Characterization of Cellulose Production by a Gluconacetobacter xylinus Strain from Kombucha

The aims of this work were to characterize and improve cellulose production by a Gluconoacetobacter xylinus strain isolated from Kombucha and determine the purity and some structural features of the cellulose from this strain. Cellulose yield in tea medium with both black tea and green tea and in Hestrin and Schramm (HS) medium under both static and agitated cultures was compared. In the tea medium, the highest cellulose yield was obtained with green tea (~0.20 g/L) rather than black tea (~0.14 g/L). Yield in HS was higher (~0.28 g/L) but did not differ between static and agitated incubation. ¹H-NMR and ¹³C-NMR spectroscopy indicated that the cellulose is pure (free of acetan) and has high crystallinity, respectively. Cellulose yield was improved by changing the type and level of carbon and nitrogen source in the HS medium. A high yield of ~2.64 g/L was obtained with mannitol at 20 g/L and corn steep liquor at 40 g/L in combination. In the tea medium, tea at a level of 3 g/L gave the highest cellulose yield and the addition of 3 g/L of tea to the HS medium increased cellulose yield to 3.34 g/L. In conclusion, the G. xylinus strain from Kombucha had different cellulose-producing characteristics than previous strains isolated from fruit. Cellulose was produced in a pure form and showed high potential applicability. Our studies extensively characterized cellulose production from a G. xylinus strain from Kombucha for the first time, indicating both similarities and differences to strains from different sources.     

Cellulose production from<Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> TQ-B2

Gluconobacter oxydans that produces the cellulose was isolated. In order to confirm the chemical features of cellulose, various spectrophtometeric analysis were carried out using electron microscopy, X-ray diffractogram, and CP/MAS¹³C NMR. The purified cellulose was found to be identical to that ofAcetobacter xylinum. For effective production of cellulose, the various carbon and nitrogen sources, mixture of calcium and magnesium ions, and biotin concentration were investigated in flask cultures. Among the various carbon sources, glucose and sucrose were found to be best for the production of cellulose, with maximum concentration of 2.41 g/L obtained when a mixture of 10 g/L of each glucose and sucrose were used. With regard to the nitrogen sources, when 20 g/L of yeast extract was used, the maximum concentration of bacterial cellulose was reached. The concentration of cellulose was increased with mixture of 2 mM of each Ca²⁺ and Mg²⁺. The optimum biotin concentration for the production of cellulose was in the range of 15 to 20 mg/L. At higher biotin concentration (25–35 mg/L), the bacterial cellulose production was lower.     

The effect of pH,temperature and sucrose concentration on high productivity continuous ethanol fermentation using Zymomonas mobilis

Summary A flocculent strain of Zymomonas mobilis was used for ethanol production from sucrose. Using a fermentor with cell recycle (internal and external settler) high sugar conversion and ethanol productivity were obtained. At a dilution rate of 0.5 h^-1 (giving 96% sugar conversion) the ethanol productivity, yield and concentrations respectively were 20 g/l/h, 0.45 g/g and 40 g/l using a medium containing 100 g/l sucrose. At a sucrose concentration of 150 g/l, the ethanol concentration reached 60 g/l. The ethanol yield was 80% theoretical due to levan and fructo-oligomer formation. No sorbitol was detected. This fermentation was conducted at a range of conditions from 30 to 36°C and from pH 4.0 to 5.5.     

Fermentation pattern of sucrose to ethanol conversions by Zymomonas mobilis

General patterns of sucrose fermentation by two strains of Zymomonas mobilis, designated Z7 and Z10, were established using sucrose concentrations from 50 to 200 g/liter. Strain Z7 showed a higher invertase activity than Z10. Strain Z10 showed a reduced specific growth rate at high sucrose concentration while Z7 was unaffected. High sucrose hydrolyzing activity in strain Z7 lead to glucose accumulation in the medium at high sucrose concentrations. Ethanol production and fermentation time depend on the rate of catabolism of the products of sucrose hydrolysis, glucose and fructose. The metabolic quotients for sucrose utilization, q_s, and ethanol production, q_p (g/g·hr), are unsuitable for describing sucrose utilization by Zymomonas mobilis, as the logarithmic phase of growth precedes the phase of highest substrate utilization (g/liter·hr) and ethanol production (g/liter·hr) in batch culture.     

