Glycerol production by Candida krusei employing NaCl as an osmoregulator in batch and continuous fermentations

Addition of 40 g NaCl l^–1 to a chemically defined medium containing 140 g glucose l^–1 in shake-flask culture improved glycerol production by Candida krusei from 16.5 g l^–1 to 47.7 g l^–1. With 40 g NaCl l^–1 at a dilution rate of 0.065 h^–1, glycerol concentration, glycerol yield (based on glucose consumed), and productivity in a four-stage cascade bioreactor were higher by 240%, 27% and 28%, respectively, than in a single-stage continuous culture system.     

Optimisation of medium composition for clavulanic acid production by Streptomyces clavuligerus

Among four different commercially available nitrogen sources containing soybean derivatives, a protein extract of soybean gave the highest yield for clavulanic acid production by Streptomyces clavuligerus. A statistical method based on factorial design of experiments was applied to optimise the medium. An empirical model was obtained by applying response surface statistical analysis. The analysis of variance showed that concentrations of protein extract of soybean and glycerol and the interaction between these two variables were significant at 95% level of confidence. The maximum clavulanic acid concentration obtained in 72 h was 1.2 g l^–1.     

Improved production of erythromycin by Saccharopolyspora erythraea by various plant oils

Various plant oils (50 g l^–1) increased the production of erythromycin by Saccharopolyspora erythraea. Maximum titer of erythromycin in media containing black cherry kernel, walnut, rapeseed, olive and cottonseed oils and control medium were 3.5, 2.8, 2.6, 2.1, 1.9, 0.7 g l^–1, respectively. Erythromycin production media containing rapeseed or cottonseed oil was growth-dependent but not in other media used.     

Multiple growth inhibition of <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> in 1,3-propanediol fermentation

The inhibition of substrate and product on the growth of Klebsiella pneumoniae in anaerobic and aerobic batch fermentation for the production of 1,3-propanediol was studied. The cells under anaerobic conditions had a higher maximum specific growth rate of 0.19 h^–1 and lower tolerance to 110 g glycerol l^–1, compared to the maximum specific growth rate of 0.17 h^–1 and tolerance to 133 g glycerol l^–1 under aerobic conditions. Acetate was the main inhibitory metabolite during the fermentation under anaerobic conditions, with lactate and ethanol the next most inhibitory. The critical concentrations of acetate, lactate and ethanol were assessed to be 15, 19, 26 g l^–1, respectively. However, cells grown under aerobic conditions were more resistant to acetate and lactate but less resistant to ethanol. The critical concentrations of acetate, lactate and ethanol were assessed to be 24, 26, and 17 g l^–1, respectivelyRevisions requested 8 september; Revisions received 2 November 2004     

Effect of culture media on protease and oxytetracycline production with mycelium and protoplasts of Streptomyces rimosus

For the simultaneous production of protease and oxytetracycline, mycelium and protoplasts of Streptomyces rimosus TM-55 were cultivated in basal medium containing soluble starch, corn steep liquid, ammonium sulphate, calcium carbonate, sodium chloride and soybean oil. Protease and oxytetracycline production increased with decreasing in ratio of culture broth to vessel volume from 1:2 to 1:5. Each ml of broth with 0.286 mg fresh mycelia yielded 168–204 units of protease and 785–972 g of oxytetracycline after replacement of corn steep liquor, sodium chloride and soybean oil with beef extract and sunflower oil, while each ml of broth with 7.5 × 10⁷ protoplasts produced 141–153 units of protease and 504–615 g of oxytetracycline. Protease and oxytetracycline production were low when the pH was 5.1 or 9.0. Soluble starch and ammonium sulphate were the best carbon and nitrogen sources, respectively. Supplementation with calcium carbonate enhanced protease and oxytetracycline production. The productivity of protoplasts decreased sharply when the incubation temperature increased from 28 to 34 °C, while the productivity of mycelium was almost unchanged.     

