Wave Bioreactor Research Articles

Development and implementation of a perfusion‐based high cell density cell banking process

A perfusion-based high cell density (HD) cell banking process has been developed that offers substantial advantages in time savings and simplification of upstream unit operations. HD cell banking provides the means to reduce the time required for culture inoculum expansion and scale-up by eliminating the need for multiple small to intermediate scale shake flask-based operations saving up to 9 days of operation during large-scale inoculum expansion. HD perfusion cultures were developed and optimized in a disposable Wave bioreactor system. Through optimization of perfusion rate, rocking speed and aeration rate, the perfusion system supported peak cell densities of >20 × 10(6) cells/mL while maintaining high cell viability (≥ 90%). The cells were frozen at HD (90-100 × 10(6) viable cells/mL) in 5-mL CryoTube vials. HD cell banks were demonstrated to enable direct inoculation of culture into a Wave bioreactor in the inoculum expansion train thus eliminating the need for intermediate shake flask expansion unit operations. The simplicity of the disposable perfusion system and high quality of the cell banks resulted in the successful implementation in a 2000 L scale manufacturing facility.

A simplified polyethylenimine-mediated transfection process for large-scale and high-throughput applications

Transient gene expression in mammalian cells is a valuable alternative to stable cell lines for the rapid production of large amounts of recombinant proteins. While the establishment of stable cell lines takes 2–6months, milligram amounts of protein can be obtained within a week following transfection. The polycation polyethylenimine (PEI) is one of the most utilized reagents for small- to large-scale transfections as it is simple to use and, when combined with optimized expression vectors and cell lines, provides high transfection efficiency and titers. As with most transfection reagents, PEI-mediated transfection involves the formation of nanoparticles (polyplexes) which are obtained by its mixing with plasmid DNA. A short incubation period that allows polyplexes to reach their optimal size is performed prior to their addition to the culture. As the quality of polyplexes directly impacts transfection efficiency and productivity, their formation complicates scalability and automation of the process, especially when performed in large-scale bioreactors or small-scale high-throughput formats. To avoid variations in transfection efficiency and productivity that arise from polyplexes formation step, we have optimized the conditions for their creation directly in the culture by the consecutive addition of DNA and PEI. This simplified approach is directly transferable from suspension cultures grown in 6-well plates to shaker flasks and 5-L WAVE bioreactors. As it minimizes the number of steps and does not require an incubation period for polyplex formation, it is also suitable for automation using static cultures in 96-well plates. This “direct” transfection method thus provides a robust platform for both high-throughput expression and large-scale production of recombinant proteins.

Experimental characterization of flow conditions in 2‐ and 20‐l bioreactors with wave‐induced motion

Quantifying the influence of flow conditions on cell viability is essential for a successful control of cell growth and cell damage in major biotechnological applications, such as in recombinant protein and antibody production or vaccine manufacturing. In the last decade, new bioreactor types have been developed. In particular, bioreactors with wave-induced motion show interesting properties (e.g., disposable bags suitable for cGMP manufacturing, no requirement for cleaning and sterilization of cultivation vessels, and fast setup of new production lines) and are considered in this study. As an additional advantage, it is expected that cultivations in such bioreactors result in lower shear stress compared with conventional stirred tanks. As a consequence, cell damage would be reduced as cell viability is highly sensitive to hydrodynamic conditions. To check these assumptions, an experimental setup was developed to measure the most important flow parameters (liquid surface level, liquid velocity, and liquid and wall shear stress) in two cellbag sizes (2 and 20 L) of Wave Bioreactors®. The measurements confirm in particular low shear stress values in both cellbags, indicating favorable hydrodynamic conditions for cell cultivation.

