运用氨基酸分析法和DOE法优化抗PD-1单克隆抗体生产用培养基

本研究采用氨基酸分析法结合DOE设计法优化并获得高表达抗PD-1单克隆抗体生产用基础和补料培养基。通过对市售多种基础和补料培养基进行筛选,获得细胞生长状况较优的基础培养基和抗体表达较高的补料培养基,利用氨基酸分析法检测较优基础培养基和补料培养基中氨基酸消耗情况,确定影响细胞生长和抗体表达的关键氨基酸种类,利用DOE分析软件设计分别在较优基础和补料培养基中添加不同浓度的氨基酸种类及浓度,根据细胞生长及抗体表达,优化得到抗PD-1单克隆抗体的基础和补料培养基组合。最终优化后基础培养基配方为:Hycell CHO培养基中添加1.04 mmol/L L-天冬酰胺和0.76 mmol/L L-谷氨酰胺。最终优化后补料培养基配方为:OPM CHOCD Feed1补料培养基中添加38.7 mmol/L L-组氨酸,75.0 mmol/L L-酪氨酸,64.0 mmol/L L-丝氨酸,49.2 mmol/L L-谷氨酰胺和18.7 mmol/L L-半胱氨酸。经过3 L反应器培养验证,优化后的培养基比未优化时,最大活细胞密度(PVCD)提高了62.7%,抗PD-1单克隆抗体表达量提高了71.5%,且活性无明显差异。     

Effects of cysteine,asparagine, or glutamine limitations in Chinese hamster ovary cell batch and fed-batch cultures

Amino acid availability is a key factor that can be controlled to optimize the productivity of fed-batch cultures. To study amino acid limitation effects, a serum-free chemically defined basal medium was formulated to exclude the amino acids that became depleted in batch culture. The effect of limiting glutamine, asparagine, and cysteine on the cell growth, metabolism, antibody productivity, and product glycosylation was investigated in three Chinese hamster ovary (CHO) cell lines (CHO-DXB11, CHO-K1SV, and CHO-S). Cysteine limitation was detrimental to both cell proliferation and productivity for all three CHO cell lines. Glutamine limitation reduced growth but not cell specific productivity, whereas asparagine limitation had no significant effect on either growth or cell specific productivity. Neither glutamine nor asparagine limitation significantly affected antibody glycosylation. Replenishing the CHO-DXB11 culture with cysteine after 1 day of cysteine limitation allowed the cells to partially recover their growth and productivity. This recovery was not observed after 2 days of cysteine limitation. Based on these findings, a fed-batch protocol was developed using single or mixed amino acid supplementation. Although cell density and antibody concentration were lower compared to a commercial feed, the feeds based on cysteine supplementation yielded comparable cell specific productivity. Overall, this study showed that different amino acid limitations have varied effects on the performance of CHO cell cultures and that maintaining cysteine availability is a critical process parameter for the three cell lines investigated.     

Enhancement of monoclonal antibody yield by hybridoma fed-batch culture, resulting in extended maintenance of viable cell population

Hybridoma batch cultures were extended using feed formulations based on nutrient consumption measured during different batch culture phases when (a) growth but negligible antibody production was taking place; (b) maximum antibody production rate and declining viable cell growth rate were observed. Strategy (a) was the more successful (2.8-fold compared with 1.8-fold antibody titer increase) and maintained cell viability for longer. Analysis of the effects of omitting individual amino acids yielded results which were consistent with those from the feeding experiment (c) 1994 John Wiley & Sons, Inc.     

The effect of amino acid supplementation in an industrial Chinese Hamster Ovary process

The main goal in biosimilar development is to increase Chinese Hamster Ovary (CHO) viability and productivity while maintaining product quality. Despite media and feed optimization during process development, depletion of amino acids still occurs. The aim of the work was to optimize an existing industrial fed batch process by preventing shortage of amino acids and to gather knowledge about CHO metabolism. Several process outputs were evaluated such as cell metabolism, cell viability, monoclonal antibodies (mAbs) production, and product quality. First step was to develop and supplement an enriched feed containing depleted amino acids. Abundance of serine and glucose increased lactate production resulting in low viability and low productivity. In the next step, we developed an amino acid feed without serine to avoid the metabolic boost. Supplemented amino acids improved cell viability by 9%; however, mAb production did not increase significantly. In the final step, we limited glucose concentration (<5.55 mmol/L) in the cell culture to avoid the metabolic boost while supplementing an amino acid feed including serine. Data analysis showed that we were able to (a) replace depleted amino acids and avoid metabolic boost, (b) increase viability by 12%, (c) enhance mAb production by 0.5 g/L (total by approximately 10 g), and (d) extend the overall process time of an already developed bioprocess.     

