) and performed well over a wide range of buffer compositions. In comparison, CyQuant® Direct and CellTracker? had smaller working ranges and were more sensitive to changes in buffer composition. For fast and sensitive quantification of a single cell type, CellTiter‐Glo? performed best, while for more complex cell mixtures flow cytometry is the method of choice. Our analysis will facilitate the selection of the most suitable method for a specific application and provides a benchmark for future HTS development in downstream processing of cell‐based products.     

High‐throughput process development of purification alternatives for the protein avidin

With an increased number of applications in the field of the avidin‐biotin technology, the resulting demand for highly‐purified protein avidin has drawn our attention to the purification process of avidin that naturally occurs in chicken egg white. The high‐throughput process development (HTPD) methodology was exploited, in order to evaluate purification process alternatives to commonly used ion‐exchange chromatography. In a high‐throughput format, process parameters for aqueous two‐phase extraction, selective precipitation with salts and polyethylene glycol, and hydrophobic interaction and mixed‐mode column chromatography experiments were performed. The HTPD strategy was complemented by a high‐throughput tandem high‐performance liquid chromatography assay for protein quantification. Suitable conditions for the separation of avidin from the major impurities ovalbumin, ovomucoid, ovotransferrin, and lysozyme were identified in the screening experiments. By combination of polyethylene glycol precipitation with subsequent resolubilization and separation in a polyethylene glycol/sulfate/sodium chloride two‐phase system an avidin purity of 77% was obtained with a yield >90% while at the same time achieving a significant reduction of the process volume. The two‐phase extraction and precipitation results were largely confirmed in larger scale with scale‐up factors of 230 and 133, respectively. Seamless processing of the avidin enriched bottom phase was found feasible by using mixed‐mode chromatography. By gradient elution a final avidin purity of at least 97% and yield >90% was obtained in the elution pool. The presented identification of a new and beneficial alternative for the purification of the high value protein thus represents a successful implementation of HTPD for an industrially relevant purification task. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:957–973, 2015     

High‐throughput generation of tagged stable cell lines for proteomic analysis

We present an optimized system for rapid generation of localization and affinity purification‐tagged mammalian stable cell lines that facilitates complex purification and interacting protein identification. The improved components of this method, including the flexibility of inducible expression, circumvent issues associated with toxicity, clonal selection, sample yields and time to data acquisition. We have applied this method to the study of cell‐cycle regulators and novel microtubule‐associated proteins.     

A practical strategy for using miniature chromatography columns in a standardized high‐throughput workflow for purification development of monoclonal antibodies

The emergence of monoclonal antibody (mAb) therapies has created a need for faster and more efficient bioprocess development strategies in order to meet timeline and material demands. In this work, a high‐throughput process development (HTPD) strategy implementing several high‐throughput chromatography purification techniques is described. Namely, batch incubations are used to scout feasible operating conditions, miniature columns are then used to determine separation of impurities, and, finally, a limited number of lab scale columns are tested to confirm the conditions identified using high‐throughput techniques and to provide a path toward large scale processing. This multistep approach builds upon previous HTPD work by combining, in a unique sequential fashion, the flexibility and throughput of batch incubations with the increased separation characteristics for the packed bed format of miniature columns. Additionally, in order to assess the applicability of using miniature columns in this workflow, transport considerations were compared with traditional lab scale columns, and performances were mapped for the two techniques. The high‐throughput strategy was utilized to determine optimal operating conditions with two different types of resins for a difficult separation of a mAb monomer from aggregates. Other more detailed prediction models are cited, but the intent of this work was to use high‐throughput strategies as a general guide for scaling and assessing operating space rather than as a precise model to exactly predict performance. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:626–635, 2014     

High‐throughput protein refolding screening method using zeolite

We established a 96‐well‐plate‐based refolding screening system using zeolite. In this system, protein denatured and solubilized with 6 M guanidine hydrochloride is adsorbed onto zeolite placed in a 96‐well plate. The refolding conditions can be tested by incubating the samples with refolding buffers under various conditions of pH, salts, and additives. In this study, we chose green fluorescent protein as the model protein. Green fluorescent protein was expressed as inclusion bodies, and we tested the effects of four pH conditions and six additives on its refolding. The results demonstrate that green fluorescent protein was more efficiently refolded with zeolite than with the conventional dilution method. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Miniaturized fluid array for high‐throughput protein expression

