Increased PHB productivity by high-cell-density fed-batch culture of Alcaligenes latus, a growth-associated PHB producer

Alcaligenes latus, a growth-associated PHB producer, was cultivated by a pH-stat modal fed-batch culture technique to attain high PHB productivity. Both sucrose solution and inorganic medium were fed in conjunction with the supply of ammonia solution which serves as a nitrogen source and as a means of pH control. Compositions of the inorganic medium were formulated by elemental analysis of A. latus cell mass. The effect on inoculum size was examined to reduce culture time. High concentrations of cell (142 g/L) and PHB (68.4 g/L) were obtained in a short culture time (18 h) with an inoculum size of 13.7 g/L. The PHB content and the PHB productivity at the end of the fed-batch culture were 50% of dry cell weight and 4.0 g PHB/(L . h), respectively. (c) 1996 John Wiley & Sons, Inc.     

Asiaticoside production from centella (Centella asiatica L. Urban) cell culture

Petiole explants of centella plants (Centella asiatica L. Urban) were cultured on Murashige and Skoog (MS) solid medium containing 20 g/L sucrose, supplemented with 1.0 mg/L benzylaminopurine and 1.0 mg/L naphthaleneacetic acid for callus production. To establish a cell suspension culture, 2 g of fresh callus was cultured in 50 mL of the same medium but without solid agent at a 100 rpm agitation speed. Every 2 g of culture was subcultured in fresh MS liquid medium for maintenance. After 24 days of culture at a 120 rpm agitation speed, the centella cell biomass reached a maximum of 9.03 g/50 mL on the same MS medium with 30 g/L sucrose and a 3 g inoculum size. A high performance liquid chromatography analysis showed that asiaticoside content in 24-day old suspension cultured cells (45.35 mg/g dry weight) was significantly higher (4.5 fold) than that of in planta leaves (10.55 mg/g dry weight).     

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.     

Chitin and chitosan biopolymer production from the Iranian medicinal fungus Ganoderma lucidum: Optimization and characterization

Abstract

Chitin and chitosan with unique properties and numerous applications can be produced from fungus. The production of chitin and chitosan from the mycelia of an Iranian Ganoderma lucidum was studied to improve cell growth and chitin productivity. Inoculum size and initial pH as two effective variables on the growth of G. lucidum and chitin production were optimized using response surface method (RSM) by central composite design (CCD). The results verified the significant effect of these two variables on the cell growth and chitin production. In optimum conditions, including pH?=?5.7 and inoculum size of 7.4%, the cell dry weight was 5.91?g/L and the amount of chitin production was 1.08?g/L with the productivity of 0.083?g/(L day). The produced chitin and chitosan were characterized using XRD and FTIR. Moreover, the antibacterial activity of the produced chitosan was investigated and compared with the commercial chitosan. The results showed that the produced chitin and chitosan had suitable quality and the Iranian G. lucidum would be a great source for safe and high-quality chitin and chitosan production.     

Effects of furfural on ethanol fermentation bySaccharomyces cerevisiae: Mathematical models

Different inocula with high yeast concentration were investigated as a means of overcoming the inhibitory effect of furfural in ethanol fermentation. In order to verify the toxicity of the furfural, a series of fermentation runs were made with 0.25, 5.50, and 9.00 g/L (dry weight) ofSaccharomyces cerevisiae inoculum and 1, 3, and 5 g/L of furfural. The extent of cell death occurring in the early phase of fermentation was dependent on the initial cell concentration. With high initial yeast concentration, the effect of furfural is canceled, because it is depleted at an early stage of fermentation. The ethanol weight yield averaged 0.45 on the basis of sugar consumed. The ethanol productivity and specific growth rate decreased with the increase of furfural concentration, and the inhibitory effect almost disappeared with high cell concentration (9 g/L). Mathematical models were developed that relate productivity and growth rate with furfural and cell concentration.     

