He-Ne laser irradiation of folate-producing Candida utilis and optimization of culture conditions under submerged fermentation

In an attempt to obtain a microbial strain with higher yield of folate for industrial applications, we mutated the wild strain Candida utilis Y1.0 using a novel mutagenic process, i.e., irradiation by a helium–neon (He-Ne) laser with an output power of 20 mW and an exposure time of 20 min. The yield of folate in the mutated cells reached 1,102 ng/mL, which was 20.4-fold that of the wild strain. The mutant strain Y3.636 was relatively stable in terms of folate production through eight successive transfers of cultures and batch fermentation in a 3.7-L stirred-tank fermenter. Optimization further increased the yield of the mutant by 110 %, i.e., to 2,314?±?13 ng/mL. The optimal culture conditions for folate production were: cultivation in fermentation culture medium composed of 62.5 g/L glucose, 15 g/L corn liquor, 3 g/L (NH₄)₂SO₄, 3 g/L MgSO₄, and 1 g/L glutamic acid; inoculum size of 9 %; incubation at 28 °C and 196 rpm for 36 h. A time-course study of cell growth and folate production by mutant strain Y3.636 strongly suggested that folate production in C. utilis is growth-associated.     

Functional properties of a manganese-activated exo-polygalacturonase produced by a thermotolerant fungus Aspergillus niveus

A thermotolerant fungus identified as Aspergillus niveus was isolated from decomposing materials and it has produced excellent levels of hydrolytic enzymes that degrade plant cell walls. A. niveus germinated faster at 40 °C, presenting protein levels almost twofold higher than at 25 °C. The crude extract of the A. niveus culture was purified by diethylaminoethyl (DEAE)-cellulose, followed by Biogel P-100 column. Polygalacturonase (PG) is a glycoprotein with 37.7 % carbohydrate, molecular mass of 102.6 kDa, and isoelectric point of 5.4. The optimum temperature and pH were 50 °C and 4.0–6.5, respectively. The enzyme was stable at pH 3.0 to 9.0 for 24 h. The DEAE-cellulose derivative was about sixfold more stable at 60 °C than the free enzyme. Moreover, the monoaminoethyl-N-aminoethyl-agarose derivative was tenfold more stable than the free enzyme. PG was 232 % activated by Mn²⁺. The hydrolysis product of sodium polypectate corresponded at monogalacturonic acid, which classifies the enzyme as an exo-PG. The K _m, V _max, K _cat, and K _cat/K _m values were 6.7 mg/ml, 230 U/mg, 393.3/s, and 58.7 mg/ml/s, respectively. The N-terminal amino acid sequence presented 80 % identity with PglB1, PglA2, and PglA3 putative exo-PG of Aspergillus fumigatus and an exo-PG Neosartorya fischeri.     

Optimization of Fermentation Medium and Conditions for Mycelial Growth and Water-soluble Exo-polysaccharides Production by Isaria farinosa B05

Abstract

The optimal fermentation medium and conditions for mycelial growth and water-soluble exo-polysaccharides production by Isaria farinosa B05 were investigated. The medium components and fermentation conditions were optimized according to the one at a time method, while the concentration of medium components was determined by the orthogonal matrix method. The results showed that the optimal fermentation medium was as follows: sucrose 3.5% (w/v), peptone 0.5%, yeast extract 0.2%, K₂HPO₄ 0.1%, and MgSO₄ 0.05%. The suitable fermentation conditions were as follows: initial pH 7.0, temperature 25°C, medium volume 75 mL/250 mL, inoculum volume 5% (v/v), time 5d. In such optimal nutrition and environmental conditions, the maximal mycelial yield was 2.124 g/100 mL after 4 day's fermentation, while maximal water-soluble exo-polysaccharides production reached 2.144 g/L after 5 day's fermentation.     

