Endo-polygalacturonase production from untreated lemon peel byAspergillus sp. CH-Y-1043

Summary Endo-polygalacturonase (endo-PG) production byAspergillus sp. CH-Y-1043 using untreated lemon peel as the sole carbon source was investigated. This strain was observed to produce more activity of endo-PG at 37°C than at 29°C. Untreated lemon peel proved to be a beeter substrate than citrus pectin for endo-PG production. Modification of the culture medium and lowering of the initial pH to 2.8 caused a 10-fold increase in the production of endo-PG activity using lemon peel.     

Constitutive exo-pectinase produced byAspergillus sp. CH-Y-1043 on different carbon source

Summary The production of a constitutive exo-pectinase byAspergillus sp. CH-Y-1043 grown on glucose, sucrose, fructose, glycerol and galacturonic acid is reported. The specific activity was found to be in the range of 26% to 75% of that produced with pectin or poly-galacturonic acid. The production of this exo-pectinase is strictly correlated to the exponential growth phase and it is highly sensitive to the pH of the culture medium     

Kinetics of kojic acid fermentation byAspergillus flavus link S44-1 using sucrose as a carbon source under different pH conditions

Kojic acid production byAspergillus flavus strain S44-1 using sucrose as a carbon source was carried out in a 250-mL shake flask and a 2-L stirred tank fermenter. For comparison, production of kojic acid using glucose, fructose and its mixture was also carried out. Kojic acid production in shake flask fermentation was 25.8 g/L using glucose as the sole carbon source, 23.6 g/L with sucrose, and 6.4 g/L from fructose. Reduced kojic acid production (13.5 g/L) was observed when a combination of glucose and fructose was used as a carbon source. The highest production of kojic acid (40.2 g/L) was obtained from 150 g/L sucrose in a 2 L fermenter, while the lowest kojic acid production (10.3 g/L) was seen in fermentation using fructose as the sole carbon source. The experimental data from batch fermentation and resuspended cell system was analysed in order to form the basis for a kinetic model of the process. An unstructured model based on logistic and Luedeking-Piret equations was found suitable to describe the growth, substrate consumption, and efficiency of kojic acid production byA. flavus in batch fermentation using sucrose. From this model, it was found that kojic acid production byA. flavus was not a growth-associated process. Fermentation without pH control (from an initial culture pH of 3.0) showed higher kojic acid production than single-phase pH-controlled fermentation (pH 2.5, 2.75, and 3.0).     

Cowpeas as growth substrate do not support the production of aflatoxin byAspergillus sp

A number of 21Aspergillus sp. strains isolated from cowpeas from Benin (Africa) were characterized by RAPD methodology. Seven of these strains grouped withA. flavus in the dendrogram generated with the RAPD data. Only three were able to produce aflatoxin in significant amounts. Twelve other isolates grouped withA. parasiticus. All of these strains except 3 produced aflatoxin. Two additional strains neither fit with theA. flavus group, nor theA. parasiticus group according to their RAPD pattern. Both did not produce aflatoxin in measurable amounts. Generally the aflatoxin positive strains produced high amounts of aflatoxin after growth on YES medium. However after growth on cowpea based medium aflatoxin biosynthesis was strongly ceased, albeit the growth of the colony was only partly reduced. This was true for media made either with the whole cowpea seed or with cowpea seed without seed coat. Interestingly when the cowpea medium was heat sterilized the fungus was able to produce high amounts of aflatoxin. This, however, was not the case after the use of gamma irradiation as sterilization method for the medium. The expression of thenor- 1 gene, which is one of the early genes involved in aflatoxin biosynthesis, was significantly repressed after growth on gamma irradiated cowpea medium in contrast to YES medium. This study was part of the project “Capability Building for Research and Quality Assurance in Traditional Food Processing in West Africa”     

Kojic acid production byAspergillus flavus using gelatinized and hydrolyzed sago starch as carbon sources

Direct conversion of gelatinized sago starch into kojic acid byAspergillus flavus strain having amylolytic enzymes was carried out at two different scales of submerged batch fermentation in a 250-mL shake flask and in a 50-L stirred-tank fermentor. For comparison, fermentations were also carried out using glucose and glucose hydrolyzate from enzymic hydrolysis of sago starch as carbon sources. During kojic acid fermentation of starch, starch was first hydrolyzed to glucose by the action of α-amylase and glucoamylase during active growth phase. The glucose remaining during the production phase (non-growing phase) was then converted to kojic acid. Kojic acid production (23.5g/L) using 100 g/L sago starch in a shake flask was comparable to fermentation of glucose (31.5 g/L) and glucose hydrolyzate (27.9 g/L) but in the 50-L fermentor was greatly reduced due to non-optimal aeration conditions. Kojic acid production using glucose was higher in the 50-L fermentor than in the shake flask.     

