Product solubility control in cellooligosaccharide production by coupled cellobiose and cellodextrin phosphorylase

Soluble cellodextrins (linear β-1,4-d -gluco-oligosaccharides) have interesting applications as ingredients for human and animal nutrition. Their bottom-up synthesis from glucose is promising for bulk production, but to ensure a completely water-soluble product via degree of polymerization (DP) control (DP ≤ 6) is challenging. Here, we show biocatalytic production of cellodextrins with DP centered at 3 to 6 (~96 wt.% of total product) using coupled cellobiose and cellodextrin phosphorylase. The cascade reaction, wherein glucose was elongated sequentially from α-d -glucose 1-phosphate (αGlc1-P), required optimization and control at two main points. First, kinetic and thermodynamic restrictions upon αGlc1-P utilization (200 mM; 45°C, pH 7.0) were effectively overcome (53% → ≥90% conversion after 10 hrs of reaction) by in situ removal of the phosphate released via precipitation with Mg²⁺. Second, the product DP was controlled by the molar ratio of glucose/αGlc1-P (∼0.25; 50 mM glucose) used in the reaction. In optimized conversion, soluble cellodextrins in a total product concentration of 36 g/L were obtained through efficient utilization of the substrates used (glucose: 98%; αGlc1-P: ∼80%) after 1 hr of reaction. We also showed that, by keeping the glucose concentration low (i.e., 1–10 mM; 200 mM αGlc1-P), the reaction was shifted completely towards insoluble product formation (DP ∼9–10). In summary, this study provides the basis for an efficient and product DP-controlled biocatalytic synthesis of cellodextrins from expedient substrates.     

Genetic mapping shows intraspecific variation and transgressive segregation for caterpillar‐induced aphid resistance in maize

Plants in nature have inducible defences that sometimes lead to targeted resistance against particular herbivores, but susceptibility to others. The metabolic diversity and genetic resources available for maize (Zea mays) make this a suitable system for a mechanistic study of within‐species variation in such plant‐mediated interactions between herbivores. Beet armyworms (Spodoptera exigua) and corn leaf aphids (Rhopalosiphum maidis) are two naturally occurring maize herbivores with different feeding habits. Whereas chewing herbivore‐induced methylation of 2,4‐dihydroxy‐7‐methoxy‐1,4‐benzoxazin‐3‐one glucoside (DIMBOA‐Glc) to form 2‐hydroxy‐4,7‐dimethoxy‐1,4‐benzoxazin‐3‐one glucoside (HDMBOA‐Glc) promotes caterpillar resistance, lower DIMBOA‐Glc levels favour aphid reproduction. Thus, caterpillar‐induced DIMBOA‐Glc methyltransferase activity in maize is predicted to promote aphid growth. To test this hypothesis, the impact of S. exigua feeding on R. maidis progeny production was assessed using seventeen genetically diverse maize inbred lines. Whereas aphid progeny production was increased by prior caterpillar feeding on lines B73, Ki11, Ki3 and Tx303, it decreased on lines Ky21, CML103, Mo18W and W22. Genetic mapping of this trait in a population of B73 × Ky21 recombinant inbred lines identified significant quantitative trait loci on maize chromosomes 1, 7 and 10. There is a transgressive segregation for aphid resistance, with the Ky21 alleles on chromosomes 1 and 7 and the B73 allele on chromosome 10 increasing aphid progeny production. The chromosome 1 QTL coincides with a cluster of three maize genes encoding benzoxazinoid O‐methyltransferases that convert DIMBOA‐Glc to HDMBOA‐Glc. Gene expression studies and benzoxazinoid measurements indicate that S. exigua ‐induced responses in this pathway differentially affect R. maidis resistance in B73 and Ky21.     