Pectinase production by a Brazilian thermophilic fungus <Emphasis Type="Italic">Thermomucor indicae-seudaticae</Emphasis> N31 in solid-state and submerged fermentation

Thermophilic organisms produce thermostable enzymes, which have a number of applications, justifying the interest in the isolation of new thermophilic strains and study of their enzymes. Thirty-four thermophilic and thermotolerant fungal strains were isolated from soil, organic compost, and an industrial waste pile based on their ability to grow at 45°C and in a liquid medium containing pectin as the only carbon source. Among these fungi, 50% were identified at the genus level as Thermomyces, Aspergillus, Monascus, Chaetomium, Neosartoria, Scopulariopsis, and Thermomucor. All isolated strains produced pectinase during solid-state fermentation (SSF). The highest polygalacturonase (PG) activity was obtained in the culture medium of thermophilic strain N31 identified as Thermomucor indicae-seudaticae. Under SSF conditions on media containing a mixture of wheat bran and orange bagasse (1 : 1) at 70% of initial moisture, this fungus produced the maximum of 120 U/ml of exo-PG, while in submerged fermentation (SmF) it produced 13.6 U/ml. The crude PG from SmF was more thermostable than that from SSF and exhibited higher stability in acidic pH.     

Optimization of fermentation medium for xylanase-producing strain Xw2

To improve the fermentation yield of xylanase by optimizing the fermentation conditions for strain Xw2, a Plackett-Burman design was used to evaluate the effects of eight variables on xylanase production by strain Xw2. The steepest ascent （descent） method was used to approach the optimal response surface experimental area. The optimal fermentation conditions were obtained by central composite design and response surface analysis. The results showed that the composition of the optimal fermentation medium was corn cob ＋ 1.5% wheat bran （1：1）, 0.04% MnSO4, 0.04% K2HPO4. 3H2O, and an inoculum size of 6% in 50 mL liquid volume （pH = 6.0）. The optimal culture conditions were 28oc at 150 r/min for 54.23 h. The results of this study can serve as the basis for the industrial production and application of xylanase.     

Brevundimonas vesicularis MF276770, a new strain for gelatinase production by utilizing chicken feet gelatin

The utilization of waste has gained momentum in the field of waste management and industrial bioprocess. In this study, waste chicken feet were used as the source for extraction of a natural inducer, i.e. gelatin for the synthesis of proteolytic enzyme gelatinase. Microorganisms with gelatinolytic activity were screened from mixed culture isolates obtained from a local poultry waste dumping site. The strain which had shown maximum activity was identified as Brevundimonas vesicularis MF276770 using 16S rRNA gene sequencing. The composition of chicken feet gelatin was analysed and further characterized by Fourier transform infrared analysis and SDS-PAGE. The maximum gelatinase activity of 18.8?U/mL was achieved for the isolated Brevundimonas vesicularis MF276770 at 12?h under optimized conditions of pH 7, substrate concentration (2%), inoculums age (12?h), inoculum volume (2%, v/v), temperature (50?°C) and RPM (140). The enzyme kinetics parameters V_max and K_m were observed as 7.4?U/mL and 0.422 µmol, respectively. The molecular weight of the produced gelatinase was determined as 67?kDa. The produced gelatinase was employed to strip the gelatin silver layer from X-ray polyester film with 1.93?U/mL of gelatinase activity.     

Medium Optimization for Improved Production of Dihydrolipohyl Dehydrogenase from <Emphasis Type="Italic">Bacillus sphaericus</Emphasis> PAD-91 in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Dihydrolipohyl dehydrogenase (DLD) is a FAD-dependent enzyme that catalyzes the reversible oxidation of dihydrolipoamide. Herein, we report medium optimization for the production of a recombinant DLD with NADH-dependent diaphorase activity from a strain of Bacillus sphaericus PAD-91. The DLD gene that consisted of 1413 bp was expressed in Escherichia coli BL21 (DE3), and its enzymatic properties were studied. The composition of production medium was optimized using one-variable-at-a-time method followed by response surface methodology (RSM). B. sphaericus DLD catalyzed the reduction of lipoamide by NAD⁺ and exhibited diaphorase activity. The molecular weight of enzyme was about 50 kDa and determined to be a monomeric protein. Recombinant diaphorase showed its optimal activity at temperature of 30 °C and pH 8.5. K _m and V _max values with NADH were estimated to be 0.025 mM and 275.8 U/mL, respectively. Recombinant enzyme was optimally produced in fermentation medium containing 10 g/L sucrose, 25 g/L yeast extract, 5 g/L NaCl and 0.25 g/L MgSO₄. At these concentrations, the actual diaphorase activity was calculated to be 345.0 ± 4.1 U/mL. By scaling up fermentation from flask to bioreactor, enzyme activity was increased to 486.3 ± 5.5 U/mL. Briefly, a DLD with diaphorase activity from a newly isolated B. sphaericus PAD-91 was characterized and the production of recombinant enzyme was optimized using RSM technique.     

