Engineering and Two-Stage Evolution of a Lignocellulosic Hydrolysate-Tolerant Saccharomyces cerevisiae Strain for Anaerobic Fermentation of Xylose from AFEX Pretreated Corn Stover

The inability of the yeast Saccharomyces cerevisiae to ferment xylose effectively under anaerobic conditions is a major barrier to economical production of lignocellulosic biofuels. Although genetic approaches have enabled engineering of S. cerevisiae to convert xylose efficiently into ethanol in defined lab medium, few strains are able to ferment xylose from lignocellulosic hydrolysates in the absence of oxygen. This limited xylose conversion is believed to result from small molecules generated during biomass pretreatment and hydrolysis, which induce cellular stress and impair metabolism. Here, we describe the development of a xylose-fermenting S. cerevisiae strain with tolerance to a range of pretreated and hydrolyzed lignocellulose, including Ammonia Fiber Expansion (AFEX)-pretreated corn stover hydrolysate (ACSH). We genetically engineered a hydrolysate-resistant yeast strain with bacterial xylose isomerase and then applied two separate stages of aerobic and anaerobic directed evolution. The emergent S. cerevisiae strain rapidly converted xylose from lab medium and ACSH to ethanol under strict anaerobic conditions. Metabolomic, genetic and biochemical analyses suggested that a missense mutation in GRE3, which was acquired during the anaerobic evolution, contributed toward improved xylose conversion by reducing intracellular production of xylitol, an inhibitor of xylose isomerase. These results validate our combinatorial approach, which utilized phenotypic strain selection, rational engineering and directed evolution for the generation of a robust S. cerevisiae strain with the ability to ferment xylose anaerobically from ACSH.     

Enzymatic synthesis of glutathione using engineered Saccharomyces cerevisiae

Two single gene cassettes, each containing one of the individual gene (γ-glutamylcysteine synthetase gene GSH1 or glutathione synthetase gene GSH2), were constructed under the control of alcohol dehydrogenase (ADH1) promoter and their respective native terminators. The recombinant plasmids constructed with Kan ^r or Hyg ^r as the selective markers and were transformed into Saccharomyces cerevisiae separately and jointly. Three engineered strains, GSH1-enhanced strain S.TS013/GSH1, GSH2-enhanced strain S.TS013/GSH2 and GSH1+GSH2 double-enhanced strain S.TS013/GSH1+GSH2, were constructed. Glutathione production using the recombinant strains to improve was then determined. By the cell dosage proportions of two engineered strains (S.TS013/GSH1, S.TS013/GSH2) and a two-stage reaction, GSH productivity increased by 84 and 59 % over that of the host strain and the S.TS013/GSH1+GSH2 strain, respectively.     

The Thioredoxin-Thioredoxin Reductase System Can Function in Vivo as an Alternative System to Reduce Oxidized Glutathione in Saccharomyces cerevisiae

Cellular mechanisms that maintain redox homeostasis are crucial, providing buffering against oxidative stress. Glutathione, the most abundant low molecular weight thiol, is considered the major cellular redox buffer in most cells. To better understand how cells maintain glutathione redox homeostasis, cells of Saccharomyces cerevisiae were treated with extracellular oxidized glutathione (GSSG), and the effect on intracellular reduced glutathione (GSH) and GSSG were monitored over time. Intriguingly cells lacking GLR1 encoding the GSSG reductase in S. cerevisiae accumulated increased levels of GSH via a mechanism independent of the GSH biosynthetic pathway. Furthermore, residual NADPH-dependent GSSG reductase activity was found in lysate derived from glr1 cell. The cytosolic thioredoxin-thioredoxin reductase system and not the glutaredoxins (Grx1p, Grx2p, Grx6p, and Grx7p) contributes to the reduction of GSSG. Overexpression of the thioredoxins TRX1 or TRX2 in glr1 cells reduced GSSG accumulation, increased GSH levels, and reduced cellular glutathione E_h′. Conversely, deletion of TRX1 or TRX2 in the glr1 strain led to increased accumulation of GSSG, reduced GSH levels, and increased cellular E_h′. Furthermore, it was found that purified thioredoxins can reduce GSSG to GSH in the presence of thioredoxin reductase and NADPH in a reconstituted in vitro system. Collectively, these data indicate that the thioredoxin-thioredoxin reductase system can function as an alternative system to reduce GSSG in S. cerevisiae in vivo.     