Large-scale bioreactor expansion of tumor-infiltrating lymphocytes

Background The aim of this study was to evaluate an improved technique for expansion of tumor-infiltrating lymphocytes (TILs) based on the WAVE Bioreactor system with perfusion and tube-welding techniques. Our hypothesis was that the bioreactor would allow for optimized provision of nutrients and removal of spent media while minimizing culture volumes. These refinements might lead to a better quality of expanded cells with lower amounts of exhausted cells compared to static expansions in culture bags. Procedures Tumor-infiltrating lymphocytes from 4 melanoma patients were expanded and compared in parallel using either the WAVE Bioreactor 2/10 System or traditional static culture methods. The parameters viability, final cell number, phenotype and effector function were measured. Results Our results show that the bioreactor system with perfusion is suitable for large-scale expansion of tumor-infiltrating lymphocytes and allows for higher cell densities and absolute cell numbers as compared to static culture conditions. Phenotypic characteristics of TILs were compared pre and post expansion and showed no consistent difference between the two expansion methods. TILs harvested had the phenotype and function corresponding to intermediate to late effector cells. The system allows one technician to operate several bioreactors simultaneously, thereby reducing the labor for one expansion to approximately 1/3 compared to static expansion. Discussion The WAVE Bioreactor system is suitable for large-scale expansion of TILs. Due to constant perfusion of fresh media and removal of spent media much higher cell densities were achieved while the culture volume and the glucose and glutamine levels were kept constant. Expansion of TILs in the bioreactor system represents a labor- and cost-effective method to reach large numbers of T cells for adoptive cell transfer therapy in the clinic. Conclusion The system presented herein offers an effective alternative to large-scale production of cell products for clinical use while meeting requirements of therapeutic cell quantities and qualities of current protocols for treatment of malignant melanoma.

A new MDCK suspension line cultivated in a fully defined medium in stirred-tank and wave bioreactor

An adherently growing MDCK cell line was adapted in a two-step process in a fully defined medium and in suspension. The resulting MDCK.SUS2 cells were subsequently evaluated for their potential as host cells for influenza vaccine production in two lab-scale bioreactors (wave and stirred-tank). Cell concentrations up to 2.3 × 10 6 cells/mL were obtained after 96 h, which is slightly higher than cell concentrations obtained with adherent MDCK cells cultivated on microcarriers (2 g/L). Infections with influenza A/PR/8/34 and B/Malaysia resulted in high virus titers (2.90 and 2.75 log HA units/100 μL, respectively). The monitoring of extracellular metabolites, including amino acids, revealed a change in some of the metabolite consumption or release profiles, which indicates changes in metabolism during the adaptation process. Overall, the MDCK.SUS2 cell line represents a new cell substrate for a robust influenza vaccine production in a fully defined process.

Use of disposable reactors to generate inoculum cultures for E. coli production fermentations

Disposable technology is being used more each year in the biotechnology industry. Disposable bioreactors allow one to avoid expenses associated with cleaning, assembly and operations, as well as equipment validation. The WAVE bioreactor is well established for Chinese Hamster Ovary (CHO) production, however, it has not yet been thoroughly tested for E. coli production because of the high oxygen demand and temperature maintenance requirements of that platform. The objective of this study is to establish a robust process to generate inoculum for E. coli production fermentations in a WAVE bioreactor. We opted not to evaluate the WAVE system for production cultures because of the high cell densities required in our current E. coli production processes. Instead, the WAVE bioreactor 20/50 system was evaluated at laboratory scale (10-L) to generate inoculum with target optical densities (OD(550)) of 15 within 7-9 h (pre-established target for stainless steel fermentors). The maximum settings for rock rate (40 rpm) and angle (10.5) were used to maximize mass transfer. The gas feed was also supplemented with additional oxygen to meet the high respiratory demand of the culture. The results showed that the growth profiles for the inoculum cultures were similar to those obtained from conventional stainless steel fermentors. These inoculum cultures were subsequently inoculated into 10-L working volume stainless steel fermentors to evaluate the inocula performance of two different production systems during recombinant protein production. The results of these production cultures using WAVE inocula showed that the growth and recombinant protein production was comparable to the control data set. Furthermore, an economic analysis showed that the WAVE system would require less capital investment for installation and operating expenses would be less than traditional stainless steel systems.

