The dataset for protein–RNA binding affinity

We have developed a non‐redundant protein–RNA binding benchmark dataset derived from the available protein–RNA structures in the Protein Database Bank. It consists of 73 complexes with measured binding affinity. The experimental conditions (pH and temperature) for binding affinity measurements are also listed in our dataset. This binding affinity dataset can be used to compare and develop protein–RNA scoring functions. The predicted binding free energy of the 73 complexes from three available scoring functions for protein–RNA docking has a low correlation with the binding Gibbs free energy calculated from K_d. © 2013 The Protein Society     

Protein Design and Evolution for Biocatalysis

Cover illustration: Soon designing proteins on demand? This is the vision expressed by the designer pencils pointing at the logo of the meeting held in September 2006 in Greifswald, Germany. This special issue was edited by Prof. Uwe Bornscheuer from Greifswald, who selected papers from keynote speakers at this meeting. With special thanks to Prof. Romas Kazlauskas, University of Minnesota, for the design of the conference logo. Pencils © FOTOLIA.     

The effect of protein a cycle number on the performance and lifetime of an anion exchange polishing step

Most mAb platform purification processes consist of an affinity capture step followed by one or two polishing steps. An understanding of the performance linkages between the unit operations can lead to robust manufacturing processes. In this study, a weak‐partitioning anion‐exchange chromatography polishing step used in a mAb purification process was characterized through high‐throughput screening (HTS) experiments, small‐scale experiments including a cycling study performed on qualified scale‐down models, and large‐scale manufacturing runs. When material from a Protein A column that had been cycled <10× was loaded on the AEX resin, early breakthrough of impurities and premature loss of capacity was observed. As the cycle number on the Protein A resin increased, the capacity of the subsequent AEX step increased. Different control strategies were considered for preventing impurity breakthrough and improving AEX resin lifetimes. Depth filtration of the Protein A peak pool significantly improved the AEX resin capacity, robustness, and lifetime. Further, the turbidity of the Protein A pool has the potential for use as an in‐process control parameter for monitoring the performance of the AEX step. Biotechnol. Bioeng. 2013; 110: 1142–1152. © 2012 Wiley Periodicals, Inc.     

Maximizing binding capacity for protein A chromatography

Advances in cell culture expression levels in the last two decades have resulted in monoclonal antibody titers of ≥10 g/L to be purified downstream. A high capacity capture step is crucial to prevent purification from being the bottleneck in the manufacturing process. Despite its high cost and other disadvantages, Protein A chromatography still remains the optimal choice for antibody capture due to the excellent selectivity provided by this step. A dual flow loading strategy was used in conjunction with a new generation high capacity Protein A resin to maximize binding capacity without significantly increasing processing time. Optimum conditions were established using a simple empirical Design of Experiment (DOE) based model and verified with a wide panel of antibodies. Dynamic binding capacities of >65 g/L could be achieved under these new conditions, significantly higher by more than one and half times the values that have been typically achieved with Protein A in the past. Furthermore, comparable process performance and product quality was demonstrated for the Protein A step at the increased loading. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1335–1340, 2014     

Progress of 1D protein structure prediction at last

Accuracy of predicting protein secondary structure and solvent accessibility from sequence information has been improved significantly by using information contained in multiple sequence alignments as input to a neural 'network system. For the Asilomar meeting, predictions for 13 proteins were generated automatically using the publicly available prediction method PHD. The results confirm the estimate of 72% three-state prediction accuracy. The fairly accurate predictions of secondary structure segments made the tool useful as a starting point for modeling of higher dimensional aspects of protein structure. © 1995 Wiley-Liss, Inc.     

Evaluation of a novel methacrylate‐based protein a resin for the purification of immunoglobulins and Fc‐fusion proteins

Protein A affinity chromatography is a central part of most commercial monoclonal antibody and Fc‐fusion protein purification processes. In the last couple years an increasing number of new Protein A technologies have emerged. One of these new Protein A technologies consists of a novel, alkaline‐tolerant, Protein A ligand coupled to a macroporous polymethacrylate base matrix that has been optimized for immunoglobulin (Ig) G capture. The resin is interesting from a technology perspective because the particle size and pore distribution of the base beads are reported to have been optimized for high IgG binding and fast mass transfer, while the Protein A ligand has been engineered for enhanced alkaline tolerance. This resin was subjected to a number of technical studies including evaluating dynamic and static binding capacities, alkaline stability, Protein A leachate propensity, impurity clearance, and pressure–flow behavior. The results demonstrated similar static binding capacities as those achieved with industry standard agarose Protein A resins, but marginally lower dynamic binding capacities. Removal of impurities from the process stream, particularly host cell proteins, was molecule dependent, but in most instances matched the performance of the agarose resins. This resin was stable in 0.1 M NaOH for at least 100 h with little loss in binding capacity, with Protein A ligand leakage levels comparable to values for the agarose resins. Pressure–flow experiments in lab‐scale chromatography columns demonstrated minimal resin compression at typical manufacturing flow rates. Prediction of resin compression in manufacturing scale columns did not suggest any pressure limitations upon scale up. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1125–1136, 2014     

