A shaking bioreactor equipped with twin ceramic membranes for acetic acid production using Acetobacter pasteurianus

A shaking bioreactor system with twin internal ceramic membranes was developed for effective perfusion culture and applied to the continuous production of acetic acid using Acetobacter pasteurianus. The system makes it possible to carry out the back-washing of the membrane without stopping the continuous operation because one membrane can be washed by medium feed flow while another membrane provides filtration of the broth by the simple switching of the medium and the broth flow direction. The medium flow through the membrane could successfully wash the surface of the membrane thereby effectively maintaining the filtration ability. By using the system, continuous operation of more than 800 h was achieved and the maximum acetic acid productivity reached 13.4 g l^–1 h^–1 using air enriched with 40% O₂.     

Stimulation of citric acid production in Aspergillus niger by addition of viscous substances in shake culture

When glucose (120mg/ml) was used as a carbon source, Aspergillus niger Yang no. 2. showed a markedly low citric acid productivity in shake culture (15.4 mg/ml) but a high productivity in semi-solid and surface cultures (72.3 mg/ml and 67.6 mg/ml, respectively). Since the viscosity of the medium was assumed to be one of the important factors for citric acid productivity in shake culture, the effects of the addition of viscous substances on citric acid productivity of strain Yang no. 2 were examined. The addition of 2.0–6.0 mg gelatin/ml as a viscous additive to the medium containing glucose as a carbon source increased slightly the medium viscosity but substantially increased the citric acid productivity in shake culture to levels of 52.0–53.3 mg/ml, about 3.4 times as much as that without gelatin. However, no influence of gelatin addition was observed in semi-solid and surface cultures, i.e. under static cultivation conditions. Different mycelial morphologies of the strain were observed when cultivations were done in shake culture with or without the addition of gelatin. Addition of 5.0 mg agar/ml, 5.0 mg carageenan/ml, 2.5 mg carboxymethylcellulose/ml and 2.5 mg polyethylene glycol 6000/ml, to the medium containing glucose as a carbon source also increased the citric acid productivity in shake culture to levels of 39.2–54.7 mg/ml. Since Yang no. 2 does not utilize these viscous substances, these results suggested that the viscous substances functioned as protectants for the mycelium from physiological stresses due to shaking and as a consequence resulted in a remarkably increased citric acid productivity in shake culture.     

Utilization of Hydrocarbons by Microorganisms

The accumulation of vitamin B₂ by Pichia guilliermondii Wickerham grown on hydrocarbon was investigated. Addition of the following materials stimulated vitamin B₂ production: metal ions such as ferrous, cobalt, manganese, and calcium ions; organic nutrients such as yeast extract and casamino acid; amino acids such as proline and arginine; vitamins such as B₁, nicotinic acid, inositol, and p-aminobenzoic acid. Optimal aeration rate for vitamin B2 production was obtained in a 500-ml shaking flask containing 75 ml of the medium.     

Riboflavin Biosynthesis by Candida robusta

During the study on the oxidative sugar metabolism of yeasts, it was found that six strains of Candida robusta, isolated from fruits, produced large amounts of yellow pigment in shaking culture and this pigment was identified as riboflavin. Riboflavin production by C. robusta has never been reported.

Some notable characteristics of C. robusta in riboflavin production were found. As nitrogen sources, ammonium salts and urea were favorable, but nitrate and organic nitrogen sources such as glycine, asparagine and peptone were not utilized for riboflavin production. Riboflavin was not produced in still culture; a highly aerobic condition, as may be obtained by shaking culture, wa, essential. The addition of excess CaCO₃ was also necessary. Acetic acid, added as the Ca salt in its production as a sole carbon source, was more effective than sugars and optimum concentration of this acid was 7%. Riboflavin were obtained in yields as high as 32 to 34 mg % from the acetate medium after 8 days.     

Production,Purification and Properties of Ribonuclease from Aspergillus niger

Aspergillus niger NRC–A–1–233 was cultivated by the shaking method. The optimal cultural conditions for ribonuclease (RNase) production were: composition of medium: sucrose, 15%; NH₄NO₃, 0.2%; KH₂PO₄, 0.1%; MgSO₄·7 aq., 0.025%; initial pH, 2.2; shaking conditions: 50 ml of medium /500 ml flask; cultivation time, 120 hr. The RNase was purified by acid clay treatment and chromatography on DEAE-cellulose and Sephadex G–75 columns. The purified RNase was homogeneous by ultracentrifuge and disc electrophoresis.

