Establishment and characterization of conditions required for tumor colonization by intravenously delivered bacteria

Transient gene expression (TGE) provides a method for quickly delivering protein for research using mammalian cells. While high levels of recombinant proteins have been produced in TGE experiments in HEK 293 cells, TGE efforts in the commercially prominent CHO cell line still suffer from inadequate protein yields. Here, we describe a cell-engineering strategy to improve transient production of proteins using CHO cells. CHO-DG44 cells were engineered to overexpress the anti-apoptotic protein Bcl-x(L) and transiently transfected using polyethylenimine (PEI) in serum-free media. Pools and cell lines stably expressing Bcl-x(L) showed enhanced viable cell density and increased production of a glycosylated, therapeutic fusion protein in shake flask TGE studies. The improved cell lines showed fusion protein production levels ranging from 12.6 to 27.0 mg/L in the supernatant compared to the control cultures which produced 6.3-7.3 mg/L, representing a 70-270% increase in yield after 14 days of fed-batch culture. All Bcl-xL-expressing cell lines also exhibited an increase in specific productivity during the first 8 days of culture. In addition to increased production, Bcl-x(L) cell lines maintained viabilities above 90% and less apoptosis compared to the DG44 host which had viabilities below 60% after 14 days. Product quality was comparable between a Bcl-xL-engineered cell line and the CHO host. The work presented here provides the foundation for using anti-apoptosis engineered CHO cell lines for increased production of therapeutic proteins in TGE applications.     

Fed-batch bioreactor performance and cell line stability evaluation of the artificial chromosome expression technology expressing an IgG1 in Chinese hamster ovary cells

The artificial chromosome expression (ACE) technology system uses an engineered artificial chromosome containing multiple site-specific recombination acceptor sites for the rapid and efficient construction of stable cell lines. The construction of Chinese hamster ovary(CHO) cell lines expressing an IgG1 monoclonal antibody (MAb) using the ACE system has been previously described (Kennard et al., Biotechnol Bioeng. 2009;104:540-553). To further demonstrate the manufacturing feasibility of the ACE system, four CHO cell lines expressing the human IgG1 MAb 4A1 were evaluated in batch and fed-batch shake flasks and in a 2-L fed-batch bioreactor. The batch shake flasks achieved titers between 0.7 and 1.1 g/L, whereas the fed-batch shake flask process improved titers to 2.5–3.0 g/L. The lead 4A1 ACE cell line achieved titers of 4.0 g/L with an average specific productivity of 40 pg/(cell day) when cultured in a non optimized 2-L fed-batch bioreactor using a completely chemically defined process. Generational stability characterization of the lead 4A1-expressing cell line demonstrated that the cell line was stable for up to 75 days in culture. Product quality attributes of the 4A1 MAb produced by the ACE system during the stability evaluation period were unchanged and also comparable to existing expression technologies such as the CHO-dhfr system. The results of this evaluation demonstrate that a clonal, stable MAb-expressing CHO cell line can be produced using ACE technology that performs competitively using a chemically defined fed-batch bioreactor process with comparable product quality attributes to cell lines generated by existing technologies.     

A high‐yielding CHO transient system: Coexpression of genes encoding EBNA‐1 and GS enhances transient protein expression

An efficient rapid protein expression system is crucial to support early drug development. Transient gene expression is an effective route, and to facilitate the use of the same host cells as for subsequent stable cell line development, we have created a high‐yielding Chinese hamster ovary (CHO) transient expression system. Suspension‐adapted CHO‐K1 host cells were engineered to express the gene encoding Epstein‐Barr virus (EBV) nuclear antigen‐1 (EBNA‐1) with and without the coexpression of the gene for glutamine synthetase (GS). Analysis of the transfectants indicated that coexpression of EBNA‐1 and GS enhanced transient expression of a recombinant antibody from a plasmid carrying an OriP DNA element compared to EBNA‐1‐only transfectants. This was confirmed with the retransfection of an EBNA‐1‐only cell line with a GS gene. The retransfected cell lines showed an increase in transient expression when compared with that of the EBNA‐1‐only parent. The transient expression process for the best CHO transient cell line was further developed to enhance protein expression and improve scalability by optimizing the transfection conditions and the cell culture process. This resulted in a scalable CHO transient expression system that is capable of expressing 2 g/L of recombinant proteins such as antibodies. This system can now rapidly provide gram amounts of recombinant antibody to supply preclinical development studies that has comparable product quality to antibody produced from a stably transfected CHO cell line. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:132–141, 2014     