Ethanol production by Saccharomyces cerevisiae using lignocellulosic hydrolysate from Chrysanthemum waste degradation

Ethanol production derived from Saccharomyces cerevisiae fermentation of a hydrolysate from floriculture waste degradation was studied. The hydrolysate was produced from Chrysanthemum (Dendranthema grandiflora) waste degradation by Pleurotus ostreatus and characterized to determine the presence of compounds that may inhibit fermentation. The products of hydrolysis confirmed by HPLC were cellobiose, glucose, xylose and mannose. The hydrolysate was fermented by S. cerevisiae, and concentrations of biomass, ethanol, and glucose were determined as a function of time. Results were compared to YGC modified medium (yeast extract, glucose and chloramphenicol) fermentation. Ethanol yield was 0.45 g g^?1, 88 % of the maximal theoretical value. Crysanthemum waste hydrolysate was suitable for ethanol production, containing glucose and mannose with adequate nutrients for S. cerevisiae fermentation and low fermentation inhibitor levels.     

Production of glutathione in extracellular form by Saccharomyces cerevisiae

The present research was aimed at inducing, in a post fermentative procedure (biotransformation) and by modifying cell permeability, glutathione (GSH) accumulation and subsequent release from cells of Saccharomyces cerevisiae. With the aim of limiting process costs, research considered the possibility of employing baker's yeasts (S. cerevisiae), inexpensive cells source available on the market, in comparison with a collection strain. The tested yeasts showed different sensitivity to the chemical/physical treatments performed to alter cell permeability. Modest effects were evidenced with Triton, active only on Zeus yeast samples (1.7 g GSH/l, near 60% of which in extracellular form). Lauroyl sarcosine showed an interesting action on GB Italy sample (2.8 g GSH/l, near 80% extracellular). Lyophilization evidenced good performance with Lievitalia yeast strain (2.9 g GSH/l, 90% extracellular). The possibility of obtaining GSH directly in extracellular form represents an interesting opportunity of reducing GSH production cost and furthering the range of application of this molecule.     

Glutathione Deficiency Leads to Riboflavin Oversynthesis in the Yeast Pichia guilliermondii

The Pichia guilliermondii GSH1 and GSH2 genes encoding Saccharomyces cerevisiae homologues of glutathione (GSH) biosynthesis enzymes, γ-glutamylcysteine synthetase and glutathione synthetase, respectively, were cloned and deleted. Constructed P. guilliermondii Δgsh1 and Δgsh2 mutants were GSH auxotrophs, displayed significantly decreased cellular GSH+GSSG levels and sensitivity to tert-butyl hydroperoxide, hydrogen peroxide, and cadmium ions. In GSH-deficient synthetic medium, growths of Δgsh1 and Δgsh2 mutants were limited to 3–4 and 5–6 cell divisions, respectively. Under these conditions Δgsh1 and Δgsh2 mutants possessed 365 and 148 times elevated riboflavin production, 10.7 and 2.3 times increased cellular iron content, as well as 6.8 and 1.4 fold increased ferrireductase activity, respectively, compared to the wild-type strain. Glutathione addition to the growth medium completely restored the growth of both mutants and decreased riboflavin production, cellular iron content, and ferrireductase activity to the level of the parental strain. Cysteine also partially restored the growth of the Δgsh2 mutants, while methionine or dithiothreitol could not restore the growth neither of the Δgsh1, nor of the Δgsh2 mutants. Besides, it was shown that in GSH presence riboflavin production by both Δgsh1 and Δgsh2 mutants, similarly to that of the wild-type strain, depended on iron concentration in the growth medium. Furthermore, in GSH-deficient synthetic medium P. guilliermondii Δgsh2 mutant cells, despite iron overload, behaved like iron-deprived wild-type cells. Thus, in P. guilliermondii yeast, glutathione is required for proper regulation of both riboflavin and iron metabolism.     

