Enhanced production of N-acetyl-d-neuraminic acid by multi-approach whole-cell biocatalyst

N-Acetyl-d-neuraminic acid (Neu5Ac) has attracted considerable interest due to its promising potential applications in medicine. Significant efforts have been made in whole-cell biocatalyst for Neu5Ac production, but the processes often result in suboptimal performance due to poor expression of enzymes, imbalances of pathway components, disturbance of competing pathways, and barriers of mass transport. In this study, we engineered Escherichia coli strains capable of producing Neu5Ac by assembling a two-step heterologous pathway consisting of N-acetyl-d-glucosamine 2-epimerase (AGE) and Neu5Ac aldolase (NanA). Multiple approaches were used to improve the efficiency of the engineered pathway and process for enhanced Neu5Ac production. Firstly, we identified that NanA was the rate-controlling enzyme in this pathway. With increased expression of NanA, a ninefold increase in Neu5Ac production (65 mM) was observed. Secondly, knocking out nanTEK genes blocked Neu5Ac uptake and the competing pathway, which kept the reactions to the synthetic direction as the final product went outside of the cells and enhanced the Neu5Ac production by threefold, resulting in 173.8 mM of Neu5Ac. Thirdly, we improved the performance of the system by promoting substrate transport and optimizing concentrations of substrates. An overall whole-cell biocatalytic process was developed and a maximum titer of 240 mM Neu5Ac (74.2 g/L) was achieved, with productivity of 6.2 g Neu5Ac/L/h and conversion yield of 40 % from GlcNAc. The engineered strain could be reused for at least five cycles with a productivity of >6 g/L/h. It is a cost-effective process for Neu5Ac production with potential applications in large-scale industrial production.     

d(−)lactic acid production by suspended and aggregated continuous cultures of Bacillus laevolacticus

Summary A new method of d(–)lactic acid production based on the aggregated form of growth of Bacillus laevolacticus in continuous culture in an anaerobic gaslift reactor is presented. With glucose as the substrate a bacterial dry weight of 25 g·1^–1 and a lactic acid production rate of 13 g·1^–1·h^–1 was attained. In conventional glucose-limited chemostat cultures elevated levels of lactic acid stimulated specific lactic acid production while the formation rates of other end-products remained unaffected. In glucose-limited aggregated cultures lactic acid positively influenced the aggregation of cells, improving the volumetric production rate. It is concluded that lactic acid itself is a positive effector in the optimisation of lactic acid production with aggregated cultures of B. laevolacticus.Offprint requests to: J. P. de Boer     

In vivo utilization ofd(−)-3-hydroxybutyrate by chick brain and spinal cord

The in vivo utilization ofd-3-hydroxy[3-¹⁴C]butyrate for oxidation in the whole animal and for lipid and amino acid synthesis in brain and spinal cord of overnight-fasted 15-day-old chicks has been measured. Appreciable amounts of injected 3-hydroxy[3-¹⁴C]butyrate were expired as¹⁴CO₂ one hour after injection, the total amount of which increased with increasing dosages. Lipid synthesis was high in both brain and spinal cord. Free, cholesterol and phospholipids were the main lipids labeled in both, tissues, increasing with time after injection up to 120 min. The incorporation of radioactivity into triglycerides, esterified cholesterol and free fatty acids was not time-dependent. Increased concentrations of 3-hydroxybutyrate gave rise to higher synthetic rates both in brain and spinal cord The rate of amino acid synthesis was slightly higher in brain than in spinal cord. Glutamate was always the major amino acid formed.     

Enhanced α-ketoglutaric acid production and recovery in Yarrowia lipolytica yeast by effective pH controlling

The replacement of chemical synthesis by environmentally friendly energy-efficient technologies for production of valuable metabolites is a principal strategy of developing biotechnological industry all over the world. In the present study, we develop a method for α-ketoglutaric acid (KGA) production from rapeseed oil with the use of Yarrowia lipolytica yeast. Sixty strains of Y. lipolytica yeasts were tested for their ability to produce KGA, and the strain Y. lipolytica 212 (Y. lipolytica VKM Y-2412) was selected as a promising KGA producer. Using a three-stage pH controlling, in which pH was 4.5 in the growth phase, then since 72 to 144 h, pH was maintained at 3.5 and in the later phase of acid production, the titration by KOH was switch off, selected strain produced 106.5 g l^?1 of KGA with mass yield of 0.95 g g^?1. KGA in the form of monopotassium salt was isolated from the culture broth and purified. The isolation procedure involved separation of biomass, extraction of residual triglycerides, filtrate bleaching, and acidification with mineral acid (to pH 2.8–3.4), concentration, precipitation of mineral salts, and crystallization of the product. The purity of KGA isolated from the culture filtrate reached 99.1 %.     