Oil production from five marine microalgae for the production of biodiesel

Marine microalgae were studied as potential resources for the production of biodiesel. Five marine microalgae, Tetraselmis suecica, Phaeodactylum tricornutum, Chaetoceros calcitrans, Isochrysis galbana, and Nannochloropsis oculata were cultured in f/2 media, 12:12 L:D cycle at 20 ± 1°C with a light intensity of 36.3 μmol/m²/sec using a 15-L circular cylindrical photobioreactor. The dry cell weight, specific growth rate, biomass productivity, oil content and fatty acid composition of palmitic acid, stearic acid, oleic acid, linoleic acid, and linolenic acid of microalgae were determined. T. suecica, I. galbana, and N. oculata showed high dry cell weights of 0.58, 0.57, and 0.57 g/L, respectively. The culture period of T. suecica to reach the stationary phase was 9 days. On the other hand, N. oculata showed the longest culture period of 28 days to reach the stationary phase. T. suecica absorbed nitrate at the initial stages of cell growth, decreasing the nitrate concentration to 0.5 mg/L on day-7 of the culture. The highest oil contents were observed in P. tricornutum with a 25.31% dry cell weight and I. galbana with a 23.15% dry cell weight on day-9 after the stationary phase. I. galbana showed 417.33 mg of palmitic acid per g oil and T. suecica showed 235.61 mg of oleic acid per g oil. Stearic acid, linoleic acid, and linolenic acid did not exceed 30.02 mg/g oil in any of the microalgae. T. suecica showed the shortest culture period of 9 days to reach the stationary phase. Therefore, the highest biomass production of 0.58 g/L was obtained and I. galbana showed high biomass production of 0.57 g/ L and oil content of 23.15% of dry cell weight. Therefore, T. suecica and I. galbana can be selected as a potential candidate for the production of biodiesel.     

Enhanced production of taxol in suspension cultures of Taxus chinensis by controlling inoculum size

Inoculum size (1.5-6.0g dry weight/l) significantly affected cell growth and accumulation of intracellular and extracellular taxol in Taxus chinensis. A shorter cultivation time and a higher biomass productivity were achieved using inoculum size of 6.0g DW/l. Both the intracellular content and total production of taxol were increased almost 30% with an increase of inoculum size from 1.5 to 3.0g DW/l, while an even higher inoculum size decreased taxol formation. The extracellular taxol concentration was relatively higher (0.091mg/l) at low inoculum sizes of 1.5 and 2.0g DW/l; and in various cases it was less than 25% of the total amount of taxol produced.     

Bioreactor operating strategy inThalictrum rugosum plant cell culture for the production of berberine

Optimal substrate feeding strategy in bioreactor operation was investigated to increase the production of secondary metabolite in a high density culture of plant cell. It was accomplished by the previously proposed structured kinetic model that describes the cell growth and synthesis of the secondary metabolite, berberine, in a batch suspension culture ofThalictrum rugosum. Four types of operation strategies for sugar feeding intoT. rugosum culture were proposed based on the model, which were the periodic fedbatch operations to maintain the cell activity, the cell viability, and the specific production rate, and the perfusion operation to maintain the specific production rate. From the simulation results of these strategies, it could be found that the periodic fed-batch operation and the perfusion operation could achieve the higher volumetric production of berberine (mg berberine/L) and specific production yield (mg berberine/g dry cell weight) than those of batch cultures. Although the highest productivity (mg berberine/day) of berberine could be achieved by the periodic fed-batch operation to maintain the cell activity compared with the other strategies in the periodic fed-batch operations, the specific production yield was low due to the higher maximum dry cell weight than other cases. The periodic fed-batch operation to maintain cell viability resulted in the highest volumetric production of berberine and specific production yield compared with the other strategies. In the cases of maintaining the specific production rate, the per-formance of the periodic fed-batch operation was better than that of the perfusion operation in the respect of the volumetric production and productivity of berberine. In order to increase the volumetric production of berberine and to get the highest specific production yield, the periodic fed-batch operation to maintain cell viability could be chosen as the optimal operating strategy in high density, culture ofT. rugosum plant cell.     

Production of Trichoderma micropropagules as a biocontrol agent in static liquid culture conditions by using an integrated bioreactor system

ABSTRACT

In this study, we optimised the conditions for the production of micropropagules of Trichoderma harzianum EGE-K38 in static liquid culture in Modified Czapec Medium (MCM) containing 8?g/L glucose in an integrated tray bioreactor system designed by our research group. Incubation temperature, air flow rate, inoculum spore concentration, inoculation size, medium volume and the use of spores or agar plugs containing mycelia as inoculum were individually studied as one factor at a time. The maximum micropropagule count was 5.2?±?0.2?×?10^9?cfu/mL and dry cell weight was 17?±?2?g/L. For the subsequent drying processes, the maximum drying yield percentage ((viable micropropagule counts after drying/viable cells before drying)*100) after drying of micropropagules was 23.30% (cfu/cfu). Results obtained from our integrated tray bioreactor system showed that static liquid culture fermentation offers potential for industrial scale fungal BCAs production.     