We describe a miniaturized fluid array device for high‐throughput cell‐free protein synthesis (CFPS), aiming to match the throughput and scale of gene discovery. Current practice of using E. coli cells for production of recombinant proteins is difficult and cost‐prohibitive to implement in a high‐throughput format. As more and more new genes are being identified, there is a considerable need to have high‐throughput methods to produce a large number of proteins for studying structures and functions of the corresponding genes. The device consists of 96 units and each unit is for expression of one protein; thus up to 96 proteins can be produced simultaneously. The function of the fluid array was demonstrated by expression of a variety of proteins, with more than two orders of magnitude reduction in reagent consumption compared with a commercially available CFPS instrument. The protein expression yield in the device was up to 87 times higher for β‐glucoronidase than that in a conventional microplate. The concentration of β‐galactosidase expressed in the device was determined at 5.5 μg/μL. The feasibility of using the device for drug screening was demonstrated by measuring the inhibitory effects of mock drug compounds on synthesized β‐lactamase without the need for harvesting proteins, which enabled us to reduce the analysis time from days to hours. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

A constitutive expression system for high‐throughput screening

To reduce the amount of consumables and number of pipetting steps in high‐throughput screening, a constitutive expression system was developed that comprises four different promoters of varying strength. The system was validated by the expression of different sucrose phosphorylase enzymes from Leuconostoc mesenteroides, Lactobacillus acidophilus and Bifidobacterium adolescentis in 96‐deep‐ and low‐well plates at three temperatures. Drastically improved soluble expression in mini‐cultures was observed for the enzymes from L. mesenteroides strains by reducing the promoter strength from strong to intermediate and by expressing the proteins at lower temperatures. In contrast, the enzymes from B. adolescentis and L. acidophilus were expressed most efficiently with a strong promoter. The constitutive expression of sucrose phosphorylases in low‐well plates resulted in a level of activity that is equal or even better than what was achieved by inducible expression. Therefore, our plasmid set with varying constitutive promoters will be an indispensable tool to optimize enzyme expression for high‐throughput screening.     

High‐throughput ion exchange purification of positively charged recombinant protein in the presence of negatively charged dextran sulfate

Product quality analyses are critical for developing cell line and bioprocess producing therapeutic proteins with desired critical product quality attributes. To facilitate these analyses, a high‐throughput small‐scale protein purification (SSP) is required to quickly purify many samples in parallel. Here we develop an SSP using ion exchange resins to purify a positively charged recombinant growth factor P1 in the presence of negatively charged dextran sulfate supplemented to improve the cell culture performance. The major challenge in this work is that the strong ionic interaction between P1 and dextran sulfate disrupts interaction between P1 and chromatography resins. To solve this problem, we develop a two‐step SSP using Q Sepharose Fast Flow (QFF) and SP Sepharose XL (SPXL) resins to purify P1. The overall yield of this two‐step SSP is 78%. Moreover, the SSP does not affect the critical product quality attributes. The SSP was critical for developing the cell line and process producing P1. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:516–520, 2014     

High‐throughput cloning and expression library creation for functional proteomics

The study of protein function usually requires the use of a cloned version of the gene for protein expression and functional assays. This strategy is particularly important when the information available regarding function is limited. The functional characterization of the thousands of newly identified proteins revealed by genomics requires faster methods than traditional single‐gene experiments, creating the need for fast, flexible, and reliable cloning systems. These collections of ORF clones can be coupled with high‐throughput proteomics platforms, such as protein microarrays and cell‐based assays, to answer biological questions. In this tutorial, we provide the background for DNA cloning, discuss the major high‐throughput cloning systems (Gateway® Technology, Flexi® Vector Systems, and Creator^TM DNA Cloning System) and compare them side‐by‐side. We also report an example of high‐throughput cloning study and its application in functional proteomics. This tutorial is part of the International Proteomics Tutorial Programme (IPTP12).     

Fluorescent probe for high‐throughput screening of membrane protein expression

Screening of protein variants requires specific detection methods to assay protein levels and stability in crude mixtures. Many strategies apply fluorescence‐detection size‐exclusion chromatography (FSEC) using green fluorescent protein (GFP) fusion proteins to qualitatively monitor expression, stability, and monodispersity. However, GFP fusion proteins have several important disadvantages; including false‐positives, protein aggregation after proteolytic removal of GFP, and reductions in protein yields without the GFP fusion. Here we describe a FSEC screening strategy based on a fluorescent multivalent NTA probe that interacts with polyhistidine‐tags on target proteins. This method overcomes the limitations of GFP fusion proteins, and can be used to rank protein production based on qualitative and quantitative parameters. Domain boundaries of the human G‐protein coupled adenosine A2a receptor were readily identified from crude detergent‐extracts of a library of construct variants transiently produced in suspension‐adapted HEK293‐6E cells. Well expressing clones of MraY, an important bacterial infection target, could be identified from a library of 24 orthologs. This probe provides a highly sensitive tool to detect target proteins to expression levels down to 0.02 mg/L in crude lysate, and requires minimal amounts of cell culture.