Pilot scale culture of the marine cyanobacterium Lyngbya majuscula for its pharmaceutically-useful natural metabolite curacin A

A Caribbean collection of Lyngbya majuscula which produces the promising antimitotic agent, curacin A, was recollected in 1993 from Curaçao and adapted to laboratory culture. A variety of culture vessel configurations and conditions were examined for their effect on growth and production of curacin A. Using these partially optimized conditions, 29 strains of curacin A producing L. majuscula were evaluated for their production levels of curacin A employing an internal standard GC-MS analytical method. Five strains were more carefully characterized for their growth and curacin A production, and led to our selection of one reliable strain, ’19L‘, for further studies. Growth and curacin A production curves were established for this strain over a 30 day growth period. This directed a scale-up culture of 640 liters of L. majuscula strain 19L in four batches of 160 L each. All four batches grew well and produced significant quantities of curacin A. In tota1, 215.5 g wet weight of L. majuscula tissue were produced which gave an isolated yield of 132.5 mg of curacin A.     

Feeding preference and deterrence in rabbitfish Siganus fuscescens for the cyanobacterium Lyngbya majuscula in Moreton Bay, south‐east Queensland, Australia

Rabbitfish Siganus fuscescens preferences for Lyngbya majuscula collected from three bloom locations in Moreton Bay, Queensland, Australia, were tested along with a range of local plant species in the laboratory. Consumption of L. majuscula by fish did not differ between wild and captive‐bred fish ( P  = 0·152) but did differ between bloom location ( P  = 0·039). No relationship was found between consumption rates and lyngbyatoxin‐a concentration ( r ² = 0·035, P  = 0·814). No correlation existed between C : N and proportion of food consumed when all food types were analysed statistically, whereas a clear correlation was observed when L. majuscula was removed from the calculations. In simulated bloom conditions, fish avoided ingestion of L. majuscula by feeding through gaps in the L. majuscula coverage. Both wild and captive‐bred S. fuscescens showed a distinct feeding pattern in 10 day no‐choice feeding assays, with less L. majuscula being consumed than the preferred red alga Acanthophora spicifera . Lyngbya majuscula however, was consumed in equal quantities to A. spicifera by wild S. fuscescens when lyngbyatoxin‐a was not detectable. Wild fish probably do not preferentially feed on L. majuscula when secondary metabolites are present and are not severely impacted by large L. majuscula blooms in Moreton Bay. Furthermore, poor feeding performance in both captive‐bred and wild S. fuscescens suggests that they would exert little pressure as a top‐down control agent of toxic L. majuscula blooms within Moreton Bay.     

Morphological, chemical, and genetic diversity of tropical marine cyanobacteria Lyngbya spp. and Symploca spp. (Oscillatoriales)

Although diverse natural products have been isolated from the benthic, filamentous cyanobacterium Lyngbya majuscula, it is unclear whether this chemical variation can be used to establish taxonomic relationships among disparate collections. We compared morphological characteristics, secondary-metabolite compositions, and partial 16S ribosomal DNA (rDNA) sequences among several collections of L. majuscula Gomont, Lyngbya spp., and Symploca spp. from Guam and the Republic of Palau. The morphological characteristics examined were cell length, cell width, and the presence or absence of a calyptra. Secondary metabolites were analyzed by two-dimensional thin-layer chromatography. Each collection possessed a distinct cellular morphology that readily distinguished Lyngbya spp. from Symploca spp. Each collection yielded a unique chemotype, but common chemical characteristics were shared among four collections of L. majuscula. A phylogeny based on secondary-metabolite composition supported the reciprocal monophyly of Lyngbya and Symploca but yielded a basal polytomy for Lyngbya. Pairwise sequence divergence among species ranged from 10 to 14% across 605 bp of 16S rDNA, while collections of L. majuscula showed 0 to 1.3% divergence. Although the phylogeny of 16S rDNA sequences strongly supported the reciprocal monophyly of Lyngbya and Symploca as well as the monophyly of Lyngbya bouillonii and L. majuscula, genetic divergence was not correlated with chemical and morphological differences. These data suggest that 16S rDNA sequence analyses do not predict chemical variability among Lyngbya species. Other mechanisms, including higher rates of evolution for biosynthetic genes, horizontal gene transfer, and interactions between different genotypes and environmental conditions, may play important roles in generating qualitative and quantitative chemical variation within and among Lyngbya species.     

