High-capacity multimodal anion-exchange membranes for polishing of therapeutic proteins

This contribution reports on a study using Purexa™-MQ multimodal anion-exchange (AEX) membranes for protein polishing at elevated solution conductivities. Dynamic binding capacities (DBC₁₀) of bovine serum albumin (BSA), human immunoglobulins, and salmon sperm DNA (ss-DNA) are reported for various salt types, salt concentrations, flowrates, and pH. Using 1 mg/ml BSA, DBC₁₀ values for Purexa™-MQ were >90 mg/ml at conductivities up to 15 mS/cm. The membranes maintained a high, salt-tolerant BSA DBC₁₀ of 89.8 ± 2.7 (SD) over the course of 100 bind-elute cycles. Polishing studies with acidic and basic monoclonal antibodies at >2 kg/L loads showed that Purexa™-MQ had higher clearance of host cell proteins and aggregate species at high conductivity (13 mS/cm) and in the presence of phosphate than other commercial AEX media. Purexa™-MQ also had a high ss-DNA DBC₁₀ of 50 mg/ml at conductivities up to 15 mS/cm, markedly outperforming other commercial products. In addition to the effectiveness of Purexa™-MQ for protein polishing at elevated solution conductivities, its unusually high binding capacity for ss-DNA indicates potential applications for plasmid DNA purification.     

Production of lentiviral vectors by large-scale transient transfection of suspension cultures and affinity chromatography purification

The use of lentiviral vectors as gene delivery vehicles has become increasingly popular in recent years. The growing interest in these vectors has created a strong demand for large volumes of vector stocks, which entails the need for scaleable vector manufacturing procedures. In this work, we present a simple and robust process for the production of lentiviral vectors using scaleable production and purification methodologies. Lentivirus particles were produced by transient transfection of serum-free suspension-growing 293 EBNA-1 cells with four plasmids encoding the vector components using linear polyethylenimine (PEI) as transfection reagent. This process was successfully scaled-up from shake flasks to a 3-L bioreactor from which 10(10) IVP were recovered. In addition, an affinity chromatography protocol designed for purification of bioactive oncoretroviral vectors has been adapted in this work for the purification of VSV-G pseudotyped lentiviral vectors. Using heparin affinity chromatography, lentiviral particles were concentrated and purified directly from the clarified supernatants. During this step, a recovery of 53% of infective lentiviral particles was achieved while removing 94% of the impurities contained in the supernatant.     

The role of polymer nanolayer architecture on the separation performance of anion-exchange membrane adsorbers: I. Protein separations

This contribution describes the preparation of strong anion-exchange membranes with higher protein binding capacities than the best commercial resins. Quaternary amine (Q-type) anion-exchange membranes were prepared by grafting polyelectrolyte nanolayers from the surfaces of macroporous membrane supports. A focus of this study was to better understand the role of polymer nanolayer architecture on protein binding. Membranes were prepared with different polymer chain graft densities using a newly developed surface-initiated polymerization protocol designed to provide uniform and variable chain spacing. Bovine serum albumin and immunoglobulin G were used to measure binding capacities of proteins with different size. Dynamic binding capacities of IgG were measured to evaluate the impact of polymer chain density on the accessibility of large size protein to binding sites within the polyelectrolyte nanolayer under flow conditions. The dynamic binding capacity of IgG increased nearly linearly with increasing polymer chain density, which suggests that the spacing between polymer chains is sufficient for IgG to access binding sites all along the grafted polymer chains. Furthermore, the high dynamic binding capacity of IgG (>130 mg/mL) was independent of linear flow velocity, which suggests that the mass transfer of IgG molecules to the binding sites occurs primarily via convection. Overall, this research provides clear evidence that the dynamic binding capacities of large biologics can be higher for well-designed macroporous membrane adsorbers than commercial membrane or resin ion-exchange products. Specifically, using controlled polymerization leads to anion-exchange membrane adsorbers with high binding capacities that are independent of flow rate, enabling high throughput. Results of this work should help to accelerate the broader implementation of membrane adsorbers in bioprocess purification steps.     