CHO cell expression,long‐term stability,and primate pharmacokinetics and brain uptake of an IgG–paroxonase‐1 fusion protein

Paraoxonase (PON)‐1 is the most potent human organophosphatase known, but recombinant forms of human PON1 have been difficult to produce owing to poor secretion by host cells. In the present investigation, human PON1 is re‐engineered as an IgG–PON1 fusion protein. The 355 amino acid human PON1 is fused to the carboxyl terminus of the heavy chain of a chimeric monoclonal antibody (MAb) against the human insulin receptor (HIR), and this fusion protein is designated HIRMAb–PON1. The HIRMAb part of the fusion protein enables brain penetration of the PON1, which was considered important, because organophosphate toxicity causes death via a central nervous system site of action. A high producing line of stably transfected Chinese hamster ovary (CHO) cells secreting the HIRMAb–PON1 fusion protein in the absence of serum or lipid acceptors was cloned. The bioreactor generated fusion protein was purified to homogeneity with low impurities by protein A affinity chromatography and anion exchange chromatography. The HIRMAb–PON1 fusion protein was stable as a sterile liquid formulation stored at 4°C for at least 1 year. The plasma pharmacokinetics (PK) of the HIRMAb–PON1 fusion protein was evaluated in Rhesus monkeys, which is the first PK evaluation of a recombinant PON1 protein. The fusion protein was rapidly removed from blood, primarily by the liver. The blood–brain barrier permeation of the HIRMAb–PON1 fusion protein was high and comparable to other HIRMAb fusion proteins. Re‐engineering human PON1 as the HIRMAb fusion protein allows for production of a stable, field‐deployable formulation of the enzyme that is brain‐penetrating. Biotechnol. Bioeng. 2011; 108:186–196. © 2010 Wiley Periodicals, Inc.     

Mcl‐1 overexpression leads to higher viabilities and increased production of humanized monoclonal antibody in Chinese hamster ovary cells

Bioreactor stresses, including nutrient deprivation, shear stress, and byproduct accumulation can cause apoptosis, leading to lower recombinant protein yields and increased costs in downstream processing. Although cell engineering strategies utilizing the overexpression of antiapoptotic Bcl‐2 family proteins such as Bcl‐2 and Bcl‐x_L potently inhibit apoptosis, no studies have examined the use of the Bcl‐2 family protein, Mcl‐1, in commercial mammalian cell culture processes. Here, we overexpress both the wild type Mcl‐1 protein and a Mcl‐1 mutant protein that is not degraded by the proteasome in a serum‐free Chinese hamster ovary (CHO) cell line producing a therapeutic antibody. The expression of Mcl‐1 led to increased viabilities in fed‐batch culture, with cell lines expressing the Mcl‐1 mutant maintaining ～90% viability after 14 days when compared with 65% for control cells. In addition to enhanced culture viability, Mcl‐1‐expressing cell lines were isolated that consistently showed increases in antibody production of 20–35% when compared with control cultures. The quality of the antibody product was not affected in the Mcl‐1‐expressing cell lines, and Mcl‐1‐expressing cells exhibited 3‐fold lower caspase‐3 activation when compared with the control cell lines. Altogether, the expression of Mcl‐1 represents a promising alternative cell engineering strategy to delay apoptosis and increase recombinant protein production in CHO cells. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Production and scale‐up of a monoclonal antibody against 17‐hydroxyprogesterone

