Molecular cloning and expression of the pyranose 2-oxidase cDNA from<Emphasis Type="Italic"> Trametes ochracea</Emphasis> MB49 in<Emphasis Type="Italic"> Escherichia coli</Emphasis>

A cDNA of a structural gene encoding pyranose 2-oxidase (P2O) from Trametes ochracea strain MB49 was cloned into Escherichia coli strain BL21(DE3) on a multicopy plasmid under the control of the trc promoter. Synthesis of P2O was studied in batch cultures in LB or M9-based mineral medium at 28°C. While there was a low specific activity of P2O in LB medium, the enzyme was synthesised constitutively in mineral medium and represented 3% of the cell soluble protein (0.3 U mg^–1). The effect of isopropyl -d-thiogalactoside on the expression of P2O was studied in mineral medium at 25 and 28°C. The synthesis of P2O at 28°C corresponded to 39% of the cell soluble protein but the major portion of P2O (93%) was in the form of non-active inclusion bodies (activity of P2O equalled 0.19 U mg^–1). At 25°C, the amount of P2O represented 14% of the cell soluble protein and the activity of P2O was 1.1 U mg^–1. The soluble enzyme represented 70% of the total amount of P2O.     

Continuous <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid production by a novelthermotolerant <Emphasis Type="Italic">Lactobacillus delbrueckii</Emphasis> subsp. <Emphasis Type="Italic">lactis</Emphasis> QU 41

We isolated and characterized a d-lactic acid-producing lactic acid bacterium (d-LAB), identified as Lactobacillus delbrueckii subsp. lactis QU 41. When compared to Lactobacillus coryniformis subsp. torquens JCM 1166 ^T and L. delbrueckii subsp. lactis JCM 1248 ^T, which are also known as d-LAB, the QU 41 strain exhibited a high thermotolerance and produced d-lactic acid at temperatures of 50 °C and higher. In order to optimize the culture conditions of the QU 41 strain, we examined the effects of pH control, temperature, neutralizing reagent, and initial glucose concentration on d-lactic acid production in batch cultures. It was found that the optimal production of 20.1 g/l d-lactic acid was acquired with high optical purity (>99.9% of d-lactic acid) in a pH 6.0-controlled batch culture, by adding ammonium hydroxide as a neutralizing reagent, at 43 °C in MRS medium containing 20 g/l glucose. As a result of product inhibition and low cell density, continuous cultures were investigated using a microfiltration membrane module to recycle flow-through cells in order to improve d-lactic acid productivity. At a dilution rate of 0.87 h⁻¹, the high cell density continuous culture exhibited the highest d-lactic acid productivity of 18.0 g/l/h with a high yield (ca. 1.0 g/g consumed glucose) and a low residual glucose (<0.1 g/l) in comparison with systems published to date.     

Gene cloning and heterologous expression of pyranose 2-oxidase from the brown-rot fungus, <Emphasis Type="Italic">Gloeophyllum</Emphasis><Emphasis Type="Italic">trabeum</Emphasis>

A pyranose 2-oxidase gene from the brown-rot basidiomycete Gloeophyllum trabeum was isolated using homology-based degenerate PCR. The gene structure was determined and compared to that of several pyranose 2-oxidases cloned from white-rot fungi. The G. trabeum pyranose 2-oxidase gene consists of 16 coding exons with canonical promoter CAAT and TATA elements in the 5′UTR. The corresponding G. trabeum cDNA was cloned and contains an ORF of 1,962 base pairs encoding a 653 amino acid polypeptide with a predicted molecular weight of 72 kDa. A Hisx6 tagged recombinant G. trabeum pyranose 2-oxidase was generated and expressed heterologously in Escherichia coli yielding 15 U enzyme activity per ml of induced culture. Structural alignment and phylogenetic analysis were performed and are discussed.     