Steps Toward High‐Performance PLA: Economical Production of d‐Lactate Enabled by a Newly Isolated Sporolactobacillus terrae Strain

Optically pure d ‐lactate production has received much attention for its critical role in high‐performance polylactic acid production. However, the current technology can hardly meet the comprehensive demand of industrialization on final titer, productivity, optical purity, and raw material costs. Here, an efficient d ‐lactate producer strain, Sporolactobacillus terrae (S. terrae) HKM‐1, is isolated for d ‐lactate production. The strain HKM‐1 shows extremely high d ‐lactate fermentative capability by using peanut meal, soybean meal, or corn steep liquor powder as a sole nitrogen source; the final titers (205.7 g L^?1, 218.9 g L^?1, and 193.9 g L^?1, respectively) and productivities (5.56 g L^?1 h^?1, 5.34 g L^?1 h^?1, and 3.73 g L^?1 h^?1, respectively) of d ‐lactate reached the highest level ever reported. A comparative genomic analysis between S. terrae HKM‐1 and previously reported d ‐lactate high‐producing Sporolactobacillus inulinus (S. inulinus) CASD is conducted. The results show that many unrelated genetic features may contribute to the superior performance in d ‐lactate production of S. terrae HKM‐1. This d ‐lactate producer HKM‐1, along with its fermentation process, is promising for sustainable d ‐lactate production by using agro‐industrial wastes.     

Bio-hydrogen production from cellulose by sequential co-culture of cellulosic hydrogen bacteria of <Emphasis Type="Italic">Enterococcus gallinarum</Emphasis> G1 and <Emphasis Type="Italic">Ethanoigenens harbinense</Emphasis> B49

Microbial conversion of lignocellulose to hydrogen is a fascinating way to provide a renewable energy source. A mesophilic bacterium strain G1 that had high cellulose degradation and hydrogen production activity (2.38 mmol H₂ g⁻¹ cellulose) was isolated from rumen fluid and identified as the Enterococcus gallinarum. Hydrogen production from cellulose by using sequential co-cultures of a cellulosic-hydrolysis bacterium G1 and Ethanoigenens harbinense B49 was investigated. With an initial Avicel concentration of 5 g l^−l, the sequential co-culture with G1 and strain Ethanoigenens harbinense B49 produced H₂ yield approximately 2.97 mmol H₂ g⁻¹ cellulose for the co-culture system.     

Lactic acid fermentation by Lactobacillus casei in free cell form and immobilised on gluten pellets

A comparative study of the fermentation of a range of carbohydrate substrates, at various temperatures, was carried out using a commercial Lactobacillus casei strain in a free cell form and immobilised on gluten pellets. This strain required yeast extract, l-cysteine HCl and Mn²⁺ at 5, 0.5 and 0.1 g l^–1, respectively, for maximum growth and lactic acid production. Sugar fermentation using free cells showed preference in the order glucose, sucrose, fructose while lactose was poorly utilised. Optimum temperature for growth and lactic acid production over (18–30 h) was 43 °C. L. casei was successfully immobilised on gluten pellets and fermented glucose and sucrose in a shorter time (18 h) with increased lactic acid production (42 and 41 g l^–1 on glucose and sucrose, respectively).     