The hybridoma 192 was used to produce a monoclonal antibody (MAb) against 17‐hydroxyprogesterone (17‐OHP), for possible use in screening for congenital adrenal hyperplasia (CAH). The factors influencing the MAb production were screened and optimized in a 2 L stirred bioreactor. The production was then scaled up to a 20 L bioreactor. All of the screened factors (aeration rate, stirring speed, dissolved oxygen concentration, pH, and temperature) were found to significantly affect production. Optimization using the response surface methodology identified the following optimal production conditions: 36.8°C, pH 7.4, stirring speed of 100 rpm, 30% dissolved oxygen concentration, and an aeration rate of 0.09 vvm. Under these conditions, the maximum viable cell density achieved was 1.34 ± 0.21 × 10⁶ cells mL^?1 and the specific growth rate was 0.036 ± 0.004 h^?1. The maximum MAb titer was 11.94 ± 4.81 μg mL^?1 with an average specific MAb production rate of 0.273 ± 0.135 pg cell^?1 h^?1. A constant impeller tip speed criterion was used for the scale‐up. The specific growth rate (0.040 h^?1) and the maximum viable cell density (1.89 × 10⁶ cells mL^?1) at the larger scale were better than the values achieved at the small scale, but the MAb titer in the 20 L bioreactor was 18% lower than in the smaller bioreactor. A change in the culture environment from the static conditions of a T‐flask to the stirred bioreactor culture did not affect the specificity of the MAb toward its antigen (17‐OHP) and did not compromise the structural integrity of the MAb. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2013     

Enhanced cell culture performance using inducible anti-apoptotic genes E1B-19K and Aven in the production of a monoclonal antibody with Chinese hamster ovary cells

Mammalian cells are used for the production of numerous biologics including monoclonal antibodies. Unfortunately, mammalian cells can lose viability at later stages in the cell culture process. In this study, the effects of expressing the anti-apoptosis genes, E1B-19K and Aven, separately and in combination on cell growth, survival, and monoclonal antibody (MAb) production were investigated for a commercial Chinese Hamster Ovary (CHO) mammalian cell line. CHO cells were observed to undergo apoptosis following a model insult, glucose deprivation, and at later stages of batch cell culture. The CHO cell line was then genetically modified to express the anti-apoptotic proteins E1B-19K and/or Aven using an ecdysone-inducible expression system. Stable transfected pools induced to express Aven or E1B-19K alone were found to survive 1-2 days longer than the parent cell line following glucose deprivation while the expression of both genes in concert increased cell survival by 3 days. In spinner flask batch studies, a clonal isolate engineered to express both anti-apoptosis genes exhibited a longer operating lifetime and higher final MAb titer as a result of higher viable cell densities and viabilities. Interestingly, survival was increased in the absence of an inducer, most likely as a result of leaky expression of the anti-apoptosis genes confirmed in subsequent PCR studies. In fed-batch bioreactors, the expression of both anti-apoptosis genes resulted in higher growth rates and cell densities in the exponential phase and significantly higher viable cell densities, viabilities, and extended survival during the post-exponential phase. As a result, the integral of viable cells (IVC) was between 40 and 100% higher for cell lines engineered to express both Aven and E1B-19K in concert, and the operational lifetime of the fed-batch bioreactors was increased from 2 to 5 days. The maximum titers of MAb were also increased by 40-55% for bioreactors containing cells expressing Aven and E1B-19K. These increases in volumetric productivity arose primarily from enhancements in viable cell density over the course of the fed-batch culture period since the specific productivities for the cells expressing anti-apoptosis genes were comparable or slightly lower than the parental hosts. These results demonstrate that expression of anti-apoptosis genes can enhance culture performance and increase MAb titers for mammalian CHO cell cultures especially under conditions such as extended fed-batch bioreactor operation.     

Production process reproducibility and product quality consistency of transient gene expression in HEK293 cells with anti-PD1 antibody as the model protein

Demonstration of reproducibility and consistency of process and product quality is one of the most crucial issues in using transient gene expression (TGE) technology for biopharmaceutical development. In this study, we challenged the production consistency of TGE by expressing nine batches of recombinant IgG antibody in human embryonic kidney 293 cells to evaluate reproducibility including viable cell density, viability, apoptotic status, and antibody yield in cell culture supernatant. Product quality including isoelectric point, binding affinity, secondary structure, and thermal stability was assessed as well. In addition, major glycan forms of antibody from different batches of production were compared to demonstrate glycosylation consistency. Glycan compositions of the antibody harvested at different time periods were also measured to illustrate N-glycan distribution over the culture time. From the results, it has been demonstrated that different TGE batches are reproducible from lot to lot in overall cell growth, product yield, and product qualities including isoelectric point, binding affinity, secondary structure, and thermal stability. Furthermore, major N-glycan compositions are consistent among different TGE batches and conserved during cell culture time.