The molecular weight of the RNase was estimated to be 28,500 on SDS-polyacrylamide gel and its isoelectric point was 2.8 by Ampholine electrofocusing method. Digestion rate of RNA by the RNase was 100%. The RNase did not have an exact base specificity and produced four kinds of 3′-nucleotides from yeast RNA.     

Continuous production of gibberellic acid in a fixed-bed reactor by immobilized mycelia of Gibberella fujikuroi in calcium alginate beads

Summary The continuous production of gibberellic acid with immobilized mycelia of Gibberella fujikuroi was maintained over a hundred days in a tubular fixed-bed reactor. Free mycelium at the beginning of the storage phase was harvested from G. fujikuroi shake-flask culture and was immobilized by ionotropic gelation in calcium alginate beads.The continuous recycle production system consisted of a fixed-bed reactor, a container in which the culture medium was heated, stirred and aerated, and valves for sample withdrawal or reactant addition during the first 1320 h (55 days). A two-phase continuous extractor was then added for the last 960 hours (40 days). Free and immobilized mycelium shake-flask cultures with the same strain used in the continuous culture system were also realized to compare growth, maintenance and production parameters. The results show about the same gibberellic acid productivity in both free and immobilized mycelium shakeflask cultures: 0.384 and 0.408 mgGA₃·gBiomass^-1 ·day^-1, respectively, whereas in the continuous system the gibberellic acid production is about twice as large for a similar biomass: 0.768 mgGA₃·gBiomass^-1·day^-1. Several factors affecting the overall productivity of the immobilized systems were found to be: the quality and the quantity of mycelia in the biocatalyst beads and the immobilization conditions.     

Production of high-quality edible protein from Candida yeast grown in continuous culture

Candida utilis NRRL Y-900 was grown in aerobic continuous culture with cane molasses as the source of the growth-limiting carbon. At 1% reducing sugar in the chemostal (10 liter working volume) feed medium, addition of Zn (25μM) to a minimal salts medium resulted in an increase in the biomass productivity of the chemostat from 1.7 to 2.6 g/liter/hr with a growth yield of 0.55 g dry biomass/g reducing sugar utilized at D_max. On the average, the yeast biomass was 50–55% protein. At S_R > 2% sugar, the biomass productivity was limited by the oxygen supply. With O₂-supplemented aeration (at S_R = 4.2%)the maximum biomass productivity Was 7.25 g/liter/hr. Aerobic ethanol production was not observed. A highquality undenatured protein fraction was isolate from the yeast homogenate by isoelectric precipitation at pH 4.5. Contaminating nucleic acid was removed as an insoluble complex by chelation with an organic cation (cetavlon). The final protein product contained about 3% RNA (DWB) and was suitable for use as a food additive.     

Gluconic Acid Fermentation by Pullularia pullulans

During the study on the sugar metabolism of molds, several strains of Pullularia pullulans were found to produce large amounts of gluconic acid from glucose. Thirty seven strains of P. pullulans were then tested for their acid-producing abilities. Seven strains did not produce any amount of gluconic acid. However, all of the other strains were shown to be capable of producing this acid. The superior strains produced yiclds of gluconic acid as high as about 90%, based on glucose available, in shaking cultures at 30°C after 2 days. The yields were increased up to approximately 100% during later stages. In addition to high yields, gluconic acid was produced exclusively by these strains. Glutamic acid and inorganic ammonium salts, such as (NH₄)₂SO₄, NH₄Cl and (NH₄)₂HPO₄, were favorable nitrogen sources for acid production. In the case of (NH₄)₂SO₄, the optimum concentration was 0.05%. The addition of CaCO₃ was essential for gluconic acid production by P. pullulans and a 3% concentration of CaC0₃ appeared to be desirable for the maximum conversion to gluconic acid in a medium containing 10% glucose.     

Inhibition of succinic acid production in metabolically engineered Escherichia coli by neutralizing agent,organic acids,and osmolarity

The economical viability of biochemical succinic acid production is a result of many processing parameters including final succinic acid concentration, recovery of succinate, and the volumetric productivity. Maintaining volumetric productivities >2.5 g L^?1 h^?1 is important if production of succinic acid from renewable resources should be competitive. In this work, the effects of organic acids, osmolarity, and neutralizing agent (NH₄OH, KOH, NaOH, K₂CO₃, and Na₂CO₃) on the fermentative succinic acid production by Escherichia coli AFP184 were investigated. The highest concentration of succinic acid, 77 g L^?1, was obtained with Na₂CO₃. In general, irrespective of the base used, succinic acid productivity per viable cell was significantly reduced as the concentration of the produced acid increased. Increased osmolarity resulting from base addition during succinate production only marginally affected the productivity per viable cell. Addition of the osmoprotectant glycine betaine to cultures resulted in an increased aerobic growth rate and anaerobic glucose consumption rate, but decreased succinic acid yield. When using NH₄OH productivity completely ceased at a succinic acid concentration of ～40 g L^?1. Volumetric productivities remained at 2.5 g L^?1 h^?1 for up to 10 h longer when K‐ or Na‐bases where used instead of NH₄OH. The decrease in cellular succinic acid productivity observed during the anaerobic phase was found to be due to increased organic acid concentrations rather than medium osmolarity. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Physiological studies on Phymatotrichum omnivorum X. Influence of nitrogen sources on free and bound amino acid pools