Improved phloroglucinol production by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Phloroglucinol is a valuable chemical which has been successfully produced by metabolically engineered Escherichia coli. However, the low productivity remains a bottleneck for large-scale application and cost-effective production. In the present work, we cloned the key biosynthetic gene, phlD (a type III polyketide synthase), into a bacterial expression vector to produce phloroglucinol in E. coli and developed different strategies to re-engineer the recombinant strain for robust synthesis of phloroglucinol. Overexpression of E. coli marA (multiple antibiotic resistance) gene enhanced phloroglucinol resistance and elevated phloroglucinol production to 0.27 g/g dry cell weight. Augmentation of the intracellular malonyl coenzyme A (malonyl-CoA) level through coordinated expression of four acetyl-CoA carboxylase (ACCase) subunits increased phloroglucinol production to around 0.27 g/g dry cell weight. Furthermore, the coexpression of ACCase and marA caused another marked improvement in phloroglucinol production 0.45 g/g dry cell weight, that is, 3.3-fold to the original strain. Under fed-batch conditions, this finally engineered strain accumulated phloroglucinol up to 3.8 g/L in the culture 12 h after induction, corresponding to a volumetric productivity of 0.32 g/L/h. This result was the highest phloroglucinol production to date and showed promising to make the bioprocess economically feasible.     

High‐yield secretion of recombinant proteins expressed in tobacco cell culture with a designer glycopeptide tag: Process development

Low‐yield protein production remains the most significant economic hurdle with plant cell culture technology. Fusions of recombinant proteins with hydroxyproline‐O‐glycosylated designer glycopeptide tags have consistently boosted secreted protein yields. This prompted us to study the process development of this technology aiming to achieve productivity levels necessary for commercial viability. We used a tobacco BY‐2 cell culture expressing EGFP as fusion with a glycopeptide tag comprised of 32 repeat of ”Ser‐Pro“ dipeptide, or (SP)₃₂, to study cell growth and protein secretion, culture scale‐up, and establishment of perfusion cultures for continuous production. The BY‐2 cells accumulated low levels of cell biomass (～7.5 g DW/L) in Schenk & Hildebrandt medium, but secreted high yields of (SP)₃₂‐tagged EGFP (125 mg/L). Protein productivity of the cell culture has been stable for 6.0 years. The BY‐2 cells cultured in a 5‐L bioreactor similarly produced high secreted protein yield at 131 mg/L. Successful operation of a cell perfusion culture for 30 days was achieved under the perfusion rate of 0.25 and 0.5 day^?1, generating a protein volumetric productivity of 17.6 and 28.9 mg/day/L, respectively. This research demonstrates the great potential of the designer glycopeptide technology for use in commercial production of valuable proteins with plant cell cultures.     

低密度和条件培养对红豆杉细胞生长的影响

红豆杉种胚来源的细胞,在改良Ｂ５液体培养基中继代培养的临界接种密度为鲜重４０ｇ／Ｌ．低密度培养下,１０－１６ｄ的条件培养液（ＣＭ）与新鲜培养液按５７：４３的比例混合时,能显著缩短细胞生长的延迟期,提高生长率,１００Ｌ生物反应器中,按４５．５％体积分数添加条件培养液,在鲜重２７ｇ／Ｌ低接种密度下培养５周,生物量增长９倍,达干重１４．３ｇ／Ｌ．对内源植物激素、精胺、维生素和氨基酸等的比较分析表明,吲哚     

Large-scale cultivation ofSolanum chrysotrichum cells: Production of the antifungal saponin SC-1 in 10-I airlift bioreactors

