Identification of a novel growth-associated promoter for biphasic expression of heterogenous proteins in Pichia pastoris.

Pichia pastoris (P. pastoris) is one of the most popular cell factories for expressing exogenous proteins and producing useful chemicals. The alcohol oxidase 1 promoter (PAOX1) is the most commonly used strong promoter in P. pastoris and has the characteristic of biphasic expression. However, the inducer for PAOX1, methanol, has toxicity and poses risks in industrial settings. In the present study, analyzing transcriptomic data of cells collected at different stages of growth found that the formate dehydrogenase (FDH) gene ranked 4960th in relative expression among 5032 genes during the early logarithmic growth phase but rose to the 10th and 1st during the middle and late logarithmic growth phases, respectively, displaying a strict biphasic expression characteristic. The unique transcriptional regulatory profile of the FDH gene prompted us to investigate the properties of its promoter (PFDH800). Under single-copy conditions, when a green fluorescent protein variant was used as the expression target, the PFDH800 achieved 119% and 69% of the activity of the glyceraldehyde-3-phosphate dehydrogenase promoter and PAOX1, respectively. After increasing the copy number of the expression cassette in the strain to approximately four copies, the expression level of GFPuv driven by PFDH800 increased to approximately 2.5 times that of the strain containing GFPuv driven by a single copy of PAOX1. Our PFDH800-based expression system exhibited precise biphasic expression, ease of construction, minimal impact on normal cellular metabolism, and high strength. Therefore, it has the potential to serve as a new expression system to replace the PAOX1 promoter.IMPORTANCEThe alcohol oxidase 1 promoter (PAOX1) expression system has the characteristics of biphasic expression and high expression levels, making it the most widely used promoter in the yeast Pichia pastoris. However, PAOX1 requires methanol induction, which can be toxic and poses a fire hazard in large quantities. Our research has found that the activity of PFDH800 is closely related to the growth state of cells and can achieve biphasic expression without the need for an inducer. Compared to other reported non-methanol-induced biphasic expression systems, the system based on the PFDH800 offers several advantages, including high expression levels, simple construction, minimal impact on cellular metabolism, no need for an inducer, and the ability to fine-tune expression.

Breeding of Saccharomyces cerevisiae with a High-Throughput Screening Strategy for Improvement of S-Adenosyl-L-Methionine Production.

S-adenosyl-l-methionine (SAM), a vital physiologically active substance in living organisms, is produced by fermentation over Saccharomyces cerevisiae. The main limitation in SAM production was the low biosynthesis ability of SAM in S. cerevisiae. The aim of this work is to breed an SAM-overproducing mutant through UV mutagenesis coupled with high-throughput selection. Firstly, a high-throughput screening method by rapid identification of positive colonies was conducted. White colonies on YND medium were selected as positive strains. Then, nystatin/sinefungin was chosen as a resistant agent in directed mutagenesis. After several cycles of mutagenesis, a stable mutant 616-19-5 was successfully obtained and exhibited higher SAM production (0.41 g/L vs 1.39 g/L). Furthermore, the transcript levels of the genes SAM2, ADO1, and CHO2 involved in SAM biosynthesis increased, while ergosterol biosynthesis genes in mutant 616-19-5 significantly decreased. Finally, building on the above work, S. cerevisiae 616-19-5 could produce 10.92 ± 0.2 g/L SAM in a 5-L fermenter after 96 h of fermentation, showing a 2.02-fold increase in the product yield compared with the parent strain. Paving the way of breeding SAM-overproducing strain has improved the good basis for SAM industrial production.

Improving ATP availability by sod1 deletion with a strategy of precursor feeding enhanced S-adenosyl-L-methionine accumulation in Saccharomyces cerevisiae.

