A process for the production of ectoine and poly(3-hydroxybutyrate) by <Emphasis Type="Italic">Halomonas boliviensis</Emphasis>

The paper reports a study involving the use of Halomonas boliviensis, a moderate halophile, for co-production of compatible solute ectoine and biopolyester poly(3-hydroxybutyrate) (PHB) in a process comprising two fed-batch cultures. Initial investigations on the growth of the organism in a medium with varying NaCl concentrations showed the highest level of intracellular accumulation of ectoine (0.74 g L⁻¹) at 10–15% (w/v) NaCl, while at 15% (w/v) NaCl, the presence of hydroxyectoine (50 mg L⁻¹) was also noted. On the other hand, the maximum cell dry weight and PHB concentration of 10 and 5.8 g L⁻¹, respectively, were obtained at 5–7.5% (w/v) NaCl. A process comprising two fed-batch cultivations was developed—the first culture aimed at obtaining high cell mass and the second for achieving high yields of ectoine and PHB. In the first fed-batch culture, H. boliviensis was grown in a medium with 4.5% (w/v) NaCl and sufficient levels of monosodium glutamate, NH₄⁺, and PO₄³⁻. In the second fed-batch culture, the NaCl concentration was increased to 7.5% (w/v) to trigger ectoine synthesis, while nitrogen and phosphorus sources were fed only during the first 3 h and then stopped to favor PHB accumulation. The process resulted in PHB yield of 68.5 wt.% of cell dry weight and volumetric productivity of about 1 g L⁻¹ h⁻¹ and ectoine concentration, content, and volumetric productivity of 4.3 g L⁻¹, 7.2 wt.%, and 2.8 g L⁻¹ day⁻¹, respectively. At salt concentration of 12.5% (w/v) during the second cultivation, the ectoine content was increased to 17 wt.% and productivity to 3.4 g L⁻¹ day⁻¹.     

Optimizing emulsan production of <Emphasis Type="Italic">A. venetianus</Emphasis> RAG-1 using response surface methodology

Statistical experimental design was used to optimize medium constituents for emulsan production by Acinetobacter venetianus RAG-1 in batch cultivation. The factors affecting emulsan production were screened by a two-level factorial design, and the optimal concentration of medium constituents for emulsan production were determined by the method of steepest path ascent and central composite experimental design. Experimental results showed that the optimal medium constituents were 9.16 g/L ethanol, 8.2 g/L KH₂PO₄, 23.32 g/L K₂HPO₄, 5.77 g/L (NH₄)₂SO₄ and 0.354 g/L MgSO₄•7H₂O. Under this optimal composition, the predicted emulsan production was 72.198 mg/L, and experimental value was 73.312 mg/L for 80 h culture in the shake flasks, and the emulsan yield by A. venetianus RAG-1 was enhanced nearly 1.48-fold (from 49.5 to 73.312 mg/L). Based on the results, we identify the optimal medium constituents for emulsan production and could take advantage of strategy for scale up the fermentation of emulsan production.     

Optimized production of Pichia guilliermondii biomass with zinc accumulation by fermentation

Zinc is an essential nutrient that plays an important role in several biological processes of living organisms. When bound to an organic substrate, Zn is more efficiently absorbed by organisms, has a high biological activity and a low toxicity. Due to its ability to incorporate metals, yeast biomass has been used frequently as a delivery vehicle for many mineral supplements. This study describes the screening of strains of yeast for production of biomass enriched with Zn by submerged fermentation. Five strains of yeasts, belonging to the genera Saccharomyces, Kluyveromyces and Pichia, were evaluated. The highest Zn concentration was 6820 mg/kg of dry weight biomass, using Pichia guilliermondii Wickerham LPB 063 after 120 h of cultivation in a medium with 0.5 g/L ZnSO₄. Process conditions were optimized using statistical experimental design methodology. Four parameters were identified in the 2⁸⁻⁴ fractional factorial design as having a significant effect on Zn accumulation: ZnSO₄ and Fe₂(SO₄)₃ concentrations, time of addition of the ZnSO₄ solution and concentration of soybean molasses. In the 3² experimental design, the influence of ZnSO₄ and Fe₂(SO₄)₃ concentrations were studied more closely. The highest Zn concentration (75,090 mg/kg dry weight) in the biomass was reached using the conditions: ZnSO₄, 10.0 g/L; Fe₂(SO₄)₃, 0.1 g/L in Erlenmeyer flasks. A batch liquid fermentation was carried out in a 2 L bioreactor for production of P. guilliermondii Wickerham LPB 063 containing organically bound Zn. The concentration of organically bound Zn after 144 h of fermentation was of 96,030 mg/kg, with a biomass production of 30 g/L. The maximum specific growth rate obtained (μ_max) was 0.0077/h, while the maximum productivity of biomass was at 0.1511 g/L/h.     