Effect of temperature on <Emphasis Type="SmallCaps">d</Emphasis>-arabitol production from lactose by <Emphasis Type="Italic">Kluyveromyces lactis</Emphasis>

d-Arabitol production from lactose by Kluyveromyces lactis NBRC 1903 has been studied by following the time courses of concentrations of cell mass, lactose, d-arabitol, ethanol, and glycerol at different temperatures. It was found that temperature is a key factor in d-arabitol production. Within temperatures ranging from 25 to 39°C, the highest d-arabitol concentration of 99.2 mmol l⁻¹ was obtained from 555 mmol l⁻¹ of lactose after 120 h of batch cultivation at 37°C. The yield of d-arabitol production on cell mass growth increased drastically at temperatures higher than 35°C, and the yield reached 1.07 at 39°C. Increasing the cell mass concentration two-fold after 24 h of culture growth at 37°C, the d-arabitol concentration further increased to 168 mmol l⁻¹. According to the distribution of the metabolic products, metabolic changes related to growth phase were also discussed. The stationary-phase K. lactis cells in the batch culture that is started with exposing the precultured inoculum to high osmotic stress, high oxidative stress, and high heat stress are found to be preferable for d-arabitol production.     

Mannose production from fructose by free and immobilized <Emphasis Type="SmallCaps">d</Emphasis>-lyxose isomerases from <Emphasis Type="Italic">Providencia stuartii</Emphasis>

A recombinant d-lyxose isomerase from Providencia stuartii was immobilized on Duolite A568 beads which gave the highest conversion of d-fructose to d-mannose among the various immobilization beads evaluated. Maximum activities of both the free and immobilized enzymes for fructose isomerization were at pH 7.5 and 45°C in the presence of 1 mM Mn²⁺. Enzyme half-lives were 14 and 30 h at 35°C and 3.4 and 5.1 h at 45°C, respectively. The immobilized enzyme in 300 g fructose/l (replaced hourly), produced 75 g mannose/l at 35°C = 25% (w/w) yield with a productivity of 75 g mannose l⁻¹ h⁻¹ after 23 cycles.     

Characterization of ribose-5-phosphate isomerase of <Emphasis Type="Italic">Clostridium thermocellum</Emphasis> producing <Emphasis Type="SmallCaps">d</Emphasis>-allose from <Emphasis Type="SmallCaps">d</Emphasis>-psicose

The rpiB gene, encoding ribose-5-phosphate isomerase (RpiB) from Clostridium thermocellum, was cloned and expressed in Escherichia coli. RpiB converted d-psicose into d-allose but it did not convert d-xylose, l-rhamnose, d-altrose or d-galactose. The production of d-allose by RpiB was maximal at pH 7.5 and 65°C for 30 min. The half-lives of the enzyme at 50°C and 65°C were 96 h and 4.7 h, respectively. Under stable conditions of pH 7.5 and 50°C, 165 g d-allose l⁻¹ was produced without by-products from 500 g d-psicose l⁻¹ after 6 h.     

Vanillin production using <Emphasis Type="Italic">Escherichia coli</Emphasis> cells over-expressing isoeugenol monooxygenase of <Emphasis Type="Italic">Pseudomonas putida</Emphasis>

The isoeugenol monooxygenase gene of Pseudomonas putida IE27 was inserted into an expression vector, pET21a, under the control of the T7 promoter. The recombinant plasmid was introduced into Escherichia coli BL21(DE3) cells, containing no vanillin-degrading activity. The transformed E. coli BL21(DE3) cells produced 28.3 g vanillin/l from 230 mM isoeugenol, with a molar conversion yield of 81% at 20°C after 6 h. In the reaction system, no accumulation of undesired by-products, such as vanillic acid or acetaldehyde, was observed.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-phenylalanine from glycerol by a recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

