Production of extracellular enzymes by immobilizedTrichoderma reesei in shake flask cultures

Polyurethane foam and nylon-web carriers were compared for simultaneous production of endo-1, 4-β-glucanase and xylanase by immobilizedTrichoderma reesei on a medium based on lactose (27 g/l), cellulose (3 g/l) and sorbose (0.3 g/l). Nylon sheet with 1.2 cm² carrier surface/ml medium was superior to the others, and it was selected for further studies. The carbon source had a marked effect on enzyme production by the immobilized fungus. With pure cellulose (10 g/l) as substrate, the maximum endoglucanase activity was 690 nkat/ml and xylanase activity 4800 nkat/ml. Supplementation with 0.5 g/l of sorbose resulted in an increase in both endoglucanase and xylanase activities in all media studied. A more detailed study on the effect of sorbose on a lactose(7 g/l)-and cellulose(3 g/l)-based medium revealed a clear optimum sorbose concentration of 1.5 g/l, with a maximum endoglucanase activity of 660 nkat/ml, xylanase activity of 3670 nkat/ml, and filter-paper activity (overall cellulolytic activity) of 2.0 filter-paper units/ml. However, the addition of 1.5 g/l sorbose to the pure-cellulose(10 g/l)-based medium resulted in a slight decrease in the enzyme production.     

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.     

Fed-batch sorbose fermentation using pulse and multiple feeding strategies for productivity improvement

Microbial oxidation of D-sorbitol tol-sorbose byAcetobacter suboxydans is of commercial importance since it is the only biochemical process in vitamin C synthesis. The main bottleneck in the batch oxidation of sorbitol to sorbose is that the process is severely inhibited by sorbitol. Suitable fed-batch fermentation designs can eliminate the inherent substrate inhibition and improve sorbose productivity. Fed-batch sorbose fermentations were conducted by using two nutrient feeding strategies. For fed-batch fermentation with pulse feeding highly concentrated sorbitol (600 g/L) along with other nutrients were fed intermittently in four pulses of 0.5 liter in response to the increased DO signal. The fed-batch fermentation was over in 24 h with a sorbose productivity of 13.40 g/L/h and a final sorbose concentration of 320.48 g/L. On the other hand, in fed-batch fermentation with multiple feeds, two pulse feeds of 0.5 liter nutrient medium containing 600 g/L sorbitol was followed by the addition of 1.5 liter nutrient medium containing 600 g/L sorbitol at a constant feed rate of 0.36 L/h till the full working capacity of the reactor. The fermentation was completed in 24 h with an enhanced sorbose productivity of 15.09 g/L/h and a sorbose concentration of 332.60 g/L. The sorbose concentration and productivity obtained by multiple feeding of nutrients was found to be higher than that obtained by pulse feeding and was therefore a better strategy for fed-batch sorbose fermentation.     

Ethanol production from native cassava starch by a mixed culture of Endomycopsis fibuligera and Zymomonas mobilis

The conversion of starch from unhydrolyzed cassava flour to ethanol by a pure culture of Endomycopsis fibuligera and by a co-culture of this amylolytic yeast and the bacterium Zymomonas mobilis was studied. The best overall results were obtained using the mixed culture. After 96 h of fermentation of a medium containing 150 g/l initial cassava starch, an ethanol concentration of 31.4 g/l, a productivity of 0.33 g ethanol/l × h and a yield of 0.21 g ethanol/g initial starch were reached. The highest yield (0.37 g/g) was obtained after 48 h when using a medium containing 50 g/l initial starch.     

Fed-batch sorbitol to sorbose fermentation by A. suboxydans

Batch kinetics for sorbitol to sorbose bioconversion was studied at 20% sorbitol concentration. The culture featured 90% conversion of sorbitol to sorbose in 20 hours. Increasing the initial substrate concentration in the bioreactor decreased the culture specific growth rate. At 40% initial sorbitol concentration no culture growth was observed. The batch kinetics and substrate inhibition studies were used to develop the Mathematical Model of the system. The model parameters were identified using the original batch kinetic data (S _o =20%). The developed mathematical model was adopted to fed-batch cultivation with the exponential nutrient feeding. The fed-batch model was simulated and implemented experimentally. No substrate inhibition was observed in the fed-batch mode and it provided an overall productivity of 12.6?g/l-h. The fed-batch model suitably described the experimentally observed results. The model is ready for further optimization studies.     