The effect of nitrogen source on the free and bound amino acids of mycelium of Phymatotrichum omnivorum (Shear) Dugg was investigated. The largest free amino acid pool was present in the natural medium and the smallest in the synthetic medium. Phymatotrichum omnivorum was able to utilize different nitrogen sources with the best growth occurring with NH₄NO₃. The ratio of glycine to alanine and aspartic to glutamic was around 0.25 in the free amino acid pool and around 1 in the bound amino acid pool. The free pool of glutamic acid ranged from 5.6 % to 27.2 % depending upon the nitrogen source in the media. The free pool of alanine ranged from 35.7 % to 17.2 % in relation to the nitrogen source. Most other amino acid ratios did not vary significantly between the free amino acids and the bound amino acids.     

Fuel ethanol from hardwood hemicellulose hydrolysate by genetically engineeredEscherichia coli B carrying genes fromZymomonas mobilis

Summary Escherichia coli B (ATCC 11303) carrying the PET operon on plasmid pLOI 297 converted hemicellulose hydrolysate to ethanol at an efficiency of 94% theoretical maximum, which is 15% better than the highest efficiency reported for pentose utilizing yeasts in a comparable system. Aspen prehydrolysate (APH), that had been produced by theBio-Hol Process using a Wenger extruder with SO₂ as catalyst, was used as feedstock. The fermentation medium contained predominantly xylose (35g/L) with acetic acid present at about 6g/L. With the pH controlled at 7.0, this concentration of acetic acid was not inhibitory for growth or xylose fermentation. When the APH was fortified with nutrients (tryptone and yeast extract), the recombinant (inoculated at 0.5 g dry wt/L) converted 100% of the xylose to ethanol with a volumetric productivity of 0.29 g/L/hr. Overliming the APH with Ca(OH)₂, followed by neutralization to pH 7 with sulphuric acid and removal of the insolubles, resulted in a 2-fold increase in productivity. The max. productivity was 0.76 g/L/hr. The productivity in Ca(OH)₂-treated APH, fortified with only mineral salts, was 0.26 g/L/hr.     

Oxalic acid production by Aspergillus niger

Aspergillus niger is able to produce a quite high concentration of oxalic acid using sucrose as carbon and energy source. Operating at pH higher than 6 and an enriched N and P medium is necessary in order to conduct the fermentation towards oxalic acid production. A pH?shift technique, operating at acid pH?in the first two days and then setting pH?to 6, allowed the productivity to slightly increase in shaking flasks cultures up to 3.0?kg/m³?·?d, with a final oxalic acid concentration of 29?kg/m³. When operating at more controlled conditions, in a stirred tank, both productivity and oxalic acid concentration were improved (4.1?kg/m³?·?d and 33.8?kg/m³, respectively). However the main drawback of this fermentation is the low yield attained (about 0.3?kg oxalic acid/kg sucrose) because most of glucose, resulting from the hydrolysis of sucrose by the extracellular enzymes secreted at the beginning of the fermentation, is very quickly oxidised to gluconic acid, a process which is favoured at a pH?close to 6. Milk whey was proved to be a very good substrate as it allows oxalic acid to be produced with a similar productivity (2.5?kg/m³?·?d in shaking flasks) giving excellent yields of almost 0.6?kg oxalic acid/kg lactose.     

Studies on Osmophilic Yeasts

Various conditions were studied which gave influences on polyalcohol production by Pichia miso. Pichia miso gave an excellent yield of polyalcohol showing good growth in the vitamin-free medium. Unlike Zygosaccharomyces high concentrations of phosphate such as 2% as KH₂PO₄ in the medium showed no detrimental effect on polyalcohol production. Remarkable reduction in polyalcohol yield was observed in the medium of high concentration of nitrogen sources, among which yeast extract showed the most striking effect. Polyalcohol fermentation was provoked in the medium of 0.1% yeast extract while the metabolic activity distinctly converted to ethanol fermentation when the organisms were incubated in the medium of 4.0% yeast extract. The fact that a large amount of ethanol more than 6% in the medium was produced aerobically by genus Pichia of oxidative dissimilation type seemed to be very interesting and noticeable. For the purpose of industrial production, it was shown that polyalcohol production in jar-fermenter scale was achieved with as good yield as that in shaking flask culture.     