Defined protein and animal component-free NS0 fed-batch culture

A chemically defined protein and animal component-free fed-batch process for an NS0 cell line producing a human IgG(1) antibody has been developed. The fed-batch feed profile was optimised in a step-wise manner. Depletion of measurable compounds was determined by direct analysis. The cellular need for non-measurable compounds was tested by continued culturing of cell suspension, removed from the bioreactor, in shake-flasks supplemented with critical substances. In the final fed-batch culture, 8.4 x 10(6) viable cells mL(-1) and 625 mg antibody L(-1) was obtained as compared to 2.3 x 10(6) cells mL(-1) and 70 mg antibody L(-1) in batch. The increase in cell density, in combination with a prolonged declining phase where antibody formation continued, resulted in a 6.2-fold increase in total cell yield, a 10.5-fold increase in viable cell hours and an 11.4-fold increase in product yield. These improvements were obtained by using a feed with glucose, glutamine, amino acids, lipids, sodium selenite, ethanolamine and vitamins. Specifically, supplementation with lipids (cholesterol) had a drastic effect on the maximum viable cell density. Calcium, magnesium and potassium were not depleted and a feed also containing iron, lithium, manganese, phosphorous and zinc did not significantly enhance the cell yield. The growth and death profiles in the final fed-batch indicated that nutrient deprivation was not the main cause of cell death. The ammonium concentration and the osmolality increased to potentially inhibitory levels, but an imbalance in the supply of growth/survival factors may also contribute to termination of the culture.     

Hybridoma cell growth and anti-neuroblastoma monoclonal antibody production in spinner flasks using a protein-free medium with microcarriers

The main disadvantages of foetal calf serum as the world-wide common serum supplement for cell growth are its content of various proteins of variable concentrations between batches as well as its high cost. The use of serum-free and protein-free media is gradually becoming one of the goals of cell culture especially for standardizing culture conditions or for simple purification of cell products like monoclonal antibodies. The mouse hybridoma cells 14/2/1 were cultivated either in protein-free UltraDOMA medium or in serum-containing RPMI medium with and without microcarriers to generate high quantities of monoclonal antibodies against neuroblastoma tumour cells. Cell growth rate, IgG production, viability, glucose and lactate concentrations, attachment rate and doubling time have been used as investigation criteria. Modifications of culture procedures (static or stirred), inoculum density, and microcarrier concentration caused an improvement of monoclonal antibody production. The kinetics of antibody synthesis was best in spinner culture with 2 ml of microcarriers in protein-free medium. These results of short-term microcarrier culture in stirred spinner flasks indicate that IgG yields in protein-free medium 2.5-fold higher to those in serum-supplemented medium can be achieved.     

Specific effects of synthetic oligopeptides on cultured animal cells

Synthetic oligopeptides, tri- to pentaglycine and tri- and tetraalanine, were found to enhance viable cell density and culture viability when applied at concentrations higher than milllimolar to the cultures of a model hybridoma line. Oligoalanines, in addition, enhanced monoclonal antibody yields. Oligoglycines promoted solely the cell growth, unless the batch culture was fed with a medium concentrate. Examination of the effects of various tripeptides composed of glycine, alanine, serine, threonine, lysine, and histidine showed that some of the peptides promoted the growth of the culture, while other peptides suppressed the growth and enhanced the monoclonal antibody yield. Determination of the levels of amino acids and peptides in culture media indicated that the observed changes of culture parameters were caused by intact peptide molecules, rather than by amino acids liberated from the peptides by enzymic cleavage.     