Production of curdlan using sucrose or sugar cane molasses by two-step fed-batch cultivation of Agrobacterium species

Maltose and sucrose were efficient carbon sources for the production of curdlan by a strain of Agrobacterium sp. A two-step, fed-batch operation was designed in which biomass was first produced, followed by curdlan production which was stimulated by nitrogen limitation. There exists an optimal timing for nitrogen limitation for curdlan production in the two-step, fed-batch operation. Maximum curdlan production (60 g L⁻¹) was obtained from sucrose with a productivity of 0.2 g L⁻¹ h⁻¹ when nitrogen was limited at a cell concentration of 16.0 g L⁻¹. It was also noted that the curdlan yield from sucrose was as high as 0.45 g curdlan g⁻¹ sucrose, and the highest specific production rate was 1.0 g curdlan g⁻¹ cells h⁻¹ right after nitrogen limitation. Of particular importance was the use of molasses as a cheap carbon source to produce curdlan in the two-step, fed-batch cultivation. As high as 42 g L⁻¹ of curdlan with a yield of 0.35 g curdlan g⁻¹ total sugar was obtained after 120 h of fed-batch cultivation. Received 20 August 1996/ Accepted in revised form 26 November 1996     

Construction of the industrial ethanol-producing strain of Saccharomyces cerevisiae able to ferment cellobiose and melibiose

The gene mel1, encoding α-galactosidase in Schizosaccharomyces pombe, and the gene bgl2, encoding and α-glucosidase in Trichoderma reesei, were isolated and co-expressed in the industrial ethanolproducing strain of Saccharomyces cerevisiae. The resulting strains were able to grow on cellobiose and melibiose through simultaneous production of sufficient extracellular α-galactosidase and β-glucosidase activity. Under aerobic conditions, the growth rate of the recombinant strain GC1 co-expressing 2 genes could achieve 0.29 OD600 h⁻¹ and a biomass yield up to 7.8 g l⁻¹ dry cell weight on medium containing 10.0 g l⁻¹ cellobiose and 10.0 g l⁻¹ melibiose as sole carbohydrate source. Meanwhile, the new strain of S. cerevisiae CG1 demonstrated the ability to directly produce ethanol from microcrystalline cellulose during simultaneous saccharification and fermentation process. Approximately 36.5 g l⁻¹ ethanol was produced from 100 g of cellulose supplied with 5 g l⁻¹ melibose within 60 h. The yield (g of ethanol produced/g of carbohydrate consumed) was 0.44 g/g, which corresponds to 88.0% of the theoretical yield.     

Gluconacetobacter sp. gel_SEA623-2, bacterial cellulose producing bacterium isolated from citrus fruit juice

Cellulose producing bacterial strain was isolated from citrus fruit juice fungus. The isolated strain was identified as Gluconacetobacter sp. gel_SEA623-2 based on several morphological characteristics, biochemical tests, and 16S rRNA conducted. Culture conditions for bacterial cellulose production by SEA623-2 were screened in static trays. Conditions were extensively optimized by varying the kind of fruit juice, pH, sugar concentration, and temperature for maximum cellulose production. SEA623-2 has a high productive capacity in citrus processing medium, but not in other fruits. The optimal combination of the media constituents for bacterial cellulose production is as follows: 10% citrus juice, 10% sucrose, 1% acetic acid, and 1% ethanol at 30 °C, pH 3.5. Bacterial cellulose produced by SEA623-2 has soft physical properties, high tensile strength, and high water retention value. The cellulose produced by the selected bacteria is suitable as a cosmetic and medical material.     

Lactosucrose production by various microorganisms harboring levansucrase activity

Production of the artificial sweetener, lactosucrose, by various microorganisms containing levansucrase activity was investigated. Of the tested bacteria, Bacillus subtilis was the most effective producer using lactose as an acceptor and sucrose as a fructosyl donor. Lactosucrose production by this strain was optimal at pH 6.0 and 55 °C whereupon 181 g lactosucrose l^–1 was produced from 225 g lactose l^–1 and 225 g sucrose l^–1 in 10 h.     