Evaluation of plastic composite-supports for enhanced ethanol production in biofilm reactors

Biofilms are a natural form of cell immobilization that result from microbial attachment to solid supports. Biofilm reactors with polypropylene composite-supports containing up to 25% (w/w) of various agricultural materials (corn hulls, cellulose, oat hulls, soybean hulls or starch) and nutrients (soybean flour or zein) were used for ethanol production. Pure cultures ofZymomonas mobilis, ATCC 31821 orSaccharomyces cerevisiae ATCC 24859 and mixed cultures with either of these ethanol-producing microorganisms and the biofilm-formingStreptomyces viridosporus T7A ATCC 39115 were evaluated. An ethanol productivity of 374g L^–1 h^–1 (44% yield) was obtained on polypropylene composite-supports of soybean hull-zein-polypropylene by usingZ. mobilis, whereas mixed-culture fermentations withS. viridosporus resulted in ethanol productivity of 147.5 g L^–1 h^–1 when polypropylene composite-supports of corn starch-soybean flour were used. WithS. cerevisiae, maximum productivity of 40 g L^–1 h^–1 (47% yield) was obtained on polypropylene composite-supports of soybean hull-soybean flour, whereas mixed-culture fermentation withS. viridosporus resulted in ethanol productivity of 190g L^–1 h^–1 (35% yield) when polypropylene composite-supports of oat hull-polypropylene were used. The maximum productivities obtained without supports (suspension culture) were 124 g L^–1 h^–1 and 5 g L^–1 h^–1 withZ. mobilis andS. cerevisiae, respectively. Therefore, forZ. mobilis andS. cerevisiae, ethanol productivities in biofilm fermentations were three- and eight-fold higher than suspension culture fermentations, respectively. Biofilm formation on the chips was detected by weight change and Gram staining of the support material at the end of the fermentation. The ethanol production rate and concentrations were consistently greater in biofilm reactors than in suspension cultures.This is Journal Paper No. J-16356 of the Iowa Agriculture and Home Economics Experiment Station, Ames, Iowa. Project No. 3253     

Extracellular production of a glycolipid biosurfactant, mannosylerythritol lipid, from Candida antarctica

Candida antarctica (sp. SY16) required avegetable oil as the carbon source to produce a biosurfactant, mannosylerythritol lipid (MEL-SY16). Biosurfactant production was 31 g l^–1 after 7 days in a batch culture and was not growth associated. In a two-stage culture, glycerol and oleic acid were used as an initial and a feeding carbon source, respectively, and 41 g l^–1 biosurfactant was produced after 8 days.     

Oxalic acid production from lipids by a mutant of Aspergillus niger at different pH

Crude rapeseed oil and post-refining fatty acids were used as substrates for oxalic acid production by a mutant of Aspergillus niger. Both the final concentration and the yield of the product were highest at pH 4 to 5. With a medium containing 50 g lipids l^–1, production reached a maximum of 68 g oxalic acid l^–1 after 7 d. A high yield of the product (up to 1.4 g oxalic acid g^–1 lipids consumed) was achieved with oil and fatty acids combined.     

Optimization of glycerol feeding for clavulanic acid production by Streptomyces clavuligerus with glycerol feeding

Glycerol at 10–20 g l^–1 increased clavulanic acid production by Streptomyces clavuligerus in shake-flask culture. The biosynthesis of clavulanic acid continued for longer by feeding glycerol and production increased to 250 mg l^–1 compared with 115 mg l^–1 without feeding. In fermenter batch culture, degradation of clavulanic acid began after 72 h. With glycerol feeding in fed-batch culture, clavulanic acid production was not only increased further to about 280 mg l^–1 but also remained stable up to 130 h.     

Production of mannitol by a novel strain of Candida magnoliae

A novel microorganism was isolated which is able to produce mannitol when grown in the presence of fructose and glucose as carbon sources. In flask culture in a medium containing 150 g fructose l^–1, it yielded 67 g mannitol l^–1 after 168 h. In fed-batch culture with 3–12% (w/v) fructose, production reached a maximum of 209 g mannitol l^–1 after 200 h, corresponding to an 83% yield and a 1.03 g l^–1 h^–1 productivity. The isolated strain was identified as Candida magnoliae based on identical sequences in the D1/D2 domain of its 26S rDNA and a similar carbon source utilization pattern with C. magnoliae reference strains.     

