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Improving Stem Cell Cultivation in Bioreactors

Bioreactor in a laboratory.
Credit: Eppendorf

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Cultivating quality cells is a key requirement for innovative approaches in regenerative medicine. Stirred-tank bioreactors are promising cultivation systems for the cultivation and differentiation of human induced pluripotent stem cells (hiPSCs), as they have the capacity to produce high cell numbers, allowing scale-up, and cutting-edge opportunities for improving the control of growth parameters. Increasing cell density is a vital component of research in stem cell bioprocessing.


In this interview, Sebastian Selzer, strategic portfolio manager bioprocess at the Eppendorf Bioprocess Center, talks about the advantages of cell culture in stirred-tank bioreactors. Dr. Robert Zweigerdt from Hannover Medical School, Germany explains how his team reached a culture yield of 35 million hiPSCs per mL.

 

Eppendorf: Therapeutic application needs high cell numbers and therefore large culture volumes. What are the advantages of 3D cultures in stirred-tank bioreactors compared to plates and flasks?


Sebastian Selzer: Stirred-tank bioreactors are the current gold standard for biopharmaceutical manufacturing. There are very well established, and researchers can profit from a lot of literature. Bioreactors allow the creation of a controlled environment to provide optimal conditions for cell growth or differentiation. Identification of critical process parameters and definition of critical quality attributes are required for regulatory approval. Furthermore, the scalability of stirred-tank bioreactors simplifies the transition from small to larger scale. One of the biggest advantages I see in the reduction of manual labor. This removes the human error more and more, which is crucial for a safe therapy.

 

Eppendorf: How easy is it to move from a static to a stirred-tank culture and how can this be optimized?


Sebastian Selzer: You need to understand your process to be able to follow the Quality by Design principle and not just rely on testing the quality of the product at the end. The small-scale model should be your first task. Start simple, for example by testing in a very small volume how your cells behave in 3D. As a first step you can identify suitable process parameters in literature and we advise to follow the recommendations from your vendor and see in iterations, how your cells behave. For example, customers of ours at MH Hannover did exactly that. They started with a 2D static culture, then moved to the bioreactor, and optimized the process using classical process development approaches. They applied technologies and methods like perfusion, media exchange, pH control and DO control, and optimized one parameter after the other. And in the end, they had a very good process to work with. Then you have to scale it up and keep the environment constant for the cells. To achieve this, it is important to identify critical process parameters at small scale. We strongly advise taking a systematic process development approach.

 

Eppendorf: Robert, your group has established expertise in cultivating hiPSCs as cell aggregates in stirred-tank bioreactors. In your latest publication, you reported attaining a cell density of 35 million cells per mL. That is a big leap! Which major hurdles did you have to overcome to reach this milestone?

 

Robert Zweigerdt: The first hurdle, which we attacked a decade ago, was to support survival and proliferation of hiPSC seeded in a three-dimensional (3D) matrix-free suspension culture, in contrast to the established cultivation protocols employing 2D matrix-dependent monolayer culture on conventional culture dishes and platforms.1, 2


The second big step, was using a modified stirring impeller design supporting a more homogeneous hiPSC aggregation3 and, subsequently, a “retention-filter” system. Such retention systems enable keeping the hPS cells, which form multicellular aggregates in stirred suspension culture, in the bioreactor upon automated perfusion feeding, defined as constant replacement of used by fresh media.4 Subsequently, perfusion feeding was the prerequisite for our latest step: that is, the identification of growth-limiting parameters such as pH dependence, glucose consumption and lactate accumulation. Having identified these growth-limiting bottlenecks, feedback-based monitoring was performed which requires the control of the overall medium throughput via perfusion feeding. Dr. Felix Manstein, of our department, who was driving these investigations in recent years, has also implemented in silico process modeling and optimization strategies, which facilitate rational process development of high density bioprocessing of hiPSCs.5

 

Eppendorf: For a prospective use in advanced therapies, hiPSCs need to be differentiated into the desired cell type. How straightforward was it to translate differentiation protocols which have been designed for monolayer cultures to cell aggregates in bioreactors?