Medium optimization for the production of a novel bioflocculant from Halomonas sp. V3a′ using response surface methodology

The novel exopolysaccharide bioflocculant HBF-3 is produced by Halomonas sp. V3a′, which is a mutant strain of the deep-sea bacterium Halomonas sp. V3a. Response surface methodology (RSM) was employed to optimize the production medium for increasing HBF-3 production. Using a Plackett–Burman experimental design to aid in the first step of optimization, edible glucose, MgSO₄·7H₂O, and NH₄Cl were found to be significant factors affecting HBF-3 production. To determine the optimal concentration of each significant variable, a central composite design was employed. Based on response surface and canonical analysis, the optimum concentrations of the critical components were obtained as follows: edible glucose, 16.14 g/l; MgSO₄·7H₂O, 2.73 g/l; and NH₄Cl, 1.97 g/l. HBF-3 production obtained by using the optimized medium was 4.52 g/l, which was in close agreement with the predicted value of 4.55 g/l. By scaling up fermentation from flask to fermenter, HBF-3 production was further increased to 5.58 g/l.     

Optimization of process parameters for ethanol production from sugar cane molasses by Zymomonas mobilis using response surface methodology and genetic algorithm

Ethanol is a potential energy source and its production from renewable biomass has gained lot of popularity. There has been worldwide research to produce ethanol from regional inexpensive substrates. The present study deals with the optimization of process parameters (viz. temperature, pH, initial total reducing sugar (TRS) concentration in sugar cane molasses and fermentation time) for ethanol production from sugar cane molasses by Zymomonas mobilis using Box–Behnken experimental design and genetic algorithm (GA). An empirical model was developed through response surface methodology to analyze the effects of the process parameters on ethanol production. The data obtained after performing the experiments based on statistical design was utilized for regression analysis and analysis of variance studies. The regression equation obtained after regression analysis was used as a fitness function for the genetic algorithm. The GA optimization technique predicted a maximum ethanol yield of 59.59 g/L at temperature 31 °C, pH 5.13, initial TRS concentration 216 g/L and fermentation time 44 h. The maximum experimental ethanol yield obtained after applying GA was 58.4 g/L, which was in close agreement with the predicted value.     

Ectoine improves yield of biodiesel catalyzed by immobilized lipase

To improve the production of biodiesel by enzymatic conversion of triglycerides in cottonseed oil, compatible solutes were added to the solvent-free methanolysis system to prevent competitive methanol inhibition on the immobilized lipase (Novozym^® 435). The results indicated that the addition of ectoine increased biodiesel synthesis using a three-step methanol addition process. The concentration of methyl ester (ME) reached a maximum of 95.0% in the presence of 1.1 mmol/l ectoine, an increase of 20.9% compared to that in the absence of ectoine. On the other hand, excess ectoine decreased the ME concentration. Ectoine was also shown to enhance reuse of the immobilized lipase, significantly improving ME concentrations in each recycling test. Total concentrations of ME with added ectoine were about 1.5 times that without ectoine during five recycling tests (molar ratio of cottonseed oil to methanol, 1:4). Enzymatic reaction kinetics showed, in the concentration ranges of 0.8–1.14 mol/l and 0.03–8 mol/l for triglyceride and methanol, respectively, that ectoine had no effect on the initial reaction rates when methanol concentrations were below 0.5 mol/l. When methanol concentration exceeded 0.5 mol/l, the addition of 0.8 mmol/l ectoine increased the initial reaction rates, and the lipase exhibited a lower affinity for methanol and higher affinity for triglyceride (kinetic parameters of K_mA increase, K_mTG decrease). However, the initial reaction rates decreased significantly when 8 mmol/l ectoine was added, with the lipase having higher affinity for methanol and lower affinity for triglyceride (K_mA decrease, K_mTG increase). The supplementation of ectoine provided a new method for the purpose of improving yield of biodiesel catalyzed by enzyme.     