Long-term effects of several biochemical and physical factors on cellulose biosynthesis in callus and suspension cultures of normal and mutant barley (Hordeum vulgare L.) strains producing less cellulose

To clarify a low level of cellulose biosynthesis of thein vitro cultured cells, the effects of several biochemical factors such as carbon sources (sucrose, maltose, and UDPG), antioxidants (ascorbic acid and glutathione) and physical factors such as artificial pressure, high gravity, on the cellulose production in barley callus and suspension cultures were investigated. In the suspension culture of two barley strains, the supplement of different concentrations (0, 1.5, 3.0, and 4.5%) of sucrose or maltose into the medium for 30 days did not promote the cellulose production and 4.5% of sugar supplement was rather inhibitory in one strain. However, in the presence of sucrose at 3%, UDPG (3 or 10 mM) supplement, as a precursor for cellulose, promoted 1.2–13 fold of the production in two strains. A low concentration (3 mM) of ascorbic acid and glutathione promoted 1.5 and 1.2 fold of the production in two strains, respectively. These results suggest that low cellulose biosynthesis of thein vitro cultured cells is due to a decreased level of the UDPG in the cytosol, and that the oxidative condition of external medium impedes cellulose synthesis in some manners. Artificial pressure applied to the callus promoted 1.4 fold of the cellulose production. High gravity (5,000 or 10,000g) applied to the suspension-cultured cells by centrifugation did not cause a substantial change.     

Sucrose enhances phosphoenolpyruvate carboxylase activity of in vitro solanum tuberosum L. under non-limiting nitrogen conditions

Summary The effect of sucrose on in vitro potato (ev. Kennebec) metabolism was evaluated. Plants were grown in three different media: Murashige and Skoog basal medium containing high nitrogen concentration with 0 or 20 g l⁻¹ sucrose; or modified medium containing reduced nitrogen amount and 20 g l⁻¹ sucrose. Plants fed with 20 g l⁻¹ sucrose and high N exhibited higher phosphoenolpyruvate carboxylase (PEPC) and pyruvate kinase activities and high PEPC protein concentration at 7, 20 and 33 d of culture compared to those grown with 20 g l⁻¹ sucrose and low N, or with 0 g l⁻¹ sucrose and high nitrogen (control). The highest accumulation of starch and sucrose was found in plants grown with sucrose and low nitrogen. This accumulation occurred concomitantly with a reduced enzyme activity resulting from a low utilization of α-ketoglutarate by nitrogen assimilation, when plants were grown with reduced nitrogen. Our investigations on tricarboxylic acid cycle activity showed that sucrose led to the reduction of organic acid amounts in both leaves and roots when high nitrogen was supplied to plants. This was probably due to the intense exit of α-ketoglutarate, which was confirmed by measurements of cytosolic isocitrate dehydrogenase activity. The low leaf glutamine/glutamate ratio observed in plants grown with 20 g l⁻¹ sucrose and high nitrogen compared to their counterparts cultivated with low nitrogen might be due to glutamine conversion into proteins when nitrogen assimilation was intense. These results demonstrate that sucrose enhanced PEPC activity by increasing protein synthesis. They also suggest that sucrose metabolism is involved in the replenishment of the tricarboxylic acid cycle by providing carbon skeletons required to sustain phosphoenolpyruvate utilization during high nitrate assimilation.     

Continuous production of enzymes under carbon-limited conditions by Trichoderma harzianum P49P11

Carbon-limited chemostat cultures were performed using different carbon sources (glucose, 10 and 20 g/L; sucrose, 10 g/L; fructose/glucose, 5.26/5.26 g/L; carboxymethyl cellulose, 10 g/L; and carboxymethyl cellulose/glucose, 5/5 g/L) to verify the capability of the wild type strain Trichoderma harzianum to produce extracellular enzymes. All chemostat cultures were carried out at a fixed dilution rate of 0.05 h^?1. Experiments using glucose, fructose/glucose and sucrose were performed in duplicate. Glucose condition was found to induce the production of enzymes that can catalyse the hydrolysis of p-nitrophenyl-β-d-glucopyranoside (PNPGase). A concentration of 20 g/L of glucose in the feed provided the highest productivity (1048 ± 16 U/mol h). Extracellular polysaccharides were considered the source of inducers. Based on the obtained results, a new PNPGase production process was developed using mainly glucose. This process raises interesting possibilities of synthesizing the inducer substrate and the induced enzymes in a single step using an easily assimilated carbon source under carbon-limited conditions.     

