The principal hurdles toward the use of recombinant lentivirus as a gene therapy vector are the low titer at which it is produced as well as the difficulty to purify it at an acceptable level without degrading it. The recent advances in the bioproduction of this vector suggest these issues are about to be resolved, making the retrovirus gene therapy a mature technology.

Manufacturing practices for recombinant adeno-associated viruses (AAV) have improved in the last decade through the development of new platforms in conjunction with better production and purification methods. In this review, we discuss the advantages and limitations of the most popular systems and methods employed with mammalian cell platforms. Methods and systems such as transient transfection, packaging and producer cells and adenovirus and herpes simplex virus are described. In terms of best production yields, they are comparable with about 10 -10 vector genomes produced per cell but transient transfection of HEK293 cells is by far the most commonly used. For small-scale productions, AAV can be directly purified from the producing cell lysate by ultracentrifugation on a CsCl or iodixanol-step gradient whereas large-scale purification requires a combination of multiple steps. Micro/macrofiltration (i.e. including tangential flow filtration and/or dead-end filtration) and chromatography based-methods are used for large-scale purification. Purified AAV products must then be quantified and characterized to ensure quality. Recent purification methods and current analytical techniques are reviewed here. Finally, AAV technology is very promising, but manufacturing improvements are still required to meet the needs of affordable, safe and effective AAV vectors essential for licensing of gene therapy clinical protocols.

Delivery of recombinant proteins to therapeutic cells is limited by a lack of efficient methods. This hinders the use of transcription factors or Clustered Regularly Interspaced Short Palindromic Repeats (CRISPR) ribonucleoproteins to develop cell therapies. Here, we report a soluble peptide designed for the direct delivery of proteins to mammalian cells including human stem cells, hard-to-modify primary natural killer (NK) cells, and cancer cell models. This peptide is composed of a 6x histidine-rich domain fused to the endosomolytic peptide CM18 and the cell penetrating peptide PTD4. A less than two-minute co-incubation of 6His-CM18-PTD4 peptide with spCas9 and/or asCpf1 CRISPR ribonucleoproteins achieves robust gene editing. The same procedure, co-incubating with the transcription factor HoxB4, achieves transcriptional regulation. The broad applicability and flexibility of this DNA- and chemical-free method across different cell types, particularly hard-to-transfect cells, opens the way for a direct use of proteins for biomedical research and cell therapy manufacturing.

Delivery of nucleic acid-based molecules in human cells is a highly studied approach for the treatment of several disorders including monogenic diseases and cancers. Non-viral vectors for DNA and RNA transfer, although in general less efficient than virus-based systems, are particularly well adapted mostly due to the absence of biosafety concerns. Non-viral methods could be classified in two main groups: physical and vector-assisted delivery systems. Both groups comprise several different methods, none of them universally applicable. The choice of the optimal method depends on the predefined objectives and the features of targeted micro-environment. Areas covered: In this review, the authors discuss non-viral techniques and present recent therapeutic achievements in ex vivo and in vivo nucleic acid delivery by most commonly used techniques while emphasizing the role of 'biological particles', namely peptide transduction domains, virus like particles, gesicles and exosomes. Expert opinion: The number of available non-viral transfection techniques used for human therapy increased rapidly, followed by still moderate success in efficacy. The prospects are to be found in design of multifunctional hybrid systems that reflect the viral efficiency. In this respect, biological particles are very promising.

Fast and efficient production of recombinant proteins for structural and functional studies is a crucial issue for research and for industry. To this end, we have developed an efficient system to generate in less than 2 months, starting from the cDNA, pools of CHO cells stably expressing high-level of recombinant proteins. It is based on lentiviral vectors (LVs) for stable transduction coupled with the cumate gene-switch for inducible and efficient gene expression. Transcription is initiated upon binding of the cumate transactivator (cTA) or the reverse cTA (rcTA) to the CR5 promoter. Binding of cTA or rcTA is prevented or induced by addition of cumate respectively. We first validated the CHO/LV production system with an LV carrying the secreted alkaline phosphatase (SEAP), whose expression was linked to the green fluorescent protein (GFP) through an internal ribosome entry site (IRES). CHO cells stably expressing the cTA (CHO-cTA) were transduced at various multiplicity of infection (MOI). Pools of cells were incubated at 37 and 30 degrees C during 10 days. Optimal SEAP production (65 microg/mL) was achieved at 30 degrees C with a MOI of 200. The pool stability was demonstrated for 48 days of culture by GFP expression analysis. The system was also evaluated using LV expressing three typical therapeutic proteins (a protein made up of the extracellular domain of CD200 fused to IgG Fc region [CD200Fc], a chimeric antibody [chB43], and erythropoietin [EPO]). CHO cells expressing rcTA (CHO-Cum2) were transduced with these LVs at a MOI of 200 and production was tested at 30 degrees C. After 13 days of culture, 235, 160, and 206 microg/mL of CD200Fc, chB43, and EPO were produced, respectively. The ON/OFF ratio of these pools was equal to 6 for CD200Fc, 16 for chB43, and 74 for EPO. In conclusion, this system should be very useful to produce mg quantities of recombinant proteins in a timely manner in serum free suspension culture of CHO cells for preclinical studies.

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Background: Despite the powerful impact in recent years of gene expression markers like the green fluorescent protein (GFP) to link the expression of recombinant protein for selection of high producers, there is a strong incentive to develop rapid and efficient methods for isolating mammalian cell clones secreting high levels of marker-free recombinant proteins. Recently, a method combining cell colony growth in methylcellulose-based medium with detection by a fluorescently labeled secondary antibody or antigen has shown promise for the selection of Chinese Hamster Ovary (CHO) cell lines secreting recombinant antibodies. Here we report an extension of this method referred to as fluorescent labeling in semi-solid medium (FLSSM) to detect recombinant proteins significantly smaller than antibodies, such as IGF-E5, a 25 kDa insulinlike growth factor derivative.

To facilitate and accelerate the production of eukaryotic proteins with correct post-translational modifications, we have developed a protein production system based on the transduction of Chinese hamster ovary (CHO) cells using adenovirus vectors (AdVs). We have engineered a CHO cell line (CHO-cTA) that stably expresses the transactivator (cTA) of our newly developed cumate gene-switch transcription system. This cell line is adapted to suspension culture and can grow in serum-free and protein-free medium. To increase the transduction level of AdVs, we have also generated a cell line (CHO-cTA-CAR) that expresses additional amounts of the coxackievirus and adenovirus receptor (CAR) on its surface. Recombinant protein production was tested using an AdV carrying the secreted alkaline phosphatase (SEAP) under the control of the CR5 promoter, which is strongly and specifically activated by binding to cTA. The SEAP expression was linked to the expression of the green fluorescent protein (GFP) through an internal ribosome entry site (IRES) to facilitate titration of the AdV. We monitored SEAP expression on a daily basis for 9 days after transduction of CHO-cTA and CHO-cTA-CAR using different quantities of AdVs at 37 and 30 degrees C. Incubation at the latter temperature increased the production of SEAP at least 10-fold, and the presence of CAR increased the transduction level of the AdV. Maximum SEAP production (63 mg/L) was achieved at 6-7 days post-infection at 30 degrees C by transducing CHO-cTA-CAR with 500 infectious particles/cell. Because numerous AdVs can now be generated within a few weeks and large-scale production of AdVs is now a routine procedure, this system could be used to produce rapidly milligram quantities of a battery of recombinant proteins as well as for large-scale protein production.