Production of aflatoxin byAspergillus parasiticus and its control

The aim of the present work was to investigate the production of aflatoxin byAspergillus parasiticus and to find out the possible ways to control it. Of 40 food samples collected from Abha region, Saudi Arabia, only 25% were contaminated with aflatoxins. Oil-rich commodities had the highly contaminated commodities by fungi and aflatoxins while spices were free from aflatoxins.Bacillus megatertum andB cereus were suitable for microbiological assay of aflatoxins. Czapek’s-Dox medium was found a suitable medium for isolation of fungi from food samples. The optimal pH for the growth ofA. parasiticus and its productivity of aflatoxin B₁ was found at 6.0, while the best incubation conditions were found at 30°C for 10 days. D-glucose was the best carbon source for fungal growth, as well as aflatoxin production. Corn steep liquor, yeast extract and peptone were the best nitrogen sources for both fungal growth and toxin production (NH₄)₂HPO₄ (1.55 gL^-1) and NaNO₂ (1.6 gL^-1) reduced fungal growth and toxin production with 37.7% and 85%, respectively. Of ten amino acids tested, asparagine was the best for aflatoxin B₁ production. Zn²⁺ and Co²⁺ supported significantly both fungal growth, as well as, aflatoxin B₁ production at the different tested concentrations. Zn²⁺ was effective when added toA. parasiticus growth medium at the first two days of the culture age. The other tested metal ions expressed variable effects depending on the type of ion and its concentration. Water activity (a_w) was an important factor controlling the growth ofA. parasiticus and toxin production. The minimum a_w for the fungal growth was 0.8 on both coffee beans and rice grains, while a_w of 0.70 caused complete inhibition for the growth and aflatoxin B₁ production. H₂O₂ is a potent inhibitor for growth ofA. parasiticus and its productivity of toxins. NaHCO₃ and C₆H₅COONa converted aflatoxin B₁ to water-soluble form which returned to aflatoxin B₁ by acidity. Black pepper, ciliated heath, cuminum and curcuma were the most inhibitory spices on toxin production. Glutathione, quinine, EDTA, sodium azide, indole acetic acid, 2,4-dichlorophenoxy acetic acid, phenol and catechol were inhibitory for both growth, as well as, aflatoxin B₁ production. Stearic acid supported the fungal growth and decreased the productivity of AFB₁ gradually. Lauric acid is the most suppressive fatty acid for both fungal growth and aflatoxin production, but oleic acid was the most potent supporter. Vitamin A supported the growth but inhibited aflatoxin B₁ production. Vitamins C and D₂ were also repressive particularly for aflatoxin production The present study included studying the activities of some enzymes in relation to aflatoxin production during 20-days ofA. parasiticus age in 2-days intervals. Glycolytic enzymes and pyruvate-generating enzymes seems to be linked with aflatoxin B₁ production. Also, pentose-phosphate pathway enzymes may provide NADPH for aflatoxin B₁ synthesis. The decreased activities of TCA cycle enzymes particularly from 4th day of growth up to 10th day were associated with the increase of aflatoxin B₁ production. All the tested enzymes as well as aflatoxin B₁ production were inhibited by either catechol or phenol.     

Lipolysis of pork fat by Staphylococcus warneri,S. Saprophyticus and Micrococcus varians

Staphylococcus saprophyticus, S. warneri and Micrococcus varians strains hydrolysed pork fat. The strain S. saprophyticus 852 was the most lipolytic and its activity was very important during incubation at 15° C. The growth and lipolysis of S. warneri strains were affected by a shift in temperature from 22° C to 15° C. The production of lipase by M. varians was dependent on O₂ as no lipolytic activity could be detected when this strain was cultivated without agitation. The S. warneri and S. saprophyticus lipases showed neither marked positional nor fatty acid specificities. The low percentage of unsaturated free fatty acids in samples inoculated with M. varians could be due to bacterial metabolism or to oxidation, as the culture was grown under shaking. Correspondence to: R. Talon     