R-(−)-mandelic acid production from racemic mandelic acids by Pseudomonas polycolor with asymmetric degrading activity

The microbial asymmetric degradation of S-(+)-mandelic acid was investigated in order to develop a practical process for R-(−)-mandelic acid production from racemic mandelic acids. Among the 790 culture strains tested, microorganisms belonging to the Brevibacterium, Pseudomonas, Rhodococcus, Rhodotorula, Rhodosporidium, Sporobolomyces and Gibberella genera exhibited high S-(+)-mandelic acid degrading activity. Pseudomonas polycolor IFO 3918 was determined to be the best strain and used as a biocatalyst for eliminating the S-(+)-isomer. The maximum rate of S-(+)-isomer degradation was obtained at 30°C and pH 7.0. Under these optimal conditions, the S-(+)-isomer in a racemic mandelic acid 45 g/l mixture was completely degraded within 24 h, with 20 g of R-(−)-mandelic acid per liter remaining in the reaction mixture. Crystalline R-(−)-mandelic acid with a chemical purity greater than 99% and optical purity of 99.9% enantiomeric excess was obtained at a yield of 35% by acidification of the reaction mixture, extraction with ethyl acetate and subsequent concentration.     

Enhanced production of succinic acid from methanol–organosolv pretreated Strophanthus preussii by recombinant Escherichia coli

Bioprocess and Biosystems Engineering - A biorefinery process for high yield production of succinic acid from biomass sugars was investigated using recombinant Escherichia coli. The major problem...     

L-lysine production at 65°C by auxotrophic-regulatory mutants ofBacillus stearothermophilus

Summary The amino acid L-lysine was produced from auxotrophic-regulatory mutants ofBacillus stearothermophilus at a temperature of 60–65°C. One of the mutants (AEC 12 A5, S-(2-aminoethyl)-cysteine^r, homoserine^–), produced L-lysine at the concentration of 7.5 g/l in shaken flasks in minimal medium containing 5% glucose. Culture conditions for optimizing L-lysine production were not investigated. The aspartokinase activity of the wild strainB. stearothermophilus Zu 183 was inhibited by lysine alone and by threonine plus lysine. AEC resistant mutants showed an aspartokinase activity genetically desensitized to the feedback inhibition. Optimal temperature and pH of aspartokinase were 45°C and 9.5, respectively. The data provide significant evidence that mutants of the speciesB. stearothermophilus have a potential value for amino acid production.     

Cell-associated acid β-xylosidase production by Penicillium sclerotiorum

In recent decades, β-xylosidases have been used in many processing industries. In this work, the study of xylosidase production by Penicillium sclerotiorum and its characterization are reported. Optimal production was obtained in medium supplemented with oat spelts xylan, pH 5.0, at 30 °C, under stationary condition for six days. The optimum activity temperature was 60 °C and unusual optimum pH 2.5. The enzyme was stable at 50 and 55 °C, with half-life of 240 and 232 min, respectively. High pH stability was verified from pH 2.0 to 4.0 and 7.5. The β-xylosidase was strongly inhibited by divalent cations, sensitive to denaturing agents SDS, EDTA and activated by thiol-containing reducing agents. The apparent V_max and K_m values was 0.48 μmol PNXP min^?1 mg^?1 protein and 0.75 mM, respectively. The enzyme was xylose tolerant with a K_i of 28.7. This enzyme presented interesting characteristics for biotechnological process such as animal feed, juice and wine industries.     

β-hydroxypropionic acid production by Byssochlamys sp. grown on acrylic acid

A strain of Byssochlamys sp. produced -hydroxypropionic acid when grown on media containing high concentrations of acrylic acid. The maximal production of -hydroxypropionic acid was 4.8% when the initial culture medium contained 7% acrylic acid and 2% glucose, and the initial culture pH was adjusted to 7.0. -Hydroxypropionic acid production from acrylic acid depended greatly on the pH of the culture medium. Calcium hydroxide was the best neutralizer. Correspondence to: K. Takamizawa     

Enhanced β-lactam antibiotic production by coimmobilization of fungus and alga

Summary It was determined thatCephalosporium acremonium, an oxygenconsuming fungus, had a symbiotic relationship withChlorella pyrenoidosa, an oxygen-generating alga. The fungus and the alga were coimmobilized by entrapment in calcium alginate beads. The production rate of -lactam antibiotics was evaluated at various ratios of the fungus and the alga cells in the free and immobilized states. When the ratio of fungus to alga was one to eight in free mixed culture, the production rate of -lactam antibiotics was 240% of the rate in the presence of fungus alone in the free state. In coimmobilized cell system, the increased amount was 370% in comparison with immobilized fungus alone.     

Continuous production of D-β-hydroxyisobutyric acid from methacrylic acid by Candida rugosa

Summary Continuous production of D- -hydroxyisobutyric acid (D-HIBA) from methacrylic acid (MA) using Candida rugosa IFO 0750 was most efficient under ammonium-limited conditions, whereas D-HIBA was not detected under glucose-limited conditions. As high as 21.5 g D-HIBA/l with 55% molar conversion yield from MA was obtained at a dilution rate of 0.04 h^-1.     