Binding site on human immunoglobulin G for the affinity ligand HWRGWV

Affinity ligand HWRGWV has demonstrated the ability to isolate human immunoglobulin G (hIgG) from mammalian cell culture media. The ligand specifically binds hIgG through its Fc portion. This work shows that deglycosylation of hIgG has no influence on its binding to the HWRGWV ligand and the ligand does not compete with Protein A or Protein G in binding hIgG. It is suggested by the mass spectrometry (MS) data and docking simulation that HWRGWV binds to the pFc portion of hIgG and interacts with the amino acids in the loop Ser383–Asn389 (SNGQPEN) located in the C_H3 domain. Subsequent modeling has suggested a possible three‐dimensional minimized solution structure for the interaction of hIgG and the HWRGWV ligand. The results support the fact that a peptide as small as a hexamer can have specific interactions with large proteins such as hIgG. Copyright © 2009 John Wiley & Sons, Ltd.     

Cover Picture: Protein folding in vivo

Cover illustration: Protein folding in vivo. This special issue, edited by Marc Blondel (Brest, France) and Mónica Marín (Montevideo, Uruguay) includes review and original articles on co-translational folding, alternative codon usage and the impacts of protein folding on protein production. The drawing on the cover illustrates the ribosome as a platform for co-translational folding of newly synthesized proteins. © HRATCH ARBACH 2011     

Vivaldi: Visualization and validation of biomacromolecular NMR structures from the PDB

We describe Vivaldi (VIsualization and VALidation DIsplay; http://pdbe.org/vivaldi ), a web‐based service for the analysis, visualization, and validation of NMR structures in the Protein Data Bank (PDB). Vivaldi provides access to model coordinates and several types of experimental NMR data using interactive visualization tools, augmented with structural annotations and model‐validation information. The service presents information about the modeled NMR ensemble, validation of experimental chemical shifts, residual dipolar couplings, distance and dihedral angle constraints, as well as validation scores based on empirical knowledge and databases. Vivaldi was designed for both expert NMR spectroscopists and casual non‐expert users who wish to obtain a better grasp of the information content and quality of NMR structures in the public archive. © Proteins 2013. © 2012 Wiley Periodicals, Inc.     

Antibody purification from CHO cell supernatant using new multimodal membranes

This contribution describes strategies to purify monoclonal antibodies from Chinese hamster ovary (CHO) cell culture supernatant using newly designed multimodal membranes (MMMs). The MMMs were used for the capture step purification of human IgG₁ following a size‐exclusion desalting column to remove chaotropic salts that interfere with IgG binding. The MMM column attained higher dynamic binding capacity than a Protein A resin column at an equivalent residence time of 1 min. The two‐step MMM chromatography process achieved high selectivity for capturing hIgG₁ from the CHO cell culture supernatant, though the desalting step resulted in product dilution. Product purity and host cell protein (HCP) level in the elution pool were analyzed and compared to results from a commercial Protein A column. The product purity was >98% and HCP levels were <20 ppm for both purification methods. In addition, hIgG₁ could be eluted from the MMM chromatography column at neutral pH, which is important for limiting the formation of aggregates; although slow elution dilutes the product. Overall, this paper shows that MMMs are highly effective for capture step purification of proteins and should be considered when Protein A cannot be used, e.g., for pH sensitive mAbs or proteins lacking an Fc binding domain. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:658–665, 2017     

News and views from the 8th annual meeting of the Italian Society of Virology

The 8th annual meeting of the Italian Society of Virology (SIV) took place in Orvieto, Italy from the 21st to the 23rd of September 2008. The meeting covered different areas of Virology and the scientific sessions focused on: general virology and viral genetics; viral oncology, virus–host interaction and pathogenesis; emerging viruses and zoonotic, foodborne and environmental pathways of transmission; viral immunology and vaccines; viral biotechnologies and gene therapy; medical virology and antiviral therapy. The meeting had an attendance of about 160 virologists from all Italy. In this edition, a satellite workshop on “Viral biotechnologies” was organized in order to promote the role of virologists in the biotechnological research and teaching fields. A summary of the plenary lectures and oral selected presentations is reported. J. Cell. Physiol. 219: 797–799, 2009. © 2009 Wiley‐Liss, Inc.     

The new and improved PhyloCode, now with types, ranks, and even polyphyly: a conference report from the First International Phylogenetic Nomenclature Meeting

A report from the first International Phylogenetic Nomenclature Meeting is presented. The meeting revealed that the PhyloCode, once implemented, will itself not require adherence to the three major tenets of philosophy that proponents have claimed required its creation. These include the abandonment of (1) non‐monophyletic taxa, (2) ranks, and (3) types. © The Willi Hennig Society 2005.     