Production of ethanol by a flocculentSaccharomyces sp. in a continuous upflow reactor using sucrose,sugar-cane juice,and molasses as the carbon source

Summary A flocculentSaccharomyces sp., isolated from spontaneously fermenting sugar-cane juice, was used to produce ethanol in a continuous upflow reactor. Media of different composition were tested using the same fermentation conditions. The best results were obtained fermenting either sugar-cane juice or molasses. The differences observed could be due to the influence of the medium composition on the growth rate and on the expression of the flocculent capacity of the yeast, both factors which modified the cell biomass concentration within the reactor.

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Resumen Una cepa floculante deSaccharomyces, aislada de jugo de caña de azúcar, se utilizó para producir etanol fermentando medios de distinta composición en un reactor continuo de flujo ascendente. Los mejores resultados se obtuvieron con jugo de caña de azúcar y con melaza. Las diferencias observadas según el mosto utilizado pueden deberse a la influencia de la composición del medio sobre la velocidad de multiplicación y capacidad foculante de la levadura, modificando de esta manera la concentración de biomasa dentro del reactor.

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Résumé Une souche floculante deSaccharomyces isolée du jus de canne à sucre a été utilisée pour produire l'éthanol, dans un réacteur continu à flux ascendant, par fermentation de milieux de culture de différentes compositions. Les meilleurs résultats ont été obtenus avec le jus de canne à sucre et les molasses. Les différences qu'on a vues selon le moût utilisé peuvent être dues à l'influence de la composition du milieu sur la vitesse de multiplication et la capacité floculante de la levure, donnant une modification de la concentration de biomasse dans le réacteur.

     

烟碱降解菌以烷烃为碳源产生物表面活性剂的研究

通过测定发酵过程中菌体浓度和发酵上清液的表面张力,研究了烷烃碳源和发酵条件对烟碱降解菌(Ochrobactrum sp.)产生物表面活性剂的影响。结果表明,菌株Ochrobactrum sp.以十三烷和十六烷为碳源生长较好,而利用液体石蜡可产生较多生物表面活性剂。以2%液体石蜡为碳源,装液量为40%(250 m L三角瓶),于30℃,120 r/min培养4 d时,发酵液表面张力能降低至42.1m N/m。     

Alcohol fermentation using lignin-related compounds as a carbon source

Clostridium indolis JCM 1380 produced 0.24 g/l of ethanol from protocatechuic acid with consumption of about 40% of the substrate (1.2 g/l) at 96 h of cultivation, while Clostridium sphenoides JCM 1415 produced 0.37 g/l of ethanol from p-hydroxybenzoic acid with consumption of about 30% of the substrate (1.5 g/l) at 60 h of cultivation. However, a long lag time was necessary to produce ehtanol from protocatechuic acid by C. indolis, whereas ethanol from p-hydroxybenzoic acid by C. sphenoides was produced without a lag time.     

Production of rhamnolipid biosurfactant by fed-batch culture of Pseudomonas aeruginosa using glucose as a sole carbon source.

The pH-stat fed-batch culture of Pseudomonas aeruginosa YPJ-80 was done to produce a rhamnolipid biosurfactant. With glucose as the sole carbon source, the final concentrations of cells and rhamnolipid biosurfactant obtained in 25 h were 25 g cell dry weight/l and 4.4 g/l, respectively.     

Production of polyhydroxyalkanoates (PHAs) with canola oil as carbon source

Wautersia eutropha was able to synthesize medium chain length polyhydroxyalkanoates (PHAs) when canola oil was used as carbon source. W. eutropha was cultivated using fructose and ammonium sulphate as carbon and nitrogen sources, respectively, for growth and inoculum development. The experiments were done in a laboratory scale bioreactor in three stages. Initially, the biomass was adapted in a batch culture. Secondly, a fed-batch was used to increase the cell dry weight and PHA concentration to 4.36 g L(-1) and 0.36 g L(-1), respectively. Finally, after the addition of canola oil as carbon source a final concentration of 18.27 g L(-1) PHA was obtained after 40 h of fermentation. With canola oil as carbon source, the polymer content of the cell dry matter was 90%. The polymer was purified from dried cells and analyzed by FTIR, NMR and DSC using PHB as reference. The polymer produced by W. eutropha from canola oil had four carbon monomers in the structure of the PHA and identified by 1H and 13C NMR analysis as 3-hydroxybutyrate (3HB), 3-hydroxyvalerate (3HV), 3-hydroxyoctanoate (3HO), and 3-hydroxydodecanoate (3HDD).     