Benchmarking of commercially available CHO cell culture media for antibody production

In this study, eight commercially available, chemically defined Chinese hamster ovary (CHO) cell culture media from different vendors were evaluated in batch culture using an IgG-producing CHO DG44 cell line as a model. Medium adaptation revealed that the occurrence of even small aggregates might be a good indicator of cell growth performance in subsequent high cell density cultures. Batch experiments confirmed that the culture medium has a significant impact on bioprocess performance, but high amino acid concentrations alone were not sufficient to ensure superior cell growth and high antibody production. However, some key amino acids that were limiting in most media could be identified. Unbalanced glucose and amino acids led to high cell-specific lactate and ammonium production rates. In some media, persistently high glucose concentrations probably induced the suppression of respiration and oxidative phosphorylation, known as Crabtree effect, which resulted in high cell-specific glycolysis rates along with a continuous and high lactate production. In additional experiments, two of the eight basal media were supplemented with feeds from two different manufacturers in six combinations, in order to understand the combined impact of media and feeds on cell metabolism in a CHO fed-batch process. Cell growth, nutrient consumption and metabolite production rates, antibody production, and IgG quality were evaluated in detail. Concentrated feed supplements boosted cell concentrations almost threefold and antibody titers up to sevenfold. Depending on the fed-batch strategy, fourfold higher peak cell concentrations and eightfold increased IgG titers (up to 5.8 g/L) were achieved. The glycolytic flux was remarkably similar among the fed-batches; however, substantially different specific lactate production rates were observed in the different media and feed combinations. Further analysis revealed that in addition to the feed additives, the basal medium can make a considerable contribution to the ammonium metabolism of the cells. The glycosylation of the recombinant antibody was influenced by the selection of basal medium and feeds. Differences of up to 50 % in the monogalacto-fucosylated (G1F) and high mannose fraction of the IgG were observed.     

Advantages of AlaGln as an additive to cell culture medium: use with anti-CD20 chimeric antibody-producing POTELLIGENT™ CHO cell lines

l-alanyl-l-glutamine (AlaGln) is dipeptide that has better solubility and stability than Glutamine (Gln). In this study, we evaluated the utility of this dipeptide during culture of POTELLIGENT™ Chinese hamster ovary (CHO) cells expressing anti-CD20 chimeric antibody. Although AlaGln in the culture medium lowered the specific growth rate, the MAb titer was maximized when Gln was completely replaced by AlaGln in both the basal and feed media. Moreover, AlaGln augmented production of antibody not only at flask scale but also at spinner scale, although the extent of this effect was dependent on the cell clone. To explore the mechanism responsible for the effect of AlaGln on cell growth, we measured apoptosis in the early phase of cell culture on days 8, 9, and 10. The apoptotic ratio was reduced in medium containing AlaGln. Ammonia was generated in medium containing Gln when it was maintained at 37 °C, which impeded the growth and productivity of the cells. In contrast, AlaGln produced less ammonia under these conditions, which may have been one of the properties associated with its beneficial effects. We conclude that certain dipeptides can serve as superior alternative sources of amino acids in cell culture and antibody production.     

Effects of Supplementation of Various Medium Components on Chinese Hamster Ovary Cell Cultures Producing Recombinant Antibody

Thirteen vitamins, twenty amino acids, hormones, inorganic salts, and other chemical agents, which constitute typical serum-free media, were evaluated for the development of fortified medium to enhance cell growth and productivity of recombinant antibody in the cultures of the recombinant Chinese hamster ovary (rCHO) cells. Two different rCHO cell lines, rCHO-A producing recombinant antibodies against the human platelet and rCHO-B secreting recombinant antibodies against the S surface antigen of Hepatitis B, respectively, were cultivated in batch suspension mode. Concentration of interested component in the tested medium was doubled to examine the fortification effect. Growth of rCHO-A cell and its antibody production were slightly improved with addition of either choline chloride, folic acid, thiamine⋅HCl, or Long^TMR³IGF-I. On the other hand, in the cultivation of rCHO-B cell which was more sensitive to its environmental changes, hormones such as Long^TMR³IGF-I and triiodothyronine (T₃) as well as various vitamins involving choline chloride, i-inositol, niacinamide, pyridoxine HCl, and thiamine⋅HCl enhanced the cell growth and antibody production. Particularly, when concentration of consuming amino acid was doubled, remarkable increase in specific productivity was served, resulting in high final antibody concentration. These results were believed to provide a fundamental strategy of medium fortification useful for improvement of recombinant antibody production in serum-free medium. These authors contributed equally to this work     