叶绿素合成缺陷型小球藻突变株的选育及其蛋白产能和品质评价

本研究旨在利用常压室温等离子体(atmospheric pressure room temperature plasma, ARTP)诱变技术构建叶绿素合成缺陷型凯式小球藻突变株,筛选出极低叶绿素、适用于发酵生产蛋白质的新藻种。首先经优化诱变处理时间后建立了野生型兼养细胞的致死率曲线,在高于95%致死率条件下处理对数早期兼养细胞,基于可视化藻落颜色变化初筛获得4株突变株。随后在摇瓶中异养培养突变株,系统评价了蛋白生产性能,发现在含有30 g/L葡萄糖和5 g/L NaNO₃的Basal培养基中,突变株P. ks4表现最优,蛋白含量及产率分别为39.25%干重及1.15g/(L·d),氨基酸评分达101.34,叶绿素a含量下降98.78%且不含叶绿素b,含有叶黄素0.62 mg/g而使藻体呈金黄色。本研究为微藻替代蛋白的发酵生产提供了高性能、高品质的新种质P. ks 4。     

Optimization of medium components for high-molecular-weight hyaluronic acid production by <Emphasis Type="Italic">Streptococcus</Emphasis> sp. ID9102 via a statistical approach

Hyaluronic acid (HA), linear high-molecular-weight glycosaminoglycan produced from Streptococcus sp., has raised interest in the medical and cosmetics industries because of the various biological functions of HA. In this paper, we report on the optimization of medium components for HA production in Streptococcus sp. ID9102 (KCTC 11935BP) by two-step optimization (one-factor-at-a-time and taguchi orthogonal array design). In the first step, medium components, such as carbon, nitrogen, phosphate, and mineral sources, were selected for HA production in Streptococcus sp. ID9102 (KCTC 11935BP) using the one-factor-at-a-time method. In the second step, the concentration of the selected medium components was optimized using taguchi orthogonal array design. The design for medium optimization was developed and analyzed using MINITAB 14 software. In addition, the effect of amino acid and organic acid, such as glutamine, glutamate, and oxalic acid, was studied for HA production in Streptococcus sp. ID9102 (KCTC 11935BP). Through these processes, the optimum medium comprising 4% glucose, 0.75% yeast extract, 1.0% casein peptone, 0.25% K₂HPO₄, 0.05% MgCl₂, 0.5% NaCl, 0.04% glutamine, 0.06% glutamate, and 0.02% oxalic acid was determined. We were able to produce HA with a molecular weight of 5.9 × 10⁶ at a productivity of 6.94 g/l on pilot scale fermentation.     

Potential of solid state fermentation for production of L(+)-lactic acid by Rhizopus oryzae

Production of l(+)-lactic acid by Rhizopus oryzae NRRL 395 was studied in solid medium on sugar-cane bagasse impregnated with a nutrient solution containing glucose and CaCO₃. A comparative study was undertaken in submerged and solid-state cultures. The optimal concentrations in glucose were 120 g/l in liquid culture and 180 g/l in solid-state fermentation corresponding to production of l(+)-lactic acid of 93.8 and 137.0 g/l, respectively. The productivity was 1.38 g/l per hour in liquid medium and 1.43 g/l per hour in solid medium. However, the fermentation yield was about 77% whatever the medium. These figures are significant for l(+)-lactic acid production.     

Galactose oxidase production by immobilized cells ofDactylium dendroides

Summary Dactylium dendroides cells were immobilized with calcium alginate, calcium pectate and k-carrageenan. Alginate immobilized cells produced relatively small amounts of (D-galactose: O₂ oxidoreductase, EC 1.1.3.9, GOase). Pectate immobilized cells gave the best yield of GOase, which was comparable with that obtained with free cells, and productivity could be extended up to 28 days (7 cycles). Controlled dosage of phosphate to the medium markedly improved GOase production with higher yields per cycle than with free cells.     

Optimum conditions for the biological production of lactic acid by a newly isolated lactic acid bacterium,Lactobacillus sp. RKY2

Lactic acid is a green chemical that can be used as a raw material for biodegradable polymer. To produce lactic acid through microbial fermentation, we previously screened a novel lactic acid bacterium. In this work, we optimized lactic acid fermentation using a newly isolated and homofermentative lactic acid bacterium. The optimum medium components were found to be glucose, yeast extract, (NH₄)₂HPO₄, and MnSO₄. The optimum pH and temperature for a batch culture ofLactobacillus sp. RKY2 was found to be 6.0 and 36°C, respectively. Under the optimized culture conditions, the maximum lactic acid concentration (153.9 g/L) was obtained from 200 g/L of glucose and 15 g/L of yeast extract, and maximum lactic acid productivity (6.21 gL⁻¹h⁻¹) was obtained from 100 g/L of glucose and 20 g/L of yeast extract. In all cases, the lactic acid yields were found to be above 0.91 g/g. This article provides the optimized conditions for a batch culture ofLactobacillus sp. RKY2, which resulted in highest productivity of lactic acid.