How Multipurpose is a Disposable Bioreactor?

March 1, 2011

BioPharm International

Volume 24, Issue 3

The authors discuss the use of single-use bioreactors.

ABSTRACT

For almost 40 years, bioprocess engineers have been indoctrinated with the technology of the stirred tank bioreactor. But many have concluded that a plastic bag can be effective and that the results achieved with cultures in a single-use bioreactor are comparable with the results achieved in the glass or stainless-steel stirred tank bioreactor. This article describes experiments performed in the bag type single-use bioreactor that suggest it can yield results that are comparable with those as achieved in the traditional stirred tank bioreactor.

An increasing number of therapeutic candidates, including monoclonal antibodies, biotherapeutic proteins, and vaccines, are currently entering early-stage process development. At the same time, biologics are being introduced onto the market or have recently been introduced. In this competitive market, time-to-market, cost-effectiveness, and manufacturing flexibility are key issues that all must be achieved while maintaining product quality.

Traditionally stirred tanks, glass vessels, and stainless steel tanks have been used at laboratory and pilot scales for process development and production of research grade, toxicological, and Phase I clinical material. Stainless steel tanks dominate large-scale manufacture (> 1000L) of bio-therapeutics. However, fixed plant equipment is costly, requiring long lead times for installation and qualification. There is also a high burden from validation efforts related to sterility and cleaning, as well as for maintenance. The risk for cross contamination in standard steel or glass equipment leads to strict rules for cleaning and cleaning validation.

During the past decade, industry has been switching to disposables in medium preparation, storage of buffers, and even for cell culturing and downstream operations. For cell culture, various types of disposable technologies have been introduced, all with specific benefits and drawbacks.

Advanced cell-line engineering and process development have resulted in more productive cell cultures. During the past 15 years, cellculture titers in fed-batch processes have increased from 0.05 to over 10 gL-1 today, allowing the use of smaller scale bioreactors.

Smaller bioreactors are gaining popularity, and this again has led to increased implementation of disposable technologies. While the industry is looking for high cell densities, high productivity, cost-effective process design, and speed to reach market introduction, the bioreactor demands are increasing, too. This is especially relevant for mixing and mass transfer but also for measuring and control of essential parameters, such as pH, dissolved oxygen (DO), glucose, lactate, and viable cell density.

High-cell density culture—including perfusion cultures—generate greater demands with regard to mixing and mass transfer. Microbial fermentation processes are even more demanding in terms of mass transfer when compared with a cell culture process. The currently available disposable bioreactor systems are less suitable for high-density cell culture processes and are not suitable for microbial fermentation processes. The exception here is the CELL-tainer bioreactor (CeLLution Biotech, Assen Netherlands). The performance of this bioreactor is comparable with the stirred tank and thus covers the complete range of applications from cell culture to microbial fermentations, from adherent cell cultures to more viscous fungal fermentations. This article will discuss a rocking-based disposable bioreactor that can be used in a wide range of biotechnological processes.

TYPES OF SINGLE USE BIOREACTORS WITH DISPOSABLE BAGS

One of the keys to properly using single-use bioreactors is the application of disposable bags available with or without integrated sensors and equipped with connections for feed, inoculums, sampling, and with gas inlet and exhaust gas filters. These bags are pre-sterilized using gamma irradiation, ensuring full sterility.

One of the challenges for using these presterilized bags is to ensure proper mixing, mass- and heat transfer, and proper process measurement and control. This all should be comparable with traditional stirred bioreactors.

To prevent oxygen limitation, a high-demanding cell-culture process requires an oxygen mass transfer capacity of 10 mmol/L.hr when 50 x 106 cells/mL are cultivated. This translates to a required k|a = 50 hr-1. For microbial systems, like an E. coli fermentation at 50 g/L dry cell weight, the required mass transfer capacity has to be 200 mmol/L.hr or even higher, meaning a k|a > 800 hr-1 using air.

Single-use bioreactors are commercially available at various scales from the laboratory scale and pilot scale (1-100 L) up to even production scale (1000 – 2000 L). The application, however, is primarily restricted to mammalian cell culture processes. (see Table I.)

Table I: Overview of commercially available disposable bioreactors.

Rocking type bioreactors

The rocking type bioreactor ensures easy operation due to its simple construction and handling. Mixing profiles might be different from stirred bioreactors; however, as the microenvironment of the cell determines the physiological status of the cell, the cells seem to do fine as long as there are no gradients of temperature, oxygen, or CO2. When the presence of nutrients is assured and the pH is acceptable, the cells "do not care" in what type of bioreactor they are cultured. The challenge is to ensure proper micromixing and mass transfer and to avoid gradients.