Optimization of Fermentation Conditions for Phytase Production by Two Strains of Bacillus licheniformis (LF1 and LH1) Isolated from the Intestine of Rohu, Labeo rohita (Hamilton)

The culture conditions for extracellular production of phytase by two strains of Bacillus licheniformis (LF1 and LH1) isolated from the proximal and distal intestine of rohu (Labeo rohita) were optimized to obtain maximum level of phytase. Both the strains were cultured TSA broth for 24 h at 37 ± 2 °C, when average viable count of 9.75 × 10⁷ cells ml^?1 culture broth was obtained. This was used as the inoculum for the production medium. Sesame (Sesamum indicum) oilseed meal was used as the source of phytic acid (substrate). The effects of moisture, pH, temperature, fermentation period, inoculum size, different nitrogen sources, vitamins and surfactants on phytase production by these two strains were evaluated. Phytase yield was highest (1.87 U in LF1 and 1.57 U in LH1) in solid-state fermentation. Enzyme production in both the isolates increased in an optimum pH range of 5.5–6.5. Minimum phytase production was observed at 50 °C, while maximum production was obtained at 40 °C. To standardize the fermentation period for phytase production, production rate was measured at 12-h intervals up to 120 h. Enzyme production increased for 72 h of fermentation in both strains, and decreased thereafter. The enzyme production increased with increased inoculum size up to 3.0 percentage points for the strain LF1 and up to 2.0 % for the strains LH1. Ammonium sulphate as the nitrogen source was most effective in LF1, while beef extract proved useful to maximize enzyme production by LH1.     

Improved extracellular expression and high-cell-density fed-batch fermentation of chitosanase from <Emphasis Type="Italic">Aspergillus Fumigatus</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Chitosanase (CSN) from Aspergillus fumigatus has good thermal stability, wide pH range duration, and effective hydrolysis for chitosan. Inhere, CSN was successfully expressed in Escherichia coli followed by extracellular secretion under the guidance of an N-terminal signal peptide PelB, which effectively prompted its secretion out of E. coli cells. To facilitate its later purification, N-terminal or C-terminal 6xHis epitope tag was added to the PelB-CSN protein complex. Our results indicated that PelB-CSN without 6xHis-tag (PelB-CSN) or with N-terminal 6xHis-tag (PelB-CSN-N) can both be effectively secreted into the medium, while CSN with 6xHis-tag anchored at C-terminus was expressed as inclusion bodies. Process optimization strategies were further developed to improve the secretion efficiency of recombinant PelB-CSN-N in E. coli. Under the induction of 10 g/L lactose in shake-flask culture, the extracellular activity of CSN reached 6015 U/mL at 25 °C in TB medium containing 1 % glycine. Moreover, a fed-batch fermentation strategy for high-cell-density cultivation was applied in a 5-L fermenter, increasing the extracellular CSN activity to 14,000 U/mL in 2-day fermentation with the optimal addition of lactose and glycine.     