S-adenosyl-L-methionine (SAM), used in diverse pharmaceutical applications, was biosynthesized from L-methionine (L-met) and adenosine triphosphate (ATP). This study aims to increase the accumulation of SAM in Saccharomyces cerevisiae by promoting ATP availability. Strain ΔSOD1 was obtained from the parent strain WT15-33 (CCTCC M 2021915) by deleting gene sod1, which improved the supply of ATP. The SAM content in strain ΔSOD1 exhibited a 22.3% improvement compared to the parent strain, which reached 93.6 mg g-1. The transformation of NADH (reduced nicotinamide adenine dinucleotide) and the relative expression of ATPase essential genes were investigated, respectively. The results showed that the lack of gene sod1 benefited the generation of ATP, which positively regulated the synthesis of SAM. Besides that, the production of SAM was further enhanced by improving substrate assimilation. With the infusion of 1.44 g L-1L-met and 0.60 g L-1 adenosine at 24 h (h) and 0 h following fermentation, the optimum medium could produce 1.54 g L-1 SAM. Based on the regulations mentioned above, the SAM concentration of strain ΔSOD1 enhanced from 7.3 g L-1 to 10.1 g L-1 in a 5-L fermenter in 118 h. This work introduces a novel idea for the biosynthesis of ATP and SAM, and the strain ΔSOD1 has the potential for industrial production.

Research progress of L-aspartate-α-decarboxylase and its isoenzyme in the ß-alanine synthesis.

Driven by the massive demand in recent years, the production of ß-alanine has significantly progressed in chemical and biological ways. Although the chemical method is relatively mature compared to biological synthesis, its high cost of waste disposal and environmental pollution does not meet the environmental protection standard. Hence, the biological method has become more prevalent as a potential alternative to the chemical synthesis of ß-alanine in recent years. As a result, the aspartate pathway from L-aspartate to ß-alanine (the most significant rate-limiting step in the ß-alanine synthesis) catalyzed by L-aspartate-α-decarboxylase (ADC) has become a research hotspot in recent years. Therefore, it is vital to comprehensively understand the different enzymes that possess a similar catalytic ability to ADC. This review will investigate the exploratory process of unique synthesis features and catalytic properties of ADC/ADC-like enzymes in particular creatures with similar catalytic capacity or high sequence homology. At the same time, we will discuss the different ß-alanine production methods which can apply to future industrialization.

Improvement of pyrroloquinoline quinone-dependent d-sorbitol dehydrogenase activity from Gluconobacter oxydans via expression of Vitreoscilla hemoglobin and regulation of dissolved oxygen tension for the biosynthesis of 6-(N-hydroxyethyl)-amino-6-deoxy-α-l-sorbofuranose.

The miglitol intermediate, 6-(N-hydroxyethyl)-amino-6-deoxy-α-l-sorbofuranose (6NSL), is catalyzed from N-2-hydroxyethyl glucamine (NHEG) by resting cells of Gluconobacter oxydans. One of the key factors limiting 6NSL production was the availability of oxygen during both cell cultivation and biotransformation of NHEG to 6NSL. Based on G. oxydans/pBBR1-sldAB-pqqABCDE-tldD (G. oxydans/AB-PQQ), the Vitreoscilla hemoglobin (VHb) was heterologously expressed in G. oxydans to enhance oxygen transfer efficiency and improve 6NSL production. The recombinant G. oxydans/AB-PQQ-VHb displayed higher biomass and NHEG oxidation activity than the control stain. The transcription levels of respiratory chain-related enzyme genes in G. oxydans/AB-PQQ-VHb exhibited up-regulation, indicating that the presence of VHb promoted the respiration. The dissolved oxygen (DO) concentration for cell cultivation was optimized in a 5-L stirred bioreactor. At a DO concentration of 20%, the maximum volumetric oxidation activity of NHEG of G. oxydans/AB-PQQ-VHb in the stirred bioreactor reached 168.3 ± 3.2 U/L. Furthermore, the biotransformation of NHEG to 6NSL using G. oxydans/AB-PQQ-VHb was carried out under different oxygen tensions to investigate the effect of oxygen on 6NSL production. Finally, up to 87.5 ± 5.9 g/L 6NSL was accumulated in the reaction mixture within 16 h when the DO was controlled at 30%.

Combinational expression of D-sorbitol dehydrogenase and pyrroloquinoline quinone increases 6-(N-hydroxyethyl)-amino-6-deoxy-α-L-sorbofuranose production by Gluconobacter oxydans through cofactor manipulation.