Cell and Protein Manipulation

Cover illustration Cell and Protein Manipulation. This second BTJ special issue on “Methods and Advances” features articles on cell manipulation (e.g. lysis methods for miniaturized high-throughput assays) or protein processing (e.g. plasma-free manufacturing of therapeutics or an inkjet printing method for manufacturing immuoassays). Image liquid nitrogen tank to store cells or proteins, © Baxter.     

Quality by design approach for viral clearance by protein a chromatography

Protein A chromatography is widely used as a capture step in monoclonal antibody (mAb) purification processes. Antibodies and Fc fusion proteins can be efficiently purified from the majority of other complex components in harvested cell culture fluid (HCCF). Protein A chromatography is also capable of removing modest levels of viruses and is often validated for viral clearance. Historical data mining of Genentech and FDA/CDER databases systematically evaluated the removal of model viruses by Protein A chromatography. First, we found that for each model virus, removal by Protein A chromatography varies significantly across mAbs, while remains consistent within a specific mAb product, even across the acceptable ranges of the process parameters. In addition, our analysis revealed a correlation between retrovirus and parvovirus removal, with retrovirus data generally possessing a greater clearance factor. Finally, we describe a multivariate approach used to evaluate process parameter impacts on viral clearance, based on the levels of retrovirus‐like particles (RVLP) present among process characterization study samples. It was shown that RVLP removal by Protein A is robust, that is, parameter effects were not observed across the ranges tested. Robustness of RVLP removal by Protein A also correlates with that for other model viruses such as X‐MuLV, MMV, and SV40. The data supports that evaluating RVLP removal using process characterization study samples can establish multivariate acceptable ranges for virus removal by the protein A step for QbD. By measuring RVLP instead of a model retrovirus, it may alleviate some of the technical and economic challenges associated with performing large, design‐of‐experiment (DoE)—type virus spiking studies. This approach could also serve to provide useful insight when designing strategies to ensure viral safety in the manufacturing of a biopharmaceutical product. Biotechnol. Bioeng. 2014;111: 95–103. © 2013 The Authors. Biotechnology and Bioengineering Published by Wiley Periodicals, Inc.     

The PhyloCode, types, ranks and monophyly: a response to Pickett

A report from the First International Phylogenetic Nomenclature Meeting recently published in Cladistics conveys several misconceptions about the PhyloCode and presents an erroneous interpretation of discussions that took place at that meeting. Contrary to Pickett's assertions, the PhyloCode is designed to name clades, not paraphyletic groups; the rejection of ranks has never been a fundamental principle of phylogenetic nomenclature; and specifiers under the PhyloCode differ in several ways from types under rank‐based nomenclature. © The Willi Hennig Society 2005.     

ATP-dependent protein kinases in bacteria

Protein phosphorylation has been shown to occur in over fifty different bacterial species and, therefore, seems to be a universal device among prokaryotes. Most of the protein kinases responsible for this modification of proteins share the common property of using adenosine triphosphate as phosphoryl donnor. However, they differ from one another in a number of structural and functional aspects. Namely, they exhibit a varying acceptor amino acid specificity and can be classified, on this basis, in three main groups: protein-histidine kinases, protein-serine/threonine kinases and protein-tyrosine kinases. © 1993 Wiley-Liss, Inc.     

ZnO nanoparticles assist the refolding of denatured green fluorescent protein

Proteins are essential for cellular and biological processes. Proteins are synthesized and fold into the native structure to become active. The inability of a protein molecule to remain in its native conformation is called as protein misfolding, and this is due to several environmental factors. Protein misfolding and aggregation handle several human diseases. Protein misfolding is believed to be one of the causes of several disorders such as cancer, degenerative diseases, and metabolic pathologies. The zinc oxide (ZnO) nanoparticle was significantly promoted refolding of thermally denatured green fluorescent protein (GFP). In the present study, ZnO nanoparticles interaction with GFP was investigated by ultraviolet ‐ visible spectrophotometer, fluorescence spectrophotometer, and dynamic light scattering. Results suggest that the ZnO nanoparticles significantly assist the refolding of denatured GFP. Copyright © 2015 John Wiley & Sons, Ltd.     

Oligoethylene glycols prevent thermal aggregation of α‐chymotrypsin in a temperature‐dependent manner: Implications for design guidelines

Protein aggregation is problematic in various fields, where aggregation can frequently occur during routine experiments. This study showed that tetraethylene glycol (TEG) and tetraethylene glycol dimethyl ether (TEGDE) act as aggregation suppressors that have different unique properties from typical additives to prevent protein aggregation, such as arginine (Arg) and NaCl. Thermal aggregation of α‐chymotrypsin was well suppressed with the addition of both TEG and TEGDE. Interestingly, the suppressive effects of Arg and NaCl on thermal aggregation were almost unchanged when temperature was shifted from 65°C to 85°C, whereas both TEG and TEGDE significantly decreased the aggregation rate with increasing temperature. Note that the effects of TEG and TEGDE were higher than Arg above 75°C. This temperature‐dependent behavior of TEG and TEGDE provides a novel design guideline to develop aggregation suppressors for use at high temperature, i.e., the importance of the ethylene oxide group. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1325–1330, 2013