Cells of two different cell lines:ccvx (cotyledon derived) andccvz (hypocotyl derived) ofSolanum chrysotrichum were cultivated in 10-1 airlift bioreactors for the production of the human antimycotic compound SC-1. When using 3 g l^-1 dry weight inoculum in a batch culture, higher levels of biomass were achieved with theccvx cell line (14.6 g l^-1) than withccvz (7.7 g l^-1), resulting in 23 and 12 mg g^-1 of SC-1 after 17 days in culture forccvx andccvz, respectively. The maximum productivity of SC-1 in bioreactors was 0.025 g l^-1 day^-1 after 9 days in culture. When using a draw-fill mode, the productivity increased by 60% to a value of 0.041 g l^-1 day, 4 days after 50% of the cell suspension was removed and replaced with fresh medium. This latter bioreactor system is a feasible alternative for the production of the antimycotic metabolite ofS. chrysotrichum on a large scale.Abbreviations DW Cell dry weight - FW Fresh weight - MS Murashige and Skoog (1962) medium - T _d Doubling time     

In vitro production of gymnemic acid from cell suspension cultures of Gymnema sylvestre R. Br

Gymnema sylvestre is an important medicinal plant that bears bioactive compound namely gymnemic acids. The present work deals with the optimization of a cell suspension culture system of Gymnema sylvestre for the production of biomass and gymnemic acid, which has anti‐diabetic properties. We investigated the effect of inoculum densities (2.5–20.0 g/L), the strength of the Murashige and Skoog (MS) medium (0.25–2.0), carbon source (sucrose, glucose, fructose, maltose), and the concentration of the sucrose (1–8% w/v) to determine their effects on biomass accumulation and production of gymnemic acid. Overall, 10 g/L of inoculum density, full‐strength MS medium supplemented with 2,4‐dichlorophenoxy acetic acid (2.0 mg/L) and Kinetin (0.1 mg/L), and 3% w/v sucrose was found best for the accumulation of biomass and gymnemic acid content (9.95 mg/g dry weight). The results of the current study will be useful for bioprocess and biochemical engineers for large‐scale production of gymnemic acid in cell culture.     

The Effective Production of Shikonin by Cultures with an Increased Cell Population

We have studied the efficient production of shikonin derivatives by suspension cultures of Lithospermum erythrorhizon with an increased cell population. The yield of shikonin derivatives was highest (800 mg/liter) when 2.8 g dry wt/liter of the cells was inoculated into the M-2 medium which we had developed for the production, but the excess inoculum lowered the yield.

We investigated suitable conditions for production with the increased cell population. The optimum amount of inoculum rose to 4.9 g dry wt/liter when the concentrations of all the components contained in the M-8 medium, which we developed for increasing the productivity by modification of the M-2 medium, were increased in proportion to the amount of inoculum, and consequently we could increase the yield of the shikonin derivatives from 1400 mg/liter to 1900 mg/liter. Moreover, the increased rate of oxygen supply in addition to the enrichment of the medium made it possible to produce 2300 mg/liter of the shikonin derivatives from a culture for which 5.6 g dry wt/liter of the cells was inoculated.     

The influence of methyl jasmonate,cholesterol and l‐arginine on solasodine production in hairy root culture of Solanum mammosum

The increasing demand of diosgenin for high‐revenue synthesis of steroid hormones by the pharmaceutical industries has driven researchers to look for other alternatives. Solasodine which was reported to be present in Solanum mammosum is known to be a potential source. The present study highlighted that added methyl jasmonate, cholesterol and l ‐arginine into the modified liquid full‐strength Murashige and Skoog (MS) medium (with ammonium to nitrate ratio 10.3 mM: 39.4 mM, and 4% (w/v) sucrose) could influence the solasodine production in the hairy roots of S. mammosum. The findings showed that both hairy root line‐ATCC31798 and line‐A4 (which were separately induced by Agrobacterium rhizogenes strain ATCC31798 and A4) acquired solasodine productivity of 4.5 mg/g dry weight roots with average dry biomass of 190 mg after 32 days culture, when using 50 mg fresh weight roots as initial inoculum size, with 100 mM cholesterol, 1000 μM l ‐arginine and 300 μM methyl jasmonate added simultaneously into the culture medium on day 20 of culture. The amount of solasodine obtained was five times higher than those without both the elicitor and precursor treatment. The improved solasodine production with a high‐biomass growth could reduce the production cost of steroid synthesis in the long run.     