Enhanced conversion of sucrose to isomaltulose by a mutant of Erwinia rhapontici

Mutagenesis of Erwinia rhapontici was performed to enhance the production of isomaltulose from sucrose. A mutant strain, BN 68089, was obtained through a screening process involving automated and miniaturized cultivation in Bioscreen C. This high-throughput, miniaturized screening system was optimized to identify the mutant strain, which had a conversion yield (90%) and productivity (194 g l^–1 h^–1). The BN 68089 mutant cells were immobilized in sodium alginate and when operated in a packed bed reactor gave a yield of 89% and a productivity of 144 g l^–1 h^–1 of at 30 °C, the optimal temperature. Immobilized BN 68089 cells exhibited 8% and 15% higher yield and productivity, respectively, than those of the wild-type strain.     

Evaluation of the potential of Aspergillus niger species for the bioconversion of L-phenylalanine into 2-phenylethanol

Aspergillus niger was explored, for the first time, for the production of 2-phenylethanol (a rose-like aroma) using L-phenylalanine as precursor. Among the strains screened, A. niger CMICC 298302 was shown to produce, in a culture medium containing 6 g L-phenylalanine l^–1 and 60 g glucose l^–1, 1375 mg 2-phenylethanol l^–1 with a productivity of 153 mg l^–1 day^–1 and a molar yield of 74%. 2-Phenylethanol concentrations of 1 to 2 g l^–1 led to a two-fold and ten-fold decrease, respectively, in the mycelial radial growth rate. However, 2-phenylethanol was synthesized as the sole aromatic product and accumulated in the culture broth.     

Fed-batch production of <Emphasis Type="SmallCaps">d</Emphasis>-ribose from sugar mixtures by transketolase-deficient <Emphasis Type="Italic">Bacillus subtilis</Emphasis> SPK1

d-Ribose, a five-carbon sugar, is used as a key intermediate for the production of various biomaterials, such as riboflavin and inosine monophosphate. A high d-ribose-producing Bacillus subtilis SPK1 strain was constructed by the chemical mutation of the transketolase-deficient strain, B. subtilis JY1. Batch fermentation of B. subtilis SPK1 with 20 g l^–1 xylose and 20 g l^–1 glucose resulted in 4.78 g l^–1 dry cell mass, 23.0 g l^–1d-ribose concentration, and 0.72 g l^–1 h^–1 productivity, corresponding to a 1.5- to 1.7-fold increase when compared with values for the parental strain. A late-exponential phase was chosen as the best point for switching to a fed-batch process. Optimized fed-batch fermentation of B. subtilis SPK1, feeding a mixture of 200 g l^–1 xylose and 50 g l^–1 glucose after the late-exponential phase reduced the residual xylose and glucose concentrations to less than 7.0 g l^–1 and gave the best results of 46.6 g l^–1d-ribose concentration and 0.88 g l^–1 h^–1 productivity which were 2.0- and 1.2-fold higher than the corresponding values in a simple batch fermentation.     

Batch xylitol production from wheat straw hemicellulosic hydrolysate using Candida guilliermondii in a stirred tank reactor

Batch production of xylitol from the hydrolysate of wheat straw hemicellulose using Candida guilliermondii was carried out in a stirred tank reactor (agitation speed of 300 rpm, aeration rate of 0.6 vvm and initial cell concentration of 0.5 g l^–1). After 54 h, xylitol production from 30.5 g xylose l^–1 reached 27.5 g l^–1, resulting in a xylose-to-xylitol bioconversion yield of 0.9 g g^–1 and a productivity of 0.5 g l^–1 h^–1.     

Influence of medium composition and aeration on the synthesis of biosurfactants produced by Candida antarctica

Candida antarctica synthesised surface-active mannosylerythritol lipids at 46 g l^–1 by adding 80 g soybean oil l^–1 to the medium and maintaining the pO₂ at 50% with an air flow rate 1 vvm. Two-stage culturing of C. antarctica avoided medium foaming but the yield of biosurfactants synthesis was 28 g l^–1. The biosurfactants decreased the surface tension of water to 35 mN m^–1.     

A novel <Emphasis Type="Italic">Candida glycerinogenes</Emphasis> mutant with high glycerol productivity in high phosphate concentration medium

A novel Candida glycerinogenes mutant, which possesses high glycerol productivity in a high phosphate concentration medium, was obtained by mutagenesis of an industrial glycerol producer. The mutant accumulated a total biomass of 11.5 g l⁻¹, which is less than the 15 g l⁻¹of the wild-type strain, but it consumed glucose faster than the wild-type strain did. The mutant reached its maximal glycerol concentration of 129 g l⁻¹ in 84 h compared to 96 h for the wild-type strain. High cytoplasmic glycerol-3-phosphate dehydrogenase activity of the mutant in the early glycerol formation phase, leading to a rapid glycerol synthesis and accumulation, may be the main reason for the short fermentation process.     