Continuous ethanol production at high glucose concentrations by a passively immobilized Zymomonas mobilis system

Summary The effect of high glucose concentrations on continuous ethanol production by passively immobilized Zymomonas mobilis cells has been studied. High effluent ethanol concentrations always led to low productivities. The maximum ethanol concentration attained was 92.8 g/l (98% glucose conversion) at a dilution rate of 0.14 h^-1 with 200 g/l glucose medium. The observed enhancement of cell immobilization in the fibrous support at high glucose concentrations in the feed input seems to be related to the formation of bacterial filaments.Preliminary results from this work were previously presented at the Second Spanish Conference on Biotechnology (Barcelona, 1988)     

新组合菌系SCB329-SCB933利用L-山梨糖发酵产生维生素C前体2-酮基-L-古龙酸的研究Ⅲ.发酵过程的特征和条件控制

在分析了新组合菌系ＳＣＢ３２９－ＳＣＢ９３３发酵过程特征的基础上,对流加发酵工艺中的种子培养、ｐＨ、溶氧的控制,以及发酵液初始培养基中的Ｌ－山梨糖浓度和流加起始点进行了优化,获得了比分批发酵更为满意的结果：发酵最终总糖达１３％（ｗ／ｖ）左右,发酵周期４０～５０ｈ,产２－酮基－Ｌ－古龙酸达１１５－１３０ｍｇ／ｍｌ,克分子转化率达８８ｍｏｌ％左右。     

Itaconic acid production by immobilized Aspergillus terreus with varied metal additions

Summary The effect of trace and alkaline metals on itaconic acid production by polyurethane-foam-immobilized Aspergillus terreus was examined in repeated shake-flask cultures according to a statistical experimental design. An increase in the glucose or copper concentration increased the need for earth alkaline metals. The experimentally obtained highest itaconic acid concentration of 51 g/l from 15% glucose with a total productivity of 3.67 g/l per day was reached during the first 14-day batch fermentation. In the fourth batch the calculated highest itaconic acid concentration of 19 g/l was reached with 25% glucose, 5 g/l of magnesium sulphate, 13 mg/l of copper sulphate and 10 g/l of calcium chloride. The immobilization of the mycelium increased the itaconic acid concentration obtained by as much as eightfold.Offprint requests to: H. Kautola     

Fed-batch cultivation of Acetobacter suboxydans for the microbial oxidation of D-sorbitol to L-sorbose

Microbial oxidation of D-sorbitol to L-sorbose is commercially important since it is the only biochemical process in Vitamin-C manufacture. The main bottleneck in the batch oxidation of D-sorbitol is that the process is severely inhibited by sorbitol. By conducting fed-batch fermentation, the inherent substrate inhibition present in batch fermentation can be eliminated. Batch fermentation with an initial sorbitol concentration of 200 g l^у featured a productivity of 14.2 g l^у h^у and a final sorbose concentration of 200 g l^у. Fed-batch fermentation conducted by feeding nutrients containing 600 g l^у of sorbitol at a constant feed rate of 0.36 l h^у yielded a productivity of 17.7 g l^у h^у and a final sorbose concentration of 320 g l^у.     

Optimisation of L-lysine production byCorynebacterium sp in fed-batch cultures

Summary The influence of initial concentration of glucose from 60 to 233 g/l on the production of L-lysine byCorynebacterium sp was studied first in batch culture. The maximum conversion rate into L-lysine was obtained at 165 g/l and the best specific production rate for L-lysine was observed at 65 g/l of glucose. In fed-batch fermentations, better conversion and the specific production rates were obtained. Maintaining of a high glucose concentration in the fed-batch technique allowed a 54% increase of the L-lysine production compared to the batch culture.     

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.     

Physiological and genetic factors for process development of cyclosporine fermentations

Summary The new immunosuppressive agent cyclosporine (Cyclosporin A, Cy) is the most prominent member of a group of cyclic peptide fungal metabolites (cyclosporins) produced byTolypocladium inflatum in submerged fermentations. In the present study, kinetics and physiology of mycelial growth and Cy production byT. inflatum were examined. A new semi-synthetic medium was formulated, consisting of a single carbon/energy source, Bacto-peptone, potassium phosphate and potassium chloride. A wide variety of carbon sources supported growth and Cy production. 3% (w/v) sorbose gave the highest final Cy titer (105.5 mg/l), based on 10-day fermentations. The best specific Cy production was observed with 2% sorbose (14.3 mg Cy/g biomass) followed by 5%myo-inositol (13.4 mg Cy/g biomass). A feeding strategy consisting of sequential addition of two carbon sources such as sorbose and maltose was developed in order to reach higher volumetric production. Genetic studies were also conducted, focussing on the development of mutants for increased Cy production and for the synthesis of novel cyclosporins. In the course of these studies, viable protoplasts ofT. inflatum have been isolated and regenerated.     