Effect of aposymbiotic conditions on colony growth and secondary metabolite production in the lichen-forming fungus Ramalina dilacerata

The production of secondary metabolites by aposymbiotic lichen-forming fungi in culture is thought to be influenced by environmental conditions. The effects of the environment may be studied by culturing fungi under defined growing parameters to provide a better understanding of the role of the large number of polyketide synthase (PKS) gene paralogs detected in the genomes of many fungi. The objectives of this study were to examine the effects of culture conditions (media composition and pH level) on the colony growth, the numbers of secondary products, and the expression of two PKS genes by the lichen-forming fungus Ramalina dilacerata. Four types of growth media at four different pH levels were prepared to culture spore isolates of R. dilacerata. Colony diameter and texture were recorded. The number of secondary compounds were determined by thin layer chromatography (TLC) and high performance liquid chromatography (HPLC). Expression of two PKS genes (non-reducing (NR) and 6-MSAS-type PKS) were compared with expression of an internal control mitochondrial small subunit gene (mtSSU). The results showed that media containing yeast extracts produced the largest colony diameters and the fewest number of secondary metabolites. Colony growth rates also varied with different media conditions, and a significant negative relationship occurred between colony diameter and number of secondary metabolites. Expression of the NR PKS gene was significantly higher at pH 6.5 on the glucose malt agar than any other media, and expression of the 6-MSAS-type (partially-reducing) PKS gene was significantly higher at pH 8.5 on (malt agar) malt agar than on the other types of agar. Gene expression was correlated with the pH level and media conditions that induced the production of the larger number of secondary substances. This is the first study to examine secondary metabolite production in R. dilacerata by comparing the number of polyketides detected with quantitative polymerase chain reaction (qPCR) of two PKS genes under different culture conditions.     

Image analysis and in vivo imaging as tools for investigation of productivity dynamics in anthocyanin-producing cell cultures of Daucus carota

An anthocyanin-producing suspension culture of Daucus carota (L.) cv. Flakkese was used as model system to study secondary metabolite production in cell culture at the individual cell level. An approach was set up in which growth and production of anthocyanins were investigated using a combination of biochemical analysis, image (colour) analysis and in vivo imaging. This novel approach was used to segment the culture in different subpopulations and dissect the productive process in the cell culture grown under two different conditions, known to differ mainly for oxygen supply and mixing intensity (volume of 50 ml or 20 ml in 250 ml flasks). The 20 ml batch cultures gave a higher content and yield of anthocyanins, which depended on a complex balance between events that positively or negatively affected anthocyanin production. A model is proposed in which the different ability of cells to respond to environmental stimuli and stress depends on the different amount of anthocyanins accumulated within cells.     

Culture conditions promoting dispersed growth and biphasic production of actinorhodin in shaken cultures of Streptomyces coelicolor A3(2)

Media and culture conditions were developed for experiments on the physiology of secondary metabolism in Streptomyces coelicolor A3(2). Well dispersed mycelial growth was obtained in a buffered starch-glutamate-salts medium; a high (5%) starch concentration and addition of glass beads aided dispersal. Under the conditions developed, production of actinorhodin was suppressed during trophophase growth and began abruptly near the growth maximum.     

Galanthamine production by Leucojum aestivum L. shoot culture in a modified bubble column bioreactor with internal sections

Shoot culture of summer snowflake (Leucojum aestivum L.) was successfully cultivated in an advanced modified glass‐column bioreactor with internal sections for production of Amaryllidaceae alkaloids. The highest amounts of dry biomass (20.8 g/L) and galanthamine (1.7 mg/L) were achieved when shoots were cultured at 22°C and 18 L/(L·h) flow rate of inlet air. At these conditions, the L. aestivum shoot culture possessed mixotrophic‐type nutrition, synthesizing the highest amounts of chlorophyll (0.24 mg/g DW (dry weight) chlorophyll A and 0.13 mg/g DW chlorophyll B). The alkaloids extract of shoot biomass showed high acetylcholinesterase inhibitory activity (IC₅₀ = 4.6 mg). The gas chromatography–mass spectrometry (GC/MS) profiling of biosynthesized alkaloids revealed that galanthamine and related compounds were presented in higher extracellular proportions while lycorine and hemanthamine‐type compounds had higher intracellular proportions. The developed modified bubble‐column bioreactor with internal sections provided conditions ensuring the growth and galanthamine production by L. aestivum shoot culture.     