Efficient production of glutathione in Saccharomyces cerevisiae via a synthetic isozyme system

Glutathione, a tripeptide consisting of cysteine, glutamic acid, and glycine, has multiple beneficial effects on human health. Previous studies have focused on producing glutathione in Saccharomyces cerevisiae by overexpressing γ-glutamylcysteine synthetase (GSH1) and glutathione synthetase (GSH2), which are the rate-limiting enzymes involved in the glutathione biosynthetic pathway. However, the production yield and titer of glutathione remain low due to the feedback inhibition on GSH1. To overcome this limitation, a synthetic isozyme system consisting of a novel bifunctional enzyme (GshF) from Gram-positive bacteria possessing both GSH1 and GSH2 activities, in addition to GSH1/GSH2, was introduced into S. cerevisiae, as GshF is insensitive to feedback inhibition. Given the HSP60 chaperonin system mismatch between bacteria and S. cerevisiae, co-expression of Group-I HSP60 chaperonins (GroEL and GroES) from Escherichia coli was required for functional expression of GshF. Among various strains constructed in this study, the SKSC222 strain capable of synthesizing glutathione with the synthetic isozyme system produced 240 mg L^-1 glutathione with glutathione content and yield of 4.3% and 25.6 mg_glutathione/g_glucose, respectively. These values were 6.6-, 4.9-, and 4.3-fold higher than the corresponding values of the wild-type strain. In a glucose-limited fed-batch fermentation, the SKSC222 strain produced 2.0 g L^-1 glutathione in 67 h. Therefore, this study highlights the benefits of the synthetic isozyme system in enhancing the production titer and yield of value-added chemicals by engineered strains of S. cerevisiae.     

Development of a Saccharomyces cerevisiae Strain with Enhanced Resistance to Phenolic Fermentation Inhibitors in Lignocellulose Hydrolysates by Heterologous Expression of Laccase

To improve production of fuel ethanol from renewable raw materials, laccase from the white rot fungus Trametes versicolor was expressed under control of the PGK1 promoter in Saccharomyces cerevisiae to increase its resistance to phenolic inhibitors in lignocellulose hydrolysates. It was found that the laccase activity could be enhanced twofold by simultaneous overexpression of the homologous t-SNARE Sso2p. The factors affecting the level of active laccase obtained, besides the cultivation temperature, included pH and aeration. Laccase-expressing and Sso2p-overexpressing S. cerevisiae was cultivated in the presence of coniferyl aldehyde to examine resistance to lignocellulose-derived phenolic fermentation inhibitors. The laccase-producing transformant had the ability to convert coniferyl aldehyde at a faster rate than a control transformant not expressing laccase, which enabled faster growth and ethanol formation. The laccase-producing transformant was also able to ferment a dilute acid spruce hydrolysate at a faster rate than the control transformant. A decrease in the content of low-molecular-mass aromatic compounds, accompanied by an increase in the content of high-molecular-mass compounds, was observed during fermentation with the laccase-expressing strain, illustrating that laccase was active even at the very low levels of oxygen supplied. Our results demonstrate the importance of phenolic compounds as fermentation inhibitors and the advantage of using laccase-expressing yeast strains for producing ethanol from lignocellulose.     