     

Design of Experiment in CHO and HEK transient transfection condition optimization

Transient gene expression (TGE) is a well-established enabling technology for rapid generation of recombinant proteins, with Human Embryonic Kidney (HEK) and Chinese Hamster Ovary (CHO) cell lines and polyethyleneimine (PEI) as the transfection reagent being its most popular components. However, despite considerable progress made in the field, volumetric titers can still be a limiting factor causing the manipulation of increasing quantities of culture media and DNA. Here, we report a systematic analysis of TGE conditions and their influence on yields and protein quality. Guided by Design of Experiments (DoE), we conclude that TGE yields with one test antibody can be maximized by a parallel increase of cell density - 2.4 to 3.0 × 10(6)cells/mL - and PEI concentration - 24 to 30 mg/L - while maintaining a 1:1 ratio of heavy chain and light chain encoding plasmids. Interestingly, we also show that in these conditions, DNA concentration can be maintained in the 1mg/L range, thereby limiting the need for large DNA preparations. Our optimized settings for PEI-mediated TGE in HEK and CHO cells evaluated on several proteins are generally applicable to recombinant antibodies and proteins.     

Production of an active anti‐CD20‐hIL‐2 immunocytokine in Nicotiana benthamiana

Anti‐CD20 murine or chimeric antibodies (Abs) have been used to treat non‐Hodgkin lymphomas (NHLs) and other diseases characterized by overactive or dysfunctional B cells. Anti‐CD20 Abs demonstrated to be effective in inducing regression of B‐cell lymphomas, although in many cases patients relapse following treatment. A promising approach to improve the outcome of mAb therapy is the use of anti‐CD20 antibodies to deliver cytokines to the tumour microenvironment. In particular, IL‐2‐based immunocytokines have shown enhanced antitumour activity in several preclinical studies. Here, we report on the engineering of an anti‐CD20‐human interleukin‐2 (hIL‐2) immunocytokine (2B8‐Fc‐hIL2) based on the C2B8 mAb (Rituximab) and the resulting ectopic expression in Nicotiana benthamiana. The scFv‐Fc‐engineered immunocytokine is fully assembled in plants with minor degradation products as assessed by SDS‐PAGE and gel filtration. Purification yields using protein‐A affinity chromatography were in the range of 15–20 mg/kg of fresh leaf weight (FW). Glycopeptide analysis confirmed the presence of a highly homogeneous plant‐type glycosylation. 2B8‐Fc‐hIL2 and the cognate 2B8‐Fc antibody, devoid of hIL‐2, were assayed by flow cytometry on Daudi cells revealing a CD20 binding activity comparable to that of Rituximab and were effective in eliciting antibody‐dependent cell‐mediated cytotoxicity of human PBMC versus Daudi cells, demonstrating their functional integrity. In 2B8‐Fc‐hIL2, IL‐2 accessibility and biological activity were verified by flow cytometry and cell proliferation assay. To our knowledge, this is the first example of a recombinant immunocytokine based on the therapeutic Rituximab antibody scaffold, whose expression in plants may be a valuable tool for NHLs treatment.     

High‐yield secretion of recombinant proteins expressed in tobacco cell culture with a designer glycopeptide tag: Process development

Low‐yield protein production remains the most significant economic hurdle with plant cell culture technology. Fusions of recombinant proteins with hydroxyproline‐O‐glycosylated designer glycopeptide tags have consistently boosted secreted protein yields. This prompted us to study the process development of this technology aiming to achieve productivity levels necessary for commercial viability. We used a tobacco BY‐2 cell culture expressing EGFP as fusion with a glycopeptide tag comprised of 32 repeat of ”Ser‐Pro“ dipeptide, or (SP)₃₂, to study cell growth and protein secretion, culture scale‐up, and establishment of perfusion cultures for continuous production. The BY‐2 cells accumulated low levels of cell biomass (～7.5 g DW/L) in Schenk & Hildebrandt medium, but secreted high yields of (SP)₃₂‐tagged EGFP (125 mg/L). Protein productivity of the cell culture has been stable for 6.0 years. The BY‐2 cells cultured in a 5‐L bioreactor similarly produced high secreted protein yield at 131 mg/L. Successful operation of a cell perfusion culture for 30 days was achieved under the perfusion rate of 0.25 and 0.5 day^?1, generating a protein volumetric productivity of 17.6 and 28.9 mg/day/L, respectively. This research demonstrates the great potential of the designer glycopeptide technology for use in commercial production of valuable proteins with plant cell cultures.     

