Multigene expression in stable CHO cell pools generated with the piggyBac transposon system

Heterogenous populations of recombinant cells (cell pools) stably expressing 1-4 transgenes were generated from Chinese hamster overy (CHO) cells with the piggyBac (PB) transposon system. The cell pools produced different combinations of three model proteinsenhanced green fluorescent protein (EGFP), secreted alkaline phosphatase (SEAP), and a monoclonal IgG1 antibody. Each transgene was present on a separate PB donor plasmid with either the same or a different selection gene. In both cases, we obtained PB-derived cell pools with higher recombinant protein yields than from cell pools generated by conventional gene delivery. In PB-derived cell pools generated using a single selection agent, both protein production and the number of integrated copies of each transgene declined as the number of transfected transgenes increased. However, the total number of integrated transgenes was similar regardless of the number of different transgenes transfected. For PB-derived cell pools generated by selection of each transgene with a different selection agent, the total number of integrated transgenes increased with the number of transfected transgenes. The results suggest that the generation of cell pools producing multiple recombinant proteins is feasible and that the method is more efficient when each individual transgene is selected with a different marker. (c) 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1308-1317, 2016

Study of transposon-mediated cell pool and cell line generation in CHO cells

Sowmya Balasubramanian

The goal of this thesis was to evaluate the use of artificial transposon systems for the generation of recombinant cell pools and cell lines with Chinese hamster ovary (CHO) cells as the production host. Transposons are naturally occurring genetic elements present in the genome of most organisms. Several transposons of metazoan origin have been engineered to facilitate the integration of one or more recombinant genes (transgenes) into the genome of the host cell. In this thesis, three of the most commonly used transposons, piggyBac (PB), Tol2, and Sleeping Beauty (SB), were used for transgene delivery into CHO-DG44 cells. The transposon systems described here involves co-transfection of the host cells with a helper plasmid for the transient expression of the transposase, and a donor plasmid coding for the transgene and a gene for the selection, both positioned between two transposon repeat sequences that are required for DNA transposition. Through the optimization of various selection parameters we showed that PB-mediated cell pools can be generated with selection duration of as little as 5 days in the presence of puromycin. All three transposon systems, PB, Tol2, and SB, resulted in cell pools with similar volumetric TNFR:Fc productivities that were about 9 times higher than those generated by conventional plasmid transfection. Transposon-mediated cell pools had 10 - 12 transgene integrations per cell. However, we demonstrated that some the integration events occurred via DNA recombination rather than transposition. We also isolated clonal cell lines from cell pools. As expected, the average volumetric TNFR:Fc productivity of transposon-derived cell lines was higher than that of cell lines generated by conventional transfection. In 14-day fed-batch cultures, protein levels up to 900 mg/L and 1.5 g/L were obtained from transposon-mediated cell pools and cell lines, respectively. The stability over time of the volumetric productivity of cell pools was determined by maintaining the cells in culture for 3 months in the absence of selection. In general, the productivity decreased to 50 % its initial level over the first 7 weeks in culture and then remained constant for the following 5 weeks. In contrast, the volumetric protein yield from transposon-mediated cell lines remained constant for up to 4 months in the absence of selection. We also showed that the three transposon systems could be used for cell pool generation with CHO-K1 and CHO-S with similar volumetric productivities as observed with CHO-DG44 cells. Finally, we utilized the PB transposon system for generating cell pools co-expressing up to 4 different transgenes, enhanced green fluorescent protein (EGFP), secreted alkaline phosphatase (SEAP), and the light and heavy chains of an IgG1 monoclonal antibody, by simultaneous transfection of all four transgenes. We showed that PB-mediated cell pools had increased volumetric productivity of each of the proteins compared to those generated by conventional co-transfection. The use of the PB transposon system increased the percentage of cells in the pools that were co-expressing all four proteins as compared to the results with cell pools generated by conventional transfection. In conclusion, the transfection of CHO cells with the PB, Tol2 or SB transposon system is a simple, efficient, and reproducible approach to the generation of cell pools and cell lines for the rapid production of recombinant proteins.

