OR WAIT null SECS
Close collaboration between academic and industrial groups is vital to ensuring glycosylation models are fit for deployment.
Many of the highest-grossing protein therapeutics, including monoclonal antibodies (mAbs), Fc-fusion proteins (etanercept [Enbrel, Amgen/Pfizer] and aflibercept [Eylea, Bayer/Regeneron]), interferon gamma (IFN-γ), erythropoietin (EPO), and tissue plasminogen activator (tPA) contain complex carbohydrates (glycans) covalently bound to their peptide backbone (1). In turn, the presence and relative abundance of different glycan motifs (e.g., α-1,3 galactose, core fucosylation, and sialylation) are well-known to influence the safety, serum-half life (pharmacokinetics) and the therapeutic mechanisms (pharmacodynamics) of the aforementioned biopharmaceuticals (2). Glycosylation is also widely acknowledged as a major source of therapeutic protein heterogeneity (3), which is highlighted by work that found considerable glycosylation variation among different commercial lots of the same biopharmaceutical product (4).
Biopharmaceutical glycosylation variability is determined by manufacturing bioprocess conditions (1). Large-scale mammalian cell culture is used for the manufacture of all therapeutic glycoproteins (TGPs), with Chinese hamster ovary (CHO) and murine myeloma (NS0 and Sp2/0) cell lines being the most-commonly used production platforms (5). During cell culture, even subtle variations in nutrient availability, dissolved oxygen, temperature, ammonia, and pH may impact the intracellular process of glycosylation (1,3) and yield product that cannot be administered to patients. Due to its bioprocess-associated variability and impact on safety, pharmacokinetics, and pharmacodynamics, glycosylation is widely regarded as a critical quality attribute (CQA) of TGPs (1).
In the context of biopharmaceutical quality assurance, 21 mathematical models for protein glycosylation have been developed over the past decade. Although the strategies to mathematically describe the glycosylation process have been diverse, all models have demonstrated potential toward addressing one or more quality assurance (QA) issues associated with TGP manufacture. This review focuses on how different modeling strategies can be leveraged to aid in product QA across the different stages of biopharmaceutical product development and manufacture. Technical details on glycosylation models have been outlined elsewhere (6).
The following individual glycosylation motifs that are known to influence the safety, pharmacokinetics, and pharmacodynamics of TGPs are presented in Figure 1:
Protein asparagine (N)-linked glycosylation occurs in two steps (18). The first occurs while the protein is being synthesized in the endoplasmic reticulum and entails the covalent addition of a large unprocessed precursor oligosaccharide to asparagine residues of the protein backbone. The glycoprotein is then transferred, via vesicles, to the Golgi apparatus, where the second and final step of the N-glycosylation process occurs: while transiting through Golgi, the protein-bound glycan is sequentially modified by several enzyme-catalyzed carbohydrate removal and addition reactions.
Serine/threonine (O)-linked glycosylation occurs entirely in the Golgi apparatus and begins with the addition of N-acetylgalactosamine (GalNAc) to serine or threonine residues on the protein backbone (19). After this first step, the glycan is modified by a sequence of enzyme-catalyzed monosaccharide addition reactions that extend its branching and length (19). CHO cells produce only two O-glycosylation variants, which consist of the mono- and bi-sialylated ‘Core 1’ structures shown in Figure 1 (20).
For the purposes of this review, the glycosylation process is considered to have two distinct inputs. The first encompasses the enzymes, which catalyze the monosaccharide removal and addition reactions (glycoenzymes). The second input for the glycosylation processes consists of nucleotide sugar donors (NSDs), which are metabolites that provide monosaccharides for the sugar addition reactions of the glycosylation process. NSDs are endogenously synthesized by the production cell lines using common nutrients, such as glucose and glutamine, as substrates (21). Thus, NSDs are the direct link between cellular metabolism (i.e., nutrient availability) and TGP glycosylation. Many cell culture NSD precursor feeding strategies have been developed to tune TGP glycosylation (22,23).
The first model for N-glycosylation, published in 1996, aimed to describe the addition of glycans to the peptide backbone of proteins (24). From then, N-glycosylation models expanded to include the extent of glycan processing within the Golgi apparatus, thus aiming to depict the variability observed in TGP glycosylation profiles. Descriptions of glycosylation soon required strategies for automatically generating the complex reaction networks involved in the process and were pioneered by Krambeck and Betenbaugh in 2005 (25). Building on these seminal studies, more than 20 mathematical models for protein glycosylation have been developed to date. Based on structure and solution strategy, the mathematical models of TGP glycosylation can be grouped into three categories: kinetic models, flux-based models, and statistical models.
Kinetic models attempt to capture the time-dependent mechanisms underlying glycosylation and are based on dynamic material balances for all TGPs and NSDs present in Golgi (26–28). Given the inherently dynamic nature of cell culture processes, kinetic models are particularly suited to describe the effects bioprocess conditions have on TGP glycosylation. A fundamental drawback of kinetic models is that they require a substantial amount of experimental data to determine robust values for their unknown parameters (e.g., enzyme kinetic rate constants).