Interplay of catalytic subsite residues in the positioning of α-d-glucose 1-phosphate in sucrose phosphorylase

Kinetic and molecular docking studies were performed to characterize the binding of α-d-glucose 1-phosphate (αGlc 1-P) at the catalytic subsite of a family GH-13 sucrose phosphorylase (from L. mesenteroides) in wild-type and mutated form. The best-fit binding mode of αGlc 1-P dianion had the phosphate group placed anti relative to the glucosyl moiety (adopting a relaxed ⁴C₁ chair conformation) and was stabilized mainly by hydrogen bonds from residues of the enzyme?s catalytic triad (Asp¹⁹⁶, Glu²³⁷ and Asp²⁹⁵) and from Arg¹³⁷. Additional feature of the αGlc 1-P docking pose was an intramolecular hydrogen bond (2.7 Å) between the glucosyl C2-hydroxyl and the phosphate oxygen. An inactive phosphonate analog of αGlc 1-P did not show binding to sucrose phosphorylase in different experimental assays (saturation transfer difference NMR, steady-state reversible inhibition), consistent with evidence from molecular docking study that also suggested a completely different and strongly disfavored binding mode of the analog as compared to αGlc 1-P. Molecular docking results also support kinetic data in showing that mutation of Phe⁵², a key residue at the catalytic subsite involved in transition state stabilization, had little effect on the ground-state binding of αGlc 1-P by the phosphorylase. However, when combined with a second mutation involving one of the catalytic triad residues, the mutation of Phe⁵² by Ala caused complete (F52A_D196A; F52A_E237A) or very large (F52A_D295A) disruption of the proposed productive binding mode of αGlc 1-P with consequent effects on the enzyme activity. Effects of positioning of αGlc 1-P for efficient glucosyl transfer from phosphate to the catalytic nucleophile of the enzyme (Asp¹⁹⁶) are suggested. High similarity between the αGlc 1-P conformers bound to sucrose phosphorylase (modeled) and the structurally and mechanistically unrelated maltodextrin phosphorylase (experimental) is revealed.     

Toward enhanced hyperforin production in St. John's wort root cultures

During the past decades, several trials targeted a stable, sustainable and economic production of St. John's wort (Hypericum perforatum) extract. The value of this extract stems from its use to treat depression and skin irritation due to its hyperforin content. Previously, hyperforin‐forming in vitro root cultures were established. Here, detailed growth and production kinetics have been analyzed over 40 days of cultivation. In the first 10 days, sucrose was completely hydrolyzed to glucose and fructose. The ammonium consumption supported the increase in the biomass and hyperforin production. When sucrose was replaced with glucose/fructose, the linear growth phase started 6 days earlier and resulted in a higher space‐time‐yield. The maximum hyperforin production was 0.82 mg L^?1 day^?1, which was 67 % higher than in the sucrose‐supplemented standard cultivation. Buffering the sucrose‐supplemented medium with phosphate caused a 2.7‐fold increase in the product to biomass yield coefficient. However, the combination of monosaccharides and buffering conditions did not cause an appreciable improvements in the production performance of the shake flask approaches. A potential scalability from flask to lab‐scale stirred bioreactors has been demonstrated. The results obtained offer a basis for a scalable production of hyperforin and a sustainable source for a tissue culture‐based phytomedicine.     

‘Last In–First Out’: seasonal variations of non‐structural carbohydrates,glucose‐6‐phosphate and ATP in tubers of two Arum species

• Knowledge on the metabolism of polysaccharide reserves in wild species is still scarce. In natural sites we collected tubers of Arum italicum Mill. and A. maculatum L. – two geophytes with different apparent phenological timing, ecology and chorology – during five stages of the annual cycle in order to understand patterns of reserve accumulation and degradation.
• Both the entire tuber and its proximal and distal to shoot portion were utilised. Pools of non‐structural carbohydrates (glucose, sucrose and starch), glucose‐6‐phosphate and ATP were analysed as important markers of carbohydrate metabolism.
• In both species, starch and glucose content of the whole tuber significantly increased from sprouting to the maturation/senescence stages, whereas sucrose showed an opposite trend; ATP and glucose‐6‐phosphate were almost stable and dropped only at the end of the annual cycle. Considering the two different portions of the tuber, both ATP and glucose‐6‐phosphate concentrations were higher in proximity to the shoot in all seasonal stages, except the flowering stage.
• Our findings suggest that seasonal carbon partitioning in the underground organ is driven by phenology and occurs independently of seasonal climate conditions. Moreover, our results show that starch degradation, sustained by elevated ATP and glucose‐6‐phosphate pools, starts in the peripheral, proximal‐to‐shoot portion of the tuber, consuming starch accumulated in the previous season, as a ‘Last In–First Out’ mechanism of carbohydrate storage.