Studies on citric acid production with immobilized Yarrowia lipolytica in repeated batch and continuous air-lift bioreactors

Citric acid was produced from glucose in repeated-batch shake-flask and continuous air-lift cultivations by calcium-alginate-immobilized Yarrowia lipolytica A-101 yeast. The medium composition was systematically studied in a batch system by using experimental design and empiric modelling. The highest citric acid product concentration of 39 g/l was reached with a medium containing 150 g/l of glucose, 0.105 g/l of potassium dihydrogen phosphate, 0.84 g/l of magnesium sulphate and 21 mg/l of copper sulphate (5.2 mg/l of copper). The results were further improved by hardening the alginate carrier beads with glutaraldehyde, and by activation of the immobilized biocatalyst in a nutrient solution. In continuous air-lift bioreactors with varying height-to-diameter ratio the highest productivity of 350 mg/l per hour with a dilution rate of 0.023 l/h and a citric acid product concentration of 12 g/l was reached with a ratio of 3. Correspondence to: H. Kautola     

ImmobilizedAspergillus terreus in itaconic acid production from glucose

Summary The production of itaconic acid by immobilizedAspergillus terreus TKK 200-5-1 was studied both in shake flask cultures, and in continuous column bioreactors. The effect of glucose and ammonium nitrate concentrations, and of pH were examined using a statistical experimental plan. The highest itaconic acid product concentration could be reached at the highest investigated glucose concentration of 150 g/l and the highest initial pH of 3.75, in the absence of ammonium nitrate. In a continuous packed bed column system operated fro 4.5 months itaconic acid was obtained at a productivity of 328 mg/d per gram of polyurethane foam carrier.     

Effects of the Plant Defence Inducer, Acibenzolar-S-Methyl, on Hypocotyl Rot of Soybean Caused by Rhizoctonia solani AG-4

The plant defence inducer, acibenzolar‐S‐methyl (ASM) was tested for its ability to protect soybean against hypocotyl rot caused by Rhizoctonia solani Kühn AG‐4. ASM in vitro exhibited an antifungal dose‐dependant activity in the form of reduced mycelial growth. This inhibition reached 40% in comparison with the control at a concentration of 0.5 g/l ASM in the growth media. Seed imbibition with ASM at a concentration of 0.08 g/l and 0.5 g/l significantly induced a reduction of the intensity of hypocotyl rot symptoms caused by R. solani AG‐4 that was correlated with a stimulation of chitinase activity. The protective effect of ASM against R. solani AG‐4 is probably due to the combination of induced resistance and its effect on pathogen growth. Seed treatment with ASM affected also the growth of 2‐day‐old seedlings. A dose‐dependant inhibition of the seminal root growth was observed which reached 53% at a concentration of 0.5 g/l ASM. This growth reduction of soybean was transitional and was rapidly recovered in optimal growth conditions except at 0.5 g/l of ASM.     

Quantitative response of cell growth and polysaccharide biosynthesis by the medicinal mushroom Phellinus linteus to NaCl in the medium

The effect of NaCl on cell growth and polysaccharide biosynthesis in the medicinal mushroom Phellinus linteus was studied. With the increase of NaCl concentration between 1 g/l and 7 g/l in the culture medium, the cell growth and intracellular polysaccharide (IPS) accumulation were decreased; extracellular polysaccharide (EPS) concentration was enhanced, with an increase of NaCl concentration from 1 g/l to 3 g/l. Under the optimum NaCl concentration of 3 g/l, the maximum EPS and IPS production reached 2.2±0.15 g/l and 53.6±2.45 mg/g DW on day 12, which improved 32.27% and decreased 16.89% compared to the control, respectively. Both EPS and IPS showed new polysaccharide components by fractionation with DEAE-cellulose ion exchange chromatography compared to the control. The results presented in this study are considered helpful for further investigation on the diversity of polysaccharide biosynthesis of this medicinal fungus under NaCl environments.     