Flux-based glycosylation models consist of material balances for all TGPs present in the Golgi apparatus and are built using reaction networks that define the production and consumption stoichiometry of each species. To solve flux models, steady state is assumed, and the resulting system of linear equations is solved for the rates (fluxes) at which all TGPs are interconverted. Because the resulting system of linear equations is usually underdetermined (more unknown fluxes than equations), flux models must be solved using constraint-based linear programming (29,30) or probabilistic methods, such as Markov chain Monte Carlo simulations (31,32). A key advantage of flux-based models is that their solution requires reduced amounts of experimental data. The main drawback of flux-based models is that their solution inherently assumes steady-state, which limits their ability to describe the dynamic shifts in TGP glycosylation often observed in cell culture processes. This limitation has been recently addressed by including parameters representing dynamic shifts in TGP residence time within Golgi (30).
Statistical models are abstract black-box mathematical representations where process inputs are quantitatively related, via statistical regression strategies, with TGP glycosylation profiles. Examples of statistical models of TGP glycosylation are design of experiment (DoE) surface response models (23) and partial least squares regression (33,34). Advantages of statistical models are that they do not require a priori knowledge of the process, require little or no end-user modeling expertise, and can therefore be deployed with relative ease. Statistical models are limited in that they are exclusively data-driven and, thus, are unable to yield insight into the mechanisms underlying TGP glycosylation. Furthermore, the predictive capability of statistical models may break down if model inputs drift outside the input space with which they were calibrated.
Table I presents the glycosylation models that have been developed since 2009 and highlights how each model has been used toward potential TGP quality assurance applications.
Table I shows that all published glycosylation models have been used for applications that can directly support TGP QA practices. Four QA application areas stand out: (i) data analytics, (ii) bioprocess characterization, (iii) cell line engineering/development, and (iv) manufacturing bioprocess optimization and control.
Kinetic models appear to be the most versatile, having been used for all four application areas. Flux-based models have mainly focused on cell line selection and glycoengineering, and statistical models have been used for bioprocess characterization, control, and optimization. The application areas for the different modeling strategies results from their underlying features. Because kinetic models aim to mechanistically describe the glycosylation process, they are capable of covering all QA application areas. Flux models are well-suited to define cell glycoengineering strategies because they focus on the rates of glycoenzyme-catalyzed reactions. By definition, statistical models quantitatively represent correlations between bioprocess conditions and TGP glycosylation. Therefore, they are particularly adept for bioprocess control and optimization QA applications when mechanistic bioprocess knowledge is lacking.
Although the deployment of statistical models in industry is increasing at an accelerated pace (49), the use of mechanistic glycosylation models remains to be widespread. This disparity may arise from the use of specialized software and the perceived need for expert user input associated with mechanistic modeling. Despite these challenges, mechanistic models are, conceptually, more versatile than their statistical counterparts because they are based on the biochemical mechanisms underlying the glycosylation process. An interesting example where these limitations are addressed is the GLYMMER (ReacTech) software platform, which is based on the work by Bennun et al. (37), runs on Microsoft Excel, and requires only moderate user input and expertise.
The deployment of different glycosylation modeling strategies depends entirely on the TGP quality assurance application they will be used for. Statistical models can be readily deployed in the industrial setting for bioprocess design, control, and optimization (33,43) with minimal user input and expertise. Mechanistic models (kinetic and flux-based) have been shown to be particularly robust for cell line characterization (27,50) and glycoengineering (26,31) as well as for bioprocess design and optimization (42,47).
To fully exploit the advances in glycosylation modeling toward the development, control, and optimization of next-generation TGP production bioprocesses, close collaboration between academic and industrial groups must continue so that the models are fit for purpose and require minimal end-user expertise for deployment.