Rosmarinic acid by Lavandula vera MM cell suspension: Phosphorus effect

Summary The growth of Lavandula vera MM cell suspension and biosynthesis of rosmarinic acid were followed during its cultivation in Linsmayer - Skoog (LS) medium (containing 170 mg/L KH₂PO₄, control cultivation) and in modified LS media, containing different concentration of KH₂PO₄. Doubled concentration of KH₂PO₄ (340 mg/L) caused an increase in the amount of biosynthesised cell biomass (17 g/L vs 13 g/L for control cultivation) and rosmarinic acid (140 mg/L vs 68 mg/L for control cultivation).     

蝉拟青霉液体发酵条件优化

采用液体发酵蝉拟青霉,对蝉拟青霉的发酵条件进行优化,以提高蝉拟青霉胞外多糖产量及生物量。摇瓶发酵条件下,在单因素基础上设计正交实验确定各因素的最佳组合。优化后得最佳发酵培养基:蔗糖8%,牛肉膏0.75%,酵母膏0.125%,MgSO_4·7H_2O 0.3%,KH_2PO_4 0.2%,麸皮0.5%。该条件下胞外多糖产量为5.96 g/L,生物量为42 g/L,较优化前提高了1倍。采用发酵罐进行扩大培养,对分批发酵时的初糖浓度进行了优化,并分析了补料分批发酵对发酵过程的影响。发酵罐培养时最适初糖浓度为5%,此时生物量最高为38 g/L,多糖含量最高为5.5 g/L;采用补料分批发酵时,多糖产量最高为5.89 g/L,生物量最高为40 g/L,效果优于分批发酵。     

Lipid production from Yarrowia lipolytica Po1g grown in sugarcane bagasse hydrolysate

This study investigated the possibility of utilizing detoxified sugarcane bagasse hydrolysate (DSCBH) as an alternative carbon source to culture Yarrowia lipolytica Po1g for microbial oil and biodiesel production. Sugarcane bagasse hydrolysis with 2.5% HCl resulted in maximum total sugar concentration (21.38 g/L) in which 13.59 g/L is xylose, 3.98 g/L is glucose, and 2.78 g/L is arabinose. Detoxification of SCBH by Ca(OH)₂ neutralization reduced the concentration of 5-hydroxymethylfurfural and furfural by 21.31% and 24.84%, respectively. Growth of Y. lipolytica Po1g in DSCBH with peptone as the nitrogen source gave maximum biomass concentration (11.42 g/L) compared to NH₄NO₃ (6.49 g/L). With peptone as the nitrogen source, DSCBH resulted in better biomass concentration than d-glucose (10.19 g/L), d-xylose (9.89 g/L) and NDSCBH (5.88 g/L). The maximum lipid content, lipid yield and lipid productivity of Y. lipolytica Po1g grown in DSCBH and peptone was 58.5%, 6.68 g/L and 1.76 g/L-day, respectively.     