Import and Metabolism of Glutathione by Streptococcus mutans

Glutathione (γ-GluCysGly, GSH) is not found in most gram-positive bacteria, but some appear to synthesize it and others, including Streptococcus mutans ATCC 33402, import it from their growth medium. Import of oxidized glutathione (GSSG) by S. mutans 33402 in 7H9 medium was shown to require glucose and to occur with an apparent K_m of 18 ± 5 μM. GSSG, GSH, S-methylglutathione, and homocysteine-glutathione mixed disulfide (hCySSG) were imported at comparable rates (measured by depletion of substrate in the medium), as was the disulfide of γ-GluCys. In contrast, the disulfide of CysGly was not taken up at a measurable rate, indicating that the γ-Glu residue is important for efficient transport. During incubation with GSSG, little GSSG was detected in cells but GSH and γ-GluCys accumulated during the first 30 min and then declined. No significant intracellular accumulation of Cys or sulfide was found. Transient intracellular accumulation of d/l-homocysteine, as well as GSH and γ-GluCys, was observed during import of hCySSG. Although substantial levels of GSH were found in cells when S. mutans was grown on media containing glutathione, such GSH accumulation had no effect on the growth rate. However, the presence of cellular GSH did protect against growth inhibition by the thiol-oxidizing agent diamide. Import of glutathione by S. mutans ATCC 25175, which like strain 33402 does not synthesize glutathione, occurred at a rate comparable to that of strain 33402, but three species which appear to synthesize glutathione (S. agalactiae ATCC 12927, S. pyogenes ATCC 8668, and Enterococcus faecalis ATCC 29212) imported glutathione at negligible or markedly lower rates.Bacteria import peptides composed of two to eight residues by means of a number of different multiprotein uptake systems or permeases (14). Of the bacterial permeases, those of Escherichia coli, Lactococcus lactis, and Salmonella typhimurium are the best studied (6, 7). In these organisms, there are individual permeases that have high affinity for dipeptides, tripeptides, dipeptides and tripeptides, or oligopeptides. Among the bacterial peptide permeases (14), there seems to be no discrimination of the specific amino acids of the transported peptides. However, switching the stereochemistry of C_α from l to d or modifying the C-terminal carboxylate or N-terminal amine of transported peptides significantly reduces the rate of transport. One transport system which does seem to recognize peptide residue side chains has been reported to exist in Enterococcus faecalis; this system transports only peptides that possess an N-terminal Asp or Glu (13).In 1978, we reported that glutathione (γ-GluCysGly, GSH) is not synthesized by most gram-positive bacteria (4), apparent exceptions being Streptococcus agalactiae and L. lactis (previously Streptococcus lactis). However, some of the gram-positive bacteria appeared to acquire GSH by import of another form of GSH from the growth medium. Uptake of glutathione by Streptococcus mutans was later studied by Thomas (16), who found that total cellular thiol content, and radioactivity from labeled GSH or oxidized GSH (GSSG), increased with the same kinetics. A careful study of L. lactis subsp. cremoris by Wiederholt and Steele (17) established that strain Z8 efficiently accumulates GSH when grown in medium supplemented with GSH but is unable to synthesize it, whereas strain C2 can neither import nor synthesize GSH. Species of Peptostreptococcus and Fusobacterium have been shown to markedly increase their production of H₂S, apparently derived by import of glutathione from the growth medium (2). Finally, cellular accumulation of radioactivity from radiolabeled GSH or GSSG added to the incubation medium has been demonstrated in Streptococcus pneumoniae, and a mutant in which the apparent transport of glutathione is blocked has been found (9).In a recent report (10), we provided evidence for accumulation of GSH through transport and synthesis of GSH by streptococci and enterococci, but the occurrence of these processes appeared to be species dependent and even, for some species, strain dependent. Such strain dependence appears most variable for L. lactis, where different strains can synthesize GSH, accumulate GSH by import, or do neither (4, 17). In the present research, we expand on our studies of streptococci in order to gain insight into the nature of the glutathione species transported, the fate of the glutathione once it enters the cell, and the function of glutathione in the cell.     