A novel and cost-effective methodology for enhanced production of industrially valuable alkaline xylano-pectinolytic enzymes cocktail in short solid-state fermentation cycle

The aim of this study was to enhance the production of xylano-pectinolytic enzymes concurrently and also to reduce the fermentation period. In this study, the effect of agro-residues extract-based inoculum on yield and fermentation time of xylano-pectinolytic enzymes was studied. Microbial inoculum and fermentation media were supplemented with xylan and pectin polysaccharides derived from agro-based residues. Enzymes production parameters were optimized through two-stage statistical design approach. Under optimized conditions (temperature 37°C, pH 7.2, K₂HPO₄ 0.22%, MgSO₄ 0.1%, gram flour 5.6%, substrate: moisture ratio 1:2, inoculum size 20%, agro-based crude xylan in production media 0.45%, and agro-based crude xylan–pectin in inoculum 0.13%), nearly 28,255 ± 565 and 9,202 ± 193 IU of xylanase and pectinase, respectively, were obtained per gram of substrate in a time interval of 6 days only. The yield of both xylano-pectinolytic enzymes was enhanced along with a reduction of nearly 24 h in fermentation time in comparison with control, using polysaccharides extracted from agro-residues. The activity of different types of pectinase enzymes such as exo-polymethylgalacturonase (exo-PMG), endo-PMG, exo-polygalacturonase (exo-PG), endo-PG, pectin lyase, pectate lyase, and pectin esterase was obtained as 1,601, 12.13, 5637, 24.86, 118.62, 124.32, and 12.56 IU/g, respectively, and was nearly twofold higher than obtained for all seven types in control samples. This is the first report mentioning the methodology for enhanced production of xylano-pectinolytic enzymes in short solid-state fermentation cycle using agro-residues extract-based inoculum and production media.     

Bioprocess optimization for pectinase production using <Emphasis Type="Italic">Aspergillus niger</Emphasis> in a submerged cultivation system

Background

Pectinase enzymes present a high priced category of microbial enzymes with many potential applications in various food and oil industries and an estimated market share of $ 41.4 billion by 2020.

Results

The production medium was first optimized using a statistical optimization approach to increase pectinase production. A maximal enzyme concentration of 76.35 U/mL (a 2.8-fold increase compared with the initial medium) was produced in a medium composed of (g/L): pectin, 32.22; (NH₄)₂SO₄, 4.33; K₂HPO₄, 1.36; MgSO₄.5H₂O, 0.05; KCl, 0.05; and FeSO₄.5H₂O, 0.10. The cultivations were then carried out in a 16-L stirred tank bioreactor in both batch and fed-batch modes to improve enzyme production, which is an important step for bioprocess industrialization. Controlling the pH at 5.5 during cultivation yielded a pectinase production of 109.63 U/mL, which was about 10% higher than the uncontrolled pH culture. Furthermore, fed-batch cultivation using sucrose as a feeding substrate with a rate of 2 g/L/h increased the enzyme production up to 450 U/mL after 126 h.

Conclusions

Statistical medium optimization improved volumetric pectinase productivity by about 2.8 folds. Scaling-up the production process in 16-L semi-industrial stirred tank bioreactor under controlled pH further enhanced pectinase production by about 4-folds. Finally, bioreactor fed-batch cultivation using constant carbon source feeding increased maximal volumetric enzyme production by about 16.5-folds from the initial starting conditions.

     

Production of thermostable and neutral glucoamylase using immobilized <Emphasis Type="Italic">Thermomucor indicae-seudaticae</Emphasis>

Thermomucor indicae-seudaticae was immobilized in alginate, κ-carrageenan, agarose, agar, polyacrylamide and loofah (Luffa cylindrica) sponge (as such or coated with alginate/starch/Emerson YpSs agar), and used for the production of glucoamylase in submerged fermentation. The mycelium developed from alginate-immobilized sporangiospores secreted higher glucoamylase titres (22.7 U ml⁻¹) than those immobilized in other gel matrices and the freely growing mycelial pellets (18.5 U ml⁻¹). Loofah network provided a good support for mycelial growth, but the enzyme production was lower than that attained with alginate beads. Glucoamylase production increased with inoculum density and the optimum levels were achieved when 40 calcium alginate beads (∼5 × 10⁶ immobilized spores) were used to inoculate 50 ml production medium. The alginate bead inoculum displayed high storage stability at 4°C and produced comparable enzyme titres up to 120 days. The glucoamylase production by hyphae emerged from the immobilized sporangiospores was almost stable over eight batches of repeated fermentation. Scanning electron micrographs of alginate beads, after batch fermentation, revealed extensive mycelial growth inside and around the beads.     