Anaerobic thermophilic fermentation for carboxylic acid production from in-storage air-lime-treated sugarcane bagasse

Wet storage and in situ lime pretreatment (50 °C, 1-atm air, 56 days, excess lime loading of 0.3 g Ca(OH)₂/g dry biomass) of sugarcane bagasse (4,000 g dry weight) was performed in a bench-scale pile pretreatment system. Under thermophilic conditions (55 °C, NH₄HCO₃ buffer, methane inhibitors), air-lime-treated bagasse (80 wt.%) and chicken manure (20 wt.%) were anaerobically co-digested in 1-L rotary fermentors by a mixed culture of marine microorganisms (Galveston, TX). During four-stage countercurrent fermentation, the resulting carboxylic acids consisted of primarily acetate (average 87.7 wt.%) and butyrate (average 9.0 wt.%). The experimental fermentation trains had the highest yield (0.47 g total acids/g volatile solids (VS) fed) and highest selectivity (0.79 g total acids/g VS digested) at a total acid concentration of 28.3 g/L, which is equivalent to an ethanol yield of 105.2 gal/(tonne VS fed). Both high total acid concentrations (>44.7 g/L) and high substrate conversions (>77.5%) are predicted for countercurrent fermentations of bagasse at commercial scale, allowing for an efficient conversion of air-lime-treated biomass to liquid transportation fuels and chemicals via the carboxylate platform.     

Fed-batch culture of astaxanthin-rich Haematococcus pluvialis by exponential nutrient feeding and stepwise light supplementation

A fed-batch culture process followed by subsequent photoautotrophic induction was established for the high density culture of astaxanthin-rich Haematococcus pluvialis using a CO₂-fed flat type photobioreactor under unsynchronized illumination. Fed-batch culture was performed with an exponential feeding strategy of the growth-limiting nutrients, nitrate and phosphate, concurrently with the stepwise supplementation of light depending on the cell concentration. During the growth phase, a biomass of 1.47 g/L was obtained at a biomass productivity of 0.33 g/L/day. Photoautotrophic induction of the well-grown vegetative cells was performed consecutively by increasing the light intensity to 400 μmol photon/m²/s, while keeping the other conditions in the CO₂-fed flat type photobioreactor fixed, yielding an astaxanthin production of 190 mg/L at an astaxanthin productivity of 14 mg/L/day. The proposed sequential photoautotrophic process has high potential as simple and productive process for the production of valuable Haematococcus astaxanthin.     

Efficient enhancement of gallic acid accumulation in cell suspension cultures of <Emphasis Type="Italic">Barringtonia racemosa</Emphasis> L. by elicitation

The bioactive compound, bacoside A, has immense importance for the treatment of memory disorders and Alzheimer’s disease. Due to the growing commercial interest in the herb, Bacopa monnieri, it has been listed as highly endangered species. The present study was aimed at enhancing the production of bacoside A using an alternative technology of plant cell suspension culture. Initial experiments of docking simulations using bacoside A showed good inhibition of acetyl cholinesterase (binding energy value of ??20 kcal/mol), when comparison was made with other phytocompounds and the synthetic drug for Alzheimer’s disease. In vitro experiments established that B. monnieri cell suspension culture can be developed in Murashige and Skoog medium containing containing 0.1 mg/L benzylaminopurine and 0.5 mg/L naphthalene acetic acid. Plackett–Burman studies predicted that the most effective factors for maximum biomass production were inoculum size (t-value of 4.87), sucrose concentration (t-value of 0.25) and KH₂PO₄ concentration (t-value of 0.007). The nitrate to ammonium ratio (t-value of ? 0.42) did not have significant effect on the cell suspension biomass. The optimum concentration of the crucial variables obtained from a central composite design were—inoculum size of 2 g/L, sucrose concentration of 30 g/L and KH₂PO₄ concentration of 1.24 mM in one-sixth strength MS medium. The best model for optimum production of biomass and bacoside A was experimentally verified and the correlation between the predicted and actual values was found to be 99% for biomass and 94% for bacoside A production. The experimental results have been discussed in the present work.     

Ectoine accumulation in Brevibacterium epidermis

As a halotolerant bacterial species, Brevibacterium epidermis DSM 20659 can grow at relatively high salinity, tolerating up to 2 m NaCl. It synthesizes ectoine and the intracellular content increases with the medium salinity, with a maximum of 0.14 g ectoine/g CDW at 1 m NaCl. Sugar-stressed cells do not synthesize ectoine. Ectoine synthesis is also affected by the presence of external osmolytes. Added betaine is taken up and completely replaced ectoine, while l-proline is only temporarily accumulated after which ectoine is synthesized. The strain can metabolize ectoine; l-glutamate is a better carbon source for ectoine synthesis than l-aspartate.     