甘油影响红曲菌产色素的碳源选择性探究

红曲菌(Monascus spp.)是我国重要的药食同源微生物,红曲色素(Monascus pigments,MPs)是其主要次级代谢产物之一。有研究表明,甘油可促进红曲菌产MPs,但作用机制不明。以丛毛红曲菌(Monascus pilosus)MS-1为实验菌株,考察甘油与葡萄糖或蔗糖复合对红曲菌产MPs的影响。在不含碳源的合成培养基中,将甘油与葡萄糖或蔗糖复合,采用分光光度法和高效液相色谱法等分析MPs的产量和组分、生物量及发酵液pH。当甘油与葡萄糖复合,添加甘油后发酵液pH、生物量无显著变化(P0.05),总色价显著降低(P0.05)。当2 g/L或40 g/L甘油与蔗糖复合,发酵液pH显著降低而生物量及总色价显著增加(P0.05)。当40 g/L甘油与蔗糖复合时,总色价是仅以蔗糖为碳源时的16.5倍,且MPs同系物数量明显增多(P0.05)。在合成培养基条件下,甘油促进红曲菌产MPs具有碳源种类的选择性。该结果可为研究甘油影响红曲菌产MPs的作用机制提供参考,为甘油用于MPs生产提供依据。     

Optimization of cellulase production by Penicillium occitanis

The mutant Pol6 of Penicillium occitanis is an interesting strain for producing cellulases and hemicellulases. The nitrogen source and substrate that regulate cellulase production were evaluated in shake-flask and fermentor (batch and fed-batch) culture. The nature of the nitrogen source and the C/N ratio markedly affected cellulase production by P. occitanis. When nitrate was used in Mandels and Weber's basal growth medium with a C/N ratio below 20.2, it resulted in more cellulase production than from urea or ammonium sulphate. Crude substrates such as wheat bran and wheat flour residues, used in combination with a local cellulose esparto grass paper pulp as an alternative nitrogen source and cellulose substrates, also gave high cellulase yields. Greatest cellulase yields and productivity were obtained by fed-batch cultivation [23 filter-paper activity units (FPU)/ml and 168 FPUI^–1h^–1].     

Effect of plant growth regulators and medium composition on cell growth and saponin production during cell-suspension culture of mountain ginseng (Panax ginseng C. A. mayer)

We have established cell-suspension cultures of mountain ginseng (Panax ginseng G A. Mayer), and have attempted to increase the yield of saponin by manipulating our processing method and culturing factors (e.g., media strengths; the presence of plant growth regulators or sucrose; ratios of NO⁺ ₃/ NH^- ₄). Maximum biomass yield was obtained in media containing 2,4-D. However, saponin productivity was much higher in a medium comprising either IBA or NAA; 7.0 mg/L IBA was optimal for promoting both cell growth (10.0 g/L dry weight) and saponin production (7.29 mg/g DW total ginsenoside). Although the addition of cytokinins (BA and kinetin) did not affect cell growth, the level of saponin (particularly in the Rb group) was enhanced when the media were supplemented with either 0.5 mg/L BA or 0.5 mg/L kinetin. Half- and full-strength MS media were equally suitable for inducing both biomass as well as saponin production. We also investigated the effect of various concentrations of sucrose and nitrogen, and found that 30 g/L sucrose enhanced biomass yield as well as saponin content However, further increases (i.e., up to 70 g/L) led to a decrease in saponin accumulation and biomass production. Maximum growth and saponin productivity were reported from treatments with an initial nitrogen concentration of 30 mM. In general, the amount of saponin increased when the test media had high NO⁺ ₃/ NH^- ₄ ratios; in fact, saponin production was greatest when nitrate was the sole nitrogen source.     