The Wave Bioreactor

The Wave Bioreactor consists of a disposable bag, which contains the cells and media and is placed on a heated rocker (Figure 1) (1). Headspace aeration is used to inflate the "cellbag", and a rocking motion should create mixing. Gas liquid mass transfer occurs via the liquid-gas surface.

Figure 1. Wave Bioreactor example. (COURTESY: GENENTECH INC.)

DO and pH might be measured using optical probes. Gas blending to maintain DO and pH is supplied using mass flow controllers and integrated controllers.

The k|a is 10 - 30 hr-1 as reported by various authors (2). Mixing times are in the order of magnitude of 2 – 3 minutes for scales up to 100 L. The mixing time increases up to 5 minutes, especially at lower rocking speeds (< 20 rpm) or at larger scales (> 100 L). From a simple regime analysis, one may conclude that the Wave type bioreactors are working in a so-called mixed regime where mixing time and mass transfer are in the same order of magnitude, possibly leading to gradients of oxygen and CO2. Scalability of this system is not obvious as demonstrated by Eibl and Eibl (3). The literature suggests that the Wave Bioreactor is not suited for mimicking the cultivation conditions of stirred bioreactors for microbial culture conditions.

A number of similar wave-like systems, operating on similar principles, have been introduced, including those from Sartorius (Cultibag) and Applikon (AppliFlex).

UNDERSTANDING THE CELL-TAINER BIOREACTOR

The CELL-tainer technology (see Figure 2) is based on a 2D rocking motion and application of a pillow-shaped or rectangular three-dimensional bag. Due to the two-dimensional rocking motion (in vertical and horizontal direction at the same time), the mass transfer is much higher when compared with other rocking systems (4).

Figure 2. CELL-tainer single use bioreactor. (COURTESY: HAN BIOCENTRE)

High mass transfer has the potential of supporting higher cell densities, better stripping capacity of CO2, cell culture application as well as application in microbial and fungal fermentation. Besides improvement of the mass transfer, this bioreactor offers a removable segmentation of the bags, which makes it possible to start at volumes as low as 200-250mL and expand the culture in one-and-the-same bag up to working volumes of 15 L. The sensors, including an electrochemical sensor for pH and a polarographic sensor for DO—both in a disposable format—are mounted in the bottom of the bag and positioned in small cups, which guarantees proper process control even with low volumes under shaking conditions. Because traditional sensor technology is used, the range of measurement for pH is not restricted (pH: 0–14) as it is with optical sensors (pH: 6.5–8.0).

Temperature control of the bioreactor bag is located inside the incubator cabinet and by convection. No heating blanket is applied. When heat is generated by the culture, (e.g., with microbial fermentation, cooling is required). The CELL-tainer is equipped with an integrated cooling plate in the rocking platform. Using a temperature difference of 25 °C, the cooling capacity is 500W, which is sufficient for a high density E. coli culture.

Investigation of the mass transfer, shows that the CELL-tainer covers a wide range of mass transfer values (see Figure 3). This is far beyond the capabilities of the traditional rocking type of bioreactors.

Figure 3. Mass transfer in a CELL-tainer bioreactor (tap water, 20 °C) (Data CELLution Biotech) compared to the Wave Bioreactor.

In most mammalian cultures, the mass transfer for oxygen seems to be sufficient to support high cell densities, at least in the stirred bioreactors. To enhance oxygen transfer, stirred bioreactor (micro-) spargers are applied and air may be enriched with oxygen. In both stirred and wave type single-use bioreactors, the exchange of CO2 might be limited due to a lower mass transfer coefficient and due to limitations in stripping efficiency. As the mass transfer coefficient in the CELL-tainer bioreactor is much higher than in wave type and stirred single-use bioreactors, the liquid phase CO2 concentration is always in equilibrium with the gas phase CO2 concentration. This results in less CO2 build-up in the liquid phase, which results in reduced alkaline addition, and which benefits the culture as a whole.

The mass transfer that can be achieved in the CELL-tainer bioreactor is significantly higher (k|a > 300 hr-1) than that seen in the wave type bioreactors and that therefore opens the application of single-use equipment for microbial fermentations as well.