     

Biosynthesis of radiolabeled cellodextrins by the Clostridium thermocellum cellobiose and cellodextrin phosphorylases for measurement of intracellular sugars

The Clostridium thermocellum cellobiose and cellodextrin phosphorylases (glucosyl transferases) in the cell extract were used to synthesize radiolabeled cellodextrins with a degree of polymerization (DP=2–6) from nonradioactive glucose-1-phosphate and radioactive glucose. Chain lengths of synthesized cellodextrin were controlled by the absence or presence of dithiothreitol and by reaction conditions. All cellodextrins have the sole radioactive glucose unit located at the reducing ends. Mixed cellodextrins (G2–G6) were separated efficiently by size-exclusion chromatography or less efficiently by thin-layer chromatography. A new rapid sampling device was developed using disposable syringes containing an ultracold methanol-quenching buffer. It was simple, less costly, and especially convenient for anaerobic fermentation. After an impulse feed of radiolabeled cellobiose, the intracellular sugar levels were measured after a series of operations—sampling, extracting, concentrating, separating, and reading. Results showed that the largest amount of radioactivity was cellobiose with lesser amounts of glucose, cellotriose, and cellotetraose, and an average DP of intracellular cellodextrins was ca. 2.     

Phosphorolytic cleavage of sucrose by sucrose-grown ruminal bacterium <Emphasis Type="Italic">Pseudobutyrivibrio ruminis</Emphasis> strain k3

Rumen bacterium Pseudobutyrivibrio ruminis strain k3 utilized over 90 % sucrose added to the growth medium as a sole carbon source. Zymographic studies of the bacterial cell extract revealed the presence of a single enzyme involved in sucrose digestion. Thin layer chromatography showed fructose and glucose-1-phosphate (Glc1P) as end products of the digestion of sucrose by identified enzyme. The activity of the enzyme depended on the presence of inorganic phosphate and was the highest at the concentration of phosphate 56 mmol/L. The enzyme was identified as the sucrose phosphorylase (EC 2.4.1.7) of molar mass ≈54 kDa and maximum activity at pH 6.0 and 45 °C. The calculated Michaelis constant (K _m) for Glc1P formation and release of fructose by partially purified enzyme were 4.4 and 8.56 mmol/L while the maximum velocities of the reaction (v _lim) were 1.19 and 0.64 μmol/L per mg protein per min, respectively.     

Efficient production of lactic acid from sucrose and corncob hydrolysate by a newly isolated <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> GY18

The aim of this study is to investigate production of l-lactic acid from sucrose and corncob hydrolysate by the newly isolated R. oryzae GY18. R. oryzae GY18 was capable of utilizing sucrose as a sole source, producing 97.5 g l⁻¹ l-lactic acid from 120 g l⁻¹ sucrose. In addition, the strain was also efficiently able to utilize glucose and/or xylose to produce high yields of l-lactic acid. It was capable of producing up to 115 and 54.2 g l⁻¹ lactic acid with yields of up to 0.81 g g⁻¹ glucose and 0.90 g g⁻¹ xylose, respectively. Corncob hydrolysates obtained by dilute acid hydrolysis and enzymatic hydrolysis of the cellulose-enriched residue were used for lactic acid production by R. oryzae GY18. A yield of 355 g lactic acid per kg corncobs was obtained after 72 h incubation. Therefore, sucrose and corncobs could serve as potential sources of raw materials for efficient production of lactic acid by R. oryzae GY18.     