Visualizing the spatial distribution of secondary metabolites produced by marine cyanobacteria and sponges via MALDI-TOF imaging

Marine cyanobacteria and sponges are prolific sources of natural products with therapeutic applications. In this paper we introduce a mass spectrometry based approach to characterize the spatial distribution of these natural products from intact organisms of differing complexities. The natural product MALDI-TOF-imaging (npMALDI-I) approach readily identified a number of metabolites from the cyanobacteria Lyngbya majuscula 3L and JHB, Oscillatoria nigro-viridis, Lyngbya bouillonii, and a Phormidium species, even when they were present as mixtures. For example, jamaicamide B, a well established natural product from the cyanobacterium Lyngbya majuscula JHB, was readily detected as were the ions that correspond to the natural products curacin A and curazole from Lyngbya majuscula 3L. In addition to these known natural products, a large number of unknown ions co-localized with the different cyanobacteria, providing an indication that this method can be used for dereplication and drug discovery strategies. Finally, npMALDI-I was used to observe the secondary metabolites found within the sponge Dysidea herbacea. From these sponge data, more than 40 ions were shown to be co-localized, many of which were halogenated. The npMALDI-I data on the sponge indicates that, based on the differential distribution of secondary metabolites, sponges have differential chemical micro-environments within their tissues. Our data demonstrate that npMALDI-I can be used to provide spatial distribution of natural products, from single strands of cyanobacteria to the very complex marine assemblage of a sponge.     

Highly efficient strategy for enhancing taxoid production by repeated elicitation with a newly synthesized jasmonate in fed-batch cultivation of Taxus chinensis cells

A highly efficient bioprocessing strategy was developed for enhancing the production of plant secondary metabolites by repeatedly eliciting a fed-batch culture with a newly synthesized powerful jasmonate analog, 2,3-dihydroxypropyl jasmonate (DHPJA). In suspension cultures of a high taxuyunnanine C (Tc)-producing cell line of Taxus chinensis, 100 microM DHPJA was added on day 7 to fed-batch cultures with feeding of 20 g L(-1) sucrose on the same day. The synergistic effect of elicitation and substrate feeding on Tc biosynthesis was observed, which resulted in higher Tc accumulation than that by elicitation or sucrose feeding alone. More interestingly, both specific Tc yield (i.e., Tc content) and volumetric yield was further improved by a second addition of 100 microM DHPJA (on day 12) to the fed-batch cultures. In particular, with repeated elicitation and sucrose feeding the Tc volumetric yield was increased to 827 +/- 29 mg L(-1), which was 5.4-fold higher than that of the nonelicited batch culture. Furthermore, the above novel strategy was successfully applied from shake flask to a 1-L airlift bioreactor. A high Tc production and productivity of 738 +/- 41 mg L(-1) and 33.2 +/- 1.9 mg L(-1) d(-1), respectively, was achieved, which is higher than previous reports on Tc production in bioreactors. The results suggest that the aforementioned bioprocessing strategy may potentially be applied to other cell culture systems for efficient production of plant secondary metabolites.     

Development of production and purification processes of recombinant fragment of pneumococcal surface protein A in <Emphasis Type="Italic">Escherichia coli</Emphasis> using different carbon sources and chromatography sequences

Pneumococcal surface protein A (PspA) is essential for Streptococcus pneumoniae virulence and its use either as a novel pneumococcal vaccine or as carrier in a conjugate vaccine would improve the protection and the coverage of the vaccine. Within this context, the development of scalable production and purification processes of His-tagged recombinant fragment of PspA from clade 3 (rfPspA3) in Escherichia coli BL21(DE3) was proposed. Fed-batch production was performed using chemically defined medium with glucose or glycerol as carbon source. Although the use of glycerol led to lower acetate production, the concentration of cells were similar at the end of both fed-batches, reaching high cell density of E. coli (62 g dry cell weight/L), and the rfPspA3 production was higher with glucose (3.48 g/L) than with glycerol (2.97 g/L). A study of downstream process was also carried out, including cell disruption and clarification steps. Normally, the first chromatography step for purification of His-tagged proteins is metal affinity. However, the purification design using anion exchange followed by metal affinity gave better results for rfPspA3 than the opposite sequence. Performing this new design of chromatography steps, rfPspA3 was obtained with 95.5% and 75.9% purity, respectively, from glucose and glycerol culture. Finally, after cation exchange chromatography, rfPspA3 purity reached 96.5% and 90.6%, respectively, from glucose and glycerol culture, and the protein was shown to have the expected alpha-helix secondary structure.     