Recent advances in bioreactor engineering

A bioreactor is the core of biological processes. To design an appropriate bioreactor system for a particular bioprocess, intensive studies on the biological system, such as cell growth, metabolism, genetic manipulation, and protein or other product expression are needed to understand the cells’ requirement on their physical and chemical environments. It is also necessary to control and optimize the bioreactor environment via operating variables in order to favor the desired functions of cells and achieve cost-effective large-scale manufacture. This article briefly describes fundamental design principles and new types of bioreactors such as centrifugal impeller and wave bioreactors. Bioreactor operation factors and modes including mixing, oxygen supply, shear force, fed-batch, and perfusion cultures are discussed. The trends in bioreactor engineering are also briefly shown.

Characterization of flow conditions in 2 L and 20 L wave bioreactors® using computational fluid dynamics

Characterization of flow conditions is of great importance to control cell growth and cell damage in animal cell culture because cell viability is influenced by the flow properties in bioreactors. Alternative reactor types like Wave Bioreactors have been proposed in recent years, leading to markedly different results in cell growth and product formation. An advantage of Wave Bioreactors is the disposability of the Polyethylenterephthalet-bags after one single use (fast setup of new production facilities). Another expected advantage is a lower shear stress compared to classical stirred-tank reactors, due to the gentle liquid motion in the rocking cellbag. This property would considerably reduce possible cell damage. The purpose of the present study is to investigate in a quantitative manner the key flow properties in Wave Bioreactors, both numerically and experimentally. To describe accurately flow conditions and shear stress in Wave Bioreactors using numerical simulations, it is necessary to compute the unsteady flow applying Computational Fluid Dynamics (CFD). Corresponding computations for two reactor scales (2 L and 20 L cellbags) are presented using the CFD code ANSYS-FLUENT. To describe correctly the free liquid surface, the present simulations employ the Volume of Fluid (VOF) method. Additionally, experimental measurements have been carried out to determine liquid level, flow velocity and liquid shear stress, which are used as a validation of the present CFD simulations. It is shown that the obtained flows stay in the laminar regime. Furthermore, the obtained shear stress levels are well below known threshold values leading to damage of animal cells.

New avian suspension cell lines provide production of influenza virus and MVA in serum-free media: Studies on growth, metabolism and virus propagation

Few suspension cells can be used for vaccine manufacturing today as they either do not meet requirements from health regulatory authorities or do not produce high virus titres. Two new avian designer cell lines (AGE1.CR and AGE1.CR.pIX) that have been adapted to grow in suspension in serum-free medium were evaluated for their potential as host cells for influenza and modified vaccinia Ankara (MVA, wild type) vaccine production. Their metabolism was studied during growth in static (T-flasks) and dynamic cultivation systems (roller bottles, stirred tank reactor, wave bioreactor). High cell concentrations up to 5.8×106cells/mL were obtained with doubling times of 23h for AGE1.CR and 35h for AGE1.CR.pIX, respectively. Both viruses were produced to high titres (3.5 logHA/100μL for influenza virus, 3.2×108pfu/mL for MVA). Hence, the CR cell lines are an appropriate substrate for pharmaceutical influenza and MVA production.