EPFL2015

Rapid recombinant protein production from piggyBac transposon-mediated stable CHO cell pools

Sowmya Balasubramanian, Lucia Baldi Unser, David Hacker, Zuzana Kadlecova, Florian Maria Wurm

Heterogeneous populations of stably transfected cells (cell pools) can serve for the rapid production of moderate amounts of recombinant proteins. Here, we propose the use of the piggyBac (PB) transposon system to improve the productivity and long-term stability of cell pools derived from Chinese hamster ovary (CHO) cells. PB is a naturally occurring genetic element that has been engineered to facilitate the integration of a transgene into the genome of the host cell. In this report PB-derived cell pools were generated after 10 days of selection with puromycin. The resulting cell pools had volumetric productivities that were 3–4 times higher than those achieved with cell pools generated by conventional plasmid transfection even though the number of integrated transgene copies per cell was similar in the two populations. In 14-day batch cultures, protein levels up to 600 and 800 mg/L were obtained for an Fc-fusion protein and a monoclonal antibody, respectively, at volumetric scales up to 1 L. In general, the volumetric protein yield from cell pools remained constant for up to 3 months in the absence of selection. In conclusion, transfection of CHO cells with the PB transposon system is a simple, efficient, and reproducible approach to the generation of cell pools for the rapid production of recombinant proteins.

Elsevier2015

The Use of Valproic Acid in Transient Gene Expression with HEK-293E Cells

Divor Kiseljak

Transient gene expression (TGE) is a rapid method for the production of recombinant proteins. Recently, valproic acid (VPA), a well known histone deacetylase inhibitor, has been suggested for the use in cell cultures to enhance recombinant protein expression. However, little was known about protein expression in HEK-293E cells under VPA treatment. Therefore, the first aim of this thesis was to describe the effects of VPA on protein expression by TGE in HEK-293E cells. The addition of VPA induced a dose-dependent increase in protein production. Under the optimal VPA concentration (3.75 mM) IgG volumetric productivity increased over 8-fold compared to the control. This was achieved through improvements in both integral viable cell density (IVCD) and cell specific productivity. The IVCD was improved by the VPA-induced cell growth arrest resulting in longer culture duration and extended protein production phase. The enhancement in specific productivity in VPA-treated cells was a consequence of higher cellular pDNA copy number and improved pDNA utilization that led to higher transgene mRNA levels. The study on limitations governing VPA-based TGE protein expression in HEK-293E cells revealed the bottlenecks at the transcriptional and translational levels, however the limitation did not appear to be at the level of protein folding or assembly for the model IgG antibody studied. In addition, the effect of VPA was tested on the expression of different recombinant monoclonal antibodies and Fc-fusion proteins. The results showed that VPA addition did not always significantly improve protein titers. Since the optimal VPA concentration was dependent on both the recombinant protein being expressed and the amount of coding pDNA used for transfection, we recommend evaluating the suitability of VPA addition and the optimization of VPA concentration in order to find the optimal conditions for TGE protein expression. We believe that this work will contribute to the design of more rational, robust, and successful expression platforms for recombinant protein production in HEK-293E cells. One of the major contributors to the cost of TGE process at large scale is the considerable amount of pDNA required for transfection. Therefore, the second aim of III this thesis was to determine a cost-effective method to reduce the pDNA amount. We showed that a part of the coding pDNA can be replaced with nonspecific (filler) DNA with minimal loss in volumetric productivity. The studies revealed that the presence of filler DNA allowed the coding pDNA to be distributed over a larger number of DNA-PEI complexes. This resulted in a higher percentage of transfected cells and may favor the better utilization of the coding pDNA by the cell’s transcription machinery. The use of filler DNA as a part of defined fed-batch process (based on the addition of glucose and plant derived protein hydrolysates) resulted in 25 fold reduction in coding pDNA amount requirement while maintaining volumetric protein productivity over 1 g/l. The cost reduction of TGE-produced proteins, due to significant decrease in pDNA amount requirement for transfections, will certainly facilitate the development and implementation of large scale TGE as a feasible method for TGE-based protein production.