High-level expression of recombinant human soluble thrombomodulin in serum-free medium by CHO-K1 cells

Cultivation of gene-engineered Chinese hamster ovary (CHO-K1) cells that produce recombinant human soluble thrombomodulin (rsTM) was investigated to optimize conditions for high-level expression of the protein in a serum-free medium. For economic protein production, oxygenation of cultures with pure O₂ permitted sufficient cell growth for high rsTM production with only 1 g/l of microcarriers and a low foetal bovine serum concentration. A longer growth phase (over 5 days) with serum was important to establish sufficient growth of this cell line on the microcarriers for subsequent serum-free culture, and to support a long-term production phase (about 2 months). In the production phase, a high glucose concentration (6.15 g/l) in the serum-free medium was very effective for prolonging the harvest cycle interval. Under these conditions, up to 100 mg/l rsTM was expressed in the conditioned medium. The rates of glucose consumption (G) and lactae production (L) were measured periodically and their ratio (L/G ratio) correlated with rsTM productivity. When the average L/G ratio was lower, reflecting a lower lactate production rate due to appropriate oxygenation of the culture, the specific rsTM production rate increased. Thus it may be possible to estimate protein productivity from L/G ratios calculated from the glucose and lactate measurements. Correspondence to: M. Ogata     

Perfusion strategy for rosmarinic acid production by Anchusa officinalis

The production of an intracellular secondary metabolite rosmarinic acid (RA) by plant cell suspensions of Anchusa officinalis cultivated with intermittent medium exchange is investigated. Initially, a two-stage perfusion culture method was employed. After being cultured in the batch mode for ca. 6 days in B5 medium plus 3% sucrose, 1 mg/L 2,4-dichlorophenoxyacetic acid (2,4-D), and 0.1 mg/L kinetin (2,4-D B5 medium), Anchusa culture was cultivated to high cell density by perfusion during the growth stage using a hormone-free Gamborg B5 medium supplemented with 6% sucrose. This was followed by a production stage, in which a complete medium exchange into B5 medium plus 3% sucrose and 0.25 mg/L naphthleneacetic acid (NAA) was conducted. The two-stage perfusion culture had a higher maximum culture RA concentration but a lower RA content per cell than the batch stock culture maintained in the 2,4-D B5 medium. Higher culture RA concentration was due primarily to high cell density. The high packed cell volume, however, seemed to reduce the synergistic effect of NAA on RA synthesis. Subsequently, a single-stage perfusion culture method was investigated. The best result was obtained by growing the culture in the batch mode for ca. 10 days using B5 medium supplemented with 3% sucrose and 0.25 mg/L NAA, followed by perfusing the culture with B5 medium plus 6% sucrose and 0.25 mg/L NAA at a constant perfusion rate of 0.1/day. A maximum cell dry weight of 35 g/L and a RA concentration of almost 4 g/L were achieved. This is the highest RA concentration ever reported in the Anchusa culture. (c) 1993 John Wiley & Sons, Inc.     

Application of a gratuitous induction system in Kluyveromyces lactis for the expression of intracellular and secreted proteins during fed-batch culture

A gratuitous induction system in the yeast Kluyveromyces lactis was evaluated for the expression of intracellular and extracellular products during fed-batch culture. The Escherichia coli lacZ gene (beta-galactosidase; intracellular) and MFalpha1 leader-BPTI cassette (bovine pancreatic trypsin inhibitor; extracellular) were placed under the control of the inducible K. lactis LAC4 promotor, inserted into partial-pKD1 plasmids, and transformed into a ga1-209 K. lactis strain. To obtain a high level of production, culture conditions for growth and expression were initially evaluated in tube cultures. A selective medium containing 5 g/L glucose (as carbon source) and 0.5 g/L galactose (as inducer) demonstrated the maximum activity of both beta-galactosidase and secreted BPTI. This level of expression had no significant effect on the growth of the recombinant cells; growth rate dropped by approximately 11%, whereas final biomass concentrations remained the same. In shake-flask culture, biomass concentration, beta-galactosidase activity, and BPTI secreted activity were 4 g/L, 7664 U/g dry cell, and 0.32 mg/L, respectively. Fed-batch culture (with a high glucose concentration and a low galactose [inducer] concentration feed) resulted in a 6.5-fold increase in biomass, a 23-fold increase in beta-galactosidase activity, and a 3-fold increase in BPTI secreted activity. The results demonstrate the success of gratuitous induction during high-cell-density fed-batch culture of K. lactis. A very low concentration of galactose feed was sufficient for a high production level.     