Xylitol production by genetically modified industrial strain of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> using glycerol as co-substrate

Xylitol is commercially used in chewing gum and dental care products as a low calorie sweetener having medicinal properties. Industrial yeast strain of S. cerevisiae was genetically modified to overexpress an endogenous aldose reductase gene GRE3 and a xylose transporter gene SUT1 for the production of xylitol. The recombinant strain (XP-RTK) carried the expression cassettes of both the genes and the G418 resistance marker cassette KanMX integrated into the genome of S. cerevisiae. Short segments from the 5′ and 3′ delta regions of the Ty1 retrotransposons were used as homology regions for integration of the cassettes. Xylitol production by the industrial recombinant strain was evaluated using hemicellulosic hydrolysate of the corn cob with glucose as the cosubstrate. The recombinant strain XP-RTK showed significantly higher xylitol productivity (212 mg L^?1 h^?1) over the control strain XP (81 mg L^?1 h^?1). Glucose was successfully replaced by glycerol as a co-substrate for xylitol production by S. cerevisiae. Strain XP-RTK showed the highest xylitol productivity of 318.6 mg L^?1 h^?1 and titre of 47 g L^?1 of xylitol at 12 g L^?1 initial DCW using glycerol as cosubstrate. The amount of glycerol consumed per amount of xylitol produced (0.47 mol mol^?1) was significantly lower than glucose (23.7 mol mol^?1). Fermentation strategies such as cell recycle and use of the industrial nitrogen sources were demonstrated using hemicellulosic hydrolysate for xylitol production.     

Exploring grape marc as trove for new thermotolerant and inhibitor-tolerant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strains for second-generation bioethanol production

Background

Robust yeasts with high inhibitor, temperature, and osmotic tolerance remain a crucial requirement for the sustainable production of lignocellulosic bioethanol. These stress factors are known to severely hinder culture growth and fermentation performance.

Results

Grape marc was selected as an extreme environment to search for innately robust yeasts because of its limited nutrients, exposure to solar radiation, temperature fluctuations, weak acid and ethanol content. Forty newly isolated Saccharomyces cerevisiae strains gave high ethanol yields at 40°C when inoculated in minimal media at high sugar concentrations of up to 200 g/l glucose. In addition, the isolates displayed distinct inhibitor tolerance in defined broth supplemented with increasing levels of single inhibitors or with a cocktail containing several inhibitory compounds. Both the fermentation ability and inhibitor resistance of these strains were greater than those of established industrial and commercial S. cerevisiae yeasts used as control strains in this study. Liquor from steam-pretreated sugarcane bagasse was used as a key selective condition during the isolation of robust yeasts for industrial ethanol production, thus simulating the industrial environment. The isolate Fm17 produced the highest ethanol concentration (43.4 g/l) from the hydrolysate, despite relatively high concentrations of weak acids, furans, and phenolics. This strain also exhibited a significantly greater conversion rate of inhibitory furaldehydes compared with the reference strain S. cerevisiae 27P. To our knowledge, this is the first report describing a strain of S. cerevisiae able to produce an ethanol yield equal to 89% of theoretical maximum yield in the presence of high concentrations of inhibitors from sugarcane bagasse.

Conclusions

This study showed that yeasts with high tolerance to multiple stress factors can be obtained from unconventional ecological niches. Grape marc appeared to be an unexplored and promising substrate for the isolation of S. cerevisiae strains showing enhanced inhibitor, temperature, and osmotic tolerance compared with established industrial strains. This integrated approach of selecting multiple resistant yeasts from a single source demonstrates the potential of obtaining yeasts that are able to withstand a number of fermentation-related stresses. The yeast strains isolated and selected in this study represent strong candidates for bioethanol production from lignocellulosic hydrolysates.