α-Ketoglutaric acid production by Yarrowia lipolytica and its regulation

The yeast Yarrowia lipolytica VKM Y-2412 was selected as a prospective producer of ??-ketoglutaric acid (KGA) from ethanol. The following peculiarities were found: (1) the intensive KGA production occurred only under the limitation of cell growth by thiamine and the excess of ethanol and nitrogen, (2) the production of KGA from ethanol required increased amount of zinc and iron ions, and (3) KGA production increased significantly with a high aeration at pH medium equal to 3.5. Under optimal conditions, the Y. lipolytica VKM Y-2412 produced up to 172?g?l^?1 of KGA with the mass yield coefficient of 0.70?g?g^?1.     

Enhanced ε-poly-l-lysine production by inducing double antibiotic-resistant mutations in Streptomyces albulus

Bioprocess and Biosystems Engineering - ε-Poly-l-lysine (ε-PL), as a food additive, has been widely used in many countries. However, its production still needs to be improved. We...     

Effect of inhibitors on acid production by baker’s yeast

Glucose-induced acid extrusion, respiration and anaerobic fermentation in baker’s yeast was studied with the aid of sixteen inhibitors. Uranyl(2+) nitrate affected the acid extrusion more anaerobically than aerobically; the complexing of Mg²⁺ and Ca²⁺ by EDTA at the membrane had no effect. Inhibitors of glycolysis (iodoacetamide, N-ethylmaleimide, fluoride) suppressed acid production markedly, and so did the phosphorylation-blocking arsenate. Fluoroacetate, inhibiting the citric-acid cycle, had no effect. Inhibition by uncouplers depended on their pK_a values: 2,4,6-trinitrophenol (pK_a 0.4) < 2,4-dinitrophenol (4.1) < azide (4.7) < 3-chlorophenylhydrazonomalononitrile (6.0). Inhibition by trinitrophenol was only slightly increased by its acetylation. Cyanide and nonpermeant oligomycin showed practically no effect; inhibition by dicyclohexylcarbodiimide was delayed but potent. The concentration profiles of inhibition of acid production differed from those of respiration and fermentation. Thus, though the acid production is a metabolically dependent process, it does not reflect the intensity of metabolism, except partly in the first half of glycolysis.     

α-Ketoglutaric acid production from rapeseed oil by Yarrowia lipolytica yeast

The possibility of using rapeseed oil as a carbon source for microbiological production of α-ketoglutaric acid (KGA) has been studied. Acid formation on the selective media has been tested in 26 strains of Yarrowia lipolytica yeast, and the strain Y. lipolytica VKM Y-2412 was selected as a prospective producer of KGA from rapeseed oil. KGA production by the selected strain was studied in dependence on thiamine concentration, medium pH, temperature, aeration, and concentration of oil. Under optimal conditions (thiamine concentration of 0.063 μg?g cells^?1, pH?3.5, 30 °C, high dissolved oxygen concentration (pO₂) of 50 % (of air saturation), and oil concentration in a range from 20 to 60 g?l^?1), Y. lipolytica VKM Y-2412 produced up to 102.5 g?l^?1 of KGA with the mass yield coefficient of 0.95 g?g^?1 and the volumetric KGA productivity (Q _KGA) of 0.8 g?l^?1?h^?1.     

Enhanced production of δ-aminolevulinic acid, bilipigments, and antioxidants from tropical algae of India

We studied the enhanced production of high quality biomass, δ-aminolevulinic acid (δ-ALA), bilipigments, and antioxidants from five tropical blue green algae (cyanobacteria) in a full factorial design using free and immobilized cells in batch culture. Production of nutraceuticals was high in spray dried powder prepared from immobilized cell cultures. Nostochopsis lobatus showed superiority over rest of the species with respect to bilipigments, δ-ALA, nutritive value, antioxidant capacity, and ascorbate oxidase (APX) activity. Antioxidative capacity of phycobiliproteins extracted from these cyanobacteria (121.15 μM TE/g, Nostoc verrucosum to 217.62 μM TE/g, Nostochopsis lobatus) was invariably higher than those observed for higher plant sources and substantially increased under immobilized cell culture condition. Antioxidative enzyme, ascorbate oxidase remained stable in dry food preparations with considerably high activity under immobilized cell preparations (APX_max, 3.40 μmol/min/mg chlorophyll). These observations have important connotations in light of upcoming food and nutraceutical industries in the global market. Use of immobilized cells in batch culture could be an effective approach for scaling up production for commercial use.     

Enhancement of γ-linolenic acid production by Mucor ambiguus with nonionic surfactants

Summary -Linolenic acid (GLA) production by Mucor ambiguus IFO 6742, immobilised in Biomass Support Particles (BSPs), has been investigated in a fluidized-bed fermenter in the presence of nonionic surfactants. In this system, repeated batch cultivation was achieved at higher yield and productivity than by conventional methods, since microbial lipids inlcuding GLA were significantly secreted into the culture broth and/or on the surface of the cell wall.