Improved paclitaxel and baccatin III production in suspension cultures of Taxus media

A cell suspension culture of Taxus media was established from a stable callus line of this species. The growth rate and production of paclitaxel and baccatin III of this cell suspension were significantly increased during the shake flask culture in its respective optimum media for cell growth and product formation, which were selected after assaying 24 different culture media. The highest yields of paclitaxel (2.09 mg L(-1)) and baccatin III (2.56 mg L(-1)) in the production medium rose (factors of 7.0 and 3.0, respectively) in the presence of methyljasmonate (220 microg g(-1) FW). When the elicitor was added together with mevalonate (0.38 mM) and N-benzoylglycine (0.2 mM), the increase in the yields of paclitaxel and baccatin III was even higher (factors of 8.3 and 4.0, respectively). Thereafter, a two-stage culture for cell suspension was carried out using a 5-l stirred bioreactor running for 36 days, the first stage being in the cell growth medium until cells entered their stationary growth phase (12 days) and the second stage being in the production medium supplemented with the elicitor and two putative precursors in the concentrations indicated above. Under these conditions, 21.12 mg L(-1) of paclitaxel and 56.03 mg L(-1) of baccatin III were obtained after 8 days of culture in the production medium.     

Bacterial removal of mercury from sewage

Mercury-resistant bacteria, which are able to reduce mercuric ion (Hg(2+)) to metallic mercury (Hg(0)), were examined for their ability to remove mercury from waste-water aerobically. Growth studies in artificial medium indicated that mercury increases the lag phase, but does not effect the growth rate of these bacteria. Further studies demonstrated that growth was minimal during a phase of rapid mercury removal, after which growth resumed. Small but significant amounts of carbohydrates are required for the mercuric ion reduction. Prolonged periods of bacterial growth under nonsterile conditions was accomplished without the loss of the mercuric reducing ability of the culture. A continuous culture of the resistant organism was maintained on raw sewage for two weeks, during which time relatively high concentrations of mercury (70 mg/L) were removed from the sewage at a rate of 2.5 mg/L h and at efficiencies exceeding 98%.     

Pullulan production from synthetic medium by a new mutant of Aureobasidium pullulans

Pullulan with different molecular-weight could be applied in various fields. A UV-induced mutagenesis Aureobasidium pullulans UVMU6-1 was obtained from the strain A. pullulans CGMCC3.933 for the production of low-molecular-weight pullulan. First, the obtained polysaccharide from A. pullulans UVMU6-1 was purified and identified to be pullulan with thin-layer chromatography, Fourier transform infrared, and nuclear magnetic resonance. Then, culture medium and conditions for this strain were optimized by flask fermentation. Based on the optimized medium and culture conditions (pH 4, addition of 4?g/L Tween 80 for 96?hr of cultivation), continuously fermentation was performed. The highest pullulan production and dry biomass was 109 and 125?g/L after fermentation for 114?hr, respectively. The average productivity was about 1?g/L/hr, which was intensively higher than the previous reported. This study would lay foundations for the industrial production of pullulan.     

Formation of germichrysone by tissue cultures of Cassia torosa: Induction of secondary metabolism in the lag phase

A callus culture of Cassia torosa which produced germichrysone, an octaketide hydroanthracene, in high yield was established on Murashige-Skoog's medium containing IAA (3 ppm) and benzyladenine (0.1 ppm). In six-week-old callus culture the main pigment was pinselin and the germichrysone content was markedly decreased. This may indicate that pinselin was formed from germichrysone. A shake culture was established in liquid Murashige-Skoogs medium containing IAA and benzyladenine. The course of germichrysone production in relation to growth was investigated with the shake culture and the production of germichrysone was found to possess two maxima. The first maximum was observed in lag phase and the second coincided with active growth. Incorporation experiments with [1-¹⁴C] acetate clearly demonstrated that the secondary metabolism was induced in the lag phase.     

