Beneficial effect of protracted sterilization of lentils on phytase production by Aspergillus ficuum in solid state fermentation

Water addition to the solid substrate preceding autoclaving increased substrate porosity and phytase production in solid state fermentation. In comparison with dry sterilization, the phytase activity increased 6‐, 8.5‐, and 10‐fold when the autoclaving time was 20, 40, and 60 min, respectively. Autoclaving increased the void space of sterilized lentils, and the increase was 16% higher when water was supplemented to the lentils before sterilization. Image analysis of SEM pictures of the solid substrate showed that water supplementation presterilization portended greater micro‐fissure surface area, which also increased with increasing the sterilization time. SEM pictures of the fermentation product showed that fungal growth into the center of the solid substrate was ubiquitous when water was supplemented before sterilization but was absent when water was supplemented post sterilization. Similarly, spore formation on the substrate surface for the presterilization water supplementation samples far exceeded spore formation for samples that received supplementation poststerilization. This evidence suggests that improved mass transfer into the solid substrate resulting from additional pore volume and the formation of micro‐fissures on the substrate surface is responsible for the observed gains in phytase productivity in solid state fermentation. © 2012 American Institute of Chemical Engineers Biotechnol. Prog., 2012     

Invertase production by Aspergillus niger in submerged and solid-state fermentation

Three Aspergillus nigerstrains were grown in submerged and solid state fermentation systems with sucrose at 100 g l^–1. Average measurements of all strains, liquid vs solid were: final biomass (g l^–1), 11 ± 0.3 vs 34 ± 5; maximal enzyme titres (U l^–1) 1180 ± 138 vs 3663 ± 732; enzyme productivity (U l^–1h^–1) 20 ± 2 vs 87 ± 33 and enzyme yields (U/gX) 128 ± 24 vs 138 ± 72. Hence, better productivity in solid-state was due to a better mould growth.     

Immobilization of Aspergillus ficuum phytase: product characterization of the bioreactor

Aspergillus ficuum phytase was covalently immobilized on Fractogel TSK HW-75 containing 2-oxy-l-alkylpyridinium salts. A packed-bed bioreactor was constructed with the immobilized phytase. An HPLC ion-exchange method was used to analyze the enzymatic products of the bioreactor. Immobilized fungal phytase was able to hydrolyze myo-inositol Hexa-, penta-, tetra-, tri-, and diphosphates. When the substrate solution was recirculated for 5 hr in the bioreactor about 50% inorganic orthophosphate was released and myo-inositol-diphosphate and mono-phosphate were the only remaining products.     

Combinatorial approach of statistical optimization and mutagenesis for improved production of acidic phytase by Aspergillus niger NCIM 563 under submerged fermentation condition

Combination of statistical optimization and mutagenesis to isolate hypersecretory strains is studied to maximize phytase production from Aspergillus niger NCIM 563 under submerged fermentation. The overall results obtained show a remarkable 5.98-fold improvement in phytase production rates when compared to that using basal medium. Optimization of culture conditions from parent strain is studied first by the Plackett–Burman technique to evaluate the effects of 11 variables for phytase production. The results showed that glucose, MgSO₄, KCl, incubation period, and MnSO₄ are the most significant variables affecting enzyme production. Further optimization in these variables, using a central composite design technique, resulted in 3.74-fold increase in the yield of phytase production to 254,500 U/l when compared with the activity observed with basal media (68,000 U/l) in shake flask. Our experiments show that the phytase from A. niger NCIM 563 exhibits desirable activity in simulated gastric fluid conditions with low pH and also improved thermostability when compared to commercial phytase. The improved yield demonstrates the potential applicability of phytase enzyme as a source of phytase supplement for phosphorus nutrition and environmental protection in animal feed industry. Physical and chemical mutagenesis experiments were carried out in parallel to isolate hypersecretory mutants that could possibly further enhance the enzyme production. Using optimized media conditions of the parent strain, our results show that mutant strain A. niger NCIM 1359 increased the phytase activity by another 1.6-fold to 407,200 U/l.     

Enhanced cellulase production using Solka Floc in a fed-batch fermentation

Summary Use of a fed-batch mode of cultivation of T. reesei has permitted high concentrations of substrate to be consumed. This has resulted in the production of high titre cellulase preparations around 30 FPU/ml at high volumetric productivities (177 IU/L.hr).Perhaps the most obvious area for major improvement in the process of cellulose utilization is the production of cellulase enzyme for hydrolysis of wood and agricultural residues. It has been estimated that some 50% of the cost of producing glucose from cellulosic material is attributable to enzyme production alone (Perez, et al., 1980). Improvements in the area would therefore have a dramatic impact, and are of paramount importance if economical hydrolysis processes are to be realized. The first major thrust in the area has been the development of improved mutant strains of T. reesei, free from catabolite repression and capable of constitutive cellulase production (Montenecourt and Eveleigh, 1977; Gallo, 1982).While this effort continues to develop further high yielding mutants, improvement must also come from developments in fermentation techniques. A major advance is the use of fed-batch cultivation, which provides a means of avoiding the agitation and aeration difficulties, as well as repression effects encountered with high substrate concentration batch fermentation. This report briefly compares batch and fed-batch operation over a range of substrate concentrations.     