6-(N-hydroxyethyl)-amino-6-deoxy-l-sorbofuranose (6NSL), a key precursor in the synthesis of miglitol, is produced from N-2-hydroxyethyl-glucamine (NHEG) by the regioselective oxidation of Gluconobacter oxydans. The limitation of PQQ biosynthesis became a bottleneck for improvement of PQQ-dependent D-sorbitol dehydrogenase (mSLDH) activity. Five expression plasmids were constructed for the co-expression of the pqqABCDE gene cluster and the tldD gene on the basis of pBBR1-gHp0169-sldAB in G. oxydans to increase the biosynthesis of PQQ. The G. oxydans/pGA004, in which pqqABCDE and tldD were expressed as a cluster under the control of gHp0169 promoter, showed the optimal performance. The intracellular PQQ concentration and specific activity of mSLDH in cells increased by 79.3 % and 53.7 %, respectively, compared to that in G. oxydans/pBBR-sldAB. Then, the repeated batch biotransformation of NHEG to 6NSL by G. oxydans/pGA004 was carried out. Up to 75.0 ±â€¯3.0 g/L of 6NSL production with 94.5 ±â€¯3.6 % of average conversion rate of NHEG to 6NSL was achieved after four cycles of run. These results indicated that G. oxydans/pGA004 with high productivity had great potential for 6NSL production in industrial bioprocess.

Effects of methyl oleate and microparticle-enhanced cultivation on echinocandin B fermentation titer.

Echinocandin B (ECB) is a key precursor of antifungal agent Anidulafungin, which has demonstrated clinical efficacy in patients with invasive candidiasis. In this study, the effects of microparticle-enhanced cultivation and methyl oleate on echinocandin B fermentation titer were investigated. The results showed that the titer was significantly influenced by the morphological type of mycelium, and mycelium pellet was beneficial to improve the titer of this secondary metabolism. First, different carbon sources were chosen for the fermentation, and methyl oleate achieved the highest echinocandin B titer of 2133 ± 50 mg/L, which was two times higher than that of the mannitol. The study further investigated the metabolic process of the fermentation, and the results showed that L-threonine concentration inside the cell could reach 275 mg/L at 168 h with methyl oleate, about 2.5 times higher than that of the mannitol. Therefore, L-threonine may be a key precursor of echinocandin B. In the end, a new method of adding microparticles for improving the mycelial morphology was used, and the addition of talcum powder (20 g/L, diameter of 45 µm) could make the maximum titer of echinocandin B reach 3148 ± 100 mg/L.

Repeated production of 6-(N-hydroxyethyl)-amino-6-deoxy-α-L-sorbofuranose by immobilized Gluconobacter oxydans cells with a strategy of in situ exhaustive cell regeneration.

The major troubles in 6-(N-hydroxyethyl)-amino-6-deoxy-α-L-sorbofuranose (6NSL) production from N-2-hydroxyethyl glucamine (NHEG) by Gluconobacter oxydans were low cell yield during cell preparation and loss of cells' biocatalytic ability during biotransformation, resulting in high production cost and low 6NSL production. The target of this work was to enhance 6NSL production by reusing cells and improving the cells biocatalytic ability. First, inhibitory effects of substrate and product on 6NSL production, and optimization of cell regeneration condition were investigated, respectively. Then repeated production of 6NSL by immobilized cell using a strategy of in situ exhaustive cell regeneration in a bubble column bioreactor was developed. As a result, the bioprocess underwent nine cycles, the average 6NSL production and conversion rate of NHEG to 6NSL reached 42.6 g L-1 and 83.1% in each batch was achieved, respectively.

Mutagenesis of echinocandin B overproducing Aspergillus nidulans capable of using starch as main carbon source.

Echinocandin B, a kind of antimycotic with cyclic lipo-hexapeptides, was produced by fermentation with Aspergillus nidulans using fructose as main carbon source. The objective of this study was to screen a high-yield mutant capable of using cheap starch as main carbon source by atmospheric and room temperature plasma (ARTP) treatment in order to decrease the production cost of echinocandin B. A stable mutant A. nidulans ZJB19033, which can use starch as optimal carbon source instead of expensive fructose, was selected from two thousands isolates after several cycles of ARTP mutagenesis. To further increase the production of echinocandin B, the optimization of fermentation medium was performed by response surface methodology (RSM), employing Plackett-Burman design (PBD) followed by Box-Behnken design (BBD). The optimized fermentation medium provided the optimal yield of echinocandin B, 2425.9 ± 43.8 mg/L, 1.3-fold compared to unoptimized medium. The results indicated that the mutant could achieve high echinocandin B production using cheap starch as main carbon source, and the cost of carbon sources in fermentation medium reduced dramatically by about 45%.