Producing defucosylated antibodies with enhanced in vitro antibody‐dependent cellular cytotoxicity via FUT8 knockout CHO‐S cells

To engineer a host cell line that produces defucosylated mAbs with superior antibody‐dependent cellular cytotoxicity, we disrupted α‐1, 6 fucosyltransferase (FUT8 ) gene in CHO‐S (CHO is Chinese hamster ovary) cells by clustered regularly interspaced short palindromic repeats‐CRISPR associated nuclease 9. The gene knockout cell line was evaluated for growth, stability, and product quality. The growth profile of FUT8 gene knockout CHO‐S (FUT8 ^?/?) cells was comparable with wild type CHO‐S cells. FUT8 catalyzes the transfer of a fucose residue from GDP‐fucose to N‐glycans residue. Defucosylated IgG1 antibodies produced by FUT8 ^?/? cells showed increased binding affinities to human FcγRIIIa and higher activities in mediating antibody‐dependent cellular cytotoxicity, comparing with conventional fucosylated IgG1. Our results demonstrated the potential of using the clustered regularly interspaced short palindromic repeats‐CRISPR associated nuclease 9 technology in cell line engineering for biopharmaceutical industrial applications.     

Partial restoration of T‐cell function in aged mice by in vitro blockade of the PD‐1/ PD‐L1 pathway

Programmed cell death‐1 (PD‐1) is a newly characterized negative regulator of immune responses. The interaction of PD‐1 with its ligands (PD‐L1 and PD‐L2) inhibits T‐cell proliferation and cytokine production in young mice. Increased PD‐1 expression has been described during chronic infections, inducing chronic activation of the immune system to control it. As aging is associated with chronic immune activation, PD‐1 may contribute to age‐associated T‐cell dysfunction. Our data showed the following results in aged mice: (i) the number of PD‐1‐expressing T cells and the level of expression of PD‐Ls was increased on dendritic cell subsets and T cells; (ii) PD‐1⁺ T cells were exhausted effector memory T cells, as shown by their lower level of CD127, CD25 and CD28, as well as their limited proliferative and cytokine‐producing capacity; (iii) the expression of PD‐1 was up‐regulated after T‐cell receptor‐mediated activation of CD8⁺ T cells, but not of CD4⁺ T cells; (iv) blockade of the PD‐1/PD‐L1 pathway moderately improved the cytokine production of T cells from old mice but did not restore their proliferation; and (v) blockade of the PD‐1/PD‐L1 pathway did not restore function of PD‐1⁺ T cells; its effect appeared to be exclusively mediated by increased functionality of the PD‐1^? T cells. Our data thus suggest that blockade of the PD‐1/PD‐L1 is not likely to be efficient at restoring exhausted T‐cell responses in aged hosts, although improving the responses of PD‐1^? T cells may prove to be a helpful strategy in enhancing primary responses.     

Tumour cell‐intrinsic CTLA4 regulates PD‐L1 expression in non‐small cell lung cancer

Cytotoxic T lymphocyte antigen 4 (CTLA4) and programmed cell death protein 1 (PD‐1) are immune checkpoint proteins expressed in T cells. Although CTLA4 expression was found in multiple tumours including non‐small cell lung cancer (NSCLC) tissues and cells, its function in tumour cells is unknown. Recently, PD‐1 was found to be expressed in melanoma cells and to promote tumorigenesis. We found that CTLA4 was expressed in a subset of NSCLC cell lines and in a subgroup of cancer cells within the lung cancer tissues. We further found that in NSCLC cells, anti‐CTLA4 antibody can induce PD‐L1 expression, which is mediated by CTLA4 and the EGFR pathway involving phosphorylation of MEK and ERK. In CTLA4 knockout cells, EGFR knockout cells or in the presence of an EGFR tyrosine kinase inhibitor, anti‐CTLA4 antibody was not able to induce PD‐L1 expression in NSCLC cells. Moreover, anti‐CTLA4 antibody promoted NSCLC cell proliferation in vitro and tumour growth in vivo in the absence of adaptive immunity. These results suggest that tumour cell‐intrinsic CTLA4 can regulate PD‐L1 expression and cell proliferation, and that anti‐CTLA4 antibody, by binding to the tumour cell‐intrinsic CTLA4, may result in the activation of the EGFR pathway in cancer cells.     

