Production of l-serine from methanol and glycine by resting cells of a methylotroph under automatically controlled conditions

Serine production from methanol and glycine was tried using frozen-thawed resting cells of a methylotroph, Protomonas extorquens NR-1 under multi-variable controlled conditions. The conditions for l-serine formation were optimized at 30°C. The production of l-serine in 0.4% CaCl₂ solution (initial pH 8.2) was the same as in 0.1 M Tris-HCl buffer (initial pH 8.3). Increasing the initial glycine concentration promoted l-serine formation. A high aeration rate decreased l-serine production. The optimum concentrations of dissolved oxygen and methanol were 0.5 ppm and 10 g/l, respectively. The highest l-serine, 24.9 g/l, was obtained at 24 h from 30.94 gl (as dry weight) resting cells using 100 g/l initial glycine with controlled pH. The relationship between the initial rate of l-serine formation and cell concentration indicated an unusual curve due to the effects of the added NaOH which was used for controlling the pH. In similar experiments without control of pH, a normal profile was observed with respect to the relationship between the initial rate of l-serine formation and cell concentration. The highest l-serine, 54.5 g/l, was obtained at 48 h by 36.4 g/l (as dry weight) resting cells. The yield (mol of l-serine/mol of added substrate) of l-serine from methanol and glycine were 8.3% and 39.3%, respectively. The selectivity of l-serine (mol of l-serine/mol of glycine consumed) was 67.9%. The stoichiometry of the maximum l-serine formation showed that the resting cells carried the highly active methanol dehydrogenase while serine transhydroxymethylase was rather low. Serine glyoxalate aminotransferase was not completely inhibited by the high concentration of glycine (about 68% of synthesized l-serine was detected in the supernatant.     

Xylitol production by a methanol yeast,Candida boidinii (Kloeckera sp.) No. 2201

A methanol yeast, Candida boidinii no. 2201, could produce xylitol and also d-xylulose during cultivation on d-xylose medium. These fermentative products were identified by high performance liquid chromatography. A large amount of xylitol was obtained from a d-xylose medium containing ammonium acetate and yeast extract at the initial pH of 7.0. Maximum productivities of xylitol and enzymes concerned with the production were observed after 4–5 d of cultivation. A d-xylose (100 g/l) medium supplemented with 2% (v/v) methanol gave higher amounts of xylitol (48.5 g/l) and d-xylulose (3.3 g/l). Enzyme activities for d-xylose reduction, d-xylulose reduction, d-xylose isomerization, and d-xylulose phosphorylation, which could be involved in the xylitol production, were measured in cell-free extracts during cultivation and a possible pathway of xylitol production was discussed.     

Production of l-Methionine-enriched cells of a mutant derived from a methylotrophic yeast,Candida boidinii

l-Methionine-enriched cells production of an ethionine-resistant mutant of Candida boidinii no. 2201 was greatly improved by the control of pH and by feeding of methanol and other medium components during cultivation in a jar fermentor. Under the optimal conditions, 38.5 g (as dry weight)_of cells abd 282 mg of pool methionine (intracellular pool of free l-methionine) per l of culture broth were obtained after 11 d of cultivation.The culture conditions for production of l-methionine-enriched cells in continuous culture were investigated. With limited methanol in continuous cultivation, pool methionine productivity reached a maximum value of 1.14 mg·l⁻¹·h⁻¹ at a dilution rate of 0.05·h⁻¹. During methanol-limited growth in continuous cultivation, the pool methionine content of the mutant was about 20–35% higher than that in batch cultivation.     

L-Sorbose production in a continuous fermenter with and without cell recycle

The kinetics of continuous l-sorbose fermentation using Acetobacter suboxydans with and without cell recycle (100%) were investigated at dilution rates (D) of 0.05, 0.10, 0.15 and 0.3 h^–1. The biomass and sorbose concentrations for continuous fermentation without recycle increased as the dilution rate was increased from 0.05 to 0.10 h^–1. A maximum biomass concentration of 8.44 g l^–1 and sorbose concentration of 176.90 g l^–1 were obtained at D=0.10 h^–1. The specific rate of sorbose production and volumetric sorbose productivity at this dilution rate were 2.09 g g^–1 h^–1 and 17.69 g l^–1 h^–1. However, on further increasing the dilution rate to 0.3 h^–1, both biomass and sorbose concentrations decreased to 2.93 and 73.20 g l^–1 respectively, mainly due to washout of the reactor contents. However, the specific rate of sorbose formation and volumetric sorbose productivity at this dilution rate increased to 7.49 g g^–1 h^–1 and 21.96 g l^–1 h^–1 respectively. Continuous fermentation with 100% cell recycle served to further enhance the concentration of biomass and sorbose to 28.27 and 184.32 g l^–1 respectively (in the reactor at a dilution rate of 0.05 h^–1). Even though, there was a decline in the biomass and sorbose concentrations to 6.8 and 83.40 g l^–1 at a dilution rate of 0.3 h^–1, the specific rates of sorbose formation and volumetric sorbose productivity increased to 3.67 g g^–1h^–1 and 25.02 g l^–1 h^–1.     