Production of lentiviral vectors by transient expression of minimal packaging genes from recombinant adenoviruses

BACKGROUND: The potential of lentiviral vectors for clinical gene therapy has not yet been evaluated. One of the reasons is the cytotoxicity of lentiviral packaging genes which makes the generation of stable producer cell lines difficult. Therefore, a novel packaging system for lentiviral vectors based on transient expression of packaging genes by recombinant adenoviruses was developed. METHODS: Adenoviral vectors expressing VSV-G, codon-optimized HIV-1 gag-pol, and codon-optimized SIV gag-pol under the control of a tetracycline-regulatable promoter (adenoviral lenti-pack vectors) were constructed and the production levels of this vector system were evaluated. RESULTS: The generated adenoviral lenti-pack vectors could be grown to high titers when transgene expression was suppressed and no evidence for instabilities was obtained. Cells stably transfected with a SIV-based vector construct were converted into lentiviral vector producer cells by infection with the adenoviral lenti-pack vectors. Lentiviral vector titers obtained were as high as vector titers obtained by transient cotransfection experiments. A protocol was developed that allowed preparation of lentiviral vector stocks with undetectable levels of contaminating adenoviral lenti-pack vectors. CONCLUSIONS: The adenoviral lenti-pack vectors described should provide a convenient alternative approach to inducible packaging cell lines for large-scale lentiviral vector production. Transient expression of cytotoxic lentiviral packaging genes by the adenoviral lenti-pack vectors circumvents loss of titers during prolonged culture of packaging cell lines. The design of the adenoviral lenti-pack vectors should reduce the risk of transfer of packaging genes to target cells and at the same time provide flexibility with respect to the lentiviral vector constructs that can be packaged.     

The role of polymer nanolayer architecture on the separation performance of anion-exchange membrane adsorbers: part II. DNA and virus separations

The surface-initiated polymerization protocol developed in part I was used to prepare strong anion-exchange membranes with variable polymer chain graft densities and degrees of polymerization for DNA and virus particle separations. A focus of part II was to evaluate the role of polymer nanolayer architecture on DNA and virus binding. Salmon sperm-DNA (SS-DNA) was used as model nucleic acid to measure the dynamic-binding capacities at 10% breakthrough. The dynamic-binding capacity increases linearly with increasing poly ([2-(methacryloyloxy)ethyl]trimethylammonium chloride) chain density up to the highest chain density used in this study. The new membranes yielded threefold higher SS-DNA-binding capacity (30 mg/mL) than a leading commercial membrane with the same functional group chemistry. Elution of bound DNA yielded a sharp peak, and resulted in a 13-fold increase relative to the feed concentration. This concentration effect further demonstrates the highly favorable transport properties of the newly designed Q-type membranes. However, unlike findings in part I on protein binding, SS-DNA binding was not fully reversible. Minute virus of mice (MVM) was used as model virus to evaluate the virus clearance performance of newly designed Q-type membranes. Log reduction of virus (LRV) of MVM increased with increasing polymer chain density. Membranes exhibited >4.5 LRV for the given MVM impurity load and may be capable of higher LRV values, as the MVM concentration in the flow-through fraction of these samples was below the limit of detection of the assay.     

Transduction of satellite cells after prenatal intramuscular administration of lentiviral vectors

BACKGROUND: We have previously reported long-term expression of lacZ in myocytes after in utero intramuscular injection of Mokola and Ebola pseudotyped lentiviral vectors. In further experiments, we have noted that these vectors also transduce small cells at the periphery of the muscle fibers that have the morphology of satellite cells, or muscle stem cells. In this study we performed experiments to further define the morphology and function of these cells. METHODS: Balb/c mice at 14-15 days gestation were injected intramuscularly with Ebola or Mokola pseudotyped lentiviral vectors carrying CMV-lacZ. Animals were harvested at various time points, muscles were stained with X-gal, and processed for electron microscopy (EM) and immunofluorescence. To determine whether transduced satellite cells were functionally capable of regenerating injured muscles, animals were injected with notexin in the same area 8 weeks after the in utero injection of viral vector. RESULTS: Transmission EM of transduced cells confirmed the ultrastructural appearance of satellite cells. Double immunofluorescence for beta-galactosidase and satellite cell markers demonstrated co-localization of these markers in transduced cells. In the notexin-injured animals, small blue cells were seen at the areas of regeneration that co-localized beta-galactosidase with markers of regenerating satellite cells. Central nucleated blue fibers were seen at late time points, indicating regenerated muscle fibers arising from a transduced satellite cell. CONCLUSIONS: This study demonstrates transduction of muscle satellite cells following prenatal viral vector mediated gene transfer. These findings may have important implications for gene therapy strategies directed toward muscular dystrophy.     

Development and characterization of a minimal inducible packaging cell line for simian immunodeficiency virus-based lentiviral vectors

Background

Lentiviral vectors allow gene transfer into non‐dividing cells. Further development of these vector systems requires stable packaging cell lines that enable adequate safety testing.