Citric acid production from sucrose using a recombinant strain of the yeast Yarrowia lipolytica

The yeast Yarrowia lipolytica is able to secrete high amounts of several organic acids under conditions of growth limitation and carbon source excess. Here we report the production of citric acid (CA) in a fed-batch cultivation process on sucrose using the recombinant Y. lipolytica strain H222-S4(p67ICL1) T5, harbouring the invertase encoding ScSUC2 gene of Saccharomyces cerevisiae under the inducible XPR2 promoter control and multiple ICL1 copies (10–15). The pH-dependent expression of invertase was low at pH 5.0 and was identified as limiting factor of the CA-production bioprocess. The invertase expression was sufficiently enhanced at pH 6.0–6.8 and resulted in production of 127–140 g l⁻¹ CA with a yield Y _CA of 0.75–0.82 g g⁻¹, whereas at pH 5.0, 87 g l ⁻¹ with a yield Y _CA of 0.51 gg⁻¹ were produced. The CA-productivity Q _CA increased from 0.40 g l ⁻¹ h⁻¹ at pH 5.0 up to 0.73 g l ⁻¹ h⁻¹ at pH 6.8. Accumulation of glucose and fructose at high invertase expression level at pH 6.8 indicated a limitation of CA production by sugar uptake. The strain H222-S4(p67ICL1) T5 also exhibited a gene–dose-dependent high isocitrate lyase expression resulting in strong reduction (<5%) of isocitric acid, a by-product during CA production.     

Continuous monitoring of cellulase action on microcrystalline cellulose

Summary Cellobiose oxidase from Phanerochaete chrysosporium was used for continuous monitoring of cellulase action on microcrystalline cellulose (Avicel). Two protocols are described, the parameter monitored being either the decline in electrode potential as ferricyanide is reduced or consumption of dioxygen. Most experiments used a commercial cellulase preparation from Trichoderma reesei and ferricyanide as acceptor. Within 1 min of an addition of cellulase, ferricyanide reduction reached a steady rate. This was converted into a rate of production of substrate for celobiose oxidase, in mol·min^–1. Experiments were conducted either with a constant concentration of cellulase and increasing Avicel, or with constant Avicel and increasing cellulase. Kinetic analysis of the experiments with constant cellulase indicated a K _mof 4.8 ± 1.0 (g cellulose)·1^–1, which was close to the value predicted from binding studies. The specific activity of the cellulase was measured as 375±25 mol·(g cellulase)^–1·min^–1 in experiments with a high cellulose concentration, but was less than half this value when the cellulose was saturated with cellulase. The maximal rate of cellulose degradation was 9.6±1.3 mol·(g cellulose)^–1·min^–1.     

Potential of the genetically transformed root cultures of Plumbago europaea for biomass and plumbagin production

Plumbago europaea L. is the main source of plumbagin which is a well-known pharmacological active compound. In this investigation, genetically transformed roots of P. europaea were obtained by improving some factors affecting the efficiency of Agrobacterium rhizoigenes-mediated transformation such as explant type, A. rhizoigenes strain, bacterial infection period, co-cultivation period and acetosyringone concentration. The leaf, hypocotyl and stem explants from in vitro grown plantlets were infected with bacterial strains (A4, ATCC15834, MSU440 and A13). The highest transformation rate of 69.3% was achieved after 7–9 days by inoculating A. rhizogenes MSU440 strain onto the 3-week-old stem explants followed by a co-cultivation period of 2 days on a medium containing 100 μM acetosyringone. To investigate the existence of the rolB gene, polymerase chain reaction was carried out using specific primers. Effects of growth media (MS, 1/2 MS, MS-B5 and ½ MS-B5), different sucrose concentrations and illumination on biomass production and plumbagin biosynthesis in P. europaea hairy root cultures were analyzed using stem explants after infection with MSU440 strain. ½ MS-B5 liquid medium containing 30 g L⁻¹ sucrose incubated in the dark resulted in the efficient biomass production of transformed hairy roots (12.5 g fresh weight, 1.8 g dry weight) with 3.2 mg g⁻¹ DW plumbagin accumulation. This procedure provides a framework for large-scale cultivation of hairy roots for plumbagin production. This is the first report describing the establishment of P. europaea hairy root culture with special emphasis on plumbagin production.