Production of red pigments byMonascus purpureus in solid-state culture

To maximize and sustain the productivity ofMonascus pigments, various environmental and nutritional parameters, such as the initial moisture content, pH, inoculum size, sample size, and nutrient supplement, that influence pigment production were evaluated in solid-state cultures as follows: initial moisture content, 50%; pH, 6.0; inoculum size 1 x 10⁴ spore cells (grams of dry solid substrate)⁻¹; sample size, 300 g. All supplementary nutrients (carbon, nitrogen, and mineral sources) added has inhibitory effects on the cell growth and red pigment production. In open tray culture the maximum biomass yield and specific productivity of red pigments were 223 mg DCW (grams of initial dry substrate)⁻¹ and, 47.6 OD₅₀₀ (DCW grams)⁻¹ h⁻¹, respectively.     

重组巴氏毕赤酵母高密度发酵表达rHSA

对基因工程菌Pichiapastoris的摇瓶发酵条件进行了试验 ,并根据摇瓶发酵的优化结果进行了补料分批高密度发酵。在摇瓶发酵时 ,甲醇诱导基因工程菌P .pastoris表达重组人血清白蛋白的发酵周期为 96h ;甲醇的最佳诱导浓度为 1 0g L ;发酵pH范围为 5 72～ 6 5 9;在摇瓶培养时 ,随着接种量的增加 ,虽然目的蛋白表达量缓慢增加 ,但单位细胞光密度的蛋白产率却明显下降 ,符合y =1 2 941x- 0 50 59方程 (线性相关系数r=0 9789) ,其限制性因子很可能为溶氧。在分批发酵 ,接种量为 1 0 %且种子细胞光密度 (OD60 0 )为 2 0左右时 ,细胞生长的延迟期为 2 1 1h左右 ,细胞生长光密度与培养时间的关系模型为 :y =0 7841e0 .2 3 19t(线性相关系数r=0 .993 6 ) ;在补料发酵时细胞干重浓度可达到 1 1 5g L— 1 6 0g L ,在 1 2 0h重组人血清白蛋白表达量最大达到 3 6g L。     

Sodium gluconate production byAspergillus niger with intermittent broth replacement

Intermittent broth replacement was carried out to enhance the productivity and purity of sodium gluconate usingAspergillus niger by reducing the concentration of unmetabolized glucose. As inoculum size increased, length of lag phase was shortened and high initial production rate of sodium gluconate was achieved. However, too high inoculum concentration lowered productivity during the later stage of fermentation and increased residual glucose at the end of cultivation. When culture broth was replaced intermittently with distilled water, fresh medium, or recycled medium for comparison with traditional fermentation method, production of sodium gluconate was enhanced more than 1.5 fold and active production period could be prolonged without residual glucose. In addition, productivity was maintained at a level higher than 6 g/L/nr. Therefore, it was found that the reduction of biomass and viscosity by intermittent broth replacement could enhance the productivity.     

Bioreactor productivity and media cost comparison for different intensified cell culture processes

Process intensification in biomanufacturing has attracted a great deal of interest in recent years. Manufacturing platform improvements leading to higher cell density and bioreactor productivity have been pursued. Here we evaluated a variety of intensified mammalian cell culture processes for producing monoclonal antibodies. Cell culture operational modes including fed‐batch (normal seeding density or high seeding density with N‐1 perfusion), perfusion, and concentrated fed‐batch (CFB) were assessed using the same media set with the same Chinese Hamster Ovary (CHO) cell line. Limited media modification was done to quickly fit the media set to different operational modes. Perfusion and CFB processes were developed using an alternating tangential flow filtration device. Independent of the operational modes, comparable cell specific productivity (fed‐batch: 29.4 pg/cell/day; fed‐batch with N‐1 perfusion: 32.0 pg/cell/day; perfusion: 31.0 pg/cell/day; CFB: 20.1 – 45.1 pg/cell/day) was reached with similar media conditions. Continuous media exchange enabled much higher bioreactor productivity in the perfusion (up to 2.29 g/L/day) and CFB processes (up to 2.04 g/L/day), compared with that in the fed‐batch processes (ranging from 0.39 to 0.49 g/L/day), largely due to the higher cell density maintained. Furthermore, media cost per gram of antibody produced from perfusion was found to be highly comparable with that from fed‐batch; and the media cost for CFB was the highest due to the short batch duration. Our experimental data supports the argument that media cost for perfusion process could be even lower than that in a fed‐batch process, as long as sufficient bioreactor productivity is achieved. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:867–878, 2017