High‐level protein expression in scalable CHO transient transfection

Chinese hamster ovary cells (CHO) have been extensively utilized as the production platform for therapeutic proteins including monoclonal antibodies in pharmaceutical industry. For early development, it would be advantageous to rapidly produce large amounts of protein in the same cell line; therefore, development of a CHO transient transfection platform with high protein expression level is highly desirable. Here, we describe the development of such a platform in CHO cells. Polyethylenimine (PEI) was used as the transfection reagent. Different media were screened for the best transfection and expression performance, and UltraCHO was chosen as the best performer. DMSO and lithium acetate (LiAc) were discovered to improve CHO transient transfection expression levels significantly. A 14-day fed-batch process was successfully developed to further increase production yield. With an optimized transient transfection process, we were able to express monoclonal antibody (Mab) in CHO cells at a high level, averaging 80 mg/L. The process was successfully scaled up to 10 L working volume in a 20 L wave bioreactor. As expected, the Mabs had similar glycosylation patterns in comparison to the Mabs produced from a stably transfected CHO cell line, while in contrast Mabs expressed transiently from HEK293EBNA cells differed.

Manufacturing validation of biologically functional T cells targeted to CD19 antigen for autologous adoptive cell therapy.

On the basis of promising preclinical data demonstrating the eradication of systemic B-cell malignancies by CD19-targeted T lymphocytes in vivo in severe combined immunodeficient-beige mouse models, we are launching phase I clinical trials in patients with chronic lymphocytic leukemia (CLL) and acute lymphoblastic leukemia. We present here the validation of the bioprocess which we developed for the production and expansion of clinical grade autologous T cells derived from patients with CLL. We demonstrate that T cells genetically modified with a replication-defective gammaretroviral vector derived from the Moloney murine leukemia virus encoding a chimeric antigen receptor (CAR) targeted to CD19 (1928z) can be expanded with Dynabeads CD3/CD28. This bioprocess allows us to generate clinical doses of 1928z+ T cells in approximately 2 to 3 weeks in a large-scale semiclosed culture system using the Wave Bioreactor. These 1928z+ T cells remain biologically functional not only in vitro but also in severe combined immunodeficient-beige mice bearing disseminated tumors. The validation requirements in terms of T-cell expansion, T-cell transduction with the 1928z CAR, biologic activity, quality control testing, and release criteria were met for all 4 validation runs using apheresis products from patients with CLL. Additionally, after expansion of the T cells, the diversity of the skewed Vbeta T-cell receptor repertoire was significantly restored. This validated process will be used in phase I clinical trials in patients with chemorefractory CLL and in patients with relapsed acute lymphoblastic leukemia. It can also be adapted for other clinical trials involving the expansion and transduction of patient or donor T cells using any CAR or T-cell receptor.

Functional cross‐kingdom conservation of mammalian and moss (Physcomitrella patens) transcription, translation and secretion machineries

Plants and mammals are separated by a huge evolutionary distance. Consequently, biotechnology and genetics have traditionally been divided into 'green' and 'red'. Here, we provide comprehensive evidence that key components of the mammalian transcription, translation and secretion machineries are functional in the model plant Physcomitrella patens. Cross-kingdom compatibility of different expression modalities originally designed for mammalian cells, such as native and synthetic promoters and polyadenylation sites, viral and cellular internal ribosome entry sites, secretion signal peptides and secreted product proteins, and synthetic transactivators and transrepressors, was established. This mammalian expression portfolio enabled constitutive, conditional and autoregulated expression of different product genes in a multicistronic expression format, optionally adjusted by various trigger molecules, such as butyrolactones, macrolide antibiotics and ethanol. Capitalizing on a cross-kingdom-compatible expression platform, we pioneered a prototype biopharmaceutical manufacturing scenario using microencapsulated transgenic P. patens protoplasts cultivated in a Wave Bioreactor. Vascular endothelial growth factor 121 (VEGF(121)) titres matched those typically achieved by standard protonema populations grown in stirred-tank bioreactors. The full compatibility of mammalian expression systems in P. patens further promotes the use of moss as a cost-effective alternative for the manufacture of complex biopharmaceuticals, and as a valuable host system to advance synthetic biology in plants.