Robert Zweigerdt: Since we initiated the development of lineage-specific differentiation strategies in suspension several years ago, shortly after the first successful hiPSC culture in 3D,6 we have established a substantial degree of competency in that area as well. The most significant challenges regarding directed differentiation in suspension culture include the impact of cell aggregates size, its heterogeneity, overall cell density and defining mechanical and hydrodynamic parameters.7


However, we also noted that the standard culture media components and differentiation-directing molecules that we are applying, as for example the WNT pathway modulators, used for mesendoderm-induction and cardiac differentiation, have equivalent effects in 2D and in 3D.8 Therefore, process transition from 2D, which is often applied for cell differentiation basic research, to 3D suspension culture is typically straightforward. However, we are convinced that in the future many differentiation strategies will benefit from advanced process control abilities enabled by the bioreactor technologies, still in the early stages of development.9


Notably, we demonstrated that stirred-tank bioreactor-based hiPSC differentiation is efficiently applicable not only for cardiac diffraction (as highlighted by references above) but also for the differentiation and production of numerous other functional hiPSC progenies, including endothelial cells,10 macrophages11 and endodermal derivatives.12

 

Eppendorf: In upstream bioprocessing, the feeding strategy strongly impacts cell growth and viability. Repeated batch and perfusion are two options for removing byproducts and replenishing nutrients. What do you consider the pros and cons of these two strategies?


Robert Zweigerdt: As mentioned above, our experience suggests that perfusion feeding, despite its complexity, is the optimal tactic for advanced hPSC cultivation.13 This is due to the highly glycolytic metabolism of the rapidly growing hPSC, which, on the one hand, requires an enormous supply of extra glucose to avoid growth-limiting starvation. Moreover, on the other hand, high glucose supplementation results in a massive accumulation of secreted lactate, which may become toxic and which induces a proliferation-inhibiting acidification of the culture. These issues increase exponentially in parallel to the exponential increase in cell density.5 For these reasons, we feel that perfusion feeding is the most successful strategy to control growth-limiting parameters, if the goal of the protocol is to optimize high density cultivation of hiPSC. Notably, in parallel to the 10-fold increase in cell density, the amount of medium required to generate a given number of cells, was reduced by 70% in consequence to the process optimization steps.

 

Eppendorf: Within a few years, you were able to increase hiPSC culture density more than tenfold. How did you optimize your process to obtain this value?


Robert Zweigerdt: A couple of years back, we gained 2.85 million hiPSCs per mL following inoculation with 0.5 million cells per mL. Recently, we obtained a more than 10-fold higher cell density following a comparable inoculation density. We follow a step-by-step strategy, systematically analyzing the challenges and then applying the bioreactor-enabled combined control of the parameters, thereby overcoming the growth-limiting hurdles. Specific bottlenecks include: promoting efficient survival and aggregation of hiPSC after single cell-based process inoculation, appropriate adaptation of the stirring speed to ensure no hiPSC-clumping and reducing aggregate diameter below ~300 µm. Next, avoiding pH drop below circa 6.7, ensuring constant glucose supply to avoid cell starvation and adapting the perfusion speed (and thus promoting the optimal medium throughput) to avoid peak accumulation of lactate and toxic osmolality levels as well as several additional parameters.5 However, once these limitations are identified, they can be systematically controlled via the bioprocess control software, and optimized in combination with in silico process modeling; details in our most recent protocol.14

 

Eppendorf: You were able to generate 5.25 billion hiPSCs in a 150 mL volume. How does that number compare to the number of cells required for cell therapy applications, for example for the heart? Do you see the need for future scale-up?


Robert Zweigerdt: Despite this substantial progress of bioprocessing of undifferentiated, pluripotent hiPSCs, we are still working on further increasing the cell density and thus the yield of differentiated cells including hiPSC-derived cardiomyocytes. While we have achieved very high lineage purity e.g., of >95% iPSC-cardiomyocytes, the cell density obtained from the differentiation protocol is still relatively low; currently ca. 1-2x106 cells per mL.8 Since estimations suggest that for the replacement of disease-depleted heart myocytes about 1–2x109 iPSC-cardiomyocytes will be required for each patient, we would currently require about a 1 liter culture to provide the appropriate cell dose for an individual patient. Regenerative medicine researchers are discussing the possibility of generating very large cell batches for an allogeneic – non-patient specific – transplantation approach, so we believe it would be appropriate to pursue a program of substantial upscaling in the future. This goal would target volumes of five, ten, twenty, one hundred-fold and eventually even greater levels.


Such an upscaling strategy is also highly attractive from a commercial perspective, which includes transition to fully controlled GMP-conditions required for regulatory compliance and clinical translation.