Synergistic improvement of PQQ-dependent D-sorbitol dehydrogenase activity from Gluconobacter oxydans for the biosynthesis of miglitol precursor 6-(N-hydroxyethyl)-amino-6-deoxy-α-L-sorbofuranose.

6-(N-hydroxyethyl) amino-6-deoxy-l-sorbofuranose (6NSL) is the direct precursor of miglitol for diabetes therapy. The regio- and stereo-selective dehydrogenation offered by the membrane-bound d-sorbitol dehydrogenase (mSLDH) from Gluconobacter oxydans provides an elegant enzymatic method for 6NSL production. In this study, two subunits sldA and sldB of mSLDH were introduced into G. oxydans ZJB-605, and the specific enzyme activity of mSLDH towards NHEG was enhanced by 2.15-fold. However, the endogenous PQQ level was dramatically reduced in the recombinant strain and became a bottleneck to support the holo-enzyme activity. A combined supplementation of four amino acids (Glu, Ile, Ser, Arg) involved in biosynthesis of PQQ in conventional media effectively increased extracellular accumulation of PQQ by 1.49-fold, which further enhanced mSLDH activity by 1.33-fold. The synergic improvement of mSLDH activity provided in this study supports the superior high dehydrogenate activity towards substrate N-2-hydroxyethyl-glucamine, 184.28 g·L-1 of 6NSL was produced after a repeated bioconversion process catalyzed by the resting cells of G. oxydans/pBB-sldAB, all of which presenting a great potential of their industrial application in 6NSL biosynthesis.

Integrated strategy of temperature shift and mannitol feeding for enhanced production of echinocandin B by Aspergillus nidulans CCTCC M2012300.

The production of echinocandin B (ECB) by Aspergillus nidulans CCTCC M2012300 was improved by integrating the temperature-shift and fed-batch control strategies. The kinetic characteristics of batch cultures were analyzed at different culture temperatures, and then a two-stage temperature control strategy was established. In the first 6 days, the temperature was maintained at 30 °C to obtain the maximal cell growth rate; subsequently, 25 °C was used to gain a high ECB formation rate. On the basis of temperature control, the ECB productivity was increased to 143.3 mg/(L day), which was a 1.3-fold improvement compared with the optimal constant-temperature cultivations. The influences of fed-batch cultures were further investigated. A maximal ECB productivity of 170.8 mg/(L day) was obtained through a three-stage mannitol pulse-feeding strategy, which was another 1.2-fold improvement than that of the batch fermentation. This is the first report of the use of a two-stage temperature control fed-batch strategy in ECB fermentation. This strategy was simple and economical to operate and may provide new guidance for the industrial-scale production of ECB.

Enhanced Production of 6-(N-Hydroxyethyl)-Amino-6-Deoxy-α-L-Sorbofuranose by Immobilized Gluconobacter oxydanson Corn Stover with a pH Control Strategy in a Bubble Column Bioreactor.

6-(N-Hydroxyethyl)-amino-6-deoxy-α-L-sorbofuranose (6NSL) is a key intermediate in the synthesis of miglitol. Biotransformation of N-2-hydroxyethyl glucamine (NHEG) to 6NSL was performed by immobilized Gluconobacter oxydans, which was prepared by cultivating the cells in a home-made bubble column bioreactor where corn stover particles were loaded. The optimal carrier addition and aeration rate for 6NSL production by immobilized cells in the bioreactor were determined to be 25 g/L and 2.5 vvm respectively. The supplementation of NH4Cl was conducive to the biotransformation of NHEG and was performed by adding aqueous ammonia and HCl, which was taken as the pH controlling agents as well. An optimal pH control strategy using the mixture of aqueous ammonia and NaOH was applied, resulting in a 9.9% increased production of 6NSL, while repeated batches of biotransformation increased from three times to four times. Finally, the 6NSL concentration and the conversion rate of NHEG to 6NSLreached 44.2 ± 1.5 g/L and 88.4 ± 2.0%, respectively, in average after four cycles of biotransformation under the optimized condition.

Biosynthesis of miglitol intermediate 6-(N-hydroxyethyl)-amino-6-deoxy-α-l-sorbofuranose by an improved d-sorbitol dehydrogenase from Gluconobacter oxydans.