l-serine production from methanol and glycine with an immobilized methylotroph

l-Serine production from methanol and glycine was attempted using immobilized resting cells of a methylotroph, Protomonas extorquens NR 1, under automatically controlled conditions. A Ca-alginate system was selected. The conditions for l-serine formation were optimized at 30°C. A concentration of glycine 100 g·l⁻¹ which was the optimum concentration for l-serine production by free resting cells was used in the reaction mixture. The optimum concentrations of methanol and dissolved oxygen were 20 g·l⁻¹ and 5 ppm, respectively. Under the optimum conditions, 11.3 g·l⁻¹ of l-serine was produced within 36 h. The selectivities (mole of l-serine/mole of substrate consumed) of l-serine from methanol and glycine were 4.5% and 95.1%, respectively. The size of gel beads affected the l-serine formation rate. The initial rate of l-serine formation decreased with an increase in the size of beads. However, the l-serine formation rate increased at elevated concentrations of dissolved oxygen, even with large sized beads. This result implies that the oxygen diffusion inside the gel beads limited the l-serine formation rate. The observed effectiveness factor of the immobilized cells could be estimated by the theoretical effectiveness factor of the zero-order reaction with respect to the dissolved oxygen.Repeated use was not feasible without reactivation of the immobilized cells. Reusability was examined by reactivation of the immobilized resting cells in appropriate media for 12 h. The reactivated immobilized resting cells were used again in the next cycle. By this procedure, several cycles of l-serine formation were made possible.     

Cytochrome c production in jar fermentor by a mutant,methlomonas sp.

The growth and cytochrome c production of Methylomonas sp. YK 56 were optimized by the control of pH, aeration and agitation in a jar fermentor. Under the optimal conditions, 5.8 g of dry cell weight (DCW) and 64 mg of cytochrome c per l of culture broth were obtained. These values were increased to 6.6 g and 76 mg, respectively, by additions of peptone and L-histidine.When methanol and the feed medium were fed during the cultivation, about 160 mg of cytochrome c per l of culture broth was obtained after 34 h of cultivation. In continuous culture, the production rate of the cytochrome c reached a maximum value of 11.6 mg per h at a dilution rate of 0.13 per h.     

Effects of pH and Lactate on Hydrogen Sulfide Production by Oral Veillonella spp.

Indigenous oral bacteria in the tongue coating such as Veillonella have been identified as the main producers of hydrogen sulfide (H₂S), one of the major components of oral malodor. However, there is little information on the physiological properties of H₂S production by oral Veillonella such as metabolic activity and oral environmental factors which may affect H₂S production. Thus, in the present study, the H₂S-producing activity of growing cells, resting cells, and cell extracts of oral Veillonella species and the effects of oral environmental factors, including pH and lactate, were investigated. Type strains of Veillonella atypica, Veillonella dispar, and Veillonella parvula were used. These Veillonella species produced H₂S during growth in the presence of l-cysteine. Resting cells of these bacteria produced H₂S from l-cysteine, and the cell extracts showed enzymatic activity to convert l-cysteine to H₂S. H₂S production by resting cells was higher at pH 6 to 7 and lower at pH 5. The presence of lactate markedly increased H₂S production by resting cells (4.5- to 23.7-fold), while lactate had no effect on enzymatic activity in cell extracts. In addition to H₂S, ammonia was produced in cell extracts of all the strains, indicating that H₂S was produced by the catalysis of cystathionine γ-lyase (EC 4.4.1.1). Serine was also produced in cell extracts of V. atypica and V. parvula, suggesting the involvement of cystathionine β-synthase lyase (EC 4.2.1.22) in these strains. This study indicates that Veillonella produce H₂S from l-cysteine and that their H₂S production can be regulated by oral environmental factors, namely, pH and lactate.     