Dichloromethane as the sole carbon source forHyphomicrobium sp. strain DM2 under denitrification conditions

Hyphomicrobium sp. strain DM2 was found to grow anaerobically in the presence of nitrate with methanol, formaldehyde, formate or dichloromethane. The estimated growth rate constants with methanol and dichloromethane under denitrification conditions were 0.04 h^–1 and 0.015 h^–1, respectively, which is twofold and fourfold lower than the rates of aerobic growth with these substrates. Slight accumulation of nitrite was observed in all cultures grown anaerobically with nitrate. Dichloromethane dehalogenase, the key enzyme in the utilization of this carbon source, was induced under denitrification conditions to the same specific activity level as under aerobic conditions. In a fed batch culture under denitrification conditionsHyphomicrobium sp. DM2 cumulatively degraded 35 mM dichloromethane within 24 days. This corresponds to a volumetric degradation rate of 5 mg dichloromethane/l·h and demonstrates that denitrificative degradation offers an attractive possibility for the development of anaerobic treatment systems to remove dichloromethane from contaminated groundwater.     

Denitrification kinetics in a fluidised bed using methanol as the carbon source

Summary Denitrification in a fluidised bed was found to follow the Michaelis-Menten rate equation. The kinetic constants for the process were determined using a shallow bed in the laboratory for the prediction of deep bed performance on a pilot plant.     

Production of targeted poly(3-hydroxyalkanoates) copolymers by glycogen accumulating organisms using acetate as sole carbon source

One of the main limitations in bacterial polyhydroxyalkanoate (PHA) production with mixed cultures is the fact that primarily polyhydroxybutyrate (PHB) homopolymers are generated from acetate as the main carbon source, which is brittle and quite fragile. The incorporation of different 3-hydroxyalkanoate (HA) components into the polymers requires the addition of additional carbon sources, leading to extra costs and complexity. In this study, the production of poly(3-hydroxybutyrate (3HB)-co-3-hydroxyvalerate (3HV)-co-3-hydroxy-2-methylvalerate (3HMV)), with 7-35C-mol% of 3HV fractions from acetate as the only carbon source was achieved with the use of glycogen accumulating organisms (GAOs). An enriched GAO culture was obtained in a lab-scale reactor operated under alternating anaerobic and aerobic conditions with acetate fed at the beginning of the anaerobic period. The production of PHAs utilizing the enriched GAO culture was investigated under both aerobic and anaerobic conditions. A polymer content of 14-41% of dry cell weight was obtained. The PHA product accumulated by GAOs under anaerobic conditions contained a relatively constant proportion of non-3HB monomers (30+/-5C-mol%), irrespective of the amount of acetate assimilated. In contrast, under aerobic conditions, GAOs only produced 3HB monomers from acetate causing a gradually decreasing 3HV fraction during this aerobic feeding period. The PHAs were characterized by gel permeation chromatography (GPC) and differential scanning calorimetry (DSC). The data demonstrated that the copolymers possessed similar characteristics to those of commercially available poly(3HB-co-3HV) (PHBV) products. The PHAs produced under solely anaerobic conditions possessed lower melting points and crystallinity, higher molecular weights, and narrower molecular-weight distributions, compared to the aerobically produced polymers. This paper hence demonstrates the significant potential of GAOs to produce high quality polymers from a simple and cheap carbon source, contributing considerably to the growing research body on bacterial PHA production by mixed cultures.     

Enhancement of cephamycin C production using soybean oil as the sole carbon source

Vegetable oils were investigated to evaluate their potential to act as the sole carbon source for production of cephamycin C in shake and jar-fermentor cultures. Soybean oil was the best carbon source for cephamycin C production. Bioautography and HPLC analyses showed that cephamycin C was exclusively produced even when soybean oil was used as the sole cabon source. The optimal pH and initial concentration of soybean oil was 7.5 and 7 g/l, respectively. Both pH and the pH-control agent affected cephamycin C production, and among phosphoric acid, acetic acid and sulfuric acid, phosphoric acid was associated with the best production. Soybean oil was slowly consumed after the soluble nitrogen source was consumed. When the initial soybean oil concentration was 7 g/l, cephamycin C production was maximal, 2.0 g/l, which was twice as high as that from starch. The product yield from soybean oil was 4.7 times higher than that from starch. These results show that vegetable oils, which are cheaper than other carbon sources, could be used as the sole carbon source in the production of antibiotics. Correspondence to: M. Okabe     

Production and characterization of cellulases and hemicellulases by Acremonium cellulolyticus using rice straw subjected to various pretreatments as the carbon source

Cellulases and hemicellulases are key enzymes in the production of alternative fuels and chemicals from lignocellulosic biomass-an abundant renewable resource. Carbon source selection is an important factor in the production of cellulases and hemicellulases. Rice straw--a potential ethanol source--has recently gained considerable interest in Asian countries. Here, we investigated the production of cellulases by using rice straw subjected to various pretreatments as substrates in order to produce cellulases at low costs; we also identified the enzymes' characteristics. Rice straw cutter milled to <3mm was pretreated by wet disk milling, dry ball milling, or hot-compressed water treatment (HCWT). Pretreated rice straw and commercial cellulose, Solka Floc (SF), were used as carbon sources for cellulase production by the fungus Acremonium cellulolyticus. Filter paper cellulase, β-xylanase, and β-xylosidase production from ball- and disk-milled samples were higher than those from SF. Enzymatic activity was absent in cultures where HCWT rice straw was used as carbon source. Wet disk-milled rice straw cultures were more suitable for enzymatic hydrolysis of pretreated rice straw than SF cultures. Thus, wet disk milling may be a suitable pretreatment for producing substrates for enzymatic hydrolysis and generating inexpensive carbon sources for cellulase production.     