The production of l-phenylalanine is conventionally carried out by fermentations that use glucose or sucrose as the carbon source. This work reports on the use of glycerol as an inexpensive and abundant sole carbon source for producing l-phenylalanine using the genetically modified bacterium Escherichia coli BL21(DE3). Fermentations were carried out at 37°C, pH 7.4, using a defined medium in a stirred tank bioreactor at various intensities of impeller agitation speeds (300–500 rpm corresponding to 0.97–1.62 m s⁻¹ impeller tip speed) and aeration rates (2–8 L min⁻¹, or 1–4 vvm). This highly aerobic fermentation required a good supply of oxygen, but intense agitation (impeller tip speed ~1.62 m s⁻¹) reduced the biomass and l-phenylalanine productivity, possibly because of shear sensitivity of the recombinant bacterium. Production of l-phenylalanine was apparently strongly associated with growth. Under the best operating conditions (1.30 m s⁻¹ impeller tip speed, 4 vvm aeration rate), the yield of l-phenylalanine on glycerol was 0.58 g g⁻¹, or more than twice the best yield attainable on sucrose (0.25 g g⁻¹). In the best case, the peak concentration of l-phenylalanine was 5.6 g L⁻¹, or comparable to values attained in batch fermentations that use glucose or sucrose. The use of glycerol for the commercial production of l-phenylalanine with E. coli BL21(DE3) has the potential to substantially reduce the cost of production compared to sucrose- and glucose-based fermentations.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-arabitol by a newly isolated <Emphasis Type="Italic">Zygosaccharomyces rouxii</Emphasis>

A newly isolated Zygosaccharomyces rouxii NRRL 27,624 produced d-arabitol as the main metabolic product from glucose. In addition, it also produced ethanol and glycerol. The optimal conditions were temperature 30°C, pH 5.0, 350 rpm, and 5% inoculum. The yeast produced 83.4 ± 1.1 g d-arabitol from 175 ± 1.1 g glucose per liter at pH 5.0, 30°C, and 350 rpm in 240 h with a yield of 0.48 g/g glucose. It also produced d-arabitol from fructose, galactose, and mannose. The yeast produced d-arabitol and xylitol from xylose and also from a mixture of xylose and xylulose. Resting yeast cells produced 63.6 ± 1.9 g d-arabitol from 175 ± 1.8 g glucose per liter in 210 h at pH 5.0, 30°C and 350 rpm with a yield of 0.36 g/g glucose. The yeast has potential to be used for production of xylitol from glucose via d-arabitol route. Mention of trade names or commercial products in this article is solely for the purpose of providing specific information and does not imply recommendation or endorsement by the U.S. department of Agriculture.     

<Emphasis Type="SmallCaps">d</Emphasis>-Psicose production from <Emphasis Type="SmallCaps">d</Emphasis>-fructose using an isolated strain, <Emphasis Type="Italic">Sinorhizobium</Emphasis> sp.

Sinorhizobium sp., which can convert d-fructose into d-psicose, was isolated from soil. The optimal pH, temperature, and cell concentration for d-psicose production with the isolated strain were 8.5, 40°C, and 60 mg/ml, respectively. The toluene-treated cells showed 2.5- and 4.8-fold increases in the d-psicose concentration and productivity compared with untreated washed cells. Under the optimal conditions, the toluene-treated cells produced 37 g d-psicose/l from 70% (w/v) (3.9 M) d-fructose after 15 h.     

Optimized expression of an acid xylanase from <Emphasis Type="Italic">Aspergillus usamii</Emphasis> in <Emphasis Type="Italic">Pichia pastoris</Emphasis> and its biochemical characterization

The xylanase gene xyn II from Aspergillus usamii E001 was placed under the control of an alcohol oxidase promoter (AOX1) in the plasmid pPIC9K and integrated into the genome of a methylotrophic yeast, P. pastoris GS115, by electroporation. His⁺ transformants were screened for on the basis of their resistance to G418 and activity assay. A transformant, P. pastoris GSC12, which showed resistance to over 6 mg G418/ml and highest xylanase activity was selected. Recombinant xylanase was secreted by P. pastoris GSC12 24 h after methanol induction of shake-flask cultures, and reached a final yield of 3139. About 68 U/mg 120 h after the induction. The molecular mass of this xylanase was estimated to be 21 kDa by SDS-PAGE. The optimum pH and temperature were 4.2 and 50 °C, respectively. Xylanase was stable below 50 °C and within pH 3.0–7.0. Its activity was increased by EDTA and Co²⁺ ion and strongly inhibited by Mn²⁺, Li⁺ and Ag⁺ ions. The K _m and V _max values with birchwood xylan as the substrate were found to be 5.56 mg/ml and 216 μmol/mg/min, respectively. This is the first report on expression and characterization of xylanase from A. usamii in P. pastoris. The hydrolysis products consisted of xylooligosaccharides together with a small amount of xylose. This property made the enzyme attractive for industrial purposes, as relatively pure xylooligosaccharides could be obtained.     