Pyruvate production by Enterococcus casseliflavus A-12 from gluconate in an alkaline medium

A newly isolated lactic acid bacterium, Enterococcus casseliflavus A-12, produced pyruvic acid (16 g/l) during aerobic culture in an alkaline medium containing sodium gluconate (50 g/l) as the carbon source. The production was dependent on the pH of the culture, the optimum initial pH being 10.0. With static culture, the organism produced lactic acid (2.7 g/l) from both gluconate and glucose. Pyruvate did not accumulate in growing cultures on glucose, but resting cells obtained from a culture on gluconate produced pyruvate from glucose as well as gluconate. The enzyme profiles of the organism, which grew on gluconate and glucose, suggested that gluconate was metabolized via the Entner-Doudoroff and Embdem-Meyerhof-Parnas pathways in aerobic culture, and that glucose was oxidized mainly via the latter pathway under both aerobic and anaerobic conditions. Gluconokinase, a key enzyme in the aerobic metabolism of gluconate, was partially purified from this strain and characterized.     

Rhamnolipid biosurfactant production by Pseudomonas nitroreducens immobilized on Ca2+ alginate beads and under resting cell condition

Pseudomonas nitroreducens MILB-8054A isolated from petroleum-contaminated soil, immobilized on calcium alginate beads, and under resting cell condition, produced biosurfactants. Immobilized cells gave a best yield of 5.6 g rhamnolipid l^?1 using sucrose as carbon source. Time course study using resting cells showed that 2 % v/v of palm oil (preculture carbon source) and 10 % diesel (carbon source) gave the best rhamnolipid yield of 5.1 g l^?1 at pH 8 and temperature of 30 °C. Carbon utilization by resting cells was compared with that of growing cells. The best biosurfactant recovery procedure was acetone extraction.     

Ethanol production from whey permeate by immobilized yeast cells

The ability of two yeast strains to utilize the lactose in whey permeate has been studied. Kluyveromyces marxianus NCYC 179 completely utilized the lactose (9.8%), whereas Saccharomyces cerevisiae NCYC 240 displayed an inability to metabolize whey lactose for ethanol production. Of the two gel matrices tested for immobilizing K. marxianus NCYC 179 cells, sodium alginate at 2% (w/v) concentration proved to be the optimum gel for entrapping the yeast cells effectively. The data on optimization of physiological conditions of fermentation (temperature, pH, ethanol concentration and substrate concentration) showed similar effects on immobilized and free cell suspensions of K. marxianus NCYC 179, in batch fermentation. A maximum yield of 42.6 g ethanol l^?1 (82% of theoretical) was obtained from 98 g lactose l^?1 when fermentation was carried at pH 5.5 and 30°C using 120 g dry weight l^?1 cell load of yeast cells. These results suggest that whey lactose can be metabolized effectively for ethanol production using immobilized K. marxianus NCYC 179 cells.     

Biosynthesis of lipids by Rhodosporidium toruloides ATCC 10788

The limiting amount of nitrogen required to trigger lipid accumulation in the oleaginous yeast Rhodosporidium toruloides ATCC 10788 was studied, batchwise, by subjecting washed mid-exponentially grown cells to nitrogen at levels of 10⁻² M down to 10⁻⁴ M per g l⁻¹ of lean cells (2–5% fat content) in a mineral medium where glucose was present at 35 g l⁻¹. The results showed that lipid accumulation always started sometime after nitrogen reached a level of 3 × 10⁻⁵ M and the specific initial lipid productivity was constant. Furthermore, the cells were subjected to nine combinations of temperature and pH, from (25° C, pH 4.5) to (35° C, pH 7.5) in the mineral medium supplemented with 0.5 g l⁻¹ of yeast extract and 1 g l⁻¹ (NH₄)₂SO₄. As was expected, lipid content in the cells was higher at 25° C, but pH around 6.0–7.5 slightly enhanced the effect of lower temperature. The effect of pH was also noticed to affect the size of changes in the temporal profiles of the oil's fatty acid distribution prior to nitrogen depletion, whereas no significant difference in the fatty acid composition of the oil was shown after exhaustion of nitrogen from the medium for all combinations of temperature and pH.     