Methods

To generate a packaging cell line for vectors based on simian immunodeficiency virus (SIV), expression plasmids were constructed that contain the codon‐optimized gag‐pol gene of SIV and the gene for the G protein of vesicular stomatitis virus (VSV‐G) under the control of an ponasterone‐inducible promoter. Stable cell lines expressing these packaging constructs were established and characterized.

Results

The RT activity and vector titers of cell clones stably transfected with the inducible gag‐pol expession plasmid could be induced by ponasterone by more than a factor of 1000. One of these clones was subsequently transfected with the ponasterone‐inducible VSV‐G expression plasmid to generate packaging cells. Clones of the packaging cells were screened for vector production by infection with an SIV vector and subsequent induction by ponasterone. In the supernatant of selected ponasterone‐induced producer clones vector titers of more than 1×10⁵ transducing units/ml were obtained. Producer cell clones were stable for at least five months, as tested by vector production.

Conclusions

The packaging cells described should be suitable for most preclinical applications of SIV‐based vectors. By avoiding regions of high homology between the vector and the packaging constructs, the design of the SIV packaging cell line should reduce the risk of transfer of packaging genes to target cells and at the same time provide flexibility with respect to the SIV vector constructs that can be packaged. Copyright © 2002 John Wiley & Sons, Ltd.

     

Purification of cell culture-derived human influenza A virus by size-exclusion and anion-exchange chromatography

A process comprising of size-exclusion chromatography (SEC) and anion-exchange chromatography (AEC) was investigated for downstream processing of cell culture-derived influenza A virus. Human influenza virus A/PR/8/34 (H1N1) was propagated in serum-free medium using MDCK cells as a host. Concentrates of the virus were prepared from clarified and inactivated cell culture supernatants by cross-flow ultrafiltration as described before. SEC on Sepharose 4 FF resulted in average product yields of 85% based on hemagglutination (HA) activity. Productivity was maximized to 0.15 column volumes (cv) of concentrate per hour yielding a reduction in total protein and host cell DNA (hcDNA) to 35 and 34%, respectively. AEC on Sepharose Q XL was used to separate hcDNA from virus at a salt concentration of 0.65 M sodium chloride. Product yields >80% were achieved for loads >160 kHAU/mL of resin. The reduction in hcDNA was 67-fold. Split peak elution and bimodal particle volume distributions suggested aggregation of virions. Co-elution with hcDNA and constant amounts of hcDNA per dose indiciated association of virions to hcDNA. An overall product yield of 52% was achieved. Total protein was reduced more than 19-fold; hcDNA more than 500-fold by the process. Estimation of the dose volume from HA activity predicted a protein content at the limit for human vaccines. Reduction of hcDNA was found insufficient (about 500 ng per dose) requiring further optimization of AEC or additional purification steps. All operations were selected to be scalable and independent of the virus strain rendering the process suitable for vaccine production.     

Evaluation of restricted access media for the purification of cell culture-derived Orf viruses

Recently, multimodal chromatography using restricted access media (RAM) for the purification of nanoparticles, such as viruses has regained increasing attention. These chromatography resins combine size exclusion on the particle shell and adsorptive interaction within the core. Accordingly, smaller process-related impurities, for example, DNA and proteins, can be retained, while larger product viruses can pass unhindered. We evaluated a range of currently available RAM, differing in the shells’ pore cut-off and the core chemistry, for the purification of a cell culture-derived clarified model virus, namely the Orf virus (ORFV). We examined impurity depletion and product recovery as relevant criteria for the evaluation of column performance, as well as scale-up robustness and regeneration potential for evaluating a multiple use application. The results indicate that some columns, for example, the Capto Core, enable both a high DNA and protein removal, while others, for example, the Monomix Core 60 (MC60), are more suitable for DNA depletion. Furthermore, column regeneration is facilitated by using columns with larger shell pores (5000 vs. 700 kDa) and weaker binding interactions (anion exchange vs. multimodal). According to these findings, the choice of RAM resins should be selected according to the respective feed sample composition and the planned number of application cycles.     