Purification and characterization of <Emphasis Type="SmallCaps">l</Emphasis>-arabinose isomerase from <Emphasis Type="Italic">Lactobacillus plantarum</Emphasis> producing <Emphasis Type="SmallCaps">d</Emphasis>-tagatose

l-arabinose isomerase (EC5.3.1.4. AI) mediates the isomerization of d-galactose into d-tagatose as well as the conversion of l-arabinose into l-ribulose. The AI from Lactobacillus plantarum SK-2 was purified to an apparent homogeneity giving a single band on SDS–PAGE with a molecular mass of 59.6 kDa. Optimum activity was observed at 50°C and pH 7.0. The enzyme was stable at 50°C for 2 h and held between pH 4.5 and 8.5 for 1 h. AI activity was stimulated by Mn²⁺, Fe³⁺, Fe²⁺, Ca²⁺ and inhibited by Cu²⁺, Ag⁺, Hg²⁺, Pb²⁺. d-galactose and l-arabinose as substrates were isomerized with high activity. l-arabitol was the strongest competitive inhibitor of AI. The apparent Michaelis–Menten constant (K _m), for galactose, was 119 mM. The first ten N-terminal amino acids of the enzyme were determined as MLSVPDYEFW, which is identical to L. plantarum (Q88S84). Using the purified AI, 390 mg tagatose could be converted from 1,000 mg galactose in 96 h, and this production corresponds to a 39% equilibrium.     

Characterization of <Emphasis Type="SmallCaps">d</Emphasis>-tagatose-3-epimerase from <Emphasis Type="Italic">Rhodobacter sphaeroides</Emphasis> that converts <Emphasis Type="SmallCaps">d</Emphasis>-fructose into <Emphasis Type="SmallCaps">d-</Emphasis>psicose

A non-characterized gene, previously proposed as the d-tagatose-3-epimerase gene from Rhodobacter sphaeroides, was cloned and expressed in Escherichia coli. Its molecular mass was estimated to be 64 kDa with two identical subunits. The enzyme specificity was highest with d-fructose and decreased for other substrates in the order: d-tagatose, d-psicose, d-ribulose, d-xylulose and d-sorbose. Its activity was maximal at pH 9 and 40°C while being enhanced by Mn²⁺. At pH 9 and 40°C, 118 g d-psicose l⁻¹ was produced from 700 g d-fructose l⁻¹ after 3 h. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

High-level heterologous expression of an alkaline lipase gene from <Emphasis Type="Italic">Penicillium cyclopium</Emphasis> PG37 in <Emphasis Type="Italic">Pichia pastoris</Emphasis>

A 777-bp cDNA fragment encoding a mature alkaline lipase (LipI) from Penicillium cyclopium PG37 was amplified by RT–PCR, and inserted into the expression plasmid pPIC9 K. The recombinant plasmid, designated as pPIC9 K-lipI, was linearized with SalI and transformed into Pichia pastoris GS115 (his4, Mut⁺) by electroporation. MD plate and YPD plates containing G418 were used for screening of the multi-copy P. pastoris transformants (His⁺, Mut⁺). One transformant resistant to 4.0 mg/ml of G418, numbered as P. pastoris GSL4-7, expressing the highest recombinant LipI (rLipI) activity was chosen for optimizing expression conditions. The integration of the gene LipI into the P. pastoris GS115 genome was confirmed by PCR analysis using 5′- and 3′-AOX1 primers. SDS–PAGE and lipase activity assays demonstrated that the rLipI, a glycosylated protein with an apparent molecular weight of about 31.5 kDa, was extracellularly expressed in P. pastoris. When the P. pastoris GSL4-7 was cultured under the optimized conditions, the expressed rLipI activity was up to 407 U/ml, much higher than that (10.5 U/ml) expressed with standard protocol. The rLipI showed the highest activity at pH 10.5 and 25°C, and was stable at a broad pH range of 7.0–10.5 and at a temperature of 30°C or below.     