Improved production of biosurfactant by a <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> mutant using vegetable oil refinery wastes

Biosurfactant production by Pseudomonas aeruginosa EBN-8 mutant was studied in shake flasks on separate wastes from canola, soybean and corn oil refineries. Of the substrates tested, canola oil refinery waste (COD=20 g l⁻¹) supplemented with sodium nitrate (at COD/N=20) showed the best microbial growth (4.50 g l⁻¹) and rhamnolipid production (8.50 g l⁻¹), at 10 d of incubation with the specific growth rate of 0.316 h⁻¹ and specific product yield of 0.597 g g⁻¹ h. Its cell-free supernatant showed the critical micelle dilution (CMD) of 150 and surface tension (ST) of 28.5 mN m⁻¹.     

Production of ψ-linolenic acid by the fungus Mucor rouxii on cheap nitrogen and carbon sources

Summary The production of -linolenic acid (GLA) by the fungus Mucor rouxii CBS 416.77 was studied on low budget nitrogen and carbon sources, i.e. rape meal, cocos expeller and two types of yeast extract (nitrogen sources), and starch, starch hydrolysate, beet molasses and cocos expeller (carbon sources). As references, Difco yeast extract and glucose were used. In flask cultivations the three yeast extracts were fully interchangeable, while the Difco yeast extract (the most expensive of those tested) gave a higher productivity of GLA in fermentor cultures (14 mg·l^–1·h^–1). The yield of lipids and GLA were increased in the order yeast extract < rape meal < cocos expeller. Thus the amount of lipid increased from 0.56 to 2.8 g·l^–1, and that of GLA from 0.15 to 0.33 g·l^–1. Use of beet molasses or cocos expeller as carbon sources gave poor growth. Starch and starch hydrolysate resulted in better productivity of GLA than glucose (4.7 and 4.9 compared to 3.4 mg·l^–1·h^–1). Offsprint requests to: A.-M. Lindberg     

By-product formation by a novel glycerol-producing yeast,Candida glycerinogenes,with different O2 supplies

Candida glycerinogenes is an aerobe which does not depend on sulphite for production of glycerol. With a sufficient O₂ supply, up to 130 g glycerol l^–1 was produced with 2.6 g acetic acid l^–1 as by-product. However, with an insufficient O₂ supply – with higher volumes of medium or at higher corn steep liquid concentrations – the glycerol concentration was lower because the by-products, ethanol, pyruvate and lactic acid, were produced in greater amounts, up to 45 g l^–1, 4.3 g l^–1, 1.6 g l^–1, respectively, whereas, less acetic acid (0.6 g l^–1) was produced. In addition, ethanol decreased to 0.4 g l^–1 and the glycerol yield improved from 34 to 50% (w/w) by adding 50 g sulphite l^–1, nevertheless, acetic acid increased to 7.8 g l^–1.     

Formation and analysis of mannosylerythritol lipids secreted by Pseudozyma aphidis

Pseudozyma aphidis DSM 70725 was found to be a novel producer of mannosylerythritol lipids (MELs). The MELs were quantified by HPLC. Glucose as carbon source for precultivation supported growth well. By contrast, at concentrations >30 g l^–1 in preculture, subsequent MEL formation in the main culture with soybean oil as sole carbon source was reduced. The type of substrate supply considerably influenced MEL formation. High concentrations of soybean oil (80 ml l^–1) at init favored the production process when compared to a stepwise (20 ml l^–1) addition. Mannose or erythritol were suitable second carbon sources that enhanced the MEL yield with soybean oil as preferred primary substrate. After 10 days, a maximum yield of 75 g l^–1 was attained during shake-flask cultivation. Biofuel (rapeseed oil methyl ester) also resulted in high yields of MEL, but glucose reduced the MEL yield. Analysis by GC-MS showed that all fatty acids contained in MEL and derived from soybean oil or related methyl ester were degraded by C2-units to differing extents. The surface (water/air) and interfacial (water/hexadecane) tension of the MELs produced from different carbon sources were reduced to a minimum of 26.2 mN m^–1 and 1 mN m^–1, respectively.