1. P. Zhang, et al., Drug Discov. Today 21 (5) 740–765 (2016).
2. L. Liu, J. Pharm. Sci. 104 (6) 1866–1884 (2015).
3. J. Fournier, Biopharm Int. 28 (10) 32–37 (2015).
4. A. Planinc, et al., Eur. J. Hosp. Pharm. Sci. Pract. 24 (5) 286–292 (2017).
5. A.L. Grilo and A. Mantalaris, Trends Biotechnol. 37 (1) 9–16 (2019).
6. C. Kontoravdi and I.J. del Val, Curr. Opin. Chem. Eng. 22 89–97 (2018).
7. A.M. Goetze, et al., Glycobiology 21 (7) 949–959 (2011).
8. M. Yu, et al., MAbs 4 (4) 475–87 (2012).
9. J.W. Steinke, T.A. Platts-Mills, and S.P. Commins, J. Allergy Clin. Immunol. 135 (3) 589–596 (2015).
10. C.J. Bosques, et al., Nat. Biotechnol. 28 (11) 1153–1156 (2010).
11. T.A. Platts-Mills, et al., Immunol. Allergy. Clin. North Am. 35 (2) 247–260 (2015).
12. T. Shinkawa, et al., J. Biol. Chem. 278 (5), 3466–3473 (2003).
13. B. Peschke, et al., Front. Immunol. 8 646 (2017).
14. M. Thomann, et al., Mol. Immunol. 73 69–75 (2016).
15. R.M. Anthony, et al., Science, 320 (5874) 373-376 (2008).
16. A. Noguchi, et al., J. Biochem. 117 (1) 59–62 (1995).
17. B. Yin, et al., Biotechnol. Bioeng. 112 (11) 2343–2351 (2015).
18. P. Stanley, N. Taniguchi, and M. Aebi, “N-Glycans”, in Essentials of Glycobiology, A. Varki, et al., Eds., pp. 99–111, (Cold Spring Harbor, New York, NY, 2nd ed., 2015).
19. I. Brockhausen and P. Stanley, “O-GalNAc Glycans”, in Essentials of Glycobiology, A. Varki, et al., Eds., pp. 113–123 (Cold Spring Harbor, New York, NY, 2nd ed., 2015).
20. S. Houel, et al., Anal. Chem. 86 (1) 576–584 (2014).
21. P.M. Jedrzejewski, et al., Int. J. Mol. Sci. 15 (3) 4492–4522 (2014).
22. N.S. Wong, et al., Biotechnol. Bioeng. 107 (2) 321–336 (2010).
23. R.K. Grainger and D.C. James, Biotechnol. Bioeng. 110 (11) 2970–2983 (2013).
24. M. Shelikoff, A.J. Sinskey, and G. Stephanopoulos, Biotechnol. Bioeng. 50 (1) 73–90 (1996).
25. F.J. Krambeck and M.J. Betenbaugh, Biotechnol. Bioeng. 92 (6) 711–728 (2005).
26. I.J. del Val, Y. Fan, and D. Weilguny, Biotechnol. J. 11 (5) 610–623 (2016).
27. F.J. Krambeck, et al., PLoS One 12 (5), e0175376 (2017).
28. T.K. Villiger, et al., Biotechnol. Prog. 32 (5) 1135–1148 (2016).
29. I. Hang, et al., Glycobiology 25 (12) 1335–1349 (2015).
30. S. Hutter, et al., Metab. Eng. 43 (Pt A) 9–20 (2017).
31. P.N. Spahn, et al., Metab. Eng. 33 52–66 (2016).
32. P.N. Spahn, et al., Biotechnol. J. 12 (2) (2017).
33. M. Sokolov, et al., Biotechnol. J. 13 (4) e1700461 (2018).
34. M. Sokolov, et al., Biotechnol. Prog. 33 (5) 1368–1380 (2017).
35. F.J. Krambeck, et al., Glycobiology 19 (11) 1163–1175 (2009).
36. I.J. del Val, J.M. Nagy, and C. Kontoravdi, Biotechnol. Prog. 27 (6) 1730–1743 (2011).
37. S.V. Bennun, et al., PLoS Comput. Biol. 9 (1) e1002813 (2013).
38. K. Ohadi, et al., IFAC Proceedings Volumes 46 (31) 30–35 (2013).
39. I.J. del Val, K.M. Polizzi, and C. Kontoravdi, Sci. Rep. 6 28547 (2016).
40. A.G. McDonald, K.F. Tipton, and G.P. Davey, PLoS Comput. Biol. 12 (4) e1004844 (2016).
41. T.K. Villiger, et al., J. Biotechnol. 229 3–12 (2016).
42. D.J. Karst, et al., Biotechnol. Bioeng. 114 (9) 1978–1990 (2017).
43. M. Sokolov, et al., Biotechnol. Prog. 33 (1) 181–191 (2017).
44. S.N. Sou, et al., Biotechnol. Bioeng. 114 (7) 1570–1582 (2017).
45. H. Aghamohseni, et al., J. Ind. Microbiol. Biotechnol. 44 (7) 1005–1020 (2017).
46. B.G. Kremkow and K.H. Lee, Metab. Eng. 47 134–142 (2018).
47. P. Kotidis, et al., Biotechnol. Bioeng. In press (2019) DOI: 10.1002/bit.26960.
48. T. Le, et al., Biotechnol. Bioeng. In press (2019) DOI: 10.1002/bit.26952.
49. P. Kroll, et al., Pharm. Res. 34 (12) 2596–2613 (2017).
50. S.V. Bennun, et al., J. Mol. Biol. 428 (16), 3337–3352 (2016).
Vol. 43, No. 6
Pages: 40–43, 46
When referring to this article, please cite it as I. Jiménez del Val, “Levaraging Computational Models of Glycosylation for Biopharma QA,” Pharmaceutical Technology 43 (6) 2019.
Ioscani Jiménez del Val is assistant professor at the School of Chemical & Bioprocess Engineering, University College Dublin, Ireland, firstname.lastname@example.org.