Bcl-2 mediated suppression of apoptosis in myeloma NS0 cultures

The influence of Bcl-2 expression on the suppression of apoptosis during the cultivation of an NS0 cell line expressing a chimeric antibody was investigated. Following selection of transfectants in medium containing G418, Western analysis revealed evidence of some up-regulation of endogenous Bcl-2 expression even in the control vector transfectants. Cultivation of the two cell lines in suspension batch cultures clearly demonstrated the enhanced robustness of the bcl-2 vector transfected cells. Suppression of apoptosis resulted in an approximately 20% increase in maximum viable cell number, and a doubling in culture duration compared to the control transfected cells. However, despite the significant affect on viability, Bcl-2 expression did not result in an increase in final antibody titre in comparison with the control cell line. Exposure of cells to various nutrient limited conditions further emphasised the influence of Bcl-2 on cell survival. After 3 days of exposure to serum, glucose, glutamate and asparagine deprivation, the viable cell number and viability were significantly higher in the bcl-2 transfected cell line. When control cells were deprived of all amino acids, there was a complete loss of viability and viable cell number within 3 days. By contrast, the bcl-2 transfected cell line retained greater than 75% of the initial viable cell number and about 70% viability. In response to exposure to 8 mM thymidine (a cytostatic agent) the control cell line underwent complete loss of viability and viable cell number after 6 days. This compared with 18 days for complete loss of viability in the bcl-2 transfected cell line. As under batch culture conditions, there was no difference between the two cell lines in final antibody titre, which indicated that MAb synthesis is limited by nutrient availability during the latter stages of culture in both cases. When fed batch cultures were carried out using a concentrated essential amino acid feed, the bcl-2 cell line exhibited a 60% increase in maximum viable cell number and a 50% increase in culture duration, when compared to the control cell line. Moreover, the bcl-2 cell line exhibited a greater than 40% increase in maximum antibody titre.     

The use of serum-free medium for the production of functionally active humanised monoclonal antibody from NS0 mouse myeloma cells engineered using glutamine synthetase as a selectable marker

A protein-free growth medium (W38 medium) had previously been developed for the NS0 mouse myeloma cell line which is cholesterol-auxotrophic. This paper describes the development of a protein-free growth medium for NS0 cells expressing humanised monoclonal antibody using GS (glutamine synthetase) as a selectable marker. Several GS-engineered NS0 cell lines expressing humanised monoclonal antibody grew in a modification of W38 medium which maintained GS-selection, supplemented with cholesterol, phosphatidylcholine and -cyclodextrin. Further studies showed that additional glutamic acid, asparagine, ribonucleosides and choline chloride improved cell growth. Amino acid analysis identified a number of amino acids that were being depleted from the culture medium. NS0 cell lines 9D4 and 2H5 expressing CAMPATH-1H^* were adapted to enable them to grow serum-free in the absence of cholesterol and -cyclodextrin. Cholesterol-independent 9D4 (9D4.CF) cells grown in shake flask culture using an enriched protein-free medium (WNSD medium), supplemented with human recombinant insulin (Nucellin), reached a maximum cell density to 1.86×10⁶ cells ml^–1 producing 76.6 mg l^–1 of antibody. CAMPATH-1H antibody produced using serum-free medium was found to be functionally activein vitro in the Antibody Dependant Cellular Cytotoxicity (ADCC) assay.Abbreviations C cholesterol - CD cyclodextrin - dhfr dihydrofolate reductase - F68 Pluronic F68 - GS glutamine synthetase - MSX methionine sulphoximine - P phosphatidylcholine - PC-FBS phosphatidylcholine, cholesterol and foetal bovine serum - RPMI RPMI 1640 medium - ADCC Antibody-dependant cellular cytotoxicity     

Expression of cell-associated and secreted forms of herpes simplex virus type 1 glycoprotein gB in mammalian cells.

The gene for glycoprotein gB1 of herpes simplex virus type 1 strain Patton was expressed in stable Chinese hamster ovary cell lines. Expression vectors containing the dihydrofolate reductase (dhfr) cDNA plus the complete gB1 gene or a truncated gene lacking the 194 carboxyl-terminal amino acids of gB1 were transfected into CHO DHFR-deficient cells. Radioimmunoprecipitation demonstrated that the complete gB1 protein expressed in CHO cell lines was cell associated, whereas the truncated protein was secreted from the cells due to deletion of the transmembrane and C-terminal domains of gB1. Cells expressing the truncated gB1 protein were subjected to stepwise methotrexate selection, and a cell line was isolated in which the gB1 gene copy number had been amplified 10-fold and the level of expression of gB1 had increased over 60-fold. The truncated gB1 protein was purified from medium conditioned by the amplified cell line. N-terminal amino acid sequence analysis of this purified protein identified the signal peptide cleavage site and predicted the cleavage of a 30-amino-acid signal sequence from the primary protein. The immunogenicity of the truncated gB1 protein was also tested in mice, and high levels of antibody and protection from virus challenge were observed.     