Enzymatic production of β-D-glucose-1-phosphate from trehalose

β-D -Glucose-1-phosphate (βGlc1P) is an efficient glucosyl donor for both enzymatic and chemical glycosylation reactions but is currently very costly and not available in large amounts. This article provides an efficient production method of βGlc1P from trehalose and phosphate using the thermostable trehalose phosphorylase from Thermoanaerobacter brockii. At the process temperature of 60°C, Escherichia coli expression host cells are lysed and cell treatment prior to the reaction is, therefore, not required. In this way, the theoretical maximum yield of 26% could be easily achieved. Two different purification strategies have been compared, anion exchange chromatography or carbohydrate removal by treatment with trehalase and yeast, followed by chemical phosphate precipitation. In a next step, βGlc1P was precipitated with ethanol but this did not induce crystallization, in contrast to what is observed with other glycosylphosphates. After conversion of the product to its cyclohexylammonium salt, however, crystals could be readily obtained. Although both purification methods were quantitative (>99% recovery), a large amount of product (50%) was lost during crystallization. Nevertheless, a production process for crystalline βGlc1P is now available from the cheap substrates trehalose and inorganic phosphate.     

Acetate formation during recombinant protein production in Escherichia coli K‐12 with an elevated NAD(H) pool

Acetate formation is a disadvantage in the use of Escherichia coli for recombinant protein production, and many studies have focused on optimizing fermentation processes or altering metabolism to eliminate acetate accumulation. In this study, E. coli MEC697 (MG1655 nadR nudC mazG) maintained a larger pool of NAD(H) compared to the wild‐type control, and also accumulated lower concentrations of acetate when grown in batch culture on glucose. In steady‐state cultures, the elevated total NAD(H) found in MEC697 delayed the threshold dilution rate for acetate formation to a growth rate of 0.27 h^?1. Batch and fed‐batch processes using MEC697 were examined for the production of β‐galactosidase as a model recombinant protein. Fed‐batch culture of MEC697/pTrc99A‐lacZ compared to MG1655/pTrc99A‐lacZ at a growth rate of 0.22 h^?1 showed only a modest increase of protein formation. However, 1 L batch growth of MEC697/pTrc99A‐lacZ resulted in 50% lower acetate formation compared to MG1655/pTrc99A‐lacZ and a two‐fold increase in recombinant protein production.     

Beta-xylosidase activity of a GH3 glucosidase/xylosidase from yak rumen metagenome promotes the enzymatic degradation of hemicellulosic xylans

Aims: To characterize the duel activities of a glycosyl hydrolase family 3 β‐glucosidase/xylosidase from rumen bacterial metagenome and to investigate the capabilities of its β‐d ‐xylosidase activities for saccharification of hemicellulosic xylans. Methods and Results: A β‐glucosidase/xylosidase gene RuBGX1 was cloned from yak (Bos grunniens) rumen using the metagenomic technology. Recombinant RuBGX1, expressed in Escherichia coli, demonstrated high hydrolytic activities on both p‐nitrophenyl‐β‐d ‐glucopyranoside (pNP‐Glc) and p‐nitrophenyl‐β‐d ‐xylopyranoside (pNP‐Xyl) substrates. Analysis of the kinetic properties indicated that RuBGX1 had a lower affinity for pNP‐Glc substrate as the K_m was 0·164 mmol l^?1 for pNP‐Glc and 0·03 mmol l^?1 for pNP‐Xyl at pH 6·0 and 50°C, respectively. The capabilities of RuBGX1 β‐xylosidase for hydrolysis of xylooligosaccharide substrates were further investigated using an endoxylanase‐coupled assay. Hydrolysis time courses illustrated that a significant increase (about 50%) in the reducing sugars, including xylobiose, xylotriose and xylotetraose, was achieved by supplementing endoxylanase with RuBGX1. Enzymatic product analysis using high‐performance anion‐exchange chromatography‐pulsed amperometric detection showed that RuBGX1 could release xyloses from intermediate xylooligosaccharides produced by endoxylanase. Conclusions: The RuBGX1 shows β‐glucosidase activity in hydrolysis of cello‐oligosaccharides; meanwhile, it has β‐xylosidase activity and functions synergistically with endoxylanase to promote the degradation of hemicellulosic xylans. Significance and Impact of the study: This was the first to report the β‐xylosidase activity of family 3 β‐glucosidase/xylosidase functioned in the degradation of hemicellulosic xylans. The bifunctional β‐glucosidase/xylosidase property of RuBGX1 can be used in simultaneous saccharification of cellulose and xylan into fermentable glucose and xylose.     