Production of High Titer cGMP-Grade SIN Gamma-Retroviral Vectors by Transfection in a Closed System Bioreactor

The need for gamma-retroviral vectors with self-inactivating (SIN) long terminal repeats for clinical trials has prompted a shift in the method with which large scale GMP-grade vectors are produced, from the use of stable producer lines to transient transfection-based techniques. The main challenge of instituting this methodology was to develop SIN retrovirus vectors that produced high amounts of genomic vector RNA in packaging cells, and to design scalable processes for closed system culture, transfection and virus harvest. Using improved expression plasmids, the Vector Production Facility, an academic GMP manufacturing laboratory that is part of the Translational Cores at Cincinnati Children's Hospital, has developed such a method based on the Wave Bioreactor® production platform. In brief, cells from a certified 293T master cell bank are expanded, mixed with transfection reagents, and pumped into a 2, 10 or 20 Liter Wave Cell Bag containing FibraCel® discs. Cells are cultured in DMEM with GlutaMax® and 10% FBS at 37°C, 5% CO2 at a rocking speed of 22 rpm and 6° angle. At 16–20 hrs post-transfection, the media is changed; virus is harvested at 12-hour intervals, filtered through a leukocyte reduction filter, aliquoted into Cryocyte freezing containers, and frozen at or below −70°C. Several processing parameters, including the confluency of cells harvested prior to transfection, the timing of transfection, the amount of plasmid DNA, exposure of cells to PBS/TrypLESelect, and the timing of the media change post-transfection affected vector titer. Mixing cells with plasmid and transfection mixture prior to seeding onto FibraCel, as compared to transfecting cells 1-day post-seeding (as is standard when using tissue culture plastic) increased the titer from 104 to 4 × 105 IU/mL. Similarly, increasing the amount of plasmid DNA per mL from 4.6 to 9.2 μg doubled the titer in the Wave, while it reduced titer by 20–40% in tissue culture flasks (Fig. 1). Using an optimized protocol, six cGMP-grade SIN gamma-retroviral vectors have now been produced in support of the FDA's National Toxicology Program (NTP), with unconcentrated vector titers ranging from 1 × 106 to as high as 4 × 107 IU/mL. Using similar processing, we have produced a large scale SIN gamma-retroviral vector (GALV pseudotyped) for an international X-linked SCID trial with average unconcentrated titers of 106 IU/mL in all viral harvests. In summary, the process developed at the Cincinnati Children's Hospital Vector Production Facility allows for large scale closed-system production of high-titer retroviral vectors for clinical trials using transient transfection. [Display omitted]

Growth and metabolic characteristics of CCO cells in static and dynamic cultivation systems

The cultivation of animal cells is of great importance for effective and reasonable bioprocess production of various therapeutic proteins as well as for fundamental laboratory research. The metabolic patterns of animal cells are altered substantially during the actions of establishment of a typical cell line designed for in vitro techniques. Therefore, characterization and understanding of cell metabolism are needed to improve the processes with cultivated animal cells. The channel catfish ovary cell line (CCO) was derived from the ovaries of a juvenile channel catfish some thirty years ago. Since then, it has been used for channel catfish virus vaccine production and related in vitro laboratory research. However there is still no enough data for basal understanding of their metabolism. We report on growth characteristics of CCO cells cultivated in multiwell plates and Wave bioreactor. Specific growth rate of CCO cells in multiwell plates was 0, 0206 h-1. The concentration of glucose in culture media remained unchanged through whole cultivation period. Glutamine was almost completely depleted and ammonia, its major wasteproduct, reached concentration of 2, 3 mM. Amino acid analysis of culture media showed that highly consumed amino acids, besides glutamine, were arginine, serine, and threonine, suggesting that they were main energy source. Cytodex 1 microcarriers were used in order to investigate medium-scale cultivation parameters of CCO cells in the Wave bioreactor. In this cultivation system oxygen transfer and mixing are accomplished by the wave-induced agitation. Micocarrier confluence was reached with cell density of 1, 8 x 10e6 cells/mL and cell growth rate of 0, 0182 h-1. The results proved the feasibility of employed culture conditions for cultivation of CCO cells.