Heterologous expression and biochemical characterization of novel pyranose 2-oxidases from the ascomycetes <Emphasis Type="Italic">Aspergillus nidulans</Emphasis> and <Emphasis Type="Italic">Aspergillus oryzae</Emphasis>

A gene encoding a pyranose 2-oxidase (POx; pyranose/oxygen 2-oxidoreductase; glucose 2-oxidase; EC 1.1.3.10) was identified in the genome of the ascomycete Aspergillus nidulans. Attempts to isolate POx directly from A. nidulans cultures or to homologously overexpress the native POx (under control of the constitutive gpdA promoter) in A. nidulans were unsuccessful. cDNA encoding POx was synthesized from mRNA and expressed in Escherichia coli, and the enzyme was subsequently purified and characterized. A putative pyranose 2-oxidase-encoding gene was also identified in the genome of Aspergillus oryzae. The coding sequence was synthetically produced and was also expressed in E. coli. Both purified enzymes were shown to be flavoproteins consisting of subunits of 65 kDa. The A. nidulans enzyme was biochemically similar to POx reported in literature. From all substrates, the highest catalytic efficiency was found with D-glucose. In addition, the enzyme catalyzes the two-electron reduction of 1,4-benzoquinone, several substituted benzoquinones and 2,6-dichloroindophenol. As judged by the catalytic efficiencies (k _cat/k _m), some of these quinone electron acceptors are better substrates for pyranose oxidase than oxygen. The enzyme from A. oryzae was physically similar but showed lower kinetic constants compared to the enzyme from A. nidulans. Distinct differences in the stability of the two enzymes may be attributed to a deletion and an insertion in the sequence, respectively.     

Highly efficient production of <Emphasis Type="SmallCaps">d</Emphasis>-lactate by <Emphasis Type="Italic">Sporolactobacillus</Emphasis> sp. CASD with simultaneous enzymatic hydrolysis of peanut meal

Highly efficient d-lactate production by Sporolactobacillus sp. strain CASD was demonstrated in this study. Peanut meal was found to be a better nutrient than yeast extract, soybean meal, soybean peptone, corn steep, liquor beef extract, and ammonium sulfate in the production of d-lactate. To improve the utilization of peanut meal, the material was enzymatically hydrolyzed and simultaneously utilized as the nitrogen source in d-lactate fermentation. Very high d-lactate production (207 g/L) was obtained using 40 g/L of peanut meal in 30-L fed-batch fermentation, with the average productivity of 3.8 g/(L·h) and optical purity of 99.3%. The production of such a high concentration of optically pure d-lactate by strain CASD, with the simultaneous enzymatic hydrolysis of peanut meal and fermentation, represents a new cost-efficient and integrated method for d-lactate production using agricultural by-products.     

Expression in <Emphasis Type="Italic">Escherichia coli</Emphasis> of the recombinant <Emphasis Type="Italic">Vibrio anguillarum</Emphasis> metalloprotease and its purification and characterization

The full length empA gene encoding Vibrio anguillarum metalloprotease was amplified by PCR and fused to the expression vector pBAD24. The carboxy-terminal 6xHis-tagged recombinant metalloprotein (rEmpA) was expressed from plasmid pBAD-VAP6his in E. coli TOP10 and purified with affinity chromatography using a Ni-NTA column. SDS-PAGE analysis and Western blotting revealed a molecular mass of the mature rEmpA predicted to be 36 kDa. The optimal temperature and pH for the purified rEmpA were 37°C and 8.0, respectively. The enzyme was stable below 30°C and between pH 5.0 and 8.0, respectively. The results show that Ca²⁺, Na⁺ and Mg²⁺ had an activating effect on the enzyme while Zn²⁺ and Cu²⁺ acted as inhibitors of the enzyme. The purified rEmpA was characterized as a zinc metalloprotease as it was inhibited by zinc- and metal-specific inhibitors, such as 1,10-phenanthroline, EDTA and EGTA. The results indicate that some characteristics of EmpA from marine V. anguillarum had been modified after expression and processing in the engineered E. coli. The purified rEmpA showed degradation activity towards various kinds of proteins, indicating its potential role in pathogenesis.     