Assessment of the potential of temporin peptides from the frog Rana temporaria (Ranidae) as anti‐diabetic agents

Temporin A (FLPLIGRVLSGIL‐NH₂), temporin F (FLPLIGKVLSGIL‐NH₂), and temporin G (FFPVIGRILNGIL‐NH₂), first identified in skin secretions of the frog Rana temporaria, produced concentration‐dependent stimulation of insulin release from BRIN‐BD11 rat clonal β‐cells at concentrations ≥1 nM, without cytotoxicity at concentrations up to 3 μM. Temporin A was the most effective. The mechanism of insulinotropic action did not involve an increase in intracellular Ca²⁺ concentrations. Temporins B, C, E, H, and K were either inactive or only weakly active. Temporins A, F, and G also produced a concentration‐dependent stimulation of insulin release from 1.1B4 human‐derived pancreatic β‐cells, with temporin G being the most potent and effective, and from isolated mouse islets. The data indicate that cationicity, hydrophobicity, and the angle subtended by the charged residues in the temporin molecule are important determinants for in vitro insulinotropic activity. Temporin A and F (1 μM), but not temporin G, protected BRIN‐BD11 cells against cytokine‐induced apoptosis (P < 0.001) and augmented (P < 0.001) proliferation of the cells to a similar extent as glucagon‐like peptide‐1. Intraperitoneal injection of temporin G (75 nmol/kg body weight) together with a glucose load (18 mmol/kg body weight) in C57BL6 mice improved glucose tolerance with a concomitant increase in insulin secretion whereas temporin A and F administration was without significant effect on plasma glucose levels. The study suggests that combination therapy involving agents developed from the temporin A and G sequences may find application in Type 2 diabetes treatment.     

Production of 3‐Fucosyllactose in Engineered Escherichia coli with α‐1,3‐Fucosyltransferase from Helicobacter pylori

3‐Fucosyllactose (3‐FL), one of the major oligosaccharides in human breast milk, is produced in engineered Escherichia coli. In order to search for a good α‐1,3‐fucosyltransferase, three bacterial α‐1,3‐fucosyltransferases are expressed in engineered E. coli deficient in β‐galactosidase activity and expressing the essential enzymes for the production of guanosine 5′‐diphosphate‐l ‐fucose, the donor of fucose for 3‐FL biosynthesis. Among the three enzymes tested, the fucT gene from Helicobacter pylori National Collection of Type Cultures 11637 gives the best 3‐FL production in a simple batch fermentation process using glycerol as a carbon source and lactose as an acceptor. In order to use glucose as a carbon source, the chromosomal ptsG gene, considered the main regulator of the glucose repression mechanism, is disrupted. The resulting E. coli strain of ?LP‐YA+FT shows a much lower performance of 3‐FL production (4.50 g L^?1) than the ?L‐YA+FT strain grown in a glycerol medium (10.7 g L^?1), suggesting that glycerol is a better carbon source than glucose. Finally, the engineered E. coli ?LW‐YA+FT expressing the essential genes for 3‐FL production and blocking the colanic acid biosynthetic pathway (?wcaJ) exhibits the highest concentration (11.5 g L^?1), yield (0.39 mol mol^?1), and productivity (0.22 g L^?1 h) of 3‐FL in glycerol‐limited fed‐batch fermentation.     

Expression of exo‐inulinase gene from Aspergillus niger 12 in E. coli strain Rosetta‐gami B (DE3) and its characterization

Inulin is a linear carbohydrate polymer of fructose subunits (2‐60) with terminal glucose units, produced as carbon storage in selected plants. It cannot directly be taken up by most microorganisms due to its large size, unless prior hydrolysis through inulinase enzymes occurs. The hydrolyzed inulin can be taken up by microbes and/or recovered and used industrially for the production of high fructose syrup, inulo‐oligosaccharides, biofuel, and nutraceuticals. Cell‐free enzymatic hydrolysis would be desirable for industrial applications, hence the recombinant expression, purification and characterization of an Aspergillus niger derived exo‐inulinase was investigated in this study. The eukaroyototic exo‐inulinase of Aspergillus niger 12 has been expressed, for the first time, in an E. coli strain [Rosetta‐gami B (DE3)]. The molecular weight of recombinant exo‐inulinase was estimated to be ～81 kDa. The values of K_m and V_max of the recombinant exo‐inulinase toward inulin were 5.3 ± 1.1 mM and 402.1 ± 53.1 µmol min^?1 mg^?1 protein, respectively. Towards sucrose the corresponding values were 12.20 ± 1.6 mM and 902.8 ± 40.2 µmol min^?1 mg^?1 protein towards sucrose. The S/I ratio was 2.24 ± 0.7, which is in the range of native inulinase. The optimum temperature and pH of the recombinant exo‐inulinase towards inulin was 55°C and 5.0, while they were 50°C and 5.5 towards sucrose. The recombinant exo‐inulinase activity towards inulin was enhanced by Cu²⁺ and reduced by Fe²⁺, while its activity towards sucrose was enhanced by Co²⁺ and reduced by Zn²⁺. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:629–637, 2016     