Cyclohexanedione modification of arginine at the active site of Aspergillus ficuum phytase.

Reaction of Aspergillus ficuum phytase with the arginine specific modifier 1,2-cyclohexanedione causes a rapid loss of activity. The inactivation can be partially reversed by 0.2 M hydroxylamine and exhibits pseudo-first order kinetics. The reaction order and second order rate constant of inactivation were 0.87 and 6.72 M-1 Min-1, respectively. Amino acid analysis of modified phytase indicates that about 7 arginine of the total 19 were modified. While the chymotryptic maps of treated and untreated phytase wer virtually identical, the tryptic maps had 4 peaks of altered mobility. An Arg containing tripeptide was identified in the phytase which is also present in other phosphohydrolases and may represent one of the labile Arg involved in the formation of the active site.     

Improved phytase production by a thermophilic mould Sporotrichum thermophile in submerged fermentation due to statistical optimization

Culture variables affecting phytase production by a thermophilic mould Sporotrichum thermophile in submerged fermentation were optimized. Soluble starch, peptone, Tween-80 and sodium phytate were identified by Plackett-Burman design as the most significant factors to affect phytase production. The 2(4) full factorial central composite design of response surface methodology was applied for optimizing the concentrations of the significant variables and to delineate their interactions. Starch, Tween-80, peptone and sodium phytate at 0.4%, 1.0%, 0.3% and 0.3% supported maximum enzyme titres, respectively. An overall 3.73-fold improvement in phytase production was achieved due to optimization. When sodium phytate was substituted with wheat bran (3%), the phytase titre in the former was comparable with that in the latter.     

Production, rapid purification and catalytic characterization of extracellular phytase from Aspergillus ficuum

A rapid purification scheme utilizing three chromatographic steps resulted in 6 fold purification of Aspergillus ficuum phytase (myo-inositol-hexakisphosphate 3-phosphohydrolase, EC 3.1.3.8). At pH 5.0 and 60 degrees C the enzyme performed acceptably for 2.0 hr with only 30% diminished catalytic rate at the end. Substrate concentration exceeding 2mM was inhibitory. The inorganic orthophosphate, the product and a weak inhibitor, exhibited a Ki of 1.9 x 10(-3)M. The extracellular phytase has the potential for industrial use since it can be over produced, easily purified, remain catalytically active for a longer period and is not subjected to severe product inhibition.     

Optimization of the extracellular production of a bacterial phytase with Escherichia coli by using different fed-batch fermentation strategies

The extracellular production of Escherichia coli phytase was studied in fed-batch fermentations. Two different feeding strategies were compared: control by keeping the glucose concentration constant, and control by keeping a low constant oxygen level in the medium. For the feeding control based on glucose concentration, a recently developed rapid glucose controlling system was tested for the first time in bacterial cultivations and used to establish the fermentative production of extracellular phytase with E. coli. High activity levels (120 U ml(-1)) at short cultivation times (14 h) were obtained. Even higher activity levels - albeit at longer cultivation times - were reached by applying a feeding control, the main characteristic of which was a constant low oxygen concentration. The optimum oxygen level for the production of phytase was in the range of 5-10% saturation.     

Enhanced sophorolipid production by feeding-rate-controlled fed-batch culture

To develop the easier control method for fed-batch culture of sophorolipid production, we chose rapeseed oil as the most productive oil and compared their productivities in relation to different concentrations of glucose. The optimal concentration of glucose was 30 g/L for sophorolipid production. A fed-batch method was conducted using Candida bombicola ATCC 22214 with rapeseed oil as a secondary substrate. The feeding rate of rapeseed oil was dependent on pH and was calculated by the consumption rate of NaOH and rapeseed oil. The glucose concentration was constantly maintained between 30 and 40 g/L. As a result, we have produced a crude sophorolipid up to 365 g/L for 8 days through a feeding-rate-controlled fed-batch process.     