Productivity and biochemical composition of <Emphasis Type="Italic">Tetradesmus obliquus</Emphasis> and <Emphasis Type="Italic">Phaeodactylum tricornutum</Emphasis>: effects of different cultivation approaches

The present work evaluated biomass productivity, carbon dioxide fixation rate, and biochemical composition of two microalgal species, Phaeodactylum tricornutum (Bacillariophyta) and Tetradesmus obliquus (Chlorophyta), cultivated indoors in high-technology photobioreactors (HT-PBR) and outdoors both in pilot ponds and low-technology photobioreactors in a greenhouse in southern Italy. Microalgae were grown in standard media, under nitrogen starvation, and in two liquid digestates obtained from anaerobic digestion of agro-zootechnical and vegetable biomass. P. tricornutum, cultivated in semi-continuous mode in indoor HT-PBRs with standard medium, showed a biomass productivity of 21.0?±?2.3 g m^?2 d^?1. Applying nitrogen starvation, the lipid productivity increased from 2.3 up to 4.5?±?0.5 g m^?2 d^?1, with a 24 % decrease of biomass productivity. For T. obliquus, a biomass productivity of 9.1?±?0.9 g m^?2 d^?1 in indoor HT-PBR was obtained using standard medium. Applying liquid digestates as fertilizers in open ponds, T. obliquus gave a biomass productivity (10.8?±?2.0 g m^?2 d^?1) not statistically different from complete medium such as P. tricornutum (6.5?±?2.2 g m^?2 d^?1). The biochemical data showed that the fatty acid composition of the microalgal biomass was affected by the different cultivation conditions for both microalgae. In conclusion, it was found that the microalgal productivity in standard medium was about doubled in HT-PBR compared to open ponds for P. tricornutum and was about 20 % higher for T. obliquus.     

A Thermostable phytase from <Emphasis Type="Italic">Neosartorya spinosa</Emphasis> BCC 41923 and its expression in <Emphasis Type="Italic">Pichia pastoris</Emphasis>

A phytase gene was cloned from Neosartorya spinosa BCC 41923. The gene was 1,455 bp in size, and the mature protein contained a polypeptide of 439 amino acids. The deduced amino acid sequence contains the consensus motif (RHGXRXP) which is conserved among phytases and acid phosphatases. Five possible disulfide bonds and seven potential N-glycosylation sites have been predicted. The gene was expressed in Pichia pastoris KM71 as an extracellular enzyme. The purified enzyme had specific activity of 30.95 U/mg at 37°C and 38.62 U/mg at 42°C. Molecular weight of the deglycosylated recombinant phytase, determined by SDS-PAGE, was approximately 52 kDa. The optimum pH and temperature for activity were pH 5.5 and 50°C. The residual phytase activity remained over 80% of initial activity after the enzyme was stored in pH 3.0 to 7.0 for 1 h, and at 60% of initial activity after heating at 90°C for 20 min. The enzyme exhibited broad substrate specificity, with phytic acid as the most preferred substrate. Its K _m and V _max for sodium phytate were 1.39 mM and 434.78 U/mg, respectively. The enzyme was highly resistant to most metal ions tested, including Fe²⁺, Fe³⁺, and Al³⁺. When incubated with pepsin at a pepsin/phytase ratio of 0.02 (U/U) at 37°C for 2 h, 92% of its initial activity was retained. However, the enzyme was very sensitive to trypsin, as 5% of its initial activity was recovered after treating with trypsin at a trypsin/phytase ratio of 0.01 (U/U).     

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).