280. Large Scale Purification of CD4+ T Cells by Negative or Positive Selection Methods Does Not Affect Their Growth in Wave Bioreactor or Their Engraftment Potential as Tested in Immunodeficient NOD/LtSz-Rag1null Mice

280. Large Scale Purification of CD4+ T Cells by Negative or Positive Selection Methods Does Not Affect Their Growth in Wave Bioreactor or Their Engraftment Potential as Tested in Immunodeficient NOD/LtSz-Rag1null Mice

Production of a recombinant industrial protein using barley cell cultures

The use of recombinant DNA-based protein production using genetically modified plants could provide a reproducible, consistent quality, safe, animal-component free, origin-traceable, and cost-effective source for industrial proteins required in large amounts (1000s of metric tons) and at low cost (below US$100/Kg). The aim of this work was to demonstrate the feasibility of using barley suspension cell culture to support timely testing of the genetic constructs and early product characterization to detect for example post-translational modifications within the industrial protein caused by the selected recombinant system. For this study the human Collagen I alpha 1 (CIa1) chain gene encoding the complete helical region of CIa1 optimized for monocot expression was fused to its N- and C-terminal telopeptide and to a bacteriophage T4 fibritin foldon peptide encoding sequences. The CIa1 accumulation was targeted to the endoplasmic reticulum (ER) by fusing the CIa1 gene to an ER-directing signal peptide sequence and an ER retention signal HDEL. The construct containing the CIa1 gene was then introduced into immature barley half embryos or barley cells by particle bombardment. Transgenic barley cells resulting from these transformations were grown as suspension cultures in flasks and in a Wave bioreactor producing CIa1 similar to CIa1 purified from the yeast Pichia pastoris based on Western blotting, pepsin resistance, and mass spectroscopy analysis. The barley cell culture derived-CIa1 intracellular accumulation levels ranged from 2 to 9 μg/l illustrating the need for further process improvement in order to use this technology to supply material for product development activities.

Production of selenomethionyl‐derivatized proteins in baculovirus‐infected insect cells

A protocol is described for the production of both intracellularly expressed and secreted selenomethionyl-derivatized recombinant proteins in baculovirus-infected insect cells. The method results in the production of recombinant soluble proteins with an SeMet occupancy of approximately 75% and with a recovery of approximately 20% that of native protein expression. The method is independent of the percentage methionine content of the protein and is reliable and consistent. Similar results are obtained using either Spodoptera frugiperda Sf9 or Trichoplusia ni High Five insect cells as the expression host, and when cultures are grown in either shake flasks or in Wave BioReactors.

Evaluation of a novel Wave Bioreactor® cellbag for aerobic yeast cultivation

The Wave Bioreactor is widely used in cell culture due to the benefits of disposable technology and ease of use. A novel cellbag was developed featuring a frit sparger to increase the system's oxygen transfer. The purpose of this work was to evaluate the sparged cellbag for yeast cultivation. Oxygen mass transfer studies were conducted in simulated culture medium and the sparged system's maximum oxygen mass transfer coefficient (kLa) was 38 h(-1). These measurements revealed that the sparger was ineffective in increasing the oxygen transfer capacity. Cultures of Saccharomyces cerevisiae were successfully grown in oxygen-blended sparged and oxygen-blended standard cellbags. Under steady state conditions for both cellbag designs, kLa values as high as 60 h(-1) were obtained with no difference in growth characteristics. This is the first report of a successful cultivation of a microbe in a Wave Bioreactor comparing conventional seed expansion in shake flasks and stirred tank bioreactors.