Optimization of phytase production by solid substrate fermentation

The production of phytase by three feed-grade filamentous fungi (Aspergillus ficuum NRRL 3135, Mucor racemosus NRRL 1994 and Rhizopus oligosporus NRRL 5905) on four commonly used natural feed ingredients (canola meal, cracked corn, soybean meal, wheat bran) was studied in solid substrate fermentation (SSF). A. ficuum NRRL 3135 had the highest yield [15 IU phytase activity/g dry matter (DM)] on wheat bran. By optimizing the supplementation of wheat bran with starch and (NH₄)₂SO₄, phytase production increased to 25 IU/g DM. Optimization was carried out by Plackett-Burman and central composite experimental designs. Using optimized medium, phytase, phosphatase, alpha-amylase and xylanase production by A. ficuum NRRL 3135 was studied in Erlenmeyer flask and tray SSF. By scaling up SSF from flasks to stationary trays, activities of 20 IU phytase activity/g DM were reproducibly obtained. Electronic Publication     

Optimization of exopolysaccharide production by Tremella mesenterica NRRL Y-6158 through implementation of fed-batch fermentation

In liquid culture conditions, the yeast-like fungus Tremella mesenterica occurs in the yeast state and synthesizes an exopolysaccharide (EPS) capsule, which is eventually released into the culture fluid. It is composed of an α-1,3-D-mannan backbone, to which β-1,2 side chains are attached, consisting of D-xylose and D-glucuronic acid. Potato dextrose broth (PDB) seemed to be an excellent medium for both growth of the yeast cells and synthesis of the EPS. This medium is composed solely of an extract of potatoes to which glucose was added. Yet an important disadvantage of this production medium is the presence of starch in the potato extract, since Tremella cells are not capable of metabolizing this component; furthermore, it coprecipitates upon isolation of the polymer [3]. In this respect, it was essential to remove the starch in order to achieve high polysaccharide production and recovery. A good method was the removal of starch through ultrafiltration of the PDB medium before inoculation of the strain. This resulted in an excellent starch-free medium in which other components essential for polysaccharide production were still present [3]. Through implementation of single and cyclic fed-batch fermentations with glucose feed, 1.6- and 2.2-fold increases in EPS yield were obtained, respectively. Lowering the carbon source level by using a cyclic fed-batch technique might decrease the osmotic effect of glucose or any catabolite regulation possibly exerted by this sugar on enzymes involved in EPS synthesis. Journal of Industrial Microbiology & Biotechnology (2002) 29, 181–184 doi:10.1038/sj.jim.7000276 Received 18 March 2002/ Accepted in revised form 20 May 2002     

Enhanced phenylpyruvic acid production with Proteus vulgaris in fed-batch and continuous fermentation

Phenylpyruvic acid is a deaminated form of phenylalanine and is used in various areas such as development of cheese and wine flavors, diagnosis of phenylketonuria, and to decrease excessive nitrogen accumulation in the manure of farm animals. However, reported phenylpyruvic acid fermentation studies in the literature have been usually performed at shake-flask scale with low production. In this study, phenylpyruvic acid production was evaluated in bench-top bioreactors by conducting fed-batch and continuous fermentation for the first time. As a result, maximum phenylpyruvic acid concentrations increased from 1350 mg/L (batch fermentation) to 2958 mg/L utilizing fed-batch fermentation. Furthermore, phenylpyruvic acid productivity was increased from 48 mg/L/hr (batch fermentation) to 104 and 259 mg/L/hr by conducting fed-batch and continuous fermentation, respectively. Overall, this study demonstrated that fed-batch and continuous fermentation significantly improved phenylpyruvic acid production in bench-scale bioreactor production.     

Optimized nikkomycin production by fed-batch and continuous fermentation

We performed fed-batch and continuous fermentations to extend the time of maximal nikkomycin production by Streptomyces tendae Tü 901/S 2566. This was achieved by the fed-batch culture technique. Furthermore, high productivity was obtained at slow growth rates in a continuous fermentation process. Different dilution rates with and without carbon limitation were done and the results were compared. Correspondence to : T. Schüz     

烟曲霉TMS-26产紫杉醇补料分批发酵条件初步探索

内生真菌发酵法是解决紫杉醇药源短缺问题的有效途径之一。本研究以摇瓶分批发酵为基础,进行摇瓶补料分批发酵研究,探究了苯丙氨酸、甘氨酸、苯甲酸钠乙酸钠混合液、3,5-二硝基水杨酸、H₂O₂、CuSO₄在发酵周期（13d）中,不同添加时间点对TMS-26菌体量及紫杉醇产量的影响,发现在第8天添加苯丙氨酸、甘氨酸、3,5-二硝基水杨酸时,其产量分别达到了(664.80±40.34)µg/L、(628.72±30.44)µg/L、(641.36±19.62)µg/L;在第9天添加CuSO₄时,其产量达到了(697.46±15.76)µg/L;在第10天添加H₂O₂、苯甲酸钠乙酸钠混合液,其产量分别达到了(615.78±36.28)µg/L、(792.54±10.04)µg/L。在摇瓶补料分批发酵研究结果的基础上,进行了5L罐发酵工艺放大研究,探究了前体和诱导子通过进行一次补加和恒速补加的方式对Aspergillus fumigatus TMS-26菌体量及紫杉醇产量的影响,结果表明恒速补加苯丙氨酸乙酸钠混合液,紫杉醇产量达到了746.17µg/L。通过本次研究,优化了TMS-26产紫杉醇摇瓶补料分批发酵和5L罐发酵工艺,为后续实现紫杉醇工业化生产奠定基础。