Titers of lentiviral vectors encoding shRNAs and miRNAs are reduced by different mechanisms that require distinct repair strategies

RNAi-based gene therapy is a powerful approach to treat viral infections because of its high efficiency and sequence specificity. The HIV-1-based lentiviral vector system is suitable for the delivery of RNAi inducers to HIV-1 susceptible cells due to its ability to transduce nondividing cells, including hematopoietic stem cells, and its ability for stable transgene delivery into the host cell genome. However, the presence of anti-HIV short hairpin RNA (shRNA) and microRNA (miRNA) cassettes can negatively affect the lentiviral vector titers. We show that shRNAs, which target the vector genomic RNA, strongly reduced lentiviral vector titers but inhibition of the RNAi pathway via saturation could rescue vector production. The presence of miRNAs in the vector RNA genome (sense orientation) results in a minor titer reduction due to Drosha processing. A major cause for titer reduction of miRNA vectors is due to incompatibility of the cytomegalovirus promoter with the lentiviral vector system. Replacement of this promoter with an inducible promoter resulted in an almost complete restoration of the vector titer. We also showed that antisense poly(A) signal sequences can have a dramatic effect on the vector titer. These results show that not all sequences are compatible with the lentiviral vector system and that care should be taken in the design of lentiviral vectors encoding RNAi inducers.     

The evolution of heart gene delivery vectors

Gene therapy holds promise for treating numerous heart diseases. A key premise for the success of cardiac gene therapy is the development of powerful gene transfer vehicles that can achieve highly efficient and persistent gene transfer specifically in the heart. Other features of an ideal vector include negligible toxicity, minimal immunogenicity and easy manufacturing. Rapid progress in the fields of molecular biology and virology has offered great opportunities to engineer various genetic materials for heart gene delivery. Several nonviral vectors (e.g. naked plasmids, plasmid lipid/polymer complexes and oligonucleotides) have been tested. Commonly used viral vectors include lentivirus, adenovirus and adeno-associated virus. Among these, adeno-associated virus has shown many attractive features for pre-clinical experimentation in animal models of heart diseases. We review the history and evolution of these vectors for heart gene transfer.     

Purification of glycomacropeptide from non-dialyzable fraction of sweet whey by anion-exchange chromatography

Glycomacropeptide (GMP) was purified from non-dialyzable fraction of sweet whey by anion-exchange chromatography on DEAE-Sephacel at two pHs 6.4 and 3.0. Chromatography at pH 3.0 (but not pH 6.4) gave a GMP fraction of high purity with its yield (1 g from every litre of whey) being approximately 100 times higher than that shown in the previous report. It was concluded that DEAE-Sephacel chromatography at pH 3.0 is a simple useful method to separate GMP from most whey proteins. It may be applicable to a large scale production of GMP.     

Countercurrent tangential chromatography for large-scale protein purification

Recent advances in cell culture technology have created significant pressure on the downstream purification process, leading to a "downstream bottleneck" in the production of recombinant therapeutic proteins for the treatment of cancer, genetic disorders, and cardiovascular disease. Countercurrent tangential chromatography overcomes many of the limitations of conventional column chromatography by having the resin (in the form of a slurry) flow through a series of static mixers and hollow fiber membrane modules. The buffers used in the binding, washing, and elution steps flow countercurrent to the resin, enabling high-resolution separations while reducing the amount of buffer needed for protein purification. The results obtained in this study provide the first experimental demonstration of the feasibility of using countercurrent tangential chromatography for the separation of a model protein mixture containing bovine serum albumin and myoglobin using a commercially available anion exchange resin. Batch uptake/desorption experiments were used in combination with critical flux data for the hollow fiber filters to design the countercurrent tangential chromatography system. A two-stage batch separation yielded the purified target protein at >99% purity with 94% recovery. The results clearly demonstrate the potential of using countercurrent tangential chromatography for the large-scale purification of therapeutic proteins.     

Quantitative proteomic analysis of lentiviral vectors using 2‐DE

Among the integrative gene therapy vectors developed to date, human immunodeficiency virus type 1 (HIV‐1)‐derived lentiviral vectors (LV) are distinguished by their capacity to infect both dividing and non‐dividing cells. Recombinant LV particles contain viral proteins necessary for their packaging, infectious and integrating functions. Like the parental HIV‐1 virus they are able to acquire various cellular proteins, but the number and localisation of these proteins are poorly characterised. In the present study we used 2‐DE followed by MALDI‐TOF to quantify the protein content of several types of vesicular stomatitis virus G‐pseudotyped LV including those that were extensively purified in the perspective of clinical gene therapy studies. A proteinase K treatment was used to distinguish between cellular proteins incorporated into virions (I‐proteins) and those co‐purified with vectors (C‐proteins). We found 10 C‐proteins and 18 I‐proteins associated with LV. Copy numbers for these core I‐proteins varied from 5 (AIP‐1/ALIX) to 280 (Cyclophilin A) per vector particle. Three novel I‐proteins, guanine nucleotide‐binding protein 2, L‐lactate dehydrogenase B chain and hnRNP core protein A1, were found. This study defines for the first time, the protein stoichiometry of infectious HIV‐1‐derived LV particles.