Adaptable exploitation of the catalytic potential of membrane-bound d-sorbitol dehydrogenase (mSLDH) from Gluconobacter oxydans is desperately needed in the industrial-scale production of miglitol. In the present study, a carbonyl group-dependent colorimetric quantification method was developed for the assay of miglitol key intermediate 6-(N-hydroxyethyl)-amino-6-deoxy-α-l-sorbofuranose (6NSL), and a high-throughput screening process of positive mutants was processed. Combined with several rounds of ultraviolet irradiation mutagenesis and screening procedure, a positive mutant strain G. oxydans ZJB16009 was obtained with significant increase in mSLDH catalytic activity by 1.5-fold, which exhibited an extremely accelerated uptake rate of d-sorbitol, and the fermentation time was significantly shortened from 22 to 11 h. In a 5-L biotransformation system, 60 g/L substrate N-2-hydroxyethyl glucamine (NHEG) was catalyzed by the resting cells of the mutant strain within 36 h and accumulated 53.6 g/L 6NSL, showing a 33.6% increase in the product yield. Therefore, it was indicated that the established high-throughput screening method could provide a highly efficient platform for the breading of G. oxydans strain for the industrial biosynthesis of miglitol intermediate 6NSL.

Repeated biotransformation of glycerol to 1,3-dihydroxyacetone by immobilized cells of Gluconobacter oxydans with glycerol- and urea-feeding strategy in a bubble column bioreactor.

Some inorganic nitrogen sources and amino acids instead of yeast extract, which resulted in trouble of product purification, were introduced for 1,3-dihydroxyacetone (DHA) production by biotransformation with Gluconobacter oxydans. The results showed that urea is an optimal nitrogen source. Furthermore, the effects of glycerol- and urea-feeding strategies for DHA production by immobilized cells in a home-made bubble column bioreactor were optimized. Cells immobilization was prepared by cultivation in the bioreactor packed with porous ceramics, and then the broth was removed. Then, repeated biotransformation by continuous-feeding of glycerol and urea was developed. Up to 96.4±4.1g/L of average DHA concentration with 94.8±2.2% of average conversion rate of glycerol to DHA was achieved after 12 cycles of run. Near colorless DHA solution with few impurities was obtained and the production cost could be decreased.

Enhancement of epoxide hydrolase production by 60 Co gamma and UV irradiation mutagenesis of Aspergillus niger ZJB-09103.

An effective epoxide hydrolase (EH) production strain was mutagenized using 60 Co gamma and UV irradiation. Among positive mutant strains, the EH activity of C2-44 reached 33.7 U/g, which was 267% as much as that of the original Aspergillus niger ZJB-09103. Compared with the wild type, there were significant changes in morphology for C2-44, including the color of mycelia on the slants and the shape of conidial head. In addition, glucose and soybean cake were the optimal carbon and nitrogen source in terms of EH activity for the mutant C2-44 instead of soluble starch and peptone for the wild-type strain. The reaction time required to reach 99% enantiomeric excesses of (S)-epichlorohydrin from racemic substrate was shortened significantly by the mutant C2-44. This phenomenon was probably explained by the higher Vmax for hydrolysis of racemic epichlorohydrin by C2-44 compared with Aspergillus niger ZJB-09103.

Enhancement of Echinocandin B Production by a UV- and Microwave-Induced Mutant of Aspergillus nidulans with Precursor- and Biotin-Supplying Strategy.

Echinocandin B belongs to lipopeptide antifungal antibiotic bearing five types of direct precursor amino acids including proline, ornithine, tyrosine, threonine, and leucine. The objective of this study is to screen over-producing mutant in order to improve echinocandin B production; a stable mutant Aspergillus nidulans ZJB12073, which can use fructose as optimal carbon source instead of expensive mannitol, was selected from thousand isolates after several cycles of UV and microwave irradiation in turn. The results showed that mutant strain ZJB12073 exhibited 1.9-fold improvement in echinocandin B production to 1656.3 ± 40.3 mg/L when compared with the parent strain. Furthermore, the effects of precursor amino acids and some chemicals on echinocandin B biosynthesis in A. nidulans were investigated, respectively. Tyrosine, leucine, and biotin were selected as key factors to optimize the medium employing uniform design method. The results showed that the optimized fermentation medium provided another 63.1 % increase to 2701.6 ± 31.7 mg/L in final echinocandin B concentration compared to that of unoptimized medium.