Regulation of extracellular acid phosphatase biosynthesis by culture conditions in entomopathogenic fungusMetarhizium anisopliae strain CQMa102

Metarhizium anisopliae is an imperfect entomopathogenic fungus. Once invading into its host,M. anisopliae needs to absorb basic nutrients such as phosphorus from the host haemolymph. A large number of phosphorylated compounds in haemolymph cannot be directly utilised by the fungal cell and must be hydrolysed into available form by phosphatase before ingested. Aims of this paper were to investigate optimum fermentation conditions for production of acid phosphatase and phosphatase isoenzymes byMetarhizium anisopliae. The optimum fermentation conditions were: glucose, 20 g/l; (NH₄)₂SO₄, 2 g/l; casein, 4 g/l; MgSO₄, 0.5 g; KCl, 0.5 g; microelement salt solution, 10 ml; inoculum size, 1×10⁷ spores per 100 ml medium; initial medium pH, 6.0. Under these conditions, the highest total acid phosphatase activity was 3.05 U/ml in 4 days at 27 °C and 160 rpm. Synthesis of the acid phosphatase was repressed by 0.01% inorganic phosphate in culture medium. The spectrum of isoenzymes produced byM. anisopliae varied depending on the phosphorus source employed in the culture. A specific isoform with pI 9.45 was induced by casein, and another isoform of pI 8.21 was induced by phytic acid and disodium phenyl phosphate.     

Fermentation of cellulosic hydrolysates obtained by enzymatic saccharification of sugarcane bagasse pretreated by hydrothermal processing

This work aims to evaluate the fermentability of cellulosic hydrolysates obtained by enzymatic saccharification of sugarcane bagasse pretreated by hydrothermal processing using Candida guilliermondii FTI 20037 yeast. The inoculum was obtained from yeast culture in a medium containing glucose as a carbon source supplemented with rice bran extract, CaCl₂·2H₂O and (NH₄)₂SO₄ in 50 mL Erlenmeyer flasks, containing 20 mL of medium, initial 5.5 pH under agitation of an orbital shaker (200 rpm) at 30°C for 24 h. The cellulosic hydrolysates, prior to being used as a fermentation medium, were autoclaved for 15 min at 0.5 atm and supplemented with the same nutrients employed for the inoculum, except the glucose, using the same conditions for the inoculum, but with a period of 48 h. Preliminary results showed the highest consumption of glucose (97%) for all the hydrolysates, at 28 h of fermentation. The highest concentration of ethanol (20.5 g/L) was found in the procedure of sugarcane bagasse pretreated by hydrothermal processing (195°C/10 min in 20 L reactor) and delignificated with NaOH 1.0% (w/v), 100°C, 1 h in 500 mL stainless steel ampoules immersed in an oil bath.     

Production and optimization of polygalacturonase from mango (<Emphasis Type="Italic">Mangifera indica</Emphasis> L.) peel using <Emphasis Type="Italic">Fusarium moniliforme</Emphasis> in solid state fermentation