Fed-batch cultivation of transgenic rice cells for the production of hCTLA4Ig using concentrated amino acids

RAmy3D promoter is capable of expressing high levels of recombinant proteins in response to the depletion of sugar in transgenic rice cell suspension cultures. For this reason, it is necessary to change the growth medium into sugar-free production medium to produce the target protein, human cytotoxic T-lymphocyte antigen 4-immunoglobulin (hCTLA4Ig), using the inducible RAmy3D promoter. Since the two-stage culture is a complex process to perform in large-scale, a fed-batch method was evaluated with the addition of concentrated amino acids before the depletion of sugar to induce hCTLA4Ig production. This fed-batch culture was found to be effective and the production of hCTLA4Ig was enhanced up to 1.2-fold compared to that of two-stage cultures with medium exchange. In addition, when this fed-batch culture was performed in a 15-l stirred-tank bioreactor, maximum hCTLA4Ig level was 76.5 mg l⁻¹ at day 10.     

Ultra-high expression of a thermally responsive recombinant fusion protein in E. coli

Elastin-like polypeptides (ELPs) are recombinant peptide-based biopolymers that contain repetitive sequences enriched in glycine, valine, proline, and alanine. Because of the unusually large fraction of these amino acids in ELPs as compared to other cellular proteins, we hypothesized that intracellular pools of these amino acids can be selectively depleted and limit protein yields during expression. In this study, we examined how culture conditions and individual medium components affect protein yields by monitoring cell growth and protein expression kinetics of E. coli expressing an ELP tagged with a green fluorescent protein (GFP). By determining the underlying principles of superior fusion protein yields generated by the hyperexpression protocol, we further improved protein yields through the addition of glycerol and certain amino acids such as proline and alanine and found that amino acid concentrations and the type of basal medium used strongly influenced this beneficial effect. Surprisingly, amino acids other than those that are abundant in ELPs, for example, asparagine, aspartic acid, glutamine, and glutamic acid, also enhanced protein yields even in a nutrient-rich medium. Compared to commonly used Luria-Bertani medium, the protein yield was improved by 36-fold to the remarkable level of 1.6 g/L in shaker flask cultures with a modified medium and optimized culture conditions, which also led to a 8-fold reduction in the cost of the fusion protein. To our knowledge, this is the highest yield of an ELP-fusion protein purified from E. coli cultured in shaker flasks. This study also suggests a useful strategy to improve the yields of other ELP fusion proteins and repetitive polypeptides.     

Fed‐batch CHO cell t‐PA production and feed glutamine replacement to reduce ammonia production

Industrial therapeutic protein production has been greatly improved through fed‐batch development. In this study, improvement to the productivity of a tissue‐plasminogen activator (t‐PA) expressing Chinese hamster ovary (CHO) cell line was investigated in shake flask culture through the optimization of the fed‐batch feed and the reduction of ammonia generation by glutamine replacement. The t‐PA titer was increased from 33 mg/L under batch conditions to 250 mg/L with daily feeding starting after three days of culture. A commercially available fed‐batch feed was supplemented with cotton seed hydrolysate and the four depleted amino acids, aspartic acid, asparagine, cysteine, and tyrosine. The fed‐batch operation increased the generation of by‐products such as lactate and ammonia that can adversely affect the fed‐batch performance. To reduce the ammonia production, a glutamine‐containing dipeptide, pyruvate, glutamate, and wheat gluten hydrolysate, were investigated as glutamine substitutes. To minimize the lag phase as the cells adjusted to the new energy source, a feed glutamine replacement process was developed where the cells were initially cultured with a glutamine containing basal medium to establish cell growth followed by feeding with a feed containing the glutamine substitutes. This two‐step feed glutamine replacement process not only reduced the ammonia levels by over 45% but, in the case of using wheat gluten hydrolysate, almost doubled the t‐PA titer to over 420 mg/L without compromising the t‐PA product quality or glycosylation pattern. The feed glutamine replacement process combined with optimizing other feed medium components provided a simple, practical, and effective fed‐batch strategy that could be applied to the production of other recombinant therapeutic proteins. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2013     