MICROBIAL ERMENTATION IN THE CELL-TAINER BIOREACTOR

Interest in microbial expression systems such as E. coli and Pichia pastoris, is increasing. That's the case not only for traditional products such as enzymes but also for production of biopharmaceuticals and the manufacturing of platform chemicals. Bulk fermentation products are produced on large scales of up to 400 – 800 m3 in stirred bioreactors, but for screening and pre-culture purposes, the single-use bioreactors offer the advantage of fast turnaround, speed in early stage development, and late stage development (scale-down experiments). The limited infrastructure required (no autoclaves or SIP/CIP) is also a key advantage for single-use equipment.

Figure 4 shows microbial culture in a 10L fed-batch performed in the CELL-tainer single-use bioreactor. The profile shows results that are comparable with those seen in stirred fermentors up to 100 L working volumes (5).

Figure 4. Cultivation of E.coli in a 10 L fed-batch in the CELL-tainer bioreactor. OD550 = biomass concentration in optical density units measured at 550 nm.

In addition to the pH and DO sensor, a device for measuring glucose and lactate is available, using the Trace Analytics (www.trace.de) technology of a dialysis membrane. The dialysis membrane is integrated in the bottom of the bag, comparable to the pH and DO sensors. The device is an integrated part of the gamma-irradiated bag (see figure 5).

Figure 5. Single-use dialysis membrane. (COURTESY: TRACE ANALYTICS GMBH/CELLUTION BIOTECH BV.)

In an E. coli fermentation, using glucose as substrate, online and offline data are compared (see figure 6). There is only a slight, negligible discrepancy between on-line and off-line data. The off-line data are based on an enzymatic method in collected samples using an autosampler. The discrepancy is easy to explain: the off-line data show lower values because of the metabolic activity that continues after a sample till analysis takes place (2–5 minutes before the sample is –5 °C). The online measurements are highly accurate because there is continuous equilibrium between the culture and the cell-free dialysate. The ability of online measurement of an important parameter such as glucose (and lactate) offers the possibility to develop advanced on-line control strategies, thus making the single-use bioreactor increasingly suitable for process development.

Figure 6. Comparison of in-line and on-line glucose measurement in an E.coli culture using the ContiTRACE dialysis membrane plug integrated in the CELL-tainer.

COST COMPARISON

Single-use bioreactors offer the advantage of fast installation, lower investments in infrastructure, and a significant decrease of validation costs. Similarly a comparison of operational costs of a 5-day microbial process as performed in a 15L autoclavable, in a 15L SIP bioreactor, versus the process in the single-use CELL-tainer, reveals significantly lower costs in the single-use system per run (see figure 7). This includes the costs of bags (fully equipped with sensors). Because the single use CELL-tainer bioreactor has a fast turnaround time, in the same bioreactor system, 40% more runs/year can be made, when compared to an autoclavable fermenter.

Figure 7. Relative operational cost comparison of 15-L bioreactors of different types.

CONCLUSION

Single-use bioreactors have become accepted by industry and academic laboratories because of ease of use, flexibility, cost of operation, and lower investments. The CELL-tainer single-use bioreactor system can be used in a wide variety of applications: intensive cell cultures, fragile cultivation systems like with micro-carriers and hybridoma cultures, and also in microbial fermentations (e.g. yeast and fungal cultures) due to its ability to deliver proper mixing and high mass transfer. Because the system is equipped with advanced process control, which could include in-line analysis of glucose and lactate, the CELL-tainer widens the application of single-use bioreactors even to traditional biotechnology processes as a process development tool or as pre-culture system.

ACKNOWLEDGMENT

The authors would like to thank Nick van Biezen and Jeroen Schouwenberg (HAN Biocenter, Nijmegen, The Netherlands) and Anton Tromper (CELLution Biotech) for their contribution in the E.coli cultivation work.

Dr. Nico M.G. Oosterhuis is CTO/CSO at CeLLution Biotech, Assen, The Netherlands (nico.oosterhuis@cellutionbiotech.com). Hans J. van den Berg is an independent business developer.

REFERENCES

1. V. Singh, Disposable bioreactor for cell culture using wave-induced agitation, Cytotechnology, 30: 149-158 (1999).

2. J. Simola, Characterization of WAVE Bioreactor to scale-up mAb cell culture process from 10L to 100L, Esact Conference Proceedings, 2009.

3. R. Eibl, D. Eibl. "Design and use of the Wave Bioreactor for plant cell culture," in Plant Tissue Culture Engineering, G.S. Dutta and Y. Ibaraki, Eds. (Springer, New York, NY, 2006).

4. P. Van der Heiden, M. Buevink, N.M.G. Oosterhuis WO 2007/001173 A2 (2007).

5. L.L. Weng, Strategies for accelerated development of microbial fermentation processes (Boston, November 2009).