     

Harnessing Genetic Diversity in Saccharomyces cerevisiae for Fermentation of Xylose in Hydrolysates of Alkaline Hydrogen Peroxide-Pretreated Biomass

The fermentation of lignocellulose-derived sugars, particularly xylose, into ethanol by the yeast Saccharomyces cerevisiae is known to be inhibited by compounds produced during feedstock pretreatment. We devised a strategy that combined chemical profiling of pretreated feedstocks, high-throughput phenotyping of genetically diverse S. cerevisiae strains isolated from a range of ecological niches, and directed engineering and evolution against identified inhibitors to produce strains with improved fermentation properties. We identified and quantified for the first time the major inhibitory compounds in alkaline hydrogen peroxide (AHP)-pretreated lignocellulosic hydrolysates, including Na⁺, acetate, and p-coumaric (pCA) and ferulic (FA) acids. By phenotyping these yeast strains for their abilities to grow in the presence of these AHP inhibitors, one heterozygous diploid strain tolerant to all four inhibitors was selected, engineered for xylose metabolism, and then allowed to evolve on xylose with increasing amounts of pCA and FA. After only 149 generations, one evolved isolate, GLBRCY87, exhibited faster xylose uptake rates in both laboratory media and AHP switchgrass hydrolysate than its ancestral GLBRCY73 strain and completely converted 115 g/liter of total sugars in undetoxified AHP hydrolysate into more than 40 g/liter ethanol. Strikingly, genome sequencing revealed that during the evolution from GLBRCY73, the GLBRCY87 strain acquired the conversion of heterozygous to homozygous alleles in chromosome VII and amplification of chromosome XIV. Our approach highlights that simultaneous selection on xylose and pCA or FA with a wild S. cerevisiae strain containing inherent tolerance to AHP pretreatment inhibitors has potential for rapid evolution of robust properties in lignocellulosic biofuel production.     

Glutathione in conditioned media of tobacco suspension cultures

Conditioned media of suspension cultures of Nicotiana tabacum var. Samsun contain 0.15-0.20 mmol/l glutathione. These concentrations correspond closely to the intracellular content of glutathione and represent about three to four times the amount of glutathione needed to maintain the intracellular level of glutathione. In contrast to the GSH:GSSG ratio inside the cells, the amount of GSSG in the media rises to 20% of the GSH content.     

Circadian Regulation of Glutathione Levels and Biosynthesis in Drosophila melanogaster

Circadian clocks generate daily rhythms in neuronal, physiological, and metabolic functions. Previous studies in mammals reported daily fluctuations in levels of the major endogenous antioxidant, glutathione (GSH), but the molecular mechanisms that govern such fluctuations remained unknown. To address this question, we used the model species Drosophila, which has a rich arsenal of genetic tools. Previously, we showed that loss of the circadian clock increased oxidative damage and caused neurodegenerative changes in the brain, while enhanced GSH production in neuronal tissue conferred beneficial effects on fly survivorship under normal and stress conditions. In the current study we report that the GSH concentrations in fly heads fluctuate in a circadian clock-dependent manner. We further demonstrate a rhythm in activity of glutamate cysteine ligase (GCL), the rate-limiting enzyme in glutathione biosynthesis. Significant rhythms were also observed for mRNA levels of genes encoding the catalytic (Gclc) and modulatory (Gclm) subunits comprising the GCL holoenzyme. Furthermore, we found that the expression of a glutathione S-transferase, GstD1, which utilizes GSH in cellular detoxification, significantly fluctuated during the circadian day. To directly address the role of the clock in regulating GSH-related rhythms, the expression levels of the GCL subunits and GstD1, as well as GCL activity and GSH production were evaluated in flies with a null mutation in the clock genes cycle and period. The rhythms observed in control flies were not evident in the clock mutants, thus linking glutathione production and utilization to the circadian system. Together, these data suggest that the circadian system modulates pathways involved in production and utilization of glutathione.     

Evaluation of cysteine ethyl ester as efficient inducer for glutathione overproduction in Saccharomyces spp.