Production of 10-hydroxy-12,15(Z,Z)-octadecadienoic acid from α-linolenic acid by permeabilized cells of recombinant Escherichia coli expressing the oleate hydratase gene of Stenotrophomonas maltophilia

Recombinant Escherichia coli, expressing the oleate hydratase gene of Stenotrophomonas maltophilia, was permeabilized by sequential treatments with 0.125 M NaCl and 2 mM EDTA. The optimal conditions for the production of 10-hydroxy-12,15(Z,Z)-octadecadienoic acid from α-linolenic acid by permeabilized cells were 35 °C and pH 7.0 with 0.1 % (v/v) Tween 40, 50 g permeabilized cells l^?1, and 17.5 g α-linolenic acid l^?1. Under these conditions, permeabilized cells produced 14.3 g 10-hydroxy-12,15(Z,Z)-octadecadienoic acid l^?1 after 18 h, with a conversion yield of 82 % (g/g) and a volumetric productivity of 0.79 g l^?1 h^?1. These values were 17 and 168 % higher than those obtained by nonpermeabilized cells, respectively. The concentration, yield, and productivity of 10-hydroxy-12,15(Z,Z)-octadecadienoic acid obtained by permeabilized cells are the highest reported thus far.     

Rifamycin B production by Nocardia mediterranei immobilized in a dual hollow fibre bioreactor

Continuous production of rifamycin B was studied using Nocardia mediterranei (ATCC 21789) immobilized in a dual hollow fibre bioreactor designed for cultivating aerobic cells. In the reactor operation the volumetric productivity based on the volume occupied by the immobilized cells was 108 mg l⁻¹ h⁻¹ when air was used for aeration and was 143 mg l⁻¹ h⁻¹ with pure oxygen. These corresponded to 22 and 30-fold increases over the productivity of the comparable batch system. These high productivities were due to the high cell mass density of 550 g l⁻¹. However, the specific productivity of the cell was 30–40% of that in the shake flask culture. As the residence time of medium in the reactor increased, pH of effluent rose to an alkaline region that was outside its optimum condition (pH 6.5–7.0) and the yield and productivity decreased.     

Effect of tannins on growth and amylase production by Calvatia gigantea

The effect of tannins was investigated on growth and α-amylase (α-1,4-glucan 4-glucanohydrolase, EC 3.2.1.1) production by the edible fungal species Calvatia gigantea, grown in a laboratory-scale fermenter on acorn starch media containing up to 2 g tannins l⁻¹. No inhibition of both growth and amylase excretion was observed when the fungus was cultivated on media containing 40 to 100 times higher tannin concentration than that reported to inhibit microbial growth. Amylase excretion was enhanced when starch was dry sterilized but specific growth rate was higher when starch was wet sterilized. Biomass and amylase production increased with increasing substrate concentration and specific growth rate reached its maximum value at 20 g l⁻¹ starch concentration. The optimum pH of biomass and amylase productionwas 5.0–5.5 and 6.0−6.5 respectively and that of temperature was 29–32 and 29–30°C respectively. Maximum yields of 68 250 U amylase and 0.58–0.60 g biomass g⁻¹ acorn were obtained at optimum growth conditions. A plot of reciprocal growth rate vs. reciprocal starch concentration made it possible to calculate K_s = 0.84 g acorn starch l⁻¹ and μ_max = 0.249 h⁻¹.     

Efficient bioconversion of <Emphasis Type="SmallCaps">l</Emphasis>-glutamate to γ-aminobutyric acid by <Emphasis Type="Italic">Lactobacillus brevis</Emphasis> resting cells

This work investigated the efficient bioconversion process of l-glutamate to GABA by Lactobacillus brevis TCCC 13007 resting cells. The optimal bioconversion system was composed of 50 g/L 48 h cultivated wet resting cells, 0.1 mM pyridoxal phosphate in glutamate-containing 0.6 M citrate buffer (pH 4.5) and performed at 45 °C and 180 rpm. By 10 h bioconversion at the ratio of 80 g/L l-glutamic acid to 240 g/L monosodium glutamate, the final titer of GABA reached 201.18 g/L at the molar bioconversion ratio of 99.4 %. This process presents a potential for industrial and commercial applications and also offers a promising feasibility of continuous GABA production coupled with fermentation. Besides, the built kinetics model revealed that the optimum operating conditions were 45 °C and pH 4.5, and the bioconversion kinetics at low ranges of substrate concentration (0 < S < 80 g/L) was assumed to follow the classical Michaelis–Menten equation.     