Kinetic analysis of hybridoma cell culture in a protein-free medium: Substrate and agitation effects

A kinetic study of a hybridoma cell line that produces monoclonal antibodies against lactoferrin was carried out. A well defined protein-free culture medium was employed to facilitate the subsequent purification of the monoclonal antibodies. It should be highlighted that most of the existing work has been carried out employing culture media enriched with fetal bovine serum (FBS). Cell growth and monoclonal antibody production were monitored and kinetic parameters were determined. Besides, fundamental nutrients such as glucose and glutamine, inhibitory products such as ammonium and lactate, and several amino acids were followed throughout the culture. Additional experiments were carried out supplementing the medium with glutamine and ammonium, none of them resulting the key compound that halted the cell growth under the tested conditions and an unstructured model can be used to describe the system. Finally, agitation of the culture by a rocker set-up has shown high values of the specific death rate.     

Fed-batch cultivation of animal cells using different medium design concepts and feeding strategies

In animal cell cultivation, cell density and product concentration are often low due to the accumulation of toxic end-products such as ammonia and lactate and/or the depletion of essential nutrients. A hybridoma cell line (CRL-1606) was cultivated in T-flasks using a newly devised medium feeding strategy. The goals were to decrease ammonia and lactate formation by the design of an initial medium which would provide a starting environment to achieve optimal cell growth. This was followed by using a stoichiometric equation governing animal cell growth and then designing a supplemental medium for feeding strategy used to control the nutritional environment. The relationship between the stoichiometric demands for glutamine and nonessential amino acids was also studied. Through stoichiometric feeding, nutrient concentrations were controlled reasonably well. Consequently, the specific production rate of lactate was decreased by fourfold compared with conventional fed-batch culture and by 26-fold compared with conventional batch culture. The specific production rate of ammonia was decreased by tenfold compared with conventional fed-batch culture and by 50-fold compared with conventional batch culture. Most importantly, total cell density and monoclonal antibody concentration were increased by five- and tenfold respectively, compared with conventional batch culture. (c) 1994 John Wiley & Sons, Inc.     

Medium-scale production and purification of monoclonal antibodies in protein-free medium.

Hybridoma cell lines can be adapted to grow in a totally protein-free tissue culture medium and cultured in spinner flasks to generate moderate-to-high quantities of monoclonal antibodies. Such antibodies are easily purified by ammonium sulfate precipitation. This system was shown to be useful for growth of 23 different hybridoma cell lines from different sources to yield an average of 40 mg of highly purified antibody per liter of tissue culture medium.     

Metabolomics analysis of soy hydrolysates for the identification of productivity markers of mammalian cells for manufacturing therapeutic proteins

Soy hydrolysates are widely used as a nutrient supplement in mammalian cell culture for the production of recombinant proteins. The batch‐to‐batch variability of a soy hydrolysate often leads to productivity differences. This report describes our metabolomics platform, which includes a battery of LC‐MS/MS modes of operation, and advanced data analysis software for automated data processing. The platform was successfully used for screening productivity markers in soy hydrolysates during the production of two therapeutic antibodies in two Chinese hamster ovary cell lines. A total of 123 soy hydrolysate batches were analyzed, from which 62 batches were used in the production runs of cell line #1 and 12 batches were used in the production runs of cell line #2. For cell line #1, out of 19 amino acids, 106 other metabolites and 4,131 peptides identified in the soy hydrolysate batches being used, several nucleosides and short hydrophobic peptides showed negative correlation with antibody titer, while ornithine, citrulline and several amino acids and organic acids correlated positively with titer. For cell line #2, only ornithine and citrulline showed strong positive correlation. When ornithine was spiked into the culture media, both cell lines demonstrated accelerated cell growth, indicating ornithine as a root cause of the performance difference. It is proposed that better soy hydrolysate performance resulted from better bacterial fermentation during the hydrolysate production. A few selected markers were used to predict the performance of other soy hydrolysate batches for cell line #1. The predicted titers agreed with the experimental values with good accuracy. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:522–531, 2015