Modeling of Xanthophyllomyces dendrorhous growth on glucose and overflow metabolism in batch and fed-batch cultures for astaxanthin production

An astaxanthin-producing yeast Xanthophyllomyces dendrorhous ENM5 was cultivated in a liquid medium containing 50 g/L glucose as the major carbon source in stirred fermentors (1.5-L working volume) in fully aerobic conditions. Ethanol was produced during the exponential growth phase as a result of overflow metabolism or fermentative catabolism of glucose by yeast cells. After accumulating to a peak of 3.5 g/L, the ethanol was consumed by yeast cells as a carbon source when glucose in the culture was nearly exhausted. High initial glucose concentrations and ethanol accumulation in the culture had inhibitory effects on cell growth. Astaxanthin production was partially associated with cell growth. Based on these culture characteristics, we constructed a modified Monod kinetic model incorporating substrate (glucose) and product (ethanol) inhibition to describe the relationship of cell growth rate with glucose and ethanol concentrations. This kinetic model, coupled with the Luedeking-Piret equation for the astaxanthin production, gave satisfactory prediction of the biomass production, glucose consumption, ethanol formation and consumption, and astaxanthin production in batch cultures over 25-75 g/L glucose concentration ranges. The model was also applied to fed-batch cultures to predict the optimum feeding scheme (feeding glucose and corn steep liquor) for astaxanthin production, leading to a high volumetric yield (28.6 mg/L) and a high productivity (5.36 mg/L/day).     

Adventitious root culture of <Emphasis Type="Italic">Polygonum multiflorum</Emphasis> for phenolic compounds and its pilot-scale production in 500 L-tank

Polygonum multiflorum Thunb. is an important medicinal plant that synthesizes an array of phenolic compounds. Its roots are used in a variety of pharmacological and cosmetic formulations, notably as hair dye. In the present study, the inoculum density (3–15 g/L) and culture period (1–7 weeks) were optimized in a 3 L bioreactor. High root biomass (14.18 g/L dry weight (DW)) was recorded with an inoculum of 7 g/L (p?≤?0.05), which is consistent with the results for 5 and 10 g/L. However, significantly higher yield of bioactive compounds (53.87 mg/g DW total phenolics and 27.96 mg/g DW total flavonoids) with high free radical scavenging activity was obtained in root samples from 5 g/L inoculum density. A 4 week culture period was sufficient for optimum root growth and metabolite production. The optimized conditions were used for large-scale (5 and 20 L) and pilot-scale (500 L) studies. Considering that the continuous aeration of root cultures may lead to oxidative stress, antioxidant enzyme activity and lipid peroxidation also were studied. The results revealed high catalase (CAT) and guaiacol peroxidase (G-POD) activities, and low malondialdehyde (MDA) production, with increasing culture scale (20 and 500 L), which may indicate low-level oxidative damage to the cultures. An optimal yield of 4.01 kg dry root biomass with 287.12 mg/L of total phenolic productivity was achieved in a 500 L pilot-scale bioreactor. This work can pave the way for commercial production of biomass and secondary metabolites at the industrial level, and meet the rising demand for natural ingredients, especially in the pharmaceutical and cosmetic industries.     

Improvement of heterologous protein productivity using recombinant Yarrowia lipolytica and cyclic fed-batch process strategy

A cyclic fed-batch bioprocess is designed and a significant improvement of rice alpha-amylase productivity of recombinant Yarrowia lipolytica is illustrated. A bioprocess control strategy developed and reported here entails use of a genetically stable recombinant cloned for heterologous protein, use of optimized media for cell growth and enzyme production phases, and process control strategy enabling high cell-density culture and high alpha-amylase productivity. This process control can be achieved through maintaining a constant optimal specific cell growth rate at a predetermined value (i.e., 0.1 h-1), controlling medium feed rate commensurate with the cell growth rate, and maintaining a high cell-density culture (i.e., 60-70 g/L) for high productivity of cloned heterologous protein. The volumetric enzyme productivity (1, 960 units/L. h) achieved from the cyclic fed-batch process was about 3-fold higher than that of the fed-batch culture process (630 units/L. h).