Filamentous fungi in microtiter plates—an easy way to optimize itaconic acid production with Aspergillus terreus

Itaconic acid is an important industrial building block and is produced by the filamentous fungi Aspergillus terreus. To make the optimization process more efficient, a scale-down from shake flasks to microtiter plates was performed. This resulted in comparable product formations, and 87.7 g/L itaconic acid was formed after 10 days of cultivation in the microtiter plate. The components of the minimal medium were varied independently for a media optimization. This resulted in an increase of the itaconic acid concentration by a variation of the KH₂PO₄ and CuSO₄ concentrations. The cultivation with a higher KH₂PO₄ concentration in a 400-mL bioreactor showed an increase in the maximum productivity of 1.88 g/L/h, which was an increase of 74 % in comparison to the reference. Neither the phosphate concentration nor the nitrogen sources were limited at the start of the product formation. This showed that a limitation of these substances is not necessary for the itaconic acid formation.     

Metabolic engineering of Escherichia coli for efficient osmotic stress-free production of compatible solute hydroxyectoine

Compatible solutes are key for the ability of halophilic bacteria to resist high osmotic stress. They have received wide attention from researchers for their excellent osmotic protection properties. Hydroxyectoine is a particularly important compatible solute, but its production by microbes faces several challenges, including low titer/yield, the presence of the byproduct ectoine, and the requirement of high salinity. Here, we aimed to metabolically engineer Escherichia coli to efficiently produce hydroxyectoine in the absence of osmotic stress without accumulating the byproduct ectoine. First, combinatorial optimization of the expression strength of key genes in the ectoine synthesis module and hydroxyectoine synthesis module was conducted. After optimization of the expression of these genes, 12.12 g/L hydroxyectoine and 0.24 g/L ectoine were obtained at 36 h in shake-flask fermentation with the addition of the co-substrate α-ketoglutarate. Further optimization of the addition of α-ketoglutarate achieved the sole production of hydroxyectoine (i.e., no ectoine accumulation), indicating that the supply of α-ketoglutarate is critically important for sole hydroxyectoine production. Finally, quorum sensing-based auto-regulation of intracellular α-ketoglutarate pool was implemented as an alternative to α-ketoglutarate addition by coupling the expression of sucA with the esaI/esaR circuit, which led to 14.93 g/L hydroxyectoine with a unit cell yield of 1.678 g/g and no ectoine accumulation in the absence of osmotic stress. This is the highest reported titer of sole hydroxyectoine production under salinity-free fermentation to date.     

不同磷、硫及二氧化碳浓度对标志链带藻生长和碳水化合物积累的影响

【目的】为了研究不同磷、硫及二氧化碳浓度对标志链带藻(Desmodesmus insignis)生长与碳水化合物积累的影响,本实验以改良BG11培养基为基础,设计了8种不同初始K_2HPO_4浓度、8种不同初始MgSO_4浓度及4种二氧化碳浓度培养标志链带藻。【方法】采用干重法和苯酚-硫酸法分别测定其生物质浓度与总碳水化合物的含量。【结果】实验结果显示,在高磷浓度(0.460 mmol/L)下生物量达到最高为6.37 g/L,磷浓度为0.230 mmol/L (对照组)时总碳水化合物含量及单位体积产率达到最高,分别为45.40%(%干重)和0.20 g/(L·d)。不同初始MgSO_4浓度实验结果显示,高硫浓度有利于标志链带藻生长及碳水化合物的积累,生物量、总碳水化合物含量及单位体积产率分别在硫浓度为1.217 mmol/L、0.609 mmol/L和1.824 mmol/L时达到最高,分别为7.02 g/L、51.6%(%干重)及0.26 g/(L·d)。当二氧化碳浓度为3%(V/V)时,标志链带藻生物量、总碳水化合物含量及单位体积产率均达到最高,分别为6.81 g/L、44.03%和0.20 g/(L·d)。【结论】因此,磷浓度为0.230 mmol/L、硫浓度为1.824 mmol/L和二氧化碳浓度为3%时最有利于标志链带藻生长及碳水化合物的积累。     