Basic conformers in β‐peptides

The conformation of oligomers of β‐amino acids of the general type Ac‐[β‐Xaa]_n‐NHMe (β‐Xaa = β‐Ala, β‐Aib, and β‐Abu; n = 1–4) was systematically examined at different levels of ab initio molecular orbital theory (HF/6‐31G*, HF/3‐21G). The solvent influence was considered employing two quantum‐mechanical self‐consistent reaction field models. The results show a wide variety of possibilities for the formation of characteristic elements of secondary structure in β‐peptides. Most of them can be derived from the monomer units of blocked β‐peptides with n = 1. The stability and geometries of the β‐peptide structures are considerably influenced by the side‐chain positions, by the configurations at the C^α‐ and C^β‐atoms of the β‐amino acid constituents, and especially by environmental effects. Structure peculiarities of β‐peptides, in particular those of various helix alternatives, are discussed in relation to typical elements of secondary structure in α‐peptides. © 1999 John Wiley & Sons, Inc. Biopoly 50: 167–184, 1999     

Isolation and basic characterization of a β‐glucosidase from a strain of Lactobacillus brevis isolated from a malolactic starter culture

Aims: To study glycosidase activities of a Lactobacillus brevis strain and to isolate an intracellular β‐glucosidase from this strain. Methods and Results: Lactic acid bacteria (LAB) isolated from a commercially available starter culture preparation for malolactic fermentation were tested for β‐glycosidase activities. A strain of Lact. brevis showing high intracellular β‐d ‐glucosidase, β‐d ‐xylosidase and α‐l ‐arabinosidase activities was selected for purification and characterization of its β‐glucosidase. The pure glucosidase from Lact. brevis has also side activities of xylosidase, arabinosidase and cellobiosidase. It is a homotetramer of 330 kDa and has an isoelectric point at pH 3·5. The K_m for p‐nitrophenyl‐β‐d ‐glucopyranoside and p‐nitrophenyl‐β‐d ‐xylopyranoside is 0·22 and 1·14 mmol l^?1, respectively. The β‐glucosidase activity was strongly inhibited by gluconic acid δ‐lactone, partially by glucose and gluconate, but not by fructose. Ethanol and methanol were found to increase the activity up to twofold. The free enzyme was stable at pH 7·0 (t_1/2 = 50 day) but not at pH 4·0 (t_1/2 = 4 days). Conclusions: The β‐glucosidase from Lact. brevis is widely different to that characterized from Lactobacillus casei ( Coulon et al. 1998 ) and Lactobacillus plantarum ( Sestelo et al. 2004 ). The high tolerance to fructose and ethanol, the low inhibitory effect of glucose on the enzyme activity and the good long‐term stability could be of great interest for the release of aroma compounds during winemaking. Significance and Impact of the study: Although the release of aroma compounds by LAB has been demonstrated by several authors, little information exists on the responsible enzymes. This study contains the first characterization of an intracellular β‐glucosidase isolated from a wine‐related strain of Lact. brevis.     