Enhancement of (S)-2,3-dichloro-1-propanol production by recombinant whole-cell biocatalyst in n-heptane-aqueous biphasic system.

The enantioselective resolution of (R,S)-2,3-dichloro-1-propanol ((R,S)-DCP) to (S)-DCP by whole cells of a recombinant Escherichia coli expressing halohydrin dehalogenase (HHDH) activity was limited by product inhibition. To solve this problem to improve the productivity of (S)-DCP, an n-heptane-aqueous biphasic system was adopted in this work. The influential operational parameters including phase volumetric ratio, buffer pH and reaction temperature were optimized. Under the optimal reaction conditions, significant improvements of substrate concentration and biocatalyst productivity (375 mM and 7.64 mmol (S)-DCP g(-1) cell) were achieved in this n-heptane-aqueous biphasic system compared with aqueous single-phase system (150 mM and 2.97 mmol g(-1)cell). The scale-up biosynthesis of (S)-DCP was successfully performed in a 2-L stirred reactor, resulting in a 128.8 mM (S)-DCP with enantiomeric excess of 99.1% and average productivity of 2.07 g (S)-DCPL(-1) h(-1), respectively.

Enhanced biotransformation of 1,3-dichloro-2-propanol to epichlorohydrin via resin-based in situ product removal process.

Biotransformation of 1,3-dichloro-2-propanol (DCP) to epichlorohydrin (ECH) by the whole cells of recombinant Escherichia coli expressing halohydrin dehalogenase was limited by product inhibition. To solve this problem and improve the ECH yield, a biotransformation strategy using resin-based in situ product removal (ISPR) was investigated. Seven macroporous resins were examined to adsorb ECH: resin HZD-9 was the best. When 10 % (w/v) HZD-9 was added to batch biotransformation, 53.3 mM ECH was obtained with a molar yield of 88.3 %. The supplement of the HZD-9 increased the ECH volumetric productivity from 0.5 to 2.8 mmol/l min compared to without addition of resin. In fed-batch biotransformation, this approach increased ECH from 31 to 87 mM. These results provide a promising basis for the biosynthesis of ECH.

Enantioselective hydrolysis of epichlorohydrin using whole Aspergillus niger ZJB-09173 cells in organic solvents.

The enantioselective hydrolysis of racemic epichlorohydrin for the production of enantiopure (S)-epichlorohydrin using whole cells of Aspergillus niger ZJB-09173 in organic solvents was investigated. Cyclohexane was used as the reaction medium based on the excellent enantioselectivity of epoxide hydrolase from A. niger ZJB- 09173 in cyclohexane. However, cyclohexane had a negative effect on the stability of epoxide hydrolase from A. niger ZJB-09173. In the cyclohexane medium, substrate inhibition, rather than product inhibition of catalysis, was observed in the hydrolysis of racemic epichlorohydrin using A. niger ZJB-09173. The racemic epichlorohydrin concentration was markedly increased by continuous feeding of substrate without significant decline of the yield. Ultimately, 18.5% of (S)-epichlorohydrin with 98 percent enantiomeric excess from 153.6 mM of racemic epichlorohydrin was obtained by the dry cells of A. niger ZJB-09173, which was the highest substrate concentration in the production of enantiopure (S)-epichlorohydrin by epoxide hydrolases using an organic solvent medium among the known reports.

Improvement of 1,3-dihydroxyacetone production from Gluconobacter oxydans by ion beam implantation.

Improvement of dihydroxyacetone (DHA) production by mutagenesis of ion beam implantation and medium optimization using response-surface methodology (RSM) were investigated in this work. More than 1000 mutant strains were selected through a mutagenesis method using N(+) ions implantation with a dose of 60 × (2.6 × 10(13)) ions/cm(2) and energy of 10 keV. Several high-yield mutant strains were showed the potent application for DHA production and the genetically stable mutant strain G. oxydans ZJB09113 was selected for optimization of cultivation condition by RSM. The optimal medium for DHA fermentation is composed (in g/L) of yeast extract 4.88, CaCO(3) 2.00, and glycerol 52.86 mL/L (initial pH 4.89). The maximal DHA concentration of 40.0 g/L was achieved after 24 hr of shaken flask fermentation at 30°C with 150 rpm, and 196.3% increase in DHA production in comparison with unoptimized conditions.