Cholesterol delivery to NS0 cells: Challenges and solutions in disposable linear low-density polyethylene-based bioreactors

We report the successful cultivation of cholesterol dependent NS0 cells in linear low-density polyethylene (LLDPE) Wave Bioreactors when employing a low ratio of cyclodextrin to cholesterol additive mixture. While cultivation of NS0 cells in Wave Bioreactors was successful when using a culture medium supplemented with fetal bovine serum (FBS), cultivation with the same culture medium supplemented with cholesterol-lipid concentrate (CLC), which contains lipids and synthetic cholesterol coupled with the carrier methyl-beta-cyclodextrin (mbetaCD), proved to be problematic. However, it was possible to cultivate NS0 cells in the medium supplemented with CLC when using conventional cultivation vessels such as disposable polycarbonate shake-flasks and glass bioreactors. A series of experiments investigating the effect of the physical conditions in Wave Bioreactors (e.g., rocking rate/angle, gas delivery mode) ruled out their likely influence, while the exposure of the cells to small squares of Wave Bioreactor film resulted in a lack of growth as in the Wave Bioreactor, suggesting an interaction between the cells, the CLC, and the LLDPE contact surface. Further experiments with both cholesterol-independent and cholesterol-dependent NS0 cells established that the concurrent presence of mbetaCD in the culture medium and the LLDPE film was sufficient to inhibit growth for both cell types. By reducing the excess mbetaCD added to the culture medium, it was possible to successfully cultivate cholesterol-dependent NS0 cells in Wave Bioreactors using a cholesterol-mbetaCD complex as the sole source of exogenous cholesterol. We propose that the mechanism of growth inhibition involves the extraction of cholesterol from cell membranes by the excess mbetaCD in the medium, followed with the irreversible adsorption or entrapment of the cholesterol-mbetaCD complexes to the LLDPE surface of the Wave Bioreactor. Controlling and mitigating these negative interactions enabled the routine utilization of disposable bioreactors for the cultivation of cholesterol-dependent NS0 cell lines in conjunction with an animal component-free cultivation medium.

Perfusion Culture of Hybridoma Cells for Hyperproduction of IgG2a Monoclonal Antibody in a Wave Bioreactor‐Perfusion Culture System

A novel wave bioreactor-perfusion culture system was developed for highly efficient production of monoclonal antibody IgG2a (mAb) by hybridoma cells. The system consists of a wave bioreactor, a floating membrane cell-retention filter, and a weight-based perfusion controller. A polyethylene membrane filter with a pore size of 7 microm was floating on the surface of the culture broth for cell retention, eliminating the need for traditional pump around flow loops and external cell separators. A weight-based perfusion controller was designed to balance the medium renewal rate and the harvest rate during perfusion culture. BD Cell mAb Medium (BD Biosciences, CA) was identified to be the optimal basal medium for mAb production during batch culture. A control strategy for perfusion rate (volume of fresh medium/working volume of reactor/day, vvd) was identified as a key factor affecting cell growth and mAb accumulation during perfusion culture, and the optimal control strategy was increasing perfusion rate by 0.15 vvd per day. Average specific mAb production rate was linearly corrected with increasing perfusion rate within the range of investigation. The maximum viable cell density reached 22.3 x 105 and 200.5 x 105 cells/mL in the batch and perfusion culture, respectively, while the corresponding maximum mAb concentration reached 182.4 and 463.6 mg/L and the corresponding maximum total mAb amount was 182.4 and 1406.5 mg, respectively. Not only the yield of viable cell per liter of medium (32.9 x 105 cells/mL per liter medium) and the mAb yield per liter of medium (230.6 mg/L medium) but also the mAb volumetric productivity (33.1 mg/L.day) in perfusion culture were much higher than those (i.e., 22.3 x 105 cells/mL per liter medium, 182.4 mg/L medium, and 20.3 mg/L.day) in batch culture. Relatively fast cell growth and the perfusion culture approach warrant that high biomass and mAb productivity may be obtained in such a novel perfusion culture system (1 L working volume), which offers an alternative approach for producing gram quantity of proteins from industrial cell lines in a liter-size cell culture. The fundamental information obtained in this study may be useful for perfusion culture of hybridoma cells on a large scale.