Economical yeast based glutathione (GSH) production is a process that is influenced by several factors like raw material and production costs, biomass production and efficient biotransformation of adequate precursors into the final product GSH. Nowadays the usage of cysteine for the microbial conversion into GSH is industrial state of practice. In the following study, the potential of different inducers to increase the GSH content was evaluated by means of design of experiments methodology. Investigations were executed in three natural Saccharomyces strains, S. cerevisiae, S. bayanus and S. boulardii, in a well suited 50 ml shake tube system. Results of shake tube experiments were confirmed in traditional baffled shake flasks and finally via batch cultivation in lab-scale bioreactors under controlled conditions. Comprehensive studies showed that the usage of cysteine ethyl ester (CEE) for the batch-wise biotransformation into GSH led up to a more than 2.2 times higher yield compared to cysteine as inducer. Additionally, the intracellular GSH content could be significantly increased for all strains in terms of 2.29 ± 0.29% for cysteine to 3.65 ± 0.23% for CEE, respectively, in bioreactors. Thus, the usage of CEE provides a highly attractive inducing strategy for the GSH overproduction.     

Enhancement of glutathione production in a coupled system of adenosine deaminase-deficient recombinant Escherichia coli and Saccharomyces cerevisiae

Adenosine triphosphate (ATP) is necessary in the enzymatic production of glutathione (GSH). Our aim was to improve GSH production by increasing the efficiency of ATP regeneration in a coupled system. Previous results suggested that low GSH production in the coupled system is due to the irreversible transformation of adenosine (Ado) to hypoxanthine (Hx) via inosine (Ino) pathway in Escherichia coli JM109 (pBV03). In this study, to block the transformation of Ado into Hx and enhance GSH production, a coupled ATP regeneration system was constructed with adenosine deaminase-deficient recombinant E. coli JW1615 (pBV03) and Saccharomyces cerevisiae WSH2. GSH production was improved (2.94-fold of the control), and ATP regeneration reaction was established in the coupled system. The results are applicable to ATP regeneration in other microbial processes.     

Glutathione S-aralkyltransferase

1. The name `glutathione S-aralkyltransferase' is proposed for the enzyme catalysing the reaction of benzyl chloride with GSH. 2. Results from heat-inactivation studies, ammonium sulphate-fractionation and acid-precipitation experiments, and studies of the distribution of activities in rat liver, in rat kidney and in the livers of other animals indicate that glutathione S-aralkyltransferase differs from glutathione S-alkyltransferase, S-aryltransferase, S-epoxidetransferase and an S-alkenetransferase. 3. The distribution of these enzymes in the livers of the animal species examined was different. 4. Glutathione S-alkyltransferase, S-aralkyltransferase and the S-alkenetransferase that are present in rat liver supernatant were inhibited by GSSG, and the nature of the inhibition varied in each case. 5. 3,5-Di-tert.-butyl-4-hydroxybenzyl acetate reacts spontaneously with GSH, but the rat liver-supernatant-catalysed reaction of GSH with this and other aralkyl esters was weak. 6. A probable function of the glutathione S-transferases is the protection of cellular constituents from strong electrophilic agents.     

Screening soy hydrolysates for the production of a recombinant therapeutic protein in commercial cell line by combined approach of near-infrared spectroscopy and chemometrics

Soy hydrolysates are widely used as the major nutrient sources for cell culture processes for industrial manufacturing of therapeutic recombinant proteins. The primary goal of this study was to develop a spectroscopy based chemometric method, a partial least squares (PLS), to screen soy hydrolysates for better yield of protein production (titers) in cell culture medium. Harvest titer values of 29 soy hydrolysate lots with production yield between 490 and 1,350 mg/L were obtained from shake flask models or from manufacture engineering runs. The soy hydrolysate samples were measured by near-infrared (NIR) in reflectance mode using an infrared fiber optic probe. The fiber optic probe could easily enable in situ measurement of the soy hydrolysates for convenient raw material screening. The best PLS calibration has a determination coefficient of R ²?=?0.887 utilizing no spectral preprocessing, the two spectral ranges of 10,000–5,376 cm^?1 and 4,980–4,484 cm^?1, and a rank of 6 factors. The cross-validation of the model resulted in a determination coefficient of R ²?=?0.741 between the predicted and actual titer values with an average standard deviation of 72 mg/L. Compared with the resource demanding shake flask model, the combination of NIR and chemometric modeling provides a convenient method for soy hydrolysate screening with the advantage of fast speed, low cost and non-destructive.