Mango peel is one of the major wastes from fruit processing industries, which poses considerable disposal problems and ultimately leads to environmental pollution. The objective of the current research was to determine the significant parameters on the production of polygalacturonase from mango peel which is a major industrial waste. Solid state culture conditions for polygalacturonase production by Fusarium moniliforme from dried mango peel powder were optimized by Taguchi’s L-18 orthogonal array experimental design methodology. Eight fungal metabolic influencing variables, viz. temperature, mango peel, inoculum, peptone, ammonium nitrate (NH₄NO₃₎, magnesium sulphate (MgSO₄), zinc sulphate (ZnSO₄) and potassium dihydrogen phosphate (KH₂PO₄) were selected to optimize polygalacturonase production. The optimized parameters composed of temperature (30°C), mango peel (6.5%, g, w/v), inoculum (8%, ml, v/v), peptone (1%, g, w/v), NH₄NO₃ (0.60%, g, w/v), MgSO₄ (0.05%, g, w/v), ZnSO₄ (0.06%, g, w/v) and KH₂PO₄ (0.4%, g, w/v). Based on the influence of interaction of fermentation components of fermentation, these could be classified as the least significant and the most significant at individual and interaction levels. The temperature, inoculum level, mango peel substrate and KH₂PO₄ showed maximum production impact at optimized conditions. From the optimized conditions the polygalacturonase activity was maximized to 43.2 U g⁻¹.     

Enhanced production of Thermomyces lanuginosus lipase in Pichia pastoris via genetic and fermentation strategies

This study attempted to enhance the expression level of Thermomyces lanuginosus lipase (TLL) in Pichia pastoris using a series of strategies. The tll gene was first inserted into the expression vector pPIC9 K and transformed into P. pastoris strain GS115. The maximum hydrolytic activity of TLL reached 4,350 U/mL under the optimal culture conditions of a 500 mL shaking flask containing 20 mL culture medium with the addition of 1.2 % (w/v) methanol, cultivation for 144 h at pH 7.0 and 27 °C. To further increase the TLL expression and copy number, strains containing two plasmids were obtained by sequential electroporation into GS115/9k-TLL #3 with a second vector, either pGAPZαA-TLL, pFZα-TLL, or pPICZαA-TLL. The maximum activity of the resultant strains GS115/9KTLL-ZαATLL #40, GS115/9KTLL-FZαATLL #46 and GS115/9KTLL-GAPTLL #45 was 6,600 U/mL, 6,000 U/mL and 4,800 U/mL, respectively. The tll copy number in these strains, as assessed by real-time quantitative PCR, was demonstrated to be seven, five, and three, respectively, versus two copies in GS115/9k-TLL #3. When a co-feeding strategy of sorbitol/methanol was adopted in a 3-L fermenter, the maximum TLL activity of GS115/9k-TLL #3 increased to 27,000 U/mL after 130 h of fed-batch fermentation, whereas, the maximum TLL activity was 19,500 U/mL after 145 h incubation when methanol was used as the sole carbon source.     

液态发酵豆粕制备纳豆激酶方法的优化

纳豆激酶是一种丝氨酸蛋白酶,具有很强的纤溶活性,由于具有安全性好、作用迅速持久、成本低等优点,适合用于开发新一代的溶栓剂或保健食品,具有广阔的市场前景。本研究探讨了以豆粕为原料液态发酵豆粕生产纳豆激酶的发酵方法。首先通过单因素实验发现影响产酶的主要因素有接菌量、发酵时间、培养基pH及豆粕含量,再由正交实验得到最优组合为接菌量1%,豆粕含量2%,pH为7.0,发酵时间48h,该条件下发酵酶活力最高达到4 429.6U/mL。本研究确定了以豆粕为原料制备纳豆激酶的最佳条件,为豆粕的合理使用和纳豆激酶的工业化生产提供了实验依据。     

The effect of methanogenesis inhibition,inoculum and substrate concentration on hydrogen and carboxylic acids production from cassava wastewater