Polyhydroxybutyrate production by Saccharophagus degradans using raw starch as carbon source

Biosynthesis of poly(3‐hydroxybutyrate) (PHB) from raw starch as the carbon source by the polysaccharide‐digesting bacteria Saccharophagus degradans was investigated in a fed‐batch culture. The production and properties of the PHB synthesized from starch were compared to those obtained using glucose as carbon source. In fed‐batch cultures, S. degradans accumulated 21.35 and 17.46% of PHB, using glucose or starch as carbon source, respectively. The physical properties of the biopolymer produced from each carbon source were similar between them. Molecular mass, melting temperature and heat of fusion were 54.23 kDa, 165.61°C and 59.59 J/g, respectively, using glucose; and 57.07 kDa, 174.31°C and 67.66 J/g, respectively, using starch. This is the first work describing the capability of S. degradans to utilize raw starch as the sole carbon source for the production of PHB.     

Biological sulfate reduction using synthesis gas as energy and carbon source

Biological sulfate reduction was studied in laboratory-scale gas-lift reactors. Synthesis gas (gas mixtures of H(2)/CO/CO(2)) was used as energy and carbon source. The required biomass retention was obtained by aggregation and immobilization on pumice particles. Special attention was paid to the effect of CO addition on the sulfate conversion rate, aggregation, and aggregate composition.Addition of 5% CO negatively affected the overall sulfate conversion rate; i.e., it dropped from 12-14 to 6-8 g SO(2-) (4)/L day. However, a further increase of CO to 10 and 20% did not further deteriorate the process. With external biomass recycling the sulfate conversion rate could be improved to 10 g SO(2-) (4)/L day. Therefore biomass retention clearly could be regarded as the rate-limiting step. Furthermore, CO affected the aggregate shape and diameter. Scanning electron microscopy (SEM) photographs showed that rough aggregates pregrown on H(2)/CO(2) changed into smooth aggregates upon addition of CO. Addition of CO also changed the aggregate Sauter mean diameter (d(32)) from 1.7 mm at 5% CO to 2.1 mm at 20% CO. After addition of CO, a layered biomass structure developed. Acetobacterium sp. were mainly located at the outside of the aggregates, whereas Desulfovibrio sp. were located inside the aggregates. (c) 1996 John Wiley & Sons, Inc.     

以聚羟基丁酸戊酸共聚酯为碳源去除循环水养殖系统的硝酸盐及生物膜中微生物群落动态

【目的】利用聚羟基丁酸戊酸共聚酯(PHBV)作为固体碳源和生物膜载体,去除循环水养殖系统的硝酸盐,并研究固体碳源反硝化反应器不同运行阶段生物膜中微生物群落结构的动态变化。【方法】采用PCR-DGGE技术对反硝化反应器中微生物群落结构的动态变化进行了分析,采用传统纯培养方法分离反应器中降解PHBV的细菌。【结果】连接固相反硝化反应器能使循环水养殖系统中积累的硝酸盐显著降低,并维持在较低水平(小于10 mg/L),而常规循环水养殖系统中硝酸盐浓度持续增加。系统发育树聚类分析结果表明,反硝化反应器生物膜细菌归属于变形菌门(β-proteobacteria、γ-proteobacteria和δ-proteobacteria)、厚壁菌门(Firmicutes)和拟杆菌门(Bacteroidetes)。反应器运行初期(40 d)的优势种群主要为Acidovorax和Bacillus;运行后期(150 d)的优势种群依次为Clostridium、Desulfitobacterium、Dechloromonas、Pseudoxanthomonas和Flavobacterium。从反应器中分离到的PHBV降解菌株分别归属于Acidovorax、Methylibium、Pseudoxanthomonas和Dechloromonas。【结论】利用PHBV为碳源能有效去除循环水养殖系统的硝酸盐。明确了反硝化反应器在运行过程中,碳源表面生物膜的优势菌群及其动态变化。     

Enhanced production of exopolysaccharides using industrial grade starch as sole carbon source

Bioprocess and Biosystems Engineering - Industrial grade soluble corn starch was used directly and effectively as the fermentation substrate for microbial exopolysaccharides production. Bacillus...