A microalgal‐based preparation with synergistic cellulolytic and detoxifying action towards chemical‐treated lignocellulose

High‐temperature bioconversion of lignocellulose into fermentable sugars has drawn attention for efficient production of renewable chemicals and biofuels, because competing microbial activities are inhibited at elevated temperatures and thermostable cell wall degrading enzymes are superior to mesophilic enzymes. Here, we report on the development of a platform to produce four different thermostable cell wall degrading enzymes in the chloroplast of Chlamydomonas reinhardtii. The enzyme blend was composed of the cellobiohydrolase CBM3GH5 from C. saccharolyticus, the β‐glucosidase celB from P. furiosus, the endoglucanase B and the endoxylanase XynA from T. neapolitana. In addition, transplastomic microalgae were engineered for the expression of phosphite dehydrogenase D from Pseudomonas stutzeri, allowing for growth in non‐axenic media by selective phosphite nutrition. The cellulolytic blend composed of the glycoside hydrolase (GH) domain GH12/GH5/GH1 allowed the conversion of alkaline‐treated lignocellulose into glucose with efficiencies ranging from 14% to 17% upon 48h of reaction and an enzyme loading of 0.05% (w/w). Hydrolysates from treated cellulosic materials with extracts of transgenic microalgae boosted both the biogas production by methanogenic bacteria and the mixotrophic growth of the oleaginous microalga Chlorella vulgaris. Notably, microalgal treatment suppressed the detrimental effect of inhibitory by‐products released from the alkaline treatment of biomass, thus allowing for efficient assimilation of lignocellulose‐derived sugars by C. vulgaris under mixotrophic growth.     

Combined Cell Surface Display of β‐d‐Glucosidase (BGL), Maltose Transporter (MAL11), and Overexpression of Cytosolic Xylose Reductase (XR) in Saccharomyces cerevisiae Enhance Cellobiose/Xylose Coutilization for Xylitol Bioproduction from Lignocellulosic Biomass

Xylitol is a highly valuable commodity chemical used extensively in the food and pharmaceutical industries. The production of xylitol from d ‐xylose involves a costly and polluting catalytic hydrogenation process. Biotechnological production from lignocellulosic biomass by micro‐organisms like yeasts is a promising option. In this study, xylitol is produced from lignocellulosic biomass by a recombinant strain of Saccharomyces cerevisiae (S. cerevisiae) (YPH499‐SsXR‐AaBGL) expressing cytosolic xylose reductase (Scheffersomyces stipitis xylose reductase [SsXR]), along with a β‐d ‐glucosidase (Aspergillus aculeatus β‐glucosidase 1 [AaBGL]) displayed on the cell surface. The simultaneous cofermentation of cellobiose/xylose by this strain leads to an ≈2.5‐fold increase in Yxylitol/xylose (=0.54) compared to the use of a glucose/xylose mixture as a substrate. Further improvement in the xylose uptake by the cell is achieved by a broad evaluation of several homologous and heterologous transporters. Homologous maltose transporter (ScMAL11) shows the best performance in xylose transport and is used to generate the strain YPH499‐XR‐ScMAL11‐BGL with a significantly improved xylitol production capacity from cellobiose/xylose coutilization. This report constitutes a promising proof of concept to further scale up the biorefinery industrial production of xylitol from lignocellulose by combining cell surface and metabolic engineering in S. cerevisiae.     

Nisin production of Lactococcus lactis N8 with hemin‐stimulated cell respiration in fed‐batch fermentation system

In this study, nisin production of Lactococcus lactis N8 was optimized by independent variables of glucose, hemin and oxygen concentrations in fed‐batch fermentation in which respiration of cells was stimulated with hemin. Response surface model was able to explain the changes of the nisin production of L. lactis N8 in fed‐batch fermentation system with high fidelity (R² 98%) and insignificant lack of fit. Accordingly, the equation developed indicated the optimum parameters for glucose, hemin, and dissolved oxygen were 8 g L^?1 h^?1, 3 μg mL^?1 and 40%, respectively. While 1711 IU mL^?1 nisin was produced by L. lactis N8 in control fed‐batch fermentation, 5410 IU mL^?1 nisin production was achieved within the relevant optimum parameters where the respiration of cell was stimulated with hemin. Accordingly, nisin production was enhanced 3.1 fold in fed‐batch fermentation using hemin. In conclusion the nisin production of L. lactis N8 was enhanced extensively as a result of increasing the biomass by stimulating the cell respiration with adding the hemin in the fed‐batch fermentation. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:678–685, 2015