Manipueira is a carbohydrate-rich agro-industrial waste from cassava processing. It is considered well suitable for biotechnological processes, such as hydrogen and carboxylic acids production, due to the high content of easily degradable organic matter. However, the proper methanogenesis inhibition method, inoculum type, and organic loads are factors still limiting the processes. The objective in this work was to evaluate the effects of such factors on byproducts production in anaerobic reactors. Batch experiments were conducted with 2.3-L flasks during two operational phases. In the first phase (P1), inhibition of methanogens in the sludge was evaluated using acetylene (1% v/v of headspace) and heat treatment (120 °C, 1 atm for 30 min). In the second phase (P2), three inoculum types obtained from common anaerobic sludges (bovine rumen and sludges from municipal and textile industrial wastewater treatment plants) were individually assayed. P2 aimed to identify the best inoculum, based on hydrogen production ability, which was tested for three initial concentrations of manipueira in terms of chemical oxygen demand (COD) (10, 20 and 40 g O₂/L). Results of P1 indicated that either acetylene or heat treatment efficiently inhibited methanogenesis, with no methane production. However, the maximum H₂ production potential by applying heat treatment (~ 563 mL) was more than twice compared with that by acetylene treatment (~ 257 mL); and butyrate was the main carboxylic acid by-product (~ 3 g/L). In P2 experiments after sludge heat treatment, the highest hydrogen yield (1.66 ± 0.07 mol H₂/mol glucose) and caproic acid production (~ 2 g/L) were observed at 20 g O₂/L of manipueira COD, when bovine rumen was the inoculum. The primary metabolic degradation products in all P2 experiments were ethanol, acetic, butyric, propionic and caproic acids. The finding of caproic acid detection indicated that the applied conditions in manipueira anaerobic degradation favored carbon chain elongation over methanogenesis.     

OPTIMIZATION OF SOLID-STATE FERMENTATION FOR PHYTASE PRODUCTION BY Thermomyces lanuginosus USING RESPONSE SURFACE METHODOLOGY

A strain of Thermomyces lanuginosus, isolated from hot spring water in Turkey, was studied for optimization of phytase production using solid-state fermentation. Effects on fermentation of different production parameters such as substrate type, moisture, culture time, and inoculum size were investigated using a one-factor-at-a-time approach. Central composite design (CCD) of response surface methodology was applied for the optimization of four factors (culture temperature, initial pH, aeration area, age of seeding culture) that were affecting phytase production by Thermomyces lanuginosus in rice bran. Maximum phytase activity was achieved by using rice bran. The optimum levels of variables that supported maximum enzyme activity were moisture 70%, culture time 7 days, inoculum size 40%, culture temperature 55°C, initial pH 7.5, aeration area 30%, age of seeding culture 5 days, sucrose 1%, and ZnSO₄ 2.5 mM. An overall 10.83-fold enhancement in phytase activity (0.30 to 3.248 U) was attained due to the optimization.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid by <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> using semicontinuous fermentation in bioreactor

Semicontinuous fermentation using pellets of Rhizopus oryzae has been recognized as a promising technology for l-lactic acid production. In this work, semicontinuous fermentation of R. oryzae AS 3.819 for l-lactic acid production has been developed with high l-lactic acid yield and volumetric productivity. The effects of factors such as inoculations, CaCO₃ addition time, and temperature on l-lactic acid yield and R. oryzae morphology were researched in detail. The results showed that optimal fermentation conditions for the first cycle were: inoculation with 4% spore suspension, CaCO₃ added to the culture medium at the beginning of culture, and culture temperature of 32–34°C. In orthogonal experiments, high l-lactic acid yield was achieved when the feeding medium was (g/l): glucose, 100; (NH₄)₂SO₄, 2; KH₂PO₄, 0.1; ZnSO₄·7H₂O, 0.33; MgSO₄·7H₂O, 0.15; CaCO₃, 50. Twenty cycles of semicontinuous fermentation were carried out in flask culture. l-lactic acid yield was 78.75% for the first cycle and 80–90% for the repeated cycles; the activities of lactate dehydrogenases (LDH) were 7.2–9.2 U/mg; fermentation was completed in 24 h for each repeated cycle. In a 7-l magnetically stirred fermentor, semicontinuous fermentation lasted for 25 cycles using pellets of R. oryzae AS 3.819 under the optimal conditions determined from flask cultures. The final l-lactic acid concentration (LLAC) reached 103.7 g/l, and the volumetric productivity was 2.16 g/(l·h) for the first cycle; in the following 19 repeated cycles, the final LLAC reached 81–95 g/l, and the volumetric productivities were 3.40–3.85 g/(l·h).