Efficient production of α-ketoglutarate in the <Emphasis Type="Italic">gdh</Emphasis> deleted <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> by novel double-phase pH and biotin control strategy

Production of l-glutamate using a biotin-deficient strain of Corynebacterium glutamicum has a long history. The process is achieved by controlling biotin at suboptimal dose in the initial fermentation medium, meanwhile feeding NH₄OH to adjust pH so that α-ketoglutarate (α-KG) can be converted to l-glutamate. In this study, we deleted glutamate dehydrogenase (gdh1 and gdh2) of C. glutamicum GKG-047, an l-glutamate overproducing strain, to produce α-KG that is the direct precursor of l-glutamate. Based on the method of l-glutamate fermentation, we developed a novel double-phase pH and biotin control strategy for α-KG production. Specifically, NH₄OH was added to adjust the pH at the bacterial growth stage and NaOH was used when the cells began to produce acid; besides adding an appropriate amount of biotin in the initial medium, certain amount of additional biotin was supplemented at the middle stage of fermentation to maintain a high cell viability and promote the carbon fixation to the flux of α-KG production. Under this control strategy, 45.6 g/L α-KG accumulated after 30-h fermentation in a 7.5-L fermentor and the productivity and yield achieved were 1.52 g/L/h and 0.42 g/g, respectively.     

Growth characteristics and corrinoid production of Methanosarcina barkeri on methanol-acetate medium

Methanosarcina barkeri strain Fusaro was grown on a mixed substrate medium of methanol and acetate. When 50 mM of acetate was added to the methanol basal medium (250 mM), the rates of methane production, methanol consumption, cell growth and corrinoid production were stimulated 3.2, 2.7, 3.5, and 2.4 times, respectively compared with those in methanol alone. Addition of acetate also has significant influence on corrinoid distribution decreasing the intracellular corrinoid content from 6.8 to 3.0 mg/g dry cell and increasing the extracellular corrinoid concentration from 4.0 to 5.4 mg/l. The carbon balance analysis for methanogenesis and cellular growth with or without acetate addition revealed that about 50% of the utilized acetate carbon might be incorporated in the cellular materials and the remaining might be oxidized to generate the electrons which stimulate the methanol reduction to methane, accelerating the metabolic activities of the methanogenesis from methanol consequently enhancing the rates of methane and corrinoid production, and cell growth.     

Production of peroxidase with horseradish hairy root cells in a two step culture system

Horseradish hairy root cells transformed by a soil bacterium Agrobacterium rhizogenes had peroxidase (POD) activity comparable to that of the original plant root tubers. To enhance POD production by the hairy root culture, various additives to the medium were tested including casein hydrolysates and plant extracts. Polypepton addition had a significant effect on the growth and POD production; at low concentrations (below 1 g/l) the growth was stimulated, while at high concentrations (3–10 g/l), POD activity in the cells was enhanced in spite of a low growth rate. Therefore, the hairy roots were at first cultured in the medium with 1 g/l Polypepton, and then 5 g/l Polypepton was added to enhance intracellular POD activity. POD activity in this two step culture system was 5.4 times higher than that in conventional culture in Polypepton-free medium.     

Chromate reduction by resting cells of Achromobacter sp. Ch-1 under aerobic conditions

Chromate reduction was carried out by resting cells of Achromobacter sp. Ch-1 with lactate as electron donor under aerobic conditions. The reduction activity of the samples supplemented with lactate was two times as those without lactate. The reduction rate was influenced by initial pH and lactate concentration. Under the optimal conditions, pH 9.0 and 4000 mg l⁻¹ lactate supplement, reduction rate was 5.45 mg l⁻¹ min⁻¹. The reduction rate decreased with increasing of Cr(VI) concentrations and increased with cell densities proportionally. The maximum reduction limit of Ch-1 cells was obtained at 2107 mg l⁻¹ of Cr(VI).     

Production of a novel compound, 10,12-dihydroxystearic acid from ricinoleic acid by an oleate hydratase from Lysinibacillus fusiformis

A recombinant oleate hydratase from Lysinibacillus fusiformis converted ricinoleic acid to a product, whose chemical structure was identified as the novel compound 10,12-dihydroxystearic acid by gas chromatograph/mass spectrometry, Fourier transform infrared, and nuclear magnetic resonance analysis. The reaction conditions for the production of 10,12-dihydroxystearic acid were optimized as follows: pH?6.5, 30 °C, 15 g?l^?1 ricinoleic acid, 9 mg?ml^?1 of enzyme, and 4 % (v/v) methanol. Under the optimized conditions, the enzyme produced 13.5 g?l^?1 10,12-dihydroxystearic acid without detectable byproducts in 3 h, with a conversion of substrate to product of 90 % (w/w) and a productivity of 4.5 g?l^?1?h^?1. The emulsifying activity of 10,12-dihydroxystearic acid was higher than that of oleic acid, ricinoleic acid, stearic acid, and 10-hydroxystearic acid, indicating that 10,12-dihydroxystearic acid can be used as a biosurfactant.