A simple high-yielding process for transient gene expression in CHO cells

Here we describe a simplified method for transient gene expression (TGE) in suspension-adapted Chinese hamster ovary (CHO) cells using polyethylenimine (PEI) for DNA delivery. Both the transfection and production phases of the bioprocess were performed at a density of 4 × 10? cells/mL at 31 °C. In addition, the amounts of both PEI and plasmid DNA were reduced up to 50% on a per cell basis compared to previously published protocols from this laboratory, resulting in higher cell viability after transfection and higher volumetric recombinant protein yields. In batch cultures of up to 14 days, reproducible recombinant antibody yields up to 300 mg/L were achieved at small scale (5 mL) and up to 250 mg/L at large scale (500 mL). The simplicity and improved yields are expected to increase the utility of CHO cells for the rapid production of recombinant proteins at larger scales by TGE.     

IgG‐single chain Fv fusion protein therapeutic for alzheimer's disease: Expression in CHO cells and pharmacokinetics and brain delivery in the rhesus monkey

Monoclonal antibodies (MAb) directed against the Abeta amyloid peptide of Alzheimer's disease (AD) are potential new therapies for AD, since these antibodies disaggregate brain amyloid plaque. However, the MAb is not transported across the blood–brain barrier (BBB). To enable BBB transport, a single chain Fv (ScFv) antibody against the Abeta peptide of AD was re‐engineered as a fusion protein with the MAb against the human insulin receptor (HIR). The HIRMAb acts as a molecular Trojan horse to ferry the ScFv therapeutic antibody across the BBB. Chinese hamster ovary (CHO) cells were stably transfected with a tandem vector encoding the heavy and light chains of the HIRMAb–ScFv fusion protein. A high secreting line was isolated following methotrexate amplification and dilutional cloning. The HIRMAb–ScFv fusion protein in conditioned serum‐free medium was purified by protein A affinity chromatography. The fusion protein was stable as a liquid formulation, and retained high‐affinity binding of both the HIR and the Abeta amyloid peptide. The HIRMAb–ScFv fusion protein was radiolabeled with the ¹²⁵I‐Bolton–Hunter reagent, followed by measurement of the pharmacokinetics of plasma clearance and brain uptake in the adult Rhesus monkey. The HIRMAb–ScFv fusion protein was rapidly cleared from plasma and was transported across the primate BBB in vivo. In conclusion, the HIRMAb–ScFv fusion protein is a new class of antibody‐based therapeutic for AD that has been specifically engineered to cross the human BBB. Biotechnol. Bioeng. 2010; 105: 627–635. © 2009 Wiley Periodicals, Inc.     

High-density transient gene expression in suspension-adapted 293 EBNA1 cells

Large-scale transient gene expression (TGE) in mammalian cells is an attractive method to rapidly produce recombinant proteins for pre-clinical studies, with some processes reported to reach 100 L. However, the yield remains low, hardly over 20 mg protein/L, mainly because the current TGEs have been performed at low cell density (approximately 5 x 10(5) cells/mL). In this study, the strategy to improve TGE focuses on facilitating transfection at high cell density. A high-density perfusion culture of 293 EBNA1 cells was established in 2-L bioreactor using Freestyle 293 expression medium (Invitrogen, Singapore) to grow the cells for transfection. Transfection was then carried out at 1 x 10(7) cells/mL using polyethylenimine (PEI) as DNA carrier, at the optimized conditions of 6 microg DNA/10(7) cells and 1:3 DNA to PEI mass ratio. During the post-transfection phase, 80.8 mg/L of the model protein, EPO was obtained at day 5.5 post-transfection (130 mg total EPO production) using a fed-batch culture mode. In comparison, perfusion cultures using an enriched SFM II medium resulted in a longer post-transfection production phase (8 days), and 227 mg of EPO was produced in 10.7 L medium, showing that high-density TGE enables the production of several hundreds of milligrams of protein in a 2 L bioreactor. In addition, a protocol for economical plasmid preparation based on anion exchange was also established to satisfy TGE's demand in terms of quality and quantity. To the best of our knowledge, this is the first report of transient transfections at a high cell density of up to 1 x 10(7) cells/mL.