Comparative study of d-xylose conversion to ethanol by immobilized growing or non-growing cells of the yeast Pachysolen tannophilus

Summary The direct conversion of d-xylose to ethanol was investigated using immobilized growing and non-growing cells of the yeast Pachysolen tannophilus. Both preparations produced ethanol from d-xylose, however the d-xylose conversion to ethanol was much better with immobilized growing cells. Ethanol concentration up to 22.9 g/l and ethanol yield of 0.351 g/g of d-xylose were obtained in batch fermentation by immobilized growing cells whereas only 17.0 g/l and 0.308 g/g of d-xylose were obtained by immobilized non-growing cells. With continuous systems, immobilized growing cells were necessary for the long-term operation, since a steady state ethanol concentration of 17.7 g/l was maintained for only one week by immobilized non-growing cell reactor. With simultaneous control of aeration rate and concentrations of nitrogen sources in feed medium, immobilized growing cells of P. tannophilus showed excellent performance. At a residence time of 25 h, the immobilized cell reactor produced 26.9 g/l of ethanol from 65 g/l of d-xylose in feed medium.     

The role of malic acid in the metabolism of Schizosaccharomyces pombe: substrate consumption and cell growth

Summary The effect of initial concentrations of malate varying from 0 to 28.6 g/l was studied. The acid was found to be inhibitory for growth of Schizosaccharomyces pombe but not for its deacidification activity. Malate was never integrated into biomass but partly transformed into ethanol if the aeration rate was weak (oxygen limitation). In the absence of glucose, resting cells of S. pombe were able to degrade malic acid if their concentration was sufficient, but their viability gradually decreased. However, for 0.15 g/l of growing cells (inoculum) 6 g/l of glucose was necessary to consume 8 g/l of malate. When the medium did not contain sugar no growth was observed despite the partial consumption of malate, showing that the acid was neither a carbon source nor an energy source. Offprint requests to: P. Strehaiano     

Effect of inhibitors formed during wheat straw pretreatment on ethanol fermentation by Pichia stipitis

The inhibitory effect of the main inhibitors (acetic acid, furfural and 5-hydroxymethylfurfural) formed during steam explosion of wheat straw was studied through ethanol fermentations of model substrates and hydrolysates from wheat straw by Pichia stipitis. Experimental results showed that an increase in acetic acid concentration led to a reduction in ethanol productivity and complete inhibition was observed at 3.5 g/L. Furfural produced a delay on sugar consumption rates with increasing concentration and HMF did not exert a significant effect. Fermentations of the whole slurry from steam exploded wheat straw were completely inhibited by a synergistic effect due to the presence of 1.5 g/L acetic acid, 0.15 g/L furfural and 0.05 g/L HMF together with solid fraction. When using only the solid fraction from steam explosion, hydrolysates presented 0.5 g/L of acetic acid, whose fermentations have submitted promising results, providing an ethanol yield of 0.45 g ethanol/g sugars and the final ethanol concentration reached was 12.2 g/L (10.9 g ethanol/100 g DM).     

Two Phytotoxins Isolated from the Pathogenic Fungus of the Invasive Weed Xanthium italicum

Alternariol and altenuisol were isolated as the major phytotoxins produced by an Alternaria sp. pathogenic fungus of the invasive weed Xanthium italicum. Altenuisol exhibited stronger phytotoxic effect compared with alternariol. At 10 μg/mL, alternariol and altenuisol promoted root growth of the monocot plant Pennisetum alopecuroides by 11.1 % and 75.2 %, respectively, however, inhibitory activity was triggered by the increase of concentration, with root elongation being suppressed by 35.5 % and 52.0 % with alternariol and altenuisol at 1000 μg/mL, respectively. Alternariol slightly inhibited root length of the dicot plant Medicago sativa at 10–1000 μg/mL, whereas altenuisol stimulated root growth by 51.0 % at 10 μg/mL and inhibited root length by 43.4 % at 200 μg/mL. Alternariol and altenuisol did not exert strong regulatory activity on another dicot plant, Amaranthus retroflexus, when tested concentration was low, however, when the concentration reached 1000 μg/mL, they reduced root length by 68.1 % and 51.0 %, respectively. Alternariol and altenuisol exerted similar effect on shoot growth of three tested plants but to a lesser extent. It is noteworthy to mention that this is the first report on the phytotoxicity of altenuisol.