Another promising approach is “blood cell farming” as for example the differentiation of functional macrophages from hiPSC. As we recently demonstrated in collaboration with the group of Nico Lachmann at the Hannover Medical School campus, this approach, in contrast to the batch-production of hiPSC-cardiomyocytes, is compatible with the continuing production of macrophages in stirred tank bioreactors over several weeks or even months.11

 

Eppendorf: Considering the cell density, do you still see room for improvement? What are the limiting factors?


Robert Zweigerdt: As indicated above, we see room for improvement for the bioprocessing of differentiated hiPSC progenies. The (limiting) factors for differentiation are even more complex compared to the expansion of hiPSC at the pluripotent state. The reasons for this include the higher complexity of differentiation processes since the cells are constantly changing their progenitor status and phenotype and thus their physiology and proliferation properties. We are working intensively to develop lineage-specific process conditions expressing numerous different lineages.


It is a challenging task but therefore inspiring and exciting!

 

References


1. Singh H, Mok P, Balakrishnan T, Rahmat SNB, Zweigerdt R. Up-scaling single cell-inoculated suspension culture of human embryonic stem cells. Stem Cell Res. 2010;4(3):165-179. doi: 10.1016/j.scr.2010.03.001

2. Zweigerdt R, Olmer R, Singh H, Haverich A, Martin U. Scalable expansion of human pluripotent stem cells in suspension culture. Nat Protoc. 2011;6(5):689-700. doi: 10.1038/nprot.2011.318

3. Olmer R, Lange A, Selzer S, et al. Suspension culture of human pluripotent stem cells in controlled, stirred bioreactors. Tissue Engineering Part C: Methods. 2012;18(10):772-784. doi: 10.1089/ten.tec.2011.0717

4. Kropp C, Kempf H, Halloin C, et al. Impact of feeding strategies on the scalable expansion of human pluripotent stem cells in single-use stirred tank bioreactors. Stem Cells Transl Med. 2016;5(10):1289-1301. doi: 10.5966/sctm.2015-0253

5. Manstein F, Ullmann K, Kropp C, et al. High density bioprocessing of human pluripotent stem cells by metabolic control and in silico modeling. Stem Cells Transl Med. 2021;10(7):1063-1080. doi: 10.1002/sctm.20-0453

6. Kempf H, Olmer R, Kropp C, et al. Controlling expansion and cardiomyogenic differentiation of human pluripotent stem cells in scalable suspension culture. Stem Cell Rep. 2014;3(6):1132-1146. doi: 10.1016/j.stemcr.2014.09.017

7. Kempf H, Kropp C, Olmer R, Martin U, Zweigerdt R. Cardiac differentiation of human pluripotent stem cells in scalable suspension culture. Nat Protoc. 2015;10(9):1345-1361. doi: 10.1038/nprot.2015.089

8. Halloin C, Schwanke K, Löbel W, et al. Continuous wnt control enables advanced hpsc cardiac processing and prognostic surface marker identification in chemically defined suspension culture. Stem Cell Rep. 2019;13(2):366-379. doi: 10.1016/j.stemcr.2019.06.004

9. Williams B, Löbel W, Finklea F, et al. Prediction of human induced pluripotent stem cell cardiac differentiation outcome by multifactorial process modeling. Front Bioeng Biotechnol. 2020;8:851. doi: 10.3389/fbioe.2020.00851

10. Olmer R, Engels L, Usman A, et al. Differentiation of human pluripotent stem cells into functional endothelial cells in scalable suspension culture. Stem Cell Rep. 2018;10(5):1657-1672. doi: 10.1016/j.stemcr.2018.03.017

11. Ackermann M, Kempf H, Hetzel M, et al. Bioreactor-based mass production of human iPSC-derived macrophages enables immunotherapies against bacterial airway infections. Nat Commun. 2018;9(1):5088. doi: 10.1038/s41467-018-07570-7

12. Sahabian A, Sgodda M, Naujok O, et al. Chemically-defined, xeno-free, scalable production of hpsc-derived definitive endoderm aggregates with multi-lineage differentiation potential. Cells. 2019;8(12):1571. doi: 10.3390/cells8121571

13. Kropp C, Massai D, Zweigerdt R. Progress and challenges in large-scale expansion of human pluripotent stem cells. Process Biochem. 2017;59:244-254. doi: 10.1016/j.procbio.2016.09.032

14. Manstein F, Ullmann K, Triebert W, Zweigerdt R. Process control and in silico modeling strategies for enabling high density culture of human pluripotent stem cells in stirred tank bioreactors. STAR Protocols. 2021;2(4):100988. doi: 10.1016/j.xpro.2021.100988

 

 

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