Two-step acid and alkaline ethanolysis/alkaline peroxide fractionation of sugarcane bagasse and rice straw for production of polylactic acid precursor

Sugarcane bagasse and rice straw were subjected to acid and alkaline ethanolysis and sequential enzymatic hydrolysis to produce glucose for lactic acid production. Influence of physico-chemical treatments using ultrasonic bath and ultrasonic probe was studied compared with mechanical stirring. The results showed that the highest glucose yield with least contamination of xylose was obtained from acid ethanolysis fractionation (5 N H₂SO₄ + 50%, v/v ethanol) when stirred at 90 °C for 4 h. Alkaline ethanolysis accomplished high amount of both glucose and xylose released, however it was not favorable substrate for homofermentative lactic acid bacteria. In order to enhance enzymatic hydrolysis of acid ethanolysis fractionated samples, lignin was subsequently removed by the second step alkaline/peroxide delignification. The maximum lactic acid was obtained at 23.6 ± 0.2 g/L from Lactobacillus casei fermentation after 72 h when hydrolysate from two-step acid hydrolysis and alkaline/peroxide fractionated sugarcane bagasse containing 24.6 g/L initial glucose concentration was used as substrate.     

Effects of macro elements and nitrogen source on biomass accumulation and bacoside A production from adventitious shoot cultures of <Emphasis Type="Italic">Bacopa monnieri</Emphasis> (L.)

The present work deals with optimization of adventitious shoot culture of Bacopa monnieri for the production of biomass and bacoside A and has investigated the effects of macro elements (NH₄NO_3, KNO_3, CaCl_2, MgSO₄ and KH₂PO₄) and nitrogen source [NH₄ ⁺/NO₃ ⁻] of Murashige and Skoog (Physiol Plant 15:473–497, 1962) medium (MS) on accumulation of biomass and bacoside A content. Optimum number of adventitious shoots (99.33 shoots explant⁻¹), fresh weight (1.841 g) and dry weight (0.150 g) were obtained in the medium with 2.0× strength of NH₄NO₃. The highest production of bacoside A content was also recorded in the medium of 2.0× NH₄NO₃, which produced 17.935 mg g⁻¹ DW. The number of adventitious shoot biomass and bacoside A content were optimum when the NO₃ ⁻ concentration was higher than that of NH₄ ⁺. Maximum number of shoots (70.00 shoots explant⁻¹), biomass (fresh weight 1.137 g and dry weight 0.080 g) and also bacoside A content (27.106 mg g⁻¹ DW) were obtained at NH₄ ⁺/NO₃ ⁻ ratio of 14.38/37.60 mM. Overall, MS medium supplemented with 2.0× NH₄NO₃ is recommended for most efficient bacoside A production.     

Pectinase production by Aspergillus niger LB-02-SF is influenced by the culture medium composition and the addition of the enzyme inducer after biomass growth

The production of pectinase by Aspergillus niger LB-02-SF was focused on a submerged cultivation, before it was evaluated in a solid-state process. This study involved the creation of a defined culture medium and an evaluation of the effects of the addition of the enzyme inducer, citrus pectin, to the medium after the intense biomass growth phase. A culture medium formulated without glucose allowed a reduction of biomass growth and greater pectinase production, facilitated by the control of process parameters such as mixing, pH and oxygen supply. The addition of pectin when a minimum pH of 2.7 was reached at 22 h of cultivation did not affect fungal growth. The maximum biomass concentration was 11.0 g/L at 48 h, a value similar to that observed for the control, in which pectin was included in the medium at the beginning of the process (11.5 g/L, at 41 h). However, this condition favored the production of 14 U/mL pectinase, which was approximately 40% higher than the value observed for the control. These results show that pectinase production by A. niger in a submerged cultivation is strongly affected by the medium composition as well as the delayed addition of pectin to the fermentation broth.